硅胶与羟乙基纤维素复合涂料的水吸附性能

Lucas Lovis, Andrew Maddocks, Priscilla Tremain, Behdad Moghtaderi
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引用次数: 0

摘要

水资源短缺是一个日益重要的全球性问题。干燥剂包覆换热器是一种潜在的大气制水吸附反应器,它可以通过对环境湿度的后续吸附、解吸和冷凝来缓解水资源短缺。微孔和介孔硅胶是常见的廉价干燥剂,具有中等的吸附和解吸速率,因此适用于多循环大气制水。为了准确模拟基于硅胶的干燥剂涂层热交换器-大气制水系统的行为,使用热重分析测量了不同涂层厚度、羟乙基纤维素粘合剂浓度、温度和相对湿度条件下硅胶的动力学和平衡特性。此外,用扫描电镜、氮吸附和比容仪分别测量了样品的粒径、孔隙结构特性和密度。涂层内的平均粒径随着羟乙基纤维素浓度的增加而增大。与粉末样品相比,涂层样品的平衡吸收率较低,并且不强烈依赖于吸附温度。动力学常数和最大理想比水量与涂层厚度呈负相关,与羟乙基纤维素浓度的关系不强。吸附顺序和动力学常数的变化取决于是否发生单层吸附、多层吸附、孔隙填充或毛细冷凝。在较厚的吸附层和较低的吸附温度下,吸附机理的变化对动力学常数的影响较小。在测量条件下,涂层样品的最大理想比水量为57 L kg−1 day−1。
本文章由计算机程序翻译,如有差异,请以英文原文为准。
Water adsorption properties of silica gel and hydroxyethyl cellulose composite coatings
Water scarcity is an increasingly significant global issue. Desiccant coated heat exchangers are a potential adsorption reactor for atmospheric water generation, which can alleviate water scarcity through the subsequent adsorption, desorption, and condensation of ambient humidity. Microporous and mesoporous silica gels are common and inexpensive desiccants that demonstrate moderate adsorption and desorption rates, and hence are suitable for multicyclic atmospheric water generation. To accurately model the behaviour of silica gel based desiccant coated heat exchanger-atmospheric water generation systems, the kinetic and equilibrium properties of silica gel were measured for varying coating thicknesses, hydroxyethyl cellulose binder concentrations, temperatures, and relative humidity conditions using thermogravimetric analysis. Additionally, the particle size, pore textural properties, and density of the samples were measured using scanning electron microscopy, nitrogen adsorption, and pycnometry respectively. The average particle size within the coatings increased with increasing hydroxyethyl cellulose concentration. The equilibrium uptake was lower for the coating samples compared to the powder sample and was not strongly dependant on the adsorption temperature. The kinetic constants and maximum ideal specific water production were inversely related to the coating thickness and were not strongly dependant on the hydroxyethyl cellulose concentration. The adsorption order and kinetic constant varied depending on whether monolayer adsorption, multilayer adsorption, pore filling, or capillary condensation were occurring. The effect of the change in adsorption mechanism on the kinetic constant was less significant for thicker layers and lower adsorption temperatures. The maximum ideal specific water production for the coating samples within the set of measured conditions was 57 L kg−1 day−1.
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