PROCESS FOR THE PRODUCTION OF HYDROGEN-ENRICHED SYNTHESIS GAS
The invention relates to a process for the production of hydrogen-enriched synthesis gas by a catalytic water-gas shift reaction, comprising the steps: introducing a gaseous flow ( 1 ) comprising at least one organic sulphide, optionally in its oxide form, in a first reactor ( 2 ) comprising a catalyst X 1 , collecting a sulfur-containing gaseous flow ( 3 ) from the first reactor, introducing the raw synthesis gas ( 4 ) in a second reactor ( 6 ), introducing the sulfur-containing gaseous flow ( 3 ) in the second reactor where the catalytic water-gas shift reaction takes place and comprising a sulfur-resistant shift catalyst X 2 , collecting an outlet flow ( 7 ) comprising hydrogen-enriched synthesis gas from the second reactor. The invention also relates to the use of said at least one organic sulphide, optionally in its oxide form, in a process for the production of hydrogen-enriched synthesis gas by a catalytic water-gas shift reaction.
1 . A process for the production of hydrogen-enriched synthesis gas by a catalytic water-gas shift reaction operated on a raw synthesis gas, the process comprising:
introducing a gaseous flow ( 1 ) comprising at least one compound of formula (I)
wherein:
R is selected from a linear or branched alkyl radical containing from 1 to 4 carbon atoms, and a linear or branched alkenyl radical containing from 2 to 4 carbon atoms,
n is 0, 1 or 2,
x is 0, 1, 2, 3 or 4,
R′ is selected from a linear or branched alkyl radical containing from 1 to 4 carbon atoms, a linear or branched alkenyl radical containing from 2 to 4 carbon atoms and, only when n=x=0, a hydrogen atom,
into a first reactor comprising a catalyst X 1 , the catalyst X 1 comprising at least one metal selected from groups VI B and VIII of the periodic table,
collecting the gaseous flow from the first reactor,
introducing a raw synthesis gas into a second reactor containing a sulfur-resistant shift catalyst X 2 ,
introducing the gaseous flow from the first reactor into the second reactor where the catalytic water-gas shift reaction takes place, the gaseous flow being introduced into the second reactor either directly through flow and/or after mixture through flow with the raw synthesis gas, and
collecting an outlet flow from the second reactor, the outlet flow comprising hydrogen-enriched synthesis gas.
2 . The process according to claim 1 , wherein the compound of formula (I) is selected from dimethyl disulfide and dimethyl sulfoxide.
3 . The process according to claim 1 , wherein the catalytic water-gas shift reaction is carried out with an inlet gas temperature of at least 230° C.
4 . The process according to claim 1 , wherein the first reactor is operated at a temperature ranging from 100 to 600° C.
5 . The process according to claim 1 , wherein the first reactor is operated at a pressure ranging from 0 to 60 bar.
6 . The process according to claim 1 , wherein the compound of formula (I) is continuously injected into the first reactor at a flow rate of 1 NI/h to 10 Nm 3 /h.
7 . The process according to claim 1 , wherein a hydrogen flow is introduced into the first reactor, the hydrogen flow coming from an exogenous source or being collected from the outlet flow of the second reactor.
8 . The process according to claim 1 , wherein the catalyst X 1 comprises molybdenum, tungsten, nickel and cobalt.
9 . The process according to claim 1 , wherein the catalyst X 2 is a cobalt and molybdenum-based catalyst.
10 . The process according to claim 1 , wherein the catalyst X 2 comprises an alkali metal.
11 . The process according to claim 1 , wherein the catalytic water-gas shift reaction is carried out at a pressure of at least 10 bar.
12 . The process according to claim 1 , wherein the raw synthesis gas comprises water and carbon monoxide in a molar ratio of water to carbon monoxide of at least 1:2.
13 . The process according to claim 1 , wherein the residence time in the second reactor ranges from 20 to 60 seconds.
14 . The process according to claim 1 , wherein the compound of formula (I) is dimethyl sulfoxide.
15 . The process according to claim 1 , wherein the compound of formula (I) is dimethyl disulfide.
16 . The process according to claim 1 , wherein the gaseous flow contains no added hydrogen sulfide.
17 . The process according to claim 1 , wherein a start-up phase of the first reactor is performed before implementation of the process.
18 . The process according to claim 5 , wherein the first reactor is operated at a pressure ranging from 10 to 40 bar.
19 . The process according to claim 12 , wherein the raw synthesis gas comprises water and carbon monoxide in a molar ratio of water to carbon monoxide of at least 1:4.