DESIGN OF DISTILLATION COLUMN

  • Type: Project
  • Department: Chemical Engineering
  • Project ID: CNG0230
  • Access Fee: ₦5,000 ($14)
  • Pages: 24 Pages
  • Format: Microsoft Word
  • Views: 692
  • Report This work

For more Info, call us on
+234 8130 686 500
or
+234 8093 423 853

Azeotropic distillation of ethanol-water mixture is accomplished by adding a volatile third

component to the liquid which changes the volatility of one of the two components more than the

other so the components are separated by distillation. The two components to be separated often

have similar boiling point components which do or do not azeotrope in the binary mixture, but

sometimes there are components which do azeotrope despite having vastly different boiling points.

It is likely that in some cases, one system can be separated either by

azeotropic distillation or by extractive distillation, for instance , alcohol/water, acid/water, etc.

The added third component, sometimes called the entrainer, may form a ternary azeotrope with

the two components being separated. However, it must be sufficiently volatile from the solution so

that it is taken overhead with one of the two components in the azeotropic distillation column

Contents 

1  Introduction ................................................................................................................................ 4 

Distillation Column Design.................................................................................................................. 4 

2  Feed Data Base ............................................................................................................................ 5 

Mole Fraction ..................................................................................................................................... 5 

Average Molecular Weight ................................................................................................................. 6 

Mass Balance ...................................................................................................................................... 6 

3  Minimum Reflux Ratio ............................................................................................................... 7 

4  Different R .................................................................................................................................... 8 

R=1.3Rmin .......................................................................................................................................... 8 

R=1.5Rmin .......................................................................................................................................... 8 

R=1.7Rmin .......................................................................................................................................... 9 

5  Temperatures and concentration of vapour ....................................................................... 10 

6  Diameter..................................................................................................................................... 11 

Top diameter .................................................................................................................................... 12 

Bottom diameter .............................................................................................................................. 13 

7  Heat loss ..................................................................................................................................... 14 

Heat loss without the insulation ....................................................................................................... 15 

Insulation .......................................................................................................................................... 16 

75 mm insulation ........................................................................................................................ 16 

50 mm insulation ........................................................................................................................ 16 

25 mm insulation ........................................................................................................................ 17 

8  Condenser .................................................................................................................................. 17 

Latent heats ...................................................................................................................................... 17 

Vapour mass flow rate in the top ..................................................................................................... 18 

Heat Transfer .................................................................................................................................... 18 

hi at 30℃ .......................................................................................................................................... 18 

Overall heat transfer coefficient ....................................................................................................... 19 

Area .................................................................................................................................................. 19 

Number of pipes ............................................................................................................................... 20 

Cross sectional area .......................................................................................................................... 20 

Velocity ............................................................................................................................................. 20 

hiat 30℃ .......................................................................................................................................... 20 

Actual overall heat transfer coefficient ............................................................................................ 21 

Actual Area ....................................................................................................................................... 21 

Actual Number of pipes .................................................................................................................... 21 

Actual Cross sectional area ............................................................................................................... 21 

Actual velocity .................................................................................................................................. 22 

Pitch ................................................................................................................................................. 22 

   

DESIGN OF DISTILLATION COLUMN
For more Info, call us on
+234 8130 686 500
or
+234 8093 423 853

Share This
  • Type: Project
  • Department: Chemical Engineering
  • Project ID: CNG0230
  • Access Fee: ₦5,000 ($14)
  • Pages: 24 Pages
  • Format: Microsoft Word
  • Views: 692
Payment Instruction
Bank payment for Nigerians, Make a payment of ₦ 5,000 to

Bank GTBANK
gtbank
Account Name Obiaks Business Venture
Account Number 0211074565

Bitcoin: Make a payment of 0.0005 to

Bitcoin(Btc)

btc wallet
Copy to clipboard Copy text

500
Leave a comment...

    Details

    Type Project
    Department Chemical Engineering
    Project ID CNG0230
    Fee ₦5,000 ($14)
    No of Pages 24 Pages
    Format Microsoft Word

    Related Works

    ABSTRACT This is an abstract on the construction of a packed distillation column. A packed distillation column is used in the separating process distillation that is the separation of two miscible liquids.  It was constructed by marking out the dimension of the column, condenser, pot, using steel rule scriber, oxyacetylene flame was used for... Continue Reading
    ABSTRACT This is an abstract on the construction of a packed distillation column. A packed distillation column is used in the separating process distillation that is the separation of two miscible liquids. It was constructed by marking out the dimension of the column, condenser, pot, using steel rule scriber, oxyacetylene flame was used for... Continue Reading
    ABSTRACT This is an abstract on the construction of a packed distillation column. A packed distillation column is used in the separating process distillation that is the separation of two miscible liquids.  It was constructed by marking out the dimension of the column, condenser, pot, using steel rule scriber, oxyacetylene flame was used for... Continue Reading
    ABSTRACT This is an abstract on the construction of a packed distillation column. A packed distillation column is used in the separating process distillation that is the separation of two miscible liquids. It was constructed by marking out the dimension of the column, condenser, pot, using steel rule scriber, oxyacetylene flame was used for... Continue Reading
    ABSTRACT In this project, distillation is made up of a column, condenser and reflux divider. An overview of the dimensions of some of the major parts is: Height of the column = 450mm Diameter of the column = 100mm Length of the condenser = 150mm Diameter of the condenser... Continue Reading
    ABSTRACT Distillation unit is the judgment used for the separation of liquid mixture depending on the volatility of the component. It has the top section and bottom section. In the top section this is where more volatile component goes and the bottom section is where the divider or less volatile component... Continue Reading
    ABSTRACT Facts have been established by researchers and they justify that the English used in Nigeria is a variation of the British English (BE) and not a deviation from the norms of BE. This is an attempt to investigate the extent to which Nigerian columnists use the lexico-semantic features of Nigerian English for their reportings. This work has... Continue Reading
    ABSTRACT Facts have been established by researchers and they justify that the English used in Nigeria is a variation of the British English (BE) and not a deviation from the norms of BE. This is an attempt to investigate the extent to which Nigerian columnists use the lexico-semantic features of Nigerian English for their reportings. This work has... Continue Reading
    ABSTRACT Facts have been established by researchers and they justify that the English used in Nigeria is a variation of the British English (BE) and not a deviation from the norms of BE. This is an attempt to investigate the extent to which Nigerian columnists use the lexico-semantic features of Nigerian English for their reportings. This work has... Continue Reading
    ABSTRACT  Facts have been established by researchers and they justify that the English used in Nigeria is a variation of the British English (BE) and not a deviation from the norms of BE. This is an attempt to investigate the extent to which Nigerian columnists use the lexico-semantic features of Nigerian English for their reportings. This work... Continue Reading
    Call Us
    Get this work
    whatsappWhatsApp Us