JPH0243078B2 - - Google Patents
Info
- Publication number
- JPH0243078B2 JPH0243078B2 JP10094481A JP10094481A JPH0243078B2 JP H0243078 B2 JPH0243078 B2 JP H0243078B2 JP 10094481 A JP10094481 A JP 10094481A JP 10094481 A JP10094481 A JP 10094481A JP H0243078 B2 JPH0243078 B2 JP H0243078B2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- low
- liquefied gas
- temperature liquefied
- liquid
- 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
Links
- 239000007788 liquid Substances 0.000 claims description 53
- 238000000034 method Methods 0.000 claims description 8
- 230000001681 protective effect Effects 0.000 claims description 8
- 230000005540 biological transmission Effects 0.000 claims description 4
- 238000001816 cooling Methods 0.000 description 10
- 238000004781 supercooling Methods 0.000 description 8
- 238000003780 insertion Methods 0.000 description 5
- 230000037431 insertion Effects 0.000 description 5
- 238000012546 transfer Methods 0.000 description 5
- 230000007423 decrease Effects 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000001704 evaporation Methods 0.000 description 3
- 238000013459 approach Methods 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 230000035515 penetration Effects 0.000 description 2
- 239000012779 reinforcing material Substances 0.000 description 2
- 239000006200 vaporizer Substances 0.000 description 2
- 238000003466 welding Methods 0.000 description 2
- 230000008602 contraction Effects 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 230000000149 penetrating effect Effects 0.000 description 1
- 230000003014 reinforcing effect Effects 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS 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
- F17C9/00—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS 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
- F17C2201/00—Vessel construction, in particular geometry, arrangement or size
- F17C2201/01—Shape
- F17C2201/0128—Shape spherical or elliptical
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS 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
- F17C2203/00—Vessel construction, in particular walls or details thereof
- F17C2203/06—Materials for walls or layers thereof; Properties or structures of walls or their materials
- F17C2203/0602—Wall structures; Special features thereof
- F17C2203/0612—Wall structures
- F17C2203/0626—Multiple walls
- F17C2203/0629—Two walls
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS 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
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/0323—Valves
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS 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
- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
- F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
- F17C2223/0146—Two-phase
- F17C2223/0153—Liquefied gas, e.g. LPG, GPL
- F17C2223/0161—Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
- F17C—VESSELS 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
- F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
- F17C2223/04—Handled 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
- F17C2223/042—Localisation of the removal point
- F17C2223/046—Localisation of the removal point in the liquid
- F17C2223/047—Localisation of the removal point in the liquid with a dip tube
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】
本発明はタンク内に貯液された低温液化ガスを
損失を低減して効果的に送液する方法とそれを実
施するための送液装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for effectively transporting low-temperature liquefied gas stored in a tank while reducing loss, and a liquid transport device for carrying out the method.
例えば、第1図に例示した送液系統によりタン
クT内の低温液化ガスを長距離の低温液化ガス送
液管4を介して使用先に送液する場合、通常、該
送液管4は大気の侵入熱を受けて昇温しているの
で、タンクTの元弁3、使用先の弁6を開けてい
きなり送液したのでは、送液途中での蒸発によつ
て低温液化ガス送液管4の配管抵抗が増大し、こ
れに伴つて流速も低下するため送液量が減少す
る。そこで、一般には、送液に先だつてタンクT
の元弁3および低温液化ガス送液管4の終端部に
設けたブロー弁5を開けてタンクT内の低温液化
ガスを低温液化ガス導出管2、元弁3を介して低
温液化ガス送液管4に通液しブロー弁5から大気
放出することによつて該送液管4を予冷した後、
弁5を閉め、弁6を開けて送液する。このように
タンクT内の低温液化ガスは、該タンクTの底部
から順次導出し送液されるが、一方、タンクT内
の低温液化ガスは上部に近い程温度が高く、また
底部に近い程低温(過冷却)になつている。即ち
ガス層A、上層液B、下層液Cの各層の温度はA
