Deprecated: The each() function is deprecated. This message will be suppressed on further calls in /home/zhenxiangba/zhenxiangba.com/public_html/phproxy-improved-master/index.php on line 456
JP7276769B2 - Flocculant for turbid water treatment - Google Patents
[go: Go Back, main page]

JP7276769B2 - Flocculant for turbid water treatment - Google Patents

Flocculant for turbid water treatment Download PDF

Info

Publication number
JP7276769B2
JP7276769B2 JP2019129045A JP2019129045A JP7276769B2 JP 7276769 B2 JP7276769 B2 JP 7276769B2 JP 2019129045 A JP2019129045 A JP 2019129045A JP 2019129045 A JP2019129045 A JP 2019129045A JP 7276769 B2 JP7276769 B2 JP 7276769B2
Authority
JP
Japan
Prior art keywords
turbid water
flocculant
blended
polymer flocculant
water treatment
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.)
Active
Application number
JP2019129045A
Other languages
Japanese (ja)
Other versions
JP2021013884A (en
Inventor
秀樹 高矢
康智 櫻井
真吾 赤坂
邦夫 福光
誠一 尾花
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Ube Material Industries Ltd
Technica Goudou Co Ltd
Original Assignee
Ube Material Industries Ltd
Technica Goudou Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Ube Material Industries Ltd, Technica Goudou Co Ltd filed Critical Ube Material Industries Ltd
Priority to JP2019129045A priority Critical patent/JP7276769B2/en
Publication of JP2021013884A publication Critical patent/JP2021013884A/en
Application granted granted Critical
Publication of JP7276769B2 publication Critical patent/JP7276769B2/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Treatment Of Sludge (AREA)

Description

本発明は、土木工事や建設工事などから発生する濁水や、湖沼や河川、港岸などの底にたまった高含水泥土を洗浄する際に発生する濁水を簡易に処理するために用いられる濁水処理用凝集剤に関する。 The present invention is a turbid water treatment used to easily treat turbid water generated from civil engineering work, construction work, etc., and turbid water generated when washing high water content mud accumulated at the bottom of lakes, rivers, port shores, etc. for flocculants.

従来、浚渫工事から発生する高含水泥土の処理方法として、有機合成高分子凝集剤による固液分離後に水分を除き、スラリーにセメントなどを添加することによる固化処理を行う処理方法や、有機汚泥より発生する濁水にカチオン系有機合成高分子を使用し、あるいはPAC(ポリ塩化アルミニウム)や硫酸バンド、ポリ塩化第二鉄などの無機凝集剤と有機合成高分子凝集剤の水溶液添加など2段階処理による減容化処理を行う処理方法が採用されてきた。 Conventionally, as a treatment method for high water content mud generated from dredging work, after solid-liquid separation with an organic synthetic polymer flocculant, water is removed and cement or the like is added to the slurry to solidify it. Two-stage treatment such as using a cationic organic synthetic polymer for the turbid water generated, or adding an aqueous solution of an inorganic flocculant such as PAC (polyaluminum chloride), aluminum sulfate, and polyferric chloride, and an organic synthetic polymer flocculant. Processing methods for volume reduction have been adopted.

こうしたことを背景にして、設備の高度化、複雑化、巨大化し、山岳や沼地などのヤードが取れない工事においては、処理の長期化や汚泥運搬が困難になることが多かった。 Against this background, facilities have become more sophisticated, complex, and huge, and in construction work in mountains and marshes where yards cannot be secured, processing often takes a long time and transporting sludge becomes difficult.

また、これに対処するものとして、例えば、特許文献1に開示されるように、高分子凝集剤にてフロックを作り、無機凝集剤の代わりをなすセメントなどを加えて固化材粒子を包含するフロックを形成させる高含水汚泥の処理方法の提案がされているが、セメント系の固化材が推奨されており、これは処理土のアルカリ化による建設発生土転用方法に制限を行うことに他ならない。 In addition, as a countermeasure to this, for example, as disclosed in Patent Document 1, flocs are made with a polymer flocculating agent, cement or the like is added instead of an inorganic flocculating agent, and flocs containing solidifying material particles are added. However, a cement-based solidification agent is recommended, and this is nothing but a restriction on the conversion of construction soil by alkalinizing the treated soil.

