JPH0210323B2 - - Google Patents
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- Publication number
- JPH0210323B2 JPH0210323B2 JP11683181A JP11683181A JPH0210323B2 JP H0210323 B2 JPH0210323 B2 JP H0210323B2 JP 11683181 A JP11683181 A JP 11683181A JP 11683181 A JP11683181 A JP 11683181A JP H0210323 B2 JPH0210323 B2 JP H0210323B2
- Authority
- JP
- Japan
- Prior art keywords
- water
- water supply
- water level
- canned
- concentration
- 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
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- Measurement Of Levels Of Liquids Or Fluent Solid Materials (AREA)
- Investigating Or Analyzing Materials By The Use Of Electric Means (AREA)
Description
【発明の詳細な説明】
この発明はボイラ系における缶水の濃縮化に伴
う缶水中の不純物濃度の増大傾向を連続的に自動
計測するための缶水濃縮度計測装置に係わり、特
に、1回の断続制御でもつてボイラに給水される
期間が缶水の濃縮化に伴つて増大する現象に基づ
いて缶水の濃縮度合いを計測するようにした缶水
濃縮度計測装置に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a can water concentration measuring device for continuously and automatically measuring the increasing tendency of impurity concentration in can water due to the concentration of can water in a boiler system, and in particular, The present invention relates to a can water concentration measurement device that measures the degree of concentration of can water based on the phenomenon that the period during which water is supplied to a boiler increases as the can water becomes more concentrated under intermittent control.
一般に、ボイラ系を長期間運転すると、缶水が
濃縮化されるので、缶水中に含まれる溶解固形分
等の不純物の濃度が増大して、缶水表面に気泡を
生ずるものである。そして、かかる気泡が気水境
界面を離れて蒸気中に混入してキヤリーオーバー
を生じ、ボイラ系に接続されたバルブ等の関連機
器の損傷を招くことが知られている。 Generally, when a boiler system is operated for a long period of time, the canned water becomes concentrated, so that the concentration of impurities such as dissolved solids contained in the canned water increases, causing bubbles to form on the surface of the canned water. It is known that such bubbles leave the air-water interface and get mixed into the steam, causing carryover, which causes damage to related equipment such as valves connected to the boiler system.
而して、キヤリーオーバーを防ぐためには、給
水あるいは蒸気の流量を流量計でもつて計測する
こと等により、缶水濃縮度を推量して、これがあ
る程度増大したときには、缶水の吹き出し(以下
ブローという)を行つて、新しい缶水と置換する
ことが行われてはいるものの、小形のボイラ系で
は、流量計を装備することの経済的負坦が相対的
に大きくなるので、その採用が一般的に困難であ
り、而して、流量計による計測に代えて、ボイラ
系の累積燃料消費量を貯蔵容器、典型的には、ド
ラム缶の単位でもつて計測することにより、ある
いは、缶水の一部を抽出してその電気伝導度を計
測することにより、缶水濃縮度を推量することが
しばしば行われている。 In order to prevent carryover, the concentration of canned water can be estimated by measuring the flow rate of water supply or steam using a flow meter, and when this concentration increases to a certain extent, the canned water can be blown out (hereinafter referred to as blowout). However, in small boiler systems, the economical burden of equipping a flow meter is relatively large, so its adoption is not common. Therefore, instead of measuring with a flowmeter, it is possible to measure the cumulative fuel consumption of the boiler system in units of storage containers, typically drums, or to The concentration of canned water is often estimated by extracting a portion of the water and measuring its electrical conductivity.
しかしながら、累積燃料消費量に基づいて累積
蒸気消費量を推量し、更に、累積蒸気消費量に基
づいて缶水濃縮度を推量する場合には、ボイラ系
の効率が蒸気消費量(負荷)に従つて変化するの
で、高精度の計測は期待し難いものであつた。 However, when estimating the cumulative steam consumption based on the cumulative fuel consumption and further estimating the can water concentration based on the cumulative steam consumption, the efficiency of the boiler system depends on the steam consumption (load). Therefore, it was difficult to expect highly accurate measurements.
加えて、ドラム缶等の貯蔵容器の計数に基づい
て計測する場合には、計量の最小単位が極めて大
きく、計測に際して多大の量子化誤差を伴うの
で、連続量による計測にはほど遠いものであつ
た。 In addition, when measuring based on counts of storage containers such as drums, the minimum unit of measurement is extremely large, and measurement involves a large amount of quantization error, so it is far from being a continuous quantity measurement.
その上、ドラム缶等による累積燃料消費量の計
測は、消費した燃料が貯蔵されていたドラム缶等
の数量をいちいち計数して、これを記録するとい
う煩雑な作業を伴うので、往往にして実行され
ず、累積蒸発量、ひいては缶水濃縮度を全く把握
できなくなつてしまうこともしばしばであつた。 Furthermore, measuring cumulative fuel consumption using drums, etc. is often not carried out because it involves the complicated work of counting and recording the number of drums, etc. in which consumed fuel was stored. In many cases, it became impossible to grasp the cumulative amount of evaporation and even the concentration of canned water.
また、缶水の電気伝導度に基づいて缶水濃縮度
を推量する場合には、間歇的な計測しかできず、
しかも、実際上計測回路が制約されるために、缶
水濃縮度の増大傾向を連続的に計測することがで
きなかつた。 Furthermore, when estimating the concentration of canned water based on the electrical conductivity of canned water, only intermittent measurements can be made;
Moreover, since the measuring circuit is actually limited, it has not been possible to continuously measure the increasing tendency of the concentration of canned water.
而して、かかる従前のボイラ系では、ブローを
実行すべき時期を正確に把握することができず、
缶水を著しい濃縮状態に至らしめ、キヤリーオー
バーを頻発させ、関連機器の損傷を招く危険性が
極めて大であるという欠点があつた。 Therefore, with such conventional boiler systems, it is not possible to accurately determine when to perform blowing.
The disadvantages are that the canned water becomes extremely concentrated, causing frequent carry-overs, and there is an extremely high risk of damage to related equipment.
この発明の目的は上記従来技術に基づく缶水濃
縮度の推量の問題点に鑑み、1回の断続制御でも
つて供給される給水量、すなわち、給水期間が、
缶水の濃縮化の進行に伴つて増大する現象に基づ
いて、給水期間の増大傾向を計測することによ
り、上記欠点を除去し、高精度に、しかも、連続
的に缶水濃縮度を計測することができる優れたボ
イラ系における缶水濃縮度計測装置を提供せんと
するものである。 In view of the problem of estimating the concentration of canned water based on the above-mentioned prior art, the purpose of this invention is to
By measuring the increasing tendency of the water supply period based on the phenomenon that increases as the concentration of canned water progresses, the above drawbacks are eliminated and the concentration of canned water is measured continuously with high accuracy. The purpose of the present invention is to provide an excellent device for measuring the concentration of can water in a boiler system.
上記目的に沿うこの発明の構成は、水管の上下
端部を連通する連通管に上下限水位センサを配設
して水位検出部を形成し、上下限水位センサの
各々からの出力信号に応答して、水管に缶水を供
給する給水ポンプを始動あるいは停止させる給水
制御部を設けて、蒸気消費に伴う缶水水位の降下
に応じて連通管の水位が降下し、下限水位に到達
したときには、下限水位センサがこれを検出して
下限水位信号を給水制御部に送つて給水ポンプを
始動させ、給水の開始に伴う缶水水位の上昇に応
じて連通管の水位が上昇し、上限水位に到達した
ときには、上限水位センサがこれを検出して上限
水位信号を給水制御部に送つて給水ポンプを停止
させるようにした断続制御の給水制御系を備えた
ボイラ系において、給水期間計測部を付設して、
給水ポンプが始動してから停止するまでの給水期
間を計測し、更に、缶水濃縮度演算部を付設し
て、給水期間計測部でもつて計測された給水期間
から缶水濃縮のない状態における基準給水期間を
減算することにより、給水開始時における連通管
の水位低下変動幅が缶水の濃縮化の進行に伴つて
増大する現象に起因する給水期間の増大傾向を演
算し、その演算結果を缶水濃縮度信号として出力
するようにしたことを特徴とするものである。 In accordance with the above object, the present invention has a structure in which upper and lower water limit water level sensors are disposed in a communication pipe that communicates the upper and lower ends of the water pipe to form a water level detection section, and the water level detector responds to output signals from each of the upper and lower water limit water level sensors. A water supply control unit is provided to start or stop a water supply pump that supplies canned water to the water pipe, and when the water level in the communication pipe falls in response to the drop in the canned water level due to steam consumption and reaches the lower limit water level, The lower limit water level sensor detects this and sends a lower limit water level signal to the water supply control unit to start the water supply pump, and as the canned water level rises with the start of water supply, the water level in the communication pipe rises and reaches the upper limit water level. In a boiler system equipped with an intermittent control water supply control system in which the upper limit water level sensor detects this and sends an upper limit water level signal to the water supply control unit to stop the water supply pump, a water supply period measuring unit is attached. hand,
The water supply period from when the water supply pump starts to when it stops is measured, and a canned water concentration calculating section is added to calculate the standard in a state where there is no concentration of canned water from the water supply period measured by the water supply period measurement section. By subtracting the water supply period, we calculate the increasing tendency of the water supply period due to the phenomenon that the fluctuation range of the water level drop in the communication pipe at the start of water supply increases as the concentration of canned water progresses, and the calculation result is This is characterized in that it is output as a water concentration signal.
