초록 ▼

An absorption chiller includes a vertically split absorber section the upper portion of which is a high temperature absorber and the lower portion of which is a low temperature absorber. Weak solution is pumped in parallel from the absorber to both a low temperature generator and a high temperature

An absorption chiller includes a vertically split absorber section the upper portion of which is a high temperature absorber and the lower portion of which is a low temperature absorber. Weak solution is pumped in parallel from the absorber to both a low temperature generator and a high temperature generator. The low temperature generator is disposed vertically above the high temperature generator. Concentrated solution flows, in parallel, from the low temperature generator to the low temperature absorber and from the high temperature generator to the high temperature absorber. The flow of concentrated solution from the low temperature generator to the low temperature absorber is as a result of the elevation of the low temperature generator above the low temperature absorber while the flow of concentrated solution from the high temperature generator to the vertically elevated high temperature absorber is as a result of the pressure differential between the high temperature generator and the high temperature absorber.

대표청구항 ▼

1. An absorption chiller comprising:a high temperature generator; a low temperature generator; a condenser; an evaporator; a solution that includes an absorbent and a refrigerant; an absorber, said absorber including a high temperature absorber and a low temperature absorber, said low temperature ab

1. An absorption chiller comprising:a high temperature generator; a low temperature generator; a condenser; an evaporator; a solution that includes an absorbent and a refrigerant; an absorber, said absorber including a high temperature absorber and a low temperature absorber, said low temperature absorber being disposed below both said high temperature absorber and said low temperature generator, a first portion of said solution flowing from said low temperature generator to and through said low temperature absorber and a second portion of said solution flowing from said high temperature generator to and through said high temperature absorber, the flow of said first solution portion from said low temperature generator to said low temperature absorber being assisted by the force of gravity and the flow of said second solution portion from said high temperature generator to said high temperature absorber being under the impetus of the pressure which exists in said high temperature generator.