Fermentation is a biochemical process in which a carbohydrate—such as the sugar glucose—is converted by bacteria or yeast to an organic compound—such as ethanol—and carbon dioxide. The process is best known for its use in making beer_ wine, and other alcoholic beverages, but it is also used to produce a wide range of other industrially important chemicals.
The diagram below shows a continuous fermentation process. An aqueous solid-liquid slurry containing a carbohydrate and bacteria enters a stirred tank where it undergoes fermentation. Fermentation products, including species condensed from the off-gas, and bacteria are withdrawn from the tank. A mixer with multiple rotating impellers keeps the solids in the tank suspended in the liquid. An air stream enters the fermenter through a sparger (something like an inverted shower head) designed to produce small bubbles that rise through the mixture and remove the CO2 formed in the reaction. Some of the oxygen in the air fed to the fermenter is consumed by the bacteria. The gas products go through a condenser, which condenses most of the water and returns it to the fermenter, and the uncondensed off-gas goes to a dryer and then to a mass spectrometer, where its composition is determined. The ?ow rate of the air feed is measured to be 0.600 SLPM (liters per minute at standard temperature and pressure) and the measured compositions of the air and the off- gas are shown on the diagram. The off-gas is at 28°C and 1.1 atm.
(a) Describe in your own words the purpose of this process and the functions of the mixer, the air, and the sparger.
(b) In a small laboratory fermenter, the mass of the broth in the tank is 0.58 kg, and the broth density is 1.05 kg/L. Calculate the carbon dioxide evolution rate (CER) and the oxygen uptake rate (OUR) in mmol/(h ( L), where the volume unit in the denominator refers to the volume of broth in the tank. Also, calculate the off-gas volumetric ?ow rate in L/min.

Want to see the full answer?
Check out a sample textbook solution
Chapter 5 Solutions
ELEM.PRIN.OF CHEM.PROCESS-ACCESS
Additional Engineering Textbook Solutions
Starting Out with Java: From Control Structures through Data Structures (4th Edition) (What's New in Computer Science)
Degarmo's Materials And Processes In Manufacturing
Starting Out with C++: Early Objects (9th Edition)
Computer Science: An Overview (13th Edition) (What's New in Computer Science)
Database Concepts (8th Edition)
Java How to Program, Early Objects (11th Edition) (Deitel: How to Program)
- #3 Orthonitroanaline (an important intermediate in dyes - called fast orange) is formed from the reaction of orthonitroanaline (ONCB) and aqueous ammonia. This liquid phase reaction is first order in both ONCB and ammonia with k = 0.0017 m³/kmol·min at 188 °C. The initial entering concentration of ONCB and ammonia are 1.8 kmol/m³ and 6.6 kmol/m³, respectively. ONCB is used as the basis of calculation. NO2 CI NO2 NH₂ + NHCI +2NH₂ a) Express the concentration of each species solely as a function of conversion.arrow_forward4. (15 pts)A chemical project with a fixed capital investment without land of $250,000. The operation of the chemical project starts at the end of year 1 with 8-years of project lifetime. The estimated revenue per year is $90,000, the estimated cost of manufacture without depreciation over the project lifetime is $30,000/yr, and the taxation rate is 40%. a. Please determine the yearly depreciation values using the standard MACRS method assuming surplus value of $5,000. b. Please determine the net profit for operation year 1, 5, and 8.arrow_forward2. (10 pts) You got a loan of $300,000 from a bank for your new house at a yearly interest rate of 6%, compounded monthly. How much do you pay total to the bank if the loan is 15 years? How much do you pay total to the bank if the loan is 30 years? 3. (10 pts) You got a 5-year loan of $50,000 to buy a BMW car at a yearly interest rate of 6% Please calculate your monthly payment if it is compounded monthly? Please calculate your quarterly payment if it is compounded quarterly?arrow_forward
- A buffer solution is made by mixing 0.1 M acetic acid (HA) and 0.05 M sodium acetate (A⁻). The pKa of acetic acid is 4.76. Due to an experimental error, the actual pH was not recorded, and we need to solve for the concentration of the conjugate base (A⁻) given that the desired pH should be 4.90. Use the Bisection Method to find the concentration of A.arrow_forward1. (15) John had an loan plan shown in the following discrete cash flow diagram: $4,000 $6,000 GI $2,000 5 7 1 2 3 4 $3,000 $4,000 ? Years a. Please describe this diagram in terms of borrowing and payback. b. How much does John need to pay to totally payoff the loan at the end of year 8 if the interest rate is 8%? c. If John pays the sam amount of money at year 8, how much can John borrow at year 0 without paying back in between with the same interest rate?arrow_forwardA buffer solution is made by mixing 0.1 M acetic acid (HA) and 0.05 M sodium acetate (A⁻). The pKa of acetic acid is 4.76. Due to an experimental error, the actual pH was not recorded, and we need to solve for the concentration of the conjugate base (A⁻) given that the desired pH should be 4.90. Use the Bisection Method to find the concentration of A.arrow_forward
