JP3009793B2 - Water level control method for multi-tube once-through boiler - Google Patents

Water level control method for multi-tube once-through boiler

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Publication number
JP3009793B2
JP3009793B2 JP4316336A JP31633692A JP3009793B2 JP 3009793 B2 JP3009793 B2 JP 3009793B2 JP 4316336 A JP4316336 A JP 4316336A JP 31633692 A JP31633692 A JP 31633692A JP 3009793 B2 JP3009793 B2 JP 3009793B2
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JP
Japan
Prior art keywords
water level
water
detecting electrode
steam
electrode bars
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
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JP4316336A
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Japanese (ja)
Other versions
JPH06147407A (en
Inventor
行夫 丸山
博 成田
Original Assignee
石川島播磨重工業株式会社
石川島汎用ボイラ株式会社
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Priority to JP4316336A priority Critical patent/JP3009793B2/en
Publication of JPH06147407A publication Critical patent/JPH06147407A/en
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Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】本発明は、多管式貫流ボイラの水
位制御方法に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a water level control method for a multi-tube once-through boiler.

【0002】[0002]

【従来の技術】蒸気発生量が0.5〜5t/h程度の小
容量ボイラとしては、図4に示すごとき貫流ボイラがあ
る。
2. Description of the Related Art As a small-capacity boiler having a steam generation amount of about 0.5 to 5 t / h, there is a once-through boiler as shown in FIG.

【0003】図4中、1はボイラ本体であって、該ボイ
ラ本体1は円周方向へ所要の間隔で立設された竪向きで
且つ複数の加熱管2と、該加熱管2で包囲された内部空
間に形成された燃焼室3と、加熱管2の下部に接続され
た環状の下部管寄せ4と、加熱管2の上部に接続された
環状の上部管寄せ5を備え、ボイラ本体1の上部管寄せ
5に包囲された空間部には、燃料油を燃焼室3内に噴射
し得るようにした竪向きのバーナ6が取付けられてい
る。
In FIG. 4, reference numeral 1 denotes a boiler main body. The boiler main body 1 is vertically erected at predetermined intervals in a circumferential direction and is surrounded by a plurality of heating tubes 2 and the heating tubes 2. A combustion chamber 3 formed in the inner space formed by the heater, an annular lower header 4 connected to a lower portion of the heating tube 2, and an annular upper header 5 connected to an upper portion of the heating tube 2. A vertical burner 6 is mounted in a space surrounded by the upper header 5 so that fuel oil can be injected into the combustion chamber 3.

【0004】7は下部管寄せ4に接続された給水管であ
って、該給水管7には、ボイラ本体1の下部管寄せ4に
水を供給し得るようにした給水ポンプ8及び下部管寄せ
4から給水ポンプ8へ水が逆流しないようにした逆止弁
9を備えている。
A water supply pipe 7 is connected to the lower header 4. The water supply pipe 7 has a water supply pump 8 and a lower header which can supply water to the lower header 4 of the boiler body 1. A check valve 9 is provided to prevent water from flowing back from 4 to the water supply pump 8.

【0005】10は気水分離器であって、該気水分離器
10の上側部と上部管寄せ5の上面とは蒸気管11によ
り接続され、気水分離器10の底部と下部管寄せ4の側
部とは降水管12により接続されている。
[0005] Reference numeral 10 denotes a steam separator. The upper portion of the steam separator 10 and the upper surface of the upper header 5 are connected by a steam pipe 11, and the bottom portion of the steam separator 10 and the lower header 4 are connected. Are connected by a downcomer 12.

【0006】13はボイラ本体1の加熱管2内にある水
のレベル(水位)を検出するために用いる水位検出用容
器であって、該水位検出用容器13の底部及び上側部に
一端を接続した連通管14,15の他端は、下部管寄せ
4或いは上部管寄せ5に接続されている。又水位検出用
容器13には、水位H1,H2,H3を検出するため長さ
の異なる3本の水位検出用電極棒16-1,16-2,16
-3が挿入されており、各水位検出用電極棒16-1,16
-2,16-3の下端位置は、夫々高さが異なり且つ1
-1,16-2,16-3の順に下端位置が高くなるよう配
設されている(H1<H2<H3)。各水位検出用電極棒
16-1,16-2,16-3により検出された水検出指令W
1,W2,W3は水位制御装置19へ与え得るようになっ
ている。
Reference numeral 13 denotes a water level detecting container used for detecting the level (water level) of water in the heating pipe 2 of the boiler main body 1. One end is connected to the bottom part and the upper part of the water level detecting container 13. The other ends of the communication pipes 14 and 15 are connected to the lower header 4 or the upper header 5. The water level detecting vessel 13 has three water level detecting electrode rods 16 -1 , 16 -2 , 16 having different lengths for detecting the water levels H 1 , H 2 , and H 3.
-3 is inserted, and each of the water level detection electrode rods 16 -1 , 16 -1
-2 and 16 -3 have different heights and 1
The lower ends are arranged in the order of 6 −1 , 16 −2 , 16 −3 (H 1 <H 2 <H 3 ). Water detection command W detected by each water level detection electrode rod 16 -1 , 16 -2 , 16 -3
1 , W 2 and W 3 can be given to the water level control device 19.

【0007】17,18は蒸気管11に接続された圧力
スイッチであって、蒸気管11を流れる蒸気の圧力Pが
予め定められた下限の圧力P1まで下降したら(P≦
1)、圧力スイッチ17から燃焼制御装置20へバー
ナ6を高燃焼状態に切替えるための作動指令V1を与え
得るようになっており、蒸気管11を流れる蒸気の圧力
Pが予め定められた上限の圧力P2よりも低く下限の圧
力P1よりも高い場合(P1<P<P2)には、圧力スイ
ッチ18から燃焼制御装置20へバーナ6を低燃焼状態
に切替えるための作動指令V2を与え得るようになって
いる。又燃焼制御装置20からは、バーナ6より噴射さ
れる燃料の流量を制御するための電磁弁等の弁(図示せ
ず)へ弁開指令V3を与え得るようになっていると共
に、燃焼制御装置20からは水位制御装置19へ圧力ス
イッチ17,18からの作動指令V1,V2を与え得るよ
うになっており、水位制御装置19からは給水ポンプ8
へ起動指令V4を与え得るようになっている。
[0007] 17, 18 is a pressure switch connected to the steam pipe 11, when lowered to the pressure P 1 is the lower limit that the pressure P of the steam flowing through the steam pipe 11 is predetermined (P ≦
P 1 ), an operation command V 1 for switching the burner 6 to the high combustion state can be given from the pressure switch 17 to the combustion control device 20, and the pressure P of the steam flowing through the steam pipe 11 is predetermined. When the pressure is lower than the upper limit pressure P 2 and higher than the lower limit pressure P 1 (P 1 <P <P 2 ), the operation command for switching the burner 6 to the low combustion state from the pressure switch 18 to the combustion control device 20. so that the can provide a V 2. Also from the combustion control device 20, with which is adapted to be given a valve opening command V 3 to the valve such as an electromagnetic valve for controlling the flow rate of the fuel injected from the burner 6 (not shown), fuel control The operation commands V 1 and V 2 from the pressure switches 17 and 18 can be given from the device 20 to the water level control device 19, and the water supply pump 8 can be supplied from the water level control device 19.
It is adapted to be given a start-up command V 4 to.

【0008】上記多管式貫流ボイラにおいては、給水ポ
ンプ8からの水は給水管7を送給されてボイラ本体1の
下部管寄せ4へ導入され、下部管寄せ4から加熱管2へ
導入されたうえバーナ6から噴射された燃料が燃焼する
ことにより発生する熱により加熱されて蒸気となり、該
蒸気は上部管寄せ5から蒸気管11を通って気水分離器
10へ導入され、該気水分離器10で水分を除去された
蒸気は、蒸気使用先へ送給されて消費され、気水分離器
10で分離された水は降水管12から下部管寄せ4へ戻
される。
In the multi-tube once-through boiler, water from a water supply pump 8 is supplied to a water supply pipe 7 and is introduced into a lower header 4 of the boiler main body 1 and is introduced from the lower header 4 to the heating pipe 2. In addition, the fuel injected from the burner 6 is heated by the heat generated by the combustion to become steam, and the steam is introduced from the upper header 5 through the steam pipe 11 into the steam separator 10, The steam from which the moisture has been removed by the separator 10 is sent to the steam usage destination and consumed, and the water separated by the steam separator 10 is returned from the downcomer 12 to the lower header 4.

【0009】又、ボイラ本体1で生成された蒸気の圧力
Pが予め定めた下限の圧力P1まで下降している場合に
は、圧力スイッチ17から燃焼制御装置20へ高燃焼の
ための作動指令V1が与えられると共に燃焼制御装置2
0から燃料の流量を制御する全ての弁に弁開指令V3
与えられることにより全ての弁が開き、バーナ6から噴
射される燃料の流量が増加してバーナ6は高燃焼状態に
なり、更に前記蒸気の圧力Pが予め定められた上限の圧
力P2よりも低く下限の圧力P1よりも高い場合には、圧
力スイッチ18から燃焼制御装置20へ低燃焼のための
作動指令V2が与えられると共に燃焼制御装置20から
燃料の流量を制御する弁のうち所定の弁に弁開指令V3
が出力されなくなって当該弁が閉止し、バーナ6から噴
射される燃料の流量が減少してバーナ6は低燃焼状態と
なり、蒸気の圧力Pが予め定めた上限の圧力P2に達す
ると、圧力スイッチ17,18からは作動指令V1,V2
が出力されず、従って、燃焼制御装置20からは弁開指
令V3が出力されなくなることにより燃料の流量と制御
する弁は全て閉止し、バーナ6からは燃料が噴射され
ず、バーナ6は停止する。
When the pressure P of the steam generated in the boiler main body 1 has decreased to a predetermined lower limit pressure P 1, an operation command for high combustion is sent from the pressure switch 17 to the combustion control device 20. V 1 is given and the combustion control device 2
All valve opening by 0 to be given the valve opening command V 3 to all valves that control the flow of fuel from the burner 6 the flow rate of the fuel injected from the burner 6 is increased in a high combustion state, further, when the pressure P of the steam is higher than the lower limit pressure P 1 of lower than the pressure P 2 of the predetermined upper limit, the actuation command V 2 for low combustion from the pressure switch 18 to the combustion control device 20 A valve opening command V 3 is given to a predetermined valve among the valves that are given and control the fuel flow rate from the combustion control device 20.
Is no longer output, the valve closes, the flow rate of fuel injected from the burner 6 decreases, the burner 6 enters a low combustion state, and when the steam pressure P reaches a predetermined upper limit pressure P 2 , the pressure Operation commands V 1 , V 2 from switches 17 and 18
There is not outputted, therefore, the combustion control unit 20 closes all valves to control the flow rate of the fuel by the valve opening command V 3 is not output, the fuel is not injected from the burner 6, the burner 6 is stopped I do.

【0010】一方、上記多管式貫流ボイラにおいては、
上述のごとき高燃焼−低燃焼−停止のいわゆる三位置制
御を行う際には、加熱管2内の水位の制御が行われる。
On the other hand, in the multi-tube once-through boiler,
When performing the so-called three-position control of high combustion-low combustion-stop as described above, control of the water level in the heating pipe 2 is performed.

