Absorption refrigeration method and apparatus

Claim 2

In an absorption refrigeration process which includes the steps of heating a dilute absorbent solution in a first phase to drive off a diluent to form a concentrated absorbent solution and condensing the diluent and delivering same to a second phase to remove heat from a refrigeration load and reabsorbing the diluent in the concentrated absorbent solution to thereby form a diluted absorbent solution for return to said first phase, the improvement comprising: maintaining a pressure within said first phase equivalent to the pressure in the second phase so as to minimize absorbent solution temperature differences and eliminate diluent temperature differences; and storing functionally sufficient quantities in liquid form of said concentrated and diluted absorbent solutions and said cold diluent produced in said first and second phases so as to enable said first and second phases to be operable independently time-wise of one another.

Claim 3

The process of claim 1 wherein said concentrated and diluted absorbent liquids and said liquid diluent are stored in three separate zones.

Claim 4

The process of claim 2 wherein at least one of said zones is separated from said first and second phases.

Claim 5

The process of claim 1 including the steps of: producing first liquid streams of said concentrated absorbent solution and cold diluent in said first phase; storing at least portions of said liquid streams in first and second zones; removing second liquid streams of each of said concentrated absorbent solution and cold diluent from said first and second zones in quantities to meet demands for same in said second phase; producing a liquid stream of diluted absorbent solution in said second phase; storing at least a portion of said liquid stream of diluted absorbent solution in a third zone; withdrawing said diluted absorbent solution from said third zone for use in said first phase only at intervals when it is required to replenish the concentrated absorbent solution and diluent stored in said first and second zones; and said steps excluding any interchange of heat with any of said absorbent solution streams outside of said zones.

Claim 6

The process of claim 1 wherein the absorbent solution is aqueous.

Claim 7

The process of claim 1 wherein the absorbent solution contains lithium bromide.

Claim 8

The process of claim 1 including the steps of distilling the diluted absorbent solution within said first phase by heating with energy expelled from a heat pump condenser and diluent vapor thereby generated is condensed within said first phase and the heat of condensation is captured and reinjected into the concentration process.

Claim 9

The process of claim 1 wherein the diluted absorbent solution is concentrated by heating within said first phase and the diluent is condensed by cooling within said first phase and each of said heating and cooling within said first phase are performed by condensing and evaporating functions of a heat pump connected in series within said first phase to receive a refrigerant gas flow from a compressor located exterior of said first phase.

Claim 10

In an improved absorption refrigeration apparatus wherein a dilute absorbent solution is heated within a concentrator vessel to produce a diluent and a concentrated absorbent solution which are delivered to an evaporator/absorber vessel wherein the diluent is heated to release vapors to combine with the concentrated absorbent solution and thereby produce a dilute absorbent solution which is returned to the concentrator vessel, the improvement comprising: means comprising a system of valves and pumps between said vessels whereby to maintain equal pressure between said vessels; and liquid storing means connected to said vessels for said concentrated absorbent solution, diluent and dilute absorbent solution, said liquid storing means being of sufficient capacity so as to enable operation of said concentrator vessel independently of said evaporator vessel.

Claim 11

In an improved absorption refrigeration apparatus wherein a dilute absorbent solution is heated within a concentrator vessel to produce a diluent and a concentrated absorbent solution which are delivered to an evaporator/absorber vessel wherein the diluent is heated to release vapors to combine with the concentrated absorbent solution and thereby produce a dilute absorbent solution which is returned to the concentrator vessel, the improvement comprising: means comprising a system of valves and pumps between said vessels whereby to maintain equal pressure between said vessels; and liquid storing means connected to said vessels for said concentrated absorbent solution, diluent and dilute absorbent solution, said liquid storing means being of sufficient capacity so as to enable operation of said concentrator vessel independently of said evaporator vessel.

Claim 12

The apparatus of claim 9 including first and second storing means for retaining at least portions of the concentrated absorbent solution and diluent produced in the concentrator vessel and connected to the evaporator vessel to deliver said concentrated absorbent solution and diluent according to the need occurring in said evaporator vessel; and third storing means for retaining at least a portion of the dilute absorbent solution produced in said evaporator vessel and connected to said concentrator vessel to deliver said dilute absorbent solution as needed to replenish said first and second storing means.

Claim 13

The apparatus of claim 9 wherein said liquid storing means is positioned between said concentrator and evaporator vessels.

Claim 14

The apparatus of claim 10 wherein said solution storing means are positioned between said concentrator and evaporator vessels and excluding any means for interchanging heat with any of said absorbent solutions outside of said vessels.

Claim 15

The apparatus of claim 9 including a heat pump connected to the concentrator vessel, and wherein a condenser coil of said heat pump is positioned within said concentrator vessel to heat the dilute absorbent solution and an evaporator coil of said heat pump is positioned within said concentrator vessel to cool and condense the diluent.

Claim 16

The apparatus of claim 13 wherein the heat pump comprises said condenser coil and evaporator coil and a compressor connected in series therewith and power means is connected to drive said compressor.

Claim 17

The apparatus of claim 14 wherein said compressor and power means are positioned outside of said concentrator vessel.

Claim 18

An improved absorption refrigeration apparatus comprising: a concentrator vessel maintained at a first pressure; a sump for concentrated absorbent solution in one section of said concentrator vessel; a spray header in said section above said sump for introducing dilute absorbent solution into said concentrator vessel; a first collection pan in another section of said concentrator vessel, said first collection pan to receive diluent released from the absorbent solution in said one section; a first reservoir connected to said concentrator vessel sump; a second reservoir connected to said first collection pan; a third reservoir connected to said spray header in said concentrator vessel; an evaporator vessel spaced from said concentrator vessel, said evaporator vessel maintained substantially said first pressure; a diluent spray header located in one section of said evaporator vessel, said diluent spray header being connected to said second reservoir; an absorbent solution spray header located in another section of said evaporator vessel, said absorbent solution spray header connected to said first reservoir; and a dilute absorbent solution sump in said one section of said evaporator vessel, said sump being connected to said third reservoir.

Claim 19

An improved absorption refrigeration apparatus comprising: a concentrator vessel maintained at a first pressure; a sump for concentrated absorbent solution in one section of said concentrator vessel; a spray header in said section above said sump for introducing dilute absorbent solution into said concentrator vessel; a first collection pan in another section of said concentrator vessel, said first collection pan to receive diluent released from the absorbent solution in said one section; a first reservoir connected to said concentrator vessel sump; a second reservoir connected to said first collection pan; a third reservoir connected to said spray header in said concentrator vessel; an evaporator vessel spaced from said concentrator vessel, said evaporator vessel maintained substantially said first pressure; a diluent spray header located in one section of said evaporator vessel, said diluent spray header being connected to said second reservoir; an absorbent solution spray header located in another section of said evaporator vessel, said absorbent solution spray header connected to said first reservoir; and a dilute absorbent solution sump in said one section of said evaporator vessel, said sump being connected to said third reservoir.

Claim 20

The apparatus claim 16 including flow control valves between each of said reservoirs and the respective spray headers.

Claim 21

The apparatus of claim 16 including a heat pump connected to the concentrator vessel, and wherein a condenser coil of said heat pump is positioned in said one section between said sump and said spray header for introducing dilute absorbent solution, and an evaporator coil of said heat pump is positioned in said another section above said first collection pan.

Claim 22

The apparatus of claim 18 including a compressor connected in series with said condenser coil and said evaporator coil, said compressor being located outside said concentrator vessel.