Greaves Patel Chem Eng Res Des 1985 199

Optimum Temperature Trajectories (Feedback Strategies) Albet, J., Le Lann, J.M., Joulia, X. and Koehret, B., In Proceedings Computer Oriented Process Engineering (Elsevier Science Publishers B.V., Amsterdam, 1991), 75. Balasubramhanya, L.S. and Doyle III, F.J., J. Proc. Cont. 10 (2000), 209. Basualdo, M.S. and Ruiz, C.A., Lat. Ame. Appl. Res. 25-S (1995), 29. Barbosa, D. and Doherty, M.F Chem. Eng. Sei. 43 (1988), 529. Bernot, C., Doherty, M.F. and Malone, M.F., Chem. Eng. Sei. 46...

Batch Reactive Distillation Bread

Reactive Distillation processes combine the benefits of traditional unit operations with a substantial progress in reducing capital and operating costs and environmental impact BP Review, 1997 Taylor and Krishna, 2000 . Traditionally, as in many chemical industries, reaction and separation take place separately Figure 9.1 in a batch reactor followed by a batch distillation column Charalambides et al., 1994 . Therefore, the distillation of desired species cannot influence the conversion of the...

Info

Batch Distillation Picture

Representation of Design, Operations and Separations Duties 7.3.1.1. Design and Operation Decision Variables It is aimed to optimally design a batch column capable of processing M number of feed mixtures, each mixture constituted of NCm number of components Multiple Separation Duties, Figure 7.3 . The most important variables characterising a batch column design are the still capacity B0 , the number of theoretical stages N and the vapour boilup rate V . The latter can be used to obtain...

C

inequality constraint model equations, equality constraints initial conditions, equality constraints inequality constraints where C is the conversion of the limiting reactant, xD tf is the composition of distillate at the end of the operation tf , r i is the reflux ratio as a function of time t . Solution method for such optimisation problem has been discussed earlier. Note that other types of dynamic optimisation problems such as minimum time, maximum profit, etc. could also be formulated and...

Design And Operation Optimisation

There are many papers in the literature dealing with the optimisation of the operation of batch distillation for a given column design and for a single separation duty Farhat et al. 1990 Bernot et al., 1991, 1993 Logsdon and Biegler, 1993 Mujtaba and Macchietto, 1993 . However, the design of batch columns has attracted much less attention. The main design parameters Al-Tuwaim and Luyben, 1991 are the Number of stages plates in the column Still capacity batch size Reboiler and condenser size...

Smr

XB1A lt 0.0, 0.0, 0.004,0.996 gt Figure 4.20. MultiBD Column - Product Amounts and Compositions 4.4. Packed Batch Distillation and Model Extensive literature survey shows that only a few considered modelling, simulation and optimal control of such column Hitch and Rousseau, 1988 Hansen and Jorgensen, 1986 . Nad and Spiegel 1987 simulated their experimental packed column using the methods developed for tray columns by estimating the number of trays representative of the packed height. The...