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JP6386314B2 - Vaporizing oil water heater - Google Patents

Vaporizing oil water heater Download PDF

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JP6386314B2
JP6386314B2 JP2014189694A JP2014189694A JP6386314B2 JP 6386314 B2 JP6386314 B2 JP 6386314B2 JP 2014189694 A JP2014189694 A JP 2014189694A JP 2014189694 A JP2014189694 A JP 2014189694A JP 6386314 B2 JP6386314 B2 JP 6386314B2
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temperature
water supply
hot water
heater
combustion
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JP2016061486A (en
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聡 古舘
聡 古舘
丸山 寛也
寛也 丸山
寿英 鈴木
寿英 鈴木
竹年 田村
竹年 田村
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Corona Corp
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Description

この発明は、気化式石油給湯装置の凍結防止に関するものである。   The present invention relates to prevention of freezing of a vaporization type oil hot water supply apparatus.

従来よりこの種の気化式石油給湯装置では、バーナに設けられている燃油を気化する加熱用ヒータを利用して、水流路である配管や熱交換器の凍結防止時に、通電させることで加熱用ヒータの熱でこれらの凍結を防止しようとしたものがあった(例えば、特許文献1参照。)。   Conventionally, this type of vaporized petroleum hot water supply system uses a heater for vaporizing the fuel oil provided in the burner to energize the pipes and heat exchangers that are water flow paths to prevent freezing. There was one that tried to prevent such freezing by the heat of the heater (see, for example, Patent Document 1).

特許第3606937号公報Japanese Patent No. 3606937

ところで、この気化式石油給湯装置では、外気温度に関係なく確実に凍結防止をする為に、加熱用ヒータの制御温度は最高値である220℃近くを維持するように制御しているが、外気温がそれ程低くない時は、これ程高い温度は必要なく、電力が無駄で経済的ではないと言う課題を有するものであった。   By the way, in this vaporization type oil hot water supply apparatus, in order to prevent freeze-up reliably regardless of the outside air temperature, the control temperature of the heater for heating is controlled so as to maintain a maximum value of around 220 ° C. When the temperature is not so low, such a high temperature is not necessary, and there is a problem that electric power is useless and not economical.

この発明は、上記課題を解決する為に、特にその構成を、加熱用ヒータを備え燃油を気化させる気化部と、この気化部の温度を検出する気化温度センサと、前記気化部で気化させた燃油を燃焼させる燃焼部とで構成されるバーナと、このバーナに燃焼空気を供給する燃焼ファンと、該バーナの燃焼により発生した燃焼ガスから顕熱を回収し一次受熱管を流通する水を加熱する一次熱交換器と、凍結防止の所定温度を検出する温度検出手段と、前記気化温度センサが検出する温度が所定の制御温度範囲になるように前記加熱用ヒータを制御する制御手段と、を備え、前記バーナの上方に前記一次熱交換器を配置した気化式石油給湯装置であって、該気化式石油給湯装置を遠隔操作するリモコンの運転スイッチがオフされ、前記気化式石油給湯装置の運転が停止している時に、前記温度検出手段が前記凍結防止の所定温度を検出した場合は、前記制御手段は、前記加熱用ヒータをオンして凍結防止運転すると共に、この凍結防止運転時の前記所定の制御温度範囲を前記温度検出手段の検出温度が低くなる程高くなるようにして前記加熱用ヒータを制御するようにしたものである。 In order to solve the above-described problems, the present invention is particularly vaporized by a vaporization section that includes a heater and vaporizes fuel, a vaporization temperature sensor that detects the temperature of the vaporization section, and the vaporization section. A burner composed of a combustion section for burning fuel oil, a combustion fan for supplying combustion air to the burner, and recovering sensible heat from the combustion gas generated by the combustion of the burner and heating water flowing through the primary heat receiving pipe a primary heat exchanger for a temperature detection means for detecting a predetermined temperature of freezing prevention, control means for the temperature which the vaporization temperature sensor is detected to control the heater to a predetermined control temperature range, the An evaporative oil hot water supply device in which the primary heat exchanger is disposed above the burner, wherein a remote control operation switch for remotely operating the evaporative oil hot water device is turned off, and the evaporative oil hot water supply device If the temperature detecting means detects the predetermined temperature for preventing freezing when the operation is stopped, the control means performs the antifreezing operation by turning on the heating heater, and at the time of the antifreezing operation. The heater is controlled such that the predetermined control temperature range becomes higher as the detected temperature of the temperature detecting means becomes lower.

