Title: NEURAL NETWORK MODELING OF THE MIXED CULTURE CULTIVATION FOR PHB PRODUCTION PROCESS
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- Lyubenova V., M. Ignatova, M. Novak, ?.
Patarinska, (2007), Reaction rates estimators of
fed-batch process for poly-?-hydroxybutyrate
(PHB) production by mixed culture, Biotechnology
BioE, No 21, (Sofia), pp 113-116. - ? ???????? ??? ?????? ??????
- Ignatova M.N., V. Lyubenova, Control of class
bioprocesses using on-line information of
intermediate metabolite production and
consumption rates, Acta Universitatis
Cibiniensis, Series E Food Technology, I.S.S.N.
1221-4973, Vol. 9, No1 (2007), Sibiu, Romania.
(in press). - Popova S., Adaptive control for PHB production,
Acta Universitatis Cibiniensis, Series E Food
Technology, I.S.S.N. 1221-4973, Vol. 9, No1
(2007), Sibiu, Romania. (in press). - Ignatova M,N, V.N. Lyubenova, (2007), Adaptive
control of fed-batch process for
poly-?-hydroxybutyrate production by mixed
culture, Proceedings of Bulgarian Academy of
Sciences, V. 60 (5), pp 517-524. - ?? ???????????
- Koprinkova-Hristova, P., Fuzzy control approach
to mixed culture cultivation for PHB production
process, Automation and Information 2007, Vol II,
pp III-65-III-68.
4FUZZY CONTROL APPROACH TO MIXED CULTURE
CULTIVATION FOR PHB PRODUCTION PROCESS
- P. Koprinkova-Hristova
- Institute of Control and System Research,
Bulgarian Academy of Sciences
5PHB PRODUCTION PROCESS
X1 - cell concentration of L. delbrueckii X2 -
cell concentration of R. euthropha S - glucose
concentration P - lactate concentration N - NH3
concentration Q - product, i.e. PHB concentration
The typical initial conditions
6specific growth and consumption rates
7Process control approaches 1
Fig. 1. Process control scheme C1- dissolved
oxygen concentration controller C2 - glucose
concentration controller as aeration speed
afr air flow rate
8Process control approaches 2change DO control
strategies
9Process control approaches 3change S control
strategy
10Crisp control results
e1-0.1 and e20.1
Fig. 2. Simulation results for the first crisp
control strategy
Fig. 3. Simulation results for the second crisp
control strategy
11Fuzzy control results 1
Change DO control strategy
- dP fuzzy levels below e1, between e1 and e2
and above e2 - DO fuzzy levels
- around 0.5, around 1.75 and around 3
- around 0.5 and around 3
- membership functions - bell-shaped
Change S control strategy
S fuzzy levels high and low dP fuzzy
levels high and low membership functions
triangular-shaped
12Fuzzy control results 2
Fig. 4. Simulation results for the first fuzzy
control strategy
Fig. 5. Simulation results for the second fuzzy
control strategy
13Comparative study of the results 1
Fig. 6. Comparative results for the lactate
concentration
14Comparative study of the results 2
Fig. 7. Comparative results for the PHB
concentration
15- Thank you
- for your
- attention!