THE
ENVIRONMENT (PROTECTION) RULES, 1986
Form I Notice of
Intention to have Sample Analyzed
Form II Memorandum
of Government Analyst
Form
III Report by Government Analyst
Form V
Environmental Statement
THE ENVIRONMENT (PROTECTION)
RULES, 19861
1. Vide Notification No.
S.O. 844 (E), dated 19th November, 1986 published in Gazette of India,
Extraordinary, Pt. 11, sec. 3(i), dated 19th November, 1986.
In
exercise of powers conferred by sections 6 and 25 of the Environment (Protection) Act, 1986 (29 of 1986), the Central Government hereby makes the following rules, namely: -
1. Short title and
commencement.
(i) These
rules may be called the Environment (Protection) Rules, 1986.
(ii) They shall come into force on the date of
their publication in the Official Gazette.
2. Definitions. -In
these rules, unless the context otherwise requires -
(a) Act means
the Environment (Protection) Act, 1986 (29 of 1986);
1[(aa) areas means all areas where the
hazardous substances are handled;]
(b) Central Board means the Central Board
for the Prevention and Control
of Water Pollution constituted under section 3 of the Water (Prevention and
Control of Pollution) Act, 1974 (6 of 1974);
(c) Form means a form set forth in Appendix
A to these rules;
(d) Government Analyst means a person
appointed or recognized as such under section 13;
(e) Person in relation to any factory or
premises means a person or occupier or his agent who has control over the
affairs of the factory or premises and includes in relation to any substance,
the person in possession of the substance;
1[(ee) prohibited substance means the substance prohibited for
handling;]
(f) Recipient system means the part of the
environment, such as, soil, water, air or other which receives the pollutants;
1[(ff) Restricted substance
means the substance restricted for handling;]
(g) "Section" means a section of
the Act;
(h) "Schedule" means a schedule
appended to these rules;
(i) "Standards" means standards
prescribed under these rules;
(j) State Board means a State Board for
the Prevention and Control of Water Pollution constituted under section 4 of
the Water (Prevention and Control of Pollution) Act, 1974 (6 of 1974), or a
State Board for the Prevention and Control of Air Pollution constituted under
section 5 of the Air (Prevention and Control of Pollution) Act, 1981 (14 of 1981).
1. Ins. by G.S.R. 93 1 (E)
dated 27th October 1989 (w.e.f. 27-10-1989).
3. Standards for emission
or discharge of environmental pollutants:
(1) For the purposes of protecting and improving the
quality of the environment and preventing and abating environmental pollution,
the standards for emission or discharge of environmental pollutants from the
industries, operations or processes shall be as specified in 1 [Schedules
I to IV]
2[ * * * ]
(2) Notwithstanding anything contained in
sub-rule (1), the Central Board or a State Board may specify more stringent
standards from those provided in 1[Schedules
I to IV] in respect of any specific industry, operation or process depending
upon the quality of the recipient system and after recording reasons, therefor,
in writing.
3(3) The standards for emission
or discharge of environmental pollutants specified under sub-rule (1) or
sub-rule (2) shall be complied with by an industry, operation or process within
a period of one year of being so specified.
4[(3A) (i) Notwithstanding
anything contained in sub-rules (1) and (2), on and from the I st day of
January, 1994, emission or discharge of environmental pollutants from the 5[industries, operations or processes other
than those industries, operations or processes for which standards have been
specified in Schedule I shall] not exceed the relevant parameters and standards
specified in Schedule VI:
Provided that the State
Boards may specify more stringent standards for the relevant parameters with
respect to specific industry or locations after recording reasons therefor in
writing;
(ii) The State Board shall while enforcing the
standards specified in Schedule VI follow the guidelines specified in Annexures
I and II in that Schedule.]
6[(3B) Any emission or discharge of environmental pollutants from the
industries, operations or possesses shall not exceed the relevant concentration
in ambient air as indicated and set out against each pollutants in (3) to (5)
of the Schedule VII],
(4) Notwithstanding anything contained in
sub-rule (3), -
(a) The Central Board or a State Board,
depending on the local conditions or nature of discharge of environment
pollutants, may, by order, specify a lesser period than a period specified
under sub-rule (3) within which the compliance of standards shall be made by an
industry, operation or process;
(b) The Central Government in respect of any
specified industry, operation or process, by order, may specify any period
other than a period specified under sub-rule (3) within which the compliance of
standards shall be made by such industry, operation or process.
(5) Notwithstanding anything contained in
sub-rule (3), the standards for emission or discharge of environmental
pollutants specified under sub-rule (1) or sub-rule (2) in respect of an
industry, operation or process before the commencement of the Environment
(Protection) Amendment Rules, 1991, shall be complied with by such industry,
operation or process by the 31 st day of December, 1991.]
7[(6) Notwithstanding anything contained in sub-rule (3), an industry,
operation or process which has commenced production on or before 16th May, 1981
and has shown adequate proof of at least
commencement of physical work for establishment of facilities to meet the
specified standards within a time-bound programme, to the satisfaction of the
concerned, State Pollution Control Board, shall comply with such standards latest
by the 31 st day of December, 1993.
(7) Notwithstanding anything contained in
sub-rule (3) or sub-rule (6) all industry, operation or process which has
commenced production after the 16th day of May, 1981 but before the 31 st day
of December, 1991 and has shown adequate proof of at least commencement of
physical work for establishment of facilities to meet the specified standards
within a time-bound programme, to the satisfaction of the concerned State
Pollution Control Board, shall comply with such standards latest by the 31 st
day of December, 1992.]
8[(8) On and from the Ist day of
June 2001, the following coal based thermal power plants shall use 9[raw or blended or beneficiated coal with
an ash content not exceeding thirty-four per cent on an annual average basis],
namely: -
(a) Any thermal power plant located beyond one
thousand kilometers from the pit-head; and
(b) Any thermal power plant located in urban
area or sensitive area or critically polluted area irrespective of their
distance from pit-head except any pit-head power plant:
10[Provided that any thermal
power plant using Fluidised Bed Combustion or Circulating Fluidised Bed
Combustion or Atmospheric Fluidised Bed Combustion or Pressurised Fluidised Bed
Combustion or Integrated Gasification Combustion Cycle technologies or any
other clean technologies as may be notified by the Central Government in the
Official Gazette shall be exempted from clauses (a) and (b)].
Explanation:
For the purpose of
this rule-
(a) Beneficiated coal means coal containing
higher calorific value but lower ash than the original ash content in the raw
coal obtained through physical separation or washing process;
(b) Pit-head power plant means power stations
having captive transportation system for its exclusive use for transportation
of coal from the loading point at the mining end up to the unloading point at
the power station without using the normal public transportation system;
(c) Sensitive area means an area whose ecological
balance is prone to be easily disturbed;
(d) Critically polluted area means the area where pollution level has reached or likely to reach to
the critical level and which has been identified as such by the Central
Government or Central Pollution Control Board or a State Pollution Control
Board.]
(e) Urban area means an area limit of a city
having a population of more than million according to 1991 census.].
1. Subs. by G.S.R. 422(E) dated 19th
May 1993 (w.e.f 19.5.1993).
2. Proviso to sub-rule (1), rule 3 omitted by S.O. 23(E), dated
16th January 1991 (w.e.f 16.1.1991).
3. Ins. by S.O. 23(E) dated 16th
January 1991 (w.e.f 16.1.1991).
4. Ins. by G.S.R. 422 (E) dated 19th
May 1993 (w.e.f 19.05.1993).
5. Subs. by G.S.R. 80(E) dated 31st
December 1993 (w.e.f 31.12.1993).
6. Ins. by G.S.R. 176(E) dated 2nd
April 1996 (w.e.f. 3.4.1996).
7. Added by G.S.R. 95 (E), dated 12th
February 1992 (w.e.f. 12-2-1992).
8. Ins. by G.S.R. 560 (E) dated 19th
September 1997 (w.e.f. 19-9-1997).
9. Subs. by G.S.R. 378(E) dated 30th
June 1998 (w.e.f. 3-7-1998).
10. Ins. by G.S.R. 378(E) dated 30th
June 1999 (w.e.f. 3-7-1998).
4. Directions. -
(1) Any
direction issued under section 5 shall be in writing.
(2) The direction shall specify the nature of
action to be taken and the time within which it shall be complied with by the
person officer or the authority to which such direction is given.
1[(3-a)] The person, officer or authority to whom any direction is
sought to be issued shall be served with a copy of the proposed direction and
shall be given an opportunity of not less than fifteen days from the date of
service of a notice to file with an officer designated in this behalf the objections,
if any, to the issue of tile proposed direction.
2[(3-b) Where the proposed direction is for the stoppage or regulation
of electricity or water or any other service affecting the carrying on any
industry, operation or process and is sought to be issued to all officer or an
authority, a copy of the proposed direction shall also be endorsed to the
occupier of the industry, operation or process, as the case may be, and
objections, if any, filed by the occupier with an officer designated in this behalf
shall be dealt with in accordance with the procedures under Sub-rules (3-a) and
(4) of this rule:
Provided that no opportunity
of being heard shall be given to the occupier if he had already been heard
earlier and the proposed direction referred to in Sub-rule (3-b) above for the
stoppage or regulation of electricity or water or any other service was the
resultant decision of the Central Government after such earlier hearing.]
(4) The Central Government shall within a
period of 45 days from tile date of receipt of the objections, if any, or from
the date up to which an opportunity is given to the person, officer or
authority to file objections whichever is earlier, after considering the
objections, if any, received from the person, officer or authority Sought to be
directed and for reasons to be recorded in writing, confirm, modify or decide
not to issue the proposed direction.
(5) In a case where the Central Government is
of the opinion that in view of the likelihood of a grave injury to the environment
it is not expedient to provide all opportunity to file objections against the
proposed direction, it may, for- reasons to be recorded in writing, issue
directions without providing such an Opportunity.
(6) Every notice or direction required to be,
issued under this rule shall be deemed to be duly served-
(a) Where the person to be served is a
company, if the document is addressed in the name of the company at its
registered office or at its principal office or place of business and is
either,-
(i) Sent by registered post; or
(ii) Delivered at its registered office or at
the principal office or place of business;
(b) Where the person to be served is an
officer serving Government, if the document is addressed to the person and a
copy thereof is endorsed to the Head of the Department and also to the
Secretary to the Government, as the case may be, in-charge of the Department in
which for the being the business relating to the Department in which the
officer is employed is transacted and is either, -
(i) Sent by registered post; or
(ii) Is given or tendered to him;
(c) In
any other case, if the document is addressed to the person to be served
and-
(i) Is given or tendered to
him; or
(ii) If Such person cannot be found, is
affixed on some conspicuous part of his last known place of residence or
business or is given or tendered to some adult member of his family or is
affixed on some conspicuous part of the land or building, if any, to which it
relates; or
(iii) Is sent by registered post to that person.
Explanation: For the purposes of this sub-rule, -
(a) Company means any body
corporate and includes a firm or other association of individuals;
(b) A servant is not a member of the
family.
1. Renumbered by S.O. 64(E), dated 18th
January 1988 (w.e.f. 18-1-1988).
2. Ins. by S.O. 64 (E) dated 18th
January 1988 (w.e.f. 18-1-1988).
5. Prohibition and
restriction on the location of industries and the carrying on processes and operations in different areas: -
(1) The Central Government may
take into consideration the following factors while prohibiting or restricting
the location of industries and carrying on of processes and operations in
different areas: -
(i) Standards for quality of environment in
its various aspects laid down for ail area.
(ii) The maximum allowable limits of
concentration of various environment Pollutants (including noise) for an area.
(iii) Tile likely emission or discharge of
environmental Pollutants from all industry, process or operation proposed to be
prohibited or restricted.
(iv) The
topographic and climatic features of ail area.
(v) The biological diversity of the area,
which, in the opinion of the Central Government, needs to be preserved.
(vi) Environmentally compatible land use.
(vii) Net adverse environmental impact likely to
be caused by all industry, process or operation proposed to be prohibited or
restricted.
(viii) Proximity to a protected area under the
Ancient Monuments and Archaeological Sites and Remains Act, 1958 or a
sanctuary, National Park, game reserve or closed area notified, as such under
the Wild Life (Protection) Act, 1972, or places protected under any treaty,
agreement or convention with any other Country or Countries or in pursuance of
any decision made in any international
conference, association or other body.
(ix) Proximity to human Settlements.
(x) Any other factors as may be considered by
the Central Government to be relevant to the protection of the environment in
ail area.
(2) While prohibiting or restricting the
location of industries and carrying on of processes and operations in an area,
the Central Government shall follow the procedure hereinafter laid down.
(3) (a) Whenever it appears to the Central Government
that it is expedient to impose prohibition or restrictions on
the location of an industry or the carrying on of
processes and operations in an area, it may, by notification in
the Official Gazette and in such other manner as the Central Government may
deem necessary from time to time, given notice of its intention to do So.
(b) Every notification under clause (a) shall
give a brief description of the area, the industries, operations processes in
that area about which such notification pertains and also specify the reasons
for the imposition of prohibition or restrictions on the location of the
industries and carrying on of processes or operations in that area.
(c) Any person interested in filing an
objection against the imposition of prohibition or restriction on
carrying on of processes of operations as notified under clause
(a) may do so in writing to the Central Government within sixty days from the
date of publication of the notification in the Official Gazette.
(d) The Central Government shall, within a
period of one hundred and twenty days from the date of publication of the
notification in the Official Gazette, consider all tile objections received
against such notification and may 1[within
2[there hundred and sixty-five
days] from such date of publication,] impose prohibition or restrictions on
location of such industries and tile carrying on of any process or operation in
an area.
3[(4) Notwithstanding, anything contained in sub-rule (3), whenever it
appears to the Central Government that it is in public interest to do so, it
may dispense with the requirement of notice under clause (a) of sub-rule (3).]
1. Ins. by G.S.R. 562(E) dated 27th
May 1992.
2. Subs. by G.S.R. 884 (E) dated 20th
November 1992.
3. Ins. by G.S.R. 320(E) dated 16th
March 1994 (w.e.f. 16-03-1994).
1[6. Procedure for taking samples: -The Central Government of
the officer empowered to take samples under section II shall collect the sample
in sufficient quantity to be divided into two uniform parts and effectively
seal and suitably mark the same and permit the person from whom the sample is taken
to add his own seal or mark to all or any of the portions so scaled and
marked. In case where the
sample is made up in containers or small volumes and is likely to deteriorate
or be otherwise damaged if exposed, the Central Government or the officer
empowered shall take two of the said samples without opening, the containers
and suitably seal and mark the same.
The Central Government or the officer empowered shall dispose of the
samples so collected as follows: -
(i) One portion shall be handed over to the
person from whom the sample is taken under acknowledgement; and
(ii) The other portion shall be sent forthwith
to the environmental laboratory for analysis.]
1. Subs. by S.O. 64(E), dated 18th
January 1988, (w.e.f. 18-01-1988).
7. Service of notice. -The Central
Government or the officer empowered shall serve on the occupier or his
agent or person in charge of the place a notice then and there in
Form I of his intention to have the sample analyzed.
8. Procedure for submission
of samples for analysis, and the form of laboratory report thereon: -
(1) Sample taken for analysis
shall be sent by the Central Government of the official empowered to the
environmental laboratory by registered Post or through special messenger along
with Form II.
(2) Another copy of Form II together with
specimen impression of seals of the officer empowered to take samples along
with the seals/marks, if any, of the person from whom the sample is taken shall
be sent separately in a sealed cover by registered post or through a special
messenger to the environmental laboratory.
(3) The findings shall be recorded in Form
III in triplicate and signed by the Government Analyst and sent to the officer
from whom the sample is received for analysis.
(4) On receipt of the report
of the findings of the Government Analyst, the officer shall send one copy of
the report to the person from whom the sample was taken for analysis, the
second copy shall be retained by film for his records and the third copy shall
be kept by him to be produced in the Court before which proceedings, is, if any
are, instituted.
9. Functions of
environmental laboratories: - The following
shall be the functions of environmental laboratories.
(i) To evolve standardized methods for
sampling and analysis of various types
of environmental Pollutants;
(ii) To analyze samples sent by the Central
Government or the officers empowered under sub-section (1) of section 11:
(iii) To carry out such investigations as may be directed
by the Central Government to lay down standards for the quality of environment
and discharge of environmental pollutants, to monitor and to enforce the
standards laid down;
(iv). To send periodical reports regarding its
activities to the Central Government.
(v) To carry out such other functions as may
be entrusted to it by the Central Government from into time to time.
10. Qualifications of
Government Analyst: -A
person shall not be qualified for appointment or
recognized as a Government Analyst unless lie is a-
(a) Graduate in science from a recognized
University with five years experience in a laboratory engaged in environmental
investigations, testing or analysis; or
(b) Post graduate in science or a graduate in engineering or a graduate in medicine or equivalent with two
years experience in a laboratory engaged in environmental]
investigations, testing or analysis; or
(c) Post-graduate in environmental
science from a recognized University with two years experience in a laboratory
engaged in environmental investigation, testing or analysis.
11. Manner of giving notice: - The manner of giving notice under
clause (b) of section 19 shall be as follows, namely: -
(1) The notice shall be in writing in Form IV.
(2) The person giving notice may send notice to, -
(a) If the alleged offence has taken place in
a Union territory:
(i) The Central Board; and
(ii) The Ministry of Environmental and Forests
(represented by the Secretary of the Government of India);
(b) If the alleged offence has taken place in
a State:
(i) The State Board; and
(ii) The Government of the State (represented by the Secretary to
the State Government in-charge of environment); and
(iii) The Ministry of Environment and Forests
(represented by tile Secretary to the Government of India).
(3) The notice shall be sent by registered
post-acknowledgement due.
(4) The period of sixty days mentioned in
clause (b) of section 19 of the Environment (Protection) Act, 1986 shall be
reckoned from the date it is first received by one of the authorities mentioned
above.
1[12. Furnishing of information
to authorities and agencies in certain cases. - Where the discharge of
environmental pollutant in excess of the prescribed standard occurs or is apprehended to occur due
to any accident or other unforeseen act or event, the person in
charge of the place at which such discharge occurs or is apprehended to
occur shall forthwith intimate the fact of such occurrence or apprehension of
such occurrence to all the following authorities or agencies, namely: -
(i) The officer-in-charge of emergency or
disaster relief operations in a district or other region of a State or
Union territory specified by whatever (resignation, by the Government of the
said State or Union territory, and in whose jurisdiction the industry, process
or operation is located;
(ii) The Central Board or a State Board, as
the case may be, and its regional officer having local jurisdiction who have
been delegated powers under sections 20, 21, 23 of the Water (Prevention and
Control of Pollution) Act, 1974 (6 of 1974), and section 24 of the Air
(Prevention and Control of Pollution) Act, 1981 (14 of 1 981);
(iii) The Statutory authorities or agencies
specified in column 3 in relation to places mentioned in column 2 against
thereof of.] 2[Schedule V]
1. Ins. by S.O. 82(E), dated 16th
February, 1987 (w.e.f. 16.02.1987),
2. Subs. by G.S.R. 422 (E) dated 19th
May 1993 (w.e.f. 19-05-1993).
1[13. Prohibition and restriction on the handling of hazardous substances in
different areas: -
(1) The Central Government may
take into consideration the following factors while prohibiting of
restricting the handling of hazardous substances in different areas:
(i) The hazardous nature of the Substance
(either in qualitative or quantitative terms) as far as may be
in terms of its damage causing potential to the environmental, human beings,
other living creatures, plants and property;
(ii) The substances that it may be or likely to be or readily available as substitutes for the
substances proposed to be prohibited or restricted-
(iii) The indigenous availability of the
substitute, or the state of
technology available in the country for developing a safe, Substitute;
(iv). The gestation period that may be
necessary for gradual introduction of a new substitute with a view to
bringing about a total protection of Environment.
(v) Any other factor its may be considered by the Central Government to by relevant to
the protection of environment.
(2) While prohibiting or restricting the
handling of hazardous substances in an area including their imports exports the
Central Government shall follow the procedure herein after laid down-
(i) Whenever it appears to the Central
Government that it is expedient to impose prohibition or restriction on file
handling of hazardous substances in an area, it may, by notification in the
Official Gazette and in such other manner as the Central Government may deem
necessary from time to time, give notice of its intention to do so.
(ii) Every notification under clause (i) shall
give a brief description of the hazardous Substances and the geographical
region or the area to which such notification penalties and also specify the
reasons for the imposition of prohibition or restriction on the handling of
such hazardous substances in that region or area.
(iii) Any person interested in filing an
objection against the imposition of prohibition or restrictions on the handling
of hazardous substances as notified under clause (i) may do so in writing to
the Central Government within thirty days from the date of publication of the
notification in the Official Gazette.
(iv). The Central Government shall within a period
of sixty days from the date of publication of the notification in the Official
Gazette consider all the objections received against such notification and may
impose prohibition or restrictions
on the handling of hazardous substances in a region or an area.]
1. Ins. by G.S.R. 93(E) dated 27th
October 1989 (w.e.f. 27-10-1989).
1[14. Submission of environment 2[statement]: - Every person carrying on an
industry, operation or process requiring consent under section 25 of the Water
(Prevention and Control Of Pollution) Act, 1974 (6 of 1974) or under section 21
of the Air (Prevention and Control Of Pollution) Act, 1981 (14 of 1981) or both
or authorisation under the Hazardous Waters (Management and Handling) Rules,
1989 issued under the
Environment (Protection) Act, 1986 (29 of 1986) shall submit all environmental 2[statement] for the financial year
ending on the 31 st March in Form V to the concerned State
Pollution Control Board on or before the thirtieth day of September] every
year, beginning.
1. Ins. by G.S.R. 329(E) dated 13th
March 1992 (w.e.f. 13-03-1992).
2. Subs. by G.S.R. 386(E) dated 22nd
April 1993 (w.e.f. 22-04-1993).
SCHEDULE 1[1]
(See Rule 3)
|
Sl. No. |
Industry |
Parameter |
Standards |
||
|
1 |
2 |
3 |
4 |
||
|
1. |
Caustic
Soda Industry |
|
Concentration not to exceed, milligramme per liter
(except for pH and flow. |
||
|
|
|
Total
concentration
of mercury in the final effluent * |
0.01 |
||
|
Mercury
bearing waste-water generation (flow) pH |
10 kiloliters/tonne of caustic soda produced |
||||
|
|
|
*Final effluent is the combined from (a) Cell house, (b) Brine plant, (c) Chlorine handling, (d)
Hydrogen handling, (e) Hydrochloric acid plant. |
|||
|
2. |
Man-Made
fiber (synthetic) |
Concentration not to exceed, milligramme per liter
(except for pH and flow. |
|||
|
|
|
Suspended solids |
100 |
||
|
2[Bio-Chemical oxygen
demand, (3-days at 72 degree C)] |
30 |
||||
|
pH |
5.5 to 9.0 |
||||
|
3 |
Oil-refinery industry |
Concentration not to exceed, milligramme per liter
(except for pH and flow. |
|
||
|
Oil and grease |
10 7 |
||||
|
Phenol |
1 |
0.7 |
|||
|
Sulphide |
0.5 |
0.35 |
|||
|
2[Bio-Chemical oxygen
demand, (3-days at 27 degree c)] |
0.15 |
10.5 |
|||
|
Suspended solids |
20 |
14 |
|||
|
pH |
6 to 8.5 |
||||
|
4. |
Sugar Industry |
|
Concentration not to exceed, milligramme per liter
|
||
|
|
|
2[Bio-chemical oxygen demand, (3 days at 27degree C)] |
100 for disposal on land 30 for disposal in surface
waters |
||
|
Suspended Solids |
100 for disposal on land 30 for disposal in
surface waters |
||||
|
5. |
Thermal Power Plants |
|
Maximum, limiting concentration, milligramme per
liter (except for pH and temperature) |
||
|
|
Condenser cooling waters |
PH |
6.5 8.5 |
||
1. Renumbered as Sch. 1 by S.O. 82(E),
dated 16th February 1987 (w.e.f. 16-02-87).
