JPH1024201A - Solid-liquid separator for waste water of ready-mixed concrete - Google Patents
Solid-liquid separator for waste water of ready-mixed concreteInfo
- Publication number
- JPH1024201A JPH1024201A JP8214016A JP21401696A JPH1024201A JP H1024201 A JPH1024201 A JP H1024201A JP 8214016 A JP8214016 A JP 8214016A JP 21401696 A JP21401696 A JP 21401696A JP H1024201 A JPH1024201 A JP H1024201A
- Authority
- JP
- Japan
- Prior art keywords
- tank
- sludge
- filtration
- thickener
- solid
- 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
- 239000002351 wastewater Substances 0.000 title claims abstract description 4
- 239000007788 liquid Substances 0.000 title claims description 8
- 239000010802 sludge Substances 0.000 claims abstract description 32
- 238000001914 filtration Methods 0.000 claims abstract description 31
- 239000002562 thickening agent Substances 0.000 claims abstract description 22
- 230000018044 dehydration Effects 0.000 claims abstract description 17
- 238000006297 dehydration reaction Methods 0.000 claims abstract description 17
- 238000005192 partition Methods 0.000 claims abstract description 10
- 239000004568 cement Substances 0.000 claims abstract description 5
- 239000004744 fabric Substances 0.000 claims abstract description 5
- 230000005484 gravity Effects 0.000 claims abstract description 3
- 239000002699 waste material Substances 0.000 claims abstract description 3
- 238000000034 method Methods 0.000 claims description 8
- 238000003756 stirring Methods 0.000 claims description 5
- 238000000926 separation method Methods 0.000 claims description 4
- 239000007787 solid Substances 0.000 claims description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 30
- 239000002002 slurry Substances 0.000 abstract description 10
- 239000006228 supernatant Substances 0.000 abstract description 6
- 238000005406 washing Methods 0.000 abstract description 3
- 238000004140 cleaning Methods 0.000 abstract 1
- 208000005156 Dehydration Diseases 0.000 description 11
- 238000010586 diagram Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 4
- 239000002440 industrial waste Substances 0.000 description 3
- 230000001105 regulatory effect Effects 0.000 description 3
- 238000004062 sedimentation Methods 0.000 description 3
- 241000209149 Zea Species 0.000 description 2
- 235000005824 Zea mays ssp. parviglumis Nutrition 0.000 description 2
- 235000002017 Zea mays subsp mays Nutrition 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 235000005822 corn Nutrition 0.000 description 2
- 239000004570 mortar (masonry) Substances 0.000 description 2
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000004898 kneading Methods 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/009—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone characterised by the material treated
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/45—Coating or impregnating, e.g. injection in masonry, partial coating of green or fired ceramics, organic coating compositions for adhering together two concrete elements
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B41/00—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone
- C04B41/53—After-treatment of mortars, concrete, artificial stone or ceramics; Treatment of natural stone involving the removal of at least part of the materials of the treated article, e.g. etching, drying of hardened concrete
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
- C04B2111/00241—Physical properties of the materials not provided for elsewhere in C04B2111/00
- C04B2111/00267—Materials permeable to vapours or gases
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B2111/00—Mortars, concrete or artificial stone or mixtures to prepare them, characterised by specific function, property or use
- C04B2111/00241—Physical properties of the materials not provided for elsewhere in C04B2111/00
- C04B2111/00284—Materials permeable to liquids
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Filtration Of Liquid (AREA)
Abstract
Description
【0001】[0001]
【発明の属する利用分野】主に小規模生コンクリート工
場において、骨材回収後のスラッジを上澄水と濃度の高
いスラッジとに区分して脱水処理する装置に関するもの
である。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for dewatering sludge after collecting aggregate, mainly in a small-scale ready-mixed concrete factory, by separating the sludge into supernatant water and highly concentrated sludge.
