JPH09174019A - Treatment of general waste incineration ash - Google Patents
Treatment of general waste incineration ashInfo
- Publication number
- JPH09174019A JPH09174019A JP7352103A JP35210395A JPH09174019A JP H09174019 A JPH09174019 A JP H09174019A JP 7352103 A JP7352103 A JP 7352103A JP 35210395 A JP35210395 A JP 35210395A JP H09174019 A JPH09174019 A JP H09174019A
- Authority
- JP
- Japan
- Prior art keywords
- water
- waste incineration
- incineration ash
- blast furnace
- mixed
- 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.)
- Withdrawn
Links
- 238000004056 waste incineration Methods 0.000 title claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 64
- 239000002893 slag Substances 0.000 claims abstract description 41
- 239000000843 powder Substances 0.000 claims abstract description 35
- 229910052602 gypsum Inorganic materials 0.000 claims abstract description 24
- 239000010440 gypsum Substances 0.000 claims abstract description 24
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 20
- 239000010959 steel Substances 0.000 claims abstract description 18
- 238000000465 moulding Methods 0.000 claims abstract description 17
- 239000000203 mixture Substances 0.000 claims abstract description 13
- 239000004575 stone Substances 0.000 claims abstract description 10
- 238000002156 mixing Methods 0.000 claims abstract description 8
- 238000000034 method Methods 0.000 claims description 41
- 239000000463 material Substances 0.000 claims description 14
- 238000001125 extrusion Methods 0.000 claims description 13
- 239000000126 substance Substances 0.000 claims description 11
- 238000009628 steelmaking Methods 0.000 claims description 8
- 238000001816 cooling Methods 0.000 claims description 7
- 238000003672 processing method Methods 0.000 claims 1
- 229910001385 heavy metal Inorganic materials 0.000 abstract description 24
- 238000006703 hydration reaction Methods 0.000 abstract description 6
- 238000010583 slow cooling Methods 0.000 abstract description 3
- 239000002657 fibrous material Substances 0.000 abstract 1
- 239000007787 solid Substances 0.000 abstract 1
- 238000001723 curing Methods 0.000 description 27
- 238000012360 testing method Methods 0.000 description 19
- 239000004568 cement Substances 0.000 description 17
- 238000007711 solidification Methods 0.000 description 17
- 230000008023 solidification Effects 0.000 description 16
- 238000010828 elution Methods 0.000 description 15
- ODINCKMPIJJUCX-UHFFFAOYSA-N Calcium oxide Chemical compound [Ca]=O ODINCKMPIJJUCX-UHFFFAOYSA-N 0.000 description 14
- 238000006243 chemical reaction Methods 0.000 description 11
- 239000010426 asphalt Substances 0.000 description 8
- 238000004898 kneading Methods 0.000 description 8
- 239000000292 calcium oxide Substances 0.000 description 7
- 235000012255 calcium oxide Nutrition 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000007789 gas Substances 0.000 description 6
- XFWJKVMFIVXPKK-UHFFFAOYSA-N calcium;oxido(oxo)alumane Chemical compound [Ca+2].[O-][Al]=O.[O-][Al]=O XFWJKVMFIVXPKK-UHFFFAOYSA-N 0.000 description 5
- 239000010813 municipal solid waste Substances 0.000 description 5
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 4
- UQSXHKLRYXJYBZ-UHFFFAOYSA-N Iron oxide Chemical compound [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 4
- 235000011941 Tilia x europaea Nutrition 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 4
- OSGAYBCDTDRGGQ-UHFFFAOYSA-L calcium sulfate Chemical compound [Ca+2].[O-]S([O-])(=O)=O OSGAYBCDTDRGGQ-UHFFFAOYSA-L 0.000 description 4
- 229910001653 ettringite Inorganic materials 0.000 description 4
- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 description 4
- 239000004571 lime Substances 0.000 description 4
- 239000002245 particle Substances 0.000 description 4
- 239000002994 raw material Substances 0.000 description 4
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 3
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 3
- 239000000920 calcium hydroxide Substances 0.000 description 3
- 235000011116 calcium hydroxide Nutrition 0.000 description 3
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 3
- 238000005056 compaction Methods 0.000 description 3
- 238000012937 correction Methods 0.000 description 3
- 238000007922 dissolution test Methods 0.000 description 3
- 230000007613 environmental effect Effects 0.000 description 3
- 238000005507 spraying Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- UXVMQQNJUSDDNG-UHFFFAOYSA-L Calcium chloride Chemical compound [Cl-].[Cl-].[Ca+2] UXVMQQNJUSDDNG-UHFFFAOYSA-L 0.000 description 2
- CPLXHLVBOLITMK-UHFFFAOYSA-N Magnesium oxide Chemical compound [Mg]=O CPLXHLVBOLITMK-UHFFFAOYSA-N 0.000 description 2
- 239000011398 Portland cement Substances 0.000 description 2
- 229910004298 SiO 2 Inorganic materials 0.000 description 2
- 239000000654 additive Substances 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- LFYJSSARVMHQJB-QIXNEVBVSA-N bakuchiol Chemical compound CC(C)=CCC[C@@](C)(C=C)\C=C\C1=CC=C(O)C=C1 LFYJSSARVMHQJB-QIXNEVBVSA-N 0.000 description 2
- 229910052793 cadmium Inorganic materials 0.000 description 2
- BDOSMKKIYDKNTQ-UHFFFAOYSA-N cadmium atom Chemical compound [Cd] BDOSMKKIYDKNTQ-UHFFFAOYSA-N 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- -1 cyanide compound Chemical class 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000155 melt Substances 0.000 description 2
- 238000002844 melting Methods 0.000 description 2
- 230000008018 melting Effects 0.000 description 2
- 229910052753 mercury Inorganic materials 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- 150000003839 salts Chemical class 0.000 description 2
- 239000002689 soil Substances 0.000 description 2
- 238000010998 test method Methods 0.000 description 2
- 229910018072 Al 2 O 3 Inorganic materials 0.000 description 1
- 239000004484 Briquette Substances 0.000 description 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 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
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 1
- 239000003513 alkali Substances 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 239000001110 calcium chloride Substances 0.000 description 1
- 229910001628 calcium chloride Inorganic materials 0.000 description 1
- JHLNERQLKQQLRZ-UHFFFAOYSA-N calcium silicate Chemical compound [Ca+2].[Ca+2].[O-][Si]([O-])([O-])[O-] JHLNERQLKQQLRZ-UHFFFAOYSA-N 0.000 description 1
- 229910052918 calcium silicate Inorganic materials 0.000 description 1
- 235000012241 calcium silicate Nutrition 0.000 description 1
- 229910052804 chromium Inorganic materials 0.000 description 1
- 239000011651 chromium Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000000748 compression moulding Methods 0.000 description 1
- 238000006477 desulfuration reaction Methods 0.000 description 1
- 230000023556 desulfurization Effects 0.000 description 1
- 238000011038 discontinuous diafiltration by volume reduction Methods 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005538 encapsulation Methods 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000003546 flue gas Substances 0.000 description 1
- 238000007429 general method Methods 0.000 description 1
- 238000005469 granulation Methods 0.000 description 1
- 230000003179 granulation Effects 0.000 description 1
- 239000003673 groundwater Substances 0.000 description 1
- 239000000383 hazardous chemical Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 230000036571 hydration Effects 0.000 description 1
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 1
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000000395 magnesium oxide Substances 0.000 description 1
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 1
- 230000007935 neutral effect Effects 0.000 description 1
- 150000002903 organophosphorus compounds Chemical class 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000012545 processing Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 238000007670 refining Methods 0.000 description 1
- 238000005464 sample preparation method Methods 0.000 description 1
- 238000005204 segregation Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000006104 solid solution Substances 0.000 description 1
- 238000005063 solubilization Methods 0.000 description 1
- 230000007928 solubilization Effects 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 239000011593 sulfur Substances 0.000 description 1
- 229910052717 sulfur Inorganic materials 0.000 description 1
Landscapes
- Fire-Extinguishing Compositions (AREA)
- Processing Of Solid Wastes (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は、一般廃棄物焼却灰(以
下、焼却灰と称する)の処理方法に関するものであり、
詳しくは焼却灰中の重金属溶出を抑制する方法に係るも
のである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating general waste incineration ash (hereinafter referred to as incineration ash),
Specifically, it relates to a method of suppressing elution of heavy metals in incinerated ash.
