JPH07232973A - Foaming inorganic composition - Google Patents
Foaming inorganic compositionInfo
- Publication number
- JPH07232973A JPH07232973A JP21361294A JP21361294A JPH07232973A JP H07232973 A JPH07232973 A JP H07232973A JP 21361294 A JP21361294 A JP 21361294A JP 21361294 A JP21361294 A JP 21361294A JP H07232973 A JPH07232973 A JP H07232973A
- Authority
- JP
- Japan
- Prior art keywords
- powder
- weight
- parts
- particle size
- fly ash
- 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
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
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P40/00—Technologies relating to the processing of minerals
- Y02P40/10—Production of cement, e.g. improving or optimising the production methods; Cement grinding
-
- 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
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/91—Use of waste materials as fillers for mortars or concrete
Landscapes
- Crushing And Grinding (AREA)
- Porous Artificial Stone Or Porous Ceramic Products (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】本発明は発泡性無機質組成物に関
する。FIELD OF THE INVENTION The present invention relates to a foamable inorganic composition.
【0002】[0002]
【従来の技術】従来、アルカリの存在下で熱により硬
化、発泡する無機質組成物については、幾つか提案され
ている。例えば、(a)発泡剤を用いることなく加熱下
において水蒸気の発生をもって発泡体を得る方法、ある
いは(b)金属粉体を加えてガスを発生させ発泡体を得
る方法などが知られていた。たとえば(b)の方法とし
ては、特開昭57−77062号公報には(A)水可溶
性アルカリ珪酸塩、(B)金属系発泡剤、(C)フライ
アッシュまたは高炉鉱滓及び(D)水を有効成分として
なる発泡性を有する無機質組成物が記載されている。2. Description of the Related Art Heretofore, there have been proposed some inorganic compositions which are cured and foamed by heat in the presence of an alkali. For example, (a) a method of obtaining a foam by generating steam under heating without using a foaming agent, or (b) a method of adding a metal powder to generate a gas to obtain a foam has been known. For example, as a method of (b), JP-A-57-77062 discloses that (A) water-soluble alkali silicate, (B) metal-based foaming agent, (C) fly ash or blast furnace slag and (D) water. An inorganic composition having foamability as an active ingredient is described.
【0003】しかし、上記の組成物を用いて得られた発
泡体は硬化速度が遅いので破泡しやすく気泡の均一性に
欠け、耐水性に劣り、低強度で低倍率の発泡体しか得ら
れず、更に乾燥時に熱収縮が発生し、クラックが発生す
るなどの他、フライアッシュ中に含まれる炭素のため白
色の発泡体が得られないという問題があった。However, since the foam obtained using the above composition has a slow curing rate, it is easily broken and lacks uniformity of cells, is poor in water resistance, and has low strength and low expansion ratio. However, there was a problem that a white foam could not be obtained due to the carbon contained in the fly ash, in addition to causing heat shrinkage and cracking during drying.
【発明が解決しようとする課題】本発明は上記の課題を
解決し、気泡の均一性、耐水性に優れ、高強度で低比重
でありながら熱収縮率の小さい発泡体を得ることのでき
る発泡性無機質組成物を提供することにある。DISCLOSURE OF THE INVENTION The present invention solves the above problems and provides a foam which is excellent in cell uniformity, water resistance, high strength, low specific gravity and a small heat shrinkage. The purpose of the present invention is to provide a porous inorganic composition.
【0004】[0004]
【0005】本発明において使用されるフライアッシュ
とはJIS A 6201に規定される、微粉炭燃焼ボ
イラーから集塵器で採取する微小な灰の粒子をいい、シ
リカ45%以上、湿分1%以下、強熱減量5%以下、比
重1.95以上、比表面積2,700cm2 /g以上、
44μm標準篩を75%以上が通過するものである。The fly ash used in the present invention means fine ash particles collected by a dust collector from a pulverized coal combustion boiler, which is defined in JIS A 6201, and has a silica content of 45% or more and a moisture content of 1% or less. , Ignition loss 5% or less, specific gravity 1.95 or more, specific surface area 2,700 cm 2 / g or more,
75% or more passes through a 44 μm standard sieve.
【0006】本発明において使用される(A)成分のう
ち、フライアッシュのうち、粒径が10μm以下であ
るものを80重量%以上含有する反応性無機質粉体と
は、上記フライアッシュをふるい分けや風力や静電気等
を利用して10μmを超える粒子を分離除去して得られ
る。猶、上記加工に際して上記粉砕や分級、分離の方法
は併用されてもよい。Of the component (A) used in the present invention, fly ash having a particle size of 10 μm or less and reactive inorganic powder containing 80% by weight or more is used as the above-mentioned fly ash. It can be obtained by separating and removing particles larger than 10 μm by using wind force, static electricity or the like. In the above processing, the methods of crushing, classifying and separating may be used together.
【0007】粒径10μm以下の反応性無機質粉体の量
は、少なくなるとアルカリ金属珪酸塩との反応性が低下
し、発泡性無機質組成物を発泡させて得られる発泡体は
発泡過程における破泡によって、気泡の均一性を欠き、
発泡倍率も低いものしか得られない。又、反応性の低下
によって、上記組成物の硬化も不良となり、得られる発
泡体の強度も脆弱なものとなってしまうので粒径10μ
m以下の反応性無機質粉体の量は80重量%以上に限定
される。When the amount of the reactive inorganic powder having a particle size of 10 μm or less decreases, the reactivity with the alkali metal silicate decreases, and the foam obtained by foaming the expandable inorganic composition is a foam-breaking material during the foaming process. The lack of uniformity of bubbles,
Only those with a low expansion ratio can be obtained. Further, due to the decrease in reactivity, the curing of the above composition also becomes poor, and the strength of the resulting foam becomes weak, so that the particle size is 10 μm.
The amount of reactive inorganic powder of m or less is limited to 80% by weight or more.
【0008】本発明において使用される(A)成分のう
ち、において、400〜1,000℃で焼成したフラ
イアッシュを使用する。フライアッシュは一般に黒色で
あるので、着色を必要とする用途に使用する場合、40
0℃以上の温度で焼成して脱色するが、1,000℃を
超える温度で焼成すると、上記アルカリ金属珪酸塩との
反応性が低下するので、上記範囲の温度で焼成すること
が好ましい。Among the components (A) used in the present invention, fly ash fired at 400 to 1,000 ° C. is used. Fly ash is generally black, so if you use it in applications that require coloring,
Although calcination is performed at a temperature of 0 ° C. or higher for decolorization, baking at a temperature of more than 1,000 ° C. lowers the reactivity with the alkali metal silicate, so calcination at a temperature in the above range is preferable.
