JP2019018138A - Calcareous water manufacturing apparatus, calcareous water manufacturing method and method for dissolving carbon dioxide into water at high concentration - Google Patents

Calcareous water manufacturing apparatus, calcareous water manufacturing method and method for dissolving carbon dioxide into water at high concentration Download PDF

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JP2019018138A
JP2019018138A JP2017137875A JP2017137875A JP2019018138A JP 2019018138 A JP2019018138 A JP 2019018138A JP 2017137875 A JP2017137875 A JP 2017137875A JP 2017137875 A JP2017137875 A JP 2017137875A JP 2019018138 A JP2019018138 A JP 2019018138A
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carbon dioxide
water
mixing tank
supply line
dioxide gas
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千治 中野
Chiharu Nakano
千治 中野
尚明 杉山
Naoaki Sugiyama
尚明 杉山
正之 稲垣
Masayuki Inagaki
正之 稲垣
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Sapporo Breweries Ltd
Resonac Gas Products Corp
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Sapporo Breweries Ltd
Showa Denko Gas Products Co Ltd
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Abstract

To provide a small-sized calcareous water manufacturing apparatus which can manufacture calcareous water of a high concentration and a manufacturing method for the same.SOLUTION: This calcareous water manufacturing apparatus is configured from: a carbon dioxide gas supply line having a carbon dioxide gas supply source; a water supply line having a water supply line; a mixing tank which is connected to the carbon dioxide gas supply line and the water supply line, and mixes carbon dioxide gas from the carbon dioxide gas supply line and water from the water supply line, thereby producing calcareous water; a circulation line of which one end is connected to a lower part of the mixing tank and the other end is connected to an upper part of the mixing tank; cooling means provided on the circulation line; a calcareous water supply line which is connected to the circulation line via a gate valve, and supplies calcareous water to the exterior; and a supply nozzle which is connected to the calcareous water supply line. The calcareous water supply line always supplies carbon dioxide gas to the mixing tank, and the circulation line continuously or intermittently circulates a liquid in the mixing gas, thereby dissolving carbon dioxide gas into water at a high concentration.SELECTED DRAWING: Figure 1

Description

本発明は、炭酸水を用いた清涼飲料水やアルコール飲料を作る際に使用できる小型の炭酸水の製造装置、炭酸水の製造方法及び水に高濃度で炭酸ガスを溶解させる方法に関する。   The present invention relates to a small-sized carbonated water production apparatus, a carbonated water production method, and a method for dissolving carbon dioxide gas in water at a high concentration, which can be used when making soft drinks or alcoholic drinks using carbonated water.

特許文献1には、「機枠と、この機枠に取付けられた比較的小容量で容量の異なる大・小のカーボネートタンクと、この大・小のカーボネートタンク内に水あるいは調合糖液と水とを混合した炭酸飲料の原液をそれぞれ選択的に供給する原液等の供給装置と、前記大・小のカーボネートタンク内の原液等をそれぞれ選択的に冷却することのできる前記機枠に取付けられた冷却装置と、前記大・小のカーボネートタンク内の原液等に炭酸ガスを吸収させる前記機枠に取付けられたカーボネーション装置と、前記大・小のカーボネートタンク内のカーボネーションを終えた製品液等を選択的に充填ポンプを備える充填通路を介してノズルを備える充填弁よりびん等の容器に充填する前記機枠に取付けられた充填装置とを備えることを特徴とする試作用炭酸飲料製造装置」が開示されている。   Patent Document 1 states that “a machine frame, large and small carbonate tanks with a relatively small capacity and different capacities attached to the machine frame, and water or mixed sugar solution and water in the large and small carbonate tanks. And a supply device such as a stock solution for selectively feeding a stock solution of a carbonated beverage mixed with each other, and the machine frame capable of selectively cooling the stock solution in the large and small carbonate tanks, respectively. A cooling device, a carbonation device attached to the machine frame that absorbs carbon dioxide gas into the stock solution in the large and small carbonate tanks, a product liquid that has finished carbonation in the large and small carbonate tanks, etc. And a filling device attached to the machine frame for filling a container such as a bottle from a filling valve having a nozzle through a filling passage having a filling pump selectively. Carbonated beverage production device "is disclosed use.

上記特許文献1は非常に大型の試作用装置であり、また、この試作用炭酸飲料製造装置では循環路を有してはいるものの、炭酸水に炭酸ガスをより高濃度で溶解させるためではなく、単に冷却するために循環するものであり、常時又は断続的にカーボネーションタンク内の液体を循環させ、その炭酸水の炭酸ガス濃度を高濃度にするものではなかった。
そのため、このような装置は非常に高額・大型となるため、飲食店等の店舗等へ設置することができないという問題点があった。
The above Patent Document 1 is a very large prototype device, and this prototype carbonated beverage production device has a circulation path, but not for dissolving carbon dioxide in carbonated water at a higher concentration. However, it was merely circulated for cooling, and the liquid in the carbonation tank was circulated constantly or intermittently, and the carbon dioxide concentration of the carbonated water was not increased.
Therefore, since such an apparatus becomes very expensive and large, there is a problem that it cannot be installed in a store such as a restaurant.

特許第2772436号公報Japanese Patent No. 2772436

本発明は以上のような従来の欠点に鑑み、高濃度の炭酸水を製造できる小型の炭酸水の製造装置及びその製造方法を提供することを目的としている。   In view of the above-described conventional drawbacks, an object of the present invention is to provide a small carbonated water production apparatus capable of producing high-concentration carbonated water and a production method therefor.

