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Recovery of nitrogen, hydrogen and carbon dioxide from hydrocarbon reformate

Patent ·
OSTI ID:6078490

This patent describes a method of separately recovering high purity carbon dioxide and ammonia synthesis gas composed of hydrogen and nitrogen at near the 3:1 stoichiometric ratio, from a starting gas mixture containing hydrogen, carbon dioxide and nitrogen as bulk components and less than a total of 10 mol % on a dry basis of minor components which comprises: (a) passing the starting gas at super atmospheric pressure into and through a first bed of solid adsorbent wherein carbon dioxide is selectively adsorbed; discharging unadsorbed gas from the first bed into and through a second bed of adsorbent effective in retaining at least part of the minor components of the starting gas; and discharging from the second bed as primary effluent the unadsorbed portion of the gas passed therethrough; (b) rinsing the first bed with a stream of high purity carbon dioxide passed into the bed for a time short of complete breakthrough of a carbon dioxide front at the effluent end while discharging effluent gas therefrom and mixing the effluent gas with fresh starting feed gas; (c) desorbing carbon dioxide from the first bed by gas with drawal to near ambient pressure level; (d) lowering the pressure in the first bed by evacuation to subatmospheric level thereby obtaining an effluent rich in carbon dioxide; (e) partly repressurizing the evacuated first bed by flow of gas into the bed from a second bed which is at superatmospheric pressure levels, to bring the first and second beds to substantially equal pressure; and (f) further repressuring the first bed to superatmospheric pressure level to prepare the same for further adsorption of CO/sub 2/ from the starting gas.

Assignee:
Air Products and Chemicals, Inc., Allentown, PA
Patent Number(s):
US 4813980
OSTI ID:
6078490
Country of Publication:
United States
Language:
English