水溶性高分子弱凝胶体系凝胶化过程的Monte Carlo模拟

为研究弱凝胶的形成过程,并把高分子弱凝胶用于三次采油,采用三维Monte Carlo模拟了高分子溶液凝胶化过程. 模拟预测了凝胶化开始的时间,得到了凝胶化过程中分子量分布的演化规律和胶团生长的三维图像. 发现生成溶胶与凝胶团的歧化过程,初始聚合物的浓度对能否形成凝胶至关重要,低于临界浓度不能形成凝胶. 模拟了凝胶化速度和聚合物浓度以及交联剂浓度的关系,并与粘度随凝胶化时间变化的实验结果进行比较, 结果表明, 聚合物浓度较高时,浓度对交联反应的影响减弱,这一趋势与实验结果相一致.     

水溶性酚醛树脂的合成及其交联性能研究

考察了部分水解聚丙烯酰胺/水溶性酚醛树脂交联体系的成胶特性,发现在聚合物浓度为1.0％时,随着交联剂浓度的增加,形成的凝胶的粘度增加,交联剂用量为0.5％,凝胶强度在30 min左右达到最高值;考察了温度、物料比等水溶性酚醛树脂的合成条件对最终凝胶体系粘度的影响,最佳反应温度为60℃,甲醛苯酚的最佳摩尔比为3:1;向甲...     

流变学法研究部分水解聚丙烯酰胺/Cr(Ⅲ)交联反应Ⅰ.浓度的影响

采用流变学法系统地考察了部分水解聚丙烯酰胺(HPAM)/Cr(Ⅲ)交联体系的反应动力学.HPAM溶液的粘性模量G"大于弹性模量G＇,且其数值随时间不发生变化,体系为粘性溶液.而HPAM/Cr(Ⅲ)体系的G＇和G"的数值都随时间变化,G"在反应开始阶段大于G＇,当反应进行一段时间后,G＇超过G"占据主要地位,体系成为弹性体系.交联过程可分为三个阶段:第一上升阶段,平缓上升阶段和第二上升阶段.利用G＇～t曲线可以推测反应机理.实验发现成胶速率随反应物HPAM和Cr(Ⅲ)的浓度的增加而增加,而成胶时间缩短.在羧基浓度过量的情况下,交联反应对Cr(Ⅲ)浓度的反应级数是1.凝胶的有效弹性交联密度随聚合物浓度的增加而增加,且随凝胶反应的进行而增加.凝胶的交联点间的链平均分子量随Cr(Ⅲ)浓度的增加和交联反应的进行而下降.     

流变学法研究部分水解聚丙烯酰胺/Cr(III)交联反应I.浓度的影响

采用流变学法系统地考察了部分水解聚丙烯酰胺（HPAM）/Cr(III)交联体系的 反应动力学。HPAM溶液的粘性模量G”大于弹性模量G’,且其数值随时间不发生变 化,体系为粘性溶液。而HPAM/Cr(III)体系的G’和G”的数值都随时间变化,G” 在反应开始阶段大于G’,当反应进行一段时间后,G’超过G”占据主要地位,体 系成为弹性体系。交联过程可分为三个阶段：第一上升阶段,平缓上升阶段和第二 上升阶段。利用G’～ t曲线可以推测反应机理。实验发现成胶速率随反应物HPAM 和Cr(III)的浓度的增加而增加,而成胶时间缩短。在羧基浓度过量的情况下,交 联反应对Cr(III)浓度的反应级数是1。凝胶的有效弹性交联密度随聚合物浓度的增 加而增,且随凝胶反应的进行而增加。凝胶的交联点间的平均分子量随Cr(III)浓 度的增加和交联反应的进行而下降。     

流变学法研究部分水解聚丙烯酰胺/Cr(III)交联反应I.浓度的影响

采用流变学法系统地考察了部分水解聚丙烯酰胺（HPAM）/Cr(III)交联体系的 反应动力学。HPAM溶液的粘性模量G”大于弹性模量G’,且其数值随时间不发生变 化,体系为粘性溶液。而HPAM/Cr(III)体系的G’和G”的数值都随时间变化,G” 在反应开始阶段大于G’,当反应进行一段时间后,G’超过G”占据主要地位,体 系成为弹性体系。交联过程可分为三个阶段：第一上升阶段,平缓上升阶段和第二 上升阶段。利用G’～ t曲线可以推测反应机理。实验发现成胶速率随反应物HPAM 和Cr(III)的浓度的增加而增加,而成胶时间缩短。在羧基浓度过量的情况下,交 联反应对Cr(III)浓度的反应级数是1。凝胶的有效弹性交联密度随聚合物浓度的增 加而增,且随凝胶反应的进行而增加。凝胶的交联点间的平均分子量随Cr(III)浓 度的增加和交联反应的进行而下降。     

