JPS6228356B2 - - Google Patents
Info
- Publication number
- JPS6228356B2 JPS6228356B2 JP7633379A JP7633379A JPS6228356B2 JP S6228356 B2 JPS6228356 B2 JP S6228356B2 JP 7633379 A JP7633379 A JP 7633379A JP 7633379 A JP7633379 A JP 7633379A JP S6228356 B2 JPS6228356 B2 JP S6228356B2
- Authority
- JP
- Japan
- Prior art keywords
- gas
- air
- filling
- insulating material
- inert gas
- 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
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
- F17C3/00—Vessels not under pressure
- F17C3/02—Vessels not under pressure with provision for thermal insulation
-
- 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
- F17C2201/0104—Shape cylindrical
- F17C2201/0109—Shape cylindrical with exteriorly curved end-piece
-
- 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
- F17C2201/0104—Shape cylindrical
- F17C2201/0119—Shape cylindrical with flat end-piece
-
- 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
- F17C2203/03—Thermal insulations
- F17C2203/0304—Thermal insulations by solid means
- F17C2203/0329—Foam
-
- 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
- F17C2203/03—Thermal insulations
- F17C2203/0304—Thermal insulations by solid means
- F17C2203/0337—Granular
- F17C2203/0341—Perlite
-
- 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
- F17C2205/0341—Filters
-
- 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
- F17C2221/00—Handled fluid, in particular type of fluid
- F17C2221/01—Pure fluids
- F17C2221/014—Nitrogen
-
- 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
Landscapes
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (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>
この発明はLNG等の低温液貯蔵用の二重殻低
温タンクの内外槽の建造後、該内外槽間に保冷材
を充填するに際し、現地にて原石を焼成して得た
発泡保冷材をガス輸送して充填するようにした保
冷材充填方法に関する発明であり、特に、原石焼
成後の発泡保冷材をN2等の不活性ガスにてガス
輸送して充填すると共に内外槽間の空気と不活性
ガスを同時併行裡に経時的に置換していくように
した二重殻低温タンクの保冷材充填方法に係る発
明である。[Detailed Description of the Invention] <Industrial Application Field> This invention is applicable to on-site construction when filling cold insulation material between the inner and outer tanks after constructing the inner and outer tanks of a double-shell cryogenic tank for storing low-temperature liquids such as LNG. This invention relates to a cold insulating material filling method in which the foamed cold insulating material obtained by firing the raw stone is filled by gas transport, and in particular, the foamed cold insulating material after firing the raw stone is filled with an inert gas such as N2 . This invention relates to a method for filling a double-shell low-temperature tank with a cold insulator, in which gas is transported and filled, and air and inert gas between the inner and outer tanks are simultaneously replaced over time.
<従来技術>
周知の如く、LNG等の低温液化ガス類の低温
液の貯蔵タンクとしては所謂二重殻低温タンクが
用いられているが、該種二重殻低温タンクにおい
ては外気温度と貯蔵液温度との温度差が極めて大
きいため、二重殻を成す内外槽間に保冷材を充填
介装するようにされている。<Prior art> As is well known, so-called double-shell cryogenic tanks are used as storage tanks for low-temperature liquids such as LNG and other low-temperature liquefied gases. Since the temperature difference is extremely large, a cold insulating material is filled and interposed between the inner and outer tanks forming a double shell.
而して、該保冷材には種々のものが用いられて
いるが、充填手段、充填率等の施工能率の条件や
断熱性、耐火性、軽量性、低温収縮率の小さいこ
と等の種々の優れた点においてパーライト等の発
泡保冷材が採用される場合が多い。 Various types of cold insulation materials are used, and various conditions such as filling means, filling rate, etc., construction efficiency, heat insulation, fire resistance, lightness, low low-temperature shrinkage, etc. Foamed cold insulation materials such as perlite are often used due to their superior properties.