また、特許文献2に開示されるように、可溶性アルミニウム化合物、鉄塩化合物、還元剤、有機合成高分子凝集剤、天然高分子凝集剤、アルカリ金属の炭酸塩及び/又はセメント粉粒体、高ゼータ電位の活性に酸化ケイ素及びアルミナを主成分とするケイ酸アルミナ系土壌鉱物粉粒体からなる凝集剤組成物の提案がされているが、具体的な撹拌方法や脱水方法にまで言及されていない。 Further, as disclosed in Patent Document 2, a soluble aluminum compound, an iron salt compound, a reducing agent, an organic synthetic polymer flocculant, a natural polymer flocculant, an alkali metal carbonate and/or cement granules, a high A flocculant composition composed of silicate-alumina-based soil mineral granules containing silicon oxide and alumina as main components has been proposed for zeta potential activity, but specific stirring methods and dehydration methods are also mentioned. do not have.

特開平9-168800号公報JP-A-9-168800 特願平9-287555号公報Japanese Patent Application No. 9-287555

本発明は、上記従来の土木工事や建設工事などから発生する濁水や、湖沼や河川、港岸などの底にたまった高含水泥土を洗浄する際に発生する濁水の処理技術の有する問題点に鑑み、狭いヤードでも濁水と薬剤の撹拌を行う撹拌設備をなくし、底部に堆積するスラッジの処理方法を簡素化することを可能とするものであって、濁水処理作業の省力化及び発生する処理水やフロックをpH中性に保ちながら、フロックからの脱水を促進し、スラッジの強度発現に寄与する濁水処理用凝集剤を提供することを目的とする。 The present invention addresses the problems associated with the technology for treating turbid water generated during conventional civil engineering and construction work, as well as turbid water that accumulates on the bottom of lakes, rivers, port shores, and the like. In view of this, it is possible to eliminate the agitating equipment for agitating turbid water and chemicals even in a narrow yard and simplify the method of treating the sludge that accumulates at the bottom. It is an object of the present invention to provide a coagulant for treating turbid water, which promotes dehydration from flocs while maintaining pH neutrality of flocs and contributes to development of strength of sludge.

上記目的を達成するため、本発明の濁水処理用凝集剤は、合成高分子凝集剤をアニオン系から2種以上配合し、天然高分子凝集剤1種以上配合し、アルカリ土類金属の中からカルシウム系化合物を2種以上配合し、アルミニウム化合物を2種以上配合し、pH調整剤としてアルカリ土類金属から酸化マグネシウム又は炭酸塩を1種以上配合し、多孔質物質の粉末を配合してなることを特徴とする。 In order to achieve the above object, the flocculant for treating turbid water of the present invention contains two or more anionic synthetic polymer flocculants, one or more natural polymer flocculants, and alkaline earth metals. Two or more kinds of calcium-based compounds are blended, two or more kinds of aluminum compounds are blended, one or more kinds of alkaline earth metals, magnesium oxides or carbonates are blended as pH adjusters, and powder of porous material is blended. It is characterized by

より具体的には、本発明の濁水処理用凝集剤は、無水硫酸カルシウムを55w%~65w%、炭酸ナトリウムを7w%~12w%、焼成珪藻土を5w%~10w%、炭酸カルシウムを0.5w%~5w%、硫酸アルミニウムを10w%~20w%、ポリ塩化アルミニウムを0.5w%~5w%、低分子アニオンポリマーを2w%~4w%、高分子アニオンポリマーを0.5w%~5w%、アルギン酸塩を1w%~4w%で配合してなることを特徴とする。 More specifically, the flocculant for treating turbid water of the present invention contains 55w% to 65w% anhydrous calcium sulfate, 7w% to 12w% sodium carbonate, 5w% to 10w% calcined diatomaceous earth, and 0.5w calcium carbonate. % to 5w%, 10w% to 20w% of aluminum sulfate, 0.5w% to 5w% of polyaluminum chloride, 2w% to 4w% of low molecular weight anionic polymer, 0.5w% to 5w% of high molecular weight anionic polymer, It is characterized by containing 1w% to 4w% of alginate.