上記目的を達成するために、本発明の炭酸水の製造装置は、炭酸ガス供給源を有する炭酸ガス供給ラインと、水供給源を有する水供給ラインと、前記炭酸ガス供給ライン及び水供給ラインに接続され、前記炭酸ガス供給ラインからの炭酸ガスと前記水供給ラインからの水を混合して炭酸水とする混合タンクと、該混合タンクの下部にその一端部が接続され、その他端部が混合タンクの上部に接続された循環ラインと、該循環ラインに設けられた冷却手段と、該循環ラインに仕切弁を介して接続され、前記炭酸水を外部へ供給する炭酸水供給ラインと、該炭酸水供給ラインに接続された供給ノズルとで構成され、前記炭酸ガス供給ラインは、前記混合タンクに常時炭酸ガスを供給するものであり、前記循環ラインは、前記混合タンク内の液体を連続的又は断続的に循環させることにより、前記水に高濃度で前記炭酸ガスを溶解させることを特徴とする。   In order to achieve the above object, a carbonated water production apparatus of the present invention includes a carbon dioxide supply line having a carbon dioxide supply source, a water supply line having a water supply source, and the carbon dioxide supply line and the water supply line. Connected, a carbon dioxide gas from the carbon dioxide gas supply line and water from the water supply line are mixed to form carbonated water, one end of the tank is connected to the lower part of the mixing tank, and the other end is mixed A circulation line connected to the upper part of the tank; cooling means provided in the circulation line; a carbonated water supply line connected to the circulation line via a gate valve to supply the carbonated water to the outside; A supply nozzle connected to a water supply line, wherein the carbon dioxide supply line constantly supplies carbon dioxide to the mixing tank, and the circulation line supplies liquid in the mixing tank. By connection or intermittently circulated, characterized in that dissolving the carbon dioxide in high concentrations in the water.

また、本発明の炭酸水の製造装置は、炭酸ガス供給源を有する炭酸ガス供給ラインと、水供給源を有する水供給ラインと、前記炭酸ガス供給ライン及び水供給ラインに接続され、前記炭酸ガス供給ラインからの炭酸ガスと前記水供給ラインからの水を混合して炭酸水とする混合タンクと、該混合タンクの下部にその一端部が接続され、その他端部が混合タンクの上部に接続された循環ラインと、該循環ラインに設けられた冷却手段と、該循環ラインに仕切弁を介して接続され、前記炭酸水を外部へ供給する炭酸水供給ラインと、該炭酸水供給ラインに接続された供給ノズルと、前記炭酸水と混合して提供される飲料を供給する飲料供給源と、該飲料供給源と飲料用仕切弁を介して接続され、前記供給ノズルに前記飲料を供給する飲料供給ラインとで構成され、前記炭酸ガス供給ラインは、前記混合タンクに常時炭酸ガスを供給するものであり、前記循環ラインは、前記混合タンク内の液体を連続的又は断続的に循環させることにより、前記水に高濃度で前記炭酸ガスを溶解させることを特徴とする。   The apparatus for producing carbonated water according to the present invention includes a carbon dioxide gas supply line having a carbon dioxide gas supply source, a water supply line having a water supply source, the carbon dioxide gas supply line, and the water supply line. A mixing tank in which carbon dioxide gas from the supply line and water from the water supply line are mixed to form carbonated water, one end of which is connected to the lower part of the mixing tank, and the other end connected to the upper part of the mixing tank. A circulation line, cooling means provided in the circulation line, a carbonated water supply line connected to the circulation line via a gate valve, and supplying the carbonated water to the outside, and connected to the carbonated water supply line A beverage supply source for supplying a beverage provided by mixing with the carbonated water, a beverage supply connected to the beverage supply source and a beverage gate valve, and supplying the beverage to the supply nozzle Rye The carbon dioxide gas supply line constantly supplies carbon dioxide gas to the mixing tank, and the circulation line circulates the liquid in the mixing tank continuously or intermittently, thereby The carbon dioxide gas is dissolved in water at a high concentration.

さらに、本発明の炭酸水の製造方法は、混合タンクに炭酸ガスを常時供給する炭酸ガス供給工程と、前記混合タンクに水を供給する水供給工程と、前記混合タンク内の液体を連続的又は断続的に循環させ、前記水に高濃度で前記炭酸ガスを溶解させた炭酸水とする炭酸ガス溶解工程と、前記混合タンク内の前記炭酸水を供給する炭酸水供給工程とで構成されることを特徴とする。   Furthermore, the method for producing carbonated water according to the present invention includes a carbon dioxide supply step for constantly supplying carbon dioxide to the mixing tank, a water supply step for supplying water to the mixing tank, and a liquid in the mixing tank continuously or It is composed of a carbon dioxide dissolving step that intermittently circulates to form carbonated water in which the carbon dioxide gas is dissolved at a high concentration in the water, and a carbonated water supply step that supplies the carbonated water in the mixing tank. It is characterized by.

本発明の水に高濃度で炭酸ガスを溶解させる方法は、混合タンクに炭酸ガスを常時供給する炭酸ガス供給工程と、前記混合タンクに水を供給する水供給工程と、前記混合タンク内の液体を連続的又は断続的に循環させ、前記水に高濃度で前記炭酸ガスを溶解させた炭酸水とする炭酸ガス溶解工程とで構成される。   The method of dissolving carbon dioxide gas at a high concentration in water according to the present invention includes a carbon dioxide supply step for constantly supplying carbon dioxide to a mixing tank, a water supply step for supplying water to the mixing tank, and a liquid in the mixing tank. Is continuously or intermittently circulated to form a carbonated gas dissolving step in which the carbonated gas is dissolved in the water at a high concentration.

