Document DDVz87gmDNpdVbpJ8DK0KkL9d
FIRE AND EXPLOSION INDEX
MANUFACTURING UNIT LIGHT HYDROCARBON H
PROCESS UNIT STORAGE AREA 2D-30A/B AND 2D-220 A/B/C/D
BACKGROUND INFORMATION FOR STORAGE AREA: Tlie 2D-30's are the storage drams for product propylene. The 2D-220's are the product ethylene storage drains. The 2D-30's are 69 feet 8 inches in lenght and 10 feet in diameter. The 2D-220's are 69 feet 8 inches in lenght and 10 feet in diameter. The normal operating conditions are for two of the ethylene storage drams to be empty and for one of the propylene storage drums to be empty. The levels are ran to where we have approimately 1 product drum of propylene and ethylene.
Volume for the dram is calculated below:
V=tit*H
V=Jt(5)2 (69.75) 5,478 cf
V= 2 (ethylene drum 50 % level) + 2 (ethylene dram empty)
V = 1 (propylene drum 30 % level) + l(propylene drum 60 % level) THIS IS NORMAL OPERATING CONDITIONS!!
V = 2 (5,478( 50)) + 2 ( 5,478 (0)) = 5478cf (30 Ib/cf>=164,340 Ethylene volume
V = 1 (5,478 (.30)) + 1 (5,478 (.6) = 4930.2cf (30 Ib/cf) = 147,906 Propylene volume
The volume of flammable product was calculated to be 164,340 lbs. of ethylene. No propylene was taken in the consideration. The dram operate with no cross ties.
Material Factor (from Appendix A of Fire & Explosion Index Hazard Classification Guide)
He
Flash
Boiling
v Compound /; MF BTU/LB nH Nr Nr ; Point;'- Point
xlO3
<F)
(F>
Ethylene
24 20.8
142
Gas
-155
Propylene
21 19.7
141
-162
-54
General Process Hazards: (Information) No penalties were taken for exothermic chemical reactions, endothermic processes, enclosed or indoor process units, and access. Penalties were taken for materia] handling and transfer of 0.85 and 0.5 for drainage and spill control. The penalty for material handling and transfer because of the Np, The penalty for drainage due to the poor drainage in the area and lack of solid surfacing under vessels.
7/10/95 FEI.doc
DOW CONFIDENTIAL
Special Process Hazards:(Information) A penalty of 0.2 was taken for toxic material. The penalty was calculated by multiplying Nh by 0.2. No penalty was taken for sub-atmospheric pressure due to the pressure the drums run. No penalty was taken for operation in or near flammable range. No penalty was taken for dust explosion. The pressure penalty was 0.73993. No low temperature penalty was taken. The quanitity of flammable/unstable materail was calculated by multiplying the quantity of ethylene in the storage drums by it's heat of combustion. The penalty was found to be. The corrosion and erosion penalty was 0.1. The leakage penalty was 0.1. No penalties were taken for use of fired equipment, hot oil heat exchange system, and rotating equipment
Loss Control Credit Factors
Process Control Credit Factor (Ci) Emergency Power -0.98 A credit was taken for Emergency Power due to the UPS system. Cooling -1.0 Explosion Control-1.0 Emergency Shutdown-1,0 Computer Control-1.0 Inert Gas-1.0 Operating Instructions/Procedure-1.0 Reactive Chemical Review-0.91 A credit was taken for reactive chemical review. Reactive chemical concerns are listed on MOC sheet and plant personal are trained and tested on reactive chemical concerns at LHC II. Other Process Hazard Analysis- 0.98 for Management of Change Review
Material Osolation Credit Factor (C2)
Remote Control Valves-1 Dump/Blowdown-1 Drainage-1 Interlock-1
Fire Protection Credit Factor (C3)
Leak Detection -.94 LHC n is protected by Bacharach gas detectors. A project is being worked on the elevalate the gas detector system and replace with a more relible system. Structural Steel-1 Fire Water Supply- 0.94 (supply pressure will be approximately 100 psig without pump and 150 psig with pump.) Sprinkler Systems-. 97 A credit was taken for the deluge systems at LHC Q. Water Curtains-1 No credit was taken for the furnace water curtain due to its height and that furnace 1-6 and 19-25 are unprotected are the lower level. Foam-1 Hand Extinguishcrs/Monitors-.97 Cable Protection-1 (This credit would change after completion of the Instrument Upgrade Project)
7/10/95 FEI.doc HWR
DOW CONFIDENTIAL
DO A 031287 CONFIDFNITIAl
FORM IMA MANUFACTURERS' DATA REPORT FOR UNFIRED PRESSURE \ESSELS Allwaste Fora for $ii|lt Cheeber Completely Skop-Fihricittd \eela 0"l)
________ _
AHF BEAIRD. INC.. SHREVEPORT. LOUISIANA
l. Ua*I. , 1 b ------------------------------------------!--------------Nfe=-5X3JS^HK5iCT=r
I.
th
craic-U. ocrgAHT,
- '"'-i&PfteT- .......... .. Sii'iJuj* >1
(nw
_ himh f pwti>*#>)
........ . " -----------------
Ye. Bailt 1969
........... .... A-i-70-n ti eo.ooo*n!:tmt(i ^.1A*u. Di,,.w. ,,.o_u.
* 5MfcU
are* ini **.< v*.)
)heedn/li
--
--
5 SEAMS: lo"f , mi.
La BuHi).T. (v*R*oH*> > .fTlo.aCt O ^c>lpltulSit)rtiiMnj (_VWam n*) Fffiricactr 100--%
Gink
Rltt H.T.______*0______
No. of Coot-- M
---------------------
If rtata4 or hraa*0 fwifbi m tally aaOar
.. HEADS. fc)6!:.i.lJWlr0^w TJ.
(To. MHO. aa4a> TUcOtu
IMIO
MO!
(>.
<fc>.
If iMMtUt, Soli* Mtf --qKg7m.ifw:irt..T.r.iu*.imA**i
Ml*
At'1 Aajla
Odot faateaiaf,
I, CNitncod bt *m.
.
llwtWi ootfci** 0t*. 300 p*i Atai.no*.
... .
Mia. teap. (whea
250 F. Iea Am -20) _
ItlM
. __ll-------------IM I* PWHIFB----ODlIasnwa m (Caavaa aa Ctstml
-8od1*1/6"lilCoacev
BNlcrKrVUIMal Hfcll
Hpdioitatic I
_ Paeiaaatic or) Teal F. Coabiaotioo ( Pmi
""" '--
. .. 486 pai.