この場合において、前記アニオン系の合成高分子凝集剤が、高分子アニオンポリマーとして、1300万~1500万のアニオン度30mol%~50mol%の高分子凝集剤(凝集反応は遅いが、大きなフロックが生成される。)と、低分子アニオンポリマーとして、600万~1200万のアニオン度10mol%~30mol%の高分子凝集剤(具体的には、200メッシュ(75μm以下)の微粉末からなる高分子凝集剤。)(大きなフロックが生成されないが、凝集反応は早い。)を用いることができる。 In this case, the anionic synthetic polymer flocculant is a high molecular weight anionic polymer having an anion degree of 13 million to 15 million and an anion degree of 30 mol % to 50 mol % (the aggregation reaction is slow, but large flocs are generated ), and as a low-molecular-weight anionic polymer, a polymer flocculant having an anion degree of 10 mol% to 30 mol% and an anion degree of 6 million to 12 million (specifically, a polymer flocculant composed of fine powder of 200 mesh (75 μm or less) agent.) (does not produce large flocs, but the aggregation reaction is fast) can be used.

また、天然の凝集剤としては、アルギン酸塩(低分子アニオンポリマーよりも微細な粒子を対象とし、凝集反応は早い。)、キチン、キトサン等を1種以上含有することができる。また、スプレードライ乾燥などによって製造された微粉末(0.2μm~60μm)を用いることがより望ましい。 Moreover, as a natural flocculant, one or more of alginates (targeted for finer particles than low-molecular-weight anionic polymers and having a fast flocculation reaction), chitin, chitosan, and the like can be contained. Further, it is more desirable to use a fine powder (0.2 μm to 60 μm) produced by spray drying or the like.

また、カルシウム系化合物は、pHに大きな影響を与えない炭酸カルシウムや硫酸カルシウムを使用し、スラッジの凝結強度を得るため、硫酸カルシウムには半水の硫酸カルシウムや無水が望ましく、特に、硫酸カルシウムには可溶性天然無水が特に好ましい。 In addition, as the calcium-based compound, calcium carbonate and calcium sulfate, which do not greatly affect the pH, are used. In order to obtain the caking strength of the sludge, the calcium sulfate is desirably semi-water calcium sulfate or anhydrous. is particularly preferred as a soluble natural anhydrous.

また、アルミニウム系化合物には、ポリ塩化アルミニウムと硫酸アルミニウムの粉末を混合したものを用いることが望ましく、泥土汚泥などは硫酸アルミニウムの割合が多いことが特に好ましい。これは硫酸カルシウムと硫酸アルミニウムの併用による凝集作用の高さからであって、特にポリ塩化アルミニウムと天然無水硫酸カルシウムか二水硫酸カルシウムと硫酸アルミニウムとの併用が望ましい。 Further, it is preferable to use a mixture of powders of polyaluminum chloride and aluminum sulfate as the aluminum-based compound, and it is particularly preferable that the ratio of aluminum sulfate is high in mud sludge and the like. This is because the combination of calcium sulfate and aluminum sulfate has a high flocculating action, and the combination of polyaluminum chloride and natural anhydrous calcium sulfate or calcium dihydrate and aluminum sulfate is particularly desirable.

また、アルミニウム系化合物によって酸性側によるpHを中性に戻すため、炭酸塩又は酸化マグネシウムを用いることが望ましく、より望ましくは凝結作用の強いMg2+を放出する酸化マグネシウムを配合することであって、最も望ましくは海水法にて製造された酸化マグネシウムが好ましい。 In addition, it is desirable to use a carbonate or magnesium oxide in order to return the pH of the acidic side to neutral with an aluminum-based compound, and more preferably, magnesium oxide that releases Mg 2+ with a strong coagulation effect is blended, Most desirably, magnesium oxide produced by the seawater method is preferred.

