Document YG0QwVD2XDeeDMpZLX4yYeVkn
FLOW^METER"SPECIFICATIONS
TAG DATE LAST REVISION PLANT DESCRIPTION
FE 13S1
14-DEC-89
14-DEC-69
BY:
CMP
h:l from vinyl
UJS
METERING DEVICE DATA ft**************-.* **-<1 *
PIPE I. D. FLANGE TYPE PRESSURE TAP MATERIAL BETA RATIO DEVICE
7. 931 INCHi-S 300# RF DOWNSTREAM 316 SS 0. 4699 SO EDGE ORIFICE- FLANGE TAPS
FLUID PROPERTIES
****************
FLUID 7)HCL GAS
VISCOSITY
O. 014 CP
CP/CV
1.410
BASE CONDITIONS
****************
SP GRAVITY : 1.2386
TEMPERATURE: 15. 56 DEGC
PRESSURE : 14.730 PSIA
DENSITY
0. 0963LB/CF
O.00154GM/CC
FLOWING CONDITIONS *********#*#**-*
MAX FLOW DIFFERENTIAL BORE
633480. 000 LBS /DAY CALCULATED
100. 00 IN. H20
INPUT
3. 750 INCHES
INPUT
PRESSURE TEMPERATURE
95. 00 PSIC 25. 00 DEGC .
DENSITY
0.7237 LB/F3
0.01159 GM/CC
LINE VELOCITY: 29.392 FT/SEC
PIPE REYNOLDS NO.
1503810. (CALCULATED AT 1007. FLOW)
UNRECOVERABLE PRESSURE LOSS: l. 53 PSI
(CALCULATED AT 757. FLOW)
*
20111.3 KWH/YR 642.56 DOLLARS/YR
KQB2:
0.13625
Y : 1.00325
FR : 1.00037 FA : 1.00012
METER CONSTANT FOR MASS FLOW PACKAGE #*#******#*##* * ** m *** ***##*##**
FLOW* 779219. 3? 5 "SORT(HTlNHOEN) * SCF /DAY
CONFIDENTIAL 00 007350
MASS- FLOW
MF
i -s5 i
TYPE
3 ENTRY
4 CAL 0 OK
DATA
20265. 9S633 Lc/H
HCL FROM VINYL 2 TO CMP
METER CONSTANT
3127. 6960
IN SERVICE
INPUT DATA SPAN
FI 1351
50. 56790 TK20
ICO. 00
EASE
TYPE 13 ENTRY 80 CAL 48 OK HCL FROM VINYL 2 FLOW DP
0. 00
IN SERVICE
.'IS1TY DATA
DN 1351 0. 84438 #/CF
TYPE
2 ENTRY
4 CAL 7 OK IN SERVICE
L FROM VINYL 2 PMTR DENSITY
DEN TEMP DATA SPAN
TI 1353
-1.39583 DEGC
50. 00
EASE
TYPE 13 ENTRY B4 CAL 0 OK HCL FROM VINYL 2 TEMPERATURE
0. 00
IN SERVICE
DEN PRESS
PI
1382
DATA
100.07405 PSIG
SPAN
149. 99 --BASE
TYPE 13 ENTRY 81 CAL 0 OK HCL FROM VINYL 2 PRESSURE
0. 00
IN SERVICE
CONFTDFNTTAL DO 007351
l_uuiaihimh mviaiuh
FLOW METER SPECIFICATIONS
TA DATE LAST REVISION PLANT DESCRIPTION
FE 1351A 14-DEC-8? 14-DEC-8? BY: JJS CMP HCL FROM VINYL 2 (REDUNDANT)
METERING DEVICE DATA * ******************
PIPE I. D. FLANGE TYPE PRESSURE TAP MATERIAL BETA RATIO DEVICE
7.981 INCHES 300# RF DOWNSTREAM 316 SS 0. 4699 SO EDGE ORIFICE- FLANGE TAPS
FLUID PROPERTIES ****************
FLUID 7>HCL AS
VISCOSITY
0.014
CP
CP/CV
1.410
BASE CONDITIONS ****************
SP GRAVITY : 1.2586
TEMPERATURE: 15.56 DEGC PRESSURE : 14. 730 PSIA
DENSITY
0. 0963LB/CF
0.00154GM/CC
FLOWING CONDITIONS ******************
MAX FLOW DIFFERENTIAL BORE
633480. 000 LBS /DAY 100. 00 IN. H20 3. 750 INCHES
CALCULATED INPUT INPUT
PRESSURE TEMPERATURE
95. 00 PSIC 25. 00 DEGC
DENSITY
0. 7237 L8/F3
0.01159 GM/CC
LINE VELOCITY: 29.392 FT/SEC
PIPE REYNOLDS NO.
1503810.
(CALCULATED AT 100X FLOW)
UNRECOVERABLE PRESSURE LOSS:
1.53 PSI
(CALCULATED AT 757. FLOW)
*
20111.3 KWH/YR 642. 56 DOLLARS/YR
K0B2:
0.13625
Y : 1.00325
FR : 1.00037 FA : 1.00012
METER CONSTANT FOR MASS FLOW PACKAGE ************************************
FLOWs
3127.-1^* SQRT(H(IN)*DEN> - LBS /HR
nnu ruCMTCAl IICA
CONFIDENTIAL DO 00735?
