JP2002254099A - Recovering method of fine powder of concrete sludge, device therefor and fine powder of concrete sludge - Google Patents

Recovering method of fine powder of concrete sludge, device therefor and fine powder of concrete sludge

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Publication number
JP2002254099A
JP2002254099A JP2001057417A JP2001057417A JP2002254099A JP 2002254099 A JP2002254099 A JP 2002254099A JP 2001057417 A JP2001057417 A JP 2001057417A JP 2001057417 A JP2001057417 A JP 2001057417A JP 2002254099 A JP2002254099 A JP 2002254099A
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JP
Japan
Prior art keywords
sludge
water
fine
concrete
mass
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
Application number
JP2001057417A
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Japanese (ja)
Other versions
JP4698043B2 (en
Inventor
Yoshiaki Sato
嘉昭 佐藤
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Individual
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Individual
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Priority to JP2001057417A priority Critical patent/JP4698043B2/en
Publication of JP2002254099A publication Critical patent/JP2002254099A/en
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Publication of JP4698043B2 publication Critical patent/JP4698043B2/en
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Classifications

    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/30Wastewater or sewage treatment systems using renewable energies
    • Y02W10/37Wastewater or sewage treatment systems using renewable energies using solar energy

Landscapes

  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Treatment Of Sludge (AREA)
  • Crushing And Grinding (AREA)
  • Disintegrating Or Milling (AREA)

Abstract

PROBLEM TO BE SOLVED: To recover the fine powder of concrete sludge which is good in quality and suitable for recycling by removing fine sand contained in wastewater formed by washing as much as possible. SOLUTION: The fine powder 15 contained in the wastewater 10 formed by washing in concrete treating facilities is removed so that a sand content can become 10 mass % or below (S1), and an inorganic flocculant 18 is added to the recovered water 16 thus obtained to separate supernatant water 19 of the recovered water and the sludge water (S2) from the recovered water. Then, the separated sludge water is dehydrated to form dehydrated cake 23 (S3), the dehydrated cake 23 is ground before hardened (S4) and rolled flatly in thickness of 10 to 15 mm, and the ground dehydrated cake is dried so as to achieve a water content of 50 to 60 mass % and its maximum particle size of at most 20 mm (S5), the dried sludge 26 thus obtained is finely ground with a grinding device 27 making use of wind power to produce fine and round particles (S6), and then the fine powder PDS of the concrete sludge is recovered by collecting the fine particle thus produced (S7).

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、建設現場、コンク
リート製品工場、レディーミクスト工場、砕石工場等の
土木建築に関連する分野から発生する廃水から、乾燥し
たコンクリートスラッジ微粉末(PDS:Pulver
ized Dry Sludge)を回収するコンクリ
ートスラッジ微粉末回収方法および装置ならびにコンク
リートスラッジ微粉末に関する。
BACKGROUND OF THE INVENTION The present invention relates to dry concrete sludge fine powder (PDS: Pulver) from wastewater generated from fields related to civil engineering such as construction sites, concrete product factories, ready mixed factories and crushed stone factories.
TECHNICAL FIELD The present invention relates to a method and an apparatus for collecting fine sludge of concrete sludge for collecting dried slurry.

【0002】[0002]

【従来の技術】コンクリート構造物は、我が国では18
82年に初めて建造され、以来100年あまりが経過し
ている。ここ数年は、建物の建て替えの時期、あるいは
改築・増築が盛んに行われるような時期に至ったことか
ら、解体されたコンクリート塊の再資源化に向けての動
きが活発である。
2. Description of the Related Art Concrete structures are widely used in Japan.
It was first built in 1982 and has been around for over 100 years. In the last few years, the time has come for rebuilding or remodeling and expansion of buildings, and there is a growing movement to recycle dismantled concrete blocks.

【0003】「廃棄物の処理及び清掃に関する法律」、
いわゆる廃棄物処理法で分類された産業廃棄物の中で安
定5品目の1つに上げられている建設廃材は、「再生資
源の利用の促進に関する法律」、いわゆるリサイクル法
において、有効利用を促進し、リサイクル率を高めるよ
うに品質などを工夫すべき副産物に指定されている。
[0003] "Waste Disposal and Cleaning Law",
Construction waste materials, which are listed as one of the five stable items among industrial waste classified by the so-called Waste Disposal Law, promote effective use in the "Law Concerning the Use of Recycled Resources", the so-called Recycling Law. In addition, it is designated as a by-product whose quality should be devised so as to increase the recycling rate.

【0004】一方、コンクリートを供給する側の環境対
策の状況は非常に立ち遅れている。コンクリートを供給
する工場が抱える共通の環境問題は、ミキサーやアジテ
ータ車の洗い廃水や、残コンクリート、戻りコンクリー
トを処理した廃水に含まれる固形分(砂・砂利は回収し
て、再利用するシステムになっている)の処理である。
前記の廃棄物処理法では、コンクリートスラッジと呼ば
れている固形分は汚泥の範疇に属し、廃棄処分する場合
には管理型埋立処分場で処分することが定められてい
る。しかし、コストや立地条件の観点から、このような
管理型処分場を将来にわたって安定的に確保することは
困難であり、スラッジを廃棄せずに有効利用する方法が
従来種々提案されている。なかでもスラッジを乾燥、粉
砕する技術が、得られた粉粒状スラッジの利用範囲が広
いことから実用的な技術として注目されている。
[0004] On the other hand, the situation of environmental measures on the side of supplying concrete is far behind. A common environmental problem for factories that supply concrete is the solid content in the wastewater from the washing of mixers and agitator trucks, as well as the wastewater from the processing of residual concrete and returned concrete (sand and gravel are collected and reused. Processing).
In the above-mentioned waste treatment method, the solid content called concrete sludge belongs to the category of sludge, and it is stipulated that when it is disposed of, it is disposed of in a managed landfill site. However, it is difficult to stably secure such a managed disposal site in the future from the viewpoint of cost and location conditions, and various methods for effectively utilizing sludge without discarding it have been proposed. Above all, the technology of drying and pulverizing sludge has attracted attention as a practical technology because of the wide range of use of the obtained granular sludge.

