Refrigeration process and apparatus

Claim 2

A refrigeration process comprising the steps of: evaporating first and second liquid refrigerants recycled from the below recited condensing step, said evaporating step forming a vapor mixture of the first and second refrigerants, absorbing the first refrigerant from the vapor mixture in a liquid absorbent to separate the first and second refrigerants and to form a second-refrigerant vapor stream, desorbing the first refrigerant by heating the liquid absorbent to generate a first-refrigerant vapor stream, compressing the second-refrigerant vapor stream, and condensing the first-refrigerant vapor stream and the compressed second-refrigerant vapor stream to form the respective first and second liquid refrigerants recycled to the evaporating step.

Claim 3

The process of claim 1, wherein the first and second liquid refrigerants are immiscible or only partly miscible, and the mixture in the evaporating step has a vapor pressure substantially greater than either vapor pressure of the individual first and second refrigerants.

Claim 4

The process of claim 1, wherein the heating of the liquid absorbent includes the use of waste heat from the compressing step.

Claim 5

The process of claim 1, including compressing vapor from the evaporating step in a first stage of a multistage compressor prior to the absorbing step, and wherein the second-refrigerant compressing step is performed in subsequent stages of the compressor.

Claim 6

The process of claim 1, wherein the first refrigerant is selected from the group consisting of ammonia, sulfur dioxide, nitrogen dioxide, carbon disulfide, carbon tetrafluoride, carbon tetrachloride, and combinations thereof, and the second refrigerant is one or more hydrocarbons having from 1 to 5 carbon atoms.

Claim 7

The process of claim 5, wherein the absorbent is water, an alcohol having from 1 to 3 carbon atoms, or mixtures thereof.

Claim 8

The process of claim 6, wherein the first refrigerant is ammonia, the second refrigerant is propane and the absorbent is water.

Claim 9

The process of claim 7, wherein the ammonia is absorbed in the water at a pressure optimized for the level of heat used in distilling the ammonia, and the propane is totally condensed using ambient temperature cooling water or air.

Claim 10

The process of claim 8, including compressing the mixture of ammonia and propane vapor in a first stage of a multiple stage compressor prior to the absorption step, and wherein the propane is compressed in a final stage of the multistage compressor to a final pressure of about 17.4 bar corresponding to a propane condensing temperature of about 49° C., resulting in a compression ratio of about 10 to 1.

Claim 11

A refrigeration apparatus having reduced horsepower requirements, comprising: a chiller for cooling a process stream or other environment by evaporation of first and second refrigerants to form a vapor mixture of the first and second refrigerants; an absorber positioned downstream of the chiller for absorbing the first refrigerant from the vapor mixture from the chiller with a liquid absorbent to separate the first refrigerant from the second refrigerant; a compressor for compressing the non-absorbed second refrigerant from the absorber; a condenser for condensing the compressed non-absorbed second refrigerant from the compressor to form a second refrigerant liquid stream; a regenerator for separating the absorbed refrigerant from the liquid absorbent for forming a first-refrigerant vapor stream; a condenser for condensing the first refrigerant vapor stream to form a first-refrigerant liquid stream; and recycle means for passing the first and second refrigerant liquid streams to the chiller.

Claim 12

A refrigeration apparatus having reduced horsepower requirements, comprising: a chiller for cooling a process stream or other environment by evaporation of first and second refrigerants to form a vapor mixture of the first and second refrigerants; an absorber positioned downstream of the chiller for absorbing the first refrigerant from the vapor mixture from the chiller with a liquid absorbent to separate the first refrigerant from the second refrigerant; a compressor for compressing the non-absorbed second refrigerant from the absorber; a condenser for condensing the compressed non-absorbed second refrigerant from the compressor to form a second refrigerant liquid stream; a regenerator for separating the absorbed refrigerant from the liquid absorbent for forming a first-refrigerant vapor stream; a condenser for condensing the first refrigerant vapor stream to form a first-refrigerant liquid stream; and recycle means for passing the first and second refrigerant liquid streams to the chiller.

Claim 13

The apparatus of claim 10, wherein the compressor is two stage, the absorber is positioned between the first and second stages and the first stage compresses the vapor mixture from the chiller.

Claim 14

The apparatus of claim 11, wherein the first refrigerant is selected from the group consisting of ammonia, sulfur dioxide, nitrogen dioxide, carbon disulfide, carbon tetrafluoride, carbon tetrachloride and combinations thereof, and the second refrigerant is one or more hydrocarbons having from 1 to 5 carbon atoms.

Claim 15

The apparatus of claim 12, wherein the absorbent is water, an alcohol having from 1 to 3 carbon atoms, or mixtures thereof.

Claim 16

The apparatus of claim 10, wherein the regenerator includes a distillation column with a reboiler which utilizes waste heat as an energy source.

Claim 17

The apparatus of claim 13, wherein the first refrigerant is ammonia, the remaining unabsorbed refrigerant is propane and the solvent is water.

Claim 18

The apparatus of claim 10 wherein the recycle means includes respective expansion valve means for the respective first and second refrigerant liquid streams.

Claim 19

The apparatus of claim 14 wherein the reboiler includes means for utilizing waste heat from the compressor.