JPH09249446A - Production of coal ash reclaimed material - Google Patents
Production of coal ash reclaimed materialInfo
- Publication number
- JPH09249446A JPH09249446A JP8055902A JP5590296A JPH09249446A JP H09249446 A JPH09249446 A JP H09249446A JP 8055902 A JP8055902 A JP 8055902A JP 5590296 A JP5590296 A JP 5590296A JP H09249446 A JPH09249446 A JP H09249446A
- Authority
- JP
- Japan
- Prior art keywords
- coal ash
- carbonization
- residue
- waste
- clay
- 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
- 239000010883 coal ash Substances 0.000 title claims abstract description 65
- 239000000463 material Substances 0.000 title claims description 40
- 238000004519 manufacturing process Methods 0.000 title claims description 11
- 238000003763 carbonization Methods 0.000 claims abstract description 52
- 239000010920 waste tyre Substances 0.000 claims abstract description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 23
- 239000004927 clay Substances 0.000 claims abstract description 21
- 239000010802 sludge Substances 0.000 claims abstract description 21
- 238000000465 moulding Methods 0.000 claims abstract description 7
- 238000004898 kneading Methods 0.000 claims abstract description 6
- 238000000197 pyrolysis Methods 0.000 claims description 21
- 239000010849 combustible waste Substances 0.000 claims description 20
- 239000011810 insulating material Substances 0.000 claims description 10
- 239000002689 soil Substances 0.000 claims description 9
- 238000009628 steelmaking Methods 0.000 claims description 6
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 5
- 239000003463 adsorbent Substances 0.000 claims description 5
- 229910052799 carbon Inorganic materials 0.000 claims description 3
- 238000010304 firing Methods 0.000 claims 1
- 239000000428 dust Substances 0.000 abstract description 10
- 238000001354 calcination Methods 0.000 abstract description 8
- 239000000203 mixture Substances 0.000 abstract description 6
- 238000002156 mixing Methods 0.000 abstract description 5
- 239000011369 resultant mixture Substances 0.000 abstract 1
- 238000000034 method Methods 0.000 description 25
- 238000009841 combustion method Methods 0.000 description 13
- 239000003245 coal Substances 0.000 description 11
- 229910000831 Steel Inorganic materials 0.000 description 10
- 239000010959 steel Substances 0.000 description 10
- 239000004568 cement Substances 0.000 description 9
- 239000002994 raw material Substances 0.000 description 8
- 239000007789 gas Substances 0.000 description 7
- 239000003921 oil Substances 0.000 description 6
- 230000005484 gravity Effects 0.000 description 5
- 239000000446 fuel Substances 0.000 description 4
- 239000002440 industrial waste Substances 0.000 description 4
- 239000000123 paper Substances 0.000 description 4
- 241000718541 Tetragastris balsamifera Species 0.000 description 3
- 229920003023 plastic Polymers 0.000 description 3
- 239000004033 plastic Substances 0.000 description 3
- 238000005406 washing Methods 0.000 description 3
- 239000002699 waste material Substances 0.000 description 3
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 2
- 239000002956 ash Substances 0.000 description 2
- 239000003638 chemical reducing agent Substances 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 239000010791 domestic waste Substances 0.000 description 2
- 238000001035 drying Methods 0.000 description 2
- 239000003337 fertilizer Substances 0.000 description 2
- 239000000835 fiber Substances 0.000 description 2
- 239000010881 fly ash Substances 0.000 description 2
- 239000010440 gypsum Substances 0.000 description 2
- 229910052602 gypsum Inorganic materials 0.000 description 2
- 238000010438 heat treatment Methods 0.000 description 2
- 239000010813 municipal solid waste Substances 0.000 description 2
- 239000008188 pellet Substances 0.000 description 2
- 239000010451 perlite Substances 0.000 description 2
- 235000019362 perlite Nutrition 0.000 description 2
- 239000000575 pesticide Substances 0.000 description 2
- 239000000843 powder Substances 0.000 description 2
- 239000004449 solid propellant Substances 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
- 235000019738 Limestone Nutrition 0.000 description 1
- 229910004298 SiO 2 Inorganic materials 0.000 description 1
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 230000000386 athletic effect Effects 0.000 description 1
- 239000000440 bentonite Substances 0.000 description 1
- 229910000278 bentonite Inorganic materials 0.000 description 1
- SVPXDRXYRYOSEX-UHFFFAOYSA-N bentoquatam Chemical compound O.O=[Si]=O.O=[Al]O[Al]=O SVPXDRXYRYOSEX-UHFFFAOYSA-N 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 230000033228 biological regulation Effects 0.000 description 1
- 239000003575 carbonaceous material Substances 0.000 description 1
- -1 chaff Inorganic materials 0.000 description 1
- 239000003610 charcoal Substances 0.000 description 1
