Atomic capacitor

Information

  • Patent Grant
  • 10650985
  • Patent Number
    10,650,985
  • Date Filed
    Friday, August 24, 2018
    5 years ago
  • Date Issued
    Tuesday, May 12, 2020
    4 years ago
Abstract
This invention describes a capacitor that formed by a charge or species specific membrane material filled with aqueous or non-aqueous liquid with soluble salts dissolved and non-dissolved in solution and contained within the membrane material. When charged, the oppositely charged ion will leave the structure, leaving behind a charged atomic capacitor.
Description
FIELD OF INVENTION

This invention relates to a specially designed capacitor and or capacitor/membrane combination for use in electrochemical devices such as but not limited to capacitive or radial deionization whereby the majority of the capacitance of the system is derived from isolated ions within the charge specific membrane spheres or material.


BACKGROUND OF THE INVENTION
Objects and Advantages of Certain Embodiments

Accordingly, several objects and advantages of our invention are:

    • a) The atomic capacitor can reach a capacitance density of up to 5,000 F/cc or greater which is up to 50 times or greater than state of the art materials.
    • b) The atomic capacitor material can be structured so as to be an integrated electrode/membrane monolith.


SUMMARY OF THE INVENTION

This invention describes a capacitor that is made up of a charge specific membrane material with highly soluble salts dissolved and non-dissolved in solution and surrounded by the charge specific membrane material. Each atomic capacitor containing the ion charged material consists of a porous anionic membrane material with a high concentration of aqueous or non-aqueous solution saturated with high solubility salts and a porous cationic membrane also filled with saturated aqueous or non-aqueous solution. When each is charged, the oppositely charged ion will leave its respective membrane, leaving behind a charged atomic capacitor, ready to reabsorb ions of interest in application.





DRAWINGS—FIGURES


FIG. 1: Purification cycle of electric double layer capacitor deionizer.



FIG. 2: Rejection cycle of electric double layer capacitor deionizer.



FIG. 3: Atomic capacitor spheres filled with salt in aqueous or non-aqueous or solution.



FIG. 4: Charge specific membrane material with voids filled with salt in aqueous or non-aqueous solution.



FIG. 5: Carbon electrode material containing hollow spheres filled with salt in aqueous or non-aqueous or solution.



FIG. 6: Integrated carbon electrode and charge specific membrane material with voids filled with salt in aqueous or non-aqueous solution and carbon.



FIG. 7: Table of highly soluble aqueous salts and estimated capacitance.





DRAWINGS—REFERENCE NUMERALS




  • 11—Cationic membrane sphere shell


  • 12—Anionic membrane sphere shell


  • 13—solution with dissolved and non-dissolved salt.


  • 15—cations


  • 17—anions


  • 19—electric field generator


  • 31—charge specific membrane material


  • 33—capacitor spheres


  • 35—cationic spheres


  • 37—anionic spheres


  • 51—carbon electrode


  • 55—current collector


  • 71—capacitor


  • 73—Mixed carbon electrode, membrane, and capacitor spheres in one layer


  • 75—Super capacitor carbon



DETAILED DESCRIPTION OF THE INVENTION

In an electric double layer capacitor system such as but not limited to the concentric capacitive deionization Radial Deionization device from Atlantis Technologies, two oppositely charged capacitors are separated by a dielectric flow channel and two charge specific membranes. In the purification mode, cations are attracted to the negatively charged carbon electrode and anions are attracted to the positively charged carbon electrode. Each type of ion passes through a membrane whose charge affinity is the same as the ion (positive or negative). After it passes through, it adsorbs onto the surface of the carbon particles that make up the carbon electrode. See FIG. 1.


Once the purification cycle is complete or the carbon electrodes are full of their respective ions, the polarity of the electric double layer capacitor is switched and the ions are pushed away from the carbon, through the membrane, into the spacer and up against the opposite side membrane. Because the membranes are charge specific, these rejected ions cannot pass through and adsorb onto the other carbon electrode and flush out of the system. See FIG. 2.


This invention proposes the partial or complete replacement of the carbon electrodes and charge specific membrane with charge specific membrane material that contains aqueous or non-aqueous solution that is saturated with high solubility salts such as but not limited to sodium chloride, antimony trichloride, ammonium salts, antimony trifluoride, zinc chloride, zinc bromide, indium bromide, or any other high solubility salt that dissolved and non-dissolved in aqueous or non-aqueous solution.


