Theoretical analysis of the tensile strength of a powder bed

The authors have proposed an experimental equation which correlates the tensile strength of a powder bed measured by split cell methods with the porosity of a powder bed. In this report, the authors discuss the relationships between the porosity and the pre-compressive stress and also between the tensile strength and the pre-compressive stress. As the results of this discussion, the physical base of the proposed experimental equation is proved theoretically.Furthermore, it has also been proved that the pre-compression of a powder bed brings not only the decrease of the porosity but also the increase of compressive force at the contact point of particles, and therefore the increase of tensile strength by increasing the-compression force cannot be explained simply by the change of the porosity, and then another factor, such as the compressive force at the contact point, must be considered.     

An evaluation of three commercially available peak flowmeters

The accuracy, reproducibility and interdevice variability of three models of portable peak flowmeters (standard and low range) were evaluated by using a computerized standard flow generator. Standard range; The mini-Wright peak flow meter generally overestimated peak flow from 120 L/min to 540 L/min and the Assess peak flowmeter underestimated peak flow at full range. The Pulmo-Graph peak flowmeter showed a similar pattern to the mini-Wright but with more accuracy. The Assess showed the best linearity. The reproducibilities of the three models deteriorated over 20 L/min at high flow rates. The interdevice variability of the mini-Wright was better than those of the Assess or the Pulmo-Graph. Low range: The accuracy and interdevice variability of the Pulmo-Graph were better than those of the Assess or the mini-Wright. The reproducibility of Assess seemed to be inferior to the other's. The measured flow from the low ranges was not the same as that of the standard ranges. The three peak flowmeter models have different spring mechanisms for their readings, and the measured flows by one model should not be compared with other models.     

Purification and comparative characterization of cytochrome P-450scc (CYP XIA1) from sheep adrenocortical mitochondria

Cytochrome P-450scc (CYP XI A1) was purified from sheep adrenocortical mitochondria. The purified cytochrome was found to be homogeneous on SDS-polyacrylamide gel electrophoresis and to have a heme content of 20.8 nmol/mg of protein. Its amino acid composition and NH2-terminal amino acid sequence were determined, and compared with those of other known mammalian and fish cytochromes P-450scc. EPR spectra of the cytochrome P-450scc were measured for oxidized and NO-reduced forms in the presence or absence of cholesterol and/or adreno-ferredoxin. Spectral properties of these various forms were very similar to those of the bovine enzyme. Circular dichroism spectra of the purified sheep cytochrome P-450scc in the oxidized and dithionite-reduced forms, and of their complexed forms with cholesterol or adreno-ferredoxin were analyzed in the region from 200 to 700 nm. The difference CD spectrum of the oxidized cytochrome P-450scc complexed with adreno-ferredoxin minus the oxidized form suggests an increase in the high-spin form upon the addition of adreno-ferredoxin. This may suggest a direct influence of the adreno-ferredoxin binding to the heme moiety of the oxidized cytochrome P-450scc.     

Spectroscopic and Kinetic Analysis of a New Low-Temperature Methanol Synthesis Reaction

The spectroscopy and kinetics of a new low-temperature methanol synthesis method were studied by using in situ DRIFTS on Cu/ZnO catalysts from syngas (CO/CO₂/H₂) using alcohol promoters. The adsorbed formate species easily reacted with ethanol or 2-propanol at 443 K and atmospheric pressure, and the reaction rate with 2-propanol was faster than that with ethanol. Alkyl formate was easily reduced to form methanol at 443 K and 1.0 MPa, and the hydrogenation rate of 2-propyl formate was found to be faster than that of ethyl formate. 2-Propanol used as promoter exhibited a higher activity than ethanol in the reaction of the low-temperature methanol synthesis.     

TiO2 promoted Co/SiO2 catalysts for Fischer–Tropsch synthesis

The addition of small amount of TiO₂ to silica-supported cobalt catalysts significantly increasing the dispersion of cobalt and Co metallic surface area resulting in the remarkable enhancement of the Fisher–Tropsch synthesis (FTS) activity in the slurry-phase reaction. The addition of TiO₂ adjusted the interaction between cobalt and silica support quite well to realize the favorite dispersion and reduction degree of supported cobalt, leading to high catalytic activity in FTS. The properties of various catalysts were characterized by in-situ DRIFT, XRD, TPR, N₂ physisorption and H₂ chemisorption.     

A new low-temperature methanol synthesis method: Mechanistic and kinetics study of catalytic process

Mechanism and kinetics of catalytic process for a new low-temperature methanol synthesis on Cu/ZnO catalysts from syngas (CO/CO₂/H₂) using catalytically active alcohol promoters were investigated by in situ diffuse reflectance infrared Fourier transform spectroscopy (DRIFTS). Two intermediate species, adsorbed formate species and alkyl formate species, were formed in this synthesis process. The adsorbed formate species easily reacted with ethanol or 2-propanol at 443 K and atmospheric pressure, and the reaction rate with 2-propanol was faster than that with ethanol. Alkyl formate was readily reduced to form methanol at 443 K and 1.0 MPa, and the hydrogenation rate of 2-propyl formate was found to be quicker than that of ethyl formate. As a promoter, 2-propanol exhibited a higher activity than ethanol in the reaction of the low-temperature methanol synthesis.     

