漆酚基乳化剂对水包油型生漆乳液流变行为的影响

以漆酚基乳化剂(UE)和聚乙烯醇(PVA)为混合乳化剂制备了水包油(O/W)型生漆乳液(RLE),用RHEOMETER(R/S)对RLE的流变性进行了研究.讨论了UE10浓度(cUE10)、混合乳化剂浓度(cME)、UE的结构对RLE流变性的影响.结果表明,RLE的黏度随着cUE10的增加而增大,用不同cUE10制备的RLE都有剪切变稀的特性,表现出假塑性流体的行为;当cME≤6.7%,RLE表现出假塑性流体的行为,而当cME≥10.0%,RLE则表现出膨胀型流体的特征;用不同UE制备的RLE均表现出假塑性流体的特征,其流变行为符合Herschel-Bulkley模型,随着UE分子中聚氧乙烯链的增长,RLE的黏度增大,RLE粒子间所形成的某种静态空间网状结构强度增强.     

P(MMA-co-AA)乳液的制备及pH响应特性

以过硫酸钾(KPS)为引发剂、十二烷基硫酸钠(SDS)为乳化剂,利用正相乳液聚合制备(甲基丙烯酸甲酯-co-丙烯酸)共聚物(P(MMA-co-AA))乳液.通过测定聚合转化率和观察聚合过程稳定性,探讨了AA与MMA不同质量比时制备稳定的共聚物乳液的工艺条件;通过黏度法测定了乳液在不同pH时的相对黏度η,利用粒度分析仪分析了乳胶粒子在不同pH时的平均粒径和粒径分布.结果表明:AA含量较高时,控制聚合时间是得到稳定聚合物乳液的关键,当m(AA)/m(MMA)=12.5/100,65 ℃下反应120 min时,所制得的乳液稳定性最好.随着pH增大,乳液黏度先增大后降低;随着m(AA)/m(MMA)增加,制得的乳液pH敏感性增大;随着乳液从酸性(pH=5.17)变到碱性(pH=8.61),聚合物乳胶粒子平均粒径减小,粒径分布变窄.     

氧化还原低温引发MMA/BA超浓乳液薄层共聚合的研究

以甲基丙烯酸甲酯-丙烯酸丁酯(MMA-BA)作为混合单体、以乳化剂十二烷基硫酸钠(SDS)和共乳化剂十六烷醇(CA)作为复合乳化剂体系、聚乙烯醇(PVA)为液膜增强剂,制备了稳定的超浓乳液.以过氧化二苯甲酰(BPO)和N,N′-二甲基苯胺(DMA)为氧化还原引发体系,用一种新的超浓乳液薄层技术,在较低温度下引发共聚合.探讨了液膜增强剂种类和聚合环境对聚合稳定性影响;研究了薄层厚度,薄层面积,聚合温度和加热方式对体系(包括单体和水)挥发性和转化率的影响.比较了薄层和试管聚合的速率.用透射电子显微镜观察了水浴与烘箱加热方式下聚合物乳胶粒的形态,得到了在水浴中反应后的聚合物粒子平均粒径和分散度都减小的结果.     

氧化-还原低温引发甲基丙烯酸甲酯/丙烯酸丁酯超浓乳液聚合研究

以乳化剂十二烷基硫酸钠 (SDS)和共乳化剂十六烷醇 (HD)作为复合乳化体系 ,过氧化二苯甲酰(BPO)和N ,N 二甲基苯胺 (DMA)作为氧化还原引发体系 ,甲基丙烯酸甲酯 丙烯酸丁酯 (MMA BA)作为混合单体 ,制备了分散相占 83 %以上的稳定的超浓乳液 ,然后在低温下引发聚合 .探讨了引发剂浓度、氧化剂与还原剂的摩尔比、乳化剂的浓度、液膜增强剂的种类、聚合温度等因素对聚合稳定性和聚合速率的影响 ,测定并计算得到了聚合速率的公式 ;用激光散射粒度分布仪测定了聚合物乳胶粒子的大小及粒径分布 ,用透射电子显微镜观察了聚合物乳胶粒的形态 ,讨论了乳化剂浓度、聚合温度等对乳胶粒形态、大小的影响     