而して、該パーライト等の発泡保冷材の充填に
際してはコスト、変成防止、作業能率等の点を勘
案し、通常現場発泡充填方式が用いられ、第1図
に示す様に、原石を焼成装置1にて焼成して発泡
させ、ガス輸送装置2でパイプにより空気輸送さ
れ、二重殻低温タンク3の内外槽6,7間に図示
しない周回ノズルを介して充填されるようにさ
れ、輸送空気はマンホール4からフイルタ5を通
して外気へ放出されるようにされている。 When filling with foamed cold insulating materials such as perlite, an on-site foam filling method is usually used, taking into consideration cost, prevention of metamorphosis, and work efficiency. 1, the air is transported through a pipe through a gas transport device 2, and the space between the inner and outer tanks 6 and 7 of the double-shell low-temperature tank 3 is filled through a circular nozzle (not shown). is discharged from the manhole 4 through the filter 5 to the outside air.
<発明が解決しようとする問題点>
ところで、二重殻低温タンク3の建造後の内外
槽6,7間には当然のことながら、空気が介在さ
れていることにより、そのままでは運転中におい
て低温化に伴い、介在空気中の水分が結露したり
するデメリツトがあるため、発泡保冷材の充填
後、N2ガス等の不活性ガスを内外槽6,7間に
送給して空気を追い出して置換するようにされて
いる。<Problems to be Solved by the Invention> By the way, as a matter of course, air is interposed between the inner and outer tanks 6 and 7 after construction of the double-shell cryogenic tank 3, so that the temperature will remain low during operation. Because of this, there is a disadvantage that moisture in the intervening air may condense, so after filling the foam cold insulation material, inert gas such as N 2 gas is sent between the inner and outer tanks 6 and 7 to expel the air. It is intended to be replaced.
しかしながら、従来は、例えば、内外槽6,7
間の底部にN2ガスの送給パイプ8を敷設する等
するため、極めてコスト高になる不利点があり、
又、パーライト等の充填後の置換がし難い難点が
あり、内槽外面にグラスウールのライニング等を
行う場合、該グラスウールに沿つてN2ガスがバ
イパスして逸散してしまうという欠点があつた。 However, conventionally, for example, the inner and outer tanks 6, 7
Since the N 2 gas supply pipe 8 is installed at the bottom of the gap, there is a disadvantage that the cost is extremely high.
In addition, it is difficult to replace after filling with pearlite, etc., and when the outer surface of the inner tank is lined with glass wool, the N2 gas bypasses and dissipates along the glass wool. .
この発明の目的は上述従来技術に基づく低温液
貯蔵タンクの内外槽内保冷材充填に伴う空気と不
活性ガスとの置換の問題点を解決すべき技術的課
題とし、原石を現場で焼成して発泡充填する利点
を生かし、充填手段に用いるガス輸送を従来の空
気輸送に代えてN2ガス等の不活性ガスを用いる
ことにより、輸送手段と空気置換を同時に行うこ
とが出来るようにしてエネルギー産業におけるタ
ンク技術利用分野に益する優れた二重殻低温タン
クの保冷材充填方法を提供せんとするものであ
る。 The purpose of this invention is to solve the technical problem of replacing air with inert gas when filling the inner and outer walls of a low-temperature liquid storage tank with cold insulating material based on the above-mentioned conventional technology, and to solve the problem by firing raw stones on-site. By taking advantage of the advantages of foam filling and using an inert gas such as N 2 gas instead of the conventional air transport for the gas transport used as a filling means, it is possible to perform transport means and air replacement at the same time, thereby improving the energy industry. The purpose of this invention is to provide an excellent method for filling a double-shell cryogenic tank with cold insulation material, which is useful for the field of tank technology application.
