JPS5888299A - Liquefied gas dripping device - Google Patents

Liquefied gas dripping device

Info

Publication number
JPS5888299A
JPS5888299A JP56185510A JP18551081A JPS5888299A JP S5888299 A JPS5888299 A JP S5888299A JP 56185510 A JP56185510 A JP 56185510A JP 18551081 A JP18551081 A JP 18551081A JP S5888299 A JPS5888299 A JP S5888299A
Authority
JP
Japan
Prior art keywords
gas
liquefied
liquefied gas
dripping
nozzle
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.)
Granted
Application number
JP56185510A
Other languages
Japanese (ja)
Other versions
JPH0135240B2 (en
Inventor
Morio Yamada
守夫 山田
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 JP56185510A priority Critical patent/JPS5888299A/en
Priority to US06/383,319 priority patent/US4489767A/en
Priority to EP82302931A priority patent/EP0074702A3/en
Priority to KR1019820002703A priority patent/KR840000761A/en
Publication of JPS5888299A publication Critical patent/JPS5888299A/en
Publication of JPH0135240B2 publication Critical patent/JPH0135240B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C9/00Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2201/00Vessel construction, in particular geometry, arrangement or size
    • F17C2201/01Shape
    • F17C2201/0104Shape cylindrical
    • F17C2201/0119Shape cylindrical with flat end-piece
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2205/00Vessel construction, in particular mounting arrangements, attachments or identifications means
    • F17C2205/03Fluid connections, filters, valves, closure means or other attachments
    • F17C2205/0302Fittings, valves, filters, or components in connection with the gas storage device
    • F17C2205/0323Valves
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2223/00Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0146Two-phase
    • F17C2223/0153Liquefied gas, e.g. LPG, GPL
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2223/00Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/04Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by other properties of handled fluid before transfer
    • F17C2223/042Localisation of the removal point
    • F17C2223/046Localisation of the removal point in the liquid
    • F17C2223/047Localisation of the removal point in the liquid with a dip tube
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2250/00Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/04Indicating or measuring of parameters as input values
    • F17C2250/0404Parameters indicated or measured
    • F17C2250/0408Level of content in the vessel

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

PURPOSE:To continuously feed liquid stably by feeding the liquid to a storing bath according to the liquefied gas level in the storing bath regardless of the internal pressure of a master tank. CONSTITUTION:When a storing bath 1 and a master tank 5 are connected to each other through a pipeline system 20, liquefied inert gas is flowed into the storing bath 1 by pressure of the master tank 5. When the liquid level in the storing bath 1 reaches a predetermined height, a bucket-type floating valve 15 is adapted to stop inflow of the liquefied gas, and after this the liquid level is kept regardless of a change in the internal pressure of the storing bath 1 which is lower than that of the master tank 5, so as to stably feed liquefied gas corresponding to the consumption automatically.

Description

【発明の詳細な説明】 この発明は、缶詰缶り巻締直前に液化不活性ガスを滴下
封入して、密封後O缶詰缶に所定υ内圧を生じさせるよ
うにした液化不活性ガスD滴下充填装置に関する。
DETAILED DESCRIPTION OF THE INVENTION This invention relates to a liquefied inert gas D drip filling method in which a liquefied inert gas is dripped into a canned can immediately before seaming, and a predetermined internal pressure of υ is generated in the canned can after sealing. Regarding equipment.

炭酸ガスを含まない飲料・食品υ缶詰にあっても、炭酸
ガスを含む飲料と同様O板y#υ薄い材料で製作された
缶を容器として用いることが望まれている。
Even for canned beverages and foods that do not contain carbon dioxide gas, it is desirable to use cans made of thin material as containers for beverages that contain carbon dioxide gas.

こDため缶υ巻締直前に液化不活性ガスを滴下封入して
、密封後0缶つ内圧を高め、薄い材料で作られた缶つ強
度不足を補うことが試みられている。しかし%滴下封入
すべき液化不活性ガスO量は、缶充填物0温凌、巻締装
置り運転速度、缶内上部空間υ大きさ等によって変化す
る。
For this reason, attempts have been made to fill in liquefied inert gas dropwise just before the can is seamed to increase the internal pressure of the can after sealing, thereby compensating for the lack of strength of the can made of thin material. However, the amount of liquefied inert gas O to be dripped and sealed varies depending on the temperature of the can filling, the operating speed of the seaming device, the size of the upper space υ inside the can, etc.

不活性ガス滴下装置は、液化不活性ガス0貯f1檜と滴
下ノズルを備えており、上記り滴下鎗O正確な制御り為
には、貯溜槽へ7)Q化ガスυ補充tυ制御が必要とな
る。
The inert gas dripping device is equipped with a liquefied inert gas storage f1 and a dripping nozzle, and in order to accurately control the above-mentioned dropping, 7) Q-gas υ replenishment tυ control is required to the storage tank. becomes.

