Double-effect integration of multicomponent alcoholic distillation columns

Energy

Volumn 45, Issue 1, 2012, Pages 603-612

  Bessa, Larissa C B A ^a   Batista, Fabio R M ^a   Meirelles, Antonio J A ^a  

^a UNIVERSITY OF CAMPINAS   (Brazil)

Author keywords

Bioethanol; Multicomponent distillation; Sugarcane; Thermal integration

Indexed keywords

BIOETHANOL; COMPUTER SOFTWARE; DISTILLATION; ETHANOL; FOSSIL FUELS; INTEGRATION; RENEWABLE ENERGY RESOURCES; SUGAR CANE;

ASPEN PLUS; DISTILLATION PROCESS; DOUBLE EFFECTS; ENERGY REQUIREMENTS; ENERGY SUPPLY SECURITY; INDUSTRIAL PROCESSS; LIQUID MIXTURE; MINOR COMPONENTS; MULTICOMPONENTS; RENEWABLE ENERGY SOURCE; STEADY-STATE SIMULATIONS; STEAM CONSUMPTION; THERMAL INTEGRATION;

DISTILLATION COLUMNS;

ALCOHOL; DISTILLATION; ENERGY EFFICIENCY; ENVIRONMENTAL IMPACT; ETHANOL; FOSSIL FUEL; INTEGRATED APPROACH; MILL; RENEWABLE RESOURCE; SUGAR CANE; TEMPERATURE EFFECT;

EID: 84865430823     PISSN: 03605442     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.energy.2012.07.038     Document Type: Article

References (54)

