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JPH0219359B2 - - Google Patents
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JPH0219359B2 - - Google Patents

Info

Publication number
JPH0219359B2
JPH0219359B2 JP57114327A JP11432782A JPH0219359B2 JP H0219359 B2 JPH0219359 B2 JP H0219359B2 JP 57114327 A JP57114327 A JP 57114327A JP 11432782 A JP11432782 A JP 11432782A JP H0219359 B2 JPH0219359 B2 JP H0219359B2
Authority
JP
Japan
Prior art keywords
pressure
valve
evaporator
gas
level sensor
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 - Lifetime
Application number
JP57114327A
Other languages
Japanese (ja)
Other versions
JPS596498A (en
Inventor
Tetsuya Oonishi
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.)
KAGURA SEISAKUSHO KK
Original Assignee
KAGURA SEISAKUSHO KK
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 KAGURA SEISAKUSHO KK filed Critical KAGURA SEISAKUSHO KK
Priority to JP57114327A priority Critical patent/JPS596498A/en
Publication of JPS596498A publication Critical patent/JPS596498A/en
Publication of JPH0219359B2 publication Critical patent/JPH0219359B2/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
    • F17C9/02Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure with change of state, e.g. vaporisation
    • 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
    • F17C2201/0109Shape cylindrical with exteriorly curved 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
    • F17C2227/00Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03Heat exchange with the fluid
    • F17C2227/0367Localisation of heat exchange
    • F17C2227/0388Localisation of heat exchange separate
    • F17C2227/0393Localisation of heat exchange separate using a vaporiser
    • 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)

Description

【発明の詳細な説明】 〔産業上の利用分野〕 本発明は、貯槽内の液化ガスを大気熱により蒸
発させて消費する液化ガス蒸発装置に関し、特に
蒸発器から液化ガスが液状のまゝ消費先若しくは
装置外に流出することを確実に防止し得るように
したものである。
[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a liquefied gas evaporator that evaporates and consumes liquefied gas in a storage tank using atmospheric heat, and particularly relates to a liquefied gas evaporator that consumes liquefied gas from an evaporator while being liquefied. This makes it possible to reliably prevent the liquid from leaking out of the device or the device.

〔従来の技術及びその問題点〕[Conventional technology and its problems]

従来は、貯槽の下部から液体のまゝ導出される
液化ガスをスプリングによる自圧式の液減圧弁に
よつて減圧した上、蒸発器にて気化させ、圧力調
整器を介して調圧して消費先に供給するのが一般
的であつた。
Conventionally, the liquefied gas is drawn out as a liquid from the bottom of the storage tank, and the pressure is reduced using a spring-based self-pressure liquid pressure reducing valve, then vaporized in an evaporator, and the pressure is regulated via a pressure regulator before being sent to the consumer. It was common to supply

この場合、蒸発器からの液化ガスが液状のまゝ
で消費先に流出するのを防止する手段としては、
オーバーロード時に上記貯槽内上層部の気相ガス
圧力を液面発信器を介して前記液減圧弁に加える
方法がとられてきたが(例えば特公昭50−16009
号公報)、このように常態において開弁方向にス
プリングが作用する構造の自圧式液減圧弁では
猶、次のような欠点があつた。
In this case, the means to prevent the liquefied gas from the evaporator from flowing out to the consumer in a liquefied state are as follows:
At the time of overload, a method has been adopted in which the gas phase gas pressure in the upper layer of the storage tank is applied to the liquid pressure reducing valve via a liquid level transmitter (for example, Japanese Patent Publication No. 50-16009).
However, the self-pressure type liquid pressure reducing valve having a structure in which a spring acts in the valve opening direction under normal conditions still has the following drawbacks.

貯槽内圧力が液減圧弁のスプリング圧以下に
低下した場合は常時開弁状態となり、蒸発器か
ら消費先えの液化ガスの流出が防止できない。
When the pressure inside the storage tank drops below the spring pressure of the liquid pressure reducing valve, the valve is always open and it is impossible to prevent the liquefied gas to be consumed from flowing out from the evaporator.

上記液減圧弁では、そのベローズ又はダイヤ
フラムが破損した場合は常時開弁状態となり、
外部えの液化ガスの流出を防止することができ
ない。
In the above liquid pressure reducing valve, if the bellows or diaphragm is damaged, the valve will remain open at all times.
It is not possible to prevent the leakage of liquefied gas from the outside.

