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在非生物环境中固体表面上水蒸汽冷凝时的传热和传质现象的特性——在生物工艺中的应用。

Characterization of simultaneous heat and mass transfer phenomena for water vapour condensation on a solid surface in an abiotic environment--application to bioprocesses.

机构信息

Laboratoire de Génie Chimique et Biochimique (LGCB), Clermont Université, Université Blaise Pascal, BP10488, 63000 Clermont-Ferrand, France.

出版信息

Appl Biochem Biotechnol. 2012 Jul;167(5):1132-43. doi: 10.1007/s12010-012-9607-x. Epub 2012 Feb 26.

Abstract

The phenomenon of heat and mass transfer by condensation of water vapour from humid air involves several key concepts in aerobic bioreactors. The high performance of bioreactors results from optimised interactions between biological processes and multiphase heat and mass transfer. Indeed in various processes such as submerged fermenters and solid-state fermenters, gas/liquid transfer need to be well controlled, as it is involved at the microorganism interface and for the control of the global process. For the theoretical prediction of such phenomena, mathematical models require heat and mass transfer coefficients. To date, very few data have been validated concerning mass transfer coefficients from humid air inflows relevant to those bioprocesses. Our study focussed on the condensation process of water vapour and developed an experimental set-up and protocol to study the velocity profiles and the mass flux on a small size horizontal flat plate in controlled environmental conditions. A closed circuit wind tunnel facility was used to control the temperature, hygrometry and hydrodynamics of the flow. The temperature of the active surface was controlled and kept isothermal below the dew point to induce condensation, by the use of thermoelectricity. The experiments were performed at ambient temperature for a relative humidity between 35-65% and for a velocity of 1.0 ms⁻¹. The obtained data are analysed and compared to available theoretical calculations on condensation mass flux.

摘要

水蒸气在湿空气中冷凝时的传热和传质现象涉及好氧生物反应器中的几个关键概念。生物反应器的高性能源于生物过程与多相传热和传质的优化相互作用。事实上,在各种过程中,如浸没式发酵罐和固态发酵罐,需要很好地控制气/液传质,因为它涉及微生物界面和整个过程的控制。对于这种现象的理论预测,数学模型需要传热和传质系数。迄今为止,关于与这些生物过程相关的湿空气流入的传质系数,只有很少的数据得到了验证。我们的研究集中在水蒸气的冷凝过程上,开发了一种实验装置和方案,以在受控环境条件下研究小尺寸水平平板上的速度分布和质量通量。使用闭路风洞设施来控制温度、湿度和流动的流体动力学。通过使用热电,主动表面的温度被控制并保持在露点以下以诱导冷凝,从而保持等温。实验在环境温度下进行,相对湿度为 35-65%,速度为 1.0 ms⁻¹。对获得的数据进行了分析,并与可用的冷凝质量通量理论计算进行了比较。

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