JPH0871595A - Solidification treatment and pressure feed equipment for soft mud - Google Patents
Solidification treatment and pressure feed equipment for soft mudInfo
- Publication number
- JPH0871595A JPH0871595A JP20972894A JP20972894A JPH0871595A JP H0871595 A JPH0871595 A JP H0871595A JP 20972894 A JP20972894 A JP 20972894A JP 20972894 A JP20972894 A JP 20972894A JP H0871595 A JPH0871595 A JP H0871595A
- Authority
- JP
- Japan
- Prior art keywords
- solidifying agent
- screw conveyor
- soft mud
- vertical screw
- solidification
- 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
- Screw Conveyors (AREA)
- Treatment Of Sludge (AREA)
Abstract
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、貯溜された軟泥を移送し、か
つ、移送中に該軟泥に固化剤を均一に混合する軟泥の固
化処理圧送設備であって、移送装置と固化剤添加装置と
からなり、該移送装置は竪型スクリュコンベヤと該竪型
スクリュコンベヤの下流に配設した加圧ポンプと排送管
と該排送管途中に配設した流量計と圧縮空気注入用のエ
ゼクタとから構成され、該固化剤添加装置は固化剤サイ
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
から構成されたものである。また、第2の発明では、固
化剤添加装置の竪型スクリュコンベヤを300〜800
rpmの範囲で可変速としたものである。さらに、第3
の発明では、固化剤供給機として、可変速のロータリフ
ィーダを採用した。また、第4の発明では、固化剤添加
装置の竪型スクリュコンベヤの直下に逆止弁を配設して
固化剤の逆流を防止した構成とした。一方、第5の発明
では、貯溜された軟泥を効率よく吸い込むために、移送
装置の竪型スクリュコンベヤの吸込口前方に竪軸回りに
回転駆動された軟泥を攪拌流動化する攪拌装置を備え
た。In order to solve the above-mentioned problems, in the present invention, a solidification treatment of soft mud in which the stored soft mud is transferred and a solidifying agent is uniformly mixed with the soft mud during the transfer. A pumping facility comprising a transfer device and a solidifying agent adding device, the transfer device comprising a vertical screw conveyor, a pressure pump disposed downstream of the vertical screw conveyor, a discharge pipe, and the discharge pipe And a solidifying agent supplying device connected to the solidifying agent silo and an upstream side of the pressurizing pump subsequent to the solidifying agent silo, and a flowmeter and an ejector for injecting compressed air. It is composed of a vertical screw conveyor. Further, in the second invention, the vertical screw conveyor of the solidifying agent adding device is 300-800.
It is a variable speed in the range of rpm. Furthermore, the third
In the invention, a variable speed rotary feeder is adopted as the solidifying agent feeder. Further, in the fourth aspect of the invention, the check valve is arranged immediately below the vertical screw conveyor of the solidifying agent adding device to prevent the solidifying agent from flowing back. On the other hand, in the fifth aspect of the invention, in order to efficiently suck the stored soft mud, a stirrer is provided in front of the suction port of the vertical screw conveyor of the transfer device to stir and fluidize the soft mud rotationally driven around the vertical axis. .