粘度法研究胶态分散凝胶交联过程

通过粘度测定方法,研究了部分水解聚丙烯酰胺（ＨＰＡＭ）／ 柠檬酸铝（ＡｌＣｉｔ） 交联过程中粘度变化的特性．聚合物浓度高的ＨＰＡＭ／ＡｌＣｉｔ 体系粘度随反应时间的延长而上升,其体系粘度最终高于相同聚合物浓度的ＨＰＡＭ 溶液粘度．聚合物浓度低的ＨＰＡＭ／ＡｌＣｉｔ 体系粘度随反应时间的延长而下降,其体系粘度低于相同聚合物浓度的ＨＰＡＭ 溶液粘度．ＨＰＡＭ／ＡｌＣｉｔ 交联体系的聚合物浓度低于临界浓度时,交联反应后形成稀胶态分散凝胶（ＴＣＤＧ） ．在实验条件下,临界浓度在１５０ ～３００ｍｇ／Ｌ 之间．当聚合物浓度于临界浓度和７００ｍｇ／Ｌ之间时,形成浓胶态分散凝胶（ＣＣＤＧ） ;当聚合物浓度高于７００ｍｇ／Ｌ 时,ＨＰＡＭ／ＡｌＣｉｔ 交联体系形成整体凝胶．     

凝胶形成动态过程在线监测方法的比较

以醋酸介质中戊二醛（Ｇｌｕ）交联壳聚糖（ＣＳ）水凝胶的形成为例,研究比较了粘度法,电导法,光度法和荧光探针法用于监测凝胶形成动态过程的可行性性和特点,结果表明：粘度法具有简单、直观等优点,但粘度法不能够跟踪凝胶点（ｇｅｌｌｉｎｇｐｏｉｎｔｓ）后体系的进一步变化,旋转粘度法在测定时对体系的扰动不容忽视。电导法和光度法跟踪的是引起凝胶化的交联反应过程,但溶液到凝胶的转化往往发生在交联反应完成之前,因此所得结果未必与宏观观察结果相一致,荧光探针法具有适用面宽,可供选用的探针种类多、方法灵活等特点,对于研究凝胶形成动态过程具有普适性,该法还可用于凝胶性质的研究。     

自由基引发的凝胶化反应的Monte Carlo模拟

基于自由基凝胶化反应的基本原理,在一个具有周期性边界条件的二维网络上,利用动态ＭｏｎｔｅＣａｒｌｏ 方法模拟了聚合物凝胶的自由基凝胶化反应,得到了凝胶的具体结构,研究了总单体浓度（ 单体浓度和交联剂浓度之和） 对凝胶的分形结构和孔径分布的影响．模拟中首次考虑了聚合后单体的运动对凝胶结构的影响．结果表明：考虑聚合后单体的运动,可使所得凝胶网络的分形维数和凝胶化所需的最低浓度均显著小于动力学凝胶化模型和ＤＬＡ 模型的相应值．用移动气泡法得到了凝胶网络的孔径分布,发现凝胶网络中大孔所占百分率明显多于随机纤维网络模型．     

不饱和聚氨酯微凝胶的制备及其自稳定作用研究

采用聚乙二醇、异佛尔酮二异氰酸酯和交联剂三羟甲基丙烷或三羟基丙烷三丙烯酸酯,在丁酮中以溶液聚合法制备了自稳定的聚氨酯微凝胶。用粘度法及凝胶渗析色谱、红外光谱分析了凝胶形成过程,观察到随反应时间(t)延长,反应体系粘度增加,但t=210min时粘度突然下降,聚合物分子量增加,表明此时形成了聚合物凝胶。用电子透射显微镜及粒度分析仪分析了凝胶的形态与粒径,观察到了聚乙二醇的自动空间稳定现象。     

超支化聚硅氧烷的紫外光固化行为及固化动力学研究

采用等温差示光量热技术(DPC)研究了超支化聚硅氧烷的紫外光固化行为及固化动力学. 探索了引发剂浓度、 光强度、 聚合温度和环境气氛对固化行为的影响规律. 研究结果表明, 增加光引发剂浓度和光强度及提高环境温度均可提高其固化速率和双键最终转化率. 在空气中固化时存在氧阻聚现象, 增大光强度可以显著缩短诱导期. 运用带扩散因子的自催化固化动力学模型研究了其光固化动力学, 计算出特定条件下的光固化动力学参数, 反应总级数约为6—7, 表观活化能为9.95 kJ/mol. 通过超支化聚合物与两种结构类似的低官能度单体光固化行为的对比, 研究了超支化聚合物固化行为与其分子结构的关系, 发现由于超支化大分子的独特结构, 在固化初始阶段便产生凝胶, 因此双键的最终转化率偏低.     

