JPH02162003A - Method and apparatus for regenerating washing residue of ready-mixed concrete - Google Patents
Method and apparatus for regenerating washing residue of ready-mixed concreteInfo
- Publication number
- JPH02162003A JPH02162003A JP31712288A JP31712288A JPH02162003A JP H02162003 A JPH02162003 A JP H02162003A JP 31712288 A JP31712288 A JP 31712288A JP 31712288 A JP31712288 A JP 31712288A JP H02162003 A JPH02162003 A JP H02162003A
- Authority
- JP
- Japan
- Prior art keywords
- sludge water
- water
- separated liquid
- sludge
- cement
- 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.)
- Granted
Links
- 238000005406 washing Methods 0.000 title claims abstract description 24
- 238000000034 method Methods 0.000 title claims abstract description 9
- 230000001172 regenerating effect Effects 0.000 title claims description 4
- 239000010802 sludge Substances 0.000 claims abstract description 103
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 99
- 239000007788 liquid Substances 0.000 claims abstract description 43
- 239000004568 cement Substances 0.000 claims abstract description 36
- 239000006228 supernatant Substances 0.000 claims abstract description 13
- 239000002245 particle Substances 0.000 claims abstract description 11
- 239000002002 slurry Substances 0.000 claims abstract description 9
- 239000004576 sand Substances 0.000 claims description 10
- 238000004064 recycling Methods 0.000 claims description 7
- 238000010298 pulverizing process Methods 0.000 claims description 6
- 238000007865 diluting Methods 0.000 claims description 3
- 239000000284 extract Substances 0.000 claims description 3
- 238000010333 wet classification Methods 0.000 claims description 3
- 238000004140 cleaning Methods 0.000 claims description 2
- 230000001105 regulatory effect Effects 0.000 claims 1
- 239000000126 substance Substances 0.000 abstract 1
- 239000010419 fine particle Substances 0.000 description 6
- 230000005484 gravity Effects 0.000 description 5
- 238000011084 recovery Methods 0.000 description 4
- 238000011069 regeneration method Methods 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 230000036571 hydration Effects 0.000 description 3
- 238000006703 hydration reaction Methods 0.000 description 3
- 239000012141 concentrate Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000008929 regeneration Effects 0.000 description 2
- 238000010923 batch production Methods 0.000 description 1
- 230000007423 decrease Effects 0.000 description 1
- 239000002612 dispersion medium Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 239000000725 suspension Substances 0.000 description 1
- 239000002966 varnish Substances 0.000 description 1
Landscapes
- Preparation Of Clay, And Manufacture Of Mixtures Containing Clay Or Cement (AREA)
Abstract
Description
【発明の詳細な説明】
[産業上の利用分野]
本発明は、生コンプラントで運搬車やプラントミキサ等
を洗ったときに発生する生コンクリートの洗い残渣の再
生方法及びその装置の改良に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a method for recycling the washing residue of ready-mixed concrete generated when a transport vehicle, a plant mixer, etc. are washed with ready-mixed concrete, and an improvement of the apparatus. be.
[従来の技術]
本出願人は、従来、利用方法が殆どなく、投棄するより
仕方なかった生コンクリートの洗い残渣からセメント未
水和物を乾燥することなく取り出して、これを新規なセ
メントと混ぜ合わせることにより高品質のコンクリート
を製造し得る生コンクリートの洗い残渣の再生方法及び
その装置について提案した(特開昭62−204867
)。[Prior Art] The present applicant has extracted unhydrated cement from the washing residue of ready-mixed concrete, which conventionally had little use and had no choice but to throw it away, without drying it, and mixed it with new cement. We proposed a method and device for recycling the washing residue of ready-mixed concrete that can produce high-quality concrete by combining them (Japanese Patent Application Laid-Open No. 62-204867
).
この再生方法は、最初に分級機により生コンクリートの
洗い残渣を湿式分級し、砂利及び砂を除去してスラッジ
水を取り出す。次いでシラフナによりこのスラッジ水の
スラッジを重力の作用で沈降させてスラッジ水を濃縮し
た後、濃度調整槽によりこの濃縮スラッジ水の濃度を更
に高めて所定濃度に調整する。そして最後に振動ボール
・ミルにより所定濃度のスラッジ水を振動微粉砕してセ
メント未水和物が表面に出現したスラッジ微粒子のスラ
リーを得るものである。In this regeneration method, the washed concrete residue is first wet-classified using a classifier, gravel and sand are removed, and sludge water is extracted. Next, the sludge water is sedimented by the action of gravity using Shirafuna to concentrate the sludge water, and then the concentration of the concentrated sludge water is further increased to a predetermined concentration using a concentration adjustment tank. Finally, the sludge water of a predetermined concentration is vibrated and pulverized using a vibrating ball mill to obtain a slurry of fine sludge particles in which unhydrated cement appears on the surface.
