JPH06294497A - Carburetor - Google Patents

Carburetor

Info

Publication number
JPH06294497A
JPH06294497A JP7690593A JP7690593A JPH06294497A JP H06294497 A JPH06294497 A JP H06294497A JP 7690593 A JP7690593 A JP 7690593A JP 7690593 A JP7690593 A JP 7690593A JP H06294497 A JPH06294497 A JP H06294497A
Authority
JP
Japan
Prior art keywords
heat exchangers
heat
temperature liquid
heat exchanger
low
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
JP7690593A
Other languages
Japanese (ja)
Inventor
Seiichi Hasegawa
清一 長谷川
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.)
IHI Corp
Original Assignee
IHI 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 IHI Corp filed Critical IHI Corp
Priority to JP7690593A priority Critical patent/JPH06294497A/en
Publication of JPH06294497A publication Critical patent/JPH06294497A/en
Pending legal-status Critical Current

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  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

PURPOSE:To continuously use a carburetor and easily defrost heat exchangers in winter and at a cold district by feeding a low-temperature liquid to one side of two heat exchangers connected in parallel to obtain hot gas, and feeding it to the other heat exchangers for defrosting. CONSTITUTION:A carburetor feeds the low-temperature liquid 2 stored in a tank 1 to air-heated heat exchangers 6, 7, 8, 9 for the heat exchange with the atmospheric air to vaporize it. Two heat exchangers 6, 8 and 7, 9 are connected in parallel, valves 4, 5, 14, 15, 17, 18 are provided as passage switching means to feed the low-temperature liquid 2 to one side of the heat exchangers 6, 8 and 7, 9, and hot-gas passages 11, 12, 13, 16 are provided to feed the low- temperature liquid 2 converted into hot gas through the heat exchangers on one side to the heat exchangers on the other side for defrosting. The low- temperature liquid 2 is heat-exchanged with the atmospheric air by the heat exchangers on one side and vaporized into hot gas, and it is fed to the heat exchangers on the other side to defrost them.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、タンク内に貯蔵された
低温液体を空温式熱交換器に流して大気と熱交換させて
気化する気化器に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a vaporizer for causing a low temperature liquid stored in a tank to flow through an air heat type heat exchanger to exchange heat with the atmosphere and vaporize.

【0002】[0002]

【従来の技術】LNG(液化天然ガス)、LN2 (液体
窒素)及びLO2 (液体酸素)等の低温液体はタンク内
に貯蔵されており、使用する場合には貯蔵された低温液
体を気化器で気化した後ユーザ等に供給される。
2. Description of the Related Art Low temperature liquids such as LNG (liquefied natural gas), LN 2 (liquid nitrogen) and LO 2 (liquid oxygen) are stored in a tank, and when used, the stored low temperature liquid is vaporized. After being vaporized in a container, it is supplied to users.

【0003】気化器には空温式熱交換器(以下熱交換器
という)が用いられており、低温液体が通過するチュー
ブと、チューブの外側に設けられ大気と熱交換するため
のフィンとで構成されている(いずれも図示せず)。低
温液体がこのチューブの内部を通過すると低温液体が空
温(大気温)で気化されるようになっている。
An air-heat type heat exchanger (hereinafter referred to as a heat exchanger) is used as a vaporizer, and is composed of a tube through which a low-temperature liquid passes and fins provided outside the tube for exchanging heat with the atmosphere. Configured (none shown). When the low temperature liquid passes through the inside of this tube, the low temperature liquid is vaporized at the air temperature (atmospheric temperature).

【0004】ところで熱交換器は、連続使用して低温液
体を気化させると、そのチューブやフィンに霜が付着し
て気化能力が指数関数的に低下して使用不能となる。
When the heat exchanger is continuously used to vaporize the low-temperature liquid, frost adheres to the tubes and fins of the heat exchanger, and the vaporization ability is exponentially reduced, making the heat exchanger unusable.

【0005】そこで図2に示すように2つの熱交換器を
バルブで切替えて使用することが行われている。
Therefore, as shown in FIG. 2, two heat exchangers are used by switching them with valves.

【0006】図2は従来の気化器を説明するための説明
図である。
FIG. 2 is an explanatory view for explaining a conventional vaporizer.

