离子交换法提取谷氨酸的研究

本文就离子交换法提取谷氨酸树脂的筛选，不同树脂对发酵液中谷氨酸静态吸附性能及其影响因素进行了系统地研究．旨在探索离子交换法提取谷氨酸的最佳工艺条件和开发新的离子交换树脂．     

离子交换法在治理含钼废水中的应用

本文综合介绍了离子交换法治理含钼废水的机理、影响因素。并列举了Ｄ３８０、ＳＷ３０５、Ｄ２９０、Ｗ—３０５Ｃ、３０４Ａ等大孔离子交换树脂处理含钼废水的工艺流程和参数。     

离子交换法分离乳酸的研究

本文对离子交换法分离乳酸的离子交换树脂、交换相平衡和交换动力学进行了研究,并在离子交换柱上测定了南开大学化工厂生产的201×4树脂的交换曲线。实验结果说明,用离子交换法分离发酵液中乳酸是可行的。     

氯化亚铜制备方法的改进

通常制备氯化亚铜的方法,是在热的浓盐酸中将CuCl_2与金属铜进行反应,然后将反应后的溶液稀释,即可得到白色的氯化亚铜沉淀。有关的化学反应如下: 2HCl(浓)+CuCl_2+Cu△=2HCuCl_2 (1) HCuCl_2稀释=HCl+CuCl↓ (2) 一般认为稀释前溶液的颜色就是CuCl_2~-离子的颜色,并将这种颜色作为上述第一个反应是否进行完全的标志。然而,对于CuCl_2~-离子的颜色,曾有过多种不同的描述。虽现已确证为无色,但按传统方     

国内离子交换法处理氰化镉废水的现状及改进意见

本文对国内现行离子交换法处理氰化镀镉废水的工艺进行了探讨，提出了用络合理论将阴树脂由Ｃｌ－１型转变成ＣｄＣｌ４２－型后交换，便可提高对水中游离氰（ＣＮ－）的吸附能力，并能使氰、镉都得到回收利用。     

离子交换法提取赖氨酸的解脱研究

本研究采用碳化母液(NH_4OH-CO_2)为解脱剂,逆流解脱的新工艺。与现行的用氨水为解脱剂,顺流解脱工艺相比较,具有缩短解脱时间、减少解脱液体积,去除解脱收集液中部分杂质离子、降低生产成本等优点和一定的经济价值。     

离子交换法降低甘草浸膏灰份的研究

本文介绍了用离子交换法降低甘草浸膏灰份的实验研究。实验表明:用国产大孔阳离子交换树脂D001-CC及强碱性阴离子交换树脂D296配合使用,可将原甘草浸膏中12％的灰份降低至5～7％,同时用氨水、稀盐酸、稀氢氧化钠溶液分次再生树脂可减少甘草浸膏有效成份的损失。并且设计了工业上可能采取的工艺路线。     

离子交换法制备注射用葡萄糖新工艺

本文阐述离子交换法生产注射用葡萄糖新工艺的工艺流程、操作方法、产品质量情况及经济效益等。     

离子交换法分离提纯木质素

本文研究了用蛇笼树脂分离粗木质素溶液中的小分子盐,用互贯磺酸树脂分离粗木质素溶液中的还原糖,以及用大孔和凝胶磺酸树脂对木质素分级作用。此外还研究了用离子交换法测定木质磺酸盐的磺化度和有木质磺酸盐存在时小分子盐含量测定,都得到了满意结果。     

氯化亚铜催化3-氯-1-丁烯异构为1-氯-2-丁烯研究

采用一价铜盐为催化剂、二甲基甲酰胺为溶剂,在均相体系中催化3-氯-1-丁烯异构化生成1-氯-2-丁烯.考察了溶剂、反应温度、催化剂种类和加入量对反应的影响,研究发现反应温度和催化剂的加入量对异构化反应有较大影响.在最优条件3-氯-1-丁烯1 mL,二甲基甲酰胺9 mL,CuCl 0.10 g,60℃反应5 h,产物和原料的浓度比为3.88 mmol L-1.采用在线红外光谱对反应过程进行监测,检测到有红外吸收峰在反应过程中先增加后减少的变化过程,提出了可能的反应机理.     

