JP2009507618A5 - - Google Patents

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Publication number
JP2009507618A5
JP2009507618A5 JP2008513750A JP2008513750A JP2009507618A5 JP 2009507618 A5 JP2009507618 A5 JP 2009507618A5 JP 2008513750 A JP2008513750 A JP 2008513750A JP 2008513750 A JP2008513750 A JP 2008513750A JP 2009507618 A5 JP2009507618 A5 JP 2009507618A5
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Prior art keywords
liquid
gas
pressure
dissolved
tank
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JP2008513750A
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JP2009507618A (en
JP5127702B2 (en
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Priority claimed from PCT/US2005/018284 external-priority patent/WO2005115598A2/en
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Priority claimed from PCT/US2006/020391 external-priority patent/WO2006127979A2/en
Publication of JP2009507618A publication Critical patent/JP2009507618A/en
Publication of JP2009507618A5 publication Critical patent/JP2009507618A5/ja
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Claims (24)

気体を液体に溶解させる装置において:
(a)(i)液体を収容し、前記液体上部に調節された気体による上部空間を提供する圧力容器と、
(ii)液体の前記圧力容器内への注入を可能にする少なくとも一の液体噴射ノズルと、
(iii)前記液体の前記圧力容器外への流出を可能にする一個の出口と、
を有する溶解タンクと、
(b)前記液体を、前記少なくとも一個の液体噴射ノズルと連通する前記溶解タンクに注入する手段と、
(c)前記溶解タンクと連通する気体源
(d)前記溶解タンクの外側に備えられ、前記出口と連通する、放出装置であって、前記溶解タンクから前記液体が該放出装置外の液体中に放出される少なくとも一つの開口部を備える、放出装置
を備える装置。
In a device that dissolves gas into liquid:
(a) (i) a pressure vessel that contains liquid and provides an upper space with a regulated gas above the liquid;
(ii) at least one liquid jet nozzle which enables injection into the pressure vessel of the liquid,
(iii) an outlet that allows the liquid to flow out of the pressure vessel ;
Having a dissolving tank,
The (b) the liquid, the dissolving tank to the communication with the at least one liquid jet nozzle, for injecting and means,
(c) said dissolving tank and the gas source communicated,
(d) provided on the outside of the melting tank, the outlets communicating with, a release device, the liquid from the dissolving tank is released into the liquid outside of the discharge device, at least one opening A discharge device comprising :
Comprising a device.
前記気体が、空気、酸素、オゾン、水素、窒素、亜酸化窒素、及び二酸化炭素からなる群から選択される、請求項1記載の装置。 The apparatus of claim 1, wherein the gas is selected from the group consisting of air, oxygen, ozone, hydrogen, nitrogen, nitrous oxide, and carbon dioxide. 前記液体を前記溶解タンクに注入する手段が、
(i)高圧圧力液体ポンプ、又は(ii)住宅又は工業的設定の配線源、又は(iii)高圧気体の圧力により、その内部の前記液体を該気体で置換し、前記液体をその出口より前記溶解タンク内に強制注入する能力を有する複数の固定容量容器、又は(iv)静的な液体柱の頭圧、
である請求項1記載の装置。
It means for injecting the liquid before Symbol dissolution tank,
(i) a high-pressure liquid pump, or (ii) a wiring source in a residential or industrial setting, or (iii) the pressure of the high-pressure gas replaces the liquid inside the gas, and the liquid is discharged from the outlet. have the ability to force inject the dissolving tank, a plurality of fixed volume container, or (iv) a static liquid column head pressure,
In a device of claim 1, wherein.