【0011】例えば、バーナ6が高燃焼状態で圧力スイ
ッチ17の作動指令V1が燃焼制御装置20を介して水
位制御装置19へ与えられている場合には、水位検出用
容器13内の水位はH1とH2との間に位置するよう制御
する必要がある。従って、例えば、バーナ6が高燃焼状
態の際に水位が水位検出用容器13内のH2とH3との間
にあり、水位検出用電極棒16-1,16-2から水検出指
令W1,W2が水位制御装置19へ与えられている場合に
は、燃焼制御装置20から給水ポンプ8に起動指令V4
は与えられず、給水ポンプ8は停止している。
For example, when the operation command V 1 of the pressure switch 17 is given to the water level control device 19 via the combustion control device 20 while the burner 6 is in the high combustion state, the water level in the water level detection container 13 becomes It is necessary to control so as to be located between H 1 and H 2 . Thus, for example, between the water level in the burner 6 is high combustion state of H 2 and H 3 in the water level detection chamber 13, the water level detecting electrode bars 16 -1, 16 -2 to water detection command W When W 1 and W 2 are given to the water level control device 19, the start command V 4 is sent from the combustion control device 20 to the water supply pump 8.
Is not given, and the water supply pump 8 is stopped.

【0012】給水ポンプ8が停止したままバーナ6が高
燃焼状態を継続すると、加熱管2内の水位延いては水位
検出用容器13内の水位は低下するが、水位がH1より
も僅かに下降して、水位検出用電極棒16-1によっても
水が検出されなくなると、水検出指令W1,W2,W3
水位制御装置19へ与えられず、このため水位制御装置
19から給水ポンプ8に起動指令V4が与えられること
により給水ポンプ8が起動され、水は給水ポンプ8によ
り下部管寄せ4へ送給される。而して、加熱管2内の水
位が上昇することにより水位検出用容器13内の水位が
2まで上昇し、水位検出用電極棒16-1,16-2によ
り水が検出されると、水検出指令W1,W2が水位制御装
置19へ与えられ、給水ポンプ8には起動指令V4が与
えられなくなるため、給水ポンプ8は再び停止する。
[0012] while the burner 6 the water supply pump 8 is stopped to continue the high combustion state, but In its water level extension of the heating pipe 2 decreases water level in the water level detection chamber 13, the water level is slightly above H 1 lowered, when the water by the water level detecting electrode bars 16 -1 is not detected, the water detection command W 1, W 2, W 3 are not given to the level control unit 19, the water supply from this for the water level control device 19 When a start command V 4 is given to the pump 8, the water supply pump 8 is started, and water is supplied to the lower header 4 by the water supply pump 8. And Thus, the water level in the water level detection container 13 by the water level in the heating pipe 2 is increased rises to H 2, the water level detecting electrode bars 16 -1 by 16 -2 When water is detected, Since the water detection commands W 1 and W 2 are given to the water level control device 19 and the start-up command V 4 is no longer given to the water supply pump 8, the water supply pump 8 is stopped again.

【0013】バーナ6が低燃焼状態の際には、水位検出
用容器13内の水位はH2とH3との間に位置するように
しなければならないため、水位がH3に達して水位検出
用電極棒16-1,16-2,16-3により水が検出される
場合には、給水ポンプ8は停止しており、水位がH2
りも僅かに停止して水位検出用電極棒16-2,16-3
よって水が検出されなくなると、水位制御装置19から
の起動指令V4により給水ポンプ8は起動され、水位が
上昇してH3に達し水位検出用電極棒16-1,16-2
16-3により水が検出されるようになると、給水ポンプ
8には起動指令V4が与えられなくなるため、給水ポン
プ8は再び停止する。
When the burner 6 is in a low combustion state, the water level in the water level detecting container 13 must be located between H 2 and H 3 , so that the water level reaches H 3 and the water level is detected. When water is detected by the electrode rods 16 -1 , 16 -2 , and 16 -3 , the water supply pump 8 is stopped, and the water level stops slightly more than H 2 and the water level detection electrode rods 16. -2, 16 the water by -3 is not detected, the start command V 4 from the level control unit 19 water supply pump 8 is activated, the water level detecting electrode bars 16 -1 reached H 3 water level rises, 16 -2 ,
When the 16 -3 water is to be detected, the water supply pump 8 for no longer given start command V 4, the water supply pump 8 is stopped again.

【0014】バーナ6の燃焼状態すなわちボイラ負荷に
よってボイラ本体1の加熱管2内における水位を異なる
高さに制御するのは次のような理由による。すなわち、
乾き度の良好な蒸気を得るための水位は、図5の傾斜曲
線状の実線イ,ロで挟まれた領域Aに示すように、ボイ
ラ負荷により異なり、ボイラ負荷が高負荷の場合は、水
位を下げないと生成された蒸気に多量の水分が混入して
蒸気乾き度が低下する虞れがあり、又ボイラ負荷が低負
荷の場合には、水位を上げないと加熱管2の温度が上昇
し過ぎて加熱管2が焼損する虞れがあるためである。図
5中、実線イよりも上方にある領域Bは蒸気乾き度悪化
領域、実線ロよりも下方にある領域Cは加熱管のメタル
温度上昇領域であり、白枠X1の下端は高燃焼状態の際
の下限の水位H1を、白枠X1の上限は高燃焼状態の際の
上限の水位H2を、白枠X2の下限は低燃焼状態の際の下
限の水位H2を、白枠X2の上限は低燃焼状態の際の上限
の水位H3を夫々表わしている。
The water level in the heating pipe 2 of the boiler body 1 is controlled to a different height depending on the combustion state of the burner 6, that is, the boiler load, for the following reasons. That is,
The water level for obtaining steam with good dryness differs depending on the boiler load, as shown in the area A between the solid lines a and b in FIG. 5, and when the boiler load is high, the water level is high. If the boiler load is low, if the boiler load is low, the temperature of the heating pipe 2 will rise unless the water level is raised. This is because there is a possibility that the heating tube 2 may be burned out due to excessive heating. In FIG. 5, the region B which is above the solid line b is steam the dryness worse region, the region C is located below the solid line b is a metal temperature rise region of the heat pipe, the lower end of the white frame X 1 is a high combustion state the lower limit level H 1 of the time, the upper limit of the white frame X 1 is an upper limit water level of H 2 during a high combustion state, the lower limit of the white frame X 2 is the water level of H 2 the lower limit of the time of low combustion state, the upper limit of the white frame X 2 is an upper limit water level H 3 of the time of the low combustion state represents respectively.

【0015】又、バーナ6が高燃焼状態の場合に加熱管
2内の水位を下げるのは、高燃焼状態の場合は加熱管2
上方における蒸気の圧力が低く、気泡の割合が多いた
め、見掛け上の水位が低くても実質的な水位が高く、十
分に加熱管2の冷却を行うことができるからであり、バ
ーナ6が低燃焼状態の場合に加熱管2内の水位を上げる
のは、低燃焼状態の場合は加熱管2上方の蒸気圧力が高
く、加熱管2上部の気泡の割合が少ないため、見掛け上
の水位が低いと実質的な水位も低く、十分に加熱管2の
冷却を行うことができないからである。
When the burner 6 is in a high combustion state, the water level in the heating pipe 2 is lowered because the heating pipe 2 is in a high combustion state.
This is because the vapor pressure in the upper part is low and the proportion of bubbles is large, so that even when the apparent water level is low, the substantial water level is high and the heating pipe 2 can be sufficiently cooled. The reason for raising the water level in the heating pipe 2 in the combustion state is that the apparent water level is low in the low combustion state because the steam pressure above the heating pipe 2 is high and the proportion of bubbles above the heating pipe 2 is small. This is because the substantial water level is low and the heating tube 2 cannot be sufficiently cooled.

【0016】[0016]

【発明が解決しようとする課題】上述の多管式貫流ボイ
ラにおいて水位の制御する範囲を変更するのは、バーナ
6の燃焼状態が高燃焼や低燃焼に切替った場合であり、
上述のごとく燃焼状態に対応して加熱管2内の水位を制
御することにより、乾き度の良好な蒸気を得ることがで
き且つボイラ寿命の長期化を図ることができる。
The range in which the water level is controlled in the above-mentioned multi-tube once-through boiler is changed when the combustion state of the burner 6 is switched to high combustion or low combustion.
By controlling the water level in the heating pipe 2 according to the combustion state as described above, it is possible to obtain steam having a good dryness and to prolong the life of the boiler.

【0017】しかしながら、例えば、高燃焼状態や低燃
焼状態における蒸気の圧力が全体的に比較的高い場合に
は、乾き度の良好な蒸気を得るための水位は、図5の白
枠X 1,X2に示すように実線イ,ロで挟まれた領域A内
にあっても、蒸気の圧力が全体的に低下した場合には、
良好な乾き度の蒸気を得るための水位は、図5の点線
ハ,ニに挟まれた領域A’に移ることになり、この場合
には、白枠X1,X2に示す水位の制御範囲では、水位が
蒸気乾き度悪化の領域Bに入ってしまう。又逆に、蒸気
の圧力が全体的に上昇した場合には、領域Aは図5の場
合よりも上方へずれ、白枠X1,X2に示す水位の制御範
囲では、水位が加熱管2のメタル温度が上昇する領域C
に入ってしまう。更に、蒸気の圧力は、バーナ6が高燃
焼状態の間或いは低燃焼状態の間中一定不変なわけでは
なく、同じ燃焼状態においても蒸気の圧力は時間的に変
化する。このため燃焼状態に対応して予め設定した水位
を変更することができないと、蒸気の圧力変化の程度に
よっては、蒸気の乾き度が不十分となったり、或いは加
熱管2のメタル温度が上昇し過ぎたりする虞れがある。
However, for example, a high combustion state or a low
When the steam pressure in the burning state is relatively high overall
Indicates the water level for obtaining steam with good dryness, as shown in FIG.
Frame X 1, XTwoAs shown in the figure, the area A between the solid lines A and B
However, if the steam pressure drops overall,
The water level for obtaining steam with good dryness is indicated by the dotted line in FIG.
It moves to the area A 'sandwiched between c and d. In this case,
Has a white frame X1, XTwoIn the water level control range shown in
It enters the region B where the steam dryness is deteriorated. Conversely, steam
If the pressure of the whole rises, the area A
White frame X1, XTwoWater level control range shown in
In the area, the water level is in the region C where the metal temperature of the heating pipe 2 rises.
Will enter. Further, the steam pressure is such that the burner 6 is highly flammable.
Not constant during burning or low combustion
And the steam pressure changes with time even in the same combustion state.
Become Therefore, the water level set in advance according to the combustion state
Can not be changed, the degree of steam pressure changes
Therefore, the steam may not be dry enough or
There is a possibility that the metal temperature of the heat tube 2 may rise too much.

【0018】本発明は上述の実情に鑑み、同じ燃焼状態
において蒸気の圧力が変動した場合に、その圧力に対応
して加熱管2内の水位を変更し得るようにすることを目
的としてなしたものである。
The present invention has been made in view of the above circumstances, and has as its object to be able to change the water level in the heating pipe 2 according to the pressure when the steam pressure fluctuates in the same combustion state. Things.

