Chapter Engineering Data Standard Specifications For Valve Materials (See table following this listing for additional specifications, crossreferenced to Material Code numbers.) 1. Cast Carbon Steel ASTM A2 Grade WCC Temp. range = to 00 F ( 29 to 27 C) Composition (Percent) C 0.25 max Mn 1.2 max P 0.0 max S 0.05 max Si 0.6 max 2. Cast Carbon Steel ASTM A352 Grade LCC Temp. range = 50 to 700 F ( 6 to 371 C) Composition Same as ASTM A2 grade WCC 3. Carbon Steel Bar AISI 1, UNS G Temp. range = to 00 F ( 29 to 27 C) Composition (Percent) C 0.15 to 0.2 Mn 0.6 to 0.9 P 0.0 max S 0.05 max. Leaded Steel Bar AISI L1, UNS G1 Temp. range = to 00 F ( 29 to 27 C) Composition (Percent) C 0.15 max Mn 0.5 to 1.15 P 0.0 to 0.09 S 0.26 to 0.35 Pb 0.15 to 0.35 191
Chapter. Engineering Data 5. AISI Cr-Mo Steel (Similar to ASTM A193 Grade B7 bolt material) Temp. range = F ( 29 C) to 0 F (56 C) less than tempering temperature to a maximum of 00 F (593 C). Composition (Percent) C 0.3 to 0.3 Mn 0.75 to 1.0 P 0.035 max S 0.035 max Si 0.15 to 0.35 Cr 0. to 1.1 Mo 0.15 to 0.25 Fe Remainder 6. Forged 3-1/2% Nickel Steel ASTM A352 Grade LC3 Temp. range = 150 to 650 F ( 1 to 33 C) Composition (Percent) C 0.15 max Mn 0.5 to 0. P 0.0 max S 0.05 max Si 0.6 max Ni 3.0 to.0 7. Cast Cr-Mo Steel ASTM A217 Grade WC6 Temp. range = to 10 F ( 29 to 593 C) Composition (Percent) C 0.05 to 0.2 Mn 0.5 to 0. P 0.0 max S 0.05 max Si 0.60 max Cr 1.0 to 1.5 Mo 0.5 to 0.65. Cast Cr-Mo Steel ASTM A217 Grade WC9 Temp. range = to 10 F ( 29 to 593 C) Composition (Percent) C 0.05 to 0.1 Mn 0. to 0.7 P 0.0 max S 0.05 max Si 0.6 max Cr 2.0 to 2.75 Mo 0.9 to 1.2 192 9. Forged Cr-Mo Steel ASTM A Grade F22 Temp. range = to 10 F ( 29 to 593 C) Composition (Percent) C 0.05 to 0.15 Mn 0.3 to 0.6 P 0.0 max S 0.0 max Si 0.5 max Cr 2.0 to 2.5 Mo 0.7 to 1.13. Cast Cr-Mo Steel ASTM A217 Grade C5 Temp. range = to F ( 29 to 69 C) Composition (Percent) C 0.2 max Mn 0. to 0.7 P 0.0 max S 0.05 max Si 0.75 max Cr.0 to 6.5 Mo 0.5 to 0.65 11. Type 2 Stainless Steel ASTM A79 Grade UNS S0 Temp. range = 325 to 1500 F ( 19 to C) Composition (Percent) C 0.15 max Mn 2.0 max P 0.05 max S 0.03 max Si 1.0 max Cr 17.0 to 19.0 Ni.0 to.0 N 0.1 max Fe Remainder. Type L Stainless Steel ASTM A79 Grade UNS S03 Temp. range = 25 to 00 F ( 25 to 27 C) Composition (Percent) C 0.03 max Mn 2.0 max P 0.05 max S 0.03 max Si 1.0 max Cr 1.0 to.0 Ni.0 to.0
N 0.1 max Fe Remainder 13. Cast Type L Stainless Steel ASTM A351 Grade CF3 Temp. range = 25 to 00 F ( 25 to 27 C) Composition (Percent) C 0.03 max Mn 1.5 max Si 2.0 max S 0.03 max P 0.05 max Cr 1.0 to 21.0 Ni.0 to 11.0 Mo 0.50 max 1. Type 3L Stainless Steel ASTM A79 Grade UNS S303 Temp. range = 25 to 50 F ( 25 to 5 C) Composition (Percent) C 0.03 max Mn 2.0 max P 0.05 max S 0.03 max Si 1.0 max Cr.0 to 1.0 Ni.0 to 1.0 Mo 2.0 to 3.0 N 0.1 max Fe Remainder 15. Type 3 Stainless Steel ASTM A79 Grade UNS S300 Temp. range = 25 to 1500 F ( 25 to C); above 00 F (53C), 0.0 C required Composition (Percent) C 0.0 max Mn 2.0 max P 0.05 max S 0.03 max Si 1.0 max Cr.0 to 1.0 Ni.0 to1.0 Mo 2.0 to 3.0 N 0.1 max Fe Remainder Chapter. Engineering Data. Cast Type 3 Stainless Steel ASTM A351 Grade CFM Temp. range = 25 to 1500 F ( 25 to C); above 00 F (53C), 0.0 C required Composition (Percent) C 0.0 max Mn 1.5 max Si 1.5 max P 0.0 max S 0.0 max Cr 1.0 to 21.0 Ni 9.0 to.0 Mo 2.0 to 3.0 17. Type 317 Stainless Steel ASTM A79 Grade UNS S31700 Temp. range = 25 to 1500 F ( 25 to C); above 00 F (53C), 0.0 C required Composition (Percent) C 0.0 max Mn 2.0 max P 0.05 max S 0.03 max Si 1.0 max Cr 1.0 to.0 Ni 11.0 to15.0 Mo 3.0 to.0 N 0.1 max Fe Remainder 1. Cast Type 317 Stainless Steel ASTM A351 Grade CGM Temp. range = 325 to 00 F ( 19 to 53 C); above 00 F (53C), 0.0 C required Composition (Percent) C 0.0 max Mn 1.5 max Si 1.5 max P 0.0 max S 0.0 max Cr 1.0 to 21.0 Ni 9.0 to 13.0 Mo 2.0 to 3.0 193
Chapter. Engineering Data 19. Type Stainless Steel ASTM A276 Grade S00 Temp. range = Annealed condition, to F ( 29 to 69 C); Heat treated 3 HRC, to 00 F ( 29 to 27 C) Composition (Percent) C 0.15 max Mn 1.0 max P 0.0 max S 0.03 max Si 1.0 max Cr 11.5 to 13.5 Fe Remainder. Type 17-PH Stainless Steel ASTM A56 Grade 6, UNS S1700 Temp. range = to 650 F ( 29 to 33 C). Can be used to 00 F (27 C) for applications, such as cages, where stresses are generally compressive, and there is no impact loading. Composition (Percent) C 0.07 max Mn 1.0 max Si 1.0 max P 0.0 max S 0.03 max Cr 15.0 to 17.5 Nb 0.15 to 0.5 Cu 3.0 to 5.0 Ni 3.0 to 5.0 Fe Remainder. Type 25 SMO Stainless Steel ASTM A79 Grade UNS S35 Temp. range = 325 to 750 F ( 19 to 399) C Composition (Percent) C 0.02 max Mn 1.0 max P 0.03 max S 0.01 max Si 0. max Cr 1.5 to.5 Ni 17.5 to 1.5 Mo 6.0 to 6.5 N 0.1 0.22 Fe Remainder 22. Cast Type 25 SMO Stainless Steel ASTM A351 Grade CK3MCuN Temp. range = 325 to 750 F ( 19 to 399 C) Composition (Percent) C 0.025 max Mn 1.2 max Si 1.0 max P 0.0 max S 0.01 max Cr 19.5 to.5 Ni 17.5 to 19.5 Mo 6.0 to 7.0 23. Type 25, S33 Duplex Stainless Steel ASTM A279 Grade UNS S33 Temp. range = to 600 F ( 29 to 3 C) Composition (Percent) C 0.03 max Mn 2.0 max P 0.03 max S 0.02 max Si 1.0 max Cr 21.0 to 23.0 Ni.5 to 6.5 Mo 2.5 to 3.5 N 0.03 to 0.2 Fe Remainder 2. Cast Type 25, S33 Stainless Steel ASTM A90 Grade a, CD3MN Temp. range = to 600 F ( 29 to 3 C) Composition (Percent) C 0.03 max Mn 1.5 max Si 1.0 max P 0.0 max S 0.02 max Cr 21.0 to 23.5 Ni.5 to 6.5 Mo 2.5 to 3.5 N 0.1 to 0.3 Fe Remainder 19
