Removal of heavy hydrocarbons from gas mixtures containing heavy hydrocarbons and methane
First Claim
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1. A process for the removing heavy hydrocarbon components from a gas mixture containing both a heavy hydrocarbon components and methane, which process comprises:
- a) conducting said gas mixture to a swing adsorption gas separation unit wherein the gas separation unit contains at least one adsorbent contactor comprising a gas inlet and a gas outlet, wherein the gas inlet and the gas outlet are in fluid connection by a plurality of open flow channels, wherein the surfaces of the open flow channels are comprised of an adsorbent material that has a selectivity for said heavy hydrocarbon components over said methane greater than 5, wherein the contactor has less than about 20% of its open pore volume in pores with diameters greater than about 20 angstroms and less than about 1 micron, and wherein at least a portion of said heavy hydrocarbon components is adsorbed into said adsorbent material, thereby resulting in a product stream depleted of said heavy hydrocarbon components;
b) collecting said the product stream;
c) desorbing the adsorbed gases from said adsorbent, thereby resulting in a waste gas stream rich in said heavy hydrocarbon components; and
d) collecting said waste gas stream,wherein said heavy hydrocarbon components are defined as the total of the hydrocarbon compounds in the gas mixture which contain at least 2 carbon atoms, and the product stream has a wt % of methane greater than the wt % of methane of said gas mixture.
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Abstract
A process for the separation of one or more heavy hydrocarbon gases from a gas mixture containing heavy hydrocarbon gas components and methane. The process is conducted in swing adsorption apparatus containing adsorbent contactor having a plurality of flow channels and wherein 20 volume percent or less of the open pore volume of the contactors, is in the mesopore and macropore range.
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Citations
42 Claims
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1. A process for the removing heavy hydrocarbon components from a gas mixture containing both a heavy hydrocarbon components and methane, which process comprises:
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a) conducting said gas mixture to a swing adsorption gas separation unit wherein the gas separation unit contains at least one adsorbent contactor comprising a gas inlet and a gas outlet, wherein the gas inlet and the gas outlet are in fluid connection by a plurality of open flow channels, wherein the surfaces of the open flow channels are comprised of an adsorbent material that has a selectivity for said heavy hydrocarbon components over said methane greater than 5, wherein the contactor has less than about 20% of its open pore volume in pores with diameters greater than about 20 angstroms and less than about 1 micron, and wherein at least a portion of said heavy hydrocarbon components is adsorbed into said adsorbent material, thereby resulting in a product stream depleted of said heavy hydrocarbon components; b) collecting said the product stream; c) desorbing the adsorbed gases from said adsorbent, thereby resulting in a waste gas stream rich in said heavy hydrocarbon components; and d) collecting said waste gas stream, wherein said heavy hydrocarbon components are defined as the total of the hydrocarbon compounds in the gas mixture which contain at least 2 carbon atoms, and the product stream has a wt % of methane greater than the wt % of methane of said gas mixture. - View Dependent Claims (2, 3, 4, 5, 6, 7, 8, 9, 10, 11, 12, 13, 14, 15, 16, 17, 18, 19, 20, 21, 22, 23, 24, 25, 26, 27, 28, 29, 30, 31, 32, 33, 34, 35, 36, 37, 38, 39, 40, 41, 42)
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Specification