单分散PS/SiO_2纳米复合微球的制备与表征

采用一种简单和低成本的方法制备单分散SiO2包覆聚苯乙烯(PS)(PS/SiO2)核-壳型纳米复合微球.首先在聚乙烯吡咯烷酮(PVP)存在下制备了PS纳米微球,然后在NH4OH/乙醇溶液中通过溶胶-凝胶过程在PS微球表面包覆SiO2.PS纳米微球的制备在水介质中进行,无需使用共单体,使用的是常用的过硫酸钾自由基引发剂;包覆处理前不用进行溶剂交换或离心处理.研究了PVP,NH4OH和原硅酸乙酯(TEOS)的用量对PS/SiO2纳米复合微球尺寸和形态的影响.随着PVP用量增加,PS微球变小,因此得到较小的PS/SiO2纳米复合微球;NH4OH用量对SiO2包覆层的厚度没有影响,但对SiO2包覆层的表面形态有影响,随着NH4OH用量增加包覆层表面变得粗糙;随着TEOS溶液用量增加,生成的SiO2增加,其包覆层的厚度增加.     

二氧化硅/聚苯乙烯单分散性核/壳复合球的制备

采用无皂乳液聚合包覆 ,制备了二氧化硅 聚苯乙烯单分散核 壳 (SiO2 PS)复合颗粒 ,包覆层厚度达到 10 0nm .选择 80～ 2 5 0nm二氧化硅粒径作为核颗粒 .为提高包覆效率 ,二氧化硅颗粒先用偶联剂甲基丙烯酰 (3 三甲氧基硅烷 )丙酯 (MPS)进行不同程度的表面改性 .控制MPS的结合率和单体的初始浓度可提高包覆效率 ,同时得到了单分散性复合颗粒 ,用透射电镜 (TEM)观察复合粒子的核 壳形态 .用动态光散射法 (DLS)测量表明所得复合颗粒具有单分散性 .     

SiO2 /Au核壳结构纳米粒子的制备及表征

通过以金纳米粒子为表面晶种和壳生长的方法制备了金纳米壳包覆二氧化硅的复合纳米粒子。采用TEM 和UV-Vis对复合粒子进行了表征和研究，结果表明所得到的复合粒子粒径均匀、金纳米壳光滑完整，且壳厚度可通过反应物的用量来控制。当核半径与壳厚度之比在4到13之间变化时,复合粒子的光学共振峰在可见光区到近红外光区范围内可发生大于500 nm波长的移动。     

核/壳纳米复合粒子填充聚苯乙烯的流变行为

采用细乳液聚合制备了以偶联剂改性纳米二氧化硅粒子(SiO2)为核、交联聚苯乙烯(PS)为壳的SiO2@PS复合纳米粒子(SCCSN).采用透射电子显微镜(TEM)、动态光散射(DIS)法考察了SCCSN的粒子形貌特征,发现SCCSN呈球形,粒径约90 nm,均匀分散;采用热失重(TG)、调制式差示扫描量热(MDSC)与动态力学分析(DMA)研究了SCCSN的结构特征,发现PS包覆率随交联剂含量增加而升高,且玻璃化转变温度(Tg)显著升高.交联壳层不仅能够将聚合物锚固在SiO2表面,屏蔽SiO2粒子与基体PS间相互作用,而且阻止PS壳层与基体PS分子链间的缠结.MDSC结果显示,SiO2与SCCSN填充可降低复合物Tg.动态流变结果表明,填充PS熔体非线性流变行为与PS分子链解缠结有关,SiO2与SCCSN均不影响填充熔体非线性流变机理.SCCSN的SiO2核对PS的增强效应略优于SiO2,且增强效应与壳层交联度有关.     

