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乙醇-碳酸二甲酯-氯苯汽液平衡数据的测定及关联 被引量:1

Measurement and correlation of vapor-liquid equilibria of ethanol-dimethyl carbonate-chlorobenzene
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摘要 测定了101.3 kPa下乙醇-碳酸二曱酯(DMC)和DMC-氯苯二元体系的汽液平衡数据,以及乙醇-DMC-氯苯体系在溶剂比(体积比)为1∶1时的三元汽液平衡数据。采用Herington面积积分法对所得的汽液平衡数据进行热力学一致性检验,并用Wilson模型对数据进行了关联,得到Wilson方程的二元交互作用参数。结果表明:氯苯的加入可以改变乙醇和DMC的相对挥发度,并且当氯苯的摩尔分数大于0.35时,乙醇-DMC二元物系的共沸点消失。因此,可以采用萃取精馏的方法以氯苯为溶剂分离乙醇和DMC的混合物。 Vapor-liquid equilibria of ethanol-dimethyl carbonate ( DMC ), DMC-chlorobenzene and ethanol-DMC- chlorobenzene in a solvent ratio(volume ratio) of 1:1 were measured at 101.3 kPa, and Herington area integration method was used to check the thermodynamic consistency. Furthermore, the experimental data were correlated by means of Wilson equation, in which the binary interaction parameters were also obtained. It shows that chlorobenzene can enlarge the relative volatility of ethanol and DMC, and the azeotropic point disappears when the mole fraction of chlorobenzene reaches 0.35, which demonstrates the feasibility of separating ethanol-DMC using extractive distillation with chlorobenzene as solvent.
出处 《化学工程》 CAS CSCD 北大核心 2013年第6期21-24,共4页 Chemical Engineering(China)
关键词 碳酸二甲酯 乙醇 氯苯 汽液平衡 dimethyl carbonate ethanol chlorobenzene vapor-liquid equilibrium
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  • 1OH J H, HANK J, PARK S J. Measurement and correlation of vapor-liquid equilibria at T = 333. 15 K and excess molar volumes at T = 298. 15 K for ethanol plus dimethyl carbonate (DMC), DMC + l-propanol, and DMC + 1-butanol[ J ]. Journal of Chemical and Engineering Data, 2006, 51(5): 1852-1855. 被引量:1
  • 2FUKANO M. Ebulliometric determination of vapor-liquid equilibria for methanol plus ethanol plus dimethyl carbonate [ J ]. Journal of Chemical and Engineering Data, 2006, 51(4) : 1458-1463. 被引量:1
  • 3LUO H P. Isobaric vapor-liquid equilibria of binary mixtures containing dimethyl carbonate under atmospheric pressure[ J]. Journal of Chemical and Engineering Data, 2001, 46(4) : 842-845. 被引量:1
  • 4赵霞,杨勇,郭睿,贾斌.碳酸二甲酯-乙醇体系等压汽液相平衡[J].化学工程,2010,38(9):54-56. 被引量:4
  • 5PERRY R H, GREEN D W. Perry'S chemical engineers' handbook [ M ]. 7th ed. New York: McGraw- Hill, 1997. 被引量:1
  • 6TASSIOS P D. Extractive and azeotropic distillation: rapid screening of extractive distillation solvent [ M ]. Washington DC: American Chemical Society, 1972. 被引量:1
  • 7时钧等主编..化学工程手册[M].北京:化学工业出版社,1996:1468.
  • 8LO T C, BAIRD M I, HANSON C. Handbook of solvent extraction[ M]. New York: Wiley, 1983. 被引量:1
  • 9FREDENSLUND A, RUSSELL L J, PRAUSNITZ J M. Group-contribution estimation of activity coefficients in nonideal liquid mixtures [ J ]. Aiche Journal, 1975, 21 (6) : 1086-1099. 被引量:1
  • 10GMEHLING J, LOHMANN J, JAKOB A, et al. A modified UNIFAC (Dortmund) model. 3. Revision and extension[J]. Ind Eng Chem Res, 1998, 37(12) : 4876- 4882. 被引量:1

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