- GUJOJGAPFQRJSV-UHFFFAOYSA-N dialuminum;dioxosilane;oxygen(2-);hydrate Chemical compound O.[O-2].[O-2].[O-2].[Al+3].[Al+3].O=[Si]=O.O=[Si]=O.O=[Si]=O.O=[Si]=O GUJOJGAPFQRJSV-UHFFFAOYSA-N 0.000 description 1
- 238000004821 distillation Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 229910001385 heavy metal 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
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 229910052500 inorganic mineral Inorganic materials 0.000 description 1
- 230000001788 irregular Effects 0.000 description 1
- 239000006028 limestone Substances 0.000 description 1
- 239000000155 melt Substances 0.000 description 1
- 150000001247 metal acetylides Chemical class 0.000 description 1
- 239000011707 mineral Substances 0.000 description 1
- 229910052901 montmorillonite Inorganic materials 0.000 description 1
- 230000003472 neutralizing effect Effects 0.000 description 1
- 239000010899 old newspaper Substances 0.000 description 1
- 229910001562 pearlite Inorganic materials 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
- 239000002002 slurry Substances 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
- 239000010455 vermiculite Substances 0.000 description 1
- 229910052902 vermiculite Inorganic materials 0.000 description 1
- 235000019354 vermiculite Nutrition 0.000 description 1
- 125000000391 vinyl group Chemical group [H]C([*])=C([H])[H] 0.000 description 1
- 229920002554 vinyl polymer Polymers 0.000 description 1
- 239000002023 wood Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02E—REDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
- Y02E50/00—Technologies for the production of fuel of non-fossil origin
- Y02E50/30—Fuel from waste, e.g. synthetic alcohol or diesel
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/60—Production of ceramic materials or ceramic elements, e.g. substitution of clay or shale by alternative raw materials, e.g. ashes
Landscapes
- Processing Of Solid Wastes (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、火力発電所から大
量に発生する石炭灰を原料として有用な再生材を製造す
る方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing a useful recycled material by using a large amount of coal ash generated from a thermal power plant as a raw material.
【0002】[0002]
【従来の技術】火力発電所では、石炭を燃焼させて電気
エネルギーを得ているが、石炭の燃焼法には石炭を微粉
砕して高温で燃焼させる微粉炭燃焼法と塊状もしくは粉
砕された石灰石と塊状の石炭を流動床で燃焼させる流動
床燃焼法がある。従来は、微粉炭燃焼法が主流であった
が、近年になり、NOxやSOxの規制が厳しくなって
きたため、NOxやSOxを低減することができかつ熱
効率が高い流動床燃焼法が着目されている。2. Description of the Related Art In a thermal power plant, coal is burned to obtain electric energy. The coal burning method is a pulverized coal burning method in which coal is pulverized and burned at a high temperature and lumpy or crushed limestone. There is a fluidized bed combustion method in which massive coal is burned in a fluidized bed. Conventionally, the pulverized coal combustion method has been the mainstream, but in recent years, regulations on NOx and SOx have become stricter. Therefore, attention has been paid to a fluidized bed combustion method which can reduce NOx and SOx and has high thermal efficiency. There is.
【0003】しかしながら、両燃焼法とも燃焼に伴い多
量の石炭灰が発生することが避けられない。However, both combustion methods inevitably generate a large amount of coal ash with combustion.
【0004】微粉炭燃焼法により発生する石炭灰は、未
燃焼炭素(以下、「未燃C」と略称する)やF・CaO
も少なく、比較的微細な球状物が多いため、JIS A
6201に適合するものはフライアッシュセメントの混
和材として利用され、粗粒部分はセメントの粘土原料と
して利用されている。また、ごく一部、粘土粉末や石炭
粉末を配合して造粒後焼成し、軽量骨材が製造されてい
るが、大部分は埋立処分されている。The coal ash produced by the pulverized coal combustion method is composed of unburned carbon (hereinafter abbreviated as "unburned C") and F.CaO.
JIS A
6201 is used as an admixture for fly ash cement, and the coarse-grained portion is used as a clay raw material for cement. In addition, a small part is mixed with clay powder or coal powder, granulated and fired to produce a lightweight aggregate, but most of it is landfilled.
【0005】一方、流動床燃焼法により発生する石炭灰
は、未燃Cが約10〜30wt%、F・CaOが約10
〜20wt%と多く、かつ、石膏を含有することもある
ので、セメントに配合すると、急速に硬化してしまい、
また混練時に減水剤を使用すると未燃Cに先に吸着され
てしまい、減水剤の使用量が増大してコスト高となる欠
点がある。しかも、石膏を含有する石炭灰をセメント原
料として使用すると、クリンカー鉱物の生成に悪影響を
及ぼす等の問題がある。従って、流動床燃焼法により発
生する石炭灰も、大部分は未利用のまま埋立処分されて
いる。しかし、最近では埋立処分地の確保が年々難しく
なっており、石炭灰の有効な処理が望まれている。On the other hand, the coal ash generated by the fluidized bed combustion method contains about 10 to 30 wt% of unburned C and about 10 of F · CaO.
Since it is as large as ~ 20 wt% and may contain gypsum, if it is mixed with cement, it will harden rapidly,
Further, when the water reducing agent is used during kneading, it is adsorbed to the unburned C first, which increases the amount of the water reducing agent used, resulting in a high cost. Moreover, when coal ash containing gypsum is used as a cement raw material, there is a problem that it adversely affects the production of clinker minerals. Therefore, most of the coal ash generated by the fluidized bed combustion method is also landfilled without being used. However, recently, it has become difficult to secure landfill sites year by year, and effective treatment of coal ash is desired.
