Material Composition Engineering Data

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Chapter 10

Engineering Data

Standard SpecificationsFor Valve Materials

(See table following this listing for

additional specifications, cross-referenced to Material Codenumbers.)

1. Cast Carbon SteelASTM A216 Grade WCCTemp. range = 20 to 800F (29 to

427C)Composition (Percent)

C 0.25 maxMn 1.2 maxP 0.04 maxS 0.045 maxSi 0.6 max

2. Cast Carbon SteelASTM A352 Grade LCCTemp. range = 50 to 700F (46 to

371C)

Composition Same as ASTM A216grade WCC

3. Carbon Steel BarAISI 1018, UNS G10180Temp. range =

20 to 800F (

29 to


C 0.15 to 0.2Mn 0.6 to 0.9P 0.04 maxS 0.05 max

4. Leaded Steel BarAISI 12L14, UNS G12144Temp. range = 20 to 800F (29 to


C 0.15 maxMn 0.85 to 1.15

P 0.04 to 0.09S 0.26 to 0.35Pb 0.15 to 0.35


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5. AISI 4140 Cr-Mo Steel(Similar to ASTM A193 Grade B7bolt material)Temp. range = 20F (29C) to

100F (56C) less than tempering

temperature to a maximum of1000F (593C).

Composition (Percent)C 0.38 to 0.43Mn 0.75 to 1.0P 0.035 maxS 0.035 maxSi 0.15 to 0.35Cr 0.8 to 1.1Mo 0.15 to 0.25Fe Remainder

6. Forged 3-1/2% Nickel SteelASTM A352 Grade LC3Temp. range = 150 to 650F (101 to


C 0.15 maxMn 0.5 to 0.8P 0.04 maxS 0.045 maxSi 0.6 maxNi 3.0 to 4.0

7. Cast Cr-Mo SteelASTM A217 Grade WC6Temp. range = 20 to 1100F (29 to


C 0.05 to 0.2

Mn 0.5 to 0.8P 0.04 maxS 0.045 maxSi 0.60 maxCr 1.0 to 1.5Mo 0.45 to 0.65

8. Cast Cr-Mo SteelASTM A217 Grade WC9Temp. range = 20 to 1100F (29 to


C 0.05 to 0.18Mn 0.4 to 0.7P 0.04 max

S 0.045 maxSi 0.6 maxCr 2.0 to 2.75Mo 0.9 to 1.2

9. Forged Cr-Mo SteelASTM A182 Grade F22Temp. range = 20 to 1100F (29 to

593C)

Composition (Percent)C 0.05 to 0.15Mn 0.3 to 0.6P 0.04 maxS 0.04 maxSi 0.5 maxCr 2.0 to 2.5Mo 0.87 to 1.13

10. Cast Cr-Mo SteelASTM A217 Grade C5Temp. range = 20 to 1200F (29 to


C 0.2 max

Mn 0.4 to 0.7P 0.04 maxS 0.045 maxSi 0.75 maxCr 4.0 to 6.5Mo 0.45 to 0.65

11. Type 302 Stainless SteelASTM A479 Grade UNS S30200Temp. range = 325 to 1500F (198

to 816C)Composition (Percent)

C 0.15 maxMn 2.0 maxP 0.045 max

S 0.03 maxSi 1.0 maxCr 17.0 to 19.0Ni 8.0 to 10.0N 0.1 maxFe Remainder

12. Type 304L Stainless SteelASTM A479 Grade UNS S30403Temp. range = 425 to 800F (254 to


C 0.03 maxMn 2.0 maxP 0.045 max

S 0.03 maxSi 1.0 maxCr 18.0 to 20.0Ni 8.0 to 12.0


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N 0.1 maxFe Remainder

13. Cast Type 304L Stainless SteelASTM A351 Grade CF3

Temp. range =

425 to 800F (

254 to427C)

Composition (Percent)C 0.03 maxMn 1.5 maxSi 2.0 maxS 0.03 maxP 0.045 maxCr 18.0 to 21.0Ni 8.0 to 11.0Mo 0.50 max

14. Type 316L Stainless SteelASTM A479 Grade UNS S31603Temp. range = 425 to 850F (254 to


C 0.03 maxMn 2.0 maxP 0.045 maxS 0.03 maxSi 1.0 maxCr 16.0 to 18.0Ni 10.0 to 14.0Mo 2.0 to 3.0N 0.1 maxFe Remainder


to 816C); above 1000F (538C),0.04 C required

Composition (Percent)C 0.08 maxMn 2.0 maxP 0.045 maxS 0.03 maxSi 1.0 maxCr 16.0 to 18.0Ni 10.0 to14.0Mo 2.0 to 3.0N 0.1 maxFe Remainder

16. Cast Type 316 Stainless SteelASTM A351 Grade CF8MTemp. range = 425 to 1500F (254

to 816C); above 1000F (538C),0.04 C required

Composition (Percent)C 0.08 maxMn 1.5 maxSi 1.5 maxP 0.04 maxS 0.04 maxCr 18.0 to 21.0Ni 9.0 to 12.0Mo 2.0 to 3.0


to 816C); above 1000F (538C),

0.04 C requiredComposition (Percent)

C 0.08 maxMn 2.0 maxP 0.045 maxS 0.03 maxSi 1.0 maxCr 18.0 to 20.0Ni 11.0 to15.0Mo 3.0 to 4.0N 0.1 maxFe Remainder

18. Cast Type 317 Stainless Steel

ASTM A351 Grade CG8MTemp. range = 325 to 1000F (198to 538C); above 1000F (538C),0.04 C required

Composition (Percent)C 0.08 maxMn 1.5 maxSi 1.5 maxP 0.04 maxS 0.04 maxCr 18.0 to 21.0Ni 9.0 to 13.0Mo 2.0 to 3.0


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19. Type 410 Stainless SteelASTM A276 Grade S41000Temp. range = Annealed

condition,20 to 1200F (29 to649C); Heat treated 38 HRC, 20

to 800F (

29 to 427C)Composition (Percent)

C 0.15 maxMn 1.0 maxP 0.04 maxS 0.03 maxSi 1.0 maxCr 11.5 to 13.5Fe Remainder

20. Type 17-4PH Stainless SteelASTM A564 Grade 630, UNS S17400Temp. range = 20 to 650F (29 to

343C). Can be used to 800F(427C) for applications, such as

cages, where stresses aregenerally compressive, and thereis no impact loading.

Composition (Percent)C 0.07 maxMn 1.0 maxSi 1.0 maxP 0.04 maxS 0.03 maxCr 15.0 to 17.5Nb 0.15 to 0.45Cu 3.0 to 5.0Ni 3.0 to 5.0Fe Remainder

20. Type 254 SMO Stainless SteelASTM A479 Grade UNS S31254Temp. range = 325 to 750F (198 to

399)CComposition (Percent)

C 0.02 maxMn 1.0 maxP 0.03 maxS 0.01 maxSi 0.8 maxCr 18.5 to 20.5Ni 17.5 to 18.5Mo 6.0 to 6.5N 0.180.22Fe Remainder

22. Cast Type 254 SMO StainlessSteelASTM A351 Grade CK3MCuNTemp. range = 325 to 750F (198 to


C 0.025 maxMn 1.2 maxSi 1.0 maxP 0.044 maxS 0.01 maxCr 19.5 to 20.5Ni 17.5 to 19.5Mo 6.0 to 7.0

23. Type 2205, S31803 DuplexStainless SteelASTM A279 Grade UNS S31803Temp. range = 20 to 600F (29 to


C 0.03 maxMn 2.0 maxP 0.03 maxS 0.02 maxSi 1.0 maxCr 21.0 to 23.0Ni 4.5 to 6.5Mo 2.5 to 3.5N 0.03 to 0.2Fe Remainder

24. Cast Type 2205, S31803Stainless Steel

ASTM A890 Grade 4a, CD3MNTemp. range = 20 to 600F (29 to


C 0.03 maxMn 1.5 maxSi 1.0 maxP 0.04 maxS 0.02 maxCr 21.0 to 23.5Ni 4.5 to 6.5Mo 2.5 to 3.5N 0.1 to 0.3Fe Remainder


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25. Cast IronASTM A126 Class B, UNS F12102Temp. range = Pressure Retaining

Components, 20 to 450F (29 to232C); Non-Pressure Retaining

Components,

100 to 800F (73 to427C); ANSI B31.5 150F(101C) minimum if the maximumstress does not exceed 40% of theambient allowable stress.

Composition (Percent)P 0.75 maxS 0.15 max

26. Cast IronASTM A126 Class C, UNS F12802Temp. range = Pressure Retaining

Components, 20 to 450F (29 to232C); Non-Pressure RetainingComponents, 100 to 800F (73 to

427C); ANSI B31.5

150

F(101C) minimum if the maximum

stress does not exceed 40% of theambient allowable stress.

Composition (Percent)P 0.75 maxS 0.15 max

27. Ductile IronASTM A395 Type 60-40-18Temp. range = 20 to 650F (29 to


C 3.0 minSi 2.5 maxP 0.08 max

28. Ductile Ni-Resist IronASTM A439 Type D-2B, UNSF43001Temp. range = 20 to 1400F (29 to


C 3.0 minSi 1.5 to 3.00Mn 0.70 to 1.25P 0.08 maxNi 18.0 to 22.0Cr 2.75 to 4.0

29. Valve Bronze

ASTM B61, UNS C92200Temp. range = 325 to 550F (198 to

288C)

Composition (Percent)Cu 86.0 to 90.0Sn 5.5 to 6.5Pb 1.0 to 2.0Zn 3.0 to 5.0Ni 1.0 maxFe 0.25 maxS 0.05 maxP 0.05 max

30. Tin BronzeASTM B564 Grade UNS C90500Temp. range = 325 to 400F (198 to


Cu 86.0 to 89.0Sn 9.0 to 11.0Pb 0.30 maxZn 1.0 to 3.0

Ni 1.0 maxFe 0.2 maxS 0.05 maxP 0.05 max

31. Manganese BronzeASTM B584 Grade UNS C86500Temp. range = 325 to 350F (198 to


Cu 55.0 to 60.0Sn 1.0 maxPb 0.4 maxNi 1.0 maxFe 0.4 to 2.0Al 0.5 to 1.5Mn 0.1 to 1.5Zn 36.0 to 42.0

32. Cast Aluminum BronzeASTM B148 Grade UNS C95400Temp. range = ANSI B31.1, B31.3,

325 to 500F (198 to 260C);ASME Section VIII, 325 to 600F(198 to 316C)

Composition (Percent)Cu 83.0 minAl 10.0 to 11.5Fe 3.0 to 5.0

Mn 0.50 maxNi 1.5 max


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33. Cast Aluminum BronzeASTM B148 Grade UNS C95800Temp. range = 325 to 500F (198 to