反应介质pH值和前驱体用量对PSt/TiO_2复合微球结构形态及TiO_2空心微球形貌的影响

首先用聚乙烯亚胺(PEI)对粒径为360 nm的单分散无皂聚苯乙烯(PSt)乳胶粒进行修饰,得到表面荷正电的PSt种子乳液,然后将其滴加到溶有钛酸正丁酯(TBT)的乙醇与水的混合介质中,通过溶胶-凝胶(sol-gel)法制备出了核壳结构PSt/TiO2复合微球,系统研究了体系pH和TBT用量对复合微球结构形态的影响.研究表明,酸性条件不利于核壳结构PSt/TiO2复合微球的形成;当体系pH值为7.2时,可得到包覆完整、TiO2壳层厚度均一的PSt/TiO2复合微球,此后随着体系pH值的升高,包覆厚度逐渐提高;当pH值升高到11.0时,壳层厚度达到最大,但出现了包覆层不完整的复合微球.在固定聚合体系pH为8.5,EtOH/H2O质量比为100/6,表面修饰PSt种子乳液用量为0.5 g(固含量为4%)的条件下,随着TBT用量从0.01 g增加到0.16 g,复合微球壳层厚度从约0 nm逐渐增加到60 nm;当TBT用量增加到0.32 g时,壳层厚度迅速降至12nm,微球表面变得粗糙,并出现大量未包覆微粒;此后随着TBT用量的增加,包覆层厚度逐渐减少,未包覆微球逐渐增多.结果显示,当复合微球中TiO2包覆层达到一定厚度时,经煅烧后才能得到形貌完整的TiO2中空微球.     

SiO2/聚甲基丙烯酸叔丁酯核壳复合微粒的制备与表征

以甲基丙烯酸-3-(三甲氧基硅基)丙酯(MPS)修饰的SiO2胶体粒子为种子,甲基丙烯酸叔丁酯(tBMA)为单体、十二烷基硫酸钠(SDS)为乳化剂,采用种子乳液聚合法制备了SiO2/聚甲基丙烯酸叔丁酯的核壳复合微粒。微粒经水解后形成具有pH敏感性的无机/有机复合微粒。研究了影响核壳复合微粒形态结构的因素,结果发现,控制SiO2种子乳液的质量分数在1.5%～2%,可避免聚合过程中生成纯聚甲基丙烯酸叔丁酯乳胶粒子;反应体系中乳化剂SDS的用量超过质量分数0.3%时,易形成纯聚合物乳胶粒子;SDS用量低于质量分数0.15%时,生成的核壳复合微粒易产生团聚;单体和交联剂用量升高,核壳复合微粒的壳层厚度增加,用量过高会导致核壳复合微粒出现团聚现象,并且有纯聚合物乳胶粒子生成。采用TEM、NMR和FTIR及接触角测试技术分析结果表明,复合微粒是由SiO和聚甲基丙烯酸叔丁酯组成的核壳结构微粒。     

Ni@C/HDPE复合材料的制备及其正温度系数性能研究

采用还原气氛喷雾燃烧法制备了具有核壳结构Ni@C纳米复合颗粒,并与HDPE共混挤出制备了聚合物基PTC导电复合材料,并且对其结构和性能进行了表征.结果表明,所制备的Ni@C复合纳米颗粒具有典型的核壳结构,其中,金属镍的核的粒径为30~50 nm,碳包覆壳层的厚度约为2.9 nm,热重分析结果表明Ni@C复合纳米颗粒的含碳量为3.4%,碳包覆层的存在阻止了金属镍颗粒的团聚;对Ni@C/HDPE复合材料的断面SEM和切片TEM分析结果表明复合颗粒在HDPE基体中分散性良好,复合材料的渗流阈值为10wt%,PTC强度为8个数量级.     

