Determination of a suitable index for a solvent via two-column extractive distillation using a heuristic method
Zhaoyou Zhu, Guoxuan Li, Yao Dai, Peizhe Cui, Dongmei Xu, Yinglong Wang
Determination of a suitable index for a solvent via two-column extractive distillation using a heuristic method
The traditional approach to solvent selection in the extractive distillation process strictly focuses on the change in the relative volatility of light-heavy components induced by the solvent. However, the total annual cost of the process may not be minimal when the solvent induces the largest change in relative volatility. This work presents a heuristic method for selecting the optimal solvent to minimize the total annual cost. The functional relationship between the relative volatility and the total annual cost is established, where the main factors, such as the relative volatility of the light-heavy components and the relative volatility of the heavy-component solvent, are taken into account. Binary azeotropic mixtures of methanol-toluene and methanol-acetone are separated to verify the feasibility of the model. The results show that using the solvent with the minimal two-column extractive distillation index, the process achieves a minimal total annual cost. The method is conducive for sustainable advancements in chemistry and engineering because a suitable solvent can be selected without simulation verification.
heuristic method / solvent selection / extractive distillation / total annual cost
[1] |
Sholl D S, Lively R P. Seven chemical separations to change the world. Nature, 2016, 532(7600): 316
CrossRef
Google scholar
|
[2] |
Wang Y L, Zhang Z, Xu D F, Liu W, Zhu Z Y. Design and control of pressure-swing distillation for azeotropes with different types of boiling behavior at different pressures. Journal of Process Control, 2016, 42: 59–76
CrossRef
Google scholar
|
[3] |
Zhu Z Y, Wang L L, Ma Y X, Wang W L, Wang Y L. Separating an azeotropic mixture of toluene and ethanol via heat integration pressure swing distillation. Computers & Chemical Engineering, 2015, 76: 137–149
CrossRef
Google scholar
|
[4] |
Pla-Franco J, Lladosa E, Loras S, Montón J B. Thermodynamic analysis and process simulation of ethanol dehydration via heterogeneous azeotropic distillation. Industrial & Engineering Chemistry Research, 2014, 53(14): 6084–6093
CrossRef
Google scholar
|
[5] |
Ahmadian Behrooz H. Robust synthesis of the pressure-swing distillation process under azeotropic feed composition disturbance—study of the tetrahydrofuran/methanol system. Computers & Chemical Engineering, 2017, 104: 211–230
CrossRef
Google scholar
|
[6] |
Yu H, Ye Q, Xu H, Zhang H, Dai X. Design and control of dividing-wall column for tert-butanol dehydration system via heterogeneous azeotropic distillation. Industrial & Engineering Chemistry Research, 2015, 54(13): 3384–3397
CrossRef
Google scholar
|
[7] |
Li J, Wang T. Coupling reaction and azeotropic distillation for the synthesis of glycerol carbonate from glycerol and dimethyl carbonate. Chemical Engineering and Processing: Process Intensification, 2010, 49(5): 530–535
CrossRef
Google scholar
|
[8] |
Ma K, Yu M X, Dai Y, Ma Y X, Gao J, Cui P Z, Wang Y L. Control of an energy-saving side-stream extractive distillation process with different disturbance conditions. Separation and Purification Technology, 2019, 210: 195–208
CrossRef
Google scholar
|
[9] |
Luyben W L. Control comparison of conventional and thermally coupled ternary extractive distillation processes. Chemical Engineering Research & Design, 2016, 106: 253–262
CrossRef
Google scholar
|
[10] |
Plesu V, Cantero S, Bonet-Ruiz A E, Bonet J, Iancu P, Llorens J. A heuristic for extractive agent flow rate in extractive distillation. Chemical Engineering Transactions, 2018, 70: 1849–1854
