JPS5980600A - Nitrogen gas enclosing device - Google Patents
Nitrogen gas enclosing deviceInfo
- Publication number
- JPS5980600A JPS5980600A JP57187575A JP18757582A JPS5980600A JP S5980600 A JPS5980600 A JP S5980600A JP 57187575 A JP57187575 A JP 57187575A JP 18757582 A JP18757582 A JP 18757582A JP S5980600 A JPS5980600 A JP S5980600A
- Authority
- JP
- Japan
- Prior art keywords
- temperature
- gas
- exit
- water
- nitrogen gas
- 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
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
- F17C2203/00—Vessel construction, in particular walls or details thereof
- F17C2203/06—Materials for walls or layers thereof; Properties or structures of walls or their materials
- F17C2203/0602—Wall structures; Special features thereof
- F17C2203/0612—Wall structures
- F17C2203/0626—Multiple walls
- F17C2203/0629—Two walls
-
- 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
- F17C2205/0323—Valves
- F17C2205/0326—Valves electrically actuated
-
- 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
- F17C2221/01—Pure fluids
- F17C2221/014—Nitrogen
-
- 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
- F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
- F17C2250/06—Controlling or regulating of parameters as output values
- F17C2250/0605—Parameters
- F17C2250/0631—Temperature
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
Abstract
Description
【発明の詳細な説明】
〔発明の利用分野〕
本発明は液化窒素低温貯槽方式による火力発電設備など
に用いる窒素ガス封入装置に関する。DETAILED DESCRIPTION OF THE INVENTION [Field of Application of the Invention] The present invention relates to a nitrogen gas filling device used in thermal power generation equipment using a liquefied nitrogen low-temperature storage tank method.
従来の発電設備用の窒素ガス封入装置は、高圧ガスボン
ベ方式が一般に広く使用されていた。一方、本発明の、
液化窒素低温貯槽方式のものも近年使用されるようにな
ってきたが、元来、液化窒素低温貯槽方式の窒素ガス供
給設備は化学プラントのバーシンク用、その他に広く用
いられている。Conventional nitrogen gas filling devices for power generation equipment have generally been of the high-pressure gas cylinder type. On the other hand, the present invention
Although liquefied nitrogen low-temperature storage tank type systems have come into use in recent years, liquefied nitrogen low-temperature storage tank type nitrogen gas supply equipment has originally been widely used for bar sinks in chemical plants and other applications.
しかし、これ等は、窒素ガスを所賛の圧力に減圧して、
供給することに主眼が置かれでいて、温度制御を行なっ
ていなかった。このため、ボンベ方式でも、減圧による
ガス温度の降−[があり、ガス供給を受ける側は低温脆
性や低温熱衝撃等による損傷に対して配慮する心安があ
った。しかし、この問題も、−196U近傍の液化窒素
を気化器を通してガス化し、そのガスを減圧して直送す
る方式の液化窒素低温貯槽方式では問題があった。However, these methods reduce the nitrogen gas to the desired pressure,
The main focus was on supply, and there was no temperature control. For this reason, even in the cylinder method, there is a drop in gas temperature due to depressurization, and the side receiving the gas supply has peace of mind that consideration should be given to damage caused by low-temperature brittleness, low-temperature thermal shock, and the like. However, this problem also occurs in the liquefied nitrogen low-temperature storage tank system, in which liquefied nitrogen around -196U is gasified through a vaporizer, and the gas is depressurized and sent directly.
即ち、−19611’の液化窒素は気化器を通じてガス
化し、その後の加温部を通じて、大気温度に至ることは
困−であり、特に、厳寒時には気化吸収熱のため、2問
〜10謔のJ9さの霜が発生し、気化部及び加温部共に
フィンデユープの熱交換は著しく妨げられ、このため、
ガス出口温度は−IOCを下まわることになる。この温
度は、一般に使用されている配管料−や高圧容器等の映
用限界温度を超えるものであシ、低温脆性や低温熱衝撃
上好ましくなく、寿命を短かくする要因であり、外気温
度の如伺によっては運転が不可能になる欠点があった。In other words, it is difficult for liquefied nitrogen of -19611' to gasify through a vaporizer and then reach atmospheric temperature through a heating section.Especially in severe cold, due to the heat absorbed by vaporization, J9 questions 2 to 10 are difficult to reach. As a result, the heat exchange of the fin duplex in both the vaporization section and the heating section is significantly hindered.
The gas outlet temperature will be below -IOC. This temperature exceeds the operational limit temperature of commonly used piping materials and high-pressure vessels, and is unfavorable in terms of low-temperature brittleness and low-temperature thermal shock, which shortens the lifespan. Depending on the Nyoki, there was a drawback that it became impossible to drive.