PS/CaCO_3复合纳米粒子及PS纳米空心球的制备研究

以CaCO3为核,采用原位乳液聚合法合成了表面接枝型和交联型PS/CaCO3复合纳米粒子,然后用稀盐酸刻蚀,得到PS纳米空心球.考察了乳化剂类型和用量、引发剂加入方式、加料间隔对乳液稳定性以及复合粒子收率、PS接枝效率的影响,并采用TGA、FT-IR和TEM等手段对刻蚀前后粒子的组成及形貌进行了表征.结果表明,阳离子型乳化剂更有利于乳液体系的稳定性;CTAB用量为3.7%~5.5%时,可获得较高的收率和接枝效率,随CTAB用量增加,粒径减小,分布变宽;AIBN应避免和单体、CaCO3粒子一起超声波处理,否则会导致不可逆凝聚;随着加料间隔延长,收率和接枝效率下降,一步加料法可获得具有高收率和高接枝效率(或交联程度)的复合粒子;经刻蚀,两种类型的复合粒子均可以制得空心粒子,但经过交联的聚合物外壳具有更好的尺寸和形状稳定性,刻蚀后仍然能保持球状的外形.     

可聚合乳化剂制备纳米色料的形貌及其影响因素

以α-烯烃磺酸钠(AOS)为可聚合乳化剂、苯乙烯(St)为非极性单体、甲基丙烯酸甲酯(MMA)为极性单体、二乙烯基苯(DVB)为交联剂、十六烷(HD)为助稳定剂,通过细乳液聚合法制备了聚合物包覆蒽醌类染料的纳米色料。利用透射电子显微镜(TEM)、激光粒度仪(DLS)等研究了可聚合乳化剂、极性单体和交联剂的用量对纳米色料形貌的影响。结果表明:该纳米色料具有明显的核壳结构,且乳液的稳定性好。随着乳化剂用量的增加,粒子粒径变小;少量极性单体的加入有助于得到粒径分布较窄的核壳结构纳米粒子,交联剂和单体彼此极性的差异会导致粒子表面粗糙。以St为聚合单体,当DVB的质量小于St质量的30%时,能够得到结构规整的纳米粒子,超过30%时,纳米粒子表面不再光滑。而以MMA为聚合单体,当DVB的质量为MMA的8%~30%时,粒子表面均凹凸不平。     

静电层层自组装制备聚苯乙烯微球(核)/MCM-41纳米粒子(壳)阶层结构复合微粒

采用聚苯乙烯磺酸钠(PSS)和聚二烯丙基二甲基氯化铵(PDDA)两种聚电解质, 通过静电层层自组装成功地将MCM-41介孔二氧化硅纳米粒子包覆到聚苯乙烯(PS)微球表面. 实验结果表明, 当以尺寸为1.4 μm的PS微球为核时, 包覆了两个聚电解质双层(PDDA/PSS)2的PS(PDDA/PSS)2(PDDA/MCM-41)复合结构微粒与包覆了一个聚电解质双层(PDDA/PSS)的PS(PDDA/PSS)(PDDA/MCM-41)复合结构微粒相比, 复合结构微粒之间的交联程度降低, 但是MCM-41纳米粒子在聚苯乙烯微球表面的包覆都比较松散, 且产物中存在大量杂质. 而当以尺寸为5 μm的聚苯乙烯微球为核时, MCM-41纳米粒子紧密地包覆在聚苯乙烯微球表面, 复合结构微粒之间只有少量桥连物, 且产物中杂质很少.     

NETWORK ENCAPSULATION OF NANOMETER CaCO_3

The encapsulation of stearic acid coated nanometer CaCO3 by a polystyrene (PS) network via emulsion polymerization is described, where γ-methacryloxypropyltrimethoxysilane (MPS) was used as an efficient crosslinker. The important factors such as the type and amount of surfactant and initiator and the content of CaCO3 are investigated as well as the role of MPS. It has been shown that little PS was extractable with only 0.6 wt% of MPS (relative to styrene). The cationic surfactant cetyl trimethylammonium bromide (CTAB) proved more effective than the anionic surfactant sodium dodecyl sulfonate (SDS). The yield rises, particles become smaller and size distribution broadens with increased amount of CTAB. It is also found that either 2,2′-azobis(isobutyronitrile) (AIBN) or ammonium persulfate (APS) is suitable for attaining high monomer conversion. With increased amount of CaCO3, the encapsulation ratio can be varied from 17.9 to 3.6, while monomer conversion and yield decrease slightly. FT-IR spectra of the products after extraction indicate tight encapsulation between PS and CaCO3, and TEM photographs of composite particles with well-defined core-shell structure give direct evidence of encapsulation.     