【0006】近年では、廃タイヤの発生量も増大してお
り、その処理も問題となっている。廃タイヤの一部は、
切断したり、冷凍粉砕して再生タイヤやゴム製品の原料
へリサイクルされている。しかしながら、廃タイヤの大
部分は、セメント会社に処理費を支払って、セメントの
焼成用補助燃料として丸ごとあるいは切断処理して利用
したり、低温乾留炉でガスとオイルを回収して、セメン
ト焼成の補助燃料としたり、残渣の炭素主体物をセメン
ト原料に配合し、エネルギー源としたり、SiO2 、A
l2 O3 源として利用する方法もある。In recent years, the amount of waste tires generated has been increasing, and the disposal thereof has become a problem. Some of the scrap tires are
It is cut, frozen and crushed and recycled as raw material for recycled tires and rubber products. However, for the majority of waste tires, you must pay the processing cost to the cement company and use it as a supplementary fuel for burning cement, in whole or by cutting it, or collect gas and oil in a low-temperature carbonization furnace to burn cement. As an auxiliary fuel, or by blending the residual carbon-based material with the cement raw material to use as an energy source, SiO 2 , A
There is also a method of using it as a source of l 2 O 3 .
【0007】さらに、一般家庭から発生する可燃性ゴミ
の約75%は、焼却場で焼却処分され、その他はそのま
ま埋立処分されている。やはり、家庭から発生するゴミ
の埋立処分地の確保も年々難しくなっている。また、可
燃性の産業廃棄物を燃焼させた後に残る、燃焼残渣の量
もかなりの量となっている。これらの家庭からでるゴミ
や、産業廃棄物等の可燃性ゴミの中には、塩化ビニール
のゴミが含まれているため、これらの可燃性ゴミを燃焼
すると塩化水素ガスが発生し、焼却場の耐火物や熱交換
パイプを損傷するという問題点があり、さらにこれらの
ゴミの焼却灰や飛灰中には、重金属が含まれているた
め、無公害化するためには、溶融処理してガラス化する
方法や、不燃物と選別して固形燃料として、セメント焼
成の補助燃料や火力発電所の補助燃料とすることもけん
とうされているが、いずれの方法もコストが高くつき、
現実的な処理法法ではない。Furthermore, about 75% of the combustible waste generated from ordinary households is incinerated at the incinerator, and the rest is landfilled as it is. After all, it is becoming increasingly difficult to secure landfill sites for household garbage. Further, the amount of combustion residue left after burning combustible industrial waste is also considerable. Since vinyl chloride dust is included in combustible waste such as household waste and industrial waste, hydrogen chloride gas is generated when these combustible waste are burned, and it is generated in the incinerator. There is a problem of damage to refractories and heat exchange pipes, and in addition, since heavy metals are contained in the incineration ash and fly ash of these dusts, in order to make them pollution-free, they must be melted and processed into glass. It is also considered to be used as an auxiliary fuel for cement burning or an auxiliary fuel for a thermal power plant as a solid fuel by separating it from the non-combustible materials and the method of making it into a solid fuel, but both methods are costly,
It is not a realistic method.
【0008】[0008]
【発明が解決しようとする課題】石炭灰、廃タイヤおよ
び可燃ゴミは、年々増大する傾向にあり、従来の処理法
法では、今後対応することがますます困難になってく
る。特に、埋立処分地の確保は将来厳しいものがあり、
これらの処理方法の開発が早急に求められている。本発
明が解決しようとする課題は、石炭灰、廃タイヤおよび
可燃性ゴミを処理し、有用な石炭灰再生材を製造する方
法を提供することである。[Problems to be Solved by the Invention] Coal ash, waste tires, and combustible waste tend to increase year by year, and it will become more and more difficult for the conventional treatment methods to deal with them in the future. In particular, securing landfill sites may be difficult in the future,
There is an urgent need for development of these treatment methods. The problem to be solved by the present invention is to provide a method for treating coal ash, waste tires and combustible waste to produce a useful coal ash recycled material.
【0009】[0009]
【課題を解決するための手段】本発明者は、上記課題を
解決すべく鋭意研究を重ねた結果、石炭灰がポーラスな
性状を有していたり、未燃Cを含有することに着目し、
石炭灰に廃タイヤや可燃性ゴミの乾留残渣等の炭化物を
配合し成形することにより、製鋼用保温材や保水材とし
て有用な石炭灰再生材を製造しうることを見出し、本発
明を完成するに至った。As a result of intensive studies to solve the above problems, the present inventor has noticed that coal ash has a porous property or contains unburned C,
It was found that a coal ash recycled material useful as a heat retaining material for steelmaking and a water retaining material can be produced by blending coal ash with carbides such as waste tires and dry distillation residue of combustible waste, and completes the present invention. Came to.
