醋酸乙烯酯与1-(2-叔丁基过氧异丙基)-3-异丙烯基苯(D120)的共聚行为研究

共聚合;竞聚率;过氧化物;醋酸乙烯酯与1-(2-叔丁基过氧异丙基)-3-异丙烯基苯(D120)的共聚行为研究     

甲基丙烯酸甲酯与1-(2-叔丁基过氧异丙基)-3-异丙烯基苯的共聚研究

讨论了甲基丙烯酸甲酯与１－（２－叔丁基过氧异丙基）－３－异丙烯基苯的共聚行为。通过自由基共聚得到了带过氧侧基的聚合物。通过红外光谱，紫外光谱和凝胶色谱对共聚物进行了表征。用碘量法测定了共聚物中活性氧的含量，并由此测定了两者的竞聚率，ｒＤ１２０＝０．６９±０．０８，ｒＭＭＡ＝０．６３±０．０８。     

甲基丙烯酸甲酯与1—（2—叔丁基过氧异丙基）—3—异丙烯基苯的共？…

讨论了甲基丙烯酸甲酯与１－（２－叔丁基过氧异丙基）－３－异丙烯基苯的共聚行为。通过自由基共聚得到了带过氧侧基的聚合物。通过红外光谱，紫外光谱和凝胶色谱对共聚物进行了表征。用碘量法测定了共聚物中活性氧的含量，并由此测定了两者的竞聚率，ｒＤ１２０＝０．６９±０．０８，ｒＭＭＡ＝０．６３±０．０８。     

(1S,6R)-1-羟基-6-(1,3-苯并二硫-2-氧)-3,5-环维生素D2的合成

以VD2为原料制备了1α，25－二羟基维生素D3的重要中间体（1S，6R）－1－羟基－6－（1，3－苯并二硫－2－氧）－3，5－环维生素D2。其中BDT（1，3－苯并二硫－2－氧）基团的引入有利于共轭三烯系统的保护。     

3-(2-胂酸基苯偶氮)-6-(3-磺苯基偶氮)变色酸与血清蛋白质反应的光度研究

研究发现牛血清白蛋白与 3 (2 胂酸基苯偶氮 ) 6 (3 磺苯基偶氮 )变色酸在 pH 2 .3的Clark Lubs缓冲介质中能形成稳定的复合物 ,最大吸收波长为 6 0 5nm ,比试剂本身红移约 6 5nm ,试验制定的几种蛋白质的标准工作曲线 ,线性范围很宽 ,至少为 2 0～ 10 0 μg·ml- 1,摩尔吸光系数为3.2 1× 10 5L·mol- 1·cm- 1。用于人血清样品测定 ,准确度高 ,基本无干扰     

新显色剂1-(2.4-二硝基苯)-3-(2-噻唑)-三氮烯的合成及与汞的显色反应研究

报道了新显色剂１－（２．４－二硝基苯）－３－（２－噻唑）－三氮烯的合成及其与Ｈｇ（Ⅱ）的显色反应。实验表明，在非离子表面活性剂ＴｒｉｔｏｎＸ－１００存在下，于ｐＨ１１．７５的三酸缓冲介质中，试剂与Ｈｇ（Ⅱ）能生成蓝绿色配合物，最大吸收波长位于６９０ｎｍ处，试剂的最大吸收波长位于４１０ｎｍ处，对比度高达２８０ｎｍ，其配合比为１∶２，表观摩尔吸光系数为１．１×１０５Ｌ·ｍｏｌ－１·ｃｍ－１，Ｈｇ（Ⅱ）含量在０～１８μｇ／２５ｍＬ范围内符合比耳定律。测定了废水中汞的含量，结果令人满意。     

1-(2-苯并噻唑)-3-(4-偶氮苯基)-三氮烯与汞的显色反应研究及应用

研究了新试剂１－（２－苯并噻唑）－３－（４－偶氮苯基）－三氮烯（ＢＴＰＡＰＴ）与汞的显色反应．在Ｔｗｅｎ－８０存在下，ｐＨ为１１．２０时，Ｈｇ（Ⅱ）与试剂生成红色的１∶１型配合物，最大吸收峰位于５１０ｎｍ，表观摩尔吸光系数为１．１０×１０５Ｌ·ｍｏｌ－１·ｃｍ－１，线性范围０－１４μｇ／２５ｍＬ．建立了可用于饮用水、生活用水和工业废水汞含量测定的方法．     

