JPH0121950B2 - - Google Patents

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Publication number
JPH0121950B2
JPH0121950B2 JP62129729A JP12972987A JPH0121950B2 JP H0121950 B2 JPH0121950 B2 JP H0121950B2 JP 62129729 A JP62129729 A JP 62129729A JP 12972987 A JP12972987 A JP 12972987A JP H0121950 B2 JPH0121950 B2 JP H0121950B2
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JP
Japan
Prior art keywords
speed
low
liquefied gas
temperature liquefied
discharge holes
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired
Application number
JP62129729A
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Japanese (ja)
Other versions
JPS6352865A (en
Inventor
Eiichi Yoshida
Nobuyasu Aoki
Toshimitsu Suzuki
Akira Ppongo
Hideki Ueda
Kazunari Nakada
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Teisan KK
Original Assignee
Teisan KK
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Filing date
Publication date
Application filed by Teisan KK filed Critical Teisan KK
Priority to JP62129729A priority Critical patent/JPS6352865A/en
Publication of JPS6352865A publication Critical patent/JPS6352865A/en
Publication of JPH0121950B2 publication Critical patent/JPH0121950B2/ja
Granted legal-status Critical Current

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Description

【発明の詳細な説明】[Detailed description of the invention]

(産業上の利用分野) 本発明は、缶詰缶に内圧を与えるための不活性
ガスを、低温の液化状態で密封直前の缶内に所定
量づつ添加してガス封入缶詰を製造する方法、特
に、途中で缶詰製造ラインの速度が変化する高速
缶詰製造ラインにおいて、内容物が充填されてか
ら缶蓋巻締機へ移動中の缶内に、低温液化ガスを
所定量づつ添加して所定内圧を有するガス封入缶
詰を製造する方法に関する。 (従来の技術) ビールや炭酸飲料の缶詰に於ては、内容液中に
大量に含有されている炭酸ガスの一部が缶内のヘ
ツドスペース部分に放出されるので、缶内圧が大
気圧よりも高くなり、その結果、薄い胴壁をもつ
缶が支障なく使用されている。 一方、殆ど炭酸ガスを含有していない内容物、
例えば、果汁飲料、果物のシロツプ漬け、果粒入
りみかん飲料、コーヒー飲料、紅茶飲料、清酒等
の缶詰の場合は、缶内圧が大気圧以下になる(加
熱充填法で製造した場合は、常温時には大気圧よ
りもかなり低くなる。)ので、外力によつてへこ
みが生じないような厚い胴壁をもつ缶を使用する
必要があつた。 ところが、最近、このような内容物であつて
も、薄い胴壁をもつ缶を使用するために、缶に内
容物を充填した後であつて、缶の開口部を缶蓋で
密封する直前に、窒素ガスやアルゴンガス等の不
活性ガスを液化状態(低温液化ガス)で缶内容物
上に所定量添加することが提案されている。 即ち、缶内容物上に添加された低温液化ガスは
極く短時間のうちに気化するので、缶内に封入さ
れる量を所定量(缶の容積、内容物充填量、内容
物の温度等によつて決まる。)以上にすると密封
後の缶内圧が大気圧よりも大となり、この缶内圧
が缶胴壁を内側から支持するので、薄い胴壁をも
つ缶を使用しても外力によるへこみが生じ難くな
るからである。 この目的を達成するための方法と装置の一例が
特開昭56−109996号公報に開示されている。 ここに記載されている不活性液化ガス定量滴下
装置は滴下用不活性液化ガスと断熱用不活性液化
ガスと断熱用真空雰囲気とをそれぞれ密封内容と
する中心槽とその外周を順次囲繞する中間層と外
槽とにより内部を三重構造に形成した密封タンク
を設け、中心槽の底端には弁座口と弁体と弁棒と
を具備する滴下用液化ガス路開閉弁機構を設け、
この弁棒を中心槽を貫通して密封タンク外上端に
取付けた操作機構と結合し、また中心槽には、中
心槽内の滴下用液化ガスの液面を一定に制御する
ための液面センサーと電磁弁付き液化ガス供給管
とが挿入又は連通されていると共に中心槽内の圧
力を一定に制御するための気化ガス排気管と加圧
窒素ガス供給管と圧力計とが連通又は取付けられ
ている。 この不活性液化ガス定量滴下装置では、中心槽
の周囲に設けられている断熱用不活性液化ガスの
中間槽と断熱用真空雰囲気の外槽との存在によ
り、外気からの熱影響による中心槽内の滴下用不
活性液化ガスの気化が抑制され、また二つの制御
機構により、中心槽の滴下用不活性液化ガスの液
面と内圧とが一定に維持されており、しかも搬送
されてきた缶が中心槽の直下を通過する直前に検
知した缶検知信号により操作機構が作動して弁棒
と弁体とを上昇させて所定時間弁座口を開口する
ので、弁座口の下を通過する缶毎にほぼ一定量の
不活性液化ガスが滴下されることになる。 又、特開昭56−4521号公報の第4頁左上欄第6
〜8行には、液体窒素滴下装置の開閉弁を常時開
放状態にして液体窒素を常時滴下させておき、こ
の下を通過する缶の移動速度を一定にすることに
よつて、一缶毎の滴下量をほぼ同一にするという
液体窒素の滴下法も記載されている。 (解決すべき問題点) 缶詰の製造コストを低減させるためには缶詰製
造ラインの速度(即ち、缶内容物の充填速度、缶
蓋巻締速度、缶の移動速度等)を高速化するのが
望ましいが、特開昭56−109996号公報に開示され
ている不活性液化ガス滴下装置は、その下を缶が
通過する毎に弁体を上下動させる(缶が弁座口の
下を通過する直前に弁体を上昇させて弁座口を解
放し、通過し終わる直前に弁体を下降させて弁座
口を閉鎖し、次の缶が弁座口の下を通過する直前
にまた弁体を上昇させて弁座口を解放し、通過し
終わる直前に弁体を下降させてまた弁座口を閉鎖
するという作動をさせる。)ので、缶詰製造ライ
ンの速度が500缶/分以上の高速になると、弁座
口の開閉が缶詰製造ラインの速度(以下ライン速
度と呼ぶことがある)に追随できなくなつて、使
用が不可能となる欠点があつた。 一方、特開昭56−4521号公報に開示されている
液体窒素の滴下法は、常時弁座口を開放状態にし
ておくのであるから、弁座口の径を大きくして常
時一定量(一定時間当たり)の液体窒素が流下し
続けるように改良することにより500缶/分以上
の高速缶詰製造ライン(以下高速ラインと呼ぶこ
とがある)にも一応対応可能となるが、以下のよ
うな欠点があるので、事実上高速ラィンには使用
できない。 即ち、缶詰製造に使用する缶蓋巻締機のうち、
その巻締能力(巻締速度)が約500缶/分(250ml
缶換算)以上のものは、運転開始後すぐには能力
一杯(高速運転)が不可能なので、運転開始後の
一定時間(30分内外)は低速運転をし(充填速
度、缶の移動速度も低速)、その後、高速運転
(低速運転時の約2倍の速度にするのが一般的で
ある)に移行するという運転方法(ライン速度を
途中で変える)が従来から採用されている。 又、高速運転に移行した後であつても、缶内に
充填する内容液等の調合に手間取つて高速充填で
は供給が間に合わなくなつた場合とか、製造した
缶詰を箱に詰めるケーサーがトラブルを起こした
場合等のように、缶詰製造ラインの速度を低速運
転に切り換えた方が缶詰製造ライン稼動上から都
合が良い場合がある。 このように、途中でライン速度の変わる缶詰製
造ラインに、もし、特開昭56−4521号公報に開示
されている液体窒素滴下装置を組み込んだ場合、
この装置の一定時間当たりの液体窒素流下量は変
わらないから、缶の移動速度が途中から上がる
と、缶内に添加される液体窒素の量が途中から減
少してしまう結果となり(即ち、缶内に添加され
る液体窒素の量は、流下し続けている液体窒素流
の横断面積とこの液体窒素流を缶の開口部が横切
る時間との積であるから、液体窒素流を缶の開口
部が横切る時間が短くすると、換言すると、缶の
移動速度が上がると、缶内に添加される液体窒素
の量は減少する。例えば、缶の移動速度が2倍に
なると、缶内に添加される液体窒素の量は1/2に
なる。)、不良品が大量に発生することになるか
ら、特開昭56−4521号公報に開示の装置は、高速
ラインでの使用が事実上不可能となるのである。 (問題を解決する手段) 上記欠点を解消するために、本発明では低温液
化ガスを流下させる吐出孔を3個以上設けたノズ
ル部を備えた低温液化ガス流下装置を用い、缶詰
製造ラインを低速運転しているときは一部の吐出
孔(2個以上)からだけ低温液化ガスを流下さ
せ、缶詰製造ラインを高速運転しているときは全
部の吐出孔から低温液化ガスを流下させる。 即ち、内容液入りの缶を次々と搬送することに
より、先ず、該缶を、低温液化ガスが連続的に流
下している低温液化ガス流下装置の吐出孔の下を
通過させて各缶内に所定量の低温液化ガスを受け
取り、次に該缶を缶蓋巻締機に送り込んで該缶を
缶蓋で密封することによりガス封入缶詰を製造す
る方法に於て、 該低温液化ガス流下装置として、3個以上の吐
出孔とこれらの吐出孔を開閉する複数個の弁体と
を有するノズル部を備えたものを用い、 該缶の搬送を、比較的低速の第1の速度で行つ
ているときは、該複数個の弁体のうちの一部の弁
体だけを開放状態にして該3個以上の吐出孔のう
ちの2個以上の吐出孔からだけ低温液化ガスを流
下させ、 該缶の搬送を、第1の速度よりも高速の第2の
速度で行つているときは、該複数個の弁体の全部
を開放状態にして、該3個以上の吐出孔の全部か
ら低温液化ガスを流下させる ことを特徴とするガス封入缶詰の製造方法であ
る。 (作用) 本発明では、缶詰製造ラインを低速運転してい
るとき(即ち、缶の移動速度が遅いとき。)には、
一部の弁体だけを開放にして一部の吐出孔からだ
け低温液化ガスを流下させ、缶詰製造ラインを高
速運転しているとき(即ち缶の移動速度が速いと
き。)には、全部の弁体を開放にして全部の吐出
孔から低温液化ガスを流下させることにより缶が
吐出孔の下を通過する時間が比較的長い場合に
は、単位時間当たりの低温液化ガス流下量を少な
くし、一方、缶が吐出孔の下を通過する時間が短
い場合には、単位時間当たりの低温液化ガス流下
量を多くさせたので、缶の移動速度が変化しても
各缶が受け取る低温液化ガスの量は実質的に変化
しない。 従つて、ガス封入缶詰製造ラインの速度を変え
る前と後で製造したガス封入缶詰の缶内圧をほぼ
等しくさせることができる。 そして、単位時間当たりの低温液化ガス流下量
を増減する手段が、缶の移動速度を速くしたとき
には、吐出孔の一部を閉鎖していた弁体を開放に
して全部の弁体を開放状態にし、一方、缶の移動
速度を遅くしたときには、一部の弁体を閉鎖にす
るだけなので、操作に熟練を必要とせず、簡単且
つ迅速に操作ができる。 (実施例) 本発明の一実施例を低温液化ガス流下装置の要
部を示す第1〜5図を参照して説明する。 第1〜2図は本発明方法を実施している低温液
化ガス流下装置の要部縦断面図であつて、第1図
は缶詰製造ラインの速度が低速のとき(即ち、缶
