ENVIRONMENTAL
STANDARDS INCLUDING SCHEDULE FOR THEIR ENFORCEMENT
10.1
EMISSION STANDARDS/GUIDELINES NOTIFIED/REVISED Emission limits for New
Diesel Engines (upto 800 KW) for generator sets applications notied in Govt. of
India Gazette GSR 371(E), May 17, 2002 at Serial No. 95, was amended vide Gazette
Notification GSR 520(E), July 1, 2003. This amendment specified the emission limits
for different ratings and presented in Table 10.1. Table 10.1 Amended
Emission Limits for Different Ratings of Diesel Engines
| Capacity
of Diesel Engines | Date
of implementation | Emission
Limits (g/kw-hr)
for | Smoke
limit (light absorption coefficient, m-1) (at full load) |
Test Cycle |
| NOx |
HC |
CO |
PM |
Torque (%) |
Weighting factors |
| Upto
19 kw | 1.7.2004 |
9.2 |
1.3 |
3.5 |
0.3 |
0.7 |
100 |
0.05 | |
75 |
0.25 | |
>19kw upto 176 kw |
1.1.2004 |
9.2 |
1.3 |
5.0 |
0.5 |
0.7 |
50 |
0.30 | |
1.7.2004 |
9.2 |
1.3 |
3.5 |
0.3 |
0.7 |
25 |
0.30 | |
>176 kw upto 800 kw |
1.7.2004 |
9.2 |
1.3 |
3.5 |
0.3 |
0.7 |
10 |
0.10 | Noise
Limits The date of implementation of the noise limits for diesel generator
sets notified vide GSR 371 (E), May 17, 2002, viz 1.7.2003 was extended by one
year vide GSR 520, July 1, 2003 to 1.7.2004. The regulation requires mandatory
provision of acoustic enclosure, at the manufacturing stage, for all new generator
sets run on diesel (upto 1000 KVA), effective from July 1, 2004. The maximum permissible
sound pressure level for new generator sets (upto 1000 KVA) run on diesel according
to this new regulation shall be 75 dB(A) at 1 m from the enclosure surface. For
diesel generator providing an acoustic enclosure or acoustic treatment of the
DG room shall control sets, not covered by above noise from the DG set. Such acoustic
enclosures/acoustically treated rooms, shall be designed for minimum 25 dB(A)
insertion loss or for meeting the ambient noise standards, whichever is on the
higher side. Collection of Bank Guarantees and Affidavits
Bank
Guarantees and Affidavits from diesel engine/genset manufacturers were collected
as per the provisions of GSR 520(E), July 1, 2003 and GSR 92 (E), dated January
29, 2004. The bank guarantees and affidavits were required to be submitted by
the manufacturers and importers desiring to obtain the benefits of extension of
time by six months to one year, for emission limits of the diesel engines for
genset application. Compliance Procedure for Emission Limits for Generator
Sets Compliance procedure for emission limits for new diesel engines
(upto 800 KW) for genset applications has been finalised and circulated among
the certification agencies. 10.2 VEHICULAR POLLUTION CONTROL Vehicular
emissions are an important source of air pollution in urban centres of the country.
Therefore, controlling vehicular emissions remained a major thrust area during
the year. The focus was not only on the National Capital Region but has been on
the entire country. Use of clean fuels like CNG, LPG, biofuels etc, for vehicles
increased gradually. Following measures on vehicular pollution control were taken
and as a result improvement in air quality was observed at various urban areas.
Vehicular Emission Norms » From 1.4.2003 only Bharat
Stage-II emission norms compliant new vehicles, except 2 & 3 wheelers, were
registered in the cities of Hyderabad, Secunderabad, Bangalore, Ahemdabad, Kanpur,
Agra & Surat . »From 1.6.2003, Bharat (Trem) Stage-II emission
compliant new agriculture tractors and construction vehicles only were registered
throughout the country.
» Emission norms for diesel vehicles
fitted with LPG engine were made effective from 1-5-2003.
»
Bharat stage-II norms for 2- & 3-wheelers were notified during September 2003.
»
Draft emission norms for in-use vehicles effective from 1-10-2004 were notified
during July 2003.
» For implementation of Bharat Stage-II
emission norms to be effective from 1-3-2004 for all categories of vehicles in
Sholapur and Lucknow were also notified during December 2003 . Fuel Quality »
Fuel quality compatible with above emission norms were ensured in corresponding
cities. Alternate Fuel » Gasoline with 5 % ethanol
will be supplied in sugar producing States and Union Territories of Maharastra,
Andhra Pradesh, Goa, Gujarat, Haryana , Karnataka, Tamil Nadu, Uttar Pradesh,
Daman & Diu, Dadara & Nagar Haveli, Chandigarh & Pondicherry from
January 2003. » BioDiesel Specification has been finalized.
Some trial run on biodiesel has also been completed. » Use
of Gaseous fuel is increasing. There are 115 CNG stations in Delhi (Table 10.2),
57 CNG and 15 LPG stations in Mumbai, 5 LPG stations in Chennai, 7 LPG stations
in Hyderabad & 6 LPG stations in Bangalore. Action plan has been prepared
to increase the LPG filling stations in Chennai, Hyderabad and Bangalore. Table
10.2 CNG Stations and Consumption in Delhi
| CNG
vehicles Category | Year
2002 (as on 31.3.02) |
Year 2003
(as on 31.8.03) | | Bus
– DTC | 2120 |
2966 | |
Bus – Private |
2111 |
6889 | |
3 – wheelers |
35678 |
55101 | |
RTV |
2165 |
5146 | |
Taxi |
4816 |
5337 | |
Private Car |
10350 |
10481 | |
Total |
57240 |
85920 | |
CNG Consumption lakhs –kg/day |
3.5 |
7.01 | |
Nos. of CNG stations |
94 |
115 | Other
measures » In Delhi number of flyovers have been constructed
to ease traffic congestion and to reduce emissions from vehicles during idling
at traffic lights. Delhi metro railway line has been extended to Trinagar from
Tis- Hazari as Mass Transport Systems for catering more people. »
Interstate trucks which are not destined to Delhi are not allowed to ply within
city limits. Action Plan for Controlling Air Pollution »
Hon'ble Supreme Court directed Union of India and State Governments to prepare
action plans for reducing RSPM level for cities of Kanpur, Ahemdabad, Sholapur,
Bangalore, Lucknow, Chennai, Hyderabad, Mumbai and Kolkata. Hon'ble Supreme Court
also directed respective State Pollution Control Boards to place the proposed
action plans before EPCA (Environmental Pollution Control Authority).
»
The action plans for the above cities have been received. MoEF, CPCB & EPCA
are reviewing these action plans. Some of the actions proposed in the action plan
have already been initiated during year 2003. » Hon'ble Supreme
had identified nine critically polluted cities namely Kanpur, Lucknow, Varanasi,
Agra, Jharia, Patna, Jodhpur, Pune & Faridabad. The action plans for these
cities have been received and being reviewed. Some of the actions proposed in
the action plan have already been initiated during year 2003.
»
The Hon'ble court has also asked the State Pollution Control Boards to prepare
action plan and scheme for compulsory switch over to CNG/LPG as automotive fuels
in the cities those are equally or more polluted than Delhi. Later, CPCB identified
these cities as Ahemdabad, Kanpur, Kolkata & Pune. The action plans along
with scheme for compulsory switch over to CNG/LPG in these cities have been received
and reviewed by CPCB. Volatile Organic Compounds in Delhi & Mumbai
The project on "Inventory of emissions of Volatile organic compounds
(VOCs) in urban air of Delhi & Mumbai" is being conducted by CPCB through
National Environmental Engineering Research Institute (NEERI), Mumbai Zonal Office.
The objectives of the study are proposed to be achieved in two phase. Phase -I
comprises of identification and measurement of VOCs in ambient air, whereas phase-II
involves inventorisation of sources of VOCs in industrial estates. The study on
phase-I has been completed during year 2003. More than 50 VOC compounds have been
identified in Delhi & Mumbai. The results of source apportionment using CMB-8
reveals that in Mumbai the gasoline evaporative emissions are the dominant source
of VOCs , while in Delhi vehicular exhaust are the dominant sources. Evaporative
Emissions of Hydrocarbons from various sources A project on Inventory
of evaporative emissions of Hydrocarbons from various sources in Delhi, Kolkata,
Mumbai and Chennai has been taken up by CPCB. National Environmental Engineering
Research Institute , Mumbai Zonal Lab will conduct the study. The study has commenced
during January 2004. Vehicular Emissions Inventory & Source Apportionment
As per MOU between MoEF & US-EPA a study on vehicular emissions
inventory & source apportionment for the city of Pune have been planned. a.
International Vehicle Emission Model
Vehicle emission study was conducted
by USEPA and James Lent University of California River side during March 2003.
