JP5670166B2 - Hot air heater for horticulture - Google Patents

Hot air heater for horticulture Download PDF

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JP5670166B2
JP5670166B2 JP2010273240A JP2010273240A JP5670166B2 JP 5670166 B2 JP5670166 B2 JP 5670166B2 JP 2010273240 A JP2010273240 A JP 2010273240A JP 2010273240 A JP2010273240 A JP 2010273240A JP 5670166 B2 JP5670166 B2 JP 5670166B2
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combustion gas
casing
furnace
smoke
chimney
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JP2012120476A (en
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征忠 高崎
征忠 高崎
鹿倉 秀文
秀文 鹿倉
山口 博光
博光 山口
大介 有留
大介 有留
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SANSHU SANGYO CO., LTD.
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/25Greenhouse technology, e.g. cooling systems therefor
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P60/00Technologies relating to agriculture, livestock or agroalimentary industries
    • Y02P60/14Measures for saving energy, e.g. in green houses

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Description

本発明は、施設園芸ハウス内を温風で暖房する温風暖房機に関するものである。   The present invention relates to a hot air heater that heats the inside of a facility horticulture house with hot air.

通常、この種の温風暖房機の炉体(熱交換部)は、製造コストの面より、一般的にワンパスタイプ(図7)が主流となっている(例えば、特許文献1、2参照)。温風暖房機によるハウス内加温は、ハウス内空気を送風機2によりケーシング1内に取り入れ、ハウス内空気とバーナ3による燃焼熱(燃焼ガス)を炉体(火炉4および煙管群5)により熱交換し、温風を吐出口6からダクトにより配風して暖房が行なわれる。燃焼ガスは煙突7より排気される。従来から、少ない燃料により効率の高い暖房機が求められてきたが、重油の価格高騰や環境政策などにより更なる効率化が求められてきている。   Usually, the furnace body (heat exchanging part) of this type of hot air heater is generally a one-pass type (FIG. 7) from the viewpoint of manufacturing cost (see, for example, Patent Documents 1 and 2). . In the house warming by the hot air heater, the air in the house is taken into the casing 1 by the blower 2, and the combustion heat (combustion gas) by the air in the house and the burner 3 is heated by the furnace body (the furnace 4 and the smoke tube group 5). Heating is performed by exchanging the warm air from the discharge port 6 through a duct. Combustion gas is exhausted from the chimney 7. Conventionally, a highly efficient heater with a small amount of fuel has been demanded, but further efficiency has been demanded due to the rising price of heavy oil and environmental policies.

特開平5−133610号公報JP-A-5-133610 特開2006−317043号公報JP 2006-317043 A

暖房機の熱効率は、単位熱量当りの低位発熱量と排ガス損失熱量の相殺比率により算出されることから、排ガス損失熱量(煙突内の排ガス温度)が低い程、熱効率が向上する。しかしながら、施設園芸用の温風暖房機の耐久年数は通常10年以上を目標に設計されるため、金属疲労などを考慮すると、熱効率は90%が限界であり、それ以上の引き上げは困難であった。   Since the thermal efficiency of the heater is calculated by the offset ratio between the lower heating value per unit heat quantity and the exhaust gas loss heat quantity, the lower the exhaust gas loss heat quantity (the exhaust gas temperature in the chimney), the higher the thermal efficiency. However, the durability of hot air heaters for horticultural horticulture is usually designed with a goal of 10 years or more, so considering metal fatigue, the thermal efficiency is limited to 90%, and it is difficult to raise it further. It was.

また、施設園芸の暖房用に使用される燃料は、価格、発熱量などによりA重油(JIS1種1号)が主流とされるが、A重油には1%弱の硫黄が含まれ、排ガス温度を下げすぎると、燃料に含まれる硫黄反応により硫酸が生成され(低温腐食)、金属を腐食させ、暖房機の耐久性を低下させるという問題がある。   In addition, heavy oil A (JIS Type 1 No. 1) is the mainstream fuel used for facility horticulture heating due to price, calorific value, etc., but heavy oil A contains less than 1% sulfur and exhaust gas temperature. If the temperature is too low, sulfuric acid is generated by the sulfur reaction contained in the fuel (low temperature corrosion), which corrodes the metal and lowers the durability of the heater.

本発明は上記課題に鑑みてなされたもので、炉体の工夫により伝熱性能を高め、もって熱効率を高めた施設園芸用温風暖房機を提供すること、また、排熱回収性能を高めて、熱効率をより高めた施設園芸用温風暖房機を提供すること、また、低温腐食性能に優れた施設園芸用温風暖房機を提供することを目的とする。   The present invention has been made in view of the above problems, and provides a warm air heater for facility horticulture that has improved heat transfer performance by improving the furnace body and thereby improved thermal efficiency, and has improved exhaust heat recovery performance. An object of the present invention is to provide a warm air heater for facility horticulture with higher thermal efficiency, and to provide a warm air heater for facility horticulture having excellent low-temperature corrosion performance.

