Olefin and methanol co-production plant and olefin and methanol co-production method
US-2020347000-A1 · Nov 5, 2020 · US
US12565544B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12565544-B2 |
| Application number | US-202117927517-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 16, 2021 |
| Priority date | Sep 25, 2020 |
| Publication date | Mar 3, 2026 |
| Grant date | Mar 3, 2026 |
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A partial oxidative coupling catalyst has a structure in which a component represented by M 2 ZrO 3 is supported on a support, where M represents an alkali metal.
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The invention claimed is: 1 . An olefin production device for producing an olefin from a raw material gas containing methane, comprising: at least one reactor containing a partial oxidative coupling catalyst, and a plurality of the reactors connected in series, wherein the partial oxidative coupling catalyst comprises a support and a component represented by M 2 ZrO 3 supported on the support, where M represents an alkali metal. 2 . The olefin production device according to claim 1 , further comprising a cooler disposed between adjacent reactors. 3 . An olefin production method for producing an olefin from a raw material gas containing methane, comprising: a first reaction step of performing partial oxidative coupling of methane in the raw material gas by using a partial oxidative coupling catalyst, wherein the partial oxidative coupling catalyst comprises a support and a component represented by M 2 ZrO 3 supported on the support, where M represents an alkali metal. 4 . The olefin production method according to claim 3 , comprising a second reaction step of performing partial oxidative coupling of methane in an effluent gas of the first reaction step by using the partial oxidative coupling catalyst. 5 . The olefin production method according to claim 4 , further comprising a step of cooling the effluent gas between the first reaction step and the second reaction step. 6 . The olefin production method according to claim 4 , wherein each of a flow velocity of a reactant gas obtained by mixing the raw material gas and oxygen in the first reaction step and a flow velocity of a reactant gas obtained by mixing the effluent gas and oxygen in the second reaction step is 10 to 100 cm/sec.
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