JP2003225513A - Flocculant for treating washing wastewater of food - Google Patents

Flocculant for treating washing wastewater of food

Info

Publication number
JP2003225513A
JP2003225513A JP2002025588A JP2002025588A JP2003225513A JP 2003225513 A JP2003225513 A JP 2003225513A JP 2002025588 A JP2002025588 A JP 2002025588A JP 2002025588 A JP2002025588 A JP 2002025588A JP 2003225513 A JP2003225513 A JP 2003225513A
Authority
JP
Japan
Prior art keywords
component
wastewater
aggregating agent
rice
water
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.)
Pending
Application number
JP2002025588A
Other languages
Japanese (ja)
Inventor
Kenji Suzuki
健司 鈴木
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.)
ICHIKAWA RAISU BUSINESS KK
Onex Corp USA
Original Assignee
ICHIKAWA RAISU BUSINESS KK
Onex Corp USA
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 ICHIKAWA RAISU BUSINESS KK, Onex Corp USA filed Critical ICHIKAWA RAISU BUSINESS KK
Priority to JP2002025588A priority Critical patent/JP2003225513A/en
Publication of JP2003225513A publication Critical patent/JP2003225513A/en
Pending legal-status Critical Current

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  • Separation Of Suspended Particles By Flocculating Agents (AREA)
  • Water Treatment By Sorption (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

<P>PROBLEM TO BE SOLVED: To provide a cleaning means for food washing wastewater high in safety capable of preventing water pollution, low in equipment cost and running cost, capable of reducing the amount of industrial waste and capable of converting the industrial waste to valuable matter. <P>SOLUTION: This flocculant for treating food washing wastewater is used for the cleaning means and contains an ion exchanging/adsorbing component (a), a coagulation component (b), and a sedimentation assisting component (c), but substantially contains no chlorine component. Artificial zeolite is compounded as the ion exchanging/adsorbing component. <P>COPYRIGHT: (C)2003,JPO

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、水質汚濁を防止
し、設備及びランニングコストが安価で、産業廃棄物を
減量化できるとともに、有価物に転換可能な、安全性が
高い食品の洗浄廃水処理用凝集剤に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to cleaning wastewater treatment of foods, which prevents water pollution, has low equipment and running costs, can reduce industrial waste, and can be converted into valuable materials, with high safety. The present invention relates to a flocculant for use.

【0002】[0002]

【従来の技術及び発明が解決しようとする課題】近年、
お米の研ぎ汁(洗米廃水)について環境を悪化させるこ
とが指摘されている。特に、最近では無洗米が工業化さ
れたことに伴い、多量の研ぎ汁が排出されることにな
り、この研ぎ汁から出るヌカには、BOD物質(有機
物)、窒素、りん等が含まれるため、水質汚濁の原因と
なっている。このヌカの量は、全国で約40万トンにも
上っている。下水道や合併浄化槽が整備されていない所
での川や海に研ぎ汁を放流すると、水質汚染や下水処理
設備の処理能力不足による弊害が懸念される。
2. Description of the Related Art In recent years,
It has been pointed out that the sharpening soup of rice (washing wastewater) will worsen the environment. In particular, with the recent industrialization of unwashed rice, a large amount of sharpening juice will be discharged, and the rice bran from this sharpening juice contains BOD substances (organic substances), nitrogen, phosphorus, etc. Causes water pollution. The amount of this nuka is about 400,000 tons nationwide. Discharging sharpening juice into rivers or seas where sewers or combined septic tanks are not maintained may cause harmful effects due to water pollution or insufficient treatment capacity of sewage treatment facilities.

【0003】現在、洗米廃水の処理には、活性汚泥法等
による大規模な設備を必要としているため、その設備は
高く、ランニングコストも高い。また、洗米廃水を処理
する際にできるヌカ等の凝集物は、産業廃棄物として廃
棄されている。これらのことは、お米の研ぎ汁に限られ
ず、水質汚濁の原因となる物質を含む、食品一般の洗浄
廃水についても同様にいえることである。
At present, a large-scale facility such as an activated sludge method is required for the treatment of rice rinsing wastewater, so that the facility is expensive and the running cost is high. In addition, agglomerates such as nuka, which are formed when treating the waste water for washing rice, are discarded as industrial waste. The same applies to washing wastewater for general foods, which includes substances that cause water pollution, not limited to rice polishing juice.

【0004】このため、お米の研ぎ汁等、広くは食品の
洗浄廃水に適用できる優れた浄化手段の開発、更には、
産業廃棄物の低減化が期待されることから、食品の洗浄
廃水から出る凝集物等を、生物や自然環境に害のない安
全性の高い有価物へ転換することが望まれていた。
For this reason, the development of an excellent purification means which can be widely applied to the washing wastewater of foods such as rice polishing juice, and further,
Since it is expected that industrial waste will be reduced, it has been desired to convert agglomerates and the like generated from washing wastewater of foods into highly valuable resources that are not harmful to living organisms and the natural environment.

【0005】一方、一般工業用廃水の処理では、大規模
な設備で、凝集剤を廃水中に添加して凝集物を形成し、
これを分離除去して水を浄化することが行なわれてい
る。そこで、このような凝集剤を食品の洗浄廃水に小規
模化した形で適用することも考えらる。しかし、一般工
業用廃水処理用の凝集剤には、通常、無機系凝集剤原料
として広く使用されているポリ塩化アルミニウム(PA
C)やポリ塩化鉄、塩化カルシウム等の、生物に対して
有害な塩素分が使用されている。
On the other hand, in the treatment of general industrial wastewater, a coagulant is added to the wastewater to form a coagulum by a large-scale facility.
This is separated and removed to purify water. Therefore, it may be possible to apply such a coagulant to food washing wastewater in a reduced scale. However, polyaluminum chloride (PA), which is widely used as a raw material for inorganic flocculants, is generally used as a flocculant for treating general industrial wastewater.
C), polyiron chloride, calcium chloride, and other chlorine content harmful to living organisms are used.