SAFETY OR RELIEF VALVE OUTLETS: Naahat
1Sue __
9. NOFZyZpLpEHS* :(Mt,
OvltM. DuIr)
NM^tf
Dl**. m IU
T|f*
ftHtiril
(2) 1-1/2" 300# Loot Veld Rack Plga.
------------------ m~TrT0 TrT50#WITTI5ci-fTgif--------
..................... car*" tz) tm~3Qu# Vamrack-Figa;----------
v____ _ Location To of tank 1b ehell
Thjahaaaa
IA-105-I
Bala/ate aaaa< Matartol
Ha-- AttaahaB
Welded
SA-10i-I
Welded
"'1A-103-I
' Welded
INSPECTION OPENINGS:
2Maakole*. No. SUo
Haadholea. No. nmM. No.
-
18"Locatioa
Mm Siaa Locaiioo
Locaiioo
<11 tech end ef tBBk la h-- <!
--
11. SUPPORTS: Skin
Laaa
Laaa
Oikct /2) SaddlCR
ITaa at Ra)
UToaocrj
OnoM*)
(MKtaf
Attached Wolfed tp tJnk hell (VM-nSi)
12. REMARKS: Oao 120" X.P. X 77* 3-11/16** O.A. Length 43.084 tf.O. Itorego Teakr .per Beelrd Pun.
Order 161910_________________________________________________________________________________________
ISU(liKtltllt iltwtMia ia* ! aa At Yaaa, la* Taaa, i.p.b.. u.-ks latsas.
* Usl mMi totataal at samal prtnats *Hh itloMta ttaparatart whaa EttlkOI).
V* can It* that Its atataiaaata Asti to tMa W* Hf/jPViW'/SJ all etilli af Oaalia. Malarial, aaaatfwctlaa, *mt atlatoaahlp at tkli mimI aaa#<'mm la tha AMI Cat* fat IWIMf frt'lC Vaaaala. IVOO IdltlOB
Dm*
1*10 19 89
Si|*H,
AMF BEAIRD. INC.
------------ " (aWUlwsT)
*
Certificate of Authotiiaiion Eapitea
December 31. 1970
CERTIFICATE SHOP INSPECTION
VIMtl. mci ev.
I ha oMiiltM*
AMF BEAIRD. INC.
SHREVEPORT. LOUISIANA
haI4la* a aaM4 eaaoliAlaa tota4 ha tha Natlaaal eaa4 4 Ballar aa4 Nnvr Vaaaal hattatM aa4/ar
N. B.
j Mtoit h THE COMMERCIAL UNION INSURANCE COMPANY
*
NEW YORKhaat toapattah tha praaaara vaaaal AaKiIMt In |HJ amAtiair't
<|[| mpml *-
1*10
ha4atata that la tha haat af mr haa*la4f4 aa4 haliaf. tha aaaafac-
)^|J ^. inttMtttf ihta pattat vaaaal la aaaaa4aaaa *Mh tha aphUcahla aaattaaaaf tha MU Ballar aa4 praaaara Vaaaal CaOa.
a iljDlio ihia cartlflaata aUha> tha feapaetar aar hla aaolar-r oakaa tap narrator, aaraaaa4 a Ipa4. (MCCA| tha proa<wa nMal 4aaarlha4 to thla atmfMtiaar'a Bata aapart. ftothnoait. aalthar tha Inapactar aar hla aopiapar ahall ha llahla to aap
... paraaaal >a|ary at prapartp A--a aa a laaa af aap hto4 arlato hmm at acta4 aaA ihIA toapactlaa.
!>>/
pna
____________ __ C--laalaaa
hat i Uahrl at Kali aa4V<
D0 A CONFTnENTlAl.
WR i *U* V / / W"ijJW7 FORM II-1A MANUFACTURERS* DATA REPORT FOR UNFIRED PRESSURE NESSELS
Alternate Forte for Single CWeber Completely Shop-Fabricated Vessels Only
I ............<f
AMF BEAIRD. INC.. SHREVEPORT. LOUI.-L.ufA_______________ ( and addrvir W Ifeatdaciwar)
2. Manufactured far
THE DOW CHEMICAL COMPANY. HOUSTON. TEXAS_____________ ptana and addirni w rifimn)
'rnm
-v--1 SjfllSfei-1V-*.,
) Natl. Bd. No*_
SA-516-70-Fbx
no.1-3/4 Cow. 11/,1-6-
A cmELL: Marl. A-300-1 .
T.S. 70.000# Tfcfc.In. Allow
In. Draw. 10 Ft. 0
(iu an* *>. m.) trig, nr r.a, hip.*. Mfa. T..)hea dsT7l6
Yr. Built.
1969
_
lit. Lencd>69 Ft. _ln. -------------------
y SEAMS: Lone Dbl. Butt H.T. Yes
(WaMad,
Lap. IUI) (Yaa U)I
Gittli Dbl. Butt H.T. Yes
R.TComplete Sectioned No
Eificinarv 100 *
(Spat ar Cm|I)I
CYi ar Ms)
ILTgomplete Sectioned So
No. o! Cooties. 10
II rlrrirt or braird tticikr ihm fully wtw
SA-516-70-Fbx
4.,,E*DS:aiMfi.m1_ftz300il--------- ^ TJ.
(Tie. batten. aada) !) Ends
TUehMH 1-3/411
Sadia*
Iktbi ____________
at* 2:1
^
Ayri Angle ________
IttM
. T&,
Dianatar
--Ml T WIIIH-- (Caavaa ar Concave) Concave
<b> H refaov.ble, bolt. ..ed
~ (pair.ai M'xnreb iketan-----------------
7. Coo atmetad far was. allowable working been. 475 pal at att.ttap.j
Mia. itap. (when F. leaa tkaa -20) . -50
Hydroatatic I
_ Pneumatic oil Teat F. Coabiaatioa j Preaa, 752 _ pgj.
S. SAFETY OR RELIEF VALVE OUTLETS: Number.
Sice
9. NOZZLES:
Furpeat (Inlet, OWlat, Drain)
Number
Dfan. ar Cue
Type
Mataria I
(2) 1-1/2" 300# Lone Weld Neck Figs.
(8) 2" (1) 3" 300# Weld Neck Figs.
(31 4" (1) 6" (3) 8" 300# Weld Neck Figs.
4" Location Top of
Thlekaeee
Re in!oriental Malarial
SA-350-LF1
SA-350-LF1 SA-350-LFl'
tank in shell
Attache*
Welded Welded
Welded
m. INSPECTION OPENINGS:
Maaholea. No_ Haadbolca, No,_ Threaded, No. .
. Sice. .Sice.
Sice.