【0009】本発明において使用される(A)成分のう
ち、及びにおいて、フライアッシュ及び粘土を溶融
し、気体中に噴霧することによって反応性無機質粉体を
得ているが、気体中に噴霧する方法として、セラミック
コーティングに適用される溶射技術が応用される。この
溶射技術は、好ましくは上記フライアッシュ及び粘土が
2,000〜16,000℃の温度で溶融され、30〜
800m/秒の速度で噴霧されるものであり、具体的に
は、プラズマ溶射法、高エネルギーガス溶射法、アーク
溶射法等が採用される。Of the component (A) used in the present invention, in and in, fly ash and clay are melted and sprayed in a gas to obtain a reactive inorganic powder, which is sprayed in a gas. As a method, thermal spraying techniques applied to ceramic coatings are applied. This spraying technique is preferably carried out by melting the fly ash and clay at a temperature of 2,000 to 16,000 ° C.
It is sprayed at a speed of 800 m / sec, and specifically, a plasma spraying method, a high energy gas spraying method, an arc spraying method or the like is adopted.
【0010】上記溶射技術によって得られる反応性無機
質粉体は、一般にその比表面積が0.1〜100m2 /
g、好ましくは0.1〜60m2 /gにコントロールさ
れる。The reactive inorganic powder obtained by the above thermal spraying technique generally has a specific surface area of 0.1 to 100 m 2 /
g, preferably 0.1 to 60 m 2 / g.
【0011】本発明において使用される(A)成分のう
ち、乃至の粘土は、化学組成として、SiO2 5〜
85重量%、Al2 O3 90〜10重量%を含有するこ
とが好ましい。このような粘土としては、例えば、カオ
リン鉱物(カオリナイト、ディッカナイト、ナクライ
ト、ハロイサイト等)、雲母粘土鉱物(白雲母、イライ
ト、フェンジャイト、海緑石、セラドナイト、パラゴナ
イト、ブランマライト等)、スメクタイト系鉱物(モン
モリロナイト、バイデイト、ノントロライト、サボナイ
ト、ソーコナイト等)、緑泥岩、パイロフィライト、タ
ルク、バーミキュライト、ろう岩、ばん土頁岩等が挙げ
られるが、組成、粒度等が適当であれば、これらに限定
されるものではない。Among the components (A) used in the present invention, the clay is composed of SiO 2 5 to 5 as a chemical composition.
It is preferable to contain 85% by weight and 90 to 10% by weight of Al 2 O 3 . Examples of such clays include kaolin minerals (kaolinite, dickanite, nacrite, halloysite, etc.), mica clay minerals (muscovite, illite, fengite, glauconite, celadonite, paragonite, blancmalite, etc.), smectite. Examples include minerals (montmorillonite, baidate, nontrolite, savonite, sauconite, etc.), chlorite, pyrophyllite, talc, vermiculite, wax rock, shale, etc. It is not limited to these.
【0012】本発明において使用される(A)成分のう
ち、乃至のフライアッシュ、粘土及びカオリン鉱物
に0.1〜30kwh/kgの機械的エネルギーを作用
させて反応性無機質粉体を得ているが、本発明におい
て、機械的エネルギーとは圧縮力、剪断力、衝撃力等を
指し、これらは単独で作用させてもよいし、2種以上を
複合させてもよい。これらを具体的に作用させる機器と
しては、例えば、ボールミル、振動ミル、遊星ミル、媒
体攪拌型ミル、ローラミル、乳鉢、ジェット粉砕装置等
が挙げられる。Among the components (A) used in the present invention, mechanical energy of 0.1 to 30 kwh / kg is applied to fly ash, clay and kaolin mineral to obtain a reactive inorganic powder. However, in the present invention, the mechanical energy refers to a compressive force, a shearing force, an impact force and the like, and these may be acted alone or in combination of two or more kinds. Examples of equipment that causes these to work concretely include a ball mill, a vibration mill, a planetary mill, a medium stirring type mill, a roller mill, a mortar, and a jet pulverizer.
【0013】上記乃至の粘土及びカオリン鉱物の粒
径は特に限定されないが、機械的エネルギーを有効に作
用させるには平均粒径が0.01〜500μmが好まし
く、更に好ましくは0.1〜100μmである。The particle sizes of the above clay and kaolin minerals are not particularly limited, but the average particle size is preferably 0.01 to 500 μm, more preferably 0.1 to 100 μm in order to effectively apply mechanical energy. is there.
【0014】上記、、及びのフライアッシュ及
び粘土に作用させる機械的エネルギーが0.1kwh/
kg未満であると、アルカリ金属珪酸塩との反応性が低
下し、30kwh/kgを超えると、上記粉砕装置等へ
の負荷が大きくなり、装置の磨耗、損傷が増大し、上記
粘土への不純物の混入等の問題が発生するので、0.1
〜30kwh/kgに限定され、好ましくは1.0〜2
6kwh/kgで作用させる。The mechanical energy acting on the fly ash and clay of the above, and, is 0.1 kwh /
If it is less than kg, the reactivity with the alkali metal silicate decreases, and if it exceeds 30 kwh / kg, the load on the crushing device and the like increases, the wear and damage of the device increases, and the impurities in the clay are increased. Since problems such as the mixture of
Limited to ~ 30 kwh / kg, preferably 1.0-2
Act at 6 kwh / kg.
【0015】又、上記のカオリン鉱物に作用させる機
械的エネルギーを0.1〜30kwh/kgに限定して
いる理由も、上記、、及びのフライアッシュ及
び粘土の場合と同様である。The reason why the mechanical energy acting on the kaolin mineral is limited to 0.1 to 30 kwh / kg is the same as in the case of the fly ash and clay described above.
【0016】本発明において機械的エネルギーを作用さ
せる際には、必要に応じて粉砕助剤が添加されてもよ
い。粉砕助剤とは、機械的エネルギーを作用させる際に
粘土乃至メタカオリンの粉体の装置内部への付着乃至は
著しい凝集を防ぐもので、例えば、メチルアルコール、
エチルアルコール等のアルコール類、トリエタノールア
ミン等のアルコールアミン類、ステアリン酸ナトリウ
ム、ステアリン酸カルシウムなどの金属石鹸類、アセト
ン蒸気等が挙げられる。これらは単独で使用されてもよ
いし、2種以上が併用されてもよい。When mechanical energy is applied in the present invention, a grinding aid may be added if necessary. The grinding aid is a material that prevents adhesion of the powder of clay or metakaolin to the inside of the apparatus or significant aggregation when mechanical energy is applied, such as methyl alcohol,
Examples thereof include alcohols such as ethyl alcohol, alcohol amines such as triethanolamine, metal soaps such as sodium stearate and calcium stearate, and acetone vapor. These may be used alone or in combination of two or more.
