JP2007069195A - Hydrophobizing/solid-liquid separating agent for treating filthy water - Google Patents

Hydrophobizing/solid-liquid separating agent for treating filthy water Download PDF

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JP2007069195A
JP2007069195A JP2005294163A JP2005294163A JP2007069195A JP 2007069195 A JP2007069195 A JP 2007069195A JP 2005294163 A JP2005294163 A JP 2005294163A JP 2005294163 A JP2005294163 A JP 2005294163A JP 2007069195 A JP2007069195 A JP 2007069195A
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water
solid
gypsum
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sludge
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Iwao Yoshikawa
巌 好川
Kazuishi Satou
一石 佐藤
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Abstract

<P>PROBLEM TO BE SOLVED: To provide a hydrophobilizing/solid-liquid separating agent which is a combination of powder of waste gypsum being industrial waste, an ionic dehydrating agent and powdery aluminum sulfate and is used for separating a solid and water from filthy water. <P>SOLUTION: The hydrophobilizing/solid-liquid separating agent for treating filthy water is obtained by uniformly mixing gypsum or powder of a gypsum board of 100 parts weight, the ionic dehydrating agent of 0.1-2 parts weight and powdery aluminum sulfate of 0.1-3 parts weight. The obtained hydrophobilizing/solid-liquid separating agent is powder and can easily hydrophobilize, flocculate, dehydrate and separate filthy water into the solid and water. <P>COPYRIGHT: (C)2007,JPO&INPIT

Description

本発明は、ダム工事などの現場で発生する建設泥土、湖沼、河川、港湾、ダム、海底などの浚渫汚泥、うどん店、ラーメン店などで発生する有機汚泥、屠殺場・食肉加工発生汚泥などに代表される産業排水・生活排水中に含まれる有機汚泥、さらには海で発生するプランクトンなどと水分とを分離させる疎水化固液分離剤に関するものである。      The present invention is applicable to construction mud generated on the site such as dam construction, lake sludge, rivers, harbors, dams, seabed sludge, organic sludge generated in udon stores, ramen stores, sludge generated in slaughterhouses and meat processing, etc. The present invention relates to a hydrophobized solid-liquid separation agent that separates moisture from organic sludge contained in representative industrial wastewater and domestic wastewater, as well as plankton generated in the sea.

従来、下水などの排水処理、浚渫汚泥処理には、例えばSS、COD、BODなどの汚濁物質除去のために、一般的に凝集沈殿処理法が利用されている。凝集沈殿処理に使用される凝集剤は、水などに溶解して使用する高分子凝集剤、硫酸アルミニウムまたは塩化アルミニウムまたは塩化第2鉄などで構成される溶液系凝集剤と無機凝集剤や有機凝集剤を併用して粉体のまま利用する固体系凝集剤とに分けられてある。      Conventionally, in wastewater treatment such as sewage and soot sludge treatment, for example, a coagulation sedimentation treatment method is generally used to remove contaminants such as SS, COD, and BOD. The coagulant used in the coagulation / precipitation treatment is a polymer coagulant dissolved in water or the like, a solution type coagulant composed of aluminum sulfate, aluminum chloride or ferric chloride, an inorganic coagulant or an organic coagulant. It is divided into solid flocculants that are used as powders in combination with the agent.