以上の説明から明らかなように、本発明にあっては次に列挙する効果が得られる。
(1)請求項1、請求項6及び請求項9に記載の各発明においては、混合タンク内の液体を連続的又は断続的に循環させることで、炭酸水の中に溶解する炭酸ガスの濃度を高めることができる。したがって、高濃度の炭酸水を得ることができる。
(2)混合タンク内の液体を循環させることで、炭酸水の中に溶解する炭酸ガスの濃度を高めるので、低圧力の炭酸ガスでも高濃度の炭酸水を得ることができる。したがって、装置を小型化することができる。
(3)請求項2及び請求項7に記載の各発明も前記(1)〜(2)と同様な効果が得られるとともに、飲料を混合した状態で提供することができる。
(4)請求項3及び請求項8に記載の各発明も前記(1)〜(3)と同様な効果が得られるとともに、炭酸ガスの供給圧力を0.75MPa以下にすることにより、装置に流れる流体の圧力を1MPa未満にすることができるので、高圧ガス保安法を適用しない設備とすることができる。したがって、設備に用いる容器等をより簡易なもの等にすることができ、装置を簡易化・小型化することができる。
(5)請求項4に記載の発明も前記(1)〜(4)と同様な効果が得られるとともに、循環ラインから戻った液体を噴霧することで、炭酸ガスとの接触面積及び接触時間が増大し、より炭酸ガスの溶解を促進することができる。
(6)請求項5に記載の発明も前記(1)〜(4)と同様な効果が得られるとともに、プレート式熱交換器を用いることにより、より小型化をすることができる。
As is clear from the above description, the present invention has the following effects.
(1) In each invention of Claim 1, Claim 6 and Claim 9, the concentration of carbon dioxide dissolved in carbonated water by circulating the liquid in the mixing tank continuously or intermittently Can be increased. Therefore, high concentration carbonated water can be obtained.
(2) Since the concentration of carbon dioxide dissolved in the carbonated water is increased by circulating the liquid in the mixing tank, a high concentration carbonated water can be obtained even with low-pressure carbon dioxide. Therefore, the apparatus can be reduced in size.
(3) Each of the inventions according to claims 2 and 7 can provide the same effects as the above (1) to (2), and can also be provided in a mixed state.
(4) Each of the inventions according to claims 3 and 8 can achieve the same effects as in the above (1) to (3), and the carbon dioxide gas supply pressure is set to 0.75 MPa or less, so Since the pressure of the flowing fluid can be reduced to less than 1 MPa, it is possible to provide equipment that does not apply the high-pressure gas safety method. Therefore, the container used for the facility can be made simpler, and the apparatus can be simplified and downsized.
(5) The invention according to claim 4 also provides the same effects as in the above (1) to (4), and by spraying the liquid returned from the circulation line, the contact area and contact time with carbon dioxide gas The carbon dioxide gas can be dissolved more easily.
(6) The invention described in claim 5 can achieve the same effects as the above (1) to (4), and can be further reduced in size by using a plate heat exchanger.

図1乃至図6は本発明の第1の実施形態を示す説明図である。
図7及び図8は本発明の第2の実施形態示す説明図である。
第1の実施形態の炭酸水の製造装置の概略説明図。 炭酸ガス供給ラインの概略説明図。 水供給ラインの概略説明図。 循環ラインの概略説明図。 炭酸水供給ラインの概略説明図。 第1の実施形態の炭酸水の製造方法の工程図。 第2の実施形態の概略説明図。 第2の実施形態の炭酸水の製造方法の工程図。
1 to 6 are explanatory views showing a first embodiment of the present invention.
7 and 8 are explanatory views showing a second embodiment of the present invention.
The schematic explanatory drawing of the manufacturing apparatus of carbonated water of a 1st embodiment. Schematic explanatory drawing of a carbon dioxide supply line. Schematic explanatory drawing of a water supply line. Schematic explanatory drawing of a circulation line. Schematic explanatory drawing of a carbonated water supply line. Process drawing of the manufacturing method of carbonated water of a 1st embodiment. Schematic explanatory drawing of 2nd Embodiment. The process drawing of the manufacturing method of carbonated water of a 2nd embodiment.

以下、図面に示す本発明を実施するための形態により、本発明を詳細に説明する。
図1乃至図6に示す本発明を実施するための第1の形態において、1は本発明の炭酸水の製造装置である。
Hereinafter, the present invention will be described in detail with reference to the embodiments shown in the drawings.
In the first embodiment for carrying out the present invention shown in FIG. 1 to FIG. 6, reference numeral 1 denotes an apparatus for producing carbonated water according to the present invention.

この炭酸水の製造装置1は、主に飲食店等の店舗に設置される小型のものである。
この炭酸水の製造装置1は、図1に示すように、炭酸ガス供給源2を有する炭酸ガス供給ライン3と、水供給源4を有する水供給ライン5と、前記炭酸ガス供給ライン3及び水供給ライン5に接続され、炭酸ガス供給源2から炭酸ガス供給ライン3を介して供給される炭酸ガス7と、水供給源4から水供給ライン5を介して供給される水6を混合して炭酸水8とする縦長の混合タンク9と、該混合タンク9の下部にその一端部10aが接続され、その他端部10bが混合タンクの上部に接続された循環ライン10と、該循環ライン10に設けられた冷却手段11と、該循環ライン10に仕切弁12を介して接続され、炭酸水8を外部へ供給する炭酸水供給ライン13と、該炭酸水供給ライン13に接続された供給ノズル14と、前記炭酸水8と混合して提供される飲料15を供給する飲料供給源16と、該飲料供給源16と飲料用仕切弁17を介して接続され、前記供給ノズル14に飲料15を供給する飲料供給ライン18とで構成されている。
The carbonated water manufacturing apparatus 1 is a small-sized device mainly installed in a restaurant or the like.
As shown in FIG. 1, the carbonated water production apparatus 1 includes a carbon dioxide supply line 3 having a carbon dioxide supply source 2, a water supply line 5 having a water supply source 4, the carbon dioxide supply line 3 and water. Carbon dioxide gas 7 connected to the supply line 5 and supplied from the carbon dioxide supply source 2 via the carbon dioxide supply line 3 is mixed with water 6 supplied from the water supply source 4 via the water supply line 5. A vertically long mixing tank 9 serving as carbonated water 8, a circulation line 10 having one end 10 a connected to the lower part of the mixing tank 9, and another end 10 b connected to the upper part of the mixing tank; A cooling means 11 provided, a carbonated water supply line 13 connected to the circulation line 10 via a gate valve 12 to supply carbonated water 8 to the outside, and a supply nozzle 14 connected to the carbonated water supply line 13 And the carbonated water 8 A beverage supply source 16 that supplies a beverage 15 that is provided by mixing, and a beverage supply line 18 that is connected to the beverage supply source 16 via a beverage gate valve 17 and supplies the beverage 15 to the supply nozzle 14. It is configured.

