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监测与控制基于沸石合成反应器的解决方案:一种补料分批策略。

Monitoring and controlling zeolite synthesis reactor-based solutions: a fed-batch strategy.

作者信息

Javdani Amirhossein, Ivanushkin Gleb, Deneyer Aron, Dusselier Michiel

机构信息

Center for Sustainable Catalysis and Engineering (CSCE), KU Leuven 3001 Leuven Belgium

出版信息

React Chem Eng. 2024 Nov 28;10(2):379-391. doi: 10.1039/d4re00440j. eCollection 2025 Jan 28.

Abstract

Most conventional zeolite synthesis takes place in closed batch autoclaves that cannot be monitored or controlled during the process. Moreover, the study of time-dependent parameters of the synthesis with the conventional "cooling-opening" procedure not only reduces accuracy as a series of reactors (never 100% identical) needs to be started in parallel (and stopped at different times), it is also labor intense. Furthermore, the classic batch concept does not permit the intermediate addition of species without disrupting synthesis and the cooling-reheating effects. In this study, we developed a technique for zeolite synthesis monitoring in one-pot experiments using the sampling feature of fed-batch (FB) reactors. These one-pot syntheses can save time and ingredients instead of performing plenty of classic batch experiments. In addition, we could control and manipulate the zeolite synthesis by using the feeding function of the FB reactor and the intermediate addition of precursors at operational temperatures and pressures. Stannosilicate and zincosilicate syntheses were carried out the FB reactor to investigate the intermediate timed-addition and the possibility of optimizing feeding rates of heteroatoms opposed to a classic synthesis, which faces challenges when a high amount of heteroatom precursor presents at the start. Finally, a modified FB platform was further developed to be able to monitor essential kinetic and synthetic parameters on-line (, , and also pH) on-line without intervention. For instance, pH profiles can allow one to estimate key events in zeolite synthesis, but in the art, these profiles are always measured (including cooling effects ).

摘要

大多数传统的沸石合成是在密闭的间歇式高压釜中进行的,在此过程中无法对其进行监测或控制。此外,采用传统的“冷却-开启”程序来研究合成过程中随时间变化的参数,不仅会降低准确性,因为需要同时启动一系列反应器(永远不会100%相同)(并在不同时间停止),而且劳动强度大。此外,经典的间歇式概念不允许在不干扰合成以及冷却-再加热效应的情况下中间添加物质。在本研究中,我们开发了一种利用补料分批(FB)反应器的取样功能在一锅法实验中监测沸石合成的技术。这些一锅法合成可以节省时间和原料,而无需进行大量经典的间歇式实验。此外,我们可以通过利用FB反应器的进料功能以及在操作温度和压力下中间添加前驱体来控制和操纵沸石合成。在FB反应器中进行了锡硅酸盐和锌硅酸盐的合成,以研究中间定时添加以及与经典合成相比优化杂原子进料速率的可能性,经典合成在开始时存在大量杂原子前驱体时面临挑战。最后,进一步开发了一种改进的FB平台,能够在线监测基本的动力学和合成参数(温度、压力以及pH)而无需干预。例如,pH曲线可以使人们估计沸石合成中的关键事件,但在现有技术中,这些曲线总是离线测量(包括冷却效应)。

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