JPH1160327A - Production of inorganic granular molded body - Google Patents

Production of inorganic granular molded body

Info

Publication number
JPH1160327A
JPH1160327A JP21624397A JP21624397A JPH1160327A JP H1160327 A JPH1160327 A JP H1160327A JP 21624397 A JP21624397 A JP 21624397A JP 21624397 A JP21624397 A JP 21624397A JP H1160327 A JPH1160327 A JP H1160327A
Authority
JP
Japan
Prior art keywords
inorganic
molded product
weight
water
parts
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
Application number
JP21624397A
Other languages
Japanese (ja)
Inventor
Yuzo Aido
勇三 相戸
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Teijin Ltd
Original Assignee
Teijin Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Teijin Ltd filed Critical Teijin Ltd
Priority to JP21624397A priority Critical patent/JPH1160327A/en
Publication of JPH1160327A publication Critical patent/JPH1160327A/en
Pending legal-status Critical Current

Links

Classifications

    • CCHEMISTRY; METALLURGY
    • C04CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
    • C04BLIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
    • C04B18/00Use of agglomerated or waste materials or refuse as fillers for mortars, concrete or artificial stone; Treatment of agglomerated or waste materials or refuse, specially adapted to enhance their filling properties in mortars, concrete or artificial stone
    • C04B18/02Agglomerated materials, e.g. artificial aggregates
    • C04B18/021Agglomerated materials, e.g. artificial aggregates agglomerated by a mineral binder, e.g. cement
    • YGENERAL 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
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/91Use of waste materials as fillers for mortars or concrete

Abstract

PROBLEM TO BE SOLVED: To produce a lightweight tough granular molded body excellent in heat resistance by mixing coal ash with an alkali metallic silicate, a hardening regulator and a specified amt. of water, molding the resultant inorg. starting material compsn. in a granule shape and firing it. SOLUTION: An inorg. starting material compsn. is prepd. by mixing 100 pts.wt. coal has having <=15 wt.% carbon content with a 20-100 pts.wt. alkali metallic silicate, a 5-30 pts.wt. hardening regulator and water corresponding to 10-30 wt.% of the compsn. The alkali metallic silicate is, e.g. sodium silicate and is used as powder not substantially contg. free water. Oxides or hydroxides of one or more metals selected from among Al, Mg, Zn, B and Ca are used as the hardening regulator. The compsn. is molded in a granule shape by an extruder system or a rotating disk system. The resultant molded body is fired at 300-600 deg.C in an oxygen-contg. atmosphere or an inert gaseous atmosphere after heating at 50-100 deg.C/hr heating rate and then it is cooled at 50-100 deg.C/hr cooling rate.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、石炭灰を主たる原
料とする無機質粒状成形物の製造方法に関するものであ
り、さらに詳細には、産業廃棄物として大量に排出され
る石炭灰を有効活用出来、かつ耐熱性、機械的性質等に
おいて優れた無機質粒状成形物を低コストで製造する方
法に関するものである。本発明方法で得られる無機質粒
状成形物は、高強度かつ軽量であり、例えば骨材として
利用することが出来る等、土木・建築材料分野において
有用な材料を提供する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing an inorganic granular molded product using coal ash as a main raw material, and more particularly, to a method for effectively utilizing coal ash discharged in large quantities as industrial waste. The present invention relates to a method for producing an inorganic granular molded product excellent in heat resistance, mechanical properties and the like at low cost. The inorganic granular molded product obtained by the method of the present invention provides a material useful in the field of civil engineering and building materials, for example, having high strength and light weight and being usable as an aggregate, for example.

【0002】[0002]

【従来の技術】火力発電用エネルギー源として、石炭が
大量に使用されており、その焼成材である石炭灰も大量
に排出されている。
2. Description of the Related Art A large amount of coal is used as an energy source for thermal power generation, and a large amount of coal ash as a fired material is also discharged.

【0003】石炭灰の中で、特に微細なフライアッシュ
がある。フライアッシュは火力発電所等で微粉炭を焼成
させた際に生じた石炭灰が溶融しそれが高温燃焼ガスと
共に煙道へ運ばれる途中で急激に冷却され、表面張力に
よってガラス質の球状の微細粒子となったものである。
これが、自己水和作用を有することから、一部のフライ
アッシュはフライアッシュセメントとして利用されてい
る。
[0003] Among the coal ash, there is particularly fine fly ash. Fly ash melts coal ash generated when pulverized coal is burned at a thermal power plant, and is rapidly cooled while being transported to the flue with high-temperature combustion gas. It has become particles.
Since this has a self-hydrating action, some fly ash is used as fly ash cement.

【0004】フライアッシュセメントは、ポルトランド
セメントと同じように、水和反応によって凝結する性質
がある。しかしながら、500℃以上に加熱すると、セ
メント凝結物中の結晶水が離脱することから、機械的強
度は著しく低下してしまう。
[0004] Like flyland cement, fly ash cement has the property of setting by hydration. However, when heated to 500 ° C. or higher, water of crystallization in the cement condensate is released, and the mechanical strength is significantly reduced.

【0005】[0005]

【発明が解決しようとする課題】一方、石炭灰をポルト
ランドセメントや水ガラス等の無機バインダーやポリビ
ニルアルコール(PVA)やカルボキシメチルセルロー
ス(CMC)等のような有機バインダーと混合した後、
高温で処理してセラミックス状の成形物を得ることも知
られているが、これらの方法では多量の水を添加する必
要があり、また非常に高い焼成温度を必要とするため、
エネルギーコスト面での不利は免れない。
On the other hand, coal ash is mixed with an inorganic binder such as Portland cement or water glass or an organic binder such as polyvinyl alcohol (PVA) or carboxymethyl cellulose (CMC).
It is also known to obtain a ceramic-like molded product by treating at a high temperature, but these methods require a large amount of water to be added, and require a very high firing temperature.
There are inevitable disadvantages in terms of energy costs.

