JP2003231592A - Apparatus and method for manufacturing gas dissolved beverage - Google Patents

Apparatus and method for manufacturing gas dissolved beverage

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Publication number
JP2003231592A
JP2003231592A JP2002032473A JP2002032473A JP2003231592A JP 2003231592 A JP2003231592 A JP 2003231592A JP 2002032473 A JP2002032473 A JP 2002032473A JP 2002032473 A JP2002032473 A JP 2002032473A JP 2003231592 A JP2003231592 A JP 2003231592A
Authority
JP
Japan
Prior art keywords
tank
beverage
gas
storage tank
carbon dioxide
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP2002032473A
Other languages
Japanese (ja)
Inventor
Akihisa Minato
明久 湊
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
AQUATECH KK
Aquatech Corp
Original Assignee
AQUATECH KK
Aquatech Corp
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by AQUATECH KK, Aquatech Corp filed Critical AQUATECH KK
Priority to JP2002032473A priority Critical patent/JP2003231592A/en
Publication of JP2003231592A publication Critical patent/JP2003231592A/en
Pending legal-status Critical Current

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Abstract

<P>PROBLEM TO BE SOLVED: To provide an apparatus and a method for manufacturing a carbonated beverage with which a required amount of carbonic acid can be poured at a bar or the like. <P>SOLUTION: The apparatus includes a pressure tank 1 for storing sake to be processed, an aerating membrane module 2 for accepting the sake in the tank 1 at one of internal and external sides of a hollow fiber membrane, a carbon dioxide gas tank 4 for feeding a carbon dioxide gas to the other of the internal and external sides of the hollow fiber membrane, and a self-priming pump 3 for cyclically feeding a beverage output from the pressure tank 1 and processed by the module 2 to the tank 1. The pressure tank is movable, and it is constructed so that a tank body 11 and an input/output part 12 are detachable. <P>COPYRIGHT: (C)2003,JPO

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【発明の属する技術分野】本発明は、居酒屋などで簡易
に炭酸入りの飲料などを製造できる製造装置及びその方
法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a manufacturing apparatus and a method for manufacturing carbonated beverages easily in an izakaya or the like.

【0002】[0002]

【従来の技術】従来、日本酒は、適度に加温して飲むの
が旨いとされており、居酒屋などでは、専ら、お燗状態
で提供されるのが一般的である。しかし、近年、日本酒
の消費量は減少傾向にあり、特に、若者層からはイメー
ジ的にも敬遠される傾向があった。なお、冷酒と称され
て、適度に冷やして飲む日本酒も提供されているが、そ
れほど消費が伸びていないのが実情である。
2. Description of the Related Art Conventionally, it has been said that sake should be heated after being moderately heated, and it is generally offered in a tasting state at taverns and the like. However, in recent years, the consumption of sake has been declining, and in particular, there has been a tendency for young people to dislike it. It should be noted that although sake called cold drink, which is appropriately cooled, is also offered, the reality is that consumption has not increased so much.

【0003】日本酒のこのような実情に相反するよう
に、生ビールは、近年着実にその消費量を伸ばしてお
り、若者層にも大きな支持を得ている。ビールにおいて
も苦味の強い従来タイプのものより喉ごしの良い生ビー
ルが好まれていることより、日本酒においても、ある程
度さっぱりした飲み心地が必要であるものと解される。
Contrary to the actual situation of sake, draft beer has been steadily increasing in consumption in recent years, and has been well received by young people. As for beer, draft beer with a good taste is preferred to the conventional type that has a strong bitterness, and it is understood that sake also needs a refreshing feeling to some extent.

【0004】かかる実情を検討するとき、日本酒につい
ても炭酸ガスを注入することで、さっぱりと飲み易いも
のに改善できれば炭酸飲料を好む若者層にも大きな支持
が得られるものと期待される。
[0004] When examining such a situation, it is expected that the injection of carbon dioxide gas into sake will improve the taste of the sake to make it refreshingly easy to drink, and will be greatly supported by the younger people who prefer carbonated drinks.

【0005】[0005]

【発明が解決しようとする課題】しかしながら、高齢層
を中心に本来の飲み方を希望する日本酒ファンも多いの
も事実であり、若者による消費増大が期待できるとはい
え、製造工場の製造ラインを新規に構築してまで製造す
るほどの必要性は感じられない。また、鮮度を維持する
と共に、顧客の好みに即応できるようエンドユーザに近
いところで炭酸を注入できる装置が望まれるところであ
る。
However, it is a fact that there are many sake fans who prefer the original way of drinking, mainly among the elderly, and although it can be expected that the consumption of young people will increase, the production line of the manufacturing plant will be increased. I don't feel the need to build a new product. There is also a need for a device that can inject carbonic acid close to the end user so as to maintain freshness and quickly respond to customer preferences.