Effect of Composition of HPAM/Chromium(III) Acetate Gels on Delayed Gelation Time

A delayed crosslinking system employed with hydrolyzed polyacrylamide (HPAM) and chromium acetate was developed for high profile control in low-temperature reservoirs. The crosslinking system formed strong gel at polymer concentration range of 3000–5000 mg/L, and the gelation time was delayed to 8–30 days, which offered the crosslinking system enough time to flow into deep water-producing zones and plug large pore paths, forcing follow-up fluids to enter low-permeability layer and reduce disproportionate permeability. The effect of polymer hydrolysis degree, polymer concentration, pH, and crosslinker concentration on delaying gelation time was evaluated using bottle testing. Meanwhile, sand-packed tube displacement experiments revealed the plugging performance of delayed crosslinking system. According to Fourier transform infrared spectroscopy (FTIR) analysis, as well as crosslinking mechanism between polymer and chromium acetate, the delayed mechanism of crosslinked system demonstrated that due to stronger affinity of acetate complexes as a ligand, its substitution in situ by carboxylate group of polyacrylamide slowed down the initial rate-determining step of crosslinking reaction.     

Dynamic thickening investigation of the gelation process of PAM/PEI system at high temperature and high pressure

The gelation process of organically polymer gel was investigated by dynamic thickening measurements. Rheological measurements were used to evaluate the viscosity of the gel. During the gelation process, high temperature resulted in higher rate of crosslinking. Rigid and stable gel was formed in neutral and alkaline media, and the higher of the pH value, the faster of the gelation process. However, gel could not be formed in acid condition. Moreover, the rate of crosslinking increased with the increase of concentration of polymer and crosslinker. The addition of NH₄Cl elongated the gelation time significantly, but played a negative role in the gel strength, while a rigid gel was formed in the presence of Sodium acetate or trisodium citrate dehydrate. This paper summarizes the results and discusses how various parameters affect the gelation process of the gel.     

Preparation of Homogeneous Hydrogels by Controlling the Crosslinker Reactivity and Availability

Network microstructures of polyacrylamide (PAAm) hydrogels were investigated by static light scattering measurements. The gels were prepared by free‐radical crosslinking polymerization of acrylamide (AAm). To suppress the degree of gel inhomogeneity, the crosslinker reactivity during gelation was controlled by decreasing its availability in the reaction system. Our first approach was the addition of the crosslinker N,N′‐methylenebis(acrylamide) (BAAm) in one or three portions during the course of the gelation reactions. As a second approach, a slightly water soluble crosslinker, namely ethylene glycol dimethacrylate (EGDM) was used as a crosslinker in AAm polymerization. Due to the low water solubility of EGDM, EGDM phase in the gelation system act as a reservoir of crosslinker so that the crosslinker can be supplied continuously to the aqueous reaction zone during the course of gelation. It was found that the delayed crosslinker addition technique further increases the degree of inhomogeneity of PAAm hydrogels. The results were explained with increasing viscosity of the reaction solution at the time of the crosslinker addition so that the crosslinking reactions are limited to local regions in the reaction system. The second approach, namely use of the slightly water soluble crosslinker EGDM significantly increases the degree of structural homogeneity of PAAm hydrogels.     

部分水解聚丙烯酰胺柠檬酸铝体系临界交联浓度的研究

采用落球粘度计、核孔膜过滤、动态光散射 (DLS)和2 7Al NMR法 ,研究了高分子量、低浓度的部分水解聚丙烯酰胺 (HPAM)与柠檬酸铝 (AlCit)体系形成交联聚合物溶液 (LPS)的临界交联浓度 .研究结果表明 ,HPAM AlCit体系在聚合物浓度较低时 ,溶液中主要发生形成交联聚合物线团 (LPC)的交联反应 ,此时形成的是LPS ,聚合物浓度增加到某一临界值后 ,体系中形成线团后 ,存在线团间的交联 ,此时形成的是弱凝胶 .不同方法所测得的HPAM AlCit体系的临界交联浓度基本相同 ,对于粘均相对分子质量为 1 4× 10 7的HPAM ,在NaCl浓度为 2 0 0 0mg L ,交联比 2 0∶1时形成的交联体系 ,其临界交联浓度在 2 0 0～ 30 0mg L间 .     

