JPH02284700A - Treating agent for purifying and separating sludge - Google Patents
Treating agent for purifying and separating sludgeInfo
- Publication number
- JPH02284700A JPH02284700A JP2012734A JP1273490A JPH02284700A JP H02284700 A JPH02284700 A JP H02284700A JP 2012734 A JP2012734 A JP 2012734A JP 1273490 A JP1273490 A JP 1273490A JP H02284700 A JPH02284700 A JP H02284700A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- agent
- purification
- purifying
- separating
- 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.)
- Granted
Links
- 239000003795 chemical substances by application Substances 0.000 title claims abstract description 58
- 239000010802 sludge Substances 0.000 title claims description 80
- 229910052751 metal Inorganic materials 0.000 claims abstract description 19
- 239000002184 metal Substances 0.000 claims abstract description 19
- 150000003839 salts Chemical class 0.000 claims abstract description 19
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims abstract description 13
- TWRXJAOTZQYOKJ-UHFFFAOYSA-L Magnesium chloride Chemical compound [Mg+2].[Cl-].[Cl-] TWRXJAOTZQYOKJ-UHFFFAOYSA-L 0.000 claims abstract description 6
- DLYUQMMRRRQYAE-UHFFFAOYSA-N tetraphosphorus decaoxide Chemical compound O1P(O2)(=O)OP3(=O)OP1(=O)OP2(=O)O3 DLYUQMMRRRQYAE-UHFFFAOYSA-N 0.000 claims abstract description 5
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 claims abstract description 3
- 239000001110 calcium chloride Substances 0.000 claims abstract description 3
- 229910001628 calcium chloride Inorganic materials 0.000 claims abstract description 3
- 229910001629 magnesium chloride Inorganic materials 0.000 claims abstract description 3
- 238000000926 separation method Methods 0.000 claims description 35
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 35
- 238000000746 purification Methods 0.000 claims description 30
- -1 alkaline earth metal salts Chemical class 0.000 claims description 13
- 239000003344 environmental pollutant Substances 0.000 claims description 13
- 231100000719 pollutant Toxicity 0.000 claims description 13
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 claims description 12
- 229920000642 polymer Polymers 0.000 claims description 12
- 239000010842 industrial wastewater Substances 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 11
- 230000003472 neutralizing effect Effects 0.000 claims description 10
- 159000000014 iron salts Chemical class 0.000 claims description 6
- 239000002904 solvent Substances 0.000 claims description 5
- 239000000395 magnesium oxide Substances 0.000 claims description 4
- CPLXHLVBOLITMK-UHFFFAOYSA-N magnesium oxide Inorganic materials [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 claims description 4
- AXZKOIWUVFPNLO-UHFFFAOYSA-N magnesium;oxygen(2-) Chemical compound [O-2].[Mg+2] AXZKOIWUVFPNLO-UHFFFAOYSA-N 0.000 claims description 4
- 239000000203 mixture Substances 0.000 claims description 4
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 3
- 239000000920 calcium hydroxide Substances 0.000 claims description 3
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 3
- 238000001035 drying Methods 0.000 abstract description 5
- 238000001179 sorption measurement Methods 0.000 abstract description 2
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 abstract 4
- 150000001342 alkaline earth metals Chemical class 0.000 abstract 2
- 229910052742 iron Inorganic materials 0.000 abstract 2
- 239000007787 solid Substances 0.000 description 14
- 239000002245 particle Substances 0.000 description 12
- 241000894006 Bacteria Species 0.000 description 11
- 239000002689 soil Substances 0.000 description 10
- 229910001385 heavy metal Inorganic materials 0.000 description 9
- 239000013049 sediment Substances 0.000 description 9
- 238000005345 coagulation Methods 0.000 description 7
- 230000015271 coagulation Effects 0.000 description 7
- 239000002351 wastewater Substances 0.000 description 7
- 230000000694 effects Effects 0.000 description 6
- 235000019645 odor Nutrition 0.000 description 6
- 238000006243 chemical reaction Methods 0.000 description 4
- 238000006297 dehydration reaction Methods 0.000 description 4
- 239000008394 flocculating agent Substances 0.000 description 4
- 235000013305 food Nutrition 0.000 description 4
- 239000013505 freshwater Substances 0.000 description 4
- 239000000126 substance Substances 0.000 description 4
