共查询到17条相似文献，搜索用时 230 毫秒
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以乙醇-水为实验体系,在常压下对JLT-97型筛板精馏塔的操作性能进行了研究,获得了该塔在全回流及部分回流条件下的全塔效率,固定回流比间歇精馏下的塔顶、塔釜温度及浓度随时间的变化曲线等.结果表明该塔操作性能稳定,可作为科研和分离提纯小批料使用. 相似文献
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通过对精馏实验设备进行改造,在每套设备上安装了回流温度测定装置,并要求学生在冷液回流的操作条件下进行精馏试验,自己设定回流温度、进料热状态、回流比等实验参数,通过对精馏过程的物料衡算和热量衡算,确定精馏塔的内回流量及精馏段操作线方程,并进行精馏分离效果的分析。 相似文献
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本文对筛板精馏塔的性能进行全面的测试,主要对低浓度乙醇精馏过程中的不同实验操作条件进行探讨,得出了塔釜浓度、回流比、进料量、进料位置等与全塔效率的关系,确定了该筛板精塔的最优实验操作条件。 相似文献
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陈国瑞 《重庆第二师范学院学报》2004,17(6):17-19
实验室制备乙酸乙酯目前主要用两种方法:第一种是半连续操作的酯化-蒸馏方法,第二种是先回流酯化,然后蒸馏的方法.第一种方法对酯化反应不利,操作困难且装置较复杂,可采用将滴液漏斗与三颈瓶联通或采用恒压漏斗来改进其操作.第二种方法先回流酯化,然后蒸馏,则回流结束后要先冷却,再将回流装置拆装为蒸馏装置,比较繁琐.笔者不用回流装置,只在蒸馏烧瓶上增加一分馏柱,其余不变,组成间歇精馏装置,操作方便,且更符合酯化反应机理,产品的产量和产率较高. 相似文献
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连续精馏实验影响因素关系测定 总被引：1，自引：0，他引：1
采用甲醇-丙酮物系进行实验,通过改变回流比以及进料液流速这两个条件,观察分析分离效果,总结出连续精馏实验影响因素的关系以及实验室连续精馏的最佳操作条件.随回流比的增大,塔顶馏分的浓度的变化关系是先增大再降低.随进料液流速的增大,塔顶馏分的浓度变化是逐步增大,增大到一定值就基本维持平稳不变.最佳操作条件是回流比R=3,进料液流速=6ml/min.在此操作条件下甲醇丙酮的分离效果最佳. 相似文献
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Azeotropic liquid mixture cannot be separated by conventional distillation. But extractive distillation or combination of the two can be valid for them. An experiment to separate benzene and cyclohexane by batch extractive distillation was carried out with N,N-dimethylformide (DMF), dimethyl sulfoxide (DMSO) and their mixture as extractive solvent. The effect of the operation parameters such as solvent flow rate and reflux ratio on the separation was studied under the same operating conditions. The results show that the separation effect was improved with the increase of solvent flow rate and the reflux ratio; all the three extractive solvents can separate benzene and cyclohexane, with DMF being the most efficient one, the mixture the second, and DMSO the least. In the experiment the best operation conditions are with DMF as extractive solvent, the solvent flow rate being 12.33 mL/min, and the reflux ratio being 6. As a result, we can get cyclohexane from the top of tower with the average product content being 86.98%, and its recovering ratio being 83.10%. 相似文献
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The pulse-control operation technique which alternates between total reflux operation and total efflux operation in batch distillation was studied along with the minimum amount of slop cut. Total reflux time was confirmed by dynamic simulation, and total efflux time was adopted by statistic method. For the mixture of hexane and cyclohexane and the traditional constant reflux ratio operation strategy, the amount of slop cut is 1.8-2.1 times of the minimum amount of slop cut; whereas for the pulse-control operation strategy, it is 1.2-1.4 times of the minimum amount of slop cut. So compared with the traditional constant reflux ratio operation, the pulse-control operation can decrease the amount of slop cut and operation time, and meanwhile, enhance separation efficiency and yield. 相似文献
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大工程观背景下开放型化工仿真实验的教学实践 总被引：6，自引：1，他引：5
在大工程观背景下分析了化工原理实验的地位。以石油炼制常减压蒸馏流程级仿真为例,从工程优势的角度探讨了开放型化工仿真实验教学的实践。最后,指出大工程观的理念指导下,开放型化工仿真实验的教学实践为培养创新型高素质工程人才做出了应有的贡献。 相似文献
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DMF萃取精馏法精制乙酸乙酯的过程模拟研究 总被引：1，自引：0，他引：1
本文利用化工流程模拟软件AspenPlus采用萃取精馏,以DMF为萃取剂,对乙酸乙酯生产中的产品精制进行了模拟计算,详细分析了理论板数、进料位置、溶剂比和回流比对产品浓度的影响。结果表明,最优工艺方案为：理论板数40,粗酯进料位置29,萃取剂进料位置6,溶剂比1.6,回流比2.0,塔顶产品乙酸乙酯含量达到99.9%,质量达到GB/T3728-2007优等品标准,为分离过程的优化操作和设计提供依据。 相似文献
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The batch extractive distillation (BED) process has the advantages of both batch and extractive distillation. It is one of the most promising means for the separation of azeotropic and close-boiling point systems. However, so far this process has not been applied in industry due to its over-complexity. A new shortcut model was proposed to simulate the operation of the batch extractive distillation operations. This algorithm is based on the assumption that the batch extractive distillation column can be considered as a continuous extractive distillation column with changing feed at any time. Namely, the whole batch process is simulated as a succession of a finite number of steady states of short duration, in which holdup is considered as constant mole. For each period of time the batch extractive distillation process is solved through the algorithm for continuous extractive distillation. Finally, the practical implementation of the shortcut model is discussed and data from the laboratory and literature are presented. It is found that this model has better adaptability, more satisfactory accuracy and less calculative load than previous rigorous model. Hence the algorithm for simulating BED is verified. 相似文献
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利用N-甲基甲酰胺（NMF）作萃取剂,萃取精馏分离醋酸和水混合物。利用Aspen Plus流程模拟软件对分离过程进行了模拟计算,确定了理论板数、加料板位置、回流比、加料比等最佳工艺条件及工艺参数。结果表明,利用NMF作萃取剂可以较好的实现醋酸和水的分离,醋酸的纯度可达99.94%,萃取剂可以循环利用;与普通精馏法相比,相同分离任务下,萃取精馏工艺的再沸器热负荷降低了60.4%,生产每吨醋酸再沸器消耗蒸汽量由7.1吨降低到2.8吨。说明萃取精馏法分离醋酸和水优于普通精馏法,节能效果明显,为工业化装置提供了重要的理论依据和设计参考。 相似文献