University of Idaho Department of Chemical Engineering DOUBLE PIPE HEAT EXCHANGER Prediction Program Rel. 2/8/92 Ch. E. 434 Laboratory D. C. Drown Date: Jan 25, 2008 Time: 0:56:53 Input File Name: G7-7.dat Start Iteration Loop Flow = 3.300 GPM Inlet Temperature = 15.56 C Steam Temperature = 111.29 T Wall Guess = 99.00 T Out Guess = 71.00 Steam Pressure = 7.00 PSIG + Temperature = 232.319 Deg F H Vaporization = 957.24 BTU/LB Density= 0.053708 LB/FT3 Barometric Pressure = 14.6955 PSIA Steam Pressure = 7.00 PSIG + Temperature = 111.286 Deg C H Vaporization = 2226645. J/Kg Density = 0.8603 Kg/M3 Fouling - Inside = .0000000 Outside = .0000000 Temperature Convergence to 0.010 Degrees N T Wall T Out Re No. H Inside H Outside U C C Watts / Sq. Meter C Units = F F BTU / Sq. Feet F 1 54.4 21.2 42984. 24614. 10081. 5984. 129.9 70.2 4335. 1775. 1054. Dittus-Boelter T film Pr.33 = 4519. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 4335. Nusselt Ent. = 5717. Sieder-Tate = 4850. Sleicher-Rouse = 4622. Petukhov-Popov = 4907. T V McAdams T bulk = 4166. 65.1 22.79 McAdams T film = 5031. 97.5 2 57.2 26.7 46952. 25733. 10264. 6150. 135.0 80.0 4532. 1808. 1083. Dittus-Boelter T film Pr.33 = 4701. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 4532. Nusselt Ent. = 5948. Sieder-Tate = 5083. Sleicher-Rouse = 4883. Petukhov-Popov = 5122. T V McAdams T bulk = 4434. 75.1 22.79 McAdams T film = 5234. 105.1 3 60.1 32.0 51276. 26872. 10456. 6318. 140.1 89.6 4733. 1841. 1113. Dittus-Boelter T film Pr.33 = 4888. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 4733. Nusselt Ent. = 6183. Sieder-Tate = 5319. Sleicher-Rouse = 5147. Petukhov-Popov = 5337. T V McAdams T bulk = 4693. 84.8 22.80 McAdams T film = 5432. 112.5 4 62.9 37.1 55959. 28027. 10655. 6488. 145.2 98.8 4936. 1877. 1143. Dittus-Boelter T film Pr.33 = 5077. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 4936. Nusselt Ent. = 6422. Sieder-Tate = 5559. Sleicher-Rouse = 5410. Petukhov-Popov = 5549. T V McAdams T bulk = 4943. 94.2 22.80 McAdams T film = 5625. 119.7 5 65.7 42.0 60995. 29192. 10862. 6660. 150.3 107.6 5141. 1913. 1173. Dittus-Boelter T film Pr.33 = 5267. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 5141. Nusselt Ent. = 6663. Sieder-Tate = 5801. Sleicher-Rouse = 5670. Petukhov-Popov = 5757. T V McAdams T bulk = 5185. 103.2 22.80 McAdams T film = 5814. 126.7 6 68.5 46.7 66368. 30361. 11078. 6834. 155.3 116.1 5347. 1951. 1204. Dittus-Boelter T film Pr.33 = 5458. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 5347. Nusselt Ent. = 6904. Sieder-Tate = 6044. Sleicher-Rouse = 5927. Petukhov-Popov = 5960. T V McAdams T bulk = 5417. 111.9 22.80 McAdams T film = 5996. 