消除夹带溶胀的新液膜操作法

消除夹带溶胀的新液膜操作法曹汉瑾，褚莹，何彦涛，吴子生，严忠（东北师范大学化学系长春１３００２４）关键词液膜，油／水乳液，溶胀，夹带，包裹消除液膜操作中的夹带溶胀对液膜的工业化具有重要意义，夹带溶胀分为包裹溶胀和再液化溶胀。前者是乳状液滴上浮时将水相...     

明胶-聚异丙基丙烯酰胺水凝胶的溶胀动力学

采用明胶（Gel)和N－异丙基丙烯酰胺（NIPAM）为原料，制备了Gel/聚异丙基丙烯酰胺（PNIPAM）水凝胶系列；研究了原料配比、pH值及温度对水凝胶溶胀速度的影响。结果表明，当温度大于PNIPAM的最低临界溶液温度（LCST）值时，Gel/PNIPAM水凝胶的溶胀速度随着组分中PNIPAM的增加而降低，且溶胀过程以扩散渗透控制为主。而pH对水凝胶溶胀速度的影响与温度有关。Gel/PNIPAM配比为5／5，温度大于LCST时，水凝胶的pH敏感性受明胶控制；温度低于LCST时，pH对水凝胶的溶胀速度的影响很小。     

乙基氰乙基纤维素/交联聚丙烯酸复合物膜的溶胀行为

研究了乙基氰乙基纤维素 [(E CE)C] 交联聚丙烯酸 [PAA]胆甾相液晶复合物膜的厚度以及膜的组成对膜在水中的溶胀行为的影响 .复合物膜越厚则达到溶胀平衡所需要的时间越长 ,但是其最大溶胀率是相同的 .复合物膜的最大溶胀率先是随着 (E CE)C浓度的增加而增加 ,当 (E CE)C的浓度大于 5 1wt%的时候 ,复合物膜的最大溶胀率几乎不再发生变化 .复合物膜的交联密度越大 ,其最大溶胀率越小 ,溶胀速率也随着膜的交联 (点 )密度的增加而减小 .研究还发现复合物膜的交联 (点 )密度越大 ,其溶胀前后最大选择性反射光波长的位移也越小 .     

[SiNi(H2O)W11O39]6-多层组装膜修饰电极及其电化学行为

采用电化学生长法制备包含杂多酸[SiNi(H2O)W11O39]6-(SiNiW11)和聚合物阳离子PDDA的多层膜修饰电极, 利用循环伏安法研究其电化学行为、 pH的影响及其对BrO3-和NO2-体系还原的电催化性能;并对多层膜电化学过程机理进行了初步探讨. 结果表明: 多层膜的增长均匀, 峰电流随层数的增加而增加;多层膜的峰电流随扫速的增加而增加;还原峰的峰电位随pH的增加而负移.     

氢键在煤大分子溶胀行为中的作用

选择对氟苯酚（ＰＦＰ）做为煤中羟基的模型化合物，考察了煤与溶剂间氢键强度对煤大分子溶胀行为的影响。发现煤在溶剂中的溶胀率随着ＰＦＰ与溶剂间氢键生成热的增大而增加；煤的溶胀率随煤化程度的提高而降低以及煤经碱、酸处理后溶胀率增加。这些结果表明，煤中羟基与溶剂间的氢键力是决定煤大分子溶胀行为的关键因素。     

