双醛淀粉制备中电氧化IO-3转化生成IO-4过程研究

双醛淀粉制备中,影响电氧化IO3-转化生成IO4-过程的因素是比较复杂的,在自制的电解反应器中,以碘酸钠为原料,研究了IO3-转化生成IO4-过程.考察了各种因素对转化率和电流效率的影响.在选定的实验条件下,恒电流操作,阳极为DSA电极,阴极为纯钛电极,阴极液为0.2mol/L的 H2SO4溶液,隔膜为聚乙烯异相阳离子交换膜;阳极室中NaIO3起始浓度为0.3mol/L,H2SO4起始浓度为0.2mol/L,电流密度为0.025A/cm2,电解时间2h,IO3-的转化率为53.54%,电流效率为86.1%.     

CS-CMC聚合物电解质膜的制备及在电生成FeO2-4中的应用

以戊二醛为交联剂,制备了壳聚糖(CS)-羧甲基纤维素(CMC)聚合物电解质膜.用电子显微镜观察其表面形貌.IR分析表明该聚合物薄膜含有COOH,NH3+官能团,具有两性离子的特征.与CS膜或CMC膜相比,该膜能稳定存在于酸碱溶液中.膜特性研究表明CS-CMC聚合物电解质膜具有离子交换和选择性渗透能力,可作为隔膜电解制备高铁酸盐.     

CS-CMC聚合物电解质膜的制备及在电生成FeO_4~(2-)中的应用

以戊二醛为交联剂,制备了壳聚糖(CS)-羧甲基纤维素(CMC)聚合物电解质膜.用电子显微镜观察其表面形貌.IR分析表明该聚合物薄膜含有COOH,NH 3官能团,具有两性离子的特征.与CS膜或CMC膜相比,该膜能稳定存在于酸碱溶液中.膜特性研究表明CS-CMC聚合物电解质膜具有离子交换和选择性渗透能力,可作为隔膜电解制备高铁酸盐.     

CS-CMC聚合物电解质膜的制备及在电生成FeO42-中的应用

以戊二醛为交联剂, 制备了壳聚糖(CS)-羧甲基纤维素(CMC)聚合物电解质膜. 用电子显微镜观察其表面形貌. IR分析表明该聚合物薄膜含有COOH, NH₃⁺官能团, 具有两性离子的特征. 与CS膜或CMC膜相比, 该膜能稳定存在于酸碱溶液中. 膜特性研究表明CS-CMC聚合物电解质膜具有离子交换和选择性渗透能力, 可作为隔膜电解制备高铁酸盐.     

CS-CMC聚合物电解质膜的制备及在电生成FeO42-中的应用

以戊二醛为交联剂, 制备了壳聚糖(CS)-羧甲基纤维素(CMC)聚合物电解质膜. 用电子显微镜观察其表面形貌. IR分析表明该聚合物薄膜含有COOH, NH₃⁺官能团, 具有两性离子的特征. 与CS膜或CMC膜相比, 该膜能稳定存在于酸碱溶液中. 膜特性研究表明CS-CMC聚合物电解质膜具有离子交换和选择性渗透能力, 可作为隔膜电解制备高铁酸盐.     

mCMC-PEG-CS双极膜在电还原制备巯基乙酸中的应用

以Fe3+改性羧甲基纤维素(CMC)和聚乙二醇(PEG)共混物为阳膜, 以戊二醛改性壳聚糖(CS)和聚乙二醇共混物为阴膜, 制备了mCMC-PEG-CS双极膜, 并将其用作电解还原制备巯基乙酸(TGA)电解槽中阴阳两室间的隔膜. 以硫代硫酸钠法合成的巯基乙酸(TGA)和二硫代二乙酸(DTDGA)混合物为原料, 研究了酸浓度、温度及电解电流密度对电还原DTDGA制备TGA的生成量和电流效率的影响. 实验结果表明, 在TGA初始合成质量分数为2.79%, 电流密度为10 mA/cm2, 35 ℃电解时, 阴极室电还原产物巯基乙酸的电流效率为74.69%, 电解过程中的平均电流效率为54.02%. 与传统的金属还原法还原DTDGA制备的TGA相比, 不仅避免了昂贵的金属还原剂锌的消耗, 而且消除了反应副产物锌泥对环境的污染.     