炭酸ガス供給ライン3は、図2に示すように、炭酸ガス供給源2として炭酸ガスボンベを用いており、該炭酸ガス供給源2に接続された減圧弁19とで構成されている。この減圧弁19は、炭酸ガス供給源2から供給される炭酸ガス7の圧力を調整している。本実施形態においては、炭酸ガス7の圧力は0.7MPaとなるように減圧されており、その圧力は最大でも0.75MPa以下となることが望ましい。このような圧力にすることにより、後述する水供給ライン5から供給される水の圧力を本実施形態では0.95MPa以下にすることができ、高圧ガス保安法の適用を受けない炭酸水の製造装置1とすることができるとともに、装置を小型化することができる。   As shown in FIG. 2, the carbon dioxide supply line 3 uses a carbon dioxide cylinder as the carbon dioxide supply source 2, and includes a pressure reducing valve 19 connected to the carbon dioxide supply source 2. The pressure reducing valve 19 adjusts the pressure of the carbon dioxide 7 supplied from the carbon dioxide supply source 2. In the present embodiment, the pressure of the carbon dioxide gas 7 is reduced to 0.7 MPa, and the pressure is desirably 0.75 MPa or less at the maximum. By making such a pressure, the pressure of water supplied from a water supply line 5 described later can be reduced to 0.95 MPa or less in the present embodiment, and production of carbonated water not subject to the application of the high-pressure gas safety method. While being able to be set as the apparatus 1, the apparatus can be reduced in size.

この炭酸ガス供給ライン3は、常時炭酸ガス7を混合タンク9へ供給している。
水供給ライン5は、図3に示すように、本実施形態では水道水を用いた水供給源4と、該水供給源4に接続された水処理フィルター20と、該水処理フィルター20の下流に設けられた給水弁21と、この給水弁21の下流に設けられた給水ポンプ22と、該給水ポンプ22と混合タンク9の間に設けられた逆止弁23とで構成されている。
The carbon dioxide supply line 3 constantly supplies carbon dioxide 7 to the mixing tank 9.
As shown in FIG. 3, the water supply line 5 includes a water supply source 4 using tap water, a water treatment filter 20 connected to the water supply source 4, and a downstream of the water treatment filter 20. A water supply valve 21 provided in the water supply valve 21, a water supply pump 22 provided downstream of the water supply valve 21, and a check valve 23 provided between the water supply pump 22 and the mixing tank 9.

この水供給ライン5は、本実施形態では混合タンク9の上部に接続されており、混合タンク9へ水6を供給する場合には、そのまま混合タンク9内へ水6自然に落下する形態となっているが、この水供給ライン5の終端部に、噴射ノズルを設けて、水供給ライン5から混合タンク9へ水6を供給する際に、噴霧して供給してもよい。   This water supply line 5 is connected to the upper part of the mixing tank 9 in this embodiment, and when water 6 is supplied to the mixing tank 9, the water 6 naturally falls into the mixing tank 9 as it is. However, when the water 6 is supplied from the water supply line 5 to the mixing tank 9 by providing an injection nozzle at the end of the water supply line 5, it may be supplied by spraying.

前記給水ポンプ22は、本実施形態では水供給源4である水道管4から0.3MPaで供給された水道水6を0.95MPaで圧送しており、この給水ポンプ22の2次側の圧力は、最大でも混合タンク9内部の圧力が高圧ガス保安法の適用がない圧力値(1MPa未満)で、かつ、炭酸ガス7の圧力よりも0.2MPa程度高圧となるように調整することが望ましい。   In the present embodiment, the water supply pump 22 pumps tap water 6 supplied at 0.3 MPa from the water pipe 4, which is the water supply source 4, at 0.95 MPa, and the pressure on the secondary side of the water supply pump 22. Is preferably adjusted so that the pressure inside the mixing tank 9 is a pressure value (less than 1 MPa) at which the high-pressure gas safety method is not applied and is about 0.2 MPa higher than the pressure of the carbon dioxide gas 7. .

この水供給ライン5に設けられた給水弁21は、混合タンク9の内部に設けられた上部レベルセンサー24と制御部25を介して接続されており、この上部レベルセンサー24の位置に常時水面(液面)が位置するように制御部25により開閉制御される。   A water supply valve 21 provided in the water supply line 5 is connected to an upper level sensor 24 provided in the mixing tank 9 via a control unit 25, and a water surface ( The controller 25 is controlled to open and close so that the liquid level is located.

前記混合タンク9は、本実施形態では直径100mm、高さ300mmの円筒状のタンクであり、その上面に前記水供給ライン5及び循環ラインの他端部10bが接続されており、その上部よりの側面には、炭酸ガス供給ライン3が接続されている。この炭酸ガス供給ライン3は、本実施形態では上面から75mmの位置に接続されている。   In the present embodiment, the mixing tank 9 is a cylindrical tank having a diameter of 100 mm and a height of 300 mm, and the water supply line 5 and the other end portion 10b of the circulation line are connected to the upper surface of the mixing tank 9 from the upper part thereof. A carbon dioxide gas supply line 3 is connected to the side surface. In this embodiment, the carbon dioxide supply line 3 is connected to a position 75 mm from the upper surface.

また、この混合タンク9の上面には、混合タンク9の内部と連通し、混合タンク9内の圧力が高くなった場合に、炭酸ガス7を大気へ自動で排出するリリーフ弁26と、炭酸ガス7を手動で大気へ排出するブロー弁27が設けられている。   The upper surface of the mixing tank 9 communicates with the inside of the mixing tank 9, and when the pressure in the mixing tank 9 becomes high, a relief valve 26 that automatically discharges the carbon dioxide 7 to the atmosphere, and carbon dioxide A blow valve 27 for manually discharging 7 to the atmosphere is provided.

