JPH07167405A - Enriched blow controlling method for boiler - Google Patents

Enriched blow controlling method for boiler

Info

Publication number
JPH07167405A
JPH07167405A JP29266793A JP29266793A JPH07167405A JP H07167405 A JPH07167405 A JP H07167405A JP 29266793 A JP29266793 A JP 29266793A JP 29266793 A JP29266793 A JP 29266793A JP H07167405 A JPH07167405 A JP H07167405A
Authority
JP
Japan
Prior art keywords
water
boiler
electric conductivity
concentration
blow
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.)
Granted
Application number
JP29266793A
Other languages
Japanese (ja)
Other versions
JP3669638B2 (en
Inventor
Takashi Morimatsu
隆史 森松
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Miura Co Ltd
Original Assignee
Miura Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Miura Co Ltd filed Critical Miura Co Ltd
Priority to JP29266793A priority Critical patent/JP3669638B2/en
Publication of JPH07167405A publication Critical patent/JPH07167405A/en
Application granted granted Critical
Publication of JP3669638B2 publication Critical patent/JP3669638B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Abstract

PURPOSE:To provide a method for controlling to correct an enriched blow rate corresponding to a change of an electric conductivity of water to be supplied in a boiler for automatically controlling enrichment based on a preset enriched blow rate. CONSTITUTION:A boiler 1 switches an enriched blow valve 7 based on a preset enriched blow rate, and automatically controls an enrichment rate of a boiler water. The boiler 1 further presets an operating time until an electric conductivity of the water becomes substantially constant, calculates a suitable enriched blow rate by using following formula (1) if an electric conductivity of the water after the operating time is elapsed and a predetermined electric conductivity of the water is different, corrects the enriched blow rate to the value, and controls it. In the formula, E: electric conductivity of the boiler water, E=E0/alpha...(1) E0: electric conductivity of supplied water, and alpha: blow rate.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】この発明は、ボイラの濃縮ブロー
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 method for controlling a concentrated blow of a boiler.

【0002】[0002]

【従来の技術】一般に、ボイラにおいては、ボイラ内の
缶水は、長時間に亘り高温で加熱され続けると、発生し
て利用される蒸気量に比例して濃縮が進行し、注入され
ている薬液濃度等の残留密度も大となり、結果的には発
生蒸気の高乾き度の維持が困難となる。
2. Description of the Related Art Generally, in a boiler, if the boiler water in the boiler is continuously heated at a high temperature for a long time, it is concentrated and injected in proportion to the amount of steam generated and used. The residual density such as chemical concentration also becomes large, and as a result, it becomes difficult to maintain the high dryness of the generated steam.

【0003】この状態を回避するために、従来、ボイラ
のセパレータの降水管に、常時は弁を自閉し、開弁され
ると缶水をブロー配管より外方に排出する濃縮ブロー弁
をストレーナを介して設置し、濃縮ブロー弁と降水管の
下流内に設置した電気伝導率測定センサとを結ぶ回路に
制御部を設け、電気伝導率測定センサにより降水管の下
流内での缶水の濃縮度に比例する電気伝導率の変化を検
出し、電気伝導率が規定値を超えたとき、電気伝導率測
定センサから発する制御信号によって制御部を制御し、
濃縮ブロー弁を開弁させて高濃縮缶水を外部に排出せし
め、同時に高濃縮缶水の排出に伴い、給水装置を介して
缶内に自動的に補給される新規の缶水により希釈され
て、缶水全体の濃縮度が低下して缶水の電気伝導率が規
定値以下に低下すると、前記ブロー作動信号が消えて濃
縮ブロー弁が自閉する構成の自動ブロー装置をボイラに
取り付けて、発生蒸気の高乾き度の維持を図っている。
In order to avoid this situation, conventionally, a strainer has a strainer equipped with a concentration blow valve that normally closes the valve in the downcomer pipe of the separator of the boiler and discharges the can water from the blow pipe to the outside when the valve is opened. Installed through the concentration blow valve and the control unit is installed in the circuit connecting the concentration blow valve and the electrical conductivity measurement sensor installed in the downstream of the downcomer, and the electrical conductivity measurement sensor is used to concentrate the can water in the downstream of the downcomer. The change of the electric conductivity proportional to the degree is detected, and when the electric conductivity exceeds the specified value, the control unit is controlled by the control signal generated from the electric conductivity measuring sensor,
The concentrated blow valve is opened to discharge the highly concentrated canned water to the outside, and at the same time, as the highly concentrated canned water is discharged, it is diluted with new canned water that is automatically replenished into the can via the water supply device. When the concentration of the whole canned water decreases and the electric conductivity of the canned water falls below a specified value, the blow operation signal disappears and the concentrated blow valve is automatically closed by attaching it to a boiler. We are trying to maintain high dryness of the generated steam.

