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首页> 外文期刊>Chemical Engineering Research & Design: Transactions of the Institution of Chemical Engineers >Development of an efficient emulsification process using miniaturized process engineering equipment
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Development of an efficient emulsification process using miniaturized process engineering equipment

机译:使用小型化的工艺工程设备开发高效的乳化工艺

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摘要

In many cases, emulsification with highly viscous materials is performed batchwise using CSTR systems being heated in a conventional way. A more efficient process may be continuous emulsification using miniaturized equipment like micro heat exchangers and micro mixers. The advantages of such systems like reduced diffusion length and increased heat transfer capacities are widely known, as well as the disadvantages, namely increased pressure losses. The present study describes the development of a continuous oil-in-water emulsification process using microstructured devices. Based on the analysis on the rheological properties, several suitable micro mixer systems were developed and tested. Some experiments under different conditions have been carried out to study the influence of different parameters to the emulsification quality referred to the droplet size. The studied range of the total mass flow rates was from roughly 4 to 9 kg/h. The oil content varied from 52 to 72%. The oil passage was heated to 120 degrees C and the water passage to 88 degrees C. Characterized droplet sizes such as Sauter diameter were used as the main quality criteria. Results show that the higher the flow velocities are, the smaller the Sauter diameter of the emulsion droplets becomes. However, the pH of the products needed to be limited between 7 and 8. In this study, two water solutions were prepared, 1% (for S2-S9) or 2% (for S1) ammonia solution (25 vol.%) was added to the water phase. Large Sauter diameters or phase separation may be faced if the pH is not adjusted correctly. A high oil content or low emulsifier content may also reduce the quality of emulsions.
机译:在许多情况下,使用以常规方式加热的CSTR系统分批进行高粘度材料的乳化。更有效的方法可能是使用微型设备(如微型热交换器和微型混合器)进行连续乳化。这样的系统的优点,例如减小的扩散长度和增加的传热能力,以及缺点,即增加的压力损失,是众所周知的。本研究描述了使用微结构器件的水包油连续乳化工艺的发展。基于对流变特性的分析,开发并测试了几种合适的微型混合器系统。已经进行了一些在不同条件下进行的实验,以研究不同参数对乳化质量的影响(以液滴大小为基准)。总质量流率的研究范围约为4至9 kg / h。含油量从52%到72%不等。将油道加热到120摄氏度,将水道加热到88摄氏度。表征的液滴尺寸(如Sauter直径)用作主要质量标准。结果表明,流速越高,乳液液滴的Sauter直径越小。但是,产品的pH值必须限制在7到8之间。在这项研究中,准备了两种水溶液,分别是1%(对于S2-S9)或2%(对于S1)氨溶液(25%(体积))。添加到水相中。如果pH值调整不正确,可能会遇到较大的索特直径或相分离现象。高油含量或低乳化剂含量也可能降低乳液的质量。

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