この混合タンク9の上部よりの側面には、前記炭酸ガス供給ライン3が接続されている。
この混合タンク9の内部には、液面の位置を検知する上部レベルセンサー24及び下部レベルセンサー28が設けられており、上部レベルセンサー24で検知した信号により制御部25で給水弁21を開閉する。なお、給水ポンプ22はこの給水弁21と連動して運転するように制御部25で制御するとよい。
The carbon dioxide supply line 3 is connected to the side surface of the mixing tank 9 from above.
Inside the mixing tank 9, an upper level sensor 24 and a lower level sensor 28 for detecting the position of the liquid level are provided, and the control unit 25 opens and closes the water supply valve 21 according to a signal detected by the upper level sensor 24. . The water supply pump 22 may be controlled by the control unit 25 so as to operate in conjunction with the water supply valve 21.

また、下部レベルセンサー28は制御部25を介して後述する循環ポンプ29と接続されている。この下部レベルセンサー28の位置まで何らかの理由で液面が低下した場合には、循環ポンプ29の空運転を防止するために循環ポンプ29を緊急停止させる。
この上部レベルセンサー24は本実施形態では、底面から160mmの位置に設けられており、下部レベルセンサー28は上部レベルセンサーから120mm下方に設けられている。
Further, the lower level sensor 28 is connected to a circulation pump 29 described later via the control unit 25. When the liquid level drops for some reason to the position of the lower level sensor 28, the circulation pump 29 is urgently stopped to prevent the circulation pump 29 from being idle.
In the present embodiment, the upper level sensor 24 is provided at a position 160 mm from the bottom surface, and the lower level sensor 28 is provided 120 mm below the upper level sensor.

循環ライン10は、図4に示すように、混合タンク9の下部にその一端部10aが接続され、その他端部10bが混合タンクの上部に接続されており、この循環ライン10には冷却手段11としてのプレート式熱交換器11と、循環ポンプ29が設けられている。   As shown in FIG. 4, the circulation line 10 has one end 10 a connected to the lower part of the mixing tank 9 and the other end 10 b connected to the upper part of the mixing tank. The plate heat exchanger 11 and the circulation pump 29 are provided.

この循環ライン10の他端部10bには噴射ノズル30が設けられており、循環ライン10を循環した炭酸水8は、噴射ノズル30から霧状に混合タンク8の内部に噴霧され、前記炭酸ガス供給ライン3から混合タンク8の内部に供給された炭酸ガス7と接触する面積を最大化している。また、噴霧された炭酸水8は、混合タンク9の内壁面に付着し、下方へ流れていくので、炭酸水8と炭酸ガス7の接触時間も大幅に増加させることができる。このような作用により、低圧の炭酸ガス7及び極低温(1℃程度)ではない水6、例えば1℃から10℃、望ましくは1℃から5℃程度の温度の水6を用いても、高濃度の炭酸水8とすることができる。なお、循環ライン10の他端部10bに噴射ノズル30を設けない形態としてもよい。   An injection nozzle 30 is provided at the other end portion 10b of the circulation line 10, and the carbonated water 8 circulated through the circulation line 10 is sprayed from the injection nozzle 30 into the inside of the mixing tank 8 in the form of mist. The area in contact with the carbon dioxide gas 7 supplied from the supply line 3 to the inside of the mixing tank 8 is maximized. Further, since the sprayed carbonated water 8 adheres to the inner wall surface of the mixing tank 9 and flows downward, the contact time between the carbonated water 8 and the carbon dioxide gas 7 can be greatly increased. By such an action, even if low pressure carbon dioxide gas 7 and water 6 which is not extremely low temperature (about 1 ° C.), for example, water 6 having a temperature of about 1 ° C. to 10 ° C., preferably about 1 ° C. to 5 ° C. are used, The concentration of carbonated water 8 can be obtained. In addition, it is good also as a form which does not provide the injection nozzle 30 in the other end part 10b of the circulation line 10. FIG.

プレート式熱交換器11は、炭酸水8よりも低温の流体と熱交換するものであり、本実施形態では、低温の流体として飲食店等の店舗に本発明の炭酸水の製造装置1と併設されるビールサーバー等のチラー水を用いている。このようにビールサーバーのチラー水程度の温度の流体を用いた場合であっても、炭酸水8を循環ライン10で循環させることにより、高濃度の炭酸水8とすることができる。このような冷却手段11を用いることにより、本発明の炭酸水の製造装置1をより小型化することができる。   The plate heat exchanger 11 exchanges heat with a fluid having a temperature lower than that of the carbonated water 8. In the present embodiment, the carbonated water production apparatus 1 of the present invention is provided in a store such as a restaurant as a low temperature fluid. Chiller water such as beer server is used. Thus, even when a fluid having a temperature of about the temperature of chiller water of a beer server is used, the carbonated water 8 can be circulated through the circulation line 10 to obtain a highly concentrated carbonated water 8. By using such a cooling means 11, the apparatus 1 for producing carbonated water of the present invention can be further downsized.

ところで、本実施形態では冷却手段11としてプレート式の熱交換器を用いているが、その他の公知の冷却手段(熱交換器等)を用いることができる。   By the way, in this embodiment, although the plate-type heat exchanger is used as the cooling means 11, other well-known cooling means (heat exchanger etc.) can be used.

循環ライン10は本実施形態では、常時混合タンク9内の液体(炭酸水8)を循環させており、高濃度の炭酸水となるように炭酸ガスを溶解させるものである。   In the present embodiment, the circulation line 10 constantly circulates the liquid (carbonated water 8) in the mixing tank 9, and dissolves the carbon dioxide gas so as to become highly concentrated carbonated water.

