JPS6065997A - Device for reliquefying liquefied gas - Google Patents
Device for reliquefying liquefied gasInfo
- Publication number
- JPS6065997A JPS6065997A JP58173221A JP17322183A JPS6065997A JP S6065997 A JPS6065997 A JP S6065997A JP 58173221 A JP58173221 A JP 58173221A JP 17322183 A JP17322183 A JP 17322183A JP S6065997 A JPS6065997 A JP S6065997A
- Authority
- JP
- Japan
- Prior art keywords
- gas
- liquefied gas
- reliquefying
- absorbing
- liquefied
- 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
Links
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J1/00—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
- F25J1/0002—Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
- F25J1/0022—Hydrocarbons, e.g. natural gas
- F25J1/0025—Boil-off gases "BOG" from storages
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2205/00—Processes or apparatus using other separation and/or other processing means
- F25J2205/60—Processes or apparatus using other separation and/or other processing means using adsorption on solid adsorbents, e.g. by temperature-swing adsorption [TSA] at the hot or cold end
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2220/00—Processes or apparatus involving steps for the removal of impurities
- F25J2220/60—Separating impurities from natural gas, e.g. mercury, cyclic hydrocarbons
- F25J2220/62—Separating low boiling components, e.g. He, H2, N2, Air
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
- F25J2270/00—Refrigeration techniques used
- F25J2270/90—External refrigeration, e.g. conventional closed-loop mechanical refrigeration unit using Freon or NH3, unspecified external refrigeration
Abstract
Description
【発明の詳細な説明】
本発明は、液化ガスの再液化装置に関し、特に、液化ガ
ス貯蔵容器の昇圧防止を図った液化ガスの再液化装置に
関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a liquefied gas reliquefaction device, and more particularly to a liquefied gas reliquefaction device that prevents pressure increase in a liquefied gas storage container.
第1図は、従来の液化ガス再液化装置の1例としての、
LNG再液化装置の概念図である。FIG. 1 shows an example of a conventional liquefied gas reliquefaction device.
It is a conceptual diagram of an LNG reliquefaction device.
LNGの地上基地又はI、N()タンカー等において、
LMG 2は断熱容器1に貯留されているが、外部入熱
により一部が蒸発(気化)シ、ガス空間7の圧力が上昇
する。この昇圧を一定限度内におさえるために気化ガス
を管路3により容器1の外にとり出し、加温器9で加温
した後、圧縮機又はファン4で充分な循環圧力まで昇圧
したあと、再液化機5により再液化し、管路6によって
容器1に戻している。At LNG ground bases or I, N () tankers, etc.
Although the LMG 2 is stored in the heat insulating container 1, a portion of the LMG 2 evaporates (vaporizes) due to external heat input, and the pressure in the gas space 7 increases. In order to suppress this pressure increase within a certain limit, the vaporized gas is taken out of the container 1 through a pipe 3, heated with a heater 9, and then raised to sufficient circulation pressure with a compressor or fan 4, and then re-circulated. It is re-liquefied by a liquefier 5 and returned to the container 1 through a pipe line 6.
しかし、現実的な問題としてLNGには主として窒素ガ
ス(GNs)が不純成分として含まれており、この窒素
ガスは沸点がLNGよりも低いためにLNGよりも相対
的に早く気化し、再液化のときもLNGが液化する温度
では液化しない。このため、第1図の如き従来の装置で
は再液化循環系3〜6及びガス空間7には窒素ガス成分
が次第に多くなシ、このままでは内圧の上昇を防止でき
なくなる。従って、逃し弁8により適宜気化ガスを系外
に投棄せざるを得ない。However, as a practical problem, LNG mainly contains nitrogen gas (GNs) as an impurity component, and because this nitrogen gas has a lower boiling point than LNG, it vaporizes relatively faster than LNG, making it difficult to reliquefy. LNG does not liquefy at the same temperature as when it liquefies. Therefore, in the conventional apparatus as shown in FIG. 1, nitrogen gas components gradually increase in the reliquefaction circulation systems 3 to 6 and the gas space 7, and if this continues, it becomes impossible to prevent the internal pressure from increasing. Therefore, the vaporized gas has to be appropriately dumped out of the system using the relief valve 8.
本発明は、上記の欠点を解消するためになされたもので
、液化ガス貯蔵容器の昇圧防止を目的とするものである
。The present invention was made in order to eliminate the above-mentioned drawbacks, and its purpose is to prevent pressure increase in a liquefied gas storage container.
上記目的は、液化ガス貯蔵容器から導出された気化ガス
を、昇圧装置、再液化装置を経由させ昇圧、再液化して
前記液化ガス貯蔵容器へ戻す配管系において、前記再液
化装置の上流に、前記液化ガス中の前記昇圧装置、再液
化装置で再液化しない不純成分ガスを選択的に吸着する
吸着装置を挿設したことを特徴とする液化ガスの再液化
装置によって達成することができる。The above object is to provide a piping system in which vaporized gas led out from a liquefied gas storage container passes through a pressure booster and a reliquefaction device to increase the pressure, reliquefy it, and return it to the liquefied gas storage container, upstream of the reliquefaction device. This can be achieved by a liquefied gas reliquefaction device characterized in that an adsorption device for selectively adsorbing impurity component gases that are not reliquefied by the pressure booster and reliquefaction device in the liquefied gas is inserted.
