JP2005201506A - Combustion control method for boiler - Google Patents

Combustion control method for boiler Download PDF

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JP2005201506A
JP2005201506A JP2004007455A JP2004007455A JP2005201506A JP 2005201506 A JP2005201506 A JP 2005201506A JP 2004007455 A JP2004007455 A JP 2004007455A JP 2004007455 A JP2004007455 A JP 2004007455A JP 2005201506 A JP2005201506 A JP 2005201506A
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combustion
water
steam
water pipe
water level
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Hideo Furukawa
英夫 古川
Tatsuro Nagabuchi
竜朗 永渕
Kyosuke Okubo
恭輔 大久保
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Miura Co Ltd
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Miura Co Ltd
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  • Control Of Steam Boilers And Waste-Gas Boilers (AREA)
  • Regulation And Control Of Combustion (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To positively maintain steam dryness without causing water level fluctuation in a combustion control method for a boiler having a water pipe. <P>SOLUTION: In the combustion control method for the boiler for adjusting the combustion quantity of a burner 6 for heating the water pipe 5, the combustion quantity is reduced when determining a lowering of steam dryness, and steam dryness is determined based on either one of steam pressure, electric conductivity of water in the water pipe 5 and the temperature of supply water to the water pipe 5. Further, steam dryness is determined based on a signal from a steam dryness sensor. <P>COPYRIGHT: (C)2005,JPO&NCIPI

Description

この発明は、水管を有するボイラの燃焼制御方法に関する。
に関する。
The present invention relates to a combustion control method for a boiler having a water pipe.
About.

この種の水管を有するボイラにおいては、水管をバーナにより加熱することにより蒸気を生成するものがある。その際、蒸気品質として、乾き度の適切な維持が要求される。この蒸気乾き度を維持する方法が提案されている(特許文献1参照)。   Some boilers having this type of water pipe generate steam by heating the water pipe with a burner. At that time, appropriate maintenance of dryness is required as the vapor quality. A method for maintaining this vapor dryness has been proposed (see Patent Document 1).

特開平11−287404号公報JP 11-287404 A

前記従来方法においては、給水ポンプの駆動により乾き度の維持を行うものである。このため、水管内の水位変動を招き、蒸気乾き度の適切な維持ができない虞がある。   In the conventional method, the dryness is maintained by driving a water supply pump. For this reason, there is a possibility that the water level in the water pipe may fluctuate and the steam dryness cannot be appropriately maintained.

この発明は、水位変動を生ずることなく蒸気乾き度を維持すること目的としている。   An object of the present invention is to maintain steam dryness without causing fluctuations in water level.

この発明は、前記の課題を解決するためになされたもので、請求項1に記載の発明は、水管を加熱するバーナの燃焼量を調整するボイラの燃焼制御方法において、蒸気乾き度に応じて燃焼量を調整することにより蒸気乾き度を維持することを特徴としている。   The present invention has been made to solve the above-mentioned problems. The invention according to claim 1 is a boiler combustion control method for adjusting a combustion amount of a burner for heating a water pipe, according to a degree of steam dryness. It is characterized by maintaining steam dryness by adjusting the amount of combustion.

請求項2記載の発明は、水管を加熱するバーナの燃焼量を調整するボイラの燃焼制御方法において、前記水管内の水位に応じて燃焼量を調整することにより蒸気乾き度を維持することを特徴としている。   According to a second aspect of the present invention, in a combustion control method for a boiler that adjusts the combustion amount of a burner that heats a water pipe, the steam dryness is maintained by adjusting the combustion quantity according to the water level in the water pipe. It is said.

この発明によれば、燃焼量の調整により蒸気乾き度を維持しているので、給水ポンプ制御による従来の方法と比較して、より確実に蒸気乾き度が維持される。   According to the present invention, since the steam dryness is maintained by adjusting the combustion amount, the steam dryness is more reliably maintained as compared with the conventional method using the feed water pump control.

