JPH08126899A - Soil solidification treatment pumping equipment - Google Patents
Soil solidification treatment pumping equipmentInfo
- Publication number
- JPH08126899A JPH08126899A JP26526894A JP26526894A JPH08126899A JP H08126899 A JPH08126899 A JP H08126899A JP 26526894 A JP26526894 A JP 26526894A JP 26526894 A JP26526894 A JP 26526894A JP H08126899 A JPH08126899 A JP H08126899A
- Authority
- JP
- Japan
- Prior art keywords
- soft mud
- solidifying agent
- flow rate
- pressure
- soft
- 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.)
- Pending
Links
Landscapes
- Treatment Of Sludge (AREA)
Abstract
(57)【要約】
【目的】 貯溜された軟泥を自動的、連続的に均一に混
合したうえ固化処理できる軟泥の固化処理圧送設備を提
供する。
【構成】 軟泥タンク110と流量調整手段120と流
量計130とからなる軟泥供給装置100と、固化剤サ
イロ310と固化剤供給機320と竪型スクリュコンベ
ヤ330とからなる固化剤供給装置300と、加圧ポン
プ410と排送管420とエゼクタ430とからなる軟
泥圧送装置400とから構成されたものである。
(57) [Summary] [Objective] To provide a solidification treatment pumping facility for softened sludge, which is capable of automatically and continuously mixing and solidifying the stored sludge. A soft mud supply device 100 including a soft mud tank 110, a flow rate adjusting means 120, and a flow meter 130, a solidification agent supply device 300 including a solidification agent silo 310, a solidification agent supply device 320, and a vertical screw conveyor 330, It comprises a pressurizing pump 410, a discharge pipe 420, and a soft mud pressure feeding device 400 including an ejector 430.
Description
【0001】[0001]
【産業上の利用分野】本発明は、河川、湖沼、港湾など
で浚渫採取された泥土や下水処理場などにおける下水汚
泥や脱水汚泥などの軟泥に連続的に固化剤を均一に添加
しつつ空気搬送により移送する軟泥の固化処理圧送設備
に関する。[Field of Industrial Application] The present invention continuously and uniformly adds a solidifying agent to soft soil such as mud dredged and collected in rivers, lakes and marshes, sewage sludge and dehydrated sludge in sewage treatment plants, etc. The present invention relates to a solidification treatment pressure-feeding facility for soft mud transferred by transportation.
【0002】[0002]
【従来の技術】従来、これらの軟泥を混練固化するに
は、一定量の軟泥とこの量に見合う固化剤をタンクへ入
れ、タンクに付属する攪拌機能を持った混練機で混ぜ合
わせたり、ポータブルの攪拌機を使って人手で攪拌する
ことによって均一に混合するか、または、容器内に入れ
られた軟泥と固化剤とをバックホーなどの土木建設機器
を使用して人間の操作により混ぜ合わせていた。2. Description of the Related Art Conventionally, in order to knead and solidify such soft mud, a certain amount of soft mud and a solidifying agent corresponding to this quantity are put into a tank and mixed with a kneader having an agitation function attached to the tank or portable. The mixture was uniformly mixed by manually stirring it with the stirrer of No. 1, or the soft mud contained in the container and the solidifying agent were mixed with each other by human manipulation using a civil construction equipment such as a backhoe.
【0003】[0003]
【発明が解決しようとする課題】上述したタンク内での
混練や攪拌機あるいは土木建設機器の操作による混練
は、いずれもバッチ方式であり、多くの時間を要し煩雑
であるばかりでなく、給泥、固化剤投入、混練、排送な
どの各操作が断続的に行われるため、作業効率が悪く、
処理される軟泥の流量が刻々変化した場合には速やかに
これに対応することが難しく、流量にマッチした適正な
固化剤の混入がなされないため、でき上がった固化軟泥
の強度が一定しない問題があった。このため、軟泥の流
量にマッチした固化剤を能率よく自動的に均一に混合す
る方策が熱望されていた。The above-mentioned kneading in the tank and kneading by the operation of the stirrer or the civil construction equipment are all batch processes, which not only take a lot of time and are complicated, but also mud feeding. , Operations such as solidifying agent addition, kneading, and discharging are performed intermittently, resulting in poor work efficiency.
If the flow rate of the treated soft mud changes momentarily, it is difficult to deal with this promptly, and since the proper solidifying agent that does not match the flow rate is not mixed, there is a problem that the strength of the solidified softened sludge produced is not constant. It was For this reason, there has been a strong demand for a method of efficiently and automatically mixing the solidifying agent that matches the flow rate of the soft mud.