【0006】[0006]

【課題を解決するための手段】本発明者は、上述の課題
を解決すべく鋭意研究の結果、フライアッシュ等の石炭
灰に、水ガラスから水分を除いた粉末状の珪酸ナトリウ
ムを無機バインダーとして配合し、これに所定量の水を
添加、混合して得られる実質的に粉体状の無機質原料組
成物を用いて、所定の形状に成形し、比較的低温で焼成
することによって、添加すべき水分の使用量を抑え、簡
便かつ安価に、機械的特性の優れた無機質成形物を得る
ことを見出し、先に提案した。
Means for Solving the Problems As a result of intensive studies to solve the above-mentioned problems, the present inventor has found that powdered sodium silicate obtained by removing water from water glass is used as an inorganic binder in coal ash such as fly ash. A predetermined amount of water is added to the mixture, and a predetermined amount of water is added to the mixture. The mixture is formed into a predetermined shape using a substantially powdery inorganic raw material composition obtained by baking at a relatively low temperature. The present inventors have found that an inorganic molded product having excellent mechanical properties can be obtained simply and inexpensively by suppressing the amount of water to be used, and proposed above.

【0007】さらに、上記無機質原料組成物を用いて、
粒状に成形し、焼成することによって、上記と同様に機
械特性の優れた無機質粒状成形物を得ることを見出し、
本発明に到達した。
Further, using the above-mentioned inorganic raw material composition,
By forming into granules and firing, it was found that an inorganic granular molded product having excellent mechanical properties as described above was obtained,
The present invention has been reached.

【0008】すなわち、本発明は、石炭灰とアルカリ金
属珪酸塩、あるいは石炭灰、アルカリ金属珪酸塩と硬化
調節剤とからなる無機質原料組成物に、組成物中10〜
30重量%に相当する水分を添加、混合して得られる実
質的に粉体状の組成物を、粒状に成形した後、300〜
600℃という低い温度で焼成することを特徴とする無
機質粒状成形物の製造方法に関するものである。
That is, the present invention relates to an inorganic raw material composition comprising coal ash and an alkali metal silicate, or coal ash, an alkali metal silicate and a hardening modifier, wherein
A substantially powdery composition obtained by adding and mixing water equivalent to 30% by weight is formed into a granular form, and then the composition is subjected to 300 to
The present invention relates to a method for producing an inorganic granular molded product, which is fired at a temperature as low as 600 ° C.

【0009】[0009]

【発明の実施の形態】本発明方法において使用する石炭
灰は、火力発電所その他の工場から排出される石炭灰が
使用される。これら石炭灰の中でも「フライアッシュ」
と呼ばれる均一で微細な石炭灰が好適に使用される。こ
のフライアッシュは火力発電所等で微粉炭を焼成した際
に生じた石炭灰が溶融し、それが高温焼成ガスと共に煙
道へ運ばれる途中で急激に冷却され、表面張力によって
ガラス質の球状の軽量、微細粒子となったものである。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS As coal ash used in the method of the present invention, coal ash discharged from a thermal power plant or other factories is used. Among these coal ash, "fly ash"
A uniform and fine coal ash referred to as ash is suitably used. This fly ash melts coal ash generated when pulverized coal is fired at a thermal power plant, etc., and is rapidly cooled while being transported to the flue together with the high-temperature firing gas. Light and fine particles.

【0010】この石炭灰は高温焼成による完全焼成灰で
も良く、また比較的低い温度での焼成で成形するフリー
の炭素成分を含むものでも良く、例えば、炭素含有率が
15重量%以下のフライアッシュが好適に使用される。
The coal ash may be completely baked ash obtained by firing at a high temperature, or may contain a free carbon component formed by firing at a relatively low temperature, for example, fly ash having a carbon content of 15% by weight or less. Is preferably used.

【0011】本発明方法では、この石炭灰に、無機バイ
ンダー、更に必要に応じて硬化調節剤を加え、無機質原
料組成物を調製する。
In the method of the present invention, an inorganic binder and, if necessary, a curing regulator are added to the coal ash to prepare an inorganic raw material composition.

【0012】本発明において無機バインダーとして使用
するアルカリ金属珪酸塩は、一般式として M2 O・nSiO2 ・nH2 O …(1) (式中、M:Na、K等のアルカリ金属、n、m:アル
カリ金属酸化物に対するモル比)で表され、上記式
(1)中のn(アルカリ金属酸化物に対する二酸化珪素
のモル比)が1.5〜3.5(好ましくは2.0〜3.
0)の範囲にあることが好ましい。
The alkali metal silicate used as the inorganic binder in the present invention is represented by the following general formula: M 2 O.nSiO 2 .nH 2 O (1) (wherein, M: an alkali metal such as Na or K; m: molar ratio to alkali metal oxide), and n (molar ratio of silicon dioxide to alkali metal oxide) in the above formula (1) is 1.5 to 3.5 (preferably 2.0 to 3). .
It is preferably in the range of 0).

【0013】上記アルカリ金属珪酸塩の具体的な例とし
ては、二珪酸ナトリウムや三珪酸ナトリウムとよばれる
珪酸ナトリウムや、JIS―号粉末、JIS―2号粉末
として規格化されている珪酸ソーダ(粉末)等をあげら
れる。
Specific examples of the alkali metal silicate include sodium silicates called sodium disilicate and sodium trisilicate, and sodium silicate (powder) standardized as JIS-No. Powder and JIS-2 No. powder. ).

【0014】上記アルカリ金属珪酸塩の使用量は、石炭
灰100重量部に対して20〜100重量部が好まし
く、さらに好ましい範囲は、30〜60重量部である。
上記使用量が20重量部に満たない場合は、混合、成形
後の焼成によって得られる成形物の固化が不完全で、脆
くなる傾向が出てくるので好ましくない。また、100
重量部を越えて使用する場合は、石炭灰との相互反応を
していない過剰のアルカリ金属珪酸塩が混在することと
なり、焼成にも拘らず温水浸漬に弱い等の欠点を持つ可
能性があり、好ましくない。
The amount of the alkali metal silicate used is preferably 20 to 100 parts by weight, more preferably 30 to 60 parts by weight, based on 100 parts by weight of coal ash.
If the amount used is less than 20 parts by weight, the molded product obtained by mixing and firing after molding is incompletely solidified and tends to become brittle, which is not preferable. Also, 100
If used in excess of parts by weight, excess alkali metal silicate that does not interact with coal ash will be mixed in, and may have drawbacks such as being weak to hot water immersion despite firing. Is not preferred.

【0015】上記アルカリ金属珪酸塩の一般式中、mは
結晶水として含有する水分の相対量を表しており、例え
ば試薬級として入手可能な2珪酸ナトリウム粉末(キシ
ダ化学製品)のような通常の粉末状のものでも、m=
2.5〜3(該珪酸塩の約20重量%の水分率に相当)
の水分を含有しているが、本発明の構成としては粉体状
無機バインダーである。すなわち、組成物作成の段階で
も粉体状の無機バインダーを使用し、下に述べる制御さ
れた量の水分の添加にも拘らず、原料組成物自身は実質
的に粉体状物として取り扱うことが可能であって、操作
上、装置上の簡便さが実現出来る。
In the general formula of the above alkali metal silicate, m represents the relative amount of water contained as water of crystallization, and is, for example, an ordinary amount such as sodium disilicate powder (Kishida Chemical Products) available as a reagent grade. Even in the form of a powder, m =
2.5-3 (corresponding to a water content of about 20% by weight of the silicate)
However, the composition of the present invention is a powdery inorganic binder. That is, the powdery inorganic binder is used even at the stage of preparing the composition, and the raw material composition itself can be substantially handled as a powdery substance, despite the addition of a controlled amount of water described below. It is possible, and simplicity in operation and apparatus can be realized.

【0016】本発明において良好な無機質粒状成形物を
得るための最も重要な要因の一つは、無機質原料組成物
中の水分添加量(水分率)の調整である。すなわち、石
炭灰とアルカリ金属珪酸塩、あるいは石炭灰、アルカリ
金属珪酸塩及び硬化調節剤からなる組成物に、水分率1
0〜30重量%に相当する量の水分を添加、混合するこ
とが、本発明において極めて重要である。水分率が5重
量%未満の場合は原料組成物を押出し方式あるいは回転
デュスク方式により粒状に成形しても、形状保持性が不
足し、引き続いて行なう焼成に際しても強固な固化を起
こすことが出来ない。一方、水分率として30重量%を
越えた多量の水分を添加、混合すると、粒状への成形に
際して過剰の水分に起因する表面への水分の滲出があ
り、粒状物相互の粘着等のため、所定の形状への成形が
困難になる上に、焼成に先立っての予備乾燥に極めて長
時間を要する等の問題を生じ、好ましくない。上記水分
率は、目的とする粒状成形物の粒径にもよるが、上記無
機質原料組成物中、15〜25重量%の範囲にすること
が好ましい。
In the present invention, one of the most important factors for obtaining a favorable inorganic granular molded product is the adjustment of the amount of water added (moisture percentage) in the inorganic raw material composition. That is, a composition comprising coal ash and an alkali metal silicate, or coal ash, an alkali metal silicate and a hardening agent, has a moisture content of 1%.
It is extremely important in the present invention to add and mix an amount of water corresponding to 0 to 30% by weight. When the water content is less than 5% by weight, even if the raw material composition is formed into granules by an extrusion method or a rotating dusk method, shape retention is insufficient, and strong solidification cannot be caused even in subsequent firing. . On the other hand, when a large amount of water exceeding 30% by weight as a water content is added and mixed, there is oozing of water on the surface due to excessive water in forming into granules, and due to adhesion between the granules, etc. In addition to this, it is difficult to form into the shape described above, and it takes a very long time to perform preliminary drying before firing, which is not preferable. The water content depends on the particle size of the target granular molded product, but is preferably in the range of 15 to 25% by weight in the inorganic raw material composition.

【0017】本発明方法では、硬化調節剤を添加するこ
とも出来る。この硬化調節剤は、石炭灰と無機バインダ
ー及び所定量の水分を混合した原料組成物から無機質粒
状成形物を得るに際し、石炭灰と無機バインダーとの硬
化反応を促進する作用を持つものであり、アルミニウ
ム、マグネシウム、亜鉛、ホウ素及びカルシウムから選
ばれた少なくとも1種の金属の酸化物または水酸化物が
好ましく使用される。特に好ましくは硬化調節剤の例と
しては、アルミナ、水酸化アルミニウム、酸化亜鉛等を
あげることが出来る。
In the method of the present invention, a curing regulator can be added. This curing regulator has an effect of accelerating the curing reaction between coal ash and the inorganic binder when obtaining an inorganic granular molded product from a raw material composition obtained by mixing coal ash with an inorganic binder and a predetermined amount of moisture, An oxide or hydroxide of at least one metal selected from aluminum, magnesium, zinc, boron and calcium is preferably used. Particularly preferably, examples of the curing regulator include alumina, aluminum hydroxide, zinc oxide and the like.

【0018】上記硬化調節剤の使用量は、石炭灰100
重量部に対して1〜30重量部(特に5〜20重量部)
が好ましい。硬化調節剤の量が過大になると成形物の生
産コストが上昇するので好ましくない。
The amount of the curing regulator used is 100 ash
1 to 30 parts by weight based on parts by weight (particularly 5 to 20 parts by weight)
Is preferred. If the amount of the curing regulator is excessive, the production cost of the molded product increases, which is not preferable.