【0019】[0019]

【課題を解決するための手段】上記目的を達成するため
に、第1の手段では、円周方向へ所要の間隔で立設され
た複数の加熱管2及び該加熱管2の下端に接続され且つ
給水ポンプ8からの水を導入し得るようにした下部管寄
せ4並に前記加熱管2の上端に接続され且つ生成された
蒸気を送出す上部管寄せ5を有するボイラ本体1と、該
ボイラ本体1内に加熱管2により包囲されて形成された
燃焼室3へ燃料を噴射するバーナ6と、下部が下部管寄
せ4と連通し且つ上部が上部管寄せ5と連通した水位検
出用容器13と、該水位検出用容器13内に下端が夫々
異なる高さに位置するよう挿入された第1、第2、第
3、第4の4本の水位検出用電極棒16−4,1
−1,16−2,16−3とを備え、且つ前記第1、
第2、第3、第4の水位検出用電極棒16−4,16
−1,16−2,16−3により水位検出用容器13内
の水位を制御するようにした多管式貫流ボイラの水位制
御方法において、前記バーナ6が高燃焼状態で且つ生成
された蒸気の圧力Pが基準となる圧力Pよりも高い場
合には、前記水位検出用容器13内の水位を、第2の
位検出用電極棒16−1の下端と、該第2の水位検出用
電極棒16−1の下端よりも下端が高い位置にある第3
水位検出用電極棒16−2の下端との間に略位置する
よう制御し、前記バーナ6が高燃焼状態で且つ生成され
た蒸気の圧力Pが基準となる圧力Pよりも低い場合に
は、前記水位検出用容器13内の水位を、前記第2の
位検出用電極棒16−1の下端と該第2の水位検出用電
極棒16−1の下端よりも下端が低い位置にある第1の
水位検出用電極棒16−4との間に略位置するよう制御
し、前記バーナ6が低燃焼状態で且つ生成された蒸気の
圧力Pが基準となる圧力Pよりも高い場合には、前記
水位検出用容器13内の水位を、下端が前記第2の水位
検出用電極棒16−1の下端よりも高い位置にある第3
水位検出用電極棒16−2の下端と該第3の水位検出
用電極棒16−2の下端よりも下端が高い位置にある
4の水位検出用電極棒16−3の下端との間に略位置す
るよう制御し、前記バーナ6が低燃焼状態で且つ生成さ
れた蒸気の圧力Pが基準となる圧力Pよりも低い場合
には、前記水位検出用容器13内の水位を、前記第3の
水位検出用電極棒16−2の下端と該第3の水位検出用
電極棒16−2の下端よりも下端が低い位置にある第2
水位検出用電極棒16−1の下端との間に略位置する
よう制御しており、第2の手段では、円周方向へ所要の
間隔で立設された複数の加熱管2及び該加熱管2の下端
に接続され且つ給水ポンプ8からの水を導入し得るよう
にした下部管寄せ4並に前記加熱管2の上端に接続され
且つ生成された蒸気を送出す上部管寄せ5を有するボイ
ラ本体1と、該ボイラ本体1内に加熱管2により包囲さ
れて形成された燃焼室3へ燃料を噴射するバーナ6と、
前記上部管寄せ5から送給された蒸気から水分を分離し
て戻す気水分離器10と、下部が下部管寄せ4と連通さ
れ且つ上部が上部管寄せ5と連通された水位検出用容器
13と、該水位検出用容器13内に下端が夫々異なる高
さに位置するよう挿入された第1、第2、第3、第4の
4本の水位検出用電極棒16−4,16−1,1
−2,16−3とを備え、且つ第1、第2、第3、第
4の水位検出用電極棒16−4,16−1,16−2
16−3により水位検出用容器13内の水位を制御する
ようにした多管式貫流ボイラの水位制御方法において、
前記バーナ6が高燃焼状態で且つ気水分離器10で分離
された水の電気伝導度Kが基準となる電気伝導度K
りも小さい場合には、前記水位検出用容器13内の水位
を、第2の水位検出用電極棒16−1の下端と該第2の
水位検出用電極棒16−1の下端よりも下端が高い位置
にある第3の水位検出用電極棒16−2の下端との間に
略位置するよう制御し、前記バーナ6が高燃焼状態で且
つ気水分離器10で分離された水の電気伝導度Kが基準
となる電気伝導度Kよりも大きい場合には、前記水位
検出用容器13内の水位を、前記第2の水位検出用電極
棒16−1の下端と該第2の水位検出用電極棒16−1
の下端よりも下端が低い位置にある第1の水位検出用電
極棒16−4との間に略位置するよう制御し、前記バー
ナ6が低燃焼状態で且つ気水分離器10で分離された水
の電気伝導度Kが基準となる電気伝導度Kよりも小さ
い場合には、前記水位検出用容器13内の水位を、下端
が前記第2の水位検出用電極棒16−1の下端よりも高
い位置にある第3の水位検出用電極棒16−2の下端と
第3の水位検出用電極棒16−2の下端よりも下端が
高い位置にある第4の水位検出用電極棒16−3の下端
との間に略位置するよう制御し、前記バーナ6が低燃焼
状態で且つ気水分離器10で分離された水の電気伝導度
Kが基準となる電気伝導度Kよりも大きい場合には、
前記水位検出用容器13内の水位を、前記第3の水位検
出用電極棒16−2の下端と該第3の水位検出用電極棒
16−2の下端よりも下端が低い位置にある第2の水位
検出用電極棒16−1の下端との間に略位置するよう制
御している。
In order to achieve the above object, in a first means, a plurality of heating tubes 2 erected at predetermined intervals in a circumferential direction and a lower end of the heating tubes 2 are connected. A boiler body 1 having an upper header 5 connected to the upper end of the heating pipe 2 and delivering generated steam, and a lower header 4 capable of introducing water from a water supply pump 8; A burner 6 for injecting fuel into a combustion chamber 3 formed in the main body 1 and surrounded by a heating pipe 2; and a water level detecting container 13 having a lower part communicating with the lower header 4 and an upper part communicating with the upper header 5. And the first, second, and second inserted in the water level detection container 13 so that the lower ends thereof are located at different heights .
Third, fourth four water level detection electrode rods 16-4 , 1
6 -1 , 16 -2 , 16-3 , and the first,
Second, third, and fourth electrode rods for water level detection 16-4 , 16
-1, 16 -2, 16 -3 by the water level control method of a multi-tube once-through boiler so as to control the water level in the water level detection container 13, the steam in which the burner 6 is and generated by the high combustion state If higher than the pressure P O of the pressure P becomes the reference has a water level in the water level detection chamber 13, and the lower end of the second water <br/> level detecting electrode bars 16 -1, the second The lower end of which is higher than the lower end of the water level detection electrode rod 16-1 .
The controlled so as to substantially located between the lower end of the water level detecting electrode bars 16 -2 when the burner 6 is less than the pressure P O of the pressure P is the reference of the steam and generated by the high combustion state lower end, the water level in the water level detection chamber 13, the lower end of the second water <br/> level detecting electrode bars 16 -1 of the lower end and the second water level detecting electrode bars 16 -1 a first <br/> controlled to substantially located between the water level detecting electrode bars 16 -4, the pressure P of the steam the burner 6 is and generated in the low combustion state is reference in the low position When the pressure is higher than the predetermined pressure P O , the water level in the water level detection container 13 is adjusted to the third level whose lower end is higher than the lower end of the second water level detection electrode rod 16-1 .
The lies in the lower end position higher than the lower end and the lower end of the third water level detecting electrode bars 16 -2 water level detecting electrode bars 16 -2
4 is controlled so as to substantially located between the lower end of the water level detecting electrode bars 16 -3, the case burner 6 is less than the pressure P O of the pressure P of the steam and generated in the low combustion state becomes the reference to the water level of the water level detection chamber 13, the third <br/> water level detecting electrode bars 16 -2 bottom and said third lower than the lower end of the water level detecting electrode bars 16 -2 Is lower in the second position
Of which is controlled so as to substantially located between the lower end of the water level detecting electrode bars 16 -1, in the second means, a plurality of heating tube 2 and the heating erected at required intervals in the circumferential direction It has a lower header 4 connected to the lower end of the pipe 2 and capable of introducing water from the water supply pump 8 and an upper header 5 connected to the upper end of the heating pipe 2 and for delivering generated steam. A boiler main body 1 and a burner 6 for injecting fuel into a combustion chamber 3 formed in the boiler main body 1 and surrounded by a heating tube 2;
A steam-water separator 10 for separating and returning moisture from the steam sent from the upper header 5, and a water level detecting container 13 having a lower part communicating with the lower header 4 and an upper part communicating with the upper header 5. And the first, second, third, and fourth inserted in the water level detection container 13 so that the lower ends thereof are located at different heights .
Four water level detecting electrode rods 16-4 , 16-1 , 1
6 -2 , 16-3 , and the first, second, third, and
4, the water level detection electrode rods 16-4 , 16-1 , 16-2 ,
By 16 -3 in water level control method of a multi-tube once-through boiler so as to control the water level in the water level detection container 13,
Wherein when the burner 6 and steam-water separator less than 10 in the electric conductivity K of the separated water is the reference electric conductivity K O in a high combustion state, the water level in the water level detection container 13 third water level detecting electrode bars 16 lower than the lower end of the second water level detecting electrode bars 16 -1 of the lower end and said second <br/> water level detecting electrode bars 16 -1 is in the high position controlled to substantially located between the lower end of -2 the burner 6 than the electrical conductivity K O to and electric conductivity K of separated water in steam-water separator 10 is the reference in high combustion state If large, the water level of the water level detection chamber 13, the second water level detecting electrode bars 16 -1 of the lower end and the second water level detecting electrode bars 16 -1
Controlled to substantially located between the first water level detecting electrode bars 16 -4 at the lower end is lower than the lower end of the burner 6 is separated by steam-water separator 10 and at a low combustion state when the electric conductivity K of the water is less than the electrical conductivity K O as a reference is the water level in the water level detection chamber 13, from the lower end of the lower end second water level detecting electrode bars 16 -1 third fourth level detecting electrode bars 16 lower end and said third lower than the lower end of the water level detecting electrode bars 16 -2 water level detecting electrode bars 16 -2 is in the high position in the even higher position controlled to substantially located between the lower end of -3, the burner 6 is than the electrical conductivity K O the electric conductivity K of separated water in steam-water separator 10 and at a low combustion state becomes the reference If larger,
The water level in the water level detection container 13, first the lower end is lower than the lower end of the third water level detecting electrode bars 16 -2 bottom and the third water level detecting electrode bars 16 -2 2 Is controlled so as to be located substantially between the lower end of the water level detection electrode rod 16-1 .