前記放出装置外の圧力が、前記放出装置内の圧力より低く、従って前記放出装置内での溶解した気体の飽和濃度が、前記放出装置外の領域の飽和濃度より大きくなる請求項1記載の装置。 Pressure outside the discharge device is lower than the pressure in the discharge device, therefore, the saturation concentration of dissolved gases in said release device is greater than the saturation concentration in the region of the discharge instrumentation 置外 claim 1 The device described. 前記液体に溶解した気体の量が前記溶解タンクの内部圧力、又は、噴射された前記液体と前記上部空間内の気体との接触時間、又は、熱的手段により制御される請求項1記載の装置。 The amount of gas dissolved in the liquid, the internal pressure of the dissolution tank, or the contact time with the injected gas in the upper space and the liquid, or thermal means, controlled by, according Item 1. The apparatus according to Item 1. 前記少なくとも一つの噴射ノズルが、液体の液滴サイズをコントロールできるよう調節可能である請求項1記載の装置。 The apparatus of claim 1 , wherein the at least one spray nozzle is adjustable to control a liquid droplet size. 前記放出装置が、前記液体を、溶解した気体での処理を必要とする目標の液体に放出する請求項1記載の装置。 The discharge device, the liquid, the liquid processing target that requires at dissolved gases, emitting apparatus of claim 1, wherein. 溶解タンク内の加圧された前記気体の前記上部空間が溶解した気体を含む液体を前記放出装置から押し出す請求項1記載の装置。 The upper space of the pressurized said gas dissolution tank is to push the liquid containing the dissolved gas from the discharge device, apparatus according to claim 1. 前記放出装置が液体の同伴手段を備えておりそれにより、前記溶解した気体を含む液体が前記放出装置を出て、より低い大気圧下にある液体と混合する請求項1記載の装置。 Includes entrainment means of the release device is a liquid, whereby liquid containing a gas having the dissolved, the leaves release device, is mixed with the liquid under lower atmospheric pressure, according to claim 1, wherein . 前記放出装置の、前記少なくとも一つの開口部と同伴手段との、数、サイズ、配置は、溶解した気体を含む液体が、より低圧の大気圧下にある液体と混合し、且つ、気体が実質的に該液体に溶解した状態で留まるように、予め設定されている、請求項1記載の装置。 Of the discharge device, and the at least one opening and the companion device, the number, size, arrangement, a liquid containing dissolved gas is mixed with more liquid under the atmospheric pressure of the low pressure, and, a gas The device according to claim 1, wherein the device is preset so as to remain substantially dissolved in the liquid. 記放出装置の少なくとも一つの開口部と同伴手段の、数、サイズ、配置は、より低圧である大気圧下にある液体と混合し、且つ、少なくとも溶解した前記気体の一部が該液体から気泡の形で放出されるように、予め設定されている、請求項1記載の装置。 Before Symbol emission device, and at least one opening with accompanying means, number, size, arrangement, and mixed with a liquid which is under atmospheric pressure is at a lower pressure, and a portion of the gas which is at least dissolved the The device according to claim 1 , which is preset to be discharged from the liquid in the form of bubbles. 前記気泡のサイズが、所定のサイズ範囲に制御可能である、請求項11記載の装置。 The size of the bubble is controllable size range of Jo Tokoro The apparatus of claim 11, wherein. 前記放出装置の、前記少なくとも一つの開口部の、数、サイズ、配置、前記放出装置から流出する液体の流速が、溶解タンクに流入する液体の速度と均衡し、それにより制御された圧力と、前記液体の溶解タンク内部での容積と上部空間の気体容積との比率とを、定常的な流れの状態下で維持できるように、予め設定されている、請求項1記載の装置。 Of the release device, said at least one opening, number, size, arrangement, the flow rate of the liquid flowing out of the discharge device, and balances the velocity of the liquid flowing into the dissolving tank, thereby controlled pressure When, the ratio of gas volumes of the upper space in the dissolving tank inside the liquid, so they can maintain in a state of steady flow, are set in advance, according to claim 1, wherein. 前記装置の操作を制御するための開ループ又は閉ループの制御システムを有する請求項1記載の装置。 For controlling the operation of the device, has an open-loop or control system closed loop apparatus of claim 1, wherein. 気体を液体に溶解させる方法において:
(a)加圧により封入型の容器を気体で充填するプロセスと
(b)液体を、前記気体が該液体に溶解可能な条件下で、前記気体を含む容器内に噴射する、プロセスと
(c)前記溶解した気体を含む液体を前記容器から、少なくとも一つの開口部を備え、且つ、目標の液体中に浸漬された放出装置内へ導くプロセスと、
(d)前記溶解した気体を含む液体を、前記目標の液体中に液体同士の混合を可能とする条件下で、放出するプロセスと、
を備えた、方法。
In the method of dissolving a gas in a liquid:
(a) a process of filling a sealed container with gas by pressurization;
(b) a process of injecting a liquid into a container containing the gas under conditions where the gas is soluble in the liquid;
(c) a liquid containing a pre Ki溶 loosening gas from the container, and process at least comprises one of the opening and was immersed in the target liquid, leading to the release device,