上記した本発明装置は、貯蔵液化ガスの気化ガスと、そ
の中に混入した不純成分の気化ガスとを混合物として放
出することを避けて、不純成分の気化ガスだけを選択的
に系外に放出できるように、不純成分の気化ガスを選択
的に吸着する吸着剤を充填した吸着装置を、再液化系に
追設した点に特徴を有する本のである。The device of the present invention described above avoids releasing the vaporized gas of the stored liquefied gas and the vaporized gas of the impure components mixed therein as a mixture, and selectively releases only the vaporized gas of the impure components to the outside of the system. This book is unique in that an adsorption device filled with an adsorbent that selectively adsorbs vaporized gases of impurity components is added to the reliquefaction system to make it possible.
第2図は、本発明装置の一実施態様例の概念図である。FIG. 2 is a conceptual diagram of an embodiment of the apparatus of the present invention.
第2図中、第1図と同一符号は第1図と同一部品を示す
。In FIG. 2, the same reference numerals as in FIG. 1 indicate the same parts as in FIG.
LNGの気化ガスは低温のまま吸着装置10に導入され
る。吸着装置10には窒素ガスを選択的に吸着する吸着
剤〔例えばモレキュラーシープス(商品名)〕が充填さ
れているので、気化ガスの内窒素ガスだけが吸着されて
吸着装置10を出ることになる。The vaporized LNG gas is introduced into the adsorption device 10 at a low temperature. Since the adsorption device 10 is filled with an adsorbent (for example, Molecular Sheeps (trade name)) that selectively adsorbs nitrogen gas, only the nitrogen gas in the vaporized gas is adsorbed and leaves the adsorption device 10. Become.
吸着装置10を出た気化ガスは熱交換器11で戻多ガス
を冷却した(即ち戻りガスで加温された)後、圧縮機4
に入って循環に必要力圧力に昇圧され、熱交換器11で
冷却され、さらに再液化機5で液化される。このとき、
気化ガス中には窒素成分は非常に少くなっているので、
大部分が再液化する。再液化したガス及び残余のガスは
管路6で容器1に戻される。The vaporized gas leaving the adsorption device 10 cools the return gas in the heat exchanger 11 (that is, is heated by the return gas), and then passes through the compressor 4.
The water enters the system, is pressurized to the pressure required for circulation, is cooled in the heat exchanger 11, and is further liquefied in the reliquefaction machine 5. At this time,
Since the nitrogen component in the vaporized gas is very low,
Most of it is reliquefied. The reliquefied gas and the remaining gas are returned to the container 1 via line 6.
このように系内の窒素ガスが吸着装置10で除去される
ので、ガス空間7の圧力上昇の原因となる窒素ガス成分
の増大がなくなり、第1図の場合のように容器1の窒素
ガスによる昇圧現象を防止できる。Since the nitrogen gas in the system is removed by the adsorption device 10 in this way, the increase in the nitrogen gas component that causes the pressure increase in the gas space 7 is eliminated, and as in the case of FIG. Pressure increase phenomenon can be prevented.
なお、吸着装置10内の吸着剤が飽和状態になったとき
は、弁12を閉じた後、図示しない手段によって吸着剤
を加熱又は減圧して再生する。乙のとき放出された窒素
ガスは弁13を開いて系外へ排出する。或は吸着装置1
0を2個以上並列に設け、使用、再生を切換えつつ連続
運転することもできる。Note that when the adsorbent in the adsorption device 10 becomes saturated, after closing the valve 12, the adsorbent is regenerated by heating or reducing the pressure by means not shown. The nitrogen gas released in step (B) is discharged out of the system by opening the valve 13. Or adsorption device 1
It is also possible to provide two or more zeros in parallel and operate continuously while switching between use and regeneration.