1. Leite R.C.C., Leal M.R.L.V., Cortez L.A.B., Griffin W.M., Scandiffio M.I.G. Can Brazil replace 5% of the 2025 gasoline world demand with ethanol?. Energy 2009, 34:655-661.
2. Gupta R., Sharma K.K., Kuhad R.C. Separate hydrolysis and fermentation (SHF) of Prosopisjuliflora, a woody substrate, for the production of cellulosic ethanol by Saccharomyces cerevisae and Pichiastipitis-NCIM 3498. Bioresource Technology 2009, 100:1214-1220.
3. Malça J., Freire F. Renewability and life-cycle energy efficiency of bioethanol and bio-ethyl tertiary butyl ether (bioETBE): assessing the implications of allocation. Energy 2006, 31:3362-3380.
4. van den Wall Bake J.D., Junginger M., Faaij A., Poot T., Walter A. Explaining the experience curve: cost reductions of Brazilian ethanol from sugarcane. Biomass and Bioenergy 2009, 33:644-658.
5. Sánchez S., Lozano L.J., Godínez C., Juan D., Pérez A., Hernández F.J. Carob pod as a feedstock for the production of bioethanol in Mediterranean areas. Applied Energy 2010, 87:3417-3424.
6. Macedo I.C., Seabra J.E.A., Silva J.E.A.R. Greenhouse gases emissions in the production and use of ethanol from sugarcane in Brazil: the 2005/2006 averages and a prediction for 2020. Biomass and Bioenergy 2008, 32:582-595.
7. Walter A., Dolzan P., Quilodrán O., de Oliveira J.G., da Silva C., Piacente F., et al. Sustainability assessment of bio-ethanol production in Brazil considering land use change, GHG emissions and socio-economic aspects. Energy Policy 2010, 39:5703-5716.
8. Quintero J.A., Montoya M.I., Sánchez O.J., Giraldo O.H., Cardona C.A. Fuel ethanol production from sugarcane and corn: comparative analysis for a Colombian case. Energy 2008, 33:385-399.
9. National Confederation of Industry [Confederação Nacional da Indústria - CNI] Energetic matrix: scenario, opportunities and challenges [Matriz Energética: Cenários, Oportunidades e Desafios]. Brasília 2007, [in Portuguese].
10. Araújo A.B., Brito R.P., Vasconcelos L.S. Exergetic analysis of distillation processes-a case study. Energy 2007, 32:1185-1193.
11. Engelien H.K., Skogestad S. Multi-effect distillation applied to an industrial case study. Chemical Engineering and Processing 2005, 44:819-826.
12. Dias M.O.S., Modesto M., Ensinas A.V., Nebra S.A., Maciel Filho R., Rossell C.E.V. Improving bioethanol production from sugarcane: evaluation of distillation, thermal integration and cogeneration systems. Energy 2011, 36:3691-3703.
13. Cardona Alzate C.A., Sánchez Toro O.J. Energy consumption analysis of integrated flowsheets for production of fuel ethanol from lignocellulosic biomass. Energy 2006, 31:2447-2459.
14. Liu X., Qian J. Operational optimization of ideal internal thermally coupled distillation columns. Developments in Chemical Engineering and Mineral Processing 2008, 9(1/2):133-142.
15. Nakaiwa M., Huang K., Owa M., Akiya T., Nakane T., Sato M., et al. Energy savings in heat-integrated distillation columns. Energy 1997, 22:621-625.
16. Jana A.K. Heat integrated distillation operation. Applied Energy 2010, 87:1477-1494.
17. Engelien H.K., Skogestad S. Selecting appropriate control variables for a heat-integrated distillation system with prefractionator. Computers and Chemical Engineering 2004, 28:683-691.
18. Marquini M.F., Meirelles A.J.A., Maciel Filho R., Santos O.A.A., Jorge L.M.M. Reduction of energy consumption and effluent generation in ethanol distilleries 2008, XVII chemical engineering Brazilian congress [XVII Congresso Brasileiro de Engenharia Química].
19. Mulia-Soto J.F., Flores-Tlacuahuac A. Modeling, simulation and controlo f na internally heat integrated pressure-swing distillation process for bioethanol separation. Computers and Chemical Engineering 2011, 35:1532-1546.
20. Huang K.J., Zhan D.Z., Masaru N., Takashi N., Takeichiro T. Modeling and analysis of internal heat integrated distillation columns. Chinese Journal of Chemical Engineering 1999, 7:67-76.
21. Boscolo M., Bezerra C.W.B., Cardoso D.R., Neto B.S.L., Franco D.W. Identification and dosage by HRGC of minor alcohols and esters in Brazilian sugar-cane spirit. Journal of the Brazilian Chemical Society 2000, 11:86-90.
22. Cardoso D.R., Lima-Neto B.S., Franco D.W., Nascimento R.F. Influence of distiller material in the chemical composition of sugarcane spirit - part II [Influência do Material do Destilador na Composição Química das Aguardentes de Cana - Parte II]. Química Nova 2003, 26:165-169. [in Portuguese].
23. Decloux M., Coustel J. Simulation of a neutral production plant using beer distillation. International Sugar Journal 2005, 107(1283):628-643.
24. Batista F.R.M., Meirelles A.J.A. Computer simulation applied to studying continuous spirit distillation and product quality control. Food Control 2011, 22:1592-1603.
25. Amorim H.V., Lopes M.L., Oliveira J.V.C., Buckeridge M.S., Goldman G.H. Scientific challenges of bioethanol production in Brazil. Applied Microbiology and Biotechnology 2011, 91:1267-1275.
26. Gutierrez L.E. Effect of the addition of sulphite in the production of higher alcohols during the alcoholic fermentation. [Efeito da adição de sulfito sobre a produção de álcoois superiores durante a fermentação alcoólica]. Annals of ESALQ 1988, 45(part 2):359-368. [in Portuguese].
27. Dalmolin I.A.L., Skovroinski E., Biasi A., Corazza M.L., Dariva C., Vladimir Oliveira J. Solubility of carbon dioxide in binary and ternary mixtures with ethanol and water. Fluid Phase Equilibria 2006, 245:193-200.
