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JPH0775720B2 - Bag-type dehydration method for sludge - Google Patents
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JPH0775720B2 - Bag-type dehydration method for sludge - Google Patents

Bag-type dehydration method for sludge

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Publication number
JPH0775720B2
JPH0775720B2 JP4097724A JP9772492A JPH0775720B2 JP H0775720 B2 JPH0775720 B2 JP H0775720B2 JP 4097724 A JP4097724 A JP 4097724A JP 9772492 A JP9772492 A JP 9772492A JP H0775720 B2 JPH0775720 B2 JP H0775720B2
Authority
JP
Japan
Prior art keywords
sludge
dehydration
bag
purifying
container
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.)
Expired - Fee Related
Application number
JP4097724A
Other languages
Japanese (ja)
Other versions
JPH05220500A (en
Inventor
榮 畑山
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.)
Individual
Original Assignee
Individual
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Filing date
Publication date
Application filed by Individual filed Critical Individual
Priority to JP4097724A priority Critical patent/JPH0775720B2/en
Publication of JPH05220500A publication Critical patent/JPH05220500A/en
Publication of JPH0775720B2 publication Critical patent/JPH0775720B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Filtering Materials (AREA)
  • Treatment Of Sludge (AREA)
  • Filtration Of Liquid (AREA)

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明はダム、湖沼、河川、海底
の堆積している底泥や浮泥、汚濁物、赤潮、青粉等、又
産業廃水の汚濁物類、即ち水産、畜産、農産食品加工の
際の廃液、或いは工業用廃液例えば金属スラッジ或いは
スラリー等の汚泥物類を浄化分離処理剤で処理し、該汚
泥物類の親水性コロイド粒子を疎水化し、水分子を分離
脱水して残留固形物及び分離水となし、ついで脱水袋等
の脱水収納体を用いて脱水することからなる汚泥物類の
袋式脱水処理方法に関する。
The present invention relates to dams, lakes, rivers, seabed sediments and sludges, pollutants, red tides, blue powders, and industrial wastewater pollutants, that is, fisheries, livestock, A liquid waste during processing of agricultural foods, or industrial liquid waste, for example, sludges such as metal sludge or slurry are treated with a purification separation treatment agent, and hydrophilic colloid particles of the sludges are hydrophobized to separate and dehydrate water molecules. The present invention relates to a bag-type dehydration treatment method for sludge, which comprises removing residual solids and separated water, and then dehydrating using a dehydration container such as a dehydration bag.

【0002】[0002]

【従来の技術】湖沼、河川、海底の堆積底泥及び産業廃
水汚濁物等の汚泥物中には一般に蛋白質、炭水化物、脂
肪酸等の有機物、無機物、細菌を含み、ミクロン単位の
微粒子又はオングストローム単位の有機或いは無機物質
の微粒子で構成され、これらが水中にコロイド状態で存
在し、その多くは親水性であるため、その除去分離が困
難となる。従来より、湖沼、河川、海底の堆積している
底泥「ヘドロ」等を、又は産業廃水汚濁物を水と分離さ
せ、残留物を固化する汚泥物類の浄化分離方法として
は、底泥に関して、 天日乾燥処理である、埋立地で長い期間を掛け圧密を
加え利用目的に合うまで自然脱水を待つ方法、 機械的脱水処理であり、脱水処理機械によって強制脱
水して泥土を固形物とする方法、 化学的脱水処理方法である高分子凝集剤によって凝集
沈澱、濃縮を行い含水率を低下させた後、石灰、セメン
ト、固化剤を用いて処理する方法、があり、その他、最
近では処理剤として、 2価又は3価の鉄塩と3価の金属塩と1価の金属塩及
び溶媒水とからなる汚泥処理剤(特開昭62−2771
99号)、 Al2,FeO3及びSO3の3成分の特定量からなる
塩基性硫酸アルミニウム鉄の水溶液からなる液体無機凝
集剤(特開昭60−14911号)等が知られ、これら
の処理剤の使用が試みられている。
BACKGROUND ART Sludges such as lakes, rivers, seabed sediments and industrial wastewater pollutants generally contain organic substances such as proteins, carbohydrates and fatty acids, inorganic substances and bacteria. It is composed of fine particles of an organic or inorganic substance, and these exist in a colloidal state in water, and most of them are hydrophilic, so that removal and separation thereof are difficult. Conventionally, as a method for purifying and separating sludge, which separates sludge from lakes, rivers, and seabed, "sludge", or industrial wastewater pollutants and solidifies the residue, It is a sun drying process, a method of waiting for natural dehydration until it meets the purpose of use by applying consolidation for a long period at a landfill, a mechanical dehydration process, forcibly dehydrating with a dehydration processing machine to make mud solid There is a method of chemical dehydration treatment such as coagulation-precipitation and concentration with a polymer flocculant to reduce the water content, and then treatment with lime, cement, and a solidifying agent. As a sludge treatment agent comprising a divalent or trivalent iron salt, a trivalent metal salt, a monovalent metal salt and solvent water (JP-A-62-2771).
99 No.), Al 2, FeO 3 and SO 3 of 3 components comprising a specific weight basic liquid inorganic coagulant comprising an aqueous solution of aluminum sulfate of iron (JP-60-14911) and the like are known, these processes Attempts have been made to use agents.

【0003】[0003]

【発明が解決しようとする課題】前記の従来技術では、
例えば次のような欠点がある。の場合の天日乾燥処理
では広い用地と長い期間をかけて底泥から水分子を蒸発
させるのであるが、その期間、底泥特有の悪臭があると
共に雨水や降雪を受けると再度液状化して悪臭を放ち、
埋立用土等に使用が困難である。の場合の機械的脱水
処理方法では、多額の費用を投下しても底泥から水分を
絞り出して含水率を低下させるにとどまり、悪臭、土
質、水質の改善はなされない。また汚泥の固化状態が完
全ではないため、埋立、盛土用土としてはその利用が困
難である。又、の化学的脱水処理方法では石灰やセメ
ントを使用するが、これらは底泥を固化させて処分を容
易にするに止まり、土質までも改善することは出来な
い。又、固化処理に伴って長い期間雨水や湧水の影響を
受けて処理地からアルカリ分が流失し、下流河川の水質
を悪化させることも問題となる。そして、上記の及び
に挙げている処理剤の場合も充分に水を分離するため
には最初に高分子凝集剤で処理する等の前処理が必要な
ばかりか、水の分離が依然として悪く長時間を要する上
に、細菌、重金属の解毒、臭気の消除については効果が
見られず、その残留固形物も利用範囲が限定される等の
点で問題があった。
In the above prior art,
For example, there are the following drawbacks. In the case of the sun drying process, water molecules are evaporated from the bottom mud over a wide area and over a long period of time, but during that period, there is a bad odor characteristic of the bottom mud, and when it receives rainwater or snow, it liquefies again and the bad odor is generated. Release
It is difficult to use for landfill soil. In the case of the method of mechanical dehydration, even if a large amount of money is invested, the water content is reduced by squeezing out the water from the bottom mud, and the malodor, soil quality, and water quality are not improved. In addition, since the sludge is not completely solidified, it is difficult to use it as landfill or embankment. Further, in the chemical dehydration treatment method, lime and cement are used, but these only solidify the bottom mud to facilitate the disposal and cannot improve the soil quality. Another problem is that the solidification process is affected by rainwater and spring water for a long period of time, causing alkalinity to be washed away from the treated area and deteriorating the water quality of the downstream river. And, in the case of the treatment agents listed in the above and, not only the pretreatment such as the treatment with the polymer coagulant is necessary in order to sufficiently separate the water, but the separation of the water is still unsatisfactory for a long time. In addition, it is not effective in detoxifying bacteria and heavy metals and eliminating odors, and there is a problem in that the range of utilization of the residual solids is limited.

