Process for producing cold operated with phase separation

Claim 2

In a process for producing cold in a phase separation cycle, which comprises the steps of: (a) compressing, in a compression zone, a gas phase of a refrigerant fluid, to form a compressed gas phase, dissolving at least in part the compressed gas phase in a liquid solvent phase, to obtain a solution, and transferring at least in part the compression heat and the dissolution heat to an external cooling fluid, (b) cooling the solution recovered from step (a) in the manner defined in step (d) hereinafter, to obtain the separation of the solution into two distinct liquid phases, (c) separating the light liquid phase from the heavy liquid phase, (d) contacting the heavy liquid phase of step (c), in heat exchange relationship, with the solution to be cooled of step (b), and thereafter supplying said heavy liquid phase, as a solvent phase, to step (a) to dissolve an additional amount of compressed gas phase, (e) expanding the light liquid phase of step (c) and vaporizing it to produce cold, (f) recycling the vaporized light phase of step (e) to the compression zone of step (a) as a gas phase of refrigerant fluid, with the improvement comprising: dividing the light liquid phase in step (e) into at least two portions (F 1 ) and (F 2 ); vaporizing the one portion (F 1 ) of the light liquid phase in heat exchange contact with the solution from step (a), to further decrease the temperature of said solution and to facilitate its separation in step (b); and vaporizing the other portion (F 2 ) of said light liquid phase in heat exchange contact with an external medium which is cooled, and said external medium being a medium other than the solution recovered from step (a).

Claim 3

In a process for cooling an external medium, which comprises the steps of: (a) compressing, in a compression zone, a gas phase of a refrigerant fluid, to form a compressed gas phase, dissolving at least in part the compressed gas phase in a liquid solvent phase, to obtain a solution, and transferring at least in part the compression heat and the dissolution heat to an external cooling fluid, (b) contacting the solution obtained in step (a), in heat exchange relationship, with a heavy liquid phase obtained in step (c) as defined hereinafter, with the contacting conducted in the manner defined in step (d) hereinafter, to cool said solution and obtain separation of the solution into two distinct liquid phases, with said two distinct liquid phases being a light liquid phase and a heavy liquid phase, (c) separating the light liquid phase from the heavy liquid phase, (d) contacting the heavy liquid phase separated in step (c), in heat exchange relationship, with the solution to be cooled in step (b), and thereafter supplying said heavy liquid phase, as a solvent phase, to step (a) to dissolve an additional amount of compressed gas phase, (e) expanding the light liquid phase separated in step (c) and vaporizing at least a fraction of the resultant expanded light liquid phase in heat exchange contact with an external medium to be cooled, and (f) recycling the vaporized light phase of step (e) to the compression zone of step (a) as gas phase of refrigerant fluid, the improvement comprising: dividing the light liquid phase of step (e) into at least two portions (F 1 ) and (F 2 ); vaporizing the one portion (F 2 ) of said light liquid phase as said vaporized fraction of the resultant light liquid phase of step (e) in said heat exchange contact with the external medium to be cooled; and vaporizing the other portion (F 1 ) of said light liquid phase in heat exchange contact with the solution to be cooled of step (b), to further decrease the temperature of said solution and make its separation easier.

Claim 4

In a process for cooling an external medium, which comprises the steps of: (a) compressing, in a compression zone, a gas phase of a refrigerant fluid, to form a compressed gas phase, dissolving at least in part the compressed gas phase in a liquid solvent phase, to obtain a solution, and transferring at least in part the compression heat and the dissolution heat to an external cooling fluid, (b) contacting the solution obtained in step (a), in heat exchange relationship, with a heavy liquid phase obtained in step (c) as defined hereinafter, with the contacting conducted in the manner defined in step (d) hereinafter, to cool said solution and obtain separation of the solution into two distinct liquid phases, with said two distinct liquid phases being a light liquid phase and a heavy liquid phase, (c) separating the light liquid phase from the heavy liquid phase, (d) contacting the heavy liquid phase separated in step (c), in heat exchange relationship, with the solution to be cooled in step (b), and thereafter supplying said heavy liquid phase, as a solvent phase, to step (a) to dissolve an additional amount of compressed gas phase, (e) expanding the light liquid phase separated in step (c) and vaporizing at least a fraction of the resultant expanded light liquid phase in heat exchange contact with an external medium to be cooled, and (f) recycling the vaporized light phase of step (e) to the compression zone of step (a) as gas phase of refrigerant fluid, the improvement comprising: dividing the light liquid phase of step (e) into at least two portions (F 1 ) and (F 2 ); vaporizing the one portion (F 2 ) of said light liquid phase as said vaporized fraction of the resultant light liquid phase of step (e) in said heat exchange contact with the external medium to be cooled; and vaporizing the other portion (F 1 ) of said light liquid phase in heat exchange contact with the solution to be cooled of step (b), to further decrease the temperature of said solution and make its separation easier.