【0019】上述のように、本発明方法で用いる無機質
原料組成物は、石炭灰、無機バインダーを主要成分と
し、これに必要に応じて硬化調節剤を含むが、さらに必
要に応じて、軽量化のための微細な無機中空粒子、補強
用の短繊維やウイスカー等を混合することも出来る。
As described above, the inorganic raw material composition used in the method of the present invention contains coal ash and an inorganic binder as main components and, if necessary, a curing control agent. Fine inorganic hollow particles, short fibers for reinforcement, whiskers and the like can be mixed.

【0020】上記の無機中空粒子は、平均粒径0.01
〜2mm(特に好ましくは0.1〜0.5mm)、見掛
け比重0.05〜0.8(特に好ましくは0.1〜0.
7)の中空粒子、具体例としては、ガラスバルーン、シ
ラスバルーン、シリカバルーン等と称されている微細な
無機中空粒子をあげることが出来る。ガラスバルーンの
具体例としては、住友スリーエム社製のグラスバブル
ス:K−1(見掛け比重0.125;50%粒径68μ
m)、K−37(見掛け比重0.37;50%粒径50
μm)、旭硝子社製のセルスターZ28(見掛け比重
0.28;平均粒径55μm)、巴工業社製のガラスバ
ルーンHGS−16(見掛け比重0.17〜0.18;
平均粒径110μm)等があげられる。また、シラスバ
ルーンの具体例としては、旭硝子社製Qセル300(見
掛け比重0.21;平均粒径65μm)や三機工業社製
サンキライトY02(見掛け比重0.23〜0.26;
粒径44〜75μm)等があげられる。更に、シリカバ
ルーンの具体例としては、日本フィライト社製フィライ
ト52/7FG(比重0.7;粒径30〜100μm)
等があげられる。
The above-mentioned inorganic hollow particles have an average particle size of 0.01.
To 2 mm (particularly preferably 0.1 to 0.5 mm), apparent specific gravity 0.05 to 0.8 (particularly preferably 0.1 to 0.5 mm).
The hollow particles of 7), specific examples thereof include fine inorganic hollow particles called glass balloons, shirasu balloons, silica balloons and the like. As a specific example of the glass balloon, a glass bubble made by Sumitomo 3M: K-1 (apparent specific gravity 0.125; 50% particle size 68 μm)
m), K-37 (apparent specific gravity 0.37; 50% particle size 50)
μm), Cellstar Z28 manufactured by Asahi Glass Co., Ltd. (apparent specific gravity 0.28; average particle size 55 μm), glass balloon HGS-16 manufactured by Tomoe Kogyo Co., Ltd. (apparent specific gravity 0.17 to 0.18;
Average particle size of 110 μm). Specific examples of the shirasu balloon include Q cell 300 (apparent specific gravity 0.21; average particle diameter 65 μm) manufactured by Asahi Glass Co., Ltd. and Sankilite Y02 manufactured by Sanki Kogyo (apparent specific gravity 0.23 to 0.26;
(Particle size: 44 to 75 μm). Further, as a specific example of the silica balloon, Nippon Philite Co., Ltd.'s Philite 52 / 7FG (specific gravity 0.7; particle size 30 to 100 µm)
And the like.

【0021】補強用としての繊維としては、ガラス繊
維、炭素繊維、炭化珪素繊維等が使用され、ミルドファ
イバーのような繊維長/繊維径皮の極めて小さい短繊維
が特に好ましい。
As fibers for reinforcement, glass fibers, carbon fibers, silicon carbide fibers and the like are used, and short fibers having a very small fiber length / fiber diameter such as milled fibers are particularly preferable.

【0022】本発明方法における石炭灰、無機バインダ
ー、硬化調節剤、所定量の水分及び各種添加剤等の原料
組成物の混合は、実質的に粉体混合の状態であり、単純
な機械混合で十分であるが、一般にニーダーあるいはブ
レンダーと称されている混合装置を使用するのが好まし
い。
The mixing of the raw material composition such as coal ash, an inorganic binder, a curing regulator, a predetermined amount of water and various additives in the method of the present invention is substantially a powder mixing state, and can be performed by simple mechanical mixing. Although sufficient, it is preferred to use a mixing device commonly referred to as a kneader or blender.

【0023】上記混合操作によって得られる原料組成物
を、粒状に成形する手段としては、例えば上記原料組成
物を回転ディスク方式の造粒装置に入れてディスクを回
転させながら望みの粒径まで成長させる方法、あるいは
望みの粒サイズに対応する小孔を有するダイスを通して
押出して得られる棒状物をカットして粒状にする方法等
をあげることが出来る。
As a means for shaping the raw material composition obtained by the mixing operation into granules, for example, the raw material composition is put into a rotating disk type granulator and the disk is grown to a desired particle size while rotating the disk. And a method in which a rod-like material obtained by extruding through a die having small holes corresponding to a desired grain size is cut into granules.