【0002】[0002]
【従来の技術】焼却灰は、多くの場合埋め立て処分され
ているが、埋め立て地の確保が年々難しくなっている現
在、その処分は次第に困難となりつつあり、焼却灰を埋
め立て用に使用したとしても、焼却灰から重金属等の有
害物質が雨水等により地下水等に溶出して、二次公害を
引き起こす恐れがある。また、焼却灰は非常に細かな粉
体であるがゆえに、含有されている重金属の安定化とと
もに減容化、もしくは埋め立て作業時の焼却灰粉塵飛散
防止等の制約があり、このため最近では造粒ないし成形
固化処理を行う例が数多くなってきている。2. Description of the Related Art Incinerated ash is often disposed of in landfills, but now that it is difficult to secure landfill sites, it is becoming increasingly difficult to dispose of it, and even if incinerated ash is used for landfills, , Hazardous substances such as heavy metals from incinerated ash may elute into groundwater etc. due to rainwater etc. and cause secondary pollution. In addition, since the incineration ash is a very fine powder, there are restrictions such as stabilization of the heavy metals contained, volume reduction, and prevention of incineration ash dust scattering during landfill work. There are many examples of performing grain or molding / solidification treatment.
【0003】焼却灰の一般的処理方法としては、セメン
ト固化法、アスファルト固化法、溶融固化法等が提案さ
れ一部実用化している。そこで、以下各焼却灰固化法に
ついて説明する。As a general method for treating incinerated ash, a cement solidification method, an asphalt solidification method, a melt solidification method, etc. have been proposed and partially put into practical use. Therefore, each incineration ash solidification method will be described below.
【0004】セメント固化法は、セメント中のアルカリ
成分による重金属の水酸化物化、セメント固化物による
重金属の吸着、セメント固化物中の成分と重金属との化
学結合、セメントゲルによる物理的封じ込み作用等によ
り、有害物質を固化物中に固定するもので、多くの場合
有害物質の溶出防止に効果的である。The cement solidification method includes hydroxide conversion of heavy metals by alkali components in cement, adsorption of heavy metals by cement solidification products, chemical bonding between components in cement solidification products and heavy metals, physical encapsulation by cement gel, etc. Therefore, the harmful substance is fixed in the solidified substance, and in many cases, it is effective in preventing the elution of the harmful substance.
【0005】アスファルト固化法は、アスファルトの加
熱により流動性が良くなるため、焼却灰とアスファルト
との混練性が良く成形物の均一化が可能で、成形直後も
適度な強度を有し長期強度の増加もあるため、成形物の
歩留まりが高い。また、アスファルト自体の撥水性によ
り成形物内部への浸水がしにくいため、埋め立て地で長
期に強度を有するといった特長がある。In the asphalt solidification method, since the fluidity is improved by heating the asphalt, the incineration ash and the asphalt can be kneaded well and the molded product can be made uniform. Since there is also an increase, the yield of molded products is high. In addition, the water repellency of the asphalt itself makes it difficult for water to enter the inside of the molded product, so it has the advantage of having long-term strength at the landfill.
【0006】溶融固化法は、燃料や電気により被溶融物
(焼却灰)を炉内において1200〜1500℃まで加
熱し、焼却灰を溶融してスラグ化する方法である。焼却
灰中の重金属のうち沸点の低いものは一部ガス中に揮発
するが、他の重金属はスラグ中に移行しガラス質のスラ
グとなり、冷却固化スラグからの重金属類の溶出を防止
することができる。すなわち、焼却灰中のシリカは溶融
した場合、SiO2 の網目構造となるが、スラグ中に移
行した重金属類をこの網目の中に包み込んだまま固化
し、極めて安全なガラス質となり重金属類の難溶化が可
能となる。The melt-solidification method is a method in which a material to be melted (incinerated ash) is heated to 1200 to 1500 ° C. in a furnace by fuel or electricity to melt the incinerated ash to form a slag. Of the heavy metals in the incinerated ash, those with a low boiling point are partially volatilized in the gas, but other heavy metals migrate into the slag and become glassy slag, which prevents the elution of heavy metals from the cooled and solidified slag. it can. That is, when the silica in the incineration ash melts, it becomes a network structure of SiO 2 , but the heavy metals that have migrated into the slag are solidified while being wrapped in this network and become an extremely safe glassy material, which makes it difficult Solubilization is possible.
【0007】[0007]
【発明が解決しようとする課題】しかしながら、セメン
ト固化法は、固化物の溶出試験における重金属の溶出濃
度が、一部判定基準値を満足しない場合があり、このよ
うな場合通常のセメント及び超速硬セメントなどの特殊
セメントを多量に使用するか、又は特別な処理法を適用
する必要があり、コスト的に不利である。また、セメン
ト系の固化法による固化物の利用法は重金属溶出濃度の
問題等により現在無く、投棄されているのが現状であ
り、いずれは投棄場が逼迫してくる問題を有する。However, in the cement solidification method, the elution concentration of heavy metals in the elution test of the solidified product may not partially meet the criterion standard value. In such a case, ordinary cement and ultra-rapid hardening are used. It is necessary to use a large amount of special cement such as cement or to apply a special treatment method, which is a cost disadvantage. In addition, there is currently no method of using the solidified material by the cement-based solidification method due to the problem of heavy metal elution concentration, etc., and the current situation is that it is dumped, and eventually there is a problem that the dump site becomes tight.
