JPS5824197B2 - Fun Iki Kitaino Jiyouka Souchi - Google Patents
Fun Iki Kitaino Jiyouka SouchiInfo
- Publication number
- JPS5824197B2 JPS5824197B2 JP50100302A JP10030275A JPS5824197B2 JP S5824197 B2 JPS5824197 B2 JP S5824197B2 JP 50100302 A JP50100302 A JP 50100302A JP 10030275 A JP10030275 A JP 10030275A JP S5824197 B2 JPS5824197 B2 JP S5824197B2
- Authority
- JP
- Japan
- Prior art keywords
- control
- damper
- intake
- blower
- rotation speed
- 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
Links
Landscapes
- Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)
- Flow Control (AREA)
- Control Of Electric Motors In General (AREA)
- Control Of Ac Motors In General (AREA)
- Prevention Of Fouling (AREA)
- Treating Waste Gases (AREA)
Description
【発明の詳細な説明】
本発明は含塵ガスや含塵空気あるいは燃焼排ガスや衛生
上好ましくない有害気体を含む空気などの雰囲気気体を
浄化する装置に係るもので、その目的は浄化における所
要動力を低減するにある。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an apparatus for purifying atmospheric gas such as dust-containing gas, dust-containing air, combustion exhaust gas, and air containing noxious gases that are undesirable for hygiene. The goal is to reduce
さて一般に各種産業では生産工程において、さまざまな
含塵ガスや燃焼排ガスなど浄化を必要とする排出物が発
生する。In general, various industries generate various types of exhaust gases such as dust-containing gases and combustion exhaust gases that require purification during production processes.
そこで排出物および排出物を含む空気を浄化するため排
出物の種別に適応した、さまざまな浄化装置たとえば乾
式あるいは湿式の集塵装置や各種洗滌液、中和剤等を用
いて処理する化学反応装置およびそれらを組合せた装置
が用いられている。Therefore, in order to purify the emissions and the air containing the emissions, various purification devices adapted to the type of emissions are used, such as dry or wet dust collectors, chemical reaction equipment that uses various cleaning solutions, neutralizing agents, etc. and devices that combine them are used.
本発明において浄化する装置とは前述の意味において用
いるものである。In the present invention, the term "purifying device" is used in the above-mentioned sense.
而して前述の雰囲気気体を吸引し浄化装置に送給するた
めのブロワ−の所要動力は前述の雰囲気気体が量的に極
めて多いために著しく多大であり、コスト高の一因とな
るのみならず前記所要動力を得るためのエネルギーたと
えば電力を生産するために、また莫大な化石燃料を必要
とし、そのためにまた燃焼排ガスが増大すると云う問題
点がある。However, the power required for the blower to suck in the above-mentioned atmospheric gas and send it to the purification device is extremely large because the above-mentioned atmospheric gas is extremely large in quantity, and this only contributes to high costs. First, there is a problem in that an enormous amount of fossil fuel is required to produce energy, such as electric power, to obtain the required power, which also increases combustion exhaust gas.
そこで浄化の目的を達することに変りはないが、前記所
要動力が著しく少なくてすむ手段を研究した結果、吸気
量制御におけるダンパー制御とブロワ−の回転数制御つ
まり駆動電動機回転数制御との組合せ制御のほか、前述
の発生個所ごとの処理を要する雰囲気気体量が工程順に
変化することから、あらかじめ吸気量を予測演算し、そ
の結果を用いて前記回転数制御を行なうことを要点とす
る手段を開発したものであって、以下図面に従ってさら
に詳細に説明する。Therefore, although the purpose of purification is still achieved, as a result of researching a means that requires significantly less power, we found a combination of damper control in intake air amount control and blower rotation speed control, that is, drive motor rotation speed control. In addition to the above, since the amount of atmospheric gas that needs to be treated at each point of occurrence changes in the order of the process, we have developed a method that focuses on calculating the amount of intake air in advance and controlling the rotation speed using the results. This will be explained in more detail below with reference to the drawings.
