초록 ▼

A distillate fuel steam reformer system in which a fuel feed stream is first separated into two process streams: an aliphatics-rich, sulfur-depleted gas stream, and an aromatics-and sulfur-rich liquid residue stream. The aliphatics-rich gas stream is desulfurized, mixed with steam, and converted in

A distillate fuel steam reformer system in which a fuel feed stream is first separated into two process streams: an aliphatics-rich, sulfur-depleted gas stream, and an aromatics-and sulfur-rich liquid residue stream. The aliphatics-rich gas stream is desulfurized, mixed with steam, and converted in a reforming reactor to a hydrogen-rich product stream. The aromatics-rich residue stream is mixed with air and combusted to provide heat necessary for endothermic process operations. Reducing the amounts of sulfur and aromatic hydrocarbons directed to desulfurzation and reforming operations minimizes the size and weight of the overall apparatus. The process of the invention is well suited to the use of microchannel apparatuses for heat exchangers, reactors, and other system components, which may be assembled in slab configuration, further reducing system size and weight.

대표청구항 ▼

We claim: 1. A compact and efficient fuel processor operating at pressures higher than one atmosphere and temperatures above 300�� C. for reforming distillate hydrocarbon fuels containing sulfur to obtain high quality hydrogen product, comprising: a separation assembly for converting and separating