含氟/硅丙烯酸酯核壳型乳液的合成及性能

采用半连续种子乳液聚合法, 在十二烷基硫酸钠(SDS)/辛基苯基聚氧乙烯醚(TX-10)复合乳化剂的作用下, 合成了以丙烯酸丁酯(BA)为核, 以甲基丙烯酸甲酯(MMA)、甲基丙烯酸十二氟庚酯(DFHMA)、3-(甲基丙烯酰氧)丙基三甲氧基硅烷(MPTMS)和甲基三甲氧基硅烷(MTMS)为壳的核壳型含氟/硅丙烯酸酯聚合物乳液. 利用FTIR, TEM, SEM-EDX和DSC等手段对乳液组成、乳胶粒子结构、膜表面及断面形态等进行了表征, 讨论了氟/硅含量对聚合物膜性能的影响. 结果表明, 核-壳粒子尺寸为20~30 nm, 乳液膜的性能与膜表面氟和硅的含量及相容性有较大的相关性, 当m(氟)∶m(硅单体)=3∶1时, 形成的膜均匀透明, 吸水率较低, 尺寸稳定性较好.     

复合微乳液聚合制备P(MMA-UA)纳米乳胶粒子的研究

将聚氨酯预聚体可聚合乳化剂 (APUA)和甲基丙烯酸甲酯 (MMA)的复合微乳液体系 ,分别用水溶性过硫酸钾 (K2 S2 O8)和油溶性偶氮二异丁腈 (AIBN)作引发剂 ,进行微乳液聚合研究 ,制备了P(MMA UA)复合纳米乳胶粒子 .研究了APUA用量、聚合温度对聚合动力学的影响 ;用透射电子显微镜 (TEM)观察了不同乳化剂浓度及引发剂体系对胶粒形态、大小及分布的影响 .结果表明 ,用可聚合乳化剂APUA可制得稳定性很好的P(MMA UA)纳米级核 壳型乳胶粒子 ,乳胶粒径在 5 0nm左右 .随着乳化剂用量增加 ,粒子变小 ;不同类型的引发剂对胶乳的性质有较大影响 ,以APUA为乳化剂 ,K2 S2 O8为引发剂 ,在聚合反应过程中或在聚合反应后的放置中 ,会出现P(MMA UA)的纳米水凝胶 (Nanogel)现象 .     

高固含量丙烯酸酯的微乳液聚合

采用半连续滴加预乳液的微乳液聚合法,合成出聚合物质量分数40%、乳化剂质量分数2.5%的丙烯酸酯微乳液. 考察了单体滴加速度、乳化剂种类及其用量、电解质用量、温度和搅拌等因素对乳液粒径及性能的影响. 研究表明,聚合在相当于Winsor-Ⅰ型的聚合体系中进行,由纯单体相(滴入的单体)和O/W微乳相构成,上层单体只起储存库的作用,它在缓慢的搅拌帮助下扩散进入微乳相中,只要微乳液液面上补加的单体不扰动微乳液的平衡,即不会产生粗粒子. 单体滴加时间控制在4 h,选择质量分数为2.5%的Dowfax2A1/OP-10乳化体系,NaHCO3质量分数为0.16%,反应温度控制在75～80 ℃,搅拌速度控制在150 r/min,可使聚合反应平稳进行,得到了m(聚合物)∶m(乳化剂)=15∶1的丙烯酸酯微乳液.     

苯丙乳液合成反应条件优化

以苯乙烯、丙烯酸、丙烯酸丁酯、甲基丙烯酸甲酯等为单体,采用乳液聚合制备了苯丙乳液,研究了合成温度、引发剂用量、乳化剂用量、功能性单体丙烯酸用量等反应条件对苯丙乳液性能的影响,并探讨了丙烯酸单体对乳液耐酸碱稳定性的影响,确定了合成反应条件.结果表明,随着合成温度的提高,混合单体的转化率迅速增加,78℃时转化率最大(达到97.1%),而后随温度继续提高基本保持不变.混合单体转化率随过硫酸钾引发剂用量的增加呈现先增加后逐渐降低的趋势,当过硫酸钾与混合单体质量比为0.010时转化率最大,此时单体转化完全.此外,随着乳化剂用量增加,乳液的外观、钙离子稳定性、凝胶等性能都有所提高,但吸水率也相应增加.最佳合成反应条件为:合成温度为78℃,混合单体组成为15g苯乙烯、2g丙烯酸、18g丙烯酸丁酯、8g甲基丙烯酸甲酯,引发剂和乳化剂与单体质量比分别为0.010和0.035.得到的苯丙乳液在酸性条件下具有良好的稳定性.     

