Ok

1. OF 1
1
SHEET
B A
SDV
104
PSV
104B
SDV
106
F A
PSV
103
SDV
102B
D B
A D
PV
101A
SDV
103
F A
TO EXPORT LIQUID
PIPELINE
4"-F
FT
103C
FV
103C
P-103
(Trim: F)
A F
4"-A
B A
PSV
102
TO FLARE SYSTEM
12"-A
SDV
102A
D A
LV
101
4"-D
PV
101B
TO FLARE SYSTEM
14"-A
A
D
D A
PSV
101
SDV
101
FROM PRODUCTION
HEADER (NOTE 1)
C-104
(Trim: B)
1ST
STAGE
C-104
GAS COMPRESSOR
CAPACITY: 0.50 MMSCFD (14160 SCMD)
SUCTION: 50 PSIG (3.4 BAR) AT 70°F (21°C)
DISCHARGE: 350 PSIG (24.1 BAR) AT 279.1°F (137.3°C)
MOTOR: 73 HP
TO EXPORT
GAS PIPELINE
10"-B
6"-B
6"-D
V-101
HIGH PRESSURE SEPARATOR
SIZE: 60" I.D. (1.52 M) X 18'-6" S/S (5.64 M)
DESIGN: 1200 PSIG (82.7 BAR)/FV AT 300°F (149°C)
OPERATING: 350 PSIG (24.2 BAR) AT 70°F (21°C)
LIQUID RESIDENCE TIME: 3 MIN.
TO FLARE SYSTEM
8"-A
PSHH
101D
PSLL
101D
V-102
LSHH
102B
LSLL
102B
PSHH
102B
PSLL
102B
6"-D
V-102
LOW PRESSURE SEPARATOR
SIZE: 42" I.D. (1.07 M) X 13'-6" S/S (4.11 M)
DESIGN: 75 PSIG (5.2 BAR)/FV AT 300°F (149°C)
OPERATING: 50 PSIG (3.5 BAR) AT 38°F (3°C)
LIQUID RESIDENCE TIME: 5 MIN.
P-103
EXPORT PUMP
CAPACITY: 100 GPM (0.38 SCM) @ 2200 PSIG (151.7 BAR)
DIFFERENTIAL PRESSURE: 2100 PSIG (144.8 BAR)
MOTOR: 200 HP
FT
103B
FV
103A
FV
104
FT
104
PV
106
LSLL
101B
V-101
LSHH
101B
4"-A
10"-A
LSLL
101B
FT
103A
PSHH
103A
PSLL
103A
PSLL
103C
PSLL
106
TO FLARE SYSTEM
10"-A
PSHH
104C
PSLL
104C
PSV
104A
H-105
(Trim: B)
H-105
COMPRESSOR DISCHARGE COOLER
DUTY: 0.12 MMBTU/HR (35.2 KW)
DESIGN: 500 PSIG (34.4 BAR) AT 350°F (177°C)
OPERATING: 350 PSIG (24.1 BAR) AT 279.1°F (137.3°C)
2
3
1
6
4
7
8
5
OBL
OBL
OBL
OBL
OBL
OBL
OBL
TSHH
104
Parameter USC Units 1 2 3 4 5 6 7 8
Temperature
o
F 70.00 70.00 70.00 38.00 38.00 279.08 70.00 38.00
Pressure PSIA 714.69 364.69 364.69 64.69 64.69 364.69 364.69 2114.69
Molecular Wt. LB/LB-MOL 20.25 18.63 67.99 21.69 74.25 21.69 18.64 74.25
Density LB/FT3 1.43 1.28 38.46 0.27 40.50 1.00 1.19 40.50
Compressibility Factor (Z) UNITLESS 0.91 0.94 n/a 0.98 n/a 0.98 0.93 n/a
Heat Value BTU/LB 23168 23311 21125 22951 21072 22951 23295 21072
Rate MOL/DAY 263512 254842 8670 1033 7637 1033 255875 7637
LB/HR 222338 197789 24549 933 23615 933 198722 23615
LB/MIN 3706 3296 409 16 394 16 3312 394
Energy Rate MMBTU/HR 5151 4611 541 21 519 21 4632 519
Std. Liq. Rate GAL/HR n/a n/a 4774 n/a 4362 n/a n/a 4362
GAL/MIN n/a n/a 80 n/a 73 n/a n/a 73
BOPD n/a n/a 2728 n/a 2492 n/a n/a 2492
Std. Vapor Rate MMSCFD 100 97 n/a 0 n/a 0 97 n/a
SCFM 69444 67160 n/a 272 n/a 272 67432 n/a
Stream Number
REV
DRAWING NUMBER
DRAWING TITLE
1
D-254-001
Process Flow Diagram
Gas Production Facility
Kenexis
3366 Riverside Drive, Suite 200, Columbus OH 43221
This drawing, © 2011 Kenexis Consulting Corporation is business confidential. No part of this document may be circulated, quoted, or reproduced for distribution other than by the above named client
without prior written approval from Kenexis Consulting Corporation.