この発明によれば、凍結防止専用のヒータを用意することなく、燃油気化用の加熱用ヒータを利用して凍結防止を行うので、特別な部品が必要なく安価で済むものであり、又この凍結防止運転時の加熱用ヒータの制御温度は、外気温が低くなる程高くなるように可変されるので、電力消費の無駄がなく経済的でありながら確実に凍結を防止することが出来るものである。   According to the present invention, since the anti-freezing is performed by using the heater for vaporizing the fuel without preparing a dedicated anti-freezing heater, no special parts are required and the cost can be reduced. Since the control temperature of the heating heater during the prevention operation is varied so as to increase as the outside air temperature decreases, the power consumption is not wasted and it is possible to reliably prevent freezing while being economical. .

この発明の一実施形態の気化式石油給湯装置を示す概略構成図。The schematic block diagram which shows the vaporization type petroleum hot water supply apparatus of one Embodiment of this invention. 同凍結防止運転のフローチャート。The flowchart of the freezing prevention operation.

次に、この発明の一実施形態の給湯装置を図1に基づき説明する。
1は本実施形態の潜熱回収型の気化式石油給湯装置、2は石油等の燃油を気化するアルミダイキャスト製の気化器で、気化器2底部には気化ガスの流出口3を有しているものである。4は気化器2に備えられ燃油を気化可能な温度まで加熱する加熱用ヒータとしての気化器ヒータ、5は気化器2下部で流出口3と連通し気化器2で気化された気化ガスと一次空気とを予混合するアルミダイキャスト製の混合室、6は混合室5底部に設けられ混合室5を加熱して流出口3から流入してくる気化ガスの液化を防止し気化を促進する加熱用ヒータとしての混合室ヒータで、上述した気化器2と混合室5とで燃油を気化させる気化部7を形成するものである。
Next, a hot water supply apparatus according to an embodiment of the present invention will be described with reference to FIG.
Reference numeral 1 denotes a latent heat recovery type vaporized petroleum water heater of the present embodiment, 2 denotes an aluminum die-cast vaporizer that vaporizes fuel such as oil, and has a vaporized gas outlet 3 at the bottom of the vaporizer 2. It is what. 4 is a vaporizer heater provided as a heater for heating the fuel oil to a temperature at which the fuel oil can be vaporized. An aluminum die-cast mixing chamber 6 for premixing with air is provided at the bottom of the mixing chamber 5 to heat the mixing chamber 5 and prevent liquefaction of the vaporized gas flowing in from the outlet 3 to promote vaporization. A vaporizing section 7 for vaporizing fuel oil is formed by the vaporizer 2 and the mixing chamber 5 described above.

8は気化器2の温度を検出する気化温度センサ、9は混合室5の温度を検出する混合室温度センサ、10は混合室5上部で気化器2の背面側に備えられ、混合室5で予混合された予混合ガスを燃焼させる燃焼部で、この燃焼部10と気化部7とでバーナ11を構成するものである。また、12は気化器2と一体的に形成され、気化器2背面で燃焼部10上に突出した複数個の吸熱フィンで、燃焼時には燃焼熱を気化熱として気化器2にフィードバックして、気化器ヒータ4の通電量を極力抑えるものである。   8 is a vaporizing temperature sensor for detecting the temperature of the vaporizer 2, 9 is a mixing chamber temperature sensor for detecting the temperature of the mixing chamber 5, and 10 is provided on the back side of the vaporizer 2 above the mixing chamber 5. In the combustion section that burns the premixed premixed gas, the combustion section 10 and the vaporization section 7 constitute a burner 11. Reference numeral 12 denotes a plurality of heat-absorbing fins formed integrally with the carburetor 2 and projecting from the back of the carburetor 2 onto the combustion unit 10. During combustion, the combustion heat is fed back to the carburetor 2 as vaporization heat and vaporized. The energization amount of the heater 4 is suppressed as much as possible.

