JPH0753700Y2 - Carbonated beverage preparation equipment - Google Patents
Carbonated beverage preparation equipmentInfo
- Publication number
- JPH0753700Y2 JPH0753700Y2 JP981590U JP981590U JPH0753700Y2 JP H0753700 Y2 JPH0753700 Y2 JP H0753700Y2 JP 981590 U JP981590 U JP 981590U JP 981590 U JP981590 U JP 981590U JP H0753700 Y2 JPH0753700 Y2 JP H0753700Y2
- Authority
- JP
- Japan
- Prior art keywords
- cooler
- mixing device
- treated water
- switching valve
- way switching
- 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 - Lifetime
Links
Description
【考案の詳細な説明】 （産業上の利用分野） 本考案は炭酸飲料の壜詰め又は缶詰に適用される炭酸飲
料混合装置に関する。DETAILED DESCRIPTION OF THE INVENTION (Industrial field of application) The present invention relates to a carbonated beverage mixing apparatus applied to bottled or canned carbonated beverages.
（従来の技術） 第２図は従来の炭酸飲料調合装置の一例を示すものであ
り処理水の脱気、脱気された処理水とシロツプの連続一
定比率混合、混合された製品液の冷却、及び冷却された
製品液のカーボネーション（炭酸ガス吸着）の機能を有
する。(Prior Art) FIG. 2 shows an example of a conventional carbonated beverage blending apparatus, which degasses the treated water, continuously mixes the degassed treated water and syrup at a constant ratio, and cools the mixed product liquid. And has a function of carbonation (adsorption of carbon dioxide gas) of the cooled product liquid.
（１）は脱気タンクで通常は図示しない手段で供給され
た処理水を脱気するために真空ポンプ（２）に依り高い
真空度に保持されている。（３）は脱気された処理水を
次工程へ送るための水ポンプであり、（４）は脱気され
た処理水と図示しない手段で供給されたシロツプとを連
続的に一定比率に混合する混合装置である。（５）は一
定比率に混合された混合液を次工程へ送液するミツクス
ポンプであり（６）は混合液を図示しない手段で供給さ
れた冷水又はブラインで冷却する冷却器である。又
（７）はカーボネータで冷却された混合液に所定の炭酸
ガスを吸収させるためのものである。(1) is a deaeration tank, which is normally maintained at a high degree of vacuum by a vacuum pump (2) for deaeration of the treated water supplied by means not shown. (3) is a water pump for sending the degassed treated water to the next step, and (4) continuously mixes the degassed treated water with the syrup supplied by means not shown in a constant ratio. It is a mixing device. (5) is a mix pump for sending the mixed liquid mixed in a constant ratio to the next step, and (6) is a cooler for cooling the mixed liquid with cold water or brine supplied by means not shown. Further, (7) is for absorbing a predetermined carbon dioxide gas in the mixed liquid cooled by the carbonator.
次に作用を説明する。Next, the operation will be described.
炭酸飲料調合装置に送られてきた処理水は脱気タンク
（１）に入り、ここで処理水中の空気が除去され、水ポ
ンプ（３）に依り混合装置（４）へ送られる。更に混合
装置（４）にシロツプと連続的に一定比率に混合され、
ミツクスポンプ（５）に依り冷却器（６）に送液され
る。この製品液は冷却器（６）で所定の温度に冷却さ
れ、カーボネータ（７）に送られる。そしてこのカーボ
ネータ（７）で所定の炭酸ガスを吸収し、壜詰機又は缶
詰機へ送液される。The treated water sent to the carbonated beverage preparation device enters the deaeration tank (1), where the air in the treated water is removed, and is sent to the mixing device (4) by the water pump (3). Furthermore, the mixing device (4) is continuously mixed with the syrup at a constant ratio,
Liquid is sent to the cooler (6) by the mix pump (5). The product liquid is cooled to a predetermined temperature by the cooler (6) and sent to the carbonator (7). Then, this carbon dioxide (7) absorbs a predetermined carbon dioxide gas, and the solution is sent to a bottle-filling machine or a canning machine.
