DAFTAR PUSTAKA

DAFTAR PUSTAKA [1].

A soedrajat s, ”Mekanika Fluida dan Hidrolika”, NOVA Bandung, 1983.

[2].

Bambang Triatmodjo, ”Hidraulika II”, BETA OFFSET, Yogyakarta, 2003.

[3].

Mekanika Fluida Jl. 1 & 2 Ed. 4 Penerbit Erlangga ISBN 9797413926, 9789797413927.

[4].

Hadi Susilo, ”Pengembangan Sumber Daya Air”, Diktat ajar UMB.

[5].

Suriady Sihombing, ”Kajian Experimental Susunan Pompa Secara Pararlel Terhadap Karakteristik Vibrasi Pompa Sentrifugal”, Tesis UNSU, Medan, 2008.

[6].

Teguh Pudji Hertanto, M.Si, Modul Perkuliahan Universitas Mercubuana. Sistem Pemipaan

[7].

Syahrul Fauzi Siregar,MT, ”Valve”, Program Studi Teknik Kimia Fakultas Teknik Universitas Sumatera Utara.

[8].

Julian Alfijar, ST,”Mekanika Fluida II”, Jurusan Teknik Mesin , FT. UNIMUS.

[9].

Aanalisis Stataik Sistem Perpipaan Untuk Penambahan Boiler VI Di PERTAMINA Unit Pengolahan V Balikpapan Menggunakan Perangkat Lunak CAESAR II 4.20.

[10].

Danang Arif Agustiyan, Dr Bambang Lelono Widjiantoro ST,MT. Jurnal tentang “Simulasi Kavitasi Pada Control Valve”.

[11].

Muhammad Muhtadi, DR. Bambang L. Widjiantoro, ST.MT, Hendra Cordova, ST.MT). Jurnal tentang “Analisis Reduksi Intensitas Kavitasi Pada Control Valve Akibat Pressure Drop Dengan Metoda Pressure Recovery Factor Di Vico Indonesia”.

[12].

Michael Parmahan Hutapea,, Tugas Sarjana “Analisis Tegangan Sistem Perpipaan Akibat Fenomena Waterhammer”.

[13].

Nugroho Wibisono / Arief Rahman Thanura, Pressure Reducer vs Back Pressure Regulator

[14].

Pipe Stress Analysis seminar notes, COADE, Inc. 1985-1998.

[15].

Charles Becht IV,2004. Process Piping : The Complete Guide to ASME B31.3 Ed,3.

[16].

E. Benjamin Wylie, Prentice-Hall, 1978. Fluid Transients.

[17].

H&S Executive - Transient vibration guidlines for fast acting valves (Acoustic Technology Limited) - likelihood of failure (LOF).

[18].

H&S Executive - Vibration Induced Fatique (Energy Institute).

[19].

J. C. Wachel, Piping Vibration and analysis.

[20].

J. C. Wachel, Piping Vibration and Stress.

[21].

J. C. Wachel, Pipeline Pump Vibration and Failure - Cavitation.

[22].

J. C. Wachel, PVP-Vol. 313-2, displacement-methode-for-determining-acceptable pipingvibration-amplitudes.

[23].

Singiresu S.Rao, “Mechanical Vibrations”, Prentice Hall, 2005.

[24].

Abdullah Mappaita, “Analisa Eksperimental Dan Teoritis Modus Getaran Beam Yang Ditumpu Sederhana”, ITB, 1987.

[25].

Kaneko, Nakamura, Inada, Kato, “Flow-Induced Vibrations. Classifications and Lessons from Practical Experiences”, Amsterdam: Elsevier, 2008.

150 http://digilib.mercubuana.ac.id/

[26].

Technical Paper, “Flow Of Fluids”, Crane Co, 1982.

[27].

Yarway, Automatic Recirculation Valve Manual Book.

[28].

http://elearning.gunadarma.ac.id/docmodul/index-mekanika_fluida_dasar.htm

[29].

http://mesin.ub.ac.id/diktat_ajar/mekflu.php

[30].

http://web.ipb.ac.id/~erizal/mekflud

[31].

http://vladvamphire.wordpress.com/sharing/pipingsystem

[32].

http://don85.wordpress.com\piping-stress-analysis\index.html

[33].

http://www.gs-harper.com/Mining_Research/Hydraulics/Transients.asp

[34].

http://www.swri.org/default.htm

[35].

http://chemeng.ugm.ac.id/personalpages/file.php?id=68&PHPSESSID

151 http://digilib.mercubuana.ac.id/

LAMPIRAN-C1

http://digilib.mercubuana.ac.id/

LAMPIRAN-C2


LAMPIRAN-C3


LAMPIRAN-C4 http://digilib.mercubuana.ac.id/

BP Berau Ltd. Tangguh LNG Project EQUIPMENT DATA SHEET FOR 062-D-1001A/B DEAERATOR

Doc No.: 62-EDS-FU-1261 KJP Doc. No. S-062-135B-002 Rev. 6C Sheet No. 2 of 5

LAMPIRAN-D1

COLUMN/DRUM SPECIFICATION SHEET Rev. 1 Item No.

062-D-1001A/B

2 Service

DEAERATOR

3 No. Required

Total 2 Sets Operating Condition

4 5 Fluid

STEAM/WATER

6 Pressure (Top/Bottom)

Kg/cm2A

2.03

/

7 Temperature (Top/Bottom)

0

C

120

/

8 Liquid Density

kg/m3

942.8

9 Total Volume

m3 m3

10 Normal Liquid Hold-up 11 Control Range Required

(NLL-LLL

) 10

min

(

)

min

(

)

min

12

Design Condition

13 14 Code / Regulation

ASME Sect. VIII Div. 1 (Stamp: Yes)

15 Special Service 16 Cyclic Service

X

No

X

No

/ MIGAS

Yes Yes

17 Inside Diameter

mm

DEAERATOR

2400

/ STORAGE 3400 (Note 2)

18 TL-TL Length

mm

DEAERATOR

6150

/ STORAGE 15150 (Note 2) 3.5

Kg/cm2G

@ 175

0

100

% Vacuum

@ 120

0

0

@ 3.5

19 Design Pressure & Temperature 20 Vacuum Condition

X

No

Yes

21 Minimum Design Metal Temperature (MDMT) 22 Test Press. Hydrostatic/Pneumatic

Kg/cm2G

23 Corrosion Allowance

mm

24 Postweld Heat Treatment

(Note 3)

20

C

C C

Kg/cm2G

/ 2.5 X

25 Radiographing 26 Head Type

X

Yes

No

Full

No

By Code

2:1 Ellip

Hemisphere

X

By Code Dish

____________________

27

DEAERATOR (Note 2) / STORAGE

28

Material

( Note 4)

29 Shell :

SA516-70 w/ SS 304 or better Lining (Note 5) / SA516-70

Internal (Removable)

30 Head :

SA516-70 w/ SS 304 or better Lining (Note 5) / SA516-70

Internal (Non-Removable)

31 Demister :

:

SS 304 or better :

SS 304 or better / C.S. (Note 6)

Support : SA36 / SA283-C

32 Nozzle Flange/Neck :

SA105 (Note 2) (Note 6)

/ SA106-B

External : C. S.

33 Bolt & Nut Ext./Int. :

SA193-B7 & SA194-2H

/

Gasket : SW 304 non-asbestos filler w/ external ring

34 35 36 Insulation

No X

37 Fire Proof

X

No

Hot Yes

Cold

PP

Thk ____50____ mm

__________ mm Accessories Supplied by Manufacturer

38 39 Ladder & Plat form Clips,

Pipe Support Clips,

40 Internal Ladder (Shell, Skirt), 41 Insulation Support,

Fire Proof Clip,

Template,

Top Davit,

Tailing Lug,

Lifting Lug,

Corrosion Point,

Anchor or Setting Bolts,

Non-Lubricant Sliding Plate

42 Notes :

(1) Deleted.

43

(2) Material, size and dimension of DEAERATOR section to be confirmed by vendor.

44

(3) Storage section only.

45

(4) Refer to Spec. S-900-1351-001Sect. 5.0 for additional requirements of materials.

46

(5) Lining not fully bonded to shell inside may be adopted subject to KJP's approval for the detail design.

47

(6) All parts coming in contact with corrosive gases shall be fabricated of SS 304 or better.

_ _ _ __ RA| D __| N I ||___ 005 EC-2 27-D DCTM_ARP.xls


Sliding Plate,

Earth Piece, Name Plate,



LAMPIRAN-D1

COLUMN/DRUM SPECIFICATION SHEET Rev. 1

Item No.

: 062-D-1001A/B

Service

: DEAERATOR

Nozzle Schedule

2

Mark

3

Size

Service

Q'ty

Rating & Facing

Remarks

4

DEAERATING HEATER

5

N1

24"

STEAM INLET

1

ASME 150# SO RF

6

N2

6"

MAKE UP WATER INLET

1

ASME 150# SO RF

W/ BAFFLE (BY VENDOR)

7

N3

2"

STEAM VENT

4

ASME 150# SO RF

W/ RESTRICTION ORIFICE (BY VENDOR)

8

N4A

20"

DOWNCOMER

1

ASME 150# SO RF

W/ VORTEX BREAKER (BY VENDOR)

9

N7A/B/E/F

12"

EQUALIZER

4

ASME 150# SO RF

W/ DRIP SHIELD (BY VENDOR)

10

N9

1

ASME 150# SO RF

N10

3/4" 16"

PRESSURE TRANSMITTER

11

CONDENSATE INLET

1

ASME 150# SO RF


12 M2

24"

MANHOLE

1

ASME 150# SO RF

W/ COVER & DAVIT (BY VENDOR)

13

12"

PSV

1

ASME 150# SO RF

N13


14 15

STORAGE DRUM

16

N4B

20"

DOWNCOMER

1

ASME 150# SO RF

W/ SCREEN (BY VENDOR)

17

N5

20"

WATER STORAGE OUTLET

1

ASME 150# SO RF

W/ VORTEX BREAKER (BY VENDOR)

18

N6 A/B

3/4"

LT CONNECTION

2

ASME 150# SO RF

19

N7C/D/G/H

12"

EQUALIZER

4

ASME 150# SO RF

20

N8

12"

BFW PUMP RECYCLE FLOW

1

ASME 150# SO RF

21

N11A/B

3/4"

LT CONNECTION

2

ASME 150# SO RF

22

N12

4"

EQUALIZING LINE

1

ASME 150# SO RF

23

M1

24"

MANHOLE

1

ASME 150# SO RF

24

N14

2"

DRAIN

1

ASME 150# SO RF

25 26 27 28 29 30 31 32 33 34 35 36 37 38

Note 1 : Nozzle sizes shall be verified by Vendor

39 40 41 42 43 44 45 46



W/ SPRAY PIPE (BY VENDOR)

W/ COVER & DAVIT (BY VENDOR)



LAMPIRAN-D1

COLUMN/DRUM SPECIFICATION SHEET Item No.

