JPH02175393A - Unloading method for lng ship - Google Patents

Unloading method for lng ship

Info

Publication number
JPH02175393A
JPH02175393A JP33006988A JP33006988A JPH02175393A JP H02175393 A JPH02175393 A JP H02175393A JP 33006988 A JP33006988 A JP 33006988A JP 33006988 A JP33006988 A JP 33006988A JP H02175393 A JPH02175393 A JP H02175393A
Authority
JP
Japan
Prior art keywords
tank
lng
gas
liquid
ship
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
JP33006988A
Other languages
Japanese (ja)
Inventor
Junshiro Ishimaru
石丸 純史郎
Hideaki Mitsumaru
三丸 秀昭
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP33006988A priority Critical patent/JPH02175393A/en
Publication of JPH02175393A publication Critical patent/JPH02175393A/en
Pending legal-status Critical Current

Links

Abstract

PURPOSE:To simplify operation and save labor and energy by carrying out unloading from the tank of an LNG ship to a tank on the land and, when the inside of the ship tank becomes atmospheric pressure, feeding an LNG gas under pressure from the land tank into the ship tank by means of a blower and pressurizing the ship tank to unload a liquid into the land tank. CONSTITUTION:By opening a liquid valve 6 and preparing a liquid system, an LNG 20 in a spherical tank 3 is unloaded by means of a liquid storage pump 2. Then, as the liquid in the spherical tank 3 is reduced to approx. 90% liquid level 19, since the volume of a gas phase portion is increased causing a gas phase portion pressure to become atmospheric pressure, a gas valve 11 is opened preparing a gas system and a gas in a land tank 4 is fed under pressure into the spherical tank 3 by means of a gas returning blower 10 to pressurize the inside of the tank 3. At the same time, the unloading from the spherical tank 3 of the ship 1 is carried out by means of the liquid storage pump 2 and the system 8. By this structure, a BOG handling device and a main fuel mode switchover operation can be dispensed with to save labor and energy.

Description

【発明の詳細な説明】 【産業上の利用分野〕 本発明はLNG船の揚荷方法に関する。[Detailed description of the invention] [Industrial application field] The present invention relates to a method for unloading an LNG ship.

〔従来の技術〕[Conventional technology]

外航LNC,船としては、従来、例えば、第2図縦断面
図に示すように、LNG輸送中に重油タンク021内の
LNGがらボイルオフするガス(以下BOGという)の
処理装置として、ガス焚ボイラー022を装備するもの
が知られている。ここで、023は推進器用タービンで
、重油タンク021は常圧に近い状態で運航され、揚荷
は本船の揚荷ポンプにより行われている。
Conventionally, ocean-going LNCs and ships have used gas-fired boilers as processing equipment for the gas (hereinafter referred to as BOG) that boils off from the LNG in the heavy oil tank 021 during LNG transportation, as shown in the vertical cross-sectional view of Figure 2. 022 is known. Here, 023 is a propeller turbine, the heavy oil tank 021 is operated under a state close to normal pressure, and unloading is performed by the ship's lifting pump.

また、第3図縦断面図に示すように、BOG処理装置と
してガス焚ディーゼル024を装備するものも知られて
いる。
Furthermore, as shown in the vertical cross-sectional view of FIG. 3, a BOG processing apparatus equipped with a gas-fired diesel engine 024 is also known.

しかしながら、このようなりOG処理装置を比較的小型
の内航LNG船に適用すると、下記のような欠点が予想
される。
However, when such an OG processing device is applied to a relatively small coastal LNG ship, the following drawbacks are expected.

(1)BOG処理装置が高価で複雑なので、建造コスト
及び運航コストが嵩み、船の経済性が低下する。
(1) Since the BOG processing equipment is expensive and complicated, the construction cost and operation cost increase, and the economic efficiency of the ship decreases.

(2)航路が短く、ガス焚きと重油焚きの主機燃焼モー
ドの切替えが停泊のたびごとに発生するので、乗組員に
繁雑な作業が増えるとともに、省エネル“ギ上からも不
具合である。
(2) The route is short, and the main engine combustion mode must be switched between gas-fired and heavy oil-fired each time the ship berths, which increases the burden of complicated work for the crew and is also problematic in terms of energy conservation.

〔発明が解決しようとする課題〕[Problem to be solved by the invention]

本発明は、このような事情に鑑みて提案されたもので、
高価なりOG処理装置及び面倒な主機燃焼モードの切替
え作業が不要で経済性、省力性、省エネルギ性に優れた
LNG船の揚荷方法を提供することを目的とする。
The present invention was proposed in view of these circumstances, and
The purpose of the present invention is to provide an LNG unloading method for an LNG ship that does not require an expensive OG processing device or a troublesome main engine combustion mode switching operation and is excellent in economy, labor saving, and energy saving.

