Compact wastewater concentrator using waste heat
A compact and portable liquid concentrator includes a gas inlet, a gas exit and a flow corridor connecting the gas inlet and the gas exit, wherein the flow corridor includes a narrowed portion that accelerates the gas through the flow corridor. A liquid inlet injects liquid into the gas stream at a point prior to the narrowed portion so that the gas-liquid mixture is thoroughly mixed within the flow corridor, causing a portion of the liquid to be evaporated. A demister or fluid scrubber downstream of the narrowed portion removes entrained liquid droplets from the gas stream and re-circulates the removed liquid to the liquid inlet through a re-circulating circuit. Fresh liquid to be concentrated is also introduced into the re-circulating circuit at a rate sufficient to offset the amount of liquid evaporated in the flow corridor.
1. A liquid concentrator system comprising:
a concentrator including a mixing corridor connectable to a stream of heated gas and having a narrowed portion, and a liquid inlet to introduce liquid into the mixing corridor upstream of the narrowed portion,
the narrowed portion of the mixing corridor defining a direct heat transfer evaporator having an operational state wherein the stream of heated gas is accelerated and mixes with the liquid from the liquid inlet to define a gas-liquid mixture as a portion, but not all, of the liquid evaporates and is absorbed by the heated gas,
a cyclonic chamber coupled to the mixing corridor, the cyclonic chamber including a separation passage in which entrained liquid droplets are removed from the gas-liquid mixture flowing in the separation passage, and a reservoir that collects the entrained liquid droplets removed from the gas-liquid mixture; and
a re-circulating circuit disposed between the reservoir and the liquid inlet to transport liquid to the mixing corridor.
2. The liquid concentrator system of claim 1 , further comprising an unconcentrated liquid inlet through which unconcentrated liquid flows to the mixing corridor.
3. The liquid concentrator system of claim 2 , wherein the unconcentrated liquid inlet is disposed in the re-circulating circuit between the reservoir and the liquid inlet.
4. The liquid concentrator system of claim 2 , wherein the unconcentrated liquid inlet is disposed in the mixing corridor.
5. The liquid concentrator system of claim 1 , wherein the concentrator includes an adjustable flow restriction disposed in the narrowed portion of the mixing corridor, the adjustable flow restriction adjustable to alter gas flow through the mixing corridor.
6. The liquid concentrator system of claim 1 , further comprising a fan coupled to the cyclonic chamber to pull the stream of heated gas and the gas-liquid mixture in turn through the mixing corridor and the separation passage.
7. The liquid concentrator system of claim 1 , wherein the liquid introduced through the liquid inlet is landfill leachate collected from a landfill.
8. A liquid concentrator system comprising:
a mixing corridor connectable to a stream of heated gas and having a narrowed portion;
a liquid inlet to introduce liquid droplets into the mixing corridor upstream of the narrowed portion,
the narrowed portion of the mixing corridor defining a direct heat transfer evaporator having an operational state wherein the stream of heated gas is accelerated and mixes with the liquid droplets from the one or more liquid inlets to define a gas-liquid mixture as a portion, but not all, of the liquid in the liquid droplets evaporates and is absorbed by the heated gas,
a cyclonic chamber coupled to the mixing corridor, the cyclonic chamber including a separation passage in which entrained droplets are removed from the gas-liquid mixture flowing in the separation passage, and a reservoir that collects the entrained liquid droplets removed from the gas-liquid mixture;
a re-circulating circuit disposed between the reservoir and the liquid inlet to transport liquid to the mixing corridor; and
a fan coupled to the separation passage to pull the stream of heated gas and the gas-liquid mixture in turn through the mixing corridor and the separation passage.
9. The liquid concentrator system of claim 8 , further comprising an unconcentrated liquid inlet through which unconcentrated liquid flows to the mixing corridor.
10. The liquid concentrator system of claim 9 , wherein the unconcentrated liquid inlet is disposed in the re-circulating circuit between the reservoir and the liquid inlet.
11. The liquid concentrator system of claim 9 , wherein the unconcentrated liquid inlet is disposed in the mixing corridor.
12. The liquid concentrator system of claim 8 , further comprising an adjustable flow restriction disposed in the narrowed portion of the mixing corridor, the adjustable flow restriction adjustable to alter gas flow through the mixing corridor.
13. The liquid concentrator system of claim 8 , further comprising a flooded elbow connected downstream of the narrowed portion of the mixing corridor, the flooded elbow changing direction of the gas flowing in the mixing corridor.
14. A concentrator system utilizing only fluid-to-fluid direct heat exchange, the concentrator system comprising:
a mixing corridor connectable to a stream of heated gas and having a narrowed portion, and including an adjustable flow restriction disposed in the narrowed portion of the mixing corridor, the adjustable flow restriction adjustable to alter gas flow through the mixing corridor;
a nozzle to inject liquid droplets into the mixing corridor upstream of the narrowed portion,
the narrowed portion of the mixing corridor defining a direct heat transfer evaporator having an operational state wherein the stream of heated gas is accelerated and mixes with the liquid droplets from the nozzle to define a gas-liquid mixture as a portion, but not all, of the liquid in the liquid droplets evaporates and is absorbed by the heated gas,
a cyclonic chamber coupled to the mixing corridor, the cyclonic chamber including a separation passage in which entrained droplets are removed from the gas-liquid mixture flowing in the separation passage, and a reservoir that collects the entrained liquid removed from the gas-liquid mixture;
a re-circulating circuit disposed between the reservoir and the nozzle to transport liquid to the mixing corridor; and
a fan coupled to the separation passage to pull the stream of heated gas and the gas-liquid mixture in turn through the mixing corridor and the separation passage.
15. The concentrator system of claim 14 , further comprising an unconcentrated liquid inlet through which unconcentrated liquid flows to the mixing corridor.
16. The concentrator system of claim 15 , wherein the unconcentrated liquid inlet is disposed in the re-circulating circuit between the reservoir and the liquid inlet.
17. The concentrator system of claim 15 , wherein the unconcentrated liquid inlet is disposed in the mixing corridor.
18. The concentrator system of claim 14 , wherein the adjustable flow restriction is an adjustable venturi device capable of changing the size or shape of the narrowed portion of the mixing corridor.
19. The concentrator system of claim 14 , further comprising a flooded elbow connected downstream of the narrowed portion of the mixing corridor, the flooded elbow changing direction of the gas flowing in the mixing corridor.
20. The concentrator system of claim 14 , wherein the stream of heated gas passing through the narrowed portion is at a temperature in the range of 150 to 215° F. in the operational state of the evaporator.