JPH1182895A - Low temperature storage installation - Google Patents

Low temperature storage installation

Info

Publication number
JPH1182895A
JPH1182895A JP24261697A JP24261697A JPH1182895A JP H1182895 A JPH1182895 A JP H1182895A JP 24261697 A JP24261697 A JP 24261697A JP 24261697 A JP24261697 A JP 24261697A JP H1182895 A JPH1182895 A JP H1182895A
Authority
JP
Japan
Prior art keywords
liquid
low
pipe
temperature
temperature storage
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.)
Pending
Application number
JP24261697A
Other languages
Japanese (ja)
Inventor
Yasuo Koda
康雄 国府田
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.)
IHI Corp
Original Assignee
IHI Corp
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 IHI Corp filed Critical IHI Corp
Priority to JP24261697A priority Critical patent/JPH1182895A/en
Publication of JPH1182895A publication Critical patent/JPH1182895A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To reduce cost and installation area. SOLUTION: A low temperature storage installation is provided with a low temperature storage tank 2 that can store low temperature liquid 1, a boil-off gas(BOG) pipe 16 for leading evaporated gas 15 generated in the low temperature storage tank 2, to the outside, A receiving pipe 6 diverged into an upper receiving pipe 7 for transferring the low temperature liquid 1 to the upper part of the low temperature storage tank 2, and a lower receiving pipe 8 for transferring the low temperature liquid 1 to the lower part of the low temperature storage tank 2, and a liquid drain pipe 25 for leading the low temperature liquid 1 accomulated in a vertical part 10 of the upper receiving pipe 7, to the outside. Such a low temperature storage installation is provided with a liquid drain drum 32 serving as a BOG suction drum provided at its upper part with a mist separator 21 for separating mist 20 contained in the evaporated gas 15 from the BOG pipe 16 and provided ast its lower part with a liquid reservoir part that can store the low temperature liquid 1 fed from the vertical part 10 of the upper receiving pipe 7 through the liquid drain pipe 25.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、低温貯蔵設備に関
するものであり、より詳しくは、コストダウンを図ると
共に据え付け面積を削減し得るようにした低温貯蔵設備
に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a low-temperature storage facility, and more particularly, to a low-temperature storage facility capable of reducing costs and reducing an installation area.

【0002】[0002]

【従来の技術】液化天然ガス(LNG)などの低温液体
を貯蔵するために、低温貯蔵設備が用いられている。
2. Description of the Related Art Cryogenic storage facilities are used to store cryogenic liquids such as liquefied natural gas (LNG).

【0003】上記低温貯蔵設備は、図2に示すように、
低温液体1を貯蔵するようにしたLNGタンクなどの低
温貯槽2によって主に構成されており、低温貯槽2は、
船3からの低温液体1を、船3に搭載されたポンプ4を
用いて低温貯槽2へ送るようにするための、送液管5及
び受入管6を備えており、受入管6は、低温貯槽2の上
部に接続される上部受入管7と低温貯槽2の下部に接続
される下部受入管8とに分岐されている。
[0003] As shown in FIG.
The low-temperature storage tank 2 mainly includes a low-temperature storage tank 2 such as an LNG tank that stores the low-temperature liquid 1.
A liquid sending pipe 5 and a receiving pipe 6 for sending the low-temperature liquid 1 from the ship 3 to the low-temperature storage tank 2 using the pump 4 mounted on the ship 3 are provided. It branches into an upper receiving pipe 7 connected to the upper part of the storage tank 2 and a lower receiving pipe 8 connected to the lower part of the low temperature storage tank 2.

【0004】尚、9は上部受入管7の垂直部10に設け
られた弁、11は下部受入管8の途中に設けられた弁で
ある。
[0004] Incidentally, reference numeral 9 denotes a valve provided in the vertical portion 10 of the upper receiving pipe 7, and reference numeral 11 denotes a valve provided in the middle of the lower receiving pipe 8.

【0005】そして、送液管5や受入管6を冷却状態に
保持するために、低温貯槽2の底部と送液管5或いは受
入管6との間には、補給用ポンプ12とレベル調整弁1
3を備えた補給管14が設けられている。
[0005] In order to keep the liquid sending pipe 5 and the receiving pipe 6 in a cooled state, a replenishing pump 12 and a level adjusting valve are provided between the bottom of the low-temperature storage tank 2 and the liquid sending pipe 5 or the receiving pipe 6. 1
3 is provided.

