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: 0:42:30 Input File Name: G5-5.dat Start Iteration Loop Flow = 5.000 GPM Inlet Temperature = 15.56 C Steam Temperature = 108.41 T Wall Guess = 99.00 T Out Guess = 71.00 Steam Pressure = 5.00 PSIG + Temperature = 227.145 Deg F H Vaporization = 960.62 BTU/LB Density= 0.049062 LB/FT3 Barometric Pressure = 14.6955 PSIA Steam Pressure = 5.00 PSIG + Temperature = 108.412 Deg C H Vaporization = 2234491. J/Kg Density = 0.7859 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 45.0 19.5 64297. 34101. 9575. 6456. 113.0 67.1 6006. 1686. 1137. Dittus-Boelter T film Pr.33 = 5992. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 6006. Nusselt Ent. = 7581. Sieder-Tate = 6564. Sleicher-Rouse = 6527. Petukhov-Popov = 6939. T V McAdams T bulk = 5754. 63.6 34.55 McAdams T film = 6675. 88.3 2 47.4 23.3 68346. 35174. 9718. 6580. 117.3 74.0 6195. 1711. 1159. Dittus-Boelter T film Pr.33 = 6173. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 6195. Nusselt Ent. = 7808. Sieder-Tate = 6789. Sleicher-Rouse = 6778. Petukhov-Popov = 7149. T V McAdams T bulk = 6014. 70.5 34.55 McAdams T film = 6886. 93.9 3 49.8 27.1 72649. 36261. 9864. 6705. 121.7 80.8 6386. 1737. 1181. Dittus-Boelter T film Pr.33 = 6355. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 6386. Nusselt Ent. = 8040. Sieder-Tate = 7017. Sleicher-Rouse = 7032. Petukhov-Popov = 7358. T V McAdams T bulk = 6269. 77.4 34.55 McAdams T film = 7094. 99.5 4 52.2 30.7 77203. 37359. 10013. 6832. 125.9 87.4 6580. 1764. 1203. Dittus-Boelter T film Pr.33 = 6541. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 6580. Nusselt Ent. = 8274. Sieder-Tate = 7248. Sleicher-Rouse = 7287. Petukhov-Popov = 7565. T V McAdams T bulk = 6518. 84.1 34.56 McAdams T film = 7298. 105.0 5 54.5 34.3 82010. 38467. 10166. 6960. 130.1 93.8 6775. 1790. 1226. Dittus-Boelter T film Pr.33 = 6728. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 6775. Nusselt Ent. = 8511. Sieder-Tate = 7481. Sleicher-Rouse = 7542. Petukhov-Popov = 7771. T V McAdams T bulk = 6761. 90.6 34.56 McAdams T film = 7498. 110.4 6 56.8 37.8 87066. 39581. 10323. 7089. 134.3 100.0 6971. 1818. 1248. Dittus-Boelter T film Pr.33 = 6916. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 6971. Nusselt Ent. = 8750. Sieder-Tate = 7716. Sleicher-Rouse = 7797. Petukhov-Popov = 7974. T V McAdams T bulk = 6998. 96.9 34.56 McAdams T film = 7694. 115.6 Flow Rate = 5.000 GPM Steam Pressure = 5.00 PSIG Temperature IN = 15.6 Degrees C 60.0 F Temperature OUT = 37.8 Degrees C 100.0 F Steam Temperature = 108.4 Degrees C 227.1 F Length Wall Temp. Temp. Water Out Inches C F C F 11.667 45.0 113.0 19.5 67.1 23.333 47.4 117.3 23.3 74.0 35.000 49.8 121.7 27.1 80.8 46.667 52.2 125.9 30.7 87.4 58.333 54.5 130.1 34.3 93.8 70.000 56.8 134.3 37.8 100.0 ..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: 0:43: 2 Input from KEYBOARD for Case Number: 2 Start Iteration Loop Flow = 2.500 GPM Inlet Temperature = 15.56 C Steam Temperature = 108.41 T Wall Guess = 60.00 T Out Guess = 45.00 Steam Pressure = 5.00 PSIG + Temperature = 227.145 Deg F H Vaporization = 960.62 BTU/LB Density= 0.049062 LB/FT3 Barometric Pressure = 14.6955 PSIA Steam Pressure = 5.00 PSIG + Temperature = 108.412 Deg C H Vaporization = 2234491. J/Kg Density = 0.7859 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 59.2 22.3 32831. 19792. 10489. 