18*'
ij>,a.iM Location Locat too
(1) Each end of tank In heads -................ ..
n. supports: a...(fcg-.S-a--a--.-d>---d---l-e---s-----
a,,.^i..A Welded to tank shell AttacBco---------fc Ha.)------------------------------------
12. REMARKS: One 120M I.D. x 77* 3-11/16" O.A. Length 43.084 W.G. Storage Tank, per Bealrd Dwg.
Order 161908
nklrl drxrlpllon of purport a( tha rvaaal as Air Tank. Vatar Tank, L.P.O.. etc --atntr ContaMa.
!tf poalareld haal-traatad.
1 Llat atIwr UUamal aa eateaaal proaawaa atltk aalacldafa tv
itw* fcaa appllaablo.
caalam
vWao canliftyy. thnati tnba aetiaiamateantia anardt*v in Ithkilni riwapp.art la tba ASMS Coda lay Unllred Prvatwa Vaaaala.
^^reg^d
^nt^all
Lon
dataUa
al
da alga,
notarial,
caaataiwllan,
and
Data
2-14
19 69
signed
aaKIp ml Hila raaaal
Certificate of Authorisation E spires
December 31. 197Q
CERTIFICATE OF SHOP INSPECTION
VtaaiLMADB IV, AMF BEAIRD. INC.
at SHREVEPORT, LOUISIANA
I IM wtdaralgnrd, balding a valid--------laauod bp lb* Natlanal land ml Boiiar and Praaawa Vaaaal fanpaelare and/ar
lb. Mat. ar
N. B.
m* .-!*< bp COMMERCIAL UNION INSURANCE COMPANY
AMERICA
__________ bava Inapactad tha praaawa vaaaal daacrlbad In ibla nanufactwir'e
dnia tapart aa.
______
2-14 t_69 andalata Ibat ta IM bvai ml ny knowladfV and ball*I, tba nantdae-
tlrst Ml canalraatad Ibla praaawa vaaaal la nee aidant# with iba appUaabla aecliana ml Iba AtMC Sellar and Pioeew# Vaaaal Cada.
Bp algnlng tbit can IfMata neither iba Inapecter naa hla anplayar an baa nap warrnMp. aapaaaaad aa lawlled, concerning Iba pree-
awa vaaaal deaerlbnd fa Ibla narufaclwer'a data rvpart. Pwtbemera. aaltbar tha faapacta, nar bit anplayar ahall be liabla la any
___ --- (M My paraanal injury or prepany image aa a Ion a al any bind aaiafag Iron ea aanaaetad wch Ibla faapacilan.
Daia
--- -- ,
** fe?
DO A 0312S9
C0NFIDFNTIA1
FORM U-1A MANUFACTURERS' DATA REPORT FOR UNFIKED PKESSOKE Alternate Form For Single Outfit b>'r Completely Shop Fabricated Vessels Only
As required by the Provisions of the ASME Code Pules and the National Board
l. Manufactured hvWilson Engineering i Mftrj - jt, Divl.sinn of-Wilson -S'jpplyKnustan, Jaxa.3 (Nun* and address ot Manufacturer)
T. Manufactured for. Thft Dnv CHn-nioal CnTinfLny,-----------
Frsgporl, .Igras-
(Nam* and address o( Purchaser)
s. Type--Horiz-
(Horlz. or
Vessel No. (_ PVJJ
.) (_ SWUO
J Nat'l Bd. No._ am. *'V.I
JTr. Built.
-49#-
y
4. SHELL: arat'iA-'^nfi-CLlr.af 70,000 T#k.'
Aimv 1/l^Diam-l 0ft.J3___ CL Da.In. Lengthj69_ftB___ SM_toJSM
(Kind and Spec. No.) (Fig. or F. B. A Spec. Min. T.S.)
5. SEAMS: T^ng t)nW
y BT .Tas J
XR Full.
(Welded, Dbl,, Single, Lip. Butt)
(Yes or No)t (Spot or Complete)
(Yes or No)
Girth__ DBW . HEADS: (a) Material.
y JIT- YffS ^ -X.R-
HnneA Mo
Nn of Courses.
$i-$hZe.gi9. ts. 70 f aoo J (b) >Uterial_SamLdfL
y
%
/
U riveted or brazed describe
scams fully under remarks.
ts. 7n1nnr/'
Location (Top, bo'*..- er.is) Thickness
Crown Radius
Knuckle Radius
ElllpUetl
Conical .Hemispherical Flat
Ratio ^ Apes angle
Radius
Diameter
Side to Presisure
OSGOOCT Conicave)
(a*.. -iad.
J *-30J Mlny-
J&L
Jlnnoavgr
(b)_
If removable, bolts used.
(Material. Spec. No.. T.S., Size. Number)
.Other fastening.
Constructed for mis. 7. tllowiblt wockifig presi.3.
-pu. tt mix. tcmp_
Min. temp, (when
*F leu dua --20*)_
j=l50_
8. SAFETY OR RELIEF VALVE OUTLETS: Number.
size4w 300 Location
(Describe or Attach Sketch) Hrdrofutic t
J
p. m$eK te_____mi.
Shelil /
9. NOZZLES:
Purpose. (Inlet Outlet. Drain)
Number 1 1
Diam. or Size
Type
300# VJ.N. FLG.
?" 300^ W.N.FLG /
Reinforcement
" * Sch. Rq/,
'
?
R" *OQi/W.II.FLG. / .
"
^Seb. 80-/
.10 INSPECTION Manholes, No._
7 .Size 18" 3004 / Location Had_
.... "
/
How Attached '/>'=!1 d pd Wei d Ad 'Lid Pd
OPENINGS Handholes, No.___________ _Size_
______ Location.
Threaded, No.___________
.11 SUPPORTS: SkirtLugs
_Size_ -Legs.
______ Location. Other S-'idt'
(Yes or No)
(Number)
(Number)
(Describe)
Attached VL1 rifid in Shall (Where & How)
12. REMARKS: -Contents of Ves/gl unknown? not to be used in Nuclear or Lethhl Serving.
r
T A|, cm. QA-, tyj-L,'j: .h- *
*
^ l r>y ____ ....
? 4"' 300* V31. FI.G. SA-^50-I.?VA-333-U Sch. 80
7 1 Alteon it T*v>! FLO. SA-ifO-LF*
'.-LI d ad
--
P.0.47n3qd_T,Fb>t
It era 7ft. 220 A_____________
(Brief description of purpose of the vessel, as Air Tank. After Cooler, Jacketed Cooker, etc. State contents of each part.)
Z If Postweld Heit.Trested 3 List other internil or extern! pressures with coincident tesspersture when applicable.