【0006】又、低温貯槽2の上部には、蒸発ガス15
を外部へ取り出すためのBOG管16(BOG=ボイル
オフガス)が取付けられており、BOG管16は、BO
Gサクションドラム17及び圧縮機18などを介して、
需要先へ送るための送ガス管19などへと接続されてい
る。
[0006] Further, an evaporative gas 15
A BOG tube 16 (BOG = boil-off gas) for taking out the air to the outside is attached.
Via the G suction drum 17 and the compressor 18
It is connected to a gas sending pipe 19 for sending to a demand destination.

【0007】上記BOGサクションドラム17は、上部
に蒸発ガス15中のミスト分20を分離するためのワイ
ヤメッシュなどのミストセパレータ21が取付けられて
おり、BOGサクションドラム17には、ミストセパレ
ータ21で分離されたミスト分20が凝縮することによ
り下部に溜まった低温液体1をポンプ22を用いて低温
貯槽2の上部へ戻すようにする戻り管23が設けられて
いる。
The BOG suction drum 17 is provided with a mist separator 21 such as a wire mesh for separating a mist 20 in the evaporative gas 15 at the upper part. The mist separator 21 separates the BOG suction drum 17 from the mist separator 21. A return pipe 23 is provided for returning the low-temperature liquid 1 accumulated in the lower portion by condensing the mist portion 20 to the upper portion of the low-temperature storage tank 2 using a pump 22.

【0008】更に、送液管5或いは受入管6には、上部
受入管7の垂直部10に溜まった低温液体1を液抜きド
ラム24へ送るための液抜き管25が接続されており、
液抜き管25の液抜きドラム24入側には開閉弁26が
設けられ、且つ、開閉弁26には並列に制限オリフィス
27が設けられている。
Further, a drain pipe 25 for sending the low-temperature liquid 1 accumulated in the vertical portion 10 of the upper receiving pipe 7 to the drain drum 24 is connected to the liquid sending pipe 5 or the receiving pipe 6.
An opening / closing valve 26 is provided on the liquid draining tube 25 on the side of the liquid draining drum 24, and a limiting orifice 27 is provided in parallel with the opening / closing valve 26.

【0009】尚、液抜きドラム24の下部には、液位検
出器28からの液位検出信号29により、ポンプ30を
用いて、液抜きドラム24の低温液体1を低温貯槽2の
上部へ戻すようにする戻り管31が設けられている。
The low temperature liquid 1 of the liquid draining drum 24 is returned to the upper part of the low temperature storage tank 2 by using a pump 30 at the lower part of the liquid draining drum 24 based on a liquid level detection signal 29 from a liquid level detector 28. A return pipe 31 is provided.

【0010】斯かる構成によれば、LNGタンクなどの
低温貯槽2にLNGガスなどの低温液体1が貯蔵される
が、低温液体1を貯蔵した状態では、外部からの入熱な
どにより、貯蔵している低温液体1が蒸発されて行くこ
とになる。そして、蒸発によって発生した蒸発ガス15
は、低温貯槽2の上部からBOG管16を介して圧縮機
18へと送られ、圧縮機18で所要の圧力に加圧されて
から、送ガス管19を介して需要先へと送られる。
According to such a configuration, the low-temperature liquid 1 such as LNG gas is stored in the low-temperature storage tank 2 such as an LNG tank. The low-temperature liquid 1 is evaporated. Then, the evaporation gas 15 generated by the evaporation
Is sent from the upper part of the low-temperature storage tank 2 to the compressor 18 via the BOG pipe 16, pressurized to a required pressure by the compressor 18, and then sent to the demand destination via the gas sending pipe 19.

【0011】又、圧縮機18で圧縮するに先立ち、BO
G管16の途中に設けられたBOGサクションドラム1
7へ蒸発ガス15を通し、ワイヤメッシュなどのミスト
セパレータ21で蒸発ガス15中のミスト分20を分離
させることにより、支障無く圧縮機18で蒸発ガス15
を圧縮できるようにする。
Prior to compression by the compressor 18, the BO
BOG suction drum 1 provided in the middle of G tube 16
7, the mist separator 20 such as a wire mesh separates the mist 20 in the evaporative gas 15 so that the evaporative gas 15 can be easily compressed by the compressor 18.
To be compressed.

【0012】そして、ミストセパレータ21で分離され
たミスト分20は、凝縮されてBOGサクションドラム
17の下部に溜められる。BOGサクションドラム17
の下部に低温液体1が有る程度溜まったら、ポンプ22
を駆動して、戻り管23を介し、低温貯槽2の上部へ戻
させるようにする。
The mist 20 separated by the mist separator 21 is condensed and accumulated in the lower part of the BOG suction drum 17. BOG suction drum 17
When the low temperature liquid 1 has accumulated to the lower part of the pump, the pump 22
Is driven to return to the upper part of the low-temperature storage tank 2 via the return pipe 23.