The Design Basis for this facility is 100 MMSCFD of natural gas at a pressure of 700 psig and a
temperature of 70oF. The incoming production header pressure is assumed to be 700 psig in normal
operation. The molar composition of the natural gas stream is: Methane – 90%, Ethane – 2%, Propane
– 2%, N-Butane – 2%, N-Pentane – 2%, and N-Hexane – 2%.
CLIENT
NOTES REV DESCRIPTION DATE BY APP
DRAWN S. A. Gray 9 Jun 09
CHECKED B. Buck 23 Jun 09
APPROVED
APPROVED
0 As Built 9 Jun 09 SAG BB
1 Revision 23 Jun 09 SAG BB
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2. OF 6
1
SHEET
Analysis
Burner, Combustion
Blowdown
Choice (Conductivity)
Choice (Density)
Voltage
Flow/Flowrate
Flow Ratio
User’s Choice
Hand
Process Variable
A
B
BD
C
D
E
F
FF
G
H
AAL
BAL
BDAHH
CAL
DAL
EAL
FAL
FFAL
AAH
BAH
CAH
DAH
EAH
FAH
FFAH
AE
BE
FE FG
AI
BI
CI
DI
EI
FI
FFI
AT
BT
CT
DT
ET
FT
FFT
AIC
BIC
CIC
DIC
FIC
FFIC
HIC
AV
BV
BDV
FV
FFV
HV
FCV
ASL
BSL
CSL
DSL
ESL
FSL
FFSL
ASH
BSH
CSH
DSH
ESH
FSH
FFSH
AY
BY
BDY
CY
DY
EY
FY
FFY
HY
Alarm
Low,
Low-Low
AL(L) AH(H) E G I L CV SL(L) SH(H) Y
Alarm
High,
High-High
Alarm
High/
Low
Element
Gauge/Glass
(Direct)
Indicate
Light
(Status
Indication)
Transmitter
(Note
1)
Controller
(Note
2)
Valve,
Damper,
Louver
Valve,
Self-
Restraining
Switch
Low
Switch
High
Switch
High/Low
Compute,
Convert,
Relay
Process
Legend
Sheet
Instrument
Function T CI V
Current (Electric)
Power
Time
Level
Level, Safety
User’s Choice (Moisture)
User’s Choice
User’s Choice
Pressure
Pressure Differential
I
J
K
L
LX
M
N
O
P
PD
IAL
JAL
LAL
LXALL
PAL
PDAL
IAH
JAH
LAH
LXAHH
PAH
PDAH
LALH LG
II
JI
LI
PI
PDI
IT
JT
LT
LXT
PT
PDT
IIC
JIC
LIC
PIC
PDIC
LV
PV
PDV
LCV
PCV
PDCV
ISL
JSL
LSL
PSL
PDSL
ISH
JSH
LSH
PSH
PDSH
IY
JY
LY
PY
PDY
LSLH
Pressure Ratio
Pressure, Safety
Quantity
Radiation
Speed
Shutdown
Temperature
Temperature Differential
Temperature, Safety
Multi-Variable
PF
PX
Q
R
S
SD
T
TD
TX
U
PFAL
PXALL
SAL
TAL
TDAL
TXALL
UAL
PFAH
PXAHH
SAH
TAH
TDAH
TXAHH
UAH
PSE
TE TG
PFI
SI
TI
TDI
PXT
ST
TT
TXT
UT
PFIC
SIC
TIC
TDIC
UIC
PFV
PSV
SV
SDV
TV
TDV
UV
TCV
PFSL
SSL
TSL
TDSL
USL
PFSH
SSH
TSH
TDSH
USH
PFY
SY
SDY
TY
TDY
UY
Vibration
Weight
