PROJECT PRE FEASIBILITY REPORT - Welcome to...

PROJECT PRE FEASIBILITY REPORT

For

Application for TORs

Of

Proposed expansion project for

manufacturing of paper from waste

paper based paper mills

At

Plot No. 97,

GIDC Estate, Vapi 396195,

Dist: Valsad.

Project proponent

M/s. Shah Pulp & Paper Mills Ltd.

Project Pre-feasibility report

i

CONTENTS

CHAPTERS

S. No. Particulars Page No.

1 EXECUTIVE SUMMARY 1-2

2 INTRODUCTION OF THE PROJECT 3-4

2.1 IDENTIFICATION OF THE PROJECT AND PROJECT PROPONENT 3

2.1.1 IDENTIFICATION OF THE PROJECT 3

2.1.2 DETAILS OF PROJECT PROPONENT 3

2.1.3 NATURE OF THE PROJECT 4

2.1.4 NEED OF PROJECT & DEMAND-SUPPLY GAP 4

2.1.5 IMPORTS VS. INDIGENOUS PRODUCTION 4

2.1.6 EXPORT POSSIBILITY 4

2.1.7 DOMESTIC/ EXPORT MARKETS 4

3 PROJECT DESCRIPTION 5-18

3.1 TYPE & LOCATION OF THE PROJECT 5

3.1.1 TYPE 5

3.1.1.1 LOCATION 5

3.2 DETAILS OF ALTERNATIVE SITE 8

3.3 SIZE & MAGNITUDE OF OPERATION 8

3.4 PROJECT DESCRIPTION WITH PROCESS DETAILS 9

3.4.1 MANUFACTURING PROCESS 9

3.4.2 FLOW DIAGRAM 10

3.5 RAW MATERIAL FOR FINISHED PRODUCT 10

3.6 HAZARDOUS CHEMICAL STORAGE & HANDLING 10

3.7 RESOURCE OPTIMIZTION & AVAILABILITY 11

3.7.1 LAND & BUILDING REQUIREMENT 11

3.7.2 EQUIPMENTS 11

3.7.3 POWER REQUIREMENT 11

3.7.4 FUEL REQUIREMENT 11

3.7.5 WATER REQUIREMENT 11

3.7.6 MAN-POWER REQUIREMENT 12

3.8 QUNTITY OF WASTE TO BE GENERATED 12

3.8.1 WASTE WATER GENERATION & MANAGMENT 13

3.8.2 WASTE WATER CHARACTERISTICS 13

3.8.3 WASTE WATER TREATMENT & DISPOSAL 14

3.8.4 AIR EMISSION & CONTROL 15

3.8.4.1 PROCESS EMISSION 15

3.8.4.2 UTILITY EMISSION 15

3.8.4.3 FUGITIVE EMISSION 16

3.8.5 HAZARDOUS/NON-HAZARDOUS WASTES MANAGEMENT 16

3.8.6 NOISE CONTROL 17

3.9 HEALTH & SAFETY MEASURES 17

3.10 ENVIRONMENTAL HEALTH & SAFETY PLAN 17

3.11 POST PROJECT MONITORING PLAN 18

4 SITE ANALYSIS 19-21

4.1 CONNECTIVITY 19

4.2 LAND FORM, LAND USE & LAND OWNERSHIP 19

4.3 TOPOGRAPHY 19

4.4 SALIENT FEATURES 19

4.5 EXISTING INFRASTRUCTURE 19

4.6 SOIL CLASSIFICATION 19

Project: Project for manufacturing of Pesticides & Synthetic Organic Chemical ii | P a g e


4.7 CLIMATE & METEROLOGY 20

4.7.1 TEMPERATURE 20

4.7.2 HUMIDITY 20

4.7.3 RAINFALL 21

4.7.4 WIND PATTERN 21

4.8 SOCIAL INFRASTRUCTURE 21

4.8.1 EDUCATION FACILITY 21

4.8.2 MEDICAL FACILITY 21

5 PLANNING BRIEF 22-23

5.1 PLANNING CONCEPT 22

5.2 POPULATION PROJECTION 22

5.3 AREA STATEMENT 22

5.4 ASSESMENT OF INFRASTRUCTURE DEMAND (PHYSICAL & SOCIAL)

22

5.5 AMENITIES/FACILITIES 22

5.5.1 DRINKING WATER FACILITY 22

5.5.2 POWER & SUPLY FACILITY 23

5.5.3 COMMUNICATION & BANKING FACILITY 23

5.5.4 TRANSPORT FACILITY 23

6 PROPOSED INFRASTRUCTURE 24-24

6.1 INDUSTRIAL AREA 24

6.2 RESIDENTIAL AREA 24

6.3 GREENBELT 24

6.4 SOCIAL INFRASTRUCTURE 24

6.5 CONNECTIVITY 24

6.6 DRINKING WATER MANAGEMENT 24

6.7 SEWERAGE SYSTEM 24

6.8 INDUSTRIAL WASTE MANAGEMENT 24

6.9 SOLID WASTE MANAGEMENT 24

6.10 POWER REQUIREMENT & SOURCE OF SUPPLY 24

7 REHABILITATION & RESETTLEMENT (R&R) PLAN 25-25

7.1 POLICY TO BE ADOPTED 25

8 PROJECT SCHEDULE & COST ESTIMATES 26-26

8.1 TIME SCHEDULE OF THE PROJECT 26

8.2 ESTIMATED PROJECT COST 26

9 ANALYSIS OF PROPOSAL 27-27

9.1 FINANCIAL & SOCIAL BENEFITS 27

Project: Project for manufacturing of Pesticides & Synthetic Organic Chemical iii | P a g e