の移動速度が遅いとき。)のノズル部の状態を示
し、第2図は缶詰製造ラインの速度が速いときの
ノズル部の状態を示す。 第3〜5図は、吐出孔の配置例を示すノズルの
底面図である。 尚、図中の矢印は、缶の移動方向を示す。1は
二重壁により断熱構造とした低温液化ガス貯溜タ
ンクで、この内壁2と外壁3との間は真空にして
ある。4は貯溜タンク1の底部に形成した低温液
化ガス12を吐出流下させるためのノズルで、5
はノズル4に設けた吐出孔(本実施例では別体と
した2個のノズル4,4にそれぞれ同一径の3個
の吐出孔5,5,5を一列に設けた例を示す)で
ある。 6は既に内容液の充填されている缶であり、7
は一定速度で移動する無端チエイン(図示せず)
に等間隔で取付けられており、缶の胴部を後方か
ら押して缶を定速搬送するための爪である。 8は移動する缶の進行方向と直交する方向の動
きを規制するためのガイドレールで、9は缶が滑
り移動するためのテーブルである。 10はノズル4の吐出孔5を開閉するための弁
体で、11は弁体10を上下動させるためのピス
トンロツドである(本実施例では、別体としたノ
ズル4,4のそれぞれに各1個ずつ弁体10を設
けてある)。 ここで、各ノズル4,4の吐出孔5,5…5の
各々と、搬送される缶6との関係を、本実施例の
様に吐出孔5,5…5が一列に並んでいる場合に
は、その各々が、搬送される缶6の開口部の中心
を通るようにする(即ち、開口部の横断面が円形
の缶であれば、缶の進行方向と平行な直径線と、
吐出孔5,5…5の列とがほぼ一致するようにす
る)のが、流下させる低温液化ガス12のロスを
少なくするという観点及び密封後の各缶毎の内圧
のバラツキを少なくするという観点から望まし
い。 尚、貯溜タンク1内の低温液化ガス12の液面
は大気圧となつており、又、液面高さは、図示し
ていない液面制御センサーと、低温液化ガス供給
管に取付けられている電磁弁によつてほぼ一定に
保たれているので、開放している吐出孔5の数を
変えない限り、一定時間内に於ける吐出孔5から
の低温液化ガス吐出総量は、常にほぼ一定とな
る。 この装置を用い、開放中の吐出孔の数を変えな
い限り、低温液化ガスの単位時間当たりの流下量
(ml/S)は、常にほぼ一定となるので、連続的
に低温液化ガスを吐出しているノズルの下方を、
上部開口缶が一定速度で移動するようにすると、
各缶内に一定量の低温液化ガスが添加されること
になる。 そして、低温液化ガスが添加された缶は、直ち
に密封されて液化ガスの気化による散逸の防止と
缶内の一定圧の保持が図られる。 さて、前述したように、本実施例の装置では2
個のノズル4,4のそれぞれに同一径の吐出孔5
を3個ずつ設けてあるので、両方のノズル4,4
の弁体10,10を開放にして6個の吐出孔5,
5…5から低温液化ガス12を流下させる場合
(第2図参照)の単位時間当りの低温液化ガス流
下量(ml/S)は、一方のノズル4の弁体10だ
けを開放して3個の吐出孔5,5,5からだけ低
温液化ガス12を流下させる場合(第1図参照)
の単位時間当りの低温液化ガス流下量の2倍とな
る。そこで、缶詰製造ラインの速度(缶内容物の
充填速度、缶の移動速度、缶蓋巻締速度)が低速
のときと高速のときとの速度比を1:2になるよ
うに設定しておき、缶詰製造ラインを低速運転し
ている(即ち、缶の移動速度が遅く、吐出孔の下
を通過する時間が比較的長い)ときは、一方のノ
ズル4の吐出孔5,5,5を弁体10で閉鎖して
おき1個のノズル4の3個の吐出孔5,5,5か
らだけ低温液化ガスを流下させ、一方、缶詰製造
ラインを高速運転している(缶の移動速度が低速
運転時の2倍となる)ときは、両方のノズル4,
4の弁体10,10を開放して6個の吐出孔5,
5…5から低温液化ガスを流下させると、結局ど
ちらの場合にも缶6への低温液化ガス添加量は同
じとなる。 従つて、ライン速度が低速のときに製造した缶
詰の内圧とライン速度が高速のときに製造した缶
詰の内圧とはほぼ等しくなるので、運転の途中で
ライン速度の変わる高速缶詰製造ラインに低温液
化ガス流下装置を導入して所定圧のガス封入缶詰
を製造することができる。 又、ライン速度が低速から高速に変わるとき、
又は、その逆のときの低温液化ガス流下装置の操
作としては、吐出孔を完全に閉鎖中の一方の弁体
を上昇させて全吐出孔を開放状態にするか又は一
方の弁体を下降させて一部の吐出孔を完全に閉鎖
状態にするだけ(微調整の必要がない)なので、
例えば、その変化時に、作業者が弁体操作ボタン
を押すか又は弁体操作装置と缶の搬送装置等の速
度計等とを連動させておく(高速運転時には、両
方の弁体が上昇位置を維持し、低速運転時には一
方の弁体が上昇位置、他方の弁体が下降位置をそ
れぞれ維持するように設定しておく)だけで良
く、その操作は極めて簡単且つ容易である。 尚、本実施例では、2個のノズル4,4の吐出
孔5として、各3個ずつの例を示したが、もつと
数を増した方が望ましく、その場合第3〜5図に
示すように、缶の進行方向と平行に吐出孔列を1
列、2列、3列と配置するのが各缶毎の缶内圧の
バラツキを少なくすると共に低温液化ガスのロス
を少なくするという観点から最も望ましい。 又、上記実施例では2個のノズルのそれぞれに
同一径で同一個数の吐出孔を設けたが、各ノズル
毎に吐出孔の径や個数を変えても、又、同一ノズ
ル内に径の異なる吐出孔を設けても良い。しか
し、各ノズルの吐出孔の径や個数の比率は缶詰製
造ラインの低速時と高速時の速度比によつて変え
ねばならないことは言うまでもない。 又、上記実施例では、ノズル部が2個のノズル
と2個の弁体とから構成されているものを用いた
が、例えば、1個のノズル(勿論、複数個の吐出
孔を備えている)と2個以上の弁体とから構成さ
れるノズル部、又は3個以上のノズルと3個以上
の弁体とから構成されるノズル部を使用しても良
いことは言うまでもない。 尚、本発明で使用するノズル部に設ける吐出孔
の数は、低速運転時であつてもガス封入缶詰の缶
内圧の各缶毎のバラツキを少なくするためには2
個以上の吐出孔から低温液化ガスを流下させるこ
とが好ましいので、少なくとも3個必要である
(ガス封入缶詰を製造する場合に、2個以上の吐
出孔から低温液化ガスを流下させる方が、1個の
吐出孔から同一量の低温液化ガスを流下させる場
合に比べて、できた缶詰の缶内圧のバラツキが少
なくなることが本発明者等の研究の結果、判明し
ている。特願昭57−66318号参照)。 次に、本発明方法の実験例を説明する。 この実験には径が約52.6mm(所謂202径)で、
高さが132mm、内容積が250mlと呼称されるブリキ
製DI缶を使用した。 このDI缶に、低速運転時は450缶/分、高速運
転時は900缶/分の速度で、95℃の水を240g
(240g±1g)充填した後、この缶を低速運転時
には、後記条件で2個ずつ設けたノズルのうちの
一方のノズルの弁体だけを上昇させて1個のノズ
ルの吐出孔だけを開放状態にし、又、高速運転時
には、両方のノズルの弁体を上昇させて2個のノ
ズルの吐出孔全部を開放状態にしてこれら吐出孔
から液体窒素を流下させ、この液体窒素流下装置
のノズルの吐出孔の下方をそれぞれの速度で通過
させて液体窒素を添加した後、直ちに缶蓋巻締機
により缶蓋を巻締めて密封した。 実験条件 *ノズル下面と缶フランジ上端との間隔(垂直距
離);約5mm *液体窒素貯溜タンク内の液面高さ;約110mm *ノズルの各吐出孔の数、直径、吐出孔間のピツ
チ(吐出孔の中心間距離):流下装置Aは2個
のノズルのそれぞれに5個、0.8mm、2.5mm、流
下装置Bは2個のノズルのそれぞれに8個、
0.6mm、2.5mm 尚、流下装置Aの2個の各ノズルの吐出孔
は、5個を一列に、また流下装置Bの2個の各
ノズルの吐出孔は4個ずつ2列にそれぞれ設け
ると共に、これらの列と進行方向に平行な缶の
開口部の直径線とがほぼ一致するか又は平行に
なるようにした(流下装置Aは、ノズルを交換
することによつて流下装置Bとすることができ
るのは勿論のことである)。 *液体窒素添加から缶蓋巻締までに要する時間;
低速運転時1.8秒、高速運転時0.9秒 窒素ガス封入缶詰製造に先立つて、各流下装
置A,Bの1個のノズルの吐出孔だけを開放状
態にした場合(低速運転時用)と2個のノズル
の吐出孔を開放状態にした場合(高速運転時
用)の1秒間当たりの液体窒素吐出量を測定し
た。 その結果を第1表に示す。
(Industrial Application Field) The present invention relates to a method for producing gas-filled canned goods by adding a predetermined amount of inert gas to give internal pressure to the canned can in a low-temperature liquefied state immediately before sealing. In a high-speed can production line where the speed of the can production line changes midway through, a predetermined amount of low-temperature liquefied gas is added into the can while it is being moved to the can lid tightening machine after being filled with contents to maintain a predetermined internal pressure. The present invention relates to a method of manufacturing a gas-filled canned food. (Prior art) In cans of beer and carbonated drinks, a portion of the carbon dioxide gas contained in large quantities in the liquid content is released into the head space inside the can, causing the internal pressure to rise below atmospheric pressure. As a result, cans with thin barrel walls can be used without problems. On the other hand, contents that contain almost no carbon dioxide,