【0004】したがって底泥の疎水化がすみやかに出
来、分離水、分離底泥の含有細菌の殺菌、重金属の解毒
をも可能にし、土粒子においては底泥前の土粒子に再生
することができ、その利用範囲が限定されず、埋立、盛
土用土或いは肥料として利用可能とする方法及び処理剤
の出現が望まれ、又産業廃水の汚濁物即ち工業用金属ス
ラッジ、或いは農産、畜産、水産食品加工の際の廃水の
汚濁物についても同様にその疎水化がすみやかに出来、
分離水、分離固形物の含有細菌の殺菌、重金属の解毒を
も可能とし、それらが利用できる分離処理剤及び処理方
法の出現が期待されている。
Therefore, the bottom mud can be quickly hydrophobized, the separated water, the bacteria contained in the separated bottom mud can be sterilized, and the heavy metals can be detoxified, and the soil particles can be regenerated into the soil particles before the bottom mud. The use range is not limited, and the appearance of a method and treatment agent that can be used as landfill, embankment soil or fertilizer is desired, and industrial wastewater pollutants, that is, industrial metal sludge, or agricultural, livestock, and marine food processing. Similarly, the wastewater polluted during the process can be immediately hydrophobized,
It is expected that a separation treatment agent and a treatment method that can utilize the separated water and bacteria containing the separated solids and the detoxification of heavy metals can be used.

【0005】[0005]

【課題を解決するための手段】本発明者は前記の問題点
を解決すべく鋭意研究の結果、先に2価又は3価の鉄
塩、3価の金属塩に加えてアルカリ土類金属塩を主成分
とする金属塩を含有する水溶液からなる汚泥物類を有効
に浄化分離できる浄化分離処理剤を提案したが、更に研
究を進めた結果、上記の浄化分離処理剤で汚泥物を処理
した後の脱水分離に脱水収納体例えば脱水袋等を用いる
ことにより、極めて容易に汚泥物の脱水、搬送及び保管
ができることを見出し、本発明に到達したものである。
即ち、本発明は2価又は3価の鉄塩、3価の金属塩及び
アルカリ土類金属塩を主成分として、該無機塩を溶媒水
に溶解してなる汚泥物類の浄化分離処理剤、或いはこの
ものに更に五酸化二燐を加えてなる汚泥物類の浄化分離
処理剤を汚泥物類に加え、或いは更に中和剤、高分子凝
集剤を順次添加して汚泥物類を疎水化分離し、ついで脱
水収納体として、外側収納体と内側収納体とからなり、
外側収納体が上部に吊り下げ具、底部に開閉自在の締め
具を有する網状収納体であり、内側収納体が汚泥物を脱
水収納するための有底の布製特に不織布の収納体からな
脱水用収納体を用いて脱水することを特徴とする汚泥
物類の浄化脱水処理方法に関するものである。
Means for Solving the Problems As a result of intensive studies to solve the above-mentioned problems, the present inventor previously found that in addition to a divalent or trivalent iron salt, a trivalent metal salt, an alkaline earth metal salt. We proposed a purification separation treatment agent that can effectively purify and separate sludge consisting of an aqueous solution containing a metal salt containing as a main component, but as a result of further research, sludge was treated with the above purification separation treatment agent. The present invention has been completed by finding that sludge can be dehydrated, transported and stored very easily by using a dehydration container such as a dehydration bag for the subsequent dehydration separation.
That is, the present invention is a purification and separation treatment agent for sludges, which comprises a divalent or trivalent iron salt, a trivalent metal salt and an alkaline earth metal salt as main components, and the inorganic salt dissolved in solvent water, Alternatively, a purification / separation treatment agent for sludges obtained by further adding diphosphorus pentoxide to this is added to the sludges, or a neutralizing agent and a polymer coagulant are sequentially added to the sludges for hydrophobic separation. Then, as a dehydration container, it consists of an outer container and an inner container,
The outer storage body has a hanging tool on the top and an openable and closable tightening on the bottom.
It is a net-shaped container with tools, and the inner container removes sludge.
Do not use a bottomed cloth container for storing water, especially a non-woven cloth container.
The present invention relates to a method for purifying and dehydrating sludge, which is characterized by dehydrating using a dehydrating container .

【0006】本発明の汚泥物類の浄化分離処理剤におい
て、2価及び3価の鉄塩としては硫酸第一鉄、硫酸第二
鉄、塩化第二鉄等が挙げられ、3価の金属塩としては硫
酸アルミニウム〔Al2(SO4)3〕、硫酸アルミニウムカリ
ウム〔AlK(SO4)3〕等である。これらの金属塩は従来汚
泥水処理のための凝集剤として一般に用いられているも
のである。本発明で用いるアルカリ土類金属塩としては
塩化マグネシウム(MgCl2・6H2O)、塩化カルシウム(CaC
l2・2H2O)等である。これらのアルカリ土類金属塩、例え
ばMgCl2・6H2Oは豆腐の凝固剤、寒剤、セメント
原料として、電解法における単体金属の原料であるCa
Cl2は乾燥剤、医薬品として骨格症のカルシウム補結
剤、アレルギー性疾患の治療などに広く使用されている
が、これらアルカリ土類金属塩を底泥や産業廃水の汚濁
物等の汚泥物類の処理剤として用いられた例はなく、こ
れを含む本願発明の浄化分離処理剤は汚泥物類の水と固
形物の分離を容易にし、アルカリ土類金属塩と硫酸アル
ミニウム、塩化第二鉄、硫酸第二鉄等の凝集剤との相剰
効果により汚泥物類が容易に凝結し、吸着固結、乾燥が
短時間に行なうことができる等のすぐれた効果を有する
ものである。
In the sludge purification and separation treatment agent of the present invention, examples of the divalent and trivalent iron salts include ferrous sulfate, ferric sulfate and ferric chloride. Examples thereof include aluminum sulfate [Al 2 (SO 4 ) 3 ], potassium aluminum sulfate [AlK (SO 4 ) 3 ], and the like. These metal salts are conventionally generally used as a flocculant for sludge water treatment. Examples of the alkaline earth metal salt used in the present invention include magnesium chloride (MgCl 2 .6H 2 O) and calcium chloride (CaC
l 2 · 2H 2 O) etc. These alkaline earth metal salts, such as MgCl 2 .6H 2 O, are used as a coagulant for tofu, a freezing agent, and a raw material for cement.
Cl 2 is widely used as a desiccant, a calcium skeletal skeletal medicine as a medicine, and a treatment for allergic diseases. These alkaline earth metal salts are used as sludges such as bottom sludge and industrial wastewater pollutants. There is no example used as a treating agent of the present invention, the purification separation treating agent of the present invention containing this facilitates the separation of water and solids of sludges, alkaline earth metal salts and aluminum sulfate, ferric chloride, It has an excellent effect that sludges easily coagulate due to an additive effect with a coagulant such as ferric sulfate, and adsorption solidification and drying can be performed in a short time.