<問題点を解決するための手段・作用>
上述目的に沿い先述特許請求の範囲を要旨とす
るこの発明の構成は前述問題点を解決するため
に、二重殻低温タンクの内槽と外槽の間に現場で
原石を焼成してパーライト等の発泡保冷材を生成
し、ガス輸送装置に移送してN2ガス供給装置か
らのN2ガス等の不活性ガスによりガス輸送して
二重殻低温タンクの内外槽間に送給し、当該プロ
セスにおいて輸送不活性ガスは内外槽間に存在す
る空気と置換するようにされ、一部の不活性ガス
は空気との混合気となつて排出され、再び保冷材
に対しガス輸送を行い、このようにして反復する
ガス輸送による保冷材充填のプロセスで排出され
る混合気内の空気の量が増加するために、排出プ
ロセスで外気に排出し、新規の不活性ガスを補給
してガス輸送に供し、かかるプロセスを反復する
ことにより、二重殻低温タンクの内外槽間に保冷
材が充填されると共に、次第に不活性ガスが空気
と置換されて充填されるようにした技術的手段を
講じたものである。<Means and operations for solving the problems> In order to solve the above problems, the structure of the present invention, which is based on the above-mentioned claims, is based on the inner tank and the outer tank of the double-shell cryogenic tank. During this process, the rough stone is fired on-site to produce a foamed cold insulating material such as perlite, which is then transferred to a gas transportation device and transported by an inert gas such as N 2 gas from an N 2 gas supply device to form a double shell. The inert gas is delivered between the outer and outer tanks of a low-temperature tank, and in this process, the transported inert gas replaces the air existing between the inner and outer tanks, and some of the inert gas is discharged as a mixture with air. , gas is transported to the cold insulation material again, and in this way, the amount of air in the mixture discharged during the process of filling the cold insulation material by repeated gas transportation increases, so it is discharged to the outside air in the discharge process, By replenishing new inert gas and supplying it for gas transport, and repeating this process, a cold insulator is filled between the inner and outer tanks of the double-shelled cryogenic tank, and the inert gas is gradually replaced with air. Technical measures have been taken to ensure that the water is filled.
<実施例>
次に、この発明の1実施例を第2,3図に従つ
て説明すれば以下の通りである。尚、第1図と同
一態様部分は同一符号を用いて説明するものとす
る。<Example> Next, an example of the present invention will be described below with reference to FIGS. 2 and 3. Note that the same parts as in FIG. 1 will be explained using the same reference numerals.
第2図に示す実施例はこの発明の原理態用を示
すものであり、焼成装置1で所定の原石を焼成し
て発泡保冷材のパーライトをガス輸送装置2′に
移送してN2ガス供給装置9からのN2ガスで二重
殻低温タンク3の内外槽6,7間にガス輸送し、
パーライト10を旋回裡に充填し、該充填プロセ
スにて輸送手段に用いたN2ガスは内外槽6,7
間に内在する空気と置換して充填され、置換され
た空気はパーライト10を輸送して空気と発泡さ
れる外に空気と混合されるN2ガスの余剰分と共
にマンホール4からフイルタ5′を通り、N2ガス
供給装置9に帰還され、この循環を繰り返し、そ
の間、環流しようとするN2ガスに浮遊するパー
ライトはフイルタ5′で濾過されて二重殻低温タ
ンク3内に残留し循環せず、所定タイミングで
N2ガスのうち循環流分をN2ガス供給装置9で大
気に放出すると共に新しいN2ガスを搬送ガスと
して補給するようにして順次空気とN2ガスを置
換しながらパーライト10を充填するようにし、
パーライト10の充填完了時においては内外槽
6,7間にN2ガスが充填されるようにする。 The embodiment shown in FIG. 2 shows the principle of the present invention, in which a predetermined raw stone is fired in a firing device 1, and pearlite, which is a foamed cold insulating material, is transferred to a gas transport device 2' to supply N2 gas. N2 gas from the device 9 is transported between the inner and outer tanks 6 and 7 of the double-shell cryogenic tank 3,
Perlite 10 is filled in a swirling manner, and the N2 gas used for transportation in the filling process is supplied to the inner and outer tanks 6 and 7.