25. Cast Iron ASTM A6 Class B, UNS F2 Temp. range = Pressure Retaining Components, to 50 F ( 29 to 232 C); Non-Pressure Retaining Components, 0 to 00 F (73 to 27 C); ANSI B31.5 150 F ( 1 C) minimum if the maximum stress does not exceed 0% of the ambient allowable stress. Composition (Percent) P 0.75 max S 0.15 max 26. Cast Iron ASTM A6 Class C, UNS F Temp. range = Pressure Retaining Components, to 50 F ( 29 to 232 C); Non-Pressure Retaining Components, 0 to 00 F (73 to 27 C); ANSI B31.5 150 F ( 1 C) minimum if the maximum stress does not exceed 0% of the ambient allowable stress. Composition (Percent) P 0.75 max S 0.15 max 27. Ductile Iron ASTM A395 Type 60-0-1 Temp. range = to 650 F ( 29 to 33 C) Composition (Percent) C 3.0 min Si 2.5 max P 0.0 max 2. Ductile Ni-Resist Iron ASTM A39 Type D-2B, UNS F01 Temp. range = to 0 F ( 29 to 760 C) Composition (Percent) C 3.0 min Si 1.5 to 3.00 Mn 0.70 to 1.25 P 0.0 max Ni 1.0 to 22.0 Cr 2.75 to.0 29. Valve Bronze ASTM B61, UNS C920 Temp. range = 325 to 550 F ( 19 to 2 C) Chapter. Engineering Data Composition (Percent) Cu 6.0 to 90.0 Sn 5.5 to 6.5 Pb 1.0 to 2.0 Zn 3.0 to 5.0 Ni 1.0 max Fe 0.25 max S 0.05 max P 0.05 max. Tin Bronze ASTM B56 Grade UNS C90500 Temp. range = 325 to 00 F ( 19 to C) Composition (Percent) Cu 6.0 to 9.0 Sn 9.0 to 11.0 Pb 0. max Zn 1.0 to 3.0 Ni 1.0 max Fe 0.2 max S 0.05 max P 0.05 max 31. Manganese Bronze ASTM B5 Grade UNS C6500 Temp. range = 325 to 350 F ( 19 to 177 C) Composition (Percent) Cu 55.0 to 60.0 Sn 1.0 max Pb 0. max Ni 1.0 max Fe 0. to 2.0 Al 0.5 to 1.5 Mn 0.1 to 1.5 Zn 36.0 to 2.0 32. Cast Aluminum Bronze ASTM B1 Grade UNS C9500 Temp. range = ANSI B31.1, B31.3, 325 to 500 F ( 19 to 260 C); ASME Section VIII, 325 to 600 F ( 19 to 3 C) Composition (Percent) Cu 3.0 min Al.0 to 11.5 Fe 3.0 to 5.0 Mn 0.50 max Ni 1.5 max 195
Chapter. Engineering Data 33. Cast Aluminum Bronze ASTM B1 Grade UNS C9500 Temp. range = 325 to 500 F ( 19 to 260 C) Composition (Percent) Cu 79.0 min Al.5 to 9.5 Fe 3.5 to.5 Mn 0. to 1.5 Ni.0 to 5.0 Si 0.1 max 3. B Yellow Brass Bar ASTM B Grade UNS C36000, 1/2 Hard Temp. range = Non-Pressure Retaining Components, 325 to 00 F ( 19 to C) Composition (Percent) Cu 60.0 to 63.0 Pb 2.5 to 3.7 Fe 0.35 max Zn Remainder 35. Naval Brass Forgings ASTM B23 Alloy UNS C600 Temp. range = 325 to 00 F ( 19 to C) Composition (Percent) Cu 59.0 to 62.0 Sn 0.5 to 1.0 Pb 0.2 max Fe 0.15 max Zn Remainder 36. Aluminum Bar ASTM B211 Alloy UNS A96061-T6 Temp. range = 52 to 00 F ( 269 to C) Composition (Percent) Si 0. to 0. Fe 0.7 max Cu 0.15 to 0. Zn 0.25 max Mg 0. to 1.2 Mn 0.15 max Cr 0.0 to 0.35 Ti 0.15 max Other Elements 0.15 max Al Remainder 37. Cobalt-base Alloy No.6 Cast UNS R006, Weld filler CoCr-A Temp. range = 325 to 1500 F ( 19 to C) Composition (Percent) C 0.9 to 1. Mn 1.0 max W 3.0 to 6.0 Ni 3.0 Cr 26.0 to 32.0 Mo 1.0 max Fe 3.0 max Si 2.0 max Co Remainder 3. Ni-Cu Alloy Bar K500 B65 Grade N05500 Temp. range = 325 F to 900 F ( 19 C to 2 C) Composition (Percent) Ni 63.0 to 70.0 Fe 2.0 max Mn 1.5 max Si 0.5 max C 0.25 max S 0.01 max P 0.02 max Al 2.3 to 3.15 Ti 0.35 to 0.5 Cu Remainder 39. Cast Ni-Cu Alloy 00 ASTM A9 Grade M35-1 Temp. range = 325 to 900 F ( 19 to 2 C) Composition (Percent) Cu 26.0 to 33.0 C 0.35 max Mn 1.5 max Fe 3.5 max S 0.03 max P 0.03 max Si 1.35 max Nb 0.5 max Ni Remainder 0. Ni-Cr-Mo Alloy C276 Bar ASTM B57 Grade N276 Temp. range = 325 to 50 F ( 19 to 677 C) 196
Chapter. Engineering Data Composition (Percent) Cr 1.5 to.5 Fe.0 to 7.0 W 3.0 to.5 C 0.01 max Si 0.0 max Co 2.5 max Mn 1.0 max V 0.35 max Mo 15.0 to 17.0 P 0.0 S 0.03 Ni Remainder 1. Ni-Cr-Mo Alloy C ASTM A9 CW2M Temp. range = 325 to 00 F ( 19 to 53 C) Composition (Percent) Cr 15.5 to 17.5 Fe 2.0 max W 1.0 max C 0.02 max Si 0. max Mn 1.0 max Mo 15.0 to 17.5 P 0.03 S 0.03 Ni Remainder 2. Ni-Mo Alloy B2 Bar ASTM B335 Grade B2, UNS N665 Temp. range = 325 to 00 F ( 19 to 27 C) Composition (Percent) Cr 1.0 max Fe 2.0 max C 0.02 max Si 0.1 max Co 1.0 max Mn 1.0 max Mo 26.0 to.0 P 0.0 max S 0.03 max Ni Remainder 3. Cast Ni-Mo Alloy B2 ASTM A9 N7M Temp. range = 325 to 00 F ( 19 to 53 C) Composition (Percent) Cr 1.0 max Fe 3.0 max C 0.07 max Si 1.0 max Mn 1.0 max Mo.0 to 33.0 P 0.0 max S 0.03 max Ni Remainder MATER- IAL CODE 1 2 3 Valve Materials Properties for Pressure Containing Components (The material codes in this table correspond to the previous Standard Specifications for Valve Materials listing.) MINIMUM MECHANICAL PROPERTIES Tensile Strength ksi (MPa) 70-95 (5-655) 70-95 (5-655) 57 (390) typical 79 (55) typical 5 (1) 135 (9) typical 6 7 70-95 (5-655) 70-95 (5-655) Yield Strength ksi (MPa) Elongation in 2-inch (50 mm) Reduction in Area (%) 0 (275) 22 35 0 (275) 22 35 2 (290) typical 71 (90) typical 115 (792) typical MODULUS OF ELASTICITY AT 70 F (21 C) PSI (MPa) 27.9E6 (19.2E) 27.9E6 (19.2E) TYPICAL BRINELL HARDNESS 137-17 137-17 37 typical 67 typical - - - 111 typical 52 typical - - - 3 22 typical 63 typical 0 (275) 2 35 0 (275) 35 (continued) 29.9E6 (.6E) 27.9E6 (19.2E) 29.9E6 (.6E) 255 137 17-0 197
Chapter. Engineering Data Valve Materials Properties for Pressure Containing Components (continued) (The material codes in this table correspond to the previous Standard Specifications for Valve Materials listing.) MINIMUM MECHANICAL PROPERTIES MATER- IAL CODE 19 Tensile Strength ksi (MPa) 70-95 (5-655) Yield Strength ksi (MPa) Elongation in 2-inch (50 mm) Reduction in Area (%) 0 (275) 35 9 75 (515) 5(3) 90-115 (6-795) 60 (15) 1 35 11 75 (515) (5) 0 70 (5) 25 (170) 0 13 70 (5) 25 (170) 0 1 70 (5) 25 (170) 0 15 (2) 0 (551) 35 () 0 70 (5) (5) 17 75 (515) 35 () 25 1 75 (515) 35 () 25 19 70 (0) 0 (275) 5 15 (00) 5 (60) 13 5 21 95(665) (5) 35 50 22 0(550) 3(260) 35 - - - 23 90(6) 65(50) 25 - - - 2 90(6) 65(50) 25 - - - 25 (3) 31 (21) 26 () 1 (22) 27 60 (15) 0 (276) 1 MODULUS OF ELASTICITY AT 70 F (21 C) PSI (MPa) 29.9E6 (.6E) 29.9E6 (.6E) 27.E6 (19.0E) 2.3E6 (19.3E) 29.0E6 (.0E) 29.0E6 (.0E) 2.3E6 (19.3E) 2.3E6 (19.5E) 2.3E6 (19.5E) 2.3E6 (19.5E) 2.3E6 (19.5E) 29.2E6 (.1E) 29E6 (.0E) 29.0E6 (.0E) 29.0E6 (.0E).5E6 (21.0E).5E6 (21.0E) 13.E6 (9.2E) 13.E6 (9.2E) 23E6 (E) TYPICAL BRINELL HARDNESS 17-0 156-7 required 176-255 150 19 19 150-170 150 3 170 170 223 2 min 90 HRB 2 HRB 290 max 9 HRB 0-2 0-2 13-17 2 5 (00) (5) 7 1-211 29 3 (23) (1) 2 (continued) 1.0E6 (9.7E) 65
Chapter. Engineering Data Valve Materials Properties for Pressure Containing Components (continued) (The material codes in this table correspond to the previous Standard Specifications for Valve Materials listing.) MINIMUM MECHANICAL PROPERTIES MATER- IAL CODE Tensile Strength ksi (MPa) Yield Strength ksi (MPa) Elongation in 2-inch (50 mm) Reduction in Area (%) 0 (275) 1() 31 65 () 25(172) 32 75 (515) (5) 33 5 (55) 35() 15 3 55 () 25(170) 35 60 (15) 27() 22 36 2 (290) 35(21) 37 (5) 15 (60) typical 93(63) typical 17 typical 3 0 (69) 70(5) 39 65 (50) 25(170) 25 0 0 (69) 1(23) 0 1 72 (96) 0(275) 2 1 (760) 51(350) 0 3 76 (525) 0(275) 1. Tempered ( F (650 C). 2. Annealed. 3. A6 Cl.B 1.5 in. (95 mm) dia bar.. A6 Cl.C 1.5 in. (95 mm) dia bar. 5. Wrought. MODULUS OF ELASTICITY AT 70 F (21 C) PSI (MPa) 1.0 (9.7E) 15.3E6 (.5E) E6 (11.0E) E6 (11.0E) 1E6 (9.6E) 15.0E6 (.3E) 9.9E6 (6.E) E6 (21E) 26E6 (17.9E) 23E6 (15.E) 29.E6 (.5E).E6 (21.2E) 31.E6 (21.7E) 2.5E6 (19.7E) TYPICAL BRINELL HARDNESS 75 9 150 1 170 60 0 HRB required 131 95 37 HRC 250 325 1 150 2 150 15 23 199