- 239000004568 cement Substances 0.000 description 3
- 239000010419 fine particle Substances 0.000 description 3
- 230000002209 hydrophobic effect Effects 0.000 description 3
- 244000144972 livestock Species 0.000 description 3
- 239000000463 material Substances 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- 239000013535 sea water Substances 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 208000005156 Dehydration Diseases 0.000 description 2
- 229910021578 Iron(III) chloride Inorganic materials 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- DIZPMCHEQGEION-UHFFFAOYSA-H aluminium sulfate (anhydrous) Chemical compound [Al+3].[Al+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O DIZPMCHEQGEION-UHFFFAOYSA-H 0.000 description 2
- 239000007864 aqueous solution Substances 0.000 description 2
- 239000011575 calcium Substances 0.000 description 2
- 239000000919 ceramic Substances 0.000 description 2
- 239000000084 colloidal system Substances 0.000 description 2
- 230000000052 comparative effect Effects 0.000 description 2
- 230000007423 decrease Effects 0.000 description 2
- 230000018044 dehydration Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- PCHJSUWPFVWCPO-UHFFFAOYSA-N gold Chemical compound [Au] PCHJSUWPFVWCPO-UHFFFAOYSA-N 0.000 description 2
- 239000010931 gold Substances 0.000 description 2
- 229910052737 gold Inorganic materials 0.000 description 2
- GPRLSGONYQIRFK-UHFFFAOYSA-N hydron Chemical compound [H+] GPRLSGONYQIRFK-UHFFFAOYSA-N 0.000 description 2
- RBTARNINKXHZNM-UHFFFAOYSA-K iron trichloride Chemical compound Cl[Fe](Cl)Cl RBTARNINKXHZNM-UHFFFAOYSA-K 0.000 description 2
- RUTXIHLAWFEWGM-UHFFFAOYSA-H iron(3+) sulfate Chemical compound [Fe+3].[Fe+3].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O RUTXIHLAWFEWGM-UHFFFAOYSA-H 0.000 description 2
- 229910000360 iron(III) sulfate Inorganic materials 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 230000007935 neutral effect Effects 0.000 description 2
- 229920002401 polyacrylamide Polymers 0.000 description 2
- 230000002195 synergetic effect Effects 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 241001098054 Pollachius pollachius Species 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 238000005054 agglomeration Methods 0.000 description 1
- 230000002776 aggregation Effects 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 208000026935 allergic disease Diseases 0.000 description 1
- 229940103272 aluminum potassium sulfate Drugs 0.000 description 1
- DKFCNIGGENJIJN-UHFFFAOYSA-L aluminum;iron(2+);sulfate Chemical compound [Al+3].[Fe+2].[O-]S([O-])(=O)=O DKFCNIGGENJIJN-UHFFFAOYSA-L 0.000 description 1
- 125000000129 anionic group Chemical group 0.000 description 1
- 239000000729 antidote Substances 0.000 description 1
- GCPXMJHSNVMWNM-UHFFFAOYSA-N arsenous acid Chemical compound O[As](O)O GCPXMJHSNVMWNM-UHFFFAOYSA-N 0.000 description 1
- 239000012752 auxiliary agent Substances 0.000 description 1
- 235000013527 bean curd Nutrition 0.000 description 1
- 238000005452 bending Methods 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 239000010796 biological waste Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 150000001720 carbohydrates Chemical class 0.000 description 1
- 235000014633 carbohydrates Nutrition 0.000 description 1
- 229920006317 cationic polymer Polymers 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 239000000701 coagulant Substances 0.000 description 1
- 230000001112 coagulating effect Effects 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 239000002826 coolant Substances 0.000 description 1
- 230000001877 deodorizing effect Effects 0.000 description 1
- 239000002274 desiccant Substances 0.000 description 1
- 239000000645 desinfectant Substances 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 235000014113 dietary fatty acids Nutrition 0.000 description 1
- 230000029087 digestion Effects 0.000 description 1
- 201000010099 disease Diseases 0.000 description 1
- 208000037265 diseases, disorders, signs and symptoms Diseases 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
- 239000000194 fatty acid Substances 0.000 description 1
- 229930195729 fatty acid Natural products 0.000 description 1
- 150000004665 fatty acids Chemical class 0.000 description 1
- 239000011790 ferrous sulphate Substances 0.000 description 1