MASS P LOW Mc 1 r * **
TYPE
3 ENTRY 67 CAL 0 OK
DATA
2 0733. 51172 L3/H
HCL FROM VINYL II (METER 2)
MEfER CONSTANT
3127.69604
IN SERVICE
INPUT DATA SPAN
FI 1351A
51.75504 IH20
100. 00
EASE
TYPE 13 ENTRY 408 CAL 48 OK HCL FROM VINYL II (METER 2)
0. 00
IN SERVICE
,NSITY DATA
DEN TEMP DATA SPAN
DN 1351 0. 84393 4/CF
TYPE
2 ENTRY
4 CAL 7 OK IN SERVICE
L FROM VINYL 2 PMTR DENSITY
------- - 1 '7'K'Z (-1. 55035 DEGC3
50-00--------
TYPE 13 ENTRY 84 CAL 0 OK HCL FROM VINYL 2 TEMPERATURE
0. 00
IN SERVICE
DEN PRESS
PI
1382
DATA
99. 88656 PSIG
SPAN
149.99
2AEE
TYPE 13 ENTRY 81 CAL O OK HCL FROM VINYL 2 PRESSURE
0. 00
IN SERVICE
CONFTDFNTTAl 00 007353
LOUISIANA UiViSiUN
FLOW METER SPECIFICATIONS
TAG DATE LAST REVISION PLANT DESCRIPTION
FE 2032
14-DEC-S9
14-DEC-B9
BY: EBB
CMP
HCL PURIFICATION FEED
M**E*T*E*R*IN*G***D*E*V*IC*E* xD*A*T*A*
F**L*U*ID***P*R*O*P*E*R*T*IE**S
FLUID DIDEAL GAS
PIPE I. D.
7.981 INCHES
VISCOSITY
0. 010
CP
FLANGE TYPE PRESSURE TAP MATERIAL
3004 RF DOWNSTREAM 316 SS
CP/CV
BASE CONDITIONS ****************
1. 400
BETA RATIO
0.4963
SP GRAVITY : 1 . 2600
DEVICE
SQ EDGE ORIFICE- FLANGE TAPS
TEMPERATURE: 15. 36 DEGC
PRESSURE
14.730 PSIA
DENSITY
0. 0964LB/CF
0. 001S4GM/CC
FL*O*W**IN*G***C*O*N*D*I*T*IO*N**S
MAX FLOW DIFFERENTIAL BORE
2S334. 027 LBS /HR 100. 00 IN. H20 3. 961 INCHES
CALCULATED INPUT INPUT
PRESSURE TEMPERATURE
DENSITY
95. 00 PSIG 35. 00 DECC
0.6730 LB/F3
O.0107S GM/CC
LINE VELOCITY: 34.257 FT/SEC
PIPE REYNOLDS NO.
2281866.
(CALCULATED AT 100X FLOW)
UNRECOVERABLE PRESSURE LOSS: 1.49 PSI
(CALCULATED AT 757. FLOW)
*
22740.5 KWH/YR 726. 56 DOLLARS/YR
K0B2:
0.15311
FR : 1.00029
Y : 1.00316 FFV. 1.00000
FA : 1.00044
*M*E*TE*R***C*O*N*S*T*A*N*T*F*OMR***MA*S*S***FL*O*W**P*A*C*K*A*G**E
FLOW
TR)*DEN) - LBS /HR
CONFTDFNTTAl 00 007354
MASS FLOW MF 2052
TYPE
3 ENTRY 30 CAL
DATA
21764.61914 LG/H
HCL PURIFICATION FEED
METER CONSTANT
3509. 87983
0 OK
IN SERVICE
INPUT DATA C7l1AN
FIC 2052
47. 07639 IH20
100. 00
BASE
TYPE 13 ENTRY 32 CAL 32 OK HCL FLOW TO PURIFICATION
0. 00
IN SERVICE
DENSITY DATA
DN 2052 0. 80207 #/CF
TYPE
2 ENTRY 20 CAL 7 OK IN SERVICE
L TO PURIFICATION
DEN TEMP DATA SPAN
TI 2051
9. 46156 DEGC
99. 98
BASE
TYPE 13 ENTRY 16 CAL 0 OK IN SERVICE HCL TO PURIFICATION TEMPERATURE
-20. 00
DEN PRESS
PI
2053
DATA
99. 49089 PSIG
SPAN
199. 98
EASE
TYPE 13 ENTRY 31 CAL 0 OK INCOMING HCL HEADER PRESSURE
0. 00
IN SERVICE
C,U7 )
^ n IS V
T
r
1 Al DO 007355
3LT-F10 HELP | VT-100 | FDX J 9600 N81 | LOG CLOSED | PRT OFF | CR
3SS FLOW
MF
2052
TYPE
3 ENTRY 30 CAL
VTA 21691.93164 LE/H
HCL PURIFICATION FEED
ETER CONSTANT
3509.87988
0 OK
IN SERVICE
MPL ATA =-AN
FIC 2052
50.84722 IH20
100.00
BASE
TYPE 13 ENTRY 32 CAL 32 OK HCL FLOW TO PURIFICATION 0.00
IN SERVICE
ENSITY ATA
DN 2052 0.75067 #/CF
TYPE
2 ENTRY 20 CAL 7 OK IN SERVICE
L TO PURIFICATION
EN TEMP ATA =>AN
TI 2051 23.78792 DEGC 99.98 BASE
TYPE 13 ENTRY 16 CAL 0 OK IN SERVICE HCL TO PURIFICATION TEMPERATURE
-20.00
EN PRESS
PI 2053
TYPE 13 ENTRY 31 CAL 0 OK
ATA
98.32433 PSIG
INCOMING HCL HEADER PRESSURE
^AN
199.98
BASE
0.00
DUTPUT TO PRINTER CY OR N ,D:ND ?
