Hydrogenation reactor and process

US2016214913A1 · US · A1

Patent metadata
FieldValue
Publication numberUS-2016214913-A1
Application numberUS-201414916377-A
CountryUS
Kind codeA1
Filing dateAug 29, 2014
Priority dateSep 6, 2013
Publication dateJul 28, 2016
Grant date

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

A reactor and process for removing unsaturated alkynes and diolefinic impurities from olefins and oxygenates is described.

First claim

Opening claim text (preview).

1 . A reactor suitable for use in a hydrogenation process, the reactor comprising: a. a catalyst bed comprising a tube for cooling the catalyst bed; b. a plurality of inlets for conveying a feed material to the catalyst bed; and c. one or more outlets, wherein the catalyst bed comprises a catalyst having a surface area of from about 15 m 2 /g to about 650 m 2 /g, and wherein the reactor can provide a space velocity of from about 500/h to about 50,000/h for hydrogenation reactions. 2 . The reactor of claim 1 , further comprising one or more distributors for distributing the feed material uniformly or substantially uniformly across the catalyst bed. 3 . The reactor of claim 1 , wherein the catalyst bed is a fixed bed comprising a selective hydrogenation catalyst. 4 . The reactor of claim 1 , wherein the catalyst bed is positioned in contact with one or more catalyst bed supports. 5 . The reactor of claim 1 , being a hydrogenation reactor comprising a plurality of inlets for an olefin feed, an oxygenate feed, or a combination thereof. 6 . The reactor of claim 1 , further comprising a drip trap for recovering a condensate and/or a green oil. 7 . The reactor of claim 1 , further comprising one or more thermowells disposed between an exterior surface of the reactor and the catalyst bed. 8 . (canceled) 9 . (canceled) 10 . (canceled) 11 . The reactor of claim 1 , wherein the catalyst has a surface area of from about 30 m 2 /g to about 650 m 2 /g. 12 . The reactor of claim 1 , having a space velocity of at least about 25,000/h. 13 . The reactor of claim 1 , having a high space velocity, a low pressure drop, a uniform distribution of feed material across the catalyst bed, or a combination thereof, as compared to a conventional hydrogenation and/or dehydrogenation reactor. 14 . A reactor system comprising a plurality of the reactors of claim 1 , arranged in a series configuration. 15 . A reactor system comprising a plurality of the reactors of claim 1 , arranged in a parallel configuration. 16 . (canceled) 17 . (canceled) 18 . (canceled) 19 . A method for a hydrogenation process, the method comprising introducing a feed material to the reactor of claim 1 through the plurality of inlets, such that the feed material uniformly or substantially uniformly contacts the catalyst bed to produce a hydrogenation reaction product. 20 . The method of claim 19 , wherein the feed material comprises acetylene, and wherein the reaction product comprises an alkene. 21 . (canceled) 22 . (canceled) 23 . (canceled) 24 . The method of claim 19 , wherein the reactor exhibits a pressure drop of from about 0.05 to about 100 bar. 25 . (canceled) 26 . The method of claim 19 , wherein the reactor provides improved control over runaway reactions, as compared to a conventional reactor. 27 . (canceled) 28 . The method of claim 19 , wherein a plurality of reactors are connected in a series configuration to provide a front-end acetylene removal system. 29 . (canceled) 30 . The method of claim 19 , wherein a plurality of reactors are connected in a parallel configuration to provide a back-end acetylene removal system.

Assignees

Inventors

Classifications

  • B01J8/008Primary

    Details of the reactor or of the particulate material; Processes to increase or to retard the rate of reaction (B01J8/0285, B01J8/067, B01J8/087, B01J8/1836 take precedence) · CPC title

  • to carbon-to-carbon double bonds · CPC title

  • B01J8/0278Primary

    Feeding reactive fluids (for solid material B01J8/0015) · CPC title

  • Flow distribution elements · CPC title

  • Feeding reactive fluids (for solid material, see B01J8/0015) · CPC title

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Frequently asked questions

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What does patent US2016214913A1 cover?
A reactor and process for removing unsaturated alkynes and diolefinic impurities from olefins and oxygenates is described.
Who is the assignee on this patent?
Saudi Basic Ind Corp
What technology area does this patent fall under?
Primary CPC classification B01J8/008. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Thu Jul 28 2016 00:00:00 GMT+0000 (Coordinated Universal Time) (A1). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).