JPS58142098A - Flow-down device for liquefied inert gas - Google Patents
Flow-down device for liquefied inert gasInfo
- Publication number
- JPS58142098A JPS58142098A JP2487982A JP2487982A JPS58142098A JP S58142098 A JPS58142098 A JP S58142098A JP 2487982 A JP2487982 A JP 2487982A JP 2487982 A JP2487982 A JP 2487982A JP S58142098 A JPS58142098 A JP S58142098A
- Authority
- JP
- Japan
- Prior art keywords
- liquefied gas
- injection
- receptacle
- filtrable
- flow
- 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.)
- Pending
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B65—CONVEYING; PACKING; STORING; HANDLING THIN OR FILAMENTARY MATERIAL
- B65B—MACHINES, APPARATUS OR DEVICES FOR, OR METHODS OF, PACKAGING ARTICLES OR MATERIALS; UNPACKING
- B65B31/00—Packaging articles or materials under special atmospheric or gaseous conditions; Adding propellants to aerosol containers
- B65B31/006—Adding fluids for preventing deformation of filled and closed containers or wrappers
Landscapes
- Chemical & Material Sciences (AREA)
- Dispersion Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- Vacuum Packaging (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は例えば内容物が収納されている未封の軟質−へ
液体窒素等の液化不活性ガス(以下単に液化ガスという
)を流下せしめる装置に関する。従来より非炭酸飲料お
よびその他の袋詰製品において、薄肉の金属製−例えr
iO,15M犀のアルミ罐またはプラスチック製罐(両
者をきめて軟質−という)を使用1、窒素等の不活性ガ
スを封入し罐内の圧力t−^め薄肉の軟質−の使用にも
かかわらず、保存、輸送における軟質−の変形や破損を
防止することが竹われている。この目的の為に種々の液
化ガスの注入装置が開発されているが、その殆んどはコ
ンベアで送られている未封の罐の到来を検知した彼、弁
を一足時間開き液化ガス′fr#i下させる−のでめっ
た。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for causing a liquefied inert gas such as liquid nitrogen (hereinafter simply referred to as liquefied gas) to flow down into an unsealed soft container containing contents, for example. Traditionally, non-carbonated beverages and other packaged products have been manufactured using thin-walled metal
iO, 15M aluminum cans or plastic cans (both are referred to as soft) are used 1, and an inert gas such as nitrogen is filled in, and the pressure inside the can is reduced to t-^ Despite the use of thin-walled soft- First, the soft material is designed to prevent deformation and damage during storage and transportation. Various liquefied gas injection devices have been developed for this purpose, but most of them detect the arrival of an unsealed can being sent on a conveyor and open the valve for a moment to inject the liquefied gas. #I let it go down - so I was disappointed.
更61i下ノズルと−との間に中間受器を設Hたもので
あっても、注入される液化ガスはWL接小滴状で−に注
ぎこまれる4のであった。このように間欠的注入および
小滴状での注入ではわずかの時間のずれおよび小滴の大
きさの不一致およびその数のバラツキによって、注入量
即ち密封稜の罐の内圧に大きな差が生じていた。特に容
量の少ない罐においてはその傾向が大であった。本発明
者らはバラツキの少ない液化ガスの添加を研究の結果、
液化ガスを細い糸状の線として連続して流下させればよ
いことに着目し本発明に到達したもので、本発明は液化
不活性ガス容器に、ニードルバルブおよび該パルプより
取出される液化不活性Aスのろ過性受器を設け、該ろ過
性受益下部より液化不活性ガスを製出流下させることを
特徴とする液化不活性ガスの流下装置である。Furthermore, even if an intermediate receiver was installed between the lower nozzle 61i and -, the injected liquefied gas would be poured into - in the form of droplets in contact with the WL. In this way, in intermittent injection and injection in the form of small droplets, slight time lags, discrepancies in the size of the droplets, and variations in their number caused large differences in the injection volume, that is, the internal pressure of the can at the sealed ridge. . This tendency was especially strong in cans with small capacity. As a result of research on adding liquefied gas with little variation, the present inventors found that
The present invention was developed by focusing on the fact that liquefied gas should be allowed to flow down continuously in the form of a thin thread-like line. This is a liquefied inert gas flowing device characterized in that a filterable receiver of A is provided and the liquefied inert gas is produced and flowed down from the lower part of the filterable receiver.
