JPH0419424B2 - - Google Patents
Info
- Publication number
- JPH0419424B2 JPH0419424B2 JP14699187A JP14699187A JPH0419424B2 JP H0419424 B2 JPH0419424 B2 JP H0419424B2 JP 14699187 A JP14699187 A JP 14699187A JP 14699187 A JP14699187 A JP 14699187A JP H0419424 B2 JPH0419424 B2 JP H0419424B2
- Authority
- JP
- Japan
- Prior art keywords
- hot water
- evaporator
- gas
- lng
- 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.)
- Expired - Lifetime
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 85
- 239000003949 liquefied natural gas Substances 0.000 claims description 28
- 238000010438 heat treatment Methods 0.000 claims description 21
- 239000007789 gas Substances 0.000 claims description 16
- 238000001704 evaporation Methods 0.000 claims description 10
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 9
- 229910001873 dinitrogen Inorganic materials 0.000 claims description 9
- 230000008020 evaporation Effects 0.000 claims description 7
- 239000007788 liquid Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 3
- 239000000446 fuel Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000010248 power generation Methods 0.000 description 3
- 230000006378 damage Effects 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000013535 sea water Substances 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 229910000838 Al alloy Inorganic materials 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
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
- F17C9/00—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
- F17C9/02—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure with change of state, e.g. vaporisation
-
- 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
- F17C2201/0109—Shape cylindrical with exteriorly curved 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
- F17C2221/00—Handled fluid, in particular type of fluid
- F17C2221/01—Pure fluids
- F17C2221/014—Nitrogen
-
- 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
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/03—Heat exchange with the fluid
- F17C2227/0302—Heat exchange with the fluid by heating
- F17C2227/0309—Heat exchange with the fluid by heating using another fluid
- F17C2227/0316—Water heating
-
- 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
- F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
- F17C2227/03—Heat exchange with the fluid
- F17C2227/0367—Localisation of heat exchange
- F17C2227/0388—Localisation of heat exchange separate
- F17C2227/0393—Localisation of heat exchange separate using a vaporiser
-
- 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
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/04—Indicating or measuring of parameters as input values
- F17C2250/0404—Parameters indicated or measured
- F17C2250/0408—Level 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)
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 Field of Industrial Application 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イリ
イテイも少ないことから最も省エネ的である。本
方式はアルミ合金製等のフイ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
器ではシエル&チユ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。
加熱用の温水はポンプ、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。Conventional technology 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 coming. Since LNG has already been refined locally at its production site, it can be used as city gas as is by evaporating it and adjusting its calorie content with LPG or air, so demand for it as city gas in small and medium-sized cities in rural areas is increasing. 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-temperature evaporation method utilizes the heat possessed by natural air, and is the most energy-saving method because it requires less heat source and other utilities. In this method, LNG is passed through a group of vertical tubes with fins made of aluminum alloy, etc., and heat is transferred by generating natural convection of air on the outside of the tubes. It has advantages such as easy operation and maintenance. 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 achieve low temperature.
LNG is heated with hot water and vaporized.
Hot water for heating is supplied to the evaporator by connecting a pump, gas-fired or steam heating type heater, etc. with a pipe to form a hot water heating circulation line. However, the hot water heating type evaporator described above has the following problems that must 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つているため停電時
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ツクアツプするがどうし
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。この間温水循環は
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 LNG hot water heating type evaporator as described above, hot water circulation is dependent on an electric pump, so in the event of a power outage, the pump will stop driving and the hot water circulation will also stop. . If a city gas production factory does not have a large gas holder, it usually has its own in-house power generation equipment, and when there is a power outage, the in-house power generation equipment is immediately activated and backed up, but the rated output cannot be reached. A short power outage (usually less than 1 minute) is unavoidable until this happens. During this time, hot water circulation stops, and in the evaporator, the latent heat of vaporization of the LNG steals heat from the hot water side, causing the temperature to drop below zero and 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用温水加熱式蒸
発装置の問題点を解決すべくなされたものであつ
てその要旨とするところは、温水レシーバーから
導出する温水を循環ポンプにより温水ヒータに送
出して所定温度に加熱した後、前記温水を蒸発器
に供給し液化天然ガスの蒸発に利用した後、前記
温水を温水レシーバーに戻し循環使用する液化天
然ガスの温水加熱式蒸発装置に於て、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つて、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LNGの温水加熱式蒸発装置である。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。図に於て1はシエル&チユーブ式の
LNGの蒸発器であり、シエル側にLNG、チユー
ブ側に加熱用の温水を夫々通している。2は温水
レシーバーであり蒸発器1を出る温水を受け入れ
るとともに温水循環ポンプ3のサクシヨンタンク
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の間に設置されてその内部圧
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
用してヘツドタンク方式としてもよい。Means for Solving the Problems The present invention has been made to solve the problems of the conventional hot water heating type evaporator for LNG as described above, and its gist is to After the hot water is sent to a hot water heater by a circulation pump and heated to a predetermined temperature, the hot water is supplied to an evaporator and used for evaporation of liquefied natural gas, and then the hot water is returned to a hot water receiver for circulation. The type evaporator is characterized by being equipped with a hot water holder in the pipe line between the hot water heater and the evaporator, which is pressurized to an appropriate pressure with gas such as nitrogen gas and holds a hot water flow rate for the required time. This is a hot water heating type evaporation device for liquefied natural gas.Although it is a very simple device, it can supply vaporized LNG gas without freezing hot water even during a power outage, and without interrupting the supply of vaporized LNG gas. This is a new LNG hot water heating type evaporation device. The contents of the present invention will be further explained in detail based on the drawings. FIG. 1 is a flow diagram showing an embodiment of the apparatus according to the present invention. In the diagram, 1 is the Ciel & Tube type.