(実施の形態1)
つぎに、この発明の実施の形態1について説明する。この発明の実施の形態1は、水管群を有する蒸気ボイラ(以下、単にボイラという。)の燃焼制御方法に適用される。前記ボイラは、水管とこの水管を加熱するバーナとこのバーナの燃焼量を調整する流量調整弁を備えるものであれば、形式、種類を特定のものに限定するものではない。
(Embodiment 1)
Next, a first embodiment of the present invention will be described. Embodiment 1 of the present invention is applied to a combustion control method for a steam boiler having a group of water tubes (hereinafter simply referred to as a boiler). The boiler is not limited to a specific type and type as long as it includes a water pipe, a burner for heating the water pipe, and a flow rate adjusting valve for adjusting the combustion amount of the burner.

この実施の形態1は、水管を加熱するバーナの燃焼量を調整するボイラの燃焼制御方法において、蒸気乾き度に応じて燃焼量を調整することにより蒸気乾き度を維持することを特徴としている。   The first embodiment is characterized in that the steam dryness is maintained by adjusting the combustion amount in accordance with the steam dryness in the combustion control method of the boiler for adjusting the combustion amount of the burner for heating the water pipe.

この実施の形態1においては、蒸気乾き度の低下が判定されると、前記バーナの燃焼量が減少され、蒸気乾き度の低下が抑制される。この燃焼量の調整は、蒸気負荷(蒸気圧力)に基づく燃焼量の調整に付加して行われる。   In the first embodiment, when it is determined that the steam dryness is lowered, the amount of combustion of the burner is reduced, and the steam dryness is prevented from being lowered. The adjustment of the combustion amount is performed in addition to the adjustment of the combustion amount based on the steam load (steam pressure).

この実施の形態1において、前記バーナは、好ましくは、燃焼量の調整が容易なガスバ
ーナとする。しかしながら、開度を変化させることにより燃焼量が調整されるものであれば、バーナの種類、形式は、特定のものに限定されない。
In the first embodiment, the burner is preferably a gas burner whose combustion amount can be easily adjusted. However, the type and form of the burner are not limited to specific ones as long as the amount of combustion is adjusted by changing the opening.

蒸気ボイラの乾き度は、水管内の蒸気圧力が低いとき、水管内の水の電気伝導度が高い時および前記水管への給水温度が高いとき、低下することが知られている。そこで、前記蒸気乾き度の低下の判定を、蒸気圧力,前記水管4内の水の電気伝導度,前記水管4への給水温度に基づいて行うように構成することができる。   It is known that the dryness of the steam boiler decreases when the steam pressure in the water pipe is low, when the electrical conductivity of the water in the water pipe is high, and when the feed water temperature to the water pipe is high. Therefore, the determination of the decrease in the steam dryness can be made on the basis of the steam pressure, the electrical conductivity of the water in the water pipe 4, and the water supply temperature to the water pipe 4.

この実施の形態1において、前記水管を複数設け、これら水管を上部ヘッダと下部ヘッダとの間に接続して缶体を構成することができる。こうした場合、前記の蒸気圧力,前記水管4内の水の電気伝導度,前記水管4への給水温度は、それぞれ前記缶体内の圧力、前記缶体内の水(缶水)の電気伝導度,缶体への給水温度と等価である。   In the first embodiment, a plurality of water pipes are provided, and the water pipes can be connected between the upper header and the lower header to form a can body. In such a case, the steam pressure, the electrical conductivity of the water in the water pipe 4, and the water supply temperature to the water pipe 4 are the pressure in the can, the electrical conductivity of the water in the can (can water), and the can, respectively. It is equivalent to the temperature of water supply to the body.

また、前記判定は、蒸気供給路に蒸気乾き度センサを設けて、同センサの信号に基づき行うように構成することができる。前記蒸気供給路は、前記缶体に接続され、蒸気利用設備へ生成蒸気を供給するためのものである。   In addition, the determination may be performed based on a signal of a steam dryness sensor provided in the steam supply path. The steam supply path is connected to the can body and supplies generated steam to steam utilization equipment.

