JP2005226954A - Fuel oil heating device - Google Patents
Fuel oil heating device Download PDFInfo
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- JP2005226954A JP2005226954A JP2004037922A JP2004037922A JP2005226954A JP 2005226954 A JP2005226954 A JP 2005226954A JP 2004037922 A JP2004037922 A JP 2004037922A JP 2004037922 A JP2004037922 A JP 2004037922A JP 2005226954 A JP2005226954 A JP 2005226954A
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Abstract
Description
本発明は、蒸気ボイラのバーナへ供給する燃料油を所定温度まで加熱し、燃焼に適した一定温度の状態で供給するための燃料油加熱装置に関するものである。 The present invention relates to a fuel oil heating apparatus for heating fuel oil supplied to a burner of a steam boiler to a predetermined temperature and supplying the fuel oil at a constant temperature suitable for combustion.
蒸気ボイラのバーナへ粘性の高い燃料油を供給するとき、従来の方法では燃料油供給配管中に電力により加熱を行うラインヒータ、自ボイラの蒸気により加熱を行う熱交換器を設置して、燃料油タンクから出る燃料油供給配管をオイルポンプ、ラインヒータ、熱交換器を通過して燃焼ノズル入口から再び前記燃料油タンクに戻る循環回路とし、これらのラインヒータおよび熱交換器を用いて燃料油を所定温度まで加熱し、供給する燃料油加熱装置がある。 When supplying highly viscous fuel oil to the burner of a steam boiler, the conventional method is to install a line heater that heats the fuel oil supply pipe with electric power and a heat exchanger that heats with the steam of its own boiler. The fuel oil supply pipe that exits from the oil tank is made into a circulation circuit that passes through the oil pump, the line heater, and the heat exchanger and returns to the fuel oil tank from the combustion nozzle inlet. The fuel oil is supplied using these line heater and heat exchanger. There is a fuel oil heating device that heats and supplies the fuel to a predetermined temperature.
ボイラの運転開始時は燃料油が所定温度まで加熱されておらず、またボイラの蒸気も発生していないため熱交換器を利用することができず、したがってラインヒータによる燃料油の加熱が行われることになる。 At the start of boiler operation, the fuel oil is not heated to a predetermined temperature, and no steam is generated in the boiler. Therefore, the heat exchanger cannot be used, so the fuel oil is heated by the line heater. It will be.
このとき、燃料油がラインヒータを一度通過するだけで所定温度まで加熱される場合、ボイラは運転開始後すぐに燃焼状態に移行できるが、複数回通過しなければ所定温度まで加熱されない場合、燃料油は再び燃料油タンクに循環するために、この燃料油タンクの燃料油を全て加熱しなければボイラは燃焼状態に移行することができず、運転開始から燃焼までに多くの時間が必要になる。 At this time, when the fuel oil is heated up to a predetermined temperature only by passing through the line heater once, the boiler can shift to the combustion state immediately after the start of operation, but if the fuel oil is not heated up to the predetermined temperature unless it passes a plurality of times, the fuel Since the oil circulates to the fuel oil tank again, the boiler cannot move to the combustion state unless all the fuel oil in the fuel oil tank is heated, and much time is required from the start of operation to combustion. .
ボイラが運転中に何らかの原因で熱交換器による燃料油の加熱が行われないか、あるいは不足するとき、ラインヒータは熱交換器の能力を補うために燃料油を所定温度まで加熱する。これらのように、ラインヒータが加熱動作をするときは電力を消費する。ランニングコスト削減の面から、このラインヒータの消費電力を必要最小限にすることが望ましい。 When the fuel oil is not heated by the heat exchanger for some reason during operation of the boiler, or is insufficient, the line heater heats the fuel oil to a predetermined temperature in order to supplement the capacity of the heat exchanger. As described above, when the line heater performs a heating operation, power is consumed. From the viewpoint of reducing running costs, it is desirable to minimize the power consumption of this line heater.
また、燃料油供給配管中にラインヒータが上流側、熱交換器が下流側に設置され、かつラインヒータ出口から熱交換器入口までの燃料油供給配管に距離がある場合、ボイラがコールドスタートのようなとき、ラインヒータで加熱された燃料油がラインヒータ出口から熱交換器入口までの燃料油供給配管、および蒸気の供給されていない熱交換器を通過する間に放熱によって温度降下が起こる。したがって、この温度降下を考慮して燃料油温度制御器の温度設定を行う必要がある。ここで、ラインヒータ出口から熱交換器入口までが非常に接近しており、加熱された燃料油がこれらの間の燃料油供給配管を通過する間の放熱が無視できるような場合は、ラインヒータ出口から熱交換器入口までの燃料油供給配管の放熱による温度降下は考慮しなくてよい。 Also, if the line heater is installed upstream and the heat exchanger is installed downstream in the fuel oil supply pipe, and the fuel oil supply pipe from the line heater outlet to the heat exchanger inlet has a distance, the boiler In such a case, the fuel oil heated by the line heater causes a temperature drop due to heat radiation while passing through the fuel oil supply piping from the line heater outlet to the heat exchanger inlet and the heat exchanger to which no steam is supplied. Therefore, it is necessary to set the temperature of the fuel oil temperature controller in consideration of this temperature drop. Here, when the line heater outlet is very close to the heat exchanger inlet, and the heat dissipation of the heated fuel oil passing through the fuel oil supply pipe between them is negligible, the line heater It is not necessary to consider the temperature drop due to heat radiation of the fuel oil supply pipe from the outlet to the heat exchanger inlet.
ボイラによって蒸気が発生し、熱交換器に蒸気が供給されると今度は熱交換器によって加熱が行われるため、ラインヒータで加熱後の温度降下を考慮した設定温度まで燃料油を加熱する必要がなくなる。したがってボイラの蒸気発生前後のような、これらの異なる状態によって温度設定値を変化させることができれば、ラインヒータの消費電力を必要最小限に抑えられることが考えられる。 When steam is generated by the boiler and steam is supplied to the heat exchanger, it is heated by the heat exchanger, so it is necessary to heat the fuel oil to a set temperature that takes into account the temperature drop after heating with the line heater. Disappear. Therefore, if the temperature set value can be changed according to these different states, such as before and after steam generation in the boiler, the power consumption of the line heater can be minimized.
熱交換器によって燃料油の加熱が行われている場合、燃料油供給配管の熱交換器より上流側の放熱による温度降下は考慮しなくてよく、また熱交換器からバーナまでの燃料油供給配管の温度降下についても、この部分の温度降下はラインヒータでの加熱および熱交換器での加熱とも同条件なので、ここでは説明を省略する。 When fuel oil is heated by a heat exchanger, the temperature drop due to heat dissipation upstream of the heat exchanger in the fuel oil supply pipe need not be considered, and the fuel oil supply pipe from the heat exchanger to the burner As for the temperature drop of this part, the temperature drop in this part is the same condition as the heating by the line heater and the heating by the heat exchanger, and therefore, the description is omitted here.
