Staged regenerated liquid desiccant dehumidification systems
A system comprises a liquid desiccant regeneration system, a first air contactor stage, and a second air contactor stage. The regeneration system has a first stage with a first concentration output and first diluted output, and a second stage with a second concentration output, different from the first concentration output, and a second diluted output. The first air contactor stage is coupled to the first concentrated output to form a first output air stream having a reduced water content and a first diluted air contactor output. The second air contactor stage is coupled to the second concentrated output to form a second output air stream having a reduced water content and a second diluted air contactor output. Both diluted air contactor outputs are recirculated into the regeneration system, and the output air streams are combined.
1. A system, comprising:
a liquid desiccant regenerator including a first stage configured to generate a first concentrated output stream having a first concentration of liquid desiccant, and a second stage configured to generate a second concentrated output stream having a second concentration of liquid desiccant different than the first concentration;
a first air contactor stage configured to be coupled to the first concentrated output stream to dispose a first input air stream having a first water content by percent mass in fluid communication with the first concentrated output stream to form a first output air stream having a second water content by percent mass lower than the first water content and a first diluted air contactor output stream, wherein the first diluted air contactor output stream is circulated back into the liquid desiccant regenerator; and
a second air contactor stage coupled to the second concentrated output stream to dispose disposing a second input air stream having a third water content by percent mass in fluid communication with the second concentrated output stream to form a second output air stream having a fourth water content by percent mass lower than the third water content and a second diluted air contactor output stream, wherein the second diluted air contactor output stream is circulated back into the liquid desiccant regenerator and the first and second output air streams are combined.
2. The system of claim 1 , wherein the liquid desiccant regenerator is an electrochemical regenerator configured to be driven by an electric potential.
3. The system of claim 1 , wherein the liquid desiccant regenerator is an electrochemical regenerator configured to be driven by an electric potential that engenders faradaic reactions happening at two different electrodes and material undergoing the faradaic reactions is circulated from one electrode to the other and back again.
4. The system of claim 1 , wherein the liquid desiccant regenerator is configured to be driven by reverse osmosis.
5. The system of claim 1 , wherein the liquid desiccant regenerator is a thermal regenerator.
6. The system of claim 1 , wherein the third water content by percent mass is different from the first water content by percent mass.
7. The system of claim 1 , wherein the first air contactor stage and the second air contactor stage are separate air contactors.
8. The system of claim 1 , wherein the first air contactor stage and the second air contactor stage are stages of the same air contactor.
9. The system of claim 1 , further comprising a heat remover fluidly coupled to at least one of the first air contactor stage or the second air contactor stage to remove heat from at least one of the first input air stream or the second input air stream.
10. The system of claim 9 , wherein the heat remover includes a first stage configured to be coupled to the first regenerated output stream and a second stage configured to be coupled to the second regenerated output stream.
11. The system of claim 9 , wherein the heat remover is configured to utilize at least one of evaporative cooling or dry cooling.
12. The system of claim 9 , wherein the heat remover is configured to utilize vapor compression.
13. The system of claim 9 , wherein the heat remover is configured to be coupled to the at least two streams within at least one of the first and second air contactor stages.
14. The system of claim 1 , wherein the liquid desiccant regenerator includes a third stage coupled to at least one of the first stage or second stage.
15. The system of claim 1 , wherein at least one of the first or second diluted output streams is configured to be fluidically coupled to a third air contactor stage that is configured to produce a concentrated air contactor output stream having an increased salt concentration as compared to at least one of the first and second diluted output streams and to increase the water content by mass of a third input air stream, wherein the concentrated air contactor output stream is circulated back into the liquid desiccant regenerator.
16. An air contactor, comprising:
a first input stream of liquid desiccant having a first concentration of desiccant;
a second input stream of liquid desiccant having a second concentration of desiccant where the second concentration is higher than the first concentration; and
an input air stream disposed in fluid communication with the first input stream of liquid desiccant and with the second input stream of liquid desiccant to produce a diluted output stream of liquid desiccant and an output air stream having a water content by mass lower than that of the input air stream.
17. The air contactor of claim 16 , wherein the input air stream is exposed to at least one of the first and second input streams of liquid desiccant through an intervening interface.
18. The air contactor of claim 16 , wherein the diluted output stream is coupled to a liquid desiccant regeneration system configured to provide the first and second input streams of liquid desiccant.
19. The air contactor of claim 16 , further comprising a heat remover configured to be coupled to the first and second input streams.
20. A system, comprising:
a first liquid desiccant regenerator configured to produce a first concentrated output stream having a first concentration of liquid desiccant;
a second liquid desiccant regenerator configured to be coupled to the first concentrated output stream and configured to produce a second concentrated output stream having a second concentration of liquid desiccant different than the first concentration;
a first air contactor stage configured to be coupled to the first concentrated output stream to dispose a first input air stream having a first water content by mass in fluid communication with the first concentrated output stream to form a first output air stream having a second water content by mass lower than the first water content and a first diluted output stream, wherein the first diluted output stream is circulated back into the first liquid desiccant regeneration system; and
a second air contactor stage configured to be coupled to the second concentrated output stream to dispose a second input air stream having a third water content by mass in fluid communication with the second concentrated output stream to form a second output air stream having a fourth water content by mass lower than the third water content and a second diluted output stream, wherein the second diluted output stream is circulated back into the second liquid desiccant regenerator and the first and second output air streams are combined.
21. The system of claim 20 , wherein the first air contactor stage and the second air contactor stage are separate air contactors.
22. The system of claim 20 , wherein the first air contactor stage and the second air contactor stage are stages of the same air contactor.