When the atomic capacitor material is initially made, the cations and anions from the highly soluble salt are in solution and the solution is contained within the charge specific membrane material 11 or 12, as shown in FIG. 3, which shows atomic capacitor spheres filled with salt in aqueous or non-aqueous or solution. The membrane material could be a porous layer of material with a multitude of holes for the aqueous or non-aqueous solution to reside 31, as shown in FIG. 4, which shows charge specific membrane material with voids filled with salt in aqueous or non-aqueous solution. This combination could also be in the form of hollow spheres containing the salt laden liquid 33, as shown in FIG. 5, which shows carbon electrode material containing hollow spheres filled with salt in aqueous or non-aqueous or solution, or FIG. 6, which shows an integrated carbon electrode and charge specific membrane material with voids filled with salt in aqueous or non-aqueous solution. In either case, it is important that the outside of the material be sealed and that there is no significant pathway for the liquid to leave the interior of the membrane sponge or sphere.


An electric double layer capacitor is formed with one of the charge specific membrane compositions constituting one electrode, and the opposite polarity membrane composition constituting the other as described in the attached drawing as optional. When an initial activation charge is applied to the device in the same orientation as the charge specific membranes (anionic side is charged negative, cationic side charged positive), the anions travel out of the anionic and move into the dielectric spacer towards the positively charged electrode. The cations leave the cationic and travel towards the anionic side. This polarity orientation is same as the “reject cycle”.


By the end of this initial activation charging cycle, most or all of the anions 17 and cations 15 have left the anionic and cationic spheres or pockets respectively and are residing in the dielectric spacer. With the polarity intact, the ejected ions are flushed out of the system by a liquid flowing through the flow channel/dielectric spacer.


After this initial charging cycle, each sphere is now charged to the opposite polarity due to the inability of the trapped ions to leave the sphere or pocket and is now ready to operate on a continuous basis. To operate, the polarity is switched to the “clean cycle” and the previously ejected ion type (anionic or cationic) is reabsorbed by the sphere from the solution flowing through the dielectric spacer flow channel.


The size, shape, and composition of the atomic capacitors can vary. Capacitor can be a stand-alone structure containing a membrane shell filled with aqueous or non-aqueous liquid containing dissolved and undissolved salts (capacitor mixture), as shown in FIG. 6. It can also be a void within a membrane structure which is also filled with capacitor mixture, as shown in FIG. 4. The shape can range from spherical to any shape that would hold volume. The total volume of the capacitor can be as small as the size of a one salt molecule with minimum liquid up to many milliliters. The wall thickness of a stand-alone structure could be the minimum to contain the liquid such as the length of a membrane molecule, a single layer of graphene or other high strength material.


Example 1

An electrode/membrane combination consisting of a porous charge specific membrane material that is filled with a highly soluble salts such as but not limited to metal halides such as sodium chloride, antimony trichloride, ammonium salts, antimony trifluoride, zinc chloride, zinc bromide, indium bromide, or any other high solubility salt that dissolved and non-dissolved in aqueous or non-aqueous solution.


Example 2

Charge specific membrane hollow spheres consisting of charge specific membrane material that is filled with a highly soluble salt such as but not limited to sodium chloride, antimony trichloride, ammonium salts, antimony trifluoride, zinc chloride, zinc bromide, indium bromide, or any other high solubility salt that dissolved and non-dissolved in aqueous or non-aqueous or solution. These spheres can be incorporated into materials used within an electrochemical device such as capacitive deionization systems.


Example 3

An electrode/membrane combination consisting of a porous charge specific membrane material that is filled with a highly soluble salt such as but not limited to sodium chloride, antimony trichloride, ammonium salts, antimony trifluoride, zinc chloride, zinc bromide, indium bromide, or any other high solubility salt that dissolved and non-dissolved in aqueous or non-aqueous solution in combination with traditional capacitance materials such as but not limited to carbon black, activated carbon, and PTFE fibrillating materials.


Example 4

Charge specific membrane hollow spheres consisting of charge specific membrane material that is filled with a highly soluble salt such as but not limited to sodium chloride, antimony trichloride, ammonium salts, antimony trifluoride, zinc chloride, zinc bromide, indium bromide, or any other high solubility salt that dissolved and non-dissolved in aqueous or non-aqueous solution. These spheres can be adhered in some fashion to the current collector with conductive adhesive and act as both the capacitor material and charge specific membrane.

