JP2003053182A - Dewatering aid and dewatering method using the same - Google Patents

Dewatering aid and dewatering method using the same

Info

Publication number
JP2003053182A
JP2003053182A JP2001249121A JP2001249121A JP2003053182A JP 2003053182 A JP2003053182 A JP 2003053182A JP 2001249121 A JP2001249121 A JP 2001249121A JP 2001249121 A JP2001249121 A JP 2001249121A JP 2003053182 A JP2003053182 A JP 2003053182A
Authority
JP
Japan
Prior art keywords
natural
dewatering
fiber
dehydration
liquid waste
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
JP2001249121A
Other languages
Japanese (ja)
Inventor
Norihiro Yaide
乃大 矢出
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.)
Ebara Corp
Original Assignee
Ebara Corp
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 Ebara Corp filed Critical Ebara Corp
Priority to JP2001249121A priority Critical patent/JP2003053182A/en
Publication of JP2003053182A publication Critical patent/JP2003053182A/en
Pending legal-status Critical Current

Links

Landscapes

  • Treatment Of Sludge (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)

Abstract

PROBLEM TO BE SOLVED: To provide a dewatering aide which allows biological decomposition utilizable as raw material of compost and a dewatering method using the same. SOLUTION: This dewatering aide comprises natural fiber 100 pts.wt. having a thickness of several μm to 1 mm and a length of 1 mm to several cm and water soluble natural polymer chemical 2-10 pts.wt. Further, in this dewatering method of liquid waste, the natural fiber is the remains of plant, the water soluble polymer chemical is biodegradable one such as carboxymethylcellulose salt, alginic acid salt and polyvinyl alcohol and, further, the dewatering assitant is added to liquid waste and is mixed and, thereafter, dewatering treatment is performed.

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、液状廃棄物の脱水
に係り、特に、下水、し尿、産業排水等の排水処理に伴
って発生する汚泥や生ごみ等の有機性廃棄物などの液状
廃棄物を、脱水処理するための脱水助剤とそれを用いた
脱水方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to dehydration of liquid waste, and more particularly to liquid waste such as sludge and organic waste such as kitchen waste generated by wastewater treatment of sewage, night soil, industrial wastewater and the like. The present invention relates to a dehydrating auxiliary agent for dehydrating a product and a dehydrating method using the same.

【0002】[0002]

【従来の技術】下水、し尿、産業排水等の排水処理に伴
って発生する余剰汚泥、凝集沈殿汚泥や生ごみ等の有機
性廃棄物を処理処分するには、脱水処理は不可欠であ
る。液状廃棄物等の脱水方法としては、液状廃棄物に有
機高分子凝集剤あるいは有機高分子凝集剤と無機凝集剤
を添加し、液状廃棄物を凝集させた後に脱水機で脱水す
るのが一般的である。一方、脱水された脱水ケーキの大
部分は、焼却処分されているが、今後脱水ケーキの再利
用を考えると、コンポスト化が望ましい処分方法であ
る。コンポスト化においては、脱水工程で使われた薬剤
等は微生物により分解できることが重要である。
2. Description of the Related Art Dewatering is indispensable for treating and disposing of organic wastes such as surplus sludge, coagulated sedimentation sludge, and garbage generated by wastewater treatment such as sewage, night soil and industrial wastewater. As a method of dehydrating liquid waste, etc., it is common to add an organic polymer coagulant or an organic polymer coagulant and an inorganic coagulant to the liquid waste, coagulate the liquid waste, and then dehydrate it with a dehydrator. Is. On the other hand, most of the dehydrated dehydrated cake is incinerated, but considering the reuse of the dehydrated cake in the future, composting is the preferred disposal method. In composting, it is important that the drugs used in the dehydration process can be decomposed by microorganisms.

【0003】従来の技術を以下に示す。 (1) 木材パルプ等植物由来のセルロース素材を、太
さ1μm以下に微細化したセルロース繊維により、タン
パク質などの高分子量の分子や粒子を吸着除去する方法
が提案されている。 (2) 天然繊維や人造繊維などの有機性の繊維物質
と、カチオン性高分子凝集剤との加圧成形された汚泥の
加圧脱水用助剤と、その助剤を使用した脱水法が提案さ
れている。
The conventional techniques are shown below. (1) A method of adsorbing and removing high molecular weight molecules and particles such as proteins by using cellulose fibers obtained by refining a plant-derived cellulose material such as wood pulp to a thickness of 1 μm or less has been proposed. (2) Auxiliary agent for pressure dehydration of sludge pressure-molded with organic fiber materials such as natural fiber and artificial fiber, and cationic polymer flocculant, and dehydration method using the auxiliary agent Has been done.

