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JP6137988B2 - Multi-pipe once-through boiler - Google Patents
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JP6137988B2 - Multi-pipe once-through boiler - Google Patents

Multi-pipe once-through boiler Download PDF

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JP6137988B2
JP6137988B2 JP2013166831A JP2013166831A JP6137988B2 JP 6137988 B2 JP6137988 B2 JP 6137988B2 JP 2013166831 A JP2013166831 A JP 2013166831A JP 2013166831 A JP2013166831 A JP 2013166831A JP 6137988 B2 JP6137988 B2 JP 6137988B2
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combustion
heat transfer
transfer tube
boiler
water
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JP2015034687A (en
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高島 博史
博史 高島
太希 菊池
太希 菊池
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株式会社サムソン
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Description

本発明は、垂直な伝熱管を環状に並べ、伝熱管列によって囲まれた中央部分を燃焼室としておき、燃焼室内で燃焼を行う燃焼装置によって伝熱管を加熱するようにしている多管式貫流ボイラに関するものである。より詳しくは、バーナは予混合ガスを伝熱管方向へ噴射して燃焼を行うものであって、伝熱管途中の高さ位置に設定している水位を保つように水位制御を行っている多管式貫流ボイラに関するものである。 The present invention relates to a multi-tube type once-through flow in which vertical heat transfer tubes are arranged in an annular shape, a central portion surrounded by the heat transfer tube rows is set as a combustion chamber, and the heat transfer tubes are heated by a combustion device that performs combustion in the combustion chamber. It relates to boilers. More specifically, the burner burns by injecting a premixed gas in the direction of the heat transfer tube, and the water level is controlled so as to keep the water level set at the height position in the middle of the heat transfer tube. It relates to a once-through boiler.

上部に環状の上部管寄せ、下部にも環状の下部管寄せを設けておき、上下の管寄せ間を多数の垂直な伝熱管で連結することで構成した缶体を持つ多管式貫流ボイラが広く普及している。このボイラでは、環状に並べた伝熱管列の中央部分が燃焼室となり、燃焼室上部に下向きのバーナを設置しておき、燃焼室内でバーナによる燃焼を行うことで、燃焼室を取り囲む伝熱管を加熱する。 An annular upper header and an annular lower header are provided at the top, and a multi-tube once-through boiler having a can body constructed by connecting the upper and lower headers with a number of vertical heat transfer tubes. Widely used. In this boiler, the central part of the heat transfer tube array arranged in a ring forms a combustion chamber, and a downward burner is installed in the upper part of the combustion chamber. Heat.

特開2006−183927号公報には、燃焼室内にバーナを設置しておき、伝熱管群の内周面に向けて予混合ガスを噴射するボイラの記載がある。特開2006−183927号公報に記載のボイラは、内側伝熱管群に近接して設けたバーナから略水平に(内側伝熱管群に対しては略垂直に)予混合ガスを噴射するものである。この状態で燃焼を行うと、内側伝熱管群に直接接触するような火炎が形成されることになる。このような構造にすると、火炎を伴うガスを即座に内側伝熱管群の内周面に衝突させるため、火炎等が効果的に冷却されて(火炎等の温度上昇を抑制するため)、NOxの生成量を低減することができるとされている。 Japanese Patent Application Laid-Open No. 2006-183927 describes a boiler in which a burner is installed in a combustion chamber and a premixed gas is injected toward the inner peripheral surface of a heat transfer tube group. The boiler described in Japanese Patent Laid-Open No. 2006-183927 ejects a premixed gas from a burner provided close to the inner heat transfer tube group substantially horizontally (substantially perpendicular to the inner heat transfer tube group). . When combustion is performed in this state, a flame that directly contacts the inner heat transfer tube group is formed. With such a structure, the flame accompanying gas is immediately collided with the inner peripheral surface of the inner heat transfer tube group, so that the flame is effectively cooled (in order to suppress the temperature rise of the flame, etc.) It is said that the production amount can be reduced.