Claims
  • 1. A method of treating an aqueous stream with a capacitive deionization device, the method comprising: feeding the aqueous stream to a dielectric spacer flow channel of the capacitive deionization device, wherein the aqueous stream comprises at least one anionic species and at least one cationic species; andtreating the aqueous stream with the capacitive deionization device to produce a treated aqueous stream;wherein the capacitive deionization device comprises: a first electrode comprising a first plurality of voids;a positive charge specific membrane material positioned proximate the first electrode and proximate the dielectric spacer flow channel;a plurality of anions from a first salt solution residing in the first plurality of voids;a negative charge specific membrane material, the negative charge specific membrane material positioned proximate the dielectric spacer flow channel opposite to the positive charge specific membrane material;a second electrode comprising a second plurality of voids, the second electrode being positioned proximate the negative charge specific membrane material opposite to the dielectric spacer flow channel; anda plurality of cations from a second salt solution residing in the second plurality of voids.
  • 2. The method of claim 1, wherein the positive charge specific membrane material comprises a first membrane layer between the first electrode and the dielectric spacer flow channel and/or wherein the negative charge specific membrane material comprises a second membrane layer between the second electrode and the dielectric spacer flow channel.
  • 3. The method of claim 2, wherein the negative charge specific membrane material comprises a second membrane layer positioned between the second electrode and the dielectric spacer flow channel.
  • 4. The method of claim 1, wherein at least one of the first salt solution and the second salt solution comprises a salt selected from the group consisting of sodium chloride, antimony trichloride, an ammonium salt, antimony trifluoride, zinc chloride, zinc bromide, and indium bromide.
  • 5. The method of claim 1, wherein at least one of the first salt solution and the second salt solution has a capacitance density of 50,000 F/cc or greater.
  • 6. The method of claim 1, wherein at least one of the first salt solution and the second salt solution is saturated.
  • 7. The method of claim 1, wherein each of the first salt solution and the second salt solution comprises a salt selected from the group consisting of sodium chloride, antimony trichloride, an ammonium salt, antimony trifluoride, zinc chloride, zinc bromide, and indium bromide.
  • 8. The method of claim 1, wherein each of the first salt solution and the second salt solution has a capacitance density of 50,000 F/cc or greater.
  • 9. A method of operating a capacitive deionization device, the method comprising: feeding a first aqueous stream comprising first cations and first anions to a dielectric spacer flow channel of the capacitive deionization device, wherein the capacitive deionization device comprises: a first electrode comprising a first plurality of voids;a positive charge specific membrane material positioned proximate the first electrode and proximate the dielectric spacer flow channel;a plurality of second anions from a first salt solution residing in the first plurality of voids;a negative charge specific membrane material, the negative charge specific membrane material positioned proximate the dielectric spacer flow channel opposite to the positive charge specific membrane material;a second electrode comprising a second plurality of voids, the second electrode being positioned proximate to the negative charge specific membrane material opposite to the dielectric spacer flow channel; anda plurality of second cations from a second salt solution residing in the second plurality of voids;while operating in a purification cycle, applying a negative charge to the first electrode to cause at least a portion of the first cations in the first aqueous stream to pass through the positive charge specific membrane material; andwhile operating in the purification cycle, applying a positive charge to the second electrode to cause at least a portion of the first anions in the first aqueous stream to pass through the negative charge specific membrane material.
  • 10. The method of claim 9, further comprising: while operating in a rejection cycle subsequent to the purification cycle, applying a positive charge to the first electrode to cause at least a portion of the first cations to pass through the positive charge specific membrane material and into the dielectric spacer flow channel; andwhile operating in the rejection cycle subsequent to the purification cycle, applying a negative charge to the second electrode to cause at least a portion of the first anions to pass through the negative charge specific membrane material and into the dielectric spacer flow channel.
