Process for producing ammonia synthesis gas
View Patent ↗A process for producing ammonia synthesis gas from a hydrocarbon-containing feedstock, with steps of primary reforming, secondary reforming with an oxidant stream, and further treatment of the synthesis gas including shift, removal of carbon dioxide and methanation, wherein the synthesis gas delivered by secondary reforming is subject to a medium-temperature shift (MTS) at a temperature between 200 and 350° C., and primary reforming is operated with a steam-to-carbon ratio lower than 2. A corresponding method for revamping an ammonia plant is disclosed, where an existing HTS reactor is modified to operate at medium temperature, or replaced with a new MTS reactor, and the steam-to-carbon ratio in the primary reformer is lowered to a value in the range 1-5−2, thus reducing inert steam in the flow rate trough the equipments of the front-end.
1. A process for producing ammonia from an ammonia synthesis gas obtained from a hydrocarbon-containing feedstock, the process comprising the steps of:
pre-reforming said feedstock;
primary reforming all of said feedstock with steam to partially reform said feedstock, wherein said primary reforming is operated with a steam-to-carbon ratio lower than 2;
secondary reforming a partially reformed gas stream delivered from said primary reforming step with an oxidant stream, wherein the ammonia synthesis gas produced by said secondary reforming is directly subject to a medium-temperature shift in a medium-temperature shift reactor over a copper-based catalyst at a temperature between 200 and 350° C. to convert CO into CO 2 , obtaining a first shifted gas;
purification of the first shifted gas involving at least a further shift conversion of CO to CO 2 , obtaining a second CO 2 containing shifted gas and subsequent removal of carbon dioxide from the second shifted gas, obtaining a purified ammonia synthesis gas, and
reacting the purified ammonia synthesis gas to form ammonia,
wherein the ammonia synthesis gas comprises hydrogen (H 2 ) and nitrogen (N 2 ) in a suitable ratio of about 3:1, and
wherein the overall feedstock required for producing the ammonia synthesis gas according to the process is fed to the pre-reforming step, and said pre-reforming step of said feedstock is carried out before the step of primary reforming.
2. The process according to claim 1 , wherein said steam-to-carbon ratio is 1.5 to 2.
3. The process according to claim 1 , wherein said oxidant stream is any of air, O 2 -enriched air or substantially pure oxygen.
4. The process according to claim 1 , wherein said medium-temperature shift is carried out in a substantially isothermal condition, by removing heat with a cooling medium.
5. The process according to claim 1 , further comprising the step of removing unreacted methane from the synthesis gas by cryogenic separation of methane from the synthesis gas, or by means of a treatment step of adsorption.
6. The process according to claim 1 , wherein said steam-to-carbon ratio is 1.5 to 1.7.
7. The process according to claim 1 , wherein the unreacted methane is removed from the synthesis gas by pressure swing adsorption.