Process for producing ammonia synthesis gas
View Patent ↗A process for producing ammonia synthesis gas, where a natural gas feedstock ( 10 ) is reformed in a primary steam reformer ( 12 ) and in a secondary reformer ( 14 ) at a pressure of at least 35 bar; the product syngas ( 16 ) at the output of the secondary reformer is cooled and subject to catalytic medium-temperature shift, converting the CO into CO 2 and H 2 ; downstream said medium-temperature shift, the carbon dioxide is removed from the syngas by physical absorption.
1. A process for producing ammonia synthesis gas from a hydrocarbon-containing feedstock, the process comprising the steps of steam-reforming of said hydrocarbon-containing feedstock in a primary reformer, wherein all feedstock is supplied to said primary reformer, obtaining a partially reformed gas stream, and secondary reforming of said partially reformed gas stream in a secondary reformer, operating with air in excess, wherein:
the primary reforming and the secondary reforming are operated at a pressure of at least 35 bar;
the product syngas at the output of the secondary reforming is cooled and subject to catalytic medium-temperature shift, converting CO into CO 2 and H 2 , said medium-temperature shift being carried out on a copper-based catalyst at a substantially constant temperature in the range 220-320° C.;
downstream said medium-temperature shift, CO 2 is removed from the syngas by physical absorption;
wherein the steam-to-carbon ratio in the primary reformer is less than 2.7.
2. The process according to claim 1 , wherein the partially reformed syngas at the outlet of the primary reformer has a temperature in the range 650-750° C.
3. The process according to claim 1 , wherein a further low-temperature shift is carried out on the syngas stream downstream the medium-temperature shift.
4. The process according to claim 1 , wherein CO 2 is removed using methanol as a solvent, or an organic solvent.