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二乙醇胺水溶液的表面张力研究 被引量:7
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作者 付东 钟智坤 +1 位作者 吕建燚 华雪莹 《华北电力大学学报(自然科学版)》 CAS 北大核心 2010年第6期81-84,89,共5页
二乙醇胺(Diethanolamine,DEA)水溶液的表面张力是二氧化碳醇胺吸收工艺的基础数据。用ZBY-1全自动表面张力仪测定了25~82℃温度范围内,DEA水溶液的表面张力,并用经验公式对实验数据进行了关联,关联结果与实验值吻合良好。应用关联的公... 二乙醇胺(Diethanolamine,DEA)水溶液的表面张力是二氧化碳醇胺吸收工艺的基础数据。用ZBY-1全自动表面张力仪测定了25~82℃温度范围内,DEA水溶液的表面张力,并用经验公式对实验数据进行了关联,关联结果与实验值吻合良好。应用关联的公式,研究了表面熵和表面焓等热力学性质与温度和溶液浓度之间的关系。 展开更多
关键词 乙醇胺水溶液 二氧化碳 表面张力
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N—甲基二乙醇胺水溶液物化数据的测定 被引量:3
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作者 吴宝存 《石油与天然气化工》 CAS 1983年第3期1-5,共5页
一、前言 1.实验目的 N—甲基二乙醇胺(分子式C_5H_(13)O_2N,分子量119.16)水溶液是新发展起来的天然气脱硫溶液,试验证明,它对选择性吸收硫化氢表现出明显的优越性。为此。
关键词 N-甲基二乙醇胺水溶液 物化数据 测定 密度-比重瓶法 表面张力-双毛细管法 比热-直接加热法 饱和蒸汽压-静态测定法
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CO_(2)在单乙醇胺溶液吸收塔中的传质阻力模拟研究 被引量:2
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作者 李宁 陈义峰 +3 位作者 叶南南 戴正兴 吉晓燕 陆小华 《南京工业大学学报(自然科学版)》 CAS 北大核心 2022年第1期28-35,共8页
为了探究吸收塔内CO_(2)传质随着塔高变化情况,进一步指导吸收塔强化。将吸收塔分为“塔顶”“塔中”“塔底”3个部分,通过鼓泡吸收实验分别对“塔顶”“塔中”“塔底”处单乙醇胺(MEA)水溶液吸收CO_(2)行为进行模拟,获得不同位置的CO_... 为了探究吸收塔内CO_(2)传质随着塔高变化情况,进一步指导吸收塔强化。将吸收塔分为“塔顶”“塔中”“塔底”3个部分,通过鼓泡吸收实验分别对“塔顶”“塔中”“塔底”处单乙醇胺(MEA)水溶液吸收CO_(2)行为进行模拟,获得不同位置的CO_(2)出口体积分数。结果表明,根据双膜理论和传递的连续性建立动力学模型对实验数据进行分析,获得模拟塔“塔顶”“塔中”“塔底”处CO_(2)的吸收速率、吸收量和传质阻力,“塔中”吸收速率是“塔顶”吸收速率的1.7倍,是“塔底”吸收速率的3.7倍;“塔中”吸收量是“塔顶”吸收量的1.7倍,是“塔底”吸收量的4.4倍;“塔底”的阻力是“塔中”阻力的6.8倍,是“塔顶”阻力的9.2倍。因此“塔顶”阻力最小,“塔中”吸收量和吸收速率最大,“塔底”阻力最大,“塔底”吸收量和吸收速率最小。吸收塔的“塔底”是CO_(2)处理能力最弱的部位,对“塔底”进行设计改造有望提高吸收塔处理CO_(2)的能力。 展开更多
关键词 CO_(2) 乙醇胺(MEA)水溶液 传质阻力 吸收塔
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MEA-CO_2-水溶液表面张力实验和模型 被引量:2
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作者 付东 徐怡斐 +1 位作者 王兰芬 陈丽虹 《中国科学:化学》 CAS CSCD 北大核心 2012年第6期865-872,共8页
用全自动表面张力仪测定了293.15-323.15K温度范围内,具有不同C02载荷的乙醇胺(Monoethanolamine,MEA)水溶液的表面张力,提出了计算MEA-CO2-水体系表面张力的半经验模型,计算结果与实验值吻合良好.通过实验和计算相结合,阐明... 用全自动表面张力仪测定了293.15-323.15K温度范围内,具有不同C02载荷的乙醇胺(Monoethanolamine,MEA)水溶液的表面张力,提出了计算MEA-CO2-水体系表面张力的半经验模型,计算结果与实验值吻合良好.通过实验和计算相结合,阐明了温度、MEA浓度和C02载荷对MEA-CO2-水体系表面张力的影响规律. 展开更多
关键词 乙醇胺水溶液 CO2载荷 表面张力
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Process Characteristics of CO2 Absorption by Aqueous Monoethanolamine in a Microchannel Reactor 被引量:7
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作者 叶春波 陈光文 袁权 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2012年第1期111-119,共9页
Process characteristics of CO2 absorption using aqueous monoethanolamine (MEA) in a microchannel reactor were investigated experimentally in this work. A T-type rectangular microchannel with a hydraulic diameter of ... Process characteristics of CO2 absorption using aqueous monoethanolamine (MEA) in a microchannel reactor were investigated experimentally in this work. A T-type rectangular microchannel with a hydraulic diameter of 408μm was used. Operating parameters, i.e. temperature, pressure and molar ratio of MEA to CO2 were studied. Under 3 MPa pressure, the mole fraction of CO2 in gaslphase could decrease from 32.3% to 300×10-6 at least when gas hourly space velocity ranged from 14400 to 68600 h- and molar ratio of MEA to CO2 was kept at 2.2. In particular, the effects of temperature on CO2 absorption flux, mass transfer driving force, gas-liquid contact time and en- hancement factor were analyzed in detail and found that mass transfer enhancement by chemical reaction was a crucial factor for the orocess of CO9 absorotion. 展开更多
关键词 miniatui'ization MICROCHANNEL microfluidic carbon dioxide ABSORPTION MONOETHANOLAMINE
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A New Method to Solve Film Model for CO_2 Absorption with Aqueous Solution of AT-Methyldiethanolamine 被引量:1
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作者 钟战铁 李伟 +2 位作者 施耀 何锋 周明华 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2003年第4期441-445,共5页
The shooting method and the difference method are used for numerical simulation of CO2 absorption with aqueous solution of methyldiethanolamine (MDEA). It is demonstrated that these methods are available for the stead... The shooting method and the difference method are used for numerical simulation of CO2 absorption with aqueous solution of methyldiethanolamine (MDEA). It is demonstrated that these methods are available for the steady-state model, which may be expressed as a set of differential algebraic equations (DAEs) with two-point boundary values. This method makes it possible not only to obtain the concentration profiles for MDEA system, but also to reveal the effect of CO2 interfacial concentration on the enhancement factor. With this numerical simulation, the mass transfer process with multicomponent diffusion and reactions can be better understood. 展开更多
