JPS586120B2 - Method for preventing rollover of low temperature liquefied gas tank - Google Patents
Method for preventing rollover of low temperature liquefied gas tankInfo
- Publication number
- JPS586120B2 JPS586120B2 JP55039052A JP3905280A JPS586120B2 JP S586120 B2 JPS586120 B2 JP S586120B2 JP 55039052 A JP55039052 A JP 55039052A JP 3905280 A JP3905280 A JP 3905280A JP S586120 B2 JPS586120 B2 JP S586120B2
- Authority
- JP
- Japan
- Prior art keywords
- liquefied gas
- low
- temperature liquefied
- heavy
- density
- 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
- F17C13/00—Details of vessels or of the filling or discharging of vessels
- F17C13/12—Arrangements or mounting of devices for preventing or minimising the effect of explosion ; Other safety measures
- F17C13/126—Arrangements or mounting of devices for preventing or minimising the effect of explosion ; Other safety measures for large storage containers for liquefied gas
-
- 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
- F17C2201/00—Vessel construction, in particular geometry, arrangement or size
- F17C2201/05—Size
- F17C2201/052—Size large (>1000 m3)
-
- 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
- F17C2221/03—Mixtures
- F17C2221/032—Hydrocarbons
- F17C2221/033—Methane, e.g. natural gas, CNG, LNG, GNL, GNC, 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
- F17C2223/01—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
- F17C2260/00—Purposes of gas storage and gas handling
- F17C2260/01—Improving mechanical properties or manufacturing
- F17C2260/016—Preventing slosh
-
- 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
- F17C2270/00—Applications
- F17C2270/01—Applications for fluid transport or storage
- F17C2270/0142—Applications for fluid transport or storage placed underground
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】
開示技術はLNG等の低温液化ガスの貯蔵タンク内に於
ける重質低温液化ガスと軽質低温液化ガスの層状現象に
基づくロールオーバーを攪拌によって防止する技術に属
する。DETAILED DESCRIPTION OF THE INVENTION The disclosed technology belongs to a technology for preventing rollover caused by a layering phenomenon of heavy low-temperature liquefied gas and light low-temperature liquefied gas in a storage tank of low-temperature liquefied gas such as LNG by stirring.
而して、この発明はタンク内のLNG等の低温液化ガス
が密度差により層状化現象を起こしてロールオーバーを
発生するのを該貯溜低温液化ガス自体を攪拌させること
により密度均一化させて解消する様にしたロールオーバ
ー防止技術に関するものであり、特に、タンクに設けた
受け入れパイプと払い出しパイプを用いフロートに付設
したサクションパイプを介して上層液を下層内に吸引送
給循環して自己攪拌混合する低温液化ガスタンクのロー
ルオーバー防止方法に係るものである。Therefore, this invention solves the problem of rollover caused by stratification of low-temperature liquefied gas such as LNG in a tank due to density differences, by making the density uniform by stirring the stored low-temperature liquefied gas itself. This technology relates to rollover prevention technology, in particular, self-agitation and mixing by suctioning and circulating the upper layer liquid into the lower layer via a suction pipe attached to a float using a receiving pipe and a discharging pipe installed in the tank. The present invention relates to a rollover prevention method for a low-temperature liquefied gas tank.
周知の如く、近時LNG等の低温液化ガス貯蔵タンクが
建造運転される時になると現実的に種々の問題が発生す
る。As is well known, various problems actually occur when storage tanks for low-temperature liquefied gases such as LNG are recently constructed and operated.
その1つに所謂ロールオーバーの問題があり、各種のL
NG等の低温液化ガスを受け入れて運転するとなると受
け入れLNGとタンク内残質LNGとの成分比が異なる
ため、密度の差により所謂層状化現象が発生する。One of them is the so-called rollover problem, and various types of L
When operating by receiving low-temperature liquefied gas such as NG, the component ratio of the received LNG and the residual LNG in the tank is different, so a so-called stratification phenomenon occurs due to the difference in density.
