Chlorination-assisted coagulation processes for water purification

Patent metadata

Field	Value
Publication number	US-2018230026-A1
Application number	US-201715791731-A
Country	US
Kind code	A1
Filing date	Oct 24, 2017
Priority date	Feb 16, 2017
Publication date	Aug 16, 2018
Grant date	—

Abstract

Chlorination-assisted coagulation processes and systems are disclosed for removing organic and inorganic contaminants from aqueous compositions and streams such as produced water generated by petroleum production operations. The chlorination-assisted coagulation process includes converting at least a portion of chloride ions in the aqueous composition to hypochlorite ions or hypochlorous acid by passing an electric current through at least a portion of the aqueous composition under anaerobic conditions, the aqueous composition including the chloride ions, iron (II) compounds, and one or more organic compounds. The chlorination-assisted coagulation process further includes reacting at least a portion of the iron (II) compounds of the aqueous composition with the hypochlorite or hypochlorous acid to produce iron (III) ions, and coagulating the one or more organic compounds with the iron (III) ions to produce a plurality of insoluble solid particles in a treated aqueous composition.

First claim

What is claimed is:

1 . A process for treating an aqueous composition, the process comprising:
converting at least a portion of chloride ions in the aqueous composition to hypochlorite ions or hypochlorous acid by passing an electric current through at least a portion of the aqueous composition under anaerobic conditions, the aqueous composition including the chloride ions, iron (II) compounds, and one or more organic compounds; reacting at least a portion of the iron (II) compounds of the aqueous composition with the hypochlorite or hypochlorous acid to produce iron (III) ions; and coagulating the one or more organic compounds with the iron (III) ions to produce a plurality of insoluble solid particles in a treated aqueous composition.

2 . The process of claim 1 where the electric current has a voltage of greater than or equal to 1.5 volts (V).

3 . The process of claim 1 where the electric current has a voltage from 1.5 V to 5.0 V.

4 . The process of claim 1 where a current density of the electric current is from 1 milliampere per square centimeter to 1 ampere per square centimeter.

5 . The process of claim 1 where the aqueous composition comprises a composition of an oilfield produced water.

6 . The process of claim 1 where a pH of the aqueous composition is from 2.5 to 8.5.

7 . The process of claim 1 where a pH of the aqueous composition is from 10.5 to 12.5.

8 . The process of claim 1 where the electric current is passed through the aqueous composition with non-sacrificial electrodes.

9 . The process of claim 8 where the non-sacrificial electrodes have an outer surface comprising one or more of zirconium, molybdenum, gold, silver, tantalum, tungsten, chromium, carbon, sulfur, silicon, or oxides of these materials.

10 . The process of claim 8 further comprising alternating polarities of the non-sacrificial electrodes.

11 . The system of claim 10 where the polarities of the non-sacrificial electrodes are alternated by an electrode polarity alternator comprising a waveform generator.

12 . The system of claim 8 further comprising rotating the non-sacrificial electrodes relative to the aqueous composition.

13 . The system of claim 12 where the non-sacrificial electrodes are rotated by an electrode rotation system comprising a shaft coupled to each of the non-sacrificial electrodes and a drive operatively coupled to the shaft, the drive operable to rotate the shaft and the non-sacrificial electrodes relative to the aqueous composition.

14 . The process of claim 1 further comprising flocculating the plurality of insoluble solid particles by introducing a flocculent to the aqueous composition.

15 . The process of claim 1 further comprising separating the plurality of insoluble solid particles from the treated aqueous composition.

16 . The process of claim 1 further comprising introducing supplemental iron (II) compounds to the aqueous composition.

17 . The process of claim 1 where all of the aqueous composition is subjected to the electric current.

18 . The process of claim 1 further comprising:
measuring a property of the aqueous composition or the treated aqueous composition; and
controlling a voltage or a current density of the electric current passing through the aqueous composition in response to the measured property.

19 . The process of claim 18 where the property comprises an oxidation-reduction potential.

20 . The process of claim 1 further comprising:
separating the aqueous composition into a first portion and a second portion;
converting at least a portion of the chloride ions in the first portion of the aqueous composition to hypochlorite or hypochlorous acid by passing an electric current through the first portion of the aqueous composition under anaerobic conditions; and
combining the first portion of the aqueous composition with the second portion of the aqueous composition after converting of the chloride ions in the first portion to hypochlorite or hypochlorous acid.

21 . The process of claim 20 further comprising:
measuring a property of the first portion of the aqueous solution, the second portion of the aqueous composition, or the treated aqueous composition; and
adjusting a ratio of the first portion to the second portion of the aqueous composition based on the measured property.

22 . The process of claim 1 where the aqueous composition comprises phenolic compounds and the treated aqueous composition comprises less than 0.01 parts per million by weight phenolic compounds, after treatment.

23 . The process of claim 1 where the aqueous composition includes greater than or equal to 0.1 weight percent crude oil and the treated aqueous composition comprises less than 50 milligrams per liter crude oil, after treatment.

24 . The process of claim 1 where the process is conducted at a pressure of from 100 kilopascals to 1,000 kilopascals and a temperature of from 25 degrees Celsius to 80 degrees Celsius.

25 . The process of claim 1 where the aqueous composition comprises hydrogen sulfide and the treated aqueous composition comprises a concentration of hydrogen sulfide less than the aqueous composition.

26 . The process of claim 1 further comprising co-precipitating inorganic cationic species from the aqueous composition and separating the co-precipitated inorganic cationic species from the treated aqueous composition.

27 . The process of claim 1 further comprising:
passing the aqueous composition to an electro-chlorination zone, where the at least a portion of chloride ions in the aqueous composition are converted to hypochlorite ions or hypochlorous acid in the electro-chlorination zone, and
passing the aqueous composition from the electro-chlorination zone to a coagulation zone downstream of the electro-chlorination zone.

28 . The process of claim 27 further comprising:
separating the aqueous composition into a first portion and a second portion;
passing the first portion of the aqueous composition to the electro-chlorination zone;
passing the second portion of the aqueous composition through a bypass line to the coagulation zone; and
passing the first portion of the aqueous composition from the electro-chlorination zone to the coagulation zone; and
combining the first portion of the aqueous composition with the second portion of the aqueous composition in the coagulation zone.

29 . A process for removing organic compounds from an aqueous composition, the process comprising:
introducing at least a portion of the aqueous composition to an electro-chlorination zone, the aqueous composition comprising at least chloride ions, iron (II) compounds, and one or more organic compounds; converting at least a portion of the chloride ions in the aqueous composition into hypochlorite or hypochlorous acid by passing an electric current through the aqueous composition under anaerobic conditions in the electro-chlorination zone; oxidizing at least a portion of the iron (II) compounds in the aqueous composition with the hypochlorite or hypochlorous acid in the electro-chlorination zone or in a coagulation zone to produce iron (III) ions; coagulating the one or more organic compounds with the iron (III) ions in the coagulation zone to produce a plurality of insoluble solid particles in the aqueous composition; and separating at least a

Assignees

• Saudi Arabian Oil Co

Inventors

• Raynel Guillaume Robert Jean-François
• Vilagines Regis Didier Alain

Classifications

• C02F2209/04

  Oxidation reduction potential [ORP] · CPC title

• C02F2209/03

  Pressure · CPC title

• C02F2103/365

  from petrochemical industry (e.g. refineries) · CPC title

• C02F2209/02

  Temperature · CPC title

• C02F2101/32

  Hydrocarbons, e.g. oil · CPC title