最も藺導には、液化ガスつ貯溜槽中にフロートを設け、
フ−o −トv上下動によって槽内り気化ガスを逸流さ
せて内圧を変動させ、こD圧力変化によって液化ガスボ
ンベから液化不活性ガスを貯溜槽に流入するようにする
ことが考えられる。
The most efficient method is to install a float in the liquefied gas storage tank.
It is conceivable that the vaporized gas in the tank is caused to flow away by vertical movement of the foot V to fluctuate the internal pressure, and the liquefied inert gas is caused to flow from the liquefied gas cylinder into the storage tank due to this pressure change.

しかし、滴下ノズルから流下する液化ガスには、常にこ
D貯溜槽内り圧力が作用するDを防ぐことが峻しいため
、こυよつな方式D%下装置では、滴下kk7)制御が
難しくなる。
However, it is difficult to prevent the liquefied gas flowing down from the dripping nozzle from being constantly affected by the pressure inside the D storage tank, so it is difficult to control the dripping with a complicated type D% dropping device. Become.

液化ガス7:)iw下t7)制御を精密にするため、貯
溜槽内に液面針を設け、そD検出[Kよって電磁弁畔に
よって液化ガスり補給量を制御する一方、槽内圧カフ)
14節によって滴下量り主調節を、滴下ノズルに附設し
たパルプによって微調節を行うよう(するもDも本発明
者によって提案されている。(特願昭55−16947
6号)こυ滴下装置は、滴下t p *t+御は精密で
あるが、制御装置が複雑で高価となる欠点を有する。
Liquefied gas 7:) iw lower t7) In order to make the control more precise, a liquid level needle is installed in the storage tank, and the liquefied gas replenishment amount is controlled by the solenoid valve, while the tank internal pressure cuff)
The main adjustment of the dripping amount is carried out according to Section 14, and the fine adjustment is made by the pulp attached to the dripping nozzle.
No. 6) Although this υ dropping device can precisely control the dropping t p *t+, it has the disadvantage that the control device is complicated and expensive.

こυ発明は、缶詰缶O巻締直前に、缶内に液化不活性ガ
スを滴下するため7)装置であって、液化不活性ガスυ
貯溜槽、駆動装置によって開閉される液化ガス0滴下バ
ルブ、該滴下パルプからυ液化ガスを滴下するノズルプ
レート、上紀貯溜槽上部空関り気化ガスを内圧調整パル
プを通じて放出するガスノズル、元タンクから上記貯溜
槽へD液化ガスD給液口を開閉するパケット式フロート
パルプから構成され、制御11vc置は簡尋であるにも
かかわらず、滴下量を精密に制御できる液化ガス滴下装
置を侍ようとするもっである。
This υ invention is a 7) device for dropping liquefied inert gas into a can immediately before sealing the liquefied inert gas υ.
A storage tank, a liquefied gas zero dripping valve that is opened and closed by a drive device, a nozzle plate that drips υ liquefied gas from the dripping pulp, a gas nozzle that releases the vaporized gas from the upper air of the upper storage tank through the internal pressure regulating pulp, and a gas nozzle that releases the vaporized gas from the original tank. I would like to use a liquefied gas dripping device that is composed of a packet-type float pulp that opens and closes the liquefied gas D supply port to the storage tank, and can precisely control the amount of dripping, although the control 11vc setting is simple. There is more to do.

以下図面を参照して詳細に説明する。A detailed explanation will be given below with reference to the drawings.

第1図はこ7)@明υ液化不活性ガス滴下装蓋7)模式
図であり、1は断熱材(発泡スチロール等)等によって
断熱される液ゝ化不活註ガス貯舖槽であり、電磁的駆動
装置2によって液化ガスυ滴下量を調節するためυ滴下
パルプ3およびノズルプレート4を備えている。そして
、こD貯溜槽17)内面は液化不活性ガス0元タンク5
からD初期給液時に、貯溜槽ID温度が十分に低下する
まで0間り急激な気化、圧力上昇を抑え、槽内圧を早期
に安定させて、給液準備時間を短縮し、液化カスを節約
するため、テフロンコートをする。
Figure 1 is a schematic diagram of the liquefied inert gas dripping cap 7), where 1 is a liquefied inert gas storage tank that is insulated with a heat insulating material (styrene foam, etc.), In order to adjust the amount of liquefied gas υ dropped by an electromagnetic drive device 2, a υ dropping pulp 3 and a nozzle plate 4 are provided. And this D storage tank 17) The inner surface is a liquefied inert gas zero source tank 5
During the initial liquid supply, the system suppresses rapid vaporization and pressure rise until the storage tank ID temperature drops sufficiently, stabilizes the tank internal pressure early, shortens liquid supply preparation time, and saves liquefied scum. To prevent this, apply a Teflon coat.

