JP2003090497A - Gas pressure type lng transfer device - Google Patents

Gas pressure type lng transfer device

Info

Publication number
JP2003090497A
JP2003090497A JP2001287214A JP2001287214A JP2003090497A JP 2003090497 A JP2003090497 A JP 2003090497A JP 2001287214 A JP2001287214 A JP 2001287214A JP 2001287214 A JP2001287214 A JP 2001287214A JP 2003090497 A JP2003090497 A JP 2003090497A
Authority
JP
Japan
Prior art keywords
lng
tank
pressure
storage tank
valve
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
JP2001287214A
Other languages
Japanese (ja)
Inventor
Akira Hayakawa
明 早川
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.)
NIHONKAI GAS CO Ltd
Original Assignee
NIHONKAI GAS CO Ltd
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 NIHONKAI GAS CO Ltd filed Critical NIHONKAI GAS CO Ltd
Priority to JP2001287214A priority Critical patent/JP2003090497A/en
Publication of JP2003090497A publication Critical patent/JP2003090497A/en
Pending legal-status Critical Current

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  • Loading And Unloading Of Fuel Tanks Or Ships (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a large size storage tank of low temperature liquefied gas such as LNG capable of performing pressurization type transfer of LNG without using an LNG pump although there are problems that conventionally an electric LNG pump is put in LNG liquid, and the LNG or the like is boosted and is transferred in order to transfer the low temperature liquefied gas such as the LNG in a large size low pressure type storage tank, however labor and cost are required for maintenance management such as constant monitoring of abnormal vibration and failure diagnosis in installing the electric LNG pump, and also the LNG in the pump is vaporized and causes trouble in operation. SOLUTION: A pressurized tank 2, which is connected by a pressurizing discharge pipe 5, and a pressurizing and depressurizing pipe 34 and is provided with a submerged valve 21, is provided in an inside of the LNG storage tank 1. An inside of the pressurized tank 2 is depressurized and the LNG is allowed to flow in from the LNG storage tank 1, and the pressurized tank 2 is pressurized and the LNG is discharged. The transfer of the LNG is performed by repeating pressurization and depressurization of the inside of the pressurized tank 2.