この他に、一般に燃料油に用いられる油類および含有水分は、温度が上昇すると体積が膨張し、すなわち密度が減少することが知られている。したがって、単位時間当り定体積移送方式の燃料ポンプを用いて燃料油供給を行う場合、燃料油の温度が上昇するにしたがって単位時間当りの燃焼量が低下することになり、このとき燃焼用送風機(図示省略)による空気量が燃料油の加熱温度に限らず一定であれば、相対的な空気過剰による燃焼が行われることになる。油温度が低下した場合は逆に密度が増加し、空気欠乏状態の燃焼になり、同時に燃料油の粘性も増加するため、燃料油の供給に不具合が生じる。このことから、燃料油は所定温度に対し一定温度で供給されることが要求される。
本発明は、前記背景技術における燃料油加熱装置において、ラインヒータの消費電力を必要最低限に抑えながら燃料油を所定温度まで加熱し、一定温度の状態で供給できる制御方法を提供することを課題とする。 It is an object of the present invention to provide a control method capable of heating a fuel oil to a predetermined temperature and supplying the fuel oil at a constant temperature while suppressing power consumption of the line heater to a necessary minimum in the fuel oil heating apparatus in the background art. And
以上の課題を解決するために請求項1に記載の発明は、オイルポンプ(3)によって燃料油供給配管(25)内を圧送される燃料油を、電力で加熱するラインヒータ(4)とボイラ(23)から送り出される蒸気の一部を燃料油加熱蒸気配管(19)により供給されて加熱する熱交換器(5)とを経てボイラ(23)のバーナ部(11)へ供給させる燃料油加熱装置において、燃料油供給配管(25)が燃料油の温度が燃焼に適した第一所定温度に上昇するまで該バーナ部(11)に供給された燃料油を少なくとも前記オイルポンプ(3)の入側に戻す循環路を有するように形成され、燃料油供給配管(25)の熱交換器(5)の出側に燃料油温度センサ(14)が、ボイラ(23)又は前記燃料油加熱蒸気配管(19)に蒸気温度を計測する蒸気温度センサ(15)が、前記燃料油加熱蒸気配管(19)にその蒸気流量を調整する流量調整弁(13)がそれぞれ設けられており、ボイラ(23)の始動開始前に燃料油供給配管(25)を循環する燃料油の温度が最初に前記第一所定温度まで上昇したことを燃料油温度センサ(14)が検出するまで燃料油の温度が第一所定温度に上昇したことを燃料油温度センサ(14)が検出すると駆動が停止される前記ラインヒータ(4)のみで燃料油を加熱し、燃料油の温度が最初に前記第一所定温度まで上昇したことを燃料油温度センサ(14)が検出すると前記バーナ部(11)を連続運転状態に駆動し、蒸気温度が規定温度以上になるまでに燃料油の温度が該第一所定温度より特定温度だけ低下したことを燃料油温度センサ(14)が検出するとラインヒータ(4)を再駆動させラインヒータ(4)のみで燃料油を加熱し、蒸気温度が規定温度以上になったことを蒸気温度センサ(15)が検出すると燃料油の温度が燃焼に適しているが第一所定温度より低い第二所定温度となるように流量調整弁(13)を作動させて熱交換器(5)のみで燃料油を加熱し、燃料油の温度が第二所定温度より特定温度だけ低下したことを燃料油温度センサ(14)が検出するとラインヒータ(4)を再駆動させ第二所定温度に達するとラインヒータ(4)を停止させる制御を行う燃料油温度制御器(16)が設けられていることを特徴とする燃料油加熱装置。 In order to solve the above-described problems, the invention according to claim 1 is directed to a line heater (4) and a boiler for heating fuel oil pumped by the oil pump (3) with fuel in the fuel oil supply pipe (25). Fuel oil heating for supplying a part of the steam sent out from (23) to the burner part (11) of the boiler (23) via the heat exchanger (5) supplied and heated by the fuel oil heating steam pipe (19) In the apparatus, at least the fuel oil supplied to the burner section (11) is supplied to the oil pump (3) until the fuel oil supply pipe (25) rises to a first predetermined temperature suitable for combustion. The fuel oil temperature sensor (14) is formed on the outlet side of the heat exchanger (5) of the fuel oil supply pipe (25), and is connected to the boiler (23) or the fuel oil heating steam pipe. (19) measure the steam temperature The steam temperature sensor (15) is provided with a flow rate adjusting valve (13) for adjusting the steam flow rate in the fuel oil heating steam pipe (19), and the fuel oil supply pipe before the start of the boiler (23). The fuel oil temperature rises to the first predetermined temperature until the fuel oil temperature sensor (14) detects that the temperature of the fuel oil circulating in (25) first rises to the first predetermined temperature. When the temperature sensor (14) detects that the fuel oil is heated only by the line heater (4) which is stopped driving, the fuel oil temperature sensor (14) indicates that the temperature of the fuel oil has first risen to the first predetermined temperature. ) Is detected, the burner section (11) is driven to a continuous operation state, and the fuel oil temperature sensor indicates that the temperature of the fuel oil has decreased by a specific temperature from the first predetermined temperature until the steam temperature becomes equal to or higher than the specified temperature. (14) When detected, the line heater (4) is re-driven, the fuel oil is heated only by the line heater (4), and when the steam temperature sensor (15) detects that the steam temperature has exceeded the specified temperature, the temperature of the fuel oil burns However, the flow rate adjustment valve (13) is operated so that the second predetermined temperature is lower than the first predetermined temperature, and the fuel oil is heated only by the heat exchanger (5). When the fuel oil temperature sensor (14) detects that the fuel oil temperature sensor (14) has decreased by a specific temperature from the predetermined temperature, the fuel oil temperature is controlled so that the line heater (4) is restarted and the line heater (4) is stopped when the second predetermined temperature is reached A fuel oil heating device provided with a controller (16).
請求項2に記載の発明は、請求項1に記載の燃料油加熱装置において、燃料油温度が制限温度未満に低下したことを燃料油温度センサ(14)が検出すると、燃料油温度制御器(16)がバーナ部(11)への燃料油の供給を停止させる制御を行うことを特徴とする。 When the fuel oil temperature sensor (14) detects that the fuel oil temperature has dropped below the limit temperature in the fuel oil heating device according to claim 1, the fuel oil temperature controller (14) 16) performs control to stop the supply of fuel oil to the burner section (11).
請求項3に記載の発明は、請求項1又は請求項2に記載の燃料油加熱装置において、燃料油が最初に第一所定温度まで上昇するとバーナ部(11)を連続運転状態に駆動させる燃料油温度制御器(16)の制御が、燃料油の温度が最初に第一所定温度まで上昇したことを燃料油温度センサ(14)が検出した際にバーナ部(11)に発せられる駆動信号による制御であることを特徴とする。 According to a third aspect of the present invention, in the fuel oil heating device according to the first or second aspect, when the fuel oil first rises to a first predetermined temperature, the fuel that drives the burner section (11) to a continuous operation state. The control of the oil temperature controller (16) is based on a drive signal issued to the burner unit (11) when the fuel oil temperature sensor (14) detects that the temperature of the fuel oil first rises to the first predetermined temperature. It is control.
請求項4に記載の発明は、請求項1又は請求項2に記載の燃料油加熱装置において、燃料油の温度が最初に第一所定温度まで上昇するとバーナ部(11)を連続運転状態に駆動させる燃料油温度制御器(16)の制御が、燃料油の温度が最初に第一所定温度まで上昇したことを燃料油温度センサ(14)が検出した際にバーナ部(11)へ供給される燃料油の圧力をバーナ部(11)の自動噴射圧力に上昇させるために燃料油供給配管(25)のバーナ部(11)からの循環路に設けられた第一電磁弁(7)に発せられる閉鎖信号による制御であることを特徴とする。 According to a fourth aspect of the present invention, in the fuel oil heating device according to the first or second aspect, when the temperature of the fuel oil first rises to a first predetermined temperature, the burner unit (11) is driven to a continuous operation state. When the fuel oil temperature sensor (14) detects that the temperature of the fuel oil first rises to the first predetermined temperature, the control of the fuel oil temperature controller (16) is supplied to the burner section (11). In order to raise the pressure of the fuel oil to the automatic injection pressure of the burner part (11), it is emitted to the first solenoid valve (7) provided in the circulation path from the burner part (11) of the fuel oil supply pipe (25). The control is based on a closing signal.
請求項5に記載の発明は、請求項1から4に記載の燃料油加熱装置において、燃料油の温度が燃焼に適した第一所定温度に上昇するまでバーナ部(11)に供給された燃料油の燃料油供給配管(25)の循環路の入口上流にオイルポンプ(3)と連動する燃料供給弁(26)が設けられ、該燃料油供給配管(25)の循環路の少なくとも前記オイルポンプ(3)の入側が、燃料油を所定量貯留させておくオイルポンプ(3)へと燃料油を供給するためのベッセル(1)であることを特徴とする。 According to a fifth aspect of the present invention, in the fuel oil heating apparatus according to the first to fourth aspects, the fuel supplied to the burner section (11) until the temperature of the fuel oil rises to a first predetermined temperature suitable for combustion. A fuel supply valve (26) interlocking with the oil pump (3) is provided upstream of the inlet of the circulation path of the fuel oil supply pipe (25), and at least the oil pump in the circulation path of the fuel oil supply pipe (25) The entry side of (3) is a vessel (1) for supplying fuel oil to an oil pump (3) for storing a predetermined amount of fuel oil.
