JP3137931B2 - Dust suppression device - Google Patents

Dust suppression device

Info

Publication number
JP3137931B2
JP3137931B2 JP09244613A JP24461397A JP3137931B2 JP 3137931 B2 JP3137931 B2 JP 3137931B2 JP 09244613 A JP09244613 A JP 09244613A JP 24461397 A JP24461397 A JP 24461397A JP 3137931 B2 JP3137931 B2 JP 3137931B2
Authority
JP
Japan
Prior art keywords
pressure
air
water
control valve
chemical
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Lifetime
Application number
JP09244613A
Other languages
Japanese (ja)
Other versions
JPH1157541A (en
Inventor
賢治 金常
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.)
Maintech Co Ltd
Original Assignee
Maintech 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 Maintech Co Ltd filed Critical Maintech Co Ltd
Priority to JP09244613A priority Critical patent/JP3137931B2/en
Publication of JPH1157541A publication Critical patent/JPH1157541A/en
Application granted granted Critical
Publication of JP3137931B2 publication Critical patent/JP3137931B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Working Measures On Existing Buildindgs (AREA)

Description

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

【0001】[0001]

【発明の属する技術分野】本発明は、固形物等の破壊時
に発生した粉塵に気泡を噴射することによって粉塵を抑
制することのできる粉塵抑制装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a dust suppressor capable of suppressing dust by injecting air bubbles into dust generated when a solid or the like is broken.

【0002】[0002]

【従来の技術】建設解体現場、再生骨材生産現場、リサ
イクル処理現場等においては、固形者等の破壊時に多量
の粉塵が発生するため、作業者の健康を害したり、近隣
の住民に迷惑をかけていた。かかる粉塵公害による環境
汚染を防止するため、従来、発生した粉塵に水を捲いて
粉塵を抑制する水散布方式と直接粉塵を吸い採る集塵方
式が知られているが、水散布方式は、大量の水を必要と
することから大きな消費となるのに加え、粉塵が混入し
た汚水の後処理や汚泥の飛散防止処理等が必要であり、
また水の使用できない場合もある。一方、集塵方式は、
設備が膨大となり、保守作業も大変で設備の変更も容易
にはできないという問題がある。
2. Description of the Related Art At construction demolition sites, recycled aggregate production sites, recycling sites, and the like, a large amount of dust is generated when solids are destroyed, which impairs workers' health and inconveniences nearby residents. I was hanging on. In order to prevent environmental pollution due to such dust pollution, conventionally, there are known a water spraying method in which generated dust is sprayed with water to suppress dust and a dust collecting method in which dust is directly sucked and collected. In addition to requiring large amounts of water, it consumes large amounts of water, and requires post-treatment of sewage mixed with dust and treatment to prevent sludge from scattering.
In some cases, water cannot be used. On the other hand, the dust collection method
There is a problem that the equipment becomes enormous, maintenance work is difficult, and the equipment cannot be easily changed.

【0003】そこで、本出願人は、水に代え気泡を使用
し、すなわち、粉塵に向けて気泡を噴射させ、あるい
は、粉塵発生源に気泡を噴射させ、噴射を、気泡の層で
覆うことにより、気泡の液膜に付着させ、空中に飛散し
ようとする粉塵を捕捉・抑制させる方法及びその装置に
ついて発明した(特願平8−353014号)。これに
よれば、水使用量の1/10に低減下することができ、
費用を大幅に抑えることができ、また装置の構造も簡単
である。
[0003] Therefore, the present applicant uses air bubbles instead of water, that is, air bubbles are sprayed toward dust, or air bubbles are sprayed at a dust generation source, and the spray is covered with a bubble layer. Invented was a method and an apparatus for trapping and suppressing dust that would adhere to the liquid film of bubbles and fly into the air (Japanese Patent Application No. 8-353014). According to this, water consumption can be reduced to 1/10,
The cost can be greatly reduced and the structure of the device is simple.

【0004】[0004]

【発明が解決しようとする課題】気泡の発生は、使用さ
れる薬品と水と空気の混合比および各圧力の調整で決定
されるが、薬品,水,空気の流量および圧力の変化に対
応させ常に安定させて気泡を発生させることは困難であ
る。したがって、気泡の噴射または散布用の複数のノズ
ルが取り付けられたマニホールドが1組しかないか、あ
るいは2組以上のマニホールドがあっても常に使用する
ときには全組使用する場合には薬品,水,空気の流量お
よび圧力の変化がなく問題はないが、通常、後述する図
1に示すように、二次クラッシャーで粉砕される時と三
次クラッシャーで粉砕される時にそれぞれ1組づつのマ
ニホールドが使用されるので、例えば二次クラッシャー
による粉砕の度合いが大きいと2組のマニホールドを同
時に使用し2個所で気泡を噴射させていても、後段の三
次クラッシャー側のマニホールドが不要となり噴射を止
める場合がある。
The generation of air bubbles is determined by adjusting the mixing ratio of the chemical used, water and air, and the respective pressures. It is difficult to always stabilize and generate bubbles. Therefore, there is only one set of manifolds to which a plurality of nozzles for spraying or spraying air bubbles are attached, or when two or more sets of manifolds are used at all times, if all sets are used, chemicals, water, and air are used. There is no problem because there is no change in the flow rate and pressure, but usually, as shown in FIG. 1 described below, one set of manifolds is used when pulverized by the secondary crusher and when crushed by the tertiary crusher Therefore, for example, if the degree of pulverization by the secondary crusher is large, even if two sets of manifolds are used at the same time and bubbles are injected at two locations, the subsequent tertiary crusher side manifold becomes unnecessary and the injection may be stopped.

【0005】この場合、2組のマニホールドのノズルに
送られる気泡を製造するために使用される薬品,水,空
気の源は一つであるので、1組のマニホールド(三次ク
ラッシャー側)の噴射が止められると薬品及び水の供給
が他の1組の方(二次クラッシャー側)に集中して圧力
がかかるが、その分に比例して空気による圧力は他の1
組側にかかることはないので、他の1組側の気泡の噴射
が安定しないという問題がある。これによれば、気泡の
大きさが不均一になり粉塵を十分に抑制することができ
ない場合がある。ここでは、2組のマニホールドを使用
しての例を示して説明したが、それ以上の複数のマニホ
ールドになっても同様のことがいえる。なお、2組以上
のマニホールドがあり、それぞれのマニホールが独立し
た薬品,水,空気の源を有している場合も問題はない
が、このような場合は費用的な面から通常考えられな
い。
In this case, since one source of chemical, water, and air is used to produce air bubbles sent to the nozzles of the two sets of manifolds, the injection of one set of manifolds (tertiary crusher side) is performed. When stopped, the supply of chemicals and water concentrates on the other set (secondary crusher side), and pressure is applied.
There is no problem on the set side, and there is a problem that the injection of bubbles on the other set side is not stable. According to this, the size of the air bubbles becomes uneven, and the dust may not be sufficiently suppressed. Here, an example in which two sets of manifolds are used has been described. However, the same applies to a case where a plurality of manifolds are used. There is no problem in the case where there are two or more sets of manifolds and each manifold has an independent source of chemicals, water and air, but such a case is not usually considered from the viewpoint of cost.

