# US 10,501,352 B2 · Non-stripping bioreactor for biological sulfide oxidation from wastewaters and groundwaters containing hydrogen sulfide

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- Number: US 10,501,352 B2
- Document ID: US10501352B2
- Status: Granted
- Kind: B2
- Application number: 15/491,732
- Filed: 2017-04-19
- Published: 2017-10-26
- Granted: 2019-12-10
- Earliest claimed: 2016-04-20
- Assignees: Uop LLC
- Applicants: Uop LLC
- Inventors: F. Stephen Lupton; William Sheridan
- Web page: https://patentgrep.com/patent/US10501352B2

## CPC

- C02F 3/345: {for biological oxidation or reduction of sulfur compounds}
- C02F 3/06: using submerged filters
- C02F 3/10: Packings; Fillings; Grids (packing elements in general B01J19/30, B01J19/32)
- C02F 2101/101: {Sulfur compounds}
- C02F 2103/06: Contaminated groundwater or leachate
- C02F 2103/365: {from petrochemical industry (e.g. refineries)}
- C02F 2301/046: Recirculation with an external loop
- Y02W 10/10: Biological treatment of water, waste water, or sewage
- 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

A method is presented for biological removal of contaminants like sulfide from ground waters and industrial waters. A portion of the bioreactor effluent water is recycled to the bioreactor and the sulfide oxidizing bacteria by biological oxidation oxidizes sulfides in the water to produce soluble sulfates. The present invention uses a packed bed bioreactor configuration that uses packing material to maximize the concentration of sulfide oxidizing bacteria.

## Claims

### Claim 1

A process for removing sulfides from a feed water stream in a bioreactor wherein the feed water stream contains from about 1 mg/L to about 2500 mg/L of sulfur compounds on an elemental sulfur basis, the process comprising:
(a) passing the feed water stream through a fixed film bioreactor containing an effective quantity of autotrophic obligate chemolithotrophic bacteria immobilized on a packing material within said bioreactor;
(b) recycling a portion of a recycle water from a bioreactor effluent to the bioreactor;
(c) passing air to the said recycle water to saturate the recycle water with dissolved oxygen to produce oxygenated recycle water;
(d) mixing the oxygenated recycle water with the feed water stream to provide a mixed water stream that is passed through the bioreactor;
(e) oxidizing the sulfides in said mixed water stream in the bioreactor to form sulfates; and
(f) removing a purified water stream comprising less than about 0.5 mg/L sulfides from said bioreactor.

### Claim 2 (depends on 1)

The process of claim 1 wherein said feed water stream is selected from the group consisting of briny ground water, fracking wastewater, sulfidic caustic wastewater, sour water from refining or from petrochemical processing, sulfidic sewer water, and sour water generated by anaerobic digesters and mixtures thereof.

### Claim 3 (depends on 1)

The process of claim 1 wherein said autotrophic obligate chemolithotrophic bacteria are selected from the group consisting of Acidithiobacillus ferrooxidans, Thermithiobacillus tepidarius, Sulfurimonas denitrificans, Desulfocapsa sulfoexigens, Thiobacillus, Halothiobacillus, Thiomicrospira, Sulfolobus, Acidianus, Sulfurisphaera, and Sulfurococcus.

### Claim 4 (depends on 1)

The process of claim 1 wherein said purified water stream comprises less than about 0.2 mg/L sulfides.

### Claim 5 (depends on 1)

The process of claim 1 wherein the ratio of the recycle water to the feed water stream is about 18 to 1.

### Claim 6 (depends on 1)

The process of claim 1 further comprising splitting the recycle water to the fixed film bioreactor and another bioreactor.

### Claim 7 (depends on 1)

The process of claim 1 wherein the concentration of oxygen dissolved in the recycle water is about 12 mg/L to 1 mg/L.

### Claim 8 (depends on 1)

The process of claim 1 wherein a majority of sulfides within said mixed water stream are oxidized to sulfates by said chemolithotrophic sulfur oxidizing bacteria.

### Claim 9 (depends on 1)

The process of claim 1 wherein said packing material contains about 10,000 mg/L of fixed biomass of said bacteria per liter of water.

### Claim 10 (depends on 1)

The process of claim 1 wherein said water stream comprises a salt concentration of more than 1% total salinity.

### Claim 11 (depends on 1)

The process of claim 1 wherein said mixed water stream flow through said autotrophic obligate chemolithotrophic bacteria.

### Claim 12 (depends on 1)

The process of claim 1 wherein said purified water is reused in an industrial processor discharged into nearby ground water.