【0013】一方、送液管5や受入管6は、常温の状態
からいきなり低温液体1を通すようにすることができな
いので、送液管5或いは受入管6の内部に所要量の低温
液体1が常時貯留されるようにして、送液管5や受入管
6を冷却状態に保持させておくようにする必要がある。
On the other hand, since the liquid sending pipe 5 and the receiving pipe 6 cannot pass the low-temperature liquid 1 from the room temperature state immediately, the required amount of the low-temperature liquid 1 is stored in the liquid sending pipe 5 or the receiving pipe 6. Must always be stored, and the liquid sending pipe 5 and the receiving pipe 6 must be kept in a cooled state.

【0014】そのために、図示しないレベル検出器など
により送液管5や受入管6内の低温液体1の液位を検出
させ、液位が低くなったら、補給用ポンプ12を駆動さ
せると共にレベル調整弁13を開き、補給管14を介し
て、低温貯槽2の底部から送液管5或いは受入管6へと
低温液体1を補給させるようにしている。尚、送液管5
或いは受入管6へ低温液体1が補給されたら、補給用ポ
ンプ12は自動的に停止し、レベル調整弁13は自動的
に閉じるようになっている。
For this purpose, the level of the low-temperature liquid 1 in the liquid sending pipe 5 and the receiving pipe 6 is detected by a level detector (not shown) or the like, and when the liquid level becomes low, the supply pump 12 is driven and the level is adjusted. The valve 13 is opened, and the low-temperature liquid 1 is supplied from the bottom of the low-temperature storage tank 2 to the liquid sending pipe 5 or the receiving pipe 6 via the supply pipe 14. In addition, the liquid sending pipe 5
Alternatively, when the low-temperature liquid 1 is supplied to the receiving pipe 6, the supply pump 12 is automatically stopped, and the level adjustment valve 13 is automatically closed.

【0015】そして、低温液体1を満載された船3が到
着すると、船3に搭載されたポンプ4を駆動することに
より、送液管5及び受入管6を介して、船3に満載され
た低温液体1を、低温貯槽2へと移送させるようにす
る。
When the ship 3 filled with the low-temperature liquid 1 arrives, the pump 3 mounted on the ship 3 is driven, so that the ship 3 is loaded on the ship 3 via the liquid sending pipe 5 and the receiving pipe 6. The low-temperature liquid 1 is transferred to the low-temperature storage tank 2.

【0016】この際、船3からの低温液体1の密度と、
低温貯槽2に貯留されている低温液体1の密度とを調べ
て、船3からの低温液体1の密度の方が大きい場合には
下部受入管8の弁11を閉じ、上部受入管7の弁9を開
くことにより上部受入管7を通して低温液体1を低温貯
槽2の上側から入れるようにする。反対に、船3からの
低温液体1の密度の方が小さい場合には、弁11と弁9
の両方を開くことにより下部受入管8を通して低温液体
1を低温貯槽2の下側から入れるようにする。これによ
り、密度差によって低温貯槽2内の低温液体1が二相に
別れるようなことのないようにすることができる。
At this time, the density of the cryogenic liquid 1 from the ship 3
The density of the low-temperature liquid 1 stored in the low-temperature storage tank 2 is checked, and when the density of the low-temperature liquid 1 from the ship 3 is higher, the valve 11 of the lower receiving pipe 8 is closed, and the valve of the upper receiving pipe 7 is closed. By opening 9, the low-temperature liquid 1 is introduced from above the low-temperature storage tank 2 through the upper receiving pipe 7. Conversely, if the density of the cryogenic liquid 1 from the ship 3 is smaller, the valves 11 and 9
By opening both, the low-temperature liquid 1 is introduced from the lower side of the low-temperature storage tank 2 through the lower receiving pipe 8. Thereby, it is possible to prevent the low-temperature liquid 1 in the low-temperature storage tank 2 from separating into two phases due to the density difference.