【0006】また、このような凝集剤により形成される
凝集物も通常塩素分を含むため、かかる凝集剤を使用し
て食品の洗浄廃水を安全性の高い有価物に転換すること
は不可能である。特に、塩素分を含む凝集物を植物生育
土壌に適用した場合には土壌を悪化させるため、かかる
凝集剤を使用して食品の洗浄廃水を肥料等の土壌用有価
物に転換することはできない。尚、一般工業用廃水処理
用の凝集剤から形成される凝集物も、産業廃棄物として
処理されている。
Further, since the agglomerates formed by such a flocculant usually also contain chlorine, it is impossible to use such flocculants to convert the washing wastewater of foods into valuable substances with high safety. is there. In particular, when a flocculant containing chlorine is applied to a plant-growing soil, it deteriorates the soil, and therefore it is not possible to use such flocculant to convert food washing wastewater into a valuable resource for soil such as fertilizer. It should be noted that aggregates formed from aggregating agents for treating general industrial wastewater are also treated as industrial wastes.

【0007】従って、本発明は、水質汚濁を防止し、設
備及びランニングコストが安価で、産業廃棄物を減量化
できるとともに、有価物に転換可能な、安全性が高い食
品洗浄廃水の浄化手段を提供することを課題とする。
Therefore, the present invention provides a highly safe means for purifying food washing wastewater which prevents water pollution, has low equipment and running costs, can reduce industrial waste, and can be converted into valuable materials. The challenge is to provide.

【0008】[0008]

【課題を解決するための手段】本発明者は、鋭意研究し
た結果、特定成分として人工ゼオライトを配合してなり
且つ特定の有害物質を実質的に含まない凝集剤を使用す
ることにより、前記課題を解決し得ることの知見を得
た。
Means for Solving the Problems As a result of earnest studies, the present inventor has achieved the above-mentioned problems by using an aggregating agent which contains an artificial zeolite as a specific component and which does not substantially contain a specific harmful substance. We have obtained the knowledge that

【0009】本発明は、前記知見に基づきなされたもの
で、(a)イオン交換/吸着成分、(b)凝結成分、及
び(c)助沈成分を少なくとも含む凝集剤であって、前
記(a)イオン交換/吸着成分として人工ゼオライトを
配合してなり、且つ塩素分を実質的に含まない、食品の
洗浄廃水処理用凝集剤を提供するものである。
The present invention has been made on the basis of the above-mentioned findings, and is a flocculant containing at least (a) an ion exchange / adsorption component, (b) a coagulation component, and (c) a coprecipitation component. The present invention provides an aggregating agent for treating food waste water, which comprises artificial zeolite as an ion-exchange / adsorption component and contains substantially no chlorine.

【0010】[0010]

【発明の実施の形態】以下、本発明をその好ましい実施
形態に基づいて詳細に説明する。本発明の凝集剤は、食
品の洗浄廃水処理に適用するものであり、その配合成分
の一つである(a)イオン交換/吸着成分として人工ゼ
オライトを配合してなり、且つ塩素分を実質的に含まな
いものである。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described in detail below based on its preferred embodiments. The coagulant of the present invention is applied to the treatment of food wastewater, and is one of the components (a) which is an artificial zeolite as an ion exchange / adsorption component, and has a substantial chlorine content. It is not included in.

【0011】本発明の凝集剤は、上記のように、人工ゼ
オライト〔(a)成分〕を配合してなるものであるた
め、そのイオン交換機能及び吸着機能の発現により、食
品を洗浄した際に発生する廃水に対する凝集作用を促進
しつつ凝集物を形成し、その凝集物の形成の際に発生す
る悪臭成分を吸着することができる。これにより、本発
明の凝集剤は、食品洗浄廃水の有価物への転換を促進で
き、得られる凝集物を悪臭成分のない有価物にして有効
に利用することが可能となる。特に、得られる凝集物を
土壌用有価物としての肥料にして使用する場合には、土
壌に散布された肥料の養分(有効成分)を吸着し、雨水
等によってその養分が流れるのを抑制することができ
る。
Since the flocculant of the present invention is prepared by mixing the artificial zeolite [component (a)] as described above, when the food is washed due to its ion exchange function and adsorption function. It is possible to form an aggregate while promoting the aggregation action on the generated wastewater, and to adsorb a malodorous component generated when the aggregate is formed. As a result, the flocculant of the present invention can promote the conversion of food washing wastewater into valuable substances, and the obtained flocculates can be effectively used by converting them into valuable substances free of malodorous components. Especially when the obtained aggregate is used as a fertilizer as a valuable resource for soil, it absorbs the nutrients (active ingredients) of the fertilizer sprinkled on the soil and suppresses the nutrient flow by rainwater etc. You can

【0012】また、本発明の凝集剤は、上記のように、
塩素分を実質的に含まないものであるため、生物や土壌
等の自然環境に対して安全性が高いものである。これに
より、本発明の凝集剤は、得られる凝集物を有価物とし
て有効に利用することが可能となる。尚、「実質的に含
まない」とは、生物や自然環境に対する影響を無視でき
る程度の量(微量)のものまで含まない趣旨ではないと
いう意味である。
The aggregating agent of the present invention, as described above,
Since it does not substantially contain chlorine, it is highly safe for the natural environment such as living things and soil. As a result, the flocculant of the present invention can effectively use the obtained flocculate as a valuable resource. In addition, "substantially free" does not mean that it does not include an amount (trace amount) such that the effect on living things and the natural environment can be ignored.

【0013】本発明の凝集剤は、このように、安全性が
高く、また凝集物を有価物にして回収できるため、問題
となっていた川や海等への廃水放流による水質汚濁を防
止し、産業廃棄物を減量化でき、しかも、廃水処理に大
規模な設備が必要でないため、設備及びランニングコス
トが安価なものである。
As described above, the flocculant of the present invention is highly safe and can collect flocculates as valuables, so that it is possible to prevent water pollution due to discharge of wastewater into rivers and the sea. In addition, the amount of industrial waste can be reduced, and since large-scale equipment is not required for wastewater treatment, equipment and running costs are low.