[発明が解決しようとする課題]
しかし、上記従来の再生方法は、シラフナでスラッジ水
中のセメントの低水和成分及び水和しないと思われる成
分も重力で沈降させ、この濃縮したスラッジ水を振動ボ
ール・ミルにより振動微粉砕するため、スラッジ微粒子
中の有用なセメント未水和物の含有率を向上し難い不具
合がある。[Problems to be Solved by the Invention] However, in the conventional regeneration method described above, the low hydration components of cement in the sludge water and the components that are considered not to be hydrated are allowed to settle by gravity, and this concentrated sludge water is shaken. Since vibration pulverization is performed using a ball mill, there is a problem in that it is difficult to increase the content of useful unhydrated cement in the sludge particles.
また濃縮機としてシラフナを用いるため、濃縮作業がバ
ッチ処理で比較的時間がかかり、かつシラフナの上澄み
水と区別して濃縮スラッジ水だけを取り出すことができ
ない。この結果、濃縮スラッジ水の濃度が低下し、振動
微粉砕の前に濃度調整槽でスラッジ水を高濃度化しなけ
ればならない問題点があった。Furthermore, since Shirafuna is used as a concentrator, the concentration work is a batch process and takes a relatively long time, and it is not possible to separate the concentrated sludge water from Shirafuna's supernatant water and take out only the concentrated sludge water. As a result, the concentration of the concentrated sludge water decreases, causing the problem that the sludge water must be concentrated in a concentration adjustment tank before vibration pulverization.
本発明の目的は、スラッジ水の濃縮時間が短く、かつ濃
度調整が容易で、スラッジ微粒子中のセメント未水和物
の含有率をより一層向上して洗い残渣を有効に利用し得
る生コンクリートの洗い残渣の再生方法及びその装置を
提供することにある。An object of the present invention is to provide a ready-mixed concrete that has a short concentration time for sludge water, is easy to adjust the concentration, and can further improve the content of unhydrated cement in sludge particles to effectively utilize washing residue. An object of the present invention is to provide a method for regenerating washing residue and an apparatus for the same.
[課題を解決するための手段]
本発明者らは、スラッジ水中のセメントの低水和成分及
び水和しないと思われる成分がセメント未水和成分より
比重が小さいことに着目し、本発明に到達した。[Means for Solving the Problems] The present inventors have focused on the fact that low hydration components of cement in sludge water and components that are considered not to be hydrated have a lower specific gravity than unhydrated components of cement, and have developed the present invention. Reached.
上記目的を達成するために、本発明の構成を第1図及び
実施例に対応する第2図に基づいて説明する。In order to achieve the above object, the configuration of the present invention will be explained based on FIG. 1 and FIG. 2 corresponding to an embodiment.
本発明の生コンクリートの洗い残渣の再生方法は、第1
図に示すように生コンクリートの洗い残渣を湿式分級し
て砂利G及び砂Sを除去したスラッジ水Hを取り出す分
級工程1と、このスラッジ水Hをセメント未水和物を主
成分とする高濃度スラッジ水KHと分離液Bとに分離す
るスラッジ水の濃縮工程2と、前記分離液Bを貯留して
上澄み水りを作り出す分離液の貯留工程5と、前記上澄
み水りにより前記高濃度スラッジ水KHを希釈して所定
濃度のスラッジ水Jに調整する濃度調整工程3と、所定
濃度のスラッジ水Jを振動ボール・ミルで振動微粉砕し
てセメント未水和物を主成分とするスラッジ微粒子のス
ラリーMを得る微粉砕工程4とを含むことを特徴とする
。The method for regenerating fresh concrete washing residue of the present invention includes the first
As shown in the figure, there is a classification step 1 in which the washing residue of fresh concrete is wet-classified to remove gravel G and sand S and sludge water H is taken out, and this sludge water H is highly concentrated with cement unhydrated as the main component. A step 2 of concentrating sludge water to separate it into sludge water KH and separated liquid B, a step 5 of storing separated liquid to create a supernatant water tank by storing the separated liquid B, and a step 5 of storing the separated liquid B to create a supernatant water tank, and the high concentration sludge water is Concentration adjustment step 3 in which KH is diluted and adjusted to sludge water J with a predetermined concentration, and sludge water J with a predetermined concentration is vibrated and pulverized in a vibrating ball mill to form sludge fine particles whose main component is unhydrated cement. The method is characterized in that it includes a pulverization step 4 for obtaining slurry M.