【0004】[0004]
【課題を解決するための手段】以上の課題を解決するた
めに、本発明においては、貯溜された軟泥に固化剤を均
一に混合し排送管に混合し排送管中を圧送する軟泥の固
化処理圧送設備であって、排出口に流量調整手段を備え
た軟泥を貯溜する軟泥タンクと該流量調整手段に後続し
軟泥を圧送する軟泥圧送装置と軟泥の移送中に該軟泥に
固化剤を添加する固化剤供給装置とからなり、該軟泥圧
送装置は前記流量調整手段に後続する加圧ポンプと排送
管と該排送管途中に配設した圧縮空気注入用のエゼクタ
とから構成され、該固化剤供給装置は固化剤サイロと該
固化剤サイロに後続し前記加圧ポンプの上流側へ接続す
る固化剤供給機ならびに竪型スクリュコンベヤとから構
成したものである。また、第2の発明では、第1の発明
の加圧ポンプとエゼクタとの間に逆止弁を配設した。さ
らに、第3の発明では、軟泥タンクの流量調整手段の下
流に流量計を配設するとともに、制御装置を介して軟泥
流量に適合する固化剤供給量となるよう固化剤供給機を
制御することとした。In order to solve the above-mentioned problems, in the present invention, a softening agent is uniformly mixed with the stored softening agent, mixed with a discharging pipe, and pressure-fed in the discharging pipe. A solidification treatment pressure-feeding facility, wherein a sludge tank having a flow rate adjusting means at its outlet for storing soft sludge, a soft mud pressure feeding device following the flow rate adjusting means for pressure-feeding soft mud, and a solidifying agent for the soft sludge during the transfer of the soft mud A solidification agent supply device for adding, the soft mud pressure feeding device is composed of a pressurizing pump following the flow rate adjusting means, a discharge pipe and an ejector for injecting compressed air disposed in the middle of the discharge pipe, The solidifying agent supply device is composed of a solidifying agent silo, a solidifying agent feeder that is connected to the solidifying agent silo and is connected to the upstream side of the pressurizing pump, and a vertical screw conveyor. Further, in the second invention, the check valve is arranged between the pressurizing pump of the first invention and the ejector. Further, in the third invention, a flow meter is arranged downstream of the flow rate adjusting means of the soft mud tank, and the solidifying agent supply machine is controlled through the control device so that the solidifying agent supply amount is adapted to the soft mud flow rate. And
【0005】[0005]
【作用】本発明においては、軟泥タンクに貯溜された軟
泥を埋立地など遠方の移送場所へ空気搬送するととも
に、途中の過程で固化剤を適量添加し、かつ、十分混練
して軟泥と固化剤とが十分に均一に混合された状態とな
って目的地へ移送される。すなわち、軟泥タンク中の軟
泥は下部の排出口より重力作用により排出され、流量調
整手段によりほぼ定量の排出がなされて後続の加圧ポン
プへ移送され、その途中において固化剤供給装置によっ
て添加された固化剤とともに加圧ポンプで昇圧され、か
つ、排送管で移送中に十分混練されエゼクタにより供給
される圧縮エアでプラグ輸送され遠方の目的地へ排送さ
れる。加圧ポンプとエゼクタとの間に逆止弁を設けた場
合には、軟泥の排送管中の逆流が防止され軟泥の円滑な
移送が確保される。また、軟泥タンクから排出される流
量を流量調整手段の後に設けた流量計によって常時測定
し軟泥流量の変化に応じて軟泥流量にマッチした固化剤
の適量の供給を制御し、固化剤が適正な一定比率で混合
された軟泥とする。In the present invention, the soft mud stored in the soft mud tank is transported by air to a distant transfer place such as a landfill, and an appropriate amount of the solidifying agent is added in the course of the process, and the kneaded mixture is sufficiently kneaded to soften the mud and the solidifying agent. And are mixed sufficiently uniformly and transferred to the destination. That is, the soft mud in the soft mud tank is discharged by gravity from the lower discharge port, is discharged in a substantially fixed amount by the flow rate adjusting means and is transferred to the subsequent pressurizing pump, and is added by the solidifying agent supplying device on the way. The pressure is increased by the pressure pump together with the solidifying agent, and is sufficiently kneaded during transfer by the discharge pipe and is plug-transported by the compressed air supplied by the ejector to be discharged to a distant destination. When the check valve is provided between the pressurizing pump and the ejector, the backflow of the soft mud in the discharge pipe is prevented, and the smooth transfer of the soft mud is ensured. Further, the flow rate discharged from the soft mud tank is constantly measured by a flow meter provided after the flow rate adjusting means, and an appropriate amount of the solidifying agent that matches the soft mud flow rate is controlled according to the change in the soft mud flow rate, so that the solidifying agent is appropriate. The soft mud is mixed at a fixed ratio.
