JP2018165168A - Method and apparatus for producing beverages contained in container - Google Patents

Method and apparatus for producing beverages contained in container Download PDF

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JP2018165168A
JP2018165168A JP2017063237A JP2017063237A JP2018165168A JP 2018165168 A JP2018165168 A JP 2018165168A JP 2017063237 A JP2017063237 A JP 2017063237A JP 2017063237 A JP2017063237 A JP 2017063237A JP 2018165168 A JP2018165168 A JP 2018165168A
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container
temperature
steam
inert gas
beverage
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JP6767910B2 (en
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峰雄 冨士
Mineo Fuji
峰雄 冨士
豪仁 道添
Takehito Michizoe
豪仁 道添
智史 緒方
Satoshi Ogata
智史 緒方
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Asahi Soft Drinks Co Ltd
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Asahi Soft Drinks Co Ltd
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Abstract

PROBLEM TO BE SOLVED: To provide a method and apparatus for producing beverages contained in a container, each of which can be enhanced a product yield.SOLUTION: A method for producing beverages contained in a container comprises a filling step for filling the container 9 with beverages, a mixing step for mixing inert gas and steam to produce inert gas mixed steam, a mixed steam jet step for jetting the air of an air residual portion in the container in which the beverages have been filled in the filling step and replacing the air of the residual air portion in the container with the inert gas mixed steam obtained in the mixing step, and a sealing step for sealing the container after the mixed steam jet step, and in the mixing step the temperature of the inert gas mixed steam is controlled according to the beverages temperature to be filled at the filling step.SELECTED DRAWING: Figure 1

Description

容器入り飲料の製造方法及び製造装置に関する。 The present invention relates to a manufacturing method and a manufacturing apparatus for a containerized beverage.

特許文献1には、容器入り非炭酸飲料の製造方法において、加熱した飲料を容器に充填後、容器の空寸部分に不活性ガスと蒸気とを混合した不活性ガス混合蒸気を噴射することが開示されている。   In Patent Document 1, in a method for producing a non-carbonated beverage in a container, after the heated beverage is filled in the container, an inert gas mixed steam obtained by mixing an inert gas and steam is injected into the empty portion of the container. It is disclosed.

特開2005−47536号公報JP-A-2005-47536

しかし、加熱した飲料を容器に充填する充填工程において、装置のトラブル等により充填工程が停止することがある。かかる充填工程の停止があると、時間経過と共に充填する飲料温度が低下し、飲料が充填された製品(容器入り飲料)の内圧(真空度)が所定の値に確保できないおそれがある。
このように、所定の内圧が確保できない製品は、その後の検査工程で不良品として廃棄される。このため、製品歩留まりが低下するという問題があった。
However, in the filling process in which the heated beverage is filled in the container, the filling process may be stopped due to troubles of the apparatus. When the filling process is stopped, the temperature of the beverage to be filled decreases with time, and the internal pressure (degree of vacuum) of the product (contained beverage) filled with the beverage may not be ensured to a predetermined value.
In this way, products for which a predetermined internal pressure cannot be ensured are discarded as defective products in the subsequent inspection process. For this reason, there has been a problem that the product yield decreases.

そこで、本発明は、製品歩留まりの向上を図ることができる容器入り飲料の製造方法及び製造装置の提供を目的とする。   Then, an object of this invention is to provide the manufacturing method and manufacturing apparatus of a packaged drink which can aim at the improvement of a product yield.

請求項1に記載の発明は、容器に飲料を充填する充填工程と、不活性ガスと蒸気とを混合して不活性ガス混合蒸気を生成するミックス工程と、ミックス工程で得た不活性ガス混合蒸気を充填工程で飲料を充填した容器の空寸部分に噴射して空寸部分の空気と置換する混合蒸気噴射工程と、混合蒸気噴射工程後の容器に封をする封止工程とを備える容器入り飲料の製造方法であって、前記ミックス工程は、充填工程で充填する飲料温度に応じて不活性ガス混合蒸気の温度を制御することを特徴とする容器入り飲料の製造方法である。   The invention described in claim 1 is a filling step for filling a container with a beverage, a mixing step for mixing an inert gas and steam to generate an inert gas mixed vapor, and an inert gas mixing obtained in the mixing step. A container comprising: a mixed steam injection process for injecting steam into an empty part of a container filled with a beverage in the filling process to replace the air in the empty part; and a sealing process for sealing the container after the mixed steam injection process It is a manufacturing method of a packaged beverage, wherein the mixing step controls the temperature of the inert gas mixed vapor according to the beverage temperature filled in the filling step.

請求項2に記載の発明は、請求項1に記載の発明において、前記ミックス工程は、充填工程で充填する飲料温度と不活性ガス混合蒸気温度と封止後の容器内圧力との関係を求めた実験に基づいて、不活性ガス混合蒸気温度を制御することを特徴とする。   The invention according to claim 2 is the invention according to claim 1, wherein the mixing step obtains a relationship among a beverage temperature to be filled in the filling step, an inert gas mixed vapor temperature, and a pressure in the container after sealing. Based on these experiments, the temperature of the inert gas mixed vapor is controlled.

