JP6236698B2 - Liquid processing equipment - Google Patents
Liquid processing equipment Download PDFInfo
- Publication number
- 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
- Authority
- JP
- Japan
- Prior art keywords
- liquid
- pipe
- switching valve
- valve
- cooling device
- 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.)
- Active
Links
- 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
Images
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
Claims (3)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2014111256A JP6236698B2 (en) | 2014-05-29 | 2014-05-29 | Liquid processing equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2014111256A JP6236698B2 (en) | 2014-05-29 | 2014-05-29 | Liquid processing equipment |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JP2015223150A JP2015223150A (en) | 2015-12-14 |
| JP6236698B2 true JP6236698B2 (en) | 2017-11-29 |
Family
ID=54840436
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2014111256A Active JP6236698B2 (en) | 2014-05-29 | 2014-05-29 | Liquid processing equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP6236698B2 (en) |
Families Citing this family (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP6449357B2 (en) * | 2017-02-02 | 2019-01-09 | 大日本印刷株式会社 | Beverage aseptic filling system |
| EP4046960A1 (en) * | 2017-02-02 | 2022-08-24 | Dai Nippon Printing Co., Ltd. | Beverage aseptic filling system and carbonated beverage aseptic filling system |
| JP6379233B2 (en) * | 2017-02-02 | 2018-08-22 | 大日本印刷株式会社 | Carbonated beverage aseptic filling system |
| JP7089849B2 (en) * | 2017-03-28 | 2022-06-23 | 株式会社明治 | Beverage filling method |
| WO2023094106A1 (en) * | 2021-11-25 | 2023-06-01 | Sidel Participations | Apparatus for filling containers with a pourable product |
Family Cites Families (30)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5920347B2 (en) * | 1977-09-09 | 1984-05-12 | 株式会社精研舎 | Fruit juice carbonated beverage production equipment |
| JPS5564788A (en) * | 1978-11-06 | 1980-05-15 | Yakult Honsha Co Ltd | Sterilization of device for thermal sterilization of liquid |
| JPS5664996A (en) * | 1979-10-31 | 1981-06-02 | Sanyo Jido Hanbaiki Kk | Liquid feeder |
| US4356681A (en) * | 1980-10-31 | 1982-11-02 | The Seven-Up Company | Method and apparatus for heating containers having a product liquid therein |
| US4416194A (en) * | 1981-12-03 | 1983-11-22 | Fmc Corporation | Beverage pasteurizing system |
| JPH0227236B2 (en) * | 1982-11-19 | 1990-06-15 | Mitsubishi Heavy Ind Ltd | EKISHORISOCHI |
| JPS60116337U (en) * | 1984-01-18 | 1985-08-06 | 株式会社 イズミフ−ドマシナリ | Circulating cleaning device in plate sterilizer |
| JPH0649520B2 (en) * | 1986-08-13 | 1994-06-29 | 三菱重工業株式会社 | Beverage filling line cleaning device |
| JPS63183096U (en) * | 1987-05-15 | 1988-11-25 | ||
| JPH0267863U (en) * | 1988-11-10 | 1990-05-23 | ||
| JPH0753700Y2 (en) * | 1990-02-05 | 1995-12-13 | 三菱重工業株式会社 | Carbonated beverage preparation equipment |
| JP3181072B2 (en) * | 1991-07-01 | 2001-07-03 | 三菱重工業株式会社 | Carbonated water production equipment |
| JPH0523150A (en) * | 1991-07-16 | 1993-02-02 | Showa Tansan Kk | Deaeration method and method and apparatus for producing carbon dioxide water |
| JPH0910286A (en) * | 1995-06-27 | 1997-01-14 | Mitsubishi Heavy Ind Ltd | Device and method for heating and sterilizing product liquid |
| SE513415C2 (en) * | 1998-04-29 | 2000-09-11 | Tetra Laval Holdings & Finance | Method of maintaining pressure difference in a heat treatment plant for liquid food products |
| JP4411701B2 (en) * | 1999-09-03 | 2010-02-10 | 澁谷工業株式会社 | Filling machine |
| JP4366779B2 (en) * | 1999-09-03 | 2009-11-18 | 澁谷工業株式会社 | Beverage production line |
| JP2003117364A (en) * | 2001-10-19 | 2003-04-22 | Mitsubishi Heavy Ind Ltd | Apparatus and method of dissolving gas in liquid and method of manufacturing gas-dissolved liquid |
| JP5090298B2 (en) * | 2002-12-17 | 2012-12-05 | サントリーホールディングス株式会社 | Liquid filling equipment and operating method thereof |
| JP4241254B2 (en) * | 2002-12-17 | 2009-03-18 | サントリー株式会社 | Liquid filling equipment, operation method thereof and heat insulation method |
| JP4265357B2 (en) * | 2003-09-30 | 2009-05-20 | 澁谷工業株式会社 | Filling system |
| JP2006129787A (en) * | 2004-11-05 | 2006-05-25 | Asahi Soft Drinks Co Ltd | Bottled nitrogen source-containing carbonated drink and method for producing the same |
