Removal of metals from wastewater

Patent metadata

Field	Value
Publication number	US-2016159669-A1
Application number	US-201514953655-A
Country	US
Kind code	A1
Filing date	Nov 30, 2015
Priority date	Dec 4, 2014
Publication date	Jun 9, 2016
Grant date	—

Abstract

A method for effecting a comprehensive removal of heavy metals from wastewater in a two stage process in which the wastewater is contacted in a first stage with a source of ferric ions under mildly acidic conditions (pH 5 to pH 8), preferably followed by the removal of the precipitated solids using a solid-liquid separation; a second stage follows in which the wastewater from the first step is contacted with a source of ferric ions under alkaline conditions (pH 8+) followed by the removal of the precipitated solids using a second solid-liquid separation. Used in conjunction with an initial oxidation step, the present method makes possible the removal of a whole suite of heavy metals present in both the anionic and cationic form in refinery wastewater. The treatment also removes metal compounds in the particulate phase. Metals concentrations can be significantly decreased from the mid to high ppb (parts per billion) range down to the low ppb range to meet the quality criteria for discharge.

First claim

1 . A process for the removal of metal ions from wastewater comprising:
contacting the wastewater containing metal ions with a source of ferric ions under acidic conditions to form a first co-precipitate of metals with ferric hydroxide, contacting the effluent from the first stage with a source of ferric ion under alkaline conditions to form a second co-precipitate of metals with ferric hydroxide, and removing the precipitated solids using a second solid-liquid separation to form a final effluent of reduced metals content.

2 . A process according to claim 1 which comprises:
in a first stage, contacting the wastewater containing metal ions with a source of ferric ions under acidic conditions to form a co-precipitate of metals with ferric hydroxide,
removing the precipitated solids by solid-liquid separation to form a liquid effluent,
in a second stage, contacting the liquid effluent from the first stage with a source of ferric ions under alkaline conditions to form a second co-precipitate of metals with ferric hydroxide, and
removing the precipitated solids using a second solid-liquid separation.

3 . A process according to claim 2 in which the precipitated solids removed in the first and second stages are each subjected to thickening in separate thickening steps.

4 . A process according to claim 2 in which the precipitated solids removed in the first and second stages are combined and subjected to thickening in a combined thickening step.

5 . A process according to claim 3 in which liquid effluent from the thickening steps is recirculated to the first stage.

6 . A process according to claim 4 in which liquid effluent from the combined thickening step is recirculated to the first stage.

7 . A process according to claim 2 in which the wastewater contains nickel and selenium ions which are removed to a nickel content in the final effluent of not more than 5 ppb and the selenium content is not more than 30 ppb.

8 . A process according to claim 3 in which the wastewater contains nickel and selenium ions which are removed to a nickel content in the final effluent of not more than 5 ppb and the selenium content is not more than 30 ppb.

9 . A process according to claim 4 in which the wastewater contains nickel and selenium ions which are removed to a nickel content in the final effluent of not more than 5 ppb and the selenium content is not more than 30 ppb.

10 . A process according to claim 5 in which the wastewater contains nickel and selenium ions which are removed to a nickel content in the final effluent of not more than 5 ppb and the selenium content is not more than 30 ppb.

11 . A process according to claim 6 in which the wastewater contains nickel and selenium ions which are removed to a nickel content in the final effluent of not more than 5 ppb and the selenium content is not more than 30 ppb.

12 . A process according to claim 1 in which the source of ferric ions is contacted with the wastewater in a first stage under acidic conditions to form a first co-precipitate of metals with ferric hydroxide and a liquid effluent, and the first co-precipitate is transferred with the liquid effluent to a second stage in which additional ferric ions are added under alkaline conditions to form a combined co-precipitate which is removed using a second solid-liquid separation.

13 . A process according to claim 1 in which the source of ferric ions is contacted with the wastewater in a first stage under acidic conditions to form a first co-precipitate of metals with ferric hydroxide and a liquid effluent and the first co-precipitate is transferred with the liquid effluent to a second stage maintained under alkaline conditions to form a combined co-precipitate which is removed using a second solid-liquid separation.

14 . A process according to claim 1 in which the first stage precipitation is carried out at ph 5 to pH 8.

15 . A process according to claim 1 in which the first stage precipitation is carried out at ph 6.5 to pH 8.

16 . A process according to claim 1 in which the second stage precipitation is carried out at ph 8 to pH 10.

17 . A process according to claim 1 in which the wastewater is treated to oxidation prior to the first stage.

18 . A process according to claim 17 in which the wastewater is treated to biological oxidation prior to the first stage to convert selenocyanate ions to selenium (IV) ions.

19 . A process according to claim 17 in which the wastewater is treated to biological oxidation prior to the first stage.

20 . A process according to claim 19 in which the wastewater is treated to biological oxidation prior to the first stage to convert selenocyanate to selenium (IV) ions.

21 . A process according to claim 1 in which the ferric ion concentration in the first and second stages is from 30 to 100 mg/L Fe 3+ as Fe.

22 . A process according to claim 1 in which the ferric ion concentration in the first and second stages is from 50 to 80 mg/L Fe 3+ as Fe.

23 . A process according to claim 1 in which the co-precipitation is carried out in the presence of a flocculant and/or a coagulant.

24 . A process according to claim 22 in which the first stage is carried out in the presence of an anionic polymer and the second stage in the presence of a cationic polymer.

25 . A process according to claim 1 in which the nickel content in the final effluent is not more than 5 ppb and the selenium content is not more than 30 ppb.

Assignees

• Barbot Elise Noelle
• Gustafsson Meredith Beck
• Havran Cynthia Marie
• Arboleda-Peña Monica Alexandra
• Exxonmobil Res & Eng Co

Inventors

• Barbot Elise Noelle
• Gustafsson Meredith Beck
• Havran Cynthia Marie
• Arboleda-Peña Monica Alexandra

Classifications

• C02F1/5227 Primary

  Processes for facilitating the dissolution of solid flocculants in water · CPC title

• C02F2101/106

  Selenium compounds · CPC title

• C02F3/00

  Biological treatment of water, waste water, or sewage {(C02F1/006 takes precedence)} · CPC title

• C02F1/5236 Primary

  using inorganic agents · CPC title

• C02F1/72

  by oxidation {(C02F1/4672 takes precedence)} · CPC title