【0008】アスファルト固化法は、アスファルトが焼
却灰の空隙に入り込み粒子表面を充分被覆して固化させ
るには、圧縮成形する必要がある。しかし、成形工程が
煩雑であり連続処理が困難なので、セメント固化法に比
べてイニシャルコスト的には高いといった欠点がある。
また、この方法は、有害物質を物理的に包み込むという
意味しかなく、被覆が破壊した場合には有害物質が溶出
するという欠点が生じる。[0008] In the asphalt solidification method, it is necessary to carry out compression molding in order for the asphalt to enter the voids of the incineration ash and sufficiently coat and solidify the surface of the particles. However, since the molding process is complicated and continuous treatment is difficult, the initial cost is higher than that of the cement solidification method.
Further, this method only means that the harmful substance is physically wrapped, and there is a drawback that the harmful substance is eluted when the coating is broken.
【0009】溶融固化法は、セメント固化法及びアスフ
ァルト固化法に比べて溶融炉又はその付帯設備がゴミ焼
却炉の後工程に必要であり、建設費が嵩むとともに燃料
費等のランニングコストも他法に比べかなり割高になる
という問題を有する。Compared with the cement solidification method and the asphalt solidification method, the melting and solidification method requires a melting furnace or its auxiliary equipment in the post-process of the refuse incinerator, which increases construction costs and running costs such as fuel costs. There is a problem that it is considerably expensive compared to.
【0010】本発明は上記問題に鑑みてなされたもので
あって、重金属の溶出濃度が基準値範囲内に収まる固化
物を、低コストで得ることができる焼却灰の処理及び利
用方法を提供することを目的とする。The present invention has been made in view of the above problems, and provides a method for treating and utilizing incinerated ash, which is capable of obtaining a solidified product having a heavy metal elution concentration within a reference value range at low cost. The purpose is to
【0011】[0011]
【課題を解決するための手段】本発明は、一般廃棄物焼
却灰に、石膏を含有する高炉水砕微粉末を水とともに添
加・混合し、該混合物を押し出し成形機にて成形する。
石膏を含有する高炉水砕微粉末の他に、製鋼スラグ粉砕
品を添加・混合しても良い。更に、おが屑等の繊維物質
を添加・混合することもできる。押し出し成形機の成形
孔形状を異形状とすれば、表面積を大きくすることがで
きる。また、水和反応を持続させるため、成形物を蒸気
養生しながら、該成形物の積み付けた山の上層部へ、水
温60〜80℃ある高炉溶融スラグを徐冷する際に使用
した回収水を散水する。上記のように処理した成形物
は、そのまま、又は該成形物を5〜0mmに粒調して粉
砕品としてから、1〜10重量%程度を天然砕石あるい
は鉄鋼スラグへ添加・混合することにより路盤材として
利用できる。According to the present invention, blast furnace granulated fine powder containing gypsum is added to and mixed with incinerator ash of general waste together with water, and the mixture is molded by an extrusion molding machine.
In addition to ground granulated blast furnace powder containing gypsum, a crushed steelmaking slag product may be added and mixed. Further, a fiber substance such as sawdust may be added and mixed. If the shape of the molding hole of the extrusion molding machine is made different, the surface area can be increased. Further, in order to maintain the hydration reaction, while recovering the molded product with steam, the recovered water used when slowly cooling the blast furnace molten slag having a water temperature of 60 to 80 ° C. is provided to the upper layer portion of the pile where the molded product is stacked. Sprinkle water. The molded product treated as described above may be used as it is or as a crushed product having a particle size of the molded product of 5 to 0 mm, and then about 1 to 10% by weight is added to and mixed with natural crushed stone or steel slag to prepare a roadbed. It can be used as a material.
【0012】[0012]
【発明の実施の形態】】一般廃棄物焼却工場では、有害
ガス除去を行う目的で排ガス中へ消石灰を添加している
が、その際ガス中の塩化水素ガス及び硫黄成分と消石灰
が反応して、塩化カルシウム及び無水石膏を生成し、ま
た、未反応の消石灰は高温ガスにより生石灰に変化す
る。これら生成物は集塵機で回収され焼却灰中へ混入さ
れる。この生成物を含有した焼却灰と石膏含有高炉水砕
微粉末及び水分が添加・混練されると、次式のような反
応形態を示す。BEST MODE FOR CARRYING OUT THE INVENTION In a municipal solid waste incineration plant, slaked lime is added to the exhaust gas for the purpose of removing harmful gases. At that time, hydrogen chloride gas and sulfur components in the gas react with slaked lime. , Calcium chloride and anhydrous gypsum are produced, and unreacted slaked lime is changed into quick lime by high temperature gas. These products are collected by a dust collector and mixed into incinerated ash. When the incinerated ash containing this product, the ground granulated blast furnace fine powder containing gypsum and water are added and kneaded, a reaction form as shown in the following formula is exhibited.
【0013】 C5AS3+2C+16H→C4AH13+3CSH(1)‥‥‥‥‥‥‥ C5AS3+2Cs+76/3H→3CSH(1)+2/3〔C3ACs3H32〕+ 2/3Al(OH)3‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥ ただし、C=CaO,A=Al2O3,S=SiO2,H
=H2O,Cs=CaSO4である。また、C5AS3は高
炉水砕微粉末、CSH(1)はカルシウムハイドロシリ
ケート、C4AH13はアルミン酸カルシウム、C3ACs
3H32はエトリンガイトである。[0013] C 5 AS 3 + 2C + 16H → C 4 AH 13 + 3CSH (1) ‥‥‥‥‥‥‥ C 5 AS 3 + 2Cs + 76 / 3H → 3CSH (1) +2/3 [C 3 ACs 3 H 32] + 2 / 3Al (OH) 3 ‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥‥ C = CaO, A = Al 2 O 3 , S = SiO 2 , H
= H 2 O and Cs = CaSO 4 . C 5 AS 3 is ground granulated blast furnace powder, CSH (1) is calcium hydrosilicate, C 4 AH 13 is calcium aluminate, C 3 ACs
3 H 32 is ettringite.
【0014】焼却灰をセメント固化した場合、焼却灰中
の重金属特に鉛、カドミウム等は、セメント水和反応か
ら生成されるアルミン酸カルシウムやエトリンガイト中
のAl原子と置換固溶し、難溶性の塩として固定される
が、一方、石膏含有高炉水砕微粉末は構造、組成上ポル
トランドセメントと異なり、ガラス質で塩基度が低くA
l2O3を15%含有するので水和特性が強く、焼却灰へ
石膏含有高炉水砕微粉末を水と共に添加・混合した場合
には、上記,式の反応形態中のアルミン酸カルシウ
ムとエトリンガイトが多量かつ長期にわたって生成す
る。以上により石膏含有高炉水砕微粉末は、ポルトラン
ドセメントに比べて焼却灰中の重金属固定能力が優れて
いる。When the incinerated ash is solidified with cement, heavy metals in the incinerated ash, particularly lead, cadmium, etc., are solid-dissolved by substitution with calcium aluminate produced by the cement hydration reaction and Al atoms in ettringite, and are insoluble salts. On the other hand, the ground granulated blast furnace fine powder containing gypsum, unlike the structure and composition of Portland cement, is vitreous and has a low basicity.
