Theory of Residence Time Distributions

[1]  B. A. Buffham Model-independent aspects of tracer chromatography theory , 1973, Proceedings of the Royal Society of London. A. Mathematical and Physical Sciences.

[2]  Noriaki Wakao,et al.  A NOTE ON CHROMATOGRAPHIC PARAMETER ESTIMATION , 1975 .

[3]  Dynamic testing—a unification , 1970 .

[4]  P. V. Danckwerts Continuous flow systems , 1953 .

[5]  P. Marchot,et al.  Mathematical modelling of the liquid trickling flow through a packed bed using the percolation theory , 1979 .

[6]  D. Luss,et al.  Packed Bed Liquid Phase Dispersion in Pulsed Gas-Liquid Downflow , 1980 .

[7]  L. Gibilaro On the residence time distribution for systems with open boundaries , 1978 .

[8]  L. Gibilaro Mean residence times in continuous flow systems , 1977, Nature.

[9]  R. Shinnar,et al.  Interpretation of Tracer Experiments in Systems with Fluctuating Throughput , 1969 .

[10]  Michael L. Michelsen,et al.  The use of residence time distribution data for estimation of parameters in the axial dispersion model , 1970 .

[11]  R. Shinnar,et al.  A comparison of lumped-parameter and diffusional models describing the effects of the outlet boundary conditions on the mixing in flow systems , 1976 .

[12]  J. Villermaux,et al.  Residence time distribution in the liquid phase of trickle flow in packed columns , 1969 .

[13]  D. D. Perlmutter,et al.  A unified treatment of the inlet boundary condition for dispersive flow models , 1976 .

[14]  David Mautner Himmelblau,et al.  Process analysis and simulation , 1968 .

[15]  Y. Zvirin,et al.  Interpretation of internal tracer experiments and local sojourn time distributions , 1976 .

[16]  Th.N. Zwietering The degree of mixing in continuous flow systems , 1959 .

[17]  Milorad P. Dudukovic,et al.  A new tracer method for determination of liquid‐solid contacting efficiency in trickle‐bed reactors , 1976 .

[18]  R. Gardner,et al.  Use of a finite-stage transport concept for analyzing residence time distributions of continuous processes , 1979 .

[19]  J. D. Perkins,et al.  The boundary conditions for a tubular vessel with well-mixed entrance region , 1974 .

[20]  A generalized mixing history model of an imperfectly mixed cstr , 1973 .

[21]  R. Higgins Fast Fourier transform: An introduction with some minicomputer experiments , 1976 .

[22]  M. Michelsen,et al.  On the use of the imperfect tracer pulse method for determination of hold-up and axial mixing† , 1969 .

[23]  J. M. Smith,et al.  Transport Rates by Moment Analysis of Dynamic Data , 1978 .

[24]  R. Shinnar,et al.  The Measurement and Interpretation of Contact Time Distributions for Catalytic Reactor Characterization , 1973 .

[25]  M. Farid,et al.  Liquid distribution and redistribution in packed columns—II. Experimental , 1978 .

[26]  F. Vergnes A simple and practical method for the determination of the Peclet number in the longitudinal dispersion model , 1976 .

[27]  E. Nauman Mixing in Polymer Reactors , 1974 .

[28]  E. Nauman,et al.  The theory of contact time distributions in gas fluidized beds , 1968 .

[29]  Yatish T. Shah,et al.  Backmixing in gas‐liquid reactors , 1978 .

[30]  L. Gibilaro Residence time distributions in regions of continuous flow systems , 1979 .

[31]  K. Westerterp,et al.  Elements of chemical reactor design and operation , 1963 .

[32]  Karl Schügerl,et al.  Gas holdup and longitudinal dispersion in different types of multiphase reactors and their possible application for microbial processes , 1977 .

[33]  L. Janssen,et al.  Residence time distributions in a plasticating twin screw extruder , 1979 .

[34]  K. B. Bischoff,et al.  MIXING AND CONTACTING IN CHEMICAL REACTORS , 1966 .

[35]  J. Buoncristiani,et al.  Parameter estimates of a left ventricular model during ejection. , 1973, IEEE transactions on bio-medical engineering.

[36]  D. Gunn Liquid distribution and redistribution in packed columns-I Theoretical , 1978 .

[37]  Jacques Villermaux,et al.  Un réacteur continu parfaitement agité par jets gazeux pour l'étude cinétique de réactions chimiques rapides , 1973 .

[38]  L. G. Gibilaro,et al.  A unified time delay model for dispersion in flowing media , 1970 .

[39]  Kenneth B. Bischoff,et al.  Patterns of Flow in Chemical Process Vessels , 1964 .

[40]  J. Moulijn,et al.  The evaluation in time domain of mass transfer parameters from chromatographic peaks , 1979 .

[41]  L. Gibilaro,et al.  Numerical evaluation of mean and variance from the Laplace transform , 1972 .

[42]  J. M. Smith,et al.  Liquid distribution in trickle‐bed reactors: Part I. Flow measurements , 1978 .

[43]  R. Shinnar,et al.  Representation and Evaluation of Residence Time Distributions , 1963 .

[44]  E. B. Nauman Residence times and cycle times in recycle systems , 1974 .

[45]  Irving Langmuir,et al.  THE VELOCITY OF REACTIONS IN GASES MOVING THROUGH HEATED VESSELS AND THE EFFECT OF CONVECTION AND DIFFUSION. , 1908 .

[46]  W. C. Clements A note on determination of the parameters of the longitudinal dispersion model from experimental data , 1969 .

[47]  J. Pearson A note on the “ Danckwerts ” boundary conditions for continuous flow reactors , 1959 .

[48]  Dudley Brian Spalding,et al.  A note on mean residence-times in steady flows of arbitrary complexity , 1958 .

[49]  Liang-tseng Fan,et al.  Critical Evaluation of Boundary Conditions for Tubular Flow Reactors , 1962 .

[50]  H. Weinstein,et al.  Estimation of circulating blood volume from a tracer-response curve. , 1973, IEEE transactions on bio-medical engineering.

[51]  P. R. Ponzi,et al.  Effect of flow maldistribution on conversion and selectivity in radial flow fixed‐bed reactors , 1979 .