上記ノズルプレート4D中央部には液化ガスを滴下する
滴下ノズル6が設けられ、全体を樹脂(telえは商標
グイフロン)で形成し、表向に霜が耐着したり、ノズル
部が凍結する1)を防止する。
A dripping nozzle 6 for dripping liquefied gas is provided in the center of the nozzle plate 4D, and the entire body is made of resin (telephone is trademark Guiflon), so that frost does not adhere to the surface or the nozzle part freezes. ).

貯榴檜ID上部空関7D気化ガスは、放出管路系8をイ
つでノズルプレート4υ外周slK導き、ガスノズル9
から放出され滴下する液化ガスを低温不活性ガスでシー
ルドすることによって、液化ガスD気化及び凍結を防止
する。一方、気化ガス誘導口10より気化ガスが電磁的
駆動装置2内に誘導され、ソレノイド11を冷却して焼
損等を防止する。また、上記放出管路系8に内圧調整パ
ルプ13及び安全弁14を設は貯溜槽1′7)内圧調整
を行っている。余剰な気化ガスは図示しない別り管路系
からシーマ−巻締部へ導き、缶内封入空気量を減少させ
るためυアンダーカバーガツシング用ガスとして利用す
る・貯溜槽1内へD給液部にはパケット式フロートパル
プ15が設けられ、液面レベルに応じてバルブυ開孔量
が自動的に調節され、常に液面レベルを一定に保持する
ように作動するって液面が安定すると共に、連続的給液
ができる。またパケット式フロートパルプ15は貯溜槽
1’Z)圧力設定変更に対しても無関係に作動するDで
貯溜槽l内O与かガス圧調節が可能でガスO節約にも有
効である。図中、16は槽内圧保持用ヒーターで、貯溜
槽12)内圧が設定値以下にならぬ機制御11fjil
17が作動して槽内圧保持用ヒーターを加熱し、て液化
ガスを気化させる。こり気化ガスを内圧調整パルプ13
を開放して連続的に逃し、貯溜槽1’7)内圧を設定値
に保持する。
The vaporized gas from the storage cypress ID upper air passage 7D is guided through the discharge pipe system 8 to the nozzle plate 4υ outer circumference slK, and then to the gas nozzle 9.
The liquefied gas D is prevented from vaporizing and freezing by shielding the liquefied gas released and dripping with a low-temperature inert gas. On the other hand, vaporized gas is guided into the electromagnetic drive device 2 through the vaporized gas induction port 10 to cool the solenoid 11 and prevent burnout. Further, an internal pressure adjusting pulp 13 and a safety valve 14 are installed in the discharge pipe system 8 to adjust the internal pressure of the storage tank 1'7). Excess vaporized gas is guided from a separate pipe system (not shown) to the seamer seaming part and used as υ undercover gassing gas to reduce the amount of air sealed in the can.・D liquid supply part into the storage tank 1 is equipped with a packet-type float pulp 15, which automatically adjusts the opening amount of the valve υ according to the liquid level, and operates to keep the liquid level constant at all times, thereby stabilizing the liquid level. , continuous liquid supply is possible. In addition, the packet type float pulp 15 operates independently of changes in the pressure setting of the storage tank 1'Z), allowing the gas pressure in the storage tank 1 to be adjusted, which is effective in saving gas. In the figure, 16 is a heater for maintaining the internal pressure of the tank, and a machine control unit 11fjil that prevents the internal pressure of the storage tank 12) from falling below a set value.
17 is activated to heat the tank internal pressure maintenance heater and vaporize the liquefied gas. Internal pressure adjustment pulp 13 for stiff vaporized gas
is opened and released continuously to maintain the internal pressure of the reservoir tank 1'7) at the set value.

元タンク5には凍結防止用ヒーター18及び元タンク5
′I)内圧設定を行うためυ圧カー贅弁19が設けられ
ている。2oは元タンク5と貯溜槽lを接続する管路系
である。
The former tank 5 has a freeze prevention heater 18 and the former tank 5.
'I) A υ pressure curve valve 19 is provided to set the internal pressure. 2o is a pipe system connecting the source tank 5 and the storage tank l.

所定DH下皺に応じて内圧11Mjfパルプ13を設定
し、それによって定まる貯溜槽17:1内圧よりも元タ
ンク5D内圧が高くなるよう圧力1111119f19
を設定して、貯溜槽lと元タンク5を管路系20で接続
すれば、元タンク5υ圧力によりて貯溜槽l内に液化不
活性ガスが流入する。
The internal pressure 11Mjf pulp 13 is set according to the predetermined DH lower wrinkle, and the pressure 1111119f19 is set so that the internal pressure of the original tank 5D is higher than the internal pressure of the storage tank 17:1 determined thereby.
If the storage tank 1 and the source tank 5 are connected by the pipe line system 20 by setting , the liquefied inert gas flows into the storage tank 1 due to the pressure of the source tank 5υ.