本発fIAにおいてニードルバルブは容器の下部に17
けることが好ましいが、後述するろ過性受器との関係で
容器の@面等に設けてもよい。液化ガス自体の温度は働
めて低いので、その内[めるニードルバルブおよびその
調節機1IItFi極度の耐寒性を要求されるのである
。従ってニードルパルプはスプリングによって調節さn
るのが好ましく、スプリングを容器外部より押し下ける
ことま7′jは引きとけることによってバルブの開閉ま
たは流量を鯛葡することが好着しい。ニードルパルプよ
り流出[7た液化βスは直ちVCろ過性受#VC入る。In this fIA, the needle valve is located at the bottom of the container.
Although it is preferable to provide the filter on the @ side of the container in relation to the filterable receiver described later. Since the temperature of the liquefied gas itself is low, extreme cold resistance is required for the needle valve and its regulator. Therefore, the needle pulp is adjusted by the spring.
It is preferable to open/close the valve or control the flow rate by pulling the spring 7'j rather than pushing it down from the outside of the container. The liquefied β gas flowing out from the needle pulp immediately enters the VC filtration receiver.
ろ過性受器の形状は有底の円筒状のもので底がゆるやか
に丸み會もっていればよく、必景に応じて底面先端に液
化ガス案内用突起を設けてもよい。The shape of the filterable receptacle may be a cylindrical one with a bottom and a gently rounded bottom. Depending on the desired view, a protrusion for guiding liquefied gas may be provided at the tip of the bottom surface.
尚、該ろ過性受器内部は外気と遮断し液化ガス答器内と
同じ圧にして製出を容易ならしめることが好ましい。It is preferable that the inside of the filterable receiver be isolated from the outside air and maintained at the same pressure as the inside of the liquefied gas reactor to facilitate production.
ここにいうろ過性受器としては、焼結金属、素焼陶磁器
、合成ゼオライト、ガラス、プラスチック轡の材質で作
られ、ろ過サイズ30μ〜200μのものであればよい
。また焼結金属としてはステンレス製のものが好ましい
が他の金属または合金でおってもよい。The filtration receptacle referred to herein may be made of a material such as sintered metal, unglazed ceramics, synthetic zeolite, glass, or plastic casing, and has a filtration size of 30 μ to 200 μ. The sintered metal is preferably made of stainless steel, but other metals or alloys may be used.
このようにすることによって液化ガスは容器より参み出
し細い糸状となって連続的に流下する。By doing this, the liquefied gas flows out from the container and flows down continuously in the form of a thin thread.
またバルブの流量の差はろ過性容器の壁を通している間
にその誤差は吸収され常に一定の流量となるものである
。一方軟質−は殆んどすきまなく連続してコンベアで送
られているので、流下する欣化ガスが糸状に連続して流
下しても殆んど無駄なく軟質線に注ぎこまれるものであ
る。勿鍮何らかの原因でコンベアが停止した時は直ちに
ニードルバルブを閉じると同時に液化ガスの糸状の流れ
を他にそらすように自動化しておけばよい。また罐の大
きさ、内容物の温度、コンベアの速度等によって液化ガ
スの流量が変るものであるが、それに合せて流量を調節
すればよい。Further, the difference in flow rate between the valves is absorbed while the flow passes through the wall of the filterable container, and the flow rate is always constant. On the other hand, since the soft wire is continuously conveyed on a conveyor with almost no gaps, even if the flowing solute gas flows down continuously in the form of a thread, it is poured into the soft wire with almost no waste. Of course, if the conveyor stops for some reason, it can be automated to immediately close the needle valve and divert the thread-like flow of liquefied gas elsewhere. Furthermore, the flow rate of the liquefied gas varies depending on the size of the can, the temperature of the contents, the speed of the conveyor, etc., and the flow rate may be adjusted accordingly.