- 235000003891 ferrous sulphate Nutrition 0.000 description 1
- 239000003337 fertilizer Substances 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 150000002505 iron Chemical class 0.000 description 1
- BAUYGSIQEAFULO-UHFFFAOYSA-L iron(2+) sulfate (anhydrous) Chemical compound [Fe+2].[O-]S([O-])(=O)=O BAUYGSIQEAFULO-UHFFFAOYSA-L 0.000 description 1
- 229910000359 iron(II) sulfate Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 239000011777 magnesium Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- GRLPQNLYRHEGIJ-UHFFFAOYSA-J potassium aluminium sulfate Chemical compound [Al+3].[K+].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O GRLPQNLYRHEGIJ-UHFFFAOYSA-J 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 238000003672 processing method Methods 0.000 description 1
- 235000018102 proteins Nutrition 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 235000014102 seafood Nutrition 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000007711 solidification Methods 0.000 description 1
- 230000008023 solidification Effects 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 239000004094 surface-active agent Substances 0.000 description 1
- 235000019465 surimi Nutrition 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
Abstract
Description
【発明の詳細な説明】
〔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
7′1.泥、汚濁物、赤潮、n粉等、又産業廃水の汚濁
物類、即ち水産、M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
濁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、それぞれを有効
に利用可能とするlη泥物類の浄化分離処理剤及び該浄
化分離処理剤を用いた汚泥物類の浄化分離方法に関する
。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention is applicable to dams, lakes, rivers, seabed sediments and 7'1. Hydrophilicity of pollutants such as mud, pollutants, red tide, n-powder, etc., and pollutants of industrial wastewater, such as wastewater from fisheries, M-products, and agricultural food processing, or industrial wastewater, such as metal sludge or slurry. A purification and separation treatment agent for sludge that hydrophobizes colloidal particles, separates and dehydrates water molecules to form residual solids and separated water, and makes each of them available for effective use, and sludge using the purification and separation treatment agent. Concerning purification and separation methods of
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1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のであ
る。Sludge such as sedimentary bottom sludge from lakes, rivers, and the ocean floor, and industrial wastewater pollutants generally contain organic substances such as proteins, carbohydrates, and fatty acids, inorganic substances, and bacteria, and fine particles of 1 micron or angstrom units of organic or inorganic substances. It is composed of fine particles, which exist in colloidal form in water, and many of them are hydrophilic, making their removal and separation difficult.
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は圧密を
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どする方法。Conventionally, methods for purifying and separating sludge, such as sludge deposited in lakes, rivers, and the seabed, or industrial wastewater pollutants, have been used to separate water and solidify the residue. , ■ Solar drying treatment, which takes a long period of time in a landfill, then consolidates and waits for natural dewatering until it meets the purpose of use, ■ Mechanical dewatering treatment, which solidifies the mud by forcibly dewatering it with a dewatering machine. How to get things done.
■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、02価又は3価の鉄塩と3価の金
属塩と1価の金屑塩及び溶媒水とからなる汚泥処理剤(
特開昭62−277199号)、
■At2.Fed、及びSO,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。■There is a chemical dehydration treatment method in which the moisture content is lowered by coagulating sedimentation and concentration using a polymer flocculant, and then treatment is performed using lime, cement, or a solidifying agent. , a sludge treatment agent consisting of a divalent or trivalent iron salt, a trivalent metal salt, a monovalent gold scrap salt, and solvent water (
JP-A-62-277199), ■At2. A liquid inorganic flocculant (Japanese Patent Application Laid-Open No. 14911/1983) consisting of an aqueous solution of basic aluminum iron sulfate containing specific amounts of three components, Fed and SO, is known, and attempts have been made to use these treatment agents. There is.
