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23-Chem-B4 Biochemical Engineering · May 2013

Question 3 of 6: Batch Culture Growth Kinetics

Nivaar worked solution (AI-drafted; not reviewed by a licensed engineer)

Notes on this paper

National Exam 04-Chem-B4, Biochemical Engineering — May 2013. 3 hours, Closed-Book Exam (any non-communicating calculator permitted). Six questions are printed; any five (5) constitute a complete paper (100 marks) and only the first five as they appear in the answer book are marked. All six are solved below for completeness.

Reference texts: Shuler & Kargi, Bioprocess Engineering: Basic Concepts, 2nd ed.; Bailey & Ollis, Biochemical Engineering Fundamentals, 2nd ed.; Madigan et al., Brock Biology of Microorganisms, 13th ed.

Question 3: Batch Culture Growth Kinetics (20 marks)

Question text not reproduced: the examination questions are © Engineers and Geoscientists BC. Open the official past paper (linked at the top of this page) to read the question, then follow the worked solution below.

Given.

QuantitySymbolValue
Inoculum concentrationX00.1 g/L
Initial glucose concentrationS010 g/L
Lag timetlag3 h
Doubling time (exponential phase)td2 h
Total time to stationary phasettotal14 h

Find. μmax, YX/S, and the total time to reach stationary phase if S0 were 2 g/L instead of 10 g/L.

Approach. The doubling time fixes μmax directly; exponential growth over the (total − lag) interval gives the biomass concentration reached when the substrate is exhausted (no decline phase ⇒ stationary phase begins exactly when S→0), which yields YX/S from the overall substrate consumed. The same YX/S and μmax then apply to the S0=2 g/L case (S≫KS throughout ⇒ growth stays at μmax right up to substrate exhaustion).

time (h)X (g/L, log scale)lagexponentialstationaryX = 4.53 g/L @ t=14 hBatch growth curve: lag → exponential (td = 2 h) → stationary
Fig. 3 — Batch growth curve (S0=10 g/L case), semi-log X vs t.
  1. Maximum specific growth rate. Exponential growth doubles X every td, so μmaxtd=ln 2: $$\mu_{max}=\frac{\ln 2}{t_d}=\frac{0.6931}{2}=\boxed{0.347\ \text{h}^{-1}}$$
  2. Biomass at the onset of stationary phase. The exponential phase lasts from t=3 h to t=14 h, i.e. texp=11 h: $$X_f=X_0\,e^{\mu_{max}t_{exp}}=0.1\,e^{0.3466(11)}=0.1(45.25)=\boxed{4.53\ \text{g/L}}$$
  3. Yield coefficient. With no decline phase, the culture enters stationary phase exactly when the glucose is exhausted (S→0), so all 10 g/L of substrate was converted to the biomass gained: $$Y_{X/S}=\frac{X_f-X_0}{S_0}=\frac{4.53-0.1}{10}=\boxed{0.443\ \text{g/g}}$$
  4. Time to stationary phase with S0=2 g/L. Since S≫KS holds throughout this fermentation, growth proceeds at μmax right up until the (now smaller) glucose supply is exhausted, using the SAME YX/S and the SAME 3 h lag: $$X_{f,new}=X_0+Y_{X/S}S_{0,new}=0.1+0.443(2)=\boxed{0.985\ \text{g/L}}$$ $$t_{exp,new}=\frac{\ln(X_{f,new}/X_0)}{\mu_{max}}=\frac{\ln(0.985/0.1)}{0.3466}=\frac{2.288}{0.3466}=6.60\ \text{h}$$ $$t_{total,new}=t_{lag}+t_{exp,new}=3+6.60=\boxed{9.60\ \text{h}}$$
QuantityValue
μmax0.347 h-1
YX/S0.443 g/g
Xf at t=14 h (S0=10 g/L)4.53 g/L
Total time to stationary phase (S0=2 g/L)9.60 h