JPS6259966B2 - - Google Patents
Info
- Publication number
- JPS6259966B2 JPS6259966B2 JP58207399A JP20739983A JPS6259966B2 JP S6259966 B2 JPS6259966 B2 JP S6259966B2 JP 58207399 A JP58207399 A JP 58207399A JP 20739983 A JP20739983 A JP 20739983A JP S6259966 B2 JPS6259966 B2 JP S6259966B2
- Authority
- JP
- Japan
- Prior art keywords
- carbon dioxide
- dioxide gas
- tank
- supply pipe
- carbonated
- 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.)
- Expired
Links
Landscapes
- Non-Alcoholic Beverages (AREA)
Description
【発明の詳細な説明】
本発明は、水を含む混合液と炭酸ガスとを混合
すると共に冷却して炭酸飲料を製造する炭酸飲料
製造装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a carbonated beverage production apparatus that produces a carbonated beverage by mixing and cooling a liquid mixture containing water and carbon dioxide gas.
従来の炭酸飲料製造装置では、例えば特公昭53
−46909号公報に開示されているように、水、シ
ロツプ等の混合液に炭酸ガスを混合して炭酸飲料
とする混合タンクと、この炭酸飲料を冷却して製
品とする冷却タンクとを別々に設けて、炭酸飲料
製品を製造している。このような従来の装置で
は、混合タンクに供給される混合液の温度が変化
すれば、混合タンク内での混合液に対する炭酸ガ
スの溶解量が変わり、その結果、炭酸飲料中の炭
酸ガス含有量が変化する。しかも、混合液は一般
に低温ではないため、炭酸ガスの圧力を高く設定
しておかなければ、十分な炭酸ガス含有量を有す
る炭酸飲料を冷却タンクに供給できず、そのた
め、冷却タンクから注出される炭酸飲料製品中の
炭酸ガス含有量も低く、舌触りのよい好適な製品
を供給することはできなかつた。また、炭酸ガス
の圧力を高く設定し過ぎてしまうと、冷却タンク
に設けられた注出コツクを開いて炭酸飲料を注出
する際に、炭酸ガス自体が注出コツクから非常な
勢いで噴出してしまうという、炭酸ガス含有量低
下よりも更に好ましくない問題が生じるので、炭
酸ガス含有量の低下を容認せざるを得なかつた。 In conventional carbonated beverage manufacturing equipment, for example,
As disclosed in Publication No. 46909, a mixing tank that mixes carbon dioxide gas with a liquid mixture of water, syrup, etc. to make a carbonated drink, and a cooling tank that cools this carbonated drink to make a product are separated. established to manufacture carbonated beverage products. In such conventional devices, if the temperature of the liquid mixture supplied to the mixing tank changes, the amount of carbon dioxide gas dissolved in the liquid mixture in the mixing tank changes, and as a result, the carbon dioxide content in the carbonated beverage changes. changes. Moreover, since the mixed liquid is generally not at a low temperature, unless the carbon dioxide gas pressure is set high, a carbonated beverage with sufficient carbon dioxide content cannot be supplied to the cooling tank, and as a result, it is poured out from the cooling tank. The carbon dioxide content of the carbonated beverage product is also low, making it impossible to provide a suitable product with good texture. In addition, if the pressure of carbon dioxide gas is set too high, when the spout provided in the cooling tank is opened to pour out the carbonated beverage, the carbon dioxide itself will gush out from the spout with great force. Since this problem, which is even more undesirable than a decrease in the carbon dioxide content, occurs, the decrease in the carbon dioxide content has had to be accepted.
