1. Executive Summery

2. IntroductionThis is a project proposal for the proposed 1500 TCD Sugar Mills & 4.9 MW Cogeneration in their

existing land area Sri Ganganagar, Rajasthan by Rajasthan State Ganganagar Sugar Mills Ltd.

The Notification no. S.O. 1533 dated 14.09.2006, under Environmental (Protection) Act (EPA)

1986. Prior Environmental Clearance from the EIA Authorities is mandatory for the

establishment of projects/activities listed in the schedule of above notification. Sugar mills

projects are categorized under 5(J) of schedule of activities and therefore, require prior

environmental clearance from the state level appraisal committee / authority. Hence project of

Rajasthan State Ganganagar Sugar Mills Ltd. is classified under 5(J) category B.

Sri Ganganagar district of Rajasthan offers suitable potential for cultivation of

sugarcane crop in the State. The agro climatic conditions in various pockets

of the district are suitable for cultivation of sugarcane crop.

The identified land is suitable for establishment of the mills complex and sufficient canal water

as well as tube well water is available at site. Setting up of modern sugar complex away from the

city and closer to the cane growing area will reduce cost of cane transportation. Majority of the

sugarcane is being transported by trucks/trolleys. The road network connecting the proposed

site is quite satisfactory and sugarcane transportation via tractors & trucks would be easily

manageable. Also the necessary electric sub-station to evacuate the exportable power from the

sugar unit located at 0.5 Km from the new site. Various infrastructure facilities like

communication and electricity are also closely available. The sugarcane crop provides

employment opportunities to a large number of rural population right from its

cultivation in the field up to its processing in sugar factory / distillery unit

3. Project Descriptioni. Type of Project:

The proposed integrated sugar complex will have an initial installed crushing capacity of 1500

tonnes of cane per day (TCD) & 4.9 MW Co Gen unit using latest technology. It will manufacture

30 KLPD rectified spirit for valued addition in products. The proposed configuration of high

pressure co-generation will ensure saving of substantial quantity of surplus bagasse, after

meeting the entire fuel and power requirement of the sugar plant and distillery.

ii. Location of Project:

Sri Ganganagar Sugar Mills Limited is presently situated at Sri Ganganagar, a district

headquarters. Ganganagar is located at 29°55′N 73°53′E / 29.92°N 73.88°E / 29.92;

73.88. The Factory Site is located on National Highway No.15 and the nearest railway

station Sri Ganganagar is at a distance of 2.5 Km from factory site.

The present factory site is now almost in town due to development over period and has

become a major urban center. This causes major difficulties with sugarcane

transportation to factory. It is proposed to set up a modern sugar complex at a new site.

It is situated at a distance of 35 km from Sri Ganganager in village- Kaminpura. About

37.40 hectare land has been identified by the mills management for setting up of Sugar

Complex. The identified land is suitable for establishment of the mills complex and

sufficient canal water as well as tube well water is available at site.

iii. Site selection criteria:

Raw Material Availability

sufficient canal water as well as tube well water is available at site.

Setting up of modern sugar complex away from the city and closer to the cane

growing area will reduce cost of cane transportation.

The road network connecting the proposed site is quite.

Infrastructure facilities like communication and electricity are also closely

available.

The proposed provides employment opportunities to a large number of rural

population.

iv. Size or Magnitude of Operation:

The proposed project M/s Rajasthan State Ganganagar Sugar Mills Ltd. is having

capacity of 1500 TCD sugar unit & 4.9 MW Co Generation plant.

v. Manufacturing Process:

Juice Extraction Section

The proposed juice extraction system comprises of a set of knives, an electric motor

driven heavy duty swing hammer fibrizer and 4 nos. mills, each having 3 nos. grooved

rollers of 762 mm dia x1525 mm length and a toothed type under feed roller, driven by

a 400 HP AC VFD through a set of reduction gearing. The milling tandem is designed for

low power consumption (about 12 KW/Tonne cane) andhigh extraction efficiency at

targeted crushing rate of 70 tonnes of cane per hour. Provision shall be kept in the lay-

out for installation of a zero mill in the future for ultimate capacity of 2500 TCD.