Chapter. Engineering Data NO. COMPOUND FORMULA 1 2 3 5 6 7 9 11 13 1 15 17 1 19 21 Methane Ethane Propane n Butane Isobutane n Pentane Isopentane Neopentane n Hexane 2 Methylpentane 3 Methylpentane Neohexane 2,3 Dimethylbutane n Heptane 2 Methylhexane 3 Methylhexane 3 Ethylpentane 2,2 Dimethylpentane 2, Dimethylpentane 3,3 Dimethylpentane Triptane CH C 2 H 6 C 3 H C H C H C 5 H C 5 H C 5 H C 6 H 1 C 6 H 1 C 6 H 1 C 6 H 1 C 6 H 1 C 7 H C 7 H C 7 H C 7 H C 7 H C 7 H C 7 H C 7 H Physical Constants of Hydrocarbons MOLECULAR WEIGHT BOILING POINT AT 1.696 PSIA ( F) VAPOR PRESSURE AT 0 F (PSIA) FREEZING POINT AT 1.696 PSIA ( F).03.070.097 5. 5. 72.151 72.151 72.151 6.17 6.17 6.17 6.17 6.17 0.5 0.5 0.5 0.5 0.5 0.5 0.5 0.5 25.69 7. 3.67 31..90 96.92 2. 9. 155.72.7 15.9 1.52 136.36 9.17 19.09 197.32 0.25 17.5 176.9.91 177.5 (5000) (2) (00) (2) 190. 51.6 72.2 15.570. 35.9.956 6.767 6.09 9.56 7.0 1.6 2.271 2.1 2.0 3.92 3.292 2.773 3.37 296.6 (5) 297.9 (5) 5. (5) 217.05 255.29 1.51 255.3 2.17 139.5 2.63 - - - 17.72 199.3 131.05.9 - - - 11. 190.6.63 2.01.2 CRITICAL CONSTANTS Critical Temperature ( F) Critical Pressure (psia) 1.63 90.09 6.01 5.65 27.9 35.7 369. 321.13 53.7 35.3.3.13 0.29 5. 95.00 503.7 513. 77.23 75.95 505.5 96. 667. 707. 6.3 550.7 529.1.6 90. 6.0 36.9 36.6 53.1 6. 53.5 396. 396.5 0.1 19.3 02.2 396.9 27.2 2. SPECIFIC GRAVITY AT 1.696 PSIA Liquid, (3),() 60 F/60 F Gas at 60 F (Air=1) (1) 0.3 () 0.356 (7) 0.5077 (7) 0.5 (7) 0.5631 (7) 0.63 0.627 0.5967 (7) 0.660 0.6579 0.669 0.650 0.666 0.62 0.6 0.6917 0.702 0.672 0.6773 0.6976 0.696 0.5539 1.032 1.5225 2.006 2.006 2.911 2.911 2.911 2.9753 2.9753 2.9753 2.9753 2.9753 3.596 3.596 3.596 3.596 3.596 3.596 3.596 3.596 0
Chapter. Engineering Data NO. 22 23 2 25 26 27 2 29 31 32 33 3 35 36 37 3 39 0 COMPOUND n Octane Diisobutyl Isooctane n Nonane n Decane Cyclopentane Methylcyclopentane Cyclohexane Methylcyclohexane Ethylene Propene 1 Butene Cis 2 Butene Trans 2 Butene Isobutene 1 Pentene 1,2 Butadiene 1,3 Butadiene Isoprene FORMULA C H 1 C H 1 C H 1 C 9 H C H 22 C 5 H C 6 H C 6 H C 7 H 1 C 2 H C 3 H 6 C H C H C H C H C 5 H C H 6 C H 6 C 5 H Physical Constants of Hydrocarbons (continued) MOLECULAR WEIGHT BOILING POINT AT 1.696 PSIA ( F) VAPOR PRESSURE AT 0 F (PSIA) FREEZING POINT AT 1.696 PSIA ( F) Critical Temperature ( F) CRITICAL CONSTANTS Critical Pressure (psia) 11.232 11.232 11.232.259.26 70.135.2.2 9.19 2.05 2.01 56. 56. 56. 56. 70.135 5.092 5.092 6.119 25.22 22.39 2.63 3.7 35. 1.65 1.25 177.29 213.6 15.62 53.90.75 3.69 33.5 19.59 5.93 51.53 2.06 93. 0.537 1.1 1.70 0.179 0.0597 9.91.503 3.26 1.609 - - - 226. 63.05 5.5 9.0 63.0 19.115 (.) (2) (60.) (2).672 70.1 132.07 1.27 6.2 21.36 136.91 22. 3.77 195.7 272.5 (5) 1.5 (5) 1.63 (5) 21.06 157.96 2.61 265.39 213..02 2.7 56.22 5. 519.6 6.6 652.1 61.5 99.35 536.7 570.27.5 196.9 295.6 32.37 311.6 292.55 376.93 (339.) (2) 6. (.) (2) 360.6 360.6 372. 332.. 653. 5.9 591. 503.5 729. 669. 53. 6. 595. 50. 590. (653.) (2) 62. (55.) (2) SPECIFIC GRAVITY AT 1.696 PSIA Liquid, (3),() 60 F/60 F Gas at 60 F (Air=1) (1) 0.706 0.6979 0.6962 0.7217 0.732 0.750 0.7536 0.73 0.770 - - - 0.52 (7) 0.6013 (7) 0.6271 (7) 0.60 (7) 0.600 (7) 0.657 0.65 7 0.6272 (7) 0.661 3.939 3.939 3.939.22.95 2.215 2.9057 2.9057 3.3900 0.966 1.529 1.9372 1.9372 1.9372 1.9372 2.215 1.676 1.676 2.3519 1
Chapter. Engineering Data NO. COMPOUND FORMULA Physical Constants of Hydrocarbons (continued) MOLECULAR WEIGHT BOILING POINT AT 1.696 PSIA ( F) VAPOR PRESSURE AT 0 F (PSIA) FREEZING POINT AT 1.696 PSIA ( F) Critical Temperature ( F) CRITICAL CONSTANTS Critical Pressure (psia) SPECIFIC GRAVITY AT 1.696 PSIA Liquid, (3),() 60 F/60 F Gas at 60 F (Air=1) (1) 1 2 3 5 6 7 9 Acetylene Benzene Toluene Ethylbenzene o Xylene m Xylene p Xylene Styrene Isopropylbenzene C 2 H 2 C 6 H 6 C 7 H C H C H C H C H C H C 9 H 1. Calculated values. 2. ( ) Estimated values. 3. Air saturated hydrocarbons.. Absolute values from weights in vacuum. 5. At saturation pressure (triple point). 6. Sublimation point. 7. Saturation pressure and 60 F.. Apparent value for methane at 60 F. 9. Specific gravity, 119 F/60 F (sublimation point). 26.03 7.11 92.11 6. 6. 6. 6..152 1.195 119. (6) 176.17 231.13 277. 291.97 22.1 21.05 293.29 6.3 - - - 3.22 1.032 0.371 0.26 0.326 0.32 (0.2) (2) 0.1 11 (5) 1.96 13.9 13.91 13. 5. 55.6 23..2 95.31 552.22 605.55 651.2 675.0 651.02 69.6 706.0 676. 90. 7. 595.9 523.5 51. 513.6 509.2 50. 65. 0.615 (9) 0. 0.71 0.71 0. 0.67 0.657 0.91 0.663 0.990 2.6969 3.1 3.6655 3.6655 3.6655 3.6655 3.5959.19 Gas Acetylene Air Argon Butane Carbon Monoxide Specific Heat Ratio (k) 1.3 1.0 1.67 1.17 1.0 1. Use property tables if available for greater accuracy. Gas Carbon Dioxide Ethane Helium Hydrogen Methane Specific Heat Ratio (k) Specific Heat Ratio (k) 1.29 1.25 1.66 1.0 1.26 Gas 0.6 Natural Gas Nitrogen Oxygen Propane Propylene Specific Heat Ratio (k) 1.32 1.0 1.0 1.21 1.15 Gas Specific Heat Ratio (k) Steam (1) 1.33 2
Chapter. Engineering Data Physical Constants of Various Fluids FLUID FORMULA MOLECULAR WEIGHT BOILING POINT ( F AT 1.696 PSIA) VAPOR PRESSURE @ 70 F (PSIG) CRITICAL CRITICAL CRITICAL TEMP. ( F) CRITICAL PRESSURE (PSIA) Acetic Acid HC 2 H 3 O 2 60.05 25 1.05 SPECIFIC GRAVITY Acetone C 3 H 6 O 5.0 133 55 691 0.79 2.01 Air N 2 O 2 2.97 317 221 57 0.6 (3) 1.0 Alcohol, Ethyl C 2 H 6 O 6.07 173 2.3 (2) 70 925 0.79 1.59 Alcohol, Methyl CH O 32.0 1.63 (2) 63 117 0.796 1.11 Ammonia NH 3 17.03 2 11 270 36 0.62 0.59 Ammonium Chloride (1) NH CI 1.07 Ammonium Hydroxide (1) NH OH 0.91 Ammonium Sulfate (1) (NH ) 2 SO 1.15 Aniline C 6 H 7N 93. 365 79 770 1.02 Argon A 39.9 2 1 705 1.65 1.3 Beer 1.01 Bromine Br 2 159. 13 575 2.93 5.52 Calcium Chloride (1) CaCI 2 1.23 Carbon Dioxide CO 2.01 9 39 72 0.01 (3) 1.52 Carbon Disulfide CS 2 76.1 115 1.29 2.63 Carbon Monoxide CO 2.01 31 2 507 0.0 0.97 Carbon Tetrachloride CCI 153. 170 52 661 1.59 5.31 Chlorine CI 2 70.91 5 291 1119 1.2 2.5 Chromic Acid H 2 CrO 11.03 1.21 Citric Acid C 6 H O 7 192. 1.5 Copper Sulfate (1) CuSO 1.17 (continued) Liquid 60/60 F Gas 3