さて実例として転炉設備をとった場合、その生産工程は
第1図に示すように装入1、吹錬2、測温試料採取3、
出鋼4、排滓5のような順に進行し、その工程順に従っ
て発塵個所や発塵個所ごとの発生量が異なり、排ガスに
ついてもその点は同様である。Now, if we take converter equipment as an actual example, the production process is as shown in Figure 1: charging 1, blowing 2, temperature measurement sample collection 3,
The process progresses in the order of tapping 4 and waste slag 5, and the dust generation locations and the amount of generation at each dust generation location differ according to the order of the steps, and the same applies to the exhaust gas.
さて従来は、前記転炉設備について、発生個所ごとに第
2図に示すようにたとえば吸気口6a〜6cs制御ダン
パー7a〜7cを有する吸気枝管8a〜8cを設け、さ
らに前記吸気枝管8a〜8cを本管ダンパー9を有する
吸気本管10に接続し、駆動電動機11によって駆動さ
れるフ七ワー12を介して雰囲気気体を浄化装置13に
送給し、処理するよう設備されており、工程順に操作者
が前記制御ダンパー7a〜7cのうち任意数を開閉する
と同時に本管ダンパー9の開度を調節して吸気量を制御
していた。Conventionally, in the converter equipment, as shown in FIG. 2, intake branch pipes 8a to 8c having intake ports 6a to 6c and control dampers 7a to 7c, for example, are provided for each occurrence location, and furthermore, the intake branch pipes 8a to 8c are provided. 8c is connected to an intake main pipe 10 having a main damper 9, and is equipped to supply atmospheric gas to a purification device 13 for treatment via a blower 12 driven by a drive motor 11. The operator sequentially opens and closes an arbitrary number of the control dampers 7a to 7c, and at the same time adjusts the opening degree of the main damper 9 to control the intake air amount.
ところで吸気量調節において制御ダンパーを操作する手
段では、吸気量とブロワ−の所要動力はほぼ比例関係に
あるとみてよい。By the way, in the means of operating a control damper in adjusting the amount of intake air, it can be considered that the amount of intake air and the required power of the blower are approximately proportional to each other.
つまり最高吸気量のときの所要動力を100%とすると
、吸気量を40係に絞った場合所要動力は40%になる
。In other words, if the required power at the maximum intake air amount is 100%, when the intake air amount is reduced to 40%, the required power becomes 40%.
ところがブロワ−の駆動電動機の回転数を下げて吸気量
の制御を行った場合、前述の吸気量を40係にするのに
必要な所要動力は8.5〜17係で済む。However, when the intake air amount is controlled by lowering the rotational speed of the blower drive motor, the required power required to increase the above-mentioned intake air amount to 40 units is only 8.5 to 17 units.
つまり著しい動力の節減が可能になる。前記所要動力が
8.5〜17係と幅があるのは、駆動電動機の種別と回
転数制御機構の相違によって所要動力に差が生ずるため
である。In other words, significant power savings can be achieved. The reason why the required power ranges from 8.5 to 17 is that the required power varies depending on the type of drive motor and the rotation speed control mechanism.
さて前述の吸気量と所要動力の相違を第1表に示す。Now, Table 1 shows the difference between the above-mentioned intake air amount and required power.
つぎに本発明における回転数制御について詳述する。Next, rotation speed control in the present invention will be explained in detail.
さて第3図において、発生個所R1,R2゜R3がそれ
ぞれ受銑設備、炉前作業床、排滓設備であった場合、工
程に従って雰囲気気体発生量が異なり、それぞれについ
てもまた作業進行にともなって発生量が増減する。Now, in Fig. 3, if the generation locations R1, R2゜R3 are the pig iron receiving equipment, the furnace front work floor, and the slag equipment, the amount of atmospheric gas generated differs depending on the process, and the amount of atmospheric gas generated for each of them also changes as the work progresses. The amount generated increases or decreases.
受銑鍋設備R1を例にとると、受銑開始前、受銑初期、
受銑中期、受銑後期、受銑終了期において雰囲気気体発
生量が異なるため、作業進行に関係なく最大能力で吸気
していたのでは、前述のように所要動力の損失が太きい
。Taking pig iron receiving pot equipment R1 as an example, before the start of pig iron receiving, at the beginning of pig iron receiving,
Since the amount of atmospheric gas generated differs in the middle, late, and final stages of pigtail receiving, if air was taken in at maximum capacity regardless of the work progress, the loss in required power would be large as described above.
