ENCH 445: Separation Processes

     Instructor: Douglas D. Frey

 


 

Lecture 1 -- Basic Concepts

 

Goals of course can be illustrated by describing several illustrative separation processes:

 

1. Production of decaffeinated instant coffee, which consists of the steps of:

 

    A. Caffeine removal from (steamed) green beans.

 

    B. Roasting and grinding of green beans.

 

    C. Coffee extraction.

 

    D. Multieffect evaporation to remove bulk of water from extract

 

    E. Spray (or freeze) drying of remainder of water.

 

2. Caffeine removal in above process can be accomplished by several methods:

 

    A. Direct method: contacting with methylene chloride

 

    B. Indirect method: contact coffee beans with hot water, caffeine removed from hot water by contacting with methylene chloride.

 

    C. Swiss method: contact coffee beans with hot water, caffeine removed from hot water by adsorption onto activated carbon.

 

    D. Contact green beans with supercritical carbon dioxide.

 

3. Points to consider for above process:

 

    A. Cost of separation equipment for a chemical process is generally greater than 50% of capital cost, and for production of decaffeinated instant coffee it is greater than 90%.

 

    B. Why use countercurrent flow?

 

    C. Why concentrate extract in several steps?

 

    D. Why is aroma retention a consideration in step 1.D but not 1.E?

 

    E. What considerations lead to the selection of solvents in decaffeination steps?

 

4. This brings us to the goals of the course, which are:

 

    A. Develop skills in qualitative reasoning and conceptual design.

 

    B. Develop skills in quantitative design.

 

5. Example 2: Sweetening of sour gas

 

    A. Natural gas often contains small amounts of hydrogen sulfide, the removal of which is termed "sweetening."

 

    B. The most common process is countercurrent absorption into a mixture of water and ethanolamine.

 

    C. Quantitative design considerations:

 

          I. What are the diameter and height for absorption column?

 

          II. What is inside the absorption column (is it empty, full of a "packing", or does it have "plates")?

 

          III. For a given flow rate of natural gas, what should the flow rate of absorbing liquid be?

 

          IV. What is the operating pressure?

 

          V. Mechanical-type design questions (e.g., how thick should the walls of absorption column be) will not be considered.

 

6. General features of separation processes:

 

    A. All separation processes require a "separating agent" to function, due to the fact that mixing is a spontaneous process. Separation processes are the opposite of mixing process and are therefore never spontaneous. The separating agent makes the separation process run in the desired direction.

 

    B. Separation processes can be classified by various methods, e.g.,

 

         I. What is the separating agent (energy, mass etc.)?

 

         II. Is it a mechanical process (heterogenous feed) or a diffusional process (homogeneous feed) where there is diffusional transfer from a "feed" phase to a "product" phase?

 

         III. Diffusional processes can be further subdivided into equilibration processes, which operate through equilibrium between phases, or rate-governed processes, which involve differential rates of mass transfer to achieve a separation.

 

7. Links of interest: