JPS6124634B2 - - Google Patents
Info
- Publication number
- JPS6124634B2 JPS6124634B2 JP3640178A JP3640178A JPS6124634B2 JP S6124634 B2 JPS6124634 B2 JP S6124634B2 JP 3640178 A JP3640178 A JP 3640178A JP 3640178 A JP3640178 A JP 3640178A JP S6124634 B2 JPS6124634 B2 JP S6124634B2
- Authority
- JP
- Japan
- Prior art keywords
- heat exchanger
- natural gas
- heat
- heat medium
- heated
- 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
Links
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 claims description 26
- 239000003949 liquefied natural gas Substances 0.000 claims description 23
- 239000013535 sea water Substances 0.000 claims description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 18
- 239000002351 wastewater Substances 0.000 claims description 14
- 239000003345 natural gas Substances 0.000 claims description 12
- 238000010438 heat treatment Methods 0.000 claims description 10
- 230000008016 vaporization Effects 0.000 claims description 5
- 239000007788 liquid Substances 0.000 claims description 2
- 238000009834 vaporization Methods 0.000 claims description 2
- 238000007599 discharging Methods 0.000 claims 1
- 239000006200 vaporizer Substances 0.000 description 13
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000009835 boiling Methods 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- 239000004215 Carbon black (E152) Substances 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 238000002485 combustion reaction Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 229930195733 hydrocarbon Natural products 0.000 description 1
- 150000002430 hydrocarbons Chemical class 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- 239000003507 refrigerant 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
- F28—HEAT EXCHANGE IN GENERAL
- F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
- F28D15/00—Heat-exchange apparatus with the intermediate heat-transfer medium in closed tubes passing into or through the conduit walls ; Heat-exchange apparatus employing intermediate heat-transfer medium or bodies
-
- 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
- F17C2201/0138—Shape tubular
-
- 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
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/0323—Valves
-
- 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
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/0352—Pipes
-
- 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
- F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
- F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
- F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
- F17C2205/0352—Pipes
- F17C2205/0358—Pipes coaxial
-
- 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
- F17C2270/00—Applications
- F17C2270/05—Applications for industrial use
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
Description
本発明は、液化天然ガス(LNG)の気化装置
に関し、より詳しくは海水又は温排水を熱源とし
てLNGを気化させ、更に使用に適した温度まで
加熱する装置に関する。