We certify that the statements made in this report are correct and that all details of design, material, construction, and workmanship of this
vessel conform to the ASME Code for Unfired Pressure Vessels.
B,--2SLL
'
Date. -3*1
-19-
g|fried
Wi 1 enn Snt*. & ?'fp. Co. (Manufacturer)
Certificate of Authorization Expires.
December 31. 1957
VESSEL MADE BY
CERTIFICATE OF SHOP INSPECTION -.Wfir-c.Q;at.Houstoa^.-lcxas...
I, the undersigned, holding a valid commission Issued by the National Board of Boiler and pressure Vessel Inspectors and/or the State of_____and employed by .__________________________________________ jLf---& I Co.___ ______ ___________________
Conn.
of--------------- - -- ,,,,--y---------------------------------- have Inspected the pressure vessel described in this manufacturer's data report
J. 'i-3-on .-- ----
-- ----- - 19--and state that to the best of my knowledge and beltet, the manufacturer has con
structed this pressure vessel In accordance with the applicable sections of the ASME Boiler and Pressure Vessel Code.
By signing this certificate neither the Inspector nor his employer makes any warranty, expressed or Implied, concerning the pressure
vessel described In this rvmuficturer'i data report. Furthermore, neither the Inspector nor his employer shall be liable in any manner
for any personal Irlury or property damage or a loss of any kind arising from or connected with this inspection.
Date........ i
Inspectors Signature
_,
Texas # 14
Commissions______________
Nat'i Board or State and No.
CPCo 10-64--SOM
------ DO A 03.1090 confidfnttai.
103 COMMAND *=>
INQUIRE FIXED EQUIPMENT
05/30/95 10:44
Equip ID Cost Center
Serial # 'ssoc Ser #
Parent ID
PSV 2D-220 A*
Eq Desc: SAFETY VALVE #802820
Unit:
0000063
criticality: 01
Area: STORGE
Project:
49-409 M3
Equip Code:
Type:
Equip Cond:
Spec:
2D-220 A
Grid:
Fleet MGMT?:
Install Dt
MFR Abbrev CROSBY
Model #:
Model Type JO-34A
Model Size: 4" X L X 6"
GEMTS->
Prod / Process: PRODUCT DISTRIBUTION
2D-220 SYST
Eqp Group / Type
: PRESSURE VESSEL/VALVE
PRESSURE R
* * * SPECIFICATION TEXT * * *
INSPECTION SCHEDULE: 60 MONTHS
VALVE SET PRESSURE: 500 PSXG
OPERATING TEMP: -25 DEG. F
OPERATING PRESSURE: 450 PSIG
BACK PRESSURE:
0
PRODUCT: ETHYLENE VAPORS
MTD Cost: Last PM: # Sel:
0 YTD Cost: Last Updated By: U432414
0 LTD Cost:
Date Installed: Date: 10/30/89
00048 17 434
222
PF1 = VIEW SPEC
PF2 -- PF3 = BROWSE
PF4 = PF5 = PF6 = MENU
PF7 * PREV RECORD PF8 = NEXT RECORD PF9 =
PF10 PF11 = PF12 s MAIN MENU
00 A 031?91 CONFIDENT! Al.
103 COMMAND ==>
INQUIRE FIXED EQUIPMENT
05/30/95 10:44
Equip ID PSV Pn-220 AB
Eq Desc: SAFETY VALVE #807951
Unit:
Cost Center OOOt.-3
Criticality: 01
Area: 8TORGE
Project:
Serial # 2824-X
Equip Code: _______________
Type:
ssoc Ser #
Equip Cond: ______________________________
Parent ID 2D-220 A
Grid: ______
Fleet MGMT?:
Install Dt
MFR Abbrev: ANDRSN
Model #:
Model Type: 33410L46-S
Model Size: 4" X L X 6"
GEMTS->
Prod / Process: PRODUCT DISTRIBUTION
2D-220 SYST
Eqp Group / Type
: PRESSURE VESSEL/VALVE
PRESSURE R
* * * SPECIFICATION TEXT * * *
INSPECTION SCHEDULE: 60 MONTHS
VALVE SET PRESSURE: 500 P8IG
OPERATING TEMP: -25 DEG. F
OPERATING PRESSURE: 450 PSIG
BACK PRESSURE:
0
PRODUCT: ETHYLENE VAPORS
MTD Cost:
0 YTD Cost:
0 LTD Cost:
Last PM: __________
Date Installed:
# Sel: 0
Last Updated By: NPL0467
GN-10
< RESET COMPLETE >
Date: 06/06/94
00048 . . 17 434
245
PF1 = VIEW SPEC PF2 = PF3 = BROWSE
PF4 = PF5 = PF6 = MENU
PF7 = PREV RECORD PF8 = NEXT RECORD PF9 =
PF10 =
PF11 = PF12 s MAIN MENU
DO A 031 CONFTDFNTIAL
103 COMMAND ==>
INQUIRE FIXED EQUIPMENT
05/30/95 10:44
Equip TD PSV 2D-220 BA
Eg Desc: SAFETY VALVE #807941
Unit:
Cost Cen'. i Serial #
ssoc Ser # Parent ID
0000063 2825-K
2D-220 B
criticality: 01
Area:
Equip Code:
Equip Cond:
Grid:
ST0R6E
Project
Type: ___ Spec: Fleet MGMT?:
xnstall Dt
MFR Abbrev ANDRSN
Model Type 33410L46-S