【0017】そして、低温液体1を低温貯槽2の下側か
ら入れる場合に、弁9を開けるのは、低温液体1に含ま
れているガス分を上部受入管7の側へ逃がさせるように
するためである。又、上記により弁9を開けると、上部
受入管7の垂直部10には、低温貯槽2の液位と等しい
液位まで、低温液体1が入り込むことになる。
When the low-temperature liquid 1 is introduced from below the low-temperature storage tank 2, the valve 9 is opened so that the gas contained in the low-temperature liquid 1 is allowed to escape to the upper receiving pipe 7 side. To do that. When the valve 9 is opened as described above, the low-temperature liquid 1 enters the vertical portion 10 of the upper receiving pipe 7 to a liquid level equal to the liquid level of the low-temperature storage tank 2.

【0018】そして、低温貯槽2へ低温液体1を入れた
ら、一旦、弁9と弁11を閉じるようにする。
After the low-temperature liquid 1 is put into the low-temperature storage tank 2, the valves 9 and 11 are closed once.

【0019】このように弁9と弁11を閉じると、上部
受入管7の垂直部10には低温液体1が残ることとなる
が、径寸法の小さい垂直部10内に残された低温液体1
は、外部からの入熱によって不安定な状態(間欠的に沸
騰するような状態)となりやすい。
When the valves 9 and 11 are closed as described above, the low-temperature liquid 1 remains in the vertical portion 10 of the upper receiving pipe 7, but the low-temperature liquid 1 remaining in the vertical portion 10 having a small diameter dimension.
Is likely to be in an unstable state (a state of intermittent boiling) due to heat input from the outside.

【0020】そこで従来は、低温貯槽2へ低温液体1を
入れた後に、弁9と開閉弁26を開けることにより、重
力を利用して、垂直部10内に残された低温液体1を、
受入管6及び液抜き管25を介し、液抜きドラム24へ
と送って、垂直部10内の液抜きを行わせるようにして
いる。
Therefore, conventionally, after the low-temperature liquid 1 is put into the low-temperature storage tank 2, the valve 9 and the opening / closing valve 26 are opened, so that the low-temperature liquid 1 remaining in the vertical portion 10 is
The liquid is sent to the draining drum 24 via the receiving pipe 6 and the draining pipe 25 so as to drain the liquid in the vertical portion 10.

【0021】そして、液抜きドラム24では、液位検出
器28によって液位が検出されており、液抜きドラム2
4の液位が上限設定値よりも高くなったら、液位検出器
28からの液位検出信号29によってポンプ30が駆動
されて、戻り管31を介し、液抜きドラム24の低温液
体1が低温貯槽2の上部へ戻されることとなる。反対
に、液抜きドラム24の液位が下限設定値よりも低くな
ったら、液位検出器28からの液位検出信号29によっ
てポンプ30が停止されることとなる。以上により、液
抜きドラム24の液位が一定範囲内に保たれる。
The liquid level in the liquid draining drum 24 is detected by a liquid level detector 28.
When the liquid level of the liquid 4 becomes higher than the upper limit set value, the pump 30 is driven by the liquid level detection signal 29 from the liquid level detector 28, and the low temperature liquid 1 of the liquid draining drum 24 is cooled down through the return pipe 31. It will be returned to the upper part of the storage tank 2. Conversely, when the liquid level of the liquid draining drum 24 becomes lower than the lower limit set value, the pump 30 is stopped by the liquid level detection signal 29 from the liquid level detector 28. As described above, the liquid level of the liquid draining drum 24 is maintained within a certain range.

【0022】尚、液抜き管25やポンプ30などは、常
温の状態からいきなり低温液体1を通すようにすること
ができないため、液抜き管25に開閉弁26と並列に制
限オリフィス27を設けることにより、少量の低温液体
1を制限オリフィス27を通して液抜きドラム24やポ
ンプ30へ常時送らせ、これらを低温状態に保たせるよ
うにしている。
Since the liquid drain pipe 25 and the pump 30 cannot pass the low-temperature liquid 1 immediately from a normal temperature state, it is necessary to provide the liquid drain pipe 25 with a restriction orifice 27 in parallel with the on-off valve 26. As a result, a small amount of the low-temperature liquid 1 is constantly sent to the liquid draining drum 24 and the pump 30 through the restriction orifice 27, and these are kept at a low temperature.

【0023】[0023]

【発明が解決しようとする課題】しかしながら、上記従
来の低温貯蔵設備には、以下のような問題があった。
However, the above-mentioned conventional low-temperature storage equipment has the following problems.

