JPS6098299A - High pressure gas feeding method - Google Patents

High pressure gas feeding method

Info

Publication number
JPS6098299A
JPS6098299A JP20444983A JP20444983A JPS6098299A JP S6098299 A JPS6098299 A JP S6098299A JP 20444983 A JP20444983 A JP 20444983A JP 20444983 A JP20444983 A JP 20444983A JP S6098299 A JPS6098299 A JP S6098299A
Authority
JP
Japan
Prior art keywords
gas
pressure
storage tank
liquefied gas
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
Application number
JP20444983A
Other languages
Japanese (ja)
Other versions
JPH0548399B2 (en
Inventor
Kazuo Seki
関　和夫
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.)
Japan Oxygen Co Ltd
Nippon Sanso Corp
Original Assignee
Japan Oxygen Co Ltd
Nippon Sanso Corp
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 Japan Oxygen Co Ltd, Nippon Sanso Corp filed Critical Japan Oxygen Co Ltd
Priority to JP20444983A priority Critical patent/JPS6098299A/en
Publication of JPS6098299A publication Critical patent/JPS6098299A/en
Publication of JPH0548399B2 publication Critical patent/JPH0548399B2/ja
Granted legal-status Critical Current

Links

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
    • F17C2201/00—Vessel construction, in particular geometry, arrangement or size
    • F17C2201/01—Shape
    • F17C2201/0104—Shape cylindrical
    • F17C2201/0119—Shape cylindrical with flat 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
    • 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
    • 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
    • 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
    • F17C2227/0318—Water heating using seawater

Landscapes

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

Abstract

PURPOSE:To totally eliminate the need for using energy for pressurizing by alternately receiving a liquefied gas in more than one small-capacity high pressure resistant storage tank, introducing a part of this liquefied gas out and gasifying it utilizing air, hot drain etc., and pressurizing the inside of a storage tank by means of this gasified gas. CONSTITUTION:After a prescribed pressure is reached in a storage tank 100, a liquefied-gas delivery valve 104 is opened, to start the delivery of the liquid. The liquefied gas, which passed through the liquefied-gas delivery valve 104, passes through a pipe 116 and enters a delivered gas evaporater 3, exchanges heat with air, hot drain, sea water, etc. to be gasified, and is sent out to a requiring part as a high pressure gas. During this time, the liquefied gas delivery valves 204, 304 for storage tanks 200 and 300 are left closed. Thus, with at least three high pressure storage tanks 100, 200, 300 being provided, and by carrying out each process of receiving liquid, prepressurization, pressurization, sending with pressure, and discharging remaining gas, repeatedly with the period for each storage tank being shifted, the pressurization and sending with pressure, of a liquefied gas can be carried out.

Description

【発明の詳細な説明】 本発明は液化ガスが気化する際の体積膨張による圧力上
昇を利用し高圧貯槽内圧を高圧に昇圧し、この圧力によ
って貯槽内より液化ガスを送出後見化することにより高
圧のガスを供給づる方法に関し、訂しくは上記高圧貯槽
を少くとも３基用い上記等の工程を交互に行うことによ
り連続的に高圧ガスを供給する方法に関する。Detailed Description of the Invention The present invention utilizes the pressure increase due to volume expansion when liquefied gas vaporizes to increase the internal pressure of the high-pressure storage tank to a high pressure, and uses this pressure to send out the liquefied gas from inside the storage tank. The present invention relates to a method of supplying gas, and more particularly, to a method of continuously supplying high-pressure gas by using at least three of the above-mentioned high-pressure storage tanks and performing the above steps alternately.

一般に貯槽内の液化ガスを連続的に気化圧送づる方法と
しては液化ガス貯槽と液ポンプの組合わせによる方法が
行なわれているが、所定の圧ツノ迄昇圧するための液ポ
ンプ駆動用エネルギーは思ガスが高圧、連続且つ大量の
場合は相当量に達する。Generally, the method of continuously vaporizing and pumping liquefied gas in a storage tank is to use a combination of a liquefied gas storage tank and a liquid pump, but the energy required to drive the liquid pump to raise the pressure to a predetermined pressure point is estimated. If the gas is at high pressure, continuous, and in large quantities, it will reach a considerable amount.

本発明は上記に鑑みなされたもので、大容量のほぼ常圧
の貯槽に貯蔵されている液化ガスをほぼそのままの圧で
小容量の複数の高耐圧貯槽に交互に受け入れ、この液化
ガスの一部を導出して空気。The present invention has been made in view of the above, and it is possible to alternately receive liquefied gas stored in a large-capacity storage tank at almost normal pressure at almost the same pressure into a plurality of small-capacity high-pressure storage tanks, and to Deriving the part of the air.