ところで貫流ボイラは、一続きの流路を形成しておき、一方から供給した水を流しながら加熱し、他方から蒸気を取り出すものである。そして貫流ボイラでは、伝熱管内の途中に設定した高さ位置まで水を入れておき、バーナによる燃焼で伝熱管を加熱することで、伝熱管表面からの熱を伝熱管内の缶水に伝え、缶水温度を上昇させる。缶水は伝熱管内を上昇しながら加熱され、伝熱管内で沸騰温度まで上昇すると蒸気を発生する。伝熱管はバーナからの熱を受けると温度の上昇が発生するが、伝熱管内に缶水があるならば、伝熱管が吸収した熱は伝熱管内面に接触している缶水に移動するため、伝熱管温度はある程度までしか上昇しない。では、水位を伝熱管の途中に設定しておくと、水位位置より上方の伝熱管では伝熱管内面で接触してる缶水が存在しないことになる。そうなると、缶水による伝熱管の冷却が行えないということになり、上部の伝熱管では温度の上昇が継続し、伝熱管が過熱されてしまうということが考えられる。しかし実際は、伝熱管内では缶水の沸騰が発生しており、沸騰による沸き上がりによって缶水は設定水位よりも上部まで達している。そのため、水位より上方の伝熱管でも缶水に接触することになる。缶水の沸き上がりによって上部の伝熱管でも内面に缶水が存在することになれば過熱は発生しない。 By the way, the once-through boiler forms a continuous flow path, heats while supplying water supplied from one side, and extracts steam from the other side. And in the once-through boiler, water is put to the height position set in the middle of the heat transfer tube, and heat from the heat transfer tube surface is transferred to the can water in the heat transfer tube by heating the heat transfer tube by combustion with a burner. Increase the temperature of the can water. Can water is heated while rising in the heat transfer tube, and steam is generated when it rises to the boiling temperature in the heat transfer tube. When the heat transfer tube receives heat from the burner, the temperature rises, but if there is can water in the heat transfer tube, the heat absorbed by the heat transfer tube moves to the can water in contact with the inner surface of the heat transfer tube. The heat transfer tube temperature only rises to a certain extent. Then, if the water level is set in the middle of the heat transfer tube, the canned water that is in contact with the inner surface of the heat transfer tube does not exist in the heat transfer tube above the water level position. In this case, the heat transfer tube cannot be cooled with the can water, and the temperature of the upper heat transfer tube continues to rise, and the heat transfer tube may be overheated. However, in reality, boiling of the can water occurs in the heat transfer tube, and the can water reaches the upper part of the set water level due to the boiling due to the boiling. Therefore, even the heat transfer pipe above the water level comes into contact with the can water. Even if the upper part of the heat transfer tube has the can water on the inner surface due to the boiling of the can water, overheating does not occur.

逆に水位が高すぎた場合には、持ち上げられる缶水の量が多くなる。ボイラの蒸気出口には気水分離器を設けておき、蒸気と缶水は気水分離器で分離するようにしているが、気水分離器に達する缶水量が多くなると、気水分離器で缶水を分離しきれなくなり、分離できなかった缶水が蒸気に含まれることで蒸気の乾き度が低下することになる。そのため、貫流ボイラでは伝熱管途中に水位を設定しておき、適正な水位を維持することができるように、精密な水位制御を行っている。 Conversely, if the water level is too high, the amount of canned water that is lifted increases. A steam / water separator is installed at the steam outlet of the boiler, and steam and can water are separated by the steam / water separator, but when the amount of can water reaching the steam / water separator increases, Canned water cannot be separated, and steam that cannot be separated is contained in the steam, thereby reducing the dryness of the steam. Therefore, in the once-through boiler, the water level is set in the middle of the heat transfer tube, and precise water level control is performed so that the appropriate water level can be maintained.

ただし、燃焼を開始した直後の場合、燃焼装置による伝熱管の加熱は行われているが、缶水の沸き上がりはまだ発生していないため、設定水位より上方の伝熱管では沸き上がりの缶水による冷却が行われないということがある。その場合、設定水位より上方の伝熱管では温度が上昇し続けることになる。特に缶水が冷えている状態で燃焼を開始する冷缶起動時は、伝熱管内で缶水が沸騰するまでの時間が長くなってしまい、伝熱管上部の温度がより高くなることがあった。伝熱管が過熱されることによって、ゆがみが発生したり、接合部で断裂が発生することになると、ボイラは早期に交換しなければならなくなる。 However, in the case immediately after the start of combustion, the heat transfer tube is heated by the combustion device, but boiling of the can water has not yet occurred. There is a case that cooling by is not performed. In that case, the temperature continues to rise in the heat transfer tube above the set water level. In particular, when starting a cold can that starts burning when the can water is cold, the time until the can water boils in the heat transfer tube becomes longer, and the temperature at the top of the heat transfer tube may become higher. . If the heat transfer tube is overheated and distortion occurs or tearing occurs at the joint, the boiler must be replaced early.

