Process for production of high quality syngas through regeneration of coked upgradation agent

Patent metadata

Field	Value
Publication number	US-10526202-B2
Application number	US-201615240425-A
Country	US
Kind code	B2
Filing date	Aug 18, 2016
Priority date	Nov 9, 2015
Publication date	Jan 7, 2020
Grant date	Jan 7, 2020

Abstract

The present invention relates to a process for the production of high quality synthesis gas rich in hydrogen during the process of upgrading the residual hydrocarbon oil feedstock by rejuvenating the spent upgrading material in Reformer in absence of air/oxygen without supplying external heat source other than the heat generated inside the process during combustion of residual coke deposited on the upgrading material. The present invention further relates to the apparatus used for preparation of syngas wherein said syngas thus produced is used for production of hydrogen gas. Furthermore, the present invention also provides system and method for preparing pure hydrogen from syngas.

First claim

The invention claimed is:

1. A process for producing syngas rich in hydrogen, during the process of upgrading residual hydrocarbon oil feedstock, the process, consisting of partially regenerating spent upgrading agent, obtained from a Riser, in a Reformer with steam and in presence of an organo-metallic additive wherein the metal of the organo-metallic additive is selected from alkali metals, alkaline earth metals or transition metals and in absence of oxygen containing gases to obtain syngas rich in hydrogen, wherein the spent upgrading agent constitutes 1 to 5 wt % coke, and the Reformer is maintained at a temperature of 650 to 850° C. without supplying external heat;
wherein the upgrading agent is selected from the group consisting of alumina, silica alumina, kaolin clay and mixtures thereof;
further wherein:
optionally, the temperature of the Reformer is maintained by circulating a rejuvenated upgrading agent from a Combustor to the Reformer;
optionally, introducing partially rejuvenated upgrading agent from the Reformer, to the Combustor and burning the partially rejuvenated upgrading agent at a temperature in the range of 750° C. to 950° C. and in presence of a stream of oxygen containing gases in the Combustor to obtain rejuvenated upgrading agent and flue gas;
optionally, introducing the rejuvenated upgrading agent from the Combustor to the Reformer;
optionally, introducing a stream of hydrocarbon lean in sulfur and nitrogen impurities into the Combustor while burning the partially rejuvenated upgrading agent;
optionally, combining the rejuvenated upgrading agent from the Combustor and the spent upgrading agent from the Riser, in a Mixer, prior to introducing to the Reformer wherein the Mixer is placed either outside the Reformer or forms a part of the Reformer; and
optionally, wherein the spent upgrading agent is separated from the cracked products obtained from the Riser, in a Stripper, prior to introducing to the Reformer.

2. The process of claim 1 , wherein the temperature of the Reformer is maintained by circulating a rejuvenated upgrading agent from a Combustor to the Reformer.

3. The process of claim 1 , wherein the process includes introducing partially rejuvenated upgrading agent from the Reformer, to the Combustor and burning the partially rejuvenated upgrading agent at a temperature in the range of 750° C. to 950° C. and in presence of a stream of oxygen containing gases in the Combustor to obtain rejuvenated upgrading agent and flue gas.

4. The process of claim 3 , wherein the process includes introducing the rejuvenated upgrading agent from the Combustor to the Reformer.

5. The process of claim 3 , wherein the process includes introducing a stream of hydrocarbon lean in sulfur and nitrogen impurities into the Combustor while burning the partially rejuvenated upgrading agent.

6. The process of claim 3 , wherein the process includes combining the rejuvenated upgrading agent from the Combustor and the spent upgrading agent from the Riser, in a Mixer, prior to introducing to the Reformer wherein the Mixer is placed either outside the Reformer or forms the part of the Reformer.

7. The process of claim 1 , wherein the spent upgrading agent is separated from the cracked products obtained from the Riser, in a Stripper, prior to introducing to the Reformer.

Assignees

• Indian Oil Corp Ltd

Inventors

• Mukthiyar Sadhullah
• Bhanuprasad Sayapaneni Gopinath
• Saidulu Gadari
• Dalai Eswar Prasad
• Singh Sanjeev
• Kumaran Satheesh Vetterkunnel
• Bhattacharyya Debasis
• Kumar Brijesh
• Das Biswapriya

Classifications

• C01B3/28 Primary

  using moving solid particles, e.g. fluidised bed technique · CPC title

• B01J8/0015

  Feeding of the particles in the reactor; Evacuation of the particles out of the reactor · CPC title

• C10G2300/70

  Catalyst aspects · CPC title

• C01B2203/045

  Purification by catalytic desulfurisation · CPC title

• C10G11/00

  Catalytic cracking, in the absence of hydrogen, of hydrocarbon oils (cracking in direct contact with molten metals or salts C10G9/34) · CPC title