従つて、本発明は、炭酸ガスの圧力を低い値に
設定しても該炭酸ガスを混合液に十分に吸収させ
て溶解できる、炭酸ガス含有量の安定した小型で
軽量の炭酸飲料製造装置を提供することを目的と
するものである。 Therefore, the present invention provides a compact and lightweight carbonated beverage production device with stable carbon dioxide content, which can sufficiently absorb and dissolve carbon dioxide gas into a liquid mixture even if the pressure of carbon dioxide gas is set to a low value. The purpose is to provide
この目的から、本発明による炭酸飲料製造装置
は、冷却装置に接続され、炭酸ガスボンベからの
炭酸ガスと、原液タンクからの原液及び弱炭酸水
貯蔵タンクからの弱炭酸水の混合液とを受け入れ
て炭酸飲料を製造する、前記弱炭酸水貯蔵タンク
の容積と比較して相対的に大きな容積を有する製
造タンクを備え、該製造タンクには、前記炭酸ガ
スボンベに一端で接続され前記炭酸ガスを供給す
る供給管の他端と、前記原液タンク及び前記弱炭
酸水貯蔵タンクに一端で接続され前記混合液を供
給する供給管の他端とが別々に接続され、前記弱
炭酸水貯蔵タンクには前記炭酸ガスの供給管から
分岐した加圧管が接続されていることを特徴とす
るものである。 For this purpose, the carbonated beverage manufacturing device according to the invention is connected to a cooling device and receives carbon dioxide gas from a carbon dioxide gas cylinder, and a mixture of concentrate from a concentrate tank and weakly carbonated water from a weakly carbonated water storage tank. A production tank for producing a carbonated beverage and having a relatively large volume compared to the volume of the weakly carbonated water storage tank, the production tank being connected at one end to the carbon dioxide gas cylinder and supplied with the carbon dioxide gas. The other end of the supply pipe and the other end of a supply pipe that is connected at one end to the raw solution tank and the weakly carbonated water storage tank and supplies the mixed liquid are separately connected, and the weakly carbonated water storage tank is connected to the other end of the supply pipe that supplies the mixed liquid. It is characterized in that a pressurizing pipe branched from the gas supply pipe is connected.
本発明による炭酸飲料製造装置は上述のような
特徴を有するため、冷却装置を有する製造タンク
に供給された混合液の温度は、該冷却装置の運転
に伴つて低下する。一般に、炭酸ガスの溶解量
は、炭酸ガスの圧力と、溶媒、即ち混合液の温度
とに依存しており、特に温度が低下するほど溶解
量は多くなるので、製造タンク内の炭酸飲料中の
炭酸ガス量は炭酸ガス圧力を下げても従来と比較
して多くすることができる。しかも、本発明では
弱炭酸水貯蔵タンクで炭酸ガスの一次混合が行な
われ、製造タンクで炭酸ガスの二次混合が行なわ
れるため、結果として製品における炭酸ガス含有
量が安定する。従つて、本発明によつて上述の目
的が好適に達成されることが分かる。 Since the carbonated beverage production apparatus according to the present invention has the above-mentioned characteristics, the temperature of the liquid mixture supplied to the production tank equipped with a cooling device decreases as the cooling device operates. Generally, the amount of dissolved carbon dioxide gas depends on the pressure of carbon dioxide gas and the temperature of the solvent, that is, the mixed liquid.In particular, the lower the temperature, the greater the amount of dissolved carbon dioxide gas, so the amount of dissolved carbon dioxide gas in the carbonated beverage in the production tank is Even if the carbon dioxide pressure is lowered, the amount of carbon dioxide can be increased compared to the conventional method. Moreover, in the present invention, primary mixing of carbon dioxide gas is performed in the weakly carbonated water storage tank, and secondary mixing of carbon dioxide gas is performed in the production tank, so that the carbon dioxide content in the product is stabilized as a result. Therefore, it can be seen that the above objects are suitably achieved by the present invention.
次に、本発明による炭酸飲料製造装置の好適な
実施例について添付図面を参照しながら詳細に説
明する。 Next, a preferred embodiment of the carbonated beverage manufacturing apparatus according to the present invention will be described in detail with reference to the accompanying drawings.
炭酸ガスボンベ1は、炭酸ガス供給管2から分
岐した加圧管6を介して、弱炭酸水を貯蔵する貯
蔵タンク8に連通すると共に、管7′を介して、
原液を貯留する原液タンク7に連通し、該炭酸ガ
スボンベ1からの炭酸ガスの圧力によりこれ等の
タンク7,8内の原液及び弱炭酸水を加圧して、
後述する製造タンク18に供給するようになつて
いる。また、炭酸ガスボンベ1は炭酸ガス供給管
2を介して製造タンク18に連通しており、後述
するような方法で炭酸飲料を製造する該製造タン
ク18内を加圧している。炭酸ガス供給管2に
は、減圧弁3、製造タンク18からの炭酸飲料の
逆流を防ぐ逆止弁4、及びガス抜き用三方弁5等
が設けられている。減圧弁3は、製造タンク18
に送られる炭酸ガスの圧力を定めると共に、製造
タンク18内の炭酸飲料中の炭酸ガス含有量を定
める。 The carbon dioxide gas cylinder 1 is connected to a storage tank 8 for storing weakly carbonated water via a pressurizing pipe 6 branched from a carbon dioxide gas supply pipe 2, and via a pipe 7'.
