JP3727303B2 - Inorganic sludge reforming coagulation purification agent - Google Patents

Inorganic sludge reforming coagulation purification agent Download PDF

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JP3727303B2
JP3727303B2 JP2002345079A JP2002345079A JP3727303B2 JP 3727303 B2 JP3727303 B2 JP 3727303B2 JP 2002345079 A JP2002345079 A JP 2002345079A JP 2002345079 A JP2002345079 A JP 2002345079A JP 3727303 B2 JP3727303 B2 JP 3727303B2
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sludge
inorganic
purification agent
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JP2004174407A (en
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文男 岩本
俊博 尾北
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Description

【0001】
【発明の属する技術分野】
本発明は無機系汚濁排水、有機系汚濁排水の汚泥凝集分離浄化剤に関し、また当該汚濁排水中に溶存する金属類(重金属類を含む)による汚濁物質と浮遊懸濁物質とを同時に吸着、あるいは収着し凝集分離するとともに、凝集汚泥の性状を改質し、金属類(重金属類を含む)も再溶出することのない極めて安定した固形物として分離することができる。即ち、当該汚濁排水を優れた水質に浄化するとともに、汚濁物質を極めて安定した疎水性に富んだ凝集汚泥として分離することができ、さらに、脱水汚泥は再び水に溶解し崩壊することがなく、経時的に自然土壌に近似した泥質に改質する機能を兼ね備えた汚濁排水浄化処理剤の新規の無機系汚泥改質凝集浄化剤に関する。
【0002】
【従来の技術】
無機系、有機系の汚濁排水の処理は、従来は無機系または有機系凝集剤を添加して汚濁排水中の浮遊懸濁物質を凝集分離し、所定の水質基準を満たすよう処理水を調整(例えばPH調整、脱色など)して放流され、分離汚泥は脱水し、さらには必要に応じて重金属類など不溶化処理して廃棄されている。
【0003】
汚濁排水処理に使用されている無機系あるいは有機系凝集剤のいずれにおいても、汚濁排水中の浮遊物質を効率よく凝集させることが主目的となっている。
したがって、汚濁排水中に溶存している金属類(重金属類を含む)などの一部は浮遊懸濁物質に取り込まれた状態で分離されているとはいえ、従来の凝集剤自体には積極的に金属類(重金属類を含む)の固定する機能は備えていないので、投棄された場合、溶出は免れない。即ち、金属類(重金属類を含む)の不溶出化処理には別法が必要となる。
【0004】
さらに、汚濁排水処理に使用されている無機系または有機系凝集剤による凝集分離汚泥、また、脱水後の汚泥のいずれの場合もその含水率が高い。
また、一般に水に再溶解しやすく、投棄した場合には土壌汚染の大きな原因となり、新たな環境汚染を引き起こすことになる。
【0005】
汚濁排水処理に使用されている無機系または有機系凝集剤で凝集分離された汚泥は脱水されるが、減容化のために焼却処分している。
この焼却処分の際に発生する排気ガス中の極めて有害とされるダイオキシン類と焼却灰および飛灰中に残留する不安定な重金属類が、新たに環境汚染の原因となり、早急の対策法が求められている。
【0006】
【発明が解決しようとする課題】
従来の無機系、有機系の汚濁排水の処理における、上記したような種々の問題を解決することのできる新規の粉体の汚濁排水の汚泥改質凝集分離浄化剤の提供を目的とする。
具体的には、当該の汚濁排水(無機系、有機系を問わず)が酸性またはアルカリ性(水素イオン濃度PH4〜9の範囲)であっても、極めて迅速に汚濁物質(溶存物質も含む)を物理的・化学的に凝集分離し、清浄な中性の分離水が得られ、しかも、凝集分離した汚泥は極めて安定な物質に改質されて、脱水性に富み、さらに、金属類(重金属類を含む)も化学的に、また生物的にも固定され、安定した難溶性の汚泥が得られる。さらに、凝集汚泥、脱水汚泥は水に難溶性となり、微生物により汚泥は土壌に近似した性状に改質される。
また、脱水汚泥の焼却処分の際に発生するダイオキシン類の有害ガスも、脱水汚泥の含水率低下と配合される無機成分の相乗効果により抑制され、焼却灰および飛灰中に残留する不安定な重金属類も化学的に安定固化・固定される。
【0007】
本発明の前記ならびにそのほかの目的と新規な特徴は次の説明を添付図面と照らし合わせて読むと、より完全に明らかになるであろう。
ただし、図面はもっぱら解説のためのものであって、本発明の技術的範囲を限定するものではない。
