of M/s. PHILODEN AGROCHEM PVT. LTD. - Gujarat Pollution ...
of M/s. PHILODEN AGROCHEM PVT. LTD. - Gujarat Pollution ...
of M/s. PHILODEN AGROCHEM PVT. LTD. - Gujarat Pollution ...
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EXECUTIVE SUMMARY OF EIA<br />
(ENGLISH)<br />
<strong>of</strong><br />
M/s. <strong>PHILODEN</strong> <strong>AGROCHEM</strong> <strong>PVT</strong>. <strong>LTD</strong>.<br />
SURVEY NO. 73, BEHIND GEB SUB‐STATION,<br />
VILLAGE – KARKHADI, TAL. PADRA,<br />
DIST: VADODARA.
INTRODUCTION<br />
EXECUTIVE SUMMARY OF EIA<br />
• M/s. Philoden Agrochem Private Ltd. is manufacturers & marketer <strong>of</strong> Polymer Solvent, Dyes<br />
& Solvent soluble dyes for coating applications. Mr. Mahesh Patel is Managing Director <strong>of</strong><br />
Philoden Agrochem Pvt. Ltd. Existing unit <strong>of</strong> dyes and pigments <strong>of</strong> M/s. Philoden Agrochem<br />
P. Ltd. is located at Survey No. 73, Village : Karkhadi, Tal: Padra, Dist: Vadodara, <strong>Gujarat</strong><br />
state. The plant is located near State Highway SH 6 at about 6.72 km South East and railway<br />
route is about 9 km South East. The plant is about 40 km North East away from Vadodara.<br />
• Its formation was a result <strong>of</strong> coming together <strong>of</strong> experienced technocrats having more than<br />
35 years <strong>of</strong> experience in manufacturing & marketing <strong>of</strong> solvent dyes.<br />
• The Company commenced operations in year August, 2003 in Vadodara, State <strong>of</strong> <strong>Gujarat</strong><br />
(India).<br />
• In short span <strong>of</strong> time, Philoden has gained sizable market share <strong>of</strong> Polymer Soluble Dyes &<br />
Solvent Soluble Dyes in domestic markets.<br />
• The company has well equipped production facilities which are managed by dedicated,<br />
qualified & skilled persons.<br />
• The company has a manufacturing capacity <strong>of</strong> 300 MT per annum, and processes<br />
capabilities to manufacture all types <strong>of</strong> Solvent Dyes.<br />
Company proposes to expand existing manufacturing activities by adding new products by<br />
using existing as well as additional manufacturing and infrastructure facilities. Total cost <strong>of</strong> the<br />
proposed project is 315 Lacs.<br />
This facility is engaged in development <strong>of</strong> new products. A team <strong>of</strong> highly qualified scientists<br />
and technicians is engaged in this process. Project Site having the advantage <strong>of</strong> close proximity<br />
to Vadodara, the commercial city <strong>of</strong> India. Due to National Highway No. 8, the city is well<br />
connected by road and rail to rest <strong>of</strong> India. Development <strong>of</strong> Communication systems is good in<br />
the region due to proximity to Vadodara. A source <strong>of</strong> water in the region includes Mahi River
and ground water resources. Secured land fill site is operated by M/s. Nandesari Enviro Control<br />
Ltd. (NECL), Nandesari is about 29 km away from project site.<br />
PROJECT DETAILS<br />
LIST OF PRODUCTS ALONG WITH THEIR PRODUCTION CAPACITY (EXISTING & PROPOSED)<br />
Sr.<br />
No.<br />
Existing<br />
Name <strong>of</strong> Product Quantity (MT/Month)<br />
Existing Proposed After Total<br />
Proposed Expansion<br />
1. Benzathrone 3.1 ‐‐ 3.1<br />
2. Pigment‐Red‐ “GB” 3.55 ‐‐ 3.55<br />
3. Pigment‐Yellow‐ “GB” 8.35 ‐‐ 8.35<br />
4. Pigment‐Orange‐ “G” 01 ‐‐ 01<br />
5. Pigment‐Brown RM/Dark<br />
Brown‐R<br />
6. Pigment‐Violet BA/Cadbury<br />
Violet R<br />
0.5 ‐‐ 0.5<br />
01 ‐‐ 01<br />
7. Pigment‐Green BP 01 ‐‐ 01<br />
8. Pigment‐Black RE 1.5 ‐‐ 1.5<br />
Proposed<br />
9. Solvent Dyes<br />