Chapter. Engineering Data Physical Constants of Various Fluids (continued) VAPOR BOILING POINT CRITICAL CRITICAL SPECIFIC GRAVITY MOLECULAR PRESSURE FLUID FORMULA ( F AT 1.696 TEMP. PRESSURE WEIGHT @ 70 F Liquid PSIA) ( F) (PSIA) Gas (PSIG) 60/60 F Ether (C 2 H 5 ) 2 O 7. 3 0.7 2.55 Ferric Chloride (1) FeCI 3 1.23 Fluorine F 2 3.00 5 0 0 09 1.11 1.31 Formaldehyde H 2 CO.03 6 0.2 1.0 Formic Acid HCO 2 H 6.03 21 1.23 Furfural C 5 H O 2 96.0 32 1. Glycerine C 3 H O 3 92.09 55 1.26 Glycol C 2 H 6 O 2 62.07 37 1.11 Helium He.003 5 50 33 0.1 0.1 Hydrochloric Acid HCI 36.7 115 1.6 Hydrofluoric Acid HF.01 66 0.9 6 0.92 Hydrogen H 2 2.0 22 00 1 0.07 (3) 0.07 Hydrogen Chloride HCI 36.7 115 613 5 119 0.6 1.26 Hydrogen Sulfide H 2 S 3.07 76 252 213 17 0.79 1.17 Isopropyl Alcohol C 3 H O 60.09 0.7 2.0 Linseed Oil 53 0.93 Mangesium Chloride (1) MgCI 2 1.22 Mercury Hg 0.61 670 13.6 6.93 Methyl Bromide CH 3B r 9.95 3 13 376 1.73 3.27 Methyl Chloride CH 3 CI 50.9 11 59 290 969 0.99 1.7 Naphthalene C H. 2 1.1.3 Nitric Acid HNO 3 63.02 17 1.5 (continued)
Chapter. Engineering Data Physical Constants of Various Fluids (continued) VAPOR BOILING POINT CRITICAL CRITICAL SPECIFIC GRAVITY MOLECULAR PRESSURE FLUID FORMULA ( F AT 1.696 TEMP. PRESSURE WEIGHT @ 70 F Liquid PSIA) ( F) (PSIA) Gas (PSIG) 60/60 F Nitrogen N 2 2.02 3 233 93 0.1 (3) 0.97 Oil, Vegetable 0.91 0.9 Oxygen O 2 32 297 11 737 1.1 (3) 1.5 Phosgene COCI 2 9.92 7.7 360 23 1.39 3.2 Phosphoric Acid H 3 PO 9.00 15 1.3 Potassium Carbonate (1) K 2 CO 3 1.2 Potassium Chloride (1) KCI 1. Potassium Hydroxide (1) KOH 1.2 Sodium Chloride (1) NaCI 1.19 Sodium Hydroxide (1) NaOH 1.27 Sodium Sulfate (1) Na 2 SO 1.2 Sodium Thiosulfate (1) Na 2 S 2 O 3 1.23 Starch (C 6 H O 5 )x 1.50 Sugar Solutions (1) C H 211 1. Sulfuric Acid H 2 SO 9.0 626 1.3 Sulfur Dioxide SO 2 6.6 1 3. 3 115 1.39 2.21 Turpentine 3 0.7 Water H 2 O 1.0 2 0.992 (2) 706 3 1.00 0.62 Zinc Chloride (1) ZnCI 2 1.2 Zinc Sulfate (1) ZnSO 1.31 1. Aqueous Solution 25% by weight of compound. 2. Vapor pressure in psia at 0 F 3. Vapor pressure in psia. 5
Chapter. Engineering Data TEMP ( F) 5 3 2 1 0 99 9 97 96 95 9 93 92 91 90 9 7 6 5 3 2 1 0 79 7 77 76 75 7 73 72 71 70 69 6 67 66 65 6 63 62 61 60 PRESSURE psia 0.996 1.01 1.07 1.135 1.1 1.2 1.29 1.3 1.0 1.6 1.52 1.59 1.65 1.72 1.79 1.6 1.9 2.02 2. 2.1 2.27 2.35 2.5 2.5 2.6 2.7 2. 2.95 3.06 3.1 3.29 3.2 3.5 3.67 3.0 3.9.0.23.3.53.69.5 5.02 5.19 5.37 5.55 Refrigerant 717 (Ammonia) Properties of Liquid and Saturated Vapor psig 27.9 (2) 27. (2) 27.7 (2) 27.6 (2) 27.5 (2) 27. (2) 27.3 (2) 27.2 (2) 27.1 (2) 26.9 (2) 26. (2) 26.7 (2) 26.6 (2) 26. (2) 26.3 (2) 26.1 (2) 26.0 (2) 25. (2) 25.6 (2) 25.5 (2) 25.3 (2) 25.1 (2) 2.9 (2) 2.7 (2) 2.5 (2) 2.3 (2) 2.1 (2) 23.9 (2) 23.7 (2) 23.5 (2) 23.2 (2) 23.0 (2) 22.7 (2) 22. (2) 22.2 (2) 21.9 (2) 21.6 (2) 21.3 (2) 21.0 (2).7 (2). (2).0 (2) 19.7 (2) 19. (2) 19.0 (2) 1.6 (2) VOLUME (CU. FT./LB.) Vapor V g 223.2 21.2 5.7 197.6 19.. 175.3.5 2.1 155.9 150.0 1.3 13.9 133..9.1 119.6 115.3 111.1 7.1 3.3 99.6 96.17 92.1 9.59 6.50 3.5 0.69 77.96 75.33 72.1 70.39 6.06 65.2 63.67 61.60 59.61 57.69 55.5 5.0 52.37 50.73 9.1 7.62 6.15.73 DENSITY (LB./CU. FT.) Liquid I/v f 5.71 5.67 5.63 5.59 5.55 5.52 5.7 5.3 5.0 5.36 5.32 5.2 5.2 5. 5. 5. 5.0 5.0 5.00.96.92...0.76.73.6.6.60.56.52...0.36.32.2.2.19.15.11.07.03 3.99 3.95 3.91 (continued) ENTHALPY (1) (BTU/LB.) Liquid h f 6.5 67.5 66. 65. 6.3 63.3 62.2 61.2 60.1 59.1 5.0 57.0 55.9 5.9 53. 52. 51.7 50.7 9.6.6 7.5 6.5 5.. 3.3 2.2 1.2 0.1 39.1 3.0 37.0 35.9 3.9 33. 32. 31.7.7 29.6 2.6 27.5 26.5 25. 2. 23.3 22.2 21.2 Vapor h g 570.3 570.7 571.2 571.6 572.1 572.5 572.9 573. 573. 57.3 57.7 575.1 575.6 576.0 576.5 576.9 577.3 577. 57.2 57.6 579.1 579.5 579.9 50. 50. 51.2 51.6 52.1 52.5 52.9 53.3 53. 5.2 5.6 55.0 55.5 55.9 56.3 56.7 57.1 57.5 5.0 5. 5. 59.2 59.6 ENTROPY (1) BTU/(LB.)( R) Liquid s f 0.177.177.171.5.55 0.26.1597.156.1539.15 0.11.152.3.1395.1366 0.133.19.1.53.25 0.1197.19.111.1113.5 0.57..02.0975.097 0.09.092.065.03.011 0.07.0757.07.0703.0676 0.0650.0623.0596.0570.053.0517 Vapor s g 1.623 1.65 1.67 1.69 1.6092 1.6055 1.601 1.592 1.595 1.59 1.57 1.53 1.503 1.576 1.573 1.5699 1.5665 1.5631 1.5597 1.556 1.5531 1.59 1.565 1.532 1.500 1.536 1.5336 1.5 1.5273 1.522 1.5211 1.5 1.519 1.5119 1.509 1.5059 1.5029 1.999 1.970 1.90 1.911 1.3 1.5 1.26 1.797 1.769 6
Chapter. Engineering Data TEMP ( F) 59 5 57 56 55 5 53 52 51 50 9 7 6 5 3 2 1 0 39 3 37 36 35 3 33 32 31 29 2 27 26 25 2 23 22 21 19 1 17 15 1 Refrigerant 717 (Ammonia) Properties of Liquid and Saturated Vapor (continued) PRESSURE psia 5.7 5.93 6.13 6.33 6.5 6.75 6.97 7. 7.3 7.67 7.91..2.6.95 9.23 9.51 9.1..1.72 11.0 11.37 11.71.05.1.77 13.1 13.52 13.90 1. 1.71 15. 15.55 15.9.2. 17.3 17.1 1. 1.79 19. 19.1.3. 21.3 psig 1.2 (2) 17. (2) 17. (2) 17.0 (2).6 (2).2 (2) 15.7 (2) 15.3 (2) 1. (2) 1.3 (2) 13. (2) 13.3 (2). (2).2 (2) 11.7 (2) 11.1 (2).6 (2).0 (2) 9.3 (2).7 (2).1 (2) 7. (2) 6. (2) 6.1 (2) 5. (2).7 (2) 3.9 (2) 3.2 (2) 2. (2) 1.6 (2) 0. (2) 0.0 0. 0. 1.3 1.7 2.2 2.6 3.1 3.6.1.6 5.1 5.6 6.2 6.7 VOLUME (CU. FT./LB.) Vapor V g 3.37 2.05 0.79 39.56 3.3 37.2 36.15 35.09 3.06 33.0 32. 31..31 29.5 2.62 27.2 27.0 26.29 25.56 2.6 2.1 23.53 22.9 22.27 21.6 21..5.00 19. 1.97 1. 1.00 17.5 17.09.66.2 15.3 15.3 15.05 1.6 1.32 13.97 13.62 13.29.97.66 DENSITY (LB./CU. FT.) Liquid I/v f 3.7 3.3 3.7 3.7 3.70 3.66 3.62 3.5 3.5 3.9 3.5 3.1 3.37 3.33 3.2 3.2 3. 3. 3. 3.0 3.0 2.99 2.95 2.90 2.6 2.2 2.7 2.73 2.69 2.65 2.61 2.57 2.5 2. 2. 2.0 2.35 2.31 2.26 2.22 2.1 2.13 2.09 2.0 2.00 1.96 (continued) ENTHALPY (1) (BTU/LB.) Liquid h f.1 19.1 1.0 17.0 15.9 1. 13..7 11.7.6 9.6.5 7. 6. 5.3.3 3.2 2.1 1.1 0.0 1.1 2.1 3.2.3 5.3 6. 7..5 9.6.7 11.7. 13.9 1.9.0 17.1 1.1 19.2.3 21. 22. 23.5 2.6 25.6 26.7 27. Vapor h g 590.0 590. 590. 591.2 591.6 592.1 592. 592.9 593.2 593.7 59.0 59. 59.9 595.2 595.6 596.0 596. 596. 597.2 597.6 59.0 59.3 59.7 599.1 599.5 599.9 600.2 600.6 601.0 601. 601.7 602.1 602.5 602. 603.2 603.6 603.9 60.3 60.6 605.0 605.3 605.7 606.1 606. 606.7 607.1 ENTROPY (1) BTU/(LB.)( R) Liquid s f 0.090.06.03.0.036 0.0360.033.07.021.0256 0.02.0.0179.0153.07 0.02.0076.0051.0025.0000 0.0025.0051.0076.01.06 0.0151.0176.01.0226.0250 0.0275.00.0325.0350.037 0.0399.023.0.072.097 0.0521.055.0570.059.061.062 Vapor s g 1.71 1.713 1.66 1.65 1.631 1.60 1.577 1.551 1.52 1.97 1.71 1.5 1.19 1.393 1.36 1.32 1.317 1.292 1.267 1.22 1.217 1.193 1.9 1.1 1.1 1.096 1.072 1.0 1.025 1.001 1.397 1.3955 1.3932 1.3909 1.36 1.363 1. 1.31 1.3796 1.377 1.3752 1.3729 1.370 1.366 1.366 1.362 7