【0008】
【課題を解決するための手段】
上記目的を達成するために、本発明は土壌菌を配合した珪藻土に対して活性炭10〜30重量部、セメント20〜50重量部、有機系凝集剤2〜5重量部を配合した主成分100重量部に対し、チオ硫酸ナトリウム10〜20重量部、酸化鉄10〜20重量部、硫酸カルシウム30〜60重量部、硫酸アルミニウム20〜50重量部、アルカリ金属炭酸塩10〜20重量部が均一に配合して無機系汚泥改質凝集剤を構成している。
【0009】
【発明の実施の形態】
以下、図面に示す実施の形態により、本発明を詳細に説明する。
【0010】
図1および図2に示す本発明の第1の実施の形態において、1は無機系汚濁排水、有機系汚濁排水を処理する無機系汚泥改質凝集浄化剤で、この無機系汚泥改質凝集浄化剤1は土壌菌2を配合した珪藻土3に対して活性炭4を10〜30重量部、セメント5を20〜50重量部、有機系凝集剤6を2〜5重量部を配合した主成分7を100重量部に対し、総重量が20〜30重量部の配合比となるようにチオ硫酸ナトリウム8を10〜20重量部、酸化鉄9を10〜20重量部、硫酸カルシウム10を30〜60重量部、硫酸アルミニウム11を20〜50重量部、アルカリ金属炭酸塩12を10〜20重量部が均一に配合されて構成されている。
【0011】
前記の珪藻土3は、淡水成珪藻土または海水成珪藻土の1種あるいは2種の混合、いずれかが選ばれる。珪藻土3は濾材として、また、油脂類の吸着などに優れた機能をもつ他、これらの天然鉱物には多種多様の鉱物性微量元素(ミネラル成分)が含有している。
この微量元素は経時的に汚濁排水中に溶出し、当該汚濁排水中の溶存酸素や解離酸イオンと相乗的に反応し、有機質の汚濁物質(溶存物質も含む)を還元または酸化・分離などにより疎水性の凝固体として分離し、浄化する機能がある。
なお、これらの天然鉱物は、当該汚濁排水の水素イオン濃度PH4〜9の範囲(酸性領域、中性領域、アルカリ領域)で、その機能を有効に発揮する。
【0012】
前記の土壌菌2は、枯草菌類バチルスBacillusとシュウドモナス菌類Pseudomonasとこれらの変成菌類を選択した。いずれも代表的存在の土壌菌であり、油類、油脂類の分解能のほか、長期にわたって汚濁物質(無機化合物、有機化合物なども含む)の分解と土壌化、さらには無害化の能力を発揮する。また、処理水の水質値低下にも寄与している。
【0013】
前記の活性炭4とセメント5および有機系凝集剤6については特に限定はしていない。活性炭4は100メッシュ以下の微細な粉末を選び、その吸着能を利用して有機物、臭気、色などの除去が目的である。
セメントはポルトランドセメント(普通、早強、超早強、中庸熱、耐硫酸塩)、高炉セメント、フライアッシュセメント、アルミナセメントから選ばれるが、実際には1種類または数種類混合して配合され、臭気、有害物質の吸着と水和反応による凝集固化などの機能を付加することを目的としている。
有機系凝集剤6については通常、汚濁排水中の浮遊懸濁物質の1.2wt%が標準使用量とされているが、本発明の無機系汚泥改質凝集浄化剤1では実質の有機系凝集剤の量は有機系凝集剤単独使用の約10分の1で同等の効果があげられる。有機系凝集剤の減量が図れる優位差がある。
また、本発明の無機系汚泥改質凝集浄化剤1は粉末のまま当該の汚濁排水に添加され、前段の反応すなわち汚濁物質の分解と汚泥改質機能が優先され、後段の反応すなわち凝集固化反応には時間差が設定されている。
配合されている有機系凝集剤6は前段の反応の間に徐々に溶解し、改質汚泥を凝集分離し固化が進行する。
【0014】
前記チオ硫酸ナトリウム8は、重金属類と積極的に反応して不溶性のチオ硫酸金属化合物を形成する。汚濁物質中の重金属類の数値に応じてチオ硫酸ナトリウム8の配合比を調整することができる。
【0015】
前記酸化鉄9(具体的にはベガラ)は、汚濁物質の凝集、改質などのそれぞれの反応における触媒として相乗効果をあげる目的がある。
【0016】
前記硫酸カルシウム10は、当該の汚濁排水中で分散して懸濁し、その一部が溶解する。後述の硫酸アルミニウム11の解離により生成する遊離酸の中和剤としての機能を発揮すると同時に、凝集、固化反応の助剤としても寄与する。
【0017】
前記硫酸アルミニウム11は、当該の汚濁排水中に容易に溶解し、加水分解して硫酸アルミニウム11と硫酸に解離する。
酸化アルミニウムはさらにコロイド状の水酸化アルミニウムと、イオン化した水酸化アルミニウムからなる重縮合水酸化アルミニウムに転化する。
この重縮合水酸化アルミニウムは、当該の汚濁排水中の浮遊懸濁物の粒子間の電位を低下させる。そのために汚濁物質の粒子間のバランスは崩壊して微粒子化し、この微粒子は有機金属類の無機化、金属類(重金属類も含む)のイオン吸着、固定などの機能を発揮して、新たに凝集し分離する。
【0018】
前記アルカリ金属炭酸塩12も当該汚濁排水に容易に溶解して、遊離酸の中和と凝集反応に寄与する。
アルカリ金属炭酸塩12としては、炭酸ナトリウム、炭酸カルシウム、炭酸マグネシウム、ドロマイトなどがあげられる。
【0019】
上記構成の無機系汚泥改質凝集浄化剤1は、微生物(土壌菌類)を含浸させた天然鉱物(粉体)と、無機系化合物(いずれも粉末)と少量の有機系凝集剤(粉末)が所定の割合で配合され、構成されていることを特徴としている。