13は気化器2に燃油を噴霧するノズル、14はノズル13に送油管15を介して燃油を圧送する電磁ポンプ、16は燃焼ファンで、送風路17を介して気化器2の入口および燃焼部10とカバー枠18との間の空気室19とに連通し、吸込口20より吸引した燃焼空気を、気化器2には予混合用の一次空気として供給し、空気室19には気化器2側方を通り混合室5の下方から燃焼部10で燃焼される二次空気として供給するものである。   13 is a nozzle for spraying fuel oil on the vaporizer 2, 14 is an electromagnetic pump for pumping fuel oil to the nozzle 13 via an oil feed pipe 15, 16 is a combustion fan, and an inlet and a combustion section of the vaporizer 2 via an air passage 17. Combustion air that is communicated with the air chamber 19 between the cover 10 and the cover frame 18 and sucked from the suction port 20 is supplied to the carburetor 2 as primary air for premixing, and the carburetor 2 is supplied to the air chamber 19. It is supplied as secondary air that passes through the side and is combusted in the combustion section 10 from below the mixing chamber 5.

21は燃焼室22内に収容された熱交換器で、この熱交換器21は、燃焼部10の燃焼により発生した燃焼ガスから顕熱を回収し一次受熱管23を流通する水を加熱するフィンチューブ式の一次熱交換器24と、一次熱交換器24を通過した後の燃焼ガスから潜熱を回収し二次受熱管25を流通する水を加熱する二次熱交換器26とから構成され、燃焼部10の上方に一次熱交換器24が配置され、一次熱交換器24の上方に二次熱交換器26が配置されているものであり、一次熱交換器24、二次熱交換器26の順に通過した燃焼ガスは排気口27より給湯装置1外に排気されるものである。   21 is a heat exchanger accommodated in the combustion chamber 22, and this heat exchanger 21 is a fin for recovering sensible heat from the combustion gas generated by the combustion of the combustion section 10 and heating the water flowing through the primary heat receiving pipe 23. A tube-type primary heat exchanger 24 and a secondary heat exchanger 26 that recovers latent heat from the combustion gas after passing through the primary heat exchanger 24 and heats the water flowing through the secondary heat receiving pipe 25; A primary heat exchanger 24 is disposed above the combustion unit 10, and a secondary heat exchanger 26 is disposed above the primary heat exchanger 24. The primary heat exchanger 24 and the secondary heat exchanger 26 are disposed. The combustion gas that has passed through in this order is exhausted out of the hot water supply device 1 through the exhaust port 27.

28は燃焼ガス中の水蒸気が二次熱交換器26の二次受熱管25を流通する水と熱交換して露点以下の温度となることにより生成されるドレンを回収するドレン受けで、ドレン受け28は、一次熱交換器24の上方且つ二次熱交換器26の下方に配置されているものであり、ここでは、二次熱交換器26を構成する耐食性を有する筐体(図示せず)の底板がドレン受け28となっているものである。また、29はドレン受け28で回収されたドレンを中和装置30に導くドレン配管である。   Reference numeral 28 denotes a drain receiver that recovers drain that is generated when the water vapor in the combustion gas exchanges heat with the water flowing through the secondary heat receiving pipe 25 of the secondary heat exchanger 26 to reach a temperature below the dew point. 28 is disposed above the primary heat exchanger 24 and below the secondary heat exchanger 26, and here, a corrosion-resistant housing (not shown) constituting the secondary heat exchanger 26. The bottom plate is a drain receiver 28. A drain pipe 29 guides the drain collected by the drain receiver 28 to the neutralizer 30.

31は給水源から供給される水を熱交換器21に流通させる給水管、32は熱交換器21で加熱された湯を流通させ、所定箇所に設けられた給湯栓(図示せず)に湯を供給する給湯管、33は給水管31から分岐した給水バイパス管であり、一次受熱管23と二次受熱管25と給水管31と給湯管32と給水バイパス管33とで水が流通する給湯回路を構成するものである。   31 is a water supply pipe for circulating water supplied from a water supply source to the heat exchanger 21, 32 is for circulating hot water heated by the heat exchanger 21, and hot water is supplied to a hot water tap (not shown) provided at a predetermined location. A hot water supply pipe 33, which is a water supply bypass pipe branched from the water supply pipe 31, has a primary heat receiving pipe 23, a secondary heat receiving pipe 25, a water supply pipe 31, a hot water supply pipe 32, and a water supply bypass pipe 33. It constitutes a circuit.