【0004】(3) 汚泥に、長さが2〜30mmの石
綿などの無機繊維や天然有機繊維、人造繊維、合成繊
維、炭素繊維、金属繊維と無機凝集剤や高分子凝集剤を
添加混合し、汚泥を脱水する方法が提案されている。そ
の繊維表面を、カチオン系界面活性剤や分散剤で処理し
た繊維や処理していない繊維も使用できる。 (4) 汚泥に、アルギン酸ナトリウムやポリビニルア
ルコールなどの水溶性有機高分子化合物及び繊維状物質
を混合し、かつ、不溶化剤で処理する汚泥の脱水方法が
提案されている。繊維状物質とは、アスベストなどの繊
維状鉱物、合成繊維、天然繊維、炭素繊維などの化学繊
維、半合成繊維、再生繊維、パルプ等である。不溶化剤
は、無機の多価カチオンを生成する化合物である。この
水溶性有機高分子化合物及び繊維状物質は、予め、混合
されていることが特徴である。
(3) An inorganic fiber such as asbestos having a length of 2 to 30 mm, a natural organic fiber, an artificial fiber, a synthetic fiber, a carbon fiber, a metal fiber and an inorganic coagulant or a polymer coagulant are added to and mixed with sludge. , A method of dehydrating sludge has been proposed. Fibers whose surface has been treated with a cationic surfactant or dispersant or untreated can also be used. (4) A method of dehydrating sludge in which a water-soluble organic polymer compound such as sodium alginate or polyvinyl alcohol and a fibrous substance are mixed with sludge and treated with an insolubilizer has been proposed. Fibrous substances include fibrous minerals such as asbestos, synthetic fibers, natural fibers, chemical fibers such as carbon fibers, semi-synthetic fibers, recycled fibers, pulp and the like. The insolubilizer is a compound that produces an inorganic polyvalent cation. The water-soluble organic polymer compound and the fibrous substance are characteristically mixed in advance.

【0005】前記した従来より提案されている方法に
は、以下のような問題点がある。 (1) 微細化したセルロース繊維は、高分子物質の吸
着除去が目的であるが、これを脱水助剤に使用するとす
れば、汚泥粒子の吸着性が良好であり、セルロース繊維
が生分解性であるが、セルロース繊維と汚泥粒子中の水
分との親和性が良いために、脱水性が低下し、かつセル
ロース繊維自体が高価である。 (2) 有機性の繊維物質とカチオン性高分子凝集剤と
の加圧成形された汚泥の加圧脱水用助剤は、加圧脱水用
の脱水助剤であるために脱水工程への用途が狭い。天然
繊維自体は生分解性を有するが、高分子凝集剤の生分解
性は未知であり、コンポストの安全性に疑問が残る。
The above-mentioned conventionally proposed method has the following problems. (1) Micronized cellulose fibers are used for the purpose of adsorbing and removing polymer substances, but if this is used as a dehydration aid, the sludge particle adsorbability is good and the cellulose fibers are biodegradable. However, since the affinity between the cellulose fiber and the moisture in the sludge particles is good, the dehydration property is lowered and the cellulose fiber itself is expensive. (2) Since the pressure dehydration aid for sludge pressure-formed with the organic fiber substance and the cationic polymer flocculant is a dehydration aid for pressure dehydration, it is suitable for use in the dehydration process. narrow. Although natural fiber itself has biodegradability, the biodegradability of the polymer flocculant is unknown, and the safety of compost remains questionable.

【0006】(3) 無機繊維や合成繊維などの繊維
と、無機凝集剤や高分子凝集剤を脱水助剤として脱水す
る方法においては、天然有機繊維も使われており、これ
は生分解性がある。しかしながら、疎水性の天然有機繊
維を親水化させるための界面活性剤は、汚泥の凝集性の
向上に寄与し、まず添加された天然有機繊維が汚泥と馴
染むためのものではない。十分に親水化された繊維と汚
泥の混合が重要である。 (4) 水溶性有機高分子化合物及び繊維状物質を混合
し、かつ、不溶化剤で処理する汚泥の脱水方法は、無機
化合物である不溶化剤をコンポスト原料となる汚泥に添
加しており、コンポスト過程で分解できないばかりか、
無機化合物に存在する金属が肥料成分のリンを固定する
ことから得策でない。
(3) Natural organic fibers are also used in the method of dehydrating fibers such as inorganic fibers and synthetic fibers, and inorganic coagulants and polymer coagulants as a dehydration aid, which is biodegradable. is there. However, the surfactant for hydrophilizing the hydrophobic natural organic fiber contributes to the improvement of the cohesiveness of the sludge and is not for the added natural organic fiber to be compatible with the sludge. It is important to mix the fully hydrophilized fiber and sludge. (4) A method for dehydrating sludge in which a water-soluble organic polymer compound and a fibrous substance are mixed and treated with an insolubilizing agent is that an insolubilizing agent which is an inorganic compound is added to sludge as a raw material for composting. Not only can you disassemble with
It is not a good idea because the metal present in the inorganic compound fixes phosphorus, which is a fertilizer component.