Solvent Blue 35<br />
Solvent Blue 104<br />
Solvent Blue 122<br />
Solvent Green 3<br />
Solvent Orange 60<br />
Solvent Orange 86<br />
Solvent Red 52<br />
‐‐<br />
40<br />
40
Solvent Red 135<br />
Solvent Red 168<br />
Solvent Red 195<br />
Solvent Red 207<br />
Solvent Violet 13<br />
Solvent Violet 14<br />
Solvent Yellow 33<br />
Solvent Yellow 157<br />
Solvent Yellow 163<br />
10. Solvent Dyes<br />
Solvent Black 27<br />
Solvent Orange 58<br />
Solvent Red 127<br />
Solvent Red 160<br />
Solvent Yellow 82<br />
Solvent Yellow 21<br />
11. Solvent Dyes<br />
Solvent Blue 98<br />
Solvent Blue 128<br />
Solvent Green 33<br />
Solvent Red 19 E<br />
Solvent Red 24<br />
Solvent Yellow 107<br />
Solvent Yellow 124<br />
12. Pigment<br />
Pigment Blue 60<br />
Pigment Orange 43<br />
Pigment Orange 70<br />
‐‐<br />
‐‐<br />
40<br />
50<br />
40<br />
50
Pigment Yellow 155<br />
Pigment Yellow 180<br />
Pigment Yellow 188<br />
Pigment Yellow 196<br />
Pigment Red 122<br />
Pigment Red 168<br />
Pigment Red 170<br />
Pigment Red 176<br />
Pigment Red 202<br />
Pigment Violet 19<br />
Pigment Yellow 147<br />
13 Optical Brighteners<br />
Optical BR 184<br />
Optical BR 199<br />
Optical BR 351<br />
Total 20 205 225<br />
POWER REQUIREMENT<br />
The total power requirement at M/s. Philoden Agrochem Private Ltd. after proposed will be<br />
met through 100 KW fulfilled by GEB and D.G. set <strong>of</strong> 125 KVA will be installed for used in<br />
emergency only.<br />
FUEL<br />
Agro Waste: 0.7 MT/Day (Existing)<br />
Agro Waste: 2.1 MT/Day additional & Natural Gas: 500 SCM/Hr (Proposed)<br />
Agro Waste: 2.8 MT/Day (Total)<br />
‐‐<br />
‐‐<br />
40<br />
20<br />
15<br />
40<br />
20<br />
15
AIR ENVIRONMENT<br />
There are sources <strong>of</strong> air pollution at M/s. Philoden Agrochem Pvt. Ltd., flue gas through boiler<br />
stack, stacks attached to Incinerator.<br />
DETAILS OF SOURCE OF EMISSION (EXISTING & PROPOSED)<br />
Sr.<br />
No.<br />
Source <strong>of</strong><br />
emission<br />
1 Boiler‐I<br />
(Existing)<br />
2 Boiler‐II<br />
(Proposed)<br />
3 Incinerator<br />
(Proposed)<br />
Type <strong>of</strong><br />
emission<br />
PM, SO2,<br />
NOx<br />
PM, SO2,<br />
NOx<br />
PM, SO2,<br />
NOx<br />
Stack<br />
Height (m)<br />
11<br />
Stack<br />
dia. (m)<br />
<strong>Pollution</strong> control<br />
equipment<br />
0.4 Cyclone Separator with<br />
Bag Filter<br />
30 1.0 Cyclone Separator with<br />
Bag Filter<br />
Fuel name<br />
Agro<br />
Waste<br />
Agro<br />
Waste<br />
30 1.2 Scrubber NG<br />
BASELINE ENVIRONMENTAL STATUS<br />
The dispersion <strong>of</strong> pollutants in the atmosphere is a function <strong>of</strong> several meteorological<br />
parameters viz. temperature, wind speed and direction, mixing depths, inversion level, etc. The<br />
ambient air samples were collected and analyzed for SPM, PM2.5, PM10, SO2, NOx, O3, Pb, CO,<br />
NH3, C6H6, Benzo (a) Pyrene (BaP) particulate phase only, As, as Ni, HC and VOCs for<br />
identification, prediction, evaluation and assessment <strong>of</strong> potential impact on ambient air<br />
environment. A number <strong>of</strong> models have been developed for the prediction <strong>of</strong> pollutant<br />
concentration at any point from an emitting source.<br />
AMBIENT AIR QUALITY MONITORING<br />
Ambient Air Quality Monitoring (AAQM) has been carried out at seven locations during summer<br />
season (March to May, 2011).<br />
At different AAQM the results were found as ranged for PM2.5 (21‐53.7 µg/m 3 ), for PM10 (62.7‐<br />
96.4 µg/m 3 ), for SO2 (11.6‐36.1 µg/m 3 ), for NOx (22.6‐48 µg/m 3 ), for Ozone (4.06‐8.75 µg/m 3 ),
for Lead (ND), for Benzene (2.21‐3.70 µg/m 3 ), for Benzo (a) pyrene (BaP) particulate phase only<br />