請求項3に記載の発明は、請求項2に記載の発明において、前記ミックス工程は、蒸気の混合量を制御することで、不活性ガス混合蒸気の温度を制御していることを特徴とする。   The invention according to claim 3 is the invention according to claim 2, wherein the mixing step controls the temperature of the inert gas mixed steam by controlling the mixing amount of the steam. .

請求項4に記載の発明は、請求項3に記載の発明おいて、所定範囲の容器内圧力に対して、充填する飲料温度と不活性ガス混合蒸気温度とを比例関数として求め、前記ミックス工程は、この比例関数に基づいて蒸気の混合量を制御することを特徴とする。   The invention according to claim 4 is the invention according to claim 3, wherein the mixing temperature and the inert gas mixed steam temperature are obtained as a proportional function with respect to the pressure in the container within a predetermined range, and the mixing step Is characterized by controlling the mixing amount of the steam based on this proportional function.

請求項5に記載の発明は、請求項4に記載の発明において、前記ミックス工程で、充填する飲料温度に対する蒸気の混合量の制御は、PID制御であることを特徴とする。   The invention according to claim 5 is characterized in that, in the invention according to claim 4, in the mixing step, the control of the mixing amount of steam with respect to the beverage temperature to be filled is PID control.

請求項6に記載の発明は、請求項1〜5のいずれか一項に記載の発明において、前記飲料は、非炭酸飲料であることを特徴とする。   The invention according to claim 6 is the invention according to any one of claims 1 to 5, wherein the beverage is a non-carbonated beverage.

請求項7に記載の発明は、請求項1〜6のいずれか一項に記載の発明において、前記容器は缶であり、前記封止工程は缶の蓋を巻き締める工程であることを特徴とする。   The invention according to claim 7 is the invention according to any one of claims 1 to 6, wherein the container is a can, and the sealing step is a step of tightening a lid of the can. To do.

請求項8に記載の発明は、容器に飲料を充填するフィラーと、不活性ガスと蒸気とを混合して不活性ガス混合蒸気を生成する混合器と、混合器で得た不活性ガス混合蒸気を、飲料を充填した容器の空寸部分に噴射する混合蒸気噴射部と、不活性ガス混合蒸気噴射後の容器に封をする封止部と、制御部とを備える容器入り飲料の製造装置であって、前記制御部は、充填部で充填する飲料温度に応じて不活性ガス混合蒸気の温度を制御することを特徴とする容器入り飲料の製造装置である。   The invention according to claim 8 is a filler for filling a container with a beverage, a mixer for mixing an inert gas and steam to generate an inert gas mixed steam, and an inert gas mixed steam obtained by the mixer. An apparatus for producing a beverage containing a container, comprising: a mixed vapor injection unit that injects the empty portion of a container filled with a beverage; a sealing unit that seals the container after the inert gas mixed vapor injection; and a control unit And the said control part is a manufacturing apparatus of the drink containing a container characterized by controlling the temperature of an inert gas mixed vapor | steam according to the drink temperature filled with a filling part.

請求項9に記載の発明は、請求項8に記載の発明において、前記制御部は、充填部で充填する飲料の温度に対して混合器における蒸気の混合量を制御することで、不活性ガス混合蒸気の温度を制御していることを特徴とする。   According to a ninth aspect of the invention, in the eighth aspect of the invention, the control unit controls the amount of steam mixed in the mixer with respect to the temperature of the beverage filled in the filling unit. The temperature of the mixed steam is controlled.

請求項1及び8に記載の発明によれば、容器に充填する飲料の温度に基づいて、不活性ガス混合蒸気の温度を制御しているので、製造時のトラブル等により容器に充填する飲料の温度が低下した場合でも、製造後の製品における真空度(内圧)を適正な範囲に保持でき、製品の真空度不備による歩留り低下を防止できる。   According to the first and eighth aspects of the invention, since the temperature of the inert gas mixed vapor is controlled based on the temperature of the beverage to be filled in the container, Even when the temperature is lowered, the degree of vacuum (internal pressure) in the manufactured product can be maintained in an appropriate range, and the yield can be prevented from being lowered due to inadequate vacuum of the product.

請求項2に記載の発明によれば、請求項1に記載の発明と同様の作用効果を奏すると共に、実験から求めた相関関係から不活性ガス混合蒸気の温度を制御するので、実測値に沿った不活性ガス混合蒸気の温度制御ができる。   According to the second aspect of the invention, the same effect as the first aspect of the invention can be obtained, and the temperature of the inert gas mixed steam is controlled from the correlation obtained from the experiment. In addition, the temperature of the inert gas mixed vapor can be controlled.

請求項3に記載の発明によれば、請求項2に記載の発明と同様の作用効果を奏すると共に、蒸気の混合量のみを制御するので、不活性ガス混合蒸気の温度制御が容易にできる。   According to the invention described in claim 3, since the same effect as that of the invention described in claim 2 is achieved and only the mixing amount of the steam is controlled, it is possible to easily control the temperature of the inert gas mixed steam.

