Liquid separation system
A separation system separates a first liquid from a compound liquid. Examples of the compound liquid are seawater, brine, rainwater, wastewater, biofuel precursors, lactic acid, or fruit juice. A plate heat exchanger includes at least one evaporation channel and at least one condensation channel. The compound liquid flows through the evaporation channel where the first liquid evaporates from the compound liquid into a gas. A direct heat exchanger further evaporates the first liquid into the gas. The gas flows from the direct heat exchanger through the condensation channel where the first liquid condenses and is thereby separated from the compound liquid.
1 . A separation system comprising:
a plurality of plates within which is disposed at least one evaporation channel;
a tank arranged to contain a compound liquid and supply the compound liquid to flow along an inner wall of the at least one evaporation channel, wherein the compound liquid comprises a first liquid having a first evaporation potential and a second component having a second evaporation potential;
a gas moving device arranged to move a gas through the at least one evaporation channel, wherein a portion of the first liquid flowing along the inner wall of the at least one evaporation channel evaporates into the gas as the gas moves through the evaporation channel;
a direct heat exchanger in thermal communication with the tank, the direct heat exchanger arranged to transfer heat to the gas and arranged to transfer heat to the compound liquid causing an additional portion of the first liquid in the tank to evaporate into the gas as the gas exits the evaporation channel and enters the direct heat exchanger;
at least one condensation channel disposed within the plurality of plates, the at least one condensation channel in thermal communication with the at least one evaporation channel, the at least one condensation channel arranged to receive the gas as the gas exits the direct heat exchanger and to cause the first liquid to condense from the gas as the gas moves through the at least one condensation channel; and
a condensation receptacle that receives the first liquid after the first liquid condenses within the at least one condensation channel.
2 . The separation system of claim 1 , wherein the compound liquid is a mixture comprising one of: seawater, brine, rainwater, wastewater, and fruit juice.
3 . The separation system of claim 1 , wherein the gas is air.
4 . The separation system of claim 1 , wherein the tank is disposed at an outlet of the at least one evaporation channel and at an inlet of the at least one condensation channel.
5 . The separation system of claim 1 , wherein the direct heat exchanger transfers heat to the gas as the gas flows through the direct heat exchanger.
6 . The separation system of claim 1 , further comprising an evaporation channel receptacle that collects a portion of the compound liquid that does not evaporate in and flows out of the at least one evaporation channel.
7 . The separation system of claim 1 , wherein the at least one evaporation channel has a longitudinal axis oriented parallel to a longitudinal axis of the at least one condensation channel.
8 . The separation system of claim 7 , further comprising a redirection means that redirects the gas exiting the direct heat exchanger into the at least one condensation channel.
9 . The separation system of claim 1 , further comprising a thermoelectric generator in thermal communication with the at least one evaporation channel and the at least one condensation channel.
10 . The separation system of claim 9 , further comprising an electric circuit that supplies power from the thermoelectric generator to the direct heat exchanger.
11 . The separation system of claim 1 , further comprising a heat pump, wherein the heat pump comprises a refrigerant circuit, a compressor, a condenser, an expansion valve, and an evaporator, and wherein heat supplied to the direct heat exchanger is generated by the compressor compressing refrigerant in the refrigerant circuit.
12 . The separation system of claim 11 , wherein the evaporator cools the gas exiting the at least one condensation channel.
13 . The separation system of claim 9 , further comprising an electric circuit that supplies power to a heat pump.
14 . A method of separating a compound fluid, the method comprising:
providing the compound fluid from a tank to at least one evaporation channel, the at least one evaporation channel disposed in a plate heat exchanger, wherein the compound fluid flows along an inner wall of the at least one evaporation channel, and wherein the compound fluid comprises a first liquid having a first evaporation potential and a second component having a second evaporation potential;
providing a gas that flows through the at least one evaporation channel, wherein a portion of the first liquid flowing along the inner wall of the at least one evaporation channel evaporates into the gas as the gas flows through the at least one evaporation channel;
providing the gas as the gas exits the at least one evaporation channel to a direct heat exchanger, wherein the direct heat exchanger provides heat to the gas and provides heat to the compound fluid in the tank causing an additional portion of the first liquid in the tank to evaporate into the gas as the gas flows through the direct heat exchanger;
providing the gas as the gas exits the direct heat exchanger to at least one condensation channel of the plate heat exchanger, the at least one condensation channel in thermal communication with the at least one evaporation channel, wherein the first liquid condenses from the gas as the gas flows through the at least one condensation channel; and
providing the first liquid that condenses in the at least one condensation channel to a condensation receptacle.
15 . The method of claim 14 , wherein the tank is disposed at an outlet of the at least one evaporation channel and at an inlet of the at least one condensation channel.
16 . The method of claim 14 , wherein the direct heat exchanger transfers heat to the gas as the gas flows through the direct heat exchanger.
17 . The method of claim 14 , further comprising redirecting the gas exiting the direct heat exchanger into the at least one condensation channel.
18 . The method of claim 14 , further comprising generating power from a thermoelectric generator in thermal communication with the at least one evaporation channel and the at least one condensation channel.
19 . The method of claim 18 , further comprising supplying the power to the direct heat exchanger.
20 . The method of claim 18 , further comprising supplying the power to a heat pump, wherein the heat pump comprises a refrigerant circuit, a compressor, a condenser, an expansion valve, and an evaporator, wherein heat supplied to the direct heat exchanger is generated by the compressor compressing refrigerant in the refrigerant circuit, and wherein the evaporator cools the gas exiting the at least on condensation channel.