JPH0975897A - Method for solidifying metal in waste - Google Patents
Method for solidifying metal in wasteInfo
- Publication number
- JPH0975897A JPH0975897A JP8198353A JP19835396A JPH0975897A JP H0975897 A JPH0975897 A JP H0975897A JP 8198353 A JP8198353 A JP 8198353A JP 19835396 A JP19835396 A JP 19835396A JP H0975897 A JPH0975897 A JP H0975897A
- Authority
- JP
- Japan
- Prior art keywords
- metal
- waste
- heavy metal
- chemical
- agent
- 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
Links
- 238000000034 method Methods 0.000 title claims abstract description 61
- 229910052751 metal Inorganic materials 0.000 title claims abstract description 32
- 239000002184 metal Substances 0.000 title claims abstract description 32
- 239000002699 waste material Substances 0.000 title claims description 28
- 229910001385 heavy metal Inorganic materials 0.000 claims abstract description 45
- 239000007800 oxidant agent Substances 0.000 claims abstract description 39
- 239000003795 chemical substances by application Substances 0.000 claims abstract description 36
- 239000000126 substance Substances 0.000 claims abstract description 32
- 238000010828 elution Methods 0.000 claims abstract description 23
- 230000001590 oxidative effect Effects 0.000 claims abstract description 6
- 230000003100 immobilizing effect Effects 0.000 claims description 13
- 239000004568 cement Substances 0.000 claims description 12
- 229940079593 drug Drugs 0.000 claims description 10
- 239000003814 drug Substances 0.000 claims description 10
- 150000002739 metals Chemical class 0.000 claims description 2
- MHAJPDPJQMAIIY-UHFFFAOYSA-N Hydrogen peroxide Chemical compound OO MHAJPDPJQMAIIY-UHFFFAOYSA-N 0.000 abstract description 25
- 239000010881 fly ash Substances 0.000 abstract description 19
- 238000004898 kneading Methods 0.000 abstract description 14
- 239000000463 material Substances 0.000 abstract description 8
- RWSOTUBLDIXVET-UHFFFAOYSA-N Dihydrogen sulfide Chemical compound S RWSOTUBLDIXVET-UHFFFAOYSA-N 0.000 abstract description 6
- 229910000037 hydrogen sulfide Inorganic materials 0.000 abstract description 6
- 238000006243 chemical reaction Methods 0.000 abstract description 4
- 150000003464 sulfur compounds Chemical class 0.000 abstract description 2
- FFBHFFJDDLITSX-UHFFFAOYSA-N benzyl N-[2-hydroxy-4-(3-oxomorpholin-4-yl)phenyl]carbamate Chemical compound OC1=C(NC(=O)OCC2=CC=CC=C2)C=CC(=C1)N1CCOCC1=O FFBHFFJDDLITSX-UHFFFAOYSA-N 0.000 abstract 1
- 238000011282 treatment Methods 0.000 description 25
- 230000000052 comparative effect Effects 0.000 description 15
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 14
- 229910052793 cadmium Inorganic materials 0.000 description 11
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 11
- 230000000694 effects Effects 0.000 description 10
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 9
- 239000007789 gas Substances 0.000 description 8
- 239000002920 hazardous waste Substances 0.000 description 6
- 239000002738 chelating agent Substances 0.000 description 5
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 4
- NBIIXXVUZAFLBC-UHFFFAOYSA-N Phosphoric acid Chemical compound OP(O)(O)=O NBIIXXVUZAFLBC-UHFFFAOYSA-N 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 238000007711 solidification Methods 0.000 description 4
- 230000008023 solidification Effects 0.000 description 4
- 238000012360 testing method Methods 0.000 description 4
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 3
- 239000003513 alkali Substances 0.000 description 3
- DKVNPHBNOWQYFE-UHFFFAOYSA-N carbamodithioic acid Chemical compound NC(S)=S DKVNPHBNOWQYFE-UHFFFAOYSA-N 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 235000011121 sodium hydroxide Nutrition 0.000 description 3
- 239000011593 sulfur Substances 0.000 description 3
- 229910052717 sulfur Inorganic materials 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 239000002253 acid Substances 0.000 description 2
- 229910000147 aluminium phosphate Inorganic materials 0.000 description 2
- 150000001732 carboxylic acid derivatives Chemical class 0.000 description 2
- 239000013522 chelant Substances 0.000 description 2
- JOPOVCBBYLSVDA-UHFFFAOYSA-N chromium(6+) Chemical compound [Cr+6] JOPOVCBBYLSVDA-UHFFFAOYSA-N 0.000 description 2
- 150000001875 compounds Chemical class 0.000 description 2
- OSVXSBDYLRYLIG-UHFFFAOYSA-N dioxidochlorine(.) Chemical compound O=Cl=O OSVXSBDYLRYLIG-UHFFFAOYSA-N 0.000 description 2
- 239000003112 inhibitor Substances 0.000 description 2
- 229910052976 metal sulfide Inorganic materials 0.000 description 2
- -1 persulfate compound Chemical class 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 239000002516 radical scavenger Substances 0.000 description 2
- 239000010802 sludge Substances 0.000 description 2
- HYHCSLBZRBJJCH-UHFFFAOYSA-M sodium hydrosulfide Chemical compound [Na+].[SH-] HYHCSLBZRBJJCH-UHFFFAOYSA-M 0.000 description 2
- 235000019830 sodium polyphosphate Nutrition 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 239000004155 Chlorine dioxide Substances 0.000 description 1
- VYZAMTAEIAYCRO-UHFFFAOYSA-N Chromium Chemical compound [Cr] VYZAMTAEIAYCRO-UHFFFAOYSA-N 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- NIPNSKYNPDTRPC-UHFFFAOYSA-N N-[2-oxo-2-(2,4,6,7-tetrahydrotriazolo[4,5-c]pyridin-5-yl)ethyl]-2-[[3-(trifluoromethoxy)phenyl]methylamino]pyrimidine-5-carboxamide Chemical compound O=C(CNC(=O)C=1C=NC(=NC=1)NCC1=CC(=CC=C1)OC(F)(F)F)N1CC2=C(CC1)NN=N2 NIPNSKYNPDTRPC-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- 229920002873 Polyethylenimine Polymers 0.000 description 1
