38
115 DAFTAR PUSTAKA 1. Schmit K., “Fiberglass Reinforced Plastics (FRP) Piping System Designing Process/Facilities Piping System with FRP A Comparison to Traditional Metallic Materials”, EDO Specialty Plastics, Baton Rouge, May 29 th , 1998. 2. Norman Yanuar, “Perancangan Pipa Penyalur Bawah Laut Menggunakan Material Komposit GRP”, Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. William D. Callister, Jr., “Materials Science and Engineering an Introduction”, Sixth edition, John Wiley & Sons, Inc., USA, 2003. 4. Michael F. Ashby, “Materials Selection in Mechanical Design”, Third edition, Elsevier Butterworth Hienemann, 2005. 5. Dr. Ir. Bambang Kismono Hadi, “Mekanika Struktur Komposit”, Penerbit ITB, Bandung, 2000. 6. Isaac M. Daniel, and Ori Ishai, Engineering Mechanics of Composite Materials, Oxford University Press, New York, 1994. 7. Robert M. Jones, Mechanics of Composite Materials, Hemisphere Publishing Corporation, New York, 1975. 8. ISO 14692, “Petroleum and Natural Gas Industries – Glass-reinforced Plastics (GRP) Piping”, 2002. 9. Bulletin No. C3030, “Time-tested Fiberglass Piping Systems from Smith Fibercast”, www.fibersmithfibercast.com , Desember 1 st , 2004. 10. Sam Kannappan, P.E., “Introduction to Pipe Stress Analysis”, John Wiley & Sons, Inc., Canada, 1986. 11. API Specification 15HR, “Specification for High Pressure Fiberglass Line Pipe”, Third edition, 2001. 12. http://www.acipco.com/adip/pipe/ , Long Span and Piping Supports. 13. http://www.kuleuven.ac.be , Lecture 6: Elastic Instability Modes. 14. API RP 1102, “Pipes Crossing Railroads and Highways”, July 2002. 15. Manual No. E5000, “Engineering & Piping Design Guide – Smith Fibercast”, October 15 th , 2003. 16. COADE Software Engineer, “CAESAR II version 4.50 Aplications Guide”, January 2003.

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Page 1: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

115

DAFTAR PUSTAKA

1. Schmit K., “Fiberglass Reinforced Plastics (FRP) Piping System Designing Process/Facilities Piping System with FRP A Comparison to Traditional Metallic Materials”, EDO Specialty Plastics, Baton Rouge, May 29th, 1998.

2. Norman Yanuar, “Perancangan Pipa Penyalur Bawah Laut Menggunakan Material Komposit GRP”, Tugas Sarjana, Teknik Mesin FTI ITB, 2006.

3. William D. Callister, Jr., “Materials Science and Engineering an Introduction”, Sixth edition, John Wiley & Sons, Inc., USA, 2003.

4. Michael F. Ashby, “Materials Selection in Mechanical Design”, Third edition, Elsevier Butterworth Hienemann, 2005.

5. Dr. Ir. Bambang Kismono Hadi, “Mekanika Struktur Komposit”, Penerbit ITB, Bandung, 2000.

6. Isaac M. Daniel, and Ori Ishai, Engineering Mechanics of Composite Materials, Oxford University Press, New York, 1994.

7. Robert M. Jones, Mechanics of Composite Materials, Hemisphere Publishing Corporation, New York, 1975.

8. ISO 14692, “Petroleum and Natural Gas Industries – Glass-reinforced Plastics (GRP) Piping”, 2002.

9. Bulletin No. C3030, “Time-tested Fiberglass Piping Systems from Smith Fibercast”, www.fibersmithfibercast.com, Desember 1st, 2004.

10. Sam Kannappan, P.E., “Introduction to Pipe Stress Analysis”, John Wiley & Sons, Inc., Canada, 1986.

11. API Specification 15HR, “Specification for High Pressure Fiberglass Line Pipe”, Third edition, 2001.

12. http://www.acipco.com/adip/pipe/, Long Span and Piping Supports.

13. http://www.kuleuven.ac.be, Lecture 6: Elastic Instability Modes.

14. API RP 1102, “Pipes Crossing Railroads and Highways”, July 2002.

15. Manual No. E5000, “Engineering & Piping Design Guide – Smith Fibercast”, October 15th, 2003.

16. COADE Software Engineer, “CAESAR II version 4.50 Aplications Guide”, January 2003.

Page 2: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

116

17. FEED Fasilitas Produksi Proyek Pengembangan Pondok Tengah, PT. Singgar Mulia, 2007.

18. American Lifelines Aliance, “Guideline for the Design of Buried Stell Pipe”, July 2001.

Page 3: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

LAMPIRAN A

Contoh Perhitungan Analisis Statik Span Menggunakan

MathCAD 2000

Page 4: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

Densitas medium c 856.2kg

m3

Densitas pipa p 1930kg

m3

t 6.2 10 3 m

tOD ID( )

2Tebal dinding pipa

D 0.203 m

DOD ID( )

2Diameter rata-rata pipa

ID 196.6mmDiameter dalam pipa

OD 209mmDiameter luar pipa

STAR FRP SERIES 800 API-15 HR ACTSeri pipa

DATA PIPA

Pe 1atmTekanan Eksternal

Percepatan Gravitasi g 9.807m

s2

DATA LINGKUNGAN

Tmax 60CTemperatur perancangan maximum

Ti 21.1CTemperatur instalasi

Pd 4.14 106PaTekanan dalam

DATA OPERASI

8" crude pipeline

KONDISI OPERASIANALISIS STATIK SPAN

Page 5: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

A2 1Faktor parsial untuk resistansi kimia

A1 1Faktor parsial untuk temperatur

Ip 2.033 10 5 m4

Ip64

OD4 ID4Inersia polar pipa

TIDAK ADA BEBAN THERMAL

BERDASARKAN TEGANGAN AKSIAL YANG DIPERBOLEHKAN(ISO 14692)

PERHITUNGAN PANJANG SPAN STATIK

o 33.382kgm

o effID2

4Kombinasi massa linear pipa + fluida(ISO 14692)

eff 1.1 103 kg

m3

eff c 4p tID

Densitas kombinasi efektif pipa + fluida(ISO 14692)

A 3.95 10 3 m2

A4

OD2 ID2Luas penampang pipa

PERHITUNGAN BERAT PIPA

r 0.45Rasio kekuatan biaxial

qs 140.2 106PaTegangan tarik axial maksimum pipa

v 0.39Poisson's Ratio (Minor)

Eh 22.8 109PaModulus Elastisitas Hoop

Ea 13.8 109PaModulus Elastisitas Axial

Page 6: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

Sat Ea Teff

Teff 33.065 C

Teff 0.85 Tmax Ti( )

15.7 10 6mmmm

CTegangan aksial akibat ekspansi termal

Sl 3.303 107 Pa

SlPd Pe( ) D

4 tTegangan aksial akibat tekanan dalam

Sh 6.605 107 Pa

ShPd Pe( ) D

2 tTegangan hoop akibat tekan dalam

A3 1Faktor parsial untuk beban siklik

A2 1Faktor parsial untuk resistansi kimia

A1 1Faktor parsial untuk temperatur

ADA BEBAN THERMAL

Ls 1.152 m

Ls root 0.67 A1 A2 A3 1 r( )Sh2

r qs2

Slo 9.81 La2 OD

16 IpLa

Panjang span statik maksimum pipa

La 0mPendefenisian awal

Sl 3.303 107 Pa

SlPd Pe( ) D

4 tTegangan aksial akibat tekanan dalam

Sh 6.605 107 Pa

ShPd Pe( ) D

2 tTegangan hoop akibat tekan dalam

A3 1Faktor parsial untuk beban siklik

Page 7: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

Faxial Fat FapGaya tekan aksial total

Fap 7.059 104 N

Fap A Ea pGaya tekan aksial akibat ekspansitekanan

p 1.295 10 3

p1

2 Eav

Eh

Pd

OD ID( )2

2t

Ekspansi pipa akibat tekanan dalam

Fat 2.83 104 N

Fat A Ea TeffGaya tekan aksial akibat ekspansi

Teff 33.065 C

Teff 0.85 Tmax Ti( )Perubahan temperatur efektif

15.7 10 6mmmm

CKoofisien ekspansi termal

BERDASARKAN EULER BUCKLING(ISO 14692)

