Three-dimensionally ordered macro-porous Pt/TiO2 catalyst used for water-gas shift reaction

Three-dimensionally ordered macro-porous (3DOM) Pt/TiO2 catalysts were prepared by template and impregna-tion methods, and the resultant samples were characterized by using TG-DTA, XRD, SEM, TEM, and TPR techniques. The catalytic performance for water-gas shift (WGS) reaction was tested, and the influences of some conditions, such as reduction temperature of catalysts, the amount of Pt loadings and space velocity on catalytic performance were investigated. It was shown that Pt particles were homogeneously dispersed on 3DOM TiO2. The reduction of TiO2 surface was important for the catalyticperformance. The activity test results showed that the 3DOM Pt/TiO2 catalysts exhibited very good catalytic performance for WGS reaction even at high space velocity, which was owing to the better mass transfer of 3DOM porous structure besides the high intrinsic activity of Pt/TiO2.     

Three-dimensionally ordered macro-porous Pt/TiO2 catalyst used for water-gas shift reaction

Three-dimensionally ordered macro-porous （3DOM） Pt/TiO2 catalysts were prepared by template and impregnation methods, and the resultant samples were characterized by using TG-DTA, XRD, SEM, TEM, and TPR techniques. The catalytic performance for water-gas shift （WGS） reaction was tested, and the influences of some conditions, such as reduction temperature of catalysts, the amount of Pt loadings and space velocity on catalytic performance were investigated. It was shown that Pt particles were homogeneously dispersed on 3DOM TiO2. The reduction of TiO2 surface was important for the catalytic performance. The activity test results showed that the 3DOM Pt/TiO2 catalysts exhibited very good catalytic performance for WGS reaction even at high space velocity, which was owing to the better mass transfer of 3DOM porous structure besides the high intrinsic activity of Pt/TiO2.     

Catalysts of alcohols' condensation tested in water-gas shift reaction

Catalytic activities of the system Sn-Ce-Rh-O and its oxide components SnO₂ and CeO₂ have been tested in the water-gas shift reaction (WGSR). The degree of conversion obtained in the presence of the system studied was similar to that obtained in the presence of low-activity iron oxides. The redox properties of the system studied, similarly as the redox properties of iron oxides, have been found responsible for their activity in WGSR. This revised version was published online in August 2006 with corrections to the Cover Date.     

Potassium-decorated active carbon supported Co-Mo-based catalyst for water-gas shift reaction

The effect of potassium-decoration was studied on the activity of water-gas shift (WGS) reaction over the Co-Mo-based catalysts supported on active carbon (AC), which was prepared by incipient wetness co-impregnation method. The decoration of potassium on active carbon in advance enhances the activities of the CoMo-K/AC catalysts for WGS reaction. Highest activity (about 92% conversion) was obtained at 250 ? C for the catalyst with an optimum K 2 O/AC weight ratio in the range from 0.12 to 0.15. The catalysts were characterized by TPR and EPR, and the results show that activated carbon decorated with potassium makes Co-Mo species highly dispersed, and thus easily reduced and sulfurized. XRD results show that an appropriate content of potassium-decoration on active carbon supports may favors the formation of highly dispersed Co 9 S 8 -type structures which are situated on the edge or a site in contact with MoS 2 , K-Mo-O-S, Mo-S-K phase. Those active species are responsible for the high activity of CoMo-K/AC catalysts.     

Development of chromium-free iron-based catalysts for high-temperature water-gas shift reaction

Chromium-free iron-based catalysts were prepared and studied in regard to their performance in the high-temperature water-gas shift reaction (HTS). The effects of various catalyst preparation variables (i.e., Fe/promoter ratio, pH of precipitation medium, calcination and reduction temperatures) and preparation methods were investigated. Aluminum is a potential chromium replacement in HTS catalysts. Further improvement in WGS activity of Fe–Al catalysts can be achieved by the addition of small amounts of copper or cobalt. Catalysts were characterized using BET surface area measurements, temperature-programmed reduction (TPR), X-ray diffraction (XRD), X-ray photoelectron spectroscopy (XPS), and diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS). As a textural promoter, aluminum and chromium prevent the sintering of iron oxides and stabilize magnetite phase by retarding its further reduction to FeO and metallic Fe. The promotional effect of Cu is found to be strongly dependent on the preparation method.     

