JPS6034261Y2 - Low temperature air supply device - Google Patents
Low temperature air supply deviceInfo
- Publication number
- JPS6034261Y2 JPS6034261Y2 JP3291479U JP3291479U JPS6034261Y2 JP S6034261 Y2 JPS6034261 Y2 JP S6034261Y2 JP 3291479 U JP3291479 U JP 3291479U JP 3291479 U JP3291479 U JP 3291479U JP S6034261 Y2 JPS6034261 Y2 JP S6034261Y2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- valve
- mixer
- pipe
- storage tank
- 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
Links
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- Thermotherapy And Cooling Therapy Devices (AREA)
Description
【考案の詳細な説明】
本考案は低温空気組成冷気を供給する、低温空気供給装
置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a low-temperature air supply device that supplies cold air with a low-temperature air composition.
近年リウマチの治療法として、あるいは機械加工の切削
刃、切断刃等を冷却するために冷気が使用されている。In recent years, cold air has been used as a treatment for rheumatism or to cool cutting blades, cutting blades, etc. in machining.
これらの冷気はその冷却効果に鑑み、極めて低い温度が
要求される。Considering the cooling effect of these cold air, extremely low temperature is required.
このため液体窒素、液体酸素、等の極低温液化ガスの利
用が考えられるが、これらの液化ガス、たとえば液体窒
素の使用に際しては、使用後の窒素ガスが室内に滞留し
て酸素欠乏を生じ、環境衛生上好ましくなく、又液体酸
素では、使用後の酸素が室内に滞留して爆発等の危険が
あり保安上好ましくない。For this reason, the use of cryogenic liquefied gases such as liquid nitrogen and liquid oxygen can be considered, but when using these liquefied gases, for example, liquid nitrogen, the nitrogen gas after use stays in the room, causing oxygen deficiency. This is unfavorable from an environmental sanitary standpoint, and liquid oxygen is unfavorable from a safety standpoint because the oxygen remains in the room after use and there is a risk of explosion.
それ故一般には大気を前記液化ガスで冷却して所望する
低温度の冷気を得ているが、周知の如く大気中の空気に
は水分あるいは炭酸ガス等が含まれ、低温度に冷却する
と、これらが凝固して配管内を閉塞せしめる不都合が生
じる。Therefore, in general, the atmosphere is cooled with the liquefied gas to obtain cold air at a desired low temperature. However, as is well known, air in the atmosphere contains moisture, carbon dioxide, etc., and when cooled to a low temperature, these This causes the inconvenience of solidification and clogging of the inside of the pipe.
このため予め不純物を除去する装置、空気を冷却するた
めの熱交換器を必要とするばかりか、冷却のための寒冷
に使用し気化したスは無駄に放出されているのが現状で
ある。For this reason, not only is a device for removing impurities in advance and a heat exchanger for cooling the air required, but the current situation is that the vaporized gas used for cooling is wasted and emitted.
本考案は上述の如き現状に鑑み提案されたもので、酸素
、窒素を空気組成に混合し、これを冷却して低温の冷気
とするものであり、この場合一方の成分を液化ガスで、
他方の成分を気体状でそれぞれ用意し、前記液化ガスを
冷却源とすると共に、冷却により生じた気化ガスを空気
組成の一方の成分ガスとして使用するようにした低温空
気供給装置である。The present invention was proposed in view of the above-mentioned current situation. Oxygen and nitrogen are mixed into the air composition and this is cooled to produce low-temperature cold air. In this case, one of the components is a liquefied gas,
In this low temperature air supply device, the other component is prepared in a gaseous state, the liquefied gas is used as a cooling source, and the vaporized gas generated by cooling is used as one component gas of the air composition.