Unclassified
Event, State, Presence
Position
V
W
X
Y
Z
VAL
WAL
ZAL
VAH
WAH
ZAH
VE
WE
VI
WI
XI
YI
ZI
YL
ZL
VT
WT
XT
ZT
WIC
XIC
ZIC
XV XCV
VSL
WSL
XSL
ZSL
VSH
WSH
XSH
ZSH
VY
WY
YY
ZY
ANSI Piping Pressure Specifications at 300°F (149°C)
Maximum Design Pressure
230 psi (15.9 bar)
655 psi (45.2 bar)
1315 psi (90.7 bar)
1970 psi (135.8 bar)
3280 psi (226.2 bar)
ANSI Class Rating
150#
300#
600#
900#
1500#
Piping Class
A
B
D
E
F
Instrument Symbols
Lines
Instrument Impulse
Lines from Process
Pneumatic Signal
Electrical Signal
Hydraulic Signal
Capillary Tube
Fiber Optic
“Soft Link”
Communication
“Serial Link”
Communication
Control Valve/Relief Device
Flow Symbols
Miscellaneous
Diaphragm Spring
Return
Piston Spring Return
Self-Actuated
Motor Operated
Solenoid Operated
Buckling Pin
Relief Valve (Spring)
Pressure/Vacuum
Safety Valve
Pilot Operated
Fixed Choke
Adjustable Choke
Actuated Choke
Rupture Disk
Deluge
Diaphragm with
Positioner
Piston with Positioner
Double Acting Piston
with Positioner
Orifice
Quick Change Orifice
Meter (SR/JR Optional)
Venturi Meter
Averaging Pilot
Meter
Turbine Meter
Vortex Meter
Magnetic
Flowmeter
Positive Displacement
Flow Meter
In-Line Flow
Glass
Rotameter
Cone Meter
Coriolis Meter
Ultrasonic
Flowmeter
Flow
Conditioner
M
S
(SR/JR)
M
FG
FG
Diaphragm
Seal
S
3 Way Solenoid
3 Way Solenoid
with Manual
Reset
S
Motor Control
Center
R
MCC
Detail “A” - SIS Inputs
XI
XXX
XT
XXX
HA
XXX
XAHHLL
XXX
XAHL
XXX
HS
XXX
XDA
XXX
Detail “B” - SIS Outputs
USC
XXX Indicator
Bypass
Switch
Trip Alarm
Pre-Alarm
Bypass
Alarm
Deviation
Alarm
XI
XXX
XV
XXX
HS
XXX
XA
XXX
USC
XXX
Output
Command
Status
Output
Activated
Reset
Material of Construction
Carbon Steel
Carbon Steel
Carbon Steel
Carbon Steel
Carbon Steel
REV
DRAWING NUMBER
DRAWING TITLE
1
D-254-002
Legend Sheet
Gas Production Facility
Kenexis
3366 Riverside Drive, Suite 200, Columbus OH 43221
This drawing, © 2011 Kenexis Consulting Corporation is business confidential. No part of this document may be circulated, quoted, or reproduced for distribution other than by the above named client
without prior written approval from Kenexis Consulting Corporation.
