# US 10,245,626 B2 · Mine drainage remediation using barium carbonate dispersed alkaline substrate

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- Number: US 10,245,626 B2
- Document ID: US10245626B2
- Status: Granted
- Kind: B2
- Application number: 15/508,757
- Filed: 2015-09-04
- Published: 2017-09-28
- Granted: 2019-04-02
- Earliest claimed: 2014-09-04
- Assignees: University of the Free State
- Applicants: University of the Free State
- Inventors: Esta Van Heerden; Julio Hernandez Castillo; Alba Gomez; Rohan Posthumus; Walter George Van Der Hoven
- Web page: https://patentgrep.com/patent/US10245626B2

## CPC

- B09C 1/10: microbiologically, {biologically} or by using enzymes
- B09C 1/00: Reclamation of contaminated soil
- B09C 1/02: Extraction using liquids, e.g. washing, leaching {, flotation}
- B09C 1/08: chemically
- C02F 1/5245: {using basic salts, e.g. of aluminium and iron}
- C02F 1/66: by neutralisation; pH adjustment (for degassing C02F1/20; using ion-exchange C02F1/42; for flocculation or precipitation of suspended impurities C02F1/52; for removing dissolved compounds C02F1/58)
- C02F 3/106: {Carbonaceous materials}
- C02F 3/2806: {Anaerobic processes using solid supports for microorganisms}
- C02F 3/305: {characterised by the denitrification}
- C02F 3/345: {for biological oxidation or reduction of sulfur compounds}
- C02F 3/107: {Inorganic materials, e.g. sand, silicates}
- C02F 2101/10: Inorganic compounds
- C02F 2101/101: {Sulfur compounds}
- C02F 2101/103: {Arsenic compounds}
- C02F 2101/105: {Phosphorus compounds}
- C02F 2101/163: {Nitrates}
- C02F 2101/20: Heavy metals or heavy metal compounds
- C02F 2101/203: {Iron or iron compound}
- C02F 2103/10: from quarries or from mining activities
- C02F 2305/06: Nutrients for stimulating the growth of microorganisms
- Y02W 10/10: Biological treatment of water, waste water, or sewage
- B09C: RECLAMATION OF CONTAMINATED SOIL (gatherers for removing stone or the like from the soil A01B43/00; sterilising soil by steam A01G11/00; removing undesirable matter, e.g. rubbish, from the land E01H15/00)
- C02F: TREATMENT OF WATER, WASTE WATER, SEWAGE, OR SLUDGE (separation in general B01D; special arrangements on waterborne vessels of installations for treating water, waste water or sewage, e.g. for producing fresh water, B63J; adding materials to water to prevent corrosion C23F; treating radioactively-contaminated liquids G21F9/04; regeneration of reactants for recirculation into processes, see the relevant places for the processes)
- Y02W: CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT

## Abstract

The present invention relates to a treatment system having a barium carbonate (BaCO3) dispersed alkaline substrate (BDAS) for use in the remediation or at least partial remediation of mine drainage (MD) and/or environmental media contaminated with a source of MD. The invention utilizes chemical, biological and combined treatment systems remove high concentrations of sulfates, hardness, heavy metals and N-compounds, that may exist in the MD as well as high concentrations of alkalinity produced during the remediation process. The invention further extends to a process for treating MD and/or environmental media contaminated with MD and to an apparatus for use in this process.

## Claims

### Claim 1

A fixed-film bioreactor for bio-remediation, or at least partial bio-remediation, of environmental media contaminated with a source of mine drainage (MD), and wherein the bioreactor is a down-flow reactor with a supernatant open to the atmosphere in order to maximize iron oxidation and to minimize iron (II) mobility in the bioreactor, said fixed-film bioreactor including:
(i) a support matrix;
(ii) a barium carbonate BaCO3 alkaline substrate for removing sulphate, cation, electrical conductivity (EC) and total dissolved solids (TDS) by precipitation; and
(iii) a microbial consortium for removing nitrates and cyanide.

### Claim 2 (depends on 1)

The fixed-film bioreactor of claim 1, wherein the fixed-film bioreactor is in the form of a fixed-film biocell.

### Claim 3 (depends on 1)

The fixed-film bioreactor of claim 1, wherein the support matrix serves as an inert physical support mechanism for a microbial community.

### Claim 4 (depends on 1)

The fixed-film bioreactor of claim 1, wherein the support matrix serves as surface media for the dispersal of the BaCO3 alkaline substrate thereby allowing the formation of a dispersed alkaline substrate (DAS).