【0010】すなわち、本発明は、 (1)石炭灰に、廃タイヤ乾留残渣炭化物、可燃性ゴミ
乾留残渣炭化物および製紙スラッジ乾留残渣炭化物から
選ばれる少なくとも1種と粘土を配合し、水を加えて混
練し成形した後、仮焼することを特徴とする石炭灰再生
材の製造方法 (2)石炭灰が10〜50wt%、製紙スラッジ乾留残
渣炭化物が5〜15wt%、廃タイヤおよび/または可
燃性ゴミ乾留残渣炭化物が10〜30wt%、および粘
土が15〜40wt%であることを特徴とする前記
(1)項記載の石炭灰再生材の製造方法 (3)石炭灰再生材が、製鋼用保温材、保水材、吸着材
または土壌改良材であることを特徴とする前記(1)項
または(2)項記載の石炭灰再生材の製造方法に関する
ものである。That is, (1) coal ash is mixed with at least one kind selected from waste tire carbonization residue carbonization, combustible waste carbonization residual carbonization and papermaking sludge carbonization residual carbonization and clay, and water is added. A method for producing a coal ash recycled material, which comprises kneading and molding, and then calcining (2) 10 to 50 wt% of coal ash, 5 to 15 wt% of carbonization residue of papermaking sludge carbonization residue, waste tire and / or flammability The method for producing a coal ash reclaimed material according to the above (1), wherein the carbonization residue of the waste carbonization residue is 10 to 30 wt% and the clay is 15 to 40 wt%. The present invention relates to a method for producing a coal ash reclaimed material according to item (1) or (2), which is a material, a water retention material, an adsorbent material, or a soil improvement material.
【0011】[0011]
【発明の実施の形態】本発明方法の原料となる石炭灰
は、火力発電所等から発生する石炭灰であれば、特に限
定されない。従って、微粉炭燃焼法により発生する石炭
灰でも、流動床燃焼法により発生する石炭灰のいずれで
も用いることができるが、流動床燃焼法により発生する
石炭灰の方が未燃Cの含有量が多く多孔性であるので、
微粉炭燃焼法により発生する石炭灰より好ましい。BEST MODE FOR CARRYING OUT THE INVENTION The coal ash as a raw material for the method of the present invention is not particularly limited as long as it is a coal ash generated from a thermal power plant or the like. Therefore, either coal ash generated by the pulverized coal combustion method or coal ash generated by the fluidized bed combustion method can be used, but the content of unburned C is higher in the coal ash generated by the fluidized bed combustion method. Because it is more porous,
Preference is given to coal ash generated by the pulverized coal combustion method.
【0012】本発明方法における、廃タイヤ乾留残渣炭
化物、可燃性ゴミ乾留残渣炭化物または製紙スラッジ乾
留残渣炭化物とは、廃タイヤ、可燃性ゴミまたは製紙ス
ラッジを乾留して得られる残渣の炭化物である。乾留方
法は特に限定されないが、例えば、廃タイヤ、可燃性ゴ
ミまたは製紙スラッジを乾留槽に入れ、約300〜35
0℃に加熱し、ガス、オイルを回収後、さらに580〜
600℃に昇温し、約30間保持すればよい。廃タイ
ヤ、可燃性ゴミまたは製紙スラッジを乾留するとガス分
とオイル分が留出し、乾留残渣としてポーラスな炭化物
が得られる。廃タイヤ、可燃性ゴミまたは製紙スラッジ
を乾留する場合は、乾留の効率を上げるために、廃タイ
ヤ、可燃性ゴミまたは製紙スラッジを約100℃前後で
乾燥することが好ましい。[0012] In the method of the present invention, carbonization residue of waste tire dry distillation, carbonization residue of combustible waste dust or carbonization residue of papermaking sludge is carbonization of residue obtained by carbonization of waste tire, combustible waste or papermaking sludge. The dry distillation method is not particularly limited, but, for example, waste tires, combustible dust or papermaking sludge may be put in a dry distillation tank to obtain about 300 to 35.
After heating to 0 ° C and collecting gas and oil,
The temperature may be raised to 600 ° C. and kept for about 30 minutes. Dry distillation of waste tires, combustible waste or papermaking sludge distills gas and oil, and porous charcoal is obtained as a dry distillation residue. When the waste tire, the combustible dust or the papermaking sludge is subjected to dry distillation, it is preferable to dry the waste tire, the combustible dust or the papermaking sludge at about 100 ° C. in order to improve the efficiency of the dry distillation.
【0013】これらの乾留残渣炭化物の原料となる、可
燃性ゴミとは、一般家庭ゴミ、産業廃棄物、都市ゴミ等
のゴミで可燃性のものであれば特に限定されず、塩化ビ
ニル等の合成樹脂製のゴミや紙や生ゴミ等を含むもので
あってもよい。The combustible waste material used as the raw material for the carbonization residue carbon residue is not particularly limited as long as it is combustible waste such as general household waste, industrial waste, and municipal waste. It may include resin-made dust, paper, garbage, and the like.
【0014】また、製紙スラッジとは、製紙工程で発生
する短繊維主体のスラッジ、および古新聞等を電気洗濯
機等を用いて水にスラリー化させ、脱水して得た短繊維
主体のパルプスラッジである。The papermaking sludge is a sludge mainly composed of short fibers generated in the papermaking process, and a pulp sludge mainly composed of short fibers obtained by slurrying old newspaper or the like into water using an electric washing machine and dehydrating it. Is.