Cu 79.0 minAl 8.5 to 9.5Fe 3.5 to 4.5Mn 0.8 to 1.5Ni 4.0 to 5.0Si 0.1 max

34. B16 Yellow Brass BarASTM B16 Grade UNS C36000, 1/2

HardTemp. range = Non-Pressure

Retaining Components, 325 to400F (198 to 204C)

Composition (Percent)Cu 60.0 to 63.0

Pb 2.5 to 3.7Fe 0.35 maxZn Remainder

35. Naval Brass ForgingsASTM B283 Alloy UNS C46400Temp. range = 325 to 400F (198 to


Cu 59.0 to 62.0Sn 0.5 to 1.0Pb 0.2 maxFe 0.15 maxZn Remainder

36. Aluminum BarASTM B211 Alloy UNS A96061-T6Temp. range = 452 to 400F (269


Si 0.4 to 0.8Fe 0.7 maxCu 0.15 to 0.4Zn 0.25 maxMg 0.8 to 1.2Mn 0.15 maxCr 0.04 to 0.35Ti 0.15 maxOther Elements 0.15 maxAl Remainder

37. Cobalt-base Alloy No.6Cast UNS R30006, Weld fillerCoCr-ATemp. range = 325 to 1500F (198

to 816C)

Composition (Percent)C 0.9 to 1.4Mn 1.0 maxW 3.0 to 6.0Ni 3.0Cr 26.0 to 32.0Mo 1.0 maxFe 3.0 maxSi 2.0 maxCo Remainder

38. Ni-Cu Alloy Bar K500B865 Grade N05500Temp. range = 325F to 900F

(198C to 482C)

Composition (Percent)Ni 63.0 to 70.0Fe 2.0 maxMn 1.5 maxSi 0.5 maxC 0.25 maxS 0.01 maxP 0.02 maxAl 2.3 to 3.15Ti 0.35 to 0.85Cu Remainder

39. Cast Ni-Cu Alloy 400ASTM A494 Grade M35-1Temp. range = 325 to 900F (198 to


Cu 26.0 to 33.0C 0.35 maxMn 1.5 maxFe 3.5 maxS 0.03 maxP 0.03 maxSi 1.35 maxNb 0.5 maxNi Remainder

40. Ni-Cr-Mo Alloy C276 BarASTM B574 Grade N10276Temp. range = 325 to 1250F (198

to 677C)


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Composition (Percent)Cr 14.5 to 16.5Fe 4.0 to 7.0W 3.0 to 4.5C 0.01 max

Si 0.08 maxCo 2.5 maxMn 1.0 maxV 0.35 maxMo 15.0 to 17.0P 0.04S 0.03Ni Remainder

41. Ni-Cr-Mo Alloy CASTM A494 CW2MTemp. range = 325 to 1000F (198


Cr 15.5 to 17.5

Fe 2.0 maxW 1.0 maxC 0.02 maxSi 0.8 maxMn 1.0 maxMo 15.0 to 17.5P 0.03S 0.03Ni Remainder

42. Ni-Mo Alloy B2 BarASTM B335 Grade B2, UNS N10665Temp. range = 325 to 800F (198 to


Cr 1.0 maxFe 2.0 maxC 0.02 maxSi 0.1 maxCo 1.0 maxMn 1.0 maxMo 26.0 to 30.0P 0.04 maxS 0.03 maxNi Remainder

43. Cast Ni-Mo Alloy B2ASTM A494 N7MTemp. range = 325 to 1000F (198

to 538C)

Composition (Percent)Cr 1.0 maxFe 3.0 maxC 0.07 maxSi 1.0 maxMn 1.0 maxMo 30.0 to 33.0P 0.04 maxS 0.03 maxNi Remainder

Valve Materials Properties for PressureContaining Components(The material codes in this table correspond to the previous Standard

Specifications for Valve Materials listing.)

MINIMUM MECHANICAL PROPERTIES

MATER-IAL

CODE

TensileStrength

ksi(MPa)

YieldStrength

ksi(MPa)

Elongationin 2-inch(50 mm)

Reductionin Area

(%)

MODULUS OFELASTICITYAT 70_F (21_C) PSI (MPa)

TYPICALBRINELL

HARDNESS

170-95

(485-655)40 (275) 22 35

27.9E6(19.2E4)

137-187

270-95

(485-655)40 (275) 22 35

27.9E6(19.2E4)

137-187

357 (390)typical

42 (290)typical

37 typical 67 typical - - - 111

479 (545)typical

71 (490)typical

16 typical 52 typical - - - 163

5(1)135 (930)

typical115 (792)

typical22 typical 63 typical

29.9E6(20.6E4)

255

670-95

(485-655)

40 (275) 24 3527.9E6

(19.2E4)

137

770-95

(485-655)40 (275) 20 35

29.9E6(20.6E4)

147-200

(continued)


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198

Valve Materials Properties for PressureContaining Components (continued)(The material codes in this table correspond to the previous Standard


MATER-IALCODE

TYPICALBRINELLHARDNESS

MODULUS OF

ELASTICITYAT 70_F (21_C) PSI (MPa)


MATER-IALCODE


MODULUS OF


Reductionin Area

(%)


YieldStrengthksi

(MPa)

TensileStrengthksi

(MPa)

870-95

(485-655)40 (275) 20 35

29.9E6(20.6E4)

147-200

9 75 (515) 45(310) 20 3029.9E6

(20.6E4)156-207required

1090-115

(620-795)60 (415) 18 35

27.4E6(19.0E4)

176-255

11 75 (515) 30 (205) 30 4028.3E6

(19.3E4)150

12 70 (485) 25 (170) 30 4029.0E6

(20.0E4)149

13 70 (485) 25 (170) 30 4029.0E6

(20.0E4)149

14 70 (485) 25 (170) 30 4028.3E6

(19.3E4)150-170

15(2) 80 (551) 35 (240) 30 4028.3E6

(19.5E4)150

16 70 (485) 30 (205) 30 28.3E6

(19.5E4)163

17 75 (515) 35 (240) 25 28.3E6

(19.5E4)170

18 75 (515) 35 (240) 25 28.3E6

(19.5E4)170

19 70 (480) 40 (275) 16 4529.2E6

(20.1E4)223

20145

(1000)125 (860) 13 45

29E6(20.0E4)

302 min

21 95(665) 44(305) 35 50 29.0E6(20.0E4)

90 HRB

22 80(550) 38(260) 35 - - -29.0E6

(20.0E4)82 HRB

23 90(620) 65(450) 25 - - -30.5E6

(21.0E4)290 max

24 90(620) 65(450) 25 - - -30.5E6

(21.0E4)98 HRB

25(3) 31 (214) 13.4E6(9.2E4)

160-220

26(4) 41 (282) 13.4E6(9.2E4)

160-220

27 60 (415) 40 (276) 18 23E6

(16E4)143-187

28 58 (400) 30(205) 7

148-211

29 34 (234) 16(110) 24 14.0E6(9.7E4)

65

(continued)


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199

Valve Materials Properties for PressureContaining Components (continued)(The material codes in this table correspond to the previous Standard


MATER-IALCODE


MODULUS OF



MATER-IALCODE


MODULUS OF


Reductionin Area

(%)


YieldStrengthksi

(MPa)

TensileStrengthksi

(MPa)

30 40 (275) 18(124) 20 14.0

(9.7E4)75

31 65 (448) 25(172) 20 15.3E6

(10.5E4)98

32 75 (515) 30(205) 12 16E6

(11.0E4)150

33 85 (585) 35(240) 15 16E6

(11.0E4)120170

34 55 (380) 25(170) 10 14E6

(9.6E4)6080 HRB

required

35 60 (415) 27(186) 22 15.0E6

(10.3E4)131142

36 42 (290) 35(241) 10 9.9E6

(6.8E4)95

37(5)154

(1060)typical

93(638)typical

17 typical 30E6

(21E4)37 HRC

38 100 (689) 70(485) 20 26E6

(17.9E4)250325

39 65 (450) 25(170) 25 23E6

(15.8E4)110150

40 100 (689) 41(283) 40 29.8E6

(20.5E4)210

41 72 (496) 40(275) 20 30.8E6

(21.2E4)150185

42 110 (760) 51(350) 40 31.4E6

(21.7E4)238

43 76 (525) 40(275) 20 28.5E6

(19.7E4)180

1. Tempered (1200_F (650_C).2. Annealed.3. A126 Cl.B 1.125 in. (95 mm) dia bar.4. A126 Cl.C 1.125 in. (95 mm) dia bar.5. Wrought.


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200

PhysicalConstantsofHydrocarbons

BOILING

VAPOR

FREEZIN

G

CRITICAL

CONSTANTS

SPECIFICGRAVITY

AT14.

696PSIA

NO.

COMPOUND

FORMULA

MOLECUL

AR

WEIGHT

POINT

AT

14.696PSIA

(_F)

VAPOR

PRESSURE

AT100_

F

(PSIA)

POINTAT

14.696PSIA

(_F)

Critical

Temperature

(_F)

Critical

Pressure

(psia)

Liquid,(

3),(4)

60_F/60_F

Gasat

60_F

(Air=1)(1)

1 2 3 4 5

M

ethane

Ethane

Propane

n

Bu

tane

Is

obu

tane

CH4

C2

H6

C3

H8

C4

H10

C4

H10

16

.043

30

.070

44

.097

58

.124

58

.124

258

.69

127

.48

43

.67

31

.10

10

.90

(5000)(2)

(800)(2)

190

.

