JP2000346339A - Liquiefied gas evaporating apparatus - Google Patents

Liquiefied gas evaporating apparatus

Info

Publication number
JP2000346339A
JP2000346339A JP16313399A JP16313399A JP2000346339A JP 2000346339 A JP2000346339 A JP 2000346339A JP 16313399 A JP16313399 A JP 16313399A JP 16313399 A JP16313399 A JP 16313399A JP 2000346339 A JP2000346339 A JP 2000346339A
Authority
JP
Japan
Prior art keywords
combustion
air
stopped
heat
post
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
JP16313399A
Other languages
Japanese (ja)
Inventor
Kazuhiro Oki
和広 大木
Toshiaki Ban
敏明 伴
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.)
Yazaki Corp
Original Assignee
Yazaki 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 Yazaki Corp filed Critical Yazaki Corp
Priority to JP16313399A priority Critical patent/JP2000346339A/en
Publication of JP2000346339A publication Critical patent/JP2000346339A/en
Pending legal-status Critical Current

Links

Landscapes

  • Filling Or Discharging Of Gas Storage Vessels (AREA)
  • Feeding And Controlling Fuel (AREA)

Abstract

PROBLEM TO BE SOLVED: To prevent a fault of an equipment due to a reverse flow of an atmosphere by providing a post-purging means for scavenging a combustion chamber by operating a blower for a predetermined time after a heating means is stopped. SOLUTION: When a temperature of a heating medium water W becomes higher than a set temperature of a warm water temperature sensor 23 during operating of the apparatus, a power source of the apparatus is turned OFF by a controller 19, and the apparatus is stopped. Simultaneously, when the operation is stopped, solenoid valves 16, 17 are closed, and a combustion is stopped. Thereafter, a blower 6 is continuously operated for a certain time (t), scavenged and then stopped. The scavenging of this time (t) is called 'post- purging'. An atmosphere is reversely fed from an air outlet of an exhaust cylinder 59 by the post-purging, introduced into a combustion chamber 52. Then, high-temperature air in the chamber 52 flows into an internal pressure container 9, thereby preventing a phenomenon of causing faults of the equipments 16, 17, 18 or the like to be controlled. The time (t) of the post-purging may be short e.g. about 20 s.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、例えば液化石油ガ
ス(LPガス)の液を熱媒液で加熱し蒸発させる液化ガ
ス蒸発装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a liquefied gas evaporator for heating a liquid liquefied petroleum gas (LP gas) with a heat carrier liquid to evaporate it.

【0002】[0002]

【従来の技術】図3に、従来技術に係る液化ガス蒸発装
置の概略構造図を示している。従来の液化ガス蒸発装置
60は、熱媒水wを加熱する熱源機61と、液化ガス、
たとえば液化石油ガスの液である液化石油液(LP液)
Lを熱媒水wで加熱し蒸発させてLPガスGpにするL
PG蒸発器74とを備えている。
2. Description of the Related Art FIG. 3 is a schematic structural view of a conventional liquefied gas evaporating apparatus. The conventional liquefied gas evaporator 60 includes a heat source device 61 for heating the heating medium water w, a liquefied gas,
For example, liquefied petroleum liquid (LP liquid) which is liquid of liquefied petroleum gas
L is heated with the heating medium water w to evaporate L into LP gas Gp
And a PG evaporator 74.

【0003】熱源機61は、燃焼用ガスGfを燃料とし
て、空気Gaと共に燃焼させて熱媒水wを加熱するもの
である。燃焼用ガスGfは、電磁弁62と調整器63を
介してバーナー65に供給される。バーナー65は、送
風機66によって燃焼用空気Gaが空気室67を介して
供給される。温水温度センサー69は、熱源機の本体6
1a内の熱媒水wの温度を検知し、その信号を熱源機制
御盤68に入力する。熱源機制御盤68は、熱媒水wの
温度信号を受けて電磁弁62、バーナー65および送風
機66を制御する。また、熱源機の本体61aには、空
焚きを防止する空焚き防止器71が設けられ、その信号
も熱源機制御盤68に入力される。
[0003] The heat source unit 61 uses the combustion gas Gf as a fuel and burns it together with the air Ga to heat the heating medium water w. The combustion gas Gf is supplied to the burner 65 via the solenoid valve 62 and the regulator 63. The combustion air Ga is supplied to the burner 65 through the air chamber 67 by the blower 66. The hot water temperature sensor 69 is connected to the main body 6 of the heat source device.
The temperature of the heat transfer water w in 1a is detected, and the signal is input to the heat source device control panel 68. The heat source device control panel 68 receives the temperature signal of the heating medium water w and controls the electromagnetic valve 62, the burner 65, and the blower 66. Further, the main body 61a of the heat source device is provided with an empty-fire prevention device 71 for preventing empty-heating, and its signal is also input to the heat-source device control panel 68.