【0017】又、本発明において使用される(A)成分
のうち、及びの反応性無機質粉体は、粘土に上記機
械的エネルギーを作用させた後、更に、100〜750
℃に加熱して得られるが、加熱温度が100℃未満であ
ると、発泡性無機質組成物の発泡硬化後の成形体の機械
的強度を低下せしめ、750℃を超えると、上記反応性
無機質粉体の結晶化が促進され、アルカリ金属珪酸塩水
溶液に対する溶解性が低下するので、加熱温度は100
〜750℃に限定され、好ましくは200〜600℃で
ある。又、加熱時間は短くなると、得られる成形体の機
械的強度を低下せしめ、長くなると、エネルギーコスト
が増大するので、1分から5時間が好ましい。上記加熱
の方法は、特に限定するものではなく、例えば、熱風乾
燥機、ロータリーキルン等の従来公知の加熱装置が適宜
選択使用される。In addition, among the component (A) used in the present invention, the reactive inorganic powder of and, after the mechanical energy is applied to the clay, 100 to 750 is further added.
It is obtained by heating to ℃, but if the heating temperature is less than 100 ℃, the mechanical strength of the molded product after foaming and hardening of the foamable inorganic composition is lowered, and if it exceeds 750 ℃, the above reactive inorganic powder. Since the crystallization of the body is promoted and the solubility in the alkali metal silicate aqueous solution is lowered, the heating temperature is 100
It is limited to 750 degreeC, Preferably it is 200-600 degreeC. Further, when the heating time is shortened, the mechanical strength of the obtained molded article is lowered, and when the heating time is prolonged, the energy cost is increased, so 1 minute to 5 hours is preferable. The heating method is not particularly limited and, for example, a conventionally known heating device such as a hot air dryer or a rotary kiln is appropriately selected and used.
【0018】本発明において使用されるメタカオリン
は、前述の粘度鉱物の一種であるカオリン鉱物を加熱脱
水することによって得られるが、加熱温度が500℃未
満であるとカオリン鉱物の水酸基が脱離せず、メタカオ
リンへの変成が起こらず、900℃を超えると結晶化が
起こり、反応性が著しく低下する。よって、加熱温度は
500〜900℃であることが好ましく、更に好ましく
は600〜800℃である。この加熱時間は短すぎると
メタカオリンへの変成が起こらず、長くしてもそれ以上
の効果は得られないので、5分〜10時間が好ましい。The metakaolin used in the present invention can be obtained by heating and dehydrating kaolin mineral which is one of the above-mentioned clay minerals. However, if the heating temperature is lower than 500 ° C., the hydroxyl groups of kaolin mineral are not eliminated, If metakaolin is not converted, and if it exceeds 900 ° C., crystallization occurs and the reactivity is significantly reduced. Therefore, the heating temperature is preferably 500 to 900 ° C, more preferably 600 to 800 ° C. If the heating time is too short, the conversion to metakaolin does not occur, and even if the heating time is long, no further effect can be obtained, so 5 minutes to 10 hours is preferable.
【0019】本発明に使用されるアルカリ金属珪酸塩
(B)とはM2 O・nSiO2 (M=K、Na、Liか
ら選ばれる1種以上の金属)で表される珪酸塩であっ
て、nの値は小さくなると緻密な発泡体が得られず、大
きくなると水溶液の粘度が上昇し混合が困難になるので
0.05〜8が好ましく、更に好ましくは0.5〜2.
5である。The alkali metal silicate (B) used in the present invention is a silicate represented by M 2 O.nSiO 2 (M = K, one or more metals selected from Na and Li). , N does not allow a dense foam to be obtained, while a larger value increases the viscosity of the aqueous solution and makes mixing difficult, so that it is preferably 0.05 to 8, and more preferably 0.5 to 2.
It is 5.
【0020】アルカリ金属珪酸塩(B)は水溶液で添加
されるのが好ましく、水溶液濃度は特に限定されない
が、薄くなると上記(A)成分の反応性無機質粉体との
反応性が低下し、濃くなると固形物が生じやすくなるの
で10〜60重量%が好ましい。The alkali metal silicate (B) is preferably added in an aqueous solution, and the concentration of the aqueous solution is not particularly limited, but when the concentration becomes thin, the reactivity with the reactive inorganic powder of the component (A) decreases and the concentration becomes high. If so, solids are likely to be formed, so 10 to 60% by weight is preferable.
【0021】上記アルカリ金属珪酸塩水溶液はアルカリ
金属珪酸塩をそのまま加圧、加熱下で水に溶解してもよ
いが、アルカリ金属水酸化物水溶液に珪砂、珪石粉など
のSiO2 成分をnが所定の量となるように加圧、加熱
下で溶解してもよい。上記アルカリ金属珪酸塩の量は、
少なくなると硬化が十分になされず、多くなると得られ
る発泡体の耐水性が低下するので上記(A)成分の反応
性無機質粉体100重量部に対して0.2〜450重量
部に限定され、好ましくは10〜350重量部である。The alkali metal silicate aqueous solution may be prepared by dissolving the alkali metal silicate in water as it is under pressure and heating. However, the alkali metal hydroxide aqueous solution may contain SiO 2 components such as silica sand and silica stone powder as n. You may melt | dissolve under pressure and heating so that it may become a predetermined amount. The amount of alkali metal silicate is
If the amount is too small, the curing will not be sufficient, and if the amount is too large, the water resistance of the resulting foam will decrease. Therefore, the amount is limited to 0.2 to 450 parts by weight with respect to 100 parts by weight of the reactive inorganic powder of the component (A), It is preferably 10 to 350 parts by weight.
【0022】本発明において使用される金属粉末(C)
とはアルカリ金属珪酸塩水溶液と反応して水素ガスを放
出するものならば特に限定されず、たとえばMg、C
a、Cr、Mn、Co、Ni、Cu、Zn、Al、G
a、Sn、Si等の粉末が挙げられる。就中、アルミニ
ウム粉末は好適に使用される。これらは単独で使用され
てもよいし、2種類以上併用されてもよい。上記金属粉
末の平均粒径は小さくなると分散性が低下し、破泡が発
生しやすくなり、大きくなるとアルカリ金属珪酸塩水溶
液との反応性が低下するので1〜200μmが好まし
い。上記金属粉末の量は少なくなると低密度の発泡体が
得られず、多くなると破泡が発生しやすくなるので上記
(A)成分の反応性無機質粉体100重量部に対して
0.01〜5重量部に限定され、好ましくは0.02〜
1重量部、更に好ましくは0.03〜0.3重量部であ
る。Metal powder (C) used in the present invention
Is not particularly limited as long as it reacts with an aqueous solution of an alkali metal silicate to release hydrogen gas, and examples thereof include Mg and C.
a, Cr, Mn, Co, Ni, Cu, Zn, Al, G
Powders of a, Sn, Si and the like are included. Above all, aluminum powder is preferably used. These may be used alone or in combination of two or more. If the average particle size of the metal powder is small, the dispersibility is lowered and foam breakage is likely to occur, and if it is large, the reactivity with the alkali metal silicate aqueous solution is lowered. When the amount of the metal powder is small, a foam having a low density cannot be obtained, and when the amount is large, breakage is likely to occur. Therefore, 0.01 to 5 is added to 100 parts by weight of the reactive inorganic powder of the component (A). Limited to parts by weight, preferably 0.02
1 part by weight, more preferably 0.03 to 0.3 part by weight.