离子键交联的聚两性电解质凝胶在不同pH和不同电解质溶液中溶胀行为研究

以丙烯酸(AA)和甲基丙烯酸二乙氨基乙酯(DEAM)形成的离子复合物与丙烯酰胺(AAm)共聚,合成了一种新型的离子键交联的聚两性电解质凝胶(PADA).由于分子之间的氢键作用,PADA凝胶并不是在A/C(负正离子单体摩尔比)为1,而是在A/C为1.55处有最大消溶胀.与共价键交联的聚两性电解质凝胶相比,PADA凝胶的溶胀行为具有更强的pH敏感性.PADA凝胶在不同pH缓冲溶液中的溶胀行为表明,在pH 3~4之间消溶胀程度最大.在偏离该pH区域时凝胶均发生溶胀.但凝胶的溶胀程度在pH<3的酸性溶液中随A/C的增加而降低;而在pH>4的偏碱性溶液中随其增加而增加.在不同价数的离子溶液中,离子浓度对于PADA凝胶的平衡溶胀有着不同的影响.对于一价的NaCl溶液,PADA凝胶有典型的反聚电解质效应.但对于高价的CaCl2和柠檬酸三钠溶液,只在较低的浓度下,才表现出反聚电解质效应.而在较高盐浓度时,随盐浓度的增加其溶胀比反而降低.这可能与高价离子形成的离子键交联有关.与pH对PADA凝胶溶胀程度的影响相似,在CaCl2溶液中,PADA凝胶的溶胀程度随A/C的增加而降低;而在柠檬酸三钠溶液中则刚好相反.这种独特的溶胀行为似乎与高价离子电荷的正负性有关.     

PVA水凝胶的弹性和溶胀特性研究

采用硼酸与聚乙烯醇化学交联方法制备了聚乙烯醇(PVA)水凝胶,通过对PVA水凝胶的弹性与溶胀性能的研究,优选出交联剂硼酸与聚乙烯醇的最佳配比量;探究温度对PVA水凝胶弹性的影响以及时间、矿化度、温度对PVA水凝胶溶胀特性的影响。结果表明,随硼酸用量的增加,PVA水凝胶的溶胀率与弹性模量值都表现出先增大后减小的特征,当硼酸:PVA=10%时,PVA水凝胶的弹性和溶胀特性均最佳;PVA水凝胶在水溶液中溶胀率随时间的增长逐渐增大,40h后基本达到溶胀平衡;随矿化度的增大而减少,耐矿化度强,在10%盐度水中还能膨胀1倍,适用于高矿化度油藏;耐温性强,随温度的增大变化不大,适用于油藏温度。     

神华抽余煤的溶胀动力学研究

研究了五种神华抽余煤在不同溶剂中的溶胀动力学,考察了溶剂抽提对溶胀性能的影响,探讨了神华抽余煤的溶胀机理.实验结果表明,CS2/NMP混合溶剂抽余煤的溶胀速率随着溶胀温度升高而增大;溶剂抽提对抽余煤的溶胀具有较大影响,其中抽余煤在NMP溶剂中溶胀速率明显大于THN;抽提率越大的抽余煤,溶胀表观活化能越大,溶胀越难进行;两种溶剂中抽余煤溶胀表观活化能均小于10 kJ/mol,表明其溶胀过程由溶剂分子的扩散控制.     

壳聚糖复合膜及异丙醇／水混合液的渗透汽化分离

用磺化聚乙烯离子膜渗透汽化分离恒沸组成的i-PrOH/H_2O(87.2/12.8W/W),分离系数α高,渗透通量J低(小于300g/m~2·h,40℃),当醇含量高于90％时,膜性能变差;用CA膜、赛璐玢膜[2]、Nation-Na~+膜,J较高,α低(<30)。甲壳素脱乙酰基产物壳聚糖(Chitosan,简称CS),易交联改性,成膜性好。CS膜分离i-PrOH/H_2O,α很高,而J低。经戊二醛交联的CS膜尺寸稳定,增加了醇/水的J值,α虽有所下降,对i-PrOH/H_2O体系仍具有很高的值。为了进一步提高J值,我们研制了以聚丙烯腈(PAN)微孔膜作支撑的CS复合膜,     

W0723F的非等温结晶与薄膜加工性能

运用差示扫描量热法(DSC)研究了W0723F和FL7540的非等温结晶行为,降温速率从25℃/min增加到40℃/min,W0723F的结晶半峰宽从9.5变为14.4,而FL7540从8.1变为11.7,W0723F结晶受较大影响,半峰宽变的更宽,结晶变得更缓慢;用Jeziorny法和莫志深法对所得数据进行分析,在相对结晶度为60%时,W0723F和FL7540的F(T)分别为14.05和8.37,W0723F结晶速率低;制膜过程改变冷辊温度,冷辊温度为20℃、40℃时对W0723F的强度和透明性有较大的影响,非等温动力学对制膜工艺参数选择有重要指导意义。     