The replaced air is filled by replacing the air existing in between, and the replaced air transports the perlite 10 and is foamed with the air.It passes from the manhole 4 through the filter 5' together with the surplus N2 gas that is mixed with the air. , the N 2 gas is returned to the N 2 gas supply device 9, and this circulation is repeated. During this period, the pearlite floating in the N 2 gas that is about to be recirculated is filtered by the filter 5' and remains in the double shell low temperature tank 3 and is not circulated. , at a given timing
The circulated portion of the N 2 gas is released into the atmosphere by the N 2 gas supply device 9, and new N 2 gas is supplied as a carrier gas, so that the pearlite 10 is filled while replacing the air and N 2 gas one by one. west,
When the filling of pearlite 10 is completed, N 2 gas is filled between the inner and outer tanks 6 and 7.
而して、第3図に示す実施例において11はパ
ーライト原石のストツカーであり、該パーライト
原石は振動フイーダ12により定量で切り出さ
れ、ベルトコンベヤ13により焼成装置1のホツ
パー14に供給され、フイーダ15からバケツト
コンベヤ16を介してフアーネス17にてバーナ
ー18により所定温度で焼成発泡されてパーライ
ト10の保冷材原料とされ、シユート19により
ガス輸送装置2′のクーリングパイプ21に移送
され、冷却されつつ該ガス輸送装置2′のサイク
ロン22に供給され、N2ガス供給装置9からの
N2ガスと図示しないブロワーを介してインジエ
クター等の適宜手段により混合装置23を介して
一種のガス輸送を行わせ、輸送パイプ24により
搬送し、二重殻低温タンク3のマンホール31内
に挿入したフレキシブルホース25から二重殻低
温タンク3の内外槽6,7間に充填し、該フレキ
シブルホース25の旋回動作により所定プロセス
でパーライト10を順次充填していく。 In the embodiment shown in FIG. 3, reference numeral 11 denotes a stocker for raw pearlite, and the raw pearlite is cut out in fixed quantities by a vibrating feeder 12, fed to a hopper 14 of a firing device 1 by a belt conveyor 13, and fed to a feeder 15. The powder is then fired and foamed at a predetermined temperature by a burner 18 in a furnace 17 via a bucket conveyor 16 to become a cold insulating material raw material for pearlite 10, and is transferred to a cooling pipe 21 of a gas transport device 2' by a chute 19, where it is being cooled. The gas is supplied to the cyclone 22 of the gas transport device 2', and is supplied from the N2 gas supply device 9.
A kind of gas transport was carried out through the mixing device 23 using N 2 gas and a blower (not shown) by an appropriate means such as an injector, and the mixture was transported through the transport pipe 24 and inserted into the manhole 31 of the double-shell cryogenic tank 3. The space between the inner and outer tanks 6 and 7 of the double-shelled low-temperature tank 3 is filled from the flexible hose 25, and perlite 10 is sequentially filled in a predetermined process by the rotating motion of the flexible hose 25.
而して、パーライト10の充填プロセスにおい
て、輸送N2ガスは内外槽6,7間に同時随伴的
に供給され、先在空気を追い出すように撹拌して
置換作用を行つて内外槽6,7間に介装される。 In the process of filling the pearlite 10, the transport N2 gas is simultaneously supplied between the inner and outer tanks 6 and 7, and is stirred and replaced to expel the pre-existing air. interposed between.
そして、N2ガスはパーライト10と共に内外
槽6,7間に充填されるが、一部の供給された
N2ガスは空気と撹拌混合され、擾乱作用を受
け、その際、浮遊するパーライト10の粒子の一
部と共にダクト4からN2ガス供給装置9の図示
しないブロワーにリターンパイプ26を介して吸
引されて二重殻低温タンク3から排出される。 Then, N2 gas is filled between the inner and outer tanks 6 and 7 together with perlite 10, but some of the supplied gas is
The N 2 gas is stirred and mixed with air and subjected to a disturbance action, and at that time, it is sucked together with some of the floating particles of pearlite 10 from the duct 4 to the blower (not shown) of the N 2 gas supply device 9 via the return pipe 26. and is discharged from the double-shell cryogenic tank 3.