また本発明の生コンクリートの洗い残渣の再生装置は、
第2図に示すように生コンクリートの洗い残渣を湿式分
級して砂利G及び砂Sを除去したスラッジ水Hを取り出
す分級機10と、このスラッジ水Hを遠心力によりセメ
ント未水和物を主成分とする高濃度スラッジ水KHと分
離液Bとに漣続的に分離する濃縮機20と、前記分離液
B、を貯留する分離液貯留槽37と、この分離液貯留槽
37の上澄み水りにより前記高濃度スラッジ水KHを希
釈して所定濃度のスラッジ水Jに調整する濃度調整槽3
0と、前記所定濃度のスラッジ水J・を振動微粉砕して
セメント未水和物を主成分とするスラッジ微粒子のスラ
リーMを得る振動ボール・ミル40とを備えたことを特
徴とする。Furthermore, the apparatus for recycling fresh concrete washing residue of the present invention has the following features:
As shown in Fig. 2, a classifier 10 extracts sludge water H from which gravel G and sand S have been removed by wet-classifying fresh concrete washing residue, and a classifier 10 extracts sludge water H from which gravel G and sand S have been removed by wet-classifying fresh concrete washing residue. A concentrator 20 that continuously separates high concentration sludge water KH and separated liquid B as components, a separated liquid storage tank 37 that stores the separated liquid B, and a supernatant water of this separated liquid storage tank 37. a concentration adjustment tank 3 for diluting the high concentration sludge water KH and adjusting it to sludge water J of a predetermined concentration;
0, and a vibrating ball mill 40 for vibrating and pulverizing the sludge water J of the predetermined concentration to obtain a slurry M of sludge fine particles containing unhydrated cement as a main component.
[作 用]
分級機10で取り出されたスラッジ水Hは濃縮機20で
遠心力によりセメント未水和物を主成分とする高濃度ス
ラッジ水KHと分離液Bとに連続的に分離される。高濃
度スラッジ水KHは濃度調整槽30に直接供給され、分
離液Bはセメントの収水和成分及び水和しないと思われ
る成分を懸濁物質(Suspended 5olid)
として含有し、分離液貯留槽37に貯留される。[Function] The sludge water H taken out by the classifier 10 is continuously separated by centrifugal force into the high concentration sludge water KH containing unhydrated cement as a main component and the separated liquid B in the concentrator 20. The high-concentration sludge water KH is directly supplied to the concentration adjustment tank 30, and the separated liquid B is a suspended solid containing hydrated components of cement and components that are considered not to be hydrated.
The separated liquid is stored in the separated liquid storage tank 37.
分離液貯留槽37に貯えられた分離液の上澄み水りを濃
度調整槽30に供給して高濃度スラッジ水KHを所定濃
度に調整した後で振動ボール・ミル40により振動微粉
砕すると、セメント未水和物の含有率のより高いスラッ
ジ微粒子が得られる。The supernatant water of the separated liquid stored in the separated liquid storage tank 37 is supplied to the concentration adjustment tank 30 to adjust the high concentration sludge water KH to a predetermined concentration, and then it is vibrated and pulverized by the vibrating ball mill 40 to form a cement-free mixture. Sludge fine particles with a higher hydrate content are obtained.
[実施例]
次に本発明の一実施例を図面に基づいて詳しく説明する
。[Example] Next, an example of the present invention will be described in detail based on the drawings.
第2図及び第3図に示すように、生コンクリート運搬車
又は生コンクリートミキサ車11を洗ったときに発生す
る生コンクリートの洗い水12がウェッジフィルタ13
及びスパイラルクラシファイヤ14からなる分級機10
により砂利Gと砂Sとスラッジ水Hに湿式分級される。As shown in FIGS. 2 and 3, the fresh concrete washing water 12 generated when washing the ready-mixed concrete transport vehicle or the ready-mixed concrete mixer vehicle 11 is filtered through the wedge filter 13.
and a classifier 10 consisting of a spiral classifier 14
It is wet classified into gravel G, sand S, and sludge water H.