关键词 film model numerical simulation carbon dioxide METHYLDIETHANOLAMINE
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The Swelling Equilibria of N-isopropylacrylamide Based Hydrogel in Aqueous Solution of Ethanol 被引量:3
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作者 许小平 HüTHER Andreas MAURER Gerd 《Chinese Journal of Chemical Engineering》 SCIE EI CAS CSCD 2003年第3期264-268,共5页
N-isopropylacrylamide (NIPAAm) was used to synthesize NIPAAm homopolymer (nonionized) and NIPAAm-sodium methacrylate copolymer (ionized). The swelling equilibria for both gels were obtained in aqueous solution of etha... N-isopropylacrylamide (NIPAAm) was used to synthesize NIPAAm homopolymer (nonionized) and NIPAAm-sodium methacrylate copolymer (ionized). The swelling equilibria for both gels were obtained in aqueous solution of ethanol with concentration ranging from 0 to 100%(by mass) at 25℃. The swollen gel in water shrank first with the addition of a small amount of ethanol and then reswelled with further addition of ethanol showing not only a discontinuous volume phase transition but also a typical reentrant phenomenon. A thermodynamic model based on the UNIQUAC with the 'free-volume' contribution was applied to correlate and predict the swelling behavior of the poly(NIPAAM)-gels in ethanol-water mixture. 展开更多
关键词 HYDROGEL SWELLING poly(N-isopropylacrylamide) model
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CO_2 solubility in aqueous solutions of N-methyldiethanolamine+piperazine by electrolyte NRTL model 被引量:1
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作者 Jicai Huang Maoqiong Gong +2 位作者 Xueqiang Dong Xiaodong Li Jianfeng Wu 《Science China Chemistry》 SCIE EI CAS CSCD 2016年第3期360-369,共10页
Accurate modeling of the solubility behavior of CO_2 in the aqueous alkanolamine solutions is important to design and optimization of equipment and process. In this work, the thermodynamics of CO_2 in aqueous solution... Accurate modeling of the solubility behavior of CO_2 in the aqueous alkanolamine solutions is important to design and optimization of equipment and process. In this work, the thermodynamics of CO_2 in aqueous solution of N-methyldiethanolamine(MDEA) and piperazine(PZ) is studied by the electrolyte non-random two liquids(NRTL) model. The chemical equilibrium constants are calculated from the free Gibbs energy of formation, and the Henry's constants of CO_2 in MDEA and PZ are regressed to revise the value in the pure water. New experimental data from literatures are added to the regression process. Therefore, this model should provide a comprehensive thermodynamic representation for the quaternary system with broader ranges and more accurate predictions than previous work. Model results are compared to the experimental vapor-liquid equilibrium(VLE), speciation and heat of absorption data, which show that the model can predict the experimental data with reasonable accuracy. 展开更多
关键词 N-METHYLDIETHANOLAMINE PIPERAZINE carbon dioxide electrolyte NRTL
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Experiments and model for the surface tension of carbonated monoethanolamine aqueous solutions 被引量:2
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作者 FU Dong XU YiFei +1 位作者 WANG LanFen CHEN LiHong 《Science China Chemistry》 SCIE EI CAS 2012年第7期1467-1473,共7页
The surface tension of carbonated monoethanolamine aqueous solutions from 293.15 to 323.15 K was measured by using an automatic surface tension-meter.A model applicable for the surface tension of MEA-CO2-water mixture... The surface tension of carbonated monoethanolamine aqueous solutions from 293.15 to 323.15 K was measured by using an automatic surface tension-meter.A model applicable for the surface tension of MEA-CO2-water mixtures was proposed and the calculated results agreed well with the experiments.The influences of temperature,MEA concentration and CO2 loading were demonstrated on the basis of experiments and calculations. 展开更多
关键词 MEA aqueous solution CO2 loading surface tension
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