JP6236698B2 - Liquid processing equipment - Google Patents
Liquid processing equipment Download PDFInfo
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- JP6236698B2 JP6236698B2 JP2014111256A JP2014111256A JP6236698B2 JP 6236698 B2 JP6236698 B2 JP 6236698B2 JP 2014111256 A JP2014111256 A JP 2014111256A JP 2014111256 A JP2014111256 A JP 2014111256A JP 6236698 B2 JP6236698 B2 JP 6236698B2
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- 239000007788 liquid Substances 0.000 title claims description 319
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 claims description 112
- 238000001816 cooling Methods 0.000 claims description 89
- 229910002092 carbon dioxide Inorganic materials 0.000 claims description 56
- 239000001569 carbon dioxide Substances 0.000 claims description 56
- 238000010438 heat treatment Methods 0.000 claims description 53
- 230000001954 sterilising effect Effects 0.000 claims description 40
- 238000004140 cleaning Methods 0.000 claims description 32
- 235000013361 beverage Nutrition 0.000 claims description 29
- 238000011144 upstream manufacturing Methods 0.000 claims description 22
- 238000004659 sterilization and disinfection Methods 0.000 claims description 15
- 238000004519 manufacturing process Methods 0.000 claims description 13
- 238000010521 absorption reaction Methods 0.000 claims description 8
- 238000010586 diagram Methods 0.000 description 4
- 235000014171 carbonated beverage Nutrition 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- KFSLWBXXFJQRDL-UHFFFAOYSA-N Peracetic acid Chemical compound CC(=O)OO KFSLWBXXFJQRDL-UHFFFAOYSA-N 0.000 description 2
- 244000005700 microbiome Species 0.000 description 2
- 239000000470 constituent Substances 0.000 description 1
- 238000005429 filling process Methods 0.000 description 1
- 235000015203 fruit juice Nutrition 0.000 description 1
- 238000003303 reheating Methods 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
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- Food Preservation Except Freezing, Refrigeration, And Drying (AREA)
- Non-Alcoholic Beverages (AREA)
- Filling Of Jars Or Cans And Processes For Cleaning And Sealing Jars (AREA)
Description
本発明は、液体を、加熱殺菌処理後常温まで冷却処理し、さらに炭酸ガス吸収に適した常温以下の低温度に冷却処理してカーボネータで炭酸ガスを吸収させることにより炭酸ガス入り飲料製造用液体(単に炭酸飲料用液体とも称する)にする液処理装置に関する。 The present invention is a liquid for producing a beverage containing carbon dioxide gas by cooling the liquid to room temperature after heat sterilization treatment, further cooling to a low temperature below room temperature suitable for carbon dioxide absorption, and absorbing carbon dioxide with a carbonator The present invention relates to a liquid processing apparatus (also simply referred to as a carbonated beverage liquid).
一般に、炭酸飲料用液体は、びん或いは缶に充填包装する場合に、充填前工程での液体への炭酸ガス吸収を効率的に行うために、液体を熱交換器などの冷却機器によって炭酸ガス吸収に適した常温以下の低温度に冷却する処理を行っている。(特許文献1,2)
また、果汁入り等の炭酸飲料用液体の場合には、該液体は、加熱機器で加熱殺菌処理をしてから冷却機器によって常温まで冷却処理し、さらに下流側の冷却機器によって炭酸ガス吸収に適した常温以下の低温度まで冷却処理して炭酸ガス吸収を行っている。
Generally, when a carbonated beverage liquid is filled and packaged in a bottle or can, the carbon dioxide gas is absorbed by a cooling device such as a heat exchanger in order to efficiently absorb the carbon dioxide gas into the liquid in the pre-filling process. Cooling to a low temperature below room temperature suitable for (Patent Documents 1 and 2)
In addition, in the case of carbonated beverage liquids such as fruit juice, the liquid is heat-sterilized with a heating device, then cooled to room temperature with a cooling device, and further suitable for absorbing carbon dioxide with a downstream cooling device. The carbon dioxide is absorbed by cooling to a low temperature below room temperature.
液体を加熱殺菌処理後常温まで冷却処理してから、さらに炭酸ガス吸収に適した常温以下の低温度に冷却処理し、下流側のカーボネータへ送液して液体に炭酸ガスを吸収させる従来の液処理装置の1例について、図4および図5に基づいて説明する。
図4は、従来の炭酸ガス入り飲料製造用液体の液処理装置をフローチャートで示す図である。
図5は、図4に示す炭酸ガス入り飲料製造用液体の液処理装置において液体の循環待機、および、液体通路の洗浄または滅菌を説明する図である。
A conventional liquid that is cooled to room temperature after heat sterilization and then cooled to a low temperature below room temperature suitable for carbon dioxide absorption, and sent to a downstream carbonator to absorb carbon dioxide into the liquid. An example of the processing apparatus will be described with reference to FIGS. 4 and 5.
FIG. 4 is a flowchart showing a conventional liquid processing apparatus for liquid for producing beverage containing carbon dioxide gas.
FIG. 5 is a view for explaining the liquid circulation standby and the cleaning or sterilization of the liquid passage in the liquid processing apparatus for producing a carbon dioxide-containing beverage shown in FIG.