特開2006−183927号公報JP 2006-183927 A

本発明が解決しようとする課題は、水位を伝熱管の途中に設定している多管式貫流ボイラにおいて、伝熱管の上部が過熱されることを防止することのできる多管式貫流ボイラを提供することにある。 The problem to be solved by the present invention is to provide a multi-tube once-through boiler that can prevent the upper portion of the heat transfer tube from being overheated in a multi-tube once-through boiler in which the water level is set in the middle of the heat transfer tube. There is to do.

請求項1に記載の発明は、垂直方向に長い多数の伝熱管を環状に配置した構造の缶体と、環状に配置した前記伝熱管列の中央部分に設ける燃焼室を持ち、前記燃焼室内の上部に燃焼装置を設け、燃焼装置による燃焼によって前記伝熱管内の缶水を加熱するようにしている多管式貫流ボイラにおいて、燃焼装置は多数の小孔を設けた筒状の燃焼部を持ち、燃焼部では前記小孔から予混合ガスを噴射することによって筒部外側表面で燃焼を行うものであり、燃焼部には下方ほど径を細くしていく円錐台形部と、円錐台形部の下方に設置した円筒形部を持っていることを特徴とする。 The invention according to claim 1 has a can body having a structure in which a large number of heat transfer tubes that are long in the vertical direction are annularly arranged, and a combustion chamber provided in a central portion of the annularly arranged heat transfer tube row, In a multi-tube once-through boiler in which a combustion device is provided at the top and the can water in the heat transfer tube is heated by combustion by the combustion device, the combustion device has a cylindrical combustion part provided with a large number of small holes. In the combustion part, the premixed gas is injected from the small holes to burn on the outer surface of the cylinder part. The combustion part has a truncated cone part with a diameter decreasing toward the lower part, and a lower part of the truncated cone part. It is characterized by having a cylindrical part installed in the.

請求項2に記載の発明は、前記の多管式貫流ボイラにおいて、円錐台形とした燃焼部の面に対して垂直方向へ延長線を延ばした場合、前記伝熱管と交差する箇所はボイラの設定水位よりも下方になるように配置していることを特徴とする。 According to the second aspect of the present invention, in the multitubular once-through boiler, when an extension line is extended in a direction perpendicular to the surface of the combustion section having a frustoconical shape, a location intersecting with the heat transfer tube is set in the boiler. It arrange | positions so that it may become below a water level, It is characterized by the above-mentioned.

バーナの燃焼部に下方ほど径を細くしていく円錐台形部を設けておくと、燃焼部から噴射している予混合ガスは、傾斜している円錐台形の面に対して垂直方向へ噴射することになるため、バーナの燃焼部から斜め下方に向けて火炎を発生することになる。火炎の燃焼によって発生する熱は、予混合ガスの噴射方向に流れるため、その延長線上にある伝熱管を加熱する。予混合ガスの噴射方向を斜め下方としておいた場合、バーナの燃焼部から伝熱管に達するまでの間に下方へと移動していくため、バーナ火炎が伝熱管を加熱することになる部分の高さ位置を低くすることができる。伝熱管内での缶水の沸き上がりが小さい場合であっても伝熱管での過熱を防止でき、バーナ火炎により加熱される部分が伝熱管の設定水位より低い位置となるようにしておくと、伝熱管の過熱は発生しなくなる。 If a frustoconical part with a diameter decreasing toward the lower part is provided in the combustion part of the burner, the premixed gas injected from the combustion part is injected in a direction perpendicular to the inclined frustoconical surface. Therefore, a flame is generated obliquely downward from the burning part of the burner. Since heat generated by the combustion of the flame flows in the injection direction of the premixed gas, the heat transfer tube on the extension line is heated. When the injection direction of the premixed gas is set obliquely downward, it moves downward from the burner combustion section until it reaches the heat transfer tube, so the burner flame heats the heat transfer tube. The position can be lowered. Even if the boiling water of the can in the heat transfer tube is small, overheating in the heat transfer tube can be prevented, and if the part heated by the burner flame is positioned lower than the set water level of the heat transfer tube, Heat transfer tube overheating no longer occurs.