その特徴は内外槽の間を断熱施工した断熱貯槽に液化ガ
スを充填するための弁を有する充填配管、内槽の底部よ
り気化器、圧力調整弁、遮断弁を介して内槽内環部に開
口する加圧用配管、内槽内環部より加温器を介してガス
取り出し弁に連結されているガス導出配管、更に内槽内
底部に設置してその両端部が外槽外に設けた弁にそれぞ
れ連結している冷却管よりなる冷却配管等の各系統を設
けて、空気組成ガス冷却及び空気組成ガスの一成分ガス
源とした断熱貯槽とし、該貯槽に空気組成分中の一威分
を液化ガスで充填し、該貯槽の冷却配管の一端の弁を混
合器の導出管と連結し、又貯槽のガス導出配管のガス取
り出し弁と混合器に設けた一成分導入管とを連結し、更
に混合器に設けた他方の成分導入管に他成分を導入して
、貯槽の冷害配管他方の弁より、空気組成の低温冷気を
導出し使用先に供給するようにした低温空気供給装置で
ある。Its features include a filling pipe with a valve for filling the insulated storage tank with liquefied gas, which is insulated between the inner and outer tanks, and a vaporizer, pressure adjustment valve, and shutoff valve from the bottom of the inner tank to the inner ring of the inner tank. A pressurizing pipe that opens, a gas outlet pipe that is connected from the inner ring of the inner tank to a gas take-out valve via a heater, and a valve that is installed at the bottom of the inner tank with both ends outside the outer tank. Each system, such as cooling piping, is provided with cooling pipes connected to each other to form an adiabatic storage tank that serves as a source for air-composition gas cooling and air-composition gas as a one-component gas source. is filled with liquefied gas, and the valve at one end of the cooling pipe of the storage tank is connected to the outlet pipe of the mixer, and the gas outlet valve of the gas outlet pipe of the storage tank is connected to the single-component inlet pipe provided in the mixer. In addition, other components are introduced into the other component introduction pipe installed in the mixer, and the low-temperature cold air of the air composition is drawn out from the other valve of the storage tank's cooling piping and supplied to the user. be.
以下に図面により本考案装置を詳細に説明する。The device of the present invention will be explained in detail below with reference to the drawings.
図において、1は外槽2と内槽3からなり、かつ内外槽
間4が断熱されてなる断熱貯槽、5は液化ガスを充填す
る管で、該管5は充填弁6を介して内槽3内部に開口し
ている。In the figure, 1 is an adiabatic storage tank consisting of an outer tank 2 and an inner tank 3, and the space between the inner and outer tanks 4 is insulated, and 5 is a pipe filled with liquefied gas, which is connected to the inner tank via a filling valve 6. 3 Opens inside.
7は加圧管で内槽3の底部より、前記断熱層4を通り外
槽2内壁に面して設けた気化器8、圧力調整弁9及び遮
断弁10を介して、内槽3内上部空間11に開口してい
る。Reference numeral 7 denotes a pressurizing pipe which connects from the bottom of the inner tank 3 through the heat insulating layer 4 and into the upper space inside the inner tank 3 via a vaporizer 8, a pressure regulating valve 9, and a shutoff valve 10 provided facing the inner wall of the outer tank 2. It opens at 11.
12はガス取り出し管で該管12は内槽3内上部空間1
1より断熱層4を通って外槽2の内壁に面して設置され
た加温器13を介してガス取り出し弁14に連結されて
いる。Reference numeral 12 denotes a gas extraction pipe, and the pipe 12 is connected to the upper space 1 in the inner tank 3.
1 through a heat insulating layer 4 and connected to a gas extraction valve 14 via a heater 13 installed facing the inner wall of the outer tank 2.
15は内槽3内の底部近傍に設けた冷却管で、該管15
の両端部はそれぞれ外部に設せた弁16.17にそれぞ
れ連結されている。15 is a cooling pipe provided near the bottom of the inner tank 3;
Both ends of the valves 16 and 17 are connected to external valves 16 and 17, respectively.