【0015】本発明方法で用いられる粘土は、石炭灰と
乾留残渣炭化物とのバインダーの役割を果たすものであ
り、モンモリロナイト主体のベントナイト等の粘土を挙
げることができる。The clay used in the method of the present invention plays a role of a binder between coal ash and carbonization residue of carbonization residue, and examples thereof include clay such as bentonite mainly composed of montmorillonite.
【0016】本発明により、石炭灰再生材を製造するに
は、石炭灰に、廃タイヤ乾留残渣炭化物、可燃性ゴミ乾
留残渣炭化物および製紙スラッジ乾留残渣炭化物から選
ばれる少なくとも1種と粘土を配合し、水を加えて混練
し成形した後、仮焼ればよいが、石炭灰、乾留残渣炭化
物および粘土の配合割合は、石炭灰が10〜50wt
%、廃タイヤ乾留残渣炭化物、可燃性ゴミ乾留残渣炭化
物および製紙スラッジ乾留残渣炭化物から選ばれる少な
くとも1種が5〜30wt%、および粘土が15〜40
wt%であり、好ましくは、石炭灰が10〜50wt
%、製紙スラッジ乾留残渣炭化物が5〜15wt%、廃
タイヤおよび/または可燃性ゴミ乾留残渣炭化物が10
〜30wt%、および粘土が15〜40wt%である。To produce a coal ash reclaimed material according to the present invention, coal ash is blended with at least one selected from waste tire carbonization residue carbonization, combustible waste carbonization residue carbonization, and papermaking sludge carbonization residue carbonization. After adding water, kneading, shaping, and then calcining, coal ash, carbonization residue residue carbide and clay are mixed at a ratio of 10 to 50 wt.
%, At least one kind selected from carbonization residue of waste tire dry distillation residue, combustible waste carbonization residue carbonization and papermaking sludge carbonization residue carbonization, and clay 15-40%.
wt%, preferably 10 to 50 wt% coal ash
%, 5-15 wt% carbonization residue of papermaking sludge carbonization, 10 carbonization residue of waste tire and / or combustible waste carbonization residue
˜30 wt%, and clay is 15-40 wt%.
【0017】石炭灰、乾留残渣炭化物および粘土に水を
加えて成型する方法は、特に限定されないが、例えば、
石炭灰、乾留残渣炭化物および粘土の混合物に水を散水
して造粒する方法、または注水後混練して、押出成型に
よりペレット状に成形するかあるいはプレス成型する方
法等を挙げることができる。また、加える水の量は、成
形が可能であれば特に限定されないが、例えば、石炭
灰、乾留残渣炭化物および粘土の合計量に対して、25
〜35wt%程度加えればよい。The method of molding by adding water to coal ash, carbonization residue of carbonization and clay is not particularly limited.
Examples thereof include a method of sprinkling water on a mixture of coal ash, carbonization residue of dry distillation residue and clay, or a method of kneading after water injection and molding into pellets by extrusion molding or press molding. Further, the amount of water to be added is not particularly limited as long as it can be molded, but is, for example, 25 with respect to the total amount of coal ash, carbonization residue of carbonization and clay.
About 35 wt% may be added.
【0018】石炭灰、乾留残渣炭化物および粘土を成型
後、仮焼することにより、石炭灰再生材を製造すること
ができるが、仮焼温度は500〜700℃の範囲で適宜
行うことができる。仮焼方法は特に限定されないが、例
えば電気炉やロータリーキルンを用いることにより効率
的に仮焼を行うことができる。A coal ash reclaimed material can be manufactured by calcining coal ash, carbonized carbon residue and clay, and then calcining, and the calcining temperature can be appropriately set within the range of 500 to 700 ° C. The calcination method is not particularly limited, but the calcination can be efficiently performed by using, for example, an electric furnace or a rotary kiln.
【0019】本発明方法により製造した石炭灰再生材
は、ポーラスな性状を有しているので、例えば、製鋼用
保温材、保水材、吸着材または土壌改良材等として有効
に利用することができる。Since the recycled coal ash produced by the method of the present invention has a porous property, it can be effectively used as, for example, a heat insulating material for steelmaking, a water retaining material, an adsorbent or a soil improving material. .
【0020】本発明方法により製造した石炭灰再生材の
製鋼用保温材として用いるには、溶融スラグの上に投入
し溶鋼温度の低下を防止しうるものであり、パーライ
ト、モミガラ、バーミキュライト等の製鋼用保温材の代
替品として使用できるものである。When used as a heat insulating material for steelmaking of a coal ash recycled material produced by the method of the present invention, it can be put on molten slag to prevent a decrease in molten steel temperature, and steel such as pearlite, chaff, vermiculite, etc. It can be used as a substitute for heat insulating materials.