また、燃焼部を円錐形にすると、先端側では燃焼を行う部分の面積は小さくなる。そして燃焼を行う面積が小さくなると、燃焼面負荷が大きくなって火炎がリフトするなどの影響が出る場合もあった。そこで、燃焼部の形状を途中までは下方ほど径を小さくした円錐台形とするが、その下方には円筒形の燃焼部を設けるようにしており、このことによって燃焼部の面積を確保している。そのために、燃焼面負荷が高くなり過ぎるといったことはなく、安定した燃焼状態を確保できる。なお、この部分はバーナの下端部分であり、燃焼を行う高さ位置が低いものであるため、傾斜を設けずともこの部分で発生した熱が加熱する伝熱管部分は低い位置となり、伝熱管の過熱は問題ない。 In addition, when the combustion part is conical, the area of the part that performs combustion is reduced on the tip side. If the area for combustion is reduced, the load on the combustion surface may increase and the flame may be lifted. Therefore, the shape of the combustion part is a truncated cone shape whose diameter is reduced toward the lower part, but a cylindrical combustion part is provided below the shape, thereby securing the area of the combustion part. . Therefore, the combustion surface load does not become too high, and a stable combustion state can be ensured. Since this part is the lower end part of the burner and the height position where combustion is performed is low, the heat transfer tube part that heats generated in this part is heated even if no inclination is provided, and the heat transfer tube Overheating is no problem.

蒸気負荷が小さく缶水の沸き上がりが小さい運転状態においても、バーナ火炎を設定水位より下方へ向けて形成するため、上部伝熱管が過熱されることを防止することができる。 Even in an operation state in which the steam load is small and the boiling of the can water is small, the burner flame is formed downward from the set water level, so that the upper heat transfer tube can be prevented from being overheated.

本発明の一実施例における多管式貫流ボイラの概要説明図Outline explanatory drawing of multi-tube type once-through boiler in one example of the present invention 図1のA−A断面図AA sectional view of FIG. 図1の燃焼装置部分の概要説明図Outline explanatory drawing of the combustion device portion of FIG.

本発明の一実施例を図面を用いて説明する。図1は本発明の一実施例における多管式貫流ボイラの概要説明図、図2は図1のA−A断面図、図3は図1の燃焼装置部分の概要説明図である。ボイラ1は上部に上部管寄せ2、下部に下部管寄せ3を設けている。上下の管寄せは、上部管寄せ2は下面、下部管寄せ3は上面が平らな断面半丸形であって、環状に形状している。上部管寄せ2と下部管寄せ3の間は、環状に並べた多数の垂直な伝熱管4で連結しておく。各伝熱管4は、間にわずかなすき間を開けて並べており、伝熱管4の間を燃焼ガスが抜け出ることができるようにしている。伝熱管列の外側には炉壁と断熱材層13を設け、炉壁の一部分には排ガス出口12の開口を設けており、排ガス出口12の先に排ガスを排出する煙突14を接続する。 An embodiment of the present invention will be described with reference to the drawings. FIG. 1 is a schematic explanatory diagram of a multi-tube once-through boiler according to an embodiment of the present invention, FIG. 2 is a cross-sectional view taken along line AA of FIG. 1, and FIG. The boiler 1 is provided with an upper header 2 at the top and a lower header 3 at the bottom. The upper and lower headers have a semicircular cross section with the upper header 2 having a lower surface and the lower header 3 having a flat upper surface, and are formed in an annular shape. The upper header 2 and the lower header 3 are connected by a large number of vertical heat transfer tubes 4 arranged in an annular shape. The heat transfer tubes 4 are arranged with a small gap between them so that the combustion gas can escape between the heat transfer tubes 4. A furnace wall and a heat insulating material layer 13 are provided outside the heat transfer tube row, an opening of the exhaust gas outlet 12 is provided in a part of the furnace wall, and a chimney 14 for discharging the exhaust gas is connected to the tip of the exhaust gas outlet 12.

