Aspen plus在“物理化学”课程精馏分离中的教学应用

将Aspen Plus化工流程模拟软件运用到工科“物理化学”课程精馏分离过程教学中,结合二甲醚(DME)-甲醇-水三元体系精馏分离的科研成果案例,探讨了Aspen Plus软件在精馏分离过程教学中的应用。实践表明,采用流程模拟软件辅助精馏分离的教学方法,不仅有助于加深学生对精馏分离理论知识点的理解,提高课程教学质量,而且有助于培养学生利用流程模拟技术解决工程实际问题的能力,提升了学生的综合素质。     

基于Aspen Plus的煤层气精馏分离案例教学探讨

为帮助学生掌握“煤矿区煤层气利用技术”基本理论,结合煤层气低温精馏分离科研成果案例,运用Aspen Plus流程模拟软件对煤层气气液相平衡和低温精馏过程进行模拟和案例教学,根据煤层气精馏分离工艺要求,进行精馏塔操作变量计算和灵敏度分析,分析操作变量变化对精馏过程的影响,让学生直观了解塔内各参数的变化,掌握精馏分离操作,加深了对煤层气分离理论的理解,极大地提高了教学效率和质量,提升了学生的综合素质。     

基于化工模拟的氨法烟气脱硫工艺设计案例教学探讨

在化工设计课程教学中将科研项目成果“氨法烟气脱硫工艺设计项目”转化为典型教学案例,并结合现代化工设计方法,引入化工模拟软件Aspen Plus进行化工过程设计,让学生更直观地理解气液两相吸收过程所涉及的化学反应设计、分离序列的选择与应用、能量匹配与集成优化等,使课程理论教学更加生动,将复杂的化工设计过程讲解透彻,提高教学质量,提高学生实际工程设计能力。     

加热状态选择对近沸体系丙烯/丙烷分离能耗影响的探讨

以近沸体系丙烯/丙烷分离为例介绍了化工模拟软件Aspen Plus在化工原理精馏单元的应用,研究了加热状态选择对能耗和年总费用的影响.为了提高学生工程实践能力,探讨了泡点、露点、过冷、过热、气液混合(气化率0.5)等5种进料状态分离丙烯/丙烷对能耗和经济费用的影响,在塔板数、进料板进料温度与压力、塔顶丙烯出料纯度不变条件下,过冷进料的常规工艺流程和泡点塔顶蒸气再压缩热泵工艺流程能耗和年度总费用(TAC)最小.相比常规工艺流程,塔顶蒸气再压缩热泵精馏工艺流程泡点进料可节能65％,年费用节约56％.     

基于Aspen Plus软件对制药化工原理精馏实验的模拟与分析

介绍并探讨了Aspen Plus化工流程模拟软件在“制药化工原理精馏实验”操作型问题分析中的应用.实践表明,采用该流程模拟软件辅助解决精馏实验操作问题,可以把精馏过程中复杂计算和繁琐图解过程化为直观、简单、精确、高效的计算,便于学生的理解和掌握, 提高了学生的学习积极性,不仅拓宽学生的视野,使学生加深了对精馏原理的深刻理解,而且有助于培养学生利用流程模拟技术解决工程实际问题和科研问题.     

基于地方特色开发的化工过程模拟实验——以变压精馏为例

基于六盘水地区海拔高、气压低的特点,开设了具有地方特色的变压精馏过程模拟实验,低压塔设定为六盘水地区大气压值。以变压精馏分离乙酸甲酯-甲醇共沸物为例,通过相图确定精馏序列及工艺流程,讨论了进料位置、回流比和塔板数等变量对年度总费用TAC的影响,对于学生掌握化工技术和经济分析具有良好的教学效果。同时,对于培养人才的工程实践能力和服务地方产业提供了有效的保障。     

加碱萃取精馏制取无水乙醇

乙醇-水体系存在共沸点，难以通过普通精馏方法制取高纯度乙醇，萃取精馏是分离共沸体系的有效途径。目前常用的萃取溶剂是乙二醇。在分离乙醇-水体系的过程中，将适当的盐类(醋酸钾)溶于乙二醇形成溶盐萃取剂，会有效提高溶剂的选择性。本文用萃取精馏方法并加入乙二醇分离效果更明显。     

