Chapter 11: Problem 87
An ammonia-water absorption refrigeration cycle is used to keep a space at \(25^{\circ} \mathrm{F}\) when the ambient temperature is \(70^{\circ} \mathrm{F}\). Pure ammonia enters the condenser at 300 psia and \(140^{\circ} \mathrm{F}\) at a rate of \(0.04 \mathrm{lbm} / \mathrm{s}\). Ammonia leaves the condenser as a saturated liquid and is expanded to 30 psia. Ammonia leaves the evaporator as a saturated vapor. Heat is supplied to the generator by geothermal liquid water that enters at \(240^{\circ} \mathrm{F}\) at a rate of \(0.55 \mathrm{lbm} / \mathrm{s}\) and leaves at \(200^{\circ} \mathrm{F}\). Determine ( \(a\) ) the rate of cooling provided by the system, in \(\mathrm{Btu} / \mathrm{h}\), the \(\mathrm{COP}\), and (b) the second-law efficiency of the system. The enthalpies of ammonia at various states of the system are: condenser inlet \(h_{2}=665.7 \mathrm{Btu} / \mathrm{lbm},\) evaporator inlet \(h_{4}=190.9 \mathrm{Btu} / \mathrm{lbm}\) evaporator exit \(h_{1}=619.2 \mathrm{Btu} / \mathrm{lbm} .\) Also, take the specific heat of geothermal water to be \(1.0 \mathrm{Btu} / \mathrm{lbm} \cdot^{\circ} \mathrm{F}\).
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