(ND‐0.86 µg/m 3 ), for Nickel (ND‐15.56 µg/m 3 ), for NH3 (ND‐3.6 µg/m 3 ), for VOCs (0.2‐1.3 ppm),<br />
for HC (0.10 to 0.46 µg/m 3) . CO, As were not detected at any locations.<br />
WATER ENVIRONMENT<br />
In existing scenario, the total water requirement at M/s. Philoden Agrochem Private Ltd. is 16<br />
m 3 /day which is met through ground water supply. After proposed expansion, the total water<br />
requirement is 176 m 3 /day and additional water requirement shall also meet through ground<br />
water supply. The baseline water quality status in the region is established by analyzing surface<br />
water and ground water.<br />
In existing scenario, waste water generation at M/s. Philoden Agrochem Private Ltd. is 5.7<br />
m 3 /day which is treated in existing ETP and treated effluent is sent to M/s. EICL, Umaraya for<br />
further treatment and final disposal. After Proposed Expansion, 5.7 m 3 /day effluent will be<br />
treated in existing ETP and treated effluent is sent to M/s. EICL, Umaraya for further treatment<br />
and final disposal. Domestic wastewater is disposed in Septic Tank/Sock Pit. And proposed<br />
waste water generation will 113 m 3 /day. The effluent will be treated in ETP and treated effluent<br />
stream will be segregated in to high and low COD stream. The high COD effluent shall be sent to<br />
incineration within premises. The low COD effluent shall be sent to RO and final treated<br />
effluent will be reused.<br />
Note: The unit possess a membership to the M/s. Enviro Infrastructure Control Ltd., Umaraya.<br />
However as per the current scenario, the state pollution control board does not allow<br />
additional effluent load to EICL (the overloaded system <strong>of</strong> ECP), the unit proposes to go for<br />
zero discharge by installing an RO plant and Incinerator and will operate the system till the<br />
ECP accepts additional load <strong>of</strong> effluent. As soon as ECP starts accepting additional load <strong>of</strong><br />
effluent, we shall dispose our effluent to M/s. Enviro Infrastructure Control Ltd., Umaraya.
BASELINE GROUND WATER QUALITY<br />
pH – 7.52 to 8.10, Turbidity – 0.22 to 3.6 NTU, TDS – 805 to 4553 mg/L, TSS – 6.0 to 66.0 mg/L,<br />
DO – 6.60 to 7.00 mg/L, COD – 0.66 to 13.66 mg/L, BOD3 ‐ 0.18 to 4.83 mg/L, Total Alkalinity –<br />
410 to 620 mg/L, Total Hardness – 475.2 to 1890.4mg/L, Calcium Hardness – 185.9 to 557.8<br />
mg/L, Chlorides – 128.1 to 2089.3 mg/L, Sulphates – 42.4 to 545.5 mg/L, Calcium – 74.5 to<br />
223.6 mg/L, Magnesium – 57.7 to 338.9 mg/L.<br />
BASELINE SURFACE WATER QUALITY<br />
pH – 7.37 to 8.51, Turbidity – 17.0 to 76.0 NTU, TDS – 693.5 to 29200 mg/L, TSS – 26.0 to 564<br />
mg/L, DO – 5.4 to 6.8 mg/L, COD – 34.5 to 145.4 mg/L, BOD3 – 4.6 to 22.6 mg/L, Total Alkalinity<br />
– 260 to 410 mg/L, Total Hardness – 289.2 to 6249.7 mg/L, Calcium Hardness – 144.6 to 1115.6<br />
mg/L, Chlorides – 147.8 to 19118.9 mg/L, Sulphates – 8.18 to 3257.6 mg/L, Calcium – 58.0 to<br />
447.1 mg/L, Magnesium – 35.1 to 1247.6 mg/L.<br />
NOISE ENVIRONMENT<br />
The objective <strong>of</strong> the noise pollution survey around the project site was to identify existing noise<br />
sources and to measure background noise levels. The study was carried out in the following<br />
steps:<br />
• Reconnaissance<br />
• Identification <strong>of</strong> noise sources and measurement <strong>of</strong> noise levels<br />
• Measurement <strong>of</strong> noise levels due to transportation<br />
• Community noise levels<br />
BASELINE NOISE LEVEL<br />
The noise level measured in study area at different locations. Noise level measured on project<br />
site was found 45.8‐55.1 dB(A)in daytime and 35.8‐40.6 dB(A) in nighttime.
