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References  141
                 Gommers J.J.M. Private communication  Kucsynski, M., Oyevaar, M.H., Pieters, R.T.,
                 Graedel, T.E., Allenby, B.R., Industrial Ecology.  Westerterp, K.R. Methanol synthesis in a
                  Prentice-Hall, 1995.              counter current gas-solid trickle flow reactor
                                                    an experimental study. Chem. Eng. Sci. 1987,
                 Grievink J. Private communication
                                                    42(8), 1887±1898.
                 Gundersen, T. From Gothenburg '92 to  Luyben, W.L., Tyreus, B.D., Luyben, M.L. Plant
                  Copenhagen '99. Major Trends and  Wide Process Control. McGraw-Hill, New
                  Developments in Process Integration.  York, 1998. ISBN 0-07-006779-1.
                  International conference on process
                  integration, Copenhagen, March 1999,  Netzer, D. Economically recover olefins from
                  Dansk Energy Analysis. E-mail dea@dea.dk  FCC off-gases. Hydrocarbon Processing 1997,
                                                    April, 83±91.
                 Hauptmann, E.G., Rae, J.M., Guenkel, A.A.
                  The jet impingement reactor a new high  Netzer, D. Integrate ethyl-benzene production
                  intensity reactor for liquid-liquid reaction  with an olefins plant. Hydrocarbon Processing
                  processes. 1st International Conference on  1999, May, 77±88.
                  Process Intensification for the Chemical  Matros, Y.S., Noskov, A.S. Theory and
                  Industry. BHR Group Conference Series,  application of unsteady catalytic detoxication
                  No. 18, 1995, pp. 181±184.        of effluent gases from sulfur dioxide,
                 Hinderink, A.P., Kerkhof, F.P.J.M., Lie, A.B.K,  nitrogen oxide and organic compounds.
                  de Swaan Arons, J., Kooi, H.J. Exergy  Chem. Eng Sci. 1988, 43(8), 2061±2066.
                  analysis with a flowsheeting simulator. Part  Perkins J.D., The Interaction between Process
                  1, Theory; Part 2, Application. Chem. Eng.  Design and Process Control, Proc. IFAC
                  Sci. 1996, 51(20), 4693±4700, 4701±4715.  Symposium on Dynamics and Control of
                 IChemE. A User Guide on Process Integration  Chemical Reactors and columns DYCORD
                  for the Efficient Use of Energy. 1982 revised in  '89, 1989,195±203.
                  1997. ISBN 0-85295-3437.         Porter, K.E., Momoh, S.O. Finding the
                 Institution of Chemical Engineers (IChemE).  optimum sequence of distillation columns.
                  Training package 027. Inherently Safer  An equation to remove the rule of thumb
                  Process Design, pp. 165±189. Railway  (Heuristics). Chem. Eng. J. 1991, 46, 97.
                  Terrace, Rugby CV 21 3HQ, UK.1995.  Schluter, S., Steif, A., Weinspach, P.M.
                 Kaibel, G. Distillation Columns with Vertical  Modeling and simulation of bubble column
                  Partitions, Chem. Eng. Technol. 1987, 10,  reactors. Chem. Eng. Process. 1992, 31,
                  92±98.                            97±117.
                 Kletz, T. Plant Design for Safety: A User-Friendly  Seader, J.D., Henley, E.J., Separation process
                  Approach. Hemisphere Publishing   principles John Wiley & Sons 1998,
                  Corporation, 1991. ISBN 1-56032-068-0.  ISBN 0-471-58626-9.
                 Kohlbrandt, H.T. The relationship between  Seider, W.D., Seader, J.D., Lewin, D.R. Process
                  theory and testing in the evaluation of  Design Principles: Synthesis, Analysis, and
                  reactive chemical hazards. Proceedings of  Evaluation. John Wiley & Sons, New York,
                  the International symposium on prevention  1999. ISBN 0-471-24312-4.
                  of major chemical accidents. CCPS/AIChE,  Skogestad, S., Postlethwaite, I. Multivariable
                  New York, 1987, pp. 4±69.         Feedback Control. John Wiley & Sons, 1996
                 Koolen, J.L.A., Sinke, D.J., Dauwe, R.  ISBN 0471±942 774.
                  Optimization of a total plant design,  Smith, R. Chemical Process Design. McGraw-
                  Escape-9. Computers Chem. Eng. 1999, 23,  Hill, Inc., 1995. ISBN 0-007-059220-9.
                  S31±S34.                         Smith, R., Linnhoff, B. The design of
                 Kotas, T.J. The Exergy Method of Thermal Plant  separators in the context of overall. Process.
                  Analysis. Krieger Publishing Co., 1995.  Trans. IChemEChem. Eng. Res. Des. 1988, 66,
                  ISBN 0-89464-941-8.               195±228.
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