【0005】たとえば、特開平7−315971号公報
には、固形物含有量20〜70質量%の生コンスラッジ
を、フィルタープレスなどの脱水機で脱水するかまたは
天日乾燥などで乾燥した脱水ケーキと、水またはコンク
リートプラントなどの廃水を添加して、ミキサーで均一
に混合撹拌し、スプレードライヤーで乾燥造粒して平均
粒径50〜100μmの顆粒状または球状で施用時発塵
や運搬時の崩壊のない取扱い性の優れたスラッジ粒状物
とし、珪酸石灰肥料として再利用する方法が開示されて
いる。
For example, Japanese Unexamined Patent Publication (Kokai) No. 7-315971 discloses that a raw dehydrated cake having a solid content of 20 to 70% by mass is dehydrated by a dehydrator such as a filter press or dried by solar drying or the like. Add water, waste water from a concrete plant, etc., mix and stir evenly with a mixer, dry granulate with a spray drier, and granulate or spherical with an average particle size of 50-100 μm. A method is disclosed in which sludge granules having excellent handling properties without waste are reused as silicate lime fertilizer.

【0006】また、特開平9−217343号公報に
は、残存生コンクリートの骨材を分離したスラッジを3
〜4時間以内に脱水して得られた活性脱水ケーキを所定
養生時間経過後、造粒装置にて粒状として粒状ケーキを
つくり、これを有天蓋の貯留場で所定日数養生をして含
水率22〜23%としたものを乾燥と粉砕工程を経て含
水率5〜6%以下で粒径0.15mm以下の粉粒体と
し、この粉粒体を土木工事現場で泥土に混入したり、軟
弱地盤の泥土に混入したりする再利用法が開示されてい
る。
[0006] Japanese Patent Application Laid-Open No. 9-217343 discloses that sludge separated from aggregate of remaining ready-mixed concrete contains 3 sludges.
After elapse of a predetermined curing time, the active dehydrated cake obtained by dehydration within 4 hours is granulated by a granulator to form a granular cake, which is cured for a predetermined number of days in a storage area of a canopy to obtain a water content of 22%. Drying and pulverizing processes are carried out to obtain a powder having a water content of 5 to 6% or less and a particle diameter of 0.15 mm or less. A reusing method for mixing in mud is disclosed.

【0007】また本発明者らは、生コンスラッジの発生
時点で乾燥処理を行い含水率30%以下にした脱水ケー
キを、旋回気流を用いた風力粉砕機で粉砕して乾燥スラ
ッジを製造する技術を開発した(コンクリートスラッジ
の有効利用に関するシンポジウム 論文報告集 199
6.5参照)。この風力粉砕機で粉砕した粉粒体は、J
IS R5201 セメントの物理試験方法によるブレ
ーン比表面積が6800cm2/g程度の微粒子とな
り、生コン混和材、空隙充填材、軽量盛土材、土壌改良
材などに使用することができる。
Further, the present inventors have developed a technology for producing a dried sludge by pulverizing a dewatered cake having a water content of 30% or less by a drying treatment at the time of generation of raw con sludge with a wind pulverizer using a swirling air flow. Developed (Symposium on Effective Use of Concrete Sludge Proceedings 199
6.5). The powder and granules crushed by this wind crusher are J
IS R5201 Fine particles having a specific surface area of about 6800 cm 2 / g according to the physical test method of cement can be used as a ready-mixed concrete admixture, a void filler, a lightweight embankment material, a soil improvement material, and the like.

【0008】上記のように生コンスラッジを乾燥、粒状
化することにより、生コンスラッジの再利用範囲も拡大
されつつある。しかしながら、上記した従来の生コンス
ラッジの乾燥、粒状化の方法においては、スラッジの脱
水ないし乾燥の効率が低く、また、得られる粉粒体の粒
径に限界がある。
[0008] As described above, by drying and granulating the raw consludge, the range of reuse of the raw consludge is also expanding. However, in the above-mentioned conventional methods for drying and granulating raw sludge, the efficiency of dewatering or drying the sludge is low, and the particle size of the obtained granules is limited.

【0009】前記特開平7−315971号公報記載の
方法では、スラッジの脱水は脱水機または天日乾燥で行
っているので含水率50%程度までしか脱水することが
できず、しかもこのような含水率のものをスプレードラ
イヤーで乾燥造粒するのであるから、造粒後の粒状体は
平均粒径50〜100μm程度のものしか得られない。
In the method described in Japanese Patent Application Laid-Open No. 7-315971, since the sludge is dehydrated by a dehydrator or solar drying, it can be dehydrated only up to a water content of about 50%. Since the granules having the above-mentioned ratio are dried and granulated by a spray dryer, the granulated granules having an average particle size of only about 50 to 100 μm can be obtained.

【0010】前記特開平9−217343号公報記載の
方法では、脱水ケーキの養生と粒状ケーキの養生に日数
を要し、また粉砕後の粉粒体は粒径150μm程度以下
のものしか得られない。
According to the method described in JP-A-9-217343, it takes a long time to cure the dehydrated cake and the granular cake, and it is only possible to obtain a powdered or granular material having a particle size of about 150 μm or less. .