:

062-D-1001A/B

Service

:

DEAERATOR

NOTE : 1. UNIT = MM, DRAWING NOT TO SCALE. 2. VESSEL SIZES SHALL BE VERIFIED BY VENDOR.

TL-TL:6,150 N3 A

N2

6"

3/4"

N3 B

2"

N3 C

N10

2"

16"

N3 D

2"

N13

2"

12"

2,400 ID

N9

24" M2

24"

N7 A

N7 B

N4 A

N7 E

N1

N7 F

N12

12"

3,400 ID

12"

450 250 150 150

N6 A

M1

3/4"

N7 D

N4 B

12" N7 G

N8

4" N7 H

12" 3/4"

N11 A

3/4"

N11 B

HLL HLA

NLL LLA

24"

1,550 150 700

N7 C

12"

20"

LLL LLLL

N6 B

3/4"

2"

20" N5

ELEVATION +14,000 From GRADE

N14

TL-TL:15,150

* THIS FIGURE SHOWS TYPICAL TYPE OF DEAERATION ONLY. VENDOR SHALL PROPOSE THE TYPE.





LAMPIRAN-D1

COLUMN/DRUM SPECIFICATION SHEET Rev. 1 Item No.

: 062-D-1001A/B

Service DEAERATOR

2 3 Operating Condition : 4 Steam Inlet : 5

- Pressure

Kg/cm2G

3.5

6

- Temperature

o

148

7

- Flowrate

Kg/h

33846

C

8 Makeup Water Inlet :

- Pressure

Kg/cm2G

1.0

10

- Temperature

o

47.2

11

- Flowrate

Kg/h

36449 (Maximum flow rate of make up is 42740 kg/hr.)

9

C

12 Condensate : 13

- Pressure

Kg/cm2G

1.0

14

- Temperature

o

87.5

15

- Flowrate

Kg/h

445945

C

16 BFW Outlet : 17

- Pressure

Kg/cm2G

1.0

18

- Temperature

o

120

19

- Flowrate

Kg/h

515724

C

20 Vent Steam 21

- Pressure

Kg/cm2G

1.0

22

- Temperature

o

120

23

- Flowrate

Kg/h

516 (Vendor to specifiy. Vendor to provide restriction orifice.)

C

24 25 Relieving Steam(PSV) 26

- Pressure

Kg/cm2G

3.50

27

- Temperature

o

153

28

- Flowrate

Kg/h

41071

mg/L

Less than 0.007

C

29 30 Specification : 31 Oxygen content in BFW 32 33 34 35 36 37 38 39 40 41 42 43 44 45 46



Doc No.: 62-EDS-MC-1401 LAMPIRAN-D2 KJP Doc. No. S-062-1358-001 Rev. 6C Sheet No. 2 of 8

BP Berau Ltd. Tangguh LNG Project 3.8 MTPA / TRAIN CAPACITY Equipment Data Sheet for 062-P-1001A/B/C Boiler Feed Water Pump

CENTRIFUGAL PUMP DATA SHEET (API 610-8TH) 1 APPLICABLE TO:

PROPOSALS

PURCHASE

AS BUILT

2 FOR

TANGGUH LNG FACILITIES PROJECT

UNIT STEAM SYSTEM

3 SITE

TANAH MERAH, PAPUA, REPUBLIC OF INDONESIA

SERVICE BOILER FEED WATER PUMP

4 NO. REQ

THREE (3)

PUMP SIZE

5 MANUFACTURER

TYPE

NO. STAGE

MODEL

SERIAL NO.

6 NOTES INFORMATION BELOW TO BE COMPLETEDBY PURCHASER 7

BY MANUFACTURER

BY MANUFACTURER OR PURCHASER

GENERAL (3.1.1)

8 PUMPS TO OPERATE IN (PARALLEL)

NO. MOTOR DRIVEN

9 (SERIES) WITH

PUMP ITEM NO.

THREE (3)

NO. TURBINE DRIVEN

062-P-1001A/B/C

PUMP ITEM NO.

10 GEAR ITEM NO.

MOTOR ITEM NO. 062-PM-1001A/B/C

TURBINE ITEM NO.

11 GEAR PROVIDED BY

MOTOR PROVIDED BY

PUMP VENDOR

TURBINE PROVIDED BY

12 GEAR MOUNTED BY

MOTOR MOUNTED BY

PUMP VENDOR

TURBINE MOUNTED BY

13 GEAR DATA SHT. NO.

MOTOR DATA SHT. NO.

14

OPERATING CONDITIONS 452

15 X CAPACITY, NORM 16

SITE AND UTILITY DATA (CONT'D)

(m3/h) RATED 526

(m3/h)

OTHER

608

20 X DIFF. HEAD

(Kg/cm2A) (Kg/cm2)

57.34

19 X DIFFERENTIAL PRESSURE (m)

13.5 *2) (m) *16)

NPSHA

PROCESS VARIATIONS

22 X STARTING CONDITIONS AUTO - START*13) 23 SERVICE: X CONT.

(kPa)

LIQUID

X PUMPING TEMPERATURE: 120

NORMAL

(3.1.3)

X VAPOR PRESSURE

(oC) MAX.

(oC) MIN. (Kg/cm2 A) @

2.03

(oC) (oC)

120

3

X RELATIVE DENSITY (SPECIFIC GRAV(Kg/m )

INTERMITTENT (STARTS/DAY)

SITE AND UTILITY DATA

942.8

NORMAL

MAX

MIN

SPECIFIC HEAT, Cp

26 LOCATION: (2.1.29) INDOOR

/

X TYPE OR NAME OF LIQUIDBOILER FEED WATER

(3.1.2)

24 X PARALLEL OPERATION REQ'D (2.1.11) (2 Para + 1 Standby) 25

(3.5.2.6)

3.31 (Kg/cm2A) INSTRUMENT AIR: MAX/MIN PRESS

/

60.65

18 X DISCHARGE PRESSURE

27

WATER SOURCE CHLORIDE CONCENTRATION (PPM)

17 X SUCTION PRESSURE MAX./RAT 6.03

21

TURBINE DATA SHT. NO.

(kJ/kg oC)

0.229

X VISCOSITY

120

(cP) @

(oC)

HEATED

UNDER ROOF

MAX. VISCOSITY

28 X OUTDOOR

UNHEATED

PARTIAL SIDES

CORROSIVE/EROSIVE AGENT

(2.11.1.8)

29 X GRADE

MEZZANINE

CHLORIDE CONCENTRATION (PPM)

(3.5.2.6)

H2S CONCENTRATION (PPM)

30 X ELECTRIC AREA CLASSIFICATION (2.1.22 / 3.1.5) 31 32

CL

T3

GR

IIA

WINTERIZATION REQ'D

ZONE

2

LIQUID (2.1.3)

X TROPICALIZATION REQ'D.

(2.11.1.11)

HAZARDOUS

FLAMMABLE

OTHER

33 SITE DATA (2.1.29) 34 X ALTITUDE

(cP)

PERFORMANCE 2

(m) BAROMETER 1.03 (Kg/cm A)

16

35 X RANGE OF AMBIENT TEMPS: MIN/M20

/

36 X RELATIVE HUMIDITYMIN / MAX

/

37 UNUSUAL CONDITIONS: (2.1.23)

FUMES

DUST

33 100

PROPOASAL CURVE NO.

RPM

(oC)

IMPELLER DIA. RATED

MAX.

(%)

RATED POWER

(BHP) EFFICIENCY

MIN.

(mm) (%)

MINIMUM CONTINUOUS FLOW:

38

OTHER

THERMAL

39

UTILITY CONDITIONS:

PREFERRED OPERATING REGION

TO

(m3/h)

ALLOWABLE OPERATING REGION

TO

(m3/h)

40 STEAM:

DRIVERS

HEATING

2

2

(m3/h) STABLE

41

MIN

(Kg/cm G)

(oC)

(Kg/cm G)

(oC)

MAX HEAD @ RATED IMPELLER *12)

42

MAX

(Kg/cm2G)

(oC)

(Kg/cm2G)

(oC)

MAX POWER @ RATED IMPELLER

43 ELECTRICITY DRIVERS HEATING CONTROL

SHUTDOWN

44

VOLTAGE 6600

220

220

220

45

HERTZ

50

50

50

50

46

PHASE

3

1

1

1

48

TEMP. INLET

45

PRESS. NORM

5.9

EST MAX SOUND PRESS. LEVEL

50

MIN RETURN

_ _ _ __ RA| D __| N I ||___ 005 UG-2 08-A DCTM_ARP.xls

0.8

REMARKS: (oC)

MAX. RETURN 55

(Kg/cmDESIGN

8.1

(m) (kW) (m) (2.1.8)

SUCTION SPECIFIC SPEED X MAX. SOUND PRESS. LEVEL REQ92 @ 1 meter

47 COOLING WATER: (2.1.17)

49

NPSHR AT RATED CAPACITY *11)

(m3/h)

(oC)

(2.1.9) (dBA) (2.1.14) (dBA) (2.1.14dBA

*1) DELETED.

*2) NPSH AVAILABLE REFERENCE IS G.L + 1 ME *3) RESTRICTION

(Kg/cm2G) ORIFICE FOR WARM UP BYPASS TO BE PROVIDED BY VENDOR IF

(Kg/cm2G) MAX Allow DP 1.0 (Kg/cm2G) REQUIRED.

*16) NPSHA AT 110% OF RATED CAPACITY IS ALSO 13.5 M.