GEMTS->
Prod / Process:
Eqp Group / Type
:
Model #:
Model Size: 4" X L X 6"
PRODUCT DISTRIBUTION
2D-220 SYST
PRESSURE VESSEL/VALVE
PRESSURE R
* * * SPECIFICATION TEXT * * *
INSPECTION SCHEDULE: 60 MONTHS OPERATING TEMP: -25 DEG. F
VALVE SET PRESSURE: 500 PSIG OPERATING PRESSURE: 450 PSIG
BACK PRESSURE:
0
PRODUCT: ETHYLENE VAPORS
MTD Cost:
Last PM: # Sel:
0 YTD Cost:
____ _ 0 Last Updated By: NPL0467
0 LTD Cost: Date Installed: ______
Date: 06/06/94
GN- 10
< RESET COMPLETE >
00048 434
PF1 = VIEW SPEC
PF2 PF3 = BROWSE
PF4 = PF5 = PF6 = MENU
PF7 = PREV RECORD PF8 = NEXT RECORD PF9
PF10 =
PF11 = PF12 = MAIN MENU
(
DO a 031 ;?93
CONFXopTNTrAI
103 COMMAND ==>
INQUIRE FIXED EQUIPMENT
05/30/95 10:44
Equip ID: PSV 2D-220 BB
Eq Desc: SAFETY VALVE #802823
Unit:
_st Center: 0000063
Criticality: 01
Ar a: STOR6B
.17530 ject:
Serial #: 49409 M3
Equip Code:
Type:
ssoc Ser #:
Equip Cond:
Spec:
?arent ID: 2D-220 B
Grid:
Fleet MGMT?:
install Dt:
MFR Abbrev: CROSBY
Model Type: JO-34A
GEMTS->
Prod / Process:
Eqp Group / Type
:
***
Model #:
Model Size: 4" X L X 6"
PRODUCT DISTRIBUTION
2D-220 SYST
PRESSURE VESSEL/VALVE
PRESSURE R
SPECIFICATION TEXT * * *
INSPECTION SCHEDULE: 60 MONTHS
OPERATING TEMP: -25 DEG. F
BACK PRESSURE:
0
VALVE SET PRESSURE: 500 P8IG OPERATING PRESSURE: 450 PSIG PRODUCT: ETHYLENE VAPORS
MTD Cost: Last PM: # Sel:
0
0 YTD Cost: Last Updated By: U432414
0 LTD Cost:
Date Installed: Date: 10/30/89
GN-10
< RESET COMPLETE >
00048 17 434
1029
PF1 = VIEW SPEC PF2 = PF3 ~ BROWSE
PF4 = PF5 = PF6 = MENU
PF7 = PREV RECORD PF8 = NEXT RECORD PF9 =
PF10 =
PFll = PF12 * MAIN MENU
Do D-Otypr 7n'^9
103 COMMAND ==>
INQUIRE FIXED EQUIPMENT
05/30/95 10:44
Equip ID Cost Center
Serial # 'ssoc Ser #
Parent ID
PSV 2D-220 CA
Eq Desc: SAFETY VALVE #807942
Unit:
0000063
Criticality: 01
Area*
GE Project:
2826-K
Equip Code: _
Type:
____________ Equip Cond: ____ _________
Spec:
2D-2-0 C
Grid:
Fleet MGMT?:
install Dt
MFR Abbrev ANDRSN
Model Type 33410L46-S
GEMTS->
Prod / Process:
Model #;
Model Size: 4" X L X 6"
PRODUCT DISTRIBUTION
2D-220 SYST
Eqp Group / Type
: PRESSURE VESSEL/VALVE
PRESSURE R
* * * SPECIFICATION TEXT * * *
INSPECTION SCHEDULE: 60 MONTHS OPERATING TEMP: -25 DEG. F
VALVE SET PRESSURE: 500 PSIG OPERATING PRESSURE: 450 PSIG
BACK PRESSURE:
0
PRODUCT: ETHYLENE VAPORS
MTD Cost:
0 YTD Cost:
Last PM: ________
# Sel: 0
Last Updated By: NPL0467
0 LTD Cost:
Date Installed: Date: 06/06/94
GN-10
< RESET COMPLETE >
00048 17 434
259
PF1 = VIEW SPEC PF2 = PF3 = BROWSE
PF4 = PF5 = PF6 = MENU
PF7 = PREV RECORD PF8 = NEXT RECORD
PF9 *
PF10 = PF11 = PF12 =
(
c^rl;3^9
103 COMMAND ==>
INQUIRE FIXED EQUIPMENT
05/30/95 10:44
Equip ID: Cost Center:
Serial #: 'ssoc Ser #:
'arent ID:
PSV 2D-220 0000063 33608 M4
2D-220 C
CB Eq Desc: SAFETY VALVE #803291
Unit:
Criticality: 01
'Area: STOROE
Project:
Equip Code:
Typ :
Equip Cond:
Spec:
Grid:
Fleet MGMT?:
00048 17 434 ____
_nstall Dt:
MFR Abbrev: CROSBY
Model #:
Model Type: JO-33 A
Model Size: 4" X L X 6"
GEMTS->
Prod / Process: PRODUCT DISTRIBUTION
2D-220 8YST
Eqp Group / Type
: PRESSURE VESSEL/VALVE
PRESSURE R
* * * SPECIFICATION TEXT * * *
INSPECTION SCHEDULE: 60 MONTHS
VALVE SET PRESSURE: 500 PSIG
OPERATING TEMP: -25 DEG. F
OPERATING PRESSURE: 450 PSIG
BACK PRESSURE: MTD Cost:
0 0 YTD Cost:
PRODUCT: ETHYLENE VAPORS 0 LTD Cost:
152
Last PM:
Date Installed:
# Sel: 0
Last Updated By: U432414
GN-10
< RESET COMPLETE >
Date: 10/30/89
PF1 = VIEW SPEC
PF2 = PF3 = BROWSE
PF4 = PF5 = PF6 = MENU
PF7 = PREV RECORD PF8 = NEXT RECORD PF9
PF10 -
PF11 = PF12 =
(
00 A 031 296
CONFTDFNTT AL
103 COMMAND ==>
INQUIRE FIXED EQUIPMENT
05/30/95 10:44
Equip ID
Cost Center Serial #
ssoc Ser #
Parent ID
PSV 2D-220 DA
Eq Desc: SAFETY VALVE #807946
Unit
0000063
Criticality;* 01 , Area: STORGE
Project
2827-K
Equip Code: _
Type
Equip Cond: __________________________S_p__e_c
2D-220 D
Grid:
Fleet MGMT?
