초록 ▼

The present invention provides for a process for producing carbon monoxide. A feed gas stream of hydrogen, carbon monoxide and carbon dioxide is directed to a membrane unit which separates the feed gas stream into two streams. The stream containing carbon monoxide is directed to second membrane unit

The present invention provides for a process for producing carbon monoxide. A feed gas stream of hydrogen, carbon monoxide and carbon dioxide is directed to a membrane unit which separates the feed gas stream into two streams. The stream containing carbon monoxide is directed to second membrane unit for further purification and the steam containing the carbon dioxide and hydrogen is fed to a reverse shift reactor to produce more carbon monoxide. The carbon monoxide recovered from the reverse shift reactor is purified in a third membrane unit and directed back to the first membrane unit and is further purified and recovered as additional carbon monoxide product.

대표청구항 ▼

Having thus described the invention, what I claim is: 1. An improved process for producing carbon monoxide from a monolith reactor comprising the steps: a) directing a feed gas mixture to said monolith reactor; b) directing a first product gas from said monolith reactor comprising carbon monoxide,

Having thus described the invention, what I claim is: 1. An improved process for producing carbon monoxide from a monolith reactor comprising the steps: a) directing a feed gas mixture to said monolith reactor; b) directing a first product gas from said monolith reactor comprising carbon monoxide, hydrogen and carbon dioxide to a first membrane unit; c) separating said carbon monoxide from said first product gas in said first membrane unit; d) directing said carbon monoxide to a second membrane unit; e) directing the carbon dioxide and hydrogen from said first membrane unit to a reverse shift reactor; f) directing a second product gas from said reverse shift reactor comprising carbon monoxide, hydrogen and carbon dioxide to a third membrane unit; g) separating the carbon monoxide from the carbon dioxide and hydrogen in said third membrane unit; h) feeding the carbon monoxide rich stream recovered from said third membrane unit to said first membrane unit for further purification; i) directing the carbon dioxide and hydrogen from said third membrane unit to said reverse shift reactor; and j) recovering the carbon monoxide from step c. 2. The process as claimed in claim 1 wherein said feed gas comprises a hydrocarbon gas, oxygen and carbon dioxide. 3. The process as claimed in claim 2 wherein said hydrocarbon gas is natural gas. 4. The process as claimed in claim 1 wherein said first membrane unit contains permeable hollow fibers. 5. The process as claimed in claim 4 wherein said second membrane unit and said third membrane unit are the same as said first membrane unit. 6. The process as claimed in claim 1 wherein said monolith reactor comprises a metal catalyst consisting essentially of a metal supported by a ceria coating disposed on a ceramic monolith wherein said metal is selected from the group consisting of nickel, cobalt, iron, platinum, palladium, iridium, rhenium, ruthenium, rhodium and osmium said ceramic is selected from the group consisting of zirconia, alumina, yttria, titania, magnesia, ceria and cordierite and said ceria coating has a weight % between about 5% and about 30% with respect to said monolith. 7. The process as claimed in claim 1 wherein said product gas is compressed before entering said first membrane unit. 8. The process as claimed in claim 6 wherein said product gas is quenched prior to being compressed. 9. An improved process for purifying carbon monoxide comprising the steps: a) directing a gas stream comprising carbon monoxide, hydrogen and carbon dioxide to a first membrane unit; b) separating said carbon monoxide from said carbon dioxide and hydrogen in said first membrane unit; c) directing said carbon monoxide to a second membrane unit, wherein impurities are removed from said carbon monoxide; d) directing said carbon dioxide and hydrogen from said first membrane unit to a reverse shift reactor; e) directing a product gas from the reverse shift reactor comprising carbon monoxide, hydrogen and carbon dioxide to a third membrane unit; e) separating the carbon monoxide from said product gas in said third membrane unit; f) feeding the carbon monoxide rich stream recovered from said third membrane unit to said first membrane unit for further purification; g) directing the carbon dioxide and hydrogen from said third membrane unit to said reverse shift reactor; and h) recovering said carbon monoxide from step c. 10. The process as claimed in claim 9 wherein said hydrocarbon gas is natural gas. 11. The process as claimed in claim 9 wherein said first membrane unit contains permeable hollow fibers. 12. The process as claimed in claim 9 wherein said second membrane unit and said third membrane unit are the same as said first membrane unit.