NOTES:
1. All electronic transmitters are indicating transmitters.
2. If an “I” is omitted, the device is a non-indication controller.
CLIENT
NOTES REV DESCRIPTION DATE BY APP
DRAWN S. A. Gray 9 Jun 09
CHECKED B. Buck 23 Jun 09
APPROVED
APPROVED
0 As Built 9 Jun 09 SAG BB
1 Revision 23 Jun 09 SAG BB
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3. OF 6
2
SHEET
C
101
D A
LV
101A
V-101
PT
101B
PV
101B
PSV
101
PT
101D
SDV
101
OBL
OBL
OBL
SHT 5
LT
101A
TO GAS COMPRESSOR
TO FLARE SYSTEM
TO FLARE SYSTEM
TO L.P. SEPARATOR
FROM PRODUCTION HEADER
IAS
S
LT
101B
PI
101C
LIC
101A
PIC
101B
H
L
H
L
SHT 3
6"-D
4"-D
8"-D
14"-A
8"-A
A
D
PT
101C
PV
101A
PIC
101A
PT
101A
USC
101
USC
101
USC
101
LG
101A
LG
101B
H
H
L
V-101
HIGH PRESSURE SEPARATOR
SIZE: 60" I.D. (1.52 M) X 18'-6" S/S (5.64 M)
DESIGN: 1200 PSIG (82.7 BAR)/FV AT 300°F (149°C)
OPERATING: 350 PSIG (24.2 BAR) AT 70°F (21°C)
LIQUID RESIDENCE TIME: 3 MIN.
USC
100
FT
101
FQI
101
Detail “A”
Detail “A”
Detail “A”
C
100
Detail “B”
HS
100
REV
DRAWING NUMBER
DRAWING TITLE
1
D-254-002
High Pressure Separator
Gas Production Facility
Kenexis
3366 Riverside Drive, Suite 200, Columbus OH 43221
This drawing, © 2011 Kenexis Consulting Corporation is business confidential. No part of this document may be circulated, quoted, or reproduced for distribution other than by the above named client
without prior written approval from Kenexis Consulting Corporation.
CLIENT
NOTES REV DESCRIPTION DATE BY APP
DRAWN S. A. Gray 9 Jun 09
CHECKED B. Buck 23 Jun 09
APPROVED
APPROVED
0 As Built 9 Jun 09 SAG BB
1 Revision 23 Jun 09 SAG BB
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4. OF 6
3
SHEET
SHT 4
4"-A
FROM PSV-103
SDV
102B
IAS
S
USC
102
B A
SHT 5
GAS COMPRESSOR SPILLBACK
6"-A
SHT 4
V-102
PSV
102
SDV
102A
SHT 2
OBL
SHT 5
LG
102A
LT
102A
TO GAS COMPRESSORS
TO FLARE SYSTEM
TO EXPORT PUMP
FROM HP SEPARATOR
IAS
S
BLOCKED FLOW
8"FB12"
SET AT
75 PSIG
LG
102B
LT
102B
PI
102A
SHT 4
I
4"-D
4"-A
D A
6"-B
12"-A
LIC
102A
4"-A
PIPELINE PUMP SPILLBACK
PT
102A
PT
102B
USC
102
USC
102
H
L
USC
102
H
SHT 4
TO FIC-103C
V-102
LOW PRESSURE SEPARATOR
SIZE: 42" I.D. (1.07 M) X 13'-6" S/S (4.11 M)
DESIGN: 75 PSIG (5.2 BAR)/FV AT 300°F (149°C)
OPERATING: 50 PSIG (3.5 BAR) AT 38°F (3°C)
LIQUID RESIDENCE TIME: 5 MIN.
Detail “A”
Detail “A”
Detail “B”
Detail “B”
REV
DRAWING NUMBER
DRAWING TITLE
1
D-254-002
Low Pressure Separator
Gas Production Facility
Kenexis
3366 Riverside Drive, Suite 200, Columbus OH 43221
This drawing, © 2011 Kenexis Consulting Corporation is business confidential. No part of this document may be circulated, quoted, or reproduced for distribution other than by the above named client
without prior written approval from Kenexis Consulting Corporation.
