Mini-CPO providing hydrogen for hydrogen desulfurization of hydrocarbon feeds

a technology of hydrocarbon feeds and hydrogen desulfurization, which is applied in the direction of combustible gas production, electrochemical generators, chemistry apparatuses and processes, etc., can solve the problems of affecting the reduction of sulfur level, consuming on the order of 2 kw of power, and high cost of hydrocarbon blower 30. , to achieve the effect of improving hydrogen generation, no operation energy, and less humidity

Inactive Publication Date: 2004-08-19
HYDROGENSOURCE
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  • Summary
  • Abstract
  • Description
  • Claims
  • Application Information

AI Technical Summary

Benefits of technology

0007] Objects of the invention include providing hydrogen to a hydrogen desulfurizing unit: which has less humidity in it than is provided by hydrogen recycled from a reformate stream, which does not require equipment costing several thousand dollars, and which requires substantially no energy for operation; and provision of: improved hydrogen generation, such as for fuel in a fuel cell; a lower cost source of hydrogen-containing reformate; and reduced parasitic power in a fuel cell power plant utilizing hydrogen-containing reformate.

Problems solved by technology

Problems with this system include the fact that the hydrogen blower 30 is expensive, and it consumes on the order of 2 kW of the power generated by the fuel cell for a 150 kW fuel cell power plant.
This can impair the reduction of the level of sulfur, which must reach the parts-per-billion (pbb) level for fuel cell applications and to avoid rapid deactivation of catalysts used in the process.

Method used

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  • Mini-CPO providing hydrogen for hydrogen desulfurization of hydrocarbon feeds
  • Mini-CPO providing hydrogen for hydrogen desulfurization of hydrocarbon feeds
  • Mini-CPO providing hydrogen for hydrogen desulfurization of hydrocarbon feeds

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Embodiment Construction

[0015] Referring to FIG. 2, a mini-CPO 36, about the size of a 12 ounce beverage can, receives humidified air through a valve 37 and receives hydrocarbon fuel, such as natural gas, through a fixed orifice 38. The multiplicity of valves and the fixed orifice allows adjusting the correct flows to the mini-CPO, the hydrogen desulfurizer and the major reformer. In the mini-CPO, the fuel, which for natural gas, is typically more than 99% methane with traces of sulfur compounds, nitrogen and other hydrocarbons, is converted, along with the humidified air, to reformate, which may comprise roughly 30% hydrogen, 12% CO, and small amounts of other gases such as CO.sub.2 and H.sub.2O, nitrogen from the humidifier, and unconverted hydrocarbons.

[0016] The reformate produced by the mini-CPO 36 in a line 38 is mixed with the fuel at the inlet to the hydrogen desulfurizer 17. Since no water is applied to the mini-CPO, the reformate is much drier than the reformate generated in the line 31 by the wa...

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Abstract

A hydrogen-rich reformate gas generator, such as a mini-CPO (catalytic partial oxidizer) (36), provides warm, dry, hydrogen-containing reformate gas to a hydrogen desulfurizer (17) which provides desulfurized reformate gas to a major reformer (14) (such as a CPO) which, after processing in a water-gas shift reactor (26) and preferential CO oxidizer (27) produces hydrogen-containing reformate in a line (31) for use, for instance, as fuel for a fuel cell power plant. The expensive prior art hydrogen blower (30) is thereby eliminated, thus reducing parasitic power losses in the power plant. The drier reformate provided by the mini-CPO to the hydrogen desulfurizer favors hydrogen sulfide adsorption on zinc oxide and helps to reduce sulfur to the parts per billion level.

Description

[0001] This invention relates to using a small catalytic partial oxidizer (mini-CPO) to generate hydrogen-containing reformate as an input, along with natural gas, liquified petroleum gas, or other hydrocarbon fuels for hydrogen desulfurization (HDS) in the production of hydrogen from hydrocarbon fuels, for use, for instance, in fuel cell power plants, refineries, or other processes.[0002] Fuel cell power plants use hydrogen as the fuel. Current technology includes conversion of hydrocarbon fuels to hydrogen by passing natural gas through a desulfurizer, a catalytic partial oxidizer, a water-gas shift reactor, and a preferential oxidizer for the generation of significant hydrogen for use as a fuel in a fuel cell, in which hydrogen and oxygen on opposite sides of the electrolyte are converted to electricity and water, in the known fashion.[0003] Referring to FIG. 1, hydrogen reformate is generated in a line 13 by a major reformer 14, such as a catalytic partial oxidizer (CPO), an aut...

Claims

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Application Information

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Patent Type & Authority Applications(United States)
IPC IPC(8): C01B3/24C01B3/38C10GC10G45/02C10G49/00
CPCB01J2219/00006H01M8/0675C01B3/382C01B3/386C01B2203/0261C01B2203/0283C01B2203/044C01B2203/047C01B2203/066C01B2203/1241C01B2203/127C01B2203/142C10G45/02C10G49/007H01M8/0618H01M8/0668B01J2219/00013Y02E60/50
Inventor LIU, KEBELLOWS, RICHARD J.PRESTON, JOHN L. JR.
Owner HYDROGENSOURCE
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