JPH0938414A - Flocculating precipitant - Google Patents

Flocculating precipitant

Info

Publication number
JPH0938414A
JPH0938414A JP21112695A JP21112695A JPH0938414A JP H0938414 A JPH0938414 A JP H0938414A JP 21112695 A JP21112695 A JP 21112695A JP 21112695 A JP21112695 A JP 21112695A JP H0938414 A JPH0938414 A JP H0938414A
Authority
JP
Japan
Prior art keywords
calcium carbonate
flocculating
average particle
fine particles
present
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.)
Withdrawn
Application number
JP21112695A
Other languages
Japanese (ja)
Inventor
Hiroshi Shibata
洋志 柴田
Shigeo Takiyama
成生 瀧山
Yusuke Hayashi
林  祐輔
Toshio Fujiwara
敏男 藤原
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.)
Maruo Calcium Co Ltd
Original Assignee
Maruo Calcium 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 Maruo Calcium Co Ltd filed Critical Maruo Calcium Co Ltd
Priority to JP21112695A priority Critical patent/JPH0938414A/en
Publication of JPH0938414A publication Critical patent/JPH0938414A/en
Withdrawn legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To obtain a flocculating precipitant having a high sedimentation velocity when added to waste water, forming large flocks and facilitating the treatment of sludge. SOLUTION: This flocculating precipitant contains coarse particles of calcium carbonate having 50-500μm average particle diameter and fine particles of calcium carbonate having 1-30μm average particle diameter.

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】本発明は凝集沈澱剤に関し、
更に詳しくは、土木・建設廃水を含め工業廃水の懸濁物
(Suspended Solid 、以下SSと略記する)等の処理に
おいて簡単に利用することができ、凝集物の沈降スピー
ドが速いため処理後のスラッジの分離を容易に行うこと
ができる凝集沈澱剤に関する。
TECHNICAL FIELD The present invention relates to a flocculating precipitant,
More specifically, it can be easily used in the treatment of suspended solids (Suspended Solid, hereinafter abbreviated as SS) of industrial wastewater including civil engineering and construction wastewater, and the sludge after treatment has a high sedimentation speed of aggregates. The present invention relates to an aggregating and precipitating agent capable of easily separating the above.

【0002】[0002]

【従来の技術】土木や建築分野においては土木・建築廃
水に、また紙・パルプ・食品・染色等の分野においては
化学工業廃水に多量に含まれる有機及び無機のSSが発
生する。一般に廃水処理は有機物質を除去するために、
活性汚泥槽等で生物処理を施し、沈澱物は各種凝集剤を
添加することにより沈澱槽で沈澱物を分離する方法が、
また、沈澱物として回収できない浮遊物は濾過によって
除去する方法が採用されている。このため、廃水処理に
は大規模な処理設備が必要とされ廃水処理コストが高く
なる。
2. Description of the Related Art A large amount of organic and inorganic SS is generated in civil engineering and construction wastewater in the field of civil engineering and construction, and in chemical industry wastewater in the fields of paper, pulp, food and dyeing. Generally, wastewater treatment is to remove organic substances,
A method of performing biological treatment in an activated sludge tank, etc., and separating the precipitate in the precipitation tank by adding various coagulants to the precipitate,
In addition, a method is adopted in which a floating material that cannot be collected as a precipitate is removed by filtration. Therefore, a large-scale treatment facility is required for wastewater treatment, and the wastewater treatment cost becomes high.

【0003】また、簡単な方法として、凝集剤と石膏、
石灰、炭酸カルシウム、セメント類等を配合することが
提案されている(特開平2−71805)。この方法は
石膏、石灰、炭酸カルシウム、セメント類等を隔離剤と
して使用しているが、粒径のコントロールが出来ていな
いため凝集剤の効果が発揮されないばかりでなく、沈降
速度についても満足できるものではなかった。
As a simple method, a coagulant and gypsum,
It has been proposed to blend lime, calcium carbonate, cements, etc. (JP-A-2-71805). This method uses gypsum, lime, calcium carbonate, cements, etc. as a sequestering agent, but because the particle size cannot be controlled, not only the effect of the coagulant is not exhibited, but also the sedimentation rate is satisfactory. Was not.

