Abstract
Comparison of the performance of a reactive distillation column with three different hardware configurations is presented. As a reaction system the methyl tertiary-butyl ether (MTBE) synthesis has been chosen. The sieve tray columns with catalyst (encased inside wire gauze envelopes) placed along the liquid flow path differ in the number of reactive trays. The column simulations have been performed using the nonequilibrium model. The steady state behaviour of the three different hardware configurations was studied regarding the three input parameters; feed flow rate of methanol, feed flow rate of butenes, and reflux ratio. It has been shown that by varying the location of the methanol feed stage, the columns exhibit significantly different solution diagrams using the butenes feed flow rate as a continuation parameter. Using dynamic simulations, different perturbations of the manipulated variables were found to cause transitions between multiple steady states and these were also investigated. The major objective of this paper is to demonstrate the importance of the hardware choice in the performance of a reactive distillation column e.g. during the start-up or if occasional variations of the operating parameters occur.
[1] Baur, R., Higler, A. P., Taylor, R., & Krishna, R. (2000). Comparison of equilibrium stage and nonequilibrium stage models for reactive distillation. Chemical Engineering Journal, 76, 33–47. DOI: 10.1016/S1385-8947(99)00114-X. http://dx.doi.org/10.1016/S1385-8947(99)00114-X10.1016/S1385-8947(99)00114-XSuche in Google Scholar
[2] Baur, R., Taylor, R., & Krishna, R. (2001). Influence of column hardware on the performance of reactive distillation columns. Catalysis Today, 66, 225–232. DOI: 10.1016/S0920-5861(00)00653-2. http://dx.doi.org/10.1016/S0920-5861(00)00653-210.1016/S0920-5861(00)00653-2Suche in Google Scholar
[3] Hauan, S., Hertzberg, T., & Lien, K. M. (1997). Multiplicity in reactive distillation of MTBE. Computers & Chemical Engineering, 21, 1117–1124. DOI: 10.1016/S0098-1354(96)00322-5. http://dx.doi.org/10.1016/S0098-1354(96)00322-510.1016/S0098-1354(96)00322-5Suche in Google Scholar
[4] Chen, F., Huss, R. S., Doherty, M. F., & Malone, M. F. (2002). Multiple steady states in reactive distillation: kinetic effects. Computers & Chemical Engineering, 26, 81–93. DOI: 10.1016/S0098-1354(01)00750-5. http://dx.doi.org/10.1016/S0098-1354(01)00750-510.1016/S0098-1354(01)00750-5Suche in Google Scholar
[5] IMSL Fortran Subroutines for Mathematical Applications, M. L. (1997). Vol. 1 and 2. Houston, USA: Visual Numerics, Inc. Suche in Google Scholar
[6] Jacobs, R., & Krishna, R. (1993). Multiple solutions in reactive distillation for methyl tert-butyl ether synthesis. Industrial Engineering Chemistry Research, 32, 1706–1709. DOI:10.1021/ie00020a025. http://dx.doi.org/10.1021/ie00020a02510.1021/ie00020a025Suche in Google Scholar
[7] Jones Jr., E. M. (1985). Contact structure for use in catalytic distillation, US Patent 4536373. Suche in Google Scholar
[8] Kooijman, H. A., & Taylor, R. (2000). The ChemSep Book. Norderstedt: Libri Books on Demand. Suche in Google Scholar
[9] Krishnamurthy, R., & Taylor, R. (1985). A nonequilibrium stage model of multicomponent separation processes II. Comparison with experiment. American Institute of Chemical Engineers Journal, 31, 456–465. DOI: 10.1002/aic.690310313. 10.1002/aic.690310313Suche in Google Scholar
[10] Kubíček, M. (1976). Algorithm 502. Dependence of solution of nonlinear systems on a parameter [C5]. ACM Transaction on Mathematical Software, 2, 98–107. DOI: 10.1145/355666.355675. http://dx.doi.org/10.1145/355666.35567510.1145/355666.355675Suche in Google Scholar
[11] Mohl, K.-D., Kienle, A., Gilles, E.-D., Rapmund, P., Sundmacher, K., & Hoffmann, U. (1999). Steady-state multiplicities in reactive distillation columns for the production of fuel ethers MTBE and TAME: theoretical analysis and experimental verification. Chemical Engineering Science, 54, 1029–1043. DOI: 10.1016/S0009-2509(98)00327-3. http://dx.doi.org/10.1016/S0009-2509(98)00327-310.1016/S0009-2509(98)00327-3Suche in Google Scholar
[12] Noeres, C., Kenig, E. Y., & Gorak, A. (2003). Modelling of reactive separation processes: reactive absorption and reactive distillation. Chemical Engineering & Processing, 42, 157–178. DOI: 10.1016/S0255-2701(02)00086-7. http://dx.doi.org/10.1016/S0255-2701(02)00086-710.1016/S0255-2701(02)00086-7Suche in Google Scholar
[13] Perry, R. H., Green, D. W., & Maloney, J. O. (1997). Perry’s chemical engineers’ handbook (7th ed.). New York: McGraw-Hill. Suche in Google Scholar
[14] Petzold, L. R., Brown, P. N., Hindmarsh, A. C., & Ulrich, C.W. (2002). ode/daskr.tgz. Center for Computational Sciences & Engineering, Livermore. http://netlib3.cs.utk.edu/cgi-bin/search.pl?query=gams/I1a2%2A. Suche in Google Scholar
