Stacked circulatable microbial electrochemical reactor and degradation method of petroleum hydrocarbon contaminated soil
US-12257615-B2 · Mar 25, 2025 · US
US11517950B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-11517950-B2 |
| Application number | US-202016843693-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 8, 2020 |
| Priority date | Apr 11, 2019 |
| Publication date | Dec 6, 2022 |
| Grant date | Dec 6, 2022 |
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Soil contamination by heavy metals constitutes an important environmental problem, whereas field applicability of existing remediation technologies has encountered numerous obstacles, such as long operation time, high chemical cost, large energy consumption, secondary pollution, and soil degradation. A design and demonstration of a method is provided which is based on asymmetrical alternating current electrochemistry (AACE) that achieves high degrees of contaminant removal for different heavy metals (Cu, Pb, Cd) at different initial concentrations (from 100 to 10,000 ppm), all reaching corresponding regulation levels for residential scenario after rational treatment time (from 30 min to 6 h). No excessive nutrient loss in treated soil was observed and no secondary toxic product was produced. Long-term experiment and plant assay showed the high sustainability of the method and its feasibility for agricultural use.
Opening claim text (preview).
What is claimed is: 1. A method for soil remediation comprising: (a) providing a recirculating soil washing system that provides a chelating agent to soil being treated in a treatment tank; (b) providing a filter in the treatment tank, wherein the filter includes a working electrode and a ground electrode sandwiching a separator; and (c) providing an alternating current (AC) electrical input between the working electrode and the ground electrode, wherein the AC electrical input has a positive and a negative voltage excursion, wherein chelation sites on the working electrode bind heavy metal cations from the soil being treated when the working electrode is positively biased with respect to the ground electrode, and wherein the heavy metal cations on the working electrode are electrochemically reduced and form solid particles when the working electrode is negatively biased with respect to the ground electrode. 2. The method as set forth in claim 1 , wherein the filter is an asymmetrical alternating current electrochemistry filter. 3. The method as set forth in claim 1 , wherein the chelating agent is an ethylenediaminetetraacetic acid (EDTA) solution, a dimercaptosuccinic acid (DMSA) solution, a 2,3-dimercaptopropanesulfonic acid (DMPS) solution, an alpha lipoic acid (ALA) solution, or a thiamine tetrahydrofurfuryl disulfide (TTFD) solution. 4. The method as set forth in claim 1 , wherein the alternating current (AC) electrical input ranges from −10V to +5V. 5. The method as set forth in claim 1 , wherein the alternating current (AC) electrical input ranges from −20V to +20V. 6. The method as set forth in claim 1 , wherein the working electrode is positively biased for a period ranging from 0.1 to 1 ms. 7. The method as set forth in claim 1 , of the working electrode is negatively biased for a period ranging from 1 to 5 ms. 8. The method as set forth in claim 1 , wherein one or more of the heavy metal cations Cu, Pb, Cd, Hg, Cr, As, Ni, Zn, Fe, or a combination thereof. 9. The method as set forth in claim 1 , wherein the alternating current (AC) electrical input has a sinusoidal waveform, a stepwise waveform or a biphasic waveform.
Treatment of the solvent · CPC title
electrochemically, e.g. by electrokinetics · CPC title
Applications, solvents · CPC title
Extraction using liquids, e.g. washing, leaching {, flotation} · CPC title
in combination with an electric or magnetic field · CPC title
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