JP3492388B2 - A relay satellite base for liquefied natural gas shipping - Google Patents

A relay satellite base for liquefied natural gas shipping

Info

Publication number
JP3492388B2
JP3492388B2 JP34365892A JP34365892A JP3492388B2 JP 3492388 B2 JP3492388 B2 JP 3492388B2 JP 34365892 A JP34365892 A JP 34365892A JP 34365892 A JP34365892 A JP 34365892A JP 3492388 B2 JP3492388 B2 JP 3492388B2
Authority
JP
Japan
Prior art keywords
gas
storage tank
tank
line
vaporized
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 - Fee Related
Application number
JP34365892A
Other languages
Japanese (ja)
Other versions
JPH06193797A (en
Inventor
嘉明 宮田
篤 久保田
収 中山
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.)
Tokyo Gas Co Ltd
Original Assignee
Tokyo Gas Co 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 Tokyo Gas Co Ltd filed Critical Tokyo Gas Co Ltd
Priority to JP34365892A priority Critical patent/JP3492388B2/en
Publication of JPH06193797A publication Critical patent/JPH06193797A/en
Application granted granted Critical
Publication of JP3492388B2 publication Critical patent/JP3492388B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/003Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production
    • F25J1/0032Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using the feed stream itself or separated fractions from it, i.e. "internal refrigeration"
    • F25J1/0045Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the kind of cold generation within the liquefaction unit for compensating heat leaks and liquid production using the feed stream itself or separated fractions from it, i.e. "internal refrigeration" by vaporising a liquid return stream
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J1/00Processes or apparatus for liquefying or solidifying gases or gaseous mixtures
    • F25J1/0002Processes or apparatus for liquefying or solidifying gases or gaseous mixtures characterised by the fluid to be liquefied
    • F25J1/0022Hydrocarbons, e.g. natural gas
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2290/00Other details not covered by groups F25J2200/00 - F25J2280/00
    • F25J2290/34Details about subcooling of liquids