This is an LNG evaporator, with LNG flowing through the shell side and hot water for heating through the tube side. A hot water receiver 2 receives the 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 the heating furnace. Reference numeral 5 denotes a hot water holder, which is installed between the hot water heater 4 and the evaporator 1, and whose internal pressure is increased by nitrogen gas from a nitrogen gas cylinder to approximately the same pressure as the connecting pipe using a pressure regulator 9. The water level 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。温水レシーバー2から抜き出される温水は
循環ポンプ3によつ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。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1のチユーブ側に流
入しシエル側の低温LNGに蒸発熱を供給した後
温水レシーバー2に戻る。この温水循環量は蒸発
器1と温水レシーバー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ー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
再開すれば温水レシーバー内の温水は徐々に温水
ヒーター4を通つた後温水ホルダー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. 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 exits the hot water heater 4. Next, 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 1 at this pressure and returns to the hot water receiver 2 after supplying the heat of evaporation to the low temperature LNG on the shell side. 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 indicator controller 8 installed in a 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, flows into the evaporator 1, supplies heat of vaporization to the low-temperature LNG, and exits the evaporator 1 as in normal times. and 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 restarts due to energization, the hot water in the hot water receiver gradually passes through the hot water heater 4 and is transferred to the hot water holder 5, but at this time, the nitrogen gas in the hot water holder 5 is released by opening the vent valve. You need to take 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 structure and operation, hot water for heating can be flowed in the same manner as in normal times even during a power outage, despite the extremely simple device.
The present invention is extremely useful industrially because it can eliminate the problem of freezing hot water in the evaporator without interrupting the generation of LNG gas.
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…温水レシーバー、3…温水循
環ポンプ、4……温水ヒーター、5…温水ホルダ
ー、L…LNG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 receiver, 3...Hot water circulation pump, 4...Hot water heater, 5...Hot water holder, L...LNG liquid, G...LNG gas, F...Fuel, W
...Supplementary water.
Claims (1)
ンプ3により温水ヒータ4に送出して所定温度に
加熱した後、前記温水を蒸発器1に供給し液化天
然ガスの蒸発に利用した後、前記温水を温水レシ
ーバー2に戻し循環使用する液化天然ガスの温水
加熱式蒸発装置に於て、温水ヒータ4と蒸発器1
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5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。1. After sending the hot water derived from the hot water receiver 2 to the hot water heater 4 by the circulation pump 3 and heating it to a predetermined temperature, the hot water is supplied to the evaporator 1 and used for evaporation of liquefied natural gas, and then the hot water is converted into hot water. In a hot water heating type evaporator for liquefied natural gas that is returned to the receiver 2 for circulation, a hot water heater 4 and an evaporator 1 are installed.
A hot water heating type evaporator for liquefied natural gas, comprising a hot water holder 5 which is pressurized to an appropriate pressure with a gas such as nitrogen gas and holds an amount of hot water for a necessary time in a pipe line between the liquefied natural gas and the like.
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 JPS63312599A (en) | 1988-12-21 |
| JPH0419424B2 true 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) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP5330030B2 (en) * | 2009-03-03 | 2013-10-30 | 株式会社神戸製鋼所 | Low temperature liquefied gas vaporizer and low temperature liquefied gas vaporization method |
-
1987
- 1987-06-15 JP JP62146991A patent/JPS63312599A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS63312599A (en) | 1988-12-21 |
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