We claim: 1. A compact and efficient fuel processor operating at pressures higher than one atmosphere and temperatures above 300�� C. for reforming distillate hydrocarbon fuels containing sulfur to obtain high quality hydrogen product, comprising: a separation assembly for converting and separating a sulfur-containing distillate fuel feed into an aliphatics-rich and sulfur-depleted gas stream and an aromatics-rich and sulfur-rich liquid stream; a desulfurization assembly for receiving the aliphatics-rich and sulfur-depleted gas stream exiting the separation assembly and for removing hydrogen sulfide therefrom to output desulfurized gas; a combustion assembly for receiving said aromatics-rich and sulfur-rich liquid stream exiting the separation assembly and for combusting said liquid stream with air to yield process heat; and a reforming assembly in which process heat from the combustion assembly is used to generate steam and convert the desulfurized gas exiting the desulfurization assembly to a hydrogen-rich stream. 2. The fuel processor as set forth in claim 1, wherein said separation assembly includes: a fuel vaporizer for generating a vaporized and superheated fuel stream from incoming distillate fuel; a catalytic cracking reactor for receiving said fuel stream from said fuel vaporizer and selectively cracking an aliphatic content of said fuel stream to light hydrocarbon gases while converting any organosulfur species to hydrogen sulfide; and a gas-liquid separator receiving and separating an output from said cracking reactor into a gas stream directed to said desulfurization assembly and a condensed liquid stream directed to said combustion assembly. 3. The fuel processor as set forth in claim 2, wherein said cracking reactor includes a catalyst that provides high activity for cracking the aliphatic content, high activity for conversion of the organosulfur species to hydrogen sulfide, and low selectivity for coke formation. 4. The fuel processor as set forth in claim 3, wherein the catalyst includes manganese on alumina with 10-15 weight percent loading. 5. The fuel processor as set forth in claim 2, wherein said combustion assembly provides heat to said separation assembly for said vaporization and superheating by said vaporizer and for said catalytic cracking by said cracking reactor. 6. The fuel processor as set forth in claim 2, wherein said separation assembly further includes: a fractionator for receiving the vaporized and superheated fuel stream and separating said fuel stream into a heavy liquid residue stream and a light vapor stream, said vapor stream being directed to the cracking reactor and said residue stream joining said condensed liquid stream output by said gas-liquid separator. 7. The fuel processor as set forth in claim 2, wherein said desulfurization assembly includes: a high temperature adsorber for conducting a first stage of hydrogen sulfide adsorption on said gas stream to produce a partially desulfurized gas stream; and a low temperature adsorber for conducting a second stage of hydrogen sulfide adsorption on said partially desulfurized gas stream. 8. The fuel processor as set forth in claim 1, wherein said steam reforming assembly includes: a steam generator for producing a steam stream; and a catalytic steam reforming reactor for receiving said steam stream and a desulfurized hydrocarbon gas stream from said desulfurizing assembly, and for generating therefrom a product stream that is rich in hydrogen. 9. The fuel processor as set forth in claim 8, wherein said steam reforming assembly further includes: a hydrogen purifier coupled to said catalytic steam reforming reactor for separating said product stream into a hydrogen-rich product stream and a hydrogen-depleted reject stream. 10. The fuel processor as set forth in claim 9, wherein said steam reforming assembly further includes a water recovery component coupled to said catalytic steam reforming reactor for recovering excess steam therefrom and directing such excess steam to said steam generator. 11. The fuel processor as set forth in claim 2, wherein said combustion assembly includes: a combustion fuel reservoir coupled to said separation assembly for receiving the condensed liquid stream; and a combustion reactor for combusting a mixture of fuel from said fuel reservoir and an air feed stream to provide heat to said separation assembly for said vaporization and superheating by said vaporizer and for said catalytic cracking by said cracking reactor. 12. The fuel processor as set forth in claim 11, wherein said combustion reactor includes a catalyst of copper, potassium and vanadium on alumina with 2-20 weight percent loading. 13. The fuel processor as set forth in claim 11, wherein said combustion assembly further includes a water recovery component coupled to said combustion reactor and fuel cell exhaust for recovering water into a condensed liquid stream that is directed to said steam reforming assembly. 14. A compact and efficient fuel processor comprising: a separation assembly for converting and separating a sulfur-containing distillate fuel feed into an aliphatics-rich/sulfur-depleted gas stream and an aromatics-rich and sulfur-rich liquid stream, said separation assembly including a fuel vaporizer, a catalytic cracking reactor downstream of said fuel vaporizer, and a gas-liquid separator downstream of said catalytic cracking reactor, said gas-liquid separator outputting a gas stream and a liquid stream; a desulfurization assembly having a high temperature adsorber and a low temperature adsorber arranged in series for removing hydrogen sulfide from the gas stream exiting the separation assembly to output desulfurized gas; a combustion assembly including a combustion fuel reservoir and a combustion reactor in which the liquid stream exiting the separation assembly is combusted with air to yield process heat; and a steam reforming assembly for generating steam using said process heat and for converting, using a catalytic steam reforming reactor, the desulfurized gas exiting the desulfurization assembly to a hydrogen-rich stream; said fuel processor operating at pressures higher than one atmosphere and temperatures above 300�� C. for reforming distillate hydrocarbon fuels containing sulfur to obtain high quality hydrogen product. 15. The fuel processor as set forth in claim 14, wherein said catalytic cracking reactor receives a vaporized and superheated fuel stream from said fuel vaporizer and selectively cracks an aliphatic content of said fuel stream to light hydrocarbon gases while converting any organosulfur species to hydrogen sulfide. 16. The fuel processor as set forth in claim 15, wherein said catalytic cracking reactor includes a catalyst of manganese on alumina with 10-15 weight percent loading. 17. The fuel processor as set forth in claim 15, wherein said separation assembly further includes a fractionator receiving the vaporized and superheated fuel stream from said fuel vaporizer and separating said fuel stream into a heavy liquid residue stream and a light vapor stream, said vapor stream being directed to the cracking reactor and said residue stream joining the liquid stream output by said gas-liquid separator. 18. The fuel processor as set forth in claim 14, wherein said steam reforming assembly further includes a hydrogen purifier coupled to said steam reforming reactor for separating said hydrogen-rich stream into a hydrogen-rich product stream and a hydrogen-depleted reject stream. 19. The fuel processor as set forth in claim 14, wherein each of said steam reforming assembly and said combustion assembly further includes a water recovery component. 20. The fuel processor as set forth in claim 14, wherein said combustion reactor includes a catalyst of copper/potassium/vanadium on alumina with 2-20 weight percent loading. 21. A compact and efficient fuel processor operating at pressures higher than one atmosphere and temperatures above 300�� C. for reforming distillate hydrocarbon fuels containing sulfur to obtain high quality hydrogen product, comprising: a separation assembly for converting and separating a sulfur-containing distillate fuel feed into an aliphatics-rich and sulfur-depleted gas stream and an aromatics-rich and sulfur-rich liquid stream; a combustion assembly for receiving said aromatics-rich and sulfur-rich liquid stream exiting the separation assembly and for combusting said liquid stream with air to yield process heat; a reforming assembly in which process heat from the combustion assembly is used to generate steam and convert the aliphatics-rich and sulfur-depleted gas stream to a hydrogen-rich stream; and a desulfurization assembly for removing hydrogen sulfide from said hydrogen-rich stream to output desulfurized hydrogen-rich gas.