請求項1に記載の発明によれば、オイルポンプ(3)によって燃料油供給配管(25)内を圧送される燃料油を、電力で加熱するラインヒータ(4)とボイラ(23)から送り出される蒸気の一部を燃料油加熱蒸気配管(19)により供給されて加熱する熱交換器(5)とを経てボイラ(23)のバーナ部(11)へ供給させる燃料油加熱装置において、燃料油供給配管(25)が燃料油の温度が燃焼に適した第一所定温度に上昇するまでバーナ部(11)に供給された燃料油を少なくとも前記オイルポンプ(3)の入側に戻す循環路を有するように形成され、燃料油供給配管(25)の熱交換器(5)の出側に燃料油温度センサ(14)が、ボイラ(23)又は前記燃料油加熱蒸気配管(19)に蒸気温度を計測する蒸気温度センサ(15)が、前記燃料油加熱蒸気配管(19)にその蒸気流量を調整する流量調整弁(13)がそれぞれ設けられており、ボイラ(23)の始動開始前に燃料油供給配管(25)を循環する燃料油の温度が最初に前記第一所定温度まで上昇したことを燃料油温度センサ(14)が検出するまで燃料油の温度が第一所定温度に上昇したことを燃料油温度センサ(14)が検出すると駆動が停止される前記ラインヒータ(4)のみで燃料油を加熱し、燃料油の温度が最初に前記第一所定温度まで上昇したことを該燃料油温度センサ(14)が検出すると前記バーナ部(11)を連続運転状態に駆動し、蒸気温度が規定温度以上になるまでに燃料油の温度が第一所定温度より特定温度だけ低下したことを燃料油温度センサ(14)が検出するとラインヒータ(4)を再駆動させラインヒータ(4)のみで燃料油を加熱し、蒸気温度が規定温度以上になったことを該蒸気温度センサ(15)が検出すると燃料油の温度が燃焼に適しているが第一所定温度より低い第二所定温度となるように流量調整弁(13)を作動させて熱交換器(5)のみで燃料油を加熱し、燃料油の温度が第二所定温度より特定温度だけ低下したことを燃料油温度センサ(14)が検出するとラインヒータ(4)を再駆動させ第二所定温度に達するとラインヒータ(4)を停止させる制御を行う燃料油温度制御器(16)が設けられている燃料油加熱装置を用いることにより、粘性の高い燃料油をボイラ(23)の前記バーナ部(11)へ燃焼に適した一定の温度で供給することができ、またラインヒータ(4)の消費電力を必要最小限に抑えることができる。 According to the first aspect of the present invention, the fuel oil pressure-fed in the fuel oil supply pipe (25) by the oil pump (3) is sent out from the line heater (4) and the boiler (23) for heating with electric power. In the fuel oil heating apparatus for supplying a part of the steam to the burner part (11) of the boiler (23) through the heat exchanger (5) supplied and heated by the fuel oil heating steam pipe (19), the fuel oil supply The pipe (25) has a circulation path for returning the fuel oil supplied to the burner section (11) to at least the inlet side of the oil pump (3) until the temperature of the fuel oil rises to a first predetermined temperature suitable for combustion. The fuel oil temperature sensor (14) is formed on the outlet side of the heat exchanger (5) of the fuel oil supply pipe (25), and the steam temperature is supplied to the boiler (23) or the fuel oil heating steam pipe (19). Steam temperature sensor to measure (15 However, the fuel oil heating steam pipe (19) is provided with a flow rate adjusting valve (13) for adjusting the steam flow rate, and circulates through the fuel oil supply pipe (25) before starting the boiler (23). The fuel oil temperature sensor (14) indicates that the temperature of the fuel oil has increased to the first predetermined temperature until the fuel oil temperature sensor (14) detects that the temperature of the fuel oil has first increased to the first predetermined temperature. When the fuel oil temperature sensor (14) detects that the fuel oil is heated only by the line heater (4), which is stopped when detected, and the temperature of the fuel oil first rises to the first predetermined temperature, the fuel oil is detected. When the fuel oil temperature sensor (14) detects that the temperature of the fuel oil has decreased by a specific temperature from the first predetermined temperature before the burner portion (11) is driven to a continuous operation state and the steam temperature becomes equal to or higher than the specified temperature. Rheinhe (4) is driven again, the fuel oil is heated only by the line heater (4), and when the steam temperature sensor (15) detects that the steam temperature has exceeded the specified temperature, the temperature of the fuel oil is suitable for combustion. However, the flow rate adjusting valve (13) is operated so that the second predetermined temperature is lower than the first predetermined temperature, and the fuel oil is heated only by the heat exchanger (5), and the temperature of the fuel oil is lower than the second predetermined temperature. When the fuel oil temperature sensor (14) detects that the temperature has decreased by a specific temperature, the fuel oil temperature controller (14) performs control to restart the line heater (4) and stop the line heater (4) when the second predetermined temperature is reached. 16), a highly viscous fuel oil can be supplied to the burner part (11) of the boiler (23) at a constant temperature suitable for combustion. Requires power consumption of heater (4) It can be minimized.
請求項2に記載の発明によれば、請求項1に記載の燃料油加熱装置において、燃料油温度が制限温度未満に低下したことを燃料油温度センサ(14)が検出すると、燃料油温度制御器(16)がバーナ部(11)への燃料油の供給を停止させる制御を行うことにより、バーナ(21)における空気欠乏状態の燃焼を防ぐことができる。 According to the invention of claim 2, in the fuel oil heating device of claim 1, when the fuel oil temperature sensor (14) detects that the fuel oil temperature has dropped below the limit temperature, the fuel oil temperature control By performing control that stops the supply of fuel oil to the burner section (11) by the vessel (16), combustion in an air-deficient state in the burner (21) can be prevented.
請求項3に記載の発明によれば、請求項1又は請求項2に記載の燃料油加熱装置において、燃料油が最初に第一所定温度まで上昇するとバーナ部(11)を連続運転状態に駆動させる燃料油温度制御器(16)の制御が、燃料油の温度が最初に第一所定温度まで上昇したことを燃料油温度センサ(14)が検出した際にバーナ部(11)に発せられる駆動信号による制御であることにより、燃焼に適した燃料油を前記バーナ部(11)へ供給することができ、バーナ(21)において安定した燃焼を行うことができる。
According to the invention described in
請求項4に記載の発明によれば、請求項1又は請求項2に記載の燃料油加熱装置において、燃料油の温度が最初に第一所定温度まで上昇するとバーナ部(11)を連続運転状態に駆動させる燃料油温度制御器(16)の制御が、燃料油の温度が最初に第一所定温度まで上昇したことを燃料油温度センサ(14)が検出した際にバーナ部(11)へ供給される燃料油の圧力をバーナ部(11)の自動噴射圧力に上昇させるために燃料油供給配管(25)のバーナ部(11)からの循環路に設けられた第一電磁弁(7)に発せられる閉鎖信号による制御であることにより、燃料油が第一所定温度未満の燃料油供給配管(25)中を循環する燃料油加熱状態から、第一所定温度まで上昇して燃料油をバーナ部(11)へ供給する連続運転状態に効率よく移行することができる。 According to the fourth aspect of the present invention, in the fuel oil heating device according to the first or second aspect, when the temperature of the fuel oil first rises to the first predetermined temperature, the burner unit (11) is continuously operated. Is supplied to the burner unit (11) when the fuel oil temperature sensor (14) detects that the temperature of the fuel oil first rises to the first predetermined temperature. The first solenoid valve (7) provided in the circulation path from the burner portion (11) of the fuel oil supply pipe (25) in order to increase the pressure of the fuel oil to be increased to the automatic injection pressure of the burner portion (11). Due to the control by the closed signal that is emitted, the fuel oil rises from the fuel oil heating state in which the fuel oil circulates in the fuel oil supply pipe (25) below the first predetermined temperature to the first predetermined temperature, and the fuel oil is burned. Efficient in continuous operation state supplied to (11) It is possible to Ku transition.