これら凝集剤を水処理に利用しようとする場合、
(イ)得られた脱水ケーキの含水率は、80〜90%程度と高い数値であり、脱水ケーキの流動性も高く、性状が不安定で経時的に含水率が増加し、再汚泥化しやすく、埋立、投棄等の最終処分が極めて困難であり、汚泥の処理費用が高騰する。
(ロ)汚泥を採取した浚渫現場などにおいて脱水処理をする場合、汚泥の沈降速度が遅いため、処理日数がかかり、腐敗・悪臭により生活環境を保全できない。
(ハ)得られた汚泥の沈降速度が遅いため、高精度の清浄化水処理に使用する逆浸透膜保護を目的とする前水処理には適さない。
(ニ)凝集剤は、荷電性を持った無機金属塩であり、イオン価の異なる物質を、複数配合するため、高価になる。
などの問題点があった。
本発明は、これらの問題点を解決するためになされたものである。
When trying to use these flocculants for water treatment,
(B) The moisture content of the obtained dehydrated cake is a high value of about 80 to 90%, the fluidity of the dehydrated cake is also high, the properties are unstable, the moisture content increases with time, and it is easy to re-sludge. In addition, final disposal such as landfill and dumping is extremely difficult, and the treatment cost of sludge increases.
(B) When dewatering is performed at a dredging site where sludge is collected, the sedimentation rate of sludge is slow, so it takes many days to process and the living environment cannot be preserved due to spoilage and odor.
(C) Since the sedimentation rate of the obtained sludge is slow, it is not suitable for pre-water treatment for the purpose of protecting the reverse osmosis membrane used for high-precision purified water treatment.
(D) The flocculant is an inorganic metal salt having a charge property, and is expensive because it contains a plurality of substances having different ionic valences.
There were problems such as.
The present invention has been made to solve these problems.

本発明者らは、上記課題を解決するため各種水処理凝集剤について研究を重ね、石こうに少量のイオン性脱水剤と硫酸アルミニウムを均一に混合分散し、配合された固液分離剤が従来の汚濁水処理に必要であったポリ塩化アルミニウムや硫酸バンド等による前処理、苛性ソーダなどによるpH調整処理、高分子凝集剤などによる凝集処理、沈殿処理などの多くの工程を簡略化あるいは省略でき、かつ他の水処理凝集剤あるいは石こうと少量のイオン性脱水剤のみからなる固液分離剤と同等あるいはそれ以上の凝集沈殿効果を示すこと、脱水性能に優れること、優れた汚濁水の清浄効果を示すことを見出し、本発明を完成するに至った。すなはち、本発明は、In order to solve the above-mentioned problems, the present inventors have repeatedly studied various water treatment flocculants, and uniformly mixed and dispersed a small amount of an ionic dehydrating agent and aluminum sulfate in gypsum. Many processes such as pre-treatment with polyaluminum chloride or sulfuric acid band, etc., pH adjustment treatment with caustic soda, etc., coagulation treatment with polymer flocculant, precipitation treatment, etc. required for the treatment of contaminated water can be simplified or omitted, and It exhibits a coagulation-precipitation effect equal to or higher than that of other water treatment flocculants or solid-liquid separation agents consisting only of gypsum and a small amount of ionic dehydrating agent, excellent dewatering performance, and excellent cleaning effect of contaminated water. As a result, the present invention has been completed. In other words, the present invention

100重量部の石こうと0.1〜2重量部のイオン性脱水剤および0.1〜3重量部の粉末硫酸アルミニウムを均一に混合し、配合された汚濁水処理用疎水化固液分離剤、100 parts by weight of gypsum, 0.1 to 2 parts by weight of an ionic dehydrating agent and 0.1 to 3 parts by weight of powdered aluminum sulfate are uniformly mixed, and a hydrophobized solid-liquid separation agent for treating contaminated water,

石こうが石こうボードに代表される産業廃棄物である廃石こうを粉砕した粉末であることを特徴とするGypsum is a powder obtained by pulverizing waste gypsum which is industrial waste represented by gypsum board

記載の汚濁水処理用疎水化固液分離剤、The hydrophobized solid-liquid separation agent for treating contaminated water as described,

イオン性脱水剤がカチオン性、アニオン性、ノニオン性あるいは両性脱水剤より選択した一種類以上を含むものであることを特徴とするThe ionic dehydrating agent includes at least one selected from cationic, anionic, nonionic or amphoteric dehydrating agents.

記載の汚濁水処理用疎水化固液分離剤である。It is the hydrophobization solid-liquid separation agent for dirty water treatment of description.