ボイラ内への給水は下部管寄せ3から行う。下部管寄せ3の下方に給水配管を接続し、給水配管途中に設けている給水ポンプ(図示せず)を作動することによって下部管寄せ3へ給水を行う。下部管寄せ3には伝熱管4を多数接続しているため、下部管寄せ内に入った水は多数設けている伝熱管4へ分岐して上向きに流れる。ボイラの給水制御は、ボイラの缶体部分と上下で接続している水位検出装置10にて検出したボイラ内水位に基づいて行う。ボイラの運転時には、伝熱管4の途中に設定している所定水位を保つように給水ポンプの作動を制御する。水位検出装置10では、給水を開始する高さ位置と、給水を停止する高さ位置で水の有無を検出しておく。水位検出装置10にて検出している水位が、給水開始水位未満になると、給水ポンプの作動を行ってボイラへの給水を行い、給水を行うことでボイラ内水位が上昇し、検出水位が給水停止水位以上になると給水ポンプの作動を停止する。 Water supply to the boiler is performed from the lower header 3. A water supply pipe is connected below the lower header 3 and water is supplied to the lower header 3 by operating a water supply pump (not shown) provided in the middle of the water supply piping. Since a large number of heat transfer tubes 4 are connected to the lower header 3, the water that has entered the lower header is branched into a plurality of heat transfer tubes 4 and flows upward. Water supply control of the boiler is performed based on the water level in the boiler detected by the water level detection device 10 connected to the boiler body at the top and bottom. During the operation of the boiler, the operation of the feed water pump is controlled so as to maintain a predetermined water level set in the middle of the heat transfer tube 4. The water level detection device 10 detects the presence or absence of water at a height position where water supply is started and a height position where water supply is stopped. When the water level detected by the water level detection device 10 is lower than the water supply start water level, the water supply pump is operated to supply water to the boiler. By supplying water, the water level in the boiler rises, and the detected water level becomes the water supply When the water level is higher than the stop water level, the operation of the water supply pump is stopped.

ボイラ1の中心部分であって、環状に並べた伝熱管4によって囲まれる円柱状の空間が燃焼室6となり、燃焼室6の上部に燃焼装置5を設ける。燃焼装置5は、燃焼用空気を供給する送風機15、燃料ガスを供給する燃料供給部16、供給してきた燃焼用空気と燃料ガスを混合して予混合ガスとする混合室17、燃焼室内で燃焼を行う予混合バーナ7などからなる。 A cylindrical space, which is the central portion of the boiler 1 and surrounded by the heat transfer tubes 4 arranged in an annular shape, becomes the combustion chamber 6, and the combustion device 5 is provided above the combustion chamber 6. The combustion device 5 includes a blower 15 that supplies combustion air, a fuel supply unit 16 that supplies fuel gas, a mixing chamber 17 that mixes the supplied combustion air and fuel gas into a premixed gas, and combustion in the combustion chamber And a premix burner 7 for performing

予混合バーナ7は、先端部分に円筒形の燃焼部を持っている。燃焼部は、多数の小孔が開いた金属製の筒からなっており、予混合ガスを筒の小孔から外へ噴射し、筒の外表面付近で燃焼を行う。燃焼部には、先端側である下部燃焼域8と根本側である上部燃焼域9を分けて設定しておき、上部燃焼域9は先側を細くした円錐台形状とし、下部燃焼域8は径の変わらない円筒形状としている。この時、下部燃焼域8はボイラ運転時の設定水位よりも低い位置になるように、予混合バーナ7の下端部に設けておく。また、円錐台形とした部分は、燃焼部の面に対して垂直方向へ延長線を延ばした場合、前記伝熱管と交差する箇所はボイラの設定水位よりも下方になるように、傾斜の角度や上部燃焼域9の高さ位置を設定しておく。 The premix burner 7 has a cylindrical combustion portion at the tip. The combustion portion is made of a metal cylinder having a large number of small holes, and injects premixed gas from the small holes of the cylinder and burns near the outer surface of the cylinder. In the combustion part, a lower combustion zone 8 which is the tip side and an upper combustion zone 9 which is the base side are set separately, and the upper combustion zone 9 has a truncated cone shape with a tapered front side. It has a cylindrical shape whose diameter does not change. At this time, the lower combustion zone 8 is provided at the lower end of the premixing burner 7 so as to be at a position lower than the set water level during boiler operation. In addition, in the case where the truncated cone portion extends an extension line in a direction perpendicular to the surface of the combustion portion, the angle of inclination or the like so that the portion intersecting with the heat transfer tube is below the set water level of the boiler. The height position of the upper combustion zone 9 is set in advance.