上記課題を解決するために、本発明に係る施設園芸用温風暖房機は、
ケーシングと、ケーシング内に横向きに配置され、ケーシングの全長に対し1/2を超える長さをもち、一端にバーナのノズル部を臨ませると共に、他端にノズル部の中心線を中心とする凹状の湾曲面からなり、燃焼ガスを炉内壁面に沿って反転させる反転部が形成された筒状の火炉と、反転された燃焼ガスを火炉の一端寄りからケーシング内で火炉外へ導出させる第1煙室と、第1煙室から火炉の他端側へ向けて燃焼ガスを案内する第1煙管群と、ケーシングの上面に取付けられ、下向きの送風により燃焼ガスとの間で熱交換を行わせる送風機と、ケーシング内で第1煙管群を流れる燃焼ガスを集合させる第2煙室と、ケーシング内で第2煙室から火炉の他端近くで下向きに燃焼ガスを案内する第2煙管群と、ケーシング内で第2煙管群を流れる燃焼ガスを集合させる第3煙室と、第3煙室から燃焼ガスをケーシング外へ排気させる煙突と、第3煙室と煙突の間または煙突の途中に燃焼ガスの排気を誘引する排気誘引手段を備え、バーナのノズル部が、ノズル本体の前方にディフューザを設け、ノズル本体を囲む外筒の先端にラッパ状のファンネル部を形成したことを最も主要な特徴とする。
In order to solve the above problems, a warm air heater for facility horticulture according to the present invention,
A casing, which is disposed sideways in the casing, has a length exceeding 1/2 of the total length of the casing, has the nozzle portion of the burner facing one end, and has a concave shape centered on the center line of the nozzle portion at the other end of consists curved surface, a cylindrical furnace which reversed portions are formed to reverse along the combustion gas in the furnace wall, the first to derive an inverted combustion gas from near one end of the furnace to the furnace outside the casing and smoke chamber, a first tobacco pipe group for guiding the combustion gases toward the other end of the furnace from the first smoke box, mounted on the upper surface of the casing, to perform heat exchange between the combustion gas by the downward air blowing A blower, a second smoke chamber for collecting combustion gas flowing through the first smoke tube group in the casing, a second smoke tube group for guiding the combustion gas downward from the second smoke chamber near the other end of the furnace in the casing, In the casing the second stack A third smoke chamber to set the combustion gas, and a chimney to exhaust from the third smoke chamber combustion gas to the outside of the casing, the exhaust attraction to attract the exhaust of the combustion gas in the middle of or between chimney third smoke chamber and the chimney The burner nozzle portion is provided with a diffuser in front of the nozzle body, and a trumpet-shaped funnel portion is formed at the tip of the outer cylinder surrounding the nozzle body .

本発明に係る施設園芸用温風暖房機によると、火炉の燃焼室内でバーナにより燃焼される燃料は、燃焼する際輝炎を発し炉壁へ輻射により燃焼熱を伝達する。引き続き、燃焼ガスはバーナのノズル部の反対側に位置する反転部で炉内壁面に沿って反転し、炉内壁面をなめるように流れ、火炉内から第1煙室内へ誘導される。その際、炉壁に対しさらに燃焼ガス熱を伝達しながら流動する。従来のワンパスタイプ、ツーパスタイプの火炉に比べ、戻り燃焼ガスにより炉内壁面との接触時間を長く取ることができ、炉壁への伝熱量が増加する。すなわち、火炉内で燃焼ガスが戻る戻り燃焼方式(リバースリターン)を採用することにより、従来対比で伝熱性能を高めることができる。
また、伝熱性能の向上により、ケーシング内に横向きに配置する火炉の大きさを小さくし、かつ、ケーシング内に、第1煙室から第3煙室に至る熱交換および排熱回収の機器をコンパクトに納めた、熱交換率の高い温風暖房機を実現できる。
According to the hot air heater for facility horticulture according to the present invention, the fuel combusted by the burner in the combustion chamber of the furnace emits a bright flame when combusting and transmits the combustion heat to the furnace wall by radiation. Subsequently, the combustion gas is reversed along the inner wall surface of the furnace at the reversing portion located on the opposite side of the nozzle portion of the burner, flows so as to lick the inner wall surface of the furnace, and is guided from the furnace into the first smoke chamber. At that time, it flows while further transferring combustion gas heat to the furnace wall. Compared with the conventional one-pass type and two-pass type furnaces, the return combustion gas can make the contact time with the inner wall of the furnace longer, and the amount of heat transfer to the furnace wall increases. That is, by adopting a return combustion method in which the combustion gas returns in the furnace (reverse return), the heat transfer performance can be enhanced as compared with the conventional case.
In addition, by improving the heat transfer performance, the size of the furnace placed sideways in the casing is reduced, and a device for heat exchange and exhaust heat recovery from the first smoke chamber to the third smoke chamber is provided in the casing. A hot air heater with a high heat exchange rate can be realized in a compact size.

本発明に係る施設園芸用温風暖房機は、前記反転部が、火炉の他端の端面から側周面にかけて滑らかに湾曲する内壁面形状を有することを第2の特徴とする。   A second feature of the hot air heater for facility horticulture according to the present invention is that the reversing portion has an inner wall surface shape that smoothly curves from an end surface at the other end of the furnace to a side peripheral surface.

本発明に係る施設園芸用温風暖房機は、前記煙管群の煙管内に、燃焼ガスをらせん状に案内するスクリュー板が配置されていることを第3の特徴とする。スクリュー板の配置により、煙管内を流れる燃焼ガスの拡散作用を助長させ、煙管の管壁との接触時間を長くとり、管壁への伝熱量が増加する。   The hot air heater for horticultural horticulture according to the present invention is characterized in that a screw plate that guides the combustion gas in a spiral shape is arranged in the smoke pipe of the smoke pipe group. The arrangement of the screw plate promotes the diffusion action of the combustion gas flowing in the smoke pipe, increases the contact time with the pipe wall of the smoke pipe, and increases the amount of heat transfer to the pipe wall.

本発明に係る施設園芸用温風暖房機は、前記第2の煙管群の煙管内に、燃焼ガスをらせん状に案内するスクリュー板が配置されていることを第6の特徴とする。スクリュー板の配置により、煙管内を流れる燃焼ガスの拡散作用を助長させ、煙管の管壁との接触時間を長くとり、管壁への伝熱量が増加する。これによって、排熱回収率が高まる。   The hot air heater for facility horticulture according to the present invention is characterized in that a screw plate for guiding the combustion gas in a spiral shape is arranged in the smoke pipe of the second smoke pipe group. The arrangement of the screw plate promotes the diffusion action of the combustion gas flowing in the smoke pipe, increases the contact time with the pipe wall of the smoke pipe, and increases the amount of heat transfer to the pipe wall. This increases the exhaust heat recovery rate.