ただし、該二重殻低温タンク3のダクト4に設
けたフイルタ5′の存在により吸引されるパーラ
イト10の粒子は排出されず、空気とN2ガスの
混合気のみ排出されてリターンパイプ26を通
り、N2ガス供給装置9に帰還される。 However, due to the presence of the filter 5' provided in the duct 4 of the double-shell low-temperature tank 3, the particles of perlite 10 that are sucked in are not discharged, and only the mixture of air and N2 gas is discharged and passes through the return pipe 26. , is returned to the N 2 gas supply device 9.
該N2ガス供給装置9に帰還された空気とN2ガ
ス混合気は図示しない適宜フイルタを通り、再び
ブロワー経由でインジエクターに至り、パーライ
ト10を吸引してタンク3へのガス輸送による供
給充填を再循環反復し、それを繰り返すことによ
り、パーライト10の充填を行いながら、空気と
N2ガスの置換を行う。 The air and N 2 gas mixture returned to the N 2 gas supply device 9 passes through an appropriate filter (not shown), reaches the injector via the blower again, sucks out the perlite 10, and supplies and fills the tank 3 by transporting the gas. By repeating recirculation and repeating this process, air and air are filled while filling with perlite 10.
Perform N2 gas replacement.
そのため、該置換プロセスを介して帰還する
N2ガスと空気との混合気の中に占める空気量が
次第に多くなるため、N2ガス供給装置9内の帰
還路に介装された図示しないバルブを適宜に切り
換えてダクト12′を介し大気に解放放出すると
共に、新規のN2ガスを補給して同じくパーライ
ト10の充填を行う。 Therefore, returning through the replacement process
Since the amount of air occupied in the mixture of N 2 gas and air gradually increases, a valve (not shown) installed in the return path in the N 2 gas supply device 9 is switched appropriately to supply air to the atmosphere through the duct 12'. At the same time, new N 2 gas is supplied and the same perlite 10 is charged.
このようにして、新規のN2ガス供給によるパ
ーライト10の充填、循環ガスの一部大気への間
欠解放を反復することにより、パーライト10は
連続的に供給充填され、空気とN2ガスも漸次置
換され、使用するN2ガス量は可及的に限定さ
れ、節約される。 In this way, by repeating the filling of pearlite 10 with a new supply of N 2 gas and the intermittent release of part of the circulating gas to the atmosphere, pearlite 10 is continuously supplied and filled, and air and N 2 gas are also gradually added. The amount of N 2 gas used is limited and saved as much as possible.
而して、パーライト10の所定量の充填が完了
すれば、インジエクターに対するパーライト10
の供給を停止し、N2ガスのみの供給循環、或
は、大気解放を伴う循環供給を所定時間反復する
ことにより、残留空気、未置換空気のパージを完
全に行い、最終的にN2ガス置換充填を行うよう
にする。 When the predetermined amount of pearlite 10 is filled, the pearlite 10 is filled into the injector.
By stopping the supply of N 2 gas and repeating supply circulation with only N 2 gas or circulation supply with atmospheric release for a specified period of time, residual air and unsubstituted air are completely purged, and finally N 2 gas Perform replacement filling.
尚、この発明の実施態様は上述実施例に限るも
のでないことは勿論であり、例えば、不活性ガス
はN2ガスに限ることなく他のものを用いること
も出来る。 It should be noted that the embodiments of the present invention are of course not limited to the above-mentioned embodiments, and for example, the inert gas is not limited to N 2 gas, and other gases can also be used.