【0006】そこで本発明の目的は、噴射個所が部分的
に中断されても安定的に気泡を発生させて粉塵を抑制し
うる粉塵抑制装置を提供することにある。
SUMMARY OF THE INVENTION It is an object of the present invention to provide a dust suppressing device capable of stably generating air bubbles and suppressing dust even when an injection point is partially interrupted.

【0007】[0007]

【課題を解決するための手段】上記の目的を達成するた
めに、請求項1に記載の粉塵抑制装置は、供給された界
面活性剤を含む薬液と水を同圧で混合して混合液を製造
する混合液製造装置(1);混合液と圧縮空気を混合処
理して気泡を発生させる発泡器(2);製造された混合
液を発泡器(2)に送る送液手段(3);圧縮空気を発
泡器(2)に送る送気手段(4);混合液製造装置
(1)の薬液と水が混合される位置より前に設けられた
送られる薬液の圧力を検出する薬液用圧力センサー
(5);送気手段(4)に設けられた送られる空気圧を
検出する空気用圧力センサー(6);複数の噴出用ノズ
ル(7)が取り付けられた少なくとも2組以上のマニホ
ールド(8,9);発泡器(2)と各マニホールド
(8,9)とを接続し、発生させた気泡を噴出用ノズル
(7)に送る気泡供給手段(10);混合液製造装置
(1)に設けられた薬液用調節弁(11)と水用調節弁
(12)を正/逆転駆動して開/閉する駆動手段(M
1);および、薬液用圧力センサー(5)の値(PC)
を空気用圧力センサー(6)の値(PA)と比較し、薬
液の圧力(PC)が空気の圧力(PA)よりも設定値
(K)分大きくなると、駆動手段(M1)を逆転駆動し
て薬液用調節弁(11)及び水用調節弁(12)を閉
め、逆に薬液の圧力(PC)が空気の圧力(PA)より
設定値(K)分小さくなると、駆動手段(M1)を正転
駆動して薬液用調節弁(11)及び水用調節弁(12)
を開けて、空気圧に対する薬液及び水の圧力を一定にす
る制御手段(13);を備えることを特徴とする。
According to a first aspect of the present invention, there is provided a dust suppression device, comprising mixing a supplied chemical solution containing a surfactant with water at the same pressure to form a mixed solution. A mixed liquid manufacturing apparatus (1) to be manufactured; a foaming device (2) for generating a bubble by mixing the mixed solution and compressed air; a liquid sending means (3) for sending the manufactured mixed solution to the foaming device (2); Air supply means (4) for sending compressed air to the foaming device (2); chemical liquid pressure for detecting the pressure of the chemical liquid to be sent, which is provided in the mixed liquid production apparatus (1) before the chemical liquid and water are mixed. A sensor (5); an air pressure sensor (6) provided in the air supply means (4) for detecting an air pressure to be sent; at least two or more sets of manifolds (8, 8) equipped with a plurality of ejection nozzles (7). 9); Connect the foamer (2) to each manifold (8, 9) and generate Supply means (10) for sending the generated bubbles to the jet nozzle (7); the chemical liquid control valve (11) and the water control valve (12) provided in the mixed liquid production apparatus (1) are driven forward / reversely. Open / close drive means (M
1); and the value (PC) of the chemical pressure sensor (5)
Is compared with the value (PA) of the pressure sensor for air (6), and when the pressure (PC) of the chemical solution is larger than the pressure (PA) of the air by the set value (K), the driving means (M1) is driven in reverse. The control valve for chemical solution (11) and the control valve for water (12) are closed. Conversely, when the pressure (PC) of the chemical solution becomes smaller than the pressure (PA) of air by the set value (K), the drive means (M1) is turned off. Rotate forward to control chemical liquid control valve (11) and water control valve (12)
, And a control means (13) for keeping the pressure of the chemical solution and the water relative to the air pressure constant.

【0008】また、請求項2に記載の発明は、送気手段
(4)に空気用調節弁(24)を正/逆転駆動して開/
閉する空気弁用駆動手段(M2)を更に備え、制御手段
(13)は、薬液用圧力センサー(5)の値(PC)を
空気用圧力センサー(6)の値(PA)と比較し、薬液
の圧力(PC)が空気の圧力(PA)よりも設定値
(K)分大きくなると、駆動手段(M1)を逆転駆動し
て薬液用調節弁(11)及び水用調節弁(12)を閉め
るとともに空気弁用駆動手段(M2)を正転駆動して空
気用調節弁(24)を開け、逆に、薬液の圧力(PC)
が空気の圧力(PA)より設定値(K)分小さくなる
と、駆動手段(M1)を正転駆動して薬液用調節弁(1
1)及び水用調節弁(12)を開けるとともに空気弁用
駆動手段(M2)を逆転駆動して空気用調節弁(24)
を閉めて、空気圧に対する薬液及び水の圧力を一定にす
ることを特徴とする請求項1に記載の粉塵抑制装置であ
る。
Further, according to the present invention, the air supply means (4) is opened / closed by driving the air control valve (24) forward / reversely.
The air valve driving means (M2) for closing is further provided, and the control means (13) compares the value (PC) of the chemical liquid pressure sensor (5) with the value (PA) of the air pressure sensor (6), When the pressure (PC) of the chemical liquid becomes larger than the pressure (PA) of the air by the set value (K), the driving means (M1) is driven in reverse to open the chemical liquid control valve (11) and the water control valve (12). Close and drive the air valve drive means (M2) forward to open the air control valve (24), and conversely, the pressure of the chemical (PC)
Is smaller than the air pressure (PA) by the set value (K), the driving means (M1) is driven to rotate in the normal direction, and the chemical liquid control valve (1) is driven.
1) and the water control valve (12) is opened, and the air valve drive means (M2) is driven in reverse to drive the air control valve (24).
2. The dust suppression device according to claim 1, wherein the pressure of the chemical and the water with respect to the air pressure are kept constant by closing the air pressure.

【0009】更に、請求項3に記載の発明は、制御手段
(13)は、少なくとも2組以上のマニホールド(8,
9)のうち1組のマニホールド(9)の複数の噴出用ノ
ズル(7)から気泡の噴射が中止又は中断になったこと
を検知すると、薬液用圧力センサー(5)の値(PC)
を空気用圧力センサーの値(PA)と比較し、その結果
に基づいて空気圧に対する薬液及び水の圧力を一定にす
る制御を行うことを特徴とする請求項1又は2に記載の
粉塵抑制装置である。
Further, according to a third aspect of the present invention, the control means (13) comprises at least two or more sets of manifolds (8, 8).
When it is detected that the injection of air bubbles is stopped or interrupted from the plurality of jet nozzles (7) of one set of manifolds (9) out of 9), the value (PC) of the pressure sensor for chemical liquid (5) is detected.
3 is compared with a value (PA) of a pressure sensor for air, and control for keeping the pressure of the chemical solution and water relative to the air pressure based on the result is performed, and the dust suppression device according to claim 1 or 2, wherein is there.