Fat crystals: A tool to inhibit molecular transport in W/O/W double emulsions

Water-in-oil-in-water (W/O/W) double emulsions are a promising technology for encapsulation applications of water soluble compounds with respect to functional food systems. Yet molecular transport through the oil phase is a well-known problem for liquid oil-based double emulsions. The influence of network crystallization in the oil phase of W/O/W globules was evaluated by NMR and laser light scattering experiments on both a liquid oil-based double emulsion and a solid fat-based double emulsion. Water transport was assessed by low-resolution NMR diffusometry and by an osmotically induced swelling or shrinking experiment, whereas manganese ion permeation was followed by means of T₂-relaxometry. The solid fat-based W/O/W globules contained a crystal network with about 80% solid fat. This W/O/W emulsion showed a reduced molecular water exchange and a slower manganese ion influx in the considered time frame, whereas its globule size remained stable under the applied osmotic gradients. The reduced permeability of the oil phase is assumed to be caused by the increased tortuosity of the diffusive path imposed by the crystal network. This solid network also provided mechanical strength to the W/O/W globules to counteract the applied osmotic forces.     

Osmotic swelling behavior of globules of W/O/W emulsion liquid membranes

The osmotic swelling behavior of water-in-oil-in-water (W/O/W) type emulsion liquid membranes (ELMs) was investigated. Using an optical microscope equipped with a camera, the changes in the size of the W/O/W globules were monitored over a long period of time (up to about 4 h). The osmotic pressure gradient between the internal and external aqueous phases was induced by creating a concentration difference of d-glucose between the two aqueous phases. The results indicate that the swelling ratio, defined as the ratio of globule diameter at time t to globule diameter at t=0, decreases with the increase in ϕ_W/O(0) (initial volume fraction of internal aqueous phase droplets). The swelling ratio generally increases with the increase in the concentration of surfactant present in the membrane (oil) phase. The permeation coefficient of water also increases with the increase in the surfactant concentration. With the increase in ϕ_W/O(0) up to about 0.42, the permeation coefficient decreases only slightly. However, with further increase in ϕ_W/O(0), a sharp reduction in the permeation coefficient occurs. The mechanism of water transfer in ELMs of the present work is reasoned to be the diffusion of hydrated surfactants.     

Swelling determination of W/O/W emulsion liquid membranes

Based on the definition of swelling in emulsion liquid membrane (ELM) process, the concepts of apparent swelling and actual swelling are proposed to illustrate the relationship between the emulsion swelling (the osmotic swelling and entrainment swelling) and the membrane breakage, focussing on the effect of the volume change caused by emulsion swelling and membrane breakage on the experimental results. Theoretical analyses indicate that “zero” or “negative” swelling may occur under certain experimental conditions. A bi-tracer method is further proposed and then used to measure the osmotic, entrainment swelling and the membrane breakage simultaneously, only requiring some initial operation conditions and measurements of concentrations of both tracers in the external and internal phases. It has been experimentally proved that this new method is highly applicable in ELM process and provides a useful tool to specify the effects of membrane breakage, osmotic swelling and entrainment swelling in the same experiment. “Negative” swelling may occur under certain operating conditions, particularly when the electrolyte concentration in the external phase is higher than that in the internal phase. The experimental results also indicate that the effect of membrane breakage on the measurement of emulsion swelling should not be neglected to avoid measurement error. Polymeric surfactant LMA is superior to other commercial surfactants as it imparts high membrane stability and small emulsion swelling.     

Demulsification of water-in-oil emulsions by permeation through Shirasu-porous-glass (SPG) membranes

To investigate the effect of the droplet/pore size ratio on membrane demulsification, water-in-oil (W/O) emulsions with uniform-sized droplets was demulsified by permeation through Shirasu-porous-glass (SPG) membranes with a narrow pore size distribution at mean droplet/pore diameter ratios of 0.52–5.75. At transmembrane pressures above a critical pressure, the water droplets larger than the membrane pore size were demulsified, where the SPG membrane acted as a coalescer because the hydrophilic membrane surface had a high affinity for the water droplets. By contrast, at transmembrane pressures below the critical pressure, the larger water droplets were all retained by the membrane due to the sieving effect of the uniform-sized pores. When a W/O emulsion with a mean droplet diameter of 2.30 μm was allowed to permeate through a membrane with a mean pore diameter of 0.86 μm, the demulsification efficiency increased with increasing transmembrane pressure, to a maximum value of 91% at a transmembrane pressure of 392 kPa, and then decreased, while the transmembrane flux increased almost linearly with increasing transmembrane pressure. The demulsification efficiency was higher for higher water phase content and lower concentration of the surfactant, tetraglycerin condensed ricinoleic acid ester, in the emulsions due to the reduction of the emulsion stability.     