曲屈の従来技術では、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。The conventional bending technology has the following drawbacks, for example. ■
In the solar drying process, water molecules are evaporated from the bottom mud over a large area and over a long period of time, but during this period, there is a foul odor peculiar to the bottom mud, and when it is exposed to rain or snow, it liquefies again and produces a bad odor. Release.
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。Difficult to use as landfill soil, etc. In the case of (2), the mechanical dewatering treatment method only reduces the water content by squeezing water out of the bottom mud, even if a large amount of money is invested, and does not improve odor, soil quality, or water quality.
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9又、同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。Furthermore, since the sludge is not completely solidified, it is difficult to use it as land for landfill or embankment. In addition, lime and cement are used in the chemical dehydration treatment method (■), but these only solidify the bottom mud and make it easier to dispose of, and cannot improve the soil quality. Along with this, alkaline content is washed away from the treatment area due to the influence of rainwater and spring water over a long period of time, causing a problem of deterioration of water quality in downstream rivers.In the case of the treatment agents listed in ■ and ■ above, In order to sufficiently separate water, not only is pretreatment such as treatment with a polymer flocculant required first, but water separation is still poor and takes a long time, and bacteria.
重金属の解毒、臭気の消除については効果が見られず、
その分離水も利用範囲が限定される等の点で問題があり
、したがって底泥の疎水化がすみやかに出来1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。No effect was observed in detoxifying heavy metals or eliminating odors.
The separated water also has problems in that its usage range is limited, so the bottom mud can be made hydrophobic quickly.1 Separated water,
It also makes it possible to sterilize bacteria and detoxify heavy metals contained in the separated bottom mud, and the soil particles can be regenerated into the soil particles before the bottom mud, and the range of use is not limited, and can be used as land fill, embankment soil, or fertilizer. It is hoped that a method and treatment agent will be developed that will make it possible to hydrophobize pollutants of industrial wastewater, such as industrial metal sludge, or pollutants of wastewater from agricultural, livestock, and seafood processing processes. Done.
分離水、分離固形物の含有細菌の殺菌、重金属の解毒を
も可能とする方法及び処理剤の出現が期待されている。It is expected that a method and a treatment agent will be developed that will make it possible to sterilize bacteria and detoxify heavy metals contained in separated water and solid matter.
本発明者は前記の問題点を解決すべく鋭意研究の結果、
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が汚泥
物類の浄化分離処理剤として前記の問題点を一挙に解決
できるものであることを見出し、本発明に到達したもの
である。As a result of intensive research to solve the above-mentioned problems, the inventor of the present invention found that
An aqueous solution containing metal salts mainly composed of alkaline earth metal salts in addition to divalent or trivalent iron salts and trivalent metal salts can be used as a purification and separation treatment agent for sludge, alleviating the above-mentioned problems at once. We have discovered that this problem can be solved, and have arrived at the present invention.
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、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
、また上記の汚泥物類の浄化分離処理剤を汚泥物類に加
え、次いで高分子凝集剤を添加して汚泥物類を疎水化分
離する汚泥物類の浄化分離処理方法、即ち、底泥や産業
廃水の汚濁物等の汚泥物類から再利用できる良質の水及
び残留物の分離回収方法に関するものである。That is, the present invention provides a purification and separation treatment agent for sludge, which has divalent or trivalent iron salts, trivalent metal salts, and alkaline earth metal salts as main components, and which is prepared by dissolving the inorganic salts in solvent water; A sludge purification and separation treatment agent is prepared by adding diphosphorus pentoxide to this product, and the above-mentioned sludge purification and separation treatment agent is added to the sludge, and then a polymer flocculant is added to the sludge. The present invention relates to a method for purifying and separating sludge by hydrophobizing and separating sludge, that is, a method for separating and recovering reusable high-quality water and residue from sludge such as bottom sludge and industrial wastewater pollutants.