| JP5064657B2 (en) * | 2005-02-02 | 2012-10-31 | アサヒ飲料株式会社 | Method for producing carbonated beverages in containers |
| US8460733B2 (en) * | 2005-05-06 | 2013-06-11 | The Quaker Oats Company | Hot-fill beverage production with flavor injection |
| JP4587964B2 (en) * | 2006-01-31 | 2010-11-24 | 関西電力株式会社 | Heating / cooling device for sterilization |
| JP5080835B2 (en) * | 2006-07-04 | 2012-11-21 | 花王株式会社 | Effervescent container beverage |
| JP5156977B2 (en) * | 2007-11-06 | 2013-03-06 | ザ コカ・コーラ カンパニー | Formulation and production method of carbon dioxide containing soft jelly beverage in sealed container |
| JP2010252702A (en) * | 2009-04-24 | 2010-11-11 | Ito En Ltd | High mineral-containing carbonated drink and method for producing the same |
| JP2012100572A (en) * | 2010-11-09 | 2012-05-31 | Tokyo Electric Power Co Inc:The | Sterilization system |
| JP5838720B2 (en) * | 2011-10-25 | 2016-01-06 | 大日本印刷株式会社 | Sterilization treatment line and purification method thereof |
-
2014
- 2014-05-29 JP JP2014111256A patent/JP6236698B2/en active Active
Also Published As
| Publication number | Publication date |
|---|---|
| JP2015223150A (en) | 2015-12-14 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JP6236698B2 (en) | Liquid processing equipment | |
| JP6460181B2 (en) | Beverage filling method | |
| JP5838720B2 (en) | Sterilization treatment line and purification method thereof | |
| JP4999935B2 (en) | Pasteurization apparatus and pasteurization method with built-in heat pump | |
| US20110209796A1 (en) | Method and apparatus for the sterile filling of two different product flows into a container | |
| JP2010516262A5 (en) | ||
| JP7271613B2 (en) | Method for cleaning-in-place hot food processing lines and food sterilization lines | |
| US8356643B2 (en) | Hot filling system with heat recovery | |
| CN109502532B (en) | A kind of process for sterilizing for sterile filling production line | |
| JP6630272B2 (en) | Method and equipment for pasteurizing products in containers | |
| WO2019245019A1 (en) | Carbonated beverage aseptic filling system, beverage filling system, and cip processing method | |
| US11000052B2 (en) | Filling line for heat-treating and filling a liquid into containers | |
| KR20130028945A (en) | Sterilisation and cleaning method for container | |
| CN111683893B (en) | Method for cleaning sterilization line and sterilization line | |
| JP2017065739A (en) | Sterilization method of beverage supply device and beverage supply device | |
| JP2023143945A (en) | beverage filling system | |
| WO2022138611A1 (en) | Beverage filling system and cip processing method | |
| JP6123870B2 (en) | Sterilization treatment line and purification method thereof | |
| CN112919711A (en) | Device for producing and supplying sterile water and method for operating the device | |
| JP6521396B2 (en) | Aseptic filling system | |
| JP2017121945A (en) | Beverage feeder | |
| TWI721075B (en) | Beverage supply apparatus and operation method and sterilization method of beverage supply apparatus | |
| JP6123871B2 (en) | Sterilization treatment line and purification method thereof | |
| JP6470093B2 (en) | Food and beverage production equipment | |
| WO2022138612A1 (en) | Beverage filling system and cip processing method |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| A625 | Written request for application examination (by other person) |
Free format text: JAPANESE INTERMEDIATE CODE: A625 Effective date: 20161005 |
|
| A711 | Notification of change in applicant |
Free format text: JAPANESE INTERMEDIATE CODE: A712 Effective date: 20170301 |
|
| A521 | Request for written amendment filed |
Free format text: JAPANESE INTERMEDIATE CODE: A821 Effective date: 20170302 |
|
| A977 | Report on retrieval |
Free format text: JAPANESE INTERMEDIATE CODE: A971007 Effective date: 20170818 |
|
| TRDD | Decision of grant or rejection written | ||
| A01 | Written decision to grant a patent or to grant a registration (utility model) |
Free format text: JAPANESE INTERMEDIATE CODE: A01 Effective date: 20170926 |
|
| A61 | First payment of annual fees (during grant procedure) |
Free format text: JAPANESE INTERMEDIATE CODE: A61 Effective date: 20171011 |
|
| R150 | Certificate of patent or registration of utility model |
Ref document number: 6236698 Country of ref document: JP Free format text: JAPANESE INTERMEDIATE CODE: R150 |