JPH0613159B2 - Sludge treatment method - Google Patents

Sludge treatment method

Info

Publication number
JPH0613159B2
JPH0613159B2 JP61260291A JP26029186A JPH0613159B2 JP H0613159 B2 JPH0613159 B2 JP H0613159B2 JP 61260291 A JP61260291 A JP 61260291A JP 26029186 A JP26029186 A JP 26029186A JP H0613159 B2 JPH0613159 B2 JP H0613159B2
Authority
JP
Japan
Prior art keywords
sludge
dehydration
screw
pressure
screw shaft
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
JP61260291A
Other languages
Japanese (ja)
Other versions
JPS63111910A (en
Inventor
文之 立松
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
MARIN KK
Original Assignee
MARIN KK
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 MARIN KK filed Critical MARIN KK
Priority to JP61260291A priority Critical patent/JPH0613159B2/en
Publication of JPS63111910A publication Critical patent/JPS63111910A/en
Publication of JPH0613159B2 publication Critical patent/JPH0613159B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は、横長い直円筒形状の全長にわたり脱水孔を開
設してなる濾過部内部を脱水処理域となし、先ず、汚泥
等を濾過部前部の脱水部へ汚泥等圧送部を介し凝集フロ
ック状にして軸芯方向に向けて圧送して充満させ、該充
満圧で半脱水状態とした後、スクリューシャフトを回動
せしめて排出口側へ圧送して、初期充満度を増すことに
より濾過部全長にわたって脱水処理を可能とし、凝集フ
ロックを効率良く供給して脱水効率、処理量の向上に資
すべくなす汚泥等の処理方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial field of application] The present invention defines a dehydration treatment area inside a filtration section having a dehydration hole formed over the entire length of a horizontally long right circular cylinder, and first, sludge and the like are filtered. To the front dewatering section through a sludge etc. feeding section, make a flocculated floc shape and feed it toward the axial center direction to fill it, and after half filling with the filling pressure, rotate the screw shaft and discharge side The present invention relates to a method for treating sludge or the like, which enables the dehydration treatment over the entire length of the filtration section by pumping to increase the initial filling degree and efficiently supplies coagulated flocs to contribute to the improvement of the dehydration efficiency and the treatment amount.

[従来の技術] 従来は、汚泥等の脱水処理を行なうため使用されていた
連続圧搾機は、横設した円筒形状の濾過部の前部へ軸芯
と直交した上側に、該汚泥等を投入しうべきホッパを全
長の約20%強の長さで開設しているものが一般的であっ
たため、該ホッパが占める開口部分へは濾過のための脱
水孔を穿設しえず、よって、該ホッパ下側の濾過部の他
周壁部分には脱水孔が穿設されてはいるも、汚泥等は該
脱水孔に自重で接しているに過ぎないので、重力濾過し
かできず、含有する水分を有効に絞り出す力がなく、従
って濾過部を相当長いものとしても、前記ホッパが占め
る長さの部分は脱水効率の低いものとなっていて、その
分連続圧搾機全体を過大なものとしなければならない等
の不具合があった。
[Prior Art] Conventionally, a continuous squeezing machine that has been used to dehydrate sludge or the like throws the sludge or the like on the front side of a horizontally installed cylindrical filtration unit at an upper side orthogonal to the axis. Since it was general that the hopper to be sewn was opened with a length of about 20% or more of the total length, a dehydration hole for filtration cannot be formed in the opening portion occupied by the hopper, therefore, Although a dehydration hole is formed in the other peripheral wall portion of the filtration section under the hopper, sludge and the like are only in contact with the dehydration hole by their own weight, so that only gravity filtration is possible and the moisture content is reduced. There is no effective squeezing force, and therefore, even if the filter section is considerably long, the portion occupied by the hopper has a low dehydration efficiency, and the continuous squeezing machine as a whole must be oversized accordingly. There was a problem such as not becoming.