すなわち、第1図に示すように、液化低温貯槽2より導
管3を通じて気化器4に流入したガスはフィンチューブ
10よシ、空気中の熱を吸収し、その熱を液体窒素に伝
導して、蒸発潜熱を得て気化し 窒素ガスとなる。この
ガスは、後段の加温部5に通じで、同様にフィンチュー
ブで外気の熱を吸収して、蒸発点の約−160Cより逐
次温度が上昇して気化器の出口に設置した減圧装置の調
整弁6に通じ、出口ヘッダ−8に通じる。このヘッダー
出口圧力はヘッダーに設けられた圧力調整器7によって
調整弁6へ信号が伝わシ、一定の圧力でガスの供給が行
なわれる。That is, as shown in FIG. 1, the gas flowing from the liquefied cryogenic storage tank 2 through the conduit 3 into the vaporizer 4 absorbs heat in the air through the fin tube 10, and transfers the heat to liquid nitrogen. It gains latent heat of vaporization and evaporates to become nitrogen gas. This gas passes through the heating section 5 in the latter stage, where it similarly absorbs the heat of the outside air with the fin tube, and the temperature gradually rises from the evaporation point of about -160C to the pressure reducing device installed at the outlet of the vaporizer. It communicates with the regulating valve 6 and with the outlet header 8 . A signal of this header outlet pressure is transmitted to a regulating valve 6 by a pressure regulator 7 provided in the header, and gas is supplied at a constant pressure.
この、従来設備のフィンチューブ10にN寒時に第2図
に示ずような鞘11がUく。この鞘11は十分な空気層
を含むため、熱伝導ね、殆んど断たれてしまい、更に、
ガスの放出を続けると、矛゛6の範囲、が拡大し、やが
て、ガス温度は月料の使用限界温度の一1OCf−下ま
わることになる。このガスは第3側に示すように、導管
12を通じて、発電設備の機器の13及び14に導入さ
れる。The fin tube 10 of this conventional equipment has a sheath 11 as shown in FIG. 2 during cold weather. Since this sheath 11 contains a sufficient air layer, heat conduction is almost cut off, and furthermore,
As the gas continues to be released, the range of target 6 will expand, and the gas temperature will eventually fall below the operating limit temperature of the monthly charge by 1 OCf. This gas is introduced through conduit 12 to the equipment 13 and 14 of the power plant, as shown on the third side.
本発明の目的は、冬期の厳寒時にも、プラントに対し十
分安全に窒素ガスを供給できる窒素側入用ガス供給装置
を提供するにある。An object of the present invention is to provide a nitrogen side inlet gas supply device that can supply nitrogen gas to a plant in a sufficiently safe manner even during the severe cold of winter.
液化窒素の低温貯槽方式に於ける窒素ガス供給装置に於
いて、液化ガスは吸熱を伴って気化するため、幾本もの
フィンチーブを並列に配置し、これを集合して、1本の
フィンチューブを通じて出口ガスを加温する構造のもの
が一般に用いられる。In the nitrogen gas supply equipment for the low-temperature storage tank system for liquefied nitrogen, since the liquefied gas vaporizes with endothermic absorption, a number of fin tubes are arranged in parallel, and they are collected and fed through a single fin tube. A structure that heats the outlet gas is generally used.
この従来方式は、フィンチューブの加温媒体は外気によ
るもので、空温式であった1、この/ヒめ、寒冷地の厳
寒時には、霜が付く欠点があり、霜付きの後Vよ、加温
の効果も激減し、外気の温度が一10C以下のときは更
に低温のガスが供給されることになる。In this conventional method, the heating medium of the fin tube is the outside air, and it is an air-heated type.1, This/Hime, has the disadvantage that frost forms during severe cold weather in cold regions, and after frost formation, The heating effect is also drastically reduced, and when the outside air temperature is below 110C, even lower temperature gas is supplied.
本発明は、気化器の気化部及び加温部の上部に流水ノズ
ルを配置し、これに接続する配管の途中に自動弁を配置
し、これの開閉を、ガスの出口温度より得た電気信号に
よって制御する。使用初め又は使用中の外気温度の低下
や、霜付による使用中のガス温度の低下や、厳寒時の低
温ガスは、摂氏零度以上の水温近くまでガスは予熱され
、−10111’以上の窒素ガスの供給が確保される。In the present invention, a running water nozzle is arranged above the vaporizing part and the heating part of a vaporizer, an automatic valve is arranged in the middle of the piping connected to this, and the opening and closing of this valve is controlled by an electric signal obtained from the gas outlet temperature. controlled by. If the outside air temperature decreases at the beginning of use or during use, the gas temperature decreases during use due to frosting, or low-temperature gas in severe cold, the gas is preheated to a temperature close to the water temperature of -10111' or higher, and nitrogen gas of -10111' or higher is used. supply will be ensured.
本発明の一実施例を第4図によって説明する。 An embodiment of the present invention will be explained with reference to FIG.
