High efficiency refrigerant recovery system

Claim 3

The apparatus according to claim 1 wherein said scrubbing column is from about 2 inches to about 1 foot in diameter.

Claim 4

The apparatus according to claim 2 wherein said scrubbing column is about 2 feet to about 10 feet in height.

Claim 5

The apparatus according to claim 1 wherein said scrubbing column is vertically disposed.

Claim 6

The apparatus according to claim 1 wherein said scrubbing column comprises a packing material having a plurality of surfaces to facilitate the intimate counter-current contact of said liquid and said purge stream.

Claim 7

The apparatus according to claim 5 wherein said packing material comprises a woven material.

Claim 8

The apparatus according to claim 1 wherein said high boiling point liquid comprises a lubrication oil.

Claim 9

The apparatus according to claim 1 wherein said high boiling point liquid is diisooctyl adipate.

Claim 10

The apparatus according to claim 1 wherein said means for recovering the mixture of high boiling point liquid and refrigerant comprises control means for controlling the level of said mixture within the lower section of said column.

Claim 11

The apparatus according to claim 9 wherein said control means comprises: detecting means for detecting the level of said mixture in said column; and valve means responsive to said detecting means for releasing said mixture from the column at a variable rate.

Claim 12

The apparatus according to claim 10 wherein said detecting means is a float.

Claim 13

The apparatus according to claim 10 wherein said valve means comprises: a housing having a central bore encircled by a plurality of peripheral bores; a stem connected at an upper portion of thereof with said float and extending downwardly from said float into said central bore; an orifice positioned at a lower portion of said housing for receiving a lower end of said stem; and a guide member attached to said stem and being slidably positioned within said central bore at a point above said orifice, and wherein said upper portion of the central bore is fluidly connected with said lower portion of the central bore via passages positioned at opposing ends of each of said peripheral bores and in communication with said central bore.

Claim 14

The apparatus according to claim 12 wherein said stem tapers from a larger to a smaller diameter from an upper to a lower portion thereof.

Claim 15

The apparatus according to claim 1 wherein said means for venting non-condensible gases comprises: pressure sensing means for determining when a predetermined amount of non-condensible gas has collected in the top of the column; and valve means responsive to said pressure sensing means for venting said non-condensible gas to the atmosphere from the top of the column after said predetermined amount of gas has collected.

Claim 16

The apparatus according to claim 14 wherein said valve means is a solenoid actuated valve.

Claim 17

The apparatus according to claim 1 further comprising means downstream of said scrubbing column for separating refrigerant from said mixture of refrigerant and high boiling point liquid.

Claim 18

The apparatus according to claim 16 wherein said gas/liquid separation means comprises a flash separation unit maintained at a thermodynamic condition sufficient for separating a substantial amount of the refrigerant from said mixture.

Claim 19

The apparatus according to claim 17 further comprising a vacuum pump for maintaining said thermodynamic condition in said gas liquid separation zone.

Claim 20

The apparatus according to claim 18 wherein said vacuum pump is a diaphragm pump.

Claim 21

The apparatus according to claim 16 further comprising means for recirculating said high boiling point liquid from the separation unit to the scrubbing column.

Claim 22

The apparatus according to claim 20 wherein said recirculating means comprises: a valve for removing said high boiling point liquid from a lower portion of the separation unit; and a pump for recirculating the high boiling point liquid removed from said separation unit to said upper section of the scrubbing column.

Claim 23

The apparatus according to claim 16 further comprising means for recycling said refrigerant to said refrigeration system.

Claim 26

A purge system for removing non-condensible gases from a refrigerant in a refrigeration system comprising: a first purge means for removing refrigerant from a refrigerant-containing purge stream; and a second purge means for receiving the refrigerant-containing purge stream from said first purge means; wherein said second purge means comprises means for counter-currently contacting said purge stream with a high boiling point liquid capable of absorbing said refrigerant and means for venting non-condensible gasses to the atmosphere.