【0006】また、日本酒に限らず、ワインや焼酎やビ
ールなどついても、顧客の好みに合わせて必要量の炭酸
を注入できれば極めて好ましい。更にまた、酸素ガスを
所定の高濃度に溶存させた水についても、これを簡易に
製造できれば、水割りやその他の用途に有効に使用でき
る。
Further, not only sake but also wine, shochu, beer and the like are extremely preferable as long as the required amount of carbonic acid can be injected according to the customer's preference. Furthermore, water in which oxygen gas is dissolved at a predetermined high concentration can be effectively used for water splitting and other purposes if it can be easily produced.

【0007】この発明は、上記の課題に鑑みてなされた
ものであって、居酒屋などにおいて必要量の炭酸ガスや
酸素ガスを注入可能なガス溶存飲料の製造装置及びその
方法を提供することを課題とする。
The present invention has been made in view of the above problems, and it is an object of the present invention to provide an apparatus and a method for producing a gas-dissolved beverage capable of injecting a necessary amount of carbon dioxide gas or oxygen gas in a pub or the like. And

【0008】[0008]

【課題を解決するための手段】上記の課題を解決するた
め、本発明に係るガス溶存飲料の製造装置は、被処理用
の飲料を蓄える貯留タンクと、前記貯留タンクの飲料を
中空糸膜の内外一方側に受ける給気膜モジュールと、前
記中空糸膜の内外他方側に炭酸ガス又は酸素ガスを供給
するガスタンクと、前記貯留タンクから出力され前記給
気膜モジュールで処理された後の飲料を、前記貯留タン
クに循環的に供給する駆動部とを備え、前記貯留タンク
は、移動可能であると共に、タンク本体と入出力部とが
着脱自在に構成されている。
In order to solve the above problems, the apparatus for producing a gas-dissolved beverage according to the present invention comprises a storage tank for storing a beverage to be treated and a hollow fiber membrane for storing the beverage in the storage tank. An air supply membrane module that receives one side inside and outside, a gas tank that supplies carbon dioxide gas or oxygen gas to the other side inside and outside the hollow fiber membrane, and a beverage that has been output from the storage tank and processed by the air supply membrane module. The storage tank is movable, and the tank body and the input / output unit are detachably configured.

【0009】また、本発明に係るガス溶存飲料の製造方
法は、被処理用の飲料を蓄える貯留タンクと、前記貯留
タンクの飲料を中空糸膜の内外一方側に受ける給気膜モ
ジュールと、前記中空糸膜の内外他方側に炭酸ガス又は
酸素ガスを供給するガスタンクとを備え、タンク本体と
入出力部とが着脱自在に構成された移動可能な前記貯留
タンクを用いて、前記貯留タンクと前記給気膜モジュー
ルの間で被処理液を循環させることで炭酸ガス又は酸素
ガスを注入するようにしている。
Further, the method for producing a gas-dissolved beverage according to the present invention comprises: a storage tank for storing a beverage to be treated; A gas tank for supplying carbon dioxide gas or oxygen gas to the other side of the hollow fiber membrane is provided, and the tank body and the input / output unit are configured to be removable by using the movable storage tank, and the storage tank and the Carbon dioxide gas or oxygen gas is injected by circulating the liquid to be treated between the gas supply membrane modules.

【0010】[0010]

【発明の実施の形態】以下、実施例に基づいて本発明を
更に詳細に説明する。図1は、ガス溶存飲料の製造装置
について、その正面状態と背面状態とを図示したもので
ある。図示の装置は、圧力タンク1と処理装置EQとで
構成されており、水や酒などに酸素ガスや炭酸ガスを所
定の高濃度で溶存させることができるが、ここでは、炭
酸ガス入りの日本酒(以下、炭酸冷酒と言うことがあ
る)を製造する装置として説明する。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in more detail based on the following examples. FIG. 1 shows a front view and a back view of a device for producing a gas-dissolved beverage. The apparatus shown in the figure is composed of a pressure tank 1 and a processing unit EQ, and can dissolve oxygen gas and carbon dioxide gas in water and liquor at a predetermined high concentration. Here, sake containing carbon dioxide gas is used. (Hereinafter, it may be referred to as carbonated cold liquor) It will be described as an apparatus for manufacturing.

