影响PET树脂反应活性因素的分析

探讨了影响连续固相增粘产品活性的因素，提出了控制主反应器的温度、氮气流量、基础切片的端羧基、氮气露点等主要因素，实现生产的平稳控制，从而保证产品黏度的稳定。     

磁性纳米SO4^2-／Fe3O4-ZrO2固体超强酸催化合成己二酸二正辛酯

利用磁性对纳米固体超强酸组合，制备出磁性纳米SO4^2-／Fe3O4-ZrO2固体超强酸催化剂，并用TEM、IR、Hammett指示剂检测磁性纳米固体超强酸催化剂性能。将其用于己二酸二正辛酯（DOA）的合成反应中。得到最佳反应条件为负压下，反应温度155℃，n（正辛醇）：n（己二酸）=3．2：1，反应时间2h，w（催化剂）=1．5％，己二酸的转化率达99％。利用催化剂的磁性可将纳米颗粒催化剂迅速分离，回收率达93．8％，并能重复使用。     

Ce和La改性固体超强酸S2O82-/ZrO2-SiO2催化剂合成及其酯化性能研究

以Zr(NO₃)₄·5H₂O和Na₂SiO₃·9H₂O为原料,利用共沉淀法制备前驱体,浸渍添加稀土Ce和La,一定温度焙烧后制得掺杂稀土S₂O₈^2-/ZrO₂-SiO₂固体超强酸。通过XRD、FT-IR和SEM对催化剂进行表征,以硬脂酸的酯化合成反应为探针,考察制备条件对催化剂性能的影响以及催化剂的重复使用率。结果表明,相对于未改性的S₂O₈^2-/ZrO₂-SiO₂催化剂,添加了Ce或La的固体超强酸酯化催化活性及重复使用性能均有提高。     

复合高稳定性固态二氧化氯释放剂的研究

目前中国市场上固态二氧化氯释放剂技术不成熟，产品多为二元包装或伪一元包装，给使用和储存带来很多不便。为解决这个问题，采取亚氯酸钠为释放剂主成分，辅以复合无机盐活化剂，借助小丸包衣技术，制备了一元化、高纯、高稳定性固态二氧化氯释放剂。     

微型反应器-HPLC催化合成水杨酸甲酯的研究

选择水杨酸甲酯的催化合成反应为基础反应体系，以固体超强酸为催化剂，建立微型催化反应器与高效液相色谱的联用新技术，并对液固相催化酯化反应进行微反催化合成研究。使用ZrO₂-SiO₂/SO_^2-4催化剂制成微型催化反应器进行试验，建立微反-HPLC联用实验装置，考察了水杨酸的加入量以及反应温度对转化率的影响。并通过X-射线衍射、红外光谱和电子透镜等技术，对反应前后催化剂的晶相、酸性特征峰以及催化剂的形态形貌进行了表征。     

配合物Zn(Him)2(OAc)2的室温固相合成及表征

乙酸锌与咪唑 (Him)通过室温固相反应一步合成配合物Zn(Him) 2 (OAc) 2 ,反应不需溶剂 ,2 0min即可完成 ,产率达 96% ,并用元素分析、红外光谱、热重分析、X -射线粉末衍射和X -射线单晶衍射对产物进行了表征。     

Solid‐state polymerization of poly(ethylene terephthalate). I. Experimental study of the reaction kinetics and properties

The solid‐state polymerization (SSP) reaction kinetics of poly(ethylene terephthalate) were investigated in connection with the initial precursor intrinsic viscosity (IV; molecular weight). Evaluations were performed with otherwise equivalent precursors melt‐polymerized to IVs of 0.50, 0.56, and 0.64 dL/g. The changes in the molecular weight and other properties were monitored as functions of the reaction times at solid‐state temperatures of 160–230°C. Precursors with higher initial molecular weights exhibited higher rates of SSP than those with lower initial values, as discussed in connection with the levels of crystallinity and the carboxyl and hydroxyl end‐group composition. Activation energies decreased at temperatures above 200°C, and this indicated a change in the SSP reaction mechanism. At temperatures of 200–230°C, similar activation energies were required for the polymerization of all three precursors. Lower temperature polymerizations, from 160 to 200°C, required higher activation energies for all precursors, with the 0.50‐IV material requirement almost twice as high as that calculated for the higher IV precursors. © 2003 Wiley Periodicals, Inc. J Appl Polym Sci 89: 197–212, 2003     

Direct ethoxylation of fatty methyl ester over Al-Mg composite oxide catalyst

For the purpose of estimating the reaction mechanism of the direct ethoxylation of a fatty ester in the presence of an Al-Mg composite oxide catalyst, a labeled fatty methyl ester C₁₁H₂₃CO¹⁸OCH₃ containing ¹⁸O isotope was synthesized and directly ethoxylated. The product was evaluated by gas chromatography-mass spectrometry (GC-MS). The GC-MS spectra showed that the ¹⁸O isotope label was present only in the methoxy group at the molecular end of the ethoxylated fatty methyl ester. This supports the reaction mechanism of coordination anionic polymerization where the bond between the acyl and methoxy groups of the fatty methyl ester molecule was broken, caused by the bifunctional effect of the acid-base active sites; an intermediate chemisorption species was formed; and then ethylene oxide was addition-polymerized sequentially, in parallel.     

SO4^2-／MxOy固体超强酸催化合成1，4-二氧六环

以乙二醇为原料,采用颗粒型SO4^2-／MxOy固体超强酸倦化剂，在常压、气相条件下,固定床催化合成了1。4-二氧六环；同时考察了不同反应温度、原料配比、进料速度等条件对催化反应的影响．并对上述影响因素进行了探讨。产品经气相色谱，红外光谱及质谱分析。结果表明。原料在260℃温度条件下，以进料流速为0．12mL／min为最佳反应条件。在该实验条件下，1。4-二氧六环的生成产率达到60％-70％左右。该合成工艺应用固体超强酸催化剂具有较高的催化活性、化学稳定性好、无环境污染。是工业生产1，4-二氧六环较理想方法，具有良好的工业生产前景。