【0007】[0007]

【発明が解決しようとする課題】本発明は、上記従来技
術に鑑み、その脱水ケーキが、コンポストの原料に利用
できるように、脱水に使用される薬剤をすべて生物分解
可能なものとして、液状廃棄物を効果的に脱水処理する
ことができる脱水助剤とそれを用いた脱水方法を提供す
ることを課題とする。
DISCLOSURE OF THE INVENTION In view of the above-mentioned prior art, the present invention provides a liquid waste in which the dehydrated cake is biodegradable for all chemicals used for dehydration so that it can be used as a raw material for compost. An object of the present invention is to provide a dehydration aid capable of effectively dehydrating a product and a dehydration method using the same.

【0008】[0008]

【課題を解決するための手段】上記課題を解決するため
に、本発明では、太さが数μm〜1mm、長さが1mm
〜数cmの天然繊維100重量部と、水溶性天然高分子
薬剤2〜10重量部とからなる脱水助剤としたものであ
る。前記脱水助剤において天然繊維が、植物遺体であ
り、水溶性天然高分子薬剤が、カルボキシメチルセルロ
ースの塩、アルギン酸塩又はポリビニルアルコール等の
生分解性のものがよい。また、本発明では、前記の脱水
助剤を、液状廃棄物に添加混合した後、脱水処理するこ
とを特徴とする液状廃棄物の脱水方法としたものであ
る。
In order to solve the above problems, the present invention has a thickness of several μm to 1 mm and a length of 1 mm.
It is used as a dehydration aid consisting of 100 parts by weight of natural fiber of several cm to 2 to 10 parts by weight of a water-soluble natural polymer drug. In the dehydration aid, the natural fiber is a plant remains, and the water-soluble natural polymer agent is preferably a biodegradable one such as a salt of carboxymethyl cellulose, alginate or polyvinyl alcohol. Further, the present invention provides a method for dehydrating liquid waste, which comprises adding and mixing the above-mentioned dehydrating aid to liquid waste, and then performing dehydration treatment.

【0009】[0009]

【発明の実施の形態】以下に、本発明を詳細に説明す
る。本発明に用いる天然繊維は、製紙原料の木質パル
プ、リサイクルで回収された木綿、ケナフ繊維、サトウ
キビの絞りかす、水草のヨシ、麻等の植物性繊維、腐植
土やピートモスなどの植物遺体である。安価で供給量が
安定し、コンポスト過程で残留しても、製品コンポスト
の品質に影響を与えない、腐植土やピートモスなどの植
物遺体が好適である。また、植物遺体の天然繊維は、そ
の形状が不定形でその表面が凹凸に富み、液状廃棄物中
の固形物や後述する親水化の薬剤である天然高分子薬剤
を保持しやすいために好適である。天然繊維の形状は、
太さが数μm〜1mm、長さが1mm〜数cmである。
太さは細い方が脱水性能には都合がよいが、天然繊維を
新たに加工するのが困難である。長さは、ハンドリング
に影響するので、スラリー状にしたときの作業性を考慮
すると、数mm〜1cmが好適である。
BEST MODE FOR CARRYING OUT THE INVENTION The present invention is described in detail below. The natural fiber used in the present invention is wood pulp of papermaking raw material, cotton recovered by recycling, kenaf fiber, sugarcane squeeze, reeds of aquatic plants, plant fibers such as hemp, plant remains such as humus and peat moss. . Plant remains such as humus soil and peat moss are preferable because they are inexpensive, have a stable supply, and do not affect the quality of product compost even if they remain in the composting process. In addition, the natural fiber of the plant remains is preferable because its shape is irregular and its surface is rich in irregularities, and it is easy to hold the solid matter in the liquid waste and the natural polymer drug which is a hydrophilic agent described later. is there. The shape of natural fiber is
The thickness is several μm to 1 mm, and the length is 1 mm to several cm.
The smaller the thickness, the better the dehydration performance, but it is difficult to newly process the natural fiber. Since the length affects handling, it is preferable that the length is several mm to 1 cm in consideration of workability when the slurry is formed.