【0004】しかしながら、前記従来のボイラに付設す
る自動濃縮ブロー装置では、給水される水の電気伝導率
がその温度によって大きく変化するので、ボイラの使用
状況やその圧力等によっては基準値をはずれたところで
作動しているケースがある。また、ボイラのメンテナン
スをするときには、給水量に対するブロー量の比率を実
測して現在の電気伝導率(センサ)の設定が正しいか否
かを確認しているため、電気伝導率(センサ)の設定に
際しては、何回にもわたって設定をし直して適正値を求
めているのが現状である。
However, in the conventional automatic concentrating blower attached to the boiler, the electric conductivity of the water to be supplied greatly changes depending on its temperature, so that it deviates from the reference value depending on the usage condition of the boiler and its pressure. By the way, there are cases that are working. In addition, when performing maintenance on the boiler, the ratio of the blow rate to the water supply rate is measured to check whether the current electrical conductivity (sensor) setting is correct. At that time, the current situation is that the proper value is obtained by re-setting many times.

【0005】[0005]

【発明が解決しようとする課題】この発明は、前述の問
題点に鑑み、予め設定した濃縮ブロー率に基づいて、缶
水の濃縮度を自動制御する制御システムにおいて、給水
する水の電気伝導度の変化に対応し、予め設定した濃縮
ブロー率を修正して缶水の濃縮度を自動制御するボイラ
の濃縮ブロー制御方法を提供することを目的とするもの
である。
SUMMARY OF THE INVENTION In view of the above-mentioned problems, the present invention provides a control system for automatically controlling the concentration of canned water based on a preset concentration blow rate. It is an object of the present invention to provide a boiler concentration blow control method for automatically controlling the concentration of canned water by correcting a preset concentration blow rate in response to changes in the above.

【0006】[0006]

【課題を解決するための手段】この発明は、前述の問題
点に鑑み、予め設定した濃縮ブロー率に基づいて、濃縮
ブロー弁を開閉し、缶水の濃縮度を自動制御するボイラ
において、前記缶水の電気伝導率がほぼ一定になるまで
の運転時間を予め設定し、その運転時間が経過した時点
での缶水の電気伝導率と、所定の缶水の電気伝導率が異
なる場合は、下記式を用いて適正な濃縮ブロー率を演
算し、その値に濃縮ブロー率を修正することを特徴と
し、または、予め設定した濃縮ブロー率に基づいて、濃
縮ブロー弁を開閉し、缶水の濃縮度を自動制御するボイ
ラにおいて、前記ボイラへ給水する水の電気伝導率を測
定し、測定された給水の電気伝導率と所定の給水の電気
伝導率が異なる場合は、下記式を用いて適正な濃縮ブ
ロー率を演算し、その値に濃縮ブロー率を修正すること
を特徴としている。 E:缶水の電気伝導率 E=E0 /α…… E0 :給水の電気伝導率 α:ブロー率
In view of the above-mentioned problems, the present invention provides a boiler in which the concentration blow valve is opened / closed and the concentration of canned water is automatically controlled based on a preset concentration blow rate. When the operating time until the electric conductivity of the canned water becomes almost constant is preset, and the electric conductivity of the canned water at the time when the operating time has passed and the electric conductivity of the predetermined canned water are different, It is characterized by calculating an appropriate concentration blow rate using the following formula and correcting the concentration blow rate to that value, or based on a preset concentration blow rate, opening and closing the concentration blow valve to In a boiler that automatically controls the enrichment, measure the electrical conductivity of the water to be supplied to the boiler, and if the measured electrical conductivity of the feed water and the electrical conductivity of the prescribed feed water are different, use the following formula Calculates the specific concentration blow rate and the value It is characterized by modifying the blowdown rate. E: electric conductivity of canned water E = E 0 / α ... E 0 : electric conductivity of feed water α: blow ratio