51

.6

72

.2

296

.46(5)

297

.89(5)

305

.84(5)

217

.05

255

.29

116

.63

90

.09

206

.01

305

.65

274

.98

667

.8

707

.8

616

.3

550

.7

529

.1

0.3

(8)

0.3

564(7)

0.5

077(7)

0.5

844(7)

0.5

631(7)

0.5

539

1.0

382

1.5

225

2.0

068

2.0

068

6 7 8

n

Pen

tane

Is

open

tane

N

eopen

tane

C5

H12

C5

H12

C5

H12

72

.151

72

.151

72

.151

96

.92

82

.12

49

.10

15

.570

20

.44

35

.9

201

.51

255

.83

2.1

7

385

.7

369

.10

321

.13

488

.6

490

.4

464

.0

0.6

310

0.6

247

0.5

967(7)

2.4

911

2.4

911

2.4

911

910

11

12

13

n

Hexane

2

Me

thy

lpen

tane

3

Me

thy

lpen

tane

N

eo

hexane

2,3

Dime

thy

lbu

tane

C6

H14

C6

H14

C6

H14

C6

H14

C6

H14

86

.178

86

.178

86

.178

86

.178

86

.178

155

.72

140

.47

145

.89

121

.52

136

.36

4.9

56

6.7

67

6.0

98

9.8

56

7.4

04

139

.58

244

.63

---

147

.72

199

.38

453

.7

435

.83

448

.3

420

.13

440

.29

436

.9

436

.6

453

.1

446

.8

453

.5

0.6

640

0.6

579

0.6

689

0.6

540

0.6

664

2.9

753

2.9

753

2.9

753

2.9

753

2.9

753

14

15

16

17

18

19

20

21

n

Hep

tane

2

Me

thy

lhexane

3

Me

thy

lhexane

3

Ethy

lpen

tane

2,2

Dime

thy

lpen

tane

2,4

Dime

thy

lpen

tane

3,3

Dime

thy

lpen

tane

Trip

tane

C7

H16

C7

H16

C7

H16

C7

H16

C7

H16

C7

H16

C7

H16

C7

H16

100

.205

100

.205

100

.205

100

.205

100

.205

100

.205

100

.205

100

.205

209

.17

194

.09

197

.32

200

.25

174

.54

176

.89

186

.91

177

.58

1.6

20

2.2

71

2.1

30

2.0

12

3.4

92

3.2

92

2.7

73

3.3

74

131

.05

180

.89

---

181

.48

190

.86

182

.63

210

.01

12

.82

512

.8

495

.00

503

.78

513

.48

477

.23

475

.95

505

.85

496

.44

396

.8

396

.5

408

.1

419

.3

402

.2

396

.9

427

.2

428

.4

0.6

882

0.6

830

0.6

917

0.7

028

0.6

782

0.6

773

0.6

976

0.6

946

3.4

596

3.4

596

3.4

596

3.4

596

3.4

596

3.4

596

3.4

596

3.4

596


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201

Phy

sicalConstantsofHydrocarbons(con

tinued)

NO.

SPECIFICGRAVITY

AT14.696PSIA

CRITICAL

CONSTANTS

FREEZIN

G

POINTAT

14.696PSIA

(_F)

VAPOR

PRESSURE

AT100_

F

(PSIA)

BOILING

POINT

AT

14.696PSIA

(_F)

MOLECUL

AR

WEIGHT

FORMULA

COMPOUND

NO.

Gasat

60_

F

(Air=1)(1)

Liquid,(

3),(4)

60_

F/60_F

Critical

Pressure

(psia)

Critical

Temperature

(_F)

FREEZIN

G

POINTAT

14.696PSIA

(_F)

VAPOR

PRESSURE

AT100_

F

(PSIA)

BOILING

POINT

AT

14.696PSIA

(_F)

MOLECUL

AR

WEIGHT

FORMULA

COMPOUND

22

23

24

25

26

27

28

29

30

nOctane

D

iisobutyl

Is

ooctane

nNonane

nDecane

C

yclopentane

M

ethylcyclopentane

C

yclohexane

M

ethylcyclohexane

C8H18

C8H18

C8H18

C9H20

C10H22

C5H10

C6H12

C6H12

C7H14

114.2

32

114.2

32

114.2

32

128.2

59

142.2

86

70.1

35

84.1

62

84.1

62

98.1

89

258.2

2

228.3

9

210.6

3

303.4

7

345.4

8

120.6

5

161.2

5

177.2

9

213.6

8

0.5

37

1.1

01

1.7

08

0.1

79

0.0

597

9.9

14

4.5

03

3.2

64

1.6

09

70.1

8

132.0

7

161.2

7

64.2

8

21.3

6

136.9

1

224.4

4

43.7

7

195.8

7

564.2

2

530.4

4

519.4

6

610.6

8

652.1

461.5

499.3

5

536.7

570.2

7

360.6

360.6

372.4

332.

304.

653.8

548.9

591.

503.5

0.7

068

0.6

979

0.6

962

0.7

217

0.7

342

0.7

504

0.7

536

0.7

834

0.7

740

3.9

439

3.9

439

3.9

439

4.4

282

4.9

125

2.4

215

2.9

057

2.9

057

3.3

900

31

32

33

34

35

36

37

38

39

40

Ethylene

Propene

1Butene

C

is2Butene

Trans2Butene

Is

obutene

1Pentene

1,2Butadiene

1,3Butadiene

Is

oprene

C2H4

C3H6

C4H8

C4H8

C4H8

C4H8

C5H10

C4H6

C4H6

C5H8

28.0

54

42.0

81

56.1

08

56.1

08

56.1

08

56.1

08

70.1

35

54.0

92

54.0

92

68.1

19

154.6

2

53.9

0

20.7

5

38.6

9

33.5

8

19.5

9

85.9

3

51.5

3

24.0

6

93.3

0

---

226.4

63.0

5

45.5

4

49.8

0

63.4

0

19.1

15

(20.)

(2)

(60.)

(2)

16.6

72

272.4

5(5)

301.4

5(5)

301.6

3(5)

218.0

6

157.9

6

220.6

1

265.3

9

213.1

6

164.0

2

230.7

4

48.5

8

196.9

295.6

324.3

7

311.8

6

292.5

5

376.9

3

(339.)

(2)

306.

(412.)

(2)

729.8

669.

583.

610.

595.

580.

590.

(653.)

(2)

628.

(558.4

)(2)

--- 0

.5220(7)

0.6

013(7)

0.6

271(7)

0.6

100(7)

0.6

004(7)

0.6

457

0.6

587

0.6

272(7)

0.6

861

0.9

686

1.4

529

1.9

372

1.9

372

1.9

372

1.9

372

2.4

215

1.8

676

1.8

676

2.3

519


12/93


202

Phy

sicalConstantsofHydrocarbons(con

tinued)

NO.

SPECIFICGRAVITY

AT14.696PSIA

CRITICAL

CONSTANTS

FREEZIN

G

POINTAT

14.696PSIA

(_F)

VAPOR

PRESSURE

AT100_

F

(PSIA)

BOILING

POINT

AT

14.696PSIA

(_F)

MOLECUL

AR

WEIGHT

FORMULA

COMPOUND

NO.

Gasat

60_

F

(Air=1)(1)

Liquid,(

3),(4)

60_

F/60_F

Critical

Pressure

(psia)

Critical

Temperature

(_F)

FREEZIN

G

POINTAT

14.696PSIA

(_F)

VAPOR

PRESSURE

AT100_

F

(PSIA)

BOILING

POINT

AT

14.696PSIA

(_F)

MOLECUL

AR

WEIGHT

FORMULA

COMPOUND

414243444546474849

Acetylene

Benzene

Toluene

Ethylbenzene

oXylene

m

Xylene

pXylene

Styrene

Is

opropylbenzene

C2H2

C6H6

C7H8

C8H10

C8H10

C8H10

C8H10

C8H8

C9H12

26.038

78.114

92.141

106.168

106.168

106.168

106.168

104.152

120.195

119.(

6)

176.17

231.13

277.16

291.97

282.41

281.05

293.29

306.34

--- 3

.224

1.032

0.371

0.264

0.326

0.342

(0.24)(2)

0.188

114(5)

41.96

138.94

138.91

13.30

54.12

55.86

23.10

140.82

95.31

552.22

605.55

651.24

675.0

651.02

649.6

706.0

676.4

890.4

710.4

595.9

523.5

541.4

513.6

509.2

580.

465.4

0.615(9)

0.8844

0.8718

0.8718

0.8848

0.8687

0.8657

0.9110

0.8663

0.8990

2.6969

3.1812

3.6655

3.6655

3.6655

3.6655

3.5959

4.1498

1.Calcu

latedvalues.

2.(

)E

stimatedvalues.

3.Airsa

turatedhydrocarbons.

4.Absolutevaluesfromweightsinvacuum.

5.Atsaturationpressure(triplepoint).

6.Sublim

ationpoint.

7.Saturationpressureand60_

F.

8.Apparentvalueformethaneat60_

F.

9.Specificgravity,119_

F/60_

F(sublimationpoint).

SpecificHeatRatio(k)

G

as

SpecificHeat

Ratio(k)

Gas

SpecificHeat

Ratio(k)

Gas

SpecificHeat

Ratio(k)

Gas

Sp

ecificHeat

Ratio(k)

Acetylen

e

AirArgon

Butane

CarbonMonoxide

1.38

1.40

1.67

1.17

1.40

CarbonDioxid

e

Ethane

Helium

Hydrogen

Methane

1.29

1.25

1.66

1.40

1.26

0.6NaturalGas

Nitrogen

Oxygen

Propane

Propylene

1.32

1.40

1.40

1.21

1.15

Steam(1)

1.33

1.Usep

ropertytablesifavailableforgreateraccuracy.


13/93


203

PhysicalConstantsofVariousFluids

BOILINGPOINT

VAPOR

CRITICAL

CRITICAL

SPECIFICGRAVITY

FLUID

FORMULA

MO

LECULAR

WEIGHT

BOILINGPOINT

(_FAT14.696

PSIA)

PRESSU

RE

@70_

F

(PSIG

)

CRITICAL

TEMP.

(_F)

CRITICAL

PRESSURE

(PSIA)

Liqu

id

60/60

_F

Gas

AceticAcid

HC2H3O2

60.0

5

245

1.05

Acetone

C3H6O

58.0

8

133

455

691

0.79

2.0

1

Air

N2O2

28.9

7

317

221

547

0.86

(3)

1.0

Alcohol,

Ethyl

C2H6O

46.0

7

173

2.3

(2)

470

925

0.79

4

1.5

9

Alcohol,

Methyl

CH4O

32.0

4

148

4.6

3(2

)

463

1174

0.79

6

1.1

1

Ammonia

NH3

17.0

3

28

114

270

1636

0.62

0.5

9

AmmoniumC

hloride(1)

NH4CI

1.07

AmmoniumH

ydroxide(1)

NH4OH

0.91

AmmoniumS

ulfate(1)

(NH4)2SO4

1.15

Aniline

C6H7N

93.1

2

365

798

770

1.02

Argon

A

39.9

4

302

188

705

1.65

1.3

8

Beer

1.01

Bromine

Br2

159.8

4

138

575

2.93

5.5

2

CalciumC

hloride(1)

CaCI2

1.23

CarbonDioxide

CO2

4

4.0

1

109

839

88

1072

0.80

1(3)

1.5

2

CarbonDisulfide

CS2

7

6.1

115

1.29

2.6

3

CarbonMonoxide

CO

2

8.0

1

314

220

507

0.80

0.9

7

CarbonTetrachloride

CCI4

15

3.8

4

170

542

661

1.59

5.3

1

Chlorine

CI2

7

0.9

1

30

85

291

1119

1.42

2.4

5

Chromic

Acid

H2CrO4

11

8.0

3

1.21

CitricAc

id

C6H8O7

19

2.1

2

1.54

CopperSulfate(1)

CuSO4

1.17

(continued)


14/93


204

PhysicalConstantsofVariousFluids(con

tinued)

FLUID

SPECIFICGRAVITY

CRITICAL

PRESSURE

(PSIA)

CRITICAL

TEMP.