.nstall Dt
MFR Abbrev ANDRSN
Model Type 33410L46-S
GEMTS->
Prod / Process:
Eqp Group / Type
:
k It *
Model #:
Model Size: 4" X L X 6"
PRODUCT DISTRIBUTION
2D-220 SYST
PRESSURE VESSEL/VALVE
PRESSURE R
SPECIFICATION TEXT * * *
INSPECTION SCHEDULE: 60 MONTHS OPERATING TEMP: -25 DEG. F
VALVE SET PRESSURE: 500 PSIG OPERATING PRESSURE: 450 PSIG
BACK PRESSURE: MTD Cost:
0 0 YTD Cost:
PRODUCT: ETHYLENE VAPORS 0 LTD Cost:
Last PM:
Date Installed:
# Sel: 0
Last Updated By: NPL0467
Date: 06/06/94
GN-10
< RESET COMPLETE >
00048 17 434 _____
245
PF1 = VIEW SPEC PF2 = PF3 = BROWSE
PF4 = PF5 = PF6 = MENU
PF7 = PREV RECORD PF8 s NEXT RECORD
PF9 =
PF10 = PF11 = PF12 = MAIN MENU
(
DO C0NF
A 03 x tbp'hiT
7 lAl
103 COMMAND ==>
INQUIRE FIXED EQUIPMENT
05/30/95 10:45
Equip ID Cost Center
Serial #
'ssoc Ser # Parent ID
PSV 2D-220 DB 0000063 33608 M4
2D-220 D
Eq Desc: SAFETY VALVE #803294
Unit:
.-icality: 01
Area: STORGE
Project:
Equip Code:
Type:
Equip cond:
Spec:
Grid:
Fleet MGMT?:
-nstall Dt
MFR Abbrev CROSBY
Model Type JO-33 A
GEMTS->
Prod / Process:
Eqp Group / Type
:
Model #:
Model Size: 4" X L X 6"
PRODUCT DISTRIBUTION
2D-220 SYST
PRESSURE VESSEL/VALVE PRESSURE R
* * * SPECIFICATION TEXT * * *
INSPECTION SCHEDULE: 60 MONTHS
VALVE SET PRESSURE: 500 PSIG
OPERATING TEMP: -25 DEG. F
OPERATING PRESSURE: 450 PSIG
BACK PRESSURE:
0
PRODUCT: ETHYLENE VAPORS
MTD Cost:
0 YTD Cost:
0 LTD Cost:
Last PM:
Date Installed:
# Sel: 0
Last Updated By: U432414
Date: 10/30/89
GN-10
< RESET COMPLETE >
0Q048 434
4252
PF1 = VIEW SPEC
PF2 = PF3 = BROWSE
PF4 =
PF5 = PF6 = MENU
PF7 = PREV RECORD PF8 = NEXT RECORD PF9 =
PF10 -
PF11 PF12 = MAIN MENU
DO a CO/VFj^
103 COMMAND ==>
INQUIRE FIXED EQUIPMENT
05/30/95 10:45
Equip ID: PSV 2D-30 AA Cost Center: 0000063
Serial #: 34855 M4 'ssoc Ser #:
Parent ID: 2D-30 A
Eq Desc: 8AFETY VALVE #803169
Unit:
Criticality: 01
Ar a: ST0R6E
ct:
Equip Code:
Type:
Equip Cond: ____ _________
Spec:
Grid: _____
Fleet MGMT?:
.nstall Dt:
MFR Abbrev: CROSBY
Model Type: JO-35-A
GEMTS->
Prod / Process:
Model #:
Model Size: 4" X M X 6"
PRODUCT DISTRIBUTION
2D-30 A/B
Eqp Group / Type
: PRESSURE VESSEL/VALVE
PRESSURE R
* * * SPECIFICATION TEXT * * *
INSPECTION SCHEDULE: 60 MONTHS
VALVE SET PRESSURE: 300 PSIG
OPERATING TEMP: 80 DEG. F
OPERATING PRESSURE: 200 PSIG
BACX PRESSURE:
0
PRODUCT: PROPYLENE VAPORS
MTD Cost:
0 YTD Cost:
0 LTD Cost:
Last PM:
Date Installed:
# Sel: 1
Last Updated By: U432414
Date: 10/30/89
00048 17 434
PF1 = VIEW SPEC PF2 PF3 = BROWSE
PF4 = PF5 = PF6 = MENU
PF7 a PREV RECORD PF8 a NEXT RECORD PF9 =
PF10 =
PF11 PF12 a MAIN
D A 03lp C0Nr^frNTlAL
103 COMMAND ==>
INQUIRE FIXED EQUIPMENT
05/30/95 10:45
Equip ID: PSV 2D-30 BA
Eq Desc: SAFETY VALVE #803170
Unit: 00048
Cost Cente1-: 0000063
Criticality: 01
Area: ST IE
Project: 17
Serial #: 34855 M4
Equip Code: ____________
Type: 434
ssoc Ser #:
________ Equip Cond: ____ _____
Spec:
Parent ID: 2D-30 B
Grid:
Fleet MGMT?:
( install Dt:
MFR Abbrev: CROSBY
Model #:
Model Type: JO-35-A
Model Size: 4" X M X 6"
GEMTS->
Prod / Process: PRODUCT DISTRIBUTION
2D-30 A/B
Eqp Group / Type
: PRESSURE VESSEL/VALVE
PRESSURE R
* * * SPECIFICATION TEXT * * *
INSPECTION SCHEDULE: 60 MONTHS
VALVE SET PRESSURE: 300 PSIG
OPERATING TEMP: 80 DEG. F
OPERATING PRESSURE: 200 PSIG
BACK PRESSURE:
0
PRODUCT: PROPYLENE VAPORS
MTD Cost:
0 YTD Cost:
0 LTD Cost:
517
Last PM:
Date installed: ___
# Sel: 0
Last Updated By: U432414
GN-10
< RESET COMPLETE >
Date: 10/30/89
PF1 = VIEW SPEC PF2 = PF3 = BROWSE
PF4 =
PF5 = PF6 = MENU
PF7 = PREV RECORD
PF8 = NEXT RECORD PF9 =
PF10 -
PF11 = PF12 = MAIN MENU
(
on oonf* lDtHTTAI
103 COMMAND
INQUIRE FIXED EQUIPMENT
05/30/95 10:45
Equip ID: PSV 2D-30 AB
Eq Desc: SAFETY VALVE #803168
Unit:
Cost Center: 0000063
Criticality: 01
-Area: STORGE
Project:
Serial #: 34855 M4
Equip Code..;______________
Type:
\ssoc Ser #:
Equip Cond: ______________________________
Parent ID: 2D-30 A
Grid:
Fleet MGMT?:
Install Dt: __
MFR Abbrev: CROSBY
Model #:
Model Type: JO-35-A
Model Size: 4" X M X 6"
GEMTS->
Prod / Process: PRODUCT DISTRIBUTION
2D-30 A/B
Eqp Group / Type
: PRESSURE VESSEL/VALVE
PRESSURE R
* * * SPECIFICATION TEXT * * *
INSPECTION SCHEDULE: 60 MONTHS
VALVE SET PRESSURE: 300 PSIG
OPERATING TEMP: 80 DEG. F
OPERATING PRESSURE: 200 PSIG
BACK PRESSURE:
0
PRODUCT! PROPYLENE VAPORS
MTD Cost:
0 YTD Cost:
0 LTD Cost:
Last PM:
Date Installed:
# Sel: 0
Last Updated By: U432414
Date: 10/30/89
GN-10
< RESET COMPLETE >
00048 17 434
124
PF1 = VIEW SPEC PF2 = PF3 = BROWSE
PF4 PF5 = PF6 = MENU
PF7 a PREV RECORD
PF8 s NEXT RECORD PF9 =*
PF10 *
PF11 PF12 = MAIN MENU
INQUIRE FIXED EQUIPMENT
05/30/95 10:'
Equip ID: PSV 2D-30 BS
Eq Desc: SAFETY VALVE #803171
Unit:
Cost Center: 0000063
Criticali^v: 01
Area: STORGE
Project:
Serial #: 34855 M4
*uip Code:
Type:
'ssoc Ser #:
________ Equip Cond: ____ _____
Spec:
Parent ID: 2D-30 B
Grid:
Fleet MGMT?:
Install Dt:
MFR Abbrev: CROSBY
Model #:
Model Type: JO-35-A
Model Size: 4" X M X 6"
GEMTS->
Prod / Process: PRODUCT DISTRIBUTION
2D-30 A/B