  • 11. The method of claim 10, further comprising: while operating in the rejection cycle, flushing the first cations and first anions out of the dielectric spacer flow channel by flowing a liquid through the dielectric spacer flow channel.
  • 12. The method of claim 9, wherein the positive charge specific membrane material comprises a first membrane layer between the first electrode and the dielectric spacer flow channel and/or wherein the negative charge specific membrane material comprises a second membrane layer between the second electrode and the dielectric spacer flow channel.
  • 13. The method of claim 12, wherein the negative charge specific membrane material comprises a second membrane layer positioned between the second electrode and the dielectric spacer flow channel.
  • 14. The method of claim 9, wherein the at least one of the first salt solution and the second salt solution comprises a salt selected from the group consisting of sodium chloride, antimony trichloride, an ammonium salt, antimony trifluoride, zinc chloride, zinc bromide, and indium bromide.
  • 15. The method of claim 9, wherein at least one of the first salt solution and the second salt solution has a capacitance density of 50,000 F/cc or greater.
  • 16. The method of claim 9, wherein at least one of the first salt solution and the second salt solution is saturated.
  • 17. The method of claim 9, wherein each of the first salt solution and the second salt solution comprises a salt selected from the group consisting of sodium chloride, antimony trichloride, an ammonium salt, antimony trifluoride, zinc chloride, zinc bromide, and indium bromide.
  • 18. The method of claim 9, wherein each of the first salt solution and the second salt solution has a capacitance density of 50,000 F/cc or greater.
  • 19. A method of preparing a capacitive deionization device for operational use, wherein the capacitive deionization device comprises a first electrode comprising a first plurality of voids; a positive charge specific membrane material, the positive charge specific membrane material positioned proximate the first electrode; a first salt solution comprising first anions and first cations residing in the first plurality of voids; a dielectric spacer flow channel positioned proximate the first charge specific membrane material; a negative charge specific membrane material, the negative charge specific membrane material positioned proximate the dielectric spacer flow channel opposite to the negative charge specific membrane material; a second electrode comprising a second plurality of voids, the second electrode being positioned proximate to the second charge specific membrane material opposite to the dielectric spacer flow channel; and a second salt solution comprising second anions and second cations residing in the second plurality of voids, the method comprising: applying a positive initial activation charge to the first electrode to cause at least a portion of the first cations of the first salt solution to pass through the positive charge specific membrane material into the dielectric spacer flow channel; andapplying a negative initial activation charge to the second electrode to cause at least a portion of the second anions of the second salt solution to pass through the negative charge specific membrane material into the dielectric spacer flow channel.
  • 20. The method of claim 19, further comprising flushing the passed through first cations and second anions out of the dielectric spacer flow channel by flowing a liquid through the dielectric spacer flow channel.
  • 21. The method of claim 19, wherein the positive charge specific membrane material comprises a first membrane layer between the first electrode and the dielectric spacer flow channel and/or wherein the negative charge specific membrane material comprises a second membrane layer between the second electrode and the dielectric spacer flow channel.
  • 22. The method of claim 21, wherein the negative charge specific membrane material comprises a second membrane layer positioned between the second electrode and the dielectric spacer flow channel.
  • 23. The method of claim 19, wherein at least one of the first salt solution and the second salt solution comprises a salt selected from the group consisting of sodium chloride, antimony trichloride, an ammonium salt, antimony trifluoride, zinc chloride, zinc bromide, and indium bromide.
  • 24. The method of claim 19, wherein at least one of the first salt solution and the second salt solution has a capacitance density of 50,000 F/cc or greater.
  • 25. The method of claim 19, wherein at least one of the first salt solution and the second salt solution is saturated.
  • 26. The method of claim 19, wherein each of the first salt solution and the second salt solution comprises a salt selected from the group consisting of sodium chloride, antimony trichloride, an ammonium salt, antimony trifluoride, zinc chloride, zinc bromide, and indium bromide.
  • 27. The method of claim 19, wherein each of the first salt solution and the second salt solution has a capacitance density of 50,000 F/cc or greater.
CROSS-REFERENCE TO RELATED APPLICATIONS