Doc No.: 62-EDS-MC-1401 KJP Doc. No. S-062-1358-001 Rev. 6C LAMPIRAN-D2 Sheet No. 3 of 8


CENTRIFUGAL PUMP DATA SHEET (API 610-8TH) 1

CONSTRUCTION

CONSTRUCTION (CONT)

2 APPLICABLE STANDARD:

SHAFT DIAMETER BETWEEN BEARINGS

(mm)

3 X API 610 8TH EDITION

SPAN BETWEEN BEARING CENTERS

(mm)

SPAN BETWEEN BEARING & IMPELLER

(mm)

4 X OTHER

99-SPE-MC-1404(S-900-1358-001) (SEE REMARKS)

5 PUMP TYPE: (1.1.2) 6

OH2

7 8

REMARKS

BB1

VS1

VS6

OH3

BB2

VS2

VS7

OH6

X BB3

VS3

OTHER

9

BB4

VS4

10

BB5

VS5

11 X NOZZLE CONDITIONS: (2.3.2) 12

SIZE

COUPLINGS: (3.2.2)

DRIVER - PUMP

MAKE MODEL

*4)

RATING

RATING (kW/100 RPM) FAC'G POSITION

X LUBRICATION

13

NON - LUBE

LIMITED END FLOAT REQUIRED

14 SUCTION

600#

RF

SIDE

SPACER LENGTH

15 DISCHARGE

600#

RF

SIDE

SERVICE FACTOR

16 BALANCE DRUM

DRIVER HALF COUPLING MOUNTED BY: (3.2.11)

17 PRESSURE CASING CONNECTIONS: (2.3.3) 18

X PUMP MFR.

3/4"

W/ FLANGED VALVE

20 X VENT

3/4"

W/ FLANGED VALVE

21

PRESSURE GAUGE

22

TEMP GAUGE

23

WARM-UP

24

BALANCE / LEAK-OFF

25

CYLINDRICAL THREADS REQUIRED (2.3.3)

API BASEPLATE NUMBER

FOOT IN-LINE

REMARKS:

MATERIAL X APPENDIX H CLASS

C-6

NEAR CENTERLINE

MIN DESIGN METAL TEMP (2.11.4.5)

SEPARATE MOUNTING PLATE

BARREL/CASE

(2.11.1.1) (oC)

IMPELLER

CASE/IMPELLER WEAR RINGS

30 CASING SPLIT: 31

(APPENDIX M)

NON-GROUT CONSTRUCTION: (3.3.13/5.3.7.3.5)

X CENTERLINE

29

PURCHASER

BASEPLATES:

26 CASING MOUNTING: ( SEE SEPARATE SHEET FOR VERTICLES)

28

DRIVER MFR.

COUPLING PER API 671 (5.2.7)

TYPE

NO. SIZE (NPS)

19 X DRAIN

27

(mm)

SHAFT

X AXIAL

RADIAL

DIFFUSERS

32 CASING TYPE:

COUPLING SPACER/HUBS

33

SINGLE VOLUTE X MULTIPLE VOLUTE

DIFFUSER

34

OVERHUNG

BARREL

X BETWEEN BEARINGS

COUPLING DIAPHAGMS (DISKS) REMARKS:

35 CASE PRESSURE RATING; 36 X MAX ALLOWABLE WORKING PRESSUR 78.0 *5) (Kg/cm2G) 37

@

(oC)

148

38 X HYDROTEST PRESSURE 39

41

105

(Kg/cm G) BEARING (TYPE/NUMBER):

SUCT'N PRESS. REGIONS MUST BE DESIGNED FOR MAWP (2.2.4) RADIAL

40 ROTATION:

42

BEARINGS AND LUBRICATION 2

(VIEWED FROM COUPLING END)

CW

THRUST

CCW

*6)

/

*6)

/

REVIEW AND APPROVE THRUST BEARING SIZE (5.2.5.2.4)

IMPELLERS INDIVIDUALLY SECURED (5.2.2.2)

LUBRICATION: (2.10) *6)

43 REMARKS:

GREASE

FLOOD

RING OIL

44

FLINGER

PURGE OIL MIST

PURE OIL MIST

45

BOLT OH3 PUMP TO PAD/FOUNDATION (5.1.2.4)

CONSTANT LEVEL OILER PREFERENCE (SEE REMARKS) (2.9.2.2)

46 SHAFT: 47

PRESSURE LUBE SYS (5.2.6)

SHAFT DIAMETER AT COUPLING

(mm)

API-610

API-614

OIL VISC. ISO GRADE (5.2.6.5)

48 REMARKS:

*4) FLANGES SHALL HAVE SMOOTH FACE WITH SPIRAL GROOVES WITH ROUGHNESS OF 125 ~ 250 AARH.

49

*5) SHUT OFF PRESSURE SHOULD NOT EXCEED 78.0kg/cm2G.

50

*6) BEARING AND LUBRICATION SLECTION SHALL BE COMPLIED WITH TABLE 2-7 of API610 8th.

_ _ _ __ RA| D __| N I ||___ 51

005 UG-2 08-A DCTM_ARP.xls



Doc No.: 62-EDS-MC-1401 KJP Doc. No. LAMPIRAN-D2 S-062-1358-001 Rev. 6C Sheet No. 7 of 8

INDUCTION MOTOR 1 2 3 4 5

X PROPOSAL APPLICABLE TO: PURCHASE FOR TANGGUH LNG FACILITIES PROJECT SITE TANAH MERAH, PAPUA, REPUBLIC OF INDONESIA SERVICE MOTOR DRIVER FOR BOILER FEED WATER PUMP MANUFACTURER MODEL

6 NOTE: INFORMATION TO BE COMPLETED: 7 MOTOR DESIGN DATA 8 APPLICABLE SPECIFICATIONS: 9

NEMA

AS BUILT FURNISHED BY PUMP VENDOR UNIT STEAM SYSTEM DRIVER EQUIP. 62-P-1001 A/B/C NO. REQUIRED THREE (3) SERIAL NO.

BY PURCHASER

MG 1

FULL VOLTAGE

10 X 99-SPE-EL-1401

X

14

GR. IIA ZONE

16 m

2

NON-HAZARDOUS

X AMB'T TEMPS:

15

MAX

33

o

MIN

20

o

%

% X IEC 34-14

NEMA STANDARD

C

85

UNLOADED

VOLTAGE DIP VIBRATION:

X CL. T3 ALT.

X REDUCED VOLTAGE

X LOADED

11 X IEC 60034 12 SITE DATA: 13 AREA:

BY MANUFACTURER MOTOR DESIGN DATA CONTINUED STARTING:

NOISE:

C

X 99-SPE-EL-1972

NEMA STANDARD

(90 dBA)

16 UNUSUAL CONDITIONS: DUST FUMES 17 OTHER DESIGN AMBIENT TEMP 40 deg-C X DIRECT CONNECTED

18 DRIVE SYSTEM:

ACCESSORY EQUIPMENT

19

GEAR

BASEPLATE

20

OTHER

MFR. STD. FANS

21 TYPE OF MOTOR: NEMA DESIGN

KW REQ'D

SYNCHRONOUS

BY:

24

POWER FACTOR REQ'D

25

EXCITATION:

26

VOLTS

PURCHASER

MANUFACTURER

DESCRIPTION

BRUSHLESS

SLIP RING

ENCLOSED COLLECTOR RINGS:

FIELD DISCHARGE RESISTOR BY MOTOR MFR.

27

STATOR SHIFT

X NONSPARKING FANS

D.C. EXCITATION

22 X SQUIRREL CAGE INDUCTION 23

SOLEPLATE

PURGED: MEDIUM

WOUND ROTOR INDUCTION

PRESS.

BARG

EXPLOSION-RESISTANT NONPURGED

28

FORCED VENTILATION

29 ENCLOSURE:

m3/h

30 X CLASS T3

GROUP

31 X TEFC, SEVERE DUTY

IIA

ZONE

2

EXP. PROOF

32

WEATHER PROTECTED, TYPE

33

TEWAC

PRESS. DROP

mm H2O

BEARING TEMP. DEVICES: LOCATION DESCRIPTION

TEIGF, USING

GAS

34

DOUBLE WALL CARBON STEEL TUBES

35

WATER SUPPLY:

36

WATER ALLOW: ∆ P

37

WATER SIDE MIN. CORR. ALLOW.

38

AND FOUL FACTOR

39

(AIR)(GAS) SUPPLY PRESS.

PRESS

o

o

C FOR ALARM

SET @

C FOR SHUTDOWN

X SPACE HEATERS:

BARG

o

TEMP.

C

o

C

BAR & TEMP. RISE

mm

KW

220

VOLTS

1

PHASE

50

MAX. SHEATH TEMP

%

WINDING TEMPERATURE DETECTOR: THERMISTORS: NO/PHASE

BARG

TYPE:

POS. TEMP. COEFF.

NEG. TEMP. COEFF.

40

FORCED VENTILATED

TEMPERATURE SWITCH:

41

OPEN-DRIPPROOF

RESISTANCE TEMPERATURE DETECTORS: NO/PHASE

42

OPEN

YES

43

SELECTOR SWITCH & INDICATOR BY: MAX. STATOR WINDING TEMPS: o C FOR ALARM

6600

VOLTS

47

NAMEPLATE HP

48

SYNCHRONOUS RPM

49 X INSULATION: 50 X TEMP. RISE: 51 NOTES: 52

NO

RESISTANCE MATL.

44 45 BASIC DATA: 46 X

3

PHASE

50

HERTZ

SERVICE FACTOR

F o

C ABOVE

TYPE

IN SAME CONDUIT BOX

REMARKS: o

C

BY

*1) TEMP. RISE CLASS : F

_ _ _ __ RA| D __| N I ||___ 005 UG-2 DCTM_ARP.xls 08-A

OHMS PURCH. o

C FOR SHUTDOWN

WINDING TEMP. DETECTOR & SPACE HEATER LEADS:

X IN SEPARATE CONDUIT BOXES

CLASS *1)

HERTZ


MFR.