Lst 2.254 m

Lst root 0.83 A1 A2 A3 1 r( )Sh2

r qs2

SLo 9.81 La2 OD

16 IpLa

Panjang span statik maksimum pipa

La 0mPendefinisian awal

SL 4.019 107 Pa

SL Sl SatTegangan aksial total akibattekanan dalam+ekspansi termal

Sat 7.164 106 Pa

Page 8: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

Lsmax 1.152 mJadi span maksimum yang diperbolehkan

Lsmax min Span( )

Span

Ls

Lst

Lse

Lse 3.053 mBerdasarkan euler buckling

Lst 2.254 mAda Beban termal (f2=0.83)

Ls 1.152 mTidak ada beban termal (f2=0.67)

Berdasarkan tegangan aksial yang diperbolehkan

Span Statik

PENENTUAN PANJANG SPAN MAKSIMUM YANG DIPERBOLEHKAN

Lse 3.053 m

Lse3 D3 t

3 8 FaxialEaPanjang span statik maksimum pipa

Faxial 9.889 104 N

Page 9: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

LAMPIRAN B

Contoh Perhitungan Kedalaman Kubur Maksimum

Menggunakan MathCAD 2000

Page 10: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

Diameter luar pipa OD 0.209m

Diameter dalam pipa ID 0.1966m

Diameter rata-rata pipa DOD ID( )

2D 0.203 m

Tebal dinding pipa tOD ID( )

2

t 6.2 10 3 m

p 1930kg

m3Densitas pipa

c 856.2kg

m3Densitas medium

Modulus Elastisitas Axial Ea 13.8 109Pa

Modulus Elastisitas Hoop Eh 22.8 109Pa

ANALISIS BURIALKONDISI OPERASI8" crude pipeline

DATA OPERASI

Tekanan dalam Pd 4.14 106Pa

Temperatur instalasi Ti 24C

Temperatur perancangan maximum Tmax 65C

DATA LINGKUNGAN

g 9.807m

s2Percepatan Gravitasi

Tekanan Eksternal Pe 1atm

DATA PIPA

Seri pipa STAR FRP SERIES 800 API-15 HR ACT

Page 11: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

A2 1Faktor parsial untuk resistansi kimia

A1 1Faktor parsial untuk temperatur

PERHITUNGAN TEGANGAN ARAH HOOP MAKSIMUM

Kz 0.108Parameter defleksi (open trench)

Kb 0.235Parameter bending (open trench)

(Jenis tanah : sand & gravel)

1500kg

m3Berat jenis tanah

DATA KONDISI LINGKUNGAN

o 33.382kgm

o effID2

4Kombinasi massa linear pipa + fluida(ISO 14692)

eff 1.1 103 kg

m3

eff c 4p tID

Densitas kombinasi efektif pipa + fluida(ISO 14692)

A 3.95 10 3 m2

A4

OD2 ID2Luas penampang pipa

PERHITUNGAN BERAT PIPA

qs 140.2 106PaTegangan tarik axial maksimum pipa

r 0.45Rasio kekuatan biaxial

v 0.39Poisson's Ratio (Minor)

Page 12: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

PEHITUNGAN TEGANGAN KEDALAMAN KUBUR RANCANG

hmaks 10.27 m

hmaks root hsum h ht6 Kb g h OD

OD2

Eh t

Eh t3 24 Kz Pd Pe( )OD2

3h

h 0m

PERHITUNGAN KEDALAMAN KUBUR MAKSIMUM

ht 1.247 107 Pa

ht Eh Teff

Teff 34.85 C

Teff 0.85 Tmax Ti( )

15.7 10 6mmmm

CTegangan aksial akibat ekspansi termal

PERHITUNGAN TEGANGAN ARAH HOOP AKIBAT EKSPANSI TERMAL

h 6.605 107 Pa

hPd Pe( ) D

2tTegangan arah hoop akibat tekanan dalam

PERHITUNGAN TEGANGAN ARAH HOOP AKIBAT TEKANAN DALAM

hsum 1.164 108 Pa

hsum 0.83 A1 A2 A3 qsTegangan arah hoop maksimum

A3 1Faktor parsial untuk beban siklik

Page 13: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

hd 1.2mkedalaman kubur rancang

Status status if hmaks hd "OK" "NOT OK"( )

status "OK"

Tegangan hoop total yang terjadi pada pipa yang dikubur dengan kedalaman rancang b

6 Kb g hd ODOD2

Eh t

Eh t3 24 Kz Pd Pe( )OD2

3

d h ht b

d 8.295 107 Pa

Safety Factor SFhsum

d

SF 1.403

Page 14: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

LAMPIRAN C

Contoh Calculation Sheet Analisis Casing Pada Road Crossing

Menggunakan Microsoft Excel 2007

Page 15: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

1

2

3 W = Load Case, (lbs)

4 H = Depth, (ft)

5 D = Outside diameter, (in.)

6 Bd = Bored diameter, (in.)

7

8

9

10

11

12

13

14 Pipe Properties : Critical Case : Tandem Axles

15 - Outside Diameter, D (in.) : Design wheel load, Pt (lbs) : = ton

16 - Design factor, F : Contact area of wheel, Ap (in.²) :

17 - Wall thichness, tw (in.) : Depth, H (ft) : = m

18 - Material : API 5L Gr. B Bored Diameter, Bd (in.) :

19 - Specified Minimum Yield Strength, SMYS (psi) : Soil type : B

20 - Specified Minimum Tensile Strength, SMTS (psi) : Modulus of soil reaction, E' (ksi) :

21 - Young's Modulus, ES (ksi) : Resilient modulus, Er (ksi) : 10

22 - Unit Weight (lb/ft³) : Soil unit weight (lb/ft³) : = lb/in³

60,000

3.00E+07

490 0.069120

0.188

12.750

35,000

4.00

SKECTH

1440.8

12.75 22,046

DATA

10

Diameter 8"Calculation Sheet Analisis Casing Pipa GRP

1.2

1.0

WROW

H

D

C

w

Bd

22 - Unit Weight, (lb/ft ) : Soil unit weight, (lb/ft ) : = lb/in

23 - Poisson's Ratio, S : Pavement type : No Pavement

24 - Coef. of thermal expansion, T (in./in.°F) :

25 - Operating pressure, p (psi) :

26 - Longitudinal joint factor, E :

27 - Type of longitudinal weld :

28

29 A. Cek Allowable Barlow Stress B. Circumferential Stress Due to Earth Load

30 tw/ D =

31 E' (ksi) =

32

33

34 SHi = psi KHe =

35

36 Allowable Stress, S (psi) : H/ Bd =

37 Soil Type =

38

39 S = psi

40 SHi (Barlow) Allowable Stress OK Be =

41 C. Impact Factor, Fi, dan Applied Design Surface Pressure, w Bd/ D =

42 H = ft

43

44

45 Ee =

46 Fi =

47 Applied design surface pressure, w :

48 Critical case = Tandem Axles

49 Pavement Type = No Pavement

50 Design Wheel Load from Tandem Axles, Pt (ki :

51 Applied Design Surface Pressure, w (psi) : SHe = psi

52

535455

22,046

153.10 379

0.83

1.50

Circumferential stress due to earth load :

1.00

4.00 From Fig.5 - Excavation Factor for Earth Load CircumferentialStress, Ee , API RP 1102 :C Fig. 7 - Recommended Impact Factor Versus

Depth, API RP 1102 :

B

From Fig.4 - Burial Factor for Earth Load Circumferential Stress, Be , API RP 110228,000

0.86

From Fig.3 - Stiffness Factor for Earth Load CircumferentialStress, KHe , API RP 1102 :

0 600

3.76

ERW

0.015

1

0.3

6.50E-06

0

1

490 0.069120

StressAllowableBarlowSHi )(

EFSMYSS

DEBKS eeHeHe

wHi t

pDBarlowS2

)(

Page 16: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

56 D. Cyclic Stresses, SHh dan SLh

57 D.1 Cyclic Circumferential Stress, SHh D.2 Cyclic Longitudinal Stress, SLh

58596061 tw/ D = tw/ D =

62 Er = 10 ksi KHh = Er = ksi KLh =

63646566 D = in. D = in.

67 H = ft GHh = H = ft GLh =

68697071 D = 13 in. R = D = in. R =72 H = ft L = H = ft L =7374 Cyclic circumferential stress due to highway vehicular load : Cyclic longitudinal stress due to highway vehicular load :75