而して、一般に下層に重質LNGを、上部に軽質LNG
を受け入れて運転すると、上層軽質LNGは蒸発過程を
経て密度は大きくなり、従って、次第に密度の均衡が行
われる様になる。Generally, heavy LNG is placed in the lower layer and light LNG is placed in the upper layer.
When the fuel cell is operated, the density of the upper light LNG increases through the evaporation process, and the density gradually becomes balanced.
さりながら、下層の重質LNGは潜在エネルギー、輸送
時及び貯蔵時の入熱等により巨大な蓄積されたエネルギ
ーを有し、上記密度均衡状態の前後に突発的に該蓄積エ
ネルギーに等しい蒸発ガスを沸出させる所謂ロールオー
バーが発生する様になり、通常の蒸発ガス処理機構では
処理出来なくなり、その結果、タンク内圧が過大になっ
て危険な状態になるおそれがある欠点があった。However, the heavy LNG in the lower layer has a huge amount of accumulated energy due to latent energy and heat input during transportation and storage, and before and after the above density equilibrium state, it suddenly releases evaporated gas equal to the accumulated energy. A so-called rollover occurs, which cannot be treated by a normal evaporative gas treatment mechanism, and as a result, the internal pressure of the tank becomes excessive, resulting in a dangerous situation.
これに対処するに該ロールオーバー防止には攪拌作用を
付与し、均質密度にして層状化現象阻止を企ることか有
効であることが判って来たが、ミキサ一方法等の機械的
手段では低温液中での駆動、作動が極めて困難である難
点がある。To deal with this problem, it has been found that it is effective to provide stirring action to prevent the layering phenomenon by creating a homogeneous density, but mechanical means such as a mixer method are not effective. The disadvantage is that it is extremely difficult to drive and operate in low-temperature liquids.
この発明の目的は上述従来技術に基づく低温液化ガスタ
ンクのロールオーバー防止の問題点ヲ解決すべき技術的
課題とし、機械的強制攪拌なしに貯溜液を循環させて混
合することによりロールオーバーしない様にして資源産
業に於ける低温液化ガス利用分野に益する優れた低温液
化ガスタンクのロールオーバー防止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 preventing rollover of low-temperature liquefied gas tanks based on the above-mentioned prior art, and to prevent rollover by circulating and mixing the stored liquid without mechanically forced stirring. The present invention aims to provide an excellent rollover prevention method for low-temperature liquefied gas tanks that is useful in the field of low-temperature liquefied gas utilization in the resource industry.
上述目的に沿うこの発明の構成は払い出しポンプを用い
て液面近傍の軽質低温液化ガスを吸引パイプを介して吸
引し払い出しパイプにより送り出しバイパスパイプを経
て、受け入れパイプによりタンク内底部の重質低温液化
ガス液の下層液下に吐出しこれによって密度の軽い上部
の軽質低温液化ガス液は密度の重い重質低温液化ガス液
中をその浮力作用により自然上昇し全域を密度均一にす
る様にし層状化現象発生を阻止し、ロールオーバーを防
止する様にした技術的手段を講じたことを要旨とするも
のである。The structure of the present invention in accordance with the above-mentioned purpose is to use a dispensing pump to suck in light low-temperature liquefied gas near the liquid surface through a suction pipe, send it out through a dispensing pipe, pass through a bypass pipe, and then liquefy heavy low-temperature gas at the bottom of the tank using a receiving pipe. The gas liquid is discharged below the lower layer of the liquid, and as a result, the light, low-temperature liquefied gas liquid in the upper part, which has a lower density, naturally rises through the heavier, lower-temperature liquefied gas liquid with a higher density due to its buoyancy, making the density uniform over the entire area and forming a layer. The gist is that technical measures have been taken to prevent the phenomenon from occurring and prevent rollover.