Description

【発明の詳細な説明】 【0001】 【発明の属する技術分野】本発明は、液化天然ガス(以
下LNGと言う。)の如き低温液化ガスを加圧して貯槽
等より移送させる装置に関するものである。 【0002】 【従来の技術】従来、大型低圧式貯槽内のLNGを移送
するためには、電動式のLNGポンプをLNG液中へ投
入し、LNG等を昇圧し移送していた。 【0003】 【発明が解決しようとする課題】しかし、電動式LNG
ポンプの設置においては異常振動を常時監視し故障診断
を行うなど維持管理に労力と経費を要するばかりではな
く、ポンプ内のLNGが気化し運転に支障をきたすなど
の問題があった。本発明は、大型の低圧式LNG貯槽に
おいて、LNGポンプを使用せず加圧式のLNG移送方
法を実現できるようにしようとするものである。 【0004】 【課題を解決するための手段】本発明は、上記課題を解
決するために、LNG貯槽1内に液中弁駆動装置22で
開閉する液中弁21、加圧払出管5および加圧減圧管3
4を設けた圧力タンク2を設置し、液中弁21によりL
NG貯槽1内のLNG11が圧力タンク2内に流入でき
るようにし、更に加圧減圧管34により圧力タンク2内
の圧力を高められるようにし、加圧払出管5によりLN
Gを払い出しする構成とする。 【0005】 【発明の実施の形態】減圧弁61を開き圧力タンク2内
を減圧し、液中弁21を開き圧力タンク2内にLNG1
1を流入させ、液中弁21および減圧弁61を閉止した
後、加圧弁33を開き、圧力タンク2内を加圧する。続
いて、払出弁51を開き圧力タンク2内のLNGを払い
出す。このように圧力タンク2内で加圧されたLNGを
加圧払出管5より払出タンク7へ払い出す。更に圧力タ
ンク2内のLNGを払い出した後、同様の手順で圧力タ
ンク2内を減圧し、再びLNG貯槽1よりLNG11を
圧力タンク2へ流入させ、更に圧力タンク2内を加圧し
LNGを払い出す。このような操作を繰り返すことによ
り、LNG貯槽1内のLNG11の移送を行う。 【0006】 【実施例】以下に、本発明の実施例を図面に基づいて説
明する。本発明のLNG移送装置は図1に示すように、
LNG貯槽1内に圧力タンク2を設置し、圧力タンク2
下部には液中弁21を設け圧力タンク2内にLNG11
が流入できるようにし、また加圧減圧管34を接続し圧
力タンク2内を加圧減圧できるようにし、更に加圧払出
管5を設け、圧力タンク2内のLNGを払い出しできる
ようにする。 【0007】減圧管6には減圧弁61を設け、減圧弁6
1を開くことにより圧力タンク2内を減圧し、更に液中
弁21を開くことによりLNG貯槽1内のLNG11を
圧力タンク2内へ流入させる。 【0008】加圧管35は払出タンク7下部と接続し、
蒸発調節弁31、加圧蒸発器32、加圧弁33を設け
る。加圧管35は加圧蒸発器32でLNGを気化した気
化ガスで加圧されており、加圧弁33を開くことにより
気化ガスを圧力タンク2内へ流入させ、圧力タンク2内
を加圧する。 【0009】加圧払出管5には払出弁51を設け、払出
弁51を開くことにより圧力タンク2内で加圧されたL
NGを払出タンク7へ払い出す。 【0010】続いて本発明のガス圧式LNG移送装置の
使用例について詳述する。LNG貯槽1に設けられたL
NG受入管4によりLNG11の受け入れを行う。ま
た、加圧管35内の圧力が一定になるように加圧調節弁
31の開度を調節する。加圧蒸発器32に流入したLN
Gは気化膨張し、加圧管35内の圧力を高める。 【0011】払出タンク7を2基設け、一方の払出タン
ク7でLNG貯槽1内のLNG11を受け入れし、他方
の払出タンク7では気化装置73へのLNGの払い出し
を行う。2基の払出タンク7は交互にLNG貯槽1より
のLNGの受け入れおよび気化装置73へのLNGの払
い出しを行う。 【0012】LNG貯槽1からLNGを受け入れしてい
る払出タンク7においては、BOG払出弁92を開き、
BOG圧縮機91を運転し払出タンク7内の圧力を一定
圧力まで下げておく。また、他方の気化装置73へLN
Gを払い出している払出タンク7においては、払出タン
ク加圧弁81を開き、払出タンク7を加圧しておく。 【0013】以上のような状態で、始めに減圧弁61を
開き圧力タンク2内の圧力をLNG貯槽1内の圧力と同
圧以下にまで下げる。続いて、液中弁21を開き、LN
G貯槽1と圧力タンク2内の圧力差によりLNG貯槽1
内のLNG11を圧力タンク2内へ流入させる。なお、
減圧管6をLNG貯槽1上部へ接続し、減圧時のガスを
LNG貯槽1へ回収できるようにしてもよい。 【0014】圧力タンク2がLNGで満たされた状態
で、液中弁21および減圧弁61を閉止する。続いて、
加圧弁33を開き、圧力タンク2内の圧力を高める。こ
の状態でLNG受け入れ中の払出タンク7に接続した払
出弁51を開き、圧力タンク2内のLNGをLNG受け
入れ中の払出タンク7へ送り出す。 【0015】圧力タンク2内のLNGが払い出しされた
後、加圧弁33および払出弁51を閉止し、減圧弁61
を開き、圧力タンク2内を減圧する。続いて、液中弁2
1を開きLNG貯槽1内のLNG11を再び、圧力タン
ク2内へ流入させる。更に圧力タンク2内を加圧し、L
NGを加圧払出管5より払い出す。以上の操作を繰り返
すことにより、LNG貯槽1内のLNG11を払出タン
ク7へ移送する。 【0016】また、他方の払出タンク7においては、払
出タンク加圧弁81を開き払出タンク7を加圧し、更に
気化払出弁75を開き払出タンク7内のLNGを気化装
置73へ送る。気化装置73へ送られたLNGは外熱に
より気化し、気化ガス管74へ送られる。 【0017】払出タンク7のLNGの払い出しが終った
後、払出弁51および気化払出弁75を閉止し、BOG
払出弁92を開きBOG圧縮機91を運転し、払出タン
ク7内の圧力を下げる。払出タンク7内の圧力が下がっ
た後、前述の手順にてLNG貯槽1内のLNG11を払
出タンク7へ移送する。 【0018】 【発明の効果】本発明は上述のように、大型のLNG貯
槽の内部に加圧用の圧力タンク2を設けており、LNG
の昇圧および払い出しが弁の開閉で行うことが可能であ
り、構造が複雑で高価なLNGポンプの使用を避けるこ
とができ、異常振動を常時監視し故障診断を行う必要が
なく、またポンプ内のLNGが気化し運転に支障をきた
すことがない利点がある。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for pressurizing a low-temperature liquefied gas such as liquefied natural gas (hereinafter referred to as LNG) and transferring it from a storage tank or the like. . 2. Description of the Related Art Conventionally, in order to transfer LNG in a large-sized low-pressure storage tank, an electric LNG pump is charged into the LNG liquid, and LNG or the like is pressurized and transferred. [0003] However, the electric LNG