すなわち洗い水12は回収槽15に回収され、この回収
槽15の底部に設多すられたポンプ15aにより管路1
6を通ってウェッジフィルタ13に供給され、砂利Gが
除去される。砂利Gはタンク13aに貯蔵される。砂利
Gを除去した洗い水はスパイラルクラシファイヤ14に
供給され、砂Sとスラッジ水Hに分級される。砂Sはタ
ンク14b内に貯蔵される。スラッジ水Hは、水を分散
媒とし、セメント未水和物とセメント水和物とからなる
スラッジを分散相とする懸濁液になっている。このスラ
ッジ水槽エ
に還流される。That is, the washing water 12 is collected in a recovery tank 15, and pumps 15a installed at the bottom of this recovery tank 15 are used to drain the pipe 1.
6 and is supplied to a wedge filter 13, where gravel G is removed. Gravel G is stored in tank 13a. Washing water from which gravel G has been removed is supplied to a spiral classifier 14, where it is classified into sand S and sludge water H. Sand S is stored in tank 14b. The sludge water H is a suspension in which water is used as a dispersion medium and sludge consisting of unhydrated cement and hydrated cement is used as a dispersed phase. The sludge is refluxed into the sludge tank.
回収槽15の上澄み水はポンプ15bにより管路17及
びサイクロン18を通ってスラッジ水槽24に送られる
。サイクロン18で残存する砂を分離してスパイラルク
ラシファイヤ14に戻す。The supernatant water in the recovery tank 15 is sent to the sludge tank 24 through the pipe 17 and the cyclone 18 by the pump 15b. The remaining sand is separated by a cyclone 18 and returned to the spiral classifier 14.
15cは液面スイッチで、回収槽15が所定の水位にな
ると、オン状態となりポンプ15bを回転駆動させる。A liquid level switch 15c is turned on when the water level in the recovery tank 15 reaches a predetermined level, driving the pump 15b to rotate.
スラッジ水槽24で攪拌機24aを低速度で攪拌してス
ラッジ水Hの硬化を防ぎながら、その底部のスラッジ濃
度5冗程度のスラッジ水Hがポンプ25により管路26
を通って濃縮機20に送られる。24bは液面スイッチ
で、スラッジ水槽24が所定の水位になると、オン状態
となりポンプ25を回転駆動させる。While stirring the sludge water H at a low speed with the agitator 24a in the sludge water tank 24 to prevent the sludge water H from hardening, the sludge water H at the bottom with a sludge concentration of about 5% is pumped into the pipe 26 by the pump 25.
and is sent to the concentrator 20. 24b is a liquid level switch which is turned on when the sludge water tank 24 reaches a predetermined water level, causing the pump 25 to rotate.
濃縮機20は外胴ボウル5oと内胴スクリュー60とフ
ィードバイブ7oとギヤボックス8oとケーシング85
を備えた遠心沈降機により構成される。外胴ボウル50
は円筒部51及び円錐部52が一体的に形成され、その
両端が軸受53及び54により回転可能に支持され、が
っ大径側に第1排出口56と小径側に第2υト出ロ57
とがそれぞれ設けられる。内胴スクリュー6oはスクリ
ュー羽根61が固着された胴体に吐出口62が設けられ
、前記円筒部51内及び円錐部52内に回転可能に支持
される。The concentrator 20 includes an outer bowl 5o, an inner screw 60, a feed vibe 7o, a gear box 8o, and a casing 85.
It consists of a centrifugal sedimentation machine equipped with Outer body bowl 50
A cylindrical portion 51 and a conical portion 52 are integrally formed, and both ends thereof are rotatably supported by bearings 53 and 54, and a first outlet 56 is provided on the larger diameter side and a second υ outlet hole 57 is provided on the smaller diameter side.
and are provided respectively. The inner barrel screw 6o is provided with a discharge port 62 in a barrel to which a screw blade 61 is fixed, and is rotatably supported within the cylindrical portion 51 and the conical portion 52.
