Lyons W.C. (ed.). Standard handbook of petroleum and natural gas engineering.2001- Volume 1

Tubing and Tubing String Design

1235

Table 4-1

63

Tubing Steed Grade Data

Yield Strength, psi

Steel Min. Tensile

Grade

Mln. Max.

Strength, psi Elongation'

H-60

40,000

80,000

60,000 27

c-75

75,000

90,000

95,000 16

c-95

95,000

11

0,000

105,000 16

N-80

80,000

11

0,000

100,000 16

P-105

105,000

135,000 120,000 15

'The minimum elongation in

2

in.

(50.80

mm) should be determined by the following formula:

J-55 55,000

80,000

75,000

20

AO.2

e

=

625,000

uo.o

where e

=

minimum elongation in

2

in.

(50.80

mm) in percent rounded

to

the nearest

%%

A

=

cross-sectional area of the tensile specimen in

in2,

based on a specified outside diameter or

nominal specimen width and specified wall thickness, rounded to the nearest

0.01

or

0.75

in?,

whichever is smaller

U

=

specified tensile strength in psi.

Table 4-164

Nonupset Tubing-Dimensions and Weights

I

2

8

4 6 6

Nmld

WdAtd

udsht.

Thrud...

Wd.htil

ah:

-

Wdl

Immld.

00t.i.j.

md

nick-

~i.-.

PW~

ud

B

Ib.Drt

In.

t

d

w,,

.u

*1.050

1.14

0.118

0.824

1.18 0.20

1.815

1.70

0.183 1.019

1.68

0.40

1.660

2.80

0.140 1380

2.27

0.80

1.900

2.76 0.146

1.610

2.72 0.60

End

IXmDllnr

lb/ft

Ib

DL.~*,

aplinr.

n.15

in.

4.00 0.167 2.041 8.94

1.60

2K

4.60 0.190 1.996 4.48 1.60

2)L 2%

5.80

0.254

1.867

6.76

1.40

6.40 0.217 2.441 6.16

8.20

"%

2% 8.60

0308

2.269

8.44

2.60

7.70 0216 8.068

7.M

5.40

334

8%

9.20 0.264 2.992 8.81

5.00

3%

10.20 0.289 2.922 9.91 4.80

3% 12.70 0.376 2.760 12.62 4.00

4 9.50 0226

8.548

9.11 6.20

434 12.60 0.271 8.958 12.24

6.00

*For

inlormmtian

only.

gsin

dme

to

cad

finishing.

1.N-d

yeiqh&

ulrrnd.

and mupiing

(Cd.

2). are

horn

lor

the

purpme

of

~dmlfidaon

I.

ordrriw

See Figure

4-409.

Source: From Ref. 11731.

3.

Wall

thickness.

Each length

of

pipe shall be measured for conformance to

wall-thickness requirements. The wall thickness at any place shall not

be

less than the tabulated thickness minus the permissible undertolerance

of

12.5%.

Wall-thickness measurements shall be made with a mechanical

caliper or with a properly calibrated nondestructive testing device

of

(text

continued

on page

1238)

c

Eo

w

0,

1.050

1.315

1.660

1.900

2%

3%

4

4%

0.113

0.133

0.140

0.145

0.190

0.254

0.217

0.308

0.254

0.375

0.262

0.271

0.824

1.049

1.380

1.610

1.995

1.867

2.441

2.269

2.992

2.750

3.476

3.958

1.13

1.68

2.27

2.72

4.43

5.75

6.16

8.44

8.81

12.52

10.46

12.24

~~

1.40

1.60

2.00

4.00

3.60

5.80

5.00

9.20

8.20

10.60

15.20

....

2.96

2.56

3.70

3.16

5.40

4.40

....

1.315

1.469

1.812

2.094

2%

2

4)

2.594

2.694

3.094

3.750

4.250

4.750

4

4%

e...

....

6

6%

....

