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PROCESS DATA SHEET DPCU FEED GAS KO DRUM CONSORTIUM

231-D9003 Company Contractor

: PT. PERTAMINA EP CEPU : Consortium Rekind / JGC / JGC Indonesia

Doc. No. Sheet No.

: JTB-RJJ000-P0-DTS-231-00003 : 5 of 9

Project Plant Location

: Jambaran Tiung Biru : Cepu Block Area, Bojonegoro, East Java

P&ID No.

: Hold

DESIGN DATA 1 ORIENTATION

Vertical

MATERIAL SPECIFICATION

2 DESIGN CODE

PART

ASTM / ASME NO

3 CERTIFICATION

SHELL

KCS

4

HEADS

KCS

5

OPERATING / MECHANICAL DATA

REINFORCING PADS

6 TEMPERATURE

NOZZLE NECK (PIPES)

7

DESIGN

°F

250

NOZZLE NECK (PLATES)

8

OPERATING

°F

73

NOZZLE NECK (FORGINGS)

9

MDMT @ BLOWDOWN CONDITION

°F

Hold 1

INTERNAL

10 PRESSURE

SS304L (Hold 1)

FORGED FLANGES

11

DESIGN

INT / EXT

psig

12

OPERATING

MIN / NORMAL / MAX

psig

13 HYDROTEST PRESSURE (N & C) 14 CYCLIC SERVICE

640

/ /

PIPE FITTINGS

561.9

/

ANODE PROTECTION

psig

SKIRT

(YES / NO)

VANE TYPE INLET DEVICE VAPOUR lb/ft³

15 DENSITY 16 FLOWRATE

MMSCFD/BPD

17 MASS FLOWRATE 18 VISCOSITY

lb/hr cP

19 MOLECULAR WEIGHT 20 SURFACE TENSION

dyne/cm

3.07

46.70

STIFFENER RINGS

328.15

1097.14

BASE RING / PLATE

953087.0

11888.0

EXTERNAL ATTACHMENTS

0.014

0.208

26.50

72.30

-

17.30

EXTERNAL

-

BOLTS

-

NUTS

GASKETS

21 VESSEL DIA (ID)

mm

3200

INTERNAL REMOV/NON.REMOV

22 VESSEL LENGTH ( T / T )

mm

3810

INTERNAL

23 SOUR SERVICE

Yes

Note 8

24 WALL THICKNESS :

-

BOLTS

-

NUTS

SS304L (Hold 1)

NAME PLATE

25

CLAD THICKNESS

mm

NAME PLATE BRACKET

26

SHELL THICKNESS

mm

ANCHOR BOLT / NUTS

27

HEAD THICKNESS

mm

28 CORROSION ALLOWANCE / LINNING

-

LIQUID

STRUCTURAL BOLT / NUTS

mm

Note 7

CONSTRUCTION

29 WELD JOINT EFFICIENCIES:

TYPE OF HEADS

30

SHELL

TYPE OF SUPPORT

31

HEAD

2:1 Ellipsoidal

PLATFORM/LADDER/PIPE CLIP

32 INSULATION THICKNESS / TYPE

-

mm

/

-

INSULATION SUPPORTS

33 TOTAL PACKED HEIGHT

mm

-

HAND HOLE DAVIT

34 HEIGHT PER BED

mm

-

EARTHING LUG (MIN 2 NOS / VESSEL)

35 SIZE AND TYPE OF PACKING

mm

-

LIFTING LUGS / EYES

36 NUMBER OF PACKED SECTION

-

NAMEPLATE

37 NUMBER OF REDISTRIBUTORS

-

FIREPROOFING SUPPORT

38 TRAY :

TYPE

-

39

SPACING / NUMBER REQUIRED

-

40 TOTAL VOLUME

m³

41 NORMAL LIQUID VOLUME

m³

42 VOLUME RANGE REQUIRED FOR LEVEL CONTROL

m³

Note 5

RELIEVE VALVE

Hold 1

43 WIND DESIGN

- TYPE /SIZE

Hold 2

- SETTING PRESS.