【0011】また、前記論文報告集記載の方法でも、ス
ラッジの乾燥は単に熱風を吹き付けて乾燥するだけのも
のであるから、風力粉砕機に投入する段階での脱水ケー
キは粒径30〜50mm程度の比較的大きなものであ
り、風力粉砕機で得られる粉粒体は平均粒径10〜20
μm程度のものしか得られない。
Also, in the method described in the above-mentioned collection of papers, the drying of sludge is simply performed by blowing hot air, so that the dewatered cake at the stage of being introduced into a wind pulverizer has a particle size of about 30 to 50 mm. Are relatively large, and the powder and granules obtained by the wind pulverizer have an average particle size of 10 to 20.
Only about μm can be obtained.

【0012】このような問題を解決するために、本発明
者らは、先に、生コンクリート製造工場などで発生した
スラッジスラリーを沈殿分離させた後のスラッジを乾燥
し粉砕して粉粒状スラッジとするスラッジの処理方法で
あって、前記沈殿分離後のスラッジを脱水処理して含水
率60%以下とした脱水スラッジを熱風乾燥により含水
率20%以下に乾燥し且つ乾燥途中で粒径15mm以下
に粉砕する乾燥粉砕工程と、前記乾燥粉砕工程後の乾燥
スラッジを旋回気流を用いた風力粉砕によりブレーン比
表面積が7000cm2/g以上となる粒径まで粉砕す
る微粉砕工程と、前記微粉砕工程後の粉粒状スラッジを
捕集する捕集工程とを含むスラッジの処理方法を提案
し、出願した(特願平11−194749号)。
In order to solve such a problem, the present inventors have previously settled and separated sludge slurry generated in a ready-mixed concrete manufacturing plant or the like, dried and pulverized the sludge, and formed a powdery granular sludge. A method of treating sludge, wherein the sludge after the sedimentation and separation is dewatered to a water content of 60% or less, and the dewatered sludge is dried to a water content of 20% or less by hot air drying and a particle size of 15 mm or less during drying. A drying and pulverizing step of pulverizing, a pulverizing step of pulverizing the dried sludge after the drying and pulverizing step by a wind pulverization using a swirling air stream to a particle size having a Blaine specific surface area of 7000 cm 2 / g or more; And a collecting process for collecting the powdery and granular sludge of the present invention was proposed and filed (Japanese Patent Application No. 11-194749).

【0013】[0013]

【発明が解決しようとする課題】ところで、洗浄廃水中
に含まれる微砂分は回収水の化学成分を分析する際に、
不溶残分(Insol.)として検出される量であり、
特に、泥分が多く含まれる場合には、これを含む水を練
り混ぜ水に再利用してコンクリートを製造するとその特
性に悪影響を及ぼす可能性があることが指摘されてい
る。そのため、JIS規定(JIS A 5308)で
はスラッジ固形分の量が単位セメント量当たり3質量%
以内とされているが、洗浄廃水の処理の段階で不純物と
なる微砂分を取り除くことができれば、含砂率の低い、
質の良い回収水が得られ、未利用資源として活用でき
る。
By the way, the fine sand content contained in the washing wastewater, when analyzing the chemical components of the recovered water,
An amount detected as an insoluble residue (Insol.),
In particular, it has been pointed out that, when a large amount of mud is contained, the properties of the concrete may be adversely affected if water containing the same is mixed and reused as water to produce concrete. Therefore, according to JIS regulations (JIS A 5308), the amount of sludge solid content is 3% by mass per unit cement.
However, if fine sand that is an impurity can be removed at the stage of treatment of washing wastewater, the sand content is low.
High quality recovered water can be obtained and can be used as unused resources.

【0014】しかしながら、前述した先の出願に係るス
ラッジの処理方法においては、特に微砂分の除去につい
ては考慮が払われておらず、含砂率の低い回収水を得る
ことができなかった。
However, in the above-mentioned method for treating sludge according to the above-mentioned application, no consideration is given particularly to the removal of fine sand, and it is not possible to obtain recovered water having a low sand content.

【0015】本発明において解決すべき課題は、洗浄廃
水中に含まれる微砂分を可能な限り除去し、再利用に適
した質のよいコンクリートスラッジ微粉末を回収するこ
とにある。
An object of the present invention is to remove fine sand contained in washing wastewater as much as possible and to recover high quality concrete sludge fine powder suitable for reuse.

【0016】[0016]

【課題を解決するための手段】前記の課題を解決するた
め、本発明のコンクリートスラッジ微粉末回収方法は、
コンクリート製品工場、レディーミクスト工場等のコン
クリート処理設備から発生する洗浄廃水に含まれる微砂
分を含砂率が10質量%以下となるように除去した回収
水を得る微砂除去工程と、この微砂除去工程で得られた
回収水に無機系凝集剤を添加して回収水上澄み水とスラ
ッジ水に分離沈殿させる凝集沈殿工程と、この凝集沈殿
工程により分離されたスラッジ水を脱水処理して脱水ケ
ーキを作製する脱水処理工程と、この脱水処理工程で得
られた脱水ケーキを硬化前に解砕し、10〜15mmの
厚さに平面圧延する解砕処理工程と、この解砕処理工程
で解砕された脱水ケーキを含水比が50〜60質量%で
最大粒径が20mm以下となるように乾燥する乾燥工程
と、この乾燥工程で得られた乾燥スラッジを風力を利用
した粉砕装置で微粉砕化して丸みを帯びた微粒子を製造
する粉砕工程と、この粉砕工程で製造された微粒子を捕
集する捕集工程とを含むコンクリートスラッジ微粉末回
収方法である。
Means for Solving the Problems To solve the above problems, a method for recovering concrete sludge fine powder according to the present invention comprises:
A fine sand removal step of obtaining recovered water by removing fine sand contained in washing wastewater generated from concrete treatment facilities such as a concrete product factory and a ready mixed factory so that the sand content is 10% by mass or less; A coagulation sedimentation step in which an inorganic coagulant is added to the recovered water obtained in the sand removal step to separate and precipitate the collected water supernatant water and sludge water; and a sludge water separated in the coagulation sedimentation step is dewatered to be dehydrated. A dewatering process for producing a cake, a dewatering cake obtained in the dewatering process is crushed before curing, and a crushing process for flat rolling to a thickness of 10 to 15 mm; A drying step of drying the crushed dewatered cake so that the water content is 50 to 60% by mass and the maximum particle size is 20 mm or less, and the dried sludge obtained in this drying step is finely pulverized by a pulverizer using wind power. A pulverizing step for producing microparticles rounded and 砕化 a concrete sludge powder recovery method comprising the collecting step of collecting the fine particles produced by this grinding process.