そこで作業進行につれて操業者が制御ダンパー7aの開
度を調節する手段が従来は採用されていたが、本発明者
等は前記作業進行に伴って必要な吸気量については工程
毎の一定のパターンがあり定型化しうろことに気づいた
。Therefore, conventionally, a means has been adopted in which the operator adjusts the opening degree of the control damper 7a as the work progresses, but the present inventors have discovered that there is a fixed pattern for each process regarding the amount of intake air required as the work progresses. I realized that it was starting to become a stereotype.
そこで作業進行開始信号、これは防塵カバー作動あるい
は混銑車傾動等の作動指令もしくは操作者の指令等とし
て得られるが、これを入力信号として、制御装置16か
ら一定のパターンに従った開度調節指令をダンパー制御
器14aに与え、ダンパー制御器14aは該指令に基い
て制御ダンパー78を作動するように構成した。Therefore, a work progress start signal, which is obtained as an operation command for dustproof cover operation or tilting of the pig iron mixer, or an operator's command, is used as an input signal to issue an opening adjustment command from the control device 16 according to a certain pattern. is given to the damper controller 14a, and the damper controller 14a is configured to operate the control damper 78 based on the command.
次に制御ダンパー7aの開度をたとえば指示シンクロな
どの開度検出装置15aによって検出した信号を演算装
置17に入力せしめる。Next, a signal that detects the opening degree of the control damper 7a by an opening detection device 15a such as an instruction synchronizer is inputted to the arithmetic unit 17.
発生個所R2,R3についても同様に、作業進行に従っ
て制御ダンパー7b 、7cを作動せしめ、該ダンパー
開度の開度検出装置15b、15cによる検出信号を、
演算装置17に入力せしめる。Similarly, for the occurrence locations R2 and R3, the control dampers 7b and 7c are operated as the work progresses, and the detection signals of the damper openings by the opening detection devices 15b and 15c are detected.
The information is input to the arithmetic unit 17.
ここで制御ダンパー7a 、7b 、7cの開度に対応
してフ宅ワーの所要吸気量を知り、該ダンパー開度をパ
ラメータとして駆動電動機の回転数を算出し、駆動電動
機11の回転数制御指令を電動機制御装置18に与える
。Here, the required intake air amount of the blower is determined in accordance with the opening degrees of the control dampers 7a, 7b, and 7c, the rotation speed of the drive motor is calculated using the damper opening degrees as a parameter, and a rotation speed control command is given to the drive motor 11. is given to the motor control device 18.
以上の通り発生個所R1゜R2,R3ほか図示していな
い他の発生個所についても全く同様にして所要吸気量を
求め、駆動電動機11はそれらの合計吸気量に対応して
制御される。As described above, the required intake air amount is determined in exactly the same manner for the occurrence locations R1, R2, R3 and other occurrence locations (not shown), and the drive motor 11 is controlled in accordance with the total intake air amount.
而して発生個所R1に対応する吸気枝管8aの制御ダン
パー73の開度のパターン(以下単に制御パターンと云
う)と発生個所R2,R3に対応する制御ダンパー7b
、7cの制御パターンは当然のことながら異なっており
、経時的にも開度状態は異なることが多い。The pattern of the opening degree of the control damper 73 of the intake branch pipe 8a corresponding to the occurrence location R1 (hereinafter simply referred to as the control pattern) and the control damper 7b corresponding to the occurrence locations R2 and R3.
, 7c are naturally different, and the opening state often changes over time.
従ってブロワ−12の吸気量制御はいいかえると駆動電
動機11の回転数制御は演算機能および設備の応答性に
応じてこまかく制御するほど、所要動力は少なくてすむ
。Therefore, the more finely the control of the intake air amount of the blower 12 or the rotational speed control of the drive motor 11 is performed in accordance with the arithmetic function and the responsiveness of the equipment, the less power is required.
また所要吸気量から該電動機回転数を求めることは、あ
らかじめ算定しておくことができるので、演算装置17
に前もって対照値を記憶させておき、それを利用せしめ
ても良い。In addition, since the motor rotation speed can be calculated in advance from the required intake air amount, the arithmetic unit 17
It is also possible to store a control value in advance and use it.
