# US 10,501,340 B2 · Surfactant removal from produced waters

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- Number: US 10,501,340 B2
- Document ID: US10501340B2
- Status: Granted
- Kind: B2
- Application number: 15/189,590
- Filed: 2016-06-22
- Published: 2016-12-22
- Granted: 2019-12-10
- Earliest claimed: 2015-06-22
- Assignees: ConocoPhillips Company
- Applicants: Conocophillips Company
- Inventors: Riley B. Needham; Sriram Solairaj
- Web page: https://patentgrep.com/patent/US10501340B2

## CPC

- C02F 1/281: {using inorganic sorbents}
- B01D 15/02: with moving adsorbents
- B01D 21/00: Separation of suspended solid particles from liquids by sedimentation ({separation of ores or the like by sedimentation B03B5/48 - B03B5/60} ; differential sedimentation B03D3/00; {purification of water, waste water, sewage or sludge C02F, e.g.} devices for separating or removing fatty or oily substances or similar floating material from water, waste water or sewage C02F1/40)
- B01J 20/06: comprising oxides or hydroxides of metals not provided for in group B01J20/04
- B01J 20/28016: {Particle form}
- B01J 20/3204: {Inorganic carriers, supports or substrates}
- B01J 20/3236: {containing metal, other than zeolites, e.g. oxides, hydroxides, sulphides or salts}
- C02F 1/288: {using composite sorbents, e.g. coated, impregnated, multi-layered}
- C02F 1/385: {by centrifuging suspensions (centrifuges B04B)}
- C02F 1/285: {using synthetic organic sorbents}
- C02F 1/72: by oxidation {(C02F1/4672 takes precedence)}
- C02F 2001/007: {Processes including a sedimentation step}
- C02F 2101/301: {Detergents, surfactants}
- C02F 2101/40: {containing sulfur}
- C02F 2103/10: from quarries or from mining activities
- 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)
- B01J: CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS

## Abstract

A method for removing a surfactant from a water stream includes contacting the water stream with a particulate support having a hydrous iron oxide coating to provide a treated water stream. The treated water stream has less surfactant than the water stream.

## Claims

### Claim 1

A method for removing a surfactant from a water stream, the method consisting essentially of:
providing a water stream comprising produced water containing surfactant recovered from an oil well,
contacting the water stream with a particulate support comprising sand with a hydrous iron oxide coating,
absorbing said surfactant to said hydrous iron oxide coating to provide a surfactant-iron-sand complex, and
separating the water stream from said particulate support to thereby provide a treated water stream comprising less surfactant than the water stream.

### Claim 2 (depends on 1)

The method of claim 1, wherein said hydrous iron oxide coating is formed by adding a hydrous iron oxide precursor to the water stream to form the hydrous iron oxide coating.

### Claim 3 (depends on 1)

The method of claim 1, wherein the particulate support is a bed of moving sand.

### Claim 4 (depends on 1)

The method of claim 1, wherein the treated water stream has less than 1 wt. % residual surfactant.

### Claim 5 (depends on 1)

The method of claim 1, wherein said surfactant is at least partially degraded.

### Claim 6 (depends on 3)

The method of claim 3, wherein said surfactant is at least partially degraded and adsorbing the degraded surfactant to the hydrous iron oxide coating to provide a degraded surfactant-iron-sand complex.

### Claim 7 (depends on 1)

The method of claim 1, wherein the surfactant of the surfactant-iron-sand complex is at least partially degraded.

### Claim 8 (depends on 1)

The method of claim 1, wherein the separating is by gravity separating, filtering, centrifuging, decanting, or a combination comprising at least one of the foregoing separating methods, preferably by gravity separating.

### Claim 9 (depends on 1)

The method of claim 1, wherein the surfactant is present in the water stream in an amount of 50 to 400 ppm.

### Claim 10 (depends on 1)

The method of claim 1, wherein the surfactant is an anionic surfactant.

### Claim 11 (depends on 10)

The method of claim 10, wherein the anionic surfactant comprises a C4-25 alkyl sulfonate, a C6-25 alkylaryl sulfonate, a C4-25 alkyl sulfate, or a salt thereof, or a combination comprising at least one of the foregoing.

### Claim 12 (depends on 1)

The method of claim 1, wherein the surfactant comprises dodecylsulfate or an alkali metal salt thereof.

### Claim 13 (depends on 2)

The method of claim 2, wherein the hydrous iron oxide precursor comprises ferric chloride, ferrous chloride, ferric sulfate, ferrous sulfate, or a combination comprising at least one of the foregoing.

### Claim 14 (depends on 3)

The method of claim 3, wherein the contacting comprises passing the water through the bed of moving sand.

### Claim 15 (depends on 2)

The method of claim 2, wherein the hydrous iron oxide precursor is present in the water stream at a hydrous iron oxide precursor:surfactant molar ratio of 0.25:1 to 5:1.

### Claim 16 (depends on 2)

The method of claim 2, wherein
the water stream is a produced water stream recovered from an oil well;
the hydrous iron oxide precursor comprises ferric chloride; and
the surfactant is an anionic surfactant in an amount of 50 to 400 ppm.

### Claim 17 (depends on 2)

The method of claim 2, comprising oxidizing the water stream prior to introducing the hydrous iron oxide precursor to the water stream.