本発明に係る施設園芸用温風暖房機は、前記第2の煙管群の各煙管が耐硫酸性材料から構成されていることを第7の特徴とする。排熱回収後の燃焼ガス温度の低下に伴う低温腐食に対する耐久性が向上する。   The facility horticultural hot air heater according to the present invention has as a seventh feature that each smoke tube of the second smoke tube group is made of a sulfuric acid resistant material. Durability against low-temperature corrosion accompanying a decrease in combustion gas temperature after exhaust heat recovery is improved.

本発明に係る施設園芸用温風暖房機は、第3煙室内に煙突入口に向かう燃焼ガスを分散させる分散手段を備えることを第8の特徴とする。   The facility horticultural hot air heater according to the present invention has an eighth feature that a dispersion means for dispersing combustion gas toward the chimney entrance is dispersed in the third smoke chamber.

本発明に係る施設園芸用温風暖房機は、排気誘引手段が、空気ファンと、煙突の入口付近に設けて空気ファンにより発生した空気流を煙突内に向くジェット流に変換する環状のノズル部を有することを第10の特徴とする。   The hot air heater for horticultural horticulture according to the present invention includes an air nozzle and an annular nozzle portion that is provided near the entrance of the chimney and converts an air flow generated by the air fan into a jet flow directed into the chimney. The tenth feature is to have

以上説明したように、本発明に係る施設園芸用温風暖房機によると、安定したバーナ燃焼を実現しながら、火炉の内壁面に沿って燃焼ガスを反転させることにより、火炉の伝熱性能を高め、もって熱交換効率を大幅に向上させることができるようになった。また、排熱回収手段を設けることにより、より一層の熱交換効率の向上を図ることができる。

As described above, according to the facility horticulture hot air heater according to the present invention, the heat transfer performance of the furnace is improved by reversing the combustion gas along the inner wall surface of the furnace while realizing stable burner combustion. As a result, the heat exchange efficiency can be greatly improved. Further, by providing the exhaust heat recovery means, it is possible to further improve the heat exchange efficiency.

さらに、本発明に係る施設園芸用温風暖房機によると、火炉をコンパクトにして、ケーシング内の空いた空間に排熱回収手段を縦に収めることができ、コンパクトで熱交換効率に優れた温風暖房機を実現できるという優れた効果を奏する。   Further, according to the hot air heater for facility horticulture according to the present invention, the furnace can be made compact, and the exhaust heat recovery means can be stored vertically in the vacant space in the casing, which is compact and has excellent heat exchange efficiency. There is an excellent effect that a wind heater can be realized.

本発明に係る施設園芸用温風暖房機を示す断面図、Sectional drawing which shows the warm air heater for facilities gardening which concerns on this invention, 図1の温風暖房機のA−A線矢視断面、AA line arrow cross section of the hot air heater of FIG. バーナのノズル部を示す拡大断面図、An enlarged sectional view showing the nozzle part of the burner, (A)は第2煙管群の配列を示す平面図、(B)は第2煙管群から第3煙室付近を示す断面図、(C)は(B)に示す第3煙室を正面から見た断面図、(A) is a plan view showing the arrangement of the second smoke tube group, (B) is a cross-sectional view showing the vicinity of the third smoke chamber from the second smoke tube group, (C) is the third smoke chamber shown in (B) from the front. Cross section seen, 排気誘引手段を示す側面図、A side view showing the exhaust attraction means, (A)は吐出部付近を示す側面図、(B)は吐出部における横断面図、(A) is a side view showing the vicinity of the discharge part, (B) is a cross-sectional view of the discharge part, 従来のワンパスタイプの施設園芸用温風暖房機を示す断面図である。It is sectional drawing which shows the conventional hot air heater for facility gardening of the one pass type.

本発明を実施するための一実施形態を図1ないし図6を参照して説明する。図1において、100は施設園芸用温風暖房機である。   An embodiment for carrying out the present invention will be described with reference to FIGS. In FIG. 1, 100 is a warm air heater for facility horticulture.

施設園芸用温風暖房機100は、図1に示すように、ケーシング101内に横向きに円筒状の火炉110が配置され、火炉110の一端にはバーナ120のノズル部121が燃焼室111に臨む形で配置されている。火炉110の他端にはノズル部121と対向して燃焼ガスGを燃焼室111の炉内壁面に沿って反転させる反転部112が形成されている。   As shown in FIG. 1, the facility horticulture hot air heater 100 has a cylindrical furnace 110 disposed horizontally in a casing 101, and a nozzle portion 121 of a burner 120 faces a combustion chamber 111 at one end of the furnace 110. Arranged in a shape. At the other end of the furnace 110, an inversion portion 112 is formed opposite the nozzle portion 121 to invert the combustion gas G along the inner wall surface of the combustion chamber 111.

この反転部112は、より具体的には、火炉110の他端側の端面110aにおける内壁面がノズル部121の中心線を中心とする凹状の湾曲面とされ、さらに同端面110aから火炉110の胴部110bの内周面にかけて滑らかに湾曲して接続する内壁面形状を有している。   More specifically, the inversion portion 112 has an inner wall surface of the end surface 110a on the other end side of the furnace 110 as a concave curved surface centered on the center line of the nozzle portion 121, and further from the end surface 110a to the furnace 110. It has an inner wall surface shape that is smoothly curved and connected to the inner peripheral surface of the trunk portion 110b.

