Patent classifications
F23K2201/1003
Process for producing solid biomass fuel
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
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
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
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
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.