【0005】[0005]
【作用】本発明においては、軟泥を埋立地などの移送場
所へ空気搬送する途中で加圧ポンプの直前から軟泥の流
量に応じて固化剤を適量添加し、加圧ポンプの通過時や
空気搬送中に排送管内の流動中に軟泥と混合攪拌され、
均一の混合状態となって目的地へ移送される。本発明に
おける固化剤添加装置は、通常は負圧状態の加圧ポンプ
の直前側に配設し、固化剤の移送泥土への混入を容易と
しているが、万一何らかの原因により加圧ポンプ直前が
正圧となり、供給中の固化剤が逆流するトラブルを防止
するため、竪型スクリュコンベヤを高速運転としたり、
あるいは固化剤サイロの下にエアシール機能を有する供
給機としてロータリフィーダを採用したり、また、逆止
弁を設けたりしている。また、第5の発明では、竪型ス
クリュコンベヤ下端の吸込口の前方に竪軸回りに回転す
る攪拌羽根を有する攪拌装置を備え、竪型スクリュコン
ベヤ吸込口周囲の軟泥の攪拌流動化を図るとともに、軟
泥中に混在する固結した大塊の泥土を切断細分化して竪
型スクリュコンベヤへの吸込みを容易にする。In the present invention, an appropriate amount of the solidifying agent is added immediately before the pressurizing pump according to the flow rate of the softener during the air transferring of the sludge to the transfer place such as a landfill, and when passing through the pressurizing pump or air conveying. It is mixed and stirred with the soft mud while flowing in the discharge pipe,
A uniform mixed state is transferred to the destination. The solidifying agent adding device in the present invention is usually arranged immediately before the negative pressure pressurizing pump to facilitate mixing of the solidifying agent into the transfer mud. In order to prevent the trouble that the positive pressure is generated and the solidifying agent flowing back flows, the vertical screw conveyor is operated at high speed,
Alternatively, a rotary feeder is used as a feeder having an air sealing function under the solidifying agent silo, and a check valve is provided. Further, in the fifth invention, a stirring device having a stirring blade that rotates around the vertical axis is provided in front of the suction port at the lower end of the vertical screw conveyor, and the stirring and fluidization of the soft mud around the vertical screw conveyor suction port is achieved. , Cutting and subdividing a large solidified mud mixed in soft mud to facilitate suction into a vertical screw conveyor.
【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は竪型スク
リュコンベヤの全体側面図、図3は図2のA−A視の側
面図、図4は図2のB−B視の平面図である。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、大別すると移送装置200と固化剤添加装置300
とから形成される。移送装置200は、土運船100や
その他の貯槽に貯えられた軟泥Mを取り込んだ後遠隔の
目的地へ移送するもので、竪型スクリュコンベヤ210
で取り込んだ軟泥Mを加圧ポンプ220で加圧し、流量
計230と逆止弁240を経由し、排送管250へ移送
し、排送管250の途中に設けたエゼクタ260により
コンプレッサ262で供給される圧縮エアを吹き込んで
プラグ輸送(栓輸送)により軟泥を空気搬送する。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 treatment pumping facility, FIG. 2 is an overall side view of the vertical screw conveyor, FIG. 3 is a side view taken along line AA of FIG. 2, and FIG. 4 is a plan view taken along line BB of FIG. It is a figure. As shown in FIG. 1, the soft mud solidification treatment pumping equipment 1000 of the present invention is roughly divided into a transfer device 200 and a solidifying agent addition device 300.
Formed from. The transfer device 200 takes in the soft mud M stored in the earth carrier 100 and other storage tanks and transfers it to a remote destination, and the vertical screw conveyor 210.
The soft mud M taken in is pressurized by the pressure pump 220, transferred to the discharge pipe 250 via the flow meter 230 and the check valve 240, and supplied by the compressor 262 by the ejector 260 provided in the middle of the discharge pipe 250. The compressed sludge is blown in and the sludge is transported by plug transport (plug transport).
【0007】一方、固化剤添加装置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。固化剤添加装置300を加圧ポン
プ220直前の排送管250へ接続した理由は、加圧ポ
ンプ220の直前は通常加圧ポンプ220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25
0内へ吸引して軟泥M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250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250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330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800r
pm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、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
きるロータリフィーダを採用した。On the other hand, the solidifying agent adding 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 adding device 300 is connected to the discharge pipe 250 immediately before the pressurizing pump 220 is that the normal pressurizing pump 220 is always in a negative pressure state immediately before the pressurizing pump 220, so that the solidifying agent is smoothed. To the discharge pipe 25
This is because the soft mud M can be mixed into the soft mud M without causing any trouble. However, due to some unforeseen circumstances during operation, a positive pressure (plus pressure) is also applied to the discharge pipe 250 immediately before the pressurizing pump.
In this case, the solidifying agent to be added flows backward to cause a trouble of hindering smooth supply. As a measure to prevent 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 250 even in a slight positive pressure state as a transfer means. A vertical screw conveyor 330 that can be transferred is used. The vertical screw conveyor 330 strongly moves the solidifying agent downward without 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.
This is because pm does not change the backflow prevention effect even if the speed is higher than the actually generated plus pressure. The solidifying agent feeder 320 may be of any type such as a table feeder, a piston feeder or a belt feeder as long as it can quantitatively supply the powdery solidifying agent. It should be noted that the rotary feeder, which has a simple structure and is compact, can supply an arbitrary fixed amount, and can be transferred and supplied in an airlock state, is adopted.