高固含量低黏度聚氨酯微乳液的制备及性能研究

以聚(四氢呋喃-co-氧化丙烯)二醇(Ng210)为软段,异佛尔酮二异氰酸酯(IPDI)为硬段,以1,2-二羟基-3-丙磺酸钠(DHPS)和二羟甲基丙酸(DMPA)作为亲水扩链剂,采用自乳化法合成了一系列了高固含量低黏度稳定聚氨酯微乳液,分析了DHPS和DMPA质量配比对乳液性能的影响,结果表明,所得乳液粒径呈多元分布,乳胶粒子呈球形;乳液为假塑性流体,表观黏度小于250mPa.s(剪切速率为25s-1)且随切变速率的变化规律呈现一定的切力变稀特征;随着DHPS/DMPA比值的增大,胶粒平均粒径逐渐减小,多分散性增强;当DHPS/DMPA值为4/10～6/10时,乳液中大小粒子粒径比为6～8,且大乳胶粒子的体积分数约为70%～75%,乳液的固含量均大于70%.另外,乳液具有较好的低温和高温以及贮存稳定性,具有较低的表面张力,相对于常规的聚氨酯乳液,所制备的高固含量聚氨酯乳液胶膜具有更好的力学性能.     

有机硅-丙烯酸酯聚合物乳液合成及粒径分析

通过种子乳液半连续法合成了有机硅改性丙烯酸酯聚合物乳液,并对其粒子形态及分布进行分析。结果表明:通过种子乳液半连续聚合工艺可制备出固含量42wt%,乳化剂含量4wt%(基于单体量)、窄分布纳米粒子的有机硅改性丙烯酸酯聚合物乳液。随反应进行,粒径分布变窄,平均粒径逐渐增大。随乳化剂中SDS与OP-10的摩尔比减少,粒径增大。     

Phase Transitions in Emulsions Formed by Aqueous Emulsifier and its Action on Improving Mobility in Oil Recovery

Transition from oil-in-water (O/W) emulsions to water-in-oil (W/O) emulsions and its action on enhanced oil recovery was investigated by viscosity, morphology, and simulated flooding experiments. This transition can be realized by increasing the volume ratio of oil to water or decreasing the emulsifier concentration. At a mass concentration of 0.3 wt%, the self-developed emulsifier FJ-1 mainly forms O/W emulsions at a volume ratio (oil to water) of 1:1. The emulsions behave as O/W emulsions with a low viscosity when the volume ratio of oil to water is below 2:1. Above 2:1, increasing volume ratio leads to the O/W emulsions transferring into W/O emulsions with high viscosity. For example, at a volume fraction of 4:1, the viscosity of W/O emulsions reaches 229.1 mPa · s, and separated water can hardly be detected. Transition from O/W emulsions to W/O emulsions with high viscosity can also be realized by decreasing the concentration of emulsifier to 0.05 wt% or lower at a volume ratio of 1:1. These may be the critical factors leading to transition from O/W emulsions to W/O emulsions at core conditions. Simulated flooding experiments show that emulsifier fluids can act as an in situ mobility improver and make an improvement of oil recovery even by 20.4%. The results indicate that the water-in-crude-oil emulsions possess great potential in enhancing oil recovery.     

Comparison of the preparation of PLGA–BSA nano- and microparticles by PVA, poloxamer and PVP

The objective of our study was to prepare nano- and microparticles economically considering some practical parameters such as size and encapsulation efficiency as well as ability of particle recovery. Bovine serum albumin (BSA) model protein was encapsulated by poly(d,l-lactide-co-glycolide) (PLGA) using a multiple water-in-oil-in-water emulsion-solvent evaporation technique. The effect of three surfactants: polyvinyl alcohol, poloxamer, and polyvinyl pyrrolidone, used in the outer water phase, on the properties of particles was investigated. The emulsifier/PLGA mass ratio played an important role in the preparation procedure of the particles. This ratio was found to be approximately 1 for polyvinyl alcohol (PVA) if the aim was to formulate nanoparticles with narrow size distribution (<220 nm), high yield and good encapsulation efficiency (>90%). Although, a ratio of 2:1 was sufficient to produce submicron particles by poloxamer with high yield, more than 70% and 90% encapsulation efficiency required minimum 4 and 10 emulsifier/PLGA mass ratio, respectively. Five times more PVA and 10 times more poloxamer than the PLGA mass were necessary to obtain nanoparticles which were easy to redisperse after centrifugation. Microparticles released more BSA than nanoparticles prepared by PVA, however, the situation was reverse with poloxamer. Microparticles formulated by polyvinyl pyrrolidone (PVP) showed the fastest in vitro release.     