【0010】また、請求項4に記載の発明は、界面活性
剤を含む薬液は、陰イオン界面活性剤に属するα−オレ
フィンスルホン酸塩(AOS)であることを特徴とする
請求項1乃至3のいずれかに記載の粉塵抑制装置であ
る。
[0010] The invention according to claim 4 is characterized in that the chemical solution containing a surfactant is an α-olefin sulfonate (AOS) belonging to an anionic surfactant. A dust suppression device according to any one of the above.

【0011】なお、上記の括弧内の記号は図面及び後述
する発明の実施の形態に記載された記号に対応するもの
である。
The symbols in parentheses above correspond to the symbols described in the drawings and the embodiments of the invention described later.

【0012】請求項1に記載の発明によれば、制御手段
は、水と同圧で発泡器に供給され混合される薬液の圧力
値を、同じ発泡器に供給される空気の圧力値と比較し、
薬液の圧力が空気の圧力よりも設定値分大きくなると、
駆動手段を逆転駆動して薬液用調節弁及び水用調節弁を
閉める。これにより、供給される薬液及び水の流量が減
り薬液用圧力センサーで検出される圧力値が減少してい
く。逆に、薬液の圧力が空気の圧力より設定値分小さく
なると、駆動手段を正転駆動して薬液用調節弁及び水用
調節弁を開ける。これにより、供給される薬液及び水の
流量が増え薬液用圧力センサーで検出される圧力値が増
加していく。このようにして、空気圧に対する薬液及び
水の圧力を一定にする制御が行われるので、噴射個所が
部分的に中断され、一時的に薬液,水,空気圧の流量及
び圧力の変動があっても自動的に修正され、安定的して
気泡をマニホールドのノズルから噴射発生させることが
できる。したがって、継続して粉塵を抑制しうる。
According to the first aspect of the invention, the control means compares the pressure value of the chemical supplied to the foaming device with the same pressure as that of water and mixed with the pressure value of the air supplied to the same foaming device. And
When the pressure of the chemical becomes larger than the air pressure by the set value,
The driving means is reversely driven to close the chemical liquid control valve and the water control valve. As a result, the flow rates of the supplied chemical liquid and water decrease, and the pressure value detected by the chemical liquid pressure sensor decreases. Conversely, when the pressure of the chemical becomes lower than the pressure of the air by the set value, the driving means is driven to rotate forward to open the chemical control valve and the water control valve. As a result, the flow rates of the supplied chemical liquid and water increase, and the pressure value detected by the chemical liquid pressure sensor increases. In this way, control is performed to keep the pressure of the chemical solution and water constant with respect to the air pressure, so that the injection point is partially interrupted, and even if there is a temporary fluctuation in the flow rate and pressure of the chemical solution, water, and air pressure, automatic control is performed. The air bubbles can be stably ejected from the nozzles of the manifold. Therefore, dust can be continuously suppressed.

【0013】また、請求項2に記載の発明によれば、制
御手段は、薬液及び水の圧力が空気圧に近づけられるの
に加え、空気用調節弁を正/逆転駆動して開/閉する空
気弁用駆動手段を利用して空気圧の方も薬液及び水の圧
力に近づけるので、空気圧に対する薬液及び水の圧力を
一定に制御する時間が短縮される。
According to the second aspect of the present invention, the control means controls the air to be opened / closed by driving the pneumatic control valve forward / reverse in addition to bringing the pressure of the chemical solution and water close to the air pressure. Since the pneumatic pressure is made closer to the pressure of the chemical and water by using the valve driving means, the time for controlling the pressure of the chemical and water with respect to the air pressure to be constant is reduced.

【0014】更に、請求項3に記載の発明によれば、請
求項1又は2の発明の作用効果に加えて、制御手段は、
少なくとも2組以上のマニホールドのうち1組のマニホ
ールドの複数の噴出用ノズルから気泡の噴射が中止又は
中断になったことを検知した時に、すなわち、薬液,
水,空気圧の流量及び圧力の変動が大きい予想される場
合に限り、空気圧に対する薬液及び水の圧力を一定に制
御することを行うものであるので、効率的である。
Further, according to the third aspect of the present invention, in addition to the functions and effects of the first or second aspect, the control means further comprises:
When it is detected that the injection of air bubbles has been stopped or interrupted from a plurality of ejection nozzles of one set of manifolds of at least two or more sets of manifolds,
Only when the fluctuation of the flow rate and the pressure of the water and the air pressure is expected to be large, the pressure of the chemical solution and the water with respect to the air pressure is controlled to be constant, so that it is efficient.

【0015】[0015]

【発明の実施の形態】本発明の実施の形態について図面
を参照して説明する。図1は、本発明の実施形態に係る
粉塵抑制装置が現場に適用された例を示す模式図、図2
は、本発明の実施形態に係る粉塵抑制装置の制御系統の
構成概要を示すブロック図、そして、図3は、各マニホ
ールドと混合液製造装置間との接続を示す構成図であ
る。
Embodiments of the present invention will be described with reference to the drawings. FIG. 1 is a schematic view showing an example in which a dust suppression device according to an embodiment of the present invention is applied to a site, and FIG.
Is a block diagram showing a configuration outline of a control system of the dust suppression device according to the embodiment of the present invention, and FIG. 3 is a configuration diagram showing connection between each manifold and the mixed liquid production device.