【0004】LPG蒸発器74は、その蒸発器本体74
a内に熱交換器75を有し、熱交換器75の一方の端の
LP液入口76から流入するLP液Lは、温水循環ポン
プ72によって送られる熱媒水wの熱を受けて蒸発し、
熱交換器75の他方の端のLPガス出口77からLPガ
スGpとして流出する。熱交換器75で熱交換し温度の
低下した熱媒水wは、循環用温水配管73を通って熱源
機61側に戻されるようになっている。
The LPG evaporator 74 has an evaporator body 74.
a, the LP liquid L flowing from the LP liquid inlet 76 at one end of the heat exchanger 75 evaporates by receiving the heat of the heat transfer water w sent by the hot water circulation pump 72. ,
The gas flows out from the LP gas outlet 77 at the other end of the heat exchanger 75 as the LP gas Gp. The heat transfer water w whose temperature has been reduced by the heat exchange in the heat exchanger 75 is returned to the heat source device 61 through the circulation hot water pipe 73.

【0005】[0005]

【発明が解決しようとする課題】LPG蒸発器74の周
囲は、異常時にLPガスが滞留する恐れがあるので(破
線で示す危険場所58)、火気・電気の使用は制限を受
ける。
The use of fire and electricity is limited around the LPG evaporator 74 because LP gas may stay in an abnormal state (dangerous area 58 indicated by a broken line).

【0006】このため液化ガス蒸発装置60において
は、熱源機61をLPG蒸発器74から一定の距離をと
る必要がある(2点鎖線で示す非危険場所57)こと、
および熱媒水wの循環用温水配管73を熱源機61と蒸
発器74との間に設け、熱媒水wを常時温水循環ポンプ
72によって循環する必要があること等により、温水循
環ポンプ72の電気代が嵩み、かつ省スペース・省エネ
ルギー性にも欠けるという問題がある。
For this reason, in the liquefied gas evaporator 60, it is necessary to keep the heat source unit 61 at a certain distance from the LPG evaporator 74 (the non-dangerous area 57 shown by a two-dot chain line)
A hot water pipe 73 for circulating the heat medium water w is provided between the heat source unit 61 and the evaporator 74, and the heat medium water w must be constantly circulated by the hot water circulation pump 72. There is a problem that the electricity bill is large and the space and energy saving properties are lacking.

【0007】本出願人は、このような課題に対処し、少
ないスペースとエネルギーで効率良く安全に液化石油ガ
ス液を蒸発させることを可能にした液化ガス蒸発装置を
提案した(特願平10−279625号)。
The applicant of the present invention has proposed a liquefied gas evaporator which can efficiently and safely evaporate a liquefied petroleum gas liquid with a small space and energy in order to cope with such a problem (Japanese Patent Application No. Hei 10-1998). 279625).

【0008】本発明は、上記先願発明の改良の係わるも
のであって、特に、燃焼室のポストパージを行うことに
より、外気の逆流による機器の故障を防止した液化ガス
蒸発装置を提供することを目的とする。
The present invention relates to an improvement of the above-mentioned prior application, and in particular, to provide a liquefied gas evaporator in which a post-purge of a combustion chamber is performed to prevent equipment failure due to backflow of outside air. With the goal.