【0010】本発明の水溶性天然高分子薬剤は、天然繊
維表面を親水性にでき、コンポスト製造時に好気性微生
物によって、あるいはコンポストにされた後に土壌細菌
によって、天然高分子薬剤が分解できるものを指す。増
粘剤や結着剤や乳化安定剤のような食品添加物でもよ
い。天然繊維に天然高分子薬剤を含浸させる方法は、天
然繊維を天然高分子薬剤又はその水溶液に浸漬させたの
ちに、スクリーン等の金網で水切りあるいは脱水する。
また、浸漬後に自然に乾燥させても良い。天然繊維の水
分は、液状廃棄物と天然繊維の混合性や添加時の粉塵発
生防止など作業性に大きく影響する。天然繊維の水分含
有率は、乾燥天然繊維あたり5〜20%である。天然繊
維の水分は、単に水分でも良いし、親水性のある本発明
の水溶性天然高分子剤を後述する添加率分添加し、その
残りを水分にしても良い。水分の場合には、乾燥天然繊
維あたり5%未満では粉塵による作業性の悪化や液状廃
棄物との混合が問題である。また、20%を超えると、
水分の比率が大きく輸送費がかさんだり、水分の浸出が
問題になる。
The water-soluble natural polymer drug of the present invention is one which can make the surface of natural fiber hydrophilic and can decompose the natural polymer drug by aerobic microorganisms during compost production or by soil bacteria after composting. Point to. It may be a food additive such as a thickener, a binder or an emulsion stabilizer. As a method of impregnating a natural polymer with a natural polymer drug, the natural fiber is immersed in the natural polymer drug or an aqueous solution thereof, and then drained or dehydrated with a wire net such as a screen.
Further, it may be naturally dried after the immersion. The water content of natural fibers has a great influence on workability such as mixing of liquid waste and natural fibers and prevention of dust generation at the time of addition. The water content of the natural fibers is 5 to 20% per dry natural fiber. The water content of the natural fiber may be simply water content, or the water-soluble natural polymer agent of the present invention having hydrophilicity may be added at an addition rate described below, and the rest may be water content. In the case of water, if it is less than 5% based on dry natural fiber, deterioration of workability due to dust and mixing with liquid waste pose problems. Also, when it exceeds 20%,
The water content is high and transportation costs are high, and water leaching becomes a problem.

【0011】天然繊維の天然高分子薬剤含有量は、乾燥
天然繊維100重量部に対して、天然高分子薬剤が2〜
10重量部である。天然繊維の天然高分子薬剤含有量が
10重量部を超えると、天然高分子薬剤を含浸させた天
然繊維の繊維同士が固着したりして作業性が劣る。ま
た、2重量部未満では親水性の改善効果が低い。しかし
ながら、2重量部未満でも、余剰汚泥のように、その中
に活性汚泥に起因するタンパク質を多く含み、菌体外ポ
リマーと言われる多糖類をもつ液状廃棄物においては、
天然繊維に液状廃棄物自身が親水性を与えるので、天然
高分子薬剤含有量が低くても、液状廃棄物と本発明の天
然繊維の混合や脱水効果に問題はない。一方、天然高分
子薬剤を含浸させていない天然繊維をスラリー状にし、
このスラリーに天然高分子薬剤を所定濃度添加すること
もできる。天然高分子薬剤により親水化させた天然繊維
は、粉体のままで液状廃棄物に添加しても良いし、スラ
リー状にして添加しても良い。天然繊維を天然高分子薬
剤により親水化させることにより、スラリー化が容易に
できる。
The content of the natural polymer drug in the natural fiber is 2 to 100 parts by weight of the dry natural fiber.
10 parts by weight. If the content of the natural polymer agent in the natural fiber exceeds 10 parts by weight, the fibers of the natural fiber impregnated with the natural polymer agent may stick to each other, resulting in poor workability. If it is less than 2 parts by weight, the effect of improving hydrophilicity is low. However, even if the amount is less than 2 parts by weight, in a liquid waste containing a large amount of protein derived from activated sludge, such as excess sludge, and having a polysaccharide called extracellular polymer,
Since the liquid waste itself imparts hydrophilicity to the natural fibers, there is no problem in the mixing or dehydrating effect of the liquid waste and the natural fibers of the present invention even if the content of the natural polymer drug is low. On the other hand, natural fibers not impregnated with natural polymer agents are slurried,
A natural polymer drug may be added to the slurry at a predetermined concentration. The natural fiber hydrophilized by the natural polymer drug may be added to the liquid waste as a powder or may be added in the form of a slurry. Slurrying can be facilitated by hydrophilizing natural fibers with a natural polymer agent.