従つて上述した従来の蒸発装置を例えばLPG
液のような可燃性ガスの蒸発に使用した場合、 (a) LPG液がそのまゝバーナー側に流出すると、
容積にして250倍のガス量に膨張するため、爆
発事故など大きな災害のもととなる。
Therefore, the above-mentioned conventional evaporator can be replaced with, for example, LPG.
When used to evaporate flammable gas such as liquid, (a) If LPG liquid flows directly to the burner side,
Because the gas expands to 250 times its volume, it can cause major disasters such as explosions.

(b) ダイヤフラムが破損した場合、LPG液が大
気中に漏洩し、前述同様250倍のガス量となる。
(b) If the diaphragm breaks, LPG liquid will leak into the atmosphere, resulting in 250 times the amount of gas as described above.

ために極めて危険であり、如何なる場合でも液
化ガスをそのまゝ消費先や装置外に流出させるこ
とのない蒸発装置が強く望まれてたものである。
Therefore, there is a strong desire for an evaporation device that does not allow the liquefied gas to leak directly to the consumer or outside the device under any circumstances.

〔問題点を解決するための手段〕[Means for solving problems]

このような実情を鑑み本発明は、この種の蒸発
装置において蒸発器からは勿論、減圧乃至調圧機
能を司るダイヤフラムが破損したような場合でも
液化ガスが液状のまゝで消費先又は装置外に流出
することを完全に防止できるようにしたものであ
る。
In view of these circumstances, the present invention provides that in this type of evaporator, even if the diaphragm that controls the pressure reduction or pressure regulation function is damaged, the liquefied gas remains liquefied and is delivered to the consumer or outside the device. It is designed to completely prevent leakage.

即ち、貯槽内の液化ガスを取出し、大気熱によ
り加熱気化させる蒸発装置において、上記貯槽と
蒸発器間の導管に閉弁スプリングを内蔵してなる
圧力調整開閉弁(以下単に「圧開弁」という)を
設置し、貯槽上層部の気相ガスをパイロツトレギ
ユレーター、絞り弁、レベルセンサー等を介して
圧開弁の上部ダイヤフラム室に加え、貯槽から取
出される液化ガスの圧力を減圧及び調圧して、蒸
発器内圧力が一定になるように構成すると共に、
蒸発器内の液化ガスの液位が上昇して、レベルセ
ンサー室内に液化ガスが流入すると、レベルセン
サーの内弁作動によつて圧開弁の上部ダイヤフラ
ム室のパイロツトガス圧を蒸発器側に逃し、圧開
弁の上部ダイヤフラム室と下部ダイヤフラム室を
同圧として圧開弁内部の閉弁スプリングにより、
弁体を閉じるようにする一方、蒸発器内の液化ガ
スの蒸発によつてレベルセンサー室内の液位が低
下すると、レベルセンサーの内弁が逆作動して蒸
発器内圧力よりも高いパイロツトガス圧が圧開弁
の上部ダイヤフラム室に加わり、下部ダイヤフラ
ム室との間に生じた差圧で上記閉弁スプリングに
抗して弁体を開くようにしたことにより、叙述の
諸問題をすべて解消したものである。
That is, in an evaporation device that extracts liquefied gas from a storage tank and heats and vaporizes it using atmospheric heat, a pressure regulating on-off valve (hereinafter simply referred to as a "pressure opening valve") that has a closing spring built into the conduit between the storage tank and the evaporator is used. ) is installed, and the gas phase gas in the upper layer of the storage tank is applied to the upper diaphragm chamber of the pressure-opening valve via the pilot regulator, throttle valve, level sensor, etc., and the pressure of the liquefied gas taken out from the storage tank is reduced and adjusted. The pressure inside the evaporator is configured to be constant, and
When the level of liquefied gas in the evaporator rises and liquefied gas flows into the level sensor chamber, the pilot gas pressure in the upper diaphragm chamber of the pressure-opening valve is released to the evaporator side by operating the inner valve of the level sensor. , the pressure-opening valve's upper diaphragm chamber and lower diaphragm chamber are at the same pressure, and the closing spring inside the pressure-opening valve
While the valve body is closed, when the liquid level in the level sensor chamber decreases due to evaporation of the liquefied gas in the evaporator, the inner valve of the level sensor operates in reverse, causing the pilot gas pressure to be higher than the pressure in the evaporator. is added to the upper diaphragm chamber of the pressure-open valve, and the differential pressure created between it and the lower diaphragm chamber opens the valve body against the valve closing spring, thereby solving all of the problems described above. It is.