"1FT31 -- Exiting due to ERROR 3
; PC = 000002
in "SEEMF " at 391
IN SERVICE
CR
ALT-F10 HELP | VT--100 j FDX | 9600 NB1 | LOG CLOSED | PRT OFF | CR | CR
5AN
199.98
BASE
0.00
DUTPUT TO PRINTER CY OR N rD:N3 ?
*1FT31 -- Exiting due to ERROR 3
t PC = 000002
in "SEEMF " at 391
5MF MF929
ASS FLOW
MF
929
TYPE
3 ENTRY 39 CAL
ATA
0.00000 LB/H
30# STEAM FLOW TO iCMP
ETER CONSTANT
10000.04004
0 OK
IN SERVICE
NPUT ATA
FR 929 -13.96471 IH20
TYPE 10 ENTRY 35 CAL 0 OK IN SERVICE 30# STEAM FLOW TO CMP
ENS*.< ATA
DN 929 0.10590 #/CF
TYPE
1 ENTRY 43 CAL 0 OK IN SERVICE
# STEAM FLOW CONSTANT DENSITY
CONFTOFNTIAL
DUTPUT TO PRINTER CY OR N ,D:ND ? MFT31 -- Exiting due to ERROR 3
DO 007356
t PC = 000002 i n "PFFMF " at 9Q1
LUUiaiHIXtt U1V1S1UN
FLOW METER SPECIFICATIONS
TAG DATE LAST REVISION PLANT DESCRIPTION
FE 2187 14-DEC-8? 14-DEC-8? CrtP C-70 FEED
BY: EBB
METERING DEVICE DATA ***************** **
PIPE I. D. FLANGE TYPE PRESSURE TAP MATERIAL BETA RATIO DEVICE
6. 065 INCHES 300# RF DOWNSTREAM 316 SS 0. 6075 SO EDGE ORIhICE- FLANGE TAPS
FLUID PROPERTIES
****************
FLUID DIDEAL GAS
VISCOSITY
0. 010
CP
CP/CV
1. 400
BASE CONDITIONS ****************
SP GRAVITY : 1 . 2600
TEMPERATURE: 15.60 DEGC
PRESSURE.
14.730 PSIA
DENSITY
0.0964LB/CF
0.00154GM/CC
FLOWING CONDITIONS *************** ***
MAX FLOW DIFFERENTIAL BORE
36058.570 LBS /HR 100. 00 IN. H20 3. 684 INCHES
CALCULATED INPUT INPUT
PRESSURE TEMPERATURE
DENSITY
222. 00 PSIC 75. 00 DEOC
1. 2851 LB/F3
0. 02059 GM/CC
LINE VELOCITY: 33.849 FT/SEC
PIPE REYNOLDS NO.
3755085.
(CALCULATED AT 100% FLOW)
UNRECOVERABLE PRESSURE LOSS: 1.27 PSI
(CALCULATED AT 757. FLOW)
*
12722.8 KWH/YR 406. 49 DOLLARS/YR
K0132:
0.24006
FR : 1.00033
Y : 1.00132 FPV: 1. OCOOO
FA : 1.00174
METER CONSTANT FOR MASS FLOW PACKAGE ******************** ***** ***********
FLOW
3180 .':B39 * SQRT(H( IN)*DEN) LBS /HR
CONFIDENTIAL DO 007357
MASS FLOW MF 2187
TYPE
3 ENTRY
DATA
18900.00000 LF/H
C-70 FEED
METER CONSTANT
3186.61011
31 CAL 0 OK OUT OF SERVICE
INPUT DATA f an
DENSITY DATA
DEN TEMP
TI 2185
DATA
60.12644 DEGC
SPAN
199.98
BASE
13 ENTRY FEED
59 CAL 5 OK IN SERVICE
2 ENTRY FEED
(21 CAL 7 OK IN SERVICE
TYPE 13 ENTRY 62 CAL 0 OK K-55 DISCHARGE TEMPERATURE
0. 00
IN SERVICE
DEN PRESS
PIC 2186
DATA
221.82431 PSIG|
SPAN
299. 99
BASE
TYPE 13 ENTRY 61 CAL 0 OK K-55 DISCHARGE CONTROL PRESS
--frrOO"
IN SERVICE
V/. cJ -c. 'Z?2S PJ-'C^_^3
CNFTr>FNTTAt 00^358
LOUISIANA DIViSiUN
FLOW METER SPECIFICATIONS
TAG DATE LAST REVISION PLANT DESCRIPTION
FE 2215
14-DEC-89
14-DEC-8?
BY:
CMP
C-70 0. H. FLOW
JJS
METERING DEVICE DATA *#*****#******< **
PIPE I. D. FLANGE TYPE PRESSURE TAP MATERIAL BETA RATIO DEVICE
6 065 INCHES 300# RF DOWNSTREAM 316 5S 0. 5560 SO EDGE ORIFICE- FLANGE TAPS
FLUID PROPERTIES
a****##****#***
FLUID DIDEAL GAS
VISCOSITY
0.010
CP
CP/CV
1. 400
BASE CONDITIONS
****************
SP GRAVITY : 1.2600
TEMPERATURE: 15. 60 DEGC
PRESSURE : 14. 730 PSIA
DENSITY
0. 0964LB/CF
0.00154GM/CC
FLOWING CONDITIONS #*#*###**#******-**
MAX FLOW DIFFERENTIAL BORE
34'U7.7?7 LBS /HR 100. 00 IN. H20 3. 372 INCHES
CALCULATED INPUT INPUT
PRESSURE TEMPERATURE
222. 00 PSIG -19.00 DEGC
DENSITY
1.7604 LB/F3
0.02820 GM/CC
LINE VELOCITY: 27.070 FT/SEC
PIPE REYNOLDS NO.
