# US 8,771,549 B2 · Chemical looping combustion method and plant with independent solid circulation control > Agents: this data is available as JSON from the patentgrep API and MCP server — see https://patentgrep.com/llms.txt - Number: US 8,771,549 B2 - Document ID: US8771549B2 - Status: Granted - Kind: B2 - Application number: 13/383,890 - Filed: 2010-06-30 - Published: 2012-06-14 - Granted: 2014-07-08 - Earliest claimed: 2009-07-16 - Assignees: Ifp Energies Nouvelles; Total SA - Applicants: Thierry Gauthier; Ali Hoteit; Ann Forret - Inventors: Thierry Gauthier; Ali Hoteit; Ann Forret - Web page: https://patentgrep.com/patent/US8771549B2 ## CPC - F23C 99/00: Subject-matter not provided for in other groups of this subclass - C10J 3/721: {Multistage gasification, e.g. plural parallel or serial gasification stages} - C10J 3/723: {Controlling or regulating the gasification process} - C10J 3/725: {Redox processes} - C10J 2300/1606: Combustion processes - F23C 2900/99008: Unmixed combustion, i.e. without direct mixing of oxygen gas and fuel, but using the oxygen from a metal oxide, e.g. FeO - Y02E 20/34: Indirect CO2mitigation, i.e. by acting on non CO2directly related matters of the process, e.g. pre-heating or heat recovery - F23C: METHODS OR APPARATUS FOR COMBUSTION USING FLUID FUEL OR SOLID FUEL SUSPENDED IN {A CARRIER GAS OR} AIR (burners F23D) - C10J: PRODUCTION OF PRODUCER GAS, WATER-GAS, SYNTHESIS GAS FROM SOLID CARBONACEOUS MATERIAL, OR MIXTURES CONTAINING THESE GASES (synthesis gas from liquid or gaseous hydrocarbons C01B; underground gasification of minerals E21B43/295); CARBURETTING AIR OR OTHER GASES - Y02E: REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION ## Abstract The invention relates to an improved plant and method for chemical looping combustion of at least one hydrocarbon feed with independent control of the circulation of the solid active mass particles between the fluidized bed reaction zones, by means of one or more non-mechanical valves of L-valve type. ## Claims ### Claim 1 A chemical looping combustion method for at least one hydrocarbon feed in at least one distinct fluidized bed reduction reaction zone (i) and at least one distinct fluidized bed oxidation reaction zone (i+1), wherein the circulation of the solid particles of active mass between each or part of the reaction zones is controlled by means of one or more non-mechanical valves consisting each of a substantially vertical line portion, a substantially horizontal line portion and an elbow connecting the two portions, by transporting the solid particles between two successive reaction zones by: introducing solid particles coming from reaction zone (i) or (i+1) through the upper end of the substantially vertical line portion of said valve, injecting a control gas with a given aeration flow rate upstream from the elbow of said valve, controlling the differential pressure conditions at the terminals of the non-mechanical valve(s) so as to adjust the flow rate of the solid particles in the substantially horizontal line portion of said valve, according to the aeration flow rate, feeding into the successive reaction zones (i+1) or (i) of the loop the solid particles leaving the non-mechanical valve(s). ### Claim 2 (depends on 1) A chemical looping combustion method as claimed in claim 1, wherein each reaction zone consists of a set of one or more fluidized reactors arranged in relation to one another. ### Claim 3 (depends on 1) A chemical looping combustion method as claimed in claim 1, wherein at least two non-mechanical valves are arranged in parallel between two successive reaction zones (i) and (i+1). ### Claim 4 (depends on 1) A chemical looping combustion method as claimed in claim 1, comprising: additionally feeding between at least two successive reaction zones (i) and (i+1), and downstream from the non-mechanical valve(s), a carrier gas in an ascending transport line, said line being fed with the solid particles leaving the non-mechanical valve(s), carrying out transport of the solid particles from zone (i) to zone (i+1) through passage of the fluidized particles into the non-mechanical valve(s) located between zones (i) and (i+1), then through transport of the solid particles by means of at least one carrier gas injected into the ascending transport line, and separating the solid particles from the carrier gas by means of