2. Subs. by G.S.R. 176(E) 2nd
April 1996 (w.e.f. 3-4-1996).
|
Sl. No. |
Industry |
Parameter |
Standards |
|
1 |
2 |
3 |
4 |
|
|
(Once
through cooling system) |
Temperature |
Not
more than 50 C than the intake water temperature |
|
|
Free
available Chlorine |
0.5 |
|
|
Boiler
blowdowns |
Suspended
solids Oil
and grease Copper
(total) Iron
(total) |
100 |
|
|
20 |
|||
|
1.0 |
|||
|
1.0 |
|||
|
Cooling-tower
blowdown
|
Free
available chlorine |
0.5 |
|
|
Zinc |
1.0 |
||
|
Chromium
(total) |
0.2 |
||
|
Phosphate |
0.5 |
||
|
Other
corrosion inhibiting material |
Limit to be established on case by case basis by
Central Board in case of Union territories and State Board in case of State |
||
|
Ash-pond
effluent |
PH |
6.5-8.5 |
|
|
Suspended
solids |
100 |
||
|
Oil
and grease |
20 |
||
|
6. |
Cotton
textile industries (composite and Processing) |
|
Concentration
not to exceed, milligramme per litre (except for pH and bio-assay) |
|
Common: |
PH |
5.5
to 9 |
|
|
Suspended
solid |
100 |
||
|
1[Bio-chemical oxygen demand, (3 days at 270 C)] |
150 |
||
|
Oil
and grease |
10 |
||
|
Bio-assay
test |
90%
survival of fish after 96 hours |
||
|
|
Special: |
Total
chromium (as Cr) |
2 |
|
Sulphide
(as S) |
2 |
||
|
Phenolic
compounds (as
C6 H5 OH) |
5 |
1. Subs. by G.S.R. 176(E), dated 2nd,
April, 1996 (w.e.f. 3.4.1996).
The special parameters to be
stipulated by the Central Board in case of Union territories and State Boards
in case of States depending upon the dye used in the industry. Where the industry uses chrome dyes, sulphur
dyes and/or phenolic compounds in the dyeing/printing process, the limits on
chromium of 2 mg/litre, sulphides of 2 mg/litre, and phenolic compounds of 5
mg/litre, respectively shall be imposed.
Where the quality
requirement of the recipient system so warrants, the limit of BOD should be
lowered up to 30 according to the requirement by the State Boards for the
States and the Central Board for the Union territories.
A limit on sodium absorption
ratio of 26 should be imposed by the State Boards for the States and the
Central Board for the Union territories if the disposal of effluent is to be
made on land.
|
Sl.
No. |
Industry |
Parameter |
Standards |
|
1 |
2 |
3 |
4 |
|
7. |
Composite woolen mills |
|
Concentration not to exceed, milligramme per litre
(except for pH and bio-assay |
|
|
Common: |
Suspended
solids |
100 |
|
pH |
5.5 to 9.0 |
||
|
1[ Bio- chemical oxygen
demand, (3-days at 270 C)] |
100 |
||
|
Oil and Grease |
10 |
||
|
Bio-assay |
90% survival of fish after 96 hours |
||
|
Special |
Total chromium (as Cr) |
2 |
|
|
Sulphide (as S) |
2 |
||
|
Phenolic compound (as C6 H5
OH) |
5 |
1. Subs. by G.S.R. 176(E) dated 2nd
April 1996 (w.e.f 3.4.1996).
The special
parameters to be stipulated by the Central Board in case of Union territories
and State Boards in case of States depending upon the dye used in the
industry. Where the industry uses
chrome dyes, sulphur dyes and/or phenolic compounds in the dyeing/printing
process, the limits on chromium of 2 mg/ litre, sulphide of 2 mg/litre and
phenolic compounds of 5 mg/litre, respectively shall b( imposed.
Where the
quality requirement of the recipient system so warrants, the limit of BOD
should be lowered up to 30 according to the requirement by the State Boards for
the State and the Central Board for the Union territories.
A limit on sodium
absorption ratio of 26 should be imposed by the State Boards for the States and
the Central Board for the Union territories if the disposal of effluent is to
be made on land.
|
Sl. No. |
Industry |
Parameter |
Standards |
|
1[8 |
Composite woolen mills |
|
Concentration not to exceed, milligramme per litre
(except for pH and bio-assay) |
|
|
Common: |
Suspended solids |
100 |
|
|
|
PH |
6 t0 8.5 |
|
|
|
Temperature |
Shall not exceed 50 C above the ambient
temperature of the receiving body |
|
|
|
Mercury (as Hg) |
0.01 |
|
|
|
Hexavalent |
0.1 |
|
|
|
Chromium (as Cr) Total Chromium (as Cr) |
2.0 |
|
|
|
Copper (as Cu) |
3.0 |
|
|
|
Zinc (as Zn) |
5.0 |
|
|
|
Nickel (as Ni) |
3.0 |
|
|
|
Cadmium (as Cd) |
2.0 |
1. Ins. by S.O. 393(E) dated 16th
April 1987 (w.e.f 16.4.1987).
|
Sl. No. |
Industry |
Parameter |
Standards |
|
1 |
2 |
3 |
4 |
|
|
|
Chloride
(as Cl) |
1000 |
|
|
|
Sulphate
(as SO40) Phenolic Compounds as (C6 H5 OH) |
1000 |
|
|
|
Oil
and Grease |
10 |
|
|
|
Bio-assay
Test (with 1:8 dilution of effluents) |
90%
survival of test animals after 96 hours |
The standards of chlorides
and sulphates are applicable for discharge into inland and surface
watercourses. However, when discharged
on land for irrigation, the limit for chloride shall not be more than
600milligrammes per litre and the sodium absorption ratio shall not exceed 26.
|
9. |
Electroplating |
|
Concentration
not exceed, milligrammes per litre (except for pH and temperature) |
|
|
|
pH |
6.0
t0 9.0 |
|
|
|
Temperature |
Shall
not exceed 5 0 C above, the ambient temperature of the receiving body |
|
|
|
Oil
and Grease |
10 |
|
|
|
Suspended
Solids |
100 |
|
|
|
Cyanides
(as CN) |
0.2 |
|
|
|
Ammonical |
50 |
|
|
|
Nitrogen
(as N) total Residual |
1.0 |
|
|
|
Chloride
(as Cl) Cadmium (as Cd) |
2.0 |
|
|
|
Nickel
(as Ni) |
3.0 |
|
|
|
Zinc
(as Zn) |
5.0 |
|
|
|
Hexavalent |
0.1 |
|
|
|
Chromium
(as Cr) Total Chromium (as Cr) |
2.0 |
|
|
|
Copper
(as Cu) |
3.0 |
|
|
|
Lead
(as pb) |
0.1 |
|
|
|
Iron
(as Fe) |
3.0 |
|
|
|
Total
metal |
10.0 |
|
10. |
Cement
Plants |
|
Not
to exceed- milligrammes per normal cubic metre |
|
|
Plant
Capacity: 200
tonnes per day |
Total
dust (All
sections) |
100 |
|
|
Greater
than 200
tonnes per day |
Total
dust (All
sections) |
250 |
The Central and State Pollution Control Boards
may fix stringent standards, not exceeding 250 milligrammes per normal cubic
metre for smaller plants and 150 milligrammes per normal cubic metre for larger
plants if the industry is located in an area, which, in their opinion, requires
more stringent standards.
Where continuous monitoring
integrators are provided on dust emission lines, the integrated average values
over a period, to be fixed by die Central and State Boards but not exceeding 72
hours shall be considered instead of
momentary dust emission values for conformity to standards.]
|
Sl. No. |
Industry |
Parameter |
Standards |
|||
|
1 |
2 |
3 |
4 |
|||
|
1[11. |
Stone-crushing unit |
Suspended particulate matter |
The suspended particulate
matter measured between 3 metres and 10 metres from any process equipment of
a stone-crushing unit shall not exceed 600 micro-grammes per cubic metre.] |
|||
|
2[12. |
Coke ovens |
|
Concentrations in the effluents when discharged
into inland surface waters not to exceed milligramme per litre (except for
pH) |
|||
|
|
|
PH |
5.5-9.0 |
|||
|
|
|
3[Biochemical Oxygen |
30 |
|||
|
|
|
Demand (3 days at 27 0 C)] Suspended Solids |
100 |
|||
|
|
|
Phenolic Compounds (as C6 H5 OH) |
5 |
|||
|
|
|
Cyanides (as CN) |
0.2 |
|||
|
|
|
Oil & Grease |
10 |
|||
|
|
|
Ammonical Nitrogen (as N) |
50 |
|||
|
13. |
Synthetic Rubber |
|
Concentration in the effluents when discharged
into inland surface waters not to exceed milligramme per litre (except for
colour, and pH) |
|||
|
|
|
Colour |
Absent |
|||
|
|
|
pH |
5.5-9.0 |
|||
|
|
|
3[Biochemical Oxygen Demand
(3 days at 270 C)] |
50 |
|||
|
|
|
Chemical Oxygen Demand |
250 |
|||
|
|
|
Oil & Grease |
10.0 |
|||
|
14. |
Small Pulp and Paper Industry |
|
Concentration
not to exceed milligramme per litre (except for pH and sodium absorption
ratio) |
|||
|
|
Discharge |
pH |
5.5-9.0 |
|||
|
|
Into inland |
Suspended Solids |
100 |
|||
|
|
Surface water |
BOD |
30 |
|||
|
|
Disposal |
pH |
5.5-9.0 |
|||
|
|
On land |
Suspended Solids |
100 |
|||
|
|
|
BOD |
100 |
|||
|
|
|
Sodium absorption Ratio |
26 |
|||
1. Ins. by S.O. 443 (E) dated 18th
April 1987 (w.e.f 18.4.1987).
2. Ins. by S.O. 64(E) dated 18th
January 1988 (w.e.f 18.1.1988).
3. Subs. by G.S.R. 176(E) dated 2nd
April, 1996 (w.e.f 3.4.1996).
|
Sl. No. |
Industry |
Parameter |
Standards |
|
1 |
2 |
3 |
4 |
|
15. |
Fermentation Industry (Distilleries, Maltries and
Brewerise) |
|
Concentration in the effluent not to
exceed milligramme per litre (except for pH and colour & odour) |
|
|
|
PH |
5.5-9.0 |
|
|
|
Colour & odour |
1[All
efforts should be made to remove colour and unpleasant odour as far as
practicable] |
|
|
|
Suspended
Solids 2[BOD (3 days at 27 0 C)] |
100 |
|
|
|
Disposal into inland surface
water/river/stream |
30 mg /1- |
|
|
|
Disposal on land or for irrigation |
100 mg/1-.] |
3[Notes. -*(1) Waste water generation shall
not exceed 250 cubic metre per tonne of paper produced.]
4[* * *]
|
Sl. No. |
Industry |
Parameter |
Standards |
||||||||
|
1 |
2 |
3 |
4 |
||||||||
|
16. |
Leather Tanneries |
|
Concentration in the effluents
not to exceed milligramme per litre (except for pH and per cent sodium) |
||||||||
|
|
|
|
Inland Surface water |
Public Sewers |
Land for Irrigation |
Marine Coastal areas |
|||||
|
|
|
|
(a) |
(b) |
(c) |
(d) |
|||||
|
|
|
Suspended Solids |
100 |
600 |
200 |
100 |
|||||
|
|
|
2[BOD (3 days at 270C)] |
30 |
350 |
100 |
100 |
|||||
|
|
|
pH |
6.0-9.0 |
6.0-9.0 |
6.0-9.0 |
6.0-9.0 |
|||||
|
|
|
Chlorides (as Cl) |
1000 |
1000 |
600 |
- |
|||||
|
|
|
Hexavalent |
0.1 |
0.2 |
0.1 |
1.0 |
|||||
|
|
|
Chromium (Cr+6) Total Chromium (as Cr) |
2.0 |
2.0 |
2.0 |
- |
|||||
|
|
|
Sulphides (as S) |
2.0 |
5.0 |
- |
5.0 |
|||||
|
|
|
Sodium per sent |
- |
60 |
60 |
- |
|||||
|
|
|
Boron (as B) |
2.0 |
2.0 |
2.0 |
- |
|||||
|
|
|
Oil & Grease |
10 |
20 |
10 |
20 |
|||||
1. Subs. by S.O.
12(E), dated 8th January, 1990 (w.e.f 8-1-1990).
2. Subs. by G.S.R. 176(E) dated 2nd
April 1996 (w.e.f. 3-4-1996).
3. Added by S.O. 12(E), dated 8th
January 1990 (w.e.f. 8-1-1990).
4. Notes 2 to 7 omitted by G.S.R. 176(E),
dated 2nd April 1996 (w.e.f 3-4-1996).
|
Sl. So. |
Industry |
Parameter |
Standards |
||
|
1 |
2 |
3 |
4 |
||
|
17. |
Fertilizer Industry |
|
Concentration in the
effluents not to exceed milligramme per litre (except for pH) |
||
|
|
Effluents straight
nitrogenous Fertilizers Excluding the Calcium Ammonium Nitrate Fertilizer |
|
Plants Commissioned January 1, 1982 onwards |
Plants commissioned prior
to January 1, 1982 |
|
|
(a) |
(b) |
||||
|
|
|
pH |
6.5-8.0 |
6.5-8.0 |
|
|
|
|
Ammonical Nitrogen |
50 |
75 |
|
|
|
|
Total Kjeldahl Nitrogen |
100 |
150 |
|
|
|
|
Free Ammonical Nitrogen |
4 |
4 |
|
|
|
|
Nitrate Nitrogen |
10 |
10 |
|
|
|
|
|
|
|
|
|
|
|
Cyanide as CN |
0.2 |
0.2 |
|
|
|
|
Vanadium as V |
0.2 |
0.2 |
|
|
|
|
Arsenic as As |
0.2 |
0.2 |
|
|
|
|
Suspended Solids |
100 |
100 |
|
|
|
|
Oil and Grease |
10 |
10 |
|
|
|
|
*Hexavalent Chromium as Cr |
0.1 |
0.1 |
|
|
|
|
*Total Chromium as Cr |
2.0 |
2.0 |
|
|
|
To be complied with at the
outlet of Chromate removal unit. Straight Nitrogenous Fertilizers Including
Calcium Ammonium Nitrate and Ammonium
Nitrate Fertilizers |
|
Plants Commissioned
January 1, 1982 0nwards |
Plants Commissioned Prior
to January 1, 1982 |
|
|
|
|
|
(a) |
(b) |
|
|
|
|
pH |
6.5-80 |
6.5-8.0 |
|
|
|
|
Ammonical Nitrogen |
50 |
75 |
|
|
|
|
Total Kjeldahl Nitrogen |
100 |
150 |
|
|
|
|
Free Ammonical Nitrogen |
4 |
4 |
|
|
|
|
Nitrate Nitrogen |
20 |
20 |
|
|
|
|
Cyanide as CN |
0.2 |
0.2 |
|
|
|
|
Vanadium as V |
0.2 |
0.2 |
|
|
|
|
Arsenic as As |
0.2 |
0.2 |
|
|
|
|
Suspended Solids |
100 |
100 |
|
|
|
|
Oil and Grease |
10 |
10 |
|
|
|
|
*Hexavalent |
0.1 |
0.1 |
|
|
|
|
Chromium as Cr* Total
Chromium |
2.0 |
2.0 |
|
|
|
* To be complied with at
the outlet of Chromate removal unit. Complex Fertilizers, excluding Calcium
Ammonium Nitrate, Ammonium Nitrate & Ammonium Nitrophosphate Fertilizes |
|
Plants commissioned
January 1, 1982 0nwards |
Plants commissioned Prior
to January 1, 1982 |
|
|
|
|
|
(a) |
(b) |
|
|
|
|
pH |
6.5-80 |
6.5-80 |
|
|
|
|
Ammonical Nitrogen |
50 |
75 |
|
|
|
|
Free Ammonical |
4 |
4 |
|
|
|
|
Nitrogen Total Kjeldahl
Nitrogen |
100 |
150 |
|
|
|
|
Nitrate Nitrogen |
10 |
10 |
|
|
|
|
Cyanide as CN |
0.2 |
0.2 |
|
|
|
|
Vanadium as V |
0.2 |
0.2 |
|
|
|
|
Arsenic as As |
0.2 |
0.2 |
|
|
|
|
Phosphate as p |
5 |
5 |
|
|
|
|
Oil and Grease |
10 |
10 |
|
|
|
|
Suspended Solids |
100 |
100 |
|
|
|
|
*Fluoride as f |
10 |
10 |
|
|
|
|
*Hexavalent |
0.1 |
0.1 |
|
|
|
|
Chromium as Cr **total Chromium as Cr |
2.0 |
2.0 |
|
|
|
Complex Fertilizers,
including Calcium Ammonium Nitrate, Ammonium Nitrate Ammonium Nitrophosphate
Fertilizers |
|
|
|
|
|
|
|
|
Plants Commissioned
January 1,1982 onwards |
Plants Commissioned prior
to January 1, 1982 |
|
|
|
|
|
(a) |
(b) |
|
|
|
|
pH |
6.5-8.0 |
6.5-8.0 |
|
|
|
|
Ammonical Nitrogen |
50 |
75 |
|
|
|
|
Free Ammonical Nitrate |
100 |
100 |
|
|
|
|
Nitrate Nitrogen |
20 |
20 |
|
|
|
|
Cyanide as CN |
0.2 |
0.2 |
|
|
|
|
Vanadium as v |
0.2 |
0.2 |
|
|
|
|
Arsenic as |
0.2 |
0.2 |
|
|
|
|
Phosphate as P |
5 |
5 |
|
|
|
|
Oil and Grease |
10 |
10 |
|
|
|
|
Suspended Solids |
100 |
100 |
|
|
|
|
* Fluoride as F |
10 |
10 |
|
|
|
|
|
(a) |
(b) |
|
|
|
|
** Hexavalent |
0.1 |
0.1 |
|
|
|
|
Chromium as Cr |
|
|
|
|
|
|
**Total Chromium as Cr |
2.0 |
2.0 |
|
|
* To be
complied with at the outlet of Fluoride removal unit. If the recipient system
so demands, Fluoride as F shall be limited to 1.5 mg/1. |
|||||
|
**To be
complied with at the outlet of Chromate removal unit. |
|||||
|
|
Straight Phosphatic Fertilizers |
PH |
7.0-9.0 |
|
|
|
Phosphate as P |
5 |
|
|
|
Oil and Grease |
10 |
|
|
|
Suspended Solids |
100 |
|
|
|
*Fluoride as F |
10 |
|
|
|
**Hexavalent |
0.1 |
|
|
|
Chromium as Cr **Total Chromium as Cr |
2.0 |
|
|
Emissions |
|
|
|
|
Phosphatic Fertilizers (Fluoride and Particulate matter emission |
Phosphoric acid manufacturing Granulation, mixing
and grinding of rock phosphate |
25 milligramme per normal Cubic metre as total Fluoride 150 milligramme per normal cubic metre of
particulate matter |
|
|
--Urea (particulate matter emission) |
Prilling Tower Commissioned prior to 1-1-1982
Commissioned after 1-1-1982 |
150 milligramme per normal cubic metre or 2
Kilogramme per tonne of product 50 milligramme per normal cubic metre or 0.5
Kilogramme per tonne of product |
*To be complied with at the
outlet of Fluoride removal unit. If the recipient system so demands, Fluoride
as F shall be limited to 1.5 mg/1
**To be complied with at the
outlet of Chromate removal unit.
|
18. |
Aluminium |
Particulate Matter Emissions: __Calcination ___Smelting |
250 milligramme per normal cubic metre of
particulate matter 150 milligramme per normal cubic metre of particulate
matter |
|
19. |
Calcium Carbide |
Particulate Matter Emissions: __Kiln __Arc Furnace |
250 milligramme per normal cubic metre 150 milligramme per normal cubic metre |
|
20. |
Carbon Black |
Particulate Matter Emission: |
150 milligramme per normal cubic metre |
|
21. |
Copper, Lead and Zinc Smelting |
Particulate Matter Emission in concentrator Emission of Oxides of suphur in Smelter &
Convertor |
150 milligramme per normal cubic metre off-gases must be utilised for sulphuric acid
manufacture. The limits of sulphur dioxide emission from stock shall not
exceed 4 kilogramme per tonne of concentrated (one hundred per cent) acid
produced |
|
22. |
Nitric Acid (emission of oxides of nitrogen) |
Emission of Oxides Nitrogen |
3 kilogramme of oxides of nitrogen per tonne of
weak acid (before concentration) produced |
|
23. |
Sulphuric Acid (emission of Sulphur dioxide and
acid mist) |
Sulphur dioxide Emissions Acid Mist |
4 kilogramme per tonne of concentrated (On hundred
per cent)acid produced 50 milligramme per normal cubic metre |
|
24. |
Iron &Steel (Integrated) |
Particulate Matter Emission __Sintering Plant __Steel making __during normal operations __during oxygen lancing __Rolling Mill __Carbon monoxide from coke oven |
150 milligramme per normal cubic metre 150 milligramme per normal cubic metre 400 milligramme per normal cubic metre 150 milligramme per normal cubic metre 3 kilogramme per tonne of coke produced] |
|
1[25. |
Thermal Power Plants |
*Particulate matter Emissions: |
|
*Depending upon the
requirement of local situation, such as protected area, the Sate Pollution
Control Boards and other implementing agencies under the Environment
(Protection) Act, 1986, may prescribe a limit of 150 milligramme per normal
cubic metre, irrespective of generation capacity of the plant.
|
|
|
__generation capacity 210 MW or more |
150 milligramme per normal cubic metre |
|
|
|
__generation capacity less than 210 MW |
350
milligramme per normal cubic metre |
|
26. |
Natural rubber industry |
|
Concentration in the effluents not to exceed
milligramme per litre (exceed for pH) |
|
|
__Discharge into inland Colour & Odour surface
waters |
|
Absent |
|
|
|
PH |
6.0-9.0 |
|
|
|
BOD |
50 |
|
|
|
COD |
250 |
|
|
|
Oil & Grease |
10 |
|
|
|
Sulphides |
2 |
|
|
|
Total Kjeldhal Nitrogen |
100 |
|
|
|
Dissolved phosphate (as P) |
5 |
|
|
|
Suspended solids |
100 |
|
|
|
Dissolved solids (inorganic |
2100 |
|
|
|
Ammonical nitrogen (as N) |
50 |
|
|
|
Free ammonia (as NH3 |
5 |
|
|
__Disposal on land for Colour & Odour
irrigation |
|
Absent |
|
|
|
pH |
6.0-8.0 |
|
|
|
BOD |
100 |
|
|
|
COD |
250 |
1. Ins. by S.O. 8 (E) dated 3rd
January 1989 (w.e.f. 3.1.1989).
|
|
|
Oil & Grease |
10 |
|
|
|
Suspended solids |
200 |
|
|
|
Dissolved |
2100] |
|
1[27. |
All type of Asbestos |
Emissions |
|
|
|
Manufacturing units: |
__Pure asbestos material |
|
|
|
(including all processes |
__total dust |
4 fibre */cc |
|
|
Involving the use of Asbestos) |
|
2 mg/m3 (normal) |
*Fibre of length more than 5
micrometre and diameter less than 3 micrometre with an aspect ratio of 3 or
more.
|
28. |
Chlor Alkali (Caustic soda) |
Emissions |
Concentration in mg/m2 (normal) |
|
|
(a) Mercury cell |
Mercury (from hydrogen gasholder stack) |
0.2 |
|
|
(b) All Processes |
Chlorine (from hypo tower) |
15.0 |
|
|
(c) All processes |
Hydrochloric acid vapour and Mist (from hydrochloric acid plant) |
35.0 |
|
29. |
Large pulp and paper |
Emissions |
Concentration in mg/m2 (normal) |
|
|
|
Particulate matter |
250 ** |
|
|
|
H2S |
10 |
**This standard of 250 mg/m3
(normal) shall apply only for a period of 3 years with effect from the date on
which the Environment (Protection) Second Amendment Rules, 1989, came into
force. After three years the standard
to be applicable is 15 mg/m3 (normal).
|
30. |
Integrated Iron and Steel Plants: |
|
|
|
|
|
I. Emissions |
|
|
|
(a)Coke oven |
Particulate matter |
50 |
|
|
(b) Refractory material particulate matter Plant |
|
150 |
|
|
|
II. Effluents |
Concentration in mg/litre (except for pH) |
|
|
(a) Coke oven By product plant: |
pH |
6.0-8.5 |
|
|
|
Suspended solids |
100 |
|
|
|
Phenol |
1.0 |
|
|
|
Cyanide |
0.2 |
1. Ins. by G.S.R. 913(E) dated 24th
October, 1989 (w.e.f 24-10-1989).
|
|
|
1[BOD (3 days at 270 C)] |
30 |
|
|
|
COD |
250 |
|
|
|
Ammonical nitrogen |
50 |
|
|
|
Oil and Grease |
10 |
|
|
(b) Other plants such as sintering plants, blast
furnace, steel |
|
|
|
|
Melting and rolling mill: |
pH |
6.0-9.0 |
|
|
|
Suspended solids |
100 |
|
|
|
Oil and Grease |
10 |
|
31. |
Reheating (Reverberatory) Furnaces: |
Emissions |
Concentration in mg/m3 (normal0 |
|
|
Capacity: All sizes |
|
150 |
|
|
Sensitive area |
Particulate matter |
|
|
|
Other area |
Particulate matter |
450] |
|
2[32. |
Foundries: |
Emissions |
|
|
|
(a) Cupola Capacity (melting rate); Less than 3 MT/hr. |
Particulate matter |
450 |
|
|
3MT/ hr. and above |
Particulate Matter |
150 |
Note. - It is essential that the stack is
constructed over the cupola beyond the charging door and the emissions are
directed through the stack which should be at least six times the diameter of
the cupola.
|
|
(b) Arc Furnace |
|
|
|
|
Capacity: All sizes |
Particulate Matter |
150 |
|
|
(b)Induction furnaces Capacity: All sizes |
Particulate Matter |
150 |
Note. -In respect of arc furnaces
and induction furnaces, provision has to be made for collecting the fumes
before discharging the emissions through the stack.
|
33. |
Thermal Power Plants |
Stack height/limits |
|
|
|
|
Power generation capacity: |
|
|
|
|
-500 MW and above |
275 |
|
|
|
-275 MV/210 MW and above to |
220 |
|
|
|
Less than 500 MW |
|
|
|
|
Less than 20OMW/210 MW |
H = 14(Q)0.3 where Q is emission rate
of SO2 in kg/hr. and H is
stack height in metres. |
1. Subs. by G.S.R. 176(E) dated 2nd
April 1996 (w.e.f. 3-4-1996).