なお18は貯槽内の液量を検知する液面計、19は貯槽
内圧力を検知する圧力計、20は貯槽内の圧力が過度に
上昇した場合作動する安全弁、21は冷却器15内の圧
力が過剰に上昇した場合作動する安全弁である。Note that 18 is a liquid level gauge that detects the amount of liquid in the storage tank, 19 is a pressure gauge that detects the pressure in the storage tank, 20 is a safety valve that operates when the pressure in the storage tank increases excessively, and 21 is the pressure in the cooler 15. This is a safety valve that operates if the temperature rises excessively.
そして本考案装置は上述の如き断熱貯槽1に、所望する
組成の混合ガスを生皮するための一方の成分ガスを液化
ガスとして充填して、これを混合器101と以下の如く
連結したものである。In the device of the present invention, the above-described insulated storage tank 1 is filled with one of the component gases as a liquefied gas for producing a mixed gas of a desired composition, and this is connected to the mixer 101 as shown below. .
即ち断熱貯槽1のガス取り出し弁14を、混合器101
に弁102、圧力調整弁103、流量調整機構104を
介して連結されている成分ガス導入管105と管106
を介して連結し、又断熱貯槽1に設けた冷却管15に連
通ずる弁16を、混合器101よりの混合ガス導出管1
07と管108で連結する。That is, the gas take-off valve 14 of the adiabatic storage tank 1 is connected to the mixer 101.
A component gas introduction pipe 105 and a pipe 106 are connected to each other via a valve 102, a pressure adjustment valve 103, and a flow rate adjustment mechanism 104.
A valve 16 connected to the cooling pipe 15 provided in the adiabatic storage tank 1 is connected to the mixed gas outlet pipe 1 from the mixer 101.
07 through a pipe 108.
そして混合器101には混合ガスの他方の成分ガスを該
器101に導入する導入管109が弁110、圧力調整
弁111、流量調整機構112を介して設置されていて
、前記導入管109には、他方の成分ガスを充填したボ
ンベ113が管114を介して連結する。An inlet pipe 109 for introducing the other component gas of the mixed gas into the mixer 101 is installed in the mixer 101 via a valve 110, a pressure regulating valve 111, and a flow rate regulating mechanism 112. , and a cylinder 113 filled with the other component gas is connected via a pipe 114.
以上のように構成された本考案装置は次のように操作運
転される。The device of the present invention constructed as described above is operated as follows.
なお理解を容易にするため、組成分のうち窒素成分を液
化ガスとして用、い、他方の酸素成分をガス状で用いた
場合を例示して説明する。For ease of understanding, an example will be described in which a nitrogen component among the components is used as a liquefied gas, and the other oxygen component is used in a gaseous state.
まず、断熱貯槽1は混合器101と分離し独立した状態
で、生産工場等で液体窒素を次の如き態様で充填する。First, the adiabatic storage tank 1 is separated from the mixer 101 and is filled with liquid nitrogen in the following manner at a production factory or the like.
即ち、貯槽1の充填弁6を開き管5を介して内槽3内に
充填する。That is, the filling valve 6 of the storage tank 1 is opened and the inner tank 3 is filled through the pipe 5.
この時充填を容易にするためガス取り出し弁14を開き
、内槽3内が大気を連通していることが好ましく、又外
の各弁は閉止されている。At this time, in order to facilitate filling, it is preferable that the gas take-off valve 14 be opened so that the inside of the inner tank 3 is communicated with the atmosphere, and the outside valves are closed.
そして液体窒素が内槽3内に充填されたら前記充填弁6
、ガス取り出し弁を閉止し、貯槽1を適宜使用先に運搬
して、使用先に於て混合器101と前記した如き態様で
連結する。When liquid nitrogen is filled into the inner tank 3, the filling valve 6
Then, the gas take-off valve is closed, and the storage tank 1 is appropriately transported to the place of use, where it is connected to the mixer 101 in the manner described above.
なお貯槽1を運搬せずに、前記混合器101に連結した
状態に維持して、タンクローリ−等により液体窒素を運
搬して来て、液体窒素を貯槽1に充填して使用すること
も可能である。Note that it is also possible to maintain the storage tank 1 connected to the mixer 101 without transporting it, transport liquid nitrogen using a tank truck, etc., and fill the storage tank 1 with liquid nitrogen for use. be.
