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pH- and Concentration-Programmable Electrodialytic Buffer Generator

机译:pH和浓度可编程的电渗析缓冲液发生器

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We have presented in a companion paper a suppressor-based electro-dialytic buffer generator (EBG) that can produce programmable pH gradients. Here we demonstrate a three-electrode EBG. In this three-compartment flow-through device, the central compartment is separated from the outer compartments with a cation-exchange membrane (CEM) and an anion-exchange membrane (AEM), respectively. One platinum electrode is disposed in each compartment. The flows through each compartment are independent. With appropriate solutions in each compartment, independent potentials are applied to the CEM and AEM electrodes with respect to the grounded central electrode. The CEM current and the AEM current can be independently manipulated to generate buffers with variable concentration and pH in the central compartment. Both the CEM and AEM currents can be positive or negative. For the CEM, a positive current (i_(cat)~(in)) indicates that cations are coming in from the CEM channel to the center. A negative current (i_(cat)~(out)) takes cations out of the center to the CEM channel. Similarly for the AEM, currents governing anion transport into the center channel from the AEM channel (AEM electrode negative) or the reverse (AEM electrode positive) are respectively denoted by i_(an)~(in) or i_(an)~(out). Most examples herein involve inward ion transport, referred to as the additive mode. Depending on whether i_(cat)~(in) < i_(an)~(in) or i_(cat)~(in) > i_(an)~(in), H~(+)/O_(2) and OH~(-)/H_(2) are respectively produced at the central electrode to maintain electroneutrality. Any gas formed is subsequently removed by a gas removal device. The pH of the central channel effluent is related to the ratio of the currents through the two membranes, while the generated concentration is controlled by the absolute value of the currents. The buffer concentration and pH can be varied in a controlled predictable manner. A pH span of 3-12 was attained and a phosphate buffer concentration up to 140 mM was generated. We demonstrate a variety of combined pH/concentration gradients from a mixture of ethylenediamine, citrate, and phosphate by manipulating i_(cat)~(in), which controls introduction of the ethylenediammonium ion, and i_(an)~(in), which controls the introduction of citrate and phosphate ions. We also demonstrate an additive-subtractive mode of operation where both inward and outward currents are used to add one type of ion while removing another type of ion to reproducibly generate pH/concentration gradients.
机译:我们在随附的论文中介绍了一种基于抑制器的电渗析缓冲液发生器(EBG),它可以产生可编程的pH梯度。在这里,我们演示了三电极EBG。在该三室流通装置中,中央室与外部室分别通过阳离子交换膜(CEM)和阴离子交换膜(AEM)隔开。每个隔室中布置一个铂电极。通过每个隔室的流量是独立的。通过在每个隔室中使用适当的溶液,相对于接地的中心电极,将独立的电势施加到CEM和AEM电极。可以独立操纵CEM电流和AEM电流,以在中央隔室中生成浓度和pH值可变的缓冲液。 CEM和AEM电流都可以为正或负。对于CEM,正电流(i_(cat)〜(in))表示阳离子从CEM通道进入中心。负电流(i_(cat)〜(out))将阳离子从中心带到CEM通道。类似地,对于AEM,控制阴离子从AEM通道(AEM电极负极)或反向(AEM电极正极)进入中心通道的电流分别表示为i_(an)〜(in)或i_(an)〜(out )。本文中的大多数示例都涉及向内离子迁移,称为加性模式。取决于i_(cat)〜(in) i_(an)〜(in),H〜(+)/ O_(2)和OH〜(-)/ H_(2)分别在中心电极处产生,以保持电子中性。随后形成的任何气体通过除气装置去除。中央通道流出物的pH与通过两个膜的电流之比有关,而生成的浓度由电流的绝对值控制。缓冲液浓度和pH值可以以可控的方式变化。 pH跨度达到3-12,产生的磷酸盐缓冲液浓度高达140 mM。我们通过控制i_(cat)〜(in)(控制引入乙烯二铵离子和i_(an)〜(in))来演示乙二胺,柠檬酸盐和磷酸盐混合物的各种组合的pH /浓度梯度。控制柠檬酸根和磷酸根离子的引入。我们还演示了加减法操作模式,其中使用内向和外向电流添加一种离子,同时去除另一种离子以可重现地生成pH /浓度梯度。

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