JP2022132413A - 帯電による水の即時ライン上炭酸化の方法及び装置 - Google Patents
帯電による水の即時ライン上炭酸化の方法及び装置 Download PDFInfo
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Abstract
Description
一実施形態では、炭酸化装置は一対の炭酸化チャンバとして実装され、第1の炭酸化チャンバは円筒形のマイクロメッシュネットを含み、第2の炭酸化チャンバは複数のビーズを内部に配置する。
マイクロメッシュネットは、直径2~100μで5~800μの開放メッシュ面積を画定するステンレス鋼撚り線から形成され得る。
[付記1]
加圧及び冷却された二酸化炭素分子と水分子の混合入力流を炭酸化するための炭酸化装置であって、
(a)入力ポートと、出力ポートと、中央チャンバとを画定する第1の炭酸化チャンバであって、第1の炭酸化チャンバの入力ポートが入力流と流体連通している第1の炭酸化チャンバと、
(b)中央チャンバ内に配置される第1のカートリッジであって、第1の炭酸化チャンバの入力ポートと流体連通する第1のマイクロメッシュネットの多孔質外面と、前記第1の炭酸化チャンバの出力ポートと流体連通する第1のカートリッジ中央空隙とを画定する第1のカートリッジと、
(c)第1のマイクロメッシュネットの材料が、前記第1のマイクロメッシュネットを通過する水分子の鎖を破壊して第1のカートリッジの中央チャンバ内の水分子と二酸化炭素分子との結合を強化するようなサイズ及び構成を有することと、
(d)前記第1のマイクロメッシュネットが、更に、前記第1のマイクロメッシュネットを通過する水分子へ分極影響を及ぼす受動分極場を生成することによって、前記第1のマイクロメッシュネットに衝突して通過する水分子及び二酸化炭素分子の流れに応答する外面を画定し、前記中央チャンバ内の前記水分子と前記二酸化炭素分子との結合をさらに強化するように形成及び構成されることと、
(e)入力ポートと、出力ポートと、中央チャンバとを画定する第2の炭酸化チャンバであって、第2の炭酸化チャンバの入力ポートは前記第1の炭酸化チャンバの出力ポートと流体連通している第2の炭酸化チャンバと、
(f)前記中央チャンバ内に配置される第2のカートリッジであって、前記第2の炭酸化チャンバの入力ポートと流体連通する第2のマイクロメッシュネットの多孔質外面と、第2の炭酸化チャンバの出力ポートと流体連通する第2のカートリッジの中央空隙とを画定する第2のカートリッジと、
(g)前記第2のマイクロメッシュネットが、前記第2のマイクロメッシュネットを通過する水分子の鎖を破壊して前記第2のカートリッジの中央チャンバ内の水分子と二酸化炭素分子との結合を強化するようなサイズ及び構成を有することと、
(h)前記第2のマイクロメッシュネットが、更に、前記第2のマイクロメッシュネットを通過する水分子へ分極作用を及ぼす受動分極場を生成することによって、前記第2のマイクロメッシュネットに衝突して通過する水分子及び二酸化炭素分子の流れに応答する外面を画定し、前記中央チャンバ内の水分子と二酸化炭素分子との結合をさらに強化するように形成及び構成されることと
を備える、炭酸化装置。
[付記2]
付記1に記載の装置は、更に、
(i)第1のカートリッジの中央チャンバ内に配置された複数の第1のビーズを備え、第1の極性の第1のビーズが外面を画定し、前記外面の特徴は、前記外面上で二酸化炭素分子を捕捉し安定化させることで前記中央チャンバ内での水分子と二酸化炭素分子との結合をさらに強化するように形成された分子捕捉凹凸である、装置。
[付記3]
付記2に記載の装置は、更に、
(j)前記カートリッジの中央チャンバ内に配置された複数の第2のビーズであって、複数の第2のビーズが外面を画定し、前記外面の特徴は、前記第2のビーズの外面上で二酸化炭素分子を捕捉し安定化させることで前記中央チャンバ内での水分子と二酸化炭素分子との結合をさらに強化するための分子捕捉凹凸である第2のビーズを備える、装置。
[付記4]
付記3に記載の装置において、
前記第1及び第2の炭酸化チャンバが、2~400cm3の内部容積を画定する、装置。
[付記5]
付記4に記載の装置において、
前記第1及び第2のマイクロメッシュネットが、直径2~100μmのステンレス鋼撚り線から形成される、装置。
[付記6]
付記5に記載の装置において、
前記第1のマイクロメッシュネットが、5~500μmの開放メッシュ面積を画定する、装置。
[付記7]
付記6に記載の装置において、
前記第2のマイクロメッシュネットが、100~800μmの開放メッシュ面積を画定する、装置。
[付記8]
付記7に記載の装置において、
前記第1及び第2のビーズが0.5~5mmの直径を有する、装置。
[付記9]
付記7に記載の装置において、
前記第1のビーズが5mmの直径を有する、装置。
[付記10]
付記9に記載の装置において、
前記第2のビーズが0.5~3mmの直径を有する、装置。
[付記11]
付記3に記載の装置において、
前記第1のカートリッジがメッシュ数100のマイクロメッシュネットを画定し、前記第1のビーズが5mmの直径を画定し、前記第2のカートリッジがメッシュ数400のマイクロメッシュネットを画定し、前記第2のビーズが0.5~3mmの直径を画定する、装置。
[付記12]
付記3に記載の装置において、
前記入力流が160ポンド/平方インチ(psi)(1103kPa)の圧力及び1.5ガロン/分(GPM)(6.8l/min)の流速を有する、装置。
[付記13]
付記12に記載の装置において、
前記第2の炭酸化チャンバの出力ポートにおける炭酸水が、65psi(448kPa)の圧力及び1.1GPM(5.0l/min)の流速を有する、装置。
[付記14]
付記13に記載の装置は、更に、
前記第2の炭酸化チャンバの出力ポートと流体連通する流補償装置を備え、前記流補償装置が、前記第2の炭酸化チャンバからの圧力及び流速を15psi(103kPa)の圧力及び0.5~1.0GPM(2.3~4.5l/min)の流速に低減するように構成される、装置。
[付記15]
付記3に記載の装置は、更に、
前記第1の炭酸化チャンバの入力ポートと流体連通する混合装置を備え、前記混合装置が、加圧冷却水の供給源と連通する第1の入力ポートと、二酸化炭素の供給源と連通する第2の入力ポートとを有し、水と二酸化炭素とを混合して入力流を形成するように構成され、前記入力流が水溶液中に遊離水分子と二酸化炭素分子とを有する、装置。
[付記16]
付記15に記載の装置において、
前記加圧冷却水が、90psi(620kPa)の圧力及び1.8GPM(8.2l/min)の流速で前記混合装置の第1の入力ポートに供給される、装置。
[付記17]
付記16に記載の装置において、
前記二酸化炭素が75psi(517kPa)の圧力で前記混合装置の第2の入力ポートに供給される、装置。
Claims (1)
- 明細書に記載した装置。
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PCT/US2017/051225 WO2018049419A2 (en) | 2016-09-12 | 2017-09-12 | Method and apparatus for instantaneous on-line carbonation of water through electrostatic charging |
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US20220401897A1 (en) * | 2019-11-08 | 2022-12-22 | Freezio Ag | Method and Device for Producing a Carbonated Beverage |
US20230405539A1 (en) * | 2022-06-17 | 2023-12-21 | C18 Llc | Control method of carbonated water machine and carbonated water machine |
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