以下、本発明を詳細に説明する。本発明では、上記      Hereinafter, the present invention will be described in detail. In the present invention, the above

で示される石こうに均一に混合し、配合されたイオン性脱水剤と粉末硫酸アルミニウムを用いる。本発明においてはこのイオン性脱水剤と粉末硫酸アルミニウムを含有することが、粉末状態で処理水中に投入し、水中での凝集フロックの沈降速度を速めるために必須である。An ionic dehydrating agent and powdered aluminum sulfate mixed uniformly with gypsum shown in FIG. In the present invention, it is essential to contain the ionic dehydrating agent and powdered aluminum sulfate in order to increase the sedimentation rate of the aggregated floc in the water in the powder state.

次に、本発明の固液分離剤に用いる石こうについて説明する。石こうは、2水石こう、天然石こう、排煙脱硫石こう、りん酸石こう、廃棄石こう型材、石こうボード廃材、あるいは、これらを加熱処理して得られる焼石こう、半水石こう、水硬性せっこう、およびこれらの混合物などが挙げられるがこれらに限定されるものではない。特に廃石こうは、環境負荷を軽減し、廃棄物を有効利用という観点から、その利用が好まれる。石こうの形態は水との接触面積を高め、汚泥中への分散効率を高めるために微粉末状であることが好ましい。      Next, the gypsum used for the solid-liquid separating agent of the present invention will be described. Gypsum is dihydrated gypsum, natural gypsum, flue gas desulfurized gypsum, phosphate gypsum, waste gypsum mold material, gypsum board waste, or calcined gypsum, hemihydrate gypsum, hydraulic gypsum obtained by heat treatment, and Examples thereof include, but are not limited to, mixtures thereof. In particular, waste gypsum is preferred from the viewpoint of reducing the environmental burden and effectively using waste. The form of gypsum is preferably in the form of fine powder in order to increase the contact area with water and increase the efficiency of dispersion in sludge.

イオン性脱水剤は、市販のカチオン性、アニオン性、ノニオン性、両性脱水剤が挙げられる。アニオン性とノニオン性脱水剤では、主成分系がアクリル酸系、ポリアクリルアミド系、アクリル酸・ポリアクリルアミド系やポリアクリル酸ソーダ系が、カチオン性では、ポリアクリル酸エステル系、アクリル酸ジメチルアミノ系、メタクリル酸ジメチルアミノエチル系、アクリル酸ジメチルアミノエチル系、ポリアミジン系やエポキシアミン系が、両性では、アクリル酸ジメチルアミノエチル、アクリル酸、アクリルアミド、メタクリル酸の少なくとも1種類以上の混合系が挙げられるが、これらに限定されるものではない。なお、環境負荷を軽減し、かつ、少ない投入量で各種汚泥の凝集効果を高めるために、強カチオン性、強アニオン性脱水剤の使用が好ましい。イオン性脱水剤の形態は、石こうの形態と同様、水との接触面積を高め、汚泥中への分散効率を高めるために粉末状であることが好ましい。      Examples of the ionic dehydrating agent include commercially available cationic, anionic, nonionic and amphoteric dehydrating agents. In anionic and nonionic dehydrating agents, the main components are acrylic acid-based, polyacrylamide-based, acrylic acid / polyacrylamide-based, and polyacrylic acid soda-based, and cationic ones are polyacrylate ester-based, dimethylamino acrylate-based Dimethylaminoethyl methacrylate, dimethylaminoethyl acrylate, polyamidine and epoxyamine are amphoteric, and in amphoteric, at least one mixed system of dimethylaminoethyl acrylate, acrylic acid, acrylamide and methacrylic acid can be mentioned. However, it is not limited to these. In order to reduce the environmental load and increase the coagulation effect of various sludges with a small input amount, it is preferable to use a strong cationic or strong anionic dehydrating agent. The form of the ionic dehydrating agent is preferably in the form of a powder in order to increase the contact area with water and increase the efficiency of dispersion in sludge, similar to the form of gypsum.

