JP2010517746A5 - - Google Patents

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Publication number
JP2010517746A5
JP2010517746A5 JP2009548244A JP2009548244A JP2010517746A5 JP 2010517746 A5 JP2010517746 A5 JP 2010517746A5 JP 2009548244 A JP2009548244 A JP 2009548244A JP 2009548244 A JP2009548244 A JP 2009548244A JP 2010517746 A5 JP2010517746 A5 JP 2010517746A5
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JP
Japan
Prior art keywords
solute
stream
desalination
supercapacitor
subsystem
Prior art date
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Ceased
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JP2009548244A
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Japanese (ja)
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JP2010517746A (en
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Publication date
Priority claimed from US11/670,232 external-priority patent/US20080185294A1/en
Priority claimed from US11/670,230 external-priority patent/US7974076B2/en
Application filed filed Critical
Priority claimed from PCT/US2007/088518 external-priority patent/WO2008094367A1/en
Publication of JP2010517746A publication Critical patent/JP2010517746A/en
Publication of JP2010517746A5 publication Critical patent/JP2010517746A5/ja
Ceased legal-status Critical Current

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Claims (15)

溶質担持電極から排出液体流中に溶質を放出させることを含む方法であって、排出液体流が、該溶質担持電極が溶質を獲得した元の供給流よりも相対的に高い濃度の溶質を有する、方法。A method comprising releasing a solute from a solute-supporting electrode into an exhaust liquid stream, wherein the exhaust liquid stream has a relatively higher concentration of solute than the original feed stream from which the solute-supporting electrode acquired the solute. ,Method. 前記電極がスーパーキャパシタ電極であり、さらに、溶質を供給流から電極上に吸収させて溶質担持電極及び出力流を形成することを含んでおり、出力流が供給流よりも相対的に低い溶質濃度を有する、請求項1記載の方法。The electrode is a supercapacitor electrode, further comprising absorbing a solute from the supply stream onto the electrode to form a solute-supporting electrode and an output stream, wherein the output stream is relatively lower in solute concentration than the supply stream The method of claim 1, comprising: 電極が第2の脱塩装置内に配置されていて、供給流を第1の脱塩装置から第2の脱塩装置へ流すことをさらに含んでいるか、或いは電極が第2の脱塩装置内に配置されていて、出力流を第2の脱塩装置から第1の脱塩装置へ流すことをさらに含む、請求項2記載の方法。The electrode is disposed in the second demineralizer and further includes flowing a feed stream from the first demineralizer to the second demineralizer, or the electrode is in the second demineralizer The method of claim 2, further comprising flowing an output stream from the second desalter to the first desalter. 第1の脱塩装置が膜を含んでいて、液体流を膜に通して流して供給流を形成するか又は出力流を第2の脱塩装置から膜に通して流して出力流を濾過することを含む、請求項3記載の方法。The first demineralizer includes a membrane and a liquid stream is passed through the membrane to form a feed stream or an output stream is passed from the second desalter through the membrane to filter the output stream. The method of claim 3 comprising: 第1の脱塩装置が透析装置又は逆浸透装置を含む、請求項3記載の方法。4. The method of claim 3, wherein the first desalting device comprises a dialysis device or a reverse osmosis device. 前記透析装置が電気透析脱塩又は電気透析逆脱塩装置である、請求項5記載の方法。The method according to claim 5, wherein the dialysis apparatus is an electrodialysis desalination or an electrodialysis reverse desalination apparatus. 第1のサブシステム、及び
第1のサブシステムと流体連通している第2のサブシステム
を備える脱塩システムであって、第2のサブシステムが溶質を溶質担持電極から排出液体流中に放出させる手段を含んでおり、排出液体流が、溶質担持電極が溶質を獲得した元の溶質担持供給流よりも相対的に高い濃度の溶質を有する、前記脱塩システム。
A desalination system comprising a first sub-system and a second sub-system in fluid communication with the first sub-system, wherein the second sub-system releases the solute from the solute carrying electrode into the discharged liquid stream Said desalination system, wherein the drained liquid stream has a higher concentration of solute than the original solute-supported feed stream from which the solute-supported electrode acquired solute.
第1のサブシステムが供給流体を受け入れて第1及び第2の流出流体流を生成し、第1の流出流体流が供給流体の溶質濃度よりも相対的に低い溶質濃度を有し、第2の流出流体流が供給流体の溶質濃度よりも相対的に高い溶質濃度を有する、請求項記載の脱塩システム。A first subsystem receives the feed fluid and generates first and second effluent fluid streams, the first effluent fluid stream having a solute concentration that is relatively lower than the solute concentration of the feed fluid; The desalination system of claim 7 , wherein the effluent fluid stream has a solute concentration that is relatively higher than a solute concentration of the feed fluid. 第1のサブシステムが逆浸透システム、電気透析脱塩システム、電気透析逆脱塩システム又はナノ濾過脱塩システムを含む、請求項記載の脱塩システム。8. The desalination system of claim 7 , wherein the first subsystem comprises a reverse osmosis system, an electrodialysis desalination system, an electrodialysis reverse desalination system or a nanofiltration desalination system. 第2のサブシステムが充電作動モードと放電作動モードとを有しており、第2のサブシステムが、
