Industrial Training Presentation
Topic- Crude Distillation Unit (CDU)
Presented By-
Priyam Jyoti Borah
Roll no- 16/275
Department- Chemical
Crude Oil
Source
1. Assam Crude (Sulphur 0.3%)
2. Ravva Crude (Sulphur 0.1%)
from the Ravva Oil fields of
Andhra Pradesh)
3. Imported Crude (through
Heldia and Miri Crude) higher
then 0.5% Sulpher content
CDU Unit
consists of the
following
Sections
 Crude Preheat
 Desalter
 Fired Heater
 Crude Distillation Section
 Stripper
 Stabilizer
 Naphtha Splitter
 LPG Wash Section
Crude Distillation and Strippers
 Height of column: about 50m
 Number of trays: 38-45
 Feed from fired heater enters under try 5
 Pressure is maintained at 1.3-1.8 kg/cm2.
 Products-
 Distillate
 Bottom Products or residue to DCU
Stabilizer
 Column has 30 trays
 Top Temperature: 65°c
 Top pressure: 10kg/cm2
 The purpose of the stabilizer is to
stabilize naphtha by separating out
liquefied petroleum gas (LPG) and
other C-4 components.
 The fractionate of lower column or
Kero II is used as heating medium
for stabilizer reboiler.
 LPG withdrawn from Stabilizer reflux
drum is first washed with caustic and
then with water which is then sent to
storage.
Function of Tray in a Distillation
Naphtha Splitter
 The stabilized naphtha is further spit into light naphtha (50-110°c) and heavy
naphtha (110-180°c) in Spitter-I
 Splitter-I bottom is further split into reformer feed naphtha (110-150°c) and Kero-I
components.
 Reboiler heating media for Splitter-II is reduced crude oil from mail fractionator
column bottom.
THANK YOU

Presentation on Crude Distillation Unit (CDU)

  • 1.
    Industrial Training Presentation Topic-Crude Distillation Unit (CDU) Presented By- Priyam Jyoti Borah Roll no- 16/275 Department- Chemical
  • 2.
    Crude Oil Source 1. AssamCrude (Sulphur 0.3%) 2. Ravva Crude (Sulphur 0.1%) from the Ravva Oil fields of Andhra Pradesh) 3. Imported Crude (through Heldia and Miri Crude) higher then 0.5% Sulpher content
  • 3.
    CDU Unit consists ofthe following Sections  Crude Preheat  Desalter  Fired Heater  Crude Distillation Section  Stripper  Stabilizer  Naphtha Splitter  LPG Wash Section
  • 5.
    Crude Distillation andStrippers  Height of column: about 50m  Number of trays: 38-45  Feed from fired heater enters under try 5  Pressure is maintained at 1.3-1.8 kg/cm2.  Products-  Distillate  Bottom Products or residue to DCU
  • 6.
    Stabilizer  Column has30 trays  Top Temperature: 65°c  Top pressure: 10kg/cm2  The purpose of the stabilizer is to stabilize naphtha by separating out liquefied petroleum gas (LPG) and other C-4 components.  The fractionate of lower column or Kero II is used as heating medium for stabilizer reboiler.  LPG withdrawn from Stabilizer reflux drum is first washed with caustic and then with water which is then sent to storage.
  • 7.
    Function of Trayin a Distillation
  • 8.
    Naphtha Splitter  Thestabilized naphtha is further spit into light naphtha (50-110°c) and heavy naphtha (110-180°c) in Spitter-I  Splitter-I bottom is further split into reformer feed naphtha (110-150°c) and Kero-I components.  Reboiler heating media for Splitter-II is reduced crude oil from mail fractionator column bottom.
  • 9.