本発明の汚濁水処理用疎水化固液分離剤中の      In the hydrophobized solid-liquid separation agent for treating contaminated water of the present invention

で示されるイオン性脱水剤の含有量は水あるいは各種汚泥中に含まれるイオン種、イオン成分量などが異なるため、その配合量が異なり、一概に限定されないが、石こう100重量部に対して、0.5重量部を基準とする。各種汚泥の凝集沈殿に効果が見られるためには、石こう100重量部に対するイオン性脱水剤の配合量は0.1〜2重量部であり、好ましくは0.1〜1重量部、さらに好ましくは0.1〜0.5重量部である。粉末硫酸アルミニウムの配合量は0.1〜3重量部であり、好ましくは0.1〜2重量部、さらに好ましくは0.1〜1重量部である。疎水化固液分離剤中のイオン性脱水剤の含有量が2重量部以上であると、処理水の透明度を阻害することになり、好ましくない。また、0.1重量部未満であると、固液分離性能や汚濁物質の除去性が低下し、好ましくない。また、疎水化固液分離剤中の粉末硫酸アルミニウムの含有量が、1重量部以上であると水のpHが低下し、0.1重量部未満であると、固液分離性能や汚濁物質の除去性が低下し、好ましくない。The content of the ionic dehydrating agent represented by is different in the amount of ionic species, ionic components, etc. contained in water or various sludges, so the blending amount is different and is not generally limited, but for 100 parts by weight of gypsum, Based on 0.5 parts by weight. In order to have an effect on the coagulation and precipitation of various sludges, the amount of the ionic dehydrating agent based on 100 parts by weight of gypsum is 0.1 to 2 parts by weight, preferably 0.1 to 1 part by weight, more preferably 0.1 to 0.5 part by weight. The compounding quantity of powder aluminum sulfate is 0.1-3 weight part, Preferably it is 0.1-2 weight part, More preferably, it is 0.1-1 weight part. When the content of the ionic dehydrating agent in the hydrophobized solid / liquid separating agent is 2 parts by weight or more, the transparency of the treated water is inhibited, which is not preferable. On the other hand, if it is less than 0.1 parts by weight, the solid-liquid separation performance and the removability of pollutants are deteriorated. Further, when the content of powdered aluminum sulfate in the hydrophobized solid-liquid separation agent is 1 part by weight or more, the pH of water is lowered, and when it is less than 0.1 part by weight, the solid-liquid separation performance and contaminants Removability is lowered, which is not preferable.

次に、本発明の汚泥水処理方法について説明する。ビーカー内に例えば、含水率400重量%の汚泥濁水を投入し、攪拌する。攪拌が維持された汚泥濁水中へ粉末状の疎水化固液分離剤 配合成分:石こう、カチオン性脱水剤、粉末硫酸アルミニウム を一気に添加する。添加終了後から約30〜40秒で粒状汚泥形成、固液分離過程は終了し、液体である水の清浄化が始まり、経時的に水は清浄化され、透明度が高くなる。疎水化固液分離剤添加時の汚泥濁水攪拌速度を上げると、フロックがより大きくなり、より高い凝集効果が得られる。疎水化固液分離剤は均一混合分散されたものを使用した時のみ、絶大な汚泥除去効果が見られ、各成分を単独で使用あるいは適当な間隔で順次添加しても汚泥除去効果・水の清浄化に大きな効果は見られない。汚泥濁水と疎水化固液分離剤の混合に際しては、予め汚泥濁水を加温するか、あるいは沸騰水のような高温水を使用するなど処理水の温度を上げると、固液分離は促進される。      Next, the sludge water treatment method of the present invention will be described. For example, sludge suspended water having a water content of 400% by weight is put into a beaker and stirred. Add powdery hydrophobized solid-liquid separation agent to the sludge suspended water with stirring. Ingredients: Gypsum, cationic dehydrating agent, powdered aluminum sulfate. After about 30 to 40 seconds from the end of the addition, the formation of granular sludge and the solid-liquid separation process are completed, and the purification of water, which is a liquid, starts, and the water is cleaned with time and the transparency is increased. Increasing the sludge turbid water stirring speed at the time of adding the hydrophobized solid-liquid separating agent increases the flocs and provides a higher coagulation effect. Only when the hydrophobized solid-liquid separation agent is uniformly mixed and dispersed, a great sludge removal effect can be seen. Even if each component is used alone or added sequentially at appropriate intervals, the sludge removal effect There is no significant effect on cleaning. When mixing sludge turbid water and hydrophobized solid-liquid separation agent, solid-liquid separation is promoted by increasing the temperature of the treated water by preheating the sludge turbid water or using high-temperature water such as boiling water. .

