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 Fermentation products, including species condensed from the off-gas, and bacteria are withdrawn from the tank.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 solutionChapter 5 Solutions
Elementary Principles of Chemical Processes, Binder Ready Version
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)
- 4.59 Using the unilateral z-transform, solve the following difference equations with the given initial conditions. (a) y[n]-3y[n-1] = x[n], with x[n] = 4u[n], y[− 1] = 1 (b) y[n]-5y[n-1]+6y[n-2]= x[n], with x[n] = u[n], y[-1] = 3, y[-2]= 2 Ans. (a) y[n] = -2+9(3)", n ≥ -1 (b) y[n]=+8(2)" - (3)", n ≥ -2arrow_forward(30) 6. In a process design, the following process streams must be cooled or heated: Stream No mCp Temperature In Temperature Out °C °C kW/°C 1 5 350 270 2 9 270 120 3 3 100 320 4 5 120 288 Use the MUMNE algorithm for heat exchanger networks with a minimum approach temperature of 20°C. (5) a. Determine the temperature interval diagram. (3) (2) (10) (10) b. Determine the cascade diagram, the pinch temperatures, and the minimum hot and cold utilities. c. Determine the minimum number of heat exchangers above and below the pinch. d. Determine a valid heat exchange network above the pinch. e. Determine a valid heat exchange network below the pinch.arrow_forwardUse this equation to solve it.arrow_forward
- Q1: Consider the following transfer function G(s) 5e-s 15s +1 1. What is the study state gain 2. What is the time constant 3. What is the value of the output at the end if the input is a unit step 4. What is the output value if the input is an impulse function with amplitude equals to 3, at t=7 5. When the output will be 3.5 if the input is a unit steparrow_forwardgive me solution math not explinarrow_forwardgive me solution math not explinarrow_forward
- give me solution math not explinarrow_forwardgive me solution math not explinarrow_forwardExample (6): An evaporator is concentrating F kg/h at 311K of a 20wt% solution of NaOH to 50wt %. The saturated steam used for heating is at 399.3K. The pressure in the vapor space of the evaporator is 13.3 KPa abs. The 5:48 O Transcribed Image Text: Example (7): Determine thearrow_forward
- 14.9. A forward feed double-effect vertical evaporator, with equal heating areas in each effect, is fed with 5 kg/s of a liquor of specific heat capacity of 4.18 kJ/kg K. and with no boiling point rise, so that 50 per cent of the feed liquor is evaporated. The overall heat transfer coefficient in the second effect is 75 per cent of that in the first effect. Steam is fed at 395 K and the boiling point in the second effect is 373 K. The feed is heated by an external heater to the boiling point in the first effect. It is decided to bleed off 0.25 kg/s of vapour from the vapour line to the second effect for use in another process. If the feed is still heated to the boiling point of the first effect by external means, what will be the change in steam consumption of the evaporator unit? For the purpose of calculation, the latent heat of the vapours and of the steam may both be taken as 2230 kJ/kgarrow_forwardExample(3): It is desired to design a double effect evaporator for concentrating a certain caustic soda solution from 12.5wt% to 40wt%. The feed at 50°C enters the first evaporator at a rate of 2500kg/h. Steam at atmospheric pressure is being used for the said purpose. The second effect is operated under 600mmHg vacuum. If the overall heat transfer coefficients of the two stages are 1952 and 1220kcal/ m2.h.°C. respectively, determine the heat transfer area of each effect. The BPR will be considered and present for the both effect 5:49arrow_forwardالعنوان ose only Q Example (7): Determine the heating surface area 개 required for the production of 2.5kg/s of 50wt% NaOH solution from 15 wt% NaOH feed solution which entering at 100 oC to a single effect evaporator. The steam is available as saturated at 451.5K and the boiling point rise (boiling point evaluation) of 50wt% solution is 35K. the overall heat transfer coefficient is 2000 w/m²K. The pressure in the vapor space of the evaporator at atmospheric pressure. The solution has a specific heat of 4.18kJ/ kg.K. The enthalpy of vaporization under these condition is 2257kJ/kg Example (6): 5:48 An evaporator is concentrating F kg/h at 311K of a 20wt% solution of NaOH to 50wt %. The saturated steam used for heating is at 399.3K. The pressure in the vapor space of the evaporator is 13.3 KPa abs. The 5:48 1 J ۲/۱ ostrarrow_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