【0023】本発明で使用される水(D)は、独立して
添加されてもよいが、前記する如く上記アルカリ金属水
酸化物水溶液として添加されるのがよい。又、水(D)
の添加量は、上記(A)成分の反応性無機質粉体100
重量部に対して35重量部未満であると、発泡性無機質
組成物を十分に硬化せず、また、破泡が発生しやすくな
り、1,500重量部を超えると、得られる発泡体の強
度が低下しやすくなるので上記(A)成分の反応性無機
質粉体100重量部に対して35〜1,500重量部に
限定され、好ましくは45〜1,000重量部、更に好
ましくは50〜500重量部である。The water (D) used in the present invention may be added independently, but as described above, it is preferably added as the above-mentioned aqueous solution of alkali metal hydroxide. Also, water (D)
The amount of addition of 100 is the reactive inorganic powder 100 of the component (A).
If the amount is less than 35 parts by weight, the expandable inorganic composition will not be sufficiently cured and foam breakage will easily occur. If the amount is more than 1,500 parts by weight, the strength of the resulting foam will be increased. Since it tends to decrease, it is limited to 35 to 1,500 parts by weight, preferably 45 to 1,000 parts by weight, more preferably 50 to 500 parts by weight, relative to 100 parts by weight of the reactive inorganic powder of the component (A). Parts by weight.
【0024】本発明において必要に応じて発泡助剤が添
加されてもよい。発泡助剤は発泡を均一に生じさせるも
のなら特に限定されず、たとえばステアリン酸亜鉛、ス
テアリン酸カルシウム、パルミチン酸亜鉛等の脂肪酸金
属塩、シリカゲル、ゼオライト、活性炭、アルミナ粉末
等の多孔質粉体などがあげられる。これらは単独で使用
されてもよいし、2種類以上併用されてもよい。In the present invention, a foaming aid may be added if necessary. The foaming aid is not particularly limited as long as it uniformly causes foaming, and examples thereof include fatty acid metal salts such as zinc stearate, calcium stearate, zinc palmitate, silica gel, zeolite, activated carbon, and porous powder such as alumina powder. can give. These may be used alone or in combination of two or more.
【0025】上記発泡助剤の量は、多くなると発泡性無
機質組成物の粘度が大きくなり、発泡時破泡が発生しや
すく、安定な発泡体が得られないので、上記(A)成分
の反応性無機質粉体100重量部に対して10重量部以
下が好ましい。When the amount of the foaming aid is large, the viscosity of the foamable inorganic composition becomes large, and the foaming tends to occur during foaming, and a stable foam cannot be obtained. It is preferably 10 parts by weight or less with respect to 100 parts by weight of the hydrophilic inorganic powder.
【0026】本発明において必要に応じて充填材が添加
されてもよい。充填材は水に溶解せず、本発明の硬化性
無機質組成物の硬化反応を阻害せず、本発明の上記組成
物で使用される総ての構成成分の作用を著しく阻害しな
いものが好ましく、例えば、珪砂、川砂等のセメントモ
ルタル用骨材、シリカフラワー、シリカフューム、ベン
トナイト、高炉スラグ等の混合セメント用混合材、セピ
オライト、ワラストナイト、ジルコンサンド、珪石粉、
けいそう土、雲母、タルク、岩石粉末、火山灰(シラ
ス、抗火石等)等の天然鉱物、炭酸カルシウム、結晶質
アルミナ等が挙げられるがこれらに限定されるものでは
ない。In the present invention, a filler may be added if necessary. Filler is not soluble in water, preferably does not inhibit the curing reaction of the curable inorganic composition of the present invention, does not significantly inhibit the action of all the components used in the above composition of the present invention, For example, silica sand, aggregate for cement mortar such as river sand, silica flower, silica fume, bentonite, mixture material for mixed cement such as blast furnace slag, sepiolite, wollastonite, zircon sand, silica stone powder,
Examples thereof include, but are not limited to, diatomaceous earth, mica, talc, rock powder, natural minerals such as volcanic ash (shirasu, anti-firestone, etc.), calcium carbonate, crystalline alumina and the like.
【0027】上記充填材は、特にアルカリ金属珪酸塩水
溶液に対して活性が低いことが求められるが、活性が高
いと、アルカリ水溶液及びアルカリ金属珪酸塩水溶液の
ゲル化が急速に進み、発泡性無機質組成物の混合作業や
成形作業が難しくなるからである。The above-mentioned filler is required to have low activity especially to the alkali metal silicate aqueous solution. When the activity is high, the gelation of the alkali aqueous solution and the alkali metal silicate aqueous solution proceeds rapidly, and the foamable inorganic material is formed. This is because the work of mixing and molding the composition becomes difficult.
【0028】本発明において使用される充填材のうち、
粒状のものは、平均粒径が小さくなるとアルカリ金属
珪酸塩に溶解されやすくなり、大きくなると熱収縮を抑
えきれなくなるので0.01〜30μmの範囲にあるも
のが好ましい。又、針状、角状あるいは柱状の形状を
有するものであるときには、長軸方向の長さは短くなる
と熱収縮を防ぐことが困難になり、長くなると混練が困
難になるので1〜250μmであることが好ましい。Among the fillers used in the present invention,
The granular particles are easily dissolved in the alkali metal silicate when the average particle size is small, and the thermal contraction cannot be suppressed when the average particle size is large, and therefore the particles are preferably in the range of 0.01 to 30 μm. Further, in the case of having a needle shape, a square shape, or a columnar shape, if the length in the major axis direction becomes shorter, it becomes difficult to prevent heat shrinkage, and if the length becomes longer, kneading becomes difficult, so that it is 1 to 250 μm. It is preferable.