【0006】[0006]
【実施例】以下図面に基づいて本発明の実施例の詳細に
ついて説明する。図1〜図4は本発明の実施例に係り、
図1は固化処理圧送設備の全体構成図、図2は固化処理
圧送設備の要部詳細縦断面図、図3は流量調整手段の種
々の実施例を示す概略説明図、図4は固化剤供給機の種
々の実施例を示す概略説明図である。本発明の軟泥の固
化処理圧送設備1000は、図1に示すように、排出口
に流量調整手段120を備えた鋼板製の軟泥タンク11
0からなる軟泥供給装置100と、軟泥タンク110に
後続する軟泥圧送装置400と、軟泥圧送装置400の
上流側へ固化剤を添加する固化剤供給装置300とから
構成される。流量調整手段120は、図3に示す種々の
タイプのものが使用される。すなわち、ナイフゲート弁
120a、バタフライ弁120b、ボール弁120cな
どのバルブ類やカットオフゲート120d、あるいはロ
ータリフィーダ120e、ベルトフィーダ120f、エ
プロンフィーダ120g、スクリュフィーダ120hな
どのフィーダ類が使用可能である。軟泥タンク110と
流量調整手段120とを軟泥供給装置100と称する。
流量調整手段120の後には流量計130が配設され
る。Embodiments of the present invention will be described below in detail with reference to the drawings. 1 to 4 relate to an embodiment of the present invention,
FIG. 1 is an overall configuration diagram of the solidification processing pressure-feeding equipment, FIG. 2 is a detailed vertical cross-sectional view of a main part of the solidification processing pressure-feeding equipment, FIG. 3 is a schematic explanatory view showing various embodiments of a flow rate adjusting means, and FIG. It is a schematic explanatory drawing showing various examples of a machine. As shown in FIG. 1, the sludge solidification treatment pressure-feeding equipment 1000 of the present invention is a steel sheet sludge tank 11 provided with a flow rate adjusting means 120 at the discharge port.
The soft mud supply device 100 consisting of 0, the soft mud pressure feeding device 400 following the soft mud tank 110, and the solidifying agent feeding device 300 for adding the solidifying agent to the upstream side of the soft mud pressure feeding device 400. As the flow rate adjusting means 120, various types shown in FIG. 3 are used. That is, valves such as a knife gate valve 120a, a butterfly valve 120b, and a ball valve 120c and a cutoff gate 120d, or feeders such as a rotary feeder 120e, a belt feeder 120f, an apron feeder 120g, and a screw feeder 120h can be used. The soft mud tank 110 and the flow rate adjusting means 120 are referred to as a soft mud supply device 100.
A flow meter 130 is provided after the flow rate adjusting means 120.
【0007】軟泥タンク110と流量調整手段120と
流量計130とからなる軟泥供給装置100と、後述す
る軟泥圧送装置400の加圧ポンプ410へ至る経路の
途中には、図1〜図2に示すように、固化剤供給装置3
00が配設される。固化剤供給装置300は、固化剤を
貯蔵する固化剤サイロ310とこれに後続する固化剤供
給機320と竪型スクリュコンベヤ330と逆止弁34
0とから形成される。固化剤供給装置300を加圧ポン
プ410直前の排送管420へ接続した理由は、加圧ポ
ンプ410の直前は通常加圧ポンプ410の駆動により
常時負圧状態になっており、固化剤を円滑に排送管42
0内へ吸引して軟泥に支障なく混入させることができる
からである。しかし、運転中何らかの不測の事態により
加圧ポンプ直前の排送管420でも正圧(プラス圧)と
なることがあり、この場合には添加しようとする固化剤
が逆流して円滑な供給を阻害するトラブルが発生する。
このようなトラブルを防止する対策として、竪型スクリ
ュコンベヤ330の下に逆止弁340を設けて逆流を防
ぎ、かつ、移送手段として若干の正圧状態でも強力に固
化剤を排送管420へ移送することのできる竪型スクリ
ュコンベヤ330を採用した。竪型スクリュコンベヤ3
30は、上述のプラス圧状態でも支障なく固化剤を逆流
させることなく強力に下方へ移送するため、その回転数
を300〜800rpmの範囲で可変とする。上述の数
値限定理由を述べると、下限値300rpmはそれ以下
では逆流の惧れがあるためであり、上限値800rpm
は、実際に発生するプラス圧に対してそれ以上の高速と
しても逆流防止効果に変わりがないからである。また、
固化剤供給機320は、粉末状の固化剤を定量供給でき
るものであれば、例えば、図4に示すように、テーブル
フィーダ、ピストンフィーダ、ベルトフィーダなどどの
ようなタイプでも使用可能であるが、前述の逆流対策に
留意するならば、構造が簡単で、かつ、コンパクトであ
り、任意の定量供給が可能で、しかも、エアロック状態
で移送供給できるタイプのものが望ましい。そして流量
調整手段120の直下に配設された流量計130によっ
て計測される軟泥流量にマッチした固化剤添加量を固化
剤供給機320で供給できるようにするため、制御装置
200を介してモータ320mを軟泥流量にマッチした
添加量を与える回転数に制御する。また、加圧ポンプ4
10の背後に配設された流量計440で、その結果を確
認する。固化剤供給機320は、粉末状の固化剤を扱う
関係上密閉カバーを具備した密閉構造のものが望まし
い。また、固化剤供給機320と接続される軟泥タンク
110からの逆圧(プラス圧)により、固化剤の逆流が
起こらないよう、図2に示すように、エアロック機構を
備えたロータリフィーダ320Aを固化剤供給機320
に採用することもできる。また、このような逆圧トラブ
ルを防止するため、竪型スクリュコンベヤ330の直下
に逆止弁340を配設することもできる。1 and 2 on the way to the soft mud supply device 100 consisting of the soft mud tank 110, the flow rate adjusting means 120 and the flow meter 130, and the path to the pressurizing pump 410 of the soft mud pumping device 400 described later. So that the solidifying agent supply device 3