Chemorheological study of the curing kinetics of a phenolic resol resin gelled

The changes in the resin viscosity, conductivity, mass, and enthalpy during curing reactions have been studied to obtain kinetic parameters that allow modeling of the resin behavior throughout its industrial application. In this work, isothermal rheological tests of a phenolic resol resin were performed in order to study its complex viscosity during crosslinking reactions. Samples were prepared by a precuring treatment in a heated plate press to reach gel point of the resin. Rheological analyses of resol resin curing were carried out at five different temperatures (80-100 °C), and the kinetic models of Arrhenius and Kiuna were applied. The resol resin curing presented an activation energy of 72.1 kJ/mol according to the Arrhenius model. The Kiuna model was proposed to fit the non-linear evolution of the resin’s complex viscosity at the highest temperatures. This kinetic model was suitable for predicting the changes in the complex viscosity of the resol resin after its gelation, and the process activation energy obtained for the second order polynomial applied in this model was 88.1 kJ/mol. In addition, the profile for the degree of curing of resol resin was determined from measurements of the material’s elastic modulus.     

Rheology and morphology of linear polyurethane and poly(methyl methacrylate) blends formed in situ

The rheological properties and morphology of flow during the in situ formation of linear polyurethane and poly(methyl methacrylate) blends of various compositions are studied. At a certain conversion of the components, the initial homogeneous blend undergoes phase separation, as evidenced by the nonadditive dependence of the logarithm of viscosity on blend composition. For individual components, the gel points correspond to appreciably different conversions. For components in blends of various compositions, this difference is less pronounced and associated with the kinetic conditions of blend formation. The morphology of flow of the reaction blend over the time (or conversion) between the onset of phase separation and gelation during flow with a high shear rate is determined by the blend composition and the ratio between the viscosity of the dispersion phase and the matrix.     

Characterization of resulting network polymer precursors in stepwise crosslinking diepoxide/diamine polymerization

Our previous mechanistic discussion of network formation in chainwise crosslinking multiallyl polymerization was extended to stepwise crosslinking diepoxide/diamine polymerization, typically including bisphenol‐A diglycidyl ether (BADGE) and 4,4′‐diaminodiphenylmethane (DDM). In allyl polymerization a monomer chain transfer is an essential termination reaction, providing only oligomeric primary polymer chains. Therefore, crosslinking multiallyl polymerization could be in the category of a classical gelation theory. Thus, the gelation behavior was discussed by comparing the actual gel point with the theoretical one. Then the resulting network polymer precursors (NPPs) were characterized by size‐exclusion chromatography‐multiangle laser light scattering‐viscometry to clarify the stepwise crosslinking BADGE/DDM polymerization mechanism. Notably, the intrinsic viscosity ratio [η]_NPP/[η]_Linear tended to decrease with the progress of crosslinking and finally, it reached less than 0.2. This suggests that the structure of resulting NPP becomes dendritic at a conversion close to the gel point. These dendritic NPPs can collide with each other to form crosslinks between NPPs, eventually leading to gelation as a reflection of the high concentration of NPP. The dilution effect on gelation was marked in polar solvent; no gelation was observed at a dilution of 1/5. However, in nonpolar solvent the gelation was promoted by dilution; this is ascribed to enhanced crosslink formation between NPPs through hydrogen bonding due to abundant hydroxyl groups in the NPP generated by the polyaddition reaction. Finally, the subject of “Is cured epoxy resin inhomogeneous?” is briefly discussed. © 2011 Wiley Periodicals, Inc. J Polym Sci Part A: Polym Chem, 2011     

水解聚丙烯酰胺柠檬酸铝体系成胶行为与形态结构的研究

采用光学显微镜、扫描电镜及流变性能测试等手段 ,研究了部分水解聚丙烯酰胺 (HPAM )与柠檬酸铝 (AlCA)的成胶行为与形态结构 .结果表明 ,当AlCA浓度超过 10 0mg/L时 ,随HPAM浓度由低向高变化 ,HPAM AlCA交联体系可形成三种不同形态结构的凝胶 :分散凝胶 (由交联聚合物颗粒形成的分散体 )、两相(分散凝胶相与连续网状凝胶相 )共存凝胶和连续网状凝胶 .HPAM AlCA形成分散凝胶时 ,无明显的粘度升高现象 ,但体系中存在由HPAM大分子交联在一起的颗粒结构 .HPAM AlCA在形成连续网状凝胶时 ,体系复模量和复粘度大幅度提高 ,网状凝胶中含有粒状凝胶颗粒 .