Process for separating gas in a PSA unit with two compressors
View Patent ↗In a PSA separation method with compression (C 1 , C 2 ) of at least one offgas ( 3 ), in case of temporary shutdown of one of the compressors (C 1 , C 2 ), the operating parameters of the PSA unit (S) are changed to increase the outlet pressure of the offgas ( 3 ), in order to maintain a production level above 50% with a single compressor (C 1 ).
1. A method for separating by adsorption, in a PSA unit with one or more adsorbers, operating in pressure cycles with given operating parameters, at least one feed gas mixture at a first pressure P 1 with production of at least a first gas mixture stream at a second pressure P 2 lower than P 1 , and at least one second gas mixture stream at a third pressure P 3 lower than P 2 , comprising the step of compressing the second stream in at least two compressors in parallel to a fourth pressure P 4 higher than P 3 , wherein the step of compressing is carried out in a modified mode at a temporary shutdown of one of the compressors of the second stream, and at least one of the said operating parameters of the PSA unit is changed to increase the pressure of the second stream at the outlet of the PSA unit to a fifth pressure P 5 higher than P 3 during the modified mode.
2. The method of claim 1 , wherein, in the modified operating mode, the flow of feed gas mixture is reduced by less than about 50%.
3. The method of claim 1 , wherein, in the modified operating mode, the flow of the first stream is reduced by less than about 25%.
4. The method of claim 1 , wherein the modified operating mode is preprogrammed in the monitoring and control system of the PSA unit.
5. The method of claim 1 , wherein the feed gas mixture contains at least three components selected from H 2 , CO, N 2 , CO 2 and CH 4 , the second stream being a hydrogen-lean mixture.
6. The method of claim 1 , wherein the feed gas mixture is rich in hydrogen, the first stream is production hydrogen, and the second stream is a combustible offgas injectable into a fuel gas network.
7. The method of claim 1 , wherein the feed gas mixture contains CO 2 , the second stream being rich in CO 2 .
8. The method of claim 1 , wherein the feed gas mixture is air, the first stream is rich in oxygen and the second stream is an oxygen-lean mixture.
9. The method of claim 1 , wherein the operating parameters of the PSA unit are selected from: a) the flow rate of the feed gas mixture, b) a number of pressure balancing stops carried out during each pressure cycle, c) the pressure levels of each pressure balancing, d) the pressure levels of the step or steps supplying an elution gas, and e) the duration of each pressure cycle and/or the duration of the steps making up the pressure cycle.
10. The method of claim 1 , wherein:
a) the flow rate of the feed gas mixture is between about 500 and about 200×10 3 Sm 3 /h, b) a number of pressure balancing stops which is lower than or equal to 5, c) the duration of a pressure cycle is between about 1 and about 30 minutes, and d) the PSA unit comprises about 2 to about 20 adsorbers.