A recent development is the introduction of milling tandems based on 2 roller design of

mills. Two such tandems are under commissioning in the season 2009-10. These may be

studied for evaluating the cost benefit analysis vis-à-vis conventional 3 roller design of

mills so that a decision may be taken whether to consider the 2 roller design of mills for

the proposed sugar complex.

Juice Processing Section

Double Sulphitation process supplemented with clarification of filtrate by

phosphoflotation process has been proposed for production of superior quality

plantation white crystal sugar.

Juice flow stabilization system and automatic ph control system for improved

clarification efficiency, uniformity of process control & better final product quality has

also been incorporated.

Modern energy-efficient quintuple effect evaporator set-up with condensate flash

recovery system and extensive vapor bleeding for juice heaters and vacuum pans has

been proposed for concentration of the clarified juice into syrup. Three massecuite

boiling scheme using low head fast boiling calandria type batch pans fitted with

circulators has been proposed for crystallization of the syrup.

For low grade massecuite, double curing of ‘C’ massecuite and single curing of ‘B’

massecuite using continuous centrifugal machines has been proposed to minimize sugar

loss in final molasses.

For high grade massecuite (‘A’), single curing using automatic recycling batch type high

gravity factor centrifugal machines has been proposed to produce premium quality

sugar.

In view of the adoption of incidental cogen configuration for the power plant, a

moderate level of process steam consumption has been envisaged, with design

flexibility for further reduction in future.

Steam & Power Generation Section

One number bagasse fired, travelling grate, high set design, water tube Boiler of 40

tonnes per hour capacity suitable for generating steam at 72 ATA 510 deg C at super-

heater outlet ,with air heater & economizer as heat recovery units with a view to obtain

rated boiler efficiency of 70% on gross calorific value of bagasse has been proposed. The

boiler shall be provided with a wet-scrubber for limiting the Solid Particulate Matter

(SPM) level in stack gases to less than 150 mg/NM3 to meet the environmental

standards applicable to sugar mills.

One no. 5.5 MW installed capacity extraction cum condensing Turbo Alternator Set

suitable for 72 Ata steam, generating 3 Phase 11 KV, 50 Hz AC and step down

transformers with 415 volts distribution system (for the various electrical units of the

complex) has also been proposed.

A switch yard of suitable capacity along with a step-up transformer and necessary

protective devices shall be provided for interfacing with the grid at a voltage of 33 KVA

for export of about 2.2 MW surplus power in season & 3.1 MW in off- season.

The above boiler and TG set shall meet the entire process steam and power

requirement for the sugar, power and distillery sections of the complex .

However, stand-by Diesel Generating Set has been proposed for installation to meet the

start-up and emergency power requirements of the complex.

vi. Raw Material:

Raw can at 1500 tonnes per day will be the raw material required.

vii. Resource Optimization:

The byproduct named bagasse obtained from sugar factory will be utilized as fuel for

boiler.

viii. Water Requirement:

Total water required for the proposed project is 960 m3/day and will be made available

through F -distributary canal found near the project site. Part water will be sourced from own tube wells.