本発明の疎水化固液分離剤は、これのみで疎水性、凝集性、脱水性があり、自重による水中脱水性を持つ。このため、脱水ケーキの流動性が低く、性状安定で経時的に含水率が下がり、再度水と混じることはないため、汚泥の処理費用の高騰を解消することができる。また、この点に加え、汚泥凝集除去速度が速く、かつ、汚泥凝集除去のために必要な攪拌駆動力が水流が利用できる点などから、汚泥濁水の処理規模が大きい河川、湖沼、港湾、海底などの現場における浚渫汚泥処理用途で特に利用価値が高い。汚泥濁水処理量に対する疎水化固液分離剤の添加量は汚泥の濃度により異なるが、含水率400%で重量比は疎水化固液分離剤/汚泥濁水=1/5000を基準とする。      The hydrophobized solid-liquid separating agent of the present invention alone is hydrophobic, cohesive, and dewatering, and has water dewatering properties due to its own weight. For this reason, since the fluidity | liquidity of a dewatering cake is low, a property is stable, a moisture content falls with time, and it does not mix with water again, Therefore The increase in the processing cost of sludge can be eliminated. In addition to this point, sludge flocculation removal speed is fast, and the agitation driving force necessary for sludge flocculation removal can be used for water flow. This is especially useful for the treatment of sludge in the field. The amount of the hydrophobized solid / liquid separating agent added to the sludge suspended water treatment amount varies depending on the sludge concentration, but the water content is 400% and the weight ratio is based on the hydrophobized solid / liquid separating agent / sludge muddy water = 1/5000.

汚泥濁水より得られたケーキは、流水による濁水の発生が抑えられるため、水の清浄化が効率的に行われる。また、疎水化作用が極めて高いため、他の凝集剤使用後ケーキと比較し、ケーキの含水率が低く、脱水速度も速い。堤防、土地造成などの埋め立て用素材、植生土壌やコンクリート用骨材として使用することが可能であり、再利用することが出来る。また、汚泥ケーキが除かれた水の性状は水質汚濁防止法の排水基準に適合する。      Since the cake obtained from sludge turbid water can suppress generation | occurrence | production of the turbid water by running water, water purification is performed efficiently. Moreover, since the hydrophobizing action is extremely high, the moisture content of the cake is low and the dehydration rate is fast compared to the cake after using other flocculants. It can be used as reclamation materials, land reclamation materials, vegetation soil and concrete aggregates, and can be reused. The properties of the water from which the sludge cake has been removed meet the drainage standards of the Water Pollution Control Law.

本発明の疎水化固液分離剤は、その高い固液分離性能を生かし、ダム工事などの現場で発生する建設泥土、湖沼、河川、港湾、ダム、海底などの浚渫汚泥、うどん店、ラーメン店などで発生する有機汚泥、屠殺場・食肉加工発生汚泥に代表される産業排水・生活排水中に含まれる有機汚泥、高精度の水処理に使用する逆浸透膜の保護のための前処理剤、さらには海で発生するプランクトンなどと水分との分離などに使用することができる。      The hydrophobized solid-liquid separation agent of the present invention makes use of its high solid-liquid separation performance, construction mud generated on the site such as dam construction, lakes, rivers, harbors, dams, submarine sludge, udon shop, ramen shop Organic sludge generated by slaughterhouse, meat sludge generated in industrial wastewater and domestic wastewater represented by meat processing, pretreatment agent for protection of reverse osmosis membrane used for high-precision water treatment, Furthermore, it can be used to separate water from plankton generated in the sea.

