JPS63312599A - Hot water heating type evaporator for liquefied natural gas - Google Patents

Hot water heating type evaporator for liquefied natural gas

Info

Publication number
JPS63312599A
JPS63312599A JP62146991A JP14699187A JPS63312599A JP S63312599 A JPS63312599 A JP S63312599A JP 62146991 A JP62146991 A JP 62146991A JP 14699187 A JP14699187 A JP 14699187A JP S63312599 A JPS63312599 A JP S63312599A
Authority
JP
Japan
Prior art keywords
hot water
hot
evaporator
water
holder
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.)
Granted
Application number
JP62146991A
Other languages
Japanese (ja)
Other versions
JPH0419424B2 (en
Inventor
Hiromasa Ariga
有賀 博政
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 Kakoki Kaisha Ltd
Original Assignee
Mitsubishi Kakoki Kaisha 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 Kakoki Kaisha Ltd filed Critical Mitsubishi Kakoki Kaisha Ltd
Priority to JP62146991A priority Critical patent/JPS63312599A/en
Publication of JPS63312599A publication Critical patent/JPS63312599A/en
Publication of JPH0419424B2 publication Critical patent/JPH0419424B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C9/00Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
    • F17C9/02Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure with change of state, e.g. vaporisation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2201/00Vessel construction, in particular geometry, arrangement or size
    • F17C2201/01Shape
    • F17C2201/0104Shape cylindrical
    • F17C2201/0109Shape cylindrical with exteriorly curved end-piece
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2221/00Handled fluid, in particular type of fluid
    • F17C2221/01Pure fluids
    • F17C2221/014Nitrogen
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2221/00Handled fluid, in particular type of fluid
    • F17C2221/03Mixtures
    • F17C2221/032Hydrocarbons
    • F17C2221/033Methane, e.g. natural gas, CNG, LNG, GNL, GNC, PLNG
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2223/00Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0146Two-phase
    • F17C2223/0153Liquefied gas, e.g. LPG, GPL
    • F17C2223/0161Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2227/00Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03Heat exchange with the fluid
    • F17C2227/0302Heat exchange with the fluid by heating
    • F17C2227/0309Heat exchange with the fluid by heating using another fluid
    • F17C2227/0316Water heating
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2227/00Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/03Heat exchange with the fluid
    • F17C2227/0367Localisation of heat exchange
    • F17C2227/0388Localisation of heat exchange separate
    • F17C2227/0393Localisation of heat exchange separate using a vaporiser
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C2250/00Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/04Indicating or measuring of parameters as input values
    • F17C2250/0404Parameters indicated or measured
    • F17C2250/0408Level of content in the vessel

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)

Abstract

PURPOSE:To supply vaporized LNG gas even at the time of service interruption by providing a hot-water holder holding a flow of hot water for required time in a pipeline between hot-water heater for heating and an evaporator. CONSTITUTION:A hot-water holder 5 is disposed between a hot-water heater 4 and an evaporator 1, the internal pressure thereof is increased to be substantially equal to the pressure in a connecting pipeline with nitrogen gas from a nitrogen gas bomb by a pressure controller 9, and the internal water level is kept at a designated position by a level controller 7. When the operation of a hot-water circulating pump 3 is stopped due to service interruption, hot water in the hot water holder 5 is pushed out by the internal pressure to flow in the evaporator 1, and heat of evaporization is supplied to low-temperature LNG similarly to the ordinary case, whereby hot water is let out of the evaporator 1 to be transferred to a hot-water receiver 2.

Description

【発明の詳細な説明】 産業上の利用分野) 本発明は液化天然ガスの温水加熱式蒸発装置に関する。[Detailed description of the invention] industrial application field) The present invention relates to a hot water heating type evaporator for liquefied natural gas.