火炉110の一端寄りの上部には、ケーシング101内で、反転された燃焼ガスGを火炉110外へ上向きに導出させる開口部110cと、同開口部110cを覆い燃焼ガスGを一旦集合させる第1煙室130が設けられている。この第1煙室130には火炉110の上方で火炉110の他端へ向けて燃焼ガスGを案内する第1煙管群140が接続されている。図2に示すように、各煙管141は左右に多数本(図示例では計11本)、上下に2列または千鳥状に配列されている。各煙管141には、内部を通過する燃焼ガスGを管内壁面に沿ってらせん状に案内するスクリュー板142が挿入配置されている。   In the upper part near one end of the furnace 110, an opening 110 c that leads the inverted combustion gas G upward in the casing 101 to the outside of the furnace 110 and a first gas that covers the opening 110 c and collects the combustion gas G once. A smoke chamber 130 is provided. Connected to the first smoke chamber 130 is a first smoke tube group 140 that guides the combustion gas G toward the other end of the furnace 110 above the furnace 110. As shown in FIG. 2, each of the smoke tubes 141 is arranged in a large number on the left and right (a total of 11 in the illustrated example) and in two rows or a zigzag on the top and bottom. A screw plate 142 that guides the combustion gas G passing through the inside in a spiral manner along the inner wall surface of the pipe is inserted and disposed in each smoke pipe 141.

バーナ120のノズル部121は、図3に示すように、ノズル本体121aの前方にディフューザ122が設けられ、ノズル本体121aを囲む外筒121bの先端にラッパ状のファンネル部123が形成されている。ファンネル部123は、外筒121bから続く拡径部123aと、拡径部123aから続く環状部123bと、環状部123bの終端から内側に屈曲する屈曲部123cが形成されている。   As shown in FIG. 3, the nozzle portion 121 of the burner 120 is provided with a diffuser 122 in front of the nozzle body 121a, and a trumpet-shaped funnel portion 123 is formed at the tip of an outer cylinder 121b surrounding the nozzle body 121a. The funnel portion 123 is formed with an enlarged diameter portion 123a that continues from the outer cylinder 121b, an annular portion 123b that continues from the enlarged diameter portion 123a, and a bent portion 123c that bends inward from the end of the annular portion 123b.

ケーシング101の上面には、2箇所に吸気口101aが設けられるとともに、各吸気口101aに対応して、送風により燃焼ガスGとの間で熱交換を行わせる2台の送風機150,150が取付けられている。これらの送風機150は、送風ファン151の回転によりハウス内空気をケーシング101内に取り入れると共に、火炉110の燃焼室111内の燃焼熱および燃焼に伴って発生する燃焼ガスGが火炉110から第1煙管群140、後述する第2煙管群170から煙突190に排気される間、熱交換により温風を生成する。   On the upper surface of the casing 101, there are provided two air inlets 101a, and two air blowers 150 and 150 that exchange heat with the combustion gas G by blowing are attached to each of the air inlets 101a. It has been. These blowers 150 take in the air in the house into the casing 101 by the rotation of the blower fan 151, and the combustion heat G in the combustion chamber 111 of the furnace 110 and the combustion gas G generated along with the combustion from the furnace 110 to the first smoke pipe. While being exhausted from the group 140, the second smoke pipe group 170 described later, to the chimney 190, hot air is generated by heat exchange.

第1煙管群140の終端には、各煙管141内を流れる燃焼ガスGを集合させる第2煙室160が接続されている。同第2煙室160の下面には、ケーシング101内で、燃焼ガスGを下向きに案内し、燃焼ガスGの残留熱を回収する縦方向に延びる第2煙管群170が接続されている。この第2煙管群170は、燃焼ガスGの残留熱を回収するためのもので、火炉120の一端側の端面120aおよびケーシング101端面間の隙間空間Sに縦(垂直)方向に配置されている。   A second smoke chamber 160 that collects the combustion gas G flowing in each smoke tube 141 is connected to the end of the first smoke tube group 140. Connected to the lower surface of the second smoke chamber 160 is a second smoke tube group 170 extending in the longitudinal direction for guiding the combustion gas G downward in the casing 101 and recovering the residual heat of the combustion gas G. The second smoke tube group 170 is for recovering the residual heat of the combustion gas G, and is arranged in the vertical (vertical) direction in the gap space S between the end surface 120a on one end side of the furnace 120 and the end surface of the casing 101. .

図4(A)に示すように、各煙管171は左右に多数本(図示例では計11本)、前後に2列または千鳥状に配列されている。各煙管171には、前記煙管141同様に、内部を下向きに流れる燃焼ガスGをらせん状に案内するスクリュー板172が挿入配置されている。各煙管171は燃焼ガスGの凝縮による低温腐食を防止するため耐硫酸鋼(商品名:新日鐵株式会社製「S−TEN鋼」)が使用されている。なお、各煙管171の下部には凝縮水を排水する排水管を取付け、排水管からケーシング101外へ排水できるようになっている。   As shown in FIG. 4 (A), each of the smoke tubes 171 is arranged in a large number on the left and right (total 11 in the illustrated example), and arranged in two rows or zigzag in the front and rear. Each smoke pipe 171 is inserted with a screw plate 172 that guides the combustion gas G flowing downward in the spiral in the same manner as the smoke pipe 141. In order to prevent low temperature corrosion due to the condensation of the combustion gas G, each smoke pipe 171 is made of sulfuric acid resistant steel (trade name: “S-TEN steel” manufactured by Nippon Steel Corp.). A drain pipe for draining condensed water is attached to the lower part of each smoke pipe 171 so that the drain can be drained out of the casing 101.

第2煙管群170の終端には、ケーシング101内で、各煙管171内を流れる排熱回収後の燃焼ガスGを集合させる第3煙室180が接続されている。第3煙室180内には、図4(B)(C)に示すように、煙突190の入口に向かう燃焼ガスGを分散させる、すなわち、煙突190の入口に近い側の燃焼ガスGを煙突190の入口に遠い側に迂回させる分散板181が設けられている。   A third smoke chamber 180 for collecting the combustion gas G after exhaust heat recovery flowing in each smoke tube 171 is connected to the end of the second smoke tube group 170 in the casing 101. In the third smoke chamber 180, as shown in FIGS. 4B and 4C, the combustion gas G toward the inlet of the chimney 190 is dispersed, that is, the combustion gas G on the side close to the inlet of the chimney 190 is discharged. A dispersion plate 181 is provided to make a detour on the far side of the entrance of 190.