本発明の液化窒素低温貯槽方式によるガス供給設備の構
造を第4図によつヤ説明する。The structure of the gas supply equipment using the liquefied nitrogen low temperature storage tank system of the present invention will be explained with reference to FIG.
即ち、気化器の気化部フィンチューブ上部と、同様、気
化器の加温部のフィンチューブの上部に、流水ノズル1
6を設置し、このノズルにjluする水道管17に制御
弁18を介して水道源に接続する。That is, the running water nozzle 1 is installed at the top of the fin tube of the vaporizing section of the vaporizer, and similarly at the top of the fin tube of the heating section of the vaporizer.
6 is installed, and a water pipe 17 that connects to this nozzle is connected to a water source via a control valve 18.
この制御弁は、ガスの出口へラダ8に設けた温度調整側
より信号を得て、制御する。This control valve is controlled by receiving a signal from the temperature adjustment side provided on the ladder 8 to the gas outlet.
この発電設備用ガス供給設備によって、作動時は、外気
温度の低下によってガス温度出口より得た信号で、フィ
ンチューブ上部より、流水を行ない、フィンチューブ表
面の霜を消失さゼ、かつ、 □加温部に流水による熱を
得て、従来の一10C程度の外気となる厳寒時にもガス
の発生を安定に続け、かつ、出口温度を一10tl?以
」二に保つことができる。With this gas supply equipment for power generation equipment, during operation, a signal obtained from the gas temperature outlet due to a drop in outside air temperature causes water to flow from the top of the fin tube to eliminate frost on the surface of the fin tube. By obtaining heat from running water in the warm part, it continues to generate gas stably even in severe cold when the outside air is about -10C, and the outlet temperature can be raised to -10tl? It can be kept as follows.
第1図は従来の系統図、第2図はフィンチューは
第4図は本発明の系統図である
16・・・流水ノズル、17・・・水道管、18制御弁
。
代理人 弁理士 高橋明夫FIG. 1 is a conventional system diagram, FIG. 2 is a fin tube, and FIG. 4 is a system diagram of the present invention. 16...Flowing water nozzle, 17...Water pipe, 18 Control valve. Agent Patent Attorney Akio Takahashi
Claims (1)
、気化器と、仁の気化器の後流に配置しだ熱又換器と、
この熱交換器の上部に散水用ノズルを配置6シ、自動弁
で加温用水を散水する手段、を設けたことを特徴とする
窒素ガス封入装置。1. In the nitrogen gas system, a water heater, a vaporizer, and a heat exchanger placed downstream of the vaporizer,
A nitrogen gas filling device characterized in that a water sprinkling nozzle is disposed above the heat exchanger, and a means for sprinkling heating water using an automatic valve is provided.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57187575A JPS5980600A (en) | 1982-10-27 | 1982-10-27 | Nitrogen gas enclosing device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP57187575A JPS5980600A (en) | 1982-10-27 | 1982-10-27 | Nitrogen gas enclosing device |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS5980600A true JPS5980600A (en) | 1984-05-10 |
Family
ID=16208496
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP57187575A Pending JPS5980600A (en) | 1982-10-27 | 1982-10-27 | Nitrogen gas enclosing device |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5980600A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04131597A (en) * | 1990-09-21 | 1992-05-06 | Kooa Gas Kagoshima:Kk | Hot air-hot water combined carburetor device |
JPH04131596A (en) * | 1990-09-21 | 1992-05-06 | Kooa Gas Kagoshima:Kk | Hot air-hot water combined type carburetor device |
EP1092911A2 (en) * | 1999-10-14 | 2001-04-18 | Koagas Nihon Co., Ltd. | Air-heated/hot-water type vaporizer and air-heated/hot-water type gas producing plant |
EP1724514A1 (en) * | 2005-05-19 | 2006-11-22 | Black & Veatch Corporation | Vaporizor |
-
1982
- 1982-10-27 JP JP57187575A patent/JPS5980600A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH04131597A (en) * | 1990-09-21 | 1992-05-06 | Kooa Gas Kagoshima:Kk | Hot air-hot water combined carburetor device |
JPH04131596A (en) * | 1990-09-21 | 1992-05-06 | Kooa Gas Kagoshima:Kk | Hot air-hot water combined type carburetor device |
EP1092911A2 (en) * | 1999-10-14 | 2001-04-18 | Koagas Nihon Co., Ltd. | Air-heated/hot-water type vaporizer and air-heated/hot-water type gas producing plant |
EP1092911A3 (en) * | 1999-10-14 | 2002-05-22 | Koagas Nihon Co., Ltd. | Air-heated/hot-water type vaporizer and air-heated/hot-water type gas producing plant |
EP1724514A1 (en) * | 2005-05-19 | 2006-11-22 | Black & Veatch Corporation | Vaporizor |
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