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problem 633a standard vapor compression cycle uses tetrafluoroethane as the refrigerant the refrigerant at the exit of
problem 634you are designing a refrigeration cycle that will absorb 100 w of heat at - 10 degf the cycle will use
problem 635an air-conditioning system powered by solar energy is being designed to maintain the temperature inside a
problem 636ammonia is liquefied in a steady-state process by first compressing the gas and then cooling until all the
problem 637figure 6-20 shows a two-stage refrigeration cycle with two evaporating temperatures flash gas removal and
using the parameters of the equation for problem 10 give a graph of temperature vs time at z 0 for t varying from 0 to
problem 339saturated steam at 1 bar is heated at constant pressure to a final temperature of 500 degc in a closed
example 410 internal combustion engineassuming the temperature obtained in the combustion of gasoline to be about 1000
example 416 feasibility of processlooking for ways to improve energy utilization in a chemical plant a young intern
problem 46one mol of methanol vapor is cooled under constant pressure in a closed system by removing 25000 j of heat
problem 48 steam is compressed by reversible isothermal process from 15 bar 250 degc to a final state that consists of
problem 3321 kg of liquid water initially at 40 degc 2 bar is heated under constant pressure if the amount of heat
problem 330 1 mol of liquid hexane at 10 bar 25 degc is mixed adiabatically and under constant pressure with hexane
problem 63you are responsible for a high-temperature process that produces two exhaust streams stream a at 600 degc 10
problem 65 liquid propane boils in a constant pressure boiler to produce propane vapor at 30 bar and 245 degc at the
problem 61a flow process produces work using water as the working medium the process is as follows steam of quality 50
problem 62the power generation unit in your plant uses a hot exhaust gas from another process to produce work the gas
problem 64you are in charge of a unit that produces two streams a at 600 degc 10 bar with molar flow rate 100 moles and
example 612 heat exchanger 2the steam in the previous example is cooled using water at 1 bar 25 degc the cooling water
example 623 liquefaction of nitrogennitrogen is liquefied in the process shown in figure 6-16 nitrogen gas is fed at 25
example 621 household refrigeratorestimate the maximum coefficient of performance of a household refrigeratorexample
example 63 stream acting as a bathin the process of example 62 the flow rte of streams 1prime and 2prime is made very
problem 516 use the lee-kesler method to do the following a calculate the entropy of propane at its critical point the
problem 514 use the srk equation to calculate the following properties of isobutane a residual enthalpy and entropy at
problem 510 propane is isothermally compressed from 001 bar -514 degc to 17 bar the process takes place reversibly in a