→B→Cの順で低温となりCが最も低温で、過冷
却状態になつている。従つて、前記予冷では過冷
却状態にあるタンク下層液Cが使用され、予冷後
の送液では、より液温の高い低温液化ガスが送液
されることになるが、液温が高いと蒸発し易いの
で、液状態での使用を前堤とする使用先にとつて
は蒸発ロスが増大し不利である。そこで、使用先
には液温の低い低温液化ガスを送液することが求
められる。このため従来は、予冷前、または予冷
後に過冷却操作を行なつていた。これは、元弁
3、タンク加圧弁8を閉じた状態でタンクTに付
設されたブロー弁1を開けてタンクTの上部のガ
ス層Aを大気放出して減圧し、これによつて低温
液化ガスの一部を蒸発させて温度降下せしめた後
弁1を閉じ、次いでタンク加圧弁8を開けてタン
クT内の低温液化ガスを気化器7に導入して蒸発
させタンク内圧を送液に必要な圧力迄昇圧を行な
うものである。 For example, when the low-temperature liquefied gas in the tank T is sent to the user via the long-distance low-temperature liquefied gas sending pipe 4 using the liquid sending system illustrated in FIG. The temperature rises due to the intrusion heat of the tank T, so if you open the main valve 3 and the destination valve 6 of the tank T and suddenly transfer the liquid, the low temperature liquefied gas transfer pipe will be damaged due to evaporation during the liquid transfer. The piping resistance of No. 4 increases, and the flow rate decreases accordingly, so the amount of liquid sent decreases. Therefore, in general, the tank T is
The blow valve 5 provided at the main valve 3 and the terminal end of the low temperature liquefied gas delivery pipe 4 is opened to send the low temperature liquefied gas in the tank T through the low temperature liquefied gas outlet pipe 2 and the main valve 3. After pre-cooling the liquid sending pipe 4 by passing liquid through the pipe 4 and releasing it into the atmosphere from the blow valve 5,
Close valve 5 and open valve 6 to send the liquid. In this way, the low-temperature liquefied gas in the tank T is sequentially led out and fed from the bottom of the tank T. On the other hand, the temperature of the low-temperature liquefied gas in the tank T is higher as it approaches the top, and as it approaches the bottom, the temperature of the low-temperature liquefied gas in the tank T is higher. The temperature has become low (supercooled). That is, the temperature of each layer of gas layer A, upper layer liquid B, and lower layer liquid C is A
The temperature decreases in the order of →B →C, and C is the lowest temperature and is in a supercooled state. Therefore, in the pre-cooling, the tank bottom liquid C in a supercooled state is used, and in the liquid transfer after pre-cooling, low-temperature liquefied gas with a higher liquid temperature is transferred, but if the liquid temperature is high, it will evaporate. Therefore, it is disadvantageous for applications where liquid state is used as a forebank because evaporation loss increases. Therefore, it is required to send low-temperature liquefied gas with a low liquid temperature to the place of use. For this reason, conventionally, a supercooling operation was performed before or after precooling. This is done by opening the blow valve 1 attached to the tank T with the main valve 3 and tank pressurizing valve 8 closed, releasing the gas layer A at the top of the tank T to the atmosphere and reducing the pressure. After evaporating a portion of the gas to lower the temperature, close the valve 1, then open the tank pressurization valve 8, introduce the low temperature liquefied gas in the tank T to the vaporizer 7, evaporate it, and raise the tank internal pressure necessary for liquid delivery. The pressure is increased to a certain level.
このように、従来は液温の低い低温液化ガスを
送液するため、予冷の前後に前記過冷却操作を行
なつているが、該操作のため低温液化ガスの一部
を損失することとなり不経済であるばかりでな
く、過冷却操作のための繁雑な作業と一定の時間
を要する不都合が避けられない。また、予冷後に
過冷却操作を行なうと、この間に予冷済みの低温
液化ガス送液管が再び昇温してくるので再度の予
冷が必要になる。 In this way, conventionally, in order to send low-temperature liquefied gas with a low liquid temperature, the above-mentioned supercooling operation is performed before and after pre-cooling, but this operation results in a loss of a part of the low-temperature liquefied gas, making it unnecessary. This is not only economical, but also requires complicated work and a certain amount of time for the supercooling operation. Furthermore, if a supercooling operation is performed after precooling, the temperature of the precooled low-temperature liquefied gas feeding pipe will rise again during this period, so precooling will be required again.