【0029】上記針状、角状あるいは柱状の形状を有
する充填材の長軸径(a)と短軸径(b)の比(a/
b)は、50/1を超える場合、成形が困難となり、気
泡が安定せず、不均一になったり、破泡したりして発泡
硬化後の成形体の機械的強度が低下し、1.5/1未満
の場合、得られる成形体の乾燥収縮、熱収縮が大きく、
成形体が歪んだり、亀裂を生じたりするので、長軸径
(a)と短軸径(b)の比(a/b)は、50/1〜
1.5/1、好ましくは30/1〜2/1、更に好まし
くは20/1〜3/1の範囲にあるものが選ばれる。The ratio of the major axis diameter (a) to the minor axis diameter (b) (a /
When the ratio b) is more than 50/1, the molding becomes difficult, the bubbles are not stable, and the mechanical strength of the molded product after foaming and hardening is reduced due to nonuniformity or breakage, and If it is less than 5/1, the resulting molded article has large dry shrinkage and heat shrinkage,
Since the molded body may be distorted or cracked, the ratio (a / b) of the major axis diameter (a) to the minor axis diameter (b) is 50/1 to
Those in the range of 1.5 / 1, preferably 30/1 to 2/1, and more preferably 20/1 to 3/1 are selected.
【0030】上記充填材の配合量は、上記(A)成分の
反応性無機質粉体100重量部に対し20重量部未満の
場合、発泡性無機質組成物の発泡硬化後の成形体の乾燥
収縮、熱収縮が大きく、800重量部を超えると、上記
成形体の機械的強度を低下せしめるため、20〜800
重量部、好ましくは30〜600重量部、更に好ましく
は40〜400重量部が添加される。When the content of the above-mentioned filler is less than 20 parts by weight based on 100 parts by weight of the reactive inorganic powder of the component (A), dry shrinkage of the molded body of the expandable inorganic composition after foam curing, If the heat shrinkage is large and exceeds 800 parts by weight, the mechanical strength of the above-mentioned molded product is lowered, so that it is 20 to 800.
Parts by weight, preferably 30 to 600 parts by weight, more preferably 40 to 400 parts by weight are added.
【0031】上記充填材は、上記の如くグループ毎にい
ずれか一方のみを単独もしくは2種以上を混合して使用
してもよいが、併用することもできる。この上記両グル
ープを併用した場合、それぞれをグループ毎にいずれか
一方のみを使用した場合よりも発泡硬化後の成形体の機
械的強度を改善する等の新たな効果を発揮する。猶、上
記充填材の配合量は、合計で上記(A)成分の反応性無
機質粉体100重量部に対し、20〜800重量部であ
り、好ましくは30〜600重量部、更に好ましくは4
0〜400重量部である。The above-mentioned fillers may be used alone or as a mixture of two or more kinds for each group as described above, or may be used in combination. When these two groups are used in combination, new effects such as improvement in mechanical strength of the molded product after foaming and hardening are exhibited as compared with the case where only one of the groups is used. The amount of the filler to be added is 20 to 800 parts by weight, preferably 30 to 600 parts by weight, and more preferably 4 parts by weight, based on 100 parts by weight of the reactive inorganic powder of the component (A).
0 to 400 parts by weight.
【0032】上記充填材の及びの両グループを併用
した場合、その配合割合は、の量が全無機質充填材量
の60重量%以下であることが熱収縮の改善に繋がり、
上記新たな効果を発揮するために必要である。When both groups of the above-mentioned fillers are used in combination, the blending ratio of 60% by weight or less of the total amount of the inorganic fillers leads to improvement of heat shrinkage,
It is necessary to exert the above new effects.
【0033】本発明においてさらに必要に応じて補強繊
維が添加されてもよい。補強繊維は、成形体に付与した
い性能に応じ任意のものが使用でき、例えば、ビニロン
繊維、セルロース繊維、ポリアミド繊維、ポリエステル
繊維、ポリプロピレン繊維、カーボン繊維、アラミド繊
維、ガラス繊維、チタン酸カリウム繊維、鋼繊維等が使
用できる。上記補強繊維の繊維径は、細くなると混合時
に再凝集し、交絡によりファイバーボールが形成されや
すくなり、最終的に得られる発泡体の強度はそれ以上改
善されず、太くなるか又は短くなると引張強度向上など
の補強効果が小さく、又、長くなると繊維の分散性及び
配向性が低下するので、繊維径1〜500μm、繊維長
1〜15mmが好ましい。上記補強繊維の添加量は多く
なると繊維の分散性が低下するので、上記(A)成分の
反応性無機質粉体100重量部に対し、10重量部以下
が好ましい。In the present invention, reinforcing fibers may further be added if necessary. Reinforcement fiber, any one can be used depending on the performance desired to impart to the molded body, for example, vinylon fiber, cellulose fiber, polyamide fiber, polyester fiber, polypropylene fiber, carbon fiber, aramid fiber, glass fiber, potassium titanate fiber, Steel fibers can be used. The fiber diameter of the reinforcing fiber is reaggregated during mixing when it becomes thin, fiber balls are easily formed by entanglement, the strength of the finally obtained foam is not further improved, and when it becomes thicker or shorter, the tensile strength increases. Since the reinforcing effect such as improvement is small and the dispersibility and the orientation of the fiber are reduced when it is long, the fiber diameter is preferably 1 to 500 μm and the fiber length is 1 to 15 mm. Since the dispersibility of the fibers decreases as the amount of the reinforcing fibers added increases, it is preferably 10 parts by weight or less with respect to 100 parts by weight of the reactive inorganic powder of the component (A).
【0034】本発明の発泡性無機質組成物は、更に発泡
体の軽量化を図る目的でシリカバルーン、パーライト、
フライアッシュバルーン、シラスバルーン、ガラスバル
ーン、発泡焼成粘土等の無機質発泡体、フェノール樹
脂、ウレタン樹脂、ポリエチレン、ポリスチレン等の有
機質発泡体、塩化ビニリデンバルーン等が添加されても
よい。これらは単独で添加されてもよいし、2種類以上
併用されてもよい。The expandable inorganic composition of the present invention contains silica balloon, pearlite, and / or silica balloon for the purpose of further reducing the weight of the foam.
Inorganic foams such as fly ash balloons, shirasu balloons, glass balloons, foamed and baked clay, organic foams such as phenol resins, urethane resins, polyethylene and polystyrene, and vinylidene chloride balloons may be added. These may be added alone or in combination of two or more.