【0002】[0002]
【従来の技術】従来の方法としては、先ず、生コンスラ
ッジをシックナーに入れ、沈降する高濃度スラッジと上
澄水に区分したものを所望する濃度に調合して生コンの
練り水に混入する方法。他の方法として、シックナーに
よって沈降した高濃度のスラッジを別槽に貯溜して自然
乾燥して規制型産業廃棄物として処理し、上澄水は生コ
ンの練り水とて使用する方法。又、さらに前2項と同様
の固液分離をなす装置において本出願人の先願として、
スラッジを脱水機にて脱水する直前に、前処理槽を介在
させて、スラリーの性状を変えることにより、即日脱水
を可能とした方法がある(特願平5−355200、特
許願平5−355228)。先の出願において、スラリ
ーの性状を変えるとは、スラッジ中に微細なエアーを混
入し、気泡を発生させることにより、生コンクリートに
混入された混和剤が気泡に連行されて浮上し、該気泡を
取り除くことによって、混和剤の作用をなくし、脱水を
容易にしようとするものである。2. Description of the Related Art As a conventional method, first, raw corn sludge is put into a thickener, and sedimentation of high-concentration sludge that sediments and supernatant water is mixed to a desired concentration and mixed into the mixing water of raw corn. As another method, high-concentration sludge settled by a thickener is stored in a separate tank, air-dried and treated as regulated industrial waste, and the supernatant water is used as kneading water for ready-mixed concrete. Further, in an apparatus for performing solid-liquid separation similar to the preceding two paragraphs,
Immediately before the sludge is dewatered by a dewatering machine, there is a method that enables the same day dewatering by changing the properties of the slurry by interposing a pretreatment tank (Japanese Patent Application No. 5-355200, Japanese Patent Application No. 5-355228). ). In the earlier application, changing the properties of the slurry means that fine air is mixed into the sludge and bubbles are generated, whereby the admixture mixed in the ready-mixed concrete is entrained by the bubbles and floats, and the bubbles are removed. By removing it, the effect of the admixture is eliminated, and the dehydration is facilitated.
【0003】[0003]
【発明が解決しようとする課題】従来技術に述べた前2
項に示す方法では放置時間が長いことと、濃縮スラッジ
の含水率は60%〜80%と高いのでケーキの圧縮強度
が低く従来どおり規制型産業廃棄物としての処理が必要
である。また、従来のフィルタープレス脱水機の機構で
は、濾板及び加圧機構が必要となるので、どうしても設
備価額を低減することができなかった。そこで本発明
は、シックナーの機能を尊重し、濾板の開閉機構を要し
ない簡易なる濾過機能を持った脱水槽の開発と、更に脱
水性を向上させるため、シックナーと脱水槽との間に先
の出願による前処理槽を介在させた2項の発明により、
経済性を考慮した脱水工法である。該工法は、脱水ケー
キ含水率を40%前後にすること、それによってケーキ
強度を向上させ、モルタル並以上の品質を得ることを達
成し、一般建築廃材と同等に処理することができるよう
にしようとするもので、とくに小規模工場において、機
構が簡易で安価で、経済性のある脱水装置を提供するこ
とを目的とするものである。SUMMARY OF THE INVENTION
In the method described in the section, since the standing time is long and the water content of the concentrated sludge is as high as 60% to 80%, the compressive strength of the cake is low and it is necessary to treat it as a regulated industrial waste as before. In addition, the conventional filter press dehydrator mechanism requires a filter plate and a pressurizing mechanism, so that the equipment value could not be reduced. Therefore, the present invention respects the function of the thickener and develops a dewatering tank having a simple filtration function that does not require a filter plate opening / closing mechanism. According to the invention of item 2 in which a pretreatment tank according to the application of
This is a dewatering method that considers economy. This method is intended to achieve a water content of the dewatered cake of about 40%, thereby improving the cake strength and obtaining a quality equal to or higher than that of the mortar, so that it can be treated at the same level as general building waste. It is an object of the present invention to provide an economical dewatering apparatus with a simple, inexpensive mechanism, particularly in a small-scale factory.
【0004】[0004]
【課題を解決するための手段】請求項1の方法は、セメ
ントスラッジを重力により自然沈降処理するシックナー
を第一工程とし、縦型円筒形槽の下方胴体部分に挿入す
る方法で濾布を張設した内筒状の濾過部と、底面には下
方に開放する濾過底板を設け、該濾過底板には、複数の
仕切濾過板を植設した濾過構造を有する脱水槽を第二工
程とし、該脱水槽はシックナーの濃縮スラッジをスラリ
ーポンプの加圧で脱水するものであって、前記二工程を
連動して固液を分離するものである。According to a first aspect of the present invention, a thickener for subjecting cement sludge to natural sedimentation by gravity is used as a first step, and a filter cloth is stretched by inserting the thickener into a lower body portion of a vertical cylindrical tank. The inner cylindrical filtration unit provided, and a bottom provided with a filtration bottom plate that opens downward on the bottom surface, the dehydration tank having a filtration structure in which a plurality of partition filtration plates are planted on the filtration bottom plate as the second step, The dewatering tank dewaters the concentrated sludge of the thickener by pressurizing a slurry pump, and separates the solid and liquid by interlocking the two steps.