76

77 SHh = psi SLh = psi

78

79 E. Circumferential Stress Due to Internal Pressurization, SHi G. Check Fatigue

1.00 4.00 1.00

2,526 1,975

4.00

From Table 2 - Highway Pavement Type Factors, R, and Axle Configuration Factors, L, API RP 1102:

1.10 12.75 1.10

From Table 2 - Highway Pavement Type Factors, R, and Axle Configuration Factors, L , API RP 1102:

10 6.80

From Fig. 14 - Highway Stiffness Factor for Cyclic Circumferential Stress, KHh , API RP 1102:

From Fig. 16 - Highway Stiffness Factor for Cyclic Longitudinal Stress, KLh , API RP 1102:

8.00

0.014750.01475

1.15

12.750 12.75

4.00

From Fig. 15 - Highway Geometric Factor for Cyclic Circumferential Stress, GHh , API RP 1102:

From Fig. 17 - Highway Geometric Factor for Cyclic Longitudinal Stress, G Lh , API RP 1102:

1.25 4.00

wFLRGKS iHhHhHh wFLRGKS iLhLhLh

79 E. Circumferential Stress Due to Internal Pressurization, SHi G. Check Fatigue

80 G.1 Girth Weld81 Circumferential stress due to internal pressure : F =

82 SLh = psi

8384

85 SHi = psi

86 SFG = psi

87 F. Principical Stresses, S1, S2, S3 SFG x F = psi

88 The girth weld fatigue check is as follows:89 Maximum Circumferential stress , S1 :

90 OK

9192 S1 = psi So, cyclic longitudinal stress from girth weld fatigue.93 Design OK.94 Maximum Longitudinal stress , S2 :

95 G.2 Longitudinal Weld96 F =

97 T1 = temperature at time of installation, °F = 70 SHh = psi

98 T2 = max. operating temperature, °F =99 S2 = psi100

101 Maximum Radial stress , S3 : SFL = psi (For ERW pipe)

102 SFL x F = psi

103104 S3 = psi The longitudinal weld fatigue check is as follows:105

106 Total effective stress, Seff : OK

107108 So, cyclic circumferential stress from longitudinal weld fatigue.109 Design OK.

110 Seff = psi

111 Cek :112113114 Feff = Seff SMYS x F115 Total Effective Stress must be smaller or same with SMYS x F , 116 Then, design is OK.

11,346 28,000

16,800

<

-9,611 Refer to Table 3 - Fatigue Endurance Limits, SFG and SFL , for Various Steel Grades, API RP 1102 , for API 5L Gr.X42 :

11,346

21,000

16,800

0

2,526

2,905 <

0.8

2,526

12,000

9,600

1,975 9,600

0.8

1,975

Refer to Table 3 - Fatigue Endurance Limits, SFG and SFL , for Various Steel Grades, API RP 1102 , for API 5L Gr. B :0

0.80

130

wFLRGKS iHhHhHh wFLRGKS iLhLhLh

w

wHi t

tDpS

2

HiSHSHeSS1

MOPorMAOPpS 3

213

232

2212

1 SSSSSSeffS

FSS FGLh

FSS FLHh

HiHesTsL SSTTESS 122

effFSMYSeffS

Page 17: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

LAMPIRAN D

Contoh Perhitungan Analisis Shell Buckling dan Euler Buckling

Menggunakan MathCAD 2000

Page 18: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

Diameter luar pipa OD 209mm

Diameter dalam pipa ID 196.6mm

Diameter rata-rata pipa DOD ID( )

2D 0.203 m

Tebal dinding pipa tOD ID( )

2

t 6.2 10 3 m

p 1930kg

m3Densitas pipa

c 856.2kg

m3Densitas medium

Modulus Elastisitas Axial Ea 13.8 109Pa

Modulus Elastisitas Hoop Eh 22.8 109Pa

ANALISIS SHELL BUCKLINGKONDISI OPERASI

8" Crude Pipeline

DATA OPERASI

Tekanan dalam Pd 4.14 106Pa

Temperatur instalasi Ti 24C

Temperatur perancangan maximum Tmax 60C

DATA LINGKUNGAN

g 9.807m

s2Percepatan Gravitasi

Tekanan Eksternal Pe 1atm

DATA PIPA

Seri pipa STAR FRP SERIES 800 API-15 HR ACT

Page 19: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

p 1.295 10 3

p1

2 Eav

Eh

Pd

OD ID( )2

2t

Ekspansi pipa akibat tekanan dalam

Ekspansi Tekanan

Fat 2.619 104 N

Fat A Ea TeffGaya tekan aksial akibat ekspansi

Teff 30.6 C

Teff 0.85 Tmax Ti( )Perubahan temperatur efektif

15.7 10 6mmmm

CKoofisien ekspansi termal

Ekspansi Termal

PERHITUNGAN TEGANGAN AKSIAL KOMPRESI(ISO 14692)

o 33.382kgm

o effID2

4Kombinasi massa linear pipa + fluida(ISO 14692)

eff 1.1 103 kg

m3

eff c 4p tID

Densitas kombinasi efektif pipa + fluida(ISO 14692)

A 3.95 10 3 m2

A4

OD2 ID2Luas penampang pipa

PERHITUNGAN BERAT PIPA

r 0.45Rasio kekuatan biaxial

qs 140.2 106PaTegangan tarik axial maksimum pipa

v 0.39Poisson's Ratio (Minor)

Page 20: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

o 1.632

o0.83

0.1 0.005IDt

Konstanta

TEGANGAN MAKSIMUM SHELL BUCKLING(ISO 14692)

at 2.64 107 Pa

at ab aeTegangan kompresi aksial total

ae 2.45 107 Pa

aeFaxial

ATegangan kompresi aksial akibat ekspansi

Tegangan Kompresi Aksial Total

Faxial 9.678 104 N

Faxial Fat FapGaya tekan aksial total

Gaya Kompresi Aksial Total

ab 1.894 106 Pa

ab

o 9.81m

s2Ls2 OD

16 IpTegangan kompresi akibat bending

Ip 2.033 10 5 m4

Ip64

OD4 ID4Inersia polar pipa

Ls 3mPanjang span

Tegangan Kompresi Akibat Bending

Fap 7.059 104 N

Fap A Ea pGaya tekan aksial akibat ekspansitekanan

Page 21: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

0.1887 0.8113 o

1.513

Modulus efektif Eeff Ea Eh( )

Eeff 1.774 1010 Pa

Tegangan maksimum shell buckling usb 0.9Eeff t

D

usb 7.384 108 Pa

SAFETY FACTOR

Safety factor Rasiousbat

Rasio 27.976

Status status if Rasio 3 "OK" "NOT OK"( )

status "OK"

Page 22: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

Diameter luar pipa OD 209mm

Diameter dalam pipa ID 196.6mm

Diameter rata-rata pipa DOD ID( )

2D 0.203 m

Tebal dinding pipa tOD ID( )

2

t 6.2 10 3 m

p 1930kg

m3Densitas pipa

c 856.2kg

m3Densitas medium

Modulus Elastisitas Axial Ea 13.8 109Pa

Modulus Elastisitas Hoop Eh 22.8 109Pa

ANALISIS EULER BUCKLINGKONDISI OPERASI

DATA OPERASI8" Crude Pipeline

Tekanan dalam Pd 4.14 106Pa

Temperatur instalasi Ti 24C

Temperatur perancangan maximum Tmax 60C

DATA LINGKUNGAN

g 9.807m

s2Percepatan Gravitasi

Tekanan Eksternal Pe 1atm

DATA PIPA

Seri pipa STAR FRP SERIES 800 API-15 HR ACT

Page 23: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

p 1.295 10 3

p1

2 Eav

Eh

Pd

OD ID( )2

2t

Ekspansi pipa akibat tekanan dalam

at 6.63 106 Pa

at Ea TeffTegangan tekan aksial akibat ekspansi

Teff 30.6 C

Teff 0.85 Tmax Ti( )Perubahan temperatur efektif

15.7 10 6mmmm

CKoofisien ekspansi termal

EULER BUCKLING

o 33.382kgm

o effID2

4Kombinasi massa linear pipa + fluida(ISO 14692)

eff 1.1 103 kg

m3

eff c 4p tID

Densitas kombinasi efektif pipa + fluida(ISO 14692)

