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Overall balance for cells growing on carbohydrate
CHmOn + a O2 + b NH3 → c CHαOβNδ + d H2O + e CO2
Components of overall cell-growth balance
Carbon source/substrate; oxygen; nitrogen source; biomass/cells; water; carbon dioxide
Carbon dioxide production during metabolism
CO2 is made at the end of glycolysis/beginning of the TCA cycle when pyruvate is converted to Acetyl-CoA and also during the TCA cycle
CO2 is not produced at
The end of the respiratory chain when electrons are transferred to O2
Mass balance for cell growth with product
CHmOn + a O2 + b NH3 → c CHαOβNδ + d CHxOyNz + e H2O + f CO2
Components of cell growth with product balance
Carbon source/substrate; nitrogen source; biomass/cells; product
Coefficient convention
The coefficient for the carbon source can be set to 1 when its formula contains one carbon; the biomass coefficient can also be set to 1 depending on how the equation is written
Elemental balance: Carbon
1 = c + d + f
Elemental balance: Hydrogen
m + 3b = cα + dx + 2e
Elemental balance: Oxygen
n + 2a = cβ + dy + e + 2f
Elemental balance: Nitrogen
b = cδ + dz
Empirical chemical formula for cell
Defined per gram atom (mole) of carbon as CHαOβNδ
Typical biomass empirical formula values
α ≈ 1.64–2; β ≈ 0.27–0.56; δ ≈ 0.13–0.25
Unknown stoichiometric coefficients
a
Known information needed
Chemical formulas for the carbon source
Mass balance when carbon source and product contain more than one carbon
CHmOn + a O2 + b NH3 → c CHαOβNδ + d CwHxOyNz + e H2O + f CO2
Carbon balance when carbon source has more than one carbon
k = c + dw + f
Hydrogen balance when carbon source has more than one carbon
m + 3b = cα + dx + 2e
Oxygen balance when carbon source has more than one carbon
n + 2a = cβ + dy + e + 2f
Nitrogen balance when carbon source has more than one carbon
b = cδ + dz
Problem with elemental balances
There are six unknowns a
Alternative equation convention
Sometimes the equation is written so the formulas for the carbon source and product contain more than one carbon atom
Alternative balance form
a CkHmOn + b O2 + c NH3 → CHαOβNδ + d CwHxOyNz + e H2O + f CO2
Carbon balance in alternative form
ka = 1 + dw + f
Hydrogen balance in alternative form
am + 3c = α + dx + 2e
Oxygen balance in alternative form
an + 2b = β + dy + e + 2f
Nitrogen balance in alternative form
c = δ + dz
Respiratory quotient (RQ)
A measurable quantity defined as the molar rate of CO2 production divided by the molar rate of O2 consumption
RQ equation
RQ = mol CO2 production / mol O2 consumption
RQ and stoichiometric coefficients
RQ is proportional to the molar coefficients on O2 and CO2 in the overall balance equation
RQ relationship
f = RQ × a
Why RQ is useful
RQ provides a fifth equation along with the carbon
Overall balance with RQ
CHmOn + a O2 + b NH3 → c CHαOβNδ + d CHxOyNz + e H2O + f CO2
Growth yield YX/S
Yield coefficient for cell growth per substrate; grams of biomass produced per gram of substrate consumed
YX/S equation
YX/S = ΔX / -ΔS
Why YX/S is not 1
Not all carbon in the carbon source is converted to cell biomass; a fraction is respired as CO2 during transformation of carbon to energy (ATP)
Substrate energy distribution
Energy from substrate is divided among biomass formation
Typical aerobic YX/S
0.4 to 0.6 g cells/g glucose
Anaerobic YX/S
Lower than the typical aerobic value
Yield coefficient based on oxygen
YX/O2 is the yield coefficient for cell growth based on oxygen
Typical YX/O2
0.9 to 1.4 g cells/g O2 for most yeast and bacteria
Reduced substrates and YX/O2
YX/O2 is lower for highly reduced substrates such as methane
YX/O2 equation
YX/O2 = ΔX / -ΔO2
Meaning of YX/O2
Change in mass of biomass (X) per change in mass of O2
Oxygen sign convention
O2 is consumed
Substrate sign convention
S is consumed
Product yield based on substrate
YP/S is the yield coefficient for product based on substrate
YP/S equation
YP/S = ΔP / -ΔS
Meaning of YP/S
Change in mass of product per change in mass of substrate
Product yield sign convention
S is consumed
Worked microorganism example
A microorganism with formula C18H29O3N3.6 and molecular weight 343.4 g/mol is grown in a batch reactor on a pentose sugar C5H10O5 with molecular weight 150 g/mol for production of ethanol C2H6O with molecular weight 46.0 g/mol
Worked mass balance equation
C5H10O5 + a O2 + b NH3 → c C18H29O3N3.6 + d C2H6O + e H2O + f CO2
Worked carbon balance
5 = c(18) + d(2) + f
Worked hydrogen balance
10 + 3b = c(29) + d(6) + e(2)
Worked oxygen balance
5 + a(2) = c(3) + d + e + f(2)
Worked nitrogen balance
b = c(3.6)
Problem with worked example
There are not enough equations to solve for a
Worked-example yield data
YX/S = 0.229 g cells/g S; YP/S = 0.2147 g P/g S
Meaning of YX/S in worked example
0.229 g cells are produced for each gram of substrate consumed
Meaning of YP/S in worked example
0.2147 g product is produced for each gram of substrate consumed
Calculating moles of cells
Use YX/S and the molecular weights of cells and substrate to convert the yield into moles of cells produced (stoichiometric coefficient c) for each mole of substrate consumed
Calculating moles of product
Use YP/S to calculate the moles of product made (stoichiometric coefficient d) for each mole of substrate consumed
Worked cell coefficient calculation
0.229 g cells/g S × 150 g S/mol S × 1 mol cells/343.4 g cells = approximately 0.1 mol cells/mol S
Worked product coefficient calculation
0.2147 g product/g S × 150 g S/mol S × 1 mol product/46 g product = approximately 0.7 mol product/mol S
Class stopping point
The class stopped here on Friday; the problem will be finished during the next class