また、多孔質物質の粉末は、濁水中に含まれる微細粒子や色素、放射性元素を吸着するためのもので、ゼオライト、活性炭、珪藻土の微粉を用いることが可能であって、特に本発明においては、高い透水係数を持つスラッジを形成させることを目的として、焼成珪藻土(pHが中性域(pH7.7±0.5程度)にあって、メジアン径(D50)8~12μm、比表面積1~5m/g)を用いることが最も望ましい。 The powder of the porous substance is for adsorbing fine particles, pigments, and radioactive elements contained in the turbid water, and fine powders of zeolite, activated carbon, and diatomaceous earth can be used. , For the purpose of forming sludge with a high hydraulic conductivity, calcined diatomaceous earth (pH is in the neutral range (about pH 7.7 ± 0.5), median diameter (D50) 8 ~ 12 μm, specific surface area 1 ~ 5 m 2 /g) is most preferred.

本発明の濁水処理用凝集剤によれば、バキュームで吸い上げた高含水泥土に当該濁水処理用凝集剤を添加し、水中ポンプや撹拌機による撹拌を必要とせず、流水撹拌のみで浮遊粒子との凝集反応が可能であって、凝集反応の即時性を有し、pHが中性のままで高い脱水性を持つスラッジを生成し、脱水の過程で強度の高いフロックを得ることができるとともに、作られるフロックは特大であることを特徴とし、フィルタプレスの設置が難しい山岳部や狭い作業スペースしか確保できない場合であっても、凝集フロックを形成後、脱水用ろ布などで脱水させた残留物がろ布に付着しにくく、剥がれ易く、また、脱水性が良いため、透水性のフレコンバッグなどを用いた脱水を可能とし、脱水されたスラッジは徐々に強度を得ることができるため、段積みすることで作業スペースの確保などの問題を解消することができる。 According to the coagulant for turbid water treatment of the present invention, the coagulant for turbid water treatment is added to the high water content mud sucked up by vacuum, and the coagulant for turbid water treatment is not required to be stirred by a submersible pump or a stirrer, and the suspended particles can be separated only by stirring with running water. It is capable of flocculation reaction, has immediacy of flocculation reaction, produces sludge with high dehydration property while pH remains neutral, and can obtain flocs with high strength in the process of dehydration. The floc that is formed is characterized by its extra-large size, and even in mountainous areas where it is difficult to install a filter press or when only a narrow work space can be secured, after forming flocculated flocs, the residue that has been dehydrated with a dewatering filter cloth or the like can be removed. It does not easily adhere to the filter cloth, is easy to peel off, and has good dewatering properties. By doing so, it is possible to solve problems such as securing work space.

以下、本発明の濁水処理用凝集剤の実施の形態を、具体的な実施形態に基づいて説明する。 Hereinafter, embodiments of the flocculant for treating turbid water of the present invention will be described based on specific embodiments.