【0007】本発明では上記の浄化分離処理剤に更に五
酸化二燐(P2O5)を添加したものを浄化分離処理剤とす
ることができる。P25は脱水、ガス乾燥、有機化学で
縮合剤、界面活性剤、医療用には消化、清涼剤として知
られているが、本発明ではこれが汚泥物類の重金属、細
菌の解毒剤、殺菌剤として、又アルカリ性を酸性に中和
する中和剤としても作用することを本発明者が初めて見
出したものである。
In the present invention, the purification / separation treatment agent can be obtained by adding diphosphorus pentoxide (P 2 O 5 ) to the purification / separation treatment agent. P 2 O 5 is known as a condensing agent, a surfactant, and a digestive / cooling agent for medical use in dehydration, gas drying, and organic chemistry, but in the present invention, this is a heavy metal of sludges, an antidote for bacteria, The present inventor has found for the first time that it acts as a bactericidal agent and also as a neutralizing agent for neutralizing alkaline to acidic.

【0008】本発明の浄化分離処理剤の成分の組成割合
は、その処理する汚泥物類の発生源、即ち汚泥物類を構
成する成分や粒度構成比、含水率、pH、温度等により
適宜選択するが、2価又は3価の鉄塩50〜30重量%、3
価の金属塩45〜30重量%、アルカリ土類金属塩30〜3重
量%、及びP251.5〜0.3重量%であることができ、そ
れにより効果的に処理することができる。
The composition ratio of the components of the purification / separation treatment agent of the present invention is appropriately selected depending on the source of the sludge to be treated, that is, the components constituting the sludge, the particle size composition ratio, the water content, the pH, the temperature and the like. However, 50 to 30% by weight of divalent or trivalent iron salt, 3
It can be 45 to 30% by weight of a valent metal salt, 30 to 3% by weight of an alkaline earth metal salt, and 1.5 to 0.3% by weight of P 2 O 5 so that it can be treated effectively.

【0009】本発明においてその主要成分の溶媒水は他
の成分の合計重量の4倍量以上が好ましく、これ以下の
量を使用することもできるが、その場合、各薬品成分同
志が反応することがあって、その作用効果が減少するこ
とがある。汚泥物類に対する浄化分離処理剤の使用量は
特に限定されないが、汚泥物類(含水率10%)1,000l
に対して1〜30l、好ましくは3〜6lである。汚泥物
類の処理に当っては、本発明の浄化分離処理剤で処理し
た後、浄化分離処理剤の正荷電金属塩等によって水中の
水素イオン濃度が上がり、pHが下がり凝集凝結反応が
鈍化するので、中和剤である水酸化カルシウム〔Ca
(OH)2〕、水酸化ナトリウム(NaOH)、酸化マ
グネシウム(MgO)等で処理し、水素イオン濃度を下
げ、pHを上げて凝集凝結反応が円滑に行なわれるよう
にするのである。これらの中和剤は汚泥物類の発生源に
より選択するが、これよりそのpHは約6〜8.6に調
整される。水酸化カルシウムは中和剤として広く利用さ
れ、水酸化ナトリウムは強アルカリ性であって、海水中
の堆積底泥処理に適合する。又MgOは中和剤として、
又亜ヒ酸と不溶性塩を形成するので解毒剤として作用す
るものである。
In the present invention, the solvent water of the main component is preferably at least 4 times the total weight of the other components, and it is also possible to use an amount less than this, but in that case, each chemical component must react. Therefore, the effect may be reduced. The amount of the purification and separation treatment agent used for sludge is not particularly limited, but sludge (water content 10%) 1,000 l
To 1 to 30 liters, preferably 3 to 6 liters. In treating sludge, after treatment with the purification / separation treatment agent of the present invention, the hydrogen ion concentration in water rises due to the positively charged metal salt or the like of the purification / separation treatment agent, the pH decreases, and the coagulation-coagulation reaction slows down. Therefore, the neutralizing agent calcium hydroxide [Ca
(OH) 2 ], sodium hydroxide (NaOH), magnesium oxide (MgO) and the like to lower the hydrogen ion concentration and raise the pH so that the aggregation-condensation reaction can be carried out smoothly. These neutralizing agents are selected according to the source of sludges, and the pH is adjusted to about 6 to 8.6. Calcium hydroxide is widely used as a neutralizing agent, sodium hydroxide is strongly alkaline and is suitable for the treatment of sedimentary sludge in seawater. Also, MgO as a neutralizing agent
It also acts as an antidote because it forms an insoluble salt with arsenous acid.

【0010】又、汚泥物類の処理に当っては、高分子凝
集剤を併用することができる。これにより、汚泥物類粒
子同志の凝集凝結反応をさらに促進させることができ
る。汚泥物類は浄化分離処理剤との相乗作用により急速
に大きなフロックを形成して沈降する。高分子凝集剤は
アニオン、ノニオン、カチオンの各種高分子凝集剤、例
えばアニオンではポリアクリルアマイド系〔ハイモロッ
クSS500、同 OK107(登録商標)(共立有機工業株式会
社)〕、ノニオンではポリアクリルアマイド系〔ハイモ
ロックSS200(登録商標)(共立有機工業株式会社)〕、
カチオンではポリアクリルアマイド系〔ハイモロックMP
173、同Q101、同Q105(登録商標)(共立有機工業株
式会社)〕等が用いられる。
In treating sludges, a polymer flocculant can be used in combination. As a result, the coagulation-condensation reaction of the sludge particles can be further promoted. Sludges rapidly form large flocs and settle due to the synergistic action with the purification and separation treatment agent. The polymer coagulant is an anion, nonion, or cation polymer coagulant, for example, anion is a polyacrylic amide type [HYMOLOCK SS500, the same OK107 (registered trademark) (Kyoritsu Organic Industry Co., Ltd.)], and nonionic is a polyacrylic amide type. Hymoloc SS200 (registered trademark) (Kyoritsu Organic Industry Co., Ltd.)],
For cations, polyacrylic amide type [Himoloc MP
173, Q101, Q105 (registered trademark) (Kyoritsu Organic Industry Co., Ltd.)] and the like are used.

