JPS6350249B2 - - Google Patents

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Publication number
JPS6350249B2
JPS6350249B2 JP60274047A JP27404785A JPS6350249B2 JP S6350249 B2 JPS6350249 B2 JP S6350249B2 JP 60274047 A JP60274047 A JP 60274047A JP 27404785 A JP27404785 A JP 27404785A JP S6350249 B2 JPS6350249 B2 JP S6350249B2
Authority
JP
Japan
Prior art keywords
mixed gas
nitrogen gas
water vapor
head space
gas
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
JP60274047A
Other languages
Japanese (ja)
Other versions
JPS62135124A (en
Inventor
Yukio Okazawa
Yoshio Aoyama
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Toyo Seikan Group Holdings Ltd
Original Assignee
Toyo Seikan Kaisha Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Toyo Seikan Kaisha Ltd filed Critical Toyo Seikan Kaisha Ltd
Priority to JP27404785A priority Critical patent/JPS62135124A/en
Publication of JPS62135124A publication Critical patent/JPS62135124A/en
Publication of JPS6350249B2 publication Critical patent/JPS6350249B2/ja
Granted legal-status Critical Current

Links

Description

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

〔産業上の利用分野〕 本発明は缶詰の充填方法に関し、特に缶のヘツ
ドスペース内の残存酸素量を所望の値以下に押え
つつ所望の真空度を自由に得ることが可能な缶詰
の充填方法に関する。 〔従来の技術〕 従来缶詰内容物の酸化を防止するために缶のヘ
ツドスペース内の残存酸素量を所定量以下に押え
る方法として、熱間充填法またはスチームフロー
法によりヘツドスペースを高真空度に保つ方法が
一般に採用されている。また近年酸化防止のため
または薄肉缶を使用する場合缶の変形を防止する
ため、熱間充填法やスチームフロー法に代り窒素
ガスをヘツドスペース内に吹き込むことによりヘ
ツドスペース内の残存酸素量を減少させる窒素フ
ロー法も使用されている。 〔発明が解決すべき問題点〕 窒素ガスフロー法はヘツドスペースの残存酸素
量を減少させる方法として有効なものであるが、
ヘツドスペース内の空気を窒素ガスで置換するの
で比較的に低い真空度しか得られない。缶詰製造
装置は一般に缶のヘツドスペース内にある程度高
い真空度があることを前提として操作されるよう
に作られているので、ヘツドスペースの真空度が
低いと、たとえばレトルト殺菌の際にヘツドスペ
ース内の気体の熱膨張によるバツクリング(缶の
膨出変形)を生じたり、内容物の変敗による異常
膨張不良缶を打検により判別する際、異常膨張に
よる圧力増大を判別することができない等の不都
合が生じる。一方熱間充填法やスチームフロー法
では充分高い真空度をとることはできるが、残存
酸素量の減少には限度があり、酸素量を所望値以
下に押えることが困難である。 よつて、本発明は、上記問題点を解決し、ヘツ
ドスペース内の残存酸素量を所望値以下に押えつ
つ所望の真空度を得ることが可能な缶詰の充填方
法を提供することを目的とする。 〔問題点を解決する手段〕 本発明者らは、上記問題点を解決するため研究
と実験を重ねた結果、窒素ガスと水蒸気を適当な
比率で予め混合して窒素ガス―水蒸気混合ガスを
作り、缶の充填巻締めに際しこの混合ガスを缶の
ヘツドスペースに吹き込むと、ヘツドスペースの
真空度と残存酸素量はいずれも所望の範囲のもの
が得られることを見出し、本発明に到達した。 すなわち、上記目的を達成する本発明の方法
は、窒素ガスと水蒸気を所定の比率で予め混合し
て混合ガスを作り、内容物を缶に充填した後この
混合ガスを缶のヘツドスペース内に吹込み巻締め
るようにしたものである。 本発明の特徴は窒素ガスと水蒸気を缶のヘツド
スペース内に吹込む方法として、窒素ガスと水蒸
気を経時的またはライン上それぞれを別々に吹込
むのではなく、予め窒素ガスと水蒸気の混合装置
において所定の比率で混合して混合ガスを作つて
置き、この準備された混合ガスをアンダーカバー
ガツシング法によりヘツドスペース内に吹き込む
方法を用いたことである。経時的またはライン上
それぞれを別々に、たとえば最初水蒸気を吹込み
次のステツプで窒素ガスを吹込むようにすると、
窒素ガス吹込時に水蒸気が除去されてしまう。逆
に窒素ガスを吹込んだ後から水蒸気を吹込むとス
チームフローと同効果を呈することになり、ヘツ
ドスペース上の窒素ガスが除かれて製品缶詰は高
真空になるが、残存酸素量は必ずしも所望値以下
に押えることができない。本発明のように予め準
備した混合ガスを一気にヘツドスペース内に吹込
むことにより常に安定した混合比で窒素ガスと水
蒸気を供給することができる。 また本発明の方法は、窒素ガスと水蒸気を所定
の比率で予め混合して混合ガスを作り、この混合
ガスを大気中で加熱し、内容物を缶に充填した後
この加熱した混合ガスを缶のヘツドスペース内に
吹込み巻締めるようにしたものである。混合ガス
をヘツドスペース内に吹込む際混合ガス中の一部
は周囲温度に影響されて霧化し、この霧化された
部分はヘツドスペース内の空気に置換する効果が
ないので、その分残存酸素量の低減に有効に働か
ないが、混合ガスを大気中で加熱してからヘツド
スペース内に吹込むことにより、このような水蒸
気の霧化を防止することができ、混合ガスの残存
酸素量低減効果を一層高めることができる。混合
ガスを加熱するにはたとえば混合ガスをパイプに
通してこのパイプを100℃以上で加熱すればよい。 〔実施例〕 実施例 1 第1図に示す装置を使つてスチームフロー法、
窒素ガスフロー法および本発明にかかる窒素ガス
―水蒸気混合ガスフロー法によるヘツドスペース
の真空度および残存酸素量を測定した。第1図に
おいて、Aは窒素ガス―水蒸気混合装置で、中空
の匡体1の両側にはそれぞれ窒素ガス供給源(図
示せず)および水蒸気供給源(図示せず)に接続
された窒素ガス供給弁2と水蒸気供給弁3とが設
けられており、匡体1の内部には撹拌用の邪魔板
4,5が設けられている。6は水となつた水蒸気
を排出するためのドレイン排管である。窒素ガス
―水蒸気混合装置Aには連通管6を介して実験用
の疑似アンダーカバーガツシング装置Bが連結さ
れている。この装置Bも中空の匡体8からなり、
その一側には缶内容物を充填後巻締前の缶9が嵌
合する横断面半円形の凹所10が形成されてお
り、この凹所10の上部にはガス吹出口11が開
口している。12は水となつた水蒸気を排出する
ためのドレイン排管である。 上記の装置を用いて各種ガスフローを行うに
は、窒素ガス供給弁2と水蒸気供給弁3を開いて
窒素ガスN2と水蒸気Sのいずれか一方または双
方を装置Aの匡体1内に供給する。内容物を充填
後巻締前の缶9を装置Bの凹所10に嵌入静置す
る。匡体1内に供給されたガスは(混合ガスの場
合は撹拌混合された後)連通管7を介して装置B
の匡体8に入りガス吹出口11から缶9のヘツド
スペース内に吹込まれる。 本実験においては、上記の装置を使用し、また
各種ガスフローの対象物として、充填温度60℃、
80℃、90℃でそれぞれ水を充填した200g入りト
ーヨーシームネツクドイン缶を使用した。シーマ
ーとしてはセミトロシーマーを使用した。 上記装置による実験において、窒素ガスの流量
は0l/分、10l/分、25l/分の3通りとし、水蒸
気の流量については吹込口に吹込む蒸気の蒸気圧
を0.01Kg/cm2および0.02Kg/cm2としたとき前記3
通りの窒素ガス流量に対してそれぞれ流れる水蒸
気の流量を測つて水蒸気流量とした。その測定結