【0004】[0004]

【発明が解決しようとする課題】本発明は、かかる実情
に鑑み、廃水処理コストを低減し、簡単で沈降速度が速
く、効率的に廃水処理を行うことのできる凝集沈澱剤を
提供することを目的とするものである。
SUMMARY OF THE INVENTION In view of such circumstances, the present invention provides a coagulating sedimentation agent which reduces wastewater treatment cost, is simple, has a high sedimentation rate, and can efficiently perform wastewater treatment. It is intended.

【0005】[0005]

【課題を解決するための手段】本発明者らは、前記した
簡単で沈降速度の速い凝集沈澱剤を開発するため種々研
究を重ねた結果、凝集剤の配合中の炭酸カルシウムの粒
度及び配合量を調整することによってその目的が達成さ
れることを見出し、この知見に基づいて本発明を完成す
るに至った。すなわち、本発明は、平均粒子径50〜5
00μmの粗粒子及び平均粒子径1〜30μmの微粒子
からなる、粒度の異なる2種類の炭酸カルシウムを含有
してなる凝集沈澱剤を内容とするものである。
The present inventors have conducted various studies to develop the above-mentioned simple and fast flocculating precipitant, and as a result, the particle size and the amount of calcium carbonate in the flocculating agent are mixed. It was found that the object can be achieved by adjusting the above, and the present invention has been completed based on this finding. That is, the present invention has an average particle size of 50 to 5
The present invention is directed to a flocculating precipitant containing two kinds of calcium carbonate having different particle sizes, each of which consists of coarse particles of 00 μm and fine particles having an average particle diameter of 1 to 30 μm.

【0006】本発明は凝集剤の沈降速度を速くするた
め、粒度の異なる2種類の重質炭酸カルシウムを使用す
ることを特徴とする。本発明に使用される炭酸カルシウ
ムの粗粒子は平均粒子径50〜500μm、好ましくは
100〜200μmで、通常、重質炭酸カルシウムが用
いられる。粗粒子の平均粒子径が50μmより小さいと
沈降速度が遅くなり、またスラッジの嵩密度が大きくな
る。また、粗粒子の平均粒子径が500μmより大きい
と凝集沈澱剤を均一に配合することが難しく、またSS
の捕捉能力が低下する。
The present invention is characterized by using two types of ground calcium carbonate having different particle sizes in order to accelerate the sedimentation rate of the flocculant. The coarse particles of calcium carbonate used in the present invention have an average particle diameter of 50 to 500 μm, preferably 100 to 200 μm, and heavy calcium carbonate is usually used. If the average particle diameter of the coarse particles is smaller than 50 μm, the sedimentation speed becomes slow and the bulk density of the sludge becomes large. Further, if the average particle size of the coarse particles is larger than 500 μm, it is difficult to uniformly mix the coagulating / precipitating agent, and
The ability to capture is reduced.

【0007】本発明に使用される炭酸カルシウムの微粒
子は、平均粒子径1〜30μm、好ましくは5〜20μ
mである。重質炭酸カルシウム、軽質炭酸カルシウムの
いずれでもよいが、粒度のコントロール及びコストの点
から重質炭酸カルシウムが好ましい。微粒子は凝集沈澱
剤中の酸性物質と容易に反応し、pHを中性に保つことが
可能である。微粒子の平均粒子径が1μmより小さいと
凝集剤の効果が低下し、沈降速度が低下する。また微粒
子の平均粒子が30μmより大きいと溶解速度が低下し
凝集沈殿剤中の酸性物質と反応が遅くなるため、pHのコ
ントロールが難しくなる。
The fine particles of calcium carbonate used in the present invention have an average particle size of 1 to 30 μm, preferably 5 to 20 μm.
m. Either heavy calcium carbonate or light calcium carbonate may be used, but heavy calcium carbonate is preferable from the viewpoint of particle size control and cost. The fine particles easily react with the acidic substance in the flocculant-precipitating agent, and the pH can be kept neutral. If the average particle size of the fine particles is smaller than 1 μm, the effect of the coagulant is reduced and the sedimentation rate is reduced. Further, if the average particle size of the fine particles is larger than 30 μm, the dissolution rate decreases and the reaction with the acidic substance in the flocculating and precipitating agent becomes slow, so that the pH control becomes difficult.

【0008】本発明における炭酸カルシウムの配合量は
60重量%以上が好ましく、より好ましくは70%以上
である。配合量が60重量%より少ないと沈降速度が遅
くなり、本発明の目的を充分に達成することができな
い。上限は99重量%が好ましい。
The content of calcium carbonate in the present invention is preferably 60% by weight or more, more preferably 70% or more. If the blending amount is less than 60% by weight, the sedimentation rate becomes slow and the object of the present invention cannot be sufficiently achieved. The upper limit is preferably 99% by weight.