次に、上記目的に沿うこの発明の一実施例を図面に従っ
て説明すれば以下の通りである。Next, an embodiment of the present invention that achieves the above object will be described below with reference to the drawings.
1は低温液化ガスタンクであり、地下式にされており、
ドーム屋根2を有する躯体3は地盤4内に構築され、内
槽5は保冷材6を介して設けられており、該ドーム屋根
2からはサスペンションロツド7,7・・・により吊り
デツキ8が吊設されている。1 is a low-temperature liquefied gas tank, which is underground.
A frame 3 with a dome roof 2 is built in the ground 4, and an inner tank 5 is provided via a cold insulating material 6. A hanging deck 8 is connected to the dome roof 2 by suspension rods 7, 7... It is suspended.
又、該内槽5内底部には払い出し用のサブマージドポン
プ9が浸漬固設されており、該サブマージドポンプ9に
は払い出しバイプ10が接続され、ドーム屋根2を貫通
されて次段処理施設に延設されている。Further, a submerged pump 9 for discharging is immersed and fixed in the inner bottom of the inner tank 5, and a discharging pipe 10 is connected to the submerged pump 9, and is passed through the dome roof 2 to the next stage treatment facility. It has been extended to
一方、同じく内槽5内底部には吐出ノズル11を有する
受け入れパイプ12がドーム屋根2を貫通して前段受け
入れ施設に接続されている。On the other hand, at the inner bottom of the inner tank 5, a receiving pipe 12 having a discharge nozzle 11 penetrates through the dome roof 2 and is connected to the previous stage receiving facility.
そして、内層5の底面5′とドーム屋根2との間にガイ
ドワイヤ13.13が張設されており、該ガイドワイヤ
13,13に遊挿されLNG14に浮上されたフロート
15が設けられており、該フロート15に下設された吸
引口16に設けたスイベルジョイント17を介して吸引
パイプ18,18・・・が同じく複段のスイベルジョイ
ント17,17を有して前記サブマージドポンプ9に接
続されている。Guide wires 13 and 13 are stretched between the bottom surface 5' of the inner layer 5 and the dome roof 2, and a float 15 that is loosely inserted into the guide wires 13 and 13 and floated on the LNG 14 is provided. , suction pipes 18, 18, . has been done.
又、前記払い出しパイプ10と受け入れバイプ12とに
は切換バルプ19.20を介してバイパスライン21が
介装連結されている。Further, a bypass line 21 is interposed and connected to the discharge pipe 10 and the receiving pipe 12 via switching valves 19 and 20.
上記構成の低温液化ガスタンク1に於て、受け入れバイ
プ12より重質LNGを受け入れると上部軽質LNGと
の間に密度差により前記の如く層状化現象が生じ様とす
るが、予測データ及び測定データ等により図示しない制
御機構を介し切換バルブ19.20を切換えてバイパス
ライン21をして受け払いパイプ10.12に接続させ
てクローズドシステムにし、サブマージドポンプ9を作
動させるとフロート15に付設された吸引口16から軽
質LNGが吸引され、スイベルジョイント17.17・
・・、吸引パイプ18.18・・・を介して該サブマー
ジドポンプ9Kより払い出しバイプ10、切換バルプ1
9,バイパスライン21、切換バルブ20、受け入れパ
イプ11を経由し吐出ノズル11から底部重質LNGに
噴出され軽質LNGと重質LNGの密度差による浮力作
用によって攪拌される。In the low-temperature liquefied gas tank 1 having the above configuration, when heavy LNG is received from the receiving pipe 12, the stratification phenomenon as described above is likely to occur due to the density difference between it and the upper light LNG. By switching the switching valve 19.20 through a control mechanism (not shown), the bypass line 21 is connected to the receiving and receiving pipe 10.12 to create a closed system, and when the submerged pump 9 is operated, the suction attached to the float 15 is Light LNG is sucked from the port 16, and the swivel joint 17.17.