【0016】本発明の実施形態に係る粉塵抑制装置は、
主に供給された界面活性剤を含む薬液と水を同圧で混合
して混合液を製造する混合液製造装置1,混合液と圧縮
空気を混合処理して気泡を発生させる発泡器2,製造さ
れた混合液を発泡器2に送る送液手段としての混合液供
給管3,圧縮空気を発泡器2に送る送気手段としての空
気圧供給管4,混合液製造装置1の薬液と水が混合され
る位置より前に設けられた送られる薬液の圧力を検出す
る薬液用圧力センサー5,空気圧供給管4に設けられた
送られる空気圧を検出する空気用圧力センサー6,複数
の噴出用ノズル7が取り付けられた少なくとも2組のマ
ニホールド8,9,発泡器2と各マニホールド8,9と
を接続し、発生させた気泡を噴出用ノズル7に送る気泡
供給手段としての気泡供給管10,混合液製造装置1に
設けられた薬液用調節弁11と水用調節弁12のゲート
を正/逆転駆動して開/閉する駆動手段としてのモータ
M1,および、供給される薬液及び水の圧力を一定にす
る制御手段として機能する中央制御装置13を備えてい
る。
A dust suppression device according to an embodiment of the present invention comprises:
A mixed liquid manufacturing apparatus for mixing a liquid chemical mainly containing a surfactant and water with the same pressure to produce a mixed liquid 1, a foaming device 2 for mixing the mixed liquid and compressed air to generate air bubbles 2, and manufacturing The mixed liquid supply pipe 3 as a liquid sending means for sending the mixed liquid to the foaming device 2, the air pressure supply pipe 4 as an air sending means for sending the compressed air to the foaming device 2, and the chemical and water of the mixed liquid manufacturing apparatus 1 are mixed. A pressure sensor for chemical solution, which is provided before the position to be sent, for detecting the pressure of the chemical solution to be sent, a pressure sensor for air, provided for the air pressure supply pipe 4 for detecting the air pressure to be sent, and a plurality of ejection nozzles 7. At least two sets of the attached manifolds 8, 9; the foaming device 2 and each of the manifolds 8, 9; a bubble supply pipe 10 as a bubble supply means for sending generated bubbles to a jet nozzle 7; For chemicals provided in device 1 A motor M1 as a driving means for opening / closing the gates of the node valve 11 and the water control valve 12 by forward / reverse rotation, and a central control functioning as a control means for keeping the pressure of the supplied chemical solution and water constant. An apparatus 13 is provided.

【0017】混合液製造装置1に送られる水は、水槽又
は水源からポンプ15によって行われ、流量及び圧力が
流量計16及び水用圧力センサー17で検出されるとと
もに、水用調節弁12の開閉で流量及び圧力が調節され
る。また、薬液もタンクからフィルター18を介してポ
ンプ19によって行われ、流量及び圧力が流量計20及
び薬液用圧力センサー5で検出されるとともに、薬液用
調節弁11の開閉で流量及び圧力が調節される。薬液用
調節弁11のゲート開閉と水用調節弁12のゲート開閉
は1つのモータM1で同時に行うものであり、薬液と水
を同圧で混合するようになっているので、水用圧力セン
サー17の値PWと薬液用圧力センサー5の値PCとは
同圧になる。なお、モータを2つ用意するようにしても
よい。また、混合液製造装置1にはコンプレッサー21
で圧縮された空気がフィルター22を介して供給され、
流量及び圧力が流量計23及び空気用圧力センサー6で
検出されるとともに、モータM2の駆動による空気用調
節弁24のゲート開閉で流量及び圧力が調節される。
The water sent to the mixed liquid producing apparatus 1 is supplied from a water tank or a water source by a pump 15, and the flow rate and pressure are detected by a flow meter 16 and a water pressure sensor 17. Is used to adjust the flow rate and pressure. The chemical is also pumped from the tank via the filter 18 by the pump 19, the flow rate and the pressure are detected by the flow meter 20 and the chemical pressure sensor 5, and the flow rate and the pressure are adjusted by opening and closing the chemical control valve 11. You. The opening and closing of the gate of the chemical liquid control valve 11 and the opening and closing of the gate of the water control valve 12 are performed simultaneously by one motor M1, and the chemical and water are mixed at the same pressure. Is equal to the value PC of the chemical liquid pressure sensor 5. Note that two motors may be prepared. In addition, the mixed liquid producing apparatus 1 includes a compressor 21.
Is supplied through the filter 22,
The flow rate and the pressure are detected by the flow meter 23 and the air pressure sensor 6, and the flow rate and the pressure are adjusted by opening and closing the gate of the air control valve 24 by driving the motor M2.

【0018】また発泡器2は、混合液と圧縮空気を円筒
状のフィルターで乱流撹拌しその後整流する工程を複数
回(通常、2〜3回)繰り返すことによって気泡を発生
するようになっている。発泡器2は、2つのマニホール
ド8,9で一つを共通するようにしても(図1)、ある
いはマニホールド毎に発泡器2を設けるようにしてもよ
い(図2)。中央制御装置13は、本発明の実施形態に
係る粉塵抑制装置全体の制御を行い、その中枢を担うC
PUやROM,RAMからなる各種記憶部を有する。ま
た、パネル設定装置及びハンデー設定装置が接続され設
定値などを外部から入力できるようになっている。
The foamer 2 generates bubbles by repeating the process of turbulently agitating the mixed liquid and compressed air with a cylindrical filter and then rectifying the mixture a plurality of times (usually two to three times). I have. One of the foaming devices 2 may be shared by the two manifolds 8 and 9 (FIG. 1), or the foaming device 2 may be provided for each manifold (FIG. 2). The central control device 13 controls the entire dust suppression device according to the embodiment of the present invention, and plays a central role in the control.
It has various storage units including a PU, a ROM, and a RAM. Also, a panel setting device and a handy setting device are connected so that setting values and the like can be input from outside.

【0019】またノズル7から気泡が空中に漂う粉塵に
噴射されると粉塵は気泡層で覆れ、気泡の液膜に付着さ
せられる。すなわち、気泡が粉塵表面に水分を補給し、
表面に残留した薬液の成分が粉塵同士を吸着させあって
早期に落下させ、粉塵の飛散を防止するようになってい
る。ここで使用される界面活性剤を含む薬液とは、陰イ
オン界面活性剤に属するα−オレフィンスルホン酸塩
(AOS)で粉塵抑制剤として化審法(化学物質の審査
及び製造等の規制に関する法律)で認可された物質であ
り、液体に溶かした時、その液体の表面張力を著しく
低下させる、水と油のように、お互い混ざり合わない
2つの液体を1つにする、水滴中に界面活性剤が含ま
れるとダストが濡れて水滴との付着が容易となる、石
鹸が代表とあげられるように洗剤、乳化剤、可溶剤など
工業分野で広く使われる、などの特徴を有している。な
お、残留効果を引き伸ばすために凝沈作用のある薬液を
添加してもよい。これによれば、砕砂洗浄で発生する泥
水の凝沈にも効果がある。
When air bubbles are sprayed from the nozzle 7 onto the dust floating in the air, the dust is covered with a bubble layer and adheres to the liquid film of the bubbles. That is, the bubbles replenish moisture to the dust surface,
The components of the chemical solution remaining on the surface cause the dust to be adsorbed to each other and fall at an early stage, thereby preventing the scattering of the dust. The chemical solution containing a surfactant used here is an α-olefin sulfonate (AOS) belonging to an anionic surfactant and used as a dust suppressant as a dust suppressant (Act on the Examination of Chemical Substances and Regulation of Manufacturing, etc.) ) Is a substance approved in) that, when dissolved in a liquid, significantly lowers the surface tension of the liquid. Two liquids that do not mix with each other, such as water and oil, are combined with one another. When the agent is contained, dust is wetted to easily adhere to water droplets, and soap is widely used in industrial fields such as detergents, emulsifiers, and solvents as typical examples. In order to extend the residual effect, a chemical solution having a coagulation action may be added. According to this, it is effective also in the sedimentation of the muddy water generated by the crushed sand washing.