For example, in the case of canned fruit juice drinks, fruits pickled in syrup, mandarin orange drinks containing fruit particles, coffee drinks, tea drinks, sake, etc., the internal pressure is below atmospheric pressure (if manufactured by the hot filling method, at room temperature (The pressure is much lower than atmospheric pressure.) Therefore, it was necessary to use cans with thick walls that would not dent due to external forces. However, in recent years, even with such contents, cans with thin body walls have been used. It has been proposed to add a predetermined amount of an inert gas such as nitrogen gas or argon gas to the contents of the can in a liquefied state (low-temperature liquefied gas). In other words, since the low-temperature liquefied gas added to the contents of the can vaporizes in a very short time, the amount sealed in the can can be controlled by a predetermined amount (the volume of the can, the amount of contents filled, the temperature of the contents, etc.). (Determined by the above.) With this, the internal pressure of the can after sealing becomes higher than atmospheric pressure, and this internal pressure supports the can body wall from the inside, so even if a can with a thin body wall is used, it will not dent due to external force. This is because it becomes less likely to occur. An example of a method and apparatus for achieving this objective is disclosed in Japanese Patent Application Laid-open No. 109996/1983. The inert liquefied gas quantitative dropping device described here includes a central tank in which an inert liquefied gas for dropping, an inert liquefied gas for insulation, and a vacuum atmosphere for insulation are each sealed, and an intermediate layer that sequentially surrounds the outer periphery of the central tank. A sealed tank is provided with a triple-layered internal structure formed by an outer tank and an outer tank, and a dripping liquefied gas passage opening/closing valve mechanism is provided at the bottom end of the center tank, which includes a valve seat opening, a valve body, and a valve stem.
This valve stem is connected to an operating mechanism that passes through the central tank and is attached to the outer upper end of the sealed tank, and a liquid level sensor is installed in the central tank to control the liquid level of the dripping liquefied gas in the central tank at a constant level. and a liquefied gas supply pipe with a solenoid valve are inserted or communicated with each other, and a vaporized gas exhaust pipe, a pressurized nitrogen gas supply pipe, and a pressure gauge for controlling the pressure in the central tank are communicated with or attached. There is. In this inert liquefied gas quantitative dripping device, due to the existence of an intermediate tank of inert liquefied gas for heat insulation and an outer tank with a vacuum atmosphere for heat insulation, which are provided around the center tank, the inside of the center tank is affected by heat from the outside air. The vaporization of the inert liquefied gas for dripping is suppressed, and the liquid level and internal pressure of the inert liquefied gas for dripping in the central tank are maintained constant by two control mechanisms. The operating mechanism is actuated by the can detection signal detected just before the can passes directly under the central tank, raises the valve stem and valve body, and opens the valve seat opening for a predetermined period of time. A substantially constant amount of inert liquefied gas is dropped each time. Also, No. 6 in the upper left column of page 4 of JP-A No. 56-4521.
Lines 8 to 8 show that by keeping the on-off valve of the liquid nitrogen dripping device open and constantly dripping liquid nitrogen, and by keeping the moving speed of the cans passing below constant, A method of dropping liquid nitrogen is also described in which the amount of drops is almost the same. (Problems to be solved) In order to reduce the manufacturing cost of canned goods, it is necessary to increase the speed of the canned manufacturing line (i.e., the filling speed of can contents, the speed of tightening can lids, the moving speed of cans, etc.). Desirably, the inert liquefied gas dripping device disclosed in JP-A-56-109996 moves the valve body up and down every time a can passes under it (as the can passes under the valve seat opening). Just before the can passes, the valve element is raised to release the valve seat opening, and just before the can is finished passing, the valve element is lowered to close the valve seat opening, and just before the next can passes under the valve seat opening, the valve element is opened again. (The valve element is lowered just before it finishes passing, and the valve seat opening is closed again.) Therefore, the canning production line is operated at a high speed of 500 cans/min or more. In this case, the opening and closing of the valve seat opening could no longer follow the speed of the can manufacturing line (hereinafter sometimes referred to as line speed), making it impossible to use. On the other hand, in the liquid nitrogen dropping method disclosed in JP-A No. 56-4521, the valve seat opening is always kept open, so the diameter of the valve seat opening is enlarged so that a constant amount (constant By improving the flow of liquid nitrogen so that the amount of liquid nitrogen (per hour) continues to flow down, it becomes possible to handle high-speed canning production lines (hereinafter sometimes referred to as high-speed lines) that can produce more than 500 cans per minute, but it has the following drawbacks: Therefore, it cannot be used for high-speed lines. In other words, among the can lid tightening machines used for can manufacturing,
Its seaming capacity (sealing speed) is approximately 500 cans/min (250ml).
