I've been interested in 'Einstein's Refrigerator' For some time. Attaching a schematic from Delano's thesis and the description.
"Figure 1 shows a schematic of the Einstein refrigeration cycle. In the Einstein cycle, ammonia acts as an inert gas to
lower the partial pressure over the refrigerant, butane, and water later provides separation by absorbing the ammonia.
Starting in the evaporator, liquid butane arrives from the condenser/absorber at point 2. In the evaporator, saturated
ammonia vapor is bubbled into the liquid butane (point 4), which reduces the partial pressure of the butane. With its
partial pressure reduced, the butane evaporates near the saturation temperature of its partial pressure and cools itself
and the ammonia, and provides external refrigeration. The ammonia-butane vapor mixture leaves the evaporator at point
3 and enters the pre-cooler, where it cools the hot vapor ammonia counter-flowing from the generator (point 5). The
now superheated ammonia-butane mixture flows out of the pre-cooler at point 6 into the condenser/absorber, which is
being continuously cooled by an environmental heat sink. Meanwhile, liquid water from the generator is sprayed into the
condenser/absorber at point 9. With its affinity for ammonia vapor, this water absorbs the vapor ammonia from the
ammonia-butane mixture. The absorption of the ammonia vapor increases the partial pressure on the butane vapor to
nearly the total pressure, allowing it now to condense at butane’s saturation temperature for the total pressure. Note
that this is higher than butane’s saturation temperature at the partial pressure in the evaporator. The butane and the
ammonia water separate due to their respective density differences and the fact that ammonia-water is immiscible with
butane at the condenser/absorber’s temperature and pressure. Since liquid butane is less dense than liquid ammonia-water, it
is the top liquid and is siphoned back to the evaporator at point 1. Meanwhile, the ammonia-water mixture leaves from the
bottom of the condenser/absorber and enters the solution heat exchanger (point 7). Here, the mixture is pre-heated before
entering the generator.
Inside the generator, heat is applied to the strong ammonia-water solution driving off ammonia vapor where it
rises and is carried to the evaporator (point 5). The remaining weak ammonia-water solution is pumped up to a reservoir via
a bubble pump at point 8. In the reservoir, any residual ammonia vapor from the bubble pump is sent to the
condenser/absorber (point 8g). The weak ammonia water solution falls to the solution heat exchanger (point 8f) where it
gives up its heat to the strong ammonia-water solution leaving the condenser. Finally, the water is sprayed into the condenser/
absorber.
While the overall pressure of the cycle is constant, there are slight pressure variations within the cycle necessary for
fluid motion. These are due to height variations and are not large enough to significantly affect property evaluation."
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