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公开(公告)号:US11767276B2
公开(公告)日:2023-09-26
申请号:US17871575
申请日:2022-07-22
Applicant: EcoCatalytic Inc.
Inventor: Gary A. Sawyer , C. Andrew Jones , John A. Sofranko
CPC classification number: C07C7/14816 , B01J21/02 , B01J27/053 , B01J27/1806 , C01B32/50 , C07C2/82 , C07C5/48 , C01B3/583 , C01B2203/044
Abstract: A method of removing CO from a mixture of CO and saturated and unsaturated hydrocarbons CO to CO2 is provided. In one embodiment, the method is to contact feed stream with an oxygen transfer agent; and then oxidize at least a portion of the CO to CO2 to produce a stream enriched in CO2. The saturated and unsaturated hydrocarbons in the feed are not further oxidized during the oxidation. The oxygen transfer agent includes at least one of: i) water; ii) at least one reducible metal oxide; iii) at least one reducible chalcogen; or mixtures thereof. In another embodiment, the CO is converted to methane. The unsaturated hydrocarbons in the feed are not hydrogenated. In both of these alternatives, the CO2 or methane are then removed. Systems for removing the CO are also provided.
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公开(公告)号:US20230043302A1
公开(公告)日:2023-02-09
申请号:US17871575
申请日:2022-07-22
Applicant: EcoCatalytic Inc.
Inventor: Gary A. Sawyer , C. Andrew Jones , John A. SOFRANKO
Abstract: A method of removing CO from a mixture of CO and saturated and unsaturated hydrocarbons CO to CO2 is provided. In one embodiment, the method is to contact feed stream with an oxygen transfer agent; and then oxidize at least a portion of the CO to CO2 to produce a stream enriched in CO2. The saturated and unsaturated hydrocarbons in the feed are not further oxidized during the oxidation. The oxygen transfer agent includes at least one of: i) water; ii) at least one reducible metal oxide; iii) at least one reducible chalcogen; or mixtures thereof. In another embodiment, the CO is converted to methane. The unsaturated hydrocarbons in the feed are not hydrogenated. In both of these alternatives, the CO2 or methane are then removed. Systems for removing the CO are also provided.
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公开(公告)号:US12187677B2
公开(公告)日:2025-01-07
申请号:US18212999
申请日:2023-06-22
Applicant: EcoCatalytic Inc.
Inventor: Gary A. Sawyer , C. Andrew Jones , John A. Sofranko
IPC: C07C7/148 , B01J21/02 , B01J27/053 , B01J27/18 , C01B3/12 , C01B3/48 , C01B3/58 , C01B32/50 , C07C2/82 , C07C5/48
Abstract: A method of removing CO from a mixture of CO and saturated or unsaturated hydrocarbons is provided. In one embodiment, the method is to contact a feed stream with an oxygen transfer agent; and then oxidize at least a portion of the CO to CO2 to produce a stream enriched in CO2. The saturated and unsaturated hydrocarbons in the feed are not further oxidized during the oxidation. The oxygen transfer agent includes at least one of: i) water; ii) at least one reducible metal oxide; iii) at least one reducible chalcogen; or mixtures thereof. In another embodiment, the CO is converted to methane. The unsaturated hydrocarbons in the feed are not hydrogenated. In both of these alternatives, the CO2 or methane are then removed. Systems for removing the CO are also provided.
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4.
公开(公告)号:US20230331646A1
公开(公告)日:2023-10-19
申请号:US18212999
申请日:2023-06-22
Applicant: EcoCatalytic Inc.
Inventor: Gary A. Sawyer , C. Andrew Jones , John A. SOFRANKO
CPC classification number: C07C7/14816 , C01B32/50 , B01J21/02 , C07C5/48 , B01J27/053 , C07C2/82 , B01J27/1806 , C01B2203/044 , C01B3/583
Abstract: A method of removing CO from a mixture of CO and saturated or unsaturated hydrocarbons is provided. In one embodiment, the method is to contact a feed stream with an oxygen transfer agent; and then oxidize at least a portion of the CO to CO2 to produce a stream enriched in CO2. The saturated and unsaturated hydrocarbons in the feed are not further oxidized during the oxidation. The oxygen transfer agent includes at least one of: i) water; ii) at least one reducible metal oxide; iii) at least one reducible chalcogen; or mixtures thereof. In another embodiment, the CO is converted to methane. The unsaturated hydrocarbons in the feed are not hydrogenated. In both of these alternatives, the CO2 or methane are then removed. Systems for removing the CO are also provided.
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