〔作用〕[Effect]

本発明の液化ガス蒸発装置は、貯槽と蒸発器間
の導管に閉弁スプリングを備えた圧開弁を設けた
ことで蒸発器内の圧力が一定に保てるようにする
と共に、該圧開弁と蒸発器の出口側とをレベルセ
ンサーを介して連通し、レベルセンサー室の液位
によつて上記圧開弁の開閉を行うようにしたこと
により、如何なる場合にも液化ガスそのものの消
費先又は装置外えの流出を確実に防止し得るとい
う格別の作用を奏するものである。
The liquefied gas evaporator of the present invention has a pressure-opening valve equipped with a valve-closing spring in the conduit between the storage tank and the evaporator, so that the pressure inside the evaporator can be kept constant, and the pressure-opening valve is By communicating with the outlet side of the evaporator via a level sensor, and opening and closing the above-mentioned pressure opening valve depending on the liquid level in the level sensor chamber, the liquefied gas itself is not consumed by the consumer or equipment in any case. This has a special effect of reliably preventing the leakage of the outer shell.

〔実施例〕〔Example〕

以下、その具体的構成を図面に示す実施例に従
つて更に詳述すると、第1図において通常の状態
では後述する圧開弁8により蒸発器10内の圧力
は、予め設定された圧力Pvに調圧され、これに
伴つて蒸発器内部の液化ガスLは低温に保たれて
いる。
Hereinafter, its specific configuration will be described in more detail according to the embodiment shown in the drawings. In the normal state in FIG. The pressure is regulated, and accordingly, the liquefied gas L inside the evaporator is kept at a low temperature.

さて、上記圧開弁8は、パイロツトレギユレー
ター2により圧力P1からP2に調圧された貯槽内
の気相ガス圧力が、絞り弁3、レベルセンサー5
を介して圧開弁の上部ダイヤフラム室Aに加えら
れることによつて開弁する構造である。
Now, the pressure opening valve 8 allows the gas phase gas pressure in the storage tank, which has been regulated from pressure P 1 to P 2 by the pilot regulator 2, to the throttle valve 3 and the level sensor 5.
The valve is opened by being applied to the upper diaphragm chamber A of the pressure-opening valve via the pressure-opening valve.

即ち、第2図に示したように弁体14は閉弁ス
プリング15により常態では閉位置にあるが、上
部ダイヤフラム室Aに上記閉弁スプリング15の
上向力Fsに打勝つだけの圧力P2が加わつて初め
て開弁するものである。
That is, as shown in FIG. 2, the valve body 14 is normally in the closed position due to the valve closing spring 15, but there is a pressure P 2 in the upper diaphragm chamber A sufficient to overcome the upward force Fs of the valve closing spring 15. The valve opens only when

而して上記圧開弁8の開弁と同時に、蒸発器1
0内の圧力Pvがレベルセンサー室5′を経て下部
ダイヤフラム室Bに加わる為、一つのダイヤフラ
ム16を介して圧力P2とPvが均り合うように上
下動し、これと連動して該弁体14の開度が変化
して蒸発器内圧力Pvを常に一定に保ち得るもの
である。
At the same time as the pressure opening valve 8 is opened, the evaporator 1
Since the pressure Pv within 0 is applied to the lower diaphragm chamber B via the level sensor chamber 5', the pressures P2 and Pv move up and down through one diaphragm 16 so that they are equalized, and in conjunction with this, the valve By changing the opening degree of the body 14, the internal pressure Pv of the evaporator can be kept constant at all times.

つまり正常な状態ではP1>P2>Pv>Psとなる。 In other words, under normal conditions, P 1 > P 2 > Pv > Ps.

但し、Psは圧力調整器12の消費側出口のガ
ス圧力を示す。
However, Ps indicates the gas pressure at the consumption side outlet of the pressure regulator 12.