A 3.95 10 3 m2

A4

OD2 ID2Luas penampang pipa

PERHITUNGAN BERAT PIPA

r 0.45Rasio kekuatan biaxial

qs 140.2 106PaTegangan tarik axial maksimum pipa

v 0.39Poisson's Ratio (Minor)

Page 24: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

status "OK"

status if rasio 3 "OK" "NOT OK"( )Status

rasio 21.534

Rasio rasiou

axial

u 5.276 108 Pa

Tegangan buckling ekuivalen uFamax

D t

Famax 2.084 106 N

Famax3 D3 t

8 L2EaGaya aksial maksimum euler buckling

L 1.152mPanjang span statik maksimum pipa

axial 2.45 107 Pa

axial at apTegangan tekan aksial total

ap 1.787 107 Pa

ap Ea pTegangan tekan aksial akibat ekspansitekanan

Page 25: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

LAMPIRAN E

Typical Drawing Sistem Perpipaan

Gambar E.1 Gambar isometrik sistem perpipaan

Gambar E.2 Typical road crossing

Gambar E.3 Typical river crossing

Gambar E.4 Typical trench of pipeline

Page 26: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

Gambar E.1 Gambar isometrik sistem perpipaan

Page 27: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES
Page 28: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

Gambar E.2 Typical road crossing

Page 29: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES
Page 30: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

Gambar E.3 Typical river crossing

Page 31: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES
Page 32: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

Gambar E.4 Typical trench of pipeline

Page 33: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES
Page 34: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

LAMPIRAN F

DATA SPESIFIKASI PRODUK PIPA STAR™ ALIPHATIC

AMINE LINE PIPE

Page 35: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

Pro

du

ct

Descri

pti

on

•P

ressu

re -

Up

to

32

50

psi (

22

,4 M

Pa

)

•R

esin

Syste

m -

Alip

hatic A

min

e C

ure

d E

poxy

•R

ein

forc

em

ent

- P

rem

ium

Fib

erg

lass

•Jo

inin

g S

yste

ms -

AP

I 8

rd

•Jo

int

Le

ng

th -

30

Fe

et

(9,1

Me

ters

) N

om

ina

l

Ra

nd

om

Le

ng

ths o

f 2

0 t

o 3

2 F

ee

t (6

,1 t

o 9

,8 M

ete

rs)

•F

ittings -

A v

ariety

of

fila

ment

wound A

PI

thre

aded f

ittings a

re a

vaila

ble

.

Purc

hase a

ll fittin

gs b

y t

hre

ad s

ize a

nd d

esig

n p

ressure

rating o

nly

.

•Te

mp

era

ture

- U

p t

o 2

00

° F

(9

3.3

° C

) M

axim

um

•S

ize

s -

th

rou

gh

8 in

ch

es

Hig

h P

ressu

re D

esig

n ≥

≥ ≥ ≥ ≥ 500 p

si

•A

PI 1

5H

R D

esig

ned, M

onogra

mm

ed P

roducts

are

indic

ate

d b

y a

check m

ark

()

•Life E

xpecta

ncy -

20 y

ears

at fu

ll ra

ting

•D

esig

n T

em

pera

ture

- 1

50°

F (65.6

° C

)

•W

all

Thic

kness - N

om

inal

•H

oop S

tress - A

vera

ge L

ong T

erm

Hydro

sta

tic S

trength

(LT

HS

), A

ST

M D

2992-B

•1

00

% F

acto

ry H

yd

rote

st - A

t 1.5

x the s

eries rate

d p

ressure

of 150°

F (

65

.6°

C)

Be

ne

fits

•C

orr

osio

n C

ontr

ol

•R

educed P

ara

ffin

& S

cale

Build

-Up

•R

educed Insta

llation C

osts

•R

educed M

ain

tance C

ost

•Im

pro

ved F

low

Effic

iency

Ph

ysic

al P

rop

ert

ies

•D

en

sity (

lbs/c

u ft)

= 1

24

•D

en

sity (

kg

s/c

u c

m)

= 1

,93

x 1

0-3

•S

pecific

Gra

vity =

1.9

9

Th

erm

al

Pro

pert

ies

•C

oe

ffic

ien

t o

f T

he

rma

l C

on

du

ctivity

0.2

BT

U/(

ft.h

r.°

F) 3

,0 c

al./(

cm

.hr.°

C)

•C

oeffic

ient

of

Therm

al

Expansio

n

8.7

x 1

0-6 in/in/°

F (

15,7

x 1

0-6 m

m/m

m/°

C)

Ap

pli

ca

tio

ns

•F

low

or In

jection L

ines

•O

il, G

as, S

altw

ate

r, C

O2 a

nd

H2S

•T

ransfe

r or D

isposal L

ines

Flo

w F

ac

tors

•H

azen W

illia

ms C

=150

•E

ffective R

oughness =

0.0

0006 in.

(1524 x

10

-6 m

m)

No

min

al

Mo

du

li

•M

odulu

s o

f E

lasticity

Hoop -

3.3

PS

I x 1

06 (

GP

a 2

2,8

)

Axia

l -

2.0

PS

I x 1

06 (

GP

a 1

3,8

)

•P

ois

son’s

Ratio (

Min

or)

= 0

.39

STAR

™ A

lip

hati

c A

min

e L

ine P

ipe

Hig

h P

ressu

re - A

PI 15H

R D

ES

IGN

- P

rod

uct D

ata

15

HR

-00

01

/ 1

5H

R-0

00

5

LIC

EN

SE

E Q

1 R

AT

ED

Ad

van

ced

C

om

po

sit

e T

hre

ad

(A

CT

)

Jo

inin

g S

yste

mA

PI

Th

rea

ds

•A

dva

nce

d C

om

po

site

Th

rea

d (

AC

T)

- M

old

ed

th

rea

ds

usin

g a

gra

ph

ite

ce

ram

ic a

nd

ep

oxy c

om

po

site

fo

r

hig

h p

erf

orm

an

ce

ap

plic

atio

ns.

(pate

nt n

o’s

4,9

99,3

89 &

5,1

79,1

40)

•P

recis

ion

Gro

un

d T

hre

ad

(P

GT

) -

Typ

ica

l gro

un

d

thre

ad

s p

rod

uce

d w

ith

nu

me

rica

l co

ntr

olle

d g

rin

din

g

equip

ment.

•A

ll 1

½”

EU

E 1

0rd

an

d 2

-3/8

” -

” E

UE

8rd

AP

I

thre

ad

s c

on

form

to

AP

I 5

B T

ab

le 1

4 (

L4

is

min

imu

m)

an

d a

ll 5

½”

- 9

-5/8

” O

D 8

rd c

asin

g t

hre

ad

s c

on

form

to A

PI

5B

Ta

ble

7 (

L4

is m

inim

um

)

Pe

rfo

rma

nc

e R

ati

ng

s v

s.

Te

mp

era

ture

AS

TM

D 2

992-B

•11

.4 Y

ear Life, LT

HS

psi

(MP

a)

•20 Y

ear

Life,

LT

HS

psi

(MP

a)

•20 Y

ear

Life,

LC

Lpsi

(Low

er

Confidence L

imit)

(MP

a)

150°

F*

(65.6

° C

)

22,2

89

(153,8

)

21,3

48

(147,2

)

20,2

55

(139,7

)

180°

F*

(82.2

° C

)

20,7

03

(142,8

)

19,5

10

(134,5

)

18,5

42

(127,9

)

200°

F

(93

.3°

C)

19,6

48

(135,5

)

18,2

85

(126,1

)

17,4

00

(120,0

)

73.4

° F

(23°

C)

26,3

53

(181,7

)

26,0

04

(179,3

)

24,5

96

(169,6

)

* 150°

F a

nd 1

80°

F d

ata

are

inte

rpola

ted

Page 36: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

LP

/STAR

™ A

lip

hati

c A

min

e (A

PI 1

5H

R D

esig

n) - P

ag

e 2

AP

I T

HR

EA

DS

(Metr

ic C

on

vers

ion

s a

re i

n P

are

nth

esis

)

32/

13

49.

2)

7,4

7(7

0.3

)0,

87(

70.

0)

8,1(

07.

0)

0,1(

02.

4)

7,6

01(

45

1)

9,6

4(4

3)

4,6

8(0

05

)4,

3(0

54

)1,

3(0

04

)8,

2(0

04

1)

7,9(

01

)1,

3(0

3(0

)2,

00

71

)8

47

3(0

4.8

)4,

4(U

N5

3

42/

14

58.