Hold 2

- NUMBER REQ'D

Hold 2

SEISMIC DESIGN

44

WIND SPEED

TOPOGRAPHIC FACTOR

SITE CLASS

SRA (SS) :

45

CLASSIFICATION CATEGORY

ELEVATION

IMPORTANCE FACTOR

SRA (S1) :

46

EXPOSURE CATEGORY

47

ESTIMATED WEIGHTS

48 TOTAL WEIGHT (SHIPPING WEIGHT)

kg

WEIGHT OF INTERNAL PARTS

49 TOTAL WEIGHT, OPERATING

kg

WEIGHT OF PLATFORM / LADDER

50 TOTAL WEIGHT, FULL OF WATER

kg

WEIGHT OF FIRE PROOFING

51

FABRICATION AND INSPECTION REQUIREMENTS

52 INSPECTION AUTHORITY 53 INSPECTION 54 STRESS RELIEVING 55 SPECIAL HEAT TREATMENT 56 RADIOGRAPHY (HEAD / SHELL) 57 OTHER NON DESTRUCTIVE TESTING 58 CHEMICAL ANALYSIS 59 CODE STAMP 60 CLASS REQUIREMENTS 61 MANUFACTURER'S CERTIFICATE 62

CHEMICAL ANALYSIS

63

MECHANICAL DATA

64 PAINTING

65 FIREPROOFING 66

CONSORTIUM

Rev A

DESIGN DATA MATERIAL SPECIFICATION ASTM / ASME NO KCS KCS

SS304L (Hold 1)

-

SS304L (Hold 1)

CONSTRUCTION 2:1 Ellipsoidal

Hold 2 Hold 2

psig

Hold 2

ESTIMATED WEIGHTS

ATION AND INSPECTION REQUIREMENTS

kg kg kg

PROCESS DATA SHEET DPCU FEED GAS KO DRUM 231-D9003 Company Contractor Project

: PT. PERTAMINA EP CEPU : Consortium Rekind / JGC / JGC Indonesia : Jambaran Tiung Biru

Plant Location

: Cepu Block Area, Bojonegoro, East Java

Doc. No. Sheet No. P&ID No.

: JTB-RJJ000-P0-DTS-231-00003 :6 : Hold

of

9

NOZZLE DATA

1 2

Mark

SIZED

RATING

FACE

TYPE

3

G01

4"

#300

PROJ. CL TO FF

Ventilation

SERVICE

4

O01

26"

#300

Outlet

5

V01

2"

#300

Vent

6

JO2

28"

#300

Inlet

7

SO2

2"

#300

Steam Out

8

WO3

3"

#300

Outlet

L02

2"

#300

BO2

24 ID

#300

9 10 11 12

INSTRUMENT CONNECTIONS

13 14

Level

15 16 17 18 19 20 21

MANHOLES ETC.

22 23

Manway

24 25 26 27 28 29 30 31 32

REFFERENCE DRAWINGS / LIST

33 1. UOP document 9023078-110-01-PFD Rev.0 Process Flow Diagram Dew Point Control Unit. 34 2. UOP document 9023078-B1-Stream Data Rev 0. 35 3. UOP document 9023078-301-01-231-D9003 (METRIC)-Vessels-Rev-0. 36 4. UOP document 9023078-115-01-MSD-Rev-A Material Selection Diagram Dew Point Control Unit. 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 GENERAL REMARKS : 59 60 61 62 63

REMARKS

Hold 4

CONSORTIUM

Rev

NOZZLE DATA REMARKS

Hold 4

INSTRUMENT CONNECTIONS

MANHOLES ETC.

REFFERENCE DRAWINGS / LIST

A

PROCESS DATA SHEET DPCU FEED GAS KO DRUM CONSORTIUM

231-D9003 Company Contractor

: PT. PERTAMINA EP CEPU : Consortium Rekind / JGC / JGC Indonesia

Doc. No. Sheet No.

: JTB-RJJ000-P0-DTS-231-00003 : 7 of 9

Project Plant Location

: Jambaran Tiung Biru : Cepu Block Area, Bojonegoro, East Java

P&ID No.

: Hold

VESSEL SKETCH

1 2 3

Unit in mm

4 5 6 7 8 9 10 11 12 13 14 15 16 17 18 19 20 21 22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40

#REF! mm

41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63

CONTROL RANGE HHLL = Hold 3 HLL = Hold 3 NLL = 380 LLL = Hold 3 LLLL = Hold 3

Rev A

PROCESS DATA SHEET DPCU FEED GAS KO DRUM CONSORTIUM

231-D9003 Company Contractor Project Plant Location 1 2 3 4 5

1. 2. 3. 4.

6 7 8 9 10 11 12 13 14

5. 6. 7. 8.