It communicates with the stock solution tank 7 that stores the stock solution, and pressurizes the stock solution and weakly carbonated water in these tanks 7 and 8 by the pressure of carbon dioxide gas from the carbon dioxide gas cylinder 1.
It is designed to be supplied to a production tank 18 which will be described later. Further, the carbon dioxide gas cylinder 1 communicates with a production tank 18 via a carbon dioxide gas supply pipe 2, and pressurizes the inside of the production tank 18 in which carbonated beverages are produced by a method that will be described later. The carbon dioxide gas supply pipe 2 is provided with a pressure reducing valve 3, a check valve 4 that prevents backflow of carbonated beverage from the production tank 18, a three-way gas venting valve 5, and the like. The pressure reducing valve 3 is connected to the production tank 18
In addition to determining the pressure of the carbon dioxide gas sent to the production tank 18, the carbon dioxide content in the carbonated beverage in the production tank 18 is determined.
一方、炭酸ガスにより加圧された貯蔵タンク8
内の弱炭酸水と原液タンク7内の原液とは、それ
ぞれ、供給管16及び15に設けられた流量調整
器11及び9により流量を調整された後、逆止弁
12及び10を介して混合器20に送られ、該混
合器20で所定の割合に混合され混合液となる。
この混合液は供給管17を介して製造タンク18
に送られる。供給管17には、製造タンク18へ
の混合液の供給量を定めるための電磁弁13が設
けられている。 On the other hand, storage tank 8 pressurized with carbon dioxide gas
The weakly carbonated water in the tank and the stock solution in the stock solution tank 7 are mixed through check valves 12 and 10 after the flow rate is adjusted by flow regulators 11 and 9 provided in supply pipes 16 and 15, respectively. The mixture is sent to a vessel 20, where it is mixed at a predetermined ratio to form a mixed liquid.
This mixed liquid is passed through the supply pipe 17 to the manufacturing tank 18.
sent to. The supply pipe 17 is provided with a solenoid valve 13 for determining the amount of mixed liquid supplied to the production tank 18 .
製造タンク18には、図示しない周知の冷却装
置及び攪拌装置が設けられており、混合液を製造
タンク18に供給し、炭酸ガス供給管2を通る炭
酸ガスの圧力を減圧弁3により所定値に定めた状
態において、前記冷却装置及び攪拌装置を運転す
ると、製造タンク18内の混合液及び炭酸ガスは
炭酸飲料となる。ここで、一般に溶媒に吸収され
て溶解される炭酸ガスの量は、該溶媒にかかる炭
酸ガスの圧力値と溶媒温度とによつて定まり、特
に溶媒温度に対する依存性が高い。即ち、製造タ
ンク18内の混合液の温度が低下すると、該混合
液に炭酸ガスが溶解され易くなる。従つて、製造
タンク18内の混合液が前記冷却装置により冷却
され始めると同時に、炭酸ガスが混合液に吸収さ
れ易くなり、そのため製造タンク18内の炭酸ガ
スの圧力が前記所定値から低下し、ある程度まで
低下した状態では、炭酸ガスは混合液内で飽和し
ている。この状態において製造タンク18に供給
される炭酸ガスの圧力が所定値に維持される。更
に冷却運転を続けると、製造タンク18内の混合
液が凍結し始めるが、炭酸ガスを液化させるほど
低温にはならないので凍結する混合液から炭酸ガ
スが放出され、該製造タンク18内の炭酸ガス圧
力が次第に上昇し、これにより製造タンク18へ
の炭酸ガスの供給を逆止弁4の作用により停止す
る。 The production tank 18 is equipped with a well-known cooling device and agitation device (not shown), and supplies the mixed liquid to the production tank 18 and reduces the pressure of the carbon dioxide gas passing through the carbon dioxide gas supply pipe 2 to a predetermined value using the pressure reducing valve 3. When the cooling device and stirring device are operated in the predetermined conditions, the mixed liquid and carbon dioxide gas in the production tank 18 become a carbonated beverage. Here, the amount of carbon dioxide gas absorbed