Variable desiccant control energy exchange system and method
US-2016298865-A1 · Oct 13, 2016 · US
US12385654B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12385654-B2 |
| Application number | US-201716606673-A |
| Country | US |
| Kind code | B2 |
| Filing date | Apr 18, 2017 |
| Priority date | Apr 18, 2017 |
| Publication date | Aug 12, 2025 |
| Grant date | Aug 12, 2025 |
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A conditioning system includes a first plenum and a second plenum. The second plenum receives heated air from an enclosed space and supplies cooled air to the space. The system also includes a first liquid-to-air membrane energy exchanger (LAMEE 1 ) arranged inside the first plenum. LAMEE 1 is configured to use a liquid desiccant to lower an enthalpy of the first air stream. A LAMEE 2 is arranged inside the first plenum downstream of LAMEE 1 . LAMEE 2 is configured to use the first air stream to evaporatively cool water flowing through LAMEE 2 . A first LAHX (LAHX 1 ) is arranged inside the second plenum. LAHX 1 is configured to directly and sensibly cool the second air stream using a first cooling fluid. A second LAHX (LAHX 2 ) is in fluid communication with LAMEE 1 and is configured to receive the liquid desiccant from LAMEE 1 and cool the liquid desiccant using outdoor air.
Opening claim text (preview).
What is claimed is: 1. A system for controlling conditions in an enclosed space, the system comprising: a first plenum configured to direct a first air stream from a first inlet to a first outlet; a second plenum configured to direct a second air stream from a second inlet to a second outlet, the second inlet receiving heated air from the space and the second outlet supplying cooled air to the space; a first liquid-to-air membrane energy exchanger (LAMEE 1 ) arranged inside the first plenum, LAMEE 1 configured to use a liquid desiccant to lower an enthalpy of the first air stream; a second LAMEE (LAMEE 2 ) arranged inside the first plenum downstream of LAMEE 1 , LAMEE 2 configured to use the first air stream to evaporatively cool water flowing through LAMEE 2 ; a first liquid-to-air heat exchanger (LAHX 1 ) arranged inside the second plenum, LAHX 1 configured to directly and sensibly cool the second air stream using a first cooling fluid; and a second LAHX (LAHX 2 ) in fluid communication with LAMEE 1 , LAHX 2 being configured to receive the liquid desiccant from LAMEE 1 and cool the liquid desiccant using outdoor air. 2. The system of claim 1 , wherein LAMEE 1 is configured to lower the enthalpy of the first air stream by removing water therefrom. 3. The system of claim 1 , wherein LAMEE 1 is configured to lower the enthalpy of the first air stream by removing water therefrom and wherein at least a portion of the water flowing through LAMEE 2 comprises the water removed from the first air stream by LAMEE 1 . 4. The system of claim 1 , further comprising a pre-cooler coil arranged inside the first plenum upstream of LAMEE 2 , the pre-cooler coil configured to condition the first air stream prior to the first air stream entering LAMEE 2 . 5. The system of claim 4 , wherein the pre-cooler coil is configured to receive at least a portion of the water cooled by LAMEE 2 to condition the first air stream. 6. The system of claim 4 , further comprising a fluid storage tank to store the water received from a fluid outlet of LAMEE 2 . 7. The system of claim 6 , further comprising a mechanical cooling system configured to cool the water in the storage tank using the first cooling fluid. 8. The system of claim 6 , further comprising a liquid-to-liquid heat exchanger (LLHX) configured to cool the water in the storage tank using the first cooling fluid. 9. The system of claim 8 , further comprising a third LAHX (LAHX 3 ), LAHX 3 arranged inside of the first plenum downstream of LAMEE 2 and configured to cool at least one of the water and the first cooling fluid using the first air stream. 10. The system of claim 9 , further comprising: a first fluid circuit configured to transport the water from a fluid outlet of LAMEE 2 , through the LLHX and return the water to a fluid inlet of LAMEE 2 ; and a second fluid circuit fluidically isolated from the first fluid circuit, the second fluid circuit configured to transport the first cooling fluid from an outlet of LAHX 3 through the LLHX to an inlet of LAHX 1 , and return the first cooling fluid from the fluid outlet of LAHX 1 to a fluid inlet of LAHX 3 . 