The study was designed to estimate the technology distribution of vehicles operating
in Pune, measuring driving pattern and estimating time and number of vehicle engine
start. b. Training cum Demonstration Project Training on air
pollution monitoring , source apportionment and emission inventory was being conducted
at Pune during September, 2003. SPCB's, CPCB, Research Institutes, Oil companies,
Automobile manufacturers, universities and Municipal Corporations have attended
the programme. Project on "Auto- Rickshaw LPG conversion Demonstration
in Bangalore & Kolkata" Environment Canada is implementing
Canada-India Environmental Institutional Strengthening Project with the Ministry
of Environment and Forests in India. CPCB is implementing Air Quality Sub-component
of the Project. The project on LPG Conversion of Autorickshaw has been initiated
as sub-component of the Air emissions and Monitoring & Control component which
includes transfer of Canadian technical expertise for conversion of autorickshaws
to LPG in Bagalore and Kolkata city. In order to supervise the activities of the
project , CPCB has constituted technical advisory committee under the chairmanship
of Dr. H.B Mathur. The autorickshaws required for testing in Canada has been shipped
to Environment Technology Centre, Canada, from India. Air quality Monitoring
and Source apportionment studies in metro cities The project is sponsored
by oil companies and will be executed by NEERI, Nagpur and ARAI, Pune. The selected
cities are Delhi, Kolkata, Mumbai, Chennai, Bangalore and Pune. CPCB is the member
of the technical and steering committee of this project and will be actively involved
in the study. Expert Committee to Evaluate Policy and Guidelines to Prevent,
Monitor and Control Fine Particulate Matter (FPM) in the Ambient Air An
expert committee to evaluate policy & guidelines to prevent , monitor and
control fine particulate matter (FPM) in the ambient air has been constituted
under the chairmanship of Prof.J.M.Dave. In accordance with the recommendations
of the expert committee four Sub-committees have been constituted on following
topics: · Prevention control & air quality standards of FPM. ·
Monitoring of FPM · Health effects of FPM. · Source apportionment
studies of FPM
The sub- committees have submitted draft reports which were
circulated to the members of the principal committee. Committees related
to vehicular pollution control in which CPCB has taken active participation ·
Working group on adulteration of petroleum products constituted by Bureau of Indian
Standards (BIS). · Environmental Pollution Control Authority for NCR
constituted by MoEF. · Standing committee on emissions constituted by
MoRTH. · Petroleum products sectional committee constituted by BIS. ·
The expert committee on Auto fuel Policy constituted by MoPNG. · Expert
committee to evaluate policy & guidelines to prevent, monitor and control
fine particulate (FPM) in the ambient air. National Report »
Report of the Expert Committee on Auto Fuel Policy was accepted by the Union cabinet
during October 2003. The road map for controlling vehicular pollution from all
categories of new vehicles is as follows. Apart from road map for new vehicles
, the road map for in-use vehicles has also been recommended (Table 10.3). Table
10.3 Road Map of in-use Vehicles as per Auto Fuel Policy
| Coverage |
Passenger Cars, light commercial
vehicles & heavy duty diesel vehicles |
Two/Three
wheelers | | Entire
Country | Bharat
stage-II- 1.4.2005. Euro
III equivalent- 1.4.2010. | Bharat
Stage II- 1.4.2005. Bharat
stage III Preferably from 1.4.2008 but not later than 1.4.2010. |
| 11
major cities (Delhi/NCR, Mumbai, Kolkata, Chennai, Bangalore, Hyderabad, Ahemdabad,
Pune, Surat, Kanpur and Agra | Bharat
stage-II- 1.4.2003. Euro
III equivalent- 1.4.2005. Euro
IV eqivalent-1.4.2010 | » Report of the
Expert Committee on Development of Bio-fuels was submitted during July 2003. The
committee recommended 5% bio-fuel blended diesel in the country by the year 2005
and 20% bio-fuel blended diesel by the year 2011-12. 10.3 INDUSTRIAL
EMISSION STANDARDS
Emission Standards, Siting Criteria and Good Practices
for Hot Mix Plants There are more than 1000 hot mix plants of different
categories operating in different parts of the country. Most of the plants are
of stationary and drum- continuous type. The rated production capacity varies
from 6-10 t/hr to 10-120 t/hr. The locations of these plants keep on changing.
Burning of fuel, feeding of aggregate, direct heating of bitumen create environmental
hazards especially `air pollution' due to dust and volatile organic compounds
such as BTX, PAH, PCB's and VOCs. Realizing the need to strike a balance
between environment and economic development, the Central Pollution Control Board,
with the help of Central Building Research Institute, Roorkee decided to prepare
Comprehensive Industry Document (COINDS) on hot mix Plants in an effort to minimize
the adverse environmental impacts by regulating emissions from these plants. Proposed
emission standards, siting criteria and good practices have been circulated to
manufacturers and other stakeholders for their comments and suggestions. Review
of Effluent Standards and Development of Emission Standards for Basic Organic
Chemicals Manufacturing Industry With respect to basic organic chemicals,
the effluent standards have been developed and there is a need to develop emission
standards and guidelines for hazardous waste management. It is also required to
review the effluent standards in view of change in BPT. Therefore, the Central
Board took up a study to review the existing effluent standards considering best
practicable technology including waste minimisation techniques; to develop emission
standards considering techno-economic feasibility within the domain of health
and environment and also to develop guidelines for hazardous waste management. Development
of Emission Standards for Wheat Processing and Flour Mills, Pulse Grinding and
Milling, Dry Rice Grinding and Rice Mills There are large number of
industrial units spread across the country engaged in pulse milling, dry rice
and besan grinding, wheat processing, flour mills and rice mills. These units
mostly use conventional production technologies and generate substantial pollution
of air, water, noise, etc. The objective of the study is the assessment
of problem of noise, emissions and effluents, best available cost-effective technology
to control pollution and to develop standards for noise, emissions and effluents
including storm water disposal for wheat flour mills, pulses making mills, dry
rice, pulses grinding mills and emission standards for rice mills. Study has been
completed based on which recommendations are drawn.
Development of
Environmental Standards, Stack Height Regulations and Good Practices for Producer
Gas Plants and Biomass Gasifiers Producer gas obtained by the process
of gasification, can be employed in thermal application or for mechanical/electrical
power generation. Like any other gaseous fuel, producer gas affords much better
control over power levels when compared to solid fuel. This also paves the way
for more efficient and cleaner operation. Producer gas plants generate various
pollutants and there are no pollution control norms for these plants presently.
During the gas manufacturing, tars are generated and discharged into the environment,
which are "non-aqueous" in nature. Coal tar is always co-mingled with
other lighter oils, which are also waste products from producer gas plants. There
are significant gaseous emissions containing certain volatile organic compounds
along with other gaseous pollutants such as CO, NOx and SO2. The producer
gas plants and biomass gasifiers are energy efficient and environment friendly,
but the local environmental benefits (such as reduction in particulate emission,
CO, SO2 and NOx) have not been studied. The Central Pollution Control Board therefore,
decided to study the environmental parameters systematically for producer gas
plants and biomass gasifiers and recommended techno-economically feasible environmental
standards following BATNEEC (best available technology not entailing excessive
costs) and strategies for better environmental conditions in association with
The Energy and Resources Institute (TERI), New Delhi. Emission Standards,
Stack Height Regulations and Siting Criteria for the Vertical Shaft Brick Kiln
(VSBK) The existing emission standards on brick kilns pertains to only
annular kilns (BTKs and high draft Kilns) and were made before VSBK emerged as
a potential technology for firing bricks in the country. With this background
it has been considered to formulate the emission standards, Stack height regulations
and Siting Criteria for Vertical Shaft Brick Kilns. Vertical Shaft Brick
Kiln (VSBK) is an energy efficient technology for firing clay bricks. It is particularly
suited to the needs of brick production in developing countries - which is small
scale and decentralized type i.e. clamps. Presently more than 30 VSBKs are in
operation in Madhya Pradesh, Maharashtra, Kerala, Orissa and Uttar Pradesh. Several
design modifications have been incorporated under the India Brick Project (IBP)
in the original Chinese VSBK design to improve its performance in energy, environment
and product quality aspects. The main advantages claimed for VSBK technology
are: · highest energy efficiency among all types of kilns; ·
lower emissions; · small area requirement; and · uniformity
in the quality of the fired bricks A study entitled "Development of
Emission Standards and Stack Height Regulation for Vertical Shaft Brick Kilns
vis-a-vis Pollution Control Measures" has been undertaken by Central Pollution
Control Board in co-operation with TERI, New Delhi. The study has been completed
and Draft Emission Standards, Guidelines and Siting Criteria have been evolved.
Recommendations for emission standards and stack height are presented in Table
10.4. Table 10.4 Recommended Emission Standards and Stack Height Regulations
for VSBK
|
S. No. |
Kiln Capacity |
Stack height in metres (From
ground level) | Particulate
Matter mg/Nm3 |
| 1. |
Less than 15,000 bricks per day (1-3
shafts) |
11.0 (Minimum 6.5 m from loading platform) |
250 | |
2. |
15,000 to 30,000 bricks per day (4-6
shafts) |
14.0 (Minimum 7.5 m from loading platform) |
250 | |
3. |
More than 30,000 bricks per day (7
shafts or more) |
16.0 (Minimum 8.5 m from loading platform) |
250 | Performance
Evaluation of Air Pollution Control System-Modification thereon and Review of
Emission Standards for Bull's Trench Brick Kilns India is the second
largest producer of bricks after China. Brick is the common building material
used in almost all parts of India. During the ninth five-year plan period, the
annual bricks demand has been estimated as 170 million. Brick making is a traditional
industry but has emerged as an important activity. There are around 150,000 kilns
engaged in brick production in the country. Brick making is energy intensive process,
with specific energy consumption varying from 1.2 to 1.75 MJ/kg of fired bricks
for BTKs and 1.5 to 3.0 MJ/kg for clamp kilns. Coal is the major fuel used for
firing bricks. It is estimated that brick industry consumes over 20 million tonnes
of coal annually. Some of the technological development in brick kilns firing,
such as fixed chimney kilns, high draught kilns and vertical shaft brick kilns
have resulted in reduction in pollution and increase in energy efficiency. The
Aligarh Muslim University (AMU), The Central Building Research Institute (CBRI),
Roorkee, The Punjab State Council for Science and Technology (PSCS&T), Chandigarh,
etc. have designed fixed chimney and air pollution control device(s) basically
to trap particulate matter from Bull Trench Kilns. Of late, apart from coal,
various fuels including vacuum residue/distillation cake of refinery, hazardous
organic wastes, rejected coal of coal-washries and agriculture residue are being
used as fuel at brick kiln industries. A Meeting of stakeholders, CPCB officials
and TERI has been held to decide the monitoring protocol. Questionnaire survey
has been prepared and circulated to all SPCBs and PCCs for collection of information.
10.4
COMPREHENSIVE INDUSTRY DOCUMENTS (COINDS) Comprehensive Industry
Document: Development of Emission Standards and Good Practices for Arc Furnaces
and Induction Furnaces in SSI sector The electric furnace plays an important
role in the recovery and recycling of waste iron resources. In areas where an
abundant supply of scrap and electric power are available, the proportion of steelmaking
via the electric furnace route is relatively high, because both energy consumption
and equipment investment are substantially smaller in the integrated route using
a BF and BOF process to produce steel from ore. Electric furnaces are classified
as arc furnaces or induction furnaces. The arc furnace is used far more extensively
for steelmaking, because its capacity is large and production efficiency is high.
In addition to melting, both oxidation refining and reduction refining are possible
in the arc furnace. The arc furnace is used for decarburization, dephosphorization,
and dehydrogenation, and the induction furnace for desulfurization and deoxidation.