〔課題を解決するための手段〕[Means to solve the problem]

そのために本発明はLNG船球型タンク内のLNGを揚
液するに当り、内圧が常圧よりも高いLPJG船球型タ
ンクから揚液ポンプ、LNG揚液ラインを通じて陸上球
型タンクへLNGを揚荷する第1工程と内圧が常圧にな
った上記LNG船球型タンクへ上記陸上球型タンクから
戻しガスブロワ−、LNG戻しガスラインを通じてLN
Gガスを圧送することにより上記LNG船球型タンクを
加圧するとともに、上記揚液ポンプ及びLNG揚液ライ
ンを経てLNG船球型タンクの揚液を行う第2工程とよ
りなることを特徴とする。
To this end, the present invention, when pumping LNG in an LNG spherical tank, pumps LNG from an LPJG spherical tank whose internal pressure is higher than normal pressure to a land spherical tank through a pump and an LNG pumping line. The LNG is returned from the land spherical tank to the LNG spherical tank whose internal pressure has become normal pressure through the gas blower and the LNG return gas line.
The method is characterized by comprising a second step of pressurizing the LNG boat-shaped tank by pumping G gas and pumping liquid from the LNG boat-shaped tank via the liquid pump and the LNG pumping line. .

〔作用〕[Effect]

上述の構成により、高価なりOC処理装置及び面倒な主
機燃焼モードの切替え作業が不要で経済性、省力性、省
エネルギ性に優れたLNG船の揚荷方法を得ることがで
きる。
With the above configuration, it is possible to obtain an LNG ship unloading method that is economical, labor-saving, and energy-saving, without requiring an expensive OC treatment device or a troublesome main engine combustion mode switching operation.

〔実施例〕〔Example〕

本発明を内航小型LNG船に適用した一実施例を図面に
ついて説明すると、第1図系統図において、1はタンク
容量約s、ooom’ 程度の内航小型LNG船で、そ
のタンクは球型タンク式、最大使用圧力は約3 ky/
’−rn′IGである。
An embodiment in which the present invention is applied to a small coastal LNG ship will be explained with reference to the drawings. Tank type, maximum working pressure is approximately 3 ky/
'-rn'IG.

2は球型タンク3内に装備されたサブマージプル型の揚
荷ポンプ、4は受入基地5に設けられた最大使用圧力約
2 ky%i’Gの球型タンク式の陸上タンク、6,7
はそれぞれ受入タンク4の液系統8の先端に装置された
液弁、液アーム。
2 is a submerged pull type lifting pump installed in the spherical tank 3; 4 is a spherical tank type land tank with a maximum operating pressure of approximately 2 ky% i'G installed at the receiving base 5; 6, 7
are a liquid valve and a liquid arm installed at the tip of the liquid system 8 of the receiving tank 4, respectively.

9.10.11.12はそれぞれ受入タンク4のガス系
統13に挿入されたガス戻し弁、ガス戻しブロワ−、ガ
ス弁、ガスアームである。
9, 10, 11, and 12 are a gas return valve, a gas return blower, a gas valve, and a gas arm, respectively, inserted into the gas system 13 of the receiving tank 4.

14.15はそれぞれガス系統13から分岐口供給系統
1.6 K合流するBOG処理系統17に挿入されたB
OG圧縮機、バイパス弁、18゜19はそれぞれ球型タ
ンク3内に貯溜されたLNG20の100%液位、90
%液位である。
14 and 15 are B inserted into the BOG processing system 17 which joins the branch port supply system 1.6 K from the gas system 13, respectively.
OG compressor, bypass valve, 18° and 19 respectively indicate the 100% liquid level of LNG20 stored in the spherical tank 3, 90
% liquid level.

このような装置において、LNG船1は航海中に自然蒸
発したBOGを球型タンク3内に蓄積し、その内圧が一
般に3 ky/cm’ G 程度になった比較的高圧の
状態で受入基地5に着桟したのち、関係路管を受入基地
5の液アーム7、ガスアーム12にそれぞれ接続する。
In such a system, the LNG carrier 1 accumulates BOG that has naturally evaporated during the voyage in the spherical tank 3, and the LNG carrier 1 carries it to the receiving terminal 5 in a relatively high-pressure state where the internal pressure is generally about 3 ky/cm'G. After arriving at the berth, the related pipelines are connected to the liquid arm 7 and gas arm 12 of the receiving base 5, respectively.

この状態で、まず第1工程として液弁6を開き液系統ラ
インアップをしたのち、LNG船1の揚荷ポンプ2によ
り球型タンク3内のLNG20を100%液位18の状
態から揚荷する。
In this state, as a first step, the liquid valve 6 is opened and the liquid system is lined up, and then the LNG 20 in the spherical tank 3 is unloaded from the state of 100% liquid level 18 by the unloading pump 2 of the LNG ship 1. .

