Method and plant for redox chemical looping combustion of a solid hydrocarbon feedstock

Patent metadata

Field	Value
Publication number	US-10215400-B2
Application number	US-201414897866-A
Country	US
Kind code	B2
Filing date	Jun 12, 2014
Priority date	Jun 13, 2013
Publication date	Feb 26, 2019
Grant date	Feb 26, 2019

Abstract

The invention relates to a method and to a device for chemical looping combustion CLC of a solid hydrocarbon feed wherein it is proposed to inject the solid hydrocarbon feed so as to limit any occurrence of sticking of the feed to the walls of the injection device. The solid feed is fed into a conveying zone operating under fluidized bed conditions and opening into a combustion reactor. A fluidization gas is injected into this conveying zone while controlling the flow of gas in such a way that the superficial velocity of the gas in the conveying zone is higher than the terminal velocity of the solid hydrocarbon feed particles and the terminal velocity of solid particles present in the combustion reactor, and while controlling the fluidization gas temperature in such a way that the temperature in the conveying zone is less than or equal to 500° C.

First claim

The invention claimed is:

1. A method for combustion of a solid hydrocarbon feed by oxidation-reduction in a chemical loop wherein a redox active mass circulates in particle form, comprising:
feeding the solid hydrocarbon feed in particle form into a conveying zone operating under fluidized bed conditions and opening into a combustion reactor,
injecting into the conveying zone a first fluidization gas so as to create a dilute phase of the fluidized bed, while controlling the rate of flow of the first fluidization gas in such a way that the superficial velocity of the gas in the conveying zone is higher than the terminal velocity of the solid hydrocarbon feed particles and the terminal velocity of solid particles present in the combustion reactor, and while controlling the temperature of the first gas in such a way that the temperature in the dilute phase of the conveying zone is less than or equal to 500° C.,
carrying out combustion of the solid hydrocarbon feed from the conveying zone through contact with the redox active mass within the fluidized-bed combustion reactor,
extracting from the combustion reactor a mixture comprising particles of the redox active mass and bottom ash through an extraction line arranged in the bottom of the combustion reactor,
feeding the mixture with a controlled flow rate into a separation zone comprising a lower part of said conveying zone, arranged below an upper part of the conveying zone into which the solid hydrocarbon feed is fed,
injecting a second fluidization gas into the separation zone, the injection being performed by controlling the flow rate of the second fluidization gas:
so as to separate by elutriation the redox active mass particles and the bottom ash agglomerated within the mixture, said the particles of the redox active mass being then conveyed to the combustion reactor and the bottom ash agglomerated within the mixture falling under the effect of gravity to the bottom of the separation zone where it is discharged, and
so that the velocity of the gas from the mixture of first fluidization gas and second fluidization gas in the upper part of the conveying zone is higher than the terminal velocity of the solid hydrocarbon feed particles and the terminal velocity of the solid particles present in said combustion reactor,

and said injection is performed by controlling also the temperature of the second fluidization gas in such a way that the temperature of the conveying zone is less than or equal to 500° C.

2. The method as claimed in claim 1 , wherein the superficial gas velocity in the dilute phase of the conveying zone ranges between 2 m/s and 50 m/s.

3. The method as claimed in claim 1 , wherein the solid hydrocarbon feed in particle form is fed into the conveying zone through gravity flow by means of a gravity flow pipe, and the solid hydrocarbon feed flow is controlled through regulation and sealing means arranged between the gravity flow pipe and a buffer zone for temporary storage of the solid hydrocarbon feed in particle form.

4. The method as claimed in claim 1 , wherein the solid hydrocarbon feed in particle form is fed into the conveying zone by means of an endless screw, the endless screw being supplied by a gravity flow of solid feed coming from a buffer zone for temporary storage of the solid hydrocarbon feed in particle form, and the solid hydrocarbon feed flow is controlled through regulation and sealing means arranged between the endless screw and the buffer zone.