メタンを主成分とするLNGは、常圧で約―160
゜Cの沸点を有しているので、温水又は蒸気を熱
源としてその気化を行なう場合にも氷結による気
化器の閉塞を生じ易い。この様な問題点を一応解
消して現在使用されるLNG気化器としては、主
として以下の如き型式のものがある。
(i) オープンラツク型気化器;この型式の気化器
においては、伝熱管内を上方に送られるLNG
に対し、伝熱管外面に海水を上方から流下させ
ることによりLNGの気化を行なう。しかしな
がら、この型式の気化器においては、伝熱管下
方部分の表面に海水が凍結して熱伝導を妨げや
すく、従つて伝熱面積を増大させる即ち必要以
上に大型の高価な装置としなければならない欠
点である。
(ii) 中間熱媒体式間接加熱気化器;この型式の気
化器においては、気化器本体内に封入されたプ
ロパン、フツ化炭水素等の中間熱媒体を熱水又
は水蒸気で加熱して気化せしめ、気化した中間
熱媒体によつてLNGを気化せしめるととも
に、LNGとの熱交換により再び液化された中
間熱媒体を引続き熱水又は水蒸気して、同様の
操作を繰返し行う。この型式の気化器は、オー
プンラツク型気化器に比して建設費は低いが、
熱水又は水蒸気を使用する必要があるので、操
業費が高くなるていう欠点がある。
(iii) 液中燃焼型気化器;この型式の気化器におい
ては、水中に浸漬されたバーナーにより生成さ
れた燃焼ガスを水中に噴出させ、該水中に配置
された管内を通過するLNGを加熱気化する。
この型式の気化器も、建設費は比較的安価であ
るものの、加熱に要する費用が大きいのが欠点
である。
本発明者は、上記の如き技術の現状に鑑み、
種種実験及び研究を重ねた結果、多管式向流熱
交換器と中間熱媒体式熱交換器とを直列に接続
し、多管式向流熱交換器においては海水又は温
排水とすでに中間熱媒体式熱交換器で気化され
た天然ガスとの間で熱交換を行わせて天然ガス
の加熱を行ない、一方中間熱媒体式熱交換器に
おいては多管式向流熱交換器で使用された水に
より熱媒体の加熱を行ない、該加熱により気化
された熱媒体によりLNGの気化を行なう場合
には、全体として小型の装置により、加熱用燃
料を使用することなく、比較的少量の海水又は
温排水を熱源として、LNGの気化及び加熱を
容易且つ安価に行ない得ることを見出した。本
発明は、この様な新知見に基いて完成されたも
のである。
以下、本発明を図面に示す実施例を参照しつ
つ、更に詳細に説明する。
第1図において、中間熱媒体式間接熱交換器1
と多管式向流熱交換器2とは直列に接続されてい
る。熱源としての海水又は温排水は、ライン3を
経て供給口26から多管式向流熱交換器2に入
り、ここで後述の中間熱媒体交換器1ですでに気
化された天然ガスと向流熱交換を行ない、気化天
然ガスを海水又は温排水の温度に近い、使用に適
した温度まで加熱する。
多管式熱交換器2内での熱交換は、液体(海水
又は温排水)と気体(気化天然ガス)との間で行
なわれるので、気体側の伝熱係数は小さく、又設
計的にも多管式熱交換器2における熱交換量を後
述の中間熱媒体式熱交換器におけるそれよりも小
さくすることが出来る。従つて、多管式熱交換器
2を出る水の温度を多管式熱交換器2に入る水の
温度よりも例えだ2〜3゜C低い程度におされる
ことが出来る。この多管式熱交換器2を出来る水
は、中間熱媒体式熱交換器における中間熱媒体
(廷いてはLNG)の加熱源となり得るに十分な高
温度を有しているていえるので、省資源、省エネ
ルギーの観点から後述の如く再度熱源として有効
に利用される。
多管式熱交換器2の送出口2dを出た水は、ラ
イン4を径て供給口1cから中間熱媒体式熱交換
器1の下方部分1aに入り、プロパン、フツ化炭
化水素等の低沸点の中間熱媒体(冷媒)を加熱し
て気化させた後、排出口1dを経てライン5から
排出されるか或いは低温水として有効に利用され
る。気化された中間熱媒体は、熱交換器1の上方
部分に1bに上昇し、ここでライン6から供給口
1eを経て伝熱管7に供給されてくるLNGと熱
交換を行ない、再び液化されて下方部分1aに戻
る。上方部分1bにおいて中間熱媒体により加熱
されて気化した天然ガスは、1fを出てライン8
を経て多管式熱交換器2の供給口2aに入り、前
述の如く、海水又は温排水により更に加熱され送
出口2cからライン9を経て取り出される。
尚、中間熱媒体式熱交換器1においては、
LNG及び中間熱媒体を高圧下に使用するのが有
利である。
本発明によれば、以下の如き効果が達成され
る。
(i) 海水又は温排水を両熱交換器の熱源として有
効に使用するので、少量の海水又は温排水を使
用するだけで良い。
(ii) 従つて、装置の小型化が可能となり建設費が
著るしく低減される。
(iii) 加熱用燃料を必要とせず且つ少量の海水又は
温排水を使用すれば良いので、操業費も大巾に
低下する。
(iv) 従来装置において避け難かつた管路の閉塞、
伝熱効率の大巾な低下等も生じない。
(v) 中間熱媒体熱交換器から排出される低温の水
を必要分野において有効に利用することが出来
る。
実施例 1〜2
海水を熱源とし、第1図に示す本発明装置を使
用して第1表に示す条件下にLNGの気下及び加
熱を行ない、第1表に示す結果を得た。
The present invention relates to an apparatus for vaporizing liquefied natural gas (LNG), and more particularly to an apparatus for vaporizing LNG using seawater or heated wastewater as a heat source and further heating it to a temperature suitable for use. LNG whose main component is methane is approximately -160 at normal pressure.
Since it has a boiling point of °C, even if it is vaporized using hot water or steam as a heat source, it is likely to clog the vaporizer due to freezing. LNG vaporizers currently in use that have solved these problems are mainly of the following types. (i) Open rack type vaporizer: In this type of vaporizer, LNG is sent upward through heat transfer tubes.