【0009】炭酸カルシウムの粗粒子と微粒子の割合
は、好ましくは2:1〜40:1がよい。粗粒子が2:
1より少ないと余り効果が発揮されず、沈降速度が遅く
なる。また、粗粒子が40:1より多いとpHコントロー
ルが難しくなる。
The ratio of coarse particles to fine particles of calcium carbonate is preferably 2: 1 to 40: 1. Coarse particles are 2:
If it is less than 1, the effect is not exerted so much and the sedimentation speed becomes slow. If the coarse particles are more than 40: 1, pH control becomes difficult.

【0010】本発明の凝集剤は上記粒度の異なる炭酸カ
ルシウムの他に、可溶性アルミニウム塩、可溶性の鉄
塩、及び有機系の高分子凝集剤等が、廃水中に含まれ反
応する物質の種類に応じて適宜1種または2種以上組み
合わせて用いられる。
The coagulant of the present invention includes soluble aluminum salts, soluble iron salts, organic polymer coagulants, etc. in addition to calcium carbonate having different particle sizes, depending on the types of substances contained in the waste water and reacting with each other. Depending on the case, they may be used alone or in combination of two or more.

【0011】具体的には、例えば無機系では硫酸アルミ
ニウム、ポリ塩化アルミニウム、硫酸第一鉄、硫酸第二
鉄等が挙げられ、これらは単独又は2種以上組み合わせ
て用いられる。これらの酸性物質は、炭酸カルシウムや
pH調整剤である水酸化カルシウム等と容易に反応しSS
を吸着する。また、有機系ではポリアクリルアミド、ポ
リアクリル酸ソーダ及びポリメタクリル酸エステル系等
の高分子凝集剤が挙げられ、これらは単独又は2種以上
組み合わせて用いられる。有機系の凝集剤は、炭酸カル
シウムと無機系凝集剤により吸着された粒子を造粒し大
きなフロックを形成する。
Specific examples of the inorganic type include aluminum sulfate, polyaluminum chloride, ferrous sulfate, ferric sulfate and the like, and these may be used alone or in combination of two or more. These acidic substances are calcium carbonate and
It easily reacts with calcium hydroxide, which is a pH adjuster, and SS
To adsorb. Examples of the organic type include polymer aggregating agents such as polyacrylamide, sodium polyacrylate and polymethacrylic acid ester, which may be used alone or in combination of two or more kinds. The organic flocculant granulates the particles adsorbed by the calcium carbonate and the inorganic flocculant to form large flocs.

【0012】本発明の凝集沈殿剤は、無機系の凝集剤が
酸性であり、炭酸カルシウムがアルカリ性であるが、凝
集沈澱剤を中性とするためにpH調整剤として水酸化カル
シウム、水酸化ナトリウム、炭酸ナトリウム等を用いる
ことができる。本発明の凝集沈澱剤は、更に通常用いら
れるセメント、フライアッシュ、ベントナイト等の添加
剤を添加することも可能である。
In the flocculating and precipitating agent of the present invention, the inorganic flocculating agent is acidic and calcium carbonate is alkaline, but calcium hydroxide and sodium hydroxide are used as pH adjusters in order to neutralize the flocculating and precipitating agent. , Sodium carbonate and the like can be used. The coagulant-precipitating agent of the present invention may further contain additives such as commonly used cement, fly ash and bentonite.

【0013】[0013]

【実施例】以下、実施例により本発明を更に詳細に説明
するが、本発明はこれら実施例により何ら制限されるも
のではない。
The present invention will be described in more detail with reference to the following examples, but the present invention is not limited to these examples.