本発明の汚泥物類の浄化分離処理剤(以下浄化分離処理
剤底泥改良剤という)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[A12(
S04)3) 、硫酸アルミニウムカリウム(AIK(
So、)、)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。In the sludge purification and separation treatment agent of the present invention (hereinafter referred to as purification and separation treatment agent bottom sludge improver), divalent and trivalent iron salts include ferrous sulfate, ferric sulfate, ferric chloride, etc. Examples of trivalent metal salts include aluminum sulfate [A12(
S04)3), aluminum potassium sulfate (AIK(
So, ), ), etc. These metal salts are commonly used as flocculants for sludge water treatment.
本発明では前記2価及び3価の鉄塩、3価の金属塩にさ
らに、アルカリ土類金属塩を添加するものであり、アル
カリ土類金属塩としては塩化マグネシウム(MgC1z
・6HJ)、塩化カルシウム(CaC12・21(、O
)等である。これらのアルカリ土類金属塩、例えばMg
Cl2・6H20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CaC1
□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 present invention, an alkaline earth metal salt is further added to the divalent and trivalent iron salts and trivalent metal salts, and the alkaline earth metal salt is magnesium chloride (MgClz
・6HJ), calcium chloride (CaC12・21(, O
) etc. These alkaline earth metal salts, such as Mg
Cl2.6H20 is used as a coagulant for tofu, a cooling agent, and a raw material for cement.
□ is a desiccant, a calcium binder for skeletal diseases as a medicine,
It is widely used in the treatment of allergic diseases, but
There are no examples of these alkaline earth metal salts being used as treatment agents for sludge such as bottom sludge or pollutants of industrial wastewater, and the purification and separation treatment agent of the present invention containing these alkaline earth metal salts can remove water and solids from sludge. The synergistic effect of alkali metal salts and flocculants such as aluminum sulfate, ferric chloride, and ferric sulfate allows sludge to coagulate easily, making adsorption, solidification, and drying possible in a short time. It has excellent effects such as being able to perform
本発明では上記の浄化分離処理剤に更に五酸化二燐(P
、Os)を添加したものを浄化分離処理剤とすることが
できる。p2o、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。In the present invention, diphosphorus pentoxide (P
, Os) can be used as a purification and separation treatment agent. P2O is used for dehydration, gas drying, condensing agent and surfactant in organic chemistry, and digestion for medical purposes.
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。Although it is known as a refreshing agent, the present inventor has discovered for the first time that it acts as a detoxifier and disinfectant for heavy metals and bacteria in sludge, and also as a neutralizing agent that neutralizes alkalinity to acidity. This is what I found.
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p、o、i、s〜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 and 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, particle size composition ratio, water content, PH, temperature, etc. 50-30% by weight of divalent or trivalent iron salts, 45-30% by weight of trivalent metal salts, 30-3% by weight of alkaline earth metal salts, and ~0.3% by weight of p, o, i, s. can be processed effectively.
本発明においてその主要成分の溶媒水は合計重量の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。In the present invention, the amount of solvent water, which is the main component, is preferably at least 4 times the total weight, but it is also possible to use an amount less than this, but in that case, the respective chemical components may react with each other, and the effects and effects may be reduced. May decrease.
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%) i、ooopに対して1〜30ρ
、好ましくは3〜6Qである。The amount of purification and separation treatment agent used is not particularly limited, but it is 1 to 30ρ for sludge (moisture content 10%) i, ooop.
, preferably 3 to 6Q.
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(○H)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。In the treatment of sludge, after treatment with the purification and separation treatment agent of the present invention, the hydrogen ion concentration in the water increases due to the positively charged metal salts of the purification and separation treatment agent, the pH decreases, and the coagulation and coagulation reaction slows down. Therefore, the neutralizing agent calcium hydroxide (
Treated with Ca(○H)2), sodium hydroxide (NaOH), magnesium oxide (MgO), etc. to lower the hydrogen ion concentration.
p H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pn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M g O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。The pH is raised to allow the coagulation and coagulation reaction to occur smoothly. These neutralizing agents are selected depending on the source of the sludge, and the pn is adjusted to about 6 to 8.6. Calcium hydroxide is widely used as a neutralizing agent, and sodium hydroxide is strongly alkaline and is compatible with sediment treatment in seawater. Moreover, MgO acts as a neutralizing agent and as an antidote since it forms an insoluble salt with arsenous acid.