133.6 Flow Rate = 3.300 GPM Steam Pressure = 7.00 PSIG Temperature IN = 15.6 Degrees C 60.0 F Temperature OUT = 46.7 Degrees C 116.1 F Steam Temperature = 111.3 Degrees C 232.3 F Length Wall Temp. Temp. Water Out Inches C F C F 11.667 54.4 129.9 21.2 70.2 23.333 57.2 135.0 26.7 80.0 35.000 60.1 140.1 32.0 89.6 46.667 62.9 145.2 37.1 98.8 58.333 65.7 150.3 42.0 107.6 70.000 68.5 155.3 46.7 116.1 ..PAGE University of Idaho Department of Chemical Engineering DOUBLE PIPE HEAT EXCHANGER Prediction Program Rel. 2/8/92 Ch. E. 434 Laboratory D. C. Drown Date: Jan 25, 2008 Time: 0:57:11 Input from KEYBOARD for Case Number: 2 Start Iteration Loop Flow = 2.000 GPM Inlet Temperature = 15.56 C Steam Temperature = 111.29 T Wall Guess = 72.00 T Out Guess = 50.00 Steam Pressure = 7.00 PSIG + Temperature = 232.319 Deg F H Vaporization = 957.24 BTU/LB Density= 0.053708 LB/FT3 Barometric Pressure = 14.6955 PSIA Steam Pressure = 7.00 PSIG + Temperature = 111.286 Deg C H Vaporization = 2226645. J/Kg Density = 0.8603 Kg/M3 Fouling - Inside = .0000000 Outside = .0000000 Temperature Convergence to 0.010 Degrees N T Wall T Out Re No. H Inside H Outside U C C Watts / Sq. Meter C Units = F F BTU / Sq. Feet F 1 65.6 23.6 26537. 16641. 10852. 5260. 150.1 74.6 2931. 1911. 926. Dittus-Boelter T film Pr.33 = 3218. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 2931. Nusselt Ent. = 4071. Sieder-Tate = 3372. Sleicher-Rouse = 3071. Petukhov-Popov = 3248. T V McAdams T bulk = 2829. 67.3 13.80 McAdams T film = 3569. 108.7 2 68.7 31.4 30141. 17731. 11093. 5482. 155.6 88.5 3123. 1954. 966. Dittus-Boelter T film Pr.33 = 3389. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 3123. Nusselt Ent. = 4287. Sieder-Tate = 3595. Sleicher-Rouse = 3323. Petukhov-Popov = 3454. T V McAdams T bulk = 3084. 81.5 13.81 McAdams T film = 3746. 118.6 3 71.8 38.8 34210. 18849. 11353. 5708. 161.2 101.8 3320. 1999. 1005. Dittus-Boelter T film Pr.33 = 3562. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 3320. Nusselt Ent. = 4507. Sieder-Tate = 3822. Sleicher-Rouse = 3575. Petukhov-Popov = 3659. T V McAdams T bulk = 3327. 95.2 13.81 McAdams T film = 3918. 128.2 4 74.9 45.7 38731. 19982. 11635. 5938. 166.9 114.4 3519. 2049. 1046. Dittus-Boelter T film Pr.33 = 3737. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 3519. Nusselt Ent. = 4728. Sieder-Tate = 4051. Sleicher-Rouse = 3824. Petukhov-Popov = 3860. T V McAdams T bulk = 3559. 108.1 13.81 McAdams T film = 4085. 137.5 5 78.0 52.3 43667. 21115. 11939. 6170. 172.5 126.2 3719. 2103. 1087. Dittus-Boelter T film Pr.33 = 3910. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 3719. Nusselt Ent. = 4946. Sieder-Tate = 4279. Sleicher-Rouse = 4066. Petukhov-Popov = 4052. T V McAdams T bulk = 3777. 120.3 13.81 McAdams T film = 4244. 146.4 6 81.1 58.5 48945. 22231. 12266. 6403. 178.0 137.2 3915. 2160. 1128. Dittus-Boelter T film Pr.33 = 4077. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 3915. Nusselt Ent. = 5158. Sieder-Tate = 4503. Sleicher-Rouse = 4297. Petukhov-Popov = 4234. T V McAdams T bulk = 3982. 131.7 13.81 McAdams T film = 4396. 