助剂对低温水煤气变换反应Au/α-Fe2O3催化剂性能的影响

采用共沉淀法制备了系列Au/αFe2O3 MOxM=Zr、Al、Mg、Ca、Ba)催化剂,通过N2物理吸附、XRD、H2-TPR和CO2-TPD-MS等手段对催化剂的物化性质进行表征,考察了富氢下低温水煤气变换（WGS）反应中助剂对Au/αFe2O3催化剂性能的影响。结果表明,助剂ZrO2能有效提高Au/α Fe2O3催化剂在富氢气氛下低温WGS反应活性和稳定性,反应温度150℃时CO转化率可达88.45%,且催化剂具有较高的稳定性。研究发现,添加ZrO2助剂能抑制载体晶粒的生长,降低载体晶粒度,提高催化剂的比表面积,改善催化剂的还原性能和表面酸碱度,从而提高催化剂的催化活性和稳定性。     

La2-xCexCu1-yZnyO4 perovskites for high temperature water-gas shift reaction

The performance of La2-xCexCu1-yZnyO4 perovskites as catalysts for the high temperature water-gas shift reaction (HT-WGSR) was inves-tigated. The catalysts were characterized by EDS, XRD, BET surface area, TPR, and XANES. The results showed that all the perovskites exhibited the La2CuO4 orthorhombic structure, so the Pechini method is suitable for the preparation of pure perovskite. However, the La1.90Ce0.10CuO4 perovskite alone, when calcined at 350/700℃, also showed a (La0.935Ce0.065)2CuO4 perovskite with tetragonal struc-ture, which produced a surface area higher than the other perovskites. The perovskites that exhibited the best catalytic performance were those calcined at 350/700 ℃ and, among these, La1.90Ce0.10CuO4 was outstanding, probably because of the high surface area associated with the presence of the (La0.935Ce0.065) 2CuO4 perovskite with tetragonal structure and orthorhombic La2CuO4 phase.     

Synthesis and activity measurement of some water-gas shift reaction catalysts

The effect of calcination temperature on the activity and some properties of low temperature water gas shift reaction catalysts has been investigated. The activities of catalysts have been determined using a fixed bed catalytic reactor. The following results may be deduced from the present study. 1. The catalysts' total surface area decreased with increasing calcination temperature, presumably due to the partial sintering of the catalysts particles. 2. The presence of an amorphous CuO phase within the structure of some catalysts may be related to the desirable conditions prevailing during synthesis of the latter. 3. Observation of a similar trend between the increase in copper crystallite particle size and enhancement of catalyst activities with increasing calcination temperature demonstrates the important contribution made by the copper crystallite phase to the overall activities of water gas shift reaction catalysts. This revised version was published online in June 2006 with corrections to the Cover Date.     

Selective Reduction of CO2 with Silanes over Platinum Nanoparticles Immobilised on a Polymeric Monolithic Support under Ambient Conditions

Here, we demonstrate the use of Pt⁰ nanoparticles immobilised on a polymeric monolithic support as a ligand‐free heterogeneous catalytic system for the reduction of ¹³CO₂ at room temperature and atmospheric pressure. The described system effectively reduces ¹³CO₂ with dihydrosilanes as the hydrogen source to yield a mixture of silylformates, silylacetals and methoxysilanes, which upon further hydrolysis with D₂O, produces their respective C1‐type products, that is H¹³COOD, ¹³CH₂(OD)₂ and ¹³CH₃OD. If a monohydrosilane was used as the hydrogen source, a selective reduction of ¹³CO₂ to a product mixture of only silylformates was observed. Addition of diethylamine to this reaction mixture results in the formation of H¹³COOH and Et₂N¹³CHO. This robust catalytic system is not only maintenance‐free and simple to handle, as compared with organometallic and organocatalyst systems, but also shows 3‐ to 11‐fold better catalytic activity and exhibits higher turnover numbers (TONs) up to 21 900 (activity=6.22 kg g_Pt^?1 bar^?1).     

Ferrofluid catalyzed water gas shift reaction to give carbon-dioxide and hydrogen

A ferrofluid consisting of colloidally dispersed magnetite particles in water was found to be an efficient selective catalyst for water gas shift reaction at 15–25 atmosphere of CO pressure in the temperature range of 423–553 K where the products obtained were only CO₂ and H₂. The reaction was studied as a function of variation of the concentration of catalyst, pressure of CO gas and temperature. Kinetic parameters suggested a mechanism involving first order dependence in CO and catalyst concentrations.     

