用凝胶渗透色谱法测定丙烯酸酯类聚合物的分子量及其分布

GPC法用于丙烯酸脂类聚合物分子量分布的测定国外已有报导。本文着重探索多孔填料、检测器和淋洗液的选择,在此基础上,测定了喷水浆料、有机玻璃二大类型的丙烯酸脂聚合物样品,并用定义法通过编制Basic程序在P—E3500型数据站上计算出分子量和分布宽度指数。     

有关聚合物平均分子量和分子量多分散性的教学点滴

从相对数均分子量和重均分子量的标准偏差角度来解释聚合物分子量分布指数与分布宽度的关系，利于学生对分子量分布指数含义的理解。     

钼体系聚1,2-丁二烯分子量及其分布

本文用粘度法和GPC法研究了MoCl_4R-i-Bu_2AlOR′催化体系合成的聚1,2-丁二烯的分子量及其分布,发现该体系聚合物分子量分布非常窄,且与聚合温度呈直线关系;利用外推法估计,在-18℃左右该体系有可能引发活性聚合。聚合温度为30—70℃时,聚合物分子量分布宽度指数为1.5—2.0。本文还研究了调节聚合物分子量及其分布的方法,发现烯丙基卤可以大幅度调节聚合物分子量,对分子量分布也有一定的调节作用,其中烯丙基碘的效果最好。     

聚硅烷亚芳弹性体的凝胶渗透色谱测量

用简易GPC柱研究了在未知合适的Mark-Houwink 系数的情况下,通过GPC和特性粘度的数据,同时计算出宽分布硅烷亚芳弹性体聚合物的分子量和这种类型聚合物的 Mark-Houwink 系数的方法。装柱填料为多孔硅胶球,理论塔板数 4200—5500块/米以上,塔板高度 0.7—0.9毫米。其分子量分布宽度指数在2左右。素炼后,分子量分布变窄,分子量下降。     

端羟基聚丁二烯和端羟基SBS遥爪聚合物的合成及表征

研究了一种以非极性烃为溶剂,α-甲基萘锂复合物为基体的双锂催化剂LM-T作为引发剂,在环已烷中使丁二烯或丁二烯/苯乙烯进行双活性阴离子聚合,用精制的环氧丙烷终止,合成了双端羟聚丁二烯(HTPB)和双端羟SBS(HTSBS)两种遥爪聚合物。研究结果表明,聚合物分子量和羟基含量可由催化剂用量调整,官能度达到或接近2。分子量分布由GPC测定,宽度指数D=1.4左右。聚合物微观结构通过IR和H-HMR测定,1.4-聚丁二烯含量达到75%左右。因此,HTPB和HTSBS是两种1.4含量较高、分子量分布较窄的离子型遥爪聚合物。     

由特性粘数和凝胶渗透色谱（GPC）图谱计算各种平均分子量

本文提出了对未知Mark-Howink常数的一个聚合物样品,从它的特性粘数和GPC图谱得到各种平均分子量的新方法。该方法对窄分布和宽分布的样品都适用,已用三组不同分子量分布和不同K和α的聚合物样品进行了验证。用该方法得到的各种平均分子量与已知K和α时用传统的普适法得到的结果是一致的。     

由特性粘数和凝胶渗透色谱（GPC）图谱计算各种平均分子量

 ]本文提出了对未知Mark-Howink常数的一个聚合物样品，从它的特性粘数和GPC图谱得到各种平均分子量的新方法。该方法对窄分布和宽分布的样品都适用，已用三组不同分子量分布和不同K和的聚合物样品进行了验证。用该方法得到的各种平均分子量与已知K和时用传统的普适法得到的结果是一致的。     

凝胶点前氯乙烯—邻苯二甲酸二烯丙基酯共聚物表征,支化度模型及悬…

根据单稀－二烯自由基共聚合反应特点，提出一种新的支化点对分子量的分布模型，讨论了用凝胶色谱－特性粘数法表征支化聚合物时，支化点对分子量分布和式〔η〕０，ｂ．〔η〕０，１＝ｇ０＾ｃ中的指数ｃ对结果的影响。建立了氯乙烯－二烯类单体悬浮合凝胶点前的平均支化度模型。用凝胶点前平均支化度和平均分子量模型拟合实验结果发现：ａ．新的支化分布模型更合理，且ｃ＝０．７２；ｂ．悬挂双键活性下降一个数量级；ｃ．对本文样     

毛细管内高分子溶液的浓度分布

采用连续自洽场理论分析了毛细管中发生凝胶化之前的聚合物溶液浓度分布的影响因素及其规律. 结果表明, 体系尺寸有限时, 改变聚合物链段、溶剂与壁面的相互作用参数之差, 聚合物溶液浓度分布会发生贫化/吸附转变; 临界作用参数与聚合物链长的倒数呈线性关系, 且拟合常数与体系尺寸、聚合物溶液平均体积分数有关; 聚合物分子量分布为多分散时, 分子量较低的组分更容易接近容器壁面, 分子量较大的组分则相反. 总之, 增加聚合物溶液浓度、链长, 选择优良溶剂, 减小体系尺寸等都会使浓度分布更加均匀.     

