Combination reactor system

US9675950B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-9675950-B2
Application numberUS-201514604790-A
CountryUS
Kind codeB2
Filing dateJan 26, 2015
Priority dateSep 26, 2011
Publication dateJun 13, 2017
Grant dateJun 13, 2017

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  1. Title

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  2. Abstract

    A short plain-language summary of the technical disclosure.

  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

    The legal scope of protection — read this for what is actually claimed.

  6. CPC / IPC classifications

    Technology tags used to group this patent with similar filings.

  7. Citations and related patents

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Abstract

Official abstract text for this publication.

The present invention is directed to a combination reactor system for exothermic reactions comprising a trickle-bed reactor and a shell-and-tube reactor. This combination allows the system to efficiently remove heat while also providing the ability to control both the temperature and/or reaction progression. The trickle-bed reactor removes heat efficiently from the system by utilizing latent heat and does not require the use of a cooling or heating medium. The shell-and-tube reactor is used to further progress the reaction and provides a heat exchanger in order to introduce fluid at the desired temperature in the shell-and-tube reactor. Also, additional reactant or reactants and/or other fluids may be introduced to the shell-and-tube section of the reactor under controlled temperature conditions.

First claim

Opening claim text (preview).

What is claimed is: 1. A reactor system for use with an exothermic reaction comprising the hydrogenation of a fluoro-olefin compound, said system comprising in combination, (a) as a first reactor in the system, a trickle-bed reactor which does not include either a heating or cooling medium, and (b) as a second reactor in the system, a shell-and-tube reactor which comprises a temperature control system selected from the group consisting of a heating medium, a cooling medium, and both a heating and a cooling medium, wherein the reactors are separated by a heat exchanger; wherein the trickle bed reactor comprises a fixed bed of reactor catalyst and two phases in the reactor; wherein the shell-and-tube reactor comprises a multi-stage, multi-tube, shell-and-tube heat exchanger which contains reactor catalyst in all tubes; and wherein the reactor system provides for the removal of heat and provides the ability to control reaction temperature and/or reaction progression. 2. The combination reactor system of claim 1 , wherein the heat exchanger is used for removing or adding heat or causing a phase change of a reaction medium. 3. The combination reactor system of claim 1 , wherein the trickle-bed reactor removes heat from the system by utilizing latent heat. 4. The reactor system of claim 1 , wherein the hydrogenation reaction is the conversion of hexafluoropropylene to 1,1,1,2,3,3-hexafluoropropane. 5. The reactor system of claim 1 , wherein the hydrogenation reaction is the conversion of 1,2,3,3,3-pentafluoropropene to 1,1,1,2,3-pentafluoropropane. 6. A combination reactor system for use with an exothermic reaction comprising the hydrogenation of a fluoro-olefin compound, said system comprising in combination, (a) a trickle-bed reactor as the first reactor in the system; and (b) a shell-and-tube reactor as the second reactor in the system; wherein the trickle-bed reactor removes heat from the system by utilizing latent heat and does not require the use of a cooling or heating medium; wherein the shell-and-tube reactor comprises a shell structure and a tubesheet located in the shell structure; wherein the tubesheet comprises one or more reaction zones and one or more temperature control zones, wherein each reaction zone comprises a plurality of aligned reaction tubes; and each temperature control zone comprises a plurality of aligned temperature control tubes; wherein the reactor system further comprises a heat exchanger in order to introduce materials to the reactors at predetermined temperatures, thereby controlling the reaction conditions in the combination reactor system; and wherein each reaction zone of the shell-and-tube reactor is adjacent to a temperature control zone. 7. The reactor system of claim 6 , wherein the hydrogenation reaction is the conversion of hexafluoropropylene to 1,1,1,2,3,3-hexafluoropropane. 8. The reactor system of claim 6 , wherein the hydrogenation reaction is the conversion of 1,2,3,3,3-pentafluoropropene to 1,1,1,2,3-pentafluoropropane.

Assignees

Inventors

Classifications

  • Provided with baffles · CPC title

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

  • containing fluorine · CPC title

  • Nozzle-type feeding elements · CPC title

  • the beds being superimposed one above the other · CPC title

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Frequently asked questions

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What does patent US9675950B2 cover?
The present invention is directed to a combination reactor system for exothermic reactions comprising a trickle-bed reactor and a shell-and-tube reactor. This combination allows the system to efficiently remove heat while also providing the ability to control both the temperature and/or reaction progression. The trickle-bed reactor removes heat efficiently from the system by utilizing latent he…
Who is the assignee on this patent?
Honeywell Int Inc
What technology area does this patent fall under?
Primary CPC classification B01J8/067. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Jun 13 2017 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). 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).