- 239000011398 Portland cement Substances 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- LSNNMFCWUKXFEE-UHFFFAOYSA-N Sulfurous acid Chemical compound OS(O)=O LSNNMFCWUKXFEE-UHFFFAOYSA-N 0.000 description 1
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 238000003916 acid precipitation Methods 0.000 description 1
- 238000011276 addition treatment Methods 0.000 description 1
- 239000012615 aggregate Substances 0.000 description 1
- 229910052783 alkali metal Inorganic materials 0.000 description 1
- 150000001340 alkali metals Chemical class 0.000 description 1
- 229910052784 alkaline earth metal Inorganic materials 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000011400 blast furnace cement Substances 0.000 description 1
- ZOMBKNNSYQHRCA-UHFFFAOYSA-J calcium sulfate hemihydrate Chemical compound O.[Ca+2].[Ca+2].[O-]S([O-])(=O)=O.[O-]S([O-])(=O)=O ZOMBKNNSYQHRCA-UHFFFAOYSA-J 0.000 description 1
- JGIATAMCQXIDNZ-UHFFFAOYSA-N calcium sulfide Chemical compound [Ca]=S JGIATAMCQXIDNZ-UHFFFAOYSA-N 0.000 description 1
- 239000013043 chemical agent Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 229940005991 chloric acid Drugs 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 235000019398 chlorine dioxide Nutrition 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 239000003818 cinder Substances 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000001784 detoxification Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 125000004119 disulfanediyl group Chemical group *SS* 0.000 description 1
- 239000010459 dolomite Substances 0.000 description 1
- 229910000514 dolomite Inorganic materials 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000006703 hydration reaction Methods 0.000 description 1
- 239000001257 hydrogen Substances 0.000 description 1
- 229910052739 hydrogen Inorganic materials 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 229910052945 inorganic sulfide Inorganic materials 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 229910021645 metal ion Inorganic materials 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000010813 municipal solid waste Substances 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 238000012856 packing Methods 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 230000035515 penetration Effects 0.000 description 1
- 230000035699 permeability Effects 0.000 description 1
- 229920001495 poly(sodium acrylate) polymer Polymers 0.000 description 1
- ZOCLAPYLSUCOGI-UHFFFAOYSA-M potassium hydrosulfide Chemical compound [SH-].[K+] ZOCLAPYLSUCOGI-UHFFFAOYSA-M 0.000 description 1
- 229940016373 potassium polysulfide Drugs 0.000 description 1
- 235000019353 potassium silicate Nutrition 0.000 description 1
- DPLVEEXVKBWGHE-UHFFFAOYSA-N potassium sulfide Chemical compound [S-2].[K+].[K+] DPLVEEXVKBWGHE-UHFFFAOYSA-N 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000011002 quantification Methods 0.000 description 1
- 230000001105 regulatory effect Effects 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- NNMHYFLPFNGQFZ-UHFFFAOYSA-M sodium polyacrylate Chemical compound [Na+].[O-]C(=O)C=C NNMHYFLPFNGQFZ-UHFFFAOYSA-M 0.000 description 1
- HYHCSLBZRBJJCH-UHFFFAOYSA-N sodium polysulfide Chemical compound [Na+].S HYHCSLBZRBJJCH-UHFFFAOYSA-N 0.000 description 1
- NTHWMYGWWRZVTN-UHFFFAOYSA-N sodium silicate Chemical compound [Na+].[Na+].[O-][Si]([O-])=O NTHWMYGWWRZVTN-UHFFFAOYSA-N 0.000 description 1
- 229910052979 sodium sulfide Inorganic materials 0.000 description 1
- GRVFOGOEDUUMBP-UHFFFAOYSA-N sodium sulfide (anhydrous) Chemical compound [Na+].[Na+].[S-2] GRVFOGOEDUUMBP-UHFFFAOYSA-N 0.000 description 1
- GWQWBFBJCRDINE-UHFFFAOYSA-M sodium;carbamodithioate Chemical compound [Na+].NC([S-])=S GWQWBFBJCRDINE-UHFFFAOYSA-M 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000004071 soot Substances 0.000 description 1
- 150000004763 sulfides Chemical class 0.000 description 1
- 150000003573 thiols Chemical class 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 238000004056 waste incineration Methods 0.000 description 1
- 229920003169 water-soluble polymer Polymers 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
- Fire-Extinguishing Compositions (AREA)
- Processing Of Solid Wastes (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、廃棄物から金属の
溶出を防止するための工程を備えた廃棄物中の金属固定
化方法に関し、公害防止や資源の再利用の分野に利用さ
れる。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for immobilizing metal in waste, which has a step of preventing metal from being eluted from the waste, and is used in the fields of pollution prevention and resource reuse.
【0002】[0002]
【従来の技術】従来、一般廃棄物焼却処理場や廃プラス
チック焼却炉の飛灰や、汚泥等のうち、重金属を一定量
以上含む有害な廃棄物は、薬品処理やコンクリート固型
化処理によって、重金属を固定化し無害化した後廃棄さ
れている。このような有害廃棄物には、飛灰のように本
来的に還元性雰囲気を持ち、水を添加することにより多
量に水素を発生させるものがある。2. Description of the Related Art Conventionally, harmful wastes containing a certain amount or more of heavy metals, such as fly ash of general waste incineration plants and waste plastic incinerators, and sludge, are treated by chemical treatment or concrete solidification treatment. The heavy metals are fixed and rendered harmless before being discarded. Some of such hazardous wastes have an inherently reducing atmosphere like fly ash and generate a large amount of hydrogen by adding water.
