System and method for heating gas in a continuous focused path within an electric heating unit
US-12109546-B1 · Oct 8, 2024 · US
US9675950B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9675950-B2 |
| Application number | US-201514604790-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jan 26, 2015 |
| Priority date | Sep 26, 2011 |
| Publication date | Jun 13, 2017 |
| Grant date | Jun 13, 2017 |
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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.
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.
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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