従来技術) 液化天然ガス(以下LNGという)は供給及び価格が安
定していること、さらには公害の少ないクリーンエネル
ギーであること等のため電力、都市ガス、鉄鋼等の大口
需要に近年盛んに用いられてきている。LNGは生産地
の現地で既に精製が済んでいるため蒸発気化しLPG又
は空気等でカロリー調整すればそのまま都市ガスとして
使用できることから地方の中小都市の都市ガス用として
も需要が広がりつつある。このLNGの蒸発気化には大
容量のものには熱源として海水を用いる海水加熱方式が
小容量のものには空気を用いる空温式蒸発方式が一般的
に用いられている。空温式蒸発方式は天然の空気の有し
ている熱を利用するものであり熱源はもとよりその他の
所要ユーティリイティも少ないことから最も省エネ的で
ある0本方式はアルミ合金製等のフィン付の垂直管群の
伝熱管内にLNGを通し、管外側には空気の自然対流を
生ぜしめて伝熱を行うものであり前記の如く省エネ的で
あると同時に運転の維持管理も容易である等の利点を有
している。しかし冬期間のように大気温度が低下する場
合にはこの空温式蒸発方式は使用できず代りに温水加熱
式蒸発器を別に設置し切換えて使用している。この温水
加熱式蒸発器ではシェル及チュー ブ型の蒸発器を用い
低温のLNGを温水により加熱して蒸発気化している。
Prior art) Liquefied natural gas (hereinafter referred to as LNG) has been widely used in recent years for large-scale demand such as electricity, city gas, and steel because its supply and price are stable and it is a clean energy with little pollution. It's been getting worse. Since LNG has already been refined locally at the production site, it can be used as city gas by evaporating it and adjusting its calorie content with LPG or air, so demand is increasing for city gas in small and medium-sized cities in rural areas. For the evaporation of LNG, a seawater heating method using seawater as a heat source is generally used for large-capacity products, and an air-heating evaporation method using air for small-capacity products. The air-heated evaporation method utilizes the heat contained in natural air, and requires less heat sources and other utilities. LNG is passed through the heat transfer tubes of the vertical tube group, and heat is transferred by generating natural convection of air on the outside of the tubes.As mentioned above, it is energy-saving and has the advantages of easy operation and maintenance. have. However, when the atmospheric temperature drops, such as during the winter, this air heating evaporation system cannot be used, and instead a hot water heating evaporator is installed separately and used. This hot water heating type evaporator uses a shell and tube type evaporator to heat low-temperature LNG with hot water and vaporize it.

加熱用の温水(まポンプ、ガス焚き或いはスチーム加熱
式のヒータ等を管路にて接続し温水の加熱循環ラインを
構成し前記蒸発器に温水を供給している。しかしながら
以上の温水加熱式蒸発装置には次のような解決すべき問
題点がある。
Hot water for heating (pump, gas-fired or steam heating type heater, etc.) is connected via a pipe to form a hot water heating circulation line to supply hot water to the evaporator. However, the hot water heating type evaporation described above The device has the following problems to be solved.

発明が解決しようとする問題点) 前記の様なLNGの温水加熱式蒸発装置に於ては温水循
環は電動ポンプによっているため停電時にはポンプが駆
動を停止するので温水循環も停止することになる。都市
ガス製造工場に於ては大きなガスホルダーを持たない場
合には通常は自家発電設備を有しており買電が停電の際
はこの自家発電設備を直ちに起動しバックアップするが
どうしても定格の出力が得られる迄短時間の停電(通常
は1分以内)は避けられない、この間湯水循環は停止し
、蒸発器内に於てはLNGの蒸発潜熱のため温水側は熱
をうばわれて温度が低下し零度以下となり伝熱管内に凍
結することになる。この伝熱管内の一旦凍結した氷を解
凍することは容易でないのみならず蒸発器の破壊にも至
る重大な損傷を与える恐れもある。この問題を解消する
方法として停電時には蒸発器への低温LNGの流入を遮
断しそして蒸発器内の水も弁操作により直ちに外部に抜
き出す方法もあるが緊急時の弁操作が大変なこととこの
間の気化LNGガスの供給中断を補償するためにはガス
ホルダーの設置が必要である等の不都合がある。
Problems to be Solved by the Invention) In the above-mentioned LNG hot water heating type evaporator, hot water circulation is carried out by an electric pump, so when a power outage occurs, the pump stops driving and the hot water circulation also stops. If a city gas production factory does not have a large gas holder, it usually has its own in-house power generation equipment, and in the event of a power outage, this in-house power generation equipment is immediately activated for backup, but the rated output cannot be reached. A short-term power outage (usually within 1 minute) is unavoidable until this happens.During this time, hot water circulation stops, and in the evaporator, heat is taken away from the hot water side due to the latent heat of evaporation of the LNG, causing the temperature to drop. The temperature will drop below zero and it will freeze inside the heat transfer tube. It is not only difficult to thaw the ice once frozen inside the heat exchanger tubes, but also there is a risk of causing serious damage, including destruction of the evaporator. One way to solve this problem is to cut off the flow of low-temperature LNG into the evaporator in the event of a power outage, and immediately drain the water inside the evaporator to the outside by operating a valve, but it is difficult to operate the valve in an emergency, and the There are inconveniences such as the need to install a gas holder to compensate for interruptions in the supply of vaporized LNG gas.

