从混联法生产中提取镓的研究

针对联合法厂家资源的分布特点,提出采用化学法和树脂吸附法相结合的方式实现同时回收烧结法和拜尔法循环母液中镓的新工艺,并通过小试和扩试结果分析,阐述了该工艺的可行性。     

共沉淀法制备锰锌软磁铁氧体前躯体共沉过程中钙、镁深度脱除的热力学分析

通过对Fe(Ⅱ)-Mn(Ⅱ)-Zn(Ⅱ)-Ca(Ⅱ)-Mg(Ⅱ)-NH3-NH4HCO3-H2O体系的热力学分析，得到各金属离子浓度与pH的关系，从而确定共沉法制备锰锌软磁铁氧体前躯体共沉过程中钙、镁深度脱除的共沉区域。热力学分析结果表明，溶液中钙、镁的含量随着体系pH的增大而降低，在相同条件下镁的溶解度大于钙的溶解度。为减少进入共沉粉中的钙、镁含量，需要保证在铁、锰、锌共沉完全的基础上降低体系的pH。当溶液中[C]T=0．1mol／L，[N]T=1．0mol／L时，pH控制在6．23～6．50之间可以大大降低进入共沉粉中的钙、镁含量。确定共沉过程钙，镁深度脱除的共沉区域，对于生产高纯锰锌软磁铁氧体前躯体具有重要的指导意义。     

在以纯碱为原料的非强酸性水溶液体系中采用酸碱滴定分析的误差来源及分析方法的改进

以三聚磷酸钠生产过程为例,论述了在以纯碱为原料的非强酸性水溶液体系中,由于反应不完全导致反应物中存在少量的碳酸盐,这部分碳酸盐干扰了用酸碱滴定法测量的中和度,并据此提出中和度分析改进方法.由此可以推广到其它以纯碱为原料的非强酸性水溶液体系中.     

高压下CO在甲醇-碳酸二甲酯中的溶解度测定

利用自行建立的高压下测定气体在液体中溶解度的装置,在温度25~75℃、压力2.00~10.00MPa条件下,首次测定了CO在甲醇、碳酸二甲酯及甲醇-碳酸二甲酯混合体系中的溶解度,并用PR方程计算了CO的气相逸度,溶解度数据符合方程f=Hx。揭示了CO在甲醇、碳酸二甲酯及甲醇-碳酸二甲酯混合体系中的溶解度规律。将亨利系数和温度进行关联,关联误差很小。这表明用此关联式可预测和推算CO在这些溶剂中的溶解度。     

利用贫软锰矿制备锰盐的研究

用二氧化硫法处理贫软锰矿，得到含硫酸锰和连二硫酸锰的溶液，继而将该溶液进行净化，除杂，浓缩，结晶处理即得工业级硫酸锰，结晶母液用碳铵沉淀即得碳酸锰产品     

Environmentally friendly, heterogeneous acid and base catalysis for the methylation of catechol: Chances for the control of chemo-selectivity

The properties of catalysts with (i) Brønsted-type acidity (H-mordenite and Al/P mixed oxide), (ii) Lewis-type acidity (Al trifluoride) or (iii) basic characteristics (Mg/Fe mixed oxide) were investigated in the gas-phase methylation of catechol. When methanol was used as the methylating agent, H-mordenite and AlF₃ gave high selectivities to guaiacol (the product of O-methylation) under mild reaction conditions, that is at very low catechol conversions. An increase in temperature led to the transformation of guaiacol to phenol and cresols, and to considerable catalyst deactivation. The basic catalyst Mg/Fe/O also favored an extensive degradation of guaiacol to phenol. On the mildly acidic catalyst Al/P mixed oxide a stable catalytic performance and a high selectivity to guaiacol at 40% catechol conversion were obtained. When methylformate, a more reactive methylating agent, was used with AlF₃ and Mg/Fe mixed oxide as catalysts, higher catechol conversions and slower deactivation rates could be achieved under mild reaction conditions, with a low extent of guaiacol degradation. However, methylformate rapidly decomposed when temperatures above 350 °C were used. Finally, tests were made by reacting catechol and diethoxymethane with acid catalysts, with the aim of synthesizing methylenedioxybenzene. The latter product was obtained with high selectivity, but with very low yield, due to both catalyst deactivation and decomposition of diethoxymethane.     

不连续增强镁基复合材料的界面行为

综述了近年来国内外关于Ａｌ２Ｏ３短纤维、ＳｉＣ晶须、ＳｉＣ颗粒、Ｂ４Ｃ颗粒增强镁基复合材料的界面结构及其对复合材料性能影响的研究进展，并对今后的研究提出了一些看法。     

试论当代中国邪教的基本特征及其防范措施

在论述邪教基本内涵的基础上,着重从五个方面分别阐述了当代中国邪教的基本特征及其防范的主要措施.     

东华原型在针织服装中的应用初探

针对针织服装结构设计的特点和现状，运用东华原型的结构原理和技术应用方法，通过试样着装实验，进行比较分析，建立了针织服装基型，并阐述了其应用的方法．     

Acidic and basic hydrolysis of poly(N‐vinylformamide)

Poly(N‐vinylformamide) (PNVF) was synthesized and hydrolyzed to poly(vinylamine) (PVAm) in both HCl and NaOH solutions. The hydrolysis kinetics and the equilibrium hydrolysis were examined experimentally at different temperatures, polymer concentrations, and acid‐ or base‐to‐amide molar ratios. The hydrolysis kinetics strongly depended on temperature, polymer, and HCl or NaOH concentrations, but showed little dependence on PNVF molecular weight. The acid hydrolysis of PNVF exhibited limited conversions because of the electrostatic repulsion among the cationic amine groups generated during hydrolysis and proton hydrates. In the basic hydrolysis, complete amide conversions were observed when the NaOH/amide molar ratios were greater than unity. The effects of temperature and PNVF concentration on the equilibrium amide conversion appeared to be negligible in both acidic and basic hydrolysis. The equilibrium conversions of base hydrolysis were higher than those of acidic hydrolysis under the same reaction conditions. At NaOH/amide ratios of less than unity, the equilibrium hydrolysis experiments revealed that one base molecule could induce the hydrolysis of more than one amide group. © 2002 Wiley Periodicals, Inc. J Appl Polym Sci 86: 3412–3419, 2002