【0035】本発明の組成物から発泡体を得るには、ま
ず上記アルカリ金属珪酸塩(B)を加圧、加熱下で水
(D)に溶解し、反応性無機質粉体(A)及び必要に応
じて発泡助剤、充填材、補強繊維を混合し、金属粉末
(C)を添加した後、注型、押圧成形、押出成形など従
来公知の方法により所望の形に発泡させて賦形し、硬化
させるなどの方法が使用できる。猶、金属粉末は予めア
ルカリ金属珪酸塩(B)水溶液以外の成分と混合して添
加してもよい。In order to obtain a foamed product from the composition of the present invention, first, the above alkali metal silicate (B) is dissolved in water (D) under pressure and heating to prepare the reactive inorganic powder (A) and necessary components. A foaming aid, a filler, and a reinforcing fiber are mixed in accordance with the above, and after the metal powder (C) is added, it is foamed into a desired shape by a conventionally known method such as casting, press molding, extrusion molding, and shaping. , Curing, etc. can be used. Alternatively, the metal powder may be added in advance by mixing it with a component other than the alkali metal silicate (B) aqueous solution.
【0036】上記硬化温度は常温でもよいが、50〜1
10℃で30分間〜8時間硬化させることにより、硬化
反応を促進でき、機械的物性を向上することができる。The above curing temperature may be room temperature, but it is 50 to 1
By curing at 10 ° C. for 30 minutes to 8 hours, the curing reaction can be promoted and the mechanical properties can be improved.
【0037】[0037]
【実施例】本発明を実施例をもって更に詳しく説明す
る。EXAMPLES The present invention will be described in more detail by way of examples.
【0038】反応性無機質粉体1、2の作製 フライアッシュ(関電化工社製、平均粒径20μm;J
IS A 6201に準ずる)を分級機(日清エンジニ
アリング社製、型式;TC−15)により分級し、粒径
が10μm以下の粉体を100重量%含有する反応性無
機質粉体1(10重量%)と、粒径が10μmを超える
粉体を100重量%含有する反応性無機質粉体2(90
重量%)とを得た。Preparation of Reactive Inorganic Powders 1 and 2 Fly ash (manufactured by KANDENKA CORPORATION, average particle size 20 μm; J
A reactive inorganic powder 1 (10% by weight) containing 100% by weight of a powder having a particle size of 10 μm or less is obtained by classifying an IS A 6201) by a classifier (manufactured by Nisshin Engineering Co., Ltd., model: TC-15). ) And 100% by weight of powder having a particle size of more than 10 μm.
% By weight).
【0039】反応性無機質粉体3の作製 上記反応性無機質粉体1を焼成炉内で200℃/hrの
昇温速度で600℃、2時間焼成し、反応性無機質粉体
3を得た。Preparation of Reactive Inorganic Powder 3 The above-mentioned reactive inorganic powder 1 was fired in a firing furnace at a temperature rising rate of 200 ° C./hr at 600 ° C. for 2 hours to obtain a reactive inorganic powder 3.
【0040】反応性無機質粉体4の作製 フライアッシュ(関電化工社製、平均粒径20μm;J
IS A 6201に準ずる)を3,000℃で溶融
後、80m/秒の速度で大気中に噴霧して平均粒径5μ
m、比表面積9.5m2 /gの反応性無機質粉体4を得
た。Preparation of Reactive Inorganic Powder 4 Fly ash (manufactured by KANDENKA CORPORATION, average particle size 20 μm; J
(According to IS A 6201) is melted at 3,000 ° C. and sprayed into the atmosphere at a speed of 80 m / sec to give an average particle size of 5 μm.
m was obtained, and a reactive inorganic powder 4 having a specific surface area of 9.5 m 2 / g was obtained.
【0041】反応性無機質粉体5の作製 カオリン(組成:SiO2 45.7%、Al2 O3 3
8.3%、平均粒径:8μm、BET比表面積:5.8
m2 /g)を燃焼温度2,500℃、噴射粒子速度50
m/秒で溶射し、組成:SiO2 49.7%、Al2 O
3 47.0%、平均粒径:14.8μm、BET比表面
積:1.96m2 /gの反応性無機質粉体5を得た。Preparation of Reactive Inorganic Powder 5 Kaolin (composition: SiO 2 45.7%, Al 2 O 3 3
8.3%, average particle size: 8 μm, BET specific surface area: 5.8
m 2 / g) with a combustion temperature of 2,500 ° C. and an injection particle velocity of 50
Sprayed at m / sec, composition: SiO 2 49.7%, Al 2 O
3 47.0%, average particle size: 14.8μm, BET specific surface area: to obtain a reactive inorganic powder 5 of 1.96m 2 / g.
【0042】反応性無機質粉体6の作製 フライアッシュ(関電化工社製、平均粒径20μm;J
IS A 6201に準ずる)100重量部にトリエタ
ノールアミン25重量%とエタノール75重量%よりな
る混合溶液0.5重量部をウルトラファインミルAT−
20(三菱重工業社製、10mmジルコニアボール使
用、ボール充填率85体積%)に供給し、25kwh/
kgの機械的エネルギーを作用させ、反応性無機質粉体
6を得た。猶、作用させた機械的エネルギーは上記ウル
トラファインミルに供給した電力を処理粉体単位重量で
除して表した。Preparation of Reactive Inorganic Powder 6 Fly ash (manufactured by KANDENKA CORPORATION, average particle size 20 μm; J
0.5 parts by weight of a mixed solution of 25% by weight of triethanolamine and 75% by weight of ethanol was added to 100 parts by weight of Ultra Fine Mill AT-.
20 (using Mitsubishi Heavy Industries' 10 mm zirconia balls, ball filling rate 85% by volume), 25 kwh /
Mechanical energy of kg was applied to obtain a reactive inorganic powder 6. The mechanical energy applied was expressed by dividing the electric power supplied to the ultrafine mill by the unit weight of the treated powder.
【0043】反応性無機質粉体7の作製 カオリン(組成:SiO2 45.7%、Al2 O3 3
8.3%、平均粒径:5μm、BET比表面積:5.8
m2 /g)95重量部とクォーツ(住友セメント社製、
商品名:ソフトシリカ)5重量部及びトリエタノールア
ミン25重量%とエタノール75重量%の混合溶液0.
5重量部を、ウルトラファインミルAT−20(三菱重
工社製、ジルコニアボール10mm使用、ボール充填率
85体積%)に供給し、25kwh/kgの機械的エネ
ルギーを作用させ、反応性無機質粉体7を得た。猶、作
用させた機械的エネルギーは上記ウルトラファインミル
に供給した電力を処理粉体単位重量で除して表した。Preparation of Reactive Inorganic Powder 7 Kaolin (Composition: SiO 2 45.7%, Al 2 O 3 3
8.3%, average particle size: 5 μm, BET specific surface area: 5.8
m 2 / g) 95 parts by weight and quartz (Sumitomo Cement Co.,
Brand name: soft silica) 5 parts by weight and a mixed solution of 25% by weight of triethanolamine and 75% by weight of ethanol.