【0012】作業性や薬剤注入設備の簡略化を考慮する
と、天然高分子薬剤を含浸させた天然繊維を使用する本
発明の方法が好適である。本発明の天然高分子薬剤は、
具体的にはCMC(カルボキシメチルセルロース)のナ
トリウム塩、メチルセルロースなどの水溶性セルロース
誘導体、デンプングリコール酸ナトリウム、アルギン酸
ナトリウム、多糖類やデンプン類糖、寒天、ゼラチン、
フノリ、PVA(ポリビニルアルコール)、サポニン、
キトサン、キチン、ソルビットなどである。上記の水溶
性天然高分子薬剤のいずれか1種類又は複数の薬剤を混
合して、天然繊維に含浸させることができる。天然繊維
をスラリー状にする解砕方法は、既存のパルパーや機械
式撹拌機を用いることができる。また、上記の脱水助剤
を用いた本発明の液状廃棄物の脱水方法においては、凝
集剤として従来のように有機性の高分子凝集剤や無機凝
集剤が使用できる。脱水機は、市販のものが使用でき、
ベルトプレス型やスクリュープレス型、遠心分離、フィ
ルタープレス型いずれも使用できる。
In view of workability and simplification of drug injection equipment, the method of the present invention using natural fiber impregnated with a natural polymer drug is preferable. The natural polymer drug of the present invention is
Specifically, CMC (carboxymethyl cellulose) sodium salt, water-soluble cellulose derivatives such as methyl cellulose, sodium starch glycolate, sodium alginate, polysaccharides and starch sugars, agar, gelatin,
Funori, PVA (polyvinyl alcohol), saponin,
Examples include chitosan, chitin and sorbit. Any one or more of the above water-soluble natural polymer drugs can be mixed to impregnate natural fibers. An existing pulper or mechanical stirrer can be used as a crushing method for making natural fibers into a slurry. Further, in the method for dehydrating liquid waste of the present invention using the above dehydration aid, an organic polymer coagulant or an inorganic coagulant can be used as a coagulant as in the conventional case. A commercially available dehydrator can be used,
Any of belt press type, screw press type, centrifugal separation, and filter press type can be used.

【0013】[0013]

【実施例】以下に、本発明を詳細に説明するが、本発明
はこれらに限定されるものでない。 参考例1 下水混合汚泥に天然繊維又は合成繊維を所定量添加し、
ジメチルアミノエチルアクリレート系のカチオン系高分
子凝集剤で凝集させた後、ベルトプレス型脱水機で脱水
処理した。下水混合汚泥の性状は以下の表1の通りであ
る。
The present invention will be described in detail below, but the present invention is not limited thereto. Reference Example 1 A predetermined amount of natural fiber or synthetic fiber is added to sewage mixed sludge,
After coagulating with a dimethylaminoethyl acrylate-based cationic polymer coagulant, dehydration treatment was performed with a belt press dehydrator. The properties of the sewage mixed sludge are as shown in Table 1 below.

【表1】 [Table 1]

【0014】天然繊維のうちピートモスは、太さが約5
0μm、長さが5mm〜15mmのカナダ産で、木綿は
衣料品のリサイクル繊維で太さが50〜100μm、長
さが10mmにカットしたものである。合成繊維は、ペ
ットボトルから再生した繊維で、その形状は、太さが1
0〜15μm、長さが10mmである。これらを5%ス
ラリーになるように水道水に添加し、ジューサーミキサ
ーで5分間解砕した。ベルトプレス型脱水機の仕様、運
転条件は以下の表2の通りである。
Among natural fibers, peat moss has a thickness of about 5
Made in Canada with a length of 0 μm and a length of 5 mm to 15 mm, cotton is a recycled fiber of clothing and cut into a thickness of 50 to 100 μm and a length of 10 mm. Synthetic fibers are fibers regenerated from plastic bottles, and their shape is 1 in thickness.
The length is 0 to 15 μm and the length is 10 mm. These were added to tap water so as to be a 5% slurry and crushed for 5 minutes with a juicer mixer. The specifications and operating conditions of the belt press type dehydrator are shown in Table 2 below.