炭酸水供給ライン13は、図5に示すように、循環ライン10に仕切弁12を介して接続されており、この炭酸水供給ライン13の終端部には、供給ノズル14が接続されている。前記仕切弁12を開状態とすると、循環ライン10を循環している炭酸水8が炭酸水供給ライン13へ流入し、供給ノズル14から炭酸水8が外部へと供給される。本実施形態では、この供給ノズル14は飲料供給ライン18から供給された飲料15も外部へと供給している。この飲料15は飲料用ポンプ31により飲料供給源16から圧送され、飲料用仕切弁17の開閉操作により供給ノズル14から供給される。この飲料用仕切弁17は、本実施形態では常時開のボール弁が用いられており、前記仕切弁12が開となった場合には、前記飲料用ポンプ31が運転するように制御部25によって制御されており、任意の濃度となるように飲料15と炭酸水8が供給ノズル14から供給され、外部に配置されたグラス等の中で混合される。   As shown in FIG. 5, the carbonated water supply line 13 is connected to the circulation line 10 via a gate valve 12, and a supply nozzle 14 is connected to the end of the carbonated water supply line 13. When the gate valve 12 is opened, the carbonated water 8 circulating in the circulation line 10 flows into the carbonated water supply line 13, and the carbonated water 8 is supplied from the supply nozzle 14 to the outside. In this embodiment, the supply nozzle 14 also supplies the beverage 15 supplied from the beverage supply line 18 to the outside. The beverage 15 is pumped from the beverage supply source 16 by the beverage pump 31 and is supplied from the supply nozzle 14 by opening and closing the beverage gate valve 17. In the present embodiment, the beverage gate valve 17 is a normally open ball valve. When the gate valve 12 is opened, the control unit 25 controls the beverage pump 31 to operate. The beverage 15 and carbonated water 8 are supplied from the supply nozzle 14 so as to have an arbitrary concentration, and are mixed in a glass or the like disposed outside.

ところで、飲料用仕切弁17に電磁弁を用いて、仕切弁12と連動して開閉するように制御してもよいし、この供給ノズル14の内部で飲料15と炭酸水8とを混合できるようなノズルを用いてもよい。   By the way, an electromagnetic valve may be used for the beverage gate valve 17 so as to be opened and closed in conjunction with the gate valve 12, and the beverage 15 and the carbonated water 8 can be mixed inside the supply nozzle 14. A simple nozzle may be used.

飲料供給ライン18は、前述のように飲料供給源16と、該飲料供給源16の下流に設けられた飲料用ポンプ31と、該飲料用ポンプ31と供給ノズル14の間に介装された飲料用仕切弁17とで構成されている。   As described above, the beverage supply line 18 includes the beverage supply source 16, the beverage pump 31 provided downstream of the beverage supply source 16, and the beverage interposed between the beverage pump 31 and the supply nozzle 14. The gate valve 17 is configured.

飲料供給ライン18から供給される飲料15としては、例えば清涼飲料水の原液(シロップ)や、焼酎、ウイスキー、果実酒、スピリッツ、ブランデー、清酒等のアルコール類等がある。   Examples of the beverage 15 supplied from the beverage supply line 18 include a soft drink stock solution (syrup), alcohol such as shochu, whiskey, fruit liquor, spirits, brandy, and sake.

また、本発明の炭酸水の製造方法32としては、図6に示すように、混合タンク9に炭酸ガス7を常時供給する炭酸ガス供給工程33と、前記混合タンク9に水6を供給する水供給工程34と、混合タンク9内の液体(炭酸水8)を連続的又は断続的のいずれか、本実施形態では好ましくは連続的に循環させ、水に高濃度で炭酸ガスを溶解させて高濃度の炭酸水とする炭酸ガス溶解工程35と、混合タンク9内で製造された炭酸水8を供給する炭酸水供給工程36とで構成されている。   Further, as shown in FIG. 6, the carbonated water production method 32 of the present invention includes a carbon dioxide supply step 33 for constantly supplying carbon dioxide 7 to the mixing tank 9, and water for supplying water 6 to the mixing tank 9. The supply process 34 and the liquid (carbonated water 8) in the mixing tank 9 are circulated either continuously or intermittently in this embodiment, preferably continuously, and the carbon dioxide gas is dissolved in water at a high concentration to increase the concentration. A carbon dioxide gas dissolving step 35 for producing carbonated water having a concentration and a carbonated water supply step 36 for supplying carbonated water 8 produced in the mixing tank 9 are constituted.

炭酸ガス供給工程33では、前述のように、炭酸ガス供給源2から炭酸ガス供給ライン3を通じて常時炭酸ガス7を混合タンク9に供給する工程である。
水供給工程34では、水供給源4から水供給ライン5を通じて水6を混合タンク9へ供給する工程で、水6は、前記上部レベルセンサー24の信号により給水弁21の開閉により供給量や供給時期が決定される。
In the carbon dioxide supply step 33, as described above, the carbon dioxide 7 is constantly supplied from the carbon dioxide supply source 2 to the mixing tank 9 through the carbon dioxide supply line 3.
In the water supply step 34, the water 6 is supplied from the water supply source 4 to the mixing tank 9 through the water supply line 5, and the water 6 is supplied and supplied by opening and closing the water supply valve 21 according to the signal of the upper level sensor 24. The timing is determined.

炭酸ガス溶解工程35は、前述のように、本実施形態では常時混合タンク9内の炭酸水8を循環ライン10に循環させ、高濃度の炭酸水8を製造する工程である。
このようにして製造された炭酸水8は炭酸水供給工程36により、炭酸水供給ライン13を通じて供給ノズル14から外部に供給される。
As described above, the carbon dioxide gas dissolving step 35 is a step of manufacturing the high-concentration carbonated water 8 by constantly circulating the carbonated water 8 in the mixing tank 9 to the circulation line 10 in the present embodiment.
The carbonated water 8 produced in this way is supplied to the outside from the supply nozzle 14 through the carbonated water supply line 13 in the carbonated water supply process 36.

なお、炭酸水供給工程36を行わず、水に高濃度で炭酸ガスを溶解させる方法37としてもよい。   In addition, it is good also as the method 37 which dissolves carbon dioxide gas with high concentration in water, without performing the carbonated water supply process 36.