5 parts by weight was supplied to Ultra Fine Mill AT-20 (manufactured by Mitsubishi Heavy Industries, Ltd., using zirconia balls 10 mm, ball filling rate 85% by volume), and mechanical energy of 25 kwh / kg was applied to the reactive inorganic powder 7 Got The mechanical energy applied was expressed by dividing the electric power supplied to the ultrafine mill by the unit weight of the treated powder.
【0044】反応性無機質粉体8の作製 上記反応性無機質粉体7を、300℃で3時間加熱して
反応性無機質粉体8を得た。Preparation of Reactive Inorganic Powder 8 Reactive inorganic powder 7 was heated at 300 ° C. for 3 hours to obtain reactive inorganic powder 8.
【0045】反応性無機質粉体9 メタカオリン(エンゲルハード社製、商品名:SATI
NTONE SP 33、平均粒径3.3μm、BET
比表面積:13.9m2 /g)Reactive Inorganic Powder 9 Metakaolin (manufactured by Engelhard, trade name: SATI)
NTONE SP 33, average particle size 3.3μm, BET
Specific surface area: 13.9 m 2 / g)
【0046】反応性無機質粉体10の作製 メタカオリン(エンゲルハード社製、商品名:SATI
NTONE SP 33、平均粒径3.3μm、BET
比表面積:13.9m2 /g)100重量部及びトリエ
タノールアミン25重量%とエタノール75重量%の混
合溶液0.5重量部を、ウルトラファインミルAT−2
0(三菱重工社製、ジルコニアボール10mm使用、ボ
ール充填率85体積%)に供給し、25kwh/kgの
機械的エネルギーを作用させ、反応性無機質粉体10を
得た。猶、作用させた機械的エネルギーは上記ウルトラ
ファインミルに供給した電力を処理粉体単位重量で除し
て表した。Preparation of Reactive Inorganic Powder 10 Metakaolin (manufactured by Engelhard, trade name: SATI)
NTONE SP 33, average particle size 3.3μm, BET
100 parts by weight of specific surface area: 13.9 m 2 / g) and 0.5 parts by weight of a mixed solution of 25% by weight of triethanolamine and 75% by weight of ethanol were added to Ultra Fine Mill AT-2.
0 (manufactured by Mitsubishi Heavy Industries, using 10 mm of zirconia balls, ball filling rate 85% by volume), and mechanical energy of 25 kwh / kg was applied to obtain reactive inorganic powder 10. The mechanical energy applied was expressed by dividing the electric power supplied to the ultrafine mill by the unit weight of the treated powder.
【0047】アルミニウム粉末1〜3 アルミニウム粉末1(ミナルコ社製、品番#350F、
平均粒径70μm以下) アルミニウム粉末2(ミナルコ社製、品番#260S、
平均粒径100μm以下) アルミニウム粉末3(ミナルコ社製、品番#220S
P、平均粒径300μm以下)Aluminum powder 1 to 3 Aluminum powder 1 (manufactured by Minarco, product number # 350F,
Average particle size 70 μm or less) Aluminum powder 2 (manufactured by Minarco, product number # 260S,
Average particle size 100 μm or less) Aluminum powder 3 (manufactured by Minarco, product number # 220S)
P, average particle size of 300 μm or less)
【0048】実施例1〜26、比較例1〜31 実施例1〜26及び比較例1〜31について、表1〜6
に示した所定量のSiO2 /M2 Oのモル比が1.8の
アルカリ金属珪酸塩(D)(NaとKのモル比が1:
1)をオートクレーブ中において、130℃、ゲージ圧
7kg/cm2 で所定量の水(E)に溶解し、所定量の
無機質充填材(B)1〜3、ビニロン繊維(クラレ社
製、品番:RM182×3)、ステアリン酸亜鉛をそれ
ぞれ添加して、ハンドミキサーで3分間混合した。得ら
れた混合物に金属粉末(C)1〜3又は過酸化水素、過
硼酸ナトリウムを添加して20秒間攪拌し、型枠内に注
入して3分間発泡させた後、型枠ごと85℃のオーブン
中で6時間加熱させて発泡体を得た。得られた発泡体を
脱型して85℃で4時間乾燥した。猶、粒径はレーザー
回折式分布計(セイシン社製、型式:PRO700S)
で測定した。得られた発泡体を下記の条件で評価し、結
果を表7〜13に示した。Examples 1 to 26, Comparative Examples 1 to 31 Tables 1 to 6 for Examples 1 to 26 and Comparative Examples 1 to 31
Alkali metal silicate (D) having a predetermined SiO 2 / M 2 O molar ratio of 1.8 shown in
In an autoclave, 1) is dissolved in a predetermined amount of water (E) at 130 ° C. and a gauge pressure of 7 kg / cm 2 , and a predetermined amount of inorganic fillers (B) 1 to 3 and vinylon fiber (manufactured by Kuraray Co., product number: RM182 × 3) and zinc stearate were added, and mixed for 3 minutes with a hand mixer. Metal powders (C) 1 to 3 or hydrogen peroxide and sodium perborate were added to the obtained mixture, and the mixture was stirred for 20 seconds, poured into a mold and foamed for 3 minutes, and then the whole mold was heated at 85 ° C. A foam was obtained by heating in an oven for 6 hours. The obtained foam was demolded and dried at 85 ° C. for 4 hours. Grasp, particle size is laser diffraction type distribution meter (manufactured by Seishin Co., model: PRO700S)
It was measured at. The obtained foam was evaluated under the following conditions, and the results are shown in Tables 7 to 13.
【0049】気泡の均一性 得られた発泡体の断面を顕微鏡で観察し、直径の最大値
と最小値の比が1.5以下のものに○、1.5以上のも
のに×を記した。Uniformity of Cells The cross section of the obtained foam was observed under a microscope, and the ratio of the maximum value to the minimum value of the diameter was 1.5 or less, and the mark was marked with X or more. .
【0050】圧縮強度 得られた発泡体を30×30×30mmに切断しJIS
A 1108に準じて圧縮強度を測定した。Compressive strength The obtained foam is cut into 30 × 30 × 30 mm and JIS
Compressive strength was measured according to A 1108.
【0051】耐水試験後の強度保持率 得られた発泡体を50×50×50mmに切断し90℃
の水中に8時間浸漬後上記と同様に圧縮強度を測定し、
強度保持率を求めた。Strength retention after water resistance test The obtained foam was cut into 50 × 50 × 50 mm and 90 ° C.
After immersing in water for 8 hours, measure the compressive strength as above,
The strength retention was determined.