【0014】本発明に用いられる(a)成分の人工ゼオ
ライトの配合量は、凝集作用及び吸着作用の向上の点か
ら、凝集剤中に、好ましくは10〜40重量%、更に好
ましくは15〜40重量%である。
The blending amount of the artificial zeolite of the component (a) used in the present invention is preferably 10 to 40% by weight, more preferably 15 to 40% by weight in the aggregating agent from the viewpoint of improving the aggregating action and the adsorbing action. % By weight.

【0015】また、人工ゼオライトは、Ca型、Mg
型、Fe型等の人工ゼオライトであることが、生物や自
然環境に対する安全性に優れる点で好ましい。特に、本
発明の凝集剤により得られる凝集物を肥料等の土壌用有
価物として利用する場合には、有価物が土壌での植物育
成に対する安全性に優れたものとなる点でも、これらの
型の人工ゼオライトは好適である。
The artificial zeolites are Ca type and Mg type.
It is preferable to use artificial zeolites of the type, Fe type, etc. because of their excellent safety against living things and natural environments. In particular, when the aggregate obtained by the aggregating agent of the present invention is used as a valuable resource for soil such as fertilizer, these types are also advantageous in that the valuable material is excellent in safety for plant growth in soil. Artificial zeolites are preferred.

【0016】これらの人工ゼオライトは、使用に際して
一種単独で又は二種以上を混合して用いることができ、
例えば、Ca型人工ゼオライト、Mg型人工ゼオライ
ト、Fe型人工ゼオライトをそれぞれ単独で用いてもよ
いし、Ca型とMg型の複合型人工ゼオライト、Ca型
とFe型の複合型人工ゼオライト、Ca型とMg型とF
e型の複合型人工ゼオライト等のように複合して用いて
もよい。このような人工ゼオライトの種類は、本発明の
凝集剤により転換しようとする有価物の用途に応じて適
宜選択される。例えば、本発明の凝集剤を土壌用有価物
にする場合には、土壌の状況に応じて適宜選択される。
These artificial zeolites can be used alone or in combination of two or more when used.
For example, Ca-type artificial zeolite, Mg-type artificial zeolite, and Fe-type artificial zeolite may be used alone, respectively, or Ca-type and Mg-type composite artificial zeolite, Ca-type and Fe-type composite artificial zeolite, and Ca-type artificial zeolite. And Mg type and F
It may be used in combination such as e-type composite artificial zeolite. The type of such artificial zeolite is appropriately selected according to the intended use of the valuable material to be converted by the coagulant of the present invention. For example, when the flocculant of the present invention is used as a valuable resource for soil, it is appropriately selected depending on the condition of the soil.

【0017】また、人工ゼオライトとしては、産業廃棄
物の減量化に更に寄与できる点で、石炭灰等の産業廃棄
物から転換したものを用いることが好ましい。具体的に
は、特開2000−1311号公報に開示されている人
工ゼオライトの製造方法によって得られる人工ゼオライ
ト等が挙げられる。
Further, as the artificial zeolite, it is preferable to use one obtained by converting industrial waste such as coal ash because it can further contribute to the reduction of the amount of industrial waste. Specific examples thereof include an artificial zeolite obtained by the method for producing an artificial zeolite disclosed in Japanese Patent Laid-Open No. 2000-1311.

【0018】本発明に用いられる(b)成分の凝結成分
としては、例えば、水溶性アルミニウム塩および/また
は高分子有機化合物が挙げられる。特に、凝結作用によ
り凝集物の形成を促進できる点で、水溶性アルミニウム
塩および高分子有機化合物の両方を用いることが好まし
い。
Examples of the coagulating component of the component (b) used in the present invention include water-soluble aluminum salts and / or polymer organic compounds. In particular, it is preferable to use both a water-soluble aluminum salt and a high molecular weight organic compound, because the formation of aggregates can be promoted by the coagulation action.

【0019】水溶性アルミニウム塩の含有量は、凝結作
用向上の点で、凝集剤中に、好ましくは20〜40重量
%であり、更に好ましくは23〜38重量%である。
The content of the water-soluble aluminum salt in the coagulant is preferably 20 to 40% by weight, more preferably 23 to 38% by weight, from the viewpoint of improving the coagulation action.

【0020】水溶性アルミニウム塩としては、例えば、
硫酸アルミニウム、アルミン酸ソーダ等が好適に挙げら
れる。
As the water-soluble aluminum salt, for example,
Preferable examples include aluminum sulfate and sodium aluminate.

【0021】また、高分子有機化合物の含有量は、凝結
作用向上の点で、好ましくは1〜5重量%、更に好まし
くは1〜4重量%である。
Further, the content of the high molecular weight organic compound is preferably 1 to 5% by weight, more preferably 1 to 4% by weight from the viewpoint of improving the coagulation action.

【0022】高分子有機化合物としては、例えば、ポリ
アクリル酸ソーダ、ポリアクリルアミド、ポリエチレン
アミン、デンプン、ゼラチン、アルギン酸ソーダ等が挙
げられ、特に、ポリアクリル酸ソーダ、ポリアクリルア
ミド、ポリエチレンアミンが好適である。
Examples of the high molecular weight organic compound include sodium polyacrylate, polyacrylamide, polyethyleneamine, starch, gelatin, sodium alginate and the like, and sodium polyacrylate, polyacrylamide and polyethyleneamine are particularly preferable. .

【0023】本発明に用いられる(c)成分の助沈成分
としては、例えば、硫酸カルシウムおよび/または粘土
類が挙げられる。特に、助沈作用により凝集物の形成を
促進できる点で、硫酸カルシウムおよび粘土類の両方を
用いることが好ましい。
Examples of the coprecipitated component (c) used in the present invention include calcium sulfate and / or clays. In particular, it is preferable to use both calcium sulfate and clays in that the formation of aggregates can be promoted by the coprecipitation action.