【0017】また、本発明のコンクリートスラッジ微粉
末回収装置は、コンクリート製品工場、レディーミクス
ト工場等のコンクリート処理設備から発生する洗浄廃水
に含まれる微砂分を含砂率が10質量%以下となるよう
に除去した回収水を得る湿式サイクロン等の微砂除去手
段と、この微砂除去手段で得られた回収水に無機系凝集
剤を添加して回収水上澄み水とスラッジ水に分離沈殿さ
せる凝集沈殿手段と、この凝集沈殿手段により分離され
たスラッジ水を脱水処理して脱水ケーキを作製する脱水
処理手段と、この脱水処理手段で得られた脱水ケーキを
硬化前に解砕し、10〜15mmの厚さに平面圧延する
解砕処理手段と、この解砕処理手段で解砕された脱水ケ
ーキを含水比が50〜60質量%で最大粒径が20mm
以下となるように乾燥する乾燥手段と、この乾燥手段で
得られた乾燥スラッジを風力を利用した粉砕装置で微粉
砕化して丸みを帯びた微粒子を製造する微粉砕手段と、
この微粉砕手段で製造された微粒子を捕集する捕集手段
とを含むコンクリートスラッジ微粉末回収装置である。
Further, the concrete sludge fine powder recovery apparatus of the present invention has a sand content of 10% by mass or less of fine sand contained in washing wastewater generated from concrete treatment facilities such as a concrete product factory and a ready mixed factory. A fine sand removal means such as a wet cyclone to obtain the recovered water removed as above, and an inorganic coagulant added to the recovered water obtained by the fine sand removal means to separate and precipitate the recovered water supernatant water and sludge water. Precipitation means, a dewatering treatment means for producing a dewatered cake by dewatering the sludge water separated by the coagulation sedimentation means, and a dewatered cake obtained by this dewatering treatment means is crushed before curing to 10 to 15 mm And a dewatered cake crushed by the crushing means having a water content of 50 to 60% by mass and a maximum particle size of 20 mm.
Drying means for drying as follows, and fine pulverizing means for finely pulverizing the dried sludge obtained by this drying means with a pulverizing device using wind power to produce rounded fine particles,
A concrete sludge fine powder collecting apparatus including a collecting means for collecting fine particles produced by the fine pulverizing means.

【0018】本発明によれば、成分がCaO30〜40
質量%,SiO210〜20質量%を含み、平均粒径が
3〜20μm、比表面積が4000〜30000cm2
/gで、角が取れた丸みを帯びた粒子の形状を呈してい
る良質なコンクリートスラッジ微粉末(PDS)を得る
ことができ、これをコンクリート用混和材料、高流動コ
ンクリート用の粉体材料、セルフレベリング材、エアー
モルタル、地盤改良材、またアルカリ性であることから
中和剤など、拡大された様々な用途に活用することが可
能となり、産業廃棄物の汚泥の範疇にあるコンクリート
スラッジをPDSとして再資源化する処理技術が提供さ
れる。
According to the present invention, the component is CaO 30-40
%, SiO 2 10 to 20% by mass, average particle size 3 to 20 μm, specific surface area 4000 to 30000 cm 2
/ G, a high-quality concrete sludge fine powder (PDS) exhibiting the shape of rounded and rounded particles can be obtained, which can be mixed with a concrete admixture material, a powder material for high-fluidity concrete, Self-leveling material, air mortar, ground improvement material, and because it is alkaline, it can be used for a wide variety of applications such as neutralizers. Concrete sludge in the category of industrial waste sludge as PDS A recycling technique is provided.

【0019】なお、本明細書において用いる含水比は、 含水比=(最初の質量−絶乾状態の質量)/最初の質量
×100(%) で表される。一方、一般的に含水比と共に併用されてい
る含水率は、 含水率=(最初の質量−絶乾状態の質量)/絶乾状態の
質量×100(%) で表される。両者は、下式で換算できる。 含水比=含水率/(含水率+1)
The water content ratio used in the present specification is represented by the following formula: water content ratio = (initial mass−mass in absolutely dry state) / initial mass × 100 (%). On the other hand, the water content commonly used together with the water content ratio is represented by: water content = (initial mass−mass in absolutely dry state) / mass in absolutely dry state × 100 (%). Both can be converted by the following formula. Water content = water content / (water content + 1)

【0020】[0020]

【発明の実施の形態】以下、本発明の実施の形態を説明
する。図1は本発明の処理工程を示す工程図、図2は本
発明の処理装置の構成を示す概略図である。この工程図
および概略図に従って説明する。
Embodiments of the present invention will be described below. FIG. 1 is a process diagram showing the processing steps of the present invention, and FIG. 2 is a schematic diagram showing the configuration of the processing apparatus of the present invention. The process will be described with reference to the process diagrams and schematic diagrams.

