Model-based hazard identification in multiphase chemical reactors

Journal of Loss Prevention in the Process Industries

Volumn 29, Issue 1, 2014, Pages 155-162

  Labovska Z ^a   Labovsky J ^a   Jelemensky L ^a   Dudas J ^a   Markos J ^a  

^a SLOVAK UNIVERSITY OF TECHNOLOGY   (Slovakia)

Author keywords

Continuation; Dynamic simulation; Model based safety analysis; MTBE; Multiple steady states

Indexed keywords

COMPUTER SIMULATION; HAZARDOUS MATERIALS; INDUSTRIAL HYGIENE; MATHEMATICAL MODELS; NONLINEAR ANALYSIS; OCCUPATIONAL DISEASES;

CONTINUATION; MAJOR INDUSTRIAL ACCIDENTS; MODEL-BASED SAFETY ANALYSIS; MTBE; MULTIPHASE CHEMICAL REACTOR; MULTIPLE STEADY STATE; STEADY STATES MULTIPLICITY; STEADY-STATE ANALYSIS;

CHEMICAL ANALYSIS;

EID: 84896268032     PISSN: 09504230     EISSN: None     Source Type: Journal    
DOI: 10.1016/j.jlp.2014.02.004     Document Type: Article

References (44)

1. AICHE AICHE bubble tray design manual 1958, AIChE, New York.
2. AICHE Guidelines for hazard evaluation procedures 1992, Center for Chemical Process Safety of the American Institute of Chemical Engineers, New York, NY. 2nd ed.
3. Chan H., Fair J.R. Prediction of point efficiencies on sieve trays. 2. Multicomponent systems. Industrial & Engineering Chemistry Process Design and Development 1984, 23(4):820-827.
4. Chen G.X., Chuang K.T. Prediction of point efficiency for sieve trays in distillation. Industrial & Engineering Chemistry Research 1993, 32:701-708.
5. Crawley, F., & Tyler, B. (2003).Hazard identification methods: Institution of Chemical Engineers (IChemE), Rugby, UK.
6. Eizenberg S., Shacham M., Brauner N. Combining HAZOP with dynamic simulation - applications for safety education. Journal of Loss Prevention in the Process Industries 2006, 19(6):754-761. 10.1016/j.jlp.2006.07.002.
7. Fuller E., Schettler P., Giddings New method for prediction of binary gas-phase diffusion coefficients. Industrial & Engineering Chemistry 1966, 58(5):18-27.
8. Hauan S., Hertzberg T., Lien K.M. Multiplicity in reactive distillation of MTBE. Computers & Chemical Engineering 1997, 21(10):1117-1124. 10.1016/S0098-1354(96)00322-5.
9. Hauptmanns U. Boundary conditions for developing a safety concept for an exothermal reaction. Journal of Hazardous Materials 2007, 148:144-150. 10.1016/j.jhazmat.2007.02.019.
10. Hauptmanns U. Comparative assessment of the dynamic behaviour of an exothermal chemical reaction including data uncertainties. Chemical Engineering Journal 2008, 140:278-286. 10.1016/j.cej.2007.09.031.
11. Jacobs R., Krishna R. Multiple solutions in reactive distillation for methyl tert-butyl ether synthesis. Industrial & Engineering Chemistry Research 1993, 32(8):1706-1709. 10.1021/ie00020a025.
12. Kletz T.A. Learning from accidents 2001, Gulf Professional, Oxford; Boston. 3rd ed.
13. Kooijman H.A., Taylor R. Modelling mass transfer in multicomponent distillation. The Chemical Engineering Journal 1995, 57(2):177-188. 10.1016/0923-0467(94)02952-0.
14. Kooijman H.A., Taylor R. The ChemSep book 2000, Libri Books on Demand, Norderstedt.
15. Krishna R., Wesselingh J.A. The Maxwell-Stefan approach to mass transfer. Chemical Engineering Science 1997, 52(6):861-911. 10.1016/S0009-2509(96)00458-7.
16. Krishnamurthy R., Taylor R. Anonequilibrium stage model of multicomponent separation processes I-model description and method of solution. AIChE Journal 1985, 31(3):449-456. 10.1002/aic.690310312.
17. Krishnamurthy R., Taylor R. Anonequilibrium stage model of multicomponent separation processes II-comparison with experiment. AIChE Journal 1985, 31(3):456-465. 10.1002/aic.690310313.
18. Labovský J., Jelemenský Ľ., Markoš J. Safety analysis and risk identification for a tubular reactor using the HAZOP methodology. Chemical Papers 2006, 60(6):454-459. 10.2478/s11696-006-0082-0.
19. Labovský J., Laššák P., Markoš J., Jelemenský Ľ. Design, optimization and safety analysis of a heterogeneous tubular reactor by using the HAZOP methodology. Computer Aided Chemical Engineering 2007, Vol. 24:1241-1246. Elsevier.
20. Labovský J., Švandová Z., Markoš J., Jelemenský Ľ. Mathematical model of a chemical reactor a useful tool for its safety analysis and design. Chemical Engineering Science 2007, 62:4915-4919. 10.1016/j.ces.2007.01.071.
21. Labovský J., Švandová Z., Markoš J., Jelemenský Ľ. Model-based HAZOP study of a real MTBE plant. Journal of Loss Prevention in the Process Industries 2007, 20(3):230-237. 10.1016/j.jlp.2007.03.015.