【0020】[0020]

【作用】第1の手段では、バーナ6が高燃焼状態で且つ
蒸気の圧力Pが基準の圧力P0よりも高い場合には、水
位検出用容器13内の水位は、水位検出用電極棒1
-1,16-2の下端間に略位置するよう制御され、バー
ナ6が高燃焼状態で且つ蒸気の圧力Pが基準の圧力P0
よりも低い場合は、前記水位検出用容器13内の水位
は、水位検出用電極棒16-4,16-1の下端間に略位置
するよう制御され、バーナ6が低燃焼状態で且つ蒸気の
圧力Pが基準の圧力P0よりも高い場合は、水位検出用
容器13内の水位は、水位検出用電極棒16-2,16-3
の下端間に略位置するよう制御され、バーナ6が低燃焼
状態で且つ蒸気の圧力Pが基準の圧力P0よりも低い場
合は、前記水位検出用容器13内の水位は水位検出用電
極棒16-1,16-2の下端間に略位置するよう制御さ
れ、第2の手段では、バーナ6が高燃焼状態で且つ気水
分離器10により蒸気から分離された水の電気抵抗Kが
基準の電気伝導度KOよりも小さい場合には、水位検出
用容器13の水位は、水位検出用電極棒16-1,16-2
の下端間に略位置するよう制御され、バーナ6が高燃焼
状態で且つ気水分離器10で蒸気から分離された水の電
気伝導度Kが基準の電気伝導度KOよりも大きい場合に
は、水位検出用容器13の水位は、水位検出用電極棒1
-2,16-3の下端間に略位置するよう制御され、バー
ナ6が低燃焼状態で且つ気水分離器10により蒸気から
分離された水の電気伝導度Kが基準の電気伝導度KO
りも小さい場合には、水位検出用容器13の水位は、水
位検出用電極棒16-2,16-3の下端間に略位置するよ
う制御され、バーナ6が低燃焼状態で且つ気水分離器1
0で蒸気から分離された水の電気伝導度Kが基準の電気
伝導度K Oよりも大きい場合には、水位検出用容器13
の水位は、水位検出用電極棒16- 1,16-2の下端間に
略位置するよう制御される。
According to the first means, the burner 6 is in a high combustion state and
The steam pressure P is the standard pressure P0Higher than the water
The water level in the level detecting container 13 is the water level detecting electrode rod 1.
6-1, 16-2Is controlled to be located approximately between the lower ends of the
The pressure 6 is in a high combustion state and the steam pressure P is a reference pressure P.0
Lower than the water level in the water level detection container 13.
Is a water level detection electrode rod 16-Four, 16-1Approximately between the lower ends of
The burner 6 is in a low combustion state and the steam is
Pressure P is the standard pressure P0If higher than, for water level detection
The water level in the container 13 is equal to the water level detecting electrode rod 16.-2, 16-3
The burner 6 is controlled to be located almost between the lower ends of the
In a state where the steam pressure P is a reference pressure P0Lower than
The water level in the water level detection container 13 is
Pole stick 16-1, 16-2Controlled to be located approximately between the lower ends of
In the second means, the burner 6 is in a high combustion state and
The electrical resistance K of the water separated from the steam by the separator 10 is
Reference electric conductivity KOIf less than, water level detection
The water level of the container 13 is determined by the electrode rod 16 for detecting the water level.-1, 16-2
The burner 6 is controlled so as to be located approximately between the lower ends of the
Of water separated from steam by the steam-water separator 10
Electric conductivity K based on air conductivity KOGreater than
Is the water level of the water level detection container 13,
6-2, 16-3Is controlled to be located approximately between the lower ends of the
The fuel 6 is in a low combustion state and is separated from steam by the steam separator 10.
The electrical conductivity K of the separated water is the standard electrical conductivity K.OYo
When the water level is lower than the water level,
Position detection electrode rod 16-2, 16-3It is located almost between the lower ends of
The burner 6 is in a low combustion state and the steam-water separator 1
Electricity based on the electric conductivity K of water separated from steam at 0
Conductivity K OIs larger than the water level detection container 13.
Of the water level detection electrode rod 16- 1, 16-2Between the lower ends of
It is controlled to be located approximately.

【0021】従って、バーナ6の燃焼状態が高燃焼状態
或いは低燃焼状態の一定の燃焼状態にある場合に、生成
された蒸気の圧力Pが変化したり或いは気水分離器10
で分離された水の電気伝導度Kが変化したりしても、乾
き度の良好な蒸気が得られ且つ加熱管2の過度な温度上
昇が防止される。
Therefore, when the combustion state of the burner 6 is a constant combustion state such as a high combustion state or a low combustion state, the pressure P of the generated steam changes or the steam-water separator 10
Even if the electric conductivity K of the water separated in the step changes, steam with good dryness can be obtained, and an excessive rise in the temperature of the heating tube 2 can be prevented.

【0022】[0022]

【実施例】以下、本発明の実施例を添付図面を参照しつ
つ説明する。
Embodiments of the present invention will be described below with reference to the accompanying drawings.

【0023】図1は本発明の一実施例で、基本的構成は
図4に示す従来のものと略同じであり、図4に示すもの
と同一のものには同一の符号が付してある。
FIG. 1 shows an embodiment of the present invention. The basic structure is substantially the same as the conventional one shown in FIG. 4, and the same parts as those shown in FIG. .

【0024】16-4は水位H1よりも低い水位H4を検出
するための水位検出用電極棒であって、該水位検出用電
極棒16-4は、図4に示す水位検出用電極棒16-1,1
-2,16-3と同様、水位検出用容器13内に挿入さ
れ、且つ常用圧力が低下した場合にも水位の制御を行い
得るよう、水位検出用電極棒16-4の下端は水位検出用
電極棒16-1の下端よりも下方に位置している。又水位
検出用電極棒16-4により検出した水検出指令W4は水
位制御装置19へ与え得るようになっており、気水分離
器10の上部に接続した圧力スイッチ21は蒸気の圧力
Pが予め定めた基準の圧力P0よりも低い場合には作動
指令VOを水位制御装置19へ与え得るようになってい
る。更に圧力スイッチ17,18から燃焼制御装置20
を介して与えられた作動指令V1,V2と圧力スイッチ2
1から与えられた作動指令VOと水位検出用電極棒16
-1,16-2,16-3,16-4から与えられた水検出指令
1,W2,W3,W4とに基いて、水位制御装置19から
は給水ポンプ8に起動指令V4を出力し得るようになっ
ている。
[0024] 16 -4 a water level detecting electrode bars for detecting the low water level H 4 than the water level H 1, the water level detecting electrode bars 16 -4, the water level detecting electrode bars shown in FIG. 4 16 -1 , 1
6-2, 16 similar to -3, is inserted into the water level detection chamber 13, and so that the common pressure may perform control of the water level even when the drop, the lower end of the water level detecting electrode bars 16 -4 level detection It is located below the lower end of the electrode bar 16-1 . The water detection command W 4 detected by the water level detection electrode rod 16 -4 can be given to the water level control device 19, and the pressure switch 21 connected to the upper part of the steam separator 10 detects the steam pressure P. When the pressure is lower than a predetermined reference pressure P 0 , an operation command V O can be given to the water level control device 19. Furthermore, the combustion control device 20
Commands V 1 , V 2 given through the pressure switch 2
The operation command V O given from 1 and the water level detection electrode rod 16
Based on the water detection commands W 1 , W 2 , W 3 , and W 4 given from -1 , 16 -2 , 16 -3 , and 16 -4 , the water level control device 19 issues a start command V to the feed water pump 8 from the water level control device 19. 4 can be output.

【0025】バーナ6が通常の高燃焼状態で且つ気水分
離器10内の蒸気の圧力Pが基準の圧力P0よりも高い
場合には、水位検出用容器13内の水位は、水位検出用
電極棒16-1の下端と16-2の下端の間、すなわち水位
1とH2(H1<H2)の間にあるよう制御が行われる
が、この場合には圧力スイッチ17からの作動指令V1
が燃焼制御装置20を介して水位制御装置19に与えら
れると共に圧力スイッチ21からの作動指令VOが水位
制御装置19へ与えられている。而して、水位が水位検
出用電極棒16-1の下端よりも僅かに低下して水が水位
検出用電極棒16- 1により検出されないようになると、
水位検出用電極棒16-4によって検出された水検出指令
4のみが水位制御装置19へ与えられ、この場合に
は、水位制御装置19からの起動指令V4により給水ポ
ンプ8が駆動され、水は給水ポンプ8により給水管7か
らボイラ本体1の下部管寄せ4へ送給されて加熱管2内
の水が上昇すると共に連通管14を介して水位検出用容
器13内の水位が上昇する。
When the burner 6 is in the normal high combustion state and the steam pressure P in the steam separator 10 is higher than the reference pressure P 0 , the water level in the water level detecting container 13 is between the lower end of the electrode rod 16 -1 of the bottom and 16 -2, i.e. controlled to lie between the water level H 1 and H 2 (H 1 <H 2 ) takes place, from the pressure switch 17 is in this case Operation command V 1
Is given to the water level control device 19 via the combustion control device 20, and an operation command V O from the pressure switch 21 is given to the water level control device 19. And Thus, the water level is lowered slightly from the lower end of the water level detecting electrode bars 16 -1 water level detecting electrode bars 16 - When not detected by 1,
Only the water detection command W 4 detected by the water level detection electrode rod 16 -4 is given to the water level control device 19. In this case, the water supply pump 8 is driven by the start command V 4 from the water level control device 19, The water is supplied from the water supply pipe 7 to the lower header 4 of the boiler body 1 by the water supply pump 8, and the water in the heating pipe 2 rises and the water level in the water level detection container 13 rises via the communication pipe 14. .

【0026】又水位検出用容器13内の水位がH1より
も僅かに上昇して水位検出用電極棒16-4,16-1によ
り水が検出されるようになると、水検出指令W4,W1
水位制御装置19に与えられるが、この場合は水位制御
装置19からの起動指令V4により給水ポンプ8は引続
き駆動され、更に加熱管2及び水位検出用容器13内の
水位がH2よりも僅かに上昇して水位検出用電極棒16
-4,16-1,16-2により水が検出されるようになる
と、水検出指令W4,W1,W2が水位制御装置19に与
えられ、水位制御装置19からは起動指令V4が出力さ
れなくなる結果、給水ポンプ8は停止する。
When the water level in the water level detection container 13 rises slightly above H 1 and water is detected by the water level detection electrode rods 16 -4 and 16 -1 , the water detection command W 4 , W 1 is given to the level control unit 19, the water supply pump 8 by the activation command V 4 from the level control unit 19 in this case is subsequently driven further water level in the heating tube 2 and the water level detection container 13 is H 2 The water level detecting electrode rod 16
-4, 16 -1, 16 becomes as water is detected by -2, water detection command W 4, W 1, W 2 is supplied to the level control unit 19, a start command V 4 from the level control unit 19 As a result, the water supply pump 8 stops.

【0027】バーナ6が通常の低燃焼状態で且つ気水分
離器10内の蒸気の圧力Pが燃焼状態により定まる基準
の圧力P0よりも高い場合には、水位検出用容器13内
の水位は、水位検出用電極棒16-2と16-3との間、す
なわち水位H2とH3(H2<H3)の間にあるように制御
が行われるが、この場合には圧力スイッチ18からの作
動指令V2が燃焼制御装置20を介して水位制御装置1
9へ与えられると共に圧力スイッチ21からの作動指令
Oが水位制御装置19へ与えられている。而して水が
水位検出用電極棒16-2の下端よりも僅かに低下して水
が水位電極棒16-2により検出されないようになると、
水位検出用電極棒16-4,16-1によって検出された水
検出指令W4,W1が水位制御装置19に与えられ、水位
制御装置19からの起動指令V4により給水ポンプ8が
駆動され、ボイラ本体1の加熱管2内の水位及び水位検
出用容器13内の水位が上昇する。
When the burner 6 is in a normal low combustion state and the steam pressure P in the steam separator 10 is higher than a reference pressure P 0 determined by the combustion state, the water level in the water level detecting container 13 becomes , between the water level detecting electrode bars 16 -2 and 16 -3, that is, control is performed such that between the water level H 2 and H 3 (H 2 <H 3 ), in this case pressure switch 18 operation command V 2 from via the combustion control device 20 water level controller 1
9 and an operation command V O from the pressure switch 21 is provided to the water level control device 19. When Thus to water so slightly lower than a lower end of the water level detecting electrode bars 16 -2 water not detected by the water level electrode rod 16 -2,
Water detection commands W 4 and W 1 detected by the water level detection electrode rods 16 -4 and 16 -1 are given to the water level control device 19, and the water supply pump 8 is driven by a start command V 4 from the water level control device 19. Then, the water level in the heating pipe 2 of the boiler body 1 and the water level in the water level detecting container 13 rise.