Preparation of highly monodisperse W/O emulsions with hydrophobically modified SPG membranes

Experimental investigations on the hydrophobic modification of SPG membranes and the preparation of monodisperse W/O (water-in-oil) emulsions using the modified membranes were carried out. Effects of the osmotic pressure of disperse phase, the average pore size of membranes, emulsifier concentrations in continuous phase and the transmembrane pressure on the average size, size distribution and size dispersion coefficient of emulsions were systematically studied. The stability of W/O emulsions was also investigated. The results showed that SPG membranes took on excellent hydrophobicity through the modification by silane coupler reagent (octyltriethoxysilane) or by silicone resin (polymethylsilsesquioxane). Monodisperse W/O emulsions with size dispersion coefficient of about 0.25, which meant high monodispersity, were successfully prepared by using the hydrophobically modified SPG membranes with average pore sizes of 1.8, 2.0, 2.5, 4.8 and 11.1 microm. When the osmotic pressure was lower than 0.855 MPa, the average size of emulsions was gradually increased while the size dispersion coefficient delta gradually decreased with the osmotic pressure; when the osmotic pressure was higher than 0.855 MPa, both the coefficients kept unvarying. When kerosene was saturated with disperse phase in advance, the average size of emulsions became larger and the monodispersity of emulsions was slightly better than that prepared using unsaturated kerosene. The smaller the pore size of SPG membranes was, the better the monodispersity of the W/O emulsions. The average size and size dispersion coefficient delta were nearly independent on the emulsifier concentrations when the PGPR concentration was in the range from 0.5 to 5.0 wt%, whereas both of them slightly increased as the PGPR concentration was below 0.5 wt%. The effect of the transmembrane pressure on size distributions was slight. Both the average size and size dispersion coefficient delta slightly increased to some extent with the increase of the transmembrane pressure in the experimental range. The stability of the W/O emulsions was dependent on the storage time. The mean size of W/O emulsions decreased gradually with the increase of storage time at the first 35 days, and then kept constant; while the size dispersion coefficient of W/O emulsions was nearly not changed.     

A review of: “Nineteenth Century Attitudes: Men of Science (Chemists and Chemistry Series,Vol. 13)”. Sydney Ross. Kluwer Academic Publishers; Dordrecht, 1991. pp. xi+235. $69.00.

Abstract

The potential of polytetrafluoroethylene (PTFE) membranes as water‐in‐oil (W/O) emulsification devices was investigated to obtain uniformly sized droplets and to convert them into microcapsules and polymer particles via subsequent treatments. Uniform W/O emulsion droplets have not been achieved using glass membranes unless the membrane was rendered hydrophobic by treatment with silanes. If a PTFE membrane is capable of providing uniform droplets for a W/O emulsion, a coordinated membrane emulsification system can be established since glass membranes have been so successful for O/W (oil‐in‐water) emulsification. In order to examine the feasibility of PTFE membrane emulsification, O/W and W/O emulsion characteristics prepared using PTFE membranes were compared with those prepared by the conventional SPG (Shirasu porous glass) membrane emulsification method. A 3 wt.% sodium chloride solution was dispersed in kerosene using a low HLB surfactant. Effects of the membrane pore size, permeation pressure, and the type of emulsifiers and concentration on the droplet size and on the size distribution (CV, coefficient of variation) were investigated. The CV of the droplets was fairly low, and the average droplet size was correlated with the critical permeation pressure of the dispersed phase, revealing that the PTFE membrane could be used as a one‐pass membrane emulsification device. Low CV values were maintained with a Span 85 (HLB = 1.8) concentration, 0.2–5.0 wt.% and a range of HLB from 1.8–5.0. For a brief demonstration of practical applications, nylon‐6,10 microcapsules prepared by interfacial polycondensation and poly(acrylamide) hydrogels from inverse suspension polymerization are illustrated.     