LAND ENVIRONMENT<br />
Five categories <strong>of</strong> hazardous wastes are generated at M/s. Philoden Agrochem Private Ltd. in<br />
existing scenario and seven categories <strong>of</strong> hazardous wastes will be generated in proposed<br />
scenario. Mode <strong>of</strong> disposal followed is as per HW (Management, Handling and Transboundary<br />
Movement) Third Amendment Rules, 2010 <strong>of</strong> Environment Protection Act, 1986.<br />
In existing scenario, hazardous waste generation is ETP sludge, Spent Solvent, Used Oil,<br />
Discarded Containers and Process Waste. ETP sludge is sent to TSDF <strong>of</strong> NECL, Nandesari for final<br />
disposal. Spent Solvent and Process waste is sent to CHWI <strong>of</strong> NECL for final disposal. Used oil is<br />
sold to register Reprocessor. Discarded Containers are sold to Sold to GPCB authorized dealer<br />
after decontamination.<br />
After proposed expansion, quantity <strong>of</strong> ETP sludge, Spent Solvent, Used oil and Discarded<br />
Containers will be increased and will be disposed in same manner as existing. Additional<br />
hazardous waste generation will be distillation residue, spent carbon. Distillation Residue and<br />
Spent Carbon will be sent to own incinerator plant.<br />
Soil quality monitoring has been carried during summer season at seven locations.<br />
BASELINE STATUS<br />
pH – 7.87 to 8.31, Moisture – 0.50 to 3.08%, Leachate – 10%, Total Hardness – 410.4 to 1067.0<br />
mg/kg, Calcium Hardness – 164.2 to 492.5 mg/kg, Chlorides –62.0 to 634.2 mg/kg, Sulphates –<br />
43.2 to 91.7 mg/kg, Calcium – 35.8 to 197.4 mg/kg, Specific gravity – 1.25 to 1.43 g/cm 3 ,<br />
Porosity – 46.66 to 55.55 %.<br />
ENVIRONMENTAL HAZARD<br />
The project proponent has considered all the safety aspects in planning, designing and<br />
operation <strong>of</strong> the project as per standard practices. Hence, no adverse impact on this account is<br />
anticipated.
Due to coming up <strong>of</strong> industry many changes are expected to occur in the socio – economic<br />
setup <strong>of</strong> the surrounding region. The socio‐economic changes may be beneficial or detrimental.<br />
General trend <strong>of</strong> socio – economic environment due to the project industry is that it increases<br />
the population density within the area and in a few <strong>of</strong> the surrounding villages. This can be<br />
attributed to more job opportunities, direct and indirect, provided by the industry.<br />
Considering the pollution control measures taken by the company environment management<br />
system adopted there is no significant adverse impact on environment.<br />
CUMULATIVE IMPACT CHART<br />
Environmental Parameter Total Cumulative Score<br />
Air Quality 16<br />
Noise and Odor 13<br />
Water Quality 11<br />
Land Requirement 11<br />
Infrastructure 15<br />
Service 13<br />
Environmental Hazards 22<br />
Housing 2<br />
Terrestrial Ecology/ Land use 8<br />
Socio Economic Status 16<br />
Aquatic Ecology 6<br />
Resource Depletion 6<br />
In general, from all the discussion undertaken above and the Environmental Impact Assessment<br />
study carried out in the winter season regarding the project, it can be concluded that there will<br />
not have any significant negative impact on environment by M/s. Philoden Agrochem Private<br />
Ltd. However, the same will be well within the statutory norms.
GREEN BELT DEVELOPMENT<br />
The main objective <strong>of</strong> the green belt is to provide a barrier between the plant and surroundings<br />
areas. M/s. Philoden Agrochem Pvt. Ltd. has developed green belt within factory premises.<br />
About 7670 sq. meter <strong>of</strong> the total land area is available Company is proposing 2460 sq. meter<br />
for green belt.