図4において、従来の炭酸ガス入り飲料製造用液体の液処理装置(以下、単に液処理装置と称することがある)5は、図示しない上流側の供給元から矢印F1の向きで送液配管POにより弁V1を経て送液部(図示では受タンク)Tへ供給された液体Lを、送液配管PAの途中に設けられたポンプPにより送液して高温(1例として135℃)で加熱殺菌処理する加熱機器Hと、該加熱機器Hと送液配管PBで接続されて前記高温の液体Lを常温(1例として30℃)へ冷却処理する冷却機器CAと、該冷却機器CAと送液配管PCで接続されて前記常温の液体Lを炭酸ガス吸収に適した常温以下の低温度(1例として1℃)まで冷却処理する冷却機器CBと、該冷却機器CBと送液配管PDで接続されて前記低温度の液体Lに炭酸ガスを所定濃度まで吸収させるカーボネータCCによって主に構成されている。 In FIG. 4, a conventional liquid processing apparatus (hereinafter sometimes simply referred to as a liquid processing apparatus) 5 for producing a beverage containing carbon dioxide gas is supplied from a non-illustrated upstream supply source in the direction of arrow F1. The liquid L supplied to the liquid feeding part (reception tank in the figure) T through the valve V1 is fed by a pump P provided in the middle of the liquid feeding pipe PA and heated at a high temperature (135 ° C. as an example). A heating device H for sterilization, a cooling device CA connected to the heating device H by a liquid feeding pipe PB and cooling the high temperature liquid L to room temperature (30 ° C. as an example), and the cooling device CA A cooling device CB that is connected by a liquid pipe PC and cools the liquid L at room temperature to a low temperature below normal temperature (1 ° C. as an example) suitable for carbon dioxide absorption, and the cooling device CB and a liquid supply pipe PD. Connect the carbon dioxide gas to the low temperature liquid L It is mainly constituted by a carbonator CC imbibing up to a concentration.
また、前記送液配管PDの途中には弁V6と弁V7によって構成される切換え弁VDが設けられ、弁V2を介して前記弁V7と前記送液部Tとを接続するリターン配管RPが設けられており、カーボネータCC内の液体Lは送液配管PPの途中に設けられたポンプP2によって図示しない充填装置に向けて送液されるようになっている。 Further, a switching valve VD composed of a valve V6 and a valve V7 is provided in the middle of the liquid supply pipe PD, and a return pipe RP for connecting the valve V7 and the liquid supply part T is provided via the valve V2. The liquid L in the carbonator CC is fed toward a filling device (not shown) by a pump P2 provided in the middle of the liquid feeding pipe PP.
次に、従来の液処理装置5の作用を図4および図5に基づいて説明する。
液処理装置5の製造運転時は、弁V1を開、弁V2を閉に、切換え弁VDの弁V6を開、弁V7を閉にして、図示しない上流側の供給元から送液部Tに送液された液体Lが、図4に太線で示すように、ポンプPによって送液部Tから矢印F2の方向に送液配管PA、加熱機器H、送液配管PB、冷却機器CA、送液配管PC、冷却機器CBへ、さらに、切換え弁VD経由で矢印F4の方向に送液配管PDをカーボネータCCに向けて送液され、前記カーボネータCCで炭酸ガスが所定量吸収されて滅菌済の炭酸ガス入り飲料となって、前記カーボネータCCからポンプP2によって送液配管PPを介して図示しない下流の充填装置へ送液される。
即ち、液体Lは、加熱機器Hでの高圧下の高温加熱により微生物が滅菌処理され、常温への冷却処理を経て、炭酸ガス吸収に適した常温以下の低温度まで冷却処理されて、カーボネータCCで所定濃度の炭酸ガスを吸収して炭酸ガス入り飲料となった後、下流側の充填装置でびん或いは缶等の容器に所定量充填される。
Next, the operation of the conventional
During the manufacturing operation of the
That is, the liquid L is sterilized by microorganisms by high-temperature heating under high pressure in the heating device H, cooled to room temperature, cooled to a low temperature below room temperature suitable for carbon dioxide absorption, and then the carbonator CC After absorbing carbon dioxide of a predetermined concentration to obtain a drink containing carbon dioxide, a predetermined amount is filled in a container such as a bottle or a can with a downstream filling device.
ここで、前記充填装置等の下流側機器の運転が一旦停止となる事態が生じた場合には、前記液体Lは、弁V1を閉、弁V2を開として、また、切換え弁VDの弁V6を閉、弁V7を開として、図5に太線で示すように、ポンプPによって送液部Tから図示矢印F2の方向に送液配管PA,加熱機器H、送液配管PB、冷却機器CA、送液配管PC、冷却機器CB、送液配管PD、切換え弁VDへ、さらに、切換え弁VDから図示矢印FPの方向にリターン配管RPを経て送液部Tへのループで循環されて循環待機状態となり、切換え弁VDから下流側のカーボネータCCへの送液が停止される。 Here, when the operation of the downstream device such as the filling device is temporarily stopped, the liquid L closes the valve V1, opens the valve V2, and the valve V6 of the switching valve VD. Is closed, the valve V7 is opened, and as shown by a thick line in FIG. 5, the pump P feeds the liquid feeding pipe PA, the heating equipment H, the liquid feeding pipe PB, the cooling equipment CA in the direction of the arrow F2 from the liquid feeding section T. Circulating and waiting for circulation to the liquid feeding pipe PC, cooling device CB, liquid feeding pipe PD, switching valve VD, and further in the direction of the arrow FP from the switching valve VD through the return piping RP to the liquid feeding section T Thus, liquid feeding from the switching valve VD to the downstream carbonator CC is stopped.