22. Labovský J., Švandová Z., Markoš J., Jelemenský Ľ. HAZOP study of a fixed bed reactor for MTBE synthesis using a dynamic approach. Chemical Papers 2008, 62(6):51-57. 10.2478/s11696-007-0078-4.
23. Laššák P., Labovský J., Jelemenský Ľ. Influence of parameter uncertainty on modeling of industrial ammonia reactor for safety and operability analysis. Journal of Loss Prevention in the Process Industries 2010, 23(2):280-288. 10.1016/j.jlp.2009.10.001.
24. Mancusi E., Maffettone P.L., Gioia F., Crescitelli S. Nonlinear analysis of an industrial ammonia reactor with heterogeneous model. Computer Aided Chemical Engineering 2001, Vol. 9:225-230. Elsevier.
25. Mancusi E., Merola G., Crescitelli S., Maffettone P.L. Multistability and hysteresis in an industrial ammonia reactor. AIChE Journal 2000, 46(4):824-828.
26. Mannan S., Lees F.P. Lee's loss prevention in the process industries: Hazard identification, assessment, and control 2005, Elsevier Butterworth-Heinemann, Amsterdam; Boston. 3rd ed.
27. Mohl K.-D., Kienle A., Gilles E.-D., Rapmund P., Sundmacher K., Hoffmann U. Steady-state multiplicities in reactive distillation columns for the production of fuel ethers MTBE and TAME: theoretical analysis and experimental verification. Chemical Engineering Science 1999, 54(8):1029-1043. 10.1016/S0009-2509(98)00327-3.
28. Molnár A., Krajčiová M., Markoš J., Jelemenský Ľ. Use of bifurcation analysis for identification of a safe CSTR operability. Journal of Loss Prevention in the Process Industries 2004, 17(6):489-498. 10.1016/j.jlp.2004.08.008.
29. Molnár A., Markoš J., Jelemenský Ľ. Safety analysis of CSTR towards changes in operating conditions. Journal of Loss Prevention in the Process Industries 2003, 16(5):373-380. 10.1016/S0950-4230(03)00069-X.
30. Molnár A., Markoš J., Jelemenský Ľ. Some considerations for safety analysis of chemical reactors. Chemical Engineering Research and Design 2005, 83(2):167-176. 10.1205/cherd.03284.
31. Morud J.C., Skogestad S. Analysis of instability in an industrial ammonia reactor. AIChE Journal 1998, 44(4):888-895. 10.1002/aic.690440414.
32. Sales J., Mushtaq F., Christou M.D., Nomen R. Study of major accidents involving chemical reactive substances: analysis and lessons learned. Process Safety and Environmental Protection 2007, 85(2):117-124. 10.1205/psep06012.
33. Singh B.P., Singh R., Pavan Kumar M.V., Kaistha N. Steady-state analyses for reactive distillation control: an MTBE case study. Journal of Loss Prevention in the Process Industries 2005, 18(4-6):283-292. 10.1016/j.jlp.2005.06.009.
34. Sudibyo M.M.N., Aziz N. Simulation studies and sensitivity analysis of methyl tert-butyl ether reactive distillation. Computer Aided Chemical Engineering 2012, Vol. 31:130-134. Elsevier.
35. Švandová Z., Kotora M., Markoš J., Jelemenský Ľ. Dynamic behaviour of a CSTR with reactive distillation. Chemical Engineering Journal 2006, 119(2-3):113-120. 10.1016/j.cej.2006.03.032.
36. Švandová Z., Labovský J., Markoš J., Jelemenský Ľ. Impact of mathematical model selection on prediction of steady state and dynamic behaviour of a reactive distillation column. Computers & Chemical Engineering 2009, 33(3):788-793. 10.1016/j.compchemeng.2008.07.004.
37. Švandová Z., Markoš J., Jelemenský Ľ. Multiple steady states in a CSTR with total condenser: comparison of equilibrium and nonequilibrium models. Chemical Papers 2006, 60(6):432-440. 10.2478/s11696-006-0079-8.
38. Švandová Z., Markoš J., Jelemenský Ľ. Impact of mass transfer coefficient correlations on prediction of reactive distillation column behaviour. Chemical Engineering Journal 2008, 140(1-3):381-390. 10.1016/j.cej.2007.10.022.
39. Švandová Z., Markoš J., Jelemenský Ľ., Molnár A. Steady states analysis and dynamic simulation as a complement in the Hazop study of chemical reactors. Process Safety and Environmental Protection 2005, 83(5):463-471. 10.1205/psep.04262.
40. Taylor R., Krishna R. Multicomponent mass transfer 1993, John Wiley & Sons, Inc, New York.
41. Taylor R., Krishna R. Modelling reactive distillation. Chemical Engineering Science 2000, 55(22):5183-5229.
42. Wang S.J., Wong D.S.H., Lee E.K. Effect of interaction multiplicity on control system design for a MTBE reactive distillation column. Journal of Process Control 2003, 13(6):503-515. 10.1016/S0959-1524(02)00111-7.
43. Wilke C.R., Chang P. Correlation of diffusion coefficients in dilute solutions. AIChE Journal 1955, 1(2):264-270. 10.1002/aic.690010222.
44. Zuiderweg F.J. Sieve trays: a view on the state of the art. Chemical Engineering Science 1982, 37(10):1441-1464.