貯溜槽l内り液面が所定り高さに達すればパケット式7
0−トバルプ15は液化ガス7)流入を止め、以後は元
タンク5D内圧よりは低い貯溜槽17)内圧υ変化に無
関係に液面レベルを維持し、消費緻に見合った液化ガス
が自動的に給液される。
When the liquid level in the storage tank l reaches a predetermined height, the packet type 7
0-Tovalp 15 stops the inflow of liquefied gas 7), and from then on the storage tank 17), which has a lower internal pressure than the original tank 5D, maintains the liquid level regardless of changes in internal pressure υ, and automatically supplies liquefied gas commensurate with consumption. Liquid is supplied.

第2図は滴下パルプ3及びノズルプレート4つ拡大図で
、21は先端に滴下パルプ37)ニードルを形成し、他
端はンレノイドIIK連結する弁杆で、22はテフロン
コート加工されたブロックで、該ブロック227)外周
部近くに放出管路系8を通って送られてきた気化ガスを
ガスノズル9.に誘導するガス誘導路23が設けられ、
中央部には貯溜槽1つ液化ガスを貯溜する貯溜室24が
設けられている。251.26は樹脂製(飼えば商標、
ダイフロン)7)0リング、27はテフロンまたはシリ
コンaυ0リング、28は貯溜槽lにブロック22を固
定するためυボルト、29V′iガスノズル商品30を
ブロック22に固定するためDボルトである。ノズルプ
レート4D上面中央には弁杆21が挿入され、弁開閉時
に弁杆217)ガイドとして作用する通孔480周囲に
液化ガス貯溜室24からノズルに液を供給する連通孔4
9が設けられており、各連通孔から流出する液tItは
互に衝突1.=て流速を弱めてノズル6から流下する。
Figure 2 is an enlarged view of the dripping pulp 3 and four nozzle plates, with 21 forming a dripping pulp 37) needle at the tip, the other end being a valve rod that connects Renoid IIK, and 22 a Teflon-coated block. The vaporized gas sent through the discharge pipe system 8 near the outer periphery of the block 227) is passed through the gas nozzle 9. A gas guide path 23 is provided to guide the gas to the
A storage chamber 24 in which one storage tank stores liquefied gas is provided in the center. 251.26 is made of resin (trademark if kept,
Diflon) 7) 0 ring, 27 is a Teflon or silicone aυ0 ring, 28 is a υ bolt for fixing the block 22 to the reservoir l, and 29 is a D bolt for fixing the gas nozzle product 30 to the block 22. A valve rod 21 is inserted into the center of the upper surface of the nozzle plate 4D, and a communication hole 4 for supplying liquid from the liquefied gas storage chamber 24 to the nozzle is arranged around a through hole 480 that acts as a guide when the valve is opened and closed.
9 are provided, and the liquid tIt flowing out from each communication hole collides with each other. = to weaken the flow velocity and flow down from the nozzle 6.

第3図は別の実施例のノズルプレート4′で該ノズルプ
レート4′の下端部外周部には第4図に−示す圧力消去
ノズル31を着脱自在に取り付けるためのネジ溝32が
切られている。上記圧力消去ノズル31け滴下ノズル6
からの液化ガスが缶内液面に衝突飛散し、滴下量のバラ
ツキが発生するのを防止するために使用するもので焼結
合金で形成されている。該圧力消去ノズル31の上部開
口部33にはノズルプレート4′のネジ溝32と螺合す
るようにネジ溝34が切られている。また圧力消去ノズ
ル31のテーパ一部35は焼結合金にて孔径2〜10μ
の通液性を有する多孔質フィルター状に形成し、該テー
パー−35の先端部には添加導線36が取り付けられて
いる。
FIG. 3 shows a nozzle plate 4' of another embodiment, in which a threaded groove 32 is cut on the outer periphery of the lower end of the nozzle plate 4' for detachably attaching a pressure-eliminating nozzle 31 shown in FIG. There is. Above pressure elimination nozzle 31 Dripping nozzle 6
It is used to prevent the liquefied gas from colliding with the liquid surface in the can and scattering, causing variations in the amount of dripping, and is made of a sintered alloy. A threaded groove 34 is cut in the upper opening 33 of the pressure erasing nozzle 31 so as to be screwed into the threaded groove 32 of the nozzle plate 4'. The tapered part 35 of the pressure erasing nozzle 31 is made of sintered alloy with a hole diameter of 2 to 10 μm.
It is formed in the shape of a porous filter having liquid permeability, and an addition lead wire 36 is attached to the tip of the taper 35.