2. Ins. by G.S.R. 742(E) dated 30th
August 1990 (w.e.f. 30-8-1990).
|
|
|
Steam generating
capacity: |
|
|
|
|
Less than 2 ton/hr. |
2-1/2 times the neighboring building height or 9
metres (whichever is more) |
|
|
|
-More than 2 ton/hr. to 5 ton/hr |
12 |
|
|
|
-More than 5 ton/hr. to 10 ton/hr. |
15 |
|
|
|
-More than 10ton/hr. |
18 |
|
|
|
__More than 15 ton/hr. to 20 ton/hr. |
15 |
|
|
|
__More than 20 ton/hr. to 25 ton/hr. |
24 |
|
|
|
__More than 25 ton/hr. to 30 ton/hr. |
27 |
|
|
|
__More than 30 ton/hr. |
30 or using formula H=14(Q)0.3 (Whichever is more) where Q is emission rate of
S02 in kg/hr. and H is stack height in metres |
|
|
|
|
|
|
34. |
Shall boilers |
Emissions |
|
|
|
Capacity of boiler |
Particulate Matter |
|
|
|
_Less than 2 ton/hr. |
|
1600 |
|
|
-2 to 15 ton/hr. |
|
1200 |
|
|
-More than 15 ton/hr. |
|
150 |
|
*All emissions normalized to 12 per cent carbon
dioxide |
|||
|
35. |
Oil refineries (Sulphur dioxide) |
Emissions |
|
|
|
|
_Distillation (Atmospheric plus vacuum) |
0.25 kg/MT of feed** |
|
|
|
_Catalytic cracker |
2.5 kg/MT of feed |
|
|
|
_Sulphur recovery unit |
120 kg/MT of sulphur in the feed |
|
**Feed indicates the feed
for that part of the process under consideration only. |
|||
|
36. |
Aluminium Plants |
Emissions |
|
|
|
(a)Aluminium plants: |
|
|
|
|
(i) Raw material handling |
Primary and secondary crusher Particulate Matter |
150 |
|
|
(ii) Precipitation area |
Particulate Matter |
250 |
|
|
_Calcination |
Carbon monoxide Stack height |
1% max. H= 14(Q)0.3 where Q is emission rate of
SO2 in kg/hr. and H is stack height in metres |
|
|
(b) Smelter plants |
|
|
|
|
(i) Green anode shop |
Particulate Matter |
150 |
|
|
(ii) Anode bake oven |
Particulate Matter Total fluoride (F) |
150 0.3 kg/MT of Aluminium |
|
|
(iii) Potroom |
Particulate Matter Total fluoride (F) VSS |
150 4.7 kg/Mt of Aluminium produced |
|
Sl. No. |
Industry |
Parameter |
Standards (Concentrations in mg/1 except for pH
temperature specific pesticideds and Bio-assay test) |
|
(1) |
(2) |
(3) |
(4) |
|
|
|
HSSs |
6.0 kg/MT of Aluminium produced |
|
|
|
PBSW |
2.5 kg/MT of Aluminium produced |
|
|
|
PBCW |
1.0 kg/MT of Aluminium produced |
|
|
|
Stack height |
H= 14(Q)0.3 Where Q is emission rate of
SO2 in kg/hr. and H is stack height in metres |
|
Note. - VSS= Vertical stud soderberg HSS= Horizontal stud soderberg PBSW= Prebacked side worked PBCW= Prebacked centre worked |
|||
|
37. |
Stone crushing unit |
Suspended Particulate Matter (SPM) |
The standards consist of two parts: |
|
|
|
|
(i)Implementation of the following pollution
control measures: |
|
|
|
|
(a) Dust
containment cum suppression system of the equipment |
|
|
|
|
(b) Construction of wind breaking walls. |
|
|
|
|
(c) Construction
of the metalled roads within the premises. |
|
|
|
|
(d) Regular
cleaning and wetting of the ground within the premises. |
|
|
|
|
(e) Growing
of a green belt along the periphery. |
|
|
|
|
(ii) Quantitative
standard for the SPM: |
|
|
|
|
The suspended Particulate Matter contribution value
at a distance of 40 metres from a controlled isolated as well as from a unit
located in a cluster should be less than 600mg/Nm3. The
measurements are to be conducted at least twice a month for all the 12 months
in a year. |
|
38. |
Petrochemicals (Basic and Effluents intermediates) |
PH |
6.5-8.5 |
|
|
|
1[BOD (3 days at 270
C)] |
50 |
1. Subs. by
G.S.R. 176(E) dated 2nd April 1996 (w.e.f. 3-4-1996).
|
Sl. No. |
Industry |
Parameter |
Standards (Concentrations
in mg/1 except for pH temperature specific pesticideds and Bio-assay test) |
|
(1) |
(2) |
(3) |
(4) |
|
|
|
**Phenol |
5 |
|
|
|
Sulphide (as S) |
2 |
|
|
|
COD |
250 |
|
|
|
Cyanide (as CN) |
0.2 |
|
|
|
***Fluoride (as F) |
15 |
|
|
|
Total suspended solids |
1000 |
|
|
|
Hexavalent Chromium (as CR0 |
0.1 |
|
|
|
****Total Chromium (as CR) |
2.0 |
|
*State Boards may prescribe the BOD value of 30
mg/l if the recipient system so demands. **The limit for phenol shall be conformed to at
the outlet of effluent treatment of phenol plant. However, at the final
disposal point, the limit shall be less than I mg/1. ***The limit for fluoride shall be conformed to at
the outlet of fluoride removal unit.
However, at the disposal point fluoride concentration shall be lower
than 5 mg/1. ****The limits for total and hexavalent chromium
shall be conformed to at the outlet of the chromate removal unit. This implies that in the final treated
effluent, total and hexavalent chromium shall be lower than prescribed
herein. |
|||
|
39. |
Pharmaceutical Manufacturing and formulation industry |
Effluents |
|
|
|
|
1. pH |
5.5-9.0 |
|
|
|
2. Oil and Grease |
10 |
|
|
|
3. Total suspended solids |
100 |
|
|
|
4. 1[BOD
(3 days at 27 0 C)] |
30 |
|
|
|
5. Bio-assay test |
90% survival of fish after 96 hrs. in 100%
effluent |
|
|
|
6. Mercury |
0.01 |
|
|
|
7. Arsenic |
0.20 |
|
|
|
8. Chromium (Hexavalent) |
0.10 |
|
|
|
9. Lead |
.10 |
|
|
|
10. Cyanide |
0.10 |
|
|
|
11. Phenolics (as C6 H5 OH) |
1.00 |
|
|
|
12. Sulphides (as S) |
2.00 |
|
|
|
13. Phosphates (as P) |
5.00 |
Note. -
(1) Parameters listed as I to 13 are
compulsory for formulators. However,
the remaining parameters (6 to 13) will be optional for others.
(2) State Board may prescribe limit for
chemical oxygen demand (COD) correlated with BOD limit.
(3) State Board may prescribe limit for total
dissolved solids depending upon uses of recipient water body.
(4) Limits should be complied with at the
terminal of the treatment unit before letting out of the factory boundary
limits.
(5) For the
compliance of limits, analysis should be done in the composite sample collected
every hour for a period of 8 hours.
|
40. |
Pesticide Manufacturing and Formulation industry |
Effluents |
|
|
|
|
1. Temperature |
Shall not exceed 50 C above the
receiving water temperature |
|
|
|
2. pH |
6.5-8.5 |
|
|
|
3. Oil and Grease |
10 |
|
|
|
4. 1[BOD(3days at 27 0 C)] |
30 |
|
|
|
5. Total suspended solids |
100 |
|
|
|
6. Bio-assay test |
90 % survival of fish after 96%hours in 100 per
cent effluent |
|
|
|
7. (a) Specific pesticides: |
|
|
|
|
Benzene hexachloride |
10 |
|
|
|
Carboryl |
10 |
|
|
|
DDT |
10 |
|
|
|
Endosulfan |
10 |
|
|
|
Diamethoate |
450 |
|
|
|
Fenitrothion |
10 |
|
|
|
Malathion |
10 |
|
|
|
Phorate |
10 |
|
|
|
Methyl parathion |
10 |
|
|
|
Phenthoate |
10 |
|
|
|
Pyrethrums |
10 |
|
|
|
Copper oxychloride |
9600 |
|
|
|
Copper sulphate |
50 |
|
|
|
Ziram |
1000 |
|
|
|
Sulphur |
30 |
|
|
|
Paraquat |
2300 |
|
|
|
Proponil |
7300 |
|
|
|
Nitrogen |
780 |
|
|
|
(b) Heavy metals: |
|
|
|
|
Copper |
1.00 |
|
|
|
Manganese |
1.00 |
|
|
|
Zinc |
1.00 |
|
|
|
Mercury |
0.01 |
|
|
|
Tin |
0.10 |
|
|
|
Any other metal like |
Shall not exceed 5 times the drinking water
standards |
|
|
|
(c) Organics: |
|
|
|
|
Phenol and phenolic Compounds as C6 H5 OH |
1.0 |
|
|
|
(d) Inorganics: Arenics (as AS) |
0.2 |
1. Subs. by G.S.R. 176(E) dated 2nd
April 1996 (w.e.f 3-4-1996).
|
|
|
Cyanide (as CN) |
0.2 |
|
|
|
Nitrate (as NO3 |
50.0 |
|
|
|
Phosphate (as P) |
5.0 |
Notes. -
1. Limits should be complied with at the
end of the treatment plant before any dilution.
2. Bio-assay test should be carried out
with available species of fish in receiving water.
3. State Boards may prescribe limits of
total dissolved solids (TDS) sulphates and chlorides depending on the use of
recipient water body.
4. State Board may prescribe COD limit
correlated with BOD limits,
5. Pesticides
are known to have metabolites and isomers.
If they are found in significant concentration, standards may be
prescribed for those in the list by Central or State Board.
6. Industries are required to analyse
pesticides in waste water by advanced analytical method such as GLC/HPLC.
7. All the parameters will be compulsory for
formulators, for others, the 7th will be optional.
|
41. |
Tannery (after primary treatment) Disposal:
Channel/Conduit Carrying waste waters to secondary treatment plants Type of tanneries -Chromo tanneries/combined chrome and vegetable
tanneries |
Effluents |
|
|
|
|
pH |
6.0-8.5 |
|
|
|
SS |
Not
to exceed 600 |
|
|
|
Chromium
concentration after treatment in the chrome waste water stream |
45 |
|
|
__Vegetable
tanneries |
pH |
6.5-9.0 |
|
|
|
SS |
Not
to exceed 600 |
Note. - The above
standards will apply to those tannery units which have made full contribution
to a Common Effluent Treatment Plant (CEIT) comprising secondary treatment.
Those who have not contributed will be governed by earlier Notification No.
S.O. 64(E), dated January 18, 1988:
|
42. |
Paint
industry (Waste-water
discharge) |
Effluents |
|
|
|
|
PH |
6.0-8.5 |
|
|
|
Suspended |
100 |
|
|
|
Solids BOD5
20 0 C |
50 |
|
|
|
Phenolics
as C6 H5 OH |
1.0 |
|
|
|
Oil
and Grease |
10.0 |
|
|
|
Bio-assay
test |
90
per cent survival in 96 hours |
|
|
|
Lead
as pb Chromium
as Cr |
0.1 |
|
|
|
Hexavalent |
2.0 |
|
|
|
Total |
2.0 |
|
|
|
Copper
as Cu |
2.0 |
|
|
|
Nickel
as Ni |
2.0 |
|
|
|
Zinc
as Zn |
5.0 |
|
|
|
Total
heavy metals |
7.0 |
|
43. |
Inorganic
chemical |
Effluents |
|
|
|
Industry
(Waste-water discharge) Part 1 (metal compounds of Chromium, Manganese,
Nickel, |
PH Chromium
as Cr Hexavalent Total |
6.0-8.5 0.1 2.0 |
|
|
Lead
and Mercury |
Manganese
as Mn |
2.0 |
|
|
|
Nickel
as Ni |
2.0 |
|
|
|
Copper
as Cu |
2.0 |
|
|
|
Zinc
as Zn |
5.0 |
|
|
|
Cadmium
as Cd |
0.2 |
|
|
|
Lead
as pb |
0.1 |
|
|
|
Mercury
as Hg |
0.01 |
|
|
|
Cyanide
as CN |
0.2 |
|
|
|
Oil
and Grease |
10.0 |
|
|
|
Suspended
solids |
30.0 |
In addition to the above, total heavy metals are to
be limited to 7 mg/1.
|
44. |
Bullion
Refining (Waste-water
discharge |
Effluents pH |
6.5-8.5 |
|
|
|
Cyanide
as CN |
0.2 |
|
|
|
Sulphide
as S |
0.2 |
|
|
|
Nitrate
as N |
10.0 |
|
|
|
Free
Cl2 and Cl |
1.0 |
|
|
|
Zinc
as Zn |
5.0 |
|
|
|
Copper
as Cu |
2.0 |
|
|
|
Nickel
as Ni |
2.0 |
|
|
|
Arsenic
as As |
0.1 |
|
|
|
Cadmium
as Cd |
0.2 |
|
|
|
Oil
and Grease |
10.0 |
|
|
|
Suspended
solids |
100 |
|
45. |
Dye
and Dye Intermediate |
|
|
|
|
Industry |
Effluents |
|
|
|
(Waste-water
discharge) |
pH |
6.0-8.5 |
|
|
|
Colour,
Hazen Unit |
400.0 |
|
|
|
Suspended
solids |
100.0 |
|
|
|
BOD5
20 0C |
100.0 |
|
|
|
Oil
and Grease |
10.0 |
|
|
|
Phenolies
as C6 H5 OH |
1.0 |
|
|
|
Cadmium
as Cd |
0.2 |
|
|
|
Copper
as Cu |
2.0 |
|
|
|
Manganese
as Mn |
2.0 |
|
|
|
Lead
as pb |
0.1 |
|
|
|
Mercury
as Hg |
0.01 |
|
|
|
Nickel
as Ni |
2.0 |
|
|
|
Zinc
as Zn |
5.0 |
|
|
|
Chromium
as Cr |
0.1 |
|
|
|
Hexavalent Total |
2.0 |
|
|
|
Bio-assay
test |
90
% survival in 96 hours |
|
Sl. No. |
Category |
Standards, Db (A) |
|
(1) |
(2) |
(3) |
|
46. |
Noise limits for automobiles (free field at one metre in dB (A) at the manufacturing stage) to be achieved by the year 1992 |
|
|
|
(a)
Motorcycles, scooters and three wheelers |
80 |
|
|
(b)
Passenger cars |
82 |
|
|
(c)
Passenger or commercial vehicles up to 4 MT |
85 |
|
|
(d)
Passenger of commercial vehicles above 4 MT and up to 12 MT |
89 |
|
|
(e)
Passenger or commercial vehicles exceeding 12 MT |
91 |
|
47. |
Domestic
appliances and construction equipments at the manufacturing stage to be
achieved by the year 1993 |
|
|
|
(a)
Window air-conditioners of 1 ton to 1.5 ton |
68 |
|
|
(b)
Air-coolers |
60 |
|
|
(c)
Refrigerators |
46 |
|
|
(d)
Diesel generators for domestic purposes |
85-90 |
|
|
(e)
Compactors (rollers) front loaders, concrete mixers, cranes (movable)
vibrators and saws. |
75] |
|
Sl. No. |
Industry |
Parameter |
Standards |
|
(1) |
(2) |
(3) |
(4) |
|
1[48. |
GLASS
INDUSTRY |
Emissions |
|
|
|
A.
Sodalime and Borosilicate and other special glass (other than lead) (a)
Furnace; Capacity |
|
|
1. Ins. by G.S.R. 93 (E) dated 21st
February 1991 (w.e.f. 27-02-1991).
|
|
(i)
Up to a product draw capacity of 60 Mt/Day |
Particulate
matter |
20kg/hr |
|
|
(ii)
Product draw capacity more than 60 Mt/Day |
Particulate
matter |
0.8
kg/Mt. Of product drawn |
|
|
(iii)
For all capacities |
Stack
height Total
fluorides |
H=
14 (Q) 0.3 where Q is the emission rate of SO2 in Kg/hr. and H is stack
height in metres. 5.0
mg/NM3 Use of low nox burners in new plants. |
|
|
(b) Implementation of the following measures for fugitive emission control from other sections: |
|
|
|
|
(i) Raw materials should be transported in leak proof containers. (ii)
Cullet preparation should be dust-free using water spraying. |
|
|
|
|
(iii)
Batch preparation section should be covered. |
|
|
|
B. |
Lead
glass |
|
|
|
|
(a)
Furnace: |
|
|
|
|
All
capacities |
Particulate
matter Lead |
50
mg./NM3 20
mg/ NM3 |
|
|
(b)
Implementation of the following measures for fugitive emission control
from other sections: (i) Batch
mixing, proportioning section and transfer points should be covered
and it should be connected to control equipments to meet following
standards: |
Particulate
matter Lead |
50
mg/NM 3 20
mg/ NM 3 |
|
|
(ii) Minimum stack height should be 30 meter in lead glass units. |
|
|
|
|
(c)Pot
Furnace at Firozabad Furnace: |
Particulate
matter |
1200
mg/NM 3 |
Note. -
Depending upon
local environmental conditions, State/Central Pollution Control Board can
prescribe more stringent standards than those prescribed above.
|
|
Glass Industry (For all categories) |
Effluents: pH |
6.5-8.5 |
|
|
|
Total suspended solids |
100 mg/1 |
|
|
|
Oil and Grease |
10 mg/1 |
|
49. |
Lim Kiln |
Stack Height |
|
|
|
Capacity:- |
Stack Height |
|
|
|
Up-to 5T/Day |
|
A hood should be provided with a stack of 30 metre height from ground
level (including kiln height). |
|
|
Above 5T/Day |
Stack Height |
H=14 (Q) 0..3 where Q is emission rate
of SO2 in Kg/hr and H= Stack height in metres. |
|
|
More than 5Tday and upto 40T/Day. |
Particulate matter |
500mg/NM3 |
|
|
Above 49T/Day |
Particulate matter |
150 mg/NM3 |
|
50. |
*Slaughter House, Meat and Sea Food Industry:_ |
|
|
|
A. |
Slaughter House (a) Above 70 TLWK |
BOD5 at 20 0C Suspended solids Oil and Grease |
100 100 10 |
|
|
(b) 70 TLWK and below |
BOD5 at 20 0C |
500 |
|
B. |
Meat
Processing (a) Frozen Meat |
BOD5 20 0C Suspended solids Oil and Grease |
30 50 10 |
|
|
(b) Raw Meat from own Slaughter house |
BOD5 at 20 0C Suspended solids Oil and grease |
30 50 10 |
|
|
(c) Raw meat from other source |
|
Disposal via screen and septic tank |
|
C. |
Sea Food Industry |
BOD5 at 20 0C Suspended solids Oil and Grease |
30 50 10 |
Note: -
(i) TLWL- Total Live Weight
Killed. (ii) In case of disposal into municipal sewer where sewage is treated
the industries shall install screen and oil and grease separation units. (iii)
The industries having slaughter house
along with meat processing units will be considered in meat processing category
as far as standards are concerned.
* The emission standards from Boiler House shall conform to the standards already prescribed under E(P) Act, 1986, vide notification No. GSR 742 (E), dated 30-08-1990: See [1991] 70 Comp. Cas. (St.) 5.
|
51. |
Food
and Fruit Processing Industry: |
Effluents |
Concentration
not to exceed mg/1 except pH |
Quantum
gm/MT of product |
|
Category: |
|
|
|
|
|
A. |
Soft
Drinks (a)
Fruit based/synthetic (More than 0.4 MT/Day Bottles and tetra pack |
|
|
|
|
PH |
6.5-8.5 |
----------- |
||
|
Suspended
solids |
100 |
|
||
|
Oil
and Grease |
10 |
|
||
|
BOD5
at 20 0C |
30 |
|
||
|
|
(b)
Synthetic (Less than) 0.4 MT/Day) |
|
Disposal
via Septic
tank |
|
|
B. |
Fruit
and vegetables |
|
|
|
|
(a)
Above 0.4 MT/Day |
PH |
6.5-8.5 |
----------- |
|
|
|
Suspended
solids |
50 |
|
|
|
Oil
and Grease |
10 |
|
||
|
BOD5
at 20 0C |
30 |
|
||
|
|
(b)0.1-0.4
MT/ Day (10MT/Yr) |
|
Disposal
via septic tank |
|
|
C. |
Bakery |
|
|
|
|
(a)
Bread and bread and biscuit |
PH BOD5
at 20 0C |
6.5-8.5
|
|
|
|
(i)Continuous
process (more than 20T/Day) |
|
200 |
25 |
|
|
(ii)
Non-continuous process (less than 20 MT/Day) |
|
Disposal
via septic tank |
|
|
|
|
(b)
Biscuit Production |
|
|
|
|
(i)10
T/Day and above |
PH |
6.5-8.5 |
|
|
|
|
BOD5
at 20 0C |
300
|
35 |
|
|
(ii) Below 10 T Day |
|
Disposal
via septic tank |
|
|
|
D. |
Confectioneries |
Effluents |
|
|
|
(a)
4 T/Day and above |
PH |
6.5-8.5 |
|
|
|
|
Suspended
solids |
50 |
|
|
|
Oil
and Grease |
10 |
|
||
|
BOD5
at 2 0C |
30 |
|
||
|
|
(b)
Below 4 T/Day |
|
Disposal via septic tank |
|
Note. -
To ascertain
the category of unit fails the average of daily production and wast water
discharge for the preceding 30 operating days from the date of sampling shall
be considered.