11. The system of claim 1 , further comprising a direct exchange (DX) coil arranged inside the second plenum downstream of LAHX 1 , the DX coil being configured to cool the second air stream using a second cooling fluid flowing there through. 12. The system of claim 1 , wherein LAMEE 1 is configured to lower the enthalpy of the first air stream by removing water and heat therefrom, a temperature of the liquid desiccant at a fluid inlet of LAMEE 1 being lower than a temperature of the liquid desiccant at a fluid outlet of LAMEE 1 . 13. The system of claim 1 , further comprising a third LAHX (LAHX 3 ) arranged inside of the first plenum downstream of LAMEE 2 and configured to receive the first cooling fluid from LAHX 1 and to cool the first cooling fluid using the first air stream. 14. The system of claim 13 , wherein: the first cooling fluid is the water; and the water flows from an outlet of the LAHX 3 to an inlet of the LAMEE 2 . 15. A system for controlling conditions in an enclosed space, the system comprising: a scavenger plenum configured to direct scavenger air from a scavenger inlet to a scavenger outlet; a process plenum configured to direct process air from a process inlet to a process outlet, the process inlet receiving heated air from the space and the process outlet supplying cooled air to the space; a first liquid-to-air membrane energy exchanger (LAMEE 1 ) arranged inside the scavenger plenum, LAMEE 1 configured to use a first fluid flowing through LAMEE 1 to reduce a humidity of the scavenger air, a first concentration of water in the scavenger air at an air inlet of LAMEE 1 being higher than a second concentration of water in the scavenger air at an air outlet of LAMEE 1 ; an evaporative cooler arranged inside the scavenger plenum downstream of LAMEE 1 , the evaporative cooler configured to use the scavenger air to evaporatively cool a second fluid flowing there through, a temperature of the second fluid at a fluid outlet of the evaporative cooler being lower than a temperature of the second fluid at a fluid inlet of the evaporative cooler; a first liquid-to-air heat exchanger (LAHX 1 ) arranged inside the process plenum, LAHX 1 configured to directly and sensibly cool the process air being directed through the process plenum using a third fluid flowing through LAHX 1 ; and a second LAHX (LAHX 2 ), LAHX 2 in fluid communication with LAMEE 1 and configured to receive the first fluid from the LAMEE 1 and cool the first fluid using outdoor air. 16. The system of claim 15 , wherein LAMEE 1 is configured to lower the enthalpy of the scavenger air by removing water therefrom. 17. The system of claim 15 , wherein the second fluid comprises water, and wherein LAMEE 1 is configured to lower the enthalpy of the scavenger air by removing water therefrom, and wherein at least a portion of the water flowing through the evaporative cooler comprises the water removed from the scavenger air by LAMEE 1 . 18. The system of claim 15 , further comprising a pre-cooler coil arranged inside the scavenger plenum upstream of LAMEE 2 , the pre-cooler coil configured to condition the scavenger air prior to the scavenger air entering LAMEE 2 . 19. The system of claim 18 , wherein the pre-cooler coil is configured to receive at least a portion of the second fluid cooled by the evaporative cooler to condition the scavenger air. 20. The system of claim 18 , further comprising a fluid storage tank to store the second fluid received from a fluid outlet of the evaporative cooler. 21. The system of claim 20 , further comprising a mechanical cooling system configured to cool the second fluid in the storage tank using a first cooling fluid. 22. The system of claim 20 , further comprising a liquid-to-liquid heat exchanger (LLHX) configured to cool the second fluid in the storage tank using a first cooling fluid. 23. The system of claim 22 , further comprising a third LAHX (LAHX 3 ), LAHX 3 arranged inside of the scavenger plenum downstream of the evaporative cooler and configured to cool at least one of the second fluid and the first cooling fluid using the scavenger air. 24. The system of claim 23 , further comprising: a first fluid circuit configured to transport the water from a fluid outlet of the evaporative cooler, through the LLHX and
using an intermediate heat-transfer fluid · CPC title
using evaporation · CPC title
using heat exchange fluid storage tanks · CPC title
comprising semi-permeable membrane · CPC title
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