【0052】加熱試験後の収縮率 得られた発泡体を100×100×100mmに切断し
100℃のオーブンで6時間加熱した後長さを測定し、
収縮率を求めた。Shrinkage after heating test The obtained foam was cut into 100 × 100 × 100 mm and heated in an oven at 100 ° C. for 6 hours, and then the length was measured.
The shrinkage rate was calculated.
【0053】比重 得られた発泡体を100×100×100mmに切断
し、重量を測定した。Specific gravity The obtained foam was cut into 100 × 100 × 100 mm and the weight was measured.
【0054】成形体の色 得られた発泡体をJIS Z 8729に準じてL* を
測定した。Color of Molded Body The obtained foam was measured for L * according to JIS Z 8729.
【0055】[0055]
【表1】 [Table 1]
【0056】[0056]
【表2】 [Table 2]
【0057】[0057]
【表3】 [Table 3]
【0058】[0058]
【表4】 [Table 4]
【0059】[0059]
【表5】 [Table 5]
【0060】[0060]
【表6】 [Table 6]
【0061】[0061]
【表7】 [Table 7]
【0062】[0062]
【表8】 [Table 8]
【0063】[0063]
【表9】 [Table 9]
【0064】[0064]
【表10】 [Table 10]
【0065】[0065]
【表11】 [Table 11]
【0066】[0066]
【表12】 [Table 12]
【0067】[0067]
【表13】 [Table 13]
【0068】[0068]
【発明の効果】本発明の発泡性無機質組成物の構成は上
述の通りであり、気泡の均一性、耐水性に優れ、加熱に
よる収縮率が小さく、断熱性の高い、高強度で低比重の
発泡体を得ることができる。The composition of the foamable inorganic composition of the present invention is as described above, and it has excellent cell uniformity and water resistance, a small shrinkage factor due to heating, high heat insulation, high strength and low specific gravity. A foam can be obtained.
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 //(C04B 28/26 18:08 B 22:04 16:06 Z 24:04) 111:40 (72)発明者 新田 勝三 京都市南区上鳥羽上調子町2−2 積水化 学工業株式会社内 (72)発明者 神谷 昌岳 京都市南区上鳥羽上調子町2−2 積水化 学工業株式会社内 (72)発明者 中野 龍俊 京都市南区上鳥羽上調子町2−2 積水化 学工業株式会社内 (72)発明者 小幡 貞宏 京都市南区上鳥羽上調子町2−2 積水化 学工業株式会社内 (72)発明者 田中 喜博 京都市南区上鳥羽上調子町2−2 積水化 学工業株式会社内─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI Technical display area // (C04B 28/26 18:08 B 22:04 16:06 Z 24:04) 111: 40 (72) Inventor Katsuzo Nitta 2-2, Kamitobaue-chokocho, Minami-ku, Kyoto, Sekisui Kagaku Kogyo Co., Ltd. (72) Inventor, Masatake Kamiya 2-2, Kamitobaue-chokocho, Minami-ku, Kyoto City Industrial Co., Ltd. (72) Inventor Tatsutoshi Nakano 2-2, Kamitoriba-chomocho, Minami-ku, Kyoto City Sekisui Kagaku Kogyo Co., Ltd. (72) Inventor, Sadahiro Obata 2-Kamitoba-chocho, Minami-ku, Kyoto 2 Sekisui Kagaku Kogyo Co., Ltd. (72) Inventor Yoshihiro Tanaka 2-2, Kamitobaue-chokocho, Minami-ku, Kyoto City Sekisui Kagaku Kogyo Co., Ltd.
Claims (1)
10μm以下であるものを80重量%以上含有する粉
体、400〜1,000℃で焼成したフライアッシュ
のうち、粒径が10μm以下であるものを80重量%以
上含有する粉体、フライアッシュを溶融し、気体中に
噴霧することによって得られる粉体、フライアッシュ
に0.1〜30kwh/kgの機械的エネルギーを作用
させて得られる粉体、フライアッシュに0.1〜30
kwh/kgの機械的エネルギーを作用させて得られる
粉体を、更に100〜750℃に加熱して得られる粉
体、粘土を溶融し、気体中に噴霧することによって得
られる粉体、粘土に0.1〜30kwh/kgの機械
的エネルギーを作用させて得られる粉体、粘土に0.
1〜30kwh/kgの機械的エネルギーを作用させて
得られる粉体を、更に100〜750℃に加熱して得ら
れる粉体、カオリン鉱物を500〜900℃で加熱脱
水して得られる粉体、メタカオリンに0.1〜30kw
h/kgの機械的エネルギーを作用させて得られる粉
体、よりなる群から選ばれる少なくとも1種以上の反応
性無機質粉体100重量部、(B)アルカリ金属珪酸塩
0.2〜450重量部、(C)金属粉末0.01〜5重
量部、(D)水35〜1,500重量部とからなる発泡
性無機質組成物。1. (A) A powder containing 80% by weight or more of fly ash having a particle size of 10 μm or less, and a fly ash fired at 400 to 1,000 ° C. having a particle size of 10 μm or less. Of 80% by weight or more, powder obtained by melting fly ash and spraying in gas, obtained by applying mechanical energy of 0.1 to 30 kwh / kg to fly ash. Powder, fly ash 0.1 to 30
Powder obtained by applying mechanical energy of kwh / kg to powder obtained by further heating at 100 to 750 ° C., clay melted and sprayed in gas Powder and clay obtained by applying mechanical energy of 0.1 to 30 kwh / kg to the clay.
A powder obtained by heating mechanical power of 1 to 30 kwh / kg to 100 to 750 ° C., a powder obtained by heating and dehydrating kaolin mineral at 500 to 900 ° C., 0.1 to 30 kW for metakaolin
100 parts by weight of at least one reactive inorganic powder selected from the group consisting of powder obtained by applying mechanical energy of h / kg, (B) 0.2 to 450 parts by weight of alkali metal silicate , (C) 0.01 to 5 parts by weight of metal powder, and (D) 35 to 1,500 parts by weight of water, a foamable inorganic composition.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP21361294A JPH07232973A (en) | 1993-10-22 | 1994-09-07 | Foaming inorganic composition |
Applications Claiming Priority (5)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP5-322913 | 1993-10-22 | ||
| JP5-264876 | 1993-10-22 | ||
| JP26487693 | 1993-10-22 | ||
| JP32291393 | 1993-12-21 | ||
| JP21361294A JPH07232973A (en) | 1993-10-22 | 1994-09-07 | Foaming inorganic composition |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH07232973A true JPH07232973A (en) | 1995-09-05 |
Family
ID=27329521
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP21361294A Pending JPH07232973A (en) | 1993-10-22 | 1994-09-07 | Foaming inorganic composition |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH07232973A (en) |
-
1994
- 1994-09-07 JP JP21361294A patent/JPH07232973A/en active Pending
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