Liquid Stripping
Table of Contents
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Design of a Stripping Column
Many things must be taken into consideration when designing a stripping column such as temperature, pressure, and flow rate of the gas and liquid entering, the temperature and pressure of the entire unit, the percentage recovery of the solute, the number of equilibrium stages and their efficiency, and the size and type of absorber. All of these must be analyzed in detail as they will all affect the cost, size, and manufacturing process of the column [2].
Equilibrium Stages
The number of equilibrium stages is a very important factor that has to be taken into consideration when designing a stripping column. Normally the desired amount of solute will not transfer into the gas stream after being contacted once, meaning more than stage where the components are contacted are required. The components of each stage leave in equilibrium with each other which results in the name equilibrium stages. The number of equilibrium stages can be determined either graphically using the McCabe-Thiele graphing method (Figure 3) or algebraically using the Kremser equation (Figure 4) [2].
Figure 3: McCabe-Thiele Graphical Method |
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Figure 4: Kremser Equation |
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Equipment
The different types of equipment that are used for liquid stripping can also be used for the very similar separation processes gas absorption and distillation. A detailed breakdown of the equipment that can be used for these 3 processes can be found here.
Simulation Software
When designing a stripper, a lot of mathematical calculations are involved as previously mentioned which can be very time consuming. Before simulation software and programs, chemical engineers would have to do all of these calculations by hand although today there is a lot of software widely available that can do these calculations much faster. Two very similar software packages, Aspen HYSYS and Aspen PLUS which are both made by AspenTech, are two of the most widely used software packages among chemical engineers. The main difference between the two is the industries they are used in as HYSYS is mainly used in petroleum engineering while PLUS is fine chemistry as both of them do a better job modelling the processes used in the industries mentioned [4]. Another useful software packages in general for engineering is MATLAB which can be used to model many separation processes including gas absorption. Another very useful software suite that is specifically designed for process simulations would be Chemstations CHEMCAD which can model many separation processes including gas absorption [5].
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Faculty Advisor: Sarah Meunier