3)

8,7

9(2

0.4

)1,

20

1(9

0.0

)3,

2(0

2.1

)8,

1(5

4.5

)4,

83

1(1

02

)3,

16(

62

)0,

66(

00

5)

4,3(

05

4)

1,3(

00

4)

8,2(

00

41

)7,

9(1

1)

4,3(

03

(0)

2,0

09

2)

39

36(

04.

41

)5,

7(U

N5

4

68/

56

39.

5)

6,0

51(

81.

6)

0,7

51(

21.

0)

0,3(

03.

2)

4,3(

51.

7)

6,1

81(

90

3)

2,4

9(7

1)

2,3

4(0

05

)4,

3(0

54

)1,

3(0

04

)8,

2(0

03

1)

0,9(

41

)3,

4(0

2(0

)1,

00

76

)1

77

41(

02.

43

)8,

71(

SM

56

88/

58

47.

7)

6,6

91(

70.

8)

0,5

02(

71.

0)

3,4(

03.

4)

4,6(

52.

9)

0,5

32(

40

4)

1,3

21(

31

)0,

33(

00

5)

4,3(

05

4)

1,3(

00

4)

8,2(

00

31

)0,

9(6

1)

9,4(

03

(0)

2,0

07

11

)4

97

52(

01.

85

)3,

03(

SM

58

Seri

es 1

250 -

AC

T (

All S

izes)

or

PG

T (

2”,

2 ½

”,

3” a

nd

4” S

izes)

Seri

es 1

000 -

AC

T o

r P

GT

(A

ll S

izes E

xcep

t 8”)

Seri

es 8

00 -

AC

T o

r P

GT

(A

ll S

izes E

xcep

t 8”)

Seri

es 5

00 -

PG

T (

All S

izes)PIP

E D

IME

NS

ION

S (N

OM

INA

L)

FG

S R

AT

ED

PR

ES

SU

RE

S(4

)

Pip

e-T

hre

ad

Siz

e

Inch

es

Insid

e

Dia

mete

r

In(m

m)

Min

imu

m

Ben

din

g

Rad

ius

Ft

(m)

Maxim

um

Defl

ecti

on

In/j

t(c

m/j

t)

Co

nn

ec

tio

n

Dia

mete

r

In(m

m)

Pip

e

Weig

ht

Lb

s/f

t(k

g/m

)

Wall

Th

ickn

ess

In(m

m)

Ou

tsid

e

Dia

mete

r

In(m

m)

Maxim

um

Su

pp

ort

Sp

an

Ft

(m)

Ult

ima

te(2

)

Pre

ssu

reA

ST

MD

-1599

psi

(MP

a)

Co

llap

se

Rati

ng

psi

(MP

a)

Sta

tic

(1)

200º F

(93.3

º C

)

psi

(MP

a)

Sta

tic

(1)

180º F

(82.2

º C

)

psi

(MP

a)

Sta

tic

(1)

150º F

(65.6

º C)

psi

(MP

a)

Sh

ort

Te

rm

Ten

sile R

ati

ng

Lb

s(k

gs)

Cap

acit

y

Bb

ls/1

,00

0 f

t

(m3/k

m)

Th

read

ed

Ad

ap

ter

Pro

du

ct

Co

de

28/

32

49.

1)

3,9

4(7

0.2

)6,

25(

70.

0)

8,1(

04.

0(0

)6,

50.

3)

5,7

7(4

01

)7,

13(

05

)0,

72

1(0

57

)2,

5(0

56

)5,

4(0

06

)1,

4(0

01

2)

5,4

1(9

)8,

2(0

01

(0)

7,0

01

1)

52

42(

07.

3)

9,1(

RN

32

2/1

28/

72

73.

2)

2,0

6(2

5.2

)0,

46(

80.

0)

0,2(

06.

0(0

)9,

55.

3)

2,0

9(6

21

)4,

83(

14

)1,

40

1(0

57

)2,

5(0

56

)5,

4(0

06

)1,

4(0

01

2)

5,4

1(9

)8,

2(0

01

(0)

7,0

07

18

47

3()

04.

5)

8,2(

UN

72

32/

13

49.

2)

7,4

7(4

1.3

)8,

97(

01.

0)

5,2(

00.

1)

5,1(

52.

4)

0,8

01(

75

1)

9,7

4(3

3)

8,3

8(0

57

)2,

5(0

56

)5,

4(0

06

)1,

4(0

01

2)

5,4

1(11

)4,

3(0

01

(0)

7,0

07

2)

25

95(

04.

8)

4,4(

UN

53

42/

14

58.

3)

8,7

9(9

0.4

)9,

30

1(2

1.0

)0,

3(0

6.1

)4,

2(5

5.5

)0,

14

1(4

02

)2,

26(

52

)5,

36(

05

7)

2,5(

05

6)

5,4(

00

6)

1,4(

00

91

)1,

31(

21

)7,

3(0

8(0

)6,

00

34

)0

84

9(0

4.4

1)

5,7(

UN

54

68/

56

05.

5)

7,9

31(

58.

5)

6,8

41(

71.

0)

3,4(

02.

3)

8,4(

53.

7)

7,6

81(

29

2)

0,9

8(8

1)

7,5

4(0

57

)2,

5(0

56

)5,

4(0

06

)1,

4(0

00

2)

8,3

1(4

1)

3,4(

08

(0)

6,0

08

8)

00

49

1(0

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67

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6)

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0)

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6)

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01.

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92

3)

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61

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04(

05

21

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7(0

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1)

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00

33

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71

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08

71

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93(

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PM

56

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58

47.

7)

6,6

91(

75.

8)

7,7

12(

24.

0)

7,0

1(04.11

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82(

82

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5,0

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05

21

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011

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50

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2,7(

00

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5(0

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2(0

02

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75

66(

01.

85

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A/N

Seri

es 1

500 -

AC

T (

All S

izes)

or

PG

T (

2”,

2 ½

”,

3” a

nd

4” S

izes)

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10

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1)

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14(

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0,5

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51

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05

31

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52

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00

04

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8)

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09

6)

8,4(

00

31

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68

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1(R

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1

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0)

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0)

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11

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3)

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31

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04(

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99(

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72

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53

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8)

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SM

53

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14

58.

3)

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3.4

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04

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96

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4(0

03

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30

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2(0

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1)

5,7(

RM

54

68/

56

05.

5)

7,9

31(

22.

6)

0,8

51(

63.

0)

1,9(

03.

6)

4,9(

47.

7)

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91(

11

3)

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9(7

1)

2,3

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05

1)

3,0

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53

1)

3,9(

05

21

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8(0

00

4)

6,7

2(7

1)

2,5(

06

6)

6,4(

00

88

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2)

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67

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5)

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27.

6)

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7)

7,0

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33

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05

21

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00

4)

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1)

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06

6)

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91

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28

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2.4

3)

8,7

1(A/

N

88/

59

47.

7)

6,6

91(

57.

8)

3,2

22(

15.

0)

0,3

1(06.31

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02(

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73

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00

51

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31

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1)

6,8(

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93

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62(

02

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6(0

66

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4(0

01

73

)1

97

18(

01.

85

)3,

03(

A/N

Seri

es 1

750 -

AC

T (

All S

izes)

or

PG

T (

2”,

2 ½

”,

3” a

nd

4” S

izes)

2/1

10

9.1

44.

1)

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3(7

6.1

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24(

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0)

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06.

0)

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07.

2)

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6(3

8)

3,5

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6)

5,7

51(

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71

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21(

00

61

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00

51

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74

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9)

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11

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7(0

05

1)

70

33(

00.

2)

0,1(

RM

91

28/

32

49.

1)

3,9

4(4

2.2

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65(

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0)

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09.

0)

3,1(

53.

3)

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8(2

11

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4)

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01

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2)

25

95(

07.

3)

9,1(

SM

32

2/1

28/

72

73.

2)

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6(4

7.2

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96(

91.

0)

8,4(

04.

1)

1,2(

67.

3)

5,5

9(7

31

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14(

83

)5,

69(

05

71

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21(

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61

)0,

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00

51

)3,

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74

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11

1)

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00

24

)9

52

9(0

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)8,

2(S

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2

32/

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49.

2)

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7(0

4.3

)4,

68(

32.

0)

8,5(

01.

2)

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05.