本発明の濁水処理用凝集剤は、薬剤と高含水泥土又は濁水とを撹拌するための水中ポンプや撹拌機などの大型設備を必要とせず、高い凝集反応を得るために、分子量とイオン度の異なる2種類の合成高分子凝集剤を用い、微細な粒子を効果的に凝集させるために天然高分子凝集剤を1種、フロックに重量を与えるための炭酸カルシウムと脱水後に強度を付与する硫酸カルシウムを配合し、塩基度の違うアルミニウム化合物からポリ塩化アルミニウムと硫酸アルミニウムの2種以上を配合することで幅広いゼータ電位を中和できるようにし、アルミニウム化合物を使用することによるpH変動を打ち消すための調整剤として炭酸水素ナトリウムや酸化マグネシウムを用いることで高い反応性とアルミニウム飽和を防ぎ、焼成珪藻土を用いることで高透水性スラッジを作り、脱水後の強度を与えることを可能として作業スペースの確保の問題を解消するようにしたものである。 The flocculant for turbid water treatment of the present invention does not require large equipment such as a submersible pump or stirrer for agitating the agent and high water content mud or turbid water. Using two different types of synthetic polymer flocculants, one natural polymer flocculant to effectively flocculate fine particles, calcium carbonate to give weight to the floc, and calcium sulfate to give strength after dehydration. By blending two or more types of aluminum compounds with different basicities, such as polyaluminum chloride and aluminum sulfate, it is possible to neutralize a wide range of zeta potentials, and adjustment to counteract pH fluctuations due to the use of aluminum compounds. By using sodium bicarbonate and magnesium oxide as agents, it is possible to prevent high reactivity and aluminum saturation, and by using calcined diatomaceous earth, it is possible to create highly water-permeable sludge and give it strength after dehydration, making it possible to secure work space. It is designed to eliminate

検討を重ねた中で、特に変化が大きかった以下の条件の配合と用いる材料を変えた濁水処理試験の結果を表に示す。
なお、試験方法はビーカ2個を用い、移し替え作業を8回行った際の変化を濁度計によって測定した。
The table below shows the results of turbid water treatment tests in which the formulations under the following conditions and the materials used were changed, in which the changes were particularly large during repeated examinations.
In the test method, two beakers were used, and the change was measured by a turbidity meter when the transfer operation was performed eight times.

[試験対象1]
・福島県ため池浚渫:比重1.01~1.02
・濁水pH:6.56
・濁度:500度以上(濁度計:TD-M500/オプテックス(株)製)
[試験対象2]
・栃木県採石場泥水:比重1.22(水道水希釈にて比重1.01に調整)
・濁水pH:5.86
・濁度:500度以上(濁度計:TD-M500/オプテックス(株)製)
[Test object 1]
・Fukushima prefecture irrigation pond dredging: specific gravity 1.01-1.02
・Muddy water pH: 6.56
・ Turbidity: 500 degrees or more (turbidity meter: TD-M500 / Optex Co., Ltd.)
[Test object 2]
・ Tochigi quarry mud: specific gravity 1.22 (adjusted to specific gravity 1.01 by diluting with tap water)
・Muddy water pH: 5.86
・ Turbidity: 500 degrees or more (turbidity meter: TD-M500 / Optex Co., Ltd.)

Figure 0007276769000001
Figure 0007276769000001

Figure 0007276769000002
Figure 0007276769000002

Figure 0007276769000003
Figure 0007276769000003

Figure 0007276769000004
Figure 0007276769000004

Figure 0007276769000005
Figure 0007276769000005

表3~表5の結果から、好ましい配合は実験例5の付近に選択性の広い凝集効果を示すと判断し、無水硫酸カルシウムを55w%~65w%、炭酸ナトリウムを7w%~12w%、珪藻土を5w%~10w%、炭酸カルシウムを0.5w%~5w%、硫酸アルミニウムを10w%~20w%、ポリ塩化アルミニウムを0.5w%~5w%、低分子アニオンポリマーを2w%~4w%、高分子アニオンポリマーを0.5w%~5w%、アルギン酸塩を1w%~4w%で配合することが望ましいと判断した。 From the results of Tables 3 to 5, it was determined that the preferred formulation exhibits a wide selective flocculation effect near Experimental Example 5. 5w% to 10w% of calcium carbonate, 0.5w% to 5w% of calcium carbonate, 10w% to 20w% of aluminum sulfate, 0.5w% to 5w% of polyaluminum chloride, 2w% to 4w% of a low-molecular anionic polymer, It was determined that it was desirable to incorporate 0.5w% to 5w% macromolecular anionic polymer and 1w% to 4w% alginate.

