以宽分布标样标定凝胶渗透色谱柱的一种新方法

 ]用已知一种平均分子量的（重均、数均、粘均）一组宽分布标样和它们对应的GPC谱图，用平均淋出体积的概念，建立的分子量校准方程是一个多项式。用迭代法确定准确的校准方程，此方程可以是线性的，也可以是非线性的。从最后校准方程得到准确的Mn、Mw、Mv、Mw/Mn的数据。用该方程（三次式）计算的平均分子量的百分偏差大约为10％。     

窄分子量分布聚四氢呋喃的合成

以发烟硫酸-高氯酸为催化剂,通过四氢呋喃的阳离子开环聚合合成了窄分子量分布的聚四氢呋喃(PTHF)。研究了发烟硫酸和高氯酸用量、反应时间、反应温度等对PTHF分子量(Mn)及其分布(Mw/Mn)的影响。结果表明,减少发烟硫酸或增加高氯酸用量可使Mn上升;反应时间超过3 h后,反应时间对Mn及Mw/Mn的影响不大;于2℃反应Mn有最大值(11 760);反应时间5 h,在N2中聚合的Mw/Mn较小;低转化率(Mw/Mn小于1.2)时,通N2对Mn(4 000~5 500)及Mw/Mn(1.12~1.19)的影响不大。     

氯化钕异丙醇合物/三异丁基铝催化剂活性中心的分离与聚合

研究了氯化钕异丙醇合物/三异丁基铝催化剂的配制方式对异戊二烯聚合和聚合产物特性的影响。 将催化剂的悬浊液分离得到清液和沉淀，分别进行聚合，并对沉淀进行了拉曼光谱表征。 结果表明，(Nd+Al)配制方式在室温和70 ℃下所得催化剂的清液均无活性，并且70 ℃下所得催化剂的沉淀也无活性。 (Nd+IP+Al)配制方式在任何条件下所得催化剂的各组分均有活性，推测该配制方式所得催化剂可能形成的是2种活性中心：(isoprenyl)2NdCl和(isoprenyl)NdCl2。 配制方式对聚异戊二烯的微观结构没有影响(96%左右)，分离前的悬浮催化剂和沉淀催化剂所得聚异戊二烯均为高分子量(Mn＞100×104)和窄分子量分布(Mw/Mn＜2.0)的聚合物，但是分离后清液所得聚合物的分子量较低(Mn＜30×104)，分子量分布很宽(Mw/Mn＞5.0)。     

含氮试剂对P-DCC／AICl3引发异丁烯正离子聚合的影响。

以对-二枯基氯（DCC），Alcl，体系引发异丁烯在二氯甲烷（CH2C12）正己烷（Hex）（40／60，V／V）混合溶剂中进行正离子聚合，探讨了DCC用量、含氮试剂2，6-二叔丁基吡啶（DtBP）和三苯胺（TPA）对异丁烯正离子聚合转化率、产物分子量及其分布的影响．结果表明，DCC和体系中微量水均可与A1C1，产生竞争络合，形成两种活性中心并引起相继的竞争引发，聚合产物的GPC谱图呈双峰分布，分子量分布宽；增加DCC用量有利于DCC与A1C1，的络合，致使链增长反应主要通过DCC与A1C1，络合形成的活性中心引发，但聚合产物分子量相对较低，分子量分布较宽；使用DtBP，可有效地抑制微量水引发及活性链向单体的转移反应，使分子量分布明显变窄，基本实现DCC的控制引发；采用DtBP与TPA共同调节聚合反应，可使聚合产物分子量分布变窄的同时，进一步提高分子量，从而得到相对较高分子量（Mw=103200）和单峰分子量分布（Mw／Mn=2．09）的聚异丁烯产物．     

聚丙烯分子量分布的一种简易流变性质表征法

<正> 分子量分布是聚丙烯的一个重要参数,它对纺丝过程中的织构形成、卷绕丝的不均匀性和牵伸性能都有很大的影响,但是它的表征和测量却不容易。目前最常见的方法是用凝胶透过色谱法(GPC)测量试样的分子量分布曲线,并用其重均与数均分子量之比(D=(?)_w/(?)_n)作为分子量分布宽窄的表征量。可是聚丙烯的高温GPC测定需要昂贵的设备和细致的实验技巧,由于难于精确测量高分子量尾端的含量等实验技术上的原因,     