【0024】本発明方法における焼成は、空気等の酸素
含有雰囲気下あるいは酸素ガス等の不活性ガス雰囲気し
たさらには燃焼ガス等の雰囲気下で、通常300℃ない
し600℃に昇温・加熱することによって実施される。
300℃未満の温度での焼成では、固化ないし硬化はす
るが、使用する無機バインダーの一部が十分に反応に関
与し得ず、十分な強度を有する無機質成形物が得られ難
く、好ましくない。また、600℃を越えた高温、例え
ば通常のセラミックスの焼成の際に採用されている10
00〜1300℃のような高温雰囲気での焼成では、同
様な強度特性の成形物が得られるものの、高温を得るた
めのエネルギー費用が高価につくため、製造コスト的に
好ましいとは言い難い。
The calcination in the method of the present invention is usually carried out by raising the temperature to 300 ° C. to 600 ° C. in an atmosphere containing oxygen such as air, or in an atmosphere of an inert gas such as oxygen gas, or further in an atmosphere of combustion gas or the like. Will be implemented.
Firing at a temperature lower than 300 ° C. solidifies or cures, but a part of the inorganic binder used cannot sufficiently participate in the reaction, and it is difficult to obtain an inorganic molded product having sufficient strength, which is not preferable. In addition, a high temperature exceeding 600 ° C., for example, 10
Firing in a high temperature atmosphere such as 00 to 1300 [deg.] C. can provide a molded product having similar strength characteristics, but it is difficult to say that it is preferable in terms of manufacturing cost because energy cost for obtaining a high temperature is high.

【0025】焼成に際しての昇温及び降温は、急激な温
度変化を避けることが好ましく、例えば50〜100℃
/1時間のようなゆっくりとした昇温、降温が特に好ま
しい。
The temperature rise and fall during firing is preferably to avoid a rapid temperature change, for example, 50 to 100 ° C.
It is particularly preferable to slowly raise and lower the temperature such as / 1 hour.

【0026】また、上記焼成に先立って、各種の成形法
法によって得られた粒状固化物を予備乾燥することが望
ましい。本発明方法において使用する水分の量は、上述
のように、比較的少ない量であるが、それでも焼成前の
段階では、水分の添加量や成形方法にもよるが、例えば
10〜20重量%に相当するフリーの水分を含んでい
る。
Prior to the above-mentioned firing, it is desirable to pre-dry the granular solid obtained by various molding methods. The amount of water used in the method of the present invention is a relatively small amount as described above. However, in the stage before firing, it depends on the amount of water added and the molding method. Contains equivalent free water.

【0027】したがって、そのまま急激な加熱処理を行
なうと粒状成形物の膨れや亀裂を発生することがあるの
で、焼成に先立って予備乾燥を行なうことが望ましいわ
けである。予備乾燥の温度としては、水の常圧での沸点
である100℃前後で実施するのが好ましい。
Therefore, if the rapid heat treatment is performed as it is, swelling or cracking of the granular molded product may occur, so that it is desirable to carry out preliminary drying before firing. The pre-drying temperature is preferably about 100 ° C., which is the boiling point of water at normal pressure.

【0028】かくして、本発明の方法により、石炭灰、
無機バインダーとしてのアルカリ金属珪酸塩、硬化調節
剤及び水分で構成される原料組成物から、強度等機械的
特性の良好な無機質粒状成形物を得ることが出来る。こ
うして得られた粒状成形物は、基本的に不燃性であり、
高強度かつ低比重の無機質粒状材料となり、例えば軽量
骨材として、土木・建材用途分野で有用な材料を提供す
ることが出来る。
Thus, according to the method of the present invention, coal ash,
From a raw material composition comprising an alkali metal silicate as an inorganic binder, a curing regulator and moisture, an inorganic granular molded product having good mechanical properties such as strength can be obtained. The granular molded product thus obtained is basically nonflammable,
It becomes a high-strength, low-specific-gravity inorganic granular material, and can provide a material useful as a lightweight aggregate in the field of civil engineering and construction materials.

【0029】[0029]

【実施例】次に、本発明方法の詳細を、実施例及び比較
例により説明するが、これらは本発明の理解をたすける
ためのものであって、これら実施例によって本発明の範
囲が限定されるものではない。なお、実施例及び比較例
中に「部」は特に断らない限り、重量部を意味する。
Next, the method of the present invention will be described in detail with reference to Examples and Comparative Examples, which are for the purpose of understanding the present invention, and the scope of the present invention is limited by these Examples. Not something. In the examples and comparative examples, “parts” means “parts by weight” unless otherwise specified.

【0030】[実施例1]火力発電所の石炭灰として得
られるフライアッシュ100部(炭素含有量10重量
%)に、無機バインダーとして珪酸ナトリウム(キシダ
化学製試薬「二珪酸ナトリウム粉末」;二酸化珪素/酸
化ナトリウムのモル比=2.0)50部及び硬化調節剤
としてのアルミナ粉末10部からなる粉体組成物を、ニ
ーダー中で混合し、さらに44部の水(全組成物中に占
める水分率21.6重量%に相当する)を少しづつ添加
しながら混合を続けて、実質的に粉体状の原料組成物を
得た。
Example 1 100 parts of fly ash (carbon content: 10% by weight) obtained as coal ash from a thermal power plant were mixed with sodium silicate (reagent "Sodium disilicate powder" manufactured by Kishida Chemical; silicon dioxide) as an inorganic binder. / Molar ratio of sodium oxide = 2.0) A powder composition consisting of 50 parts of alumina powder as a curing regulator and 10 parts of alumina was mixed in a kneader, and further mixed with 44 parts of water (water content in the total composition). (Corresponding to 21.6% by weight) was added little by little, and the mixing was continued to obtain a substantially powdery raw material composition.

【0031】上記原料組成物を、傾斜角度45°に設定
した回転ディスクシキ造粒装置に入れ、60rpmで回
転させながら造粒した。得られた粒径約5mmの粒状体
を約100℃に設定した乾燥機中に移して予備乾燥を行
なった。ついで、この乾燥した粒状体を、焼成炉にセッ
トし、常温から300℃まで3時間かけて昇温し、さら
に300℃に2時間維持した後、焼成炉の中で自然冷却
を行なった。得られた粒状成形物の見掛け比重は1.3
0であり、圧壊強力は20〜30Kgfと、良好な機械
特性を有することが確認された。
The above raw material composition was placed in a rotating disk shear granulator set at an inclination angle of 45 °, and granulated while rotating at 60 rpm. The obtained granular material having a particle size of about 5 mm was transferred into a dryer set at about 100 ° C. and preliminarily dried. Then, the dried granules were set in a firing furnace, heated from room temperature to 300 ° C. over 3 hours, and maintained at 300 ° C. for 2 hours, and then naturally cooled in the firing furnace. The apparent specific gravity of the obtained granular molded product is 1.3.
It was 0 and the crushing strength was 20 to 30 kgf, confirming that it had good mechanical properties.