34は給湯管32と給水バイパス管33との接続部に設けられ、給湯管32からの湯と給水バイパス管33からの水とを混合し、その混合比を可変できる混合弁、35は給水管31に設けられ給水温度を検出する温度検出手段としての給水温度センサ、36は給水管31に設けられ流量を検出する流量センサ、37は給湯管32に設けられ熱交換器21で加熱された湯の温度を検出する温度検出手段としての熱交出口温度センサで、運転停止時には凍結防止の所定温度を検出するものであり、38は給湯管32に設けられ混合弁34で混合された湯の温度を検出する温度検出手段としての給湯温度センサであり、39は燃焼ファン16の吸引口20近傍に備えられ燃焼空気温度を検出する空気サーミスタである。   A mixing valve 34 is provided at a connection portion between the hot water supply pipe 32 and the water supply bypass pipe 33, mixes hot water from the hot water supply pipe 32 and water from the water supply bypass pipe 33, and can change the mixing ratio. A water supply temperature sensor provided as a temperature detecting means for detecting a water supply temperature provided at 31, a flow sensor for detecting a flow rate provided at a water supply pipe 31, and a hot water provided at a hot water supply pipe 32 and heated by the heat exchanger 21. A heat exchange outlet temperature sensor as a temperature detecting means for detecting the temperature of the hot water, which detects a predetermined temperature for preventing freezing when the operation is stopped, and 38 is a temperature of hot water provided in the hot water supply pipe 32 and mixed by the mixing valve 34. Is a hot water supply temperature sensor as temperature detecting means for detecting the air temperature, and 39 is an air thermistor provided near the suction port 20 of the combustion fan 16 for detecting the combustion air temperature.

40はマイクロコンピュータを主体として、この潜熱回収型気化式石油給湯装置1の各センサの信号を受け、気化器ヒータ4や混合室ヒータ6や燃焼ファン16等の各アクチュエータの駆動を制御する制御手段であり、給湯装置1の運転停止状態で外気温度が下がり凍結防止の所定温度を温度検出手段37が検出するとこの制御手段40が判断して、加熱用ヒータ4、6を通電させて発生した熱気を自然対流させ、配管や熱交換器21の凍結を防止するものであり、また、制御手段40は温度検出手段37が検出する凍結防止の所定温度が低くなる程、加熱用ヒータ4、6の制御温度を高くするものであり、具体的には、温度検出手段37が−5℃を検出すると気化温度センサ8によって加熱用ヒータ4、6の制御温度を130℃〜140℃に制御し、外気温度が更に下がり−10℃に達すると170℃〜180℃に制御し、−3℃で元の制御温度に戻るもので、更に下がり−20℃に達すると220℃〜225℃に制御し、−8℃で元の制御温度に戻るもので、無駄な電力消費をなくし効率が良くしかも確実に凍結防止が行われるようにしたものであり、外気温度が3℃になるとこの凍結防止運転は一旦停止されるものである。   40 is a control means for controlling the driving of the actuators such as the vaporizer heater 4, the mixing chamber heater 6, and the combustion fan 16 by receiving signals from the sensors of the latent heat recovery type vaporized petroleum hot water supply apparatus 1 mainly using a microcomputer. When the temperature detection means 37 detects that the outside air temperature has dropped and the predetermined temperature for preventing freezing is detected when the hot water supply device 1 is stopped, the control means 40 determines that the hot air generated by energizing the heaters 4 and 6 is generated. The control means 40 prevents the freezing of the heating heaters 4 and 6 as the temperature of the anti-freezing detected by the temperature detecting means 37 decreases. The control temperature is raised. Specifically, when the temperature detecting means 37 detects −5 ° C., the control temperature of the heating heaters 4 and 6 is set to 130 ° C. to 140 ° C. by the vaporization temperature sensor 8. When the outside air temperature further decreases to reach −10 ° C., the temperature is controlled to 170 ° C. to 180 ° C., and returns to the original control temperature at −3 ° C., and further decreases to −20 ° C. to reach 220 ° C. to 225 ° C. Control and return to the original control temperature at -8 ° C, which eliminates wasteful power consumption and is efficient and reliable freezing prevention. When the outside air temperature reaches 3 ° C, this freezing prevention The operation is temporarily stopped.

41は前記制御手段40と通信可能に接続され、潜熱回収型気化式石油給湯装置1の遠隔操作を行うリモコンで、リモコン41は潜熱回収型気化式石油給湯装置1の運転のオンオフを指示する運転スイッチ42や、給湯温度を設定するための給湯温度設定スイッチなどからなる操作部43や、潜熱回収型気化式石油給湯装置1の状態や給湯設定温度などを表示する表示部44を備えているものである。   41 is a remote controller that is communicably connected to the control means 40 and remotely controls the latent heat recovery vaporization type petroleum hot water supply apparatus 1. The remote control 41 is an operation that instructs on / off operation of the latent heat recovery type vaporization type petroleum hot water supply apparatus 1. An operation unit 43 including a switch 42, a hot water supply temperature setting switch for setting a hot water supply temperature, and a display unit 44 for displaying the state of the latent heat recovery type vaporized petroleum hot water supply device 1 and the hot water supply set temperature. It is.