水性环氧复合乳化剂的合成及性能

以环氧树脂E-44、2-氨基-5-磺酸基苯甲酸、乙二醇丁醚和正丁醇为原料,合成一种新型阴离子环氧乳化剂EP-D;同时,E-44和聚乙二醇(PEG6000)以摩尔比2∶1反应,合成端环氧基非离子环氧乳化剂EP-PEG;将EP-D与EP-PEG按不同质量比复配获得不同配比的EP-D/EP-PEG水性环氧复合乳化剂。 分别研究了EP-D/EP-PEG及EP-PEG在环氧树脂中加入质量分数为6%~12%时的乳化性能及形成乳液的表面张力、电导率和胶粒的Zeta电位、粒径。 结果表明,当EP-D和EP-PEG以质量比3∶5复配,总加入质量分数为9%时,制备的环氧乳液性能最佳。 与EP-PEG形成的环氧乳液相比,复配环氧乳化剂用量少,乳液铺展性好、稳定性高,且乳液在相反转时的固含量提高了10%以上。 复配环氧树脂乳液中胶粒的Zeta电位为-41.9 mV、粒径为342 nm、表面张力为25.5 mN/m、粘度为14 mPa·s。 这表明利用乳化剂EP-D与EP-PEG复配新合成的EP-D/EP-PEG水性环氧复合乳化剂可制备稳定性好,固含量高的乳液。     

Preparation of electrospun chitosan/poly(vinyl alcohol) membranes

Electrospinning of chitosan from its solutions in 2% aqueous acetic acid was studied by adding poly(vinyl alcohol) (PVA) as a “guest” polymer. Properties of the chitosan/PVA solutions including viscosity, conductivity, and surface tension were measured, and effects of the polymer concentration, chitosan/PVA mass ratio and processing parameters (applied voltage, flow rate, capillary-to-collector distance) on the electrospinnability of chitosan/PVA were investigated. Analyses of scanning electron micrographs and transmission electron micrographs suggested that the chitosan/PVA ultrafine fibers were often obtained along with beads, and chitosan was located in the elctrospun fibers as well as in the beads. Uniform chitosan/PVA fibers with an average diameter of 99 ± 21 nm could be prepared from a 7% chitosan/PVA solution in 40:60 mass ratio. Results of Fourier transform infrared spectroscopy and X-ray diffraction demonstrated that there were possible hydrogen bonds between chitosan and PVA molecules, which could weaken the strong interaction in chitosan itself and facilitate chitosan/PVA electrospinnability. The electrospun chitosan/PVA membranes showed higher water uptake and would have potential applications in wound dressings.     

INTERACTION OP POLYVINYL ALCOHOL WITH LECITHIN AT THE AIR/WATER AND OIL/WATER INTERFACES AND ITS EFFECT ON EMULSION STABILITY

The interaction of polyvinyl alcohol (PVA) with lecithin films at the air/water and xylene/water interfaces was studied at pH 3, the isoelectric point of lecithin. Surface and interfacial tension measurements and electro-phoretie mobility data showed that PVA either replaces the lecithin molecules or becomes coadsorbed with it at the interface. This mixed film has no elasticity and very low interfacial viscosity. However, coalescence rate measurements showed that the emulsion formed by the polymer* lecithin is more stable than that formed with either polymer or lecithin alone. The enhanced stability by the PVA-lecithin mixed film was attributed to steric interaction produced by the adsorbed polymer.     

高固含量低粘度P(MMA/BA/AA)乳液的制备及性能研究

先利用半连续种子乳液聚合法制备固含量为50%,粒径480nm的单分散甲基丙烯酸甲酯(MMA)、丙烯酸丁酯(BA)与丙烯酸(AA)的共聚物种子乳液;然后以上述种子乳液为介质,十二烷基硫酸钠为乳化剂,碳酸氢钠为缓冲剂,过硫酸铵为引发剂制备固含量72%,乳胶粒具有二元分布特征的高固含量、低粘度稳定乳液:其中大乳胶粒径500～600nm,小乳胶粒径约80nm.所得乳液中乳化剂总含量为聚合物质量的2.1%;粘度在剪切速率为21s-1时为400mPa·s.另外,相对于常规乳液,所制备高固含量乳液胶膜具有更好的光泽度.     