【0014】実施例1、2、3 重質炭酸カルシウムの粗粒子(平均粒子径 100μ
m)、重質炭酸カルシウムの微粒子(平均粒子径 3.
1μm)、硫酸バンド(硫酸アルミニウム)、水酸化カ
ルシウム及び高分子凝集剤ポリアクリルアミドを表1に
示す配合量で添加し、ミキサーで5分間混合し、凝集沈
澱剤を得た。得られた凝集沈澱剤を用いて、土木現場で
発生した泥水に凝集剤の濃度が一定になるように添加し
て沈降試験を行った。評価は凝集の度合い(フロックの
大きさ)、沈降速度、透明度、pH、スラッジの濾過性に
ついて行い、その評価結果を表1に併記した。
Examples 1, 2, 3 Coarse particles of heavy calcium carbonate (average particle size 100 μm
m), fine particles of heavy calcium carbonate (average particle size 3.
1 μm), a sulfuric acid band (aluminum sulfate), calcium hydroxide and a polymer flocculant polyacrylamide were added in amounts shown in Table 1 and mixed with a mixer for 5 minutes to obtain a flocculating precipitant. Using the obtained coagulant-precipitating agent, the coagulant was added to mud generated at a civil engineering site so that the concentration of the coagulant was constant, and a sedimentation test was conducted. The evaluation was performed on the degree of aggregation (size of flocs), sedimentation speed, transparency, pH, and sludge filterability, and the evaluation results are also shown in Table 1.

【0015】凝集の度合い、沈降速度、透明度、スラッ
ジの濾過性の評価基準は下記のとおりである。 凝集度合: 〇:良好である。 沈降速度: 〇:速い △:やや遅い 透明度: 〇:透明である △:やや不透明である ×:不透
明である スラッジの濾過性: 〇:良好である △:やや不良である ×:不良で
ある
The evaluation criteria for the degree of aggregation, sedimentation speed, transparency and sludge filterability are as follows. Aggregation degree: ◯: Good. Sedimentation rate: ◯: Fast △: Slightly slow Transparency: 〇: Transparent Δ: Slightly opaque ×: Opaque Sludge filterability: ◯: Good Δ: Slightly bad ×: Bad

【0016】比較例1、2、3 重質炭酸カルシウムの粗粒子と微粒子を混合しないで、
表1に示す配合物及び配合量で凝集沈澱剤を得た。実施
例1と同様に沈降試験の評価を行い、その評価結果を表
1に併記した。
Comparative Examples 1, 2, 3 Without mixing coarse particles and fine particles of heavy calcium carbonate,
Aggregating and precipitating agents were obtained in the formulations and amounts shown in Table 1. The sedimentation test was evaluated in the same manner as in Example 1, and the evaluation results are also shown in Table 1.

【0017】表1から明らかなように、実施例1〜3
は、比較例1〜3に比べて沈降速度が大きく、透明度も
良好である。比較例1では重質炭酸カルシウムの微粒子
が含まれていないため、凝集沈澱剤中の酸性物質との反
応が遅く、透明度が劣りpHは酸性となった。また、比較
例2においては、重質炭酸カルシウムの粗粒子が含まれ
ていないため沈降速度が遅く透明度が劣るとともに、ス
ラッジを濾過処理する際に濾過性が悪くスラッジの処分
に問題のあることがわかる。更に比較例3は重質炭酸カ
ルシウムの量が少なく、沈降速度が遅い。
As is apparent from Table 1, Examples 1 to 3
Has a higher sedimentation rate and better transparency than Comparative Examples 1 to 3. In Comparative Example 1, since fine particles of heavy calcium carbonate were not included, the reaction with the acidic substance in the flocculating and precipitating agent was slow, the transparency was poor, and the pH was acidic. Further, in Comparative Example 2, since coarse particles of heavy calcium carbonate are not included, the sedimentation speed is slow and the transparency is poor, and the sludge is poor in filterability when it is subjected to a filtering process, and there is a problem in sludge disposal. Recognize. Further, in Comparative Example 3, the amount of heavy calcium carbonate is small and the sedimentation rate is slow.

【0018】比較例4 重質炭酸カルシウムの代わりにセメントを配合し、凝集
沈澱剤を得た。同様にして沈降試験を行い、その評価結
果を表1に併記した。沈降速度、透明度のいずれにおい
ても劣り、またpHはアルカリ性となった。
Comparative Example 4 Cement was blended in place of the ground calcium carbonate to obtain a coagulating sedimentation agent. A sedimentation test was conducted in the same manner, and the evaluation results are also shown in Table 1. Both the sedimentation rate and the transparency were inferior, and the pH became alkaline.

