초록 ▼

An apparatus for carrying out a multi-step process of converting hydrocarbon fuel to a substantially pure hydrogen gas feed includes a plurality of modules arranged in a nested manner along a common axis. The multi-step process includes: providing a fuel processor having a plurality of modules arran

An apparatus for carrying out a multi-step process of converting hydrocarbon fuel to a substantially pure hydrogen gas feed includes a plurality of modules arranged in a nested manner along a common axis. The multi-step process includes: providing a fuel processor having a plurality of modules arranged so that they are nested one within the other; and feeding the hydrocarbon fuel successively through each of the modules in the reactor to produce the hydrogen rich gas.

대표청구항 ▼

1. A compact fuel processor for converting a hydrocarbon fuel feed into hydrogen rich gas suitable for direct feed to a fuel cell, the compact fuel processor comprising a processor assembly containing multiple concentric vessels for converting the hydrocarbon fuel feed into the hydrogen rich gas, th

1. A compact fuel processor for converting a hydrocarbon fuel feed into hydrogen rich gas suitable for direct feed to a fuel cell, the compact fuel processor comprising a processor assembly containing multiple concentric vessels for converting the hydrocarbon fuel feed into the hydrogen rich gas, the processor assembly comprising:an oxidation core vessel containing an oxidation catalyst;a reforming vessel surrounding the oxidation core vessel and forming a first annular space filled with autothermal reforming catalyst;a desulfurizing vessel surrounding the reforming vessel and forming a second annular space filled with desulfurization catalyst; anda shift vessel surrounding the desulfurizing vessel and forming a third annular space filled with water gas shift catalyst. 2. The compact fuel processor of claim 1, further comprising a second desulfurizing vessel external to the processor assembly for desulfurizing the hydrocarbon fuel feed. 3. The compact fuel processor of claim 2, wherein the second desulfurizing vessel is a replaceable canister. 4. The processor of claim 1, wherein the processor assembly further comprises a preferred oxidation vessel surrounding the shift vessel and forming a fourth annular space filled with preferred oxidation catalyst. 5. The compact fuel processor of claim 4, wherein the oxidation core vessel oxidizes fuel cell anode tail gas to produce a hot exhaust gas. 6. The compact fuel processor of claim 5, wherein the hot exhaust gas preheats the hydrocarbon fuel. 7. The compact fuel processor of claim 5, further comprising an electric heater for preheating the anode tail gas prior to introducing the anode tail gas to the oxidation core vessel. 8. The compact fuel processor of claim 4, wherein the hydrocarbon fuel feed is sequentially introduced to the first annular space, then to the second annular space, then to the third annular space, and then to the fourth annular space to produce the hydrogen rich gas. 9. The compact fuel processor of claim 4, further comprising a plurality of cooling coils for removing the heat of reaction produced in the first annular space, the second annular space, the third annular space, and the fourth annular space. 10. The compact fuel processor of claim 9, wherein a circulating coolant flows through the cooling coils. 11. The compact fuel processor of claim 10, wherein the circulating coolant is selected from a group consisting of air, water, and the hydrocarbon fuel feed. 12. The compact fuel processor of claim 4, wherein each annular space is surrounded by heat resisting refractory. 13. A compact fuel processor for converting a hydrocarbon fuel feed into hydrogen rich gas, comprising:a heat exchanger coil;a reforming core vessel containing an autothermal reforming catalyst bed;a desulfurizing vessel surrounding the reforming core vessel and forming a first annular space filled with desulfurization catalyst;a shift vessel surrounding the desulfurizing vessel and forming a second annular space filled with water gas shift catalyst; anda preferred oxidation vessel surrounding the shift vessel and forming a third annular space filled with preferred oxidation catalyst; andwherein the hydrocarbon fuel feed is preheated by the hydrogen rich gas in the heat exchanger coil to produce a preheated hydrocarbon fuel feed; andwherein the preheated hydrocarbon fuel feed is sequentially introduced to the reforming core vessel, then to the second annular space, then to the third annular space, and then to the fourth annular space to produce the hydrogen rich gas.