The arc furnace is also capable of melting higher fraction of alloy scraps. With
the rapid industrialization, the consumption of steel continues to grow and as
a result scarp generation will also continue to increase. Increased scrap generation
in India and import from foreign countries means increased use of such furnaces,
which will require adequate emission control and collection methods. The
Project is undertaken in association with Punjab State Council for Science &
Technology (PSCS&T), Chandigarh with the objectives · To study
and characterize fumes and emissions from electric arc furnace, induction furnace
and inbuilt facilities (argon oxygen decarborizer, turning furnaces, pre-heater,
etc.),
· To study fugitive emissions during raw material handling,
additives handling and tilting of pot /crucible for molten metal testing or during
transferring,
· To study noise pollution, minimization of fugitive
emission and noise pollution, issues concerning generation, handling and disposal
of slag (solid waste), suitable cost effective modifications for better performance,
effluent handling for ETPs (i.e. provided for air pollution control system); and
· To evolve suitable environmental standards (emission, noise,
effluent and solid waste) and good practice for electric arc and induction furnaces
including inbuilt facilities. Comprehensive Industry Document
(COINDS) and Evolving Environmental Standards and Good Practices for Cashew Seed
Processing Industry. Cashew nut processing industry is one of the promising
sector producing valuable commodity exported to Gulf and European countries. The
industry is categorized as small-scale. There are about 300 units scattered in
Nagercoil district, Tamilnadu. The density of these industries is also high at
Cheerla and Palasa in Andhra Pradesh; Kollam, Pathanamthitta, Trivandrum districts
in Kerala and in Goa. Even though there is cashew seeds cultivation in these areas,
most of the production demand is met by importing cashew seeds from South Africa.
There are two commonly followed methods of Cashew nut processing, viz roasting
process and cooling process. In cooling process vegetable oil is extracted from
the shells of the seeds, which has market in paint industry. Due to limited market
demand for the oil, most of the industries are following roasting process. The
cashew seeds roasting process releases thick smoke from the roasting drum through
the stack. The smoke has irritating odour and source of public nuisance for the
neighbourhood. The process also discharges wastewater from the quenching operation
of the roasted seeds. The industries are mostly in small scale and cottage sector
with no conventional and techno-economically cost-effective pollution abatement
systems. Though pollution load from individual unit is relatively low, but the
magnitude of pollution problem from the cluster of units is substantial. The
environmental standards for cashew seed processing industry are yet to be developed.
The Central Pollution Control Board is developing 'Comprehensive Industry Document
on Cashewseed Processing Industry to evolve Environmental Standards and Cost Effective
Good Practices' with the active co-operation of AIP- NPC, Chennai. Comprehensive
Industry Document (COINDS) on Bullion industry Bullion refining is an
important industry from economic view point. Importance of this industry is very
well illustrated by the fact that India invests huge amounts in purchase of gold
and silver as the demand for these metals is increasing. The operations and process
involved in bullion refining industry are energy and water intensive, also generate
emissions, effluents and solid waste in the environment. Environmental standards
need to be developed to regulate these discharges. Also to suggest in-plant pollution
control & resource conservation measures and other alternative pollution control,
waste-handling measures including that of the treatment plants so as to meet the
discharge standards. Services of M/s ENC Consulting Engineers have been hired
to undertaken preparation of 'Comprehensive Industry Document for Bullion Industry'. Comprehensive
Industry Document on Electroplating Industry The study has been undertaken
to prepare a comprehensive industry document (COINDS) on electroplating industry.
The information such as number of industries, their location, environmental problems
and available pollution control technologies has been collected. The draft report
includes detailed information on Electroplating Industry, processes & chemicals
used, Environmental effects, In depth studies of 20 electroplating units, Recovery
of metals, waste minimization & best available technology option, review of
existing environmental standards comparison with environmental standards in other
countries and suggestions for revision of effluent & emission standards emission. Comprehensive
Industry Document (COINDS) on Stone Crushers Final report of the project
including proposed environmental standards, code of practice for pollution prevention
and the shifting criteria suggested in the report was placed before Peer &
Core Committee for consideration. The matter was discussed and was decided that
a sub-committee comprising Prof. J.M.Dave and Shri N.S.Tiwana may examine the
issue along with officials of CPCB, SPCB and consultants. Comprehensive
Industry Document (COINDS) on Soaps & Detergents Soaps and detergents
are extensively used household products, which are indispensable to health, hygiene
and cleanliness. So far, no industry specific emission / effluent standards have
been stipulated by CPCB for the soaps & detergents manufacturing industry.
It was decided to undertake the task of preparation of COINDS to provide necessary
information on the status of Soaps & detergents industry in the country. CPCB
entered into a 'Memorandum of Understanding' with Harcourt Butler Technological
Institute (HBTI), Kanpur for the preparation of the document, which will include
the minimal national standards and other relevant information needed for the prevention
of environmental pollution from this industrial sector. The studies are in progress. Comprehensive
Industry Document for Sugar Mills (Revised) The sugar industry is one
of the major agro-based industries. The number of sugar factories in operation
was around 139 in 1950-51 producing 11 lakh tonnes of sugar, while the total number
of sugar factories have rose to 525 and the sugar processed was around 186 lakh
tonnes. Though India ranks first in sugar production; per capita availability
of sugar is very low as compared to other sugar producing countries. The industry
has its base mostly in rural areas and playing important role in country's economy
in the rural sector. The farmers find that sugarcane crop is highly remunerative
and also robust which can sustain the natural calamities. Thus, it is very much
essential to protect the interests of this industry in all respects. It is very
important to address the industry and impress that the socio-economic and political
considerations cannot override the interests of rural economy. It is a general
belief that sugar industry consumes considerable amount of water and also generate
sizeable amount of liquid effluent. The suspended particulate matter (SPM) is
a cause of concern, as it is felt that cost effective Air Pollution Control (APC)
equipments are yet to be identified for bagasse fired boilers. With the realisation
of the importance of water conservation and waste minimization concepts and indigenously
developed APC equipment, the waste management and air emission control are now
well within the reach of the industry. The solid wastes such as press mud, agricultural
trash, fly-ash generated can be converted into useful bio-fertilisers to enrich
micro and macro-nutrients of soil and improved crop yields. The Central
Pollution Control Board published a comprehensive document on sugar industry in
1980-81 and the present efforts are to upgrade this document to incorporate various
aspects such as wastewater minimization & identification of appropriate technologies
for reduction in emissions. As per COINDS 1980-81, the industries have
been following Double Carbonation and Double Sulphitation (DCDS) process and the
conventional Double Sulphitation (DS) process. At present the DCDS process is
being discontinued except at two units (Mawana Sugars in Uttar Pradesh and Saraswati
Sugars in Haryana). It is reliably learnt that these industries may also switch
over to double sulphonation process. The sugar industry may be classified
broadly into three categories, capacity wise, as given below: · Small
: Crushing capacity upto 2500 TCD;
· Medium: Crushing capacity
greater than 2500 and upto 5000 TCD
· Large: Crushing capacity
greater than 5000TCD Recently many of the sugar units have installed co-generation
units based on bagasse and many more are in the process of establishing the co-generation
plants to ease the power crisis faced all over the country. The profitability
of the industry would considerably improve if the co-generation plants are established.
There can be another classification based on exportable power generation which
is as below. a. Co-generation sugar unit to export power
b. Conventional
sugar units Inplant Control Measures · It shall be made mandatory
to recirculate excess condensate, compressor cooling waters, sulphur burner cooling
water, mill bearing and turbine cooling waters. If necessary, mini cooling towers
may be installed to reduce temperature, to facilitate the recirculation and reuse
of these streams. These measures are to be incorporated by the plant suppliers
and also as the specifications of the plant machinery. · Mechanical
seals shall be used wherever applicable to avoid leakages from pump glands. ·
If the cleaning operation of the equipment is carried out continuously it would
help to reduce shock-loads on Effluent Treatment Plant. Wherever monthly cleaning
practice is followed at fixed intervals and the effluents are discharged directly
into Effluent Treatment Plants, the performance is affected due to shock loads.
Most of the industries are now constructing Washing Holding Tanks whereby, the
effluent from equipment cleanings, leakages and process upsets are stored and
pumped in controlled manner to Effluent Treatment Plants. In the industries,
where inplant control measures and water recycling techniques are followed, the
targets of water consumption & wastewater discharge of <100l/tonne of cane
crushed are already achieved. Water and waste Management ·
The water management practices are to be strengthened in most of the sugar units.
It is observed that water consumption varies between 400 to 1000 litre per tonne
of cane crushed (Table 10.5). Taking into account the availability of sixty percent
water in sugarcane, it is suggested that there should not be any water abstraction
from surface or ground. Spray ponds/cooling towers should be adopted for maximum
utilization of water. The quality of water at the upstream and downstream side
of the discharge point should be monitored for pH, Temperature, suspended solids,
BOD and dissolved oxygen etc. · The industry shall be advised to
measure water consumption on a rational basis. Most of the industries estimate
the water usage based on pump capacities and the number of hours of pumping. Most
of the industries are of the opinion that water meters do not work properly. In
such a case, the levels of reservoirs may be recorded and the water consumption
per day can be estimated by multiplying the level difference and area. The
usual method of measuring the effluent quantity is through "V" notch.
The mild steel "V" notch plates get corroded due to acidic nature of
effluent. The industry shall be advised to use Brass or Stainless steel plates
for "V" notch and calibrate every year during the off- season. It is
suggested to use continuous flow recorders. · The effluent quantity
varies between 100 litre to 400 litre per tonne of cane crushed. The norms for
effluent quantity may be fixed as 100 litre per tonne of cane crushed. ·
In case of domestic effluent treatment plant, two methods of treatment are suggested
as Root Zone treatment and the combined treatment for domestic and sugar factory
effluents. However, there can be a number of alternatives, which the industry
may like to choose. Air Pollution The industry is to be addressed
on the adoption of efficient Air Pollution Control measures such as Wet Scrubbers
and ESP (Electrostatic precipitators) systems. It is suggested to replace multicyclones
with wet scrubbers / ESP units; as the Multicyclones do not provide more than
40-50% efficiency. Many sugar units have started replacing multicyclones with
wet scrubbers. It is suggested to install ESP unit wherever a sugar unit has Co-generation
plant. A few industries have already taken this step and the performance of these
control measures have been found extremely good. Table 10.5 National
average for water requirement, raw material consumption and effluent generation
| Particulars | |
Small Plant <2500
TCD Crushing Capacity |
Medium Plant 2500-5000 TCD Crushing
Capacity | Large
Plant 5000-7500 TCD Crushing
Capacity | Suggested
norms irrespective of the capacity | |
Avg. |
SD |
Avg. |
SD |
Avg. |
SD | |
Water Requirement (Lit/MT) |
Process |
268 |
80 |
236 |
63 |
250 |
90 |
200 | |
Cooling |
147 |
150 |
161 |
71 |
130 |
70 |
100 | |
Domestic Cum/day) |
109 |
105 |
193 |
234 |
250 |
130 |
100 | |
Raw material consumption (Kg/quintal
of sugar produced) | Bagasse |
314 |
30 |
276 |
39 |
233 |
40 |
250 | |
Lubricants |
0.116 |
0.068 |
0.123 |
0.085 |
0.105 |
0.049 |
0.050 | |
Lime |
1.60 |
0.50 |
1.50 |
0.30 |
0.90 |
0.48 |
1.000 | |
Sulphur |
0.460 |
0.150 |
0.430 |
0.14 |
0.40 |
0.16 |
0.350 | |
Caustic soda |
0.053 |
0.029 |
0.027 |
0.015 |
0.024 |
0.012 |
0.015 | |
Coagulants |
0.0059 |
0.0082 |
0.0095 |
0.011 |
0.0048 |
0.0050 |
0.010 | |
HCL |
0.08 |
0.08 |
0.18 |
0.189 |
0.10 |
0.105 | |
| O.P.