またフィードパイプ7oはこの胴体内に配置され、管路
26から送られてきたスラッジ水を内胴スクリュー60
内に導入する。ケーシング85は外胴ボウル50を被包
し、第1排出ロ56側に分離液出口86と第2排出ロ5
7側に高濃度スラッジ水出口87をそれぞれ設けている
。Further, the feed pipe 7o is arranged inside this body, and the sludge water sent from the pipe line 26 is fed to the inner body screw 60.
to be introduced within. The casing 85 encloses the outer bowl 50 and has a separated liquid outlet 86 and a second discharge hole 5 on the side of the first discharge hole 56.
A high concentration sludge water outlet 87 is provided on each side.
ギヤボックス80はプーリ81により駆動される遊星歯
車装置からなる。このギヤボックス80は外胴ボウル5
0と内胴スクリュー60とを内胴スクリュー60の回転
速度が外胴ボウル50の回転速度より若干小さくなるよ
うに回転差を与えながら同一回転方向に駆動する。この
駆動中にポンプ25により送られたスラッジ水Hを濃縮
機20のフィードパイプ70から内胴スクリュー、60
内に導入すると、スラッジ水中の比重の大きいセメント
未水和物を主成分とするスラッジ分には遠心力により外
胴ボウル50の円筒部51の内壁面に堆積する(第3図
)。このスラッジ分には内胴スクリュー60のスクリュ
ー羽根61の回転により矢印に示すように円錐部52に
移行し、第2排出口57を通ってスラッジ濃度が60〜
70%の高濃度スラッジ水K Hの形態で出口87より
排出される。Gear box 80 consists of a planetary gear set driven by pulley 81. This gear box 80 has the outer body bowl 5
0 and the inner barrel screw 60 are driven in the same rotational direction while giving a rotational difference so that the rotational speed of the inner barrel screw 60 is slightly smaller than the rotational speed of the outer barrel bowl 50. During this drive, the sludge water H sent by the pump 25 is sent from the feed pipe 70 of the concentrator 20 to the inner barrel screw 60.
When the sludge water is introduced into the sludge water, the sludge mainly composed of unhydrated cement having a high specific gravity is deposited on the inner wall surface of the cylindrical portion 51 of the outer bowl 50 due to centrifugal force (FIG. 3). This sludge transfers to the conical part 52 as shown by the arrow by the rotation of the screw blade 61 of the inner barrel screw 60, passes through the second discharge port 57, and reaches a sludge concentration of 60~
The sludge water is discharged from the outlet 87 in the form of 70% high concentration sludge water KH.
一方、スラッジ分により分離した液Bはスラッジ水中の
比重の小さいセメントの収水和成分及び水和しないと思
われる成分を懸濁物質(5uspendedSolid
)として5〜15%程度含有し、第1排出口56を通っ
て出口86から吐出し、管路27を通って分離液貯留槽
37に送られる。On the other hand, the liquid B separated by the sludge content contains the hydrated components of cement with a small specific gravity in the sludge water and the components that do not seem to be hydrated.
), and is discharged from the outlet 86 through the first discharge port 56 and sent to the separation liquid storage tank 37 through the pipe line 27.
出口87より排出された高濃度スラッジ水KHは導管3
1により案内されて、出口87の直下に配置された濃度
調整槽30に貯蔵される。分離液貯留槽37の分離液の
上澄み水りがポンプ33により管路34を通って濃度調
整槽30に供給され、攪拌機30aを攪拌して高濃度ス
ラッジ水KHが所定濃度のスラッジ水Jに希釈される。The high concentration sludge water KH discharged from the outlet 87 is transferred to the conduit 3.
1 and stored in the concentration adjustment tank 30 located directly below the outlet 87. The supernatant water of the separated liquid in the separated liquid storage tank 37 is supplied by the pump 33 through the pipe line 34 to the concentration adjustment tank 30, and is stirred by the agitator 30a to dilute the high concentration sludge water KH to sludge water J of a predetermined concentration. be done.
この例では調整槽30の送出口30bにおけるスラッジ
濃度の測定値に基づいて、スラッジ濃度が30%〜40
%の範囲内に調整される。スラッジ濃度が所定の濃度に
なれば、ポンプ35により管路36を通って所定濃度の
スラッジ水Jを振動ボール・ミル40に送る。In this example, the sludge concentration is 30% to 40% based on the measured value of the sludge concentration at the outlet 30b of the adjustment tank 30.
Adjusted within the range of %. When the sludge concentration reaches a predetermined concentration, the pump 35 sends sludge water J having a predetermined concentration to the vibrating ball mill 40 through the pipe line 36.