【0021】本発明方法により製造した石炭灰再生材を
保水材として、ゴルフ場の芝の下土に砂等と混合した
り、陸上競技場や野球場等の屋外競技場の表土やアンツ
ーカーの下に、マサ土等と混合したり、単味で5〜10
cm厚さに敷きつめたり、街路樹を植える場合に、マサ
土等と混合して用いることにより、夏場に木が枯れた
り、粉塵となり飛散する粘土分の防止やイレギラバウン
ドを防止することができる。The coal ash recycled material produced by the method of the present invention is used as a water retaining material to mix the soil under the turf of a golf course with sand or the like, or the topsoil of an outdoor stadium such as an athletic stadium or a baseball stadium or an antoker. Underneath, mix with masa earth, or just 5-10
When it is laid down to a thickness of cm or is planted on a roadside tree, it can be mixed with masa soil to prevent the tree from withering in the summer, to prevent the amount of clay that becomes dust and to scatter, and to prevent irregular bounce. .
【0022】本発明方法により製造した石炭灰再生材
は、例えば農薬や肥料を良好に吸着することができるの
で、農薬や肥料の吸着材として有効に利用することがで
きる。土壌改良材として用いるには、マサ土壌や火山灰
土壌地の保水力維持や酸性土壌の中和のために用いれば
よい。The recycled coal ash produced by the method of the present invention can adsorb pesticides and fertilizers well, and therefore can be effectively used as adsorbents for pesticides and fertilizers. When it is used as a soil improving material, it may be used for maintaining the water retaining capacity of Masa soil or volcanic ash soil and for neutralizing acidic soil.
【0023】[0023]
【実施例】以下に、本発明を実施例により詳細に説明す
るが、本発明はこれらの実施例に限定されることはな
い。EXAMPLES The present invention will be described below in detail with reference to examples, but the present invention is not limited to these examples.
【0024】実施例1 表1に示す性状の石炭灰、廃タイヤ乾留残渣炭化物、可
燃性ゴミ乾留残渣炭化物、製紙スラッジ乾留残渣炭化物
および粘土を用いて石炭灰再生材を製造した。表1中の
石炭灰は微粉炭燃焼法による発生物、石炭灰は流動
床燃焼法による発生物であり、廃タイヤ、製紙スラッジ
および可燃性ゴミの乾留残渣炭化物は以下のように調製
した。Example 1 A coal ash recycled material was produced by using coal ash having the properties shown in Table 1, carbonization residue of waste tire dry distillation residue, carbonization of combustible waste dry distillation residue, carbonization residue of papermaking sludge carbonization residue and clay. The coal ash in Table 1 is the product generated by the pulverized coal combustion method, and the coal ash is the product generated by the fluidized bed combustion method, and the carbonization residue of the dry distillation residue of waste tires, papermaking sludge and combustible waste was prepared as follows.
【0025】(廃タイヤ乾留残渣炭化物)自動車用スチ
ールラジアルタイヤを約1/4に切断し、約200Lの
乾留槽に入れ、300〜350℃に加熱し、ガスとオイ
ルを回収し、さらに580〜600℃に昇温後、約30
分保持し、その後室温まで冷却し、スチール分を磁選し
て除去し、炭化物を得た。(Carbide of waste tire dry distillation residue) A steel radial tire for automobiles is cut into about 1/4, put in a dry distillation tank of about 200 L, heated to 300 to 350 ° C., gas and oil are recovered, and further 580 to 580. After heating to 600 ° C, about 30
After that, the steel component was cooled to room temperature, and the steel component was magnetically removed to obtain a carbide.
【0026】(製紙スラッジ乾留炭化物)新聞紙を約1
/4に切断し、通常の洗濯の場合同様に水を入れた電気
洗濯機に投入し、約20分間回転させてスラリー状とし
た後、脱水し、ロータリーキルン(内径0.3m×長さ
2.9m,8rpm,傾斜5%)で乾燥し、約200L
の乾留槽に入れ、300〜350℃に加熱し、ガスとオ
イルを回収し、さらに580〜600℃に昇温後、約3
0分保持し、その後室温まで冷却し、炭化物を得た。(Carbon Distillation of Paper Sludge) About 1 newspaper
Cut into quarters, put into an electric washing machine containing water in the same manner as in normal washing, rotate for about 20 minutes to make a slurry, dehydrate, and then rotary kiln (inner diameter 0.3 m x length 2. 9m, 8rpm, 5% inclining), about 200L
In a dry distillation tank, heated to 300 to 350 ° C to collect gas and oil, further heated to 580 to 600 ° C, and then heated to about 3
Hold for 0 minutes and then cool to room temperature to obtain a carbide.
【0027】(可燃性ゴミ乾留残渣炭化物)都市ゴミ
(ビニール、紙、プラスチックトレー、野菜クズ等)を
カッターで約15〜20cmに切断し、約1/3の水
(約140〜150L)を入れたドラム缶状容器に投入
し、水に浮くものをすくい上げて除去した後、脱水し、
約105〜110℃に保持した乾燥機の中で約24時間
乾燥し、約200Lの乾留槽に入れ、300〜350℃
に加熱し、ガスとオイルを回収し、さらに580〜60
0℃に昇温後、約30分保持し、その後室温まで冷却
し、炭化物を得た。(Carbide of dry distillation residue of combustible waste) City waste (vinyl, paper, plastic tray, vegetable scraps, etc.) is cut into about 15 to 20 cm with a cutter, and about 1/3 of water (about 140 to 150 L) is put therein. Put it in a drum-shaped container, scoop up what is floating in water to remove it, and then dehydrate it.