【0011】本発明の汚泥物類の浄化脱水処理方法は、
例えば次のようにして行なわれる。汚泥物類に一定量の
本発明の浄化分離処理剤を加えて混合処理する。これに
より水と固形物の分離が進み、汚泥物類が容易に凝固
し、凝集される。さらに、これに中和剤、ついで高分子
凝集剤を加え、処理物を汚泥物類分離槽で凝集物と水を
分離し、分離固形物を脱水袋を用いてで脱水し固形残留
物(分離土等)を得る。本発明の浄化分離処理剤は有
機、無機、中性淡水中の堆積底泥の処理、金属層細菌を
含む淡水中の堆積底泥の処理、重金属細菌を含む海水中
の堆積底泥の処理等の各種底泥等及び各種産業廃水砕濁
物、即ち工業用各種廃水汚濁物、例えば各種金属スラッ
ジ、農・水・畜産尾種食品加工廃水汚濁物等の汚泥物類
の処理に有効である。
The method for purifying and dehydrating sludges according to the present invention comprises:
For example, it is performed as follows. A certain amount of the purification / separation treatment agent of the present invention is added to sludge and mixed. As a result, water and solids are separated, and sludges are easily solidified and aggregated. Further, a neutralizer and then a polymer flocculant are added to the treated product to separate the flocculate from water in a sludge separation tank, and the separated solid is dehydrated with a dehydration bag to remove solid residue (separation). Get the soil). The purification / separation treatment agent of the present invention is a treatment of sedimentary mud in organic, inorganic or neutral fresh water, treatment of sedimentary mud in fresh water containing metal layer bacteria, treatment of sedimentary mud in seawater containing heavy metal bacteria, etc. It is effective for treating various kinds of bottom mud, etc. and various industrial wastewater suspended matter, that is, various industrial wastewater pollutants such as various sludges such as various metal sludges, agricultural / water / cattle breeding food processing wastewater pollutants.

【0012】又、本発明の脱水用収納体は外側収納体と
内側収納体とからなり、外側収納体が上部に吊り下げ
具、底部に開閉自在の締め具を有する網状収納体であ
り、内側収納体が含水汚泥混合物を脱水収納するための
有底の布製収納体からなる脱水用収納体であり(図
,図,図10)、外側収納体が筒状の網状袋(図
,図)、筒状のカゴ状容器(図,図10)を用い
ることができる。そして、カゴ状容器は、カゴの胴部を
形成する多数の穴を有する長方形の板、その上下に頭部
及び底部を形成する多数の穴を有する1以上の台形板か
らなる合成樹脂製ユニットの胴部長方形板の両側部に設
けられた結合部により複数のユニットを組合わせ組立て
ることからなるもの(図)、或いはカゴの胴部を形成
する多数の穴を有する長方形の板、その上下に頭部及び
底部を形成するための櫛状板からなる合成樹脂製ユニッ
トの胴部長方形板の両側部に設けられた結合部により複
数のユニットを組合わせ組立てることからなるもの等で
ある(図10)。又、内側収納体は合成樹脂製連続長繊
維の不織布からなる筒状の袋、合成樹脂製糸の編物から
なる袋等であり(図,図)、それらは崩壊性又は腐
食性の材質からなるものであることができる。これによ
り更に分離固形物の脱水及び固形残留物の脱水、搬送及
び保管が極めて便利なものとなることを見出した。そし
て、脱水用収納体の外袋である網状物は、例えば筒状の
網状袋からなるものでは引張り強度の大きい合成樹脂
製、例えばナイロン糸等で作成される。この外袋は、汚
泥物類の浄化分離処理剤で処理した疎水化分離処理物の
脱水の際には、該処理物の脱水のために用いる内袋を収
納するため、底部は締め具で閉じ、内側収納体例えば内
袋での脱水が終った後、該底部締め具を開き、外側収納
体を底のない筒状として、収納していた内袋を排出し、
内袋は残留固形物を収納して、搬送され、保管される。
脱水収納体において、内袋は疎水化分離処理物の脱水と
収納或いは保管を同時に行なうことができるものであ
る。内袋は前記の脱水袋と同じ材質からなる不繊布から
なることができる。この内袋は外袋があるので、厚さの
薄い不繊布を用いることができ、そのため脱水効率を更
に上げることができる。そして、外側収納体がカゴ状の
ものであるときは、内袋を更に薄くでき、更により脱水
効果を上げることができる。又内袋が崩壊性又は腐食性
の収納体では、底泥を脱水して土中に長く置くことによ
って土に還えされるので好ましい。
[0012] Also, dehydrating storage body of the present invention is composed of a outer side container and the inner container, instrument suspending outer container at the top, a mesh container having a reclosable fastener at the bottom, An inner container for dewatering and containing the hydrous sludge mixture.
It is a container for dehydration consisting of a bottomed cloth container (Fig. 6 ,
7 , 8 and 10 ), the outer container is a tubular mesh bag (Fig.
6 , FIG. 7 ) and a cylindrical basket-shaped container (FIGS. 8 and 10 ) can be used. The basket-like container is a synthetic resin unit composed of a rectangular plate having a large number of holes forming the body of the basket, and one or more trapezoidal plates having a large number of holes at the top and bottom of the basket. One that consists of assembling multiple units by combining the units provided on both sides of the body rectangular plate (Fig. 8 ), or a rectangular plate with many holes forming the body of the basket A synthetic resin unit for forming a head portion and a bottom portion is formed by combining a plurality of units by combining portions provided on both sides of a rectangular body plate of a body of a synthetic resin unit (FIG. 10 ). ). Further, the inner container is a tubular bag made of synthetic resin continuous long-fiber non-woven fabric, a bag made of synthetic resin yarn knitting, etc. (FIGS. 4 and 5 ), which are made of a collapsible or corrosive material. Can be. It has been found that this further facilitates dehydration of the separated solid and dehydration of the solid residue, transportation and storage. The net-like material, which is the outer bag of the dehydrating container, is made of synthetic resin having a large tensile strength, such as nylon thread, if it is a tubular net-like bag. This outer bag stores the inner bag used for dehydration of the hydrophobized separation-treated product treated with the sludge purification and separation treatment agent, so the bottom is closed with a fastener. After the inner container, for example, the inner bag has been dehydrated, the bottom fastener is opened, the outer container is formed into a bottomless cylinder, and the inner bag stored is discharged.
The inner bag contains residual solid matter, and is transported and stored.
In the dehydrated container, the inner bag is capable of dehydrating and storing or storing the hydrophobized and separated product at the same time. The inner bag may be made of a non-woven cloth made of the same material as the dehydration bag. Since this inner bag has an outer bag, a non-woven cloth having a small thickness can be used, so that the dehydration efficiency can be further improved. When the outer container is basket-shaped, the inner bag can be made thinner, and the dehydration effect can be further enhanced. Further, it is preferable that the inner bag has a collapsible or corrosive container because it can be returned to the soil by dehydrating the bottom mud and placing it in the soil for a long time.