10

10%

10

%

10%

U

3,

e

5'

1

2

3

4

6

7 8 9

10

11

09

Uput

B

81u:

Lautk

x.mstb.

-

a

6

in.

lb.

Der

ft

in

in.

v

c'-nca

lb

Table

4-165

External Upset Tubing-Dimensions and Welghts

C.kllkt.d

Wdht

otlwd.

Nomind

F-

'ad

cwpllne

oUt.id#

Ead

d

Pi-

End

of

Pi-

End

of

Pi#

Dhmetu.

W*i.bt:'

spccm'

DW,

toatartof

t~p..ing

tom-of

f

Pkln

Thh-gd

tag?!^.

Dim*.

lb,ft

Inaide

e

t.p.r.in.

ph16

in.

uI#bodt.

End

hL

in.

+0.0691)

+o.-1

D

t

d

WU

C

D.

L,

LO

Lb

1.20

1.80

2.40

2.90

4.70

5.95

6.50

8.70

9.30

12.95

11.00

12.76

'Nominal weights, threads

and

coupling

(Col.

Z),

are

shown

for

the

Somce: From

Ref.

[173].

2The minimum outside diameter

of

upset,

D,,

is limited

by

the

'Weight gain due

to

end

finiahing.

purpose

of

identification in ordering. minimum length

of

full-crest

thnds.

Scc

API

Std

5B.

See

Figure

4-410.

Tubing and Tubing String Design

1237

Table

4-166

Integral Joint Tubing-Dimensions

and

Weights

1

2

S

4

5

6

size:

Outside

Diameter,

in.

D

1.315

1.660

1.900

1900

2.063

1.72

2.10

2.33

2.40

2.76

3.25

~~

CnlNL.ted

Weight

W.ll

Inside

Upet'

t

e,

WP

d

0.133

1.U49

1.68

0.20

0.125

1.410

2.05

0.20

0.140 1.380 2.27 0.20

0.125 1.650 2.37 0 20

0.145

1.610

2.72

0.20

0.156

1.751

3.18 0.20

Tbidm~

Dbeler,

-End

mdbds

in.

Ib/ft

Ib

I

2

7

8

9

10

11 12

13

14

15

UIlOet

Dimmdnu,

in.

NomLull

,

Sire:

Weial:

Outside

Upsetmd

Outside,

Ina'de'

Dipmeter,

Threaded,

Diameter, Dinmeter,

Lmgth.

in.

Ibperft

+O.O6P5

d.015

Mbr.,

D

04

di.

L,

1.315

1.72

. . .

,

,970

1%

1.660 2.10

.

,

1.301

IM

I.tiR(I

2.53

.

1301

IM

1.900

4.40

. . .

,

1.531

158

1.9011

2.76

. .

1.531

1%

9.065 "1.29

2.094

1.672

1lLL6

Box

I_

Outside

length

Diameter,

Diameter

Min..

-0.09.5

Min.,

ofTaper,

Reeaa

ofTaper

4.005

rCn@

Len@ of

ntiv

wb

La

ma

Q

H

1.550 1.75~

I

1.m

H

1.880

1.875

1

1.723

L4

1,880

I875

1

1.723

14

2.110

2.0MI

1

1.963

1$

2.110

2.000

1

1.9R5

W

2.525

2.125

1

2.15fi

Wadth

of

Fee

Min.,

b

H2

82

LQe

192

M2

1Nominal

welghts,

upset

and

threaded (Col.

2).

are

rho- for the

purpose

of

identification

L"

ordering.

Weight

gain

due

10

endfinuhing.

4hc

minimum

outside diameter

D+,

is

limited

by

the

minimum

length

of

full

crest

Breads. See

API

Std

5B

4The

minimum inside diameter.

d,",

IS

hired

by

the

drift

test.

Sourcc.

From

Ref.

[I731

LrFigiire+IlI

D

d

BASIC

POWERTIGHT MAKEUP HANDTIGHT MAKEUP

Figure

4-409.