【0003】薬品処理法においては、薬品として、アル
カリ金属や土類金属の硫化物や、チオール型やジチオカ
ルバミン酸型のような硫黄化合物から成るもの等が従来
から一般的に使用されていた。しかしながら、このよう
な薬剤を用いる従来の処理方法では、その還元性雰囲気
のため、硫黄が還元されたり反応して硫化水素が発生
し、難溶性の金属硫化物を生成する反応を阻害すると共
に、添加する薬剤量が多くなるという問題があった。更
に、薬剤の添加によって却って重金属を溶出される場合
があった。又、この重金属の溶出が、薬品による処理
後、時間の経過と共に発生する場合もあった。In the chemical treatment method, as chemicals, sulfides of alkali metals and earth metals and those composed of sulfur compounds such as thiol type and dithiocarbamic acid type have been generally used conventionally. However, in the conventional treatment method using such an agent, due to its reducing atmosphere, sulfur is reduced or reacted to generate hydrogen sulfide, which inhibits the reaction of forming a sparingly soluble metal sulfide, There is a problem in that the amount of added drug increases. Further, heavy metals may be eluted rather by the addition of chemicals. Further, the elution of the heavy metal may occur with the lapse of time after the treatment with the chemical.
【0004】コンクリート固型化処理を行う場合には、
発生する水素ガスの影響により、コンクリートが割れた
りぼろぼろになり、十分な固型化が阻害されたり、高ア
ルカリ条件では、三価クロムが空気酸化されて六価クロ
ムを生じるという問題があった。In the case of concrete hardening treatment,
Due to the effect of the generated hydrogen gas, there is a problem that concrete is cracked or broken to prevent sufficient solidification, and under high alkaline conditions, trivalent chromium is air-oxidized to produce hexavalent chromium.
【0005】一方、雨水、特に酸性雨に曝されたときに
金属の溶出を防止する廃棄物処理方法もしくは薬剤とし
て、金属捕集剤と水溶性高分子とを添加する方法(特開
平4−267982号公報参照)、一定の金属捕集剤及
び薬品を添加する方法(特開平5−50055号公報参
照)、キレート化剤及び無機硫化物を含有する重金属固
定剤(特開昭6−166862号公報参照)等が提案さ
れている。しかしながら、このような薬品を用いる処理
方法でも、薬品量が多く薬品費用が高価になり、処理費
用が高くなるという問題がある。On the other hand, a method of adding a metal scavenger and a water-soluble polymer as a waste treatment method or a chemical agent for preventing elution of metals when exposed to rainwater, particularly acid rain (Japanese Patent Laid-Open No. 2-267982). (See Japanese Patent Laid-Open No. 6-166862), a method of adding a certain metal scavenger and chemicals (see Japanese Patent Laid-Open No. 500555), and a heavy metal fixing agent containing a chelating agent and an inorganic sulfide (Japanese Laid-Open Patent Publication No. 6-166862). Etc.) are proposed. However, even with such a treatment method using a chemical, there is a problem that the amount of the chemical is large and the chemical cost is high, and the treatment cost is high.
【0006】[0006]
【発明が解決しようとする課題】本発明は従来技術に於
ける上記問題を解決し、少ない薬品量で長期間にわたり
有害金属の溶出が殆ど発生しない安定した処理を行うこ
とができる廃棄物中の金属固定化方法を提供することを
課題とする。DISCLOSURE OF THE INVENTION The present invention solves the above-mentioned problems in the prior art, and enables stable treatment with a small amount of chemicals for a long period of time in which toxic metal elution hardly occurs and in waste products. It is an object to provide a metal fixing method.
【0007】[0007]
【課題を解決するための手段】本発明は上記課題を解決
するために、請求項1の発明は、廃棄物から金属の溶出
を防止するための工程を備えた廃棄物中の金属固定化方
法において、前記工程の初期段階で酸化剤を加える酸化
剤添加工程を有することを特徴とし、請求項2の発明
は、上記に加えて、前記工程は、重金属処理剤添加工程
を有することを特徴とする。請求項3の発明は、廃棄物
から金属の溶出を防止するための工程を備えた廃棄物中
の金属固定化方法において、前記工程の初期段階で酸化
剤と重金属処理剤とを予め混ぜ合わせた薬剤を添加する
混合薬剤添加工程を有することを特徴とする。請求項4
の発明は、請求項1又は3の発明の特徴に加えて、前記
工程は、セメントを加えるセメント添加工程を有するこ
とを特徴とする。In order to solve the above-mentioned problems, the present invention provides a method for immobilizing a metal in a waste, comprising the step of preventing the elution of metal from the waste. In the above, the method according to claim 2 further comprises an oxidizing agent adding step of adding an oxidizing agent at an initial stage of the step, and in addition to the above, the step includes a heavy metal treating agent adding step. To do. According to a third aspect of the present invention, in a method for immobilizing a metal in a waste, which includes a step for preventing metal elution from the waste, an oxidizing agent and a heavy metal treating agent are mixed in advance in the initial stage of the step. It is characterized by having a mixed drug addition step of adding a drug. Claim 4
In addition to the features of the invention of claim 1 or 3, the invention of 1 is characterized in that the step includes a cement adding step of adding cement.
【0008】[0008]
【発明の実施の形態】図1は、廃棄物から金属の溶出を
抑制する廃棄物中の金属固定化方法の実施の形態の一例
を示し、図2は図1の方法を部分的に変更した他の例を
示す。図1の方法は、工程の初期段階で酸化剤を加える
酸化剤添加工程を含んでいて、解砕工程1、酸化剤添加
工程2、混練工程3、重金属処理薬剤添加工程4、混練
工程5、固定薬剤添加工程6、混練工程7、及び養生工
程8によって構成されている。図2の方法では、酸化剤
と重金属処理剤とを予め混ぜ合わせた薬剤である混合薬
剤を使用し、図1の3つの工程2、3、4を混合薬剤添
加工程2´の1つの工程にしている。DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS FIG. 1 shows an example of an embodiment of a method for immobilizing metal in waste which suppresses the elution of metal from the waste, and FIG. 2 is a partial modification of the method of FIG. Another example is shown. The method of FIG. 1 includes an oxidizing agent addition step of adding an oxidizing agent in the initial stage of the step, and includes a crushing step 1, an oxidizing agent addition step 2, a kneading step 3, a heavy metal treatment chemical addition step 4, a kneading step 5, It is composed of a fixed chemical addition step 6, a kneading step 7, and a curing step 8. In the method of FIG. 2, a mixed chemical, which is a chemical in which an oxidizing agent and a heavy metal treating agent are premixed, is used, and the three steps 2, 3 and 4 of FIG. 1 are made one step of the mixed chemical addition step 2 ′. ing.
