Abstract The present invention relates to an energy and equipment efficient cyclic process for the recovery of a condensable organic compound from an inert gas stream carrier. Such process comprises expansively cooling a gas in a turbine expander to effect a condensing separation and a recovery of the condensable organic compound from the relatively noncondensable inert gas component. The motive force required to pass the stream through the expander is advantageously supplied by a vacuum pump positioned after the corrosive condensables have been removed from the inert gas carrier stream. The inert gas component optionally may be passed from the vacuum pump into a compressor in order to effect its compressive heating prior to its passage into contact with the condensable organic compound to thereby effect its ladening therewith and a repetition of the cycle. Advantageously, the compressor or, alternatively, the vacuum pump, may be powered in part by the energy liberated from the expansive cooling of the organic compound-laden inert gas stream.
A cyclic process for recovering a condensable organic compound from an inert gas stream laden therewith, which comprises the steps of: (a) passing said inert gas laden stream in heat exchange relationship with a regenerated gas stream from a later step of the process; (b) separating solvent from the heat exchanged gas laden stream of step (a); (c) passing the separated gas stream from step (b) through an expander to further cool said separated gas stream; (d) separating additional solvent from the expanded stream of step (c) and forming a regenerated gas stream; (e) passing said regenerated gas stream to step (a) of the process; (f) passing the heat exchanged regenerated gas stream from step (a) of the process through a vacuum pump; (g) passing the regenerated gas stream of step (f) into contact with a condensable organic compound for forming said inert gas laden stream passed into step (a) of the process.
Claim 2
Dependent Claim
153 words
A cyclic process for recovering a condensable organic compound from an inert gas stream laden therewith, which comprises the steps of: (a) passing said inert gas laden stream in heat exchange relationship with a regenerated gas stream from a later step of the process; (b) separating solvent from the heat exchanged gas laden stream of step (a); (c) passing the separated gas stream from step (b) through an expander to further cool said separated gas stream; (d) separating additional solvent from the expanded stream of step (c) and forming a regenerated gas stream; (e) passing said regenerated gas stream to step (a) of the process; (f) passing the heat exchanged regenerated gas stream from step (a) of the process through a vacuum pump; (g) passing the regenerated gas stream of step (f) into contact with a condensable organic compound for forming said inert gas laden stream passed into step (a) of the process.
Claim 3
Dependent Claim
24 words
The method of claim 1 wherein said gas stream of step (f) is passed through a compressor for its heating prior to step (g).
Claim 4
Dependent Claim
41 words
The method of claim 2 wherein step (g) comprises passing said gas stream of step (f) into contact with a solid adsorbent containing adsorbed condensable organic compound for forming said inert gas laden stream passed into step (a) of the process.
Claim 5
Dependent Claim
11 words
The method of claim 2 wherein said inert gas comprises nitrogen.
Claim 6
Dependent Claim
41 words
The method of claim 1 wherein step (g) comprises passing said gas stream of step (f) into contact with a solid adsorbent containing adsorbed condensable organic compound for forming said inert gas laden stream passed into step (a) of the process.
Claim 7
Dependent Claim
11 words
The method of claim 1 wherein said inert gas comprises nitrogen.