（考案が解決しようとする課題） 従来の炭酸飲料調合装置は次の様な欠点を有している。
即ち、粗大パルプを含んだ製品を製造する場合冷却器
（６）で粗大パルプが詰まり、運転不能となったり、洗
浄時に完全に除去出来ないことがあるため、他の種類の
製品を運転するときに混入したり菌の発生の原因となっ
たりする。(Problems to be Solved by the Invention) The conventional carbonated beverage compounding device has the following drawbacks.
That is, when a product containing coarse pulp is produced, the cooler (6) may become clogged with coarse pulp and may not be able to operate, or may not be completely removed during washing. It may be mixed in with or cause the generation of bacteria.
本考案はかゝる欠点に対処するため開発されたものであ
って粗大パルプを含んだ製品を製造する場合の冷却器で
の詰まりを防止することを目的とする。The present invention was developed to address such shortcomings and aims to prevent clogging in a cooler when producing a product containing coarse pulp.
（課題を解決するための手段） 上記の目的を達成するための本考案の構成を実施例に対
応する第１図を用いて説明すると本考案は脱気した処理
水をシロツプと連続一定比率に混合する混合装置（４）
と、該混合装置（４）により混合された混合液を冷却す
る冷却器（６）と、該冷却器（６）により冷却された混
合液に所定の炭酸ガスを吸収させるカーボネータ（７）
とを有する炭酸飲料調合装置において、前記脱気した処
理水を、前記混合装置（４）と前記冷却器（６）とに切
換え送液する第１三方切換弁（８）と前記混合装置
（４）からの混合液を、前記冷却器（６）と前記カーボ
ネータ（７）とに切換え送液する第２三方切換弁（９）
と、前記冷却器（６）からの冷却された処理水又は混合
液を前記混合装置（４）と前記カーボネータ（７）とに
切換え送液する第３三方切換弁（10）とを具えたことを
特徴とする。(Means for Solving the Problems) The structure of the present invention for achieving the above object will be described with reference to FIG. 1 corresponding to an embodiment. The present invention shows that degassed treated water is continuously and continuously mixed with a syrup at a constant ratio. Mixing device for mixing (4)
A cooler (6) for cooling the mixed liquid mixed by the mixing device (4); and a carbonator (7) for absorbing a predetermined carbon dioxide gas in the mixed liquid cooled by the cooler (6).
In a carbonated beverage preparation device having: a first three-way switching valve (8) for switching and sending the degassed treated water to the mixing device (4) and the cooler (6); and the mixing device (4). Second) three-way switching valve (9) for switching and sending the mixed liquid from (1) to the cooler (6) and the carbonator (7).
And a third three-way switching valve (10) for switching and sending the cooled treated water or mixed liquid from the cooler (6) to the mixing device (4) and the carbonator (7). Is characterized by.
（作用） そして本考案は上記の手段により脱気した処理水を混合
装置から冷却器を介してカーボネータへ送液する第１通
路と脱気した処理水を冷却器から混合装置を介してカー
ボネータへ送液する第２通路とが形成され、かくて第２
通路によれば、冷却器での冷却は処理水とシロツプとの
混合液ではなく処理水のみとなるため冷却器でのつまり
はなくなる。(Operation) And, the present invention provides a first passage through which the treated water degassed by the above means is sent from the mixing device to the carbonator through the cooler and the degassed treated water is sent from the cooler to the carbonator through the mixing device. A second passage for liquid delivery is formed, and thus a second passage is formed.
According to the passage, the cooling in the cooler is not the mixed liquid of the treated water and the syrup but only the treated water, so that the clogging in the cooler is eliminated.
（実施例） 以下第１図に基づいて本考案の一実施例を示すと（１）
は脱気タンク、（２）は真空ポンプ、（３）は水ポン
プ、（４）は混合装置、（５）はミツクスポンプ、
（６）は冷却器、（７）はカーボネータを示し、これら
の接続路には脱気した処理水を混合装置（４）と冷却器
（６）とに切換え送液する自動の第１三方切換（８）と
混合装置（４）からの混合液を冷却器（６）とカーボネ
ータ（７）とに切換え送液する自動の第２三方切換弁
（９）と冷却器（６）から冷却された処理水又は混合液
を混合装置（４）とカーボネータ（７）とに切換え送液
する自動の第３三方切換弁（10）とを具えている。(Embodiment) An embodiment of the present invention will be described below with reference to FIG. 1 (1)
Is a degassing tank, (2) is a vacuum pump, (3) is a water pump, (4) is a mixing device, (5) is a mix pump,
(6) indicates a cooler, (7) indicates a carbonator, and the automatic first three-way switching for transferring the degassed treated water to the mixing device (4) and the cooler (6) in these connection paths. It was cooled from the cooler (6) and the automatic second three-way switching valve (9) that switches the liquid mixture from (8) and the mixing device (4) to the cooler (6) and the carbonator (7). It is provided with an automatic third three-way switching valve (10) for switching and sending the treated water or the mixed liquid to the mixing device (4) and the carbonator (7).