【0009】これらの方法の対象とされる被処理物は、
主にゴミ焼却場や産業廃棄物焼却炉等のばいじん(飛
灰)であるが、重金属類を溶出させる汚泥、燃え殻、鉱
滓等の有害廃棄物も含まれる。被処理物が硬質系のもの
や飛灰のようにパサパサしたケーク状のものである場合
には、上記のように前処理として解砕工程1を設ける。
この工程では、解砕機等を用いて、例えば粒径が5mm
程度以下になるまで被処理物を粉砕する。この処理によ
れば、被処理物全体として表面積が大きくなるので、被
処理物と薬剤との反応が均一化され、混練時間が短縮さ
れる。解砕された被処理物は、バッチ式ミキサー等の適
当な混練装置に入れられる。The objects to be processed by these methods are:
It is mainly soot and dust (fly ash) from garbage incinerators and industrial waste incinerators, but it also contains hazardous waste such as sludge, cinders, and slag that elute heavy metals. When the object to be treated is a hard material or a cake-like material such as fly ash, the crushing step 1 is provided as a pretreatment as described above.
In this step, using a crusher, for example, the particle size is 5 mm
The object to be processed is crushed until the amount becomes less than the above. According to this treatment, the surface area of the object to be treated is increased as a whole, so that the reaction between the object to be treated and the chemical is made uniform and the kneading time is shortened. The crushed material to be treated is put into an appropriate kneading device such as a batch mixer.
【0010】図1の酸化剤添加工程2では、酸化剤とし
て例えば30%過酸化水素を用い、これを約20倍程度
の水で薄め、被処理物が飛灰であるときには、飛灰10
0に対して過酸化水素水溶液を重量で約70%程度加え
る。酸化剤としては、過酸化水素の他に、オゾン、二酸
化塩素、過硫酸化合物、過マンガン酸化合物、塩素酸化
合物等があり、これらの何れを用いてもよい。In the oxidizing agent adding step 2 of FIG. 1, for example, 30% hydrogen peroxide is used as an oxidizing agent, and this is diluted with about 20 times the amount of water.
About 70% by weight of an aqueous solution of hydrogen peroxide is added to 0. Examples of the oxidizing agent include ozone, chlorine dioxide, a persulfate compound, a permanganate compound, and a chloric acid compound in addition to hydrogen peroxide, and any of these may be used.
【0011】図1の混練工程3では、ミキサー等の中
で、過酸化水素水溶液を添加された被処理物がペースト
状になるまでよく混ぜ合わせる。In the kneading step 3 of FIG. 1, the material to be treated to which the aqueous hydrogen peroxide solution has been added is thoroughly mixed in a mixer or the like until it becomes a paste.
【0012】図1の工程4で添加する重金属処理薬剤と
しては、硫化ナトリウム、硫化カリウム、硫化カルシウ
ム、水硫化ナトリウム、水硫化カリウム、多硫化ナトリ
ウム、多硫化カリウム、ジチオカルバミン酸型・カルボ
ン酸型・ジチオ酸型・リン酸型・チオ尿素型・チオール
型・アミノ型等のキレート化剤のように、種々のものが
従来から一般的に使用され、又、有効な薬剤として提案
されている。本発明の方法においては、これらのうちの
何れの薬剤を使用してもよい。Heavy metal treating agents added in step 4 of FIG. 1 include sodium sulfide, potassium sulfide, calcium sulfide, sodium hydrosulfide, potassium hydrosulfide, sodium polysulfide, potassium polysulfide, dithiocarbamic acid type / carboxylic acid type Various kinds of chelating agents such as dithio acid-type, phosphoric acid-type, thiourea-type, thiol-type and amino-type chelating agents have been generally used conventionally and proposed as effective agents. Any of these agents may be used in the method of the present invention.
【0013】図2の混合薬剤添加工程2´では、酸化剤
として例えば30%過酸化水素と、重金属処理剤として
例えばリン酸型のキレート化剤とを予め混合した混合薬
剤を加える。この例でも、混合薬剤に使用する酸化剤と
しては上記の図1の方法に用いる酸化剤を使用できる。
酸化剤と混合可能な重金属処理剤としては、リン酸型、
カルボン酸型等がある。In the mixed chemical addition step 2'of FIG. 2, a mixed chemical in which, for example, 30% hydrogen peroxide as an oxidizing agent and a phosphoric acid type chelating agent as a heavy metal treating agent are mixed in advance is added. Also in this example, the oxidizing agent used in the method of FIG. 1 can be used as the oxidizing agent used in the mixed drug.
As a heavy metal treatment agent that can be mixed with an oxidizing agent, a phosphoric acid type agent,
There are carboxylic acid type and the like.
【0014】図1の方法における重金属処理剤の添加量
は、被処理物の性状や含有する重金属の量によって異な
るが、本発明では、この工程4の前の初期段階に酸化剤
添加工程2を設けているので、例えば飛灰に対して、通
常の半分以下で十分である。図2の方法でも、重金属処
理剤を酸化剤と共に用いるので、図1の場合と同様にそ
の添加量を半減できる。The amount of the heavy metal treating agent added in the method of FIG. 1 differs depending on the properties of the object to be treated and the amount of heavy metal contained, but in the present invention, the oxidizing agent adding step 2 is performed in the initial stage before the step 4. Since it is provided, for example, with respect to fly ash, half or less than usual is sufficient. Also in the method of FIG. 2, since the heavy metal treating agent is used together with the oxidizing agent, the addition amount can be halved as in the case of FIG.
