中,高温钛乳浊釉显微结构的研究

应用ＸＲＤ、ＴＥＭ、ＳＡＤ及ＥＤＳ等测试技术，系统地研究了ＴｉＯ２及烧成温度对Ｋ２Ｏ－Ｎａ２Ｏ－ＣａＯ－ＭｇＯ－ＺｎＯ－Ａｌ２Ｏ３－ＳｉＯ２系瓷釉显微结构的作用。结果表明，在１１４０－１２２０℃烧 ，瓷釉中都存在分相与析晶现象，液滴相富含Ｔｉ＾４＋、Ｃａ＾２＋、Ｚｎ＾２＋而基体玻璃相富含Ｓｉ＾４＋，析出的晶体主要为钛榍石。随烧成温度的提高，析出晶体的数量不断减少。另外，当ＴｉＯ２加入量增加时瓷釉的     

Na^＋和Ti^4＋对CaO—Al2O3—SiO2系玻璃结构和晶化的影响

使用ＲＡＭＡＮ光谱和ＤＴＡ方法研究了含少量Ｎａ＋和Ｔｉ４＋的ＣａＯ－Ａｌ２Ｏ３－ＳｉＯ２系玻璃，发现在纯ＣＡＳ系玻璃（Ｃａ／Ａｌ≥１／２，Ａｌ／Ｓｉ≤１）中，Ａｌ３＋仅有一部分进入玻璃网络，少量Ｎａ＋的引入，有助于Ａｌ３＋进一步进入玻璃网络中，Ｎａ＋起了间接补强玻璃网络的作用，Ｎａ＋和Ｃａ２＋离子对Ａｌ３＋进入玻璃网络结构程度的影响可认为是Ｎａ＋和Ｃａ２＋离子分别以［ＡｌＯ４］Ｎａ和［ＡｌＯ４］Ｃａ［ＡｌＯ４］基团的形式进入玻璃网络中，由于结合几率和体积效应，使［ＡｌＯ４］Ｎａ较［ＡｌＯ４］Ｃａ［ＡｌＯ４］更易进入玻璃网络中。Ｔｉ４＋以［ＴｉＯ４］的形式进入玻璃网络，它对Ａｌ３＋是否能进入玻璃网络无明显影响。Ｎａ＋和Ｔｉ４＋的单独引入，均能使玻璃网络的聚合程度增强，析晶活化能提高；而当Ｎａ＋和Ｔｉ４＋同时引入时，玻璃网络聚合程度和纯ＣＡＳ系玻璃相差不大，析晶活化能有所降低。少量Ｎａ＋的引入，不会影响析出主晶相的种类和数量，而Ｔｉ４＋的引入，则会影响到所析出主晶相的种类和数量。     

CaO—Al2O3—SiO2系统玻璃晶化时首析晶相及TiO2的作用机理预测和…

通过ＣａＯ－Ａｌ２Ｏ３－ＳｉＯ２系统玻璃的结构分析预测玻璃晶化时首析晶相是钙长石。选取ＣａＯ－Ａｌ２Ｏ３－ＳｉＯ２三元相图成玻璃区内的某点作为基础玻璃的组成，在基础玻璃吕加入ＴｉＯ２。用ＤＴＡ，ＸＲＤ和ＳＥＭ方法的研究结果表明，不玻璃中加ＴｉＯ２与否，晶化时首先析出的晶相都是钙长石，且均为从表面向内部生长，驰预测相符。     

CaO—SiO2—P2O5—H2O系统中CBC材料的溶胶—凝胶过程研究：II.凝胶的…

利用ＸＲＤ，ＩＲ，ＳＥＭ及＾２９Ｓｉ，＾３１Ｐ－ＮＭＲ等测试技术研究了ＣａＯ－ＳｉＯ２－Ｐ２Ｏ５－Ｈ２Ｏ系统中干凝胶在烧成过程中的物相变化及物相间发生的化学反应，认为凝胶在烧成过程的不同阶段发生的主要化学反应如下：（１）６７３～７７３Ｋ，由Ｃａ２Ｐ２Ｏ７和Ｃａ（ＮＯ３）２．４Ｈ２Ｏ反应生成了ＯＨＡｐ；（２）７３３～８７３Ｋ，由Ｃａ２Ｐ２Ｏ７和ＣａＯ反应生成了β－Ｃ３Ｐ；（３）８７３～９７３Ｋ；由Ｃ     