154.8 Flow Rate = 2.000 GPM Steam Pressure = 7.00 PSIG Temperature IN = 15.6 Degrees C 60.0 F Temperature OUT = 58.5 Degrees C 137.2 F Steam Temperature = 111.3 Degrees C 232.3 F Length Wall Temp. Temp. Water Out Inches C F C F 11.667 65.6 150.1 23.6 74.6 23.333 68.7 155.6 31.4 88.5 35.000 71.8 161.2 38.8 101.8 46.667 74.9 166.9 45.7 114.4 58.333 78.0 172.5 52.3 126.2 70.000 81.1 178.0 58.5 137.2 ..PAGE University of Idaho Department of Chemical Engineering DOUBLE PIPE HEAT EXCHANGER Prediction Program Rel. 2/8/92 Ch. E. 434 Laboratory D. C. Drown Date: Jan 25, 2008 Time: 0:57:31 Input from KEYBOARD for Case Number: 3 Start Iteration Loop Flow = 1.000 GPM Inlet Temperature = 15.56 C Steam Temperature = 111.29 T Wall Guess = 90.00 T Out Guess = 75.00 Steam Pressure = 7.00 PSIG + Temperature = 232.319 Deg F H Vaporization = 957.24 BTU/LB Density= 0.053708 LB/FT3 Barometric Pressure = 14.6955 PSIA Steam Pressure = 7.00 PSIG + Temperature = 111.286 Deg C H Vaporization = 2226645. J/Kg Density = 0.8603 Kg/M3 Fouling - Inside = .0000000 Outside = .0000000 Temperature Convergence to 0.010 Degrees N T Wall T Out Re No. H Inside H Outside U C C Watts / Sq. Meter C Units = F F BTU / Sq. Feet F 1 80.9 27.8 13696. 9708. 12242. 4067. 177.6 82.1 1710. 2156. 716. Dittus-Boelter T film Pr.33 = 2013. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1710. Nusselt Ent. = 2546. Sieder-Tate = 2037. Sleicher-Rouse = 1775. Petukhov-Popov = 1853. T V McAdams T bulk = 1661. 71.0 6.89 McAdams T film = 2208. 124.3 2 83.7 39.3 16646. 10682. 12572. 4362. 182.6 102.7 1881. 2214. 768. Dittus-Boelter T film Pr.33 = 2153. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1881. Nusselt Ent. = 2724. Sieder-Tate = 2229. Sleicher-Rouse = 1997. Petukhov-Popov = 2034. T V McAdams T bulk = 1881. 92.4 6.90 McAdams T film = 2344. 137.5 3 86.7 49.9 20157. 11687. 12970. 4665. 188.1 121.8 2058. 2284. 822. Dittus-Boelter T film Pr.33 = 2294. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 2058. Nusselt Ent. = 2902. Sieder-Tate = 2424. Sleicher-Rouse = 2218. Petukhov-Popov = 2212. T V McAdams T bulk = 2085. 112.3 6.90 McAdams T film = 2474. 150.2 4 89.8 59.5 24156. 12690. 13441. 4969. 193.7 139.2 2235. 2367. 875. Dittus-Boelter T film Pr.33 = 2429. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 2235. Nusselt Ent. = 3073. Sieder-Tate = 2617. Sleicher-Rouse = 2428. Petukhov-Popov = 2379. T V McAdams T bulk = 2273. 130.5 6.90 McAdams T film = 2597. 162.1 5 92.9 68.1 28459. 13647. 13997. 5270. 199.3 154.7 2404. 2465. 928. Dittus-Boelter T film Pr.33 = 2552. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 2404. Nusselt Ent. = 3228. Sieder-Tate = 2798. Sleicher-Rouse = 2619. Petukhov-Popov = 2530. T V McAdams T bulk = 2442. 146.9 6.90 McAdams T film = 2711. 173.1 6 95.9 75.7 32774. 14512. 14642. 5559. 204.6 168.2 2556. 2579. 979. Dittus-Boelter T film Pr.33 = 2657. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 2556. Nusselt Ent. = 3361. Sieder-Tate = 2959. Sleicher-Rouse = 2782. Petukhov-Popov = 2658. T V McAdams T bulk = 2592. 161.5 6.90 McAdams T film = 2813. 