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1例えばアニオンで
はポリアクリルアマイド系〔ハイモロツク5S500、
同0K107 (登録商標)(共立有機工業株式会社)
〕、ノノニンではポリアクリルアマイド系〔ハイモロツ
ク55200 (登録商標)(共立有機工業株式会社)
〕。Furthermore, in treating sludge, a polymer flocculant can be used in combination. Thereby, the coagulation and coagulation reaction between the sludge particles can be further promoted. The sludge quickly forms large flocs and settles due to the synergistic effect with the purification and separation treatment agent. Polymer flocculants include various types of anionic, nonionic, and cationic polymer flocculants.
0K107 (registered trademark) (Kyoritsu Organic Industry Co., Ltd.)
], Nononin uses polyacrylamide [Himoloku 55200 (registered trademark) (Kyoritsu Organic Industry Co., Ltd.)
].
カチオンではポリアクリルアマイド系〔ハイモロツクM
P]、73、同Q 101、同Q+、05(登録商標)
(共立有機工業株式会社)〕等が用いられる。For cations, polyacrylamide type [Himoloku M
P], 73, Q 101, Q+, 05 (registered trademark)
(Kyoritsu Organic Industry Co., Ltd.)] etc. are used.
本発明の浄化分離処理剤を用いての汚泥物類の処理は、
例えば次のようにして行なわれる。汚泥物類に一定量の
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
離固形物を脱水機で脱水し固形残留物(分離上等)を得
る。The treatment of sludge using the purification and separation treatment agent of the present invention is as follows:
For example, this is done as follows. A certain amount of purification and separation treatment agent is added to sludge and mixed. As a result, the separation of water and solids progresses, and the sludge easily coagulates and coagulates. Furthermore, a neutralizing agent and then a polymer flocculant are added to this, the treated material is separated into flocs and water in a sludge separation tank, and the separated solids are dehydrated in a dehydrator to form a solid residue (separation top, etc.) get.
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」二廃水汚濁物等の汚泥物類の処理に有効である。The purification and separation treatment agent of the present invention can be used to treat organic, inorganic, or neutral sediment in fresh water, to treat sediment in freshwater containing metal layer bacteria, to treat sediment in sea water containing heavy metal bacteria, etc. It is effective in treating sludge such as various types of bottom sludge and various industrial wastewater turbidities, such as various industrial wastewater pollutants, such as various metal sludges, agricultural, water, and livestock wastewater pollutants. be.
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、生機粒子
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。The main component of the sludge purification and separation treatment agent of the present invention is a positively charged inorganic metal salt, which binds to and neutralizes the negatively charged fine particles constituting the sludge, thereby reducing the solid matter of the sludge and the biological waste. Water molecules that have been attached and restrained around the particles are separated from the particles, and further water molecules are pushed out due to the agglomeration and coagulation reaction of the solid particles, forming flocs that are aggregated into large particles. it is conceivable that. In particular, since the purification and separation treatment agent of the present invention contains an alkaline earth metal salt, conventional sludge treatment agents of this type required first treatment with a polymer flocculant as an auxiliary agent.
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。The present invention does not require such pretreatment,
Hydrophilic colloid particles can be effectively converted into hydrophobic colloid particles, which can be aggregated, adsorbed and solidified to form a solid mass, and the particles can be made into large agglomerates. It also has a deodorizing effect, eliminating bad odors, sterilizing bacteria and heavy metals, and detoxifying. Also, the separated water has no contaminants and is of high quality.
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、埋立用上、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
可能である。The soil from the separated bottom sludge has low water retention and high permeability, and can be used as soil for reclamation and embankment, and the solids obtained from industrial wastewater, such as metal sludge, can be used as additives for the ceramic industry. Each can be used in a variety of ways, including as a.
以下に実施例で本願発明を説明するが、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。The present invention will be explained below with reference to examples, but it goes without saying that the present invention is not limited to these examples.