次に、この一実施形態の潜熱回収型気化式石油給湯装置1の動作について説明する。
前記リモコン41の運転スイッチ42がオンされると、前記制御手段40は、気化温度センサ8の検出する温度に基づき気化器ヒータ4を制御すると共に、混合室温度センサ9の検出する温度に基づき混合室ヒータ6を制御し、気化器2および混合室5の予熱を行い、気化器2が燃油を気化可能な温度、例えば気化器2の温度が220℃〜250℃に維持され、混合室5の温度が125℃〜130℃に維持されるスタンバイ状態となる。このスタンバイ状態では、燃焼要求が発生した場合には素早くバーナ11を着火でき、必要最低限の温度を維持することでスタンバイ時の消費電力を低減することができるものである。
Next, the operation of the latent heat recovery type vaporized petroleum hot water supply device 1 of this embodiment will be described.
When the operation switch 42 of the remote controller 41 is turned on, the control means 40 controls the vaporizer heater 4 based on the temperature detected by the vaporization temperature sensor 8 and mixes based on the temperature detected by the mixing chamber temperature sensor 9. The chamber heater 6 is controlled to preheat the vaporizer 2 and the mixing chamber 5, the temperature at which the vaporizer 2 can vaporize the fuel oil, for example, the temperature of the vaporizer 2 is maintained at 220 ° C. to 250 ° C. It will be in the standby state in which temperature is maintained at 125 to 130 degreeC. In this standby state, when a combustion request is generated, the burner 11 can be ignited quickly, and the power consumption during standby can be reduced by maintaining the necessary minimum temperature.

前記スタンバイ状態において、給湯栓が開栓され、流量センサ36が最低作動流量以上の流量を検出して燃焼要求が発生したと前記制御手段40が判断すると、気化器ヒータ4および混合室ヒータ6を強制的にオンして着火性を良くし、電磁ポンプ14および燃焼ファン16を駆動させて、気化器2で気化された気化ガスと一次空気とを混合室5で予混合し、予混合ガスを燃焼部10より噴出して燃焼を開始させるものである。   In the standby state, when the hot water tap is opened and the flow rate sensor 36 detects a flow rate equal to or higher than the minimum operating flow rate and the control means 40 determines that a combustion request has occurred, the carburetor heater 4 and the mixing chamber heater 6 are turned on. It is forcibly turned on to improve the ignitability, and the electromagnetic pump 14 and the combustion fan 16 are driven to premix the vaporized gas vaporized in the vaporizer 2 and the primary air in the mixing chamber 5. It is ejected from the combustion section 10 to start combustion.

前記バーナ11の燃焼により発生した燃焼ガスは、一次熱交換器24を流通し、一次熱交換器24を通過した後、二次熱交換器26を流通し、二次熱交換器26を通過した後、排気口27から潜熱回収型気化式石油給湯装置1外へ排出されるものである。また、給水源から供給された水は、給水管31から二次受熱管25に導かれ、二次受熱管25から一次受熱管23へ順に流通して、ここで燃焼ガスとの熱交換により加熱され、そして、一次受熱管23から給湯管32へ導かれ、混合弁34の開度調整によって給湯設定温度に温調された湯が最終的に給湯栓から給湯されるものである。   The combustion gas generated by the combustion of the burner 11 flows through the primary heat exchanger 24, passes through the primary heat exchanger 24, then flows through the secondary heat exchanger 26, and passes through the secondary heat exchanger 26. Thereafter, the heat is discharged from the exhaust port 27 to the outside of the latent heat recovery type vaporized petroleum water heater 1. Further, the water supplied from the water supply source is led from the water supply pipe 31 to the secondary heat receiving pipe 25 and flows in order from the secondary heat receiving pipe 25 to the primary heat receiving pipe 23 where it is heated by heat exchange with the combustion gas. Then, the hot water led from the primary heat receiving pipe 23 to the hot water supply pipe 32 and adjusted to the hot water supply set temperature by adjusting the opening of the mixing valve 34 is finally supplied from the hot water tap.