【0024】硫酸カルシウムの含有量は、助沈作用向上
の点で、凝集剤中に、好ましくは10〜40重量%、更
に好ましくは10〜34重量%である。
The content of calcium sulfate in the coagulant is preferably 10 to 40% by weight, more preferably 10 to 34% by weight from the viewpoint of improving the coprecipitation effect.

【0025】一方、粘土類の含有量は、助沈作用向上の
点で、凝集剤中に、好ましくは5〜40重量%、更に好
ましく6〜33重量%はである。
On the other hand, the content of the clay is preferably 5 to 40% by weight, more preferably 6 to 33% by weight in the coagulant, from the viewpoint of improving the coprecipitation effect.

【0026】粘土類としては、例えば、カオリン、タル
ク、ベントナイト、酸性白土等が挙げられ、特に、カオ
リン、タルク、ベントナイトが好適である。
Examples of the clays include kaolin, talc, bentonite and acid clay, and kaolin, talc and bentonite are particularly preferable.

【0027】本発明の凝集剤には、塩素分を実質的に含
まない限り、前記(a)、(b)及び(c)成分以外に
も、必要に応じて活性二酸化ケイ素等の電荷中和剤等を
配合することができる。
As long as the coagulant of the present invention does not substantially contain a chlorine component, in addition to the components (a), (b) and (c) described above, charge neutralization of active silicon dioxide or the like may be carried out if necessary. Agents and the like can be added.

【0028】本発明の凝集剤は、例えば、前述した各成
分をそれぞれ粉末状にした各原料を用いて混合すること
等により調製することができる。
The flocculant of the present invention can be prepared, for example, by mixing the above-mentioned components in the form of powder and mixing them.

【0029】本発明の凝集剤の調製に際しては、凝集速
度を早くし、かつ凝集剤の食品洗浄廃水への添加量を極
力少なく抑えることができる点で、粉末状の各原料は全
て、出来るだけ粒度が小さい事が好ましく、その平均粒
径が100ミクロンメータ以下とされる。中でも、
(b)凝結成分の一つである高分子有機化合物の粒度
は、特に細かいことが好ましく、その平均粒径が約50
ミクロンメータに調整される。尚、平均粒径の調整は、
粉砕機等を用いて行なうことができる。
In the preparation of the flocculant of the present invention, all the powdery raw materials are used as much as possible in that the flocculation rate can be increased and the amount of the flocculant added to the food washing wastewater can be minimized. It is preferable that the particle size is small, and the average particle size is 100 μm or less. Above all,
(B) The particle size of the high molecular weight organic compound, which is one of the coagulation components, is particularly preferably small, and the average particle size is about 50.
Adjusted to micron meter. The average particle size can be adjusted by
It can be performed using a crusher or the like.

【0030】また、本発明の凝集剤の調製に際しては、
各原料が十分に乾燥状態にあることが好ましく、各原料
の含水率を10重量%以下とされる。吸湿すると凝集剤
として配合された原料間で化学反応を起こして変質する
おそれがあるからである。尚、含水率が高い原料でも、
凝集剤の調製前に、予め熱風等により乾燥して所望の含
水率に調整してから使用することができる。
When preparing the flocculant of the present invention,
It is preferable that each raw material is sufficiently dried, and the water content of each raw material is set to 10% by weight or less. This is because if moisture is absorbed, a chemical reaction may occur between the raw materials blended as the aggregating agent and the quality may change. In addition, even if the raw material has a high water content,
Before the coagulant is prepared, it can be used after being dried in advance with hot air or the like to have a desired water content.

【0031】さらに、本発明の凝集剤の調製に際して
は、各原料を均一に混合することが好ましく、例えば、
V型混合機等を用いて均一に混合することができる。混
合する際、各原料の比重差が大きい場合、均一な混合が
困難になる場合があるため、混合の方式と混合時間を適
宜に設定することが望まれる。尚、混合機としては、V
型混合機以外の方式の混合機を用いても良い。また、均
一な混合の確認は、一定条件下での凝集試験等により行
うことができる。
Further, when preparing the flocculant of the present invention, it is preferable to uniformly mix the respective raw materials, for example,
A V-type mixer or the like can be used for uniform mixing. When mixing, if the difference in specific gravity between the raw materials is large, uniform mixing may be difficult, so it is desirable to appropriately set the mixing method and mixing time. As a mixer, V
A mixer other than the mold mixer may be used. Further, confirmation of uniform mixing can be carried out by a coagulation test or the like under certain conditions.

【0032】本発明の凝集剤は、食品の洗浄廃水処理の
用途に使用するものであり、具体的には、米、大豆、海
草、もやし、ギャベツ等のカット野菜や、雑穀、コーヒ
ー豆、牡蛎等を洗浄する際に排出する廃水の処理に使用
できる。
The flocculant of the present invention is used for the treatment of food waste water, and specifically, cut vegetables such as rice, soybean, seaweed, sprouts, and gabets, millet, coffee beans, oysters. It can be used for the treatment of wastewater discharged when washing etc.

【0033】本発明の凝集剤は、特に、洗米廃水処理用
の凝集剤として、米を洗浄する際に排出する廃水(洗米
廃水、即ちお米の研ぎ汁)に対して適用することが、昨
今の無洗米の工業化に伴う環境悪化の改善に寄与すると
ともに、ヌカ等を含む凝集物の脱水・乾燥処理により、
窒素、りんを豊富に含む肥料等の有価物への転換が可能
となる点で好ましい。また、本発明の凝集剤は、主とし
て、無洗米製造業、弁当製造業、及び食堂やレストラン
等の飲食業、外食産業等に利用できるものである。
The coagulant of the present invention has recently been applied as a coagulant for treating waste water of washing rice to waste water discharged during washing of rice (rice washing waste water, that is, rice polishing juice). Contributes to the improvement of the environmental deterioration associated with the industrialization of non-washed rice, and by the dehydration / drying treatment of the agglomerates including nuka,
It is preferable in that it can be converted into valuable substances such as fertilizers rich in nitrogen and phosphorus. Moreover, the flocculant of the present invention can be mainly used in the non-washed rice manufacturing industry, the bento manufacturing industry, the eating and drinking business such as a cafeteria and a restaurant, and the restaurant business.