かくて粗大パルプを含まない炭酸飲料の製造の場合は第
１図（ａ）のフロー図示すように脱気タンク（１）にて
脱気された処理水は水ポンプ（３）に依り第１三方切換
弁（８）に送られ、この第１三方切換弁（８）は本運転
の場合は混合装置（４）へ流れるように切換えられてい
るので脱気処理水は混合装置（４）へ送られ、混合装置
（４）でシロツプと一定比率に混合された製品液はミツ
クスポンプ（５）に依り自動の第２三方切換弁（９）に
送られる。この自動第２三方切換弁（９）は本運転の場
合は冷却器（６）側へ切換えられいるので製品液は冷却
器（６）へ送られ、ここで冷却され、更に自動の第３三
方切換弁（10）を通ってカーボネータ（７）へ送られて
この第１通路によりカーボネーシヨンされ、図示しない
壜詰機又は缶詰機へ送られる。Thus, in the case of the production of carbonated beverages that do not contain coarse pulp, the treated water deaerated in the deaeration tank (1) is first processed by the water pump (3) as shown in the flow chart of FIG. 1 (a). The first three-way switching valve (8) is sent to the three-way switching valve (8), and in this operation, since the first three-way switching valve (8) is switched so as to flow to the mixing device (4), the degassed treated water flows to the mixing device (4). The product liquid sent and mixed with the syrup at a constant ratio by the mixing device (4) is sent to the automatic second three-way switching valve (9) by the mix pump (5). In this operation, the automatic second three-way switching valve (9) is switched to the cooler (6) side, so that the product liquid is sent to the cooler (6), where it is cooled, and further the automatic third three-way valve is used. It is sent to the carbonator (7) through the switching valve (10), carbonized by this first passage, and sent to a bottle or canning machine (not shown).
次に粗大パルプを含む炭酸飲料の製造の場合は第１図
（ｂ）のフロー図に示すように脱気（１）にて脱気され
た処理水は水ポンプ（３）に依り自動の第１三方切換弁
（８）に送られ、この自動の第１三方切換弁（８）は本
運転の場合は冷却器（６）へ流れるよう切換えられてい
るので、脱気処理水はシロツプと混合する前に冷却器
（６）へ送られ、冷却される。そして自動第３三方切換
弁（10）を経由して混合装置（４）へ送られここでシロ
ツプと一定比率に混合される。この処理水とシロツプの
混合液はミツクスポンプ（５）に依り自動第２三方切換
弁（９）へ送られ更にカーボネータ（７）へ送られてこ
の第２通路によりカーボネーシヨンされ、図示しない壜
詰機又は缶詰機へ送られる。Next, in the case of producing carbonated beverages containing coarse pulp, the treated water degassed by degassing (1) is automatically processed by the water pump (3) as shown in the flow chart of FIG. 1 (b). 1) Three-way switching valve (8), and this automatic first three-way switching valve (8) is switched to flow to the cooler (6) in this operation, so the degassed water is mixed with syrup. It is sent to the cooler (6) and cooled before being processed. Then, it is sent to the mixing device (4) via the automatic third three-way switching valve (10) and mixed there with the syrup at a constant ratio. The mixed liquid of the treated water and the syrup is sent to the automatic second three-way switching valve (9) by the mix pump (5) and further to the carbonator (7) to be carbonized by the second passage, and a bottle filling machine (not shown). Or sent to a canning machine.