【0013】脱水袋の大きさは汚泥物の疎水化処理のス
ケールに応じて適宜選択することが出来る。本発明の袋
を用いる袋式脱水方法は、他の脱水機や濾過装置を用い
る物に比べて、残留固形物の回収が容易であり、袋に残
留固形物をそのまま入れて、搬送ができ、利用に供する
ことができるので、極めて便利であり、残留固形物の分
離回収利用が言わば一段階で行なうことができるので極
めて効率的である。
The size of the dehydration bag can be appropriately selected according to the scale of the hydrophobizing treatment of sludge. The bag-type dehydration method using the bag of the present invention is easier to collect the residual solid matter as compared with other dehydrators and those using a filtering device, and the residual solid matter is put in the bag as it is, which can be conveyed. It is very convenient because it can be used, and it is extremely efficient because the separation and recovery of residual solids can be performed in one step.

【0014】[0014]

【作用】本発明の汚泥物類の浄化分離処理剤の主要成分
は正荷電の無機金属塩であり、これが汚泥物類を構成す
る負荷電の微粒子と結合し中和し、汚泥物類の固形物、
土微粒子の周囲に付着し、拘束されていた水分子が該粒
子から分離されるとともに、固形物粒子の凝集、凝結反
応により、さらに水分子が押し出され大きな粒子に凝集
されたフロックが形成されるものと考えられる。特に本
発明の浄化分離処理剤はアルカリ土類金属塩を含むた
め、これまでのこの種の汚泥処理剤では最初に補助剤と
しての高分子凝集剤の処理が必要であったが、本発明の
ものではそのような前処理をする必要がなく、有効に親
水コロイド粒子を疎水コロイド粒子とすることができ、
凝集、吸着固結し、固形物塊を形成し、粒子を大きな団
塊とすることができる。さらに消臭作用があり悪臭を消
臭でき、細菌や重金属の殺菌、解毒がなされる。又分離
された水中には混入物がなく、良質の水質のものとな
り、分離された底泥からの土は保水性が低下し、透水性
が高く、埋立用土、盛土用土として利用でき、又工業廃
水からのもの、例えば金属スラッジから得られる固形物
は窯業用添加剤として利用が可能などそれぞれ種々の利
用が可能となるなど汚泥の種類に応じてそれぞれの分野
での利用が可能である。そして、浄化分離処理剤での汚
泥の疎水化処理の後の脱水工程において、袋式脱水処理
を行なうため、残留固形物の分離回収、収納が一工程で
処理でき、残留固形物の搬送も容易でその利用を円滑に
行なうことができる。
The main component of the sludge purification and separation treatment agent of the present invention is a positively charged inorganic metal salt, which binds and neutralizes negatively charged fine particles constituting the sludge to solidify the sludge. object,
Water molecules attached around the soil fine particles and bound are separated from the particles, and due to the agglomeration / condensation reaction of solid particles, water molecules are further extruded to form flocs agglomerated into large particles. It is considered to be a thing. In particular, since the purification / separation treatment agent of the present invention contains an alkaline earth metal salt, the sludge treatment agents of this type heretofore required the treatment of the polymer flocculant as an auxiliary agent first. However, the hydrophilic colloid particles can be effectively converted into the hydrophobic colloid particles without the need for such pretreatment.
Agglomeration, adsorption and solidification to form a solid mass, and the particles can be made into a large agglomerate. In addition, it has a deodorizing effect and can remove bad odors, and sterilizes and detoxifies bacteria and heavy metals. In addition, there is no contaminant in the separated water, and the quality of the water is good. The soil from the separated bottom mud has low water retention and high water permeability, and can be used as landfill and embankment soil. The solid matter obtained from wastewater, for example, the solid matter obtained from metal sludge can be used as an additive for the ceramic industry, and various uses are possible. For example, the solid matter can be used in each field depending on the type of sludge. In the dehydration step after the sludge's hydrophobic treatment with the purification / separation treatment agent, the bag-type dehydration treatment is performed, so that the separation and collection and storage of the residual solids can be performed in one step, and the transportation of the residual solids is easy. Can be used smoothly.

【0015】[0015]

【実施例】以下に実施例で本発明を説明するが、本発明
はこれらに限定されるものでないことは言うまでもな
い。具体的に用いた本発明の浄化分離処理剤の溶媒水1
l中の成分の配合量(配合割合)及び汚泥物類の処理に
当っての処理剤の添加順序を第1表に示す。なお、第1
表において、実施例1は有機、無機、中性淡水中の堆積
底泥、実施例2は重金属細菌を含む淡水中の堆積底泥、
の処理用を示し、比は比較例(特開昭62−27719
9号に相当するもの)を示し、実施例1と同一の底泥を
処理したものである。
EXAMPLES The present invention will be described below with reference to examples, but it goes without saying that the present invention is not limited to these. Solvent water of the purification and separation treatment agent of the present invention used specifically 1
Table 1 shows the blending amounts (blending ratios) of the components in 1 and the order of addition of the treating agents in treating sludges. The first
In the table, Example 1 is organic, inorganic, sedimentary mud in neutral fresh water, Example 2 is sedimentary mud in fresh water containing heavy metal bacteria,
Of the comparative example (JP-A-62-27719).
(Corresponding to No. 9) is shown, and the same bottom mud as in Example 1 is treated.

【0016】処理方法は以下のとおりである。 (1)底泥:産業排水等の汚泥物類を処理槽に入れ、
浄化分離処理剤を原液1.0m3当り、約2.0〜8.0lを投
入して、15〜30秒間撹拌し、疎水化する。この撹拌によ
り、相乗効果が発揮され、イオン交換が為され、嫌気性
細菌が好気性にかわり、悪臭が消除される。これに、
中和剤を約2.0〜8.0l投入し、約15〜30秒間撹拌し、p
Hを5.8〜8.6の範囲内に調節する。次いで凝集剤(カ
チオン性又はアニオン性)を加え、約20〜30秒間撹拌す
る。疎水化された固形分は凝集体を形成して沈殿する。
更に必要により、凝集剤(アニオン性又はノニオン
性)を投入して約30〜60秒間撹拌すると、既に形成され
た凝集体固形物は更に大きな凝集体(5〜20mm)とな
り固さを増して、沈殿する。即ち疎水化された凝集体は
大きさを増し、脱水性が容易となる。この処理された混
合物のpHは環境基準内に調整される。次いで、袋詰め
機に脱水袋(ポリプレピロンの連続長繊維の不織布で製
造した袋或いは合成樹脂製の糸で編んだ袋)を置き、そ
れに、凝集処理された水濁物を投入し脱水処理する。脱
水原液の凝集状態によって、上記工程終了後、脱水工
程に付してもよい。脱水袋で脱水した分離液は放流し、
袋中には残留固形物が収納され、そのまま袋の口を締め
て、保管し、各種適当な分野への再利用が行なわれる。
The processing method is as follows. (1) Bottom mud: Put sludge such as industrial wastewater in the treatment tank,
About 2.0 to 8.0 l of the purification and separation treatment agent is added per 1.0 m 3 of the stock solution, and the mixture is stirred for 15 to 30 seconds to make it hydrophobic. By this agitation, a synergistic effect is exerted, ion exchange is performed, anaerobic bacteria are changed to aerobic, and malodor is eliminated. to this,
Add about 2.0 to 8.0 liters of neutralizing agent, stir for about 15 to 30 seconds, and p
Adjust H to within 5.8-8.6. The flocculant (cationic or anionic) is then added and stirred for about 20-30 seconds. The hydrophobized solids form aggregates and precipitate.
Further, if necessary, by adding a flocculant (anionic or nonionic) and stirring for about 30 to 60 seconds, the already formed aggregate solid matter becomes a larger aggregate (5 to 20 mm) to increase the hardness, Settle. That is, the hydrophobized aggregates increase in size and are easily dehydrated. The pH of this treated mixture is adjusted within environmental standards. Then, a dehydration bag (a bag made of a continuous long-fiber non-woven fabric of polyprepyrone or a bag knitted with a thread made of synthetic resin) is placed in a bag-filling machine, and the agglomerated water suspended matter is put therein and dehydrated. Depending on the aggregation state of the dehydrated stock solution, the dehydrated step may be performed after the above steps. The separated liquid dehydrated in the dehydration bag is discharged,
Residual solids are stored in the bag, and the bag is closed as it is, stored, and reused in various appropriate fields.

