Method for co-processing of waste incineration fly ash and chromium slag in landfill

US11298732B2 · US · B2

Patent metadata
FieldValue
Publication numberUS-11298732-B2
Application numberUS-201916722818-A
CountryUS
Kind codeB2
Filing dateDec 20, 2019
Priority dateJun 20, 2017
Publication dateApr 12, 2022
Grant dateApr 12, 2022

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  1. Title

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  2. Abstract

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  3. Assignees and inventors

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  4. Key dates

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  5. First independent claim

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  6. CPC / IPC classifications

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  7. Citations and related patents

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Abstract

Official abstract text for this publication.

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.

First claim

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.

Assignees

Inventors

Classifications

  • B09B3/65Primary

    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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Frequently asked questions

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What does patent US11298732B2 cover?
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 diversio…
Who is the assignee on this patent?
Univ Qingdao Technology, Qingdao Jiehua Environmental Tech Co Ltd
What technology area does this patent fall under?
Primary CPC classification B09B3/65. Mapped technology areas include Operations & Transport.
When was this patent published?
Publication date Tue Apr 12 2022 00:00:00 GMT+0000 (Coordinated Universal Time) (B2). Legal status and post-grant events are not shown on this page.
What related patents are in patentsdb?
We list 8 related publications on this page (citations in our corpus or others sharing the same primary CPC).