Deacidification of citric acid solutions by electrodialysis

Electrodialysis is a useful process to deacidify citrus juices. Besides the known allanion exchange membrane process, two alternative electrodialysis processes were investigated: a three-stream process using cation and anion exchange membranes and a twostream process with alternately arranged bipolar and anion exchange membranes. The results taken from a laboratory electrodialysis cell show, that according to current efficiency, consumption of sodium hydroxide and by-production of sodium citrate or citric acid the alternative processes are favourable, especially the process using bipolar membranes.     

Study of pH correction process of chloride-bicarbonate dilute solutions by electrodialysis with bipolar membranes

The pH of a dilute chloride-hydrocarbonate solution and the concentrations of chloride ions and carbonic acid anions at the outlet of the alkaline and acid chambers of the electrodialysis cell formed by bipolar and anion-exchange membranes were determined. The decrease in the concentration of hydrocarbonate ions in the alkaline chamber with growth of current density was not equal to its increase in the acid chamber. This disbalance was caused by two concurrent processes: the electromigration ion transport through the anion-exchange membrane and the chemical reactions of hydrocarbonate ions with the water dissociation products formed on the bipolar and anion-exchange membranes. A mathematical model was suggested to describe the electrodialysis correction of the pH of a dilute chloride-hydrocarbonate solution. The experimental data on the correction of pH of the chloride-hydrocarbonate solution were well approximated by both the model that takes into account water dissociation on the anion-exchange membrane and the simplified model that neglects water dissociation. The experimental data agreed well with the results of calculations by the model in which the effective anion transport numbers were calculated only from ion concentrations and diffusion coefficients in solution. This reflects the outer diffusion character of the kinetics of ion transport through the anion-exchange membrane, with pH of dilute solutions corrected by electrodialysis.     

Competitive anion transport in desalting of mixtures of organic acids by batch electrodialysis

Desalting and separation of binary and quaternary acid mixtures via batch electrodialysis are investigated in this article. A monoselective cation exchange membrane and either a non-selective or a monoselective anion exchange membrane are employed in the electrodialysis stack. The effects of current density and composition of the initial feed of the electrodialysis stack (employing a non-selective anion exchange membrane) on its performance are studied in experiments involving mixtures of acetic and succinic acids. The effect of the type of the anion exchange membrane on the process performance is examined in desalting experiments involving a mixture of acetic, formic, lactic, and succinic acids. The trends observed in the experiments are interpreted in terms of species-specific parameters (such as molar concentration, charge on ionic species, molecular weight, degree of ionization, and ionic equivalent conductivity) and characteristics of anion exchange membrane used.     

Influences of colloidal stability and electrokinetic property on electrodialysis performance in the presence of silica sol

Negatively charged silica sol is known to lead to fouling of anion exchange membranes during electrodialysis (ED) as a result of its deposition on the membrane surface. It is known that the fouling potential is related to the physical and electrochemical properties of the silica particles as well as those of the anion exchange membranes. In this study, the properties of the silica sol were characterized in terms of its particle size, turbidity, and zeta potential in order to predict their effects on the electrodialysis performance. In the stability of colloidal particles, the critical coagulation concentrations of silica sol were determined as functions of ionic strength, cation species, and solution pH. In the electrodialysis of NaCl solution containing silica sol with various concentrations of CaCl(2), the colloidal behavior related to deposition and transport was examined during and after electrodialysis. The electrodialysis experiments clearly showed that the deposition and transport of silica sol during electrodialysis were related to the colloidal stability of dispersion.     

Electrodialysis with Bipolar Membranes: Principles,Optimization, and Applications

This paper is an overview of the bipolar membrane technology. The process of electrodialysis with bipolar membrane (EDBM) along with the different EDBM process configurations are presented. Some ways of optimization of both the bipolar membranes and the EDBM technology are envisaged. Most of the applications relate to the production or recovery of organic acids while the first plant has been commissioned by 1986 at Washington Steel (USA) for the recovery of HF/HNO₃ from waste pickling liquors. In the last few years, there has been increasing interest in using bipolar electrodialysis stacks in chemical and agro industrial processes to directly acidify or basify process streams without the addition of chemicals. This attractive feature of this technology has contributed to the implementation of several plants in fermentation process for the production of organic and amino acids.     