スーパーキャパシタ脱塩ユニットが第2の放電作動モードにあるときに排出流をスーパーキャパシタ脱塩ユニットに供給する再生源、及び
スーパーキャパシタ脱塩ユニットが第1の充電作動モードにあるときに第1のサブシステムから第2の流出流体流を受け入れるスーパーキャパシタ脱塩ユニット
を含む、請求項記載の脱塩システム。
The second subsystem has a charge operation mode and a discharge operation mode, and the second subsystem is:
A regeneration source that supplies an exhaust stream to the supercapacitor desalination unit when the supercapacitor desalination unit is in the second discharge mode of operation, and a first when the supercapacitor desalination unit is in the first charge mode of operation. The desalination system of claim 7 , comprising a supercapacitor desalination unit that receives a second effluent fluid stream from the subsystem.
前記再生源が、スーパーキャパシタ脱塩ユニットが第2の放電作動モードにあるときにスーパーキャパシタ脱塩ユニットから排出流を受け入れる、請求項10記載の脱塩システム。The desalination system of claim 10 , wherein the regeneration source receives an exhaust stream from the supercapacitor desalination unit when the supercapacitor desalination unit is in a second discharge mode of operation. 第1のサブシステム、
第1のサブシステムと流体連通している第2のサブシステム、及び
第2のサブシステムと接続したコントローラ
を備える処理システムであって、コントローラからの信号に応答して、第2のサブシステムが溶質を溶質担持電極から排出液体流へ放出させ、排出液体流が、溶質担持電極が溶質を獲得した元の溶質担持供給流よりも相対的に高い濃度の溶質を有する、処理システム。
A first subsystem,
A processing system comprising: a second subsystem in fluid communication with the first subsystem; and a controller connected to the second subsystem, wherein the second subsystem is responsive to a signal from the controller A processing system in which solute is discharged from a solute-carrying electrode into a discharge liquid stream, the discharge liquid stream having a relatively higher concentration of solute than the original solute-carrying supply stream from which the solute-carrying electrode acquired solute.
充電作動モード及び放電作動モードで作動可能なスーパーキャパシタ脱塩ユニット、
スーパーキャパシタ脱塩ユニットが充電作動モードにあるときにスーパーキャパシタ脱塩ユニットに供給流を供給するように構成された供給源、並びに
スーパーキャパシタ脱塩ユニットが放電作動モードにあるときにスーパーキャパシタ脱塩ユニットに飽和供給流又は過飽和供給流を供給するように構成された再生源
を含む、脱塩システム。
A supercapacitor desalination unit operable in a charge operation mode and a discharge operation mode;
A source configured to supply a supply stream to the supercapacitor desalination unit when the supercapacitor desalination unit is in a charging operation mode, and a supercapacitor desalination when the supercapacitor desalination unit is in a discharge operation mode A desalination system comprising a regeneration source configured to supply a saturated or supersaturated feed stream to the unit.
スーパーキャパシタ脱塩ユニット、
システムが第1の作動モードにあるときにスーパーキャパシタ脱塩ユニットを通して液体を案内するように構成された第1のフィードバックループを含む第1の液体流路、及び
システムが第2の作動モードにあるときにスーパーキャパシタ脱塩ユニットを通して液体を案内するように構成された第2のフィードバックループを含む第2の液体流路
を含む脱塩システム。
Supercapacitor desalination unit,
A first liquid flow path including a first feedback loop configured to guide liquid through the supercapacitor desalination unit when the system is in a first mode of operation; and the system is in a second mode of operation A desalination system that includes a second liquid flow path that includes a second feedback loop that is sometimes configured to guide liquid through a supercapacitor desalination unit.
第1の期間の時間充電作動モード中第1の源からの第1の液体流をスーパーキャパシタ脱塩ユニットに通して供給し、
第2の期間の時間放電作動モード中第2の源からの第2の液体流をスーパーキャパシタ脱塩ユニットに通して供給する
ことを含む液体処理方法。
Supplying a first liquid stream from a first source through a supercapacitor desalination unit during a first period time charging mode of operation;
A liquid treatment method comprising supplying a second liquid stream from a second source through a supercapacitor desalination unit during a time discharge mode of operation for a second period.
JP2009548244A 2007-02-01 2007-12-21 Desalination method and apparatus including supercapacitor electrode Ceased JP2010517746A (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
US11/670,232 US20080185294A1 (en) 2007-02-01 2007-02-01 Liquid management method and system
US11/670,230 US7974076B2 (en) 2007-02-01 2007-02-01 Desalination device and associated method
PCT/US2007/088518 WO2008094367A1 (en) 2007-02-01 2007-12-21 Desalination method and device comprising supercapacitor electrodes

Publications (2)

Publication Number Publication Date
JP2010517746A JP2010517746A (en) 2010-05-27
JP2010517746A5 true JP2010517746A5 (en) 2011-02-10

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JP2009548244A Ceased JP2010517746A (en) 2007-02-01 2007-12-21 Desalination method and apparatus including supercapacitor electrode

Country Status (7)

Country Link
EP (1) EP2109587A1 (en)
JP (1) JP2010517746A (en)
AU (1) AU2007345554B2 (en)
BR (1) BRPI0720810A2 (en)
IL (1) IL199976A0 (en)
TW (1) TW200846291A (en)
WO (1) WO2008094367A1 (en)

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