LIST OF TABLES


TABLE 1.1 PROJECT SUMMARY 1

TABLE 2.1 LIST OF PRODUCTS 3

TABLE 2.2 LIST OF DIRECTORS 3

TABLE 3.1 AREA STATEMENT 8

TABLE 3.2 LIST OF RAW MATERIALS 10

TABLE 3.3 DETAILS OF HAZARDOUS CHEMICALS/ MATERIALS STORAGE AND HANDLING

10

TABLE 3.4 LIST OF EQUIPMENT/ MACHINERIES 11

TABLE 3.5 CATEGORY WISE FRESH WATER REQUIREMENT 12

TABLE 3.6 MAN-POWER REQUIREMENT 12

TABLE 3.7 WASTE WATER GENERATION 12

TABLE 3.8 EXPECTED CHARACTERISTICS OF COMPOSITE WASTE WATER 14

TABLE 3.9 DETAILS OF ETP UNITS 15

TABLE 3.10 DETAILS OF UTILITY EMISSIONS 16

TABLE 3.11 HAZARDOUS AND NON-HAZARDOUS WASTE GENERATION AND ITS MANAGEMENT

16

TABLE 3.12 SAFETY DETAILS 17

TABLE 3.13 ENVIRONMENTAL MONITORING PLAN 18

TABLE 4.1 SALIENT FEATURES OF THE PROJECT SITE 19

TABLE 4.2 SUMMARY METEOROLOGICAL DATA AT NEAREST IMD STATION- DAHANU

20

TABLE 5.1 DISTRIBUTION OF POPULATION 22

TABLE 5.2 AREA STATEMENT 22

TABLE 8.1 TOTAL CAPITAL COST PROJECTION 26

TABLE 8.2 TOTAL CAPITAL COST POWER PLANT 26

TABLE 8.3 RECURRING COST PROVISION FOR EHS 26

LIST OF FIGURES


FIGURE 3.1 LOCATION OF THE PROJECT SITE 6

FIGURE 3.2 SATELLITE IMAGE OF THE PROJECT SITE 7

FIGURE 3.3 SITE LAYOUT PLAN 8

FIGURE 3.4 WATER BALANCE DIAGRAM FOR EXISTING SCENARIO 13

FIGURE 3.5 WATER BALANCE DIAGRAM FOR PROPSOED SCENARIO 13

FIGURE 3.6 FLOW DIAGRAM OF ETP 15

FIGURE 3.7 ORGANOGRAM OF EHS MANAGEMENT CELL 18

LIST OF ANNEXURES

ANNEXURE No. Particulars

ANNEXURE-1 EXISTING CC&A

ANNEXURE-2 NOC GRANTED

ANNEXURE-3 LAND DOCUMENTS


Proposed Expansion project for manufacturing of paper from waste paper based paper mills Page | 1

CHAPTER – 1

EXECUTIVE SUMMARY

Table- 1.1 Project Summary

PARTICULARS DETAILS

NAME OF THE UNIT

M/s. Shah Pulp & Paper Mills Ltd.

PRODUCTS The list of products are as follows:

Sr. No.

Name of the product

Existing Qty. (T/month)

Proposed Qty. (T/month)

Total Qty. (T/month)

1 Printing/ Writing/ News/ Print Paper

5500 500 6000

2. Co-generation Power plant*

0.5 MW 4.9 MW 4.9 MW

Note: 1. *CTE has been obtained. 2. Existing 13 T/hr boiler will be kept as stand-by after the installation of 30 T/hr

Boiler.

LOCATION Plot No. 97, GIDC Estate, Vapi 396 195 Dist. Valsad.

NAME OF PROJECT

Proposed expansion project for manufacturing of paper from waste paper based paper mills (Printing/ Writing/ News/ Print Paper).

RESOURCES

Resource type Requirement Source

Land Existing land: 39113.84 m2

No additional land will be required for proposed expansion. Necessary modifications will be done in the existing infrastructure.

The existing site is located in GIDC Estate, Vapi.

Water Existing Scenario: Total kl/day

Domestic: 10.00 kl/day

Industrial: Process: 564.00 kl/day Utilities: 51.00 kl/day

Total: 615.00 kl/day

After proposed expansion: Total kl/day

Domestic:10.00 kl/day

Industrial: Process: 680.00 kl/day Utilities: 570.00 kl/day

Total: 1250.00 kl/day

The fresh water is/will be supplied by GIDC water supply department.

Power Existing: 4000 kVA

After proposed expansion: 4500kVA

The power supply is/will be supplied by Dakshin Gujarat Vij Co. Ltd.

Fuel Existing:

Coal/Lignite: 48 T/day

After proposed expansion:

Coal/Lignite: 48 T/day (Stand-by)

Coal: 120 T/day* (Note: *CTE has been obtained)

----



PARTICULARS DETAILS

POLLUTION POTENTIAL & MITIGATION MEASURES

Parameter Potential Mitigation

Wastewater Existing: Total kl/day


Industrial: 125.00 kl/day

After proposed expansion: Total kl/day


Industrial: 300.00 kl/day

Domestic waste water is/will be disposed through septic tank/soak pit system.

The industrial effluent is/will be treated in the in-house ETP and after conforming the CETP inlet norms is/will be discharged to CETP.

Air Emissions Existing:

Utilities: Boiler (13 T/hr) with 0.5 MW Co-generation power plant.

Process: No process emission

After proposed expansion:

Utilities: Boiler (30 T/hr) with 4.9 MW Co-generation power plant.*

Boiler: 13 T/hr. (Stand-by).

Process: No process emission

(Note: *CTE has been obtained)

Presently for boiler (13 T/hr) E.S.P is installed as the Air pollution control system.

Additionally, CTE has been obtained for 30 T/hr boiler with 4.9 MW Co-generation power plant. For the proposed installation new E.S.P. will be installed as air pollution control system.

The existing 0.5 MW Turbine will be dismantelled and 13 T/hr Boiler will remain stand-by.

There is/will be no process emissions from the proposed expansion project.

Hazardous & solid waste

Existing:

ETP waste: 40 T/ annum.

Deinking sludge: 8600 T/annum

Used oil: 0.25 KL/annum

Discarded containers: 200 Nos/annum

Non-recyclable plastic waste- 5040 T/annum

Used resin: As & when generated

After Proposed Expansion:

ETP waste: 44 T/ annum

Deinking sludge: 14000 T/annum

Used oil: 0.27 KL/annum.

Discarded containers: 218 Nos/ annum.

Non-recyclable plastic waste- 5498 T/ annum.

Used resin: As & when generated

ETP waste is/will be sent to TSDF-VWEMCL (Vapi Waste and Effluent Management Co. Ltd.) for disposal.

Used oil is/will be sent to registered reprocessors.

Discarded containers/bags is/will be sent to registered de-contaminators

Non- recyclable plastic waste is/will be disposed by incineration at TSDF sites/for co-processing at cement industries.

Used resin is/will be sent to TSDF-VWEMCL (Vapi Waste and Effluent Management Co. Ltd.) for disposal.

Noise Expected levels

Within the premises: <75 dB(A) during day time <70 dB(A) during night time.