また、液処理装置5は、製造運転の前或いは後は、加熱機器Hで加熱された熱水或いは過酢酸溶液等の適宜温度の滅菌液から成る洗浄または滅菌用液体S(図5では洗浄または滅菌用液体Sを( )表示している。)が、図5の太線で示すルートで所定時間循環されて、前記液体Lの通路が洗浄または滅菌される。
In addition, before or after the manufacturing operation, the
前記説明の従来の炭酸ガス入り飲料製造用液体の液処理装置5の技術では、切換え弁VDから送液部Tへ送液するリターン配管RPを経る液体Lが循環待機状態の場合に、一旦加熱機器Hにより高温の殺菌温度で加熱殺菌された液体Lが、冷却機器CAによって常温へ冷却され、さらに冷却機器CBによって常温以下の低温度まで冷却された後、再び送液部Tを経て加熱機器Hによって高温の殺菌温度まで再加熱を受けることになり、多くの熱エネルギーを消費し、エネルギーコストが多大となっている可能性がある。
In the technology of the conventional
さらに、従来の炭酸ガス入り飲料製造用液体の液処理装置の他の1例について、図6から図8に基づいて説明する。
図6は、従来の炭酸ガス入り飲料製造用液体の液処理装置の他の1例をフローチャートで示す図である。
図7は、図6に示す炭酸ガス入り飲料製造用液体の液処理装置における液体の循環待機を説明する図である。
図8は、図6に示す炭酸ガス入り飲料製造用液体の液処理装置における洗浄または滅菌用液体の循環を説明する図である。
なお、図6において、先に説明した図4と同じ構造のものについては同じ記号を付してあり、重複する説明は省略する。
Furthermore, another example of a conventional liquid processing apparatus for a liquid for producing a beverage containing carbon dioxide gas will be described with reference to FIGS.
FIG. 6 is a flowchart illustrating another example of a conventional liquid processing apparatus for liquid for producing beverage containing carbon dioxide gas.
FIG. 7 is a diagram for explaining the liquid circulation standby in the liquid processing apparatus for producing carbon dioxide-containing beverages shown in FIG. 6.
FIG. 8 is a diagram for explaining the circulation of the cleaning or sterilizing liquid in the liquid processing apparatus for the liquid for producing a carbonated gas beverage shown in FIG.
In FIG. 6, the same structures as those in FIG. 4 described above are denoted by the same reference numerals, and redundant description is omitted.
図6において、他の1例の従来の炭酸ガス入り飲料製造用液体の液処理装置(以下、単に液処理装置と称することがある)7は、先に図4に基づいて説明した液処理装置5と同様に、送液部T、加熱機器H、冷却機器CA、冷却機器CB、カーボネータCCによって主に構成されているが、冷却機器CAと冷却機器CBがそれぞれ別に配置され、該冷却機器CAと冷却機器CBとが離れた位置になっていて、冷却機器CAと冷却機器CBとを接続する送液配管が、冷却機器CAの下流側の送液配管PEと冷却機器CBの上流の受タンクT7の上流側の送液配管PFが図示しない接続配管で接続されている。 In FIG. 6, another example of a conventional liquid processing apparatus (hereinafter sometimes simply referred to as a liquid processing apparatus) 7 for producing beverage containing carbon dioxide gas is the liquid processing apparatus described above with reference to FIG. 5, the liquid feeding unit T, the heating device H, the cooling device CA, the cooling device CB, and the carbonator CC are mainly configured, but the cooling device CA and the cooling device CB are separately arranged, and the cooling device CA And the cooling device CB are separated from each other, and the liquid supply pipe connecting the cooling device CA and the cooling device CB is a liquid supply pipe PE downstream of the cooling device CA and a receiving tank upstream of the cooling device CB. The liquid supply pipe PF on the upstream side of T7 is connected by a connection pipe (not shown).
なお、前記送液配管PFの前記受タンクT7の入口側には弁V11が設けられている。
さらに、前記受タンクT7と前記冷却機器CBは送液配管PGで接続され、送液配管PGの途中にはポンプP7が設けられていて、受タンクT7内の液体Lが送液配管PG、冷却機器CB、切換え弁VDを伴う送液配管PDを経由してカーボネータCCへ送液されるようになっている。
A valve V11 is provided on the inlet side of the receiving tank T7 of the liquid feeding pipe PF.
Further, the receiving tank T7 and the cooling device CB are connected by a liquid feeding pipe PG, and a pump P7 is provided in the middle of the liquid feeding pipe PG, and the liquid L in the receiving tank T7 is supplied by the liquid feeding pipe PG and the cooling. The liquid is fed to the carbonator CC via the equipment CB and the liquid feed pipe PD with the switching valve VD.
また、送液配管PEの途中には弁V8、弁V9から成る切換え弁VEが設けられ、弁2を介して前記弁V9と送液部Tとを接続するリターン配管RCが設けられているとともに、弁V12を介して切換え弁VDの弁V7と前記受タンクT7とを接続するリターン配管RHが設けられ、該リターン配管RHの途中には加熱機器CHが設けられていて、該加熱機器CHによって後述する洗浄または滅菌用液体Sが所定温度に加熱される構成となっている。 In addition, a switching valve VE including a valve V8 and a valve V9 is provided in the middle of the liquid feeding pipe PE, and a return pipe RC for connecting the valve V9 and the liquid feeding part T via the valve 2 is provided. A return pipe RH is provided for connecting the valve V7 of the switching valve VD and the receiving tank T7 via the valve V12, and a heating device CH is provided in the middle of the return pipe RH. A cleaning or sterilization liquid S described later is heated to a predetermined temperature.