Acid | 0.073 |
0.043 |
0.20 |
0.274 |
0.090 |
0.080 |
0.050 | |
Bye products Kg per tonne of cane
crushed | Bagasse |
313.46 |
11.41 |
291.22 |
44.56 |
300 |
30.0 |
260-300 | |
Molasses |
43.58 |
3.17 |
41.00 |
1.89 |
40.00 |
1.90 |
38-42 | |
Pressmud |
33.00 |
4.01 |
35.12 |
3.52 |
38.00 |
2.00 |
35-40 | |
Effluent generated |
(Lit/TCD) |
230 |
145 |
250 |
132 |
233 |
83 |
100 | |
Capital and recurring cost of ETP
in Rs/TCD | Capital
cost | 1236 |
620 |
1180 |
890 |
1000 |
333 |
3000-4000 | |
Recurring cost |
460 |
312 |
525 |
480 |
466 |
200 |
1200-1500 | |
Steam |
Kgs/T of cane crushed |
490.00 |
30.0 |
500.00 |
20.00 |
480 |
15.0 |
440-460 | |
Power |
Kw/MT cane crushed |
22.00 |
3.00 |
20.00 |
2.00 |
24 |
5.00 |
16-20 | Minimum
National Standards (as discussed in the 18th Peer & Core Committee meeting) Even
though some of the industries have mentioned that it is difficult to achieve the
existing Minimum National Standards (MINAS), the detailed study of some of the
industries reveal that it is not difficult to meet the standards. It is, therefore,
suggested to continue the existing MINAS for sugar industry for discharge on land
for irrigation as BOD<100 mg/l and S.S. <100 mg/l and BOD 30 mg/l and SS
30 mg/l for discharge into inland surface waters (Table 10.6). The industry shall
be addressed on proper design, operation and maintenance of effluent treatment
plants through training programmes and workshops. The permissible wastewater discharge
shall be 100 liters per tonne of cane crushed. The SPM of the stack emission shall
not exceed 150 mg/Nm3 irrespective of the type of furnace and shall be achieved
as per CREP decisions for sugar industries. Table 10.6 Suggested Minimal
National Standards for Sugar Industry
| S. No. |
Parameter |
Suggested Standards |
Remark | |
1. | B.O.D.
3 days 27oC, mg/l | ≯100 |
Disposal on land for irrigation |
| 2 |
B.O.D. 3 days 27oC,
mg/l | ≯30 |
Disposal into inland surface waters
(The standards may be made stringent depending on the dilution available in the
stream) | | 3. |
Suspended Solids, mg/l |
≯100 |
Disposal on land for irrigation |
| 4. |
Suspended Solids, mg/l |
≯30 |
Disposal into inland surface water |
| 5. |
Stack emissions, SPM, mg/Nm3 |
≯150 |
All natural draft boilers shall
be replaced by forced draft boilers with ECS. | 10.5
INDUSTRIAL POLLUTION CONTROL Performance Study of Tannery units situated
in and around Delhi About ten tanneries located at Delhi, Haryana and
Uttar Pradesh were studied with the objectives to improve their pollution control
performance. Some common problems were observed and the suitable remedial measures
were suggested. Some of the suggested measures are as follows: ·
Solid waste including chrome-bearing sludge to be stored properly in lined pits
with a shed over it to protect from rains.
· The algae growth in
the aeration tank indicates that aeration tank is not maintained and not been
put to use. MLSS level is to be maintained as per design.
· Acoustic
enclosures are to be provided for the DG set(s) for control of noise pollution,
as per Notification under the Environment (Protection) Rules, 1986.
·
Boron bearing salts are not to be used in the manufacturing process.
·
Dry desalter machine should be installed to reduce load on the solar evaporation
ponds.
· Sprinkler system for solar evaporation ponds to be provided
for effluent from soaking and pickling unit. Prevention and control of
pollution in tanneries in Kanpur Kanpur city has one of the biggest
tannery clusters in the country with as many as 354 tanneries (Fig 10.1), as a
result associated environmental problem have also been equally alarming. The pollution
of surface and groundwater has been observed to acquire serious proportions. The
high content of chromium in the tannery wastewater has been reported to render
the sludge from treatment plant, as highly hazardous substance.
 
Fig
10.1 Scale of Operation and type of Tanning in Tannery Units of Kanpur As
a result of regular surveillance by the Central Pollution Control Board and follow
up for enforcement the scenario has shown appreciable improvement. Some of the
salient achievements are as follows: v Feasibility study for Common Chrome
Recovery Plant v After a series of meetings with local authorities, Tannery
Association and other apex agencies a proposal for cost mobilization for the plant
prepared for Kanpur Nagar Nigam. The proposal is under active consideration of
Ministry of Environment and Forest, Govt of India v Identification of land
for the plant v The defaulting tanneries have been issued with closure orders v
Number of individual chrome recovery plant established by tanneries has increased
from 8 in 1996 to over 80 in 2004 (Fig 10.2). 
*As per the latest status, there are 80 individual plants already established
Fig
10.2 Individual Chrome Recovery Plants established over the years Latest
status of Common Chrome Recovery Plant at Kanpur · A formal proposal
has been submitted by KNN to NRCD with assured contribution of 15% of the capital
cost by KNN and 15% by tanners. The rest of the capital cost is being considered
by NRCD. . · Land for the proposed plant has been identified Problems
observed in tanneries at Kanpur · The primary treatment plant installed
at individual tanneries are generally not operated / operated improperly ·
Tannery conveyance system is choked at many places resulting into discharge of
untreated effluent into river Ganga · Lifting of solid waste and PETP
sludge is highly irregular resulting in a big nuisance in the area Proposed
Leather Technology Park, Banthar, Unnao In order to promote Export oriented
leather industries in U.P., a Leather Technology Park is being established at
Banthar, Unnao in U.P.. The proposal to establish was submitted by UPSIDC to MoEF
and after a detailed scrutiny, a five-member Sub-committee including by the Central
Pollution Control Board Officers, visited the project site on July 22, 2003 .
In order to stress environmentally sustainable leather tanning process, CPCB ensured
to include following issues as recommendation to be implemented by the project
authorities: a. Installation of separate flow meter and (intake) water
meter by tanneries
b. Automatic monitoring equipments by CETP / large tanneries
c.
Annual environmental auditing by all tanneries processing > 5 ton hide /day
d.
Resource recovery from process sludge / ETP sludge by generating bio-gas. This
option may be tried in-line with the re-use of fleshing from tanneries in "
Bio-methenisation" process. Since such option is under full-scale operation
in Tamilnadu with technical support of CLRI, it is recommended that techno-economical
feasibility of this option be worked-out in consultation with CLRI. In case the
option of " Bio-methanisation" is declared not-feasible, it is strongly
suggested that the option of using them in glue manufacture shall be avoided in
keeping with crude processing techniques and high potential of air pollution associated
with such industries.
e. Restricting wastewater generation from individual
tanneries to the tune of 28m3/tone hyde processed
f. Dispensing boron bearing
chemicals by tanneries / CETP Separation of Chromium from waste chrome
shavings to minimize disposal problems of hazardous solid wastes in tanneries It
is estimated that about 20,000 tonnes of chrome shavings are generated per annum
from tanning industry in the country. In this project, the technology for chromium
separation from the leather shavings has been developed. The study has been carried
out in collaboration with Central Leather Research Institute, Chennai. The important
findings of the study are as follows: » Concentration of the
chromium varies from 1.9-3.8% as Cr on dry solid basis.
»
Moisture content of the shavings and trimmings varies from 40-55% depending upon
the storage period.
» 80-90% removal of chromium from shavings
and trimmings with moisture content of about 50% was observed.
»
Increase in the percentage of chromium extraction was observed for wetting back
of the shavings and trimmings before detanning.
» Detanning
process duration time of one hour is sufficient for chrome bearing waste with
the moisture content of about 50%. More process duration time will be needed for
low moisture content waste.
» 500% float volume is sufficient
for effective detanning in drums for shavings and 800% float volume for effective
detanning in drums for trimmings. No enzyme or heating is involved in detanning.
»
Intermittent mixing of 10 minutes per hour is sufficient for detanning and extraction
for shavings. Continuous mixing is needed for trimmings. Lime at pH 12 is selected
as a detanning agent.
» One time washing is sufficient.
Washing is carried out in drum for a float volume of 500% for shavings and 800%
for trimmings for a duration time of 30 minutes.
» Filtering
of the shavings was done using a 2 mm sieve and filter bag.
»
Detanned liquor and wash water can be reused for the next cycle, which will minimize
quantity of the chemicals and process water. Formic acid at pH 3 is selected for
chromium extraction.
» Two times extraction is needed for
chrome shavings and three times extraction is needed for trimmings.
»
Pulping occurs immediately after the addition of acid only in the case of shaving.
Because of the pulping, the filtrate volume reduces and thereby reduces the percentage
chromium extracted. The manual filtration process also takes more time due to
clogging of the pores.
» Mechanical dewatering equipment
are necessary for effective separation of liquor and solid for commercial scale
operation.