LAMPIRAN-E1 POINT/ LOKASI -1 x y z

Verical Direction (y) Displacement Frequency µm mils Hz 4.69 119.126 45.6 12.61 320.294 1.875 11.88 301.752 25.625 9.41 239.014 26.875 10.97 278.638 2.5

Horizontal Direction (x) Displacement Frequency µm mils Hz 3.39 86.106 0.625 4.84 122.936 0.625 6.28 159.512 0.625 5.36 136.144 1.25 5.79 147.066 1.25

Axial Direction (z) Displacement Frequency µm mils Hz 2.84 72.136 0.625 3.73 94.742 3.738 6.63 168.402 0.625 4.91 124.714 0.625 4.56 115.824 0.625

Source. Piping Vibration and Stress (J. C. Wachel) http://digilib.mercubuana.ac.id/


Verical Direction (y) Displacement Frequency µm mils Hz 7.53 191.262 0.625 14.97 380.238 0.625 15.25 387.35 8.75 22.04 559.816 0.625

Horizontal Direction (x) Displacement Frequency µm mils Hz 12.95 328.93 8.75 15.02 381.508 0.65 14.86 377.444 0.625 21.75 552.45 1.25

Axial Direction (z) Displacement Frequency µm mils Hz 2.48 62.992 low 7.31 185.674 0.625 6.02 152.908 26.875 9.12 231.648 0.625



Verical Direction (y) Displacement Frequency µm mils Hz 7.32 185.928 7.32 9.74 247.396 1.875 9.41 239.014 6.25 9.97 253.238 0.625 11.91 302.514 23.75 10.09 256.286 0.625

Horizontal Direction (x) Displacement Frequency µm mils Hz 4.54 115.316 0.625 6.8 172.72 8.75 8.09 205.486 0.625 7.74 196.596 0.65 9.01 228.854 0.625 13.376 339.7504 1.25

Axial Direction (z) Displacement Frequency µm mils Hz 4.78 121.412 0.625 4.34 110.236 1.875 3.51 89.154 0.625 5.65 143.51 0.625 5.75 146.05 0.625 5.09 129.286 0.625



Verical Direction (y) Displacement Frequency µm mils Hz 12.86 326.644 0.625 18.15 461.01 19.375 9.8 248.92 10

Horizontal Direction (x) Displacement Frequency µm mils Hz 8.6 218.44 4.375 3.62 91.948 0.625 5.32 135.128 8.125

Axial Direction (z) Displacement Frequency µm mils Hz 4.89 124.206 0.625 3.46 87.884 3.463 2.51 63.754 0.625



Verical Direction (y) Displacement Frequency µm mils Hz 4.82 122.428 11.875 3.785 96.139 11.25

Horizontal Direction (x) Displacement Frequency µm mils Hz 4.8 121.92 6.25 3.53 89.662 1.875

Axial Direction (z) Displacement Frequency µm mils Hz 3.16 80.264 10.625 2.86 72.644 0.625



Verical Direction (y) Displacement Frequency µm mils Hz 6.03 153.162 11.875 9.4 238.76 13.75 4.14 105.156 13.75 5.84 148.336 19.375

Horizontal Direction (x) Displacement Frequency µm mils Hz 2.99 75.946 0.625 4.8 121.92 0.625 1.96 49.784 7.5 2.94 74.676 7.5

Axial Direction (z) Displacement Frequency µm mils Hz 3.35 85.09 0.625 7.45 189.23 11.875 2.62 66.548 0.625 3.81 96.774 0.625


PIPING CLASS 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S

PIPE (P) PIPE (P) PIPE (P) PIPE (P) 90 ELBOW (9L) 90 ELBOW (9L) 90 ELBOW (9L) 90 ELBOW (9L) 45 ELBOW (4L) 45 ELBOW (4L) 45 ELBOW (4L) 45 ELBOW (4L) STRAIGHT TEE (TS) STRAIGHT TEE (TS) STRAIGHT TEE (TS) STRAIGHT TEE (TS) REDUCING TEE (TR) REDUCING TEE (TR) REDUCING TEE (TR) REDUCING TEE (TR) REDUCING TEE (TR) REDUCING TEE (TR) REDUCING TEE (TR) REDUCING TEE (TR) REDUCING TEE (TR) REDUCING TEE (TR) REDUCING TEE (TR) REDUCING TEE (TR) REDUCING TEE (TR) REDUCING TEE (TR) REDUCING TEE (TR) REDUCING TEE (TR) REDUCING TEE (TR) CONCENTRIC REDUCER (RC) CONCENTRIC REDUCER (RC) CONCENTRIC REDUCER (RC) CONCENTRIC REDUCER (RC) CONCENTRIC REDUCER (RC) CONCENTRIC REDUCER (RC) CONCENTRIC REDUCER (RC) CONCENTRIC REDUCER (RC) CONCENTRIC REDUCER (RC) CONCENTRIC REDUCER (RC) CONCENTRIC REDUCER (RC) CONCENTRIC REDUCER (RC) CONCENTRIC REDUCER (RC)

Short Code

Size (L/Run) 0.5-1.5 2-10 12-24 30 0.5-1.5 2-10 12-24 30 0.5-1.5 2-10 12-24 30 0.5-1.5 2-10 12-24 30 0.75 1 1.5 3 4 6 8 10 12 14 14 16 18 20 22 24 30 3 4 6 8 10 12 14 14 16 16 18 18 20

Size (S/Branch) Wall-T(L) Wall-T(S) Description XS Pipe A106-B Seamless ASME B36.10M/B36.19M PE XS Pipe A106-B Seamless ASME B36.10M/B36.19M BE SCH60 Pipe A106-B Seamless ASME B36.10M/B36.19M BE 28.58mm Pipe API5L-PSL1-B SAW ASME B36.10M/B36.19M BE PWHT 90Elbow A105 CL3000 ASME B16.11 SW XS 90Elbow LR A234-WPB Seamless ASME B16.9 BW SCH60 90Elbow LR A234-WPB Seamless ASME B16.9 BW 28.58mm 90Elbow LR A234-WPB-W Weld ASME B16.9 BW PWHT 45Elbow A105 CL3000 ASME B16.11 SW XS 45Elbow LR A234-WPB Seamless ASME B16.9 BW SCH60 45Elbow LR A234-WPB Seamless ASME B16.9 BW 28.58mm 45Elbow LR A234-WPB-W Weld ASME B16.9 BW PWHT Straight Tee A105 CL3000 ASME B16.11 SW XS Straight Tee A234-WPB Seamless ASME B16.9 BW SCH60 Straight Tee A234-WPB Seamless ASME B16.9 BW 28.58mm Straight Tee A234-WPB-W Weld ASME B16.9 BW PWHT 0.5 Reducing Tee A105 CL3000 ASME B16.11 SW 0.5-0.75 Reducing Tee A105 CL3000 ASME B16.11 SW 0.5-1 Reducing Tee A105 CL3000 ASME B16.11 SW 2 XS XS Reducing Tee A234-WPB Seamless ASME B16.9 BW 2-3 XS XS Reducing Tee A234-WPB Seamless ASME B16.9 BW 3-4 XS XS Reducing Tee A234-WPB Seamless ASME B16.9 BW 4-6 XS XS Reducing Tee A234-WPB Seamless ASME B16.9 BW 6-8 XS XS Reducing Tee A234-WPB Seamless ASME B16.9 BW 8-10 SCH60 XS Reducing Tee A234-WPB Seamless ASME B16.9 BW 10 SCH60 XS Reducing Tee A234-WPB Seamless ASME B16.9 BW 12 SCH60 SCH60 Reducing Tee A234-WPB Seamless ASME B16.9 BW 12-14 SCH60 SCH60 Reducing Tee A234-WPB Seamless ASME B16.9 BW 14-16 SCH60 SCH60 Reducing Tee A234-WPB Seamless ASME B16.9 BW 14-18 SCH60 SCH60 Reducing Tee A234-WPB Seamless ASME B16.9 BW 14-20 SCH60 SCH60 Reducing Tee A234-WPB Seamless ASME B16.9 BW 14-20 SCH60 SCH60 Reducing Tee A234-WPB Seamless ASME B16.9 BW 14-24 28.58mm SCH60 Reducing Tee A234-WPB-W Weld ASME B16.9 BW PWHT 2 XS XS Concentric Reducer A234-WPB Seamless ASME B16.9 BW 2-3 XS XS Concentric Reducer A234-WPB Seamless ASME B16.9 BW 3-4 XS XS Concentric Reducer A234-WPB Seamless ASME B16.9 BW 4-6 XS XS Concentric Reducer A234-WPB Seamless ASME B16.9 BW 4-8 XS XS Concentric Reducer A234-WPB Seamless ASME B16.9 BW 6-10 SCH60 XS Concentric Reducer A234-WPB Seamless ASME B16.9 BW 6-10 SCH60 XS Concentric Reducer A234-WPB Seamless ASME B16.9 BW 12 SCH60 SCH60 Concentric Reducer A234-WPB Seamless ASME B16.9 BW 8-10 SCH60 XS Concentric Reducer A234-WPB Seamless ASME B16.9 BW 12-14 SCH60 SCH60 Concentric Reducer A234-WPB Seamless ASME B16.9 BW 10 SCH60 XS Concentric Reducer A234-WPB Seamless ASME B16.9 BW 12-16 SCH60 SCH60 Concentric Reducer A234-WPB Seamless ASME B16.9 BW 12-18 SCH60 SCH60 Concentric Reducer A234-WPB Seamless ASME B16.9 BW

