Energy process in methanol synthesis

Claim 2

In a process for producing methanol by the steps of: (a) reacting a methanol synthesis gas containing hydrogen and at, least one of carbon monoxide and carbon dioxide over a methanol synthesis catalyst to effect partial conversion to methanol; (b) cooling the resulting partly reacted gas and separating methanol from it; (c) recycling unreacted gas from separation Step (b) to synthesis Step (a); and (d) purging a portion of unreacted gas whereby to prevent excessive build-up of the proportion of non-reacting gases in the synthesis gas, the improvement resulting in decreased energy consumption per unit of methanol output which comprises passing said purged gas to one or more fuel cells whereby to generate electricity by oxidation of hydrogen contained therein.

Claim 3

A process according to claim 1 in which the purge gas contains carbon monoxide and which includes a stage of reacting it with steam over a shift catalyst selected from the group consisting of iron-chrome and copper/zinc oxide to convert carbon monoxide to hydrogen, before passing said gas to the fuel cell.

Claim 4

A process according to claim 1 in which the methanol synthesis step is operated using excess hydrogen and the purge gas contains hydrogen in excess of the quantity that can be methanated by the carbon oxides contained in it, wherein said whole purge gas is methanated over a catalyst selected from the group consisting of supported nickel, supported cobalt and supported ruthenium and then passed to the said one or more fuel cells whereby to generate electricity by oxidation of the hydrogen still present after methanation.

Claim 5

A process according to claim 1 which comprises also recovering energy by letting-down said purge gas in an expansion engine before passing it to said one or more fuel cells.

Claim 6

A process according to claim 1 in which the fuel cell uses a liquid acid electrolyte and electrodes not poisoned by carbon oxides.

Claim 7

A process according to claim 1 in which the fuel cell employs molten alkali metal carbonates as electrolyte.

Claim 8

A methanol synthesis process according to claim 1 in which a gas enriched in carbon oxides is recovered from the fuel cell and recycled to the synthesis catalyst.

Claim 9

A process for producing methanol in a plant by the steps of: (a) generating methanol synthesis gas; (b) passing hot gases produced in synthesis gas generation through a waste heat boiler whereby to generate steam; (c) expanding such steam in one or more pass-out turbines; (d) compressing synthesis gas to synthesis pressure and circulating said gas through methanol synthesis, methanol separation and unreacted gas recycle, by means of one or more machines driven by said pass-out turbines; (e) purging a minor portion of said unreacted gas, whereby to prevent the build-up of an excessive concentration of non-reacting gases in said synthesis gas; (f) passing said purge gas to one or more fuel cells whereby to generate electricity by oxidation of hydrogen contained therein; (g) using such electricity to power one or more machines of the plant.

Claim 10

A process for producing methanol in a plant by the steps of: (a) generating methanol synthesis gas; (b) passing hot gases produced in synthesis gas generation through a waste heat boiler whereby to generate steam; (c) expanding such steam in one or more pass-out turbines; (d) compressing synthesis gas to synthesis pressure and circulating said gas through methanol synthesis, methanol separation and unreacted gas recycle, by means of one or more machines driven by said pass-out turbines; (e) purging a minor portion of said unreacted gas, whereby to prevent the build-up of an excessive concentration of non-reacting gases in said synthesis gas; (f) passing said purge gas to one or more fuel cells whereby to generate electricity by oxidation of hydrogen contained therein; (g) using such electricity to power one or more machines of the plant.

Claim 11

A process according to claim 8 wherein said methanol synthesis gas is generated by reacting a carbonaceous fuel with steam and/or oxygen at a temperature in the range 700°-1200° C.