【0017】(2)図1に示す汚泥物類の浄化脱水装置
において、反応タンク1に底泥物を入れ、撹拌機2(モ
ーター11で駆動)でかきまぜながら、疎水化処理剤を
投入口3より前記(1)と同様に底泥物1.0m3当り約2.
0〜8.0l投入し、約15〜30秒間かきまぜ、中和剤(水酸
化ルシウム)を入れ約15〜30秒間かきまぜ、pH5.8〜
8.6以内に調整する。次いで高分子凝集剤(カチオン性
又はアニオン性)を混入し、約20〜30秒間撹拌し既に疎
水化されている固形分が凝集体を形成して沈殿する。更
に必要により凝集体を更に大きな凝集体とするために高
分子凝集剤(アニオン性又はノニオン性)を投入し、約
30〜60秒間撹拌する。凝集体は5〜20mmの大きさのも
のとなり、脱水が容易となる。次いで反応タンク1の下
部にある弁4を開き、モノポンプ5(モーター12で駆
動)を通して、袋固定機6にある孔明きプレート7を通
して脱水袋8に入れ、脱水する。孔明きプレート7は脱
水袋8に入れる前に大量の水を分離する役目をするもの
である。脱水袋の下部にも孔明きプレート9が置かれ袋
中の水が排出される。脱水袋8での脱水は極めて短時間
で行なわれる。脱水完了後、脱水袋8は移動滑車10に
より搬出される。
(2) In the sludge purification and dewatering apparatus shown in FIG. 1, the bottom sludge is put in the reaction tank 1 and the agitator 2 (driven by the motor 11) is stirred and the hydrophobic treatment agent is introduced into the inlet 3 more (1) Like the sediment was 1.0 m 3 per about 2.
Add 0 to 8.0 liters, stir for about 15 to 30 seconds, add a neutralizer (lucium hydroxide) and stir for about 15 to 30 seconds, pH 5.8 to
Adjust within 8.6. Next, a polymer flocculant (cationic or anionic) is mixed in, and the mixture is stirred for about 20 to 30 seconds, and the already hydrophobized solids form aggregates and precipitate. If necessary, a polymer flocculant (anionic or nonionic) is added to make the agglomerates larger, and
Stir for 30-60 seconds. The aggregates have a size of 5 to 20 mm, which facilitates dehydration. Next, the valve 4 at the lower part of the reaction tank 1 is opened, and the dehydration bag 8 is put through the mono pump 5 (driven by the motor 12) and the perforated plate 7 in the bag fixing machine 6 for dehydration. The perforated plate 7 serves to separate a large amount of water before putting it in the dehydration bag 8. The perforated plate 9 is also placed under the dehydration bag to drain the water in the bag. Dehydration in the dehydration bag 8 is performed in an extremely short time. After the dehydration is completed, the dehydration bag 8 is carried out by the movable pulley 10.

【0018】本発明の脱水袋8は図2〜図11に示すと
おりである。この脱水袋8は外側収納体8’と内側収納
体8”からなる脱水袋であり、図は網状外側収納体
8’を開いた状態の摸式図であり、図は外側収納体
8’を閉じた状態の模式図である。又図は開いた状態
の内側収納体8”であり、図は閉じた状態の内側収納
体8”である。図は外側収納体8’に内側収納体8”
を入れ脱水する際の模式図である。図に示すように、
網状の開いた状態の外側収納体8’に開いた状態の内側
収納体8”を入れ、外側収納体底部の引き絞りひも14
を引き締めて内側収納体8”を外側収納体8’内に収納
し吊り下げ具13で吊り下げた状態にし、浄化処理され
た含水混合物をその口から内側収納体8”に入れて脱水
し、脱水された残留固形物は内側収納体8”に入ったま
ま外側収納体8’の底部を開いて外袋より取出され、保
管あるいは搬送される。図は網状外側収納体8’の吊
り下げ具13が外側収納体8’の胴部中間部に設けられ
ている図である。図及び図10はカゴ状外側収納体
8’であり、これらはそれぞれ図及び図11に示す合
成樹脂製ユニットを数枚組合わせ組立てられたものであ
り、これにより上記同様に含水混合物が脱水され、保管
あるいは搬送される。本発明の処理方法により、得られ
た結果を表2に示す。
The dewatering bag 8 of the present invention is shown in FIGS. 2 to 11. This dehydration bag 8 is a dehydration bag composed of an outer storage body 8'and an inner storage body 8 ". Fig. 2 is a schematic view of the mesh outer storage body 8'in an open state, and Fig. 3 is an outer storage body 8". 'is a schematic diagram of a closed state. Matazu 4 ", and 5 the inner container 8 in the closed position" state of the inner container 8 opened a. FIG. 6 is an outer container 8' Inner storage 8 "
It is a schematic diagram at the time of putting and dehydrating. As shown in FIG. 6,
Put the inner storage body 8 ″ in the open state in the net-shaped outer storage body 8 ′, and pull the draw string 14 at the bottom of the outer storage body.
The inner container 8 ″ is stored in the outer container 8 ′ and is hung by the suspending tool 13, and the purified water-containing mixture is put into the inner container 8 ″ from its mouth to be dehydrated, The dehydrated residual solids are taken out from the outer bag by opening the bottom of the outer container 8'while remaining inside the inner container 8 "and stored or transported. Fig. 7 shows the hanging of the mesh outer container 8 '. It is a figure in which ingredient 13 is provided in the trunk middle part of outside storage object 8 '. Drawing 8 and Drawing 10 are basket-like outside storage object 8', and these are the synthetic resin shown in Drawing 9 and Drawing 11 , respectively. A plurality of manufacturing units are assembled and assembled, whereby the water-containing mixture is dehydrated and stored or transported in the same manner as described above.Table 2 shows the results obtained by the treatment method of the present invention.