Regular maintenance of the machinery is/will be carried out.



CHAPTER – 2

INTRODUCTION OF THE PROJECT

2.1 IDENTIFICATION OF THE PROJECT AND PROJECT PROPONENT

2.1.1 IDENTIFICATION OF THE PROJECT

M/s. Shah pulp and paper mills Ltd. is unit for manufacturing of paper from waste paper based paper

mills, at plot no. 97, G.I.D.C Estate, Vapi 396195Dist: Valsad. The company has obtained CC&A vide

consent order no. AWH-50741dated 20/11/2012 for its existing products attached as Annexure-1.

M/s. Shah Pulp and paper mills Ltd. has proposed the project expansion for manufacturing of paper

from waste paper based paper mills.

Table-2.1: List of products

Sr. No.

Name of the product

Existing Qty. (T/month)

Proposed Qty. (T/month)

Total Qty. (T/month)

1 Printing/ Writing/ News/ Print Paper

5500 500 6000

2. Co-generation Power plant*

0.5 MW 4.9 MW 4.9 MW

Note: 1. *CTE has been obtained.

2. Existing 13 T/hr boiler will be kept as stand-by after the installation of 30 T/hr Boiler. (Source: M/s. Shah Pulp & Paper Mills Ltd.)

2.1.2 PROJECT PROPONENT

The company is promoted by 7 Directors. List of directors with name, residential address

anddesignation is provided in below table:

Table 2.2: List of Directors

Sr. No Name Residential Address Designation

1 MahendraHirji Shah

202,Ashwamegh, Sarojini Road, Vile Parle (W), Mumbai 400056., Maharastra, India

Managing Director

2 AmritlalKhimji Shah Haria, Plot No. 207, Residential area, GIDC, Vapi, Valsad, 396195, Gujarat, India

Director

3 Ashok Zaverchand Shah

Plot No. 313,Opp. Vikas emporium, Gunjanarea, GIDC, Vapi, Valsad, 396195, Gujarat, India

Director

4 Rai Harish Kumar Sinha

F-13/204, Green City, Near pal Road, Bhatha, Surat, 394510, Gujarat, India

Director

5 HirenbhaiVinodraiPrajapati

A/201 Landmark Prestige, Opp. Castrol Housing Complex Gurudev-phase 2, Silvassa, 396230, Dadra &Nagar Haveli, India

Independent Director

6 Bharat Gajananrao Dixit

A-402, Asthaawas, Triveni Society balitha, Vapi, Near GEB, NH No.8 Balitha, vapi, Valsad, Pardi Valsad, 396191, Gujarat, India

Independent Director

(Source: M/s. Shah Pulp & Paper Mills Ltd.)



2.1.3 NATURE OF THE PROJECT

The proposed expansion project involves manufacturing of paper from waste paper based paper mills

which falls under the item no. “5(i) category i.e. Pulp and paper industry” and Category B as per

the EIA notification, 2006 (as amended time to time), and needs to obtain environmental clearance

from SEIAA.

2.1.4 NEED OF PROJECT & DEMAND-SUPPLY GAP

M/s. Shah Pulp and paper mills Ltd. is engaged in the manufacturing of paper from waste based

paper mills. Company is going for the expansion of the project with increasing production capacity as

Demand of paper per capita is increasing every year with the “Sarva siksha abhiyan” mission.

Company has better export market for the better quality of paper and to reach the demand of the

market company increases the production capacity. To save environment/ cutting of trees the

government is giving preference to recycled paper.

2.1.5 IMPORTS VS. INDIGENOUS PRODUCTION

Presently company’s sale is around 3750 T/day for domestic & 1250 T/day for export. After the

proposed expansion the total sale will be around 4500 T/day for domestic & 1500 T/day for export.

2.1.6 EXPORT POSSIBILITY

Company has better export market for the better quality of paper and to reach the demand of the

market company increases the production capacity.

2.1.7 DOMESTIC / EXPORT MARKETS

Looking to the market requirement at the same time to improve the productivity of the company.

Presently company’s sale is around 3750 T/day for domestic & 1250 T/day for export. After the

proposed expansion the total sale will be around 4500 T/day for domestic & 1550 T/day for export.



CHAPTER – 3

PROJECT DESCRIPTION

3.1 TYPE & LOCATIONOF THE PROJECT

3.1.1 TYPE

The proposed expansion project involves manufacturing of paper from waste paper based paper

mills. The proposed expansion is to be carried out on existing site located in GIDC estate of Vapi.

Necessary modifications will be done in the existing infrastructure.

3.1.1.1 LOCATION

The project site is located in the GIDC notified industrial area of Vapi. The existing site selection was

guided by many factors like infrastructure, availability of land, water sources, fuel transportation and

power availability. Specific site selection criteria are as follows:

Availability of common effluent treatment plant and hazardous waste disposal facility within the

estate.

Availability of trained and skilled manpower nearby because of the proximity to various industrial

areas and city/town.

The location of the project site is provided in figure 3.1, satellite image of the project site is provided in

figure 3.2 and the site layout plan of the project site in figure 3.3. The area statement is provided in

table 3.1.



Figure 3.1: Location of the project site

(Source: Google.co.in)

Project site



Figure 3.2: Satellite image of the project site

(Source: Google Earth)



Figure 3.3: Site layout plan


Table: 3.1 Area Statement

Particulars Unit Area

Built up area m2 17513.05

Open area m2 13399.04

Greenbelt area m2 8201.75

Total Area m2 39113.84

3.2 DETAILS OF THE ALTERNATIVE SITE

The proposed expansion will be carried out on the existing site. No additional land will be required for

the proposed expansion.

3.3 SIZE & MAGNITUDE OF OPERATION

Total production after the proposed expansion for Printing/ Writing/ News/ Print Paperwill be 6000

T/month.



3.4 PROJECT DESCRIPTION WITH PROCESS DETAILS

The proposed expansion project involves manufacturing of paper from waste paper based paper

mills. The process details are as under:

3.4.1 Manufacturing process for Printing/ Writing/ News/ Print Paper

Manufacture of news print paper is mainly a physical & partly chemical process. Waste paper is

continuously fed by means of a belt conveyor to the pulper. Water is also fed continuously to the

pulper& the waste paper is slushed there into pulp. The pulp is collected in a pit & transferred to the

High Density Cleaner by means of a pump. The H.D. Cleaner removes metals and other impurities.

The pulp is then fed to the bigger turbo separator, which separates plastic impurities from the pulp.