温排水、海水等を利用して気化せしめ、この気化ガスで
該貯槽内を加圧することにより加圧のためのエネルギー
を全く必要とせずに液化ガスを加圧送出し、この各貯槽
より交互に送出された液化ガスを大気、温排水、海水等
により気化して高圧ガスとし連続的に供給する方法であ
る。By vaporizing heated wastewater, seawater, etc. and pressurizing the storage tank with this vaporized gas, liquefied gas is sent under pressure without requiring any energy for pressurization, and is sent out alternately from each storage tank. In this method, the liquefied gas is vaporized in the atmosphere, heated waste water, seawater, etc., and the high-pressure gas is continuously supplied.

以下、図により本発明の詳細な説明する。図は本発明方
法の高耐圧貯槽が３Ｍの場合の実施例に於ける詳細流路
および弁の位置を示す系統図である。図に於いて１は液
化ガスを大気圧近い状態で貯蔵する地上または地下式の
大型貯槽である。、１００．２００．３００は夫々液化
ガスを受入れ切換周期の間貯蔵し、加圧・圧送するため
の高耐圧貯槽である。２は液化ガスポンプで上記大型貯
槽１内の液化ガスを低圧になった前記各貯槽１００゜２
００または３００に揚液するためのものである。Hereinafter, the present invention will be explained in detail with reference to the drawings. The figure is a system diagram showing detailed flow paths and valve positions in an embodiment in which the high-pressure storage tank used in the method of the present invention is 3M. In the figure, 1 is a large above-ground or underground storage tank that stores liquefied gas at near atmospheric pressure. , 100, 200, and 300 are high-pressure storage tanks for receiving liquefied gas, storing it during the switching cycle, pressurizing it, and pumping it out. 2 is a liquefied gas pump that pumps the liquefied gas in the large storage tank 1 to each of the storage tanks 100° 2 at low pressure.
It is for pumping liquid to 00 or 300.

３は加圧状態の液化ガスを空気温、温排水、海水等で気
化させる送ガス蒸発器である。まず大型貯槽１より揚液
ポンプ２によって、内圧がはは大気圧になっている貯槽
１００に液化ガスを送り込む。3 is a gas supply evaporator that vaporizes pressurized liquefied gas using air temperature, heated waste water, seawater, etc. First, liquefied gas is pumped from a large storage tank 1 by a pump 2 into a storage tank 100 whose internal pressure is at atmospheric pressure.

この場合液化カス受入れ弁１０１は開、２０１および３
０１は開である。大気圧の液化ガスが満たされた貯槽１
００は弁１０１を閉じ次いで圧送終了後の貯槽３００の
残ガスを受け入れ該貯槽３０Ｏ内の圧力を下げる。貯槽
１００内の液は大気圧の飽和液であり、一方貯槽３００
内のガスは温度。In this case, the liquefied waste receiving valve 101 is open, 201 and 3
01 is open. Storage tank 1 filled with liquefied gas at atmospheric pressure
00 closes the valve 101 and then receives the remaining gas in the storage tank 300 after the end of the pressure feeding to lower the pressure in the storage tank 300. The liquid in the storage tank 100 is a saturated liquid at atmospheric pressure, while the liquid in the storage tank 300
The gas inside has a temperature.