On the other hand, LNG is vaporized by flowing seawater from above onto the outer surface of the heat transfer tube. However, this type of vaporizer has the drawback that seawater tends to freeze on the surface of the lower portion of the heat transfer tube and impede heat transfer, thus increasing the heat transfer area, which means that the device must be larger and more expensive than necessary. It is. (ii) Intermediate heat medium indirect heating vaporizer: In this type of vaporizer, an intermediate heat medium such as propane or fluorinated hydrocarbon sealed in the vaporizer body is heated with hot water or steam to vaporize it. , LNG is vaporized by the vaporized intermediate heat medium, and the intermediate heat medium that is liquefied again by heat exchange with the LNG is subsequently converted into hot water or steam, and the same operation is repeated. This type of vaporizer is less expensive to construct than an open rack vaporizer, but
The disadvantage is that it requires the use of hot water or steam, which increases operating costs. (iii) Submerged combustion type vaporizer: In this type of vaporizer, combustion gas generated by a burner immersed in water is ejected into the water, and LNG passing through a pipe placed in the water is heated and vaporized. do.
Although this type of vaporizer is relatively inexpensive to construct, the disadvantage is that it requires high heating costs. In view of the current state of the technology as described above, the inventors of the present invention
As a result of various experiments and research, we connected a shell-and-tube countercurrent heat exchanger and an intermediate heat medium heat exchanger in series. The intermediate heat exchanger heats the natural gas by exchanging heat with the vaporized natural gas, while the intermediate heat exchanger is used in a shell-and-tube countercurrent heat exchanger. When a heat medium is heated by water and LNG is vaporized by the heat medium vaporized by the heating, a relatively small amount of seawater or heated We have discovered that LNG can be easily and inexpensively vaporized and heated using wastewater as a heat source. The present invention was completed based on such new knowledge. Hereinafter, the present invention will be explained in more detail with reference to embodiments shown in the drawings. In Fig. 1, an intermediate heat medium type indirect heat exchanger 1
and the multi-tubular countercurrent heat exchanger 2 are connected in series. Seawater or heated wastewater as a heat source enters the multi-tubular countercurrent heat exchanger 2 from the supply port 26 via the line 3, where it is countercurrently mixed with the natural gas already vaporized in the intermediate heat medium exchanger 1, which will be described later. Heat exchange is performed to heat the vaporized natural gas to a usable temperature close to that of seawater or heated wastewater. Heat exchange within the shell-and-tube heat exchanger 2 is carried out between liquid (seawater or heated wastewater) and gas (vaporized natural gas), so the heat transfer coefficient on the gas side is small, and also due to the design. The amount of heat exchanged in the shell-and-tube heat exchanger 2 can be made smaller than that in the intermediate heat medium heat exchanger described later. Therefore, the temperature of the water exiting the shell-and-tube heat exchanger 2 can be made lower, for example, by 2 to 3°C, than the temperature of the water entering the shell-and-tube heat exchanger 2. The water used in this multi-tube heat exchanger 2 can be said to have a high enough temperature to serve as a heating source for the intermediate heat medium (or LNG) in the intermediate heat exchanger. From the viewpoint of resource and energy conservation, it can be effectively used again as a heat source as described later. The water that has exited the outlet 2d of the multi-tube heat exchanger 2 passes through the line 4 and enters the lower part 1a of the intermediate heat medium heat exchanger 1 from the supply port 1c. After the intermediate heat medium (refrigerant) at the boiling point is heated and vaporized, it is discharged from the line 5 through the discharge port 1d or is effectively used as low-temperature water. The vaporized intermediate heat medium rises to the upper part 1b of the heat exchanger 1, where it exchanges heat with LNG supplied from the line 6 to the heat transfer tube 7 via the supply port 1e, and is liquefied again. Return to lower part 1a. The natural gas heated and vaporized by the intermediate heat medium in the upper part 1b exits 1f and flows into line 8.
The water then enters the supply port 2a of the multi-tubular heat exchanger 2, is further heated by seawater or heated waste water, and is taken out from the delivery port 2c via the line 9, as described above. In addition, in the intermediate heat medium type heat exchanger 1,
It is advantageous to use LNG and intermediate heat carriers under high pressure. According to the present invention, the following effects are achieved. (i) Since seawater or heated wastewater is effectively used as a heat source for both heat exchangers, only a small amount of seawater or heated wastewater needs to be used. (ii) Therefore, it is possible to downsize the device and the construction cost is significantly reduced. (iii) Since heating fuel is not required and only a small amount of seawater or heated wastewater can be used, operating costs are also significantly reduced. (iv) Blockage of pipes that was difficult to avoid with conventional equipment;
There is no significant decrease in heat transfer efficiency. (v) Low-temperature water discharged from the intermediate heat medium heat exchanger can be effectively used in necessary fields. Examples 1-2 Using seawater as a heat source, LNG was heated under the conditions shown in Table 1 using the apparatus of the present invention shown in FIG. 1, and the results shown in Table 1 were obtained.