(_F)

VAPOR

PRESSU

RE

@70_

F

(PSIG

)

BOILINGPOINT

(_FAT14.696

PSIA)

MO

LECULAR

WEIGHT

FORMULA

FLUID

Gas

Liqu

id

60/60

_

F

CRITICAL

PRESSURE

(PSIA)

CRITICAL

TEMP.

(_F)

VAPOR

PRESSU

RE

@70_

F

(PSIG

)

BOILINGPOINT

(_FAT14.696

PSIA)

MO

LECULAR

WEIGHT

FORMULA

Ether

(C2

H5

)2O

7

4.1

2

34

0.74

2.5

5

Ferr

icChlori

de

(1)

Fe

CI3

1.23

Fluorine

F2

3

8.0

0

305

300

200

809

1.11

1.3

1

Formalde

hy

de

H2

CO

3

0.0

3

6

0.82

1.0

8

Form

icA

cid

HCO2

H

4

6.0

3

214

1.23

Furfural

C5

H4

O2

9

6.0

8

324

1.16

Glycerine

C3

H8

O3

9

2.0

9

554

1.26

Glyco

l

C2

H6

O2

6

2.0

7

387

1.11

He

lium

He

4.0

03

454

450

33

0.18

0.1

4

Hy

droch

loric

Ac

id

HCI

3

6.4

7

115

1.64

Hy

dro

flu

oric

Ac

id

HF

2

0.0

1

66

0.9

446

0.92

Hy

droge

n

H2

2.0

16

422

400

188

0.07

(3)

0.0

7

Hy

droge

nChlori

de

HCI

3

6.4

7

115

613

125

1198

0.86

1.2

6

Hy

droge

nSu

lfide

H2

S

3

4.0

7

76

252

213

1307

0.79

1.1

7

Isopropy

lAlco

ho

l

C3

H8

O

6

0.0

9

180

0.78

2.0

8

Linseed

Oil

538

0.93

Manges

ium

Chlori

de

(1)

Mg

CI2

1.22

Mercury

Hg

20

0.6

1

670

13

.6

6.9

3

Me

thy

lB

rom

ide

CH3Br

9

4.9

5

38

13

376

1.73

3.2

7

Me

thy

lC

hlori

de

CH3

CI

5

0.4

9

11

59

290

969

0.99

1.7

4

Nap

htha

lene

C10

H8

12

8.1

6

424

1.14

4.4

3

Nitric

Ac

id

HNO3

6

3.0

2

187

1.5

(continued)


15/93


205

PhysicalConstantsofVariousFluids(con

tinued)

FLUID

SPECIFICGRAVITY

CRITICAL

PRESSURE

(PSIA)

CRITICAL

TEMP.

(_F)

VAPOR

PRESSU

RE

@70_

F

(PSIG

)

BOILINGPOINT

(_FAT14.696

PSIA)

MO

LECULAR

WEIGHT

FORMULA

FLUID

Gas

Liqu

id

60/60

_

F

CRITICAL

PRESSURE

(PSIA)

CRITICAL

TEMP.

(_F)

VAPOR

PRESSU

RE

@70_

F

(PSIG

)

BOILINGPOINT

(_FAT14.696

PSIA)

MO

LECULAR

WEIGHT

FORMULA

Nitrogen

N2

28.0

2

320

233

493

0.81

(3)

0.9

7

Oil,Vegetable

0.9

10

.94

Oxygen

O2

32

297

181

737

1.14

(3)

1.1

05

Phosgen

e

COCI2

98.9

2

47

10.7

360

823

1.39

3.4

2

Phospho

ricAcid

H3PO4

98.0

0

415

1.83

Potassiu

mCarbonate(1)

K2CO3

1.24

Potassiu

mChloride(1)

KCI

1.16

Potassiu

mHydroxide(1)

KOH

1.24

SodiumChloride(1)

NaCI

1.19

SodiumHydroxide(1)

NaOH

1.27

SodiumSulfate(1)

Na2SO4

1.24

SodiumThiosulfate(1)

Na2S2O3

1.23

Starch

(C6H10O5)x

1.50

SugarSolutions(1)

C12H22011

1.10

SulfuricAcid

H2SO4

98.0

8

626

1.83

SulfurDioxide

SO2

64.6

14

34.4

316

1145

1.39

2.2

1

Turpentine

320

0.87

Water

H2O

18.0

16

212

0.9492(2)

706

3208

1.00

0.6

2

ZincChloride(1)

ZnCI2

1.24

ZincSulfate(1)

ZnSO4

1.31

1.AqueousSolution

25%byweightofcompound.

2.Vaporpressureinpsiaat100_

F

3.Vaporpressureinpsia.


16/93


206

Refrigerant 717 (Ammonia)Properties of Liquid and Saturated Vapor

TEMP_

PRESSUREVOLUME

(CU.FT./LB.)

DENSITY(LB./CU.

FT.)

ENTHALPY(1)

(BTU/LB.)ENTROPY(1)

BTU/(LB.)(_R)

(_

F) psia psig VaporVg

LiquidI/vf

Liquidhf

Vaporhg

Liquidsf

Vaporsg

105104103102101

10099989796

9594939291

90

89888786

8584838281

8079787776

7574

73

7271

7069686766

656463626160

0.9961.0411.0871.1351.184

1.241.291.341.401.46

1.521.591.651.721.79

1.861.942.022.102.18

2.272.352.452.542.64

2.742.842.953.063.18

3.293.42

3.543.673.80

3.944.084.234.384.53

4.694.855.025.195.375.55

27.9(2)

27.8(2)

27.7(2)

27.6(2)

27.5(2)

27.4(2)

27.3(2)

27.2(2)

27.1(2)

26.9(2)

26.8(2)

26.7(2)

26.6(2)

26.4(2)

26.3(2)

26.1(2)26.0(2)

25.8(2)

25.6(2)

25.5(2)

25.3(2)

25.1(2)

24.9(2)

24.7(2)

24.5(2)

24.3(2)

24.1(2)

23.9(2)

23.7(2)

23.5(2)

23.2(2)

23.0(2)

22.7(2)22.4(2)

22.2(2)

21.9(2)

21.6(2)

21.3(2)

21.0(2)

20.7(2)

20.4(2)

20.0(2)

19.7(2)

19.4(2)

19.0(2)

18.6(2)

223.2214.2205.7197.6189.8

182.4175.3168.5162.1155.9

150.0144.3138.9133.8128.9

124.1119.6115.3111.1107.1

103.399.6896.1792.8189.59

86.5083.5480.6977.9675.33

72.8170.39

68.0665.8263.67

61.6059.6157.6955.8554.08

52.3750.7349.1447.6246.1544.73

45.7145.6745.6345.5945.55

45.5245.4745.4345.4045.36

45.3245.2845.2445.2045.16

45.1245.0845.0445.0044.96

44.9244.8844.8444.8044.76

44.7344.6844.6444.6044.56

44.5244.48

44.4444.4044.36

44.3244.2844.2444.1944.15

44.1144.0744.0343.9943.9543.91

68.567.566.465.464.3

63.362.261.260.159.1

58.057.055.954.953.8

52.8

51.750.749.648.6

47.546.545.444.443.3

42.241.240.139.138.0

37.035.9

34.9

33.832.8

31.730.729.628.627.5

26.525.424.423.322.221.2

570.3570.7571.2571.6572.1

572.5572.9573.4573.8574.3

574.7575.1575.6576.0576.5

576.9577.3577.8578.2578.6

579.1579.5579.9580.4580.8

581.2581.6582.1582.5582.9

583.3583.8

584.2584.6585.0

585.5585.9586.3586.7587.1

587.5588.0588.4588.8589.2589.6

0.1774.1774.1714.1685.1655

0.1626.1597.1568.1539.1510

0.1481.1452.1423.1395.1366

0.1338

.1309.1281.1253.1225

0.1197.1169.1141.1113.1085

0.1057.1030.1002.0975.0947

0.0920.0892

.0865

.0838.0811

0.0784.0757.0730.0703.0676

0.0650.0623.0596.0570.0543.0517

1.62431.62051.61671.61291.6092

1.60551.60181.59821.59451.5910

1.58741.58381.58031.57681.5734

1.56991.56651.56311.55971.5564

1.55311.54981.54651.54321.5400

1.53681.53361.53041.52731.5242

1.52111.5180

1.51491.51191.5089

1.50591.50291.49991.49701.4940

1.49111.48831.48541.48261.47971.4769

(continued)


17/93


207

Refrigerant 717 (Ammonia)Properties of Liquid and Saturated Vapor (continued)

TEMP(_F)

ENTROPY(1)

BTU/(LB.)(_R)ENTHALPY(1)

(BTU/LB.)

DENSITY(LB./CU.

FT.)

VOLUME(CU.

