Document e7aL4j3zm2m57bJLBp8dEYYdg
TM_ tO* 17*1*iO 1WX 710 OMTH
Crawford a Hussell
INCORPORATED
CHEMICAL 0 PROCESS PLANTS
STAMPORD, CONNECTICUT QSS04
Hardi 24, 1967
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fi/c ~ //*&*}t,J*iort**t**-
Hr* Hilton Sogers Kseaabia Chrod, cal Corporation P.O. Box 46? Pensacola, Florida
Dear Mr* Rogers:
Attached are three cost sheets for manufacture of chlorine.^ .ethylene, and vinyl chloride. ^S^S^/pc/^
The chlorl'cfe plant is a Tfo-lfrLllion pound per year plant with a cost of chlorine of 1*W per pound based on $7*5/ton salt., $28/ton credit for caustic, and 0.7^/FW electrlo power*
Hie ethylene plant is a 500 million pound per year plant with a cost or ethylene of 2*67^ per pound based on 1*2^ per pound for propane* Only half of the 500 million pound per year is required to make the required production of VCM* It is assumed the remainder can be sold (at 35l per pound at the plant gate)*
The VCM plant has a capacity of 500 million pounds per year* The prices for chlorine and ethylene are those developed above, giving a cost for VCM of 3 45_-per pound. with no allowance for sales expenses, transpos'd.on, etc*
The capital requirements for the facilities is $89.500.000. using only half of the capital cost of the ethylene plant. Start-up expense and working capital were assumed at $500,000 and $4,000,000 respectively giving a total capital requirements of $44.000.0flQ*_ The attached table gives a breakdown of oapital and operating requirements*
\
AP00034069
Crawford a S3,trsuDz Mr. KLlton Rogers
2
March 24, 19&?
Aa X told you on the phone. CAR is now designing a 300 ton per day chlorine plant Tor Olin Mathieson, and we are a licensee of Olin. We have engineers in our offloe who have worked on the design of ethylene plants, and, as a result, ve think our estimate of the ethylene plant is reasonably accurate. Cb the oxychlorination process, ve are familiar with the economic figures for the process.
Some capital and operating savings should result from the integration of the three plants in one complex* We have not taken this into account, however.
X trust that this information will serve your present needs. If ve can be of further help, please call.
Very truly yours,
CRAWFCRD & RUSSELL Incorporated
LB spot Enclosures
coi Hr. H* Harwell - New Xork
L. Basel Vice President - Sales
i
AP00034070
500 KM #/YR VCH CCttFLEX FOR ESCAMBIA
CAPITAL COSTt *`
Chlorine Plant Ethylene Plant VCM Plant
Capital
Start-up Expenses Working Capital
Total Capital
$ 18,000,000
7.500,000 , 14.000.000
450 T/D
i of 500 MM #/yr 500 MK Hrr
* 39.500,000
500,000 4,000,000
$ 44,000,000 _
DIRECT LABOR:
Chlorine Ethylene
vcm
Total Direct Labor
27 15 la
60
FEEDSTOCKS:
Rocksalt Propane
285,000 tons/yr 296,250 tons/yr 3 0.8 - 1.2^/lb,
PRODUCTS:
VCM Caustic Soda Hydrogen
Liquid Distillate
250,000 tons/yr 169,500 tons/yr
4,750 tons/yr 37,800 tons/yr
CHEMICALS: UTILITIES:
Acetylene Conversion Catalyst
1,600 cu. ft,/yr
Desiccant (Alumina) MEA
128,000 Hyr 48,000 i/yr
RC1 (30jC)
26,500,000 #/yr
Methanol
400 Barrels/yr
Graphite
725,000 #/yr
Mercury
64,000 #/yr
YCH Plant Chemicals
$ 312,500 per yr.
Fuel 40 MM Btu/hr Credit Power 80,000 KW Consumption 150 psig Steam 30,000 #/hr Consumption 50 psig Steam 62,000 #/hr Consumption
BFW - 71 GPM Consumption Cooling Water 54,000 GPM Consumption
The mercury inventory of 400,000# cannot be depreciated. Part of the 20 HC1 water stream of the VCH Plant may be upgraded to 3^ to supply the Chlorine Plant. This has not been taken into account, however.
AP00034071
PRODUCTION COST ESTIMATE
;flP. Co>T JliS.ooo.ooo
Products CHLOAiNfe
HYDftO&*6N
Quantity
Units
MVnoo.ooo 4k
S"Vi. ooo.oou 4b.
Nor
an
Sales Price
UA d
Annual Value
S. ? OO. OOO
COST OF FRCDUCTIQN RAW MATERIALS
Hoc.* iflUT
CL
&ulfur<c. non
r e.
Mercury tflysnttnepit
RAW MATERIAL CCST UTILITIES
Stean Ste&n Coolina Water Power Fuel
Quantity
51>, ooo.oco Afe.Soo.ooo 5. 000.000 >feS.OOf OOO.OOn
fi . 52 O. ooo
Units
4 a a * s
ft
\ ooo Cr
Price
0.31s d a-so d
I.&F < 6f%fSO d
koo d 1.4- l_
Subtotal
Annual Cost
2.. \ ACa. ooo A&o. Ooo 4o. ooo *.--o. Onrs aftO . o on
-- s, ioo. ooo - 1 . ~UO . OOO
A o.o2 > o.oo>
S-O. ooo i o 4o. OOO
Product Unit Cost
- O.Sf
UTILITY COST
OPERATING EXPENSES
Labor F orewen
.1.30 ____
Suoervisicn
J______
_1
Maintenance s /9 op- capiTbL
Suonlies
ft /o o* Lfl&ea
Subtotal
IS..OOO
OPERATING EXPENSE OVERHEAD EXPENSES
Subtotal
Payroll Overhead
i
G.i.r.1 P1.-.-T, 0TM-h*,,d ) 10 "
lProo.