Description

【発明の詳細な説明】 【0001】 【産業上の利用分野】本発明は、熱調済液化天然ガスを
タンクローリーを利用して消費側に設けたサテライト基
地まで出荷するための中継用のサテライト基地に関す
る。 【0002】 【従来の技術】工場から消費側へ熱調済の液化天然ガス
(LNG)を輸送する場合には、広範な消費地域に多数
のサテライト基地を建設し、LNG受入基地からこのサ
テライト基地まではタンクローリーを利用してピストン
輸送している。 【0003】 【発明が解決しようとする課題】このため、次のような
問題が生じている。 a.受入基地はLNGタンカーで輸送されて来たものを
直接受け入れるために海岸に建設されており、一方サテ
ライト基地は、消費地に近いところに広範囲に点在して
いる。このため、タンクローリーを用いて熱調済の液化
天然ガスを受入基地からサテライト基地まで輸送するに
は多くの時間とコストがかかる。 b.タンクローリーにより市街地を輸送する場合には、
各種の走行規制があり、この輸送ルートを確保すること
が困難になりつつある。 c.サテライト基地の貯蔵タンク内には熱調済の液化天
然ガスが貯蔵されているが、入熱によりBOGが発生す
ると、所謂煮詰まりにより品質が変化するため、安定し
た品質の液化ガスを出荷するのが難しい。 【0004】本発明の目的は、輸送コストがかからず、
輸送ルート上の問題を一挙に解決する液化天然ガスの出
荷用中継サテライト基地を提案することである。 【0005】 【課題を解決するための手段】本発明の構成は次のとお
りである。 【0006】1.都市ガスの高圧又は中圧幹線に沿って
中継用のサテライト基地を設けたこと、この中継用のサ
テライト基地には、前記幹線から一部取り出した熱調済
気化ガスを再液化するための再液化装置を設けたこと、
この再液化装置により再液化された液化ガスを貯蔵する
ための貯蔵タンクを設けたこと、前記再液化装置で再液
化された液化ガスを前記貯蔵タンク内に導入する導入ラ
インに過冷却器を取り付けたこと、前記過冷却器内に再
液化後の液化ガスの一部をとり込んで気化させ、この気
化潜熱を利用して貯蔵タンク内に入る再液化ガスを冷却
するように構成したこと、前記過冷却器内で気化したガ
スは圧縮機にて昇圧後消費側へ送出するように構成した
こと、前記貯蔵タンクの液中には熱交換器を組み込み、
貯蔵タンク内に貯蔵されている再液化ガスの一部を一旦
タンク外にとり出し、これを前記熱交換器内で気化させ
ることにより、この気化潜熱を利用してタンク内の再液
化ガスを冷却してBOGの発生を抑制するように構成し
たこと、前記貯蔵タンクには、タンクローリーに対する
出荷ラインが設けられていること、を特徴とする液化天
然ガス出荷用サテライト基地。 【0007】 【作用】LNG等の受入基地に隣接して気化設備が建設
されており、都市ガスは、通常この気化設備から幹線を
経由して高圧で送り出され、途中の整圧基地を経由する
間に、中圧、低圧に減圧されて需要家に供給される。本
発明の中継用のサテライト基地は、高圧又は中圧幹線に
沿って建設される。この中継用のサテライト基地におい
ては、幹線から分岐された導入ラインを経由して高圧又
は中圧のガスがとり出され、このとり出されたガスは再
液化装置により再液化されて基地内の貯蔵タンク内に一
旦貯蔵される。消費側へ輸送するためのタンクローリー
は、この貯蔵タンクに取り付けられた出荷ラインより荷
積みを受けて消費側に設けられているサテライト基地ま
で輸送する。再液化した液化天然ガスを貯蔵タンク内に
受け入れる受入ラインに取り付けられている過冷却器
は、再液化ガスの一部がこの過冷却器内で気化されるこ
とにより、この気化潜熱で貯蔵タンク内に送り込まれる
再液化ガスを冷却する。又、貯蔵タンク内にBOGが発
生し、タンク圧力が上昇した場合には、タンク内に組み
込んだ熱交換器内にタンク内の再液化ガスの一部が減圧
後導入され、ここで気化し、この気化潜熱によりタンク
内の再液化ガスを冷却する。この結果、BOGの発生が
抑制されるため、熱量及び品質の安定した液化天然ガス
をローリーに出荷できる。過冷却器及び熱交換器から出
たガスは昇圧器で昇圧後、消費側へ送り出される。 【0008】 【実施例】図1に本発明の中継用のサテライト基地の実
施例を示す。1は幹線より分岐された導入ライン、2は
再液化装置、3は前記再液化装置2から貯蔵タンク4に
至るラインに取り付けられた過冷却器にして、導入ライ
ン1から導入された熱調済の天然ガスは再液化装置2に
おいて再液化されたのち、過冷却器3を経由して貯蔵タ
ンク4内に貯蔵される。5は過冷却器3と貯蔵タンク4
間のラインを分岐して再液化ガスの一部をとり出し、こ
れを過冷却器3内に導く過冷却ラインであって、この過
冷却ライン5からとり出された再液化ガスは、過冷却器
3内で気化することによりその気化潜熱で受け入れ中の
再液化天然ガスを自己冷却する。気化した再液化ガス
は、昇圧器6により昇圧された後、ライン5aから消費
側へ送出される。7は貯蔵タンク4内に組み込まれた熱
交換器にして、貯蔵タンク4内にBOGが発生した場
合、貯蔵タンク4内の再液化ガスの一部を冷却ライン8
を経由してこの熱交換器7内に導入し、ここで気化させ
てこの気化潜熱により貯蔵タンク4内の再液化ガスを冷
却することによりBOGの発生を抑制する機能を有して
いる。9は出荷ラインにして、タンクローリーへの荷積
みは、この出荷ライン9により行われる。 【0009】 【発明の効果】本発明による効果は次のとおりである。 a.幹線に沿って中継用のサテライト基地を建設し、幹
線を経由して送り出された熱調済のガスを再液化して基
地内に低温・低圧で貯蔵し、これをタンクローリーに荷
積みする方式のため、LNG受入基地と中継用のサテラ
イト基地間においてはタンクローリーによるピストン輸
送を行う必要がない。この結果、タンクローリーを用い
て行うための輸送時間及びコストが一切かからない。 b.受入基地と中継用のサテライト基地間をタンクロー
リーでピストン輸送する必要がないので、輸送ルート上
の問題が一挙に解決する。 c.貯蔵タンク内の液化ガスを冷却しながらBOGの発
生を抑制しているため、熱量、品質の安定した液化ガス
をローリーに出荷できる。
Description: BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a relay satellite base for shipping a heat-conditioned liquefied natural gas to a satellite base provided on a consumer side by using a tank lorry. About. 2. Description of the Related Art When transporting heat-conditioned liquefied natural gas (LNG) from a factory to a consumer side, a large number of satellite bases are constructed in a wide area of consumption, and the satellite bases are received from the LNG receiving base. Until then, the piston is transported using a tank lorry. [0003] Therefore, the following problems have arisen. a. Receiving stations are being built on the shore to directly receive what has been transported by LNG tankers, while satellite stations are widely scattered near the consuming area. Therefore, it takes a lot of time and cost to transport the liquefied natural gas that has been thermally adjusted from the receiving terminal to the satellite terminal using the tank lorry. b. When transporting city areas by tank lorry,
There are various driving regulations, and it is becoming difficult to secure this transportation route. c. Thermally adjusted liquefied natural gas is stored in the storage tank at the satellite base, but when BOG is generated due to heat input, the quality changes due to so-called clogging, so it is necessary to ship liquefied gas of stable quality. difficult. An object of the present invention is to reduce the cost of transportation,
The purpose of the present invention is to propose a transit satellite base for liquefied natural gas that solves the problems of transport routes at once. [0005] The constitution of the present invention is as follows. [0006] 1. Provision of a satellite base for relaying along the high or medium pressure trunk line of city gas, and re-liquefaction for re-liquefying the thermally conditioned vaporized gas partially removed from the trunk line at this satellite base for relaying That the device was provided,
