Treatment of gas streams
AssigneeBOC Limited
InventorsDavid J. Graham, John W. Armond
Life of this patent
Estimating the term…
Abstract
A portion of a component of a gas stream is condensed with the remaining non-condensed gas stream being passed to an adsorber. The remainder of the component in the non-condensed stream is adsorbed in the adsorber and in a later stage of the adsorber cycle, the adsorbed component is desorbed and supplied to the inlet of a condenser together with the gas stream to promote condensation of the component by providing an increased concentration of the component in the gas stream.
Claims3
A method of treating a gas mixture comprised of a carrier gas and a minor fraction of vinyl chloride monomer comprising the steps of:
- (a) passing said gas mixture in heat exchange relation with a refrigerant in a condensation device to condense at least a part of the vinyl chloride monomer;
- (b) recovering condensed vinyl chloride monomer from the condensation device;
- (c) supplying the non-condensed portion of said gas mixture from the condensation device to an adsorption unit;
- (d) preferentially adsorbing vinyl chloride monomer from the non-condensed gas mixture in the adsorption unit;
- (e) desorbing the adsorbed vinyl chloride monomer from the adsorption unit;
- (f) passing said desorbed, vinyl chloride monomer to said condensation device thereby increasing the concentration of said vinyl chloride monomer in said condensation device and reducing the refrigeration required to condense a given amount of said vinyl chloride monomer;
- and
- (g) continuously adding nitrogen gas to the gas mixture upstream of the addition of desorbed vinyl chloride monomer to the gas mixture.
A method of treating a gas mixture comprised of a carrier gas and a minor fraction of a condensible vapour comprising the steps of:
- (a) passing said gas mixture in heat exchange relation with a refrigerant in a condensation device to condense at least part of said condensible vapour;
- (b) recovering condensed vapour from said condensation device;
- (c) supplying the non-condensed portion of said condensible vapour and said carrier gas from said condensation device to the first adsorption bed of an adsorption unit having at least four adsorption beds to preferentially adsorb said condensible vapour in said first bed while discharging said carrier gas therefrom;
- (d) passing a portion of said discharged carrier gas to a second adsorption bed to desorb the condensible vapour previously adsorbed therein and passing said desorbed, condensible vapour to said condensation device to increase the concentration of said condensible vapour therein and reduce the refrigeration required to condense a given amount of said condensible vapour;
- (e) passing a further portion of said discharged carrier gas in heat exchange relation with a third adsorption bed to cool the same prior to supplying the non-condensed portion of the condensible vapor from the condensation device to said third bed;
- and
- (f) passing said gas mixture in heat exchange relation with a fourth adsorption bed containing adsorbed condensible vapour to heat said fourth adsorption bed before said condensible vapour is desorbed therefrom at a greater temperature than the temperature at which said condensible vapour is adsorbed.
Dependencies are inferred from the claim text.