【0021】S0:骨材回収処理 品質のよいPDSを製造するためには、最初の工程であ
る洗浄廃水10の処理が重要で、予備段階ではトロンメ
ル、サンドスクリュー等の骨材回収装置11を用いて洗
浄廃水10中の大径の砂利、砂等を除去して回収骨材1
2とし、上澄み液13を分離する。
S0: Aggregate recovery treatment In order to produce high-quality PDS, it is important to treat the washing wastewater 10, which is the first step, and use an aggregate recovery apparatus 11 such as a trommel or a sand screw in a preliminary stage. To remove large-size gravel, sand, etc. from the washing wastewater 10 and collect recovered aggregate 1
2, and the supernatant 13 is separated.

【0022】S1:微砂除去処理 さらに、湿式サイクロン14を用いて上澄み液13中に
含まれる微砂分15を可能な限り除去して、含砂率10
質量%以下、好ましくは5%程度以下にする。レディー
ミクストコンクリート工場における含砂率は各地域の工
場によって大きくばらつき、5〜35質量%の範囲にあ
る。含砂率が10質量%を超えると、これを含むスラッ
ジ水を利用してコンクリートを製造する場合、コンクリ
ートの性状が大きくばらつく可能性があり、また泥分を
多く含むような場合はコンクリートのフレッシュ性状に
悪影響を及ぼすことが指摘されている。コンクリートの
性状に悪影響を及ぼさないためには、洗浄廃水中に含ま
れる微砂分を極力取り除く必要があり、含砂率を10質
量%以下にする。この処理で質のよい回収水16が得ら
れる。
S1: Fine sand removal treatment Further, the fine sand content 15 contained in the supernatant liquid 13 is removed as much as possible using a wet cyclone 14 to obtain a sand content of 10%.
Mass% or less, preferably about 5% or less. The sand content in the ready-mixed concrete factory varies greatly depending on the factory in each region, and is in the range of 5 to 35% by mass. If the sand content exceeds 10% by mass, the concrete properties may vary greatly when producing concrete using sludge water containing the same, and when the concrete contains a large amount of mud, the concrete may become fresh. It has been pointed out that it adversely affects the properties. In order not to adversely affect the properties of the concrete, it is necessary to remove the fine sand contained in the washing wastewater as much as possible, and the sand content is reduced to 10% by mass or less. By this treatment, high-quality recovered water 16 is obtained.

【0023】湿式サイクロン14においては、微砂を含
んだ洗浄廃水をポンプの圧力で連続して円錐状側板に圧
送通過させる。速度を保持した洗浄廃水が回転しながら
傾斜板を通過するが、このとき、洗浄廃水中の比重の重
いものは外板側に沿って放出口付近で速度を速めながら
回転することになる。この状態で中心部分を負圧にでき
れば、比重の軽い洗浄廃水を上部に押し上げ、上部セン
ター孔に無負荷状態で開放すれば、微砂を含まない汚水
を放出できる。その結果、微砂分は下部から排出できる
ようになる。中心部分に負圧を生じる流量および回転速
度を増長する傾斜板の角度は放出口口径の設定による。
湿式サイクロンを連層式に構成すれば、負圧を増幅する
ことができ、より微砂除去率を高めることができる。
In the wet cyclone 14, the washing wastewater containing fine sand is continuously passed through the conical side plate under pressure from the pump. The washing wastewater maintaining the speed passes through the inclined plate while rotating, and at this time, the heavy wastewater with the specific gravity rotates along the outer plate side while increasing the speed near the discharge port. If a negative pressure can be applied to the central part in this state, the washing wastewater having a low specific gravity can be pushed upward, and if the upper central hole is opened without load, sewage containing no fine sand can be discharged. As a result, the fine sand can be discharged from the lower part. The flow rate that generates a negative pressure in the central portion and the angle of the inclined plate that increases the rotation speed depend on the setting of the discharge port diameter.
If the wet cyclone is formed in a continuous layer type, the negative pressure can be amplified, and the fine sand removal rate can be further increased.

【0024】S2:凝集沈殿処理 質のよい回収水上澄み水19とスラッジ水に分離するた
めに、凝集沈殿装置17を利用する。スラッジ水中に含
まれる固形分の固化を防ぎ、かつ分離を迅速に行い、上
澄み水19をコンクリート用練り混ぜ水として再利用す
るために、この処理工程では凝集剤を使用する。凝集剤
としては、高分子系凝集剤を用いた処理技術が開発さ
れ、利用されているが、凝集沈殿までの時間を要し、そ
のため、大容量の濃縮槽を多数備えた複雑な処理システ
ムが必要になる。さらに、凝集物は粘りを持つことか
ら、再利用が困難である。また、回収水中の固形分はフ
ロック状態で沈殿するが、この固形分には未水和セメン
トが多く含まれており、しかも水中においては硬化せず
にセメントの活性作用を保持した状態にある。これをコ
ンクリートに混入すれば強度の増進が期待できる。本発
明では、処理水をコンクリート用材料として再利用する
観点から、コンクリートの特性に無害な無機系凝集剤1
8(無機質95質量%以上、好ましくは98質量%以
上)の使用が不可欠である。無機質が95質量%未満で
あると、有機成分がコンクリートの特性に悪影響を及ぼ
すことがあり好ましくない。無機系凝集剤18として
は、アルミニウム塩やカルシウム塩、マグネシウム塩を
使用することができる。凝集沈殿装置17で分離された
スラッジ水は、濃縮槽20で沈殿され、原水槽21に上
澄み水が供給される。
S2: Coagulation-sedimentation treatment The coagulation-sedimentation apparatus 17 is used to separate the recovered water of high quality into supernatant water 19 and sludge water. A coagulant is used in this treatment step in order to prevent solidification of the solids contained in the sludge water, to quickly separate the sludge, and to reuse the supernatant water 19 as mixing water for concrete. As a coagulant, a processing technology using a polymer-based coagulant has been developed and used, but it requires time until coagulation and sedimentation. Will be needed. In addition, the aggregates are sticky and difficult to reuse. Further, the solid content in the recovered water precipitates in a floc state, but the solid content contains a large amount of unhydrated cement, and is not hardened in water and retains the activity of the cement. If this is mixed into concrete, it can be expected to increase the strength. In the present invention, from the viewpoint of reusing treated water as a concrete material, an inorganic coagulant 1 that is harmless to the properties of concrete
8 (95% by mass or more, preferably 98% by mass or more) is indispensable. If the inorganic content is less than 95% by mass, the organic component may adversely affect the properties of the concrete, which is not preferable. As the inorganic coagulant 18, aluminum salts, calcium salts, and magnesium salts can be used. The sludge water separated by the coagulation sedimentation device 17 is settled in the concentration tank 20, and the supernatant water is supplied to the raw water tank 21.