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NOx<br />
2 bi[elr -2<br />
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30 1.2 Ak\br n[crl g[s<br />
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hvin&> p\d&PN:<br />
vitivrNmi> p\d&Pki[n&> (vKrivv&> {p\srv&>}, hvimin s>b>F) (v(Bºn GTki[ j[vi k[<br />
uONtipmin, hvin) g(t an[ (dSi, u>DiNY) (mV\N Yv&> (Mixing Depths) (vg[r[n)<br />
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vitivrN)y hvin) g&Nv_ii ckisN)<br />
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j&d) j&d) AYLi[a[ vitivrN)y hvin) g&Nv_ii ckisN), PM10 n) mi#ii 62.7-96.4<br />
miek|i[g\im/m) 3 an[ PM2.5 n) mi#ii 21-53.7 miek|i[ g\im/m) 3 , NOX n) mi#ii 22.6-48<br />
miek|i[g\im/m) 3 an[ SO2 n) mi#ii 11.6-36.1 miek|i[g\im/m) 3 , ai[zi[nn) mi#ii 4.06-8.75<br />
miek|i[g\im/m) 3 , l[Dn) mi#ii ND, b[(ºznn) mi#ii 2.21 – 3.70 miek|i[g\im/m) 3 , b)a[p)n)<br />
mi#ii a[nD) – 0.86 miek|i[g\im/m) 3 , (nkln) mi#ii a[nD) – 15.56 miek|i[g\im/m) 3 ,<br />
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n) mi#ii 0.18 Y) 4.83 m).l)g\im/ (lTrn) myi mil&m pD[l C[. Ti[Tl si[l)D an[ DO<br />
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m).l).g\im/(lTrn) myi mil&m pD[l C[. m[³n[(Symn) mi#ii 57.7-338.9<br />
m).l).g\im/(lTrn) myi mil&m pD[l C[. Ti[Tl hiD
jm)n prni> piN) {srf[S vi[Tr}n) m&LB&t g&Nvti:<br />
jm)n Atr prni piN)ni nm&niai[n) pH 7.37 – 8.51n) myi mil&m pD[ C[. Ti[Tl<br />
(Dzi[ÃD si[l)D an[ Ti[Tl sAp[ºD[D si[l)D an&k|m[ 693.5-29200 m).l).g\im/(lTr an[<br />
26-564 m).l).g\im/(lTrn) myi mil&m pD[l C[. COD n) dr[k AYLi[ prn) mi#ii<br />
an&k|m[ 34.5-145.4 m).l).g\im/(lTrn) myi mil&m pD[l C[. BOD3 n) mi#ii 4.6 Y)<br />
22.6 m).l)g\im/ (lTrn) myi mil&m pD[l C[. Tb) aiv[ C[.<br />
Kis p\kirn) kiy Atr mipv&>.<br />
vihn Äyvhir Yk) uÑBvti avijni Atrn) mipN) krv).<br />
vsihti[ Yk) avijni Atrn) mipN).
[zliEn avijn&> Atr:<br />
avijn&> Atr a¿yis (vAtirni j&di> j&di> AYLi[ prY) ckisN) krvimi> aiv[l C[.<br />
p\i[j[kT siET pr avijni> Atrn) mi#ii 45.8 Y) 55.1 dB(A) (dvs dr(myin an[ 35.8<br />
Y) 40.6 dB(A) ri(#i dr(myin Ô[vi mL[l C[.<br />
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Úiri mi[klvimi> aiv[ C[. Ap[ºT kib aivS[. Ap[ºT si[lvºT Jp)s)b) v[ºDrn[ v[cvimi> aivS[. y&z`D<br />
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ai[Yi[Tim)n[Sn bid v[cvimi> aiv[ C[.<br />
jm)nn) g&Nv_ii ÔNvi miT[ uniLi ätZ dr(myin 7 {sit} AYL prY) miT)ni nm&ni<br />
le pZ¸YkrN krvimi> aiÄy&> C[.<br />
b[zlien AT^[Ts:<br />
pHn) mi#ii 7.87-8.31n) (v(vFtimi> Ô[vi mL[l C[. k[(ÃSymn) mi#ii 35.8-197.4 mg/kg<br />
n) myi Ô[vi mL[l C[. kli[riEDs`n) mi#ii 62 Y) 634.2 mg/kg n) myi Ô[vi<br />
mL[l C[. [ Ti[Tl hiD
mi[EÆcrn) mi#ii 0.5% -3.08% n) myi Ô[vi mL[l C[. pi[ri[s)T) n) mi#ii 46.66%<br />
- 55.55 % myi Ô[vi mL[l C[.<br />
pyi u(ct<br />
kiy l[vimi> aivS[ k[ j[Y) ai gNtr)mi> ki[EpN p\(tk&L asr lxmi><br />
l[vin) rh) n Ôy.<br />
ai uFi[gni aivviY) aispisni x[#imi> simi(jk ai(Y an[ aispisni gimDin) vAt)n&> p\miN vF[ j[n&> kirN<br />
uFi[gi[ Úiri aipvimi> aivt) s)F) an[ aiDktr) ni[kr) t[mj ri[jgirn) tki[ hi[y Sk[.<br />
s>AYini py#i Úiri l[vimi> aiv[l p\d&PN (nvirN pgli> dSitrmiLKi>k)y ÄyvAYi 15<br />
s[vi 13<br />
pyi Jvn/jm)n vpriS 8<br />
simi(jk- ai(Y