【0028】又水位検出用容器13内の水位がH2より
も僅かに上昇して水位検出用電極棒16-4,16-1,1
-2により水が検出されるようになっても、水検出指令
4,W1,W2が水位制御装置19に与えられて水位制
御装置19からの起動指令V4により給水ポンプ8は駆
動されているが、更に水位検出用容器13内の水位がH
3よりも僅かに上昇して水位検出用電極棒16-4,16
-1,16-2,16-3により水が検出されるようになる
と、水検出指令W4,W1,W2,W3が水位制御装置19
に与えられ、水位制御装置19からは起動指令V4が出
力されなくなる結果、給水ポンプ8は停止する。
The water level in the water level detecting container 13 is HTwoThan
Rises slightly and the water level detecting electrode rod 16-Four, 16-1, 1
6-2Even if water is detected by the
WFour, W1, WTwoIs supplied to the water level control device 19 to control the water level.
Start command V from control device 19FourFeed pump 8
The water level in the water level detecting container 13 is H
ThreeThe water level detecting electrode rod 16-Four, 16
-1, 16-2, 16-3Allows water to be detected
And the water detection command WFour, W1, WTwo, WThreeIs the water level control device 19
From the water level control device 19,FourComes out
As a result, the water supply pump 8 stops.

【0029】バーナ6が高燃焼状態で且つ気水分離器1
0内の蒸気の圧力Pが燃焼状態により定まる基準の圧力
0よりも低い場合には、圧力スイッチ17からの作動
指令V1が燃焼制御装置20を介して水位制御装置19
へ与えられると共に圧力スイッチ21からの作動指令V
Oが水位制御装置19に与えられ、水位検出用容器13
内の水位は、水位検出用電極棒16-4と16-1との間、
すなわち水位H4とH1(H4<H1)の間にあるよう制御
が行われる。このため、水位が水位検出用電極棒16-4
の下端よりも僅かに低下して水が水位検出用電極棒16
-4により検出されないようになると、水位検出用電極棒
16-4,16-1,16-2,16-3からの水検出指令
4,W1,W2,W3は水位制御装置19には与えられ
ず、この場合には、水位制御装置19からの起動指令V
4により給水ポンプ8が駆動され、水は給水ポンプ8に
よりボイラ本体1へ送給されて加熱管2の水位延いては
水位検出用容器13内の水位が上昇する。
The burner 6 is in a high combustion state and the steam-water separator 1
When the pressure P of the steam within 0 is lower than the reference pressure P 0 determined by the combustion state, the operation command V 1 from the pressure switch 17 is transmitted to the water level control device 19 via the combustion control device 20.
To the operation command V from the pressure switch 21
O is given to the water level control device 19 and the water level detection container 13
Water level is between the water level detection electrode rods 16 -4 and 16 -1
That is, control is performed so that the water level is between H 4 and H 1 (H 4 <H 1 ). For this reason, the water level is changed to the water level detection electrode rod 16-4.
The water is slightly lower than the lower end of the
-4, the water detection commands W 4 , W 1 , W 2 , W 3 from the water level detection electrode rods 16 -4 , 16 -1 , 16 -2 , 16 -3 are transmitted to the water level control device 19. In this case, the start command V from the water level control device 19 is not provided.
The water supply pump 8 is driven by 4 , and water is supplied to the boiler main body 1 by the water supply pump 8, and the water level of the heating pipe 2 and the water level in the water level detection container 13 rise.

【0030】又、水位検出用容器13内の水位がH4
より僅かに上昇して水位検出用電極棒16-4により水が
検出されるようになると、水検出指令W4が水位制御装
置19に与えられるが、この場合は水位制御装置19か
らの起動指令V4により給水ポンプ8は引続き駆動さ
れ、更に加熱管2及び水位検出用容器13内の水位がH
1よりも僅かに上昇して水位検出用電極棒16-4,16
-1により水が検出されるようになると、水検出指令
4,W1が水位制御装置19に与えられ、水位制御装置
19からは起動指令V4が出力されなくなる結果、給水
ポンプ8は停止する。
The water level in the water level detecting container 13 is HFourTo
The electrode rod 16 for detecting the water level which rises slightly more-FourWater
When it is detected, the water detection command WFourIs a water level control device
To the water level controller 19 in this case.
Start command VFourFeed pump 8 is continuously driven by
And the water level in the heating pipe 2 and the water level detecting container 13 is H
1The water level detecting electrode rod 16-Four, 16
-1When water is detected by the
WFour, W1Is supplied to the water level control device 19,
Starting command V from 19FourIs no longer output, resulting in water supply
The pump 8 stops.

【0031】バーナ6が低燃焼状態で且つ気水分離器1
0内の蒸気の圧力Pが燃焼状態により定まる基準の圧力
0よりも低い場合には、圧力スイッチ18からの作動
指令V2が燃焼制御装置20を介して水位制御装置19
へ与えられると共に圧力スイッチ21からの作動指令V
Oが水位制御装置19に与えられ、水位検出用容器13
内の水位は、水位検出用電極棒16-1と16-2の間、す
なわち水位H1とH2(H1<H2)の間にあるよう制御が
行われる。このため、水位が水位検出用電極棒16-1
下端よりも僅かに低下して、水が水位検出用電極棒16
-1,16-2,16-3により検出されず、水位検出用電極
棒16-4によってのみ検出されるようになると、水位検
出用電極棒16-1,16-2,16-3からは水検出指令W
1,W2,W3は水位制御装置19には与えられず、水位
検出用電極棒16-4からの水検出指令W4が水位制御装
置19に与えられることになり、この場合には、水位制
御装置19からの起動指令V4により給水ポンプ8が駆
動され、水は給水ポンプ8によりボイラ本体1へ送給さ
れて加熱管2内の水位延いては水位検出用容器13内の
水位が上昇する。
The burner 6 is in a low combustion state and the steam-water separator 1
When the pressure P of the steam within 0 is lower than the reference pressure P 0 determined by the combustion state, the operation command V 2 from the pressure switch 18 is transmitted via the combustion control device 20 to the water level control device 19.
To the operation command V from the pressure switch 21
O is given to the water level control device 19 and the water level detection container 13
Water level of the inner during the water level detecting electrode bars 16 -1 and 16 -2, that is controlled to lie between the water level H 1 and H 2 (H 1 <H 2 ) takes place. Therefore, the water level is lowered slightly from the lower end of the water level detecting electrode bars 16 -1, water level detecting electrode bars 16
-1 , 16 -2 , 16 -3 , but not detected by the water level detection electrode rod 16 -4 , the water level detection electrode rods 16 -1 , 16 -2 , 16 -3 Water detection command W
1, W 2, W 3 are not given to the level control unit 19, will be water detection command W 4 from the water level detecting electrode bars 16 -4 given level control device 19, in this case, The water supply pump 8 is driven by a start command V 4 from the water level control device 19, and water is supplied to the boiler main body 1 by the water supply pump 8 so that the water level in the heating pipe 2 and the water level in the water level detection container 13 are reduced. To rise.

【0032】又、水位検出用容器13内の水位がH1
りも僅かに上昇して水位検出用電極棒16-4,16-1
より水が検出されるようになると、水検出指令W4,W1
が水位制御装置19へ与えられるようになるが、この場
合は、水位制御装置19からの起動指令V4により給水
ポンプ8は引続き駆動され、更に加熱管2及び水位検出
用容器13内の水位がH2よりも僅かに上昇して水位検
出用電極棒16-4,16-1,16-2により水が検出され
るようになると、水検出指令W4,W1,W2が水位制御
装置19に与えられ、水位制御装置19からは起動指令
4が出力されなくなる結果、給水ポンプ8は停止す
る。
When the water level in the water level detection container 13 rises slightly above H 1 and water is detected by the water level detection electrode rods 16 -4 and 16 -1 , the water detection command W 4 , W 1
Although but so applied to level control unit 19, in this case, the water supply pump 8 by the activation command V 4 from the level control unit 19 is subsequently driven, the water level further inside the heating tube 2 and the water level detection container 13 water level detecting electrode bars 16 -4 slightly higher than H 2, 16 -1, 16 becomes as water is detected by -2, water detection command W 4, W 1, W 2 water level controller given 19, from the level controller 19 results start command V 4 is not outputted, the water supply pump 8 is stopped.

【0033】上述のように、バーナ6の燃焼状態(燃焼
量)が同じであっても、蒸気の圧力Pが予め定めた基準
の圧力P0よりも高い場合と低い場合とで水位検出用容
器13内の制御すべき水位を変更する際の燃焼量(ボイ
ラ負荷)と水位との関係は図3に示されている。
As described above, even when the combustion state (burning amount) of the burner 6 is the same, the water level detecting container is different depending on whether the steam pressure P is higher or lower than a predetermined reference pressure P 0. FIG. 3 shows the relationship between the amount of combustion (boiler load) and the water level when changing the water level to be controlled in 13.

【0034】図3において、上下の傾斜曲線状の実線
イ,ロに挟まれた領域Aは、蒸気の圧力Pが予め定めた
基準となる圧力P0よりも高い場合に乾き度の良好な蒸
気を得るための水位の許容制御範囲を示し、領域A中の
白枠X1の下限は蒸気の圧力Pが予め定めた基準の圧力
0よりも高い場合で且つ高燃焼の際の下限の水位H
1を、白枠X1の上限は蒸気の圧力Pが予め定めた基準の
圧力POよりも高い場合で且つ高燃焼の際の上限の水位
2を、領域A中の白枠X2の下限は蒸気の圧力Pが予め
定めた基準の圧力P0よりも高い場合で低燃焼の際の下
限の水位H2を、白枠X2の上限は蒸気の圧力Pが予め定
めた基準の圧力POよりも高い場合で低燃焼の際の上限
の水位H3を表わしている。
[0034] In FIG. 3, the upper and lower inclined curved solid line b, the region A sandwiched Russia, good steam the dryness is higher than the pressure P 0 the pressure P of the steam is predetermined reference shows the allowable control range of the water level in order to obtain a lower limit water level during the lower limit of the white frame X 1 in region a and high combustion at higher than the pressure P 0 of the reference pressure P of the steam is predetermined H
1 , the upper limit of the white frame X 1 is when the steam pressure P is higher than a predetermined reference pressure P O and the upper limit water level H 2 at the time of high combustion is the upper limit of the white frame X 2 in the area A. The lower limit is the lower limit water level H 2 at the time of low combustion when the steam pressure P is higher than the predetermined reference pressure P 0 , and the upper limit of the white frame X 2 is the steam pressure P at the predetermined reference pressure. When it is higher than P O, it indicates the upper limit water level H 3 at the time of low combustion.