2-(1H-唑基)-1-(2,3,4-三甲氧基)苯乙酮衍生物的合成与结构表征

首先以2－溴－1－（2，3，4－三甲氧基）苯乙酮，四丁基铵－1H－1，2，4－三唑或咪唑为原料，分别合成了2－（1H－1，2，4－三唑－1－基）－1－（2，3，4－三甲氧基）苯乙酮（Ia)和2－（1H－咪唑0－1－基）－1－（2，3，4－三甲氧基）苯乙酮（Ib)与盐酸羟胺反应生成2－（1H－1，2，4－三唑－1－基）－1－（2，3，4－三甲氧基）苯乙酮肟和1－（1H－咪唑－1－基）－1－（2，3，4三甲氧基）苯乙酮肟，产率为63％－72％，并经元素分析，IR和1H NMR进行了表征。     

新试剂1-(6-硝基-2-苯并噻唑)-3-(4-硝基苯)-三氮烯与汞(Ⅱ)显色反应的研究及应用

新试剂１－（６－硝基－２－苯并噻唑）－３－（４－硝基苯）－三氮烯与汞（Ⅱ）显色反应的研究及应用金传明龚楚儒胡宗球杨明华（湖北师范学院化学系黄石４３５００２）关键词１－（６－硝基－２－苯并噻唑）－３－（４－硝基苯）－三氮烯显色反应汞中图分类号Ｏ６５７．...     

新试剂1-(6-硝基-2-苯并噻唑)-3-(4-硝基苯)-三氮烯与锌的显色反应研究及应用

研究了新显色剂１－（６－硝基－２－苯并噻唑）－３－（４－硝基苯）－三氮烯（ＮＢＴＮＰＴ）与锌的显色反应，在非离子表面活性剂ＴｒｉｔｏｎＸ－１００存在下，ｐＨ１０．１～１０．８的Ｎａ２Ｂ４Ｏ７－ＮａＯＨ缓冲溶液中，Ｚｎ２＋与试剂能形成１∶２的橙黄色配合物，最大吸收波长为４４６ｎｍ，同时在５２８ｎｍ处配合物表现有最大负吸收，其表观摩尔吸光系数分别为ε＝７．０３×１０４Ｌ·ｍｏｌ－１·ｃｍ－１和ε＝１．０６×１０５Ｌ·ｍｏｌ－１·ｃｍ－１．用拟定的方法测定了人发和婴儿奶粉中的微量锌，结果令人满意．     

K2S2O8/Na2SO3引发St/BA微乳液共聚合的研究

以十二烷基硫酸钠／十二烷基苯磺酸钠(SDS／SDBS)为乳化剂，过硫酸钾／亚硫酸钠(K2S2O3／Ni2SO3)为引发剂进行苯乙烯／丙烯酸丁酯(SL／BA)微孔液共聚合反应。研究了引发剂浓度[I]OR、单体总浓度[M]、乳化剂含量[E]和聚合温度T对微孔液共聚合最大反应速率Rmax和共聚物粘均分子量^-Mη的影响，测定了共聚单体的竞聚率，结果得到：Rmax∝[I]^0.98OR[M]^0.81[E]^-0．34e^-4712／T，^-Mη∝[I]^-0.27OR[M]^0.48[E]^-0.68e^2304/T；rSt=0.598，rBA=0.0206。     

Bulk Copolymerization of Conjugated Linoleic Acid With Styrene and Butyl Acrylate: Reactivity Ratio Estimation

Free radical bulk copolymerizations of conjugated linoleic acid (CLA)/styrene (Sty) and CLA/butyl acrylate (BA) were performed at 80°C. Copolymers were characterized for composition, conversion, molecular weights and glass transition temperature (T_g). A pseudo-kinetic model was developed and validated with experimental data. Reactivity ratios estimations were performed and one impurity commonly found in CLA, oleic acid, influenced the reaction kinetics significantly. The T_g of CLA homopolymer was predicted to be 5°C.     

醋酸乙烯酯及丙烯酸丁酯半连续法乳液共聚合

我们曾对丙烯酸丁酯(BA)与醋酸乙烯酯(VAc)一步法乳液共聚合机理进行过研究,并对其胶膜及胶乳性能进行了表征。结果表明一步法共聚乳胶粒具有类似于“核壳结构”的形态,其内核由BA含量高的共聚物组成,外壳基本是PVAc均聚物,对此用不同的方法进行了验证。在此基础上我们以VAc-BA进行了半连续法乳液共聚合,以与一步法相比较,从而探讨反应过程与胶粒结构及材料性能的关系。     

Temperature and pH Dependency of Copolymerization Parameters of Acrylic Acid and 2-Hydroxypropyl Acrylate

Summary: Since copolymerization parameters of acrylic acid (AA) and 2-hydroxypropyl acrylate (HPA) in aqueous solutions are scarcely investigated a new method and different experimental setups were developed to run copolymerization experiments at different temperatures and pH values. The experiments were done with UV- or azo- initiation and analyzed by residual monomer analytics with HPLC and GPC methods. Based on the data obtained the conversion and copolymerization parameters were calculated with different mathematical models.     