さて、後続するこの発明の実施例の説明に先が
けて、この発明の構成を付設することができる典
型的な小形ボイラ系の構成及び動作を説明すれば
以下の通りである。 Now, before explaining the subsequent embodiments of the present invention, the structure and operation of a typical small boiler system to which the structure of the present invention can be attached will be explained as follows.
第1図Aは、かかるボイラ系の構成を示すブロ
ツク説明図であり、ボイラ1はその断面が示され
ている。第1図Bは第1図AにおけるA−A断面
図である。 FIG. 1A is a block explanatory diagram showing the configuration of such a boiler system, and a cross section of the boiler 1 is shown. FIG. 1B is a sectional view taken along the line AA in FIG. 1A.
図において、ボイラ1の内部は壁1aの内周面
に沿つて多数の水管1bが立設され、水管1bは
中空筒状体から成り、その下端部は環状の下部管
寄せ1c(水室)に、そして、その上端部は同じ
く環状の上部管寄せ1d(蒸気室)にそれぞれ連
通し、下部管寄せ1c及び水管1bの下部には、
缶水が収納される。 In the figure, inside a boiler 1, a large number of water pipes 1b are installed along the inner circumferential surface of a wall 1a, and the water pipes 1b are made of a hollow cylindrical body, and the lower end thereof is an annular lower header 1c (water chamber). The upper end portions thereof communicate with the annular upper header 1d (steam chamber), and the lower portions of the lower header 1c and the water pipe 1b,
Canned water is stored.
水管1bで囲まれたボイラ1の中心部には、燃
焼室1eが形成され、その上部には、電動機1f
で駆動されるブロア1gに連通する風道1hが設
けられ、風道1h内には、ノズル棒1iと電極棒
1jが垂設される。 A combustion chamber 1e is formed in the center of the boiler 1 surrounded by water pipes 1b, and an electric motor 1f is provided above the combustion chamber 1e.
An air passage 1h is provided which communicates with a blower 1g driven by a blower 1g, and a nozzle rod 1i and an electrode rod 1j are vertically provided within the air passage 1h.
燃焼室1eの下端部は、多数の水管1bの中空
部を経て煙道1kに連通する。上部管寄せ1dか
らは、連通管1lが壁1a外に延びて下部管寄せ
1cに連通する。 The lower end of the combustion chamber 1e communicates with the flue 1k through the hollow portions of a large number of water pipes 1b. From the upper header 1d, a communication pipe 1l extends outside the wall 1a and communicates with the lower header 1c.
連通管1lの中間部には、缶水水位を目視可能
に表示する水位ゲージ1mと水位検出部2が介装
される。水位検出部2には、給水制御部3が接続
され、その出力端子は給水ポンプ4を駆動する電
動機4aに接続される。給水ポンプ4の導入管は
図示しない水源に連通し、その吐出管は下部管寄
せ1cに連通する。 A water level gauge 1m and a water level detector 2 for visually displaying the canned water level are installed in the middle of the communication pipe 1l. A water supply control section 3 is connected to the water level detection section 2 , and an output terminal thereof is connected to an electric motor 4 a that drives a water supply pump 4 . An inlet pipe of the water supply pump 4 communicates with a water source (not shown), and a discharge pipe thereof communicates with the lower header 1c.
更に、連通管1lの上部には、圧力検出部5が
接続され、その出力端子は燃焼制御部6に接続さ
れる。燃焼制御部6からは、制御信号線6a〜6
cが延びて電動機1f、電極棒1j、燃料ポンプ
6dの導入管は図示しない燃料タンクに連通し、
その吐出管はノズル棒1iに連通する。そして、
下部管寄せ1cからはブロー管1nが延びて、ブ
ローコツク1pを介して図示しない排水路に連通
し、上部管寄せ1dからは蒸気管1qが延びて図
示しない所望の蒸気負荷に連通する。 Further, a pressure detection section 5 is connected to the upper part of the communication pipe 1l, and its output terminal is connected to a combustion control section 6. From the combustion control unit 6, control signal lines 6a to 6
c extends, and the introduction pipes of the electric motor 1f, the electrode rod 1j, and the fuel pump 6d communicate with a fuel tank (not shown),
Its discharge pipe communicates with the nozzle rod 1i. and,
A blow pipe 1n extends from the lower header 1c and communicates with a drainage channel (not shown) via a blow stock 1p, and a steam pipe 1q extends from the upper header 1d and communicates with a desired steam load (not shown).
上記ボイラ系の構成では、蒸気を発生させるに
際しては、電動機1fでもつてブロア1gを駆動
して風道1h内に空気を圧送しつつ電極棒1jに
高電圧を印加してノズル棒1iの先端から噴射さ
れる燃料を着火させ、これを燃焼室1e内で燃焼
させる。かかる燃焼により生じた高温度の燃焼ガ
スは、燃焼室1e下端部から水管1bの中空部に
進入し、これを通過して煙道1kに至り排気され
る。この間に熱交換が行われて水管1b中の缶水
が加熱されて蒸気となり、これが上部管寄せ1d
にて集収、蓄積され、蒸気管1qを通じて蒸気負
荷に供給されるものである。 In the configuration of the boiler system described above, when generating steam, the electric motor 1f drives the blower 1g to forcefully send air into the air passage 1h, and applies a high voltage to the electrode rod 1j to generate steam from the tip of the nozzle rod 1i. The injected fuel is ignited and combusted within the combustion chamber 1e. High-temperature combustion gas generated by such combustion enters the hollow part of the water pipe 1b from the lower end of the combustion chamber 1e, passes through this, reaches the flue 1k, and is exhausted. During this time, heat exchange takes place and the canned water in the water pipe 1b is heated and becomes steam, which is then transferred to the upper header 1d.
The steam is collected and stored at the steam pipe 1q and supplied to the steam load through the steam pipe 1q.
そして、燃焼制御に関しては、上部管寄せ1d
内の蒸気圧を連通管1lを通じて抽出して圧力検
出部5に供給し、圧力検出部5は上部管寄せ1d
内の蒸気圧が予め設定された下限蒸気圧に達した
ことを検出したときには、下限蒸気圧信号を、同
様に、上限蒸気圧に達したことを検出したときに
は、上限蒸気圧信号を燃焼制御部6に送る。 Regarding combustion control, the upper header 1d
The steam pressure in the upper header 1d is extracted through the communication pipe 1l and supplied to the pressure detector 5.
When the combustion control section detects that the vapor pressure within the combustion chamber has reached a preset lower limit vapor pressure, the lower limit vapor pressure signal is sent to the combustion control section. Send to 6.
燃焼制御部6は、蒸気の消費が続行して上部管
寄せ1d内の蒸気圧が降下し、下限蒸気圧信号を
受けたときには、制御信号線6aを通じて電動機
1fを始動させて、ブロア1gでもつて風道1h
を空気パージしてから制御信号線6bを通じて電
極棒1jに高電圧を印加するとともに、制御信号
線6cを通じて燃料ポンプ6dを始動させて、ノ
ズル棒1iから噴射される燃料に点火し燃焼を開
始させ、更に、蒸気の発生が続行して蒸気圧が上
昇し、圧力検出部5から上限蒸気圧信号を受けた
ときには、制御信号線6cを通じて燃料ポンプ6
dを停止させて、燃料供給を断つことにより燃焼
を停止させるとともに、燃焼ガスの排出を待つて
制御信号線6aを通じて電動機1fを停止させて
ブロア1gからの送風を断つ。 When the steam pressure in the upper header 1d drops due to continued consumption of steam and a lower limit steam pressure signal is received, the combustion control section 6 starts the electric motor 1f through the control signal line 6a and starts the blower 1g. Wind path 1h
After purging with air, a high voltage is applied to the electrode rod 1j through the control signal line 6b, and at the same time, the fuel pump 6d is started through the control signal line 6c to ignite the fuel injected from the nozzle rod 1i and start combustion. Furthermore, when steam generation continues and the steam pressure increases and an upper limit steam pressure signal is received from the pressure detection section 5, the fuel pump 6
d to stop combustion by cutting off the fuel supply, and after waiting for the combustion gas to be discharged, the electric motor 1f is stopped via the control signal line 6a and the air blowing from the blower 1g is cut off.