Chapter. Engineering Data 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) Vapor s g Liquid s f Vapor h g Liquid h f Liquid I/v f Vapor V g psig psia 13 11 9 7 6 5 3 2 1 0 1 2 3 5 (3) 6 7 9 11 13 1 15 17 1 19 21 22 23 2 25 26 27 2 29 31 32 21.99 22.56 23.15 23.7 2.35 2.97 25.61 26.26 26.92 27.59 2.2 2.9 29.69.2 31. 31.92 32.69 33.7 3.27 35.09 35.92 36.77 37.63 3.51 39.0 0.31 1.2 2.1 3.1. 5. 6.13 7..21 9.2 50.36 51.7 52.59 53.73 5.90 56.0 57.2 5.50 59.7 61.00 62.29 7.3 7.9.5 9.0 9.7.3.9 11.6.2.9 13.6 1.3 15.0 15.7.5 17.2 1.0 1. 19.6. 21.2 22.1 22.9 23. 2.7 25.6 26.5 27.5 2. 29.. 31. 32.5 33.5 3.6 35.7 36. 37.9 39.0 0.2 1. 2.6 3. 5.0 6.3 7.6.36.06 11.7 11.50 11.23.97.71.7.23 9.991 9.763 9.51 9.326 9.1.9.71.521.333.150 7.971 7.79 7.629 7.6 7. 7.1 6.996 6.7 6.703 6.562 6.25 6.291 6.1 6.03 5.9 5.79 5.671 5.556 5.3 5.33 5.227 5.3 5.021.922.25.7.637 1.91 1.7 1.2 1.7 1.7 1.69 1.65 1.60 1.56 1.52 1.7 1.3 1.3 1.3 1.29 1.25 1. 1. 1.11 1.07 1.01 0.9 0.93 0.9 0. 0.0 0.75 0.71 0.66 0.61 0.57 0.52 0. 0.3 0.3 0.3 0.29 0.25 0. 0.15 0. 0.06 0.01 39.96 39.91 39.6 2.9.0 31.0 32.1 33.2 3.3 35. 36. 37.5 3.6 39.7 0.7 1. 2.9.0 5.1 6.2 7.2.3 9. 50.5 51.6 52.7 53. 5.9 56.0 57.1 5.2 59.2 60.3 61. 62.5 63.6 6.7 65. 66.9 6.0 69.1 70.2 71.3 72. 73.5 7.6 75.7 76. 77.9 607.5 607. 60.1 60.5 60. 609.2 609.5 609. 6.1 6.5 6. 611.1 611. 611. 6.1 6. 6.7 613.0 613.3 613.6 613.9 61.3 61.6 61.9 615.2 615.5 615. 6.1 6.3 6.6 6.9 617.2 617.5 617. 61.0 61.3 61.6 61.9 619.1 619. 619.7 619.9 6.2 6.5 6.7 621.0 0.0666.0690.071.073.0762 0.076.009.033.057.00 0.0909.092.0951.0975.099 0.22.5.69.92.1115 0.113.12.115.1.31 0.5.77..1323.136 0.1369.1392.115.137.0 0.13.1505.152.1551.1573 0.1596.1.1.63.6.170 1.362 1.3600 1.3579 1.355 1.3537 1.35 1.393 1.37 1.35 1.333 1.313 1.3393 1.3372 1.3352 1.3332 1.33 1.3292 1.3273 1.3253 1.323 1.321 1.3195 1.3176 1.3157 1.3137 1.311 1.99 1.1 1.62 1.3 1.25 1.06 1.29 1.2969 1.2951 1.2933 1.2915 1.297 1.279 1.261 1.23 1.223 1.9 1.2790 1.2773 1.2755 (continued)
Chapter. Engineering Data 9 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) Vapor s g Liquid s f Vapor h g Liquid h f Liquid I/v f Vapor V g psig psia 33 3 35 36 37 3 39 0 1 2 3 5 6 7 9 50 51 52 53 5 55 56 57 5 59 60 61 62 63 6 65 66 67 6 69 70 71 72 73 7 75 76 77 7 63.59 6.91 66.26 67.63 69.02 70.3 71.7 73.32 7.0 76.31 77.3 79.3 0.96 2.55.1 5.2 7.9 9.19 90.91 92.66 9.3 96.23 9.06 99.91 1. 3.7 5.6 7.6 9.6 111.6 113.6 115.7 117. 1.0 2.1.3 6.5. 131.1 133. 135.7 13.1.5 13.0 15. 17.9.9 50.2 51.6 52.9 5.3 55.7 57.2 5.6 60.1 61.6 63.1 6.7 66.3 67.9 69.5 71.1 72. 7.5 76.2 7.0 79.7 1.5 3. 5.2 7.1 9.0 90.9 92.9 9.9 96.9 9.9 1.0 3.1 5.3 7. 9.6 111. 11.1 1. 11.7 1.0 3. 5..3 1.7 133.2.57.59.373.29.7.6.0 3.971 3.97 3.23 3.752 3.62 3.61 3.57 3.1 3.1 3.355 3.29 3.23 3.176 3.119 3.063 3.00 2.95 2.902 2.51 2.00 2.751 2.703 2.656 2.6 2.565 2.5 2.77 2.35 2.393 2.352 2.3 2.273 2.235 2.197 2.1 2.5 2.09 2.055 2.021 39.2 39.77 39.72 39.67 39.63 39.5 39.5 39.9 39. 39.39 39.3 39.29 39.2 39.19 39.1 39. 39.05 39.00 3.95 3.90 3.5 3.0 3.75 3.70 3.65 3.60 3.55 3.50 3.5 3.0 3.35 3. 3.25 3. 3.15 3. 3.05 3.00 37.95 37.90 37. 37.79 37.7 37.69 37.6 37.5 79.0 0.1 1.2 2.3 3..6 5.7 6. 7.9 9.0 90.1 91.2 92.3 93.5 9.6 95.7 96. 97.9 99.1 0.2 1.3 2. 3.5.7 5. 6.9.1 9.2 1.3 111.5 1.6 113.7 11. 1.0 117.1 11.3 119. 1.5 1.7 2..0 5.1 6.2 7..5 9.7 621.2 621.5 621.7 622.0 622.2 622.5 622.7 623.0 623.2 623. 623.7 623.9 62.1 62. 62.6 62. 625.0 625.2 625.5 625.7 625.9 626.1 626.3 626.5 626.7 626.9 627.1 627.3 627.5 627.7 627.9 62.0 62.2 62. 62.6 62. 62.9 629.1 629.3 629. 629.6 629. 629.9 6.1 6.2 6. 0.17.1753.1775.1797.119 0.11.3.15.190.19 0.1952.197.1996.1.0 0.62.3.25.27.219 0.2171.2192.221.2236.2257 0.2279.21.2322.23.2365 0.237..2.251.273 0.29.2515.2537.255.2579 0.2601.2622.263.266.265.2706 1.273 1.2721 1.270 1.266 1.2669 1.2652 1.2635 1.261 1.2602 1.255 1.256 1.2552 1.2535 1.251 1.292 1.2 1.269 1.253 1.237 1.221 1.5 1.232 1.2372 1.2357 1.231 1.2325 1.23 1.229 1.2273 1.2263 1.227 1.2231 1.2213 1.21 1.213 1.2179 1.2155 1.2 1.25 1.21 1.95 1.0 1.65 1.50 1.35 1. (continued)
Chapter. Engineering Data 2 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) Vapor s g Liquid s f Vapor h g Liquid h f Liquid I/v f Vapor V g psig psia 79 0 1 2 3 5 6 (3) 7 9 90 91 92 93 9 95 96 97 9 99 0 1 2 3 5 6 7 9 1 111 1 113 11 115 1 117 11 119 1 1 2 3 5 150.5 153.0 155.6 15.3 1.0 3.7 6. 9.2 172.0 17. 177.7.6 13.6.6 19.6 192.7 195. 19.9 2.1 5.3.6 211.9 215.2 21.6 222.0 225. 22.9 232.5 236.0 239.7 23.3 27.0 250. 25.5 25. 262.2 266.2 270.1 27.1 27.2 22.3 26. 290.6 29. 299.1 3. 7. 135. 13.3.9 13.6.3 19.0 151.7 15.5 157.3 0.1 3.0 5.9.9 171.9 17.9 17.0 11.1 1.2 17. 190.6 193.9 197.2 0.5 3.9 7.3 2.7 21.2 217. 221.3 225.0 22.6 232.3 236.1 239. 23.7 27.5 251.5 255. 259. 263.5 267.6 271.7 275.9.1 2. 2.7 293.1 1.9 1.955 1.923 1.92 1.61 1.31 1.01 1.772 1.7 1.7 1.6 1.661 1.635 1.609 1.5 1.559 1.53 1.5 1.7 1.6 1.1 1.19 1.397 1.375 1.35 1.33 1.313 1.293 1.27 1.25 1.235 1.217 1.19 1. 1.3 1.15 1. 1.1 1.095 1.079 1.063 1.07 1.032 1.017 1.002 0.97 0.973 37.53 37. 37.3 37.37 37.32 37.26 37.21 37. 37.11 37.05 37.00 36.95 36.9 36. 36.7 36.73 36.67 36.62 36.56 36.51 36.5 36.0 36.3 36.29 36.23 36.1 36. 36.06 36.01 35.95 35.90 35. 35.7 35.72 35.67 35.61 35.55 35.9 35.3 35.3 35.32 35.26 35. 35.1 35.0 35.02 3.96 1. 132.0 133.1 13.3 135. 136.6 137. 13.9.1 11.2. 13.5 1.7 15. 17.0 1.2 19. 150.5 151.7 152.9 15.0 155.2 156. 157.6 15.7 159.9 1.1 2.3 3.5.6 5. 7.0.2 9. 170.6 171. 173.0 17.2 175. 176.6 177. 179.0.2 11..6 13.9 15.1 6.5 6.7 6. 631.0 631.1 631.3 631. 631.5 631.7 631. 631.9 632.0 632.1 632.2 632.3 632.5 632.6 632.6 632. 632.9 632.9 633.0 633.1 633.2 633.3 633. 633. 633.5 633.6 633.6 633.7 633.7 633. 633. 633.9 633.9 633.9 63.0 63.0 63.0 63.0 63.0 63.0 63.0 63.0 63.0 63.0 0.272.279.2769.2791.2 0.233.25.275.295.2917 0.2937.295.2979.00.21 0.1.62.3.3.35 0.315.36.317.37.322 0.32.3269.329.33.33 0.3351.3372.3392.313.333 0.353.37.395.3515.3535 3556 0.3576.3597.361.363.3659.3679 1.06 1.1991 1.1976 1.1962 1.197 1.1933 1.191 1.190 1.19 1.175 1.0 1. 1.132 1.11 1. 1.179 1.1775 1.1761 1.177 1.1733 1.1719 1.1705 1.91 1.77 1.63 1.9 1.35 1.21 1.07 1.1593 1.150 1.1566 1.1552 1.153 1.152 1.15 1.197 1.13 1.9 1.155 1.11 1.7 1.11 1.0 1.136 1.1372 1.135 1. Based on 0 for the saturated liquid at 0 F. 2. Inches of mercury below one standard atmosphere. 3. Standard cycle temperatures.