【0007】[0007]

【実施例】以下、この発明の請求項1の具体的実施例を
図面に基づいて詳細に説明する。図面に示す実施例は、
一例として多管式貫流ボイラにこの発明に係る濃縮ブロ
ー制御方法を適用した場合の説明である。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS A concrete embodiment of claim 1 of the present invention will be described below in detail with reference to the drawings. The embodiment shown in the drawings is
As an example, it is a case where the concentration blow control method according to the present invention is applied to a multi-tube once-through boiler.

【0008】図1に示すように、ボイラ1の下部には、
逆止弁、瀘過器、薬注装置等を備えた給水装置(図示省
略)の給水管2が連通接続されている。給水管2の他端
は、水道、井戸等の水源に連通接続され、給水ポンプP
の作動により、水源の水が瀘過され薬液注入された薬注
缶水となってボイラ1の缶内に供給される。また、ボイ
ラ1の一側には、図1に図示のごとく、発生した蒸気の
気水分離を行うセパレータ3が蒸気連絡管4および降水
管5を介してボイラ1の缶内上下部に連通して接続され
ており、また降水管5の下部には、電気伝導率測定セン
サ6及び電磁開閉式の濃縮ブロー弁7を備えたブロー配
管8が連通接続されている。
As shown in FIG. 1, at the bottom of the boiler 1,
A water supply pipe 2 of a water supply device (not shown) including a check valve, a filter, a chemical injection device, etc. is connected and connected. The other end of the water supply pipe 2 is connected to a water source such as a water supply or a well, and is connected to a water supply pump P.
The water of the water source is filtered and the water is supplied into the can of the boiler 1 as the water for the medicinal can in which the medicinal solution is injected. Further, as shown in FIG. 1, a separator 3 for separating steam of the generated steam into one side of the boiler 1 communicates with the upper and lower parts of the boiler 1 via a steam communication pipe 4 and a downfall pipe 5, as shown in FIG. A blow pipe 8 having an electric conductivity measuring sensor 6 and an electromagnetic open / close type concentration blow valve 7 is connected to the lower part of the downcomer pipe 5 so as to communicate therewith.

【0009】この種のボイラ1の稼動、停止は、通常、
負荷の状況に基づき、ボイラ1の缶内圧を検出する圧力
検出器9の信号に基づいて、燃焼制御器(図示省略)に
より制御する。すなわち、缶内圧が予め設定しておいた
圧力値以上になれば燃焼を停止させ、それ以下になれば
燃焼を開始する。また、ボイラ1のバーナ16には、ボ
イラ1内での燃焼を検出する燃焼検出センサ10が設定
されていて、ボイラ1内の燃焼状況と燃焼時間が計測さ
れるようになっている。すなわち、これらの圧力検出器
9および燃焼検出センサ10は、ボイラ1の運転状況を
制御する検出手段を構成している。
The operation and shutdown of this type of boiler 1 are usually
Based on a load condition, a combustion controller (not shown) controls the pressure based on a signal from a pressure detector 9 that detects the internal pressure of the boiler 1. That is, the combustion is stopped when the internal pressure of the can exceeds a preset pressure value, and the combustion is started when the internal pressure falls below the preset pressure value. A combustion detection sensor 10 that detects combustion in the boiler 1 is set in the burner 16 of the boiler 1, and the combustion state and combustion time in the boiler 1 are measured. That is, the pressure detector 9 and the combustion detection sensor 10 form a detection unit that controls the operating condition of the boiler 1.