請求項4に記載の発明によれば、請求項3に記載の発明と同様の作用効果を奏すると共に、充填する飲料温度と不活性ガス混合蒸気温度とを比例関数として求め、比例関数に基づいて制御するので、簡易な関数で制御が容易である。   According to the fourth aspect of the present invention, the same effects as those of the third aspect of the present invention are obtained, and the beverage temperature to be filled and the inert gas mixed vapor temperature are obtained as a proportional function, and based on the proportional function. Since it controls, control is easy with a simple function.

請求項5に記載の発明によれば、請求項4に記載の発明と同様の作用効果を奏すると共に、不活性ガス混合蒸気の温度管理が迅速に且つ小さな変動幅で制御できる。   According to the fifth aspect of the present invention, the same effect as that of the fourth aspect of the invention can be achieved, and the temperature management of the inert gas mixed vapor can be controlled quickly and with a small fluctuation range.

請求項6に記載の発明によれば、請求項1〜5に記載の発明と同様の作用効果を奏すると共に、自動販売機や製品販売時における加温による容器の変形を防止できる。   According to the sixth aspect of the present invention, the same effects as those of the first to fifth aspects of the present invention can be achieved, and deformation of the container due to heating at the time of vending machine or product sales can be prevented.

請求項7に記載の発明によれば、請求項1〜6に記載の発明と同様の作用効果を奏すると共に、特に蓋の巻き締めを行う缶製品の歩留まりを高めることができる。   According to the seventh aspect of the present invention, the same effects as those of the first to sixth aspects of the present invention can be achieved, and in particular, the yield of can products for tightening the lid can be increased.

請求項9に記載の発明によれば、請求項1に記載の発明と同様の作用効果を奏すると共に、蒸気の混合量のみを制御するので、不活性ガス混合蒸気の温度制御が容易にできる。   According to the ninth aspect of the invention, the same effect as that of the first aspect of the invention can be obtained, and only the mixing amount of the steam is controlled, so that the temperature control of the inert gas mixed steam can be easily performed.

本発明の実施の形態にかかる容器入り飲料の製造方法を概念的に示す断面図であり、(a)は混合蒸気噴射工程であり、(b)は封止工程である。It is sectional drawing which shows notionally the manufacturing method of the drink containing a container concerning embodiment of this invention, (a) is a mixed vapor injection process, (b) is a sealing process. 本発明の実施の形態における混合蒸気噴射工程前の容器と蓋の状態を示す正面図である。It is a front view which shows the state of the container and lid | cover before the mixed steam injection process in embodiment of this invention. 本発明の実施の形態における不活性ガス混合蒸気噴射工程を示す正面図である。It is a front view which shows the inert gas mixed vapor injection process in embodiment of this invention. 本発明の実施の形態における封止工程前の状態を示す正面図である。It is a front view which shows the state before the sealing process in embodiment of this invention. 本発明の実施の形態における封止工程後の状態を示す正面図である。It is a front view which shows the state after the sealing process in embodiment of this invention. フィラーで飲料を充填後の容器の流れを示す平面図である。It is a top view which shows the flow of the container after filling a drink with a filler. ミックス工程の回路図である。It is a circuit diagram of a mixing process. ファイラー充填液温度と不活性ガス混合蒸気温度(混合ガス温度)との関係を示すグラフである。It is a graph which shows the relationship between a filler filling liquid temperature and an inert gas mixed steam temperature (mixed gas temperature). 不活性ガス混合蒸気を温度制御した場合のフィラー充填液温度と真空度との関係を示すグラフである。It is a graph which shows the relationship between the filler filling liquid temperature at the time of carrying out temperature control of the inert gas mixed vapor | steam, and a vacuum degree.

以下に、添付図面を参照して本発明の実施の形態について説明する。
図1に示すように、本実施の形態にかかる容器入り飲料の製造装置1は、蒸気導入管3と不活性ガス導入管5と、混合器7と、混合ガス噴射部12と、容器9に飲料を充填するフィラー11(図6参照)と、フィラー11における飲料(充填液)の温度検知部13と、制御部15と、容器に封をする封止部17とを備えている。
飲料は、加熱して容器に充填する種類の飲料であり、いわゆる陰圧充填製品の飲料である。例えば、乳入りコーヒー飲料である。
Embodiments of the present invention will be described below with reference to the accompanying drawings.
As shown in FIG. 1, the container-containing beverage production apparatus 1 according to the present embodiment includes a steam introduction pipe 3, an inert gas introduction pipe 5, a mixer 7, a mixed gas injection unit 12, and a container 9. The filler 11 (refer FIG. 6) with which a drink is filled, the temperature detection part 13 of the drink (filler liquid) in the filler 11, the control part 15, and the sealing part 17 which seals a container are provided.
The beverage is a type of beverage that is heated and filled into a container, and is a so-called negative pressure filling product beverage. For example, a milky coffee drink.