さて、このような制御でも所要動力を大幅に低減するこ
とができるが、さらに効率の向上を探究した結果、前記
開度検出装置15aおよび15b。Now, even with such control, the required power can be significantly reduced, but as a result of searching for further improvement in efficiency, the opening degree detection devices 15a and 15b.
15cからの入力(図では15a〜15cからの信号は
入力端子01〜C3を経て演算装置17に入力される)
を利用する手段は時間的遅れがあるために、変化の早い
パターンではやや損であることが判った。Input from 15c (in the figure, signals from 15a to 15c are input to the arithmetic unit 17 via input terminals 01 to C3)
It turns out that the method using ``is a bit of a loss when it comes to rapidly changing patterns because of the time delay.
そこで、前記制御装置16から出力端子T1.T3を経
てダンパー制御器14a〜14C(本発明ではダンパー
制御器14a〜14cは制御装置に包摂して用いる)に
発信される開度調節指令信号(以下開度信号と言う)を
同時に演算装置17に入力せしめ、該信号を基蛇前述の
如くして所要の電動機回転数を求め、制御し、前記開度
検出装置15a〜15cからの開度信号は制御ダンパー
7a〜7cの開度確認用のフィードバック信号として利
用する手段を開発し、所要動力をさらに低減することに
成功した。Therefore, the control device 16 outputs the output terminal T1. At the same time, an opening adjustment command signal (hereinafter referred to as an opening signal) transmitted to the damper controllers 14a to 14C (in the present invention, the damper controllers 14a to 14c are used as a control device) via T3 is sent to the arithmetic device 17. The required motor rotational speed is determined and controlled as described above, and the opening signals from the opening detection devices 15a to 15c are used to confirm the opening of the control dampers 7a to 7c. We developed a means to use it as a feedback signal and succeeded in further reducing the required power.
前記電動機11の制御についても回転数検出器19を用
いて、フィードバック制御を行う。Feedback control is also performed for controlling the electric motor 11 using the rotation speed detector 19.
而して本発明者等は前記駆動電動機11に巻線形誘導電
動機を用い、二次抵抗を調節することによって回転数制
御を行ったが、これに限定することなく、プロセスに応
じた機種と制御手段を選定すべきである。Therefore, the present inventors used a wound induction motor as the drive motor 11, and controlled the rotation speed by adjusting the secondary resistance. The means should be selected.
さて本発明における前記回転数の設定は次のようにして
行なう。Now, in the present invention, the rotation speed is set as follows.
ブロワ−の圧力をP1吸気量(風量)をQ、回転数をN
とすると、
N=f(P、Q) ・・・・・・(1
)の関係がある。The blower pressure is P1, the intake air volume (air volume) is Q, and the rotation speed is N.
Then, N=f(P,Q) ・・・・・・(1
).
また吸気枝管8a〜8c、吸気本管10などの管路の圧
損をPp1浄化装置13が集塵機であった場合の圧損を
Pcとしてこれらの総圧損PL=PI)+PCは風量Q
及びダンパー開度と関係しており、これらの関数である
。In addition, the pressure loss in the pipes such as the intake branch pipes 8a to 8c and the intake main pipe 10 is Pp1, and the pressure loss when the purifier 13 is a dust collector is Pc, and the total pressure loss PL = PI) + PC is the air volume Q
and the damper opening degree, and is a function of these.
即ち、前記発生個所R1〜R3の作業状態換言すると特
定時間t1での制御ダンパー7a〜7cの開度状態を総
称して状態S1とすると、PL=fS1(Q)であり、
特定時間t2での状態S2はPL二f S2 (Q)と
なり、同様にして状態SiではPL=fsi(Q)とな
る。In other words, if the opening states of the control dampers 7a to 7c at the specific time t1 are collectively referred to as state S1, then PL=fS1(Q),
The state S2 at the specific time t2 becomes PL2f S2 (Q), and similarly, PL=fsi(Q) in the state Si.