- 1. Liquid heptane is stored in a 100,000-L storage vessel that is vented directly to air. The heptane is stored at 25°C and 1 atm pressure. The liquid is drained from the storage vessel and all that remains in the vessel is the air saturated with heptane vapor. a. Is the vapor in the storage vessel flammable? b. What is the TNT equivalent for the vapor remaining in the vessel? c. If the vapor explodes, what is the overpressure 50 m from the vessel? d. What damage can be expected at 50 m?arrow_forward2. You have decided to use a vacuum purging technique to purge oxygen from a reactor vessel to reduce the concentration to 2.0% (mol). The reactor is 18 ft diameter and 40 ft tall. The temperature is 80°F. Assume that the vacuum purge goes from atmospheric pressure to 10.0 psia. How many purge cycles are required and how many total moles of nitrogen must be used? Assume the purge is done with pure nitrogen. 3. If the purging described in problem 2 takes place using nitrogen that has 1% (mol) oxygen in it, how many vacuum purge cycles are required? How many total moles of the inert gas must be used? 4. If the purging described in problem 2 is done by way of a "sweep-through" purge instead of a vacuum purge, for how long (in minutes) must the inert gas flow through the vessel if there is a 20 psig supply of pure nitrogen available at 150 CFM (ft³/min)? How much nitrogen must be used (lbm)?arrow_forward5. Look at Figure 7-14. Determine the voltage developed between the steel nozzle and the grounded vessel, and how much energy is stored in the nozzle. Explain the potential hazards for cases A and B from the following table: Case A Case B Hose length (ft) 75 75 Hose diameter (in) 2.0 2.0 Flow rate (gpm) 30 30 Liquid conductivity (mho/cm) 2x10-8 1x10-14 Dielectric constant 2.3 25 Density (g/cm³) 0.8 0.9 6. In Problem 5, case B, what would be the most effective way to reduce the potential hazards in this situation?arrow_forward
- 2. You have decided to use a vacuum purging technique to purge oxygen from a reactor vessel to reduce the concentration to 2.0% (mol). The reactor is 18 ft diameter and 40 ft tall. The temperature is 80°F. Assume that the vacuum purge goes from atmospheric pressure to 10.0 psia. How many purge cycles are required and how many total moles of nitrogen must be used? Assume the purge is done with pure nitrogen.arrow_forwardAn 8-foot ion exchange bed needs to be backwashed with water to remove impurities. The particles have a density of 1.24 g/cm³ and an average size of 1.1 mm. Calculate: a. The minimum fluidization velocity using water at 30°C? b. The velocity required to expand the bed by 30%? Assumptions: The ion exchange bed particles are spherical (sphericity = 1.1), and the minimum fluidization porosity (ɛM) is 0.3. Notes: At 30°C, the viscosity (μ) of water is 0.797 cP, and the density (ρ) is 0.995 g/cm³.arrow_forwardfluidized bed reactor uses a solid catalyst with a particle diameter of 0.25 mm, a bulk density of 1.50 g/mL, and a sphericity of 0.90. Under packed bed conditions, the porosity is 0.35, and the bed height is 2 m. The gas enters from the bottom of the reactor at a temperature of 600°C, with a viscosity of 0.025 cP and a density of 0.22 lb/ft³. At minimum fluidization, the porosity reaches 0.45. Calculate: a. The minimum superficial velocity (VM) of the gas entering the fluidized column. b. The bed height if V = 2 VM c. The pressure drop under conditions where V =2.5 VMarrow_forward
- Introduction to Chemical Engineering Thermodynami...Chemical EngineeringISBN:9781259696527Author:J.M. Smith Termodinamica en ingenieria quimica, Hendrick C Van Ness, Michael Abbott, Mark SwihartPublisher:McGraw-Hill EducationElementary Principles of Chemical Processes, Bind...Chemical EngineeringISBN:9781118431221Author:Richard M. Felder, Ronald W. Rousseau, Lisa G. BullardPublisher:WILEYElements of Chemical Reaction Engineering (5th Ed...Chemical EngineeringISBN:9780133887518Author:H. Scott FoglerPublisher:Prentice Hall
- Industrial Plastics: Theory and ApplicationsChemical EngineeringISBN:9781285061238Author:Lokensgard, ErikPublisher:Delmar Cengage LearningUnit Operations of Chemical EngineeringChemical EngineeringISBN:9780072848236Author:Warren McCabe, Julian C. Smith, Peter HarriottPublisher:McGraw-Hill Companies, The