【0005】請求項2の方法は、セメントスラッジを沈
降処理するシックナーを第一工程とし、縦型円筒槽の下
方胴体部分と底面に濾布を張設した濾過板に着脱式に設
けた仕切濾過板を有する濾過構造の円筒型脱水槽を第二
工程とした間に、前処理槽を介在させ三工程としたもの
である。該前処理槽は、中心に攪拌縦軸を設け、下方部
に水平に回転するエアー管に複数の噴出口を設けてい
て、エアー噴出によりスラッジの性情を変化させる機能
を具備してる。攪拌縦軸の下端部は、上向き送りの羽根
を設けている 。[0005] In the method of claim 2, a thickener for sedimentation of cement sludge is used as a first step, and the filter is detachably provided on a filter plate having a filter cloth stretched on a lower body portion and a bottom surface of a vertical cylindrical tank. A pretreatment tank is interposed between the second step of the cylindrical dehydration tank having a filtration structure having a plate, and three steps are performed. The pretreatment tank has a stirring longitudinal axis at the center, and a plurality of ejection ports provided on a horizontally rotating air pipe at a lower portion, and has a function of changing the properties of sludge by air ejection. The lower end of the stirring longitudinal axis is provided with an upwardly feeding blade.
【0006】[0006]
【作用】本発明の作動要領を説明する。生コン運搬車の
洗浄水及び戻りコンクリートは骨材分離装置1にて固液
分離され、骨材は骨材溜槽に移送され、スラッジは一旦
貯溜槽2へ送入する。ここからポンプ3によってシック
ナー4へ流入する。この槽で沈降するスラッジは排出弁
5を開としスラリーポンプ6により脱水槽7へ圧送す
る。シックナー上縁にはオーバーフロートイ8を設けて
いて上澄水は、この円周のトイへ溢流して濾過水槽へ導
入する。シックナーへの流入量と、スラリーポンプ6の
送水量の調整は、夫々配水管に設けてある弁9,9′に
より行う。脱水槽7の底面は濾過底板10によって片開
きに開閉自在とし、下方部には濾過機能を具備した内筒
11を挿入しており、該内筒の内面は下方へ抜勾配をつ
けており、ケーキは下方へ落下を容易としている。濾過
底板10には複数の仕切り濾過板12を植設し、濾過底
板とは着脱式とし、濾過底板を開く場合、仕切り濾過板
共一体として下方へ抜き取ることができるように抜勾配
をつけた形状としている。The operation of the present invention will be described. The washing water and the returned concrete of the ready-mixed concrete carrier are separated into solid and liquid by the aggregate separating device 1, the aggregate is transferred to the aggregate storage tank, and the sludge is once sent to the storage tank 2. From here, it flows into the thickener 4 by the pump 3. The sludge settling in this tank is sent to the dewatering tank 7 by the slurry pump 6 with the discharge valve 5 opened. An overflow toy 8 is provided on the upper edge of the thickener, and the supernatant water overflows to the toy on the circumference and is introduced into the filtered water tank. Adjustment of the inflow amount to the thickener and the water supply amount of the slurry pump 6 is performed by valves 9 and 9 'respectively provided in the water distribution pipes. The bottom surface of the dewatering tank 7 is openable and closable by a filter bottom plate 10 so that it can be opened and closed in one side, and an inner cylinder 11 having a filtering function is inserted in a lower portion, and the inner surface of the inner cylinder has a downward slope. The cake is easy to fall down. A plurality of partition filter plates 12 are planted on the filter bottom plate 10 and detachable from the filter bottom plate. When the filter bottom plate is opened, the partition filter plate is integrally formed with a draft so as to be able to be withdrawn downward. And
【0007】脱水槽の内筒11の上方位には排出弁13
を設けている。脱水槽よりの排水量はケーキ層の創成に
より脱水量が漸減してくるのでその減水の度合いを弁2
1を調整しておき、所定の濾過発生水量に低減した場合
において脱水終了とする。スラリーポンプ6を停止する
と同時に排出弁13を開として残っているスラッジをス
ラッジ槽2へ戻す。残量スラッジの排出が終わると濾過
底板10を開きケーキを下方のケーキ台車(図示せず)
へ落下させる。脱水中は、濾過水受け皿14によって濾
過水を集め濾過水槽15へ導入する。脱水が終了する
と、該受皿は基軸により水平方向へ90°の旋回をして
ケーキ落下に支障のないようにする。A discharge valve 13 is provided in the upper direction of the inner cylinder 11 of the dewatering tank.