00 is provided. The solidifying agent supply device 300 includes a solidifying agent silo 310 for storing the solidifying agent, a solidifying agent supplier 320 following the solidifying agent silo 310, a vertical screw conveyor 330, and a check valve 34.
It is formed from 0 and. The reason why the solidifying agent supply device 300 is connected to the discharge pipe 420 immediately before the pressurizing pump 410 is that the normal pressurizing pump 410 is always in a negative pressure state immediately before the pressurizing pump 410, and the solidifying agent is smoothly supplied. To the discharge pipe 42
This is because it can be sucked into 0 and mixed in the soft mud without any trouble. However, due to some unforeseen circumstances during operation, the discharge pipe 420 immediately before the pressurizing pump may have a positive pressure (plus pressure), and in this case, the solidifying agent to be added flows backward and hinders smooth supply. Trouble occurs.
As a measure for preventing such trouble, a check valve 340 is provided under the vertical screw conveyor 330 to prevent backflow, and the solidifying agent is strongly transferred to the discharge pipe 420 as a transfer means even in a slight positive pressure state. A vertical screw conveyor 330 that can be transferred is used. Vertical screw conveyor 3
No. 30 strongly transfers the solidifying agent downward without causing backflow even in the above-mentioned positive pressure state, so that the rotation speed thereof is variable in the range of 300 to 800 rpm. The reason for limiting the above numerical values is that the lower limit value of 300 rpm is likely to cause backflow below the upper limit value of 800 rpm.
Is because the backflow prevention effect remains the same even if the speed is higher than the actually generated plus pressure. Also,
The solidifying agent feeder 320 may be of any type, such as a table feeder, a piston feeder, and a belt feeder, as long as it can quantitatively supply the powdery solidifying agent, as shown in FIG. If attention is paid to the above-mentioned backflow countermeasure, it is desirable that the structure is simple, compact, and capable of supplying an arbitrary fixed amount and capable of being transferred and supplied in an airlock state. Then, in order to enable the solidifying agent supply device 320 to supply the solidifying agent addition amount that matches the flow rate of the soft mud measured by the flow meter 130 arranged immediately below the flow rate adjusting means 120, the motor 320 m is supplied via the control device 200. Is controlled to a rotation speed that gives an addition amount that matches the soft mud flow rate. In addition, the pressure pump 4
The result is confirmed by the flow meter 440 arranged behind the 10. The solidifying agent feeder 320 preferably has a closed structure including a closed cover in order to handle the powdery solidifying agent. Further, as shown in FIG. 2, a rotary feeder 320A equipped with an air lock mechanism is provided so that the back flow of the solidification agent does not occur due to the reverse pressure (plus pressure) from the soft mud tank 110 connected to the solidification agent feeder 320. Solidifying agent feeder 320
Can also be adopted. Further, in order to prevent such a back pressure trouble, a check valve 340 may be arranged immediately below the vertical screw conveyor 330.