而して、燃焼の断続制御でもつて、上部管寄せ
1d内の蒸気圧を上下限蒸気圧として予め設定さ
れた両圧力値の間の圧力値に保つことができるも
のである。 Thus, even with intermittent control of combustion, the steam pressure in the upper header 1d can be maintained at a pressure value between the two pressure values preset as the upper and lower steam pressure limits.
なお、簡便な装置では、電動機1f、燃料ポン
プ6dの始動・停止制御、及び電極棒1jへの高
電圧の印加を同時に行つてもよい。 In addition, in a simple device, the start/stop control of the electric motor 1f and the fuel pump 6d, and the application of high voltage to the electrode rod 1j may be performed simultaneously.
更に、給水系に関しては、連通管1l内の気水
境界面、すなわち、水管1b中の缶水水位の変化
を水位検出部2に伝達し、水位検出部2は缶水水
位が予め設定された下限水位に達したことを検出
したときには、下限水位信号を、同様に、上限水
位に達したことを検出したときには、上限水位信
号を給水制御部3に送る。 Furthermore, regarding the water supply system, changes in the canned water level in the air-water interface in the communication pipe 1l, that is, in the water pipe 1b, are transmitted to the water level detection section 2, and the water level detection section 2 detects the canned water level set in advance. When it is detected that the lower limit water level has been reached, a lower limit water level signal is sent to the water supply control unit 3, and similarly, when it is detected that the upper limit water level has been reached, an upper limit water level signal is sent to the water supply control unit 3.
給水制御部3は、蒸気の消費により水管中の缶
水水位が降下し、水位検出部2から下限水位信号
を受けたときには、電動機4aを始動させて給水
ポンプ4でもつて下部管寄せ1cを通じて水管1
bへの給水を開始させ、給水が続行して缶水水位
が上昇し、水位検出部2から上限水位信号を受け
たときには、電動機4aを停止させて水管1bへ
の給水を断つ。 When the canned water level in the water pipe drops due to steam consumption and a lower limit water level signal is received from the water level detection unit 2, the water supply control unit 3 starts the electric motor 4a and causes the water supply pump 4 to lower the water pipe through the lower header 1c. 1
When the water supply to b is started, water supply continues, the can water level rises, and an upper limit water level signal is received from the water level detector 2, the electric motor 4a is stopped to cut off the water supply to the water pipe 1b.
而して、給水の断続制御でもつて、水管1b内
の缶水水位を上下限水位として予め設定された両
水位値の間の水位値に保つことができるものであ
る。 Thus, even with the intermittent water supply control, the water level of the canned water in the water pipe 1b can be maintained at a water level between the upper and lower limit water levels preset.
そして、かかる給水の断続制御と、前記燃焼の
断続制御は互いに別個独立に行われるものであ
る。 The intermittent control of water supply and the intermittent control of combustion are performed separately and independently from each other.
また、缶水のブローに際してはブローコツク1
pを開くことにより、排水管1nを通じて下部管
寄せ1c及び水管1b中の缶水の一部あるいは全
部をブローすることができるものである。 Also, when blowing canned water, use blowing stick 1.
By opening p, part or all of the canned water in the lower header 1c and the water pipe 1b can be blown out through the drain pipe 1n.
なお、ブロア1g、風道1h、ノズル棒1i、
電極棒1jから成るバーナは、これに限られるも
のではなく、要すれば、水管1b中の缶水を加熱
して蒸気を発生させ得れば足りるので、一般的に
は、電気ヒータ等をも含む加熱装置であればよ
い。 In addition, blower 1g, air passage 1h, nozzle rod 1i,
The burner consisting of the electrode rod 1j is not limited to this, and if necessary, it is sufficient to heat the canned water in the water pipe 1b to generate steam, so generally an electric heater or the like is also used. Any heating device including the above may be used.
而して、同様に、燃焼制御部6も加熱装置を断
続する加熱制御部であればよい。 Similarly, the combustion control section 6 may also be a heating control section that turns on and off the heating device.
続いて、第2図〜第4図に基づいて、この発明
の一実施例の構成及び動作を説明すれば以下の通
りである。 Next, the configuration and operation of an embodiment of the present invention will be described below based on FIGS. 2 to 4.
第2図は第1図における水位検出部2及び給水
制御部3の構成を抽出して示すブロツク図であ
る。 FIG. 2 is a block diagram showing extracted configurations of the water level detection section 2 and water supply control section 3 in FIG. 1.
そして、第1図の構成との対比において、導管
1l′,1l″は上部管寄せ1dと下部管寄せ1cに
それぞれ接続されており、連通管1lには、水管
1b中の缶水の一部が抽出されて導かれている。 In comparison with the configuration shown in Fig. 1, the conduits 1l' and 1l'' are connected to the upper header 1d and the lower header 1c, respectively, and a portion of the canned water in the water pipe 1b is connected to the communicating pipe 1l. are extracted and derived.
水位検出部2は、連通管1lの水位が下限水位
Lに達したことを検知する下限水位プローブ2a
と、連通管1lの水位が上限水位Hに達したこと
を検知する上限水位プローブ2bとがそれぞれ下
限水位L、上限水位Hにその先端が位置するよう
に配設され、また、水中に埋没した水中電極2c
と、水中電極2cに一端が接続された交流電源2
dと、交流電源2dの他端と下限水位プローブ2
aとの間に挿入された第一の電流検出器2eと、
交流電源2dと上限水位プローブ2bとの間に挿
入された第二の電流検出器2fとを具備してい
る。 The water level detection unit 2 includes a lower limit water level probe 2a that detects that the water level of the communication pipe 1l has reached the lower limit water level L.
and an upper limit water level probe 2b that detects when the water level of the communication pipe 1l has reached the upper limit water level H are arranged so that their tips are located at the lower limit water level L and the upper limit water level H, respectively, and are buried in water. Underwater electrode 2c
and an AC power source 2 whose one end is connected to the underwater electrode 2c.
d, the other end of the AC power supply 2d, and the lower limit water level probe 2
a first current detector 2e inserted between the
It includes a second current detector 2f inserted between the AC power source 2d and the upper limit water level probe 2b.
ここに、上限水位H及び下限水位Lは、水位検
出部2の連通管1l中に、給水の断続制御におけ
る缶水の上下限水位として予め設定された水位で
ある。 Here, the upper limit water level H and the lower limit water level L are water levels preset in the communication pipe 1l of the water level detection unit 2 as the upper and lower limit water levels of canned water in the intermittent control of water supply.
そして、△Lは、連通管1l中の下限水位Lの
給水開始時における水位低下変動幅である。 Further, ΔL is a fluctuation width of the lower limit water level L in the communication pipe 1l at the start of water supply.
給水制御部3は、第一の電流検出器2eの出力
端子がそのセツト端子に接続され、第二の電流検
出器2fの出力端子がインバータ3aを通じて、
そのリセツト端子に接続されたフリツプフロツプ
3bと、フリツプフロツプ3bの正相出力端子が
ドライバ3cを通じてその一端に接続され、その
他端が電源3dに接続されたリレー3eとから成
り、リレー3eの接点3e′は給水ポンプ4を駆動
する電動機4aの電源供給線4bに挿入される。 In the water supply control section 3, the output terminal of the first current detector 2e is connected to its set terminal, and the output terminal of the second current detector 2f is connected to the set terminal through the inverter 3a.
It consists of a flip-flop 3b connected to the reset terminal, and a relay 3e whose positive-phase output terminal is connected to one end of the flip-flop 3b through a driver 3c, and whose other end is connected to a power source 3d.The contact 3e' of the relay 3e is It is inserted into the power supply line 4b of the electric motor 4a that drives the water supply pump 4.
第3図は水位検出部2内の連通管1lの水位変
化Aと、第一、第二の電流検出器2e,2fの出
力信号C,Bと、フリツプフロツプ3bの正相出
力信号Dとを対比して示す波形図である。 Figure 3 compares the water level change A in the communication pipe 1l in the water level detector 2, the output signals C and B of the first and second current detectors 2e and 2f, and the positive phase output signal D of the flip-flop 3b. FIG.
上記構成から成る水位検出部2、給水制御部3
に関して、先ず、缶水濃縮のない状態、典型的に
は、ブロー後の給水直後の状態での給水制御の動
作を説明すれば以下の通りである。 Water level detection unit 2 and water supply control unit 3 configured as above
Regarding this, first, the operation of water supply control in a state where canned water is not concentrated, typically, immediately after water supply after blowing, will be described as follows.
いま、第3図Aaに示すように連通管1lの水
位が下限水位Lよりも高い位置にある場合には、
下限水位プローブ2aが水没して、水中電極2c
との間が水を通じて導通状態となり、交流電源2
dに対して第一の電流検出器2e、下限水位プロ
ーブ2a、水中電極2cから成る負荷回路が形成
されるので、第一の電流検出器2eに電流が流
れ、これを検出して第一の電流検出器2eは第3
図Cbに示すように「1」を出力する。 Now, as shown in Figure 3 Aa, if the water level of the communication pipe 1l is higher than the lower limit water level L,
The lower limit water level probe 2a is submerged, and the underwater electrode 2c
A state of conduction is established between the AC power source 2 through water, and the
Since a load circuit consisting of a first current detector 2e, a lower limit water level probe 2a, and an underwater electrode 2c is formed for d, a current flows through the first current detector 2e, which is detected and the first The current detector 2e is the third
Outputs "1" as shown in Figure Cb.