凝胶渗透色谱在确定特性粘数——分子量关系中的应用

粘度法测聚合物的分子量,有方便、快速、重复性好等优点。但此法需要由其他的测定分子量的绝对法如光散射,渗透压等测一组聚合物样品的分子量,与其在某一溶剂中,特定温度下的特性粘数合并使用。定出特性粘数——分子量关系式[η]=kM~a中的K、α值。式中K值是受高聚物分子量分布影响的。因此用G、P、C法测定的各聚合物样品的分子量分布指数对K值作多分散改正,有重要意义。     

松香改性苯乙烯聚合物分子量及分子量分布的GPC测定

本文利用凝胶渗透色谱测定新型高分子材料（苯乙烯-歧化松香树脂乙烯酯）的分子量及分子量分布，实验数据重视性较好。标准偏差为0．074，变异系数为3．360％。     

Molecular weight distributions of linear polymers: Detailed analysis from GPC data

The GPC method is used widely to measure molecular weights of linear polymers. High-quality GPC data contains detailed information on many aspects of the polymer's molecular weight distribution (MWD). This information can be extracted from the data using computer analysis. Equations have been derived for the two simplest MWD functions in the GPC coordinates: the Flory function (one growing polymer chain produces one polymer molecule), and for the case when two polymer radicals combine into one polymer molecule. The equations were used to analyze MWD of two classes of polymers. The first class includes polymers with narrow MWD: polyethylene, ethylene-propylene and ethylene-hexene copolymers, syndiotactic polystyrene, and radical polystyrene. The second class includes polymers with broad MWD: ethylene copolymers and polypropylene produced with heterogeneous, Ti-based catalysts. The examples demonstrate that the resolution of complex GPC curves into their constitutents serve as an important source of information about kinetics of polymerization reactions. © 1995 John Wiley & Sons, Inc.     

利用流变仪测定聚苯乙烯的分子量和分子量分布的研究

用先进流变扩展系统ARES（Advanced Rheology Expanded System）对聚苯乙烯的分子量和分子量分布进行了测定,并且将所得的结果与GPC的结果进行了比较,发现误差非常小．因此认为用ARES进行特定聚合物的分子量及分子量分布测定,是一种快速、准确的测定方法,对生产的质量控制有一定的帮助．     

凝胶色谱法测定顺丁橡胶平均分子量及其分布的研究

通过一系列的条件试验,包括样品浓度、样品量及流动相流速对柱效的影响,确定了最佳的凝胶色谱（ＧＰＣ）试验条件;采用普适校正法将聚苯乙烯（ＰＳ）标定曲线转换成顺丁橡胶（ＰＢ）标定曲线,并对Ｍａｒｋ－Ｈｏｕｗｉｎｋ方程式中Ｋ,α值的选择进行了讨论;采用４种分子量加宽方程对色谱柱加宽效应进行改正计算,通过比较,选定适合本试验系统的加宽效应的改正方法;用粘度法测得的顺丁橡胶特性粘度（η）吻合ＧＰＣ所测得特性粘度值,证明了方法的可靠性。     

Determination and Temperature Dependence of Plateau Modulus for Polymerization of Propylene to Isotactic Polypropylene with Ultra-high Molecular Weight under Catalysis of Ziegler-Natta Catalyst

The viscoelastic behavior of isotactic polypropylene with ultra-high molecular weight (UHPPH) and broad molecular weight distribution(MWD), produced in the presence of Ziegler-Natta catalyst, was investigated by means of oscillatory rheometry at 180 and 200 ℃, whose loss modulus(G") plots at 180 and 200 ℃versus the natural logarithm of angular frequency(ω) present a pronounced maximum at 34.35 and 69.21 rad/s, respectively, and do not show a maximum peak at 0. 01-100 rad/s for Ziegler-Natta catalyzing ethylenepropylene random copolymerization (PPR) with a conventional molecular weight and broad MWD. The fact indicates that the high molecular weight is responsible for a maximum peak of G"(ω) vs. lnω curves for UHPPH. This makes it possible to determine the plateau modulus (G0N) of UHPPH from a certain experimental temperature G"(ω) curve directly. For UHPPH, the G0N determined to be 4. 28×105 and 3. 62×105 Pa at 180and 200 ℃, respectively, decreases with the increase of temperature and is independent of the molecular weight, which directly confirms reputation theoretical prediction that the G0N has no relation to the molecular weight.     