このように連結した後、次に断熱貯槽の加圧配管7に設
けた遮断弁10を開くと断熱貯槽内の液体窒素が底部よ
り管7で導出され気化器8で気化されて圧力調整弁9、
遮断弁10を経て内槽3内の上部空間11に導びかれ内
槽3内の圧力を高める。After connecting in this way, when the shutoff valve 10 provided on the pressurizing pipe 7 of the insulated storage tank is opened, liquid nitrogen in the insulated storage tank is led out from the bottom through the pipe 7, vaporized in the vaporizer 8, and then passed through the pressure regulating valve 9. ,
It is led to the upper space 11 inside the inner tank 3 through the shutoff valve 10 and increases the pressure inside the inner tank 3.
なお内槽3内の圧力は圧力調整弁9を適宜所望する圧力
に設定すれば、圧力調整弁9が自動的に所望圧力を保持
するよう作動する。Note that the pressure in the inner tank 3 is automatically operated to maintain the desired pressure by setting the pressure regulating valve 9 to a desired pressure.
そして所望圧力に内槽3内が高められたらガス取り出し
弁14及び冷却管15の両端部に設けた弁16.17を
開くと共に、混合器101に連通ずるそれぞれ成分のガ
ス導入管105,109に設けた弁102.110を開
く。When the pressure inside the inner tank 3 is raised to the desired pressure, the gas take-off valve 14 and the valves 16 and 17 provided at both ends of the cooling pipe 15 are opened, and the respective component gas introduction pipes 105 and 109 communicating with the mixer 101 are opened. Open the provided valves 102,110.
すると貯槽内の上部空間11の一定圧力に保持された会
素ガスは、ガス取り出し管12より加温器13を経てほ
ぼ大気温度となりガス取り出し弁14より連結管106
を介して混合器101に連通ずる導入管105に導入さ
れ、そして弁102、圧力調整弁103、流量調整機構
104を経て混合器101に所望する一定圧力に保持さ
れた一定流量の窒素ガスが供給される。Then, the nitrogen gas maintained at a constant pressure in the upper space 11 in the storage tank passes through the gas take-off pipe 12, the warmer 13, and reaches almost atmospheric temperature, and then passes through the gas take-off valve 14 through the connecting pipe 106.
Nitrogen gas is introduced into an inlet pipe 105 communicating with the mixer 101 through a valve 102, a pressure regulating valve 103, and a flow rate regulating mechanism 104, and a constant flow rate of nitrogen gas maintained at a desired constant pressure is supplied to the mixer 101. be done.
そして混合器101で該器101に別途ガスボンベ11
3より管114、導入管109、弁110、圧力調整弁
111、流量調整機構112を経て一定圧力に保持され
た一定流量で供給されてくる酸素ガスと均一に混合され
る。Then, in the mixer 101, a separate gas cylinder 11 is added to the container 101.
3, the oxygen gas is uniformly mixed with oxygen gas that is supplied at a constant flow rate maintained at a constant pressure via the pipe 114, the introduction pipe 109, the valve 110, the pressure regulating valve 111, and the flow rate regulating mechanism 112.
なお、混合器101で混合組成割合は、それぞれの導入
管105.109に設けた圧力調整弁103と111の
設定圧力を等値とし、流量調整機構104と112の流
量比率を所望する割合に調整すれば容易に所望組成の割
合が得られる(空気組成では酸素:窒素=1:4)。The mixing composition ratio in the mixer 101 is determined by setting the set pressures of the pressure regulating valves 103 and 111 provided in the respective introduction pipes 105 and 109 to the same value, and adjusting the flow rate ratio of the flow rate regulating mechanisms 104 and 112 to a desired ratio. By doing so, the desired composition ratio can be easily obtained (oxygen:nitrogen=1:4 for air composition).