そして、水位が降下して、第3図Acに示すよ
うに、下限水位Lに達すると、下限水位プローブ
2aの先端が水面から離れ、交流電源2dに対す
る負荷回路が遮断されるので、第一の電流検出器
2eを通過する電流が零となり、これを検出し
て、第一の電流検出器2eは第3図Cdに示すよ
うに「0」を出力する。かかる第一の電流検出器
2eの出力信号の「1」から「0」への反転をセ
ツト端子に受けて、フリツプフロツプ3bが
「1」にセツトされ、その正相出力端子には、第
3図Deに示すように「0」から「1」への反転
信号が現われる。この信号を受けて、ドライバ3
cが導通状態となり、リレー3eが励磁されて、
接点3e′が閉成し、電動機4aに電源が供給され
るので、給水ポンプ4による給水が行われる。 Then, when the water level falls and reaches the lower limit water level L as shown in Figure 3 Ac, the tip of the lower limit water level probe 2a leaves the water surface and the load circuit to the AC power source 2d is cut off. The current passing through the current detector 2e becomes zero, and upon detecting this, the first current detector 2e outputs "0" as shown in FIG. 3 Cd. In response to the inversion of the output signal of the first current detector 2e from "1" to "0" at the set terminal, the flip-flop 3b is set to "1", and its positive phase output terminal has the signal shown in FIG. As shown in De, an inverted signal from "0" to "1" appears. Upon receiving this signal, driver 3
c becomes conductive, relay 3e is energized,
Since the contact 3e' is closed and power is supplied to the electric motor 4a, water is supplied by the water supply pump 4.
而して、フリツプフロツプ3bが「1」になつ
ている期間中、給水が続行し、第3図Afに示す
ように、水位が上昇し続ける。 Thus, while the flip-flop 3b is at "1", water supply continues and the water level continues to rise as shown in FIG. 3Af.
やがて、第3図Agに示すように、水位が上限
水位Hに達すると、いままで上限水位プローブ2
bが水没していなかつたために、第3図Bhに示
すように、「0」を出力していた第二の電流検出
器2fが第3図Biに示すように、「1」を出力す
るようになる。かかる第二の電流検出器2fの出
力信号の「0」から「1」への反転はインバータ
3aにより「1」から「0」への反転に変換され
て、フリツプフロツプ3bのリセツト端子に供給
されて、これを「0」にリセツトする。 Eventually, as shown in Figure 3Ag, when the water level reaches the upper limit water level H, the upper limit water level probe 2
b was not submerged in water, the second current detector 2f, which had been outputting "0" as shown in Figure 3 Bh, now outputs "1" as shown in Figure 3 Bi. become. The inversion of the output signal of the second current detector 2f from "0" to "1" is converted by the inverter 3a into an inversion from "1" to "0" and is supplied to the reset terminal of the flip-flop 3b. , reset this to "0".
而して、第3図Djに示すように、フリツプフ
ロツプ3bの正相出力が「0」となるので、リレ
ー3eが非励磁となり、接点3e′が開成し、給水
が停止する。 Then, as shown in FIG. 3Dj, the positive phase output of the flip-flop 3b becomes "0", so the relay 3e is de-energized, the contact 3e' is opened, and the water supply is stopped.
このようにして、給水ポンプ4が始動してから
停止するまでの期間T1(以下給水期間という)は
フリツプフロツプ3bが「1」になつている期間
でもつて特定されるものである。 In this way, the period T 1 from when the water supply pump 4 starts until it stops (hereinafter referred to as water supply period) is specified even during the period when the flip-flop 3b is set to "1".
そして、かかる給水ポンプの断続制御では、一
つの給水期間中に水管1bに蓄積される水量は下
限水位Lと上限水位Hとの差Wに基づいて各ボイ
ラ系固有の値に特定されるものである。 In such intermittent control of the water supply pump, the amount of water accumulated in the water pipe 1b during one water supply period is specified to a value unique to each boiler system based on the difference W between the lower limit water level L and the upper limit water level H. be.
給水を停止した後は、第3図Akに示すように、
水位は再び降下して下限水位Lに達し、更に、同
様の動作が繰返し行われて、水位が下限水位Lと
上限水位Hとの間の水位に保たれる。 After stopping the water supply, as shown in Figure 3 Ak,
The water level falls again and reaches the lower limit water level L, and the same operation is repeated to maintain the water level between the lower limit water level L and the upper limit water level H.
次に缶水の濃縮化が進行した状態での給水制御
動作を説明すれば以下の通りである。 Next, the water supply control operation in a state where the concentration of canned water has progressed will be explained as follows.
缶水の濃縮化が進行した状態では、缶水の物性
の変化に起因して、高温下における水管1b中で
の缶水の泡立ちが激しくなるので、その泡立ちの
反作用を受けて、連通管1lの水位が押し上げら
れて、水管1bの缶水水位よりも高くなり、しか
も、給水開始時には、缶水の温度が低下して、泡
立ちが抑制されるので、上記反作用も消滅して、
連通管1lの水位が水管1bの缶水水位に等しく
なるという現象が観測される。 In a state where the concentration of canned water has progressed, the canned water foams violently in the water pipe 1b under high temperature due to changes in the physical properties of the canned water. The water level is pushed up and becomes higher than the can water level in the water pipe 1b, and when water supply starts, the temperature of the can water decreases and foaming is suppressed, so the above reaction also disappears,
A phenomenon is observed in which the water level in the communication pipe 1l becomes equal to the canned water level in the water pipe 1b.
而して、第3図Acに示すように、連通管1l
の水位が下限水位Lに達すると、前記動作に従つ
て、水管1bへの給水が開始されて、水管1b中
の缶水の温度が低下し、缶水の泡立ちが慎静化
し、泡立ちによる反作用が消滅するので、連通管
1lの水位は第3図Ac′に示すように、急激に降
下して、泡立ち消滅後における水管1bの缶水水
位に等しくなる。 Therefore, as shown in Fig. 3 Ac, the communication pipe 1l
When the water level reaches the lower limit water level L, water supply to the water pipe 1b is started according to the above operation, the temperature of the canned water in the water pipe 1b decreases, the bubbling of the canned water becomes calm, and the reaction caused by the bubbling is reduced. disappears, the water level in the communication pipe 1l drops rapidly, as shown in Fig. 3 Ac', and becomes equal to the can water level in the water pipe 1b after the bubbling disappears.
すなわち、缶水の泡立ちの反作用により押し上
げられた連通管1lの水位が下限水位に達した時
点では、水管1b中の泡立つた缶水の気泡層を除
く缶水水面は、下限水位Lよりも△Lだけ下方に
存在しており、給水開始に伴う気泡層の消滅に際
して、連通管1lの水位は缶水水面に向つて、水
位変化変動幅△Lだけ低下するものである。 That is, at the time when the water level in the communication pipe 1l pushed up by the reaction of the bubbling of the canned water reaches the lower limit water level, the water level of the canned water excluding the bubble layer of the bubbling canned water in the water pipe 1b is △ lower than the lower limit water level L. When the bubble layer disappears with the start of water supply, the water level in the communicating pipe 1l decreases by the water level change range ΔL toward the water surface of the can.
そして、缶水の供給が続行されると、水管1b
中の缶水水位の上昇に対応して連通管1lの缶水
も第3図Af′に示すように上昇して、第3図
Ag′に示す時点で、上限水位センサHに達し、給
水が停止する。 Then, when the supply of canned water continues, water pipe 1b
Corresponding to the rise in the water level in the can, the can water in the 1 liter communication pipe also rises as shown in Fig. 3 Af'.
At the time indicated by Ag', the upper limit water level sensor H is reached and the water supply is stopped.
このとき、同時点で開始した水位上昇工程で
も、第3図Af′に示すような缶水が濃縮された状
態での水位上昇工程では、第3図Ac′に示すよう
に、水位低下変動幅△Lだけ下方を起点としてい
るので、第3図Ag,g′に示すように、上限水位
Hに到達する時点が△T1だけ遅れることとなる。 At this time, even if the water level raising process starts at the same time, the water level lowering fluctuation range will change as shown in Figure 3 Ac' in the water level raising process in a state where the canned water is concentrated as shown in Figure 3 Af'. Since the starting point is ΔL downward, the time point at which the upper limit water level H is reached is delayed by ΔT 1 , as shown in FIG. 3Ag and g'.