次に、従来の炭酸ガス入り飲料製造用液体の液処理装置7の作用を図6から図8に基づいて説明する。
液処理装置7の製造運転時は、弁V1を開、弁V2を閉に、切換え弁VEの弁V8を開、弁V9を閉に、弁V11を開、弁V12を閉に、切換え弁VDの弁V6を開、弁V7を閉にして、図示しない上流側の供給元から送液部Tに送液された液体Lが、図6に太線で示すように、ポンプPによって送液部Tから矢印F2の方向に送液配管PA、加熱機器H、送液配管PB、冷却機器CA、切換え弁VEを伴う送液配管PE、図示しない接続配管、送液配管PF、弁V11、受タンクT7へ、さらに、ポンプP7によって受タンクT7から送液配管PG、冷却機器CB、切換え弁VDを伴う送液配管PDを経て矢印F4の方向にカーボネータCCへ送液され、前記カーボネータCCで炭酸ガスが所定量吸収されて滅菌済の炭酸ガス入り飲料となって、前記カーボネータCCからポンプP2によって送液配管PPを介して図示しない下流の充填装置へ送液される。
Next, the operation of the conventional
During the manufacturing operation of the
ここで、前記充填装置等の下流側機器の運転が一旦停止となる事態が生じた場合には、前記液体Lは、弁V1を閉、弁V2を開として、また、切換え弁VEの弁V8を閉、弁V9を開として、図7に太線で示すように、ポンプPによって送液部Tから図示矢印F2の方向に送液配管PA、加熱機器H、送液配管PB、冷却機器CA、送液配管PE、切換え弁VEから図示矢印FCの方向にリターン配管RCを、弁V2経由で送液部Tへのループで循環されて循環待機状態となり、切換え弁VEから下流側への送液が停止される。 Here, when the operation of the downstream device such as the filling device is temporarily stopped, the liquid L closes the valve V1, opens the valve V2, and the valve V8 of the switching valve VE. Is closed, the valve V9 is opened, and as shown by a thick line in FIG. 7, the pump P feeds the liquid feeding pipe PA, the heating equipment H, the liquid feeding pipe PB, the cooling equipment CA in the direction of the arrow F2 from the liquid feeding section T. The return pipe RC is circulated in a loop from the liquid feed pipe PE and the switching valve VE in the direction of the arrow FC to the liquid feed section T via the valve V2 to enter a circulation standby state, and the liquid feed from the switch valve VE to the downstream side. Is stopped.
また、液処理装置7は、製造運転の前或いは後は、洗浄または滅菌用液体Sが送液部T内に満たされ、弁V1を閉、弁V2を開として、また、切換え弁VEの弁V8を閉、弁V9を開として、前記送液部T内に満たされた洗浄または滅菌用液体Sが、図8に太線で示すように、ポンプPによって送液部Tから図示矢印F2の方向に送液配管PA、加熱機器H、送液配管PB、冷却機器CA、送液配管PE、切換え弁VEから図示矢印FCの方向にリターン配管RCを弁V2経由で送液部Tへのループで、加熱機器Hで適宜温度に加熱されて所定時間循環され、前記液体Lの通路が洗浄または滅菌される。
さらに、洗浄または滅菌用液体Sが受タンクT7内に満たされ、弁V11を閉、弁V12を開として、また、切換え弁VDの弁V6を閉、弁V7を開として、前記受タンクT7内に満たされた洗浄または滅菌用液体Sが、図8に太線で示すように、ポンプP7によって受タンクT7から図示矢印F3の方向に送液配管PG、冷却機器CB、送液配管PD、切換え弁VDから図示矢印FHの方向に、リターン配管RHを加熱機器CH経由で弁V12を介して受タンクT7へのループで、加熱機器CHで適宜温度に加熱されて所定時間循環され、前記受タンクT7から切換え弁VDの液体Lの通路が洗浄または滅菌される。
即ち、弁V7から加熱機器CH、弁V12経由のリターン配管RHは、洗浄または滅菌用液体Sを前記液体Lの通路が所定条件で洗浄または滅菌されるように適宜温度に加熱する作用を有している。
In addition, before or after the manufacturing operation, the
Further, the cleaning or sterilizing liquid S is filled in the receiving tank T7, the valve V11 is closed, the valve V12 is opened, the valve V6 of the switching valve VD is closed, and the valve V7 is opened. As shown by a thick line in FIG. 8, the cleaning or sterilizing liquid S filled in the tank is fed by the pump P7 from the receiving tank T7 in the direction of the arrow F3 to the liquid feeding pipe PG, the cooling device CB, the liquid feeding pipe PD, and the switching valve. In the direction of the arrow FH from VD, the return pipe RH is heated to an appropriate temperature by the heating device CH through the heating device CH and through the valve V12 to the receiving tank T7, and is circulated for a predetermined time. To the passage of the liquid L of the switching valve VD is cleaned or sterilized.
That is, the return pipe RH from the valve V7 to the heating device CH and the valve V12 has an action of heating the cleaning or sterilizing liquid S to an appropriate temperature so that the passage of the liquid L is cleaned or sterilized under predetermined conditions. ing.