【0009】[0009]

【課題を解決するための手段】前記目的を達成するた
め、請求項1記載の発明は、燃料と空気を供給して燃焼
させる加熱手段と、該加熱手段に前記空気を供給する送
風機と、前記加熱手段を配置する燃焼室を有し該燃焼室
で発生する燃焼熱で加熱する熱媒液を保持する熱媒液槽
と、該熱媒液槽内に設けられ前記熱媒液の熱で液化ガス
液を蒸発させる熱交換手段と、前記燃料を制御する制御
機器が内部に設けられ前記空気を供給して大気圧を超え
る圧力に加圧可能な内圧容器と、該内圧容器に連通し前
記空気を溜めて前記加熱手段に供給する空気室と、を備
えた液化ガス蒸発装置であって、前記加熱手段の停止
後、前記送風機を所定の時間稼働させて前記燃焼室の掃
気を行うポストパージ手段を備えたことを特徴とするも
のである。
In order to achieve the above object, the invention according to claim 1 comprises a heating means for supplying fuel and air for combustion, a blower for supplying the air to the heating means, A heat medium liquid tank that has a combustion chamber in which a heating means is disposed and holds a heat medium liquid that is heated by combustion heat generated in the combustion chamber; A heat exchange means for evaporating the gas liquid, an internal pressure container provided with a control device for controlling the fuel therein and capable of supplying the air and pressurizing to a pressure exceeding atmospheric pressure, and communicating with the internal pressure container and the air A liquefied gas evaporator comprising: an air chamber for storing and supplying air to the heating means, wherein after the heating means is stopped, the blower is operated for a predetermined time to scavenge the combustion chamber. It is characterized by having.

【0010】このため、本発明では、排気筒からの逆流
が生じても内圧容器内が高温になることがなく、制御機
器の故障が防止されると共に、燃焼室内の湿度を下げ腐
食を防止する。
Therefore, in the present invention, even if a backflow from the exhaust stack occurs, the inside of the internal pressure vessel does not become hot, thereby preventing the failure of the control device and reducing the humidity in the combustion chamber to prevent corrosion. .

【0011】[0011]

【発明の実施の形態】以下、本発明の実施の形態を図面
に基づいて説明する。なお、図3と同一部材または同一
機能のものは同一符号で示している。
Embodiments of the present invention will be described below with reference to the drawings. The same members or those having the same functions as those in FIG. 3 are denoted by the same reference numerals.

【0012】図1は、本発明に係る液化ガス蒸発装置の
一実施形態を示す概略構造図である。本実施形態の液化
ガス蒸発装置1は、燃料である燃焼用ガスGfと燃焼用
空気Gaを供給して燃焼させる加熱手段としてのバーナ
ー12と、このバーナー12に燃焼用空気Gaを供給す
る空気供給手段としての防爆型の送風機6および吸い込
み管7とを備える。
FIG. 1 is a schematic structural view showing one embodiment of a liquefied gas evaporator according to the present invention. The liquefied gas evaporator 1 of the present embodiment includes a burner 12 as a heating unit for supplying and burning the combustion gas Gf and the combustion air Ga as a fuel, and an air supply for supplying the combustion air Ga to the burner 12. An explosion-proof blower 6 and a suction pipe 7 are provided as means.

【0013】さらに、バーナー12を配置する燃焼室5
2を有し、この燃焼室52で発生する燃焼熱で加熱する
熱媒水(熱媒液)wを保持する温水槽(熱媒液槽)51
と、この温水槽51内に設けられ熱媒水wの熱でLP液
Lを蒸発させる熱交換手段である熱交換器53とを備え
る。この熱交換器53では、一方の端のLP液入口54
から流入するLP液Lは、熱媒水wの熱を受けて蒸発
し、他方の端のLPガス出口55からLPガスGpとし
て流出する。
Further, the combustion chamber 5 in which the burner 12 is disposed
A hot water tank (heat medium liquid tank) 51 for holding a heat medium water (heat medium liquid) w heated by combustion heat generated in the combustion chamber 52
And a heat exchanger 53 which is provided in the hot water tank 51 and is a heat exchange means for evaporating the LP liquid L by the heat of the heat medium water w. In this heat exchanger 53, the LP liquid inlet 54 at one end
The LP liquid L flowing in from the evaporator receives the heat of the heat medium water w, evaporates, and flows out as the LP gas Gp from the LP gas outlet 55 at the other end.

【0014】送風機6の出口側に内圧容器9が連接さ
れ、この内圧容器9に空気室11が連接され、内圧容器
9から空気室11に供給される空気は、燃焼用空気とし
てバーナー12に供給される。
An internal pressure vessel 9 is connected to the outlet side of the blower 6, an air chamber 11 is connected to the internal pressure vessel 9, and air supplied from the internal pressure vessel 9 to the air chamber 11 is supplied to the burner 12 as combustion air. Is done.