Reactive Surfactant in the Emulsion Copolymerization of Methyl Methacrylate and Octyl Acrylate

The emulsion copolymerization of methyl methacrylate and octyl acrylate was studied using a reactive surfactant ammonium sulfate allyloxy nonylphenoxy poly(ethyleneoxy) (10) ether (DNS‐86), and a conventional surfactant sodium dodecylbenzene sulfonate (DBS) with a similar structure as a comparison sample. A series of latex samples have been prepared with two kinds of surfactants, and their properties have been characterized and compared. ¹H‐NMR proves that the reactive surfactant has been incorporated into the resulting copolymers. The atomic force microscopy (AFM) proves that the reactive surfactant DNS‐86 migrate to the surface of the latex film to a much less degree than the conventional surfactant DBS. Transmission electron microscopy (TEM) demonstrates that there are some differences in the particle morphologies. The stability and water‐resistance of the latex films prepared by reactive surfactant DNS‐86 are better than those prepared by the conventional surfactant DBS.     

Bulk Free‐Radical Copolymerization of n‐Butyl Acrylate and n‐Butyl Methacrylate: Reactivity Ratio Estimation

The reactivity ratios for the bulk free‐radical copolymerization of n‐butyl acrylate (BA)/n‐butyl methacrylate (BMA) are estimated at 80 °C. By performing a series of low conversion runs including replicate runs, the reactivity ratios are estimated as r_BA = 0.460 and r_BMA = 2.008. Runs to high conversions are then conducted at three different feed compositions (f_BMA = 0.2, 0.5, and 0.8) to validate the reactivity ratios. The composition data from the high conversion experiments show good agreement with the estimated reactivity ratios in the integrated form of the Mayo–Lewis model. The molecular weight, gel content, and glass transition temperature of BA/BMA copolymers are also determined.

     

High Temperature Semibatch Free Radical Copolymerization of Styrene and Butyl Acrylate

Summary: High temperature semibatch free radical solution copolymerizations of n-butyl acrylate (BA) and styrene (ST) were carried out over a range of copolymer composition. The significant increase in experimental polymer weight-average molecular weight with time, as well as the shift in the entire polymer molecular weight distribution, is explained by assuming fast β-scission of BA midchain radicals with an adjacent styrene unit, followed by subsequent addition of the resultant macromonomer to growing radicals. A mechanistic model including backbiting and β-scission, macronomer incorporation, long-chain branching, and propagation and termination penultimate effects was constructed in Predici; the model provides a good representation of the experimental data using rate coefficients taken from literature.     

Copolymerization of vinyl monomers with Gd(OCOCCl3)3-(i-Bu)3Al-Et2AlCl

The polymerization of polar monomers such as methyl methacrylate (MMA), methyl acrylate (MA), methacrylonitrile (MAN), and acrylonitrile (AN) was carried out with gadolinium-based Ziegler–Natta catalysts [Gd(OCOCCl₃)₃-(i-Bu)₃Al-Et₂AlCl] in hexane at 50°C under N₂ to elucidate the effect of the monomer's HOMO(highest occupied moleculor orbital) and LUMO (lowest unoccupied molecular orbital) levels on the polymerizability. In the case of homopolymerization, all monomers were found to polymerize and the order of relative polymerizability was as follows: MM > MA > MAN > AN. On the other hand, the result of copolymerization of St with MMA shows that the values of the monomer reactivity ratios are r₁ = 0.06 and r₂ = 1.98 for St(M₁)/MMA(M₂). The monomer reactivity ratios of styrene (St), p-methoxystyrene (PMOS), p-methylstyrene (PMS), and p-chlorostyrene (PCS) evaluated as r₁ = 0.55 and r₂ = 1.07 for St(M₁)/PMOS(M₂), r₁ = 0.38 and r₂ = 0.51 for St(M₁)/PMS(M₂), and r₁ = 0.72 and r₂ = 1.25 for St(M₁)/PCS(M₂) were compared with those for St(M₁)/MMA(M₂). The copolymerization behavior is apparently different from the titanium-based Ziegler—Natta catalyst, regarding a larger monomer reactivity ratio of PCS. The lower LUMO level of PCS and MMA may enhance a back-donation process from the metal catalyst, therefore resulting in high polymerizability. These results are discussed on the basis of the energy level of the gadolinium catalyst and the HOMO and LUMO levels of the monomers. © 1997 John Wiley & Sons, Inc. J Polym Sci A: Polym Chem 35: 2591–2597, 1997