PROBLEM 1 A desired yeast concentration of 50 g dry cell weight / L will be achieved using 100,000 L batch reactor. The aerobic growth is described by the following equation, with glucose as the carbon source. C6 H12O6 + 3 02 + 0.48 NH3 0.48 C6 H10 NO3 (yeast) + 3.12 CO2 + 4.32 H2O Question 1.2 Determine the total mass of (NH4), SO4 (in kilograms) needed to be mixed with the nutrient medium. Ammonium sulfate will be the source of ammonia as given by the reaction below. (NH4), SO4 – 2 NH3 + H2 SO4

Introduction to Chemical Engineering Thermodynamics
8th Edition
ISBN:9781259696527
Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Publisher:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark Swihart
Chapter1: Introduction
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Question 8
PROBLEM 1
A desired yeast concentration of 50 g dry cell weight / L will be achieved using 100,000 L batch reactor. The aerobic growth is
described by the following equation, with glucose as the carbon source.
C6 H12O6 + 3 02 + 0.48 NH3
» 0.48 C6 H10 NO3 (yeast) + 3.12 CO2 + 4.32 H20
Question 1.2 Determine the total mass of (NH4), SO, (in kilograms) needed to be mixed with the nutrient medium.
Ammonium sulfate will be the source of ammonia as given by the reaction below.
(NH4), SO4 – 2 NH3 + H, SO4
Next
Transcribed Image Text:Question 8 PROBLEM 1 A desired yeast concentration of 50 g dry cell weight / L will be achieved using 100,000 L batch reactor. The aerobic growth is described by the following equation, with glucose as the carbon source. C6 H12O6 + 3 02 + 0.48 NH3 » 0.48 C6 H10 NO3 (yeast) + 3.12 CO2 + 4.32 H20 Question 1.2 Determine the total mass of (NH4), SO, (in kilograms) needed to be mixed with the nutrient medium. Ammonium sulfate will be the source of ammonia as given by the reaction below. (NH4), SO4 – 2 NH3 + H, SO4 Next
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