而して、上限水位プローブ2bの出力信号が
「0」から「1」に反転する時点も、第3図Bi′に
示すように、△T1だけ遅れ、結局、フリツプフ
ロツプ3bがリセツトされる時点も第3図Dj′に
示すように、△T1だけ遅れるので、給水期間T1
が△T1だけ増大するものである。 Therefore, the time when the output signal of the upper limit water level probe 2b is reversed from "0" to "1" is also delayed by ΔT1 , as shown in FIG. 3 Bi', and eventually the time when the flip-flop 3b is reset is reached. As shown in Figure 3 Dj', there is a delay of △T 1 , so the water supply period T 1
increases by △T 1 .
付言すれば、缶水が濃縮されている場合でも、
給水が続行し、連通管1lの水位が上限水位Hに
達するまでには、温度低下により泡立ちが消滅し
て、連通管1lの水位は缶水水位に等しくなり、
結局、給水停止時における水管1b中の缶水保有
量は、缶水が濃縮されていない場合のそれに等し
くなるので、給水期間の増大に伴つて、1回の断
続制御でもつて供給される水量が増大することと
なる。 Additionally, even if canned water is concentrated,
Water supply continues, and by the time the water level in the communication pipe 1L reaches the upper limit water level H, the bubbling has disappeared due to the temperature drop, and the water level in the communication pipe 1L has become equal to the can water level.
In the end, the amount of canned water held in the water pipe 1b when the water supply is stopped is equal to that when the canned water is not concentrated, so as the water supply period increases, the amount of water supplied even with one intermittent control will decrease. It will increase.
かかる給水期間の増大傾向は、給水開始直前に
おける水管1b中の缶水の泡立ちに起因する連通
管1lの水位低下変動幅△Lに依存しているので
あるが、一般に、缶水の濃縮化の進行に伴つて、
給水開始直前における泡立ちが激化する傾向にあ
るので、缶水の濃縮化の進行に応じて、水位低下
変動幅△Lが増大し、而して、給水期間T1も増
大するものである。 This tendency to increase the water supply period depends on the fluctuation width ΔL of the decrease in the water level in the communicating pipe 1l due to bubbling of canned water in the water pipe 1b immediately before the start of water supply, but in general, it is due to the concentration of canned water. As the progress progresses,
Since foaming tends to intensify just before the start of water supply, as the canned water becomes more concentrated, the water level drop fluctuation range ΔL increases, and thus the water supply period T1 also increases.
したがつて、給水期間の増大傾向が缶水の濃縮
度合いを表わしているので、これを計測すること
により、缶水濃縮度を推量することができるわけ
である。 Therefore, since the increasing tendency of the water supply period represents the degree of concentration of the canned water, by measuring this, the degree of concentration of the canned water can be estimated.
更に、付言すれば、缶水が濃縮されている状態
で、第3図Ag′に示すように、連通管1lの水位
が上限水位Hに到達し、給水が停止されると、缶
水の蒸発に伴つて、連通管1lの水位は第3図
Ak′に示すように、湾曲部を有する曲線に沿つて
降下する。 Furthermore, in a state where the canned water is concentrated, when the water level in the communication pipe 1l reaches the upper limit water level H and the water supply is stopped, as shown in Fig. 3Ag', the canned water will evaporate. Accordingly, the water level of 1 liter of communication pipe is as shown in Figure 3.
As shown in Ak', it descends along a curved line with a curved part.
そして、かかる湾曲部は、給水期間中に泡立ち
が消滅していた缶水が、給水の停止により、再び
泡立ちを生じ始め、連通管1lの水位が缶水水位
に対して押し上げられることに起因するものであ
る。 This curved portion is caused by the fact that the canned water, which had lost its foaming during the water supply period, begins to foam again when the water supply is stopped, and the water level of the communication pipe 1l is pushed up relative to the canned water level. It is something.
なお、上記実施例では、上下限水位プローブ2
b2aと水中電極2c間の電導性を利用して、水
位を検出しているが、これに限られるものではな
く、上下限水位プローブ2b2a等の構成に代え
て、上下限位置に発光素子と受光素子を対向配置
して成る光学的水位センサ、磁気を帯びた浮子を
上下限位置に配設された磁気センサでもつて検出
する磁気的水位センサ等を含む上下限水位センサ
を採用することは随意である。 In addition, in the above embodiment, the upper and lower limit water level probe 2
Although the water level is detected using the conductivity between b2a and the underwater electrode 2c, the present invention is not limited to this. Instead of the upper and lower limit water level probes 2b2a, etc., a light emitting element and a light receiving element may be installed at the upper and lower limit positions. It is optional to adopt an upper and lower limit water level sensor including an optical water level sensor in which elements are arranged facing each other, a magnetic water level sensor in which a magnetic float is detected by a magnetic sensor placed at the upper and lower limit positions, etc. be.
あるいは、唯一の圧力センサから缶水水位に比
例する水圧信号を得て、この信号が上下限設定値
に達したことをコンパレータでもつて検出する構
成としてもよい。上記構成のように、唯一のハー
ドウエアでもつて、上下限水位センサを一体に実
現することもできるので、この明細書にいう下限
水位センサと上限水位センサは必ずしも別個独立
のハードウエアとして実現される構成に限定され
るものではない。 Alternatively, a configuration may be adopted in which a water pressure signal proportional to the can water level is obtained from a single pressure sensor, and a comparator detects when this signal reaches the upper and lower limit set values. As in the above configuration, it is possible to realize the upper and lower limit water level sensors in one piece using only one piece of hardware, so the lower limit water level sensor and upper limit water level sensor referred to in this specification are not necessarily realized as separate and independent hardware. It is not limited to the configuration.
第4図は、給水期間計測部と缶水濃縮度演算部
の構成を示すブロツク図である。同図において、
給水期間計測部7は、クロツクパルス発振器7a
と、一つの入力端子がクロツクパルス発振器7a
の出力端子に接続され、他の一つの入力端子が給
水制御部3(フリツプフロツプ3bの正相出力端
子)に接続されたアンドゲート7bと、アンドゲ
ート7bの出力端子がその入力端子に接続された
カウンタ7cと、その入力端子がフリツプフロツ
プ3bの正相出力端子に接続され、その出力端子
がカウンタ7のクリア端子に接続された単安定マ
ルチバイブレータ7dとから成る。 FIG. 4 is a block diagram showing the configuration of the water supply period measurement section and the canned water concentration calculation section. In the same figure,
The water supply period measuring section 7 includes a clock pulse oscillator 7a.
and one input terminal is the clock pulse oscillator 7a.
and an AND gate 7b whose other input terminal is connected to the water supply control section 3 (the positive phase output terminal of the flip-flop 3b), and the output terminal of the AND gate 7b is connected to its input terminal. It consists of a counter 7c and a monostable multivibrator 7d whose input terminal is connected to the positive phase output terminal of the flip-flop 3b and whose output terminal is connected to the clear terminal of the counter 7.
缶水濃縮度演算部8は、一つの入力端子がカウ
ンタ7cの出力端子に接続され、その制御端子が
フリツプフロツプ3bの正相出力端子に接続され
た演算器8aと、その出力端子が演算器8aの他
の入力端子に接続された基準給水期間設定器8b
とから成る。9は演算部8aに接続された表示部
である。 The canned water concentration calculation unit 8 includes a calculation unit 8a whose one input terminal is connected to the output terminal of the counter 7c and whose control terminal is connected to the positive phase output terminal of the flip-flop 3b, and whose output terminal is connected to the calculation unit 8a. Reference water supply period setting device 8b connected to the other input terminal of
It consists of 9 is a display unit connected to the calculation unit 8a.
上記構成からなる給水期間計測部7と缶水濃縮
度演算部8の動作を説明すれば以下の通りであ
る。 The operations of the water supply period measurement section 7 and the canned water concentration calculation section 8 having the above configuration will be explained as follows.
給水制御部3のフリツプフロツプ3bの正相出
力端子から信号を受けて、これが第3図Deに示
すように、「1」になると、フリツプフロツプ3
bが「1」である期間中、すなわち、給水期間中
に限り、アンドゲート7bが開いてクロツクパル
ス発振器7aからのクロツクパルスをカウンタ7
cに導き、これを計数させる。 When a signal is received from the positive phase output terminal of the flip-flop 3b of the water supply control unit 3 and becomes "1" as shown in FIG. 3 De, the flip-flop 3
Only during the period when b is "1", that is, during the water supply period, the AND gate 7b is opened and the clock pulse from the clock pulse oscillator 7a is sent to the counter 7.
c and have them counted.
