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)
Biomass yield from glycerol, $Y_{XS}$ (dry wt., incl. ash)
0.40 g/g
Ash content of biomass
8%
Biomass formula (ash-free)
CH1.75O0.43N0.22, MW = 23.71 g/cmol
MW glycerol
92 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.
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
$$c=\frac{33.856}{23.71}=\boxed{1.428\ \text{cmol biomass/mol glycerol}}.$$
Nitrogen balance → $b$. NH3 is the only N source and biomass the only N sink:
$$b=0.22c=0.22(1.428)=0.314\ \text{mol NH}_3\text{/mol glycerol}.$$
Carbon balance → $d$. Glycerol supplies 3 C per mole, split between biomass and CO2:
$$3=c+d \;\Rightarrow\; d=3-1.428=1.572\ \text{mol CO}_2\text{/mol glycerol}.$$
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.
Convert to mass terms. Using $a=1.990$ mol O2/mol glycerol (MW O2 = 32):
$$\text{O}_2\ \text{requirement}=\frac{1.990(32)}{92}=\boxed{0.692\ \text{g O}_2\text{/g glycerol consumed}}.$$