Please wait a minute...
Frontiers of Chemical Science and Engineering

ISSN 2095-0179

ISSN 2095-0187(Online)

CN 11-5981/TQ

邮发代号 80-969

2019 Impact Factor: 3.552

Frontiers of Chemical Science and Engineering  2020, Vol. 14 Issue (5): 847-856   https://doi.org/10.1007/s11705-019-1848-6
  本期目录
Thermodynamic analysis of ethanol synthesis from hydration of ethylene coupled with a sequential reaction
Jie Gao1,2, Zhikai Li1(), Mei Dong1, Weibin Fan1, Jianguo Wang1,2
1. State Key Laboratory of Coal Conversion, Institute of Coal Chemistry, Chinese Academy of Sciences, Taiyuan 030001, China
2. University of the Chinese Academy of Sciences, Beijing 100049, China
 全文: PDF(631 KB)   HTML
Abstract

Coal-based ethanol production by hydration of ethylene is limited by the low equilibrium ethylene conversion at elevated temperature. To improve ethylene conversion, coupling hydration of ethylene with a potential ethanol consumption reaction was analyzed thermodynamically. Five reactions have been attempted and compared: (1) dehydration of ethanol to ethyl ether (2C2H5OHC2H5OC2H5+H2O), (2) dehydrogenation of ethanol to acetaldehyde (C2H5OHCH3CHO+H2), (3) esterification of acetic acid with ethanol (C2H5OH+CH3COOHCH3COOC2H5+H2O), (4) dehydrogenation of ethanol to ethyl acetate (2C2H5OHCH3COOC2H5+2H2), and (5) oxidative dehydrogenation of ethanol to ethyl acetate (2C2H5OH+O2CH3COOC2H5+2H2O). The equilibrium constants and equilibrium distributions of the coupled reactions were calculated and the effects of feed composition, temperature and pressure upon the ethylene equilibrium conversion were examined. The results show that dehydrogenation of ethanol to acetaldehyde has little effect on ethylene conversion, whereas for dehydrogenation of ethanol to acetaldehyde and ethyl acetate, ethylene conversion can be improved from 8% to 12.8% and 18.5%, respectively, under conditions of H2O/C2H4 = 2, 10 atm and 300°C. The esterification of acetic acid with ethanol can greatly enhance the ethylene conversion to 22.5%; in particular, ethylene can be actually completely converted to ethyl acetate by coupling oxidative dehydrogenation of ethanol.