圧力共に貯槽１００内の液より高いため、残ガス戻し弁
３０２を開にすることによりこのガスは管３１１．３１
２を経て貯槽１００内に流れ込み貯１３００内はほぼ大
気圧造圧が下がる。残ガス戻しライン１’１１．１１２
，２１１．２１２および３１１．３１２の中間にはそれ
ぞれ残ガス戻し弁１０２．２０２．３０２が設けられて
おり、ラインの末端にはリング状で上部に小孔が穿けで
あるガス噴出環１１３，２１３，３１３が夫々貯槽１０
０．２００，３００の内部中間位置または下部に設けら
れている。該ガス噴出環１１３より噴出した前記貯槽３
００の残ガスは・貯槽１００内の液中を上昇する間に低
温の液と直接熱交換し液化する。この場合の貯！１００
内の圧力上昇は０．１に９　／　ｃｙｒｔに過ぎず、受
は入れはほぼ大気圧で行なえる。残ガス戻し弁３０２を
閉じた後、圧力調節弁１０３を開とし、槽内下部の液を
一部、管１１４より抜き出し加圧蒸発器１２０により気
化し、この気化ガスを管１１５より再び貯槽１００へ導
入して槽内を規定圧力迄加圧する。この圧力は等該液化
ガスの臨界圧以上であっても可能でありその際の省エネ
ルギー母は大となる。上記加圧蒸発器は貯Ｍｉ２００お
よび３００にも夫々２２０，３２０が管２１４，３１４
、圧力調節弁２０３．．３０３そして管２１５，３１５
を介して設けられている。また圧力調節弁１０３，２０
３，３０３は自動調節弁とし、各貯槽内の圧を検出して
自動的にこれを調節し、槽内圧を規定圧に保持ツる。加
圧蒸発器１２０，２２０，３２０は空湿式、温水式また
は海水式等いづれも良く容量により適宜選択する。さて
貯槽１００が上記規定圧力に達した後、液化ガス送出弁
１０４を開き送液を開始する。Both pressures are higher than the liquid in the storage tank 100, so by opening the residual gas return valve 302, this gas is released into the pipes 311 and 31.
2 into the storage tank 100, and the pressure inside the storage tank 1300 is reduced to almost atmospheric pressure. Residual gas return line 1'11.112
, 211.212 and 311.312 are respectively provided with residual gas return valves 102.202.302, and at the ends of the lines are gas ejection rings 113, 213 which are ring-shaped and have a small hole in the upper part. , 313 are storage tanks 10, respectively.
0.200, 300 at an internal intermediate position or lower part. The storage tank 3 ejected from the gas ejection ring 113
The remaining gas of 00 is liquefied by directly exchanging heat with the low temperature liquid while rising through the liquid in the storage tank 100. Savings in this case! 100
The internal pressure rise is only 0.1 to 9 cyrt, and receiving and receiving can be done at almost atmospheric pressure. After closing the residual gas return valve 302, the pressure regulating valve 103 is opened, and a portion of the liquid at the bottom of the tank is extracted from the pipe 114 and vaporized by the pressurized evaporator 120, and this vaporized gas is returned to the storage tank 100 from the pipe 115. and pressurize the inside of the tank to the specified pressure. This pressure can even be equal to or higher than the critical pressure of the liquefied gas, and in that case the energy savings will be significant. The pressurized evaporator also has pipes 220 and 320 in the storage Mi 200 and 300, respectively.
, pressure regulating valve 203. ．． 303 and tubes 215, 315
It is provided through. Also, pressure regulating valves 103, 20
Reference numeral 3, 303 denotes an automatic control valve, which detects the pressure in each storage tank and automatically adjusts it to maintain the tank internal pressure at a specified pressure. The pressurized evaporators 120, 220, and 320 may be air/humid type, hot water type, sea water type, etc., and are appropriately selected depending on the capacity. After the storage tank 100 reaches the specified pressure, the liquefied gas delivery valve 104 is opened and liquid delivery is started.

圧力調節弁１’０３は開のままであり送液中液圧は一定
に保持される。液化ガス送出弁１’　０４を経た液化ガ
スは管１１６を経て送ガス蒸発器３に入り空気、温排水
、海水等と熱交換して気化し高圧ガスとなって需要先へ
送出される。この間貯槽２００および３００の液化ガス
送出弁２０４，３０４は閉の状態にある。この様に本発
明は少くとも３基の高圧貯槽、該実施例では貯槽１００
，２００．３００を有し液受入れ、予圧（残ガス受入れ
）、加圧、圧送、残ガス放出（残ガス戻し）の各工程を
各貯槽に於て周期をずらせて繰返すことにより一定圧以
上、必要に応じ臨界圧以上に液化ガスを加圧、圧送しこ
れを気化して需要先へ送出する方法である。上記各工程
に於ける各貯槽ｊ５よびそれらを結ぶ系統に設けられた
各弁の開閉状態を表に示す。The pressure control valve 1'03 remains open and the liquid pressure is kept constant during liquid feeding. The liquefied gas that has passed through the liquefied gas delivery valve 1'04 enters the gas supply evaporator 3 through the pipe 116, exchanges heat with air, heated waste water, seawater, etc., evaporates, becomes high-pressure gas, and is sent to the consumer. During this time, the liquefied gas delivery valves 204, 304 of the storage tanks 200 and 300 are in a closed state. Thus, the present invention provides at least three high pressure storage tanks, in this embodiment 100 storage tanks.
, 200.300, and by repeating the steps of liquid reception, prepressure (residual gas reception), pressurization, pressure feeding, and residual gas release (residual gas return) in each storage tank with different cycles, the pressure can be increased to a certain level or higher. This is a method in which liquefied gas is pressurized to a level above the critical pressure as necessary, and the liquefied gas is pumped, vaporized, and sent to the consumer. The opening/closing state of each valve provided in each storage tank j5 and the system connecting them in each of the above steps is shown in the table.