Water budget

S.No. Source Possible contamination Quantity

m3/day

1. Spray pond blow down Concentrated dissolved

solids and sugar traces

80

2. Excess condensate water

of vapors

Traces of organics 750

3. Mill washing Mill washing Water with

bagasse, grease & oil

10

4. Process washing Sugar traces and bagasse 20

Total Discharge from factory, m3/day 960

ix. STEAM AND FUEL BALANCE

S.No. Particulars Unit Quantity

1. Total cane crush per season @ 90 % cap utilization T o n n e s 1,62,000

2. Gross duration of season Days 120

3. Average crushing per gross day Tonnes 1350

4. Bagasse production in season

4.1 Bagasse % cane % 29.51

4.2 Bagasse production per hour Tonnes 20.66

4.3 Total bagasse produced in season Tonnes 47806

@ 90 % capacity utilization Tonnes 43025

5. Steam generated from bio-gas in season Tonnes/day 30

5.1 Equivalent quantity of bagasse saved Tonnes/day 13.95

5.2 Net bagasse saved in season due to bio gas Tonnes 1674

6. Total bagasse consumption in season

6.1 Bagasse consumption at vac. filters @ 0.80 % cane Tonnes 1166

6.2 Bagasse reqd. for start-up & losses @ 0.25 % cane Tonnes 364.5

6.3 Bagasse consumption in boiler @ 19.91 % cane Tonnes 29028.78

6.4 Total bagasse consumption in season Tonnes 30,558

6.5 Less saving of bagasse due to bio-gas (para 5.2) Tonnes 1,674

6.6 Net total bagasse consumed in season (6.4 – 6.5) Tonnes 28,884

7. Bagasse saved at the end of season (4.3-6.5) Tonnes 14,141

ESTIMATED FUEL BALANCE: OFF-SEASON

S.No. Particulars Unit Quantity

1. Steam flow in off-season Tonnes/hr 29

2. Steam fuel ratio of the boiler Ratio 2.35

3. Quantity of bagasse required / hr Tonnes/hr 12.34

4. Bagasse required / day @ 90 % cap.

Utilization Tonnes/day 266.55

5. No. of working days possible with saved

Bagasse Days 57.63

6. Total fuel required for 170 days operation Tonnes 45313

7. Storage & windage loss of bagasse

in offseason Tonnes 250

8. Available fuel / saved in season Tonnes 14,141

9. Extra bio-mass required for off season Tonnes 31172

So, for running the cogen for a period of 170 days in off-season, extra bagasse / bio-mass

required is 31172 tonnes, depending on the comparable calorific values of the bio-mass.

Average calorific value of the bio-mass is almost equal to the calorific value of Bagasse.

*Estimated Calorific value of Mustard crop residue = 3800 kcal/kg

**Estimated Calorific value of cotton stalks = 1750 kcal/kg

x. Power Requirement:

Present power consumption and addition required if full capacity is to be used are detailed

below:

POWER BALANCE OF SUGAR PLANT & DISTILLERY - IN SEASONInstalled capacity of sugar plant TG set kw 5500Gross power generation at 26.25 T/hr steam flow kw 4900Power required for sugar plant kw 2100Power required for distillery kw 700Total power consumed for sugar & distillery kw 2800Surplus power for export kw 2100

xi. Waste Generation & Disposal:

Waste generated from the distillery include waste water from process and domestic

sources, flue gases from boiler, smoke from diesel generators, boiler ash and yeast

sludge. The Source of these pollutants and control measures to prevent impacts on

environmental parameters is discussed bellow.

Adequate environment management systems will be put in place for the treatment of

all liquid, solid & gaseous discharges from the sugar complex to achieve the required

emission levels well within the permissible limits of state pollution boards.

As a result there shall be no adverse impact on either the air or water quality in and

around the sugar complex.

Quantity, source and treatment procedures for the effluent generated from sugar

complex is as detailed below.

Liquid effluent from sugar mill

Estimated quantity of sugar factory effluent

S.No. Source Possible contamination

Quantity

m3/day

1. Spray pond blow down Concentrated dissolved

solids and sugar traces

80

2. Mill washing Mill washing Water with bagasse, grease & oil

10

3. Process washing Sugar traces and bagasse

20

Total Discharge from factory, m3/day 110

Typical characteristics of sugar factory effluent

Sr No Parameters Value

1 pH 5.5-6.5

2 BOD(5 days at 20 C) 1200-1400 mg/liters

3 COD 2200-2400 mg/liters

4 Suspended Solids 1200-1600 mg/liters

5 Oil & Grease 50-70 mg/liters

Treatment scheme for sugar factory effluent

Screen Chamber

Screening is the first unit operation during the effluent treatment. Screening necessarily involves

interception of the coarse solids by means of a bar rack inclined at 45-60 deg. in the flow direction. The

screened material to be removed by a manual bar rack.

Oil & Grease Trap

After screening the effluent will enter a Oil & Grease Trap. The floatable free oil & grease shall rise to the

surface and removed by means of a mechanical skimmer. The skimmed oil & grease will be collected

into an oil trough and disposed off as per requirement.

