Method for increasing gas oil yield and energy efficiency in crude oil distillation

• US 9,546,324 B2
• Filed: 11/03/2014
• Issued: 01/17/2017
• Est. Priority Date: 11/01/2013
• Status: Active Grant

• Current Assignee: Council of Scientific & Industrial Research
• Original Assignee: Council of Scientific & Industrial Research
• Inventors: Kumar, Sunil, Madhusudan, Nanoti Shrikant, Onkarnath, Garg Madhukar
• Primary Examiner(s): Stein, Michelle
• Application Number:
  US14/531,276
• Publication Number:
  US 20150122704A1
• Time in Patent Office: 806 Days
• US Class Current: 1/1
• CPC Class Codes: C10G 7/00 Distillation of hydrocarbon oils

Abstract

A method for significant increase in gas oil yield and energy efficiency in crude oil distillation is provided. The present invention relates to a method of separating the components of crude oil. This method utilizes the innovative and novel application of lighter fraction of crude through its superheating and its injection in the stripping section consisting of bottom to flash zone of main distillation column. Method also illustrates the innovative utilization of water in crude distillation unit to eliminate the bottom striping steam and for significant energy saving.

Claims

1. A method for increasing gas oil yield and energy efficiency in crude oil distillation, the method comprising the steps of:

a. separating a lighter fraction vapor and a liquid fraction from a desalted crude oil by passing the desalted crude oil through one or more flash drums;

b. superheating the lighter fraction vapor by passing the lighter fraction vapor through a first furnace to obtain a superheated lighter fraction;

c. injecting the superheated lighter fraction vapor into a distillation column having a plurality of trays, the superheated lighter fraction vapor injected either at a bottom of the distillation column or at a stripping section located between a flash zone and the bottom of the distillation column;

d. heating the liquid fraction in a second furnace to obtain a heated liquid fraction and feeding the heated liquid fraction to the flash zone of the distillation column; and

e. distilling the superheated lighter fraction and the liquid fraction and passing the distillates to side strippers from different trays of the plurality of trays of the distillation column, to obtain lighter products and residue.

2. The method as claimed in claim 1, wherein the lighter fraction of crude is mixed with steam before feeding to the first furnace.

3. The method as claimed in claim 1, wherein the one or more flash drums includes a first flash drum and a second flash drum, and passing desalted crude oil through one or more flash drums comprises:

passing the desalted crude oil through the first flash drum to separate a first lighter fraction and a first liquid fraction.

4. The method as claimed in claim 3 further comprising:

passing the first liquid fraction through the second flash drum to separate a second lighter fraction and a second liquid fraction; and

combining the first and second lighter fractions downstream of the second flash drum and upstream of the distillation column.

5. The method as claimed in claim 1, wherein the heat from the distillation column is removed by one or more pump-rounds and at least one condenser connected to the distillation column.

6. The method as claimed in claim 1, wherein the lighter fraction vapor of crude is preheated in a heat exchanger before the lighter fraction vapor is fed to the first furnace.

7. The method as claimed in claim 1, wherein the liquid fraction of crude is preheated (280-320°

C.) in a heat exchanger before the liquid fraction is fed to the second furnace.

8. The method as claimed in claim 1, wherein the desalted crude is entering the one or more flash drums in a temperature range of 180-260°

C.

9. The method as claimed in claim 1 further comprising:

adding water to the desalted crude upstream of the one or more flash drums and downstream of a desalter, wherein the water is added in a range of 2000-6000 kg/hr.

10. The method of claim 1 further comprising:

feeding steam through the bottom of the distillation column in a range of 0-10000 kg/h.