【0032】上記粒状成形物の60部を骨材として、ポ
ルトランドセメント40部及び水20部と混合し、4c
m×4cm×16cmの棒状金型に流し込み、常温で2
日間自然養生して骨材強化のブロックを調製した。得ら
れたブロックの見掛け比重は1.6であり、圧縮強度は
263Kgf/cm2 、圧縮弾性率は28,000Kg
f/cm2 と良好であった。また、各特性を比重で除し
た比圧縮強度、比圧縮弾性率はそれぞれ163Kgf/
cm2 、17,000Kgf/cm2 であった。
Using 60 parts of the above granular molded product as an aggregate, 40 parts of Portland cement and 20 parts of water were mixed, and 4c
pour into a bar mold of mx 4cm x 16cm,
After natural curing for a day, aggregate-reinforced blocks were prepared. The apparent specific gravity of the obtained block is 1.6, the compressive strength is 263 kgf / cm 2 , and the compressive modulus is 28,000 kg.
f / cm 2 was good. The specific compression strength and the specific compression elastic modulus obtained by dividing each characteristic by the specific gravity are 163 kgf /
cm 2 and 17,000 Kgf / cm 2 .

【0033】比較のため、本件発明の粒状成形物の代わ
りに海砂を骨材としたモルタル成形物を調製したとこ
ろ、見掛け比重は2.0、圧縮強度243Kgf/cm
2 、圧縮弾性率は35,000Kgf/cm2 、さらに
比圧縮強度122Kgf/cm2 、比圧縮弾性率18,
000Kgf/cm2 となり、本発明方法による粒状成
形物の配合が軽い上に良好な骨材としての配合効果を示
すことが認められた。
For comparison, a mortar molded product using sea sand as an aggregate instead of the granular molded product of the present invention was prepared. The apparent specific gravity was 2.0 and the compressive strength was 243 kgf / cm.
2 , the compression modulus is 35,000 Kgf / cm 2 , the specific compression strength is 122 Kgf / cm 2 , the specific compression modulus is 18,
It was 000 kgf / cm 2 , and it was confirmed that the compounding of the granular molded product according to the method of the present invention was light and showed a good mixing effect as an aggregate.

【0034】[比較例1]実施例1の原料組成物におけ
る水分の添加量を8部(原料組成物中の水分率として
4.8%に相当)に減少したところ、原料組成物の均一
混合は良好であったが、回転ディスク方式による造粒装
置を用いても、粉体表面の粘着性がなく、粒状に成形す
ることが出来なかった。
Comparative Example 1 When the amount of water added to the raw material composition of Example 1 was reduced to 8 parts (corresponding to 4.8% as the water content in the raw material composition), the raw material composition was uniformly mixed. However, even if a granulating apparatus using a rotating disk method was used, the powder surface had no tackiness and could not be formed into granules.

【0035】一方、上記実施例1の原料組成物における
水分の添加量を160部(原料組成物中の水分率として
50重量%に相当)に増加したところ、原料組成物の混
合の段階ですでに粉体状を維持することが出来ず、所望
の粒状成形物を得ることは出来なかった。すなわち、本
発明方法における原料組成物中の水分率を所定の範囲に
制御することが重要なポイントであることが確認出来
た。
On the other hand, when the amount of water added to the raw material composition of Example 1 was increased to 160 parts (corresponding to 50% by weight as the water content in the raw material composition), it was just at the stage of mixing the raw material composition. In addition, the powdery state could not be maintained, and a desired granular molded product could not be obtained. That is, it was confirmed that controlling the moisture content in the raw material composition in the method of the present invention within a predetermined range is an important point.

【0036】[実施例2]実施例1と同じフライアッシ
ュ100部に、無機バインダーとして珪酸ソーダJIS
―1号粉末(富士化学社製;二酸化珪素/酸化ナトリウ
ムのモル比=2.19)40部、粉末状ガラス繊維(日
東紡績社製PF A101)5部及び水40部(原料組
成物中、21.6重量%に相当)を混合して原料組成物
とし、これを実施例1と同様にして回転ディスク方式の
造粒装置を用いて、粒径が5〜8mmの粒状化物を得
た。この粒状化物を予備乾燥の後、電気炉に入れて常温
から350℃まで昇温、加熱し、さらに同温度に1時間
保持して、粒状成形物を得た。自然冷却後、得られた粒
状成形物の見掛け比重は1.54、圧壊強力は80〜1
00kgfと極めて良好であった。上記粒状成形物は、
セメントモルタルの骨材成分として使用することが可能
であり、人工軽量骨材として有用であることが認められ
た。
[Example 2] Sodium silicate JIS as an inorganic binder was added to 100 parts of fly ash as in Example 1.
No. 1 powder (Fuji Chemical Co., Ltd .; molar ratio of silicon dioxide / sodium oxide = 2.19) 40 parts, powder glass fiber (Nitto Boseki PF A101) 5 parts and water 40 parts (in the raw material composition, (Corresponding to 21.6% by weight) to obtain a raw material composition, which was obtained in the same manner as in Example 1 by using a rotary disk type granulator to obtain a granulated product having a particle size of 5 to 8 mm. After preliminary drying, the granulated material was placed in an electric furnace, heated from room temperature to 350 ° C., heated, and kept at the same temperature for 1 hour to obtain a granular molded product. After natural cooling, the apparent specific gravity of the obtained granular molded product is 1.54, and the crushing strength is 80 to 1
It was extremely good at 00 kgf. The granular molded product is
It could be used as an aggregate component of cement mortar, and was found to be useful as an artificial lightweight aggregate.