【0015】ここで、送風機6の吸い込み管7の吸い込
み口8は、非危険場所57に開口し、ここから燃焼用空
気Gaを導入する。また、燃焼用ガスGfは、吸い込み
管15を介して導入される。このバーナー12に供給さ
れる燃焼用ガスGfと燃焼用空気Gaとを燃焼室52に
噴射し燃焼させ、発生する燃焼排気ガスGgは排気筒5
9を通って上方に排出される。
Here, the suction port 8 of the suction pipe 7 of the blower 6 opens to a non-dangerous area 57, from which combustion air Ga is introduced. Further, the combustion gas Gf is introduced through the suction pipe 15. The combustion gas Gf and the combustion air Ga supplied to the burner 12 are injected into the combustion chamber 52 and burned, and the generated combustion exhaust gas Gg is discharged from the exhaust pipe 5.
It is discharged upward through 9.

【0016】前記排気筒59が、非危険場所60まで配
管されている。これにより、燃焼排気ガスGgが、非危
険場所60に放出され、危険場所58に放出されるのが
防止される。必要に応じて排気筒59の表面に断熱材を
施してもよい。なお、上記非危険場所57,60は、液
化ガス蒸発装置1から水平距離で8m以上離れるか、あ
るいは地盤から3m以上高い場所が一般的であるが、こ
の位置に限定するものではない。
The exhaust pipe 59 is connected to the non-dangerous area 60 by piping. Thereby, the combustion exhaust gas Gg is released to the non-dangerous place 60 and is prevented from being released to the dangerous place 58. A heat insulating material may be provided on the surface of the exhaust pipe 59 as needed. The non-dangerous locations 57 and 60 are generally located at a distance of 8 m or more horizontally from the liquefied gas evaporator 1 or at a height of 3 m or more from the ground, but are not limited to these positions.

【0017】内圧容器9内の内部9aには、燃焼用ガス
Gfを制御する制御機器である電磁弁16、17および
調整器18が設けられている。この内圧容器9は、燃焼
用空気Gaを供給して大気圧を超える圧力に加圧可能で
ある。さらに、内圧容器9の圧力が大気圧を超えたこと
を確認して、電磁弁16、17およびバーナー12に通
電を開始し、バーナー12に燃焼を行わせる制御装置1
9を備える。
In the interior 9a of the internal pressure vessel 9, there are provided solenoid valves 16, 17 and a regulator 18, which are control devices for controlling the combustion gas Gf. The internal pressure container 9 is capable of supplying combustion air Ga to be pressurized to a pressure exceeding atmospheric pressure. Further, after confirming that the pressure of the internal pressure vessel 9 has exceeded the atmospheric pressure, the control device 1 that starts energizing the solenoid valves 16 and 17 and the burner 12 and causes the burner 12 to perform combustion.
9 is provided.

【0018】前記制御装置19は、送風機制御盤28
と、温水温度センサー23および過熱防止装置31と、
圧力スイッチ20とを有する。そして、制御装置19
は、上記のように、内圧容器9内の圧力が大気圧を超え
たことを確認し、さらに好ましくは予め決められた一定
時間経過後に前記制御機器16,17,18およびバー
ナー12に通電を開始し、バーナー12に燃焼を行わせ
る。送風機6、温水温度センサー23、過熱防止装置3
1、圧力スイッチ20、及び送風機制御盤28などは防
爆型とする。
The control device 19 includes a blower control panel 28
Hot water temperature sensor 23 and overheat prevention device 31,
And a pressure switch 20. And the control device 19
Confirms that the pressure in the internal pressure vessel 9 has exceeded the atmospheric pressure as described above, and more preferably starts energizing the control devices 16, 17, 18 and the burner 12 after a predetermined period of time has elapsed. Then, the burner 12 burns. Blower 6, hot water temperature sensor 23, overheat prevention device 3
1, the pressure switch 20, the blower control panel 28, etc. are of explosion-proof type.