【0010】濃縮ブロー弁7の開閉を制御する制御器1
1は、たとえばマイコン内蔵の演算機能を有し、圧力検
出器9、燃焼検出センサ10等の検出手段からの検出信
号と、予め設定しているブロー率より、濃縮ブロー弁7
の開閉タイミングを演算し、濃縮ブロー弁7の開閉を間
歇的に行うタイムを決定し、濃縮ブロー弁7にその信号
を出力するようになっている。したがって、この制御器
11は、ボイラ1の検出手段を構成する圧力検出器9、
燃焼検出センサ10と通信線12、13を介してそれぞ
れ接続され、かつ濃縮ブロー弁7と通信線14を介し
て、電気伝導率測定センサ6と通信線15を介してそれ
ぞれ接続されている。
A controller 1 for controlling the opening and closing of the concentration blow valve 7.
1 has a calculation function with a built-in microcomputer, for example, and based on detection signals from detection means such as the pressure detector 9 and the combustion detection sensor 10 and a preset blow rate, the concentration blow valve 7
Is calculated, the time for intermittently opening and closing the concentration blow valve 7 is determined, and the signal is output to the concentration blow valve 7. Therefore, this controller 11 is a pressure detector 9 that constitutes the detecting means of the boiler 1.
It is connected to the combustion detection sensor 10 via communication lines 12 and 13, respectively, and is connected to the concentration blow valve 7 to communication line 14 and the electrical conductivity measuring sensor 6 to communication line 15 respectively.

【0011】一般的に、ブロー率(ブロー量と給水量と
の比率)の設定は、事前に、供給する原水(井戸水、水
道水)の水質(pHほか)を分析し、必要な清缶剤の投
入量等から勘案して決定するが、概ね10%から15%
程度となる。なお、給水量は、給水時間より算出するこ
とも可能であるが、給水ポンプPの能力変化やボイラ1
の圧力変動等により単位時間当たりの給水量が変動する
ことがあるので、給水量を蒸発量×燃焼時間により算出
し、ブロー率を、ブロー量と蒸発量×燃焼時間との比率
とした。すなわち、ボイラ1の圧力検出器9および燃焼
検出センサ10よりの検出信号でブロー量を算出する方
がより正確である。これは、ボイラ1の蒸発量は、定格
で決まっているからである。
Generally, the blow rate (ratio between the blow rate and the water supply rate) is set by analyzing the water quality (pH, etc.) of the raw water (well water, tap water) to be supplied in advance, and the necessary cleaning agent. It is decided by taking into consideration the input amount, etc., but generally 10% to 15%
It will be about. The water supply amount can be calculated from the water supply time, but the change in the capacity of the water supply pump P and the boiler 1
Since the water supply amount per unit time may fluctuate due to the pressure fluctuation, etc., the water supply amount was calculated by the evaporation amount x the combustion time, and the blow rate was defined as the ratio of the blow amount and the evaporation amount x the combustion time. That is, it is more accurate to calculate the blow amount with detection signals from the pressure detector 9 and the combustion detection sensor 10 of the boiler 1. This is because the evaporation amount of the boiler 1 is determined by the rating.

【0012】前記構成の濃縮度を自動制御する制御シス
テムによれば、ボイラ1が稼動中は、缶内圧力、バーナ
の燃焼状態、燃焼時間等は、圧力検出器9、燃焼検出セ
ンサ10、および電気伝導率測定センサ6等の検出手段
が常時検出しており、その検出信号を制御器11に出力
する。出力信号を受けた制御器11は、予め設定してあ
るブロー率とその検出信号とにより濃縮ブロー弁7の開
閉タイミングを計算し、濃縮ブロー弁7の開閉を間歇的
に行うタイムを決定して、濃縮ブロー弁7を自動的に開
閉するようにしている。
According to the control system for automatically controlling the enrichment having the above-mentioned configuration, the pressure detector 9, the combustion detection sensor 10, and the combustion detection sensor 10 can detect the internal pressure of the can, the combustion state of the burner, the combustion time, etc. while the boiler 1 is in operation. The detection means such as the electric conductivity measuring sensor 6 always detects and outputs the detection signal to the controller 11. The controller 11 receiving the output signal calculates the opening / closing timing of the concentration blow valve 7 based on the preset blow rate and its detection signal, and determines the time for intermittently opening / closing the concentration blow valve 7. The concentration blow valve 7 is automatically opened and closed.