請求項5に記載の発明は、請求項1から4に記載の燃料油加熱装置において、燃料油の温度が燃焼に適した第一所定温度に上昇するまでバーナ部(11)に供給された燃料油の燃料油供給配管(25)の循環路の入口上流にオイルポンプ(3)と連動する燃料供給弁(26)が設けられ、燃料油供給配管(25)の循環路の少なくとも前記オイルポンプ(3)の入側が、燃料油を所定量貯留させておくオイルポンプ(3)へと燃料油を供給するためのベッセル(1)であることにより、燃料油加熱中またはボイラ(23)の運転停止後の余熱によってボイラ(23)の該燃料油供給配管(25)中に発生する燃料油の体積膨張を吸収することができる。 According to a fifth aspect of the present invention, in the fuel oil heating apparatus according to the first to fourth aspects, the fuel supplied to the burner section (11) until the temperature of the fuel oil rises to a first predetermined temperature suitable for combustion. A fuel supply valve (26) interlocking with the oil pump (3) is provided upstream of the inlet of the circulation path of the fuel oil supply pipe (25), and at least the oil pump ( 3) The entry side of 3) is a vessel (1) for supplying fuel oil to an oil pump (3) for storing a predetermined amount of fuel oil, so that fuel oil is being heated or the boiler (23) is shut down. The volume expansion of the fuel oil generated in the fuel oil supply pipe (25) of the boiler (23) can be absorbed by the residual heat afterwards.
以下、本発明の燃料油加熱装置の実施例を図面に基づいて詳細に説明する。 Hereinafter, embodiments of the fuel oil heating device of the present invention will be described in detail with reference to the drawings.
図1に記載された本発明の燃料油加熱装置は、オイルポンプ(3)によって燃料油供給配管(25)内を圧送される燃料油を、電力で加熱するラインヒータ(4)とボイラ(23)から送り出される蒸気の一部を燃料油加熱蒸気配管(19)により供給されて加熱する熱交換器(5)とを経てボイラ(23)のバーナ部(11)へ供給させる燃料油加熱装置において、燃料油供給配管(25)が燃料油の温度が燃焼に適した第一所定温度に上昇するまでバーナ部(11)に供給された燃料油を少なくとも前記オイルポンプ(3)の入側に戻す循環路を有するように形成され、燃料油供給配管(25)の熱交換器(5)の出側に燃料油温度センサ(14)が、ボイラ(23)又は前記燃料油加熱蒸気配管(19)に蒸気温度を計測する蒸気温度センサ(15)が、前記燃料油加熱蒸気配管(19)にその蒸気流量を調整する流量調整弁(13)がそれぞれ設けられており、ボイラ(23)の始動開始前に燃料油供給配管(25)を循環する燃料油の温度が最初に前記第一所定温度まで上昇したことを燃料油温度センサ(14)が検出するまで燃料油の温度が第一所定温度に上昇したことを燃料油温度センサ(14)が検出すると駆動が停止される前記ラインヒータ(4)のみで燃料油を加熱し、燃料油の温度が最初に前記第一所定温度まで上昇したことを燃料油温度センサ(14)が検出すると前記バーナ部(11)を連続運転状態に駆動し、蒸気温度が規定温度以上になるまでに燃料油の温度が第一所定温度より特定温度だけ低下したことを燃料油温度センサ(14)が検出するとラインヒータ(4)を再駆動させラインヒータ(4)のみで燃料油を加熱し、蒸気温度が規定温度以上になったことを蒸気温度センサ(15)が検出すると燃料油の温度が燃焼に適しているが第一所定温度より低い第二所定温度となるように流量調整弁(13)を作動させて熱交換器(5)のみで燃料油を加熱し、燃料油の温度が第二所定温度より特定温度だけ低下したことを燃料油温度センサ(14)が検出するとラインヒータ(4)を再駆動させ第二所定温度に達するとラインヒータ(4)を停止させる制御を行う燃料油温度制御器(16)が設けられている。 The fuel oil heating apparatus of the present invention shown in FIG. 1 includes a line heater (4) and a boiler (23 that heats the fuel oil pumped by the oil pump (3) through the fuel oil supply pipe (25) with electric power. In the fuel oil heating apparatus for supplying a part of the steam sent out from the fuel oil heating steam pipe (19) to the burner section (11) of the boiler (23) via the heat exchanger (5) for heating. The fuel oil supply pipe (25) returns at least the fuel oil supplied to the burner section (11) to the inlet side of the oil pump (3) until the temperature of the fuel oil rises to a first predetermined temperature suitable for combustion. A fuel oil temperature sensor (14) is formed on the outlet side of the heat exchanger (5) of the fuel oil supply pipe (25), and is connected to the boiler (23) or the fuel oil heating steam pipe (19). Steam temperature sensor for measuring steam temperature The sensor (15) is provided with a flow rate adjusting valve (13) for adjusting the steam flow rate in the fuel oil heating steam pipe (19), and before the start of the boiler (23), the fuel oil supply pipe (25 The fuel oil temperature sensor indicates that the temperature of the fuel oil has increased to the first predetermined temperature until the fuel oil temperature sensor (14) detects that the temperature of the fuel oil circulating through the first gas temperature has increased to the first predetermined temperature. When the fuel oil is heated only by the line heater (4) whose driving is stopped when (14) is detected, the fuel oil temperature sensor (14) indicates that the temperature of the fuel oil first rises to the first predetermined temperature. When detected, the burner unit (11) is driven to a continuous operation state, and the fuel oil temperature sensor (14) indicates that the temperature of the fuel oil has decreased by a specific temperature from the first predetermined temperature before the steam temperature becomes equal to or higher than the specified temperature. When detected When the steam temperature sensor (15) detects that the steam temperature has exceeded the specified temperature by re-driving the heater (4) and heating the fuel oil only with the line heater (4), the temperature of the fuel oil is suitable for combustion. However, the flow rate adjusting valve (13) is operated so that the second predetermined temperature is lower than the first predetermined temperature, and the fuel oil is heated only by the heat exchanger (5), and the temperature of the fuel oil is lower than the second predetermined temperature. When the fuel oil temperature sensor (14) detects that the temperature has decreased by a specific temperature, the fuel oil temperature controller (14) performs control to restart the line heater (4) and stop the line heater (4) when the second predetermined temperature is reached. 16).
前記燃料油加熱装置において、ボイラ(23)はバーナ(21)の燃焼熱により蒸気を発生させる構造を持つ。発生した蒸気は、気水分離器(22)中で蒸発しきれなかった液体分と分けられ、主蒸気弁(12)を通過して蒸気の使用先へ供給される。このとき、ボイラ(23)は大気圧以上の圧力の蒸気を発生させることができる構造を持つため、通常大気圧中では100℃の蒸気しか得られないが、この場合例えばボイラ(23)内の絶対圧力が0.2MPaのときは、約120℃の蒸気を得ることができる。 In the fuel oil heating apparatus, the boiler (23) has a structure for generating steam by the combustion heat of the burner (21). The generated steam is separated from the liquid component that could not be evaporated in the steam separator (22), passes through the main steam valve (12), and is supplied to the use destination of the steam. At this time, since the boiler (23) has a structure capable of generating steam at a pressure higher than atmospheric pressure, normally only steam at 100 ° C. can be obtained at atmospheric pressure. In this case, for example, in the boiler (23) When the absolute pressure is 0.2 MPa, steam at about 120 ° C. can be obtained.