容器9は、缶容器であり、缶本体9aに蓋9bが巻き締められている。
蒸気導入管3には、流量コントロールバルブ21が設けてあり、混合器7に導入する蒸気の流入量を制御している。
不活性ガスは窒素ガス(N)が用いられており、不活性ガス導入管5にも流量コントロールバルブ23が設けてある。
混合器7は蒸気導入管3と不活性ガス導入管5とに接続されており、導入された窒素ガス(不活性ガス)と蒸気とを混合して、混合ガス噴射部12に供給する。混合器7は本実施の形態ではエジェクターである。
The container 9 is a can container, and a lid 9b is wound around the can body 9a.
The steam introduction pipe 3 is provided with a flow rate control valve 21 to control the inflow amount of steam introduced into the mixer 7.
Nitrogen gas (N 2 ) is used as the inert gas, and the inert gas introduction pipe 5 is also provided with a flow rate control valve 23.
The mixer 7 is connected to the steam introduction pipe 3 and the inert gas introduction pipe 5. The introduced nitrogen gas (inert gas) and steam are mixed and supplied to the mixed gas injection unit 12. The mixer 7 is an ejector in the present embodiment.

混合ガス噴射部12は、缶蓋9bの巻き締め工程前に、飲料が充填された缶本体9aの空寸部分Sに向けて窒素ガス(不活性ガス)と蒸気との混合ガス(以下単に、「混合ガス」という)を噴射する。尚、図1では、説明の為に、混合ガス噴射部12は缶本体9aの上方から下方に向けて混合ガスを噴射しているが、実際には缶本体9aと缶蓋9bとの間に側方から混合ガスを噴射する(図2〜4参照)。
制御部15は、フィラーチャンバ(図示せず)に設けてフィラー11の充填液温度を検知する温度検知部13と、蒸気の流量コントロールバルブ21とに接続されており、温度検知部13で検知した温度に基づいて流量コントロールバルブ21を制御している。
封止部17では、缶本体9aに蓋9bを巻き締める。
The mixed gas injection unit 12 is a mixed gas of nitrogen gas (inert gas) and steam (hereinafter simply referred to as “empty space portion S” of the can body 9a filled with a beverage before the can lid 9b is tightened). "Mixed gas"). In FIG. 1, the mixed gas injection unit 12 injects the mixed gas from the upper side to the lower side of the can body 9a for the sake of explanation, but in actuality, between the can body 9a and the can lid 9b. A mixed gas is injected from the side (see FIGS. 2 to 4).
The control unit 15 is provided in a filler chamber (not shown) and connected to a temperature detection unit 13 that detects the filling liquid temperature of the filler 11 and a steam flow rate control valve 21, and is detected by the temperature detection unit 13. The flow control valve 21 is controlled based on the temperature.
In the sealing part 17, the lid 9b is wound around the can body 9a.

ここで、図6を参照して、フィラー11で缶本体9aに飲料を充填してから製品までの概略的な流れを説明する。
フィラー11で缶本体9aに飲料を充填した後、缶本体9aは混合ガス噴射部12へ搬送される。
一方、缶蓋9bは、缶蓋スタック29からキャンフィードターレット31に供給される。混合ガス噴射部12では、本体9aの空寸部分Sに混合ガスを噴射(図1(a)参照)した後、封止部17で缶本体9aに缶蓋9bが巻き締められた後(図1(b)参照)、センターターレット33及びディスチャージターレット35を経由して、下流側の次工程へ搬送される。尚、図6では缶蓋9bにハッチを付している。
Here, with reference to FIG. 6, a schematic flow from filling of the can body 9 a with the beverage with the filler 11 to the product will be described.
After filling the can main body 9 a with the filler 11, the can main body 9 a is conveyed to the mixed gas injection unit 12.
On the other hand, the can lid 9 b is supplied from the can lid stack 29 to the can feed turret 31. In the mixed gas injection unit 12, after the mixed gas is injected into the empty portion S of the main body 9a (see FIG. 1A), the can lid 9b is wound around the can main body 9a by the sealing unit 17 (see FIG. 1). 1 (b)), it is conveyed to the downstream downstream process through the center turret 33 and the discharge turret 35. In FIG. 6, the can lid 9b is hatched.

次に、混合ガス噴射部12及び封止部17の工程について説明する。
図2及び図6に示すように、飲料が充填された缶本体9a及び缶蓋9bが、混合ガス噴射部12に搬送されてくる。
次に、図3及び図4に示すように、缶本体9a及び缶蓋9bの搬送中に、缶本体9aと缶蓋9bとの間の空間にキャンフィードターレット31の下方に位置するガスターレット30の混合ガス噴射部12から混合ガスが噴射されて、缶本体9aの空寸部分Sにある空気が混合ガスと置換される。尚、混合ガスは、缶本体9aと缶蓋9bとの間の空間に側方から噴射される。
その後、図4に示すように、缶蓋9bが缶本体9aの上方位置から、缶蓋9bを押し下げて後、図5に示すように、封止部17で缶蓋9bを缶本体9aに巻き締める(図1(b)参照)。
Next, the process of the mixed gas injection part 12 and the sealing part 17 is demonstrated.
As shown in FIGS. 2 and 6, the can body 9 a and the can lid 9 b filled with beverage are conveyed to the mixed gas injection unit 12.
Next, as shown in FIGS. 3 and 4, the gas turret 30 positioned below the can feed turret 31 in the space between the can body 9a and the can lid 9b during the conveyance of the can body 9a and the can lid 9b. The mixed gas is injected from the mixed gas injection unit 12 to replace the air in the empty portion S of the can body 9a with the mixed gas. The mixed gas is injected from the side into the space between the can body 9a and the can lid 9b.
Thereafter, as shown in FIG. 4, after the can lid 9b pushes down the can lid 9b from a position above the can body 9a, the can lid 9b is wound around the can body 9a by the sealing portion 17 as shown in FIG. Tighten (see FIG. 1B).