The accepted pulp then goes to Deinking process, where, by flotation, printing ink gets removed from

the pulp, which is then fed to centricelaner where sand etc. comes out as reject and then fed to

Decker. The accepted pulp then goes to the thickener. The rejected pulp goes to the smaller turbo

separator for recovery of pulp from slurry. Here also, the accepted pulp goes to tile thickener, while

the rejected slurry goes to Johnson's screen. The Johnson screen screens rejected slurry to recover

any fibrous pulp, which goes to the pulper, and the rejects like plastic and cotton thread are

separated.

The thickener reduces the water level of pulp and the mixture has a solid consistency of 4 to 5%. The

thickened pulp is collected in the first chest. The second chest takes the pulp for refining through the

Disc Refiners (DDR's). The refiners hydrate the fiber and the stock is transferred to the third chest.

The third chest is where rosin and dyes are mixed and the resultant mixture is transferred to the fourth

chest for addition of alum. Mixing of rosin and alum imparts resistance to absorption of water to the

paper. Optical bleaching, tinting with dyes and mineral addition is carried out to impart certain

properties for better printing effect. The fifth chest collects the stock to be sent to the paper machine.

The pulp is now ready to be supplied to the paper machine section. Through S.R. Box the pulp is

passed through the first stage centri cleaner, consisting of six centri cleaner bottles. Sand particles

are removed here. The accepted pulp is taken to the wire part, while rejected part goes to the second

stage centricleaner consisting of two centricleaner bottles. The accepted part goes back to the wire

part while the rejected part goes to the third stage consisting of one centricleaner bottle. Here too the

accepted part goes to the second stage centri cleaners while the sand particles are separated.

In the wire section wet sheet is formed consisting of about 18% solid and 82% water. The sheet thus

formed is carried to the press where the water content is further reduced to 60%. The sheet is then

taken on to the pre dryer to partly evaporate water from sheet. The partially dried sheet is fed to size

press where surface sizing is carried out to improve smoothness of paper by application of starch

spread on both surfaces of paper under pressure between two rolls. Finally the paper sheet is

transferred to post dryer section to achieve 6% moisture.

In order to improve better printability, paper is passed between chilled cast iron rolls stack called

calendar stack. The paper is fed to the pope reeler, where the paper is wound in the form of jumbo

rolls. The rolls are then rewound on the rewinder where they are cut to required width and the

trimming formed here goes back as waste paper to pulper.

The cut rolls are then packed in hessian cloth, weighed and kept ready for dispatch.



3.4.2 Flow Diagram


3.5 RAW MATERIAL FOR FINISHED PRODUCTS

The list of raw-materials required are as follows:

Table 3.2: List of raw materials

Sr. No.

Name of raw material

Existing Proposed Total

1 Waste paper 6600 T/month 600 T/month 7200 T/month

2 Enzymes 0.64 T/month 0.058 T/month 0.698 T/month

3 Di (Incopper) optical Brightener

5.36 T/month 0.487 T/month 5.847 T/month

4 Whitening Agent 14.52 T/month 1.32 T/month 15.84 T/month (Source: M/s. Shah Pulp & Paper Mills Ltd.)

3.6 HAZARDOUS CHEMICAL STORAGE & HANDLING

The list of hazardous chemicals/materials storage, handling and transportation details are as follows:

Table 3.3: Details of hazardous chemicals/materials storage and handling

Sr. No.

Name of chemical/ material Means of storage and Handling Transportation

1 Hydrogen Peroxide Tank (17 mq) By Truck

2 Hydrosulphite Drum By Truck

3 Caustic Tank (28 mq) By Truck (Source: M/s. Shah Pulp & Paper Mills Ltd.)



3.7 RESOURCE OPTIMIZATION& AVAILABILITY

The main resources for the proposed expansion project will be raw-materials, utility, power, fuel,

water, man-power etc.

3.7.1 LAND & BUILDING REQUIREMENT

The existing land is 39113.84 m2. Necessary modifications will be done in the existing plant. No

additional land will be required for the proposed expansion. The land document is attached as

Annexure-2.

3.7.2 EQUIPMENT

The list of equipment’s required for the proposed expansion project are as follows:

Table 3.4: List of equipment/machineries

Sr.

No.

Equipments/Machineries Quantity

1 Screw Press 200TPD 01

2 Pressure screen SPS-12 01

3 Couch suction roll 01

4 SR-3600 DR-H Sereies Slitter Rewinder 01

5 Screw Press PFB 750, 60 TPD for ETP sludge 01

6 Vacuum Pump, Model KEN2000 01

7 Screw pump 110 MQ 01

8 Belt Press 25 TPD for ETP sludge 02

9 ETP upgradation 01


3.7.3 POWER REQUIREMENT

The existing power requirement is 4200kVA which will increase ot 4700kVA after the proposed

expansion. It is sourced from Dakshin Gujarat Vij Company Limited. (DGVCL).

Company has obtained CTE for installation of 4.9 MW co-generation power plant with 30 T/hr coal

fired boiler by removing existing 0.5 MW co-generation power plant & using 13 TPH boiler as a stand-

by.

3.7.4 FUEL REQUIREMENT

For existing operations, Coal/Lignite @48 T/day is used as fuel in boiler, Co-generation power plant &

captive power plant. After the proposed expansion, Coal/Lignite @48 T/day for 13 TPH boiler and

Coal: 120 T/day for the 30 TPH boiler will be used as fuel.

3.7.5 WATER REQUIREMENT

Fresh water requirement is 625 kl/day, which will increase to @1260 kl/day after the proposed

expansion. The fresh water is/will be sourced from GIDC water supply department.

Other than general requirement of water in domestic and boiler, it will also be required in process.

The category wise bifurcation of fresh water is given as follows:



Table 3.5: Category wise fresh water requirement

Particulars Existing operation (kl/day) After proposed expansio (kl/day)

Domestic 10.00 10.00

Industrial

Process 564.00 680.00

Boiler 45.00 110.00

Cooling makeup (for Turbine) 6.00 460.00

Sub: Industrial 615.00 1250.00

Total 625.00 1260.00


3.7.6 MAN-POWER REQUIREMENT

In existing operations, the man-power requirement is 245 and after the proposed expansion project it

will be 272 person. The man-power will be employed locally. The bifurcation of man-power is given as

below:

Table 3.6: Man-power requirement

Phase of project Type of labor No. of workers

(Existing Scenario)

No. of workers

(Proposed Scenario)

During construction Contractual 55 60

During commissioning Contractual

During operations Managerial 25 27

Skilled 70 80

Un-skilled 95 105


3.8 QUANTITY OF WASTE TO BE GENERATED

The quantity wise bifurcation of waste water is provided below table.