Claim 5

A process according to claim 1, wherein said vaporization of the portion (F 1 ) of the light liquid phase is effected simultaneously to the heat exchange of step (d).

Claim 6

A process according to claim 1, wherein said vaporization of the portion (F 1 ) of the light liquid phase is effected in contact with the solution recovered from step (a), after that solution has been cooled in step (b).

Claim 7

A process according to claim 1, wherein, in step (e), the portion (F 1 ) of the light liquid phase to be vaporized in contact with the solution recovered from step (a) is subjected to a smaller expansion than the portion (F 2 ) of the light liquid phase to be vaporized in contact with the external medium to be cooled, and wherein the portion (F 2 ), after vaporization, is fed to the inlet of the compression zone and the portion (F 1 ) to an intermediate point of said compression zone.

Claim 8

A process according to claim 1, wherein the portion (F 2 ) of the light liquid phase, after expansion and vaporization in contact with the external medium to be cooled, is contacted in heat exchange relation, with an additional amount of the same portion (F 2 ) before expansion of the latter.

Claim 9

A process according to claim 1, wherein the portion (F 2 ) of the light liquid phase, after expansion and vaporization in contact with the external medium to be cooled, is contacted, in heat exchange relation, with the solution to be cooled, recovered from step (a) before its fractionation in step (c).

Claim 10

A process according to claim 2, wherein the refrigerant fluid consists of one or more hydrocarbons, one or more halogenated hydrocarbons, carbon dioxide, carbon monoxide, ammonia, nitrogen, helium, hydrogen or a mixture of several of these fluids, and the solvent is a compound selected from the alcohols, ketones, aldehydes, ethers, esters, nitro derivatives, nitriles, amides, amines, hydrocarbons, fluorinated or chlorinated hydrocarbons, or a mixture of several of these compounds.

Claim 11

A process according to claim 2, wherein the refrigerant fluid consists of one or more halogenated hydrocarbons and the solvent is propanol.

Claim 12

A process according to claim 2, wherein the refrigerant fluid is ethane and the solvent is a mixture of 20 to 80% by mole of acetone with 80 to 20% by mole of methanol.

Claim 13

A process according to claim 2, wherein the refrigerant fluid is ethane and the solvent is acetone.

Claim 14

A process according to claim 1 to 10, wherein the heat exchange between the portion (F 1 ) of the vaporized light liquid phase and the solution recovered from step (a) is effected in counter-current.

Claim 15

A process according to claim 2, operated in a refrigeration machine comprising a lubricated compressor and wherein the refrigerant fluid is selected from the halogenated hydrocarbons and the solvent consists of the same liquid as used to lubricate the compressor.

Claim 16

A process according to claim 1 further comprising controlling the amount of cooling of the solution in step (b) by adjusting the amount in the fraction of the portion (F 1 ) which is vaporized in contact with the solution being cooled in step (b).

Claim 17

A process according to claim 13 further comprising controlling the amount of cooling of the solution in step (b) by adjusting the amount in the fraction of the portion (F 1 ) which is vaporized in contact with the solution being cooled in step (b).

Claim 18

A process according to claim 2, wherein said vaporization of the portion (F 1 ) of the light liquid phase is effected simultaneously to the heat exchange of step (d).

Claim 19

A process accorrding to claim 2, wherein said vaporization of the portion (F 1 ) of the light liquid phase is effected in contact with the solution recovered from step (a), after that solution has been cooled in step (b).

Claim 20

A process according to claim 2, wherein, in step (e), the portion (F 1 ) of the light liquid phase to be vaporized in contact with the solution recovered from step (a) is subjected to a smaller expansion than the portion (F 2 ) of the light liquid phase to be vaporized in contact with the external medium to be cooled, and wherein the portion (F 2 ), after vaporization, is fed to the inlet of the compression zone and the portion (F 1 ) to an intermediate point of said compression zone.

Claim 21

A process according to claim 2, wherein the portion (F 2 ) of the light liquid phase, after expansion and vaporization in contact with the external medium to be cooled, is contacted in heat exchange relation, with an additional amount of the same portion (F 2 ) before expansion of the latter.

Claim 22

A process according to claim 2, wherein the portion (F 2 ) of the light liquid phase, after expansion and vaporization in contact with the external medium to be cooled, is contacted, in heat exchange relation, with the solution to be cooled, recovered from step (a) before its fractionation in step (c).