Non-upset tubing and coupling.

(From

Ref.

[173].)

See

Table

4-164

for

pipe dimensions.

1238

Drilling and Well Completions

BASIC

POWERTIGHT

MAKEUP HANDTIGHT MAKEUP

*SEE

TIELL

6.11

fOR

TOLERANCE

ON

OUTSIDE

DIAMETER

AT

OISTANCE

L.

FROM

END

OF

PIPE

Figure

4-410.

External-upset tubing and coupling.

(From

Ref.

17731.)

See Table

4-165

for pipe dimensions.

DASHEO

LINES INDICATE

POWERTIGHT

MAKEUP

Figure

4-411.

Integral-joint tubing.

(From

Ref.

[773].)

See Table

4-166

for pipe dimensions.

(text continued

from

page

123s)

appropriate accuracy. In case of dispute, the measurement determined by

use of the mechanical caliper shall govern.

4.

Weight.

Each length of tubing in sizes

1.660

in. and larger shall be weighed

separately. Lengths

of

tubing

in

sizes

1.050

and

1.315

in.

shall be weighed either

individually or in convenient

lots.

Threaded-and-coupled pipe shall be weighed with the couplings screwed

on or without couplings, provided proper allowance is made for the weight

of

the coupling. Threaded-and-coupled pipe, integral joint pipe and pipe

shipped without couplings shall be weighed without thread protectors

except

for

carload weighings, for which proper allowances shall be made

for the weight of the thread protectors.

5.

Calculated weights shall be determined in accordance with the following

formula:

Tubing and Tubing String Design

1239

W,

=

(Wpe

x

L)

+

e,

where W,

=

calculated weight of a piece of pipe of length

L

in lb (kg)

Wpe

=

plain-end weight in lb/ft (kg/m)

L

=

length of pipe, including end finish, as defined below in ft (m)

e,

=

weight gain or loss due to end finishing in lb (kg) (for plain-

6.

Length.

Pipe shall be furnished in range lengths conforming to the following

as specified on the purchase order: When pipe is furnished with threads

and couplings, the length shall be measured to the outer face of the

coupling, or if measured without couplings, proper allowance shall be made

to include the length of the coupling. For integral joint tubing, the length

shall be measured to the outer face of the box end.

end pipe, e,

=

0)

Pipe Range Lengths

Range

1

Range

2

Total range length' 20-24 28-32

Permissible variation, max. 2 2

Permissible length, min.

20 28

Range length

for

100%

of

carload:+

'By agreement between purchaser and manufacturer, the total range length for

Range

1

tubing may

be

6.10-8.53

m.

'Carload tolerances shall not apply to orders less than a carload shipped from the

mill. For any carload of pipe shipped from the mill

to

the final destination without

transfer or removal from the car, the tolerance shall apply to each car. For any order

consisting of more than a carload and shipped from the mill by rail, but not to the

final destination in the rail cars loaded at the mill, the carload tolerances shall apply

to the total order, but not to the individual carloads.

Performance Properties

Tubing performance properties, according to API Bulletin 5C2, 18th Edition

(March 1982), are given in Table

4-167.

Formulas and procedures for calculating

the values in Table

4167

are given in API Bulletin 5C3, 3rd Edition (March

1980).

Running and Pulling Tubing

The following are excerpts from "API Recommended Practice for Care and

Use of Casing and Tubing," API RP

5C1,

12th Edition (March 1981).

Preparation and Inspection before Running

1.

New tubing is delivered free of injurious defects as defined in API Standard

5A, 5AC and 5AX, and within the practical limits of the inspection

procedures therein prescribed. Some users have found that, for a limited

number of critical well applications, these procedures do not result in

casing sufficiently free of defects to meet their needs for such critical

applications. Various nondestructive inspection services have been employed

by users to assure that the desired quality of tubing is being run. In view

of this practice, it is suggested that the individual user:

(text continued on page

1246)

1240

Drilling and Well Completions

Table

4-167

Minimum Performance Properties

of

Tubing

1

2

3

4

5

6

7

8

9

10

11

Nominal

Weight Threaded and Coupled

Size:

lb

per ft

r

7

Outside

r

.