28. a ed.
29. Marquini M.F., Mariani D.C., Meirelles A.J.A., Santos O.A.A., Jorge L.M.M. Simulation and analysis of an industrial system of ethanol distillationcolumns [Simulação e Análise de um Sistema Industrial de Colunas de Destilação de Etanol]. Acta Scientiarum (UEM) 2002, 29:23-28. [in Portuguese].
30. Hayden J.G., O'Connell J.P.A. Generalized method for predicting second virial coefficients. Industrial and Engineering Chemistry, Process Design and Development 1975, 14:209-216.
31. Faúndez C.A., Valderrama J.O. Phase equilibrium modeling in binary mixtures found in wine and must distillation. Journal of Food Engineering 2004, 65:577-583.
32. Gmehling J., Onken U. Vapor-liquid equilibrium data collection. Frankfurd: Dechema 1981.
33. Cai J., Cui X., Zhang Y., Li R., Feng T.J. Vapor-liquid equilibrium and liquid-liquid equilibrium of methyl acetate + methanol + 1-ethyl-3-methylimidazolium acetate. Journal of Chemical and Engineering Data 2011, 56:282-287.
34. Gao D., Zhu D., Sun H., Zhang L., Chen H., Si J.J. Isobaric vapor-liquid equilibria for binary and ternary mixtures of methanol, ethanoic acid and propanoic acid. Journal of Chemical and Engineering Data 2010, 55:4002-4009.
35. Navarro-Espinosa I.R., Cardona C.A., López J.A. Experimental measurements of vapor-liquid equilibria at low pressure: systems containing alcohols, esters and organic acids. Fluid Phase Equilibria 2010, 287:141-145.
36. Resa J.M., Goenaga J.M., Lanz J. Vapor-liquid equilibrium of binary mixtures containing ethyl acetate + 2-methyl-1-propanol and ethyl acetate + 2-methyl-1-butanol at 101,3 kPa. Journal of Chemical and Engineering Data 2006, 51:595-598.
37. Carta R., Dernini S., Sanna P. Isobaric vapor-liquid equilibria for the ternary system acetone-ethyl acetate-ethanol. Journal of Chemical and Engineering Data 1984, 29:463-466.
38. Ramalho R.S., Drolet J.F. Vapor-liquid equilibrium data for the ternary system acetone-2-propanol-water and corresponding binaries from total pressure measurements. Journal of Chemical and Engineering Data 1971, 16:12-15.
39. Gultekin N. Vapor-liquid equilibria for binary and ternary systems composed of acetone, 2-propano1, and I-propanol. Journal of Chemical and Engineering Data 1989, 34:168-171.
40. Verhoeye L., de Schepper H. The vapour-liquid equilibria of the binary, ternary and quaternary systems formed by acetone, methanol, propan-2-ol, and water. Journal of Applied Chemistry and Biotechnology 1973, 23:607-619.
41. Bunch D.W., James W.J., Ramalho R.S. A rapid method for obtaining vapor-liquid equilibrium data: distillate analysis technique as applied to a ternary system. I&EC Process Design and Development 1963, 2:282-284.
42. Amer H.H., Paxton R.R., van Winkle M. Methanol- ethanol-acetone: vapor-liquid equilibria. Industrial and Engineering Chemistry 1956, 48:142-146.
43. Dawe R.A., Newsham D.M.T., Ng S.B. Vapor-Liquid equilibria in mixtures of water, n-propanol, and n-butanol. Journal of Chemical and Engineering Data 1973, 18:44-49.
44. Gabaldón C., Marzal P., Montón J.B., Rodrigo M.A. Isobaric vapor-liquid equilibria for binary and ternary systems composed of water, 1-propanol, and 2-propanol at 100 kPa. Journal of Chemical and Engineering Data 1996, 41:1379-1382.
45. Aicher T., Bamberger T., Schlünder E.-U. Liquid-liquid and vapor-liquid phase equilibria for 1-butanol + water + 2-propanol at ambient pressure. Journal of Chemical and Engineering Data 1995, 40:696-698.
46. Resa J.M., Goenaga J.M. Measurement and modeling of phase equilibria for ethanol + water + methanol at isobaric condition. Journal of Chemical and Engineering Data 2006, 51:2114-2120.
47. Tan T.C., Tan R., Soon L.H., Ong S.H.P. Prediction and experimental verification of the effect of salt on the vapour-liquid equilibrium of ethanol/1-propanol/water mixture. Fluid Phase Equilibria 2005, 234:84-93.
48. Newsham D.M.T., Vahdat N. Prediction of vapour-liquid-liquid equilibria from liquid-liquid equilibria part I: experimental results for the systems methanol-water-n-butanol, ethanol-water-n-butanol and n-propanol-water-n-butanol. The Chemical Engineering Journal 1977, 13:27-31.
49. Nagata I., Tamura K., Miyai K. Isothermal vapor-liquid equilibria of mixtures of (methanol + ethanol + 1-propanol or 2-propanol) at 333.15 K. Fluid Phase Equilibria 2000, 170:37-48.
50. El-Yafi A.H., Martinez H., Newsham D.M.T., Vahdat N. Vapour-liquid equilibria for ethanol + t-butanol + water and methanol + isopropanol + water at atmospheric pressure. Journal of Chemical Thermodynamics 1976, 8:1061-1073.
51. Gultekin N. Vapor-liquid equilibria at 1 atm for ternary and quarternary systems composed of acetone, methanol, 2-propano1, and I-propanol. Journal of Chemical and Engineering Data 1990, 35:132-136.
52. BRASIL Department of agriculture, livestock and supply. Normative instruction n°13 June 29, 2005, Technical regulation for setting standards of identity and quality of spirit and cachaça.
53. Matsuda K., Kawazuishi K., Kansha Y., Fushimi C., Nagao M., Kunikiyo H., et al. Advanced energy saving in distillation process with self-heat recuperation technology. Energy 2011, 36:4640-4645.
54. Kiran B., Jana A.K., Samanta A.N. A novel intensified heat integration in multicomponent distillation. Energy 2012, 41:443-453.