【0013】この発明の濃縮ブロー制御方法は、上記構
成の缶水の濃縮度を自動制御するシステムにおいて、前
記ボイラ1の運転開始時より缶水の電気伝導率がほぼ一
定になるまでの時間を予め設定し、この運転時間経過後
の缶水の電気伝導率を測定し、この実測電気伝導率より
修正ブロー率を演算する。ここで、缶水の濃縮度は溶媒
(水)中の溶質(全蒸発残留物)の量であるが、水中の
全蒸発残留物と電気伝導率との間には、ほぼ次の関係が
成り立つ。 全蒸発残留物〔mg/l〕=0.7×電気伝導率〔μs
/cm〕 したがって、全蒸発残留物の代わりに電気伝導率にて缶
水の濃縮度を計算することができる。例えば、缶水の電
気伝導率をE〔μs/cm〕、燃焼時間をT〔h〕、実
際蒸発量をG〔kg/h〕、保有水量をL〔l〕、給水
電気伝導率をE0 〔μs/cm〕、濃縮ブロー量をB
〔kg/h〕、濃縮ブロー率をαとすると次式が成り立
つ。 E={E0 ×L+E0 ×(G+B)×T−E×B×T}
/L E×{1+(B×T)/L}=E0 ×{1+(G+B)
/L×T} 濃縮倍数はE/E0 であるから、 E/E0 ={1+(G+B)/L×T)}/{1+(B
×T)/L} α=B/(G+B)であるから E/E0 ={1+(B×T)/(α×L)}/{1+
(B×T)/L} Tが大きくなると E=E0 /α……
In the system for automatically controlling the concentration of canned water having the above-described structure, the method for controlling concentration blow of the present invention provides a time period from the start of the operation of the boiler 1 until the electric conductivity of the canned water becomes substantially constant. The electric conductivity of the can water after the preset operation time is measured, and the corrected blow rate is calculated from the measured electric conductivity. Here, the concentration of canned water is the amount of solute (total evaporation residue) in the solvent (water), but the following relationship is established between the total evaporation residue in water and electrical conductivity. . Total evaporation residue [mg / l] = 0.7 × electrical conductivity [μs
/ Cm] Therefore, the concentration of the can water can be calculated by the electric conductivity instead of the total evaporation residue. For example, the electric conductivity of can water is E [μs / cm], the burning time is T [h], the actual evaporation amount is G [kg / h], the amount of retained water is L [l], and the electric conductivity of feed water is E 0. [Μs / cm], concentrated blow amount is B
[Kg / h], and the concentration blow rate is α, the following equation holds. E = {E 0 × L + E 0 × (G + B) × T−E × B × T}
/ L E × {1+ (B × T) / L} = E 0 × {1+ (G + B)
/ L × T} Since the enrichment factor is E / E 0 , E / E 0 = {1+ (G + B) / L × T)} / {1+ (B
× T) / L} because α = B / (G + B) E / E 0 = {1+ (B × T) / (α × L)} / {1+
(B × T) / L} When T increases, E = E 0 / α ...

【0014】前記電気伝導率測定センサ6は、稼動中の
缶水の電気伝導率を常時検出し、所定運転時間経過後の
缶水の電気伝導率E2 と、予め設定した所定の缶水の電
気伝導率E1 とを比較し、両者が異なっている場合は、
前記制御器11の演算部で前記式に、検出した缶水の
電気伝導率E2 と予め設定していた濃縮ブロー率α1
代入して給水の電気伝導率E3 を演算し(E3 =E2 ×
α1 )、つぎに、この給水の電気伝導率E3 と前記所定
の缶水の電気伝導率E1 とを前記式に代入して適正な
濃縮ブロー率α2 を演算し(α2 =E3 /E1 =E2
1 ×α1 )、この値に前記濃縮ブロー率を修正して缶
水の濃縮度を自動制御する。したがって、給水の電気伝
導率の変化にも自動的に対応し、常に適正な濃縮ブロー
率でボイラの缶水濃度を制御することができる。
The electric conductivity measuring sensor 6 constantly detects the electric conductivity of the can water in operation, and calculates the electric conductivity E 2 of the can water after the elapse of a predetermined operation time and a predetermined predetermined can water. Compare with the electric conductivity E 1, and if they are different,
The electric conductivity E 3 of the feed water is calculated by substituting the electric conductivity E 2 of the detected can water and the preset concentration blow rate α 1 in the above equation in the calculation unit of the controller 11 (E 3 = E 2 ×
α 1 ), and then the electric conductivity E 3 of this feed water and the electric conductivity E 1 of the predetermined canned water are substituted into the above formula to calculate an appropriate concentration blow rate α 22 = E 3 / E 1 = E 2 /
E 1 × α 1 ), and the concentration blow rate is corrected to this value to automatically control the concentration of the can water. Therefore, it is possible to automatically respond to changes in the electrical conductivity of the feed water and always control the boiler water concentration at an appropriate concentration blow rate.