【0019】熱媒水wの温度が低く、バーナー12の燃
焼が要求されると、送風機6は、吸い込み管7を介して
非危険場所57から燃焼用空気Gaを内圧容器9に圧送
する。内圧容器9は、空気室11と連通されるので、送
風機6から圧送される燃焼用空気Gaは、バーナーの燃
焼室52に流入する。この時、内圧容器9の内部9aの
圧力が大気圧十△P(大気圧を超える圧力)以上で、先
に記した一定時間保持されたことが確認されれば、バー
ナー12に点火され、燃焼が開始される。
When the temperature of the heat medium water w is low and the combustion of the burner 12 is required, the blower 6 sends the combustion air Ga from the non-dangerous place 57 to the internal pressure container 9 through the suction pipe 7. Since the internal pressure container 9 is communicated with the air chamber 11, the combustion air Ga pressure-fed from the blower 6 flows into the combustion chamber 52 of the burner. At this time, if it is confirmed that the pressure in the inner portion 9a of the internal pressure container 9 is equal to or higher than the atmospheric pressure of 10 △ P (pressure exceeding the atmospheric pressure) and is maintained for the above-described predetermined time, the burner 12 is ignited and the combustion is performed. Is started.

【0020】内圧容器9の内部9aは、大気圧を超える
圧力であるので、万一LPガスが内圧容器9や温水槽5
1の周囲に滞留していても内圧容器9内にLPガスが流
入することはない。なお、制御機器の電気部品は防爆配
線(符号26の各黒印)される。
Since the interior 9a of the internal pressure vessel 9 is at a pressure exceeding the atmospheric pressure, the LP gas should be supplied to the internal pressure vessel 9 or the hot water tank 5 by any chance.
The LP gas does not flow into the internal pressure container 9 even if it stays around the periphery of the pressure vessel 1. The electrical components of the control device are explosion-proof wiring (each black mark 26).

【0021】何らかの原因によって、内圧容器9内にL
Pガスが侵入しても、非危険場所57から導入される清
浄な燃焼用空気Gaによって掃気されてから内圧容器9
内の制御機器16、17、18に通電が開始され、バー
ナー12への着火が行われるため危険性はない。
For some reason, L
Even if the P gas enters, it is scavenged by clean combustion air Ga introduced from the non-hazardous area 57 and then the internal pressure vessel 9
There is no danger because the power supply to the control devices 16, 17, and 18 is started and the burner 12 is ignited.

【0022】つぎに、図2に基づいて作動の要点を説明
する。
Next, the essential points of the operation will be described with reference to FIG.

【0023】先ず、装置の電源を投入し、運転を開始す
ると、少し遅れて内圧容器9内の圧力が上昇して圧力ス
イッチ20がONし、送風機6は、電源投入と同時にO
Nして燃焼用空気Gaの供給を開始し、電磁弁16、1
7が開になると燃焼用ガスGfがバーナー12に送ら
れ、着火により燃焼を開始する。
First, when the power of the apparatus is turned on and the operation is started, the pressure in the internal pressure container 9 is increased with a slight delay, the pressure switch 20 is turned on, and the blower 6 is turned on at the same time as the power is turned on.
N, the supply of the combustion air Ga is started, and the solenoid valves 16 and 1 are started.
When 7 is opened, the combustion gas Gf is sent to the burner 12, and the combustion starts by ignition.

【0024】装置の運転中に熱媒水wの温度が、温水温
度センサー23の設定温度より高くなると、制御装置1
9により装置の電源をOFFとし、装置の運転が停止す
る。運転停止と同時に電磁弁16、17は、閉となり、
燃焼は止まるが、その後も送風機6は、ある時間tだけ
運転を継続し、掃気を行った後停止するようにしている
(この時間tの掃気をポストパージと称する)。
If the temperature of the heat transfer water w becomes higher than the temperature set by the hot water temperature sensor 23 during the operation of the apparatus, the controller 1
The power of the apparatus is turned off by 9 and the operation of the apparatus is stopped. At the same time as the operation is stopped, the solenoid valves 16 and 17 are closed,
Although the combustion stops, the blower 6 continues to operate for a certain time t and stops after scavenging (this scavenging at time t is called post-purge).

【0025】燃焼が停止した後、そのまま放置すると、
排気筒59の吹き出し口59aから外気が逆流して燃焼
室52に入り、燃焼室52内の高温の空気が内圧容器9
内に流れ込み、制御機器16、17、18等の故障の原
因となる。上記ポストパージにより燃焼室52の余熱を
冷ますことにより、このような現象を防止できる。この
ポストパージの時間tは、20秒程度の短時間でよい。
このようなポストパージの動作及び時間設定は制御装置
19により行うことができる。
After the combustion has stopped, if left as it is,
The outside air flows backward from the outlet 59 a of the exhaust pipe 59 into the combustion chamber 52, and the high-temperature air in the combustion chamber 52 flows into the internal pressure vessel 9.
And cause a failure of the control devices 16, 17, 18 and the like. By cooling the residual heat of the combustion chamber 52 by the post-purge, such a phenomenon can be prevented. The post-purge time t may be as short as about 20 seconds.
Such a post-purge operation and time setting can be performed by the control device 19.