この実施の形態1において、燃焼量の調整は、流量調整弁の開度調整により実現され、調整の態様は、連続的調整または段階的調整により実施される。前記開度調整の際には、適正空気比にて燃焼が行われるように、燃焼用空気を供給する送風機の回転数制御などの手段により、燃焼用空気の量も同時に調整される。   In the first embodiment, the adjustment of the combustion amount is realized by adjusting the opening of the flow rate adjusting valve, and the mode of adjustment is performed by continuous adjustment or stepwise adjustment. When adjusting the opening, the amount of combustion air is also adjusted at the same time by means such as rotational speed control of a blower that supplies combustion air so that combustion is performed at an appropriate air ratio.

この発明は、前記の実施の形態1に限定されるものではなく、つぎの実施の形態2を含む。   The present invention is not limited to the first embodiment, but includes the following second embodiment.

(実施の形態2)
実施の形態2は、水管を加熱するバーナの燃焼量を調整するボイラの燃焼制御方法において、前記水管内の水位に応じて燃焼量を調整することにより蒸気乾き度を維持することを特徴としている。
(Embodiment 2)
Embodiment 2 is a combustion control method for a boiler that adjusts the combustion amount of a burner that heats a water pipe, and is characterized by maintaining the steam dryness by adjusting the combustion quantity according to the water level in the water pipe. .

この実施の形態2においては、前記水管内の水位が低いとき燃焼量を増大し、水位が高いとき燃焼量を減少することにより蒸気乾き度を維持する。   In the second embodiment, the steam dryness is maintained by increasing the combustion amount when the water level in the water pipe is low and decreasing the combustion amount when the water level is high.

前記実施の形態2は、前記ボイラを複数台設置する所謂多缶設置のシステムにおいて、蒸気の質を落としたくない場合、前記水管内の水位が満水に近いとき、低燃焼でも問題のない水位までは低燃焼より少ない燃焼量により燃焼を行う形態を含む。前記の低燃焼より少ない燃焼量とは、低燃焼時の燃焼量を高燃焼時の50%とした場合、10〜30%程度とされる。   In the so-called multi-can installation system in which a plurality of boilers are installed in the second embodiment, when it is not desired to lower the quality of the steam, when the water level in the water pipe is close to the full water level, there is no problem even in low combustion. Includes a mode in which combustion is performed with a combustion amount smaller than low combustion. The combustion amount smaller than the low combustion is about 10 to 30% when the combustion amount at the low combustion is 50% at the high combustion.

以下、この発明の具体的実施例1を図面に基づいて詳細に説明する。図1は、実施例1のボイラの概略構成図であり、図2は、同実施例1の制御手順を示すフローチャート図である。   Hereinafter, a specific embodiment 1 of the present invention will be described in detail with reference to the drawings. FIG. 1 is a schematic configuration diagram of the boiler according to the first embodiment, and FIG. 2 is a flowchart illustrating a control procedure according to the first embodiment.

前記実施例1は、蒸気を生成する小型貫流ボイラに適用されたものである。このボイラ1は、上部ヘッダ2および下部ヘッダ3との間に多数の水管5,5,…を接続した缶体4と、前記各水管5を加熱するガスバーナ(以下、単にバーナという。)6と、前記バーナ6の燃焼量を調整するための流量調整弁7と、前記缶体4へ給水するポンプ8と、前記流量調整弁7および前記ポンプ8などを制御する制御器9とを主要部として備えている。   The first embodiment is applied to a small once-through boiler that generates steam. The boiler 1 includes a can 4 in which a large number of water pipes 5, 5,... Are connected between an upper header 2 and a lower header 3, and a gas burner (hereinafter simply referred to as a burner) 6 for heating the water pipes 5. The main components are a flow rate adjusting valve 7 for adjusting the combustion amount of the burner 6, a pump 8 for supplying water to the can body 4, and a controller 9 for controlling the flow rate adjusting valve 7, the pump 8 and the like. I have.