さらに、前記ホッパタイプにあっては、ホッパをシュー
トとして凝集混和槽で処理されてなる凝集フロックが落
し込んで供給されるので、スクリューシャフトの胴部に
衝突して壊れる。よって、壊れないようにするために、
多量の凝集剤を必要とするが、多量の凝集剤を含んだ凝
集フロックは、粘性が出て濾過部の金鋼等のパンチング
部の目詰りとなって、処理量の低下や含水率の悪いもの
となり、また、液面制御を行なうために、ホッパに電極
等を取付けて液面を測定しているが、汚泥通過部分に設
けるから、どうしても動作不良を起こしたり、該電極棒
が破損してスクリュー内へ移送されてパンチング等を破
壊する欠点を有している。
Further, in the hopper type, since the floc flocs processed by the flocculation and mixing tank using the hopper as the chute is dropped and supplied, the flocs collide with the body of the screw shaft and are broken. Therefore, in order not to break it,
A large amount of flocculant is required, but flocculation flocs containing a large amount of flocculant become viscous and clog the punching part such as gold steel in the filtering part, resulting in a decrease in treatment amount and poor water content. In addition, in order to control the liquid level, electrodes are attached to the hopper to measure the liquid level.However, since it is provided in the sludge passage part, malfunctions are inevitable and the electrode rod is damaged. It has the drawback of being transferred into the screw and destroying punching and the like.

[発明が解決しようとする問題点] そこで本発明は、上記従来技術による連続圧搾機が濾過
部の前部へ軸芯と直交した上側に全長の約20%強長を開
設したホッパを設けていたため、その開口部分へは脱水
孔を穿設しえず、かつ、該ホッパ下側は脱水孔を穿設し
てあるも、重力のみで供給される汚泥等は、充満圧が低
くて良好な脱水効果を生ずる圧力で脱水孔に接すること
ができないから、有効な充満圧となる初期充満点が排出
側に寄り、所望含水率のケーキを生成するためにはその
分濾過部を長くする必要があったものを初期充満点を最
前部に配設しうべくなして、連続圧搾機を小型化可能と
したり、さらには、スクリューシャフトと直角方向より
圧入すると、凝集フロックは該スクリューシャフトに衝
突して、該凝集フロックが壊れるために、密閉の凝集混
和槽で凝集された凝集フロックを、汚泥ポンプ圧を低圧
でスクリュー面に乗るように軸芯方向よりスクリュー内
へ圧入して、該凝集フロックが壊れることがないように
する汚泥等の処理方法を提供することを目的とするもの
である。
[Problems to be Solved by the Invention] Therefore, according to the present invention, the continuous squeezing machine according to the above-mentioned conventional art is provided with a hopper having a length of about 20% or more of the total length on the upper side orthogonal to the axial center to the front part of the filtering part. Therefore, the dehydration hole cannot be formed in the opening portion, and the dehydration hole is formed in the lower side of the hopper, but sludge and the like supplied only by gravity has a low filling pressure and is preferable. Since it is not possible to contact the dehydration hole with a pressure that produces a dehydration effect, the initial filling point, which is an effective filling pressure, is closer to the discharge side, and in order to produce a cake with a desired water content, it is necessary to lengthen the filtration part accordingly. If there is an existing filling point at the forefront, it is possible to downsize the continuous squeezing machine, and further, if it is pressed in from the direction perpendicular to the screw shaft, the flocculation flocs collide with the screw shaft. Because the floc flocs break , Sludge to prevent the flocculation flocs aggregated in the closed flocculation mixing tank from being pushed into the screw from the axial direction so that the sludge pump pressure is applied to the screw surface at a low pressure so that the flocculation flocs are not broken. The object of the present invention is to provide a processing method of.