含铬R2O—CaO—Al2O3—SiO2系统结晶质玻璃球状析晶机理的研究

采用顺磁共振（ＥＳＲ）、扫描电镜（ＳＥＭ）、能谱分析（ＥＤＡＸ）、Ｘ射线衍射（ＸＲＤ）等实验方法，研究了Ｃｒ２ＯＥ对Ｒ２Ｏ－ＣａＯ－Ａｌ２Ｏ３－ＳｉＯ２系统更上一层楼的晶行为的影响，并对 球状析晶机理进行了分析。球晶是由放射状的针形晶体所构成，尺寸约为几个毫米，且呈均匀分布，主晶相为β－ＣａＳｉＯ３。析晶机理是玻璃中的铬在热处理过程中首先以铬钙尖晶石固熔体「ＣａＣｒ２Ｏｒ」的形式析出，然后β－Ｃａ     

CaO-Al_2O_3-SiO_2系统玻璃晶化时首析晶相及TiO_2的作用机理预测和研究

通过ＣａＯＡｌ２Ｏ３ＳｉＯ２系统玻璃的结构分析预测玻璃晶化时首析晶相是钙长石。选取ＣａＯＡｌ２Ｏ３ＳｉＯ２三元相图成玻璃区内的某点作为基础玻璃的组成，在基础玻璃中加入ＴｉＯ２。用ＤＴＡ，ＸＲＤ和ＳＥＭ方法的研究结果表明，不管玻璃中加ＴｉＯ２与否，晶化时首先析出的晶相都是钙长石，且均为从表面向内部生长，与预测相符。ＴｉＯ２作为晶核剂，效果不太明显，在高温时ＴｉＯ２只能使玻璃网络结构松弛，粘度降低，促进玻璃中晶相的成核和生长。     

CaO-SiO_2-P_2O_5-H_2O系统中CBC材料的溶胶凝胶过程研究 Ⅱ凝胶的烧成过程

利用ＸＲＤ，ＩＲ，ＳＥＭ及２９Ｓｉ，３１ＰＮＭＲ等测试技术研究了ＣａＯＳｉＯ２Ｐ２Ｏ５Ｈ２Ｏ系统中干凝胶在烧成过程中的物相变化及物相间发生的化学反应。认为凝胶在烧成过程的不同阶段发生的主要化学反应如下：（１）６７３～７７３Ｋ：由Ｃａ２Ｐ２Ｏ７和Ｃａ（ＮＯ３）２·４Ｈ２Ｏ反应生成了ＯＨＡｐ；（２）７７３～８７３Ｋ：由Ｃａ２Ｐ２Ｏ７和ＣａＯ反应生成了βＣ３Ｐ；（３）８７３～９７３Ｋ：由ＣａＯ和ＳｉＯ２反应生成βＣ２Ｓ。因此粉末材料的主要晶相有：ＯＨＡｐ，βＣ３Ｐ和βＣ２Ｓ，其中Ｓｉ和Ｐ之间有相互固溶现象。     

Si_3N_4-Al_2O_3-ZrO_2系陶瓷表面氧化层组成的EPMA分析

利用ＥＰＭＡ和ＸＲＤ的分析方法，研究了Ｓｉ＿３Ｎ＿４－Ａｌ＿２Ｏ＿３－ＺｒＯ＿２系陶瓷材料表面氧化层组成。结果表明，Ｓｉ＿３Ｎ＿４－Ａｌ＿２Ｏ＿３－ＺｒＯ＿２系陶瓷材料表面氧化层是由方石英相、ＺｒＳｉＯ＿４相和含有Ａｌ＿２Ｏ＿３、ＣａＯ等的ＳｉＯ＿２玻璃相所组成，其中ＳｉＯ＿２玻璃相中Ａｌ＿２Ｏ＿３、ＣａＯ等的含量，随着氧化时间的增加而逐渐增加。     

涂敷型铬酸盐钝化膜的结构与耐蚀性

采用ＳＲＤ，ＥＤＸＡ，ＧＤＳ等方法研究了镀锌钢板表面涂敷型ＣｒＯ３－Ｈ３ＰＯ４－ＳｉＯ２系钝化膜的成分与结构。该钝化膜是一种由ＣｒＯ３，Ｃｒ（ＯＨ）３，ＣｒＯＯＨ，ＺｎＣｒＯ４，ＺｎＳｉＯ３，Ｚｎ３（ＰＯ４）２，ＣｒＰＯ４和ＳｉＯ２组成的凝胶网络状结构的涂敷型复合转化膜。探讨了其耐蚀机理，中性盐雾试验表明：该钝化膜的耐蚀性大大优于ＣｒＯ３－ＳｉＯ２系钝化膜。     