In the installation of the pump, not only maintenance and management are required, such as constantly monitoring abnormal vibrations and performing fault diagnosis, but also there is a problem that LNG in the pump is vaporized and hinders operation. An object of the present invention is to realize a pressurized LNG transfer method without using an LNG pump in a large low-pressure LNG storage tank. [0004] In order to solve the above-mentioned problems, the present invention provides a submerged valve 21 which is opened and closed by a submerged valve driving device 22 in an LNG storage tank 1, a pressurized discharge pipe 5, and a pump. Pressure reducing tube 3
4 is installed, and L is controlled by a submerged valve 21.
The LNG 11 in the NG storage tank 1 is allowed to flow into the pressure tank 2, and the pressure in the pressure tank 2 is increased by the pressurizing and depressurizing pipe 34.
G is paid out. [0005] The pressure reducing valve 61 is opened to reduce the pressure in the pressure tank 2, the submerged valve 21 is opened and the LNG 1
After the submerged valve 1 and the pressure reducing valve 61 are closed, the pressurizing valve 33 is opened to pressurize the inside of the pressure tank 2. Subsequently, the discharge valve 51 is opened to discharge LNG in the pressure tank 2. The LNG pressurized in the pressure tank 2 is discharged from the pressurized discharge pipe 5 to the discharge tank 7. Further, after the LNG in the pressure tank 2 is discharged, the pressure in the pressure tank 2 is reduced by the same procedure, the LNG 11 flows into the pressure tank 2 from the LNG storage tank 1 again, and the pressure in the pressure tank 2 is further increased to discharge the LNG. . By repeating such an operation, the LNG 11 in the LNG storage tank 1 is transferred. Embodiments of the present invention will be described below with reference to the drawings. The LNG transfer device of the present invention, as shown in FIG.
The pressure tank 2 is installed in the LNG storage tank 1 and the pressure tank 2
A submerged valve 21 is provided at the lower part, and LNG 11 is provided in the pressure tank 2.
And a pressure reducing pipe 34 is connected so that the pressure in the pressure tank 2 can be reduced and reduced. Further, a pressure discharging pipe 5 is provided to discharge LNG in the pressure tank 2. The pressure reducing pipe 6 is provided with a pressure reducing valve 61.
By opening 1, the pressure in the pressure tank 2 is reduced, and by further opening the submerged valve 21, the LNG 11 in the LNG storage tank 1 flows into the pressure tank 2. [0008] The pressurizing pipe 35 is connected to the lower part of the dispensing tank 7,
An evaporation control valve 31, a pressure evaporator 32, and a pressure valve 33 are provided. The pressurizing pipe 35 is pressurized by the vaporized gas obtained by vaporizing LNG by the pressurized evaporator 32. By opening the pressurizing valve 33, the vaporized gas flows into the pressure tank 2 and pressurizes the pressure tank 2. A discharge valve 51 is provided in the pressurized discharge pipe 5, and the pressure L in the pressure tank 2 is increased by opening the discharge valve 51.
NG is dispensed to the dispensing tank 7. Next, an example of use of the gas pressure type LNG transfer device of the present invention will be described in detail. L provided in LNG storage tank 1
The NG receiving pipe 4 receives the LNG 11. Further, the opening of the pressure control valve 31 is adjusted so that the pressure in the pressure pipe 35 becomes constant. LN flowing into pressurized evaporator 32