【0007】同図において、1は冷却された低温液体2
を貯蔵するためのタンクであり、分岐チューブ3を介し
て2つのバルブ4、5に接続されている。バルブ(図の
上側)4は空温式熱交換器(以下熱交換器という)6の
入口にチューブを介して接続されており、バルブ(図の
下側)5は熱交換器7の入口にチューブを介して接続さ
れている。両熱交換器6、7の出口はさらに熱交換器
8、9の入口に接続され両熱交換器8、9の出口は合流
チューブ10に接続されている。そのため、いずれか一
方のバルブ、例えばバルブ4だけ開けて実線矢印のよう
に低温液体の流路を形成し、熱交換器6、8に霜が付着
したときにはそのバルブ4を閉じて熱交換器6、8の自
然除霜を行なうと共に、他のバルブ5を開けて破線矢印
のように低温液体の流路を形成して熱交換器7、9を使
用することにより低温液体2を気化している。
In the figure, 1 is a cooled low temperature liquid 2
Is a tank for storing the gas and is connected to two valves 4 and 5 via a branch tube 3. The valve (upper side of the figure) 4 is connected to the inlet of the air-heat type heat exchanger (hereinafter referred to as heat exchanger) 6 via a tube, and the valve (lower side of the figure) 5 is connected to the inlet of the heat exchanger 7. It is connected via a tube. The outlets of both heat exchangers 6 and 7 are further connected to the inlets of heat exchangers 8 and 9, and the outlets of both heat exchangers 8 and 9 are connected to merging tube 10. Therefore, only one of the valves, for example, the valve 4 is opened to form the flow path of the low temperature liquid as shown by the solid arrow, and when frost is adhered to the heat exchangers 6 and 8, the valve 4 is closed and the heat exchanger 6 is closed. , 8 is naturally defrosted, the other valve 5 is opened to form a flow path of the low temperature liquid as shown by the broken line arrow, and the heat exchangers 7 and 9 are used to vaporize the low temperature liquid 2. .

【0008】[0008]

【発明が解決しようとする課題】しかしながら、上述し
た気化器を冬季や寒冷地で使用した場合には一方の熱交
換器には4時間程で霜が付着し、定格能力以下になるの
で連続使用する場合にはバルブを切替えなければならな
いが他方の熱交換器も同様に4時間程で霜が付着し定格
能力以下になる。そのため霜を自然除霜するのに1〜2
日かかってしまいその間待機しなければならず非能率的
である。また、連続使用できる気化器を実現するには熱
交換器を6組並列に接続して4時間毎にバルブを順番に
1つずつ開けると共に他のバルブを閉めて熱交換器の自
然除霜を行わなければならず装置が大型化してしまう。
However, when the vaporizer described above is used in winter or in cold regions, frost adheres to one heat exchanger in about 4 hours and falls below the rated capacity, so continuous use is possible. In that case, the valve must be changed, but the other heat exchanger also becomes frosted in about 4 hours and falls below the rated capacity. Therefore 1-2 to defrost frost naturally
It takes days and it is inefficient to wait during that time. Also, in order to realize a vaporizer that can be continuously used, six sets of heat exchangers are connected in parallel, one valve is opened one by one every 4 hours, and other valves are closed to allow natural defrosting of the heat exchanger. This must be done, and the device becomes large.

【0009】そこで、本発明の目的は、上記課題を解決
し、冬季や寒冷地でも連続使用できる気化器を提供する
ことにある。
Therefore, an object of the present invention is to solve the above problems and to provide a carburetor which can be continuously used even in the winter and cold regions.

【0010】[0010]

【課題を解決するための手段】上記目的を達成するため
に本発明は、タンク内に貯蔵された低温液体を空温式熱
交換器に流して大気と熱交換させて気化する気化器にお
いて、2つの熱交換器を並列に接続すると共に、これら
の熱交換器のいずれか一方に低温液体を流す流路切替手
段を設け、さらにそのいずれか一方の熱交換器を通って
ホットガスとされた低温気体を他方の熱交換器に流して
除霜を行うためのホットガス流路を設けたものである。
In order to achieve the above object, the present invention provides a vaporizer in which a low temperature liquid stored in a tank is passed through an air temperature type heat exchanger to exchange heat with the atmosphere and vaporize. Two heat exchangers were connected in parallel, and one of these heat exchangers was provided with a flow path switching means for flowing a low-temperature liquid, and further, a heat gas was passed through one of the heat exchangers. A hot gas flow path for defrosting the low temperature gas by flowing it through the other heat exchanger is provided.