氯化亚铜在活性炭载体表面单层分散的密度泛函理论计算

 应用量子化学计算方法研究了活性炭载体表面CuCl活性组分的单层分散行为. 以C16H10,C13H9和C12H12原子簇模型模拟活性炭表面,用密度泛函理论中的B3LYP方法计算得到了CuCl在活性炭表面分散的活性位、稳定构型、相互作用能以及单层分散阈值. 结果表明,CuCl以铜端垂直附着在活性炭表面的顶位和桥位上,相互作用能为76.84～80.79 kJ/mol,单层分散阈值为0.471 g/g. 而XRD测得的单层分散阈值为0.467 g/g,与量子化学计算的结果一致; 按照密置单层模型计算得出的单层分散阈值为0.941 g/g,远大于实验测定结果. 因此,应用量子化学计算方法可以得到活性炭表面活性组分单层分散的丰富信息,并能确定活性组分的单层分散阈值.     

多元醇法形貌可控制备氧化亚铜微纳米颗粒

以硝酸铜、乙酸铜、乙酰丙酮铜为原料,采用多元醇还原法合成制备了氧化亚铜立方体、微球、空心球、核壳结构等微纳米颗粒。 利用X射线衍射仪(XRD)、场发射扫描电子显微镜(FE-SEM)、透射电子显微镜(TEM)、高分辨透射电子显微镜(HRTEM)和紫外可见吸收光谱(UV-Vis)等测试手段对样品的物相、形貌、元素组分及吸光性能进行了表征。 同时考察了铜源、反应时间、和多元醇类型对氧化亚铜微纳米材料形貌的影响,对产物形成机理进行了初步的探讨。 对产物形成机理进行了初步的探讨。 采用简单低廉的多元醇合成法,可以控制合成不同相貌的氧化亚铜微纳米结构。 对制备形貌可控的氧化物具有一定的指导意义。     

铜与氯化铁溶液反应颜色呈浅绿色的原因

通过实验探究和理论分析,发现Cu和FeCl3溶液反应颜色呈浅绿色的原因是：Cu和CuCl2反应生成CuCl白色沉淀,消耗了溶液中的Cu2+。根据这一结论,对一篇文章中的实验设计和观点进行修正,同时也对2道关于Cu与FeCl3反应的试题提出质疑并进行科学性改造,以服务于化学教学。     

Ion-Exchange equilibria in cationic polyelectrolytes

A method which allows the evaluation of phenomenological ion exchange constants K_ex is proposed and tested in a cationic polyelectrolyte system. Results for nitrate/chloride exchange are nearly constant over the entire concentration range studied. However, for nitrate/bromide exchange, the results depend on the polyelectrolyte concentration, with K_ex following the same trend as the mean activity coefficient for the polyion bromide. For polyion fluoride, a conformational change is probably induced as nitrate is added to the solution and the result deviates from the linear relationship predicted by the method. Benzene sulfonate behaves like a hydrophilic anion, whereas tosylate and ethylbenzene sulfonate also induce conformational changes by hydrophobic interactions. These results are supported by viscosity measurements and agree well with those recently reported by Satoh, who considered changes in apparent molar volume. © 1994 John Wiley & Sons, Inc.     

电化学法制备氧化亚铜的研究

采用电化学法制备氧化亚铜 .研究了电解液组成及其浓度、温度以及电流密度等因素对氧化亚铜产品质量的影响 ,选定的优化工艺条件 :ρ(NaCl) =2 6 0～ 2 90g/L ,ρ(NaOH) =0 .5 0g/L(pH =12 .1) ;电解温度为 75～ 80℃ ;电流密度为 75 0A/m2     

Ion-Exchange Properties of Alkali-Metal Redox-Intercalated Vanadyl Phosphate

Ion exchange of alkali metals in M_xVOPO₄·yH₂O (M=H, Na, K, Rb, Cs) is reported. The role of valence, size, and affinity of the cations in the exchange process is discussed. The interlayer distance in the H_1-xK_xVOPO₄·yH₂O system is discussed in terms of finite layer rigidity theory. Different behavior is observed for K_xNa_1-xVOPO₄·yH₂O dependening on the starting compound used. When potassium in KVOPO₄·H₂O is exchanged for Na⁺, one phase compound is formed. In contrast, K_xNa_1-xVOPO₄·yH₂O formed from NaVOPO₄·H₂O and K⁺ is a multiphase system. Ion exchange does not proceed when exchanging ions differ distinctly from each other in size, e.g., sodium and cesium.     