そして、第3図Dj′に示すように、フリツプフ
ロツプ3bが「1」から「0」に反転すると、ア
ンドゲート7bが閉じて、カウンタ7cへのクロ
ツクパルスの供給が断たれ、カウンタ7cには、
缶水の濃縮度に応じて増大した給水期間、第3図
Dに示す例に従えば、(T1+△T1)なる給水期間
を表わすデイジタル符号が成生され、カウンタ7
cはこれを給水期間信号S1として出力する。この
ときに、同時に、フリツプフロツプ3bの「1」
から「0」への反転を制御端子に受けて演算器8
aは後述の演算処理を実行する。 Then, as shown in FIG. 3Dj', when the flip-flop 3b is inverted from "1" to "0", the AND gate 7b is closed and the supply of clock pulses to the counter 7c is cut off, and the counter 7c has the following values:
According to the example shown in FIG. 3D, which increases the water supply period according to the concentration of canned water, a digital code representing the water supply period (T 1 +△T 1 ) is generated, and the counter 7
c outputs this as the water supply period signal S1 . At this time, at the same time, flip-flop 3b's "1"
When the control terminal receives the inversion from 0 to 0, the arithmetic unit 8
a executes arithmetic processing to be described later.
上記演算器8aによる演算処理が完了した後
に、前述のフリツプフロツプ3bの「1」から
「0」への反転に際して、トリガされ、準安定状
態に移行していた単安定マルチバイブレータ7d
が安定状態に復帰して、クリアパルスをカウンタ
7cのクリア端子に送るので、カウンタ7cはク
リアされ、次回の計測に備えられる。 After the arithmetic processing by the arithmetic unit 8a is completed, the monostable multivibrator 7d is triggered and transitioned to a metastable state when the flip-flop 3b is inverted from "1" to "0".
returns to a stable state and sends a clear pulse to the clear terminal of the counter 7c, so the counter 7c is cleared and ready for the next measurement.
この間、すなわち、カウンタ7cがクリアされ
る前に、演算器8aは、カウンタ7cが出力する
給水期間信号S1から、デイジタルスイツチ等より
成る基準給水期間設定器8bに予め設定されてい
る缶水濃縮のない状態における給水期間(以下基
準給水期間という)を表わす基準給水期間信号S2
を減算して、その減算結果、すなわち、第3図D
に示す例に従えば、給水期間(T1+△T1)の基
準給水期間T1に対する増分△T1を表わす缶水濃
縮度信号S3を出力する。 During this time, that is, before the counter 7c is cleared, the calculator 8a calculates the canned water concentration preset in the reference water supply period setting device 8b, which is made of a digital switch, etc., from the water supply period signal S1 outputted by the counter 7c. Standard water supply period signal S 2 representing the water supply period in the absence of (hereinafter referred to as standard water supply period)
, and the subtraction result, that is, Fig. 3D
According to the example shown in , a can water concentration signal S 3 representing an increment ΔT 1 of the water supply period (T 1 +ΔT 1 ) with respect to the reference water supply period T 1 is output.
このようにして得られた缶水濃縮度信号S3は、
缶水の濃縮化の進行に応じて増大する傾向にある
ので、この信号に基づいて缶水濃縮度を推量する
ことができるものである。 The canned water concentration signal S3 obtained in this way is
Since it tends to increase as the concentration of canned water progresses, the degree of concentration of canned water can be estimated based on this signal.
表示部9は、演算器8aから缶水濃縮度信号S3
を受けて、これを直接的に、あるいは、実験式に
従つて現実の缶水濃縮度を表わす数値に変換し
て、計数表示管でもつて目視可能に表示する。 The display unit 9 receives a can water concentration signal S3 from the calculator 8a.
Then, this is converted directly or according to an experimental formula into a numerical value representing the actual concentration of canned water, and the numerical value is visually displayed on a digital display tube.
この発明に牽連する第二の発明の構成は、前記
この発明の構成における水位検出部2と給水制御
部3に加えて、給水回数計測部を付設して、特定
期間中の給水回数を計測し、更に、缶水濃縮度演
算部を付設して、予め設定された缶水濃縮のない
状態における基準給水回数から給水回数計測部に
て計測された給水回数を減算して、給水回数の基
準給水回数に対する減分を算出することにより、
特定期間中の給水回数の減少傾向を演算して、そ
の演算結果を缶水濃縮度信号として出力するよう
にしたことを特徴とするものである。 A second configuration of the invention that is related to the present invention is that, in addition to the water level detection unit 2 and the water supply control unit 3 in the configuration of the present invention, a water supply frequency measuring unit is attached to measure the number of water supply during a specific period. Furthermore, a canned water concentration calculating section is attached, and the number of times of watering measured by the number of times of watering is measured by the number of times of watering is subtracted from the standard number of times of watering in a state where there is no concentration of canned water, which is set in advance, to determine the standard number of times of watering. By calculating the decrement for the number of times,
The present invention is characterized in that a decreasing trend in the number of water supplies during a specific period is calculated, and the result of the calculation is output as a canned water concentration signal.
第5図に基づいて、この発明に牽連する第二の
発明の実施例の構成及び動作を説明すれば以下の
通りである。 Based on FIG. 5, the structure and operation of the embodiment of the second invention related to the present invention will be explained as follows.
第5図は、この発明に牽連する第二の発明の実
施例における給水回数計測部と、缶水濃縮度演算
部の構成を抽出して示すブツク図である。 FIG. 5 is a book diagram extracting the configuration of the water supply frequency measuring section and the canned water concentration calculation section in an embodiment of the second invention related to the present invention.
なお、他の構成要素は第2図に示す構成要素と
同一である。 Note that the other components are the same as those shown in FIG.
第5図において、給水回数計測部10は、その
入力端子が給水制御部3に接続されたカウンタ1
0aと、カウンタ10aに接続されたラツチ10
bと、その出力端子がラツチ10bのクロツク端
子に接続されたタイマ10cと、その入力端子が
タイマ10cの出力端子に接続され、その出力端
子がカウンタ10aのクリア端子に接続された単
安定マルチバイブレータ10dとから成る。 In FIG. 5, the water supply frequency measuring unit 10 is connected to a counter 1 whose input terminal is connected to the water supply control unit 3.
0a and latch 10 connected to counter 10a.
b, a timer 10c whose output terminal is connected to the clock terminal of latch 10b, and a monostable multivibrator whose input terminal is connected to the output terminal of timer 10c and whose output terminal is connected to the clear terminal of counter 10a. 10d.
缶水濃縮度演算部11は、一つの入力端子がラ
ツチ10bに接続され、その制御端子にタイマ1
0cの出力端子が接続された演算器11aと、演
算器11aのもう一つの入力端子に接続された基
準給水回数設定器11bとから成る。12は演算
器11aに接続された表示部である。 The canned water concentration calculating section 11 has one input terminal connected to the latch 10b, and a timer 1 connected to the control terminal.
It consists of an arithmetic unit 11a connected to an output terminal of 0c, and a reference water supply frequency setting device 11b connected to another input terminal of the arithmetic unit 11a. 12 is a display section connected to the computing unit 11a.
上記構成では、給水制御部3に含まれるフリツ
プフロツプ3bの正相出力端子から給水期間中
「1」となる信号の供給を受けて、カウンタ10
aはその信号の「1」から「0」への反転回数、
すなわち、給水が停止された回数を計数する。そ
の間、タイマ10cは経時動作を続け、予め設定
された特定期間の経過を検出した際に、出力信号
をラツチ10のクロツク端子に送り、その時点で
のカウンタ10aの内容、すなわち、特定期間中
の給水停止回数を表わすデイジタル符号をラツチ
10bに一旦記憶させる。 In the above configuration, the counter 10 receives a signal that becomes "1" during the water supply period from the positive phase output terminal of the flip-flop 3b included in the water supply control section 3.
a is the number of times the signal flips from “1” to “0”;
That is, the number of times the water supply is stopped is counted. Meanwhile, the timer 10c continues to operate over time, and when it detects the elapse of a preset specific period, it sends an output signal to the clock terminal of the latch 10, and displays the contents of the counter 10a at that time, i.e., the contents of the counter 10a during the specific period. A digital code representing the number of water supply stops is temporarily stored in the latch 10b.
そして、この時点でトリガされ準安定状態に移
行した単安定マルチバイブレータ10dでもつ
て、上記ラツチ10bによる記憶が完了するのを
待つて、直ちに、カウンタ10aをクリアする。 The monostable multivibrator 10d, which has been triggered at this point and has entered the metastable state, immediately clears the counter 10a after waiting for the storage by the latch 10b to be completed.
而して、カウンタ10aは特定期間の給水停止
回数を計数した後、直ちに、次の特定期間につい
ての給水停止回数の計数が可能な状態で待期する
ことができる。 Thus, after the counter 10a counts the number of water supply stops in a specific period, it can immediately wait in a state where it can count the number of water supply stops in the next specific period.
なお、上記実施例では、カウンタ10aは給水
停止回数を計数しているが、給水制御部3に含ま
れるフリツプフロツプ3bの補相出力端子をカウ
ンタ10aの入力端子に接続する構成とすれば、
カウンタ10aでもつて給水停止回数を計数する
ことができる。 In the above embodiment, the counter 10a counts the number of water supply stops, but if the complementary output terminal of the flip-flop 3b included in the water supply control unit 3 is connected to the input terminal of the counter 10a,
The counter 10a can also count the number of times water supply is stopped.