また、前記缶体4には、前記各水管4内の水位を検出するための第一水位検出10および第二水位検出器11を有する水位検出筒12を接続している。前記第一水位検出器10は、前記各水管5内の水位を第一水位A(低燃焼時の水位)に制御するための電極であり、前記第二検出器11は、前記水位検出筒12内の水位を前記第一水位Aよりも低い第二水位B(高燃焼時の水位)に制御するための電極である。   Further, a water level detection cylinder 12 having a first water level detection 10 and a second water level detector 11 for detecting the water level in each water pipe 4 is connected to the can body 4. The first water level detector 10 is an electrode for controlling the water level in each water pipe 5 to the first water level A (water level at low combustion), and the second detector 11 is the water level detection cylinder 12. It is an electrode for controlling the inner water level to the second water level B (water level at the time of high combustion) lower than the first water level A.

また、前記缶体4には、水管過熱を検出するための第三水位検出器13と、前記缶体4内の圧力を検出するための圧力検出器14とを備えている。   Further, the can body 4 includes a third water level detector 13 for detecting water pipe overheating and a pressure detector 14 for detecting the pressure in the can body 4.

前記流量調整弁7は、開度が調節可能で、前記バーナ6の燃焼量を0,低燃焼時の燃焼量(高燃焼時を100%としてそのの約半分の燃焼量),高燃焼時の75%の燃焼量,高燃焼時の燃焼量に制御可能な比例制御弁であり、燃料供給路15に設けられる。また、前記燃料供給路15には、燃料遮断弁(図示省略)を備えている。前記ポンプ7は、給水路16にそれぞれ設けられる。   The flow rate adjusting valve 7 is adjustable in opening degree, the combustion amount of the burner 6 is 0, the combustion amount at the time of low combustion (combustion amount of about half of that when the high combustion time is 100%), and at the time of high combustion This is a proportional control valve that can be controlled to a combustion amount of 75% and a combustion amount at the time of high combustion, and is provided in the fuel supply passage 15. The fuel supply passage 15 is provided with a fuel cutoff valve (not shown). The pumps 7 are respectively provided in the water supply channels 16.

前記制御器9は、前記圧力検出器14,前記第一水位検出器10〜前記第三水位検出器13などの信号を入力して、前記流量調整弁7,前記ポンプ8および前記遮断弁などを所定の処理手順に基づき制御するように構成されている。   The controller 9 inputs signals from the pressure detector 14, the first water level detector 10 to the third water level detector 13, etc., and controls the flow rate adjusting valve 7, the pump 8, the shutoff valve, and the like. Control is performed based on a predetermined processing procedure.

前記制御器9の処理手順は、前記缶体4内圧力を前記圧力検出器14の信号に基づき前記缶体4内圧力が設定となるように、また所定蒸気乾き度を維持するように前記流量調整弁6などを制御する燃焼制御のための制御手順と、前記第一水位検出器10および前記第二水位検出器11からの信号に基づき、前記水位検出筒12内水位を低燃焼時第一水位Aに、高燃焼時第二水位Bにそれぞれ制御する制御手順を含む。前記燃焼制御の処理手順の要部を図2に示す。図2の処理手順は、所定蒸気乾き度の維持を維持するように前記流量調整弁6を制御する手順のみを示している。   The processing procedure of the controller 9 is such that the pressure in the can body 4 is set based on the signal from the pressure detector 14 so that the pressure in the can body 4 is set and the predetermined steam dryness is maintained. Based on the control procedure for combustion control for controlling the regulating valve 6 and the like and the signals from the first water level detector 10 and the second water level detector 11, the water level in the water level detection cylinder 12 is set to the first during low combustion. A control procedure for controlling the water level A to the second water level B during high combustion is included. The main part of the processing procedure of the combustion control is shown in FIG. The processing procedure of FIG. 2 shows only the procedure of controlling the flow rate adjusting valve 6 so as to maintain the predetermined steam dryness.