次に、混合ガス噴射部12で噴射する混合ガスについて説明する。
図7はミックス工程における混合ガスの回路図を示している。図7に示すように、蒸気導入管3には、蒸気供給部41と混合器7との間で蒸気供給部41側から順に、開閉弁43、圧力計45、流量コントロールバルブ21、圧力計45、電磁弁49、ニードル弁51及び圧力計45がこの順序で設けてある。また、開閉弁43と流量コントロールバルブ21との間の圧力計45の位置には、スチームトラップ46が設けてある。流量コントロールバルブ21には制御部15が接続されており、フィラー充填液の温度を検知する温度検知部13の検知温度に基づいて制御部15により蒸気の流量が制御されている。
Next, the mixed gas injected by the mixed gas injection unit 12 will be described.
FIG. 7 shows a circuit diagram of the mixed gas in the mixing step. As shown in FIG. 7, the steam introduction pipe 3 includes an on-off valve 43, a pressure gauge 45, a flow rate control valve 21, and a pressure gauge 45 in order from the steam supply section 41 between the steam supply section 41 and the mixer 7. The solenoid valve 49, the needle valve 51, and the pressure gauge 45 are provided in this order. A steam trap 46 is provided at the position of the pressure gauge 45 between the on-off valve 43 and the flow control valve 21. A control unit 15 is connected to the flow rate control valve 21, and the flow rate of the steam is controlled by the control unit 15 based on the temperature detected by the temperature detection unit 13 that detects the temperature of the filler filling liquid.

窒素ガス導入管5には、窒素ガス供給部53と混合器7との間に窒素ガス供給部53側から順に、開閉弁43、圧力計45、開閉弁43、流量コントロールバルブ23、圧力計45、流量計48、電磁弁49、ニードル弁51がこの順序で設けてある。尚、流量コントロールバルブ23の上流側にはカバーガッシング経路54が分岐されているが、カバーガッシング経路54の説明は省略する。
混合器7と混合ガス噴射部12との間には、混合器7側から分離器55、ニードル弁51が設けてあり、分離器55にはスチームトラップ46及び圧力計45が設けてある。
In the nitrogen gas introduction pipe 5, an opening / closing valve 43, a pressure gauge 45, an opening / closing valve 43, a flow rate control valve 23, and a pressure gauge 45 are arranged between the nitrogen gas supply section 53 and the mixer 7 in this order from the nitrogen gas supply section 53 side. The flow meter 48, the electromagnetic valve 49, and the needle valve 51 are provided in this order. A cover gassing path 54 is branched on the upstream side of the flow control valve 23, but the description of the cover gassing path 54 is omitted.
A separator 55 and a needle valve 51 are provided between the mixer 7 and the mixed gas injection unit 12 from the mixer 7 side, and a steam trap 46 and a pressure gauge 45 are provided in the separator 55.

次に、図8を参照して、フィラー充填液温度と混合ガス温度との関係について説明する。
図8のグラフにおいて、黒四角はフィラー充填液温度の変化に関係なく混合ガスの温度を一定にした場合である(追従制御無)。
黒丸はフィラー充填液温度の変化に対して、製品内圧力(真空度)が36〜40kPa(キロパスカル)の範囲内になるように制御部15で制御したときの混合ガスの温度である(追従制御有)。制御した混合ガスの温度は、蒸気の混合量を変えることにより調整した。
混合ガスの温度は、各フィラー充填液温度に対して3個の検体についておこなった測定値の平均をグラフにプロットした。
Next, the relationship between the filler filling liquid temperature and the mixed gas temperature will be described with reference to FIG.
In the graph of FIG. 8, the black square is the case where the temperature of the mixed gas is made constant regardless of the change in the filler filling liquid temperature (no follow-up control).
The black circle is the temperature of the mixed gas when the control unit 15 controls the pressure in the product (vacuum degree) to be in the range of 36 to 40 kPa (kilopascal) with respect to the change in the filler filling liquid temperature (follow-up). With control). The temperature of the controlled mixed gas was adjusted by changing the mixing amount of the steam.
As for the temperature of the mixed gas, the average of the measured values of three specimens with respect to each filler filling liquid temperature was plotted in a graph.