A storage tank for storing the liquefied gas reliquefied by the reliquefaction device is provided, and a supercooler is attached to an introduction line for introducing the liquefied gas reliquefied by the reliquefaction device into the storage tank. That a part of the liquefied gas after reliquefaction is taken into the supercooler and vaporized, and the reliquefied gas entering the storage tank is cooled by utilizing the latent heat of vaporization; The gas vaporized in the subcooler is configured to be sent out to the consumption side after the pressure is increased by the compressor, and a heat exchanger is incorporated in the liquid of the storage tank,
A part of the reliquefied gas stored in the storage tank is once taken out of the tank, and is vaporized in the heat exchanger, thereby utilizing the latent heat of vaporization to cool the reliquefied gas in the tank. Wherein the storage tank is provided with a shipping line for a tank lorry, wherein the storage tank is provided with a shipping line for a tank lorry. [0007] A vaporizing facility is constructed adjacent to a receiving base for LNG or the like, and city gas is normally sent from this vaporizing facility at a high pressure via a main line, and passes through a pressure regulating base on the way. In the meantime, the pressure is reduced to a medium pressure and a low pressure and supplied to customers. The relay satellite base of the present invention is constructed along a high-voltage or medium-voltage main line. At this relay satellite base, high-pressure or medium-pressure gas is extracted via an introduction line branched from the main line, and the extracted gas is re-liquefied by a re-liquefaction device and stored in the base. Once stored in the tank. The tank lorry for transportation to the consumer side receives cargo from a shipping line attached to the storage tank and transports the cargo to a satellite base provided on the consumer side. The supercooler attached to the receiving line that receives the reliquefied liquefied natural gas into the storage tank is partially cooled by the subcooler, which is vaporized in the supercooler. Cools the reliquefied gas sent to the tank. Also, when BOG is generated in the storage tank and the tank pressure increases, a part of the reliquefied gas in the tank is introduced into the heat exchanger incorporated in the tank after depressurization, where it is vaporized. The reliquefied gas in the tank is cooled by the latent heat of vaporization. As a result, generation of BOG is suppressed, so that liquefied natural gas with stable calorific value and quality can be shipped to lorries. The gas discharged from the subcooler and the heat exchanger is boosted by the booster and sent to the consumer side. FIG. 1 shows an embodiment of a relay satellite base according to the present invention. 1 is an introduction line branched from the main line, 2 is a reliquefaction device, and 3 is a supercooler attached to a line from the reliquefaction device 2 to the storage tank 4, and is heat-conditioned introduced from the introduction line 1. Is re-liquefied in the re-liquefaction unit 2 and stored in the storage tank 4 via the supercooler 3. 5 is a subcooler 3 and a storage tank 4
Is a subcooling line that branches out a part of the line to take out a part of the reliquefied gas and guides it into the subcooler 3. The reliquefied gas taken out from the subcooling line 5 is subcooled. By vaporizing in the vessel 3, the re-liquefied natural gas being received is self-cooled by the latent heat of vaporization. The vaporized reliquefied gas is boosted by the booster 6 and then sent out from the line 5a to the consuming side. Reference numeral 7 denotes a heat exchanger incorporated in the storage tank 4, and when BOG is generated in the storage tank 4, a part of the reliquefied gas in the storage tank 4 is cooled by a cooling line 8.
And has a function of suppressing the generation of BOG by being vaporized here and cooling the reliquefied gas in the storage tank 4 by the latent heat of vaporization. Reference numeral 9 denotes a shipping line, and loading on the tank lorry is performed by the shipping line 9. The effects of the present invention are as follows. a. A satellite base for relaying is constructed along the main line, and the heat-conditioned gas sent out via the main line is reliquefied, stored at low temperature and low pressure in the base, and loaded into a tank lorry. Therefore, there is no need to transport the piston by tank lorry between the LNG receiving terminal and the relay satellite terminal. As a result, there is no need for any transportation time and cost for carrying out using a tank truck. b. Since there is no need to use a tank lorry to transport pistons between the receiving terminal and the relay satellite terminal, problems on the transportation route can be solved at once. c. Since the generation of BOG is suppressed while cooling the liquefied gas in the storage tank, the liquefied gas with stable calorie and quality can be shipped to the lorry.