183.0 Flow Rate = 1.000 GPM Steam Pressure = 7.00 PSIG Temperature IN = 15.6 Degrees C 60.0 F Temperature OUT = 75.7 Degrees C 168.2 F Steam Temperature = 111.3 Degrees C 232.3 F Length Wall Temp. Temp. Water Out Inches C F C F 11.667 80.9 177.6 27.8 82.1 23.333 83.7 182.6 39.3 102.7 35.000 86.7 188.1 49.9 121.8 46.667 89.8 193.7 59.5 139.2 58.333 92.9 199.3 68.1 154.7 70.000 95.9 204.6 75.7 168.2 ..PAGE University of Idaho Department of Chemical Engineering DOUBLE PIPE HEAT EXCHANGER Prediction Program Rel. 2/8/92 Ch. E. 434 Laboratory D. C. Drown Date: Jan 25, 2008 Time: 0:57:51 Input from KEYBOARD for Case Number: 4 Start Iteration Loop Flow = 0.500 GPM Inlet Temperature = 15.56 C Steam Temperature = 111.29 T Wall Guess = 98.00 T Out Guess = 88.00 Steam Pressure = 7.00 PSIG + Temperature = 232.319 Deg F H Vaporization = 957.24 BTU/LB Density= 0.053708 LB/FT3 Barometric Pressure = 14.6955 PSIA Steam Pressure = 7.00 PSIG + Temperature = 111.286 Deg C H Vaporization = 2226645. J/Kg Density = 0.8603 Kg/M3 Fouling - Inside = .0000000 Outside = .0000000 Temperature Convergence to 0.010 Degrees N T Wall T Out Re No. H Inside H Outside U C C Watts / Sq. Meter C Units = F F BTU / Sq. Feet F 1 93.2 32.4 7096. 5674. 14051. 2870. 199.7 90.4 999. 2475. 505. Dittus-Boelter T film Pr.33 = 1241. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 999. Nusselt Ent. = 1569. Sieder-Tate = 1216. Sleicher-Rouse = 1063. Petukhov-Popov = 1069. T V McAdams T bulk = 978. 75.2 3.44 McAdams T film = 1344. 137.5 2 95.4 47.9 9311. 6467. 14514. 3197. 203.6 118.2 1139. 2556. 563. Dittus-Boelter T film Pr.33 = 1346. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1139. Nusselt Ent. = 1702. Sieder-Tate = 1367. Sleicher-Rouse = 1244. Petukhov-Popov = 1214. T V McAdams T bulk = 1149. 104.3 3.44 McAdams T film = 1442. 154.0 3 97.9 61.6 12064. 7282. 15158. 3532. 208.2 142.8 1282. 2670. 622. Dittus-Boelter T film Pr.33 = 1444. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1282. Nusselt Ent. = 1827. Sieder-Tate = 1519. Sleicher-Rouse = 1416. Petukhov-Popov = 1355. T V McAdams T bulk = 1304. 130.5 3.45 McAdams T film = 1533. 169.3 4 100.5 73.2 15134. 8049. 16015. 3855. 212.9 163.8 1418. 2821. 679. Dittus-Boelter T film Pr.33 = 1528. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1418. Nusselt Ent. = 1933. Sieder-Tate = 1658. Sleicher-Rouse = 1564. Petukhov-Popov = 1477. T V McAdams T bulk = 1439. 153.3 3.45 McAdams T film = 1615. 183.1 5 103.0 82.7 18086. 8693. 17125. 4147. 217.5 180.9 1531. 3016. 730. Dittus-Boelter T film Pr.33 = 1590. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1531. Nusselt Ent. = 2012. Sieder-Tate = 1773. Sleicher-Rouse = 1676. Petukhov-Popov = 1572. T V McAdams T bulk = 1552. 172.3 3.45 McAdams T film = 1685. 194.9 6 105.3 90.2 20486. 9166. 18521. 4394. 221.5 194.5 1614. 3262. 774. Dittus-Boelter T film Pr.33 = 1631. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1614. Nusselt Ent. = 2064. Sieder-Tate = 1855. Sleicher-Rouse = 1751. Petukhov-Popov = 1637. T V McAdams T bulk = 1643. 187.7 3.45 McAdams T film = 1743. 