【0024】即ち、上記低温貯蔵設備には、蒸発ガス1
5中のミスト分20を分離するためのBOGサクション
ドラム17と、垂直部10内の低温液体1の抜き先とな
る液抜きドラム24とがそれぞれ別個に設けられている
が、このようにBOGサクションドラム17と液抜きド
ラム24とを別個に設けると、コストアップの要因とな
ると共に、据え付けに広い面積が必要となる。
That is, the low-temperature storage equipment includes the evaporative gas 1
5 is provided separately from the BOG suction drum 17 for separating the mist 20 in the mist 5, and the liquid draining drum 24 from which the low-temperature liquid 1 in the vertical portion 10 is drawn. Providing the drum 17 and the liquid draining drum 24 separately increases the cost, and requires a large area for installation.

【0025】本発明は、上述の実情に鑑み、コストダウ
ンを図ると共に据え付け面積を削減し得るようにした低
温貯蔵設備を提供することを目的とするものである。
The present invention has been made in view of the above circumstances, and has as its object to provide a low-temperature storage facility capable of reducing costs and reducing an installation area.

【0026】[0026]

【課題を解決するための手段】本発明は、低温液体1を
貯蔵可能な低温貯槽2と、低温貯槽2内で発生した蒸発
ガス15を外部へ導くBOG管16と、低温貯槽2の上
部へ低温液体1を移送するための上部受入管7及び低温
貯槽2の下部へ低温液体1を移送するための下部受入管
8に分岐された受入管6と、上部受入管7の垂直部10
に溜まった低温液体1を受入管6を介し外部へ導く液抜
き管25とを備えた低温貯蔵設備において、上部に、B
OG管16からの蒸発ガス15に含まれるミスト分20
を分離するためのミストセパレータ21を備えると共
に、下部に、液抜き管25を介して送られてきた、上部
受入管7の垂直部10からの低温液体1を貯留可能な液
溜め部を有するBOGサクションドラム兼用液抜きドラ
ム32を設けたことを特徴とする低温貯蔵設備にかかる
ものである。
SUMMARY OF THE INVENTION The present invention provides a low-temperature storage tank 2 capable of storing a low-temperature liquid 1, a BOG pipe 16 for guiding an evaporative gas 15 generated in the low-temperature storage tank 2 to the outside, and an upper part of the low-temperature storage tank 2. An upper receiving pipe 7 for transferring the low-temperature liquid 1, a receiving pipe 6 branched into a lower receiving pipe 8 for transferring the low-temperature liquid 1 to a lower part of the low-temperature storage tank 2, and a vertical portion 10 of the upper receiving pipe 7.
Low-temperature storage equipment provided with a drain pipe 25 for guiding the low-temperature liquid 1 accumulated in the tank through the receiving pipe 6 to the outside.
Mist 20 contained in evaporative gas 15 from OG pipe 16
BOG having a mist separator 21 for separating the low temperature liquid 1 from the vertical portion 10 of the upper receiving pipe 7 which is sent through the liquid draining pipe 25 at the bottom. The present invention relates to a low-temperature storage facility provided with a suction drum and liquid drainage drum 32.

【0027】上記手段によれば、以下のような作用が得
られる。
According to the above means, the following effects can be obtained.

【0028】外部からの入熱などによって低温貯槽2に
貯蔵されている低温液体1が蒸発されることにより発生
した蒸発ガス15は、低温貯槽2の上部からBOG管1
6を介して外部へと送られ、BOG管16の途中に設け
られたBOGサクションドラム兼用液抜きドラム32で
ミストセパレータ21により蒸発ガス15中のミスト分
20を分離される。
The evaporative gas 15 generated by evaporating the low-temperature liquid 1 stored in the low-temperature storage tank 2 due to heat input from the outside, etc., flows from the upper part of the low-temperature storage tank 2 to the BOG pipe 1.
The mist 20 is sent out to the outside through the mist separator 21 and separated by the mist separator 21 by the mist separator 21 at the middle of the BOG pipe 16.

【0029】又、下部受入管8などを介して低温貯槽2
の下側へ低温液体1を入れた後に、上部受入管7の垂直
部10内に残された低温液体1を、受入管6及び液抜き
管25を介し、BOGサクションドラム兼用液抜きドラ
ム32へと送って、垂直部10内の液抜きを行わせるよ
うにする。
Also, the low-temperature storage tank 2 is connected via the lower receiving pipe 8 or the like.
After the low-temperature liquid 1 has been introduced into the lower side of the container, the low-temperature liquid 1 remaining in the vertical portion 10 of the upper receiving pipe 7 is transferred to the BOG suction drum / liquid discharging drum 32 via the receiving pipe 6 and the liquid discharging pipe 25. And the liquid is drained from the vertical portion 10.

