Enzymes, micro-organisms and uses thereof, and a method of degrading hydrocarbon chains
US-2024228990-A9 · Jul 11, 2024 · US
US11298732B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11298732-B2 |
| Application number | US-201916722818-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 20, 2019 |
| Priority date | Jun 20, 2017 |
| Publication date | Apr 12, 2022 |
| Grant date | Apr 12, 2022 |
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Disclosed is a method of simultaneously processing fly ash and COPR, which can treat the fly ash and COPR harmlessly during the landfilling process through biochemical and engineering measures. The method includes: transferring the fly ash and COPR to the yard; laying an impervious layer inside the yard; laying a diversion material at a bottom of the yard; laying a mixture layer on the diversion material, where the mixture layer contains a biogas residue, a waste carbon source, ferrous sulfate, a nutritional additive, the waste incineration fly ash and COPR; placing an internal-electrolysis ceramsite layer on the mixture layer; injecting a carbon source solution from an upper portion of the yard and collecting a leachate to a collection device through the diversion material irregularly during the operation; and recirculating the leachate to a top of the yard for spray reinjection.
Opening claim text (preview).
What is claimed is: 1. A method for simultaneously processing a waste incineration fly ash and a chromite ore processing residue (COPR) in a landfill, comprising: laying an impervious layer at inner side walls of a yard; laying a diversion material at a bottom of the yard; laying a mixture layer on the diversion material, wherein the mixture layer comprises a biogas residue, a waste carbon source, ferrous sulfate, a nutritional additive, the waste incineration fly ash and COPR; placing an internal-electrolysis ceramsite layer on the mixture layer; injecting a carbon source solution from an upper portion of the yard and collecting a leachate to a collection device through the diversion material irregularly; and recirculating the leachate to a top of the yard for spray reinjection. 2. The method of claim 1 , wherein in the mixture layer, a weight ratio of the waste incineration fly ash to COPR to the biogas residue to the waste carbon source to ferrous sulfate to the nutritional additive is 1:(0.1-10):(0.01-5):(0.01-5):(0.15-3):(0.1-1). 3. The method of claim 1 , wherein the mixture layer has a thickness of 1-8 m; and the internal-electrolysis ceramsite layer has a thickness of 1 m or less. 4. The method of claim 1 , wherein the spray reinjection of the leachate is performed at a time interval of 1-48 h. 5. The method of claim 1 , wherein the step of recirculating the leachate to a top of the yard for spray reinjection comprises adjusting the leachate to pH 2-5. 6. The method of claim 1 , wherein the biogas residue is organic wastewater, solid organic waste or sludge. 7. The method of claim 6 , wherein the biogas residue is an anaerobically-treated solid organic waste. 8. The method of claim 1 , wherein the injection of the carbon source solution is performed once every 1-100 days. 9. The method of claim 1 , wherein the nutritional additive is a nitrogen source, a phosphorus source, a trace element source or a combination thereof. 10. The method of claim 9 , wherein a carbon source is 50% or less by weight of the carbon source solution. 11. The method of claim 9 , wherein the trace element source is selected from the group consisting of boron, zinc, copper, manganese, cobalt and a combination thereof. 12. The method of claim 1 , wherein the carbon source solution is a solution comprising ethanol, methanol, acetic acid or a combination thereof. 13. The method of claim 1 , wherein the carbon source solution is further doped with ferrous sulfate. 14. The method of claim 1 , wherein the waste incineration fly ash is a biochemically-, physically- or chemically-treated fly ash. 15. The method of claim 1 , wherein COPR is a chromium-containing soil or a chromium-containing waste. 16. The method of claim 1 , wherein an internal-electrolysis ceramsite of the internal-electrolysis ceramsite layer is a Fe-C internal-electrolysis ceramsite containing metallic iron and a carbon material.
Anaerobic treatment · CPC title
Chemical treatment, e.g. pH adjustment or oxidation (involving an extraction step B09B3/80) · CPC title
Removing ash, clinker, or slag from combustion chambers ({removing flyash from flue gas F23J15/022;} devices for removal of material from the bed of fluidised bed combustion apparatus F23C10/24) · CPC title
Recycling · CPC title
Ash removal means for incinerators · CPC title
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