そこで状態Siにおける吸気枝管8a〜8c(以下多数
の枝管があり最終枝管を8にとする)での所要風量をQ
l (s i )・C2(Si)、 C3(si)・・
・・・・Qk(si)とすると総風量は
Ql (si) +Q2 (s i) +Q3 (s
i)・・・・・+Qk(s i ) =ΣQk (s
i ) ””(2)として求められ、そこでブ
ロワ−の所要圧力P(si)は
P(si)−fsi(ΣQk (s i ) )
・”・(3)であるから、ブロワ−の回転数Nは
として算出でき、従って駆動電動機11の回転数も設定
できる。Therefore, the required air volume in the intake branch pipes 8a to 8c (hereinafter there are many branch pipes and the final branch pipe is 8) in state Si is Q.
l (s i )・C2(Si), C3(si)...
...If Qk (si), the total air volume is Ql (si) +Q2 (s i) +Q3 (s
i)...+Qk(s i ) =ΣQk(s
i ) "" (2), where the required pressure of the blower P(si) is P(si) - fsi(ΣQk (s i ))
. . . (3) Therefore, the rotation speed N of the blower can be calculated as follows, and therefore the rotation speed of the drive motor 11 can also be set.
而して前記制御ダンパー7a〜7c(場合によっては7
kまでを含むことは前述と同様である)の開度状態は制
御装置16の開度調節指令信号からも求められるので、
前述の状態Siとはその意味をも有するものと理解せら
るべきである。The control dampers 7a to 7c (or 7 in some cases)
The opening state (including up to k is the same as above) can also be obtained from the opening adjustment command signal of the control device 16, so
It should be understood that the above-mentioned state Si also has that meaning.
次に前述の説明において制御装置16と演算装置17を
別個の装置として説明したが、これを同一ユニットに組
込んで単一の演算制御装置としてもよく、また演算装置
17を機能的に分割し、回転数設定器、回転数設定値と
検出値を比較し偏差を零にする指令信号を発信する回転
数制御回路などとして用いることも自由であり、これら
はすべて本発明の自由な設計範囲に属するものである。Next, in the above description, the control device 16 and the arithmetic device 17 were explained as separate devices, but they may be combined into the same unit to form a single arithmetic control device, or the arithmetic device 17 may be functionally divided. It can also be freely used as a rotation speed setting device, a rotation speed control circuit that compares the rotation speed setting value and the detected value and sends a command signal to make the deviation zero, and these are all within the free design scope of the present invention. It belongs.
また本管ダンパー9は本発明にとって必須のものではな
いが、設備故障その他の用途に用いて差しつかえない。Although the main damper 9 is not essential to the present invention, it may be used for equipment failure or other purposes.
第4゛図は転炉換気集塵システムの1具体例を示す。Figure 4 shows one specific example of a converter ventilation dust collection system.
21,22はA、B2つの転炉であり、各転炉にはそれ
ぞれ3本の吸気枝管が配設さへA1−A3、B1〜B3
は各枝管に設けられた制御ダンパーである。21 and 22 are two converters A and B, and each converter has three intake branch pipes, A1-A3, B1-B3.
is a control damper installed in each branch pipe.
第5図a、bはこれらA、B2つの転炉の作業シーケン
スと各作業状態における制御ダンパーA1〜B3の開閉
状態、および吸気本管10における風量パターンを示す
。5A and 5B show the working sequence of these two converters A and B, the opening/closing states of the control dampers A1 to B3 in each working state, and the air volume pattern in the main intake pipe 10.
第5図に示すように第4図の系では風量は各作業状態に
応じて75〜100係の範囲で変動し、そして各風量の
継続時間は次表の通りである。As shown in FIG. 5, in the system shown in FIG. 4, the air volume fluctuates within a range of 75 to 100 degrees depending on each work state, and the duration of each air volume is as shown in the following table.
即ち風量75係での運転時間は大きな割合を占め、従っ
て低風量運転時の電力消費量を低減することは大きな意
味を持つ。That is, the operating time at an air volume of 75 occupies a large proportion, and therefore it is of great significance to reduce the power consumption during low air volume operation.
第6図は風量Qと消費電力りとの関係を正規化して示す
グラフである。FIG. 6 is a graph showing a normalized relationship between air volume Q and power consumption.