【0030】このように、BOGサクションドラム兼用
液抜きドラム32を設けて、BOGサクションドラム兼
用液抜きドラム32に、蒸発ガス15中のミスト分20
の分離と、上部受入管7の垂直部10内の低温液体1の
液抜きの両方の機能を行わせるようにしているので、コ
ストダウンと据え付け面積の削減を図ることができる。
As described above, the BOG suction drum dual-purpose liquid draining drum 32 is provided, and the BOG suction drum dual-purpose liquid draining drum 32 is provided with the mist 20 in the evaporation gas 15.
, And the function of draining the low-temperature liquid 1 in the vertical portion 10 of the upper receiving pipe 7, so that the cost can be reduced and the installation area can be reduced.

【0031】[0031]

【発明の実施の形態】以下、本発明の実施の形態を、図
示例と共に説明する。
Embodiments of the present invention will be described below with reference to the drawings.

【0032】図1は、本発明の実施の形態の一例であ
る。
FIG. 1 shows an embodiment of the present invention.

【0033】低温貯蔵設備の基本的な構成については、
図2と同様であるため、同一の部分については同一の符
号を付すことにより説明を省略する。
Regarding the basic configuration of the low-temperature storage facility,
2 are the same as those in FIG.

【0034】本実施の形態では、上部に、BOG管16
からの蒸発ガス15に含まれるミスト分20を分離する
ためのミストセパレータ21を備えると共に、下部に、
液抜き管25を介して送られてきた、上部受入管7の垂
直部10からの低温液体1を貯留可能な液溜め部を有す
るBOGサクションドラム兼用液抜きドラム32を設け
たところにその特徴がある。
In this embodiment, the BOG tube 16
A mist separator 21 for separating a mist component 20 contained in the evaporated gas 15 from
A characteristic feature is that a BOG suction drum and liquid drainage drum 32 having a liquid storage part capable of storing the low-temperature liquid 1 from the vertical part 10 of the upper receiving pipe 7 sent through the liquid drainage pipe 25 is provided. is there.

【0035】次に、作動について説明する。Next, the operation will be described.

【0036】低温貯蔵設備の基本的な作動については図
2の場合と同様なので説明を省略する。
The basic operation of the low-temperature storage facility is the same as that of FIG.

【0037】本実施の形態では、外部からの入熱などに
よって低温貯槽2に貯蔵されている低温液体1が蒸発さ
れることにより発生した蒸発ガス15は、低温貯槽2の
上部からBOG管16を介して圧縮機18へと送られ、
圧縮機18で所要の圧力に加圧されてから、送ガス管1
9を介して需要先へと送られる。
In the present embodiment, the evaporative gas 15 generated by evaporating the low-temperature liquid 1 stored in the low-temperature storage tank 2 due to heat input from the outside or the like passes through the BOG pipe 16 from the upper part of the low-temperature storage tank 2. To the compressor 18 via
After being pressurized to a required pressure by the compressor 18, the gas delivery pipe 1
9 to the demand destination.

【0038】そして、圧縮機18で圧縮するに先立ち、
BOG管16の途中に設けられたBOGサクションドラ
ム兼用液抜きドラム32へ蒸発ガス15を通し、ワイヤ
メッシュなどのミストセパレータ21で蒸発ガス15中
のミスト分20を分離させることにより、支障無く圧縮
機18で蒸発ガス15を圧縮できるようにする。
Then, prior to compression by the compressor 18,
The evaporative gas 15 is passed through a BOG suction drum and liquid drainage drum 32 provided in the middle of the BOG pipe 16, and the mist 20 in the evaporative gas 15 is separated by a mist separator 21 such as a wire mesh. At 18, the evaporative gas 15 is compressed.

【0039】そして、ミストセパレータ21で分離され
たミスト分20は、凝縮してBOGサクションドラム兼
用液抜きドラム32の下部に溜められる。
The mist 20 separated by the mist separator 21 is condensed and stored in the lower part of the BOG suction drum and liquid drainage drum 32.

【0040】一方、船3から送液管5及び受入管6並び
に下部受入管8を介して低温貯槽2の下側へ低温液体1
を入れた後に、弁9と開閉弁26を開けることにより、
重力を利用して、上部受入管7の垂直部10内に残され
た低温液体1を、受入管6及び液抜き管25を介し、B
OGサクションドラム兼用液抜きドラム32へと送っ
て、垂直部10内の液抜きを行わせるようにする。
On the other hand, the low-temperature liquid 1 is transferred from the ship 3 to the lower side of the low-temperature storage tank 2 through the liquid sending pipe 5, the receiving pipe 6, and the lower receiving pipe 8.
, After opening the valve 9 and the on-off valve 26,
Using the gravity, the low-temperature liquid 1 left in the vertical portion 10 of the upper receiving pipe 7 is transferred through the receiving pipe 6 and the drain pipe 25 to B
The liquid is sent to the OG suction drum and liquid drainage drum 32 so that the liquid in the vertical portion 10 is drained.

