碳黑的研磨

在水溶性有机颜料的分散体系中，得到好的颗粒尺寸和窄的粒径分布很不容易。因此，要达到预想的粒径指标、稳定的分散体系，就必须充分利用砂磨机和化学物质。介绍了砂磨机钢球大小和分散剂对于难研磨碳黑粒径的影响。     

Gas Hold‐Up in Stirred Tank Reactors in the Presence of Inorganic Electrolytes

Gas hold‐up (?_G) in air‐aqueous electrolyte solutions in stirred tank reactors (STR) is correlated using a relative gas dispersion parameter, N/N_cd and a surface tension factor (STF), (c/z)(dδ/dc)². For electrolyte concentration below transition concentration (c_t) a single correlation in the form of ?_G = f(N/N_cd, vvm, STF) shows good agreement with gas hold‐up data over a wide range of system and operating conditions. Above ct no effect of STF on gas hold‐up is observed and the correlation obtained is of the form ?_G = f(N/N_cd, vvm). Data available in the literature on large STR show good fit with the proposed correlation.     

Influence of oxidation on heat-treated activated carbon support properties and metallic dispersion of Ru/C catalyst

Heat-treated activated carbon has been oxidized to improve the properties related to the use as a support for the preparation of 5wt% Ru/C catalysts by impregnation. The pore structure, surface oxygen groups of the heat-treated activated carbon before and after oxidation in the gas and liquid phase, as well as catalytic activities and dispersion of Ru in the catalysts were investigated systematically. The pore structures of the samples were characterized by N₂ physisorption. Temperature-programmed desorption (TPD) was conducted to determine the chemical properties of the samples. Ru dispersion was measured by CO pulse chemisorption. The effects of oxidation treatments on carbon surface chemistry and pore structure which are closely related to Ru dispersion and catalytic activity, was examined. Furthermore, the modified heat-treated activated carbon support obtained by gas phase oxidation in CO₂ and liquid phase oxidation in nitric acid was more suitable to prepare Ru-based catalysts for ammonia synthesis than that without treatment.     

红花黄色素提取工艺的研究

对红花黄色素提取条件进行了系统研究.以羟基红花黄色素A为对照品,选定水为最佳提取剂,实验确定红花黄色素的适宜提取条件为:浸取温度70 ℃,料液比为1∶100,浸取30 min,提取两次.     

Ultrasonic Dispersion of Ceramic Powders

Ultrasonication is very effective in dispersing alumina and barium titanate slurries. When optimum conditions are used, very short durations (2 to 3 min) are enough to achieve well-dispersed, stable suspensions.     

CFD simulation of large-scale bubble plumes: Comparisons against experiments

Computational fluid dynamics (CFD) simulations have been carried out to simulate a turbulent, bubble plume in a liquid pool. A two-fluid enhanced k-? model has been used, with the extra source terms introduced to account for the interaction between the bubbles and the liquid and transient calculations have been performed to study the plume growth, the acceleration of the liquid due to viscous drag, and the approach to steady-state conditions. In order to obtain correct spreading of the plume observed experimentally, it was observed that interfacial forces like lift and turbulent dispersion plays important role. The sensitivity analysis for drag coefficient and two different turbulent dispersion forces is presented. The development of the flow variables has been compared with the experimental data. From the CFD predictions obtained in the present work, it can be concluded that a two-dimensional (2D) axisymmetric assumption in this case is justified, with 2D model predictions in good agreement with the experimental data and those of a three-dimensional (3D) model, except for the shear stresses and turbulent kinetic energy. In general, quantitative comparison with the experimental data has revealed that, by applying proper models of inter-phase momentum transfer, and performing simulations based on the two-fluid model, satisfactory predictions of mean flow quantities can be obtained for this application away from the injector.     

Self-emulsifiable soybean oil phosphate ester polyols for low-VOC corrosion resistant coatings

A series of soybean oil phosphate ester polyols (SOPEP) was prepared by reaction of fully epoxidized soybean oil with phosphoric acid and simultanoeous hydrolysis in the presence of a polar solvent. The polyols were characterized by determination of acid value, oxirane number, hydroxyl value, molecular weight (GPC), and FTIR spectra. These polyols with varying amounts of acid phosphate groups could be self-emulsified to form aqueous dispersions after neutralization with organic base. These aqueous dispersion showed varying degrees of stability and their appearance ranged from opaque dispersions to translucent to clear solutions. Waterborne coating compositions were prepared using these aqueous dispersions as principal components and their thermally cured film properties were studied. it was found that by careful selection and formulation, SOPEPs can be successfully used for low-VOC waterborne coating formulations. SOPEPs with 3.5% phosphate ester content showed visibly superior corrosion resistance properties.     

Étude expérimentale du mélange réactif au sein d'un réacteur torique ondulé (RTO)

Reactive mixing in a wavy torus reactor (WTR) has been examined experimentally. Its performances are compared to these of two other reactors: a plane torus reactor (PTR) and a baffled stirred tank reactor (BSTR). hydrodynamics of mixing has been studied using a plug flow model with axial dispersion for the WTR and PTR. The effect of axial dispersion on the kinetic of a chemical reaction was then analysed for the WTR, PTR and BSTR. Mixing times were slightly longer for the WTR due to a weaker axial dispersion. We also noticed an improvement of the convertion rate for low dissipated power.     

工业聚合反应装置—Ⅶ.悬浮聚合反应器（下）

讨论了悬浮聚合反应器的放大问题及计算机控制技术，介绍了具有预分散器的悬浮聚合反应器和连续悬浮聚合反应器。     

An XPS study of dispersion and valence state of TiO2 supported vanadium oxide catalysts

Monolayer vanadium species are mainly in the V(V) valence state, but with XPS a small fraction of V⁴⁺ species are identified. Prolonged analysis treatment increases the V⁴⁺ concentration. With increasing vanadium concentration, a monolayer coverage corresponding to 1 mg V₂O₅ per m² develops, and it contains additional layers with a thickness of about 250 Å at 4 mg V₂O₅ per m², covering 3% of its surface area.