なお、図示しない上流側の供給元から矢印F1の向きで送液配管POにより弁V1を経て送液部Tへ供給された洗浄または滅菌用液体Sを、ポンプPによって送液部Tから矢印F2の方向に送液配管PA、加熱機器H、送液配管PB、冷却機器CA、切換え弁VEを伴う送液配管PE、図示しない接続配管、送液配管PF、弁V11、受タンクT7へ送液する際に、適宜温度になった洗浄または滅菌用液体Sが所定時間通過することにより前記弁V8以降受タンクT7までの送液配管、弁は所定条件で洗浄または滅菌される。
また、前記弁V6以降カーボネータCCまでの送液配管、弁も同様に受タンクT7からカーボネータCCへの洗浄または滅菌用液体Sの送液の際に、前記洗浄または滅菌用液体Sが所定時間通過することにより所定条件で滅菌される。
The cleaning or sterilizing liquid S supplied from the upstream supply source (not shown) to the liquid feeding part T through the valve V1 by the liquid feeding pipe PO in the direction of the arrow F1 is sent from the liquid feeding part T by the pump P to the arrow F2. Liquid feed pipe PA, heating equipment H, liquid feed pipe PB, cooling equipment CA, liquid feed pipe PE with switching valve VE, connection pipe (not shown), liquid feed pipe PF, valve V11, liquid receiving tank T7 At this time, when the cleaning or sterilizing liquid S having an appropriate temperature passes for a predetermined time, the liquid supply piping and valves from the valve V8 to the receiving tank T7 are cleaned or sterilized under predetermined conditions.
Similarly, the liquid supply piping and valves from the valve V6 to the carbonator CC are also passed through the cleaning or sterilizing liquid S for a predetermined time when cleaning from the receiving tank T7 to the carbonator CC or when the sterilizing liquid S is supplied. To sterilize under predetermined conditions.
前記説明の従来の液処理装置7では、冷却機器CAから離れた場所に配置されている冷却機器CBの製造運転の前或いは後の洗浄または滅菌用液体Sを適宜の所定温度にするために、加熱機器CHを設けて洗浄または滅菌用液体Sの循環時の熱負荷を小さくしているが、加熱機器CHの設備費が高価になっている可能性がある。
In the conventional
本発明は、上述の事情に鑑み、製造運転時に下流側機器の運転が一旦停止となる事態が生じた場合において、液体を下流側へ送液しない循環待機状態を低いエネルギーコストで実現でき、また、製造運転の前或いは後の液体通路の洗浄または滅菌のための設備を安価にできる炭酸ガス入り飲料製造用液体の液処理装置を提供することを目的としている。 In view of the above-described circumstances, the present invention can realize a circulation standby state in which liquid is not sent to the downstream side at a low energy cost when the operation of the downstream device is temporarily stopped during the manufacturing operation. An object of the present invention is to provide a liquid processing apparatus for producing a liquid containing carbon dioxide gas, which can reduce the cost of equipment for cleaning or sterilizing the liquid passage before or after the production operation.
前記の課題に対し、本発明は以下の手段により解決を図る。
本発明の第一の態様によれば、炭酸ガス入り飲料製造用液体の液処理装置は、上流側の送液部から送液配管PAによって送液されてくる液体を加熱殺菌する加熱機器Hと、前記加熱機器Hと送液配管PBで接続されて前記加熱機器Hで加熱殺菌された液体を常温まで冷却する冷却機器CAと、前記冷却機器CAと送液配管PCで接続されて前記冷却機器CAで常温まで冷却された液体を炭酸ガス吸収に適した常温以下の低温度に冷却する冷却機器CBと、前記送液配管PCの途中に設けた切換え弁VCと、前記冷却機器CBからカーボネータ等の下流側機器への送液配管PDの途中に設けた切換え弁VDと、前記切換え弁VCと前記上流側の送液部とを接続するリターン配管RAと、前記切換え弁VDと前記切換え弁VCを接続するリターン配管RBにより構成する。
The present invention solves the above problems by the following means.
According to the first aspect of the present invention, the liquid processing apparatus for carbon dioxide-containing beverage production includes a heating device H that heats and sterilizes the liquid sent from the upstream liquid feeding section through the liquid feeding pipe PA. The cooling device CA connected to the heating device H by the liquid feeding pipe PB and cooled to the room temperature by the liquid sterilized by the heating device H, and the cooling device CA and the liquid feeding pipe PC connected to the cooling device CA. A cooling device CB that cools the liquid cooled to normal temperature by CA to a low temperature below normal temperature suitable for carbon dioxide absorption, a switching valve VC provided in the middle of the liquid feeding pipe PC, a carbonator from the cooling device CB, etc. A switching valve VD provided in the middle of the liquid feeding pipe PD to the downstream side device, a return pipe RA connecting the switching valve VC and the upstream liquid feeding section, the switching valve VD and the switching valve VC. Connect to return Constituted by a tube RB.
本発明の第二の態様によれば、前記第一の態様に係る炭酸ガス入り飲料製造用液体の液処理装置において、前記冷却機器CB側への前記液体の供給を一時停止する時には、前記上流側の送液部から、送液配管PA、加熱機器H、送液配管PB、冷却機器CA、送液配管PC、切換え弁VC、リターン配管RA、前記上流側の送液部へのループで順次前記液体の循環を行って液体を循環待機状態にし、前記冷却機器CB側には液体を供給しないように構成する。 According to the second aspect of the present invention, in the liquid processing apparatus for producing liquid containing carbon dioxide gas according to the first aspect, when the supply of the liquid to the cooling device CB side is temporarily stopped, the upstream From the liquid supply part on the side, the liquid supply pipe PA, the heating equipment H, the liquid supply pipe PB, the cooling equipment CA, the liquid supply pipe PC, the switching valve VC, the return pipe RA, and the loop from the upstream liquid supply part in order. The liquid is circulated to bring the liquid into a circulation standby state, and the liquid is not supplied to the cooling device CB side.