【0020】
上記構成の無機系汚泥改質凝集浄化剤1の使用上の条件は、
(1)粉末のまま所定量を添加する。
(2)添加後の混合撹拌、設計された反応(分解、汚泥改質、固定、凝集、分離など)をより効果的にするために強い撹拌が望ましい。
(3)標準添加量は、当該汚濁排水中の汚濁物質の5wt%tが目安となる。
【0021】
上記構成の無機系汚泥改質凝集浄化剤1の凝集反応は極めて速く、凝集汚泥は撹拌によりさらに固く高密度化して分離する。
凝集分離汚泥は疎水性の極めて安定した汚泥であり、崩壊や再溶解することがない。
また、凝集分離汚泥の脱水性は高く、脱水汚泥の臭気も緩和され、自然土壌に近似した汚泥に改質し、金属類(重金属類を含む)の溶出もなく、汚泥中の残留有機物の腐敗なども土壌菌により抑制され、経時的に自然に腐植化される。
【0022】
【発明の異なる実施の形態】
次に、図3および図4に示す本発明の異なる実施の形態につき説明する。なお、この本発明の異なる実施の形態の説明に当って、前記本発明の第1の実施の形態と同一構成部分には同一符号を付して重複する説明を省略する。
【0023】
図3および図4に示す本発明の第2の実施の形態において、前記本発明の第1の実施の形態と主に異なる点は、主成分7を100重量部に対し、チオ硫酸ナトリウム8を10〜20重量部、酸化鉄9を10〜20重量部、硫酸カルシウム10を30〜60重量部、硫酸アルミニウム11を10〜50重量部、アルカリ金属炭酸塩12を10〜20重量部のうちの、少なくとも3種以上を均一に配合した点で、このように構成した無機系汚泥改質凝集浄化剤1Aにしてもよい。
【0024】
【実験例】
(1)無機系汚泥改質凝集浄化剤の調整
・主要成分の調整:珪藻土3はRadiolite#800を選び、これに予め土壌菌2の培養液を散水して含浸させた後、乾燥させておく。
配合比は、珪藻土3が100重量部に対して活性炭4が(100メッシュ以下)10重量部、普通ポルトランドセメント20重量部、高分子凝集剤(+)3重量部とし、これらを均一に混合する。
・必須成分の調整:配合比は、主成分7が100重量部に対してチオ硫酸ナトリウム8が10〜20重量部、酸化鉄9が10重量部、硫酸カルシウム10が35重量部、硫酸アルミニウム11が40重量部、炭酸カルシウム12が15重量部とした。
それぞれ所定量を採り、均一になるよう混合して本発明の無機系汚泥改質凝集浄化剤を調整した。
(2)対象物としては、現在一般に使用されている無機系または有機系の凝集剤によるデータを採用した。
1.下水処理場の一次処理水の浄化試験の結果を図5に、濃縮汚泥の脱水試験の結果を図6に示した。
2.し尿処理場の脱離液の浄化試験の結果を図7に示した。
3.畜産(豚)し尿の前処理の結果を図8に示した。
4.工場排水:製紙工場の排水の水質浄化試験の結果を図9に示した。
5.鉱山排水:排水および汚泥の重金属類の固定処理の結果を図10に示した。
【0025】
【発明の効果】
以上の説明から明らかなように、本発明にあっては次に列挙する効果が得られる。
【0026】
(1)土壌菌を配合した珪藻土に対して活性炭10〜30重量部、セメント20〜50重量部、有機系凝集剤2〜5重量部を配合した主成分100重量部に対し、チオ硫酸ナトリウム10〜20重量部、酸化鉄10〜20重量部、硫酸カルシウム30〜60重量部、硫酸アルミニウム20〜50重量部、アルカリ金属炭酸塩10〜20重量部が均一に配合されているので、無機系汚濁排水、有機系汚濁排水が酸性またはアルカリ性(水素イオン濃度PH4〜9の範囲)であっても、極めて迅速に汚濁物質(溶存物質も含む)を物理的・化学的に凝集分離し、清浄な中性の分離水が得られる。
しかも、凝集分離した汚泥は極めて安定な物質に改質されて、脱水性に富み、さらに、金属類(重金属類を含む)も化学的に、また生物的にも固定され、安定した難溶性の汚泥が得られる。
【0027】
(2)前記(1)によって、凝集汚泥、脱水汚泥は水に難溶性となり、微生物により汚泥は土壌に近似した性状に改質できる。
【0028】
(3)前記(1)によって、脱水汚泥の焼却処分の際に発生するダイオキシン類の有害ガスも脱水汚泥の含水率低下と、配合される無機成分の相乗効果により抑制され、焼却灰および飛灰中に残留する不安定な重金属類も化学的に安定固化・固定させることができる。
【0029】
(4)請求項2ないし7も前記(1)〜(3)と同様な効果が得られる。
【図面の簡単な説明】
【図1】本発明の第1の実施の形態の主成分の説明図。
【図2】本発明の第1の実施の形態の説明図。
【図3】本発明の第2の実施の形態の主成分の説明図。
【図4】本発明の第2の実施の形態の説明図。
【図5】無機系汚泥改質凝集浄化剤による下水処理場の一次処理水の浄化試験結果を示す図。
【図6】無機系汚泥改質凝集浄化剤による下水処理場の濃縮汚泥の脱水試験結果を示す図。
【図7】無機系汚泥改質凝集浄化剤によるし尿処理場の脱離液の浄化試験結果を示す図。
【図8】無機系汚泥改質凝集浄化剤による畜産(豚)し尿の前処理試験結果を示す図。
【図9】無機系汚泥改質凝集浄化剤による製紙工場排水の水質浄化試験結果を示す図。
【図10】無機系汚泥改質凝集浄化剤による鉱山排水の浄化と重金属類の固定試験結果を示す図。