果は次表1のとおりである。
[Industrial Field of Application] The present invention relates to a method for filling canned goods, and in particular, a method for filling canned goods that can freely obtain a desired degree of vacuum while suppressing the amount of residual oxygen in the head space of a can to a desired value or less. Regarding. [Prior art] Conventionally, in order to prevent the contents of cans from oxidizing, the amount of residual oxygen in the head space of a can is kept below a predetermined amount by applying a hot filling method or steam flow method to the head space to a high degree of vacuum. This method is generally adopted. In recent years, in order to prevent oxidation or to prevent can deformation when using thin-walled cans, nitrogen gas has been blown into the headspace instead of the hot filling method or steam flow method to reduce the amount of residual oxygen in the headspace. Nitrogen flow methods have also been used. [Problems to be solved by the invention] Although the nitrogen gas flow method is effective as a method for reducing the amount of residual oxygen in the head space,
Since the air in the head space is replaced with nitrogen gas, only a relatively low degree of vacuum can be obtained. Canning manufacturing equipment is generally designed to operate on the assumption that there is a certain degree of vacuum in the can head space, so if the head space has a low vacuum, for example during retort sterilization, Inconveniences such as buckling (bulging deformation of the can) due to thermal expansion of the gas, or inability to detect pressure increase due to abnormal expansion when identifying cans with abnormal expansion due to deterioration of the contents. occurs. On the other hand, although a sufficiently high degree of vacuum can be obtained using the hot filling method or the steam flow method, there is a limit to the reduction in the amount of residual oxygen, and it is difficult to suppress the amount of oxygen below a desired value. SUMMARY OF THE INVENTION Therefore, an object of the present invention is to solve the above-mentioned problems and provide a method for filling canned goods that can obtain a desired degree of vacuum while suppressing the amount of residual oxygen in the head space to a desired value or less. . [Means for Solving the Problems] As a result of repeated research and experiments in order to solve the above problems, the present inventors created a nitrogen gas-water vapor mixed gas by pre-mixing nitrogen gas and water vapor at an appropriate ratio. It was discovered that when this mixed gas is blown into the head space of a can when filling and sealing the can, the degree of vacuum in the head space and the amount of residual oxygen can both be within the desired ranges, and the present invention has been achieved. That is, the method of the present invention for achieving the above object is to prepare a mixed gas by pre-mixing nitrogen gas and water vapor at a predetermined ratio, and to blow this mixed gas into the head space of the can after filling the can with the contents. It is designed to be tightly wound. The feature of the present invention is that the method of blowing nitrogen gas and water vapor into the head space of a can is not to blow nitrogen gas and water vapor separately over time or on a line, but to mix the nitrogen gas and water vapor in advance in a mixing device. This method uses a method in which a mixed gas is prepared by mixing at a predetermined ratio, and the prepared mixed gas is blown into the head space using an undercover gassing method. Over time or separately on each line, for example, first blowing steam and then blowing nitrogen gas,