【0034】本発明の凝集剤によれば、その浄化作用に
より、食品の洗浄廃水中のSS、BOD物質、窒素、り
ん等の濃度を減少させて、透明な水にすることができ
る。
According to the coagulant of the present invention, due to its purifying action, it is possible to reduce the concentration of SS, BOD substances, nitrogen, phosphorus, etc. in the washing wastewater of foods to make it transparent water.

【0035】本発明の凝集剤によれば、前述したよう
に、それ自体が生物や土壌等の自然環境に対して安全性
が高いこと及び対象となる廃水がお米の研ぎ汁等の食品
の洗浄廃水であることが相俟って、生物や自然環境に害
のない安全性の高い有価物、例えば、肥料、堆肥の熟成
促進剤、水耕栽培用培養液添加剤等を得ることができ
る。中でも、本発明の凝集剤中に配合される人工ゼオラ
イトの保肥力や保水力を活用できる点で、肥料等の土壌
用有価物として特に有用である。
According to the coagulant of the present invention, as described above, the coagulant itself is highly safe against the natural environment such as organisms and soil, and the target wastewater is food such as sharpening juice of rice. Combined with the fact that it is a washing wastewater, it is possible to obtain highly safe valuable substances that are not harmful to living organisms and the natural environment, such as fertilizers, compost ripening accelerators, culture solution additives for hydroponic cultivation, etc. . Among them, it is particularly useful as a valuable resource for soil such as fertilizer because it can utilize the fertilizing ability and water retaining ability of the artificial zeolite blended in the flocculant of the present invention.

【0036】本発明の凝集剤は、これを食品の洗浄廃水
に添加することで凝集物を形成し、この凝集物を脱水及
び乾燥処理することで有価物を形成することができる。
この有価物の製造方法の具体的な一例は、下記の通りで
ある。
The aggregating agent of the present invention can be added to the washing wastewater of food to form an agglomerate, and can be dehydrated and dried to form a valuable product.
A specific example of the method for producing this valuable material is as follows.

【0037】即ち、本発明の凝集剤を、食品の洗浄廃水
100重量部に対して、好ましくは0.1〜0.4重量
部となる量で添加し、撹拌する。そして、凝集物が上澄
み水と分離して沈降するのを確認した後、上澄み水を捨
て、沈降した凝集物を取り出す。この凝集物を、布袋等
によって回収した後、凝集物の含水率が好ましくは30
〜40重量%となるように遠心分離装置等の所望の脱水
手段にて脱水する。次いで、脱水した凝集物を所望の形
態とし、さらに熱風乾燥炉中等で好ましくは100〜2
50℃の温度で乾燥し、有価物として形成する。
That is, the aggregating agent of the present invention is added in an amount of preferably 0.1 to 0.4 parts by weight to 100 parts by weight of food washing wastewater, and the mixture is stirred. Then, after confirming that the aggregate is separated from the supernatant water and settled, the supernatant water is discarded and the precipitated aggregate is taken out. After the aggregate is collected with a cloth bag or the like, the moisture content of the aggregate is preferably 30.
It is dehydrated by a desired dehydrating means such as a centrifuge so as to have a concentration of -40% by weight. Then, the dehydrated agglomerate is formed into a desired form, and further preferably 100 to 2 in a hot air drying oven or the like.
Dry at a temperature of 50 ° C. and form as a valuable.

【0038】特に、食品の洗浄廃水として洗米廃水を使
用する場合には、所望の含水率に脱水した凝集物に、米
糠を好ましくは25〜45重量%混合して混合粉体と
し、これをペッレト状等に造粒した後、乾燥させる。こ
の米糠は、上記洗米廃水とは別に、精米時に調製してお
いたものを用いることができる。また、米糠の含水率
は、10〜25重量%であることが好ましい。また、で
きるだけ澱粉質を減らして、土壌の養分となるりん分や
窒素分の割合を多くし、肥料等の土壌用有価物としての
効果を高めるために、脱水した凝集物と米糠からなる上
記混合粉体に、発酵酵素を添加し、2日間程度発酵処理
を行って肥料化することも更に好ましい。このようにし
て、所望のりん分、窒素分を有する有用な肥料等の土壌
用有価物を形成することができる。尚、この洗米廃水を
使用する場合における方法で特に詳述しない点について
は、上記の有価物の製造方法が適宜適用される。
In particular, when the rice washing wastewater is used as the food washing wastewater, the agglomerates dehydrated to a desired water content are mixed with rice bran, preferably in an amount of 25 to 45% by weight, to obtain a mixed powder, which is pelletized. After granulating into a shape or the like, it is dried. As this rice bran, one prepared at the time of rice polishing can be used separately from the above-mentioned waste water for washing rice. The water content of rice bran is preferably 10 to 25% by weight. In order to reduce the starch quality as much as possible and increase the proportion of phosphorus and nitrogen that are nutrients of the soil, and to enhance the effect as a valuable resource for soil such as fertilizer, the above mixture consisting of dehydrated aggregate and rice bran. It is further preferable to add a fermenting enzyme to the powder and perform a fermentation treatment for about 2 days to form a fertilizer. In this way, valuable resources for soil such as useful fertilizers having desired phosphorus content and nitrogen content can be formed. In addition, regarding the point which is not described in detail in the method in the case of using this waste water for washing rice, the above-mentioned method for producing a valuable resource is appropriately applied.