【0015】図1の重金属処理剤を添加して混練した工
程5又は図2の混合薬剤を添加して混練した工程5まで
の状態では、被処理物はスラリー状を呈していて、この
状態で廃棄処分すると、長期間の養生を必要とし、又、
搬送や廃棄作業にも困難性を伴う。このため、固化剤の
添加及びその後の混練工程7、8を設けることが望まし
い。固化剤としては、ポルトランドセメント、アルミナ
セメント、半水石こう、高炉セメント、ドロマイトセメ
ント、シリカセメント、水ガラス、フライアッシュセメ
ント、高硫酸塩セメント等の何れかを用いることができ
る。In the state up to the step 5 in which the heavy metal treating agent in FIG. 1 is added and kneaded or the step 5 in which the mixed chemicals in FIG. 2 is added and kneaded, the object to be treated is in a slurry state. Disposal requires long-term curing, and
Difficulties are involved in transportation and disposal. For this reason, it is desirable to add a solidifying agent and then provide kneading steps 7 and 8. As the solidifying agent, any of Portland cement, alumina cement, hemihydrate gypsum, blast furnace cement, dolomite cement, silica cement, water glass, fly ash cement, high sulfate cement and the like can be used.
【0016】養生工程8では、被処理物が固化剤によっ
て固定化されその性状が安定するまで、例えば24時間
程度熟成する。固化剤を5%程度添加すれば、数時間後
に凝結を始め、24時間後には固化する。このように固
化したものは透水性が低く、その値は粘度と同程度にな
っているので、埋め立てに用いると、内部への雨水の浸
透が防止される。又、この固化物はある程度の圧縮強度
を備え、圧縮変形量も小さいので、地盤沈下を発生させ
ない。In the curing step 8, the material to be treated is aged for about 24 hours, for example, until it is fixed by the solidifying agent and its properties are stabilized. If a solidifying agent of about 5% is added, it will start to set after a few hours and will solidify after 24 hours. The solidified material has low water permeability and its value is about the same as the viscosity. Therefore, when it is used for landfill, penetration of rainwater into the interior is prevented. Further, since this solidified material has a certain degree of compressive strength and a small amount of compressive deformation, it does not cause ground subsidence.
【0017】図3は実施の形態の他の例として、コンク
リート固形化方法を示す。この方法は、解砕工程11、
酸化剤添加工程12、混練工程13、セメント又は必要
に応じてセメント及び骨材を加える工程14、これらに
水を加えて混練する混練工程15、及び養生工程16に
よって構成される。この方法では、酸化剤添加工程によ
り、飛灰の本来有する還元性雰囲気が酸化性雰囲気に変
わり、水素ガスの発生がなくなるので、強固な固形化物
が形成される。FIG. 3 shows a concrete solidifying method as another example of the embodiment. This method includes a crushing step 11,
It comprises an oxidizing agent adding step 12, a kneading step 13, a step 14 of adding cement or cement and aggregate as required, a kneading step 15 of adding water to these and kneading, and a curing step 16. In this method, due to the oxidizing agent adding step, the originally reducing atmosphere of fly ash is changed to an oxidizing atmosphere, and hydrogen gas is not generated, so that a strong solidified product is formed.
【0018】以上では酸化剤添加工程を含む処理方法と
して、重金属添処理及びコンクリート固形化処理方法の
例を示したが、本発明は、酸化剤添加工程を含む方法で
あれば、例えば、アルカリを添加する水酸化物方法、水
に難溶性の金属硫化物を生成させる硫化物方法、金属イ
オンと選択的に不溶解性の錯体形成を行わせるキレート
化合物法、等の従来から一般的に行われている方法や、
最近提案されている薬剤を用いる方法など、公知の各種
工程を用いることができる。そして、それぞれの方法に
おいて、酸化剤の添加によって廃棄物を酸化性雰囲気に
し、重金属の確実な固定化と、処理薬品量の低減を図る
ことができる。In the above, examples of the heavy metal addition treatment and the concrete solidification treatment method have been shown as the treatment method including the oxidizing agent addition step. The hydroxide method of addition, the sulfide method of forming a metal sulfide that is hardly soluble in water, the chelate compound method of selectively forming a complex insoluble with metal ions, etc. The way you are
Various known steps such as a method using a recently proposed drug can be used. Then, in each of the methods, it is possible to make the waste into an oxidizing atmosphere by adding an oxidizing agent, to reliably fix the heavy metal, and to reduce the amount of treatment chemicals.
【0019】[0019]
【実施例】有害廃棄物として飛灰を用い、本発明の方法
を実施すると共に、従来の方法と比較した結果を表1に
示し、以下に説明する。EXAMPLE The method of the present invention was carried out using fly ash as a hazardous waste, and the results of comparison with the conventional method are shown in Table 1 and described below.
【0020】[0020]
【表1】 [Table 1]
【0021】焼却炉の排ガスは、塩化水素ガス、亜硫酸
ガス等の酸性ガスを含んでいるが、これらのガスの排出
は法律によって規制されているので、最近の焼却設備で
は、排ガス洗浄装置を設け、苛性ソーダ等のアルカリで
それらのガスを中和・吸収して消滅させている。しか
し、本発明の作用効果を明瞭にするため、実施例及び比
較例における諸試験は、上記のような酸性ガス対策の採
られていない古い形式の焼却炉の飛灰を採取して行っ
た。この飛灰は、大量の鉛及びカドミウムとして、それ
ぞれ14000及び540mg/kgを含有している。
なお同表では、以下の実施例や比較例の何れにおいて
も、六価クロムやその他の重金属の溶出は定量下限であ
ったので、それらの値については記載していない。Exhaust gas from the incinerator contains acid gases such as hydrogen chloride gas and sulfurous acid gas. Since the discharge of these gases is regulated by law, recent incinerators are equipped with an exhaust gas cleaning device. , These gases are neutralized and absorbed with alkali such as caustic soda to eliminate them. However, in order to clarify the action and effect of the present invention, various tests in Examples and Comparative Examples were carried out by collecting fly ash of an old type incinerator in which measures for acid gas as described above are not taken. This fly ash contains 14000 and 540 mg / kg, respectively, as a large amount of lead and cadmium.
In the same table, since the elution of hexavalent chromium and other heavy metals was at the lower limit of quantification in any of the following Examples and Comparative Examples, those values are not described.
