Temperature controlled adsorption process for recovering condensable components from a gas stream
AssigneeDow Global Technologies LLC
InventorsRoss E. Dugas, Ajay N. Badhwar
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Abstract
Disclosed is an improved process for recovering condensable components from a gas stream, in particular, hydrocarbons from a gas stream such as natural gas. The present process uses solid adsorbent media to remove said hydrocarbons wherein the adsorbent media is regenerated in a continuous fashion in a heated continuous counter-current regeneration system, wherein said heated regenerated adsorbent media is cooled prior to reuse.
Claims6
A continuous process for separating hydrocarbons from a gas feedstream comprising methane and one or more of ethane, propane, butane, pentane, or heavier hydrocarbons, consisting of the steps of:
- (a) providing one or more adsorbent bed consisting of an adsorbent media selected from a porous cross-linked polymeric adsorbent, a pyrolized macroporous polymer, or mixtures thereof, wherein said adsorbent media adsorbs one or more of ethane, propane, butane, pentane, heavier hydrocarbons, and/or mixtures thereof,
- (b) passing the gas feedstream through the one or more adsorbent bed to provide a methane rich gas stream and a loaded adsorbent media,
- (c) recovering, transporting, liquefying, combusting, or flaring the methane rich gas stream,
- (d) using a heat to regenerate the loaded adsorbent media to produce a heated regenerated adsorbent media and a product gas comprising one or more desorbed ethane, propane, butane, pentane, heavier hydrocarbons, and/or mixtures thereof,
- (e) recovering, transporting, liquefying, re-injecting, excluding, by-passing, combusting, or flaring the one or more desorbed ethane, propane, butane, pentane, and/or heavier hydrocarbons individually and/or as mixtures,
- (f) cooling the heated regenerated adsorbent media in a cooling unit to form a cooled regenerated adsorbent media wherein the temperature for the cooled regenerated adsorbent media is equal to or greater than 10° F. cooler than the temperature of the heated regenerated adsorbent media prior to entering the cooling unit,
- and
- (g) introducing the cooled regenerated adsorbent media back into the adsorption bed for reuse.
Dependencies are inferred from the claim text.