» Drum with 12-15 rpm is sufficient for detanning
and extraction process. Sulphur Balance and Material Balance in Oil Refineries
In-depth study of four selected Oil Refineries located in western part
of the country was carried out in association with IIT Kanpur. These refineries
are - Reliance Industries Limited, Jamnagar; Indian Oil Corporation Limited, Vadodara;
Hindustan Petroleum Corporation Limited, Mumbai and Bharat Petroleum Corporation
Limited, Mumbai. Distribution of sulphur in different stages of crude refining
was studied and compared for all four refineries. The stack monitoring and wastewater
quality monitoring was also carried out at all the refineries. The study highlights
that sulphur content in products is only 29.7% at Reliance Industries Limited
(RIL), but the same is high in other refineries. At RIL only 0.56% of sulphur
contributed to the environment, but its concentration is quite high in other refineries.
The sulphur recovery is also very high at this refinery as compared to other refineries,
because of better technology and much larger sulphur recovery units. Study
of Dye Industries Located at Vatva Industrial Estate, Gujarat As a mandatory
requirement, 14 dye manufacturing units located at Vatva Industrial Estate had
applied to the Ministry of Environment and Forests, Government of India, for ex-post
facto environmental clearance during February 2002. While considering the proposal
for environmental clearance, the EIA Committee had visited these industries and
recommended suggestions to the Ministry of Environment & Forests. The committee
suggested that each unit should ensure reduction of COD to 400 mg/l at their ETP,
so that after treatment in the CETP, the COD remains well within the specified
environmental standard of 250 mg/l. Status of Pollution Control Measures
in Ceramics units in West Bengal The units namely ceramics are categorised
under the small scale sector and the entire manufacturing process is undertaken
in batches. The most important part of the manufacturing process is the kiln.
There are two types of kilns used in the process - the tunnel kiln and the rectangular
/ dome shaped kiln, the former being the conventional one. However, with improvement
in technology there is a gradual shift to the tunnel kiln for convenience, fuel
efficiency and 'green product' management. In West Bengal most of the kilns have
abandoned coal as the fuel. As of now the burners of the kilns use light diesel
oil (LDO) as the fuel. The emission norms are not stipulated for SOx except for
stack height. However, the stack monitoring results indicate that the emission
norms have been complied with respect to other parameters. Status of
Disaster Management Plan at Haldia, West Bengal There has always been
an anxiety of the safety measures taken particularly at isolated storage sites
of hazardous chemicals particularly fuels. The important statutes that cover these
critical areas issued under the Environment (Protection) Act 1986 are: ·
Chemical Accidents (Emergency Planning, Preparedness and responses) Rule 1996
· Manufacture, Storage and Import of Hazardous Chemicals (MSIHC)
Rules 1989
· Hazardous Wastes (Management & Handling) Rules
1989. Questionnaires were circulated to the three major oil companies located
in the Eastern region namely Indian Oil Corporation, IBP and Hindustan Petroleum
Corporation. It was observed that the major fuels stored are : superior kerosene
oil (KO), Motor spirit (MS), ultra low sulphur high speed diesel (ULSHDS), mineral
turpentine oil (MTO), aviation turbine fuel (ATF) and gases (like LPG, propane
and butane). In this context major fuel storage sites were visited including Haldia
in West Bengal. The plants have a detailed on-site emergency plan. In West Bengal,
Haldia has been developed as major industrial estate dealing predominantly with
hazardous chemicals. It was observed from the available reports that the District
Administrator prepares the calendar for mock drills particularly for each units
in the Haldia region. As per schedule, all the industries participate in the mock
drill along with the unit which is demonstrating its on-site safety precautions.
The outcome of these exercises is widely publicized. At Haldia, ships which anchor
at the jetties - the precautions for the pipelines emanating from the jetty areas
are also taken during movement of chemicals through pipes. At the bay stations
i.e. lorry (tank) fuel filling yards, the filling was automated leaving any scope
for manual handling. The effluent (if any) is being skimmed for oil before discharge
into the municipal drains. The units are participating in the eco-development
of regions in the vicinity and there are adequate provisions for the green belt. Status
of waste utilisation by industries
A project was initiated to identify
industries among the 17 categories of industries which used to generate such 'waste
/ wastes' having potential usage in other industries. To begin with, the following
industry categories (Table 10.7) have been considered, as the waste generated
from these categories not only have the potential to be used by other industries
but their quantity is also quite enormous creating 'waste management problems'.
Questionnaires have been circulated to ascertain the waste load and the potential
users. Table 10.7 Solid Waste Generated from Selected group of Industries
|
Industry category |
Major Waste(s) |
| Thermal
Power plants | Fly
ash / Bottom ash | | Steel |
Blast furnace & SMS slag |
| Sugar |
Press Mud | Solid
Waste Management at Slaughter House Waste management in slaughter houses
has special significance, because their wastes tend to form breeding ground for
pathogenic micro-organisms. Burning or burying of wastes lead to the total loss
of potential by-products. The waste processing and disposal has to be economical
and environmentally acceptable. With a view to suggest proper waste management
practices in slaughter houses, a study was undertaken. Recommendations on best
practicable methods currently available for processing and disposal of different
wastes and classes of slaughter houses have been identified and presented in Table
10.8. Incineration can also be used, which is one of the effective means for treatment
of many wastes. Table 10.8 Methods for processing, utilisation and disposal
of Solid Wastes from Slaughter House
| Type
of Waste | Constituents
of wastes | Category
of Slaughter House | Solid
Waste Diposal Method | |
Type
I | Vegetable
matter such as rumen, stomach and intestinal contents, dung, agriculture residues
etc. | Large (>
70 TLWK/d) | Biomethanation
| | Medium (15-70
TLWK/d) | Biomethanation
Or Composting |
| Small (<
15 TLWK/d) | Biomethanation
Or Composting |
| Type
II | Animal
matter such as inedible offals, tissues, meat trimmings, waste and condemned meat,
bones etc. | Large (>
70 TLWK/d) | Rendering
| | Medium (15-70
TLWK/d) | Rendering
Or Composting
with Type-I waste | | Small (<
15 TLWK/d) | Composting
with Type-I waste Or
Burial* |
*Should be considered as provisional measure.; TLWK/d- Tonnes of live
weight killed per day Environmental Guidelines for Control of Fugitive
Emissions during Cement Manufacturing During cement manufacturing, fugitive
emissions are generated at various stages. The degree of fugitive emission and
the type of controls adopted varies from industry to industry. A study on "Assessment
of fugitive emissions and development of environmental guidelines for control
of fugitive emissions from cement manufacturing units" has been undertaken
in association with National Productivity Council (NPC), New Delhi and IIT Kanpur.
The study includes identification of all fugitive emission sources, monitoring
and quantification of fugitive emissions, characterization of dust and analysis
of metals. Based on the study, the standards for fugitive emissions and environmental
guidelines to control fugitive emission will be finalized. There are a large
number of hazardous waste generating units located in 373 districts of 21 states
in the country. So far 11,138 units have been given authorization by State Pollution
Control Boards under Hazardous Waste (Management & Handling) Rules, 2003 mostly
for temporary storage of hazardous waste, within the plant premises. It is estimated
that about 4.43 million tonnes of hazardous waste is generated annually, out of
which 71,833 tonnes of hazardous waste are incinerable. The benefits of using
hazardous waste as a fuel in cement kiln are as ahead: · High temperature
and residence time of 4-5 seconds in an oxygen rich environment, ensure the destruction
of organic compounds found in the waste.
· Any acid gases formed
during combustion are neutralized by the raw material being alkaline in nature
and are incorporated into the cement clinker.
· Interaction of
the flue gases and the raw material present in the kiln ensures that the non-combustible
part of the residue is held back in the process and is incorporated into the clinker
in a practically irreversible manner.
· No waste is generated
that requires subsequent processing. There is the need to promote utilization
of hazardous combustible waste having higher calorific value in cement kiln as
fuel. This will not only solve the disposal problem associated with hazardous
waste but also conserve natural fuel resources. There is possibility of emissions
of toxic metals, volatile organic carbon compounds and other toxic gases, which
needs to be controlled. As a policy measure, several procedures and guidelines
for utilization of hazardous waste in cement kiln as fuel has been suggested.
Pollution
Control in Iron & Steel Sector Iron and steel is one of the largest
industrial sector in the country. Production of steel is the key factor denoting
development, but is also a major source of water, air and solid waste pollution.
Following major achievements have been made in the field of environmental management
and pollution control from the integrated iron and steel industries sector. ·
About 98% stacks are complying with emission standards;
· Ambient
air quality is within the statutory norms;
· Discharge effluent
quality for the plant/units are generally within effluent norms, except BOD plant
for the cyanide;
· 62.5% of the solid waste generated in steel
plants are being utilized either through recycling/reuse or commercial disposal;
and,
· Tree plantation has been undertaken in and around steel
plants with a target of plantation of one tree for the production of one tonne
of steel. The report on "Description of Clean Technology during steel
making in Integrated Iron & Steel Industry, Development of Environmental Standards
and Preparation of Comprehensive Document" has been prepared. National Environmental
Standards and clean technology developed for blast furnace and steel melting shop
is under finalization for their notification. Environmental Management
in Mining Sector Draft report on "Description of Clean Technology
for iron ore mining, development of Environmental Standards and Comprehensive
Industry Document" has been prepared. The Ministry of Environment & Forests,
Government of India, vide its notification on 7th May 1992 has restricted certain
activities in specified area of Aravalli Range. A document on "Study of Environmental
Problems of Aravalli Hills & Preparation of Action Plan for Restoration of
Environmental Quality (Gurgaon and Alwar Districts)" has been prepared. Based
on the data generated, the impact on environment due to the industrial activities
and mining will be assessed. The environmental impacts of cluster of the proposed
mines and processing units under the present environmental scenario will be addressed
separately. The Central Pollution Control Board has decided to include two other
districts of Rajasthan - Chittorgarh and Udaipur - within the purview of study.