*The emission
from the boiler house shall conform to the standards already prescribed under
the Environment (Protection) Act, 1986, vide
Notification No. GSR 742 (E), dated 30-08-1990: See [1991] 70
Comp. Cas. (St.)5.
|
Sl. No. |
Industry |
Parameter |
Standards |
|
1 |
2 |
3 |
4 |
|
52. |
*Jute Processing Industry: |
Effluents |
Concentration in mf/1 except pH and water
consumption |
|
PH |
5.5-9.0 |
||
|
BOD5 at 200C |
30 |
||
|
Suspended solids |
100 |
||
|
Oil and Grease |
10 |
||
|
Water consumption |
1.60 Cum/Ton of product produced. |
Note. -
1. Water
consumption for the jute processing industry will be 1.5 Cum/Ton of product
from January, 1992.
2. At
present no limit for colour is given for liquid effluent. However, as far as possible, colour should
be removed.
*Stack emissions from boiler
house shall conform to the standards already prescribed under Environment
(Protection) Act, 1986, vide Notification No. GSR 742 (E), dated 30-8-90.
|
53. |
Large Pulp and Paper/news Print/rayon Grade Plants
of Capacity Above 24,000 mt/annum |
Effluents |
Concentration in mg/1 except PH and TOCL |
|
|
pH |
7.0-8.5 |
|
|
BOD5 at 20 0C |
30 |
||
|
COD |
350 |
||
|
Suspended solids |
50 |
||
|
*TOCL |
2.0 kg/Ton of product |
||
|
Flow (Total waste water discharge) |
|
||
|
**(i) Large pulp and paper |
200 Cum/Ton of paper produced |
||
|
(ii) Large rayon grade/News print |
150 Cum/Ton of paper produced |
Note. -
*The Standards for Total Organic Chloride (TOCL) will be applicable
from January, 1992.
** The standards with respect to total waste water discharge for the
large pulp and paper mills to be established from 1992, will meet the standards
of 100 Cum/Ton of paper produced.
|
54. |
Small Pulp and Paper,
Paper Plants of Capacity Upto 24,000 MT/Annum: Category: |
Effluent |
|
|
A. |
*Agro-based |
Total waste-water discharge |
200 Cum/Ton paper produced |
|
B. |
**Waste-paper based |
-Do- |
75 Cum/Ton of paper
produced |
Note. -
* The
agro-based mills to be established from January, 1992 will meet the standards
of 150 Cum/Ton of paper produced.
**The waste-paper mills to be established from January, 1992 will meet
the standards of 50 Cum/ Ton of paper produced.
|
55.
|
Common
Effluent Treatment Plants: A.
Primary Treatment |
Effluents
(inlet effluent quality for CETP) |
(Concentration
in mg/1) |
|
pH |
5.5-9.0 |
||
|
Temperature
0C |
45 |
||
|
Oil
and Grease |
20 |
||
|
Phenolic
compounds (as
C6 H5 OH) |
5.0 |
||
|
Ammonial
Nitrogen (As
N) |
50 |
||
|
Cyanide
(as CN) |
20 |
||
|
Chromium
(haxavalent) (as
Cr+6) |
2.0 |
||
|
Chromium
(Total) as (Cr) |
2.0 |
||
|
Copper
(as Cu) |
3.0 |
||
|
Lead
(as Pb) |
1.0 |
||
|
Nickel
(as Ni) |
3.0 |
||
|
Zinc
(as Zn) |
15 |
||
|
Arsenic
(as AS) |
0.2 |
||
|
Mercury
(as Hg) |
0.01 |
||
|
Cadmium
(as Cd) |
1.0 |
||
|
Selenium
(Se) |
0.05 |
||
|
Fluoride
(as F) |
15 |
||
|
Boron
(as B) |
2.0 |
||
|
Radioactive
Materials |
|
||
|
Alpha
emitters, Hc/mL |
10.7 |
||
|
Beta
emitters, Hc/mL |
10.8
|
||
|
Notes. - 1. These standards apply to the
small-scale industries, i.e., total discharge up to 25 KL/Day. 2. For each CETP and its constituent
units, the State Board will prescribe standards as per the local needs and
conditions; these can be more stringent than those prescribed above. However, in case of clusters of units, the
State Boards with the concurrence of CPCB in writing, may prescribe suitable
limits. |
|||
|
|
Into
inland Surface waters |
On
land For Irrigation |
Into
Marine Coastal areas |
|
|
(a) |
(b) |
(c) |
|
|
Treated
Effluent |
Quality
of common effluent Treatment plant |
Concentration
in mg/1 except pH and Temperature |
|||
|
pH |
5.5-9.0 |
5.5-9.0 |
5.5-9.0 |
|||
|
BOD5
at 20 0C |
30 |
100 |
100 |
|||
|
Oil
and Grease |
10 |
10 |
20 |
|||
|
Temperature
|
Shall
not Exceed
40 0C in any section |
|
45 0C
at the point of discharge |
|||
|
Of
the stream within 15 metres downstream from the effluent outlet. |
||||||
|
Into
inland Surface Waters |
On
land For Irrigation |
Into
Marine Coastal
areas |
||||
|
|
|
(a) |
(b) |
(c) |
||
|
|
Suspended
solids |
100 |
200 |
(a)For process waste waters- 100 (b) For cooling water effluents 10 per cent above total suspended matter of ineffluent cooling water |
|
|
Dissolved
solids (Inorganic) |
2100 |
2100 |
- |
|
Total
residual chlorine |
1.0 |
- |
1.0 |
|
|
Ammonical
Nitrogen (as N) |
50 |
- |
50 |
|
|
Total
Kjeldahi Nitrogen (as N) |
100 |
- |
100 |
|
|
Chemical
Oxygen demand |
250 |
- |
250 |
|
|
Arsenic
(as As) |
0.2 |
0.2 |
0.2 |
|
|
Mercury
(as Hg) |
0.01 |
- |
0.01 |
|
|
Lead
(as Pb) |
0.1 |
- |
1.0 |
|
|
Cadmium
(as Cd) |
1.0 |
- |
2.0 |
|
|
Total
Chromium (as Cr) |
2.0 |
- |
2.0 |
|
|
Copper
(as Cu) |
3.0 |
- |
3.0 |
|
|
Zinc
(as Zn) |
5.0 |
- |
15 |
|
|
Selinium
(as Se) |
0.05 |
- |
0.05 |
|
|
Nickel
( Ni) |
3.0 |
- |
5.0 |
|
|
Boron
(as B) |
2.0 |
2.0 |
- |
|
|
Percent
Sodium |
- |
60 |
- |
|
|
Cynide
(as CN) |
0.2 |
0.2 |
0.2 |
|
|
Chloride
(as Cl) |
1000 |
600 |
- |
|
|
Fluoride(as
F) |
2.0 |
- |
15 |
|
|
Sulphate
(as SO4) |
1000 |
1000 |
- |
|
|
Sulphide
(as S) |
2.8 |
- |
5.0 |
|
|
Pesticides |
Absent |
Absent |
Absent |
|
|
Phenolic
Compounds (as
C6H5OH) |
1.0 |
- |
5.0 |
Note. -
All
efforts should be made to remove colour and unpleasant odour as far as
possible.]
|
1[56 |
Dairy |
Effluents |
Concentration
in mg/1 except |
Quantum
per product processed |
|
pH |
|
|||
|
PH |
6.5-8.5 |
- |
||
|
*BOD5
at 20 0C |
100 |
- |
||
|
**Suspended
solids Oil
and Grease |
150 10 |
- - |
||
|
Waste
water generation |
- |
3m3/Kl of milk |
Note. - *BOD may be made stringent up to 30 mg/1 if the recipient fresh water body is a source for drinking waster
supply. BOD shall be up to 350 mg/1 for
the chilling plant effluent for applying on land provided the land is designed and operated as a
secondary treatment system with suitable monitoring facilities. The drainage water from the land after
secondary treatment has to satisfy a limit of 30 mg/1 of BOD and 10 mg/1 of nitrate expressed as "N". The net addition to the
groundwater quality should not be more than 3 mg/1 of BOD and 3 mg/1 of nitrate
expressed as "N". This limit for applying on land is allowed subject
to the availability of adequate land for discharge under the control of the
industry, BOD value is relaxable up to 350 mg/1, provided the waste water is
discharged into a town sewer leading to secondary treatment of sewage.
** Suspended
solids limit is relaxable upto 450 mg/1, provided wastewater is discharged into
a town sewer leading to secondary treatment of the sewage.
|
57. |
Tanneries |
Effluents |
Concentration
in mg/1, except pH |
Quantum
per raw hide processed |
|
pH |
6.5-90 |
|
||
|
*BOD5
at 20 0C |
100 |
|
||
|
Suspended
solids |
100 |
- |
||
|
Sulphides
(as S) |
1 |
- |
||
|
Total
chromium (as Cr) |
2 |
- |
||
|
Oil
and Grease |
0.1 |
- |
||
|
Waste
water generation |
- |
28m3/T |
Note. _
*For effluent discharge into inland surface waters
BOD limit shall be made stricter to 30
mg/1 by the concerned State Pollution Control Board.
|
*****58. |
Natural
rubber |
Centrifuging
and creaming units |
Crape
and curmb units |
|||
|
|
Processing industry |
For
disposal into Inland surface water |
For
disposal on land for irrigation |
For disposal into Inland surface water |
For
disposal on land for irrigation |
|
1. Added by GSR 475 (E), dated 6th
May, 1992.
|
|
|
|
(a) |
(b) |
(a) |
(b) |
|
(Concentration in mg/1, except pH and quantum of
waste water generation) |
(Concentration mg/1, except pH and quantum of
waste water generation) |
|||||
|
pH |
6-8 |
6-8 |
6-8 |
6-8 |
||
|
Total
kjeldhyl nitrogen (as N) |
200
(100*) |
*** |
50 |
*** |
||
|
Amonical |
100(50*) |
*** |
25 |
*** |
||
|
Nitrogen
(as N) |
50 |
100 |
30 |
100 |
||
|
BOD5
at 20 0C |
250 |
*** |
250 |
*** |
||
|
COD |
10 |
20 |
10 |
20 |
||
|
Oil
and Grease |
2 |
*** |
2 |
*** |
||
|
Sulphide |
2100 |
NP** |
2100 |
NP** |
||
|
TDS |
100 |
200 |
100 |
200 |
||
|
SS Quantum
of Waste water generation |
5
lit/kg. Of Product
processed |
8
lit/kg.of Product
processed |
40 lit/kg. of Product processed |
40 lit/kg.of Product Processed |
||
* To be
achieved in three years.
** Not
prescibed in case effluent is used for rubber plantation of their own, in other
cases suitable limit, as necessary may be prescribed by the State Board.
***Not
specified.
**** These
standards supersede the standards notified at serial No. 26. vide Notification
No. S.O. 8(E), dated 3rd January,
1989.
|
59. |
Bagasse- fired boilers |
Emissions |
(Concentration in mg/1 |
|
(a) Step grate |
Particulate matter |
250 |
|
|
(b) Horse shoe/pulsating grate |
Particulate matter |
250 (12% CO2) |
|
|
(c) Spreader stroker |
Particulate matter |
800 (12% CO2) |
Note. - In the case of horse shoe
and spreader stroker boilers, if more than one boiler is attached to a single
stack, the standard shall be fixed based on added capacity of all the boilers
connected with the stack.
|
60. |
Man-made fibre industry (semi-synthetic) |
Effluents |
(Concentrate in mg/1 except for pH) |
|
|
|
pH |
5.5-9.0 |
|
|
|
Suspended solids |
100 |
|
|
|
BOD5 at 20 0C |
30 |
|
|
|
Zinc (as Zn) |
1 |
|
61. |
Ceramic industry A. Kilns |
Emissions |
(Concentration in mg/Nm3) |
|
|
(a) tunnel, Top Hat, Chamber |
Particulate matter |
150 |
|
|
|
Fluoride |
10 |
|
|
|
Chloride |
100 |
|
|
|
Sulphur dioxide |
** |
|
|
(b) Down-draft |
Particulate matter |
1200 |
|
|
|
Fluoride |
10 |
|
|
|
Chloride |
100 |
|
|
|
Sulphur dioxide |
** |
|
|
(c) Shuttle |
Particulate matter |
150 |
|
|
|
Fluoride |
10 |
|
|
|
Chloride |
100 |
|
|
|
Sulphur dioxide |
** |
|
|
(d) Vertical shaft kiln |
Particulate matter |
250 |
|
|
|
Fluoride |
10 |
|
|
|
Sulphur dioxide |
** |
|
|
(e) Tank furnace |
Particulate matter |
150 |
|
|
|
Fluoride |
10 |
|
|
|
Sulphur dioxide |
** |
|
B. |
Raw material handlng, processing and operations |
|
|
|
|
(a) Dry raw materials handling and processing
operations |
Particulate matter |
150 |
|
|
(b) Basic raw materials and processing operations |
Particulate matter |
* |
|
|
(c) Other sources of air pollution generation |
Particulate matter |
* |
|
C. |
Automatic spray unit (a) Dryers (i) Fuel fired dryers |
Particulate matter |
150 |
|
|
(ii) For heat recovery dryers |
Particulate matter |
* |
|
|
(b) Mechanical finishing operation |
Particulate matter |
* |
|
|
(c) Lime/plaster of Paris manufacture |
|
|
|
Capacity |
Stack height |
|
|
|
Up to 5T/day |
-Do- |
A. Hood should be provided with a stack of 30
metre height from ground level (including kiln height) |
|
|
|
Above 5T/day |
-Do- |
H-14 (Q)0..3 |
|
|
|
|
Where Q is emission rate of So2 in/kg/hr and
H-Stack Height in meters |
|
|
More than 5T/day and up to 40T/day |
Particulate matter -Do- |
500 mg/NM3 150 mg/ NM3 |
Note. - Oxygen reference level for
particulate matter concentration calculations far kilns mentioned at A (c) is
18% and for those at A(b), and A(e) is 8%.
*All possible preventive measures should be taken to
control pollution is for as practicable.
** The standard for sulphur dioxide in terms of
stack height limits for kilns with various capacities of coal consumption shall
be as indicated below:-
|
Coal consumed per day |
Stack height |
|
|
Less than 8.5 mt. |
9m. |
|
|
More than 8.5 to 21 mt. |
12m. |
|
|
More than21 to 42 mt. |
15m. |
|
|
More than 42 to 64 mt. |
18 m. |
|
|
More than 64 to 104 mt. |
21 m. |
|
|
More than 104 to 105 mt. |
24 m. |
|
|
More than 105 to 126 mt. |
27 m. |
|
|
More than 126mt. |
30 m. or using formula H-14 (Qg)0.3 (whichever is more). |
|
Note.
- In this notification, H-Physical height of the stack, Qg- Emission of
sulphur dioxide in kg/hr., MT-Metric tonnes and m-metres.]
|
Sl.
No. |
Industry |
Parameter |
Standards |
|
(1) |
(2) |
(3) |
(4) |
|
1[62. |
Viscose-Filament Yarn (sub-sector of man-made
fibres semi-synthetic industry) |
Effluents |
(Concentration in mg/1 except for pH) |
|
|
|
PH |
5.5-9.0 |
|
|
|
Suspended solids |
100 |
|
|
|
BDD, at 20 0C |
30 |
|
|
|
Zinc (as Zn) |
5] |
|
2[63. |
Starch Industry (Maize products) |
Effluents |
Concentration not to exceed mg/1 (except pH and
waste water discharge) |
|
|
|
pH |
6.5-8.5 |
|
|
|
[BOD (3 days at 27 0C) |
100 |
|
|
|
Suspended solids |
150 |
|
|
|
Waste water discharge |
8 m3/tonne of maize processed |
Notes. -The prescribed limits for BOD and suspended solids shall be made more
stringent or less stringent depending upon the conditions and local requirements
as mentioned below:
(i) BOD shall be made
stringent upto 30 mg/1 if the recipient fresh water body is a
source for drinking water Supply.
(ii) BOD shall be allowed
upto 350 mg/1 for applying on land,
provided the land designed and operated as a secondary treatment system with
the requisite monitoring facilities. The drainage water from the land after
secondary treatment has to satisfy a limit of 30 mg/1 of BOD and 10 mg/1 of
nitrate expressed as N. The net addition to ground water quality should not
be more than 3 mg/1 of BOD and 10 mg/1 of nitrate expressed as N.
(iii) BOD shall be allowed
upto 350 mg/1 for discharge into a town sewer, if such sewer leads to a
secondary biological treatment system.
(iv) Suspended solids shall be allowed upto 450
mg/1 for discharge into a town sewer, if such sewer leads to a secondary
biological treatment system.
(v) In the event of bulking
of Sludge, the industry shall immediately apprise the respective State
Pollution Control Board.
1. Added by G.S.R. 80(E), dated 3 1 st
December, 1993 (w.e.f. 31.12.1993).
2. Entry 63 to 78
inserted by G.S.R. 176(E), dated 2nd April, 1996 (w.e.f. 3.4.1996).
|
64. |
Beehive hard coke oven |
|
|
|
|
|
(i). New Unit |
Emission: Particular matter (Corrected to 6% Co2) |
150mg/Nm3 |
|
|
Hydrocarbons |
25 ppm |
|||
|
|
(ii). Existing Units |
Particular matter (Corrected to 6% CO2) |
350 mg/Nm3 |
|
|
Notes:
For
control of emissions and proper dispensation of pollutants
the following guidelines shall be followed |
||||
|
(i) |
Units set up after the
publication of this notification shall be treated as new units. |
|||
|
(ii) |
Minimum stack height of 20 metres shall be provide by each unit. |
|||
|
(iii) |
Emissions from coke ovens shall be canalized through a
tunnel and finally emitted through a stack.
Damper adjustment techniques shall be used to have optimum
beautification and also to control the emission of unbrunt carbon particles
and combustible flue gases. |
|||
|
(iv) |
Wet scrubbing system or waste heat utilisation for power generation
or byproduct recovery systems should be installed preferably to achieve the
pre scribed standards |
|||
|
(v) |
After four years from the date of this
notification, all the existing units shall comply with the standards
prescribed for the new units. |
|
65 |
Briquette Industry (Coal) |
Emission: |
|
|
|
|
(a) |
Unit having capacity less than 10 tonnes. |
Particular matter (Corrected to 6% CO2) |
350 mg/Nm3 |
|
(b) |
Units having capacity
10 tonnes or more |
Particular matter (Corrected to 6% CO2) |
150 mg/Nm3 |
|
|
Notes. -For control of emissions/and proper dispersal of pollutants,
the following guidelines shall be followed by the industry: - |
|
|
(i) |
A minimum stack height of 20 meters shall be pro vided. |
|
(ii) |
All ovens shall be modified to single chimney multioven systems. |
|
|
Emissions from ovens shall
be channelised through inbuilt draft stack.
Optimum heat utilisation technique shall be used. |
|
|
In case of
units having capacity 10 tonnes and above, wet scrubbing system shall be
provided to control air pollution. |
|
66 |
Soft Coke Industry |
|
|
|
|
|
|
|
Particular matter (Corrected to 6% CO2) |
350 mg/Nm3 |
|
Note: - Wet scrubbing system along with by
product recovery system be provided. |
||
|
|
Guidelines
for Emission Control to Improve Work Zone Environment (applicable for
industries at serial number 64, 65 and 66). |
|
|
|
(a) |
Water used for quenching
and wet scrubbing shall be recirulated and reused through catch-pits |
|
|
(b) |
Leakages in
the oven shall be sealed by bentonite or by cable paste and by proper
maintenance to avoid fugitive emission. |
|
|
(c) |
Unloading of local trucks shall be
carried out with proper care avoiding dropping of the materials from height.