又所望する圧力は圧力調整弁103と111とを所望す
る圧力値に設定すればよい。Further, the desired pressure can be obtained by setting the pressure regulating valves 103 and 111 to desired pressure values.
このようにして得られた所望する酸素、窒素空気組成混
合ガスは101より導出管107、連結管108を経て
弁16に至り、モして内槽3内に設けた冷却管15に導
びかれ、該管15で内槽3内の液体窒素で冷却されて弁
17に至り、該弁17より低温に冷却された空気組成混
合ガスの冷気として使用先に供給して適宜使用される。The desired oxygen/nitrogen/air composition mixed gas obtained in this way reaches the valve 16 via the outlet pipe 107 and the connecting pipe 108 from 101, and is then led to the cooling pipe 15 provided in the inner tank 3. It is cooled by the liquid nitrogen in the inner tank 3 through the pipe 15 and reaches the valve 17. From the valve 17, the cooled air composition mixture gas is supplied to the user as appropriate for use.
一方、前記冷却管15に流れる空気組成混合ガスを冷却
した結果液体窒素は気化し内槽3内の上部空間11に滞
留し逐次ガス取り出し管より混合器101へと供給され
混合ガスの組成の一成分として使用される。On the other hand, as a result of cooling the air composition mixed gas flowing through the cooling pipe 15, the liquid nitrogen is vaporized and retained in the upper space 11 in the inner tank 3, and is sequentially supplied to the mixer 101 from the gas extraction pipe to improve the composition of the mixed gas. used as an ingredient.
以上は酸素、窒素を空気組成分の混合ガスに混合し、こ
れを冷却して冷気として供給するに当って、窒素成分を
液体窒素とし酸素成分をガス状にした場合について説明
したが、酸素成分を液体酸素とし窒素成分をガス状とし
て行うことも出来、この場合液体酸素を本考案の断熱貯
槽に充填すればよい。The above describes the case where oxygen and nitrogen are mixed into a mixed gas of air composition, and when this is cooled and supplied as cold air, the nitrogen component is liquid nitrogen and the oxygen component is gaseous. It is also possible to use liquid oxygen as liquid oxygen and gaseous nitrogen as the nitrogen component. In this case, the liquid oxygen may be filled into the adiabatic storage tank of the present invention.
なお又、他の混合ガスを生威し、これを冷却して使用す
る場合にも同様に使倫し得る。Furthermore, it can also be used in the same way when other mixed gases are produced and used after being cooled.
本考案は以上のように貯槽内に冷却管を設けて、必要と
する空気組成ガスの冷気を1戒する寒冷として貯槽内の
液化ガスを使用すると共に、前記冷気生成のため寒冷と
して使用したがため生皮する前記液化ガスが気化したガ
スを常温で導出するようにして空気組成ガスの一成分と
して使用し得るように別の成分のガス導入管が連設され
た混合器への一成分のガス導入管に連結すると共に、混
合器よりのガス導出管を前記冷却管と連結したものであ
り、これにより、別途に寒冷剤を用意したり、又熱交換
器を必要とせず、設備が低減し得るばかりか、寒冷剤と
して生じる液化ガスの気化ガスを混合ガスの一成分とし
て有効利用し得て経済的な効果を高め、更に使用に際し
て前記した如く一成分の液化ガスを充填した貯槽を運搬
して混合器と連結するのみで極めて容易に使用が可能で
ある等の作用効果を奏する。As described above, the present invention provides a cooling pipe in the storage tank, and uses the liquefied gas in the storage tank as the cold to produce the cold air of the required air composition gas, and also uses it as the cold to generate the cold air. Therefore, the liquefied gas to be rawhide is transferred to a mixer connected to a gas inlet pipe for another component so that the vaporized gas can be discharged at room temperature and used as a component of the air composition gas. In addition to connecting to the inlet pipe, the gas outlet pipe from the mixer is connected to the cooling pipe, which eliminates the need for a separate cryogen or heat exchanger, reducing the amount of equipment required. Not only that, but also the vaporized gas of the liquefied gas produced as a cryogen can be effectively used as a component of the mixed gas, increasing the economic effect. It has the advantage of being extremely easy to use just by connecting it to a mixer.