【0019】[0019]

【表1】 [Table 1]

【0020】[0020]

【発明の効果】上記のように、本発明の凝集沈澱剤は、
廃水に添加した場合に沈降速度が速く大きなフロックを
形成し、且つスラッジの処理を簡単に行うことができ
る。また本発明の凝集沈澱剤は粉体状で取扱が容易であ
る。
As described above, the flocculating and precipitating agent of the present invention is
When added to wastewater, the sedimentation speed is high and large flocs are formed, and sludge can be easily treated. The flocculating and precipitating agent of the present invention is in the form of powder and is easy to handle.

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 平均粒子径50〜500μmの粗粒子及
び平均粒子径1〜30μmの微粒子からなる、粒度の異
なる2種類の炭酸カルシウムを含有してなる凝集沈澱
剤。
1. An aggregating and precipitating agent comprising two kinds of calcium carbonate having different particle sizes, which comprises coarse particles having an average particle size of 50 to 500 μm and fine particles having an average particle size of 1 to 30 μm.
【請求項2】粗粒子と微粒子との混合割合が重量比で
2:1〜40:1である請求項1記載の凝集沈澱剤。
2. The flocculating and precipitating agent according to claim 1, wherein the mixing ratio of the coarse particles and the fine particles is 2: 1 to 40: 1 by weight.
【請求項3】 炭酸カルシウムの含有量が60重量%以
上である請求項1又は2記載の凝集沈澱剤。
3. The flocculating precipitant according to claim 1, wherein the content of calcium carbonate is 60% by weight or more.
【請求項4】 更に、可溶性アルミニウム塩、可溶性の
鉄塩、及び有機系の高分子凝集剤からなる群から選ばれ
る少なくとも1種を配合してなる請求項1〜3記載の凝
集沈澱剤。
4. The flocculating precipitant according to claim 1, further comprising at least one selected from the group consisting of a soluble aluminum salt, a soluble iron salt, and an organic polymer flocculant.
JP21112695A 1995-07-26 1995-07-26 Flocculating precipitant Withdrawn JPH0938414A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21112695A JPH0938414A (en) 1995-07-26 1995-07-26 Flocculating precipitant

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21112695A JPH0938414A (en) 1995-07-26 1995-07-26 Flocculating precipitant

Publications (1)

Publication Number Publication Date
JPH0938414A true JPH0938414A (en) 1997-02-10

Family

ID=16600829

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21112695A Withdrawn JPH0938414A (en) 1995-07-26 1995-07-26 Flocculating precipitant

Country Status (1)

Country Link
JP (1) JPH0938414A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101356688B1 (en) * 2011-12-15 2014-01-28 한국건설기술연구원 Nano-sized metal oxide-laponite composites to treat recalcitrant organic pollutant complexes and manufacturing method the same
KR20190005058A (en) * 2017-07-05 2019-01-15 (주)큐앤테크 Measurement method for mixed liquor suspended solids
DE202018006098U1 (en) 2018-05-03 2019-03-15 Schaefer Kalk Gmbh & Co. Kg Means for lowering the phosphate content in waste water
EP3563917A1 (en) 2018-05-03 2019-11-06 Schaefer Kalk GmbH & Co. KG Agent for lowering the phosphate content in waste waters
US11414550B2 (en) * 2015-04-27 2022-08-16 Imerys Usa, Inc. Compositions including blends of hydrophobic and non-hydrophobic inorganic particulate material, for use in covering products

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR101356688B1 (en) * 2011-12-15 2014-01-28 한국건설기술연구원 Nano-sized metal oxide-laponite composites to treat recalcitrant organic pollutant complexes and manufacturing method the same
US11414550B2 (en) * 2015-04-27 2022-08-16 Imerys Usa, Inc. Compositions including blends of hydrophobic and non-hydrophobic inorganic particulate material, for use in covering products
KR20190005058A (en) * 2017-07-05 2019-01-15 (주)큐앤테크 Measurement method for mixed liquor suspended solids
DE202018006098U1 (en) 2018-05-03 2019-03-15 Schaefer Kalk Gmbh & Co. Kg Means for lowering the phosphate content in waste water
EP3563917A1 (en) 2018-05-03 2019-11-06 Schaefer Kalk GmbH & Co. KG Agent for lowering the phosphate content in waste waters
WO2019211375A1 (en) 2018-05-03 2019-11-07 Schaefer Kalk Gmbh & Co. Kg Agent for reducing the phosphate concentration in wastewater
EP4122574A1 (en) 2018-05-03 2023-01-25 Schaefer Kalk GmbH & Co. KG Agent for lowering the phosphate content in waste waters

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