Temperature ( F) Saturation Pressure (Pounds Per Square Inch Absolute) Properties of Water Weight (Pounds Per Gallon) Chapter. Engineering Data Specific Gravity 60/60 F Conversion Factor, (1) lbs./hr. to GPM 32.05.35 1.0013.00199 0.17.35 1.0013.00199 50.171. 1.0007.00199 60.2653.33 1.0000.00199 70.3631.325.999.000 0.5069.31.9976.000 90.692.3.9963.000 0.992.29.996.001 1 1.27.267.9919.001 1 1.692.253.9901.001 1 2.2225.227.972.002 2.6.7.9.003 150 3.71..91.003 0.71.156.976.00 170 5.992.7.9752.005 7.5.09.9717.005 190 9.339.06.961.006 0 11.526.039.966.007 2 1.3.005.9605.00 2 1.696 7.996.959.00 2 17. 7.972.9566.009 2.969 7.901.90.002 260 35.29 7.22.936.00211 9.3 7.76.929.00215 0 67.013 7.662.919.00217 350 13.63 7.32.91.0022 00 27.31 7.172.606.00232 50 22.6 6.92.270.0021 500 60. 6.553.763.0025 550 5.2 6.132.735.00271 600 152.9 5.66.6796.0029 700 93.7 3.623.37.0060 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. gallons per cubic foot. 211
Chapter. Engineering Data 2 Properties of Saturated Steam ABSOLUTE PRESSURE VACUUM TEMPER HEAT LATENT HEAT TOTAL HEAT SPECIFIC VOLUME Lbs Per Sq In. P Inches of Hg VACUUM (INCHES OF Hg) ATURE t ( F) OF THE LIQUID (BTU/LB) OF EVAPOR ATION (BTU/LB) OF STEAM H g (BTU/LB) VOLUME (CU FT PER LB) 0. 0.25 0. 0.35 0.0 0.5 0.50 0.60 0.70 0.0 0.90 1.0 1.2 1. 1.6 1. 2.0 2.2 2. 2.6 2. 3.0 3.5.0.5 5.0 5.5 6.0 6.5 7.0 7.5.0.5 9.0 9.5.0 11.0.0 13.0 1.0 0.1 0.51 0.61 0.71 0.1 0.92 1.02 1.22 1.3 1.63 1.3 2.0 2. 2.5 3.26 3.66.07..9 5.29 5.70 6.11 7.13.1 9..1 11..22 13.23 1.25 15.27.29 17.31 1.32 19.3.36 22.0 2.3 26.7 2.50 29.51 29.1 29.31 29.21 29.11 29.00 2.90 2.70 2.9 2.29 2.09 27. 27. 27.07 26.66 26.26 25.5 25. 25.03 2.63 2.22 23.1 22.79 21.7.76 19.7 1.72 17.70.69 15.67 1.65 13.63.61 11.60.5 9.56 7.52 5.9 3.5 1.2 53.1 59. 6.7 6.93 72.6 76.3 79.5 5.21 90.0 9.3 9.2 1.7 7.92 113.26 117.99 2.23 6.0 9.62 132.9 135.9 13.79 11. 17.57 152.97 157.3 2.2 6. 170.06 173.56 176.5 179.9.6 15.6 1.2 190.0 193.21 197.75 1.96 5. 9.56 21.21 27.36 32.52 36.97 0.9.1 7.60 53.21 5.07 62.36 66.21 69.70 75.7 1. 5.91 90.1 93.99 97.52 0.79 3.3 6.6 9.37 115.6 1.6 5.71 1.13 13.19 137.96 11.7 1.76 17.6 150.79 153.57 156.22 15.75 1.17 5.73 9.96 173.91 177.61 63. 60.3 57. 5.9 52.7 50.7. 5.7 2.9 0. 3.3 36.3 32.7 29.6 26.9 2.5 22.2.2 1.3.5 1. 13.2 09.6 06. 03.6 01.0 99.5 996.2 99.1 992.1 990.2 9.5 96. 95.2 93.6 92.1 979.3 976.6 97.2 971.9 5.0 7.7 90.0 91.9 93.6 95.1 96. 9.9 11.0 12. 1.5.0 1.6 11. 11. 111.6 11.2 1117.7 1119.1 11.3 11.5 12.6 15.1 17.3 19.3 1131.1 1132.7 113.2 1135.6 1136.9 113.1 1139.3 1. 111. 1.3 113.3 115.0 1.6 11.1 119.5 1526.0 35.3 39.5 9.5 791.9 70.5 61. 50.0 66.9 11.7 36. 333.6.9 23.0 21.3 191. 173.73 15.5.3 135.7 6.65 11.71 2.72 90.63 1. 73.52 67.2 61.9 57.50 53.6 50.29 7.3.73 2.0 0.31 3.2 35.1 32.0.06 2.0
Chapter. Engineering Data 213 Properties of Saturated Steam PRESSURE (LBS. PER SQ IN.) TEMPER ATURE HEAT OF THE LATENT HEAT OF EVAPOR TOTAL HEAT OF SPECIFIC VOLUME Absolute P Gauge P t ( F) LIQUID (BTU/LB) EVAPOR ATION (BTU/LB) STEAM H g (BTU/LB) (CU FT PER LB) 1.696 15.0.0 17.0 1.0 19.0.0 21.0 22.0 23.0 2.0 25.0 26.0 27.0 2.0 29.0.0 31.0 32.0 33.0 3.0 35.0 36.0 37.0 3.0 39.0 0.0 1.0 2.0 3.0.0 5.0 6.0 7.0.0 9.0 50.0 51.0 52.0 53.0 5.0 0.0 0.3 1.3 2.3 3.3.3 5.3 6.3 7.3.3 9.3.3 11.3.3 13.3 1.3 15.3.3 17.3 1.3 19.3.3 21.3 22.3 23.3 2.3 25.3 26.3 27.3 2.3 29.3.3 31.3 32.3 33.3 3.3 35.3 36.3 37.3 3.3 39.3 2.00 213.03 2.32 219. 222.1 225.2 227.96 2.57 233.07 235.9 237.2.07 22.25 2.36 26.1 2.0 250.33 252.22 25.05 255. 257.5 259.2 260.95 262.57 26. 265.72 267.25 26.7 270.21 271.6 273.05 27. 275.0 277.13 27.5 279.7 21.01 22.26 23.9 2.70 25.90.07 11.11 1.2 17.56 190.56 193.2 196. 19.79 1.33 3.7 6.1.2 2.62 2.75 21.3 2.6 21.2 2.73 222.59 22.1 226.1 227.91 229.60 231.26 232.9 23. 236.03 237.55 239.0.51 21.95 23.36 2.75 26. 27.7 2.79 250.09 251.37 252.63 253.7 255.09 970.3 969.7 967.6 965.5 963.6 961.9 960.1 95. 956. 955.2 953.7 952.1 950.7 99.3 97.9 96.5 95.3 9.0 92. 91.6 90.3 939.2 93.0 936.9 935. 93.7 933.7 932.6 931.6 9.6 929.6 92.6 927.7 926.7 925. 92.9 92.0 923.0 922.2 921.3 9.5 1150. 1150. 1152.0 1153.1 115.2 1155.3 1156.3 1157.2 115.1 1159.0 1159. 10.6 11.3 12.0 12.7 13. 1.1 1.7 15. 16.0 16.5 17.1 17.6 1.2 1.7 19.2 19.7 1170.2 1170.7 1171.1 1171.6 1172.0 1172. 1172.9 1173.3 1173.7 117.1 117. 117. 1175.2 1175.6 26.0 26.29 2.75 23.39 22.17 21.0.09 19.192 1.375 17.627.93.3 15.715 15.170 1.663 1.19 13.76 13.3.90.572.226 11.9 11.5 11.29 11.015.750.9.25.029 9. 9.601 9.01 9.9 9.025..67.515.359..062 7.922 (continued)
Chapter. Engineering Data 21 Properties of Saturated Steam (continued) PRESSURE (LBS. PER SQ IN.) SPECIFIC VOLUME (CU FT PER LB) TOTAL HEAT OF STEAM H g (BTU/LB) LATENT HEAT OF EVAPOR ATION (BTU/LB) HEAT OF THE LIQUID (BTU/LB) TEMPER ATURE t ( F) Absolute P SPECIFIC VOLUME (CU FT PER LB) TOTAL HEAT OF STEAM H g (BTU/LB) LATENT HEAT OF EVAPOR ATION (BTU/LB) HEAT OF THE LIQUID (BTU/LB) TEMPER ATURE t ( F) Gauge P 55.0 56.0 57.0 5.0 59.0 60.0 61.0 62.0 63.0 6.0 65.0 66.0 67.0 6.0 69.0 70.0 71.0 72.0 73.0 7.0 75.0 76.0 77.0 7.0 79.0 0.0 1.0 2.0 3.0.0 5.0 6.0 7.0.0 9.0 90.0 91.0 92.0 93.0 9.0 95.0 96.0 97.0 9.0 99.0 0.3 1.3 2.3 3.3.3 5.3 6.3 7.3.3 9.3 50.3 51.3 52.3 53.3 5.3 55.3 56.3 57.3 5.3 59.3 60.3 61.3 62.3 63.3 6.3 65.3 66.3 67.3 6.3 69.3 70.3 71.3 72.3 73.3 7.3 75.3 76.3 77.3 7.3 79.3 0.3 1.3 2.3 3.3.3 27.07 2.23 29.37 290.50 291.61 292.71 293.79 29.5 295.90 296.9 297.97 29.99 299.99 0.9 1.96 2.92 3..3 5.76 6.6 7.60.50 9.0 3.29 311. 3.03 3.9 313.7 31.59 315.2 3.25 317.07 317. 31.6 319. 3.27 321.06 321.3 322.60 323.36 32. 32.7 325.61 326.35 327.0 256. 257.50 25.67 259.2 260.96 262.09 263. 26. 265.3 266.5 267.50 26.55 269.5 270.60 291.61 272.61 273.60 27.57 275.5 276.9 277.3 27.37 279..21 21. 22.02 22.91 23.79 2.66 25.53 26.39 27.2 2.0 2.91 29.7 290.56 291.3 292.1 292.9 293.7 29.56 295.3 296. 296.9 297.65 919.6 91. 917.9 917.1 9.3 915.5 91.7 913.9 913.1 9.3 911.6 9. 9.1 909. 90.7 907.9 907.2 906.5 905. 905.1 90.5 903.7 903.1 902. 901.7 901.1 900. 99.7 99.1 9.5 97. 97.2 96.5 95.9 95.3 9.7 9.1 93.5 92.9 92.3 91.7 91.1 90.5 9.9 9. 1175.9 1176.3 1176.6 1176.9 1177.3 1177.6 1177.9 117.2 117.5 117. 1179.1 1179. 1179.7 1.0 1.3 1.6 1. 111.1 111.3 111.6 111.9 1.1 1. 1.6 1. 113.1 113.3 113.5 113. 11.0 11.2 11. 11.6 11. 115.1 115.3 115.5 115.7 115.9 1.1 1.2 1. 1.6 1. 117.0 7.77 7.656 7.529 7.07 7.29 7.175 7.06 6.957 6.53 6.752 6.655 6.560 6.6 6.37 6.291 6.6 6. 6.0 5.966 5.90 5. 5.73 5.673 5.60 5.537 5.72 5.0 5.36 5.25 5.226 5. 5.111 5.055 5.001.9.96.5.796.77.699.652.606.561.517.7 (continued)
