JPH04200739A - Production of fine ceramic balloon - Google Patents
Production of fine ceramic balloonInfo
- Publication number
- JPH04200739A JPH04200739A JP33921290A JP33921290A JPH04200739A JP H04200739 A JPH04200739 A JP H04200739A JP 33921290 A JP33921290 A JP 33921290A JP 33921290 A JP33921290 A JP 33921290A JP H04200739 A JPH04200739 A JP H04200739A
- Authority
- JP
- Japan
- Prior art keywords
- granules
- fine
- particle size
- product
- predetermined particle
- 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.)
- Granted
Links
- 239000000919 ceramic Substances 0.000 title claims abstract description 16
- 238000004519 manufacturing process Methods 0.000 title claims description 13
- 239000008187 granular material Substances 0.000 claims abstract description 32
- 239000002245 particle Substances 0.000 claims abstract description 28
- 239000002994 raw material Substances 0.000 claims abstract description 16
- 239000000463 material Substances 0.000 claims abstract description 13
- 239000000843 powder Substances 0.000 claims abstract description 9
- 229910052500 inorganic mineral Inorganic materials 0.000 claims abstract description 7
- 239000011707 mineral Substances 0.000 claims abstract description 7
- 239000011230 binding agent Substances 0.000 claims abstract description 6
- 239000010419 fine particle Substances 0.000 claims description 11
- 238000010304 firing Methods 0.000 claims description 7
- 238000005187 foaming Methods 0.000 claims description 7
- 238000001035 drying Methods 0.000 claims description 3
- 238000005469 granulation Methods 0.000 claims description 3
- 230000003179 granulation Effects 0.000 claims description 3
- 238000003756 stirring Methods 0.000 claims description 3
- 238000007873 sieving Methods 0.000 claims description 2
- 239000006260 foam Substances 0.000 abstract description 4
- 239000000203 mixture Substances 0.000 abstract 1
- 238000012216 screening Methods 0.000 abstract 1
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 12
- 238000000034 method Methods 0.000 description 7
- 241000975357 Salangichthys microdon Species 0.000 description 3
- 239000004568 cement Substances 0.000 description 3
- 239000004570 mortar (masonry) Substances 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 239000007864 aqueous solution Substances 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- BVKZGUZCCUSVTD-UHFFFAOYSA-N carbonic acid Chemical compound OC(O)=O BVKZGUZCCUSVTD-UHFFFAOYSA-N 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 230000006835 compression Effects 0.000 description 1
- 238000010276 construction Methods 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- -1 flintstone Substances 0.000 description 1
- 238000010438 heat treatment Methods 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000005306 natural glass Substances 0.000 description 1
- 239000010451 perlite Substances 0.000 description 1
- 235000019362 perlite Nutrition 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000010008 shearing Methods 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
Landscapes
- Glanulating (AREA)
- Manufacturing Of Micro-Capsules (AREA)
Abstract
Description
【発明の詳細な説明】
(産業上の利用分野〕
本発明は、例えば押出し成形やプレス成形により加工さ
れる薄肉厚のセメント、モルタル等の建築用軽量骨材に
使用できる細粒セラミックバルーンの製造方法に関する
。Detailed Description of the Invention (Industrial Field of Application) The present invention is directed to the production of fine-grained ceramic balloons that can be used as lightweight construction aggregates such as thin-walled cement and mortar processed by extrusion molding or press molding, for example. Regarding the method.
従来から、セメント、モルタル等においては砂の代わり
に軽量骨材が使用されているが、薄肉厚のセメント、モ
ルタル用骨材には加工上及び性能上の制約より、細粒の
軽量骨材が要求される。ところが、従来の製造方法では
製造される造粒物の粒度幅が広く、特に細粒のものが少
なかった。このため焼成発泡品を改めて篩分け、細粒の
ものだけを使用していた。Traditionally, lightweight aggregates have been used instead of sand in cement, mortar, etc., but due to processing and performance constraints, fine-grained lightweight aggregates have been used as aggregates for thin-walled cement and mortar. required. However, in the conventional production method, the particle size range of the produced granules was wide, and there were particularly few fine particles. For this reason, fired foam products were sieved again and only fine-grained products were used.