Is provided. The amount of water drained from the dewatering tank gradually decreases as the cake layer is created.
1 is adjusted in advance, and the dehydration is terminated when the amount of generated filtration water is reduced to a predetermined value. At the same time as the slurry pump 6 is stopped, the discharge valve 13 is opened and the remaining sludge is returned to the sludge tank 2. When the residual sludge has been discharged, the filter bottom plate 10 is opened, and the cake is placed on a lower cake trolley (not shown).
Drop to During dehydration, filtered water is collected by the filtered water tray 14 and introduced into the filtered water tank 15. When the dehydration is completed, the pan is rotated 90 ° in the horizontal direction by the base axis so that the cake does not hinder falling.
【0008】本発明は、脱水処理において、各工程の特
質を考慮した上でそれらの組み合わせにより、全体の効
率を向上させる作用を利用したもので、シックナーは、
低濃度の泥水の処理効率が大であること。一方、前処理
槽では、高濃度のスラッジの処理に効果が良好であるこ
と。そして、円筒形の濾過槽は、従来方式のフィルター
プレス脱水機よりも低圧であり能力は劣るが、前記の利
点を組み合わせることにより、小型工場の廃水処理には
充分の機能を発揮するものである。[0008] The present invention utilizes the effect of improving the overall efficiency of the dehydration treatment by considering the characteristics of each step and by combining them in a dehydration treatment.
High treatment efficiency for low-concentration mud. On the other hand, in the pretreatment tank, the effect should be good for treating high-concentration sludge. The cylindrical filtration tank is lower in pressure and lower in performance than the conventional filter press dewatering machine, but by combining the above advantages, it exhibits a sufficient function for wastewater treatment in small factories. .
【0009】[0009]
【実施例】本発明の実施例を図面に従って説明する。図
1は、シックナーと、脱水槽の二工程よりなる請求項1
記載の実施例の正面系統図を示し。図2は平面図を示
す。ミキサー車の洗浄廃水は洗車トイを経てトロンメル
1に入り、該トロンメルで骨材を取り除かれたスラッジ
は、スラッジ槽2に入る。該スラッジ槽2より、ポンプ
3でシックナー4に送水する。該シックナー4の底部に
排出弁5を設け、沈殿した高濃度のスラッジは、スラリ
ーポンプ6で脱水槽7へ圧送する。一方シックナー4の
上澄水は上方円周状に設けたオーバーフロートイ8より
濾過水槽へ導入するように形成する。An embodiment of the present invention will be described with reference to the drawings. FIG. 1 shows two steps of a thickener and a dewatering tank.
Figure 2 shows a front system diagram of the described embodiment. FIG. 2 shows a plan view. The washing wastewater of the mixer truck enters the trommel 1 via the carwash toy, and the sludge from which the aggregate has been removed by the trommel enters the sludge tank 2. Water is supplied from the sludge tank 2 to the thickener 4 by the pump 3. A discharge valve 5 is provided at the bottom of the thickener 4, and the precipitated high-concentration sludge is pumped to a dewatering tank 7 by a slurry pump 6. On the other hand, the supernatant water of the thickener 4 is formed so as to be introduced into a filtration water tank from an overflow toy 8 provided in an upper circumferential shape.