直線C1はダンパー制御の場合であって、風量と消費電
力とけはゾ比例関係にある。The straight line C1 is for damper control, and there is a proportional relationship between the air volume and the power consumption.
C2〜C4は速度制御を行なった場合で02はブロワ−
駆動誘導電動機の2次抵抗制御、C3はセルビウス制御
、C4は流体接手制御による場合で、これらははゾ2乗
曲線をなす。C2 to C4 are when speed control is performed, and 02 is when the blower is used.
The secondary resistance control of the drive induction motor, C3 is Cerbius control, and C4 is fluid joint control, these form a zo-squared curve.
従って速度制御を行なうと、低風量時の消費電力節減が
顕著である。Therefore, if speed control is performed, power consumption can be significantly reduced when the air volume is low.
ブロワ−の軸動力L1は吸引気体の比重量をr1圧力を
P1風量をQl ブロワ−の効率をηとしてL1= r
PQ177 ・−・(5)の関係
にある。The shaft power L1 of the blower is defined by the specific weight of the suction gas as r1, the pressure as P1, the air volume as Ql, and the efficiency of the blower as η, L1= r
PQ177 --- There is a relationship as shown in (5).
制御ダンパーを開閉した場合のηの変化は種々の要因に
よって変化し、数式では表現しにくいが実積からLl
y Qの関係は第6図の直線C1の如くなる(第6図で
はLlをLとしている)。The change in η when the control damper is opened and closed depends on various factors, and it is difficult to express it mathematically, but from the actual result Ll
The relationship between y and Q is as shown by the straight line C1 in FIG. 6 (Ll is set as L in FIG. 6).
但しこの関係はQ>4o%で成立する。次に回転数制御
の場合は、軸動力りは回転数Nの3乗に比例し、100
係回転数(同期速度) N100のときのブロワ−所要
動力をL100%スリップをSとすると次の関係が成立
する。However, this relationship holds true when Q>4o%. Next, in the case of rotation speed control, the shaft power is proportional to the cube of the rotation speed N, and is 100
If the required power for the blower is L when the coefficient rotation speed (synchronous speed) is N100, and S is the 100% slip, the following relationship holds true.
2次効率η2は1−8であるから2次入力をLaとすれ
ば
La=L/η2 =L/ (1−8)−Lloo (1
−8)2速度制御を2次抵抗制御により行なう場合はL
a−Lが2次抵抗損となる。Since the secondary efficiency η2 is 1-8, if the secondary input is La, then La=L/η2 =L/ (1-8)-Lloo (1
-8) When performing two-speed control using secondary resistance control, L
a-L is the secondary resistance loss.
電動機の消費電力りは1次効率をη1として
即ちり、Nは2乗の関係にあり、第6図の曲線C2とな
る。The power consumption of the electric motor is determined by setting the first-order efficiency as η1, and N has a square relationship, resulting in a curve C2 in FIG. 6.
セルビウスの場合はこれに変換電力が加わるが、やはり
2乗特性を持つ。In the case of Servius, converted power is added to this, but it still has a square characteristic.
風量制御に回転数制御を行なうことは例えば家庭用扇風
機に見られるところである。For example, controlling the rotation speed to control the air volume can be seen in household electric fans.
が、ダンパーを設けた大型給排気設備ではブロワ−の回
転数を制御することは行なっておらず、風量制御は全て
ダンパーの開度制御に依っている。However, in large air supply and exhaust equipment equipped with a damper, the number of rotations of the blower is not controlled, and air volume control is entirely dependent on the opening degree control of the damper.
しかしながらこれでは上記で詳述したように省エネルギ
の点で不充分である。However, as detailed above, this is insufficient in terms of energy saving.
この点本発明のようにダンパー制御と共に回転数制御を
行なうと上述の大きな電力節減が可能となり、しかも要
浄化雰囲気気体の各発生箇所に所要の吸気を行なうこと
ができる。In this regard, if the rotational speed is controlled together with the damper control as in the present invention, the above-mentioned large power saving can be achieved, and the required amount of air can be taken into each location where the atmospheric gas to be purified is generated.
