초록 ▼

Gasifying liquid hydrocarbon fuels, and in particular liquid heavy hydrocarbon fuels, at high fuel-to-air equivalence ratios with no significant soot formation comprises the steps of mixing the fuel and heated air in a prevaporization and mixing zone to prevaporize only a portion of the liquid fuel

Gasifying liquid hydrocarbon fuels, and in particular liquid heavy hydrocarbon fuels, at high fuel-to-air equivalence ratios with no significant soot formation comprises the steps of mixing the fuel and heated air in a prevaporization and mixing zone to prevaporize only a portion of the liquid fuel using only the sensible heat in the air, passing the partially vaporized fuel-air mixture through a catalyst zone to catalytically combust at least some of the prevaporized portion of the fuel while simultaneously, without the use of an external heat source, vaporizing and gasifying as-yet unvaporized fuel using the additional heat generated by the catalytic combustion, wherein the length of the catalyst zone, the catalyst configuration, and the fuel flow rate have been preselected to obtain the desired amount of gasification and to sustain continuous gasification with no significant soot formation.

대표청구항 ▼

1. A process for gasifying, at an overall fuel/air equivalence ratio φ o of greater than 3.0 and without significant soot formation, a liquid heavy hydrocarbon fuel having an end boiling point of 650° F. or greater, comprising the steps of: introducing the liquid fuel and heated air at φ o greate

1. A process for gasifying, at an overall fuel/air equivalence ratio φ o of greater than 3.0 and without significant soot formation, a liquid heavy hydrocarbon fuel having an end boiling point of 650° F. or greater, comprising the steps of: introducing the liquid fuel and heated air at φ o greater than 3 into a prevaporization and mixing zone and vaporizing in said zone less than 50% of the liquid fuel using only sensible heat in said air forming a mixture of air, vaporized fuel, and unvaporized fuel; passing the entire mixture from said prevaporization and mixing zone through a catalyst zone disposed immediately downstream of said prevaporization and mixing zone said catalyst zone including a catalyst monolith consisting essentially of a ceramic or metal substrate having catalytic wall surfaces, said catalytic wall surfaces extending in a downstream direction defining a plurality of parallel cells with a cell dimension of between 0.05 and 0.50 inch said catalyst having been initially preheated sufficiently to initiate catalytic combustion of the vaporized fuel and air upon start-up of the process; the catalyst, the length of the catalyst zone, the catalyst cell dimension, and the fuel flow rate having been preselected such that continuous vaporization and gasification of unvaporized liquid fuel is sustained within the catalyst zone after start-up using only the heat generated by the reactions within the catalyst zone and no significant soot is formed. 2. The process according to claim 1 wherein no more than 10% of the fuel is prevaporized. 3. The process according to claim 1 wherein said cells have a cell dimension of between 0.1875 and 0.30 inch. 4. The process according to claim 1 wherein the gas phase equivalence ratio φ g is less than φ o over at least a major portion of the length of the catalyst zone. 5. The process according to claim 1, 2 or 3 wherein essentially 100% of the fuel is gasified within the catalyst zone. 6. The process according to claim 1 or 2 wherein the product gas temperature exiting the catalyst zone is 1000° F. to 2400° F. 7. The process according to claim 1 or 2 wherein the product gas temperature exiting the catalyst zone is 1300° F. to 1800° F.