【0020】上記構成要素のうち、混合液製造装置1,
各種圧力センサー5,6,17,各種調節弁11,1
2,24,各種流量計16,20,23,ポンプ15,
19,フィルター18,22,中央制御装置13,モー
タM1,M2は、本実施形態においては、発泡制御装置
100として組込まれている。その他、発泡制御装置1
00の混合液及び圧縮空気が出力される側にはシャット
ダウン用の電磁弁25及び電磁弁26が設けられてい
る。また、混合液製造装置1には、各種調節弁11,1
2,24と各種流量計16,20,23にそれぞれ接続
された調節計28,29,30とポンプ15,19と中
央制御装置13との間に接続されたコントローラ31,
32を備えている。このように、各構成要素が発泡制御
装置100に組込まれ一体型になっているが、別体分割
型の構成にしてもよい。また、これらを建設機械に分割
して配置したり、あるいは一体型で搭載することも可能
である。
Among the above components, the mixed liquid production apparatus 1
Various pressure sensors 5, 6, 17, various control valves 11, 1
2, 24, various flow meters 16, 20, 23, pump 15,
In the present embodiment, the filter 19, the filters 18, 22, the central control device 13, and the motors M1, M2 are incorporated as a foam control device 100. Other, foam control device 1
A solenoid valve 25 and a solenoid valve 26 for shutting down are provided on the side where the mixed liquid of 00 and the compressed air are output. In addition, the mixed liquid production apparatus 1 includes various control valves 11, 1
2, 24, controllers 28, 29, 30 connected to the various flow meters 16, 20, 23, respectively, and the controller 31 connected between the pumps 15, 19 and the central controller 13.
32. As described above, the respective components are incorporated into the foam control device 100 and are integrated, but may be configured separately. It is also possible to divide and arrange them on the construction machine or to mount them integrally.

【0021】混合液供給管3および空気圧供給管4は、
金属鋼管又は硬質ゴム管からなっている。マニホールド
8,9に取り付けられたノズル7は噴射口の口径サイズ
を選定できるようになっている。また、各マニホールド
8,9と気泡供給管10との間には開閉弁33,34,
35,36が設けられている。
The mixed liquid supply pipe 3 and the pneumatic supply pipe 4
It consists of a metal steel tube or a hard rubber tube. The nozzles 7 attached to the manifolds 8 and 9 can select the diameter of the injection port. On-off valves 33, 34, 34 are provided between each of the manifolds 8, 9 and the bubble supply pipe 10.
35 and 36 are provided.

【0022】このような粉塵抑制装置は、例えば、図1
に示すようにして現場にて適用される。すなわち、2組
のマニホールド8,9のうち、一方のマニホールド8
は、一次クラッシャで粉砕された固形物がコンベアで運
ばれ二次クラッシャーで粉砕される入口側に配置され、
他方のマニホールド9は、その後二次クラッシャーで粉
砕された固形物が運ばれ三次クラッシャーで粉砕される
入口側に配置にされている。
Such a dust suppressing device is, for example, shown in FIG.
Applied on site as shown in That is, one of the two manifolds 8, 9 is
Is placed on the inlet side where the solid material crushed by the primary crusher is carried by the conveyor and crushed by the secondary crusher,
The other manifold 9 is arranged on the inlet side where the solids crushed by the secondary crusher are transported and then crushed by the tertiary crusher.

【0023】次に、図4に示すフローチャートを参照し
て、中央制御装置13の圧力制御処理の内容を示す。マ
ニホールド8,9の両方から泡が噴射されている場合に
は、薬品,水,空気の流量および圧力の変化がなく問題
がないが、一方のマニホールドからの泡の噴射がストッ
プすると薬品,水,空気の流量および圧力が変動して他
の可動中のマニホールドから噴射される泡の大きさが不
均一となり粉塵抑制処理が安定しないため、一方のマニ
ホールド9からの泡の噴射が中止又は中断されると(ス
テップ1:以下括弧内ではステップという語を省略す
る)、以下の処理を実行する。
Next, the contents of the pressure control processing of the central control unit 13 will be described with reference to the flowchart shown in FIG. When bubbles are ejected from both the manifolds 8 and 9, there is no problem because there is no change in the flow rate and pressure of the chemical, water, and air. However, when the injection of the foam from one of the manifolds is stopped, the chemical, water, and the like are stopped. Since the flow rate and pressure of the air fluctuate and the size of the foam injected from the other moving manifold becomes uneven and the dust suppression processing becomes unstable, the injection of the foam from one manifold 9 is stopped or interrupted. (Step 1: Hereinafter, the word “step” is omitted in parentheses), the following processing is executed.

【0024】なお、マニホールド9からの泡の噴射が中
止又は中断される場合とは例えば二次クラッシャーによ
る粉砕の度合いが大きく三次クラッシャーが不要な場合
などで、開閉弁35,36が閉鎖されることによって行
われる。ここでは、中央制御装置13は、開閉弁35,
36の開から閉の動作を検知してマニホールド9からの
泡の噴射が中止又は中断されたと判断するが、これにか
えて、例えば作業者などが別のスイッチを押すことによ
って判断するようにしてもよい。
The case where the injection of the foam from the manifold 9 is stopped or interrupted means that the on-off valves 35 and 36 are closed, for example, when the degree of pulverization by the secondary crusher is large and the tertiary crusher is unnecessary. Done by Here, the central control device 13 includes an on-off valve 35,
By detecting the operation from opening to closing of 36, it is determined that the injection of the foam from the manifold 9 has been stopped or interrupted, but instead, for example, by pressing another switch by an operator or the like, Is also good.

【0025】中央制御装置13は、マニホールド9から
の噴射が中止又は中断されたことを検知すると(1)、
フラグFを0にセットして(2)、各圧力センサー5,
6,17の値PC,PA,PWを読み取る(3)。な
お、薬液と水は同圧で混合して混合液を製造するもので
あるので薬液用圧力センサー5の値PCと水用圧力セン
サー17の値PWとは等しい。次に、中央制御装置13
は、薬液用圧力センサー5の値PCと空気用圧力センサ
ー6の値PAとを比較し、値PCから値PAを差し引い
た値の絶対値が設定値K以下であるか否かを判断する
(4)。そして、設定値Kよりも大きくなると、フラグ
Fに1をセットし(5)、値PCと値PAのうちいずれ
が大きいか判断する(6)。なお、設定値Kは上述した
パネル設定装置から入力され、例えば設定値K=0とす
れば、薬液用圧力センサー5の値PCを空気用圧力セン
サー6の値PAにするための許容誤差をなくすことにな
る。
When the central controller 13 detects that the injection from the manifold 9 is stopped or interrupted (1),
The flag F is set to 0 (2), and each pressure sensor 5,
The values PC, PA and PW of 6, 17 are read (3). Since the chemical and the water are mixed at the same pressure to produce a mixed liquid, the value PC of the chemical pressure sensor 5 and the value PW of the water pressure sensor 17 are equal. Next, the central controller 13
Compares the value PC of the chemical liquid pressure sensor 5 with the value PA of the air pressure sensor 6 and determines whether or not the absolute value of the value obtained by subtracting the value PA from the value PC is equal to or less than the set value K ( 4). When the value becomes larger than the set value K, the flag F is set to 1 (5), and it is determined which of the value PC and the value PA is larger (6). The set value K is input from the panel setting device described above. For example, if the set value K is set to 0, an allowable error for changing the value PC of the chemical pressure sensor 5 to the value PA of the air pressure sensor 6 is eliminated. Will be.

