[1]CHEN Wei-hang,ZHOU Hui,JIANG Yuan-li,et al.Vapor-liquid Equilibrium for 2-Methoxyethanol-Methyl Glycollate under Vacuum[J].Journal of Zhengzhou University (Engineering Science),2013,34(02):11-14.[doi:10.3969/j.issn.1671-6833.2013.02.004]
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Journal of Zhengzhou University (Engineering Science)[ISSN
1671-6833/CN
41-1339/T] Volume:
34
Number of periods:
2013 02
Page number:
11-14
Column:
Public date:
2013-03-28
- Title:
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Vapor-liquid Equilibrium for 2-Methoxyethanol-Methyl Glycollate under Vacuum
- Author(s):
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CHEN Wei-hang1; ZHOU Hui1; JIANG Yuan-li2; ZHOU Bao-hong1; CHEN Jun-hang1; ZHANG Hao-qin1
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1.School of Chemical Engineering and Energy , Zhengzhou University , Zhengzhou 450001, China; 2.Henan Coal Chemical In-dustry Group Co. Ltd., Zhengzhou 450001 ,China
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- Keywords:
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vapor-liquid equilibrium; 2-methoxyethanol; methyl glycollate; vacuum
- CLC:
-
TQ013.1
- DOI:
-
10.3969/j.issn.1671-6833.2013.02.004
- Abstract:
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The vapor-liquid equilibrium(VLE) data of 2-methoxyethanol-methyl glycollate binary system weremeasured under the pressure of 50mmHg by using a VLE still,and the obtained data satisfy the thermodynam-ic consistencies . Then the VLE data were correlated by NRTL\Wilson\UNIQUAC models,and the corre-sponding binary interaction parameters of these models were obtained. With these models associated with thebinary system of VLE data, the average relative deviations of temperature between calculated and experimentalvalues were 0.2215% ,0.2398% ,0.2374% respectively ; the average relative deviations of 2-methoxyethanol’s vapor mass fraction were 3.7216% ,3.4378% ,3.338% respectively.The simulation results are close to ex-perimental values and these models are suitable to be used for the engineering seperation design.