更に、本発明ではブ爾ワーに必要量のみ吸気するように
回転数制御するから、ブロワ−回転数は一定のま5全ダ
ンパーを閉じたときに発生する吸気管負圧の増大による
損傷事故などは発生せず、それを回避する特別な制御を
行なう必要がない利点を有する。Furthermore, in the present invention, the rotation speed is controlled so that only the necessary amount of air is taken into the blower, so the blower rotation speed remains constant.5 Accidents such as damage due to an increase in negative pressure in the intake pipe that occurs when all dampers are closed can be avoided. does not occur, and has the advantage that there is no need to perform special control to avoid it.
以上詳細に説明したように本発明の装置は浄化の目的を
充分満足したうえで、所要動力を大幅に低減することが
でき、転炉工場の集塵に用いた実施例では周知装置に比
して消費電力量で25〜30係の節電が達成できた。As explained in detail above, the device of the present invention satisfies the purpose of purification and can significantly reduce the required power, and in the example used for dust collection in a converter factory, compared to known devices. We were able to achieve a power saving of 25 to 30 units in terms of power consumption.
第1図は転炉設備での工程順を示すブロック図、第2図
は周知の浄化装置の概略説明図、第3図は本発明にがか
る一実施例装置の概略説明図、第4図は転炉換気集塵シ
ステムの具体例を示す説明図、第5図は操業状態に対す
る風量パターン等を示す説明図、第6図は風量と消費電
力との関係を示すグラフである。
6a〜6c・・・・・・吸気口、7a〜7c・・・・・
・制御ダンパー、8a〜8c・・・・・・吸気枝管、9
・・・・・・本管ダンパー、10・・・・・・吸気本管
、11・・・・・・駆動電動機、12・・・・・・ブ冶
ワー、13・・・・・・浄化装置、14a〜14c・・
・・・・ダンパー制御器、15a〜15c・・・・・・
開度検出装置、16・・・・・・制御装置、17・・・
・・・演算装置、18・・・・・・電動機制御装置、1
9・・・・・・回転数検出器。Fig. 1 is a block diagram showing the process order in converter equipment, Fig. 2 is a schematic explanatory diagram of a well-known purification device, Fig. 3 is a schematic explanatory diagram of an embodiment of the device according to the present invention, and Fig. 4 is FIG. 5 is an explanatory diagram showing a specific example of a converter ventilation dust collection system, FIG. 5 is an explanatory diagram showing air volume patterns etc. with respect to operating conditions, and FIG. 6 is a graph showing the relationship between air volume and power consumption. 6a-6c...Intake port, 7a-7c...
・Control damper, 8a to 8c...Intake branch pipe, 9
... Main pipe damper, 10 ... Intake main pipe, 11 ... Drive motor, 12 ... Blower, 13 ... Purification Devices, 14a to 14c...
...damper controller, 15a to 15c...
Opening degree detection device, 16... Control device, 17...
... Arithmetic device, 18 ... Motor control device, 1
9...Rotation speed detector.