【0008】また、軟泥Mの流量を検出する流量計23
0の検出信号を受信する制御装置400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400で演算したうえ、固化剤供給機320
の駆動装置320aに操作指令を発信して適正な量の固
化剤を供給させ、加圧ポンプ220の直前へ導き加圧ポ
ンプ220の負圧吸引力により軟泥Mへ混入させる。A flow meter 23 for detecting the flow rate of the soft mud M.
The control device 400 that receives a detection signal of 0 stores in advance the set value of the supply amount of the solidifying agent that is adapted to the soft mud flow rate, and the controller 400 sets the solidifying agent supply amount that is compatible with the actual measured value of the soft mud flow rate during operation. After calculating, solidifying agent supply machine 320
An operation command is sent to the driving device 320a of FIG. 2 to supply an appropriate amount of the solidifying agent, which is introduced immediately before the pressure pump 220 and mixed into the soft mud M by the negative pressure suction force of the pressure pump 220.
【0009】一方、本発明の実施例における竪型スクリ
ュコンベヤ210は、図2〜図4に示すように、垂直な
円筒状のケーシング211内にケーシング211と同芯
状に周囲に螺旋状のスクリュ羽根213を取り付けた回
転軸212を上下端の軸受を介して回転自在に軸承し、
頂上の油圧モータ212aで可変速に回転駆動され、下
部側面に設けた開口である吸込口214より取り込んだ
軟泥を排出口215より吐出し、前述したように加圧ポ
ンプ220へ移送して加圧する。スクリュ回転数は40
0〜1200rpmで可変とする。竪型スクリュコンベ
ヤ210における吸込口214の回りの軟泥を攪拌・流
動して吸込口214への移送を円滑・容易にする目的
で、吸込口214の前方には攪拌装置216を配設す
る。On the other hand, in the vertical screw conveyor 210 according to the embodiment of the present invention, as shown in FIGS. 2 to 4, a vertical cylindrical casing 211 is concentric with the casing 211 and has a spiral screw around the periphery thereof. The rotary shaft 212 to which the blades 213 are attached is rotatably supported via bearings at the upper and lower ends,
It is rotatably driven at a variable speed by the hydraulic motor 212a at the top, and the soft mud taken in from the suction port 214 which is an opening provided in the lower side surface is discharged from the discharge port 215 and transferred to the pressure pump 220 to be pressurized as described above. . Screw speed is 40
Variable from 0 to 1200 rpm. A stirrer 216 is provided in front of the suction port 214 in order to stir and flow the soft mud around the suction port 214 in the vertical screw conveyor 210 to facilitate and facilitate the transfer to the suction port 214.
【0010】攪拌装置216は、ケーシング211の上
下2個所より水平に張り出したサポート216a、21
6bの先端に配設した軸受217b、217cに軸承さ
れた垂直の攪拌軸217に取り付けた上下一対の攪拌羽
根218(218a、218b)を油圧ポンプ217a
を介して可変速に回転駆動するよう構成される。攪拌装
置216は吸込口214の前方1個所に設置されるほ
か、図4に示すように、吸込口214の前方と左右にそ
れぞれ1個所合計3個所設置される。攪拌羽根218
は、攪拌軸217より水平に複数本(図2〜図4の例で
は4本)のアームの先端をほぼ直角に上方または下方へ
屈曲させ、その外側に略等間隔で複数個の突起を配設し
たもので、突起の先端は鋭利な刃物状に形成される。3
個所の攪拌装置216を有するタイプにおいては、中央
の攪拌装置216のみ上下の攪拌羽根218a、218
bを備え、左右の攪拌装置216は下方の攪拌羽根21
8bのみを備えたものも採用され、浚渫現場で直接本設
備1000により浚渫し移送する場合に使用され、特に
攪拌による水質汚濁を嫌う場合に好適である。勿論この
ような惧れのない貯槽内の軟泥を処理する装置では、左
右の攪拌装置216も上下一対の攪拌羽根218a、2
18bをともに備えたものを採用し得る。図2〜図4に
示した攪拌装置216は、いずれも駆動は各々頂部に備
えた油圧モータ217aで回転駆動するようになってお
り、回転方向や回転速度もそれぞれ独立に自由に選定で
きるメリットがある。一方、他の駆動方式として、3個
所の攪拌装置216のうち中央の攪拌装置216を油圧
モータ212aで駆動し、両側の攪拌装置216はスプ
ロケットを介してチェン駆動するタイプのものもある。
このタイプは回転方向や回転速度をそれぞれ独立に設定
できないが、駆動装置コストの低減を図ることができ
る。攪拌装置216の攪拌軸217の回転数は通常5〜
50rpmの可変速とし、軟泥の粘度や含有水分(含水
率)の程度に応じて回転数を増減する。流量計230
は、流れ方向に垂直に磁界を加えて軟泥の通過量の大小
にしたがって誘起される起電力を測定する原理の電磁流
量計が採用されるが、その他の流量計を使用してもよ
い。The stirrer 216 includes supports 216a, 21 extending horizontally from the upper and lower portions of the casing 211.