また、本発明の疎水化固液分離剤は、その優れた凝集沈殿性能、脱水性能、水質清浄性能を活かして、重金属などによる汚染土壌の改良、農地排水処理、淡水・海水養殖場の水質浄化、生コンクリート車の洗浄廃水処理、コンクリート工場末端廃水処理、製鉄会社・製紙会社の廃水処理、塗装・メッキ処理工場の廃水処理、食品工場の廃水処理、下水・し尿・浄化槽の汚泥処理などに使用することができる。      In addition, the hydrophobized solid-liquid separation agent of the present invention makes use of its excellent coagulation and sedimentation performance, dewatering performance, and water purification performance to improve contaminated soil with heavy metals, farmland wastewater treatment, and water purification of freshwater and seawater farms. Used for cleaning wastewater from raw concrete vehicles, wastewater treatment at the end of concrete factories, wastewater treatment at steel and paper companies, wastewater treatment at painting and plating plants, wastewater treatment at food factories, sludge treatment of sewage, human waste, and septic tanks can do.

本発明により、環境負荷を軽減するために産業廃棄物を有効利用することと同時に少量使用で効力を発揮する浚渫汚泥、産業排水・生活排水、さらには海で発生するプランクトンなどに適用できるクリーンな環境保全に貢献する汚泥沈降性能・脱水性能・汚濁水の清浄作用に優れた汚濁水処理用疎水化固液分離剤を提供する。      In accordance with the present invention, in order to reduce the environmental load, industrial waste can be used effectively, and at the same time, it can be applied to dredged sludge, industrial wastewater, domestic wastewater, and plankton generated at sea. We provide a hydrophobized solid-liquid separation agent for the treatment of polluted water that excels in sludge sedimentation performance, dewatering performance, and polluted water purification that contribute to environmental conservation.

以下、本発明について、実施例を用いて発明の効果をさらに具体的に説明するが、本発明はこれらの実施例に限定されるものではない。      Hereinafter, the effects of the present invention will be described more specifically with reference to examples. However, the present invention is not limited to these examples.

産業廃棄物である石こうボードより、石こう部のみを取り出し、これを卓上強力粉砕機FDSで5分間粉砕し、石こう粉末を得た。この粉末石こうをワーリングブレンダーMMB142のカップ内に100g入れた後、市販品である粉末イオン性脱水剤 ポリアクリル酸エステル系高分子凝集剤 を0.2gを添加し、60秒間の均一分散操作を行い、粉末汚濁水処理用疎水化固液分離剤1を作製した。Only the gypsum part was taken out from the gypsum board as industrial waste, and this was pulverized for 5 minutes with a tabletop powerful crusher FDS to obtain gypsum powder. After putting 100 g of this powder gypsum into the cup of Waring blender MMB142, 0.2 g of powder ionic dehydrating agent polyacrylate ester polymer flocculant which is a commercial product is added, and a uniform dispersion operation is performed for 60 seconds. Then, a hydrophobized solid-liquid separating agent 1 for treating powder polluted water was prepared.

同様に、産業廃棄物である石こうボードより、石こう部のみを取り出し、これを卓上強力粉砕機FDSで5分間粉砕して得られた粉末石こうをワーリングブレンダーMMB142のカップ内に100g入れた後、市販品である粉末イオン性脱水剤 ポリアクリル酸エステル系高分子凝集剤 を0.2gを添加し、さらに市販品である粉末硫酸アルミニウム(日本軽金属(株)製 固型1号)を0.1g添加した後、60秒間の均一分散操作を行い、粉末汚濁水処理用疎水化固液分離剤2を作製した。    Similarly, only the gypsum part is taken out from the gypsum board, which is industrial waste, and 100 g of powder gypsum obtained by crushing it with a tabletop powerful crusher FDS for 5 minutes is put into a cup of the Waring blender MMB142, and then commercially available. 0.2 g of powdered ionic dehydrating agent polyacrylic acid ester polymer flocculant and 0.1 g of commercially available powdered aluminum sulfate (solid type No. 1 manufactured by Nippon Light Metal Co., Ltd.) were added. Thereafter, a uniform dispersion operation for 60 seconds was performed to prepare a hydrophobized solid-liquid separation agent 2 for treating powder polluted water.