【0039】また、本発明の凝集剤を用いて、下記凝集
処理装置を使用することが、栄養素を十分に保持した性
質に優れた有価物、特に肥料が得られる点で好ましい。
即ち、凝集剤を出来るだけ最少の添加量に抑えること、
かつ凝集物が腐敗しないように凝集物の回収及びその乾
燥を出来るだけ早く行なうことが可能な構造の装置が好
ましい。具体的には、図1に示すように、凝集剤を細か
く散布し投入する凝集剤投入部1と、回転速度の調節が
可能でかつ回転方向が可逆可能である撹拌部2と、装置
底部に位置する凝集物回収部3と、装置上部に接続され
る廃水供給ラインaと、装置中部に接続される上澄み水
排出ラインbと、を備える凝集処理装置10が一例とし
て好適である。
It is preferable to use the flocculating agent of the present invention and use the flocculating treatment device described below, in order to obtain a valuable resource having sufficient nutrients and excellent properties, particularly a fertilizer.
That is, keep the coagulant to the smallest possible amount,
Moreover, an apparatus having a structure capable of collecting the aggregate and drying it as soon as possible so that the aggregate does not decompose is preferable. Specifically, as shown in FIG. 1, a coagulant feeding unit 1 for finely sprinkling and feeding a coagulant, a stirring unit 2 whose rotation speed can be adjusted and whose rotation direction is reversible, and an apparatus bottom portion. A coagulation treatment device 10 including the located agglomerate recovery part 3, a wastewater supply line a connected to the upper part of the device, and a supernatant water discharge line b connected to the middle part of the device is suitable as an example.

【0040】上記凝集処理装置10において、凝集剤投
入部1は、廃水供給ラインaから供給され蓄えられた食
品洗浄廃水中へ出来るだけ最少の添加量に抑えて凝集剤
を散布・投入できる。また、撹拌部2は、素早く凝集を
完了させることができる。また、凝集物回収部3は、凝
集物回収袋4等への凝集物の回収を容易にし、上澄み水
への凝集物の混入を回避することができる。尚、凝集後
の上澄み水は上澄み水排出ラインbから排出される。こ
の凝集処理装置10は、間欠的な、いわゆるバッチ式で
あるが、連続式になっていても良い。
In the aggregating apparatus 10, the aggregating agent feeding section 1 can spray and feed the aggregating agent into the food washing wastewater supplied from the wastewater supply line a and stored therein with the minimum addition amount. Further, the stirring unit 2 can quickly complete the aggregation. Further, the agglomerate collection unit 3 can facilitate the collection of the agglomerates in the agglomerate collection bag 4 and the like, and can avoid the inclusion of the agglomerates in the supernatant water. The supernatant water after coagulation is discharged from the supernatant water discharge line b. The aggregating apparatus 10 is of a so-called batch type, which is intermittent, but may be of a continuous type.

【0041】前述した製造方法や凝集処理装置を使用す
ることによって、特に有用な肥料等の有価物を得ること
が可能となる。
By using the above-described manufacturing method and aggregating treatment apparatus, it is possible to obtain a particularly useful valuable material such as fertilizer.

【0042】[0042]

【実施例】以下、実施例を挙げて本発明を更に具体的に
説明する。尚、本発明はこれらの実施例により何等限定
されるものではない。
EXAMPLES The present invention will be described in more detail below with reference to examples. The present invention is not limited to these examples.

【0043】〔実施例(1)〜(3)〕表1に示す組成
(%は重量%を示す)からなる各実施例の凝集剤を、後
述の調製法により調製した。尚、表1中の人工ゼオライ
トは、産業廃棄物である石炭灰を原料としてアルカリ水
溶液中で加熱処理することにより転換したものである。
そのプロセスの詳細は、次の通りである。即ち、1キロ
グラムの石炭灰と3規定の苛性ソーダ3リッターを内容
積10リッターのオートクレーブに入れ、130℃で3
時間保持した後、冷却、遠心分離機による脱水及び水洗
の各工程を経て、Na型の人工ゼオライト1キログラム
を得た。この後に、塩化カルシウム、塩化マグネシウ
ム、塩化鉄の水溶液中で処理することにより、それぞれ
Ca型、Mg型およびFe型の人工ゼオライトを得た。
[Examples (1) to (3)] The aggregating agent of each Example having the composition shown in Table 1 (% represents% by weight) was prepared by the preparation method described below. The artificial zeolites in Table 1 were converted by heat-treating coal ash, which is an industrial waste, as a raw material in an alkaline aqueous solution.
The details of the process are as follows. That is, 1 kilogram of coal ash and 3 liters of 3N caustic soda were put into an autoclave with an internal volume of 10 liters, and the mixture was heated at 130 ° C. for 3 hours.
After holding for a period of time, cooling, dehydration by a centrifuge, and washing with water were carried out to obtain 1 kg of Na-type artificial zeolite. Then, by treating in an aqueous solution of calcium chloride, magnesium chloride, and iron chloride, Ca-type, Mg-type, and Fe-type artificial zeolites were obtained, respectively.

【0044】〔凝集剤の調製法〕凝集剤の各原料は、平
均粒径が100ミクロンメータ以下の粉状物を用いた。
但し、高分子有機化合物のみ、平均粒径を約50ミクロ
ンメータに調整した粉状物を用いた。平均粒径は、必要
に応じ粉砕機を用いて調整した。また、各原料は、含水
率が10重量%以下のものを用いた。含水率は、必要に
応じて熱風乾燥により調整した。これらの原料をV型混
合機により均一に混合して、凝集剤(粉末状)を調製し
た。
[Preparation Method of Coagulant] As each raw material of the coagulant, a powder having an average particle diameter of 100 μm or less was used.
However, only the high molecular weight organic compound was used as a powdery substance having an average particle size adjusted to about 50 μm. The average particle size was adjusted using a pulverizer as needed. Further, as each raw material, one having a water content of 10% by weight or less was used. The water content was adjusted by hot air drying as needed. These raw materials were uniformly mixed with a V-type mixer to prepare an aggregating agent (powder).