[問題点を解決するための手段] すなわち本発明は、横長い直円筒形状で全長にわたり脱
水孔を開設し、前端部に側壁を後端部にケーキ排出口を
設け、かつ、金鋼を内設してなる濾過部へ、前端部から
後端部に向けて大径となるテーパ状の胴部にスパイラル
状のスクリュー羽根を備えたスクリューシャフトを回動
自在に枢設することにより該濾過部の全長にわたり脱水
処理域を形成し、かつ、前記前端部の側壁に軸芯方向に
向けて供給口を開設して凝集混和槽や撹拌機等よりなる
汚泥等圧送部を連結し、該汚泥等圧送部よりの凝集フロ
ック状の汚泥を先ずスクリュー羽根前端の脱水処理域前
部へ圧送して、該スクリュー羽根のリード方向に沿うべ
くこれの軸芯方向に圧送することにより、該スクリュー
羽根上へ凝集フロック状に保持したまま載置状に供給し
て順次充満せしめて該充満圧で半脱水状態として後、該
スクリューシャフトを回動せしめ前記脱水処理域で脱水
し、ついで前記脱水処理域前部を介して順次該回動のス
クリューシャフトでなる該脱水処理域で脱水しつつ排出
口側へ圧送して該排出口よりケーキを押し出すことを特
徴とする汚泥等の処理方法である。
[Means for Solving the Problems] That is, according to the present invention, a dehydration hole having a horizontally long right cylindrical shape is formed over the entire length, a side wall is provided at a front end portion and a cake discharge port is provided at a rear end portion, and gold steel is provided inside. A screw shaft having spiral screw blades is rotatably pivoted on a tapered barrel having a large diameter from the front end toward the rear end, and the filter is provided to the filter. Forming a dewatering area over the entire length of the front end, and opening a supply port toward the axial direction on the side wall of the front end to connect a sludge equalizing pumping section composed of a coagulation mixing tank, a stirrer, etc. The flocculated sludge sludge from the pumping unit is first pumped to the front part of the dehydration treatment zone at the front end of the screw blade and then to the axial direction of the screw blade so as to follow the lead direction of the screw blade. While holding in the form of floc After being supplied in a stationary state and sequentially filled up to a semi-dewatering state at the filling pressure, the screw shaft is rotated to dehydrate in the dehydration treatment area, and then the rotation is sequentially performed through the front portion of the dehydration treatment area. The method for treating sludge or the like is characterized in that the cake is extruded from the discharge port by being pumped to the discharge port side while being dehydrated in the dehydration treatment area consisting of the screw shaft.

なお、本発明でいう脱水処理域(以下単に処理域とのみ
いう)とは、濾過部内側とスクリューシャフト間に形成
される空間をいう。
The dehydration treatment area (hereinafter, simply referred to as a treatment area) in the present invention means a space formed between the inner side of the filtration section and the screw shaft.

[作用] 上記手段により構成される本発明は、濾過部前部の側壁
に、スクリューシャフトのスラスト軸受がこれの中心部
に設けられ、これの上部に軸芯方向に向けて供給口を開
口し、該供給口は汚泥等を圧送しうべきポンプを経て、
該汚泥等の凝集混和槽と凝集混和剤槽等よりなる汚泥等
圧送部に連結されているから、凝集混和槽へ汚泥等を満
たし、これに適量の凝集混和剤が混合されるよう調整し
てポンプを運転させるならば、適量の凝集混和剤が混じ
った汚泥等が凝集混和槽に注入され凝集混和槽攪拌機に
よって、凝集混和された凝集フロックが加圧されて供給
口より軸芯方向に向け、スクリュー面に乗るようにして
スクリュー羽根前端の脱水部前部へ略0.1〜0.2kg
/cm2の汚泥ポンプ圧で圧送されるので、この供給によ
って、凝集フロックが壊れることがない。
[Operation] According to the present invention constituted by the above means, the thrust bearing of the screw shaft is provided in the central portion of the side wall of the front portion of the filtering portion, and the supply port is opened in the upper portion thereof in the axial direction. , The supply port is via a pump that should pump sludge,
Since it is connected to a sludge equalizing pumping section comprising an aggregating and mixing tank for the sludge and an aggregating admixture tank, the aggregating and admixing tank is filled with sludge and the like, and an appropriate amount of the aggregating admixture is mixed and adjusted. If the pump is operated, sludge containing an appropriate amount of coagulant admixture is injected into the coagulation and mixing tank, and the coagulation and mixing tank agitator pressurizes the coagulated and mixed floc to direct it from the supply port toward the axial direction. Approximately 0.1 to 0.2 kg to the front part of the dehydration section at the front end of the screw blade so that it rides on the screw surface.
Since it is pumped at a sludge pump pressure of / cm 2 , this supply does not break the floc.