【0008】次に、軟泥圧送装置400について述べ
る。軟泥圧送装置400は、軟泥供給装置100に後続
する加圧ポンプ410と加圧ポンプ410以降の軟泥を
移送する排送管420と排送管420の途中に設けた圧
縮空気注入用のエゼクタ430および圧縮空気の供給源
となるコンプレッサ432とから構成される。固化剤供
給装置300で固化剤と混合された軟泥は加圧ポンプ4
10で加圧されるとともに十分混練され、排送管420
の内部を下流へ移送され、途中のエゼクタ430から注
入される圧縮空気でさらにプラグ輸送(栓輸送)とさ
れ、遠方の目的地へ空気搬送される。加圧ポンプ410
とエゼクタ430との間には、望ましくは流量計440
と逆止弁450とが配設され、逆止弁450はエゼクタ
430から注入された圧縮空気が逆流するのを防止し、
流量計440は前述したように、固化剤添加後の軟泥流
量の測定をし、一方、流量調整手段120後の流量計1
30は、軟泥の流量を検出する流量計130の検出信号
を受信する制御装置200にあらかじめ軟泥流量に適合
した固化剤の供給量の設定値を記憶させておき、運転中
軟泥流量の実測値に適合する固化剤供給量を制御装置2
00で演算したうえ、固化剤供給機320の駆動装置
(モータ)320mに操作指令を発信して適正な量の固
化剤を竪型スクリュコンベヤ330へ供給させる。Next, the soft mud pressure feeding device 400 will be described. The soft mud pressure feeding device 400 includes a pressurizing pump 410 following the soft mud feeding device 100, a discharge pipe 420 for transferring the soft mud after the pressurizing pump 410, and an ejector 430 for injecting compressed air provided in the middle of the discharge pipe 420. It is composed of a compressor 432 which is a supply source of compressed air. The soft mud mixed with the solidifying agent in the solidifying agent supply device 300 is a pressure pump 4
Pressurized at 10 and kneaded sufficiently, discharge pipe 420
The compressed air injected from the ejector 430 on the way is further transported by plug (transportation by plug), and is transported to a distant destination by air. Pressure pump 410
Between the ejector 430 and the ejector 430 is preferably a flow meter 440.
And a check valve 450 are provided, and the check valve 450 prevents the compressed air injected from the ejector 430 from flowing backward,
As described above, the flow meter 440 measures the flow rate of the soft mud after addition of the solidifying agent, while the flow meter 1 after the flow rate adjusting means 120 is measured.
The control unit 200, which receives the detection signal of the flow meter 130 that detects the flow rate of the soft mud, stores the set value of the supply amount of the solidifying agent that is adapted to the soft mud flow rate in advance, and stores the measured value of the soft mud flow rate during operation. The controller 2 controls the supply amount of the suitable solidifying agent.
00, and then sends an operation command to the drive device (motor) 320m of the solidifying agent supplier 320 to supply an appropriate amount of the solidifying agent to the vertical screw conveyor 330.