Figure 0007276769000006
Figure 0007276769000006

Figure 0007276769000007
Figure 0007276769000007

表6~表7の結果から、本件発明で使用される珪藻土は、焼成品である焼成珪藻土が望ましく、特に、pHが中性域(pH7.7±0.5程度)にあって、メジアン径(D50)8~12μm、比表面積1~5m/gのものがより望ましいと判断した。 From the results in Tables 6 and 7, the diatomaceous earth used in the present invention is desirably calcined diatomaceous earth that is a calcined product. (D50) of 8 to 12 μm and a specific surface area of 1 to 5 m 2 /g were judged to be more desirable.

以上、本発明の濁水処理用凝集剤について、その実施形態に基づいて説明したが、本発明は上記実施形態の記載に限定されるものではなく、その趣旨を逸脱しない範囲において適宜その構成を変更することができるものである。 As described above, the flocculant for treating turbid water of the present invention has been described based on the embodiments, but the present invention is not limited to the description of the above embodiments, and the configuration can be changed as appropriate without departing from the spirit of the present invention. It is something that can be done.

本発明の濁水処理用凝集剤は、濁水処理作業の省力化及び発生する処理水やフロックをpH中性に保ちながら、フロックからの脱水を促進し、スラッジの強度発現に寄与する特性を有していることから、土木工事や建設工事などから発生する濁水や、湖沼や河川、港岸などの底にたまった高含水泥土を洗浄する際に発生する濁水を処理する用途に好適に用いることができる。 The coagulant for turbid water treatment of the present invention has the characteristics of saving labor in turbid water treatment work, promoting dehydration from flocs while maintaining the pH of treated water and flocs generated, and contributing to the development of sludge strength. Therefore, it can be suitably used for treating turbid water generated from civil engineering and construction work, and turbid water generated when washing high water content mud accumulated at the bottom of lakes, marshes, rivers, port shores, etc. can.

Claims (2)

合成高分子凝集剤として1300万~1500万のアニオン度30mol~50mol%の高分子凝集剤0.5w%~5w%と、600万~1200万のアニオン度10mol%~30mol%の高分子凝集剤2w%~4w%とを配合し、
天然高分子凝集剤としてアルギン酸塩1w%~4w%を配合し、
アルカリ土類金属の中から無水又は半水硫酸カルシウム55w%~65w%と、炭酸カルシウム0.5w%~5w%とを配合し、
アルミニウム化合物として硫酸アルミニウム10w%~20w%と、ポリ塩化アルミニウム0.5w%~5w%とを配合し、
pH調整剤として炭酸ナトリウム7w%~12w%を配合し、
多孔質物質として焼成珪藻土の粉末5w%~10w%を配合してなる
ことを特徴とする濁水処理用凝集剤。
As a synthetic polymer flocculant, a polymer flocculant with an anion degree of 30 to 50 mol% of 13 to 15 million and an anion degree of 0.5 to 5 w% and a polymer flocculant of 6 to 12 million and an anion degree of 10 to 30 mol%. Formulated with 2w% to 4w% ,
Alginate 1w% to 4w% is blended as a natural polymer flocculant,
55w% to 65w% of anhydrous or hemihydrate calcium sulfate and 0.5w% to 5w% of calcium carbonate are blended from alkaline earth metals,
10w% to 20w% of aluminum sulfate and 0.5w% to 5w% of polyaluminum chloride are blended as an aluminum compound,
Contains 7w% to 12w% sodium carbonate as a pH adjuster,
A coagulant for treating turbid water, characterized in that 5w% to 10w% of calcined diatomaceous earth powder is blended as a porous material.
前記焼成珪藻土が、メジアン径が8~12μm、比表面積が1~5 m/gのものであることを特徴とする請求項に記載の濁水処理用凝集剤。 The flocculant for turbid water treatment according to claim 1 , wherein the calcined diatomaceous earth has a median diameter of 8 to 12 µm and a specific surface area of 1 to 5 m 2 /g.
JP2019129045A 2019-07-11 2019-07-11 Flocculant for turbid water treatment Active JP7276769B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2019129045A JP7276769B2 (en) 2019-07-11 2019-07-11 Flocculant for turbid water treatment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2019129045A JP7276769B2 (en) 2019-07-11 2019-07-11 Flocculant for turbid water treatment