次いで、球型タンク3内が90%液位19程度になると
、そこの気相部容積が増え、ボイルシャールの法則に従
い気相部圧は常圧になる。
Next, when the inside of the spherical tank 3 reaches a 90% liquid level of about 19, the volume of the gas phase increases, and the pressure of the gas phase becomes normal pressure according to Boyleschard's law.

そこで第2工程として、以降は公知の外航LNG船の揚
荷で行われているように1ガス弁IIを開いてガス系統
ラインアップをしたのち、球型タンク3の内圧を常圧に
維持するため、陸上タンク4のガスをガス戻しブロワ−
10を経由してLNG船1の球型タンク3内へ圧送する
ことによりそれの内部を加圧するとともに、揚荷ポンプ
2及び液系統8を経てLNG船1の球型タンク3の揚液
を行う。
Therefore, as a second step, after opening 1 gas valve II and lining up the gas system, as is done in the unloading of known ocean-going LNG ships, the internal pressure of the spherical tank 3 is maintained at normal pressure. In order to
10 into the spherical tank 3 of the LNG ship 1 to pressurize the inside thereof, and pump liquid from the spherical tank 3 of the LNG ship 1 through the lifting pump 2 and liquid system 8. .

また、球型タンク3が比較的高圧の状態でガス弁11が
開となって了っだ非常事態においても、陸上タンク4は
球型タンクなので、設計圧2 ky/cm I G程度
には十分耐えられるので、実用上安全である。
In addition, even in an emergency situation where the gas valve 11 is opened while the spherical tank 3 is under relatively high pressure, the land tank 4 is a spherical tank, so the design pressure of about 2 ky/cm I G is sufficient. It is safe for practical use because it can withstand it.

なお、上記非常事態の対策別案として、BOG圧縮機1
4のバイパス弁15とガス戻し弁9とを調節して供給系
統16へ直接移送することも可能である。
In addition, as an alternative measure for the above emergency situation, BOG compressor 1
It is also possible to transfer the gas directly to the supply system 16 by adjusting the bypass valve 15 and the gas return valve 9 of 4.

このような方法によれば、揚荷開始時LNG船球型タン
クの内圧が陸上球型タンクの内圧より高くてもLNGを
陸上球型タンクへ揚荷することができるので、下記効果
が奏せられる。
According to this method, even if the internal pressure of the LNG spherical tank is higher than the internal pressure of the land spherical tank at the start of unloading, LNG can be unloaded to the land spherical tank, so the following effects can be achieved. It will be done.

(1)  内航小型LNG船の場合、航海日数が短く球
型タンクσ径も左程大きくないので、現状の球型タンク
でもってBOGをそのまま蓄積しておくことができ、従
って高価なりOG処理装置及びそれの複雑な取扱いが不
要となり、LNG船の経済性、省力性、省エネルギ性が
向上する。
(1) In the case of small coastal LNG ships, the voyage days are short and the spherical tank σ diameter is not as large as the one on the left, so BOG can be stored as is in the current spherical tank, making it expensive to process the OG. The equipment and its complicated handling become unnecessary, improving the economic efficiency, labor saving, and energy saving of the LNG ship.

(2)揚荷開始時、LNG船球型タンクの内圧が高くな
っているので、揚荷ポンプの押込みヘッドが便利に作用
し、従って揚荷時間が短縮する。
(2) At the start of unloading, the internal pressure of the LNG spherical tank is high, so the pushing head of the unloading pump acts conveniently, thus shortening the unloading time.

〔発明の効果〕〔Effect of the invention〕

要するに本発明によれば、LNG船球型タンク内のLN
Gを揚液するに当り、内圧が常圧よりも高いLNG船球
型タンクから揚液ポンプ。
In short, according to the present invention, the LNG in the LNG spherical tank
When pumping G, a pump pumps liquid from an LNG spherical tank whose internal pressure is higher than normal pressure.

LNG揚液ラインを通じて陸上球型タンクへLNGt揚
荷する第1工程と、内圧が常圧になった上記LNG船球
型タンクへ上記陸上球型タンクから戻しガスブロワ−、
LNG戻しガスラインを通じてLNGガスを圧送するこ
とにより上記LNG船球型タンクを加圧するとともに、
上記揚液ポンプ及びLNGI液ラインを経てLNG船球
型タンクの揚液を行う第2工程とよりなることにより、
高価なりOG処理装置及び面倒な主機燃焼モードの切替
え作業が不要で経済性。
A first step of unloading LNG to the land spherical tank through the LNG lifting line, and a gas blower returning the LNG from the land spherical tank to the LNG ship spherical tank whose internal pressure has become normal pressure.
Pressurizing the LNG tank by pressurizing the LNG gas through the LNG return gas line, and
By comprising a second step of pumping liquid into the LNG spherical tank via the liquid pump and the LNGI liquid line,
Economical as there is no need for expensive OG processing equipment or troublesome main engine combustion mode switching work.