【0026】そして、値PCの方が大きいと、中央制御
装置13は、モータM1を逆転駆動させ、薬液用調節弁
11のゲート及び水用調節弁12のゲートをともに閉め
る方向に動かす(7)。これにより、供給される薬液及
び水の流量が減り薬液用圧力センサー5で検出される圧
力値PCが減少していく(水用圧力センサー17で検出
される圧力値PWも同様に減少していく)。逆に、ステ
ップ6で値PCの方が小さいと、中央制御装置13は、
モータM1を正転駆動させ、薬液用調節弁11のゲート
及び水用調節弁12のゲートをともに開く方向に動かす
(8)。これにより、供給される薬液及び水の流量が増
え薬液用圧力センサー5で検出される圧力値PCが増加
していく(水用圧力センサー17で検出される圧力値P
Wも同様に増加していく)。そして、ステップ3に戻
り、ステップ3−4−5−6−7(又は8)−3−・・
・の処理を繰り返して行う。
If the value PC is larger, the central controller 13 drives the motor M1 in the reverse direction to move both the gate of the chemical liquid control valve 11 and the gate of the water control valve 12 in a direction to close (7). . Thereby, the flow rates of the supplied chemical solution and water decrease, and the pressure value PC detected by the chemical pressure sensor 5 decreases (the pressure value PW detected by the water pressure sensor 17 also decreases similarly). ). Conversely, if the value PC is smaller in step 6, the central controller 13
The motor M1 is driven to rotate forward, and both the gate of the chemical liquid control valve 11 and the gate of the water control valve 12 are moved in the opening direction (8). As a result, the flow rates of the supplied chemical solution and water increase, and the pressure value PC detected by the chemical pressure sensor 5 increases (the pressure value P detected by the water pressure sensor 17).
W also increases similarly). Then, returning to step 3, step 3-4-5-6-7 (or 8) -3-.
・ Repeat the process.

【0027】その後、ステップ4で、薬液用圧力センサ
ー5の値PCから空気用圧力センサー6の値PAを差し
引いた値の絶対値が設定値K以下になると、中央制御装
置13は、フラグFが1にセットされているか否かを判
断し(9)、フラグFが0であればモータM1は駆動状
態にないのでリターンするが、フラグFが1にセットさ
れているとモータM1の正転あるいは逆転いずれかの駆
動を停止させ、薬液用調節弁11のゲート及び水用調節
弁12のゲートの開度をその位置でホールドさせる(1
0)。これによって、空気圧に対する薬液及び水の圧力
を一定に制御することができるので、噴射個所が部分的
に中断されても安定的に気泡を発生させて粉塵を抑制さ
せることができる。
Thereafter, in step 4, when the absolute value of the value obtained by subtracting the value PA of the air pressure sensor 6 from the value PC of the chemical pressure sensor 5 becomes equal to or smaller than the set value K, the central control unit 13 sets the flag F to It is determined whether or not the motor M1 is set to 1 (9). If the flag F is 0, the motor M1 is not in the driving state and the routine returns. The drive of any of the reverse rotations is stopped, and the opening of the gate of the chemical liquid control valve 11 and the gate of the water control valve 12 are held at that position (1).
0). As a result, the pressure of the chemical solution and the water with respect to the air pressure can be controlled to be constant, so that bubbles can be stably generated even when the injection point is partially interrupted, and dust can be suppressed.

【0028】なお、空気圧に対する薬液及び水の圧力を
一定に制御する際に、空気用調節弁24を正/逆転駆動
して開/閉するモータM2を利用して、薬液用圧力セン
サー5の値PCを空気用圧力センサー6の値PAと比較
し、薬液の圧力PCが空気の圧力PAよりも設定値K分
大きくなると、ステップ7でモータM1を逆転駆動して
薬液用調節弁11及び水用調節弁12を閉めるとともに
モータM2を正転駆動して空気用調節弁24を開け、逆
に薬液の圧力PCが空気の圧力PAより設定値K分小さ
くなると、ステップ8でモータM1を正転駆動して薬液
用調節弁11及び水用調節弁12を開けるとともにモー
タM2を逆転駆動して空気用調節弁24を閉めるように
してもよい。これによれば、薬液及び水の圧力が空気圧
に近づけられるのに加え、空気圧の方も薬液及び水の圧
力に近づけられるので、空気圧に対する薬液及び水の圧
力を一定に制御する時間が短縮される。
When controlling the pressure of the chemical and the water with respect to the air pressure to a constant value, the value of the pressure sensor 5 for the chemical is measured by using a motor M2 that opens / closes the air control valve 24 by rotating the air forward / reverse. The PC is compared with the value PA of the air pressure sensor 6, and when the pressure PC of the chemical solution is larger than the pressure PA of the air by the set value K, the motor M1 is driven in reverse in step 7 to control the control valve 11 for the chemical solution and the water. When the control valve 12 is closed and the motor M2 is driven forward to open the air control valve 24, conversely, when the pressure PC of the chemical solution is smaller than the pressure PA of the air by the set value K, the motor M1 is driven forward in step 8. Then, the control valve for chemical liquid 11 and the control valve for water 12 may be opened, and the motor M2 may be driven in reverse to close the control valve for air 24. According to this, in addition to bringing the pressure of the chemical solution and water close to the air pressure, the air pressure also approaches the pressure of the chemical solution and water, so that the time for controlling the pressure of the chemical solution and water with respect to the air pressure to be constant is reduced. .

【0029】また、本実施形態例では中央制御装置13
は、ステップ1でマニホールド9からの気泡の噴射が中
止又は中断された場合を検知してその時に限り効率的に
圧力を一定に制御するようにしたが、これに加えて、あ
るいはこれとは別に、気泡の噴射が中断されたマニホー
ルド9がその噴射を再開したことを開閉弁35,36の
閉から開の動作を検知をすることによって、ステップ2
以下の処理を行うようにしてもよい。
In this embodiment, the central control unit 13
Detects that the injection of air bubbles from the manifold 9 is stopped or interrupted in step 1 and controls the pressure to be efficiently constant only at that time. In addition to this, or in addition to this, Step 2 detects that the manifold 9 in which the injection of the bubble has been interrupted has restarted its injection by detecting the operation of the on-off valves 35 and 36 from the closing to the opening.
The following processing may be performed.