この時、二次熱交換器26において、二次受熱管25を流通する水と燃焼ガスとが熱交換され、燃焼ガス中の水蒸気が露点以下となることにより生成されたドレンはドレン受け28で回収され、ドレン配管29を介して、内部に中和剤が充填された中和装置30に流入し、中和装置30内で中和処理された後、中和装置30外に排出され、所定箇所の下水に排水されるものである。   At this time, in the secondary heat exchanger 26, the water flowing through the secondary heat receiving pipe 25 and the combustion gas are heat-exchanged, and the drain generated when the water vapor in the combustion gas falls below the dew point is drained by the drain receiver 28. It is collected and flows into the neutralizing device 30 filled with a neutralizing agent through the drain pipe 29, neutralized in the neutralizing device 30, and then discharged to the outside of the neutralizing device 30. It is drained into the sewage.

次に、低温環境下での潜熱回収型気化式石油給湯装置1の状況について図2に示すフローチャートで説明すると、冬季等で外気温度が低い時であって、リモコン41の運転スイッチ42がオフされて潜熱回収型気化式石油給湯装置1の運転が停止している状態が長時間続いた時、潜熱回収型気化式石油給湯装置1内の温度は潜熱回収型気化式石油給湯装置1外の外気温度に近似し、一次受熱管23、二次受熱管25では水の流通がないため、一次受熱管23内および二次受熱管25内に滞留している水は凍結する可能性がある。   Next, the situation of the latent heat recovery vaporization type petroleum hot water supply device 1 in a low temperature environment will be described with reference to the flowchart shown in FIG. 2. When the outside air temperature is low in winter or the like, the operation switch 42 of the remote controller 41 is turned off. When the operation of the latent heat recovery vaporization type petroleum hot water supply device 1 is stopped for a long time, the temperature inside the latent heat recovery type vaporization type petroleum hot water supply device 1 is the outside air outside the latent heat recovery type vaporization type petroleum hot water supply device 1. Since the temperature approximates to that of the primary heat receiving pipe 23 and the secondary heat receiving pipe 25 and there is no flow of water, the water staying in the primary heat receiving pipe 23 and the secondary heat receiving pipe 25 may be frozen.

ここで、上記のように、リモコン41の運転スイッチ42がオフされて潜熱回収型気化式石油給湯装置1の運転が停止している時において、温度検出手段37(熱交出口温度センサ)の検出する温度が、凍結のおそれがある予め設定された所定温度の−5℃を検出した場合(ステップ45)、YESでステップ46に進み前記制御手段40は加熱用ヒータである気化器ヒータ4及び混合室ヒータ6をオンさせ、気化温度センサ8によって加熱用ヒータ4、6の制御温度を130℃〜140℃に制御し、気化器2の熱が燃焼部10および吸熱フィン12に伝熱し、燃焼部10および吸熱フィン12を介して効率的に放熱され、その熱によって燃焼部10上の空気が加熱される。この加熱された空気は燃焼室22内へ上昇し、燃焼部10の上方すなわちバーナ11の上方で燃焼室22内に位置する一次受熱管23および二次受熱管25を加熱するものである。それによって、一次受熱管23内に滞留する水および二次受熱管25内に滞留する水の凍結防止を確実に行うことができ、燃油を気化するための気化器2に備えられた気化器ヒータ4及び混合室ヒータ6を凍結防止に使用するので、一次受熱管23および二次受熱管25内の水の凍結を防止するための専用の凍結防止用ヒータを設ける必要がなく部品コストを抑えることができると共に、凍結防止用ヒータの組み付け作業を不要とすることができ、さらに、凍結防止用ヒータを設ける必要がないことから部品故障のリスクを低減させることができるものである。   Here, as described above, when the operation switch 42 of the remote controller 41 is turned off and the operation of the latent heat recovery vaporization type petroleum hot water supply device 1 is stopped, the temperature detection means 37 (heat exchange outlet temperature sensor) detects. When the temperature to be detected is detected as -5 ° C., which is a preset predetermined temperature at which there is a risk of freezing (step 45), the process proceeds to step 46 with YES, and the control means 40 is mixed with the vaporizer heater 4 which is a heater for heating. The chamber heater 6 is turned on, the control temperature of the heaters 4 and 6 is controlled to 130 ° C. to 140 ° C. by the vaporization temperature sensor 8, and the heat of the vaporizer 2 is transferred to the combustion unit 10 and the heat sink fins 12. The heat is efficiently radiated through the heat sink 10 and the heat absorbing fins 12, and the air on the combustion unit 10 is heated by the heat. The heated air rises into the combustion chamber 22 and heats the primary heat receiving pipe 23 and the secondary heat receiving pipe 25 located in the combustion chamber 22 above the combustion section 10, that is, above the burner 11. Thereby, it is possible to reliably prevent freezing of the water staying in the primary heat receiving pipe 23 and the water staying in the secondary heat receiving pipe 25, and the vaporizer heater provided in the vaporizer 2 for vaporizing the fuel oil. 4 and the mixing chamber heater 6 are used to prevent freezing, so that it is not necessary to provide a dedicated anti-freezing heater for preventing freezing of the water in the primary heat receiving pipe 23 and the secondary heat receiving pipe 25, thereby reducing the component cost. In addition, it is possible to eliminate the work of assembling the anti-freezing heater and to reduce the risk of component failure because it is not necessary to provide the anti-freezing heater.