Aerobic System

Excess condensate after cooling in cooling ponds along with above effluent, from other sources to be

sent to a primary clarifier to separate solid by settling. This will improve the performance of aerobic

system for aeration to reduce COD & BOD.

Overflow of primary clarifier will be sent to an Aeration Tank operating on the principle of Extended

Aeration process. In the aeration tank, an aerobic bacterial culture is maintained in suspension. The

aerobic environment in the tank is achieved through a mechanical surface aerator, which also ensures

that the contents remain in a well mixed regime of effluent and aerobic sludge.

After a specified time, the mixture is passed into a Secondary Clarifier, where the cells are separated as

sludge from the wastewater. The settled activated sludge is recycled to the Aeration Tank to maintain

the desired concentration of MLSS (Mixed Liquor Suspended Solids).

Excess Sludge Disposal & Treatment

The excess activated sludge from the Aerobic system will be taken to Sludge Drying Beds for necessary

dewatering. During the drying period, the moisture will evaporate and also filter through the filtering

media. The sludge cakes to be used as manure while the filtrate will be taken to Equalization cum Buffer

Tank.

Pressure Sand Filtration

Treated effluent from the secondary clarifier will be put to sand filtration to remove all the suspended

impurities.

Activated Carbon bed

Filtered effluent will be passed through carbon bed to remove colors and part of the organics.

Treated effluent will be used for irrigation and discharged to the land area. The

typical characteristic of treated effluent is as below.

Sr No Parameters Value

1 pH 7.5-7.8

2 BOD(5 days at 20 oC) <30 mg/liters

3 COD <250 mg/liters

4 Suspended Solids <30 mg/liters

5 Oil & Grease 2-5 mg/liters

GASEOUS EMISSIONS

Gaseous emissions are generated from boiler and diesel generator. Diesel generators are used only

during power failure to meet the supply of power to essential services.

Details of Gaseous Emissions

Parameters Proposed

Boiler capacity 40 T/hr

Fuel consumption,

100% Bagasse

Chimney height As Per Norms.

Chimney diameter 3.0 meters

D G Sets

Fuel - HSD

Fuel consumption Used only during power failure

SPM in flue gas (max.), mg/Nm3 less than 150 mg/NM3

Control Equipment wet scrubber

Control for particulate emission

As per pollution control regulations of State, the limit for the particulate matter emission from the

bagasse-fired boiler is 150 mg/Ncu m.

Wet Scrubber is proposed for the boiler to contain the dust emissions from the plant within the

prescribed pollution control norms. Besides above the height of the stack; which disburses the

pollutants is to be fixed based on the guidelines given by the pollution regulation of the state .

SOLID WASTES AND ITS DISPOSAL

Fermenter Sludge and boiler ash are the main solid wastes generated from the distillery. Disposal of solid wastes is given bellow.

Parameters Production Utilization/disposal

Boiler Ash. 1.5 % Total fuel consumption Fine ash sold to cement manufacturer.

Coarse sold to fire bricks manufactures,

ETP Sludge will be used as manure.

Bagasse 450 MT/day Used as boiler fuel.

ENVIRONMENTAL MONITORING PROGRAMME

The effectiveness of these measures will be ascertained by systematic monitoring of discharges at

factory and receiving levels.

Environmental Cell

Environmental cell consisting of departmental heads will be created to effectively manage the

environmental activities in the distillery. Environmental department will be formed with environmental

scientist, laboratory chemists and operators to implement and operate pollution control and

environmental protection measures. Third party monitoring will be carried out to double check

effectiveness of mitigation measures. Proponent analysis report, third party report will be corroborated

with statuary body, so that results are in line with standards all time.

Monitoring Facilities and Schedule

A laboratory will be established with manpower and facilities to analyze water, wastewater, stack

emission, ambient air etc. The parameters monitored are temperature, SPM, SO2

and NOX

for gaseous

emissions and SPM, RSPM, SO2

and NOX

ambient air. Till such time analysis may be carried out by

competent third party.

The quality of discharges including spent wash, wastewater, flue gas, yeast sludge and the receiving

bodies such as ambient air, water, surface water and soil will be monitored for the desired parameters.

Sampling locations and post project monitoring schedule have been worked out.

