螺杆挤压机混合能力的分析

分析螺槽中熔体的流动状态 ,运用加权平均总应变来评价螺杆挤压机的混合能力 ,进而提出提高混合能力的途径。对于单螺纹螺杆 ,稍长的计量段 ,稍浅的计量段螺槽及较高的螺杆转速 ,有利于混合作用 ;开发新型螺杆 ,如犁钉分流混合螺杆 ;研制高效混合型螺杆挤压机 ,如球窝型高效混合型螺杆挤压机     

核电厂小型承压容器泄漏率直读的可行性分析

对比气体泄漏率的精确计算值与直读值的差异,分析误差的成因并找出切实可行的缩小误差的方法,使得直读法在小型承压容器的大批量泄漏率检测中发挥了重要的作用。     

硅整流元件纯水冷却系统换热设备的化学清洗

介绍了硅整流元件的纯水冷却系统换热设备化学清洗中药剂的评定筛选原则。质量标准，清洗工艺等。并对其清洗效果加以评定。     

保护胶体稳定的丙烯酸酯乳液流变性

分别采用常规乳化剂和羟乙基纤维素为保护胶体制备丙烯酸酯乳液。通过TEM分别观察乳胶粒的形态。利用流变仪测定剪切速率（Ds）-剪切应力（τ）关系、剪切速率（Ds）-黏度（η）关系。结果表明：采用羟乙基纤维素为保护胶体制备的乳液与常规乳液具有不同结构，该结构使其乳液体系流变性能不同。在相同剪切速率下，保护胶体制备的丙烯酸酯乳液的剪切力明显大于常规乳液的剪切力，该乳液在一定剪切速率范围内有剪切稀化现象。     

炼厂外排污水回用于循环冷却水腐蚀影响因素初探

从单因素、多因素和复杂水系考察了炼厂外排污水回用于循环冷却水腐蚀的影响因素，结果表明，碳钢腐蚀的主要影响因素取决于离子特性、氧化膜的形成和溶解氧的扩散等综合协同作用，其中以离子特性的,影响为最大（如：Cl^-、Ca^2 、CO3^2-的腐蚀性较强）。碳钢腐蚀反应又可由以上三种主要影响因素分为三个反应控制区，而当电导率在0．1－2．0mS/cm范围时，其水质属于腐蚀危险高发区。从而也进一步说明水质的低电导率处理，其防腐效果并不理想，相反在高电导率情况下却表现出相对较好的低腐蚀性能。     

复合材料热膨胀成型工艺研究与应用

简要叙述热膨胀工艺的原理和成型工艺过程，对热膨胀芯模的材料性能和设计、制造进行试验，分析影响膨胀压力的因素，并与热压罐成型工艺进行性能对比。以硅橡胶材料制作的芯模与钢模组合使用制备碳纤维复合材料制件，应用效果较好。研究表明，该工艺适用于多腔体复合材料制件的整体共固化成型。     

助催化剂对BCZ-108催化剂聚合行为的影响研究

在铝钛物质的量比为25、50、100、150、200、300条件下,研究丙烯聚合用BCZ-108催化剂的聚合行为及聚丙烯的主要性能,并与常规应用的NA催化剂进行对比。结果表明,随着铝钛物质的量比的增大,两种催化剂的聚合反应速率的衰减越来越快,聚丙烯的立体定向性越来越低,熔点越来越低,分子量分布越来越宽;BCZ-108催化剂的聚合活性比NA催化剂高30%以上;两种催化剂的聚合活性在铝钛物质的量比为50时达到最高,此时BCZ-108催化剂的活性为1 212 g·g^-1,NA催化剂的活性为907 g·g^-1。     

Ammonia synthesis: The bellwether reaction in heterogeneous catalysis

This is a personal account of the Havreholm Conference with a choice of topics dealing with catalytic ammonia synthesis. Among the general concepts that were retained are: the rate determining step with rates of adsorption and desorption of nitrogen; the direct activated dissociative adsorption of N₂; the surface crystalline anisotropy of iron; the role of promoters in industrial iron based catalysts; and the atomic structure of the metallic surface on the industrial multiply promoted catalyst. Finally, a new isotope jump technique to measure an upper limit to the real turnover frequency is discussed.     

Characterization of dilute and dense phase vertical upflow gas-solid transport based on average concentration and velocity data

Dilute, ‘dense phase 1’, and possibly a third regime-‘dense phase 2’, were observed in a vertical 0.02 m diameter pneumatic conveyor using 210 μm sand particles. The transitions were marked by the alterations in the trend of the measured average solids hold-up while varying the solids mass flowrate at constant air velocity. Hydrodynamic characteristics together with the transition criteria for the various transport modes were established. A novel regime diagram based on average gas velocities and solids mass flowrates was developed to identify the operating conditions for these regimes, as well as the limiting solids carrying capacities of the present conveyor. A probable cause of the dilute to dense phase transition is speculated upon.     

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.