JPS6057097A - Method to obtain gas with different component in cold liquefied gas storage tank - Google Patents

Method to obtain gas with different component in cold liquefied gas storage tank

Info

Publication number
JPS6057097A
JPS6057097A JP58165771A JP16577183A JPS6057097A JP S6057097 A JPS6057097 A JP S6057097A JP 58165771 A JP58165771 A JP 58165771A JP 16577183 A JP16577183 A JP 16577183A JP S6057097 A JPS6057097 A JP S6057097A
Authority
JP
Japan
Prior art keywords
tank
heat
gas
liquefied gas
storage tank
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.)
Pending
Application number
JP58165771A
Other languages
Japanese (ja)
Inventor
Masaaki Kuroki
黒木 正章
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 JP58165771A priority Critical patent/JPS6057097A/en
Publication of JPS6057097A publication Critical patent/JPS6057097A/en
Pending 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
    • 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

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

PURPOSE:To obtain gas with different component in a liquefied gas storage tank by applying heat to gas from outside by incorporating a heat exchanger in a cold liquefied gas storage tank, evaporating only the component of high specific volatility, and introducing it outside the tank. CONSTITUTION:Heat medium which is heated in an outer heat exchanger 7 proceeds to a heat-exchanger 5 in a tank 1 through a circulating line 6, and here it applies heat to LNG in the tank and only the high volatility component in the LNG is evaporated in the upper space in the tank. The evaporated gas is introduced outside the tank through an evaporating gas line 9, and it is boosted by a compressor 10 and sent to the destination. The outer beat exchanger 7 performs supplying of heat toward a heat medium of the circulating line 6 by a heat supplying medium circulating line 8.

Description

【発明の詳細な説明】 という)中から成分の異なるガスを得る方法に関するも
のである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for obtaining gases having different components from a gaseous mixture.

LNGの成分は表1に示すように、各種の成分から成っ
ており、通常LNGが燃ネ′1として使用される場合に
は、各成分は混在のまま気化して消費されている。一方
、LNGを燃料として使用している各種の反応炉或いは
化学原料メーカー等においては表1に示した各成分のう
ち、例えばメタン成分のみを使用したい希望を持ってい
る例もめ従来においては、LNGについて異なる成分の
みを気化して消費するという方法を採っていないため、
特に都市ガスの需要家からはある成分のみのカスを供給
して欲しいという要望がある。
As shown in Table 1, LNG consists of various components, and when LNG is normally used as fuel fuel '1, each component is vaporized and consumed as a mixture. On the other hand, various reactors or chemical raw material manufacturers that use LNG as fuel have a desire to use, for example, only the methane component among the components shown in Table 1. Because we do not use a method of vaporizing and consuming only the different ingredients,
In particular, there are requests from city gas consumers to supply waste containing only certain components.

本発明は以上の如き要望に応えるために提案されるもの
で、極めて簡単な方法により成分の異なるガスを得る方
法を提案するのが目的である。
The present invention has been proposed in response to the above-mentioned needs, and an object of the present invention is to propose a method of obtaining gases having different components using an extremely simple method.

本発明は上記目的を達成する手段として、先ず低温液化
天然ガス貯蔵タンク(以下「タンク」という)を利用す
ることにした。又、LNGの各成分はそれぞれその比揮
発度が異なるので、前記タンク内において夫々の成分に
合った揮発熱をLNGに与え、該タンク内上部空間に揮
発ガスを貯え、これをタンク外に導き出して消費する方
法を採用した。
As a means to achieve the above object, the present invention first utilizes a low temperature liquefied natural gas storage tank (hereinafter referred to as "tank"). Furthermore, since each component of LNG has a different specific volatility, heat of vaporization suitable for each component is given to the LNG in the tank, volatile gas is stored in the upper space of the tank, and this is led out of the tank. The method of consumption was adopted.

次に、タンク内のLNGに対して熱を与える方法として
、タンク内に熱交換器を装入し、タンク外からこの熱交
換器に対して熱媒を循環させる方法を採用した。
Next, as a method of applying heat to the LNG inside the tank, a method was adopted in which a heat exchanger was inserted into the tank and a heat medium was circulated to the heat exchanger from outside the tank.

添付図面は上記構成から成る本発明の一実施例を示すも
ので、1はタンク、2は受入ライン、3は液移送ライン
、4は液移送ポンプ、5はタンク1内のLNG中に浸漬
せしめて設置した熱交換器、6は前記熱交換器5内に熱
媒を循環させるための熱媒循環ライン、7は外部熱交換
器にして、前記熱媒循環ライン6内の熱媒に対して熱補
給を行なうtのである。、8は熱補給媒体循環ラインを
示す。なお、熱補給媒体循環ライン8内に通す媒体とし
て、例えばペーパーライザーにて気化された天然ガスを
用いるようにしてもよい。
The attached drawing shows an embodiment of the present invention having the above-mentioned configuration, in which 1 is a tank, 2 is a receiving line, 3 is a liquid transfer line, 4 is a liquid transfer pump, and 5 is immersed in LNG in the tank 1. 6 is a heat medium circulation line for circulating the heat medium in the heat exchanger 5; 7 is an external heat exchanger, and 6 is a heat medium circulation line for circulating the heat medium in the heat medium circulation line 6; It is for heat replenishment. , 8 indicates a heat replenishment medium circulation line. Note that as the medium passed through the heat supply medium circulation line 8, for example, natural gas vaporized in a paper riser may be used.