4

LAMPIRAN F



Short Code CONCENTRIC REDUCER (RC) CONCENTRIC REDUCER (RC) ECCENTRIC REDUCER (RE) ECCENTRIC REDUCER (RE) ECCENTRIC REDUCER (RE) ECCENTRIC REDUCER (RE) ECCENTRIC REDUCER (RE) ECCENTRIC REDUCER (RE) ECCENTRIC REDUCER (RE) ECCENTRIC REDUCER (RE) ECCENTRIC REDUCER (RE) ECCENTRIC REDUCER (RE) ECCENTRIC REDUCER (RE) ECCENTRIC REDUCER (RE) ECCENTRIC REDUCER (RE) ECCENTRIC REDUCER (RE) ECCENTRIC REDUCER (RE) ECCENTRIC REDUCER (RE) CAP (CA) CAP (CA) CAP (CA) CAP (CA1) STRAIGHT NIPPLE PEPE (PPP) STRAIGHT NIPPLE PETH (PPT) SWAGED NIPPLE BEPE (NBP) SWAGED NIPPLE BETH (NBT) SWAGED NIPPLE PEPE (NPP) SWAGED NIPPLE PEPE (NPP) SWAGED NIPPLE PEPE (NPP) SWAGED NIPPLE PETH (NPT) SWAGED NIPPLE PETH (NPT) SWAGED NIPPLE PETH (NPT) SWAGED NIPPLE THPE (NTP) COUPLING SW-SW (CSS) COUPLING SW-THREAD (CST) RED COUPLING SW-SW (CRSS) RED COUPLING SW-THRD (CRST) SOCKOLET (DS) SOCKOLET (DS) SOCKOLET (DS) SOCKOLET (DS) SOCKOLET (DS) SOCKOLET (DS) SOCKOLET (DS) SOCKOLET (DS) SOCKOLET (DS)

Size (L/Run) 22 24 3 4 6 8 10 12 14 14 16 16 18 18 20 22 24 30 0.5-1.5 2-10 12-24 0.5-1.5 0.5-1.5 0.5-1.5 2 2 0.75 1 1.5 0.75 1 1.5 1 0.5-1.5 0.5-1 0.75 0.75 2 3 4 6 8 10 12 14 16

http://digilib.mercubuana.ac.id/ 0.5 0.5 0.5-1.5 0.5-1.5 0.5-1.5 0.5-1.5 0.5-1.5 0.5-1.5 0.5-1.5 0.5-1.5 0.5-1.5

0.75-1.5 0.75-1.5 0.5 0.5-0.75 0.5-1 0.5 0.5-0.75 0.5-1 0.75

Size (S/Branch) 14-20 16-20 2 2-3 3-4 4-6 4-8 6-10 6-10 12 8-10 12-14 10 12-16 12-18 14-20 16-20 20

SCH160 SCH160 XS XS SCH160 SCH160 SCH160 SCH160 SCH160 SCH160 SCH160

XS SCH60

Wall-T(L) SCH60 SCH60 XS XS XS XS XS SCH60 SCH60 SCH60 SCH60 SCH60 SCH60 SCH60 SCH60 SCH60 SCH60 28.58mm

XS XS SCH160 SCH160 SCH160 SCH160 SCH160 SCH160 SCH160

Wall-T(S) SCH60 SCH60 XS XS XS XS XS XS XS SCH60 XS SCH60 XS SCH60 SCH60 SCH60 SCH60 SCH60

Description Concentric Reducer A234-WPB Seamless ASME B16.9 BW Concentric Reducer A234-WPB Seamless ASME B16.9 BW Eccentric Reducer A234-WPB Seamless ASME B16.9 BW Eccentric Reducer A234-WPB Seamless ASME B16.9 BW Eccentric Reducer A234-WPB Seamless ASME B16.9 BW Eccentric Reducer A234-WPB Seamless ASME B16.9 BW Eccentric Reducer A234-WPB Seamless ASME B16.9 BW Eccentric Reducer A234-WPB Seamless ASME B16.9 BW Eccentric Reducer A234-WPB Seamless ASME B16.9 BW Eccentric Reducer A234-WPB Seamless ASME B16.9 BW Eccentric Reducer A234-WPB Seamless ASME B16.9 BW Eccentric Reducer A234-WPB Seamless ASME B16.9 BW Eccentric Reducer A234-WPB Seamless ASME B16.9 BW Eccentric Reducer A234-WPB Seamless ASME B16.9 BW Eccentric Reducer A234-WPB Seamless ASME B16.9 BW Eccentric Reducer A234-WPB Seamless ASME B16.9 BW Eccentric Reducer A234-WPB Seamless ASME B16.9 BW Eccentric Reducer A234-WPB-W Weld ASME B16.9 BW PWHT Cap A105 CL3000 ASME B16.11 SW Cap A234-WPB Seamless ASME B16.9 BW Cap A234-WPB Seamless ASME B16.9 BW Cap A105 CL3000 ASME B16.11 NPT Straight Nipple A106-B Seamless ASME B36.10M/B36.19M PE - PE L=100mm Straight Nipple A106-B Seamless ASME B36.10M/B36.19M PE - NPT L=100mm Swaged Nipple A234-WPB Seamless MSS SP-95 BE(L) - PE(S) Swaged Nipple A234-WPB Seamless MSS SP-95 BE(L) - NPT(S) Swaged Nipple A234-WPB Seamless MSS SP-95 PE(L) - PE(S) Swaged Nipple A234-WPB Seamless MSS SP-95 PE(L) - PE(S) Swaged Nipple A234-WPB Seamless MSS SP-95 PE(L) - PE(S) Swaged Nipple A234-WPB Seamless MSS SP-95 PE(L) - NPT(S) Swaged Nipple A234-WPB Seamless MSS SP-95 PE(L) - NPT(S) Swaged Nipple A234-WPB Seamless MSS SP-95 PE(L) - NPT(S) Swaged Nipple A234-WPB Seamless MSS SP-95 NPT(L) - PE(S) Coupling A105 CL3000 ASME B16.11 SW - SW Coupling A105 CL3000 ASME B16.11 SW - NPT Reducing Coupling A105 CL3000 ASME B16.11 SW(L) - SW(S) Reducing Coupling A105 CL3000 ASME B16.11 SW(L) - NPT(S) Olet A105 CL3000 MSS SP-97 SW Olet A105 CL3000 MSS SP-97 SW Olet A105 CL3000 MSS SP-97 SW Olet A105 CL3000 MSS SP-97 SW Olet A105 CL3000 MSS SP-97 SW Olet A105 CL3000 MSS SP-97 SW Olet A105 CL3000 MSS SP-97 SW Olet A105 CL3000 MSS SP-97 SW Olet A105 CL3000 MSS SP-97 SW

4

LAMPIRAN F


Short Code SOCKOLET (DS) SOCKOLET (DS) SOCKOLET (DS) SOCKOLET (DS) SOCKOLET (DS) WELDOLET (DW) WELDOLET (DW) WELDOLET (DW) WELDOLET (DW) WELDOLET (DW) WELDOLET (DW) WELDOLET (DW) WELDOLET (DW) WELDOLET (DW) WELDOLET (DW) WELDOLET (DW) WELDOLET (DW) WELDOLET (DW) WELDOLET (DW) WELDOLET (DW) WELDOLET (DW) PLUG (PL) FLANGE (F) FLANGE (F) FLANGE (F) FLANGE (F) FLANGE (F) FLANGE (F) FLANGE (F2) FLANGE (F2) BLIND FLANGE (FB) GASKET (G) GASKET (G) GASKET (G) GASKET (G) GASKET (G2) BOLT AND NUT (B) BOLT AND NUT (B) BOLT AND NUT (B2) GATE VALVE (V) GATE VALVE (V) GATE VALVE (V) GATE VALVE (V) GATE VALVE (V1) GLOBE VALVE (W) GLOBE VALVE (W)

Size (L/Run) 18 20 22 24 30 6 8 10 12 14 16 18 18 20 20 22 22 24 24 30 30 0.5-2 0.5-1.5 2-10 12-20 22 24 30 10 12 0.5-24 0.5-20 22 24 30 10-12 0.5-1 1.125-1.8 1.875-2 0.5-1.5 2-6 8-24 30 0.5-0.75 0.5-1.5 2-4

Size (S/Branch) 0.5-1.5 0.5-1.5 0.5-1.5 0.5-1.5 0.5-1.5 2 2-3 2-4 2-6 2-8 2-10 2-10 12 2-10 12 2-10 12 2-10 12 2-10 12 XS XS SCH60 SCH60 SCH60 28.58mm XS SCH60

XS XS XS SCH60 SCH60 SCH60 SCH60 SCH60 SCH60 SCH60 SCH60 SCH60 SCH60 SCH60 28.58mm 28.58mm

XS XS XS XS XS XS XS SCH60 XS SCH60 XS SCH60 XS SCH60 XS SCH60

Wall-T(L) Wall-T(S)

Description Olet A105 CL3000 MSS SP-97 SW Olet A105 CL3000 MSS SP-97 SW Olet A105 CL3000 MSS SP-97 SW Olet A105 CL3000 MSS SP-97 SW Olet A105 CL3000 MSS SP-97 SW Olet A105 MSS SP-97 BW Olet A105 MSS SP-97 BW Olet A105 MSS SP-97 BW Olet A105 MSS SP-97 BW Olet A105 MSS SP-97 BW Olet A105 MSS SP-97 BW Olet A105 MSS SP-97 BW Olet A105 MSS SP-97 BW Olet A105 MSS SP-97 BW Olet A105 MSS SP-97 BW Olet A105 MSS SP-97 BW Olet A105 MSS SP-97 BW Olet A105 MSS SP-97 BW Olet A105 MSS SP-97 BW Olet A105 MSS SP-97 BW Olet A105 MSS SP-97 BW Plug Round Head A105 ASME B16.11 NPT Flange SW A105 CL600 ASME B16.5 RF Flange WN A105 CL600 ASME B16.5 RF Flange WN A105 CL600 ASME B16.5 RF Flange WN A105 CL600 Standard Dwg RF Flange WN A105 CL600 ASME B16.5 RF Flange WN A105 CL600 ASME B16.47-B RF Flange WN A105 CL1500 ASME B16.5 RF Flange WN A105 CL1500 ASME B16.5 RF Blind Flange A105 CL600 ASME B16.5 RF Spiral Wound Gasket SS316 Winding / Graphite Filler CL600 ASME B16.20 FLG B16.5 RF OR CS IR SS316 4.5mm-T Spiral Wound Gasket SS316 Winding / Graphite Filler CL600 Standard Dwg FLG SP-DSN RF OR CS IR SS316 4.5mm-T Spiral Wound Gasket SS316 Winding / Graphite Filler CL600 ASME B16.20 FLG B16.5 RF OR CS IR SS316 4.5mm-T Spiral Wound Gasket SS316 Winding / Graphite Filler CL600 ASME B16.20 FLG B16.47-B RF OR CS IR SS316 4.5mm-T Spiral Wound Gasket SS316 Winding / Graphite Filler CL1500 ASME B16.20 FLG B16.5 RF OR CS IR SS316 4.5mm-T Bolt and Nut A193-B7 / A194-2H ASME B1.1 UNC with Two Heavy HEX Nuts Stud Bolt and Nut A193-B7 / A194-2H ASME B1.1 8UN with Two Heavy HEX Nuts Stud Bolt and Nut A193-B7 / A194-2H ASME B1.1 8UN with Two Heavy HEX Nuts Stud Gate-V A105 CL800 API 602 SW Trim No. 8 BB-BG-OS&Y Handwheel Gate-V A216-WCB CL600 API 600 FLG B16.5 RF Trim No. 8 BB-BG-OS&Y Handwheel Gate-V A216-WCB CL600 API 600 FLG B16.5 RF Trim No. 8 BB-BG-OS&Y Gear Operated Gate-V A216-WCB CL600 API 600 FLG B16.47-B RF Trim No. 8 BB-BG-OS&Y Gear Operated Gate-V A105 CL800 API 602 SW - NPT Trim No. 8 BB-BG-OS&Y Handwheel Globe-V A105 CL800 API 602-Type SW Trim No. 8 BB-BG-OS&Y Handwheel Globe-V A216-WCB CL600 ASME B16.34 FLG B16.5 RF Trim No. 5 BB-BG-OS&Y Handwheel