Since it is impossible to operate at full capacity (high-speed operation) immediately after starting operation, it is necessary to operate at low speed for a certain period of time (around 30 minutes) after starting operation (filling speed, can movement speed, etc.). Conventionally, an operating method (the line speed is changed midway) has been adopted in which the line speed is changed at a low speed) and then a high speed operation (generally, the speed is approximately twice that of the low speed operation). In addition, even after shifting to high-speed operation, there may be cases where high-speed filling is unable to supply the liquid in time due to the time it takes to mix the liquid content to be filled into the cans, or there is a problem with the caser that packs manufactured canned goods into boxes. In some cases, such as when an emergency occurs, it may be more convenient to switch the speed of the can manufacturing line to low speed operation from the viewpoint of operating the can manufacturing line. If the liquid nitrogen dripping device disclosed in JP-A-56-4521 is installed in a can manufacturing line where the line speed changes midway,
Since the amount of liquid nitrogen flowing down per certain period of time in this device does not change, if the moving speed of the can increases midway, the amount of liquid nitrogen added into the can will decrease midway (i.e., the amount of liquid nitrogen added into the can will decrease). The amount of liquid nitrogen added to the can opening is the product of the cross-sectional area of the continuing falling liquid nitrogen stream and the time it takes the can opening to cross this liquid nitrogen stream. As the traversal time decreases, in other words as the speed of can movement increases, the amount of liquid nitrogen added into the can decreases.For example, if the speed of movement of the can doubles, the amount of liquid added into the can decreases. (The amount of nitrogen is reduced to 1/2.), resulting in a large number of defective products, making it virtually impossible to use the device disclosed in JP-A-56-4521 on high-speed lines. It is. (Means for Solving the Problem) In order to eliminate the above-mentioned drawbacks, the present invention uses a low-temperature liquefied gas flow-down device equipped with a nozzle section provided with three or more discharge holes through which low-temperature liquefied gas flows down, and a can manufacturing line is operated at a low speed. When the line is in operation, the low temperature liquefied gas is allowed to flow down only from some of the discharge holes (two or more), and when the can manufacturing line is being operated at high speed, the low temperature liquefied gas is allowed to flow down from all the discharge holes. That is, by conveying cans containing liquid one after another, the cans are first passed under the discharge hole of a low-temperature liquefied gas flow device through which low-temperature liquefied gas is continuously flowing down, and into each can. In a method for manufacturing gas-filled canned goods by receiving a predetermined amount of low-temperature liquefied gas, then sending the can to a can lid sealing machine and sealing the can with a can lid, as the low-temperature liquefied gas flowing device. , a nozzle portion having three or more discharge holes and a plurality of valve bodies for opening and closing these discharge holes, and conveying the can at a relatively low first speed. In this case, only some of the plurality of valve bodies are opened to allow the low temperature liquefied gas to flow down only from two or more discharge holes among the three or more discharge holes; When the gas is being transported at a second speed that is higher than the first speed, all of the plurality of valve bodies are opened, and the low temperature liquefied gas is discharged from all of the three or more discharge holes. This is a method for producing gas-filled canned goods, which is characterized by causing gas-filled cans to flow down. (Function) In the present invention, when the can manufacturing line is operated at low speed (that is, when the can movement speed is slow),
When only some of the valve bodies are opened and low-temperature liquefied gas flows down only from some discharge holes, when the can manufacturing line is operated at high speed (i.e., when the cans are moving quickly), all of the If the valve body is opened and the low-temperature liquefied gas flows down from all the discharge holes, and the time it takes for the can to pass under the discharge holes is relatively long, the amount of low-temperature liquefied gas flowing down per unit time is reduced, On the other hand, when the time for the cans to pass under the discharge hole is short, the amount of low-temperature liquefied gas flowing down per unit time is increased, so even if the moving speed of the cans changes, the amount of low-temperature liquefied gas received by each can increases. The amount remains virtually unchanged. Therefore, the internal pressures of the gas-filled cans manufactured before and after changing the speed of the gas-filled can can manufacturing line can be made approximately equal. When the means for increasing or decreasing the amount of low-temperature liquefied gas flowing down per unit time increases the moving speed of the can, the valve body that had closed part of the discharge hole is opened and all the valve bodies are opened. On the other hand, when the moving speed of the can is slowed down, only a part of the valve body is closed, so the operation does not require any skill and can be performed easily and quickly. (Embodiment) An embodiment of the present invention will be described with reference to FIGS. 1 to 5, which show the main parts of a low-temperature liquefied gas flow device. Figures 1 and 2 are longitudinal cross-sectional views of main parts of a low-temperature liquefied gas flow device implementing the method of the present invention. Fig. 2 shows the state of the nozzle part when the canning line is running at a high speed. 