Since it contains 15% of 1 2 O 3 , it has a strong hydration property, and when gypsum-containing granulated blast furnace fine powder is added and mixed with incinerated ash together with water, calcium aluminate and ettringite in the reaction form of the above formula are added. Is produced in large quantities over a long period of time. As described above, the gypsum-containing granulated fine powder of blast furnace is superior to Portland cement in the ability to fix heavy metals in incinerated ash.
【0015】次に、石膏を含有していない高炉水砕微粉
末を焼却灰へ水と共に添加・混合した場合について以下
説明する。上記で説明したように、一般廃棄物焼却工場
では、排煙脱硫工程から生成した塩化カルシウム,無水
石膏,生石灰が焼却灰中へ混入されているが、該無水石
膏と生石灰の生成割合を比較した場合、まず生石灰につ
いては無水石膏と比べて生成量が多いため、式の反応
は充分促進されアルミン酸カルシウムが多量に生成す
る。しかし、無水石膏については生石灰に比べて生成量
が少ない上に、焼却炉内挙動等の要因に左右され、生成
量がその都度変化するので、上記式でのエトリンガイ
ト生成量が安定しないため、高炉水砕微粉末配合成形物
からの重金属溶出が、基準値を外れる場合がある。すな
わち、固化物の重金属溶出を常時安定的に規定内に抑え
るには、石膏含有高炉水砕微粉末を一定量以上添加する
ことが必要となる。Next, the case of adding and mixing granulated blast furnace fine powder containing no gypsum with water together with water will be described. As described above, in a general waste incineration plant, calcium chloride, anhydrous gypsum, and quick lime produced from the flue gas desulfurization process are mixed in the incineration ash. The production rates of the anhydrous gypsum and quick lime were compared. In this case, since the amount of quick lime produced is larger than that of anhydrous gypsum, the reaction of the formula is sufficiently promoted and a large amount of calcium aluminate is produced. However, the amount of anhydrous gypsum produced is less than that of quicklime, and the amount of ettringite produced in the above formula is not stable because the amount produced varies depending on factors such as the behavior in the incinerator, etc. The elution of heavy metals from granulated fine powder blended molded products may deviate from the standard value. That is, it is necessary to add a certain amount or more of gypsum-containing granulated blast furnace fine powder in order to constantly and stably suppress the heavy metal elution of the solidified product within the prescribed range.
【0016】一方、製鋼スラグは、石灰(CaO),シ
リカ(SiO2)を主成分とし、その他マグネシア(M
gO),酸化鉄(FeO,Fe2O3)及び酸化マンガン
(MnO)等を含有している。石灰は製鋼の精錬時に副
原料として用いられ、十分スラグ化されないと不安定な
状態のままスラグ中に残存する。この石灰分は遊離石灰
(free−CaO)と呼ばれ、この遊離石灰が高炉水
砕微粉末中性分C5AS3と反応し、式に示すようにC
4AH13アルミン酸カルシウムを長期かつ多量に生成
し、前述したように重金属はこのC4AH13のAl原子
と置換固溶し、難溶性の塩として固定化される。On the other hand, steelmaking slag contains lime (CaO) and silica (SiO 2 ) as main components, and other magnesia (M
gO), iron oxide (FeO, Fe 2 O 3 ) and manganese oxide (MnO). Lime is used as an auxiliary raw material during the refining of steel making, and remains in the slag in an unstable state if not sufficiently slagged. This lime component is called free lime (free-CaO), and this free lime reacts with blast furnace granulated fine powder neutral component C 5 AS 3 to give C as shown in the equation.
A large amount of 4 AH 13 calcium aluminate is produced for a long period of time, and as described above, the heavy metal substitutes for the Al atom of C 4 AH 13 to form a solid solution and is immobilized as a sparingly soluble salt.
【0017】供試体の成形方法については、他の成形方
法、例えばパン型造粒機又はブリケットマシーン等を使
用した場合は、最適造粒・成形水分が10〜15%であ
り、上記式,式の反応初期に必要な水分が得られ
ず、また混合物が加圧されることにより密度を高め強度
も向上するため、本発明においての成形方法は押し出し
成形法を採用した。Regarding the method of molding the specimen, when other molding methods such as a pan type granulator or a briquette machine are used, the optimum granulation / molding water content is 10 to 15%. Since the required water content is not obtained in the initial stage of the reaction and the mixture is pressed to increase the density and the strength, the extrusion method is adopted as the molding method in the present invention.
【0018】養生方法については、気中,水中養生等が
考えられるが、処理水の問題等経済性を考慮し当初は気
中養生とした。しかし気中養生は、長期の養生時間とそ
れに伴う広大な養生ヤードを要するという問題が発生す
るため、本発明は上記による促進養生に着目した。The curing method may be atmospheric curing, underwater curing, etc. In consideration of economic efficiency such as the problem of treated water, the initial curing method was air curing. However, since air curing causes a problem of requiring a long curing time and a vast curing yard associated therewith, the present invention focused on the accelerated curing described above.
【0019】蒸気養生方法については蒸気配管を床部に
設け、その上に対象物いわゆる成形物を積み付けるが、
床部からの蒸気は積み付け山の上層部まで行き届かず、
上層部雰囲気温度が低くなり、前述式,式の反応が
促進されない欠点を有する。そこで、本発明では、水温
が60〜80℃ある高炉溶融スラグを徐冷する際に使用
した水の回収水に着目した。該回収水は、PHも高く水
温が60〜80℃あるため積み付け山の上層部へ適宜散
水すると、上層部はアルカリ雰囲気と60〜80℃の温
度雰囲気及び適量の水分が保たれ、前述式,式の反
応が促進される。Regarding the steam curing method, a steam pipe is provided on the floor, and a so-called molded object is stacked on it.