A pair of upper and lower stirring blades 218 (218a, 218b) attached to a vertical stirring shaft 217 supported by bearings 217b and 217c arranged at the tip of the hydraulic pump 217a.
It is configured to be rotationally driven at a variable speed via. The stirrer 216 is installed at one position in front of the suction port 214, and as shown in FIG. Stirring blade 218
Bends the ends of a plurality of arms (four in the example of FIGS. 2 to 4) horizontally from the stirring shaft 217 upward or downward at a substantially right angle, and arranges a plurality of protrusions on the outside at substantially equal intervals. It is provided, and the tip of the protrusion is formed into a sharp blade shape. Three
In the type having the stirring device 216 at the part, only the stirring device 216 at the center has upper and lower stirring blades 218a and 218.
b, and the left and right stirring devices 216 are provided on the lower stirring blades 21.
The one provided with only 8b is also used, and it is used when the equipment 1000 directly dredges and transfers it at the dredging site, and is particularly suitable when water pollution due to stirring is disliked. Of course, in such a device for treating soft mud in a storage tank without fear, the left and right stirring devices 216 also include a pair of upper and lower stirring blades 218a, 2a.
One provided with both 18b may be adopted. All of the stirring devices 216 shown in FIGS. 2 to 4 are driven to rotate by a hydraulic motor 217a provided at the top, and there is a merit that the rotation direction and the rotation speed can be freely selected independently. is there. On the other hand, as another driving method, there is also a type in which the central stirring device 216 among the three stirring devices 216 is driven by the hydraulic motor 212a, and the stirring devices 216 on both sides are chain-driven via sprockets.
In this type, the rotation direction and the rotation speed cannot be set independently, but the drive device cost can be reduced. The rotation speed of the stirring shaft 217 of the stirring device 216 is usually 5 to 5.
The speed is variable at 50 rpm, and the number of rotations is increased / decreased according to the viscosity of the soft mud and the degree of water content (water content). Flow meter 230
The electromagnetic flowmeter of the principle of measuring the electromotive force induced by applying a magnetic field perpendicular to the flow direction according to the size of the amount of the soft mud passing is used, but other flowmeters may be used.
【0011】一方、固化剤添加装置300は、前述した
ように、竪型スクリュコンベア210の排出口215と
加圧ポンプ220との間の排送管250に接続され、排
送管250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310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3
20は、例えば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230
で計測した軟泥の実際流量に応じて駆動装置320a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にミキサ(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排
出する。固化剤は軟泥1m3 に対して、50〜200k
g(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250内を空気搬送され
る軟泥に固化剤を加圧ポンプ220の負圧を利用して加
圧ポンプ220の直前から導入し、加圧ポンプ220の
羽根の回転により軟泥と十分混練したうえ軟泥流量に見
合った量だけ粉体または水分を添加混合したスラリを供
給するため、プラグ輸送中の軟泥に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kgf/cm
2 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250の長さは少なくとも50mは必要とさ
れる。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、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、固化剤添加装置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で加圧ポンプ220の直前へ移送
されるから負圧状態の排送管250内へ円滑に導入され
るばかりでなく、排送管内に何らかの原因でプラス圧が
発生しても、竪型スクリュコンベヤ330を300rp
m以上の高速としたり、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、竪型スク
リュコンベヤ330の直下に逆止弁340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 adding device 300 is connected to the discharge pipe 250 between the discharge port 215 of the vertical screw conveyor 210 and the pressurizing pump 220 as described above, and the discharge pipe 250 is being transferred. The solidifying agent corresponding to the flow rate is supplied to the soft mud. The solidifying agent silo 310 contains powder such as cement or cement-based solidifying agent, and the solidifying agent feeder 3
20 is, for example, a rotary feeder or a table feeder,
Flow meter 230 using a feeder such as a piston feeder