【0019】[0019]

【表1】 [Table 1]

【0020】[0020]

【表2−1】 [Table 2-1]

【0021】[0021]

【0022】[0022]

【表2−2】 [Table 2-2]

【0023】[0023]

【発明の効果】本発明の汚泥物類の浄化分離処理剤によ
り、ダム、湖沼、河川、海底等の底泥、工業、或いは農
・水・畜産物食品加工の際の各種廃水汚濁物等の汚泥物
類の脱水が極めて短時間にでき、得られた分離土等の固
形物は再泥化(液状化)せず、例えば底泥処理の場合は
底泥前の土粒子に再生できる。そして本発明では脱水に
脱水袋を使用するため、脱水された残留固形物の乾燥が
早く、雨水にかかっても泥流化しない。脱水操作が簡単
で、脱水と残留固形物の収納或いは梱包が一段階で出
来、又利用のための搬送が容易という利点を有する。更
に脱水袋を網状の外袋と不繊布からなる内袋とからなる
ものとすることにより、脱水処理、保管、搬送が一層容
易となる。脱水袋で脱水できるのは本発明の特定の浄化
分離処理剤を使用することによってのみ得られ、従来の
疎水化剤では脱水袋での脱水は出来ず、この脱水方法は
処理剤との組合せの効果と言うことができる。又、本発
明の浄化分離処理剤は汚泥物類特有の悪臭を消臭又は脱
臭し得、含有する細菌の殺菌、重金属の解毒をも可能に
し、得られた残留固形物はその構成成分に応じて再利用
が可能であり、例えば底泥からの分離土は埋立用土、盛
土用土、農耕地の土壌改良材として、又金属スラッジ、
或いはスラリーからの残留固形物の場合は窯業用の添加
物として利用でき、分離水は湖沼、河川、海等に戻し、
水資源として供することが可能であると言う極めて優れ
た効果が奏せられる。
EFFECT OF THE INVENTION The sludge purification and separation treatment agent according to the present invention can be used to remove various types of wastewater pollutants such as dams, lakes, rivers, seabeds, industrial mud, agricultural, water and livestock products. The sludge can be dehydrated in an extremely short time, and the obtained solid matter such as separated soil is not re-slurried (liquefied), and for example, in the case of bottom sludge treatment, it can be regenerated into soil particles before the bottom sludge. Further, in the present invention, since a dehydration bag is used for dehydration, the dehydrated residual solid matter is dried quickly and does not form a mud stream even when it is exposed to rainwater. It has the advantages that the dehydration operation is simple, the dehydration and the storage or packing of the residual solids can be done in one step, and the transport for use is easy. Further, by forming the dehydration bag from the net-like outer bag and the inner bag made of non-woven cloth, the dehydration treatment, storage and transportation are further facilitated. Dehydration in a dehydration bag can be obtained only by using the specific purification / separation treatment agent of the present invention, and dehydration in a dehydration bag cannot be performed with a conventional hydrophobizing agent. It can be said to be an effect. Further, the purification / separation treatment agent of the present invention can deodorize or deodorize the bad odor peculiar to sludges, and also enables the sterilization of contained bacteria and the detoxification of heavy metals, and the obtained residual solid matter depends on its constituent components. It is possible to reuse as a soil improvement material for landfill soil, embankment soil, agricultural land, metal sludge,
Or, in the case of residual solids from the slurry, it can be used as an additive for the ceramic industry, and the separated water is returned to lakes, rivers, the sea, etc.
It has an extremely excellent effect that it can be used as a water resource.

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

【図1】本発明の汚泥物類の袋式脱水処理のための装置
の模式図である。
FIG. 1 is a schematic view of an apparatus for bag-type dehydration treatment of sludge according to the present invention.

【図】本発明の汚泥物類の脱水袋の開いた状態の外袋
の模式図である。
FIG. 2 is a schematic view of the outer bag of the present invention in which the sludge dewatering bag is open.

【図】本発明の汚泥物類の脱水袋の閉じた状態の外袋
の模式図である。
FIG. 3 is a schematic view of the outer bag of the sludge dewatering bag of the present invention in a closed state.

【図】本発明の汚泥物類の脱水袋の開いた状態の内袋
の模式図である。
FIG. 4 is a schematic view of an inner bag of the sludge dewatering bag of the present invention in an open state.

【図】本発明の汚泥物類の脱水袋の閉じた状態の内袋
の模式図である。
FIG. 5 is a schematic view of the inner bag of the sludge dewatering bag of the present invention in a closed state.

【図】本発明の汚泥物類の脱水用収納体において、網
状外側収納体に内側収納体である内袋を入れた脱水用収
納体の一模式図である。
[Fig. 6 ] Fig. 6 is a schematic view of a dewatering container for the sludge dewatering of the present invention, in which an inner bag as an inner container is placed in a mesh outer container.

【図】本発明の汚泥物類の脱水用収納体において、網
状外側収納体に内側収納体である内袋を入れた脱水用収
納体の一模式図である。
FIG. 7 is a schematic diagram of a dewatering container for sludges according to the present invention, in which an inner bag, which is an inner container, is placed in a net-shaped outer container.

【図】本発明の汚泥物類の脱水用収納体において、カ
ゴ状外側収納体に内側収納体である内袋を入れた脱水用
収納体の一模式図である。
[Fig. 8 ] Fig. 8 is a schematic view of a dewatering container for the sludge dewatering according to the present invention in which an inner bag as an inner container is placed in a basket-shaped outer container.

【図】本発明の汚泥物類の脱水用収納体において、カ
ゴ状外側収納体を組立てるための一つのユニットの展開
図である。
FIG. 9 is a development view of one unit for assembling the basket-shaped outer storage body in the storage body for dewatering sludges of the present invention.

【図10】本発明の汚泥物類の脱水用収納体において、
カゴ状外側収納体に内側収納体である内袋を入れた脱水
用収納体の一模式図である。
FIG. 10 shows a sludge dewatering container according to the present invention,
It is a schematic diagram of a dewatering container in which an inner bag as an inner container is put in a basket-shaped outer container.

【図11】本発明の汚泥物類の脱水用収納体において、
カゴ状外側収納体を組立てるための一つのユニットの展
開図である。
FIG. 11 shows a storage body for dehydrating sludge of the present invention,
It is a development view of one unit for assembling a basket-like outer side storage body.