Claim 27

A purge system for removing non-condensible gases from a refrigerant in a refrigeration system comprising: a first purge means for removing refrigerant from a refrigerant-containing purge stream; and a second purge means for receiving the refrigerant-containing purge stream from said first purge means; wherein said second purge means comprises means for counter-currently contacting said purge stream with a high boiling point liquid capable of absorbing said refrigerant and means for venting non-condensible gasses to the atmosphere.

Claim 28

A purge system for removing non-condensible gases from a refrigerant in a refrigeration system comprising a receiving means for receiving a refrigerant-containing gaseous purge stream from said refrigeration system, means for countercurrently contacting said purge stream with a high boiling point liquid capable of absorbing said refrigerant, means for venting non-condensible gasses to the atomsphere, and separating means for separating refrigerant from a mixture of said refrigerant and said high boiling point liquid.

Claim 29

A purge system for removing non-condensible gases from a refrigerant in a refrigeration system comprising a receiving means for receiving a refrigerant-containing gaseous purge stream from said refrigeration system, means for countercurrently contacting said purge stream with a high boiling point liquid capable of absorbing said refrigerant, means for venting non-condensible gasses to the atomsphere, and separating means for separating refrigerant from a mixture of said refrigerant and said high boiling point liquid.

Claim 30

A process for removing non-condensible gases from a refrigerant in a refrigeration system, the process comprising: introducing a gaseous stream including refrigerant and non-condensible gases from a refrigeration system into a lower section of a scrubbing zone; introducing a high boiling point liquid capable of absorbing said refrigerant into an upper section of said scrubbing zone; flowing said high boiling point liquid downwardly through said scrubbing zone in countercurrent relationship to said gaseous stream so that at least a portion of the refrigerant is absorbed by said high boiling point liquid; recovering a mixture comprising refrigerant and high boiling point liquid from a lower section of said scrubbing zone; and removing a non-condensible gas stream from the top of said scrubbing zone.

Claim 31

A process for removing non-condensible gases from a refrigerant in a refrigeration system, the process comprising: introducing a gaseous stream including refrigerant and non-condensible gases from a refrigeration system into a lower section of a scrubbing zone; introducing a high boiling point liquid capable of absorbing said refrigerant into an upper section of said scrubbing zone; flowing said high boiling point liquid downwardly through said scrubbing zone in countercurrent relationship to said gaseous stream so that at least a portion of the refrigerant is absorbed by said high boiling point liquid; recovering a mixture comprising refrigerant and high boiling point liquid from a lower section of said scrubbing zone; and removing a non-condensible gas stream from the top of said scrubbing zone.

Claim 32

The process according to claim 26 wherein said scrubbing zone comprises a packing material having a plurality of surfaces.

Claim 33

The process according to claim 27 wherein said packing material comprises a woven packing material.

Claim 34

The process according to claim 26 wherein said scrubbing zone is defined by a vertically disposed packed column.

Claim 35

The process according to claim 26 wherein said high boiling point liquid is a lubrication oil.

Claim 36

The process according to claim 30 wherein said high boiling point liquid is diisooctyl adipate.

Claim 37

The process according to claim 26 wherein said high boiling point liquid absorbs at least about 90 wt. % of the refrigerant from said gaseous stream.

Claim 38

A process according to claim 26 wherein said high boiling point liquid absorbs at least about 95 wt. % of the refrigerant from said gaseous stream.

Claim 39

The process according to claim 26 wherein said high boiling point liquid absorbs at least about 99 wt. % of the refrigerant from said gaseous stream.

Claim 40

The process according to claim 26 wherein the step of recovering the mixture comprising refrigerant and high boiling point liquid from a lower section of the scrubbing zone comprises: removing said mixture from said scrubbing zone at a variable rate sufficient to maintain a substantially constant height of liquid in the lower portion of said scrubbing zone.

Claim 41

The process according to claim 26 wherein the step of removing the non-condensible gas stream comprises continuously venting the stream to the atmosphere.

Claim 42

The process according to claim 26 wherein the step of removing the non-condensible gas stream comprises: detecting when a predetermined amount of non-condensible gas stream has been collected in an upper portion of said scrubbing zone; and venting the stream to the atmosphere in response to said detecting step.