Cr_2O_3在SiO_2-Al_2O_3-MgO-B_2O_3系玻璃和玻璃陶瓷中的作用

利用ＳＭＥ和ＸＲＤ等技术,系统研究了Ｃｒ２Ｏ３对ＳｉＯ２－Ａｌ２Ｏ３－ＭｇＯ－Ｂ２Ｏ３系玻璃和玻璃陶瓷中的作用。当Ｃｒ２Ｏ３％＜１时,随着Ｃｒ２Ｏ３。含量的增加,玻璃试样的颜色由浅绿色逐渐转变成灰色;Ｃｒ２Ｏ３％＞１时,镁铬（铝）类晶石,Ｍｇ（Ａｌ１．５Ｃｒ０．５）Ｏ４,在玻璃试样中析出;在玻璃陶瓷中,Ｃｒ２Ｏ３％的含量的增加有助于Ｍｇ（Ａｌ１．５Ｃｒ０．５）Ｏ４相的析出,对云母晶体的析出有抑制作用。同时还发现Ｃｒ２Ｏ３的含量对云母晶体显微组织也有显著的影响作用。     

HBA／PET／HQ—TPA液晶共聚芳酯的合成与表征

采用熔融缩聚方法合成了ＨＢＡ／ＰＥＴ及ＨＢＡ／ＰＥＴ／Ｈ１－ＴＰＡ液晶共聚酯。应用ＤＳＣ，偏光显微镜等对共聚酯性能进行了表征。结果表明：加入第三单体后，可以改善二元聚酯ＨＢＡ／ＰＥＴ的共聚反应条件，并且所有样品匀具有较大的特性粘度，较小的熔融热焓，二元体系的玻璃化转变较明显，加入第三单体后的三元共聚体系玻璃化转变消失，并且随着第三单体含量的增加，共聚酯熔点上升。     

液晶聚酯的液晶行为与加工性能

液晶聚酯由于具有特异的液晶行为和高强高模性能而越来越受到人们的关注。本文对液晶聚酯的液晶态形成原因、液晶态类型与链结构的关系、液晶态热稳定性及其成型加工性能进行了讨论，指出了提高液晶态热稳定性的方法及液晶聚酯的发展趋势。     

Effect of a fluorine lateral moiety on the liquid crystallinity of wholly aromatic polyester-amides

We have identified the effect of a fluorine lateral moiety on the liquid crystallinity of wholly aromatic polyester-amides. The evolution of liquid crystal texture for two reaction systems, p-acetoxybenzoic acid (ABA)/acetoxy acetanilide (AAA)/3-fluorophthalic acid (FPA) and ABA/AAA/phthalic acid (PA), were examined and compared by in situ polymerizations under a polarizing microscope with a heating-stage. The fluorine lateral moiety was found to have an adverse effect on the liquid crystallinity. The system containing FPA needs higher critical ABA content (the rigid and straight monomer) to form liquid crystallinity than the system containing PA. In addition, the LC phase emerges faster in the ABA/AAA/PA system than in the ABA/AAA/FPA system during polymerizations. Amorphous phase reappears in the later stage of thin film polymerizations for both systems if ABA content is in a particular range. However, the ABA/AAA/FPA system has a greater amorphous area than the ABA/AAA/PA system.     

液体石蜡的应用

本文介绍了液体石蜡的来源,加工方法,对液体石蜡的应用进行了综述。指出,沈北原油含丰富的液体石蜡,提取液体石碏并进行深加工将获得很好的经济效益。     

用改进的金属膜池法测定二元物系液相扩散系数

为进一步缩短液相扩散系数的测定时间,对传统膜池的结构和实验方法作了改进,测定时间缩短为以前金属膜池的一半,仅约1小时。实验测定了苯、乙苯、邻二甲苯、环己烷和环己酮分别与正庚烷所组成的二元物系在25℃的扩散系数,还测定了甲苯+正庚烷物系在20℃、25℃、30℃、35℃的扩散系数以初步考察温度的影响。由实验数据回归得到了各物系微分扩散系数随浓度变化的多项关联式的系数。对上述物系扩散系数的变化规律进行了讨论。     

高分子液晶材料的应用及发展趋势

液晶相是不同于固相和液相的一种中介相态。系统地阐述了液晶的发现、形成机制以及分类,简单介绍了液晶高分子的结构特点,介绍了主链型和侧链型液晶高分子研究的新进展,并对液晶在各个领域的应用研究和潜在性能进展作了简要的阐述。     