このときはまだ、スクリューシャフトは回動させていな
いので、圧送された汚泥等による該凝集フロックは該脱
水部前部へ次第に充満して、充満圧力が高まって含有水
分がこの部分の濾過部で絞り出され、かつ、脱水孔を通
って摘下する水量が増加してくる。このタイミングを見
はからいスクリューシャフトを回動させると、半脱水状
態の汚泥等はさらに処理域内で圧搾脱水されつつ排出口
側へ圧送され、完全なケーキとなって排出口から押出さ
れる。
At this time, since the screw shaft has not been rotated yet, the flocculated flocs due to the sludge or the like that has been pressure-fed gradually fills the front part of the dehydration section, and the filling pressure increases, so that the water content in the filtration section of this section increases. The amount of water that is squeezed out and removed through the dehydration hole increases. When the screw shaft is turned to avoid this timing, the semi-dehydrated sludge and the like is further squeezed and dehydrated in the treatment area while being pressure-fed to the discharge port side to be a complete cake and extruded from the discharge port.

さらに前記した処理域内へは前記脱水部前部を介し連続
して新しい汚泥等が圧送されるので、上記脱水処理は連
続して実施されることとなり、よって処理域前部におい
て既に圧力をもって充満し半脱水状態となるから、濾過
部の全長が有効に脱水のため利用されて適切な含水率と
なり、従って濾過部を長くして濾過面積を増大させる
か、または、汚泥等の滞留時間を延長したのと同様の効
果となるので、連続圧搾機を小型化することが可能とな
る。
Further, since new sludge and the like are continuously pumped into the treatment area through the front portion of the dehydration section, the dehydration treatment is continuously carried out, so that the front portion of the treatment area is already filled with pressure. Since it is in a semi-dewatered state, the entire length of the filtration section is effectively used for dehydration and an appropriate water content is obtained, so the filtration section is lengthened to increase the filtration area or the retention time of sludge etc. is extended. Since the same effect as described above is obtained, it is possible to reduce the size of the continuous pressing machine.

[実施例] 以下引き続き本発明の要旨をさらに明確にするため、図
面を利用して、一実施例を説明する。
[Embodiment] An embodiment will be described below with reference to the drawings in order to further clarify the gist of the present invention.

第1図において連続圧搾機Aは、脱水部1と汚泥等圧送
部2(以下単に圧送部とのみいう)とよりなり、脱水部
1はパンチングプレートで全長にわたる全周面に小径の
脱水孔111aを無数に穿設されてなる直円筒形状の円筒
部111と、該円筒部111の内側に張りつけられている金鋼
112とでなる濾過部11とこれの前端部に汚泥等の供給口1
21を軸芯に向けて開設し、かつ、スクリューシャフト13
のスラスト軸受122を備えて該濾過部11を閉じる側壁12
と、該スラスト軸受122に軸前部13aを枢支して、前部
から後部に向けて大径となるテーパ状の胴部131に、前
記金鋼112内側に沿って回動しうべくスパイラル状に設
けられたスクリュー羽根132とよりなるスクリューシャ
フト13及び出口側スタンド14(以下単にスタンドとのみ
いう)よりなる。
In FIG. 1, a continuous pressing machine A comprises a dewatering section 1 and a sludge equal pressure feeding section 2 (hereinafter simply referred to as a pressure feeding section). The dewatering section 1 is a punching plate and has a small diameter dewatering hole 111a on the entire circumferential surface. A cylindrical portion 111 in the shape of a right circular cylinder formed by innumerable holes, and gold steel attached inside the cylindrical portion 111.
112 is a filtration unit 11 and a supply port 1 for sludge or the like at the front end of the filtration unit 11.
Open 21 toward the axis and screw shaft 13
Side wall 12 which is provided with a thrust bearing 122 and closes the filtering portion 11.
The shaft front portion 13a is pivotally supported on the thrust bearing 122, and the spiral body portion 131 having a tapered shape having a large diameter from the front portion toward the rear portion is rotated along the inside of the gold steel 112. It comprises a screw shaft 13 and a stand 14 on the outlet side (hereinafter, simply referred to as a stand).