また前記制御器9の処理手順には、ボイラ1の排ガスの性状(O2濃度,CO濃度,NOx濃度など)を検出して、排ガスの性状を安定させるための前記流量調整弁6を制御する手順も含まれている。具体的には、設定値に対して排ガス中のO2濃度が下がればバーナ6への供給ガス量を減少させ、上がれば供給ガス量を増加させる。また、排ガス中のCO濃度が上がれば、供給ガス量を減らし高空気比で運転し、それでも上がるようであれば、供給ガス量を増加させ、CO濃度がある範囲に収まるように制御する。さらには、排ガス中のNOx濃度が上がれば、供給ガス量を減少させて高空気比で運転する。 The processing procedure of the controller 9 is to detect the properties of the exhaust gas (O 2 concentration, CO concentration, NOx concentration, etc.) of the boiler 1 and control the flow rate adjusting valve 6 for stabilizing the properties of the exhaust gas. Procedures are also included. Specifically, the amount of gas supplied to the burner 6 is decreased when the O 2 concentration in the exhaust gas is reduced with respect to the set value, and the amount of supplied gas is increased when the concentration is increased. Further, if the CO concentration in the exhaust gas increases, the operation is performed at a high air ratio by reducing the supply gas amount, and if it still increases, the supply gas amount is increased and control is performed so that the CO concentration is within a certain range. Furthermore, if the NOx concentration in the exhaust gas increases, the amount of supplied gas is reduced and operation is performed at a high air ratio.

以下に、図2の処理手順に従って、上記構成の蒸気乾き度維持に関する実施例1の作用を説明する。以下の説明において、前記流量調整弁7により開度調整を行う際には、適正空気比にて燃焼が行われるように、燃焼用空気を供給する送風機(図示省略)の回転数制御により、燃焼用空気の量も同時に調整される。   Below, according to the process sequence of FIG. 2, the effect | action of Example 1 regarding the steam dryness maintenance of the said structure is demonstrated. In the following description, when the opening degree is adjusted by the flow rate adjusting valve 7, the combustion is performed by controlling the rotational speed of a blower (not shown) for supplying combustion air so that combustion is performed at an appropriate air ratio. The amount of working air is also adjusted at the same time.

前記圧力検出器13の検出値が設定値(たとえば、0.6Mpa)以下となると、S1にてYES(蒸気乾き度の低下の判定)が判定され、S2へ移行して、前記流量調整弁7を制御して、燃焼量を微調整,すなわち一例として高燃焼時の90%まで減少する。これにより、前記各水管5内の沸騰が抑制され、乾き度の低下が抑制される。   When the detection value of the pressure detector 13 becomes a set value (for example, 0.6 Mpa) or less, YES (determination of decrease in steam dryness) is determined in S1, and the flow proceeds to S2, and the flow rate adjusting valve 7 Is controlled to finely adjust the combustion amount, that is, as an example, it is reduced to 90% at the time of high combustion. Thereby, the boiling in each said water pipe 5 is suppressed, and the fall of a dryness is suppressed.

前記圧力検出器14の検出値が設定値よりディファレンシャル分だけ高い圧力となり、S1において、NOが判定されると、前記流量調整弁7を制御して、燃焼量を増大して元に戻す。   If the detected value of the pressure detector 14 becomes a pressure higher than the set value by a differential amount, and NO is determined in S1, the flow rate adjusting valve 7 is controlled to increase the combustion amount and restore it.

前記実施例1においては、圧力検出器13の検出信号により、蒸気乾き度の判定を行う
ように構成しているが、前記給水路16内の給水の温度を検出するセンサ(図示省略)を設け、このセンサの検出信号に基づき判定したり、前記缶体2内の缶水の電気伝導度を検出するセンサ(図示省略)を設け、このセンサの検出信号に基づき判定するように構成することもできる。また、前記蒸気乾き度を間接的に検出するのではなく、前記上部ヘッダ2に接続され、蒸気利用設備(図示省略)へ蒸気を供給する蒸気供給路(図示省略)に蒸気乾き度検出器(図示省略)設け、この検出器の検出信号に基づき判定するように構成することもできる。
In the first embodiment, the steam dryness is determined based on the detection signal of the pressure detector 13, but a sensor (not shown) for detecting the temperature of the water supply in the water supply channel 16 is provided. In addition, it is possible to make a determination based on the detection signal of this sensor, or to provide a sensor (not shown) for detecting the electrical conductivity of the can water in the can body 2 and to make the determination based on the detection signal of this sensor. it can. In addition, instead of indirectly detecting the steam dryness, a steam dryness detector (not shown) connected to the upper header 2 and supplying steam to a steam utilization facility (not shown) (not shown) (Not shown) may be provided and configured to make a determination based on the detection signal of the detector.