【0011】図2に示すように、この製造装置は、圧力
タンク1と、多数の中空糸膜からなる給気膜モジュール
2と、圧力タンク1に挿入されている内筒10から日本
酒を吸引して給気膜モジュール2に供給する自吸式ポン
プ3と、給気膜モジュール2に所定圧の炭酸ガスを供給
するガスタンク4と、各部の圧力を指示する圧力計5,
6とで構成されている。
As shown in FIG. 2, this manufacturing apparatus sucks sake from a pressure tank 1, an air supply membrane module 2 composed of a large number of hollow fiber membranes, and an inner cylinder 10 inserted in the pressure tank 1. Self-priming pump 3 for supplying air to the air supply membrane module 2, a gas tank 4 for supplying carbon dioxide gas at a predetermined pressure to the air supply membrane module 2, and a pressure gauge 5, which indicates the pressure of each part.
6 and 6.

【0012】この実施例では、圧力タンク1には、別工
程で予め10リットル程度の日本酒が注入されている
が、適宜な冷却機構によって5℃程度に温度管理してお
くのが好ましい。また、炭酸ガスタンク4から給気膜モ
ジュール2に向けて、2〜3kg/cm2程度の圧力で
炭酸ガスが供給される。
In this embodiment, about 10 liters of sake is preliminarily injected into the pressure tank 1 in a separate process, but it is preferable to control the temperature to about 5 ° C. by an appropriate cooling mechanism. Further, carbon dioxide gas is supplied from the carbon dioxide gas tank 4 toward the gas supply membrane module 2 at a pressure of about 2 to 3 kg / cm 2 .

【0013】図2の炭酸飲料製造装置では、循環流路に
設けられた圧力計6の検出値が所定値に達したら、自吸
式ポンプ3の運転が停止されると共に、炭酸ガスタンク
4の出力が停止されるようになっている。そして、この
実施例の場合には、10分程度の運転によって、600
0ppm程度の炭酸ガスを日本酒に注入できる。
In the carbonated beverage manufacturing apparatus of FIG. 2, when the detection value of the pressure gauge 6 provided in the circulation flow path reaches a predetermined value, the operation of the self-priming pump 3 is stopped and the output of the carbon dioxide gas tank 4 is stopped. Is to be stopped. Then, in the case of this embodiment, the operation of about 10 minutes, 600
Carbon dioxide of about 0 ppm can be injected into sake.

【0014】給気膜モジュール2とは、具体的には中空
糸膜モジュールであり、自吸式ポンプ3から供給された
日本酒を通水させつつ中空糸膜の外側から炭酸ガスを供
給して炭酸冷酒を製造するものである。この中空糸膜モ
ジュールは、図3(a)に示すような中空糸膜20を数
千から数万本束ねて形成して、これを支持ケースに入れ
て構成されている。また、この中空糸膜モジュールは、
通常の使用条件下では寿命が長く、かつメンテナンスを
ほとんど必要としない特徴を有している。
The air supply membrane module 2 is specifically a hollow fiber membrane module, and while the sake supplied from the self-priming pump 3 is passed through, carbon dioxide gas is supplied from the outside of the hollow fiber membrane to generate carbon dioxide. It manufactures cold sake. This hollow fiber membrane module is formed by bundling thousands to tens of thousands of hollow fiber membranes 20 as shown in FIG. 3 (a), and putting this in a support case. In addition, this hollow fiber membrane module
It has the characteristics that it has a long life under normal use conditions and requires almost no maintenance.

【0015】給気膜モジュール2を構成する中空糸膜2
0としては、図3(a)に示すように非多孔質膜21を
多孔質膜22,22でサンドイッチ状に挟み込んで筒状
に成形された三層複合膜構造のものを使用することがで
きる。この非多孔質膜21は、水の透過を遮断する一
方、選択的なガス透過性を有するので、中空糸膜の外側
から気体を加圧すると、中空糸膜の内側の水に気体を混
入させることができる。
Hollow fiber membrane 2 constituting the air supply membrane module 2
As 0, it is possible to use a three-layer composite membrane structure in which a non-porous membrane 21 is sandwiched between porous membranes 22 and 22 and formed into a tubular shape as shown in FIG. 3 (a). . Since this non-porous membrane 21 blocks the permeation of water while having selective gas permeability, when gas is applied from the outside of the hollow fiber membrane, the gas is mixed into the water inside the hollow fiber membrane. be able to.