また、スタンド14は立置された中空の柱状で、その一側
壁部に濾過部11後部の排出口113から排出されるケーキ
を該スタンド14内へ落すために、濾過部と略同径の円孔
141が開設され、該円孔141端縁近傍で濾過部11の後部を
支承しており、また、該円孔141が開設されている対時
側壁部で、かつ、該円孔141と同心にスクリューシャフ
ト13の軸後部13bを挿通枢支すべく軸受142が設けてあ
り、さらに、排出される被脱水汚泥等の脱水度を調整し
て所望のケーキを生成させるスクレーパ143と、これを
操作して該スクレーパ143を軸芯方向へ作動しうべくな
した操作部144が設けられていて、かつ、軸後部13bは
軸受142を挿通してさらに延長され、後端近傍で図示し
ない駆動源から駆動されるようスプロケット等133が固
着してあり、後端部は軸受145で枢支され、濾過部11が
水平となるよう据え付けられている。
In addition, the stand 14 is an upright hollow pillar, and has a side wall of a circle having substantially the same diameter as that of the filtering part in order to drop the cake discharged from the discharge port 113 at the rear of the filtering part 11 into the stand 14. Hole
141 is provided, supports the rear part of the filtering section 11 near the edge of the circular hole 141, and is a side wall portion at the time when the circular hole 141 is opened and concentric with the circular hole 141. A bearing 142 is provided to pivotally support the shaft rear portion 13b of the screw shaft 13, and further, a scraper 143 for adjusting a dehydration degree of discharged sludge to be dehydrated to generate a desired cake, and a scraper 143 for operating the scraper. Is provided with an operating portion 144 for operating the scraper 143 in the axial direction, and the shaft rear portion 13b is further extended by inserting the bearing 142, and is driven from a drive source (not shown) near the rear end. As described above, a sprocket or the like 133 is fixed, the rear end portion is pivotally supported by a bearing 145, and the filtration portion 11 is installed so as to be horizontal.

さらに、圧送部2は、凝集混和槽21と圧力センサー22と
を、脱水部1の側壁12上部に直交して開設されている供
給口121へ結ぶ圧送管23及び図示しない汚泥等の給泥ポ
ンプと凝集混和剤を貯蔵し適宜に供給しうべくなした混
和剤槽と凝集混和槽攪拌機24とよりなる。
Further, the pressure feeding unit 2 connects the coagulation / mixing tank 21 and the pressure sensor 22 to a feed port 121 opened orthogonally to the upper portion of the side wall 12 of the dewatering unit 1 and a mud feed pump such as sludge (not shown). And a coagulant-mixing tank agitator 24 for storing the coagulant-mixing agent and appropriately supplying it.

なお、圧力センサー22は、処理域S内の汚泥等の圧力を
検知して図示しない給泥ポンプへ伝え、給泥ポンプの出
力を加減して常に最適圧力で汚泥等を圧送しうべくなす
ものである。
The pressure sensor 22 detects the pressure of sludge or the like in the treatment area S and transmits it to a sludge supply pump (not shown), and adjusts the output of the sludge supply pump to constantly send the sludge or the like at an optimum pressure. Is.

続けて、本実施例における作用について説明すれば、図
示しない汚泥等の投入槽へ充たされた汚泥等は給泥ポン
プを運転することにより、図示しない混和剤槽から適量
添加される凝集混和剤を混入しつつ凝集混和槽21を通
り、凝集混和槽攪拌機24によって、凝集混和されて該ス
クリューシャフト13の軸芯に沿って配設の圧送管23を通
って供給口121から低圧でスクリュー面に乗るように処
理域Sの前部内へ圧送される。
Continuing, the operation of the present embodiment will be described. Sludge and the like filled in a tank for sludge not shown is operated by a mud feed pump to add an appropriate amount of coagulant admixture from an admixture tank not shown. Through the aggregating and mixing tank 21 while being mixed with, by the aggregating and mixing tank agitator 24, the mixture is agglomerated and mixed through the pressure feed pipe 23 disposed along the axis of the screw shaft 13 to the screw surface at a low pressure from the supply port 121. It is pumped into the front of the processing area S so that it rides.