端羟基聚丁二烯预聚物的表征

本文用VPO、IR、GPC、TLC方法表征国产端羟基聚丁二烯(HTPB),其结果是:Mn为3220,Mw/Mn为1.69,f_n为2.16,f_w为2.27。证明国产HTPB预聚物的数均官能度随分子量增加而增加。探讨了用TLC法研究HTPB官能度分布的可靠性。     

Ziegler-Natta催化体系中影响聚丙烯分子量分布的因素研究进展

分子量分布是聚丙烯产品的一个重要参数,直接影响材料的使用和应用,关于聚丙烯分子量和分子量分布的控制和影响因素的研究对于工业界和学术研究都有十分重要的意义。本文主要从催化剂组成、聚合条件等方面对Ziegler-Natta催化体系中影响聚丙烯分子量分布的因素进行了详细的综述。在催化剂组成方面,主要讨论了内给电子体、外给电子体及给电子体复合技术对聚丙烯分子量分布的影响;在聚合条件方面,主要讨论了聚合时间、聚合温度、助催化剂、聚合工艺对聚丙烯分子量分布的影响。     

不同氨基酸直接改性聚乳酸的性能研究

分别以甘氨酸(Gly)和L-天冬氨酸(Asp)与L-乳酸(L-LA)直接熔融共聚制备改性聚乳酸(PLA),所得两种共聚物聚(乳酸-甘氨酸)[P(LA-co-Gly)]和聚(乳酸-天冬氨酸)[P(LA-co-Asp)]进行了表征。对P(LA-co-Gly),不同投料比时共聚物重均分子量(Mw)和分散度(Mw/Mn)随Gly投料量的增加而变小。与双官能团Gly直接改性的PLA相比,多官能团Asp直接改性的PLA具有一定的支链结构,分散度(Mw/Mn)二者接近或P(LA-co-Asp)的更高,但两种共聚物的Tg均比PLA的要大,亲水性有所提高。同时,所得共聚物均呈无定形态,且Mw都在2400到5600之间,能满足药物缓释对聚乳酸类高分子材料分子量的要求。     

TiCl4共引发异丁烯正离子聚合合成反应活性聚异丁烯

由H2O/TiCl4/甲醇或乙醚体系引发异丁烯在二氯甲烷与己烷混合溶剂中进行正离子聚合,探讨甲醇用量、聚合时间等因素对正离子聚合以及产物分子量、分子量分布和末端基结构的影响,并在此基础上探讨TiCl4共引发混合C4馏分中异丁烯选择性正离子聚合以制备活性聚异丁烯的可行性.结果表明,含氧试剂对聚合反应起到明显的调节作用,可适当稳定碳正离子活性中心,降低链增长速率,降低聚合产物的分子量(Mn=1600~4600),使分子量分布明显变窄(Mw/Mn=1.35~2.05),并可调节大分子链末端基结构及其含量.降低聚合体系中微量单体浓度以及适当延长聚合反应时间,均有利于提高聚异丁烯大分子链末端α-双键结构含量.通过TiCl4共引发异丁烯正离子聚合制备出末端α-双键含量可以达到70%以上的低分子量高反应活性聚异丁烯.此外,该引发体系还可引发混合C4馏分原料中异丁烯进行高选择性正离子聚合,得到Mn=2000、Mw/Mn=2.59、端基α-双键含量为38.9%的聚异丁烯.     

化学降解聚丙烯树脂分子量和分子量分布的模拟计算

采用化学控制降解法调节聚丙烯的分子量和分子量分布，以控制纺丝线上的结晶，可明显降低聚丙烯纺丝温度，提高成丝质量和生产效率，产生显著的经济效益。作者曾提出用聚丙烯流动性能估算它的分子量及分子量分布的方法，同时还指出，模拟计算也是一种     

经不同程度降解聚丙烯的熔体流变性质

<正> 聚丙烯(PP)的热降解和化学控制降解法七十年代开始应用于聚合物工业加工过程。聚丙烯在高温下热降解,一般认为服从无规断链机理。随降解过程进行,分子量变小,分子量分布变窄,由定向聚合反应产生的特征性高分子量尾端降解最为显著。该过程往往可显著改善PP熔体加工性,因此研究降解过程对PP熔体流变性质的影响殊属     