【0016】なお、特に三層複合膜構造のものに限定さ
れるものではなく、ガス脱気性能を有する一層構造のポ
リプロピレン中空フィルタなどでも良い。例えば、0.
03μmの絶対濾過精度を有する中空糸カプセルフィル
タを使用した場合にも、10分程度の運転によって、6
000ppm程度の炭酸ガスを日本酒に注入できること
を確認している。
It should be noted that the structure is not particularly limited to the one having a three-layer composite membrane structure, and a polypropylene hollow filter having a single-layer structure having gas degassing performance may be used. For example, 0.
Even if a hollow fiber capsule filter having an absolute filtration accuracy of 03 μm is used, 6 hours can be obtained by operating for about 10 minutes.
It has been confirmed that about 000 ppm of carbon dioxide can be injected into sake.

【0017】上記いずれの膜構造の場合にも、本装置で
は、図3(b)に示すように、中空糸膜20の内側に日
本酒を通水させつつ、中空糸膜20の外側から炭酸ガス
を加圧しながら供給することによって炭酸冷酒を製造し
ている。但し、中空糸膜20の外側に日本酒を通水させ
つつ、中空糸膜20の内側から炭酸ガスを加圧しながら
供給して炭酸冷酒を製造しても良い。
In any of the above membrane structures, in this apparatus, as shown in FIG. 3 (b), while sake is passed through the inside of the hollow fiber membrane 20, carbon dioxide gas is introduced from the outside of the hollow fiber membrane 20. The cold soda is manufactured by supplying while heating. However, it is also possible to produce carbonated cold liquor by supplying carbon dioxide from the inside of the hollow fiber membrane 20 while pressurizing it while allowing sake to pass through the outside of the hollow fiber membrane 20.

【0018】何れにしても、本装置においては、中空糸
膜20の内外で圧力勾配を生じさせることにより、中空
糸膜20に対する炭酸ガスの溶解効率が非常に高くな
り、原水に対して飽和濃度まで溶解した炭酸冷酒を容易
に製造することができる。
In any case, in this apparatus, by generating a pressure gradient inside and outside the hollow fiber membrane 20, the dissolution efficiency of carbon dioxide gas in the hollow fiber membrane 20 becomes very high, and the saturation concentration with respect to the raw water is increased. It is possible to easily produce cold carbonated sake that has been dissolved.

【0019】図4は、圧力タンクの入出力部を図示した
概略断面図である。この圧力タンクは、内部液を導出す
る円筒状の内筒10を備えたタンク本体11と、タンク
本体11に着脱自在に装着される入出力部12とで構成
されている。タンク本体11は、そのネック部13に内
筒10が内挿されて固定されており、内筒10の本体1
0aはタンク本体11の上端から下端近くに至る長さを
有している(図2、図3(a)参照)。
FIG. 4 is a schematic sectional view showing the input / output section of the pressure tank. This pressure tank is composed of a tank main body 11 having a cylindrical inner cylinder 10 for drawing out the internal liquid, and an input / output unit 12 detachably attached to the tank main body 11. The inner cylinder 10 is inserted and fixed to the neck portion 13 of the tank body 11, and the body 1 of the inner cylinder 10 is fixed.
0a has a length from the upper end to the vicinity of the lower end of the tank body 11 (see FIGS. 2 and 3 (a)).

【0020】内筒10の上端部には、外周部に複数の丸
孔が形成されたハウジング15と、ハウジング15に保
持された第1バネ部材SP1と、内筒本体10aの上部
外周を封止するシール部材SEとが設けられている。ま
た、内筒本体10aの内周側には、内筒本体10aに保
持される第2バネ部材SP2と、第2バネ部材SP2に
よって上向きに付勢される開閉バルブ14が設けられて
いる。
The upper end of the inner cylinder 10 has a housing 15 in which a plurality of round holes are formed in the outer circumference, a first spring member SP1 held by the housing 15, and an upper outer circumference of the inner cylinder body 10a. And a sealing member SE that is provided. Further, a second spring member SP2 held by the inner cylinder body 10a and an opening / closing valve 14 biased upward by the second spring member SP2 are provided on the inner peripheral side of the inner cylinder body 10a.

【0021】この開閉バルブ14が、第2バネ部材SP
2の付勢力によって限界位置まで上昇することで、内筒
本体10aの導出口が確実に閉塞されている(図3
(a))。また、第1バネ部材SP1の付勢力によって
内筒本体10aが限界位置まで上昇することで、シール
部材SEがハウジング15のシール部材と当接して、圧
力タンク1が気密状態に密閉される。
The opening / closing valve 14 is the second spring member SP.
By ascending to the limit position by the urging force of 2, the outlet of the inner cylinder body 10a is reliably closed (FIG. 3).
(A)). Further, the inner cylinder body 10a is raised to the limit position by the urging force of the first spring member SP1, the seal member SE comes into contact with the seal member of the housing 15, and the pressure tank 1 is hermetically sealed.