gas-solid separation means arranged at the outlet of the ascending line so as to supply zone (i+1) with solid particles, carrying out transport of the solid particles from the outlet of zone (i+1) to zone (i) through passage of the fluidized particles into the non-mechanical valve(s) located between zones (i+1) and (i), then through transport of the solid particles by means of at least one carrier gas injected into the ascending transport line, and separating the particles from the carrier gas by means of gas-solid separation means arranged at the outlet of the ascending line so as to supply zone (i) with solid particles. ### Claim 5 (depends on 1) A chemical looping combustion method as claimed in claim 1, wherein a reaction zone (i+1) is located at least partly above the previous reaction zone (i) and: the solid particles are transported from zone (i+1) to zone (i) by gravity flow by means of the non-mechanical valve(s) located between zones (i+1) and (i) transport of the solid particles from zone (i) to zone 9i+1)is performed by passage of the fluidized particles into the non-mechanical valve(s) located between zones (i) and (i+1), then by transport of the solid particles by means of at least one carrier gas injected into an ascending transport line, and the solid particles are separated from the carrier gas by means of gas-solid separation means arranged at the outlet of the ascending line so as to supply zone (i+1) with solid particles. ### Claim 6 (depends on 1) A chemical looping combustion method as claimed in claim 1, wherein circulation of the solids is controlled through servo-control of the aeration flow rate of the control gas of the non-mechanical valves by level measurements in the fluidized reactors and/or pressure drop measurements in the transport lines, performed in the reaction zones. ### Claim 7 (depends on 6) A chemical looping combustion method as claimed in claim 6, wherein the aeration flow rate of the control gas is controlled by a regulation valve servo-controlled by the level measurement in at least one fluidized bed of reduction reaction zone (i) and the aeration flow rate of the control gas is controlled by a regulation valve servo-controlled by the pressure drop measurement in the ascending transport line carrying the particles to the other reaction zone. ### Claim 8 (depends on 1) A method as claimed in claim 1, wherein a length of the horizontal portion of the non-mechanical valve(s) Lh is selected between 1 and 20 times the diameter of the horizontal line portion Dh. ### Claim 9 (depends on 1) A method as claimed in claim 1, wherein the diameter of the vertical line portion Dv is selected greater than or equal to the diameter of the horizontal line portion Dh of the non-mechanical valve(s). ### Claim 10 (depends on 9) A method as claimed in claim 9, wherein the diameter of the vertical line portion Dv and the diameter of the horizontal line portion Dh of the non-mechanical valve(s) are selected substantially identical. ### Claim 11 (depends on 1) A method as claimed in claim 1, wherein the control gas injection point upstream from the elbow is positioned at a distance x (difference between the height of the injection point in the vertical part and the lowest point of the non-mechanical valve) of the order of 1 to 5 times the diameter of the vertical line portion Dv. ### Claim 12 (depends on 1) A chemical looping combustion method as claimed in claim 1, wherein the solid active mass particles belong to group B of Geldart's classification. ### Claim 13 (depends on 1) A chemical looping combustion method as claimed in claim 1, wherein the solid active mass particles are metal oxides. ### Claim 14 (depends on 1) A chemical looping combustion method as claimed in claim 1, further comprising: exposing reduced solid particles of active mass to a material selected from the group consisting of hydrocarbon or water vapour for hydrogen production. ### Claim 15 (depends on 1) A chemical looping combustion method as claimed in claim 1, further comprising: partly oxidizing the hydrocarbon feed in the reduction reaction zone (i) to produce synthesis gas. ### Claim 16 (depends on 1) A chemical looping combustion method as claimed in claim 1, further comprising: recovering combustion heat from the zone selected from the group consisting of the oxidation reaction zone (i+1) and the reduction reaction zone (i).