【表2】 [Table 2]

【0015】表3に参考例1の結果を示す。脱水助剤と
しての天然繊維や合成繊維は共に含水率が低く、ろ布か
らの脱水ケーキの剥離が良好であった。
Table 3 shows the results of Reference Example 1. Both the natural fiber and the synthetic fiber as the dewatering aid had a low water content, and the dewatering cake peeled from the filter cloth was good.

【表3】 [Table 3]

【0016】実施例1 参考例1の下水混合汚泥を用いて、参考例1のピートモ
スや木綿やPET再生繊維に天然高分子剤を添加して製
造した脱水助剤を混合して、参考例1と同様に脱水試験
をした。表4に結果を示す。
Example 1 Using the sewage-mixed sludge of Reference Example 1, a dehydration aid produced by adding a natural polymer agent to the peat moss, cotton or PET recycled fiber of Reference Example 1 was mixed, and then Reference Example 1 A dehydration test was conducted in the same manner as in. The results are shown in Table 4.

【表4】 [Table 4]

【0017】参考例2 参考例1の下水混合汚泥にセルロース繊維及び参考例1
のピートモスを加圧成形したペレットを添加して参考例
1の条件で脱水した。セルロース繊維は、市販の太さが
約1μm、長さが10mmのビスコースレーヨン繊維を
使用した。ピートモスの加圧成形ペレットは、ピートモ
スと参考例1のカチオン高分子凝集剤とを混合し、油圧
プレス機にて10Mpaで直径約5mmで長さが約5m
mの円柱形に加工した。表5に参考例2の結果を示す。
セルロース繊維使用では、吸湿性のために脱水ケーキの
含水率や剥離性が悪い。高分子凝集剤を併用しても脱水
性は改善されなかった。ピートモスの加圧成形ペレット
では、高分子凝集剤を多くしないと、加圧成形ペレット
に加工できなかった。高分子凝集剤を多くすると、脱水
ケーキの含水率が高く、剥離性も低下した。
REFERENCE EXAMPLE 2 Cellulose fiber and sewage mixture in sewage mixed sludge of Reference Example 1
The pellets obtained by press-molding peat moss were added and dehydrated under the conditions of Reference Example 1. As the cellulose fiber, a commercially available viscose rayon fiber having a thickness of about 1 μm and a length of 10 mm was used. The pressure-molded pellets of peat moss were obtained by mixing peat moss with the cationic polymer flocculant of Reference Example 1 and using a hydraulic press machine at 10 MPa at a diameter of about 5 mm and a length of about 5 m.
It was processed into a cylindrical shape of m. Table 5 shows the results of Reference Example 2.
When cellulose fibers are used, the moisture content and peelability of the dehydrated cake are poor due to the hygroscopicity. Dehydration was not improved even when a polymer flocculant was used in combination. The pressure-molded pellets of Pete Moss could not be processed into the pressure-molded pellets without increasing the amount of the polymer flocculant. When the amount of the polymer flocculant was increased, the water content of the dehydrated cake was high and the peeling property was lowered.

【0018】[0018]

【表5】 [Table 5]

【0019】参考例3 参考例1の下水混合汚泥に水溶性有機高分子化合物と繊
維状物質を添加混合後、不溶化剤を添加して参考例1の
条件で脱水した。水溶性有機高分子化合物はアルギン酸
ナトリウムを、繊維状物質は参考例1のピートモスを、
不溶化剤はポリ鉄を使用した。表6に参考例3の結果を
示す。ピートモス添加率を増やすことにより、無機凝集
剤や高分子凝集剤を使用しなくても脱水ができた。
Reference Example 3 A water-soluble organic polymer compound and a fibrous substance were added to and mixed with the sewage-mixed sludge of Reference Example 1, and an insolubilizer was added to dehydrate the sludge under the conditions of Reference Example 1. The water-soluble organic polymer compound is sodium alginate, and the fibrous substance is the peat moss of Reference Example 1,
Polyiron was used as the insolubilizer. Table 6 shows the results of Reference Example 3. By increasing the addition rate of peat moss, dehydration was possible without using an inorganic coagulant or a polymer coagulant.