本発明は前記不都合に鑑み提案されたもので、
その特徴は、タンク内に貯液された低温液化ガス
を低温液化ガス送液管を介して使用先へ送液する
にあたり、低温液化ガス送液管の予冷をタンク上
部のガス層又は上層液を導出して行なつた後タン
ク底部の下層液を送液する方法、及び低温液化ガ
スタンクの垂直方向のほぼ中間の位置でタンク内
外槽を気密に貫通する保護管に、外槽側から挿着
した低温液化ガス導出管と、内槽側から挿通し駆
動装置からの動力を受ける動力伝達部とタンク内
部に開口した吸込口とを有するL字状吸込管と
を、前記保護管内でスイーベル継手等の可動式接
手を介して連設し、前記駆動装置を操作すること
によつて吸込口がタンク内の任意の高さに位置さ
せられる送液装置である。 The present invention was proposed in view of the above-mentioned disadvantages.
The feature is that when the low-temperature liquefied gas stored in the tank is sent to the user via the low-temperature liquefied gas pipe, the low-temperature liquefied gas pipe is pre-cooled by the gas layer or upper liquid layer at the top of the tank. After the liquid is drawn out, the lower liquid at the bottom of the tank is sent, and the liquid is inserted from the outer tank side into a protective tube that airtightly penetrates the tank's inner and outer tanks at approximately the vertical midpoint of the low-temperature liquefied gas tank. A low-temperature liquefied gas outlet pipe, an L-shaped suction pipe that is inserted from the inner tank side and has a power transmission part that receives power from the drive device, and a suction port that opens inside the tank are connected by a swivel joint or the like in the protective pipe. This liquid feeding device is connected via a movable joint, and the suction port can be positioned at an arbitrary height within the tank by operating the drive device.
そして、本発明によれば、上述の如く送液管の
予冷をタンク内上部のガス層または上層液を導出
して行なうので、下層液を用いて予冷する従来方
法より予冷後の送液管の温度は高くなつており、
前記予冷後に下層液を流すことによつて送液管は
更に冷却されるが、温度が高くなつているとはい
つても、予冷前よりかなりの低温になつているの
で、最初から下層液を用いる従来方法より送液管
の冷却に使用される下層液の量が大幅に減少す
る。 According to the present invention, as described above, the liquid pipe is pre-cooled by drawing out the gas layer or the upper liquid in the upper part of the tank. The temperature is rising;
The liquid sending pipe is further cooled by flowing the lower layer liquid after the pre-cooling, but even though the temperature is high, it is still considerably lower than before pre-cooling, so it is necessary to flow the lower layer liquid from the beginning. The amount of lower liquid used for cooling the liquid pipe is significantly reduced compared to the conventional method used.
先ず本発明の送液装置を第2図に一実施例を例
示して説明するとタンクTは内槽9、外槽10で
構成され、内外槽9,10間は断熱施工されてお
り、該タンクTの垂直方向のほぼ中間の位置に、
保護管11がタンク内槽9、タンク外槽10を溶
接等により、気密に貫通して取り付けられてい
る。保護管11の肉厚は大気の熱をタンク内へ侵
入し難くするため、機械的強度が許す範囲で薄く
することが好ましく、又必要によつては前記内槽
9が低温液化ガスと接触して生ずる伸縮に対し保
護管11の一部をフレキシブルな構造とすること
もできる。又保護管11の外槽側端部には、低温
液化ガス導出管20が貫通し、かつ挿着部18に
溶接等により固定されている。この低温液化ガス
導出管20は、保護管11内でスイーベル接手1
5等の可動式接手を介して吸込管14と連設さ
れ、該管14は導出管20に対して自由に回動で
きるよう構成する。 First, the liquid transfer device of the present invention will be explained by illustrating one embodiment in FIG. At approximately the midpoint in the vertical direction of T,
A protective tube 11 is attached to the tank inner tank 9 and the tank outer tank 10 by penetrating the tank inner tank 9 and the tank outer tank 10 in an airtight manner by welding or the like. The thickness of the protective tube 11 is preferably as thin as its mechanical strength allows, in order to make it difficult for atmospheric heat to enter the tank. A part of the protective tube 11 can also be made to have a flexible structure to withstand expansion and contraction that occurs. A low temperature liquefied gas outlet pipe 20 passes through the outer tank side end of the protective tube 11 and is fixed to the insertion portion 18 by welding or the like. This low-temperature liquefied gas outlet pipe 20 is connected to the swivel joint 1 in the protection pipe 11.