3 to 5 are bottom views of the nozzle showing examples of arrangement of discharge holes. Note that the arrow in the figure indicates the direction of movement of the can. Reference numeral 1 denotes a low temperature liquefied gas storage tank with a double-walled heat insulating structure, and a vacuum is created between the inner wall 2 and the outer wall 3. 4 is a nozzle for discharging and flowing down the low temperature liquefied gas 12 formed at the bottom of the storage tank 1;
is a discharge hole provided in the nozzle 4 (this example shows an example in which three discharge holes 5, 5, 5 of the same diameter are provided in a row in two separate nozzles 4, 4). . 6 is a can already filled with liquid; 7
is an endless chain moving at a constant speed (not shown)
These claws are attached at equal intervals to the cans and push the body of the can from behind to transport the can at a constant speed. Reference numeral 8 denotes a guide rail for regulating the movement of the moving can in a direction perpendicular to the traveling direction, and reference numeral 9 denotes a table on which the can slides. 10 is a valve body for opening and closing the discharge hole 5 of the nozzle 4, and 11 is a piston rod for moving the valve body 10 up and down (in this embodiment, a piston rod is provided for each of the separate nozzles 4, 4). (The valve bodies 10 are provided individually.) Here, the relationship between each of the discharge holes 5, 5...5 of each nozzle 4, 4 and the can 6 to be conveyed is shown in the case where the discharge holes 5, 5...5 are lined up in a line as in this embodiment. , each of them should pass through the center of the opening of the can 6 to be transported (i.e., if the cross section of the opening is circular, the diameter line parallel to the direction of travel of the can,
The rows of the discharge holes 5, 5...5 are made to almost coincide with each other from the viewpoint of reducing the loss of the low temperature liquefied gas 12 flowing down and from the viewpoint of reducing the variation in the internal pressure of each can after being sealed. desirable. The liquid level of the low-temperature liquefied gas 12 in the storage tank 1 is at atmospheric pressure, and the liquid level height is determined by a liquid level control sensor (not shown) and a low-temperature liquefied gas supply pipe installed. Since it is kept almost constant by the solenoid valve, the total amount of low-temperature liquefied gas discharged from the discharge holes 5 within a certain period of time will always be almost constant unless the number of open discharge holes 5 is changed. Become. Using this device, unless the number of open discharge holes is changed, the flow rate (ml/S) of low-temperature liquefied gas per unit time will always be approximately constant, so low-temperature liquefied gas can be continuously discharged. below the nozzle
If the top-opening can is made to move at a constant speed,
A certain amount of low temperature liquefied gas will be added into each can. The can into which the low-temperature liquefied gas has been added is immediately sealed to prevent the liquefied gas from evaporating and dissipating and to maintain a constant pressure inside the can. Now, as mentioned above, in the device of this embodiment, two
Discharge holes 5 of the same diameter in each of the nozzles 4, 4
There are three nozzles each, so both nozzles 4, 4
With the valve bodies 10, 10 open, the six discharge holes 5,
When the low-temperature liquefied gas 12 is caused to flow down from 5...5 (see Figure 2), the flow rate (ml/S) of low-temperature liquefied gas per unit time is 3 when only the valve body 10 of one nozzle 4 is opened. When the low temperature liquefied gas 12 is made to flow down only from the discharge holes 5, 5, 5 (see Fig. 1)
This is twice the flow rate of low temperature liquefied gas per unit time. Therefore, the speed ratio between low and high speeds of the can production line (filling speed of can contents, can movement speed, can lid tightening speed) is set to 1:2. When the can manufacturing line is operated at low speed (i.e., the moving speed of the can is slow and the time it takes to pass under the discharge hole is relatively long), the discharge holes 5, 5, 5 of one nozzle 4 are closed. The low temperature liquefied gas is allowed to flow down only from the three discharge holes 5, 5, 5 of one nozzle 4, which is closed by the body 10, while the can manufacturing line is operated at high speed (the moving speed of the cans is slow). (double the operating time), both nozzles 4,
4 valve bodies 10, 10 are opened to open the 6 discharge holes 5,
When low-temperature liquefied gas is allowed to flow down from 5...5, the amount of low-temperature liquefied gas added to can 6 becomes the same in both cases. Therefore, the internal pressure of canned goods manufactured when the line speed is low is almost equal to the internal pressure of canned goods manufactured when the line speed is high, so low-temperature liquefaction is applied to a high-speed canning manufacturing line where the line speed changes midway through operation. A gas-filled can can be manufactured at a predetermined pressure by introducing a gas flow device. Also, when the line speed changes from low to high speed,