燃料油温度制御器(16)は、ラインヒータ(4)および熱交換器(5)の燃料油加熱温度を設定する機器であり、蒸気温度センサ(15)によって検出されるボイラ(23)の蒸気の温度を、蒸気温度検出器(17)を経由してこの燃料油温度制御器(16)に入力し、蒸気の規定温度によって2通りの燃料油の加熱設定温度SP0、SP1およびVP0、VP1を切替えて、燃料油温度センサ(14)で検出される燃料油加熱温度によってラインヒータ(4)への駆動信号を、同じく燃料油温度センサ(14)で検出された燃料油の温度変化を解析しながら燃料油の加熱設定温度に対して0%から100%に割振った信号を熱交換器(5)へボイラ(23)の蒸気を供給する流量調整弁(13)への作動信号を発信することができる機能を持つ。 The fuel oil temperature controller (16) is a device for setting the fuel oil heating temperature of the line heater (4) and the heat exchanger (5), and the steam of the boiler (23) detected by the steam temperature sensor (15). Is input to the fuel oil temperature controller (16) via the steam temperature detector (17), and two fuel oil heating set temperatures SP0, SP1 and VP0, VP1 are set according to the specified temperature of the steam. By switching, the drive signal to the line heater (4) is analyzed by the fuel oil heating temperature detected by the fuel oil temperature sensor (14), and the temperature change of the fuel oil detected by the fuel oil temperature sensor (14) is also analyzed. However, an operation signal to the flow rate adjusting valve (13) for supplying the steam of the boiler (23) to the heat exchanger (5) is transmitted to the heat exchanger (5) with a signal allocated from 0% to 100% with respect to the heating temperature of the fuel oil. Function that can With.
ラインヒータ(4)は、燃料油温度センサ(14)で検出された燃料油の温度によって、燃料油温度制御器(16)からの信号で駆動が行われるものである。熱交換器(5)はボイラ(23)で発生した蒸気の熱を燃料油へ熱交換するものであり、同じく燃料油温度センサ(14)で検出された燃料油の温度変化を燃料油温度制御器(16)が解析しながら、燃料油の加熱設定温度に対して0%から100%に割振って発信される作動信号で流量調節弁(13)が比例的に開閉され、この開閉度による蒸気の供給量の制御によって燃料油の加熱制御が行われるものである。 The line heater (4) is driven by a signal from the fuel oil temperature controller (16) according to the temperature of the fuel oil detected by the fuel oil temperature sensor (14). The heat exchanger (5) exchanges the heat of the steam generated in the boiler (23) with fuel oil, and also controls the temperature change of the fuel oil detected by the fuel oil temperature sensor (14). The flow rate control valve (13) is proportionally opened / closed by an operation signal transmitted by allocating from 0% to 100% with respect to the set heating temperature of the fuel oil while being analyzed by the vessel (16). The heating control of the fuel oil is performed by controlling the supply amount of the steam.
流量調節弁(13)は、燃料油温度センサ(14)で検出される燃料油の加熱温度によってラインヒータ(4)を駆動させるように全開状態または全閉状態で作動させることで燃料油の加熱制御を行うことも可能であるが、前記のような作動方法によって加熱設定温度に対してより安定な燃料油の加熱制御を行うことができる。 The flow rate control valve (13) heats the fuel oil by operating in the fully open state or the fully closed state so as to drive the line heater (4) according to the heating temperature of the fuel oil detected by the fuel oil temperature sensor (14). Although it is possible to perform control, it is possible to perform more stable fuel oil heating control with respect to the heating set temperature by the operation method as described above.
ボイラ(23)が始動すると、オイルポンプ(3)によって燃料油供給配管(25)内を圧送される燃料油は、供給過程でラインヒータ(4)および熱交換器(5)で第一所定温度まで加熱される。燃料油温度センサ(14)において検出される燃料油の加熱温度が第一所定温度未満の場合、バーナ(21)は燃焼動作に入らず燃料油は燃料供給配管(25)を循環しながら第一所定温度まで加熱される。そして、燃料油温度センサ(14)によって燃料油が第一所定温度以上まで加熱されたことを検出すると、燃料油温度制御器(16)からバーナ(21)へ駆動信号が発せられて燃焼動作に移行する。バーナ(21)が燃焼動作に移行すると燃料油温度制御器(16)から第一電磁弁(7)に閉鎖信号が発信され、これにより第一電磁弁(7)が閉じる。バーナ部(11)中の燃料油回路がオイルポンプ(3)の燃料油圧送圧力によって循環路側から燃焼側に切替わり、低燃焼側ノズル(9)より加熱された燃料油が噴霧され、バーナ(21)の着火動作によって低燃焼が行われる。そして、蒸気の使用先で負荷が高くなることによってさらに多くの蒸気が要求されれば、燃料油温度制御器(16)から第二電磁弁(8)に開放信号が発信され、これにより第二電磁弁(8)が開き、高燃焼側ノズル(10)から燃料油が噴霧され、高燃焼が行われる。 When the boiler (23) is started, the fuel oil pressure-fed through the fuel oil supply pipe (25) by the oil pump (3) is supplied to the first predetermined temperature by the line heater (4) and the heat exchanger (5). Until heated. When the heating temperature of the fuel oil detected by the fuel oil temperature sensor (14) is lower than the first predetermined temperature, the burner (21) does not enter the combustion operation and the fuel oil circulates through the fuel supply pipe (25). Heated to a predetermined temperature. When the fuel oil temperature sensor (14) detects that the fuel oil has been heated to the first predetermined temperature or higher, a drive signal is issued from the fuel oil temperature controller (16) to the burner (21), and the combustion operation is started. Transition. When the burner (21) shifts to the combustion operation, a closing signal is transmitted from the fuel oil temperature controller (16) to the first electromagnetic valve (7), thereby closing the first electromagnetic valve (7). The fuel oil circuit in the burner section (11) is switched from the circulation path side to the combustion side by the fuel hydraulic pressure feed pressure of the oil pump (3), and the fuel oil heated from the low combustion side nozzle (9) is sprayed and burner ( The low combustion is performed by the ignition operation of 21). Then, if more steam is required due to an increase in the load at the place where the steam is used, an open signal is transmitted from the fuel oil temperature controller (16) to the second solenoid valve (8). The solenoid valve (8) is opened, fuel oil is sprayed from the high combustion side nozzle (10), and high combustion is performed.
本実施例で説明されているものは、燃焼方式が「停止−低燃焼−高燃焼」の燃料油供給回路であるが、前記のような燃料油加熱のための循環路が形成されていれば、燃焼方式が「停止−燃焼」の燃料油回路でも同様の効果が得られる。 What is described in the present embodiment is a fuel oil supply circuit whose combustion method is “stop-low combustion-high combustion”, but if a circulation path for heating the fuel oil as described above is formed. The same effect can be obtained even in a fuel oil circuit whose combustion mode is “stop-combustion”.
図3はボイラ(23)で発生し、蒸気温度センサ(15)で検出される蒸気温度をTVとし、また規定温度を100℃とした場合において、(ア)は蒸気温度TVが100℃未満のとき、(イ)は同じく蒸気温度TVが100℃以上のときのラインヒータ(4)の駆動状況および燃料油温度センサ(14)で検出される燃料油加熱温度に対する流量調節弁(13)の比例開閉による熱交換器(5)への蒸気供給割合を示している。そして、これら(ア)、(イ)の2通りの燃料油加熱設定温度SP0からSP1およびVP0からVP1またはその逆への切替えが、蒸気温度センサ(15)で検出されるボイラ(23)の蒸気温度の変化により、蒸気温度検出器(17)から出力される信号を受けて燃料油温度制御器(16)によって行われる。 FIG. 3 shows that when steam temperature generated by the boiler (23) and detected by the steam temperature sensor (15) is TV and the specified temperature is 100 ° C., (A) shows that the steam temperature TV is less than 100 ° C. (I) is the proportionality of the flow rate control valve (13) to the driving condition of the line heater (4) when the steam temperature TV is 100 ° C. or higher and the fuel oil heating temperature detected by the fuel oil temperature sensor (14). The steam supply ratio to the heat exchanger (5) by opening and closing is shown. Then, the steam of the boiler (23), which is detected by the steam temperature sensor (15), is switched from the two fuel oil heating set temperatures SP0 to SP1 and VP0 to VP1 or vice versa (a) and (b). The fuel oil temperature controller (16) receives a signal output from the steam temperature detector (17) due to the temperature change.