第2煙管群170を下向きに流れる燃焼ガスGは、上向きと異なり、ガス抵抗が増す傾向にあり、抵抗の低い部分(煙突190の入口に近い部分)へ集中する流れが生じる。分散板181の存在により煙突190の入口に遠い燃焼ガスGも平均した流れとなり、バランスの良い熱交換、すなわちより効率的な排熱回収が可能である。   Unlike the upward direction, the combustion gas G that flows downward through the second smoke tube group 170 tends to increase the gas resistance, and a flow that concentrates on a portion with a low resistance (portion close to the inlet of the chimney 190) occurs. Due to the presence of the dispersion plate 181, the combustion gas G far from the inlet of the chimney 190 becomes an average flow, and a balanced heat exchange, that is, more efficient exhaust heat recovery is possible.

第3煙室180の側面にはケーシング101外に延びる煙突190が接続されている。第3煙室180の出口と煙突190の入口の間には、燃焼ガスGを煙突190側に誘引する排ガス誘引器(排ガスブースター)200が設けられている。排ガス誘引器200は、第3煙室180の出口に接続された第1筒体201と、煙突190の入口に接続された第2筒体202との間に環状の噴出ノズル部203が形成されている。   A chimney 190 extending outside the casing 101 is connected to the side surface of the third smoke chamber 180. Between the outlet of the third smoke chamber 180 and the inlet of the chimney 190, an exhaust gas inducer (exhaust gas booster) 200 for attracting the combustion gas G to the chimney 190 side is provided. In the exhaust gas attractor 200, an annular ejection nozzle portion 203 is formed between the first cylinder 201 connected to the outlet of the third smoke chamber 180 and the second cylinder 202 connected to the inlet of the chimney 190. ing.

図5に示すように、噴出ノズル部203は、第1筒体201の先端部が次第に小径となる縮径部201aとされ、第2筒体202の後端部が次第に小径となる縮径部202aとされ、第1筒体201側の縮径部201aの先端が水平に延在する環状の水平部201bに形成され、第2筒体202の縮径部202aの先端が第1筒体201側の水平部201bの外側にあって、第1筒体201の縮径部201aの外面に沿って上向きに曲がる拡径部202bに形成されている。第2筒体202の後端部と第1筒体201の先端部との間には環状の隙間dが形成されている。 As shown in FIG. 5, the ejection nozzle portion 203 has a reduced diameter portion 201 a in which the distal end portion of the first cylindrical body 201 is gradually reduced in diameter, and a reduced diameter portion in which the rear end portion of the second cylindrical body 202 is gradually reduced in diameter. 202a, the tip of the reduced diameter portion 201a on the first cylinder 201 side is formed in an annular horizontal portion 201b that extends horizontally, and the tip of the reduced diameter portion 202a of the second cylinder 202 is the first cylinder 201. It is formed on the outer side of the horizontal portion 201b on the side, and on the enlarged diameter portion 202b that bends upward along the outer surface of the reduced diameter portion 201a of the first cylindrical body 201. An annular gap d 1 is formed between the rear end portion of the second cylinder 202 and the front end portion of the first cylinder 201.

環状の噴出ノズル部203を囲むように第1筒体201と第2筒体202の周囲には環状の通風室204が設けられている。環状の通風室204には側面に吸気口205aを開口するケーシング205A、205Bが取り付けられ、各ケーシング205A、205B内にはモータ206で回転駆動される2段式の吸込みファン(インペラ)が収容されている。   An annular ventilation chamber 204 is provided around the first cylinder 201 and the second cylinder 202 so as to surround the annular ejection nozzle portion 203. Casings 205A and 205B that open air inlets 205a are attached to the side of the annular ventilation chamber 204, and a two-stage suction fan (impeller) that is driven to rotate by a motor 206 is accommodated in each of the casings 205A and 205B. ing.

かかる排ガス誘引器200は、モータ206により吸込みファンを回転駆動させると、ハウス内空気をケーシング205A、205Bから環状の通風室204内に誘引して、環状の噴出ノズル部203から煙突190の内部に向けて高速で噴出させ、これにより、第1筒体201および第2筒体202内部に負圧を発生させ、第3煙室180内の燃焼ガスGを煙突190へ向けて誘引するようになっている。   When the suction fan is driven to rotate by the motor 206, the exhaust gas attractor 200 attracts the air in the house from the casings 205A and 205B into the annular ventilation chamber 204 and enters the inside of the chimney 190 from the annular ejection nozzle portion 203. As a result, a negative pressure is generated inside the first cylinder 201 and the second cylinder 202, and the combustion gas G in the third smoke chamber 180 is attracted toward the chimney 190. ing.

煙突190の配列によっては、煙突190の局部抵抗により燃焼ガスGの引きの悪い(排気抵抗)場合が生じる。排ガス誘引器200により、煙突190の局部抵抗による損失をなくし、安定したバーナ燃焼を実現できる。また、噴出ノズル部203からの外気の吹き込みで燃焼ガスGが希釈化され、燃焼ガス温度が低下し、高所への排気筒設置工事も不要になるなどの煙突レス化も可能となる。   Depending on the arrangement of the chimney 190, the local resistance of the chimney 190 may cause the combustion gas G to be pulled poorly (exhaust resistance). The exhaust gas attractor 200 eliminates the loss due to the local resistance of the chimney 190 and realizes stable burner combustion. Further, the combustion gas G is diluted by blowing the outside air from the ejection nozzle portion 203, the temperature of the combustion gas is lowered, and it is possible to eliminate the chimney such that the construction of installing the exhaust pipe at a high place becomes unnecessary.