FT./LB.)PRESSURE

TEMP(_F)

Vaporsg

Liquidsf

Vaporhg

Liquidhf

LiquidI/vf

VaporVg

psigpsia

5958575655

5453525150

4948474645

44

43424140

3938373635

3433323130

2928

27

2625

2423222120

191817161514

5.745.936.136.336.54

6.756.977.207.437.67

7.918.168.428.688.95

9.239.519.8110.1010.41

10.7211.0411.3711.7112.05

12.4112.7713.1413.5213.90

14.3014.71

15.1215.5515.98

16.2416.8817.3417.8118.30

18.7919.3019.8120.3420.8821.43

18.2(2)

17.8(2)

17.4(2)

17.0(2)

16.6(2)

16.2(2)

15.7(2)

15.3(2)

14.8(2)

14.3(2)

13.8(2)

13.3(2)

12.8(2)

12.2(2)

11.7(2)

11.1(2)10.6(2)

10.0(2)

9.3(2)

8.7(2)

8.1(2)

7.4(2)

6.8(2)

6.1(2)

5.4(2)

4.7(2)

3.9(2)

3.2(2)

2.4(2)

1.6(2)

0.8(2)

0.0

0.40.81.3

1.72.22.63.13.6

4.14.65.15.66.26.7

43.3742.0540.7939.5638.38

37.2436.1535.0934.0633.08

32.1231.2030.3129.4528.62

27.8227.0426.2925.5624.86

24.1823.5322.8922.2721.68

21.1020.5420.0019.4818.97

18.4818.00

17.5417.0916.66

16.2415.8315.4315.0514.68

14.3213.9713.6213.2912.9712.66

43.8743.8343.7843.7443.70

43.6643.6243.5843.5443.49

43.4543.4143.3743.3343.28

43.2443.2043.1643.1243.08

43.0442.9942.9542.9042.86

42.8242.7842.7342.6942.65

42.6142.57

42.5442.4842.44

42.4042.3542.3142.2642.22

42.1842.1342.0942.0442.0041.96

20.119.118.017.015.9

14.813.812.711.710.6

9.68.57.46.45.3

4.3

3.22.11.10.0

1.12.13.24.35.3

6.47.48.59.610.7

11.712.8

13.914.916.0

17.118.119.220.321.4

22.423.524.625.626.727.8

590.0590.4590.8591.2591.6

592.1592.4592.9593.2593.7

594.0594.4594.9595.2595.6

596.0596.4596.8597.2597.6

598.0598.3598.7599.1599.5

599.9600.2600.6601.0601.4

601.7602.1

602.5602.8603.2

603.6603.9604.3604.6605.0

605.3605.7606.1606.4606.7607.1

0.0490.0464.0438.0412.0386

0.0360.0334.0307.0281.0256

0.0230.0204.0179.0153.0127

0.0102

.0076.0051.0025.0000

0.0025.0051.0076.0101.0126

0.0151.0176.0201.0226.0250

0.0275.0300

.0325.0350

.0374

0.0399.0423.0448.0472.0497

0.0521.0545.0570.0594.0618.0642

1.47411.47131.46861.46581.4631

1.46041.45771.45511.45241.4497

1.44711.44451.44191.43931.4368

1.43421.43171.42921.42671.4242

1.42171.41931.41691.41441.4120

1.40961.40721.40481.40251.4001

1.39781.3955

1.39321.39091.3886

1.38631.38401.38181.37961.3774

1.37521.37291.37081.36861.36641.3642

(continued)


18/93


208


TEMP(_F)

ENTROPY(1)


(BTU/LB.)

DENSITY(LB./CU.

FT.)

VOLUME(CU.

FT./LB.)PRESSURE

TEMP(_F)

Vaporsg

Liquidsf

Vaporhg

Liquidhf

LiquidI/vf

VaporVg

psigpsia

131211109

87654

32101

2345(3)

6

7891011

1213141516

1718

192021

2223242526

272829303132

21.9922.5623.1523.7424.35

24.9725.6126.2626.9227.59

28.2828.9829.6930.4231.16

31.9232.6933.4734.2735.09

35.9236.7737.6338.5139.40

40.3141.2442.1843.1444.12

45.1246.13

47.1648.2149.28

50.3651.4752.5953.7354.90

56.0857.2858.5059.7461.0062.29

7.37.98.59.09.7

10.310.911.612.212.9

13.614.315.015.716.5

17.218.018.819.620.4

21.222.122.923.824.7

25.626.527.528.429.4

30.431.4

32.533.534.6

35.736.837.939.040.2

41.442.643.845.046.347.6

12.3612.0611.7811.5011.23

10.9710.7110.4710.239.991

9.7639.5419.3269.1168.912

8.7148.5218.3338.1507.971

7.7987.6297.4647.3047.148

6.9966.8476.7036.5626.425

6.2916.161

6.0345.9105.789

5.6715.5565.4435.3345.227

5.1235.0214.9224.8254.7304.637

41.9141.8741.8241.7841.74

41.6941.6541.6041.5641.52

41.4741.4341.3841.3441.29

41.2541.2041.1641.1141.07

41.0140.9840.9340.8940.84

40.8040.7540.7140.6640.61

40.5740.52

40.4840.4340.38

40.3440.2940.2540.2040.15

40.1040.0640.0139.9639.9139.86

28.930.031.032.133.2

34.335.436.437.538.6

39.740.741.842.944.0

45.146.247.248.349.4

50.551.652.753.854.9

56.057.158.259.260.3

61.462.5

63.664.765.8

66.968.069.170.271.3

72.473.574.675.776.877.9

607.5607.8608.1608.5608.8

609.2609.5609.8610.1610.5

610.8611.1611.4611.8612.1

612.4612.7613.0613.3613.6

613.9614.3614.6614.9615.2

615.5615.8616.1616.3616.6

616.9617.2

617.5617.8618.0

618.3618.6618.9619.1619.4

619.7619.9620.2620.5620.7621.0

0.0666.0690.0714.0738.0762

0.0786.0809.0833.0857.0880

0.0909.0928.0951.0975.0998

0.1022.1045.1069.1092.1115

0.1138.1162.1185.1208.1231

0.1254.1277.1300.1323.1346

0.1369.1392

.1415.1437

.1460

0.1483.1505.1528.1551.1573

0.1596.1618.1641.1663.1686.1708

1.36241.36001.35791.35581.3537

1.35161.34931.34741.34541.3433

1.34131.33931.33721.33521.3332

1.33121.32921.32731.32531.3234

1.32141.31951.31761.31571.3137

1.31181.30991.30811.30621.3043

1.30251.3006

1.29881.29691.2951

1.29331.29151.28971.28791.2861

1.28431.28231.28091.27901.27731.2755

(continued)


19/93


209


TEMP(_F)

ENTROPY(1)


(BTU/LB.)

DENSITY(LB./CU.

FT.)

VOLUME(CU.

FT./LB.)PRESSURE

TEMP(_F)

Vaporsg

Liquidsf

Vaporhg

Liquidhf

LiquidI/vf

VaporVg

psigpsia

3334353637

3839404142

4344454647

4849505152

5354555657

5859606162

6364

656667

6869707172

737475767778

63.5964.9166.2667.6369.02

70.4371.8773.3274.8076.31

77.8379.3880.9682.5584.18

85.8287.4989.1990.9192.66

94.4396.2398.0699.91101.8

103.7105.6107.6109.6111.6

113.6115.7

117.8120.0122.1

124.3126.5128.8131.1133.4

135.7138.1140.5143.0145.4147.9

48.950.251.652.954.3

55.757.258.660.161.6

63.164.766.367.969.5

71.172.874.576.278.0

79.781.583.485.287.1

89.090.992.994.996.9

98.9101.0

103.1105.3107.4

109.6111.8114.1116.4118.7

121.0123.4125.8128.3130.7133.2

4.5474.4594.3734.2894.207

4.1264.0483.9713.8973.823

3.7523.6823.6143.5473.481

3.4183.3553.2943.2343.176

3.1193.0633.0082.9542.902

2.8512.8002.7512.7032.656

2.6102.565

2.5202.4772.435

2.3932.3522.3122.2732.235

2.1972.1612.1252.0892.0552.021

39.8239.7739.7239.6739.63

39.5839.5439.4939.4439.39

39.3439.2939.2439.1939.14

39.1039.0539.0038.9538.90

38.8538.8038.7538.7038.65

38.6038.5538.5038.4538.40

38.3538.30

38.2538.2038.15

38.1038.0538.0037.9537.90

37.8437.7937.7437.6937.6437.58

79.080.181.282.383.4

84.685.786.887.989.0

90.191.292.393.594.6

95.796.897.999.1100.2

101.3102.4103.5104.7105.8

106.9108.1109.2110.3111.5

112.6113.7

114.8116.0117.1

118.3119.4120.5121.7122.8

124.0125.1126.2127.4128.5129.7

621.2621.5621.7622.0622.2

622.5622.7623.0623.2623.4

623.7623.9624.1624.4624.6

624.8625.0625.2625.5625.7

625.9626.1626.3626.5626.7

626.9627.1627.3627.5627.7

627.9628.0

628.2628.4628.6

628.8628.9629.1629.3629.4

629.6629.8629.9630.1630.2630.4

0.1730.1753.1775.1797.1819

0.1841.1863.1885.1908.1930

0.1952.1974.1996.2018.2040

0.2062.2083.2105.2127.2149

0.2171.2192.2214.2236.2257

0.2279.2301.2322.2344.2365

0.2387.2408

.2430.2451

.2473

0.2494.2515.2537.2558.2579

0.2601.2622.2643.2664.2685.2706

1.27381.27211.27041.26861.2669

1.26521.26351.26181.26021.2585

1.25681.25521.25351.25181.2492

1.24841.24691.24531.24371.2421

1.24051.23821.23721.23571.2341

1.23251.23101.22941.22731.2263

1.22471.2231

1.22131.22011.2183

1.21791.21551.21401.21251.2110

1.20951.20801.20651.20501.20351.2020

(continued)


20/93


210


TEMP(_F)

ENTROPY(1)


(BTU/LB.)

DENSITY(LB./CU.

FT.)

VOLUME(CU.

FT./LB.)PRESSURE

TEMP(_F)

Vaporsg

Liquidsf

Vaporhg

Liquidhf

LiquidI/vf

VaporVg

psigpsia

7980818283

848586(3)

8788

8990919293

9495969798

99100101102103

104105106107108

109110

111112113

114115116117118119

120121122123124125

150.5153.0155.6158.3161.0

163.7166.4169.2172.0174.8

177.7180.6183.6186.6189.6

192.7195.8198.9202.1205.3

208.6211.9215.2218.6222.0

225.4228.9232.5236.0239.7

243.3247.0

250.8254.5258.4

262.2266.2270.1274.1278.2282.3

286.4290.6294.8299.1303.4307.8

135.8138.3140.9143.6146.3

149.0151.7154.5157.3160.1

163.0165.9168.9171.9174.9

178.0181.1184.2187.4190.6

193.9197.2200.5203.9207.3

210.7214.2217.8221.3225.0

228.6232.3

236.1239.8243.7

247.5251.5255.4259.4263.5267.6

271.7275.9280.1284.4288.7293.1

1.9881.9551.9231.8921.861

1.8311.8011.7721.7441.716

1.6881.6611.6351.6091.584

1.5591.5341.5101.4871.464

1.4411.4191.3971.3751.354

1.3341.3131.2931.2741.254

1.2351.217

1.1981.1801.163

1.1451.1281.1121.0951.0791.063

1.0471.0321.0171.0020.9870.973

37.5337.4837.4337.3737.32

37.2637.2137.1637.1137.05

37.0036.9536.8936.8436.78

36.7336.6736.6236.5636.51

36.4536.4036.3436.2936.23

36.1836.1236.0636.0135.95

35.9035.84

35.7835.7235.67

35.6135.5535.4935.4335.3835.32

35.2635.2035.1435.0835.0234.96

130.8132.0133.1134.3135.4

136.6137.8138.9140.1141.2

142.4143.5144.7145.8147.0

148.2149.4150.5151.7152.9

154.0155.2156.4157.6158.7

159.9161.1162.3163.5164.6

165.8167.0

168.2169.4170.6

171.8173.0174.2175.4176.6177.8

179.0180.2181.4182.6183.9185.1

630.5630.7630.8631.0631.1

631.3631.4631.5631.7631.8

631.9632.0632.1632.2632.3

632.5632.6632.6632.8632.9

632.9633.0633.1633.2633.3

633.4633.4633.5633.6633.6

633.7633.7

633.8633.8633.9

633.9633.9634.0634.0634.0634.0

634.0634.0634.0634.0634.0634.0

0.2728.2749.2769.2791.2812

0.2833.2854.2875.2895.2917

0.2937.2958.2979.3000.3021

0.3041.3062.3083.3104.3125

0.3145.3166.3187.3207.3228

0.3248.3269.3289.3310.3330

0.3351.3372

.3392.3413

.3433

0.3453.3474.3495.3515.35353556

0.3576.3597.3618.3638.3659.3679

1.20061.19911.19761.19621.1947

1.19331.19181.19041.18891.1875

1.18601.18461.18321.18181.1804

1.17891.17751.17611.17471.1733

1.17191.17051.16911.16771.1663

1.16491.16351.16211.16071.1593

1.15801.1566

1.15521.15381.1524

1.15101.14971.14831.14691.14551.1441

1.14271.14141.14001.13861.13721.1358

1. Based on 0 for the saturated liquid at 40_F.2. Inches of mercury below one standard atmosphere.3. Standard cycle temperatures.