3584216. (CALCULATED AT 100X FLOW)
UNRECOVERABLE PRESSURE LOSS: 1.38 PSI
(CALCULATED AT 7SX FLOW)
*
9598.8 KWH/YR 306.68 DOLLARS/YR
K0B2:
0.19636
FR : 1.00024
Y ; 1. 00140 FPV. 1. 00000
FA : 0.99874
METER CONSTANT FOR MASS FLOW PACKAGE *##***#*#***##***#**##****#***#'#**#
FLOW**
-2594.TWT SQRT(H (IN) *DEN) - LBS /HR
< *'
nnu rucMtrAi tie a
CONFTDFNTTAl DO 007359
MASS' FLOW MF 2215
TYPE
3 ENTRY
DATA
2 1808.55078 LE/H
C-70 0. H. FLOW
NE T ER CONSTANT
2594.38989
32 CAL
0 OK
IN SERVICE
INPUT
DATA cn t\|\|
FI 2215
34. 05555 IH20
100. 00
BASE
TYPE 13 ENTRY 20 CAL 32 OK C-70 OVERHEAD FLOW
0. 00
IN SERVICE
DENSITY DATA
DN 2215 2. 07658 *t/CF
TYPE
2 ENTRY 22 CAL 7 OK IN SERVICE
70 0. H. FLOW
DEN TEMP DATA SPAN
TI 2201
-18.54249 DEGC
79. 99
EASE
TYPE 13 ENTRY 36 CAL 0 OK C-70 OVERHEAD TEMPERATURE
40. 00
IN SERVICE
DEN PRESS
PIC 2200
DATA
223. 07425` PSIG
SPAN
299. 99
BASE
TYPE 13 ENTRY 42 CAL C-70 TOP PRESSURE
0. 00
0 OK
IN SERVICE
CONFTDFNTTAl D0 0073&0
l_UU 1S1 MIMfl UlViSl UIM
FLOW METER SPECIFICATIONS
TAG DATE LAST REVISION PLANT DESCRIPTION
FE 2182 14-DEC-89 14-DEC-89 BY; EBB
CKP RECYCLE FLOW TO E-51
METERING DEVICE DATA ********************
PIPE I. D. FLANGE TYPE PRESSURE TAP MATERIAL BETA RATIO DEVICE
6, 065 INC Hr S 3004 RF DOWNSTREAM 316 SS 0. 5981 SQ EDGE ORIFICE- FLANGE TAPS
FLUID PROPERTIES
****************
FLUID DIDEAL GAS
VISCOSITY
O.010
CP
CP/CV
1. 400
BASE CONDITIONS
****************
SP GRAVITY 1. 2600
TEMPERATURE 15.60 DEGC
PRESSURE
14. 730 PSIA
DENSITY
0. 0964LB/CF
0. 00154GM/CC
FLOWING CONDITIONS ******************
MAX FLOW DIFFERENTIAL BORE
343S9.273 LBS /HR 100. 00 IN. H20 3.627 INCHES
CALCULATED INPUT INPUT
PRESSURE TEMPERATURE
200. 00 PSIC 40. 00 DECS
DENSITY
1.2959 LS/F3
0.02076 GM/CC
LINE VELOCITY: 37. 275 FT/SEC
PIPE REYNOLDS NO.
3633317. (CALCULATED AT 100% FLOW)
UNRECOVERABLE PRESSURE LOSS:
1.29 PSI
(CALCULATED AT 757. FLOW)
*
12398.8 KWH/YR 396. 14 DOLLARS/YR
K0B2:
0.23153
FR : 1.00032
Y : 1.00147 FPV: 1.00000
FA : 1.00060
M**E*TE*R**C*O**N*S*TA*N*T**FxO*R**M*A*S*S**F*L*O*W**P*A*C*K*A*G*E*
FLOW*
3064.-773'**-SQRT(H(IN)*DEN) * LBS /HR
nnu pmfmtcai ura
CONFTDFNTT At 00 007361
MASH FLOW MF 2182
TYPE
3 ENTRY 33 CAL 0 OK IN SERVICE
DATA
6685. 87842 LS/H
RECYCLE FLOW TO E--51 (HCL PURIF)
METER CONSTANT
3068. 27002
INPUT DATA `--''AN
FI 2 5 82
3.27431 IH20
100. 00
3AE
TYPE 13 ENTRY 64 CAL 32 OK IN SERVICE RECYCLE FLOW TO E-51 (HCL PURIFI
0. 00
DENSITY DATA
DN 2182 1.43794 #/CF
TYPE
2 ENTRY
CYCLE FLOW
23 CAL 7 OK IN SERVICE
DEN TEMP DATA SPAN
TI 2177
31. 96074 DEGC
99. 98
EASE
TYPE 13 ENTRY 58 CAL 0 OK E-72 OUTLET TEMPERATURE
0. 00
IN SERVICE
DEN PRESS
PIC 2179
DATA
200. 07520 PSIG
SPAN
299.99
BASE
TYPE 13 ENTRY 63 CAL HCL PRESSURE TO USERS
0. 00
0 OK
IN SERVICE
vj,^f iJ c<\u 7
40, IS0-C
2.4?
p-
AV DO 00736?