<発明の効果>
以上、この発明によれば、二重殻低温タンクの
内外槽間に現場焼成で発泡した保冷材をガス輸送
充填する方法において、従来の空気輸送に代えて
N2ガス等の不活性ガスを輸送手段に用いるよう
にしたことにより、基本的に発泡保冷材の現場充
填の利点に加えて発泡材の充填後に空気に対する
不活性ガス置換という1工程を省略出来、1工程
でパーライト等の保冷材充填と空気に対する不活
性ガス置換が行え、したがつて、工期が著しく短
縮され、コスト的にも安価になる優れた効果が奏
される。<Effects of the Invention> As described above, according to the present invention, in the method of gas transporting and filling the foamed cold insulating material by on-site firing between the inner and outer tanks of a double-shelled low-temperature tank, it is possible to replace the conventional pneumatic transport.
By using inert gas such as N2 gas in the transportation means, in addition to the basic advantages of filling foam cold insulation materials on-site, it is possible to omit the step of replacing the air with inert gas after filling the foam material. , the filling of a cold insulating material such as perlite and the replacement of air with an inert gas can be carried out in one step, and therefore the construction period is significantly shortened and the cost is also reduced.
又、そのように不活性ガスを保冷材の充填の輸
送手段に用いると共に空気と置換充填させるよう
にすることが可能となることにより、従来のよう
に二重殻低温タンクの内外槽間に不活性ガス充填
用の配管設備も不要になり、その点からも工数削
減、低コスト化が図れるという優れた効果があ
る。 In addition, by using inert gas as a transportation means for filling the cold insulation material and replacing it with air, it is possible to eliminate the gap between the inner and outer tanks of a double-shelled low-temperature tank as in the past. There is no need for piping equipment for charging active gas, which also has the excellent effect of reducing man-hours and lowering costs.
そして、不活性ガスはパーライト充填時に一種
の撹拌作用を不可避的に行えることにより、空気
や不活性ガスのバイパス現象をなくし、確実に置
換を全うせる効果もある。 Furthermore, since the inert gas can unavoidably perform a kind of stirring action when filling the pearlite, it has the effect of eliminating the bypass phenomenon of air and inert gas and ensuring complete replacement.
更に、不活性ガスと空気との混合物が循環され
るため、使用する不活性ガスの可及的完全使用が
出来、その点からも安価に施工することが出来る
メリツトがある。 Furthermore, since the mixture of inert gas and air is circulated, the inert gas used can be used as completely as possible, and from this point of view, there is an advantage that construction can be carried out at low cost.
而して、不活性ガスによる保冷材の二重殻低温
タンクの内外槽間への充填を行う際に、内外槽間
に存在する一部と不活性ガスが置換され、置換に
用いられた不活性ガスは置換された空気と共に混
合気となつて排出されるプロセスを繰り返すうち
に、排出混合気の空気の量が多くなるために、そ
れを大気に放出し、新規な不活性ガスを補給して
保冷材に対するガス輸送を行うプロセスを反復す
ることにより、経時的に内外槽間に保冷材が充填
されると共に不活性ガスが空気に対して次第にそ
の置換量を増やし、経時的に空気を不活性ガスが
完全に置き換えることが出来るようにされるとい
う効果が奏される。 Therefore, when filling the space between the inner and outer tanks of a double-shelled cryogenic tank with inert gas, a part of the space between the inner and outer tanks is replaced by the inert gas, and the inert gas used for the replacement is replaced. The active gas becomes a mixture with the replaced air and is discharged. As the process is repeated, the amount of air in the discharged mixture increases, so it is released into the atmosphere and replaced with new inert gas. By repeating the process of transporting gas to the cold insulating material, the cold insulating material is filled between the inner and outer tanks over time, and the amount of inert gas replacing the air gradually increases, causing the air to become inert over time. The effect is that the active gas can be completely replaced.
加えて、発泡保冷材の輸送が不活性ガスを用い
るため、輸送中に保冷材が吸湿したり、変成した
りしないため、タンク完了後のクールダウンや運
転状態における保冷機能、タンク性能に悪影響を
与えないで済む利点もある。 In addition, since inert gas is used to transport foamed cold insulation materials, the cold insulation materials do not absorb moisture or undergo denaturation during transportation, which has a negative impact on cool-down after tank completion, cooling function during operation, and tank performance. There is also the advantage of not having to give it.