このスラッジ水Jは振動ボール・ミル40により振動微
粉砕される。この例では振動ボール・ミル40は第1段
のミル40aと第2段のミル40bからなる。振動微粉
砕されたスラリーMはスラリー貯留槽42に送られ、攪
拌機42aで硬化を防ぎながら貯えられる。このスラリ
ーMの分散相はセメント未水和物の含有率のより高いス
ラッジ微粒子になる。このスラッジ微粒子を定量ポンプ
43により必要量だけプラントミキサに送出し、新規な
セメントに加えて生コンクリートを調製すれば、生コン
クリートの洗い残渣を有効利用することができる。This sludge water J is vibrated and pulverized by a vibrating ball mill 40. In this example, the vibratory ball mill 40 consists of a first stage mill 40a and a second stage mill 40b. The vibration-pulverized slurry M is sent to the slurry storage tank 42, and is stored therein while being prevented from hardening by an agitator 42a. The dispersed phase of this slurry M becomes sludge fine particles with a higher content of unhydrated cement. By sending the required amount of the sludge particles to the plant mixer using the metering pump 43 and adding them to new cement to prepare fresh concrete, the washing residue of the fresh concrete can be effectively used.
また分離液貯留槽37に貯留される分離液はポンプ38
により管路39を通って生コンクリート運搬車又は生コ
ンクリートミキサ車12等の生コンクリート付着物の洗
浄に使用される。ここで分離液に含まれるセメントの収
水和成分及び水和しないと思われる成分は砂利、砂に吸
着してそれぞれタンク13a又は14a内に貯蔵される
。The separated liquid stored in the separated liquid storage tank 37 is pumped by a pump 38.
It passes through a conduit 39 and is used for cleaning fresh concrete deposits from a fresh concrete transport vehicle or a fresh concrete mixer vehicle 12 or the like. Here, the hydrated components of the cement contained in the separated liquid and the components considered not to be hydrated are adsorbed to gravel and sand and stored in the tank 13a or 14a, respectively.
上記実施例の再生装置によれば、特開昭62−2048
67号公報の再生装置と比較して、セメント未水和物の
含有率を2〜3倍以上向上させることができた。According to the reproducing apparatus of the above embodiment, Japanese Patent Application Laid-Open No. 62-2048
Compared to the regeneration device of Publication No. 67, the content of unhydrated cement could be increased by 2 to 3 times or more.
[発明の効果]
以上述べたように、従来、濃縮スラッジ水にセメント未
水和物の外にセメントの収水和成分及び水和しないと思
われる成分を含んでいたため、振動ボール・ミルで微粉
砕したスラッジ微粒子のセメント未水和物の含有率を十
分に向上できながったものが、本発明によればセメント
の収水和成分及び水和しないと思われる成分を懸濁物質
(Sus−pended 5olid)として分離液に
含有させ、高濃度スラッジ水に含ませないため、振動ボ
ール・ミルで微粉砕したスラッジ微粒子のセメント未水
和物の含有率をより一層向上することができる。この結
果、本発明のスラッジ微粒子を用いたコンクリートの品
質を安定して高めることができ、新規なセメント量を節
減することができる。[Effects of the Invention] As mentioned above, conventionally, concentrated sludge water contained cement hydration components and components that are considered not to be hydrated in addition to unhydrated cement. According to the present invention, the content of unhydrated cement in finely pulverized sludge particles cannot be sufficiently improved, but according to the present invention, hydrated components of cement and components that are considered not to be hydrated are removed by suspended solids ( Since it is contained in the separated liquid as a suspended solid (Sus-pended 5 solid) and not contained in the high concentration sludge water, it is possible to further improve the content of unhydrated cement in the sludge fine particles pulverized with a vibrating ball mill. As a result, the quality of concrete using the sludge fine particles of the present invention can be stably improved, and the amount of new cement can be reduced.
特に、本発明の濃縮機は連続的にかつ高濃度にスラッジ
水を濃縮できるので、スラッジ水の濃縮効率が高く、濃
度調整が容易になり、装置全体の再生効率を向上させる
ことができる。In particular, since the concentrator of the present invention can continuously concentrate sludge water to a high concentration, the efficiency of concentrating sludge water is high, the concentration can be easily adjusted, and the regeneration efficiency of the entire apparatus can be improved.