次に香川県さぬき市の沼より採取したアオコが発生した沼水を1000g計量し、2つの2Lビーカ内へそれぞれ投入した。ビーカー内のアオコが発生した沼水の攪拌を攪拌機を用いて開始し、攪拌羽の回転数が80rpmで安定した後、それぞれのビーカ内へ0.4gの粉末汚濁水処理用疎水化固液分離剤1および粉末汚濁水処理用疎水化固液分離剤2を一気に投入後、30秒間攪拌を継続した後、攪拌を停止した。撹拌停止からフロックが完全に静止し、沈降終了するまでの時間とフロックが沈降開始してから終了するまでに見られる浮遊フロックの大きさを目視により観察した。結果を表1に示す。表1より、粉末汚濁水処理用疎水化固液分離剤2は従来の粉末汚濁水処理用疎水化固液分離剤1よりも良好な凝集沈殿性能を示した。

Figure 2007069195
*粉末汚濁水処理用疎水性固液分離剤1を使用した場合に見られる浮遊フロックの大きさを小と定義し、これと比較して大きい場合を大と定義した。Next, 1000 g of the swamp water generated from the marsh in Sanuki City, Kagawa Prefecture was weighed and put into two 2 L beakers. Stirring of swamp water in which beaks are generated in a beaker is started using a stirrer, and the number of rotations of the stirring blade is stabilized at 80 rpm. After the agent 1 and the hydrophobized solid / liquid separating agent 2 for treating powder polluted water were added all at once, stirring was continued for 30 seconds, and then stirring was stopped. The time from when the stirring was stopped until the floc completely stopped and the sedimentation was completed, and the size of the floating floc that was observed from the start of the floc to the completion of the sedimentation were visually observed. The results are shown in Table 1. From Table 1, the hydrophobized solid / liquid separating agent 2 for powdered polluted water treatment showed better coagulation precipitation performance than the conventional hydrophobized solid / liquid separating agent 1 for treating powdered polluted water.
Figure 2007069195
* The size of the floating floc seen when using the hydrophobic solid-liquid separation agent 1 for treating powder polluted water was defined as small, and the case where it was larger than this was defined as large.

実施例1で得られた粉末汚濁水処理用疎水化固液分離剤2を用い、汚濁水の沈降試験を下記の手順に従い行った。    Using the hydrophobized solid-liquid separation agent 2 for treating powdery polluted water obtained in Example 1, the sedimentation test of polluted water was performed according to the following procedure.

4mm目のふるいを用い通過させた乾燥土壌100gとMillipore社製MilliQA10で作製した純水1000mlを3Lビーカに加えて、回転数10rpmで10分間連続して、撹拌機で撹拌したものを3つ準備した。その後、3つのビーカ共に撹拌を維持したまま、1つ目は粉末汚濁水処理用固液分離剤2を汚濁水重量に対し1%一気に添加、2つ目は粉末汚濁水処理用固液分離剤2を汚濁水重量に対し0.2%一気に添加、3つ目は無添加を同時に行った後、全3サンプルともに撹拌維持の状態のまま、さらに30秒程度撹拌した後、静置時間の経過に伴う土壌の沈降状態を調べた。      100 g of dry soil passed through a 4 mm sieve and 1000 ml of pure water produced by MilliQA10 manufactured by Millipore were added to a 3 L beaker, and three things were continuously stirred with a stirrer at 10 rpm for 10 minutes. did. Then, while maintaining the stirring of the three beakers, the first added the solid-liquid separating agent 2 for treating the powdered polluted water at a rate of 1% with respect to the weight of the polluted water. The second was the solid-liquid separating agent for treating the polluted water. 2 was added 0.2% at a time with respect to the weight of the contaminated water, and after the third, no addition was performed at the same time, all the three samples were stirred and maintained for about 30 seconds, and the standing time elapsed. The sedimentation state of the soil was investigated.