【0037】[実施例3]実施例1と同じフライアッシ
ュ100部に、無機バインダーとして珪酸ソーダJIS
―1号粉末(日本化学社製;二酸化珪素/酸化ナトリウ
ムのモル比=2.19)50部及び硬化調節剤としての
アルミナ粉末10部をニーダーを用いて混合し、さらに
水30部(原料組成物中、14.9重量%に相当)をす
こしづつ添加、混合して、原料組成物を得た。次いで、
この原料組成物を、直径2mmの多数の小孔を持つキャ
ップ面を有する押出し装置に供給し、スクリューを回転
することによって短いロッド状物を調製した。これを約
100℃の乾燥機で乾燥させた後、回転式クラッシャー
(例えば、不二パウダル社製整粒機「フラッシュミ
ル」)を用いて円柱型粒状形状に加工した。こうして得
られた粒状物を、実施例1と同様にして電気炉に入れ、
400℃まで昇温して焼成を行なった。得られた粒状成
形物は、見掛け比重1.30、圧壊強力40〜50Kg
fであり、骨材として有用であることが認められた。
[Example 3] Sodium silicate JIS as an inorganic binder was added to 100 parts of fly ash as in Example 1.
50 parts of No. 1 powder (manufactured by Nippon Chemical Co., Ltd .; molar ratio of silicon dioxide / sodium oxide = 2.19) and 10 parts of alumina powder as a curing modifier were mixed using a kneader, and further 30 parts of water (raw material composition) (Equivalent to 14.9% by weight in the product) was added little by little and mixed to obtain a raw material composition. Then
This raw material composition was supplied to an extruder having a cap surface having a large number of small holes having a diameter of 2 mm, and a short rod was prepared by rotating a screw. This was dried in a dryer at about 100 ° C., and then processed into a columnar granular shape using a rotary crusher (for example, “Flush Mill”, a particle sizer manufactured by Fuji Paudal Co., Ltd.). The granules thus obtained were placed in an electric furnace in the same manner as in Example 1,
The temperature was raised to 400 ° C. for firing. The obtained granular molded product has an apparent specific gravity of 1.30 and a crushing strength of 40 to 50 kg.
f, which proved to be useful as an aggregate.

【0038】[実施例4]実施例1と同じフライアッシ
ュ100部に対し、無機バインダーとしてJIS―1号
珪酸ソーダ粉末(富士化学社製:実施例2で使用したも
の)25部及びJIS―2号珪酸ソーダ粉末(富士化学
社製;二酸化珪素/酸化ナトリウムの比=2.52)2
5部、硬化促進剤としてのアルミナ粉末10部、形状保
持用添加剤としてのポリビニルアルコール2部及び水3
6部(原料組成物中、水分率18.2重量%に相当)を
添加して、原料混合物とした。次いで、この混合物を、
実施例1と同じ回転ディスク方式の造粒装置を用いて造
粒し、粒径2〜5mmの粒状体を得た。この粒状体を、
100℃の乾燥機中で予備乾燥した後、300℃の電気
炉に入れて3時間焼成することによって、粒状成形物を
得た。
Example 4 25 parts of JIS No. 1 sodium silicate powder (manufactured by Fuji Chemical Co., Ltd .: used in Example 2) as an inorganic binder and 100 parts of fly ash same as in Example 1 and JIS-2 No. sodium silicate powder (manufactured by Fuji Chemical; ratio of silicon dioxide / sodium oxide = 2.52) 2
5 parts, 10 parts of alumina powder as a curing accelerator, 2 parts of polyvinyl alcohol as a shape-maintaining additive, and 3 parts of water
6 parts (corresponding to a water content of 18.2% by weight in the raw material composition) was added to obtain a raw material mixture. This mixture is then
Granulation was performed using the same rotary disk granulator as in Example 1 to obtain granules having a particle size of 2 to 5 mm. This granular material,
After preliminary drying in a dryer at 100 ° C., it was placed in an electric furnace at 300 ° C. and calcined for 3 hours to obtain a granular molded product.

【0039】[0039]

【発明の効果】以上のごとき本発明方法によれば、軽量
かつ強靭で耐熱性の優れた無機質粒状成形物を得ること
が出来る。特に原料組成物中の水分率を所定の範囲に制
御することによって、望みのサイズ及び形状の、機械特
性の優れた軽量、無機質粒状成形物を得ることが出来
る。したがって、本発明方法による無機質粒状成形物
は、土木・建築用材料の骨材として、あるいは各種触媒
や農薬・肥料等の担持体として、さらには充填用材料と
して、広範な用途に有効に活用することが出来る。
According to the method of the present invention as described above, it is possible to obtain an inorganic granular molded product which is lightweight, tough, and excellent in heat resistance. In particular, by controlling the moisture content in the raw material composition to a predetermined range, a light-weight, inorganic granular molded product having a desired size and shape and excellent in mechanical properties can be obtained. Therefore, the inorganic granular molded product according to the method of the present invention is effectively used for a wide range of applications as an aggregate of civil engineering and building materials, or as a carrier for various catalysts, agricultural chemicals, fertilizers, and the like, and further as a filling material. I can do it.