次に本実旅例の方法によって液化天然ガス（以下ＬＮＧ
という）をが圧気化して連続的に供給する場合の省エネ
ルギーの量をめると、ＬＮＧ５Ｑ　Ｔｏｎ　／　ｈを液
ポンプで大気圧から５　Ｑ　ａｔａ迄加圧・圧送する場
合の所要動力は１５１ｋＷであり、年間では約１３２２
７６０ｋｗにも達づる量となる。Next, using the method described in this example, liquefied natural gas (hereinafter referred to as LNG)
Considering the amount of energy saved when LNG is vaporized and continuously supplied, the power required to pressurize and pump 5 Q Ton/h of LNG from atmospheric pressure to 5 Q ata using a liquid pump is 151 kW. , approximately 1322 per year
The amount will reach 760kW.

そしてＬＮＧ加圧用ポンプに代わる設備として必要なの
は前記蓄圧用の貯槽およびその加圧蒸発器のみである。All that is required as equipment to replace the LNG pressurizing pump is the pressure accumulating storage tank and its pressurizing evaporator.

この貯槽の容ωは切替周期５分として である。即ち従来より用いられているコールドエバポレ
ーター型式の高圧貯槽を最低３基設置することにより殆
ど動力を必要と゛けず高圧力のガスを連続的に供給でき
る。The capacity ω of this storage tank is based on a switching period of 5 minutes. That is, by installing at least three high-pressure storage tanks of the conventional cold evaporator type, high-pressure gas can be continuously supplied with almost no power required.

以上の如く本発明は加圧蒸発器付液化ガス高圧貯槽を少
くとも３基用いて自己加圧方式により液化ガスを高圧に
、必要に応じて臨界圧以上に昇圧し、「圧送」、「ガス
戻し」、「液受入れ」。As described above, the present invention utilizes at least three high-pressure storage tanks for liquefied gas with pressurized evaporators to raise the pressure of liquefied gas to high pressure and, if necessary, to a critical pressure or higher using a self-pressurizing method. "Return", "Liquid Reception".

［予圧（残ガス受入れ）」、「加圧」の各工程を各貯槽
に於て周期をづらせて繰返し、圧送した液化ガスを大気
、温排水、海水等で加温気化させて高圧ガスを連続的に
供給する方法であり、従って高圧貯槽への揚液用エネル
ギー以外を全く不要即ち所要エネルギーを殆ど必要′と
しない効果を有する。[Prepressure (receiving residual gas)] and pressurization processes are repeated in different cycles in each storage tank, and the liquefied gas that has been pumped is heated and vaporized in the atmosphere, warm wastewater, seawater, etc., and high-pressure gas is produced. It is a method of continuously supplying liquid, and therefore has the effect that it requires no energy other than the energy for pumping the liquid to the high-pressure storage tank, that is, it requires almost no energy.

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

図は本発明方法の一実施例を示す系統図である。 １は液化ガスの大型貯槽、２は液化ガスの揚液ポンプ、
３は送ガス蒸発器、１００，２００及び３００は高耐圧
貯槽、１２０，２２０及び３２０は加圧蒸発器である。 特　許　出　願　人　日本酸素株式会社手続補正歯動式
） １．事件の表示 昭和５８年特許願第２．０４４４９号 ２、発明の名称 高圧ガスの供給方法 ３、補正をする者 事件との関係　特許出願人 日本酸素株式会社 ４、代理人 東京都千代田区鍛冶町−丁目９番１６号５、補正命令の
日付 昭和５９年１月３１日 ６、補正の対象 明細書全文The figure is a system diagram showing an embodiment of the method of the present invention. 1 is a large liquefied gas storage tank, 2 is a liquefied gas pump,
3 is a gas feed evaporator, 100, 200 and 300 are high pressure storage tanks, and 120, 220 and 320 are pressurized evaporators. Patent applicant: Nippon Sanso Co., Ltd. Procedural correction gear type) 1. Display of the case 1982 Patent Application No. 2.04449 2 Name of the invention High-pressure gas supply method 3 Person making the amendment Relationship to the case Patent applicant Nippon Sanso Co., Ltd. 4 Agent Kajicho, Chiyoda-ku, Tokyo - Chome 9-16 No. 5, Date of amendment order January 31, 1980 6, Full text of the specification subject to amendment

