Distillation unit for separation of benzene-toluene mixture
- Added: 11.07.2018
- Size: 1 MB
- Downloads: 1
Description
1. The apparatus is designed to separate the benzene-toluene mixture. 2. Nominal capacity 10.6 m ³ 3. Capacity 1.944 kg/s. 4. The pressure in the column is atmospheric. 5. The temperature of the medium in the cube is 67.6 ° C. 6. The medium in the apparatus is toxic, corrosive. 7. Type of trays - cap. 8. The number of trays is 20.
Project's Content
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rect.doc
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rect.dwg
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Additional information
Contents
Contents
PLANT FLOW CHART AND DESCRIPTION
PROCESS CALCULATION OF THE APPARATUS
1. Construction of stages of rectification process
1.1 Material balance of the column
1.2 Mass Share Recalculation
1.3 Calculation of working reflux number
1.4 Determination of average mass flow rate of liquid and steam in the column
2. Steam velocity and column diameter
2.1 Physical and chemical properties of the steam and liquid phases of the column
2.2 Steam velocity for poppet columns
2.3 Calculation of column diameter
3. Column Height Determination
3.1 Determination of number and dimensions of caps
4. Calculation of hydraulic resistance
5. Calculation of nozzles and nozzles
6. Heat exchanger calculation Error! Bookmark is not defined
6.1 Refined Heat Transfer Surface Calculation
LIST OF LITERATURE
rect.dwg
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