CLIENT
NOTES REV DESCRIPTION DATE BY APP
DRAWN S. A. Gray 9 Jun 09
CHECKED B. Buck 23 Jun 09
APPROVED
APPROVED
0 As Built 9 Jun 09 SAG BB
1 Revision 23 Jun 09 SAG BB
SCALE -
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5. OF 6
4
SHEET
F A
PSV
103
BLOCKED FLOW
8"FB10"
SET AT
2200 PSIG
F A
SHT 3
A F
SDV
103
IAS
S
MCC
S
T
O
P
SIS
FT
103C
FIC
103C
FV
103C
OBL
SHT 3
TO EXPORT LIQUID PIPELINE
FROM LP SEPARATOR
P-103
(Trim: F)
4"-A
4"-F
PT
103B
PI
103B
PIPELINE PUMP SPILLBACK TO LP
SEPARATOR
4"-A
FT
103A
FIC
103A
FV
103A
P-103
EXPORT PUMP
CAPACITY: 100 GPM (0.38 SCM) @ 2200 PSIG (151.7 BAR)
DIFFERENTIAL PRESSURE: 2100 PSIG (144.8 BAR)
MOTOR: 200 HP
SHT 3
FROM LIC-102A
USC
103
USC
103
H
FT
103B
TO LP SEPARATOR
4"-A
USC
103
C
103B
PT
103A
USC
103
TT
103
TI
103
H
Detail “A”
C
103A
PT
103C
Detail “A”
Detail “A” Detail “B”
SHT 3
Detail “B”
REV
DRAWING NUMBER
DRAWING TITLE
1
D-254-002
Pipeline Pump
Gas Production Facility
Kenexis
3366 Riverside Drive, Suite 200, Columbus OH 43221
This drawing, © 2011 Kenexis Consulting Corporation is business confidential. No part of this document may be circulated, quoted, or reproduced for distribution other than by the above named client
without prior written approval from Kenexis Consulting Corporation.
CLIENT
NOTES REV DESCRIPTION DATE BY APP
DRAWN S. A. Gray 9 Jun 09
CHECKED B. Buck 23 Jun 09
APPROVED
APPROVED
0 As Built 9 Jun 09 SAG BB
1 Revision 23 Jun 09 SAG BB
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1oo2
1oo2

6. OF 6
5
SHEET
B A
IAS
S USC
106
SDV
106
SDV
104
IAS
S
D B
SHT 2
D A
SHT 3
MCC
S
T
O
P
C-104
(Trim: B)
1ST
STAGE
VENDOR FURNISHED
UNIT CONTROL
PANEL
SHT 3
FROM LP SEPARATOR
OBL
TO EXPORT GAS PIPELINE
XL
104A
XL
104B
XL
104C
SY
104D
RUN
STATUS
IR1
RUN
STATUS
ELS
KW
ELS
RUN
STATUS
6"-B
10"-B
10"-A
GAS COMPRESSOR SPILLBACK TO
LP SEPARATOR
FV
104
FT
104
FIC
104
ANTI-SURGE
PT
106
PI
106
C
106
6"-D
FROM HP SEPARATOR
PT
106A
TT
105
TI
105
H
H
PIC
106A
PV
106
USC
104
H
L
C-104
GAS COMPRESSOR
CAPACITY: 0.50 MMSCFD (14160 SCMD)
SUCTION: 50 PSIG (3.4 BAR) AT 70°F (21°C)
DISCHARGE: 350 PSIG (24.1 BAR) AT 279.1°F (137.3°C)
MOTOR: 73 HP
C
102
USC
104
USC
106
PT
106B
H-105
COMPRESSOR DISCHARGE COOLER
DUTY: 0.12 MMBTU/HR (35.2 KW)
DESIGN: 500 PSIG (34.4 BAR) AT 350°F (177°C)
OPERATING: 350 PSIG (24.1 BAR) AT 279.1°F (137.3°C)
OBL
10"-A
TO FLARE SYSTEM
PSV
104B
RUPTURE
8"FB10"
SET AT
250 PSIG
PT
104C
USC
104
BACKFLOW
6"FB10"
SET AT
640 PSIG
PSV
104A
H-105
(Trim: B)
C
104
USC
104
TT
104
Detail “A”
Detail “B”
Detail “A”
Detail “A”
Detail “B”
Detail “B”
REV
DRAWING NUMBER
DRAWING TITLE
1
D-254-002
Gas Compressor
Gas Production Facility
Kenexis
3366 Riverside Drive, Suite 200, Columbus OH 43221
This drawing, © 2011 Kenexis Consulting Corporation is business confidential. No part of this document may be circulated, quoted, or reproduced for distribution other than by the above named client
without prior written approval from Kenexis Consulting Corporation.
CLIENT
NOTES REV DESCRIPTION DATE BY APP
DRAWN S. A. Gray 9 Jun 09
CHECKED B. Buck 23 Jun 09
APPROVED
APPROVED
0 As Built 9 Jun 09 SAG BB
1 Revision 23 Jun 09 SAG BB
SCALE -
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7. OF 6
6
SHEET
IAS
S
5"
HV
105
1"
3"
3"
PCV
105C
4"
PCV
105B
LT
110
1"
1"
1"
PDV
105A
3/4"
1"
1"
1"
3/4"
3/4"
C-104
GAS COMPRESSOR
CAPACITY: 0.50 MMSCFD (14160 SCMD)
SUCTION: 50 PSIG (3.4 BAR) AT 70°F (21°C)
DISCHARGE: 350 PSIG (24.1 BAR) AT 279.1°F (137.3°C)
MOTOR: 73 HP
C-104
1"-D
1"
F-104A
SEAL GAS
FILTER
PIC
105A
H
L
PCV
105A
PT
105A
1"
1" 1" 1" 1"
PDT
105A
PDI
105A
H
1"
1"
1"
TO DRAIN
F-104B&C
LUBE OIL
FILTERS
T-110
OIL TANK
H-110
OIL TANK
HEATER
LG
110
USC
104
TO DRAIN
M
P-104B
AUX. LUBE OIL
PUMP
4"-D
4"-D
PSV
105
PSV
106
4"-D
4"
4"
SET PRESSURE
450 PSIG
SET PRESSURE
450 PSIG
M
P-104A
MAIN OIL PUMP
4"-D
8"-D
4"-D
1"-D
1"-D
3" x 1”
3" x 1”
3" x 1”
1"-D
2"
GT
105A
USC
104
TT
105A
TI
105A
H
TT
105B
USC
104 TT
105C
TI
105C
H
TT
105D
USC
104
XT
105B
XT
105A
USC
104
USC
104
TT
105F
TT
105E
TI
105E
H
MONITORING
TRAPS
LG
106A
LG
106B
M-104
1 / 2”
PRV
105A PRV
105C
PRV
105B
PDT
105C
TT
105G
TI
105G
H
TT
105H
USC
104
XT
105C
XT
105D
USC
104
PT
105B
USC
104
TT
105I
TI
105I
H
TT
105J
USC
104
XT
105E
XT
105F
USC
104
TT
105P
TI
105P
H
TT
105O
TI
105O
H
TT
105N
TI
105N
H
TT
105K
TI
105K
H
TT
105L
TI
105L
H
TT
105M
TI
105M
H
5"-D
FROM COMPRESSOR
PANEL
HY
105
FT
105
FI
105
L
FLAME
ARRESTOR
1"
3" x 1” 3" x 1”
3"
4" x 3”
Detail “A”
Detail “A”
Detail “A”
Detail “A”
Detail “A”
Detail “A”
Detail “A”
Detail “A”
Detail “A”
Detail “A”
Detail “A”
REV
DRAWING NUMBER
DRAWING TITLE
1
D-254-002
Gas Compressor Utility Details
Gas Production Facility
Kenexis
3366 Riverside Drive, Suite 200, Columbus OH 43221
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without prior written approval from Kenexis Consulting Corporation.
CLIENT
NOTES REV DESCRIPTION DATE BY APP
DRAWN S. A. Gray 9 Jun 09
CHECKED B. Buck 23 Jun 09
APPROVED
APPROVED
0 As Built 9 Jun 09 SAG BB
1 Revision 23 Jun 09 SAG BB
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FILE PATH
SERVER1Kenexis DataTraining CoursesSample Process for
TrainingDWG-PFD_PIDs.vsd
General Oil and Gas Operating CO.
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