【0010】脱水槽7の底面は、下向きで片開きの濾過
底板10を設け、脱水槽の下方部の内周には濾過機能を
有し、沈着したケーキを抜き取れるように下方へ抜勾配
を設けた内筒11を挿入する。濾過底板10には、複数
の仕切り濾過板12を設け、濾過底板10が下方へ開放
する時に同時に下方へ抜き取ることができるようにす
る。脱水が終了したら、残存スラッジは上方に設けた排
出弁13を開とし、スラッジ槽2へ戻す。内筒に創成さ
れたケーキは、濾過底板10の開放により下方へ落下し
てケーキ台車(図示せず)によって搬出される。脱水中
の濾過水は、下方の濾過水受皿14で受け、濾過水槽1
5へ導水するようになし、ケーキが落下するときには、
落下位置より逃げるように旋回自在とする。The bottom surface of the dewatering tank 7 is provided with a downward, one-sided filter bottom plate 10 having a filtering function on the inner periphery of the lower part of the dewatering tank, and having a downward slope so that the deposited cake can be removed. The provided inner cylinder 11 is inserted. The filtration bottom plate 10 is provided with a plurality of partition filtration plates 12 so that the filtration bottom plate 10 can be simultaneously withdrawn downward when the filtration bottom plate 10 is opened downward. When the dehydration is completed, the residual sludge is returned to the sludge tank 2 by opening the discharge valve 13 provided above. The cake created in the inner cylinder falls down by opening the filtration bottom plate 10 and is carried out by a cake cart (not shown). The filtered water during dehydration is received in the filtered water receiving tray 14 below, and the filtered water tank 1
5 so that when the cake falls,
Swivel to escape from the drop position.
【0011】図7は、シックナーと脱水機の間に前処理
槽を介在させた三工程よりなる請求項2記載の実施例の
正面系統図を示す。シックナー4と、脱水槽7の構造
は、前記実施例と同様である。前処理槽16は、シック
ナー4の排出弁5と連結する。前処理槽16によって前
処理されたスラッジはスラリーポンプ6で脱水槽7へ圧
送する。前処理槽の内部構造は、中心部中空の攪拌縦軸
17を設けて、その軸は下端部排出口付近に羽根18を
設ける。該羽根は上方送りとしており、排出口の詰まり
を防止している。その上方部には水平横管19を設け、
該横管には複数のノーズルを設けており軸の回転と共に
水平面に無数の気泡が噴出するようになしている。エア
ー導入は縦軸上端においてエアー源と連結している。前
処理槽に電極棒20を設け、前処理槽の水量の調整を排
出弁5によって行うものである。以上のような構造を有
するものである。FIG. 7 is a front system diagram of an embodiment according to claim 2, which comprises three steps in which a pretreatment tank is interposed between a thickener and a dehydrator. The structures of the thickener 4 and the dewatering tub 7 are the same as in the above embodiment. The pretreatment tank 16 is connected to the discharge valve 5 of the thickener 4. The sludge pretreated by the pretreatment tank 16 is pumped to the dewatering tank 7 by the slurry pump 6. The internal structure of the pretreatment tank is provided with a stirring shaft 17 having a hollow central portion, and the shaft is provided with a blade 18 near a lower end discharge port. The blades are fed upward to prevent clogging of the outlet. A horizontal horizontal pipe 19 is provided in the upper part,
The horizontal tube is provided with a plurality of nosepieces so that an infinite number of air bubbles are ejected on a horizontal plane as the shaft rotates. The air inlet is connected to the air source at the upper end of the vertical axis. The electrode rod 20 is provided in the pretreatment tank, and the amount of water in the pretreatment tank is adjusted by the discharge valve 5. It has the above structure.
【0012】[0012]
【効果】従来の脱水工法に使用している濾過板及び濾過
板の加圧機構を不用とした工法であるので、設備費が従
来方式の50%程度となり、且つケーキの含水率におい
ても40%前後にすることができるので圧縮強度におい
ても一般モルタル同等とすることが可能となるので、規
制型産業廃棄物の発生をなくし、処理費の大幅な削減と
環境問題への配慮が達成されるものである。[Effect] Since the filter plate and the pressurizing mechanism of the filter plate used in the conventional dewatering method are not required, the equipment cost is about 50% of that of the conventional method, and the water content of the cake is 40%. Because the compression strength can be set to the same level as ordinary mortar because it can be set back and forth, the generation of regulated industrial waste is eliminated, and a significant reduction in processing costs and consideration for environmental issues are achieved. It is.
【図1】本発明請求項1記載の実施例正面系統図であ
る。FIG. 1 is a front system diagram of an embodiment according to claim 1 of the present invention.
【図2】図1の平面図である。FIG. 2 is a plan view of FIG.
【図3】脱水槽濾過底板近傍部分図である。FIG. 3 is a partial view in the vicinity of a dewatering tank filtration bottom plate.
【図4】脱水槽濾過底板の平面図である。FIG. 4 is a plan view of a dewatering tank filtration bottom plate.
【図5】仕切り濾過板正面部分図である。FIG. 5 is a partial front view of a partition filter plate.