第5図は液化不活性ガスを滴下する制御回路Aで、37
は通過缶を検知して検知信号を送る缶検知装置で光電管
や近接スイッチ等で構成されている〇 缶検知装置37で検知された信号は微分回路38で微分
され7リツプフロツプ回路39iC送られる。該フリツ
プフロツプ回路39は滴下パルプ3を作動させる電磁的
駆動装置2とカウンター4υに接続され、該カウンター
4tlVi設定器41と発振器42とタイマー43にそ
れぞれ接続されている。44は滴下バルブ30連続開放
又は断続開放を選択する切換スイッチである。
Figure 5 shows the control circuit A for dropping liquefied inert gas, 37
A can detection device detects passing cans and sends a detection signal. The signal detected by the can detection device 37, which is composed of a phototube, a proximity switch, etc., is differentiated by a differentiation circuit 38 and sent to a lip-flop circuit 39iC. The flip-flop circuit 39 is connected to the electromagnetic drive device 2 for operating the dropping pulp 3 and the counter 4υ, and is connected to the counter 4tlVi setting device 41, oscillator 42 and timer 43, respectively. 44 is a changeover switch for selecting continuous opening or intermittent opening of the dripping valve 30.

液化ガス′7)滴下量υ調整は制(転)装置17で貯溜
槽ID内圧を一定に制御し、制御回路ADO定器41を
所定時間にセ、ツトして滴下パルプ3D開いている時間
O14整設定で行なうが、滴下パルプ3D応答速度が追
従できないような高速ライン(たとえば600缶/mi
n以上)へり適用は制御回路A7)切換スイッチ44を
連続開放に切換へて滴下パルプ3を連続開放して行なう
Liquefied gas '7) The dripping amount υ is adjusted by controlling the internal pressure of the storage tank ID at a constant level with the control device 17, setting the control circuit ADO regulator 41 at a predetermined time, and adjusting the opening time of the dropping pulp 3D O14. However, when using a high-speed line where the dropping pulp 3D response speed cannot follow (e.g. 600 cans/mi)
n or more) The edge application is performed by switching the control circuit A7) changeover switch 44 to continuous open and continuously opening the dripping pulp 3.

こD場合り滴下量7)調整は貯溜槽lυ内圧制御と適宜
ノズル径Oノズルプレート4′及び圧力消去ノズル31
を収り付けることによって行なうまた。液化ガスを封入
した缶り内圧を缶内圧検出装[45で測定しながら測定
値を71゛−ドバツクして液化ガス7)@正量を調節す
ることもできる。
In this case, the dripping amount 7) is adjusted by controlling the internal pressure of the storage tank lυ and using the appropriate nozzle diameter O nozzle plate 4' and pressure elimination nozzle 31.
This is also done by accommodating. It is also possible to adjust the correct amount of liquefied gas 7) by backing up the measured value by 71° while measuring the internal pressure of the can filled with liquefied gas with the can internal pressure detector [45].

缶内圧り安定りためには封入液化ガス量を一定にするこ
とが必要であるが、流下する液化ガスにはタンク1内O
圧力が作用し、ノズル6から高速で流下し、缶内充填物
に衝突画数するDを防ぐことが峻しい。圧力消去ノズル
31を用いれば、こつ圧力を消すことが1丁能であるが
In order to stabilize the pressure inside the can, it is necessary to keep the amount of sealed liquefied gas constant;
It is difficult to prevent D from flowing down from the nozzle 6 at high speed and colliding with the contents in the can due to the pressure applied thereto. It is possible to eliminate the pressure by using the pressure elimination nozzle 31.

流下する液化ガスは一時消去ノズル31内に滞溜するた
め、連続l−下υv7h会には良いが、間欠滴下2)l
会には適当とは云えない。
Since the flowing liquefied gas temporarily accumulates in the erasing nozzle 31, it is good for continuous l-down υv7h, but intermittent dropping 2) l
I can't say it's appropriate for the meeting.

第6図%第7図は、流下液化ガス′り流速を減するため
Dノズル7)変形例を示し、@6図に示すノズルプレー
トは、全体として幡第2凶に不すもDとほぼ同じである
が、ノズル6υ下品にこれに斜設する衝突l1i61を
設けた流出口62を設けである。これによりノズル6を
流下する液化ガスは、衝突面61に衝突して運動エネル
ギーを失い、流出速度が低下する。
Fig. 6% Fig. 7 shows a modification of the D nozzle 7) to reduce the flow velocity of the flowing liquefied gas. It is the same, but the nozzle 6υ is provided with an outlet 62 provided with an impingement l1i61 obliquely provided thereon. As a result, the liquefied gas flowing down the nozzle 6 collides with the collision surface 61 and loses kinetic energy, reducing the outflow speed.