【0025】S3:脱水処理 原水槽21から供給されるスラッジ水は脱水処理装置2
2で脱水処理して、脱水ケーキ23(スラッジケーキ)
を作製する。脱水処理装置22としては、フィルタープ
レスなどの脱水機を使用することができる。
S3: Dehydration treatment Sludge water supplied from the raw water tank 21 is supplied to the dehydration treatment device 2
Dewatering process 2 and dewatering cake 23 (sludge cake)
Is prepared. As the dehydration processing device 22, a dehydrator such as a filter press can be used.

【0026】S4:解砕処理 脱水処理S3により作製された脱水ケーキ23は、含水
比が50質量%程度あることから、これを放置しておく
と硬化し、また表面のみが乾燥するため、後の微粉砕処
理が非常に難しくなる。そこで、脱水ケーキ23を作製
後、解砕機24で直ちに解砕を行い、粗くほぐすように
する。このような処理は品質のよいPDSを製造するた
めには不可欠な工程である。解砕工程は、一次解砕で脱
水ケーキ23をローラ間を通して10〜15mmの厚さ
に平面圧延し、次の二次解砕では乾燥処理工程前に同じ
くローラ間で平面圧延することで行う。
S4: Disintegration treatment The dewatered cake 23 produced by the dehydration treatment S3 has a water content of about 50% by mass, so that it is hardened if left as it is, and only the surface is dried. Is very difficult to pulverize. Therefore, after the dehydrated cake 23 is prepared, it is immediately crushed by the crusher 24 to loosen it roughly. Such a process is an indispensable step for producing high-quality PDS. The crushing process is performed by flat rolling the dehydrated cake 23 to a thickness of 10 to 15 mm through rollers between the first crushing and flat rolling between the rollers before the drying process in the next secondary crushing.

【0027】S5:乾燥処理 ほぐされた脱水ケーキは例えば循環式のベルトコンベア
式の乾燥機25で処理されるが、品質のよいPDSを製
造するためには、含水比が10〜30質量%、好ましく
は20質量%程度で、最大粒径が20mm以下、好まし
くは15mm程度の粒子である乾燥スラッジ26を製造
することが不可欠である。このとき、均一な乾燥を与え
ることができるような乾燥機25でなければならない。
含水比が30質量%を超える場合、水分を多く含む質量
のある乾燥スラッジは重力作用のため次工程の風力式粉
砕機27内での風砕処理時間が短く、粒子径の大きな粉
末しか得られないこと、含水比を10質量%未満に調整
すれば非常に微細な粉末を製造できる可能性はあるが、
乾燥工程のコストアップにつながること、また20質量
%程度の含水比で目的の微粉末を製造できることから、
上記の範囲の含水比とした。また、最大粒径が30mm
を超えると質量のある乾燥スラッジとなり、重力作用の
ため風砕処理の時間が短く、粒子径の大きな粉末しか製
造できないため、好ましくない。
S5: Drying Process The loosened dewatered cake is processed, for example, by a circulating belt conveyor dryer 25. In order to produce high-quality PDS, the water content is 10 to 30% by mass. It is indispensable to produce the dry sludge 26 which is preferably about 20% by mass and has a maximum particle size of 20 mm or less, preferably about 15 mm. At this time, the dryer 25 must be capable of providing uniform drying.
When the water content is more than 30% by mass, the dry sludge containing a large amount of moisture has a short time in the next step in the wind-type pulverizer 27 due to the action of gravity, so that only a powder having a large particle diameter can be obtained. There is a possibility that a very fine powder can be produced by adjusting the water content to less than 10% by mass,
Because it leads to an increase in the cost of the drying process and can produce the desired fine powder with a water content of about 20% by mass,
The water content was in the above range. The maximum particle size is 30mm
If it exceeds, the dried sludge becomes heavy, and the time required for the air crushing treatment is short due to the action of gravity, and only a powder having a large particle diameter can be produced, which is not preferable.

【0028】S6:微粉砕処理 乾燥スラッジ26を、風力式粉砕機27で微粉砕化す
る。この装置の特徴は、角張った形状をした粒子が風の
中で互いに衝突しあい、丸みを帯びた微粒子を製造でき
ることにある。従来、サイクロン方式は粉末の分級のた
めに用いられることが多いが、空気流の流れや流量、吸
引量、傾斜板の角度などを適切にコントロールすること
によって、粉砕を主とした装置として使用できる。
S6: Pulverization treatment The dried sludge 26 is pulverized by a wind-type pulverizer 27. The feature of this device is that angular particles can collide with each other in the wind to produce rounded fine particles. Conventionally, the cyclone method is often used for classification of powder, but can be used as a device mainly for pulverization by appropriately controlling the flow and flow rate of air flow, the amount of suction, the angle of the inclined plate, etc. .

