Si removal from aqueous streams of minerals processing plants
A method for removing soluble and/or colloidal Si-compounds from an aqueous stream of a minerals processing plant is provided. The method includes adding coagulant(s) and/or flocculant(s) and/or flotation chemical(s) to the aqueous stream in order to facilitate formation of flocs comprising at least some of the Si-compounds, and in order to form a treated aqueous stream, subjecting the treated aqueous stream to cleaning flotation in order to separate at least some of the Si-compounds as a cleaning flotation overflow, and removing the cleaning flotation overflow. The cleaning flotation comprises gas bubbles, at least 90% of the gas bubbles having a diameter of from 0.2 to 250 μm.
1 . A method for removing soluble and/or colloidal Si-compounds from an aqueous stream of a minerals processing plant, the method comprising:
adding coagulant(s) and/or flocculant(s) and/or flotation chemical(s) to the aqueous stream in order to facilitate formation of flocs comprising at least some of the Si-compounds, and in order to form a treated aqueous stream;
subjecting the treated aqueous stream to cleaning flotation in order to separate at least some of the Si-compounds as a cleaning flotation overflow; and
removing the cleaning flotation overflow,
wherein the cleaning flotation comprises gas bubbles, at least 90% of the gas bubbles having a diameter of from 0.2 to 250 μm, wherein the aqueous stream comprises water obtained from dewatering equipment, wherein the aqueous stream obtained from the dewatering equipment originates from a flotation arrangement comprising a mineral flotation circuit arranged to treat ore particles suspended in a slurry by flotation for recovery of ore.
2 . The method according to claim 1 , wherein the dewatering equipment comprises a sedimentation device or a filter.
3 . The method according to claim 1 , wherein the dewatering equipment comprises a sedimentation device that is a thickener.
4 . The method according to claim 1 , wherein the aqueous stream comprises at least a part of a stream obtained from the dewatering equipment.
5 . The method according to claim 1 , wherein the flotation arrangement is arranged to recover Ni and/or Cu.
6 . The method according to claim 1 , wherein the mineral flotation circuit of the flotation arrangement comprises a first mineral flotation circuit arranged to recover Cu and a second mineral flotation circuit arranged to recover Ni.
7 . The method according to claim 1 , wherein the step of subjecting the treated aqueous stream to cleaning flotation creates a cleaning flotation underflow, wherein the method further comprises recirculating at least part of the cleaning flotation underflow back to the flotation arrangement.
8 . The method according to claim 1 , wherein at least one coagulant is added to the aqueous stream and the at least one coagulant comprises an aluminum salt.
9 . The method according to claim 1 , wherein at least one coagulant is added to the aqueous stream and the at least one coagulant comprises an iron salt.
10 . The method according claim 1 , wherein pH of the aqueous stream is adjusted to be in a range of 4.5-10 prior to subjecting the treated aqueous stream to the cleaning flotation.
11 . The method according to claim 1 , wherein the aqueous stream comprises Fe complexed with Si, and the method comprises removing at least some of the Fe from the aqueous stream.
12 . The method according to claim 1 , wherein the cleaning flotation comprises a dissolved air flotation method step.
13 . An arrangement for removing soluble and/or colloidal Si-compounds from an aqueous stream of a minerals processing plant, comprising:
a flotation arrangement comprising a mineral flotation circuit arranged to treat ore particles suspended in a slurry by flotation for recovery of ore;
dewatering equipment arranged to receive the aqueous stream from the flotation arrangement;
a mixing system arranged to provide the aqueous stream from the dewatering equipment with coagulant(s) and/or flocculant(s) and/or flotation chemical(s), and
a cleaning flotation unit arranged to receive the aqueous stream from the mixing system and to separate at least some of the Si-compounds from the aqueous stream as a cleaning flotation overflow and to form a residual process water as a cleaning flotation underflow.
14 . The arrangement according to claim 13 , wherein the dewatering equipment comprises a sedimentation device or a filter.
15 . The arrangement according to claim 13 , wherein the dewatering equipment comprises a sedimentation device, wherein the sedimentation device is a thickener.
16 . The arrangement according to claim 13 , wherein the cleaning flotation unit is a dissolved air flotation unit.