Abstract: A non-line-of-sight (NLOS) coating process is provided for a substrate having first and second transverse surfaces where the second surface lacks a LOS for depositional processing. The NLOS coating process includes electroplating or electroless plating a crack-resistant interlayer coating to at least the second surface and applying a wear-resistant coating to the crack-resistant interlayer coating by electrolytic or electroless plating.

Abstract: A method is disclosed for removing ozone from a gas. According to this method, the gas is contacted with an adsorbent that includes a transition metal oxide or metal organic framework to form a treated gas. The treated gas is contacted with a noble metal catalyst to catalytically decompose ozone in the treated gas, thereby forming an ozone-depleted treated gas.

Abstract: A fuel cell includes a chromium-containing metal support, a ceramic electrode layer on the metal support and an electroconductive ceramic layer between the chromium-containing metal support and the ceramic electrode layer. The electroconductive ceramic layer includes a ceramic material selected from lanthanum-doped strontium titanate and perovskite oxides.

Abstract: A method for processing biomass to produce biofuel includes decomposing lignocellulosic material into byproduct polymers that include lignin, decomposing the lignin into targeted chemical fragments, and chemically converting the targeted chemical fragments into a biofuel.

Abstract: A fuel cell includes a chromium-containing metal support, a ceramic electrode layer on the metal support and an electroconductive ceramic layer between the chromium-containing metal support and the ceramic electrode layer. The electroconductive ceramic layer includes a ceramic material selected from lanthanum-doped strontium titanate and perovskite oxides.

Abstract: A method for processing biomass to produce biofuel includes decomposing lignocellulosic material into byproduct polymers that include lignin, decomposing the lignin into targeted chemical fragments, and chemically converting the targeted chemical fragments into a biofuel.

Abstract: A substrate or method for the sorption of sulfur compounds with a high capacity includes providing a substrate that defines at least one layer of ultra-short-channel-length mesh, coating at least a portion of the substrate with a desired sorbent for sulfur sorption, and passing a flowstream through the substrate and in contact with the sorbent during sorption.

Abstract: A technique and equipment are provided for regenerating a potentially sulfur-burdened, noble metal catalyst (44) in a water gas shift reactor (150, 152, 154), which may be part of a fuel processing system (120) for a fuel cell power plant (110). An oxidant (91) is supplied to the reactor and catalyst during a period when the water gas shift reaction is terminated, and sulfur entities burdening the catalyst undergo an oxidation reaction to become SO2. The SO2 is then vented outside the system containing the reactor, as to the ambient. The oxidation reaction preferably occurs immediately upon the shift reaction being terminated to take advantage of the residual heat associated with the water gas shift reaction. Oxidant is conveniently admitted to the shift reactor and SO2 is vented from the reactor by appropriately-controlled valving that may work in combined alternation with the normal flow of process fuel through the shift reactor and fuel processing system.

Abstract: A substrate or method for the sorption of sulfur compounds with a high capacity includes providing a substrate that defines at least one layer of ultra-short-channel-length mesh, coating at least a portion of the substrate with a desired sorbent for sulfur sorption, and passing a flowstream through the substrate and in contact with the sorbent during sorption.

Abstract: A fuel processing system (FPS) (120, 220, 320) provides a hydrogen-rich reformate having a reduced level of CO (34, 234, 62), as for use in a fuel cell power plant (120). The FPS includes, in combination, a reformer (30, 230) for converting hydrocarbon feedstock (22) to reformate and a multistage hybrid WGS reactor (150, 250, 350) for converting CO with H2O in the reformate to H2 and CO2 to reduce the CO in the reformate. The multistage hybrid WGS reactor (150, 250, 350) has one stage (154, 254, 352) of active noble metal catalyst (174, 274, 374), typically platinum and/or rhenium, and an other stage (152, 252, 354) of Cu-based WGS catalyst (172, 272, 372), e.g. Cu/ZnO, whereby the collective volume of the one and the other stages is relatively small, being less than about ½ that of prior WGS reactors. The Cu-based WGS catalyst may be modified to reduce self-heat. Protection from sulfur in the reformate is also provided. The multistage hybrid WGS reactor (150, 250, 350) may further include an O2 guard.

Abstract: A shift converter, or reactor, (16HT, 16LT) in a fuel processing subsystem (14, 16HT, 16LT, 18), as for a fuel cell (12), uses an improved catalyst bed (34, 50) and the addition of oxygen (40, 40A, 40B, 40C, 40D, 41A, 41B, 41C, 41D) to reduce the amount of carbon monoxide in a process gas stream. The catalyst of bed (34, 50) is a metal, preferably a noble metal, having a promoted support of metal oxide, preferably ceria and/or zirconia. A water gas shift reaction converts carbon monoxide to carbon dioxide. The oxygen may be introduced as air, and causes an improvement in carbon monoxide removal. Use of the added oxygen enables the shift reactor (16HT, 16LT) and its catalyst bed (34, 50) to be relatively more compact for performing a given level of carbon monoxide conversion. The catalyst bed (34, 50) obviates the requirement for prior reducing of catalysts, and minimizes the need to protect the catalyst from oxygen during operation and/or shutdown.

Abstract: A fuel cell power plant (110) has a fuel cell stack assembly (CSA) (16) including an anode (18), and a fuel processing system (FPS) (120) providing a hydrogen-rich reformate/fuel stream (34, 134, 62) for the anode (18) of the CSA (16). A relatively active metal catalyst is associated with one or both of the anode (18) and the FPS (120), and is subject to degradation by the presence of even low levels, e.g. 100 ppb to 5 ppb-wt. reformate, of sulfur in the fuel stream. A guard bed (70) containing a guard material (72) is provided in the FPS (120) for protecting the relatively active metal catalysts by adsorbing, and further reducing the level of, sulfur in the fuel stream. The guard material (72) is a metal or metal oxide capable of forming a stable sulfide in the presence of low levels of H2S in the fuel stream (34), and is preferably selected from the group consisting of: ZnO, CuO on CeO2-based support, NiO on CeO2-based support, and Cu/ZnO.

Abstract: A shift converter, or reactor, (16HT, 16LT) in a fuel processing subsystem (14, 16HT, 16LT, 18), as for a fuel cell (12), uses an improved catalyst bed (34, 50) and the addition of oxygen (40, 40A, 40B, 40C, 40D, 41A, 41B, 41C, 41D) to reduce the amount of carbon monoxide in a process gas stream. The catalyst of bed (34, 50) is a metal, preferably a noble metal, having a promoted support of metal oxide, preferably ceria and/or zirconia. A water gas shift reaction converts carbon monoxide to carbon dioxide. The oxygen may be introduced as air, and causes an improvement in carbon monoxide removal. Use of the added oxygen enables the shift reactor (16HT, 16LT) and its catalyst bed (34, 50) to be relatively more compact for performing a given level of carbon monoxide conversion. The catalyst bed (34, 50) obviates the requirement for prior reducing of catalysts, and minimizes the need to protect the catalyst from oxygen during operation and/or shutdown.