Micelle-like particles based on self-assembly of rod-like FPEEK and coil-like PVA

The self-assembly of a rod-like polymer [hydroxyl-terminated trifluoromethylphenyl-substituted fluorinated poly(ether ether ketone) (FPEEK)] and a coil-like polymer (polyvinyl alcohol, PVA) in water has been studied. It was found that this polymer pair could form micelle-like particles. Hydrogen bonding between the hydroxy groups of rod-like FPEEK and coil-like PVA, and parallel packing of the rod-like FPEEK are the main factors affecting the formation of micelle-like particles. Over a broad range, when the FPEEK/PVA mass ratio or the tetrahydrofolate/H₂O volume ratio is decreased, the diameter of micelle-like particles is decreased. The diameters (around 250 nm) of micelle-like particles measured by scanning electron microscopy and dynamic light scattering are similar, but are different from that measured by transmission electron microscopy (around 150 nm). Thus, it can be concluded that micelle-like particles have a core–shell structure and the cores of micelles are composed of FPEEK, and that the shells of micelles are composed of PVA. When polyethylene glycol was used instead of PVA, micelle-like particles were also formed, but the average diameter was bigger than that of the particles formed by PVA and FPEEK. This work was supported by the National Nature Science Foundation of China (50203004).     

Different viscosity grade sodium alginate and modified sodium alginate membranes in pervaporation separation of water + acetic acid and water + isopropanol mixtures

Different viscosity grade sodium alginate (NaAlg) membranes and modified sodium alginate membranes prepared by solution casting method and crosslinked with glutaraldehyde in methanol:water (75:25) mixture were used in pervaporation (PV) separation of water+acetic acid (HAc) and water+isopropanol mixtures at 30 °C for feed mixtures containing 10–50 mass% of water. Equilibrium swelling experiments were performed at 30 °C in order to study the stability of membrane in the fluid environment. Membranes prepared from low viscosity grade sodium alginate showed the highest separation selectivity of 15.7 for 10 mass% of water in the feed mixture, whereas membranes prepared with high viscosity grade sodium alginate exhibited a selectivity of 14.4 with a slightly higher flux than that observed for the low viscosity grade sodium alginate membrane. In an effort to increase the PV performance, low viscosity grade sodium alginate was modified by adding 10 mass% of polyethylene glycol (PEG) with varying amounts of poly(vinyl alcohol) (PVA) from 5 to 20 mass%. The modified membranes containing 10 mass% PEG and 5 mass% PVA showed an increase in selectivity up to 40.3 with almost no change in flux. By increasing the amount of PVA from 10 to 20 mass% and keeping 10 mass% of PEG, separation selectivity decreased systematically, but flux increased with increasing PVA content. The modified sodium alginate membrane with 5% PVA was further studied for the PV separation of water+isopropanol mixture for which highest selectivity of 3591 was observed. Temperature effect on pervaporation separation was studied for all the membranes; with increasing temperature, flux increased while selectivity decreased. Calculated Arrhenius parameters for permeation and diffusion processes varied depending upon the nature of the membrane.     

Pervaporation separation of water + isopropanol mixtures using novel nanocomposite membranes of poly(vinyl alcohol) and polyaniline

Novel nanocomposite polymeric membranes containing nanosized (30–100 nm) polyaniline (PANI) particles dispersed in poly(vinyl alcohol) (PVA) were prepared and used in the pervaporation separation of water–isopropanol feed mixtures ranging from 10 to 50 mass% of water at 30 °C. Of the three nanocomposite membranes prepared, the membrane containing 40:60 surface atomic concentration ratio of PANI:PVA produced the highest selectivity of 564 compared to a value of 77 observed for the plain PVA membrane. Flux of the nanocomposite membranes was lower than those observed for the plain PVA membrane, but selectivity improved considerably. Membranes were characterized by differential scanning calorimetry, dynamic mechanical thermal analyzer, X-ray photoelectron spectroscopy, Fourier transform infrared spectroscopy and scanning electron microscopy. The highest selectivity with the lowest flux was observed for 10 mass% water containing feed mixture. Flux increased with increasing amount of water in the feed, but selectivity decreased considerably. These results were attributed to the acid-doped PANI particles in the PVA membrane as a result of change in the micromorphology of the nanocomposite membranes. In addition, molar mass between cross-links and fractional free volume of the membranes are responsible for the varying membrane performance. Temperature effect on permeability was investigated for 10 mass% water containing feed with the membrane containing higher concentration of PANI particles, the presence of which could be responsible for varied effect of water permeation through the membrane. Membranes of this study could remove as much as 98% of water from the feed.