【0015】つぎに、この発明の請求項2の実施例を図
面に基づいて説明する。尚、請求項1の実施例と同一部
材には同一番号を付し、重複する説明は省略する。図2
に示す実施例は、ボイラ1の給水管2の途中に、給水す
る水の電気伝導率を測定するセンサ17を挿入し、この
センサ17を通信線18を介して制御器11に接続した
ものである。尚、この実施例では、缶水の電気伝導率を
測定するセンサは不要となる。センサ17は、給水する
水の電気伝導率を常時検出し、予め設定した所定の給水
の電気伝導率E4 と検出した給水の電気伝導率E5 とを
比較し、両者が異なっている場合は、前記制御器11の
演算部で前記式に、検出した給水の電気伝導率E5
予め設定してある所定の缶水の電気伝導率E1 を代入し
て適正な濃縮ブロー率α2 を演算し、(α2 =E5 /E
1 )この値に前記濃縮ブロー率を修正して缶水の濃縮度
を自動制御する。したがって、給水の電気伝導率の変化
に自動的に対応し、常に適正な濃縮ブロー率でボイラの
缶水濃度を制御することができる。
Next, a second embodiment of the present invention will be described with reference to the drawings. The same members as those in the embodiment of claim 1 are designated by the same reference numerals, and the duplicated description will be omitted. Figure 2
In the embodiment shown in, a sensor 17 for measuring the electrical conductivity of water to be supplied is inserted in the water supply pipe 2 of the boiler 1, and the sensor 17 is connected to the controller 11 via a communication line 18. is there. In this embodiment, the sensor for measuring the electric conductivity of the can water is unnecessary. Sensor 17 detects the electrical conductivity of the water to the water supply at all times, compared with the water supply of the electrical conductivity E 5 in which predetermined detected water supply of electric conductivity E 4 set in advance, if it is different In the calculation unit of the controller 11, the detected electrical conductivity E 5 of the feed water and the preset electrical conductivity E 1 of the can water are substituted into the equation to obtain an appropriate concentration blow rate α 2 . And calculate (α 2 = E 5 / E
1 ) Correct the concentration blow rate to this value to automatically control the concentration of can water. Therefore, it is possible to automatically respond to changes in the electrical conductivity of the feed water and always control the boiler water concentration at an appropriate concentration blow rate.

【0016】[0016]

【発明の効果】以上説明したように、この発明は、予め
設定した濃縮ブロー率に基づいて缶水の濃縮度を自動制
御するシステムにおいて、所定の缶水の電気伝導率と所
定運転時間経過後に検出した缶水の電気伝導率が異なっ
ているとき、あるいは、予め設定した所定の給水の電気
伝導率と検出した給水の電気伝導率が異なっているとき
は、制御器で関係数値を演算し適正な濃縮ブロー率を算
出して自動制御するようにしたので、給水する水の電気
伝導率の変化に対応して濃縮ブロー率を修正し、適正な
濃縮ブローをすることができる。
As described above, according to the present invention, in a system for automatically controlling the concentration of canned water based on a preset concentration blow rate, the electric conductivity of a predetermined canned water and a predetermined operating time have elapsed. If the electric conductivity of the detected canned water is different, or if the electric conductivity of the predetermined feed water that is set in advance is different from the electric conductivity of the detected feed water, calculate the relevant numerical value with the controller and make it appropriate. Since the effective concentration blow rate is calculated and automatically controlled, the appropriate concentration blow rate can be corrected by correcting the concentration blow rate in response to the change in the electric conductivity of the water to be supplied.

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

【図1】 この発明の請求項1の濃縮ブロー制御方法を
実施した多管式貫流ボイラの各機器の配置を示す説明図
である。
FIG. 1 is an explanatory diagram showing an arrangement of respective devices of a multi-tube type once-through boiler that implements the method for controlling concentration blow according to claim 1 of the present invention.

