Removal of amines from aqueous streams

Patent metadata

Field	Value
Publication number	US-2023037949-A1
Application number	US-201917790200-A
Country	US
Kind code	A1
Filing date	Dec 31, 2019
Priority date	Dec 31, 2019
Publication date	Feb 9, 2023
Grant date	—

Abstract

A method and an arrangement for removing amine(s) from a thickener overflow of a mineral processing plant. The method includes supplying the thickener overflow to an electrocoagulation unit and subjecting the thickener overflow to electrocoagulation in order to separate at least some of the amine(s) as an electrocoagulation overflow and in order to form a residual process water as an electrocoagulation underflow, and removing the electrocoagulation overflow. The method is free of all of the following: a coagulant, a flocculant, an adsorbent and an additional flotation chemical.

First claim

1 . A method for removing amine(s) from a thickener overflow of a mineral processing plant, wherein the thickener overflow comprises process water and amine(s);
the method comprising:
supplying the thickener overflow to an electrocoagulation unit and subjecting the thickener overflow to electrocoagulation in order to separate at least some of the amine(s) as an electrocoagulation overflow and in order to form a residual process water as an electrocoagulation underflow, and
removing the electrocoagulation overflow;
wherein the method is free of all of the following: a coagulant, a flocculant, an adsorbent and an additional flotation chemical.

2 . The method according to claim 1 , wherein the thickener overflow originates from a flotation arrangement comprising a mineral flotation circuit arranged to treat ore particles suspended in a slurry by flotation for separation of the slurry into an underflow of a mineral flotation circuit and an overflow of a mineral flotation circuit; and
wherein the overflow of the mineral flotation circuit is dewatered in the thickener in order to produce the thickener overflow and a thickener underflow.

3 . The method according to claim 2 , wherein the mineral flotation circuit is arranged to recover Fe.

4 . The method according to claim 1 ,
wherein the method further comprises
prior to supplying the thickener overflow to the electrocoagulation unit, determining a solid matter content of the thickener overflow, and
if the solid matter content of the thickener overflow is determined to be over a pre-determined threshold value for electrocoagulation, pre-treating the thickener overflow in at least one pre-treatment unit; wherein the pre-treatment unit is a cleaning flotation unit and/or a sand filter unit and the thickener overflow to be treated in the electrocoagulation unit being a pre-treated thickener overflow.

5 . The method according to claim 4 , wherein the method comprises
supplying the thickener overflow to the cleaning flotation unit for pre-treatment and subjecting the thickener overflow to cleaning flotation in order to separate a cleaning flotation overflow and in order to form the pre-treated thickener overflow as a cleaning flotation underflow; wherein the cleaning flotation comprises gas bubbles, at least 90% of the gas bubbles having a diameter of from 0.2 to 250 μm.

6 . The method according to claim 4 , wherein the method comprises
supplying the thickener overflow or the cleaning flotation underflow to the sand filter unit for pre-treatment and filtering the thickener overflow or the cleaning flotation overflow by allowing it to flow through a sand filter in the sand filter unit in order to produce a filtered thickener overflow or a filtered cleaning flotation underflow as the pre-treated thickener overflow.

7 . The method according to claim 1 , wherein the method further comprises
supplying the electrocoagulation underflow to a (secondary) cleaning flotation unit and subjecting the electrocoagulation underflow to cleaning flotation in order to separate a (secondary) cleaning flotation overflow and in order to form a (secondary) cleaning flotation underflow.

8 . The method according to claim 1 , wherein the method further comprises
supplying the electrocoagulation underflow to a (secondary) sand filter unit and filtering the electrocoagulation underflow by allowing it to flow through a sand filter in the (secondary) sand filter unit in order to produce a filtered electrocoagulation underflow.

9 . The method according to claim 4 , wherein the cleaning flotation is a dissolved air flotation.

10 . The method according to claim 1 , wherein the method further comprises
leading the electrocoagulation underflow and/or the (secondary) cleaning flotation underflow and/or the filtered electrocoagulation underflow via a tailings area into the environment.

11 . The method according to claim 1 , wherein the method further comprises
recirculating the electrocoagulation underflow and/or the (secondary) cleaning flotation underflow and/or the filtered electrocoagulation underflow back into the process for use as process water.

12 . The method according to claim 1 , wherein the electrocoagulation unit comprises Fe electrodes.

13 . The method according to claim 1 , wherein the electrocoagulation unit comprises Ti electrodes.

14 . The method according to claim 1 , wherein prior to subjecting the thickener overflow to electrocoagulation, temperature of the overflow is from 0 to 50° C.

15 . The method according to claim 1 , wherein the thickener overflow comprises amine(s) adsorbed onto silicate(s), and the method comprises removing at least some of the silicate(s) from the thickener overflow.

16 . An arrangement for removing amine(s) from a thickener overflow of a mineral processing plant, wherein the thickener overflow comprises process water and amine(s) the arrangement comprising;
a thickener arranged to dewater an overflow of a mineral flotation circuit in order to produce a thickener overflow and a thickener underflow, an electrocoagulation unit arranged separate at least some of the amine(s) from the thickener overflow as an electrocoagulation overflow and to form a residual process water as an electrocoagulation underflow.

17 . The arrangement according to claim 16 , further comprising
a mineral flotation circuit arranged to treat ore particles suspended in a slurry by flotation and arranged to separate the slurry into an underflow of a mineral flotation circuit and the overflow of a mineral flotation circuit.

18 . The arrangement according to claim 16 , further comprising
a device arranged to determine a solid matter content of the thickener overflow, and at least one pre-treatment unit arranged to pre-treat the thickener overflow; wherein the pre-treatment unit is a cleaning flotation unit and/or a sand filter unit.

19 . The arrangement according to claim 16 , further comprising
a (secondary) cleaning flotation unit arranged to separate a (secondary) cleaning flotation overflow and to form a (secondary) cleaning flotation underflow.

20 . The arrangement according to claim 16 , further comprising
a (secondary) sand filter unit arranged to produce a filtered electrocoagulation underflow.

21 . The arrangement according to claim 18 , wherein the (secondary) cleaning flotation unit is a dissolved air flotation unit.

Assignees

• Metso Outotec Finland Oy

Inventors

• Jansson Kaj
• Saari Eija

Classifications

• C02F2101/10

  Inorganic compounds · CPC title

• C02F9/00

  Multistage treatment of water, waste water or sewage · CPC title

• B03D1/1431 Primary

  Dissolved air flotation machines · CPC title

• B03D1/02 Primary

  Froth-flotation processes · CPC title

• B03D1/082

  of the froth product, e.g. washing · CPC title