【0029】S7:捕集処理 品質のよいPDS33の製造のためには、風力式粉砕機
27のほかに周知の乾式サイクロン28、捕集機30が
システム化された装置を用いる。前記の風力式粉砕機2
7および乾式サイクロン28で分離された材料はふるい
29に移送され、一定の粒径未満の粉粒は吸引補助装置
31で吸引されて吸引調整捕集機32により回収され、
ふるい29で分離された一定粒径より大きな粉粒は再度
風力式粉砕機27に搬送されて微粉砕処理される。これ
により回収率を向上させる。このようにして、粉末度
(比表面積)が4000〜30000cm2/gの良質
なPDSを得ることができる。本発明のPDSの成分分
析結果などの特性を、比較例とともに表1に示す。
S7: Collection Process In order to produce a high quality PDS 33, a well-known dry type cyclone 28 and a system in which a collector 30 is systemized in addition to the wind-type pulverizer 27 are used. The aforementioned wind mill 2
7 and the material separated by the dry cyclone 28 are transferred to a sieve 29, and powder particles having a particle diameter smaller than a certain particle size are sucked by a suction auxiliary device 31 and collected by a suction adjusting and collecting device 32.
The powder particles larger than a certain particle size separated by the sieve 29 are again conveyed to the wind mill 27 and pulverized. This improves the recovery rate. In this way, a high-quality PDS having a fineness (specific surface area) of 4000 to 30000 cm 2 / g can be obtained. Table 1 shows the characteristics of the PDS of the present invention, such as the results of component analysis, along with Comparative Examples.

【0030】[0030]

【表1】PDSの特性 OPC:普通ポルトランドセメント PDS:微粉砕乾燥スラッジ[Table 1] Characteristics of PDS OPC: ordinary Portland cement PDS: finely ground dry sludge

【0031】また、各試料の形状を表す顕微鏡写真を図
3に示す。表1および図3からわかるように、本発明の
PDSは、角が取れた丸みを帯びた形状をしており、ま
たコンクリートの粒径分布よりも小さい粒径であるた
め、コンクリート用混和剤として用いた場合、セメント
粒子の隙間を埋める状態でコンクリートと混和され、密
実なコンクリート製品ないし構造物を構築することがで
きる。
FIG. 3 shows a micrograph showing the shape of each sample. As can be seen from Table 1 and FIG. 3, the PDS of the present invention has a rounded shape with sharp corners and a particle size smaller than the particle size distribution of concrete. When used, concrete is mixed with concrete in a state of filling gaps between cement particles, and a dense concrete product or structure can be constructed.

【0032】[0032]

【発明の効果】上述したように、本発明によれば、以下
の効果を奏する。 (1)洗浄廃水中に含まれる微砂分を可能な限り除去す
ることにより、再利用に適した質のよいコンクリートス
ラッジ微粉末を回収することができる。 (2)回収されたコンクリートスラッジ微粉末を高流動
コンクリート用の粉体材料、セルフレベリング材、エア
ーモルタル、地盤改良材として再使用することができ
る。 (3)回収されたコンクリートスラッジ微粉末はアルカ
リ性であることから中和剤など、拡大された様々な用途
に活用することが可能となり、産業廃棄物の汚泥の範疇
にあるコンクリートスラッジをPDSとして再資源化す
ることができる。
As described above, according to the present invention, the following effects can be obtained. (1) By removing the fine sand content contained in the washing wastewater as much as possible, high-quality concrete sludge fine powder suitable for reuse can be recovered. (2) The recovered concrete sludge fine powder can be reused as a powder material for high-fluidity concrete, a self-leveling material, an air mortar, and a ground improvement material. (3) Since the recovered concrete sludge fine powder is alkaline, it can be used for various expanded applications such as neutralizers, and concrete sludge in the category of industrial waste sludge is recycled as PDS. Can be turned into resources.

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

【図1】 本発明の処理工程を示す工程図である。FIG. 1 is a process chart showing the processing steps of the present invention.

【図2】 本発明の処理装置の構成を示す概略図であ
る。
FIG. 2 is a schematic diagram showing a configuration of a processing apparatus of the present invention.

【図3】 各試料の形状を表す顕微鏡写真である。FIG. 3 is a micrograph showing the shape of each sample.

【符号の説明】[Explanation of symbols]

10 洗浄廃水 11 骨材回収装置 12 回収骨材 13 上澄み液 14 湿式サイクロン 15 微砂分 16 回収水 17 凝集沈殿装置 18 無機系凝集剤 19 上澄み水 20 濃縮槽 21 原水槽 22 脱水処理装置 23 脱水ケーキ 24 解砕機 25 乾燥機 26 乾燥スラッジ 27 風力式粉砕機 28 乾式サイクロン 29 ふるい 30 捕集機 31 吸引補助装置 32 吸引調整捕集機 33 微粉砕乾燥スラッジ(PDS) DESCRIPTION OF SYMBOLS 10 Wash wastewater 11 Aggregate collection device 12 Collected aggregate 13 Supernatant liquid 14 Wet cyclone 15 Fine sand 16 Collected water 17 Coagulation sedimentation device 18 Inorganic coagulant 19 Supernatant water 20 Concentration tank 21 Raw water tank 22 Dehydration treatment device 23 Dehydration cake 24 Crusher 25 Dryer 26 Dry sludge 27 Wind-type pulverizer 28 Dry cyclone 29 Sieve 30 Collector 31 Suction auxiliary device 32 Suction adjustment collector 33 Fine pulverized dry sludge (PDS)