Table 3.7: Waste water generation

Particulars Existing operation (kl/day) After proposed expansion (kl/day)

Domestic 8.00* 8.00**

Industrial

Process 6600.00^ 7225.00^^

Boiler blow down 10.00ª 15.00 ª ª

Cooling blow down 1.00£ 60.00££

Sub-total: Industrial 6611.00 7300.00

TOTAL 6619.00 7308.00

Note:

1)* 8 kl/day (To Septic tank/Soak pit system), ** 8 kl/day (To Septic tank/Soak pit system)

2) ^ 5290 kl/day (Recycled through save-all) 1195 kl/day (Recycled after primary treatment) 115 kl/day (Sent

to CETP after secondary treatment), ^^ 5660 kl/day (Recycled through save-all) 1280.00 kl/day (Recycled

after primary treatment) 285.00 kl/day (Sent to CETP after secondary treatment)

3) ª 10.00 kl/day (Sent to CETP after secondary treatment), ªª 15.00 kl/day (Sent to CETP after secondary

treatment)

4) £ 1.00 kl/day (Recycled to Process), ££ 60.00 kl/day (Recycled to Process)


The water balance diagram for existing scenario is provided in figure 3.4 and for proposed scenario is

provided is provided in figure 3.5.



Figure 3.4: Water balance diagram for existing scenario


Figure 3.5: Water balance diagram for proposed scenario


3.8.1 WASTE WATER GENERATION & MANAGEMENT

The domestic waste water generated is/will be disposed to soak pit/septic tank system. The industrial

effluent after confirming the CETP norms is/will be discharged to CETP, Vapi.

3.8.2 WASTE WATER CHARACTERISTICS

The expected characteristics of composite waste water are as follows:



Table 3.8: Expected characteristics of composite waste water

Sr.

No.

Parameters Expected Characteristics

Existing –

Untreated

Proposed –

Untreated

Treated (CETP

norms)

1. pH 6.5 to 7.5 6.5 to 7.5 6.5-8.5

2. Total dissolved solids (TDS) 2800-3000 2800-3000 2100

3. COD 6000-7000 6000-7000 1000

4. BOD 2000-3000 2000-3000 400

5. Oil & Grease 9-10 9-10 10

Note: All the values are in mg/l except pH.


3.8.3 WASTE WATER TREATMENT & DISPOSAL

The domestic waste water generated is/will be disposed to soak pit/septic tank system.

In existing operations, the waste water from process and boiler blow down is diverted to ETP. After

the treatment in the ETP treated water @6485kl/day for existing and @6940kl/day for proposed is/will

be recycled/reused to process, and rest of the treated wastewater @125kl/day for existing and @326

kl/day after the proposed expansion after confirming the CETP norms is/will be sent to CETP, Vapi.

The effluent from all the process streams is taken to the SAVE ALL SYSTEM where pressurized air is

injected and the lighter particles are carried to the top. The floating sludge from the top of the SAVE

ALL SYSTEM is taken to the belt press filter at the bottom of the SAVE ALL SYSTEM where the

sludge is dewatered totally and dry sludge is either used in sundry board manufacturing or is sold to

the actual users. The clear effluent from the top of the SAVE ALL SYSTEM is taken to the primary

clarifier for solids removal. The sludge from the hopper is sent to the pulp mill for reuse in plant and

the bottom of the clarifier is sent to the Decanter for dewatering. Some part of clarified effluent from

the primary clarifier is passed through the sand filters in series and taken into backwater tank and

reuse in process and some part of clarified effluent from primary clarifier is taken into aeration tank for

biological treatment. In aeration tank biodegradation takes place in the presence of active biomass

and dissolved oxygen, which is provided by means of surface aerator. Here, Urea and DAP is added

as nutrients to biomass. Now the overflow of the aeration tank is diverted into the secondary clarifier

for biomass separation. Settled biomass sludge from the bottom of the secondary clarifier is recycled

back into the aeration tank to maintain biomass ratio in the aeration tank and excess biomass sludge

is diverted to the sludge drying beds for dewatering, The treated effluent from secondary clarifier is

discharged into the GIDC underground drainage system, which leads to the CETP.

After the proposed expansion project, necessary modifications will be done in the existing ETP for the

treatment of waste water.

The flow diagram of ETP is provided in figure 3.6 and the details of each unit is given in table 3.9.



Figure 3.6: Flow diagram of ETP


Table 3.9: Details of ETP units

Sr.

No.

Description Capacity

1 Belt filter press-1 25mq/hr

2 Belt filter press-1 25mq/hr

3 Primary Clarifier 650 mq

4 Filtrate water storage tank ( Sump-1) 50 mq

5 Saveall 120mq

6 Sludge storage chest ( Sump-2) 50 mq

7 Aeration tank 750 mq

8 Secondary Clarifier 50 mq (Source: M/s. Shah Pulp & Paper Mills Ltd.)

3.8.4 AIR EMISSIONS & CONTROL

The details of air emissions are given as follows:

3.8.4.1 PROCESS EMISSION

There is/will be no process emissions after the proposed expansion project.

3.8.4.2 UTILITY EMISSION

In existing operations, one boiler having capacity 13 TPH is installed. Coal/Lignite @48 T/day is used

as fuel. After the proposed expansion new 30 TPH boiler will be installed and the existing 13 TPH

boiler will be kept stand-by. Coal @120 T/day for 30 TPH boiler and is used as fuel and coal/lignite

@48 T/day for 13 TPH boiler.



The details of utility emissions are provided in table 3.11.

Table 3.10: Details of utility emissions

Installation Fuel Fuel

Consumpti

on

Details of

stack

Pollution

Parameters

Emission Rate

APCD

Existing installation

Boiler-1 with

0.5MW

Turbine:

Capacity 13

T/hr

Coal/

Lignite

48 T/day Stack height:

30m

PM 150 mg/Nm3 ESP

SO2 100 ppm

NO2 50 ppm

Proposed installation*

Boiler-2

With 4.9MW

Turbine:

Capacity 30

T/hr

Coal

Coal/Lignite

(stand-by)

120 T/day

48 T/day

(stand-by)

Stack height:

50 m

PM 150 mg/Nm3 ESP

SO2 100 ppm

NO2 50 ppm

Note:

1. *CTE has been obtained.