【0035】又、上下の傾斜曲線状の点線ハ,ニに挟ま
れ且つ上部が領域Aの下部と部分的に重なり合う領域
A’は、蒸気の圧力Pが予め定めた基準となる圧力PO
よりも低い場合に乾き度の良好な蒸気を得るための水位
の許容制御範囲を示し、領域A’中の黒枠Y1の下限
は、蒸気の圧力Pが予め定めた基準の圧力POよりも低
い場合で且つ高燃焼の際の下限の水位H4を、白枠X1
下限に接する黒枠Y1の上限は、蒸気の圧力Pが予め定
めた基準の圧力P0よりも低い場合で且つ高燃焼の際の
上限の水位H1を、領域A’中の黒枠Y2の下限は、蒸気
の圧力Pが予め定めた基準の圧力POよりも低い場合で
且つ低燃焼の際の下限の水位H1を、白枠X2の下限に接
する黒枠Y1の上限は、蒸気の圧力Pが予め定めた基準
の圧力POよりも低い場合で且つ低燃焼の際の上限の水
位H2を表わしている。
An area A 'sandwiched between dotted lines C and D of the upper and lower inclined curves and whose upper part partially overlaps the lower part of the area A is a pressure P O at which the steam pressure P becomes a predetermined reference.
Shows the allowable control range of the water level in order to obtain a good steam dryness fraction is lower than the lower limit of the black frame Y 1 in the region A ', rather than the pressure P O of the reference pressure P of the steam is predetermined and the lower limit level H 4 of the time of high burn if low, the upper limit of the black frame Y 1 in contact with the lower limit of the white frame X 1 is and when lower than the pressure P 0 of the reference pressure P of the steam is predetermined the water level H 1 of the upper limit during high combustion, the black frame Y 2 in the region a 'lower limit, the lower limit during and low combustion at lower than the pressure P O of the reference pressure P of the steam is predetermined the water level H 1, the black border Y 1 in contact with the lower limit of the white frame X 2 upper limit, the water level of H 2 limit during and low combustion at lower than the pressure P O of the reference pressure P of the steam is predetermined It represents.

【0036】更に、実線イよりも上方の領域は、蒸気の
圧力Pが予め定めた基準の圧力POよりも高い場合の蒸
気乾き度の悪化領域を、点線ハよりも上方の領域は、蒸
気の圧力Pが予め定めた基準の圧力POよりも低い場合
の蒸気乾き度の悪化領域を夫々表わし、実線ロよりも下
方の領域は、蒸気の圧力Pが予め定めた基準の圧力P O
よりも高い場合の加熱管2(図1参照)のメタル温度上
昇領域を、点線ニよりも下方の領域は、蒸気の圧力Pが
予め定めた基準の圧力POよりも低い場合の加熱管2の
メタル温度上昇領域を夫々表わしている。
Further, the area above the solid line A is
The pressure P is a predetermined reference pressure POIf higher than steam
The area where the air dryness deteriorates and the area above the dotted line
Gas pressure P is a predetermined reference pressure POLower than
Represents the area where the steam dryness deteriorates, and is below the solid line b.
In the other region, the steam pressure P is a predetermined reference pressure P O
Above the metal temperature of heating tube 2 (see Fig. 1)
In the region below the dotted line d, the pressure P of the steam
Predetermined reference pressure POLower than the heating tube 2
Each of the metal temperature rising regions is shown.

【0037】更に又、図3においては、白枠X1,X2
上端部は曲線ハの上方へ突出しており、蒸気の圧力Pが
基準の圧力POよりも高い場合には、乾き度の良好な蒸
気を得るための水位の許容制御範囲であった領域が、蒸
気の圧力Pが予め定めた基準の圧力POよりも低くなっ
た場合には、蒸気乾き度の悪化領域となるため、水位の
制御範囲を下げる必要があることが分る。
Further, in FIG. 3, the upper ends of the white frames X 1 and X 2 project above the curve C, and when the steam pressure P is higher than the reference pressure P O , the dryness When the pressure P of the steam becomes lower than a predetermined reference pressure P O , the region where the water level is in the allowable control range for obtaining good steam becomes a region where the steam dryness is deteriorated. It turns out that it is necessary to lower the control range of the water level.

【0038】従って、この場合には、本実施例のように
水位の制御範囲を下げることにより、バーナ6(図1参
照)の燃焼状態が同一の燃焼状態である場合と蒸気の圧
力Pが基準となる圧力POよりも低下したような場合に
は、水位の制御範囲を下げることにより乾き度の良好な
蒸気を得ることができ、且つ加熱管2のメタル温度が徒
らに上昇するのを防止することができる。
Therefore, in this case, by reducing the control range of the water level as in the present embodiment, the case where the combustion state of the burner 6 (see FIG. 1) is the same as the combustion state is the same as the case where the steam pressure P is the reference. When the pressure is lower than the pressure P O , the control range of the water level can be reduced to obtain steam with good dryness, and the metal temperature of the heating pipe 2 can be prevented from rising unnecessarily. Can be prevented.

【0039】なお、蒸気の圧力Pが基準となる圧力PO
よりも低下した場合に制御する水位を下るのは次の理由
による。すなわち、ボイラ本体1や気水分離器10内の
飽和蒸気圧力が8Kg/cm2Gの場合の蒸気の比容積
は0.21884m3/Kgであるのに対し、例えば飽
和蒸気圧力が5Kg/cm2Gの場合の蒸気の比容積は
0.32135m3/Kgであり、飽和蒸気圧力が5K
g/cm2Gの場合の蒸気の比容積は飽和蒸気圧力が8
Kg/cm2Gの場合の蒸気の比容積の1.47倍であ
る。従って、蒸気の圧力Pが低くなればなる程加熱管2
上部の蒸気の気泡が多くなるため、水位制御管柱である
加熱管2内の見掛け上の水位を低くしても加熱管2内の
実質的な水位は低下せず、加熱管2は十分に冷却され、
メタル温度が過度に上昇することはない。而して、試験
結果によれば、最高圧力が10Kg/cm2Gのボイラ
の場合、制御する水位を変更するための基準となる圧力
Oは5〜6Kg/cm2Gにすると良い。
The pressure P O based on the steam pressure P is a reference.
If the water level falls below the control level when the water level falls below this level, the reason is as follows. That is, when the saturated steam pressure in the boiler body 1 or the steam separator 10 is 8 kg / cm 2 G, the specific volume of steam is 0.21884 m 3 / kg, whereas, for example, the saturated steam pressure is 5 kg / cm. The specific volume of steam in the case of 2 G is 0.32135 m 3 / Kg, and the saturated steam pressure is 5 K
The specific volume of steam in the case of g / cm 2 G is a saturated steam pressure of 8
It is 1.47 times the specific volume of steam in the case of Kg / cm 2 G. Accordingly, the lower the steam pressure P, the higher the heating pipe 2
Since the number of bubbles in the upper steam increases, even if the apparent water level in the heating pipe 2 as the water level control column is lowered, the substantial water level in the heating pipe 2 does not decrease, and the heating pipe 2 is sufficiently cooled. Cooled,
The metal temperature does not rise excessively. According to the test results, in the case of a boiler having a maximum pressure of 10 Kg / cm 2 G, the pressure P O serving as a reference for changing the water level to be controlled is preferably 5 to 6 Kg / cm 2 G.

【0040】図2は本発明の他の実施例で、前記実施例
においては、制御する水位の変更を蒸気の圧力を基準と
して行っているのに対し、本実施例においては、気水分
離器10で分離されてボイラ本体1の下部管寄せ4に戻
される水(缶水)の電気伝導度(缶水濃度)を基準とし
て制御する水位を変更するようにしている。
FIG. 2 shows another embodiment of the present invention. In the above embodiment, the water level to be controlled is changed on the basis of the steam pressure. On the other hand, in this embodiment, a steam-water separator is used. The water level to be controlled is changed based on the electric conductivity (can water concentration) of water (can water) separated at 10 and returned to the lower header 4 of the boiler body 1.

【0041】図中、22は降水管12に接続された電気
伝導度検出器、23は演算制御装置であって、電気伝導
度検出器22で検出された電気伝導度Kは演算制御装置
23へ与え得るようになっており、演算制御装置23で
は、予め設定された基準の電気伝導度KOと検出された
電気伝導度Kとの偏差ΔKがKO−Kにより求められる
と共にΔK<0の場合は作動指令V5が水位制御装置1
9に与えられて図3の白枠X1,X2で示す水位の高い制
御範囲が選定されるようになっており、ΔK≧0の場合
は作動指令V6が水位制御装置19に与えられて図3の
黒枠Y1,Y2で示す水位の低い制御範囲が選定されるよ
うになっている。
In the figure, reference numeral 22 denotes an electric conductivity detector connected to the downcomer 12, and reference numeral 23 denotes an arithmetic control unit. The electric conductivity K detected by the electric conductivity detector 22 is sent to the arithmetic control unit 23. In the arithmetic and control unit 23, the deviation ΔK between the preset reference electric conductivity K O and the detected electric conductivity K is obtained by K O −K and the deviation ΔK <0. water level control device operation command V 5 If 1
9, the control range of the high water level indicated by the white frames X 1 and X 2 in FIG. 3 is selected. When ΔK ≧ 0, the operation command V 6 is supplied to the water level control device 19. Thus, a control range with a low water level indicated by black frames Y 1 and Y 2 in FIG. 3 is selected.

【0042】なお、本実施例に対応させた場合、図3の
領域Aは缶水の電気伝導度Kが予め定めた基準となる電
気伝導度KOよりも小さい場合に乾き度の良好な蒸気を
得るための水位の許容制御範囲を示し、領域A中の白枠
1の下限は、缶水の電気伝導度Kが前記基準の電気伝
導度KOよりも小さい場合で且つ高燃焼の際の下限の水
位H1を、白枠X1の上限は缶水の電気伝導度Kが前記基
準の電気伝導度KOよりも小さい場合で且つ高燃焼の際
の下限の水位H2を、領域A中の白枠X2の下限は、缶水
の電気伝導度Kが前記基準の電気伝導度KOよりも小さ
い場合で且つ低燃焼の際の下限の水位H2を、白枠X2
上限は、缶水の電気伝導度Kが前記基準の電気伝導度K
0よりも小さい場合で且つ低燃焼の際の上限の水位H3
表わしている。
In the case of this embodiment, the region A in FIG. 3 is a steam having a good dryness when the electric conductivity K of the still water is smaller than a predetermined standard electric conductivity K O. shows the allowable control range of the water level in order to obtain the lower limit of the white frame X 1 in region a, during and high fire when the electric conductivity K of the boiler water is less than the electrical conductivity of K O of the reference water level H 1, the water level of H 2 lower during maximum white frame X 1 is and high fire when the electric conductivity K of the boiler water is less than the electrical conductivity of K O of the reference, a region lower limit of the the lower limit of the white frame X 2 in a is a water level of H 2 lower during and low fire when the electric conductivity K of the boiler water is less than the electrical conductivity of K O of the reference, a white frame X 2 The upper limit is that the electric conductivity K of the canned water is the electric conductivity K of the above standard.
It represents the upper limit water level H 3 when the value is smaller than 0 and at the time of low combustion.