本発明の第三の態様によれば、前記第一の態様に係る炭酸ガス入り飲料製造用液体の液処理装置において、該液処理装置の液体通路を洗浄または滅菌する時には、前記上流側の送液部から、送液配管PA、加熱機器H、送液配管PB、冷却機器CA、切換え弁VCを伴う送液配管PC、冷却機器CB、送液配管PD、切換え弁VD、リターン配管RBおよび該リターン配管RBと切換え弁VCで接続されたリターン配管RA、前記上流側の送液部へのループで順次洗浄または滅菌用液体を循環するように構成する。 According to the third aspect of the present invention, in the liquid processing apparatus for producing a carbon dioxide-containing beverage according to the first aspect, when the liquid passage of the liquid processing apparatus is washed or sterilized, the upstream feed is performed. From the liquid part, the liquid feeding pipe PA, the heating equipment H, the liquid feeding pipe PB, the cooling equipment CA, the liquid feeding pipe PC with the switching valve VC, the cooling equipment CB, the liquid feeding pipe PD, the switching valve VD, the return pipe RB and the The return pipe RA is connected to the return pipe RB by the switching valve VC, and the cleaning or sterilization liquid is circulated sequentially in the loop to the upstream liquid feeding section.
上記本発明の態様に係る炭酸ガス入り飲料製造用液体の液処理装置は、上流側の送液部から送液配管PAによって送液されてくる液体を加熱殺菌する加熱機器Hと、前記加熱機器Hと送液配管PBで接続されて前記加熱機器Hで加熱殺菌された液体を常温まで冷却する冷却機器CAと、前記冷却機器CAと送液配管PCで接続されて前記冷却機器CAで常温まで冷却された液体を炭酸ガス吸収に適した常温以下の低温度に冷却する冷却機器CBと、前記送液配管PCの途中に設けた切換え弁VCと、前記冷却機器CBからカーボネータ等の下流側機器への送液配管PDの途中に設けた切換え弁VDと、前記切換え弁VCと前記上流側の送液部とを接続するリターン配管RAと、前記切換え弁VDと前記切換え弁VCを接続するリターン配管RBにより構成して、前記冷却機器CB側への前記液体の供給を一時停止する時には、前記上流側の送液部から、送液配管PA、加熱機器H、送液配管PB、冷却機器CA、送液配管PC、切換え弁VC、リターン配管RA、前記上流側の送液部へのループで順次前記液体の循環を行って液体を循環待機状態にし、前記冷却機器CB側には液体を供給しないようにしたので、循環待機状態で液体を加熱機器Hで再加熱殺菌する際に、冷却機器CBを経由させずに液体を再加熱することができ、循環待機状態における加熱機器Hでの再加熱で消費するエネルギーコストが小さくて済む。 The liquid processing apparatus for producing a carbon dioxide-containing beverage according to the aspect of the present invention includes a heating device H for heating and sterilizing a liquid fed from a liquid feeding section on the upstream side by a liquid feeding pipe PA, and the heating device. A cooling device CA that cools the liquid that has been sterilized by the heating device H and is connected to H by the liquid feeding pipe PB to room temperature, and is connected to the cooling device CA by the liquid feeding pipe PC and is cooled to room temperature by the cooling device CA. A cooling device CB that cools the cooled liquid to a low temperature below normal temperature suitable for carbon dioxide absorption, a switching valve VC provided in the middle of the liquid feeding pipe PC, and downstream devices such as a carbonator from the cooling device CB A switching valve VD provided in the middle of the liquid feeding pipe PD to the pipe, a return pipe RA for connecting the switching valve VC and the upstream liquid feeding section, and a return for connecting the switching valve VD and the switching valve VC. Piping R When the supply of the liquid to the cooling device CB side is temporarily stopped, the liquid supply portion PA, the heating device H, the liquid supply piping PB, the cooling device CA, The liquid is circulated sequentially by the liquid pipe PC, the switching valve VC, the return pipe RA, and the loop to the upstream liquid feeding unit to circulate the liquid, and the liquid is not supplied to the cooling device CB side. Therefore, when the liquid is reheated and sterilized with the heating device H in the circulation standby state, the liquid can be reheated without going through the cooling device CB, and the reheating with the heating device H in the circulation standby state is possible. The energy cost to be consumed is small.
また、該液処理装置の液体通路を洗浄または滅菌する時には、冷却機器CBを冷却機器CAの近くに配置して、前記上流側の送液部から、送液配管PA、加熱機器H、送液配管PB、冷却機器CA、切換え弁VCを伴う送液配管PC、冷却機器CB、送液配管PD、切換え弁VD、リターン配管RBおよび該リターン配管RBと切換え弁VCで接続されたリターン配管RA、前記上流側の送液部へのループで順次洗浄または滅菌用液体を循環するように構成したので、冷却機器CB周りの液体通路を洗浄または滅菌するに際して高価な加熱機器を設ける必要がなく、また、該液体通路の洗浄および滅菌のエネルギーコストが少なくて済む。 Further, when cleaning or sterilizing the liquid passage of the liquid processing apparatus, the cooling device CB is arranged near the cooling device CA, and from the upstream liquid supply unit, the liquid supply pipe PA, the heating device H, the liquid supply Piping PB, Cooling equipment CA, Liquid feeding piping PC with switching valve VC, Cooling equipment CB, Liquid feeding piping PD, Switching valve VD, Return piping RB and Return piping RA connected to the return piping RB with switching valve VC, Since the cleaning or sterilization liquid is circulated sequentially in the loop to the upstream liquid feeding section, there is no need to provide an expensive heating device when cleaning or sterilizing the liquid passage around the cooling device CB. The energy cost of cleaning and sterilizing the liquid passage can be reduced.