本実施例では、前記のように燃料油加熱後の温度降下を考慮して燃料油温度制御器(16)のラインヒータ(4)、燃焼制限、熱交換器(5)の設定温度は、ボイラ(23)で発生し、蒸気温度センサ(15)で検出される蒸気温度TVが100℃以上のときに対して、蒸気温度TVが100℃未満のときは10℃高く設定している。 In this embodiment, in consideration of the temperature drop after heating the fuel oil as described above, the set temperatures of the line heater (4), combustion limit, and heat exchanger (5) of the fuel oil temperature controller (16) are boilers. The steam temperature TV generated at (23) and detected by the steam temperature sensor (15) is set to be higher by 10 ° C. when the steam temperature TV is lower than 100 ° C., when the steam temperature TV is lower than 100 ° C.
燃焼制限とは、燃料油温度がバーナの定常燃焼に影響を及ぼすと思われる温度のときにバーナの燃焼を停止、待機させる動作である。 Combustion restriction is an operation of stopping and waiting for burner combustion when the temperature of the fuel oil is assumed to affect the steady combustion of the burner.
またここで、蒸気の規定温度が100℃というのは一例である。規定温度は熱交換器(5)の能力によって決定できるが、言い換えれば過度に規定温度が高くなくとも蒸気と燃料油が熱交換できるように熱交換器(5)を選定できる。 Here, the specified temperature of the steam is 100 ° C. is an example. The specified temperature can be determined by the capacity of the heat exchanger (5). In other words, the heat exchanger (5) can be selected so that the steam and the fuel oil can exchange heat even if the specified temperature is not excessively high.
例えば飽和蒸気の場合、蒸気温度が100℃のときの保有潜熱は約2256kJ/kgであるが、150℃のときの保有潜熱は約2113kJ/kgであり、蒸気温度が高くなるにつれて単位質量当りの保有潜熱が減少することから、蒸気温度が高ければ効率が良いとは限らず、熱交換のために多くの蒸気量が必要になることが分かる。このことから、蒸気の規定温度は過度に高く設定する必要はない。 For example, in the case of saturated steam, the retained latent heat at a steam temperature of 100 ° C. is about 2256 kJ / kg, but the retained latent heat at 150 ° C. is about 2113 kJ / kg, and as the steam temperature increases, the per unit mass Since the retained latent heat decreases, it can be seen that if the steam temperature is high, the efficiency is not always good, and a large amount of steam is required for heat exchange. For this reason, the specified temperature of the steam does not need to be set too high.
また、本発明ではボイラ(23)で発生し、蒸気温度センサ(15)で検出される蒸気温度を規定温度として燃料油温度制御器(16)のラインヒータ(4)、熱交換器(5)に対する設定温度の切替えを行っているが、水蒸気の飽和温度、圧力および保有潜熱の関係は公に知られており、この場合も蒸気温度の代わりにボイラ(23)で発生する蒸気の圧力を燃料油温度制御器(16)のラインヒータ(4)、熱交換器(5)に対する設定温度の切替えのパラメータに用いてもよい。 In the present invention, the line heater (4) of the fuel oil temperature controller (16) and the heat exchanger (5) are generated with the steam temperature generated by the boiler (23) and detected by the steam temperature sensor (15) as a specified temperature. However, in this case, the steam pressure generated in the boiler (23) is used instead of the steam temperature as the fuel instead of the steam temperature. You may use for the parameter of the setting temperature switching with respect to the line heater (4) and heat exchanger (5) of an oil temperature controller (16).
例えば蒸気温度が100℃のとき、蒸気圧力は絶対圧力約0.101MPaであり、同じく150℃のときは約0.476MPaとなる。 For example, when the steam temperature is 100 ° C., the steam pressure is about 0.101 MPa, and when it is 150 ° C., it is about 0.476 MPa.
図3(ア)に示すように、コールドスタートのようなボイラ(23)中に蒸気が発生していないような状態でのボイラ(23)の始動で蒸気温度センサ(15)で検出されるボイラ(23)で発生する蒸気の温度が100℃未満の場合、ラインヒータ(4)が主体の燃料油加熱制御となる。本図によるとラインヒータ(4)の加熱設定温度SP0よりも熱交換器(5)の加熱設定温度VP0の方が高く設定されているが、実際は蒸気温度が100℃未満のため、このときは熱交換器(5)では燃料油の加熱は行われていないと考えてよい。したがって、燃料油はラインヒータ(4)によってSP0の温度に加熱されることになる。この温度が前記第一所定温度に対応する。 As shown in FIG. 3A, the boiler detected by the steam temperature sensor (15) at the start of the boiler (23) in a state where steam is not generated in the boiler (23) such as a cold start. When the temperature of the steam generated in (23) is less than 100 ° C., the fuel oil heating control is mainly performed by the line heater (4). According to this figure, the heating set temperature VP0 of the heat exchanger (5) is set higher than the heating set temperature SP0 of the line heater (4). However, since the steam temperature is actually less than 100 ° C., at this time It may be considered that the fuel oil is not heated in the heat exchanger (5). Therefore, the fuel oil is heated to the temperature of SP0 by the line heater (4). This temperature corresponds to the first predetermined temperature.
そして、図3(イ)のように蒸気温度センサ(15)で検出されるボイラ(23)で発生する蒸気の温度が100℃以上になれば、蒸気温度検出器(17)を経由して出力された信号により燃料油温度制御器(16)によって燃料油の加熱設定温度が切替わり、熱交換器(5)主体の燃料油加熱制御に移行する。このとき、ラインヒータ(4)の燃料油加熱設定温度SP1は図3(ア)のときよりも低く設定されるが、これは熱交換器(5)の加熱能力を優先させるためであり、蒸気の比例流量による熱交換器(5)の燃料油加熱制御の方が、ラインヒータ(4)のON−OFFの駆動による燃料油加熱制御より安定に行えるためである。このとき燃料油はVP1の温度に加熱されることになる。この温度が前記第二所定温度に対応する。 When the temperature of the steam generated in the boiler (23) detected by the steam temperature sensor (15) becomes 100 ° C. or higher as shown in FIG. 3 (a), the output is made via the steam temperature detector (17). The set temperature of the fuel oil is switched by the fuel oil temperature controller (16) based on the signal, and the control proceeds to the fuel oil heating control mainly of the heat exchanger (5). At this time, the fuel oil heating set temperature SP1 of the line heater (4) is set to be lower than that in FIG. 3 (a). This is for giving priority to the heating capacity of the heat exchanger (5). This is because the fuel oil heating control of the heat exchanger (5) with the proportional flow rate can be performed more stably than the fuel oil heating control by ON-OFF driving of the line heater (4). At this time, the fuel oil is heated to the temperature of VP1. This temperature corresponds to the second predetermined temperature.