【符号の説明】[Explanation of symbols]

1.反応タンク 2.撹拌機 3.投入口 4.弁 5.モノポンプ 6.袋固定機 7.孔明きプレート 8.脱水袋 8’.脱水袋の外袋 8''.脱水袋の内袋 9.孔明きプレート 10.移動滑車 11.撹拌機用モーター 12.モノポンプ用モーター 13.吊り下げ具 14.引き絞りひも 15.カゴの穴 16.ユニット結合部 17.結合棒 18.ロープ固定具 19.引き絞り紐穴 1. Reaction tank 2. Stirrer 3. Input port 4. Valve 5. Mono pump 6. Bag fixing machine 7. Perforated plate 8. Dehydration bag 8 '. Outer bag of dehydration bag 8 ″. Inner bag of dehydration bag 9. Perforated plate 10. Mobile pulley 11. Stirrer motor 12. Motor for mono pump 13. Hanging tool 14. Drawstring 15. Basket hole 16. Unit connection part 17. Connecting rod 18. Rope fixing device 19. Drawstring string hole

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C02F 11/12 C 7446−4D D 7446−4D ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location C02F 11/12 C 7446-4D D 7446-4D

Claims (3)

【特許請求の範囲】[Claims] 【請求項1】2価又は3価の鉄塩、3価の金属塩及びア
ルカリ土類金属塩を主成分として、該無機塩を溶媒水に
溶解してなる汚泥物類の浄化分離処理剤を汚泥物類に加
え、該汚泥物類を疎水化分離し、次いで外側収納体と内
側収納体とからなり、外側収納体が上部に吊り下げ具、
底部に開閉自在の締め具を有する網状収納体であり、内
側収納体が汚泥物を脱水収納するための有底の布製収納
体からなる脱水用収納体を用いて脱水処理することを特
徴とする汚泥物類の浄化脱水処理方法。
1. A purifying / separating agent for sludges, which comprises a divalent or trivalent iron salt, a trivalent metal salt and an alkaline earth metal salt as a main component and the inorganic salt dissolved in solvent water. In addition to sludges, the sludges are hydrophobized and separated, and then the outer container and the inner
It consists of the side storage body, the outer storage body is a hanging tool on the top,
It is a net-shaped storage body that has a fastener that can be opened and closed at the bottom.
A bottomed cloth storage for the side storage to dewater sludge.
A method for purifying and dehydrating sludges, which comprises performing dehydration treatment using a dehydration storage body comprising a body.
【請求項2】請求項1記載の浄化分離処理剤に更に五酸
化二燐を加えてなる浄化分離処理剤を用いる請求項1記
載の汚泥物類の浄化脱水処理方法。
2. The method for purifying and dehydrating sludge according to claim 1, wherein the purifying and separating treating agent obtained by adding diphosphorus pentoxide to the purifying and separating treating agent according to claim 1 is used.
【請求項3】請求項1又は2記載の浄化分離処理剤を汚
泥物類に添加処理し、次いで中和剤さらに高分子凝集剤
を添加して汚泥物類を疎水化分離し、次いで請求項1記
載の脱水用収納体を用いて脱水処理することを特徴とす
る汚泥物類の浄化脱水処理方法。 【請求項】 外側収納体が筒状の網状袋からなるもの
である請求項1記載の汚泥物類の浄化脱水処理方法。 【請求項】 外側収納体が筒状のカゴ状容器からなる
ものである請求項1記載の汚泥物類の浄化脱水処理方
法。 【請求項】 内側収納体が合成樹脂製連続長繊維の不
織布からなる筒状の袋からなるものである請求項1記載
の汚泥物類の浄化脱水処理方法。 【請求項】 内側収納体が合成樹脂製糸の編物からな
る袋からなるものである請求項1記載の汚泥物類の浄化
脱水処理方法。 【請求項】 内側収納体が崩壊性又は腐食性の材質か
らなる袋からなるものである請求項1記載の汚泥物類の
浄化脱水処理方法。
3. A purification separation treatment agent according to claim 1 or 2, wherein the addition process on sludge material such, then the sludge was such separated hydrophobic by adding a neutralizing agent further polymer flocculant, followed claim 1 notes
Purification dehydration method of the sludge product class, characterized in that the dehydration process by using a dehydrating container mounting. 4. The method for purifying and dehydrating sludges according to claim 1, wherein the outer container is a tubular mesh bag. 5. The method for purifying and dehydrating sludge according to claim 1, wherein the outer container is a cylindrical basket-shaped container. 6. The method for purifying and dehydrating sludges according to claim 1, wherein the inner container is a tubular bag made of a synthetic resin continuous long-fiber non-woven fabric. 7. A cleaning dehydration method of the sludge product such claim 1, wherein the inner container is made of a bag made from knitted fabric of synthetic resin reeling. 8. The method for purifying and dehydrating sludge according to claim 1, wherein the inner container is a bag made of a disintegrating or corrosive material.
JP4097724A 1991-04-17 1992-04-17 Bag-type dehydration method for sludge Expired - Fee Related JPH0775720B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4097724A JPH0775720B2 (en) 1991-04-17 1992-04-17 Bag-type dehydration method for sludge

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
JP8523091 1991-04-17
JP3-190088 1991-07-30
JP3-85230 1991-07-30
JP19008891 1991-07-30
JP4097724A JPH0775720B2 (en) 1991-04-17 1992-04-17 Bag-type dehydration method for sludge

Publications (2)

Publication Number Publication Date
JPH05220500A JPH05220500A (en) 1993-08-31
JPH0775720B2 true JPH0775720B2 (en) 1995-08-16

Family

ID=27304799

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4097724A Expired - Fee Related JPH0775720B2 (en) 1991-04-17 1992-04-17 Bag-type dehydration method for sludge

Country Status (1)

Country Link
JP (1) JPH0775720B2 (en)

Families Citing this family (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4166510B2 (en) * 2002-06-07 2008-10-15 住友林業株式会社 Cement cleaning water purification method and purifying bag body
JP4828378B2 (en) * 2005-11-08 2011-11-30 株式会社錢高組 Powdered muddy water treatment agent, muddy water dewatering method, and muddy water volume reducing treatment device
JP4964083B2 (en) * 2007-10-09 2012-06-27 株式会社ファーストソリューション Mud processing equipment
JP5144420B2 (en) * 2008-07-31 2013-02-13 株式会社クリタス Method for dewatering sludge accumulated in storage tanks of human waste treatment facilities
JP2016036798A (en) * 2014-08-11 2016-03-22 志郎 中村 Dewatering bag and dewatering apparatus using the same
CN113354075A (en) * 2020-03-04 2021-09-07 湘西科亮环保科技有限公司 Block-based treatment system for medical sewage and sludge
CN119504102A (en) * 2024-12-24 2025-02-25 南京齐超环保科技有限公司 A sludge dehydration and solidification treatment device

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH02122900A (en) * 1988-11-02 1990-05-10 Sakae Hatayama Treating agent for dehydrating, coagulating and stabilizing mud and dehydrating, coagulating and stabilizing treatment of mud
JPH0677759B2 (en) * 1988-12-09 1994-10-05 株式会社ゲット Sludge treatment method

Also Published As

Publication number Publication date
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