問題点を解決するための手段) 本発明は如上の従来型のLNG用温水温水加熱式蒸発装
置題点を解決すべくなされたものであってその要旨とす
るところは加熱した温水により液化天然ガスを蒸発する
蒸発装置に於て、加熱用の温水ヒータと蒸発器の間の管
路中に窒素ガス等の気体により適宜圧力に加圧され必要
時間分の温水流量を保有する温水ホルダーを具備するこ
とを特徴とする液化天然ガスの温水加熱式蒸発装置であ
って、非常に簡単な装置であるにもかかわらず停電時に
も温水を凍結することなしにしかも気化したLNGガス
を中断、することなしに供給することができる新規なL
NGの温水加熱式蒸発装置である。
Means for Solving the Problems) The present invention has been made to solve the problems of the conventional hot water hot water heating type evaporator for LNG as described above, and its gist is to evaporate liquefied natural gas using heated hot water. In an evaporator that evaporates water, a hot water holder is provided in the pipe between the hot water heater and the evaporator, which is pressurized to an appropriate pressure with gas such as nitrogen gas and holds the flow rate of hot water for the required time. This is a hot water heating type evaporation device for liquefied natural gas, and although it is a very simple device, the hot water does not freeze even during a power outage, and the vaporized LNG gas is not interrupted. A new L that can be supplied to
This is an NG hot water heating type evaporator.

本発明の内容を図面に基づきさらに詳述する。第1図は
本発明に係る装置の一実施例を示すフロー系統図である
0図に於て1はシェル及チュー1式のLNGの蒸発器で
あり、シェル側にLNG、チューブ側に加熱用の温水を
夫々通している。2は温水レシーバ−であり蒸発器1を
出る温水を受は入れるとともに温水循環ポンプ3のサク
ションタンクの役目も果している。4は加熱炉型の温水
ヒーターであり都市ガス等の燃料を燃焼して循環温水を
所要温度に加熱昇温し、その温水の出口温度は温度指示
調節計6により燃料量を調節して所定温度に制御される
。加熱炉の代りにスチーム加熱の熱交換器でもよい、5
は温水ホルダーであり温水ヒーター4と蒸発器1の間に
設置されその内部圧力は窒素ガスボンベからの窒素ガス
により圧力調節計9を用いて接続管路と略同じ圧力迄昇
圧され、その内部水位は液面調節計7により所定位置に
維持される。圧力空気がある場合には窒素ガスの代りに
この空気を用いて加圧してもよいし水に不溶性であれば
他の不凝縮ガスでもよい。又ガスによる加圧の代りに高
い構築物があればこれを利用してヘッドタンク方式とし
てもよい。
The contents of the present invention will be further explained in detail based on the drawings. Fig. 1 is a flow system diagram showing one embodiment of the device according to the present invention. hot water is passed through each. 2 is a hot water receiver which receives hot water coming out of the evaporator 1 and also serves as a suction tank for the hot water circulation pump 3. Reference numeral 4 is a furnace-type hot water heater that burns fuel such as city gas to heat the circulating hot water to a required temperature, and the outlet temperature of the hot water is set to a predetermined temperature by adjusting the amount of fuel with a temperature indicator controller 6. controlled by. A steam heating heat exchanger may be used instead of a heating furnace.5
is a hot water holder, which is installed between the hot water heater 4 and the evaporator 1, and its internal pressure is increased by nitrogen gas from a nitrogen gas cylinder to approximately the same pressure as the connecting pipe using the pressure regulator 9, and its internal water level is It is maintained at a predetermined position by a liquid level controller 7. If pressurized air is available, this air may be used instead of nitrogen gas for pressurization, or other non-condensable gas may be used as long as it is insoluble in water. Alternatively, instead of pressurizing with gas, if there is a high structure, it may be used as a head tank system.