2. Existing 13 TPH boiler will be kept as stand-by after the installation of 30 T/hr Boiler


3.8.4.3 FUGITIVE EMISSION

Minor quantity of fugitive emission is/will be occurred by the expansion project.

3.8.5 HAZARDOUS/NON-HAZARDOUS. WASTES MANAGEMENT

Hazardous and non-hazardous is/will be generated from the proposed expansion project. All such

types of wastes is/will be stored in the proper designated storage areas. The details of hazardous

and non-hazardous waste generation and its management are provide in table 3.12.

Table 3.11: Hazardous and non-hazardous waste generation and its management

Sr.

No.

Type of

waste

Category Quantity Mode of disposal

Existing After proposed

expansion

1. ETP

waste

34.3 40.00 T/annum. 44.00 T/annum. Collection, storage,

transportation, disposal at

TSDF-VWEMCL.

2. Deinking

sludge

-- 8600.00

T/annum

14000 T/annum Collection, storage,


TSDF-VWEMCL.

3. Plastic

waste

(Non-

recyclable

waste)

21.1 5040 T/ annum. 5498 T/ annum. Collection, Storage,

Transportation, Disposal by

co-incineration at Ambuja

cement Ltd. Or disposal at

TSDF site, Vapi.

4. Used oil 5.1 0.25 kl/ annum. 0.27 kl/ annum. Collection, storage,

Transportation, sold to

registered re-refiners.

5. Discarded

containers

/ bags

33.3 200 Nos/annum. 218 Nos/

annum.

Collection, storage,

transportation sold to

authorized scrap vendors.



Sr.

No.

Type of

waste

Category Quantity Mode of disposal

Existing After proposed

expansion

6. Used

resin

34.2 As & when

generated

As & when

generated

Collection, storage,


TSDF-VWEMCL, Vapi.


3.8.6 NOISE CONTROL

Presently there is no major noise generation. Industry has taken adequate measures for control of

noise levels and also regular maintenance is carried out. After the installation of 4.9 MW turbine,

acoustic enclosures and sturdy non-vibrating foundation with necessary paddings will be provided to

control the nosie generation.

3.9 HEALTH AND SAFETY MEASURES

The details of safety measures provided and safety procedure followed at our unit are as below:

Table 3.12: Safety details

Sr. No.

Particulars Remarks/ Details

1. Safety Officer Safety officer is available

2. Manual call bells Yes

3. Emergency Control Room At main gate security office

4. Emergency Sirens Yes

5. Assembly Point 1 point

6. Ambulance Point Near main gate

7. First Aid facility Provided at prominent places by trained persons.

8. Personal Protective Equipments

Hand gloves, gum boots, safety shoes, dust masks, safety goggles, and apron.

9. Health Check ups Regular health checkups at every six months.

10. Regular Training Provided

11. Safety & Health Records Maintained as per Factory Act.

12. MSDS MSDS available at prominent places for ready references. (Source: M/s. Shah Pulp & Paper Mills Ltd.)

3.10 ENVIRONMENTAL HEALTH & SAFETY CELL

The company promotes environmental protection and insists on complying with all applicable

environmental regulations. Every measure is taken for the prevention of pollution.



Figure 3.7: Organogram of EHS management cell


3.11 POST PROJECT MONITORING PLAN

The proposed post-project monitoring plan to ensure effective implementation of EHS Management

system is given below:

Table 3.13: Environmental Monitoring Plan

Component Parameter Frequency

Air – Ambient SO2, NO2, PM10, PM2.5 Monthly

Noise monitoring Noise levels in decibels Monthly at all noise generating equipments & plant boundary

Work place monitoring

PM, SO2, NO2. Monthly

Haz. Waste management

Maintaining records of generation, receipt & disposal in Form-3

Daily

Filing of annual returns in Form-4 for Haz. Waste handling

Every year by 31st Jan

Maintaining records of transportation in Form-9 While sending for disposal

Submission of returns of used oil in Form-13 Every year by 31st Jan

CC&A Obtaining consent to operate (and renewal) under Air & Water Acts and authorization under HW rules.

Before expiry of validity

Water cess Filing of annual returns for cess incurred on water consumption

Every year by 30th Sept

Environmental Statement

Submission of audit statement in form-V Every year by 30th Sept

Compliance of EC conditions

Submission of compliance reports Half yearly on 1st June & 1st Dec


General Manager

Head Environment

Department

ETP Manager

ETP Operator ETP Chemist ETP Supervisor

Workers



CHAPTER – 4

SITE ANALYSIS

4.1 CONNECTIVITY

This proposed expansion project is located at Plot No. 97, GIDC Estate, Vapi 396 195 Dist. Valsad.

The land and infrastructure is already available. And the raw material is easily available through the

easy transport via road connectivity. The nearest railway station is Vapi railway station which is at

approx. 2 km radial distance from the site.

4.2 LANDFORM, LAND USE & LAND OWNERSHIP

The existing land is about 28279 m2. No additional land will be required for the proposed expansion

project. The existing plot is located in the industrial estate of GIDC, Vapi designated for the industrial

purpose. Hence, there will be no change in the land-use pattern of the area. The land is owned by the

company.

4.3 TOPOGRAPHY

The topography of the Vapi is relatively flat terrain with series of deeply incised creeks of river. The

site is relatively flat.

4.4 SALIENT FEATURES

The salient features of the project site is provided in table 4.1.

Table 4.1: Salient Features of the Project Site

Particulars Details

Co-ordinates Latitude: 20°21'38.35", Longitude: 72°55'26.33"

Village/Town Vapi

Taluka/ Tehsil Vapi

District Valsad

Nearest Water body River Damanganga ( 2.62 km - SW)

Nearest Highway NH-08 (0.5 km N)

Nearest Railway station & Railway

line

Vapi Railway station (2.01 km NW)

Nearest Airport/ Airbase Surat Airport (86.18 km NW)

State/ National borders UT of Daman ( 3.65 km NW)

Protected Area/ Sanctuaries None within 10 km radial periphery

CRZ applicability No

Seismicity Seismic Zone – III (Moderate)

Note: All the above mentioned distances are the aerial distance from the project site.

4.5 EXISTING INFRASTRUCTURE

The proposed expansion is to be carried out in the existing site. The company has the required infrastructure.

