High productivity thermo energy simplified bio-cokes furnace and method for producing high carbon charcoal
Abstract
A process and a business method for converting wood waste to charcoal have been invented. Multiple high productive thermo energy simplified bio-cokes furnaces create an outlet discharging the earned volatile gas and the wood tar from the carbonization device. By taking back the gas and the wood tar mixed with the air into the furnace, the present invention produces evenly distributed heat with higher energy productivity. The present invention adopts different Coefficients of Thermal Expansion (CTE) for the top opening zone and the carbonization chamber, to avoid transmittal of oxygen from outside the furnace. Charcoal produced with a reduced energy use by the present invention can replace bio-cokes produced from general waste incineration. Through the creation of higher carbon charcoal, the present invention introduces a source of environment-friendly, cost effective and sustainable heat use. Accordingly, the present invention proposes promising business models both to the suppliers and the consumers.
Claims
exact text as granted — not AI-modifiedI claim:
1 . A bio-coke furnace comprising:
a carbonization chamber formed with an opening sized to receive cellulose waste; a top sized to seal said carbonization chamber; a combustion chamber within said carbonization chamber and having a volatile gas burner; a guide pipe passing from the atmosphere to said carbonization chamber; a first valve along said guide pipe configured to selectively interrupt passage of gasses therethrough; a flue extending from said combustion chamber and in gaseous communication with an adjacent furnace; and a second valve along said flue configured to selectively interrupt passage of combustion gasses therethrough.
2 . The bio-coke furnace of claim 1 , further comprising a tuyere configured to supply combustion gas to said combustion chamber during combustion.
3 . The bio-coke furnace of claim 1 , further comprising said carbonization chamber having an outer surface; and
an insulation later covering said outer surface of said carbonization chamber.
4 . The bio-coke furnace of claim 3 , wherein said insulation layer further comprises firebricks and rock wool double insulators to improve the heat insulating effect.
5 . The bio-coke furnace of claim 1 wherein said top further comprises a dome-shaped top.
6 . The bio-coke furnace of claim 5 , wherein said top is made from fireproof bricks.
7 . The bio-coke furnace of claim 1 , wherein said first valve is reversible and configurable to transmit volatile gas to any adjacent furnace.
8 . The bio-coke furnace of claim 1 , wherein said second valve is reversible and configurable to transmit volatile gas to any adjacent furnace.
9 . The bio-coke furnace of claim 1 , wherein said flue is insulated.
10 . The bio-coke furnace of claim 1 , wherein said guide pipe is insulated.
11 . The bio-coke furnace of claim 1 , wherein said gas burner within said combustion chamber is configured to receive volatile gasses from an adjacent furnace.
12 . A bio-coke furnace assembly, comprising:
six furnaces, each of said six furnaces comprising:
a carbonization chamber formed with an opening sized to receive cellulose waste; a top sized to seal said carbonization chamber; a combustion chamber within said carbonization chamber and having a volatile gas burner; a guide pipe in gaseous communication with said carbonization chamber; a first valve along said guide pipe configured to selectively interrupt passage of gasses therethrough; a flue extending from said combustion chamber; and a second valve along said flue configured to selectively interrupt passage of combustion gasses therethrough;
wherein the carbonization chamber of each said furnace is in gaseous communication with the carbonization chamber of at least one adjacent furnace through said guide pipe; wherein the combustion chamber of each said furnace is in gaseous communication with the combustion chamber of at least one adjacent furnace through said flue; and wherein said first valve and said second valve are configurable to control the flow of gasses between adjacent furnaces.
13 . The bio-coke furnace of claim 12 , further comprising a tuyere configured to supply combustion gas to said combustion chamber during combustion.
14 . The bio-coke furnace of claim 12 further comprising said carbonization chamber having an outer surface; and
an insulation later covering said outer surface of said carbonization chamber.
15 . The bio-coke furnace of claim 14 , wherein said insulation layer further comprises firebricks and rock wool double insulators to improve the heat insulating effect.
16 . The bio-coke furnace of claim 12 wherein said top further comprises a dome-shaped top.
17 . A method of creating high carbon coal, comprising the steps of:
providing a first furnace, said furnace having a carbonization chamber having a top, a combustion chamber, a guide pipe having a first valve and a flue having a second valve; loading said carbonization chamber with cellulose waste; applying heat to said carbonization chamber to initiate the heating of the carbonization chamber to a required temperature; opening said first valve and said second valves to facilitate carbonization; monitoring the temperature within said carbonization chamber until said temperature reaches a carbonization temperature generating volatile gasses; closing said first valve and said second valve; waiting for carbonization to occur; and cooling said carbonization chamber.
18 . The method of claim 17 , further comprising removing said high carbon charcoal from said chamber.
19 . The method of claim 18 , further comprising:
refilling said combustion chamber with cellulose waste; and initiating another carbonization cycle.
20 . The method of claim 17 , further comprising:
Providing multiple furnaces, each said furnace of said multiple furnaces in gaseous communication with at least one other adjacent furnace; initiating carbonization in said first furnace; transmitting volatile gasses from said first furnace to an adjacent furnace once said first furnace reaches a carbonization temperature; and initiating carbonization in an adjacent furnace to said first furnace.Join the waitlist — get patent alerts
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