Eqp Group / Type
: PRESSURE VESSEL/VALVE
PRESSURE R
* * * SPECIFICATION TEXT * * *
INSPECTION SCHEDULE: 60 MONTHS
VALVE SET PRESSURE: 300 PSIG
OPERATING TEMP: 80 DEG. F
OPERATING PRESSURE: 200 PSIG
BACK PRESSURE:
0
PRODUCT: PROPYLENE VAPORS
MTD Cost:
0 YTD Cost:
0 LTD Cost:
Last PM:
Date Installed: _________
# Sel: 0
Last Updated By: U432414
Date: 10/30/89
GN-10
< RESET COMPLETE >
00041 17 434
450
PF1 = VIEW SPEC PF2 * PF3 = BROWSE
PF4 = PF5 = PF6 = MENU
PF7 = PREV RECORD PF8 = NEXT RECORD PF9 s
PF10 = PF11 = PF12 = MAIN MENU
DO A 031302 CONFIDENTIAL
FIRE & EXPLOSION INDEX
AltEA/COUNTRY
LOCATION
DATE
USA
SITE
Louisiana
MANUFACTURING UNIT
Ptaquemlne
PROCESS UNIT
June 19,1995
Louisiana
PREPARED BY:
Light Hydrocarbon II DeMethanizer (2C-S1)
APPROVED BY: (BuyrlfWndnt)
BUILDING
Holly Reed
REVIEWED BY;
? REVIEWED SY: (TMhnotoffy C*mw)
64901 REVIEWED BY: (Safety A Loa* PmmWcti)
? MATERIALS IN PROCESS UNIT
?
?
Hydrogen, Methane,Ethy1enetEthane,PrDpane,Propytene
STATE OF OPERATION
SASIC MATERIAL^) FOR MATERIAL FACTOR
tTAATUF _X_POMMt OPERATION XUTDOWW
Ethylene
MATERIAL FACTOR (See Table 1 or Appendices A or B) Note requirements when unit temperatures over 140 l
24
1. General Process Hazards
Penalty Fac Penalty Fac tor Range tor Used (1)
Base Factor...............................................................................................
1.00
A. Exothermic Chemical Reactions
0.30 to 1.25
B. Endothermic Processes
0.20 to 0.40
C. Material Handling and Transfer
0.25 to 1.05
D. Enclosed or Indoor Process Units
0.25 to 0.90
E. Access
0.20 to 0.35
F. Drainage and Spill Control
75.690 oaltons 0.25 to 0.50
1.00 0.00 0.00 0.00 0.00 0.00 0.50
General Process Hazards Fictnr (FI)..........................................................................
1.50
2. Special Process Hazards Base Factor...............................................................................................
1.00
1.00
A Toxic Materials)
0.20 to 0.80
0.20
B. Sub-Atmospheric Pressure (< 500 mm Hg) C. Operation In or Near Flammable Range ___ INERTED _X_ NOT INERTED
0.50
0.00
1. Tank Farms Storage Flammable Liquids 2. Process Upset or Purge Failure 3. Always in Flammable Range D. Dust Explosion (See Table 3) E. Pressure (See Haure 21
0.50 0.30 0 80 0.25 to 2.00 Ooeratina Pressure 380 osic Relief Setting 575 Dsifl
0.00 0.00 0.00 0.00
0.60
F. Low Temperature G. Quantity of Flannmeble/Unstabie Material
0.20 to 0.30 Quantity 21.846 lb He 20.800 BTU/lb
0.30
1. Liquids or Gases in Process (See Figure 3) 2. Liquids or Gases in Storage (See Figure 4) 3. Combustible Solids in Storage, Dust in Process (See Figure 5) H. Corrosion and Erosion
0.10 to 0.75
0.94 0.00 0.00 0.10
1. Leakage Joints and Packing
0.10 to 1.50
0.10
J. Use of Fired Equipment (See Figure 6)
0.00
K. Hot Oil Heat Exchange System (See Table 5)
0.15 to 1.15
0.00
L. Rotating Equipment
0.50
0.00
Special Process Hazards Factor (F2)..--.....................--.............................
3.24
Process Unit Hazards Factor (FI x F2) " F3............................................................ Fite and Explosion Index (F3 x MF F&EI).................................................................
4.86
117
(1) For no penalty um 0.00.
D0 A 031303
C0NF1DPNTTAI-
FORU C-22340 Rw/01-M (471-000W) - |FIE-7 System Vsr-2. 1 - 8131/#4|
Print Data: 7/10/95
LOSS CONTROL CREDIT FACTORS
1. Process Control Credit Factor (Cl)
Faatura
*. Emergency Power b. Cooling c. Explosion Control d. Emergency Shutdown
Computer Control
Credit Factor Range 0.98 0.97 to 0.99 0.84 to 0.88 0.96 to 0.99 0.93 to 0.99
Credit Factor Used (2)
0.98 1.00 1.00 1.00 1.00
Feeture
r. Inert Ges
9- Operating Instructions/Procedures h. Reactive Chemical Review i. Other Process Hazard Analysis
Cradit Factor Range 0.94 to 0.96 0.91 to 0.99 0.91 to 0.98 0.91 to 0.98
Credit Factor Used (2)
1.00 1.00 0.91 0.98
Cl Value (3) | 0.874 |
2. Material Isolation Credit Factor (C2)
Feature
e. Remote Control Valves b. Dump/Blowdown
Credit Factor Range 0.96 to 0.98 0.96 to 0.98
Credit Factor Used (2)
1.00 1.00
Feature
c. Drainage d. Interlock
C2 Value (3) | 1.000 |
Credit Factor Range 0.91 to 0.97
0.98
Credit Factor Used (2)
1.00 1.00
3 Fire Protection Credit Factor (C3)
Feature
a. Leak Detection b. Structural Steel c. Fire Water Supply d. Special Systems a. Sprinkler Systems
Credit Factor Range 0 94 to 0.98 0 95 to 0.98 0.94 to 0.97
0.91 0.74 to 0.97
Credit Factor Used (2) 0.98
1.00 0.94 1.00 0.97
Feature
f. VNbter Curtains 9 Foam h. Hand Extinguishers/Monitore i. Cable Protection
C3 Value (3) | 0.867 j
Loss Control Credit Factor Cl x C2 x C3 (3)
| 0.7W"1
Credit Factor Range 0.97 to 0.98 0.92 to 0.97 0.93 to 0.98 0.94 to 0 98
Credit Factor Used (2)
1.00 1.00 0.97 1.00
PROCESS UNIT RISK ANALYSIS SUMMARY
1. Fire and Explosion Index (F&Ef)...........
(See Front)
117
2. Radius of Exposure.....................................
<n*7]
98
ft
3. Area of Exposure...................................................................
30135
sq.ft.
