# US 2020/0392017 A1 · Systems and methods for water purification

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- Number: US 2020/0392017 A1
- Document ID: US20200392017A1
- Status: Published application
- Kind: A1
- Application number: 16/772,559
- Filed: 2017-12-18
- Published: 2020-12-17
- Earliest claimed: 2017-12-18
- Assignees: Qatar Foundation for Education, Science and Community Development
- Applicants: Qatar Foundation for Education, Science and Community Development
- Inventors: Ahmad Kayvani FARD; Muataz; HUSSIEN
- Web page: https://patentgrep.com/patent/US20200392017A1

## CPC

- C02F 1/283: {using coal, charred products, or inorganic mixtures containing them}
- B01D 67/00411: {by sintering}
- B01D 69/147: {containing embedded adsorbents}
- B01D 71/021: {Carbon}
- B01D 71/025: {Aluminium oxide}
- C02F 1/288: {using composite sorbents, e.g. coated, impregnated, multi-layered}
- C02F 1/444: {by ultrafiltration or microfiltration}
- B01D 17/02: Separation of non-miscible liquids
- B01D 2325/28: Degradation or stability over time
- C02F 2101/006: {Radioactive compounds}
- C02F 2101/103: {Arsenic compounds}
- C02F 2101/32: Hydrocarbons, e.g. oil
- 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)
- B01D: SEPARATION (separating solids from solids by wet methods B03B, B03D; by pneumatic jigs or tables B03B; by other dry methods B07; magnetic or electrostatic separation of solid materials from solid materials or fluids, separation by high-voltage electric fields B03C; centrifuges, vortex apparatus B04; presses per se for squeezing-out liquid from liquid-containing material B30B9/02; treatment of water C02F, e.g. softening by ion-exchange C02F1/42; {arrangements of air intake cleaners in gas turbine plants F02C7/05} ; arrangements or mounting of filters in air-conditioning, air-humidification or ventilation F24F13/28)

## Abstract

The present disclosure provides systems and methods for treatment of produced water that combine a separation technique using an inorganic membrane (Al2O3) with an adsorption process using activated carbon in the membrane. In one embodiment, a water tank includes an inlet and an outlet, and the membrane is in fluid communication with the inlet. The tank is configured to receive a spent water stream that includes a contaminant. In operation, the spent water stream is contacted with the membrane so as to strip at least a portion of the contaminant from the spent water stream.

## Claims

### Claim 1

A system for water purification, the system comprising:
a water tank comprising an inlet and an outlet, the tank configured to receive a spent water stream that includes a contaminant; and
a membrane in fluid communication with the inlet, the membrane comprising alumina and activated carbon, and the membrane configured to contact the spent water stream and strip at least a portion of the contaminant from the spent water stream.

### Claim 2 (depends on 1)

The system of claim 1, wherein the contaminant includes at least one selected from the group consisting of emulsified oil, barium, arsenic, lead, and strontium.

### Claim 3 (depends on 1)

The system of claim 1, wherein the membrane strips the contaminant in entirety from the spent water stream.

### Claim 4 (depends on 1)

The system of claim 1, wherein the activated carbon has an average particle size in the range of 0.025 mm to 0.18 mm.

### Claim 5 (depends on 1)

The system of claim 1, wherein the alumina has an average particle size in the range of 0.1 μm to 10 μm.

### Claim 6 (depends on 1)

The system of claim 1, wherein the alumina has an average particle size in the range of 0.1 μm to 5 μm.

### Claim 7 (depends on 1)

The system of claim 1, wherein the membrane comprises 5% to 40% activated carbon by weight.

### Claim 8 (depends on 1)

The system of claim 1, wherein the membrane comprises 10% to 30% activated carbon by weight.

### Claim 9 (depends on 1)

The system of claim 1, wherein a thickness of the membrane is 0.5 mm to 20 mm.

### Claim 10 (depends on 1)

The system of claim 1, wherein the membrane consists of alumina and activated carbon.

### Claim 11 (depends on 1)

The system of claim 1, wherein the membrane is tubular and configured for an industrial scale water treatment.

### Claim 12

A method of purifying water, the method comprising:
providing a spent water stream that includes a contaminant; and
contacting the spent water stream with a membrane so as to strip at least a portion of the contaminant from the spent water stream, the membrane comprising alumina and activated carbon.

### Claim 13 (depends on 12)

The method of claim 12, wherein the contaminant includes at least one selected from the group consisting of emulsified oil, barium, arsenic, lead, and strontium.

### Claim 14 (depends on 12)

The method of claim 12, wherein the membrane strips the contaminant in entirety from the spent water stream.

### Claim 15 (depends on 12)

The method of claim 12, wherein the activated carbon has an average particle size in the range of 0.025 mm to 0.18 mm.

### Claim 16 (depends on 12)

The method of claim 12, wherein the alumina has an average particle size in the range of 0.1 ∞m to 10 μm.

### Claim 17 (depends on 12)

The method of claim 12, wherein the alumina has an average particle size in the range of 0.1 μm to 5 μm.

### Claim 18 (depends on 12)

The method of claim 12, wherein the membrane comprises 5% to 40% activated carbon by weight.

### Claim 19 (depends on 12)

The method of claim 12, wherein the membrane comprises 10% to 30% activated carbon by weight.

### Claim 20

(canceled)

### Claim 21 (depends on 12)

The method of claim 12, wherein the membrane consists of alumina and activated carbon.

### Claim 22

(canceled)