Claims (1)

【特許請求の範囲】 １、少くとも３基の高耐圧液化ガス貯槽を有し、その中
の任意の１基の貯槽より規定圧力に加圧した液化ガスを
送出し、送ガス蒸発器を通して加温し気化後送比する工
程、当該貯槽の残ガスを液受入れの終了した他の貯槽に
移送して当該貯槽内をほぼ大気圧とした後液化ガスを受
け入れる工程、貯槽内の液化ガスの一部を導出し気化後
当該貯槽に導入することにより当該貯槽内を規定圧力に
加圧する工程、の３工程を前記３基以上の各貯槽に於て
周期をずらせて順次繰返すことを特徴とする液化ガスの
気化による高圧ガスの供給方法。 ２、前記規定圧力が当該液化ガスの臨界圧以上の圧であ
ることを特徴とする特許請求の範囲第１項記載の液化ガ
スの気化による高圧ガスの供給方法。[Claims] 1. It has at least three high-pressure liquefied gas storage tanks, and the liquefied gas pressurized to a specified pressure is sent from any one storage tank among them, and the liquefied gas is fed through a gas evaporator. A step of heating, vaporizing and then transferring the gas, transferring the remaining gas in the storage tank to another storage tank that has finished receiving liquid, bringing the inside of the tank to almost atmospheric pressure, and then receiving the liquefied gas; Liquefaction characterized in that the three steps of pressurizing the inside of the storage tank to a specified pressure by deriving the liquid, vaporizing it, and introducing it into the storage tank are sequentially repeated at staggered intervals in each of the three or more storage tanks. A method of supplying high-pressure gas by vaporizing the gas. 2. The method for supplying high-pressure gas by vaporizing liquefied gas according to claim 1, wherein the specified pressure is a pressure higher than the critical pressure of the liquefied gas.
JP20444983A 1983-10-31 1983-10-31 High pressure gas feeding method Granted JPS6098299A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP20444983A JPS6098299A (en) 1983-10-31 1983-10-31 High pressure gas feeding method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP20444983A JPS6098299A (en) 1983-10-31 1983-10-31 High pressure gas feeding method

Publications (2)

Publication Number Publication Date
JPS6098299A true JPS6098299A (en) 1985-06-01
JPH0548399B2 JPH0548399B2 (en) 1993-07-21

Family

ID=16490707

Family Applications (1)

Application Number Title Priority Date Filing Date
JP20444983A Granted JPS6098299A (en) 1983-10-31 1983-10-31 High pressure gas feeding method

Country Status (1)

Country Link
JP (1) JPS6098299A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001248963A (en) * 2000-01-05 2001-09-14 Boc Group Inc:The Method and apparatus for producing pressurized high purity liquid carbon dioxide stream
JP2002532668A (en) * 1998-12-18 2002-10-02 エクソンモービル アップストリーム リサーチ カンパニー Method of discharging compressed liquefied natural gas from container
JP2002317899A (en) * 2001-04-20 2002-10-31 Ishikawajima Plant Construction Co Ltd Method for delivering low-temperature liquid in small capacity and at high pressure
JP2012132558A (en) * 2010-12-18 2012-07-12 Boeing Co:The Continuous flow thermodynamic pump
JP2018179017A (en) * 2017-04-03 2018-11-15 レール・リキード−ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード Lng continuous supply system and lng continuous supply method

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002532668A (en) * 1998-12-18 2002-10-02 エクソンモービル アップストリーム リサーチ カンパニー Method of discharging compressed liquefied natural gas from container
JP2001248963A (en) * 2000-01-05 2001-09-14 Boc Group Inc:The Method and apparatus for producing pressurized high purity liquid carbon dioxide stream
JP4494652B2 (en) * 2000-01-05 2010-06-30 ザ・ビーオーシー・グループ・インコーポレーテッド Method and apparatus for generating a pressurized high purity liquid carbon dioxide stream
JP2002317899A (en) * 2001-04-20 2002-10-31 Ishikawajima Plant Construction Co Ltd Method for delivering low-temperature liquid in small capacity and at high pressure
JP2012132558A (en) * 2010-12-18 2012-07-12 Boeing Co:The Continuous flow thermodynamic pump
JP2018179017A (en) * 2017-04-03 2018-11-15 レール・リキード−ソシエテ・アノニム・プール・レテュード・エ・レクスプロワタシオン・デ・プロセデ・ジョルジュ・クロード Lng continuous supply system and lng continuous supply method

Also Published As

Publication number Publication date
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