Adsorption condensation solvent recovery system

Claim 2

A process for the recovery of a first gaseous component from a gas stream containing said first gaseous component, at least one inert gaseous component having a boiling point below the boiling point of said first gaseous component and at least one gaseous impurity having a freezing point above the freezing point of said first gaseous component, comprising the steps of: (a) flowing said gas stream through a first adsorption zone containing an adsorbent which preferentially adsorbs said at least one gaseous impurity thereby depleting the gas stream of said at least one gaseous impurity; (b) flowing the at least one gaseous impurity-depleted gas stream exiting said first adsorption zone through a heat transfer zone maintained at a temperature below the boiling point of said first gaseous component, thereby condensing first gaseous component from the gas stream and producing a gaseous effluent that is substantially depleted of said at least one gaseous impurity and said first gaseous component; (c) heating at least part of said gaseous effluent to a temperature above about 90° C.; (d) flowing the heated gaseous effluent through a second adsorption zone containing an adsorbent which preferentially adsorbs said at least one gaseous impurity and that contains as adsorbate said at least one gaseous impurity, thereby purging said at least one gaseous impurity from said second adsorption zone; (e) reversing the role of said first and second adsorption zones when the buildup of at said least one gaseous impurity in said first adsorption zone reaches a predetermined level, so that said at least one gaseous impurity undergoes adsorption in said second adsorption zone and desorption in said first adsorption zone; and (f) cyclically repeating steps (a) to (e), thereby continually recovering said first gaseous component from said gas stream.

Claim 3

The process of claim 1, wherein said at least one gaseous impurity comprises water vapor, carbon dioxide or mixtures of these.

Claim 4

The process of claim 1 or claim 2, wherein said first gaseous component is an organic compound.

Claim 5

The process of claim 3, wherein said organic compound is selected from hydrocarbons, oxygen-substituted hydrocarbons, chlorinated hydrocarbons and mixtures of these.

Claim 6

The process of claim 3 wherein said gas stream contains oxygen as an impurity.

Claim 7

The process of claim 5 wherein said inert gaseous component is nitrogen, argon or mixtures of these.

Claim 8

The process of claim 1 or claim 2, wherein said gaseous impurity-depleted gas stream is compressed to a pressure of at least about 2 psig prior to flowing it through said heat transfer zone.

Claim 9

The process of claim 7, wherein the gas stream is compressed to a pressure of about 2 to about 25 psig.

Claim 10

The process of claim 1 or claim 2, wherein part of the gaseous effluent exiting said heat transfer zone is recycled to said source.

Claim 11

The process of claim 9 wherein said source is an inert gas blanketed reaction vessel or a solvent-borne resin coating drying oven.

Claim 12

A process for the recovery of a vaporized volatile component from a gas stream containing said vaporized volatile component, at least one inert gaseous component having a boiling point below the boiling point of said volatile component, at least one first gaseous impurity selected from water vapor, carbon dioxide and mixtures of these, and at least one noncondensable gaseous impurity that is chemically reactive with said first gaseous component, comprising the steps of: (a) flowing said gas stream through a first adsorption zone containing an adsorbent which preferentially adsorbs said at least one first gaseous impurity, thereby depleting the gas stream of said at least one first gaseous impurity; (b) flowing the first gaseous impurity-depleted gas stream exiting said first adsorption zone through a heat transfer zone maintained at a temperature in the range between the freezing point and the boiling point of said volatile component, thereby condensing volatile component from the gas stream and producing a gaseous effluent that is substantially depleted of said at least one first gaseous impurity and said volatile component; (c) heating at least part of said gaseous effluent to a temperature above about 90° C.; (d) flowing said heated gaseous effluent through a second adsorption zone containing an adsorbent which preferentially adsorbs said at least one first gaseous impurity and that contains as adsorbate said at least one first gaseous impurity, thereby purging said at least one first gaseous impurity from said second adsorption zone; (e) reversing the role of said first and second adsorption zones when the buildup of said at least one first gaseous impurity in said first adsorption zone reaches a predetermined level, so that said at least one first gaseous impurity undergoes adsorption in said second adsorption zone and desorption in said first adsorption zone; and (f) cyclically repeating steps (a) to (e), thereby continually recovering said volatile component from said gas stream.

Claim 13

A process for the recovery of a vaporized volatile component from a gas stream containing said vaporized volatile component, at least one inert gaseous component having a boiling point below the boiling point of said volatile component, at least one first gaseous impurity selected from water vapor, carbon dioxide and mixtures of these, and at least one noncondensable gaseous impurity that is chemically reactive with said first gaseous component, comprising the steps of: (a) flowing said gas stream through a first adsorption zone containing an adsorbent which preferentially adsorbs said at least one first gaseous impurity, thereby depleting the gas stream of said at least one first gaseous impurity; (b) flowing the first gaseous impurity-depleted gas stream exiting said first adsorption zone through a heat transfer zone maintained at a temperature in the range between the freezing point and the boiling point of said volatile component, thereby condensing volatile component from the gas stream and producing a gaseous effluent that is substantially depleted of said at least one first gaseous impurity and said volatile component; (c) heating at least part of said gaseous effluent to a temperature above about 90° C.; (d) flowing said heated gaseous effluent through a second adsorption zone containing an adsorbent which preferentially adsorbs said at least one first gaseous impurity and that contains as adsorbate said at least one first gaseous impurity, thereby purging said at least one first gaseous impurity from said second adsorption zone; (e) reversing the role of said first and second adsorption zones when the buildup of said at least one first gaseous impurity in said first adsorption zone reaches a predetermined level, so that said at least one first gaseous impurity undergoes adsorption in said second adsorption zone and desorption in said first adsorption zone; and (f) cyclically repeating steps (a) to (e), thereby continually recovering said volatile component from said gas stream.