a liquid containing a gas having; (d) dissolved in the liquid of the target, under conditions that allow the mixing of the liquid between the process of release,
With a method.
前記気体が、空気、酸素、オゾン、水素、窒素、亜酸化窒素、及び二酸化炭素からなる群から選択される、請求項15記載の方法。 The method of claim 15, wherein the gas is selected from the group consisting of air, oxygen, ozone, hydrogen, nitrogen, nitrous oxide, and carbon dioxide. 溶解タンクの圧力下で、前記気体が前記液体に飽和濃度又は飽和濃度近くで溶解する請求項15記載の方法。 Under a pressure of the dissolving tank, the gas, the liquid, dissolved in saturated concentration or saturation concentration near, The method of claim 15. 継続的モード又はパルス的モードで行われる請求項15記載の方法。 It carried out in continuous mode or pulsed mode, The method of claim 15. 前記気体がほぼ大気圧下で前記容器に入り、前記液体前記容器から放出する前に、より高い所望の圧力が達成されるまで、閉鎖システムでの液体の噴射を通じて、前記気体が加圧される請求項15記載の方法。 The gas enters the vessel substantially at atmospheric pressure, the pre-Symbol liquid prior to releasing from said container, to a higher desired pressure is achieved through the injection of a liquid in a closed system, the gas pressure pressure is method of claim 15. 前記タンクの加圧に使われたエネルギーが、前記溶解した気体を含む液体を、強制的に目標の液体中に排出し、二つの液体を混合することに使われる、請求項15記載の方法。   The method of claim 15, wherein the energy used to pressurize the tank is used to force the liquid containing the dissolved gas to drain into the target liquid and to mix the two liquids. 前記液体の混合速度が、溶解した気体の大部分が溶液中に残存するように制御される請求項15記載の方法。 Mixing speed of the liquid, so that the majority of dissolved gas remaining in the solution, being controlled method of claim 15. 前記液体の混合速度が、少なくとも溶解した気体の一部が溶液から気泡の形で放出されるように、制御される請求項15記載の方法。 The method of claim 15 , wherein the mixing rate of the liquid is controlled such that at least a portion of the dissolved gas is released from the solution in the form of bubbles. 前記気泡のサイズが、所定のサイズ範囲に制御される請求項22記載の方法。 The size of the bubbles, to a predetermined size range is controlled method of claim 22, wherein. 高圧ポンプから前記容器に入る前記液体が、前記溶解タンク内に設置された液体の水準を示すセンサーからのフィードバックで制御される請求項15記載の方法。 The liquid body from the high-pressure pump enters the vessel, the feedback from the sensor indicative of the level of the liquid which is placed in the dissolution tank, being controlled method of claim 15.
JP2008513750A 2005-05-25 2006-05-25 System and method for dissolving a gas into a liquid and supplying the same dissolved gas Active JP5127702B2 (en)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
USPCT/US2005/018284 2005-05-25
US11/137,856 2005-05-25
PCT/US2005/018284 WO2005115598A2 (en) 2004-05-25 2005-05-25 System and method for dissolving gases in liquids
US11/137,856 US7255332B2 (en) 2004-05-25 2005-05-25 System and method for dissolving gases in liquids
PCT/US2006/020391 WO2006127979A2 (en) 2005-05-25 2006-05-25 System and method for dissolving gases in fluids and for delivery of dissolved gases

Publications (3)

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JP2009507618A JP2009507618A (en) 2009-02-26
JP2009507618A5 true JP2009507618A5 (en) 2009-07-09
JP5127702B2 JP5127702B2 (en) 2013-01-23

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AU (1) AU2006249808B2 (en)
NZ (1) NZ563542A (en)

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CN107434308B (en) * 2017-08-22 2021-01-15 江西楚杭环保科技有限公司 High-efficiency dissolved oxygen sewage aeration tank
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JP7260429B2 (en) 2019-07-19 2023-04-18 株式会社荏原製作所 Gas solution manufacturing equipment
CN112842403B (en) * 2020-12-24 2022-05-03 中国水产科学研究院南海水产研究所 Collection of aquatic animal breath release14CO2And method of use thereof
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