4.6 SOIL CLASSIFICATION

The catchment area of the proposed project site consists of flat topped, highly dissected plateaus and

dyke ridges running in a west to east direction. The Main River (Daman Ganga) in the catchment area

flows in incised meanders forming steep geomorphologic ally ‘V’ shaped valleys with steep sides. The

entire catchment has a rectangular and trellis pattern of drainage depicting the influence of the

structures on the drainage development. The piedmonts at the base of the steep plateaus and dyke



ridges are covered with thin soils, which support agriculture in very few areas. The river valley,

wherever flat, has good quality soil and is mostly cultivated based on the availability of water. The

river valley fills with thick alluvium provides the only area for cultivation.

4.7 CLIMATE & METEROLOGY

The year can be divided into four seasons. Climate is warm and dry from mid-March to June, during season of summer, climate remains warm and dry, while during rainy season, from mid-June to end of September, climate is humid and pleasant. From October to November mild warm climate prevails, and from December to February climate is cold.

The Table 4.2 indicates the summary of meteorological pattern at the nearest observatory of IMD,

Bharuch published by IMD.

Table 4.2: Summary Meteorological Data at nearest IMD Station –Dahanu

Month Temperature (oC)

Relative Humidity

(%)

Cloud Cover (Oktas)

Mean Wind

Speed (km/hr)

Pre-dominant

Wind Direction

Rainfall (mm)

Max. Min. Mor. Eve. Max. Min.

January 32.5 13.2 66 67 1.1 1.0 9.5 N 0.1

February 33.1 14.0 64 66 0.9 0.8 10.1 NW 0.1

March 35.2 17.1 66 64 1.2 0.9 11.1 NW 0.1

April 35.8 21.2 73 67 1.9 1.2 12.1 W 0.2

May 35.7 24.1 75 70 3.2 2.1 14.1 W 9.4

June 35.3 23.4 83 77 5.7 5.4 16.3 SW 400.3

July 32.8 23.1 88 84 6.8 6.8 20.2 SW 665.8

August 31.6 23.2 88 83 6.9 6.7 20.4 SW 464.2

September 32.6 22.5 86 77 5.2 4.8 12.3 W 254.2

October 35.5 20.2 75 70 2.4 2.2 8.5 NW 35.3

November 35.1 17.3 66 69 1.6 1.7 8.1 E 18.9

December 33.8 14.5 66 70 1.4 1.5 8.3 E 2.8

Seasonal Average Values

Period Temperature (oC)

Relative Humidity (%)

Cloud Cover (Oktas)

Mean Wind

Speed (km/hr)

Avg. PDW Direction

Total Rainfall

(mm) Avg. Max.

Avg. Min.

Avg. Mor.

Avg. Eve.

Avg. Max.

Avg. Min.

Summer 35.6 26.2 71 67 2.1 1.4 12.4 W 9.7

Winter 33.1 13.9 65 68 1.1 1.1 9.3 E 3.0

Monsoon 33.0 23.0 87 80 6.1 5.9 17.3 SW 1784.5

Post monsoon 35.3 18.7 70.5 69.5 2 2 8.3 NW/E 54.2

Note: Winter: December, January & February, Summer: March, April & May, Monsoon: June, July, August & September, Post monsoon: October & November

(Source: Climatological tables of observations in India (1961-1990), IMD)

4.7.1 TEMPERATURE

The summer season from March to May is a one of continuous increase in temperatures which decreases during monsoons, increases slightly during the post-monsoon season and again decreases during the winter. May is generally the hottest month with the mean daily maximum temperature recorded at 35.70C and mean daily minimum temperature recorded at 24.10C. January is the coldest month with the mean daily maximum temperature as 32.50C and mean daily minimum temperature observed as 13.20C.

4.7.2 HUMIDITY

The climate of the region is characterized by a humid summer because of the closeness to coastline. Humidity is usually high during the monsoon months, with average relative humidity generally exceeding 80%. Humidity decreases gradually during the post-monsoon months and for rest of the year i.e. the period of December to April, the average relative humidity ranges around 50-70%.



4.7.3 RAINFALL

About 95% of the annual rainfall is received during the southwest monsoon season i.e. from June to September, July being the month with highest rainfall. The total annual rainfall observed from the historical data of year 1951-1980 is 1784.5 mm.

4.7.4 WIND PATTERN

The annual resultant vector for wind direction shows winds blowing from WSW. During summers and monsoon, the winds blow mostly from the sea i.e. the SW or WSW direction. The post-monsoon & winter seasons experience a change in direction, with the winds blowing from NE, ENE or NNE. The wind speed is high during monsoon and post monsoon seasons, slightly moderate during summer and winter seasons.

4.8 SOCIAL INFRASTRUCTURE

The infrastructure available in the study area denotes the economic well being of the Pardi Taluka. There are about 70 villages and 8 Towns in the Pardi Taluka.

4.8.1 EDUCATIONAL FACILITIES

As per census of India, 150 Primary school, 20 Secondary School, 11 senior secondary school. There were no Middle School & Training institute found in 70 villages. The female literacy rate is 43%.

4.8.2 MEDICAL FACILITIES

Out of the 70 villages, hospitals were available in 2 villages, Primary health centers in 6 villages and Primary health sub center in 58 villages. There was no Dispensary found in 70 villages.



CHAPTER – 5

PLANNING BRIEF

5.1 PLANNING CONCEPT

The proposed expansion project is located at Plot No. 97, GIDC Estate, Vapi 396 195 Dist. Valsad.

The nearest city is Vapi which is a Vapi is the largest industrial area in Asia in terms of small-scale

industries, dominated by chemical industry plants. Major raw materials will be sourced locally. The

region is well planned with all the basic infrastructural facilities like internal roads, water supply,

arrangements for power, streetlights, solid waste disposal sites etc.

5.2 POPULATION PROJECTION

The average household size is around 4 to 5.

Table 5.1: Distribution of population

Sr. No.

Particulars Observed values in 10 km Radius

1 Total Population 585054

2 No. of Households 134542

3 Avg. household size (persons) 4-5

4 Male population 311336

5 Male population (in %) 53.2%

6 Female population 273718

7 Female population (in %) 46.8%

8 Sex ratio 879 (Source: Primary Census Abstract – Census of India, 2011)

5.3 AREA STATEMENT

The total area of the plot is 39113.84 m2 out of which Greenbelt area of theplant is. 8201.75 m2 which

is approx. 20 %. The bifurcation of the same is given below in table no. 5.2.

