F23K2201/1003

Process for producing solid biomass fuel
11624037 · 2023-04-11 ·

The present invention relates to a process for producing a solid biomass fuel from agricultural waste such as grass, rice husk, yam, straw, corn cob or any combination thereof, as well as a solid biomass fuel produced by said process. Additionally, the present invention relates to a combustion process comprising combusting said solid biomass fuel so as to produce energy and a pre-treatment process for pre-treating one or more sources of biomass for use in the production of a solid biomass fuel.

SYSTEM, METHOD AND APPARATUS FOR CONTROLLING THE FLOW DISTRIBUTION OF SOLID PARTICLES

A deflector ring includes a generally annular body, and a plurality of static straightening vanes arranged interior to the body, the vanes dividing the body into a plurality of substantially equal sections. The vanes are configured to straighten a swirling flow of solid particles as they enter the annular body, and to divide the swirling flow into a plurality of straightened flows that are communicated to a turret positionable above the deflector ring.

PROCESS FOR PRODUCING SOLID BIOMASS FUEL
20220033727 · 2022-02-03 ·

The present invention relates to a process for producing a solid biomass fuel from agricultural waste such as grass, rice husk, yam, straw, corn cob or any combination thereof, as well as a solid biomass fuel produced by said process. Additionally, the present invention relates to a combustion process comprising combusting said solid biomass fuel so as to produce energy and a pre-treatment process for pre-treating one or more sources of biomass for use in the production of a solid biomass fuel.

PROCESSES AND SYSTEMS FOR PRODUCING BIOCOKE IN A KINETIC INTERFACE REACTOR, AND BIOCOKE PRODUCED THEREFROM
20230323230 · 2023-10-12 ·

A process for producing biocoke is provided, comprising: providing a heated biogas stream comprising carbon-containing vapors; providing a kinetic interface media, in solid form; introducing the kinetic interface media and the heated biogas stream to a kinetic interface reactor, operated to convert at least some of the carbon-containing vapors to biocoke; removing the solid biocoke-containing kinetic interface media from the kinetic interface reactor; and recovering the solid biocoke-containing kinetic interface media. Other variations provide a process for producing biocoke, comprising: providing a bioliquid stream comprising carbon-containing liquids; providing a kinetic interface media, in solid form; introducing the kinetic interface media and the bioliquid stream to a kinetic interface reactor, operated to convert at least some of the carbon-containing liquids to biocoke; removing the solid biocoke-containing kinetic interface media from the kinetic interface reactor; and recovering the solid biocoke-containing kinetic interface media. Many embodiments are described.

PROCESSES AND SYSTEMS FOR PRODUCING BIOCOKE IN A KINETIC INTERFACE REACTOR, AND BIOCOKE PRODUCED THEREFROM
20230323229 · 2023-10-12 ·

A process for producing biocoke is provided, comprising: providing a heated biogas stream comprising carbon-containing vapors; providing a kinetic interface media, in solid form; introducing the kinetic interface media and the heated biogas stream to a kinetic interface reactor, operated to convert at least some of the carbon-containing vapors to biocoke; removing the solid biocoke-containing kinetic interface media from the kinetic interface reactor; and recovering the solid biocoke-containing kinetic interface media. Other variations provide a process for producing biocoke, comprising: providing a bioliquid stream comprising carbon-containing liquids; providing a kinetic interface media, in solid form; introducing the kinetic interface media and the bioliquid stream to a kinetic interface reactor, operated to convert at least some of the carbon-containing liquids to biocoke; removing the solid biocoke-containing kinetic interface media from the kinetic interface reactor; and recovering the solid biocoke-containing kinetic interface media. Many embodiments are described.

Pulverizing device, throat for pulverizing device, and pulverized-coal fired boiler

A pulverizing device includes: a housing; a pulverization table configured to rotate inside the housing; and a throat, disposed inside the housing on a radially outer side of the pulverization table, for forming an upward air flow. The throat includes: an inner ring extending along an outer periphery of the pulverization table; an outer ring, disposed on a radially outer side of the inner ring so as to form an annular flow passage between the inner ring and the outer ring; and a plurality of throat vanes disposed between the inner ring and the outer ring. The following expressions are satisfied: 2.0≤L/d≤4.0; and 0.5≤H/d≤1.5, where H is a gap between the inner ring and the outer ring with respect to a radial direction, L is a length of the throat vanes, and ‘d’ is a distance between adjacent two of the throat vanes.

System, method and apparatus for controlling the flow distribution of solid particles

A deflector ring includes a generally annular body, and a plurality of static straightening vanes arranged interior to the body, the vanes dividing the body into a plurality of substantially equal sections. The vanes are configured to straighten a swirling flow of solid particles as they enter the annular body, and to divide the swirling flow into a plurality of straightened flows that are communicated to a turret positionable above the deflector ring.

PULVERIZING DEVICE, THROAT FOR PULVERIZING DEVICE, AND PULVERIZED-COAL FIRED BOILER

A pulverizing device includes: a housing; a pulverization table configured to rotate inside the housing; and a throat, disposed inside the housing on a radially outer side of the pulverization table, for forming an upward air flow. The throat includes: an inner ring extending along an outer periphery of the pulverization table; an outer ring, disposed on a radially outer side of the inner ring so as to form an annular flow passage between the inner ring and the outer ring; and a plurality of throat vanes disposed between the inner ring and the outer ring. The following expressions are satisfied: 2.0L/d4.0; and 0.5H/d1.5, where H is a gap between the inner ring and the outer ring with respect to a radial direction, L is a length of the throat vanes, and d is a distance between adjacent two of the throat vanes,

Pulverized fuel supply method for oxyfuel combustion boiler, and oxyfuel combustion boiler system
10024535 · 2018-07-17 · ·

In an oxyfuel combustion boiler system, nitrogen gas separated by an air separation unit (ASU) is supplied as carrier gas to a pulverizer for drying and pulverization of fuel. A fluid mixture of the nitrogen gas from the pulverizer with pulverized fuel is supplied to a powder separation device where the pulverized fuel is separated. The separated pulverized fuel is mixed with the primary recirculated flue gas and supplied to a burner.