..., a suction pipe 18, a discharge pipe 10 from the submerged pump 9K via a suction pipe 18, a switching valve 1
9. It is ejected from the discharge nozzle 11 to the bottom heavy LNG via the bypass line 21, the switching valve 20, and the receiving pipe 11, and is stirred by the buoyancy effect due to the density difference between the light LNG and heavy LNG.
この循環プロセスを反復するとタンク内は次第に軽質L
NGと重質LNGが攪拌混合されて密度均一化され、そ
の結果、層状化現象は発生せず、従って,ロールオーバ
ー現象も生じない。As this circulation process is repeated, the inside of the tank gradually becomes lighter L.
NG and heavy LNG are stirred and mixed to make the density uniform, and as a result, no stratification phenomenon occurs, and therefore no rollover phenomenon occurs.
伺、発生蒸気については図示しない集ガス管を介して所
定に処理される。The generated steam is then processed in a predetermined manner via a gas collection pipe (not shown).
而して、密度均一化が終了すると前記とは逆に切換バル
ブ19,20を受け払いラインに戻し、払い出しについ
てはサブマージドポンプ9の作動によりフロート15の
吸引口16から上記密度均一化されたLNGをスイベル
ジョイント17,17・・・、吸引パイプ18.18・
・・より吸引し、払い出しパイプ10より次段処理に送
給されていく。When the density uniformization is completed, the switching valves 19 and 20 are returned to the receiving and discharging line, contrary to the above, and the density is uniformized from the suction port 16 of the float 15 by the operation of the submerged pump 9. Connect LNG to swivel joints 17, 17..., suction pipes 18, 18,
...is sucked in and sent to the next stage of processing through the discharge pipe 10.
そして、LNG14の受け払いによる液面の昇降につい
てはフロート15のガイドワイヤ13.13に沿う昇降
によって吸引され、吸引バイプ18,18・・・はスイ
ベルジョイント17,17・・・により高さ変位姿勢を
吸収される。The liquid level rises and falls due to receiving and discharging the LNG 14, which is sucked by the float 15 moving up and down along the guide wire 13.13, and the suction vitrees 18, 18... is absorbed.
尚、この発明の実施態様は上記実施例に限るものでない
ことは勿論であり、種々の態様が可能である。Incidentally, it goes without saying that the embodiments of the present invention are not limited to the above embodiments, and various embodiments are possible.
上記の様にこの発明によれば、LNG等の低温液化ガス
タンク内の貯液循環攪拌によるロールオーバー防止方法
に於て、サブマージポンプ及び払い出しパイプ、そして
、受け入れパイプを介し低温液化ガス上層部を吸引して
底部に吐出する様にしたことにより、タンク内の軽質低
温液化ガスを吸引し底部重質低温液化ガス中に吐出させ
ることが出来、従って、他の何らの攪拌手段を用いるこ
となく自己の流動性によって上層と下層とが攪拌混合さ
れ、そのため、経時的に密度が均一化され、その結果、
層状化現象が阻止され、その限り前記ロールオーバーも
発生防止される優れた効果が奏される。As described above, according to the present invention, in a rollover prevention method by circulating and stirring a stored liquid in a tank of low-temperature liquefied gas such as LNG, the upper layer of low-temperature liquefied gas is sucked through a submerged pump, a discharge pipe, and a receiving pipe. By discharging it to the bottom, the light low-temperature liquefied gas in the tank can be sucked and discharged into the heavy low-temperature liquefied gas at the bottom. The fluidity allows the upper and lower layers to be stirred and mixed, thus homogenizing the density over time, resulting in
The stratification phenomenon is prevented, and as long as the occurrence of the rollover is also prevented, an excellent effect is achieved.