ケーシング101の他端寄りの下面にはケーシング101内で生成された温風を吐出させる吐出室211を備える吐出部210が設けられ、この吐出部210の各側面には温風を吐出させる吐出口210aが形成されている。各吐出口210aには図示しないダクトが接続され、各ダクトを通じて施設園芸用ハウス内の全域に温風を行き渡らせるようになっている。   On the lower surface near the other end of the casing 101, there is provided a discharge unit 210 having a discharge chamber 211 for discharging hot air generated in the casing 101, and a discharge port for discharging hot air on each side surface of the discharge unit 210. 210a is formed. Ducts (not shown) are connected to the respective outlets 210a, and warm air is distributed throughout the entire area of the facility horticulture house through the ducts.

吐出室211には、図6(A)(B)に示すように、ケーシング101内から下面の開口部を通して下向きに流出される温風を吐出室211内で拡散させる温風拡散板212が配置されている。この温風拡散板212はちょうど開口部の真下に水平姿勢に保持され、温風拡散板212の中央には開口部212aが設けられ、温風拡散板212の周囲と吐出室211の内周面との間に隙間dが設けられている。 As shown in FIGS. 6A and 6B, the discharge chamber 211 is provided with a hot air diffusion plate 212 for diffusing the warm air flowing downward from the inside of the casing 101 through the opening on the lower surface in the discharge chamber 211. Has been. The hot air diffusion plate 212 is held in a horizontal posture just below the opening, and an opening 212 a is provided at the center of the hot air diffusion plate 212, and the periphery of the hot air diffusion plate 212 and the inner peripheral surface of the discharge chamber 211. clearance d 2 is provided between the.

従来の温風暖房機により吐出される温風は混合部がほとんどない状態で配風されるため、通常5〜10℃程度の温度ばらつきがある。そこで、吐出室210内に温風拡散板212を配置することで、下向きに吐出室211内に流出する温風は、温風拡散板212中央の開口部212aと周囲の隙間dを流れることにより拡散が促進され、吐出室211内の混合が促進される。その結果、均一な温度(温度ばらつき3℃以内)の温風として各吐出口210aからそれぞれ吐出されるようになる。 Since the warm air discharged by the conventional warm air heater is distributed with almost no mixing part, there is usually a temperature variation of about 5 to 10 ° C. Therefore, by disposing the hot air diffuser 212 into the discharge chamber 210, hot air flowing into the discharge chamber 211 to downward, flow through the hot air diffuser 212 central opening 212a and the surrounding gap d 2 Thus, diffusion is promoted and mixing in the discharge chamber 211 is promoted. As a result, the air is discharged from each discharge port 210a as warm air having a uniform temperature (temperature variation within 3 ° C.).

なお、図1中、符号220はハウス内に設置された温度センサ等に基づき、バーナ120、2台の送風機150、排ガス誘引器200の各運転を制御する制御部を示している。   In FIG. 1, reference numeral 220 denotes a control unit that controls each operation of the burner 120, the two blowers 150, and the exhaust gas attractor 200 based on a temperature sensor or the like installed in the house.

次に、上記構成の施設園芸用温風暖房機100の作用について説明する。まず、2台台の送風機150を運転し、バーナ120のノズル部121から燃焼室111内に噴霧した燃料を点火装置により着火して燃焼させると、燃焼熱が輻射により炉内壁に伝達されると共に、高温(約1700℃〜1900℃程度)の燃焼ガスGが前方の端面110aの炉内壁面に達し、そこから湾曲する炉内壁面および胴部110bの炉内周面をなめるように反転して反対側の開口部101bに向かい、その間、高温の燃焼ガスGが炉壁に熱を伝達し、開口部101bから第1煙室130内に上向きに入る。   Next, an operation of the facility horticulture hot air heater 100 having the above-described configuration will be described. First, when two blowers 150 are operated and the fuel sprayed into the combustion chamber 111 from the nozzle part 121 of the burner 120 is ignited and burned by an ignition device, the combustion heat is transmitted to the furnace inner wall by radiation. The combustion gas G at a high temperature (about 1700 ° C. to 1900 ° C.) reaches the furnace inner wall surface of the front end face 110a, and reverses so as to lick the furnace inner wall surface and the furnace inner peripheral surface of the body 110b. While facing the opening 101b on the opposite side, the high-temperature combustion gas G transfers heat to the furnace wall and enters upward into the first smoke chamber 130 from the opening 101b.

また、図3に示すように、ノズル部121のノズル本体121aから前方のディフューザ122を通して噴霧された燃料は、着火により火炎を前方に吹き出すが、このとき、ファンネル部123内でその中心および周囲に渦流Uを発生させ、発生した渦流Uが火炎を整流化する作用を発揮する。これにより、高温の燃焼ガスGが真っ直ぐ前方の炉内壁面に直進し、反転して炉壁に熱を効率よく伝達する。   Further, as shown in FIG. 3, the fuel sprayed from the nozzle body 121a of the nozzle part 121 through the front diffuser 122 blows out a flame forward by ignition. At this time, in the funnel part 123, at the center and the periphery thereof. The vortex flow U is generated, and the generated vortex flow U exerts an effect of rectifying the flame. As a result, the high-temperature combustion gas G travels straight to the furnace inner wall straight ahead and reverses to efficiently transfer heat to the furnace wall.