Chapter. Engineering Data 215 Properties of Saturated Steam (continued) PRESSURE (LBS. PER SQ IN.) SPECIFIC VOLUME (CU FT PER LB) TOTAL HEAT OF STEAM H g (BTU/LB) LATENT HEAT OF EVAPOR ATION (BTU/LB) HEAT OF THE LIQUID (BTU/LB) TEMPER ATURE t ( F) Absolute P SPECIFIC VOLUME (CU FT PER LB) TOTAL HEAT OF STEAM H g (BTU/LB) LATENT HEAT OF EVAPOR ATION (BTU/LB) HEAT OF THE LIQUID (BTU/LB) TEMPER ATURE t ( F) Gauge P 0.0 1.0 2.0 3.0.0 5.0 6.0 7.0.0 9.0 1.0 111.0 1.0 113.0 11.0 115.0 1.0 117.0 11.0 119.0 1.0 1.0 2.0 3.0.0 5.0 6.0 7.0.0 9.0 1.0 131.0 132.0 133.0 13.0 135.0 136.0 137.0 13.0 139.0.0 11.0.0 13.0 1.0 5.3 6.3 7.3.3 9.3 90.3 91.3 92.3 93.3 9.3 95.3 96.3 97.3 9.3 99.3 0.3 1.3 2.3 3.3.3 5.3 6.3 7.3.3 9.3 1.3 111.3 1.3 113.3 11.3 115.3 1.3 117.3 11.3 119.3 1.3 1.3 2.3 3.3.3 5.3 6.3 7.3.3 9.3 327.1 32.53 329.25 329.96 3.66 331.36 332.05 332.7 333.2 33. 33.77 335. 336.11 336.77 337.2 33.07 33.72 339.36 339.99.62 31.25 31. 32.50 33.11 33.72 3.33 3.9 35.5 36.13 36.73 37.32 37.90 3. 39.06 39.6 350.21 350.7 351.35 351.91 352.7 353.02 353.57 35. 35.67 355.21 29.0 299.15 299.90 0.6 1.37 2. 2.2 3.5.26.97 5.66 6.37 7.06 7.75.3 9.11 9.79 3.6 311. 311.7 3. 313. 313.75 31.0 315.0 315.6 3.31 3.9 317.57 31.19 31.1 319.3 3.0 3.65 321.25 321.5 322.5 323.05 323.6 32.23 32.2 325.0 325.9 326.56 327.13..2 7.6 7.1 6.5 6.0 5..9.3 3.7 3.2 2.6 2.1 1.6 1.1 0.6 0.0 79.5 79.0 7. 77.9 77. 76.9 76. 75.9 75. 7.9 7. 73.9 73. 72.9 72.5 72.0 71.5 71.0 70.6 70.1 69.6 69.1 6.7 6.2 67.7 67.2 66.7 66.3 117.2 117. 117.5 117.7 117.9 11.1 11.2 11. 11.6 11.7 11.9 119.0 119.2 119. 119.5 119.7 119. 1190.0 1190.1 1190.2 1190. 1190.5 1190.7 1190. 1190.9 1191.1 1191.2 1191.3 1191.5 1191.6 1191.7 1191.9 1192.0 1192.1 1192.2 1192. 1192.5 1192.6 1192.7 1192.9 1193.0 1193.1 1193.2 1193.3 1193..32.391.350.3.271.232.19.157.1.0.09.015 3.91 3.97 3.91 3.2 3.50 3.19 3.7 3.75 3.72 3.699 3.670 3.62 3.61 3.57 3.560 3.533 3.507 3.1 3.55 3. 3.05 3.31 3.357 3.333 3.3 3.27 3.26 3.22 3.2 3.19 3.177 3.155 3.13 (continued)
Chapter. Engineering Data 2 Properties of Saturated Steam (continued) PRESSURE (LBS. PER SQ IN.) SPECIFIC VOLUME (CU FT PER LB) TOTAL HEAT OF STEAM H g (BTU/LB) LATENT HEAT OF EVAPOR ATION (BTU/LB) HEAT OF THE LIQUID (BTU/LB) TEMPER ATURE t ( F) Absolute P SPECIFIC VOLUME (CU FT PER LB) TOTAL HEAT OF STEAM H g (BTU/LB) LATENT HEAT OF EVAPOR ATION (BTU/LB) HEAT OF THE LIQUID (BTU/LB) TEMPER ATURE t ( F) Gauge P 15.0.0 17.0 1.0 19.0 150.0 152.0 15.0 156.0 15.0 0.0 2.0.0 6.0.0 170.0 172.0 17.0 176.0 17.0.0.0 1.0.0 1.0 190.0 192.0 19.0 196.0 19.0 0.0 5.0 2.0 215.0 2.0 225.0 2.0 235.0.0 25.0 250.0 255.0 260.0 265.0 270.0 1.3 131.3 132.3 133.3 13.3 135.3 137.3 139.3 11.3 13.3 15.3 17.3 19.3 151.3 153.3 155.3 157.3 159.3 1.3 3.3 5.3 7.3 9.3 171.3 173.3 175.3 177.3 179.3 11.3 13.3 15.3 190.3 195.3 0.3 5.3 2.3 215.3 2.3 225.3 2.3 235.3.3 25.3 250.3 255.3 355.76 356.29 356.3 357.36 357.9 35.2 359.6 360.9 361.52 362.53 363.53 36.53 365.51 366. 367.5 36.1 369.35 370.29 371.22 372.1 373.06 373.96 37.6 375.75 376.6 377.51 37.3 379.2..95 31.79 33.6 35.90 37.9 39.6 391.79 393.6 395.5 397.37 399.1 00.95 02.70 0.2 06.11 07.7 327.70 32.27 32.3 329.39 329.95 3.51 331.61 332.70 333.79 33.6 335.93 336.9 33.02 339.05.07 31.09 32. 33. 3.09 35.06 36.03 37.00 37.96 3.92 39.6 350.79 351.72 352.6 353.55 35.6 355.36 357.5 359.77 361.91 36.02 366.09 36.13 370.1 372. 37.0 376.00 377.9 379.76 31.60 33.2 65. 65.3 6.9 6.5 6.0 63.6 62.7 61. 60.9 60.0 59.2 5.3 57.5 56.6 55.7 5.9 5.1 53.3 52. 51.6 50. 50.0 9.2. 7.6 6. 6.1 5.3.5 3.7 3.0 1.1 39.2 37. 35.6 33. 32.0.3 2.5 26. 25.1 23. 21..1 1.5 1193.5 1193.6 1193. 1193.9 119.0 119.1 119.3 119.5 119.7 119.9 1195.1 1195.3 1195.5 1195.7 1195. 1196.0 1196.2 1196. 1196.5 1196.7 1196.9 1197.0 1197.2 1197.3 1197.5 1197.6 1197. 1197.9 119.1 119.2 119. 119.7 1199.0 1199.3 1199.6 1199.9.1..6.9 11.1 11.3 11.5 11.7 11.9 3.11 3.09 3.07 3.05 3.03 3.015 2.977 2.90 2.90 2.69 2.3 2.01 2.76 2.736 2.705 2.675 2.65 2.6 2.57 2.559 2.532 2.505 2.79 2.5 2.29 2.0 2. 2.356 2.333 2.3 2.2 2.23 2.13 2.13 2.07 2.022 1.9992 1.9579 1.913 1.03 1.3 1.06 1.77 1.722 1.77 (continued)
Chapter. Engineering Data 217 Properties of Saturated Steam (continued) PRESSURE (LBS. PER SQ IN.) SPECIFIC VOLUME (CU FT PER LB) TOTAL HEAT OF STEAM H g (BTU/LB) LATENT HEAT OF EVAPOR ATION (BTU/LB) HEAT OF THE LIQUID (BTU/LB) TEMPER ATURE t ( F) Absolute P SPECIFIC VOLUME (CU FT PER LB) TOTAL HEAT OF STEAM H g (BTU/LB) LATENT HEAT OF EVAPOR ATION (BTU/LB) HEAT OF THE LIQUID (BTU/LB) TEMPER ATURE t ( F) Gauge P 275.0.0 25.0 290.0 295.0 0.0 3.0.0 360.0.0 00.0.0 0.0 60.0 0.0 500.0 5.0 50.0 560.0 50.0 600.0 6.0 60.0 660.0 60.0 700.0 7.0 70.0 760.0 70.0 00.0.0 0.0 60.0 0.0 900.0 9.0 90.0 960.0 90.0 00.0 50.0 10.0 1150.0.0 260.3 265.3 270.3 275.3.3 25.3 5.3 325.3 35.3 365.3 35.3 05.3 25.3 5.3 65.3 5.3 505.3 525.3 55.3 565.3 55.3 605.3 625.3 65.3 665.3 65.3 705.3 725.3 75.3 765.3 75.3 05.3 25.3 5.3 65.3 5.3 905.3 925.3 95.3 965.3 95.3 35.3 5.3 1135.3 115.3 09.3 11.05.65 1.23 15.79 17.33 23.29 2.97 3.0 39.60.59 9.39 5.02 5.50 62.2 67.01 71.07 75.01 7.5 2.5 6.21 9.75 93.21 96.5 99. 503. 506.25 509.3 5.36 515.33 51.23 521.0 523. 526.63 529.33 531.9 53.59 537. 539.6 52.17 5.61 550.57 556.31 561.6 567.22 35.21 36.9 3.73 390.6 392. 393. 00.39 06.66.67 1.5 2.0 29. 3.6 39.7.6 9. 5.1 5.6 63.0 67. 71.6 75.7 79. 3. 7.7 91.5 95.3 99.0 502.6 506.2 509.7 513.2 5.6 5.0 523.3 526.6 529. 533.0 536.2 539.3 52. 550.0 557. 56.6 571.7.9 15.3 13.7.1.5 09.0 03.0 797.1 791. 75. 70.5 775.2 770.0 76.9 759.9 755.0 750.1 75. 70. 736.1 731.6 727.2 722.7 71.3 71.0 709.7 705. 701.2 697.1 692.9 6.9 6. 60. 676. 672. 66. 66.9 661.0 657.1 653.3 69. 639.9 6. 621.0 611.7.1.3..6.7. 13. 13.7 1.1 1.3 1.5 1.6 1.6 1.6 1.5 1. 1.2 1.0 13. 13.5 13.2.9.5.1 11.7 11.2.7.2 1199.7 1199.1 119.6 119.0 1197. 1196. 1196.1 1195. 119.7 119.0 1193.3 1192.6 1191. 119.9 117. 115.6 113. 1.60 1.6511 1.622 1.595 1.569 1.533 1.5 1.365 1.295 1.2222 1.13 1.61 1.0556 1.009 0.9670 0.927 0.915 0.57 0.265 0.7973 0.769 0.70 0.719 0.6971 0.6757 0.655 0.6362 0.6 0.6007 0.53 0.567 0.553 0.5396 0.5260 0.51 0.5006 0.6 0.772 0.663 0.557 0.56 0.21 0.001 0.2 0.3619 (continued)