【0011】[0011]

【作用】上記構成によれば、低温液体を2つの熱交換器
のいずれか一方に流して大気と熱交換させて気化させて
ホットガスとし、この低温液体のホットガスを他方の熱
交換器に流すことで他方の熱交換器の除霜を行うことが
できる。
According to the above construction, the low temperature liquid is caused to flow into one of the two heat exchangers to exchange heat with the atmosphere to be vaporized into hot gas, and the hot gas of the low temperature liquid is passed to the other heat exchanger. By flowing, the other heat exchanger can be defrosted.

【0012】[0012]

【実施例】以下、本発明の一実施例を添付図面に基づい
て詳述する。
An embodiment of the present invention will be described in detail below with reference to the accompanying drawings.

【0013】図1は本発明の気化器を説明するための説
明図である。尚図2に示した部材と同一の部材には同一
の符号を用いた。
FIG. 1 is an explanatory view for explaining the vaporizer of the present invention. The same members as those shown in FIG. 2 are designated by the same reference numerals.

【0014】同図において、1は低温液体2を貯蔵する
ためのタンクであり、分岐チューブ3を介して2つのバ
ルブ4、5に接続されている。バルブ4は分岐チューブ
11を介して熱交換器6の入口に接続されており、バル
ブ5は分岐チューブ12を介して熱交換器7の入口に接
続されている。熱交換器6の出口はチューブを介して熱
交換器8の入口に接続され、熱交換器7の出口はチュー
ブを介して熱交換器9の入口に接続されている。
In the figure, reference numeral 1 is a tank for storing a low temperature liquid 2, which is connected to two valves 4 and 5 through a branch tube 3. The valve 4 is connected to the inlet of the heat exchanger 6 via a branch tube 11, and the valve 5 is connected to the inlet of the heat exchanger 7 via a branch tube 12. The outlet of the heat exchanger 6 is connected to the inlet of the heat exchanger 8 via a tube, and the outlet of the heat exchanger 7 is connected to the inlet of the heat exchanger 9 via a tube.

【0015】熱交換器8の出口は分岐チューブ13を介
してバルブ14、15に接続され、熱交換器9の出口は
分岐チューブ16を介してバルブ17、18に接続され
ている。バルブ15は分岐チューブ12に接続され、バ
ルブ17は分岐チューブ11に接続されている。バルブ
14、18は合流チューブ19に接続されている。
The outlet of the heat exchanger 8 is connected to the valves 14 and 15 via the branch tube 13, and the outlet of the heat exchanger 9 is connected to the valves 17 and 18 via the branch tube 16. The valve 15 is connected to the branch tube 12, and the valve 17 is connected to the branch tube 11. The valves 14 and 18 are connected to a merging tube 19.

【0016】尚、分岐チューブ13及び分岐チューブ1
2と、分岐チューブ11及び分岐チューブ16とはそれ
ぞれホットガス流路を形成している。バルブ4、5、1
4、15、17、18で流路切替手段を形成している。
The branch tube 13 and the branch tube 1
2, the branch tube 11 and the branch tube 16 respectively form a hot gas flow path. Valves 4, 5, 1
4, 15, 17, and 18 form a flow path switching unit.

【0017】次に実施例の作用を述べる。Next, the operation of the embodiment will be described.

【0018】まず操作者がバルブ4、15、18を開け
る(全開)と共にバルブ5、14、17を閉じる(全
閉)と、タンク1から低温液体が実線矢印の方向に流れ
る。すなわち低温液体2は分岐チューブ3、バルブ4及
び分岐チューブ11を通って熱交換器6、8内を流れる
と共に気化され、その液体ガスが分岐チューブ13、バ
ルブ15及び分岐チューブ12を通って熱交換器7、9
内を通過して分岐チューブ16、バルブ18及び合流チ
ューブ19からユーザ等に供給される。
First, when the operator opens the valves 4, 15, 18 (fully open) and closes the valves 5, 14, 17 (fully closed), the cryogenic liquid flows from the tank 1 in the direction of the solid arrow. That is, the cryogenic liquid 2 flows through the branch tube 3, the valve 4 and the branch tube 11 in the heat exchangers 6 and 8 and is vaporized, and the liquid gas passes through the branch tube 13, the valve 15 and the branch tube 12 to exchange heat. Bowl 7, 9
After passing through the inside, it is supplied to the user or the like from the branch tube 16, the valve 18, and the confluent tube 19.