【表】
尚、実施例1と同等のLNG気化及び加熱能力
を有する従来のオープンラツク型式気化器を使用
したところ、海水5.00ton/hを必要とした。[Table] Note that when a conventional open rack type vaporizer having the same LNG vaporization and heating capacity as in Example 1 was used, 5.00 tons/h of seawater was required.
第1図は、本発明装置の一実施態様を示すもの
である。
1…中間熱媒体式間接熱交換器、2…多管式向
流交換器、3…海水又は温排水の供給ライン、4
…多管式向流熱交換器2からの水供給ライン、5
…使用済水の排出ライン、6…LNG供給ライ
ン、7…伝熱管、8…気化した天然ガスの供給ラ
イン、9…気化及び加熱された天然ガスの取出し
ライン。
FIG. 1 shows one embodiment of the device of the present invention. 1...Intermediate heat medium indirect heat exchanger, 2...Multiple tube countercurrent exchanger, 3...Seawater or heated wastewater supply line, 4
...Water supply line from multi-tubular countercurrent heat exchanger 2, 5
...Discharge line for used water, 6. LNG supply line, 7. Heat exchanger tube, 8. Supply line for vaporized natural gas, 9. Takeoff line for vaporized and heated natural gas.
Claims (1)
換器とを備え、海水又は温排水を熱源として液と
して液化天然ガスを気化せしめて使用に適した温
度まで加熱する装置において、 (i) 上方部分1bには液化然ガスと熱交換してこ
れを気化させる中間熱媒体蒸気を収容し、下方
部分1aには液化天然ガスとの熱交換により液
化された中間熱媒体を収容する熱交換器本体;
前記下方部分1aの中間熱媒体と熱交換してこ
れを気化させる為の下記多管式熱交換器2から
の海水又は温排水の供給口1c;前記液化中間
熱媒体との熱交換を終えた水を系外に排出する
排出口1d;液化天然ガスを前記熱交換器本体
の上部分1bに供給する供給口1l;及び気化
された天然ガスを下記多管式熱交管器2に送給
する為の送出口1fを備えた中間熱媒体式間接
熱交換器1、並びに (ii) 前記中間熱媒体式間接熱交換器1から送られ
てくる気化天然ガスの供給口2a;該気化天然
ガスと向流熱交換してこれを使用に適した温度
まで加熱する為の海水又は温排水の供給口2
b;該加熱された気化天然ガスの送出口2c;
及び気化天然ガスの加熱に使用された海水又ま
温排水を前記中間熱媒体式間接熱交換器1本体
の下方部分1aに送る為の送出口2dを備えた
多管式向流熱交換器2 を備えたことを特徴とする液化天然ガスの気化及
び加熱装置。[Claims] 1. Comprising an intermediate heat medium type indirect heat exchanger and a multi-tube type countercurrent heat exchanger, it vaporizes liquefied natural gas as a liquid using seawater or heated wastewater as a heat source to a temperature suitable for use. In the heating device, (i) the upper part 1b houses intermediate heat medium vapor that vaporizes it by exchanging heat with the liquefied natural gas, and the lower part 1a houses the intermediate heat medium vapor that has been liquefied by heat exchange with the liquefied natural gas; a heat exchanger body that accommodates a heat medium;
A supply port 1c for seawater or heated waste water from the multi-tubular heat exchanger 2 described below for exchanging heat with the intermediate heat medium in the lower part 1a and vaporizing it; heat exchange with the liquefied intermediate heat medium has been completed. A discharge port 1d for discharging water out of the system; a supply port 1l for supplying liquefied natural gas to the upper portion 1b of the heat exchanger body; and supplying vaporized natural gas to the multi-tubular heat exchanger 2 described below. (ii) a supply port 2a for the vaporized natural gas sent from the intermediate heat medium indirect heat exchanger 1; Supply port 2 for seawater or heated wastewater to heat it to a temperature suitable for use by countercurrent heat exchange
b; outlet port 2c for the heated vaporized natural gas;
and a multi-tubular countercurrent heat exchanger 2 equipped with an outlet 2d for sending the seawater used for heating vaporized natural gas or heated wastewater to the lower part 1a of the main body of the intermediate heat medium type indirect heat exchanger 1. A liquefied natural gas vaporization and heating device characterized by comprising:
Priority Applications (11)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3640178A JPS54136413A (en) | 1978-03-28 | 1978-03-28 | Liquefied natural gas gasifier |
GB7910278A GB2018967B (en) | 1978-03-28 | 1979-03-23 | Apparatus and process for vaporizing liquefied natural gas |
SE7902725A SE437560B (en) | 1978-03-28 | 1979-03-27 | DEVICE AND PROCEDURE FOR VAPORATION OF CONDENSED NATURAL GAS |