Catalytic activity in water-gas shift reaction of platinum group metals supported on iron oxides

Summary The activity of systems made of a platinum metal supported on Fe₂O₃ in the water-gas shift reaction (WGSR) has been studied. The iron oxide catalysts activity in WGSR are apparently determined by their redox properties that can be improved by addition of platinum metals.     

Development of high performance Cu/ZnO-based catalysts for methanol synthesis and the water-gas shift reaction

Our groups studies on Cu/ZnO-based catalysts for methanol synthesis via hydrogenation of CO₂ and for the water-gas shift reaction are reviewed. Effects of ZnO contained in supported Cu-based catalysts on their activities for several reactions were investigated. The addition of ZnO to Cu-based catalyst supported on Al₂O₃, ZrO₂ or SiO₂ improved its specific activity for methanol synthesis and the reverse water-gas shift reaction, but did not improve its specific activity for methanol steam reforming and the water-gas shift reaction. Methanol synthesis from CO₂ and H₂ over Cu/ZnO-based catalysts was extensively studied under a joint research project between National Institute for Resources and Environment (NIRE; one of the former research institutes reorganized to AIST) and Research Institute of Innovative Technology for the Earth (RITE). It was suggested that methanol should be produced via the hydrogenation of CO₂, but not via the hydrogenation of CO, and that H₂O produced along with methanol should greatly suppress methanol synthesis. The Cu/ZnO-based multicomponent catalysts such as Cu/ZnO/ZrO₂/Al₂O₃ and Cu/ZnO/ZrO₂/Al₂O₃/Ga₂O₃ were highly active for methanol synthesis from CO₂ and H₂. The addition of a small amount of colloidal silica to the multicomponent catalysts greatly improved their long-term stability during methanol synthesis from CO₂ and H₂. The purity of the crude methanol produced in a bench plant was 99.9 wt% and higher than that of the crude methanol from a commercial methanol synthesis from syngas. The water-gas shift reaction over Cu/ZnO-based catalysts was also studied. The activity of Cu/ZnO/ZrO₂/Al₂O₃ catalyst for the water-gas shift reaction at 523 K was less affected by the pre-treatments such as calcination and treatment in H₂ at high temperatures than that of the Cu/ZnO/Al₂O₃ catalyst. Accordingly, the Cu/ZnO/ZrO₂/Al₂O₃ catalyst was considered to be more suitable for practical use for the water-gas shift reaction. The Cu/ZnO/ZrO₂/Al₂O₃ catalyst was also highly active for the water-gas shift reaction at 673 K. Furthermore, a two-stage reaction system composed of the first reaction zone for the water-gas shift reaction at 673 K and the second reaction zone for the reaction at 523 K was found to be more efficient than a one-stage reaction system. The addition of a small amount of colloidal silica to a Cu/ZnO-based catalyst greatly improved its long-term stability in the water-gas shift reaction in a similar manner as in methanol synthesis from CO₂ and H₂.     

Catalysts of new generation and microstructured heat-exchanger reactors for the water-gas shift reaction

The catalytic systems of new generation and microstuctured heat-exchanger reactors for the water-gas shift reaction have been considered.     

Polymeric cryogels as a new family of macroporous and supermacroporous materials for biotechnological purposes

The review is devoted to a specific kind of polymeric gels formed as a result of non-deep freezing of solutions or colloidal sols of the corresponding precursors. These materials are termed as cryogels. They possess a series of unique properties, first of all, the specific character of porosity (macroporous cryogels with the pore cross-section from tenth fractions of μm to ∼10 μm and supermacroporous (gigaporous) cryogels with pores of tens and hundreds of μm) and are attractive from the viewpoint of biotechnological implementation. Approaches to the preparation of the so-called “smart” composites based on the cryogels are considered. The use of various cryogels as carriers of immobilized biocatalysts (enzymes, cells), matrices for wide-porous affinity sorbents and immunosorbents, and spongy scaffolds for 3D culturing of animal cells is discussed. Published in Russian in Izvestiya Akademii Nauk. Seriya Khimicheskaya, No. 5, pp. 996–1013, May, 2008.     