5602. 138.5 72.1 3486. 1847. 987. Dittus-Boelter T film Pr.33 = 3715. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 3486. Nusselt Ent. = 4700. Sieder-Tate = 3947. Sleicher-Rouse = 3681. Petukhov-Popov = 3898. T V McAdams T bulk = 3356. 66.1 17.26 McAdams T film = 4131. 102.3 2 62.2 28.8 36477. 20865. 10710. 5795. 143.9 83.8 3675. 1886. 1021. Dittus-Boelter T film Pr.33 = 3886. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 3675. Nusselt Ent. = 4916. Sieder-Tate = 4168. Sleicher-Rouse = 3929. Petukhov-Popov = 4103. T V McAdams T bulk = 3610. 77.9 17.26 McAdams T film = 4316. 110.9 3 65.1 35.0 40506. 21958. 10943. 5993. 149.2 94.9 3867. 1927. 1055. Dittus-Boelter T film Pr.33 = 4061. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 3867. Nusselt Ent. = 5137. Sieder-Tate = 4393. Sleicher-Rouse = 4179. Petukhov-Popov = 4306. T V McAdams T bulk = 3854. 89.3 17.26 McAdams T film = 4495. 119.3 4 68.1 40.9 44913. 23066. 11191. 6193. 154.6 105.6 4062. 1971. 1091. Dittus-Boelter T film Pr.33 = 4237. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 4062. Nusselt Ent. = 5359. Sieder-Tate = 4620. Sleicher-Rouse = 4427. Petukhov-Popov = 4506. T V McAdams T bulk = 4088. 100.3 17.27 McAdams T film = 4669. 127.4 5 71.0 46.5 49679. 24178. 11454. 6396. 159.9 115.8 4258. 2017. 1126. Dittus-Boelter T film Pr.33 = 4413. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 4258. Nusselt Ent. = 5582. Sieder-Tate = 4848. Sleicher-Rouse = 4671. Petukhov-Popov = 4700. T V McAdams T bulk = 4311. 110.7 17.27 McAdams T film = 4837. 135.3 6 73.9 51.9 54767. 25284. 11731. 6600. 165.0 125.4 4453. 2066. 1162. Dittus-Boelter T film Pr.33 = 4586. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 4453. Nusselt Ent. = 5802. Sieder-Tate = 5073. Sleicher-Rouse = 4907. Petukhov-Popov = 4887. T V McAdams T bulk = 4523. 120.6 17.27 McAdams T film = 4999. 142.8 Flow Rate = 2.500 GPM Steam Pressure = 5.00 PSIG Temperature IN = 15.6 Degrees C 60.0 F Temperature OUT = 51.9 Degrees C 125.4 F Steam Temperature = 108.4 Degrees C 227.1 F Length Wall Temp. Temp. Water Out Inches C F C F 11.667 59.2 138.5 22.3 72.1 23.333 62.2 143.9 28.8 83.8 35.000 65.1 149.2 35.0 94.9 46.667 68.1 154.6 40.9 105.6 58.333 71.0 159.9 46.5 115.8 70.000 73.9 165.0 51.9 125.4 ..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: 0:43:26 Input from KEYBOARD for Case Number: 3 Start Iteration Loop Flow = 1.000 GPM Inlet Temperature = 15.56 C Steam Temperature = 108.41 T Wall Guess = 78.00 T Out Guess = 55.00 Steam Pressure = 5.00 PSIG + Temperature = 227.145 Deg F H Vaporization = 960.62 BTU/LB Density= 0.049062 LB/FT3 Barometric Pressure = 14.6955 PSIA Steam Pressure = 5.00 PSIG + Temperature = 108.412 Deg C H Vaporization = 2234491. J/Kg Density = 0.7859 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 79.0 27.4 13657. 9695. 12284. 4068. 174.2 81.4 1707. 2163. 716. Dittus-Boelter T film Pr.33 = 1992. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1707. Nusselt Ent. = 2521. Sieder-Tate = 2026. Sleicher-Rouse = 1772. Petukhov-Popov = 1851. T V McAdams T bulk = 1658. 70.7 6.89 McAdams T film = 2189. 122.5 2 81.8 38.6 16495. 10636. 12630. 4357. 179.2 101.4 1873. 2224. 767. Dittus-Boelter T film Pr.33 = 2128. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1873. Nusselt Ent. = 2692. Sieder-Tate = 2212. Sleicher-Rouse = 1986. Petukhov-Popov = 2025. T V McAdams T bulk = 1871. 