Delayed coking process

Patent metadata

Field	Value
Publication number	US-9840671-B2
Application number	US-201414549525-A
Country	US
Kind code	B2
Filing date	Nov 20, 2014
Priority date	Nov 23, 2013
Publication date	Dec 12, 2017
Grant date	Dec 12, 2017

Abstract

The present invention provides a delayed coking process comprising a step of subjecting a mixed feed comprises residual heavy hydrocarbon feedstock and bio oil obtained from fast pyrolysis of lignocellulosic biomass of one or more of Jatropha, Cashew nut, Karanjia and Neem to a delayed coking process and a system for the delayed coking process.

First claim

We claim:

1. A delayed coking process comprising a step of subjecting a mixed feed comprising residual heavy hydrocarbon feedstock and bio oil obtained from fast pyrolysis of lignocellulosic biomass of one or more of Jatropha, Cashew nut, Karanjia and Neem to the delayed coking process,
wherein the residual heavy hydrocarbon feedstock has Conradson carbon residue content of 22 to 27 wt % and the bio oil has Conradson carbon residue content of 7 to 10 wt %, wherein the mixed feed comprises 97 to 85 wt % of the residual heavy hydrocarbon feedstock and 3 to 15 wt % of the bio oil.

2. The process as claimed in claim 1 , wherein the residual heavy hydrocarbon feedstock has boiling point in the range of 400° to 700° C.

3. The process as claimed in claim 1 , wherein the bio oil has boiling point in the boiling range of about 200° to 620° C.

4. The process as claimed in claim 1 , wherein the lignocellulosic biomass are selected from the group consisting of roots, stems, leaves and seeds or combination thereof.

5. The process as claimed in claim 1 , wherein the mixed feed is obtained by:
(a) mixing residual heavy hydrocarbon feedstock and bio oil to obtain a mixture;
(b) feeding the mixture thus obtained in step (a) to a bottom of a fractionator along with a condensed recycle oil; and
(c) withdrawing the mixed feed from the bottom of the fractionator.

6. The process as claimed in claim 1 , wherein the mixed feed is obtained by:
(a) feeding the residual heavy hydrocarbon feedstock to a bottom of a fractionator along with a condensed recycle oil;
(b) withdrawing a bottom fraction from the bottom of the fractionator; and
(c) mixing bio oil with the bottom fraction thus obtained in step (b) to obtain the mixed feed.

7. The process as claimed in claim 1 , wherein the mixed feed is heated to a coking temperature prior to subjecting the same to delayed coking process.

8. The process as claimed in claim 7 , wherein the coking temperature is in the range of 475° to 510° C.

9. The process as claimed in claim 1 , wherein the delayed coking process comprises:
(a) feeding the mixed feed to a coker drum and providing residence time for allowing thermal cracking of the mixed feed under coking conditions;
(b) withdrawing vapours from the coker drum and adding a quench media to the vapours thus withdrawn to obtain effluent vapours;
(c) transporting the effluent vapours thus obtained to a fractionator for separation into various products according to desired boiling ranges.

10. The process as claimed in claim 9 , wherein the residence time is in the range of 12 to 38 hours.

Assignees

• Indian Oil Corp Ltd

Inventors

• Thakur Ram Mohan
• Arora Ajay Kumar
• Devi Prasad Terapalli Hari Venkata
• Ramachandran Pradeep Ponoly
• Dixit Jagdev Kumar
• Rajesh
• Bhattacharyya Debasis
• Puri Suresh Kumar
• Kumar Brijesh
• Rajagopal Santanam
• Malhotra Ravinder Kumar

Classifications

• Y02P20/145

  the feedstock being materials of biological origin · CPC title

• Y02P30/20

  using bio-feedstock · CPC title

• C10G2300/1077

  Vacuum residues · CPC title

• C10G2300/107

  Atmospheric residues having a boiling point of at least about 538 °C · CPC title

• C10G9/005 Primary

  Coking (in order to produce liquid products mainly) · CPC title