Standing-wave Design of Three-Zone, open-loop non-isocratic SMB for purification

David Harvey, Yi Ding, Nien-Hwa Linda Wang
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Abstract

Chromatography with step changes in modulator properties such as pH, solvent strength, or ionic strength to facilitate desorption is widely used in the purification of proteins and other chemicals. Step changes can be incorporated into non-isocratic simulated moving beds; however, applications of such systems have been limited because one must select numerous operating parameters (zone velocities and port velocities). The operating parameters must be selected correctly to achieve high purity, yield, and productivity and depend on a large number of system parameters (feed, material, and equipment parameters). To address this challenge, the Standing-Wave Design method has been developed for three-zone, open-loop, non-isocratic, and non-ideal systems with both linear and non-linear isotherms. This method directly links the operating parameters to the system parameters. The operating parameters can be solved from a set of algebraic equations. In contrast, for non-ideal systems, previous literature design methods require extensive search using rate model simulations, which involve solving partial differential equations at each grid point. Two examples were tested for the effectiveness of the SWD method using rate model simulations. In both examples, sorbent productivity was pressure limited. Higher pressure sorbents or equipment would lead to higher sorbent productivity. In the first example, a 3-zone open-loop simulated moving bed was designed and compared with an optimal batch step-wise elution system. Compared to batch step-wise elution systems, the simulations showed that the 3-zone open-loop SMB could give an order of magnitude higher productivity in systems with weakly competing impurities and two orders of magnitude higher in systems with strongly adsorbing impurities. In the second example, the simulations showed that an SMB designed using the Standing-Wave method could achieve an order of magnitude higher productivity than a system designed using the Triangle Theory.

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净化用三区开环非等压SMB驻波设计
随着调制剂性质(如pH值、溶剂强度或离子强度)的阶跃变化,色谱法促进解吸,被广泛用于蛋白质和其他化学物质的纯化。阶跃变化可以纳入非等距模拟移动床;然而,这种系统的应用受到限制,因为必须选择许多操作参数(区域速度和端口速度)。必须正确选择操作参数,以实现高纯度,产量和生产率,并依赖于大量的系统参数(饲料,材料和设备参数)。为了应对这一挑战,针对具有线性和非线性等温线的三区、开环、非等温和非理想系统,开发了驻波设计方法。这种方法直接将运行参数与系统参数联系起来。运行参数可由一组代数方程求解。相比之下,对于非理想系统,以前的文献设计方法需要使用速率模型模拟进行广泛的搜索,这涉及在每个网格点上求解偏微分方程。通过速率模型模拟测试了两个实例的SWD方法的有效性。在这两个例子中,吸附剂的产量都受到压力限制。更高压力的吸附剂或设备将导致更高的吸附剂生产率。在第一个算例中,设计了一个3区开环模拟移动床,并与最优分批阶跃洗脱系统进行了比较。模拟结果表明,与间歇式逐步洗脱系统相比,3区开环SMB在具有弱竞争杂质的系统中生产率提高了一个数量级,在具有强吸附杂质的系统中生产率提高了两个数量级。在第二个例子中,模拟表明,使用驻波方法设计的SMB比使用三角理论设计的系统的生产率高一个数量级。
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