Chapter. Engineering Data PRESSURE (LBS. PER SQ IN.) Absolute P 50.0.0 1350.0 0.0 150.0 Gauge P 35.3 5.3 1335.3 135.3 135.3 Properties of Saturated Steam (continued) TEMPER ATURE t ( F) 572.2 577.6 52.35 57. 591.73 HEAT OF THE LIQUID (BTU/LB) 57.6 55. 592.1 59.7 605.2 LATENT HEAT OF EVAPOR ATION (BTU/LB) 602. 593.2 5.0 57.7 565.5 TOTAL HEAT OF STEAM H g (BTU/LB) 111.0 117.6 1176.1 1173. 1170.7 SPECIFIC VOLUME (CU FT PER LB) 0.350 0.3293 0.31 0. 0.2 1500.0 00.0 1700.0 0.0 1900.0 15.3 155.3 5.3 175.3 15.3 596.23 60.90 613.15 621.03 62.5 611.6 62.1 636.3 6.3 660.1 556.3 53.0 519.6 501.1 2. 17.9 12.1 1155.9 119. 1. 0.2765 0.25 0.235 0.2179 0.21 00.0 20.0 20.0 20.0 0.0 195.3 5.3 215.3 225.3 235.3 635.2 62.77 69.6 655.91 662. 671.7 63.3 69. 706.5 71. 63..1 2. 03.9 32.7 1135.1 17. 1119.2 11. 11.1 0.17 0.176 0.25 0.1513 0.7 2500.0 2600.0 2700.0 0.0 2900.0 25.3 255.3 265.3 275.3 25.3 66.13 673.9 679.55 6.99 690.26 7.6 73.0 756.2 770.1 75. 360.5 337.2 3.1 2.7 253.6 91.1 0.2 6.3 5. 39.0 0.17 0.13 0.13 0.35 0.097 00.0 30.0.0 36.2 295.3 5.3 315.3 3191.5 695.36 700.31 705.11 705.0 02.5 25.0 72. 902.7 217..1 62.0 0.0.3 993.1 93. 902.7 0.05 0.0753 0.050 0.0503 21
Chapter. Engineering Data Properties of Superheated Steam = specific volume, cubic feet per pound h g = total heat of steam, Btu per pound PRESSURE (LBS PER SQ IN) SAT. TOTAL TEMPERATURE DEGREES FAHRENHEIT (t) Absolute P Gauge P 1.696 0.0 2.00.0 5.3 227.96.0 15.3 250.33 0.0 25.3 267.25 50.0 35.3 21.01 60.0 5.3 292.71 70.0 55.3 2.92 0.0 65.3 3.03 90.0 75.3 3.27 0.0 5.3 327.1 TEMP. t 360 00 0 0 500 600 700 00 900 00 33.03 h g 21.1 2.21 h g.3.072 h g 1.6.001 h g.9 9.557 h g 15.2 7.927 h g 13. 6.762 h g 11.5 5. h g 19.7 5. h g 17.7.663 h g 15.7 3.6 39.9 25.3 39.2.97 37.9.62 36.5.065 35.1.357 33.6 7.136 32.1 6.2.7 5.50 29.1.937 27.6 36.32 5. 26.65 5.2 17.71 57.0 13.27 55.9.567 5.7.779 53.5 7.502 52.3 6.5 51.1 5.799 9. 5.2.6 37.96 77.6 27.6 77.1 1.52 76.2 13.62 75.2 11.062 7.2 9.196 73.2 7.63 72.2 6.62 71.1 6.0 70.1 5.62 69.0 3.7 7.1 2.6 6.6 1.933 5.7 1.. 11.9 3.9 9.03 3.0.01 2.0 7.0 1.1 6.225 1.1 5.59 79.1 2.6 133. 31.7 133..95 1333. 15.6 1333.1.532 1332.5.27 1331..92 1331.1 7.797 13.5 6.9 1329. 6.21 1329.1 6.9 133.2 3.7 132.9 22.96 132. 17.19 131.9 13.7 131. 11.1 1.9 9.796 1..562 1379.9 7.603 1379. 6.35 137.9 51.00 132.3 37.6 132.1 2.96 131.7 1.702 131.3 1.950 1.9.9 1.5.662 1.1 9.322 9.7.279 9.3 7.6.9 55.07.3 0.5.1 26.95 11.. 11..152 11.1 13.52. 11.52.5.077.1.952 179..052 179.5 59.13 1533.1 3. 1533.0 2.95 1532.7 21.70 1532. 17.352 1532.1 1.5 1531.9.33 1531.6. 1531.3 9.623 1531.0.656 15. 67.25 37.5 9.1 37. 32.93 37.2 2.69 37.0 19.77 36..51 36.6 1.097 36.3.332 36.2.959 35.9 9.60 35.7 Continued 219
Chapter. Engineering Data Properties of Superheated Steam (continued) = specific volume, cubic feet per pound h g = total heat of steam, Btu per pound PRESSURE (LBS PER SQ IN) SAT. TOTAL TEMPERATURE DEGREES FAHRENHEIT (t) Absolute P Gauge P 1.0 5.3 31.25.0 5.3 353.02 0.0 15.3 363.53.0 5.3 373.06 0.0 15.3 31.79 2.0 5.3 39.6.0 225.3 397.37 260.0 25.3 0.2.0 265.3 11.05 0.0 25.3 17.33 TEMP. t 360 00 0 0 500 600 700 00 900 00 3. h g 11.6 3.25 h g 1197.3 - - - h g - - - - - - h g - - - - - - h g - - - - - - h g - - - - - - h g - - - - - - h g - - - - - - h g - - - - - - h g - - -.01 2. 3.6 21.1 3.00 17.6 2.69 1.0 2.361.3 2.5.5 1.9276.5 - - - - - - - - - - - - - - - - - -.7 6.0 3.667 3.3 3.17 1.6 2.13 37. 2.513 3.9 2.267 31.9 2.062 2. 1.2 25.7 1.73 22. 1.6090 19.1.527 66.90 3.60 6.7 3.359 62. 2.969 60.2 2.656 57. 2.00 55. 2.17 53.0 2.006 50.5 1.5 7.9 1.75 5.3.636 77.2 3.95 75.2 3.3 73.1 3.0 71.0 2.726 6.9 2.65 66.7 2.27 6.5 2.063 62.3 1.907 60.0 1.7675 57.6 5.5 1327.7.13 1326. 3.9 1325.0 3.11 1323.5 3.060 1322.1 2.772 13.7 2.533 1319.2 2.3 1317.7 2.156 13.2 2.005 131.7 5.63 1377..61 1376..2 1375.7 3.76 137.7 3. 1373.6 3.066 1372.6 2.0 1371.5 2.52 1370. 2.392 1369. 2.227 136.3 6.195.1 5.1 7.3.631 6..1 5.6 3.693. 3.352.0 3.06 3.2 2.27 2.3 2.621 1.5 2.2 1.6 6.702 17. 5.73 17.2 5.015 177.5.52 176..002 176.2 3.63 175.5 3.327 17. 3.067 17.2 2.5 173.5 2.652 172. 7.7 15.2 6.172 1529.7 5.396 1529.1.792 152.6.9 152.0 3.913 1527.5 3.5 1526.9 3.5 1526.3 3.066 1525. 2.59 1525.2.2 35.3 7.035 3.9 6.152 3.5 5.66 3.1.917 33.7.67 33.3.093 32.9 3.776 32.5 3.50 32.1 3.269 31.7 Continued 2
Chapter. Engineering Data Properties of Superheated Steam (continued) = specific volume, cubic feet per pound h g = total heat of steam, Btu per pound PRESSURE (LBS PER SQ IN) SAT. TOTAL TEMPERATURE DEGREES FAHRENHEIT (t) Absolute P Gauge P 3.0 5.3 23.29.0 325.3 2.97 360.0 35.3 3.0 TEMP. t 360 00 0 0 500 600 700 00 900 00 - - - h g - - - - - - h g - - - - - - h g - - - - - - - - - - - - - - - - - - - - - 1.950 15.6 1.391.1 1.1 1. 1.595 2.6 1.91 39.9 1.0 37.1 1.672 55.2 1.5 52. 1.6 50.3 1.73 1313.2 1.7569 1311.6 1.6533 13.1 2.03 1367.2 1.9562 1366.1 1.31 1365.0 2.25 119. 2.17 119.0 2.025 11.1 2.3 172.1 2.33 171.5 2.2 170. 2.67 152.7 2.51 152.1 2.376 1523.5 3.063 31.3 2.1.9 2.719.5 Continued 221
Chapter. Engineering Data Properties of Superheated Steam (continued) = specific volume, cubic feet per pound h g = total heat of steam, Btu per pound PRESSURE (LBS PER SQ IN) SAT. TOTAL TEMPERATURE DEGREES FAHRENHEIT (t) Absolute P Gauge P.0 365.3 39.60 TEMP. t 500 50 600 60 660 700 70 00 900 00 1.36 h g 7.7 1. 73.1 1.5605 1.5 1.635 1331.0 1.6707 132.0 1.719 1363. 1.11 135.3 1.919 117.3 2.03 170.1 2.29 1523.0 2.575.0 00.0 35.3.59 1.251 h g 5.1 1.3652 71.0 1.770.9 1.50 1329.6 1.527 1. 1.650 1362.7 1.7177 13.3 1.1 1. 1.9767 9. 2.13 1522. 2.5 29.6.0 05.3 9.39 1.215 h g 2.5 1.2935 6.9 1.01 15.3 1.697 132.3 1.50 1339.5 1.56 1361.6 1.632 133.3 1.7267 115.5 1.02.7 2.031 1521.9 2.327 29.2 0.0 25.3 5.02 1.1526 h g 39. 1.222 66.7 1.3327 13.6 1.39 1326.9 1.6 133.2 1.93 1360. 1.559 132.3 1.65 11.7 1.7925.1 1.936 1521.3 2.2 2. 60.0 5.3 5.50 1.09 h g 37.0 1.5 6.5 1.269 12.0 1.333 1325. 1.36 1336.9 1.250 1359.3 1.2 131.3 1.5711 113. 1.7 7. 1.50 15.7 2.2 2. 0.0 65.3 62.2 1.017 h g 3.2 1.113 62.3 1.22.3 1.2737 132.0 1.3 1335.6 1.3622 135.2 1.193 1.3 1.5031 1.9 1.6390 6.7 1.77 15.2 2.033 2.0 500.0 5.3 67.01 0.9927 h g 31.3 1.0633 60.0 1.1591 9.6 1.21 1322.6 1.27 133.2 1. 1357.0 1.3596 1379.3 1.05 1.1 1.5715 6.0 1.6996 1519.6 1.950 27.6 5.0 505.3 71.07 0.973 h g 2.3 1.06 57.7 1.11 96.9 1.1 1321.1 1.1962 1332.9 1.2511 1355. 1.5 137.2 1.326 111.2 1.5091 5.3 1.6326 1519.0 1.73 27.2 50.0 525.3 75.01 0.9052 h g 25.3 0.9733 55. 1.066 95.2 1.11 1319.7 1.15 1331.5 1.17 135.6 1.2535 1377.2 1.3291 1.3 1.51.6 1.5707 151.5 1.039 26. 560.0 55.3 7.5 0.659 h g 22.2 0.93 53.0 1.022 93. 1.0775 131.2 1.1 13.2 1.155 1353.5 1.60 1376.1 1.279 9. 1.397 3.9 1.5132 1517.9 1.735 26. 50.0 565.3 2.5 0.291 h g 19.0 0.95 50.5 0.9 91.7 1.036 13.7 1.0627 132. 1.1331 1352.3 1.19 1375.1 1.2331.6 1.379 3.2 1.596 1517.3 1.6776 26.0 600.0 55.3 6.21 0.797 h g 15.7 0.602.1 0.963 9.9 0.99 1315.2 1.021 1327. 1.0732 1351.1 1.17 137.0 1.199 7.7 1.13 2.5 1.096 15.7 1.6 25.5 222