Water vapor is removed when nitrogen gas is blown. Conversely, if water vapor is blown in after nitrogen gas is blown in, it will have the same effect as a steam flow, and the nitrogen gas in the head space will be removed and the canned product will be in a high vacuum, but the amount of residual oxygen will not necessarily decrease. It is not possible to keep the value below the desired value. By blowing a mixed gas prepared in advance into the head space at once as in the present invention, nitrogen gas and water vapor can always be supplied at a stable mixing ratio. In addition, the method of the present invention involves pre-mixing nitrogen gas and water vapor at a predetermined ratio to create a mixed gas, heating this mixed gas in the atmosphere, filling the contents into a can, and then pouring the heated mixed gas into the can. It is designed to be blown into the head space and tightened. When the mixed gas is blown into the headspace, a portion of the mixed gas is atomized due to the influence of the ambient temperature, and this atomized portion has no effect of displacing the air in the headspace, so the remaining oxygen is reduced accordingly. However, by heating the mixed gas in the atmosphere and then blowing it into the headspace, this atomization of water vapor can be prevented and the amount of residual oxygen in the mixed gas can be reduced. The effect can be further enhanced. To heat a mixed gas, for example, the mixed gas can be passed through a pipe and the pipe heated to 100°C or higher. [Example] Example 1 Using the apparatus shown in Fig. 1, the steam flow method,
The degree of vacuum in the head space and the amount of residual oxygen were measured using the nitrogen gas flow method and the nitrogen gas-water vapor mixed gas flow method according to the present invention. In FIG. 1, A is a nitrogen gas-steam mixing device, and nitrogen gas supplies are connected to a nitrogen gas supply source (not shown) and a water vapor supply source (not shown) on both sides of the hollow casing 1, respectively. A valve 2 and a steam supply valve 3 are provided, and baffle plates 4 and 5 for stirring are provided inside the casing 1. 6 is a drain pipe for discharging water vapor that has turned into water. A pseudo undercover gassing device B for experimental use is connected to the nitrogen gas-steam mixing device A via a communication pipe 6. This device B also consists of a hollow case 8,
A recess 10 having a semicircular cross section is formed on one side of the recess 10 into which the can 9 is fitted after being filled with the contents of the can and before being sealed, and a gas outlet 11 is opened in the upper part of the recess 10. ing. 12 is a drain pipe for discharging water vapor that has become water. To perform various gas flows using the above device, open the nitrogen gas supply valve 2 and the steam supply valve 3 to supply either one or both of nitrogen gas N 2 and steam S into the enclosure 1 of the device A. do. After filling the contents, the can 9 before being sealed is inserted into the recess 10 of the device B and left standing. The gas supplied into the enclosure 1 (after being stirred and mixed in the case of mixed gas) is transferred to the device B via the communication pipe 7.
The gas enters the casing 8 and is blown into the head space of the can 9 through the gas outlet 11. In this experiment, the above device was used, and the filling temperature was 60℃,
A 200 g Toyo Seamnet can filled with water at 80°C and 90°C was used. A semitro seamer was used as the seamer. In the experiment using the above device, the flow rate of nitrogen gas was set to three types: 0 l/min, 10 l/min, and 25 l/min, and the flow rate of water vapor was set to 0.01 Kg/cm 2 and 0.02 Kg. / cm2 When the above 3
The flow rate of water vapor was measured with respect to the flow rate of nitrogen gas on the street, and was determined as the water vapor flow rate. The measurement results are shown in Table 1 below.