21/93


211

Properties of Water

Temperature(_F)

SaturationPressure

(Pounds PerSquare Inch

Absolute)

Weight(Pounds Per

Gallon)

SpecificGravity60/60 _F

ConversionFactor,(1)

lbs./hr.

to GPM

32 .0885 8.345 1.0013 .00199

40 .1217 8.345 1.0013 .00199

50 .1781 8.340 1.0007 .00199

60 .2653 8.334 1.0000 .00199

70 .3631 8.325 .9989 .00200

80 .5069 8.314 .9976 .00200

90 .6982 8.303 .9963 .00200

100 .9492 8.289 .9946 .00201

110 1.2748 8.267 .9919 .00201

120 1.6924 8.253 .9901 .00201

130 2.2225 8.227 .9872 .00202

140 2.8886 8.207 .9848 .00203

150 3.718 8.182 .9818 .00203

160 4.741 8.156 .9786 .00204

170 5.992 8.127 .9752 .00205

180 7.510 8.098 .9717 .00205

190 9.339 8.068 .9681 .00206

200 11.526 8.039 .9646 .00207

210 14.123 8.005 .9605 .00208

212 14.696 7.996 .9594 .00208

220 17.186 7.972 .9566 .00209

240 24.969 7.901 .9480 .00210

260 35.429 7.822 .9386 .00211

280 49.203 7.746 .9294 .00215

300 67.013 7.662 .9194 .00217

350 134.63 7.432 .8918 .00224

400 247.31 7.172 .8606 .00232

450 422.6 6.892 .8270 .00241

500 680.8 6.553 .7863 .00254

550 1045.2 6.132 .7358 .00271

600 1542.9 5.664 .6796 .00294

700 3093.7 3.623 .4347 .00460

1. Multiply flow in pounds per hour by the factor to get equivalent flow in gallons per minute.Weight per gallon is based on 7.48 gallons per cubic foot.


22/93


212

Properties of Saturated Steam

ABSOLUTEPRESSURE VACUUM

TEMPER HEATLATENT

HEATTOTALHEAT

SPECIFICVOLUME

Lbs Per

Sq In.P

Inchesof Hg

VACUUM(INCHES

OF Hg)

ATUREt

(_F)

OF THELIQUID

(BTU/LB)

OFEVAPOR

ATION(BTU/LB)

OFSTEAM

Hg(BTU/LB)

VOLUME

r

(CU FTPER LB)

0.20

0.25

0.30

0.35

0.40

0.45

0.50

0.60

0.70

0.80

0.90

1.0

1.2

1.4

1.6

1.8

2.0

2.2

2.4

2.6

2.8

3.0

3.5

4.0

4.5

5.0

5.5

6.0

6.5

7.0

7.5

8.0

8.5

9.0

9.5

10.0

11.0

12.0

13.0

14.0

0.41

0.51

0.61

0.71

0.81

0.92

1.02

1.22

1.43

1.63

1.83

2.04

2.44

2.85

3.26

3.66

4.07

4.48

4.89

5.29

5.70

6.11

7.13

8.14

9.16

10.18

11.20

12.22

13.23

14.25

15.27

16.29

17.31

18.32

19.34

20.36

22.40

24.43

26.47

28.50

29.51

29.41

29.31

29.21

29.11

29.00

28.90

28.70

28.49

28.29

28.09

27.88

27.48

27.07

26.66

26.26

25.85

25.44

25.03

24.63

24.22

23.81

22.79

21.78

20.76

19.74

18.72

17.70

16.69

15.67

14.65

13.63

12.61

11.60

10.58

9.56

7.52

5.49

3.45

1.42

53.14

59.30

64.47

68.93

72.86

76.38

79.58

85.21

90.08

94.38

98.24

101.74

107.92

113.26

117.99

122.23

126.08

129.62

132.89

135.94

138.79

141.48

147.57

152.97

157.83

162.24

166.30

170.06

173.56

176.85

179.94

182.86

185.64

188.28

190.80

193.21

197.75

201.96

205.88

209.56

21.21

27.36

32.52

36.97

40.89

44.41

47.60

53.21

58.07

62.36

66.21

69.70

75.87

81.20

85.91

90.14

93.99

97.52

100.79

103.83

106.68

109.37

115.46

120.86

125.71

130.13

134.19

137.96

141.47

144.76

147.86

150.79

153.57

156.22

158.75

161.17

165.73

169.96

173.91

177.61

1063.8

1060.3

1057.4

1054.9

1052.7

1050.7

1048.8

1045.7

1042.9

1040.4

1038.3

1036.3

1032.7

1029.6

1026.9

1024.5

1022.2

1020.2

1018.3

1016.5

1014.8

1013.2

1009.6

1006.4

1003.6

1001.0

998.5

996.2

994.1

992.1

990.2

988.5

986.8

985.2

983.6

982.1

979.3

976.6

974.2

971.9

1085.0

1087.7

1090.0

1091.9

1093.6

1095.1

1096.4

1098.9

1101.0

1102.8

1104.5

1106.0

1108.6

1110.8

1112.8

1114.6

1116.2

1117.7

1119.1

1120.3

1121.5

1122.6

1125.1

1127.3

1129.3

1131.1

1132.7

1134.2

1135.6

1136.9

1138.1

1139.3

1140.4

1141.4

1142.3

1143.3

1145.0

1146.6

1148.1

1149.5

1526.0

1235.3

1039.5

898.5

791.9

708.5

641.4

540.0

466.9

411.7

368.4

333.6

280.9

243.0

214.3

191.8

173.73

158.85

146.38

135.78

126.65

118.71

102.72

90.63

81.16

73.52

67.24

61.98

57.50

53.64

50.29

47.34

44.73

42.40

40.31

38.42

35.14

32.40

30.06

28.04


23/93


213

Properties of Saturated Steam

PRESSURE(LBS. PER SQ IN.)

TEMPER

ATURE

HEAT OF

THE

LATENT

HEAT OFEVAPOR

TOTAL

HEAT OF

SPECIFIC

VOLUME

Absolute P Gauge Pt

(_

F)

LIQUID(BTU/LB)

EVAPOR

ATION

(BTU/LB)

STEAM Hg(BTU/LB)

(CU FT

PER LB)14.696

15.0

16.0

17.0

18.0

19.0

20.0

21.0

22.0

23.0

24.0

25.0

26.0

27.0

28.0

29.0

30.0

31.0

32.0

33.0

34.0

35.0

36.0

37.0

38.0

39.0

40.0

41.0

42.0

43.0

44.0

45.0

46.0

47.0

48.0

49.0

50.0

51.0

52.0

53.0

54.0

0.0

0.3

1.3

2.3

3.3

4.3

5.3

6.3

7.3

8.3

9.3

10.3

11.3

12.3

13.3

14.3

15.3

16.3

17.3

18.3

19.3

20.3

21.3

22.3

23.3

24.3

25.3

26.3

27.3

28.3

29.3

30.3

31.3

32.3

33.3

34.3

35.3

36.3

37.3

38.3

39.3

212.00

213.03

216.32

219.44

222.41

225.24

227.96

230.57

233.07

235.49

237.82

240.07

242.25

244.36

246.41

248.40

250.33

252.22

254.05

255.84

257.58

259.28

260.95

262.57

264.16

265.72

267.25

268.74

270.21

271.64

273.05

274.44

275.80

277.13

278.45

279.74

281.01

282.26

283.49

284.70

285.90

180.07

181.11

184.42

187.56

190.56

193.42

196.16

198.79

201.33

203.78

206.14

208.42

210.62

212.75

214.83

216.86

218.82

220.73

222.59

224.41

226.18

227.91

229.60

231.26

232.89

234.48

236.03

237.55

239.04

240.51

241.95

243.36

244.75

246.12

247.47

248.79

250.09

251.37

252.63

253.87

255.09

970.3

969.7

967.6

965.5

963.6

961.9

960.1

958.4

956.8

955.2

953.7

952.1

950.7

949.3

947.9

946.5

945.3

944.0

942.8

941.6

940.3

939.2

938.0

936.9

935.8

934.7

933.7

932.6

931.6

930.6

929.6

928.6

927.7

926.7

925.8

924.9

924.0

923.0

922.2

921.3

920.5

1150.4

1150.8

1152.0

1153.1

1154.2

1155.3

1156.3

1157.2

1158.1

1159.0

1159.8

1160.6

1161.3

1162.0

1162.7

1163.4

1164.1

1164.7

1165.4

1166.0

1166.5

1167.1

1167.6

1168.2

1168.7

1169.2

1169.7

1170.2

1170.7

1171.1

1171.6

1172.0

1172.4

1172.9

1173.3

1173.7

1174.1

1174.4

1174.8

1175.2

1175.6

26.80

26.29

24.75

23.39

22.17

21.08

20.089

19.192

18.375

17.627

16.938

16.303

15.715

15.170

14.663

14.189

13.746

13.330

12.940

12.572

12.226

11.898

11.588

11.294

11.015

10.750

10.498

10.258

10.029

9.810

9.601

9.401

9.209

9.025

8.848

8.678

8.515

8.359

8.208

8.062

7.922

(continued)


24/93


214

Properties of Saturated Steam (continued)

PRESSURE

(LBS. PER SQ IN.)SPECIFIC

VOLUMEr

(CU FT

PER LB)

TOTAL

HEAT OFSTEAM Hg(BTU/LB)