91.4 6.90 McAdams T film = 2322. 135.3 3 84.7 48.8 19841. 11603. 13044. 4653. 184.6 119.9 2043. 2297. 820. Dittus-Boelter T film Pr.33 = 2264. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 2043. Nusselt Ent. = 2864. Sieder-Tate = 2400. Sleicher-Rouse = 2198. Petukhov-Popov = 2197. T V McAdams T bulk = 2069. 110.7 6.90 McAdams T film = 2448. 147.6 4 87.8 58.1 23628. 12565. 13531. 4951. 190.0 136.7 2213. 2383. 872. Dittus-Boelter T film Pr.33 = 2395. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 2213. Nusselt Ent. = 3030. Sieder-Tate = 2585. Sleicher-Rouse = 2400. Petukhov-Popov = 2359. T V McAdams T bulk = 2250. 128.3 6.90 McAdams T film = 2567. 159.1 5 90.8 66.5 27692. 13485. 14100. 5246. 195.4 151.6 2375. 2483. 924. Dittus-Boelter T film Pr.33 = 2514. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 2375. Nusselt Ent. = 3181. Sieder-Tate = 2760. Sleicher-Rouse = 2584. Petukhov-Popov = 2505. T V McAdams T bulk = 2414. 144.1 6.90 McAdams T film = 2677. 169.8 6 93.6 73.8 31782. 14321. 14762. 5533. 200.5 164.8 2522. 2600. 974. Dittus-Boelter T film Pr.33 = 2618. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 2522. Nusselt Ent. = 3312. Sieder-Tate = 2917. Sleicher-Rouse = 2743. Petukhov-Popov = 2630. T V McAdams T bulk = 2559. 158.2 6.90 McAdams T film = 2776. 179.4 Flow Rate = 1.000 GPM Steam Pressure = 5.00 PSIG Temperature IN = 15.6 Degrees C 60.0 F Temperature OUT = 73.8 Degrees C 164.8 F Steam Temperature = 108.4 Degrees C 227.1 F Length Wall Temp. Temp. Water Out Inches C F C F 11.667 79.0 174.2 27.4 81.4 23.333 81.8 179.2 38.6 101.4 35.000 84.7 184.6 48.8 119.9 46.667 87.8 190.0 58.1 136.7 58.333 90.8 195.4 66.5 151.6 70.000 93.6 200.5 73.8 164.8 ..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: 0:43:40 Input from KEYBOARD for Case Number: 4 Start Iteration Loop Flow = 0.750 GPM Inlet Temperature = 15.56 C Steam Temperature = 108.41 T Wall Guess = 95.00 T Out Guess = 78.00 Steam Pressure = 5.00 PSIG + Temperature = 227.145 Deg F H Vaporization = 960.62 BTU/LB Density= 0.049062 LB/FT3 Barometric Pressure = 14.6955 PSIA Steam Pressure = 5.00 PSIG + Temperature = 108.412 Deg C H Vaporization = 2234491. J/Kg Density = 0.7859 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 84.4 29.3 10388. 7755. 12999. 3557. 184.0 84.7 1366. 2289. 626. Dittus-Boelter T film Pr.33 = 1633. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1366. Nusselt Ent. = 2065. Sieder-Tate = 1639. Sleicher-Rouse = 1423. Petukhov-Popov = 1470. T V McAdams T bulk = 1330. 72.3 5.17 McAdams T film = 1785. 128.2 2 87.0 42.0 12929. 8628. 13396. 3865. 188.6 107.6 1520. 2359. 681. Dittus-Boelter T film Pr.33 = 1754. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1520. Nusselt Ent. = 2219. Sieder-Tate = 1808. Sleicher-Rouse = 1621. Petukhov-Popov = 1632. T V McAdams T bulk = 1524. 96.1 5.17 McAdams T film = 1901. 142.4 3 89.8 53.5 15985. 9524. 13897. 4180. 193.6 128.4 1677. 2447. 736. Dittus-Boelter T film Pr.33 = 1874. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1677. Nusselt Ent. = 2371. Sieder-Tate = 1980. Sleicher-Rouse = 1816. Petukhov-Popov = 1789. T V McAdams T bulk = 1703. 118.0 5.17 McAdams T film = 2011. 155.8 4 92.6 63.8 19441. 10402. 14516. 4495. 198.7 146.8 1832. 2556. 792. Dittus-Boelter T film Pr.33 = 1985. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1832. Nusselt Ent. = 2511. Sieder-Tate = 2145. Sleicher-Rouse = 1995. Petukhov-Popov = 1934. T V McAdams T bulk = 1863. 