Propane gas, Table 1 – first stage pipe sizing, Page 8 – Louisville Tin and Stove BFT201 User Manual

Page 8

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TABLE 1 – first stage pipe sizing

10 PSIG Inlet with a 1 PSIG Pressure Drop
Maximum capacity of pipe or tubing, in thousands of BTU/hr. of L.P. Gas

Size of Pipe

LENGTH OF PIPE OR TUBING, FEET*

Or Copper
Tubing, Inches

1 0

2 0

3 0

4 0

5 0

6 0

7 0

8 0

9 0

1 0 0

3/8

5 58

3 83

30 9

265

2 3 5

2 1 3

1 9 6

1 8 2

1 7 1

1 6 1

Copper

½

1387

870

7 00

5 99

5 3 1

4 8 1

4 4 3

4 1 2

3 8 6

3 6 5

Tubing

5/8

2360

1622

1303

1115

9 8 8

8 9 6

8 2 4

7 6 7

7 1 9

6 7 9

(O.D.)

¾

3993

2475

2205

1887

1672

1515

1394

1297

1217

1149

½

3339

2295

1843

1577

1398

1267

1165

1084

1017

9 6 1

Pipe

¾

6982

4799

3854

3298

2923

2649

2437

2267

2127

2009

Size

1

13153

9040

7259

6213

5507

4989

4590

4270

4007

3785

1-1/4

27004

18560

14904

12756

11306

10244

9424

8767

8226

7770

1-1/2

40461

27809

22331

19113

16939

15348

14120

13136

12325

11642

2

77924

53556

43008

36809

32623

29559

27194

25299

23737

22422

12 5

150

1 75

2 00

2 2 5

2 5 0

2 7 5

3 0 0

3 5 0

4 0 0

3/8

1 42

1 30

11 8

111

1 0 4

9 0

8 9

8 9

8 2

7 6

Copper

½

32 3

293

2 69

2 51

235

222

2 1 1

2 0 1

1 85

1 7 2

Tubing

5/8

6 01

5 46

50 2

467

4 3 8

4 1 4

3 9 3

3 7 5

3 4 5

3 2 1

(O.D.)

¾

1018

923

8 43

7 90

7 4 0

7 0 0

6 6 4

6 3 4

5 8 4

5 4 3

½

85 2

772

7 10

6 60

6 1 9

5 8 5

5 5 6

5 3 0

4 8 8

4 5 4

Pipe

¾

1780

1613

1484

1381

1296

1224

1162

1109

1020

9 4 9

Size

1

3354

3039

2796

2601

2441

2305

2190

2089

1922

1788

1-1/4

6887

6240

5741

5340

5011

4733

4495

4289

3945

3670

1-1/2

10318

9349

8601

8002

7508

7092

6735

6426

5911

5499

2

19871

18005

16564

15410

14459

13658

12971

12375

11385

10591

*Total length of piping from outlet of first stage regulator to inlet of second stage regulator (or to inlet of second stage regulator furthest
away).
Notes:

1) To allow 2 PSIG pressure drop, multiply total gas demand by .707, and use capacities from table.
2 )

For different first stage pressures, multiply total gas demand by the following factors, and use capacities from table.
First State Pressure PSIG Multiply by
2 0

.844

2 1

.912

Data Calculated per NFPA #54 & 58.

TABLE 4 – Second, Single, or Integral Twin Stage Pipe Sizing

11 Inches Water Column Inlet with a ½ Inch Water Column Drop
Maximum capacity of pipe or tubing in thousands of BTU/hr of LP-Gas

Size of Pipe

LENGTH OF PIPE OR TUBING, FEET*

Or Copper
Tubing, Inches

1 0

2 0

3 0

4 0

5 0

6 0

7 0

8 0

9 0

1 0 0

3/8

4 9

3 4

2 7

2 3

2 0

1 9

Copper

1/2

1 1 0

7 6

6 1

5 2

4 6

4 2

3 8

3 6

3 3

3 2

Tubing

5/8

2 06

1 41

11 4

9 7

8 6

7 8

7 1

6 7

6 2

5 9

(O.D.)

3/4

3 4 8

2 3 9

1 9 2

1 6 4

146

132

1 2 0

1 1 3

1 0 5

1 0 0

7/8

53 6

36 8

29 6

253

2 2 4

2 0 3

1 8 5

1 7 4

1 6 1

1 5 4

1/2

29 1

20 0

16 1

137

1 2 2

1 1 0

1 0 2

9 4

8 7

8 4

Pipe

3/4

60 8

41 8

33 6

287

2 5 5

2 3 1

2 1 2

1 9 8

1 8 5

1 7 5

Size

1

1146

788

6 32

54 1

4 8 0

4 3 5

4 0 0

3 7 2

3 4 9

3 3 0

1-1/4

2353

1617

1299

1111

9 8 5

8 9 2

8 2 1

7 6 4

7 1 7

6 7 7

1-1/2

3525

2423

1946

1665

1476

1337

1230

1144

1074

1014

2

6789

4666

3747

3207

2842

2575

2369

2204

2068

1954

12 5

150

1 75

20 0

2 2 5

2 5 0

2 7 5

3 0 0

3 5 0

4 0 0

3/8

Copper

1/2

Tubing

5/8

(O.D.)

3/4

7/8

1/2

7 4

6 7

6 2

5 8

5 4

5 1

4 8

4 6

4 3

4 0

Pipe

3/4

15 5

14 1

12 9

120

1 1 3

1 0 7

1 0 1

9 7

8 9

8 3

Size

1

2 9 2

26 5

244

2 27

2 1 3

2 0 1

1 9 1

1 8 2

1 6 7

1 5 6

1-1/4

6 0 0

54 4

50 0

465

437

412

3 9 2

37 4

34 4

3 20

1-1/2

89 9

81 5

74 9

697

654

618

5 8 7

56 0

51 5

4 79

2

1731

1569

1443

1343

1260

1190

1130

1078

9 9 2

9 2 3

*Total length of piping from outlet of regulator to appliance furthest away.

Data Calculated per NFPA #54 & 58.

Page 8

PROPANE GAS

PROPANE GAS

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