It is connected to the suction pipe 14 via a movable joint such as No. 5, and the pipe 14 is configured to be freely rotatable with respect to the outlet pipe 20.
吸込管14は、内槽側から前記保護管11を挿
通して、挿通部19にパツキン等により、回動自
在にてシールされていると共にタンク内部の先端
に吸込口13を有し、該吸込口13がタンクの内
槽9と接触せずかつタンク内の低温液化ガスのガ
ス層から下層液まで吸込できる適当な位置で約直
角に曲げられてL字状となつている。又吸込管1
4には内槽9とスイーベル接手15との間に動力
伝達部としての歯車16が設けられ、駆動装置1
7により回動する。即ち吸込管14に固着されて
いる歯車16は小歯車22に噛合し、小歯車22
は駆動装置17のロツド23に固着され、ロツド
23は保護管11を貫通部24で貫通し、外部に
ハンドル25が取り付けられてなり、ハンドル2
5を回動すると、ロツド23は貫通部24に支承
されて回転し、これにより小歯車22が回転して
歯車16が回転される。従つて吸込管14はスイ
ーベル接手15と挿通部19に支承されて回転
し、吸込口13を任意の高さに位置させることが
でき、低温液化ガスのガス層から下層液まで吸込
むことが可能となる。 The suction pipe 14 is inserted through the protection pipe 11 from the inner tank side, is rotatably sealed in the insertion part 19 with a gasket, etc., and has a suction port 13 at the tip inside the tank. The opening 13 is bent approximately at a right angle to form an L-shape at an appropriate position that does not contact the inner tank 9 of the tank and can suck in the lower liquid from the gas layer of low-temperature liquefied gas in the tank. Also suction pipe 1
4 is provided with a gear 16 as a power transmission section between the inner tank 9 and the swivel joint 15, and the drive device 1
It rotates by 7. That is, the gear 16 fixed to the suction pipe 14 meshes with the pinion 22.
is fixed to a rod 23 of the drive device 17, the rod 23 passes through the protective tube 11 at a penetration part 24, and a handle 25 is attached to the outside.
5, the rod 23 is supported by the through portion 24 and rotates, thereby rotating the small gear 22 and rotating the gear 16. Therefore, the suction pipe 14 is supported by the swivel joint 15 and the insertion part 19 and rotates, and the suction port 13 can be positioned at an arbitrary height, making it possible to suck in the low-temperature liquefied gas from the gas layer to the lower layer liquid. Become.
本実施例では、吸込管14の回転をハンドル2
5により手動にて操作しているが、該ハンドル2
5をタンクに付属している液面計と連動させ液面
の低下に応じて吸込口13が下がるような機構と
することも可能である。又動力伝達部としての前
記歯車16はベルト、チエーン、リンク機構等に
よつても可能である。なお21は吸込管14を補
強するための補強材である。 In this embodiment, the rotation of the suction pipe 14 is controlled by the handle 2.
5, but the handle 2
It is also possible to have a mechanism in which the suction port 13 is lowered in accordance with the drop in the liquid level by linking the pump 5 with a liquid level gauge attached to the tank. Further, the gear 16 as a power transmission unit can also be formed by a belt, a chain, a link mechanism, or the like. Note that 21 is a reinforcing material for reinforcing the suction pipe 14.