第1図は従来の液化ガス再液化装置を示す図、第2回は
本発明装置の一実施態様例を示す図である。
復代理人 内 1) 明
復代理人 萩 原 亮 −FIG. 1 is a diagram showing a conventional liquefied gas reliquefaction device, and FIG. 2 is a diagram showing an embodiment of the device of the present invention. Sub-agents 1) Meifuku agent Ryo Hagiwara -
Claims (1)
、再液化装置を経由させ昇圧、再液化して前記液化ガス
貯蔵容器へ戻す配管系において、前記再液化装置の上流
に、前記液化ガス中の前記昇圧装置、再液化装置で再液
化しない不純成分ガスを選択的に吸着する吸着装置を挿
設したととを特徴とする液化ガスの再液化装置。In a piping system in which the vaporized gas led out from the liquefied gas storage container passes through a pressure booster and a reliquefaction device to increase the pressure, reliquefy it, and return it to the liquefied gas storage container, upstream of the reliquefaction device, there is a pipe in the liquefied gas. A reliquefaction device for liquefied gas, characterized in that an adsorption device for selectively adsorbing impurity gases that are not reliquefied in the pressure booster and the reliquefaction device is inserted.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58173221A JPS6065997A (en) | 1983-09-21 | 1983-09-21 | Device for reliquefying liquefied gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58173221A JPS6065997A (en) | 1983-09-21 | 1983-09-21 | Device for reliquefying liquefied gas |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6065997A true JPS6065997A (en) | 1985-04-15 |
JPH0444159B2 JPH0444159B2 (en) | 1992-07-20 |
Family
ID=15956374
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58173221A Granted JPS6065997A (en) | 1983-09-21 | 1983-09-21 | Device for reliquefying liquefied gas |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6065997A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0723144A2 (en) * | 1995-01-20 | 1996-07-24 | Technischer Überwachungs-Verein Österreich | Method for testing the pressure of a liquid gas container used for storing a liquid gas |
KR100681557B1 (en) | 2005-12-01 | 2007-02-09 | 대우조선해양 주식회사 | Boil off gas reliquefaction treatment system of liquefied natural gas carrier |
KR100747232B1 (en) | 2006-10-04 | 2007-08-07 | 대우조선해양 주식회사 | Apparatus and method for reliquefying boil-off gas, and lng carrier with the apparatus |
KR100747231B1 (en) | 2006-10-04 | 2007-08-07 | 대우조선해양 주식회사 | Apparatus and method for reliquefying boil-off gas |
KR100761975B1 (en) | 2006-10-04 | 2007-10-04 | 신영중공업주식회사 | Lng bog reliquefaction apparatus and lng bog reliquefaction method |
WO2014203530A1 (en) * | 2013-06-21 | 2014-12-24 | 川崎重工業株式会社 | Liquefied gas-storing tank and liquefied gas transport vessel |
JP2019056381A (en) * | 2017-09-19 | 2019-04-11 | 三井E&S造船株式会社 | Boil-off gas treatment system |
Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS586116A (en) * | 1981-07-03 | 1983-01-13 | Toshiba Corp | Vapor phase drying for contents of stationary induction electric apparatus |
-
1983
- 1983-09-21 JP JP58173221A patent/JPS6065997A/en active Granted
Patent Citations (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS586116A (en) * | 1981-07-03 | 1983-01-13 | Toshiba Corp | Vapor phase drying for contents of stationary induction electric apparatus |
Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0723144A2 (en) * | 1995-01-20 | 1996-07-24 | Technischer Überwachungs-Verein Österreich | Method for testing the pressure of a liquid gas container used for storing a liquid gas |
EP0723144A3 (en) * | 1995-01-20 | 1997-01-02 | Tech Ueberwachungs Verein Oest | Method for testing the pressure of a liquid gas container used for storing a liquid gas |
KR100681557B1 (en) | 2005-12-01 | 2007-02-09 | 대우조선해양 주식회사 | Boil off gas reliquefaction treatment system of liquefied natural gas carrier |
KR100747232B1 (en) | 2006-10-04 | 2007-08-07 | 대우조선해양 주식회사 | Apparatus and method for reliquefying boil-off gas, and lng carrier with the apparatus |
KR100747231B1 (en) | 2006-10-04 | 2007-08-07 | 대우조선해양 주식회사 | Apparatus and method for reliquefying boil-off gas |
KR100761975B1 (en) | 2006-10-04 | 2007-10-04 | 신영중공업주식회사 | Lng bog reliquefaction apparatus and lng bog reliquefaction method |
WO2014203530A1 (en) * | 2013-06-21 | 2014-12-24 | 川崎重工業株式会社 | Liquefied gas-storing tank and liquefied gas transport vessel |
KR20160009680A (en) * | 2013-06-21 | 2016-01-26 | 카와사키 주코교 카부시키 카이샤 | Liquefied gas-storing tank and liquefied gas transport vessel |
JPWO2014203530A1 (en) * | 2013-06-21 | 2017-02-23 | 川崎重工業株式会社 | Liquefied gas holding tank and liquefied gas carrier |
JP2017194166A (en) * | 2013-06-21 | 2017-10-26 | 川崎重工業株式会社 | Liquefied gas retention tank and liquefied gas carrying vessel |
US10317010B2 (en) | 2013-06-21 | 2019-06-11 | Kawasaki Jukogyo Kabushiki Kaisha | Liquefied gas storage tank and liquefied gas carrier ship |
JP2019056381A (en) * | 2017-09-19 | 2019-04-11 | 三井E&S造船株式会社 | Boil-off gas treatment system |
Also Published As
Publication number | Publication date |
---|---|
JPH0444159B2 (en) | 1992-07-20 |
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