【0022】実施例1:酸化剤としては30%過酸化水
素を3mlを用いた。これを67mlの水と混合して希
薄な過酸化水素液とし、これを飛灰100gに添加して
10分間混練し、これに重金属処理剤として、ジチオカ
ルバミン酸型のキレート化剤ポリエチレンイミンジチオ
カルバミン酸ナトリウム15%液2に30%水硫化ナト
リウム8を混合したものを3ml添加して10分間混練
し、一昼夜放置した後、溶出試験を行った。その結果に
よれば、鉛及びカドミウム溶出量はそれぞれ0.05及
び0.005mg/l以下であった。即ち、被処理物と
して鉛及びカドミウムを大量に含有した飛灰を用いたに
もかかわらず、これらの重金属を非常に少ない溶出量に
押さえることができた。現在、陸上に埋め立てる場合の
法律で定められている基準値はそれぞれ0.3mg/l
以下であるが、本実施例の結果はこれを十分クリアする
ものである。なお、重金属処理剤は硫黄を多量に含有し
ているが、硫化水素臭の発生は僅かであった。又、重金
属処理剤として、 ポリアクリル酸ナトリウム、ポリリ
ン酸ナトリウム等を用いて実施した結果においても、同
様の数値が得られた。Example 1 3 ml of 30% hydrogen peroxide was used as an oxidizing agent. This was mixed with 67 ml of water to form a diluted hydrogen peroxide solution, which was added to 100 g of fly ash and kneaded for 10 minutes. As a heavy metal treating agent, a dithiocarbamic acid type chelating agent polyethyleneimine sodium dithiocarbamate was added. 3 ml of a mixture of 15% liquid 2 and 30% sodium hydrosulfide 8 was added, and the mixture was kneaded for 10 minutes, allowed to stand for a day and night, and then subjected to an elution test. According to the results, the amounts of lead and cadmium eluted were 0.05 and 0.005 mg / l or less, respectively. That is, although the fly ash containing a large amount of lead and cadmium was used as the object to be treated, these heavy metals could be suppressed to a very small elution amount. Currently, the standard value set by law for landfill is 0.3 mg / l.
As will be described below, the results of this embodiment sufficiently clear this. The heavy metal treating agent contained a large amount of sulfur, but the generation of hydrogen sulfide odor was slight. Also, similar results were obtained in the results obtained by using sodium polyacrylate, sodium polyphosphate, etc. as the heavy metal treating agent.
【0023】実施例2:酸化剤として30%過酸化水素
1と重金属処理剤としてポリリン酸ナトリウム30%液
9とを混合した混合薬剤3mlを70mlの水に混ぜて
希薄な混合薬剤液とし、これを飛灰100gに添加して
10分間混練し、一昼夜放置した後溶出試験を行った。
その結果によれば、鉛及びカドミウム溶出量はそれぞれ
0.05及び0.005mg/l以下であった。即ち、
酸化剤と重金属処理剤とを予め混合した薬剤を用いて
も、実施例1と同様の効果が得られることが実証され
た。この方法によれば、飛灰処理等における処理工程を
より簡略化することができる。Example 2 3 ml of a mixed drug prepared by mixing 30% hydrogen peroxide 1 as an oxidizing agent and 30% sodium polyphosphate solution 9 as a heavy metal treating agent was mixed with 70 ml of water to prepare a diluted mixed drug solution. Was added to 100 g of fly ash, kneaded for 10 minutes, allowed to stand for a day and night, and then subjected to an elution test.
According to the results, the amounts of lead and cadmium eluted were 0.05 and 0.005 mg / l or less, respectively. That is,
It was demonstrated that the same effect as in Example 1 can be obtained by using a chemical in which an oxidizing agent and a heavy metal treating agent are mixed in advance. According to this method, the processing steps in fly ash processing and the like can be further simplified.
【0024】実施例3:実施例1において、重金属処理
剤を添加する代わりに、アルカリ処理として、48%苛
性ソーダを1ml添加した。この実施例では、鉛及びカ
ドミウム溶出量はそれぞれ0.02及び0.012mg
/lとなり、同様に陸上埋立基準値を十分クリアできる
という結果が得られた。次に、本発明の特徴である過酸
化水素添加の効果をより明瞭にするために行った比較例
を示す。Example 3: Instead of adding the heavy metal treating agent in Example 1, 1 ml of 48% caustic soda was added as an alkali treatment. In this example, the lead and cadmium elution amounts were 0.02 and 0.012 mg, respectively.
/ L was obtained, and similarly, the result was obtained that the landfill standard value could be sufficiently cleared. Next, a comparative example performed to clarify the effect of adding hydrogen peroxide, which is a feature of the present invention, will be shown.
【0025】比較例1:実施例1において、過酸化水素
及び苛性ソーダを添加することなく、水70mlを添加
するだけで同様の処理を行った。即ち、飛灰100gに
水70mlを添加して10分間混練し、一昼夜放置した
後溶出試験を行った。この例では、鉛及びカドミウム溶
出量はそれぞれ2.1及び21.2mg/lであった。Comparative Example 1: The same treatment as in Example 1 was carried out by adding 70 ml of water without adding hydrogen peroxide and caustic soda. That is, 70 ml of water was added to 100 g of fly ash, the mixture was kneaded for 10 minutes, and allowed to stand overnight for an elution test. In this example, the lead and cadmium elution rates were 2.1 and 21.2 mg / l, respectively.
【0026】比較例2:比較例1において、水70ml
を添加する代わりに、実施例1と同様に30%過酸化水
素3mlを水67mlと混合した過酸化水素水を添加し
た。この場合には、PHも上昇し、鉛及びカドミウム溶
出量がそれぞれ0.30及び0.95mg/lになり、
比較例1よりも大幅に減少した。従って、酸化剤として
過酸化水素を添加した効果が明瞭に表れた。Comparative Example 2: 70 ml of water in Comparative Example 1
Instead of adding the above, hydrogen peroxide solution obtained by mixing 3 ml of 30% hydrogen peroxide with 67 ml of water was added in the same manner as in Example 1. In this case, the pH is also increased, and the lead and cadmium elution amounts are 0.30 and 0.95 mg / l, respectively,
It was significantly reduced as compared with Comparative Example 1. Therefore, the effect of adding hydrogen peroxide as an oxidizing agent was clearly shown.