热致液晶性聚合物的序态结构及其相变行为

本文介绍用透射电子显微镜（ＴＥＭ）、光学显微镜（ＯＭ）、热台Ｘ射线衍射（ＨＸＲＤ）等方法研究组成不同全芳香族热致液晶聚合物的序态结构和液晶行为。研究结果表明，它们在序态结构、相变热效应以及衍射强度随温度的变化规律等方面存在明显差异。并证明这种差异不仅取决于材料的组成，而且在一定条件下取决于晶体发育程度和其本身的致密性。     

液氯充装系统技术改造

为了减少电解精制盐水中产生的物质NCl3在液氯充装过程中聚集而发生爆炸的危害,满足安全生产和节能的要求,对液氯充装的隐患及危害进行了分析,提出了采用新的工艺方式,利用液氯屏蔽泵充装液氯钢瓶和物料输送改造方案;同时,为保证液氯屏蔽泵的安全运行,对其进行相关的安全自控方面的设置,应用于实践操作中取得了效果。     

Characterization of star-shaped poly(l-lactide)s by liquid chromatography at critical conditions

A series of linear and star-shaped poly(l-lactide)s (PLA's) have been prepared by living polymerization of l,l-dilactide (LA) and analyzed by liquid chromatography at critical conditions (LC-CC). For the analysis of the PLA's LC-CC conditions have been used corresponding to silica gel as the stationary phase and a mixture of 1,4-dioxane/n-hexane (56.25/43.75 by vol%) at 50 °C as the mobile phase. At the critical point of adsorption, a series of linear C₄H₉-PLA-OH's having molar masses (M_n) in the range from 2.3×10³ to 7.4×10⁴, prepared by ring-opening polymerization of LA initiated with Sn(OC₄H₉)₂ (THF, 80 °C), showed no dependence of the elution volumes on molar mass. In subsequent experiments, star-shaped PLA's bearing various numbers of PLA-OH arms (R-(PLA-OH)_x) have been prepared in a controlled synthesis starting from various polyols (R-(OH)_x) containing exclusively primary hydroxyl groups: diethyleneglycol (x=2), trimethylolpropane (x=3), di(trimethylolpropane) (x=4), dipentaerithritol (x=6), and poly(3-ethyl-3-hydroxymethyloxetane) (〈x〉=13.4) and LA monomer. As coinitiator/catalyst tin(II) octoate (Sn(Oct)₂) has been used (bulk polymerization, 120 °C). ¹H NMR analysis of the resulting star-shaped polymers revealed that all OH-groups in the polyols started growth of the PLA chains. The series of star-shaped PLA's have been analyzed by LC-CC as well as by two-dimensional (2D) chromatography (i.e. LC-CC versus size exclusion chromatography (SEC)) with regard to possible structural imperfections. It has been shown, that the LC-CC elution volumes of the resulting R-(PLA-OH)_x increase with the number of PLA-OH arms, allowing discrimination of the individual R-(PLA-OH)_x's in their mixture. An exponential increase of the retention volume as a function of the number of arms has been found. Eventually, LC-CC measurements of the elution volumes carried out for acetylated star-shaped PLA's (R(PLA-OOCCH₃)_x) have shown that for the interactions of the R-(PLA-OH)_x macromolecules with the column packing the hydroxyl end-groups are mostly responsible.     

Liquid flow texture analysis in trickle bed reactors using high-resolution gamma ray tomography

Trickle bed reactor performance and safety may suffer from radial and axial liquid maldistribution and thus from non-uniform utilization of the catalyst packing. Therefore, experimental analysis and fluid dynamic simulation of liquid–gas flow in trickle bed reactors is an important topic in chemical engineering. In the present study for the first time a truly high-resolution gamma ray tomography technique was applied to the quantitative analysis of the liquid flow texture in a laboratory cold flow trickle bed reactor of 90 mm diameter. The objective of this study was to present the comparative analysis of the liquid flow dynamics for two different initial liquid distributions and two different types of reactor configurations. Thus, the hydrodynamic behavior of a glass bead packing was compared to a porous Al₂O₃ catalyst particle packing using inlet flow from a commercial spray nozzle (uniform initial liquid distribution) and inlet flow from a central point source (strongly non-uniform initial liquid distribution), respectively. The column was operated in downflow mode at a gas flow rate of 180 L h⁻¹ and at liquid flow rates of 15 and 25 L h⁻¹.