以磷酸型质子交换膜为固体电解质的定电位电解型气体传感器

SO2;以磷酸型质子交换膜为固体电解质的定电位电解型气体传感器     

m(SA-CS)BM串联电解槽双成对电解制备乙醛酸

分别用戊二醛和二价锡离子改性壳聚糖(CS)和海藻酸钠(SA),制备改性海藻酸钠/亮聚糖双极膜[m(SA-CS)BM].将其作为双阴阳极电解槽的隔膜,应用于双成对电合成乙醛酸体系.在电场的作用下,双极膜中水电离后生成的H+透过Msa阳离子膜进入阴极室,以补充草酸电还原生成乙醛酸过程中H+的消耗;OH-透过Mcs阴离子膜进入阳极室,与乙二醛电氧化生成乙醛酸过程中产生的H+结合生成H2O,以增大正向反应的速度.在电流密度为30mA/cm2,20℃下电解,双阴极室的电流效率分别可达86.94%和82.81%,双阳极室的电流效率可达81.99%和78.62%,电解电压稳定在3.0V左右.     

磺化聚醚醚酮与壳聚糖共混制备直接甲醇燃料电池用质子交换膜

给出了不同磺化度下的磺化聚醚醚酮(SPEEK)用作质子交换膜的一系列性能,另外提出了一种新型的酸碱共混质子交换膜,其中,磺化聚醚醚酮和壳聚糖分别被选为酸性、碱性高分子电解质,并对所制备的质子交换膜的相关性能如质子传导性,甲醇渗透性,吸水率以及膜溶胀性、热稳定性等进行了表征,结果表明此种新型复合膜尽管在质子传导性能方面有所下降,阻醇性能改变不大,但是膜溶胀性和吸水率方面有了较大的改善.磺化度为71.4%的SPEEK与壳聚糖以5∶1摩尔比共混制备的质子交换膜,其性质可以与商品化的Nafion 117相媲美,有望在甲醇燃料电池中得到应用.     

发泡镍电极电化学还原嘌呤中间体

由三维发泡镍电极H2SO4电解质和阳离子交换膜,组成隔膜式三维发泡镍电解循环装置.利用该装置将3-甲基-4-亚氨基-5-异亚硝基脲嗪(NAU)电还原为3-甲基-4,5-二氨基脲嗪(DAU).比较发泡镍阴极的电流密度,测定不同pH条件下的反应电位.结果表明,发泡镍电极的电流密度比平板镍高77.3%～86.7%,电流效率平均90.3%,NAU还原转化率平均98.4%,电还原能耗平均2.92kWh/kg.恒电流电还原过程出现峰电位,继续延长电还原时间则有副反应产生.分别以传统铁粉还原和电还原的DAU完成下游嘌呤产品的合成,证明电还原产品收率不低于铁粉还原.     

四磺酸基铜酞菁-海藻酸钠/壳聚糖双极膜的制备与表征

分别用Fe3+和戊二醛作为交联剂对海藻酸钠(SA)阳离子交换膜和壳聚糖(CS)阴离子交换膜进行改性,制备了四磺酸基铜酞菁(CuTsPc)-海藻酸钠/改性壳聚糖双极膜(CuTsPc-SA/mCSBPM).在海藻酸钠阳膜层中添加四磺酸基铜酞菁,以提高阳膜层的离子交换容量,促进双极膜中间层中水的解离.采用X射线光电子能谱(XPS)对CuTsPc-SA阳离子交换膜进行了表征.实验结果表明,改性后SA阳膜层的离子交换容量、H+透过率均获得提高.与Fe3+改性或二茂铁离子改性的mSA/mCS双极膜相比,CuTsPc-SA/mCS双极膜的阻抗及电阻压降(即膜IR降)均下降.当电流密度为120mA/cm2时槽电压仅为5.6V.当CuTsPc含量为2.5%(质量分数)时CuTsPc-SA/mCS双极膜在H+离子浓度小于8mol/L的酸溶液中具有稳定的工作性能.     

PREPARATION AND CHARACTERIZATION OF ION EXCHANGE MEMBRANES BASED ON POLYVINYLIDENE FLUORIDE

 A new ion exchange membrane based on polyvinylidene fluoride (PVDF) and sulfonated poly(styrene- divinylbenzene) was prepared by in-situ polymerization. The incorporation of sulfonic groups into the polyvinylidene fluoride composite membrane was confirmed by infrared spectroscopy (IR), ion exchange capacity (IEC) and energy dispersive X-ray analysis (EDAX). Area resistance, IEC and water uptake of the treated membrane were evaluated. When 20% of the crosslinked membrane was sulfonated at 80°C for 22 h, the PVDF ion exchange membrane can attain 0.8 Ω·cm²area resistance in NaCl aqueous solution at 25℃, IEC is as high as 2.43 millimoles per gram of the wet membrane. The hydrophilicity of PVDF membrane is also significantly improved after treatment. When 60% of crosslinked membrane was sulfonated at 80 ℃ for 6 h, water uptake of the treated membrane can attain 64.7%.     