作 用) 以上の構成からなる本発明の作用について説明する。温
水レシーバ−2から抜き出される温水は循環ポンプ3に
よって昇圧され温水ヒーター4に入り加熱されて温度指
示調節計6により所定温度(一般には80℃前後)に制
御されて温水ヒーター4を出る0次いで温水ホルダー5
に入るがその入る量は液面調節計7のコントロール弁に
より制御されるが、実質的には温水ホルダー5を出る温
水流量に比例することになる。温水ホルダー5内の圧力
は圧力調節計9により適宜窒素ガスを導入して所定圧力
以上に常時維持される。温水ホルダー内の温水はこの圧
力で蒸発器lのチューブ側に流入しシェル側の低温LN
Gに蒸発熱を供給した後温水レシーバ−2に戻る。この
温水循環量は蒸発器1と温水レシーバ−2の間の管路に
設置される流量指示調節計8により蒸発器1の負荷に応
じて所要流量に制御される。停電により温水循環ポンプ
3が運転停止した時には温水ホルダー5内の温水はその
内部圧力により押し出され蒸発器1に流入し低温LNG
に通常時と同様に蒸発気化熱を供給して蒸発器1を出て
温水レシーバ−2に移送される。温水ホルダー5内の液
面は温水の流出につれて低下するが窒素ガスが圧力調節
計9により導入されるのでその内部圧力は一定に維持さ
れるため温水の流出量も一定量になる。温水ホルダー5
の滞留容量は自家発電設備が起動する迄の時間に相当す
るものであればよく通常は約1分間分の容量とする。通
電により温水循環ポンプ3が起動を再開子れば温水レシ
ーバ−内の温水は徐々に温水ヒーター4を通った後温水
ホルダー5に移送されるがこの際温水ホルダー5内の窒
素ガスはベント弁を開にして抜き出しておく必要がある
。温水ホルダー5内の温水レベルが所定位置に達したら
前記ベント弁を閉にして窒素ガスにより加圧状態にする
Function) The function of the present invention having the above configuration will be explained. The hot water extracted from the hot water receiver 2 is pressurized by the circulation pump 3, enters the hot water heater 4, is heated, is controlled to a predetermined temperature (generally around 80°C) by the temperature indicator controller 6, and leaves the hot water heater 4. hot water holder 5
The amount of hot water entering the hot water holder 5 is controlled by the control valve of the liquid level controller 7, and is substantially proportional to the flow rate of hot water leaving the hot water holder 5. The pressure inside the hot water holder 5 is constantly maintained at a predetermined pressure or higher by appropriately introducing nitrogen gas using a pressure regulator 9. The hot water in the hot water holder flows into the tube side of the evaporator L at this pressure, and the low temperature LN on the shell side flows.
After supplying the heat of evaporation to G, it returns to hot water receiver 2. The amount of hot water circulated is controlled to a required flow rate according to the load on the evaporator 1 by a flow rate indicating controller 8 installed in the pipe between the evaporator 1 and the hot water receiver 2. When the hot water circulation pump 3 stops operating due to a power outage, the hot water in the hot water holder 5 is pushed out by its internal pressure and flows into the evaporator 1, where it is converted into low-temperature LNG.
Heat of evaporation is supplied to the water in the same way as in normal times, and the water leaves the evaporator 1 and is transferred to the hot water receiver 2. The liquid level in the hot water holder 5 decreases as the hot water flows out, but since nitrogen gas is introduced by the pressure regulator 9, the internal pressure is maintained constant, so the amount of hot water flowing out is also constant. hot water holder 5
The retention capacity may be sufficient as long as it corresponds to the time it takes for the private power generation equipment to start up, and it is usually the capacity for about one minute. When the hot water circulation pump 3 is restarted by energization, the hot water in the hot water receiver gradually passes through the hot water heater 4 and then is transferred to the hot water holder 5. At this time, the nitrogen gas in the hot water holder 5 is released through the vent valve. You need to open it and pull it out. When the hot water level in the hot water holder 5 reaches a predetermined level, the vent valve is closed and the water is pressurized with nitrogen gas.