Molecular weight distribution in emulsion polymerization. I. The homopolymer case

A model for evaluating the instantaneous degree of polymerization distribution of homopolymers produced in emulsion, based on the mathematics of the Markov chains, is developed. The model accounts for any number of active chains per particle, as well as for the two fundamental mechanisms of chain termination: mono- and bi-molecular, both by combination and by disproportionation. The core of the model is the so called subprocessmain process treatment, which allows us to correctly evaluate the degree of polymerization of the chains growing in the polymer particles, by distinguishing between the events experienced by the polymer chain which imply a change of its degree of polymerization (subject transitions) and those which imply only a change in the particle state (environment transitions). This is obtained by properly defining the one-step transition probability matrix of the relevant Markov process. Once this is done, the evaluation of the distribution of the degrees of polymerization reduces to a few simple operations among matrices. Explicit expressions for the instantaneous probability density functions and the relative cumulative distributions are obtained. The application of such relationships is facilitated by the numerical procedures reported in the Appendices. The results of the model developed in this work are in agreement with those of earlier models in the range of parameter values of practical interest. In the limit of very low molecular weights, only the model developed in this work provides the correct answer. Moreover, a much more significant result is its applicability to the case of emulsion copolymerization, as it is shown in Part II.     

低分子量N,O-羧甲基壳聚糖的合成及吸湿保湿性能

采用不同反应温度、反应时间和低分子量壳聚糖与氯乙酸摩尔比,在非均相反应体系中合成了不同取代度的低分子量N,O-羧甲基壳聚糖。当反应温度为60°C,反应时间为4h,低分子量壳聚糖与氯乙酸投料比为1∶1.5时,目标产物的取代度可达71%。吸湿保湿性能测定表明:取代度越大,低分子量N,O-羧甲基壳聚糖的吸湿保湿性越好,在相对湿度为81%,取代度从27%增大到71%时,其吸湿性从32.14%增大到37.27%,保湿性从310.72%增大到348.69%。     

Aqueous RAFT polymerization of acrylamide: A convenient method for polyacrylamide with narrow molecular weight distribution

Controlled and homogeneous free-radical polymerization of acrylamide(AM) in aqueous phase was realized by using S,S'-bis(α,α'-dimethyl-α'-acetic acid)-trithiocarbonate as a reversible addition-fragmentation transfer(RAFT) agent. Linear increases in molecular weight with conversion and narrow molecular weight distribution were observed for polyacrylamide(PAM) throughout the polymerization. By this method, PAMs with controlled molecular weight(up to 1.0 × 10~6) and narrow molecular weight distribution(M_w/M_n 1.2) were prepared. This study provides an effective method for synthesis of PAMs with narrow molecular weight distribution under environmentally friendly conditions.     

田菁胶、羟丙基田菁胶和瓜胶的分子量及其分布研究

用凝胶色谱（ＧＰＣ）法测定了羟丙基田菁胶（ＨＰＳ）、田菁胶（ＳＧ）和瓜胶原粉（ＧＧ）三种样品的分子量,其重均分子量顺序Ｍ＿（ＷＨＰＳ）＞Ｍ＿（ＷＧＧ）＞Ｍ＿（ＷＳＧ）,分子量范围为２．３×１０￣５～３．４×１０￣５,分散系数关系为Ｄ＿（ＨＰＳ）＝Ｄ＿（ＳＧ）＞Ｄ＿（ＧＧ）,并讨论了聚糖的多分散性与产品性能的关系。     

Step‐Growth Polymerizing Systems of General Type “AfiBgi”: Calculating the Bivariate (Molecular Size) × (Number of Branch Points) Weight Distribution Using Generating Functions and Recurrences

This study considers step‐growth polymerizing systems of general type “AfiBgi” whereby one or more of the reacting monomer species bear at least three reactive groups. The random polymerization process will lead to a population of polymer molecules in which the individual molecules may differ widely with respect to degree of polymerization and number of branch points. This study presents an algorithmic method to calculate the statistical distribution of weight over these two molecular properties. The method uses bivariate generating functions, recurrences, and integer arithmetic.