省力性、省エネルギ性に優れたLNG船の揚荷方法を得
るから、本発明は産業上極めて有益なものである。
The present invention is industrially extremely useful because it provides an LNG ship unloading method that is excellent in labor-saving and energy-saving properties.

【図面の簡単な説明】[Brief explanation of the drawing]

第1図は本発明を内航小型LNG船に適用した一実施例
を示す系統図である。 第2図、第3図はそれぞれ公知の外航LNG船の異なる
BOG処理装置を示す縦断面図である。 1・・・LNG船、2・・・揚荷ポンプ、3・・・球型
タンク、4・・・陸上タンク、5・・・受入基地、6・
・・液弁、7・・・液アーム、8・・・液系統、9・・
・ガス戻し弁、10・・・ガス戻しプロワ−11・・・
ガス弁、12・・・ガスアーム、13・・・ガス系統、
14・・・BOG圧縮機、15・・・バイパス弁、16
・・・供給系統、17・・・BOG処理系統、18・・
・100%液位、1.9−90%液位、2O−LNG、
FIG. 1 is a system diagram showing an embodiment in which the present invention is applied to a small coastal LNG ship. FIG. 2 and FIG. 3 are longitudinal cross-sectional views showing different BOG processing devices of a known ocean-going LNG ship, respectively. 1... LNG ship, 2... Lifting pump, 3... Spherical tank, 4... Land tank, 5... Receiving base, 6...
...Liquid valve, 7...Liquid arm, 8...Liquid system, 9...
・Gas return valve, 10...Gas return blower 11...
Gas valve, 12... Gas arm, 13... Gas system,
14... BOG compressor, 15... Bypass valve, 16
... Supply system, 17... BOG processing system, 18...
・100% liquid level, 1.9-90% liquid level, 2O-LNG,

Claims (1)

【特許請求の範囲】[Claims]  LNG船球型タンク内のLNGを揚液するに当り、内
圧が常圧よりも高いLNG船球型タンクから揚液ポンプ
、LNG揚液ラインを通じて陸上球型タンクへLNGを
揚荷する第1工程と、内圧が常圧になつた上記LNG船
球型タンクへ上記陸上球型タンクから戻しガスブロワー
、LNG戻しガスラインを通じてLNGガスを圧送する
ことにより上記LNG船球型タンクを加圧するとともに
、上記揚液ポンプ及びLNG揚液ラインを経てLNG船
球型タンクの揚液を行う第2工程とよりなることを特徴
とするLNG船の揚荷方法。
When pumping LNG in an LNG spherical tank, the first step is to unload LNG from the LNG spherical tank, where the internal pressure is higher than normal pressure, to the land spherical tank through the pump and the LNG pumping line. Then, the LNG ship tank is pressurized by pressure-feeding LNG gas from the land tank to the LNG ship tank whose internal pressure has become normal pressure through the return gas blower and the LNG return gas line, and A method for unloading an LNG ship, comprising a second step of pumping liquid into an LNG spherical tank via a liquid pump and an LNG liquid lifting line.
JP33006988A 1988-12-27 1988-12-27 Unloading method for lng ship Pending JPH02175393A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP33006988A JPH02175393A (en) 1988-12-27 1988-12-27 Unloading method for lng ship

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP33006988A JPH02175393A (en) 1988-12-27 1988-12-27 Unloading method for lng ship

Publications (1)

Publication Number Publication Date
JPH02175393A true JPH02175393A (en) 1990-07-06

Family

ID=18228433

Family Applications (1)

Application Number Title Priority Date Filing Date
JP33006988A Pending JPH02175393A (en) 1988-12-27 1988-12-27 Unloading method for lng ship

Country Status (1)

Country Link
JP (1) JPH02175393A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100458142B1 (en) * 1995-10-30 2005-01-31 윌리엄스 파워 캄파니 인코포레이티드 Compressed Natural Gas Transportation Ship Foundation System
KR100952669B1 (en) * 2007-10-09 2010-04-13 대우조선해양 주식회사 Pressure regulating apparatus and lng carrier with the pressure regulating apparatus

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100458142B1 (en) * 1995-10-30 2005-01-31 윌리엄스 파워 캄파니 인코포레이티드 Compressed Natural Gas Transportation Ship Foundation System
KR100952669B1 (en) * 2007-10-09 2010-04-13 대우조선해양 주식회사 Pressure regulating apparatus and lng carrier with the pressure regulating apparatus

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