material composition engineering data
TRANSCRIPT
-
7/28/2019 Material Composition Engineering Data
1/93
191
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
427C)Composition (Percent)
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
427C)Composition (Percent)
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
-
7/28/2019 Material Composition Engineering Data
2/93
Chapter 10. Engineering Data
192
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
343C)Composition (Percent)
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
593C)Composition (Percent)
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
593C)Composition (Percent)
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
649C)Composition (Percent)
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
427C)Composition (Percent)
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
-
7/28/2019 Material Composition Engineering Data
3/93
Chapter 10. Engineering Data
193
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
454C)Composition (Percent)
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
15. Type 316 Stainless SteelASTM A479 Grade UNS S31600Temp. range = 425 to 1500F (254
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
17. Type 317 Stainless SteelASTM A479 Grade UNS S31700Temp. range = 425 to 1500F (254
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
-
7/28/2019 Material Composition Engineering Data
4/93
Chapter 10. Engineering Data
194
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
399C)Composition (Percent)
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
316C)Composition (Percent)
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
316C)Composition (Percent)
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
-
7/28/2019 Material Composition Engineering Data
5/93
Chapter 10. Engineering Data
195
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
343C)Composition (Percent)
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
760C)Composition (Percent)
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
204C)Composition (Percent)
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
177C)Composition (Percent)
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
-
7/28/2019 Material Composition Engineering Data
6/93
Chapter 10. Engineering Data
196
33. Cast Aluminum BronzeASTM B148 Grade UNS C95800Temp. range = 325 to 500F (198 to
260C)Composition (Percent)
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
204C)Composition (Percent)
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
to 204C)Composition (Percent)
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
482C)Composition (Percent)
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)
-
7/28/2019 Material Composition Engineering Data
7/93
Chapter 10. Engineering Data
197
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
to 538C)Composition (Percent)
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
427C)Composition (Percent)
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)
-
7/28/2019 Material Composition Engineering Data
8/93
Chapter 10. Engineering Data
198
Valve Materials Properties for PressureContaining Components (continued)(The material codes in this table correspond to the previous Standard
Specifications for Valve Materials listing.)
MATER-IALCODE
TYPICALBRINELLHARDNESS
MODULUS OF
ELASTICITYAT 70_F (21_C) PSI (MPa)
MINIMUM MECHANICAL PROPERTIES
MATER-IALCODE
TYPICALBRINELLHARDNESS
MODULUS OF
ELASTICITYAT 70_F (21_C) PSI (MPa)
Reductionin Area
(%)
Elongationin 2-inch(50 mm)
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)
-
7/28/2019 Material Composition Engineering Data
9/93
Chapter 10. Engineering Data
199
Valve Materials Properties for PressureContaining Components (continued)(The material codes in this table correspond to the previous Standard
Specifications for Valve Materials listing.)
MATER-IALCODE
TYPICALBRINELLHARDNESS
MODULUS OF
ELASTICITYAT 70_F (21_C) PSI (MPa)
MINIMUM MECHANICAL PROPERTIES
MATER-IALCODE
TYPICALBRINELLHARDNESS
MODULUS OF
ELASTICITYAT 70_F (21_C) PSI (MPa)
Reductionin Area
(%)
Elongationin 2-inch(50 mm)
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.
-
7/28/2019 Material Composition Engineering Data
10/93
Chapter 10. Engineering Data
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
-
7/28/2019 Material Composition Engineering Data
11/93
Chapter 10. Engineering Data
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
-
7/28/2019 Material Composition Engineering Data
12/93
Chapter 10. Engineering Data
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.
-
7/28/2019 Material Composition Engineering Data
13/93
Chapter 10. Engineering Data
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)
-
7/28/2019 Material Composition Engineering Data
14/93
Chapter 10. Engineering Data
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)
-
7/28/2019 Material Composition Engineering Data
15/93
Chapter 10. Engineering Data
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.
-
7/28/2019 Material Composition Engineering Data
16/93
Chapter 10. Engineering Data
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)
-
7/28/2019 Material Composition Engineering Data
17/93
Chapter 10. Engineering Data
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)
-
7/28/2019 Material Composition Engineering Data
18/93
Chapter 10. Engineering Data
208
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
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)
-
7/28/2019 Material Composition Engineering Data
19/93
Chapter 10. Engineering Data
209
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
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)
-
7/28/2019 Material Composition Engineering Data
20/93
Chapter 10. Engineering Data
210
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
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.
-
7/28/2019 Material Composition Engineering Data
21/93
Chapter 10. Engineering Data
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.
-
7/28/2019 Material Composition Engineering Data
22/93
Chapter 10. Engineering Data
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
-
7/28/2019 Material Composition Engineering Data
23/93
Chapter 10. Engineering Data
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)
-
7/28/2019 Material Composition Engineering Data
24/93
Chapter 10. Engineering Data
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
HEAT OFSTEAM Hg(BTU/LB)
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)
-
7/28/2019 Material Composition Engineering Data
25/93
Chapter 10. Engineering Data
215
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
HEAT OFSTEAM Hg(BTU/LB)
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)
-
7/28/2019 Material Composition Engineering Data
26/93
Chapter 10. Engineering Data
216
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
HEAT OFSTEAM Hg(BTU/LB)
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)
-
7/28/2019 Material Composition Engineering Data
27/93
Chapter 10. Engineering Data
217
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
HEAT OFSTEAM Hg(BTU/LB)
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)
-
7/28/2019 Material Composition Engineering Data
28/93
Chapter 10. Engineering Data
218
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
HEAT OFSTEAM Hg(BTU/LB)
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
-
7/28/2019 Material Composition Engineering Data
29/93
Chapter 10. Engineering Data
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