流程模拟软件Aspen Plus在化工原理课程设计教学中的应用

介绍了化工原理课程设计的特点和重要性,通过实例说明流程模拟软件Aspen Plus在课程设计教学中的应用。应用DSTWU模型进行简捷设计计算、应用灵敏度分析优化工艺流程、应用RadFrac模型进行严格精馏计算、塔板或填料的设计与校核,并与手工计算结果进行对比。实践经验表明,将流程模拟软件同传统课程设计相结合的教学方式拓宽了教师的选题范围,提高了课程设计的质量和效率,强化了学生的工程意识,提高了课程的教学质量。     

基于Aspen Plus耦合生命周期评价的科研案例在环境工程原理教学中的应用

将化工流程模拟Aspen Plus软件与环境影响评估领域常用的生命周期评价(LCA)进行集成应用,围绕环境工程原理教学中有关化工过程质量能量衡算与环境污染防治内容的协同应用与拓展,构建化工流程模拟-环境风险评估科研案例“苯酐生产流程模拟及环境风险研究”,并将其作为环境工程原理的综合教学案例。教学实践经验表明,通过引入工程相关综合教学案例,不仅使得抽象的理论知识更加生动具体,而且在深化学生对课程理论知识理解的同时,提高学生应用专业知识分析和解决化工生产环境污染工程问题的综合能力和素质,为学生将来步入相关领域工作奠定扎实的基础。     

膜蒸馏分离甲酸-水共沸混合物

共沸混合物的分离通常是采用共沸蒸馏或萃取蒸馏来进行。本文研究了用膜蒸馏技术来分离甲酸-水共沸混合物的可能性。结果表明,采用膜蒸馏来处理甲酸-水溶液时不存在共沸现象。表明膜蒸馏在分离共沸物方面具有潜在的应用价值。     

Design of extractive distillation process with mixed entrainer

The separation of two systems containing minimum boiling azeotropes (acetone—methanol and tetrahydrofuran (THF)—water) was performed using extractive distillation with a heavy boiling mixed entrainer consisting of two compounds. The entrainer constituents did not form new azeotropes with each other and with the components of the original mixture. An analysis of the mixed entrainer influence on the vapor-liquid equilibrium (VLE) and relative volatility provides an understanding of the cases in which the separation by extractive distillation (ED) in the presence of the mixed entrainer revealed energy benefits over their individual constituents. New results for application of the mixed entrainer monoethanolamine (MEA)—ethylene glycol (EG) and dimethyl-sulphoxide (DMSO)—glycerol for the separation of THF—water and acetone—methanol, respectively, are presented for the first time. The individual selective agents were chosen from the efficient entrainers discussed in the literature. The calculations were performed using the platform Aspen Plus 7.3. Different extractive distillation flowsheets are provided for the zeotropic mixed agents, viz. with two or three columns. For the ED of the binary mixtures investigated, the structures of the different separation schemes, the operating parameters of the columns, and the energy consumptions are presented and compared. The application of the mixed entrainer MEA—EG fed into the ED column with pre-mixing can be recommended, providing up to 1.7 % of energy saving for acetone—methanol separation. In the case of THF—water, the mixed entrainer DMSO—glycerol provides 0.8 % of energy saving. The separate inputs of the individual constituents of the mixed entrainer led to a significant increase in the energy consumptions of the flowsheet because of the third regeneration column, hence this flowsheet cannot be recommended for use in the separation of both mixtures.     

醋酸H2O精馏中萃取剂的计算机辅助筛选

醋酸H2O精馏中萃取剂的计算机辅助筛选;Flash;萃取剂筛选;萃取精馏;醋酸     

膜蒸馏海水淡化实验——介绍一个新型的膜分离化工实验

介绍了一个应用于本科教学的膜分离化工实验项目,实验中考查了膜蒸馏海水淡化的效果。学生从本实验中了解了膜蒸馏相关的前沿知识,学习了膜蒸馏海水淡化的实验技术,同时增加了将科技成果转变为生产力的应用意识。     

Ionic liquids in separations of azeotropic systems – A review

Efforts to make existing separation methods more efficient and eco-friendly may get a boost from the use of a relatively new class of compounds known as ionic liquids (ILs). The separation of azeotropic mixtures has conventionally been one of the most challenging tasks in industrial processes due to the fact that their separation by simple distillation is basically impossible.This paper provides a critical review of methods using ILs as azeotrope breakers. Three separation processes were addressed: liquid–liquid extraction, extractive distillation, and supported liquid membranes. We examine the azeotrope breaking potential of ILs and compare their performance to that of conventional solvents. A systematic analysis of the influence of the structure of ILs on their azeotrope breaking capacity contributes to the establishment of guidelines for selecting the most suitable ILs for the separation of specific azeotropic mixtures.     

