Abstract
The development of a model for simulating the recoveries by pilot-scale disc-stack centrifugation of whole yeast cells, yeast cell debris and protein precipitates prepared by ammonium sulphate salting-out is presented. The model is based on the grade efficiency concept and incorporates the effects of hindered settling at high biomass concentrations and the breakage of shear-sensitive material within the centrifuge feed-zone to give an accurate prediction of solid/liquid separation. The simulations have been proven by comparison with data from pilot-scale verification trials. The trials have highlighted where improvements to the models were required to increase their accuracy. The value of verification trials in proving the validity of models is commented upon.
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Abbreviations
- C v :
-
volume concentration of solids in suspension (−)
- D :
-
dilution factor (−)
- d :
-
particle diameter (μm)
- d c :
-
critical particle diameter (μm)
- E :
-
enzyme activity (U mL−1)
- E T :
-
centrifuge mass yield (−)
- g :
-
acceleration due to gravity (9.81 ms−2)
- k :
-
constant (−)
- k B :
-
breakage constant (−)
- n :
-
constant (−)
- Q :
-
volumetric flowrate (m3 s−1)
- R :
-
total protein concentration (mg mL−1)
- R o :
-
outer disc radius (m)
- R i :
-
inner disc radius (m)
- (T(d) :
-
grade efficiency (−)
- V :
-
volume (L)
- Z :
-
number of discs (−)
- Δϱ :
-
solid-liquid density difference (Kg m−3)
- Δt :
-
change in time (s)
- ΔF :
-
representation for particle size distributions (−)
- θ :
-
disc conical half-angle (rads)
- μ :
-
suspension dynamic viscosity (N s m−2)
- ρ L :
-
liquid phase density (Kg m−3)
- ρ A :
-
aggregate phase density (Kg m−3)
- Σ:
-
area of a simple gravity settling tank of equivalent sedimentation characteristics to that of the centrifuge (m2)
- σ :
-
particle geometric factor (−)
- ω :
-
centrifuge angular velocity (rad s−1)
- R :
-
Total protein
- E :
-
Enzyme
- PPT :
-
Precipitant
- s :
-
Sheared
- f :
-
Feed
- sup :
-
Supernatant
- sed :
-
Sediment
- ppt :
-
Precipitate phase
- sol :
-
Soluble phase
References
Ambler, C.M.: The evaluation of centrifuge performance. Chem. Eng. Prog., March, (1952) 150–158
Bartsch, M.J.: Mathematische Formeln, VEB Fachbuchverlag, Leipzig, (1977)
Baron, G.; Wajc, S.: Fluidised settling in centrifuges, Synopsis 686, Chemical Engineering Technology, 4, (1979) 333–338
Bell, D.J.; Dunnill, P.: Shear disruption of soya protein precipitate particles and the effect of ageing in a stirred tank, Biotechnology and Bioengineering, 24, (1982) 1271–1285
Bell, D.J.; Dunnill, P.: The influence of precipitation reactor configuration on the centrifugal recovery of isoelectric soya protein precipitate, Biotechnology and Bioengineering, 24, (1982b) 2319–2336
Bell, D.J.; Hoare, M.; Dunnill, P.: The formation of protein precipitates and their centrifugal recovery, Advances in Biochemical Engineering/Biotechnology, 26, (1983) Ed. A. Fiechter. Berlin: Springer Verlag, Berlin, 1–72
Bell, D.J.; Heywood-Waddington, D.; Hoare, M.; Dunnill, P.: The density of protein precipitates and its effect on centrifugal sedimentation. Biotechnology and Bioengineering, 24, (1982) 127–141
Bell, D.J.; Brunner, K.-H.: A method for the evaluation of floc breakup in centrifuges, Filtration and Separation, 20 (4), (1983) 274–301
Bergmeyer, H.O.: Methods of Enzymic Analysis, Verlag Chemie, Weinheim (1979)
Bohman, H.: Hydrodynamics of the liquid in the disc-stack of a centrifugal separator, Paper F3, 1st European Conference on Mixing and Centrifugal Separation, September, Cranfield (1974)
Bradford, M.: A rapid and sensitive method for the quantitation of microgram quantities of protein utilizing the principle of proteindye binding, Analytical Biochemistry, 72, (1976) 248–254
Brunner, K.-H.; Molerus, O.: Theoretical and experimental investigation of separation efficiency of disc centrifuges, German Chemical Engineering, 2, (1979) 228–233
Brunning, P.: Scale-up Probleme bei Tellerseparatoren, Technische Dokumentation, Westfalia Separator AG, Oelde, Germany (1987)
Bulmer, M.; Clarkson, A.I.; Titchener-Hooker, N.J.: Pilot-scale verification of bioprocess models, paper in preparation, (1955)