Or, to operate the low-temperature liquefied gas flow device in the opposite case, one valve element whose discharge holes are completely closed can be raised to open all the discharge holes, or one valve element can be lowered. All you have to do is close some of the discharge holes completely (no need for fine adjustment).
For example, when the temperature changes, the operator should press the valve body operating button, or the valve body operating device should be linked with a speedometer, etc. of the can conveyor (during high-speed operation, both valve bodies should be in the raised position). The operation is extremely simple and easy, and the operation is extremely simple and easy. In this embodiment, the two nozzles 4, 4 each have three discharge holes 5, but it is preferable to increase the number of discharge holes 5, as shown in FIGS. 3 to 5. In this way, one row of discharge holes is arranged parallel to the direction of travel of the can.
It is most desirable to arrange them in one row, two rows, or three rows from the viewpoint of reducing variations in the internal pressure of each can and reducing the loss of low-temperature liquefied gas. In addition, in the above embodiment, each of the two nozzles has the same diameter and the same number of discharge holes, but even if the diameter and number of discharge holes are changed for each nozzle, A discharge hole may also be provided. However, it goes without saying that the diameter and number ratio of the discharge holes of each nozzle must be changed depending on the speed ratio between low speed and high speed of the can manufacturing line. In addition, in the above embodiment, the nozzle part is composed of two nozzles and two valve bodies, but for example, it is possible to use a nozzle part composed of two nozzles (of course, a plurality of discharge holes). ) and two or more valve bodies, or a nozzle part composed of three or more nozzles and three or more valve bodies may of course be used. In addition, the number of discharge holes provided in the nozzle used in the present invention is set to 2 in order to reduce the variation in the internal pressure of gas-filled cans from one can to another even during low-speed operation.
It is preferable to let the low-temperature liquefied gas flow down from two or more discharge holes, so at least three are required. As a result of research by the present inventors, it has been found that the variation in the internal pressure of canned cans is reduced compared to when the same amount of low-temperature liquefied gas is allowed to flow down from each discharge hole. -Refer to No. 66318). Next, an experimental example of the method of the present invention will be explained. For this experiment, the diameter was approximately 52.6 mm (so-called 202 diameter),
A tin DI can with a height of 132 mm and an internal volume of 250 ml was used. Add 240 g of 95°C water to this DI can at a rate of 450 cans/min during low-speed operation and 900 cans/min during high-speed operation.
(240g±1g) When this can is operated at low speed after filling, only the valve body of one of the two nozzles is raised under the conditions described below, leaving only the discharge hole of one nozzle open. In addition, during high-speed operation, the valve bodies of both nozzles are raised to open all the discharge holes of the two nozzles, and liquid nitrogen flows down from these discharge holes, thereby reducing the discharge of liquid nitrogen from the nozzles of this liquid nitrogen flow device. After liquid nitrogen was added by passing through the holes at different speeds, the can lid was immediately tightened and sealed using a can lid tightening machine. Experimental conditions * Distance (vertical distance) between the bottom surface of the nozzle and the top of the can flange; approximately 5 mm * Liquid level height in the liquid nitrogen storage tank; approximately 110 mm * The number, diameter, and pitch between the discharge holes of each nozzle ( Distance between centers of discharge holes): Flow device A has 5 pieces on each of the two nozzles, 0.8 mm, 2.5 mm, Flow device B has 8 pieces on each of the two nozzles,
0.6mm, 2.5mm In addition, the discharge holes of each of the two nozzles of the flow-down device A are arranged in a row of five, and the discharge holes of each of the two nozzles of the flow-down device B are arranged in two rows of four. , these rows and the diameter line of the opening of the can parallel to the direction of travel were made to almost match or be parallel (the flow down device A could be changed to the flow down device B by replacing the nozzle). (Of course, it is possible to do so.) *Time required from adding liquid nitrogen to tightening the can lid;
1.8 seconds at low speed operation, 0.9 seconds at high speed operation When only one nozzle discharge hole of each flow device A and B is opened (for low speed operation) and two The amount of liquid nitrogen discharged per second was measured when the discharge hole of the nozzle was opened (for high-speed operation). The results are shown in Table 1.