第1図は従来技術に基づく二重殻低温タンクへ
の保冷材充填の概略部分断面側面図、第2図以下
はこの発明の1実施例の説明図であり、第2図は
原理態様の実施例の概略部分断面側面図、第3図
は実施プラント部分断面図である。
3……二重殻低温タンク、7……外槽、6……
内槽、10……保冷材。
Fig. 1 is a schematic partial cross-sectional side view of filling a cold insulator into a double-shell cryogenic tank based on the prior art, Fig. 2 and the following are explanatory diagrams of one embodiment of the present invention, and Fig. 2 is an implementation of the principle aspect. FIG. 3 is a schematic partial cross-sectional side view of an example, and FIG. 3 is a partial cross-sectional view of an implementation plant. 3...Double shell low temperature tank, 7...Outer tank, 6...
Inner tank, 10... Cold insulation material.
Claims (1)
冷材を該内外槽間に充填するに際し原石を現地焼
成して発泡保冷材をガス輸送にて充填する方法に
おいて、上記原石焼成後の発泡保冷材を不活性ガ
スにてガス輸送して上記内外槽間に充填すると共
に該充填に伴つて該内外槽間の空気を該不活性ガ
スにより置換し、一部の不活性ガスと置換空気と
の混合気のみを内外槽間から排出し、排出後の混
合気で再び発泡保冷材を内外槽に輸送充填し、こ
のプロセスの反復中に排出混合気を外気に排出
し、新規の不活性ガスを補給して発泡保冷材を輸
送するようにして発泡保冷材充填完了時に不活性
ガス置換も完了するようにしたことを特徴とする
二重殻低温タンクの保冷材充填方法。1. In a method of constructing an outer tank and an inner tank of a double-shell low-temperature tank and filling a cold insulating material between the inner and outer tanks, the raw stone is fired on-site and the foamed cold insulating material is filled by gas transportation, after the raw rock is fired. The foamed cold insulating material is gas-transported using an inert gas and filled between the above-mentioned inner and outer tanks, and along with the filling, the air between the inner and outer tanks is replaced with the inert gas, and some of the inert gas is replaced. Only the mixture with air is discharged from between the inner and outer tanks, and the foamed cold insulation material is transported and filled into the inner and outer tanks again with the discharged mixture. During this process, the discharged mixture is discharged to the outside air and a new insulating material is created. A method for filling a double-shell low-temperature tank with a cold insulating material, characterized in that active gas is supplied and the foamed cold insulating material is transported so that inert gas replacement is completed when filling of the foamed cold insulating material is completed.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7633379A JPS563399A (en) | 1979-06-19 | 1979-06-19 | method of charging cold keeping material into double-shell cold tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP7633379A JPS563399A (en) | 1979-06-19 | 1979-06-19 | method of charging cold keeping material into double-shell cold tank |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS563399A JPS563399A (en) | 1981-01-14 |
| JPS6228356B2 true JPS6228356B2 (en) | 1987-06-19 |
Family
ID=13602424
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP7633379A Granted JPS563399A (en) | 1979-06-19 | 1979-06-19 | method of charging cold keeping material into double-shell cold tank |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS563399A (en) |
Families Citing this family (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS61110000U (en) * | 1984-12-24 | 1986-07-11 | ||
| JP2002224820A (en) * | 2001-02-01 | 2002-08-13 | Araco Corp | Method and device for heating magnesium chip |
| CN111928106B (en) * | 2020-07-24 | 2022-04-15 | 北京金海鑫压力容器制造有限公司 | Sand adding system and sand adding method for storage tank |
| JP2023180542A (en) * | 2022-06-09 | 2023-12-21 | 川崎重工業株式会社 | Liquefied gas tank insulation material supply device and liquefied gas tank insulation material supply method |
-
1979
- 1979-06-19 JP JP7633379A patent/JPS563399A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS563399A (en) | 1981-01-14 |
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