Property Taxes. Insurance, etc. 2.7?.% efip
Deoreciaticn in
cApvthu
OVERHEAD EXPENSE TOTAL COST CF PRODUCTION
Subtotal TOTAL
4 oSo.ooo
aio. ooo
3 o. ooo ie,ooo
t , 2.^0. OOO
>S.Ooe
4jro.ooo
1. S oo. ooo
. S' AS. ooC 6,1 3, ooo
1.2.2. O'AS__________
o.lS
AP00034072
PRODUCTION COST ESTIMATE
'ftp. COfat -*\S, 000.000
.USTQMER: __ PROJECT NO.
PLANT;
E-TnyLEMf8. PiftNT
CAPACITY: j?ootoW**/v*
LOCATION ^TJlc Cqaat
OPERATING HCURS PER YEAR: _ BY:
__________________________________ DATE: __________
TJ P
s-Ai-A*}
*
Products
..ETMVL6NE LjCtht
Quantity Soo,ooo,ooo \s i. i oo.ooo
Units
Sales Price I <
Annual Value ooe
COST CF PRODUCTION
RAW MATERIALS
Quantity
Tropahs
I.Ol,oeo. 006
LI&Hr DIVriLLfiTG l Sl,2.oc>,ooo
Units
& rffc
Price t.2.
e*
Annual Cost
1 2. 000.000 - 1. SI2.000
?72fc Product Unit Cost
RAW MATERIAL COS? UTILITIES
Steam Steam Cooline Water
Power Fuel soiT BfW
fcSSo.ooo
6.4-50.000 e.48o.ooo SSk. ooo
Subtotal o, 4RP. ooo
IOOO Gr
KWH MMRTU
t ooo <y
S C.OS. 3 0. oo*V
4b o.O>
4ff.o0 _ Aio.mvi
41.000
-.\o
UTILITY COST
OPERATING EXPENSES
Labor Foremen
\ 30
Supervision
J
Maintenance
of capital
SuDnlies .cftTftWsri'OHiMicfii.i
Subtotal - 2.07.000
l&. OOO
560.ooo
4^o non go,ooo
- o. o4-
OPERATING EXPENSE
-
Subtotal
OVERHEAD EXPENSES
Payroll Overhead
1 f<-*/
> L^r>o
General Plant Overhead >
Pr ooe r tv Taxes. Insurance, etc. 3, '/?. V. eft P
Deoreciation
la /. ,rcaw;HT
OVERHEAD EXPENSE TOTAL COST CF PRODUCTION
Subtotal TOTAL
go.OOO
o.i8
4>o, ooo
575.ooo l.5oo, ooo
-----
a. H S.ooo
o.43
I 3. 55 4.0_oo----- _______ ff.Vfr_______
AP00034073
PRODUCTION COST ESTIMATE
rp. cobr; 1^000,000
CUSTOMER: EscrniRAft
PLANT:
vct-\
_____________________ ______ _____________
CAPACITY: .goo mm &/va
LOCATKW: frWlplcOftVr
OPERATING HOURS PER YEAR;
PROJECT NO. DATE:
BY Tap
Products
Quantity
Units
Sales Price Annual Value
COST CF PRODUCTION RAW MATERIALS 61* fWLtNE CHlOftlNE
CAT
Quantity 2. A-l. 060, oon AVf.OO. odo
Unite
ft
Price 4.6? I.S4
Annual Cost
6 A 4,3 nan A l 95. ooo
& \ 4. 66
Product Unit Cost
RAW MATERIAL CCS?
UTILITIES
_________
Steam iso pfct<4-
0 0 0
0
Stean go p&ig- a.6ls.ooo
Coolinff Water
iff. iso.ooo
Pover
svrso.ooo
Fuel
87s. ooo
i on V 60O &
KW H
Subtotal
A o 'Jo A o.8o ii o.2. S O.oo% A 0.45
1.l le.ooo
l rA. OOO 414. 003 ii5,ooo
OOO &\o.Ooo
UTILITY COST
Subtotal
OPERATING EXPENSES
Labor Foremen
Suoervision
Je; IB
i
ia.. (soo
Maintenance S* /o op
Suottlies
A */o OPlunfcOK i
OPERATING EXPENSE OVERHEAD EXPENSES
Subtotal
Payroll Overhead * oc tsTbl LflP.o General Plant Overhead V ,w' '*
Prooertv Taxes. Insurance, etc. iVa.% cap.
Deoreciation
ia / bTP.ftxrt-HT
OVERHEAD EXPENSE TOTAL COST CP PRODUCTION
Subtotal TOTAL
1,418. OOP
411. ooo
> no. ooo IT- OOO
R4V ooo 1 4 4. Oo
3 5*o .OOO f , 4op, 06 0 i. 3 \ i .ooo \\. 433.000
. 0.44-
o. 19
a. %8 3.4^-.
AP00034074
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AP00034075
P. O. BOX 467
PENSACOLA. FLORIDA
DATE
SIGNATURE
ORIttlNATORl DETACH THIS COPY, SEND REMAINING SET. CARBON INTACT, FOR USE BY REPLIER.
AP00034076
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AP00034078
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AP00034079
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AP00034080
AP00034081
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AP00034082
ESCAMBIA CHEMICAL CORF.
JOB NO-
Location Subjbct__________ ____________________________
- yy
paok. DATS. BV___
CAfZr/MC ^3*3 ^T"
~/twLoC. /M&i
AP00034083