第1煙室130内に上向きに入った高温の燃焼ガスGは、横向きの第1煙管群140に入り、各煙管141内を通り、その間、高温の燃焼ガスGが管壁に熱を伝達しながら、第2煙室160に向かう。ここで、上方の2台の送風機150,150からケーシング101内に取り入れられたハウス内空気と、煙管141の管壁および火炉110の炉壁に伝達された熱との間で熱交換が行われ、熱交換により生成された温風がケーシング101内を通り、下部の吐出室211内へ向かう。   The high-temperature combustion gas G that has entered the first smoke chamber 130 upward enters the horizontal first smoke tube group 140 and passes through each smoke tube 141, while the high-temperature combustion gas G transfers heat to the tube wall. However, it goes to the second smoke chamber 160. Here, heat exchange is performed between the air in the house taken into the casing 101 from the upper two blowers 150 and 150 and the heat transferred to the tube wall of the smoke tube 141 and the furnace wall of the furnace 110. The warm air generated by the heat exchange passes through the casing 101 and goes into the lower discharge chamber 211.

火炉110内の反転部112により反転される燃焼ガスGの熱伝達効果と、第1煙管部140内に配置されたスクリュー板142による燃焼ガスGの拡散および熱伝達効果により、第1煙管部140の出口における燃焼ガスG温度を約60℃程度低下させる効果(熱効率3〜4%向上)が生じる。   Due to the heat transfer effect of the combustion gas G reversed by the reversing unit 112 in the furnace 110 and the diffusion and heat transfer effect of the combustion gas G by the screw plate 142 disposed in the first smoke tube unit 140, the first smoke tube unit 140. The effect of reducing the combustion gas G temperature at the outlet of the gas by about 60 ° C. (thermal efficiency is improved by 3 to 4%) occurs.

第2煙室160に入った燃焼ガスGは、下向きに第2煙管群170に入り、各煙管171内を下向きに流れ、その間、燃焼ガスGの残留熱を管壁に伝達しながら、第3煙室180に向かう。ここで、下方の吐出室211へ向かう前述の温風、すなわち熱交換により生成された温風が、第2煙管群170で回収された熱との間で再び熱交換されて、さらに加温され、加温された温風が下方の吐出室211へ向かう。   The combustion gas G that has entered the second smoke chamber 160 enters the second smoke tube group 170 downward and flows downward in each smoke tube 171, while transferring the residual heat of the combustion gas G to the tube wall while Head to the smoke chamber 180. Here, the above-described warm air toward the lower discharge chamber 211, that is, warm air generated by heat exchange, is again heat-exchanged with the heat collected by the second smoke tube group 170, and further heated. The heated warm air goes to the discharge chamber 211 below.

第2煙管群170自身の排熱回収効果と、各煙管171内に配置されたスクリュー板172による燃焼ガスGの拡散および熱伝達効果により、第2煙管部170の出口における燃焼ガスG温度をさらに約100℃程度低下させる効果(熱効率5%向上)が生じる。   Due to the exhaust heat recovery effect of the second smoke tube group 170 itself and the diffusion and heat transfer effect of the combustion gas G by the screw plate 172 disposed in each smoke tube 171, the combustion gas G temperature at the outlet of the second smoke tube unit 170 is further increased. An effect of reducing the temperature by about 100 ° C. (thermal efficiency improved by 5%) is produced.

吐出室211に入った温風は、吐出口210aからダクトを通じてハウス内に配風されるが、従来では吐出温度差が通常5〜10℃程度あったが、吐出室211内の温風拡散板212の存在により吐出室211内の混合性能を上げ、吐出温度差を3℃以内に小さくすることができた。   The hot air that has entered the discharge chamber 211 is distributed into the house through the duct from the discharge port 210a. Conventionally, the discharge temperature difference is normally about 5 to 10 ° C. Due to the presence of 212, the mixing performance in the discharge chamber 211 was improved, and the discharge temperature difference could be reduced within 3 ° C.

第2煙管群170を下向きに流れる燃焼ガスGは、排熱回収により凡そ150℃程度の排気温度となって第3煙室180に入り、分散板181による分散効果によって、略均等な流れとなり、煙突190の入口に向かう。煙突190の入口に設けられた排ガス誘引器200による排ガス誘引効果により、排熱回収された燃焼ガスGは、煙突190内に滞留することなく、速やかに排気される。これによって安定したバーナ燃焼となり、燃焼ガスの伝熱、熱交換、排熱回収、排気という一連の流れがスムーズに行われる。   The combustion gas G flowing downward through the second smoke tube group 170 enters the third smoke chamber 180 at an exhaust temperature of about 150 ° C. by exhaust heat recovery, and becomes a substantially uniform flow due to the dispersion effect by the dispersion plate 181. Head to the chimney 190 entrance. Due to the exhaust gas attracting effect of the exhaust gas attractor 200 provided at the inlet of the chimney 190, the exhaust gas recovered combustion gas G is quickly exhausted without staying in the chimney 190. As a result, stable burner combustion is achieved, and a series of flows of heat transfer, heat exchange, exhaust heat recovery, and exhaust of the combustion gas are performed smoothly.

かくして、従来の温風暖房機の熱効率はせいぜい90%が限界であったのに対し、本実施形態の施設園芸用温風暖房機100によると、熱効率を95%まで高めることに成功した。   Thus, while the thermal efficiency of the conventional hot air heater was limited to 90% at most, the hot air heater 100 for horticulture in this embodiment succeeded in increasing the thermal efficiency to 95%.

本発明に係る施設園芸用温風暖房機は、施設園芸ハウス内を温風で暖房する温風暖房機として幅広く利用できる。   The warm air heater for facility horticulture according to the present invention can be widely used as a warm air heater for heating the inside of a facility horticulture house with warm air.