LATENTHEAT OF

EVAPOR

ATION

(BTU/LB)

HEAT OF

THELIQUID

(BTU/LB)

TEMPER

ATUREt

(_

F)Absolute P

SPECIFIC

VOLUMEr

(CU FT

PER LB)

TOTAL


LATENTHEAT OF

EVAPOR

ATION

(BTU/LB)

HEAT OF

THELIQUID

(BTU/LB)

TEMPER

ATUREt

(_

F)Gauge P

55.0

56.0

57.0

58.0

59.0

60.0

61.0

62.0

63.0

64.0

65.0

66.0

67.0

68.0

69.0

70.0

71.0

72.0

73.0

74.0

75.0

76.0

77.0

78.0

79.0

80.0

81.0

82.0

83.0

84.0

85.0

86.0

87.0

88.0

89.0

90.0

91.0

92.0

93.0

94.0

95.0

96.0

97.0

98.0

99.0

40.3

41.3

42.3

43.3

44.3

45.3

46.3

47.3

48.3

49.3

50.3

51.3

52.3

53.3

54.3

55.3

56.3

57.3

58.3

59.3

60.3

61.3

62.3

63.3

64.3

65.3

66.3

67.3

68.3

69.3

70.3

71.3

72.3

73.3

74.3

75.3

76.3

77.3

78.3

79.3

80.3

81.3

82.3

83.3

84.3

287.07

288.23

289.37

290.50

291.61

292.71

293.79

294.85

295.90

296.94

297.97

298.99

299.99

300.98

301.96

302.92

303.88

304.83

305.76

306.68

307.60

308.50

309.40

310.29

311.16

312.03

312.89

313.74

314.59

315.42

316.25

317.07

317.88

318.68

319.48

320.27

321.06

321.83

322.60

323.36

324.12

324.87

325.61

326.35

327.08

256.30

257.50

258.67

259.82

260.96

262.09

263.20

264.30

265.38

266.45

267.50

268.55

269.58

270.60

291.61

272.61

273.60

274.57

275.54

276.49

277.43

278.37

279.30

280.21

281.12

282.02

282.91

283.79

284.66

285.53

286.39

287.24

288.08

288.91

289.74

290.56

291.38

292.18

292.98

293.78

294.56

295.34

296.12

296.89

297.65

919.6

918.8

917.9

917.1

916.3

915.5

914.7

913.9

913.1

912.3

911.6

910.8

910.1

909.4

908.7

907.9

907.2

906.5

905.8

905.1

904.5

903.7

903.1

902.4

901.7

901.1

900.4

899.7

899.1

898.5

897.8

897.2

896.5

895.9

895.3

894.7

894.1

893.5

892.9

892.3

891.7

891.1

890.5

889.9

889.4

1175.9

1176.3

1176.6

1176.9

1177.3

1177.6

1177.9

1178.2

1178.5

1178.8

1179.1

1179.4

1179.7

1180.0

1180.3

1180.6

1180.8

1181.1

1181.3

1181.6

1181.9

1182.1

1182.4

1182.6

1182.8

1183.1

1183.3

1183.5

1183.8

1184.0

1184.2

1184.4

1184.6

1184.8

1185.1

1185.3

1185.5

1185.7

1185.9

1186.1

1186.2

1186.4

1186.6

1186.8

1187.0

7.787

7.656

7.529

7.407

7.289

7.175

7.064

6.957

6.853

6.752

6.655

6.560

6.468

6.378

6.291

6.206

6.124

6.044

5.966

5.890

5.816

5.743

5.673

5.604

5.537

5.472

5.408

5.346

5.285

5.226

5.168

5.111

5.055

5.001

4.948

4.896

4.845

4.796

4.747

4.699

4.652

4.606

4.561

4.517

4.474

(continued)


25/93


215


PRESSURE


VOLUMEr

(CU FT

PER LB)

TOTAL


LATENTHEAT OF

EVAPOR

ATION

(BTU/LB)

HEAT OF

THELIQUID

(BTU/LB)

TEMPER

ATUREt

(_

F)Absolute P

SPECIFIC

VOLUMEr

(CU FT

PER LB)

TOTAL


LATENTHEAT OF

EVAPOR

ATION

(BTU/LB)

HEAT OF

THELIQUID

(BTU/LB)

TEMPER

ATUREt

(_

F)Gauge P

100.0

101.0

102.0

103.0

104.0

105.0

106.0

107.0

108.0

109.0

110.0

111.0

112.0

113.0

114.0

115.0

116.0

117.0

118.0

119.0

120.0

121.0

122.0

123.0

124.0

125.0

126.0

127.0

128.0

129.0

130.0

131.0

132.0

133.0

134.0

135.0

136.0

137.0

138.0

139.0

140.0

141.0

142.0

143.0

144.0

85.3

86.3

87.3

88.3

89.3

90.3

91.3

92.3

93.3

94.3

95.3

96.3

97.3

98.3

99.3

100.3

101.3

102.3

103.3

104.3

105.3

106.3

107.3

108.3

109.3

110.3

111.3

112.3

113.3

114.3

115.3

116.3

117.3

118.3

119.3

120.3

121.3

122.3

123.3

124.3

125.3

126.3

127.3

128.3

129.3

327.81

328.53

329.25

329.96

330.66

331.36

332.05

332.74

333.42

334.10

334.77

335.44

336.11

336.77

337.42

338.07

338.72

339.36

339.99

340.62

341.25

341.88

342.50

343.11

343.72

344.33

344.94

345.54

346.13

346.73

347.32

347.90

348.48

349.06

349.64

350.21

350.78

351.35

351.91

352.47

353.02

353.57

354.12

354.67

355.21

298.40

299.15

299.90

300.64

301.37

302.10

302.82

303.54

304.26

304.97

305.66

306.37

307.06

307.75

308.43

309.11

309.79

310.46

311.12

311.78

312.44

313.10

313.75

314.40

315.04

315.68

316.31

316.94

317.57

318.19

318.81

319.43

320.04

320.65

321.25

321.85

322.45

323.05

323.64

324.23

324.82

325.40

325.98

326.56

327.13

888.8

888.2

887.6

887.1

886.5

886.0

885.4

884.9

884.3

883.7

883.2

882.6

882.1

881.6

881.1

880.6

880.0

879.5

879.0

878.4

877.9

877.4

876.9

876.4

875.9

875.4

874.9

874.4

873.9

873.4

872.9

872.5

872.0

871.5

871.0

870.6

870.1

869.6

869.1

868.7

868.2

867.7

867.2

866.7

866.3

1187.2

1187.4

1187.5

1187.7

1187.9

1188.1

1188.2

1188.4

1188.6

1188.7

1188.9

1189.0

1189.2

1189.4

1189.5

1189.7

1189.8

1190.0

1190.1

1190.2

1190.4

1190.5

1190.7

1190.8

1190.9

1191.1

1191.2

1191.3

1191.5

1191.6

1191.7

1191.9

1192.0

1192.1

1192.2

1192.4

1192.5

1192.6

1192.7

1192.9

1193.0

1193.1

1193.2

1193.3

1193.4

4.432

4.391

4.350

4.310

4.271

4.232

4.194

4.157

4.120

4.084

4.049

4.015

3.981

3.947

3.914

3.882

3.850

3.819

3.788

3.758

3.728

3.699

3.670

3.642

3.614

3.587

3.560

3.533

3.507

3.481

3.455

3.430

3.405

3.381

3.357

3.333

3.310

3.287

3.264

3.242

3.220

3.198

3.177

3.155

3.134

(continued)


26/93


216


PRESSURE


VOLUMEr

(CU FT

PER LB)

TOTAL


LATENTHEAT OF

EVAPOR

ATION

(BTU/LB)

HEAT OF

THELIQUID

(BTU/LB)

TEMPER

ATUREt

(_

F)Absolute P

SPECIFIC

VOLUMEr

(CU FT

PER LB)

TOTAL


LATENTHEAT OF

EVAPOR

ATION

(BTU/LB)

HEAT OF

THELIQUID

(BTU/LB)

TEMPER

ATUREt

(_

F)Gauge P

145.0

146.0

147.0

148.0

149.0

150.0

152.0

154.0

156.0

158.0

160.0

162.0

164.0

166.0

168.0

170.0

172.0

174.0

176.0

178.0

180.0

182.0

184.0

186.0

188.0

190.0

192.0

194.0

196.0

198.0

200.0

205.0

210.0

215.0

220.0

225.0

230.0

235.0

240.0

245.0

250.0

255.0

260.0

265.0

270.0

130.3

131.3

132.3

133.3

134.3

135.3

137.3

139.3

141.3

143.3

145.3

147.3

149.3

151.3

153.3

155.3

157.3

159.3

161.3

163.3

165.3

167.3

169.3

171.3

173.3

175.3

177.3

179.3

181.3

183.3

185.3

190.3

195.3

200.3

205.3

210.3

215.3

220.3

225.3

230.3

235.3

240.3

245.3

250.3

255.3

355.76

356.29

356.83

357.36

357.89

358.42

359.46

360.49

361.52

362.53

363.53

364.53

365.51

366.48

367.45

368.41

369.35

370.29

371.22

372.14

373.06

373.96

374.86

375.75

376.64

377.51

378.38

379.24

380.10

380.95

381.79

383.86

385.90

387.89

389.86

391.79

393.68

395.54

397.37

399.18

400.95

402.70

404.42

406.11

407.78

327.70

328.27

328.83

329.39

329.95

330.51

331.61

332.70

333.79

334.86

335.93

336.98

338.02

339.05

340.07

341.09

342.10

343.10

344.09

345.06

346.03

347.00

347.96

348.92

349.86

350.79

351.72

352.64

353.55

354.46

355.36

357.58

359.77

361.91

364.02

366.09

368.13

370.14

372.12

374.08

376.00

377.89

379.76

381.60

383.42

865.8

865.3

864.9

864.5

864.0

863.6

862.7

861.8

860.9

860.0

859.2

858.3

857.5

856.6

855.7

854.9

854.1

853.3

852.4

851.6

850.8

850.0

849.2

848.4

847.6

846.8

846.1

845.3

844.5

843.7

843.0

841.1

839.2

837.4

835.6

833.8

832.0

830.3

828.5

826.8

825.1

823.4

821.8

820.1

818.5

1193.5

1193.6

1193.8

1193.9

1194.0

1194.1

1194.3

1194.5

1194.7

1194.9

1195.1

1195.3

1195.5

1195.7

1195.8

1196.0

1196.2

1196.4

1196.5

1196.7

1196.9

1197.0

1197.2

1197.3

1197.5

1197.6

1197.8

1197.9

1198.1

1198.2

1198.4

1198.7

1199.0

1199.3

1199.6

1199.9

1200.1

1200.4

1200.6

1200.9

1201.1

1201.3

1201.5

1201.7

1201.9

3.114

3.094

3.074

3.054

3.034

3.015

2.977

2.940

2.904

2.869

2.834

2.801

2.768

2.736

2.705

2.675

2.645

2.616

2.587

2.559

2.532

2.505

2.479

2.454

2.429

2.404

2.380

2.356

2.333

2.310

2.288

2.234

2.183

2.134

2.087

2.0422

1.9992

1.9579

1.9183

1.8803

1.8438

1.8086

1.7748

1.7422

1.7107

(continued)