Metal doped silica membrane reactor: Operational effects of reaction and permeation for the water gas shift reaction

In this work, we investigate the performance of metal (Cobalt) doped silica membranes in a membrane reactor (MR) configuration for the low temperature water gas shift (WGS) reaction. The membranes were hydrostable and showed activated transport even after 2 weeks exposure to steam. High CO conversions resulted in the H₂ and CO partial pressures in the reaction chamber moving in opposite directions, thus favouring H₂/CO separation to treble (5–15) from 150 to 250 °C. On the other hand, the separation of H₂/CO₂ remained relatively low (2–4) as the driving force for diffusion or partial pressure of these gases remained equal in the reaction chamber irrespective of the extent of conversion. Below approximately 40% CO conversion, the MR is ineffective as the H₂ driving force for permeation was so low that H₂/CO selectivity was below unity. Operating under equilibrium limited conversion (space velocities 7500 h⁻¹) conditions, very high conversions in excess of 95% were observed and there were no significant advantages of the MR performance over the packed bed reactor (PBR). However, for higher throughputs (space velocities 38000 and 75000 h⁻¹) conversion is affected by the reaction rate, and relatively enough H₂ is removed from the reactor through the membrane. Increasing temperature to 250 °C as a function of the space velocity (75000 h⁻¹) allowed for the CO conversion in the MR to shift up to 12% as compared to the PBR.     

La2−xCexCu1−yZnyO4 perovskites for high temperature water-gas shift reaction

The performance of La_2−xCe_xCu_1−yZn_yO₄ perovskites as catalysts for the high temperature water-gas shift reaction (HT-WGSR) was investigated. The catalysts were characterized by EDS, XRD, BET surface area, TPR, and XANES. The results showed that all the perovskites exhibited the La₂CuO₄ orthorhombic structure, so the Pechini method is suitable for the preparation of pure perovskite. However, the La_1.90Ce_0.10CuO₄ perovskite alone, when calcined at 350/700 °C, also showed a (La_0.935Ce_0.065)₂CuO₄ perovskite with tetragonal structure, which produced a surface area higher than the other perovskites. The perovskites that exhibited the best catalytic performance were those calcined at 350/700 °C and, among these, La_1.90Ce_0.10CuO₄ was outstanding, probably because of the high surface area associated with the presence of the (La_0.935Ce_0.065)₂CuO₄ perovskite with tetragonal structure and orthorhombic La₂CuO₄ phase.     

Synthesis of ternary mesoporous Cu-Zn-SiO2 materials at ambient temperature and their application for the water gas shift reaction

A series of ternary mesoporous CuZnMCM-41 materials has been synthesized at ambient temperature and their structure was characterized by XRD, N₂ physical adsorption and TPR techniques. Their catalytic applications in CO water gas shift reaction were studied.     

Monolithic macroporous albumin/chitosan cryogel structure: a new matrix for enzyme immobilization

A novel monolithic macroporous material was developed by cross-linking hen egg albumin (HEA) and chitosan with glutaraldehyde at subzero temperatures. A macroporous cryogel structure allowed efficient mass transport of solutes within the material. In one application, albumin was partially replaced with active enzymes (glucose oxidase and horseradish peroxidase) resulting in the production of macroporous biocatalyst preparations suitable for flow-injection analysis of glucose in the low millimolar range. In another application, the proteolytic enzymes savinase and esperase were coupled to the macroporous structure via free amino groups on the pore walls using glutaraldehyde as cross-linker/spacer agent. The low hydraulic resistance of the matrix allowed for the development of a generic, high-performance online protein digestion system utilizing the wall-bound proteases.     

CeO_2-Al_2O_3负载金催化剂用于水煤气变换反应的催化活性

采用浸渍法和沉积-沉淀法制备了CeO2-Al2O3复合氧化物,比较了复合氧化物负载纳米金催化剂对水煤气变换反应的催化活性。通过N2物理吸附、XRD、TEM、H2-TPR等表征手段对复合氧化物及其负载金催化剂的物相和结构进行分析,发现复合氧化物的制备方法及其焙烧温度对其比表面积、孔结构及水煤气变换反应活性有明显的影响。与沉积-沉淀法相比,浸渍法制备的CeO2-Al2O3复合氧化物具有较大的CeO2晶粒尺寸,经500℃焙烧后再负载金,所得催化剂具有更高的活性,250℃时CO转化率可达78.1%。