そして、特定期間中における両者の発生回数
は、一般に等しいので、給水回数として給水停止
回数を計測するか、給水始動回数を計測するかは
随意である。 Since the number of occurrences of both during a specific period is generally the same, it is optional whether to measure the number of water supply stops or the number of water supply starts as the number of water supply times.
さて、この間に、演算器11aは、経時動作完
了時のタイマ10cからの出力信号に応答して、
基準給水回数設定器11bが出力している基準給
水回数信号S2′、すなわち、基準給水期間に対応
する給水回数を表わす信号からラツチ10bが出
力している給水回数信号S1′を減算して、その減
算結果、すなわち、特定期間中における給水回数
の基準給水回数に対する減分を表わす缶水濃縮度
信号S3′を出力する。 Now, during this time, the arithmetic unit 11a responds to the output signal from the timer 10c at the time of completion of the elapsed operation, and
The water supply frequency signal S 1 ' output by the latch 10b is subtracted from the reference water supply frequency signal S 2 ' output by the reference water supply frequency setting device 11b , that is, the signal representing the water supply frequency corresponding to the reference water supply period. , outputs a can water concentration signal S 3 ' representing the result of the subtraction, that is, the decrement of the number of times of water supply during the specific period from the reference number of times of water supply.
このようにして得られた缶水濃縮度信号S3′は
缶水の濃縮化の進行に応じて減少するところにあ
るので、この信号に基づいて缶水濃縮度を推量す
ることができるものである。 Since the canned water concentration signal S 3 ′ obtained in this way decreases as the concentration of canned water progresses, it is possible to estimate the canned water concentration based on this signal. be.
表示部12は演算器11aからの缶水濃縮度信
号S3′を受けて、これを直接的に、あるいは、実
験式に従つて現実の缶水濃縮度を表わす数値に変
換して、計数表示管等でもつて、目視可能に表示
する。 The display unit 12 receives the canned water concentration signal S 3 ' from the calculator 11a, and displays it directly or by converting it into a numerical value representing the actual canned water concentration according to an experimental formula. Even pipes, etc. should be clearly marked.
なお、この発明及びこの発明に牽連する第二の
発明の上記実施例では、給水期間計測部3、給水
回数計測部10は、1回の給水に関して給水期間
を、また、一つの特定期間に関して給水回数を計
測して、それぞれ、一つの給水期間信号S1、一つ
の給水回数信号S1′を出力し、これらに基づいて、
缶水濃縮度演算部8,11は一つの缶水濃縮度信
号S3S3′を算出しているが、複数回の給水に関し
て給水期間を計測して、これらの平均値を算出し
て、一つの給水期間信号として処理し、あるい
は、複数の特定期間に関して給水回数を計測し
て、これらの平均値を算出して、これを一つの給
水回数信号として処理することもできる。そのよ
うにすれば、ボイラ系の瞬時的変動に起因する給
水期間信号、給水回数信号のバラツキを回避で
き、より安定で正確な判断が得られるという実益
がある。 In the above embodiments of this invention and the second invention linked to this invention, the water supply period measuring section 3 and the water supply frequency measuring section 10 measure the water supply period for one water supply and the water supply period for one specific period. The number of times is measured, and one water supply period signal S 1 and one water supply frequency signal S 1 ' are output, respectively, and based on these,
The canned water concentration calculation units 8 and 11 calculate one canned water concentration signal S 3 S 3 ', but they measure the water supply period for multiple water supplies and calculate the average value of these. It is also possible to process this as one water supply period signal, or to measure the number of water supplies for a plurality of specific periods, calculate the average value thereof, and process this as one water supply frequency signal. By doing so, it is possible to avoid variations in the water supply period signal and water supply frequency signal caused by instantaneous fluctuations in the boiler system, and there is a practical benefit in that more stable and accurate judgment can be obtained.
また、この発明及びこの発明に牽連する第二の
発明の上記実施例では、基準給水期間設定器8
b、基準給水回数設定器11bを設けて、基準給
水期間、基準給水回数を予め手動操作により設定
する構成を採用しているが、設定は手動操作によ
る設定に限られるものではなく、ブロー後の給水
直後に給水期間計測部7、給水回数計測部10に
て得られる給水期間信号、給水回数信号を基準給
水期間設定器8b、基準給水回数設定器11bに
転送してこれを記憶させることにより、基準給水
期間、基準給水回数を自動的に設定できる構成と
してもよい。 Further, in the above embodiment of this invention and the second invention linked to this invention, the reference water supply period setting device 8
b. A reference water supply frequency setting device 11b is provided, and the reference water supply period and reference water supply frequency are set in advance by manual operation. However, the setting is not limited to manual operation; Immediately after water supply, the water supply period signal and water supply frequency signal obtained by the water supply period measuring section 7 and the water supply frequency measuring section 10 are transferred to the reference water supply period setting device 8b and the reference water supply frequency setting device 11b and stored therein. A configuration may be adopted in which the standard water supply period and the standard water supply frequency can be automatically set.
このようにすれば、簡便な操作でもつて、ボイ
ラ系個有の基準給水期間、基準給水回数を正確に
設定することができるという実益がある。 This has the practical benefit of being able to accurately set the standard water supply period and standard water supply frequency specific to the boiler system with a simple operation.
特に、この発明及びこの発明に牽連する第二の
発明の構成では、蒸気負荷によつて基準給水期
間、基準給水回数が変化するので、各蒸気負荷ご
との基準値を自動的に設定できるという上記実益
は大である。 In particular, in the configuration of this invention and the second invention linked to this invention, the reference water supply period and the reference water supply frequency change depending on the steam load, so the reference value for each steam load can be automatically set. The actual benefits are huge.
以上のように、この発明は連通管で缶水が導か
れた水位検出部と給水制御部を備えて、連通管の
水位が下限水位に到達したときに給水ポンプを始
動させ、連通管の水位が上限水位に到達したとき
に給水ポンプを停止させるようにしたボイラ系に
おいて、給水期間計測部と缶水濃縮度演算部とを
付設して、給水期間を計測し、これと基準給水期
間との差を算出することにより、給水開始直前の
高温下では、缶水の濃縮化の進行に応じた度合い
で水管中に気泡が発生し、その反作用を受けて連
通管の水位が押し上げられ、給水開始に際して
は、水管中の気泡が消滅して連通管の水位が、缶
水の濃縮化の進行に応じた水位低下変動幅だけ低
下して、水管中の缶水水位に等しくなり、そし
て、給水期間中は連通管の水位が缶水水位に特し
く保たれるために、缶水の濃縮化が進むにつれて
給水開始時の缶水水位の位置と給水停止時の缶水
水面の位置との差が増大することに起因する給水
期間の増大傾向を缶水濃縮度信号として出力する
ように構成されている。 As described above, the present invention is equipped with a water level detection unit and a water supply control unit to which canned water is guided through a communication pipe, and starts the water supply pump when the water level in the communication pipe reaches the lower limit water level, and controls the water level in the communication pipe. In a boiler system in which the water supply pump is stopped when the water level reaches the upper limit water level, a water supply period measurement section and a canned water concentration calculation section are attached to measure the water supply period and calculate the difference between this and the standard water supply period. By calculating the difference, it was found that under high temperatures just before the start of water supply, air bubbles are generated in the water pipe at a rate corresponding to the progress of concentration of canned water, and the water level in the communication pipe is pushed up by the reaction, causing water supply to start. At this time, the air bubbles in the water pipe disappear and the water level in the communicating pipe decreases by the amount of the water level drop fluctuation range that corresponds to the progress of concentration of canned water, and becomes equal to the canned water level in the water pipe, and the water supply period ends. Inside, the water level in the communication pipe is kept specifically at the canned water level, so as canned water becomes more concentrated, the difference between the canned water level when water supply starts and the canned water level when water supply stops increases. It is configured to output an increasing tendency of the water supply period due to the increase as a canned water concentration signal.
更に、この発明に牽連する第二の発明は、この
発明の水位検出部と給水制御部に加えて、給水回
数計測部と缶水濃縮度演算部とを付設して、特定
期間中の給水回数を計数し、これと基準給水回数
との差を検出することにより、特定期間中の給水
回数の減少傾向を缶水濃縮度製信号として出力す
るように構成されている。 Further, a second invention related to the present invention is that, in addition to the water level detection section and the water supply control section of the present invention, a water supply frequency measuring section and a canned water concentration calculating section are attached, and the number of water supply times during a specific period is determined. By counting the number of times and detecting the difference between this and the reference number of times of water supply, the system is configured to output a decreasing tendency of the number of times of water supply during a specific period as a canned water concentration signal.