[15] Rapmund, P., Sundmacher, K., & Hoffmann, U. (1998). Multiple steady states in a reactive distillation column for the production of the fuel ether TAME Part II: Experimental validation. Chemical Engineering & Technology, 21, 136–139. DOI: 10.1002/(SICI)1521-4125(199802)21:2〈136::AIDCEAT136〉3.0.CO;2-4. http://dx.doi.org/10.1002/(SICI)1521-4125(199802)21:2<136::AID-CEAT136>3.0.CO;2-410.1002/(SICI)1521-4125(199802)21:2<136::AID-CEAT136>3.0.CO;2-4Suche in Google Scholar
[16] Rehfinger, A., & Hoffmann, U. (1990). Kinetics of methyl tertiary butyl ether liquid phase synthesis catalyzed by ion exchange resin I. Intrinsic rate expression in liquid phase activities. Chemical Engineering Science, 45, 1605–1617. DOI: 10.1016/0009-2509(90)80013-5. http://dx.doi.org/10.1016/0009-2509(90)80013-510.1016/0009-2509(90)80013-5Suche in Google Scholar
[17] Reid, R. C., Prausnitz, J. M., & Sherwood, T. K. (1977). The Properties of Gases and Liquids (3rd ed.). New York: McGraw-Hill. Suche in Google Scholar
[18] Taylor, R., & Krishna, R. (1993). Multicomponent Mass Transfer. New York: John Wiley & Sons, Inc. Suche in Google Scholar
[19] Taylor, R., & Krishna, R. (2000). Modelling reactive distillation. Chemical Engineering Science, 55, 5183–5229. DOI: 10.1016/S0009-2509(00)00120-2. http://dx.doi.org/10.1016/S0009-2509(00)00120-210.1016/S0009-2509(00)00120-2Suche in Google Scholar
[20] Švandová, Z., Markoš, J., & Jelemenský, Ľ (2006). Multiple steady states in a CSTR with total condenser: Comparison of equilibrium and nonequilibrium models. Chemical Papers, 60, 432–440. DOI: 10.2478/s11696-006-0079-8. http://dx.doi.org/10.2478/s11696-006-0079-810.2478/s11696-006-0079-8Suche in Google Scholar
[21] Wesselingh, J. A., & Krishna, R. (1990). Mass Transfer. Chichester, England: Ellis Horwood. Suche in Google Scholar
© 2008 Institute of Chemistry, Slovak Academy of Sciences
Artikel in diesem Heft
- Photocatalytic reduction of CO2 over TiO2 based catalysts
- Modeling of enzymatic reaction in an airlift reactor using an axial dispersion model
- Hydrolysis of titanium sulphate compounds
- Mathematical modelling of selected characterisation procedures for oil fractions
- High gravity batch and continuous processes for beer production: Evaluation of fermentation performance and beer quality
- Liquid-liquid equilibria of butyric acid for solvents containing a phosphonium ionic liquid
- HAZOP study of a fixed bed reactor for MTBE synthesis using a dynamic approach
- Influence of the reactive distillation column configuration on its performance: A computational study
- Reactive distillation — experimental data for propyl propionate synthesis
- Mixing time of a non-Newtonian liquid in an unbaffled agitated vessel with an eccentric propeller
- Heat transfer coefficient and pressure drop during refrigerant R-134a condensation in a plate heat exchanger
- Pore structure of pyrolyzed scrap tires
- Distribution of local heat transfer coefficient values in the wall region of an agitated vessel
- Chemical pretreatment of feed water for membrane distillation
- Selective methane oxidation to formaldehyde using polymorphic T-, M-, and H-forms of niobium(V) oxide as catalysts
- Validation of the Tessier scheme for speciation of metals in soil using the Bland and Altman test
- Production of potassium sulfate from potassium hydrosulfate solutions using alcohols
Artikel in diesem Heft
- Photocatalytic reduction of CO2 over TiO2 based catalysts
- Modeling of enzymatic reaction in an airlift reactor using an axial dispersion model
- Hydrolysis of titanium sulphate compounds
- Mathematical modelling of selected characterisation procedures for oil fractions
- High gravity batch and continuous processes for beer production: Evaluation of fermentation performance and beer quality
- Liquid-liquid equilibria of butyric acid for solvents containing a phosphonium ionic liquid
- HAZOP study of a fixed bed reactor for MTBE synthesis using a dynamic approach
- Influence of the reactive distillation column configuration on its performance: A computational study
- Reactive distillation — experimental data for propyl propionate synthesis
- Mixing time of a non-Newtonian liquid in an unbaffled agitated vessel with an eccentric propeller
- Heat transfer coefficient and pressure drop during refrigerant R-134a condensation in a plate heat exchanger
- Pore structure of pyrolyzed scrap tires
- Distribution of local heat transfer coefficient values in the wall region of an agitated vessel
- Chemical pretreatment of feed water for membrane distillation
- Selective methane oxidation to formaldehyde using polymorphic T-, M-, and H-forms of niobium(V) oxide as catalysts
- Validation of the Tessier scheme for speciation of metals in soil using the Bland and Altman test
- Production of potassium sulfate from potassium hydrosulfate solutions using alcohols