离子色谱法分析土壤中的矮壮素和缩节胺

建立了离子交换色谱一直接电导法同时测定土壤中矮壮素和缩节胺残留的分析方法。样品经磨碎超声提取后,用固相萃取（SPE）柱祛除蛋白质,过0．22μm过滤膜,进样检测。考察了不同的阳离子色谱柱SH-CC-1,SH-CC-2,SH—CC_3及其不同的淋洗液对矮壮素、缩节胺的保留时间和分离度的影响。确定了最佳色谱条件：SH—CC-3阳离子色谱柱;直接电导检测;淋洗液选用3．0mmol／L甲烷磺酸,流速为1．0mL／min;柱温：40℃;进样量：100μL。在此条件下,矮壮素及缩节胺在0．20-20．0mg／地范围内,线性相关系数,均大于0．999,矮壮素和缩节胺的检出限（S／N=3）分别为0．070,0．073mg／kg,加标回收率分别为86．0％-93．8％,84．9％～93．2％,测定结果的相对标准偏差小于4．2％。方法选择性好,灵敏度高,抗干扰能力强,适用于检测土壤中矮壮素和缩节胺。     

聚氯乙烯负载席夫碱树脂的合成及其对金属离子的吸附

聚氯乙烯负载席夫碱树脂的合成及其对金属离子的吸附刘理中，俞善信，肖立新（湖南师范大学化学系长沙４１００８１）（中南工业大学冶金化学研究所长沙）关键词聚氯乙烯，负载树脂．席夫碱，金属离子，吸附高分子负载席夫碱可用于离子吸附和催化等领域，汪信［１，２］等...     

Characterization and Optimization of Polymeric Bispicolamine Chelating Resin: Performance Evaluation via RSM Using Copper in Acid Liquors as a Model Substrate through Ion Exchange Method

Advanced technologies of electronics industries have led to environmental contamination concerns, especially waste print circuit boards containing a very high concentration of copper (II) ions, which can be discharged in wastewater containing many contaminated metals. A low pH is a necessity for treating industrial wastewater containing heavy metals to meet engineering process design. A novel polymeric bispicolamine chelating resin, Dowex-M4195, was applied as an alternative for investigating the behavior of copper (II) in acidic solution via an ion exchange method in a batch experiment system. Characterization of physical and chemical properties before and after ion exchange were also explored through BET, SEM-EDX, FTIR and XRD. Response surface methodology was also applied for optimization of copper (II) removal capacity using design of experiment for selective chelating resin at a low pH. The results indicate that H⁺ Dowex-M4195 chelating resin had a high-carbon content and specific surface area of >64% and 26.5060 m²/g, respectively. It was predominantly macropore porous in nature due to the N₂ gas adsorption isotherm and exhibited type IV with insignificant desorption hysteresis loop of H1-type. It was spherical and cylindrical. After the ion exchange process of copper (II)-loaded H⁺ Dowex-M4195, the specific surface area and total pore volume decreased by about 17.82% and 5.39%, respectively, as compared to H⁺ Dowex-M4195. Hysteresis loop, isotherm and pore size distribution were also similar. Regarding the functional group, the surface morphology and crystalline structures of H⁺ Dowex-M4195 showed copper (II) compound based on the structure of chelating resin that confirmed effective ion exchange behavior. The design of optimization indicated that copper (II) removal capacity of about 31.33 mg/g was achieved, which could be obtained at 6.96 h, pH of 2 (a desirable low pH), dose of 124.13 mg and concentration of 525.15 mg/L. The study indicated that the H⁺ Dowex-M4195 (which is commercially available on the market) can successfully be applied as an alternative precursor through the ion exchange method for further reuse and regeneration of the copper (II) in the electronic waste industries and other wastewater applications needed to respond the policy of biocircular green economy in Thailand.