The steam from the floor does not reach the upper layers of the loading mountain,
There is a drawback that the temperature of the atmosphere in the upper layer becomes low and the reaction of the above equations and equations is not promoted. Therefore, in the present invention, attention was paid to the recovered water of the water used when gradually cooling the blast furnace molten slag having a water temperature of 60 to 80 ° C. Since the recovered water also has a high PH and a water temperature of 60 to 80 ° C., if water is appropriately sprayed to the upper layer portion of the pile, the upper layer portion retains an alkaline atmosphere, a temperature atmosphere of 60 to 80 ° C., and an appropriate amount of water. The reaction of the formula is accelerated.
【0020】また、更に式,式の反応を促進する方
法として、押し出し成形時の成形孔を異形状とすること
で、蒸気養生時の該成形物と蒸気との接触面積を増やし
蒸気養生効果を向上させる方法を本発明では発案した。
ただし、後述する実施例4では、該成形物の表面積の増
加の指標として成形物の単位容積質量を採用した。これ
は、焼却灰と石膏含有高炉水砕微粉末との同一配合にお
いて異形状とした成形物の方が、それ同士が噛み合わせ
が良くなり単位容積質量を大きくし、結果的には該異形
状成形物が蒸気養生時の積み付けの際、表面積が大とな
り式,式の反応を促進させる。Further, as a method of further promoting the reaction of the formula, the forming hole at the time of extrusion molding is made to have a different shape, thereby increasing the contact area between the molded product and steam at the time of steam curing to improve the steam curing effect. The present invention has devised a way to improve.
However, in Example 4 described later, the unit volume mass of the molded product was adopted as an index of the increase in the surface area of the molded product. This is because when the incineration ash and the gypsum-containing granulated blast furnace fine powder of the same composition have different shapes, they are better meshed with each other and the unit volume mass is increased. When the molded products are packed during steam curing, they have a large surface area and accelerate the reaction of the formula.
【0021】他の式,式の反応を促進する方法とし
て、成形物をポーラス状にすれば蒸気養生時に該成形物
内部へ蒸気が行き渡り易くなり、更に蒸気養生時に適宜
散水する水(高炉溶融スラグを徐冷する際に使用した水
の回収水)の該成形物の吸水性を向上させる効果をも有
し、式,式の反応を促進する。この手段としては、
焼却灰への石膏含有高炉水砕微粉末の配合・混練時にお
が屑等の繊維物質を加え、該成形物の表面を粗面化及び
内部ポーラス化とする。この方法の効果確認として、実
施例5では焼却灰と石膏含有高炉水砕微粉末との同一配
合において、おが屑の添加有無における成形物の吸水率
比較でポーラス化を確認した。As a method of accelerating the reaction of other formulas, if the molded product is made into a porous shape, the steam easily spreads inside the molded product during steam curing, and further water sprinkled appropriately during steam curing (blast furnace molten slag). It also has an effect of improving the water absorption of the molded product of the recovered water used for the slow cooling), and accelerates the reaction of the formula. This means:
A fibrous substance such as sawdust is added at the time of mixing and kneading the gypsum-containing granulated blast furnace fine powder into incinerated ash to roughen the surface of the molded product and to make it internal porous. In order to confirm the effect of this method, in Example 5, in the same mixture of incinerated ash and gypsum-containing granulated blast furnace fine powder, it was confirmed that the formed article was porous by comparing the water absorption rate of the molded product with and without the addition of sawdust.
【0022】一方、蒸気処理を施した成形物は相対的に
天然砕石又は鉄鋼スラグより強度が低いため、天然砕石
あるいは鉄鋼スラグへ所定量添加・混合し転圧すること
で路盤材として良好な粒度と転圧効果が得られる。ま
た、この成形物には高炉水砕微粉末が配合され、なおか
つ蒸気養生時に散水された水(高炉溶融スラグを徐冷す
る際に使用した水の回収水)が該成形物に保持されてい
るため、長期に渡り水和反応が続き、路盤材としての強
度を安定的に保つ効果を有する。また、蒸気養生中に散
水した水が吸水性の高い該成形物へ保水され、その状態
で現場において天然砕石あるいは鉄鋼スラグと共に施工
され、施工後、該成形物が天然砕石あるいは鉄鋼スラグ
の水分を吸水し最適含水比状態を崩す恐れがないため、
路盤材の最適含水比調整を簡単にできる。しかし、成形
物が乾燥した状態で現場施工する際は、該成形物が吸水
し最適含水比を保つのが困難となる。On the other hand, since the molded product subjected to the steam treatment is relatively lower in strength than natural crushed stone or steel slag, it is possible to add a predetermined amount to natural crushed stone or steel slag and mix it to obtain a good particle size as a roadbed material. A compaction effect can be obtained. Further, this molded product is blended with ground granulated blast furnace powder, and the water sprinkled during steam curing (recovered water of water used when gradually cooling the blast furnace molten slag) is retained in the molded product. Therefore, the hydration reaction continues for a long period of time, and has the effect of stably maintaining the strength of the roadbed material. Further, water sprinkled during steam curing is retained in the molded article having high water absorbency, and in that state, it is constructed with natural crushed stone or steel slag at the site, and after the construction, the molded article removes moisture of natural crushed stone or steel slag. Since there is no risk of absorbing water and breaking the optimum water content ratio state,
It is possible to easily adjust the optimum water content of the roadbed material. However, when the molded product is applied on site in a dry state, the molded product absorbs water and it is difficult to maintain the optimum water content ratio.
【0023】また、成形物を5〜0mmに粉砕・粒調し
たものを天然砕石又は鉄鋼スラグへ添加・混合した場合
は、該成形物を有姿で添加・混合した際より天然砕石又
は鉄鋼スラグの間隙へ偏析なく分散し上記の効能を更に
向上させるものである。When a molded product crushed to a grain size of 5 to 0 mm is added to and mixed with natural crushed stone or steel slag, the natural crushed stone or steel slag is added more than when the molded product is tangibly added and mixed. It is dispersed in the gaps of No. 1 without segregation to further improve the above effects.
【0024】[0024]
【実施例】以下、本発明の実施例について説明する。Embodiments of the present invention will be described below.
【0025】(実施例1)一般廃棄物焼却工場より発生
した焼却灰を用い、まずテスト1として高炉水砕微粉末
(ブレーン値:約4000cm2、以下同じ)を0〜5
0%混合し押し出し成形を行い、気中養生後、重金属溶
出試験を実施した。結果を表1に示す。(Example 1) Incinerator ash generated from a municipal solid waste incineration plant was used, and as test 1, 0 to 5 granulated blast furnace fine powder (Blaine value: about 4000 cm 2 , the same applies hereinafter) was used.