最初は処理域Sの該前部内に汚泥等が存在しないか、存
在しても少量の場合は圧入された汚泥等は、スクリュー
羽根132が未だ回動してないので処理域Sの前記前部に
略滞留しながら、徐々に充満するので、充満するまでは
給泥ポンプによって加えられた圧力は元の大気圧に戻っ
て、この間汚泥等は自重により濾過部11に接して重力で
少量づつ脱水しているのみであり、未だ有効な圧力脱水
作用は始まっていないから、圧力センサー22も給泥ポン
プに対してなんらの信号も伝達せず、給泥ポンプは全力
運転して汚泥等を急速に供給口121から処理域Sの前部
内へ送り込まれる。
Initially, if there is no sludge or the like in the front part of the processing area S, or if there is a small amount of sludge or the like, the screw blades 132 have not yet rotated so that the sludge or the like is pressed into the front part of the processing area S. Since it gradually fills up while almost staying in the tank, the pressure applied by the mud pump returns to the original atmospheric pressure until it fills up, and during this time, sludge and the like contact the filter section 11 by its own weight and dehydrate little by little by gravity. However, since the effective pressure dehydration action has not yet started, the pressure sensor 22 does not transmit any signal to the mud pump, and the mud pump operates at full power to rapidly remove sludge and the like. It is fed into the front part of the processing area S from the supply port 121.

次に処理域Sの前部内へ送り込まれた汚泥等のうち、一
部はスクリュー羽根132の隙間や、スパイラルに沿って
排出口113側へ進むが、大部分は前部に留まってやがて
前部に充満すると急激に前部の内圧が高まり、含有水が
大量に絞り出され始めて、脱水孔111aからは大量の水
が流下するようになるが、通常はこの状態を確認してス
クリューシャフト13に回転力を伝達する。
Next, of the sludge and the like sent into the front part of the processing area S, some of it advances to the discharge port 113 side along the gaps of the screw blades 132 and the spiral, but most of it stays at the front part and eventually the front part. When it fills up with water, the internal pressure of the front part suddenly rises, a large amount of contained water begins to be squeezed out, and a large amount of water starts to flow down from the dehydration hole 111a. Transmits rotational force.

なお、スクリューシャフト13の始動が遅れても圧力セン
サ22が過昇圧を検知して、給泥ポンプの運転を停止また
は低下させるので、スクリュー羽根132等を破損する心
配はない。処理域Sの前部内で昇圧し含有水を絞られて
半脱水状態になった汚泥等は回動を始めたスクリューシ
ャフト13のスクリュー羽根132に導かれて、同部131の大
径側へと押送され、狭くなる処理域S内でますます圧搾
されてどんどん含有水が絞られ、濾過部11の全周に穿設
された脱水孔111aから直ちに浸出し滴下するので、該
被脱水汚泥等は、排出口113に至る頃は完全なケーキ状
となっている。該被脱水のケーキは、胴部131の大径端
近傍でスクレーパ143によって掻き落とされ、スタンド1
4底部に堆積するのであとはそれを集めて所要の処理を
する。また、投入槽内に汚泥等が残っている限り、給泥
ポンプは該汚泥を処理域S内へ圧送し続けるので、連続
して脱水処理が行なえるものである。
Even if the start of the screw shaft 13 is delayed, the pressure sensor 22 detects the excessive pressurization and stops or lowers the operation of the mud supply pump, so that there is no fear of damaging the screw blades 132 and the like. The sludge, etc., which has become semi-dehydrated by pressurizing the contained water and squeezing the contained water in the front part of the treatment area S, is guided to the screw blades 132 of the screw shaft 13 which started to rotate, and to the large diameter side of the part 131. The water contained is squeezed and squeezed more and more in the narrowed treatment area S, and the water contained therein is squeezed and leaches out immediately from the dehydration holes 111a formed in the entire circumference of the filtration section 11, so that the sludge to be dehydrated, etc. By the time it reaches the outlet 113, it has a perfect cake shape. The cake to be dehydrated is scraped off by a scraper 143 near the large diameter end of the body 131, and the
4 As it accumulates on the bottom, it is collected and processed as required. Further, as long as sludge or the like remains in the input tank, the sludge supply pump continuously feeds the sludge into the treatment area S, so that the dehydration treatment can be continuously performed.