【符号の説明】
1、1A:無機系汚泥改質凝集浄化剤、
2:土壌菌、 3:珪藻土、
4:活性炭、 5:セメント、
6:有機系凝集剤、 7:主成分、
8:チオ硫酸ナトリウム、9:酸化鉄、
10:硫酸カルシウム、 11:硫酸アルミニウム、
12:アルカリ金属炭酸塩。
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a sludge agglomeration separation and purification agent for inorganic polluted wastewater and organic polluted wastewater, and simultaneously adsorbs polluted substances and suspended suspended substances due to metals (including heavy metals) dissolved in the polluted wastewater, or While sorbing and aggregating and separating, the properties of the agglomerated sludge can be improved and separated as a very stable solid without re-elution of metals (including heavy metals). That is, while purifying the polluted wastewater to an excellent water quality, it is possible to separate the pollutant as a highly stable and agglomerated sludge rich in hydrophobicity, and the dehydrated sludge is dissolved again in water and does not collapse, The present invention relates to a novel inorganic sludge reforming and coagulating purification agent of a polluted wastewater purification treatment agent having a function of reforming to a mud that approximates natural soil over time.
[0002]
[Prior art]
In the treatment of inorganic and organic polluted wastewater, conventionally, an inorganic or organic flocculant is added to agglomerate and separate suspended suspended solids in the polluted wastewater, and the treated water is adjusted to meet the prescribed water quality standards ( For example, pH adjustment, decolorization, etc.) are discharged, and the separated sludge is dehydrated and, if necessary, insolubilized with heavy metals and discarded.
[0003]
In either inorganic or organic flocculants used for the treatment of polluted wastewater, the main purpose is to efficiently agglomerate suspended solids in the polluted wastewater.
Therefore, although some of the metals (including heavy metals) dissolved in the polluted wastewater are separated in a state of being taken up by the suspended suspended solids, they are positive for the conventional flocculant itself. Since it does not have the function of fixing metals (including heavy metals), elution is unavoidable when it is dumped. That is, another method is required for the non-eluting treatment of metals (including heavy metals).