A new method of low-temperature methanol synthesis on Cu/ZnO/Al2O3 catalysts from CO/CO2/H2

A new synthesis method of low-temperature methanol proceeded on Cu/ZnO/Al₂O₃ catalysts from CO/CO₂/H₂ using 2-butanol as promoters. The Cu/ZnO/Al₂O₃ catalysts were prepared by co-impregnation of r-Al₂O₃ with an aqueous solution of copper nitrate and zinc nitrate. The total carbon turnover frequency (TOF), the yield and selectivity of methanol were the highest by using the Cu/ZnO/Al₂O₃ catalyst with copper loading of 5% and the Zn/Cu molar ratio of 1/1, which precursor were not calcined, and reduced at 493 K. The activity of the catalysts increased due to the presence of the CuO/ZnO phase in the oxidized form of impregnation Cu/ZnO/Al₂O₃ catalysts. The active sites of the Cu/ZnO/Al₂O₃ catalyst for methanol synthesis are not only metallic Cu but also special sites such as the Cu–Zn site, i.e. metallic Cu and the Cu–Zn site work cooperatively to catalyze the methanol synthesis reaction.     

某钒钛磁铁矿尾矿微粉对自密实混凝土性能的影响

为了拓展某钒钛磁铁矿尾矿的应用领域,选用该钒钛磁铁矿尾矿微粉等体积替代粉煤灰制备C₃₀、C₃₅自密实混凝土,研究了其对混凝土工作性能、力学性能、体积稳定性、水化热的影响。结果表明：钒钛磁铁矿尾矿微粉等体积替代粉煤灰,V漏时间减少,扩展度提高,T500用时和J环差值均减少,施工性能得到改善;尾矿微粉混凝土早期强度高于使用粉煤灰配制的混凝土,28 d的混凝土抗压强度达到设计要求,56 d的混凝土体积收缩率都在可控范围内,尾矿微粉胶凝体系7 d累积水化热较粉煤灰胶凝体系略低。     

Direct synthesis of isoparaffin from synthesis gas under supercritical conditions

To produce isoparaffins from synthesis gas directly, modified Fischer–Tropsch (FT) synthesis was carried out under supercritical conditions using n-butane as a medium. One-step FT synthesis using a hybrid catalyst consisting of Co/SiO₂, HZSM-5 and Pd/SiO₂ was carried out. Introduction of supercritical-phase n-butane increased light isoparaffins significantly and suppressed the formation of the by-product, methane. Under supercritical-phase butane, hydrogenolysis and isomerization reactions were promoted. Due to the fact that the optimum temperatures for FT and HZSM-5 catalysts are different, 513 K and over 573 K, respectively, two-step FT synthesis was also carried out to optimize the reaction temperatures. The first-step reaction used Co/SiO₂ catalyst containing small amount of HZSM-5 for FT synthesis at 513 K, and the second-step reaction used a hybrid catalyst containing Pd/SiO₂ and zeolite for hydrogenolysis and isomerization of hydrocarbons at 573 K. Introduction of supercritical n-butane increased the isoparaffin selectivity, and decreased the methane selectivity significantly. The production of heavy hydrocarbons C₉+ was inhibited in both gas and supercritical phase. The isoparaffin selectivity in the gas phase decreased with time-on-stream, but very stable for the supercritical-phase reaction. Because water and heavy hydrocarbons were removed from active sites on zeolite and the zeolite acidity was promoted in the supercritical medium, the selectivity of isoparaffin was considered stable. Among zeolites added to the hybrid catalyst in the second-step reactor, HZSM-5 and H-beta zeolite were suitable for producing light isoparaffins. These results indicated that two-step FT synthesis under supercritical n-butane was superior for producing light isoparaffins from synthesis gas directly.     

One-step conversion of syngas to light olefins over bifunctional metal-zeolite catalyst

Light olefins(C_2–C_4) are fundamental building blocks for the manufacture of polymers, chemical intermediates,and solvents. In this work, we realized a composite catalyst, comprising Mn_xZr _yoxides and SAPO-34 zeolite,which can convert syngas(CO + H_2) into light olefins. Mn_xZr_yoxide catalysts with different Mn/Zr molar ratios were facilely prepared using the coprecipitation method prior to physical mixing with SAPO-34 zeolite. The redox properties, surface morphology, electronic state, crystal structure, and chemical elemental composition of the catalysts were examined using H_2-TPR, SEM, XPS, XRD, and EDS techniques, respectively. Tandem reactions involved activation of CO and subsequent hydrogenation over the metal oxide catalyst, producing methanol and dimethyl ether as the main reaction intermediates, which then migrated onto SAPO-34 zeolite for light olefins synthesis. Effects of temperature, pressure and reactant gas flow rate on CO conversion and light olefins selectivity were investigated in detail. The Mn_1Zr_2/SAPO-34 catalyst(Mn/Zr ratio of 1:2) attained a CO conversion of 10.8% and light olefins selectivity of 60.7%, at an optimized temperature, pressure and GHSV of 380 °C, 3MPa and 3000 h~(-1) respectively. These findings open avenues to exploit other metal oxides with CO activation capabilities for a more efficient syngas conversion and product selectivity.