Clarkson, A.I.; Lefevre, P.; Titchener-Hooker, N.J.: A study of process interactions between cell disruption and debris clarification stages in the recovery of yeast intracellular proteins, Biotechnol. Prog., 3, (1993) 462–467
Clarkson, A.I.; Bulmer, M.; Siddiqi, S.; Titchener-Hooker, N.J.: Pilot-scale verification of bioprocess models, Computers Chem. Eng., 18, (1994) S651-S655
Clarkson, A.I.; Bulmer, M.; Titchener-Hooker, N.J.: Pilot-scale verification and a computer-based simulation for fractional protein precipitation, Paper accepted Bioproc. Eng. (1995)
Datar, R.; Rosen, C.J.: Centrifugal separation in the recovery of intracellular protein from E. coli, The Chemical Engineering Journal, 34, (1987) B49-B56
Dehghani, M.; Bulmer, M.; Thornhill, N.F.; Gregory, M.E.; Ison, A.: Assays for fermentation processes with measurement variability analysis, Paper accepted Bioproc. Eng (1995)
Gupta, S.K.: Scale-up procedures for disc-stack centrifuges, Chemical Engineering Journal, 22, (1981) 43–49
Hetherington, P.J.; Follows, M.; Dunnill, P.; Lilly, M.D.: Release of protein from Baker's yeast (Saccharomyces cerevisiae) by disruption in an industrial homogeniser, Trans. Instn. Chem. Engrs., 49, (1971) 142–148
Hemfort, H.: Separatoren, Technische Dokumentation der Westfalia Separator AG, Oelde, Germany (1979)
Hemmingson, A.: Applied Biochemistry and Bioengineering, 2, (1979) 157–183
Higgins, J.J.; Lewis, D.J.; Daly, W.H.; Mosqueira, F.G.; Dunnill, P.; Lilly, M.D.: Investigation f the unit operations involved in the continuous flow isolation of β-galactosidase, Biotechnology and Bioengineering, 20, (1978) 159–182
Mannweiler, K.: The recovery of biological particles in high-speed continuous centrifuges with special reference to feed-zone bream-up effects, Ph.D. Thesis, University of London (1990)
Mannweiler, K.; Hoare, M.: The scale-down of an industrial disc stack centrifuge, Bioprocess Engineering, 8, (1992) 19–25
Mannweiler, K.; Titchener-Hooker, N.J.; Hoare, M.: Biochemical Engineering improvements in the centrifugal recovery of biological particles, I. Chem. E. Symposium — Advances in Biochemical Engineering, (1989) 105–117
Mosqueira, F.G.; Higgins, J.J.; Dunnill, P.; Lilly, M.D.: Characteristics of mechanically disrupted Baker's yeast in relation to its separation in industrial centrifuges, Biotechnology and Bioengineering, 23, (1981) 335–343
Pantelides, C.C.: Speed-up — recent advances in process simulation, Computers and Chemical Engineering, 12 (7), (1988) 745–755
Rehm, H.: Industrielle Mikrobiologie, Berlin, Heidelberg, New York, Tokyo, Springer-Verlag (1980)
Richardson, J.F.; Zaki, W.N.: Sedimentation and Fluidisation: Part I, Trans. Instn. Chem. Engrs. 32, (1954) 35–53
Rumpus, J.: Ph.D. Thesis, University of London (1995)
Sargent, R.W.H.; Westerberg, A.W.: SPEED-UP in chemical engineering design, Trans. Instn. Chem. Engrs., 42, (1964) T190-T197
Siddiqi, S.F.; Titchener-Hooker, N.J.; Ayazi Shamlou, P.: The operating conditions on the generation of cell debris in high-pressure homogenisation of Baker's yeast, Biotech. Bioeng., (submitted) (1995)
Stokes, G.G.: On the effect of the internal fraction on the motion pendulum, Trans. Cam. Phil. Soc. 9, (1951) 8
Titchener-Hooker, N.J.; Hoare, M.; Dunnill, P.: New approaches to the more efficient purification of proteins and enzymes, Biochemical Engineering, 6, Annals New York Acad. Sci., 589 (1991) 157–171
Willus, C.A.; Fitch, B.: Centrifuges: flow patterns in a disc centrifuge, Chemical Engineering Progress, 69 (9), (1973) 93–94
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UCL is the Biotechnology and Biological Sciences Research Council's Interdisciplinary Research Centre for Biochemical Engineering and the Council's support to the participating UCL departments is gratefully acknowledged.
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Clarkson, A.I., Bulmer, M. & Titchener-Hooker, N.J. Pilot-scale verification of a computer-based simulation for the centrifugal recovery of biological particles. Bioprocess Engineering 14, 81–89 (1996). https://doi.org/10.1007/BF00387961
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DOI: https://doi.org/10.1007/BF00387961