【表】 こうして得られた混合比の窒素ガス―水蒸気混
合ガスを吹込んだ缶のヘツドスペースの真空度を
測定した結果を第2図に、ヘツドスペースの残存
酸素量を測定した結果を第3図にそれぞれ示す。
第2図から窒素ガス―水蒸気混合ガスフローの場
合は窒素ガスフロー単独の場合(スチーム0Kg/
cm2)に比べて真空度を5〜10cmHg高くとれるこ
とが判る。また第3図から窒素ガス―水蒸気混合
ガスフローの場合は残存酸素量は窒素ガスフロー
単独の場合に比べて0.05〜0.7ml程度増加するが、
水蒸気フロー単独の場合(N2:0l/分)に比べ
ると大幅に減少することが判る。(たとえば充填
温度80℃で比較すると約1〜1.3ml)。 今第1表から窒素ガス―水蒸気の混合比を算出
し、望ましい真空度を30cmHg以上、望ましい残
存酸素量を0.4ml未満として、好適な窒素ガス―
水蒸気混合比を第2図および第3図の測定結果か
ら導き出すと次表のとおりとなる。
[Table] Figure 2 shows the results of measuring the degree of vacuum in the head space of the can into which the nitrogen gas-steam mixture gas of the mixture ratio obtained is blown, and Figure 3 shows the results of measuring the amount of residual oxygen in the head space. Each is shown in the figure.
From Figure 2, in the case of nitrogen gas-steam mixed gas flow, and in the case of nitrogen gas flow alone (steam 0 kg/
It can be seen that the degree of vacuum can be increased by 5 to 10 cmHg compared to cm 2 ). Also, from Figure 3, in the case of nitrogen gas-steam mixed gas flow, the amount of residual oxygen increases by about 0.05 to 0.7 ml compared to the case of nitrogen gas flow alone.
It can be seen that this is significantly reduced compared to the case of water vapor flow alone (N 2 : 0 l/min). (For example, about 1 to 1.3 ml when compared at a filling temperature of 80°C). Now, calculate the nitrogen gas-water vapor mixing ratio from Table 1, set the desired degree of vacuum to 30 cmHg or more, and the desired amount of residual oxygen to less than 0.4 ml, and select a suitable nitrogen gas -
The water vapor mixing ratio is derived from the measurement results shown in Figures 2 and 3 as shown in the following table.