【0020】[0020]

【表6】 [Table 6]

【0021】参考例4 参考例1の下水混合汚泥に参考例3の水溶性有機高分子
化合物、アルギン酸ナトリウムと繊維状物質の乾燥ピー
トモスとを粉末状態で予め混合したものを添加混合し、
更に不溶化剤を添加して参考例1の条件で脱水した。表
7に参考例4の結果を示す。乾燥ピートモスとアルギン
酸ナトリウムを粉末状態で混合したものを汚泥に添加し
ても十分に汚泥と馴染まなかったために脱水性能が低下
した。
Reference Example 4 To the sewage-mixed sludge of Reference Example 1, a water-soluble organic polymer compound of Reference Example 3, sodium alginate, and dry peat moss of a fibrous substance were mixed in advance in a powder state, and mixed.
Further, an insolubilizer was added and dehydration was performed under the conditions of Reference Example 1. Table 7 shows the results of Reference Example 4. Even if a mixture of dry peat moss and sodium alginate in a powder state was added to sludge, it did not become sufficiently compatible with sludge, so that the dehydration performance deteriorated.

【表7】 [Table 7]

【0022】参考例5 参考例1の下水混合汚泥に、参考例3の乾燥ピートモス
とアルギン酸ナトリウムを粉末状態で混合したものに、
水を添加して、その混合物の含水率を約30%にしたも
のを添加混合し、更に不溶化剤を添加して参考例1の条
件で脱水した。表8に参考例5の結果を示す。
Reference Example 5 The sewage mixed sludge of Reference Example 1 was mixed with the dry peat moss of Reference Example 3 and sodium alginate in a powder state,
Water was added to the mixture to make it have a water content of about 30%, and the mixture was mixed. An insolubilizing agent was further added to dehydrate the mixture under the conditions of Reference Example 1. Table 8 shows the results of Reference Example 5.

【表8】 [Table 8]

【0023】[0023]

【発明の効果】本発明は、水溶性で生分解性の天然高分
子剤で親水化させた天然繊維を、脱水助剤として使用す
ることにより、以下の効果を有する。 (1) 無機凝集剤や高分子凝集剤を使用しなくても脱
水性能が向上する。 (2) 生分解性で安全性の高い薬剤を脱水に使用する
ために、脱水ケーキはコンポストに利用できる。 (3) 廃棄物のコンポスト化が促進されて廃棄物量の
削減が可能。 (4) 脱水助剤の天然繊維がコンポストに残留する
と、土壌改良材として土壌の通気性が改善される。
INDUSTRIAL APPLICABILITY The present invention has the following effects by using a natural fiber hydrophilized with a water-soluble and biodegradable natural polymer agent as a dehydration aid. (1) The dehydration performance is improved without using an inorganic coagulant or a polymer coagulant. (2) The dehydrated cake can be used for compost in order to use a biodegradable and highly safe drug for dehydration. (3) The amount of waste can be reduced by promoting the composting of waste. (4) When the natural fiber of the dehydration aid remains in the compost, the air permeability of the soil is improved as a soil improving material.

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】 太さが数μm〜1mm、長さが1mm〜
数cmの天然繊維100重量部と、水溶性天然高分子薬
剤2〜10重量部とからなる脱水助剤。
1. A thickness of several μm to 1 mm and a length of 1 mm to
A dehydration aid comprising 100 parts by weight of a few cm of natural fiber and 2 to 10 parts by weight of a water-soluble natural polymer drug.
【請求項2】 前記天然繊維が、植物遺体であり、水溶
性天然高分子薬剤が、カルボキシメチルセルロースの
塩、アルギン酸塩又はポリビニルアルコールであること
を特徴とする請求項1記載の脱水助剤。
2. The dehydration aid according to claim 1, wherein the natural fiber is a plant remains, and the water-soluble natural polymer agent is a salt of carboxymethyl cellulose, an alginate or polyvinyl alcohol.
【請求項3】 請求項1又は2記載の脱水助剤を、液状
廃棄物に添加混合した後、脱水処理することを特徴とす
る液状廃棄物の脱水方法。
3. A method for dehydrating liquid waste, which comprises adding and mixing the dehydration auxiliary agent according to claim 1 or 2 to liquid waste, and then performing dehydration treatment.
JP2001249121A 2001-08-20 2001-08-20 Dewatering aid and dewatering method using the same Pending JP2003053182A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2001249121A JP2003053182A (en) 2001-08-20 2001-08-20 Dewatering aid and dewatering method using the same

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2001249121A JP2003053182A (en) 2001-08-20 2001-08-20 Dewatering aid and dewatering method using the same

Publications (1)

Publication Number Publication Date
JP2003053182A true JP2003053182A (en) 2003-02-25