[0004]
Furthermore, the water content is high in both cases of coagulated and separated sludge by inorganic or organic coagulant used for the treatment of contaminated wastewater, and sludge after dehydration.
Further, it is generally easy to redissolve in water, and if discarded, it causes a large amount of soil contamination and causes new environmental pollution.
[0005]
Sludge that has been coagulated and separated with inorganic or organic flocculants used in polluted wastewater treatment is dehydrated, but is incinerated for volume reduction.
Dioxins, which are considered extremely harmful in the exhaust gas generated during incineration, and unstable heavy metals remaining in the incineration ash and fly ash newly cause environmental pollution, and an urgent countermeasure method is required. It has been.
[0006]
[Problems to be solved by the invention]
It is an object of the present invention to provide a novel powdery sludge reforming flocculation separation / purification agent that can solve various problems as described above in the treatment of conventional inorganic and organic polluted wastewater.
Specifically, even if the polluted wastewater (whether inorganic or organic) is acidic or alkaline (in the range of hydrogen ion concentration PH4 to 9), the pollutant (including dissolved substances) can be collected very quickly. Clean and neutral separation water is obtained by physical and chemical flocculation, and the sludge that has been flocculated and separated is reformed to a very stable substance, rich in dehydration, and metals (heavy metals) Are stable chemically and biologically, and a stable, hardly soluble sludge can be obtained. Further, the coagulated sludge and the dehydrated sludge become insoluble in water, and the sludge is modified to a property approximate to the soil by microorganisms.
In addition, harmful gases of dioxins generated during incineration of dewatered sludge are suppressed by the synergistic effect of the inorganic components mixed with the reduced moisture content of the dehydrated sludge, and unstable gases remaining in the incinerated ash and fly ash. Heavy metals are also solidified and fixed chemically.
[0007]
The above and other objects and novel features of the present invention will become more fully apparent when the following description is read in conjunction with the accompanying drawings.
However, the drawings are for explanation only and do not limit the technical scope of the present invention.
[0008]
[Means for Solving the Problems]
In order to achieve the above object, the present invention is based on diatomaceous earth mixed with soil fungi, 10 to 30 parts by weight of activated carbon, 20 to 50 parts by weight of cement, and 100 parts by weight of a main component containing 2 to 5 parts by weight of organic flocculant. 10 to 20 parts by weight of sodium thiosulfate, 10 to 20 parts by weight of iron oxide, 30 to 60 parts by weight of calcium sulfate, 20 to 50 parts by weight of aluminum sulfate, and 10 to 20 parts by weight of alkali metal carbonate with respect to parts Thus, an inorganic sludge modifying flocculant is constituted.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
Hereinafter, the present invention will be described in detail with reference to embodiments shown in the drawings.
[0010]
In the first embodiment of the present invention shown in FIGS. 1 and 2, reference numeral 1 denotes an inorganic sludge reforming and coagulating purification agent for treating inorganic polluted wastewater and organic polluted wastewater. Agent 1 is composed of 10 to 30 parts by weight of activated carbon 4, 20 to 50 parts by weight of cement 5, and 2 to 5 parts by weight of organic flocculant 6 for diatomaceous earth 3 in which soil fungus 2 is blended. 10 to 20 parts by weight of sodium thiosulfate 8, 10 to 20 parts by weight of iron oxide 9, and 30 to 60 parts by weight of calcium sulfate so that the total weight is 20 to 30 parts by weight with respect to 100 parts by weight. Parts, 20 to 50 parts by weight of aluminum sulfate 11 and 10 to 20 parts by weight of alkali metal carbonate 12 are uniformly mixed.
[0011]
As the diatomaceous earth 3, one kind or a mixture of two kinds of freshwater diatomaceous earth or marine diatomaceous earth is selected. Diatomaceous earth 3 has an excellent function as a filter medium and the adsorption of fats and oils, and these natural minerals contain various mineral trace elements (mineral components).
This trace element elutes in the polluted waste water over time, reacts synergistically with dissolved oxygen and dissociated acid ions in the polluted waste water, and reduces or oxidizes and separates organic pollutants (including dissolved substances). It has the function of separating and purifying as a hydrophobic coagulum.
In addition, these natural minerals exhibit their functions effectively in the range of the hydrogen ion concentration PH4 to 9 (acidic region, neutral region, alkaline region) of the polluted wastewater.
[0012]
As the soil fungus 2, Bacillus subtilis Bacillus, Pseudomonas fungus Pseudomonas, and their modified fungi were selected. These are representative soil fungi, and they have the ability to decompose oils and fats, decompose pollutants (including inorganic compounds, organic compounds, etc.), make them soil, and make them harmless over the long term. . It also contributes to a reduction in the quality of treated water.