【0019】熱交換器6、8のチューブ及びフィンは大
気と熱交換するため霜が付着するが、所定の時間(例え
ば定格運転時間)が経過した後で操作者がバルブ4、1
5、18を閉めると共にバルブ5、14、17を開ける
と、ホットガス流路が切り替わり、タンク1から低温液
体が破線矢印の方向に流れる。すなわち、低温液体2は
分岐チューブ3、バルブ5及び分岐チューブ12を通っ
て熱交換器7、9内を通過して気化されると共に気化し
た低温ガスが分岐チューブ16、バルブ17及び分岐チ
ューブ11を通って熱交換器6、8内を流れる。これと
共に気化したガスが熱交換器6、8に内部から熱を加え
るため熱交換器6、8の霜取りが行われる。気化した低
温ガスは分岐チューブ13、バルブ14及び合流チュー
ブ19からユーザ等に供給される。
Frost adheres to the tubes and fins of the heat exchangers 6 and 8 because they exchange heat with the atmosphere, but after a predetermined time (for example, the rated operation time) has passed, the operator operates the valves 4 and 1.
When the valves 5, 14, 17 are opened and the valves 5, 14, 17 are closed, the hot gas flow paths are switched, and the low temperature liquid flows from the tank 1 in the direction of the broken line arrow. That is, the low temperature liquid 2 passes through the branch tube 3, the valve 5 and the branch tube 12 to pass through the heat exchangers 7 and 9 to be vaporized, and the vaporized low temperature gas passes through the branch tube 16, the valve 17 and the branch tube 11. Flow through the heat exchangers 6, 8. At the same time, the vaporized gas applies heat from the inside to the heat exchangers 6 and 8, so that the heat exchangers 6 and 8 are defrosted. The vaporized low temperature gas is supplied to the user or the like through the branch tube 13, the valve 14 and the confluent tube 19.

【0020】以下所定の時間毎に操作者がバルブ4、
5、14、15、17、18を操作してホットガス流路
を切替えることにより、冬季や寒冷地でも新たに熱源を
設けたり、熱交換器を増設することなく気化器の連続使
用が可能となる。
The operator operates the valve 4,
By operating 5, 14, 15, 17, 18 to switch the hot gas flow path, it is possible to continuously use the carburetor without installing a new heat source or adding a heat exchanger even in winter or cold regions. Become.

【0021】以上において本実施例では、低温液体を2
つの熱交換器のいずれか一方に低温液体を流して大気と
熱交換させて気化させてホットガスとし、この低温液体
のホットガスを他方の熱交換器に流すことで他方の熱交
換器の除霜を行うことができ、新たな熱源を設けたり、
熱交換器を増設したりせずに冬季や寒冷地でも連続使用
できる気化器を実現することができる。
As described above, in this embodiment, the low temperature liquid is
One of the two heat exchangers is supplied with a cryogenic liquid and exchanges heat with the atmosphere to be vaporized into hot gas.The hot gas of the cryogenic liquid is passed through the other heat exchanger to remove the other heat exchanger. You can frost, provide a new heat source,
It is possible to realize a carburetor that can be continuously used even in the winter and cold regions without adding a heat exchanger.

【0022】尚、本実施例では各バルブの切替えを操作
者が行っているが、これに限定されるものではなく、バ
ルブに電磁弁を用いてマイクロコンピュータやタイマ等
によりホットガス流路を自動的に切替えるように構成し
てもよい。この場合、バルブの切替え作業は不要とな
る。又、本実施例では熱交換器が2台ずつ2列、計4台
の場合で説明したが、これに限定されるものではなく、
各列に1台ずつ設けられていても3台以上設けられてい
てもよい。さらに、本実施例ではバルブを全開または全
閉する場合で説明したが、これに限定されるものではな
く、熱交換器の容量や液体ガスの流量等に応じてバルブ
の開度を変えるようにしてもよい。
In this embodiment, the operator switches each valve, but the present invention is not limited to this. An electromagnetic valve is used for the valve to automatically control the hot gas flow path by a microcomputer or a timer. It may be configured to be switched selectively. In this case, valve switching work is unnecessary. Further, in the present embodiment, the case where the number of heat exchangers is 2 in 2 rows and 4 in total is explained, but the present invention is not limited to this.
One may be provided in each row, or three or more may be provided. Further, in the present embodiment, the case where the valve is fully opened or fully closed has been described, but the present invention is not limited to this, and the valve opening may be changed according to the capacity of the heat exchanger, the flow rate of the liquid gas, or the like. May be.