Key wordsethylene    ethanol    thermodynamics    coupling
收稿日期: 2019-02-26      出版日期: 2020-05-25
Corresponding Author(s): Zhikai Li,Jianguo Wang   
 引用本文:   
. [J]. Frontiers of Chemical Science and Engineering, 2020, 14(5): 847-856.
Jie Gao, Zhikai Li, Mei Dong, Weibin Fan, Jianguo Wang. Thermodynamic analysis of ethanol synthesis from hydration of ethylene coupled with a sequential reaction. Front. Chem. Sci. Eng., 2020, 14(5): 847-856.
 链接本文:  
https://academic.hep.com.cn/fcse/CN/10.1007/s11705-019-1848-6
https://academic.hep.com.cn/fcse/CN/Y2020/V14/I5/847
Species Δf Hmè /(kJ?mol?1) Δf Gmè /(kJ?mol?1) A B×103 C×106 D×10?5
C2H4 (g) 52.26 68.15 1.424 14.394 ?4.392 0
H2O (g) ?241.818 ?228.572 3.470 1.450 0 0.121
C2H5OH (g) ?235.10 ?168.49 3.518 20.001 ?6.002 0
C2H5OC2H5 (g) ?252.21 ?112.19 0.1013 49.5 2.0078 0
CH3CHO (g) ?166.1 ?133.0 1.693 17.978 ?6.158 0
H2 (g) 0 0 3.249 0.422 0 0.083
CH3COOH (g) ?432.2 ?374.2 0.7119 26.338 ?10.417 0
C4H8O2 (g) ?443.6 ?327.4 2.2089 43.159 ?17.265 0
O2 (g) 0 0 3.693 0.506 0 ?0.227
Tab.1  
Species Critical temperature Tc /K Critical pressure Pc /bar Acentric factor /ω
C2H4 (g) 282.3 50.4 0.087
H2O (g) 647.1 220.55 0.345
C2H5OH (g) 513.9 61.48 0.645
C2H5OC2H5 (g) 466.7 36.4 0.281
CH3CHO (g) 466.0 55.5 0.291
H2 (g) 33.19 13.13 ?0.216
CH3COOH (g) 592 57.86 0.467
C4H8O2 (g) 523.3 38.8 0.366
O2 (g) 154.6 50.43 0.022
Tab.2  
Fig.1  
Fig.2  
Fig.3  
Fig.4  
Fig.5  
Fig.6  
Fig.7  
1 M Ni, D Y C Leung, M K H Leung. A review on reforming bio-ethanol for hydrogen production. International Journal of Hydrogen Energy, 2007, 32(15): 3238–3247
https://doi.org/10.1016/j.ijhydene.2007.04.038
2 M Al-Hasan. Effect of ethanol-unleaded gasoline blends on engine performance and exhaust emission. Energy Conversion and Management, 2003, 44(9): 1547–1561
https://doi.org/10.1016/S0196-8904(02)00166-8
3 A C Hansen, Q Zhang, P W L Lyne. Ethanol–diesel fuel blends––a review. Bioresource Technology, 2005, 96(3): 277–285
https://doi.org/10.1016/j.biortech.2004.04.007
4 B S Dien, M A Cotta, T W Jeffries. Bacteria engineered for fuel ethanol production: Current status. Applied Microbiology and Biotechnology, 2003, 63(3): 258–266
https://doi.org/10.1007/s00253-003-1444-y
5 E Gnansounou, A Dauriat. Techno-economic analysis of lignocellulosic ethanol: A review. Bioresource Technology, 2010, 101(13): 4980–4991
https://doi.org/10.1016/j.biortech.2010.02.009
6 M A Haider, M R Gogate, R J Davis. Fe-promotion of supported Rh catalysts for direct conversion of syngas to ethanol. Journal of Catalysis, 2009, 261(1): 9–16
https://doi.org/10.1016/j.jcat.2008.10.013
7 X Pan, Z Fan, W Chen, Y Ding, H Luo, X Bao. Enhanced ethanol production inside carbon-nanotube reactors containing catalytic particles. Nature Materials, 2007, 6(7): 507–511
https://doi.org/10.1038/nmat1916
8 M Kitson, P Williams. Catalyzed hydrogenation of carboxylic acids and their anhydrides to alcohols and/or esters. US Patent, 4985572, 1991-01-15
9 L Xingang, S Xiaoguang, Z Yi, I Takashi, M Ming, T Yisheng, T Noritatsu. Direct synthesis of ethanol from dimethyl ether and syngas over combined H-Mordenite and Cu/ZnO catalysts. ChemSusChem, 2010, 3(10): 1192–1199
https://doi.org/10.1002/cssc.201000109
10 M Llano-Restrepo, Y M Muñoz-Muñoz. Combined chemical and phase equilibrium for the hydration of ethylene to ethanol calculated by means of the Peng-Robinson-Stryjek-Vera equation of state and the Wong-Sandler mixing rules. Fluid Phase Equilibria, 2011, 307(1): 45–57
https://doi.org/10.1016/j.fluid.2011.05.007
11 Y Ding. Research progress of synthesis of ethanol and mixed high carbon primary alcohols from syngas derived from coal. Coal Chemical Industry, 2018, 46(1): 1–5
12 I J Castellanos-Beltran, G P Assima, J M Lavoie. Effect of temperature in the conversion of methanol to olefins (MTO) using an extruded SAPO-34 catalyst. Frontiers of Chemical Science and Engineering, 2018, 12(2): 226–238
https://doi.org/10.1007/s11705-018-1709-8
13 D Cai, Y Cui, Z Jia, Y Wang, F Wei. High-precision diffusion measurement of ethane and propane over SAPO-34 zeolites for methanol-to-olefin process. Frontiers of Chemical Science and Engineering, 2018, 12(1): 77–82
https://doi.org/10.1007/s11705-017-1684-5
14 E R Gilliland, R C Gunness, V O Bowles. Free energy of ethylene hydration. Industrial & Engineering Chemistry, 1936, 28(3): 370–372
https://doi.org/10.1021/ie50315a023
15 T Ushikubo. Recent topics of research and development of catalysis by niobium and tantalum oxides. Catalysis Today, 2000, 57(3): 331–338