[0013]
The activated carbon 4 and the cement 5 and the organic flocculant 6 are not particularly limited. The activated carbon 4 is a fine powder of 100 mesh or less, and its purpose is to remove organic substances, odors, colors, etc. using its adsorption ability.
The cement is selected from Portland cement (ordinary, early strength, very early strength, moderate heat, sulfate-resistant), blast furnace cement, fly ash cement, and alumina cement. The purpose is to add functions such as adsorption of harmful substances and aggregation and solidification by hydration reaction.
As for the organic flocculant 6, 1.2 wt% of the suspended suspended solids in the polluted wastewater is normally used as a standard amount. However, the inorganic sludge-modified flocculant purifying agent 1 of the present invention is substantially organic flocculant. The amount of the agent is about one-tenth that of the organic flocculant used alone, and the same effect can be obtained. There is an advantage that can reduce the amount of organic flocculant.
In addition, the inorganic sludge reforming and coagulating purification agent 1 of the present invention is added to the polluted wastewater as a powder, and the former reaction, that is, the decomposition of the pollutant and the sludge reforming function are given priority, and the latter reaction, that is, the aggregation and solidification reaction A time difference is set in.
The blended organic coagulant 6 gradually dissolves during the previous reaction, coagulates and separates the modified sludge and solidifies.
[0014]
The sodium thiosulfate 8 reacts positively with heavy metals to form an insoluble metal thiosulfate compound. The mixing ratio of sodium thiosulfate 8 can be adjusted according to the value of heavy metals in the pollutant.
[0015]
The iron oxide 9 (specifically Vegara) has the purpose of providing a synergistic effect as a catalyst in each reaction such as aggregation and reforming of pollutants.
[0016]
The calcium sulfate 10 is dispersed and suspended in the polluted waste water, and a part thereof is dissolved. It functions as a neutralizer for the free acid produced by the dissociation of aluminum sulfate 11 described later, and at the same time contributes as an agglomeration and solidification reaction aid.
[0017]
The aluminum sulfate 11 is easily dissolved in the contaminated waste water, hydrolyzed and dissociated into aluminum sulfate 11 and sulfuric acid.
Aluminum oxide is further converted to polycondensed aluminum hydroxide consisting of colloidal aluminum hydroxide and ionized aluminum hydroxide.
This polycondensed aluminum hydroxide lowers the potential between the particles of the suspended suspension in the polluted waste water. Therefore, the balance between the particles of the pollutant is broken down into fine particles, and these fine particles are newly agglomerated by performing functions such as mineralization of organic metals, ion adsorption of metals (including heavy metals), and fixation. And separate.
[0018]
The alkali metal carbonate 12 is also easily dissolved in the polluted waste water and contributes to neutralization of free acid and agglomeration reaction.
Examples of the alkali metal carbonate 12 include sodium carbonate, calcium carbonate, magnesium carbonate, and dolomite.
[0019]
The inorganic sludge modified flocculating and purifying agent 1 having the above-described structure comprises a natural mineral (powder) impregnated with microorganisms (soil fungi), an inorganic compound (both powders), and a small amount of an organic flocculating agent (powder). It is characterized by being blended and configured in a predetermined ratio.
[0020]
The conditions for use of the inorganic sludge modified agglomerated purification agent 1 having the above-described configuration are as follows:
(1) A predetermined amount is added as a powder.
(2) Strong mixing is desirable to make mixing agitation after addition and designed reaction (decomposition, sludge modification, fixation, aggregation, separation, etc.) more effective.
(3) The standard addition amount is 5 wt% t of the pollutant in the polluted waste water.
[0021]
The agglomeration reaction of the inorganic sludge reforming aggregating and purifying agent 1 having the above-described configuration is extremely fast, and the agglomerated sludge is further solidified and separated by stirring.
Aggregated and separated sludge is a hydrophobic and extremely stable sludge and does not collapse or re-dissolve.
In addition, the dewatering property of the coagulated and separated sludge is high, the odor of the dewatered sludge is reduced, the sludge is modified to a sludge that is close to natural soil, the elution of metals (including heavy metals) does not occur, and the residual organic matter in the sludge is spoiled Etc. are also suppressed by soil fungi and become naturally humus over time.
[0022]
Different Embodiments of the Invention
Next, different embodiments of the present invention shown in FIGS. 3 and 4 will be described. In the description of the different embodiments of the present invention, the same components as those in the first embodiment of the present invention are denoted by the same reference numerals, and redundant description is omitted.