【0009】一方、固化剤供給装置300は、前述した
ように、軟泥供給装置100と軟泥圧送装置400との
間に接続され、排送管420を移送中の軟泥にその流量
に見合った固化剤を供給するもので、固化剤サイロ31
0には、セメントやセメント系固化剤などの粉体を入
れ、固化剤供給機320は、例えば前述したように図4
に示すような、ロータリフィーダやテーブルフィーダ、
ピストンフィーダなどの供給機を採用し、流量計130
で計測した軟泥の実際流量に応じてモータ320mを制
御し、供給量を調整する。固化剤は、粉体のまま、ある
いは水を添加したスラリ状のもののいずれでもよく、そ
の選択は土質による混合度合によって決定する。ただ
し、粉体のままの方が経済的であるので、大差ない場合
は粉体のまま使用する。粉体で送る場合は、固化剤供給
機320で定量供給された固化剤は竪型スクリュコンベ
ヤ330で強制的に下方へ移送される。固化剤は粉体の
まま供給してもよいが、土質によっては、軟泥と均一に
混合させるためには水を添加したスラリ状が望ましい。
スラリ状の添加の場合には、固化剤供給機320はミキ
サ(混合攪拌機)を備えた貯槽を設け、そこに給水ライ
ンを接続して粉体の固化剤をスラリとしたうえピストン
ポンプで構成し、排出する。固化剤は軟泥1m3に対し
て、50〜200kg(通常は100kg)の比率で添
加する。本発明においては、以上のように、排送管42
0内を空気搬送される軟泥に事前に固化剤を添加して十
分混練し均一状態とするために、加圧ポンプ410の羽
根の回転による圧送作用の際に軟泥と固化剤とを十分に
混ぜ合わせて吐出し、さらにプラグ輸送中にも均一にほ
どよく混合され、遠隔の目的地に達した後、一定期間経
過後(通常2〜7日間)に必要強度以上に固化する。つ
まり、固化剤添加量は、泥土土質の種類や何日後に何k
gf/cm2 の強度が欲しいかによって添加量を決定す
る。当然のことながら、添加量が多くなる程、早く、固
く、固化する。このように、本発明における軟泥と固化
剤との均一混合はあらかじめ加圧ポンプ410で十分混
合された後、さらに排送管中のプラグ輸送中に能率よく
実施されるため、排送管420の長さは従来少なくとも
50mは必要とされた長さをさらに短縮できる。なお、
本発明の設備を直接浚渫船に装備し、海底のヘドロなど
の軟泥を浚渫し、固化処理を行って遠方の目的地へ搬送
することもできる。本発明の特徴は、固化剤と軟泥との
混合が、まず加圧ポンプの回転による1段混合と排送管
中のプラグ輸送におけるプラグ生成〜破壊の繰り返し作
動による2段混合とを有するため混合・攪拌が十分に行
われ均一度(混練度)が非常に高いという点である。ま
た、本発明では、固化剤供給装置300として、固化剤
サイロ310から供給される固化剤は竪型スクリュコン
ベヤ330へ供給され竪型スクリュコンベヤ330内の
軟泥のヘッド圧で加圧ポンプ410の直前へ移送される
から負圧状態の排送管420内へ円滑に導入されるばか
りでなく、排送管420内に何らかの原因でプラス圧が
発生しても、固化剤が逆流しない。また、固化剤供給機
320をエアシール機能を具備するロータリフィーダと
したり、固化剤供給機320の直下に逆止弁を設けるな
どして固化剤の逆流を防止することができるから、逆流
トラブルを回避できる。On the other hand, the solidifying agent supplying device 300 is connected between the soft mud supplying device 100 and the soft mud pressure feeding device 400 as described above, and the solidifying agent corresponding to the flow rate of the soft mud being transferred through the discharge pipe 420 is supplied. Solidifying agent silo 31
0 contains powder such as cement and cement-based solidifying agent, and the solidifying agent supply device 320 is, for example, as shown in FIG.
Rotary feeder, table feeder,
Adopting a feeder such as a piston feeder, flow meter 130
The motor 320 m is controlled in accordance with the actual flow rate of the soft mud measured in step 3, and the supply amount is adjusted. The solidifying agent may be a powder as it is or a slurry with water added, and the selection is determined by the degree of mixing depending on the soil. However, it is more economical to use the powder as it is, so use the powder as it is if there is not much difference. When the powder is sent, the solidifying agent supplied in a fixed amount by the solidifying agent feeder 320 is forcibly transferred downward by the vertical screw conveyor 330. The solidifying agent may be supplied as a powder, but depending on the soil quality, a slurry with water added is desirable in order to mix it uniformly with the soft mud.