After mixing in 0% and extruding and curing in air, a heavy metal elution test was performed. The results are shown in Table 1.
【0026】[0026]
【表1】 [Table 1]
【0027】サンプル作成方法は、石膏含有高炉水砕微
粉末と焼却灰(混練温度は実機設備に準じ乾燥機で昇温
を行い、約50℃で行った)を、表1のテスト水準の各
配合割合に準じてJISR5201に記載されている練
り混ぜ機により空練りを5分間行い、次に空練り原料を
水分30%に調湿し再度3分間混練した後、練り混ぜ機
を一旦停止して練り、はち底部及びパドルに付着してい
る原料を30秒間でかき落とした後、再度3分間混練し
た。次に、該混練原料を、処理能力400kg/hrの
双軸押し出し成形機にて直径10mm,長さ約30〜5
0mmの大きさに成形し供試料とした。The sample preparation method was as follows: Granulated gypsum-containing granulated blast furnace powder and incinerated ash (kneading temperature was raised at about 50 ° C. in a dryer according to actual equipment) According to the mixing ratio, dry kneading is carried out for 5 minutes by a kneading machine described in JISR5201, then the air kneading raw material is adjusted to a water content of 30% and kneaded again for 3 minutes, and then the kneading machine is temporarily stopped. After kneading, the raw materials adhering to the bottom of the bee and the paddle were scraped off for 30 seconds, and then kneaded again for 3 minutes. Next, the kneading raw material was processed by a twin-screw extrusion molding machine having a processing capacity of 400 kg / hr to have a diameter of 10 mm and a length of about 30 to 5
The sample was molded into a size of 0 mm.
【0028】重金属溶出試験については、表2に示した
セメント固化体溶出試験結果から、規定外成分は鉛のみ
であるため今回は対象成分を鉛として、環境庁告示第1
3号により実施した。なお、溶出試験用試料の粒度は安
全性を考慮し0.5〜0mmのサイズとした。Regarding the heavy metal elution test, from the results of the elution test of the cement solidified body shown in Table 2, since the only non-regular component is lead, the target component was lead this time and the Environmental Agency Notification No. 1
It carried out by No. 3. The particle size of the dissolution test sample was set to 0.5 to 0 mm in consideration of safety.
【0029】[0029]
【表2】 [Table 2]
【0030】次に、テスト2として、テスト1で実施し
た高炉水砕微粉末の添加量の削減も含めて、製鋼スラグ
粉砕品(サイズ:1.2〜0mm,以下同じ)を10,
15%のみと高炉水砕微粉末5%に製鋼スラグ粉砕品を
10,15%添加・混合し、押し出し成形を行い、気中
養生後、重金属溶出試験を実施した。結果を表3に示
す。Next, in Test 2, the slag crushed steelmaking product (size: 1.2 to 0 mm, the same hereinafter) including 10, including the reduction of the addition amount of the granulated blast furnace fine powder in Test 1,
Only 15% and 10% crushed steelmaking slag product was added and mixed with granulated blast furnace fine powder 5%, and extrusion molding was carried out. After curing in air, heavy metal elution test was carried out. Table 3 shows the results.
【0031】[0031]
【表3】 [Table 3]
【0032】テスト結果については、テスト1では高炉
水砕微粉末添加20%で、養生6週間後の鉛溶出試験結
果は不検出となった。またテスト2では高炉水砕微粉末
5%を加えたものに、転炉スラグ粉砕品を10,15%
を添加した結果、灰単味の鉛溶出試験結果がテスト1で
は1.05mg/lに対し、テスト2では約3倍の2.
94mg/lという値を示しているにもかかわらず、養
生5週目において新水質環境基準値(鉛:0.01mg
/l以下)を満足した。ここで表4に製鋼(転炉)スラ
グの成分例を示す。With respect to the test results, in Test 1, the addition of 20% of granulated blast furnace fine powder and lead leaching test results after 6 weeks of curing were not detected. Also, in Test 2, 10% and 15% of the crushed converter slag were added to 5% of granulated blast furnace powder.
As a result, the lead elution test result of ash alone was 1.05 mg / l in Test 1 and about 3 times in Test 2 2.
Despite the value of 94 mg / l, the new water quality environmental standard value (lead: 0.01 mg at the 5th week of curing)
/ L or less) was satisfied. Here, Table 4 shows examples of the components of steelmaking (converter) slag.
【0033】[0033]
【表4】 [Table 4]
【0034】更に、高炉水砕微粉末5%,製鋼スラグ粉
砕品10%を配合して10週間気中養生し、主な水質環
境基準項目(カドミウム,シアン化合物,有機リン化合
物,鉛,六価クロム,総水銀,アルキル水銀,PCB)
の溶出試験を実施したところ、全てについて不検出とな
った。Further, 5% of granulated blast furnace fine powder and 10% of crushed steelmaking slag were blended and cured in air for 10 weeks. Main water quality environmental standard items (cadmium, cyanide compound, organophosphorus compound, lead, hexavalent) Chromium, total mercury, alkyl mercury, PCB)
When the dissolution test was conducted, all were not detected.
【0035】(実施例2)一般廃棄物焼却工場から発生
した焼却灰に、一般廃棄物焼却工場から発生したセメン
ト固化体を採取したもの及び石膏含有高炉水砕微粉末を
実施例1に準じて混合し、同様に成形した。これを、水
温80℃ある高炉溶融スラグを徐冷する際に使用した水
の回収水を適宜散水しながら、蒸気圧力2kgf/cm
2で6時間養生・12時間養生及び蒸気養生のみで蒸気
圧力2kgf/cm2で6時間養生・12時間養生し各
々の溶出試験を実施した。結果を表5に示す。(Example 2) Incinerator ash generated from a municipal solid waste incineration plant, solidified cement produced from a municipal solid waste incineration plant and gypsum-containing ground granulated blast furnace fine powder were used in accordance with Example 1. Mixed and molded similarly. While appropriately spraying the recovered water of the water used when slowly cooling the blast furnace molten slag having a water temperature of 80 ° C., a steam pressure of 2 kgf / cm
Only 2 in 6 hours curing, 12 hours curing and steam curing in aged in steam pressure 2 kgf / cm 2 for 6 hours curing, 12 hours a dissolution test was performed for each. Table 5 shows the results.