Environmental Records

Environmental department will maintain log sheets and manuals for operation and maintenance of

pollution control and related facilities. Progress reports and statuary records as per environmental acts

will also be maintained.

ENVIRONMENTAL MANAGEMENT PLAN

Ours is an existing industry planning expansion, modernization and relocation. We have well established

environmental management plan (EMP). The sugar plant and power plant utilize resource such as water,

grain, bagasse etc. and discharge liquid, gaseous and solid waste products. Mitigation measures are

incorporated in the project to protect environment against any harm. A comprehensive environmental

management plan is adopted consisting of proposed pollution control measures and additional

mitigation measures for abatement undesirable impacts. .Summary of these measures includes:

1. Green belt and greenery development in the factory premises.

2. Waste water management Recycle & Reuse

3. Impervious storage pond will be constructed to hold at least 1 month’s effluent during monsoon.

4. Paving and lining of roads, solid storage yards of ash etc.

5. Piezometres will be installed at various locations down gradient to monitor and ensure no adverse

impacts due to percolation.

6. Self monitoring system is established in the industry with man power and facilities to ascertain the

compliances of environmental norms and standards.

7. Personal health care programme, emergency management plan and safety management systems

will be implemented in the distillery.

8. Operation and Maintenance of pollution control measures

9. Establishment of waste reduction measure

xii. Schematic Representation of feasibility drawings

4. Site Analysis:

i) ConnectivityThe Factory Site is located on National Highway No.15 and the nearest railway station Sri Ganganagar is at a distance of 2.5 Km from factory site.

Sr. No Feature Particulars

1. Location Sri Ganganagar

2. Nearest major road National highway 15

3. Nearest railway station Sri Ganganagar is at a distance of 35 Km from factory site

4. Nearest village Kaminpura.

5. Nearest major city Sri Ganganagar

6. Nearest water body canal water F distributary and tubewells

7. Nearest industry I) Fazllka Cooperative Sugar Mills, 1500 TCD, 60 kmii) Markfed Cooperative Sugar, Malout, 1750 TCD, 70 km

8. Sensitive locations None

RSGSML in consultation with the Govt. of Rajasthan has decided to set up an integrated sugar

complex at a new location at village: Kaminpura on the Ganganagar – Karanpur main road, at a

distance of 35 kms from Sri Ganganagar town in the state of Rajasthan. The proposed site is barren

land doesn’t include any forests, national parks, wild life sanctuaries, eco sensitive areas as well as

water bodies.

The distillery is located near NOC has been obtained from Gram Panchayat for Industrial use which

is attached. The operational area of the sugar factory is spread over in 130 villages . The details of

factory area, built up area and the area reserved for green belt development is given in layout

drawing.

The land holdings pattern in the district is generally extraordinarily large, although small farmers are

also cultivating various crop in the area. The land holdings are suitable for educating and motivating

the farmers to encourage them to cultivate sugarcane using modern cultivation techniques.

ii) Existing Infrastructure:

iii) Soil Condition

The texture of soils of the area is ranging from sandy to loam and sufficient land area of sandy loam

type is available for cultivation of sugarcane crop. The topography of the land is plain and soils are

well drained. The pH of the soil is 7 to 8. The soils are slightly deficient in nitrogen but are rich in

phosphorous and potash. The agro climatic conditions of the zone are as follows:-

Soil characteristics

i) Type of Soil - Sandy loam

ii) Soil pH - 7.0 to 7.5

iii) Soil nutrients - Sufficient

iv) Climatic data:

Rain-fall in the last five years has been recorded as below:

Year Rainfall (mm)

2001-02 323.60

2002-03 114.10

2003-04 369.52

2004-05 229.50

2005-06 260.80

The annual rainfall varies from 114 mm to 370 mm during the year. However, the maximum rainfall is during monsoon season which reaches its peak in the month of July and August.

It is very hot in summer and moderately cold in winter. Hot winds blow through out the summer. Winds are generally light during the post monsoon and winter months.

The minimum and maximum temperature varies between 4°C to 44°C.