【0041】そして、BOGサクションドラム兼用液抜
きドラム32では、液位検出器28によって液位が検出
されており、BOGサクションドラム兼用液抜きドラム
32の液位が上限設定値よりも高くなったら、液位検出
器28からの液位検出信号29によってポンプ30が駆
動されて、戻り管31を介し、BOGサクションドラム
兼用液抜きドラム32の低温液体1が低温貯槽2の上部
へ戻されることとなる。反対に、BOGサクションドラ
ム兼用液抜きドラム32の液位が下限設定値よりも低く
なったら、液位検出器28からの液位検出信号29によ
ってポンプ30が停止されることとなる。以上により、
BOGサクションドラム兼用液抜きドラム32の液位が
所定の範囲内に保たれる。
Then, in the BOG suction drum and liquid drainage drum 32, the liquid level is detected by the liquid level detector 28. When the liquid level of the BOG suction drum and liquid drainage drum 32 becomes higher than the upper limit set value, The pump 30 is driven by the liquid level detection signal 29 from the liquid level detector 28, and the low temperature liquid 1 of the BOG suction drum and liquid drainage drum 32 is returned to the upper part of the low temperature storage tank 2 via the return pipe 31. . Conversely, when the liquid level of the BOG suction drum and liquid drainage drum 32 becomes lower than the lower limit set value, the pump 30 is stopped by the liquid level detection signal 29 from the liquid level detector 28. From the above,
The liquid level of the BOG suction drum and liquid drainage drum 32 is maintained within a predetermined range.

【0042】尚、液抜き管25やポンプ30などは、常
温の状態からいきなり低温液体1を通すようにすること
ができないため、液抜き管25に開閉弁26と並列に制
限オリフィス27を設けて、少量の低温液体1を、制限
オリフィス27を通してBOGサクションドラム兼用液
抜きドラム32やポンプ30へ常時送らせ、これらを低
温状態に保たせるようにしている。
Since the low-temperature liquid 1 cannot be immediately passed through the drain tube 25 and the pump 30 from the room temperature state, a restricting orifice 27 is provided in the drain tube 25 in parallel with the on-off valve 26. A small amount of the low-temperature liquid 1 is constantly sent to the BOG suction drum and liquid drain drum 32 and the pump 30 through the restriction orifice 27 so that these are kept at a low temperature.

【0043】このように、BOGサクションドラム兼用
液抜きドラム32を設けて、BOGサクションドラム兼
用液抜きドラム32に、蒸発ガス15中のミスト分20
の分離と、上部受入管7の垂直部10内の低温液体1の
液抜きの両方の機能を行わせるようにしているので、コ
ストダウンと据え付け面積の削減を図ることができる。
As described above, the BOG suction drum dual-purpose liquid draining drum 32 is provided, and the BOG suction drum dual-purpose liquid draining drum 32 is provided with the mist 20 in the evaporation gas 15.
, And the function of draining the low-temperature liquid 1 in the vertical portion 10 of the upper receiving pipe 7, so that the cost can be reduced and the installation area can be reduced.

【0044】尚、本発明は、上述の実施の形態にのみ限
定されるものではなく、本発明の要旨を逸脱しない範囲
内において種々変更を加え得ることは勿論である。
It should be noted that the present invention is not limited to the above-described embodiment, and it is needless to say that various changes can be made without departing from the spirit of the present invention.

【0045】[0045]

【発明の効果】以上説明したように、本発明の低温貯蔵
設備によれば、コストダウンを図ると共に据え付け面積
を削減することができるという優れた効果を奏し得る。
As described above, according to the low-temperature storage facility of the present invention, it is possible to achieve an excellent effect that the cost can be reduced and the installation area can be reduced.

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

【図1】本発明の実施の形態の一例の概略系統図であ
る。
FIG. 1 is a schematic system diagram of an example of an embodiment of the present invention.

【図2】従来例の概略系統図である。FIG. 2 is a schematic system diagram of a conventional example.