次にステップ47で外気温度が更に下がり−10℃に達すると、YESでステップ48に進み気化温度センサ8によって加熱用ヒータ4、6の制御温度を170℃〜180℃と高い温度に制御するが、ステップ49で温度検出手段37による検出温度が−3℃を検出するとステップ46の元の制御温度に戻るもので、逆にステップ50で更に温度検出手段37の検出温度が下がり−20℃を検出することで、YESでステップ51に進み気化温度センサ8によって加熱用ヒータ4、6の制御温度を220℃〜225℃と更に高い温度に制御するが、ステップ52で温度検出手段37による検出温度が−8℃を検出するとステップ48の一つ前の制御温度に戻るもので、次にステップ53で外気温温度が3℃になるとステップ54で一旦凍結防止運転が停止されるが、再び外気温度が低下すれば凍結防止運転は再開されるものであり、無駄な電力消費をなくし効率が良くしかも確実に凍結防止が行われるようにしたものである。   Next, when the outside air temperature further decreases to −10 ° C. in step 47, the process proceeds to step 48 in YES, and the control temperature of the heaters 4 and 6 is controlled to a high temperature of 170 ° C. to 180 ° C. by the vaporization temperature sensor 8. When the temperature detected by the temperature detecting means 37 is detected to be −3 ° C. in step 49, the control temperature returns to the original control temperature in step 46. Conversely, in step 50, the temperature detected by the temperature detecting means 37 further decreases to detect −20 ° C. Then, the process proceeds to step 51 with YES, and the control temperature of the heaters 4 and 6 is controlled to a higher temperature of 220 ° C. to 225 ° C. by the vaporization temperature sensor 8, but the detected temperature by the temperature detection means 37 is determined at step 52. When −8 ° C. is detected, the control temperature returns to the control temperature immediately before step 48. Next, when the outside air temperature reaches 3 ° C. in step 53, in step 54 it is temporarily frozen. Although the operation is stopped, in which as the freeze prevention operation if decreased ambient air temperature is intended to be resumed, without unnecessary power consumption efficiency is good and reliably antifreeze is performed again.

なお、本発明は先に説明した一実施形態に限定されるものではなく、本実施形態では、凍結防止温度を検出する温度検出手段を熱交出口温度センサ37としたが、温度検出手段は、冬季等で外気温度が低く、潜熱回収型気化式石油給湯装置1の運転が停止している時に、一次受熱管23、二次受熱管25内に滞留している水が凍結するおそれがあるか否かを判断するための温度を検出できるものであればよく、熱交出口温度センサ37の代わりに、潜熱回収型気化式石油給湯装置1内の給水温度センサ35や給湯温度センサ38を凍結防止温度を検出する温度検出手段としてもよく、また、潜熱回収型気化式石油給湯装置1内の雰囲気温度を検出する専用の温度センサを設けて、それを凍結防止温度を検出する温度検出手段としてもよいものである。   The present invention is not limited to the embodiment described above. In this embodiment, the temperature detection means for detecting the antifreezing temperature is the heat exchange outlet temperature sensor 37, but the temperature detection means is Whether the water staying in the primary heat receiving pipe 23 and the secondary heat receiving pipe 25 may freeze when the outside air temperature is low and the operation of the latent heat recovery type vaporized petroleum water heater 1 is stopped in winter or the like What is necessary is just to be able to detect the temperature for judging whether or not, and instead of the heat exchange outlet temperature sensor 37, the water supply temperature sensor 35 and the hot water supply temperature sensor 38 in the latent heat recovery type vaporized hot water supply apparatus 1 are prevented from freezing. The temperature detecting means for detecting the temperature may be used, or a dedicated temperature sensor for detecting the ambient temperature in the latent heat recovery type vaporized petroleum hot water supply apparatus 1 may be provided and used as a temperature detecting means for detecting the anti-freezing temperature. good thing A.