The drive device 320a is controlled in accordance with the actual flow rate of the soft mud measured in 1. to adjust the supply amount. The solidifying agent may be in the form of powder, or a slurry with water added,
The choice is determined by the degree of soil mix. 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 as a powder, the solidifying agent supplied in a fixed amount by the solidifying agent feeder 320 is 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, a solidifying agent supply device 320 is provided with a storage tank equipped with a mixer (mixing stirrer), and a water supply line is connected thereto to make powdery solidifying agent into a slurry, which is then discharged by a piston pump. To the solidifying agent ooze 1m 3, 50~200k
g (usually 100 kg). In the present invention, as described above, the solidifying agent is introduced from immediately before the pressurizing pump 220 by using the negative pressure of the pressurizing pump 220 into the soft sludge that is pneumatically conveyed in the discharge pipe 250. By rotating the blades, the slurry is mixed well with the soft mud and the powder or water is added in an amount commensurate with the flow rate of the soft mud to supply the slurry, so that it is evenly mixed with the soft mud during plug transport to a remote destination. After reaching, after a certain period of time (usually 2 to 7 days), it solidifies beyond the required strength. In other words, the amount of solidifying agent added depends on the type of mud soil and how many kgf / cm
Determine the addition amount depending on whether you want the strength of 2 . As a matter of course, the larger the added amount, the faster and harder the solidified. As described above, since the uniform mixing of the soft mud and the solidifying agent in the present invention is efficiently performed during the plug transportation in the discharge pipe, the length of the discharge pipe 250 is required to be at least 50 m. It is also possible to directly equip the dredger with the equipment of the present invention, dredge soft mud such as sludge on the sea floor, perform solidification treatment, and transport to a distant destination. The feature of the present invention is that mixing of the solidifying agent and the soft mud has one-stage mixing by rotation of the pressure pump and two-stage mixing by repeated operation of plug generation to destruction in plug transportation in the discharge pipe. This is that the stirring is sufficiently performed and the homogeneity (kneading degree) is very high. Further, in the present invention, as the solidifying agent adding device 300, the solidifying agent supplied from the solidifying agent silo 310 is transferred to the vertical screw conveyor 330 immediately before the pressurizing pump 220. The vertical screw conveyor 330 can be installed at 300 rp even if a positive pressure is generated in the discharge pipe for some reason.
It is possible to prevent the backflow of the solidifying agent by increasing the speed to m or more, using the solidifying agent feeder 320 as a rotary feeder having an air-sealing function, or providing a check valve 340 directly below the vertical screw conveyor 330. Therefore, the backflow trouble can be avoided.
【0012】[0012]
【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、移送、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、固化剤添加装置は、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, in the solidification treatment pressure-feeding facility of the present invention, mud feeding, transfer, solidifying agent feeding, kneading, and discharging are automatically performed in a continuous operation. As described above, since a solidifying and kneading step is not required separately, an efficient and uniform mixed and solidified softened sludge 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. Moreover, since the solidifying agent adding 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竪型スクリュコンベヤの
全体側面図である。FIG. 2 is an overall side view of a vertical screw conveyor according to an embodiment of the present invention.
【図3】図2のA−A視の側面図である。FIG. 3 is a side view taken along the line AA of FIG.
【図4】図2のB−B視の平面図である。FIG. 4 is a plan view taken along the line BB of FIG.