【0022】入出力部12は、圧力タンク1からの液体
を導出する導出円筒16と、回転操作に応じて導出円筒
16を降下させる操作ハンドル17と、導入口18と一
体化された把持ハンドル19とで構成されている。導入
口18にはゴム製の逆止弁18aが設けられ、また、導
出円筒16にもゴム製のボール体16aが設けられて、
流体の逆流を防止している。
The input / output unit 12 has a lead-out cylinder 16 for leading out the liquid from the pressure tank 1, an operation handle 17 for lowering the lead-out cylinder 16 according to a rotating operation, and a grip handle 19 integrated with an inlet 18. It consists of and. The inlet 18 is provided with a rubber check valve 18a, and the outlet cylinder 16 is also provided with a rubber ball body 16a.
Prevents backflow of fluid.

【0023】図3(a)の構成からなる圧力タンク1
は、使用時には、タンク本体11に入出力部12を装着
すると共に、導入口18と給気膜モジュール2の出口と
を適宜な連結ホースによって接続する。また、導出円筒
16と自吸式ポンプ3の吸入口とを適宜な連結ホースに
よって接続する。
A pressure tank 1 having the structure shown in FIG.
In use, the I / O unit 12 is mounted on the tank body 11 and the inlet 18 and the outlet of the air supply membrane module 2 are connected by an appropriate connecting hose during use. Further, the lead-out cylinder 16 and the suction port of the self-priming pump 3 are connected by an appropriate connecting hose.

【0024】しかる後、操作ハンドル17を回転させる
ことで導出円筒16を降下させる。すると、図3(b)
に示すように、導出円筒16の降下に応じて、先ず、内
筒本体10aが降下され、導出円筒16を更に降下させ
ると開閉バルブ14が降下されることになる。
After that, by rotating the operation handle 17, the lead-out cylinder 16 is lowered. Then, FIG. 3 (b)
As shown in (1), the inner cylinder body 10a is first lowered in response to the lowering of the lead-out cylinder 16, and when the lead-out cylinder 16 is further lowered, the opening / closing valve 14 is lowered.

【0025】この動作の結果、圧力タンク1の内筒本体
10aに導出円筒16の最下端が導入され、導出円筒1
6の最下端外周部に形成された隙間を通して、内筒本体
10aと導出円筒16とが連通する。また、内筒本体1
0aのシール部材SEがハウジング15のシール部材か
ら離脱して、導入口18と圧力タンク1の内部とが連通
する。
As a result of this operation, the lowermost end of the guiding cylinder 16 is introduced into the inner cylinder body 10a of the pressure tank 1, and the guiding cylinder 1
The inner cylinder body 10a and the lead-out cylinder 16 communicate with each other through a gap formed on the outermost portion of the lowermost end of 6. Also, the inner cylinder body 1
The seal member SE of 0a separates from the seal member of the housing 15, and the inlet 18 and the inside of the pressure tank 1 communicate with each other.

【0026】図3(b)の状態で自吸式ポンプ3を運転
すると、内筒本体10aと連通している導出円筒16を
通して、圧力タンク1の日本酒が出力されることにな
り、この日本酒は、自吸式ポンプ3によって給気膜モジ
ュール2に供給される。
When the self-priming pump 3 is operated in the state shown in FIG. 3 (b), the sake in the pressure tank 1 is output through the outlet cylinder 16 communicating with the inner cylinder body 10a. , Is supplied to the air supply membrane module 2 by the self-priming pump 3.

【0027】そして、給気膜モジュール2で処理された
後の出力処理液(炭酸冷酒)は、導入口18に供給さ
れ、上部ハウジング15の外周に形成された丸孔を通し
て、圧力タンク1に導入される(図3(b)参照)。な
お、給気膜モジュール2から導入された出力処理液は、
内筒本体10aの最下部から内筒本体10aの内側に導
入され(図2参照)、再度、導出円筒16→自吸式ポン
プ3→給気膜モジュール2の経路で流通して炭酸ガスの
注入処理が実行される。
Then, the output treatment liquid (carbonated cold liquor) after being treated by the air supply membrane module 2 is supplied to the inlet port 18 and introduced into the pressure tank 1 through the round hole formed on the outer periphery of the upper housing 15. (See FIG. 3B). The output treatment liquid introduced from the air supply membrane module 2 is
It is introduced from the lowermost part of the inner cylinder body 10a to the inside of the inner cylinder body 10a (see FIG. 2), and is again circulated in the route of the discharge cylinder 16 → the self-priming pump 3 → the air supply membrane module 2 to inject carbon dioxide The process is executed.