Linear viscoelastic behaviors of polybutene-1 melts with various structure parameters

The effects of weight-average molecular(Mw), molecular weight distribution(MWD), and isotacticity on the linear viscoelastic behavior of polybutene-1 melts are studied. It is observed that the linear viscoelastic region becomes slightly narrower with increasing frequency. In frequency sweeps, the transition of the polymer melts flow from Newtonian flow to power-law flow can be observed. The melts with higher Mw and/or broader MWD, as well as higher isotacticity exhibit higher complex viscosity, zero shear viscosity, viscoelasticity moduli, relaxation modulus, broader transition zone, while lower critical shear rate, non-Newtonian index, and the frequency at which elasticity begins to play an important role. The relationship of zero shear viscosity on Mw has been established, which agrees with the classical power law. Furthermore, it is found that the cross-over frequency decreases with increasing Mw and the cross-over modulus increases with narrowing MWD.     

聚丙烯熔体的零切变粘度与粘均分子量的关系

<正> 零切变粘度η_0是聚丙烯熔体流变性能的一个基本物理量,零切变粘度-分子量关系不仅具有理论上的兴趣,而且也有较大的实用意义。在文献中零切变粘度通常都是用毛细管粘度计数据外推求得的,但是由于聚丙烯熔体有较强的非牛顿性,即使在毛细管粘度计测量下限测得的粘度仍表现出明显的切变速率依赖性。因此,难于用外推的方法     

Study on the shear viscosity behavior of keratin/PEO blends for nanofibre electrospinning

Graessley's theory has been applied to keratin/PEO concentrated aqueous solutions giving qualitative insight to the rheology of these polymer blends in electrospinning. The shear rate dependent viscosity of different blends was compared with that of pure polymer solutions. The characteristic time τ_η was calculated by the minimum value of at the beginning of the non‐Newtonian viscosity behavior. Flow curves of PEO (at concentration from 1.0 to 7.0 wt %) reduce to a single curve by plotting η/η₀ against . Moreover, PEO solutions exhibit a linear proportionality between zero‐shear viscosity and the characteristic time η₀ ∝ τ_η. Keratin/PEO blend solutions follow the same proportionality at very high and low keratin content, whereas linearity drops when the keratin content range from 50 to 70%. The departure from the theory has been interpreted as a sign of some interaction between the macromolecules of keratin and PEO. It was supposed that keratin displaces solvent molecules and expands the PEO chain coils increasing the relaxation time of the polymer solution. This behavior was correlated with changes in the morphology of the nanofibres produced by electrospinning from these polymer blends. Finally, additive rules to zero‐shear viscosity were applied to keratin and PEO solutions, indicating that the experimental η₀ values were higher than the theoretical ones for all the proportions of the blends, especially for high keratin amount. © 2008 Wiley Periodicals, Inc. J Polym Sci Part B: Polym Phys 46: 1193–1201, 2008     

Steady-shear viscosity of polydimethylsiloxanes over the range from the lower to the upper Newtonian region

The mechanism of non-Newtonian behavior for flow from the lower to the upper Newtonian region is explained by a modification of Graessley's theory. In the theory proposed here, a viscosity η_fric, which is based on friction between polymer segments and is almost shear-independent, is introduced in addition to Graessley's entanglement viscosity η_ent, which decreases with increasing shear rate. The theory is applied to previously obtained data on steady flow of polydimethylsiloxanes of different molecular weights. The agreement between calculated and experimental results is good. In polymers with the molecular weight above the critical molecular weight for entanglement M_c, the major contribution to viscosity near zero shear rate is η_ent. As the shear rate increases, the flow curve has an inflection where η_fric cannot be disregarded in comparison with η_ent. In the upper Newtonian region, η_fric has more influence on the viscosity than η_ent. The theory can also explain the experimental results on flow of polymers with molecular weight below M_c, which were shown to be slightly non-Newtonian in the previous paper.     