100 施設園芸用温風暖房機
101,205A,205B ケーシング
101a,205a 吸気口
101b,110c,212a 開口部
110 火炉
110a 端面
110b 胴部
111 燃焼室
112 反転部
120 バーナ
121 ノズル部
121a ノズル本体
121b 外筒
122 ディフューザ
123 ファンネル部
123a 拡径部
123b 環状部
123c 屈曲部
130 第1煙室
140 第1煙管群
141,171 煙管
142,172 スクリュー板
150 送風機
151,207 送風ファン
160 第2煙室
170 第2煙管群
180 第3煙室
181 分散板
190 煙突
200 排ガス誘引器(排ガス誘引手段)
201 第1筒体
201a,202a 縮径部
201b 水平部
202 第2筒体
202b 拡径部
203 噴出ノズル部
204 通風室
206 モータ
210 吐出部
211 吐出室
210a 吐出口
212 温風拡散板
220 制御部
,d 隙間
G 燃焼ガス
DESCRIPTION OF SYMBOLS 100 Facility gardening warm air heater 101,205A, 205B Casing 101a, 205a Inlet 101b, 110c, 212a Opening part 110 Furnace 110a End face 110b Body part 111 Combustion chamber 112 Reversing part 120 Burner 121 Nozzle part 121a Nozzle main body 121b Outer cylinder 122 diffuser 123 funnel part 123a enlarged diameter part 123b annular part 123c bent part 130 first smoke chamber 140 first smoke tube group 141,171 smoke tube 142,172 screw plate 150 blower 151,207 blower fan 160 second smoke chamber 170 second smoke tube Group 180 Third smoke chamber 181 Dispersing plate 190 Chimney 200 Exhaust gas attractor (exhaust gas attracting means)
201 1st cylinder 201a, 202a Diameter reduction part 201b Horizontal part 202 2nd cylinder 202b Diameter expansion part 203 Jet nozzle part 204 Ventilation chamber 206 Motor 210 Discharge part 211 Discharge room 210a Discharge port 212 Hot air diffusion plate 220 Control part d 1 , d 2 gap G Combustion gas

Claims (1)

ケーシングと、ケーシング内に横向きに配置され、ケーシングの全長に対し1/2を超える長さをもち、一端にバーナのノズル部を臨ませると共に、他端にノズル部の中心線を中心とする凹状の湾曲面からなり、燃焼ガスを炉内壁面に沿って反転させる反転部が形成された筒状の火炉と、反転された燃焼ガスを火炉の一端寄りからケーシング内で火炉外へ導出させる第1煙室と、第1煙室から火炉の他端側へ向けて燃焼ガスを案内する第1煙管群と、ケーシングの上面に取付けられ、下向きの送風により燃焼ガスとの間で熱交換を行わせる送風機と、ケーシング内で第1煙管群を流れる燃焼ガスを集合させる第2煙室と、ケーシング内で第2煙室から火炉の他端近くで下向きに燃焼ガスを案内する第2煙管群と、ケーシング内で第2煙管群を流れる燃焼ガスを集合させる第3煙室と、第3煙室から燃焼ガスをケーシング外へ排気させる煙突と、第3煙室と煙突の間または煙突の途中に燃焼ガスの排気を誘引する排気誘引手段を備え、バーナのノズル部が、ノズル本体の前方にディフューザを設け、ノズル本体を囲む外筒の先端にラッパ状のファンネル部を形成したことを特徴とする、施設園芸用温風暖房機。 A casing, which is disposed sideways in the casing, has a length exceeding 1/2 of the total length of the casing, has the nozzle portion of the burner facing one end, and has a concave shape centered on the center line of the nozzle portion at the other end of consists curved surface, a cylindrical furnace which reversed portions are formed to reverse along the combustion gas in the furnace wall, the first to derive an inverted combustion gas from near one end of the furnace to the furnace outside the casing and smoke chamber, a first tobacco pipe group for guiding the combustion gases toward the other end of the furnace from the first smoke box, mounted on the upper surface of the casing, to perform heat exchange between the combustion gas by the downward air blowing A blower, a second smoke chamber for collecting combustion gas flowing through the first smoke tube group in the casing, a second smoke tube group for guiding the combustion gas downward from the second smoke chamber near the other end of the furnace in the casing, In the casing the second stack A third smoke chamber to set the combustion gas, and a chimney to exhaust from the third smoke chamber combustion gas to the outside of the casing, the exhaust attraction to attract the exhaust of the combustion gas in the middle of or between chimney third smoke chamber and the chimney A hot air heater for horticultural horticulture, characterized in that a burner nozzle portion is provided with a diffuser in front of the nozzle body and a trumpet-shaped funnel portion is formed at the tip of an outer cylinder surrounding the nozzle body .
JP2010273240A 2010-12-08 2010-12-08 Hot air heater for horticulture Active JP5670166B2 (en)

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CN104566951A (en) * 2013-10-11 2015-04-29 宁夏琪凯节能设备有限公司 Novel energy-saving vertical fire tube boiler
CN105594456A (en) * 2016-01-29 2016-05-25 柳州市宣荣农业有限公司 Heating device for planting black fungi
CN106225231A (en) * 2016-07-23 2016-12-14 芜湖长启炉业有限公司 Hexahedro heat exchange air stove
CN106949448A (en) * 2017-05-09 2017-07-14 吉林省圣诺尔新能源科技股份有限公司 A kind of helical blade type flue tube boiler
CN107166489B (en) * 2017-07-18 2023-03-24 唐山精研实业有限责任公司 Small house type device for storing energy, heating, disinfecting and reducing PM2.5 by using off-peak electricity
CN108050693A (en) * 2017-12-04 2018-05-18 浙江武义万达干燥设备制造有限公司 fuel gas hot-blast stove
KR102159748B1 (en) * 2019-08-23 2020-09-24 권순성 Direct contact and pressureless type water heater

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JPS5926515U (en) * 1982-08-12 1984-02-18 富士工器株式会社 Hot air heater for greenhouse cultivation
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JPS61106749U (en) * 1984-12-14 1986-07-07
JPS63313529A (en) * 1987-06-15 1988-12-21 Showa Sangyo Kk Dehumidifying heating apparatus for greenhouse
JPS6441251U (en) * 1987-09-03 1989-03-13
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