Month 2004 2005 2006

Max. Min. Rain Fall

Max. Min. Rain Fall

Max. Min. Rain Fall

Jan 18.96 07.38 15.7 19.88 6.42 13.60 22.12 6.96 11.0

Feb 27.43 10.32 2.3 21.85 10.90 44.70 29.75 12.55 -

Mar 35.60 15.82 - 31.10 16.25 47.00 31.00 14.90 42.6

Apr 39.46 21.65 1.4 38.82 19.96 2.40 40.40 21.28 1.7

May 41.94 26.12 40.8 40.22 23.42 42.50 43.64 28.20 8.7

June 39.84 27.49 82.4 41.30 28.80 20.90 39.72 22.25 121.9

July 40.51 29.18 13.4 40.52 29.37 39.20 37.87 28.17 23.7

Aug 39.75 27.42 18.8 40.47 28.65 - 37.85 27.12 14.0

Sep 38.75 24.39 1.8 36.87 23.25 44.30 38.27 125.1 11.6

Oct 32.00 17.36 22.6 36.26 17.64 - 35.20 19.44 -

Nov 29.70 12.27 - 29.39 10.12 6.20 27.82 12.57 7.4

Dec 24.11 07.70 30.3 23.75 04.20 - 22.12 7.45 8.9

v) SOCIO ECONOMIC CONDITION OF REGION

Desert land was converted to a green town, credited to the Maharaja who brought the Gang canal which carries the excess waters of Punjab and Himachal Pradesh to the region, making Ganganagar district known as "the food basket of Rajasthan". The economy of the city is based on agriculture, its main crops are Wheat, Mustard and Cotton. Other crops are Guar, Bajra, Sugar Cane and Grams. In recent years farmers are also diverting towards Horticulture, and Kinnu(A Citrus Family fruit) has become a major crop of the area. The industries in the city are mostly based on agriculture. The city has Cotton Ginning and Pressing factories, Mustard Oil mills and Wheat Flour mills and of course the famous Rajasthan State Ganganagar Sugar Mills Ltd., which is known for its Royal Heritage Liqueurs. It also has spinning and textile factories such as J C T Mills. Because of its prosperity from agriculture, Ganganagar District also has a large number of automobiles which includes tractors and MUVs and because of the large population of automobiles in the district, Sri Ganganagar has become one of the largest automobile markets in India.

DemographicsAs of 2001 Indian census, Ganganagar had a population of 210,788. Males constitute 55% of the population and females 45%. Ganganagar has an average literacy rate of 71%, higher than the national average of 59.5%: male literacy is 76%, and female literacy is 64%. In Ganganagar, 13% of the population is under 6 years of age. Majority in population are Sikhs and Hindus while only a few people constituting other sects stay here. The main languages spoken in the town are Punjabi,Hindi, Bagri or Marwari.

5. Planning Brief:i) Planning Concept

The existing 1000 tonnes cane per day (TCD) crushing capacity sugarplant in the heart of the Sri

Ganganagar town is more than 40 years old and is equipped with obsolete design of plant & machinery,

resulting in high sugar losses, non production of value added products and huge expense on purchase of

extra fuel and power.

Therefore, RSGSML in consultation with the Govt. of Rajasthan has decided to set up an integrated sugar

complex at a new location at village: Kaminpura on the Ganganagar – Karanpur main road, at a distance

of 35 kms from Sri Ganganagar town in the state of Rajasthan.

The proposed integrated sugar complex will have an initial installed crushing capacity of 1500 tonnes of

cane per day (TCD) using latest technology. It will generate power in excess of its requirement. It will

manufacture 30 KLPD rectified spirit for valued addition in products

The proposed configuration of high pressure co-generation will ensure saving of substantial quantity of

surplus bagasse, after meeting the entire fuel and power requirement of the sugar plant and distillery.

This saved bagasse, along-with other supplemental bio-fuels like cotton & mustard stalk will be used for

the off-season operation of the power plant making the complex self-sufficient in its fuel and power

requirements for the total operating period of 290 days per annum (120 days in season and 170 days of

distillery operation in off-season).

The proposed Complex will be configured to achieve the following main objectives:

Thermal and electrical energy consumption of the complex to be at par with the best standards in the Indian sugar industry.