茂金属 乙烯的流变性与加工性

研究了丁烯－１共聚的茂金属聚乙烯（mＰＥ）的流变性,发现茂金属聚乙烯的窄分子量分 布导致它在挤出加工剪切范围里熔体粘度高、对剪切敏感性差以及熔体从牛顿型转为非牛顿型所需的剪切速率、转变应力高,在挤出加工条件下流动性差,加工困难。对茂金属聚乙烯（mＰＥ）进行改性制得ＭmＰＥ,ＭmＰＥ熔体对温度、剪切速率的敏感性提高,在加工温 度、加工剪切范围里的天观粘度降低,加工流动性得到了显著的改进,可在普通聚乙烯加工     

茂金属聚乙烯的流变性与加工性

研究了丁烯 １ 共聚的茂金属聚乙烯（ｍＰＥ） 的流变性,发现茂金属聚乙烯的窄分子量分布导致它在挤出加工剪切速率范围里熔体粘度高、对剪切敏感性差以及熔体从牛顿型转为非牛顿型所需的剪切速率、转变应力高,在挤出加工条件下流动性差,加工困难．对茂金属聚乙烯（ｍＰＥ） 进行改性制得ＭｍＰＥ,ＭｍＰＥ 熔体对温度、剪切速率的敏感性提高,在加工温度、加工剪切速率范围里的表观粘度降低,加工流动性得到了显著的改进,可在普通聚乙烯加工设备上,制备性能优良的茂金属聚乙烯薄膜制品．     

丁醛等离子体处理填料对填充聚烯烃熔体流变性的影响

用毛细管流变仪研究了经丁醛等离子体处理的云母粉填充高密度聚乙烯熔体(160℃)和聚丙烯熔体(180℃)的流变性。数据表明,处理削弱填充聚烯烃熔体流动的非牛顿性,熔体流动非牛顿指数随等离子体处理时间的延长而增大;处理降低填充聚烯烃熔体在低切变速率下的表观粘度,提高其在高切变速率下的表观粘度,发生转变的临界切变速率对填充聚乙烯和聚丙烯分别为150S~(-1)和50S~(-1)。扫描电镜观察熔体形态证实,处理对熔体粘度的复杂影响,是处理改善填料在熔体中的分散性和提高填料与基体界面结合力两者综合作用的结果。     

Rheology of dilute and semidilute suspensions of spherical polyelectrolyte brushes

The viscosity, η, of dilute aqueous suspensions of spherical polyelectrolyte brushes is discussed. The spherical polyelectrolyte brushes consist of a solid polystyrene core of 100-nm diameter onto which linear poly(acrylic acid) chains are grafted. The relative viscosity, η/η_S (η_S is the viscosity of the solvent) of these suspensions is studied as a function of shear rate in the presence of different amounts of added salt. A marked dependence on shear rate is found, in particular when going to higher concentrations. Extrapolation to zero shear rate leads to the relative zero-shear viscosity, η₀/η_S, which can be described in terms of an effective volume fraction, φ_eff, for all salt concentrations under consideration. Moreover, the hydrodynamic radii derived from φ_eff coincide with data obtained by dynamic light scattering in the infinitely dilute regime. Data taken at higher concentrations point to a shrinking of the brush layer owing to mutual interaction.     

Modified graessley theory for non-newtonian viscosities of polydimethylsiloxanes and their solutions

A deviation from Graessley's theory of entanglement viscosity appears at very high shear rates when the flow of polydimethylsiloxanes of various molecular weights and their solutions with various concentrations is measured by the capillary method. In order to explain this deviation, a modified Graessley theory is proposed according to the previously reported suggestion that frictional viscosity appears not to be negligible at high shear rates. A reducing procedure taking a frictional viscosity parameter into account was performed. All of the reduced data are combined to give a master curve in spite of a wide range of molecular weight, concentration, and shear rate (from the lower Newtonian to very highest non-Newtonian flow region). The findings from the reducing procedure completely explain the mechanism of non-Newtonian flow for the bulk polymers with various molecular weights, including those below the critical molecular weight for entanglement, and for polymer solutions at any concentration. The viscosity of the linear polymer system consists of the shear-dependent entanglement term η_ent proposed by Graessley and the shear-independent frictional term η_fric. The non-Newtonian behavior depends on the ratio of η_ent/η_fric at the shear rate of measurement. The ratio of zero-shear entanglement viscosity η_ent,0 to η_fric and the critical shear rate for onset of the non-Newtonian flow may be used as a measure of the non-Newtonian behavior of the system and a measure of capability for its rising, respectively. The Graessley theory is to be included in the present modified theory and is applicable to the case of η_entη_fric ? 1.