It is advisable to moist the material by sprinkling water while unload. |
|
|
(b) |
Pulversiation of coal
shall be carried out in an enclosed place and water-sprinkling arrangement
shall be provided at coal heaps, crushing area and no land around the
crushing unit. |
|
|
(c) |
Work area surrounding the plant shall be asphalted or concerned. |
|
|
(d) |
Green belt shall be developed
along the boundary of the industry. |
|
|
(e) |
Open burning of coal to
manufacture soft coke shall be stopped. |
|
67 |
Edible oil & Vanaspati Industry |
Effluents: |
|
|
|
|
|
Temperature |
Not more than 5 degree
Centigrade above ambient temperature of the recipient water body. |
|
|
|
|
pH |
6.5 - 6.8 |
|
|
|
|
Suspended
solids |
150
mg/l |
|
|
|
|
Oil
and Grease |
20
mg/l |
|
|
|
|
BOD
(3 days at 270C) |
100
mg/l |
|
|
|
|
COD |
200
mg/l |
|
|
|
|
Waste water discharge |
|
|
|
|
(i) |
Solvent extraction |
2.0 cum/tonne of
product (oil) |
|
|
|
(ii) |
Refinery/ Vanaspati |
2.0 cum/tonne of
product (refined oil/vanaspati). |
|
|
|
(iii) |
Integrated unit of
solvent extraction & refinery/vanaspati). |
4.0 cum/tonne of
refined oil /vanaspati oils. |
|
|
|
(iv) |
Barometric cooling
water/ De-odoriser water. |
15.0 cum/tonne of
refined oil/vanaspati. |
|
|
Note: - |
||||
|
(i) |
The above standards shall be applicable to
waste water from process and cooling.
|
|||
|
(ii) |
BOM
shall be made stringed upto 30 mg/l if the receipient fresh water body is
source of drinking water supply. |
|||
|
|
(ii) |
The
standards for boiler emissions shall be applicable as prescribed under
Schedule I of these rules. |
||
|
68. |
Effluents: |
|
|
|
|
|
(a) |
Compulsory
parameters |
PH BOD
(3 days at 270C) Oil
& Grease |
6.8-8.5 100
mg/l 10
mg/l |
|
|
|
|
Bioassay |
Minimum
90% survival after 96 hours with fish at 100% effulent). |
|
|
(b) |
Additional
parameters |
|
Mg/l |
|
|
|
|
Nitrate
(as N) |
10 |
|
Arsenic |
0.2 |
|||
|
Hexavalent
Chromium |
0.1 |
|||
|
Total
Chromium |
1.0 |
|||
|
Lead |
0.1 |
|||
|
Cyanide
as CN |
0.2 |
|||
|
Zinc
|
0.5 |
|||
|
Mercury |
0.001 |
|||
|
Copper |
2.0 |
|||
|
Nickel |
2.0 |
|||
|
Phenolics
as C6H5OH
|
5.0 |
|||
|
Sulphate |
2.0 |
|||
|
Notes: |
|
|
(i) |
No limit for COD is
prescribed but it shall be monitored. If the COD in a treated effluent is
persistently greater than 250 mg/l, such industrial units are required to
identify chemicals causing the same. In case these are found to be toxic as
defined in Hazardous Chemicals Rules, 1989 in part I, the State Board in such
cases may direct the industries to install tertiary treatment system
stipulating time limit. This may be done on case-to-case basis. |
|
|
|
|
(ii) |
These standards are not
applicable to small-scale detergent (formulating units). |
|
(iii) |
The standards for
boiler emissions shall be applicable as per the existing emission
regulations. |
|
(iv) |
Industry covered under this group are
halo-aliphatic, prasticizers, aromatics (calcohols, phenols, esters, acids
and salts, aldehydes and ketonne), substituted aromatics, aliphatic
(alcohols, esters, acids, aldehydes, ketones, amines and amides) and
detergents. |
|
69. |
Flour
Mills |
Effluents: |
|
|
|
|
|
|
pH |
6.8-8.5 |
|
BOD
(3days at 270C) |
100
mg/l |
|||
|
Total
Suspended solids |
100
mg/l |
|||
|
Oil
and Grease |
10
mg/l |
|||
|
Waste
water discharge. |
2
cubic meter per tonne of wheat processed. |
|||
|
Notes: |
||||
|
(i) |
BOD shall be made
stringent upto 30 mg/l if the recipient freshwater body is a source for
drinking water supply. |
|||
|
(ii) |
BOD shall be allowed upto 350 mg/l for applying on
land, provided the land is designed and operated as a secondary treatment
system with the requisite monitoring facilities. The drainage water from the land after secondary treatment has
to satisfy a limit of 30 mg/l of BOD and 10 mg/l of nitrate expressed as
N. The net addition to ground water
quality should not be more than 3 mg/l of BOD and 10mg/l of nitrate expressed
as N. |
|||
|
(iii) |
BOD shall be allowed upto 350 mg/l for discharge
into a town sewer, if such sewer leads to a secondary biological treatment
system. |
|||
|
(iv) |
Suspended solids shall be allowed upto 450 mg/l
for discharge into a town sewer, if such sewer leads to a secondary
biological treatment system. |
|||
|
70. |
Boilers
small |
Steam
generation Capacity
(ton/hors) |
Particular
emission matter (mg/ Nm3) |
|||
|
|
|
Less than 2 |
1200 * |
|||
|
2
to less than 10 |
800 * |
|||||
|
10
to less than 15 |
600 * |
|||||
|
15
and above |
150 ** |
|||||
|
Note: - |
|
|||||
|
|
* To meet the respective standards,
cyclone/ multicyclone is recommended as control equipment with the boiler. |
|||||
|
|
** to meet the standard, bag filter/ESP is
recommended as control equipment with the boiler. |
|||||
|
Notes. - |
|
|||||
|
(i) |
12% of CO, correction
shall be the reference value for particulate matter emission standards for
all categories of boilers. |
|||||
|
|
These limits
shall supercede the earlier limits notified under Schedule I at serial number
34 of Environment (Protection) Act, 1986 vide.
notification GSR 742 (E), dated 30th August, 1990. |
|||||
|
(iii) |
Stack Height for small
Boilers. For the
small boilers using coal or liquid fuels, the required stack height with the
boiler shall be calculated by using the formula H= 14Q03 Where H-Total stack height
in meters from the ground level. Q = SO2
emission rate
in kg/hr. In no case
the stack height shall be less than 11 meters. Where
providing all stacks are not feasible using above formula the limit of 400
mg/Nm3 for SO2, emission shall be met by
providing necessary control equipment with a minimum stack height of 11
meters. |
|||||
|
71. |
(i) |
Compulsory Parameters |
Mg/l except pH |
|||
|
|
|
pH |
6.5 8.5 |
|||
|
BOD (3days at 270C) |
100 |
|||||
|
Oil & Grease |
10 |
|||||
|
Suspended solids |
100 |
|||||
|
Bioassay test: |
Minimum 90%
survival of fish after 96 hours with 90% effluent and 10% dilution water.
Test shall be carried out as per IS: 6502-1971. |
|||||
|
|
(ii) |
|
Additional Parameters |
M/gl |
||
|
|
|
(a) |
Heavy metal |
|
||
|
|
|
|
Copper |
1.0 |
||
|
|
|
|
Manganese |
1.0 |
||
|
|
|
|
Zinc |
1.0 |
||
|
|
|
|
Tin |
0.01 |
||
|
|
|
|
Any other like |
0.1 |
||
|
|
|
|
Nickel |
Shall not exceed 5 times
the drinking water standards (BIS) Individually. |
||
|
|
|
(b) |
Organics Phenol & Phenolic Compounds as C6H5OH |
1.0 |
||
|
|
|
(c) |
Inorganics |
|
||
|
Arsenic as AS |
0.2 |
|||||
|
Cyanide as CN |
0.2 |
|||||
|
Nitrate as NO3 |
50 |
|||||
|
Phosphate as P |
5.0 |
|||||
|
|
|
(d) |
Specific pesticide |
Microgram/litre |
||
|
|
|
|
Benzene
hexachloride |
10 |
||
|
DDT |
10 |
|||||
|
Dimethoate |
450 |
|||||
|
Copper
oxychloride |
9600 |
|||||
|
Ziram |
1000 |
|||||
|
2,
4D |
400 |
|||||
|
Paraquat |
23000 |
|||||
|
Propanil |
7300 |
|||||
|
Nitrofen |
780 |
|||||
|
Other/below Mentioned pesticides individually) |
100 |
|||||
|
Other pesticides |
|
|
|
|||
|
(i) |
Insecticides |
|
|
|||
|
|
Aluminium Phosphide |
Lindane |
Pyrethrum extract |
|||
|
|
Dichlorovos |
Malathion |
Quinalphos |
|||
|
|
ETDC Mixer |
Methyl Bromide |
Monocrotophos |
|||
|
|
Ethylene Dibromide |
Nicotine sulphate |
Carbaryl |
|||
|
|
Ethion |
Oxydemeton Methyl |
Endosulfan |
|||
|
|
Fenitrothion |
Methyl parathion |
Fenvalerate |
|||
|
|
Lime-sulphur |
Phosphamidon |
Phorate |
|||
|
|
Temephos |
|
|
|||
|
(ii) |
Fungicides |
|
|
|||
|
|
Aureofungin |
Organomercurias |
|
|||
|
|
|
(MEMC & PMA) |
|
|||
|
|
Barjum Polysulphide |
Suphur (Colloidal, Wettable & Dust) |
|
|||
|
|
Cuprous oxide Ferbam Mancozeb Manab Nickel Chloride |
Stretocycline Thiram Zineb Carbendazim Tridemorph |
|
|||
|
(iii) |
Rodenticides: Comafuryl Warfrain Zinc Phosphide |
|
|
|||
|
(iv) |
Nematicides: Metham N-Sodium |
|
|
|||
|
(v) |
Weedicides: Fluchloralin Isoproturon Butachlor Anilphos |
|
|
|||
|
(vi) |
Plant Growth Regulants: Chloromequat Chloride Nemphalene Acetic Acid. |
|
|
|||
|
(vii) |
Any other pesticide not specified above |
|
||||
|
|
||||||
|
Notes: - |
|
|||||
|
(1) |
Limits shall be complied with at the end of the
treatment plant before any dilution. |
|||||
|
(2) |
From the Additional
Parameters specified in 71(ii), only the relevant parameters (based on the
raw-materials used and products manufactured) may be prescribed by the
concerned State Board on a case-to-case basis. |
|||||
|
(3) |
No limit for COD is
prescribed. If the COD in a treated
effluent is presistently more than 250 mg/l such industrial units are
required to identify the chemicals causing the same. In case, these are found to be toxic as
defined in Schedule I of the Hazardous Chemicals Rules, 1989, the State
Boards in such cases may direct the industries to install tertiary treatment,
stipulating time limit. This may be
done on a case-to-case basis. |
|||||
|
(4) |
Solar evaporation followed
by incineration is a recognised practice; provide the guidelines of solar
evaporation as given below are followed. |
|||||
|
|
Guidelines on solar
evaporation system or wastewater from pesticide industry. |
|||||
|
(i) |
Solar evaporation pans
shall be constructed in such a way that the bottom is atleast one meter above
the ground level. |
|||||
|
|
(ii) |
Solar evaporation pans
shall be leak proof and of impervious construction and designed as per IS:
7290. |
||||
|
|
(iii) |
The solar evaporation pans
shall be designed on the basis of evaporation rate matching to the out put of
wastewater |
||||
|
|
(iv) |
Wastewater must be
pre-treated as below before subjecting to solar evaporation: |
||||
|
|
|
(a) |
Oil and grease and
floating organics shall be removed so that the rate of evaporation is not
affected. |
|||
|
|
|
(b) |
Acidic/Alkaline waste must
be neutralized before solar evaporation to maintain pH in the range of 6.5 to
8.5. |
|||
|
|
|
(c) |
Toxic volatile matter
shall be removed so as not to cause air pollution. |
|||
|
|
(v) |
During the rainy season,
storm water shall not be allowed to mix with process waste and enter the
pans. The wastewater shall in no case
outflow from the evaporation pans.
Alternative arrangements shall be made to hold the wastewater in
proper impervious tanks and if necessary, force evaporated. |
|
|
|
(vi) |
In no circumstances, the
liquid effluent shall be discharged without conforming to the minimal
national standards or stored in a holding arrangement, which is likely to
cause pollution. |
|
|
|
(vii) |
The sludge from the solar
evaporation pans shall be incinerated or disposed as per the guidelines for
management and handling of hazardous waste, published by the Ministry of
Environment and Forests, Government of India, after obtaining authorization
from the State Pollution Control Board under the Hazardous Wastes (Handling
and Management Rules, 1989. |
|
|
|
(viii) |
The facility
shall be protected from flood and storm to prevent embankments from
commission or any other damage, which may render any portion inoperable. |
|
|
|
(ix) |
Facilities
shall have protective enclosure to keep wildlife, domestic animals, unauthorized
persons, etc., away. |
|
|
72. |
|
Oil Drilling
and Gas Extraction Industry |
|
|
|
A. |
Stands for
Liquid Effluent 1.0 On-Shore facilities (For Marine Disposal) |
|
|
|
|
pH |
5.5 9.0 |
|
|
|
Oil and Grease |
10 mg/l |
|
|
|
Suspended
solids |
100 mg/l |
|
|
|
BOD (3 days
at 270C) |
|
|
Note: - |
|
|||
|
(i) |
For on-shore discharge of
effluents, in addition to the standards prescribed above, proper marine
outfall has to be provided to achieve the individual pollutant concern level
in sea water below their toxicity limits as given below, within a distance of
50 metre from the discharge point in order to product the marine aquatic
life. |
|||
|
|
Parameter |
Toxicity
limit, mg/l |
||
|
|
Chromium as Cr |
0.1 |
|
|
|
|
Copper, as Cu |
0.05 |
|
|
|
|
Cyanide, as CN |
0.005 |
|
|
|
|
Fluoride, as F |
1.5 |
|
|
|
|
Lead, as Pb |
0.05 |
|
|
|
|
Mercury, as Hg |
0.01 |
|
|
|
|
Nickel, as Ni |
0.1 |
|
|
|
|
Zinc, as Zn |
0.1 |
|
|
|
(ii) |
Oil and gas drilling and processing facilities,
situated on land and away from saline water sink may opt either for disposal
of treated water by on-shore disposal or by re-injection in abandoned well,
which is allowed only below a depth of 1000 metres from the ground
level. In case of re-injection in
abandoned well the effluent have to coin ply only with respect to suspended
solids and oil and grease at 100 mg/l and 10 mg/l, respectively. For on-shore disposal, the permissible
limits are given below: |
|
S. No. |
Parameters |
On-shore discharge standards (Not to exceed) |
|
1 |
2 |
3 |
|
1 |
PH |
5.5 9.0 |
|
2 |
Temperature |
400C |
|
3 |
Suspended Solids |
100 mg/l |
|
4 |
Zinc |
2 mg/l |
|
5 |
BOD |
30 mg/l |
|
6 |
COD |
100 mg/l |
|
7 |
Chlorides |
600 mg/l |
|
8 |
Sulphates |
1000 mg/l |
|
9 |
TDS |
2100 mg/l |
|
10 |
% Sodium |
60 mg |
|
11 |
Oil and grease |
10 mg/l |
|
12 |
Phenolics |
1.2 mg/l |
|
13 |
Cyanides |
0.2 mg/l |
|
14 |
Fluorides |
1.5 mg/l |
|
15 |
Sulphides |
2.0 mg/l |
|
16 |
Chromium (Cr+6) |
0.1 mg/l |
|
17 |
Chromium (Total) |
1.0 mg/l |
|
18 |
Copper 0.2 mg/l |
|
|
19 |
Lead 0.1 mg/l |
|
|
20 |
Mercury |
0.01 mg/l |
|
21 |
Nickel 3.0 mg/l |
|
|
2.0 |
Off-shore facilities: |
|
|
For offshore discharge of
effluents, the oil content of the treated effluent without dilution shall not
exceed 40 mg/l for % of the observation and shall never exceed 100 mg/l. Three 8-hourly grab samples are required
to be collected daily and the average value of oil and grease content of the
three samples shall comply with these standards. |
|
B. |
Guidelines for Discharge
of Gaseous Emission |
|
1.0 |
D.G Sets. |
|
1.1 |
DG sets at drill site as
well as production station shall conform with the norm notified under the
Environment (Protection) Act, 1986. |
|
2.0 |
Elevated/ground flares |
|
2.1 |
Cold Venting of gases
shall never be resorted to and all the gaseous emission are to be flared. |
|
2.2 |
All flaring shall be done
by elevated flares except where there is any effect on crop production in
adjoining areas due to the flaring. In such cases, one may adopt ground. |
|
2.3 |
In case of ground flare,
to minimize the effects of flaring, the flare pit at Group Gathering Station
(GGS) Oil Collecting Station (OCS) and Group Collection Station (GCS) shall
be made of RCC surrounded by a permanent wall (made of refractory brick) of
minimum 5m height to reduce the radiation and glaring effects in the
adjoining areas. |
|
2.4 |
A green belt
of 100m width may be developed around the flare after the refractory wall in
case of ground flaring. |
|
2.5 |
If the ground
flaring with provision of green belt is not feasible, enclosed ground flare
system shall be adopted, and be designed with proper enclosure height, to
meet the round level concentration (GLC) requirement. |
|
2.6 |
In case of
elevated flaring, the minimum stack freight shall be 30m. Height of the stack shall be such that the
maximum GLC never exceeds the prescribed ambient air quality limit. |
|
3.0 |
Burning of
effluent in the pits shall not be carried out at any stage. |
|
C |
Guidelines for Disposal of Solid Waste |
|
1.0 |
Disposal of drill cuttings |
|
1.1 |
The drill cuttings shall
be conveyed through a conveyor system to the disposal pit after proper
washing. |
|
1.2 |
No drill cuttings (of any
composition) shall be disposed offshore.
For offshore installation, drill cuttings separated from mud shall be
transported on on-shore through supply vessels for secured landfill disposal
as per Ministry of Environment and Forests guidelines. The site shall be approved by the
concerned authority, (State Government /State Pollution Control Board). |
|
1.3 |
The disposal of drill
cuttings (on-shore/off-shore) shall confirm to the guidelines provided by the
Ministry of Environment and Forests. |
|
1.4 |
The secured land-fill pit
shall be covered with a thick layer of local top soil provided with proper
top slope, after drilling, operation is over. |
|
2.0 |
Disposal of drilling load |
|
2.1 |
The unusable portion of
the drilling mud (of any composition); after reclamation shall be disposed of
only at a secured landfill site approved by the concerned authority (State
Government /State Pollution Control Boards).
The disposal of mud shall conform to the guidelines provided by the
Ministry of Environment and Forests under the Hazardous Wastes (Management
and Handling) Rules, 1989. |
|
2.2 |
No mud (of any
composition) shall be disposed off-shore.
For off-shore installation, the unusable portion of the mud shall be
brought back to the shore for disposal in a secured landfill. |
|
2.3 |
Only water-based Mud
system shall be used. Where oil-based
muds are used, the muds, after they become unusable, shall be properly
treated/incinerated, in a centralized treatment facility. In case of off-shore installation, these
may be brought to the shore and treated. |
|
3.0 |
Production stage solid
waste disposal. |
|
3.1 |
The dried sludge from
wastewater treatment plant and other solid wastes at production stage shall
be disposed in a secured land-fill. |
|
3.2 |
In case oil content in the
sludge is high, it shall be properly treated/incinerated and ash shall be
disposed of in a secured land-fill |
73. Pharmaceuticals industry
(Bulk Drugs)
(i) Compulsory (mg/l
except pH)
Parameters
pH 6-5-8.5
Oil & Grease 10
BOD (3 days at 270C) 100
Total suspended solids 100
Bioassay test 90% survival after 96
Hours
in 100% effluent test
shall be carried out as
per IS:6582-1971
(ii) Additional parameters mg/l
Mercury 0.01
Arsenic 0-2
Chromium 0.1
(Hexavalent)
Lead 0.1
Cyanide 0.1
Phenolics (C6H5OH) 1.0
Sulphides (as S) 2-0
Phosphate (as P) 5.0
Notes-
(i) The limit of BOD (3 days at 27C) shall be 30 mg/i if effluent
is discharged directly to a fresh water body-
(ii) The additional parameters are applicable
to bulk drug-manufacturing units depending upon the process and product-
(iii) No limit for COD is prescribed, but it
shall be monitored. If the COD of the
treated effluent is greater than 250 mg/l, such industrial units are required
to identify chemicals causing the same.
In case these are found to be toxic, as defined in the Hazardous
Chemicals Rules, 1989 (Schedule 1), the State Boards in such cases shall direct
the industries to install tertiary treatment system within the stipulated time
limit. This may be done on a
case-to-case basis.
|
74. Emission
Standards for brick kilns: |
||
|
I. Minimal
National Emission Standards for Brick Kilns |
||
|
Size |
Kiln Capacity |
Maximum limit for the Concentration of particulate
matter (mg/N cum) |
|
1 |
2 |
3 |
|
Small |
Less than 15,000 bricks
per day (less than 15 ft trench width) |
1000 |
|
Medium |
15,000-30,000 bricks per day (15-22 ft trench width) |
750 |
|
Large |
More than 30,000 bricks per day (more than 22 ft trench width) |
750 |
Note- The above
particulate matter emission limits arc achievable by installing fixed chimney
high draught kilns and/or settling chamber.
II- Stack Height Regulation:
The following stack heights are recommended for
optional dispersion of particular matter
|
Kiln Capacity |
Stack
Height |
|
1 |
2 |
|
Less than 15,000 bricks per day (Less than 1 5 ft
trench width) |
Minimum stack height of 22m or, |
|
Induced draught fan
operating with minimum draught of 50mm Water Gauge with 12 m stack height. |
|
|
15,000-30,000 bricks per
day (15-22 ft trench width) |
Minimum stack height of
27m with gravitational settling chamber or |
|
Induced draught fan
operating with minimum draught of 50mm Water Guage with 15 m stack height. |
|
|
More than
30,000 bricks per day More than 22 ft. trench
width) |
Minimum stack
height of 30m with gravitational settling chamber or, |
|
Induced draught fan
operating with minimum draught of 50mm Water Guage with 17m stack height. |
|
|
III. Existing moving chimney Bulls trench
kilns shall be dispensed with by December 31, 1997 and no new moving chimney kilns shall be allowed to come up. |
|
|
IV. Considering the immediate need to protect
the top soil and to find ways for safe disposal/ utilisation of flyash,
it is provided that from the 1st January, 1997, all brick
manufacturing units within a radious of 50 kms from any thermal power plant,
shall utilise flyash in optimal proportion for making bricks. |
|
75. Soda Ash Industry (Solvay
Process)
|
PARAMETER |
MINAS (Recipient body
specified) |
||||
|
|
Marine |
Brackish |
Inland
surface water |
||
|
PH |
6.5
- 9 |
6.5
9 |
6.5
9 |
||
|
Temperature |
450C or less |
450C or less |
450C or less |
||
|
Oil
or Grease |
2
mg/l |
20
mg/l |
10
mg/l |
||
|
Suspended
solids (SS) |
500
mg/l |
200
mg/l |
100
mg/l |
||
|
Ammoniacal
nitrogen |
5
mg/l |
50
mg/l |
1[50mg/l |
||
|
|
|||||
|
Bio-assay |
96
Hours 1[90]%
survival |
96
Hours 90
% survival |
96
Hours 90%
survival |
||
|
Note: -
MINAS for disposal in brackish and inland surface water are without any dilution.
Standards for Dual Process Soda Ash Plants: |
|||||
|
|
Parameters |
MINAS |
|||
|
|
|
(Inland
surface water) |
|||
|
|
pH |
6.5 8.0 |
|||
|
|
Ammoniacal
nitrogen as N (mg/l) |
50 |
|||
|
|
Nitrate
nitrogen, as N (mg/l) |
10 |
|||
|
|
Cyanide |
0.2 |
|||
|
|
Hexavalent
chromium (mg/l) |
0.1 |
|||
|
|
Total
chromium (mg/l) |
2.0 |
|||
|
|
Suspended
solids, (mg/l) |
100 |
|||
|
|
Oil and
Grease (mg/l) |
10 |
|||
Note. The standards are to be
implemented by the industry in a time targeted schedule within two years. The progress on the time targeted
implementation schedule shall be periodically submitted by the industry to the
State Pollution Control Board and Central Pollution Control Board.
1. Vide
Corrigendum G.S.R. 57 (E), dated 14th
February 1997.
76. Emission Standard
For SO2 from Cupola
furnace:
Standard for Sulphur Dioxide omission from Cupola
Furnace
|
|
Characteristics |
Emission limit |
|
|
Sulphur dioxide (SO2) emission |
300 mg/Nm3 at 12% CO2 correction |
To achieve the standard, foundries may install
scrubber, followed by a stack of height six times the diameter of the Cupola
beyond the charging door.
Note: - In case due to some
technical reasons, installation of scrubber is not possible, then value of SO,
to the ambient air has to be effected through the stack height.
77. Specification
of Motor Gasoline for Emission Related Parameters
|
Sl. No. |
Characteristics |
Required
|
Method
of Test ref, to P; of IS: 1448 |
|
|
(i) |
Reid Vapour Pressure at 380C, KPa |
35 to 70 |
P: 39 |
|
|
(ii) |
Benzene, Percent by volume |
5.0 (1) |
P: 104 |
|
|
(iii) |
Lead content as (pb) g/l, Max |
0.15 (low leaded) (2) |
P: 38 |
|
|
|
|
0.013 (unleaded) |
|
|
|
(iv) |
Sulphur, percent by mass, Max |
0.10
(unleaded) |
P: 34 |
|
|
(v) |
Potential Gum, g/m3, max |
50 |
ASTM 873: 8 |
|
|
(vi) |
Gum (Solvent Washed) g/m3 Max |
40 |
P: 29 |
|
|
(vii) |
Oxygenates
Content Ether (MTBE, ETBE) Alcohol, percent by volume, Max |
15 |
|
|
|
(viii) |
Phosphorous |
See Foot Note (3) |
ASTMD 3231 |
|
|
|
(1) |
3.0 percent by volume maximum in metro cities by
2000 AD. |
||
|
|
(2) |
0.15 by 3 lst December 1996 (for entries country). 0.013 g/l by lst April,
1995 (in four-metro-cities) By 1st December, 1998 (for
all State capitals/UTS, and major metro cities) and by Ist (April, 2000 for
the entire country. |
||
|
|
(3)
|
Phosphorous containing
additives shall be absent |
||
|
|
|
|
||
Note. -
(a) Above specifications applies to leaded is
well as unleaded petrol except lead content.