【0030】なお、複数のノズル7が取り付けられたマ
ニホールド8,9は直線状のものにかえて、図5に示す
ように、枠型のマニホールド50にしてもよい。
The manifolds 8 and 9 to which the plurality of nozzles 7 are attached may be frame-shaped manifolds 50 as shown in FIG. 5 instead of linear ones.

【0031】[0031]

【発明の効果】以上のとおり請求項1に記載の発明によ
れば、薬液の圧力値と空気の圧力値とを比較しそれに対
応して、駆動手段を正転又は逆転駆動して薬液用調節弁
及び水用調節弁を開けたり閉めたりして、空気圧に対す
る薬液及び水の圧力を一定にする制御が行われるので、
噴射個所が部分的に中断され、一時的に薬液,水,空気
圧の流量及び圧力の変動があっても自動的に修正され、
安定的して気泡をマニホールドのノズルから噴射発生さ
せることができる。したがって、継続して粉塵を抑制し
うる。
As described above, according to the first aspect of the present invention, the pressure value of the chemical solution is compared with the pressure value of the air, and the driving means is driven forward or reverse to adjust the chemical solution. Opening and closing the valve and the water control valve to control the pressure of the chemical and water relative to the air pressure is performed,
The injection point is partially interrupted, and even if there is a temporary change in the flow rate and pressure of the chemical, water, and air pressure, it is automatically corrected.
Air bubbles can be stably emitted from the nozzles of the manifold. Therefore, dust can be continuously suppressed.

【0032】また、請求項2に記載の発明によれば、制
御手段は、薬液及び水の圧力が空気圧に近づけられるの
に加え、空気用調節弁を正/逆転駆動して開/閉する空
気弁用駆動手段を利用して空気圧の方も薬液及び水の圧
力に近づけるので、空気圧に対する薬液及び水の圧力を
一定に制御する時間が短縮される。
According to the second aspect of the present invention, the control means controls the air to be opened / closed by driving the pneumatic control valve forward / reversely in addition to bringing the pressure of the chemical and water close to the air pressure. Since the pneumatic pressure is made closer to the pressure of the chemical and water by using the valve driving means, the time for controlling the pressure of the chemical and water with respect to the air pressure to be constant is reduced.

【0033】更に、請求項3に記載の発明によれば、請
求項1又は2の発明の作用効果に加えて、制御手段は、
少なくとも2組以上のマニホールドのうち1組のマニホ
ールドの複数の噴出用ノズルから気泡の噴射が中止又は
中断になったことを検知した時に、すなわち、薬液,
水,空気圧の流量及び圧力の変動が大きい予想される場
合に限り、空気圧に対する薬液及び水の圧力を一定に制
御することを行うものであるので、効率的である。
Further, according to the third aspect of the present invention, in addition to the functions and effects of the first or second aspect, the control means further comprises:
When it is detected that the injection of air bubbles has been stopped or interrupted from a plurality of ejection nozzles of one set of manifolds of at least two or more sets of manifolds,
Only when the fluctuation of the flow rate and the pressure of the water and the air pressure is expected to be large, the pressure of the chemical solution and the water with respect to the air pressure is controlled to be constant, so that it is efficient.

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

【図1】本発明の実施形態に係る粉塵抑制装置が現場に
適用された例を示す模式図である。
FIG. 1 is a schematic diagram illustrating an example in which a dust suppression device according to an embodiment of the present invention is applied to a site.

【図2】本発明の実施形態に係る粉塵抑制装置の制御系
統の構成概要を示すブロック図である。
FIG. 2 is a block diagram illustrating a configuration outline of a control system of the dust suppression device according to the embodiment of the present invention.

【図3】各マニホールドと混合液製造装置間との接続を
示す構成図である。
FIG. 3 is a configuration diagram showing a connection between each manifold and a mixed liquid manufacturing apparatus.

【図4】中央制御装置の圧力制御処理の内容を示すフロ
ーチャートである。
FIG. 4 is a flowchart showing the contents of a pressure control process of the central control device.

【図5】マニホールドの他の実施形態例を示す斜視図で
ある。
FIG. 5 is a perspective view showing another embodiment of the manifold.

【符号の説明】[Explanation of symbols]

1 混合液製造装置 2 発泡器 3 混合液供給管 4 空気圧供給管 5 薬液用圧力センサー 6 空気用圧力センサー 7 ノズル 8,9 マニホールド 10 気泡供給管 11 薬液用調節弁 12 水用調節弁 13 中央制御装置 15 ポンプ 17 水用圧力センサー 19 ポンプ 21 コンプレッサー 24 空気用調節弁 33,34,35,36 開閉弁 50 マニホールド 51 ノズル 100 発泡制御装置 M1 モータ M2 モータ REFERENCE SIGNS LIST 1 mixed liquid production apparatus 2 foamer 3 mixed liquid supply pipe 4 air pressure supply pipe 5 chemical liquid pressure sensor 6 air pressure sensor 7 nozzle 8,9 manifold 10 bubble supply pipe 11 chemical liquid control valve 12 water control valve 13 central control Apparatus 15 Pump 17 Water pressure sensor 19 Pump 21 Compressor 24 Air control valve 33, 34, 35, 36 On-off valve 50 Manifold 51 Nozzle 100 Foaming control device M1 motor M2 motor

───────────────────────────────────────────────────── フロントページの続き (72)発明者 金常 賢治 広島市安芸区矢野新町二丁目3番24号 株式会社メンテック内 (56)参考文献 特開 平2−300500(JP,A) 特開 平9−47682(JP,A) 特開 平5−96213(JP,A) 特開 平6−277573(JP,A) 特開 平10−169218(JP,A) 特公 昭51−35024(JP,B2) 実公 平2−5896(JP,Y2) 実用新案登録2548547(JP,Y2) (58)調査した分野(Int.Cl.7,DB名) B05B 7/26 B05C 11/10 B01F 3/04 B02C 23/00 E04G 23/08 ──────────────────────────────────────────────────続 き Continuation of the front page (72) Inventor Kenji Kaneshiro 2-3-24 Yano Shinmachi, Aki-ku, Hiroshima City Mentec Co., Ltd. (56) References JP-A-2-300500 (JP, A) JP-A-Hei 9-47682 (JP, A) JP-A-5-96213 (JP, A) JP-A-6-277573 (JP, A) JP-A-10-169218 (JP, A) JP-B-51-35024 (JP, A) B2) Jiko 2-5896 (JP, Y2) Utility model registration 2548547 (JP, Y2) (58) Fields investigated (Int. Cl. 7 , DB name) B05B 7/26 B05C 11/10 B01F 3/04 B02C 23/00 E04G 23/08