Preparation and characterization of W/O/W double emulsions containing MgCl2

The aim of present study is to design food-grade W/O/W double emulsions encapsulating Mg²⁺ and investigate their stability and release properties. Prepared emulsions were characterized in terms of global stability, particle size, rheological properties, and interfacial tension. The double emulsions were sensitive to the presence of magnesium salt. The mean droplet size and viscosity of emulsions was positively correlated to MgCl₂ concentration. The microscopic pictures confirmed that the water transfer between two aqueous phases caused the reduced stability of double emulsions. It was suggested that swelling breakdown was the main mechanism in controlling the release of encapsulated Mg²⁺.     

Stability of W/O Emulsions Encapsulating Polysaccharides

In the frame of formulation of W/O emulsions entrapping polysaccharides devoted to agricultural applications, the aim of this work was to study the stability over time of these emulsions, stabilized with either soybean lecithin or polyglycerol polyricinoleate (PGPR) as emulsifiers. Emulsifiers were dissolved in oil phase, and polysaccharides (carboxymethycellulose (CMC), guar, xanthan) in ultrapure water. Emulsions stability was studied through natural aging tests and accelerated aging tests, using bottle tests, microscopy and calorimetry. Experiments showed that PGPR was more efficient than lecithin to stabilize emulsions containing the polysaccharides studied, and that emulsions prepared with CMC showed the best stability.     

酯化淀粉乳化剂制备的高效氯氟氰菊酯O/W乳液的稳定机制

通过测定辛烯基琥珀酸淀粉钠的用量、盐离子、pH值和温度等因素对油滴Zeta电位及表面吸附量的影响,分析了以酯化淀粉辛烯基琥珀酸淀粉钠为乳化剂制备的5％高效氯氟氰菊酯水乳剂的稳定机制.结果表明,辛烯基琥珀酸淀粉钠质量分数为7％时,Zeta电位达到最大值,油滴表面吸附量接近饱和;Na+、Mg2+和Al3+压缩油滴表面的双电层,降低Zeta电位,削弱静电排斥作用,增加辛烯基琥珀酸淀粉钠分子柔性,提高辛烯基琥珀酸淀粉钠表面吸附量,且随着Na+、Mg2、Al3+离子强度依次增大,压缩双电层能力依次增强,Zeta 电位降低和表面吸附量增加程度依次增大;pH值影响辛烯基琥珀酸淀粉钠在水中的解离,在碱性范围内解离出较多羧酸根,静电排斥力较大,Zeta电位较高,但表面吸附量有所降低;温度升高,辛烯基琥珀酸淀粉钠在水溶液中溶解度增大,呈舒展状态,且辛烯基琥珀酸淀粉钠从油滴表面逃逸的趋势增加,油滴表面Zeta电位和表面吸附量均随着温度升高而降低,在低温区差别不大,温度越高二者变化越明显.辛烯基琥珀酸淀粉钠通过吸附于油滴表面为其提供较强的静电斥力和空间位阻作用而维持O/W乳液稳定.     

用混合乳化剂UE20/PVA制备的水包油型生漆乳液的性能

以漆酚基乳化剂(UE20)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), 研究了UE20与PVA的质量比、混合乳化剂质量分数(wME)、水与天然生漆(RL)的质量比、温度和贮存时间对RLE性能的影响, 并用透射电镜观察了wME对RLE粒子的大小及形态的影响. 结果表明, RLE的黏度随着PVA的增加而增大; 当wME≤6.7%时, RLE表现出假塑性流体的特征, 其黏度随着wME的增大而增大, 乳液的稳定性增强; 而当wME≥10.0%时, RLE则表现出膨胀型流体的特征, 乳液的黏度较低; 随着温度的升高及水的用量增加, RLE粒子间相互作用减弱, 乳液的稳定性降低. 正交实验结果表明, 影响RLE的黏度及稳定性的顺序为wME＞mH2O∶mRL＞mUE20∶mPVA＞乳化温度. 随着wME的增大, RLE粒子的粒径减小, 其形态也由不规则的形状转变为球形粒子.