【符号の説明】[Explanation of symbols]

1 低温液体 2 低温貯槽 6 受入管 7 上部受入管 8 下部受入管 10 垂直部 15 蒸発ガス 16 BOG管 20 ミスト分 21 ミストセパレータ 25 液抜き管 32 BOGサクションドラム兼用液抜きドラム DESCRIPTION OF SYMBOLS 1 Low-temperature liquid 2 Low-temperature storage tank 6 Receiving pipe 7 Upper receiving pipe 8 Lower receiving pipe 10 Vertical part 15 Evaporation gas 16 BOG pipe 20 Mist 21 Mist separator 25 Liquid drain pipe 32 BOG suction drum and liquid drain drum

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 低温液体(1)を貯蔵可能な低温貯槽
(2)と、低温貯槽(2)内で発生した蒸発ガス(1
5)を外部へ導くBOG管(16)と、低温貯槽(2)
の上部へ低温液体(1)を移送するための上部受入管
(7)及び低温貯槽(2)の下部へ低温液体(1)を移
送するための下部受入管(8)に分岐された受入管
(6)と、上部受入管(7)の垂直部(10)に溜まっ
た低温液体(1)を受入管(6)を介し外部へ導く液抜
き管(25)とを備えた低温貯蔵設備において、上部
に、BOG管(16)からの蒸発ガス(15)に含まれ
るミスト分(20)を分離するためのミストセパレータ
(21)を備えると共に、下部に、液抜き管(25)を
介して送られてきた、上部受入管(7)の垂直部(1
0)からの低温液体(1)を貯留可能な液溜め部を有す
るBOGサクションドラム兼用液抜きドラム(32)を
設けたことを特徴とする低温貯蔵設備。
A low-temperature storage tank (2) capable of storing a low-temperature liquid (1), and an evaporative gas (1) generated in the low-temperature storage tank (2).
BOG pipe (16) for guiding 5) to the outside, and low-temperature storage tank (2)
An upper receiving pipe (7) for transferring the low-temperature liquid (1) to the upper part of the container and a receiving pipe branched to a lower receiving pipe (8) for transferring the low-temperature liquid (1) to the lower part of the low-temperature storage tank (2). (6) and a liquid drainage pipe (25) for guiding the low-temperature liquid (1) accumulated in the vertical portion (10) of the upper receiving pipe (7) to the outside via the receiving pipe (6). A mist separator (21) for separating a mist (20) contained in the evaporative gas (15) from the BOG pipe (16) at the upper part, and a lower part via a liquid drain pipe (25). The vertical part (1) of the upper receiving pipe (7)
A low-temperature storage facility comprising a BOG suction drum and liquid drainage drum (32) having a liquid storage portion capable of storing the low-temperature liquid (1) from (0).
JP24261697A 1997-09-08 1997-09-08 Low temperature storage installation Pending JPH1182895A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP24261697A JPH1182895A (en) 1997-09-08 1997-09-08 Low temperature storage installation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP24261697A JPH1182895A (en) 1997-09-08 1997-09-08 Low temperature storage installation

Publications (1)

Publication Number Publication Date
JPH1182895A true JPH1182895A (en) 1999-03-26

Family

ID=17091715

Family Applications (1)

Application Number Title Priority Date Filing Date
JP24261697A Pending JPH1182895A (en) 1997-09-08 1997-09-08 Low temperature storage installation

Country Status (1)

Country Link
JP (1) JPH1182895A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002095285A1 (en) * 1999-11-05 2002-11-28 Osaka Gas Co., Ltd. Device and method for pressure control of cargo tank of liquefied natural gas carrier
WO2008066390A1 (en) * 2006-11-28 2008-06-05 Moss Maritime As Re-gasification of lng
KR20200023504A (en) * 2013-09-27 2020-03-04 익셀러레이트 에너지 리미티드 파트너쉽 Apparatus, system and method for the capture, utilization and sendout of latent heat in boil off gas onboard a cryogenic storage vessel

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2002095285A1 (en) * 1999-11-05 2002-11-28 Osaka Gas Co., Ltd. Device and method for pressure control of cargo tank of liquefied natural gas carrier
US6901762B2 (en) * 1999-11-05 2005-06-07 Osaka Gas Co., Ltd. Device and method for pressure control of cargo tank of liquefied natural gas carrier
WO2008066390A1 (en) * 2006-11-28 2008-06-05 Moss Maritime As Re-gasification of lng
KR20200023504A (en) * 2013-09-27 2020-03-04 익셀러레이트 에너지 리미티드 파트너쉽 Apparatus, system and method for the capture, utilization and sendout of latent heat in boil off gas onboard a cryogenic storage vessel

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