4)

3,4

11(

07

1)

8,1

5(1

3)

7,8

7(0

57

1)

1,2

1(0

06

1)

0,1

1(0

05

1)

3,0

1(0

06

4)

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1)

0,4(

05

01

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7(0

04

6)

90

14

1(0

4.8

)4,

4(S

M5

3

42/

14

58.

3)

8,7

9(4

4.4

)8,

21

1(0

3.0

)6,

7(0

7.3

)5,

5(5

9.5

)1,

15

1(2

22

)7,

76(

32

)4,

85(

05

71

)1,

21(

00

61

)0,

11(

00

51

)3,

01(

00

64

)7,

13(

41

)3,

4(0

40

1)

2,7(

00

90

1)

03

04

2(0

4.4

1)

5,7(

RM

54

68/

56

05.

5)

7,9

31(

53.

6)

3,1

61(

24.

0)

7,0

1(0

3.7

)9,

01(

29.

7)

2,1

02(

71

3)

6,6

9(6

1)

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1)

1,2

1(0

06

1)

0,1

1(0

05

1)

3,0

1(0

06

4)

7,1

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1)

2,5(

04

01

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7(0

03

22

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61

94(

04.

92

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51(

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56

67

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5)

6,0

51(

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6)

2,4

71(

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0)

7,1

1(0

5.8

)6,

21(

04.

8)

4,3

12(

34

3)

5,4

01(

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83(

05

71

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21(

00

61

)0,

11(

00

51

)3,

01(

00

64

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13(

81

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5(0

60

1)

3,7(

00

26

2)

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77

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2.4

3)

8,7

1(A/

N

88/

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47.

7)

6,6

91(

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8)

1,7

22(

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0)

2,5

1(01.61

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42(

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3,2

03(

74

4)

2,6

31(

21

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03(

05

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21(

00

61

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11(

00

51

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01(

00

64

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13(

02

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6(0

60

1)

3,7(

00

54

4)

50

18

9(0

1.8

5)

3,0

3(A/

N

N/A

- N

ot A

vaila

ble

(R

epair J

oin

t R

equired)

Page 37: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

LP

/STAR

™ A

lip

hati

c A

min

e (A

PI 1

5H

R D

ES

IGN

) - P

ag

e 4

AP

I T

HR

EA

DS

(Metr

ic C

on

vers

ion

s a

re i

n P

are

nth

esis

)

Seri

es 3

000 -

AC

T (

On

ly)

se

hc

nI-e

ziS

epi

12

½2

34

56

68

8m

ets

yS

gni

nio

J

)3(

eziS

da

erh

T"

09.

1"

8/3

2"

8/7

2"

½3

4"

½5

"8/

56

"7

"8/

58

"8/

59

dr0

1E

UE

dr8

EU

Edr

8E

UE

dr8

EU

Edr

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UE

dr8

DO

dr8

DO

dr8

DO

dr8

DO

dr8

DO

D.O

te

sp

Uni

P•

nI5

1.2

06.

20

1.3

57.

35

7.4

55.

55

6.6

50.

75

6.8

56.

9

)m

m()

6,4

5()

0,6

6()

7,8

7()

3,5

9()

7,0

21(

)0,

14

1()

9,8

61(

)1,

97

1()

7,9

12(

)1,

54

2

htg

ne

Ld

aer

hT

nI6

3.2

49.

25

2.3

05.

38

8.3

57.

45

2.4

88.

45

8.4

31.

5

)m

m()

9,9

5()

7,4

7()

6,2

8()

9,8

8()

6,8

9()

7,0

21(

)0,

80

1()

0,4

21(

)2,

32

1()

3,0

31(

ss

oL

htg

ne

Lp

Ue

ka

M•

nI6

0.2

65.

28

8.2

31.

35.

38

3.4

88.

30

5.4

05.

45

7.4

)m

m()

4,2

5()

1,5

6()

0,3

7()

4,9

7()

9,8

8()

1,1

11(

)4,

89(

)3,

41

1()

3,4

11(

)7,

02

1(

Seri

es 2

000 -

AC

T (

All S

izes)

or

PG

T (

2”,

” a

nd

3” S

izes)

Seri

es 2

250 -

AC

T (

All S

izes)

or

PG

T (

2”,

” a

nd

3” S

izes)

Seri

es 2

500 -

AC

T (

All S

izes)

or

PG

T (

2” a

nd

” S

izes)

Jo

inin

g S

ys

tem

In

form

ati

on

(M

etr

ic C

on

vers

ion

s a

re in

Pare

nth

esis

)

2/1

10

9.1

44.

1)

6,6

3(4

8.1

)7,

64(

02.

0)

1,5(

00.

1)

5,1(

89.

2)

7,5

7(2

9)

0,8

2(6

5)

2,2

41(

00

03

)7,

02(

00

72

)6,

81(

05

52

)6,

71(

00

08

)2,

55(

01

)1,

3(0

92

5)

5,6

3(0

09

2)

39

36(

00.

2)

0,1(

A/N

28/

32

49.

1)

3,9

4(9

4.2

)2,

36(

72.

0)

9,6(

08.

1)

7,2(

56.

3)

7,2

9(4

21

)8,

73(

24

)7,

60

1(0

00

3)

7,0

2(0

07

2)

6,8

1(0

55

2)

6,7

1(0

00

8)

2,5

5(2

1)

7,3(

06

35

)0,

73(

00

35

)4

86

11(

07.

3)

9,1(

A/N

2/1

28/

72

73.

2)

2,0

6(3

0.3

)0,

77(

33.

0)

4,8(

06.

2)

9,3(

32.

4)

4,7

01(

25

1)

3,6

4(4

3)

4,6

8(0

00

3)

7,0

2(0

07

2)

6,8

1(0

55

2)

6,7

1(0

00

8)

2,5

5(3

1)

0,4(

06

35

)0,

73(

00

08

)7

36

71(

04.

5)

8,2(

A/N

3C

T2/

14

49.

2)

7,4

7(7

7.3

)8,

59(

14.

0)

4,0

1(0

9.4

)3,

7(0

0.7

)8,

77

1(8

81

)3,

75(

82

)1,

17(

00

03

)7,

02(

00

72

)6,

81(

05

52

)6,

71(

00

08

)2,

55(

41

)3,

4(0

43

5)

8,6

3(0

03

21

)7

11

72(

04.

8)

4,4(

A/N

2/1

32/

14

33.

3)

6,4

8(7

2.4

)5,

80

1(7

4.0

)9,

11(

04.

5)

0,8(

57.

6)

5,1

71(

31

2)

9,4

6(4

2)

0,1

6(0

00

3)

7,0

2(0

07

2)

6,8

1(0

55

2)

6,7

1(0

00

8)

2,5

5(5

1)

6,4(

09

25

)5,

63(

00

85

1)

33

84

3(0

8.0

1)

6,5(

A/N

42/

15

58.

3)

8,7

9(3

9.4

)2,

52

1(4

5.0

)7,

31(

03.

7)

9,0

1(7

4.7

)7,

98

1(7

42

)3,

57(

12

)3,

35(

00

03

)7,

02(

00

72

)6,

81(

05

52

)6,

71(

00

08

)2,

55(

61

)9,

4(0

63

5)

0,7

3(0

01

12

)7

15

64(

04.

41

)5,

7(A/

N

2/1

10

9.1

44.

1)

6,6

3(7

7.1

)0,

54(

61.

0)

1,4(

08.

0)

2,1(

48.

2)

1,2

7(8

8)

8,6

2(8

5)

3,7

41(

00

52

)2,

71(

05

22

)5,

51(

00

12

)5,

41(

00

66

)5,

54(

01

)1,

3(0

70

3)

2,1

2(0

03

2)

17

05(

00.

2)

0,1(

QM

91

28/

32

49.

1)

3,9

4(9

3.2

)7,

06(

22.

0)

6,5(

04.

1)

1,2(

06.

3)

4,1

9(9

11

)3,

63(

44

)8,

11

1(0

05

2)

2,7

1(0

52

2)

5,5

1(0

01

2)

5,4

1(0

06

6)

5,5

4(1

1)

4,3(

09

03

)3,

12(

00

24

)9

52

9(0

7.3

)9,

1(P

M3

2

2/1

28/

72

73.

2)

2,0

6(1

9.2

)9,

37(

72.

0)

9,6(

01.

2)

1,3(

30.