Claims (10)

【特許請求の範囲】[Claims] 【請求項1】 石炭灰、アルカリ金属珪酸塩及び組成物
中10〜30重量%に相当する水分とを混合して得られ
る無機質原料組成物を、粒状に成形した後、焼成するこ
とを特徴とする無機質粒状成形物の製造方法。
An inorganic raw material composition obtained by mixing coal ash, an alkali metal silicate and 10 to 30% by weight of water in the composition is formed into granules and then fired. A method for producing an inorganic granular molded product.
【請求項2】 石炭灰、アルカリ金属珪酸塩、硬化調節
剤及び組成物中10〜30重量%に相当する水分とを混
合して得られる無機質原料組成物を、粒状に成形した
後、焼成することを特徴とする無機質粒状成形物の製造
方法。
2. An inorganic raw material composition obtained by mixing coal ash, an alkali metal silicate, a hardening modifier and 10 to 30% by weight of water in the composition is formed into granules and then fired. A method for producing an inorganic granular molded product, characterized in that:
【請求項3】 石炭灰100重量部に対し、20〜10
0重量部のアルカリ金属珪酸塩及び、組成物中10〜3
0重量%に相当する水分を混合して得られる無機系組成
物を、粒状に成形した後、焼成することを特徴とする無
機質粒状成形物の製造方法。
3. 20 to 10 parts by weight of coal ash
0 parts by weight of alkali metal silicate and 10 to 3 parts by weight in the composition
A method for producing an inorganic granular molded product, comprising forming an inorganic composition obtained by mixing water equivalent to 0% by weight into granules, and firing.
【請求項4】 該アルカリ金属珪酸塩が、硅酸ナトリウ
ムであることを特徴とする請求項1、請求項2または請
求項3記載の無機質粒状成形物の製造方法。
4. The method for producing an inorganic granular molded product according to claim 1, wherein the alkali metal silicate is sodium silicate.
【請求項5】 該アルカリ金属珪酸塩が珪酸ナトリウム
であり、かつ実質的にフリーの水分を含まない粉末状で
あることを特徴とする請求項1ないし請求項4記載のい
ずれかの無機質粒状成形物の製造方法。
5. The inorganic particulate molding according to claim 1, wherein said alkali metal silicate is sodium silicate and is in the form of powder substantially free of water. Method of manufacturing a product.
【請求項6】 該アルカリ金属珪酸塩が珪酸ナトリウム
であり、かつ酸化ナトリウム(Na2 O)に対する二酸
化珪素(SiO2 )のモル比が1.5〜3.5の範囲に
あることを特徴とする請求項1ないし請求項5記載のい
ずれかの無機質粒状成形物の製造方法。
6. The alkali metal silicate is sodium silicate, and the molar ratio of silicon dioxide (SiO 2 ) to sodium oxide (Na 2 O) is in the range of 1.5 to 3.5. The method for producing an inorganic granular molded product according to any one of claims 1 to 5.
【請求項7】 該硬化調節剤が、アルミニウム、マグネ
シウム、亜鉛、ホウ素及びカルシウムから選ばれた少な
くとも1種の金属の酸化物または水酸化物であることを
特徴とする請求項2記載の無機質粒状成形物の製造方
法。
7. The inorganic particulate material according to claim 2, wherein the curing regulator is an oxide or hydroxide of at least one metal selected from aluminum, magnesium, zinc, boron and calcium. Manufacturing method of molded product.
【請求項8】 該硬化調節剤の添加量が、石炭灰100
重量部に対し、5〜30重量部であることを特徴とする
請求項2記載の無機質粒状成形物の製造方法。
8. The method according to claim 8, wherein the amount of the curing regulator is 100 ash.
The method for producing an inorganic granular molded product according to claim 2, wherein the amount is 5 to 30 parts by weight based on parts by weight.
【請求項9】 焼成を300〜600℃の酸素含有雰囲
気または不活性ガス雰囲気中で行なうことを特徴とする
請求項1ないし請求項8記載のいずれかの無機質粒状成
形物の製造方法。
9. The method according to claim 1, wherein the calcination is performed in an oxygen-containing atmosphere or an inert gas atmosphere at 300 to 600 ° C.
【請求項10】 粒状に成形する際に、押出し機方式ま
たは回転ディスク方式を使用することを特徴とする請求
項1ないし請求項9記載のいずれかの無機質粒状成形物
の製造方法。
10. The method for producing an inorganic granular molded product according to claim 1, wherein an extruder method or a rotating disk method is used for forming the granular material.
JP21624397A 1997-08-11 1997-08-11 Production of inorganic granular molded body Pending JPH1160327A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP21624397A JPH1160327A (en) 1997-08-11 1997-08-11 Production of inorganic granular molded body

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP21624397A JPH1160327A (en) 1997-08-11 1997-08-11 Production of inorganic granular molded body

Publications (1)

Publication Number Publication Date
JPH1160327A true JPH1160327A (en) 1999-03-02

Family

ID=16685527

Family Applications (1)

Application Number Title Priority Date Filing Date
JP21624397A Pending JPH1160327A (en) 1997-08-11 1997-08-11 Production of inorganic granular molded body

Country Status (1)

Country Link
JP (1) JPH1160327A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0667667A3 (en) * 1988-11-11 1996-01-10 Sanyo Electric Co Battery charging apparatus.
JP2007186910A (en) * 2006-01-13 2007-07-26 Japan Fine Ceramics Center Ceramic sintered body, ballast, and ballast track bed
JP2015067526A (en) * 2013-09-30 2015-04-13 太平洋セメント株式会社 Method for processing coal ash, and cured product of coal ash residue of the processed product

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP0667667A3 (en) * 1988-11-11 1996-01-10 Sanyo Electric Co Battery charging apparatus.
JP2007186910A (en) * 2006-01-13 2007-07-26 Japan Fine Ceramics Center Ceramic sintered body, ballast, and ballast track bed
JP2015067526A (en) * 2013-09-30 2015-04-13 太平洋セメント株式会社 Method for processing coal ash, and cured product of coal ash residue of the processed product

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