1iK7図に示す別り実施例では、ノズル流出口はノズ
ルパイプ71を有し、こ0ノズルパイプ71唸流出ロア
2とは偏心し、た位瞳に設けられ、流下する液化ガスは
、一旦ノズルパイブ727)上端に衝突し7、運動エネ
ルギーを失った後、ノズルパイプ72を流下する。こO
ように流下速度を下げるこ七によって充填時D@敗し、
充填量を安定させることが可能となるに υ発明は上記り簡単な構成よりなり、貯溜槽1へD給液
は、元タンク5内圧に無関係に、貯溜槽10液化ガスυ
レベル71によ、って行われるOで、連続的に安定した
給液が可能であると共に、液面レベルも一定に保たれる
。貯溜槽17)内面をテフロンコートしたつで一時的な
断熱効果が得られ、スタートまでつ準備時間り短縮化が
可能である。滴下バルブつノズルプレート4やそつ附I
Is品を樹脂で形成したつでノズルプレート4等υ我面
に霜が耐着するDを防止できるばかりか、ノズル穴部つ
凍結も防止できる。ノズルプレート4υ外周邪に気化ガ
スを導きブローする構成でおるから液化ガスυ冷却効果
があるばかりか霜付(凍結)を防止できる。
In the alternative embodiment shown in Fig. 1iK7, the nozzle outlet has a nozzle pipe 71, which is eccentric to the whirling outflow lower 2 and is provided at the pupil, and the liquefied gas flowing down is once connected to the nozzle pipe 71. 727) After colliding with the upper end 7 and losing kinetic energy, it flows down the nozzle pipe 72. KoO
By lowering the flow rate, D@defeats when filling,
In order to make it possible to stabilize the filling amount, the υ invention has the above-mentioned simple configuration, and the liquid D supplied to the storage tank 1 is connected to the liquefied gas υ in the storage tank 10, regardless of the internal pressure of the original tank 5.
O performed by the level 71 allows continuous and stable liquid supply and also keeps the liquid level constant. Reservoir tank 17) By coating the inner surface with Teflon, a temporary insulation effect can be obtained, and the preparation time until the start can be shortened. Dripping valve and nozzle plate 4 and attachment I
By forming the Is product with resin, it is possible not only to prevent frost from adhering to the surfaces of the nozzle plate 4, etc., but also to prevent the nozzle holes from freezing. Since the structure is such that vaporized gas is guided and blown to the outer periphery of the nozzle plate 4υ, not only is there a cooling effect of the liquefied gas υ, but also frosting (freezing) can be prevented.

液化ガスを滴下する制御回路Aを設けたりで通過缶を検
知して自動的に1缶毎に滴下バルブ3を1′F、%lh
させて滴下瞳を調整した液化ガスを缶に滴下封入で良る
。ノズルプレート4′に圧力消去ノズル31を取り付け
ることによって滴下ノズル6からD液化ガスが缶内液面
に衝突して部数するOを防止できる。槽内圧保持用ヒー
ター16及び内圧pl軽バルブ13を設けたつで制御装
置17に′よって自動的に貯溜槽l内υ内圧を設定値に
保持できる。貯溜槽l内θ気化ガスを電磁的躯勧装置2
内に誘導する構成にしたつで電磁コイルを冷却して焼損
を防止できる。
By installing a control circuit A that drips liquefied gas, it detects passing cans and automatically controls the dripping valve 3 for each can at 1'F, %lh.
The liquefied gas with adjusted drip pupil can be dripped into a can. By attaching the pressure erasing nozzle 31 to the nozzle plate 4', it is possible to prevent the liquefied gas D from the dripping nozzle 6 from colliding with the liquid surface in the can, thereby preventing the liquefied gas from colliding with the liquid surface in the can. By providing the heater 16 for maintaining tank internal pressure and the internal pressure PL light valve 13, the internal pressure υ in the storage tank 1 can be automatically maintained at a set value by the control device 17'. Electromagnetic evacuation device 2 for θ vaporized gas in the storage tank l
The electromagnetic coil can be cooled and burnout can be prevented by inducing the electromagnetic coil inward.