Pollution Control in Copper Industry The copper industries
have agreed upon the following action points for protection of environment within
the specified time bound targets: · To meet the SO2 emission limits
by Dec, 2005
· Installation of continuous SO2 monitoring system
·
Proper operation and maintenance of tailing dams
· To achieve
zero discharge through 100% recycle/reuse of treated wastewater
·
To reduce fugitive emissions and overall housekeeping
· To develop
canopy based greenbelt around the periphery of manufacturing unit and township Pollution
Control in Zinc Industry The zinc industries have agreed upon the following
action points for protection of environment within the specified time bound targets: ·
To meet the SO2 emission limits by Dec, 2006
· Installation,
proper operation, maintenance and calibration of continuous SO2 monitoring system
·
Construction of secured landfill for disposal of hazardous waste such as jerosite
cake, ETP cake and spent catalyst as per CPCB guidelines
· To
achieve zero discharge through 100% recycle/reuse of the treated wastewater by
Dec, 2004
· To reduce the generation of fugitive dust from vehicle
movements and improve overall housekeeping
· To develop canopy
based greenbelt around the periphery of plant and township Pollution
Control in Aluminium Industry First meeting of the National Task Force
constituted for implementation of the CREP recommendations deliberated on following
important action points (Table 10.9): · Phase II Fluoride emission
limits for soderberg process as agreed in CREP shall be finalised after Phase
I is implemented
· More information on fluoride needs to be collected
before environmental standards are finalised · Pot life of 2000 days
for Soderberg technology was felt more practical and the same was recommended
Table
10.9 Action Points and Targets for Aluminium Industry
| Issues |
Action Points |
Targets |
| Technology |
Allowing new Potlines only with
pre-baked technology | Environmental
clearance for new Potlines to be given by MoEF after June, 2003, only with pre-baked
technology | | Fluoride
Emissions | Prescribing
maximum size of the Plant Revision
of fluoride emission standards Phasing
out wet scrubbing system for fluoride Allowing
Potlines only with Dry Scrubbing system Monitoring
of Fugitive emissions from pot rooms |
Maximum size of the plant shall
be decided based on the assimilative capacity of each plant location For
Soderberg – 2.8
kg/t by Dec 2005, 1.1 kg/t (VSS) & 1.30 kg/t (HSS) by Dec 2010 For
Pre-baked technology – 0.8
kg/t by
December 2006 Environmental
clearance for new potlines shall be given by MoEF, after June 2003, only with
Dry Scrubbing System To
start with Indal or any other better method and submit data from January 2004,
regularly to SPCBs and CPCB | |
Fluoride Consumption |
Fluoride consumption per tonne
of aluminium produced (as F) | For
Soderberg – 15
kg/t by Dec 2005 For
Pre-baked – 10
kg/t by Dec 2005 | | Ambient
Fluoride | Forage
fluoride standards Measurement
of forage fluoride |
- 12 consecutive months
average – 40 ppm
- 2
consecutive months average – 60 ppm
- 1
month – 80 ppm
To
start monitoring and submit data from January 2004, regularly to SPCBs and CPCB.
The locations of monitoring may be selected in collaboration with SPCBs and CPCB |
| Spent
Pot Lining | Setting
up a centralized SPL treatment & disposal facility with aluminium fluoride
recovery and utilization of SPL in steel/cement industries Limit
for Pot life SPL
(Carbon & Refractory) to be disposed in secured landfill |
Discussed in the NTF meeting individual
industries have already gone ahead with in-site treatment of SPL The
NTF suggested 2500 days coverage/for pre-baked pots installed after December 31,
2003 and 2000 days for Soderberg pots installed after December 31, 2006 With
immediate effect | | Red
Mud | Phasing
out wet disposal Red
Mud Utilization | To
achieve minimum 50% solids in red mud by Dec, 2005 A
proposal for practical utilization to be prepared by Aluminium Association of
India within 6 months | | Anode
Baking Oven | Achieving
particulate matter limit of 50 mg/Nm3 |
By December, 2005 |
Pollution Control in Thermal Power Plants There are 83
coal-based thermal power plants in the country, of which 5 thermal power plants
are closed. A total number of 56 Thermal Power plants with the prescribed emission
standards while 22 thermal power plants are yet to comply with the emission standards.
As many as 63 plants comply with effluent standards while 15 plants are not complying
in this regard. A Task Force (TF) for implementation of recommendations
of the Charter on Corporate Responsibility for Environment Protection (CREP) in
thermal power plants was constituted. The Task Force met twice in the year and
reviewed the status of non-compliant power plants. The Task Force decided that
non-compliant thermal power plants shall prepare an action plan for installation/augmentation
of pollution control systems in time-bound manner as per recommendations of CREP.
The sub-committees comprising representatives from CPCB, SPCBs, MoEF and CEA,
in the non-compliant power plants located in West Bengal, Jharkhand, Uttar Pradesh
and Haryana conducted inspections. Emphasis was given on Bank Guarantee from all
non-compliant plants, i.e. 10% of the cost of pollution equipment. Study
on the development of standards for trace toxic metals has been completed and
proposed standards will be placed in the meeting of Peer & Core Group. The
study on "Leachability assessment of trace heavy metals from ash ponds to
groundwater" is undertaken with association of IIT Kanpur. Field investigations
have been completed and findings of the study will suggest extent of leaching
of trace metals from ash ponds and its impact on groundwater quality. Guidelines
for prevention and control of leaching of trace metals including better ash pond
management practices will also be prepared. The study on "Cost benefit
analysis including environmental benefits of recycling of ash pond effluents in
thermal power plants" was undertaken with association of IIT Kanpur. The
findings of the study will suggest feasibility of recycling of ash pond effluent
and its benefits in water conservation and mitigating environmental problems.
Guidelines for better ash pond water recycling systems will also be prepared. Use
of Beneficiated Coal It has been suggested that the Ministry of Environment
& Forests should consider an amendment in the notification for effective implementation
of directives related to use of beneficiated coal. The Ministry of Power
has set up two different committees to look into ways and means for meeting the
requirement of beneficiated coal as per the notification. The latest committee
under Adviser (Energy) with members from CEA, Ministry of Coal, CIL, BSES, BHEL,
MSEB, APGENCO is deliberating on the installation of coal washeries as long term
solution to meet the stipulations. Beneficiated/blended coal is supplied to 17
thermal power plants, however other 14 plants have not yet indicated their plan
for meeting the requirement of use of beneficiated coal. Utilization
of Flyash There are 108 power plants including 78 plants of utilities.
About 242 million tones of coal and 20 million tones of lignite were consumed
in these plants, as a result 92 million tones of ash is generated and only 25
percent is utilized. Indian Road Congress has issued directives to all agencies
on 31st July, 2003 for use of flyash in road construction. CPWD is yet to introduce
the flyash use in RCC, in road construction and related activities. With respect
to backfilling of ash in abandoned mines, 169 mines are available for backfilling.
To give further impetus in flyash utilization, following recommendations were
made: · SPCBs should ensure implementation of the provisions of the
notification
· Thermal Power Plants should market the flyash and
should have separate division
· Only service charge for facilitating
the handling of flyash may be levied by the thermal power plants
·
Thermal power plants should not encourage third parties/agencies for supply of
flyash
· EIA studies should be must for Highway construction
·
Ministry of coal should give subsidy for disposal of ash into the mines Development
of Technologies for Pollution Control from Selected Drugs Manufacturing Units
- Paracetamol: A Case Study Paracetamol is an important drug manufactured
in India and is being used as an analgesic and antipyretic drug in a number of
drug formulations. Its production is reserved for small-scale sector in India
and present production capacity is estimated as 17,000 tonnes per year. The
Central Pollution Control Board took up a study with the association of the National
Chemical Laboratory, Pune and in-depth studies are under way to arrive at affordable
cleaner options for production of paracetamol bulk-drug. Determination
of Optimum Water Consumption Limit for the Bulk Drug Manufacturing Industry A
study has been taken up by the Central Pollution Control Board to review the existing
patterns of water use by the bulk drug industry, options for optimisation and
to arrive at optimum water consumption limit. Based on this study, optimum water
consumption limit for selected 84 drugs has been arrived, which are being further
reviewed to explore the feasibility to have common value. Risk Assessment
in Oil Refineries and Petrochemical Complexes Safety, health and environment
protection are the key concerns for the oil refineries and petrochemical industries.
The Central Pollution Control Board took up a project to study some oil refineries
and petrochemical complexes in detail and to establish and train the regulatory
officers on the procedures and techniques for carrying out risk assessment in
these industries. Status of pollution control in sponge iron industries
in Chhattisgarh Sponge iron plants have installed capacity of 2.5 MTPA
in Chhattisgarh. 60 kilns were in operation and may touch 100 in coming years.
Concentrated in Raigarh, Bilaspur and Raipur Districts, these units generate large
scale air pollution and huge quantities of solid wastes. Development of standards
for sponge iron plants is in progress. Sponge iron is a metallic product
formed by the reduction of iron ore at temperature just below the fusion point
of iron. This product has derived the name sponge iron due to its porous nature.
It is also called as Direct Reduced Iron (DRI). Sponge iron has now succeeded
in becoming a preferred raw material in secondary steel making. It is a substitute
of steel scrap for the secondary route of Direct Reduction / Electric Furnace
(DR/EF). The main raw materials required are iron ore, coal and dolomite.
The iron ore used is hematite with an iron content of 60-66%. The consumption
of iron ore has decreased from about 1600 kg. per tonne of sponge iron to 1500
kg levels mainly due to a better understanding of the process, improvements of
the equipment and increased levels of automation. In the initial days, the size
of iron ore was kept at 5-20 mm and washed in a scrubber before fed into the kiln.
But presently, it has become a standard norm to use 5-18 mm ore as feed without
scrubbing or washing. This has resulted in reducing the cost of iron ore fed to
the kiln. Non-coking coal is used having certain important parameters considered
as necessary for the direct reduction of iron ore viz. reactivity ash softening
temperature, caking and swelling indices and sulphur content, etc. Initially,
only 'B' grade coal was consumed. The industry has successfully adopted measures
to utilize 'C' & 'D' grade coal through better process control, shale picking
belts and coal washing plants. With these measures, the coal cost has come down
by nearly 20-30%, when compared to the 'B' grade coal. Dolomite is mainly
used as a desulphurising agent to prevent the pick up of sulphur by the sponge
iron from the sulphur released by the burning of coal inside the kiln. The 4-8
mm size dolomite is being used in place of the earlier 1-4 mm size. The loss of
dolomite fines to waste gases has been reduced by 50% after the increase in size
to 4-8 mm. In the inclined rotary kiln, iron ore and coal are passed through
in a counter current direction to the oxidizing flue gases. Fine coal is injected
from the material end for uniform combustion. The temperature in the range of
900 to 1050o C is maintained in the kiln. Air fans are mounted on the kiln to
force air inside the kiln to react with the carbon from the coal to form carbon
monoxide. After material heating, ore reduction and carbon gasification take place
in close association with each other. The volatile constituents of coal and carbon
monoxide are burnt over the entire length of the kiln with a controlled amount
of air. The metallisation process completes in the kiln and the discharge is cooled
indirectly with water in a rotary cooler connected to the kiln, screened and subjected
to the magnetic separation in order to remove the non-magnetics from the sponge
iron. In coal based sponge iron plants, depending on the quality of the
coal used, about 60% of the total heat input is utilised in the reduction process.