【0028】圧力タンク1に内蔵された日本酒は、この
ような循環動作を繰り返すことで限界レベルまでの炭酸
ガスの注入が可能となる。その後、所定レベルまで炭酸
ガスが注入されたら、圧力計6の検出値に基づいて自吸
式ポンプの運転が停止されるので、続いて、タンク本体
11から入出力部12を分離すれば良い。なお、入出力
部を分離するに当っては、操作ハンドル17を逆回転さ
せて導出円筒16を上昇させれば、開閉バルブ14や内
筒本体10aが限界位置まで上昇して、圧力タンク1が
密閉される(図3(a))。
The sake contained in the pressure tank 1 can be injected with carbon dioxide up to a limit level by repeating such a circulation operation. After that, when the carbon dioxide gas is injected to a predetermined level, the operation of the self-priming pump is stopped based on the detection value of the pressure gauge 6, so that the input / output unit 12 may be subsequently separated from the tank body 11. In separating the input / output unit, if the operation handle 17 is rotated in the reverse direction to raise the lead-out cylinder 16, the on-off valve 14 and the inner cylinder body 10a are raised to the limit position, and the pressure tank 1 is It is sealed (FIG. 3 (a)).

【0029】図5は、炭酸ガスの注入処理を完了した日
本酒について、それを顧客に提供する動作を概略的に図
示したものである。炭酸ガスの注入された日本酒は、圧
力タンク1にそのまま蓄えられるが、使用時には、タン
ク本体11に給気動作時に使用したものとは別の入出力
部12’を装着する。そして、導入口18と炭酸ガスタ
ンク40とを接続すると共に、導出円筒16と冷却機構
30とを接続する。
FIG. 5 is a schematic diagram showing the operation of providing sake to a customer who has completed the injection process of carbon dioxide gas. The sake into which carbon dioxide gas is injected is stored in the pressure tank 1 as it is, but at the time of use, the tank body 11 is equipped with an input / output unit 12 'different from that used at the time of the air supply operation. Then, the inlet 18 and the carbon dioxide gas tank 40 are connected, and the outlet cylinder 16 and the cooling mechanism 30 are connected.

【0030】この状態で流路を開放すると、圧力タンク
1に炭酸ガスが導入され、そのガス圧によって炭酸冷酒
が導出円筒16から押し出されて、冷却機構30で冷却
されつつ、顧客側に供給される。具体的には、適度に冷
やされた炭酸冷酒が、サーバの蛇口などから注ぎ出され
る。
When the flow path is opened in this state, carbon dioxide gas is introduced into the pressure tank 1, the carbonated cold liquor is pushed out from the discharge cylinder 16 by the gas pressure, and is cooled by the cooling mechanism 30 and supplied to the customer side. It Specifically, carbonated cold sake that has been appropriately cooled is poured out from a faucet of a server or the like.

【0031】以上、炭酸冷酒の製造方法及び提供方法に
ついて説明したが、同じ装置によってぶどう酒や焼酎や
ビールについても、所望の濃度の炭酸ガスを溶存させる
ことができる。なお、上記の実施例は居酒屋での製造を
例示したが、極めて小規模に地ビールを製造するような
場合や、炭酸水の自動販売機などでも有効に活用でき
る。また、炭酸ガスに限られるものではなく、酸素ガス
を所望の高濃度に溶存させることもできる。
Although the method for producing and providing cold carbonated liquor has been described above, the same device can dissolve carbon dioxide gas of a desired concentration in wine, shochu, and beer. In addition, although the above-mentioned embodiment illustrated the production in an izakaya, it can be effectively utilized in the case of manufacturing microbrewery on an extremely small scale, or in a vending machine for carbonated water. Further, it is not limited to carbon dioxide gas, and oxygen gas can be dissolved in a desired high concentration.

【0032】[0032]

【発明の効果】以上のように、本発明によれば、居酒屋
などにおいて必要量の炭酸を注入可能な炭酸飲料の製造
装置及びその方法を実現できる。
As described above, according to the present invention, it is possible to realize an apparatus and method for producing carbonated drinks in which a required amount of carbonic acid can be injected in a pub or the like.