This Application is a continuation of U.S. application Ser. No. 15/826,053, entitled “ATOMIC CAPACITOR” filed Nov. 29, 2017, which is a continuation of U.S. application Ser. No. 15/492,406, entitled “ATOMIC CAPACITOR” filed Apr. 20, 2017, now U.S. Pat. No. 9,859,066 issued on Jan. 2, 2018, which is a continuation of U.S. application Ser. No. 14/120,497, entitled “ATOMIC CAPACITOR” filed on May 27, 2014, now U.S. Pat. No. 9,633,798 issued on Apr. 25, 2017, which claims priority under 35 U.S.C. § 119(e) to U.S. Provisional Application Ser. No. 61/855,769, entitled “ATOMIC CAPACITOR” filed on May 24, 2013, all of which are herein incorporated by reference in their entireties.

US Referenced Citations (122)
Number Name Date Kind
3281511 Goldsmith Oct 1966 A
3890417 Vallance Jun 1975 A
4153661 Ree et al. May 1979 A
4320185 Bernstein et al. Mar 1982 A
4337140 Solomon Jun 1982 A
4379772 Solomon et al. Apr 1983 A
4556618 Shia Dec 1985 A
4862328 Morimoto et al. Aug 1989 A
5145585 Coke Sep 1992 A
5192432 Andelman Mar 1993 A
5196115 Andelman Mar 1993 A
5200068 Andelman Apr 1993 A
5260855 Kaschmitter et al. Nov 1993 A
5360540 Andelman Nov 1994 A
5415768 Andelman May 1995 A
5425858 Farmer Jun 1995 A
5476878 Pekala Dec 1995 A
5508341 Mayer et al. Apr 1996 A
5538611 Otowa Jul 1996 A
5547581 Andelman Aug 1996 A
5620597 Andelman Apr 1997 A
5626977 Mayer et al. May 1997 A
5636437 Kaschmitter et al. Jun 1997 A
5731360 Pekala et al. Mar 1998 A
5748437 Andelman May 1998 A
5779891 Andelman Jul 1998 A
5932185 Pekala et al. Aug 1999 A
5954937 Farmer Sep 1999 A
6072692 Hiratusuka et al. Jun 2000 A
6127474 Andelman Oct 2000 A
6309532 Tran Oct 2001 B1
6325907 Andelman Dec 2001 B1
6346187 Tran et al. Feb 2002 B1
6413409 Otowa et al. Jul 2002 B1
6628505 Andelman Sep 2003 B1
6709560 Andelman et al. Mar 2004 B2
6761809 Tran et al. Jul 2004 B2
6778378 Andelman Aug 2004 B1
6781817 Andelman Aug 2004 B2
7138042 Tran et al. Nov 2006 B2
7175783 Curran et al. Feb 2007 B2
7368191 Andelman et al. May 2008 B2
8470152 Sullivan Jun 2013 B2
8685255 Knapp et al. Apr 2014 B2
8730650 Reinhoudt et al. May 2014 B2
8865351 Mayes Oct 2014 B2
8968544 Van Limpt et al. Mar 2015 B2
9067216 Reinhoudt et al. Jun 2015 B2
9096451 Van Der Wal et al. Aug 2015 B2
9193612 Curran Nov 2015 B2
9365440 Van Der Wal et al. Jun 2016 B2
9540260 Reinhoudt et al. Jan 2017 B2
9633798 Curran Apr 2017 B2
9637399 Van Der Wal et al. May 2017 B2
9859066 Curran Jan 2018 B2
20020017463 Merida-Donis et al. Feb 2002 A1
20020084188 Tran et al. Jul 2002 A1
20030161781 Cabasso et al. Aug 2003 A1
20040076885 Sato et al. Apr 2004 A1
20040170821 Iwaida et al. Sep 2004 A1
20050103634 Andelman et al. May 2005 A1
20060029857 Cherepy et al. Feb 2006 A1
20060049105 Max Mar 2006 A1
20060288743 van Kralingen et al. Dec 2006 A1
20070053141 Fujino Mar 2007 A1
20070075300 Curran et al. Apr 2007 A1
20070158185 Andelman et al. Jul 2007 A1
20070170060 Bourcier et al. Jul 2007 A1
20080078673 Elson et al. Apr 2008 A1
20080223795 Bakajin et al. Sep 2008 A1
20090114598 van Kralingen et al. May 2009 A1
20090218227 Noh et al. Sep 2009 A1
20100025247 Daily, III Feb 2010 A1
20100065438 Sullivan Mar 2010 A1
20100102009 Silva Apr 2010 A1
20100216023 Wei et al. Aug 2010 A1
20100230277 Sullivan et al. Sep 2010 A1
20100300287 Aines et al. Dec 2010 A1
20100328841 Reinhoudt et al. Dec 2010 A1
20110056843 Curran Mar 2011 A1
20110132762 O'Brien et al. Jun 2011 A1