G evaporates and expands to increase the pressure in the pressure tube 35. Two dispensing tanks 7 are provided. One dispensing tank 7 receives the LNG 11 in the LNG storage tank 1, and the other dispensing tank 7 dispenses LNG to the vaporizer 73. The two discharge tanks 7 alternately receive the LNG from the LNG storage tank 1 and discharge the LNG to the vaporizer 73. In the discharge tank 7 receiving LNG from the LNG storage tank 1, the BOG discharge valve 92 is opened,
The BOG compressor 91 is operated to reduce the pressure in the discharge tank 7 to a constant pressure. Also, LN is sent to the other vaporizer 73.
In the dispensing tank 7 that dispenses G, the dispensing tank pressurizing valve 81 is opened to pressurize the dispensing tank 7. In the above state, first, the pressure reducing valve 61 is opened to lower the pressure in the pressure tank 2 to the same or less than the pressure in the LNG storage tank 1. Subsequently, the submerged valve 21 is opened and LN
Due to the pressure difference between the G storage tank 1 and the pressure tank 2, the LNG storage tank 1
LNG 11 in the tank is caused to flow into the pressure tank 2. In addition,
The decompression pipe 6 may be connected to the upper part of the LNG storage tank 1 so that the gas at the time of decompression can be collected in the LNG storage tank 1. With the pressure tank 2 filled with LNG, the submerged valve 21 and the pressure reducing valve 61 are closed. continue,
The pressure valve 33 is opened to increase the pressure in the pressure tank 2. In this state, the discharge valve 51 connected to the discharge tank 7 receiving LNG is opened, and the LNG in the pressure tank 2 is sent out to the discharge tank 7 receiving LNG. After the LNG in the pressure tank 2 is discharged, the pressure valve 33 and the discharge valve 51 are closed, and the pressure reducing valve 61 is discharged.
Is opened, and the pressure in the pressure tank 2 is reduced. Subsequently, the submerged valve 2
1, the LNG 11 in the LNG storage tank 1 is allowed to flow into the pressure tank 2 again. Further, the pressure in the pressure tank 2 is increased, and L
NG is dispensed from the pressure dispensing pipe 5. By repeating the above operation, the LNG 11 in the LNG storage tank 1 is transferred to the discharge tank 7. In the other discharging tank 7, the discharging tank pressurizing valve 81 is opened to pressurize the discharging tank 7, and the vaporizing discharging valve 75 is further opened to send the LNG in the discharging tank 7 to the vaporizing device 73. The LNG sent to the vaporizer 73 is vaporized by external heat and sent to the vaporized gas pipe 74. After the dispensing of LNG from the dispensing tank 7, the dispensing valve 51 and the vaporizing dispensing valve 75 are closed, and the BOG is discharged.
The discharge valve 92 is opened, the BOG compressor 91 is operated, and the pressure in the discharge tank 7 is reduced. After the pressure in the dispensing tank 7 decreases, the LNG 11 in the LNG storage tank 1 is transferred to the dispensing tank 7 by the above-described procedure. According to the present invention, as described above, the pressure tank 2 for pressurizing is provided inside the large LNG storage tank, and the LNG
Pressure can be increased and decreased by opening and closing the valve, the use of an expensive LNG pump having a complicated structure can be avoided, and there is no need to constantly monitor abnormal vibrations and perform failure diagnosis. There is an advantage that LNG does not vaporize and hinder driving.