（考案の効果） このように本考案によるときは脱気した処理水を混合装
置と冷却器とに切換え送液する第１三方切換弁と混合装
置からの混合液を冷却器とカーボネータに切換え送液す
る第２三方切換弁と、冷却器からの冷却された処理水又
は混合液を混合装置とカーボネータとに切換え送液する
第３三方切換弁を設けたものであるからこれら第１乃至
第３の三方切換弁の切換えによって脱気した処理水を混
合装置から冷却器を介してカーボネータへ送液する第１
通路と脱気した処理水を冷却器から混合装置を介してカ
ーボネータへ送液する第２通路とが形成され、かくて粗
大パルプを含んだ製品を製造する場合でも第２通路を使
用することにより冷却器の詰りを防止することができ特
殊な冷却器を必要としないため、コストダウンとなると
共に省スペースとなる効果を有する。(Effects of the Invention) As described above, according to the present invention, the degassed treated water is switched between the mixing device and the cooler and the liquid is sent from the first three-way switching valve and the mixing device to the cooler and the carbonator. Since the second three-way switching valve for liquid and the third three-way switching valve for switching and sending the cooled treated water or the mixed liquid from the cooler to the mixing device and the carbonator are provided, these first to third First, the treated water deaerated by switching the three-way switching valve is sent from the mixing device to the carbonator through the cooler.
A passage and a second passage for sending the deaerated treated water from the cooler to the carbonator through the mixing device are formed, and thus the second passage is used even when producing a product containing coarse pulp. Since the clogging of the cooler can be prevented and no special cooler is required, the cost can be reduced and the space can be saved.
第１図は本考案の一実施例を示す系統図でａは第１フロ
ー図、ｂは第２フロー図、第２図は従来例を示す系統図
である。 （４）…混合装置、（６）…冷却器 （７）…カーボネータ、（８）…第１三方切換弁 （９）…第２三方切換弁、（10）…第３三方切換弁FIG. 1 is a system diagram showing an embodiment of the present invention. A is a first flow diagram, b is a second flow diagram, and FIG. 2 is a system diagram showing a conventional example. (4) ... Mixing device, (6) ... Cooler (7) ... Carbonator, (8) ... First three-way switching valve (9) ... Second three-way switching valve, (10) ... Third three-way switching valve
Claims (1)
に混合する混合装置と、該混合装置により混合された混
合液を冷却する冷却器と、該冷却器により冷却された混
合液に所定の炭酸ガスを吸収させるカーボネータとを有
する炭酸飲料調合装置において、前記脱気した処理水
を、前記混合装置と前記冷却器とに切換え送液する第１
三方切換弁と前記混合装置からの混合液を、前記冷却器
と前記カーボネータとに切換え送液する第２三方切換弁
と、前記冷却器からの冷却された処理水又は混合液を前
記混合装置と前記カーボネータとに切換え送液する第３
三方切換弁とを具えたことを特徴とする炭酸飲料調合装
置。1. A mixing device for continuously mixing deaerated treated water with a syrup at a constant ratio, a cooler for cooling the mixed liquid mixed by the mixing device, and a predetermined amount for the mixed liquid cooled by the cooler. A carbonated beverage blending apparatus having a carbon dioxide absorbing carbon dioxide gas, and a method for sending the degassed treated water by switching to the mixing apparatus and the cooler.
A second three-way switching valve for switching and sending the mixed liquid from the three-way switching valve and the mixing device to the cooler and the carbonator, and the cooled treated water or mixed liquid from the cooling device to the mixing device. The third for switching to the carbonator and sending liquid
A carbonated drink blending device comprising a three-way switching valve.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP981590U JPH0753700Y2 (en) | 1990-02-05 | 1990-02-05 | Carbonated beverage preparation equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP981590U JPH0753700Y2 (en) | 1990-02-05 | 1990-02-05 | Carbonated beverage preparation equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH03102233U JPH03102233U (en) | 1991-10-24 |
| JPH0753700Y2 true JPH0753700Y2 (en) | 1995-12-13 |
Family
ID=31513404
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP981590U Expired - Lifetime JPH0753700Y2 (en) | 1990-02-05 | 1990-02-05 | Carbonated beverage preparation equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0753700Y2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6236698B2 (en) * | 2014-05-29 | 2017-11-29 | 三菱重工機械システム株式会社 | Liquid processing equipment |
-
1990
- 1990-02-05 JP JP981590U patent/JPH0753700Y2/en not_active Expired - Lifetime
Also Published As
| Publication number | Publication date |
|---|---|
| JPH03102233U (en) | 1991-10-24 |
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