4

LAMPIRAN F


PIPING CLASS 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S 6CS1S

Short Code GLOBE VALVE (W) CHECK VALVE (X) CHECK VALVE (X) ORIFICE FLANGE (FO) ORIFICE FLANGE (FO) SPECT BLANK/SPACER (SB) SPECT BLANK/SPACER (SB)

Size Size (L/Run) (S/Branch) Wall-T(L) Wall-T(S) Description 6-8 Globe-V A216-WCB CL600 ASME B16.34 FLG B16.5 RF Trim No. 5 BB-BG-OS&Y Gear Operated 0.5-1.5 Check-V A105 CL800 API 602-Type SW Trim No. 8 Lift Type BC 2-24 Dual-PL Check-V A216-WCB CL600 API 594 Lug-type B16.5 RF Trim and Wetted Parts 13Cr Seat STL-6 Spring Inconel 2-10 XS Orfc Flg NPT-Tap WN A105 CL600 Standard Dwg RF S-900-1360-103 0.5" Tap Type 2 with 2 x Jack Screws 12-24 SCH60 Orfc Flg NPT-Tap WN A105 CL600 Standard Dwg RF S-900-1360-103 0.5" Tap Type 2 with 2 x Jack Screws 0.5-8 Spectacle Blank A515-70 CL600 Standard Dwg RF 10-24 Pdl-Blank & Spacer A515-70 CL600 Standard Dwg RF

4

LAMPIRAN F


0,125 0.25 0,375 0,5 0,75 1 1,25 1,5 2 2,5 3 3,5 4 5 6 8 10 12 14 16 18 20 22 24 26 28 30 32 34 36 38 40 42 44 46 48 52 56 60 64 68 72 76 80

Nominal Size

10,3 13,7 17,1 21,3 26,7 33,4 42,2 48,3 60,3 73,0 88,9 101,6 114,3 141,3 168,3 219,1 273,0 323,8 355,6 406,4 457,2 508,0 558,8 609,6 660,4 711,2 762,0 812,8 863,6 914,4 965,2 1016,0 1067,0 1117,6 1168,0 1219,2 1321,0 1422,0 1524,0 1626,0 1727,0 1829,0 1930,0 2032,0

Outside Diameter

P i p e

746,2

18,0 23,4 30,1 38,9 45,0 57,0 68,8 84,7 97,4 110,1 135,8 162,7 213,5 266,2 315,9 347,7 398,0 448,6 498,4 549,4 598,9

749,3

10S

7,8 10,4 13,8 17,1 22,5 27,9 36,7 42,7 54,8 66,9 82,8 95,5 108,2 134,5 161,5 211,6 264,7 314,7 346,0 396,8 447,4 496,9 546,1 597,3

5S

6,8 9,3 12,5 15,8 20,9 26,6 35,1 40,9 52,5 62,7 77,9 90,1 102,2 128,2 154,1 202,7 254,5 304,8

40S 5,5 7,7 10,7 13,8 18,9 24,3 32,5 38,1 49,2 59,0 73,7 85,4 97,2 122,3 146,3 193,7 247,6 298,5

80S

342,9 393,7 444,5 495,2 546,1 597,3 644,6 695,4 746,2 797,0 847,8 898,6

10

I n s i d e d i a m e t e r (ANSI)

206,4 260,4 311,2 339,8 390,6 441,4 489,0 539,7 590,6 634,6 685,6 736,6 787,6 838,6 888,6

20

575,0

777,8 826,6 875,9

679,4 730,2 781,0 831,8 882,6

6,8 9,3 12,5 15,8 20,9 26,6 35,1 40,9 52,5 62,7 77,9 90,1 102,2 128,2 154,1 202,7 254,5 303,2 333,3 381,0 428,7 477,8

205,0 257,6 307,1 336,6 387,4 434,9 482,6 533,4 581,1

30

198,5 247,7 295,3 325,4 373,1 419,1 466,8 514,5 560,8

S c h e d u l e 40 60 5,5 7,7 10,7 13,8 18,9 24,3 32,5 38,1 49,2 59,0 73,7 85,4 97,2 122,3 146,3 193,7 242,9 289,0 317,5 363,5 409,3 455,6 501,8 548,1

N o. 80

188,9 236,5 281,1 308,0 354,0 398,3 442,9 489,1 532,2

100

92,0 115,9 139,7 182,5 230,2 273,1 300,0 344,4 387,4 431,8 476,4 518,0

120

177,8 222,3 266,7 292,0 333,3 377,7 419,1 463,7 505,3

140

11,8 15,5 20,7 29,5 34,0 42,8 54,0 66,6 87,3 109,6 131,8 173,1 215,9 257,3 284,1 325,4 366,8 408,0 451,0 490,9

160 6,8 9,3 12,5 15,8 20,9 26,6 35,1 40,9 52,5 62,7 77,9 90,1 102,2 128,2 154,1 202,7 254,5 304,8 336,6 387,4 438,2 489,0 539,7 590,6 641,4 692,2 743,0 793,8 844,6 895,4 945,9 996,9 1047,9 1098,9 1148,9 1199,9

STD 5,5 7,7 10,7 13,9 18,9 24,3 32,5 38,1 49,2 59,0 73,7 85,4 97,2 122,3 146,3 193,7 247,7 298,5 330,2 381,0 431,8 482,6 533,4 584,6 634,6 685,6 736,6 787,6 838,6 888,6 939,6 990,6 1041,6 1092,6 1142,6 1193,6

XS

Unit :[mm]

80,1 103,2 124,4 174,6 222,3 273,1

6,4 11,0 15,2 22,8 27,9 38,2 45,0 58,4

XXS

635,0 685,8 736,6 787,4 838,2 889,0

XS20

LAMPIRAN-F2


Luas Area Faktor gesekan Bilangan Reynold Drop-tekanan/ 100m Kecepatan fluida

Tekanan operasi Temperatur desain (maksimum) Temperatur operasi NPS pipa Tebal dinding Pipa Sch Tebal dinding Pipa Diameter Luar Pipa Diameter Dalam Pipa

Material pipa Modulus Elastisitas Dingin Modulus Elastisitas Panas Modulus borongan (bulk ) Tekanan desain (maksimum)

Fase fluida Temperatur Tekanan mutlak Flow rate (massa) Flow rate Berat molekul Massa Jenis Viskositet Dinamik

Stream No

v

A=(PI()*Din^2)/4 f Re

t Dext Din

t

Pope Tdes Tope

Ec Eh K @80°C Pdes

Kg/m3

ρ μ

kg/cm2/100m m/det

mm mm mm 2 mm

°C °C Inch STD (Sch.40)

Kg/cm2 G

Carbon Mpa Mpa N/m2 Kg/cm2 G

c.P (Centi Poise)

°C Kg/cm2 A Kg/jam m3/jam

T P W Q

Unit

13 13 22

14 16

26 32 32

29 31b 21

40 38 40 32

LAMP-F2

LAMP-F1

1 1

3 9

19 22 21

Rujukan Pers hal

246459,23 0,03 2307,38 2,8548E-08 1,00

60,00 148,00 120,00 24 17,48 60 24,61 609,4 560,18 48168,88 0,04 5219,24 1,89196E-06 5,12

60,00 148,00 120,00 10 9,27 XS 12,7 273,05 247,65 29461,81 0,03 6673,61 6,05151E-06 8,37

60,00 148,00 120,00 8 8,18 XS 12,7 219,08 193,68

1 2 Data Proses (Process Data ) Cair Cair 120,3 120,3 2 56 836,9 836,9 887,6 885,1 18 18 942,8 942,8 0,229 0,229 Data Perpipaan (Piping Data ) A106 Gr. B A106 Gr. B 203469,21 203469,21 203469,21 196972,71 196972,71 196972,71 2170000000 2170000000 2170000000 78,00 78,00 78,00 120,3 3,5 216,8 230 18 942,8 0,229

Cair 120,3 56 96,7 102,3 18 942,8 0,229

Cair

5

120,3 56 96,7 102,3 18 942,8 0,229

Cair

6

120,3 56 96,7 102,3 18 942,8 0,229

Cair

7

120,3 56 546,7 578,2 18 942,8 0,229

29461,81 0,04 1729,16 4,31978E-07 2,17

60,00 148,00 120,00 8 8,18 XS 12,7 219,08 193,68 48168,88 0,05 1352,33 1,61602E-07 1,33

60,00 148,00 120,00 10 9,27 XS 12,7 273,05 247,65

109318,54 0,16 400,31 1,39917E-08 0,26

60,00 148,00 120,00 16 12,7 60 16,66 406,4 373,08

109318,54 0,16 400,31 1,39917E-08 0,26

60,00 148,00 120,00 16 12,7 60 16,66 406,4 373,08

109318,54 0,16 400,31 1,39917E-08 0,26

60,00 148,00 120,00 16 12,7 60 16,66 406,4 373,08

109318,54 0,03 2263,18 9,24903E-08 1,47

60,00 148,00 120,00 16 12,7 60 16,66 406,4 373,08

A106 Gr. B A106 Gr. B A106 Gr. B A106 Gr. B A106 Gr. B 203469,21 203469,21 203469,21 203469,21 203469,21 203469,21 196972,71 196972,71 196972,71 196972,71 196972,71 196972,71 2170000000 2170000000 2170000000 2170000000 2170000000 2170000000 78,00 78,00 78,00 78,00 78,00 78,00