次に逆止弁7は、上記圧開弁8のダイヤフラム
16が上下動することにより、上部ダイヤフラム
室AのP2が変化し、それに伴つてPvが漸次高く
なることを防ぐ一方、ガスの消費が止まり蒸発器
10内の発生ガス圧力が高くなつた場合に、その
逆流によつてパイロツトガス圧P2が上昇するの
を防止する役目をも果たし、また絞り弁6は圧開
弁8の制御特性を変えるために設けられている。
Next, the check valve 7 prevents the P2 of the upper diaphragm chamber A from changing due to the vertical movement of the diaphragm 16 of the pressure-opening valve 8, and thereby preventing the Pv from gradually increasing. The throttle valve 6 also serves to prevent the pilot gas pressure P 2 from increasing due to the reverse flow when the generated gas pressure in the evaporator 10 increases due to the stoppage of the flow. It is provided to change the characteristics.

このようにして蒸発器10内の液化ガスLの圧
力は一定に制御され、そこで発生したガスは圧力
調整器12により更に調圧されて消費側出口より
消費先に送られるのである。
In this way, the pressure of the liquefied gas L in the evaporator 10 is controlled to be constant, and the gas generated therein is further pressure-regulated by the pressure regulator 12 and sent to the consumer through the consumer outlet.

しかしガス消費量の増大や外気温度の低下等、
状況の変化によつて蒸発量が不足した場合は、液
化ガスが液状のまゝレベルセンサー室5′に流入
することになるが、上記レベルセンサー5は、例
えばフロートと二方弁などによつて構成される内
弁(図示せず)を備えており、その液位を検知し
て上記内弁が作動し、貯槽1の上層部から圧開弁
8に送り込まれていたパイロツトガス圧P2をレ
ベルセンサー5、レベルセンサー室5′を通じて
蒸発器側へ逃すと同時に、圧開弁8の上部ダイヤ
フラム室Aを蒸発器10の出口側に連通させたこ
とにより、上部ダイヤフラム室A内の圧力がPv
となり、圧開弁8においてPv×S(ダイヤフラム
16に働く下向き力)<Fs+Pv×S(同じく上向
き力)の関係が成立して、直ちに該圧開弁8を閉
状態にするから、それ以降は蒸発器の液位が上ら
ず消費先に液化ガスが液状のまゝで流出する事態
を確実に阻止し得るものである。
However, due to increases in gas consumption, decreases in outside temperature, etc.
If the amount of evaporation becomes insufficient due to a change in the situation, the liquefied gas will flow into the level sensor chamber 5' in its liquefied state. The internal valve is equipped with an inner valve (not shown), which operates when the liquid level is detected, and the pilot gas pressure P 2 that was being sent from the upper part of the storage tank 1 to the pressure opening valve 8 is reduced. At the same time, by communicating the upper diaphragm chamber A of the pressure opening valve 8 with the outlet side of the evaporator 10, the pressure inside the upper diaphragm chamber A is reduced to Pv.
Therefore, the relationship of Pv×S (downward force acting on the diaphragm 16) < Fs+Pv×S (also upward force) is established in the pressure-opening valve 8, and the pressure-opening valve 8 is immediately closed. From then on, This can reliably prevent a situation in which the liquid level in the evaporator does not rise and the liquefied gas flows out to the consumer in a liquefied state.

尚、Sは圧開弁8のダイヤフラム16の有効面
積を表す。
Note that S represents the effective area of the diaphragm 16 of the pressure-opening valve 8.

他方、圧開弁8が閉止しても蒸発器10内の液
化ガスは蒸発を続けるのであるが、その消費量に
不足が生じた場合は、貯槽1内上層部の気相ガス
が別途設けられた圧力調整器13を介して消費先
に随時安定的に補給されるのである。但し、この
場合は圧力調整器13の設定圧力P13と圧力調整
器12の設定圧力P12をP12=P13+αとなるよう
に差を持たせ、通常な蒸発器10からの発生ガス
量で充分送ガス圧力Psが保てるようしておくの
である。
On the other hand, even if the pressure-opening valve 8 is closed, the liquefied gas in the evaporator 10 continues to evaporate, but if there is a shortage in its consumption, a separate gas phase gas in the upper layer of the storage tank 1 is provided. It is constantly and stably supplied to the consumer through the pressure regulator 13. However, in this case, the set pressure P 13 of the pressure regulator 13 and the set pressure P 12 of the pressure regulator 12 are set to have a difference such that P 12 = P 13 + α, and the amount of gas generated from the normal evaporator 10 is reduced. This is done so that a sufficient gas supply pressure Ps can be maintained.

