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04-BS-13 · December 2015

Question 1 of 10: Klebsiella aerogenes Oxygen Requirement from Glycerol

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

Notes on this paper

National Exams — December 2015 — 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. Q1–Q4, Q7, and Q8 are calculation questions; Q5, Q9, and Q10 are essay questions; Q6 is a derivation.

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

Question 1: Klebsiella aerogenes Oxygen Requirement from Glycerol (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.

QuantityValue
Biomass yield from glycerol, $Y_{XS}$ (dry wt., incl. ash)0.40 g/g
Ash content of biomass8%
Biomass formula (ash-free)CH1.75O0.43N0.22, MW = 23.71 g/cmol
MW glycerol92 g/mol
$\gamma_S$ (glycerol) / $\gamma_B$ (biomass)4.67 / 4.23

Find. The oxygen requirement of the culture, in mass terms (g O2 per g glycerol consumed).

Approach. The yield and ash correction fix the biomass coefficient $c$; the nitrogen balance then gives $b$, and the C/H/O atom balances solve the remaining unknowns $d$, $e$, $a$. The available-electron (degree-of-reduction) balance provides an independent cross-check on $a$ that does not depend on the C/H/O bookkeeping at all.

  1. Biomass coefficient $c$ from the yield and ash correction. Per mole glycerol (92 g), dry biomass formed $=Y_{XS}(92)=0.40(92)=36.8$ g. Only 92% of this is the ash-free CH1.75O0.43N0.22 material (the ash carries no C/H/N/O balance obligation): ash-free mass $=36.8(0.92)=33.856$ g, so $$c=\frac{33.856}{23.71}=\boxed{1.428\ \text{cmol biomass/mol glycerol}}.$$
  2. Nitrogen balance → $b$. NH3 is the only N source and biomass the only N sink: $$b=0.22c=0.22(1.428)=0.314\ \text{mol NH}_3\text{/mol glycerol}.$$
  3. Carbon balance → $d$. Glycerol supplies 3 C per mole, split between biomass and CO2: $$3=c+d \;\Rightarrow\; d=3-1.428=1.572\ \text{mol CO}_2\text{/mol glycerol}.$$
  4. Hydrogen balance → $e$. $$8+3b=1.75c+2e \;\Rightarrow\; e=\frac{8+3(0.314)-1.75(1.428)}{2}=\boxed{3.222\ \text{mol H}_2\text{O/mol glycerol}}.$$
  5. Oxygen balance → $a$ (atom-balance route). $$3+2a=0.43c+2d+e \;\Rightarrow\; a=\frac{0.43(1.428)+2(1.572)+3.222-3}{2}=\boxed{1.990\ \text{mol O}_2\text{/mol glycerol}}.$$
  6. Cross-check via the available-electron balance. With NH3 at zero reference degree of reduction, the substrate's available electrons split between biomass and the O2 sink (no other product): $$\gamma_S\,(3\ \text{C atoms})=\gamma_B\,c+4a \;\Rightarrow\; a=\frac{4.67(3)-4.23(1.428)}{4}=1.992\ \text{mol O}_2\text{/mol glycerol}.$$ This agrees with the atom-balance value of 1.990 to within rounding of the given $\gamma$ values — a strong, independent confirmation.
  7. Convert to mass terms. Using $a=1.990$ mol O2/mol glycerol (MW O2 = 32): $$\text{O}_2\ \text{requirement}=\frac{1.990(32)}{92}=\boxed{0.692\ \text{g O}_2\text{/g glycerol consumed}}.$$
QuantityResult
Biomass coefficient, $c$1.428 cmol/mol glycerol
NH₃ coefficient, $b$0.314 mol/mol glycerol
CO₂ / H₂O coefficients, $d$, $e$1.572 / 3.222
O₂ coefficient, $a$ (atom / electron balance)1.990 / 1.992 mol/mol glycerol
Oxygen requirement (mass)0.692 g O₂/g glycerol
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