Nanocomposite interface coupled with thickness optimization promoting water dissociation in heterogeneous bipolar membrane

Bipolar membranes (BPMs) are multilayered composite film containing an interface layer sandwiched between cation exchange layer (CEL) and anion exchange layer (AEL), and are capable of dissociating water molecules under reverse bias potential. Woven fabric supported heterogeneous bipolar membranes (HBMs) were synthesized adopting layer-by-layer solvent casting technique. Nanocomposite layer based on sulfonated polyether ether ketone (SPEEK) and GO (graphene oxide) were applied at the interface of CEL/AEL made of cation/anion exchange resins and poly (vinyl chloride) as binder to advance water dissociation in HBMs. Thickness of monopolar layers were initially optimized without any interfacial layer. Introduction of SPEEK interface substantially lowered onset water dissociation potential, U_diss (~1.87 V) relative to the HBM without interface (~3.27 V), which got further reduced (~1.80 V) by nanocomposite (GO + SPEEK) interface. U_diss recorded with SPEEK + GO as interface was much lower than some of the recently reported homogeneous BPM. The NaOH production from NaCl (1.0 mol?L^?1) solution in a bipolar membrane electrodialysis set up containing synthesized HBM with nanocomposite interface (SPEEK + GO) was double than that of NaOH concentration obtained with HBM having no interface, where the current density was fixed at 50.0 mA·cm^?2. Careful optimization of monopolar/interface layer thickness and composition of nanocomposite interface results in developing cost effective HBMs facilitating water dissociation at lower potential.     

Highly effective electrodialysis for selective elimination of nitrates from drinking water

This paper considers a new and highly effective process for selective elimination of nitrates from drinking water through electrodialysis. It is based on coupled use of a modified anion exchange membrane with a nitrate-selective anion exchange resin. The latter is placed in the desalination compartment and constitutes a part of a new type of ion-conducting intermembrane spacer. A highly preferential transport of nitrate anions against chlorides and sulphates is observed to take place at low current densities. The results obtained prove that electrodialysis is a practical solution to the problem of selective elimination of nitrates from drinking water.     

采用柱后抑制器技术降低流动相中三氟乙酸对质谱信号抑制作用的研究

研究柱后抑制器(CSRS)技术有效降低流动相中三氟乙酸(TFA)对质谱信号的抑制.采用双三元液相系统,左泵以反相模式分离细胞色素C酶解肽段(流动相含0.1%TFA,流速0.25 m L/min),柱后选择CSRS作为抑制器.同时右泵提供碳酸氢铵(浓度为0.05 mol/L,流速1.00 m L/min)作为再生液.碳酸氢铵和三氟乙酸在抑制器CSRS中通过阴离子交换膜进行离子交换,降低流动相中TFA离子抑制效应,提高肽段在质谱上的响应(S/N提高1~16倍).采用柱后抑制器技术对硫酸依替米星主成分及杂质进行定性分析(0.2 mol/L TFA),流动相经过抑制器后由强酸性变成中性,实现样品在LC和MS之间无缝连接分析.     

Capillary electrochromatography using a fluoropolymer as the chromatographic support material

Fused-silica capillary columns were packed with ethylene chlorotrifluoroethylene (ECTFE) particles for use in capillary electrochromatography (CEC). Electroosmotic flow (EOF) was generated in these columns using acetonitrile-water mixtures as the mobile phase. Electroosmotic mobilities of 1.6 x 10(-4) cm2 V(-1) s(-1) (linear velocities of 1 mm s(-1)) were observed using a mobile phase without an electrolyte present. The EOF in the ECTFE-packed columns is enhanced when using trifluoroacetic acid (TFA) as a mobile phase additive; electroosmotic mobilities of 3.65 x 10(-4) cm2 (V-1) s(-1) (linear velocity of 2.5 mm s(-1)) were observed. This enhancement of EOF is attributed to dynamic coating of the ECTFE particles by TFA. Other electrolytes (i.e., Tris/Tris-HCl buffer and H3PO4) in the mobile phase did not have such an enhancement of EOF. However, a slight enhancement of EOF is observed, for example, if small quantities of TFA are added to the mobile phase containing Tris buffer. The potential of ECTFE for CEC is demonstrated by separating a mixture of amino acids.     

Correction of pH of diluted solutions of electrolytes by electrodialysis with bipolar membranes

The current efficiencies of the water dissociation water and the voltage-current characteristics of the bipolar (asymmetric bipolar) membranes were measured in a two-chamber electrochemical cell. The cell was formed of an MB-3 bipolar membrane or an asymmetric bipolar membrane, which is an MA-40 heterogeneous membrane with a thin surface layer in the form of a cation-selective homogeneous film and MA-40 and MA-41 heterogeneous monopolar membranes. The dissociation of water on MA-40 in 0.01 M sodium chloride decreased the current efficiency of the acid and alkali both in the channel with a bipolar membrane and in the channel with an asymmetric bipolar membrane. The effective ion transport numbers across MA-40 and MA-41 at different pH values were determined. The water dissociation rate on MA-40 decreased at pH > 9.5. A kinetic model of the electrodialysis of a dilute solution of sodium chloride in a two-chamber unit cell with a bipolar and anionite membranes was suggested.     