【0026】以上のように、本実施の形態の液化ガス蒸
発装置1では、バーナー12での燃焼停止後、送風機6
を所定の時間稼働させてポストパージを行って燃焼停止
直後の燃焼室52を冷却するようにしたので、排気筒5
9からの逆流が生じても内圧容器9内が高温になること
がなく、また、燃焼室52内に結露が生じてもポストパ
ージで燃焼室52の湿度をも下げるため、燃焼室52内
の腐食も防止できる。
As described above, in the liquefied gas evaporator 1 of the present embodiment, after the combustion in the burner 12 is stopped, the blower 6
Is operated for a predetermined time to perform post-purge to cool the combustion chamber 52 immediately after the combustion is stopped.
Even if the backflow from 9 occurs, the inside of the internal pressure vessel 9 does not become hot, and even if dew condensation occurs in the combustion chamber 52, the humidity of the combustion chamber 52 is also reduced by post-purge. Corrosion can also be prevented.

【0027】さらに、ポストパージを行うことにより、
次の燃焼要求があった場合、プレパージ(燃焼室52を
予め掃気しておくこと)の時間が短縮され、運転停止時
間がそれだけ短縮されるため、熱媒水wの温度調節の追
従性が向上する。
Further, by performing post-purging,
When the next combustion request is made, the pre-purge time (preliminary scavenging of the combustion chamber 52) is shortened, and the operation stop time is shortened accordingly, so that the follow-up of the temperature control of the heat transfer water w is improved. I do.

【0028】[0028]

【発明の効果】以上、詳述したように、本発明によれ
ば、燃焼停止後送風機を所定の時間稼働させてポストパ
ージを行うようにしたので、燃焼停止直後の燃焼室が冷
却され、排気筒からの逆流が生じても内圧容器内が高温
になることがなく、制御機器の故障が防止されると共
に、燃焼室の湿度を下げるため、燃焼室内の腐食も防止
できる。
As described above in detail, according to the present invention, after the combustion is stopped, the blower is operated for a predetermined time to perform the post-purge, so that the combustion chamber immediately after the stop of the combustion is cooled and the exhaust gas is discharged. Even if the backflow from the cylinder occurs, the inside of the internal pressure vessel does not become high temperature, and the failure of the control device is prevented, and the humidity in the combustion chamber is reduced, so that the corrosion in the combustion chamber can be prevented.

【0029】また、本発明によれば、燃焼停止後次の燃
焼要求があった場合、プレパージの時間が短縮され、運
転停止時間がそれだけ短縮されるため、熱媒水の温度調
節の追従性が向上する。
Further, according to the present invention, when the next combustion request is made after the stop of the combustion, the pre-purge time is shortened and the operation stop time is shortened accordingly, so that the followability of the temperature control of the heat transfer water is improved. improves.

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

【図1】本発明に係る液化ガス蒸発装置の実施の形態を
示す概略構造図である。
FIG. 1 is a schematic structural view showing an embodiment of a liquefied gas evaporator according to the present invention.

【図2】本発明の制御動作の説明図である。FIG. 2 is an explanatory diagram of a control operation according to the present invention.

【図3】従来技術に係る液化ガス蒸発装置の概略構造図
である。
FIG. 3 is a schematic structural view of a liquefied gas evaporator according to the related art.

【符号の説明】[Explanation of symbols]

1 液化ガス蒸発装置 6 送風機 9 内圧容器 11 空気室 12 バーナー(加熱手段) 16、17 電磁弁(制御機器) 18 調整器(制御機器) 19 制御装置(ポストパージ手段) 51 熱媒液槽 52 燃焼室 53 熱交換器(熱交換手段) w 熱媒水(熱媒液) REFERENCE SIGNS LIST 1 liquefied gas evaporator 6 blower 9 internal pressure vessel 11 air chamber 12 burner (heating means) 16, 17 solenoid valve (control device) 18 regulator (control device) 19 controller (postpurge means) 51 heating medium liquid tank 52 combustion Room 53 Heat exchanger (heat exchange means) w Heat medium water (heat medium liquid)