and dissolved in a solvent is generally determined by the pressure value of carbon dioxide gas applied to the solvent and the solvent temperature, and is particularly highly dependent on the solvent temperature. That is, when the temperature of the liquid mixture in the production tank 18 decreases, carbon dioxide gas becomes easier to dissolve in the liquid mixture. Therefore, at the same time that the mixed liquid in the production tank 18 begins to be cooled by the cooling device, carbon dioxide gas becomes easily absorbed into the mixed liquid, and therefore the pressure of the carbon dioxide gas in the production tank 18 decreases from the predetermined value. When the carbon dioxide gas has decreased to a certain level, the mixed liquid is saturated with carbon dioxide gas. In this state, the pressure of carbon dioxide gas supplied to the production tank 18 is maintained at a predetermined value. As the cooling operation continues, the mixed liquid in the manufacturing tank 18 begins to freeze, but the temperature does not reach a low enough temperature to liquefy carbon dioxide, so carbon dioxide is released from the frozen mixed liquid, and the carbon dioxide in the manufacturing tank 18 is The pressure gradually increases, and the supply of carbon dioxide gas to the production tank 18 is thereby stopped by the action of the check valve 4.
炭酸ガスを含んだ混合液である製造タンク18
内の炭酸飲料は、製造タンク18に設けられた注
出コツク19の操作により該注出コツク19を介
して注出することができる。炭酸飲料を注出する
際の製造タンク18内のガス圧は最初の所定の炭
酸ガス圧より高く、炭酸飲料を注出するにつれて
低下する。そして製造タンク18内のガス圧が最
初の所定圧力より下がつた時に減圧弁3を介して
該製造タンク18に炭酸ガスが再び供給される。 Production tank 18 which is a mixed liquid containing carbon dioxide gas
The carbonated beverage inside can be poured out through the pouring pot 19 by operating the pouring pot 19 provided in the production tank 18. The gas pressure in the production tank 18 when dispensing the carbonated beverage is higher than the initial predetermined carbon dioxide gas pressure, and decreases as the carbonated beverage is dispensed. Then, when the gas pressure in the production tank 18 drops below the initial predetermined pressure, carbon dioxide gas is again supplied to the production tank 18 via the pressure reducing valve 3.
以上のように、本発明の炭酸飲料製造装置によ
れば、冷却装置に接続された炭酸飲料製造タンク
に、弱炭酸水貯蔵タンク及び原液タンクに連通し
た混合液の供給管と炭酸ガスボンベに連通した炭
酸ガスの供給管とを別々に接続したので、予め炭
酸ガスの一次混合が行なわれた混合液を冷却し、
この冷却された混合液に炭酸ガスを溶解させるこ
とになり、製造タンクに供給される炭酸ガスの圧
力を従来より低い値に設定しても、より多くの炭
酸ガスを溶解できるだけでなく、
また、本発明の好適な実施例においては、製造
タンクへの炭酸ガスの供給管に減圧弁が設けられ
ているので、製造タンクに供給される炭酸ガスの
圧力を変更して、炭酸飲料中の炭酸ガス含有量を
容易に変更することができると共に、製造タンク
からの炭酸飲料の注出速度を調節することもでき
る。 As described above, according to the carbonated beverage production apparatus of the present invention, the carbonated beverage production tank connected to the cooling device is connected to the mixed liquid supply pipe that communicates with the weakly carbonated water storage tank and the stock solution tank, and the carbon dioxide gas cylinder. Since the carbon dioxide gas supply pipe is connected separately, the mixed liquid that has been primarily mixed with carbon dioxide gas can be cooled.