(b) For new refineries coining
tip during or after 1997 the specification applicable by 2000 for existing
refineries shall be applicable by 1997.
78. Specification of Diesel Fuel for Emission Related Parameters
|
Sl. No. |
Characteristics |
Requirement |
Method of Test To P: of IS: 1448 |
|
(i) |
Density
at 150C, Kg/m3 |
820 to 880(l) |
P: 32 |
|
(ii) |
Cetane
Number, Min |
45 .0(2) |
P: 9 |
|
(iii) |
Distillation
85 per cent by volume recovery at recovery at 0C Max |
350 |
P: 18 |
|
95
percent by volume recovery at 0C, Max |
370 |
|
|
|
(iv) |
Sulphur,
percent by mass |
0.50(3) |
P: 33 |
(1) 820 to 860 by 2000 AD
(2) 49 by 31st December 1998
(except in the refineries-Digboi, Gauhati, and
Bongaigaon Refineries & Petrochemicals Ltd.).
(3) (i) 0.50
per cent by mass by 1st April, 1996 in four metros and Taj Trapezium.
(ii) 0.25 per cent by mass by 1st October 1996
in Taj Trapezium.
(iii) 0.25 per cent by mass by 1st April 1999 throughout the country.
Note. -
(a) Above specifications apply to HSD only.
(b) For new refineries coining during or
after 1997 specification applicable by 2000 for existing refineries shall be
applicable by 1997.
(c) P refers to parts of IS: 1448.]
|
1[Sl No. |
Industry |
Parameter |
Standards |
|||||
|
|
New Batteries |
Existing Batteries |
||||||
|
1. |
Coke
oven plants |
Fugitive
visible, Emission |
|
|
||||
|
|
(By product recovery type |
a. |
Leakage
from door |
5(PLD)* |
10(PLD)* |
|||
|
|
|
b. |
Leakage
from charging lids |
1(PLL)* |
1(POLL)* |
|||
|
|
|
c. |
Leakage
from AAP Covers |
4(PLO) |
4(PLO) |
|||
|
|
|
d. |
Charging
emission (second/charge) |
16(with
HPLA)* |
50
[with HPLA)* |
|||
|
|
Stack
Emission of Coke Oven |
|||||||
|
(a) |
SO2 (mg. Nm3) |
800 |
800 |
|||||
|
(b) |
NOx, (mg/Nm3) |
500 |
500 |
|||||
|
(c) |
SPM,
emission during charging stack (emission) mg/Nm3 |
50 |
50 |
|||||
|
|
(a) |
SPM emission during charging (stack emission)
mg/Nm3 |
|
|||||
|
|
(b) |
SPM emission during charging (stack emission)
gm/ton of coke |
5 |
5 |
||||
|
|
Sulphur in Coke Oven Gas Used (for heating (mg/Nm3) |
800 |
800 |
|||||
|
|
Emission for quenching operation Particulate matter gm/MT of coke produced |
50 |
50 |
|||||
|
|
Benzo-pyerine (BOP) concentration in work zone air
(ug/m3) |
|
|
|||||
|
|
-Battery area (top of the battery) |
5 |
5 |
|||||
|
|
-Other units in coke oven plant |
2 |
2 |
|||||
|
|
-Ambient standards (ng/m3) |
10 |
10 |
|||||
1. Ins by G.S.R. 631 (E), dated of 31 st October 1997 (w.e.f. 31-10-1997).
For- Control of emissions and to maintain
environmental quality in work zone area, the following guidelines shall be
followed, namely:-
(i) New coke oven units shall follow any of the low-emission procedures, such is, coke dry cooling, non-recovery coke-ovens. Indirect Quenching Process, Jumbo coke oven
reactor, Modified Wet Quenching System with appropriate environmental controls
(e. g, baffles, filtering media, collection and treatment of residential water
from quench tower and recycling;
Use of process water as quenching water shall not be permissible).
(ii) Effective pollution control measures (for
e.g. Extensive maintenance and cleaning of oven doors and frame seals,
ascension pipes, charging holes and lids and other equipment; On main charging
system (HPLA): Luting charging holes with clay-suspension; Modified
guide/transfer car with emission control system etc.) shall be taken to reduce
coal charging and coke pushing emission.
The bleeder of the coke oven shall he flared.
(iii) In the case of existing coke ovens with
wet quenching, the new procedure as in (i) and (ii) shall be adopted and
emission standards achieved within four years (by 2001)
Note. -Units set up after
the publication of this notification shall be treated is new units.
*HPLA- Aspiration through hi- pressure liquor injection in
goose neck.
*PLD -
Percent leaking doors.
*PLL -
Percent leaking lids.
*PLO -
Percent leaking off takes.]
1[81. Battery manufacturing industry-
1. Ins. by G.S.R. 7, dated 22nd December
1998, published in the Gazette of India, dated 2-1-1999, Pt. II, sec. 3 (1), P.
40.
(i) Lead Acid Battery Manufacturing Industries. Emission Standards.
|
Source |
Pollutant |
Standards Conc. Based (mg/Nm3) |
|
|
|
Grid casting |
Lead |
10 |
|
|
|
Particulate Matter |
25 |
|
|
Oxide Manufacturing |
Lead |
10 |
|
|
|
Particulate matter |
25 |
|
|
Paste mixing |
Lead |
10 |
|
|
|
Particulate matter |
25 |
|
|
Assembling |
Lead |
10 |
|
|
|
Particulate matter |
25 |
|
|
PVC section |
Particulate matter |
150 |
To comply with the
respective standards, all the emissions from the abovementioned sources shall
be routed through stack connected with hood and fan. In addition to above, installation of control equipment viz., bag
filter/ventury scrubber, is also recommended.
- The minimum stack height shall be 30
m.
Liquid
effluent discharge standards:
Pollutant
Concentration based standards
pH 6.5-8.5
Suspended solids 50
mg/l
Lead 0.1
mg/l
(ii) Dry, cell-manufacturing industry: emission
standards
Pollutant Standards Concentration based (mg/Nm3)
Particulate matter 50
Manganese
as Mn 5
- To comply with the
respective standards, all the emissions from the abovementioned sources shall
be routed through stack connected with hood and fan. In addition to above, installation of control equipment viz., bag
filter/ventury scrubber, is also recommended.
- The minimum stack height shall be 30
m.
Effluent
standards
Pollutant Concentration based
standards
pH 6.5-8.5
Total suspended solids 100mg/l
Manganese as Mn 2 mg/l
Mercury as Hg 0.02 mg/l
Zinc as Zn 5 mg/l
(iii) Secondary lead smelters:
Pollutant Concentration-based
standards
Lead
as Pb 10 mg/NMp3
Particulate
matter 50 mg/Nm3
Minimum
stack height 30m
82. Environmental standards
for gas/naphtha-based Thermal Power Plants
(i) Limit
for emission of NOx
(a) For existing units-150 ppm (v/v) at 15
percent. Excess oxygen.
(b) For new units with effect from 1-6-1999.
|
Total generation of gas turbine |
Limit
for Stack NOx emission [(v/v), at 15 Percent excess oxygen] |
|
(a) 400-MW and above |
(i) 50 ppm for the units burning natural
gas. (ii) 100 ppm for the units burning naphtha |
|
(b) Less
than 400 MW but up to100 MW |
(i) 75 ppm for the units
burning natural gas (ii) 100 ppm for the units
burning naphtha |
|
(c) Less than 100 MW |
100
ppm for units burning natural gas or Naphtha as fuel |
|
(d) For
the plants burning gas in a conventional boiler. |
100 ppm |
(ii) Stack height H in m
should be calculated using the formula H=14 Q0.5,
where
Q
is the emission rate of SO 2 in
ka/hr, subject
to a minimum of 30 mts.
(iii) Liquid waste discharge limit
|
Parameter |
Maximum limit of
concentration (mg/l except for pH and temperature) |
|
pH |
6.5-8.5 |
|
Temperature |
As
applicable for other theremal power plants. |
|
Free available chlorine |
0.5 |
|
Suspended solids |
100.0 |
|
Oil and grease |
20.0 |
|
Copper (total) |
1.0 |
|
Iron (total) |
1.0 |
|
Zinc |
1.0 |
|
Chromium (total) |
0.2 |
|
Phosphate |
5.0 |
83. Standards/guidelines for control of noise
pollution from stationary diesel generator (DG) Sets
(A) Noise standards for DG sets
(15-500 KVA)
The total sound power level,
Lw, of a DG set should be less than, 94+10 log10, (KVA), dB (A), at the
manufacturing stage, where, KVA is the nominal power rating of a DG set.
This level should fall by 5
dB (A) every five years, till 2007, i.e.,
in 2002 and then in 2007.
(B) Mandatory acoustic enclosure/accoustic
treatment of room for stationary DG sets (5 KVA and above).
Noise from the DG set should
be controlled by providing an accoustic enclosure or by treating the room
acoustically.
The acoustic
enclosure/acoustic treatment of the room should be designed for minimum 25 dB
(A) Insertion Loss or for meeting the ambient noise standards, whichever is on
the hi-her side (if the actual ambient noise is on the higher side, it may not
be possible to check the performance of the acoustic enclosure/acoustic
treatment. Under such circumstances the
performance may be checked for noise reduction upto actual ambient noise level,
preferably, in the night-time). The
measurement for insertion loss may be done at different points at 0.5m from the
acoustic enclosure/room, and then averaged.
The DG set should also be
provided with proper exhaust muffler with insertion loss of minimum 25 dB (A).
(C) Guidelines for the manufacturers/users of
DG sets (5 KVA and above).
01 The manufacturer should offer to the user
a standard acoustic enclosure of 25 dB (A) insertion loss and also a suitable
exhaust muffler with insertion loss of 25 dB (A).
02 The user should make efforts to bring down
the noise levels due to the DG set, outside his premises, within the ambient
noise requirements by proper sitting and control measures.
03 The manufacturer should furnish noise
power levels of the unsilenced DG sets as per standards prescribed under (A).
04 The total sound power level of a DG set,
at the users end, shall be within 2 dB(A) of the total sound power level of the
DG set, at the manufacturing stage, as prescribed under (A).
05 installation of a DG set must be strictly
in compliance with the recommendations of the DG set manufacturer.
06 A proper routine and preventive
maintenance procedure for the DG set should be set and followed in consultation
with the DG set manufacturer which would help prevent noise levels of tile DG
set from deteriorating with use.
84. Temperature limit for discharge of
condenser cooling water from Thermal Power Plant.
A: New thermal power plants commissioned
after June 1, 1999:
New thermal power plants,
which will be using water from rivers/ lakes/reservoirs, shall install cooling
towers irrespective of location and capacity.
Thermal power plants which will use sea water for cooling purposes, the
condition below will apply.
B: New projects in coastal areas using sea
water:
The thermal power plants
using sea water should adopt suitable system to reduce water temperature at the
final discharge point so that the resultant rise in the temperature of
receiving water does not exceed 70C over and above the ambient
temperature of the receiving water bodies.
C: Existing thermal power plants:
Rise in temperature of
condenser cooling water from inlet to the outlet of condenser shall not be more
than 100C.
D: Guidelines for discharge point:
(1) The discharge point shall preferably be
located at the bottom of the water body at mid-stream for proper dispersion of
thermal discharge.
(2) In case of discharge of cooling water
into sea, proper marine outfall shall be designed to achieve the prescribed
standards. The point of discharge may
be selected in consultation with the concerned State authorities/NIO.
(3) No cooling water discharge shall be
permitted in estuaries or near ecologically sensitive areas such as mangroves,
coral reefs/spawning and breeding grounds of aquatic flora and fauna.
85. Environmental standards for coal washeries.
-
1. Fugitive emission standards
- The
difference in the value of suspended particulate matter, delta (A), measured
between 25 and 30 metres from the enclosure of coal crushing, plant in the
downward and leeward wind direction shall not exceed 150 microgram per cubic
metre. Method of measurement shall be
High Volume sampling and Average flow rate, not less than
1.1. m3 per minute, using upwind downwind method of
measurement.
2. Effluent discharge standards:
- The coal washeries shall maintain the close circuit operation
with zero effluent discharge.
-If in case due to some
genuine problems like periodical cleaning of the system, heavy rainfall, etc., it becomes necessary to discharge
the effluent to sewer/land/stream then the effluent shall conform to the
following standards at the final outlet of the coal washery.
|
SI. No. |
Parameter |
Limits |
|
1 2. 3. 4. 5. 6. |
pH Total
suspended solids Oil
and Grease B.O.D.
(3 days 27 deg C) COD Phenolics |
5.5-9.0 100
mg/l 10
mg/i 30
mg/l 250
mg/l 1.0
mg/l |
3. Noise level standards:
Operational/working Zone
- not to exceed 85 dB (A) Leq for 8 hours exposure.
The ambient air quality standards in respect of noise as
notified under the Environmental (Protection) Rules, 1986, shall be followed at
the boundary line of the coal washery.
4. Code of practice for coal washery.
Water or water mixed
chemical shall be sprayed at all
strategic coal water points such as conveyors, loading/unloading points, etc.
As far as practically possible conveyors, transfer points, etc., shall be provided with enclosures.
The crushers/pulverisers of
the coal washeries shall be provided with enclosures, fitted with suitable air
pollution control measures and finally emitted through a stack of minimum height
of 30m, conforming particulate matter emission standard of 150 mgt Nm3 or provided with adequate
water shrinking arrangement.
Water sprinkling by using
fine atomizer nozzles arrangement shall be provided on the coal heaps and on
around the crushers/pulverisers.
Area, in and around the coal
washery shall be pucca either asphalted
or concreted. Water consumption in the coal washery shall not exceed 1.5 cubic
meters per tonne of coal.
The efficiency of the
settling ponds of the waste water
treatment system of the coal washery shall not be less than 90 percent.
Green belt shall be developed along the road, side, coal handling plants, residential complex, office building and all around the boundary
line of the coal washery.
Storage bunkers, hoppers,
rubber decks in chutes and centrifugal chutes shall be provided with proper
rubber linings.
Vehicle movement in the coal
washery area shall be regulated effectively to avoid traffic congestion. High-pressure horn shall be prohibited. Smokes emission from heavy-duty vehicle
operation- in the coal washeries should confirm the standards prescribed under
the Motor Vehicle Rules, 1989.
86. Water quality standards for coastal waters marine outfalls.
In a coastal segment marine
water is subjected to several types of uses.
Depending on the types of uses and activities, water quality criteria
have been specified to determine its suitability for a particular purpose. Among the various types of uses there is one
use that demands highest level of water quality/purity and that is termed a
designated best use in that stretch of the coastal segment. Based on this, the primary water quality
criteria haves been specified for following five designated best uses-.
|
Class |
Designated best use |
|
SW-1 (See Table 1.1) |
Salt
pans, shell fishing, mariculture and ecologically sensitive zone. |
|
SW-II (See Table 1.2) |
Bathing,
contact water sports and commercial
fishing. |
|
SW-III (See Table 1.3). |
Industrial
cooling, recreation (non-contact) and
aesthetics. |
|
SW-IV (See Table 1.4). |
Harbour. |
|
SW-V (See Table 1.5). |
Navigation
and controlled waste disposal. |
The standards along with
rationale/remarks for various parameters, for different designated best uses,
are given in Tables 1.1 to 1.5
TABLE 1.1
PRIMARY WATER QUALITV CRITERIA FOR CLASS SW-1 WATERS
(For
Salt pans, shell fishing, mariculture and ecologically sensitive zone)
|
Sl.
No. |
Parameters |
Standards |
Rationale/Remarks
|
|
(1) |
(2) |
(3) |
(4) |
|
1. |
pH
range |
6.5
8.5 |
General
board range, conductive for propagation of aquatic lives, is given. Value
largely dependant upon soil-water integration. |
|
Sl.
No. |
Parameters |
Standards |
Rationale/Remarks
|
|
(1) |
(2) |
(3) |
(4) |
|
2. |
Dissolved
oxygen |
5.0 mg/l or 60 percent saturation value, whichever
is higher |
Not less than 3.5 mg/l at any time of the year for
protection of aquatics lives. |
|
3. |
Colour
and odour |
No noticeable colour or offensive odour. |
Specially caused by chemical compounds like
creosols, phenols, naptha, pyridine, benzene, toluene etc., causing visible
coloration of salt crystal and tainting of fish flesh. |
|
4. |
Floating
matters |
Nothing obnoxious or detrimental for use purples. |
Surfactants should not exceed an upper limit of
1.0 mg/l and the concentration not to cause any visible foam. |
|
5. |
Suspended
solids |
None from sewage or industrial waste origin. |
Settleale inert matters not in such concentration
that would impair any usages specially assigned to this class. |
|
6. |
Oil
& Grease (Including
petroleum products) |
0.1 mg/l |
Concentration should not exceed 0.1 mg/l as
because it has effect on fish eggs and larvae. |
|
7. |
Heavy
metals: |
|
Values depend upon: |
|
Mercury
(as Hg) |
0.01 mg/l |
(i)
Concentration in salt. Fish and shell fish. |
|
|
Lead
(as Pb) |
0.01 mg/l |
(ii) Average per capita consumption per day |
|
|
Cadmium
(as Cd). |
0.01 mg/l |
(iii) Minimum ingestion rate that induces
symptoms of resulting diseases. |
Note. - SW-1 is desirable to be safe
and relatively free from hazardous chemicals like pesticides, heavy metals and
radionuclide concentrations. Their combined (synergetic or antagonistic)
effects on health and aquatic lives are not yet clearly known. These chemicals undergo bio-accumulation,
magnification and transfer to human and other animals through food chain. In areas where fisheries, salt pans are the
governing considerations, and presence of such chemicals apprehended/reported,
bioassay test should be performed following appropriate methods for the purpose
of setting case specific limits.
TABLE 1.2
PRIMARY WATER QUATITY CRITERIA FOR CLASS SW-II WATERS
(For
Bathing, Contract Water Sports and Commercial Fishing)
|
Sl.
No. |
Parameter |
Standards |
Rationale/Remarks |
|
1. |
pH
range |
6.5-8.5 |
Range does not cause skin or eye irritation and is also conductive for propagating aquatic lives. |
|
2. |
Dissolved
oxygen |
4.0 mg/l or 50 per cent saturation value, which
ever is higher. |
Not less than 3.5 mg/l at anytime for protection of aquatic lives. |
|
3. |
Colour
and odour |
No noticeable colour or offensive odour. |
Specially caused by chemical compound like creosols, phenols, naptha, benzene, pyridine, toluene etc., causing visible colouration of water and tainting of and odour in fish flesh. |
|
Sl.
No. |
Parameter |
Standards |
Rationale/Remarks |
|
4. |
Floating
matters |
Nothing obnoxious or
detrimental for use purpose. |
None in concentration that would impair usages specially assigned to this class. |
|
5. |
Turbidity |
30 NTU (Nephelo Turbidity
Unit). |
Measured at 0.9 depth |
|
6. |
Fecal
coliform |
100/100 ml (MPN) |
The average value not exceeding 200/100 ml. in 20 percent of samples in the year and in 3 consecutive samples in monsoon months. |
|
7. |
Biochemical
oxygen demand (BOD) (3 days at 270C) |
3 ml/l |
Restricted for lathing (aesthetic quality of water). Also prescribed by IS: 2296-1974. |
TABLE 1.3
PRIMARY WATER QUALITY CRITERIA FOR CIASS
SW-III WATER
(For
Industrial Cooling, Recreation (non-contact) and Aesthetics)
|
Sl.
No. |
Parameter |
Standards |
Rationale/Remarks |
|
1. |
pH
range |
6.5-8.5 |
The range is conductive for propagation of aquatic species and restoring natural. |
|
2. |
Dissolved
oxygen |
3.0 mg/l or 40 per cent saturation value, which
ever is higher. |
To protect aquatic lives. |
|
Sl.
No. |
Parameter |
Standards |
Rationale/Remarks |
|
3. |
Colour
and odour |
No noticeable colour or offensive odour. |
None in such concentration that would impair usages specifically assigned to this class. |
|
4. |
Floating
matters |
No visible obnoxious
floating debris oil slick, scum. |
As in (3) above. |
|
5. |
Fecal
coliform |
500/100 ml (MPN) |
Not exceeding 1000/100 ml in 20 percent of samples in the year and in 3 consecutive samples in monsoon months. |
|
6. |
Turbidity |
30 NTU |
Reasonably clear water for recreation, aesthetic appreciation and industrial cooling purposes. |
|
7. |
Dissolved
iron (as Fe) |
0.5 mg/l or less |
It is desirable to have the collective concentration of dissolved Fe and Mn less or equal to 0.5 mg mg/l to avoid scaling effect. |
|
8. |
Dissolved
manganese (as Man) |
0.5 mg/l or less |
|
|
* Standards included exclusively for Industrial Cooling purpose, Other parameters same. |
|||
TABLE
1.4
PRIMARY
WATER QUALITY CRITERIA FOR
CLASS
SW-IV WATERS
(For
Harbour Waters)
|
Sl.
No. |
Parameter |
Standards |
Rationale/Remarks |
|
1. |
pH
range |
6.5-9.5 |
The minimum corrosive and scaling effect. |
|
2. |
Dissolved
oxygen |
3.0 mg/l or 40 per cent saturation value,
whichever is higher. |
Considering bio-degradation of oil and inhibition to oxygen production through photosynthesis. |
|
3. |
Colour
and odour |
No visible colour or offensive odour. |
None from reactive chemicals, which may corrode paints/ metallic surfaces. |
|
4. |
Floating materials, oil, grease and scum
(including petroleum products) |
10 mg/l |
Floating matter should be free from excessive living organism, which may clog or coat operative parts of marine vessels/equipment. |
|
5. |
Fecal
coliform |
500/100 ml (MPN) |
Not exceeding 1000/100 ml in 20 percent of samples in the year and in 3 consecutive samples in monsoon months. |
|
6. |
Biochemical
oxygen demand (3
days at 270C) |
5 ml/l |
To maintain water relatively free from pollution caused by sewage and other decomposable wastes. |
TABLE
1.5
PRIMARY
WATER QUALITY CRITERIA FOR
CLASS
SW-V WATERS
(For Navigation and Controlled Waste Disposal)
|
Sl.
No. |
Parameter |
Standards |
Rationale/Remarks
|
|
1. |
pH
range |
6.5-9.0 |
As specified by the New England Interstate Water
Pollution Control Commission. |
|
2. |
Dissolved
oxygen |
3.0 mg/l or 40 per cent saturation value,
whichever is higher. |
To protect aquatic lives. |
|
3. |
Colour
and odour |
None is such concentration that would impair any
usages specifically assigned to this class.
|
As in (1) above. |
|
4. |
Sludge deposits, solid refuse, floating solids,
oil, grease and scum. |
None except for such small
amount that may result from discharge of appropriately treated sewage and/or
industrial waste effluents. |
As in (1) above. |
|
5. |
Fecal
coliform |
500/100 ml (MPN) |
Not exceeding 1000/100 ml in 20 percent of samples in the year and in 3 consecutive samples in monsoon months. |
87. Emission regulations for rayon industry:
(a) Existing plants
Estimation of uncontrolled emission quantity (EQ) of
CS2
For VSF,
EQ= 125 kg
of CS2/t of fibre
For VFY,
EQ= 225 kg of CS2/t of fibre
|
Stack
Height (H) Requirement, m |
Remarks |
|
11Q 0.41-3 Vs D/u |
A minimum of 80 percent of
total emission shall pass through stack.
If the calculated stack height is less than 30m, a minimum height of
30m shall be provided |
Where Q-CS2
emission rate, kg/hr
Vs-stack
exit velocity, m/sec.