【0045】〔洗米廃水の調製〕当実施例では、専用の
洗米装置を使用して洗米廃水を調製した。洗米装置は、
お米と水の撹拌槽、水の連続供給装置、洗米廃水のオー
バーフロー口、洗米廃水の受槽からなる構造である。ま
ず、お米(銘柄:秋田こまち)5キログラムを撹拌槽に
入れ、室温(約15℃)水を少しずつ撹拌槽内に入れな
がら撹拌を開始した。洗米廃水は撹拌槽内で一定量以上
になるとオーバーフローして、洗米廃水の受槽に溜めら
れた。洗米に要した水量は35リッターであった。この
間の洗米に要した時間は5分であった。洗米廃水は最後
に洗米廃水の受槽にて全て回収された。以上の方法で、
洗米廃液を調製した。尚、この洗米廃水(凝集処理前)
のSS及びBODそれぞれの濃度を予め調べたところ、
SS…1600mg/L、BOD…650mg/Lであ
った。
[Preparation of Rice Washing Wastewater] In this example, rice washing wastewater was prepared using a dedicated rice washing apparatus. Rice washing equipment
The structure consists of a stirring tank for rice and water, a continuous water supply device, an overflow port for waste water of washing rice, and a tank for receiving waste water of washing rice. First, 5 kg of rice (brand: Akita Komachi) was put in a stirring tank, and stirring was started while gradually adding room temperature (about 15 ° C.) water to the stirring tank. The waste water of rice washing overflowed when it exceeded a certain amount in the stirring tank and was stored in the receiving tank of the waste water of rice washing. The amount of water required for washing rice was 35 liters. The time required for washing rice during this period was 5 minutes. Finally, all the waste water of washing rice was collected in the receiving tank of the waste water of washing rice. With the above method,
A rice washing waste liquid was prepared. In addition, this rice washing wastewater (before coagulation treatment)
When the respective concentrations of SS and BOD of
SS ... 1600 mg / L, BOD ... 650 mg / L.

【0046】<凝集試験>得られた洗米廃液1L中に、
実施例(1)の凝集剤を2g添加した。また、実施例
(2)及び(3)の各凝集剤についても、実施例(1)
と同様に、それぞれ洗米廃液1L中に2g添加した。こ
のとき、凝集剤を添加してから廃液中の成分が凝集を開
始するときまでの時間を調べた。また、凝集終了後の上
澄水の透明度を目視により評価した。更に、凝集終了後
における上澄水中のSS及びBODそれぞれの濃度(m
g/L)を調べた。それらの結果を表1に示す。尚、凝
集開始時は、小さな凝集物(フロック)の生成開始のと
きをいうものとする。一方、凝集終了時は、廃液が上澄
み水と凝集物に分離完了のときをいうものとする。
<Agglomeration test> In 1 L of the obtained washing water of the rice,
2 g of the flocculant of Example (1) was added. Further, regarding each of the coagulants of Examples (2) and (3), Example (1)
In the same manner as above, 2 g was added to each 1 L of the washed rice liquor. At this time, the time from the addition of the aggregating agent to the start of aggregation of the components in the waste liquid was examined. Further, the transparency of the supernatant water after completion of aggregation was visually evaluated. Furthermore, the concentration of each of SS and BOD in the supernatant water after completion of aggregation (m
g / L). The results are shown in Table 1. Incidentally, the start of aggregation means the start of the formation of small aggregates (flocs). On the other hand, when the aggregation is completed, it means when the waste liquid is completely separated into the supernatant water and the aggregate.

【0047】[0047]

【表1】 [Table 1]

【0048】<有価物の形成>750グラムのお米を5
リットルの水で研ぎ、その洗米廃水に、本発明の凝集剤
(実施例(1)の凝集剤)を10グラム添加、撹拌して
約60秒後に凝集物が上澄み水と分離して沈降した。沈
降した凝集物は、凝集剤の成分とお米からの米糠と澱粉
質を含有している。上澄み水を捨て、沈降した凝集物を
取り出した後、やや目の粗い布袋の回収し、その後遠心
分離装置にて脱水した。この時点での凝集物の含水率は
約35%であった。次に、凝集物に精米時に得られた含
水率約15%の米糠を30〜40%混合した。次に、混
合粉体をペッレト状などに造粒し、さらに熱風乾燥炉中
で約150℃の温度で乾燥させて、ペレットを形成し
た。このペッレトは、分析の結果、りん分が1.5%、
窒素分が1.6%であることが分かり、有価物、特に肥
料としての性能を十分に持っていることが判明した。
<Formation of valuables> 5 pieces of 750 grams of rice
After polishing with 1 liter of water, 10 g of the flocculant of the present invention (flocculant of Example (1)) was added to the washed rice waste water, and after stirring for about 60 seconds, the flocculate separated from the supernatant water and settled. The sedimented agglomerate contains the components of the aggregating agent, rice bran from rice and starch. After discarding the supernatant water and taking out the sedimented aggregate, a slightly coarse cloth bag was collected and then dehydrated by a centrifugal separator. The water content of the aggregate at this point was about 35%. Next, 30 to 40% of rice bran having a water content of about 15% obtained during rice polishing was mixed with the agglomerate. Next, the mixed powder was granulated into pellets or the like and further dried in a hot air drying oven at a temperature of about 150 ° C. to form pellets. As a result of analysis, this pellet has a phosphorus content of 1.5%,
It was found that the nitrogen content was 1.6%, and it proved to have sufficient performance as a valuable resource, especially as a fertilizer.

【0049】[0049]

【発明の効果】本発明によれば、水質汚濁を防止し、設
備及びランニングコストが安価で、産業廃棄物を減量化
できるとともに、有価物に転換可能な、安全性が高い食
品の洗浄廃水処理用凝集剤を提供できる。
EFFECTS OF THE INVENTION According to the present invention, it is possible to prevent water pollution, reduce equipment and running costs, reduce industrial waste, and convert waste into valuable resources. A flocculant for use can be provided.

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

【図1】図1は、本発明の食品の洗浄廃水処理用凝集剤
によって有価物を形成するための凝集処理装置の一例を
示す概略図である。
FIG. 1 is a schematic view showing an example of an aggregating treatment apparatus for forming a valuable substance with the aggregating agent for treating food waste water of the present invention.