5. The method as claimed in claim 1 , wherein the solid hydrocarbon feed in particle form is fed into the conveying zone by means of a dense pneumatic conveying line, the dense pneumatic conveying line being supplied by a gravity flow of solid feed coming from a buffer zone for temporary storage of the solid hydrocarbon feed in particle form and by a carrier gas, and the solid hydrocarbon feed flow is controlled through regulation and sealing means arranged between the dense pneumatic conveying line and the buffer zone.

6. The method as claimed in claim 1 , wherein a raw solid hydrocarbon feed is sent from a storage zone to a mill so as to shape the hydrocarbon feed in particle form, the flow of the raw solid hydrocarbon feed being controlled by regulation and sealing means arranged between the mill and the storage zone, then the hydrocarbon feed in particle form is fed into conveying zone by means of a pipe supplied from the mill into which a carrier gas is sent for carrying the feed into the pipe.

7. The method as claimed in claim 1 , wherein the conveying zone is a substantially vertical pipe.

8. The method as claimed in claim 1 , wherein the redox active mass reduced in the combustion reactor is reoxidized in an oxidation reactor prior to being again contacted with the solid hydrocarbon feed in the combustion reactor.

9. The method as claimed in claim 1 , wherein the solid hydrocarbon feed is selected from among coal, coke, pet coke, biomass, bituminous sands and household, agricultural or industrial waste.

10. A plant for chemical looping redox combustion of a solid hydrocarbon feed by oxidation-reduction in a chemical loop wherein a redox active mass circulates in particle form, comprising a combustion reactor and an oxidation reactor, the combustion reactor comprising:
a supply means for the redox active mass in particle form coming from the oxidation reactor,
a third fluidization gas supply means,
a supply means for a solid hydrocarbon feedstock in particle form, the solid hydrocarbon feedstock supply means comprising:
a conveying zone operating under fluidized bed conditions for conveying the solid hydrocarbon feed to the combustion reactor, the conveying zone having a temperature less than or equal to 500° C.,
means for injecting the solid hydrocarbon feed in particle form into the conveying zone, and
means for injecting a first fluidization gas into the conveying zone, and the oxidation reactor comprising:
a supply means for the redox active mass particles reduced in the combustion reactor,
an oxidizing gas supply means,
a discharge means for the oxidizing gas reduced after oxidation of the redox active mass, and

a discharge means for sending the reoxidized redox active mass particles to the combustion reactor,
a pipe for extracting a mixture comprising redox active mass particles and agglomerated bottom ash contained in the combustion reactor, the extraction pipe being positioned in the bottom of the reactor,
a separation zone comprising a lower part of the conveying zone, for separation by elutriation of the particles of the mixture coming from the extraction pipe, the separation zone comprising:
a supply means for the mixture coming from the extraction pipe, the supply means comprising means of controlling the flow rate of the mixture fed into the separation zone,
means for injecting a second fluidization gas,
a dilute phase zone of the fluidized bed in the upper part of the separation zone, and
an agglomerated bottom ash discharge means arranged in the lower part of the separation zone.

11. A combustion plant as claimed in claim 10 , wherein the means for injecting the solid hydrocarbon feed into the conveying zone comprise a gravity flow pipe opening into the conveying zone, the pipe being supplied by a buffer zone via regulation and sealing means allowing the solid feed flow to be controlled.

12. A combustion plant as claimed in claim 10 , wherein the means for injecting the solid hydrocarbon feed into the conveying zone comprise an endless screw opening into the conveying zone, the endless screw being supplied by a buffer zone via regulation and sealing means allowing the solid feed flow to be controlled.

Assignees

• Ifp Energies Now
• Total Raffinage Chimie

Inventors

• Guillou Florent
• Sozinho Tiago
• Dreux Heloise
• Stainton Helene

Classifications

• F23C10/28

  Control devices specially adapted for fluidised bed, combustion apparatus · CPC title

• F23C10/22

  Fuel feeders specially adapted for fluidised bed combustion apparatus (F23C10/26 takes precedence) · CPC title

• F23C10/04

  the particles being circulated to a section, e.g. a heat-exchange section or a return duct, at least partially shielded from the combustion zone, before being reintroduced into the combustion zone · CPC title

• F23C10/005 Primary

  comprising two or more beds · CPC title

• F23D1/00

  Burners for combustion of pulverulent fuel · CPC title