d(ryie Jv 6<br />
A#i[itni[ avxy 6<br />
bF) j cci< (vcirNi an[ s&(ct yi[jni miT[ uniLi ät& dr(myin a¿yis kr) t]yir<br />
krvimi> aiv[l a[ºviyri[m[ºT eÀp[kT a[s[sm[ºT a¿yis prY) si(bt Yiy C[ k m[ss<<br />
(fli[D[n a[g\i[k[m p\iev[T (lm)T[D Úiri pyiFpi#i miq) asr Yvini[<br />
s>Bv nY). t[m Cti> pN ki[e ud`gmn) siYi[siY kiydi(ky (nymi[n&> piln krS[.<br />
g\)nb[ÃTni[ (vkis:<br />
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(vkis kr[l C[. k>pn) hilmi> aiSr[ 7670 Akv[r m)Trni[ k&l jm)n (vAtir Friv[ C[;<br />
ai (vAtirmi>Y) aiSr[ 2460 Akv[r m)Tr {32.07%} (vAtirmi> g\)n b[Ãtni[ (vkis<br />
krvimi> aivS[.
EXECUTIVE SUMMARY OF PROJECT<br />
(ENGLISH)<br />
<strong>of</strong><br />
M/s. <strong>PHILODEN</strong> <strong>AGROCHEM</strong> <strong>PVT</strong>. <strong>LTD</strong>.<br />
SURVEY NO. 73, BEHIND GEB SUB‐STATION,<br />
VILLAGE – KARKHADI, TAL. PADRA,<br />
DIST: VADODARA.
EXECUTIVE SUMMARY OF PROJECT<br />
_________________________________________________________________________________<br />
INTRODUCTION<br />
• M/s. Philoden Agrochem Private Ltd. group is manufacturers & marketer <strong>of</strong> Polymer Solvent,<br />
Dyes & Solvent soluble dyes for coating applications. Mr. Mahesh Patel is Managing Director <strong>of</strong><br />
Philoden Agrochem Private Ltd. Existing unit <strong>of</strong> dyestuffs and dye intermediates <strong>of</strong> M/s.<br />
Philoden Agrochem Private Ltd. is located at Survey No. 73, Village – Karkhadi, Tal. Padra, Dist.<br />
Vadodara, <strong>Gujarat</strong> state.<br />
• Its formation was a result <strong>of</strong> coming together <strong>of</strong> experienced technocrats having more than 35<br />
years <strong>of</strong> experience in manufacturing & marketing <strong>of</strong> solvent dyes.<br />
• The Company commenced operations in year August 2003 in Vadodara, State <strong>of</strong> <strong>Gujarat</strong> (<br />
India ).<br />
• In short span <strong>of</strong> time, Philoden has gained sizable market share <strong>of</strong> Polymer Soluble Dyes &<br />
Solvent Soluble Dyes in domestic markets.<br />
• The company has well equipped production facilities which are managed by dedicated,<br />
qualified & skilled persons.<br />
• The company has a manufacturing capacity <strong>of</strong> 300 MT per annum, and processes capabilities to<br />
manufacture all types <strong>of</strong> Solvent Dyes.<br />
Company proposes to expand existing manufacturing activities by adding new products by using<br />
existing as well as additional manufacturing and infrastructure facilities.<br />
This facility is engaged in development <strong>of</strong> new products. A team <strong>of</strong> highly qualified scientists and<br />
technicians is engaged in this process. Project Site having the advantage <strong>of</strong> close proximity to<br />
Vadodara, the commercial city <strong>of</strong> India. Due to National Highway No. 8, the city is well connected<br />
by road and rail to rest <strong>of</strong> India. Development <strong>of</strong> Communication systems are good in the region<br />
due to proximity to Vadodara. A source <strong>of</strong> water in the region includes Mahi River and ground<br />
water resources.