27/93


217


PRESSURE


VOLUMEr

(CU FT

PER LB)

TOTAL


LATENTHEAT OF

EVAPOR

ATION

(BTU/LB)

HEAT OF

THELIQUID

(BTU/LB)

TEMPER

ATUREt

(_

F)Absolute P

SPECIFIC

VOLUMEr

(CU FT

PER LB)

TOTAL


LATENTHEAT OF

EVAPOR

ATION

(BTU/LB)

HEAT OF

THELIQUID

(BTU/LB)

TEMPER

ATUREt

(_

F)Gauge P

275.0

280.0

285.0

290.0

295.0

300.0

320.0

340.0

360.0

380.0

400.0

420.0

440.0

460.0

480.0

500.0

520.0

540.0

560.0

580.0

600.0

620.0

640.0

660.0

680.0

700.0

720.0

740.0

760.0

780.0

800.0

820.0

840.0

860.0

880.0

900.0

920.0

940.0

960.0

980.0

1000.0

1050.0

1100.0

1150.0

1200.0

260.3

265.3

270.3

275.3

280.3

285.3

305.3

325.3

345.3

365.3

385.3

405.3

425.3

445.3

465.3

485.3

505.3

525.3

545.3

565.3

585.3

605.3

625.3

645.3

665.3

685.3

705.3

725.3

745.3

765.3

785.3

805.3

825.3

845.3

865.3

885.3

905.3

925.3

945.3

965.3

985.3

1035.3

1085.3

1135.3

1185.3

409.43

411.05

412.65

414.23

415.79

417.33

423.29

428.97

434.40

439.60

444.59

449.39

454.02

458.50

462.82

467.01

471.07

475.01

478.85

482.58

486.21

489.75

493.21

496.58

499.88

503.10

506.25

509.34

512.36

515.33

518.23

521.08

523.88

526.63

529.33

531.98

534.59

537.16

539.68

542.17

544.61

550.57

556.31

561.86

567.22

385.21

386.98

388.73

390.46

392.16

393.84

400.39

406.66

412.67

418.45

424.0

429.4

434.6

439.7

444.6

449.4

454.1

458.6

463.0

467.4

471.6

475.7

479.8

483.8

487.7

491.5

495.3

499.0

502.6

506.2

509.7

513.2

516.6

520.0

523.3

526.6

529.8

533.0

536.2

539.3

542.4

550.0

557.4

564.6

571.7

816.9

815.3

813.7

812.1

810.5

809.0

803.0

797.1

791.4

785.8

780.5

775.2

770.0

764.9

759.9

755.0

750.1

745.4

740.8

736.1

731.6

727.2

722.7

718.3

714.0

709.7

705.4

701.2

697.1

692.9

688.9

684.8

680.8

676.8

672.8

668.8

664.9

661.0

657.1

653.3

649.4

639.9

630.4

621.0

611.7

1202.1

1202.3

1202.4

1202.6

1202.7

1202.8

1203.4

1203.7

1204.1

1204.3

1204.5

1204.6

1204.6

1204.6

1204.5

1204.4

1204.2

1204.0

1203.8

1203.5

1203.2

1202.9

1202.5

1202.1

1201.7

1201.2

1200.7

1200.2

1199.7

1199.1

1198.6

1198.0

1197.4

1196.8

1196.1

1195.4

1194.7

1194.0

1193.3

1192.6

1191.8

1189.9

1187.8

1185.6

1183.4

1.6804

1.6511

1.6228

1.5954

1.5689

1.5433

1.4485

1.3645

1.2895

1.2222

1.1613

1.1061

1.0556

1.0094

0.9670

0.9278

0.8915

0.8578

0.8265

0.7973

0.7698

0.7440

0.7198

0.6971

0.6757

0.6554

0.6362

0.6180

0.6007

0.5843

0.5687

0.5538

0.5396

0.5260

0.5130

0.5006

0.4886

0.4772

0.4663

0.4557

0.4456

0.4218

0.4001

0.3802

0.3619

(continued)


28/93


218


PRESSURE


VOLUMEr

(CU FT

PER LB)

TOTAL


LATENTHEAT OF

EVAPOR

ATION

(BTU/LB)

HEAT OF

THELIQUID

(BTU/LB)

TEMPER

ATUREt

(_

F)Absolute P

SPECIFIC

VOLUMEr

(CU FT

PER LB)

TOTAL


LATENTHEAT OF

EVAPOR

ATION

(BTU/LB)

HEAT OF

THELIQUID

(BTU/LB)

TEMPER

ATUREt

(_

F)Gauge P

1250.0

1300.0

1350.0

1400.0

1450.0

1500.0

1600.0

1700.0

1800.0

1900.0

2000.0

2100.0

2200.0

2300.0

2400.0

2500.0

2600.0

2700.0

2800.0

2900.0

3000.0

3100.0

3200.0

3206.2

1235.3

1285.3

1335.3

1385.3

1435.3

1485.3

1585.3

1685.3

1785.3

1885.3

1985.3

2085.3

2185.3

2285.3

2385.3

2485.3

2585.3

2685.3

2785.3

2885.3

2985.3

3085.3

3185.3

3191.5

572.42

577.46

582.35

587.10

591.73

596.23

604.90

613.15

621.03

628.58

635.82

642.77

649.46

655.91

662.12

668.13

673.94

679.55

684.99

690.26

695.36

700.31

705.11

705.40

578.6

585.4

592.1

598.7

605.2

611.6

624.1

636.3

648.3

660.1

671.7

683.3

694.8

706.5

718.4

730.6

743.0

756.2

770.1

785.4

802.5

825.0

872.4

902.7

602.4

593.2

584.0

574.7

565.5

556.3

538.0

519.6

501.1

482.4

463.4

444.1

424.4

403.9

382.7

360.5

337.2

312.1

284.7

253.6

217.8

168.1

62.0

0.0

1181.0

1178.6

1176.1

1173.4

1170.7

1167.9

1162.1

1155.9

1149.4

1142.4

1135.1

1127.4

1119.2

1110.4

1101.1

1091.1

1080.2

1068.3

1054.8

1039.0

1020.3

993.1

934.4

902.7

0.3450

0.3293

0.3148

0.3012

0.2884

0.2765

0.2548

0.2354

0.2179

0.2021

0.1878

0.1746

0.1625

0.1513

0.1407

0.1307

0.1213

0.1123

0.1035

0.0947

0.0858

0.0753

0.0580

0.0503


29/93


219

PropertiesofSuperheatedSteam

r=specificvolume,cubicfeetperpou

nd

hg

=totalheatofsteam,

Btuperpoun

d

PRESSURE

(LBSPE

RSQ

IN)

SAT.

TOTALTEMPERATURED

EGREESFAHRENHEIT(t)

Absolut

e

P

Gauge

P

TEMP.

t

360_

400_

440_

480_

500_

60

0_

700_

800_

900_

1000_

1200_

14.6

96

0.0

212.0

0

rhg33.0

3

1221.1

34.6

8

1

239.9

36.3

2

1258.8

37.9

6

1277.6

38.7

8

1287.1

42

.86

133

4.8

46.9

4

1383.2

51.0

0

1432.3

55.0

7

1482.3

59.1

3

1533.1

67.2

5

1637.5

20.0

5.3

227.9

6

rhg24.2

1

1220.3

25.4

3

1

239.2

26.6

5

1258.2

27.8

6

1277.1

28.4

6

1286.6

31

.47

133

4.4

34.4

7

1382.9

37.4

6

1432.1

40.4

5

1482.1

43.4

4

1533.0

49.4

1

1637.4

30.0

15.3

250.3

3

rhg16.0

72

1218.6

1

6.8

97

1

237.9

17.7

14

1257.0

18.5

28

1276.2

18.9

33

1285.7

20

.95

133

3.8

22.9

6

1382.4

24.9

6

1431.7

26.9

5

1481.8

28.9

5

1532.7

32.9

3

1637.2

40.0

25.3

267.2

5

rhg12.0

01

1216.9

1

2.6

28

1

236.5

13.2

47

1255.9

13.8

62

1275.2

14.1

68

1284.8

15.

688

133

3.1

17.1

98

1381.9

18.7

02

1431.3

20.2

0

1481.4

21.7

0

1532.4

24.6

9

1637.0

50.0

35.3

281.0

1

rhg9.5

57

1215.2

1

0.0

65

1

235.1

10.5

67

1254.7

11.0

62

1274.2

11.3

09

1283.9

12.

532

133

2.5

13.7

44

1381.4

14.9

50

1430.9

16.1

52

1481.1

17.35

2

1532.1

19.7

47

1636.8

60.0

45.3

292.7

1

rhg7.9

27

1213.4

8.3

57

1

233.6

8.7

79

1253.5

9.1

96

1273.2

9.4

03

1283.0

10.

427

133

1.8

11.4

41

1380.9

12.4

49

1430.5

13.4

52

1480.8

14.45

4

1531.9

16.4

51

1636.6

70.0

55.3

302.9

2

rhg6.7

62

1211.5

7.1

36

1

232.1

7.5

02

1252.3

7.8

63

1272.2

8.0

41

1282.0

8.9

24

133

1.1

9.7

96

1380.4

10.6

62

1430.1

11.5

24

1480.5

12.38

3

1531.6

14.0

97

1636.3

80.0

65.3

312.0

3

rhg5.8

88

1209.7

6.2

20

1

230.7

6.5

44

1251.1

6.8

62

1271.1

7.0

20

1281.1

7.7

97

133

0.5

8.5

62

1379.9

9.3

22

1429.7

10.0

77

1480.1

10.83

0

1531.3

12.3

32

1636.2

90.0

75.3

320.2

7

rhg5.2

08

1207.7

5.5

08

1

229.1

5.7

99

1249.8

6.0

84

1270.1

6.2

25

1280.1

6.9

20

132

9.8

7.6

03

1379.4

8.2

79

1429.3

8.9

52

1479.8

9.6

23

1531.0

10.9

59

1635.9

100.0

85.3

327.8

1

rhg4.6

63

1205.7

4.9

37

1

227.6

5.2

Documents

Material Composition Engineering Data