本実施例のように、燃料油の所定温度を90℃としてボイラ(23)のバーナ(21)に供給するとき、コールドスタートのようなボイラ(23)中に蒸気が発生していないような状態でのボイラ(23)の始動で蒸気温度センサ(15)で検出されるボイラ(23)で発生する蒸気の温度が100℃未満の場合、燃料油温度センサ(14)で検出された燃料油の温度によるラインヒータ(4)のON−OFFの駆動による燃料油加熱制御のみでは燃料油の所定温度に対し、ラインヒータ出口から熱交換器入口までの燃料油供給配管、および蒸気の供給されていない熱交換器を通過する間の放熱による温度降下を考慮して燃料油を加熱しなければならないが、ボイラ(23)で発生し、蒸気温度センサ(15)で検出される蒸気温度TVが100℃以上のときは熱交換器(5)を使用することによって、燃料油温度センサ(14)で検出された燃料油の温度変化を燃料油温度制御器(16)が解析しながら、燃料油の加熱設定温度に対して0%から100%に割振って発信される作動信号で流量調節弁(13)が比例的に開閉され、この開閉度による蒸気の供給量の制御によって安定した燃料油の加熱制御ができる。 As in this embodiment, when the predetermined temperature of the fuel oil is set to 90 ° C. and supplied to the burner (21) of the boiler (23), no steam is generated in the boiler (23) such as a cold start. When the temperature of the steam generated in the boiler (23) detected by the steam temperature sensor (15) at the start of the boiler (23) is less than 100 ° C, the fuel oil temperature detected by the fuel oil temperature sensor (14) The fuel oil supply pipe from the line heater outlet to the heat exchanger inlet and the steam are not supplied to the predetermined temperature of the fuel oil only by the fuel oil heating control by driving the line heater (4) on and off according to the temperature. The fuel oil must be heated in consideration of the temperature drop due to heat dissipation while passing through the heat exchanger, but the steam temperature TV generated by the boiler (23) and detected by the steam temperature sensor (15) is 1. When the temperature is 0 ° C. or higher, the fuel oil temperature controller (16) analyzes the change in the temperature of the fuel oil detected by the fuel oil temperature sensor (14) by using the heat exchanger (5). The flow rate control valve (13) is proportionally opened / closed by an operation signal transmitted by allocating from 0% to 100% with respect to the heating set temperature of the fuel, and stable fuel oil is obtained by controlling the amount of steam supplied based on the degree of opening / closing. Can be controlled.
ここでは燃料油の所定温度を90℃としているので、本来ならば図3(ア)に示すような蒸気温度TVが100℃未満のときもSP0は90℃に設定されるが、ラインヒータ出口から熱交換器入口までの燃料油供給配管、および蒸気の供給されていない熱交換器を通過する間の放熱による温度降下を5℃考慮しているため、SP0は95℃に設定されている。 Here, since the predetermined temperature of the fuel oil is 90 ° C., SP0 is set to 90 ° C. even when the steam temperature TV as shown in FIG. SP0 is set to 95 ° C. because the temperature drop due to heat radiation while passing through the fuel oil supply pipe to the heat exchanger inlet and the heat exchanger not supplied with steam is taken into account at 5 ° C.
図3(イ)に示すような蒸気温度TVが100℃以上のとき、ラインヒータ(4)が駆動するのは燃料油温度センサ(14)で検出される燃料油温度が90℃から84℃まで降下した場合であるが、蒸気温度TVを100℃以上に確保できれば熱交換器(5)によって燃料油を90℃まで加熱できるように設計してあるため、コールドスタート時以外でボイラ(23)が定常運転中は、熱交換器(5)主体の燃料油加熱制御が可能である。したがって前記の燃料油加熱装置によって、ボイラ(23)の運転中はラインヒータ(4)は熱交換器(5)の補助的な役割として取り扱うことができ、消費電力を必要最小限に抑えることができる。 When the steam temperature TV as shown in FIG. 3 (a) is 100 ° C. or higher, the line heater (4) is driven from the fuel oil temperature detected by the fuel oil temperature sensor (14) from 90 ° C. to 84 ° C. Although it is a case where it falls, since it is designed so that the fuel oil can be heated to 90 ° C. by the heat exchanger (5) if the steam temperature TV can be secured at 100 ° C. or higher, the boiler (23) During steady operation, the fuel oil heating control of the heat exchanger (5) can be performed. Therefore, with the fuel oil heating device, the line heater (4) can be handled as an auxiliary role of the heat exchanger (5) during operation of the boiler (23), and power consumption can be minimized. it can.
本発明では燃料油の所定温度を90℃としているが、本発明者らが行った燃料油の燃焼に適した所定温度を求める実験では、燃料油の温度が約120℃以上あるいは約70℃以下の状況で、前記のような燃料油の密度減少による空気過剰燃焼あるいは密度増加による空気欠乏燃焼および燃料油の粘性増加により、バーナ(21)における振動燃焼および燃焼排ガス中の煤の発生のような異常燃焼が確認された。 In the present invention, the predetermined temperature of the fuel oil is set to 90 ° C., but in experiments conducted by the present inventors for determining the predetermined temperature suitable for the combustion of the fuel oil, the temperature of the fuel oil is about 120 ° C. or higher or about 70 ° C. or lower. In such a situation, due to excess air combustion due to a decrease in the density of the fuel oil or air deficiency combustion due to an increase in density and an increase in the viscosity of the fuel oil, vibration combustion in the burner (21) and generation of soot in the combustion exhaust gas Abnormal combustion was confirmed.
これを受けて本発明では、何らかの理由により燃料油の加熱が不十分の状態でバーナ(23)に燃料油が供給されることを防止するために、燃焼制限として蒸気温度TVが100℃未満のときは燃料油温度センサ(14)で検出される燃料油温度が80℃以下になった場合、蒸気温度TVが100℃以上のときは同じく燃料油温度が70℃以下になった場合燃料油温度制御器(16)がバーナ部(11)への燃料油の供給を停止させる制御を行い、バーナ(21)の燃焼を停止、待機させるようにした。この、燃料油の給油を停止させるための設定温度が前記制限温度に対応する。また、この燃焼制限の燃料油温度はSP0、SP1に対して各々10℃温度降下した場合に設定してあり、この10℃が前記特定温度に対応する。 Accordingly, in the present invention, in order to prevent the fuel oil from being supplied to the burner (23) when the fuel oil is not sufficiently heated for some reason, the steam temperature TV is less than 100 ° C. as a combustion limit. When the fuel oil temperature detected by the fuel oil temperature sensor (14) is 80 ° C. or lower, the fuel oil temperature is 70 ° C. or lower when the steam temperature TV is 100 ° C. or higher. The controller (16) performs control to stop the supply of fuel oil to the burner section (11) to stop and wait for the combustion of the burner (21). The set temperature for stopping the fuel oil supply corresponds to the limit temperature. Further, the fuel oil temperature for combustion restriction is set when the temperature drops by 10 ° C. with respect to SP0 and SP1, respectively, and this 10 ° C. corresponds to the specific temperature.
また、本発明のような燃料油を約90℃まで加熱するとき、熱交換器(5)のような加熱機器を使用して液体による燃料油加熱を行う場合、交換する熱は顕熱のみのため温水の場合は伝熱面積を大きくして多くの交換熱量を得るか、また熱媒油のような高温に昇温ができる液体を利用する等の必要がある。これに対し蒸気による燃料油加熱を行う場合、前記のように蒸気の保有潜熱を利用できるために、飽和蒸気でも熱交換ができるような熱交換器(5)を選定すれば、過熱蒸気を利用しなくとも液体に比べ容易に燃料油加熱を行うことができる。 In addition, when the fuel oil as in the present invention is heated to about 90 ° C., when the fuel oil is heated with a liquid using a heating device such as the heat exchanger (5), the heat to be exchanged is only sensible heat. Therefore, in the case of hot water, it is necessary to increase the heat transfer area to obtain a large amount of exchange heat, or to use a liquid that can be heated to a high temperature, such as heat transfer oil. On the other hand, when fuel oil is heated by steam, since the retained latent heat of steam can be used as described above, if a heat exchanger (5) that can exchange heat with saturated steam is selected, superheated steam is used. Even if not, the fuel oil can be heated more easily than the liquid.
これらの理由から本発明の燃料油加熱装置は蒸気ボイラで使用し、本実施例では燃料油の所定温度を90℃としている。 For these reasons, the fuel oil heating device of the present invention is used in a steam boiler, and the predetermined temperature of the fuel oil is 90 ° C. in this embodiment.