而して、前述の如く圧開弁8が閉止中は蒸発ガ
ス量が不足するから、圧力調整器12の消費側出
口圧力Psも徐々に下降して、それが設定圧力P12
以下になると圧力調整器13が自動的に作動し
て、消費側出口のガス圧Psを所定圧力に保つよ
うにするものである。
As mentioned above, while the pressure opening valve 8 is closed, the amount of evaporated gas is insufficient, so the consumption side outlet pressure Ps of the pressure regulator 12 also gradually decreases, which becomes the set pressure P12 .
When the pressure falls below, the pressure regulator 13 automatically operates to maintain the gas pressure Ps at the outlet on the consumption side at a predetermined pressure.

以上要するに本発明の装置は、圧開弁8のスプ
リング15の強さFsを適当に設定することによ
り、任意に開弁条件を選択することができるし、
又万一圧開弁8のベローズ又はダイヤフラム等が
破損した場合でも、上記閉弁スプリング15の作
用により、その弁体14は確実に閉止するので、
如何なる場合にも液化ガスを液状のまゝで消費先
又は装置外に流出させることがないのである。
In summary, the device of the present invention allows the valve opening condition to be arbitrarily selected by appropriately setting the strength Fs of the spring 15 of the pressure opening valve 8.
Furthermore, even if the bellows or diaphragm of the pressure opening valve 8 is damaged, the valve element 14 will be reliably closed by the action of the valve closing spring 15.
Under no circumstances will the liquefied gas be allowed to flow out of the consumer or the equipment in its liquefied state.

更に又、上述したようにレベルセンサー室5′
に液化ガスが流入し、レベルセンサー5の作動に
よつて圧開弁8が閉止した後も蒸発器10内の液
化ガスは蒸発を続けるものであるから、その液位
は次第に降下し、レベルセンサー5が液面を検知
しなくなるとレベルセンサーの内弁作動によつて
再び蒸発器内圧力よりも高い圧力のパイロツトガ
ス圧が圧開弁8の上部ダイヤフラム室Aに加わ
り、弁体14を開いて上述した如く蒸発器内圧力
の調圧を再開するのである。
Furthermore, as mentioned above, the level sensor chamber 5'
Since the liquefied gas in the evaporator 10 continues to evaporate even after the pressure opening valve 8 is closed by the operation of the level sensor 5, the liquid level gradually decreases and the level sensor 5 no longer detects the liquid level, the pilot gas pressure higher than the evaporator internal pressure is again applied to the upper diaphragm chamber A of the pressure opening valve 8 by the inner valve operation of the level sensor, and the valve body 14 is opened. As described above, the pressure regulation within the evaporator is resumed.

この場合に蒸発器10からの送ガス量が充分で
ある時は、消費側出口のガス圧Psが圧力調整器
12の設定圧力P12まで回復し、圧力調整器13
を閉止して貯槽からの気相ガスの補給を自動的に
遮断するのである。
In this case, when the amount of gas sent from the evaporator 10 is sufficient, the gas pressure Ps at the consumption side outlet recovers to the set pressure P12 of the pressure regulator 12, and the pressure regulator 13
This automatically shuts off the replenishment of gas phase gas from the storage tank.

尚、第1図中、各部材間を結ぶ線分は導管を示
す。
In FIG. 1, the line segments connecting each member indicate conduits.

〔発明の効果〕〔Effect of the invention〕

以上の説明から明らかな如く、本発明は特に大
気熱を利用した可燃性ガス等の液化ガス蒸発装置
として一基の圧開弁8によつて、(a)蒸発ガス圧力
の制御、(b)消費先えの液化ガス流出の完全防止、
(c)ダイヤフラムの破損時における大気中えの液化
ガスの流出阻止等々の重要な役割を果たし、更に
蒸発量の低下による送ガス量の不足時には貯槽上
層部の気相ガスを自動的に補給できるという、従
来のこの種蒸発装置では得られなかつた特徴を有
する他、熱源や各部の制御に他の動力源を全く必
要としないから安全性及び経済性が極めて高く、
しかもガスの安全供給が可能である等、多くの利
点を有するものである。
As is clear from the above description, the present invention provides (a) control of evaporated gas pressure, (b) Complete prevention of liquefied gas leakage before consumption.
(c) It plays an important role in preventing the leakage of liquefied gas in the atmosphere when the diaphragm is damaged, and can also automatically replenish the gas phase gas in the upper layer of the storage tank when the amount of gas sent is insufficient due to a drop in evaporation. In addition to having features not available with conventional evaporators of this type, it is extremely safe and economical as it does not require any heat source or other power source to control each part.
Moreover, it has many advantages, such as the ability to safely supply gas.

