Process to control the outlet temperature of a heat exchange reformer in syngas production for chemical and fuel industries
AssigneeTopsoe A/S
InventorsKaushal DHYANI, Claus Fallesen HANSEN, Sanghdeep GAUTAM
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AssigneeTopsoe A/S
InventorsKaushal DHYANI, Claus Fallesen HANSEN, Sanghdeep GAUTAM
Estimating the term…
A process to control the outlet temperature of a heat exchange reformer in the production of synthesis gas wherein a first stream of feed gas is directed to a first reforming section and a second stream of feed gas is directed to said heat exchange reformer, wherein the outlet stream of said reforming section is divided into at least a first and a second sub-streams. The first sub-stream is directed into said heat exchange reformer to provide heat for the reforming section and the outlet stream of the heat exchange reformer is directed to a first waste heat boiler. The second sub-stream bypasses the heat exchange reformer and is directed to a second waste heat boiler for heat recovery and high pressure steam production. The outlet temperature of said heat exchange reformer is adjusted in this manner.
A process to control an outlet temperature of a heat exchange reformer in syngas production for chemicals and fuels, wherein a first stream of feed gas is directed to a reforming section and a second stream of feed gas is directed to said heat exchange reformer, wherein an outlet stream of said reforming section is divided into at least two sub-streams including a first sub-stream and a second sub-stream, wherein:
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