Branched gax absorption vapor compressor

Claim 2

An absorption cycle apparatus adapted for compressing a vapor comprised of: (a) a generator which is heated by an external source of heat; (b) an absorber which is cooled by an external source of cooling; (c) a second generator, and a second absorber which is cooled by supplying heat to said second generator; (d) a means for transporting absorbent liquid from said absorber to said second generator; (e) a means for branching the absorbent flow from said second absorber into at least two streams and transporting one stream to said absorber and the remaining stream to said generator; (f) at least one conduit for supplying vapor to said absorbers; (g) at least one conduit for removing compressed vapor from said generators, and; (h) a generator heat exchange (GHX) exchanger in said generator.

Claim 3

The absorption cycle apparatus according to claim 1 additionally comprised of: (a) an absorber heat exchange (AHX) exchanger in said absorber for exchange of heat between fluids contained therein and absorbent liquid exiting therefrom; and (b) an absorber heat exchange (AHX) exchanger in said second absorber for exchange of heat between fluids contained therein and said branched absorbent stream to said generator.

Claim 4

An absorption cycle apparatus adapted for at least one of useful heating and useful cooling comprised of: (a) a generator which is heated by an external source of heat; (b) an absorber which is cooled by an external source of cooling; (c) a second generator, and a second absorber which is cooled by supplying heat to said second generator; (d) a means for transporting absorbent liquid from said absorber to said second generator; (e) a means for branching the absorbent flow from said second absorber into at least two streams and transporting one stream to said absorber and the remaining stream to said generator; (f) an evaporator which supplies said useful cooling and said vapor; (g) a condenser which receives said compressed vapor and supplies part of said useful heating; and (h) a generator heat exchange (GHX) exchanger in said generator.

Claim 5

An absorption cycle apparatus adapted for at least one of useful heating and useful cooling comprised of: (a) a generator which is heated by an external source of heat; (b) an absorber which is cooled by an external source of cooling; (c) a second generator, and a second absorber which is cooled by supplying heat to said second generator; (d) a means for transporting absorbent liquid from said absorber to said second generator; (e) a means for branching the absorbent flow from said second absorber into at least two streams and transporting one stream to said absorber and the remaining stream to said generator; (f) an evaporator which supplies said useful cooling and said vapor; (g) a condenser which receives said compressed vapor and supplies part of said useful heating; and (h) a generator heat exchange (GHX) exchanger in said generator.

Claim 6

The absorption cycle apparatus according to claim 3 additionally comprised of a charge of volatile liquid absorbent, and wherein both said second absorber and said second generator are adapted for countercurrent contact between vapor and said absorbent liquid.

Claim 7

The absorption cycle apparatus according to claim 4 additionally comprised of a closed cycle heat transfer loop which transfers heat from said second absorber to said second generator.

Claim 8

The apparatus according to claim 4 wherein said first absorber and first generator are adapted for countercurrent vapor-liquid contact, and additionally comprised of a rectifier for the desorbed vapor.

Claim 9

The apparatus according to claim 6 additionally comprised of: a) an absorber heat exchange (AHX) exchanger in each of said first and second absorbers; and b) a reflux heat exchanger in said rectifier; and c) a means for supplying sorbent to said reflux heat exchanger.

Claim 10

The apparatus according to claim 7, adapted for space conditioning, and wherein said absorbent is aqua ammonia, and additionally comprised of a condenser, an ammonia subcooler, an ammonia pressure letdown valve, an evaporator, and a sorbent pressure letdown valve.

Claim 11

The apparatus according to claim 3 additionally comprised of direct heat exchange between said second absorber and said second generator.

Claim 12

The apparatus according to claim 9 additionally comprised of: a) a charge of non-volatile absorbent; b) a means for establishing upward slug flow of absorbent and vapor in said second absorber; and c) a means for establishing vertical falling film flow of sorbent in said second generator.

Claim 13

The apparatus according to claim 3 additionally comprised of a third absorber and third generator in heat exchange relationship, and a pump which transports part of the sorbent from said third absorber to one of said generators.