さらに、前記ボイラ1を複数台設置する所謂多缶設置のシステムにおいて、蒸気の質を落としたくない場合、前記缶体2内のの水位が満水に近い時、すなわち前記第一水位検出器10が水有りを検出している時または前記第三水位検出器13が水有りを検出している時、低燃焼でも問題のない水位まで,すなわち前記第一水位検出器10が水無しを検出するか、前記第三水位検出器13が水無しを検出するまでは低燃焼(高燃焼の50%)より少ない燃焼量(高燃焼の30%)で燃焼を行うように構成することができる。   Further, in a so-called multi-can installation system in which a plurality of boilers 1 are installed, when it is not desired to reduce the quality of the steam, when the water level in the can body 2 is almost full, that is, the first water level detector 10 is When detecting the presence of water or when the third water level detector 13 detects the presence of water, whether the low water level does not cause any problem even if the combustion is low, that is, whether the first water level detector 10 detects the absence of water Until the third water level detector 13 detects the absence of water, combustion can be performed with a smaller combustion amount (30% of high combustion) than low combustion (50% of high combustion).

本発明の実施例1の概略構成を示す説明図である。It is explanatory drawing which shows schematic structure of Example 1 of this invention. 同実施例1の処理手順の要部を示すフローチャート図である。It is a flowchart figure which shows the principal part of the process sequence of the Example 1. FIG.

符号の説明Explanation of symbols

1 ボイラ
5 水管
6 バーナ
7 流量調整弁
9 制御器
1 Boiler 5 Water Pipe 6 Burner 7 Flow Control Valve 9 Controller

Claims (2)

水管5を加熱するバーナ6の燃焼量を調整するボイラの燃焼制御方法において、蒸気乾き度に応じて燃焼量を調整することにより蒸気乾き度を維持することを特徴とするボイラの燃焼制御方法。 A boiler combustion control method for adjusting a combustion amount of a burner 6 for heating a water pipe 5, wherein the steam dryness is maintained by adjusting a combustion amount according to the steam dryness. 水管5を加熱するバーナ6の燃焼量を調整するボイラの燃焼制御方法において、前記水管5内の水位に応じて燃焼量を調整することにより蒸気乾き度を維持することを特徴とするボイラの燃焼制御方法。


In a boiler combustion control method for adjusting a combustion amount of a burner 6 for heating a water pipe 5, the boiler combustion is characterized in that the steam dryness is maintained by adjusting the combustion amount according to the water level in the water pipe 5. Control method.


JP2004007455A 2004-01-15 2004-01-15 Combustion control method for boiler Pending JP2005201506A (en)

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Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007271593A (en) * 2006-03-08 2007-10-18 Miura Co Ltd Electrode rod for detecting water level of once-through boiler, method of detecting water level of once-through boiler and method of controlling water level of once-through boiler
JP2011185510A (en) * 2010-03-08 2011-09-22 Kawasaki Thermal Engineering Co Ltd Combustion control method and device for boiler
KR101329371B1 (en) 2006-03-08 2013-11-14 미우라고교 가부시키카이샤 Electrode rod for detecting water-level, method of detecting water-level, method of controlling water-level in a boiler, and method of controlling water-level in a steam separator
JP2016050716A (en) * 2014-08-30 2016-04-11 株式会社サムソン Multi-can installation boiler

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2007271593A (en) * 2006-03-08 2007-10-18 Miura Co Ltd Electrode rod for detecting water level of once-through boiler, method of detecting water level of once-through boiler and method of controlling water level of once-through boiler
KR101329371B1 (en) 2006-03-08 2013-11-14 미우라고교 가부시키카이샤 Electrode rod for detecting water-level, method of detecting water-level, method of controlling water-level in a boiler, and method of controlling water-level in a steam separator
JP2011185510A (en) * 2010-03-08 2011-09-22 Kawasaki Thermal Engineering Co Ltd Combustion control method and device for boiler
JP2016050716A (en) * 2014-08-30 2016-04-11 株式会社サムソン Multi-can installation boiler

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