ボイラの運転制御について説明する。ボイラで運転を開始する場合、まず水位検出装置10で検出している水位が給水停止水位よりも低い場合には、給水停止水位となるまで給水ポンプを作動し、水位を給水停止水位まで上昇させておく。ボイラでは、燃焼装置5による燃焼を開始する前に燃焼室6内を換気するプレパージを行う。燃料供給部16からの燃料供給は停止したままで、送風機15の作動を行うと、燃焼室内へは空気のみを供給することになり、燃焼室6内に未燃ガスが残っていたとしても未燃ガスは煙突14を通して排出される。ボイラ内水位が十分に高く、かつプレパージも終了すると、予混合バーナ7による燃焼を開始する。 The operation control of the boiler will be described. When starting operation with a boiler, when the water level detected by the water level detection device 10 is lower than the water supply stop water level, the water supply pump is operated until the water supply stop water level is reached, and the water level is raised to the water supply stop water level. Keep it. In the boiler, pre-purge for ventilating the inside of the combustion chamber 6 is performed before the combustion by the combustion device 5 is started. When the blower 15 is operated while the fuel supply from the fuel supply unit 16 is stopped, only air is supplied into the combustion chamber, and even if unburned gas remains in the combustion chamber 6, The fuel gas is exhausted through the chimney 14. When the water level in the boiler is sufficiently high and pre-purge is completed, combustion by the premix burner 7 is started.

予混合バーナ7での燃焼域部分にはパイロットバーナ(図示せず)を設けておき、パイロットバーナで発生させている火種を使用して燃焼を行う。パイロットバーナを燃焼させている状態で、上部燃焼域9及び下部燃焼域8の小孔から予混合ガスを噴射すると、パイロットバーナの火炎が上部燃焼域及び下部燃焼域8の表面で燃え広がり、燃焼域の全面で燃焼する。 A pilot burner (not shown) is provided in the combustion zone portion of the premixing burner 7, and combustion is performed using a fire type generated by the pilot burner. When the premixed gas is injected from the small holes of the upper combustion zone 9 and the lower combustion zone 8 while the pilot burner is burning, the flame of the pilot burner spreads on the surfaces of the upper combustion zone and the lower combustion zone 8, and the combustion zone Burns all over.

予混合バーナ7の燃焼部に達した予混合ガスは、上部燃焼域9及び下部燃焼域8から燃焼室6へ噴射するものであり、その際には上部燃焼域9と下部燃焼域8の燃焼面に対して垂直な方向へ予混合ガスを噴射する。予混合バーナ7での火炎は、上部燃焼域9及び下部燃焼域8の外側表面近くで発生し、高温の燃焼ガスは予混合ガス噴射方向の延長線上に流れていく。 The premixed gas that has reached the combustion section of the premix burner 7 is injected into the combustion chamber 6 from the upper combustion zone 9 and the lower combustion zone 8, and in this case, the combustion in the upper combustion zone 9 and the lower combustion zone 8 is performed. The premixed gas is injected in a direction perpendicular to the surface. The flame in the premix burner 7 is generated near the outer surfaces of the upper combustion zone 9 and the lower combustion zone 8, and the high-temperature combustion gas flows on an extension line in the premixed gas injection direction.

この場合、下部燃焼域8では垂直な燃焼面を持ち、予混合ガスの噴射方向は燃焼面に対して垂直になるために、水平方向へ予混合ガスを噴射する。この場合の火炎の熱は、伝熱管4の下部燃焼域8と同じ高さ位置部分を最初に加熱する。その後、燃焼ガスは燃焼室6に面している伝熱管4の表面に沿って流れながらさらに伝熱管4の加熱を行い、さらに伝熱管4のすき間を通して伝熱管列の外側へ流れ、外側からも伝熱管を加熱する。火炎の熱は、予混合バーナ7の燃焼面に近い部分で最も高くなっており、燃焼ガスが伝熱管4と接触しながら熱交換を行うことで温度を低下させていくものとなる。 In this case, since the lower combustion zone 8 has a vertical combustion surface and the injection direction of the premixed gas is perpendicular to the combustion surface, the premixed gas is injected in the horizontal direction. The heat of the flame in this case first heats the same height position portion as the lower combustion zone 8 of the heat transfer tube 4. Thereafter, the combustion gas further heats the heat transfer tube 4 while flowing along the surface of the heat transfer tube 4 facing the combustion chamber 6, and further flows to the outside of the heat transfer tube row through the gap of the heat transfer tube 4. Heat the heat transfer tube. The heat of the flame is highest at a portion near the combustion surface of the premix burner 7, and the temperature is lowered by exchanging heat while the combustion gas is in contact with the heat transfer tube 4.