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

第1凶はこυ発明の液化不活性ガス滴下鍮置θl!A式
図、第2図はこり発明p滴下バルブ及びノズルグレート
等O拡大断面凶、第3図は別υ実施例υノズルグレート
υ拡大断面図、第4図は圧力消去ノズルD拡大断th1
図、第5図は液化ガスを滴下する劃−回路υ概略−、W
、6図、−7図は滴下ノズルの他の実施例の拡大断面図
である。 1:貯溜槽 2:電磁的駆動f2置 3:1lli下パ
ルプ 4.4:ノズルプレート 5:元タンク 6:滴
下ノズル 7:上部空間 8:放出管路系 9:ガスノ
ズル 1o:気化ガス酵導口 11:ソレノイド 13
:内圧調整バルブ14:安全弁 15:パケット式フロ
ートバルブ 16:槽内圧保持用ヒーター 17:制御
装置 18:凍結防止用ヒーター 19:圧力調整弁 
20:管路系 21:弁杆 22ニブロツク 23:ガ
ス誘導路 2.4:貯溜室26:0リング 27:0リ
ング 28:ボルト 29:ボルト 3o:ガスノズル
部品 31:圧力消去ノズル 32:ネジ溝 ・33:
上S開口部 34:ネジ溝 35:テーパ一部36:添
加導線 37:缶検知装@  38:做分回路 39:
フリツプフロツプ回路 40:門クンター 41:設定
器 42:発振器43:タイY−44:切換スイッチ 
45:缶内圧検出装置 A:制御回路 61:液化ガス
衝突面 71:ノズルパイプ 特軒出幀人  東洋製罐味弐会仕 出願人代理人 弁理士 佐  藤  文  男(ほか1
名) 第   2   図 ?P   :L   図 8
The first problem is this υ invented liquefied inert gas dripping brass position θl! A formula diagram, Fig. 2 is an enlarged sectional view of the invention P dripping valve and nozzle grating, etc., Fig. 3 is an enlarged sectional view of another example υ nozzle grating υ, and Fig. 4 is an enlarged sectional view of the pressure elimination nozzle D.
Figure 5 is a schematic diagram of the circuit υ for dropping liquefied gas, W
, 6 and 7 are enlarged sectional views of other embodiments of the drip nozzle. 1: Storage tank 2: Electromagnetic drive f2 position 3: 1lli lower pulp 4.4: Nozzle plate 5: Original tank 6: Dripping nozzle 7: Upper space 8: Discharge piping system 9: Gas nozzle 1o: Vaporized gas fermentation inlet 11: Solenoid 13
: Internal pressure adjustment valve 14: Safety valve 15: Packet type float valve 16: Heater for maintaining tank internal pressure 17: Control device 18: Freeze prevention heater 19: Pressure adjustment valve
20: Piping system 21: Valve rod 22 Niblock 23: Gas guiding path 2.4: Storage chamber 26: 0 ring 27: 0 ring 28: Bolt 29: Bolt 3o: Gas nozzle parts 31: Pressure elimination nozzle 32: Thread groove ・33:
Upper S opening 34: Thread groove 35: Taper part 36: Additive conductor 37: Can detection device @ 38: Subtraction circuit 39:
Flip-flop circuit 40: Gate controller 41: Setting device 42: Oscillator 43: Tie Y-44: Changeover switch
45: Can internal pressure detection device A: Control circuit 61: Liquefied gas collision surface 71: Nozzle pipe Tokuken developer Patent attorney Fumi Sato (and 1 others)
name) Figure 2? P:L Figure 8

Claims (1)

【特許請求の範囲】 <1)  缶詰缶の巻締直前に、缶内に液化不活比ガス
を滴下するための装置であって、液化不活性ガスの貯溜
槽、液化不活性ガスを滴下する制御回路によって駆動さ
れる電磁的駆動装置、該電磁的駆動装置によって液化ガ
スの滴下量を−節するための滴下パルプ及びノズル7レ
ート、咳ノズルプレートの外周部に設けられた貯溜槽の
気化ガスを放出管路系を通って放出するガスノズル、該
放出管路系に設けられた内圧調整パルプ、元タンクから
貯溜槽への液化ガスの給液口を開閉する70−トパルブ
を備えていることを特徴とする液化ガス滴下装置。 2)貯溜槽の内面にテフロンコートした特1!FMII
求の範囲第1項記載の液化ガス滴下装置。 3)ノズルプレートをw脂で形成した特軒−青求つ範囲
第1項記載p液化ガス滴下装置 4)ノズルプレートに圧力消去ノズルを取り付けた特許
請求の範囲第1項記a7)液化ガス滴下装置。 5)貯溜槽に気化ガス誘導口を設けた特許請求の範囲第
1項記載7)液化ガス滴下装置。 6) 液化ガスを滴下する制−回路に缶内圧検出装置を
接続した特許請求の範囲第1項記載υ液化ガス滴下装置
[Claims] <1) A device for dripping liquefied inert gas into a can immediately before seaming the can, the device comprising a liquefied inert gas storage tank and a liquefied inert gas reservoir for dripping the liquefied inert gas. An electromagnetic drive device driven by a control circuit, a dropping pulp and nozzle rate for regulating the amount of liquefied gas dripped by the electromagnetic drive device, and a vaporized gas in a reservoir provided on the outer periphery of the cough nozzle plate. A gas nozzle for discharging liquefied gas through a discharge pipe system, an internal pressure adjusting pulp provided in the discharge pipe system, and a 70-top valve for opening and closing a supply port for liquefied gas from a source tank to a storage tank. Characteristic liquefied gas dripping device. 2) Special feature 1: Teflon coating on the inner surface of the storage tank! FMII
The liquefied gas dripping device according to item 1. 3) Tokuken with a nozzle plate formed of w fat - blue sought range p liquefied gas dripping device as described in claim 1 4) Claim 1 as described in claim 1 a7) Liquefied gas dripping device in which a pressure erasing nozzle is attached to the nozzle plate Device. 5) A liquefied gas dripping device according to claim 1, wherein the storage tank is provided with a vaporized gas guide port. 6) A liquefied gas dripping device according to claim 1, wherein an internal pressure detection device is connected to a control circuit for dripping liquefied gas.
JP56185510A 1981-09-08 1981-11-20 Liquefied gas dripping device Granted JPS5888299A (en)