第1図は本発明生コンクリートの洗い残渣の再生方法を
説明するためのブロック図。
第2図は本発明一実施例の生コンクリートの洗い残渣の
再生装置の構成図。
第3図はその濃縮機の要部拡大断面図。
H:スラッジ水、
KH:高濃度スラッジ水
B:分離液、
L:上澄み水、
J:所定濃度のスラッジ水、
Mニスラリ−
10:分級機、
20:濃縮機、
30:濃度調整槽、
37:分離液貯留槽、
40:振動ボール・ミル、
50:外胴ボウル、
51:円筒部、
52:円錐部、
53.54:軸受、
56:第1排出口、
57:第2排出口、
60:内胴スクリュー
61ニスクリユ一羽根、
62:吐出口、
70:フィードパイプ、
80:ギヤボックス、
85:ケーシング、
86:分離液出口、
87:高濃度スラッジ水出口。FIG. 1 is a block diagram for explaining the method for recycling fresh concrete washing residue according to the present invention. FIG. 2 is a block diagram of an apparatus for recycling fresh concrete washing residue according to an embodiment of the present invention. Figure 3 is an enlarged sectional view of the main parts of the concentrator. H: sludge water, KH: high concentration sludge water, B: separated liquid, L: supernatant water, J: sludge water with predetermined concentration, M Nislurry 10: classifier, 20: concentrator, 30: concentration adjustment tank, 37: Separated liquid storage tank, 40: Vibrating ball mill, 50: Outer bowl, 51: Cylindrical part, 52: Conical part, 53.54: Bearing, 56: First discharge port, 57: Second discharge port, 60: Inner body screw 61 varnish screw, 62: discharge port, 70: feed pipe, 80: gear box, 85: casing, 86: separated liquid outlet, 87: highly concentrated sludge water outlet.
Claims (1)
砂を除去したスラッジ水を取り出す分級工程と、 このスラッジ水をセメント未水和物を主成分とする高濃
度スラッジ水と分離液とに分離するスラッジ水の濃縮工
程と、 前記分離液を貯留して上澄み水を作り出す分離液貯留工
程と、 前記上澄み水により前記高濃度スラッジ水を希釈して所
定濃度のスラッジ水に調整する濃度調整工程と、 所定濃度のスラッジ水を振動ボール・ミルで振動微粉砕
してセメント未水和物を主成分とするスラッジ微粒子の
スラリーを得る微粉砕工程とを含む生コンクリートの洗
い残渣の再生方法。 2)分離液を生コンクリート付着物の洗浄に使用する請
求項1記載の生コンクリートの洗い残渣の再生方法。 3)生コンクリートの洗い残渣を湿式分級して砂利及び
砂を除去したスラッジ水を取り出す分級機と、 このスラッジ水を遠心力によりセメント未水和物を主成
分とする高濃度スラッジ水と分離液とに連続的に分離す
る濃縮機と、 前記分離液を貯留する分離液貯留槽と、 前記分離液貯留槽の上澄み水により前記高濃度スラッジ
水を希釈して所定濃度のスラッジ水に調整する濃度調整
槽と、 前記所定濃度のスラッジ水を振動微粉砕してセメント未
水和物を主成分とするスラッジ微粒子のスラリーを得る
振動ボール・ミルと を備えた生コンクリートの洗い残渣の再生装置。 4)濃縮機は、円筒部及び円錐部が一体的に形成され、
両端が軸受により回転可能に支持され、かつ大径側に第
1排出口と小径側に第2排出口とがそれぞれ設けられた
外胴ボウルと、 スクリュー羽根が固着された胴体に吐出口が設けられ、
かつ前記円筒部内及び円錐部内に回転可能に支持された
内胴スクリューと、 前記分級機から取り出されたスラッジ水を前記内胴スク
リュー内に導入するフィードパイプと、前記外胴ボウル
と前記内胴スクリューに同一方向で前記内胴スクリュー
の回転速度が前記外胴ボウルの回転速度より若干小さく
なるように回転差を与えるギヤボックスと、前記外胴ボ
ウルを被包し、前記第1排出口側に分離液出口と前記第
2排出口側に高濃度スラッジ水出口がそれぞれ設けられ
たケーシングと を備えた請求項3記載の生コンクリートの洗い残渣の再
生装置。[Scope of Claims] 1) A classification step of wet-classifying fresh concrete washing residue to remove gravel and sand and extracting sludge water; a step of concentrating sludge water to separate it into a separated liquid; a separating liquid storage step of storing the separated liquid to produce supernatant water; and diluting the highly concentrated sludge water with the supernatant water to obtain sludge water of a predetermined concentration. and a pulverization step of vibrating and pulverizing sludge water of a predetermined concentration using a vibrating ball mill to obtain a slurry of sludge particles containing unhydrated cement as a main component. How to play. 2) The method for recycling fresh concrete washing residue according to claim 1, wherein the separated liquid is used for cleaning the fresh concrete deposits. 3) A classifier that wet-classifies fresh concrete washing residue to remove gravel and sand and extracts sludge water, and separates this sludge water from high-concentration sludge water mainly composed of unhydrated cement using centrifugal force. a concentrator that continuously separates the separated liquid, a separated liquid storage tank that stores the separated liquid, and a concentration that adjusts the high concentration sludge water to a predetermined concentration by diluting the high concentration sludge water with supernatant water of the separated liquid storage tank. An apparatus for regenerating fresh concrete washing residue, comprising a regulating tank and a vibrating ball mill that vibrates and pulverizes the sludge water of a predetermined concentration to obtain a slurry of fine sludge particles containing unhydrated cement as a main component. 4) The concentrator has a cylindrical part and a conical part integrally formed,