【図2】 この発明の請求項2の濃縮ブロー制御方法を
実施した多管式貫流ボイラの各機器の配置を示す説明図
である。
FIG. 2 is an explanatory diagram showing an arrangement of respective devices of a multi-tube type once-through boiler that implements the concentration blow control method according to claim 2 of the present invention.

【符号の説明】[Explanation of symbols]

1 ボイラ 7 濃縮ブロー弁 1 Boiler 7 Concentration blow valve

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 予め設定した濃縮ブロー率に基づいて、
濃縮ブロー弁7を開閉し、缶水の濃縮度を自動制御する
ボイラ1において、前記缶水の電気伝導率がほぼ一定に
なるまでの運転時間を予め設定し、その運転時間経過後
の缶水の電気伝導率と、所定の缶水の電気伝導率が異な
る場合は、下記式を用いて適正な濃縮ブロー率を演算
し、その値に濃縮ブロー率を修正することを特徴とする
ボイラの濃縮ブロー制御方法。 E:缶水の電気伝導率 E=E0 /α…… E0 :給水の電気伝導率 α:ブロー率
1. Based on a preset concentration blow rate,
In the boiler 1 in which the concentration blow valve 7 is opened and closed to automatically control the concentration of the canned water, the operating time until the electric conductivity of the canned water becomes almost constant is preset, and the canned water after the operating time elapses. If the electric conductivity of the boiler is different from the electric conductivity of the predetermined canned water, the appropriate concentration blow rate is calculated using the following formula, and the concentration blow rate is corrected to that value. Blow control method. E: electric conductivity of canned water E = E 0 / α ... E 0 : electric conductivity of feed water α: blow ratio
【請求項2】 予め設定した濃縮ブロー率に基づいて、
濃縮ブロー弁7を開閉し、缶水の濃縮度を自動制御する
ボイラ1において、前記ボイラ1へ給水する水の電気伝
導率を測定し、測定された給水の電気伝導率と所定の給
水の電気伝導率が異なる場合は、下記式を用いて適正
な濃縮ブロー率を演算し、その値に濃縮ブロー率を修正
することを特徴とするボイラの濃縮ブロー制御方法。 E:缶水の電気伝導率 E=E0 /α…… E0 :給水の電気伝導率 α:ブロー率
2. Based on a preset concentration blow rate,
In the boiler 1 in which the concentration blow valve 7 is opened and closed to automatically control the concentration of canned water, the electrical conductivity of the water to be supplied to the boiler 1 is measured, and the measured electrical conductivity of the supplied water and the electricity of the predetermined supply water are measured. When the conductivity is different, an appropriate concentration blow rate is calculated by using the following formula, and the concentration blow rate is corrected to the value, a boiler concentration blow control method. E: electric conductivity of canned water E = E 0 / α ... E 0 : electric conductivity of feed water α: blow ratio
JP29266793A 1993-10-27 1993-10-27 Concentration blow control method for boiler Expired - Lifetime JP3669638B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP29266793A JP3669638B2 (en) 1993-10-27 1993-10-27 Concentration blow control method for boiler

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP29266793A JP3669638B2 (en) 1993-10-27 1993-10-27 Concentration blow control method for boiler

Related Child Applications (2)

Application Number Title Priority Date Filing Date
JP2000328052A Division JP3669687B2 (en) 2000-10-27 2000-10-27 Boiler concentration blow control device
JP2003204212A Division JP2004045023A (en) 2003-07-31 2003-07-31 Concentrated blow control device of boiler

Publications (2)

Publication Number Publication Date
JPH07167405A true JPH07167405A (en) 1995-07-04
JP3669638B2 JP3669638B2 (en) 2005-07-13

Family

ID=17784746

Family Applications (1)

Application Number Title Priority Date Filing Date
JP29266793A Expired - Lifetime JP3669638B2 (en) 1993-10-27 1993-10-27 Concentration blow control method for boiler

Country Status (1)

Country Link
JP (1) JP3669638B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2019163883A (en) * 2018-03-19 2019-09-26 栗田工業株式会社 Boiler water concentration magnification measuring device

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2019163883A (en) * 2018-03-19 2019-09-26 栗田工業株式会社 Boiler water concentration magnification measuring device

Also Published As

Publication number Publication date
JP3669638B2 (en) 2005-07-13

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