Scale removal in humidification-dehumidification systems

Patent metadata

Field	Value
Publication number	US-10345058-B1
Application number	US-201615355242-A
Country	US
Kind code	B1
Filing date	Nov 18, 2016
Priority date	Nov 18, 2015
Publication date	Jul 9, 2019
Grant date	Jul 9, 2019

Abstract

Systems and methods for the removal of scale in humidification-dehumidification desalination apparatuses are generally described.

First claim

What is claimed is:

1. A method for removing scale from a heat exchanger of a humidification-dehumidification desalination apparatus, comprising:
transporting a liquid composition comprising a multidentate ligand from a source of the liquid composition through a fluidic pathway of the heat exchanger to at least partially remove the scale from the heat exchanger, the fluidic pathway of the heat exchanger fluidically connected to an inlet of a humidifier of the humidification-dehumidification desalination apparatus, the humidifier of the humidification-dehumidification desalination apparatus being fluidically connected to a dehumidifier of the humidification-dehumidification desalination apparatus;
during at least a portion of time during which the liquid composition is transported through the fluidic pathway of the heat exchanger:
determining a measure indicative of an amount of the multidentate ligand that remains active within the liquid composition; and
adjusting at least one of a flow rate of the liquid composition and a level of active multidentate ligand within the liquid composition based at least in part upon the determination of the measure indicative of the amount of the multidentate ligand that remains active within the liquid composition.

2. The method of claim 1 , further comprising recycling at least a portion of the liquid composition from the fluidic pathway of the heat exchanger back to the source of the liquid composition.

3. The method of claim 1 , wherein determining a measure indicative of an amount of the multidentate ligand that remains active comprises adding a cation to the liquid composition and subsequently determining a measure indicative of an amount of the cation that does not form a complex with the multidentate ligand.

4. The method of claim 1 , comprising, during at least a portion of time during which the liquid composition is transported through the fluidic pathway of the heat exchanger, adjusting a flow rate of the liquid composition based at least in part upon the determination of the measure indicative of the amount of the multidentate ligand that remains active within the liquid composition.

5. The method of claim 1 , comprising, during at least a portion of time during which the liquid composition is transported through the fluidic pathway of the heat exchanger, adjusting a level of active multidentate ligand within the liquid composition based at least in part upon the determination of the measure indicative of the amount of the multidentate ligand that remains active within the liquid composition.

6. The method of claim 1 , wherein:
transporting the liquid composition comprising the multidentate ligand is part of a cleaning process performed after a desalination process; and
the desalination process comprises:
transporting an aqueous stream containing at least one dissolved salt through the fluidic pathway of the heat exchanger and subsequently through the humidifier of the humidification-dehumidification desalination apparatus such that at least a portion of the water from the aqueous stream is evaporated, within the humidifier, from the aqueous stream to produce a concentrated stream enriched in the at least one dissolved salt relative to the aqueous stream transported to the humidifier and a humidified gaseous stream; and
condensing, within the dehumidifier of the humidification-dehumidification desalination apparatus, water from the humidified gaseous stream to produce a water-containing stream and a dehumidified gaseous stream.

7. The method of claim 1 , wherein transporting the liquid composition comprising the multidentate ligand through the fluidic pathway of the heat exchanger removes at least about 50 wt % of scale that was present within the heat exchanger prior to transporting the liquid composition comprising the multidentate ligand through the fluidic pathway of the heat exchanger.

8. The method of claim 1 , wherein the scale comprises a salt comprising at least one of Mg 2+ , Ca 2+ , Sr 2+ , Ba 2+ , a carbonate anion, a bicarbonate anion, a sulfate anion, a bisulfate anion, dissolved silica, and/or a hydroxide anion.

9. The method of claim 1 , wherein the multidentate ligand comprises diethylenetriaminepentaacetic acid (DTPA).

10. The method of claim 1 , wherein the liquid composition transported through the fluidic pathway of the heat exchanger comprises oxalate anions.

11. The method of claim 1 , wherein the liquid composition transported through the fluidic pathway of the heat exchanger has a pH of at least about 8.

12. The method of claim 1 , wherein the humidifier contains packing.

13. The method of claim 1 , wherein the humidifier is a bubble-column humidifier.

14. The method of claim 2 , wherein the fluidic pathway is a first fluidic pathway, and during at least a portion of the time during which the liquid composition is transported through the first fluidic pathway of the heat exchanger, heat is transferred from a second fluidic pathway of the heat exchanger to at least a portion of the liquid composition.

15. The method of claim 2 , wherein the heat exchanger is a first heat exchanger, and during at least a portion of the time during which the liquid composition is transported through the fluidic pathway of the first heat exchanger, heat is transferred from a second heat exchanger to at least a portion of the liquid composition, the second heat exchanger fluidically connected to the dehumidifier of the humidification-dehumidification desalination apparatus.

16. The method of claim 3 , wherein determining a measure indicative of an amount of the cation that does not form a complex with the multidentate ligand comprises measuring an amount of the cation that remains dissociated within the liquid composition.

17. The method of claim 6 , wherein a volumetric flow rate of the aqueous stream transported through the fluidic pathway of the heat exchanger during the desalination process is at least about 5 times a volumetric flow rate of the liquid composition comprising the multidentate ligand transported through the fluidic pathway of the heat exchanger during the cleaning process.

18. The method of claim 15 , wherein the second heat exchanger transfers heat from water condensed from a gaseous stream within the dehumidifier of the humidification-dehumidification desalination apparatus to the portion of the liquid composition.

19. The method of claim 15 , wherein the heat that is transferred to the portion of the liquid composition raises the temperature of the portion of the liquid composition by at least 1° C., relative to the initial temperature of the liquid composition at the source.

20. The method of claim 15 , wherein the heat that is transferred to the portion of the liquid composition raises the temperature of the portion of the liquid composition by at least 1° C., relative to the temperature the liquid composition would have in the absence of the heat transfer but under otherwise identical conditions.

21. The method of claim 17 , wherein the volumetric flow rate of the aqueous stream transported through the fluidic pathway of the heat exchanger during the desalination process is less than or equal to about 100 times the volumetric flow rate of the liquid composition comprising the multidentate ligand transported through the fluidic pathway of the heat exchanger during the cleaning process.

Assignees

• Gradiant Corp

Inventors

• St John Maximus G
• Andrews Jonn-Ross
• Govindan Prakash Narayan

Classifications

• F28G9/00 Primary

  Cleaning by flushing or washing, e.g. with chemical solvents (appliances using jets of fluid for removing debris F28G1/16, F28G3/16) · CPC title

• C02F2103/10

  from quarries or from mining activities · CPC title

• B01D1/0011 Primary

  Heating features · CPC title

• B01D5/003

  within column(s) · CPC title

• B01D5/006

  with evaporation or distillation · CPC title