Wall

Inside Drift Outside Diameter of

Diameter Threads

and

Integral

Thick-

Diameter Diameter

coupling,

in.

-.

in.

Upset

in.

Coupling Joint Grade

ness

in.

r

.

Non-

r

.

Upset Upset Upset Regular Special

D

1.050 1.14 1.20

-

H40 0.113 0.824 0.730 1.313 1.660

-

1.14 1.20

-

5-55 0.113 0.824 0.730 1.313 1.660

-

1.14 1.20

-

G75 0.113 0.824 0.730 1.313 1.660

-

1.14 1.20

-

L80&N-80 0.113 0.824 0.730 1.313 1.660

-

1.315 1.70 1.80 1.72 H40 0.133 1.049 0.955 1.660 1.900

-

1.70 1.80 1.72 5-55 0.133 1.049 0.955 1.660 1.900

-

1.70 1.80 1.72 G75 0.133 1.049 0.955 1.660 1.900

-

1.70 1.80 1.72

L80&

N-80 0.133 1.049 0.955 1.660 1.900

-

1.660

-

2.10 H40 0.125 1.410

-

- - -

2.30 2.40 2.33 H-40 0.140 1.380 1.286 2.054 2.200

-

2.10 5-55 0.125 1.410

-

- -

2.30

2.40

2.33 5-55 0.140

1.380 1.286

2.054 2.200

-

2.30

2.40 2.33 C75 0.140 1.380

1.286

2.054 2.200

-

2.30

2.40 2.33

L-80

&

N-80 0.140 1.380

1.286

2.054 2.200

-

1.900

-

2.40 H40 0.125 1.650

- -

-

2.75 2.90 2.76 H40 0.145 1.610 1.516 2.200 2.500

-

2.40 J-55 0.125 1.650

- -

-

2.75

2.90 2.76 5-55 0.145

1.610

1.516

2.200 2.500

-

2.75

2.90 2.76 C75 0.145

1.610 1.516

2.200 2.500

-

2.75

2.90 2.76 L808~N-80 0.145

1.610 1.516

2.200 2.500

-

Tubing and Tubing String Design

1241

Table

4-1

67

(continued)

1

2

3 4

6

7

8 9 10 11

Nominal

Weight

Thruded

and

Coupled

~.UWW

Thdand

InWml

Thick-

Dhmctcl

Dhp-

Coupling.

in.

She:

lb.

per

It.

r

outside

I

,

Wall

Imide

Dtift

OutsideDi8meterof

in.

COUPh

Joint

GdC

nu

in.

Y

Non-

-

Uptet

Regular

Spmid

Cleurncr

in.