【0027】比較例3:比較例1において、温度が高い
状態では流動性が良くなるので、水70mlを35ml
にし、混練温度を60°Cにして20分間混練した。こ
の場合には、鉛及びカドミウム溶出量がそれぞれ0.2
1及び2.00mg/lになり、実施例1より大幅に低
下した。これにより、加熱すること、即ち空気酸化によ
る効果が明らかになった。但し、陸上埋立基準値を満足
できる値には至っていない。Comparative Example 3: In Comparative Example 1, since the fluidity is improved when the temperature is high, 70 ml of water is replaced with 35 ml of water.
The kneading temperature was set to 60 ° C. and kneading was performed for 20 minutes. In this case, the elution amount of lead and cadmium are each 0.2
It was 1 and 2.00 mg / l, which was much lower than in Example 1. This revealed the effect of heating, ie air oxidation. However, it has not reached the level that can satisfy the landfill landfill standard value.
【0028】比較例4:比較例1において、水70ml
を20mlにし、更に、実施例1と同じ重金属処理剤を
同じ量である3ml添加した。この場合には、鉛及びカ
ドミウム溶出量がそれぞれ3.4及び7.9mg/lに
なり、実施例1とは比較にならない程大きい値になり、
陸上埋立基準値を全くクリアできない結果になった。こ
の例からも、酸化剤の添加の効果が極めて明瞭になっ
た。なお、この例では、硫化水素臭が多大であった。Comparative Example 4: 70 ml of water in Comparative Example 1
To 20 ml, and the same heavy metal treating agent as in Example 1 was added in the same amount of 3 ml. In this case, the elution amounts of lead and cadmium were 3.4 and 7.9 mg / l, respectively, which were so large that they could not be compared with Example 1.
The result was that the landfill landfill standard value could not be cleared at all. Also from this example, the effect of the addition of the oxidizing agent became very clear. In this example, the smell of hydrogen sulfide was large.
【0029】比較例5:比較例4において、重金属処理
剤の添加量を8mlに増加した。この場合には、鉛及び
カドミウム溶出量がそれぞれ0.05及び0.005m
g/l以下になり、実施例2と同じ結果が得られ、陸上
埋立基準値を十分満足する結果となった。従って、重金
属処理剤の添加量を多くすれば、本発明の特徴部分であ
る酸化剤の添加工程を設けなくてもよい。しかし、重金
属処理剤のコストは酸化剤の価額のほぼ5〜10倍であ
り、この比較例の方法では処理コストが高くなるという
問題が残る。なお、この例でも硫化水素臭の発生が多大
であり、重金属処理剤が有効に作用していないことが明
らかになった。Comparative Example 5: In Comparative Example 4, the amount of the heavy metal treating agent added was increased to 8 ml. In this case, the lead and cadmium elution amounts are 0.05 and 0.005 m, respectively.
The value was less than g / l, the same result as in Example 2 was obtained, and the result was that the landfill standard value was sufficiently satisfied. Therefore, if the amount of the heavy metal treatment agent added is increased, the step of adding the oxidizing agent, which is a feature of the present invention, need not be provided. However, the cost of the heavy metal treating agent is about 5 to 10 times the price of the oxidizing agent, and the method of this comparative example has a problem that the treating cost becomes high. In this example, too, the generation of hydrogen sulfide odor was large, and it was revealed that the heavy metal treating agent did not act effectively.
【0030】比較例6:実施例2において、酸化剤を添
加する工程を省いた。この場合には、鉛及びカドミウム
溶出量がそれぞれ0.13及び0.92mg/lにな
り、陸上埋立基準値を全くクリアできなかった。この結
果、アルカリ処理方法を用いる場合に、本発明の特徴部
分である酸化剤の添加工程を設ける効果が極めて明瞭に
なった。Comparative Example 6: In Example 2, the step of adding an oxidizing agent was omitted. In this case, the lead and cadmium elution amounts were 0.13 and 0.92 mg / l, respectively, and the landfill standard value could not be cleared at all. As a result, when the alkali treatment method is used, the effect of providing the oxidizing agent addition step, which is a feature of the present invention, has become extremely clear.
【0031】[0031]
【発明の効果】本発明によれば、従来では、有害廃棄物
の無害化処理においては阻害性物質とされていた酸化剤
を積極的に加える工程を設けることにより、飛灰等の有
害廃棄物の有する還元性雰囲気が、酸化性雰囲気に転換
される。EFFECTS OF THE INVENTION According to the present invention, by providing a step of actively adding an oxidizing agent which has been conventionally regarded as an inhibitor in the detoxification treatment of hazardous waste, hazardous waste such as fly ash is provided. The reducing atmosphere of is converted into an oxidizing atmosphere.
【0032】これにより、その後の工程において、通常
用いられる硫黄系の重金属溶出防止剤によって薬品処理
をする場合に、廃棄物と薬剤とが反応しても硫化水素が
発生せず、且つ、重金属が不感金属から不動態もしくは
腐食金属になるので、薬剤が極めて効果的に作用し、そ
の溶出重金属との反応がスムースに行われる。その結
果、重金属と薬剤との反応物は、強力なキレート結合に
なり、又、未反応物もごく僅かになるため、長期間にわ
たって安定した性状のものになる。更に、重金属処理剤
が有効に作用するため、その消費量が大幅に低減し、廃
棄物中の金属固定化処理のためのコストも低減する。な
お、酸化剤に加えて重金属処理剤を用いる場合には、こ
れらの薬剤を予め混ぜ合わせておき、その混合薬剤を加
えて飛灰等を処理するようにすれば、より簡略化された
工程で上記と同様の効果を得ることができる。As a result, in the subsequent step, when the chemical treatment is carried out with the usually used sulfur-based heavy metal elution inhibitor, hydrogen sulfide is not generated even when the waste and the chemical react with each other, and the heavy metal is removed. Since the insensitive metal becomes a passive or corrosive metal, the drug acts extremely effectively, and the reaction with the eluted heavy metal is smoothly performed. As a result, the reaction product of the heavy metal and the drug becomes a strong chelate bond, and the amount of the unreacted product becomes very small, so that the property is stable for a long period of time. Further, since the heavy metal treating agent acts effectively, the consumption amount thereof is significantly reduced, and the cost for the treatment for fixing the metal in the waste is also reduced. If a heavy metal treatment agent is used in addition to the oxidizing agent, these chemicals should be mixed in advance and the mixed chemicals should be added to treat fly ash, etc., in a more simplified process. The same effect as above can be obtained.