【0043】又、領域A’中の黒枠Yの下限は、缶水の
電気伝導度Kが予め定めた基準の電気伝導度KOよりも
高い場合に乾き度の良好な蒸気を得るための水位の許容
制御範囲を示し、領域A’中の黒枠Y1の下限は、缶水
の電気伝導度Kが前記基準の電気伝導度KOよりも高い
場合で且つ低燃焼の際の下限の水位H4を、黒枠Y1の上
限は、缶水の電気伝導度Kが前記基準の電気伝導度KO
よりも高い場合で且つ高燃焼の際の上限の水位H1を、
領域A’中の黒枠Y2の下限は、缶水の電気伝導度Kが
基準の電気伝導度KOよりも高い場合で且つ低燃焼の際
の下限の水位H1を、黒枠Y2の上限は、缶水の電気伝導
度Kが基準の電気伝導度KOよりも高い場合で且つ低燃
焼の際の上限の水位H2を表わしている。
The lower limit of the black frame Y in the area A 'is the water level for obtaining good dryness steam when the electric conductivity K of the can water is higher than a predetermined standard electric conductivity K O. shows the allowable control range, the lower limit of the black frame Y 1 in the region a 'is a lower limit upon and low fire when the electric conductivity K of the boiler water is higher than the electrical conductivity of K O of the reference water level H 4, the upper limit of the black frame Y 1 is an electric conductivity K O of the electrical conductivity K of the boiler water is the reference
Higher and the upper limit water level H 1 at the time of high combustion,
The lower limit of the black frame Y 2 in the region A 'is the water level H 1 of a lower limit at the time of and low fire when the electric conductivity K of the boiler water is higher than the electrical conductivity of K O reference, the upper limit of the black frame Y 2 Represents the upper limit water level H 2 when the electric conductivity K of the can water is higher than the standard electric conductivity K O and at the time of low combustion.

【0044】本実施例においては、気水分離器10で分
離されて降水管12から下部管寄せ4に戻される水の電
気伝導度Kが電気伝導度検出器22により検出されて演
算制御装置23へ与えられ、演算制御装置23では、電
気伝導度の偏差ΔKがΔK=KO−Kにより求められ、
ΔK<0の場合は作動指令V5が、又ΔK≧0の場合は
作動指令V6が、演算制御装置23から水位制御装置1
9へ与えられる。
In this embodiment, the electric conductivity K of the water separated by the steam separator 10 and returned from the downcomer 12 to the lower header 4 is detected by the electric conductivity detector 22 and the arithmetic and control unit 23 is operated. In the arithmetic and control unit 23, the deviation ΔK of the electric conductivity is obtained by ΔK = K O −K,
When ΔK <0, the operation command V 5 is given, and when ΔK ≧ 0, the operation command V 6 is given from the arithmetic control unit 23 to the water level control unit 1.
9

【0045】而して、水位制御装置19へ作動指令
1,V5が与えられる場合は、バーナ6は高燃焼状態で
水位検出用容器13内の水位は、水位検出用電極棒16
-1の下端と水位検出用電極棒16-2の下端の間すなわち
水位H1とH2の間となるよう制御が行われ、水位制御装
置19へ作動指令V2,V5が与えられる場合は、バーナ
6は低燃焼状態で、水位検出用容器13内の水位は、水
位検出用電極棒16-2の下端と水位検出用電極棒16-3
の下端の間すなわち水位H2とH3の間となるよう制御が
行われ、又水位制御装置19へ作動指令V1,V6が与え
られる場合は、バーナ6が高燃焼状態で水位検出用容器
13内の水位は、水位検出用電極棒16-4の下端と水位
検出用電極棒16-1の下端の間すなわち水位H4とH1
間となるよう制御が行われ、水位制御装置19へ作動指
令V2,V6が与えられる場合は、バーナ6が低燃焼状態
で水位検出用容器13内の水位は、水位検出用電極棒1
-1の下端と水位検出用電極棒16-2の下端の間、すな
わち水位H1とH2との間となるよう制御が行われる。水
位の制御のやり方は前述の実施例と同じなので説明は省
略する。
When the operation commands V 1 and V 5 are given to the water level control device 19, the burner 6 is in a high combustion state and the water level in the water level detection container 13 is equal to the water level detection electrode rod 16.
Control lower water level between the lower end of the detection electrode rod 16 -2 i.e. so as to be between the water level H 1 and H 2 -1 is performed, operation command V 2 to the level control unit 19, if V 5 is given the burner 6 in the low combustion state, the water level in the water level detection container 13, the water level detecting electrode bars 16 -2 bottom and the water level detecting electrode bars 16 -3
Controlled to be between between the lower end i.e. the water level H 2 and H 3 are performed, and also when the water level control device operation command V 1 to 19, V 6 is given, water level detection burner 6 is in a high combustion state the water level in the container 13, is controlled to be between the water level detecting electrode bars 16 -4 bottom and the water level detecting electrode bars 16 -1 during i.e. the water level H 4 of the lower end of the H 1 is performed, the water level controller When the operation commands V 2 , V 6 are given to 19, the water level in the water level detecting container 13 is set to the water level detecting electrode rod 1 when the burner 6 is in the low combustion state.
6-1 the lower end and between the lower end of the water level detecting electrode bars 16 -2, that is controlled to be between the water level H 1 and H 2 is carried out. The manner of controlling the water level is the same as that of the above-described embodiment, and the description is omitted.

【0046】このように、基準となる電気伝導度KO
検出した電気伝導度Kよりも大きい場合は、制御する水
位を高くし、基準となる電気伝導度KOが検出した電気
伝導度Kよりも小さい場合は、制御する水位を低くする
ようにしても、缶水の電気伝導度の変化が大きい場合に
乾き度の良い蒸気を得ることができ、且つ加熱管2の過
度のメタル温度上昇を防止することができる。
As described above, when the reference electric conductivity K O is larger than the detected electric conductivity K, the water level to be controlled is raised, and the detected electric conductivity K O is used as the reference electric conductivity K O. If it is smaller than that, even if the water level to be controlled is lowered, it is possible to obtain steam with good dryness when the electric conductivity of the can water is large, and an excessive rise in metal temperature of the heating pipe 2. Can be prevented.

【0047】電気伝導度Kが小さい場合に水位検出用容
器13内の制御する水位を低くできるのは以下の理由に
よる。すなわち、水が蒸発して缶水中の不純物の濃度が
高くなると電気伝導度も高くなるが、加熱管2上部の気
泡も増えるため、水位制御管柱である加熱管2内の見掛
け上の水位を低くしても気泡の多い分だけ実質水位は低
くならず、加熱管2の冷却効果は十分に期待でき、メタ
ル温度が過度に上昇することはない。実験によれば、電
気伝導度が約500μs/cm2で制御する水位を変更
するのが良い。
The reason that the water level controlled in the water level detecting container 13 can be lowered when the electric conductivity K is small is as follows. That is, when the water evaporates and the concentration of impurities in the still water increases, the electrical conductivity also increases. However, since the number of bubbles at the top of the heating tube 2 also increases, the apparent water level in the heating tube 2 serving as a water level control column is reduced. Even if it is lowered, the substantial water level is not lowered by the amount of bubbles, the cooling effect of the heating tube 2 can be sufficiently expected, and the metal temperature does not rise excessively. According to experiments, it is better to change the water level at which the electric conductivity is controlled at about 500 μs / cm 2 .

【0048】なお、本発明の実施例においては、制御す
る水位を高い状態から低い状態へ切替える場合について
説明したが、低い状態から高い状態へ切替えるようにし
ても実施できること、その他、本発明の要旨を逸脱しな
い範囲内で種々変更を加え得ること、等は勿論である。
In the embodiment of the present invention, the case where the controlled water level is switched from a high state to a low state has been described. However, the present invention can be implemented by switching from a low state to a high state. It goes without saying that various changes can be made without departing from the scope of the present invention.

【0049】[0049]

【発明の効果】本発明の多管式貫流ボイラの水位制御方
法においては請求項1、2の何れの場合においても、同
一の燃焼状態の際に蒸気の圧力Pの変動する範囲が大き
い場合であっても乾き度が良好な蒸気を得ることができ
ると共に加熱管2の過度の温度上昇を抑制することがで
きてボイラ寿命の長期化を図ることができる、等種々の
優れた効果を奏し得る。
According to the water level control method of the multi-tube once-through boiler of the present invention, in any one of the first and second embodiments, when the range in which the steam pressure P fluctuates in the same combustion state is large. Even if it does, it is possible to obtain various excellent effects, such as being able to obtain steam having a good dryness, suppressing an excessive rise in temperature of the heating tube 2 and prolonging the life of the boiler. .

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の多管式貫流ボイラの水位制御方法の一
実施例の制御ブロック図である。
FIG. 1 is a control block diagram of an embodiment of a water level control method for a multi-tube once-through boiler of the present invention.

【図2】本発明の多管式貫流ボイラの水位制御方法の他
の実施例の制御ブロック図である。
FIG. 2 is a control block diagram of another embodiment of the water level control method of the multi-tube once-through boiler of the present invention.

【図3】本発明の多管式貫流ボイラの水位制御方法にお
ける燃焼量(ボイラ負荷)と制御する水位との関係を示
すグラフである。
FIG. 3 is a graph showing a relationship between a combustion amount (boiler load) and a controlled water level in the water level control method of the multi-tube once-through boiler of the present invention.

【図4】従来の多管式貫流ボイラの水位制御方法の一例
の制御ブロック図である。
FIG. 4 is a control block diagram of an example of a conventional water level control method for a multi-tube once-through boiler.

【図5】従来の多管式貫流ボイラの水位制御方法におけ
る燃焼量(ボイラ負荷)と制御する水位との関係を示す
グラフである。
FIG. 5 is a graph showing a relationship between a combustion amount (boiler load) and a water level to be controlled in a conventional water level control method for a multi-tube once-through boiler.

【符号の説明】[Explanation of symbols]

1 ボイラ本体 2 加熱管 3 燃焼室 4 下部管寄せ 5 上部管寄せ 6 バーナ 8 給水ポンプ 10 気水分離器 13 水位検出用容器 16-1,16-2,16-3,16-4 水位検出用電
極棒 P,P0 圧力 K,KO 電気伝導度
DESCRIPTION OF SYMBOLS 1 Boiler main body 2 Heating tube 3 Combustion chamber 4 Lower header 5 Upper header 6 Burner 8 Water supply pump 10 Steam separator 13 Water level detection container 16-1 , 16-2 , 16-3 , 16-4 For water level detection Electrode P, P 0 Pressure K, K O Electric conductivity

───────────────────────────────────────────────────── フロントページの続き (56)参考文献 特開 平3−236502(JP,A) 特開 平4−148102(JP,A) 実開 昭61−48208(JP,U) (58)調査した分野(Int.Cl.7,DB名) F22D 5/00 ──────────────────────────────────────────────────続 き Continuation of the front page (56) References JP-A-3-236502 (JP, A) JP-A-4-148102 (JP, A) JP-A-61-48208 (JP, U) (58) Survey Field (Int. Cl. 7 , DB name) F22D 5/00