UP&

e

UP&

Upld

D

t

d

w

we

2.063

-

326

H4O

0.166 1.751

-

3.26

J-66

0.166 1.761

-

- -

3.26 C-76 0.166 1.761

-

- -

3.25

L-80&N-80

0.156 1.761

-

236

4.00

4.60

-

4.70

-

H-40

0.167

-

H-40

0.190

2.041 1.947

1.996 1.901

2.876

-

2.876 3.G 2.910

-

5-66

0.167

-

5-65 0.190

2.041 1.947

1.996 1.901

2.876

-

2.876 3.&3 2.910

4.00

4.60

-

4.70

4.00

4.60

6.80

-

C76

0.167

-

C-76

0264

-

C76

0,190

2.041 1.947

1.996 1.901

1.867 1.773

2.876

-

2.876

3.G

2.910

2.875 3.063 2.910

-

4.70

6.96

4.00

4.60

5.80

-

L-80&N-80

0.167

-

G80&N-80 0.190

-

L-80&N-80

0.264

2.041 1.947

1.996 1901

1.867 1.773

2.876

-

2.876 3.&3 2310

2.876 3.068 2.910

-

4.70

5.95

-

P-106

0.190

-

P-106 0264

1.996 1.901

1.867 1.773

2876 3.063

2310

2.876 3.063

2.910

4.60

6.80

4.70

6.96

2%

6.40 6.60

-

H-40

0217

2.441 2.347 3.600 3.668 3.460

-

f-66

0.217

2.441 2347 3.600

2.441 2.347 3.600

2.259 2.166 3.600

3.668

8.460

6.40 6.SO

6.40

6.60

8.60 8.70

-

(3-76

0217

-

C76

0.308

3.888

3.668

8.480

3.460

-

L-80&N-80

0.217

-

L-80&N-80 0.308

2.441 2.347

3.600

2369 2.166 3.600

3.668

am

3.460

6.40 6.50

8.60

8.70

-

P-106 0217

-

P-106 0308

2.441

2347

3.600

2.259

2.166

3.600

3.668

3.460

6.40 6.50

8.60

8.70

1444 Drilling and Well Completions

Table

4-167

(continued)

12

13

14

15

16

17

18

Integral Joint Joint Yield

I

,

Saength, lb

Drift Outside Collapse Internal

r

,

Diameter Diameter Resist- Yield Threaded

and

of

Box

ance

PreSSUre

Coupled Integral

,-

,

Joint

in.

psi psi Non-Upset Upset

Wk

-

7,680

7,530 6,360

13,310

-

10,560

10,360 8,740 18,290

-

14,410

14,130 11,920 24,950

-

- -

15,370

15,070 12,710 26,610

-

0.955 1.550

7,270 7,080 10,960 19,760

15,970

0.955 1.550 10,000 9,730 15,060 27,160 21,960

0.955 1.550 13,640 13,270 20,540

37,040 29,940

0.955

1.550 14,550

14,160 21,910

39,510 3 1,940

1.286 1.880

5,570

5,270

-

22,180

1.286 1.880 6,180

5,900 15,530

26,740 22,180

1.286 1.880 7,660

7,250

-

30,500

1.286 1.880 8,490

8,120

21,360 36,770 30,500

1.286

1.880 11,580

11,070

29,120 50,140 41,600

1.286 1.880 12,360 11,810

31,060 53,480 44,370

-

26,890

1.516 2.110 4,920 4,610

-

1.516 2.110 5,640 5,340 19,090 3 1,980 26,890

1.516 2.110 6,640 6,330

-

36,970

1.516 2.110

7,750

7,350 26,250

43,970 36,970

1.516 2.110

10,570

10,020 35,800

59,960 50,420

1.516

2.110 11,280

10,680 38,180

63,960 53,780

Tubing

and

Tubing String Design

1243

Table

4-1

67

(continued)

12 13 14 15 16 11 18 19 20

Joint

Yield

Stmtath.

Ib

-.

J

Integral

Joint

Inlernd

Yield

P-n

UP&

'

Thd

and

CouDkd

Phin-end

___JI__

Reau1.r

spew

and

Drift

Outddc

Diameter Diameter

Coliapsc

of

Box

Rt.isuncc

Non-UDd

Couplins

ClannoC

'tz

Coup'inr

Non-Upd UDUt

in.