: PT. PERTAMINA EP CEPU : Consortium Rekind / JGC / JGC Indonesia : Jambaran Tiung Biru : Cepu Block Area, Bojonegoro, East Java

Doc. No. Sheet No. P&ID No.

NOTES Design life of the equipment shall be 25 years. Material in contact with process fluid shall comply with NACE MR0175. Vessel sizing and drawing is based on UOP document 9023078-301-01-231-D9003 (METRIC)-Vessels-Rev-0. Flow rate and fluid properties is based on UOP document 9023078-110-01-PFD Rev.0 Process Flow Diagram Dew Point Control Unit and UOP document 9023078-B1-Stream Data Rev 0 (stream 407) Case 2. Total volume exclude volume of vessel head. All internals shall be removable through vessel manholes unless otherwise noted. The entire vessel shall be lined with 0.125" thick 304L. Lining is corrosion allowance. Sour component composition, provide from [Ref.2] Case 2. H₂S 0.996 %-mol CO₂ 33.05 %-mol COS 0.009 %-mol RSH 0.026 %-mol

15 16

HOLDS

17 18 19 20 21

1. The data to be confirmed by UOP. 2. The PSV size, type and required number to be finalized. 3. HHLL, HLL, LLL and LLLL to be verified during detailed engineering design. 4. Provision for PSV nozzle to be confirmed by UOP.

22 23 24 25 26 27 28 29 30 31 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46 47 48 49 50 51 52 53 54 55 56 57 58 59 60 61 62 63

: JTB-RJJ000-P0-DTS-231-00003 : 8 of 9 : Hold

GENERAL NOTES :

Rev A

NOTES

HOLDS

Calculation sheet for VERTICAL PRESSURE VESSELS Equipment No.:

224-D9101A/B

Number required:

Design book Contr. job

No. No.

: : 4650000076

Comp. Doc

No.

: JTB-RJJ000-AE-P0-DTS-224-00001

2 (Two)

CALCULATION BASIS 1. CALCULATION OBJECTIVE This calculation was performed to size the 2 phase separator with 50% margin. (refer to document JTB-SF-P-DBS-900-00004 Eqiupment Design Criteria revision 5 section 6.3.2). 2. CALCULATION METHODE Vessel sizing is carried out using 2 phase vertical separator calculation sheet 3. ASSUMPTION a. VRU Inlet Scrubber is a vertical two phase separator with Vane type inlet device and Vane Pack internals as per JTB-SF-P-CAL-900-00004. b.

Base case for vessel sizing is case 2.

c.

K factor is 0.49 as per document JTB-SF-P-CAL-900-00004 "Equipment Sizing - Process Vessel Sizing" on bid bulletin 19.

4. DESIGN BASIS a.

Separator sizing is designed based on flowrate gas 1 x 100%.

b. c.

50% margin on inlet flowrate will be applied. Level settings for hydrocarbon liquid will be as per document JTB-SF-P-DBS-900-00004 "Equipment Design Criteria" Section 6.3.3. times, whicever is greater :

d.

HHLL to HLL

1 min

or minimum 150 mm

HLL to LLL LLL to LLLL

3 min + slug allowance 0.5 min

or (300 mm) or minimum 150 mm

LLLL to BTL

N/A

minimum 250 mm

Fluid properties are obtained from Hysys simulation and document JTB-RJJ000-AE-P0-HMB-224-00002 Heat and Material Balances Vapor Recovery Unit Design Case 2 - High H2S.

LCULATION BASIS

page:

10

4650000076 JTB-RJJ000-AE-P0-DTS-224-00001 version 4.0.

Conversion from MMSCFD to ton per hour : Flow rate =

336 MMSCFD 335,760,000 f3/day

3.358E+08

f3/day =

335,760,000

=

x

day

1

day

24

hour

x

0.0283

396,153 m3/hour P·V=n·R·T

Ideal gas equation → P·V R·T

n= Standard condition :

P= T= R= 1

n= 0.0820575 =

f3

1 15.56

atm °C

(14.696 psia) (60 °F) =

288.71 K

0.0820575 atm · m3 / (kmol · K)

atm

x

396,153

atm · m3 kmol · K

x

288.71

m3 hour K

16,721.78 kmol/hour Molecular Weight =

26.5 kg/kmol

Density =

3.07 49.18

Mass Flow =

443,127.16 kg/hr 976927.00 lb/hr

→

443.13 ton/hr =

9,010.9

m3 f3

lb/f³ kg/m3 m3/hr