Dry for about 24 hours in a dryer kept at about 105 to 110 ° C, put in a dry distillation tank of about 200 L, and 300 to 350 ° C.
Heat to 50% to recover gas and oil, then 580-60
After the temperature was raised to 0 ° C., the temperature was maintained for about 30 minutes and then cooled to room temperature to obtain a carbide.
【0028】(石炭灰再生材の製造)表2および表3に
示す配合割合で各原料を試験用パッグミルに入れて、水
を添加(25〜35wt%)して混合し、不足する水を
散水しながらパン型ペレタイザー(50cmφ×10c
m,18〜20rpm)で約5〜20mmφのペレット
状に成形した。次いで105〜110℃に保持した乾燥
機の中で24時間以上乾燥し、約600〜650℃に保
持したシリコニット電気炉の中で約20〜30分間焼成
し、炉外で冷却して石炭灰再生材を製造した。得られた
石炭灰再生材の溶融性、嵩比重、比熱および吸湿性を測
定した。その結果を、表2および表3に併せて示す。な
お、石炭灰再生材の製鋼用保温材としての効果を調べる
ために、表4に代表的な製鋼用保温材の溶融性、嵩比
重、比熱および吸湿性を調べて示した。(Production of Recycled Coal Ash Material) Each raw material was put in a test pug mill at a blending ratio shown in Tables 2 and 3, and water was added (25 to 35 wt%) to mix, and insufficient water was sprinkled. While pan-type pelletizer (50cmφ × 10c
m, 18 to 20 rpm) and formed into pellets of about 5 to 20 mmφ. Then, it is dried in a dryer kept at 105 to 110 ° C. for 24 hours or more, and fired in a silicon knit electric furnace kept at about 600 to 650 ° C. for about 20 to 30 minutes, and cooled outside the furnace to regenerate coal ash. The wood was manufactured. The meltability, bulk specific gravity, specific heat and hygroscopicity of the obtained coal ash recycled material were measured. The results are also shown in Tables 2 and 3. In order to investigate the effect of the recycled coal ash as a heat insulating material for steelmaking, Table 4 shows the meltability, bulk specific gravity, specific heat and hygroscopicity of typical heat insulating materials for steelmaking.
【0029】溶融性、嵩比重、比熱および吸湿性の測定
方法を以下に示す。The methods for measuring the meltability, bulk specific gravity, specific heat and hygroscopicity are shown below.
【0030】(溶融性)ハイアルミナルツボに各試料を
入れ、電気炉で約400〜500℃にで約10分間予熱
し、さらに電気炉で1250℃、1400℃、1550
℃の各温度で各々20分間保持し、溶融性の有無を調べ
た。(Fusability) Each sample was put in a high alumina crucible and preheated at about 400 to 500 ° C. for about 10 minutes in an electric furnace, and further at 1250 ° C., 1400 ° C., 1550 in an electric furnace.
Each temperature was kept at 20 ° C. for 20 minutes, and the presence or absence of meltability was examined.
【0031】(嵩比重)1000mlのメスシリンダー
で石炭灰再生材の体積を計り、石炭灰再生材の重量を計
り測定した。(Bulk Specific Gravity) The volume of the recycled coal ash material was measured by a graduated cylinder of 1000 ml, and the weight of the recycled coal ash material was measured.
【0032】(比熱)石炭灰再生材をハイアルミナルツ
ボに入れ、電気炉で500℃にて10分間保持した後、
水につけその時の水の吸熱量と石炭灰再生材の放熱量と
から求めた。 (吸湿性)乾燥機(105〜110℃で24時間以上)
で乾燥後、ビニール袋に入れて重量を測定し、ビニール
袋の上口を開いて7日間放置して重量を測定し、乾燥直
後の重量と7日間放置後の重量の差から吸湿量を求め
た。(Specific heat) A coal ash recycled material was placed in a high alumina crucible and held in an electric furnace at 500 ° C for 10 minutes,
It was calculated from the amount of heat absorbed by water and the amount of heat released from the recycled coal ash at that time. (Hygroscopic) dryer (at 105-110 ° C for 24 hours or more)
After drying, put it in a plastic bag and weigh it, open the upper opening of the plastic bag and leave it for 7 days to measure the weight. Calculate the moisture absorption from the difference between the weight immediately after drying and the weight after standing for 7 days. It was
【0033】[0033]
【表1】 [Table 1]
【0034】[0034]
【表2】 [Table 2]
【0035】[0035]
【表3】 [Table 3]
【0036】[0036]
【表4】 [Table 4]
【0037】表2および表3に示した結果から明らかな
ように、試料番号1〜23の本発明方法により製造した
石炭灰再生材は、1400℃では未溶融であり、155
0℃でも焼結か未溶融で溶鋼用保温材として優れている
ことが認められた(市販のモミ殻以外は1400℃では
溶融するし、モミ殻自体は減反のため入手が難しくなっ
ている)。試料番号24〜27の石炭灰単独もしくは石
炭灰と粘土のみからなる再生材は、嵩比重が大きすぎた
り、硬化しなかったりし、粉塵の発生も多く、作業環境
も悪化させ、C量が少なく、保温力も少ないので、溶鋼
用保温材として適していなかった。As is clear from the results shown in Tables 2 and 3, the recycled coal ash materials produced by the method of the present invention of Sample Nos. 1 to 23 are unmelted at 1400 ° C.