9はタンクl向上部空間に貯えられた揮発度の高いガス
をタンク1外に導き出すための揮発ガスライン、10は
コンプレッサーである。
9 is a volatile gas line for leading the highly volatile gas stored in the upper space of the tank 1 to the outside of the tank 1, and 10 is a compressor.

」1記実施例においては外部熱交換器7にて温められた
熱媒が循環ライン6を介してタンク1内の熱交換器5に
至り、ここでタンク1内のLNGに熱を与え、LNGの
うち揮発度の高い成分のみをタンク1内上部空間に揮発
させる。そして、揮発ガスは揮発ガスライン9を介して
タンク1外に導き出し、コンプレッサー10により昇圧
して目的の消費基地に送る。
In the first embodiment, the heat medium heated in the external heat exchanger 7 reaches the heat exchanger 5 in the tank 1 via the circulation line 6, where it gives heat to the LNG in the tank 1, and the LNG Among them, only the highly volatile components are volatilized into the upper space inside the tank 1. Then, the volatile gas is led out of the tank 1 via the volatile gas line 9, pressurized by the compressor 10, and sent to the target consumption base.

本発明は以上のように、タンク内に熱交換器を装入し、
この熱交換器に熱媒を循環させることでタンク内のLN
Gに熱を与え5強制的にタンク内において揮発度の高い
ガスのみを分離してタンク外に導き出し、これを消費す
ることができるようにしたので、特定成分のガスの使用
を希望する需要家に対し、筒中な設備のみで応えること
力くできる効果がある。
As described above, the present invention includes a heat exchanger installed in a tank,
By circulating the heat medium through this heat exchanger, the LN in the tank is
By applying heat to G and forcibly separating only the highly volatile gas in the tank and leading it out of the tank, this can be consumed, making it possible for consumers who wish to use gas with specific components. In contrast, it has the effect of being able to respond simply with the necessary equipment.

又、本発明はタンク内の熱交換器で冷却された熱媒は熱
媒ラインを介してタンク外に循環するので、この熱媒が
回収した冷熱をタンフタ目こおし\て利用することがで
きる。
Furthermore, in the present invention, the heat medium cooled by the heat exchanger inside the tank is circulated outside the tank via the heat medium line, so the cold heat recovered by this heat medium can be used by passing through the tank lid. can.

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

図は本発明の一実施例を示す系統図である。 1・・・・・・タンク、?・・・・・・受入ライン、3
・・・・・・液移送ライン、4・・・・・・液移送ポン
プ、5・・・・・・熱交換器、6・・・・・・熱媒循環
ライン、7・・・・・・外部熱交換器、8−・−熱補給
媒体循環ライン、9・・・・・・揮発ガスライン、10
・・・・・・コンプレッサー。
The figure is a system diagram showing one embodiment of the present invention. 1...tank?・・・・・・Acceptance line, 3
...Liquid transfer line, 4...Liquid transfer pump, 5...Heat exchanger, 6...Heat medium circulation line, 7...・External heat exchanger, 8--Heat replenishment medium circulation line, 9... Volatile gas line, 10
······compressor.

Claims (1)

【特許請求の範囲】[Claims] 低温液化ガス貯蔵タンク内に熱交換器を装入し、外部か
らこの熱交換器内に熱媒を循環させることによりタンク
内の低温液化ガスに熱を与え、比揮発度の高い低温液化
ガス成分のみを揮発させてタンク外に導き出すことによ
り低温液化ガス貯蔵タンク内において成分の異なるガス
を得る方法。
A heat exchanger is installed in the low-temperature liquefied gas storage tank, and a heat medium is circulated through the heat exchanger from the outside to provide heat to the low-temperature liquefied gas in the tank, and the low-temperature liquefied gas components with high relative volatility are A method of obtaining gases with different components in a low-temperature liquefied gas storage tank by volatilizing only the liquefied gas and leading it out of the tank.
JP58165771A 1983-09-08 1983-09-08 Method to obtain gas with different component in cold liquefied gas storage tank Pending JPS6057097A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP58165771A JPS6057097A (en) 1983-09-08 1983-09-08 Method to obtain gas with different component in cold liquefied gas storage tank

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP58165771A JPS6057097A (en) 1983-09-08 1983-09-08 Method to obtain gas with different component in cold liquefied gas storage tank

Publications (1)

Publication Number Publication Date
JPS6057097A true JPS6057097A (en) 1985-04-02

Family

ID=15818721

Family Applications (1)

Application Number Title Priority Date Filing Date
JP58165771A Pending JPS6057097A (en) 1983-09-08 1983-09-08 Method to obtain gas with different component in cold liquefied gas storage tank

Country Status (1)

Country Link
JP (1) JPS6057097A (en)

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