具体的に用いた本発明の浄化分離処理剤の溶媒水IQ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
用、実施例2は重金属細菌を含む淡水中の堆積底泥用、
実施例3は重金属細菌を含む海水中の堆積底泥の処理用
、実施例4は魚類缶詰食品加工の際の廃水汚濁物、実施
例5はスケソーダラすり身の食品加工の際の廃水lη濁
物、実施例6は電子部品製造の際の洗浄廃水スラリーの
処理用を示し、比は比較例(特開昭62−277199
号に相当するもの)を示し、実施例〕、と同一の底泥を
処理したものである。Table 1 shows the amount (blending ratio) of the components in the solvent water IQ of the purification and separation treatment agent of the present invention used specifically and the order of addition of the treatment agent in treating sludge. In Table 1, Example 1 is for organic, inorganic, and neutral freshwater sediment sediments, Example 2 is for freshwater sediment sediments containing heavy metal bacteria,
Example 3 is for treatment of sedimentary bottom sludge in seawater containing heavy metal bacteria, Example 4 is for wastewater pollution during canned fish food processing, and Example 5 is for wastewater lη turbidity during food processing of Alaska pollack surimi. Example 6 shows the treatment of cleaning wastewater slurry during the manufacture of electronic parts, and the ratio is that of the comparative example (Japanese Patent Application Laid-Open No. 62-277199).
The same bottom mud as in Example] was treated.
処理方法は以下のとおりである。The processing method is as follows.
底泥等の汚泥物類をパイプ輸送し、そのパイプ中に、汚
泥物類(金泥率10%) 1,0OOQに対して7浄化
分離処理剤を3〜6Qの割合で加えて、パイプ中で混合
輸送しながら、さらに中和剤及び高分子凝集剤を加えて
、汚泥物類を処理した後、汚泥物類分離槽中に導き、水
と凝集沈殿する固体残留物(土等)を分離し、該残留物
を脱水機で処理(7゜脱水、乾燥分離固形物を得た。又
、比較例については先ず高分子凝集剤、汚泥化疎水剤、
中和剤及び高分子凝集剤の順で処理した。Sludge such as bottom sludge is transported through a pipe, and 7 purification and separation treatment agents are added at a ratio of 3 to 6 Q per 1,0 OOQ of the sludge (gold mud ratio: 10%). While transporting the mixture, a neutralizing agent and a polymer flocculant are added to treat the sludge, which is then introduced into a sludge separation tank to separate water and solid residues (soil, etc.) that coagulate and precipitate. , the residue was treated with a dehydrator (7° dehydration to obtain a dry separated solid. Also, for comparative examples, first, a polymer flocculant, a sludge-forming hydrophobic agent,
It was treated with a neutralizing agent and a polymer flocculant in this order.
得られた結果を第2表に示す。表中、中和剤及び高分子
凝集剤の濃度はそれぞれ110g/Q及び2 g /
Qであった。The results obtained are shown in Table 2. In the table, the concentrations of the neutralizing agent and polymer flocculant are 110 g/Q and 2 g/Q, respectively.
It was Q.
第2表
第2表
〔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、得られた分離上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。Table 2 Table 2 [Effects of the Invention] The sludge purification and separation treatment agent of the present invention can be used to treat bottom sludge from dams, lakes, rivers, seabeds, etc., as well as various wastewaters from industries, agricultural water, livestock products, and food processing. Sludge materials such as pollutants can be dehydrated in an extremely short period of time, and the resulting separated solids do not re-sludge (liquefy). Can be played.
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上は埋立用土
、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り、経済的に安価に
汚泥物類の浄化とその利用に貢献でき、画期的な発明で
あると言うことができる。In addition, the purification and separation treatment agent of the present invention can deodorize or deodorize the bad odor peculiar to sludge, sterilize the bacteria contained therein, and detoxify heavy metals. It can be reused, for example, when separated from bottom mud, it can be used as a soil improvement material for landfills, embankments, and agricultural land, and in the case of solids from metal sludge or slurry, it can be used as an additive for the ceramic industry. , the separated water is returned to lakes, rivers, oceans, etc.
It can be said to be an epoch-making invention as it can be used as a water resource and contributes to the purification and utilization of sludge at an economical cost.
Claims (7)
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。(1) A purification and separation treatment agent for sludge, which contains divalent or trivalent iron salts, trivalent metal salts, and alkaline earth metal salts as main components, and is prepared by dissolving the inorganic salts in solvent water.