Cair

Gambar 61 Diagram Alir BFW 3 4

LAMPIRAN-F3



Hitung manual dan Spectrum/ input force "F " (close Time history system) Spectrum/ Hitung manual dan Time history input force "F "

Spectrum/ Hitung manual dan Time history input force "F "

Pembukaan katup secara mendadak dapat menyebabkan aliran fluida transien dan ketidaksetimbangan momentum (gaya) pada selang waktu tertentu

Buka-tutup katup secara mendadak atau sangat lambat dapat menyebabkan aliran fluida transien sehingga timbul ketidaksetimbangan momentum (gaya) Aliran dua fasa atau lebih bisa menyebabkan kompresibilas fluida yang menyimpan energi sampai waktu tertentu untuk kemudian akan dibebaskan dalam bentuk gaya terhadap pipa

Hammering/ Surge

Slug Flow/ flashing

-

PRV

Metoda displacement

Metoda displacement

Umum

Umum

Pseudo static

Perubahan penampang mendadak kecil akan menyebabkan kecepatan sangat ting bisa melebihi kecepatan suara (bunyi) dan drop pressure yg besar bisa menyebabkan kavitasi

Harmonic

Spectrum

Spectrum

Analisa Dinamik

Getaran Akustik (vortex, flow meter, orrifice , katup)

Sistem perpipaan berisolasi dengan frekuensi mesin

Pembebanan pada tahap desain dilakukan secara statik, besarnya gaya tergantung zona area kilang dan dimasukan dalam case "u-seismics "

Pembebanan normal diluar pengaruh vortex shedding biasanya pada tahap desain dilakukan secara statik, besarnya gaya tergantung ketinggian dan dimasukan dalam case "WIND-forces "

Deskripsi

Gerakkan pompa/ kompressor menyebabkan pulsasi dan turbulensi pada fluida dan eksitasi dari fluida tersebut berisolasi dengan pipa

Profil beban - waktu

Pulsasi dari pompa/ kompressor reciprocating

Eksitasi dari mesin

Gempa (seismic, earth quake )

Angin

Jenis beban

Catatan: Modal analysis selalu dilakukan untuk mencari frekuensi pribadi sistem perpipaan

Impulse

Harmonik

Random

Profil

Besar beban merayap naik dari nol ke harga tertentu kemudian relatif konstan dan turun kembali ke titik nol

Arah dan atau besar beban mengikuti profil sinusoidal

Perubahan arah beban dan atau besarnya tidak dapat diperkirakan terhadap waktu, meskipun masih memungkinkan sebagian besar dominan terhadap profil beban yang telah dipelajari/ survey

Keterangan

LAMPIRAN G1

LAMPIRAN-G3


LAMPIRAN-G3


LAMPIRAN-G3


LAMPIRAN-G3


J1

J3

P1 Q=253 m3/hr V=0,27 meters/sec P In=1,2 kg/cm2 (g) P Out=2,3 kg/cm2 (g) Pv Min=0,99 kg/cm2 (g) Re=6,3E+05 L=50 meters D=23 inches a=1.262 meters/sec

P1

P7

J2 P3

P6

P2 Q=253 m3/hr V=1,4 meters/sec P In=2,3 kg/cm2 (g) P Out=2,3 kg/cm2 (g) Pv Min=0,99 kg/cm2 (g) Re=1,4E+06 L=1,0 meters D=10 inches a=1.288 meters/sec

P2

AFT Impulse Model C:\AFT Products\AFT Impulse\Yogie\Min Flow BFW2.imp Base Scenario

XJ7

J6

J8 P5

P3 Q=253 m3/hr V=2,2 meters/sec P In=69 kg/cm2 (g) P Out=69 kg/cm2 (g) Pv Min=0,99 kg/cm2 (g) Re=1,8E+06 L=4,0 meters D=8,0 inches a=1.288 meters/sec

P4

J4

P7 Q=0,0 m3/hr V=0,0 meters/sec P In=2,0 kg/cm2 (g) P Out=1,1 kg/cm2 (g) Pv Min=0,99 kg/cm2 (g) Re=0,0E+00 L=75 meters D=8,0 inches a=1.305 meters/sec

P5 Q=253 m3/hr V=0,60 meters/sec P In=8,5 kg/cm2 (g) P Out=2,8 kg/cm2 (g) Pv Min=0,99 kg/cm2 (g) Re=9,3E+05 L=1.000 meters D=15 inches a=1.233 meters/sec

P6 Q=0,0 m3/hr V=0,0 meters/sec P In=69 kg/cm2 (g) P Out=69 kg/cm2 (g) Pv Min=0,99 kg/cm2 (g) Re=0,0E+00 L=10 meters D=8,0 inches a=1.288 meters/sec

P4 Q=253 m3/hr V=2,2 meters/sec P In=69 kg/cm2 (g) P Out=69 kg/cm2 (g) Pv Min=0,99 kg/cm2 (g) Re=1,8E+06 L=2,0 meters D=8,0 inches a=1.288 meters/sec

LAMPIRAN H-1



AFT Impulse Model

(1 of 4)

Pump Summary

***CAUTION*** Transient data did not extend to Stop Time at Junction 7 (BPR). Final data point was used. ***CAUTION*** Transient data did not extend to Stop Time at Junction 8 (ARV). Final data point was used.

Atmospheric Pressure= 1 atm Gravitational Acceleration= 1 g Turbulent Flow Above Reynolds Number= 4000 Laminar Flow Below Reynolds Number= 2300 Total Inflow= 0,07019 m3/sec Total Outflow= 0,07019 m3/sec Maximum Steady-State Pressure is 69,39 kg/cm2 (g) at Junction 2 (BFW Pump (062-P-1001)) Outlet. Minimum Steady-State Pressure is 2,013 kg/cm2 (g) at Junction 7 (BPR) Outlet. Maximum Transient Pressure is 78,37 kg/cm2 (g) at Pipe 6 (Minimum flow in) Station 10. Minimum Transient Pressure is 0,9927 kg/cm2 (g) at Pipe 1 Station 1.

Constant Fluid Property Model Fluid Database: ASME Steam/Water Tables Fluid: ASME '97 Water Temperature= 120 deg. C Pressure= 60 kg/cm2 (g) Density= 945,9741 kg/m3 Viscosity= 0,2335683 centipoise Bulk Modulus= 19640,73 kg/cm2 Vapor Pressure= 2,025971 kg/cm2 Viscosity Model= Newtonian

Pressure/Head Tolerance= 0,00001 relative change Flow Rate Tolerance= 0,00001 relative change Flow Relaxation= (Automatic) Pressure Relaxation= (Automatic)

Transient Execution Time= 0,00 seconds Model Start Time= 0 seconds Model Stop Time= 15 seconds Time Step Size= 7,766659E-04 seconds Total Number of Time Steps= 19313 Transient Cavitation Model= Discrete Vapor Cavity Model Artificial Transient Criteria= 0,5% Artificial Transient Criteria Minimum Flow= 0 m3/sec Time Step Output Written to File= 1

Steady-State Execution Time= 2,92 seconds Total Number Of Head/Pressure Iterations= 0 Total Number Of Flow Iterations= 53 Number Of Pipes= 7 Number Of Junctions= 7 Matrix Method= Gaussian Elimination

Title: AFT Impulse Model Analysis run on: 25/08/2011 23:58:18 Application version: AFT Impulse Version 3.0 (2005.02.03) Input File: C:\AFT Products\AFT Impulse\Yogie\Min Flow BFW2.imp Output File: C:\AFT Products\AFT Impulse\Yogie\Min Flow BFW2_1.out

AFT Impulse 3.0 Output Home

26/08/2011

LAMPIRAN H-2

BPR ARV

X7 8

PSV REGULAR

Vol. Flow (m3/sec) 0,00000 0,07019

Mass Flow (kg/sec) 0,00 66,40

DH (meters) N/A 643,1

DP (kg/cm2) N/A 60,84

P Inlet (kg/cm2 (g)) 69,12 69,28

Control Valve Junction 7 (BPR) regained control at Time: 0 seconds Control Valve Junction 7 (BPR) lost control and failed open at Time: 7,766659E-04 seconds Valve Junction 8 (ARV) first event started at Time: 1,009666E-02 seconds

N/A 36,80

Cv

0 2.667

K


Vapor Pressure Min (kg/cm2 (g)) 0,9927 0,9927 0,9927 0,9927

P Stag. P Stag. Out In (kg/cm2 (g)) (kg/cm2 (g)) 2,296 1,161 2,294 2,293 69,412 69,311 69,311 69,308

Pipe

1 2 3 4

1 2 3 4 5 6 7

(meters/sec) 0,2706 1,3797 2,1747 2,1747 0,5956 0,0000 0,0000

Velocity

Vol. Flow (m3/hr) 252,7 Pipe Suction Pump 252,7 Discharge Pump 252,7 Upstream ARV 252,7 Downstream ARV 252,7 Minimum flow in 0,0 Minimum flow out 0,0

Name

Pipe

Pipe Output Table P Static P Static Min Max (kg/cm2 (g)) (kg/cm2 (g)) 1,161 2,296 2,284 2,284 69,389 69,288 69,288 69,285 8,463 2,836 69,311 69,122 2,013 1,067

Elevation Inlet (meters) 12,000 0,000 0,000 1,000 1,000 1,000 3,000

Elevation Outlet (meters) 0,000 0,000 1,000 1,000 0,000 3,000 13,000

Closed By User Open

dP Stag. Total (kg/cm2) -1,1348281 0,0005115 0,1011687 0,0032822 5,6268129 0,1892087 0,9460436

dP Gravity (kg/cm2) -1,13525 0,00000 0,09460 0,00000 -0,09460 0,18921 0,94604

NPSHA % of BEP (Percent) (meters) 13,75 0,02340

dP Static Total (kg/cm2) -1,1348281 0,0005115 0,1011687 0,0032822 5,6268129 0,1892087 0,9460436

