Department of Chemistry and Biochemistry, University of Texas at Arlington, Arlington, Texas 76019-0065, USA.
Anal Chem. 2012 Jan 3;84(1):59-66. doi: 10.1021/ac2023734. Epub 2011 Dec 12.
We have presented in a companion paper a suppressor-based electrodialytic 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.
我们在一篇相关的论文中介绍了一种基于抑制剂的电渗析缓冲液生成器(EBG),它可以产生可编程的 pH 梯度。在这里,我们展示了一种三电极 EBG。在这个三隔室流动装置中,中央隔室分别与阳离子交换膜(CEM)和阴离子交换膜(AEM)隔开。每个隔室都有一个铂电极。每个隔室的流动是独立的。在每个隔室中使用适当的溶液,通过对与接地中央电极相对的 CEM 和 AEM 电极施加适当的电势,可以独立控制 CEM 和 AEM 电流,从而在中央隔室中产生具有可变浓度和 pH 的缓冲液。CEM 电流和 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))将阳离子从中心带出到 CEM 通道。对于 AEM 也是如此,控制阴离子从 AEM 通道进入中心通道的电流(AEM 电极负)或相反(AEM 电极正)分别表示为 i(an)(in)或 i(an)(out)。本文中的大多数示例都涉及到离子的内向运输,称为加和模式。根据 i(cat)(in)是否小于 i(an)(in)或 i(cat)(in)是否大于 i(an)(in),在中央电极处分别产生 H(+) / O(2) 和 OH(-) / H(2)以维持电中性。随后通过气体去除装置去除任何形成的气体。中央通道流出物的 pH 值与通过两个膜的电流之比有关,而产生的浓度则由电流的绝对值控制。缓冲液浓度和 pH 值可以以可控和可预测的方式变化。通过操纵 i(cat)(in),我们实现了 3-12 的 pH 跨度和 140mM 的磷酸盐缓冲液生成。通过操纵 i(cat)(in),我们控制了乙二胺离子的引入,通过操纵 i(an)(in),我们控制了柠檬酸盐和磷酸盐离子的引入,实现了由乙二胺、柠檬酸盐和磷酸盐组成的混合物的各种组合 pH/浓度梯度。我们还展示了一种加和-减和模式的操作,其中同时使用内向和外向电流来添加一种离子,同时去除另一种离子,以可重复地生成 pH/浓度梯度。