神华煤液化油窄馏分的临界性质

引入Aspen Plus软件,用COAL LIQ模块计算得到神华煤液化油300℃以前8个窄馏分的临界温度、临界压力、临界体积。同时利用MXXC基团贡献法,以GC MS数据为基准对8个馏分的临界性质进行验证计算。结果表明,计算结果与利用化学结构法测定的基本一致。随馏出温度的提高,馏分临界温度逐渐升高,临界压力先升高再降低,临界体积先减小后增大,转折点出现在180℃~200℃馏分段。通过对化合物的结构分析表明,馏分中大量极性化合物的富集是造成计算数据点转折及跳跃的原因。为验证两种计算方法的一致性,引入斯米尔切诺夫统计检验法进行分析。结果表明,两种方法计算结果的总体分布函数在95%的置信区间内一致,表明对于计算临界性质,Aspen Plus计算方法可以代替基团贡献法估算法。此外,Aspen软件计算简便,其结果可为煤液化反应器的放大及过程优化直接引用。     

闯关式与翻转式结合的课堂教学方法——以化工原理课程为例

Flipped classroom and open classroom are both new teaching modes to improve the efficiency of teaching. Based on the combination of these two teaching strategies and the principles of chemical engineering course, this article uses the distillation section as an example to illustrate the implement process of this teaching mode. In light of the characteristics of the principles of chemical engineering course, we design and introduce the combination of the flipped and open classroom into teaching, and results of this strategy, mainly including teaching analysis, teaching strategy, teaching process and effectiveness. We come up with teaching methods and modes that are well suited to the learning characteristics of undergraduates, aiming to provide references.     

高温高压下煤液化油气液平衡体系的研究

煤液化过程中,反应单元和分离单元是整个液化体系的核心部分,反应器和分离器中各组分在气、液相中的平衡组成确定不仅决定设备的尺寸设计,而且对液化过程中供氢溶剂的选择和反应条件的优化起到关键作用。但由于煤液化油在高温高压下的气、液平衡数据不足,使得反应器内的组成分布无法预测,相关的反应器设计过程仅能凭经验进行。为得到反应条件下的气液平衡数据,研究引入流程模拟软件Aspen Plus,将煤液化油蒸馏得到的窄馏分段与各种气体组分（如H₂、C₂H₆等）共同建立了煤液化油闪蒸过程,得到了高温高压下煤液化油气液平衡体系。利用闪蒸体系计算得到在给定温度、压力情况下,各组分在高温、低温分离器内的气、液两相分布情况,通过改变高温分离器的温度和压力,分析了高温分离器内相平衡常数随温度（623.15K~723.15K）、压力（10MPa~21MPa）变化的规律。为进一步归纳适用于煤液化油的气液平衡方程,以高温分离器数据为基础,对推导建立的高压下烃类相平衡方程中的参数进行回归,得到高温高压下,适用于神华煤液化油并具有物理意义的二元（T,p）气液相平衡常数方程。     

萃取精馏过程的非平衡态热力学分析

对萃取精馏过程进行了非平衡热力学分析,提出了分离过程得以进行的判据.推导出了熵产生的数学表达式,并可将其用于萃取精馏过程的节能分析.此项研究结果只适用于萃取精馏板式塔,且在非平衡热力学的线性区域内     

Evaluation of liquid-liquid extraction process for separating acrylic acid produced from renewable sugars

In this article, the separation and the purification of the acrylic acid produced from renewable sugars were studied using the liquid-liquid extraction process. Nonrandom two-liquids and universal quasi-chemical models and the prediction method universal quasi-chemical functional activity coefficients were used for generating liquid-liquid equilibrium diagrams for systems made up of acrylic acid, water, and solvents (diisopropyl ether, isopropyl acetate, 2-ethyl hexanol, and methyl isobutyl ketone) and the results were compared with available liquid-liquid equilibrium experimental data. Aspen Plus (Aspen Technology, Inc., version 2004.1) software was used for equilibrium and process calculations. High concentration of acrylic acid was obtained in this article using diisopropyl ether as solvent.