Publications (2)

Publication Number Publication Date
JP2021013884A JP2021013884A (en) 2021-02-12
JP7276769B2 true JP7276769B2 (en) 2023-05-18

Family

ID=74531606

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2019129045A Active JP7276769B2 (en) 2019-07-11 2019-07-11 Flocculant for turbid water treatment

Country Status (1)

Country Link
JP (1) JP7276769B2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001129309A (en) 1999-11-04 2001-05-15 Kci:Kk Powder type flocculating and precipitating agent

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2774096B2 (en) * 1996-10-11 1998-07-09 小松 達利 Purification agent for polluted wastewater
JPH10118408A (en) * 1996-10-22 1998-05-12 Tomen Constr Kk Powder flocculant composition and water treatment

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001129309A (en) 1999-11-04 2001-05-15 Kci:Kk Powder type flocculating and precipitating agent

Also Published As

Publication number Publication date
JP2021013884A (en) 2021-02-12

Similar Documents

Publication Publication Date Title
JP4183741B1 (en) Adsorption / coagulation wastewater treatment agent
JP4515273B2 (en) Condensation separation purification agent and purification method of polluted waste water
JP5042589B2 (en) Powder solidifying material for soft mud soil and method for producing the same
JPH09225208A (en) Sewage treatment agent and treatment method
KR100247126B1 (en) Solid flocculant and high speed flocculation separator
JP7276769B2 (en) Flocculant for turbid water treatment
US5520819A (en) Method of removing suspensions from wastewater
JP2000246013A (en) Flocculating sedimentation agent and flocculation treatment method
JP4158127B2 (en) Special solid fine powder flocculant composition for treatment of hexavalent chromium contaminated water and treatment method using the same
JP2001347104A (en) Powdery decontaminant and method of decontaminating clean water and waste water
JP3262194B2 (en) Treatment of colored concrete wastewater.
JP2010172882A (en) Coagulant, and method of treating muddy effluent
JPH1028808A (en) Special solid fine powdery flocculant composition and water treatment method
JP3705012B2 (en) Muddy water dehydration
JP6322398B2 (en) Waste water treatment agent and waste water treatment method
JP2002045610A (en) Powdery cleaning agent, and method for cleaning city water and waste water
JP2001129309A (en) Powder type flocculating and precipitating agent
JPH09239207A (en) Special solid fine powdery flocculant composition and water treatment method
JP2715017B2 (en) Coagulant for civil engineering
JP4828378B2 (en) Powdered muddy water treatment agent, muddy water dewatering method, and muddy water volume reducing treatment device
JPH09192674A (en) Flocculating method and flocculant
JP2000334210A (en) Flocculant and method for treating suspension using the same
JP2006247630A (en) Waste water treating hydrophobization solid-liquid separating medium
JP3398182B2 (en) Sludge treatment method and treatment material used therefor
JP3464448B2 (en) Flocculant

Legal Events

Date Code Title Description
A621 Written request for application examination

Free format text: JAPANESE INTERMEDIATE CODE: A621

Effective date: 20220525

RD02 Notification of acceptance of power of attorney

Free format text: JAPANESE INTERMEDIATE CODE: A7422

Effective date: 20220525

A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20230126

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20230207

A521 Request for written amendment filed

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20230329

TRDD Decision of grant or rejection written
A01 Written decision to grant a patent or to grant a registration (utility model)

Free format text: JAPANESE INTERMEDIATE CODE: A01

Effective date: 20230418

A61 First payment of annual fees (during grant procedure)

Free format text: JAPANESE INTERMEDIATE CODE: A61

Effective date: 20230425

R150 Certificate of patent or registration of utility model

Ref document number: 7276769

Country of ref document: JP

Free format text: JAPANESE INTERMEDIATE CODE: R150