共查询到17条相似文献,搜索用时 120 毫秒
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设计了CO_2降膜吸收反应器,对比了四种工质20%MEA、20%IL、5%IL+15%MEA、10%IL+10%MEA吸收CO_2性能。结果表明:工质5%[N_(1111)][Gly]+15%MEA每摩尔胺吸收的CO_2量最大,且其CO_2吸收能力被完全利用程度高达89.0%。选取5%[N_(1111)][Gly]+15%MEA为吸收剂,考察了液体流量,液体温度,气体流量,气体进口CO_2浓度对5%[N1111][Gly]+15%MEA吸收剂降膜吸收性能的影响.结果表明:吸收速率随液体流量先增加之后下降,随液体温度、气体流量及气体进口CO_2浓度的增加而增加. 相似文献
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旋转床填料空间液体的液相传质分析 总被引:4,自引:0,他引:4
1前言旋转床。又称Higee或超重机,是八十年代初发展起来的一种新型、高效的传质分离设备[1],图1为其示意图。由填料和填料框构成的转子安装在固定的外壳内,并以每分钟数百至数千转的转速旋转。其中,液体在强离心力(上千倍于重力)作用下,由转子中心沿径向向外甩出,在填料床内与向内的气体逆向接触,进行复杂的热、质传递。屈指可数的传质理论模型系建立在填料表面液膜的基础上[2],而实验表明:旋转填料层空间内飞行的液体(滴、丝、膜)可能是传质的主体[2]。为此,本文将首先试探建立滴、丝和膜传质的理论模型,用它们分析计算在… 相似文献
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This article presents the research on the air–water system flowing in a pipe section with electrical heating with a wire-mesh bed inside it. The heat flux was determined and so was the convective heat transfer coefficient for the two-phase flow through a pipe length that had been completely or partially filled with the wire-mesh packing. The packing level was found to strongly affect the heat transfer potential. Also, the dominant role was identified for a liquid in the heat exchange process under two-phase gas–liquid flow through the wire-mesh packing. 相似文献
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Convective heat transfer coefficients were measured experimentally for a tube immersed vertically in a circulating fluidized bed. Circulating fluidized beds operate in the dilute transport regime of two-phase (solid/gas) flow. The dominant mechanism for heat transfer to surfaces is particle-induced convection. In this study, experiments were carried out in a circulating fluidized bed of15 cm diameter and 11 m height. An instrumented tube of 9.5 mm diameter and 1.3 m length was placed vertically at the centeriine of the fluidized bed to measure convective heat transfer coefficients at several different elevations in the bed. Three types of particles, with mean diameters ranging from 68 to 2S1 urn, were used in the experiments at superficial gas velocities in the range of 1.3 to 8.2 m/s. Results showed that the convective heat transfer coefficients with solid/gas two-phase circulation were two to three times greater than those for single-phase gas convection at the same velocity. For a given gas velocity, the coefficients increased with increasing solid mass flux, but decreased with elevation. It was demonstrated that the heat transfer coefficients for the immersed tube and for the bed wall could be correlated with different functional dependence on the two-phase suspension density. 相似文献
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多孔介质内受迫对流凝结时两相共存区的非达西模型 总被引:2,自引:0,他引:2
本文提出多孔介质内受迫对流凝结时两相共存区的二维非达西流模型。分析了蒸气在多孔介质内沿水平平板和填充国管内受迫对流凝结时两相共存区的厚度。假定局部平衡和暂先假设蒸气为理想气体,化简了能量方程。 相似文献