【0023】[0023]

【発明の効果】以上要するに本発明によれば、次のよう
な優れた効果を発揮する。
In summary, according to the present invention, the following excellent effects are exhibited.

【0024】(1) 冬季や寒冷地でも気化器の連続使用が
できる。
(1) The vaporizer can be continuously used even in winter or cold regions.

【0025】(2) 新たな熱源を用いたり、熱交換器を増
設したりせずに熱交換器の霜取りができる。
(2) The heat exchanger can be defrosted without using a new heat source or adding a heat exchanger.

【図面の簡単な説明】[Brief description of drawings]

【図1】本発明の気化器を説明するための説明図であ
る。
FIG. 1 is an explanatory diagram for explaining a vaporizer of the present invention.

【図2】従来の気化器を説明するための説明図である。FIG. 2 is an explanatory diagram for explaining a conventional vaporizer.

【符号の説明】[Explanation of symbols]

2 低温液体 4、5、14、15、17、18 流路切替手段(バル
ブ) 6、7、8、9 (空温式)熱交換器 11、12、13、16 ホットガス流路(分岐チュー
ブ)
2 Low-temperature liquid 4, 5, 14, 15, 17, 18 Flow path switching means (valve) 6, 7, 8, 9 (air temperature type) heat exchanger 11, 12, 13, 16 Hot gas flow path (branch tube) )

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 タンク内に貯蔵された低温液体を空温式
熱交換器に流して大気と熱交換させて気化する気化器に
おいて、2つの熱交換器を並列に接続すると共に、これ
らの熱交換器のいずれか一方に低温液体を流す流路切替
手段を設け、さらにそのいずれか一方の熱交換器を通っ
てホットガスとされた低温気体を他方の熱交換器に流し
て除霜を行うためのホットガス流路を設けたことを特徴
とする気化器。
1. A vaporizer in which a low temperature liquid stored in a tank is passed through an air-heat type heat exchanger to exchange heat with the atmosphere to vaporize, and two heat exchangers are connected in parallel and the heat of these heat exchangers is connected. A flow path switching means for flowing a low-temperature liquid is provided in either one of the exchangers, and the low-temperature gas that has been made into hot gas through one of the heat exchangers is flowed to the other heat exchanger to perform defrosting. A vaporizer characterized in that a hot gas flow path is provided for the vaporizer.
JP7690593A 1993-04-02 1993-04-02 Carburetor Pending JPH06294497A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7690593A JPH06294497A (en) 1993-04-02 1993-04-02 Carburetor

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7690593A JPH06294497A (en) 1993-04-02 1993-04-02 Carburetor

Publications (1)

Publication Number Publication Date
JPH06294497A true JPH06294497A (en) 1994-10-21

Family

ID=13618688

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7690593A Pending JPH06294497A (en) 1993-04-02 1993-04-02 Carburetor

Country Status (1)

Country Link
JP (1) JPH06294497A (en)

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002081598A (en) * 2000-09-08 2002-03-22 Tokyo Gas Co Ltd Method and device for manufacturing city gas
JP2006242274A (en) * 2005-03-03 2006-09-14 Osaka Gas Co Ltd Vaporization device and vaporization system
JP2007032600A (en) * 2005-07-22 2007-02-08 Osaka Gas Co Ltd Vaporizer system
KR100831946B1 (en) * 2007-02-13 2008-05-26 삼성중공업 주식회사 Liquefied natural gas regasification process and plant
KR100888339B1 (en) * 2007-07-25 2009-03-10 대우조선해양 주식회사 Method and system for treating fluid used in lng regasification on maine structure
JP2012519821A (en) * 2009-06-30 2012-08-30 ハムワージ・オイル・アンド・ガス・システムズ・アーエス Method and system for storing and transporting liquefied petroleum gas
KR20160067482A (en) * 2014-12-04 2016-06-14 한국가스공사 Vaporization Apparatus for Liquefied Natural Gas

Cited By (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002081598A (en) * 2000-09-08 2002-03-22 Tokyo Gas Co Ltd Method and device for manufacturing city gas
JP4668398B2 (en) * 2000-09-08 2011-04-13 東京瓦斯株式会社 Method and apparatus for producing city gas
JP2006242274A (en) * 2005-03-03 2006-09-14 Osaka Gas Co Ltd Vaporization device and vaporization system
JP2007032600A (en) * 2005-07-22 2007-02-08 Osaka Gas Co Ltd Vaporizer system
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