【図面の簡単な説明】[Brief description of drawings]

【図1】実施例に係る炭酸飲料の製造装置の外観状態を
示す斜視図である。
FIG. 1 is a perspective view showing an appearance state of a carbonated beverage manufacturing apparatus according to an embodiment.

【図2】実施例に係る炭酸飲料の製造装置を示すブロッ
ク図である。
FIG. 2 is a block diagram showing a carbonated beverage manufacturing apparatus according to an embodiment.

【図3】給気モジュールの要部を示す概略図である。FIG. 3 is a schematic view showing a main part of an air supply module.

【図4】圧力タンクの要部を説明する概略断面図であ
る。
FIG. 4 is a schematic sectional view illustrating a main part of a pressure tank.

【図5】製造後の炭酸飲料の提供方法を説明する図面で
ある。
FIG. 5 is a diagram illustrating a method for providing a carbonated drink after production.

【符号の説明】[Explanation of symbols]

1 貯留タンク(圧力タンク) 2 給気膜モジュール 3 駆動部(自吸式ポンプ) 4 炭酸ガスタンク(炭酸ガスタンク) 11 タンク本体 12 入出力部 1 Storage tank (pressure tank) 2 Air supply membrane module 3 Drive unit (self-priming pump) 4 Carbon dioxide tank (carbon dioxide tank) 11 Tank body 12 Input / output section

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 被処理用の飲料を蓄える貯留タンクと、
前記貯留タンクの飲料を中空糸膜の内外一方側に受ける
給気膜モジュールと、前記中空糸膜の内外他方側に炭酸
ガス又は酸素ガスを供給するガスタンクと、前記貯留タ
ンクから出力され前記給気膜モジュールで処理された後
の飲料を、前記貯留タンクに循環的に供給する駆動部と
を備え、 前記貯留タンクは、移動可能であると共に、タンク本体
と入出力部とが着脱自在に構成されていることを特徴と
するガス溶存飲料の製造装置。
1. A storage tank for storing a beverage to be processed,
An air supply membrane module that receives the beverage in the storage tank on one side inside and outside the hollow fiber membrane, a gas tank that supplies carbon dioxide gas or oxygen gas to the other side inside and outside the hollow fiber membrane, and the air supply that is output from the storage tank. A drive unit that cyclically supplies the beverage after being processed by the membrane module to the storage tank, the storage tank is movable, and the tank body and the input / output unit are detachably configured. An apparatus for producing a gas-dissolved beverage, characterized in that
【請求項2】 前記加圧流路には圧力計が設けられ、こ
の圧力計の検出値に基づいて運転時間が管理されている
ことを特徴とする請求項1に記載の製造装置。
2. The manufacturing apparatus according to claim 1, wherein a pressure gauge is provided in the pressurizing flow passage, and the operating time is managed based on the detection value of the pressure gauge.
【請求項3】 タンク本体には、タンク本体の最上部か
ら最下部にほぼ至る内筒が設けられ、 前記内筒は、第1の付勢力によって上向きに付勢される
シール材によってタンク本体を封止すると共に、第2の
付勢力によって上向きに付勢されるバルブによって前記
内筒の出口を封止しており、 前記入出力部を装着する場合には、この装着に応じて、
前記シール材が降下して前記入出力部の導入口とタンク
本体とを連通させると共に、前記バルブが降下して前記
内筒の出口を開放するようになっていることを特徴とす
る請求項1又は2に記載の製造装置。
3. The tank main body is provided with an inner cylinder extending from the uppermost part to the lowermost part of the tank main body, and the inner cylinder forms the tank main body with a sealing material biased upward by a first biasing force. In addition to sealing, the outlet of the inner cylinder is sealed by a valve that is biased upward by a second biasing force, and when the input / output unit is mounted, according to this mounting,
2. The seal member descends to connect the inlet of the input / output unit with the tank body, and the valve descends to open the outlet of the inner cylinder. Or the manufacturing apparatus according to 2.
【請求項4】 前記飲料は、日本酒、ぶどう酒、ビー
ル、焼酎、又は水であることを特徴とする請求項1〜3
の何れかに記載の製造装置。
4. The beverage as claimed in claim 1, wherein the beverage is sake, wine, beer, shochu, or water.
The manufacturing apparatus according to any one of 1.
【請求項5】 被処理用の飲料を蓄える貯留タンクと、
前記貯留タンクの飲料を中空糸膜の内外一方側に受ける
給気膜モジュールと、前記中空糸膜の内外他方側に炭酸
ガス又は酸素ガスを供給するガスタンクとを備え、 タンク本体と入出力部とが着脱自在に構成された移動可
能な前記貯留タンクを用いて、前記貯留タンクと前記給
気膜モジュールの間で被処理液を循環させることで炭酸
ガス又は酸素ガスを注入するようにしたことを特徴とす
るガス溶存飲料の製造方法。
5. A storage tank for storing a beverage to be processed,
An air supply membrane module that receives the beverage in the storage tank on one side inside and outside the hollow fiber membrane, and a gas tank that supplies carbon dioxide gas or oxygen gas to the inside and outside the other side of the hollow fiber membrane are provided. Using the movable storage tank configured to be detachable, carbon dioxide gas or oxygen gas is injected by circulating the liquid to be treated between the storage tank and the gas supply membrane module. A method for producing a characteristic gas-dissolved beverage.
JP2002032473A 2002-02-08 2002-02-08 Apparatus and method for manufacturing gas dissolved beverage Pending JP2003231592A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002032473A JP2003231592A (en) 2002-02-08 2002-02-08 Apparatus and method for manufacturing gas dissolved beverage