[発明を実施するための異なる形態]
次に、図7及び図8に示す本発明を実施するための異なる形態につき説明する。なお、これらの本発明を実施するための異なる形態の説明に当って、前記本発明を実施するための第1の形態と同一構成部分には同一符号を付して重複する説明を省略する。
図7及び図8に示す本発明を実施するための第2の形態において、前記本発明を実施するための第1の形態と主に異なる点は、混合タンク9の内部の液体(炭酸水8)を断続的に循環ライン10に循環させるように制御する炭酸水の製造装置1Aとし、このように循環させる炭酸ガス溶解工程35Aを用いた炭酸水の製造方法32A及び水に高濃度で炭酸ガスを溶解させる方法37Aにしても、前記本発明を実施するための第1の形態と同様な作用効果が得られる。
[Different forms for carrying out the invention]
Next, different modes for carrying out the present invention shown in FIGS. 7 and 8 will be described. In the description of the different embodiments for carrying out the present invention, the same components as those in the first embodiment for carrying out the present invention are denoted by the same reference numerals, and redundant description is omitted.
The second embodiment for carrying out the present invention shown in FIGS. 7 and 8 is mainly different from the first embodiment for carrying out the present invention in that the liquid in the mixing tank 9 (carbonated water 8 ) Is intermittently circulated in the circulation line 10, and the carbonated water production apparatus 1 A is controlled to circulate in this manner. Even when the method 37A is used to dissolve the water, the same effects as those of the first embodiment for carrying out the present invention can be obtained.

この炭酸ガス溶解工程35Aでは、例えば5分間混合タンク9の内部の液体を循環させた後、5分間は循環を停止させ、その後5分間循環させる等を繰り返す制御が行われる。ところで、この循環・停止させる時間は、適宜変更できるものである。
なお、本発明の実施形態では飲料供給源や飲料供給路等を有し、これらを炭酸水と混合して提供する形態について説明したが、これらの構成を有さず、炭酸水のみを提供する炭酸水の製造装置や炭酸水の製造方法としてもよい。
In this carbon dioxide gas dissolving step 35A, for example, after the liquid inside the mixing tank 9 is circulated for 5 minutes, the circulation is stopped for 5 minutes, and then circulated for 5 minutes. By the way, the circulation / stop time can be changed as appropriate.
In addition, although embodiment which has a drink supply source, a drink supply path, etc. and mixed these with carbonated water was demonstrated in embodiment of this invention, it does not have these structures and provides only carbonated water. It may be a carbonated water production apparatus or a carbonated water production method.

本発明は炭酸水を製造する産業及び、飲食店等の店舗等に利用される。   The present invention is used in industries that produce carbonated water and stores such as restaurants.

1、1A:炭酸水の製造装置、 2:炭酸ガス供給源、
3、3A:炭酸ガス供給ライン、 4:水供給源、
5:水供給ライン、 6:水、
7:炭酸ガス、 8:炭酸水、
9:混合タンク、 10:循環ライン、
11:冷却手段、 12:仕切弁、
13:炭酸水供給ライン、 14:供給ノズル、
15:飲料、 16:飲料供給源、
17:飲料用仕切弁、 18:飲料供給ライン、
19:減圧弁、 20:水処理フィルター、
21:給水弁、 22:給水ポンプ、
23:逆止弁、 24:上部レベルセンサー、
25:制御部、 26:リリーフ弁、
27:ブロー弁、 28:下部レベルセンサー、
29:循環ポンプ、 30:噴射ノズル、
31:飲料用ポンプ、 32:炭酸水の製造方法、
33:炭酸ガス供給工程、 34:水供給工程、
35、35A:炭酸ガス溶解工程、 36:炭酸水供給工程、
37、37A:水に高濃度で炭酸ガスを溶解させる方法。
1, 1A: Carbonated water production device, 2: Carbon dioxide gas supply source,
3, 3A: Carbon dioxide supply line, 4: Water supply source,
5: Water supply line, 6: Water,
7: Carbon dioxide, 8: Carbonated water,
9: Mixing tank, 10: Circulation line,
11: Cooling means, 12: Gate valve,
13: carbonated water supply line, 14: supply nozzle,
15: beverage, 16: beverage source,
17: Beverage gate valve, 18: Beverage supply line,
19: Pressure reducing valve, 20: Water treatment filter,
21: Water supply valve, 22: Water supply pump,
23: Check valve, 24: Upper level sensor,
25: Control unit, 26: Relief valve,
27: Blow valve, 28: Lower level sensor,
29: Circulation pump, 30: Injection nozzle,
31: Beverage pump, 32: Production method of carbonated water,
33: Carbon dioxide supply process, 34: Water supply process,
35, 35A: carbon dioxide dissolving step, 36: carbonated water supply step,
37, 37A: A method of dissolving carbon dioxide gas in water at a high concentration.

Claims (9)