〔発明が解決しようとするI1題〕
しかしながら、上記方法では細粒の歩留りが低くコスト
高になるという問題点があった。[Problem I1 to be solved by the invention] However, the above method has a problem in that the yield of fine particles is low and the cost is high.
本発明はこのような事情に鑑みてなされたもので、比較
的大量に存在する天然ガラス賞鉱物及び/または人工の
ガラス質素材を原料とし、細粒の軽量骨材を製造できる
細粒セラミックバルーンの製造方法を提供することを目
的とする。The present invention was made in view of the above circumstances, and provides a fine-grained ceramic balloon that can produce fine-grained lightweight aggregate using natural glass minerals and/or artificial glassy materials that exist in relatively large amounts as raw materials. The purpose is to provide a manufacturing method for.
上記目的に沿う請求項第1項記載の細粒セラミックバル
ーンの製造方法は、原料である微粉砕した天然ガラス質
鉱物及び/または人工のガラス質素材にバインダーを加
えて造粒し、次に乾燥して乾燥造粒物を造り、しかる後
練乾燥造粒物を篩分けして所定の粒度範囲の乾燥造粒物
を焼成発泡すると共に、該篩上産物をクラッシャで破砕
した後、該破砕物を篩分けあるいは分級して所定粒度以
下の微粉物を除いた破砕物を上記乾燥造粒物と共に焼成
発泡して構成されている。The method for manufacturing a fine-grained ceramic balloon according to claim 1, which meets the above object, involves adding a binder to finely ground natural vitreous minerals and/or artificial vitreous materials as raw materials, granulating them, and then drying them. The dried granules are then kneaded, the dried granules are sieved, and the dried granules in a predetermined particle size range are fired and foamed.The sieved product is crushed with a crusher, and then the crushed It is constructed by sifting or classifying the powder to remove fine particles with a predetermined particle size or less, and firing and foaming the crushed product together with the dried granules.
また、請求項第2項記載の細粒セラミックバルーンの製
造方法は、請求項第1項記載の方法において、造粒は内
部に攪拌羽根を有し底面が可撓性素材からなる揺動型ミ
キサーによって行うようにして構成されている。Further, the method for producing a fine-grained ceramic balloon according to claim 2 is the method according to claim 1, in which the granulation is carried out using an oscillating type mixer having stirring blades inside and having a bottom surface made of a flexible material. It is configured to perform the following.
そして、請求項第3項記載の細粒セラミックバルーンの
製造方法は、請求項第1項記載または第2項記載の細粒
セラミックバルーンの製造方法において、篩上産物は略
11オーバーの乾燥造粒物であって、微粉物は略0.L
++−以下であるようにして構成されている。The method for producing a fine ceramic balloon according to claim 3 is the method for producing a fine ceramic balloon according to claim 1 or 2, in which the sieved product is dried and granulated with approximately 11 over The fine powder is approximately 0. L
++- or less.
請求項第1項〜第3項記載の細粒セラミックバルーンの
製造方法は、原料である微粉砕した天然ガラス質鉱物及
び/またはあるいは人工のガラス質素材にバインダーを
加え、造粒し、乾燥して乾燥造粒物を造り、該乾燥造粒
物を篩分けして所定の粒度範囲の乾燥造粒物を焼成発泡
しているが、所定の粒度を越える篩上分については、ク
ラッシャで破砕して分級し、所定粒変分を上記乾燥造粒
物と一緒に焼成発泡している。The method for producing a fine-grained ceramic balloon according to claims 1 to 3 includes adding a binder to finely pulverized natural vitreous minerals and/or artificial vitreous materials as raw materials, granulating them, and drying them. The dry granules are made by sieving, and the dry granules within a predetermined particle size range are fired and foamed. However, the portion of the sieve that exceeds the predetermined particle size is crushed with a crusher. Then, a predetermined particle size is fired and foamed together with the dried granules.
従って、破砕された造粒物は多少の角を有するが、焼成
発泡の過程で軟化し表面張力によって角が取れて丸くな
り、造粒物と略同様の性状を有す〔実施例〕
続いて、本発明を具体化した実施例につき説明し、本発
明の理解に供する。Therefore, although the crushed granules have some edges, they soften during the firing and foaming process and become rounded due to surface tension, and have substantially the same properties as the granules [Example] , Examples embodying the present invention will be explained to provide an understanding of the present invention.