発明の効果) 以上の構成と作用を有する本発明によれば、非常に簡単
な装置にもかかわらず停電時にも加熱用の温水を通常時
と同じ様に流すことができるのでLNGガスの発生を中
断することなく且つ蒸発器内の温水の凍結問題も解消で
きるので本発明は産業上極めて有益である。
Effects of the Invention) According to the present invention having the above-described configuration and operation, hot water for heating can be flowed in the same way as in normal times even during a power outage, despite being a very simple device, so that generation of LNG gas can be prevented. The present invention is extremely useful industrially because it eliminates the problem of hot water freezing in the evaporator without interruption.

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

第1図は本発明に係る装置の一実施例を示すフロー系統
図である。 1:蒸発器、2:温水レジ−°バー、3:温水循環ポン
プ、4:温水ヒーター、5:温水ホルダー、L : L
NG液、G:LNGガス、F:燃料、W:補給水。
FIG. 1 is a flow diagram showing an embodiment of the apparatus according to the present invention. 1: Evaporator, 2: Hot water register - ° bar, 3: Hot water circulation pump, 4: Hot water heater, 5: Hot water holder, L: L
NG liquid, G: LNG gas, F: Fuel, W: Make-up water.

Claims (1)

【特許請求の範囲】[Claims] 加熱した温水により液化天然ガスを蒸発する蒸発装置に
於て、加熱用の温水ヒータと蒸発器の間の管路中に窒素
ガス等の気体により適宜圧力に加圧され且つ必要時間分
の温水量を保有する温水ホルダーを具備することを特徴
とする液化天然ガスの温水加熱式蒸発装置。
In an evaporator that evaporates liquefied natural gas using heated hot water, the pipe between the hot water heater and the evaporator is pressurized to an appropriate pressure with gas such as nitrogen gas, and the amount of hot water for the required time is increased. A hot water heating type evaporator for liquefied natural gas, characterized in that it is equipped with a hot water holder having:
JP62146991A 1987-06-15 1987-06-15 Hot water heating type evaporator for liquefied natural gas Granted JPS63312599A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP62146991A JPS63312599A (en) 1987-06-15 1987-06-15 Hot water heating type evaporator for liquefied natural gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP62146991A JPS63312599A (en) 1987-06-15 1987-06-15 Hot water heating type evaporator for liquefied natural gas

Publications (2)

Publication Number Publication Date
JPS63312599A true JPS63312599A (en) 1988-12-21
JPH0419424B2 JPH0419424B2 (en) 1992-03-30

Family

ID=15420138

Family Applications (1)

Application Number Title Priority Date Filing Date
JP62146991A Granted JPS63312599A (en) 1987-06-15 1987-06-15 Hot water heating type evaporator for liquefied natural gas

Country Status (1)

Country Link
JP (1) JPS63312599A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010203520A (en) * 2009-03-03 2010-09-16 Kobe Steel Ltd Apparatus of vaporizing low-temperature liquefied gas and method of vaporizing low-temperature liquefied gas

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2010203520A (en) * 2009-03-03 2010-09-16 Kobe Steel Ltd Apparatus of vaporizing low-temperature liquefied gas and method of vaporizing low-temperature liquefied gas

Also Published As

Publication number Publication date
JPH0419424B2 (en) 1992-03-30

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