上述の如く構成された本発明のタンク装置によ
る低温液化ガスの送液方法を第3図を用いて説明
する。なお第1図又は第2図と同一構成部分につ
いては同一符号を付して説明を省略する。 A method for feeding low-temperature liquefied gas using the tank device of the present invention configured as described above will be described with reference to FIG. Components that are the same as those in FIG. 1 or FIG. 2 are designated by the same reference numerals and their explanations will be omitted.
まず吸込口13をタンク上部のガス層Aに向け
た状態で弁3、弁5を開けて低温液化ガス送液管
4を予冷し、引き続き吸込口13を次第に下げて
低温液化ガスの上層液Bに位置させて更に予冷を
続け、予冷終了後に吸込口13をタンク底部に向
けた後弁6を開け、弁5を閉じて送液を開始す
る。なお上記方法で上層液Bを導出して予冷を開
始してもよく、この場合にはガス層Aを導出して
予冷を開始するのに比べ若干の寒冷の有効利用は
劣るが予冷時間を短縮できる利点がある。 First, with the suction port 13 facing the gas layer A at the top of the tank, open the valves 3 and 5 to pre-cool the low-temperature liquefied gas liquid supply pipe 4, and then gradually lower the suction port 13 to lower the low-temperature liquefied gas upper layer liquid B. After the precooling is completed, the suction port 13 is directed toward the bottom of the tank, the valve 6 is opened, and the valve 5 is closed to start liquid feeding. Note that the above method may be used to derive the upper layer liquid B and start precooling. In this case, the effective use of cold is slightly less than when the gas layer A is derived and precooling is started, but the precooling time is shortened. There are advantages that can be achieved.
このように予冷後の送液開始時には吸込口13
をタンク底部に向け、タンク内の低温液化ガスの
うち最低温(過冷却)に維持されている下層液を
はじめて送液することになるので送液される低温
液化ガスの過冷度は充分であり受入れ先に液状態
を保持して給送される。 In this way, when starting liquid feeding after pre-cooling, the suction port 13
Since the lower layer liquid, which is maintained at the lowest temperature (supercooled) of the low-temperature liquefied gas in the tank, is sent to the bottom of the tank, the degree of supercooling of the low-temperature liquefied gas being sent is sufficient. The liquid is maintained in a liquid state and delivered to the receiving destination.
以上述べた通り本発明に係る低温液化ガスの送
液方法によれば従来のタンク底部よりのみ抽出す
る送液方法で必要とされた過冷却操作を省略可能
としたので、この結果低温液化ガスの損失を無く
すと共に従来の過冷却操作に伴う繁雑な作業及び
作業時間を無くすことができる。更に過冷却操作
によつて生じていた低温液化ガス送液管の予冷中
断という状態を無くしスムーズな一連の簡単な操
作によつて低温液化ガスを充分液状態を保持して
送給先に送液することができるので、その経済的
効果が大なると共に実用上優れた利点がある。な
お上述の如き効果は低温液化ガス送液管が長い程
著しい効果を示すが、該送液管が短距離の場合で
あつても、該送液管の予冷が必要な場合には同様
な効果がある。 As described above, according to the method of sending low-temperature liquefied gas according to the present invention, it is possible to omit the supercooling operation required in the conventional method of sending liquid that extracts only from the bottom of the tank. Loss can be eliminated, as well as the complicated work and work time associated with conventional supercooling operations. Furthermore, the pre-cooling interruption of the low-temperature liquefied gas delivery pipe that occurs due to supercooling operations is eliminated, and the low-temperature liquefied gas is maintained in a sufficiently liquid state and sent to the destination through a series of smooth and simple operations. Therefore, it has great economical effects and excellent practical advantages. The effect described above is more pronounced as the low-temperature liquefied gas pipe is longer, but even if the pipe is short, the same effect can be obtained if pre-cooling of the pipe is required. There is.
