Biomedical Engineering Reference
In-Depth Information
23. Soons ZITA, Voogt JA, van Straten G, van Boxtel AJB (2006) Constant specific growth rate
in
fed-batch
cultivation
of
Bordetella
pertussis
using
adaptive
control.
J
Biotechnol
125(2):252-268
24. Bodizs L, Titica M, Faria N, Srinivasan B, Dochain D, Bonvin D (2007) Oxygen control for
an
industrial
pilot-scale
fed-batch
filamentous
fungal
fermentation.
J
Process
Control
17(7):595-606
25. Chung YC, Chien IL, Chang DM (2006) Multiple-model control strategy for a fed-batch high
cell-density culture processing. J Process Control 16(1):9-26
26. Ranjan AP, Gomes J (2009) Simultaneous dissolved oxygen and glucose regulation in fed-
batch methionine production using decoupled input output linearizing control. J Process
Control 19(4):664-677
27. Davison E (1976) Multivariable tuning regulators: the feedforward and robust control of a
general servomechanism problem. IEEE Trans Autom Control 21(1):35-47. doi: 10.1109/tac.
1976.1101126
28. Penttinen
J,
Koivo
HN
(1980)
Multivariable
tuning
regulators
for
unknown
systems.
Automatica 16(4):393-398
29. Maciejowski JM (1989) Multivariable feedback design. Addison-Wiley, Upper Saddle River
30. Bastin G, Dochain D (1990) On-line estimation and adaptive control of bioreactors, vol 1.
Elsevier, Amsterdam
31. Roeva O, Slavov T, Dimov I, Dimova S, Kolkovska N (2011) Fed-batch cultivation control
based on genetic algorithm PID controller tuning numerical methods and applications. vol
6046. Lecture Notes in Computer Science. Springer, Berlin, pp 289-296. doi: 10.1007/978-
3-642-18466-6_34
32. Roeva
O
(2008)
Improvement
of
genetic
algorithm
performance
for
identification
of
cultivation
process
models.
Paper
presented
at
the
proceedings
of
the
9th
WSEAS
international conference on evolutionary computing, Sofia, Bulgaria
33. Roeva O (2005) Genetic algorithms for a parameter estimation of a fermentation process
model: a comparison. Bioautomation 3:19-28
34. Perrier M, de Azevedo SF, Ferreira EC, Dochain D (2000) Tuning of observer-based
estimators: theory and application to the on-line estimation of kinetic parameters. Control
Eng Pract 8(4):377-388
35. Mazouni D, Ignatova M, Harmand J (2004) A simple mass balance model for biological
sequencing batch reactors used for carbon and nitrogen removal. Automatic systems for
building the infrastructure in developing countries, vol IFAC-DECOM04. Bansko, Bulgaria
36. Lyubenova V, Ignatova M, Novak M, Patarinska T (2007) Reaction rates estimators of fed-
batch process for poly- b-hydroxybutyrate (PHB) production by mixed culture. Biotechnol
BioE 21(1):113-116
37. Ignatova M, Lyubenova V (2007) Control of class bioprocesses using on-line information of
intermediate metabolite production and con-sumption rates. Acta universitatis cibiniensis
Series E: Food Technol 11:3-16
38. Ignatova
M,
Lyubenova
V
(2007)
Adaptive
control
of fed-batch
process
for
poly-b
hydroxybutyrate production by mixed culture. Acad Sci 60(5):517-524
39. Kansha Y, Jia L, Chiu MS (2008) Self-tuning PID controllers based on the Lyapunov
approach. Chem Eng Sci 63(10):2732-2740
40. Chang WD, Hwang RC, Hsieh JG (2002) A self-tuning PID control for a class of nonlinear
systems based on the Lyapunov approach. J Process Control 12(2):233-242. doi: 10.1016/s09
59-1524(01)00041-5
41. Renard F, Vande Wouwer A, Valentinotti S, Dumur D (2006) A practical robust control
scheme
for
yeast
fed-batch
cultures—an
experimental
validation.
J
Process
Control
16(8):855-864. doi: 10.1016/j.jprocont.2006.02.003
42. Renard F, Vande Wouwer A (2008) Robust adaptive control of yeast fed-batch cultures.
Comput Chem Eng 32(6):1238-1248. doi: 10.1016/j.compchemeng.2007.05.008
Search WWH ::




Custom Search