In the case of slurry-like addition, the solidifying agent feeder 320 is provided with a storage tank equipped with a mixer (mixing stirrer), and a water supply line is connected thereto to make the powder solidifying agent into a slurry, which is constituted by a piston pump. ,Discharge. The solidifying agent is added at a ratio of 50 to 200 kg (usually 100 kg) to 1 m 3 of soft mud. In the present invention, as described above, the discharge pipe 42
In order to add a solidifying agent in advance to the soft sludge that is pneumatically conveyed in 0 and knead it sufficiently to make it uniform, the soft sludge and the solidifying agent are sufficiently mixed during the pressure-feeding action by the rotation of the blades of the pressure pump 410. They are discharged together, and evenly mixed evenly during plug transportation, and after reaching a remote destination, after a certain period of time (usually 2 to 7 days), they solidify beyond the required strength. In other words, the amount of solidifying agent added depends on the type of mud and soil and how many days later
The addition amount is determined depending on whether the strength of gf / cm 2 is desired. As a matter of course, the larger the added amount, the faster and harder the solidified. As described above, the uniform mixing of the soft mud and the solidifying agent in the present invention is sufficiently performed in advance by the pressurizing pump 410 and then efficiently performed during the plug transportation in the discharge pipe. A length of at least 50 m in the past can further reduce the required length. In addition,
It is also possible to equip the dredger directly with the equipment of the present invention, to dredge soft mud such as sludge on the seabed, perform solidification treatment, and transport it to a distant destination. The feature of the present invention is that the solidifying agent and the soft mud are mixed firstly by one-stage mixing by rotation of a pressure pump and two-stage mixing by repeated operation of plug generation-breakage in plug transportation in a discharge pipe. -The point is that the stirring is sufficiently performed and the homogeneity (kneading degree) is very high. Further, in the present invention, as the solidifying agent supplying device 300, the solidifying agent supplied from the solidifying agent silo 310 is supplied to the vertical screw conveyor 330 and immediately before the pressurizing pump 410 by the head pressure of the soft mud in the vertical screw conveyor 330. Not only is it smoothly introduced into the negative pressure discharge pipe 420, but the solidifying agent does not flow backward even if a positive pressure is generated in the discharge pipe 420 for some reason. Further, since the solidifying agent supply device 320 can be a rotary feeder having an air sealing function, or a check valve can be provided directly below the solidifying agent supply device 320, the reverse flow of the solidifying agent can be prevented, so that a backflow trouble can be avoided. it can.
【0010】[0010]
【発明の効果】以上説明したように、本発明の軟泥の固
化処理圧送設備は、給泥、固化剤供給、混練、排送が自
動的に、かつ、連続操作で実施され、従来技術のよう
に、固化混練工程を別個に必要としないから、能率的
で、かつ、均一な混合固化軟泥とすることができる。ま
た、固化剤は加圧ポンプより導入するため供給が容易
で、かつ、軟泥との混練が十分に行われるので一層均一
な混合状態が確保される。また、固化剤供給装置は、排
送管内のプラス圧に起因する固化剤の逆流を防止する機
能を備えているので、固化剤の円滑な供給が確保され
る。Industrial Applicability As described above, the sludge solidification treatment pressure-feeding equipment of the present invention automatically feeds mud, solidifying agent, kneading, and discharge in a continuous operation. Moreover, since a solidifying and kneading step is not separately required, an efficient and uniform mixed and solidified soft mud can be obtained. Further, since the solidifying agent is introduced from the pressure pump, the solidifying agent is easily supplied, and the kneading with the soft mud is sufficiently performed, so that a more uniform mixed state is secured. Further, since the solidifying agent supply device has a function of preventing the reverse flow of the solidifying agent due to the positive pressure in the discharge pipe, the smooth supply of the solidifying agent is ensured.
【図1】本発明の実施例に係る固化処理圧送設備の全体
構成図である。FIG. 1 is an overall configuration diagram of a solidification processing pressure-feeding facility according to an embodiment of the present invention.
【図2】本発明の実施例に係る固化処理圧送設備の要部
詳細縦断面図である。FIG. 2 is a detailed vertical cross-sectional view of a main part of a solidification processing pressure-feeding facility according to an embodiment of the present invention.
【図3】本発明に係る流量調整手段の種々の実施例を示
す概略説明図である。FIG. 3 is a schematic explanatory view showing various embodiments of the flow rate adjusting means according to the present invention.
【図4】本発明の実施例に係る種々の固化剤供給機の概
略説明図である。FIG. 4 is a schematic explanatory view of various solidifying agent feeders according to an embodiment of the present invention.