図面は本考案装置の一実施例を示す系統図である。
1は断熱貯槽、2は外槽、3は内槽、4は断熱層、5は
充填配管、7は加圧配管、8は気化器、9は圧力調整弁
、10は遮断弁、11は内槽向上部空間、12はガス取
り出し管、13は加温器、14はガス取り出し弁、15
は冷却管、16,17は弁、101は混合器、102は
弁、103は圧力調整弁、104は流量調整機構、10
5は一成分ガス導入管、107は混合ガス導出管、10
9は他方の成分ガス導入管、110は弁、111は圧力
調整弁、112は流量調整機構、113はガスボンベで
ある。The drawing is a system diagram showing one embodiment of the device of the present invention. 1 is a heat insulating storage tank, 2 is an outer tank, 3 is an inner tank, 4 is a heat insulating layer, 5 is a filling pipe, 7 is a pressurizing pipe, 8 is a vaporizer, 9 is a pressure regulating valve, 10 is a shutoff valve, 11 is an inner tank Tank upper space, 12 a gas extraction pipe, 13 a warmer, 14 a gas extraction valve, 15
16 and 17 are cooling pipes, 101 is a mixer, 102 is a valve, 103 is a pressure regulating valve, 104 is a flow rate regulating mechanism, 10
5 is a single component gas introduction pipe, 107 is a mixed gas outlet pipe, 10
9 is the other component gas introduction pipe, 110 is a valve, 111 is a pressure regulating valve, 112 is a flow rate regulating mechanism, and 113 is a gas cylinder.
Claims (1)
下で供給するにあたり、前記成分の一方を液状で貯蔵す
る断熱貯槽1と他方をガス状で貯蔵する容器113とを
設け、前記断熱貯槽1には充填弁6を有する液化ガス充
填系統、気化器8、圧力調整弁9を有する加圧系統、ガ
ス放出弁14を有するガス導出系統ならびに冷却管15
を有する冷却系統を設け、該冷却系統の一端を供給系統
に、他端を混合器101に連設腰かつ前記ガス導出系統
と混合器101とを圧力調整弁103、流量調整機構1
04を介して連設すると共に、前記ガス容器113を圧
力調整弁111.流量調整機構112を介して混合器1
01と連設したことを特徴とする低温空気供給装置。When oxygen gas and nitrogen gas are mixed at an air composition ratio and supplied at low temperatures, an insulated storage tank 1 for storing one of the components in a liquid state and a container 113 for storing the other in a gaseous state are provided. The storage tank 1 includes a liquefied gas filling system having a filling valve 6, a vaporizer 8, a pressurizing system having a pressure regulating valve 9, a gas outlet system having a gas release valve 14, and a cooling pipe 15.
A cooling system is provided, one end of which is connected to the supply system, and the other end is connected to the mixer 101, and the gas derivation system and the mixer 101 are connected to a pressure regulating valve 103 and a flow rate regulating mechanism 1.
04, and the gas container 113 is connected to the pressure regulating valve 111. Mixer 1 via flow rate adjustment mechanism 112
A low temperature air supply device characterized by being connected to 01.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3291479U JPS6034261Y2 (en) | 1979-03-14 | 1979-03-14 | Low temperature air supply device |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3291479U JPS6034261Y2 (en) | 1979-03-14 | 1979-03-14 | Low temperature air supply device |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS55131753U JPS55131753U (en) | 1980-09-18 |
| JPS6034261Y2 true JPS6034261Y2 (en) | 1985-10-12 |
Family
ID=28887345
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3291479U Expired JPS6034261Y2 (en) | 1979-03-14 | 1979-03-14 | Low temperature air supply device |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS6034261Y2 (en) |
-
1979
- 1979-03-14 JP JP3291479U patent/JPS6034261Y2/en not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS55131753U (en) | 1980-09-18 |
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