【表】【table】

【表】 表2から、窒素ガス―水蒸気混合ガス中の水蒸
気の比率が高くなると真空度は充分高くとれる一
方残存酸素量が多くなり、逆に混合ガス中の窒素
の比率が高くなると残存酸素量は少くなるが真空
度は低くなることが判る。また同表から、適当な
比率の窒素ガス―水蒸気混合ガスを用いれば、充
分高い真空度と充分少い残存酸素量を同時に実現
しうることが判る。同表において所望の真空度を
30cmHg以上、所望の残存酸素量を0.4ml未満とし
た場合、混合ガスの好適混合比(容積)の範囲は
1:2.5〜1:12.5である。第2図および第3図
の各特性曲線から、一般的な缶詰の充填巻締め条
件下において好適な水蒸気:窒素混合比は1:2
ないし1:50の範囲であり、好ましくは1:3な
いし1:15の範囲であることが判る。 実施例 2 各種ガスフローの対象物として250g入りトー
ヨーシームネツクドイン缶に充填温度85〜90℃で
コーヒーを250g充填し、アンダーカバーガツシ
ング装置付21Mシーマーを使用して実験した結果
を次表に示す。ヘツドスペース残存酸素量は巻締
直後レトルト加熱殺菌前の測定値である。混合ガ
スの水蒸気:窒素混合比は1:2.5、ラインスピ
ードは150cpm、窒素ガスの流量は120l/分、水
蒸気の流量は300l/分である。
[Table] From Table 2, as the ratio of water vapor in the nitrogen gas-steam mixture increases, the degree of vacuum can be sufficiently high, but the amount of residual oxygen increases; conversely, as the ratio of nitrogen in the mixed gas increases, the amount of residual oxygen increases. It can be seen that the degree of vacuum decreases, although the amount decreases. Also, from the same table, it can be seen that by using a nitrogen gas-steam mixture gas in an appropriate ratio, a sufficiently high degree of vacuum and a sufficiently small amount of residual oxygen can be achieved at the same time. In the same table, the desired degree of vacuum is
When the desired residual oxygen amount is 30 cmHg or more and less than 0.4 ml, the preferred mixing ratio (volume) of the mixed gas is in the range of 1:2.5 to 1:12.5. From the characteristic curves in Figures 2 and 3, the suitable water vapor:nitrogen mixture ratio is 1:2 under typical canned filling and sealing conditions.
It can be seen that the ratio ranges from 1:50 to 1:50, preferably from 1:3 to 1:15. Example 2 The following table shows the results of an experiment using a 21M seamer with an undercover gashing device, in which 250g of coffee was filled into a 250g Toyo Seam Network can at a filling temperature of 85 to 90°C as an object for various gas flows. show. The amount of oxygen remaining in the head space is the value measured immediately after seaming and before retort heat sterilization. The water vapor:nitrogen mixing ratio of the mixed gas is 1:2.5, the line speed is 150 cpm, the nitrogen gas flow rate is 120 l/min, and the water vapor flow rate is 300 l/min.