Claims (4)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】供給された界面活性剤を含む薬液と水を同
圧で混合して混合液を製造する混合液製造装置;混合液
と圧縮空気を混合処理して気泡を発生させる発泡器;前
記製造された混合液を発泡器に送る送液手段;圧縮空気
を発泡器に送る送気手段;前記混合液製造装置の薬液と
水が混合される位置より前に設けられた送られる薬液の
圧力を検出する薬液用圧力センサー;送気手段に設けら
れた送られる空気圧を検出する空気用圧力センサー;複
数の噴出用ノズルが取り付けられた少なくとも2組以上
のマニホールド;前記発泡器と各マニホールドとを接続
し、発生させた気泡を噴出用ノズルに送る気泡供給手
段;前記混合液製造装置に設けられた薬液用調節弁と水
用調節弁を正/逆転駆動して開/閉する駆動手段;およ
び、 薬液用圧力センサーの値を空気用圧力センサーの値と比
較し、薬液の圧力が空気の圧力よりも設定値分大きくな
ると、前記駆動手段を逆転駆動して薬液用調節弁及び水
用調節弁を閉め、逆に薬液の圧力が空気の圧力より設定
値分小さくなると、駆動手段を正転駆動して薬液用調節
弁及び水用調節弁を開けて、空気圧に対する薬液及び水
の圧力を一定にする制御手段;を備えることを特徴とす
る粉塵抑制装置。
1. A mixed liquid producing apparatus for producing a mixed liquid by mixing a supplied chemical liquid containing a surfactant and water at the same pressure; a foaming device for mixing the mixed liquid and compressed air to generate air bubbles; Liquid sending means for sending the produced mixed solution to the foaming device; air sending means for sending compressed air to the foaming device; of the sent chemical solution provided in the mixed solution manufacturing apparatus before the chemical solution and water are mixed. A pressure sensor for a chemical solution for detecting pressure; a pressure sensor for air provided in an air supply means for detecting an air pressure to be sent; at least two or more sets of manifolds to which a plurality of ejection nozzles are attached; And a bubble supply means for sending generated bubbles to a nozzle for jetting; a drive means for opening / closing the control valve for chemical liquid and the control valve for water provided in the mixed liquid production apparatus by forward / reverse rotation; And the pressure sensor for chemicals The value of the sensor is compared with the value of the air pressure sensor, and when the pressure of the chemical solution is larger than the pressure of the air by a set value, the driving means is driven in reverse to close the chemical liquid control valve and the water control valve, and When the pressure of the chemical solution is smaller than the pressure of the air by a set value, the drive means is driven to rotate forward to open the control valve for the chemical solution and the control valve for the water so as to make the pressure of the chemical solution and water constant with respect to the air pressure; A dust suppression device comprising:
【請求項2】前記送気手段に空気用調節弁を正/逆転駆
動して開/閉する空気弁用駆動手段を更に備え、前記制
御手段は、薬液用圧力センサーの値を空気用圧力センサ
ーの値と比較し、薬液の圧力が空気の圧力よりも設定値
分大きくなると、前記駆動手段を逆転駆動して薬液用調
節弁及び水用調節弁を閉めるとともに空気弁用駆動手段
を正転駆動して空気用調節弁を開け、逆に、薬液の圧力
が空気の圧力より設定値分小さくなると、駆動手段を正
転駆動して薬液用調節弁及び水用調節弁を開けるととも
に空気弁用駆動手段を逆転駆動して空気用調節弁を閉め
て、空気圧に対する薬液及び水の圧力を一定にすること
を特徴とする請求項1に記載の粉塵抑制装置。
2. The air supply means further comprises air valve drive means for opening / closing the air control valve by rotating the air control valve forward / reversely, and the control means uses the value of the chemical liquid pressure sensor as the air pressure sensor. When the pressure of the chemical is greater than the pressure of the air by the set value, the driving means is driven in reverse to close the chemical liquid control valve and the water control valve, and the air valve driving means is driven in normal rotation. On the contrary, when the pressure of the chemical solution is smaller than the air pressure by the set value, the driving means is driven forward to open the control valve for the chemical solution and the control valve for the water and to drive the air valve. 2. The dust suppression device according to claim 1, wherein the means is reversely driven to close the air control valve so that the pressure of the chemical and the water with respect to the air pressure is constant.
【請求項3】前記制御手段は、少なくとも2組以上のマ
ニホールドのうち1組のマニホールドの複数の噴出用ノ
ズルから気泡の噴射が中止又は中断になったことを検知
すると、前記薬液用圧力センサーの値を空気用圧力セン
サーの値と比較し、その結果に基づいて空気圧に対する
薬液及び水の圧力を一定にする制御を行うことを特徴と
する請求項1又は2に記載の粉塵抑制装置。
3. When the control means detects that the injection of bubbles from a plurality of ejection nozzles of one set of at least two or more sets of manifolds is stopped or interrupted, the control means detects the pressure of the chemical liquid pressure sensor. 3. The dust suppression device according to claim 1, wherein the value is compared with a value of an air pressure sensor, and control is performed to make the pressure of the chemical solution and water constant with respect to the air pressure based on the result. 4.
【請求項4】前記界面活性剤を含む薬液は、陰イオン界
面活性剤に属するα−オレフィンスルホン酸塩(AO
S)であることを特徴とする請求項1乃至3のいずれか
に記載の粉塵抑制装置。
4. The chemical solution containing a surfactant is an α-olefin sulfonate (AO) belonging to an anionic surfactant.
The dust suppression device according to any one of claims 1 to 3, wherein S).
JP09244613A 1997-08-25 1997-08-25 Dust suppression device Expired - Lifetime JP3137931B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP09244613A JP3137931B2 (en) 1997-08-25 1997-08-25 Dust suppression device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP09244613A JP3137931B2 (en) 1997-08-25 1997-08-25 Dust suppression device

Publications (2)

Publication Number Publication Date
JPH1157541A JPH1157541A (en) 1999-03-02
JP3137931B2 true JP3137931B2 (en) 2001-02-26

Family

ID=17121350

Family Applications (1)

Application Number Title Priority Date Filing Date
JP09244613A Expired - Lifetime JP3137931B2 (en) 1997-08-25 1997-08-25 Dust suppression device

Country Status (1)

Country Link
JP (1) JP3137931B2 (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008169655A (en) * 2007-01-13 2008-07-24 Fujibayashi Shokai:Kk Building material disposal method

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN103646518A (en) * 2013-12-18 2014-03-19 北京风华时代环境工程有限公司 Section controller

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2008169655A (en) * 2007-01-13 2008-07-24 Fujibayashi Shokai:Kk Building material disposal method

Also Published As

Publication number Publication date
JPH1157541A (en) 1999-03-02

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