その結果、粉末汚濁水処理用固液分離剤2の添加量が0.2%、1.0%、共に添加直後から土壌粒子の沈降が見られ、30秒後にはビーカー反対側がはっきりと見える状態になった。一方、粉末汚濁水処理用固液分離剤2無添加のサンプル水はビーカーの底に粒子の大きな土壌は沈降しているが、小さな粒子状物は浮遊したままであり、30分経過後も、濁り状態はほとんど変化がなかった。    As a result, the amount of addition of the solid / liquid separating agent 2 for treating powder polluted water was 0.2% and 1.0%, and in both cases, sedimentation of the soil particles was observed immediately after the addition, and the opposite side of the beaker was clearly visible after 30 seconds. Became. On the other hand, in the sample water without addition of the solid-liquid separating agent 2 for treating powder polluted water, the soil with large particles settles at the bottom of the beaker, but the small particulate matter remains floating, and after 30 minutes, The cloudiness was almost unchanged.

実施例2における実験で扱った水に関して、粉末汚濁水処理用固液分離剤2の添加直後および、静置後30分のサンプルの上澄み液を採取し、排水基準項目であるBOD,COD,SS,大腸菌群、ノルマルヘキサン抽出物質(油分)およびその他として一般細菌、濁度の分析を行った。結果を表2に示す。表2より、BOD,COD,SS、濁度は、粉末汚濁水処理用固液分離剤2を投入してから、直後、30分経過後共に、極めて低い値を示し、水の清浄化が格段に進んでいることが分かった。

Figure 2007069195
Regarding the water handled in the experiment in Example 2, the supernatant of the sample was collected immediately after the addition of the solid / liquid separating agent 2 for treatment of powder polluted water and after standing for 30 minutes, and BOD, COD, SS as drainage standard items. , Escherichia coli, normal hexane extract (oil) and other general bacteria, turbidity was analyzed. The results are shown in Table 2. From Table 2, BOD, COD, SS, and turbidity are extremely low immediately after 30 minutes have elapsed since the solid-liquid separating agent 2 for treating powder polluted water was added, and water purification was marked. It turns out that it has advanced to.
Figure 2007069195

Claims (3)

100重量部の石こうと0.1〜2重量部のイオン性脱水剤および0.1〜3重量部の粉末硫酸アルミニウムを均一に混合し、配合された汚濁水処理用疎水化固液分離剤。A hydrophobized solid-liquid separation agent for treating contaminated water, in which 100 parts by weight of gypsum, 0.1 to 2 parts by weight of an ionic dehydrating agent and 0.1 to 3 parts by weight of powdered aluminum sulfate are uniformly mixed. 石こうが石こうボードに代表される産業廃棄物である廃石こうを粉砕した粉末であることを特徴とする請求項1記載の汚濁水処理用疎水化固液分離剤。2. The hydrophobized solid-liquid separating agent for treating polluted water according to claim 1, wherein the gypsum is a powder obtained by pulverizing waste gypsum which is industrial waste represented by gypsum board. イオン性脱水剤がカチオン性、アニオン性、ノニオン性あるいは両性脱水剤より選択した一種類以上を含むものであることを特徴とする請求項1、2記載の汚濁水処理用疎水化固液分離剤。The hydrophobized solid-liquid separation agent for treating contaminated water according to claim 1, wherein the ionic dehydrating agent contains one or more selected from cationic, anionic, nonionic or amphoteric dehydrating agents.
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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009121123A1 (en) * 2008-04-01 2009-10-08 Ultimate Nominees Pty Ltd Non-toxic liquids for water treatment

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2009121123A1 (en) * 2008-04-01 2009-10-08 Ultimate Nominees Pty Ltd Non-toxic liquids for water treatment

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