【表】 混合ガス

実施例 3 対象物として200g入りトーヨーシームネツク
ドイン缶に充填温度60〜62℃でコーンスープを充
填し、他は実施例2と同一条件で実験した結果を
次表に示す。
[Table] Mixed gas

Example 3 The following table shows the results of an experiment conducted under the same conditions as in Example 2, except that a 200 g Toyo Seam Network can was filled with corn soup at a filling temperature of 60 to 62°C.

【表】 混合ガス

実施例 4 対象物として200g入りトーヨーシームネツク
ドイン缶に充填温度88〜91℃で緑茶を充填し、他
は実施例2と同一条件で実験した結果を次表に示
す。
[Table] Mixed gas

Example 4 The following table shows the results of an experiment conducted under the same conditions as in Example 2, except that a 200 g Toyo Seam Network can was filled with green tea at a filling temperature of 88 to 91°C.

【表】 混合ガス
〔発明の効果〕 本発明によれば、窒素ガスと水蒸気を所定の比
率で予め混合して混合ガスを作り、この混合ガス
を缶のヘツドスペース内に吹込むことにより、ヘ
ツドスペース内の残存酸素量を所定値以下に押え
つつ、従来の窒素ガスフロー法によつては得られ
なかつた種々のレベルの所望の真空度を得ること
ができる。したがつて窒素ガスフロー法において
生じうるバツクリングや検缶上の問題を解消する
ことができる。また従来のスチームフロー法に比
較して残存酸素量を減少させるとともに真空度を
低くすることもできるので、缶詰内容物の品質劣
化を有効に防止しうるとともに、缶の薄肉化を図
ることができる。 本発明の方法は、ジユース等の飲料、加工食品
等広い範囲の缶詰に適用することができる。ま
た、最近缶に肉等の固形食品を充填する場合、固
形食品から滲み出す液分以外液体を封入しないで
レトルト殺菌ゆ行ういわゆるドライパツク缶詰と
呼ばれる缶詰充填方法が開発されているが、本発
明はこの方法に適用しても有効である。 また、いわゆる高真空缶詰においても、この方
法を適応すると、容易に封入酸素量を低く抑えた
ままで、真空度が軽減できるのでハイバキユウム
シーマーがいらなくなる等製造上有利であるとと
もに、缶の薄肉化等を図ることができるので有効
である。
[Table] Mixed gas
[Effects of the Invention] According to the present invention, by mixing nitrogen gas and water vapor in advance at a predetermined ratio to create a mixed gas, and blowing this mixed gas into the head space of the can, residual oxygen in the head space is removed. While keeping the amount below a predetermined value, it is possible to obtain desired degrees of vacuum at various levels that could not be obtained by conventional nitrogen gas flow methods. Therefore, it is possible to eliminate backling and canister inspection problems that may occur in the nitrogen gas flow method. In addition, compared to the conventional steam flow method, it is possible to reduce the amount of residual oxygen and lower the degree of vacuum, so it is possible to effectively prevent quality deterioration of the contents of canned goods and to make cans thinner. . The method of the present invention can be applied to a wide range of canned goods such as drinks such as youth and processed foods. Furthermore, recently, when filling solid foods such as meat into cans, a method of filling cans called dry pack canning has been developed, in which retort sterilization is performed without sealing in any liquid other than the liquid that oozes from the solid food. It is also effective to apply this method. In addition, if this method is applied to so-called high-vacuum canning, the degree of vacuum can be reduced while keeping the amount of oxygen sealed low, which is advantageous in terms of manufacturing, such as eliminating the need for a high-vacuum seamer, and making the cans thinner. This is effective because it allows you to improve your performance.