以下、この発明の実施の形態につき図面を参照しつつ詳細に説明する。なお、この実施の形態によりこの発明が限定されるものではない。また、下記実施の形態における構成要素には、当業者が容易に想定できるもの、あるいは実質的に同一のものが含まれる。 Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings. Note that the present invention is not limited to the embodiments. In addition, constituent elements in the following embodiments include those that can be easily assumed by those skilled in the art or those that are substantially the same.
(本発明の実施の形態)
本発明の実施の形態を図1から図3に基づいて説明する。
図1は、本発明の実施の形態に係わる炭酸ガス入り飲料製造用液体の液処理装置をフローチャートで示す図である。
図2は、図1に示す炭酸ガス入り飲料製造用液体の液処理装置における液体の循環待機を説明する図である。
図3は、図1に示す炭酸ガス入り飲料製造用液体の液処理装置における洗浄または滅菌用液体の循環を説明する図である。
なお、図1において、従来の液処理装置5および液処理装置7で説明した図4および図6と同じ構造のものは同じ記号を付してあり、重複する説明は省略する。
(Embodiment of the present invention)
An embodiment of the present invention will be described with reference to FIGS.
FIG. 1: is a figure which shows the liquid processing apparatus of the liquid for drinks containing a carbon dioxide gas concerning embodiment of this invention with a flowchart.
FIG. 2 is a diagram for explaining a liquid circulation standby in the liquid processing apparatus for producing a carbon dioxide-containing beverage shown in FIG.
FIG. 3 is a diagram for explaining the circulation of the cleaning or sterilizing liquid in the liquid processing apparatus for the liquid for producing a beverage containing carbon dioxide gas shown in FIG.
In FIG. 1, the same structures as those in FIGS. 4 and 6 described in the conventional
図1において、本発明の実施の形態に係わる炭酸ガス入り飲料製造用液体の液処理装置(以下、単に液処理装置と称することがある)1は、先に図4に基づいて説明した液処理装置5と同様に、送液部T、加熱機器H、冷却機器CA、冷却機器CB、カーボネータCCによって主に構成されているが、冷却機器CAと冷却機器CBが近い位置に配置されていて、冷却機器CAと冷却機器CBとを接続する送液配管PCの途中に弁V3、弁V4、弁V5によって構成される切換え弁VCが設けられ、弁V4と弁V2を介して送液部Tと接続するリターン配管RAが、また、弁V7と弁V5を接続するリターン配管RBが設けられている。
なお、前記リターン配管RAとリターン配管RBは、切換え弁VCの弁V5を開にすることにより接続状態とすることができるようになっている。
In FIG. 1, a liquid processing apparatus (hereinafter, simply referred to as a liquid processing apparatus) 1 for producing a carbon dioxide-containing beverage according to an embodiment of the present invention is the liquid processing described above with reference to FIG. Like the
The return pipe RA and the return pipe RB can be connected by opening the valve V5 of the switching valve VC.
次に、本発明の実施の形態に係わる炭酸ガス入り飲料製造用液体の液処理装置1の作用を図1から図3に基づいて説明する。
液処理装置1の製造運転時は、切換え弁VCの弁V3を開、弁V4を閉に、切換え弁VDの弁V6を開、弁V7を閉にして、図示しない上流側の供給元から送液部Tに送液された液体Lが、図1に太線で示すように、ポンプPによって送液部Tから矢印F2の方向に送液配管PA、加熱機器H、送液配管PB、冷却機器CA、切換え弁VCを伴う送液配管PC、冷却機器CBへ、さらに、矢印F4の方向に切換え弁VDを伴う送液配管PDを介してカーボネータCCへ送液され、前記カーボネータCCで炭酸ガスが所定量吸収されて滅菌済の炭酸ガス入り飲料となって、前記カーボネータCCからポンプP2によって送液配管PPを介して図示しない下流の充填装置へ送液される。
即ち、液体Lは、加熱機器Hでの高圧下の高温加熱により微生物が滅菌処理され、常温への冷却処理を経て、炭酸ガス吸収に適した常温以下の低温度まで冷却処理されて、カーボネータCCで所定濃度の炭酸ガスを吸収して炭酸ガス入り飲料となった後、下流側の充填装置でびん或いは缶等の容器に所定量充填される。
Next, the operation of the liquid treatment apparatus 1 for producing liquid containing carbon dioxide gas according to the embodiment of the present invention will be described with reference to FIGS.
During the manufacturing operation of the liquid processing apparatus 1, the valve V3 of the switching valve VC is opened, the valve V4 is closed, the valve V6 of the switching valve VD is opened, and the valve V7 is closed. The liquid L fed to the liquid part T is fed by the pump P from the liquid feed part T in the direction of the arrow F2, as shown by a thick line in FIG. The liquid is fed to the carbonator CC via the liquid feed pipe PC with the switching valve VD in the direction of the arrow F4 to the CA, the liquid feed pipe PC with the switching valve VC, and the cooling device CB. A predetermined amount is absorbed and becomes a sterilized carbon dioxide-containing beverage, which is fed from the carbonator CC to the downstream filling device (not shown) via the liquid feeding pipe PP by the pump P2.
That is, the liquid L is sterilized by microorganisms by high-temperature heating under high pressure in the heating device H, cooled to room temperature, cooled to a low temperature below room temperature suitable for carbon dioxide absorption, and then the carbonator CC After absorbing carbon dioxide of a predetermined concentration to obtain a drink containing carbon dioxide, a predetermined amount is filled in a container such as a bottle or a can with a downstream filling device.