Family

ID=19078170

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2001249121A Pending JP2003053182A (en) 2001-08-20 2001-08-20 Dewatering aid and dewatering method using the same

Country Status (1)

Country Link
JP (1) JP2003053182A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006305518A (en) * 2005-05-02 2006-11-09 Ebara Engineering Service Co Ltd Method and apparatus for dewatering sludge
JP2007283225A (en) * 2006-04-18 2007-11-01 Ebara Engineering Service Co Ltd Dehydration assistant for sludge and dehydration method/device for sludge using this assistant
JP2010131498A (en) * 2008-12-03 2010-06-17 Sumitomo Heavy Ind Ltd Sludge treatment method
JP2012071296A (en) * 2010-08-31 2012-04-12 Swing Corp Dehydration aid for sludge, method and apparatus for dehydrating sludge
JP2016097373A (en) * 2014-11-25 2016-05-30 株式会社石垣 Sludge dehydration treatment method and sludge dehydration treatment system

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006305518A (en) * 2005-05-02 2006-11-09 Ebara Engineering Service Co Ltd Method and apparatus for dewatering sludge
JP4533232B2 (en) * 2005-05-02 2010-09-01 荏原エンジニアリングサービス株式会社 Sludge dewatering method and apparatus
JP2007283225A (en) * 2006-04-18 2007-11-01 Ebara Engineering Service Co Ltd Dehydration assistant for sludge and dehydration method/device for sludge using this assistant
JP2010131498A (en) * 2008-12-03 2010-06-17 Sumitomo Heavy Ind Ltd Sludge treatment method
JP2012071296A (en) * 2010-08-31 2012-04-12 Swing Corp Dehydration aid for sludge, method and apparatus for dehydrating sludge
JP2016097373A (en) * 2014-11-25 2016-05-30 株式会社石垣 Sludge dehydration treatment method and sludge dehydration treatment system

Similar Documents

Publication Publication Date Title
US8821733B2 (en) Systems and methods for recovering fine particles from fluid suspensions for combustion
FI120319B (en) A novel composite product based on fibers and fillers and a process for making such a novel product
AU2008270600B2 (en) Use of cyclodextrins for odor control in papermaking sludges, and deodorized sludge and products
JP4189479B2 (en) Dehydration aid and method for producing the same
WO2015108762A1 (en) Use of celluloses in sludge dewatering, and sludge products thereof
EP3294674B1 (en) Water treatment
CN108359125B (en) Preparation method of modified cellulose aerogel based on waste newspaper
JP6861554B2 (en) Dehydrating agent for sludge
GB2048845A (en) Process for the Preparation of Coal-containing Sludge Pellets Valuable as Fertilizer and Fuel
EP3294675A1 (en) Water treatment
JP2003053182A (en) Dewatering aid and dewatering method using the same
CA2625253C (en) Method for manufacture of sanitised organic sludge
JP2005248337A (en) Highly active cellulose fiber, method for producing the same, and dehydrating auxiliary using the same
JP2003088900A (en) Animal excrement treatment method
CN106192532B (en) Sludge modification and reuse method
JP4150523B2 (en) Manufacturing method of compost fertilizer
FI73253C (en) FOERFARANDE FOER AOTERVINNING AV MATERIAL I AVLOPPSVATTEN.
CN106007220B (en) A kind of Catalyzed by Ultrasonic Wave crosslinking-cellulose filters pressing separation system
Nawawi et al. Lignocellulosic fiber media filters as a potential technology for primary industrial wastewater treatment
CN111533412A (en) Sludge heat treatment recycling process
JP2002219500A (en) Dehydrating agent and method for dehydrating organic sludge
Boonsong et al. Efficiency Improvement of Some Agricultural Residue Modified Materials for Textile Dyes Absorption
JP2003010681A (en) Oil removing agent and oil removing method and apparatus
Bisht et al. Extraction of Cellulose from Organic Waste for Nanocomposites Synthesis with Red Mud and Application
MX2008005585A (en) Method for manufacture of sanitised organic sludge

Legal Events

Date Code Title Description
A977 Report on retrieval

Free format text: JAPANESE INTERMEDIATE CODE: A971007

Effective date: 20041224

A131 Notification of reasons for refusal

Free format text: JAPANESE INTERMEDIATE CODE: A131

Effective date: 20050105

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20050302

A521 Written amendment

Free format text: JAPANESE INTERMEDIATE CODE: A523

Effective date: 20050316

A02 Decision of refusal

Free format text: JAPANESE INTERMEDIATE CODE: A02

Effective date: 20050513