【図6】仕切り濾過板の側断面図である。FIG. 6 is a side sectional view of a partition filter plate.
【図7】本発明請求項2記載の実施例正面系統図であ
る。FIG. 7 is a front system diagram of an embodiment according to claim 2 of the present invention.
1 トロンメル 2 貯溜槽 3 ポンプ 4 シックナー 5 排出弁 6 スラリーポンプ 7 脱水槽 8 オーバーフロートイ 9 弁 9′ 弁 10 濾過底板 11 内筒 12 仕切り濾過板 13 排出弁 14 濾過水受皿 15 濾過水槽 16 前処理槽 17 攪拌縦軸 18 羽根 19 水平横管 20 電極棒 21 弁 Reference Signs List 1 trommel 2 storage tank 3 pump 4 thickener 5 discharge valve 6 slurry pump 7 dehydration tank 8 overflow toy 9 valve 9 'valve 10 filtration bottom plate 11 inner cylinder 12 partition filtration plate 13 discharge valve 14 filtered water tray 15 filtration water tank 16 pretreatment tank 17 Stirring longitudinal axis 18 Blade 19 Horizontal horizontal tube 20 Electrode rod 21 Valve
Claims (2)
処理するシックナーを第一工程とし、縦型円筒形槽の下
方胴体部分に濾布を張設した内筒状の濾過部と、底面に
は下方に開放する濾過底板を設け、該濾過底板には、複
数の仕切濾過板を植設した濾過構造を有する脱水槽を第
二工程とし、前記二工程を連動し、固液を分離すること
を特徴とする生コンクリート廃水の固液分離装置。1. A thickener, which naturally setstles cement sludge by gravity as a first step, an inner cylindrical filtering section in which a filter cloth is stretched on a lower body portion of a vertical cylindrical tank, and a lower surface on a bottom surface. A filtration bottom plate to be opened is provided, and the filtration bottom plate has a dehydration tank having a filtration structure in which a plurality of partition filtration plates are planted as a second step, and the two steps are interlocked to separate solid and liquid. Solid-liquid separation equipment for waste concrete.
ナーを第一工程とし、縦型円筒形槽の下方胴体部分と底
面に濾布を張設した濾過構造を有する脱水槽を第二工程
とした間に、縦型攪拌軸に、かき羽根とエアーブロー水
平軸を備えた前処理槽を介在させ、三工程として連動し
て固液を分離することを特徴とする生コンクリート廃水
の固液分離装置。2. A thickener for sedimenting cement sludge as a first step, and a dewatering tank having a filtering structure in which a filter cloth is stretched on a lower body portion and a bottom surface of a vertical cylindrical tank during a second step. A solid-liquid separation device for ready-mixed concrete wastewater, wherein a solid-liquid separation device is interlocked as a three-step process by interposing a pretreatment tank having a shaving blade and an air blow horizontal axis on a vertical stirring shaft.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8214016A JPH1024201A (en) | 1996-07-10 | 1996-07-10 | Solid-liquid separator for waste water of ready-mixed concrete |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP8214016A JPH1024201A (en) | 1996-07-10 | 1996-07-10 | Solid-liquid separator for waste water of ready-mixed concrete |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH1024201A true JPH1024201A (en) | 1998-01-27 |
Family
ID=16648887
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP8214016A Pending JPH1024201A (en) | 1996-07-10 | 1996-07-10 | Solid-liquid separator for waste water of ready-mixed concrete |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH1024201A (en) |
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002282611A (en) * | 2001-03-29 | 2002-10-02 | Sumitomo Heavy Ind Ltd | Pretreatment tank |
| FR3031051A1 (en) * | 2014-12-30 | 2016-07-01 | Vdb | CONCRETE SLUDGE TREATMENT |
| CN113510111A (en) * | 2021-05-19 | 2021-10-19 | 王兆春 | Concrete cement slurry recycling system |
-
1996
- 1996-07-10 JP JP8214016A patent/JPH1024201A/en active Pending
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2002282611A (en) * | 2001-03-29 | 2002-10-02 | Sumitomo Heavy Ind Ltd | Pretreatment tank |
| FR3031051A1 (en) * | 2014-12-30 | 2016-07-01 | Vdb | CONCRETE SLUDGE TREATMENT |
| CN113510111A (en) * | 2021-05-19 | 2021-10-19 | 王兆春 | Concrete cement slurry recycling system |
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