ここで、製造運転時に、前記充填装置等の下流側機器の運転が一旦停止となる事態が生じた場合には、前記液体Lは、弁V1を閉、弁V2を開として、また、切換え弁VCの弁V4を開、弁V3を閉、弁V5を閉として、図2に太線で示すように、ポンプPによって送液部Tから図示矢印F2の方向に送液配管PA、加熱機器H、送液配管PB、冷却機器CA、送液配管PC、切換え弁VCへ、さらに、切換え弁VCから図示矢印FAの方向にリターン配管RAを経て送液部Tへのループで循環されて、循環待機状態となり、切換え弁VCから下流側の冷却機器CBへの送液が停止される。 Here, when the operation of the downstream equipment such as the filling device is temporarily stopped during the manufacturing operation, the liquid L is closed with the valve V1 and the valve V2 open. The valve V4 of the VC is opened, the valve V3 is closed, the valve V5 is closed, and as shown by a thick line in FIG. 2, the liquid feed pipe PA, the heating device H, Circulated to the liquid feeding pipe PB, the cooling device CA, the liquid feeding pipe PC, the switching valve VC, and further circulated in a loop from the switching valve VC to the liquid feeding section T via the return pipe RA in the direction of the arrow FA shown in the figure. Then, the liquid feeding from the switching valve VC to the downstream cooling device CB is stopped.
また、液処理装置1は、製造運転の前或いは後は、洗浄または滅菌用液体Sが送液部T内に満たされ、弁V1を閉、弁V2を開として、また、切換え弁VCの弁V3を開、弁V5を開、弁V4を閉として、前記送液部T内に満たされた洗浄または滅菌用液体Sが、図3に太線で示すように、ポンプPによって送液部Tから図示矢印F2の方向に送液配管PA、加熱機器H、送液配管PB、冷却機器CA、切換え弁VCを伴った送液配管PC、冷却機器CB、送液配管PD,切換え弁VDから図示矢印FBの方向にリターン配管RBを弁V5へ、さらに弁V2経由でリターン配管RAを送液部Tへのループで、加熱機器Hで適宜温度に加熱されて所定時間循環され、前記液体Lの通路が所定条件で洗浄または滅菌される。
なお、前記説明では弁V4を閉にした場合を説明したが、弁V4を適宜流量調整できる開度で開にして、洗浄または滅菌用液体Sを送液配管PCから冷却機器CB,送液配管PD、切換え弁VD、リターン配管RB、弁V5経由リターン配管RAへ送液するとともに、送液配管PCから弁V4を経由してリターン配管RAへ送液するというように送液を分岐するとしてもよい。
In addition, before or after the manufacturing operation, the liquid processing apparatus 1 is filled with the cleaning or sterilizing liquid S in the liquid feeding portion T, the valve V1 is closed, the valve V2 is opened, and the valve of the switching valve VC. The V3 is opened, the valve V5 is opened, and the valve V4 is closed, and the cleaning or sterilizing liquid S filled in the liquid feeding part T is discharged from the liquid feeding part T by the pump P as shown by a bold line in FIG. In the direction of the illustrated arrow F2, the arrow from the liquid feeding pipe PA, the heating equipment H, the liquid feeding pipe PB, the cooling equipment CA, the liquid feeding pipe PC with the switching valve VC, the cooling equipment CB, the liquid feeding pipe PD, and the switching valve VD. The return pipe RB is routed to the valve V5 in the direction of FB, and the return pipe RA is looped to the liquid feeding section T via the valve V2, and is heated to an appropriate temperature by the heating device H and circulated for a predetermined time, and the passage of the liquid L Is washed or sterilized under predetermined conditions.
In the above description, the valve V4 is closed. However, the valve V4 is opened at an opening that allows the flow rate to be appropriately adjusted, and the cleaning or sterilizing liquid S is supplied from the liquid supply pipe PC to the cooling device CB and the liquid supply pipe. Even if the liquid feeding is branched such that the liquid is fed to the return pipe RA via the PD, the switching valve VD, the return pipe RB, and the valve V5, and the liquid is fed from the liquid feeding pipe PC to the return pipe RA via the valve V4. Good.
前記説明のように、液体Lの循環待機の場合に液体Lが冷却機器CBを経由しないので、加熱機器Hでの加熱の際の熱エネルギーが少なくてすみ、さらに、冷却機器CBを冷却機器CAに近い配置として、切換え弁VCを設けることにより、冷却機器CB周りのための液体通路の洗浄または滅菌用液体Sの加熱装置を設ける必要がなく、また、加熱機器Hによる前記洗浄または滅菌用液体Sの加熱が有効利用されるので、効率的である。 As described above, since the liquid L does not pass through the cooling device CB when the liquid L is in circulation standby, less heat energy is required when heating with the heating device H, and the cooling device CB is replaced with the cooling device CA. By providing the switching valve VC as an arrangement close to the above, there is no need to provide a liquid passage cleaning or sterilizing liquid S heating device around the cooling device CB, and the cleaning or sterilizing liquid by the heating device H is not necessary. Since heating of S is effectively used, it is efficient.
1 (炭酸ガス入り飲料製造用液体の)液処理装置
CA 冷却機器
CB 冷却機器
CC カーボネータ
H 加熱機器
PA、PB、PC、PD 送液配管
RA、RB リターン配管
T 送液部
VC、VD 切換え弁
1 Liquid processing device CA (liquid for carbon dioxide-containing beverage production) Cooling equipment CB Cooling equipment CC Carbonator H Heating equipment PA, PB, PC, PD Liquid feed pipe RA, RB Return pipe T Liquid feed section VC, VD Switching valve
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