The outer body bowl is rotatably supported by bearings at both ends and has a first discharge port on the large diameter side and a second discharge port on the small diameter side, and a discharge port is provided in the body to which the screw blade is fixed. is,
and an inner screw rotatably supported within the cylindrical portion and the conical portion, a feed pipe for introducing sludge water taken out from the classifier into the inner screw, the outer bowl and the inner screw. a gear box that provides a rotational difference such that the rotational speed of the inner screw is slightly smaller than the rotational speed of the outer bowl in the same direction; and a gear box that encloses the outer bowl and is separated to the first discharge port side. 4. The apparatus for recycling fresh concrete washing residue according to claim 3, comprising a liquid outlet and a casing provided with a high concentration sludge water outlet on the second discharge port side.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63317122A JPH0620740B2 (en) | 1988-12-15 | 1988-12-15 | Method and apparatus for reclaiming washing residue of green concrete |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP63317122A JPH0620740B2 (en) | 1988-12-15 | 1988-12-15 | Method and apparatus for reclaiming washing residue of green concrete |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02162003A true JPH02162003A (en) | 1990-06-21 |
JPH0620740B2 JPH0620740B2 (en) | 1994-03-23 |
Family
ID=18084683
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP63317122A Expired - Lifetime JPH0620740B2 (en) | 1988-12-15 | 1988-12-15 | Method and apparatus for reclaiming washing residue of green concrete |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0620740B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0492675A1 (en) * | 1990-12-20 | 1992-07-01 | Dirk De Neef | Process for the consolidation of waste sludge or similar |
JP2009023291A (en) * | 2007-07-23 | 2009-02-05 | Aizawa Koatsu Concrete Kk | Method and drum for retrieving rinse water of truck agitator drum |
CN113045234A (en) * | 2021-03-19 | 2021-06-29 | 惠州市鑫业建材有限公司 | Slurry recycling system and process |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49120914A (en) * | 1973-03-23 | 1974-11-19 | ||
JPS62204867A (en) * | 1986-03-05 | 1987-09-09 | P M Concrete Eng:Kk | Method and apparatus for regenerating washing residue of ready-mixed concrete |
-
1988
- 1988-12-15 JP JP63317122A patent/JPH0620740B2/en not_active Expired - Lifetime
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49120914A (en) * | 1973-03-23 | 1974-11-19 | ||
JPS62204867A (en) * | 1986-03-05 | 1987-09-09 | P M Concrete Eng:Kk | Method and apparatus for regenerating washing residue of ready-mixed concrete |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0492675A1 (en) * | 1990-12-20 | 1992-07-01 | Dirk De Neef | Process for the consolidation of waste sludge or similar |
JP2009023291A (en) * | 2007-07-23 | 2009-02-05 | Aizawa Koatsu Concrete Kk | Method and drum for retrieving rinse water of truck agitator drum |
CN113045234A (en) * | 2021-03-19 | 2021-06-29 | 惠州市鑫业建材有限公司 | Slurry recycling system and process |
Also Published As
Publication number | Publication date |
---|---|
JPH0620740B2 (en) | 1994-03-23 |
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