Priority Applications (4)

Application Number Priority Date Filing Date Title
JP56185510A JPS5888299A (en) 1981-11-20 1981-11-20 Liquefied gas dripping device
US06/383,319 US4489767A (en) 1981-09-08 1982-05-28 Apparatus for dropping liquefied gases
EP82302931A EP0074702A3 (en) 1981-09-08 1982-06-08 Apparatus for dropping a liquefied inert gas into a can
KR1019820002703A KR840000761A (en) 1981-09-08 1982-06-17 Liquefied Gas Dropping Device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56185510A JPS5888299A (en) 1981-11-20 1981-11-20 Liquefied gas dripping device

Publications (2)

Publication Number Publication Date
JPS5888299A true JPS5888299A (en) 1983-05-26
JPH0135240B2 JPH0135240B2 (en) 1989-07-24

Family

ID=16172040

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56185510A Granted JPS5888299A (en) 1981-09-08 1981-11-20 Liquefied gas dripping device

Country Status (1)

Country Link
JP (1) JPS5888299A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS58161299U (en) * 1982-04-22 1983-10-27 テイサン株式会社 Low temperature liquefied gas outflow device
JPS58161298U (en) * 1982-04-22 1983-10-27 大和製罐株式会社 Low-temperature liquefied gas quantitative flow or dripping device
JPS58161300U (en) * 1982-04-22 1983-10-27 テイサン株式会社 Low temperature liquefied gas outflow device
JPS591899A (en) * 1982-06-26 1984-01-07 Suntory Ltd Supply method of liquefied inactive gas
JPS6160416A (en) * 1984-08-22 1986-03-28 東洋製罐株式会社 Liquefied inert gas dropping device
JPS62124398A (en) * 1985-11-21 1987-06-05 Takeuchi Press Kogyo Kk Low-temperature liquefied gas falling device
JPS62147195A (en) * 1985-12-18 1987-07-01 Toyo Seikan Kaisha Ltd Liquefied gas adder
JPS633903U (en) * 1986-06-27 1988-01-12
JP2011038581A (en) * 2009-08-10 2011-02-24 Taiyo Nippon Sanso Corp Liquefied gas injecting device
KR20220117811A (en) * 2021-02-17 2022-08-24 주식회사 씨브이에스 Double storage type gas-liquid separator

Cited By (15)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6233198Y2 (en) * 1982-04-22 1987-08-25
JPS58161298U (en) * 1982-04-22 1983-10-27 大和製罐株式会社 Low-temperature liquefied gas quantitative flow or dripping device
JPS58161300U (en) * 1982-04-22 1983-10-27 テイサン株式会社 Low temperature liquefied gas outflow device
JPH0110331Y2 (en) * 1982-04-22 1989-03-24
JPS58161299U (en) * 1982-04-22 1983-10-27 テイサン株式会社 Low temperature liquefied gas outflow device
JPS6240883Y2 (en) * 1982-04-22 1987-10-20
JPS6251805B2 (en) * 1982-06-26 1987-11-02 Suntory Ltd
JPS591899A (en) * 1982-06-26 1984-01-07 Suntory Ltd Supply method of liquefied inactive gas
JPS6160416A (en) * 1984-08-22 1986-03-28 東洋製罐株式会社 Liquefied inert gas dropping device
JPS6254689B2 (en) * 1984-08-22 1987-11-16 Toyo Seikan Kaisha Ltd
JPS62124398A (en) * 1985-11-21 1987-06-05 Takeuchi Press Kogyo Kk Low-temperature liquefied gas falling device
JPS62147195A (en) * 1985-12-18 1987-07-01 Toyo Seikan Kaisha Ltd Liquefied gas adder
JPS633903U (en) * 1986-06-27 1988-01-12
JP2011038581A (en) * 2009-08-10 2011-02-24 Taiyo Nippon Sanso Corp Liquefied gas injecting device
KR20220117811A (en) * 2021-02-17 2022-08-24 주식회사 씨브이에스 Double storage type gas-liquid separator

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