mi

P.i

D.i

Dai

Wb

1.657

2.325

5,590

5,290

- -

35,700

1.651

2.325

7,690

7,280

-

- -

49.000

1.651 2.325 10,480

9,920

-

66,900

1.657

2.325

11,180

10.590

-

71,400

-

5,230

4,920

-

30,100

-

5,890

5,600

5.600 36,000 52,200

-

41,400

-

56,500

-

- -

7,190 6,110

-

8,100 1,100 1,700 7,100 49,500 11,700

-

I

9,520 9.230

67,400 97,800

-

I

11,040 10,500 10,500 10,500

-

14,330 14,040 13,960 10,120 96,600 126,900

-

60,300

- -

-

15,280 14,910 14,890 11,440 103,000 135,400

-

9,980 9,840

-

11,180 11,200 11,200 11,200 71,900 104,300

-

- -

15,460

14,700

14,000

14,100 94,400

136,900

-

20,060

19,650 19,540

16.010

135,200 111,700

-

5,580

5,280

6.280

5,510 52,800

12,500

-

1,680

1,260 1,200

1,260

12,600 99,100

-

I

10,410

9,910 9,910

9,910 99,000

135,900

-

I

14,350 14,060 14,010 10,340 149,400 186,300

-

11,160

10,670 10,510

10,510 105,600

145,000

-

15,300

15,000 14.940

11,030

169,300 198,100

-

14,010

13,810

13.870

13,870

138,600 190,300

-

20,090

19,690 19,610

14,480 209,100

260,800

-

1244

Drilling

and

Well Completions

Table

4-167

(continued)

9 10

11

1

2

3

4

6

6 7

8

Nomid

Weight

Threaded

and

Coupled

Thick-

Diameter Diameter

Coupling,

in.

I

Wall

Inside

Drift

Oubide

Diameter

of

in.

Sire:

Ib.

rn

it.

Ouuide

in.

Diw

Threadsand

IIItesrd

CoODlinP

Joint

G&

nu

in.

r

UDIe

Nom-

0

Clearance

Non-

Urn

Runkr

Sweial

urn

up.*

D

t

d

w

we

3%

7.70

9.20

10.20

7.70

9.20

10.20

7.70

9.20

10.20

12.70

7.70

9.20

10.20

12.70

9.20

12.70

9.60

-

4

9.60

-

9.60

-

9.60

-

4%

12.60

-

930

-

9.30

-

930

12.96

-

9.30

12.95

-

9.30

12.96

-

E40

0.218

-

H-40

0.264

-

H-40

0.289

-

J-66

0.216

-

J-66

0.264

-

5-56

0.289

-

E76 0.216

-

C-76

0.264

-

C-76 0.289

-

(2-76

0.376

-

L-80&N-80

0.216

-

G80&N-80

0.264

-

L-808tN-80

0.289

-

G80&N-80

0.575

P-106

0.264

0.376

s.068

2.94

2.992 2.867

2.922 2.797

3.068

2.943

2.992 2.887

2.922 2.797

3.068 2.943

2.992 2.867

2.922 2.797

2.760 2.626

3.068 2.943

2.992 2.867

2.922 2.797

2.760 2.626

2.992 2867

2.760 2.626

4.260

-

4.260 4.600

4.180

4.260

-

4.260

-

4.260 4.600

4.180

4.250

-

4.260

-

4.260

4.600

4.GO

4.260

-

4.260

4.600 4.180

4.260

-

4.260

4.600

4.zO

4.260

-

4.260

4.600

4.180

4.260

4.600

4.180

4.260

4.600

4.180

-

H-40

0.226

11.00

-

8-40

0.262

-

J-66

0.228

11.0

-

J-66 0.282

1170

-

C-76

0.262

-

C-76

OB6

- -

L-808tN-80

0.226

11.00

-

G80&N-80

0.262

12.76

-

H-40

0.271

12.76

-

J-66 0.271

12.76

-

C-76

0.271

12.75

-

L-806N-80

0.271

a.648

8.w

3.476 3.861

3.548

3.428

3.476 3.361

3.648

3.428

3.476 3.861

3.968

3.883

3.968

3.883

4.760

-

6.OOo

-

4.760

-

6.000

-

4.760

- -

-

6.000

-

4.760

-

6.000

-

6.200

6d68

-

6200

6.668

-

6.200

6.668

-

Lyons W.C. (ed.). Standard handbook of petroleum and natural gas engineering.2001- Volume 1

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