この実験では、フィラーを停止し、10分、20分、30分、40分、50分後の各再稼働時にその時の各フィラー充填液温度で、フィラー充填液の充填、混合ガスの噴射及び缶蓋の巻き締めを行った。更に、50分経過後にフィラーを含むライン全体を再稼働したときのフィラー充填液温度と混合ガス温度を測定した。   In this experiment, the filler was stopped, filled with filler filling liquid, mixed gas injection and can at each filler filling liquid temperature at each restart after 10 minutes, 20 minutes, 30 minutes, 40 minutes and 50 minutes. The lid was tightened. Furthermore, the filler filling liquid temperature and mixed gas temperature when the whole line containing a filler was restarted after 50 minutes passed were measured.

図8に示すグラフから、黒丸のプロットの相関関係を求めると、一点鎖線で示すように、フィラー充填液温度に対する混合ガス温度との関係は比例関係(線形)にあることが分かった。図8に示すように実験結果から、下記(制御式1)を求めた。
y=−0.2254x+112.53 (制御式1)
ここでxはフィラー充填液温度、yは混合ガス温度である。
更に、求めた制御式1の確認実験を行ったので、図9を参照して、その内容について説明する。フィラー充填液温度に対する混合ガス温度との関係で得た(制御式1)に対して、混合ガス温度を、制御式1をそのまま(破線)、制御式1+0.2℃(実線)、制御式1+0.4℃(一点鎖線)、制御式1+0.6℃(二点鎖線)に混合ガスの温度を制御して、混合ガスの噴射を行い、得られた製品について真空度を測定した。その結果を図9に示す。この実験についても、フィラーを停止後、10分、20分、30分、40分、50分後の経過時間に伴って温度が低下したフィラー充填液について、各温度で3個の検体について測定した真空度の平均値を、グラフにプロットした。
From the graph shown in FIG. 8, when the correlation between the black circle plots was obtained, it was found that the relationship between the filler gas filling liquid temperature and the mixed gas temperature was proportional (linear) as indicated by the alternate long and short dash line. As shown in FIG. 8, the following (control formula 1) was obtained from the experimental results.
y = −0.2254x + 112.53 (control formula 1)
Here, x is the filler filling liquid temperature, and y is the mixed gas temperature.
Furthermore, since the confirmation experiment of the obtained control formula 1 was performed, the content will be described with reference to FIG. In contrast to (control equation 1) obtained in relation to the gas mixture temperature with respect to the filler filling liquid temperature, the control gas equation 1 remains unchanged (broken line), control equation 1 + 0.2 ° C. (solid line), control equation 1 + 0. The temperature of the mixed gas was controlled to 4 ° C. (one-dot chain line) and control formula 1 + 0.6 ° C. (two-dot chain line), and the mixed gas was injected, and the degree of vacuum of the obtained product was measured. The result is shown in FIG. In this experiment, three specimens were measured at each temperature for the filler filling liquid whose temperature decreased with the elapsed time after 10 minutes, 20 minutes, 30 minutes, 40 minutes, and 50 minutes after stopping the filler. The average value of the degree of vacuum was plotted on a graph.

図9には、真空度36〜40KPaの管理領域Pをドッド領域で示している。真空度36〜40KPaの管理領域Pは、製品内圧として良好としている範囲であり、この範囲からずれた真空度は、不良品として排斥している。
図9から明らかなように、図8で求めた制御式1のまま(破線)では、フィラー充填液温度の低下に伴って真空度は低下し、フィラー充填液温度が72°以下では、真空度は32KPa付近まで低下した。また、制御式1+0.4、制御式1+0.6では真空度40を越えて、41〜44KPa付近となり、管理領域Pよりも上方にずれた不良品となった。
これに対して、制御式1+0.2(実線)は、フィラー充填液温度が78℃から68℃に低下した場合でも、真空度36〜40KPaの範囲内にあり管理領域P内である良品であった。
したがって、混合ガスの温度が、制御式1+0.2℃ になるように蒸気の混合量を制御することで、ファイラー充填液温度が低下した場合でも真空度に関して不良品の発生を防止できる。
In FIG. 9, the management area P having a degree of vacuum of 36 to 40 KPa is shown as a dod area. The management area P having a degree of vacuum of 36 to 40 KPa is a range in which the product internal pressure is good, and the degree of vacuum deviating from this range is rejected as a defective product.
As is clear from FIG. 9, with the control equation 1 obtained in FIG. 8 (broken line), the degree of vacuum decreases as the filler filling liquid temperature decreases, and when the filler filling liquid temperature is 72 ° C. or less, the degree of vacuum is reduced. Decreased to around 32 KPa. In addition, in the control formula 1 + 0.4 and the control formula 1 + 0.6, the degree of vacuum exceeded 40 and the vicinity of 41 to 44 KPa, which was a defective product shifted upward from the management region P.
On the other hand, the control formula 1 + 0.2 (solid line) is a non-defective product that is within the management range P within the vacuum range of 36 to 40 KPa even when the filler filling liquid temperature falls from 78 ° C. to 68 ° C. It was.
Therefore, by controlling the mixing amount of the steam so that the temperature of the mixed gas becomes the control formula 1 + 0.2 ° C., it is possible to prevent the occurrence of defective products regarding the degree of vacuum even when the filer filling liquid temperature is lowered.