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

添付図面において、第1図は本発明の方法を実
施するための実験装置の1例を示す斜視図、第2
図は窒素―水蒸気混合ガスフローによる真空度へ
の影響を示すグラフ、第3図は同混合ガスフロー
による残存酸素量への影響を示すグラフである。
In the accompanying drawings, FIG. 1 is a perspective view showing an example of an experimental apparatus for carrying out the method of the present invention, and FIG.
The figure is a graph showing the effect of the nitrogen-water vapor mixed gas flow on the degree of vacuum, and FIG. 3 is a graph showing the effect of the same mixed gas flow on the amount of residual oxygen.

Claims (1)

【特許請求の範囲】 1 窒素ガスと水蒸気を所定の比率で予め混合し
て混合ガスを作り、内容物を缶に充填した後この
混合ガスを缶のヘツドスペース内に吹込み巻締め
ることを特徴とする缶詰の充填方法。 2 窒素ガスと水蒸気を所定の比率で予め混合し
て混合ガスを作り、この混合ガスを大気下で加熱
し、内容物を缶に充填した後この加熱した混合ガ
スを缶のヘツドスペース内に吹込み巻締めること
を特徴とする缶詰の充填方法。
[Claims] 1. A mixed gas is prepared by pre-mixing nitrogen gas and water vapor at a predetermined ratio, and after the contents are filled into a can, this mixed gas is blown into the head space of the can and the can is tightened. How to fill canned goods. 2 Prepare a mixed gas by pre-mixing nitrogen gas and water vapor at a predetermined ratio, heat this mixed gas in the atmosphere, fill the contents into a can, and then blow this heated mixed gas into the head space of the can. A method for filling canned goods characterized by rolling and tightening.
JP27404785A 1985-12-04 1985-12-04 Method of filling can Granted JPS62135124A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP27404785A JPS62135124A (en) 1985-12-04 1985-12-04 Method of filling can

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP27404785A JPS62135124A (en) 1985-12-04 1985-12-04 Method of filling can

Publications (2)

Publication Number Publication Date
JPS62135124A JPS62135124A (en) 1987-06-18
JPS6350249B2 true JPS6350249B2 (en) 1988-10-07

Family

ID=17536228

Family Applications (1)

Application Number Title Priority Date Filing Date
JP27404785A Granted JPS62135124A (en) 1985-12-04 1985-12-04 Method of filling can

Country Status (1)

Country Link
JP (1) JPS62135124A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0435946U (en) * 1990-07-23 1992-03-25

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0786012B2 (en) * 1987-01-16 1995-09-20 東洋製罐株式会社 Method for manufacturing sealed container
JPH01267120A (en) * 1988-04-20 1989-10-25 Pokka Corp Drink canning method
KR102257693B1 (en) * 2015-11-26 2021-05-31 델 몬트 필리핀, 아이엔씨. Fruit packing in plastic cans

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3191352A (en) * 1962-09-18 1965-06-29 Aluminum Co Of America Container sealing method and apparatus
JPS57122774A (en) * 1981-01-23 1982-07-30 Toyo Seikan Kaisha Ltd Preparation of canned juice

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3191352A (en) * 1962-09-18 1965-06-29 Aluminum Co Of America Container sealing method and apparatus
JPS57122774A (en) * 1981-01-23 1982-07-30 Toyo Seikan Kaisha Ltd Preparation of canned juice

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0435946U (en) * 1990-07-23 1992-03-25

Also Published As

Publication number Publication date
JPS62135124A (en) 1987-06-18

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