Claim 43

The process according to claim 26 wherein said non-condensible gas stream comprises less than about 0.10 pounds of refrigerant per pound of non-condensible gases.

Claim 44

The process according to claim 26 further comprising the step of separating the refrigerant from said mixture comprising refrigerant and high boiling point liquid.

Claim 45

The process according to claim 39 wherein said separating step comprises: directing said mixture from the lower section of the column to a gas/liquid separation zone; and maintaining the temperature and pressure conditions within said gas/liquid separation zone sufficient to effect removal of a substantial amount of the refrigerant from said mixture in gaseous form.

Claim 46

The process according to claim 39 further comprising the step of removing said high boiling point liquid from a lower portion of the separation zone and directing said liquid to the upper section of said scrubbing zone.

Claim 47

The process according to claim 40 further comprising the steps of collecting refrigerant vapor from an upper portion of the separation zone and directing said vapor to the refrigeration system.

Claim 48

A process for removing non-condensible gases from a refrigerant in a refrigeration system, the process comprising: introducing a gaseous stream including refrigerant and non-condensible gases from a refrigeration system into a lower section of a vertically disposed scrubbing column comprising a plurality of contacting surfaces; introducing a high boiling point liquid capable of dissolving said refrigerant into an upper section of said column; flowing said high boiling point liquid downwardly through said column in countercurrent relationship to said gaseous stream so that at least about 90 wt. % of the refrigerant is absorbed by said high boiling point liquid; recovering a mixture comprising refrigerant and high boiling point liquid from a lower section of said column; and removing a non-condensible gas stream from the top of said column.

Claim 49

A process for removing non-condensible gases from a refrigerant in a refrigeration system, the process comprising: introducing a gaseous stream including refrigerant and non-condensible gases from a refrigeration system into a lower section of a vertically disposed scrubbing column comprising a plurality of contacting surfaces; introducing a high boiling point liquid capable of dissolving said refrigerant into an upper section of said column; flowing said high boiling point liquid downwardly through said column in countercurrent relationship to said gaseous stream so that at least about 90 wt. % of the refrigerant is absorbed by said high boiling point liquid; recovering a mixture comprising refrigerant and high boiling point liquid from a lower section of said column; and removing a non-condensible gas stream from the top of said column.

Claim 50

A process for removing non-condensible gases from a refrigerant in a refrigeration system, the process comprising: introducing a gaseous stream including refrigerant and non-condensible gases from a refrigeration system into a lower section of a vertically disposed scrubbing column comprising a plurality of contacting surfaces; introducing a liquid comprising a high boiling alkyl ester into an upper section of said column; flowing said liquid downwardly through said column in countercurrent relationship to said gaseous stream under condition such that at least about 95 wt. % of the refrigerant is absorbed by said liquid; recovering a mixture of said liquid and refrigerant from a lower section of said column; directing said mixture from the lower section of the column to a gas/liquid separation zone maintained at a thermodynamic condition sufficient for separating said refrigerant from said mixture; separately recovering said refrigerant and said high boiling point liquid from said separation zone; recycling said high boiling point liquid from said separation zone to said upper section of said column; and removing a gaseous stream from an upper section of said column.

Claim 51

A process for removing non-condensible gases from a refrigerant in a refrigeration system, the process comprising: introducing a gaseous stream including refrigerant and non-condensible gases from a refrigeration system into a lower section of a vertically disposed scrubbing column comprising a plurality of contacting surfaces; introducing a liquid comprising a high boiling alkyl ester into an upper section of said column; flowing said liquid downwardly through said column in countercurrent relationship to said gaseous stream under condition such that at least about 95 wt. % of the refrigerant is absorbed by said liquid; recovering a mixture of said liquid and refrigerant from a lower section of said column; directing said mixture from the lower section of the column to a gas/liquid separation zone maintained at a thermodynamic condition sufficient for separating said refrigerant from said mixture; separately recovering said refrigerant and said high boiling point liquid from said separation zone; recycling said high boiling point liquid from said separation zone to said upper section of said column; and removing a gaseous stream from an upper section of said column.