Use of manganese oxide and activated carbon fibers for removing a particle, volatile organic compound or ozone from a gas
US-9427728-B2 · Aug 30, 2016 · US
US11338243B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11338243-B2 |
| Application number | US-201916394568-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 25, 2019 |
| Priority date | Apr 27, 2018 |
| Publication date | May 24, 2022 |
| Grant date | May 24, 2022 |
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Methods and apparatus to thermally destruct volatile organic compounds are disclosed. An example thermal oxidizer for a furnace includes: an oxidation chamber comprising an inlet configured to receive exhaust gases from a furnace and an outlet configured to output resultant gases; and a plurality of heating elements within the oxidation chamber configured to heat the exhaust gases to oxidize one or more components of the exhaust gases between the inlet and the outlet to result in the resultant gases, the plurality of heating elements comprising resistive heating elements forming coils having respective axes, the plurality of heating elements being oriented within the oxidation chamber such that the axes of the coils are transverse to an exhaust gas flow direction from the inlet to the outlet of the oxidation chamber.
Opening claim text (preview).
What is claimed is: 1. A thermal oxidizer for a furnace, the thermal oxidizer comprising: an oxidation chamber comprising an inlet configured to receive exhaust gases from a furnace and an outlet configured to output resultant gases; and a plurality of heating elements within the oxidation chamber configured to heat the exhaust gases to oxidize one or more components of the exhaust gases between the inlet and the outlet to result in the resultant gases, the plurality of heating elements comprising resistive heating elements forming coils having respective axes, the plurality of heating elements being oriented within the oxidation chamber such that the axes of the coils are transverse to an exhaust gas flow direction from the inlet to the outlet of the oxidation chamber. 2. The thermal oxidizer of claim 1 , wherein the plurality of heating elements are configured to partially obstruct multiple cross-sections of the oxidation chamber. 3. The thermal oxidizer of claim 1 , wherein the plurality of heating elements are configured to create a tortuous path from the inlet to the outlet for flow of the exhaust gases. 4. The thermal oxidizer of claim 3 , wherein the plurality of heating elements are configured to create the tortuous path from the inlet to the outlet without the use of baffling. 5. The thermal oxidizer of claim 1 , wherein the plurality of heating elements are configured to heat the exhaust gases to a temperature sufficient to oxidize the one or more components of the exhaust gases without the use of a catalyst. 6. The thermal oxidizer of claim 5 , wherein the plurality of heating elements are configured to heat the oxidation chamber to at least 700° Celsius and to provide a dwell time for the exhaust gases of at least 0.2 seconds within the oxidation chamber. 7. The thermal oxidizer of claim 1 , wherein the plurality of heating elements comprise cores, in which the coils are wrapped around the respective cores. 8. The thermal oxidizer of claim 7 , wherein the cores comprise at least one of ceramic, galvanized steel, stainless steel, or brass. 9. The thermal oxidizer of claim 1 , further comprising a temperature sensor configured to measure a temperature of at least one of the exhaust gas or the resultant gas, and a controller configured to control at least one of a power applied to the plurality of heating elements or an airflow speed of the exhaust gas. 10. A firing furnace for solar cell production, the firing furnace comprising: a heating chamber configured to fire solar cells within the heating chamber; and a thermal oxidizer configured to receive exhaust gases from the furnace, the thermal oxidizer comprising: an oxidation chamber comprising an inlet configured to receive exhaust gases from a furnace and an outlet configured to output resultant gases; and a plurality of heating elements within the oxidation chamber configured to heat the exhaust gases to oxidize one or more components of the exhaust gases between the inlet and the outlet to result in the resultant gases, the plurality of heating elements comprising resistive heating elements forming coils having respective axes, the plurality of heating elements being oriented within the oxidation chamber such that the axes of the coils are transverse to an exhaust gas flow direction from the inlet to the outlet of the oxidation chamber. 11. The firing furnace of claim 10 , further comprising a plurality of conveyors configured to convey separate sets of wafers through the heating chamber, wherein each of the conveyors is thermally isolated from the others of the plurality of conveyors within the heating chamber. 12. The firing furnace of claim 11 , wherein the thermal oxidizer is configured to receive the exhaust gases from the wafers on the plurality of conveyors. 13. The firing furnace of claim 11 , wherein the thermal oxidizer comprises a plurality of oxidation chambers configured to receive the exhaust gases from respective ones of the plurality of conveyors. 14. The firing furnace of claim 11 , wherein the thermal oxidizer is configured to receive the exhaust gas immediately and directly from the heating chamber. 15. The firing furnace of claim 11 , wherein the plurality of heating elements are configured to heat the exhaust gases to a temperature sufficient to oxidize the one or more components of the exhaust gases without the use of a catalyst.
Gas phase processes, e.g. by using aerosols · CPC title
Electrical resistance ignition · CPC title
Heating elements specially adapted for furnaces (H05B3/60 takes precedence; arrangements of elements for electric heating in or on furnaces using ohmic resistance heating F27D11/02) · CPC title
Organic components · CPC title
non-flexible · CPC title
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