Method and apparatus for absorption refrigeration system

Claim 2

An absorption refrigeration system using a thermodynamic cycle comprising generator means, condenser means, evaporator means, and absorber means operatively connected together; said absorber means including a low pressure absorber and a high pressure absorber; said generator means including a low pressure generator and a high pressure generator; and said high pressure absorber being operatively associated to absorb vapor generated in said low pressure generator.

Claim 3

The system defined by claim 1 wherein said high pressure absorber is operatively associated to absorb vapor into an absorption solution partially diluted in said low pressure absorber.

Claim 4

The system defined by claim 1 wherein said low pressure generator is operatively associated to further concentrate absorption solution partially concentrated in said high pressure generator.

Claim 5

The system defined by claim 1 wherein said low pressure generator has a higher operating pressure than said high pressure absorber.

Claim 6

The system defined by claim 1 wherein each of said high and said low pressure generators are heated by a heating medium delivered to said generators at approximately the same temperature.

Claim 7

The system defined by claim 5 wherein the flow relationship of the heating medium delivered to said generators is a parallel flow relationship.

Claim 8

An absorption refrigeration system comprising: a refrigerant flow circuit extending from a high pressure generator, through a condenser and evaporator to a low pressure absorber; a solution flow circuit extending from said low pressure absorber through a first heat exchanger, a high pressure absorber, a second heat exchanger, a high pressure generator, said second heat exchanger, a low pressure generator, said first heat exchanger and back to said low pressure absorber; and a vapor flow circuit extending from said low pressure generator portion of said solution circuit to said high pressure absorber portion of said solution flow circuit.

Claim 9

An absorption refrigeration system comprising: a refrigerant flow circuit extending from a high pressure generator, through a condenser and evaporator to a low pressure absorber; a solution flow circuit extending from said low pressure absorber through a first heat exchanger, a high pressure absorber, a second heat exchanger, a high pressure generator, said second heat exchanger, a low pressure generator, said first heat exchanger and back to said low pressure absorber; and a vapor flow circuit extending from said low pressure generator portion of said solution circuit to said high pressure absorber portion of said solution flow circuit.

Claim 10

The system defined by claim 7 including a pump in that portion of said solution flow circuit downstream of said low pressure absorber and upstream of said high pressure absorber for passing solution from said low pressure absorber to said high pressure absorber.

Claim 13

In an absorption refrigeration process, the seriatim steps of treating the absorption solution comprising: a. heating solution which has been partially diluted from a first temperature to a second temperature while maintaining its concentration substantially constant; b. diluting said solution by absorbing vapor therein at a substantially constant vapor pressure thereby fully diluting the solution; c. heating the fully diluted solution from a third temperature to a fourth temperature while maintaining its concentration substantially constant; d. further heating the fully diluted solution to a fifth temperature thereby vaporizing a portion thereof to thereby form a partially concentrated solution; e. cooling the partially concentrated solution from said fifth temperature to a sixth temperature while maintaining its concentration substantially constant; f. further heating the partially concentrated solution from said sixth temperature to a seventh temperature thereby vaporizing a portion thereof to form a fully concentrated solution; g. cooling the fully concentrated solution from said seventh temperature to an eighth temperature while maintaining its concentration substantially constant; h. diluting the concentrated solution by absorbing vapors therein at substantially constant vapor pressure thereby partially diluting the solution; and i. recycling the solution formed by step (h) in the manner defined by steps (a) through (h).

Claim 14

In an absorption refrigeration process, the seriatim steps of treating the absorption solution comprising: a. heating solution which has been partially diluted from a first temperature to a second temperature while maintaining its concentration substantially constant; b. diluting said solution by absorbing vapor therein at a substantially constant vapor pressure thereby fully diluting the solution; c. heating the fully diluted solution from a third temperature to a fourth temperature while maintaining its concentration substantially constant; d. further heating the fully diluted solution to a fifth temperature thereby vaporizing a portion thereof to thereby form a partially concentrated solution; e. cooling the partially concentrated solution from said fifth temperature to a sixth temperature while maintaining its concentration substantially constant; f. further heating the partially concentrated solution from said sixth temperature to a seventh temperature thereby vaporizing a portion thereof to form a fully concentrated solution; g. cooling the fully concentrated solution from said seventh temperature to an eighth temperature while maintaining its concentration substantially constant; h. diluting the concentrated solution by absorbing vapors therein at substantially constant vapor pressure thereby partially diluting the solution; and i. recycling the solution formed by step (h) in the manner defined by steps (a) through (h).

Claim 15

The process as defined by claim 10 wherein the vapor absorbed into the solution at step (b) is derived from step (f).

Claim 16

The process as defined by claim 10 wherein said fifth and seventh temperatures are about the same value and said first and third temperatures are about the same value.