【表】 次に、上記条件にしたがい、運転途中で内容液
の充填速度(缶の移動速度、缶蓋巻締速度)を変
える(450缶/分→900缶/分)と共に液体窒素貯
溜タンクからの液体窒素の吐出量を変え(2.56
ml/S→5.17ml/S、2.58ml/S→5.11ml/S)
て、窒素ガス封入缶詰を製造し、室温まで冷却し
た後、それぞれの条件で製造した缶詰の缶内圧を
25缶ずつ測定した。 その結果を第2表に示す。
[Table] Next, according to the above conditions, the filling speed of the liquid contents (can movement speed, can lid tightening speed) was changed (from 450 cans/min to 900 cans/min) during operation, and the liquid nitrogen was removed from the liquid nitrogen storage tank. Change the discharge amount of liquid nitrogen (2.56
ml/S→5.17ml/S, 2.58ml/S→5.11ml/S)
After manufacturing canned goods filled with nitrogen gas and cooling them to room temperature, the internal pressure of the canned goods manufactured under each condition was measured.
25 cans each were measured. The results are shown in Table 2.

【表】 第2表から明らかなように、充填速度(缶の移
動速度、缶蓋巻締速度)を450缶/分から900缶/
分に変えても、変える前に製造した窒素ガス封入
缶詰の缶内圧と、変えた後に製造した窒素ガス封
入缶詰の缶内圧とはほとんど変わりがなく、しか
も缶内圧のバラツキもほとんど変わりがない。 (発明の効果) 上述したように、本発明方法では途中で缶詰製
造ラインの速度が変化しても、製造されたガス封
入缶詰の缶内圧がほとんど変わらないので、途中
で缶詰製造ラインの速度が変化する高速缶詰製造
ラインを使用して効率良く、従つて、低コストで
ガス封入缶詰を製造することができる。 そして、ライン速度が変化するときに行う操作
も極めて簡単である。
[Table] As is clear from Table 2, the filling speed (can movement speed, can lid tightening speed) is 450 cans/900 cans/
Even if the amount is changed to 10 minutes, there is almost no difference between the internal pressure of the nitrogen gas-filled canned goods manufactured before the change and the canned pressure of the nitrogen gas-filled canned goods manufactured after the change, and there is also almost no difference in the variation in the can internal pressure. (Effects of the Invention) As described above, in the method of the present invention, even if the speed of the can manufacturing line changes during the process, the internal pressure of the manufactured gas-filled cans hardly changes. Gas filled cans can be manufactured efficiently and therefore at low cost using a variable high speed canning line. Moreover, the operations performed when the line speed changes are also extremely simple.