そして上部燃焼域9は、下部燃焼域8よりも高い位置になるが、上部燃焼域9では下方ほど径が細くなる円錐台形状としており、上部燃焼域9から噴射する予混合ガスは傾斜している燃焼面に対して垂直になるため、斜め下方へ噴射することになる。この場合、上部燃焼域9で発生する火炎の熱は、伝熱管4までの距離を伝わる間に下方へ下がるため、バーナ火炎により加熱される伝熱管4の高さ位置は、予混合バーナ7の上部燃焼域9を設置している高さ位置よりも低い位置とできる。 The upper combustion zone 9 is positioned higher than the lower combustion zone 8, but the upper combustion zone 9 has a truncated cone shape whose diameter decreases toward the lower side, and the premixed gas injected from the upper combustion zone 9 is inclined. Since it is perpendicular to the burning surface, it is injected obliquely downward. In this case, since the heat of the flame generated in the upper combustion zone 9 falls downward while traveling the distance to the heat transfer tube 4, the height position of the heat transfer tube 4 heated by the burner flame is set at the height of the premix burner 7. The position can be lower than the height position where the upper combustion zone 9 is installed.

燃焼開始直後の場合には伝熱管4内での缶水の沸き上がりは少ないため、もしこの時に火炎による加熱部が伝熱管4の水位よりも高い位置にあると、内周面側で缶水に接触していない部分がバーナ火炎により加熱されることとなり、缶水による冷却が行われないということになると、伝熱管が過熱されることとなる。本実施例では、下部燃焼域8は伝熱管4の水位よりも低い位置としておき、下部燃焼域8からの火炎が最初に加熱する伝熱管の部分は、内周面側で缶水に接触している部分としておく。この部分では、内側にある缶水によって冷却されるために、伝熱管が過熱される問題はない。 Since the boiling of the can water in the heat transfer tube 4 is small immediately after the start of the combustion, if the heating part by the flame is at a position higher than the water level of the heat transfer tube 4 at this time, the can water is formed on the inner peripheral surface side. If the portion not in contact with the heater is heated by the burner flame and cooling with canned water is not performed, the heat transfer tube will be overheated. In the present embodiment, the lower combustion zone 8 is set at a position lower than the water level of the heat transfer tube 4, and the portion of the heat transfer tube heated by the flame from the lower combustion zone 8 first comes into contact with the can water on the inner peripheral surface side. Keep it as a part. In this part, since it is cooled by the inside can water, there is no problem that the heat transfer tube is overheated.

また、上下方向に長くなる燃焼域の全てを伝熱管内の設定水位よりも低い位置に設置しようとすると、予混合バーナ7の燃焼部は燃焼室6内に大きく入り込ませることが必要となり、予混合バーナの全長が長くなってしまう。バーナの全長が長くなるとバーナ取り外し時にはボイラの上方に大きなメンテスペースが必要になり、扱いづらいものとなる。そこで、上下に長い燃焼域の全てを設定水位よりも低い位置に設置することはせず、上部の燃焼域では、燃焼部を傾斜させることでバーナ火炎の形成方向を伝熱管内の設定水位よりも低くなるようにすることで、伝熱管4の上部が過熱されることがなくなる。 In addition, if it is attempted to install all of the combustion region that is long in the vertical direction at a position lower than the set water level in the heat transfer tube, the combustion portion of the premixing burner 7 needs to be largely inserted into the combustion chamber 6, The total length of the mixing burner becomes longer. If the overall length of the burner is long, a large maintenance space is required above the boiler when the burner is removed, which makes it difficult to handle. Therefore, do not install all of the upper and lower combustion zones at a position lower than the set water level, and in the upper combustion zone, tilt the combustion section to change the direction of formation of the burner flame from the set water level in the heat transfer tube. As a result, the upper portion of the heat transfer tube 4 is not overheated.