【符号の説明】[Explanation of symbols]

10…凝集処理装置,1…凝集剤投入部,2…撹拌部,
3…凝集物回収部,4…凝集物回収袋,a…廃水供給ラ
イン,b…上澄み水排出ライン
10 ... Aggregation processing device, 1 ... Coagulant injection part, 2 ... Stirring part,
3 ... Aggregate collection part, 4 ... Aggregate collection bag, a ... Waste water supply line, b ... Supernatant water discharge line

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.7 識別記号 FI テーマコート゛(参考) C02F 1/28 C02F 1/28 Z 1/52 1/52 C 1/56 1/56 C Fターム(参考) 4D015 BA04 BA05 BA11 BA17 BA19 BB08 BB12 CA04 DA02 DA05 DA08 DA25 DA32 DA35 DB01 DB03 DB12 DB24 DB33 DB35 DC04 EA06 EA32 4D024 AA04 AB00 BA07 BB01 BC04 CA01 CA06 DA10 DB12 DB21 4G066 AA62B BA09 CA02 DA08─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 7 Identification code FI theme code (reference) C02F 1/28 C02F 1/28 Z 1/52 1/52 C 1/56 1/56 C F term (reference) ) 4D015 BA04 BA05 BA11 BA17 BA19 BB08 BB12 CA04 DA02 DA05 DA08 DA25 DA32 DA35 DB01 DB03 DB12 DB24 DB33 DB35 DC04 EA06 EA32 4D024 AA04 AB00 BA07 BB01 BC04 CA01 CA06 DA10 DB12 DB21 4G066 AA62B BA09 CA02 DA08

Claims (8)

【特許請求の範囲】[Claims] 【請求項1】 (a)イオン交換/吸着成分、(b)凝
結成分、及び(c)助沈成分を少なくとも含む凝集剤で
あって、 前記(a)イオン交換/吸着成分として人工ゼオライト
を配合してなり、且つ塩素分を実質的に含まない、食品
の洗浄廃水処理用凝集剤。
1. A coagulant containing at least (a) an ion exchange / adsorption component, (b) a coagulation component, and (c) a coprecipitation component, wherein an artificial zeolite is blended as the (a) ion exchange / adsorption component. And a coagulant for treating food wastewater, which is substantially free of chlorine.
【請求項2】 前記人工ゼオライトの配合量が、10〜
40重量%である、請求項1記載の食品の洗浄廃水処理
用凝集剤。
2. The blending amount of the artificial zeolite is 10 to 10.
The aggregating agent for treating food wastewater according to claim 1, which is 40% by weight.
【請求項3】 前記人工ゼオライトが、Ca型、Mg型
及びFe型からなる群より選択される一種以上の人工ゼ
オライトである、食品の洗浄廃水処理用請求項1又は2
記載の凝集剤。
3. The cleaning wastewater treatment of foods according to claim 1, wherein the artificial zeolite is one or more artificial zeolites selected from the group consisting of Ca type, Mg type and Fe type.
The aggregating agent described.
【請求項4】 前記(b)凝結成分が、水溶性アルミニ
ウム塩および/または高分子有機化合物である、請求項
1〜3の何れかに記載の食品の洗浄廃水処理用凝集剤。
4. The aggregating agent for cleaning food wastewater according to claim 1, wherein the coagulating component (b) is a water-soluble aluminum salt and / or a high molecular weight organic compound.
【請求項5】 前記水溶性アルミニウム塩の含有量が2
0〜40重量%であり、前記高分子有機化合物の含有量
が1〜5重量%である、請求項4記載の食品の洗浄廃水
処理用凝集剤。
5. The content of the water-soluble aluminum salt is 2
The aggregating agent for cleaning food wastewater according to claim 4, wherein the aggregating agent is 0 to 40% by weight, and the content of the high molecular weight organic compound is 1 to 5% by weight.
【請求項6】 前記(c)助沈成分が、硫酸カルシウム
および/または粘土類である、請求項1〜5の何れかに
記載の食品の洗浄廃水処理用凝集剤。
6. The flocculant for treating food wastewater according to claim 1, wherein the coprecipitating component (c) is calcium sulfate and / or clay.
【請求項7】 前記硫酸カルシウムの含有量が10〜4
0重量%であり、前記粘土類の含有量が5〜40重量%
である、請求項6記載の食品の洗浄廃水処理用凝集剤。
7. The calcium sulfate content is 10 to 4
0% by weight, and the clay content is 5 to 40% by weight
The aggregating agent for treating food wastewater according to claim 6, which is
【請求項8】 洗米廃水処理用である、請求項1〜7の
何れかに記載の食品の洗浄廃水処理用凝集剤。
8. The aggregating agent for treating washing wastewater of food according to any one of claims 1 to 7, which is for treating washing wastewater of rice.
JP2002025588A 2002-02-01 2002-02-01 Flocculant for treating washing wastewater of food Pending JP2003225513A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2002025588A JP2003225513A (en) 2002-02-01 2002-02-01 Flocculant for treating washing wastewater of food

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2002025588A JP2003225513A (en) 2002-02-01 2002-02-01 Flocculant for treating washing wastewater of food

Publications (1)

Publication Number Publication Date
JP2003225513A true JP2003225513A (en) 2003-08-12

Family

ID=27747701

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2002025588A Pending JP2003225513A (en) 2002-02-01 2002-02-01 Flocculant for treating washing wastewater of food

Country Status (1)

Country Link
JP (1) JP2003225513A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005199248A (en) * 2004-01-15 2005-07-28 Nippon Solid Co Ltd Raw water treatment process
JP2010029756A (en) * 2008-07-25 2010-02-12 Kameda Seika Co Ltd Method for subjecting rice washing drainage to solid-liquid separation
CN103979711A (en) * 2014-05-16 2014-08-13 吴江市英力达塑料包装有限公司 Method for treating soybean processing wastewater

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005199248A (en) * 2004-01-15 2005-07-28 Nippon Solid Co Ltd Raw water treatment process
JP2010029756A (en) * 2008-07-25 2010-02-12 Kameda Seika Co Ltd Method for subjecting rice washing drainage to solid-liquid separation
CN103979711A (en) * 2014-05-16 2014-08-13 吴江市英力达塑料包装有限公司 Method for treating soybean processing wastewater

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