4)

4,2

01(

54

1)

2,4

4(6

3)

4,1

9(0

05

2)

2,7

1(0

52

2)

5,5

1(0

01

2)

5,4

1(0

06

6)

5,5

4(2

1)

7,3(

05

03

)0,

12(

00

36

)9

88

31(

04.

5)

8,2(

PM

72

32/

13

49.

2)

7,4

7(1

6.3

)7,

19(

43.

0)

6,8(

02.

3)

8,4(

58.

4)

2,3

21(

18

1)

2,5

5(9

2)

7,3

7(0

05

2)

2,7

1(0

52

2)

5,5

1(0

01

2)

5,4

1(0

06

6)

5,5

4(4

1)

3,4(

07

03

)2,

12(

00

89

)5

06

12(

04.

8)

4,4(

PM

53

2/1

32/

14

33.

3)

6,4

8(0

1.4

)1,

40

1(9

3.0

)9,

9(0

5.4

)7,

6(0

5.6

)1,

56

1(5

02

)5,

26(

52

)5,

36(

00

52

)2,

71(

05

22

)5,

51(

00

12

)5,

41(

00

76

)2,

64(

41

)3,

4(0

12

3)

1,2

2(0

08

21

)9

12

82(

08.

01

)6,

5(A/

N

42/

15

58.

3)

8,7

9(3

7.4

)1,

02

1(4

4.0

)2,

11(

00.

6)

9,8(

21.

7)

8,0

81(

63

2)

9,1

7(2

2)

9,5

5(0

05

2)

2,7

1(0

52

2)

5,5

1(0

01

2)

5,4

1(0

06

6)

5,5

4(5

1)

6,4(

07

03

)2,

12(

00

76

1)

71

86

3(0

4.4

1)

5,7(

A/N

2/1

10

9.1

44.

1)

6,6

3(4

7.1

)2,

44(

51.

0)

8,3(

07.

0)

0,1(

08.

2)

1,1

7(7

8)

5,6

2(0

6)

4,2

51(

05

22

)5,

51(

05

02

)1,

41(

00

91

)1,

31(

00

06

)4,

14(

9)

8,2(

08

22

)7,

51(

00

02

)9

04

4(0

0.2

)0,

1(Q

M9

1

28/

32

49.

1)

3,9

4(4

3.2

)4,

95(

02.

0)

1,5(

03.

1)

9,1(

05.

3)

9,8

8(7

11

)7,

53(

44

)8,

11

1(0

52

2)

5,5

1(0

50

2)

1,4

1(0

09

1)

1,3

1(0

00

6)

4,1

4(11

)4,

3(0

72

2)

7,5

1(0

07

3)

75

18(

07.

3)

9,1(

QM

32

2/1

28/

72

73.

2)

2,0

6(5

8.2

)4,

27(

42.

0)

1,6(

08.

1)

7,2(

49.

3)

1,0

01(

34

1)

6,3

4(6

3)

4,1

9(0

52

2)

5,5

1(0

50

2)

1,4

1(0

09

1)

1,3

1(0

00

6)

4,1

4(2

1)

7,3(

01

32

)9,

51(

00

65

)6

43

21(

04.

5)

8,2(

QM

72

32/

13

49.

2)

7,4

7(4

5.3

)9,

98(

03.

0)

6,7(

08.

2)

2,4(

47.

4)

4,0

21(

77

1)

9,3

5(9

2)

7,3

7(0

52

2)

5,5

1(0

50

2)

1,4

1(0

09

1)

1,3

1(0

00

6)

4,1

4(3

1)

0,4(

05

22

)5,

51(

00

68

)0

69

81(

04.

8)

4,4(

QM

53

42/

14

58.

3)

8,7

9(4

6.4

)9,

71

1(0

4.0

)2,

01(

09.

4)

3,7(

52.

6)

8,8

51(

23

2)

7,0

7(2

2)

9,5

5(0

52

2)

5,5

1(0

50

2)

1,4

1(0

09

1)

1,3

1(0

01

6)

1,2

4(5

1)

6,4(

04

32

)1,

61(

00

05

1)

96

03

3(0

4.4

1)

5,7(

A/N

2/1

10

9.1

44.

1)

6,6

3(0

7.1

)2,

34(

31.

0)

3,3(

06.

0)

9,0(

57.

2)

9,9

6(5

8)

9,5

2(1

6)

9,4

51(

00

02

)8,

31(

00

81

)4,

21(

00

71

)7,

11(

00

35

)5,

63(

9)

8,2(

00

61

)0,

11(

00

81

)8

69

3(0

0.2

)0,

1(R

M9

1

28/

32

49.

1)

3,9

4(9

2.2

)2,

85(

71.

0)

3,4(

01.

1)

6,1(

04.

3)

4,6

8(4

11

)7,

43(

54

)3,

41

1(0

00

2)

8,3

1(0

08

1)

4,2

1(0

07

1)

7,1

1(0

03

5)

5,6

3(1

1)

4,3(

06

51

)8,

01(

00

23

)5

50

7(0

7.3

)9,

1(Q

M3

2

2/1

28/

72

73.

2)

2,0

6(9

7.2

)9,

07(

12.

0)

3,5(

06.

1)

4,2(

58.

3)

8,7

9(9

31

)4,

24(

73

)0,

49(

00

02

)8,

31(

00

81

)4,

21(

00

71

)7,

11(

00

35

)5,

63(

21

)7,

3(0

75

1)

8,0

1(0

08

4)

28

50

1(0

4.5

)8,

2(Q

M7

2

32/

13

49.

2)

7,4

7(7

4.3

)1,

88(

72.

0)

9,6(

05.

2)

7,3(

36.

4)

6,7

11(

47

1)

0,3

5(0

3)

2,6

7(0

00

2)

8,3

1(0

08

1)

4,2

1(0

07

1)

7,1

1(0

03

5)

5,6

3(3

1)

0,4(

02

61

)2,

11(

00

57

)5

35

61(

04.

8)

4,4(

RM

53

42/

14

58.

3)

8,7

9(4

5.4

)3,

51

1(5

3.0

)9,

8(0

3.4

)4,

6(0

1.6

)9,

45

1(7

22

)2,

96(

32

)4,

85(

00

02

)8,

31(

00

81

)4,

21(

00

71

)7,

11(

00

35

)5,

63(

51

)6,

4(0

95

1)

0,1

1(0

08

21

)9

12

82(

04.

41

)5,

7(P

M5

4

67

05.

5)

7,9

31(

84.

6)

6,4

61(

94.

0)

4,2

1(0

9.8

)2,

31(

08.

8)

5,3

22(

42

3)

8,8

9(6

1)

6,0

4(0

00

2)

8,3

1(0

08

1)

4,2

1(0

07

1)

7,1

1(0

03

5)

5,6

3(8

1)

5,5(

06

51

)8,

01(

00

16

2)

04

57

5(0

4.9

2)

3,5

1(Q

M5

6

PIP

E D

IME

NS

ION

S (N

OM

INA

L)

FG

S R

AT

ED

PR

ES

SU

RE

S(4

)

Pip

e-T

hre

ad

Siz

e

Inch

es

Insid

e

Dia

mete

r

In(m

m)

Min

imu

m

Be

nd

ing

Rad

ius

Ft

(m)

Maxim

um

Defl

ecti

on

In/j

t(c

m/j

t)

Co

nn

ec

tio

n

Dia

mete

r

In(m

m)

Pip

e

We

igh

t

Lb

s/f

t(k

g/m

)

Wa

ll

Th

ickn

ess

In(m

m)

Ou

tsid

e

Dia

mete

r

In(m

m)

Maxim

um

Su

pp

ort

Sp

an

Ft

(m)

Ult

ima

te(2

)

Pre

ssu

reA

ST

MD

-1599

psi

(MP

a)

Co

llap

se

Ra

tin

g

psi

(MP

a)

Sta

tic

(1)

200º F

(93.3

º C)

psi

(MP

a)

Sta

tic

(1)

180º F

(82.2

º C)

psi

(MP

a)

Sta

tic

(1)

150º F

(65.6

º C)

psi

(MP

a)

Sh

ort

Term

Ten

sile R

ati

ng

Lb

s(k

gs)

Cap

acity

Bb

ls/1

,000 ft

(m3/k

m)

Th

read

ed

Ad

ap

ter

Pro

du

ct

Co

de

Seri

es 3

250 -

AC

T (

On

ly)

Availab

le U

po

n R

eq

uest

N/A

- N

ot A

vaila

ble

(R

epair J

oin

t R

equired)

Page 38: Daftar Pustaka - digilib.itb.ac.id...... Tugas Sarjana, Teknik Mesin FTI ITB, 2006. 3. ... Tekanan dalam Pd 4.14 10 6Pa DATA OPERASI 8" crude pipeline ... Seri pipa STAR FRP SERIES

Issu

ed N

ove

mber 2004

Supers

edes M

arc

h 2

004

HE

AD

QU

AR

TE

RS

P.O

. B

ox 3

7389

2425 S

.W.