【0033】一方、酸化剤添加後の処理としてコンクリ
ート固形化を行う場合にも、水素ガスの発生がなく、水
和反応を阻害する有機物も分解するため、強固な固形化
物を得ることができる。コンクリート固形化法自体が安
価な工法であるため、酸化剤を添加する工程が追加され
ても、この方法によれば、安価に且つ確実に有害廃棄物
中の重金属の溶出防止処理をすることができる。そし
て、このように安定化されたコンクリートは、輸送中の
取扱いに便利で、埋立処分したり土木構造物として利用
する場合に、充填密度が大きく、均質で、地耐力も大き
く地盤沈下を起こしにくいという良好な性質を有する。
従って、本発明の方法を用いて廃棄物をコンクリート固
形化処理すれば、資源の再利用に貢献することもでき
る。On the other hand, even when concrete is solidified as a treatment after the addition of the oxidizing agent, hydrogen gas is not generated and organic substances which inhibit the hydration reaction are decomposed, so that a solid solidified product can be obtained. Since the concrete solidification method itself is an inexpensive construction method, even if a step of adding an oxidizer is added, this method makes it possible to inexpensively and reliably prevent the elution of heavy metals in hazardous waste. it can. The stabilized concrete is convenient for handling during transportation, and has a high packing density, is homogeneous, and has a large bearing capacity and is unlikely to cause ground subsidence when it is used for landfill disposal or as a civil engineering structure. It has good properties.
Therefore, if the waste is solidified with concrete using the method of the present invention, it can contribute to the reuse of resources.
【図1】廃棄物中の金属固定化方法の一例を示す工程図
である。FIG. 1 is a process drawing showing an example of a method for immobilizing a metal in waste.
【図2】廃棄物中の金属固定化方法の他の例を示す工程
図である。FIG. 2 is a process diagram showing another example of a method for immobilizing a metal in waste.
【図3】廃棄物中の金属固定化方法の更に他の例を示す
工程図である。FIG. 3 is a process drawing showing still another example of the method for immobilizing the metal in the waste.
2 酸化剤添加工程 2´ 混合薬剤添加工程 4 重金属処理剤添加工程 12 酸化剤添加工程 14 セメント添加工程 2 Oxidizing agent adding step 2'Mixed chemical adding step 4 Heavy metal treating agent adding step 12 Oxidizing agent adding step 14 Cement adding step
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 B09B 3/00 301N 304H Continuation of the front page (51) Int.Cl. 6 Identification code Office reference number FI Technical display location B09B 3/00 301N 304H
Claims (4)
工程を備えた廃棄物中の金属固定化方法において、 前記工程の初期段階で酸化剤を加える酸化剤添加工程を
有することを特徴とする廃棄物中の金属固定化方法。1. A method for immobilizing a metal in a waste, comprising a step for preventing the elution of a metal from the waste, comprising an oxidant addition step of adding an oxidant in an initial stage of the step. Method for immobilizing metals in waste.
することを特徴とする請求項1に記載の廃棄物中の金属
固定化方法。2. The method for immobilizing metal in waste according to claim 1, wherein the step includes a step of adding a heavy metal treating agent.
工程を備えた廃棄物中の金属固定化方法において、 前記工程の初期段階で酸化剤と重金属処理剤とを予め混
ぜ合わせた薬剤を添加する混合薬剤添加工程を有するこ
とを特徴とする廃棄物中の金属固定化方法。3. A method for immobilizing a metal in waste, comprising a step for preventing the elution of metal from the waste, wherein a chemical prepared by previously mixing an oxidizing agent and a heavy metal treating agent in the initial stage of the step is used. A method for immobilizing a metal in a waste, comprising a step of adding a mixed drug to be added.
添加工程を有することを特徴とする請求項1又は請求項
3に記載の廃棄物中の金属固定化方法。4. The method for immobilizing metal in waste according to claim 1, wherein the step includes a cement addition step of adding cement.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8198353A JPH0975897A (en) | 1995-07-11 | 1996-07-08 | Method for solidifying metal in waste |
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7-199021 | 1995-07-11 | ||
JP19902195 | 1995-07-11 | ||
JP8198353A JPH0975897A (en) | 1995-07-11 | 1996-07-08 | Method for solidifying metal in waste |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH0975897A true JPH0975897A (en) | 1997-03-25 |
Family
ID=26510936
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8198353A Pending JPH0975897A (en) | 1995-07-11 | 1996-07-08 | Method for solidifying metal in waste |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH0975897A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH11193374A (en) * | 1997-11-06 | 1999-07-21 | Miyoshi Oil & Fat Co Ltd | Metal scavenger |
JP2001191063A (en) * | 2000-01-12 | 2001-07-17 | Kurita Water Ind Ltd | Soil treatment method |
US6786966B1 (en) * | 2002-06-07 | 2004-09-07 | William B. Johnson | Pulverulent ash composition as a portland cement substitute for improving concrete products and method |
JP2019025446A (en) * | 2017-08-02 | 2019-02-21 | 宇部興産株式会社 | Storage method of municipal refuse incineration ash |
-
1996
- 1996-07-08 JP JP8198353A patent/JPH0975897A/en active Pending
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH11193374A (en) * | 1997-11-06 | 1999-07-21 | Miyoshi Oil & Fat Co Ltd | Metal scavenger |
JP2001191063A (en) * | 2000-01-12 | 2001-07-17 | Kurita Water Ind Ltd | Soil treatment method |
JP4576654B2 (en) * | 2000-01-12 | 2010-11-10 | 栗田工業株式会社 | Soil treatment method |
US6786966B1 (en) * | 2002-06-07 | 2004-09-07 | William B. Johnson | Pulverulent ash composition as a portland cement substitute for improving concrete products and method |
JP2019025446A (en) * | 2017-08-02 | 2019-02-21 | 宇部興産株式会社 | Storage method of municipal refuse incineration ash |
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