Process for preparing a H2-rich gas and a CO2-rich gas at high pressure
View Patent ↗The present invention comprises a method for production of a CO 2 -rich gas stream and a H 2 -rich gas stream, the method comprising the following steps: a) natural gas and water are fed to a reforming reactor and are converted to synthesis gas under supply of a O 2 -containing gas: b) the gas stream from a) is shifted, whereby the content of CO is reduced and the amounts of CO 2 and H 2 are increased by reaction of H 2 O; c) the gas stream from b) is separated in a separation unit into a CO 2 -rich and a H 2 -rich gas stream, respectively. The invention also concerns the use of a CO 2 -rich gas stream for injection into marine formations, and the use of a H 2 -rich gas stream for hydrogenation, as a source of energy/fuel in fuel cells or for production of electricity.
1. Method for production of a CO 2 -rich gas stream and a H 2 -rich gas stream, characterized in that the method comprises the following steps:
a) natural gas and water are fed to a reforming reactor and converted to synthesis gas under supply of an O 2 -rich gas to the reactor;
b) the gas stream from a) is shifted, in one step, whereby the content of CO is reduced and the amounts of CO 2 and H 2 are increased by reaction of H 2 O at a ratio H 2 O:CO of from 1 to 9;
c) the gas stream from b) is separated in a separation unit into a CO 2 -rich and a H 2 -rich gas stream, respectively, wherein the pressure in the CO 2 -rich gas stream after the separation is from 5 to 100 bar.
2. Method according to claim 1 , characterized in that the ratio H 2 O:CO in the shift process is from 1.5 to 4.
3. Method according to claim 1 , characterized in that the pressure in the CO 2 -rich gas stream after the separation unit is from 5 to 50 bar.
4. Method according to claim 1 , characterized in that the carbon part in the H 2 -rich gas stream is from 1 to 20% by volume.
5. Method according to claim 1 , characterized in that the carbon part in the H 2 -rich gas stream is from 5 to 15% by volume.
6. Method according to claim 1 , characterized in that the natural gas in step a) is supplied with air/oxygen enriched air.
7. Method according to claim 1 , characterized in that the reformer reactor is a partial oxidation reactor.
8. Method according to claim 1 , characterized in that the reformer reactor is an autothermal reformer.
9. Method according to claim 8 , characterized in that the gas stream from a combustion chamber in an autothermal reformer is contacted with a catalyst bed.
10. Method according to claim 7 , characterized in that the reforming is carried out without a catalyst.
11. Method according to claim 1 , characterized in that the gas stream out of the reformer has a temperature within the interval from 800 to 1200° C.
12. Method according to claim 6 , characterized in that the CO 2 -rich gas stream includes at least part of N 2 .
13. Method according to claim 1 wherein the produced CO 2 -rich gas stream is applied for injection into marine formations.
14. Method according to claim 1 wherein the produced H 2 -rich gas stream is applied for hydrogenation.
15. Method according to claim 1 wherein the produced H 2 -rich gas stream is applied as a source of energy/fuel in fuel cells.
16. Method according to claim 1 wherein the produced H 2 -rich gas stream is applied for the production of electricity.