MASS FLOW MF 2182
TYPE
3 ENTRY 33 CAL 0 OK IN SERVICE
DATA
12405.62109 LB/H
RECYCLE FLOW TO E-51 (HCL PURIF)
METER CONSTANT
3063 27002
INPUT DATA FDAN
FI 2182
11. 66319 IH20
100. 00
BASE
TYPE 13 ENTRY 64 CAL 32 OK IN SERVICE RECYCLE FLOW TO E-51 (HCL PURIFI
0. 00
DENSITY DATA
DN 2182 1.39168 #/CF
TYPE
2 ENTRY
CYCLE FLOW
23 CAL 7 OK IN SERVICE
DEN TEMP DATA SPAN
TI 217 7
40. 080491 DEGC
99. 98
BASE
TYPE 13 ENTRY 58 CAL 0 OK E-72 OUTLET TEMPERATURE
0. 00
IN SERVICE
DEN PRESS
PIC 2179
DATA
199.99187 PSIG
SPAN
299. 99
BASE
TYPE 13 ENTRY 63 CAL MCL PRESSURE TO USERS
0. 00
0 OK IN SERVICE
,
DO 0073&3
mass PLOW
f'l r
21S2
TYPE
3 ENTRY 33 CAL 0 OK IN SERVICE
DATA
5062. 75635 LB/H
RECYCLE FLOW TO E-51 (HCL PURIF)
METER CONSTANT
3063.2700 P
INPUT DATA SPAN
FI 21S2
1. 99653 1^20
100. 00
EASE
TYPE 13 ENTRY 64 CAL 32 OK IN SERVICE RECYCLE FLOW TO E-51 (HCL PURIFI
0. 00
N3ITY DATA
DN 2182 1. 42307 t/CF
TYPE
2 ENTRY
CYCLE FLOW
23 CAL 7 OK IN SERVICE
DEN TEMP DATA SPAN
TI 2177
37. 69913 DEOC
99. 9e
EASE
TYPE 13 ENTRY 58 CAL 0 OK E--72 OUTLET TEMPERATURE
0. 00
IN SERVICE
DEN PRESS
PIC 2179
DATA
202. 40842 PS 10
SPAN
299. 99 " "BASE
TYPE 13 ENTRY 63 CAL HCL PRESSURE TO USER'S
0. 00
0 OK
IN SERVICE
\
CONFTDFNTT At, DO 007364
L.uwiaiMiMn uiviaiuM FLOW METER SPECIFICATIONS
TAG DATE LAST REVISION PLANT DESCRIPTION
FE 2190
14-DEC-6?
14-DEC-S9
BY:
CMP
HCL TO SOLVENTS
EBB
METERING DEVICE DATA ********************
PIPE I. D. FLANGE TYPE PRESSURE TAP MATERIAL BETA RATIO DEVICE
6. 065 INCHES 300 RF DOWNSTREAM 316 SS
0. 4741 S3 EDGE ORIFICE- FLANGE TAPS
FLUID PROPERTIES
****************
FLUID DIDEAL GAS
VISCOSITY
0. 010
CP
CP/CV
1.400
BASE CONDITIONS ****************
SP GRAVITY : 1.2600
TEMPERATURE: 15. 60 DEGC
PRESSURE : 14.730 PSIA
DENSITY
0.0964LB/CF
0.00154GM/CC
FLOWING CONDITIONS **-****************
MAX FLOW DIFFERENTIAL BORE
506363. 812 LBS /DAY 100. 00 IN. H20 2.8753 INCHES
CALCULATED INPUT INPUT
PRESSURE TEMPERATURE
200. 00 PSIG 35. 00 DEGC
DENSITY
1.3170 LB/F3
0.02110 GM/CC
LINE VELOCITY: 22. 181 FT/SEC
PIPE REYNOLDS NO.
2197165. (CALCULATED AT 100% FLOW)
UNRECOVERABLE PRESSURE LOSS: 1.53 PSI
(CALCULATED AT 757. FLOW)
*
8723.9 KWH/YR 278. 73 DOLLARS/YR
KQB2:
0.13890
FR : 1.00022
Y : 1.00164 FPV. 1.00000
FA : 1.00044
METER CONSTANT FOR HASS FLOW PACKAGE ******************** ******* **********
FLOW=
1838.496 * SQRT(H(IN)*DEN) * LBS /HR
nnu rurM t r ai I leA
CONFTDFNTr^ 00 007365
MASS FLOW MF 2190
TYPE
3 ENTRY 43 CAL 0 OK
DATA
14074.5312 5 LB/H
HCL TQ SOLVENTS II PAYMETER
METER CONSTANT
1S3 ?. 94995
IN SERVICE
INPUT DATA SPAN
FI 2190
41. 7235 3 IH20
ICO. 00
BASE
TYPE 13 ENTRY 97 CAL 48 OK HCL TO SOLVENTS II FLOW
0. 00
IN SERVICE
T\ .NS1TV DATA
DN 2X90 1.44338 #/CF
TYPE
2 ENTRY 25 CAL 7 OK IN SERVICE
L TO SOLVENTS II DENSITY
DEN TEt'F DATA SPAM
TI 21C9
27. 61826 DEGC
99. 95
BASE
TYPE 13 ENTRY 99 CAL 0 OK HCL TO SOLVENTS TEMPERATURE
0. 00
IN SERVICE
PRES S PI 2191
i_' r *
197. 14824 PSIG
SPAN
299. 99 "" 'BASE
TYPE 13 ENTRY 98 CAL 0 OK HCL TO SOLVENTS II PRESSURE
0. 00
IN SERVICE
CONFIDENTIAL do 007366
LUUlblANA UiVl&iUlM
FLOW METER SPECIFICATIONS
TAG
DATE LAST REVISION PLANT DESCRIPTION
FE 2180 14-DEC-89 14-DEC-B9 BY: JJS CMH HCL TO SOLVENTS PAYMETER
METERING DEVICE DATA ft************* a>
PIPE I. D. FLANGE TYPE PRESSURE TAP MATERIAL BETA RATIO DEVICE
6 065 INCHES 3004 RF DOWNSTREAM
316 S5 0. 4741 S3 EDGE ORIFICE- FLANGE TAPS
FLUID PROPERTIES
**#*******#*##
FLUID DIDEAL GAS
VISCOSITY
0. 010
CP
CP/CV
1.400
BASE CONDITIONS
*#-******#****
SP GRAVITY 1. 2600
TEMPERATURE 15. 60 DEGC
PRESSURE DENSITY
14. 730 PSIA
0. 0964LB/CF 0. 00154GM/CC
FLOWING CONDITIONS **#***#********+*
MAX FLOW DIFFERENTIAL BORE
522559.937 LBS /DAY 100. 00 IN. H20 2.8753 INCHES
CALCULATED INPUT INPUT
PRESSURE TEMPERATURE
200. 00 PSIC 35. 00 DECC
DENSITY
1.4026 LB/F3
0.02247 GM/CC
LINE VELOCITY; 21.493 FT/SEC
PIPE REYNOLDS NO.