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 コンクリート製品工場、レディーミクス
ト工場等のコンクリート処理設備から発生する洗浄廃水
に含まれる微砂分を含砂率が10質量%以下となるよう
に除去した回収水を得る微砂除去工程と、 この微砂除去工程で得られた回収水に無機系凝集剤を添
加して回収水上澄み水とスラッジ水に分離沈殿させる凝
集沈殿工程と、 この凝集沈殿工程により分離されたスラッジ水を脱水処
理して脱水ケーキを作製する脱水処理工程と、 この脱水処理工程で得られた脱水ケーキを硬化前に解砕
し、10〜15mmの厚さに平面圧延する解砕処理工程
と、 この解砕処理工程で解砕された脱水ケーキを含水比が5
0〜60質量%で最大粒径が20mm以下となるように
乾燥する乾燥工程と、 この乾燥工程で得られた乾燥スラッジを風力を利用した
粉砕装置で微粉砕化して丸みを帯びた微粒子を製造する
微粉砕工程と、 この微粉砕工程で製造された微粒子を捕集する捕集工程
とを含むコンクリートスラッジ微粉末回収方法。
1. Fine sand removal to obtain recovered water by removing fine sand contained in washing wastewater generated from concrete treatment facilities such as a concrete product factory and a ready mixed factory so that the sand content is 10% by mass or less. A coagulation sedimentation step of adding an inorganic coagulant to the recovered water obtained in the fine sand removal step and separating and precipitating the collected water supernatant water and sludge water; and A dewatering treatment step of producing a dewatered cake by dehydration treatment; a crushing treatment step of crushing the dewatered cake obtained in the dewatering treatment before curing and flat rolling to a thickness of 10 to 15 mm; The dewatered cake crushed in the crushing process has a water content of 5
A drying step of drying so that the maximum particle size is 20 mm or less at 0 to 60% by mass, and finely pulverizing the dried sludge obtained in this drying step with a pulverizer using wind power to produce rounded fine particles. And a collecting step of collecting the fine particles produced in the fine pulverizing step.
【請求項2】 コンクリート製品工場、レディーミクス
ト工場等のコンクリート処理設備から発生する洗浄廃水
に含まれる微砂分を含砂率が10質量%以下となるよう
に除去した回収水を得る微砂除去手段と、 この微砂除去手段で得られた回収水に無機系凝集剤を添
加して回収水上澄み水とスラッジ水に分離沈殿させる凝
集沈殿手段と、 この凝集沈殿手段により分離されたスラッジ水を脱水処
理して脱水ケーキを作製する脱水処理手段と、 この脱水処理手段で得られた脱水ケーキを硬化前に解砕
し、10〜15mmの厚さに平面圧延する解砕処理手段
と、 この解砕処理手段で解砕された脱水ケーキを含水比が5
0〜60質量%で最大粒径が20mm以下となるように
乾燥する乾燥手段と、 この乾燥手段で得られた乾燥スラッジを風力を利用した
粉砕装置で微粉砕化して丸みを帯びた微粒子を製造する
微粉砕手段と、 この微粉砕手段で製造された微粒子を捕集する捕集手段
とを含むコンクリートスラッジ微粉末回収装置。
2. Fine sand removal to obtain recovered water by removing fine sand contained in washing wastewater generated from concrete treatment facilities such as a concrete product factory and a ready mixed factory so that the sand content is 10% by mass or less. Means, an inorganic coagulant is added to the recovered water obtained by the fine sand removing means, and a coagulating sedimentation means for separating and precipitating the collected water supernatant water and sludge water; and a sludge water separated by the coagulating sedimentation means. A dewatering treatment means for producing a dewatered cake by performing a dehydration treatment; a crushing treatment means for crushing the dewatered cake obtained by the dehydration treatment before curing and flat rolling to a thickness of 10 to 15 mm; The dewatered cake crushed by the crushing means has a water content of 5
Drying means for drying so that the maximum particle size is 20 mm or less at 0 to 60% by mass; and drying sludge obtained by the drying means is finely pulverized by a pulverizer using wind power to produce rounded fine particles. A concrete sludge fine powder recovery device, comprising: a fine pulverizing means for collecting fine particles produced by the fine pulverizing means;
【請求項3】 微砂除去手段は湿式サイクロンである請
求項2記載のコンクリートスラッジ微粉末回収装置。
3. The concrete sludge fine powder collecting apparatus according to claim 2, wherein the fine sand removing means is a wet cyclone.
【請求項4】 成分がCaO30〜40質量%,SiO
210〜20質量%を含み、平均粒径が3〜20μm、
比表面積が4000〜30000cm2/gで、角が取
れた丸みを帯びた粒子の形状を呈しているコンクリート
スラッジ微粉末。
4. A composition comprising 30 to 40% by mass of CaO and SiO
Containing 2 to 20% by mass, having an average particle size of 3 to 20 μm,
Fine concrete sludge powder having a specific surface area of 4000 to 30000 cm 2 / g and having the shape of rounded particles with sharp corners.
JP2001057417A 2001-03-01 2001-03-01 Concrete sludge fine powder recovery method and apparatus Expired - Fee Related JP4698043B2 (en)

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JP2008062161A (en) * 2006-09-06 2008-03-21 Eacle Kk Thickener
KR100826952B1 (en) * 2005-07-05 2008-05-02 주식회사 광토자원 The process and device of mud formation of the aggregate sorting operations
JP4472776B1 (en) * 2009-09-25 2010-06-02 三和石産株式会社 Concrete sludge fine powder recovery method and recovery apparatus, and concrete sludge fine powder
JP2010260015A (en) * 2009-05-08 2010-11-18 Yukio Yanagisawa Dephosphorizing material, dephosphorizing apparatus, and dephosphorizing by-product
JP2013039551A (en) * 2011-08-19 2013-02-28 Univ Of Tokyo Method for producing water cleaning material
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