【図面の簡単な説明】[Brief explanation of drawings]

第1〜2図は本発明方法を実施している低温液
化ガス流下装置の要部縦断面図であつて、第1図
は缶詰製造ラインの速度が低速のときのノズル部
の状態を示し、第2図は缶詰製造ラインの速度が
高速のときのノズル部の状態を示す。第3〜5図
は本発明方法を実施するのに好適な吐出孔の配置
例を示すノズルの底面図である。 4……ノズル、5……吐出孔、6……缶、10
……弁体、12……低温液化ガス。
Figures 1 and 2 are longitudinal cross-sectional views of main parts of a low-temperature liquefied gas flow device implementing the method of the present invention, and Figure 1 shows the state of the nozzle section when the speed of the can manufacturing line is low; FIG. 2 shows the state of the nozzle section when the speed of the can manufacturing line is high. 3 to 5 are bottom views of nozzles showing examples of arrangement of discharge holes suitable for carrying out the method of the present invention. 4... Nozzle, 5... Discharge hole, 6... Can, 10
... Valve body, 12 ... Low temperature liquefied gas.

Claims (1)

【特許請求の範囲】 1 内容液入りの缶を次々と搬送することによ
り、先ず、該缶を、低温液化ガスが連続的に流下
している低温液化ガス流下装置の吐出孔の下を通
過させて各缶内に所定量の低温液化ガスを受け取
り、 次に、該缶を缶蓋巻締機に送り込んで該缶を缶
蓋で密封することによりガス封入缶詰を製造する
方法に於いて、 該低温液化ガス流下装置として、3個以上の吐
出孔とこれらの吐出孔を開閉する複数個の弁体と
を有するノズル部を備えたものを用い、 該缶の搬送を、比較的低速の第1の速度で行つ
ているときは、該複数個の弁体のうちの一部の弁
体だけを開放状態にして、該3個以上の吐出孔の
うちの2個以上の吐出孔からだけ低温液化ガスを
流下させ、 該缶の搬送を、第1の速度よりも高速の第2の
速度で行つているときは、該複数個の弁体の全部
を開放状態にして、該3個以上の吐出孔の全部か
ら低温液化ガスを流下させる ことを特徴とするガス封入缶詰の製造方法。
[Claims] 1. By conveying cans containing liquid one after another, the cans are first passed under the discharge hole of a low-temperature liquefied gas flow device through which low-temperature liquefied gas is continuously flowing down. A method for producing gas-filled canned goods by receiving a predetermined amount of low-temperature liquefied gas into each can, and then feeding the can into a can lid sealing machine and sealing the can with a can lid. The low-temperature liquefied gas flow down device is equipped with a nozzle section having three or more discharge holes and a plurality of valve bodies for opening and closing these discharge holes, and the conveyance of the can is carried out using a relatively low-speed first When the flow is carried out at a speed of When the gas is flowing down and the can is being transported at a second speed higher than the first speed, all of the plurality of valve bodies are opened and the three or more discharge A method for manufacturing a gas-filled canned food, characterized in that low-temperature liquefied gas is allowed to flow down from all of the holes.
JP62129729A 1987-05-28 1987-05-28 Production of gas-sealed canned food Granted JPS6352865A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62129729A JPS6352865A (en) 1987-05-28 1987-05-28 Production of gas-sealed canned food

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62129729A JPS6352865A (en) 1987-05-28 1987-05-28 Production of gas-sealed canned food

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP6631982A Division JPS58183419A (en) 1982-04-22 1982-04-22 Low-temperature liquefied gas discharge adding method

Publications (2)

Publication Number Publication Date
JPS6352865A JPS6352865A (en) 1988-03-07
JPH0121950B2 true JPH0121950B2 (en) 1989-04-24

Family

ID=15016755

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62129729A Granted JPS6352865A (en) 1987-05-28 1987-05-28 Production of gas-sealed canned food

Country Status (1)

Country Link
JP (1) JPS6352865A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2011025973A (en) * 2009-07-28 2011-02-10 Toyo Seikan Kaisha Ltd Method of manufacturing canned product
JP2023090547A (en) * 2021-12-17 2023-06-29 大和製罐株式会社 Canned powder, method and apparatus for producing canned powder

Also Published As

Publication number Publication date
JPS6352865A (en) 1988-03-07

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