36th

Str

eet

San A

nto

nio

, Texas 7

8237

Phone:

1 (

210)

434-5

043

Fax:

1 (

210)

434-7

543

ww

w.s

tarf

ibe

rgla

ss.c

om

E-M

ail:

in

fo@

sta

rfib

erg

lass.c

om

® T

he

AP

I Q

MS

Re

gis

tere

d m

ark

is e

ith

er

a t

rad

em

ark

of

reg

iste

red

tra

de

ma

rk o

f th

e A

me

rica

n P

etr

ole

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In

stitu

te in

th

e U

nite

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tate

s a

nd

/or

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co

un

trie

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LP

/STAR

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lip

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min

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PI 1

5H

R D

esig

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ag

e 6

Co

rresp

on

din

g N

um

bere

d N

ote

s:

1.

SE

RIE

S P

RE

SS

UR

E -

The m

axim

um

opera

ting p

ressure

at

desig

n t

em

pera

ture

.

2.

ULT

IMA

TE

S -

The t

ypic

al m

ode o

f fa

ilure

for

pre

ssure

is w

eep a

nd f

or

tensile

it

is a

n a

cro

ss t

he join

t pip

e b

ody s

hear.

3.

AP

I C

ON

NE

CT

ION

S -

Any o

rder

may inclu

de u

p t

o 1

5%

thre

aded a

nd c

ouple

d p

ipe.

All

pro

ducts

are

pro

duced inte

gra

l jo

int

unle

ss indic

ate

d (

TC

) T

hre

aded a

nd C

ouple

d.

All

” E

UE

10rd

and 2

3/8

” -

” E

UE

8rd

AP

I th

reads c

onfo

rm t

o A

PI

5B

Table

14 (

L4 is m

inim

um

) and a

ll 5½

” -

9 5

/8”

OD

8rd

casin

g t

hre

ads c

onfo

rm t

o A

PI

5B

Table

7 (

L4 is

min

imu

m).

4.

CY

CL

IC -

Consult a

Fib

er

Gla

ss S

yste

ms t

echnic

al

serv

ices p

ers

onnel

in a

pplic

ation w

here

pre

ssure

flu

ctu

ations o

f m

ore

than 2

0 p

erc

ent

of

the s

teady p

ressure

rating a

re

an

ticip

ate

d.

LIM

ITE

D W

AR

RA

NT

Y

Se

lle

r w

arr

an

ts t

ha

t P

RO

DU

CT

S m

an

ufa

ctu

red

by S

elle

r w

he

n p

rop

erl

y i

nsta

lle

d,

use

d,

an

d m

ain

tain

ed

sh

all b

e f

ree

fro

m d

efe

cts

in

ma

teri

al

an

d w

ork

ma

nsh

ip.

Se

lle

r’s

responsib

ility

under

this

warr

anty

shall

be lim

ited t

o r

epla

cin

g o

r re

pairin

g P

RO

DU

CT

S,

at

Selle

r’s o

ption,

the P

RO

DU

CT

S t

hat

pro

ve d

efe

ctive in m

ate

rial or

work

manship

within

one

(1)

year

from

the d

ate

of

insta

llation,

pro

vid

ed t

hat

Buyer

giv

es S

elle

r pro

mpt

notice o

f any d

efe

ct

or

failu

re a

nd s

atisfa

cto

ry p

roof

there

of. A

ny d

efe

ctive p

roduct

must

be r

etu

rned t

o

Selle

r’s f

acto

ry,

or

any o

ther

repair f

acili

ty d

esig

nate

d b

y S

elle

r.

Selle

r w

ill d

eliv

er

repla

cem

ent

of

defe

ctive P

RO

DU

CT

S t

o B

uyer

freig

ht

pre

paid

to t

he d

estination p

rovid

ed f

or

in t

he

origin

al

ord

er.

P

RO

DU

CT

S r

etu

rned t

o S

elle

r fo

r w

hic

h S

elle

r pro

vid

es r

epla

cem

ent

under

this

warr

anty

shall

becom

e t

he p

ropert

y o

f th

e S

elle

r.

This

lim

ited w

arr

anty

does n

ot

apply

to f

ailu

re o

f P

RO

DU

CT

S c

aused b

y a

bra

siv

e m

ate

rials

, exposure

to a

ggre

ssiv

e f

luid

s,

impro

per

applic

ation,

mis

handlin

g,

or

abuse.

In t

he e

vent

PR

OD

UC

TS

are

altere

d o

r re

paired b

y t

he B

uyer

and/o

r end u

ser

without

prior

written a

ppro

val

of

the S

elle

r, a

ll w

arr

anties a

re v

oid

. E

quip

ment

and a

ccessories n

ot

manufa

ctu

red b

y t

he s

elle

r w

arr

ante

d o

nly

to t

he e

xte

nt

of

and b

y t

he o

rigin

al

manufa

ctu

rer’

s w

arr

anty

. A

new

warr

anty

period s

hall

not

be e

sta

blis

hed f

or

repaired o

r re

pla

ced

mate

rials

, P

RO

DU

CT

S,

or

supplie

s.

Such i

tem

s s

hall

rem

ain

under

warr

anty

only

for

the r

em

ain

der

of

the w

arr

anty

period o

n o

rig

inal

mate

rials

, P

RO

DU

CT

S,

or

supplie

s.

The f

ore

goin

g w

arr

anties a

re i

n l

ieu o

f all

oth

er

warr

anties,

wheth

er

ora

l, w

ritten,

expre

ss,

implie

d o

r sta

tuto

ry.

Im

plie

d w

arr

anties o

f fitn

ess a

nd m

erc

hanta

bili

ty s

hall

not

apply

.

Selle

r’s w

arr

anty

oblig

ations a

nd B

uyer’s r

em

edie

s t

here

under

(except

as t

o t

itle

) are

sole

ly a

nd e

xclu

siv

ely

as s

tate

d h

ere

in.

In n

o c

ase w

ill S

elle

r be l

iable

for

consequential

dam

ages,

labor

perf

orm

ed i

n c

onnection w

ith r

em

oval

and r

epla

cem

ent

of

the P

RO

DU

CT

S,

loss o

f pro

duction o

r any o

ther

loss i

ncurr

ed b

ecause o

f in

terr

uption o

f serv

ice.

IMP

OR

TA

NT

NO

TIC

E

Th

is lit

era

ture

is in

ten

ded

as a

gu

ide o

nly

. A

ll v

alu

es lis

ted

in

th

is p

rod

uct

sp

ecif

icati

on

are

no

min

al. U

nsatisfa

cto

ry p

roduct re

sults m

ay o

ccur

due to e

nvironm

enta

l fluctu

a-

tions,

variations i

n o

pera

ting p

rocedure

s,

or

inte

rpola

tion o

f data

. W

e s

uggest

that

pers

onnel

usin

g t

his

data

have s

pecia

lized t

rain

ing a

nd e

xperience i

n t

he a

pplic

ation o

f th

ese

pro

ducts

and t

heir n

orm

al

insta

llation a

nd o

pera

ting c

onditio

ns.

Your

inte

nded a

pplic

ation o

f th

ese p

roducts

should

be v

erifie

d f

or

pro

priety

by y

our

engin

eers

. W

e e

xpre

ssly

dis

cla

im r

esponsib

ility

for

any c

onsequential

or

incid

enta

l dam

ages r

esultin

g f

rom

the i

nsta

llation o

r use o

f th

ese p

roducts

sin

ce w

e d

o n

ot

dete

rmin

e t

he d

egre

e o

f care

utiliz

ed

during t

he p

roduct

insta

llation o

r serv

ice.

We r

eserv

e t

he r

ight

to r

evis

e t

his

data

, as n

ecessary

, w

ithout

notice.

We w

elc

om

e c

om

ments

regard

ing t

his

pro

duct

litera

ture

.