100 軟泥供給装置 110 軟泥タンク 120 流量調整手段 130 流量計 200 制御装置 300 固化剤供給装置 310 固化剤サイロ 320 固化剤供給機 320A ロータリフィーダ 320m モータ 330 竪型スクリュコンベヤ 340 逆止弁 400 軟泥圧送装置 410 加圧ポンプ 410a モータ 420 排送管 430 エゼクタ 432 コンプレッサ 440 流量計 450 逆止弁 1000 固化処理圧送設備 100 Soft Mud Supply Device 110 Soft Mud Tank 120 Flow Rate Adjustment Unit 130 Flow Meter 200 Control Device 300 Solidifying Agent Supply Device 310 Solidifying Agent Silo 320 Solidifying Agent Feeder 320A Rotary Feeder 320m Motor 330 Vertical Screw Conveyor 340 Check Valve 400 Soft Mud Pressure Feeding Device 410 Pressure pump 410a Motor 420 Exhaust pipe 430 Ejector 432 Compressor 440 Flowmeter 450 Check valve 1000 Solidification treatment pressure feeding facility
Claims (3)
排送管に混合し排送管中を圧送する軟泥の固化処理圧送
設備であって、排出口に流量調整手段を備えた軟泥を貯
溜する軟泥タンクと該流量調整手段に後続し軟泥を圧送
する軟泥圧送装置と軟泥の移送中に該軟泥に固化剤を添
加する固化剤供給装置とからなり、 該軟泥圧送装置は前記流量調整手段に後続する加圧ポン
プと排送管と該排送管途中に配設した圧縮空気注入用の
エゼクタとから構成され、 該固化剤供給装置は固化剤サイロと該固化剤サイロに後
続し前記加圧ポンプの上流側へ接続する固化剤供給機な
らびに竪型スクリュコンベヤとから構成された軟泥の固
化処理圧送設備。1. A solidification treatment pumping facility for softened sludge in which a solidifying agent is uniformly mixed with the stored softened sludge, which is mixed with a discharge pipe and pressure-fed in the discharge pipe, wherein the discharge port has a flow rate adjusting means. A soft mud tank for storing the soft mud, a soft mud pressure feeding device following the flow rate adjusting means for pressure feeding the soft mud, and a solidifying agent supplying device for adding a solidifying agent to the soft mud during the transfer of the soft mud, the soft mud pressure feeding device is provided with the flow rate adjusting means. The solidification agent supply device comprises a pressurizing pump following the means, a discharge pipe, and an ejector for injecting compressed air disposed in the discharge pipe. A solidification treatment pumping facility for soft mud, which is composed of a solidifying agent feeder connected to the upstream side of a pressure pump and a vertical screw conveyor.
配設した請求項1記載の軟泥の固化処理圧送設備。2. The solidification treatment pressurizing equipment for soft mud according to claim 1, wherein a check valve is provided between the pressurizing pump and the ejector.
計を配設するとともに、制御装置を介して軟泥流量に適
合する固化剤供給量となるよう固化剤供給機を制御する
請求項1または請求項2記載の軟泥の固化処理圧送設
備。3. The method according to claim 1, wherein a flow meter is provided downstream of the flow rate adjusting means of the soft mud tank, and the solidification agent supply machine is controlled by a control device so that the solidification agent supply amount is adapted to the soft mud flow rate. The solidification treatment pressure-feeding equipment of the soft mud according to claim 2.
Priority Applications (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26526894A JPH08126899A (en) | 1994-10-28 | 1994-10-28 | Soil solidification treatment pumping equipment |
| EP95305575A EP0699633A2 (en) | 1994-09-02 | 1995-08-10 | Solidification and pneumatic transportation equipment for soft mud |
| KR1019950026106A KR960010554A (en) | 1994-09-02 | 1995-08-23 | Solidified and Pneumatic Transport Devices |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP26526894A JPH08126899A (en) | 1994-10-28 | 1994-10-28 | Soil solidification treatment pumping equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH08126899A true JPH08126899A (en) | 1996-05-21 |
Family
ID=17414874
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP26526894A Pending JPH08126899A (en) | 1994-09-02 | 1994-10-28 | Soil solidification treatment pumping equipment |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH08126899A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108435017A (en) * | 2018-04-28 | 2018-08-24 | 慈溪市启承机械科技有限公司 | A kind of waterproof construction construction method |
| CN110735645A (en) * | 2019-09-17 | 2020-01-31 | 高春梅 | underground excavation broken object dredging device for subway tunnel excavation and construction |
| CN114455215A (en) * | 2022-02-16 | 2022-05-10 | 中交疏浚技术装备国家工程研究中心有限公司 | Accurate addition system of mud conditioner |
-
1994
- 1994-10-28 JP JP26526894A patent/JPH08126899A/en active Pending
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN108435017A (en) * | 2018-04-28 | 2018-08-24 | 慈溪市启承机械科技有限公司 | A kind of waterproof construction construction method |
| CN110735645A (en) * | 2019-09-17 | 2020-01-31 | 高春梅 | underground excavation broken object dredging device for subway tunnel excavation and construction |
| CN110735645B (en) * | 2019-09-17 | 2021-05-18 | 徐成晓 | Broken thing pull throughs of underground excavation is built in subway tunnel excavation |
| CN114455215A (en) * | 2022-02-16 | 2022-05-10 | 中交疏浚技术装备国家工程研究中心有限公司 | Accurate addition system of mud conditioner |
| CN114455215B (en) * | 2022-02-16 | 2023-07-04 | 中交疏浚技术装备国家工程研究中心有限公司 | Accurate adding system of mud conditioner |
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