また、予混合バーナ7において燃焼部を先細り形状にすると、燃焼を行う部分の面積が小さくなる。燃焼量が同じで燃焼面積が小さくなると、単位面積当たりの燃焼負荷が増大することになり、予混合バーナ7では火炎のリフトなどが発生することがある。しかし本実施例では、燃焼面を先細り形状とするのは上部燃焼域9のみとし、上部燃焼域9の下方に円筒形の下部燃焼域8を設けることで燃焼面積は確保するようにしている。このことにより、燃焼面の面積を確保することができ、火炎にリフトが発生するなど不安定な燃焼状態を防止することができる。 In addition, when the combustion part is tapered in the premix burner 7, the area of the part that performs combustion is reduced. If the combustion amount is the same and the combustion area is reduced, the combustion load per unit area will increase, and the premix burner 7 may cause a flame lift or the like. However, in this embodiment, the combustion surface is tapered only in the upper combustion zone 9, and a cylindrical lower combustion zone 8 is provided below the upper combustion zone 9 to ensure the combustion area. As a result, the area of the combustion surface can be ensured, and an unstable combustion state such as the occurrence of lift in the flame can be prevented.

なお、本発明は以上説明した実施例に限定されるものではなく、多くの変形が本発明の技術的思想内で当分野において通常の知識を有する者により可能である。 The present invention is not limited to the embodiments described above, and many modifications can be made by those having ordinary knowledge in the art within the technical idea of the present invention.

1 ボイラ
2 上部管寄せ
3 下部管寄せ
4 伝熱管
5 燃焼装置
6 燃焼室
7 予混合バーナ
8 下部燃焼域
9 上部燃焼域
10 水位検出装置
11 気水分離器
12 排ガス出口
13 断熱材層
14 煙突
15 送風機
16 燃料供給部
17 混合室
1 boiler
2 Upper header
3 Lower header
4 Heat transfer tube 5 Combustion device
6 Combustion chamber 7 Premix burner 8 Lower combustion zone 9 Upper combustion zone 10 Water level detector 11 Steam / water separator 12 Exhaust gas outlet 13 Heat insulation material layer 14 Chimney
15 Blower 16 Fuel supply part 17 Mixing chamber

Claims (2)

垂直方向に長い多数の伝熱管を環状に配置した構造の缶体と、環状に配置した前記伝熱管列の中央部分に設ける燃焼室を持ち、前記燃焼室内の上部に燃焼装置を設け、燃焼装置による燃焼によって前記伝熱管内の缶水を加熱するようにしている多管式貫流ボイラにおいて、
燃焼装置は多数の小孔を設けた筒状の燃焼部を持ち、燃焼部では前記小孔から予混合ガスを噴射することによって筒部外側表面で燃焼を行うものであり、燃焼部は下方ほど径を細くしていく円錐台形部と、円錐台形部の下方に円筒形部を持っていることを特徴とする多管式貫流ボイラ。
A can having a structure in which a large number of heat transfer tubes that are long in the vertical direction are arranged in an annular shape, and a combustion chamber that is provided in a central portion of the heat transfer tube array that is arranged in an annular shape. In the multi-tube once-through boiler configured to heat the can water in the heat transfer tube by combustion by
The combustion device has a cylindrical combustion portion provided with a large number of small holes, and the combustion portion performs combustion on the outer surface of the cylindrical portion by injecting a premixed gas from the small holes. A multi-tube type once-through boiler characterized by having a truncated cone-shaped portion with a reduced diameter and a cylindrical portion below the truncated cone-shaped portion.
請求項1に記載の多管式貫流ボイラにおいて、円錐台形とした燃焼部の面に対して垂直方向へ延長線を延ばした場合、前記伝熱管と交差する箇所はボイラの設定水位よりも下方になるように配置していることを特徴とする多管式貫流ボイラ。


In the multi-tube type once-through boiler according to claim 1, when an extension line is extended in a direction perpendicular to the surface of the combustion part having a truncated cone shape, a portion intersecting with the heat transfer tube is below a set water level of the boiler. A multi-pipe once-through boiler, which is arranged to be


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