炭酸ガス供給源を有する炭酸ガス供給ラインと、水供給源を有する水供給ラインと、前記炭酸ガス供給ライン及び水供給ラインに接続され、前記炭酸ガス供給ラインからの炭酸ガスと前記水供給ラインからの水を混合して炭酸水とする混合タンクと、該混合タンクの下部にその一端部が接続され、その他端部が混合タンクの上部に接続された循環ラインと、該循環ラインに設けられた冷却手段と、該循環ラインに仕切弁を介して接続され、前記炭酸水を外部へ供給する炭酸水供給ラインと、該炭酸水供給ラインに接続された供給ノズルとで構成され、前記炭酸ガス供給ラインは、前記混合タンクに常時炭酸ガスを供給するものであり、前記循環ラインは、前記混合タンク内の液体を連続的又は断続的に循環させることにより、前記水に高濃度で前記炭酸ガスを溶解させる炭酸水の製造装置。 A carbon dioxide gas supply line having a carbon dioxide gas supply source; a water supply line having a water supply source; and the carbon dioxide gas supply line and the water supply line connected to the carbon dioxide gas supply line and the water supply line. A mixing tank that is mixed with water to form carbonated water, a circulation line having one end connected to the lower part of the mixing tank and the other end connected to the upper part of the mixing tank, and the circulation line. The carbon dioxide gas supply comprising a cooling means, a carbonated water supply line connected to the circulation line via a gate valve and supplying the carbonated water to the outside, and a supply nozzle connected to the carbonated water supply line The line constantly supplies carbon dioxide gas to the mixing tank, and the circulation line has a high concentration in the water by continuously or intermittently circulating the liquid in the mixing tank. Apparatus for producing carbonated water to dissolve the carbonic acid gas. 炭酸ガス供給源を有する炭酸ガス供給ラインと、水供給源を有する水供給ラインと、前記炭酸ガス供給ライン及び水供給ラインに接続され、前記炭酸ガス供給ラインからの炭酸ガスと前記水供給ラインからの水を混合して炭酸水とする混合タンクと、該混合タンクの下部にその一端部が接続され、その他端部が混合タンクの上部に接続された循環ラインと、該循環ラインに設けられた冷却手段と、該循環ラインに仕切弁を介して接続され、前記炭酸水を外部へ供給する炭酸水供給ラインと、該炭酸水供給ラインに接続された供給ノズルと、前記炭酸水と混合して提供される飲料を供給する飲料供給源と、該飲料供給源と飲料用仕切弁を介して接続され、前記供給ノズルに前記飲料を供給する飲料供給ラインとで構成され、前記炭酸ガス供給ラインは、前記混合タンクに常時炭酸ガスを供給するものであり、前記循環ラインは、前記混合タンク内の液体を連続的又は断続的に循環させることにより、前記水に高濃度で前記炭酸ガスを溶解させる炭酸水の製造装置。 A carbon dioxide gas supply line having a carbon dioxide gas supply source; a water supply line having a water supply source; and the carbon dioxide gas supply line and the water supply line connected to the carbon dioxide gas supply line and the water supply line. A mixing tank that is mixed with water to form carbonated water, a circulation line having one end connected to the lower part of the mixing tank and the other end connected to the upper part of the mixing tank, and the circulation line. A cooling means, a carbonated water supply line connected to the circulation line via a gate valve and supplying the carbonated water to the outside, a supply nozzle connected to the carbonated water supply line, and the carbonated water mixed. A beverage supply source for supplying a beverage to be provided; and a beverage supply line connected to the beverage supply source and a beverage gate valve for supplying the beverage to the supply nozzle; The carbon dioxide gas is constantly supplied to the mixing tank, and the circulation line circulates the liquid in the mixing tank continuously or intermittently, thereby supplying the water with a high concentration of the carbon dioxide gas. A device for producing carbonated water to be dissolved. 前記炭酸ガス供給源から供給される炭酸ガスの圧力は0.75MPa以下であることを特徴とする請求項1又は請求項2のいずれかに記載の炭酸水の製造装置。 The apparatus for producing carbonated water according to claim 1, wherein the pressure of carbon dioxide supplied from the carbon dioxide supply source is 0.75 MPa or less. 前記循環路の他端部には、循環路を循環した液体を霧状に前記混合タンク内に噴霧する噴射ノズルが設けられていることを特徴とする請求項1乃至請求項3のいずれかに記載の炭酸水の製造装置。 The spray nozzle which sprays the liquid which circulated through the circulation path in the shape of the mist in the mixing tank is provided in the other end part of the circulation path. The apparatus for producing carbonated water as described. 前記冷却手段は、プレート式熱交換器であることを特徴とする請求項1乃至請求項4のいずれかに記載の炭酸水の製造装置。 The apparatus for producing carbonated water according to any one of claims 1 to 4, wherein the cooling means is a plate heat exchanger. 混合タンクに炭酸ガスを常時供給する炭酸ガス供給工程と、前記混合タンクに水を供給する水供給工程と、前記混合タンク内の液体を連続的又は断続的に循環させ、前記水に高濃度で前記炭酸ガスを溶解させた炭酸水とする炭酸ガス溶解工程と、前記混合タンク内の前記炭酸水を供給する炭酸水供給工程とで構成される炭酸水の製造方法。 A carbon dioxide supply step for constantly supplying carbon dioxide to the mixing tank; a water supply step for supplying water to the mixing tank; and a liquid in the mixing tank is circulated continuously or intermittently, so that the water has a high concentration. A method for producing carbonated water, comprising: a carbon dioxide gas dissolving step for producing carbonated water in which the carbon dioxide gas is dissolved; and a carbonated water supply step for supplying the carbonated water in the mixing tank. 前記炭酸ガス供給工程では、炭酸水と飲料を混合して提供することを特徴とする請求項6に記載の炭酸水の製造方法。 The method for producing carbonated water according to claim 6, wherein in the carbon dioxide supply step, carbonated water and a beverage are mixed and provided. 前記炭酸ガス供給工程で供給される炭酸ガスの圧力は0.75MPa以下であることを特徴とする請求項6又は請求項7のいずれかに記載の炭酸水の製造方法。 The method for producing carbonated water according to claim 6 or 7, wherein the pressure of the carbon dioxide gas supplied in the carbon dioxide supply step is 0.75 MPa or less. 混合タンクに炭酸ガスを常時供給する炭酸ガス供給工程と、前記混合タンクに水を供給する水供給工程と、前記混合タンク内の液体を連続的又は断続的に循環させ、前記水に高濃度で前記炭酸ガスを溶解させた炭酸水とする炭酸ガス溶解工程とで構成される水に高濃度で炭酸ガスを溶解させる方法。 A carbon dioxide supply step for constantly supplying carbon dioxide to the mixing tank; a water supply step for supplying water to the mixing tank; and a liquid in the mixing tank is circulated continuously or intermittently, so that the water has a high concentration. A method of dissolving carbon dioxide gas at a high concentration in water composed of a carbon dioxide gas dissolving step in which carbon dioxide gas is dissolved into carbonated water.
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