上記のようにして得た下記式2を用いて混合ガス温度を制御した場合(実験1)と、温度制御することなく停止前と同じ混合ガス温度で混合ガスの噴射を行った場合(比較実験1)について実験をおこなったのでその結果について説明する。
(実験1)
制御部15では、混合ガス温度が下記式2で求めた目標温度になるように、流量コントロールバルブ21をPID制御した。
混合ガス温度=制御式1+0.2℃ (式2)
y=−0.2254x+112.53 (制御式1)
実験は、フィラーを50分停止した後、再稼働して、充填、混合ガス噴射及び巻き締めを行い、検体を製造した。その後、各検体について真空度を測定した。真空度は打鍵器で測定し、良品か不良品かを判定した。
尚、フィラー停止後のファイラー充填液の温度は、停止後、10分が76.2℃、20分が74.7、30分が73.0℃、40分が71.2℃、50分が70.2℃であった。
実験1において、検体数18、706本に対して不良は65本であり、不良率は0.330%であった。
When the mixed gas temperature is controlled using the following formula 2 obtained as described above (Experiment 1), and when the mixed gas is injected at the same mixed gas temperature as before the stop without temperature control (Comparative experiment) Since an experiment was conducted on 1), the results will be described.
(Experiment 1)
In the control unit 15, the flow rate control valve 21 is PID-controlled so that the mixed gas temperature becomes the target temperature obtained by the following formula 2.
Mixed gas temperature = Control formula 1 + 0.2 ° C. (Formula 2)
y = −0.2254x + 112.53 (control formula 1)
In the experiment, the filler was stopped for 50 minutes and then restarted to perform filling, mixed gas injection, and tightening to produce a specimen. Thereafter, the degree of vacuum was measured for each specimen. The degree of vacuum was measured with a keystroke device to determine whether the product was good or defective.
The temperature of the filler filling liquid after stopping the filler is 76.2 ° C. for 10 minutes, 74.7 for 20 minutes, 73.0 ° C. for 30 minutes, 71.2 ° C. for 40 minutes, and 50 minutes for 50 minutes. It was 70.2 ° C.
In Experiment 1, the number of defects was 65 with respect to 18,706 samples, and the defect rate was 0.330%.

(比較実験1)
実験1と同様に、フィラーを50分停止した後、再稼働して、充填、混合ガス噴射及び巻き締めを行い、検体を製造した。比較実験1では混合ガス温度の制御を行わないで、停止前と同じ混合ガス温度で混合ガス噴射を行った。フィラー充填液温度は、停止後の時間10分が76.2℃、20分が74.4、30分が72.9℃、40分が71.5℃、50分が69.9℃であった。
検体数は22350本に対して不良は230本であり、不良率は1.029%であった。
以上のように、比較実験1の不良率が1.029%であるのに対して、本実施の形態にかかる実験1では不良率は0.330%であり、混合ガスの温度制御をすることで、不良率を大幅に低減できた。
(Comparative Experiment 1)
In the same manner as in Experiment 1, the filler was stopped for 50 minutes and then restarted to perform filling, mixed gas injection, and tightening to produce a specimen. In Comparative Experiment 1, the mixed gas was injected at the same mixed gas temperature as before the stop without controlling the mixed gas temperature. The filler filling liquid temperature was 76.2 ° C for 10 minutes after the stop, 74.4 for 20 minutes, 72.9 ° C for 30 minutes, 71.5 ° C for 40 minutes, and 69.9 ° C for 50 minutes. It was.
The number of specimens was 230 with respect to 22350, and the defect rate was 1.029%.
As described above, the failure rate in Comparative Experiment 1 is 1.029%, whereas in Experiment 1 according to the present embodiment, the failure rate is 0.330%, and the temperature of the mixed gas is controlled. The defect rate was greatly reduced.

本発明は、前述した実施の形態に限定されるものではなく、その要旨を逸脱しない範囲で種々変形可能である。
例えば、容器入り飲料の容器は、缶の蓋を巻き締めすることに限らず、ボトル状の缶容器であっても良く、この場合に封止工程では、キャップをボトルの口部に回して閉め付ける。
飲料は、コーヒー飲料に限らず、乳入り紅茶やお茶、果汁飲料等であっても良い。
The present invention is not limited to the embodiment described above, and various modifications can be made without departing from the scope of the invention.
For example, the container of the beverage in a container is not limited to tightening the lid of the can but may be a bottle-shaped can container. In this case, in the sealing process, the cap is turned to the mouth of the bottle and closed. wear.
Beverages are not limited to coffee drinks, and may be milk tea, tea, fruit juice drinks, or the like.