PROJECT SETTING<br />
M/s. Philoden Agrochem Pvt. Ltd. is located at Karkhadi, Tal. Padra, Dist: Vadodara is located at 22º<br />
12’ 20.61” North latitude and 72º 55’ 03.43” East longitude. Total area covered by Padra Taluka is<br />
about 693.62 Sq. Km.<br />
Important places around Project Site are:<br />
Padra city ‐To the East<br />
Vadodara City ‐ To the North‐East<br />
Secured land fill site is operated by M/s. Nandesari Enviro Control Ltd. (NECL), Nandesari is about<br />
29 km away from project site.<br />
PROJECT DETAILS<br />
LIST OF PRODUCTS ALONG WITH THEIR PRODUCTION CAPACITY (EXISTING & PROPOSED)<br />
Sr.<br />
No.<br />
Existing<br />
Name <strong>of</strong> Product Quantity (MT/Month)<br />
Existing Proposed After Total<br />
Proposed Expansion<br />
1. Benzathrone 3.1 ‐‐ 3.1<br />
2. Pigment‐Red‐ “GB” 3.55 ‐‐ 3.55<br />
3. Pigment‐Yellow‐ “GB” 8.35 ‐‐ 8.35<br />
4. Pigment‐Orange‐ “G” 01 ‐‐ 01<br />
5. Pigment‐Brown RM/Dark<br />
Brown‐R<br />
6. Pigment‐Violet BA/Cadbury<br />
Violet R<br />
0.5 ‐‐ 0.5<br />
01 ‐‐ 01<br />
7. Pigment‐Green BP 01 ‐‐ 01<br />
8. Pigment‐Black RE 1.5 ‐‐ 1.5<br />
Proposed
9. Solvent Dyes<br />
Solvent Blue 35<br />
Solvent Blue 104<br />
Solvent Blue 122<br />
Solvent Green 3<br />
Solvent Orange 60<br />
Solvent Orange 86<br />
Solvent Red 52<br />
Solvent Red 135<br />
Solvent Red 168<br />
Solvent Red 195<br />
Solvent Red 207<br />
Solvent Violet 13<br />
Solvent Violet 14<br />
Solvent Yellow 33<br />
Solvent Yellow 157<br />
Solvent Yellow 163<br />
10. Solvent Dyes<br />
Solvent Black 27<br />
Solvent Orange 58<br />
Solvent Red 127<br />
Solvent Red 160<br />
Solvent Yellow 82<br />
Solvent Yellow 21<br />
11. Solvent Dyes<br />
Solvent Blue 98<br />
Solvent Blue 128<br />
Solvent Green 33<br />
Solvent Red 19 E<br />
‐‐<br />
‐‐<br />
‐‐<br />
40<br />
40<br />
50<br />
40<br />
40<br />
50
Solvent Red 24<br />
Solvent Yellow 107<br />
Solvent Yellow 124<br />
12. Pigment<br />
Pigment Blue 60<br />
Pigment Orange 43<br />
Pigment Orange 70<br />
Pigment Yellow 155<br />
Pigment Yellow 180<br />
Pigment Yellow 188<br />
Pigment Yellow 196<br />
Pigment Red 122<br />
Pigment Red 168<br />
Pigment Red 170<br />
Pigment Red 176<br />
Pigment Red 202<br />
Pigment Violet 19<br />
Pigment Yellow 147<br />
13 Optical Brighteners<br />
Optical BR 184<br />
Optical BR 199<br />
Optical BR 351<br />
Total 20 205 225<br />
‐‐<br />
‐‐<br />
40<br />
20<br />
15<br />
40<br />
20<br />
15
PROJECT COST<br />
Total cost <strong>of</strong> the proposed project is Rs.315 Lacs.<br />
Break‐up <strong>of</strong> total cost <strong>of</strong> the project<br />
Sr.<br />
Particulars Capacity Nos. Cost <strong>of</strong> each<br />
No.<br />
I) Equipment<br />
(Rs. In Lakhs)<br />
Total Cost<br />
(Rs. In Lakhs)<br />
1 SS Reactor 10 KL 3 20 60<br />
2 Glass Lined Reactor 10 KL 1 20 20<br />
3 MSRL Reactor 10 KL 1 5 5<br />
4 MSRL Reactor 20 KL 1 8 8<br />
5 PP Filter Press 2400 X 2400 2 10 20<br />
6 MS Centrifuge 48” 1 7 7<br />