137.6 5.17 McAdams T film = 2112. 168.2 5 95.4 72.6 23045. 11210. 15267. 4798. 203.8 162.7 1974. 2689. 845. Dittus-Boelter T film Pr.33 = 2080. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1974. Nusselt Ent. = 2631. Sieder-Tate = 2294. Sleicher-Rouse = 2150. Petukhov-Popov = 2058. T V McAdams T bulk = 2004. 154.7 5.18 McAdams T film = 2204. 179.3 6 98.1 80.1 26463. 11900. 16167. 5082. 208.5 176.2 2096. 2847. 895. Dittus-Boelter T film Pr.33 = 2156. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 2096. Nusselt Ent. = 2728. Sieder-Tate = 2420. Sleicher-Rouse = 2275. Petukhov-Popov = 2158. T V McAdams T bulk = 2124. 169.5 5.18 McAdams T film = 2284. 189.0 Flow Rate = 0.750 GPM Steam Pressure = 5.00 PSIG Temperature IN = 15.6 Degrees C 60.0 F Temperature OUT = 80.1 Degrees C 176.2 F Steam Temperature = 108.4 Degrees C 227.1 F Length Wall Temp. Temp. Water Out Inches C F C F 11.667 84.4 184.0 29.3 84.7 23.333 87.0 188.6 42.0 107.6 35.000 89.8 193.6 53.5 128.4 46.667 92.6 198.7 63.8 146.8 58.333 95.4 203.8 72.6 162.7 70.000 98.1 208.5 80.1 176.2 ..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: 0:44: 8 Input from KEYBOARD for Case Number: 5 Start Iteration Loop Flow = 0.500 GPM Inlet Temperature = 15.56 C Steam Temperature = 108.41 T Wall Guess = 102.00 T Out Guess = 90.00 Steam Pressure = 5.00 PSIG + Temperature = 227.145 Deg F H Vaporization = 960.62 BTU/LB Density= 0.049062 LB/FT3 Barometric Pressure = 14.6955 PSIA Steam Pressure = 5.00 PSIG + Temperature = 108.412 Deg C H Vaporization = 2234491. J/Kg Density = 0.7859 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 91.0 31.9 7068. 5663. 14144. 2870. 195.7 89.4 997. 2491. 505. Dittus-Boelter T film Pr.33 = 1226. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 997. Nusselt Ent. = 1551. Sieder-Tate = 1209. Sleicher-Rouse = 1056. Petukhov-Popov = 1067. T V McAdams T bulk = 975. 74.7 3.44 McAdams T film = 1331. 135.2 2 93.1 46.9 9189. 6428. 14633. 3188. 199.6 116.4 1132. 2577. 561. Dittus-Boelter T film Pr.33 = 1327. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1132. Nusselt Ent. = 1679. Sieder-Tate = 1356. Sleicher-Rouse = 1230. Petukhov-Popov = 1207. T V McAdams T bulk = 1141. 102.9 3.44 McAdams T film = 1426. 151.3 3 95.6 60.1 11796. 7209. 15302. 3513. 204.0 140.1 1270. 2695. 619. Dittus-Boelter T film Pr.33 = 1423. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1270. Nusselt Ent. = 1800. Sieder-Tate = 1502. Sleicher-Rouse = 1394. Petukhov-Popov = 1342. T V McAdams T bulk = 1291. 128.2 3.45 McAdams T film = 1514. 166.1 4 98.1 71.3 14691. 7946. 16181. 3828. 208.6 160.4 1399. 2850. 674. Dittus-Boelter T film Pr.33 = 1506. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1399. Nusselt Ent. = 1905. Sieder-Tate = 1636. Sleicher-Rouse = 1537. Petukhov-Popov = 1461. T V McAdams T bulk = 1421. 150.2 3.45 McAdams T film = 1593. 179.4 5 100.5 80.5 17502. 8573. 17308. 4114. 212.9 176.9 1510. 3048. 725. Dittus-Boelter T film Pr.33 = 1569. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1510. Nusselt Ent. = 1985. Sieder-Tate = 1749. Sleicher-Rouse = 1649. Petukhov-Popov = 1555. T V McAdams T bulk = 1530. 168.6 3.45 McAdams T film = 1661. 190.8 6 102.6 87.8 19853. 9046. 18715. 4361. 216.7 190.1 1593. 3296. 768. Dittus-Boelter T film Pr.33 = 1613. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1593. Nusselt Ent. = 2040. Sieder-Tate = 1832. Sleicher-Rouse = 1726. Petukhov-Popov = 1621. T V McAdams T bulk = 1619. 183.5 3.45 McAdams T film = 1717. 200.1 Flow Rate = 0.500 GPM Steam Pressure = 5.00 PSIG Temperature IN = 15.6 Degrees C 60.0 F Temperature OUT = 87.8 Degrees C 190.1 F Steam Temperature = 108.4 Degrees C 227.1 F Length Wall Temp. Temp. Water Out Inches C F C F 11.667 91.0 195.7 31.9 89.4 23.333 93.1 199.6 46.9 116.4 35.000 95.6 204.0 60.1 140.1 46.667 98.1 208.6 71.3 160.4 58.333 100.5 212.9 80.5 176.9 70.000 102.6 216.7 87.8 190.1 ..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: 0:44:26 Input from KEYBOARD for Case Number: 6 Start Iteration Loop Flow = 0.300 GPM Inlet Temperature = 15.56 C Steam Temperature = 108.41 T Wall Guess = 105.00 T Out Guess = 95.00 Steam Pressure = 5.00 PSIG + Temperature = 227.145 Deg F H Vaporization = 960.62 BTU/LB Density= 0.049062 LB/FT3 Barometric Pressure = 14.6955 PSIA Steam Pressure = 5.00 PSIG + Temperature = 108.412 Deg C H Vaporization = 2234491. J/Kg Density = 0.7859 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 97.2 35.2 4352. 3811. 15850. 2113. 207.0 95.4 671. 2791. 372. Dittus-Boelter T film Pr.33 = 846. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 671. Nusselt Ent. = 1070. Sieder-Tate = 820. Sleicher-Rouse = 739. Petukhov-Popov = 716. T V McAdams T bulk = 659. 77.7 2.06 McAdams T film = 912. 142.4 2 98.9 52.9 5977. 4434. 16500. 2416. 210.0 127.2 781. 2906. 425. Dittus-Boelter T film Pr.33 = 923. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 781. Nusselt Ent. = 1168. Sieder-Tate = 937. Sleicher-Rouse = 878. Petukhov-Popov = 830. T V McAdams T bulk = 791. 111.3 2.06 McAdams T film = 984. 160.6 3 100.8 67.8 8004. 5059. 17478. 2721. 213.5 154.0 891. 3078. 479. Dittus-Boelter T film Pr.33 = 992. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 891. Nusselt Ent. = 1255. Sieder-Tate = 1051. Sleicher-Rouse = 1004. Petukhov-Popov = 937. T V McAdams T bulk = 906. 140.6 2.07 McAdams T film = 1049. 177.0 4 102.8 79.7 10127. 5607. 18866. 2999. 217.1 175.5 988. 3323. 528. Dittus-Boelter T film Pr.33 = 1044. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 988. Nusselt Ent. = 1320. Sieder-Tate = 1149. Sleicher-Rouse = 1100. Petukhov-Popov = 1024. T V McAdams T bulk = 1001. 164.8 2.07 McAdams T film = 1104. 190.9 5 104.6 88.6 11908. 6010. 20741. 3223. 220.2 191.6 1058. 3653. 568. Dittus-Boelter T film Pr.33 = 1077. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1058. Nusselt Ent. = 1362. Sieder-Tate = 1219. Sleicher-Rouse = 1163. Petukhov-Popov = 1082. T V McAdams T bulk = 1075. 183.5 2.07 McAdams T film = 1147. 201.9 6 105.9 95.1 13112. 6259. 23152. 3390. 222.7 203.1 1102. 4077. 597. Dittus-Boelter T film Pr.33 = 1095. BTU/Ft2 F Dittus-Boelter T bulk Pr.4 = 1102. Nusselt Ent. = 1386. Sieder-Tate = 1261. Sleicher-Rouse = 1198. Petukhov-Popov = 1117. T V McAdams T bulk = 1130. 197.4 2.07 McAdams T film = 1180. 210.0 Flow Rate = 0.300 GPM Steam Pressure = 5.00 PSIG Temperature IN = 15.6 Degrees C 60.0 F Temperature OUT = 95.1 Degrees C 203.1 F Steam Temperature = 108.4 Degrees C 227.1 F Length Wall Temp. Temp. Water Out Inches C F C F 11.667 97.2 207.0 35.2 95.4 23.333 98.9 210.0 52.9 127.2 35.000 100.8 213.5 67.8 154.0 46.667 102.8 217.1 79.7 175.5 58.333 104.6 220.2 88.6 191.6 70.000 105.9 222.7 95.1 203.1 ..PAGE