このように本発明では、従来の連続圧搾機においては投
入ホッパがあり、その部分の濾過部は脱水には殆んど寄
与しないものであったが、全長にわたって有効に脱水作
用が行なえ、かつ、初期充満圧を上げ前部内で半脱水状
態まで脱水するので、該ホッパの占めていた長さ以上に
濾過部を長くしたと同様の効果があるものである。
As described above, in the present invention, in the conventional continuous pressing machine, there is a charging hopper, and the filtering part of the part hardly contributes to dewatering, but the dewatering action can be effectively performed over the entire length, and, Since the initial filling pressure is raised to dehydrate the semi-dehydrated state in the front part, the same effect can be obtained by making the filtration part longer than the length occupied by the hopper.

なお、本実施例において出口側スタンドにおけるスクレ
ーパは適宜の手段でロッドを水平方向に伸縮させること
ができる操作部によって胴部大径端周面を摺動して排出
口面積を変化させるものについて説明したが、本発明は
本実施例に限定されるものではなく、前記した本発明の
目的、作用及び後記する発明の効果が達成される範囲に
おいてこれらは本発明の要旨を何ら変更するものでない
ことは申すまでもない。
It should be noted that in the present embodiment, a description will be given of the scraper in the outlet side stand, which changes the discharge port area by sliding on the large-diameter end peripheral surface of the body part by the operation part capable of horizontally expanding and contracting the rod by appropriate means. However, the present invention is not limited to the examples, and these do not change the gist of the present invention within a range in which the above-mentioned objects, functions, and effects of the invention described below are achieved. Needless to say.

[発明の効果] 以上、詳細に説明したように本発明は、濾過部をスクリ
ューシャフトの全長にわたり囲繞して周設し、かつ、全
長に脱水処理域を形成し、これの前部に設けられている
側壁に供給口を軸芯方向へ開設し、ここより密閉された
凝集混和槽を介して汚泥等を凝集フロックとして軸芯方
向へ圧送し、先ず、脱水処理域前部へ供給しスクリュー
羽根のリード方向に沿うべくこれの軸芯方向に圧送し、
該スクリュー羽根上へ凝集フロック状に保持したまま載
置状に供給するから凝集フロックが壊れることなく、よ
って、少量の凝集剤でよいから、濾過部のパンチングの
目詰りを防止しえて、さらに、初期の充満点を濾過部の
最前部に形成しえて、かつ、脱水処理域内へ供給される
汚泥等の充満度を増しえて、よって、濾過面積を増大さ
せ、脱水効率や処理量の向上を計ることが可能となっ
て、さらに、大幅に小型化することが可能で、これによ
って製造価格や設置費用等が節減され、また、設置場所
の選択幅を広くなしえて、汚泥やケーキの運搬経費等も
節減される等、波及効果が大なる優れた発明である。
[Effects of the Invention] As described above in detail, according to the present invention, the filtration unit is provided so as to surround and surround the entire length of the screw shaft, and the dehydration treatment region is formed in the entire length, and is provided in the front portion thereof. A supply port is opened on the side wall in the axial direction, and sludge etc. is pressure-fed in the axial direction as coagulation flocs through a coagulation and mixing tank which is sealed from here. It is pressure-fed in the axial direction of this so as to follow the lead direction of
Since the flocculate flocs are supplied while being held on the screw blades while being held in the flocculation flocs, the flocculation flocs are not broken, and therefore a small amount of the flocculating agent is enough to prevent clogging during punching of the filtration unit. The initial filling point can be formed at the forefront of the filtration section, and the filling degree of sludge etc. supplied into the dehydration treatment area can be increased, thus increasing the filtration area and improving the dehydration efficiency and treatment amount. It is possible to further reduce the size, which reduces manufacturing costs and installation costs, and also allows a wide range of installation locations to be selected, such as transportation costs for sludge and cake. It is an excellent invention that has a great ripple effect, such as saving energy.

