Process and equipment for the production of ammonia make-up syngas with an air separation unit as nitrogen source
View Patent ↗A process and a plant for producing a makeup synthesis gas ( 6 ) for the synthesis of ammonia where a hydrocarbon feedstock is reformed in a primary reformer ( 10 ) and in an autothermal reformer ( 14 ) in parallel with said primary reformer; nitrogen is furnished by an air separation unit ( 13 ), and O 2 -enhched air ( 8 ) produced in said air separation unit is fed to the autothermal reformer. A method for the revamping of the front-end of an ammonia plant is also disclosed.
1. A process for producing a makeup synthesis gas for the synthesis of ammonia, comprising the steps of:
reforming a hydrocarbon feedstock in a primary reformer with no secondary reformer obtaining a syngas stream, and treating said syngas stream obtaining a purified syngas containing hydrogen;
separating an air feed into a nitrogen stream and an oxygen-enriched air stream;
adding said nitrogen stream to the purified syngas, obtaining a makeup syngas containing hydrogen and nitrogen in a suitable molar ratio for synthesis of ammonia;
wherein:
said oxygen-enriched air stream is fed to at least one additional reformer;
a portion of the total hydrocarbon input is reformed in said additional reformer in parallel with the primary reformer, obtaining an additional syngas flow, said additional syngas flow is joined with the syngas output of said primary reformer.
2. The process according to claim 1 , wherein said additional reformer is an autothermal reformer ATR.
3. The process according to claim 1 , wherein the syngas obtained from the additional reformer is cooled before it is joined with the syngas output of the primary reformer.
4. The process according to claim 1 , wherein the enriched air stream is delivered by an air separation unit and compressed before it is fed to said additional reformer.
5. The process according to claim 1 , wherein the hydrocarbon feed of the additional reformer is mixed with process steam and/or pre-heated in one or more heat recovery heat exchanger(s) before entering said additional reformer.
6. The process according to claim 1 , wherein treatment of the reformed syngas is carried out in a shift converter and then in a PSA section, respectively to convert CO into CO 2 and to remove the CO 2 , N 2 and residual hydrocarbons.