【0036】[0036]
【表5】 [Table 5]
【0037】(実施例3)一般廃棄物焼却工場から発生
した焼却灰と石膏含有高炉水砕微分末を実施例1に準じ
て成形した。ただし、押し出し成形機の成形孔を通常の
円形とした場合と異形状とした場合の二形態で成形し
た。その成形物を、水温80℃ある高炉溶融スラグを徐
冷する際に使用した水の回収水を適宜散水しながら蒸気
圧力2kgf/cm2で12時間養生した。そこで養生
済該成形物の乾燥単位容積質量を測定比較した。結果を
表6に示す。(Example 3) Incinerator ash and gypsum-containing granulated blast furnace differential powder generated from a general waste incineration plant were molded according to Example 1. However, the extrusion was performed in two forms, that is, the case where the forming hole of the extruder is a normal circle and the case where the forming hole is a different shape. The molded product was aged at a steam pressure of 2 kgf / cm 2 for 12 hours while appropriately spraying recovered water of water used for gradually cooling the blast furnace molten slag having a water temperature of 80 ° C. Therefore, the dry unit volume mass of the cured molded article was measured and compared. Table 6 shows the results.
【0038】[0038]
【表6】 [Table 6]
【0039】(実施例4)一般廃棄物焼却工場から発生
した焼却灰と石膏含有高炉水砕微粉末を実施例1に準じ
て成形した。ただし、石膏含有高炉水砕微粉末添加・混
合時に、おが屑を添加したものと添加しないものの二形
態について、成形孔を通常の円形として成形し、その成
形物を、水温80℃である高炉溶融スラグを徐冷する際
に使用した水の回収水を適宜散水しながら蒸気圧力2k
gf/cm2で12時間養生した。そこで養生済該成形
物の吸水率を測定比較した。結果を表7に示す。(Example 4) Incinerator ash and gypsum-containing granulated blast furnace fine powder generated from a municipal solid waste incineration plant were molded according to Example 1. However, when adding / mixing granulated gypsum-containing granulated blast furnace powder, two forms, one with and without sawdust added, are formed into normal circular shaped holes, and the formed product is a blast furnace molten slag with a water temperature of 80 ° C. Steam pressure of 2k while sprinkling the recovered water used for slow cooling
It was aged at gf / cm 2 for 12 hours. Therefore, the water absorption of the cured molded article was measured and compared. Table 7 shows the results.
【0040】[0040]
【表7】 [Table 7]
【0041】(実施例5)実施例2における回収水を適
宜散水しながら蒸気養生を12時間行った成形物を有姿
又は5〜0mmに粉砕したもの(成形物の一軸圧縮強度
は4週で70kgf/cm2以上)を、鉄鋼スラグ路盤
材MS25に各々4%,10%添加し、一軸圧縮強度を
測定したところ、基になるMS25の一軸圧縮強度は
9.6kgf/cm2に対し、有姿4%で13.9kg
f/cm2,有姿10%で15.8kgf/cm2,また
5〜0mm粉砕品4%で17.1kgf/cm2,5〜
0mm粉砕品10%で18.8kgf/cm2となり、
規格値12kgf/cm2以上を充分満足する結果とな
った。ちなみにこの時の通常生産におけるHMS25は
14.5kgf/cm2であった。なお、この一軸圧縮
強度試験方法は、添加材を混合した鉄鋼スラグ路盤材を
約15kgを最適含水比(締め固め試験により求め、通
常9〜10%)で24時間保持したものを、「JISA
5015道路用鉄鋼スラグ」により、10cmモールド
にて4.5kgランマーで3層42回突き固めたものを
13日間、温度20℃、湿度60%の恒温恒湿室におい
た後、1日水浸し圧縮するものである。結果は表8に示
す。(Example 5) A molded product obtained by steam curing for 12 hours while appropriately spraying the recovered water in Example 2 and crushed to a size or 5 to 0 mm (uniaxial compressive strength of molded product in 4 weeks) 70 kgf / cm 2 or more) was added to the steel slag roadbed material MS25 at 4% and 10%, respectively, and the uniaxial compressive strength was measured. As a result, the base MS25 had a uniaxial compressive strength of 9.6 kgf / cm 2 . 13.9 kg with 4% appearance
f / cm 2, 17.1kgf / cm 2 at Yusugata 10% 15.8kgf / cm 2, and in 5~0mm crushed product 4%, 5
With 0% crushed product 10%, 18.8 kgf / cm 2
The result was that the standard value of 12 kgf / cm 2 or more was sufficiently satisfied. Incidentally, HMS25 in the normal production at this time was 14.5 kgf / cm 2 . In addition, this uniaxial compressive strength test method is a method in which about 15 kg of a steel slag roadbed material mixed with an additive material is held at an optimum water content ratio (obtained by a compaction test, usually 9 to 10%) for 24 hours, and the "JIS A
"5015 Road steel slag" was crushed in a 10 cm mold with a 4.5 kg Rammer for 3 layers 42 times, and placed in a constant temperature and humidity room at a temperature of 20 ° C and a humidity of 60% for 13 days, and then immersed in water for 1 day for compression. It is a thing. The results are shown in Table 8.
【0042】[0042]
【表8】 [Table 8]
【0043】(実施例6)実施例2と同様の成形物を有
姿で鉄鋼スラグMS25にそれぞれ4%,10%添加
し、15cmモールドにて4.5kgランマーで3層9
2回突き固め、4日間水浸の後行ったCBR試験におい
て、もとのMS25のCBR値は287%に対し、4%
添加で322%,10%添加で400%の値となり、道
路用材としての強度向上に効果がみられた。なお、供試
体はJISA1211路床土支持力(CBR)試験方法
に則り、添加材を混合したものを約10kg、含水比9
〜10%24時間保持したものを、JISA1210の
突き固めによる土の締め固め試験方法で作成した。結果
は表9に示す。(Example 6) A molded product similar to that of Example 2 was added to steel slag MS25 in the form of 4% and 10%, respectively, and a 15 cm mold was used to form a 4.5 kg Rammer in three layers 9
In the CBR test conducted by tamping twice and soaking in water for 4 days, the original CBR value of MS25 was 4% compared to 287%.
Addition of 322% and addition of 10% resulted in a value of 400%, which was effective in improving the strength as a road material. In addition, the test piece was approximately 10 kg with a mixture of additive materials and a water content ratio of 9 in accordance with the JIS A1211 subgrade soil bearing capacity (CBR) test method.
What was held for 10% to 10% for 24 hours was prepared by the method of compaction test of soil by tamping with JIS A1210. The results are shown in Table 9.
【0044】[0044]
【表9】 [Table 9]
【0045】[0045]
【発明の効果】本発明は、一般廃棄物焼却灰と少量の石
膏含有高炉水砕微粉末更に製鋼スラグ粉砕品及びおが屑
等の繊維物質を配合し、成形もしくは異形状成形するも
ので、一般廃棄物焼却灰からの重金属溶出を、廉価に入
手できる廃棄材料を利用して抑制できる。また、一般廃
棄物焼却灰を含む全ての廃棄材料を、重金属溶出しない
安全性が高い、かつ経済性や吸水性等が優れた成形物と
して再生できる。INDUSTRIAL APPLICABILITY The present invention is one in which general waste incineration ash and a small amount of gypsum-containing ground granulated blast furnace fine powder, steel slag crushed products, and fibrous substances such as sawdust are mixed and molded or shaped into different shapes. Elution of heavy metals from incinerated ash can be suppressed by using waste materials that are available at low cost. In addition, all waste materials, including general waste incineration ash, can be regenerated as molded articles that are highly safe and do not elute heavy metals, and that have excellent economic efficiency and water absorption.