したがつて、この発明及びこの発明に牽連する
第二の発明によれば、給水期間の増大傾向、及び
特定期間中の給水回数の減少傾向と缶水濃縮度と
の強い相関関係を直接的に利用しているので、従
前における累積燃料消費量をドラム缶等の貯蔵容
器を単位として計量する場合に比べれば、高精度
に缶水濃縮度を計測でき、ブロー時期を正確に把
握できるという効果がある。 Therefore, according to this invention and the second invention linked to this invention, it is possible to directly determine the strong correlation between the increasing tendency of the water supply period, the decreasing tendency of the number of water supply during a specific period, and the concentration of canned water. Compared to the conventional method of measuring cumulative fuel consumption in units of storage containers such as drums, this method has the effect of being able to measure canned water concentration with high accuracy and accurately determining the timing of blowing. .
更に、給水期間及び特定期間中の給水回数とい
う比較的短期間の計測でもつて得られる情報に基
づいて演算処理を実行しているので、缶水濃縮度
を実質的に連続計測できるという効果もある。 Furthermore, since calculation processing is performed based on information obtained even from relatively short-term measurements such as the water supply period and the number of water supplies during a specific period, it has the effect of being able to virtually continuously measure the concentration of canned water. .
加えて、自動的に缶水濃縮度信号が得られるの
で、従前のように、ドラム缶等の貯蔵容器をいち
いち計数して記録するという煩雑な作業が不要と
なり、而して、計数記録の懈怠もなく、ブロー時
期を失する危険性が極めて少なくなるという効果
もある。 In addition, since canned water concentration signals can be obtained automatically, the complicated work of counting and recording storage containers such as drums is no longer necessary, and there is no need to neglect counting and recording. There is also the effect that the risk of losing the blow-drying time is extremely reduced.
しかも、この発明及びこの発明に牽連する第二
の発明の構成における水位検出部と給水制御部
は、給水の断続制御には不可欠の構成要素であ
り、これらをそつくりそのまま利用して、給水制
御部から得られる給水ポンプの始動停止信号を処
理するための構成要素を付設すれば足りるので、
構成が簡潔で無駄がなく、低コストで実現できる
という利点がある。 Moreover, the water level detection section and the water supply control section in the configuration of this invention and the second invention linked to this invention are essential components for the intermittent control of the water supply, and these can be used as they are to control the water supply. It is sufficient to add a component to process the water pump start/stop signal obtained from the section.
It has the advantage of having a simple configuration, no waste, and can be realized at low cost.
第1図Aはこの発明の構成を付設することがで
きる小形ボイラ系の構成を示すブロツク図、第1
図Bは第1図Aにおけるボイラ1のA−A断面
図、第2図〜第4図はこの発明の実施例に関する
ものであり、第2図は水位検出部と給水制御部の
構成を示すブロツク図、第3図は第2図の構成に
おける要部の波形図、第4図は給水期間計測部と
缶水濃縮度演算部の構成を示すブロツク図、第5
図はこの発明に牽連する第二の発明の実施例の構
成を示すブロツク図である。
1……ボイラ、2……水位検出部、3……給水
制御部、4……給水ポンプ、7……給水期間計測
部、8……蒸発量演算部、9,12……表示部、
10……給水回数計測部、11……缶水濃縮度計
測部。
Figure 1A is a block diagram showing the configuration of a small boiler system to which the configuration of the present invention can be attached.
Figure B is an AA sectional view of the boiler 1 in Figure 1A, Figures 2 to 4 relate to embodiments of the present invention, and Figure 2 shows the configuration of the water level detection section and water supply control section. 3 is a waveform diagram of the main parts in the configuration of FIG. 2, FIG. 4 is a block diagram showing the configuration of the water supply period measurement section and the canned water concentration calculation section, and FIG.
The figure is a block diagram showing the configuration of an embodiment of the second invention related to this invention. 1...Boiler, 2...Water level detection section, 3...Water supply control section, 4...Water supply pump, 7...Water supply period measurement section, 8...Evaporation amount calculation section, 9, 12...Display section,
10...Water supply frequency measuring unit, 11...Canned water concentration measuring unit.
Claims (1)
する連通管と、連通管の水位が下限水位であるこ
とを検出して下限水位信号を出力する下限水位セ
ンサと、連通管の水位が上限水位であることを検
出して上限水位信号を出力する上限水位センサと
から成る水位検出手段と、下限水位信号に応答し
て水管に管水を供給する給水ポンプを始動させ、
上限水位信号に応答して給水ポンプを停止させる
断続制御の給水制御手段とを備えたボイラ系にお
いて、給水ポンプが始動してから停止するまでの
期間を計測して、その計測結果を給水期間信号と
して出力する給水期間計測手段と、給水期間信号
に基づいて缶水濃縮度を計測するための演算を実
行し、その演算結果を缶水濃縮度信号として出力
する缶水濃縮度演算手段とを付設して成り、上記
缶水濃縮度演算手段は給水期間から缶水濃縮のな
い状態における基準給水期間を減算する演算を実
行することを特徴とするボイラ系における缶水濃
縮度計測装置。 2 水管の上下端部を連通し、缶水の一部を抽出
する連通管と、連通管の水位が下限水位であるこ
とを検出して下限水位信号を出力する下限水位セ
ンサと、連通管の水位が上限水位であることを検
出して上限水位信号を出力する上限水位センサと
から成る水位検出手段と、下限水位信号に応答し
て水管中に缶水を供給する給水ポンプを始動さ
せ、上限水位信号に応答して給水ポンプを停止さ
せる断続制御の給水制御手段とを備えたボイラ系
において、特定期間中の給水ポンプの始動回数若
しくは停止回数を計数して、その計数結果を給水
回数信号として出力する給水回数計測手段と、給
水回数信号に基づいて缶水濃縮度を計測するため
の演算を実行し、その演算結果を缶水濃縮度信号
として出力する缶水濃縮度演算手段とを付設して
成り、上記缶水濃縮度演算手段は缶水濃縮のない
状態における基準給水回数から給水回数を減算す
る演算を実行することを特徴とするボイラ系にお
ける缶水濃縮度計測装置。[Claims] 1. A communication pipe that connects the upper and lower ends of the water pipe to extract a portion of the canned water, and a lower limit water level that outputs a lower limit water level signal when detecting that the water level of the communicating pipe is at the lower limit water level. Water level detection means consisting of a sensor, an upper limit water level sensor that detects that the water level of the communication pipe is at the upper limit water level and outputs an upper limit water level signal, and a water supply pump that supplies pipe water to the water pipe in response to the lower limit water level signal. start the
In a boiler system equipped with an intermittent control water supply control means that stops the water supply pump in response to an upper limit water level signal, the period from when the water supply pump starts until it stops is measured, and the measurement result is used as a water supply period signal. and canned water concentration calculation means that executes calculations for measuring the canned water concentration based on the water supply period signal and outputs the calculation results as a canned water concentration signal. A device for measuring can water concentration in a boiler system, characterized in that the can water concentration calculating means executes a calculation for subtracting a reference water supply period in a state where there is no concentration of can water from the water supply period. 2. A communication pipe that connects the upper and lower ends of the water pipe and extracts a portion of the canned water; a lower limit water level sensor that detects that the water level of the communication pipe is at the lower limit water level and outputs a lower limit water level signal; Water level detection means includes an upper limit water level sensor that detects that the water level is at the upper limit water level and outputs an upper limit water level signal; and a water supply pump that supplies canned water into the water pipe in response to the lower limit water level signal is started, and In a boiler system equipped with an intermittent control water supply control means that stops the water supply pump in response to a water level signal, the number of times the water supply pump starts or stops during a specific period is counted, and the counting result is used as a water supply frequency signal. A water supply frequency measuring means for outputting the water supply frequency and a can water concentration calculation means for executing a calculation for measuring the concentration of canned water based on the water supply frequency signal and outputting the calculation result as a can water concentration signal are attached. A device for measuring can water concentration in a boiler system, characterized in that the can water concentration calculating means executes a calculation of subtracting the number of times of water supply from the reference number of times of water supply in a state where there is no concentration of can water.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11683181A JPS5818004A (en) | 1981-07-24 | 1981-07-24 | Measuring device for degree of concentration of boiler water in boiler system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11683181A JPS5818004A (en) | 1981-07-24 | 1981-07-24 | Measuring device for degree of concentration of boiler water in boiler system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5818004A JPS5818004A (en) | 1983-02-02 |
| JPH0210323B2 true JPH0210323B2 (en) | 1990-03-07 |
Family
ID=14696699
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11683181A Granted JPS5818004A (en) | 1981-07-24 | 1981-07-24 | Measuring device for degree of concentration of boiler water in boiler system |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5818004A (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4382010B2 (en) | 2005-06-23 | 2009-12-09 | 本田技研工業株式会社 | Engine valve gear |
-
1981
- 1981-07-24 JP JP11683181A patent/JPS5818004A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5818004A (en) | 1983-02-02 |
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