https://doi.org/10.1016/S0920-5861(99)00344-2
16 N Katada, Y Iseki, A Shichi, N Fujita, I Ishino, K Osaki, T Torikai, M Niwa. Production of ethanol by vapor phase hydration of ethene over tungsta monolayer catalyst loaded on titania. Applied Catalysis A, General, 2008, 349(1): 55–61
https://doi.org/10.1016/j.apcata.2008.07.005
17 G Towler, S Lynn. Novel applications of reaction coupling: Use of carbon dioxide to shift the equilibrium of dehydrogenation reactions. Chemical Engineering Science, 1994, 49(16): 2585–2591
https://doi.org/10.1016/0009-2509(94)E0074-Z
18 A Sun, Z Qin, J Wang. Reaction coupling of ethylbenzene dehydrogenation with water-gas shift. Applied Catalysis A, General, 2002, 234(1): 179–189
https://doi.org/10.1016/S0926-860X(02)00222-3
19 Z Qin, J Liu, A Sun, J Wang. Reaction coupling in the new processes for producing styrene from ethylbenzene. Industrial & Engineering Chemistry Research, 2003, 42(7): 1329–1333
https://doi.org/10.1021/ie020762y
20 A Sun, Z Qin, J Wang. Reaction coupling of ethylbenzene dehydrogenation with nitrobenzene hydrogenation. Catalysis Letters, 2002, 79(1): 33–37
https://doi.org/10.1023/A:1015395906114
21 M E E Abashar. Coupling of ethylbenzene dehydrogenation and benzene hydrogenation reactions in fixed bed catalytic reactors. Chemical Engineering and Processing: Process Intensification, 2004, 43(10): 1195–1202
https://doi.org/10.1016/j.cep.2003.11.004
22 R H Perry. Perry’s Chemical Engineers’ Handbook. 7th ed. New York: McGraw-Hill, 1999, 230–650
23 F J Sanders, B F Dodge. Catalytic vapor-phase hydration of ethylene. Industrial & Engineering Chemistry, 1934, 26(2): 208–214
https://doi.org/10.1021/ie50290a019
24 C S Cope. Equilibria in the hydration of ethylene and of propylene. AIChE Journal. American Institute of Chemical Engineers, 1964, 10(2): 277–281
https://doi.org/10.1002/aic.690100230
25 G Garbarino, P Riani, M Villa García, E Finocchio, V Sánchez Escribano, G Busca. A study of ethanol conversion over zinc aluminate catalyst. Reaction Kinetics, Mechanisms and Catalysis, 2018, 124(2): 503–522
https://doi.org/10.1007/s11144-018-1395-z
26 Y Guan, E J M Hensen. Ethanol dehydrogenation by gold catalysts: The effect of the gold particle size and the presence of oxygen. Applied Catalysis A, General, 2009, 361(1-2): 49–56
https://doi.org/10.1016/j.apcata.2009.03.033
27 A Rodriguez-Gomez, J P Holgado, A Caballero. Cobalt carbide identified as catalytic site for the dehydrogenation of ethanol to acetaldehyde. ACS Catalysis, 2017, 7(8): 5243–5247
https://doi.org/10.1021/acscatal.7b01348
28 P Liu, T Li, H Chen, E J M Hensen. Optimization of Au0–Cu+ synergy in Au/MgCuCr2O4 catalysts for aerobic oxidation of ethanol to acetaldehyde. Journal of Catalysis, 2017, 347: 45–56
https://doi.org/10.1016/j.jcat.2016.11.040
29 R He, Y Zou, Y Dong, Y Muhammad, S Subhan, Z Tong. Kinetic study and process simulation of esterification of acetic acid and ethanol catalyzed by. Chemical Engineering Research & Design, 2018, 137: 235–245
https://doi.org/10.1016/j.cherd.2018.07.020
30 M Nielsen, H Junge, A Kammer, M Beller. Towards a green process for bulk-scale synthesis of ethyl acetate: Efficient acceptorless dehydrogenation of ethanol. Angewandte Chemie International Edition, 2012, 51(23): 5711–5713
https://doi.org/10.1002/anie.201200625
31 L R McCullough, E S Cheng, A A Gosavi, B A Kilos, D G Barton, E Weitz, H H Kung, J M Notestein. Gas phase acceptorless dehydrogenative coupling of ethanol over bulk MoS2 and spectroscopic measurement of structural disorder. Journal of Catalysis, 2018, 366: 159–166
https://doi.org/10.1016/j.jcat.2018.07.039
32 T B Lin, D L Chung, J R Chang. Ethyl acetate production from water-containing ethanol catalyzed by supported Pd catalysts: Advantages and disadvantages of hydrophobic supports. Industrial & Engineering Chemistry Research, 1999, 38(4): 1271–1276
https://doi.org/10.1021/ie9805887
33 B Jørgensen, S Egholm Christiansen, M L Dahl Thomsen, C H Christensen. Aerobic oxidation of aqueous ethanol using heterogeneous gold catalysts: Efficient routes to acetic acid and ethyl acetate. Journal of Catalysis, 2007, 251(2): 332–337
https://doi.org/10.1016/j.jcat.2007.08.004
34 R D Weinstein, A R Ferens, R J Orange, P Lemaire. Oxidative dehydrogenation of ethanol to acetaldehyde and ethyl acetate by graphite nanofibers. Carbon, 2011, 49(2): 701–707
https://doi.org/10.1016/j.carbon.2010.10.027
[1] FCE-19006-of-GJ_suppl_1 Download
Viewed
Full text


Abstract

Cited

  Shared   
  Discussed