双极膜技术在环境工程中的应用与展望

简述了双极膜的水解离电渗析及双重电荷排斥性能。介绍了双极膜在含氟废液的处理、有价氟的回收应用、垃圾发酵连续制备有机酸、脱除烟气中的SO2气体、水处理以及双极膜蓄电池等方面的应用现状及前景。双极膜作为一种新型膜,以其水解离电渗析的独特优点,为解决环境工程中存在已久的一些技术难题提供了许多新的思路和解决办法。巧妙地利用双极膜与单极膜的组合,可以设计出许多工艺。双极膜在环境工程中的应用研究值得引起重视。     

Operational variables in high-performance liquid chromatography-electrospray ionization mass spectrometry of peptides and proteins using poly(styrene-divinylbenzene) monoliths

Capillary reversed-phase high-performance liquid chromatography (RP-HPLC) utilizing monolithic poly(styrene-divinylbenzene) columns was optimized for the coupling to electrospray ionization mass spectrometry (ESI-MS) by the application of various temperatures and mobile phase additives during peptide and protein analysis. Peak widths at half height improved significantly upon increasing the temperature and ranged from 2.0 to 5.4 s for peptide and protein separations at 70 degrees. Selectivity of peptide elution was significantly modulated by temperature, whereas the effect on proteins was only minor. A comparison of 0.10% formic acid (FA), 0.050% trifluoroacetic acid (TFA), and 0.050% heptafluorobutyric acid (HFBA) as mobile phase additives revealed that highest chromatographic efficiency but poorest mass spectrometric detectabilities were achieved with HFBA. Clusters of HFBA, water, and acetonitrile were observed in the mass spectra at m/z values >500. Although the signal-to-noise ratios for the individual peptides diverged considerably both in the selected ion chromatograms and extracted mass spectra, the average mass spectrometric detectabilities varied only by a factor of less than 1.7 measured with the different additives. Limits of detection for peptides with 500 nl sample volumes injected onto a 60 mm x 0.20 mm monolithic column were in the 0.2-13 fmol range. In the analysis of hydrophobic membrane proteins, HFBA enabled highest separation selectivity at the cost of lower mass spectral quality. The use of 0.050% TFA as mobile phase additive turned out to be the best compromise between chromatographic and mass spectrometric performance in the analysis of peptides and proteins by RP-HPLC-ESI-MS using monolithic separation columns.     

ESI-MS of Peptides in the Presence of <Emphasis Type="SmallCaps">l</Emphasis>-Ascorbic Acid

A mass spectrometric method with electrospray ionisation (ESI-MS) is described for detection and quantification of selected peptides [glutathione, phytochelatin 2, bombesin, salmon luteinising hormone, and peptide fragment Cys(Xx)₁₂]. A reaction coil was used to introduce a solution of sample in mobile phase consisting of acetonitrile (ACN) and an aqueous solution of trifluoroacetic acid (TFA). l-Ascorbic acid (AA), which substantially increased the abundance of the molecular ions of the peptides analysed, was added to aqueous solutions of the peptides or amino acids at a final concentration of 10 mM. This addition probably eliminated the negative effect on the ionisation processes of the strong acid TFA present in the mobile phase, thus enabling analysis of lower concentrations of the peptides.     

反相高效液相色谱法分离蛋白质的研究

采用反相高效液相色谱法考察了几种大孔硅胶烷基键合固定相在等度淋洗条件下进行蛋白质分离的色谱性能。研究了冲洗剂中有机溶剂异丙醇的浓度、离子对酸（ＴＦＡ）浓度对蛋白质保留时间的影响。探讨了蛋白质在ＲＰ－ＨＰＬＣ中的保留机理。结果表明,大孔硅胶（２０～３０ｎｍ）短链（Ｃ４和Ｃ８）烷基键合固定相适合蛋白质的分离。     

Membrane electrodialysis process for recovery of sulfur dioxide from power plant stack gases

A new regenerative process for recovery of sulfur dioxide from stack gases by sodiumbased solution scrubbing is described. The spent solution from the scrubber, consisting mostly of bisulfite, is converted through the use of a novel low-energy membrane electrodialysis technique to a basic solution of sulfite/hydroxide suitable for reuse in the SO₂ absorbers, and a solution of sulfurous acid from which concentrated SO₂ is easily regenerated. p]This electrodialysis process, based on bipolar membrane technology, requires only a fraction of the energy required in conventional electrolysis. Engineering estimates indicate that this membrane/SO₂ process has a significant economical advantage over other gas desulfurization processes. In addition, this process has internal flexibility to operate under various conditions without the requirement of significant equipment modification.     