(m3/sec) 300,0

BEP

Valve State

0 Control Valve Junction 7 (BPR) regained control at Time: 0 seconds 7,766659E-04 Control Valve Junction 7 (BPR) lost control and failed open at Time: 7,766659E-04 seconds 1,009666E-02 Valve Junction 8 (ARV) first event started at Time: 1,009666E-02 seconds

*** Events Sorted By Time ***

AFT Impulse Model

(2 of 4)

Overall Speed Overall DH DP Mass Vol. Power Efficiency Flow Flow (kW) (m3/sec) (kg/sec) (kg/cm2) (meters) (Percent) (Percent) 461,7 100,0 100,0 709,5 67,12 66,40 0,07019

*** Events Sorted By Jct Number ***

Name

Jct

Valve Type

BFW Pump (062-P-1001)

2

Valve Summary

Name

Jct


P Static P Static Out In (kg/cm2 (g)) (kg/cm2 (g)) (meters) 2,296 1,161 0,004484 0,005407 2,284 2,284 0,069387 69,389 69,288 0,034693 69,288 69,285 60,477312 8,463 2,836 0,000000 69,311 69,122 0,000000 2,013 1,067 dH

(meters) N/A

NPSHR

26/08/2011

LAMPIRAN H-2

P Stag. P Stag. Out In (kg/cm2 (g)) (kg/cm2 (g)) 2,838 8,465 69,311 69,122 2,013 1,067

Vapor Pressure Min (kg/cm2 (g)) 0,9927 0,9927 0,9927


1 2 3

Pipe

Max. Mass Max. Mass Flowrate Flowrate Station Time (seconds) 8 0,2897 0,2547 1 0,2050 0

Pipe Transient Max/Min Results Max. Stag. Pipe Max. Stag. Pressure Pressure (kg/cm2 (g)) Time (seconds) 0,5763 1 5,915 2 10,684 0,2563 3 77,856 0,2540 4 77,832 0,2579 5 8,674 0,2206 6 78,395 0,2672 7 25,089 0,1126

Min. Mass Max. Volumetric Max. Volumetric Max. Volumetric Min. Volumetric Min. Volumetric Min. Volumetric Min. Mass Flowrate Flowrate Flowrate Flowrate Flowrate Flowrate Flowrate Flowrate Station Time (seconds) (m3/hr) Station Time (seconds) (m3/hr) Station Time (seconds) 19 0,6027 185,304447 8 0,2897 813,2 19 0,6027 0,1328 0 699,9 0,2547 1 0,000000 0,1328 0 0,01087 0 592,6 0,2050 0 252,679322 0,01087 0

Station 51 0 4 2 0 10 0 Time (seconds) 0,5305 0,3371 0,01165 0,01010 7,695 0,01553 1,743 (meters) 10,50 10,58 546,12 518,44 21,24 535,31 13,60 Station 51 1 4 2 0 10 0 Time (seconds) 0,5763 0,2563 0,2594 0,2579 0,2206 0,2672 0,1126

Max. Mass Flowrate (kg/sec) 213,70 183,90 155,71 70,15 68,85 87,38 110,96

Min. Mass Flowrate (kg/sec) 48,6925618 0,0000000 66,3966978

Min. EGL Min. EGL Min. EGL Max. EGL Max. EGL

26/08/2011

Min. Stag. Min. Stag. Pressure Pressure (kg/cm2 (g)) Time (seconds) 0,6027 0,9929 1,0011 0,3371 51,5705 0,01165 48,9519 0,01010 1,9147 7,695 50,3593 0,01553 0,9964 1,741

Min. Stag. Max. EGL Pressure (meters) Station 62,52 19 0 112,93 4 823,44 2 823,71 0 92,69 10 831,66 4 268,20

AFT Impulse Model

(3 of 4)

Max. Stag. Pressure Station 51 1 1 2 0 10 0

Pipe Transient Results (Currently Displayed Only) Step: 0 Stag. EGL Mass Volumetric Time: 0,00000E+00 Pressure Flowrate Flowrate Pipe -- Station (kg/cm2 (g)) (meters) (kg/sec) (m3/hr) 1 -- 0 1,161 24,28 66,40 252,7 1 -- 51 2,296 24,27 66,40 252,7 2 -- 0 2,294 24,24 66,40 252,7 2 -- 1 2,293 24,24 66,40 252,7 3 -- 0 69,412 733,71 66,40 252,7 3 -- 4 69,311 733,64 66,40 252,7 4 -- 0 69,311 733,64 66,40 252,7 4 -- 2 69,308 733,61 66,40 252,7 5 -- 0 8,465 90,48 66,40 252,7 5 -- 1044 2,838 30,00 66,40 252,7 6 -- 0 69,311 733,64 0,00 0,0 6 -- 10 69,122 733,64 0,00 0,0 7 -- 0 2,013 24,28 0,00 0,0 7 -- 74 1,067 24,28 0,00 0,0

5 6 7

Pipe


LAMPIRAN H-2

1 2 3 4 6 X7 8

AFT Impulse Model

(4 of 4)

26/08/2011

P Static Out (kg/cm2 (g)) N/A 69,389 2,284 2,838 69,301 2,013 8,463

P Stag. P Stag. In Out (kg/cm2 (g)) (kg/cm2 (g)) 1,067 N/A 2,293 69,412 2,296 2,294 0,000 2,838 69,311 69,311 69,122 2,013 69,308 8,465

Vol. Flow Into System (m3/hr) 252,7 0,0 0,0 -252,7 0,0 0,0 0,0

Mass Flow Loss Into System Factor (K) (kg/sec) 66,40 0,000 0,00 0,000 0,00 7,386 -66,40 0,000 0,00 0,000 0,00 0,000 0,00 2.667,114

Min. Mass Max. Volumetric Max. Volumetric Max. Volumetric Min. Volumetric Min. Volumetric Min. Volumetric Min. Mass Flowrate Flowrate Flowrate Flowrate Flowrate Flowrate Flowrate Flowrate Station Time (seconds) (m3/hr) Station Time (seconds) (m3/hr) Station Time (seconds) 0 9,321 -0,263504 0 0,2151 267,0 0 9,321 8,825 1044 262,0 0,2206 0 -28,527222 8,825 1044 7,767E-03 0 332,5 0,2066 0 -0,001198 7,767E-03 0 0,000 0 422,3 0,1701 74 0,000000 0,000 0

P Static In (kg/cm2 (g)) 1,067 2,284 2,296 0,000 69,301 69,122 69,285

Min. Mass Flowrate (kg/sec) -0,0692410 -7,4961152 -0,0003148 0,0000000

Daerator (062-D-1001) BFW Pump (062-P-1001) Area Change BOILER-HRSG-DESUPERHEATER Branch BPR ARV

Name

Max. Mass Max. Mass Flowrate Flowrate Station Time (seconds) 0 0,2151 0,2206 0 0,2066 0 0,1701 74

All Junction Table Jct

4 5 6 7

Pipe


LAMPIRAN H-2


Pressure Static (kg/cm2 (g))


0

20

40

60

80

0

5

Time (seconds)

10

Pressure Static vs. Time

15

Pipe 7, Station 74 (Outlet)

Pipe 7, Station 0 (Inlet)


LAMPIRAN H-3

Pressure Static (kg/cm2 (g))

0

20

40

60

80

0

5

Time (seconds)

10

Pressure Static vs. Time

15



LAMPIRAN H-4


Volumetric Flowrate Upstream (m3/hr)

-100

0

100

200

300

400

500

600

0

Time (seconds)

5

10

Volumetric Flowrate Upstream vs. Time

15




LAMPIRAN H-5


CASE 33

3.4414 Hz.

printed: 08/26/11 13:53:44

LAMPIRAN I-1


model: C:\DOCUMENTS AND SETTINGS\YOGIE.MARADO...\C000-211-TOC-1 MODAL

CASE 82

8.7213 Hz.

printed: 08/26/11 15:05:44

LAMPIRAN I-2


model: C:\DOCUMENTS AND SETTINGS\YOGIE.MARADO...\C000-211-TOC-1 MODAL

3/29/2011

Surge analysis - Intergraph CADWorx …

Home Page » Forums » Analysis Solutions » CAESAR II » Surge analysis Forum List

My Stuff

Calendar

Active Topics

Welcome yogie4061. [Log out] Search

FAQ

New Reply Topic Options

Search #33839 - 03/23/10 07:57 AM

Surge analysis G.SARAVANAN Member Registered: 07/21/07 Posts: 19 Loc: Tamilnadu,India

Dear Sir, Is it possible to do the surge analysis. If yes, try to explain (or any attachment pls send)this.

Go Advanced Who's Online

Reply

Top

Quote

Quick Reply

Quick Quote

Notify

Email Post

#33842 - 03/23/10 08:01 AM

Re: Surge analysis [Re: G.SARAVANAN]

0 registered (), 4 Guests and 2 Spiders online. Key: Admin, Global Mod, Mod

March

Richard Ay Member Registered: 12/13/99 Posts: 3739 Loc: Houston, Texas, USA

You cannot perform a surge analysis with CAESAR II. You need a fluid hydraulic program, such as:

Su M Tu W Th F Sa 6

- Sunrise Systems "PipeNet" - Paulin Research Group "Boss Fluids"

7

1

2

3

4

5

8

9 10 11 12

13 14 15 16 17 18 19 20 21 22 23 24 25 26

There are other fluids programs also.

27 28 29 30 31

_________________________ Regards, Richard Ay Intergraph CAS

Forum Stats 7132 Members 12 Forums 8730 Topics 40295 Posts Max Online: 57 @

12/06/09 11:14 AM Top

Reply

Quote

Quick Reply

Quick Quote

Notify

Email Post

Search Results Quick Reply: HTML is enabled UBBC ode is enabled Add Signature


65.57.255.42/…/ubbthreads.php?ubb…

LAMPIRAN I-3

1/2

DAFTAR PUSTAKA

Recommend Documents