### Claim 5 (depends on 4)

The fixed-film bioreactor of claim 4, wherein the dispersed alkaline substrate (DAS) is in the form of a BACO3 dispersed alkaline substrate (BDAS).

### Claim 6 (depends on 1)

The fixed-film bioreactor of claim 1, wherein the support matrix material comprises a material selected from the group consisting of an inert organic medium, wood chips and gravel.

### Claim 7 (depends on 6)

The fixed-film bioreactor of claim 6, wherein the support matrix material comprises wood chips.

### Claim 8 (depends on 6)

The fixed-film bioreactor of claim 6, wherein the support matrix material consists of a combination of wood chips and quartz gravel.

### Claim 9 (depends on 7)

The fixed-film bioreactor of claim 7, wherein the ratio of wood chips to BACO3 is 4:1 (v/v).

### Claim 10 (depends on 6)

The fixed-film bioreactor of claim 6, wherein the support matrix provides an electron donor for the microbial consortium.

### Claim 11 (depends on 6)

The fixed-film bioreactor of claim 6, wherein the inert organic material is manure.

### Claim 12 (depends on 11)

The fixed-film bioreactor of claim 11, wherein the manure is horse manure.

### Claim 13 (depends on 1)

The fixed-film bioreactor of claim 1, wherein the microbial consortium comprises sulfate reducing microorganisms.

### Claim 14 (depends on 1)

The fixed-film bioreactor of claim 1, wherein the dissolution of barium carbonate BACO3 has a pH of about pH 3 to about pH 8.5.

### Claim 15 (depends on 1)

The fixed-film bioreactor of claim 1, wherein a zero valent iron (ZVI) is included.

### Claim 16 (depends on 1)

The fixed-film bioreactor of claim 1, wherein the fixed-film bioreactor operates under aerobic conditions.

### Claim 17 (depends on 1)

The fixed-film bioreactor of claim 1, wherein the fixed-film bioreactor operates under anaerobic conditions.

### Claim 18 (depends on 1)

The fixed-film bioreactor of claim 1, wherein the bioreactor can operate at either continuous or pulsed flow.

### Claim 19 (depends on 1)

The fixed-film bioreactor of claim 1, wherein the precipitation is in the form of any one or more of barium sulfate (BaSO4), carbonates ((Me2+)CO3) and oxy-hydroxides (Me2+/3+O(OH)).

### Claim 20

A process for the bioremediation, or at least partial bioremediation, of environmental media contaminated with MD, wherein the process includes the step of removing environmental media from a mine drainage contaminated site and exposing the environmental media to a mixture including an indigenous microbial consortium of microorganisms from MD, wood chips as a minimal source of electron donor, and a dispersed alkaline substrate including dispersed barium carbonate BaCO3, allowing for the chemically and biologically mediated precipitation of sulfate, nitrate, phosphate and metals.

### Claim 21 (depends on 1)

A process for the bioremediation, or at least partial bioremediation, of environmental media contaminated with MD, wherein the process includes the step of removing environmental media from a mine drainage contaminated site and exposing the environmental media to a mixture including an indigenous microbial consortium of microorganisms from MD, wood chips as a minimal source of electron donor, and a dispersed alkaline substrate including dispersed barium carbonate BaCO3, allowing for the chemically and biologically mediated precipitation of sulfate, nitrate, phosphate and metals, and wherein said process includes the following stages:
a first stage including the steps of:
(i) providing a bioreactor as claimed in claim 1, wherein the bioreactor includes a support matrix which has been wetted and pre-treated with BaCO3 to form a BaCO3 dispersed alkaline substrate;
(ii) introducing the MD contaminated media into the bioreactor and subsequently introducing the indigenous microbial consortium of microorganisms; and
(iii) controlling the hydraulic retention time of the bioreactor such that the hydraulic retention time is between about 9 hours and about 24 hours; and
a second stage including the steps of:
(iv) allowing for the precipitation of the sulfate present in the source of the MD contaminated environmental media as barium sulfate (BaSO4);
(v) allowing for the precipitation of Ca, Mg, Na and trace metals present in the source of the MD contaminated environmental media as calcite and aragonite (CaCO3);
(vi) allowing for the precipitation of heavy metals present in the source of the MD contaminated environmental media as oxy-hydroxides (Me2+/3+O(OH)); and
(vii) removing cyanide and nitrates.