□゛・1、
本発明は以上述べたようにろ過性受器を介して液化ガス
を細い糸状にしてゆるやかに罐に注入するので、小滴状
の注入と比較して注入の際のショックが少ないものであ
る。従って従来の小滴状の注入に比較して注入時による
ショックによる液化ガスの飛散および蒸@が少lく、し
かも一定して注入できるので注入量のバラツキが殆んど
ないという、すぐれた効果を有するものである。□゛・1. As described above, in the present invention, the liquefied gas is made into a thin thread and is gently injected into the can through the filterable receiver, so there is less shock during injection compared to injection in the form of small droplets. There are few. Therefore, compared to conventional small droplet injection, there is less scattering and evaporation of liquefied gas due to shock during injection, and since it can be injected constantly, there is almost no variation in the injection amount, which is an excellent effect. It has the following.
次に図面によって本発明装置の一例を説明する。第1図
μ不装置中央縦断向図であり、第2凶rJその111部
の拡大中央縦断面図である。1は容器本体、2は保冷用
外筒、3は保−筒、4はニードルバルブのインナパル7
’、5U(−のシートバルブ、6は焼結金m製ろ過性受
器、7は液化ガス流路、8は軸、9は輔支持枠、lOは
スプリング、11は固定スプリング支持枠、12は可動
スプリング支持枠、13は軸8の上下駆動棒、14は1
3の支持枠、15は液化ガス流路、16.17は焼結金
属製受器6の支持枠、18は保冷用外筒、19Fi液化
ガスの流下口、20は駆動棒13の駆動部、21に液化
ガス供、給管5.22は液面センサー、23は液化ガス
供給管バルブである。Next, an example of the apparatus of the present invention will be explained with reference to the drawings. FIG. 1 is a central longitudinal cross-sectional view of the μ-less device, and is an enlarged central longitudinal cross-sectional view of the 111th part of the second rJ. 1 is the container body, 2 is the outer cylinder for cold storage, 3 is the storage cylinder, 4 is the inner pallet 7 of the needle valve.
', 5U (- seat valve, 6 is a filterable receiver made of sintered gold, 7 is a liquefied gas flow path, 8 is a shaft, 9 is a support frame, IO is a spring, 11 is a fixed spring support frame, 12 1 is a movable spring support frame, 13 is a vertical drive rod of shaft 8, and 14 is 1
3 support frame, 15 liquefied gas channel, 16.17 support frame for sintered metal receiver 6, 18 cold insulation outer cylinder, 19Fi liquefied gas flow outlet, 20 drive part of drive rod 13, 21 is a liquefied gas supply, supply pipe 5.22 is a liquid level sensor, and 23 is a liquefied gas supply pipe valve.
インナバルブ4は可動スプリング支持枠12を取り付け
られた軸8と一体である。軸8にスプリング104Cよ
って常に上方への力が加わっている。この軸8は上下駆
動棒13の位t!ftによってその位置が決まる。よっ
てインチバルブ4とシートバルブ5の相対位置も決まり
、める一定の量の液化ガスがろ過性受器に入る。ろ過性
受器6に入った液化ガスは整流され液化ガス流下口19
より糸状に流下する。流下した液化ガスは軟質線へ注入
される。The inner valve 4 is integral with a shaft 8 to which a movable spring support frame 12 is attached. An upward force is always applied to the shaft 8 by the spring 104C. This shaft 8 is at the position of the vertical drive rod 13! Its position is determined by ft. Therefore, the relative positions of the inch valve 4 and the seat valve 5 are also determined, and a certain amount of liquefied gas enters the filterable receiver. The liquefied gas that has entered the filterable receiver 6 is rectified and passed through the liquefied gas outlet 19.
Flows down like a thread. The flowing liquefied gas is injected into the soft wire.
第3図は本装置の使用の態様を示す一部切欠き斜視図で
あり、24ij液化ガスの流れ、25は軟質線、26F
i本装置の上部カバー、27にセンサーリード部である
。FIG. 3 is a partially cutaway perspective view showing the mode of use of this device, in which 24ij is the flow of liquefied gas, 25 is a soft wire, and 26F is a flow of liquefied gas.
i The upper cover of this device, 27 is the sensor lead part.