|
[11] |
Tauanov Z, Shah D, Inglezakis V, Jamwal P K. Hydrothermal synthesis of zeolite production from coal fly ash: A heuristic approach and its optimization for system identification of conversion. Journal of Cleaner Production, 2018, 182: 616–623
CrossRef
Google scholar
|
[12] |
Golenko-Ginzburg D, Gonik A, Papic L. Developing cost-optimization production control model via simulation. Mathematics and Computers in Simulation, 1999, 49(6): 335–351
CrossRef
Google scholar
|
[13] |
Luyben W L. Improved design of an extractive distillation system with an intermediate-boiling solvent. Separation and Purification Technology, 2015, 156: 336–347
CrossRef
Google scholar
|
[14] |
Kiss A A, David J, Suszwalak P C. Enhanced bioethanol dehydration by extractive and azeotropic distillation in dividing-wall columns. Separation and Purification Technology, 2012, 86: 70–78
CrossRef
Google scholar
|
[15] |
Luyben W L. Comparison of extractive distillation and pressure-swing distillation for acetone/chloroform separation. Computers & Chemical Engineering, 2013, 50: 1–7
CrossRef
Google scholar
|
[16] |
Zhang Z G, Huang D H, Lv M, Jia P, Sun D Z, Li W X. Entrainer selection for separating tetrahydrofuran/water azeotropic mixture by extractive distillation. Separation and Purification Technology, 2014, 122: 73–77
CrossRef
Google scholar
|
[17] |
Li G Z, Bai P. New operation strategy for separation of ethanol–water by extractive distillation. Industrial & Engineering Chemistry Research, 2012, 51(6): 2723–2729
CrossRef
Google scholar
|
[18] |
Zhao Y T, Ma K, Bai W T, Du D Q, Zhu Z Y, Wang Y L, Gao J. Energy-saving thermally coupled ternary extractive distillation process by combining with mixed entrainer for separating ternary mixture containing bioethanol. Energy, 2018, 148: 296–308
CrossRef
Google scholar
|
[19] |
Quijada-Maldonado E, Meindersma G W, de Haan A B. Pilot plant study on the extractive distillation of toluene–methylcyclohexane mixtures using NMP and the ionic liquid [hmim][TCB] as solvents. Separation and Purification Technology, 2016, 166: 196–204
CrossRef
Google scholar
|
[20] |
Ebrahimzadeh E, Matagi J, Fazlollahi F, Baxter L L. Alternative extractive distillation system for CO2–ethane azeotrope separation in enhanced oil recovery processes. Applied Thermal Engineering, 2016, 96: 39–47
CrossRef
Google scholar
|
[21] |
Ebrahimzadeh E, Baxter L L. Plant-wide control of coupled distillation columns with partial condensers. Applied Thermal Engineering, 2016, 102: 785–799
CrossRef
Google scholar
|
[22] |
Aniya V, De D, Singh A, Satyavathi B. Design and operation of extractive distillation systems using different class of entrainers for the production of fuel grade tert-butyl Alcohol: A techno-economic assessment. Energy, 2018, 144: 1013–1025
CrossRef
Google scholar
|
[23] |
An Y, Li W S, Li Y, Huang S Y, Ma J, Shen C L, Xu C J. Design/optimization of energy-saving extractive distillation process by combining preconcentration column and extractive distillation column. Chemical Engineering Science, 2015, 135: 166–178
CrossRef
Google scholar
|
[24] |
Rodríguez-Donis I, Gerbaud V, Joulia X. Entrainer selection rules for the separation of azeotropic and close-boiling-temperature mixtures by homogeneous batch distillation process. Industrial & Engineering Chemistry Research, 2001, 40(12): 2729–2741
CrossRef
Google scholar
|
[25] |
Deorukhkar O A, Rahangdale T B, Mahajan Y S. Entrainer selection approach for distillation column. International Journal of Chemical Engineering Research, 2016, 8: 29–38
|
[26] |
Malone M F, Glinos K, Marquez F E, Douglas J M. Simple, analytical criteria for the sequencing of distillation columns. AIChE Journal. American Institute of Chemical Engineers, 1985, 31(4): 683–689
CrossRef
Google scholar
|
