High-temperature fuel cell system
US-2017338506-A1 · Nov 23, 2017 · US
US2020384431A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2020384431-A1 |
| Application number | US-201816764655-A |
| Country | US |
| Kind code | A1 |
| Filing date | Dec 19, 2018 |
| Priority date | Dec 20, 2017 |
| Publication date | Dec 10, 2020 |
| Grant date | — |
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In an adiabatic axial flow converter, in which process gas passes from an outer annulus via a catalyst bed, wherein the process gas is converted to a product, to an inner centre tube, the catalyst bed comprises at least one module comprising one or more catalyst layers. Feed means are arranged to provide a flow of process gas from the outer annulus to an inlet part of one or more modules, and collector means are arranged to provide a flow of product stream of converted process gas which passes axially through the catalyst bed of one or more of the modules to the centre tube.
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1 . Adiabatic axial flow converter, in which process gas passes from an outer annulus via a catalyst bed wherein the process gas is converted to a product, to an inner centre tube, wherein the catalyst bed comprises at least one module comprising one or more catalyst layers having a height hcat, feed means are arranged to provide a flow of process gas from the outer annulus to an inlet part of one or more modules, and collector means are arranged to provide a flow of product stream of converted process gas which has passes axially through the catalyst bed of one or more of the modules to the centre tube. 2 . Adiabatic axial flow converter according to claim 1 , comprising two or more modules. 3 . Adiabatic axial flow converter according to claim 1 , wherein the converter is arranged for two or more modules to be operated in parallel and/or in series. 4 . Adiabatic axial flow converter according to claim 1 , wherein the pressure drop Dp is the same within +−5% across modules operated in parallel. 5 . Adiabatic axial flow converter according to claim 1 , wherein the one or more catalyst layers in modules operated in parallel comprises the same catalysts. 6 . Adiabatic axial flow converter according to claim 1 , wherein the height of the one or more catalyst layers in modules operated in parallel is the same. 7 . Adiabatic axial flow converter according to claim 1 , wherein the collector means is part of at least one module. 8 . Adiabatic axial flow converter according to claim 1 , wherein the reactor is arranged with two or more module sections, each module section comprising one or more modules. 9 . Adiabatic axial flow converter according to claim 1 , comprising a quenching zone wherein the product gas from a section is quenched, obtaining a quench product stream, and, wherein the converter comprises means to provide at least part of the quenched process stream as feed for one or more subsequent sections. 10 . Adiabatic axial flow converter according to claim 9 , wherein fresh process gas or partly converted, optionally cooled process gas is used as quench gas. 11 . Adiabatic axial flow converter according to claim 9 , wherein the modules in different sections may be different from each other, contain different catalyst and be differently arranged. 12 . Adiabatic axial flow converter according to claim 9 , wherein at least two or more sections are arranged to operate in parallel. 13 . Adiabatic axial flow converter according to claim 9 , wherein two or more sections are arranged to operate in series. 14 . Adiabatic axial flow converter according to claim 1 , which is used as ammonia reactor, methanol reactor, methanization reactor, shift reactor and other exothermic reaction processes.
Heating or cooling the reactor (for tubular reactors in furnaces B01J8/062) · CPC title
comprising a plurality of beds with flow of reactants in parallel · CPC title
in tube reactors; the solid particles being arranged in tubes · CPC title
Tubes · CPC title
in a cylindrical annular shaped bed · CPC title
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