2267442. <CALCULATED AT 100% FLOW)
UNRECOVERABLE PRESSURE LOSS:
1.53 PSI
(CALCULATED AT 757. FLOW)
*
8453.3 KWH/YR 270.08 DOLLARS/YR
K0B2;
0.13890
FR : 1.00021
Y : 1.00164 FfV: 1.03200
FA : 1.00044
METER CONSTANT FOR MASS FLOW PACKAGE
**#**********#* a
*#*** a-****##*###
FLOW*
1838. 470 * SGRT(H(IN)*DEN) * LBS /HR
T*m.l rUCMTTAI I icA
C0NFT0FNT1M DO 007367
MASS FLOW MF 2180
DATA
14191.14844 LF/H
TVPE
3 ENTRY 42 CAL 0 OK
HCL TO SOLVENTS FROM CMP
METER CONSTANT
1837.94995
IN SERVICE
INPUT DATA SPAN
FI 2130
39.44102 IH2D
100.00
DASE
TYPE 13 ENTRY 95 CAL 48 OK HCL TO SOLVENTS I FLOW
0. 00
IN SERVICE
. _NSITV DATA
DN 2180 1. 48678 */CF
TYPE
2 ENTRY 24 CAL 7 OK IN SERVICE
L TO SOLVENTS I DENSITY
DEN TENP DATA SPAN
TI 2189
27.61826 DEGC
99. 98
EASE
TYPE 13 ENTRY 99 CAL 0 OK HCL TO SOLVENTS TEMPERATURE
0. 00
IN SERVICE
DEN PRESS PI 2163
DATA
202. 96049 FSIG
SPAN
299. 99 ' BASE
TYPE 13 ENTRY 96 CAL 0 OK HCL TO SOLVENTS I PRESSURE
0. 00
IN SERVICE
OONFTDFNTTAl DO 007368
LUUlSlMWft U1V131UN
FLOW METER SPECIFICATIONS
TAG DATE LAST REVISION PLANT DESCRIPTION
FE 2181A
14-DEC-89
14-DEC-69
BY: JJS
Cf'iP
HCL TO CMP PAYMETER
METERING DEVICE DATA * ******************
PIPE I. D. FLANGE TYPE PRESSURE TAP MATERIAL BETA RATIO
DEVICE
6. 065 INCHES 300* RF DOWNSTREAM 316 SS 0. 4288 SQ EDGE ORIFICE- FLANGE TAPS
FLUID PROPERTIES
****************
FLUID DIDEAL GAS
VISCOSITY
O. 010
CP
CP/CV
1.400
BASE CONDITIONS ****************
SP GRAVITY : 1.2600
TEMPERATURE: 15.60 DEGC
PRESSURE : 14. 730 PSIA
DENSITY
0.0964LB/CF
0. 00154GM/CC
FLOWING CONDITIONS ***************<**
MAX FLOW DIFFERENTIAL BORE
542365 500 LBS /DAY 175.00 IN. H20 2 6007 INCHES
CALCULATED INPUT INPUT
PRESSURE TEMPERATURE
DENSITY
200. 00 PSIO 35 00 DEGC
1. 3170 L8/F3
0.02110 CM/CC
LINE VEi-CCITY: 23.780 FT/SEC
PIPE REYNOLDS NO.
2355550. (CALCULATED AT 100*4 FLOW)
UNRECOVERABLE PRESSURE LOSS:
2. SO PSI
(CALCULATED AT 75*4 FLOW)
*
17162. 7 KWH/YR 548.35 DOLLARS/YR
K0B2:
0.11243
FR : 1.00015
Y : 1.00293 FPV. 1.00000
FA : 1.00044
METER CONSTANT FOR MASS FLOW PACKAGE **************** *** ***** ************
"FLOW*
14e9.-955 * SQRT(H( IN)*DEN) * LBS /HR
tm-ii.i rucMTr&i lie*
coiyfidfnttai
DO 007369
mas;j plow rv 21S1 A
TYPE
3 ENTRY 17 CAL
DATA
5934.71045 LB /H
HCL TO CMP (METER 2)
MET PR CONSTANT
I49 5799a
0 OK
IN SERVICE
INPUT DATA SPAN
FI 161A
11.37628 1K2Q
175. 00
EASE
TYPE 13 ENTRY 405 CAL 48 OK HCL TO CMP (METER 2)
0. 00
IN SERVICE
v -NS1TY DATA
DN 2181 1. 17-166 #/CF
TYPE
2 ENTRY 26 CAL 7 OK IN SERVICE
L TO CMP DENSITY
DEM TEMP DATA SPAN
TI 2187
28. 66661 DEGC
99. 98
EASE
TYPE 13 ENTRY 102 CAL HCL TO CMP TEMPERATURE
0. 00
0 OK
IN SERVICE
DEN PRESS! PI 2192
DATA
161. 14770 PSIG
SPAN
299. 99 -BASE
TYPE 13 ENTRY 101 CAL HCL TO CMP PRESSURE
0. 00
0 OK
IN SERVICE
conf
007370 00
LOUISIANA DiViSiUIN
FLOW METER SPECIFICATIONS
TAG DATE LAST REVISION PLANT DESCRIPTION
FE 2181
14-DEC-87
14-DEC-8?