D-diameter
of stack, m
U-annual
average wind speed at top of stack, m/sec.
Multiple stacks:
1. If there are more than
one stack existing in the plant, the required height of all stacks shall be
based on the maximum emission rate in any of the stacks. In other words, all the stacks carrying CS2, emission shall be of same
heights (based on the maximum emission rate).
2. Number of stacks shall
not be increased from the existing number. However, the number of stacks may be
reduced. The existing stacks may be
rebuilt and if stacks are to be relocated, condition 3 below applies.
3. Spacing among the stack
(x) at the minimum shall be 3.0 H (in m).
If distance, x, between two stacks is less than 3.0 H (in m), emission
shall be considered as single point
source and height of both the stacks shall be calculated considering all
emission is going through one stack.
(b)
Ambient air quality monitoring:
The industry
shall install three air quality-monitoring stations for CS2, and H2S measurements in
consultation with State Pollution Control Board (SPCB) to ensure attainment of
WHO recommended ambient air quality norms (CS2 = 100 mg/m3 and H2S=150 mg/m3 24 = hr, average).
(c) For new plants/expansion
projects being commissioned oil or after June 1, 1999.
Permissible emission limits are:
CS2 =21 kg/t of fibre
H2S = 6.3 kg/t of fibre
(Note:
a. and b. above also apply to new plants/expansion projects).
SCHEDULE II
1[***]
1. Schedule II relating to
Rule 3, inserted vide G.S.R. 919 (E),
dated 12th September, 1988, now omitted by G.S.R. 80 (E), dated 31st December,
1993 (w.e.f. 31.12.1993).
2. Ins. by G.S.R. 1063 (E) dated 26th December
1989 (w.e.f. 26-12-1989).
(See Rule 3)
Ambient Air Quality
Standards in Respect of Noise
|
Area Code |
Category of Area |
Limits in dB (A) |
Leg- |
|
|
|
Day Time |
Night Time |
|
(A) |
Industrial
area |
75 |
70 |
|
(B) |
Commercial
area |
65 |
55 |
|
(C) |
Residential
area |
55 |
45 |
|
(D) |
Silence
Zone |
50 |
40 |
Note-1. Day time is reckoned in between 6
a.m. and 9 p.m.
Note-2 Nigh time is reckoned in between 9
p.m. and 6 a.m.
Note-3 Silence zone is
defined as areas upto 100 metres around such premises as hospitals, educational
institutions and courts. The Silence zones are to be declared by the Competent
Authority.
Use of
vehicular horns, loudspeakers and bursting of crackers shall be banned in these
zones.
Note-4 Mixed categories
of areas should be declared as one of the four above mentioned categories by
the Competent Authority and the corresponding standards shall apply.)
1. Ins.
by G.S.R. 54 (E) dated 5th February 1990 (w.e.f. 05.02.1990).
(See Rule 3)
Standards for Emission of
Smoke, Vapour, etc. from Motor Vehicles
(1) Every motor vehicle
shall be manufactured and maintained in such condition and shall be so driven
that smoke, visible vapour, grit, sparks, ashes, cinders or only substance do
not emit therefrom.
(2) On and from the 1st day of March 1990, every motor
vehicle in use shall comply with the following standards: -
(a) Idling CO (Carbon
monoxide) emission limit for all four-wheeled petrol driven vehicles shall not
exceed 3 per cent by volume;
(b) Idling CO emission limit
for all two and three-wheeled petrol driven vehicles shall not exceed 4.5 per cent by volume;
(c) Smoke density for all diesel driven vehicles shall be as
follows--
|
Method
of Test |
Maximum smoke density |
||
|
|
Light
absorption co-efficient m-1 |
Bosch
Units |
Harridge
Units |
|
Full load at a speed of 60% to 70% of maxi- mum
engine rated speed declared |
3.1 |
5.2 |
75 |
|
Free acceleration |
2.3 |
|
65 |
(3) On and from the Ist day of April, 1991,
all petrol driven vehicles shall be so manufactured that they comply with the
mass emission standards as specified at Annexure I. The breakdown of the
operating cycle used for the test shall be as specified at Annexure 11 and
the reference fuel for all such tests shall be as specified in Annexure III
to this Schedule.
(4) On and from the Ist day of April, 1991
all diesel driven vehicles shall be so manufactured that they comply with the
mass emission standards based on exhaust gas opacity as specified at Annexure IV
to this Schedule.
(5) On and from the Ist day of April, 1992,
all diesel driven vehicles shall be so manufactured that they comply with the
following levels of emissions under the Indian driving cycle: -
|
Mass of Carbon Monoxide
(CO). Maximum. Grams per KWH |
Mass of Hydro Carbons (HC) Maxim. Grams per KWH |
Mass of
Nitrogen Oxides (NO) Maximum
Grams per KWH |
|
14 |
3.5 |
18 |
(6) Each motor vehicle manufactured on and
after the dates specified in paragraphs (2), (3), (4) and
(5) Shall be certified by the manufacturers
to be conforming to the standards specified in the said paragraphs and the
manufactures shall further certify that the components liable to effect the
emission of gaseous pollutants are so designed, constructed and assembled as to
enable the vehicle, in nominal use, despite the vibration to which it may be
subjected, to comply with the provisions of the said paragraphs.
(7) Test for smoke emission level and Carbon Monoxide level for
motor vehicles. -
(a) Any officer not below the rank of a
Sub-inspector of police or an Inspector of motor vehicles, who has reason to
believe that a motor vehicle is by virtue of smoke emitted from it or other
pollutants like Carbon Monoxide emitted from it, is likely to cause
environmental pollution, endangering the health or safety of any other user of
the road or the public, may direct the driver or any person in-charge of the
vehicle to submit the vehicle for undergoing a test to measure the standard of
black smoke or the standard of any other pollutants.
(b) The driver or any person in-charge of the
vehicle shall upon demand by any officer referred to in sub-paragraph (a),
submit the vehicle for testing for the purpose of measuring the standard of
smoke or the levels of other pollutants or both.
(c) The measurement of standard of smoke
shall be done with a smoke meter of a type approved by the State Government and
the measurement of other pollutants like Carbon Monoxide shall be done with
instruments of a type approved by the State Government.
ANNEXURE-I
(See paragraph 3)
Mass Emission
Standards for Petrol driven Vehicles
1. Type Approval Tests:
Two and Three Wheeler
Vehicles
|
Reference
Mass, R (Kg) |
CO
(g/km) |
HC
(g/km) |
|
1 |
2 |
3 |
|
R < 150 |
12 |
8 |
|
150 < |
12 18 (R-150) 200 |
8+ 4(R-150) 200 |
|
R > 350 |
30 |
12 |
Light Duty Vehicles:
|
Reference
Mass, rw (Kg) |
CO (g/km) |
HC (g/km) |
|
1 |
2 |
3 |
|
r w < 1020 |
14.3 |
2.0 |
|
1020<
r w < 1250 |
16.5 |
2.1 |
|
1250<
r w < 1470 |
18.8 |
2.1 |
|
1470<
r w < 1700 |
20.7 |
2.3 |
|
1700<
r w < 1930 |
22.9 |
2.5 |
|
1930<
r w < 2150 |
24.9 |
2.7 |
|
r w < 2150 |
27.1 |
2.9 |
2.
Conformity of Production Tests:
|
Reference Mass, rw (Kg) |
CO (g/km) |
HC (g/km) |
|
1 |
2 |
3 |
|
R < 150 |
15 |
8 |
|
150 < 350 |
15+ 25 (R-150) 200 |
10+ 5 (R-150) 200 |
|
R > 350 |
40 |
15 |
|
r w < 1020 |
17.3 |
2.7 |
|
1020< r w < 1250 |
19.7 |
2.7 |
|
1250< r w < 1470 |
22.5 |
2.8 |
|
1470< r w < 1700 |
24.9 |
3.0 |
|
1700< r w < 1930 |
27.6 |
3.3 |
|
1930< r w < 2150 |
29.9 |
3.5 |
|
r w < 2150 |
32.6 |
3.7 |
For any of the pollutants referred to above of the
three results obtained may exceed the limit specified for the vehicle by not
more than 10 percent.
Explanation. -Mass emission standards refer to the gm.
of pollutants emitted per km. run of the vehicle, as determined by a
chassis dynamometer test using the Indian Driving Cycle.
ANNEXURE
(See paragraph -3)
Breakdown of the
Operating Cycle used for the Tests.
|
Sl. No. |
No. of Operation |
Acceleration (m/ac2) |
Speed (Km/h) |
Duration of each Operation(s) |
Cumulative Time (s) |
|
1 |
2 |
3 |
4 |
5 |
6 |
|
01. |
Idling |
- |
- |
16 |
16 |
|
02. |
Accelera6on |
0.65 |
0-14 |
6 |
22 |
|
03. |
Acceleration |
0.56 |
14-22 |
4 |
26 |
|
04. |
Deceleration |
-0.63 |
22-13 |
4 |
30 |
|
05. |
Steady speed |
- |
13 |
2 |
32 |
|
06. |
Acceleration |
0.56 |
13-23 |
5 |
37 |
|
07. |
Acceleration |
0.44 |
23-31 |
5 |
42 |
|
08. |
Deceleration |
-0.56 |
31-25 |
3 |
45 |
|
09. |
Steady speed |
- |
25 |
4 |
49 |
|
10. |
Deceleration |
-0.56 |
25-21 |
2 |
51 |
|
11. |
Acceleration |
0.45 |
21-34 |
8 |
59 |
|
12. |
Acceleration |
0.32 |
34-42 |
7 |
66 |
|
13. |
Deceleration |
-0.46 |
42-37 |
3 |
69 |
|
14. |
Steady
speed |
- |
37 |
7 |
76 |
|
15. |
Deceleration |
-0.42 |
34-34 |
2 |
78 |
|
16. |
Acceleration |
0.32 |
34-42 |
7 |
85 |
|
17. |
Deceleration |
-0.46 |
42-47 |
9 |
94 |
|
18. |
Deceleration |
-0.52 |
27-14 |
7 |
101 |
|
19. |
Deceleration |
-0.56 |
14-00 |
7 |
108 |
ANNEWRE -III
(See paragraph 3)
Reference Fuel
for type and Production Conformity Tests
|
S.
No. |
Characteristic |
Requirements |
Method
of test (ref. of P: or IS: 1448*) |
||||
|
87 Octane |
93 Octane |
||||||
|
1 |
2 |
3 |
4 |
5 |
|||
|
1. |
Colour,
visual |
Orange |
Red |
- |
|||
|
2. |
Copper-strip
corrosion for 3 hours at 500C |
Not
worse than No. 1 |
|
P: 15 (1968) |
|||
|
3. |
Density
at 150C Not |
Not limited but to be reported |
|
P: 16(1967) |
|||
|
4. |
Distillation: |
|
|
P:18 (1967) |
|||
|
|
(a) |
Initial boiling point |
Not
limited but to be reported |
|
|||
|
|
(b) |
Recovery upto 200C percent by Volume Min, |
10 |
10 |
|
||
|
|
(c) |
Recovery upto 1250C 50 per cent by
volume |
50 |
50 |
|
||
|
|
(d) |
Recovery upto 1300C 50 percent by
volume, Min |
90 |
90 |
|
||
|
Sl.
No. |
Characteristic |
Requirements |
Method
of test (ref. of P: or IS: 1448*) |
||||
|
87 Octane |
93 Octane |
||||||
|
1 |
2 |
3 |
4 |
5 |
|||
|
4. |
(e) |
Final boiling poin4 Max. |
2150C |
2150C |
|
||
|
|
(f) |
Residue percent by volume, Max. |
2 |
2 |
|
||
*Methods of test for petroleum and its products.
|
5. |
Octane
number (Research method) Max. |
87 |
94 |
P:
27 (1960) |
|
6. |
Oxidation
stability in minutes, Min. |
360 |
360 |
P:
28 (2966) |
|
7. |
Residue
on evaporation mg/100 ml, Max. |
4.0 |
4.0 |
P:
29 (1960) |
|
|
Air-jet solvent washed |
|||
|
8. |
Sulphur,
total, percent by weight Max. |
0.25 |
0.20 |
P:
34 (1966) |
|
9. |
Lead
content (as Pb), g/l Max. |
0.56 |
0.80 |
P:
37 (1967) or |
|
|
|
|
|
P:
38 (1967) |
|
10. |
Reid
vapour pressure at 38 degree C |
0.70 |
0.70 |
P:
39 (1967) |
ANNEXURE IV
(See paragraph 4)
Limit Values of Exhaust Gas Opacity applicable for Diesel Driven Vehicles The engine tests at steady speed
|
Nominal
Flow G(I/s) |
Absorption
Co-efficient K(m-1) |
Nominal
Flow G(I/s) |
Absorption
Co-efficent |
|
42 |
2.00 |
120 |
1.20 |
|
45 |
1.91 |
125 |
1.17 |
|
50 |
1.82 |
130 |
1.15 |
|
55 |
1.75 |
135 |
1.31 |
|
60 |
1.68 |
140 |
1.11 |
|
65 |
1.61 |
145 |
1.09 |
|
70 |
1.56 |
150 |
1.07 |
|
75 |
1.50 |
155 |
1.05 |
|
80 |
1.46 |
160 |
1.04 |
|
85 |
1.41 |
165 |
1.02 |
|
90 |
1.38 |
170 |
1.01 |
|
95 |
1.34 |
175 |
1.00 |
|
100 |
1.31 |
180 |
0.99 |
|
105 |
1.27 |
185 |
0.97 |
|
110 |
1.25 |
190 |
0.96 |
|
115 |
1.22 |
195 <200 |
0.95 0.93 |
1SCHEDULE 2[V]
(See Rule 12)
|
Sl.
No. |
Place
at which the discharge of any environment pollutant in excess of prescribed
standards occurs or is apprehended to occur |
Authorities
or agencies to be intimated |
Appointed
under |
|
|
|
|
|
|
1.
|
Factories
as defined under the Factories 1948- |
|
|
|
(a)
Owned by the Central Government and engaged in carrying out the
purposes of the Atomic Energy Act, 1962. |
(i)Atomic
Entergy Regulatory Board
(AERB). |
The
Atomic Energy Act,
1962 |
|
|
(ii)
The Ministry of Environment and Forests |
|||
|
|
(b) Factories other than those mentioned in para. (a) |
(i) The Chief Inspector of Factories |
The
Factories Act, 1948 |
|
(ii) The Inspector of Factories having local
jurisdiction |
-Do- |
||
|
(iii) The Ministry of Environment and Forests |
|
||
|
2.
|
Mine
as defined under the Mines and |
3[(i) Controller- |
The
Mines and |
|
|
Minerals
Mines and (Regulation and Development) Act, 1957 |
General of Mines] |
Minerals
(Regulation and
Development) Act,
1957 |
|
3[(ii) Regional Controller
of Mines having local jurisdictions |
-Do- |
||
|
(iii) The Ministry of Environment and Forests |
|
||
|
3.
|
Port
as defined under the Indian Ports Act, 1908 |
(i) Conservator of Ports |
The
Indian Ports Act, 1908 |
|
(ii) The Ministry of Environment and Forests |
-Do- |
||
|
4. |
Plantation as defined under the Plantations Labour Act, 1951 |
(i) The Chief Inspector of Plantations |
The
Plantations Labour
Act, 1951 |
|
|
|
(ii) The Inspector of Plantations having local
jurisdiction |
-Do- |
|
(iii) The Ministry of Environment and Forests |
|
||
|
5.
|
Motor
Vehicle as defined under the Motor Vehicles
Act, 1939 |
(i) State Transport Authority |
The
Motor Vehicles Act,
1939 |
|
(ii) Regional Transport Authority having Regional jurisdictions |
-Do- |
||
|
(iii) The Ministry of Environment and Forests |
|
||
|
6. |
Ship
as defined under the Merchant Shipping
Act, 1958 |
(i) Director-General of
Shipping |
The
Merchant Shipping Act, 1958 |
|
(ii) Surveyor having jurisdiction |
-Do- |
||
|
(iii) The Ministry of Environment and Forests |
-Do- |
(See Rule 3-A)
General Standards for discharge of environmental
Pollutants Part-A Effluents
|
Sl.
No. |
Parameters |
STANDARDS |
|||
|
|
Inland
surface Water |
Public
Sewers |
Land
for irrigation |
Marine
coastal areas |
|
|
1 |
2 |
3 (a) |
3 (b) |
3 (c) |
3 (d) |
|
1. |
Colour
and odour |
See
6 of |
See
6 of |
See
6 of Annexure-I |
See
6 of Annexure-I |
|
2. |
Suspended
solids mg/l, Nax. |
100 |
600 |
200 |
(a) For process waste water-100. |
|
|
|
|
|
|
For cooling water effluent 10 percent above total
suspended matter of influent. |
|
3. |
Particle
size of suspended solids. |
Shall
pass 850 micron IS Sieve |
_______ |
|
(a) Floatable solids max. 3 mm. |
|
|
|
|
|
|
(b). Settleable solids, max 850 microns. |
|
4 |
2[***] |
|
|
|
|
|
5. |
pH
value. |
5.5
to 9.0 |
5.5
to 9.0 |
5.5
to 9.0 |
5.5 to 9.0 |
|
6. |
Temperature |
Shall
not exceed 50C above the receiving water temperature |
Shall
not exceed 50C
above the receiving water temperature |
|
|
|
7. |
Oil
and grease mg/1 Max. |
10 |
20 |
10 |
20 |
|
8.
|
Total
residual chlorine mg/1 Max. |
1.0 |
|
|
1.0 |
|
9. |
Ammonical
nitrogen (as N), mg/1 Max. |
50 |
50 |
|
50 |
|
10. |
Total
Kjeldhal nitrogen 3[N]; |
100 |
|
|
100 |
|
11. |
Free
ammonia 3[NH3]
mg/1, Max. |
|
|
|
|
|
12. |
Biochemical
oxygen demand (5 days at 200C) 3[mg/1,
Max.] |
30 |
350 |
100 |
100 |
1. Ins. by G.S.R. 422 (E), dated 19th May,
1993 (w.e.f. 19.05.1993).
2. Omitted by G.S.R. 80 (E), dated 31st
December, 1993 (w.e.f. 31.12. 1993).
3. Subs. by G.S.R. 80 (E), dated 31st
December, 1993 (w.e.f. 31.12. 1993).
|
13. |
Chemical Oxygen demand, mg/1, Max. |
250 |
|
|
250 |
|
14. |
Arsenic (as As). 1[mg/1],
Max. |
0.2 |
0.2 |
0.2 |
0.2 |
|
15. |
Mercury (As Hg), mg/1, Max. |
0.01 |
0.01 |
|
0.01 |
|
16. |
Lead (as Pb) mg/1, Max |
0.1 |
1.0 |
|
2.0 |
|
17. |
Cadmium (as Cd0 mg/1, Max. |
2.0 |
1.0 |
|
2.0 |
|
18. |
Hexavalent chromium (as Cr+ 6), mg/1, Max. |
0.1 |
2.0 |
|
1.0 |
|
19. |
Total chromium (as Cr) mg/1, Max. |
2.0 |
2.0 |
|
2.0 |
|
20. |
Copper (as Cu) mg/1, Max. |
3.0 |
3.0 |
|
3.0 |
|
21. |
Zinc (as Zn) mg/1, Max. |
5.0 |
15 |
|
15 |
|
22. |
Selenium (as Se) mg/1, Max. |
0.05 |
0.05 |
|
0.05 |
|
23. |
Nickel (as Ni) Mg/1, Max. 2[* * *] |
3.0 |
3.0 |
|
5.0 |
|
27. |
Cyanide (as CN) mg/1, Max. 2[* * *] |
0.2 |
2.0 |
0.2 |
0.2 |
|
29. |
1[Fluoride] (as F) mg/1, Max. 2[* * *] |
2.0 |
15 |
|
15 |
|
30. |
Dissolved phosphates (as P), mg/1, Max. 2[* * *] |
5.0 |
|
|
|
|
32. |
Sulphide (as S) mg/1, Max. |
2.0 |
|
|
5.0 |
|
33. |
Phenolic compounds 1[as C6H5OH] mg/1, Max. |
1.0 |
5.0 |
|
5.0 |
1. Subs. by G.S.R. 80(E), dated 31st
December, 1993 (w.e.f. 31.12.1993).
2. Omitted by G.S.R. 80(E), dated 31st
December, 1993 (w.e.f. 31.12.1993).
|
34. |
Radioactive materials: (a) Alpha emitters 1[Micro curie/ml] Max. |
10-7 |
10-7 |
1[0-8] |
10-7 |
|
(b) Beta emitters 1[Micro curie/ml] Max. |
10-6 |
10-6 |
10-7 |
1[10-6] |
|
|
35. |
Bio-assay test |
90% survival of fish after 96 hours in 100%
effluent |
90% survival of fish after 96 hours in 100%
effluent |
90% survival of fish after 96 hours in 100%
effluent |
90% survival of fish after 96 hours in 100% effluent |
|
36. |
Manganese (as Man) |
2 mg/1 |
2 mg/1 |
|
2 mg/1 |
|
37. |
Iron (as Fe) |
3mg/1 |
3mg/1 |
|
3mg/1 |
|
38. |
Vanadium (as V) |
0.2 mg/1 |
0.2 mg/1 |
|
0.2 mg/1 |
|
39. |
Nitrate Nitrogen |
10 mg/1 |
|
|
20 mh/1 |
|
40. |
Pesticides: (microgm per lit, maximum) |
|
|
|
|
|
|
(i) Benzene hexa-chloride |
10 |
__________ |
10 |
10 |
|
(ii) Carboryl |
10 |
__________ |
10 |
10 |
|
|
(iii) DDT |
10 |
__________ |
10 |
10 |
|
|
(iv) Endosulfan |
10 |
__________ |
10 |
10 |
|
|
(v) Diamethoate |
450 |
__________ |
450 |
450 |
|
|
(vi) Penitrothion |
10 |
__________ |
10 |
10 |
|
|
(vii) Malathion |
10 |
__________ |
10 |
10 |
|
|
(viii) Phorate |
10 |
__________ |
10 |
10 |
|
|
(ix) Methyl Parathion |
10 |
__________ |
10 |
10 |
|
|
(x)Phenthoate |
10 |
__________ |
10 |
10 |
|
|
(xi)Pyrethrums |
10 |
__________ |
10 |
10 |
|
|
(xii)
Copper Oxychloride |
9600 |
__________ |
9600 |
9600 |
|
|
(xiii)Copper Sulphate |
50 |
__________ |
50 |
50 |
|
|
(xiv) Ziram |
1000 |
__________ |
1000 |
1000 |
|
|
(xv) Sulphur |
30 |
__________ |
30 |
30 |
|
|
(xvi) Parsouat |
2300 |
__________ |
2300 |
2300 |
|
|
(xvii) Proponil |
7300 |
__________ |
7300 |
7300 |
|
|
(xviii) Nitrogen |
780 |
__________ |
780 |
780 |
1. Subs. by G.S.R. 80(E), dated 31st
December, 1993 (w.e.f. 31.12.1993).
PART B
Waste Water Generation Standards
|
Sl.