また、本実施形態では、熱交出口温度センサ37の検出する温度が、凍結のおそれがある予め設定された凍結防止温度を検出した場合、気化器ヒータ4及び混合室ヒータ6の両方をオンするようにしたが、気化器ヒータ4と混合室ヒータ6のどちらか一方を選択したり、温度検出手段37の検出温度で変更するようにしてもよいものである。   In the present embodiment, when the temperature detected by the heat exchange outlet temperature sensor 37 detects a preset anti-freezing temperature at which there is a risk of freezing, both the vaporizer heater 4 and the mixing chamber heater 6 are turned on. However, one of the vaporizer heater 4 and the mixing chamber heater 6 may be selected, or may be changed depending on the temperature detected by the temperature detecting means 37.

1 気化式石油給湯装置
2 気化器
4 気化器ヒータ(加熱用ヒータ)
5 混合室
6 混合室ヒータ(加熱用ヒータ)
7 気化部
10 燃焼部
11 バーナ
16 燃焼ファン
23 一次受熱管
24 一次熱交換器
37 熱交出口温度センサ(温度検出手段)
40 制御手段
41 リモコン
42 運転スイッチ
DESCRIPTION OF SYMBOLS 1 Vaporization type petroleum hot water supply device 2 Vaporizer 4 Vaporizer heater (heater for heating)
5 Mixing chamber 6 Mixing chamber heater (heater for heating)
7 Vaporizing section 10 Combusting section 11 Burner 16 Combustion fan 23 Primary heat receiving pipe 24 Primary heat exchanger 37 Heat exchange outlet temperature sensor (temperature detecting means)
40 Control means 41 Remote control 42 Operation switch

Claims (1)

加熱用ヒータを備え燃油を気化させる気化部と、この気化部の温度を検出する気化温度センサと、前記気化部で気化させた燃油を燃焼させる燃焼部とで構成されるバーナと、このバーナに燃焼空気を供給する燃焼ファンと、該バーナの燃焼により発生した燃焼ガスから顕熱を回収し一次受熱管を流通する水を加熱する一次熱交換器と、凍結防止の所定温度を検出する温度検出手段と、前記気化温度センサが検出する温度が所定の制御温度範囲になるように前記加熱用ヒータを制御する制御手段と、を備え、前記バーナの上方に前記一次熱交換器を配置した気化式石油給湯装置であって、該気化式石油給湯装置を遠隔操作するリモコンの運転スイッチがオフされ、前記気化式石油給湯装置の運転が停止している時に、前記温度検出手段が前記凍結防止の所定温度を検出した場合は、前記制御手段は、前記加熱用ヒータをオンして凍結防止運転すると共に、この凍結防止運転時の前記所定の制御温度範囲を前記温度検出手段の検出温度が低くなる程高くなるようにして前記加熱用ヒータを制御するようにした事を特徴とする気化式石油給湯装置。 A burner comprising a heater for heating and vaporizing fuel, a vaporization temperature sensor for detecting the temperature of the vaporization unit, and a combustion unit for burning the fuel vaporized by the vaporization unit, and a burner A combustion fan that supplies combustion air, a primary heat exchanger that recovers sensible heat from the combustion gas generated by the combustion of the burner and heats the water flowing through the primary heat receiving pipe, and temperature detection that detects a predetermined temperature for freezing prevention means and, and a control means for the temperature in which the vaporization temperature sensor is detected to control the heater to a predetermined control temperature range, evaporative placing the said primary heat exchanger above the burner When the operation switch of the remote controller for remotely operating the vaporizing oil hot water supply apparatus is turned off and the operation of the vaporizing oil hot water supply apparatus is stopped, the temperature detecting means is the oil hot water supply apparatus. When a predetermined temperature for prevention is detected, the control means turns on the heater for anti-freezing operation, and the detected temperature of the temperature detecting means is within the predetermined control temperature range during this anti-freezing operation. A vaporizing petroleum hot water supply apparatus characterized in that the heating heater is controlled so as to become higher as it becomes lower.
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