CBEN 408 Spring 2018 ‐1‐ December 28, 2017 Homework #2 Problems 3.1, 3.2 (with extra below), 3.3, & extra problem below. Extra for 3.2: What is the relative difference in heat transfer area if you use a 1‐2 heat exchanger (1 shell pass, 2 tube passes) instead of pure counter current flow? Consider both the water on shell side in one instance & on the tube side in another instance. Extra problem: You’d like to condense 5,000 lb/hr of propane in a 4‐pass aerial cooler. Consider the following: You want to condense propane at a sufficient pressure so that it will be saturated at 120°F. The propane enters as a saturated gas, exits as a saturated liquid, & there is no pressure drop through the exchanger. Ambient air is 85°F. Consider its heat capacity as 0.25 Btu/lb·°F. The exchanger should have a minimum 10°F approach temperature. Answer the following: What mass flow rate of air is needed (in lb/hr)? If the heat transfer coefficient (based on the extended area) is 3.5 Btu/hr·ft 2 ·°F then what surface area is needed (in ft 2 )?

Homework 02 HeatExchangersjjechura/GasProcessing/...What are the relative merits Qf the types of the heat exchangers discussed in Section 3.4? What are the advantages and disadvantages

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Page 1: Homework 02 HeatExchangersjjechura/GasProcessing/...What are the relative merits Qf the types of the heat exchangers discussed in Section 3.4? What are the advantages and disadvantages

CBEN408Spring2018 ‐1‐ December28,2017

Homework #2

Problems3.1,3.2(withextrabelow),3.3,&extraproblembelow.Extrafor3.2:Whatistherelativedifferenceinheattransferareaifyouusea1‐2heatexchanger(1shellpass,2tubepasses) instead of pure counter current flow?Consider both thewater on shell side in oneinstance&onthetubesideinanotherinstance.Extraproblem:You’dliketocondense5,000lb/hrofpropaneina4‐passaerialcooler.Considerthefollowing:

Youwanttocondensepropaneatasufficientpressuresothatitwillbesaturatedat120°F. Thepropaneenters asa saturatedgas, exitsasa saturated liquid,& there isnopressure

dropthroughtheexchanger. Ambientairis85°F.Consideritsheatcapacityas0.25Btu/lb·°F. Theexchangershouldhaveaminimum10°Fapproachtemperature.

Answerthefollowing:

Whatmassflowrateofairisneeded(inlb/hr)? If theheat transfercoefficient(basedontheextendedarea) is3.5Btu/hr·ft2·°F thenwhat

surfaceareaisneeded(inft2)?

Page 2: Homework 02 HeatExchangersjjechura/GasProcessing/...What are the relative merits Qf the types of the heat exchangers discussed in Section 3.4? What are the advantages and disadvantages

Page 3: Homework 02 HeatExchangersjjechura/GasProcessing/...What are the relative merits Qf the types of the heat exchangers discussed in Section 3.4? What are the advantages and disadvantages

21 의학유전체 검사의뢰서 [Converted] [Converted] › upload › requestFile › 9036cf5b-7a39-468a... · 2017-10-19 · Abortus, AF, H.W, QF-21 QF-21, 18, 13 QF-21, 18,

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