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002032473A JP2003231592A (en) 2002-02-08 2002-02-08 Apparatus and method for manufacturing gas dissolved beverage

Publications (1)

Publication Number Publication Date
JP2003231592A true JP2003231592A (en) 2003-08-19

Family

ID=27775586

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002032473A Pending JP2003231592A (en) 2002-02-08 2002-02-08 Apparatus and method for manufacturing gas dissolved beverage

Country Status (1)

Country Link
JP (1) JP2003231592A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2014019454A (en) * 2012-07-13 2014-02-03 Suntory Holdings Ltd Beverage dispensing system
US8808775B2 (en) 2010-02-01 2014-08-19 Keurig Green Mountain, Inc. Method and apparatus for cartridge-based carbonation of beverages
US9327900B2 (en) 2014-09-09 2016-05-03 Keurig Green Mountain, Inc. Method and apparatus for cartridge-based carbonation of beverages
US9364018B1 (en) 2015-02-11 2016-06-14 Keurig Green Mountain, Inc. Adsorbent particle sizing for gas dissolution in beverages
US9867493B2 (en) 2010-02-01 2018-01-16 Bedford Systems Llc Method and apparatus for cartridge-based carbonation of beverages
US10201171B2 (en) 2014-10-20 2019-02-12 Bedford Systems Llc Flow circuit for carbonated beverage machine
CN116726742A (en) * 2023-08-09 2023-09-12 杭州千岛湖啤酒有限公司 Carbonated water preparation equipment for beer production

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US10842313B2 (en) 2010-02-01 2020-11-24 Bedford Systems Llc Method and apparatus for cartridge-based carbonation of beverages
US8808775B2 (en) 2010-02-01 2014-08-19 Keurig Green Mountain, Inc. Method and apparatus for cartridge-based carbonation of beverages
US9790076B2 (en) 2010-02-01 2017-10-17 Bedford Systems Llc Method and apparatus for cartridge-based carbonation of beverages
US9867493B2 (en) 2010-02-01 2018-01-16 Bedford Systems Llc Method and apparatus for cartridge-based carbonation of beverages
US9936834B2 (en) 2010-02-01 2018-04-10 Bedford Systems Llc Method and apparatus for cartridge-based carbonation of beverages
US10343885B2 (en) 2010-02-01 2019-07-09 Bedford Systems Llc Method and apparatus for cartridge-based carbonation of beverages
JP2014019454A (en) * 2012-07-13 2014-02-03 Suntory Holdings Ltd Beverage dispensing system
US9327900B2 (en) 2014-09-09 2016-05-03 Keurig Green Mountain, Inc. Method and apparatus for cartridge-based carbonation of beverages
US10843866B2 (en) 2014-09-09 2020-11-24 Bedford Systems Llc Method and apparatus for cartridge-based carbonation of beverages
US10201171B2 (en) 2014-10-20 2019-02-12 Bedford Systems Llc Flow circuit for carbonated beverage machine
US9364018B1 (en) 2015-02-11 2016-06-14 Keurig Green Mountain, Inc. Adsorbent particle sizing for gas dissolution in beverages
CN116726742A (en) * 2023-08-09 2023-09-12 杭州千岛湖啤酒有限公司 Carbonated water preparation equipment for beer production
CN116726742B (en) * 2023-08-09 2023-11-10 杭州千岛湖啤酒有限公司 Carbonated water preparation equipment for beer production

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