第1図は従来の送液方法を説明するためのフロ
ーシート図、第2図は本発明の一実施例を示す送
液装置を取り付けた状態を示すタンクの断面図、
第3図は本発明の送液方法を説明するためのフロ
ーシート図である。
1,3,5,6,8は弁、2,20は低温液化
ガス導出管、4は低温液化ガス送液管、7はタン
ク気化器、9はタンク内槽、10はタンク外槽、
11は保護管、12,24は貫通部、13は吸込
口、14は吸込管、15はスイーベル接手、16
は歯車、17は歯車駆動装置、18は挿着部、1
9は挿通部、21は補強材、22は小歯車、23
はロツド、25はハンドル、Tはタンク、Aはガ
ス層、Bは上層液、Cは下層液である。
FIG. 1 is a flow sheet diagram for explaining a conventional liquid feeding method, and FIG. 2 is a sectional view of a tank showing a state in which a liquid feeding device according to an embodiment of the present invention is attached.
FIG. 3 is a flow sheet diagram for explaining the liquid feeding method of the present invention. 1, 3, 5, 6, 8 are valves, 2, 20 are low temperature liquefied gas outlet pipes, 4 is low temperature liquefied gas feed pipe, 7 is a tank vaporizer, 9 is a tank inner tank, 10 is a tank outer tank,
11 is a protection tube, 12 and 24 are penetration parts, 13 is a suction port, 14 is a suction pipe, 15 is a swivel joint, 16
1 is a gear, 17 is a gear drive device, 18 is an insertion part, 1
9 is an insertion part, 21 is a reinforcing material, 22 is a small gear, 23
is the rod, 25 is the handle, T is the tank, A is the gas layer, B is the upper liquid, and C is the lower liquid.
Claims (1)
化ガス送液管を介して使用先へ送液するにあた
り、低温液化ガス送液管の予冷をタンク上部のガ
ス層又は上層液を導出して行なつた後タンク底部
の下層液を送液することを特徴とするタンク内に
貯液された低温液化ガスの送液方法。 2 低温液化ガスタンクの垂直方向のほぼ中間の
位置でタンク内外槽を気密に貫通する保護管に、
外槽側から挿着した低温液化ガス導出管と、内槽
側から挿通し駆動装置からの動力を受ける動力伝
達部とタンク内部に開口した吸込口とを有するL
字状吸込管とを、前記保護管内でスイーベル継手
等の可動式接手を介して連接し、前記駆動装置を
操作することによつて吸込口がタンク内の任意の
高さに位置させられることを特徴とするタンク内
に貯液された低温液化ガスの送液装置。[Claims] 1. When sending the low-temperature liquefied gas stored in a tank to a user via a low-temperature liquefied gas pipe, the low-temperature liquefied gas pipe is pre-cooled by a gas layer at the top of the tank or 1. A method for transferring low-temperature liquefied gas stored in a tank, which comprises drawing out the upper layer liquid and then transferring the lower layer liquid at the bottom of the tank. 2. A protective tube that airtightly penetrates the tank's inner and outer tanks at approximately the vertical midpoint of the low-temperature liquefied gas tank.
L having a low temperature liquefied gas outlet pipe inserted from the outer tank side, a power transmission part inserted from the inner tank side and receiving power from the drive device, and a suction port opened inside the tank.
The suction port can be positioned at any height within the tank by connecting the letter-shaped suction pipe through a movable joint such as a swivel joint within the protection pipe and operating the drive device. Features: A liquid delivery device for low-temperature liquefied gas stored in a tank.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56100944A JPS585597A (en) | 1981-06-29 | 1981-06-29 | Method of delivering low-temperature liquefied gas stored in tank and device for it |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP56100944A JPS585597A (en) | 1981-06-29 | 1981-06-29 | Method of delivering low-temperature liquefied gas stored in tank and device for it |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS585597A JPS585597A (en) | 1983-01-12 |
| JPH0243078B2 true JPH0243078B2 (en) | 1990-09-27 |
Family
ID=14287455
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP56100944A Granted JPS585597A (en) | 1981-06-29 | 1981-06-29 | Method of delivering low-temperature liquefied gas stored in tank and device for it |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS585597A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS59122498U (en) * | 1983-02-04 | 1984-08-17 | 石川島播磨重工業株式会社 | Liquid extraction device inside the tube |
| JPS6382899U (en) * | 1986-11-18 | 1988-05-31 |
-
1981
- 1981-06-29 JP JP56100944A patent/JPS585597A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS585597A (en) | 1983-01-12 |
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