[0023]
The second embodiment of the present invention shown in FIGS. 3 and 4 is mainly different from the first embodiment of the present invention in that sodium thiosulfate 8 is added to 100 parts by weight of the main component 7. 10-20 parts by weight, 10-20 parts by weight of iron oxide 9, 30-60 parts by weight of calcium sulfate 10, 10-50 parts by weight of aluminum sulfate 11, and 10-20 parts by weight of alkali metal carbonate 12 In addition, at least three or more types may be uniformly blended, and thus the inorganic sludge modified aggregating and purifying agent 1A configured as described above may be used.
[0024]
[Experimental example]
(1) Adjustment of inorganic sludge modifying flocculation and purification agent / adjustment of main components: Diatomite 3 is selected from Radiolite # 800, and the culture solution of soil fungus 2 is pre-watered and impregnated therein, and then dried. .
The mixing ratio is 10 parts by weight of activated carbon 4 (100 mesh or less), 20 parts by weight of ordinary Portland cement, and 3 parts by weight of polymer flocculant (+) with respect to 100 parts by weight of diatomaceous earth 3 and these are mixed uniformly. .
Adjustment of essential components: The blending ratio is 10 to 20 parts by weight of sodium thiosulfate 8 with respect to 100 parts by weight of the main component 7, 10 parts by weight of iron oxide 9, 35 parts by weight of calcium sulfate 10, and aluminum sulfate 11 Was 40 parts by weight and calcium carbonate 12 was 15 parts by weight.
Predetermined amounts were respectively taken and mixed so as to be uniform to prepare the inorganic sludge reforming flocculating and purifying agent of the present invention.
(2) As an object, data based on inorganic or organic flocculants generally used at present is adopted.
1. The result of the purification test of the primary treated water of the sewage treatment plant is shown in FIG. 5, and the result of the dewatering test of the concentrated sludge is shown in FIG.
2. The result of the purification test of the effluent from the human waste treatment plant is shown in FIG.
3. The result of pretreatment of livestock (pig) manure is shown in FIG.
4). Industrial wastewater: Fig. 9 shows the results of a water purification test for wastewater from a paper mill.
5. Mine drainage: The results of the drainage and sludge heavy metal fixation treatment are shown in FIG.
[0025]
【The invention's effect】
As is clear from the above description, the present invention has the following effects.
[0026]
(1) 10 to 30 parts by weight of activated carbon, 20 to 50 parts by weight of cement and 2 to 5 parts by weight of organic flocculant for 100 parts by weight of sodium thiosulfate ~ 20 parts by weight, iron oxide 10-20 parts by weight, calcium sulfate 30-60 parts by weight, aluminum sulfate 20-50 parts by weight, alkali metal carbonate 10-20 parts by weight, so inorganic pollution Even if wastewater or organic polluted wastewater is acidic or alkaline (hydrogen ion concentration range of PH4-9), pollutants (including dissolved substances) are aggregated and separated very quickly and cleanly. Sexual separation water is obtained.
In addition, the coagulated and separated sludge is reformed to a very stable substance and is highly dehydrated. Furthermore, metals (including heavy metals) are fixed chemically and biologically, and are stable and hardly soluble. Sludge is obtained.
[0027]
(2) According to the above (1), the coagulated sludge and the dewatered sludge become hardly soluble in water, and the sludge can be modified to a property approximate to the soil by microorganisms.
[0028]
(3) By the above (1), the harmful gas of dioxins generated during the incineration of dewatered sludge is also suppressed by the reduced moisture content of the dehydrated sludge and the synergistic effect of the blended inorganic components. Unstable heavy metals remaining inside can also be chemically solidified and fixed.
[0029]
(4) Claims 2 to 7 can provide the same effects as the above (1) to (3).
[Brief description of the drawings]
FIG. 1 is an explanatory diagram of main components of a first embodiment of the present invention.
FIG. 2 is an explanatory diagram of the first embodiment of the present invention.
FIG. 3 is an explanatory diagram of main components of a second embodiment of the present invention.
FIG. 4 is an explanatory diagram of a second embodiment of the present invention.
FIG. 5 is a diagram showing a purification test result of primary treated water in a sewage treatment plant using an inorganic sludge modified flocculating and purifying agent.
FIG. 6 is a graph showing the results of a dewatering test of concentrated sludge in a sewage treatment plant using an inorganic sludge modifying agglomerated purification agent.
FIG. 7 is a view showing the purification test result of the effluent from the excreta treatment plant using the inorganic sludge modified agglomerated purification agent.