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 燃料と空気を供給して燃焼させる加熱手
段と、該加熱手段に前記空気を供給する送風機と、前記
加熱手段を配置する燃焼室を有し該燃焼室で発生する燃
焼熱で加熱する熱媒液を保持する熱媒液槽と、該熱媒液
槽内に設けられ前記熱媒液の熱で液化ガス液を蒸発させ
る熱交換手段と、前記燃料を制御する制御機器が内部に
設けられ前記空気を供給して大気圧を超える圧力に加圧
可能な内圧容器と、該内圧容器に連通し前記空気を溜め
て前記加熱手段に供給する空気室と、を備えた液化ガス
蒸発装置であって、 前記加熱手段の停止後、前記送風機を所定の時間稼働さ
せて前記燃焼室の掃気を行うポストパージ手段を備えた
ことを特徴とする液化ガス蒸発装置。
1. A heating means for supplying and burning fuel and air, a blower for supplying the air to the heating means, and a combustion chamber in which the heating means is disposed, wherein a combustion heat generated in the combustion chamber is used. A heat medium liquid tank for holding a heat medium liquid to be heated, heat exchange means provided in the heat medium liquid tank for evaporating a liquefied gas liquid by heat of the heat medium liquid, and a control device for controlling the fuel are internally provided. A liquefied gas evaporator, comprising: an internal pressure vessel provided at a pressure chamber capable of supplying the air to pressurize to a pressure exceeding atmospheric pressure; and an air chamber communicating with the internal pressure vessel and storing the air and supplying the air to the heating means. A liquefied gas evaporator, comprising: a post-purge unit for operating the blower for a predetermined time after the heating unit is stopped to scavenge the combustion chamber.
JP16313399A 1999-06-09 1999-06-09 Liquiefied gas evaporating apparatus Pending JP2000346339A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP16313399A JP2000346339A (en) 1999-06-09 1999-06-09 Liquiefied gas evaporating apparatus

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP16313399A JP2000346339A (en) 1999-06-09 1999-06-09 Liquiefied gas evaporating apparatus

Publications (1)

Publication Number Publication Date
JP2000346339A true JP2000346339A (en) 2000-12-15

Family

ID=15767832

Family Applications (1)

Application Number Title Priority Date Filing Date
JP16313399A Pending JP2000346339A (en) 1999-06-09 1999-06-09 Liquiefied gas evaporating apparatus

Country Status (1)

Country Link
JP (1) JP2000346339A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103629693A (en) * 2013-12-02 2014-03-12 北京市燃气集团有限责任公司 Control system and control method of LNG immersion combustion gasifier

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103629693A (en) * 2013-12-02 2014-03-12 北京市燃气集团有限责任公司 Control system and control method of LNG immersion combustion gasifier

Similar Documents

Publication Publication Date Title
JPS6246708A (en) Controller for quick heater
US20090107128A1 (en) Cogeneration system
US8276548B2 (en) Low cost tankless portable water heater
JP3931619B2 (en) Combustion device control method
JP2000346339A (en) Liquiefied gas evaporating apparatus
JP3505639B2 (en) Liquefied gas evaporator and operating method thereof
JP2000346291A (en) Liquefied gas evaporator device
JP2001116197A (en) Liquefied gas vaporizing device
JP2001116194A (en) Liquefied gas vaporizing device
JP2011117680A (en) Storage type water heater
JP2001012692A (en) Liquefied gas evaporating device
JPH07190484A (en) Hot water supplying apparatus
JP2001116195A (en) Liquefied gas vaporizing device
JP2001116196A (en) Liquefied gas vaporizing device
JPS6112515Y2 (en)
KR20000004189A (en) Overheating prevention method of gas boiler
FI72194B (en) ANORDINATION FOR STYLING AV EN SPJAELLREGULATOR VID VAERMEPANNOR
JP2004514864A (en) Overpressure combustor for burning lean concentration of combustible gas
JP2820892B2 (en) Combustion equipment
JP2589208Y2 (en) Burner for high pressure spray combustion device
KR0157000B1 (en) Method of protecting instruments accompanied with efficient post-purge performance
CN117781478A (en) Forced-ventilated gas water heater
KR20220099051A (en) System for prevention of heat loss through air jacket
KR100284940B1 (en) Freezing Control Method of Gas Boiler
SU1460361A1 (en) Method of relieving a central heating/power plant