【図面の簡単な説明】 【図1】本発明に係る液化ガスの出荷方法及び液化ガス
出荷基地の説明図。 【符号の説明】 1 幹線からの導入ライン 2 再液化装置 3 過冷却器 4 貯蔵タンク 5 過冷却ライン 6 昇圧機 7 熱交換器 8 冷却ライン 9 出荷ライン
BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is an explanatory view of a liquefied gas shipping method and a liquefied gas shipping base according to the present invention. [Description of Signs] 1 Introductory line from main line 2 Reliquefaction device 3 Subcooler 4 Storage tank 5 Supercool line 6 Booster 7 Heat exchanger 8 Cooling line 9 Shipping line

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平3−236589(JP,A) 特開 昭63−199998(JP,A) 特開 昭56−143899(JP,A) 特公 昭46−15781(JP,B1) (58)調査した分野(Int.Cl.7,DB名) F17C 1/00 - 13/12 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-3-236589 (JP, A) JP-A-63-199998 (JP, A) JP-A-56-143899 (JP, A) 15781 (JP, B1) (58) Fields investigated (Int. Cl. 7 , DB name) F17C 1/00-13/12

Claims (1)

(57)【特許請求の範囲】 【請求項1】 都市ガスの高圧又は中圧幹線に沿って中
継用のサテライト基地を設けたこと、この中継用のサテ
ライト基地には、前記幹線から一部取り出した熱調済気
化ガスを再液化するための再液化装置を設けたこと、こ
の再液化装置により再液化された液化ガスを貯蔵するた
めの貯蔵タンクを設けたこと、前記再液化装置で再液化
された液化ガスを前記貯蔵タンク内に導入する導入ライ
ンに過冷却器を取り付けたこと、前記過冷却器内に再液
化後の液化ガスの一部をとり込んで気化させ、この気化
潜熱を利用して貯蔵タンク内に入る再液化ガスを冷却す
るように構成したこと、前記過冷却器内で気化したガス
は圧縮機にて昇圧後消費側へ送出するように構成したこ
と、前記貯蔵タンクの液中には熱交換器を組み込み、貯
蔵タンク内に貯蔵されている再液化ガスの一部を一旦タ
ンク外にとり出し、これを前記熱交換器内で気化させる
ことにより、この気化潜熱を利用してタンク内の再液化
ガスを冷却してBOGの発生を抑制するように構成した
こと、前記貯蔵タンクには、タンクローリーに対する出
荷ラインが設けられていること、を特徴とする液化天然
ガス出荷用中継サテライト基地。
(57) [Claims 1] A relay satellite base is provided along a high- or medium-pressure main line of city gas, and the relay satellite base is partially taken out from the main line. A re-liquefaction device for re-liquefying the heat-conditioned vaporized gas, a storage tank for storing a liquefied gas re-liquefied by the re-liquefaction device, and a re-liquefaction by the re-liquefaction device. A supercooler is attached to an introduction line for introducing the liquefied gas into the storage tank, and a part of the liquefied gas after reliquefaction is taken into the supercooler and vaporized, and the latent heat of vaporization is used. And that the re-liquefied gas that enters the storage tank is configured to be cooled, the gas that has been vaporized in the supercooler is configured to be sent out to the consumer side after being pressurized by the compressor, A heat exchanger is incorporated in the liquid A part of the reliquefied gas stored in the storage tank is once taken out of the tank, and is vaporized in the heat exchanger, thereby utilizing the latent heat of vaporization to cool the reliquefied gas in the tank. Wherein the storage tank is provided with a shipping line for a tank lorry, wherein the storage tank is provided with a shipping line for a tank lorry.
JP34365892A 1992-12-24 1992-12-24 A relay satellite base for liquefied natural gas shipping Expired - Fee Related JP3492388B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP34365892A JP3492388B2 (en) 1992-12-24 1992-12-24 A relay satellite base for liquefied natural gas shipping

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP34365892A JP3492388B2 (en) 1992-12-24 1992-12-24 A relay satellite base for liquefied natural gas shipping

Publications (2)

Publication Number Publication Date
JPH06193797A JPH06193797A (en) 1994-07-15
JP3492388B2 true JP3492388B2 (en) 2004-02-03

Family

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Family Applications (1)

Application Number Title Priority Date Filing Date
JP34365892A Expired - Fee Related JP3492388B2 (en) 1992-12-24 1992-12-24 A relay satellite base for liquefied natural gas shipping

Country Status (1)

Country Link
JP (1) JP3492388B2 (en)

Families Citing this family (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5644920A (en) * 1995-09-25 1997-07-08 Rockwell International Corporation Liquid propellant densification
JP7091041B2 (en) * 2017-09-11 2022-06-27 株式会社Ihiプラント Plant control device and plant control method

Also Published As

Publication number Publication date
JPH06193797A (en) 1994-07-15

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