五酸化二燐を加えてなる汚泥物類の浄化分離処理剤。(2) A purification and separation treatment agent for sludge, which is obtained by adding diphosphorus pentoxide to the agent for purification and separation of sludge according to claim 1.
の汚泥物類の浄化分離処理剤。(3) The agent for purifying and separating sludge according to claim 1 or 2, wherein the sludge is bottom sludge.
くは2記載の汚泥物類の浄化分離処理剤。(4) The agent for purifying and separating sludge according to claim 1 or 2, wherein the sludge is industrial wastewater pollutant.
カルシウムである請求項1又は2記載の汚泥物類の浄化
分離処理剤。(5) The agent for purifying and separating sludge according to claim 1 or 2, wherein the alkaline earth metal salt is magnesium chloride or calcium chloride.
を汚泥物類に加え、該汚泥物類を疎水化分離することを
特徴とする汚泥物類の浄化分離処理方法。(6) A method for purifying and separating sludge, which comprises adding the agent for purifying and separating sludge according to claim 1 or 2 to sludge, and hydrophobizing and separating the sludge.
を汚泥物類に添加処理し、次いで水酸化カルシウム、水
酸化ナトリウム又は酸化マグネシウム及びそれらの混合
物よりなる中和剤さらに高分子凝集剤を添加して汚泥物
類を疎水化分離することを特徴とする、汚泥物類の浄化
分離処理方法。(7) The agent for purification and separation of sludge according to claim 1 or 2 is added to sludge, and then a neutralizing agent comprising calcium hydroxide, sodium hydroxide or magnesium oxide and a mixture thereof, and a polymer A method for purifying and separating sludge, which comprises adding a flocculant to hydrophobize and separate sludge.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1-14112 | 1989-01-25 | ||
JP1411289 | 1989-01-25 |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02284700A true JPH02284700A (en) | 1990-11-22 |
JPH08240B2 JPH08240B2 (en) | 1996-01-10 |
Family
ID=11852033
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2012734A Expired - Fee Related JPH08240B2 (en) | 1989-01-25 | 1990-01-24 | Purification and separation treatment agent for sludge |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH08240B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009214069A (en) * | 2008-03-12 | 2009-09-24 | Daiyanitorikkusu Kk | Treatment method for sewage sludge |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS52148953A (en) * | 1976-06-07 | 1977-12-10 | Japan Gasoline | Enhancing method for water deameating speed of flocculated sludge |
JPS5619526A (en) * | 1979-07-26 | 1981-02-24 | Hitachi Maxell Ltd | Magnetic disc |
JPS5670893A (en) * | 1979-11-09 | 1981-06-13 | Norihiko Base | Treatment of muddy water |
JPS6297698A (en) * | 1985-10-25 | 1987-05-07 | レナ−ト・ジ−・エリツクソン | Method of reconstituting and inverting sludge |
JPS62277199A (en) * | 1986-05-23 | 1987-12-02 | San:Kk | Hydrophobicity imparting agent for sludge |
-
1990
- 1990-01-24 JP JP2012734A patent/JPH08240B2/en not_active Expired - Fee Related
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS52148953A (en) * | 1976-06-07 | 1977-12-10 | Japan Gasoline | Enhancing method for water deameating speed of flocculated sludge |
JPS5619526A (en) * | 1979-07-26 | 1981-02-24 | Hitachi Maxell Ltd | Magnetic disc |
JPS5670893A (en) * | 1979-11-09 | 1981-06-13 | Norihiko Base | Treatment of muddy water |
JPS6297698A (en) * | 1985-10-25 | 1987-05-07 | レナ−ト・ジ−・エリツクソン | Method of reconstituting and inverting sludge |
JPS62277199A (en) * | 1986-05-23 | 1987-12-02 | San:Kk | Hydrophobicity imparting agent for sludge |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2009214069A (en) * | 2008-03-12 | 2009-09-24 | Daiyanitorikkusu Kk | Treatment method for sewage sludge |
Also Published As
Publication number | Publication date |
---|---|
JPH08240B2 (en) | 1996-01-10 |
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