磺化聚苯醚酮质子交换膜的制备与表征

设计、合成了一种含氰基双氯单体,其结构特点是氰基分布在3个以间位醚键相连的苯环上。以此单体和2,5-二氯-3'-磺酸钠二苯甲酮为原料,利用Ni(0)催化偶联反应制备了微嵌段型质子交换膜材料(中等长度磺化聚苯-三氰基聚苯醚酮共聚物(m-SPP-co-PAEK 3CN x),x代表聚合物的离子交换容量)。结果表明,与相同离子交换容量的磺化聚合物相比,该类聚合物膜表现出较低的吸水、溶胀率和较低的甲醇渗透性能。以离子交换容量2.16为例,80℃下,m-SPP-co-PAEK 3CN 2.16的吸水率、溶胀率分别为29.7%、28.2%,而SPP-co-PAEK MO 2.33的吸水率、溶胀率分别为80.2%、37.2%。25℃下,二者的甲醇渗透系数分别为2.38和7.20。聚合物骨架结构中存在丰富的氰基基团,导致膜具有良好的尺寸稳定性和较低的甲醇渗透性能。基于这些优异的性能,新制备的膜材料在燃料电池领域显示了潜在的应用前景。     

Preparation of anion exchange membrane based on block copolymers. Part II: the effect of the formation of macroreticular structure on the membrane properties

The anion exchange membrane was prepared by conducting the formation of macroreticular structure and the introduction of ion exchange groups to the chloromethylated copolymers simultaneously. The membrane properties are summarized below; 0.9–1.4 Ω cm² for area resistivity in 2 M KCl aqueous solution, 1.46–3.7 meq/g-dry-resin for the ion exchange capacity and 0.68–0.87 for the static transport number. The membrane properties of the membrane prepared by forming the macroreticular structure and the introduction of the ion exchange groups to the chloromethylated copolymers simultaneously (B membrane) had higher performance than that of the membrane prepared by the amination of the chloromethylated copolymers (A membrane). It would be expected that the formation of macroreticular structure in the membrane has an effect on the membrane properties. The chemical stability of B membrane which was determined by the oxidative degradation in 2 M nitric acid, had long lifetime with almost the same value of the area resistivity and ion exchange capacity as before durability test.     

PREPARATION AND CHARACTERIZATION OF ION EXCHANGE MEMBRANES BASED ON POLYVINYLIDENE FLUORIDE

A new ion exchange membrane based on polyvinylidene fluoride (PVDF) and sulfonated poly(styrenedivinylbenzene) was prepared by in-situ polymerization. The incorporation of sulfonic groups into the polyvinylidene fluoride composite membrane was confirmed by infrared spectroscopy (IR), ion exchange capacity (IEC) and energy dispersive X-ray analysis (EDAX). Area resistance, IEC and water uptake of the treated membrane were evaluated. When area resistance in NaCl aqueous solution at 25℃, IEC is as high as 2.43 millimoles per gram of the wet membrane. The hydrophilicity of PVDF membrane is also significantly improved after treatment. When 60% of crosslinked membrane was sulfonated at 80℃ for 6 h, water uptake of the treated membrane can attain 64.7%.     

Transport properties of highly ordered heterogeneous ion-exchange membranes

Model "ordered" heterogeneous ion exchange membranes are made with ion exchange particles heaving ion exchange capacity in the range 3 to 2.5 meq/gr (dry basis) and diameters ranging from 37 to 7 microm and 2 component room-temperature vulcanizing silicon rubber as a polymeric matrix, by applying an electric field normal to the membrane surface during preparation. These membranes were shown to have an improved ionic conductivity compared with "nonordered" membranes based on the same ion exchange content (for instance, at 10% resin content "nonordered" membranes show <10(-5) mS/cm while "ordered" membranes have conductivity of 1 mS/cm). The transport properties of ordered membranes were compared with those of nonordered membranes, through the current-voltage characteristics. Limiting currents measured for the ordered membranes were significantly higher than those of the nonordered membranes with the same resin concentration. In addition, higher limiting currents were observed in ordered membranes as the resin particles became smaller. Energy dispersion spectrometry analyses revealed that the concentration of cation exchange groups on the membrane surface was higher for ordered membrane as compared to that of nonordered membranes. This implies that the local current density for the conducting domains at the surface of the nonordered membranes is higher, leading to higher concentration polarization and, eventually, to lower average limiting current densities. The effect of ordering the particles on the membrane conductivity and transport properties was studied, and the advantages of the ordered membranes are discussed.     