1 容器入り飲料の製造装置
7 混合器
9 容器
12 混合ガス噴射部
13 充填液温度検知部
15 制御部
17 封止部
21 流量コントロールバルブ
S 空寸部分
DESCRIPTION OF SYMBOLS 1 Manufacturing apparatus of a drink in a container 7 Mixer 9 Container 12 Mixed gas injection part 13 Filling liquid temperature detection part 15 Control part 17 Sealing part 21 Flow control valve S Empty part

Claims (9)

容器に飲料を充填する充填工程と、不活性ガスと蒸気とを混合して不活性ガス混合蒸気を生成するミックス工程と、ミックス工程で得た不活性ガス混合蒸気を充填工程で飲料を充填した容器の空寸部分に噴射して空寸部分の空気と置換する混合蒸気噴射工程と、混合蒸気噴射工程後の容器に封をする封止工程とを備える容器入り飲料の製造方法であって、
前記ミックス工程は、充填工程で充填する飲料温度に応じて不活性ガス混合蒸気の温度を制御することを特徴とする容器入り飲料の製造方法。
A filling process for filling a container with a beverage, a mixing process for mixing an inert gas and steam to generate an inert gas mixed steam, and a filling process for filling the inert gas mixed steam obtained in the mixing process with the beverage. A method for producing a beverage containing a container, comprising: a mixed vapor injection step of injecting into an empty portion of a container to replace air of the empty portion; and a sealing step of sealing the container after the mixed vapor injection step,
The said mixing process controls the temperature of an inert gas mixed vapor | steam according to the drink temperature filled at a filling process, The manufacturing method of the drink containing a container characterized by the above-mentioned.
前記ミックス工程は、充填工程で充填する飲料温度と不活性ガス混合蒸気温度と封止後の容器内圧力との関係を求めた実験に基づいて、不活性ガス混合蒸気温度を制御することを特徴とする請求項1に記載の容器入り飲料の製造方法。   The mixing step is characterized in that the inert gas mixed vapor temperature is controlled based on an experiment for determining the relationship between the beverage temperature to be filled in the filling step, the inert gas mixed vapor temperature, and the pressure in the container after sealing. The method for producing a containerized beverage according to claim 1. 前記ミックス工程は、蒸気の混合量を制御することで、不活性ガス混合蒸気の温度を制御していることを特徴とする請求項2に記載の容器入り飲料の製造方法。   The said mixing process is controlling the temperature of the inert gas mixed vapor | steam by controlling the mixing amount of vapor | steam, The manufacturing method of the packaged beverage of Claim 2 characterized by the above-mentioned. 所定範囲の容器内圧力に対して、充填する飲料温度と不活性ガス混合蒸気温度とを比例関数として求め、前記ミックス工程は、この比例関数に基づいて蒸気の混合量を制御することを特徴とする請求項3に記載の容器入り飲料の製造方法。   The beverage temperature to be filled and the inert gas mixed steam temperature are obtained as a proportional function with respect to the pressure in the container in a predetermined range, and the mixing step controls the mixing amount of the steam based on the proportional function. The manufacturing method of the drink containing a container of Claim 3 to do. 前記ミックス工程で、充填する飲料温度に対する蒸気の混合量の制御は、PID制御であることを特徴とする請求項4に記載の容器入り飲料の製造方法。   5. The method for producing a containerized beverage according to claim 4, wherein the control of the mixing amount of the steam with respect to the beverage temperature to be filled in the mixing step is PID control. 前記飲料は、非炭酸飲料であることを特徴とする請求項1〜5のいずれか一項に記載の容器入り飲料の製造方法。   The said drink is a non-carbonated drink, The manufacturing method of the drink in a container as described in any one of Claims 1-5 characterized by the above-mentioned. 前記容器は缶であり、前記封止工程は缶の蓋を巻き締める工程であることを特徴とする請求項1〜6のいずれか一項に記載の容器入り飲料の製造方法。   The said container is a can, The said sealing process is a process of tightening the lid | cover of a can, The manufacturing method of the drink containing a container as described in any one of Claims 1-6 characterized by the above-mentioned. 容器に飲料を充填するフィラーと、不活性ガスと蒸気とを混合して不活性ガス混合蒸気を生成する混合器と、混合器で得た不活性ガス混合蒸気を、飲料を充填した容器の空寸部分に噴射する混合蒸気噴射部と、不活性ガス混合蒸気噴射後の容器に封をする封止部と、制御部とを備える容器入り飲料の製造装置であって、
前記制御部は、充填部で充填する飲料温度に応じて不活性ガス混合蒸気の温度を制御することを特徴とする容器入り飲料の製造装置。
A filler for filling a container with a beverage, a mixer for mixing an inert gas and steam to generate an inert gas mixed steam, and an inert gas mixed steam obtained by the mixer are used to empty the container filled with the beverage. A device for producing a beverage containing a container, comprising: a mixed vapor injection unit that injects into the size part; a sealing unit that seals the container after the inert gas mixed vapor injection; and a control unit,
The said control part controls the temperature of an inert gas mixed vapor | steam according to the beverage temperature with which a filling part is filled, The manufacturing apparatus of the drink with a container characterized by the above-mentioned.
前記制御部は、充填部で充填する飲料の温度に対して混合器における蒸気の混合量を制御することで、不活性ガス混合蒸気の温度を制御していることを特徴とする請求項8に記載の容器入り飲料の製造装置。   The said control part is controlling the temperature of the inert gas mixed steam by controlling the mixing amount of the vapor | steam in a mixer with respect to the temperature of the drink with which a filling part is filled, The characterized by the above-mentioned. The manufacturing apparatus of the drink with a container of description.
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