【図面の簡単な説明】 【図1】 本発明の説明図である。 【符号の説明】 1 LNG貯槽 2 圧力タンク 21 液中弁 33 加圧弁 51 払出弁 61 減圧弁[Brief description of the drawings] FIG. 1 is an explanatory diagram of the present invention. [Explanation of symbols] 1 LNG storage tank 2 Pressure tank 21 Submerged valve 33 Pressure valve 51 Dispensing valve 61 Pressure reducing valve

Claims (1)

【特許請求の範囲】 【請求項1】 LNG貯槽1内に設置した圧力タンク2
内を減圧することによりLNGの如き低温液化ガスをL
NG貯槽1より流入せしめ、圧力タンク2内を加圧する
ことにより低温液化ガスを加圧した状態で払い出しを行
い、圧力タンク2内の減圧および加圧を繰り返すことに
より低温液化ガスの移送を行う装置。
Claims: 1. A pressure tank 2 installed in an LNG storage tank 1.
By depressurizing the inside, low temperature liquefied gas such as LNG
A device that flows in from the NG storage tank 1, discharges the pressurized low-temperature liquefied gas by pressurizing the pressure tank 2, and transfers the low-temperature liquefied gas by repeating depressurization and pressurization in the pressure tank 2. .
JP2001287214A 2001-09-20 2001-09-20 Gas pressure type lng transfer device Pending JP2003090497A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001287214A JP2003090497A (en) 2001-09-20 2001-09-20 Gas pressure type lng transfer device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001287214A JP2003090497A (en) 2001-09-20 2001-09-20 Gas pressure type lng transfer device

Publications (1)

Publication Number Publication Date
JP2003090497A true JP2003090497A (en) 2003-03-28

Family

ID=19110060

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001287214A Pending JP2003090497A (en) 2001-09-20 2001-09-20 Gas pressure type lng transfer device

Country Status (1)

Country Link
JP (1) JP2003090497A (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100708523B1 (en) 2006-08-08 2007-04-16 한국가스공사 System and method for refueling lng without power
JP2009079600A (en) * 2007-09-25 2009-04-16 Nissan Diesel Motor Co Ltd Natural gas feeder
JP2015025496A (en) * 2013-07-25 2015-02-05 東京ガス・エンジニアリング株式会社 Cryogenic liquid storage facility
KR20220096459A (en) * 2020-12-31 2022-07-07 한국가스공사 Liquefied Gas Emergency Supply System and Method

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100708523B1 (en) 2006-08-08 2007-04-16 한국가스공사 System and method for refueling lng without power
JP2009079600A (en) * 2007-09-25 2009-04-16 Nissan Diesel Motor Co Ltd Natural gas feeder
JP2015025496A (en) * 2013-07-25 2015-02-05 東京ガス・エンジニアリング株式会社 Cryogenic liquid storage facility
KR20220096459A (en) * 2020-12-31 2022-07-07 한국가스공사 Liquefied Gas Emergency Supply System and Method
KR102446871B1 (en) * 2020-12-31 2022-09-30 한국가스공사 Liquefied Gas Emergency Supply System and Method

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