用于碱性膜燃料电池的新型聚苯醚阴离子交换膜的制备与性能

以2,6-二甲基聚苯醚(PPO)为原料, 经溴代及N-甲基咪唑季铵化反应, 制备了N-甲基咪唑季铵化PPO, 并进行了红外光谱(FTIR)和氢核磁共振波谱(¹H NMR)表征.所得季铵化产物与聚乙烯醇(PVA)按不同比例共混后用戊二醛交联成膜, 在碱性液中浸泡转化为OH^-型, 得到一系列阴离子交换膜.通过扫描电子显微镜(SEM) 、交流阻抗(AC)、拉伸实验和热重分析(TGA)等手段考察了膜的微观形貌及电导率、力学性能、热稳定性及耐碱性等性能.结果表明, 膜的外观形貌平整均一; 含水率为50.4%~151.2%; 溶胀度为79.2%~164.2%; 离子交换容量为0.47~1.52 mmol/g; 90℃时, M4膜的电导率高达49.1 mS/cm; 断裂伸长率达到128%, 极大改善了PPO膜应力易裂的状况.同时, N-甲基咪唑鎓基团分解温度达到170℃, 高于常用的阴离子交换膜中的季铵基团(120℃).在2 mol/L的NaOH溶液中浸泡192 h后, 电导率仅下降19%, 具备良好的耐碱性能力.     

Novel Crosslinked Alkaline Exchange Membranes Based on Poly(phthalazinone ether ketone) for Anion Exchange Membrane Fuel Cell Applications

Novel crosslinked anion exchange membranes based on poly(phthalazinone ether ketone) (PPEK) were successfully prepared through chloromethylation, quaternization, membrane casting and OH‐ ionic exchange reaction from the quaternized PPEK (QPPEK) membrane. The quaternization was performed with N‐methylimidazolium (MIm) as ammonium agent and tetramethylethylenediamine (TMEDA) as crosslinking agent. The ion‐exchange capacity, swelling ratio (SR), water uptake (WU), and ionic conductivity of the QPPEK alkaline membranes have been systematically investigated. The results showed that QPPEK membranes have a high hydroxide conductivity and very low SR. For the QPPEK‐4 alkaline membrane with ion‐exchange capacity (IEC) 2.63 mmol/g, the WU was 35.8%, and the hydroxide conductivity was 0.028 S/cm at 30 °C and 0.032 S/cm at 70 °C, while its SR was only 7.6%. The thermal properties of the QPPEK alkaline membrane and CMPPEK were characterized using thermo‐gravimetric analysis measurements in a nitrogen atmosphere. The alkaline resistance of membrane QPPEK ?4 was also briefly investigated in 6 M KOH at 60 °C. © 2013 Wiley Periodicals, Inc. J. Polym. Sci., Part B: Polym. Phys. 2013 , 51, 1632–1638     

微囊化海藻酸离子移变凝胶的制备、结构与性能

通过静电脉冲技术制备了海藻酸-壳聚糖-海藻酸(Alginate-Chitosan-Alginate,ACA)微胶囊,红外光谱分析表明,ACA是一种以聚电解质配合物为囊膜,以海藻酸钠离子吸附剂为囊心物的微胶囊型离子吸附体系.扫描电镜测试表明,ACA吸附重金属离子的过程是微胶囊囊内海藻酸凝胶化的过程,其解吸附过程是海藻酸凝胶转变成海藻酸溶液的过程.与传统离子交换树脂相比,ACA对Pb²⁺的吸附具有较高的去除率、很强的富集能力和较低的极限吸附浓度,并且能够被多次重复使用.ACA的离子交换速率比传统离子交换树脂快得多,离子交换过程中,交换离子和吸附剂海藻酸分子的相互扩散大大提高了离子交换速率.     

Preparation and basic characterization of heterogeneous weak acid cation exchange membrane

The goal of this article is focused on the preparation and the basic characterization of heterogeneous weak acid cation exchange membranes. The six weak cation exchange resins were chosen for the preparation of the membranes. The strong acid cation exchange membrane was prepared for the comparison of properties and preparation parameters. Heterogeneous membranes were prepared in the several steps. The last operations were the extrusion and hydraulic hot-pressing. The torque and pressure in the extrusion head were observed while the extrusion of heterogeneous membranes. According to the type of the ion exchange resin, parameters varied greatly. The strong acid cation exchange membrane and weak acid cation exchange membranes with carboxylic groups had the lowest values of the torque and pressure while the homogenization and extrusion. All membranes were characterized. Electrochemical (permselectivity, ion exchange capacity, resistance), physical (relative water content, swelling in the different solutions), and mechanical properties were measured. Properties varied distinctly according to the type of the ion exchange resins. Swelling dimensional changes of ion exchange membranes in sodium hydroxide and water were bigger than changes in hydrochloric acid. Ion exchange capacity of membranes related with ion exchange capacity of used ion exchange resins. Weak acid cation exchange membranes with carboxylic functional groups compared to the strong membrane had the best specific and areal resistance.