20110240474 Seed et al. Oct 2011 A1
20120103818 Reinhoudt et al. May 2012 A1
20120125776 Van Der Wal et al. May 2012 A1
20120138470 Van Der Wal et al. Jun 2012 A1
20120214219 Aines et al. Aug 2012 A1
20120217170 Van Der Wal et al. Aug 2012 A1
20120273359 Suss et al. Nov 2012 A1
20130075260 Reinhoudt et al. Mar 2013 A1
20130098766 Van Der Wal et al. Apr 2013 A1
20130105399 Aines et al. May 2013 A1
20130105406 Van Der Wal et al. May 2013 A1
20130146463 Van Der Wal et al. Jun 2013 A1
20130153423 Van Der Wal et al. Jun 2013 A1
20130186761 Van Der Wal et al. Jul 2013 A1
20130213870 Tempest et al. Aug 2013 A1
20130284601 Van Der Wal et al. Oct 2013 A1
20140034501 Van Der Wal et al. Feb 2014 A1
20140048418 Van Der Wal et al. Feb 2014 A1
20140190838 Curran Jul 2014 A1
20140197102 Van Der Wal et al. Jul 2014 A1
20140238862 Van Der Wal et al. Aug 2014 A1
20140339099 Van Der Wal et al. Nov 2014 A1
20140346046 Andelman Nov 2014 A1
20150072267 Suss et al. Mar 2015 A1
20160042880 Curran Feb 2016 A1
20160083274 Curran Mar 2016 A1
20160096751 Curran Apr 2016 A1
20160207800 Seo et al. Jul 2016 A1
20160332897 Van Der Wal et al. Nov 2016 A1
20170001885 Verschueren Jan 2017 A1
20170032900 Curran Feb 2017 A9
20170129791 Van Der Wal et al. May 2017 A1
20170144902 Stadermann et al. May 2017 A1
20170200566 Stadermann et al. Jul 2017 A1
20180111854 Stadermann et al. Apr 2018 A1
20180134588 Hunter et al. May 2018 A1
20180151306 Curran May 2018 A1
20180155221 Curran et al. Jun 2018 A1
20180162752 Van Der Wal et al. Jun 2018 A1
20180282183 Curran et al. Oct 2018 A1
20190367386 Austin et al. Dec 2019 A1
Foreign Referenced Citations (25)
Number Date Country
2 409 955 Jan 2012 EP
2 607 321 Jun 2013 EP
2 980 027 Feb 2016 EP
3 037 389 Jun 2016 EP
1 453 565 Oct 1976 GB
2003-200164 Jul 2003 JP
WO 2006079417 Aug 2006 WO
WO 2009062872 May 2009 WO
WO 2010030383 Mar 2010 WO
WO 2010030384 Mar 2010 WO
WO 2010030385 Mar 2010 WO
WO 2010131951 Nov 2010 WO
WO 2011056066 May 2011 WO
WO 2011072400 Jun 2011 WO
WO 2011135048 Nov 2011 WO
WO 2012074397 Jun 2012 WO
WO 2012129532 Sep 2012 WO
WO 2013055220 Apr 2013 WO
WO 2013063567 May 2013 WO
WO 2013098193 Jul 2013 WO
WO 2015118036 Aug 2015 WO
WO 2016001325 Jan 2016 WO
WO 2016016313 Feb 2016 WO
WO 2016001325 Nov 2016 WO
WO 2016193166 Dec 2016 WO
Non-Patent Literature Citations (5)
Entry
Kenny et al., Basic Water Treatment of Steam Boilers. Western Dry Kiln Association. May 2000:8 pages.
Kuran et al., Flow Through Capacitor Technology. The International Workshop on Marine Pollution and the Impact of Seawater Desalination Plants on the Coastal Environment, Dubai, UAE, Dec. 1-3, 2003, pp. 1-15.
Lee et al., Desalination of a thermal power plant wastewater by membrane capacitive deionization. Desalination. Sep. 5, 2006;196(1-3):125-34.
Liu et al., Research of the Operating Parameters from Reducing Industrial Water Conductivity through Electro Sorption Technology. Applied Mechanics and Materials. Nov. 2012;229-31:2522-6.
Van Limpt et al., Water and chemical savings in cooling towers by using membrane capacitive deionization. Desalination. Jun. 2, 2014;342:148-55.
Related Publications (1)
Number Date Country
20190228920 A1 Jul 2019 US
Provisional Applications (1)
Number Date Country
61855769 May 2013 US
Continuations (3)
Number Date Country
Parent 15826053 Nov 2017 US
Child 16112424 US
Parent 15492406 Apr 2017 US
Child 15826053 US
Parent 14120497 May 2014 US
Child 15492406 US