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

図面は本発明汚泥等の処理方法の一実施例を示したもの
で、第1図は連続圧搾機の要部を一部を断面で示す側面
図である。 11……濾過部、113……排出口 12……側壁、121……供給口 13……スクリューシャフト 131……胴部 132……スクリュー羽根 S……脱水処理域
The drawings show one embodiment of the method for treating sludge or the like of the present invention, and FIG. 1 is a side view showing a partial cross section of a main part of a continuous pressing machine. 11 …… Filtration part, 113 …… Discharge port 12 …… Side wall, 121 …… Supply port 13 …… Screw shaft 131 …… Body part 132 …… Screw blade S …… Dehydration treatment area

フロントページの続き (51)Int.Cl.5 識別記号 庁内整理番号 FI 技術表示箇所 C02F 11/12 D 7824−4D Continuation of front page (51) Int.Cl. 5 Identification code Office reference number FI technical display area C02F 11/12 D 7824-4D

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】横長い直円筒形状で全長にわたり脱水孔を
開設し、前端部に側壁を後端部にケーキ排出口を設け、
かつ、金鋼を内設してなる濾過部へ、前端部から後端部
に向けて大径となるテーパ状の胴部にスパイラル状のス
クリュー羽根を備えたスクリューシャフトを回動自在に
枢設することにより該濾過部の全長にわたり脱水処理域
を形成し、かつ、前記前端部の側壁に軸芯方向に向けて
供給口を開設して凝集混和槽や撹拌機等よりなる汚泥等
圧送部を連結し、該汚泥等圧送部よりの凝集フロック状
の汚泥を先ずスクリュー羽根前端の脱水処理域前部へ圧
送して、該スクリュー羽根のリード方向に沿うべくこれ
の軸芯方向に圧送することにより、該スクリュー羽根上
へ凝集フロック状に保持したまま載置状に供給して順次
充満せしめて該充満圧で半脱水状態として後、該スクリ
ューシャフトを回動せしめて前記脱水処理域で脱水し、
ついで前記脱水処理域前部を介して順次該回動のスクリ
ューシャフトでなる該脱水処理域で脱水しつつ排出口側
へ圧送して該排出口よりケーキを押し出すことを特徴と
する汚泥等の処理方法。
1. A horizontally long straight cylindrical shape having a dehydration hole formed along its entire length, a side wall at the front end and a cake discharge port at the rear end,
In addition, a screw shaft equipped with spiral screw blades is rotatably pivotally attached to the filtering part, which is internally provided with gold steel, and has a tapered barrel with a large diameter from the front end to the rear end. To form a dehydration treatment area over the entire length of the filtration section, and to open a supply port in the side wall of the front end in the axial direction to form a sludge equalizing pressure feeding section including a coagulation mixing tank or a stirrer. By connecting, the floc-like sludge from the sludge equalizing pumping unit is first pressure-fed to the front part of the dehydration treatment area at the front end of the screw blade, and is fed in the axial direction of the screw blade along the lead direction. , While being held in a flocculated state on the screw blades while being supplied in a stationary state and sequentially filled to be in a semi-dewatering state at the filling pressure, the screw shaft is rotated to be dehydrated in the dehydration treatment area,
Then, the sludge or the like is characterized in that the cake is pushed out from the discharge port by pumping to the discharge port side while dehydrating in the dehydration processing region consisting of the rotating screw shaft through the front part of the dehydration processing region. Method.
JP61260291A 1986-10-30 1986-10-30 Sludge treatment method Expired - Lifetime JPH0613159B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP61260291A JPH0613159B2 (en) 1986-10-30 1986-10-30 Sludge treatment method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP61260291A JPH0613159B2 (en) 1986-10-30 1986-10-30 Sludge treatment method

Publications (2)

Publication Number Publication Date
JPS63111910A JPS63111910A (en) 1988-05-17
JPH0613159B2 true JPH0613159B2 (en) 1994-02-23

Family

ID=17346003

Family Applications (1)

Application Number Title Priority Date Filing Date
JP61260291A Expired - Lifetime JPH0613159B2 (en) 1986-10-30 1986-10-30 Sludge treatment method

Country Status (1)

Country Link
JP (1) JPH0613159B2 (en)

Families Citing this family (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR100817391B1 (en) * 2001-01-10 2008-03-27 츠키시마기카이가부시키가이샤 Screw press dewatering machine
JP5116783B2 (en) * 2010-02-05 2013-01-09 三菱重工環境・化学エンジニアリング株式会社 Water content drying equipment
CN103373799A (en) * 2012-04-17 2013-10-30 泰州市蓝海环保科技有限公司 Novel spiral shaft applicable to spiral sludge squeezing and dewatering machine

Also Published As

Publication number Publication date
JPS63111910A (en) 1988-05-17

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