JPWO2020021186A5 - - Google Patents

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JPWO2020021186A5
JPWO2020021186A5 JP2021503848A JP2021503848A JPWO2020021186A5 JP WO2020021186 A5 JPWO2020021186 A5 JP WO2020021186A5 JP 2021503848 A JP2021503848 A JP 2021503848A JP 2021503848 A JP2021503848 A JP 2021503848A JP WO2020021186 A5 JPWO2020021186 A5 JP WO2020021186A5
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liquid
zone
collector
flowing
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JP2021503848A
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JP7334233B2 (en
JP2021531446A (en
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Priority claimed from FR1856934A external-priority patent/FR3084454B1/en
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Claims (6)

交換器(100、200、300)であって、
蒸気に対して透過性を有し、かつ、液体に対して不透過性を有する、実質的に平行かつ鉛直に配置された複数の膜(30)であって、前記複数の膜は、複数の領域を定めており、前記複数の領域のそれぞれは、第一のタイプの領域及び第二のタイプの領域に交互に属する、複数の膜(30)と、
上部において、前記複数の膜に実質的に平行な面に沿って液体を噴霧するように構成された噴霧ノズルを含み、かつ、下部において、第一のコレクターを含み、前記第二のタイプの前記領域から独立しているとともに隔てられている、前記第一のタイプの前記領域と、
前記第一のタイプの前記領域(Z20、Z21)の前記噴霧ノズル(20、21)に液体を供給する第一管と、を含む、交換器(100、200、300)。
an exchanger (100, 200, 300),
A plurality of substantially parallel and vertically arranged membranes (30) permeable to vapor and impermeable to liquid, said membranes comprising a plurality of a plurality of membranes (30) defining regions, each of said plurality of regions belonging alternately to regions of a first type and regions of a second type;
At the top it comprises a spray nozzle configured to spray a liquid along a plane substantially parallel to the plurality of membranes and at the bottom it comprises a first collector, said of said second type said regions of said first type being separate from and separated from regions;
a first pipe supplying liquid to said spray nozzles (20, 21) of said zones (Z20, Z21) of said first type.
前記第二のタイプの前記領域(Z30)に、ガスが流れることを可能にする通路を含むことを特徴とする、請求項1に記載の交換器(100、200)。 2. An exchanger (100, 200) according to claim 1, characterized in that said zone (Z30) of said second type comprises passageways allowing gas to flow. 前記第二のタイプの前記領域(Z30)に、比較的高温多湿のガスを流すステップと、
比較的低温かつ塩濃度の高い液体を前記第一管(10)に流して、前記噴霧ノズル(20)によって、前記第一のタイプの前記領域(Z20)に前記液体が噴霧されるステップと、
前記第一のコレクター(50)に、加熱及び希釈された液体を集めるステップと、を含む、請求項2に記載の交換器(100)を使用するための方法。
flowing a relatively hot and humid gas through said zone (Z30) of said second type;
flowing a relatively cold and salty liquid through said first tube (10) and spraying said liquid onto said zone (Z20) of said first type by said spray nozzle (20);
and C. collecting heated and diluted liquid in said first collector (50).
前記第二のタイプの前記領域(Z30)に比較的低温のガスを流すステップと、
比較的高温かつ塩濃度の低い液体を前記第一管(11)に流して、前記噴霧ノズル(21)によって、前記第一のタイプの前記領域(Z21)に前記液体が噴霧されるステップと、
前記第一のコレクター(51)に、冷却及び濃縮された液体を集めるステップと、を含む、請求項2に記載の交換器(200)を使用するための方法。
flowing a relatively cold gas through said zone (Z30) of said second type;
Flowing a relatively hot and low-salinity liquid through the first tube (11) to spray the liquid onto the zone (Z21) of the first type by the spray nozzle (21);
and C. collecting the cooled and concentrated liquid in the first collector (51).
前記第二のタイプの前記領域は、上部において、前記膜(30)に実質的に平行な面に沿って液体を蒸発させるように構成された噴霧ノズルを含み、かつ、下部において、第二のコレクターを含み、前記第一のタイプの前記領域から独立しているとともに隔てられており、
前記交換器は、また、
前記第二のタイプの前記領域(Z20、Z21)の前記噴霧ノズル(20、21)に液体を供給する第二管を含むことを特徴とする、請求項1に記載の交換器(300)。
Said region of said second type comprises at the top a spray nozzle configured to evaporate liquid along a plane substantially parallel to said membrane (30) and at the bottom a second comprising a collector, independent and separated from said region of said first type;
The exchanger also
2. Exchanger (300) according to claim 1, characterized in that it comprises a second pipe supplying liquid to said spray nozzles (20, 21) of said zone (Z20, Z21) of said second type.
比較的低温かつ塩濃度の低い液体を前記第一管(10)に流して、前記噴霧ノズル(20)によって、前記第一のタイプの前記領域(Z20)に前記液体が噴霧されるステップと、
比較的高温かつ塩濃度の高い液体を前記第二管(11)に流して、前記噴霧ノズル(21)によって、前記第二のタイプの前記領域(Z21)に前記液体が噴霧されるステップと、
前記第一のタイプの前記領域(Z20)の下部において、前記第のコレクター(50)に、加熱及び希釈された液体を集めるステップと、
前記第二のタイプの前記領域(Z21)の下部において、前記第二のコレクター(51)に、冷却及び濃縮された液体を集めるステップと、を含む、請求項5に記載の交換器(300)を使用するための方法。
Flowing a relatively cold and low-salinity liquid through the first tube (10) and spraying the liquid onto the zone (Z20) of the first type by the spray nozzle (20);
flowing a relatively hot and salty liquid through said second tube (11) to spray said liquid onto said zone (Z21) of said second type by said spray nozzle (21);
collecting the heated and diluted liquid in the first collector (50) at the bottom of the zone (Z20) of the first type;
collecting the cooled and concentrated liquid in the second collector (51) in the lower part of the zone (Z21) of the second type. method for using.
JP2021503848A 2018-07-25 2019-07-18 heat mass exchanger Active JP7334233B2 (en)

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
FR1856934 2018-07-25
FR1856934A FR3084454B1 (en) 2018-07-25 2018-07-25 HEAT AND MATERIAL EXCHANGER
PCT/FR2019/051812 WO2020021186A1 (en) 2018-07-25 2019-07-18 Heat and material exchanger

Publications (3)

Publication Number Publication Date
JP2021531446A JP2021531446A (en) 2021-11-18
JPWO2020021186A5 true JPWO2020021186A5 (en) 2022-08-01
JP7334233B2 JP7334233B2 (en) 2023-08-28

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP2021503848A Active JP7334233B2 (en) 2018-07-25 2019-07-18 heat mass exchanger

Country Status (17)

Country Link
US (1) US20210302107A1 (en)
EP (1) EP3827211B1 (en)
JP (1) JP7334233B2 (en)
KR (1) KR20210066793A (en)
CN (1) CN112585421B (en)
AU (1) AU2019308722A1 (en)
BR (1) BR112021001246A2 (en)
DK (1) DK3827211T3 (en)
ES (1) ES2932729T3 (en)
FR (1) FR3084454B1 (en)
HR (1) HRP20221458T1 (en)
IL (1) IL280309B2 (en)
MX (1) MX2021000988A (en)
PL (1) PL3827211T3 (en)
SI (1) SI3827211T1 (en)
WO (1) WO2020021186A1 (en)
ZA (1) ZA202100532B (en)

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