4. Value of Area of Exposure (1994 Doltara)............................................................................... $MM
5. Damage Factor.......................................................... 0.80
6. Base Maximum Probable Property Damage - (Base MPPD) [4x5]....................
7. Loss Control Credit Factor ......................... (See Above)]
0.76
$MM
8. Actual Maximum Probable Property Damage - (Actual MPPD) [6x7]....
................ JMM
9. Maximum Probable Days Outage - (MPDO)
112 days
10 Business Interruption - (Bh .......... ........ ...................... ..........* ...... ............................. JMM
27.55 21.94 16.62 78.23
| | | |
(2) For no credit factor enter 1.00
(3) Product of all factors used
Refsr to 'Fir* & Explosion Indox Hazard Classification Guide" (Form #471-00001) for details
BACK OF FORM C-22330
(471-OOBM) - (FIE-7 SyMwn V-21 S/3VMJ
Print Date: 7/1 (V95
0 A 031304 CONFTDFNTTAL
FIRE & EXPLOSION INDEX - DATA AND COMMENTS
Material Factor
Malarial la From Datataaa Malarial Nama - Briyrana Baaa Malarial Facer* 24 A^uatad Malarial Factor * 24 Had dComriudlon(BTU/Ii)-30000
M)> 1
Nf 4 Nr>2 Fiaari PoW (-F) Gaa BsaaigPcmrF)B-19S Precaaa UM Tamparatuia fF) * 39
Brntriarm Tamparatua <*F) * 1000000 Aiaolgniltm Tampantura (*F) * 943
Date For Poor Snocjfiad Matortel
Ctenaral Procaaa Hazard! A. Exedtatmrc Cnarmcil Paactora
Procaaa Ur* MOT A REACTOft anator NO EXOTHERM oceua (Panaty-O) Comma 0 B. Btdotlrannic Proriaaaa Procaaa Un* HOT A REACTOR --* Panaty-0 Comma 0 C. Malarial Homing and Tranaiar Nona d ora waordtgaOuaoonaappty (Panaty-O) Comma 0 D Endcaari or Indoor Procaaa Unto Procaaa a NOT ENdOSED (Pana*y-0) Comma 0 E. Accaaa Aceaaa daetmlrad adaquata (or amargancy aquMmate (PanalyHl) Comma 0 F Dratraga and spN Codtd FM, imdftad araa wWch aaowa apda to ipraad out (Panety-0 SO) Comma 0
todllProtwHlMm K Tone MaiariaM)
EquafetrttanttradtnaNn 0 SubJUmoadraric Praaaiaa (a 900 mm HgJ
Ctaalar man MO tnmHg (PanatyrrO) Comma 0 C. Oparaton In or Naar Flammarila Ranga Procaaa wB not raaclt Ota flammada ranga (Panaty*0). Comma 0 0. DoatExptoaajn Procaaa doaa not Orckjda data (Pana*y*0) Comma 0 E. Proaauta
Comma 0 F. LowTamparatiao
Procaaa uteiaa carrion ateal riatoa te ttanaMon tamparatua Comma 0 0. Quarrty d Fnmnranwuracada Matarial In Procaaa Comma 0 H. Conoalon and Emaion Corrodon ralaa riakrw 0.9 mmiyr VMTN (tear d pWng andlor Comma 0 1. Laakago - JoHa and Packing Minor Malaga terry d pump and gland aaa (Fanafy-O. to) Comma 0 J. uaodFMdEqufcmod DOES NOT atat Or ttra plant n Ora Procaaa Ut* Comma 0 K. Hot04HaatExeriangaSyatam Procaaa doaa nd uaa a rid dl ancrianga aydam, or ttra rid 04 Comma 0 L RoMng Eqdpmarrt No rdattig aqulpnwt daamad e ba a riazard (No Pardty) Comma 0
re-r anua wn-nai
'iOC> PrirtOata T/KV99
LOSS CONTROL CREDIT FACTORS - DATA AND COMMENTS
Process Control Credit Factor IC1)
a) Emergency Power Autorrwtic twitch to emergency power tor CRITICAL SERVICES Comma 0
b) Cooling No credit (Factor-1.0) Comma 0
c) Explosion Control No credit (F*etor1.0) Comma 0
d) Emergency Shutdown No credit (Faetor-i.Q)
Comma 0 e) Computer Control
No credit (Faetor*1.0) Comma 0 f) Inert Gas No credit (Factor-1.0) Comme 0 g) Operating IntbucUom/Proceduiea
Cornea 0 n) Reactive Chemical Review
Reactive Chemcal program a a continuing pert of operation*
Comm* 0 I) Other Process Hoard Analysis
Management of Change Review (Factor-0.96) Comm* 0
Material Isolation Credit Factor IC2I a) Remote Control Valves
No credit (Factor-1 .0) Comme 0 b) Dump/Blowdown No credit (Factor-1.0) Comme 0 c) Drainage No credit (Faetoml.O) Comme 0 d) interlock No credit (Factor-1.0) Comme 0
Fire Protection Credit Factor (C3I
a) Leak Detection Gat detectors alarm and Identity a zone only (Factor=0 96) Comma 0
b) Structural Steel No credit (Factor-1.0)
Comma 0 c) Fire Water Supply
Firefighting water can be supplied tor 4 hour* at 100 peig (7 Corrme 0 d) Special Systems No credit (Factor-1.0) Comme 0 a) Sprinkler System* Deluge system protects process (Fsctor-0.97) Comme 0 f) water Curtains No credit (Factor-1.0) Comme 0 g) Foam No credit (Factor-1.0) Comma 0 h) Hand Extmgurshars/Monttor* The procast a protected by monitor gun* (FacMr-0 97) Comme 0 i) Cable Protection No credit (Factor-1.0) Comma 0
pit-J Sy-w- v4.i mm)
DO A 031006 CONFIDENTIAL
Print Date: 7/10/95