204.6 Flow Rate = 0.500 GPM Steam Pressure = 7.00 PSIG Temperature IN = 15.6 Degrees C 60.0 F Temperature OUT = 90.2 Degrees C 194.5 F Steam Temperature = 111.3 Degrees C 232.3 F Length Wall Temp. Temp. Water Out Inches C F C F 11.667 93.2 199.7 32.4 90.4 23.333 95.4 203.6 47.9 118.2 35.000 97.9 208.2 61.6 142.8 46.667 100.5 212.9 73.2 163.8 58.333 103.0 217.5 82.7 180.9 70.000 105.3 221.5 90.2 194.5 ..PAGE University of Idaho Department of Chemical Engineering DOUBLE PIPE HEAT EXCHANGER Prediction Program Rel. 2/8/92 Ch. E. 434 Laboratory D. C. Drown Date: Jan 25, 2008 Time: 0:58:11 Input from KEYBOARD for Case Number: 5 Start Iteration Loop Flow = 0.250 GPM Inlet Temperature = 15.56 C Steam Temperature = 111.29 T Wall Guess = 110.00 T Out Guess = 100.00 Steam Pressure = 7.00 PSIG + Temperature = 232.319 Deg F H Vaporization = 957.24 BTU/LB Density= 0.053708 LB/FT3 Barometric Pressure = 14.6955 PSIA Steam Pressure = 7.00 PSIG + Temperature = 111.286 Deg C H Vaporization = 2226645. J/Kg Density = 0.8603 Kg/M3 Fouling - Inside = .0000000 Outside = .0000000 Temperature Convergence to 0.010 Degrees N T Wall T Out Re No. H Inside H Outside U C C Watts / Sq. Meter C Units = F F BTU / Sq. Feet F 1 101.4 37.1 3680. 3317. 16381. 1881. 214.6 98.8 584. 2885. 331. Dittus-Boelter T film Pr.33 = 749. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 584. Nusselt Ent. = 947. Sieder-Tate = 716. Sleicher-Rouse = 662. Petukhov-Popov = 623. T V McAdams T bulk = 575. 79.4 1.72 McAdams T film = 803. 147.0 2 102.9 56.3 5216. 3914. 17068. 2183. 217.3 133.3 689. 3006. 384. Dittus-Boelter T film Pr.33 = 821. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 689. Nusselt Ent. = 1039. Sieder-Tate = 828. Sleicher-Rouse = 795. Petukhov-Popov = 733. T V McAdams T bulk = 699. 116.1 1.72 McAdams T film = 870. 166.7 3 104.8 72.3 7156. 4510. 18161. 2484. 220.6 162.1 794. 3199. 438. Dittus-Boelter T film Pr.33 = 882. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 794. Nusselt Ent. = 1116. Sieder-Tate = 935. Sleicher-Rouse = 910. Petukhov-Popov = 834. T V McAdams T bulk = 807. 147.7 1.72 McAdams T film = 930. 184.2 4 106.7 84.7 9109. 5007. 19776. 2747. 224.0 184.4 882. 3483. 484. Dittus-Boelter T film Pr.33 = 924. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 882. Nusselt Ent. = 1168. Sieder-Tate = 1022. Sleicher-Rouse = 992. Petukhov-Popov = 911. T V McAdams T bulk = 894. 173.3 1.72 McAdams T film = 980. 198.6 5 108.3 93.6 10586. 5337. 22006. 2942. 226.9 200.5 940. 3876. 518. Dittus-Boelter T film Pr.33 = 947. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 940. Nusselt Ent. = 1198. Sieder-Tate = 1079. Sleicher-Rouse = 1039. Petukhov-Popov = 959. T V McAdams T bulk = 960. 192.5 1.72 McAdams T film = 1018. 209.7 6 109.5 99.8 11439. 5513. 24907. 3074. 229.0 211.6 971. 4387. 541. Dittus-Boelter T film Pr.33 = 957. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 971. Nusselt Ent. = 1211. Sieder-Tate = 1108. Sleicher-Rouse = 1060. Petukhov-Popov = 983. T V McAdams T bulk = 1006. 206.1 1.73 McAdams T film = 1045. 