It was recognized that it is excellent as a heat insulating material for molten steel even at 0 ° C because it is sintered or unmelted (except for commercially available fir shells, it melts at 1400 ° C, and the fir shells themselves are difficult to obtain due to their reduced weight) . Recycled materials of sample number 24 to 27, which consist of coal ash alone or coal ash and clay only, have too large a bulk density or do not harden, generate a lot of dust, deteriorate the working environment, and have a small amount of C. Since it has a low heat retaining power, it was not suitable as a heat retaining material for molten steel.
【0038】本発明方法により製造した石炭灰再生材
は、従来のパーライトやモミガラ等の溶鋼用保温材と比
べると嵩比重がやや大きいが、パーライトやモミガラの
ように使用時に飛散することがないので、溶鋼用保温材
として好ましい。The recycled coal ash produced by the method of the present invention has a slightly higher bulk specific gravity than conventional heat insulating materials for molten steel such as perlite and chaff, but does not scatter during use as perlite and chaff. It is preferable as a heat insulating material for molten steel.
【0039】[0039]
【発明の効果】本発明方法により、産業廃棄物として大
量に発生し、埋め立て処分地の確保が問題となっている
石炭灰から溶鋼用保温材や吸着材等として有用な再生材
を製造することができ、さらに廃タイヤ、製紙スラッ
ジ、可燃性ゴミの処理も同時に行うことができる。Industrial Applicability According to the method of the present invention, it is possible to produce a recycled material useful as a heat insulating material for molten steel, an adsorbent, etc. from coal ash, which is a large amount of industrial waste and has a problem of securing landfill disposal sites. In addition, waste tires, paper sludge, and combustible dust can be treated at the same time.
Claims (3)
燃性ゴミ乾留残渣炭化物および製紙スラッジ乾留残渣炭
化物から選ばれる少なくとも1種と粘土を配合し、水を
加えて混練し成形した後、仮焼することを特徴とする石
炭灰再生材の製造方法。1. A coal ash is blended with at least one selected from carbonization residue of waste tire dry distillation residue, carbonization of combustible waste dry distillation residue and carbonization residue of papermaking sludge dry distillation residue, and clay, and after adding water, kneading and molding, A method for producing a coal ash recycled material, which comprises firing.
ジ乾留残渣炭化物が5〜15wt%、廃タイヤおよび/
または可燃性ゴミ乾留残渣炭化物が10〜30wt%、
および粘土が15〜40wt%であることを特徴とする
請求項1記載の石炭灰再生材の製造方法。2. Coal ash is 10 to 50 wt%, papermaking sludge carbonization residue carbon is 5 to 15 wt%, waste tire and / or
Or 10 to 30 wt% of carbonized residue of combustible waste carbonization residue,
And 15 to 40 wt% of clay, The method for producing a coal ash recycled material according to claim 1, wherein the clay is 15 to 40 wt%.
材、吸着材または土壌改良材であることを特徴とする請
求項1または2記載の石炭灰再生材の製造方法。3. The method for producing a coal ash recycled material according to claim 1, wherein the coal ash recycled material is a heat insulating material for steelmaking, a water retaining material, an adsorbent material or a soil improving material.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8055902A JPH09249446A (en) | 1996-03-13 | 1996-03-13 | Production of coal ash reclaimed material |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP8055902A JPH09249446A (en) | 1996-03-13 | 1996-03-13 | Production of coal ash reclaimed material |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH09249446A true JPH09249446A (en) | 1997-09-22 |
Family
ID=13012056
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP8055902A Pending JPH09249446A (en) | 1996-03-13 | 1996-03-13 | Production of coal ash reclaimed material |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH09249446A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20030070204A (en) * | 2002-02-21 | 2003-08-29 | 경기대학교 | Composition for light weight artificial aggregate made from waste material and method for manufacturing the same |
JP2006241803A (en) * | 2005-03-02 | 2006-09-14 | Ehime Prefecture | Water-absorbing pavement, and aggregate for use therein |
KR20220023631A (en) * | 2020-08-21 | 2022-03-02 | (주)동부그린 | apparatus for treating wastewater produced from manufacture process of oxydianiline and treating mothed using the same |
-
1996
- 1996-03-13 JP JP8055902A patent/JPH09249446A/en active Pending
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR20030070204A (en) * | 2002-02-21 | 2003-08-29 | 경기대학교 | Composition for light weight artificial aggregate made from waste material and method for manufacturing the same |
JP2006241803A (en) * | 2005-03-02 | 2006-09-14 | Ehime Prefecture | Water-absorbing pavement, and aggregate for use therein |
KR20220023631A (en) * | 2020-08-21 | 2022-03-02 | (주)동부그린 | apparatus for treating wastewater produced from manufacture process of oxydianiline and treating mothed using the same |
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