7 M.S. Filter Box 5 KL 2 1.5 3<br />
8 Pulverisers 100 Kg/hr 2 1 2<br />
9 SS Blender 3 KL 1 2 2<br />
10 KBC Filter 0.2 KL 1 1 1<br />
11 Tray Driers 100 Trays 4 12.5 50<br />
12 Methanol Tank 10 KL 1 2 2<br />
13 Solvent Storage Tank 5 KL 2 1 2<br />
II) Building 15<br />
III) ETP 25<br />
IV) RO Unit 10<br />
V) Incinerator Unit 50<br />
VI) Electricals 10<br />
VII) Contingencies 23<br />
Total (RS. in Lakhs) 315
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2. p)³m[ºT r[D- “Jb)” 3.55 ‐‐ 3.55<br />
3. p)³m[ºT yli[- “Jb)” 8.35 ‐‐ 8.35
4. p)³m[ºT ai[r[ºj- “Jb)” 01 ‐‐ 01<br />
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6. p)³m[ºT viyi[l[T<br />
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01 ‐‐ 01<br />
7. p)³m[ºT g\)n b)p) 01 ‐‐ 01<br />
8. p)³m[ºT ¾l[k aire 1.5 ‐‐ 1.5<br />
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si[lvºT ¾l& 35<br />
si[lvºT ¾l& 104<br />
si[lvºT ¾l& 122<br />
si[lvºT g\)n 3<br />
si[lvºT ai[r[ºj 60<br />
si[lvºT ai[r[ºj 86<br />
si[lvºT r[D 52<br />
si[lvºT r[D 135<br />
si[lvºT r[D 168<br />
si[lvºT r[D 195<br />
si[lvºT r[D 207<br />
si[lvºT viyi[l[T 13<br />
‐‐<br />
40<br />
40
si[lvºT viyi[l[T 14<br />
si[lvºT yli[ 33<br />
si[lvºT yli[ 157<br />
si[lvºT yli[ 163<br />
10. si[lvºT Diez<br />
si[lvºT ¾l[k 27<br />
si[lvºT ai[r[ºj 58<br />
si[lvºT r[D 127<br />
si[lvºT r[D 160<br />
si[lvºT yli[ 82<br />
si[lvºT yli[ 21<br />
11. si[lvºT Diez<br />
si[lvºT ¾l& 98<br />
si[lvºT ¾l& 128<br />
si[lvºT g\)n 33<br />
S si[lvºT r[D 19e<br />
si[lvºT r[D 24<br />
si[lvºT yli[ 107<br />
si[lvºT yli[ 124<br />
12. p)³m[ºT<br />
‐‐<br />
‐‐<br />
40<br />
50<br />
40<br />
50
p)³m[ºT ¾l& 60<br />
p)³m[ºT ai[r[ºj 43<br />
p)³m[ºT ai[r[ºj 70<br />
p)³m[ºT yli[ 155<br />
p)³m[ºT yli[ 180<br />
p)³m[ºT yli[188<br />
p)³m[ºT yli[ 196<br />
p)³m[ºT r[D 122<br />
p)³m[ºT r[D 168<br />
p)³m[ºT r[D 170<br />
p)³m[ºT r[D 176<br />
p)³m[ºT r[D 202<br />
p)³m[ºT viyil[T 19<br />
p)³m[ºT yli[ 147<br />
13. ai[¼T)kl bi\eTns<<br />
ai[¼T)kl b)air 184 15 15<br />
ai[¼T)kl b)air 199<br />
ai[¼T)kl b)air 351<br />
k&l 20 205 225<br />
‐‐<br />
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40<br />
20<br />
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p\i[j[kT (k>mt:<br />
s&(ct p\i[j[kTn) k&l (k>mt $.315 liK C[.<br />
k\mi>k. (vgt xmti> s>²yi dr[kn) (k>mt<br />
{$.liKmi>}<br />
k&l (k>mt<br />
{$.liKmi>}<br />
1. siFni[<br />
1 SS Reactor 10 KL 3 20 60<br />
2 Glass Lined Reactor 10 KL 1 20 20<br />
3 MSRL Reactor 10 KL 1 5 5<br />
4 MSRL Reactor 20 KL 1 8 8<br />
5 PP Filter Press 2400 X 2400 2 10 20<br />
6 MS CENTRIFUGE 48” 1 7 7<br />
7 M.S. FILTER BOX 5 KL 2 1.5 3<br />
8 PULVERISERS 100 KG/HR 2 1 2<br />
9 SS BLENDER 3 KL 1 2 2<br />
10 KBC FILTER 0.2 KL 1 1 1<br />
11 TRAY DRIERS 100 TRAYS 4 12.5 50<br />
12 METHANOL TANK 10 KL 1 2 2<br />
13 SOLVENT STORAGE TANK 5 KL 2 1 2<br />
2. Building 15<br />
3. ETP 25<br />
4. RO Unit 10<br />
5. Incinerator Unit 50<br />
6. Electricals 10<br />
7. Contingencies 23<br />
k&l (k>mt {$.liKmi>} 315