100 土運船 200 移送装置 210 竪型スクリュコンベヤ 211 ケーシング 212 回転軸 212a 油圧モータ 213 スクリュ羽根 214 吸込口 215 排出口 216 攪拌装置 216a サポート 216b サポート 217 攪拌軸 217a 油圧モータ 217b 軸受 217c 軸受 218 攪拌羽根 218a 攪拌羽根(上) 218b 攪拌羽根(下) 219 固定羽根 220 加圧ポンプ 220a 油圧モータ 230 流量計 240 逆止弁 250 排送管 260 エゼクタ 262 コンプレッサ 300 固化剤添加装置 310 固化剤サイロ 320 固化剤供給機(ロータリフィーダ) 320a 駆動装置 330 竪型スクリュコンベヤ 340 逆止弁 400 制御装置 1000 固化処理圧送設備 100 earth carrier 200 transfer device 210 vertical screw conveyor 211 casing 212 rotary shaft 212a hydraulic motor 213 screw blade 214 suction port 215 discharge port 216 stirring device 216a support 216b support 217 stirring shaft 217a hydraulic motor 217b bearing 217c bearing 218 stirring blade 218a Stirring blade (upper) 218b Stirring blade (lower) 219 Fixed blade 220 Pressurizing pump 220a Hydraulic motor 230 Flowmeter 240 Check valve 250 Discharge pipe 260 Ejector 262 Compressor 300 Solidifying agent addition device 310 Solidifying agent silo 320 Solidifying agent feeder (Rotary feeder) 320a Drive device 330 Vertical screw conveyor 340 Check valve 400 Control device 1000 Solidification processing pumping facility
Claims (5)
に該軟泥に固化剤を均一に混合する軟泥の固化処理圧送
設備であって、移送装置と固化剤添加装置とからなり、
該移送装置は竪型スクリュコンベヤと該竪型スクリュコ
ンベヤの下流に配設した加圧ポンプと排送管と該排送管
途中に配設した流量計と圧縮空気注入用のエゼクタとか
ら構成され、該固化剤添加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 sludge solidification treatment pressure-feeding facility for transporting stored soft sludge and uniformly mixing a solidifying agent with the soft sludge during transport, comprising a transport device and a solidifying agent adding device.
The transfer device is composed of a vertical screw conveyor, a pressure pump arranged downstream of the vertical screw conveyor, a discharge pipe, a flow meter arranged in the middle of the discharge pipe, and an ejector for injecting compressed air. A solidification processing pressure-feeding facility for soft mud, wherein the solidification agent addition device is composed of a solidification agent silo, a solidification agent feeder that is connected to the solidification agent silo and is connected to the upstream side of the pressure pump, and a vertical screw conveyor.
を300〜800rpmの範囲で可変速とする請求項1
記載の軟泥の固化処理圧送設備。2. The vertical screw conveyor of the solidifying agent adding device has a variable speed in the range of 300 to 800 rpm.
Equipment for solidification treatment and pumping of soft mud as described.
ダとする請求項1または請求項2記載の軟泥の固化処理
圧送設備。3. The solidification processing pressure-feeding facility for soft mud according to claim 1 or 2, wherein the solidifying agent feeder is a variable speed rotary feeder.
の直下に逆止弁を付設した請求項1または請求項2また
は請求項3記載の軟泥の固化処理圧送設備。4. The soft mud solidification treatment pressure-feeding facility according to claim 1, 2 or 3, wherein a check valve is provided directly below the vertical screw conveyor of the solidifying agent addition device.
口前方に竪軸回りに回転駆動された軟泥を攪拌流動化す
る攪拌装置を備えた請求項3または請求項4記載の軟泥
の固化処理圧送設備。5. The softening treatment pressure feeding of soft mud according to claim 3 or 4, further comprising a stirrer in front of the suction port of the vertical screw conveyor of the transfer device for stirring and fluidizing the soft mud which is rotationally driven about the vertical axis. Facility.
Priority Applications (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP20972894A JPH0871595A (en) | 1994-09-02 | 1994-09-02 | Solidification treatment and pressure feed equipment for soft mud |
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 |
---|---|---|---|
JP20972894A JPH0871595A (en) | 1994-09-02 | 1994-09-02 | Solidification treatment and pressure feed equipment for soft mud |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0871595A true JPH0871595A (en) | 1996-03-19 |
Family
ID=16577661
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP20972894A Pending JPH0871595A (en) | 1994-09-02 | 1994-09-02 | Solidification treatment and pressure feed equipment for soft mud |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0871595A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014525820A (en) * | 2011-05-23 | 2014-10-02 | ナノシル エス.エー. | Equipment and methods for functionalization of granular and powdered products |
-
1994
- 1994-09-02 JP JP20972894A patent/JPH0871595A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2014525820A (en) * | 2011-05-23 | 2014-10-02 | ナノシル エス.エー. | Equipment and methods for functionalization of granular and powdered products |
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