217.5 Flow Rate = 0.250 GPM Steam Pressure = 7.00 PSIG Temperature IN = 15.6 Degrees C 60.0 F Temperature OUT = 99.8 Degrees C 211.6 F Steam Temperature = 111.3 Degrees C 232.3 F Length Wall Temp. Temp. Water Out Inches C F C F 11.667 101.4 214.6 37.1 98.8 23.333 102.9 217.3 56.3 133.3 35.000 104.8 220.6 72.3 162.1 46.667 106.7 224.0 84.7 184.4 58.333 108.3 226.9 93.6 200.5 70.000 109.5 229.0 99.8 211.6 ..PAGE University of Idaho Department of Chemical Engineering DOUBLE PIPE HEAT EXCHANGER Prediction Program Rel. 2/8/92 Ch. E. 434 Laboratory D. C. Drown Date: Jan 25, 2008 Time: 0:59:10 Input from KEYBOARD for Case Number: 6 Start Iteration Loop Flow = 0.170 GPM Inlet Temperature = 15.56 C Steam Temperature = 111.29 T Wall Guess = 110.00 T Out Guess = 105.00 Steam Pressure = 7.00 PSIG + Temperature = 232.319 Deg F H Vaporization = 957.24 BTU/LB Density= 0.053708 LB/FT3 Barometric Pressure = 14.6955 PSIA Steam Pressure = 7.00 PSIG + Temperature = 111.286 Deg C H Vaporization = 2226645. J/Kg Density = 0.8603 Kg/M3 Fouling - Inside = .0000000 Outside = .0000000 Temperature Convergence to 0.010 Degrees N T Wall T Out Re No. H Inside H Outside U C C Watts / Sq. Meter C Units = F F BTU / Sq. Feet F 1 104.5 39.7 2554. 2460. 17952. 1453. 220.0 103.4 433. 3162. 256. Dittus-Boelter T film Pr.33 = 561. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 433. Nusselt Ent. = 709. Sieder-Tate = 531. Sleicher-Rouse = 515. Petukhov-Popov = 464. T V McAdams T bulk = 428. 81.7 1.17 McAdams T film = 599. 150.9 2 105.6 60.7 3773. 2956. 18818. 1723. 222.2 141.3 521. 3314. 303. Dittus-Boelter T film Pr.33 = 618. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 521. Nusselt Ent. = 782. Sieder-Tate = 624. Sleicher-Rouse = 624. Petukhov-Popov = 555. T V McAdams T bulk = 529. 122.3 1.17 McAdams T film = 653. 172.3 3 107.1 77.6 5299. 3437. 20294. 1986. 224.8 171.6 605. 3574. 350. Dittus-Boelter T film Pr.33 = 663. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 605. Nusselt Ent. = 838. Sieder-Tate = 710. Sleicher-Rouse = 711. Petukhov-Popov = 637. T V McAdams T bulk = 614. 156.5 1.17 McAdams T film = 699. 190.6 4 108.6 89.8 6693. 3801. 22573. 2195. 227.4 193.6 669. 3976. 387. Dittus-Boelter T film Pr.33 = 689. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 669. Nusselt Ent. = 872. Sieder-Tate = 772. Sleicher-Rouse = 765. Petukhov-Popov = 694. T V McAdams T bulk = 680. 182.6 1.17 McAdams T film = 736. 205.0 5 109.7 97.9 7579. 4005. 25779. 2329. 229.4 208.3 705. 4540. 410. Dittus-Boelter T film Pr.33 = 701. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 705. Nusselt Ent. = 887. Sieder-Tate = 807. Sleicher-Rouse = 791. Petukhov-Popov = 723. T V McAdams T bulk = 726. 200.9 1.17 McAdams T film = 762. 215.2 6 110.4 103.1 7993. 4095. 29945. 2407. 230.7 217.7 721. 5274. 424. Dittus-Boelter T film Pr.33 = 705. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 721. Nusselt Ent. = 892. Sieder-Tate = 821. Sleicher-Rouse = 800. Petukhov-Popov = 736. T V McAdams T bulk = 757. 213.0 1.17 McAdams T film = 779. 221.9 Flow Rate = 0.170 GPM Steam Pressure = 7.00 PSIG Temperature IN = 15.6 Degrees C 60.0 F Temperature OUT = 103.1 Degrees C 217.7 F Steam Temperature = 111.3 Degrees C 232.3 F Length Wall Temp. Temp. Water Out Inches C F C F 11.667 104.5 220.0 39.7 103.4 23.333 105.6 222.2 60.7 141.3 35.000 107.1 224.8 77.6 171.6 46.667 108.6 227.4 89.8 193.6 58.333 109.7 229.4 97.9 208.3 70.000 110.4 230.7 103.1 217.7 ..PAGE