[27] |
Rod V, Marek J. Separation sequences in multicomponent rectification. Collection of Czechoslovak Chemical Contributions, 1959, 24(10): 3240–3248
CrossRef
Google scholar
|
[28] |
Zhang X, Li X, Li G X, Zhu Z Y, Wang Y L, Xu D M. Determination of an optimum entrainer for extractive distillation based on an isovolatility curve at different pressures. Separation and Purification Technology, 2018, 201: 79–95
CrossRef
Google scholar
|
[29] |
Porter K E, Momoh S O. Finding the optimum sequence of distillation columns-an equation to replace the “rules of thumb” (heuristics). Chemical Engineering Journal, 1991, 46(3): 97–108
CrossRef
Google scholar
|
[30] |
Li Y, Xu C J. Pressure-swing distillation for separating pressure-insensitive minimum boiling azeotrope methanol/toluene via introducing a light entrainer: Design and control. Industrial & Engineering Chemistry Research, 2017, 56(14): 4017–4037
CrossRef
Google scholar
|
[31] |
Underwood A J V. Fractional distillation of multi-component mixtures. Chemical Engineering Progress, 1948, 44: 603–614
|
[32] |
Fenske M R, Quiggle D, Tongberg C O. Composition of straight-run pennsylvania gasoline. Industrial & Engineering Chemistry, 1932, 24(4): 408–418
CrossRef
Google scholar
|
[33] |
Wang Y, Zhang X, Liu X B, Bai W T, Zhu Z Y, Wang Y L, Gao J. Control of extractive distillation process for separating heterogenerous ternary azeotropic mixture via adjusting the solvent content. Separation and Purification Technology, 2018, 191: 8–26
CrossRef
Google scholar
|
[34] |
Sadegh N, Stenby E H, Thomsen K. Thermodynamic modeling of CO2 absorption in aqueous N-Methyldiethanolamine using Extended UNIQUAC model. Fuel, 2015, 144: 295–306
CrossRef
Google scholar
|
[35] |
Gmehling J, Menke J, Krafczyk J, Fischer K. Azeotropic Data. Wancouver: Wiley-VCH, 1994
|
[36] |
Muñoz R, Monton J B, Burguet M C, De la Torre J. Separation of isobutyl alcohol and isobutyl acetate by extractive distillation and pressure-swing distillation: Simulation and optimization. Separation and Purification Technology, 2006, 50(2): 175–183
CrossRef
Google scholar
|
[37] |
Arifin S, Chien I L. Design and control of an isopropyl alcohol dehydration process via extractive distillation using dimethyl sulfoxide as an entrainer. Industrial & Engineering Chemistry Research, 2008, 47(3): 790–803
CrossRef
Google scholar
|
[38] |
Douglas J M. Conceptual design of chemical processes. New York: McGraw-Hill, 1988
|
[39] |
Extractive distillation optimization software. V1.0. Qingdao University of Science & Technology, 2015
|
[40] |
Li L M, Guo L J, Tu Y Q, Yu N, Sun L Y, Tian Y Y, Li Q S. Comparison of different extractive distillation processes for 2-methoxyethanol/toluene separation: Design and control. Computers & Chemical Engineering, 2017, 99: 117–134
CrossRef
Google scholar
|
[41] |
Liang S S, Cao Y J, Liu X Z, Li X, Zhao Y T, Wang Y K, Wang Y L. Insight into pressure-swing distillation from azeotropic phenomenon to dynamic control. Chemical Engineering Research & Design, 2017, 117: 318–335
CrossRef
Google scholar
|
[42] |
Zhu Z Y, Xu D F, Liu X Z, Zhang Z, Wang Y L. Separation of acetonitrile/methanol/benzene ternary azeotrope via triple column pressure-swing distillation. Separation and Purification Technology, 2016, 169: 66–77
CrossRef
Google scholar
|
[43] |
Modla G, Lang P. Separation of an acetone-methanol mixture by pressure-swing batch distillation in a double-column system with and without thermal integration. Industrial & Engineering Chemistry Research, 2010, 49(8): 3785–3793
CrossRef
Google scholar
|
[44] |
Gil I D, Botia D C, Ortiz P, Sanchez O F. Extractive distillation of acetone/methanol mixture using water as entrainer. Industrial & Engineering Chemistry Research, 2009, 48(10): 4858–4865
CrossRef
Google scholar
|
/
〈 | 〉 |