第1図は本発明にかかる装置の中央縦断面図、第2図は
その要部の縦拡大断面図、第3図に本装置の使用の態様
を示す一部切欠き斜視図である。lは液化ガス容器、4
tiニードルバルブのインナバルブ、5flニードルバ
ルブのシ一トハルブ、6ijろ過性受器。
出願人 サン) IJ−株式会社
代理人 滝 月1 敏 雄
第1図
第2図
q
515−
第う図FIG. 1 is a central vertical cross-sectional view of the device according to the present invention, FIG. 2 is an enlarged vertical cross-sectional view of the main part thereof, and FIG. 3 is a partially cutaway perspective view showing the mode of use of the device. l is a liquefied gas container, 4
TI needle valve inner valve, 5fl needle valve seat valve, 6ij filtration receiver. Applicant Sun) IJ-Co., Ltd. Agent Tsuki 1 Toshio Taki Figure 1 Figure 2 Q 515- Figure U
Claims (1)
より取出される液化不活性ガスのろ過性受器を設け、該
ろ過性受器下部より液化不粘性ガスを1出流下させるこ
とを特徴とする液化不活性ガスの流下装置0The liquefied inert gas container 6 is provided with a filterable receiver for the needle pulp and the liquefied inert gas taken out from the valve, and the liquefied inviscid gas is caused to flow down once from the lower part of the filterable receiver. Liquefied inert gas flow device 0
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2487982A JPS58142098A (en) | 1982-02-17 | 1982-02-17 | Flow-down device for liquefied inert gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2487982A JPS58142098A (en) | 1982-02-17 | 1982-02-17 | Flow-down device for liquefied inert gas |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS58142098A true JPS58142098A (en) | 1983-08-23 |
Family
ID=12150473
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2487982A Pending JPS58142098A (en) | 1982-02-17 | 1982-02-17 | Flow-down device for liquefied inert gas |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS58142098A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58166884U (en) * | 1982-04-26 | 1983-11-07 | セイレイ工業株式会社 | Biting grain discharge structure on the sorting belt in a soybean sorter |
JPS5934098A (en) * | 1982-08-20 | 1984-02-24 | Toyo Seikan Kaisha Ltd | Liquefied-gas dripping nozzle |
EP0271031A2 (en) * | 1986-12-10 | 1988-06-15 | Linde Aktiengesellschaft | Dosing device for low-boiling liquefied gases |
JPH01501057A (en) * | 1986-07-21 | 1989-04-13 | エーヂーエー アクチボラグ | Condensed gas dosing device |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5786699A (en) * | 1980-11-17 | 1982-05-29 | Toyo Seikan Kaisha Ltd | Quantitative addition method for inert liquefied gas and its apparatus |
-
1982
- 1982-02-17 JP JP2487982A patent/JPS58142098A/en active Pending
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5786699A (en) * | 1980-11-17 | 1982-05-29 | Toyo Seikan Kaisha Ltd | Quantitative addition method for inert liquefied gas and its apparatus |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS58166884U (en) * | 1982-04-26 | 1983-11-07 | セイレイ工業株式会社 | Biting grain discharge structure on the sorting belt in a soybean sorter |
JPS6223583Y2 (en) * | 1982-04-26 | 1987-06-16 | ||
JPS5934098A (en) * | 1982-08-20 | 1984-02-24 | Toyo Seikan Kaisha Ltd | Liquefied-gas dripping nozzle |
JPS6150199B2 (en) * | 1982-08-20 | 1986-11-01 | Toyo Seikan Kaisha Ltd | |
JPH01501057A (en) * | 1986-07-21 | 1989-04-13 | エーヂーエー アクチボラグ | Condensed gas dosing device |
EP0271031A2 (en) * | 1986-12-10 | 1988-06-15 | Linde Aktiengesellschaft | Dosing device for low-boiling liquefied gases |
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