No. |
Industry |
Quantum |
|
1. |
Integrated
Iron & Steel |
16
1[m3/tonne] of
finished steel |
|
2. |
Sugar |
0.4
1[m3/tonne] of
cane crushed |
|
3. |
Pulp & Paper Industries |
|
|
(a) Larger pulp & paper |
||
|
(i) Pulp& paper |
175
1[m3/tonne] of
paper produced |
|
|
1[(ii) Viscose Staple Fibre |
150
m3/tonne of product |
|
|
(iii) Viscose Filament Yarn |
500m3/tonne
of Product] |
|
|
(b) Small pulp & paper: |
||
|
(i) Agro-residue based |
150
1[m3/tonnelof
paper produced |
|
|
(ii) Waste paper based |
50
1 [m3/tonne] of
paper produced |
|
|
4. |
Fermentation Industries |
|
|
(a) Maltry |
3.5
1 [m3/tonnel of
grain produced |
|
|
(b) Brewery |
0.25
M3/KL of beer produced |
|
|
(c) Dis6liery |
12
M3/KL of alcohol produced |
|
|
5. |
Caustic
Soda |
|
|
(a) Membrane cell process |
1 [m/tonne] of caustic soda produced excluding
cooling tower blow down |
|
|
(b) Mercury cell process |
4
1 [m3/tonne] of
caustic soda produced (mercury
hearing), 10% blow down permitted
for cooling tower |
|
|
6. |
Textile
Industries: Man-made
Fibre |
|
|
(i) Nylon & Polyster |
120
1 [ml/tonne] of Fibre
produced |
|
|
(ii) Viscose rayon |
150
1 [m3/tonne] of
product 28 |
|
|
7. |
Tanneries |
28
1 [m+/tonne] of raw hide |
|
8. |
Starch,
Glucose and related products |
8
1 [m3/tonne] of
maize crushed |
|
9. |
Dairy |
3M3/KL
of Milk |
|
10. |
Natural
rubber processing industry |
4
1 [m3/tonne] of
rubber |
|
11. |
Fertiliser |
|
|
(a) Straight nitrogenous fertiliser |
5
1 [m3/tonne] of
urea or equivalent produced |
|
|
(b) Straight phosphatic fertiliser (SSP & TSP) "eluding
manufacture of any acid |
0.5
1 [m3/tonnel of
SSP/TSP |
|
|
(c) Complex fertiliser |
Standards
of nitorgenous and phosphatic
fertiliser are applicable depending on the primary product. |
1. Subs. by G.S.R.
80 (E), dated 31st December, 1993 (w.e.f. 31.12.1993).
PART C
Load Based Standards
1. Oil Refinery Industry:
|
Parameter |
Quantum
in 1[Kg]/1000 tonnes of
crude processed |
|
Oil
& grease |
10.00 |
|
Phenol |
0.70 |
|
BOD |
10.50 |
|
Suspended
solids |
14.00 |
|
Sulphide |
0.35 |
|
2. Large Pulp & Paper, News Print/Rayon grade plants of
capacity above 24000 1[tonne]/Annum |
|
|
Parameter |
Quantum |
|
Total
Organic Chloride (TOCI) |
2
1[Kg/tonne] of product. |
PART D
General Emission Standards
I. Concentration Based Standards:
|
Sl. No. |
Parameter |
Standard Concentration not to exceed (in mg/Nm3) |
|
1. |
1[Particulate Matter (PM)] |
150 |
|
2. |
1[Total Fluoride] |
1[25] |
|
3. |
Asbestos |
1[4Fibres/ccanddustshould not be more then
2 mg/Nm3] |
|
4. |
Mercury |
0.2 |
|
5. |
Chlorine |
15 |
|
6. |
Hydrochloric
acid vapour and mist 2[***] |
35 |
|
8. |
Sulphuric
acid mist |
50 |
|
9. |
Carbon
monoxide 2[***] |
1[1% max (v/v)] |
|
11. |
Lead 2[***] |
1[10 mg(Nm3] |
1. Subs. by G.S.R. 80 (E), dated 31st
December, 1993 (w.e.f. 31.12.1993).
2. Omitted by G.S.R. 80 (E), dated 31st
December, 1993 (w.e.f. 31.12.1993).
II. Equipment Based Standards:
1[For dispersal of sulphur
dioxide, a minimum stack height limit is accordingly prescribed as below:]
|
Sl.
No. |
Parameter |
Standard |
|
1. |
Sulphur
dioxide |
Stack-height
limit in 1[metre] |
|
(i) Power generation capacity: -500 MW and more -200/210 MW and above to less than 500 MW -4ess than 200/210 MW |
275 220 H
= 14 (Q)0..3 |
|
|
(ii)
Steam generation capacity -Less than 2 1[tonne/hr] -2 to 5 1
[tonne/hr] -5 to 10 1[tonne/hr] -10 to 15 1 [tonne/hr] -15 to 20 1[tonne/hr] -20 to 25 1[tonne/hr] -25 to 30 1[tonne/hr] -More than 30 T/hr |
Coal
consumption per day 2[***] |
Note- H-Physical height of the stack in 1[Metre]
Q-Emission rate of S02 in kg/hr. 2[***]
III. Load/Mass-based Standards:
|
Sl.
No. |
Industry |
Parameter |
Standard |
|
1. |
1[Fertiliser] (Urea) Commissioned
prior to 1-1-1982 Commissioned
after 1-1-1982 |
1 [Particulate Matter PM)] 1 [particulate Matter PM)] |
2
1 [kg/tonne] of product 0.5
1 [kg/tonne] of product |
|
2. |
Copper,
Lead and 1 [Zinc Smelter
Converter] |
Sulphur
dioxide |
4
1 [kg/tonne] of concentrated 1 [(100%) and acid produced] |
|
3. |
Nitric
Acid |
Oxides
of Nitrogen |
3
1 [kg/tonne] of weak acid (before
concentration) produced |
|
4. |
Sulphuric
Acid |
Sulphur
dioxide |
4
1 [kg/tonne] of concentrated (100%)
acid produced |
|
5. |
Coke
Oven |
Carbon
monoxide |
3
1 [kg/tonne] of coke
produced |
|
6. |
Oil Refineries |
|
|
1. Subs. by G.S.R. 80 (E), dated 31st
December, 1993 (w.e.f. 31.12.1993).
2. Omitted by G.S.R. 80 (E), dated 31st December,
1993 (w.e.f. 31.12.1993).
(a) 1 [For the
oil refineries the following standards shall be applicable:]
|
Process |
Parameter |
Standard |
|
-Distillation
1[(Atmospheric plus Vaccum)] |
Sulphur
dioxide |
0.25
1 [kg/tonne] of feed in this process |
|
-Catalytic
cracker |
-Do- |
2.5
1 [kg/tonne] of feed in this
process |
|
-Sulphur
Recovery Unit |
-Do- |
120
1 [kg/tonne] of Sulphur in the
feed |
|
2[***] |
|
|
|
7. Aluminium Plants: |
|
|
|
(i) Anode Bake Oven |
Total
Fluoride |
0.3
Kg/MT of Aluminium |
|
(ii) Pot room |
|
|
|
(a) VSS - |
-do- |
4.7
Kg/MT of Aluminium |
|
(b) HSS - |
-do- |
6
Kg/MT of Aluminium |
|
(c) PBSW - |
-do- |
2.5
Kg/MT of Aluminium |
|
(d) PBCW - |
-do- |
1.0
Kg/MT of Aluminium |
|
Note: |
|
|
|
VSS = Vertical Stud Soderberg |
||
|
HSS = Horizontal Stud Soderberg |
||
|
1[PBSW = Pre Backed Side Work] |
||
|
1[PBCW = Pre Backed Centre Work] |
||
|
8. Glass Industry |
|
|
|
(a) Furnace Capacity |
|
|
|
(i) Up to the product draw-do- capacity of 60 MT/Day |
Particulate
matter |
2
kg/hr |
|
(ii) Product draw capacity more than 60 MT/Day |
-Do- Drawn |
0.8
Kg/MT of product |
PART E
Noise Standards
A.
Noise
limits for Automobiles 1[Free
Field Distance at 7.5 Metre] in dB(A) at the manufacturing Stage
|
(a) Motorcycle,
Scooters & Three-wheelers (b) Passenger
Cars (c) Passenger
or Commercial vehicles up to 4 MT (d) Passenger
or Commercial vehicles above 4 MT and up to 12 MT (e) Passenger
or Commercial vehicles exceeding 12 MT |
80 82 85 89 91 |
B. Domestic appliances and construction equipments at the
manufacturing stage to be achieved by 31st December, 1993
|
(a) Window Air Conditioners of I ton to 1.5 ton |
68 |
|
(b)
Air 1[coolers] |
60 |
|
(c) Refrigerators |
46 |
|
(d)
Diesel generator for domestic purposes |
85-90 |
|
(e)
Compactors (rollers), Front loaders, Concrete mixers, Cranes (movable),
Vibraturs and Saws. |
75 |
1. Subs. by G.S.R. 80(E), dated 31st
December, 1993 (w.e.f. 31.12.1993).
2. Omitted by G.S.R. 80(E), dated 31st
December, 1993 (w.e.f. 31.12.1993).
ANNEXURE I
(For the purposes of Parts A, B and C)
The State Boards shall follow the following
guidelines in enforcing the standards specified under Schedule VI: -
1. The waste waters and gases are to be treated with the best
available technology 1[(BAT)]
in order to achieve the prescribed standards.
2. The industries need to be encouraged for recycling and reuse
of waste materials as far as practicable in order to minimise the discharge of
wastes into the environment.
3. The industries are to be encouraged for recovery of biogas,
energy and reusable materials.
4. While permitting the discharge of effluents and omissions
into the environment, State Boards have to take into account the assimilative
capacities of the receiving bodies, especially water bodies so that quality of
the intended use of the receiving water is not affected. Where such quality is likely to be affected,
discharges should not be allowed into water bodies.
5. The Central and State Boards shall put emphasis on the
implementation of clean technologies by the industries in order to increase
fuel efficiency and reduce the generation of environmental pollutants.
6. All efforts should be made to remove colour and unpleasant
odour as for as practicable.
7. The standards mentioned in this Schedule 1[shall also apply to all other 1[effluents] discharged such as] mining, and
mineral processing activities and sewage.
8. The limit given for the total concentration of mercury in the
final effluent of caustic soda industry, is for the combined effluent from (a)
Cell house, (b) Brine plant, (c) Clorine handling, (d) Hydrogen handling, and
(e) Hydro chloric acid plant.
2[Omitted]
10. All effluents discharged including from the industries such as
cotton textile, composite woollen mills, synthetic rubber, small pulp and
paper, natural rubber, petrochemicals, tanneries, paint, dyes, slaughter
houses, food & fruit processing and dairy 1[industries]
into surface waters shall conform to the BOD limits specified above, namely, 30
mg/]. For discharge of an effluent
having a BOD more than 30 mg/I, the standards shall conform to those given
above for other receiving bodies, namely, sewers, coastal waters and land for
irrigation.
3[***]
12. In case of fertilizer industry the limits in respect of
chromium and 1[fluoride] shall
be complied with at the outlet of chromium and 1[fluoride]
removal units respectively.
13. In case of pesticides:
(a) The limits should be complied with at the end of treatment
plant before dilution.
(b) Bio-assay test should be carried out with
the available species of fish in the receiving water, the COD limits to be
specified in the consent conditions should be correlated with the BOD limits.
1. Subs. by G.S.R. 80(E), dated 31st
December, 1993 (w.e.f 31.12.1993).
2. Clause 9 was omitted by G.S.R. 176(E),
dated 2nd April, 1996 (w.e.f 3.4.1996).
3. Omitted by G.S.R. 80(E), dated 31st
December, 1993 (w.e.f 31.12.1993).
(c) In case metabolities and isomers of the
Pesticides in the given list are found in significant concentrations, standards
should be prescribed for these also in the same concentration as the individual
pesticides.
(d) Industries are required to analyse
pesticides in waste water by advanced analytical methods such as GLC/HPLC.
1[14. The chemical oxygen demand (COD) concentration in a treated
effluent, if observed to be persistently greater than 250 mg/l before disposal
to any receiving body (public sewer, land for irrigation, inland surface water
and marine coastal areas), such industrial units are required to identify
chemicals causing the same. In case
these are found to be toxic as defined in the Schedule I of the Hazardous
Wastes (Management and Handling) Rules, 1989 the State Boards in such cases
shall direct the industries to install tertiary treatment stipulating time limit.
15.
Standards specified in Part A of
Schedule VI for discharge of effluents into the public sewer shall be applicable only if such
sewer lead to a secondary treatment including biological treatment system,
otherwise these discharge into sewers shall be treated as discharge into inland
surface waters.]
ANNEXURE II
(For the purpose of Part D)
1. The State Boards shall follow the following guidelines in
enforcing the standards specified under Schedule VI: -
(a) In case of cement plants, the total dust
(from all sections) shall be within 400 mg/2[Nm3] and 250 Mg/2 [Nm] for the plants up to 200
t/d and more than 200 t/d capacities respectively.
(b) In respect of calcination process (e.g.
aluminium plants), Kilns and Step Grate Bagasse-fired Boilers. Particulate Matter (PM) emissions shall be
within 250 mg/2[Nm3].
(c) In case of thermal power plants
commissioned prior to 1-1-1982 and having generation capacity less than 62.5
MW, the PM emission shall be within 350 mg/2[Nm3].
(d) In case of Lime Kilns of capacity more
than 5t/day and up to 40t/day, the PM emission shall be within 500 Mg/2 [Nm3].
(e) In case of horse shoe/Pulsating Grate and
Spreader Stroker Bagasse-fired-Boilers, the PM emission shall be within 500
(12% CD,) and 800 (12% CO,) mg/2[NM3] respectively. In respect of these boilers, if more than
attached to a single stack, the emission standard shall be fixed, based on
added capacity of all the boilers connected with the stack.
(f) In case of asbestos dust, the same shall
not exceed 2 mg/2[Nm3].
(g) In case of the urea plants commissioned
after 1- 1 -1982, coke ovens and lead glass units, the PM emission shall be
within 50 Mg/2 [Nm3].
(h) In case of small boilers of capacity less
than 2 tons/hr and between 2 to 5 tons/hr the PM emissions shall be within 1600
and 1200 Mg/2 [Nm3].
(i) In case of integrated Iron and Steel
Plants, PM emission up to 400 Mg/2 [Nm3] shall be allowed
during oxygen lancing.
(j) In case of stone crushing units the
suspended PM contribution value at a distance of 40 metres from a controlled,
isolated as well as from a unit located in the cluster should be less than 600 2[micrograms/Nm3]. 3[***]
These units must also adopt
the following pollution control measures:-
(i) Dust containment cum suppression system for the equipment;
(ii) Construction of wind breaking walls;
(iii) Construction of the metalled roads within the premises;
1. Ins. by G.S.R. 80 (E), dated 31st
December, 1993 (w.e.f 31.12. 1993).
2. Subs. by G.S.R. 80 (E), dated 31st December,
1993 (w.e.f. 31.12.1993).
3. Omited by G.S.R. 80 (E), dated 31st
December, 1993 (w.e.f. 31.12.1993).
(iv) Regular cleaning and
Wetting of the ground within the premises;
(v) Growing of a green belt along the periphery,
(k) In case of Ceramic industry, form the
other sources of pollution, such as basic raw material and processing
operations, heat recovery dryers, mechanical finishing operation, all possible
preventive measures should be taken to control PM emissions as far as
practicable.
2. The total fluoride emissions in respect of Glass and
Phosphatic Fertilizers shall not exceed 5 mg/NM3 and 25 mg/NM3
respectively.
3. 1[In case of
copper, lead and zinc smelting, the off-gases may, as far as possible, be
utilized for manufacturing sulphuric acid.]
2[4. In case of cupolas (Foundries) having capacity (melting rate)
less than 3 tonne/hour, the particulate matter emission shall be within 450
mg/Nm3. In these cases it is
essential that stack is constructed over the cupola beyond the charging door
and the emissions are directed through the stack, which should be at least six
times the diameter of cupola. In
respect of are Furnaces and Induction Furnaces, provision has to be made for
collecting the fumes before discharging the emissions through the stack.]
1. Subs. by G.S.R. 80 (E), dated 31st
December, 1993 (w.e.f 31.12.1993).
2. Added by G.S.R. 80 (E), dated 31st
December, 1993 (w.e.f 31.12.1993).
3. Ins. by G.S.R. 176(E), dated 2nd April,
1996 (w.e.f 3.4.1996).
4[SCHEDULE VII]
[See Rule (3B)]
National
Ambient Air Quality Standards (NAAQS)
4. Ins. by G.S.R. 176(E), dated 2nd April,
1996 (w.e.f 3.4.1996 .
|
Pollutant |
Time
weighted Average |
Concentration
in Ambient Air |
|||
|
Industrial
Area |
Residential
Rural and other area |
Sensitive
Area |
Method
of measurement |
||
|
1 |
2 |
3 |
4 |
5 |
6 |
|
Sulphur
Dioxide (SO)
2 |
Annual
Average* 24
hours** |
80
ug/m3 120
ug/m3 |
60
ug/m3 80
ug/m3 |
15
ug/m3 30
ug/m3 |
-Improved
West
and Gaeke
method -
Ultraviolet Fluorescence |
|
Oxides
of nitrogen as No2 |
Annual Average* 24
hours** |
80
ug/m3 120
ug/m3 |
60
ug/m3 80
ug/m3 |
15
ug/m3 30
ug/m3 |
-
Jacab & Hochheiser
modefied (Na-Arsenite) Method -Gas
Phase Chemiluminescensce |
|
Suspended
pariculate Matter
(SPM) |
Annual
Average* 24
hours** |
360
ug/m3 500
ug/m3 |
140
ug/m3 200
ug/m3 |
70
ug/m3 100
ug/m3 |
-
High Volume Sampling -[Average
flow rate not less than 1.1 m3/minute] |
|
Respirable
particulate Matter (size less than 10 um) (RPM) |
Annual
Average* 24
hours** |
120
ug/m3 150
ug/m3 |
60
ug/m3 100
ug/m3 |
50
ug/m3 75
ug/m3 |
-Respirable
particulate matter sampler. |
|
Lead
(Pb) |
Annual
Average* 24
hours** |
1.0
ug/m3 1.5
ug/m3 |
0.75
ug/m3 1.00
ug/m3 |
0.50
ug/m3 0.75
ug/m3 |
-AAS
method after sampling using EMP
2000 or equivalent-filter paper. |
|
Carbon
Monoxide |
8
hours** 1
hours |
5.0
ug/m3 10.0
ug/m3 |
2.0
ug/m3 4.0
ug/m3 |
1.0
ug/m3 2.0
ug/m3 |
-Non
disbersive, infrared spectroscopy. |
* Annual Arithmatic mean of minimum 104
measurements in a year taken twice a week 24 hourly at uniform interval.
** 24 hourly/8 hourly values shall be met 98% of
the time in a year, 2% of the time, it may exceed but not on two consecutive
days.
Note.
-
1. National
Ambient Air Quality Standard: The levels of a air quality necessary with an adequate
margin of safety, to protect the public health, vegetation and property.
2. Whenever and wherever two
consecutive values exceeds die limit specified above for the respective
category, it shall be considered adquate, reason to institute regular/continuous
monitoring and furter investigations.].
APPENDIX A
(See Rule 7)
Notice of Intention to have Sample Analysed
To......................
Take notice that is intended
to have analysed the sample of*
..which has been taken today, the
.day
of
..19
from
(Name and designation of the person who takes the sample)
..
*Specify the place from where the sample is taken.
(Seal)
Date
..
(See Rule 8)
Memorandum to Government Analyst
From
.......................................
To
The Government Analyst
........................................
The portion of sample
described below is sent herewith for analysis (under rule 6 of the Environment
(Protection) Rules, 1986.
The portion of the sample
has been marked by me with the following mark:
Details of the portion of
samples taken.
Name and designation of
person who sends the sample.
(SEAL)
Date
..
(See Rule 8)
Report by Government Analyst
Report No
Date
.
I hereby certify that
I
.Government Analyst duly appointed under Section 13 of the Environment (Protection) Act, 1986,
received on the............... .................. day of
19
......................... ..................from.............................................................................................................
*
a sample
of
.or analysis.
The-sample was in a
condition fit for analysis as reported below.
I further certify that I
have analysed the afore-mentioned sample on
and declare that the result of
the analysis to be as follows:
**...........................................................................................................................
.................................................................................................................
The condition of seals,
fastening of samples on receipt was as follows:
Signed this
day of
..19
.
Address
Signature
(Government Analyst)
To
........................................
* Here write
the names of the officer/authority from whom the sample was obtained.
**Here write full details of analysis and method of
analysis
(See Rule 11)
Form of Notice
By registered
post-acknowledgement due
From
Shri..............................
..............................
To..........................
.............................
Notice under Section 19(b)
of the Environment (Protection) Act, 1986.
Whereas an offence under the
Environment (Protection) Act, 1986, has been committed/is being committed
by
(2) I/We hereby give notice of 60 days under Section 19 (b) of
Environment (Protection) Act, 1986, of my/our intention to file a complaint in
the Court against
.(3) for violation of section
..of the
Environment (Protection) Act, 1986.
In support of my/our notice,
I am/we are enclosing the following documents (3) as evidence of proof of
violation of the Environment (Protection) Act, 1986.
Place
.
Date
.
Signature (s)
Explanation:
(1) In case the notice is
given in the name of a company, documentary evidence authorising the person to
sign the notice on behalf of the company shall be enclosed to this notice.
Company for
this purpose means a company defined in the explanation to sub-rule (6) of rule
4.
(2) Here give the name and
address of the alleged offender. In
case of a manufacturing/processing/operating unit, indicate the
name/location/nature of activity, etc.
(3) Documentary evidence
shall include photographs/technical reports/health reports of the area, etc.,
for enabling enquiry into the alleged violation/ offence.
1[FORM V
(See Rule 14)
Environmental Statement for
the financial year ending the 31st March...........
PART - A
(i) Name and address of the
owner/occupier of the industry operation or process.
(ii) Industry category
Primary - (STC Code) Secondary- (STC Code).
(iii) Production
capacity-Units-
(iv) Year of establishment.
(v) Date of the last environmental statement
submitted.
PART
- B
Water and Raw Material
Consumption
(1) Water consumption m3/d
Process
Cooling
Domestic
|
Name of products |
Process water consumption per unit of product
output |
||
|
During the previous financial year |
During the current financial year |
||
|
(1) (2) (3) |
(1) |
(2) |
|
|
(2) Raw
material consumption |
|||
|
*Name of raw materials |
Name of products |
Consumption of raw material per unit |
|
|
During the previous financial year |
During the current financial year |
||
* Industry may use codes if
disclosing details of raw material would violate contractual obligations,
otherwise all industries have to name the raw materials used.
1. Subs. by G.S.R. 386(E), dated 22nd
April, 1993 (w.e.f.22.04.1993), previously inserted by G.S.R. 329(E) dated 13th
March, 1992 (w.e.f. 13.03.1992).
PART - C
Pollution discharged to environrnent/unit of output.
(Parameter as specified in the consent issued)
|
(1)
Pollution |
Quantity
of pollutants discharged (mass/day) |
Concentrations
of pollutants
in discharges (mass/ volume) |
Percentage
of variation from prescribed standards with reasons |
|
(a)
Water (b)
Air |
|
|
|
PART
- D
Hazardous Wastes
(as
specified under Hazardous Wastes (Management and
Handling) Rules,
1989)
|
Hazardous Wastes |
Total Quantity (Kg) |
|
|
During the previous financial year |
During the current financial year |
|
|
(a) From process (b) From pollution control facilities. |
||
PART - E
Solid Wastes
|
|
Total Quantity |
|
|
During the previous financial year |
During the current financial year |
|
|
(a) From
process (b) From
pollution control facility (c) (1)
Quantity recycled or re-utilised within the unit (2) Sold (3)
Disposed |
||
PART-F
Please specify the
characterisation (i n terms of composition and quantum) of hazardous as well as
solid wastes and indicate disposal practice adopted for both these categories
of wastes.
PART - G
Impact of the pollution
abatement measures taken on conservation of natural resources and on the cost
of production.
PART - H
Additional measures/investment
proposal for environmental protection abatement of pollution, prevention of
pollution.
PART - I
Any other particulars for
improving the quality of the environment.]