About 40% of the heat input is discharged with the kiln waste gases. The hot waste
gas and the char produced thus contain considerable energy potential. The waste
gas heat recovery boilers have become norm in the industry, as the cost of power
generation is equal to the hydel power generation cost. The sponge iron
industry in Chhattisgarh is growing in unplanned hapazard manner, as it is seen
as a quick money minting business proposition today. The liberal institutional
financial support coupled with the low-cost technology has encouraged many people
to establish a unit. A standard sponge iron unit may start with a kiln of 100
TPD. The normal kilns have capacities of 100, 300 and 500 TPD. Some units have
installed 50 TPD and even 25 TPD kilns, which operate intermittently. The local
fabricators and suppliers have modified the kiln, cooler and auxiliary equipment
to produce 200 and 400 TPD capacities also. Due to mushroom growth in sponge
iron industry, the important aspect of pollution control has been neglected altogether.
Many units have not even applied for consents from State Board. Some have started
production without even obtaining required licenses from various departments.
If not properly planned at design stage, the sponge iron industry is a highly
polluting industry in nature. Huge quantities of gases containing dust concentrations
of more than 50 gm/Nm3 will be released into the atmosphere. The coal and iron
ore crushers were being operated without any control equipment. There is also
very high number of fugitive emission sources in the plant area. The cooling water
could get easily contaminated with the dust and fines in the plant. The solid
waste materials generated in the form of char, dolchar, iron ore fines, coal fines
and dust require careful and expert handling because of their quantities and size.
After thorough study of these units the observations are as follows: Most
of the new units are coming up in Raigarh, Bilaspur and Raipur Districts. The
best quality of iron ore mines are located in Orissa State and the coal in required
quantities is available from Korba/Raigarh Districts in the State. A standard
sponge iron unit may start with a kiln capacity of 100 TPD. Readily available
kilns normally have the capacities of 100, 300 & 500 TPD. The local fabricators
and suppliers have modified the kiln, cooler and auxiliary equipment to produce
200 & 400 TPD capacities also. Some small-scale units have installed 50 TPD
and even 25 TPD kilns, which operate intermittently. It is expected that the total
units may go up to 100 kilns from the present estimate of 60 operating kilns of
various sizes. The industrial units are operated with one or two technical
persons knowing metallurgical process in sponge iron. The person is made responsible
for all aspects of the production, including pollution generated from the process.
In view of the limited knowledge and time, the technical persons are unable to
work for pollution control. The monitoring of ambient air quality and stack emissions
has been entrusted to the local consultants. The necessary documents including
consents and data records are also maintained by the consultants on behalf of
the industries. Sponge iron industry is a highly polluting industry in
nature. Huge quantities of gases containing dust concentrations of more than 50
gm/Nm3 will be released from the kiln. At a time when Pollution Control Boards
have been advocating and promoting cleaner technology, adoption of such dirty
technology of production is a matter of concern. Pollution control measures
taken by most of the sponge iron plants are far from satisfactory. The status
of pollution control in small units with production capacity below 30,000 TPA
is further bad. Installation of Waste Heat Recovery Boiler (WHRB) and power
generation in the units with 100 TPD and above capacity may be made compulsory.
CECB may take extra efforts to ensure compliance of consent conditions
in the existing plants. No industry should be allowed to operate without pollution
control devices. Industries operating without control devices may be closed immediately.
It is observed that many of the existing sponge iron producing industries
have expanded and increased their production without obtaining necessary approvals.
SPCB have to exercise strict vigil to ensure that such plants should not come
up without proper and adequate pollution control systems. Mercury emission
from Caustic Soda Industries The Alkali Manufacturers Association of
India (AMAI) has provided technical inputs to all the caustic soda manufacturing
units for accounting mercury consumption/loss. The Association has also provided
general mercury calculations for all the industries irrespective of the plant
condition and processes adopted by them. For example, handling loss is assumed
as 2% of mercury consumed. In spite of several recommendations, none of the units
have actually started measuring mercury escaping into the environment. It
was observed that during cell cut outs and power failures, huge quantities of
mercury were reaching in brine mud which is disposed in the landfill sites. All
the units have provided calculation on the basis of 10 power failures, without
stating the actual duration of power failure in hours. Similarly, while disposing
the exposed activated carbon, FUNDABAC filters, residues from distillation units
etc. were not measured for actual concentration of mercury in them before their
disposal. The emission, ambient air quality, surface and groundwater quality
and sediments of effluent receiving water bodies were not monitored on regular
basis by the industries. In the absence of reliable database, it is not possible
to conclude with one short-term study, the actual mercury release into the environment. Among
the action points of CREP, the installation of continuous online mercury analyzer
has been differed by all the units as they claimed that mercury bearing effluents
are being 100% recycled after treatment. The Association has informed the National
Task Force for Caustic Soda industry that the actual consumption of mercury for
the year 2002-2003 had already been brought down to 78 gm/tonne and the target
set in CREP, 50 gm/tonne will be achieved by December, 2005. Bio -Composting
in Distilleries Treatment of distillery effluent has always been a problem
for industry. Spent wash generated from distillation process has very high pollution
potential and it is detrimental to the recipient environment to which it is discharged.
Typical characteristics of spent wash is presented in Table 10.10. Table
10.10 Typical Characteristics of Spent Wash
| Parameter |
Batch Process |
Continuous process |
| PH |
3.7- 4.5 |
4.0-4.3 | |
BOD |
45000 |
50000 | |
COD |
100000 |
130000 | |
Inorganic dissolve solids |
30000 |
35000 | (All
values are in mg/l , except pH) So far distilleries has adopted various
treatment options to treat the distillery effluent but none of them is adequate
enough to meet the stipulated norms of discharge within affordable economical
range of the industry. Bio - composting of press mud with distillery effluent
is one option through which distillery can achieve zero discharge and get valuable
bio compost. Composting process is carried out by mixing distillery effluent with
press mud to make compost. Thus liquid effluent is converted into solid compost,
which is easier to transport for wider area use. Filler material is arranged in
wind rows and composted with effluent .Some time microbial starter culture is
used to expedite the composting. The quantity of effluent employed is controlled
to maintain optimum moisture in the windrows suitable for composting but not to
soak the filler material and leak out of composting heaps. Temperature and moisture
content are rigidly controlled and enough air is provided for composting reactions.
Exothermic humification reaction accelerated by microbial culture completely decomposes
all organic matter of effluent. A distinctive black loamy, free flowing and baggable
bio-compost is produced. CPCB has developed guidelines for bio composting.
Distilleries are now adopting this technology in order to reduce the effluent
discharge and in due course of time they are supposed to be zero discharge industry.
Information regarding bio composting from the units of UP were collected and some
distilleries were inspected to assess the efficacy of bio composting. Bio composting
scenario in some of the industries are summarized in Table 10.11. Table
10.11 Status of Bio-composting in some industries
| Name
of Industry | Area
of compost Yard | Technology |
Cycle Days |
Storage facility for Effluent |
Quantity of Press mud being used
for one cycle | Arrangements
for rainy season | | M/s
Balrampur Chini Mill (Distillery Division) |
20 Acre (Being
expanded to 47 acre) | Self |
60 |
52969 m3 |
16650 MT |
Bio compost is covered with polythene
sheets | | M/s
K.M Sugar, Masodha | 12
Acre | Trio
chem | 45 |
10000 m3 |
250 |
No arrangement |
| M/s
IGL Kashipur | 4
acre | M/s
Trio chem | 60
days | 7.13
lac m3 | | |
| M/s
National Industrial Corporaton, Moradabad |
18 acre |
IBF Envirotech |
60 days |
No separate arrangement |
2500 MT |
No arrangements |
| M/s
Somaiya Organics, Gorakhpur | 5
acre | Alfa
Lavel | 45
days | Storage
facility for 3 months in lagoons | 3900
MT | Bio
compost is covered with polethene sheet | |
M/s Daurala Sugar works |
3 acre |
In house |
60 days |
1000 m3 storage pit
at ETP | 3300
MT | Finished
product stored in godown. Wind rows are covered | |
M/s Bajaj Hidustan Ltd |
14 acre |
Trio Chem |
45 days |
LDPE and brick lined Lagoons |
5500 MT |
Storage shed | |
M/s Dhampur Sugar Mills |
12 acre |
IBF Enviro pune |
60 days |
6-7 days storage |
1500 MT |
No processing of bio compost |
| M/s
Rampur Distillery | 12
Acre | |
45 days |
Storage for 2.75 lac m3 |
300 MT |
No arrangements |
Limitations of bio composting · Press mud availability
is limiting factor.
· Less demand for bio compost. Efforts should
be made for promotion of use of bio fertilizers.
· Availability
of land as the process needs vast land.
· During rainy season
it is very difficult to run the bio compost plant, for that period only option
left is to store the effluent or shutdown the plant. Chances of ground water
pollution is always there if bio composting is done on unlined or poorly prepared
surface. Silk Screen Printing Dyeing and Printing of textiles
are made to convert the raw textile fibres into finished goods having better appearance.
Printing is a process of decorating textile fabrics by application of pigments,
dyes or other related materials in the form of patterns. Screen-printing may be
a hand operation or an automatic mechanical process. The major unit operations
in Screen-Printing are: Image Preparation, Stencil (Printing screen) Preparation,
Printing, Drying and Finishing. Colour in the effluents is the main problem alongwith
the Organic Matters. Serampore, District of Hooghly, West Bengal is famous
for Silk Screen-Printing Units and reportedly about 100 Units of various sizes
are operating and as all the Units are directly discharging their raw effluent
into Sewer or Municipal/Panchayet Drain, the condition of the drains have become
worsened primarily and due to colour of the waste aesthetically objectionable
secondarily. The main problem in these types of Unit is that their discharge is
not continuous and often intermittent depending on the number and time of washings.