Claims (1)
脚ダンパーを有する吸気枝管を配設し、ブロワ−を備え
て吸引気体を浄化装置へ導く吸気本管へ前記の各枝管を
連結し、 該ブロワ−を駆動する電動機にはその回転数を制御する
電動機制御装置を設け、 前記の各制御ダンパーには、当該吸気枝管が属する前記
発生箇所の工程進行に対応させて予め設定したダンパー
制御パターンに従ってダンパー開閉制御を行なう装置を
設け、 更に、各制御ダンパーの開度信号を入力されて所要総吸
気量の吸引に必要な前記電動機の回転数を求め、それを
前記電動機制御装置へ回転数指令信号として入力する演
算制御装置を設けたことを特徴とする雰囲気気体の浄化
装置。[Scope of Claims] 1. Intake branch pipes each having a crawler damper are arranged at locations where atmospheric gases that require purification are frequently generated, and a blower is provided to direct the suction gas to the purification device to the main intake pipe. The branch pipes are connected, and the electric motor that drives the blower is provided with a motor control device that controls its rotation speed, and each of the control dampers is configured to correspond to the process progress of the generation point to which the intake branch pipe belongs. A device is provided to control damper opening/closing according to a damper control pattern set in advance, and further, the opening signal of each control damper is inputted to determine the rotational speed of the electric motor required to suck the required total intake amount, and the 1. An atmospheric gas purification device comprising an arithmetic and control device that inputs a rotational speed command signal to a motor control device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP50100302A JPS5824197B2 (en) | 1975-08-19 | 1975-08-19 | Fun Iki Kitaino Jiyouka Souchi |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP50100302A JPS5824197B2 (en) | 1975-08-19 | 1975-08-19 | Fun Iki Kitaino Jiyouka Souchi |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5223565A JPS5223565A (en) | 1977-02-22 |
| JPS5824197B2 true JPS5824197B2 (en) | 1983-05-19 |
Family
ID=14270362
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP50100302A Expired JPS5824197B2 (en) | 1975-08-19 | 1975-08-19 | Fun Iki Kitaino Jiyouka Souchi |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5824197B2 (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2014035172A (en) * | 2012-08-10 | 2014-02-24 | Amano Corp | Airflow volume control system and exhaust gas process system |
Families Citing this family (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS58159884A (en) * | 1982-03-15 | 1983-09-22 | 株式会社神戸製鋼所 | Method of controlling collection of dust in raw-material yard of shaft furnace |
| JPS5952315A (en) * | 1982-08-16 | 1984-03-26 | Kawasaki Steel Corp | Flaw rate control method |
| JPS6115081A (en) * | 1984-06-29 | 1986-01-23 | 日新製鋼株式会社 | Method of controlling flow rate of exhaust gas in concentrated dust collection having plurality of electric furnace |
Family Cites Families (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS5343123B2 (en) * | 1972-12-20 | 1978-11-17 | ||
| JPS5610364B2 (en) * | 1973-01-09 | 1981-03-07 |
-
1975
- 1975-08-19 JP JP50100302A patent/JPS5824197B2/en not_active Expired
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2014035172A (en) * | 2012-08-10 | 2014-02-24 | Amano Corp | Airflow volume control system and exhaust gas process system |
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5223565A (en) | 1977-02-22 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| JPS5824197B2 (en) | Fun Iki Kitaino Jiyouka Souchi | |
| CN209166127U (en) | Coke oven flue gas back distribution system | |
| CN210886172U (en) | Ferronickel production facility | |
| CN212523669U (en) | Cement grinding system flue gas denitration treatment device | |
| JP4759872B2 (en) | Blast temperature control method for hot stove | |
| CN201539877U (en) | Rotary air preheater rotor variable speed operation system | |
| CN221403937U (en) | Novel self-adaptive full-automatic smoke exhaust device | |
| CN205481567U (en) | A economizer system that is used for clean laboratory to keep constant voltage | |
| CN223882779U (en) | Energy-saving control system of flue gas dust removal fan | |
| CN201916232U (en) | Special frequency converter for chain coal-fired boiler blower | |
| CN120578047B (en) | A cascade control method for smoke concentration emission values of coal-fired units | |
| JP2680352B2 (en) | Furnace draft control method | |
| SU1590673A1 (en) | Method and apparatus for controlling compressor capacity | |
| CN211579901U (en) | Novel full-automatic variable-frequency speed control device for motor of dust removal fan | |
| CN2237826Y (en) | Controllable waste heat low-temp temper furnace | |
| JP2628123B2 (en) | Furnace pressure control method | |
| CN202171257U (en) | Running system for changing speed of GGH (gas-gas heater) rotor | |
| JP2001317877A (en) | Sintered exhaust gas treatment apparatus and operation method thereof | |
| SU901741A1 (en) | Apparatus for controlling burning process in drum boiler fire box | |
| CN107289459A (en) | A kind of Industrial Boiler Automatic Optimal control system and control method | |
| CN119287099A (en) | A dust removal system and automatic control method for converter steelmaking | |
| JPH0550326B2 (en) | ||
| JPS57207521A (en) | Operating method for dust collection system for central dust collection of dusty waste gases generated in plural places | |
| JPS643131B2 (en) | ||
| CN121274685A (en) | Novel seamless switching type glass fiber tank furnace waste gas treatment device and treatment method thereof |