Sugar losses in the sugar plant to be at par with the best standards in the Indian sugar industry.

Self-sufficiency in fuel & power requirements of the complex during the entire period of operation of sugar plant and distillery.

Export of surplus power, throughout the year, through dedicated cogeneration route.

Superior product quality of sugar and alcohol.

Par with the best standards in the Indian sugar industry.

THE PROJECT DETAILS

Sr.

No.

Feature Particulars

1. Location Village Kaminpura, Sri Ganganagar, Rajasthan

2. Project, 1500 TCD Sugar Plant with 5.5 MW cogeneration of power.

3. Working days per year 120 days season duration

4. Products Main Product-

Superior quality Plantation white sugar of 80-100 ICUMSA --- 14823 MT/season

Co-Product-

Final molasses 7890 MT/season

Surplus bagasse 12204 MT / season

Press mud 5265 MT/season

Power @ 5.5 MW

5. Main raw material Sugar cane 1500 tonnes per day

6. Man power in the industry

Workers/Staff/Contractual

workers

300

7. Total land area 37.40 hectare

8. Steam requirement 32.9 MT/hr

9. Boiler Steam generation capacity 40 TPH capacity at 72 Ata, 510+/_5 deg C steam at

super-heater outlet .

10. Boiler fuel consumption

Bagasse

Any other

11. Sugar plant Power requirement 2100 KW

12. Source of water canal water as well as tube well will be used

13 D G set 500 KW - 2 Nos and 100 KW - 1 No

14. Dust collector Venturi scrubber

ii) Population Projection

MAN POWER

STAFFING PATTERN FOR SUGAR & POWER PLANT

Sr.No. Department Permanent Seasonal

Total

1. Administration Section 4 - 4

2. General office 10 - 10

3. Legal section 2 - 2

4. Audit 3 - 3

5. Guest house 2 - 2

6. Medical section 2 - 2

7. Purchase 6 - 6

8. Stores 4 2 6

9. Accounts 10 - 10

10. Lab welfare 2 - 2

11. Time office 10 3 13

12. Cane Deptt. 10 40 50

13. Engineeering 15 50 65

14. Workshop 10 5 15

15. Production 10 30 40

16. Contracts - 60 60

Total 100 190 290

iii) Land use planning (Break up along with green belt etc.)

iv) Assessment of Infrastructure & demand:

v) Amenities:

About 28633 Sq M land has been enmarked for residential Colony at proposed site, soak pith will be provided.

6. Proposed Infrastructure:i) Industrial area (Processing area)ii) Residential area (non Processing area)iii) Green beltiv) Social infrastructurev) Connectivity: Nearest Road is NH 15 & SH 7B. nearest railway station is Sri Ganganagar is

at a distance of 35 Km from factory site. Nearest village is kaminpura while nearest major city is Sri Ganganagar.

vi) Drinking water management: Water source is F Distributary canal & tube wells.vii) Sewerage system:viii) Industrial waste management: Full fledged ETP will be provided for treatment of

wastewater while stack and wet scrubber will be provided for air pollution control. Solid waste management: Baggase will be used as a fuel for boiler and boiler ash sold to cement manufacturers. Coarse sold to fire bricks manufactures, ETP Sludge will be used as manure.

ix) Power Requirement & source: Power required for sugar plant is 2100 kw which will meet from own 4.9 MW Co Gen unit.

7. Rehabilitation & Resettlement Plan: Rehabilitation or resettlement will not takes place in case of proposed project.

8. Project Schedule & Cost Estimates:

The total project cost for the Sugar & Power in complex is estimated as follows:

S No Particulars Rs in lacs

1. Site development and Civil works 1100.00

2. Plant and Machinery including Taxes and Duties, Freight &

Erection etc.

4430.00

3. Cane Development 30.00

4. Miscellaneous Fixed Assets 215.00

5. Pre-operative Expenses 300.00

6. Contingencies 345.00

7. Start-up expenses 20.00

8. Stores & spares 40.00

9. Margin money (incremental) 20.00

Total cost 6500.00

9. Analysis of Proposal (Final Recommendation):