Catalytic gas synthesis apparatus
AssigneeExxon Research & Engineering Co.
InventorsRobert M. Osman, Larry J. Shulik
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AssigneeExxon Research & Engineering Co.
InventorsRobert M. Osman, Larry J. Shulik
Estimating the term…
The present invention is generally directed to an improved process and apparatus for the production of gaseous products such as ammonia by catalytic, exothermic gaseous reactions and is specifically directed to an improved process which utilizes a gas-phase catalytic reaction of nitrogen and hydrogen for the synthesis of ammonia. This improved process for the production of ammonia utilizes an ammonia converter apparatus designed to comprise at least two catalyst stages and a reheat exchanger so arranged as to provide indirect heat exchange of the gaseous effluent from the last reactor catalyst stage with the effluent from at least one other reactor catalyst stage having a higher temperature level in order to reheat the effluent from the last reactor catalyst stage prior to exiting the reactor vessel, thereby facilitating higher level heat recovery from the reactor effluent.
In an exothermic catalytic reactor having at least two catalytic beds arranged for sequential gas flow therethrough;
In an exothermic catalytic reactor having at least two catalytic reactor beds arranged for sequential flow of a gas therethrough and for partial reaction of said gas in each said catalytic reactor bed;
In an exothermic catalytic reactor having at least two catalytic reactor beds arranged for sequential flow of a gas therethrough and for partial reaction of said gas therein;
In an exothermic catalytic reactor having at least two catalytic reactor beds arranged for sequential flow of a gas therethrough and for partial reaction of said gas therein;
Dependencies are inferred from the claim text.