It was observed and reported that about 40 Units are having capacities
to print 100 or more clothes per day. 50 Units having capabilities to print 50-60
clothes per day and about 60 -70 very small units printing only 20 - 30 clothes
per day. The process adopted in all the Units of Serampore are more or less same,
only variation is in the Capacity or Quantity being produced per day. The
salient findings are as follows · Colour solution for dying and printing
purposes are prepared by mixing following constituents Dry Colour - 300
Gm Gum - 400 Gm Water - 8 litre · The dye used is primarily
of Acid Colour (Azo free, Non Benzodine) type. The dyes of Ciba, Clariant, IDI,
Nerolac are being frequently used. The Local made dyes are also in use have been
reported by the Units. · The dye/colour is used in two processes:
for Dyeing the clothes; requirement varying in the range of 5-15 gms per cloth
depending on Shade (Light, Dark etc.) whereas for Printing purposes, the requirement
is more or less uniform and varies between 15 -20 gms per cloth. ·
In general, it was observed that water requirement for washing is in the range
of 10 -15 litre per Unit cloth. · Only 3 Units have installed Effluent
Treatment Plant (ETP) which rest Units are directly discharging their polluted
coloured effluent to nearby Municipal / Panchayet/ Low lying lands. Only 4 units
have changed their Boiler to Oil Fired till date · From the analytical
results, it is evident that the Chemical Oxygen Demand (COD) of the wastewater
is in general 2-5 times the Biochemical Oxygen Demand (BOD). However, in some
cases the COD/BOD ratio of the effluent was found as high as 21 and even 50. The
very low BOD in comparison to the COD (high COD/BOD ratio) with some cases might
be due to the presence of higher non-biodegradable organic matters or presence
of some other substances, which interfere, in the analytical results. However,
the exact reason behind it, is yet to be established by investigation and analysis
of various components. The heavy metal concentration in the effluent and
the corresponding discharge standards are presented in Table 10.12. Table
10.12 Heavy Metal concentrations in Effluent and discharge Standards
| Heavy
Metal | Observed
Conentration Range mg/l |
Discharge Standard mg/l |
| Lead
(Pb) | BDL
- 0.49 | 0.1 |
| Zinc
(Zn) | 0.03
- 147 | 5.0 |
| Copper
(Cu) | 0.004
- 1.65 | 3.0 |
| Nickel
(Ni) | BDL
- 0.01 | 3.0 |
| Cadmium
(Cd) | BDL |
2.0 | |
Arsenic (As) |
BDL - 0.003 |
0.2 | |
Chromium (Cr+6) |
BDL |
0.1 | |
Total Chromium (T-Cr) |
BDL - 6.5 |
2.0 | It
is evident that the effluent of the Silk Screen Printing are gross violators in
terms of discharge of various metals such as Lead, Zinc and Chromium. The Metal
concentration in the Dyes frequently used for Screen Printing are presented in
Table 10.13. Table 10.13 Heavy Metal concentrations in frequently used
Dyes |
Dyes |
Metal Concentration in mg / Kg
(Dry Weight) | | Pb |
Cd |
Cu |
Zn |
Ni |
As |
Cr | |
Blue BN |
BDL |
BDL |
3.5 |
291 |
BDL |
0.7 |
980 | |
Blue AS |
BDL |
BDL |
2.33 |
194 |
BDL |
0.61 |
BDL | |
Brown 2RL |
BDL |
BDL |
9.6 |
154 |
0.6 |
1 |
4809 | |
Black WA |
BDL |
BDL |
2.5 |
2.0 |
0.3 |
0.4 |
7849 | |
Yellow 5GN |
BDL |
BDL |
2.7 |
247 |
2.6 |
1.4 |
44.5 | |
Red RS |
BDL |
BDL |
1.75 |
152 |
2.8 |
0.36 |
BDL | |
Violet 4B |
BDL |
BDL |
2.54 |
277 |
3.6 |
BDL |
241 | |
Golden |
BDL |
BDL |
7.56 |
11.27 |
0.59 |
0.64 |
BDL | |
Royal Blue |
BDL |
BDL |
4.57 |
155.42 |
2.46 |
0.77 |
1401.73 | Pollution
Control at Large and Small Pulp & Paper Industries Central Pollution
Control Board published comprehensive industry document for large pulp & paper
industries and small scale pulp & paper industry during the year 1991 and
1986 respectively. These reports were comprehensive and findings were based on
in-depth studies carried out in selected pulp & paper mills using diversified
raw materials, pulping processes, different waste treatment systems. Based on
the findings in these reports, environmental standards for discharge of effluent
and emissions were notified. The scenario of pulp & paper industry
has been under considerable change since then with respect to process technology,
raw material and environmental technology. Looking into the changed scenario,
increased environmental awareness, choice for ecofriendly products, cost competitiveness,
recently emerged environmental issues, increased concept of recycling of water
and also limitations of pulp & paper mills, Central Pollution Control Board
has decided to review and revise the COINDS of pulp & paper mills. Eight
industries from each group i.e. large pulp & paper industries and small pulp
& paper industries have been selected for carrying out in-depth studies. The
indepth study has been completed and report is under preparation. Based on the
findings from the present studies, the discharge standards for effluent and emissions
shall be recommended. Development of Guidelines for Water Conservation
in Pulp & paper industry Pulp & Paper industries have been considered
as high water intensive industry using high volume of water in paper making. The
water consumption ranges between 100-200 Cum/tonne of paper depending upon the
process technology employed and water management practices followed by the paper
mills. Indian paper industry lags behind with respect to water conservation in
comparison to pulp & paper industries in developed countries where water consumption
is very low ranging between 50-70 cum/tonne of paper. Considering the poor practices
of wastewater recycling and reuse followed by Indian Pulp & Paper Industries,
CPCB has taken up a project on framing guidelines for water conservation in pulp
& paper mills. Under the project, section wise water balance is being undertaken
in selected pulp & paper mills to assess the actual use of water in paper
making. Different technological options for water reuse and recycling shall be
suggested to minimize water consumption. The water consumption/discharge
pattern in different category of pulp & paper mills is presented in Table
10.14. 
The
activities in various sections of pulp & paper mill that consume water are
briefly described below:
» Raw material preparation:
Raw material preparation involves depithing in case of Agro based raw material
like Bagasse, while washing and chipping of logs in case of wood based plant. »
Pulping section: Pulping section involves digestion of the wood or agrobased raw
material, followed by brown stock washing and bleaching operations, pulp cleaning
equipments etc. In addition, water is used for pulp dilution and also for non
process purposes like pump gland cooling and sealing, floor washing, etc. »
Wastepaper pulping: Waste paper pulping involves hydro pulping, followed by centricleaning,
thickening. Mostly recycled water is used in the hydropulper. Fresh water is mostly
used in decker thickner showers. » Stock Preparation
and Paper machine: Water is required for chemical preparation, in wire and press
section showers, vacuum pump sealing, etc. »
Chemical Recovery Plant: Chemical recovery Plant does not require any fresh water
for the process. Fresh water is required for non process operations like pump
gland cooling & sealing, slaker roller bearing cooling, floor washing, etc. »
Utilities: Utilities include Water treatment Plant, DM Plant, Softner Plant, Boiler
House, Cooling tower. 10.6 NOISE POLLUTION Meetings
of the National Committee 11th & 12th Meetings of the National Committee
on Noise Pollution Control were held on April 22, 2003, and January 30, 2004,
respectively in New Delhi. Some major issues discussed during the meetings were: ·
Amendment in Noise Rules/Regulations
· Noise limits for motor
vehicle horns
· Noise limits for in-use motor vehicles
·
Aircraft noise Compliance Testing of Fire-crackers Compliance
testing of fire-crackers for noise limits was carried out in March 2004, in association
with the National Physical Laboratory, New Delhi. The objective of the project
was to study whether the noise levels of fire-crackers available in the market
meet the prescribed noise limits. The test results of the present study are presented
in Table 10.15. Table 10.15 Noise levels produced by a variety of Firecrackers
under free-field condition, at 4 m distance from the point of bursting
| Type
of Cracker | Generated
Noise Level | | dB(Al) |
dB ©pk |
| Hydro
Bomb (Foiled) | 127+1 |
159+1 | |
Hydro Bomb (Green Sutli) |
126+0.5 |
160+1 | |
Atom Bomb (Foiled) |
128+1 |
162+1 | |
Atom Bomb (Green Sutli) |
127+1 |
162+1 | |
Timing Bomb |
127+1 |
159+1 | |
500/5 Crackers |
126+1 |
153+1 | |
100 Lar |
118 |
140 | |
Sky Shot |
111+3 |
133+1.5 |
| Hydro
Bomb (Foiled) | 128+1 |
161+0.5 |
| Mild
Bomb (Foiled) | 125+1 |
151+1.5 |
| Hydro
Bomb (Green) | 127+0.5 |
161+1 | |
Mini Bullet |
127+1 |
155+1 | |
Liberty Ladi |
121 |
142 | |
Agni Max (Green Sutli) |
128+0.5 |
162+1 | |
Agni Max (Green Foiled) |
127+0.5 |
162+1 | |
Classic Super Bullet |
127+0.5 |
157+1 | Stationary
noise level measurement of motor vehicles The project was carried out
in association with Automotive Research Association of India, Pune. Pass-by-noise
as per IS:3028 and stationary-noise as per IS:10399 for 91 new vehicles and 61
in-use vehicles were tested. 10.7 BIO-MEDICAL WASTE MANAGEMENT Bio-medical
Waste Management in Bangalore A total of 31 hospitals and 2 Common Waste
Treatment Facilities were inspected and monitored in Bangalore. Hospitals, both
Government and Private, with and without incinerators were selected based on the
number of beds and their contribution of waste. The study was focused on incinerators,
combustion efficiency, autoclaving, segregation of waste, treatment of liquid
effluent, disposal of waste and sharps etc. It was observed that out of 31 hospitals,
12 have their own incinerators and others are sending their waste either to CWTFs
or to own landfill sites. The stack monitoring at 12 hospitals and both the CWTFs
were carried out. Based on a multi-parameter based indexing system, grading of
hospitals is in progress. Bio-medical Waste Management in Madhya Pradesh
& Rajasthan Many hospitals in Madhya Pradesh and Rajasthan have
provided incinerators to treat the bio-medical waste. Most of them were found
violating the required specifications and were not operating regularly. Incinerators
installed by the Common Treatment Facility (CTF) providers and the incinerators
in eight hospitals were monitored. |