BY: JJS
CMP
HCt. TO CMP PAYMETER
METERING DEVICE DATA ********************
PIPE I. D. FLANGE TYPE PRESSURE TAP MATERIAL BETA RATIO DEVICE
6.065 INCHES
300# RP DOWNSTREAM 316 SS 0. 4283 SO EDGE ORIFICE- FLANGE TAPS
FLUID PROPERTIES ****************
FLUID DIDEAL GAS
VISCOSITY
0.010
CP
CP/CV
1. 400
BASE CONDITIONS ****************
SP GRAVITY : 1.2600
TEMPERATURE: IS. 60 DEGC
PRESSURE * : 14. 730 PSIA
DENSITY
0. 0964LB/CF
0.00154GM/CC
FLOWING CONDITIONS
it*******#**#*#*-*-*-*
MAX FLOW DIFFERENTIAL
BORE
542365.500 LBS /DAY 175. 00 IN. H20 2, 6007 INCHES
CALCULATED INPUT INPUT
PRESSURE TEMPERATURE
200. 00 PSIO 35. 00 DECC
DENSITY
1.3170 L5/F3
0. 02110 GM/CC
LINE VELOCITY. 23.780 FT/SEC
PIPE REYNOLDS NO.
2355550.
(CALCULATED AT 100% FLOW)
UNRECOVERABLE PRESSURE LOSS: 2. 80 PSI
(CALCULATED AT 75% FLOW)
*
17162. 7 KWH/YR 548.35 DOLLARS/YR
K0B2:
0.11243
FR : 1.00015
Y : 1.00273 FPV: 1.00000
FA : 1.00044
METER CONSTANT FOR MASS FLOW PACKAGE *************** * **** >**** ***********
FLOW
1487."7^S""*~'*'SGRT(H(IN)*DEN) LBS /HR
nm.i r-ucMT r ai i ica
CONPTDFNTTAt DO 007371
MASS I1 LOW M' 2151
TYPE
3 ENTRY 44 CAL
DATA
0.00000 LE/H
KCL TO CMP PAYMETER
METER CONSTANT
146?. 57996
0 BAD IN SERVICE
INPUT DATA SPAN
FI 2181
0.00000 IH20
175.00
EASE
TYPE 13 ENTRY 100 CAL 48 BAD IN SERVICE HCL TO CMP FLOW
0.00
. .'I3ITY DATA
DN 2181 1.17537 #/CF
TYPE
2 ENTRY 26 CAL 7 OK IN SERVICE
L TO CMP DENSITY
DEN TEMP DATA SPAN
TI 2187
28. 66661 DEGC
99. 98
EASE
TYPE 13 ENTRY 102 CAL HCL TO CMP TEMPERATURE
0. 00
0 OK
IN SERVICE
DEN PRESS PI 2192
DATA
161. 14970 ,, PSIG
SPAN ' -- -2*90 ^'9E
TYPE 13 ENTRY 101 CAL HCL TO CMP PRESSURE
o.OO
O OK
IN SERVICE
confidential
00 007372
DOW CHEMICAL USA LOUISIANA DIVISION FLOW METER SPECIFICATIONS
TAG DATE LAST REVISION PLANT DESCRIPTION
FE 2212
01-DEC-89
Oo-SEP-8?
BY:
Ci-iP
FREON TO E-73
EBB
METERING DEVICE DATA ***#**#*********#a*
PIPE I. D. FLANGE TYPE PRESSURE TAP MATERIAL BETA RATIO DEVICE
2.067 INCHES 300# RF DOWNSTREAM 316 SS 0. 5433 SO EDGE ORIFICE- FLANGE TAPS
FLUID PROPERTIES
***#****#####*#*
FLUID 31)GENERAL LIG
VISCOSITY
0. 500
CP
BASE CONDITIONS
****************
SP GRAVITY :1 . 4800
TEMPERATURE: 15. 60 DEGC
PRESSURE
14.730 PSIA
DENSITY
: 92.3017LB/CF
1.47856GM/CC
FLOWING CONDITIONS *#****#*****#*** *
MAX FLOW DIFFERENTIAL BORE
20000.000 LBS /HR 50. 00 IN. H20
1.1344 INCHES
INPUT INPUT CALCULATED
PRESSURE TEMPERATURE
100. 00 PSIG -28. 00 DEGC
FLOWING GRAV : 1.4800
DENSITY
92.3017 L3/F3
1.47856 GM/CC
LINE VELOCITY: 2. 583 FT/SEC
PIPE REYNOLDS NO.
122225.