Optimum concentration of trifluoroacetic acid for reversed-phase liquid chromatography of peptides revisited

Trifluoroacetic acid (TFA) remains the dominant mobile phase additive for reversed-phase high-performance liquid chromatography (RP-HPLC) of peptides after more than two decades since its introduction to this field. Generally, TFA has been employed in a concentration range of 0.05-0.1% (6.5-13 mM) for the majority of peptide separations. In order to revisit the question as to whether such a concentration range is optimum for separations of peptide mixtures containing peptides of varying net positive charge, the present study examined the effect of varying TFA concentration on RP-HPLC at 25 and 70 degrees C of three groups of synthetic 10-residue synthetic peptides containing either one (+1) or multiple (+3, +5) positively charged groups. The results show that the traditional range of TFA concentrations employed for peptide studies is not optimum for many, perhaps the majority, of peptide applications. For efficient resolution of peptide mixtures, particularly those containing peptides with multiple positive charges, our results show that 0.2-0.25% TFA in the mobile phase will achieve optimum resolution. In addition, the use of high temperature as a complement to such TFA concentration levels is also effective in maximizing peptide resolution.     

The perchlorate anion is more effective than the trifluoroacetate anion as an ion-pairing reagent for reversed-phase chromatography of peptides

The addition of salts, specifically sodium perchlorate (NaClO4), to mobile phases at acidic pH as ion-pairing reagents for reversed-phase high-performance liquid chromatography (RP-HPLC) has been generally overlooked. To demonstrate the potential of NaClO4 as an effective anionic ion-pairing reagent, we applied RP-HPLC in the presence of 0-100 mM sodium chloride (NaCl), sodium trifluoroacetate (NaTFA) or NaClO4 to two mixtures of synthetic 18-residue peptides: a mixture of peptides with the same net positive charge (+4) and a mixture of four peptides of +1, +2, +3 and +4 net charge. Interestingly, the effect of increasing NaClO4 concentration on increasing peptide retention times and selectivity changes was more dramatic than that of either NaCl or NaTFA, with the order of increasing anion effectiveness being Cl- < TFA- < C104-. Such effects were more marked when salt addition was applied to eluents containing 10 mM phosphoric acid (H3PO4) compared to 10 mM trifluoroacetic acid (TFA) due to the lesser starting anion hydrophobicity of the former mobile phase (containing the phosphate ion) compared to the latter (containing the TFA- ion).     

Potentiometric and theoretical studies of the carbonate sensors based on 3-bromo-4-hexyl-5-nitrotrifluoroacetophenone

Novel carbonate ionophore, trifluoroacetophenone derivative (TFA) substituted by two acceptor substituents in the phenyl ring (3-bromo-4-hexyl-5-nitrotrifluoroacetophenone), was synthesized. Solvent polymeric membrane sensors based on this ionophore exhibited heightened selectivity to carbonate ions in the presence of the most important interfering anions. A wide range of potentiometric properties were studied and compared with those of sensors based on mono-substituted ionophores. Special attention was paid to pH dependence of sensor responses and to elaboration of appropriate conditions for carbonate analysis. A segmented-sandwich membrane method was applied for determination of the stoichiometry of ionophore-carbonate complexes, which was determined to be 1:3, and apparent complex formation constants which were 14.4 and 13.6 for DOS- and NPOE-plasticized membranes, respectively. Theoretical studies on TFA derivatives by semi-empirical (AM1 and PM3) and ab initio(6-31+G*) methods were performed, considering different types of possible ionophore-ion interactions. The formation of hydrogen bonds between carbonate and hydrated TFA was proved to be much more favourable in terms of energy compared to tetrahedral nucleophilic adducts that earlier were postulated to being formed in the membrane phase. The final conclusion on the mechanism of carbonate sensing by TFA-based solvent polymeric membrane sensors was made on the basis of computational data and detailed analysis of the literature.     

mPAM/mCMC双极膜电解槽中MnO2电催化氧化制备甘油醛

分别以FeCl3和戊二醛等对羧甲基纤维素(CMC)和聚丙烯酰胺(PAM)进行改性, 制备了mPAM/mCMC双极膜. 测定了PAM、CMC胶体的电荷密度, mPAM/mCMC双极膜离子交换能力、I-V工作曲线等参数. 用扫描电镜和红外光谱对膜形貌与成分作表征, 膜厚≈260 μm, 中间界面层厚为纳米级. 热重分析表明膜具有较好的热稳定性. 以mPAM/mCMC双极膜为电解槽的隔膜, 间接电氧化甘油为甘油醛. 在电场的作用下, 双极膜中间层中的水离解产生H＋和OH&#8722;, OH&#8722;及时地传输入阳极室, 中和了电生成甘油醛时生成的H＋, 促进了正向反应的进行. 槽电压稳定, 产率达91.6%, 电流效率为65.5%.     

反相液相色谱法制备纯化柠檬苦素类似物配糖体

 利用反相制备液相色谱结合吸附树脂柱色谱和离子交换色谱方法 ,从甜橙种子的提取物中纯化制备了一种柠檬苦素类似物配糖体 ,经 NMR测定为奥巴叩酮配糖体。