又、貯液循環に際しては払い出し用サブマージドポンプ
、払い出しパイプ、受け入れパイプが用いられるのでそ
れだけ装置的にも構成が簡単となるメリットがある。Furthermore, since a submerged pump for dispensing, a dispensing pipe, and a receiving pipe are used for circulating the stored liquid, there is an advantage that the configuration of the device is simplified accordingly.
図面はこの発明の一実施例を示すものであり、全体概略
説明図である。
1・・・タンク、14・・・低温液化ガス、10・・・
払い出しパイプ、12・・・受け入れパイプ。The drawings show one embodiment of the present invention and are overall schematic explanatory views. 1...tank, 14...low temperature liquefied gas, 10...
Dispensing pipe, 12... receiving pipe.
Claims (1)
の間に層状化現象が発生する場合に該低温液化ガス内部
に密度均一化攪拌作用を付与してロールオーバーを防止
する様にした方法において、該低温液化ガス液面近傍よ
り上部軽質液化ガス液を内底部付近に設けた払い出しポ
ンプを介して吸引し同じく内底部に設けた受け入れパイ
プにより重質液化ガス液中に噴出して循環させ、上部軽
質液化ガス液と下部重質液化ガス液との密度差を介して
自然上昇させて前記重質低温液化ガスと軽質低温液化ガ
スとを密度均一に混合攪拌する様にしたことを特徴とす
る低温液化ガスタンクのロールオーバー防止方法。1. A method for preventing rollover by imparting a density-uniforming stirring action to the inside of the low-temperature liquefied gas when a stratification phenomenon occurs between the heavy low-temperature liquefied gas and the light low-temperature liquefied gas in the tank. The upper light liquefied gas liquid is sucked from near the low temperature liquefied gas liquid level through a payout pump provided near the inner bottom, and is spouted into the heavy liquefied gas liquid through a receiving pipe also provided at the inner bottom for circulation. , characterized in that the heavy low-temperature liquefied gas and the light low-temperature liquefied gas are mixed and stirred to have a uniform density by allowing the upper light liquefied gas liquid to naturally rise through the density difference between the lower heavy liquefied gas liquid. A method to prevent rollover of low-temperature liquefied gas tanks.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55039052A JPS586120B2 (en) | 1980-03-28 | 1980-03-28 | Method for preventing rollover of low temperature liquefied gas tank |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP55039052A JPS586120B2 (en) | 1980-03-28 | 1980-03-28 | Method for preventing rollover of low temperature liquefied gas tank |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS56138599A JPS56138599A (en) | 1981-10-29 |
| JPS586120B2 true JPS586120B2 (en) | 1983-02-03 |
Family
ID=12542350
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP55039052A Expired JPS586120B2 (en) | 1980-03-28 | 1980-03-28 | Method for preventing rollover of low temperature liquefied gas tank |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS586120B2 (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6066979U (en) * | 1983-10-14 | 1985-05-13 | 東城 巧 | hot air panel |
| JPS6066980U (en) * | 1983-10-14 | 1985-05-13 | 東城 巧 | hot air panel |
| JPS62120120U (en) * | 1986-01-22 | 1987-07-30 |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58151800U (en) * | 1982-04-07 | 1983-10-11 | 石川島播磨重工業株式会社 | Cryogenic storage tank with multiple ducts |
| KR100620104B1 (en) | 2005-01-17 | 2006-09-11 | 홍종국 | Fly Ash Storage Structure |
Family Cites Families (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5641784Y2 (en) * | 1978-02-13 | 1981-09-30 |
-
1980
- 1980-03-28 JP JP55039052A patent/JPS586120B2/en not_active Expired
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS6066979U (en) * | 1983-10-14 | 1985-05-13 | 東城 巧 | hot air panel |
| JPS6066980U (en) * | 1983-10-14 | 1985-05-13 | 東城 巧 | hot air panel |
| JPS62120120U (en) * | 1986-01-22 | 1987-07-30 |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS56138599A (en) | 1981-10-29 |
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