(CALCULATED AT 1007. FLOW)
UNRECOVERABLE PRESSURE LOSS:
0. 70 PSI
(CALCULATED AT 757. FLOW)
*
53. 7 KWH/YR 1.72 DOLLARS/YR
K0B2:
0.19158
FR : 1.00343 FA : 0.99846
METER CONSTANT FOR MASS FLOW PACKAGE
*W*##**#******4
***##*#***
FLOW=
23.86067 * SORT(H(IN)*DEN) - GAL /HR
DO 007373
ASS FLOW MF 2212
TYPE
3 ENTRY
ATA 7249.41504 LB/H FREON TO E-73
ETER CONSTANT
294.39999
34 CAL 0 OK IN SERVICE
MPUT ATA =AN
FIC 2212
6.55556 IH20
50.00
BASE
TYPE 13 ENTRY 47 CAL 32 OK FREON FLOW TO E-73
0.00
IN SERVICE
ENSIlY VTA
DN 2212 92.30000 #/CF
TYPE
1 ENTRY
EON TO E-73
38 CAL 0 OK IN SERVICE
DUTPUT TO PRINTER CY OR N ,D:N3 ? '1FT31 -- Exiting due to ERROR 3 t PC = 000002
in "SEEMF " at 391
ALT-F10 HELP I VT-100 ! FDX I 9600 N81 I LOS CLOSED I PRT OFF I CR
OUTPUT TO PRINTER CY OR N ,D:N3 ? *1FT31 -- Exiting due to ERROR 3 t PC = 000002
in "SEEMF " at 391
3MF MF2208
ASS FLOW MF 2208
TYPE
3 ENTRY 37 CAL
ATA 23354.21484 LB/H
FREON FLOW TO E--74
ETER CONSTANT
196.73000
0 OK
IN SERVICE
MPUT ATA ^AK
FIC 2208
175.16667 IH20
200.00
BASE
TYPE 13 ENTRY 21 CAL 32 OK IN SERVICE FREON TO E--74 CC-70 REBOILER)
0. 00
ENSITY ATA
DN 2208 80.45220 #/CF
TYPE
1 ENTRY 41 CAL 0 OK IN SERVICE
EON FLOW TO E-74 CONSTANT DENS
OUTPUT TO PRINTER CY OR N ,D:N3 ? MFT31 -- Exiting due to ERROR 3 t PC = 000002
in SEEMF " at 391
CR
ALT-F10 HELP | VT-100 | FDX | 9600 NB1 | LOG CLOSED | PRT OFF | CR | CR
ASS FLOW MF 2052
TYPE
3 ENTRY 30 CAL
ATA
21763.52344 LB/H
HCL PURIFICATION FEED
ETER CONSTANT
3509.87988
0 OK
IN SERVICE
i/'
MPUT ATA 11 AN
FIC 2052
51.23611 IH20
100.00
BASE
"NSITY TA
DN 2052 0.75041 #/CF
TYPE 13 ENTRY 32 CAL 32 OK HCL FLOW TO PURIFICATION
0. 00
IN SERVICE
TYPE
2 ENTRY 20 CAL 7 OK IN SERVICE
L TO PURIFICATION
' TEMP \
TI 2051
23.86082: DEGC
99.98
BASE
TYPE 13 ENTRY 16 CAL 0 OK IN SERVICE
HCL TO PURIFICATION TEMPERATURE
-20.00
CONFIDENTIAL
REr
PI 2053
TYPE 13 ENTRY 31 CAL 0 OK IN SERVICE
DO 007374
DOW CHEMICAL USA LOUISIANA DIVISION FLOW METER SPECIFICATIONS
TAG DATE LAST REVISION PLANT DESCRIPTION
FE 2208
01--DEC--89
24--JUN--S3
BY
CMP
FREON TO E-74
METERING DEVICE DATA ***#***#******* x * ***
PIPE I. D. FLANGE TYPE PRESSURE TAP MATERIAL BETA RATIO DEVICE
4.026 INCHES 3004RF DOWNSTREAM 316 SS 0. 2373 SO EDGE ORIFICE- FLANGE TAPS
FLUID PROPERTIES
##****-#*******
FLUID 31)GENERAL LIQ
VISCOSITY
0. 500
CP
BASE CONDITIONS ****************
SP GRAVITY :1 . 2900
TEMPERATURE: 15. 60 DEGC
PRESSURE DENSITY
14. 730 PSIA 80.4521LB/CF
1.28874GM/CC
FLOWING CONDITIONS ***#***** *** *
MAX FLOW DIFFERENTIAL BORE
'4965. 64S LBS /HR 200. 00 IN. H20 0.9575 INCHES
CALCULATED INPUT INPUT
PRESSURE TEMPERATURE
226. 00 PSIO 40. 00 DECC
FLOWING GRAV : 1.2900
DENSITY
80.4521 LB/F3
1.28S74 GM/CC
LINE VELOCITY:
0.975 FT/SEC
PIPE REYNOLDS NO.
78332.
(CALCULATED AT 1007. FLOW)
UNRECOVERABLE PRESSURE LOSS:
3.70 PSI
(CALCULATED AT 757. FLOW)
*
409.4 KWH/YR 13.08 DOLLARS/YR
K0B2:
0.03375
FR : 1.00149 FA : 1.00060
METER CONSTANT FOR MASS FLOW PACKAGE
*##*******#****< 4 t4***1<4****#t
FLOW=
18.30126 * SORT(H(IN)*DEN) GAL /HR
CONFIDENTIAL DO 007375
MASH FLOW MF 203
TYPE
3 ENTRY 37 CAL
DATA
15379.79297 LR/H
FREON FLOW TO E-74
METER CONSTANT
196. 73000
0 OK
IN SERVICE
INPUT DATA fcnAN
FIC 2208
80.98611 IH20
00. 00
EASE
TYPE 13 ENTRY 21 CAL 32 OK IN SERVICE FREON TO E-74 (C-70 REBOILER)
O. 00
DENSITY DATA
DN 2203 80.45220 */CF
TYPE
1 ENTRY 41 CAL 0 OK IN SERVICE
EON FLOW TO E-74 -CONSTANT DENS
OO/vysTa^TT
00 007376