Table 5.2: Area Statement

Particulars Unit Area

Built up area m2 17513.05

Open area m2 13399.04

Greenbelt area m2 8201.75

Total Area m2 39113.84 (Source: M/s. Shah Pulp & Paper Mills Ltd.)

5.4 ASSESMENT OF INFRASTRUCTURE DEMAND (PHYSICAL & SOCIAL)

For proposed expansion project the company will not acquire any machinery so there will be no

demand of change in physical infrastructure and social infrastructure. As manpower requirement for

the proposed project shall be locally fulfilled, employment generation will lead to additional benefits to

social infrastructure.

5.5AMENITIES/FACILITIES

5.5.1 DRINKING WATER FACILITIES

Tap water is available in 69 villages as per the Census 2011. 67 had Wells, 39 villages had tanks and 69 had hand pumps. 53 Villages had River/Canal passing. Power supply was also available in all the villages.



5.5.2 POWER SUPPLY FACILITIES

As per census 2011, all the villages have power supply facilities in the Pardi Taluka.

5.5.3 COMMUNICATION & BANKING FACILITIES

Out of the 70 villages, Post Office is available in 1 village, telephone facility exist in all the villages as

per the 2011 census.

5.5.4 TRANSPORT FACILITIES

Bus service is available in the Pardi Taluka and is the most preferable mode of transport in the Pardi Taluka. The villages are well connected with the State Highways. National Highway-8 also passes from Vapi. The Western railway line between Bombay to Ahmedabad passes from the Pardi Taluka and Vapi Town has a railway station on the same.



CHAPTER – 6

PROPOSED INFRASTRUCTURE

6.1 INDUSTRIAL AREA

The total area of the plot is 39113.84 m2 out of which 17513.05 m2 is the buildup area.

6.2 RESIDENTIAL AREA

In the said proposal no residential area has been proposed for workers and/or for staff.

6.3 GREENBELT

Maximum open land will be allotted for green belt development. If required, experts will also be

consulted for selection of species for the development of the greenbelt. Total greenbelt area is

Approx 20 % of total plot area and Approx 60% of the total open land area.

6.4 SOCIAL INFRASTUCURE

Existing infrastructure will be sufficient to accommodate the existing load from the proposed project

which is very low.

6.5 CONNECTIVITY

This proposed expansion project is located at Plot No. 97, GIDC Estate, Vapi 396 195 Dist. Valsad.

The site is 0.47 km from National highway-8. The land and infrastructure is already available. And the

raw material is easily available through the easy transport via road connectivity. The nearest railway

station is Vapi railway station which is 2.01 km and Daman Airport is 11.49 km from the project site.

6.6 DRINKING WATER MANAGEMENT

The source of drinking water is/ will be GIDC water supply.

6.7 SEWERAGE SYSTEM

Domestic waste water generated from the existing and proposed expansion is/will be disposed of through soak pit/septic tank.

6.8 INDUSTRIAL WASTE MANAGEMENT

Industrial Effluent will be treated in the Effluent Treatment Plant at the site and final effluent is/will be

sent to CETP, Vapi after confirming the CETP inlet norms. Details are explained in Chapter 03,

Section 3.8.3

6.9 SOLID WASTE MANAGEMENT

Hazardous wastes generated will be in the form of ETP waste, Used oil, Discarded containers, Non-

recyclable plastic waste, Used resin. Company will provide adequate storage area for proper storage

of wastes. Details of solid waste generation are given in table 3.12.

6.10 POWER REQUIREMENT & SOURCE OF SUPPLY

The power requirement for proposed expansion4700 kVA which will be sourced from Gujarat

Electricity Board.



CHAPTER – 7

REHABILITATION &RESETTLEMENT (R &R) PLAN

7.1 POLICY TO BE ADOPTED

The proposed expansion project is to be developed in the land designated for industrial use. Hence,

no displacement of any population is proposed for the project. Therefore, detailed Social Impact

Assessment studies or R&R action study has not been proposed.



CHAPTER – 8

PROJECT SCHEDULE & COST ESTIMATES

8.1 TIME SCHEDULE OF THE PROJECT

The installation/ construction will be started after getting approval for Environmental Clearance and NOC from authorities.

8.2 ESTIMATED PROJECT COST

Environment Protection has also been considered in planning the cost projection. Green belt

development is also considered. The estimated project cost will be approximately 50 Crores.

Table 8.1: Total Capital Cost Projection

Sr. No. Purpose Total cost (Rs. In lakhs)

1. Land 0.00

2. Plant & Machinery 800.00

3. Building 0.00

4. Electrification and Laboratory set up 0.00

5. Effluent Treatment Palnt 215

6. Green belt development 25

TOTAL 1040.00

Table 8.2: Total Capital Cost Power plant

Sr. No. Purpose Total cost (Rs. In lakhs)

1 Boiler 900.00

2 Turbine 750.00

3 DM Plant 60.00

4 ESP 250.00

5 Building 300.00

6 Ash Handling 60.00

7 Coal Handling 100.00

8 Coal yard 150.00

9 PLC/DCS 80.00

10 Instrumentation 100.00

11 Electrical 200.00

12 Transportation 100.00

13 Steam Pipe line and PRDS 100.00

TOTAL 3150.00

Table 8.3: Recurring cost provision for EHS

Sr. No. Purpose Provision per Annum (Rs. in lakhs)

1. ETP (Operation & maintenance) 30.00

2. Greenbelt maintenance 5.00

3. Environment & Safety Management System 10.00

TOTAL 45.00



CHAPTER – 9

ANALYSIS OF PROPOSAL 9.1 FINANCIAL & SOCIAL BENEFITS

M/s. Shah pulp and paper mills Ltd. is a unit manufacturing paper from waste paper based paper mills

located at Plot no. 97, G.I.D.C Estate, Vapi-396 195. M/s. Shah pulp and paper mills Ltd. has

proposed the project for expansion of production for manufacturing of paper from waste paper based

paper mills at its existing unit.

Annexure

Annexure-1 Existing CC&A

A1

Annexure-2 Granted NOC

A3

Annexure-2 Land Allotment Letter

A6

PROJECT PRE FEASIBILITY REPORT - Welcome to...

Documents

Transcript of PROJECT PRE FEASIBILITY REPORT - Welcome to...