Carbon dioxide gas is dissolved in this cooled mixed liquid, and even if the pressure of carbon dioxide gas supplied to the production tank is set to a lower value than before, not only can more carbon dioxide gas be dissolved, but also In a preferred embodiment of the present invention, a pressure reducing valve is provided in the carbon dioxide gas supply pipe to the production tank, so that the pressure of the carbon dioxide gas supplied to the production tank can be changed to reduce the carbon dioxide gas in the carbonated beverage. The content can be easily changed, and the speed at which the carbonated beverage is dispensed from the production tank can also be adjusted.
図は、本発明による炭酸飲料製造装置の好適な
実施例を示す系統図である。
1……炭酸ガスボンベ、2……炭酸ガスの供給
管、3……減圧弁、6……加圧管、7……原液タ
ンク、8……弱炭酸水貯蔵タンク、17……混合
液の供給管、18……製造タンク。
The figure is a system diagram showing a preferred embodiment of the carbonated beverage manufacturing apparatus according to the present invention. 1... Carbon dioxide cylinder, 2... Carbon dioxide gas supply pipe, 3... Pressure reducing valve, 6... Pressurizing pipe, 7... Stock solution tank, 8... Weakly carbonated water storage tank, 17... Mixed liquid supply pipe , 18... Production tank.
Claims (1)
炭酸ガスと、原液タンクからの原液及び弱炭酸水
貯蔵タンクからの弱炭酸水の混合液とを受け入れ
て炭酸飲料を製造する、前記弱炭酸水貯蔵タンク
の容積と比較して相対的に大きな容積を有する製
造タンクを備え、該製造タンクには、前記炭酸ガ
スボンベに一端で接続され前記炭酸ガスを供給す
る供給管の他端と、前記原液タンク及び前記弱炭
酸水貯蔵タンクに一端で接続され前記混合液を供
給する供給管の他端とが別々に接続され、前記弱
炭酸水貯蔵タンクには前記炭酸ガスの供給管から
分岐した加圧管が接続されていることを特徴とす
る炭酸飲料製造装置。1. The weakly carbonated water storage tank that is connected to a cooling device and receives carbon dioxide gas from a carbon dioxide gas cylinder, a mixed solution of stock solution from a stock solution tank, and weakly carbonated water from a weakly carbonated water storage tank to produce a carbonated drink. The production tank includes a supply pipe connected at one end to the carbon dioxide gas cylinder and supplying the carbon dioxide gas, the other end of the supply pipe connected to the carbon dioxide gas cylinder at one end, and the raw solution tank and the carbon dioxide gas cylinder. One end of the supply pipe is connected to a weak carbonated water storage tank and the other end of the supply pipe for supplying the mixed liquid is connected separately, and a pressurizing pipe branched from the carbon dioxide gas supply pipe is connected to the weak carbonated water storage tank. A carbonated beverage manufacturing device characterized by:
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58207399A JPS6099331A (en) | 1983-11-07 | 1983-11-07 | Apparatus for producing carbonated beverage |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP58207399A JPS6099331A (en) | 1983-11-07 | 1983-11-07 | Apparatus for producing carbonated beverage |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6099331A JPS6099331A (en) | 1985-06-03 |
| JPS6259966B2 true JPS6259966B2 (en) | 1987-12-14 |
Family
ID=16539096
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP58207399A Granted JPS6099331A (en) | 1983-11-07 | 1983-11-07 | Apparatus for producing carbonated beverage |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6099331A (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH025261U (en) * | 1988-06-23 | 1990-01-12 | ||
| JPH07500946A (en) * | 1992-06-06 | 1995-01-26 | フォスロー シュヴァーベ ゲゼルシャフト ミット ベシュレンクテル ハフツング | electrical connection terminal device |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2012187516A (en) * | 2011-03-10 | 2012-10-04 | Shinno Epack:Kk | Apparatus for producing soda water and beauty utensil using apparatus for producing the soda water |
-
1983
- 1983-11-07 JP JP58207399A patent/JPS6099331A/en active Granted
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPH025261U (en) * | 1988-06-23 | 1990-01-12 | ||
| JPH07500946A (en) * | 1992-06-06 | 1995-01-26 | フォスロー シュヴァーベ ゲゼルシャフト ミット ベシュレンクテル ハフツング | electrical connection terminal device |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6099331A (en) | 1985-06-03 |
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