ES478991A ES478991A1 (en) | 1978-03-28 | 1979-03-27 | Apparatus and process for vaporizing liquefied natural gas |
IT05148/79A IT1120651B (en) | 1978-03-28 | 1979-03-27 | APPARATUS AND PROCEDURE FOR THE VAPORIZATION OF LIQUEFIED NATURAL GAS |
BE2/57690A BE875118A (en) | 1978-03-28 | 1979-03-27 | METHOD AND APPARATUS FOR VAPORIZING LIQUEFIED NATURAL GAS |
FR7907632A FR2421334A1 (en) | 1978-03-28 | 1979-03-27 | APPARATUS AND METHOD FOR VAPORIZING LIQUEFIED NATURAL GAS |
NL7902430A NL7902430A (en) | 1978-03-28 | 1979-03-28 | DEVICE AND METHOD FOR VAPORIZING LIQUEFIED NATURAL GAS. |
DE2912321A DE2912321C2 (en) | 1978-03-28 | 1979-03-28 | Device for vaporizing liquefied natural gas |
US06/024,535 US4224802A (en) | 1978-03-28 | 1979-03-28 | Apparatus and process for vaporizing liquefied natural gas |
NL8203601A NL176805C (en) | 1978-03-28 | 1982-09-17 | DEVICE FOR VAPORIZING LIQUEFIED NATURAL GAS. |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP3640178A JPS54136413A (en) | 1978-03-28 | 1978-03-28 | Liquefied natural gas gasifier |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS54136413A JPS54136413A (en) | 1979-10-23 |
JPS6124634B2 true JPS6124634B2 (en) | 1986-06-11 |
Family
ID=12468820
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP3640178A Granted JPS54136413A (en) | 1978-03-28 | 1978-03-28 | Liquefied natural gas gasifier |
Country Status (2)
Country | Link |
---|---|
JP (1) | JPS54136413A (en) |
BE (1) | BE875118A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011080361A (en) * | 2009-10-02 | 2011-04-21 | Mitsubishi Heavy Ind Ltd | Liquefied gas fuel supply system, method for operating the liquefied gas fuel supply system, liquefied gas carrier provided with the liquefied gas fuel supply system, and liquefied gas storage installation provided with the liquefied gas fuel supply system |
JP2017106655A (en) * | 2015-12-08 | 2017-06-15 | 株式会社Ihi | Heat exchanger |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US7293600B2 (en) | 2002-02-27 | 2007-11-13 | Excelerate Energy Limited Parnership | Apparatus for the regasification of LNG onboard a carrier |
ES2333301T3 (en) | 2002-03-29 | 2010-02-19 | Excelerate Energy Limited Partnership | IMPROVED METANERO VESSEL. |
US6598408B1 (en) | 2002-03-29 | 2003-07-29 | El Paso Corporation | Method and apparatus for transporting LNG |
WO2005056377A2 (en) | 2003-08-12 | 2005-06-23 | Excelerate Energy Limited Partnership | Shipboard regasification for lng carriers with alternate propulsion plants |
AU2011255490B2 (en) | 2010-05-20 | 2015-07-23 | Excelerate Energy Limited Partnership | Systems and methods for treatment of LNG cargo tanks |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4917549A (en) * | 1972-06-12 | 1974-02-16 | ||
JPS4921402A (en) * | 1972-06-19 | 1974-02-25 |
-
1978
- 1978-03-28 JP JP3640178A patent/JPS54136413A/en active Granted
-
1979
- 1979-03-27 BE BE2/57690A patent/BE875118A/en not_active IP Right Cessation
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4917549A (en) * | 1972-06-12 | 1974-02-16 | ||
JPS4921402A (en) * | 1972-06-19 | 1974-02-25 |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011080361A (en) * | 2009-10-02 | 2011-04-21 | Mitsubishi Heavy Ind Ltd | Liquefied gas fuel supply system, method for operating the liquefied gas fuel supply system, liquefied gas carrier provided with the liquefied gas fuel supply system, and liquefied gas storage installation provided with the liquefied gas fuel supply system |
JP2017106655A (en) * | 2015-12-08 | 2017-06-15 | 株式会社Ihi | Heat exchanger |
Also Published As
Publication number | Publication date |
---|---|
JPS54136413A (en) | 1979-10-23 |
BE875118A (en) | 1979-07-16 |
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