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04-BS-13 · December 2013

Question 4 of 10: Yeast Growth on Glucose — Yield Coefficients and Oxygen Requirement

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

Notes on this paper

National Exams — December 2013 — 04-BS-13, Biology. Three-hour, closed-book exam (one double-sided aid sheet permitted, approved Casio/Sharp calculator allowed). Format: Part I offers 6 questions (any 3 constitute a complete answer, 20 marks each) and Part II offers 4 questions (any 2 constitute a complete answer, 20 marks each) — a full paper is 5 questions. All 10 are solved below for completeness. Most questions require an essay-format answer; Q1–Q4 and Q7 are calculation questions.

Reference texts: Shuler & Kargi, Bioprocess Engineering: Basic Concepts (2nd ed., Prentice Hall) — elemental/electron balances, yield coefficients, fermenter energy balances, growth kinetics; Madigan et al., Brock Biology of Microorganisms (15th ed., Pearson) — bacterial/viral morphology, physiology and growth control; Toledo, Fundamentals of Food Process Engineering (3rd ed., Springer) — plant/animal tissue structure.

Question 4: Yeast Growth on Glucose — Yield Coefficients and Oxygen Requirement (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.

QuantityValue
Balanced equation coefficients1 glucose : 3 O₂ : 0.48 NH₃ → 0.48 biomass : 4.32 H₂O : 3.12 CO₂
MW glucose / O₂ / yeast / NH₃180 / 32 / 144 / 17 g/mol
Reactor volume, $V$100 000 L
Final yeast concentration, $X_f$50 g/L
Exponential-phase growth rate, $r_X$0.7 g biomass/(L·h)

Find. (a) $Y_{XS}$, $Y_{XO_2}$; (b) total O2 required for the batch; (c) O2 consumption rate during exponential growth.

Approach. The equation is already fully balanced, so both yield coefficients follow directly from mass ratios of the stoichiometric coefficients (moles × MW). Part (b) scales the total biomass to be produced by $1/Y_{XO_2}$; part (c) applies the same yield coefficient to convert the given biomass-formation rate into an O2-consumption rate.

  1. Part (a): yield coefficients directly from the balanced equation (basis 1 mol glucose). $$Y_{XS}=\frac{0.48(144)}{1(180)}=\frac{69.12}{180}=\boxed{0.384\ \text{g biomass/g glucose}},$$ $$Y_{XO_2}=\frac{0.48(144)}{3(32)}=\frac{69.12}{96}=\boxed{0.720\ \text{g biomass/g O}_2}.$$
  2. Part (b): total biomass to be produced, then total O₂. $$m_{X,\text{total}}=X_f\cdot V = 50(100\,000)=5.0\times10^6\ \text{g}=5000\ \text{kg}.$$ $$m_{\text{O}_2,\text{total}}=\frac{m_{X,\text{total}}}{Y_{XO_2}}=\frac{5.0\times10^6}{0.720}=\boxed{6.944\times10^6\ \text{g} = 6944\ \text{kg O}_2}.$$
  3. Part (c): O₂ consumption rate at $r_X=0.7$ g/(L·h). $$r_{\text{O}_2}=\frac{r_X}{Y_{XO_2}}=\frac{0.7}{0.720}=\boxed{0.972\ \text{g O}_2/\text{(L}\cdot\text{h)}}.$$
QuantityResult
$Y_{XS}$0.384 g biomass/g glucose
$Y_{XO_2}$0.720 g biomass/g O₂
Total biomass produced5000 kg
Total O₂ required6944 kg (2.17×10⁵ mol)
O₂ consumption rate (exp. phase)0.972 g O₂/(L·h)