超浓乳液聚合制备PU/PS的SIPN粉状树脂研究

将聚氨酯予聚体 (PU ) 苯乙烯 (St)的复合体系 ,用超浓乳液聚合方法制备了半互穿聚合物网络(SIPN)复合聚合物 ,得到了用聚氨酯予聚体改性的聚苯乙烯 (PU/PS)SIPN粉状树脂 .研究了分散相的比例(α)和聚合温度对聚合稳定性及聚合转化率 -时间的关系 ;测定了聚合物胶乳粒子的大小、形态 ,玻璃化温度 ,动态力学性能等 .结果表明 ,超浓乳液聚合较之本体聚合具有较高的聚合速率 ,容易控制所制备的胶乳粒径 ,能够制得PU/PS复合聚合物的SIPN粉状树脂 .该粉状树脂便于加工 ,具有良好的强韧性 ,有利于扩大应用     

Kinetics and mechanism of emulsifier-free emulsion polymerization. III. Styrene/nonionic comonomer (2-hydroxyethyl methacrylate) system

The emulsifier-free emulsion polymerizations of styrene in the presence of about 0.33–2.7% (relative to styrene) of the water soluble comonomer, 2-hydroxyethyl methacrylate (HEMA), and of the initiator, potassium persulfate (KPS), were carried out. It was found that KPS plays a predominant role in the particle nucleation process, since the number density of polymer particles (N_p) was dependent on the 0.97-power of [KPS]. The nucleation ability of HEMA was weak, since N_p was dependent only on the 0.17-power of [HEMA]. The particle nucleation stage ceased quite early before 1% conversion, leading to nearly monodispersed polymer particles. The nucleation is suggested to be via the homogeneous nucleation mechanism. The particles grow via the core-shell structure mechanism (shell region polymerization), since the particle size is rather large—from 1500 to 6000 Å. The amount of HEMA can affect the shell thickness and physical properties of the shell, such as the monomer swelling capacity and monomer diffusion rate.     

悬浮-乳液复合聚合聚苯乙烯-聚甲基丙烯酸甲酯复合粒子的颗粒特性和成粒机理

采用在苯乙烯 (St)悬浮聚合过程中滴加甲基丙烯酸甲酯 (MMA)乳液聚合组分的悬浮 乳液复合聚合方法 ,制备大粒径聚苯乙烯 聚甲基丙烯酸甲酯 (PS PMMA)复合粒子 .研究聚合物粒径分布和颗粒形态的变化发现 ,在St悬浮反应中期滴加MMA乳液聚合组分后 ,聚合体系逐渐由悬浮粒子与乳胶粒子并存向形成单峰分布复合粒子转变 ,最终形成核 壳结构完整的大粒径PS PMMA复合粒子 ;在St悬浮反应初期滴加MMA乳液聚合组分 ,St与MMA一起分散成更小液滴 ,反应后期凝并成非核 壳结构复合粒子 ;在St悬浮反应后期滴加MMA乳液聚合组分 ,PMMA乳胶粒子与PS悬浮粒子基本独立存在 .根据以上结果 ,提出了St MMA悬浮 乳液复合聚合的成粒机理 .     

Synthesis of Core-Shell Particles of Polystyrene and Poly(methyl methacrylate) Using Emulsion Photopolymerization

Summary: Submicron core-shell particles of polystyrene (PS) and polystyrene-co-poly(methyl methacrylate) (PS-co-PMMA) coated with PMMA were obtained by emulsion photopolymerization. The seeds of PS or PS-co-PMMA were prepared by emulsion polymerization with or without emulsifier and a ratio of functional monomer and crosslinker (SVBS/EDGMA) in order to obtain different surfaces for the subsequent coating with PMMA. At each stage, the evolution of the average particle size were monitored by using photon correlation spectroscopy (DLS) and the final polymer particles was analyzed via transmission electron microscopy (TEM) and differential scanning calorimetry (DSC). The core-shell morphology was identified as the increase of the average particle size in the second stage by DLS technique and by the direct observation by TEM of the differentiation between PS core and PMMA shell, and by the presence of two glass transition temperatures (T_g) as a consequence of the existence of two partially miscible phases.     