Claim 14

A thermally activated process for at least one of compressing a vapor, heating, and cooling comprising: a) absorbing said vapor into a circulating absorbent liquid over an absorbing temperature range, b) cooling the absorbent liquid in the lower temperature portion of said absorbing step with an external source of cooling; c) desorbing compressed vapor from said circulating absorbent liquid over a desorbing temperature range; d) heating the absorbent liquid in the higher temperature portion of said desorbing step with an external source of heating; e) heating the absorbent liquid in the lower temperature portion of said desorbing step and cooling the absorbent liquid in the higher temperature portion of said absorbing temperature range by exchanging heat there-between; f) circulating a major fraction of a liquid absorbent comprised of absorbent component and condensed vapor sequentially through all of both of said absorbing and desorbing steps; and g) circulating a minor fraction of said liquid absorbent between only the higher temperature portion of said absorbing step and the higher temperature portion of said desorbing step, whereby the amount of absorbent component circulated to those portions exceeds that circulated to the remaining portions.

Claim 15

A thermally activated process for at least one of compressing a vapor, heating, and cooling comprising: a) absorbing said vapor into a circulating absorbent liquid over an absorbing temperature range, b) cooling the absorbent liquid in the lower temperature portion of said absorbing step with an external source of cooling; c) desorbing compressed vapor from said circulating absorbent liquid over a desorbing temperature range; d) heating the absorbent liquid in the higher temperature portion of said desorbing step with an external source of heating; e) heating the absorbent liquid in the lower temperature portion of said desorbing step and cooling the absorbent liquid in the higher temperature portion of said absorbing temperature range by exchanging heat there-between; f) circulating a major fraction of a liquid absorbent comprised of absorbent component and condensed vapor sequentially through all of both of said absorbing and desorbing steps; and g) circulating a minor fraction of said liquid absorbent between only the higher temperature portion of said absorbing step and the higher temperature portion of said desorbing step, whereby the amount of absorbent component circulated to those portions exceeds that circulated to the remaining portions.

Claim 18

The apparatus according to claim 13 wherein said means for transferring heat is comprised of: a) vertically oriented heat transfer tubes; b) a means for supplying sorbent liquid and vapor to the inside of the tubes at the bottom; and c) a means for supplying sorbent liquid to the outside of the tubes at the top.

Claim 19

The process according to claim 12 additionally comprising: (a) exchanging sensible heat between fluid undergoing said higher temperature portion of said desorbing step and sorbent liquid withdrawn therefrom; (b) exchanging sensible heat between fluid undergoing said lower temperature portion of said absorbing step and said major fraction of sorbent liquid; (c) exchanging sensible heat between fluid undergoing said higher temperature portion of said absorbing step and said minor fraction of sorbent liquid; (d) routing liquid sorbent through the desorption step portions in order of increasing temperature and countercurrently withdrawing vapor therefrom in order of descreasing temperature; and (e) routing liquid sorbent through the absorption step portions in order of decreasing temperature and countercurrently supplying vapor thereto in order of increasing temperature.

Claim 20

The apparatus according to claim 2 additionally comprised of: (a) an absorber heat exchange (AHX) exchanger in said externally-cooled absorber; (b) an absorber heat exchange (AHX) exchanger in said internally-cooled absorber; (c) vapor conduit for withdrawing vapor from the sorbent-liquid-supply portion of said externally-cooled absorber and supplying said vapor to the sorbent-liquid-withdrawal portion of said internally-cooled absorber; and (d) vapor conduit for withdrawing vapor from the sorbent-liquid-supply portion of said externally-heated desorber and supplying said vapor to the sorbent-liquid-withdrawal portion of said internally-heated desorber.

Claim 21

Apparatus according to claim 4 wherein said externally-cooled absorber, said externally-heated desorber, and said GAX absorber and GAX desorber are all adapted for internal countercurrent vapor-liquid contact, and also for inter-component countercurrent vapor-liquid contact.