FIG. 8 is a view showing the results of a pretreatment test of livestock (pig) manure with an inorganic sludge-modified flocculant cleaner.
FIG. 9 is a view showing the results of a water purification test of paper mill effluent using an inorganic sludge-modified coagulant cleaner.
FIG. 10 is a diagram showing the result of a mine drainage purification and heavy metal fixation test using an inorganic sludge reforming coagulation purification agent.
[Explanation of symbols]
1, 1A: Inorganic sludge reforming agglomeration purification agent,
2: soil fungus, 3: diatomaceous earth,
4: Activated carbon, 5: Cement,
6: Organic flocculant, 7: Main component,
8: Sodium thiosulfate, 9: Iron oxide,
10: calcium sulfate, 11: aluminum sulfate,
12: Alkali metal carbonate.

Claims (7)

土壌菌を配合した珪藻土に対して活性炭10〜30重量部、セメント20〜50重量部、有機系凝集剤2〜5重量部を配合した主成分100重量部に対し、チオ硫酸ナトリウム10〜20重量部、酸化鉄10〜20重量部、硫酸カルシウム30〜60重量部、硫酸アルミニウム20〜50重量部、アルカリ金属炭酸塩10〜20重量部が均一に配合されていることを特徴とする無機系汚泥改質凝集浄化剤。  10 to 20 parts by weight of sodium thiosulfate with respect to 100 parts by weight of the main component containing 10 to 30 parts by weight of activated carbon, 20 to 50 parts by weight of cement, and 2 to 5 parts by weight of organic flocculant to diatomaceous earth with soil fungus Part, iron oxide 10-20 parts by weight, calcium sulfate 30-60 parts by weight, aluminum sulfate 20-50 parts by weight, alkali metal carbonate 10-20 parts by weight, inorganic sludge Modified flocculating and purifying agent. 珪藻土は淡水成珪藻土、海水成珪藻土のいずれか一方あるいは両方が使用されていることを特徴とする請求項1に記載の無機系汚泥改質凝集浄化剤。  The inorganic sludge-modified coagulant cleaner according to claim 1, wherein the diatomaceous earth is either freshwater diatomaceous earth or marine diatomaceous earth or both. 活性炭は100メッシュ以下の微細な粉末であることを特徴とする請求項1、2いずれかに記載の無機系汚泥改質凝集浄化剤。  Activated carbon is a fine powder of 100 mesh or less, The inorganic type sludge reforming coagulation purification agent according to any one of claims 1 and 2. セメントは各種のポルトランドセメント、高炉セメント、フライアッシュセメント、アルミナセメントのいずれか一方あるいはこれらを複数種配合したものであることを特徴とする請求項1、2、3いずれかに記載の無機系汚泥改質凝集浄化剤。  The inorganic sludge according to any one of claims 1, 2, and 3, wherein the cement is any one of various Portland cements, blast furnace cements, fly ash cements, alumina cements, or a mixture thereof. Modified flocculating and purifying agent. 土壌菌が枯草菌類、バチルス(Bacillus bacteria)と、シュウドモナス菌類(Pseudomonas)と、これらの変成菌類のいずれかであることを特徴とする請求項1、2、3、4いずれかに記載の無機系汚泥改質凝集浄化剤。  The inorganic system according to any one of claims 1, 2, 3, and 4, wherein the soil fungi are Bacillus subtilis, Bacillus (Bacillus bacteria), Pseudomonas (Pseudomonas), and any of these modified fungi. Sludge reforming coagulation purification agent. 主成分100重量部に対し、チオ硫酸ナトリウム、酸化鉄、硫酸カルシウム、硫酸アルミニウム、アルカリ金属炭酸塩の総重量が20〜30重量部の配分比であることを特徴とする請求項1ないし5いずれかに記載の無機系汚泥改質凝集浄化剤。  The total weight of sodium thiosulfate, iron oxide, calcium sulfate, aluminum sulfate, and alkali metal carbonate is a distribution ratio of 20 to 30 parts by weight with respect to 100 parts by weight of the main component. An inorganic sludge modifying agglomerated purification agent according to claim 1. アルカリ金属炭酸塩は炭酸ナトリウム、炭酸カルシウム、炭酸マグネシウム、ドロマイドの群から選ばれる少なくとも1種であることを特徴とする請求項1ないし6いずれかに記載の無機系汚泥改質凝集浄化剤。  The inorganic sludge reforming and coagulating purification agent according to any one of claims 1 to 6, wherein the alkali metal carbonate is at least one selected from the group consisting of sodium carbonate, calcium carbonate, magnesium carbonate and dolomide.
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