Sef Heijnen, Department of Biotechnology, Faculty of Applied Sciences
Energy consuming and energy producing products Technology for - - PowerPoint PPT Presentation
Energy consuming and energy producing products Technology for - - PowerPoint PPT Presentation
Energy consuming and energy producing products Technology for Biobased Products Sef Heijnen, Department of Biotechnology, Faculty of Applied Sciences Pseudo steady state flux coupling Substrate limitation q s (c s ) (constant T, pH,
SLIDE 1
SLIDE 2
Pseudo steady state flux coupling
qp(cs) μ(cs) qs(cs)
Product produces energy = anaerobic Product consumes energy = aerobic Substrate limitation à qs(cs) (constant T, pH, pressure)
Black box qCO2(cs) qi(cs)
SLIDE 3
Substrate uptake
qs cs
Hyperbolic function of qs
Parameters qs,max and Ks
Energy consuming and energy producing product
- Assumed to be constant
- Need to be determined
- Depends on organism,
substrate, T and pH
,max * s s s s s
c q K c q = +
SLIDE 4
Substrate for maintenance energy
Repair ms Leakage Degradation Energy producing product Energy consuming product
Anaerobic ms = 0.05 (mol glucose/h)/mol x Aerobic ms = 0.005 (mol glucose/h)/mol x
energy
SLIDE 5
Black box model energy consuming product
qp(cs) μ(cs) qs(cs)
|ms| |a| |b| Branchpoint
Herbert-Pirt substrate distribution relation
qs = a*μ + b*qp + ms qp(μ) = non-linear
Kinetic coupling of qp and μ
mol s mol x mol s mol p
growth product maintenance
SLIDE 6
Aerobic black box PDO model
Glucose uptake rate
- qs = 0.20 cs / (0.5 + cs)
Herbert-Pirt substrate distribution
- qs = 0.25 μ + 0.8 qp+ 0.005
Non-linear qp(μ) relation qp = 0.05 μ /(0.03 + μ) 3 equations 4 variables = 1 free variable which can be μ or cs
growth product maintenance
SLIDE 7
Economics aerobic PDO production
= 1.05 + 5μ + 0.003/μ |qs/qp|= mol glucose
mol PDO
|qs/qp|= 0.25 μ + 0.8 + 0.005 . 0.05 μ /(0.03 + μ) 0.05 μ /(0.03 + μ)
mol glucose mol PDO
0.25 μ + 0.8 qp+ 0.005 0.05 μ /(0.03 + μ) = qs qp =
SLIDE 8
0.5 1 1.5 2 2.5 3 3.5 4 4.5 0.1 0.2 0.3 μ (h-1)
Economics aerobic PDO production
μopt = 0.0245 qp,opt= 0.0227 qs,opt = 0.0294
mol x / h mol x in fermenter mol PDO / h mol x in fermenter mol glucose / h mol x in fermenter
=1.29
mol glucose mol PDO 0.0294 0.0227
=|qs/qp|=
mol glucose mol PDO 0.80 Herbert-Pirt
= 1.05 + 5μ + 0.003/μ |qs/qp|= mol glucose
mol PDO
SLIDE 9
- qs,opt = 0.25 μ,opt
+ 0.8 qp,opt + 0.005
- qs,opt = 0.25*0.0245 + 0.8*0.0227 + 0.005
- qs,opt = 0.0062
+ 0.0182 + 0.005
growth = 21% product = 62% maintenance = 17%
Economics aerobic PDO production
μopt = 0.0245 qp,opt= 0.0227 qs,opt = 0.0294
SLIDE 10
Anaerobic BB model energy producing product
qs(cs)
|ms| |a| ethanol
μ(cs)
Herbert-Pirt substrate distribution relation Stoichiometric (energy) coupling of qp and μ
qs = a*μ + ms qp = ap*μ + mp = linear qp(cs)
energy
growth maintenance
SLIDE 11
Summary black box model
Energy producing product Energy consuming product
Aerobic Anaerobic
qs = a*μ + b* qp + ms qp (μ) is non linear qs = a*μ + ms qp = ap*μ + mp which is linear
,max * s s s s s
c q q K c = +
,max * s s s s s
c q q K c = +
Kinetic coupling qp and μ Stoichiometric (energy) coupling qp and μ
SLIDE 12