Semi-continuous emulsion polymerization of styrene in the presence of poly(methyl methacrylate) seed particles. Polymerization conditions giving core-shell particles

This work reports the morphology of two-phase latex particles prepared by semi-continuous seed emulsion polymerization of styrene in the presence of polar poly(methyl methacrylate), PMMA, seed particles, using different conditions of non-polar styrene feed rate, rate of initiation, seed particle concentration and temperature of polymerization.The expected latex particle morphology at thermodynamic equilibrium is an inverted core-shell structure where the non-polar polystyrene would form the core. However, depending on the set of process conditions used the morphology of the resulting two-phase particles varied from that of a pure core-shell structure, over intermediate structures in which a shell of PS surrounded a PMMA core containing an increasing number of PS phase domains, to a structure in which the entire PS phase was present as discrete PS phase domain, more or less evenly distributed in a matrix of PMMA.By the use of a caloirimetric reactor system the monomer concentration in the particles during the different polymerization experiments could be calculated by comparing the integral of the polymerization rate curve with the integral of the monomer feed rate. A comparison between particle morphology and the calculated concentration of plasticizing monomer in the polymerizing particles strongly suggested that the diffusivity of the entering oligo radicals determined by the difference between polymerization temperature and the glass transition temperature of the monomer-swollen core polymer is a key factor determining the morphology of two-phase particles prepared by semi-continuous seed emulsion polymerization.Two-phase particles with a true core-shell structure were obtained in experiments where the estimated glass transition temperature of the PMMA phase was only a few degrees below the polymerization temperature. The results show that such particles can be obtained under conditions of high as well as low styrene feed rates, provided that the rate of initiation is properly adjusted.     

核/壳乳液聚合工艺中乳化剂的定量研究

以十二烷基硫酸钠(SDS)为乳化剂,采用多步种子乳液聚合方法制备了核/壳结构乳液,研究了乳化剂加入量以及加料速率对核壳乳液聚合的影响,并推导了核及壳乳液聚合阶段所需乳化剂量的计算公式.研究表明,当种子、核、壳乳液聚合阶段单体量分别为12g、50g和50g,种子乳液聚合阶段加入的乳化剂量为0.44g时,控制核、壳乳液聚合阶段乳化剂的加入量分别在0.64～2.07g及0.04～2.12g之间,且预乳化单体的滴加速度低于2.3g/min时,可以防止二次成核及新乳胶粒子的形成,制得粒径分布窄、核/壳结构明显的乳胶粒子.利用透射电镜(TEM)对所制备的核壳结构乳胶粒子的结构形态进行了验证,试验结果与理论预测结果一致.     

Emulsion polymerization of styrene and methyl methacrylate using a hydrophobically modified inulin and comparison with other surfactants

The use of a new class of graft polymer surfactants, based on inulin, in emulsion polymerization of poly(methyl methacrylate) (PMMA) and polystyrene (PS) particles is described. PS and PMMA were synthesized by emulsion polymerization, and stable particles with a high monomer content (50 wt %) were obtained with a very small amount of polymeric surfactant ([surfactant]/[monomer] = 0.0033). The latex dispersions were characterized by dynamic light scattering and by transmission electron microscopy to obtain the average particle size and the polydispersity index, and the stability was determined by turbidimetry measurements and expressed in terms of critical coagulation concentration. The last section gives a comparison of PMMA particles prepared by emulsion polymerization using classical surfactants from different types as emulsifiers with that obtained using the copolymer surfactant. It shows the superiority of INUTEC SP1 as it is the only one that allows stable particles at 20 wt % monomer content, with a smaller ratio [surfactant]/[monomer] = 0.002.