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Absorption Process

Autor:   •  October 29, 2017  •  Lab Report  •  6,078 Words (25 Pages)  •  758 Views

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Contents

1.        Introduction        2

2.        Background theory        2

2.1 Absorption        2

2.2 Absorption Equipment        3

2.3 Tower packing        3

2.4 Tower fluid mechanics        4

3.        Design Considerations        4

4.        Chemical Engineering Design        5

4.1 Mass balance        5

4.2 Packed Column Diameter        7

4.3 Operating Line        8

4.4 Packed Column Height        8

4.5        Mass transfer        10

5.        Mechanical design        12

5.1 Absorption column        12

5.2 Support plates        13

5.3 Hold down Plates        14

5.4 Liquid Distributors and Redistributors        15

6.        Process Control        16

7.        Safety Considerations        18

  1. Introduction

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As proposed in part one of the report ethanol and carbon dioxide coming out from the fermenter is going to the absorption column for the maximum recovery of ethanol. They both are in the vapour phase and a homogenous separation is needed to be carried out. For the recovery of ethanol a packed tower absorption column is installed which will absorb the carbon dioxide introduced from the bottom of the column with the help of the solvent water introduced from the top (counter current). A compressor is also needed which compress the carbon dioxide coming from the column so that it can be sold to the chemical industries.

  1. Background theory

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In this section some brief background theory is described about the packed column absorption and how it works.

2.1 Absorption

Absorption is a process by which a gas mixture is contacted with a liquid solvent that preferentially dissolves one or more components of the gas. It is generally used for separating low molecular weight materials and often requires an extraneous material (liquid solvent).

Absorption is based on Henry’s law:

Pi= Hi xi

Where, pi = partial pressure of component i                                                                                     Hi = Henry’s law constant (determined experimentally)                                                                           xi= mole fraction of component i in the liquid phase

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