Claim 14

The process of claim 11, wherein said volatile component is an organic compound.

Claim 15

The process of claim 12, wherein said organic compound is selected from hydrocarbons, oxygen-substituted hydrocarbons, chlorinated hydrocarbons and mixtures of these.

Claim 16

The process of claim 11 wherein said noncondensable gaseous impurity is oxygen.

Claim 17

The process of claim 14 wherein said inert gaseous component is nitrogen, argon or mixtures of these.

Claim 18

The process of claim 11, wherein said first gaseous impurity-depleted gas stream is compressed to a pressure of at least about 2 psig prior to flowing it through said heat transfer zone.

Claim 19

The process of claim 16, wherein the gas stream is compressed to a pressure of about 2 to about 25 psig.

Claim 20

The process of claim 1 or claim 11, wherein said heat transfer zone is cooled by indirect heat transfer with a refrigerant.

Claim 21

The process of claim 18, wherein said refrigerant is selected from chilled inert gas, liquefied inert gas and mixtures of these.

Claim 22

The process of claim 19, wherein said inert gas is selected from nitrogen, argon and mixtures of these.

Claim 23

The process of claim 18, wherein the gas stream entering said heat transfer zone is compressed to about 5 to about 15 psig.

Claim 24

The process of claim 18, wherein said refrigerant cools an intermediate refrigerant which provides cooling in said heat transfer zone.

Claim 25

The process of claim 18, wherein said refrigerant is selected from hydrocarbons, alcohols and mixtures of these.

Claim 26

A process for the recovery of one or more vaporized volatile components from a gas stream containing said at least one vaporized volatile component, nitrogen, water vapor and oxygen, comprising the steps of: (a) withdrawing said gas stream from a source; (b) flowing said gas stream through a first adsorption zone containing an adsorbent which preferentially adsorbs water vapor, thereby depleting the gas stream of water vapor; (b) flowing the water vapor-depleted gas stream exiting said first adsorption zone through a heat transfer zone maintained at a temperature in the range between the freezing point and the boiling point of said one or more volatile components, thereby condensing said one or more volatile components from the gas stream and producing a gaseous effluent that is substantially depleted of water vapor and said at least one volatile component; (c) heating at least part of said gaseous effluent to a temperature in the range of about 90° C. to about 260° C.; (d) flowing said heated gaseous effluent through a second adsorption zone containing an adsorbent which preferentially adsorbs water vapor and contains adsorbed water vapor, thereby purging said adsorbed water vapor from said second adsorption zone; (e) introducing substantially pure nitrogen into said source (f) reversing the role of said first and second adsorption zones when the buildup of water vapor in said first adsorption zone reaches a predetermined levels so that water vapor undergoes adsorption in said second adsorption zone and desorption in said first adsorption zone; and (g) cyclically repeating steps (a) to (f), thereby continually recovering said volatile component from said gas stream.

Claim 27

A process for the recovery of one or more vaporized volatile components from a gas stream containing said at least one vaporized volatile component, nitrogen, water vapor and oxygen, comprising the steps of: (a) withdrawing said gas stream from a source; (b) flowing said gas stream through a first adsorption zone containing an adsorbent which preferentially adsorbs water vapor, thereby depleting the gas stream of water vapor; (b) flowing the water vapor-depleted gas stream exiting said first adsorption zone through a heat transfer zone maintained at a temperature in the range between the freezing point and the boiling point of said one or more volatile components, thereby condensing said one or more volatile components from the gas stream and producing a gaseous effluent that is substantially depleted of water vapor and said at least one volatile component; (c) heating at least part of said gaseous effluent to a temperature in the range of about 90° C. to about 260° C.; (d) flowing said heated gaseous effluent through a second adsorption zone containing an adsorbent which preferentially adsorbs water vapor and contains adsorbed water vapor, thereby purging said adsorbed water vapor from said second adsorption zone; (e) introducing substantially pure nitrogen into said source (f) reversing the role of said first and second adsorption zones when the buildup of water vapor in said first adsorption zone reaches a predetermined levels so that water vapor undergoes adsorption in said second adsorption zone and desorption in said first adsorption zone; and (g) cyclically repeating steps (a) to (f), thereby continually recovering said volatile component from said gas stream.

Claim 28

The process of claim 24, wherein said at least one volatile component is an organic compound.

Claim 29

The process of claim 25, wherein said organic compound is selected from hydrocarbons, oxygen-substituted hydrocarbons, chlorinated hydrocarbons and mixtures of these.

Claim 30

The process of claim 24, additionally comprising the step of compressing the water vapor-depleted gas stream exiting said first adsorption zone to a pressure of about 2 to about 25 psig prior to flowing it into said heat transfer zone.

Claim 31

The process of claim 24, wherein part of the gaseous effluent exiting said heat transfer zone is recycled to said source.

Claim 32

The process of claim 28 wherein said source is an inert gas blanketed reaction vessel or a solvent-borne resin coating drying oven.

Claim 33

The process of claim 24, wherein said heat transfer zone is chilled with a cooled or liquefied inert gaseous substance and said inert gaseous substance is subsequently transported to said source.

Claim 34

The process of claim 24, wherein the amount of substantially pure nitrogen introduced into said source is sufficient to substantially replace the volume of noncondensable gases removed from the system during step (d).