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Published byBruce Gallagher Modified over 5 years ago
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EXAMPLE 1 β Diluting a Toxic Water Supply (Elementary)
A continuous stirred tank (CSTR) has a total volume of 5 liters. It contains 0.5 liters of βdirtyβ water with an initial concentration, π 0 =100 π/πΏ, of some toxic substance represented by variable π. At some moment, 2.5 liters of clean water is added. Draw the process diagram. Does this process seem like batch or continuous? Calculate π after adding the clean, fresh water. In order to be able to clean this water using micro-organisms, the concentration of π needs to be lower than 0.1 π/πΏ. Is it possible to add a sufficient amount of water to the tank such that the concentration of π is below this limit?
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EXAMPLE 2 β Diluting within a Stirred Tank Reactor (Medium)
A continuous stirred tank is filled with water that contains kitchen salt at a concentration of 30 ππ/ π 3 . The water volume is 100 liters. From time π‘=0 onward, fresh water flows in at a flow rate of 5 πΏ/π . The flow rate out of the tank is the same. Draw the process diagram. What is the salt concentration if time π‘ goes to infinity? Setup the salt component mass balance for the stirred tank. Solve this balance and find what the concentration in the salt is at time π‘=20 π .
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EXAMPLE 3 β Antibiotics in a Body (Advanced)
The human kidney removes all kinds of molecules from our bodies. This includes medicine, that you might receive in your blood during a serious illness. This could be an antibiotic, e.g. Gentamicin. In this exercise, we are going to investigate how long it takes to remove 50% of the used Gentamicin. We assume that the intake is instantaneous and that your blood has a concentration of π π‘=0 = π 0 of Gentamicin. Our kidneys do not process our entire blood stream during one cycle. They roughly process 20% of the total blood stream. They donβt remove all Gentamicin that flows through them; actually only a small fraction. We can model this by stating that a blood flow of 0.5 ππΏ/π is going through our kidneys and is completely cleaned from Gentamicin. We can treat our blood system as a CSTR and our heart as the pump (of negligible volume) that pumps the blood around. For the removal of the Gentamicin, 0.5 ππΏ/π of blood flows through our kidneys and gets cleaned. For the modeling of this system, treat the blood system as a 5 liter CSTR. Draw the process diagram. Set up a mass balance for the blood system, treating it as a CSTR. The mass to be considered is that of Gentamicin. At time π‘=0, the concentration of Gentamicin is π 0 . Solve this mass balance and compute how long it takes before the concentration of Gentamicin is half of π 0 .
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EXAMPLE 4 β Unsteady State Mass Balance (Medium)
Letβs consider a vessel where a certain mass flow rate of an aqueous salt solution ( π ππππ‘πππ =1.0 π/πΏ) enters a well-defined volume and the same amount leaves the volume. Initially, the volume was filled with a salt solution with a concentration of 5 π/πΏ water. The vessel is well-mixed by a stirrer. Draw the process diagram. What is the concentration after 20 seconds in the vessel if the volume flow rate is equal to 10 πΏ/π and the volume of the vessel is 100 liters?
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EXAMPLE 5 β Balance on a Mixing Unit (Elementary)
An aqueous solution of sodium hydroxide contains 20% NaOH by mass. It is desired to produce an 8% NaOH solution by diluting a stream of the 20% solution with a stream of pure water. Draw the process diagram. Calculate the ratios (π π» 2 π/π of feed solution) and (π πππππ’ππ‘ π πππ’π‘πππ/π feed solution). Determine the feed rates of 20% solution and diluting water needed to produce 2310 π π π /πππ of the 8% solution.
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EXAMPLE 6 β Balance on a Distillation Column (Medium)
A mixture containing 45% benzene (B) and 55% toluene (T) by mass is fed to a distillation column. An overhead stream of 95wt% B is produced, and 8% of the benzene fed to the column leaves in the bottom stream. The feed rate is 2000 kg/h. Determine the overhead flow rate and the mass flow rates of B and T in the bottom stream.
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EXAMPLE 7 β Two Unit Distillation Process (Advanced)
A labeled flowchart of a continuous steady-state two-unit distillation process is shown below. Each stream contains two components, A and B, in different proportions. Three streams whose flow rates and/or compositions are not known are labeled 1, 2, and 3. Calculate the unknown flow rates and compositions of streams 1, 2, and 3.
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