ELECTRODIALYSIS PROCESS FOR HIGH ION REJECTION IN THE PRESENCE OF BORON
Provided are water treatment systems and methods of treating water that include separating boron and concentrating lithium. For example, described are water treatment systems comprising: a first phase comprising a first plurality of electrodialysis units configured to separate boron from a feed stream, and a second phase comprising a second plurality of electrodialysis units, wherein the feed stream of at least one electrodialysis unit of the second plurality of electrodialysis units comprises an outlet brine stream of at least one electrodialysis unit of the first plurality of electrodialysis units, and wherein the second plurality of electrodialysis units are configured to produce a product brine stream achieving 90-99% lithium recovery.
1 . A water treatment system comprising:
a first phase comprising a first plurality of electrodialysis units configured to separate boron from a feed stream, wherein each electrodialysis unit of the first plurality of electrodialysis units comprises an inlet feed stream, an inlet brine stream, an outlet product stream, and an outlet brine stream; and
a second phase comprising a second plurality of electrodialysis units, wherein each electrodialysis unit of the second plurality of electrodialysis units comprises an inlet feed stream, an inlet brine stream, an outlet product stream, and an outlet brine stream,
wherein the feed stream of at least one electrodialysis unit of the second plurality of electrodialysis units comprises an outlet brine stream of at least one electrodialysis unit of the first plurality of electrodialysis units, and
wherein the second plurality of electrodialysis units are configured to produce a product brine stream achieving 90-99% lithium recovery.
2 . The water treatment system of claim 1 , wherein the first phase comprises a first electrodialysis unit, a second electrodialysis unit, and a third electrodialysis unit.
3 . The water treatment system of claim 2 , wherein the inlet feed stream of the first electrodialysis unit of the first phase comprises the feed stream.
4 . The water treatment system of claim 2 , wherein the inlet feed stream of the second electrodialysis unit of the first phase comprises the outlet product stream of the first electrodialysis system of the first phase.
5 . The water treatment system of claim 2 , wherein the inlet feed stream of the third electrodialysis system of the first phase comprises the outlet product stream of the second electrodialysis unit of the first phase.
6 . The water treatment system of claim 2 , wherein the outlet product stream of the third electrodialysis unit of the first phase recovers greater than 95% of the boron ions of the feed stream.
7 . The water treatment system of claim 2 , wherein at least one of the inlet feed stream of the first electrodialysis unit of the first phase, the inlet feed stream of the second electrodialysis unit of the first phase, or the inlet feed stream of the third electrodialysis unit of the first phase are controlled to a pH of 7 or lower.
8 . The water treatment system of claim 2 , wherein the second phase comprises a first electrodialysis unit, a second electrodialysis unit, and a third electrodialysis unit.
9 . The water treatment system of claim 8 , wherein the inlet feed stream of the first electrodialysis system of the second phase comprises at least one of the outlet brine stream of the second electrodialysis unit of the first phase or the outlet brine stream of the third electrodialysis system of the first phase.
10 . The water treatment system of claim 8 , wherein the inlet brine stream of the first electrodialysis unit of the second phase comprises the outlet brine stream of the first electrodialysis unit of the first phase.
11 . The water treatment system of claim 8 , wherein the inlet brine stream of the first electrodialysis unit of the second phase comprises the outlet brine stream of the first electrodialysis unit of the second phase.
12 . The water treatment system of claim 8 , wherein the inlet feed stream of the second electrodialysis unit of the second phase comprises the outlet product stream of the first electrodialysis unit of the second phase.
13 . The water treatment system of claim 8 , wherein the inlet feed stream of the third electrodialysis unit of the second phase comprises the outlet brine stream of the second electrodialysis unit of the second phase.
14 . The water treatment system of claim 8 , wherein the inlet brine stream of the third electrodialysis unit of the second phase comprises the outlet brine stream of the first electrodialysis unit of the second phase.
15 . The water treatment system of claim 8 , wherein the inlet feed stream of the first electrodialysis system of the second phase comprises at least one of the outlet brine stream of the first electrodialysis system of the first phase, the outlet brine stream of the second electrodialysis system of the first phase, or the outlet brine stream of the third electrodialysis system of the first phase.
16 . The water treatment system of claim 8 , wherein the inlet brine stream of the first electrodialysis system of the second phase comprises at least one of the outlet brine stream of the first electrodialysis system of the first phase, the outlet brine stream of the second electrodialysis system of the first phase, or the outlet brine stream of the third electrodialysis system of the first phase.
17 . The water treatment system of claim 8 , wherein the inlet brine stream of the first electrodialysis unit of the second phase comprises the outlet brine stream of the first electrodialysis system of the second phase.
18 . The water treatment system of claim 8 , wherein the inlet feed stream of the third electrodialysis unit of the first phase comprises the outlet product stream of the second electrodialysis unit of the second phase.
19 . A method of separating boron and concentrating lithium comprising:
passing water through a first phase comprising a first plurality of electrodialysis units configured to separate boron from a feed stream, wherein each electrodialysis unit of the first plurality of electrodialysis units comprises an inlet feed stream, an inlet brine stream, an outlet product stream, and an outlet brine stream; and
passing water through a second phase comprising a second plurality of electrodialysis units, wherein each electrodialysis unit of the second plurality of electrodialysis units comprises an inlet feed stream, an inlet brine stream, an outlet product stream, and an outlet brine stream,
wherein the feed stream of at least one electrodialysis unit of the second plurality of electrodialysis units comprises an outlet brine stream of at least one electrodialysis unit of the first plurality of electrodialysis units, and
wherein the second plurality of electrodialysis units are configured to produce a product brine stream achieving 90-99% lithium recovery.
20 . The method of claim 19 , wherein the outlet product stream of the third electrodialysis unit of the first phase recovers greater than 95% of the boron ions of the feed stream.