図2に記載された本発明の燃料油加熱装置は、図1に記載された本発明の燃料油加熱装置において燃料油の温度が燃焼に適した第一所定温度に上昇するまでバーナ部(11)に供給された燃料油の燃料油供給配管(25)の循環路の入口上流に燃料供給弁(26)が設けられ、燃料油供給配管(25)の循環路の少なくとも前記オイルポンプ(3)の入側に、燃料油を所定量貯留させておくオイルポンプ(3)へと燃料油を供給するためのベッセル(1)が設けられている。 The fuel oil heating apparatus of the present invention shown in FIG. 2 is a burner section (11) until the temperature of the fuel oil rises to a first predetermined temperature suitable for combustion in the fuel oil heating apparatus of the present invention shown in FIG. ) Is provided upstream of the inlet of the circulation path of the fuel oil supply pipe (25), and at least the oil pump (3) in the circulation path of the fuel oil supply pipe (25). A vessel (1) for supplying fuel oil to an oil pump (3) for storing a predetermined amount of fuel oil is provided on the inlet side.
例えばボイラ(23)の設置位置と燃料油タンク(図示省略)の設置位置の高低差によって、ボイラ(23)が停止しているとき燃料油タンク中の燃料油が燃料油供給配管(25)を通過してバーナ(21)へ供給されることを防止するために燃料油供給配管(25)の循環路の入口上流にオイルポンプ(3)と連動する燃料供給弁(26)が設けられることが考えられる。 For example, when the boiler (23) is stopped due to the difference in height between the installation position of the boiler (23) and the installation position of the fuel oil tank (not shown), the fuel oil in the fuel oil tank passes through the fuel oil supply pipe (25). A fuel supply valve (26) interlocking with the oil pump (3) may be provided upstream of the inlet of the circulation path of the fuel oil supply pipe (25) in order to prevent passage and supply to the burner (21). Conceivable.
ボイラ(23)が通常運転後停止したとき、燃料油供給配管(25)は燃料供給弁(26)が閉鎖していることにより密閉された循環路となる。燃料油供給配管(25)中の燃料油がボイラ(23)停止後のボイラ(23)自身およびその周辺の余熱によって体積膨張することにより燃料油供給配管(25)の継目から漏出して火災を起こしたり、あるいは同様に低燃焼側ノズル(9)、高燃焼側ノズル(10)からボイラ(23)内に漏出し次回のバーナ(21)の着火の際に爆発を起こしたりする恐れがある。これらの事故を防止するために燃料油供給配管(25)の循環路の少なくともオイルポンプ(3)の入側にベッセル(1)を設けている。ベッセル(1)はボイラ(23)停止後のボイラ(23)自身およびその周辺の余熱によって発生する燃料油の体積膨張を吸収できる構造を持つ。 When the boiler (23) stops after normal operation, the fuel oil supply pipe (25) becomes a closed circulation path because the fuel supply valve (26) is closed. The fuel oil in the fuel oil supply pipe (25) leaks from the joint of the fuel oil supply pipe (25) due to volume expansion due to the residual heat of the boiler (23) itself and its surroundings after the boiler (23) stops. There is also a risk that it may occur or, similarly, leak from the low combustion side nozzle (9) and the high combustion side nozzle (10) into the boiler (23) and cause an explosion when the burner (21) is ignited next time. In order to prevent these accidents, the vessel (1) is provided at least on the inlet side of the oil pump (3) in the circulation path of the fuel oil supply pipe (25). The vessel (1) has a structure capable of absorbing the volume expansion of the fuel oil generated by the boiler (23) itself after stopping the boiler (23) and the residual heat in the vicinity thereof.
本実施例の燃料油加熱装置において、実施例1の燃料油加熱装置と同様の燃料油加熱制御を行うことによってコールドスタート時以外でボイラ(23)が定常運転中は、熱交換器(5)主体の燃料油加熱制御が可能である。したがって前記の燃料油加熱装置によって、ボイラ(23)の運転中はラインヒータ(4)は熱交換器(5)の補助的な役割として取り扱うことができ、消費電力を必要最小限に抑えることができる。 In the fuel oil heating apparatus of the present embodiment, the fuel oil heating control similar to that of the fuel oil heating apparatus of the first embodiment is performed, so that the boiler (23) is in steady operation except during a cold start, and the heat exchanger (5) The main fuel oil heating control is possible. Therefore, with the fuel oil heating device, the line heater (4) can be handled as an auxiliary role of the heat exchanger (5) during operation of the boiler (23), and power consumption can be minimized. it can.
1 ベッセル
2 逆止弁
3 オイルポンプ
4 ラインヒータ
5 熱交換器
6 スチームトラップ
7 第一電磁弁
8 第二電磁弁
9 低燃焼側ノズル
10 高燃焼側ノズル
11 バーナ部
12 主蒸気弁
13 流量調節弁
14 燃料油温度センサ
15 蒸気温度センサ
16 燃料油温度制御器
17 蒸気温度検出器
18 主蒸気配管
19 燃料油加熱蒸気配管
20 ウィンドボックス
21 バーナ
22 気水分離器
23 ボイラ
24 回線
25 燃料油供給配管
26 燃料供給弁
TV 蒸気温度センサ(15)で検出されるボイラ(23)の蒸気温度
SP0 TVが規定温度未満のときのラインヒータによる燃料油加熱設定温度
SP1 TVが規定温度以上のときのラインヒータによる燃料油加熱設定温度
VP0 TVが規定温度未満のときの熱交換器による燃料油加熱設定温度
VP1 TVが規定温度以上のときの熱交換器による燃料油加熱設定温度
1 Vessel 2
Claims (5)
Interlocking with the oil pump (3) upstream of the circulation path of the fuel oil supply pipe (25) of the fuel oil supplied to the burner section (11) until the temperature of the fuel oil rises to a first predetermined temperature suitable for combustion A fuel supply valve (26) is provided, and at least an input side of the oil pump (3) in a circulation path of the fuel oil supply pipe (25) leads to an oil pump (3) for storing a predetermined amount of fuel oil. The fuel oil heating device according to any one of claims 1 to 4, which is a vessel (1) for supplying fuel oil.
Priority Applications (1)
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JP2004037922A JP2005226954A (en) | 2004-02-16 | 2004-02-16 | Fuel oil heating device |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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JP2004037922A JP2005226954A (en) | 2004-02-16 | 2004-02-16 | Fuel oil heating device |
Publications (1)
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JP2005226954A true JP2005226954A (en) | 2005-08-25 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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JP2004037922A Pending JP2005226954A (en) | 2004-02-16 | 2004-02-16 | Fuel oil heating device |
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Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101270683B1 (en) | 2011-11-04 | 2013-06-04 | 대우조선해양 주식회사 | System for controlling fuel viscosity of main boiler and method thereof |
KR101291129B1 (en) * | 2011-10-25 | 2013-08-01 | 삼성중공업 주식회사 | Cylinder oil heating system of engine for ship |
JP2019117024A (en) * | 2017-12-27 | 2019-07-18 | 三菱日立パワーシステムズ株式会社 | Oil burner device, boiler and boiler operating method |
WO2023233886A1 (en) * | 2022-06-03 | 2023-12-07 | 三菱パワー株式会社 | Fuel supply device, plant provided with same, and fuel supply method |
-
2004
- 2004-02-16 JP JP2004037922A patent/JP2005226954A/en active Pending
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101291129B1 (en) * | 2011-10-25 | 2013-08-01 | 삼성중공업 주식회사 | Cylinder oil heating system of engine for ship |
KR101270683B1 (en) | 2011-11-04 | 2013-06-04 | 대우조선해양 주식회사 | System for controlling fuel viscosity of main boiler and method thereof |
JP2019117024A (en) * | 2017-12-27 | 2019-07-18 | 三菱日立パワーシステムズ株式会社 | Oil burner device, boiler and boiler operating method |
JP7075211B2 (en) | 2017-12-27 | 2022-05-25 | 三菱重工業株式会社 | Oil burner device, boiler and how to operate the boiler |
WO2023233886A1 (en) * | 2022-06-03 | 2023-12-07 | 三菱パワー株式会社 | Fuel supply device, plant provided with same, and fuel supply method |
JP2023177893A (en) * | 2022-06-03 | 2023-12-14 | 三菱重工業株式会社 | Fuel supply device, plant comprising the same, and fuel supply method |
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