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

第1図は本発明の液化ガス蒸発装置の系統図、
第2図は圧力調整開閉弁の縦断面図である。 尚、図中1……貯槽、2……パイロツトレギユ
レーター、3,6……絞り弁、5……レベルセン
サー、7……逆止弁、8……圧力調整開閉弁(圧
開弁)、10……蒸発器、12,13……圧力調
整器、14……弁体、15……閉弁スプリング。
FIG. 1 is a system diagram of the liquefied gas evaporator of the present invention,
FIG. 2 is a longitudinal sectional view of the pressure regulating on-off valve. In the figure, 1... Storage tank, 2... Pilot regulator, 3, 6... Throttle valve, 5... Level sensor, 7... Check valve, 8... Pressure adjustment on-off valve (pressure opening valve). , 10... Evaporator, 12, 13... Pressure regulator, 14... Valve body, 15... Valve closing spring.

Claims (1)

【特許請求の範囲】[Claims] 1 貯槽内の液化ガスを蒸発器に取出し、大気熱
によつて加熱気化させた蒸発ガスを圧力調整器を
介して消費側出口に送給するようにした液化ガス
蒸発装置において、貯槽1と蒸発器10間の導管
に閉弁スプリング15を内蔵してなる圧力調整開
閉弁8を設置し、上記貯槽の上層部からの導管の
一つはパイロツトレギユレーター2、絞り弁3お
よび内弁を備えてなるレベルセンサー5を介して
上記圧力調整開閉弁の上部ダイヤフラム室Aと連
通させ、他の導管末端は別の圧力調整器13を経
て消費側出口に臨ませる一方、上記蒸発器の出口
側はレベルセンサー室5′を介してレベルセンサ
ー5と、またレベルセンサー室は上記圧力調整開
閉弁の下部ダイヤフラム室Bとそれぞれ連通せし
め、更に上部ダイヤフラム室と蒸発器の出口側を
結ぶ導管に逆止弁7及び絞り弁6を配設したこと
を特徴とする大気熱を利用した液化ガス蒸発装
置。
1 In a liquefied gas evaporator that extracts liquefied gas in a storage tank to an evaporator, heats and vaporizes the gas using atmospheric heat, and sends the evaporated gas to a consumer outlet via a pressure regulator, the storage tank 1 and the evaporator are connected to each other. A pressure regulating on-off valve 8 with a built-in valve closing spring 15 is installed in the conduit between the containers 10, and one of the conduits from the upper layer of the storage tank is equipped with a pilot regulator 2, a throttle valve 3, and an inner valve. It communicates with the upper diaphragm chamber A of the pressure regulating on-off valve through a level sensor 5 consisting of a The level sensor chamber 5' communicates with the level sensor 5, and the level sensor chamber communicates with the lower diaphragm chamber B of the pressure regulating on-off valve, and a check valve is connected to the conduit connecting the upper diaphragm chamber and the outlet side of the evaporator. 7 and a throttle valve 6.
JP57114327A 1982-06-30 1982-06-30 Liquefied gas evaporation device utilizing atmospheric heat Granted JPS596498A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57114327A JPS596498A (en) 1982-06-30 1982-06-30 Liquefied gas evaporation device utilizing atmospheric heat

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57114327A JPS596498A (en) 1982-06-30 1982-06-30 Liquefied gas evaporation device utilizing atmospheric heat

Publications (2)

Publication Number Publication Date
JPS596498A JPS596498A (en) 1984-01-13
JPH0219359B2 true JPH0219359B2 (en) 1990-05-01

Family

ID=14635043

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57114327A Granted JPS596498A (en) 1982-06-30 1982-06-30 Liquefied gas evaporation device utilizing atmospheric heat

Country Status (1)

Country Link
JP (1) JPS596498A (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS61282699A (en) * 1985-06-06 1986-12-12 Sumitomo Light Metal Ind Ltd Liquefied gas vaporizing device
JP2008008330A (en) * 2006-06-27 2008-01-17 Iwatani Internatl Corp Liquefied gas filling device

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ES425624A1 (en) * 1973-05-14 1976-06-16 Union Special Corp IMPROVEMENTS INTRODUCED IN A DRIVING INSTALLATION FOR SEWING MACHINES.

Also Published As

Publication number Publication date
JPS596498A (en) 1984-01-13

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