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 円周方向へ所要の間隔で立設された複数
の加熱管2及び該加熱管2の下端に接続され且つ給水ポ
ンプ8からの水を導入し得るようにした下部管寄せ4並
に前記加熱管2の上端に接続され且つ生成された蒸気を
送出す上部管寄せ5を有するボイラ本体1と、該ボイラ
本体1内に加熱管2により包囲されて形成された燃焼室
3へ燃料を噴射するバーナ6と、下部が下部管寄せ4と
連通し且つ上部が上部管寄せ5と連通した水位検出用容
器13と、該水位検出用容器13内に下端が夫々異なる
高さに位置するよう挿入された第1、第2、第3、第4
の4本の水位検出用電極棒16−4,16−1,16
−2,16−3とを備え、且つ前記第1、第2、第3、
第4の水位検出用電極棒16−4,16−1,1
−2,16−3により水位検出用容器13内の水位を
制御するようにした多管式貫流ボイラの水位制御方法に
おいて、前記バーナ6が高燃焼状態で且つ生成された蒸
気の圧力Pが基準となる圧力Pよりも高い場合には、
前記水位検出用容器13内の水位を、第2の水位検出用
電極棒16−1の下端と、該第2の水位検出用電極棒1
−1の下端よりも下端が高い位置にある第3の水位検
出用電極棒16−2の下端との間に略位置するよう制御
し、前記バーナ6が高燃焼状態で且つ生成された蒸気の
圧力Pが基準となる圧力Pよりも低い場合には、前記
水位検出用容器13内の水位を、前記第2の水位検出用
電極棒16−1の下端と該第2の水位検出用電極棒16
−1の下端よりも下端が低い位置にある第1の水位検出
用電極棒16−4との間に略位置するよう制御し、前記
バーナ6が低燃焼状態で且つ生成された蒸気の圧力Pが
基準となる圧力Pよりも高い場合には、前記水位検出
用容器13内の水位を、下端が前記第2の水位検出用電
極棒16−1の下端よりも高い位置にある第3の水位検
出用電極棒16−2の下端と該第3の水位検出用電極棒
16−2の下端よりも下端が高い位置にある第4の水位
検出用電極棒16−3の下端との間に略位置するよう制
御し、前記バーナ6が低燃焼状態で且つ生成された蒸気
の圧力Pが基準となる圧力Pよりも低い場合には、前
記水位検出用容器13内の水位を、前記第3の水位検出
用電極棒16−2の下端と該第3の水位検出用電極棒1
−2の下端よりも下端が低い位置にある第2の水位検
出用電極棒16−1の下端との間に略位置するよう制御
することを特徴とする多管式貫流ボイラの水位制御方
法。
1. A plurality of heating tubes 2 erected at predetermined intervals in a circumferential direction and a lower header 4 connected to a lower end of the heating tubes 2 and capable of introducing water from a water supply pump 8. A boiler body 1 having an upper header 5 connected to the upper end of the heating tube 2 and delivering generated steam, and a combustion chamber 3 formed by being surrounded by the heating tube 2 in the boiler body 1. A burner 6 for injecting fuel, a water level detecting container 13 having a lower part communicating with the lower header 4 and an upper part communicating with the upper header 5, and a lower end located at a different height in the water level detecting container 13; First, second, third, fourth inserted
Of the four water level detection electrode rods 16-4 , 16-1 , 16
-2 , 16-3 , and the first, second, third,
Fourth water level detection electrode rod 16 -4 , 16 -1 , 1
6-2, the water level control method of the multi-tube once-through boiler which is by 16 -3 to control the water level in the water level detection chamber 13, the pressure P of the steam the burner 6 is and produced in a high combustion state If higher than the pressure P O as a reference is,
Wherein the water level of the water level detection chamber 13, and the lower end of the second water level detecting electrode bars 16 -1, the second water level detecting electrode bars 1
6 lower than the lower end of -1 is controlled to substantially located between the third lower end of the water level detecting electrode bars 16 -2 at a high position, steam the burner 6 is and generated by the high combustion state of when the pressure P is lower than the pressure P O as a reference, the water level of the water level detection chamber 13, for the lower end and said second level detection of the second water level detecting electrode bars 16 -1 Electrode rod 16
Lower than the lower end of -1 is controlled to substantially located between the first water level detecting electrode bars 16 -4 at a low position, the pressure P of the steam the burner 6 is and produced at a low combustion state Is higher than the reference pressure P O , the water level in the water level detection container 13 is set to a third level whose lower end is higher than the lower end of the second water level detection electrode rod 16-1 . between the lower end of the water level detecting electrode bars 16 -2 bottom and said third fourth lower end than the lower end of the water level detecting electrode bars 16 -2 is in the high position of the water level detecting electrode bars 16 -3 When the burner 6 is in a low combustion state and the pressure P of the generated steam is lower than a reference pressure P O , the water level in the water level detection container 13 is adjusted to the second level . 3 the lower end and the water level detecting electrode bars 16 -2 third water level detecting electrode bars 1
Second level control method of a multi-tube once-through boiler, characterized by controlling so as to substantially located between the lower end of the water level detecting electrode bars 16 -1 in 6-2 lower end position lower than the lower end of the .
【請求項2】 円周方向へ所要の間隔で立設された複数
の加熱管2及び該加熱管2の下端に接続され且つ給水ポ
ンプ8からの水を導入し得るようにした下部管寄せ4並
に前記加熱管2の上端に接続され且つ生成された蒸気を
送出す上部管寄せ5を有するボイラ本体1と、該ボイラ
本体1内に加熱管2により包囲されて形成された燃焼室
3へ燃料を噴射するバーナ6と、前記上部管寄せ5から
送給された蒸気から水分を分離して戻す気水分離器10
と、下部が下部管寄せ4と連通され且つ上部が上部管寄
せ5と連通された水位検出用容器13と、該水位検出用
容器13内に下端が夫々異なる高さに位置するよう挿入
された第1、第2、第3、第4の4本の水位検出用電極
棒16−4,16−1,16−2,16−3とを備え、
且つ第1、第2、第3、第4の水位検出用電極棒16
−4,16−1,16−2,16−3により水位検出用
容器13内の水位を制御するようにした多管式貫流ボイ
ラの水位制御方法において、前記バーナ6が高燃焼状態
で且つ気水分離器10で分離された水の電気伝導度Kが
基準となる電気伝導度Kよりも小さい場合には、前記
水位検出用容器13内の水位を、第2の水位検出用電極
棒16−1の下端と該第2の水位検出用電極棒16−1
の下端よりも下端が高い位置にある第3の水位検出用電
極棒16−2の下端との間に略位置するよう制御し、前
記バーナ6が高燃焼状態で且つ気水分離器10で分離さ
れた水の電気伝導度Kが基準となる電気伝導度Kより
も大きい場合には、前記水位検出用容器13内の水位
を、前記第2の水位検出用電極棒16−1の下端と該
2の水位検出用電極棒16−1の下端よりも下端が低い
位置にある第1の水位検出用電極棒16−4との間に略
位置するよう制御し、前記バーナ6が低燃焼状態で且つ
気水分離器10で分離された水の電気伝導度Kが基準と
なる電気伝導度Kよりも小さい場合には、前記水位検
出用容器13内の水位を、下端が前記第2の水位検出用
電極棒16−1の下端よりも高い位置にある第3の水位
検出用電極棒16−2の下端と該第3の水位検出用電極
棒16−2の下端よりも下端が高い位置にある第4の
位検出用電極棒16−3の下端との間に略位置するよう
制御し、前記バーナ6が低燃焼状態で且つ気水分離器1
0で分離された水の電気伝導度Kが基準となる電気伝導
度Kよりも大きい場合には、前記水位検出用容器13
内の水位を、前記第3の水位検出用電極棒16−2の下
端と該第3の水位検出用電極棒16−2の下端よりも下
端が低い位置にある第2の水位検出用電極棒16−1
下端との間に略位置するよう制御することを特徴とする
多管式貫流ボイラの水位制御方法。
2. A plurality of heating pipes 2 erected at predetermined intervals in a circumferential direction, and a lower header 4 connected to a lower end of the heating pipe 2 and capable of introducing water from a water supply pump 8. A boiler body 1 having an upper header 5 connected to the upper end of the heating tube 2 and delivering generated steam, and a combustion chamber 3 formed by being surrounded by the heating tube 2 in the boiler body 1. A burner 6 for injecting fuel, and a steam-water separator 10 for separating and returning moisture from steam supplied from the upper header 5
And a water level detection container 13 having a lower part communicated with the lower header 4 and an upper part communicated with the upper header 5, and inserted into the water level detection container 13 such that lower ends thereof are located at different heights. First, second, third, and fourth four water level detection electrode rods 16-4 , 16-1 , 16-2 , 16-3 ;
And first, second, third, and fourth electrode rods 16 for detecting a water level.
-4, 16 -1, 16 -2, the water level control method of the multi-tube once-through boiler which is by 16 -3 to control the water level in the water level detection chamber 13, and the burner 6 is in a high combustion state gas when the electric conductivity K of separated water in a water separator 10 is smaller than the electric conductivity K O as a reference is the water level in the water level detection chamber 13, the second water level detecting electrode bars 16 -1 lower end and said second water level detecting electrode bars 16 -1
The lower end is higher than the lower end of the third electrode rod 16-2 for detecting water level, which is higher than the lower end. The burner 6 is in a high combustion state and separated by the steam separator 10. been if the electric conductivity K of the water is greater than the electrical conductivity K O as a reference is the water level in the water level detection chamber 13, and the lower end of the second water level detecting electrode bars 16 -1 the first
The lower end of the second water level detecting electrode bars 16 -1 to control so as to substantially located between the first water level detecting electrode bars 16 -4 at the lower end is lower position, the burner 6 is at a low combustion state and air-water when the electrical conductivity K of separated water in separator 10 is smaller than the electric conductivity K O as a reference is the water level in the water level detection chamber 13, the lower end is the second water level third lower end position higher than the lower end of the water level detecting electrode bars 16 -2 bottom and the third water level detecting electrode bars 16 -2 at a position higher than the lower end of the detection electrode rod 16 -1 controlled to substantially located between one fourth lower water <br/> level detecting electrode bars 16 -3, air-water the burner 6 and at a low combustion state separator 1
When the electric conductivity K of the water separated at 0 is larger than the electric conductivity K O as a reference, the water level detecting container 13
The water level of the inner, the third second water level detecting electrode bars lower than the lower end of the water level detecting electrode bars 16 -2 bottom and the third water level detecting electrode bars 16 -2 is in the low position of the multitubular level control method of once-through boiler, characterized by controlling so as to substantially located between the lower end of the 16 -1.
JP4316336A 1992-10-30 1992-10-30 Water level control method for multi-tube once-through boiler Expired - Lifetime JP3009793B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4316336A JP3009793B2 (en) 1992-10-30 1992-10-30 Water level control method for multi-tube once-through boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4316336A JP3009793B2 (en) 1992-10-30 1992-10-30 Water level control method for multi-tube once-through boiler

Publications (2)

Publication Number Publication Date
JPH06147407A JPH06147407A (en) 1994-05-27
JP3009793B2 true JP3009793B2 (en) 2000-02-14

Family

ID=18075993

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4316336A Expired - Lifetime JP3009793B2 (en) 1992-10-30 1992-10-30 Water level control method for multi-tube once-through boiler

Country Status (1)

Country Link
JP (1) JP3009793B2 (en)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2002295804A (en) * 2001-03-29 2002-10-09 Kawasaki Thermal Engineering Co Ltd Method and device for controlling feed water of boiler
TWI401422B (en) 2006-03-08 2013-07-11 Miura Kogyo Kk Electrode rod for water level detection, water level detecting method, water level control method of boiler and water level control method of gas water separator
JP5534251B2 (en) * 2012-01-31 2014-06-25 三浦工業株式会社 boiler
JP5534253B2 (en) * 2012-03-16 2014-06-25 三浦工業株式会社 Separatorless boiler

Also Published As

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