【0046】成形後に、高炉溶融スラグを徐冷する際に
使用した水の回収水を適宜添加しながら蒸気養生するこ
とにより、長期に渡り水和反応を持続させることができ
る。また、成形物もしくは該成形物を5〜0mmに粉砕
・粒調したものを天然砕石もしくは鉄鋼スラグへ添加・
混合することで、路盤材としても有効利用することがで
きる。After the molding, the hydration reaction can be maintained for a long period of time by steam-curing while appropriately adding the recovered water of the water used for slowly cooling the blast furnace molten slag. Further, a molded product or a product obtained by crushing and molding the molded product into 5 to 0 mm is added to natural crushed stone or steel slag.
By mixing, it can be effectively used as a roadbed material.
─────────────────────────────────────────────────────
─────────────────────────────────────────────────── ───
【手続補正書】[Procedure amendment]
【提出日】平成8年7月23日[Submission date] July 23, 1996
【手続補正1】[Procedure amendment 1]
【補正対象書類名】明細書[Document name to be amended] Statement
【補正対象項目名】0036[Correction target item name] 0036
【補正方法】変更[Correction method] Change
【補正内容】[Correction contents]
【0036】[0036]
【表5】 [Table 5]
フロントページの続き (72)発明者 加藤 範行 千葉県君津市君津1番地 新日本製鐵株式 会社君津製鐵所サービスセンタービル内株 式会社鐵原君津支店内 (72)発明者 奥村 博昭 千葉県君津市君津1番地 新日本製鐵株式 会社君津製鐵所内Front Page Continuation (72) Inventor Noriyuki Kato 1 Kimitsu, Kimitsu-shi, Chiba Nippon Steel Co., Ltd. Kimitsu Works Co., Ltd. Service Center Building Stock company, Mr. Kimitsu Branch, (72) Inventor Hiroaki Okumura Kimitsu, Chiba Prefecture Kimitsu No. 1 Kimitsu Steel Works, Nippon Steel Co., Ltd.
Claims (7)
水砕微粉末を水とともに添加・混合し、該混合物を押し
出し成形機にて成形することを特徴とする一般廃棄物焼
却灰の処理方法。1. A general waste incineration ash, characterized in that blast furnace granulated fine powder containing gypsum is added to and mixed with general waste incineration ash, and the mixture is molded by an extrusion molding machine. Processing method.
水砕微粉末と製鋼スラグ粉砕品とを水とともに添加・混
合し、該混合物を押し出し成形機にて成形することを特
徴とする一般廃棄物焼却灰の処理方法。2. A blast furnace granulated fine powder containing gypsum and a steel slag crushed product are added and mixed with water to municipal waste incineration ash, and the mixture is molded by an extrusion molding machine. General waste incineration ash treatment method.
水砕微粉末を水とともに添加・混合し、更におが屑等の
繊維物質を添加・混合し、該混合物を押し出し成形機に
て成形することを特徴とする一般廃棄物焼却灰の処理方
法。3. A blast furnace granulated fine powder containing gypsum is added and mixed with water to general waste incineration ash, and fibrous substances such as sawdust are added and mixed, and the mixture is molded by an extrusion molding machine. A method for treating municipal waste incineration ash, characterized by:
水砕微粉末と製鋼スラグ粉砕品とを水とともに添加・混
合し、更におが屑等の繊維物質を添加・混合し、該混合
物を押し出し成形機にて成形することを特徴とする一般
廃棄物焼却灰の処理方法。4. A blast furnace granulated fine powder containing gypsum and a crushed steelmaking slag product are added and mixed with water to municipal waste incineration ash, and fibrous substances such as sawdust are added and mixed, and the mixture is mixed. A method for treating general waste incineration ash, which comprises molding with an extrusion molding machine.
ることを特徴とする請求項1、2、3又は4に記載の一
般廃棄物焼却灰の処理方法。5. The method for treating general waste incineration ash according to claim 1, 2, 3 or 4, wherein the shape of the molding hole of the extrusion molding machine is made different.
生しながら、該成形物の積み付けた山の上層部へ、水温
60〜80℃ある高炉溶融スラグを徐冷する際に使用し
た水の回収水を散水することを特徴とする請求項1、
2、3、4又は5に記載の一般廃棄物焼却灰の処理方
法。6. The water used for slowly cooling the blast furnace molten slag having a water temperature of 60 to 80 ° C. to the upper layer portion of the pile on which the molded product is stacked while steam-curing the molded product molded by an extrusion molding machine. Collected water is sprinkled, Claim 1 characterized by the above-mentioned.
The method for treating municipal waste incineration ash according to 2, 3, 4 or 5.
た成形物、又は該成形物を5〜0mm粒調した粉砕品
を、1〜10重量%の範囲で天然砕石あるいは鉄鋼スラ
グへ添加・混合し、路盤材とすることを特徴とする一般
廃棄物焼却灰の処理方法。7. A molded product treated according to claim 1, 2, 3, 4, 5 or 6, or a crushed product obtained by adjusting the molded product to a grain size of 5 to 0 mm in a range of 1 to 10% by weight for natural crushed stone or A method for treating general waste incineration ash, which is characterized by adding to and mixing with steel slag to make roadbed material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7352103A JPH09174019A (en) | 1995-12-27 | 1995-12-27 | Treatment of general waste incineration ash |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP7352103A JPH09174019A (en) | 1995-12-27 | 1995-12-27 | Treatment of general waste incineration ash |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH09174019A true JPH09174019A (en) | 1997-07-08 |
Family
ID=18421804
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP7352103A Withdrawn JPH09174019A (en) | 1995-12-27 | 1995-12-27 | Treatment of general waste incineration ash |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH09174019A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE1015866A3 (en) * | 2003-01-31 | 2005-10-04 | Group Portier Ind | Incinerator smoke solid residue treatment comprises washing with hot water to dissolve soluble residues and precipitate heavy metals |
-
1995
- 1995-12-27 JP JP7352103A patent/JPH09174019A/en not_active Withdrawn
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
BE1015866A3 (en) * | 2003-01-31 | 2005-10-04 | Group Portier Ind | Incinerator smoke solid residue treatment comprises washing with hot water to dissolve soluble residues and precipitate heavy metals |
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