4.12 Production of 1,3-propanediol A process for microbial synthesis of 1,3-propanediol is being developed for the manufacture of 'green'...

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Chemistry

4.12 Production of1,3-propanediol

A process for microbial synthesisof 1,3-propanediol is being developed for the manufacture of'green' polyester fabric from renewable resources. Under anaerobicconditions, a selected strain of Klebsiella pneumoniae convertsglycerol ((231-1803) to 1,3-propanedi01 (C3H802) and acetic acid(C2H402), with minimal formation of other fermentation productssuch as butyric acid, ethanol, and 1-12 gas. The fermentation andcell growth equation can be written as:

                68 C3H803 + 3 NH3 = 3 C4H702N + 49 C3H802 + 15 C2H402 + 15 C02 + 40H20

where C4H702N represents thebiomass.

A continuous fermenter is set up for1,3-propanediol production at 37o c and atmosphericpressure. Anaerobic conditions are maintained by sparging the brothwith nitrogen gas at a flow rate of 1000 litres min—I. The feedrate of medium into the fermenter is 1000 kg h—l; the mediumcontains ammonia and 14% w/ w glycerol. The yield of 1,3propanediolis strongly affected by glycerol concentration, which must be keptabove a certain level to suppress the formation of undesiredby-products. Accordingly, the fermentation process is designed sothat the product stream contains an unreacted glycerolconcentration of 3% w/ w.

A: What is the volumetric flow rateand composition of the off-gas?

B: What minimum concentration of NH3 is needed in the feedstream?

C: If the NH3 concentration from (b) is used, what is theconcentration of 1,3-propanediol in the product stream?

Answer & Explanation Solved by verified expert
3.9 Ratings (406 Votes)
The feed of glycerol is 14 ww of glycerol which means that 100 Kg feed contains 14 Kg Glycerol The flow rate of the medium is 1000 Kgh so it contains 140 Kgh of glycerol The off gas from the reaction will be the CO2 produced and the Nitrogen blowing through the    See Answer
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