Method and apparatus for efficient production of activated carbon
Abstract
This invention relates to a system for regenerating or manufacturing activated carbon wherein the exhaust gases and vapors from various sections of the furnace are supplied to other sections of the furnace in a recycling manner or are simultaneously cleaned and transformed into fuel gas. In a down-flow embodiment, the water vapor and calorific gasses generated in excess in the drying and devolatilization sections, respectively, are provided, either directly or through a combustion chamber, to the activation section. In an up-flow embodiment, heat from the activation section is recycled to the drying and devolatilization section and the down-flow brings the water vapor from the drying section and volatile material from the devolatilization section into the activation section where it can be effectively used.
Claims
exact text as granted — not AI-modified1 . A fuel gas cleaning and power generation method, comprising the steps of:
a. acquiring a gas from one or more exhausts of a furnace utilized in transforming a carbon source into activated carbon; b. heating the gas in a superheat chamber to a decomposition temperature sufficient to cause the condensable organics to decompose toward non-condensable organics; c. separating H 2 O from the gas; and d. combusting the gas to provide energy.
2 . The fuel gas cleaning and power generation method of claim 1 , further comprising the steps of:
a. mixing the gas with an oxygen source; and b. utilizing the combustion energy to turn the shaft of an electrical generator.
3 . The fuel gas cleaning and power generation method of claim 2 , further comprising the step of:
a. compressing the oxygen source and gas.
4 . The fuel gas cleaning and power generation method of claim 1 , further comprising the step of:
a. pre-heating the gas prior to the step of heating the gas in the superheat chamber.
5 . The fuel gas cleaning and power generation method of claim 1 , further comprising the step of:
a. removing particulate matter from the gas.
6 . The fuel gas cleaning and power generation method of claim 1 , wherein the step of separating H 2 O from the gas includes a condenser and liquid gas separator.
7 . The fuel gas cleaning and power generation method of claim 1 , wherein the non-condensable organics are ethane and methane.
8 . A method of transforming exhaust from a furnace being utilized to manufacture activated carbon, the exhaust being a gas containing condensable organics and water vapor, into fuel gas and electrical energy, comprising the steps of:
a. venting the gas from the furnace; b. heating the gas to a temperature sufficient to cause the condensable organics to decompose toward non-condensable organics; c. separating H 2 O from the gas; d. compressing the gas; e. mixing the gas with an oxygen source; f. combusting the gas and oxygen mixture; and g. utilizing the combustion energy to turn the shaft of an electrical generator.
9 . The method of claim 8 , further comprising the step of:
a. pre-heating the gas prior to the step of heating the gas.
10 . The method of claim 8 , further comprising the step of:
a. removing particulate matter from the gas.
11 . The method of claim 8 , wherein the step of separating H 2 O from the gas includes a condenser and liquid gas separator.
12 . The method of claim 8 , wherein the oxygen source is compressed atmospheric air.
13 . The method of claim 8 , wherein the non-condensable organics are ethane and methane.
14 . A method for recycling and reusing a stream of exhaust gas from a furnace producing activated carbon comprising the steps of heating the exhaust gas to a temperature at which condensable organics are eliminated and non-condensable organics are created, removing water vapor from the exhaust gas, compressing the exhaust gas, mixing the exhaust gas with a source of oxygen, utilizing the exhaust gas/oxygen source mixture as fuel for a gas turbine and generating power with the gas turbine.
15 . The method of claim 14 , further comprising the step of pre-heating the exhaust gas prior to the step of heating the exhaust gas.
16 . The method of claim 15 , further wherein the pre-heating step utilizes extraneous heat contained in the exhaust gas subsequent to the heating step.
17 . The method of claim 14 , wherein the step of removing water vapor from the gas includes a condenser and liquid gas separator.
18 . The method of claim 14 , wherein the oxygen source is compressed atmospheric air.
19 . The method of claim 14 , wherein the non-condensable organics are ethane and methane.Join the waitlist — get patent alerts
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