まず、原料である天然ガラス質鉱物の一例であるシラス
の成分を第1表に示し、使用したシラスの粒度分布を第
2表に示す。First, Table 1 shows the components of shirasu, which is an example of a natural glassy mineral that is a raw material, and Table 2 shows the particle size distribution of the shirasu used.
第 1 表 数字は重量%
なお、第1表においてIg、 1ossは結晶水が主成
分である。Table 1 Numbers are weight %. In Table 1, Ig and 1oss are mainly composed of water of crystallization.
第2表
上記シラスの原料において大粒の物を含むとその後の処
理に支障を生ずるので、篩に通し44μm以下の微粉を
原料として使用する。Table 2 If the raw material for the whitebait above contains large particles, it will cause problems in subsequent processing, so fine powder of 44 μm or less is passed through a sieve and used as the raw material.
次に、このシラスの微粉を内部に攪拌羽根を有し底面が
可撓性素材からなる揺動型ミキサー(商品名、オムニミ
キサー)にいれ、バインダーの一例である水酸化ナトリ
ウム水溶液を投入する。この水酸化ナトリウム水溶液は
、Mail(純分の添加量が外割りでシラス微粉の9〜
11重量%の範囲になるようにして添加すると、細粒物
の造粒歩留りが向上する。Next, this whitebait fine powder is placed in a rocking mixer (trade name, Omnimixer) having internal stirring blades and a bottom made of a flexible material, and an aqueous sodium hydroxide solution, which is an example of a binder, is added thereto. This aqueous sodium hydroxide solution was prepared by mail (the amount of pure content added was 9 to 90% of the whitebait fine powder based on the outer division).
When added in a range of 11% by weight, the granulation yield of fine granules is improved.
これによって、種々の粒度の細粒が造られるがこの後造
粒物を乾燥し、篩分けした場合の粒度分布は第3表の通
りであった。As a result, fine granules of various particle sizes were produced, and when the granules were then dried and sieved, the particle size distribution was as shown in Table 3.
第3表
ここで1.0■−以上の粒度の物は、そのまま発泡焼成
すると、製品の粒径が大きくなるので、−旦クラッシャ
で破砕して粒径を小さくし、再度篩分する。そして、粒
径が0.1mm以下の物は、再度原料として還元する。Table 3: If the product has a particle size of 1.0 cm or more, if it is foamed and fired as it is, the particle size of the product will become large, so it is first crushed with a crusher to reduce the particle size and then sieved again. Then, particles with a particle size of 0.1 mm or less are reduced as raw materials again.
ここで、クランシャに圧縮によって原料を破砕するロー
ルクラッシャ(A)、衝撃によって原料を破砕するハン
マークランシャ(B)、剪断によって原料を破砕するブ
ラウンミル(C)を使用して破砕した場合に、破砕物の
粒度について第4表に示す。Here, when crushing is performed using a roll crusher (A) that crushes the raw material by compression, a hammer crusher (B) that crushes the raw material by impact, and a brown mill (C) that crushes the raw material by shearing, Table 4 shows the particle size of the crushed material.
第 4 表
第4表から分かるように、原料を11以下の細粒に破砕
する場合には、ロールクランシャを使用するのが好まし
い。Table 4 As can be seen from Table 4, when crushing the raw material into fine particles of 11 or less, it is preferable to use a roll crusher.
ここで、破砕された細粒と、造粒されたままの細粒とを
別々に以下に説明する工程を経て焼成発泡してその性状
を比較したものを第5表に示すが、破砕品であっても造
粒品とは遜色なく使用できることが分かる。更には、出
来た製品を拡大して調べると、破砕によって生じる角は
、焼成発泡の過程で無くなり、全体として丸みを有する
細粒となっていた。Here, Table 5 shows a comparison of the properties of crushed fine grains and as-granulated fine grains after firing and foaming them through the steps described below. It can be seen that even if it is present, it can be used with no inferiority to the granulated product. Furthermore, when the finished product was examined under magnification, it was found that the corners caused by crushing disappeared during the firing and foaming process, and the product became fine particles with roundness as a whole.
第 5 表
ここで、吸水率とはJISA1109細骨材の吸水率試
験方法によって行い、強度は本屋式硬度計を使用して2
0点の平均の圧潰強度をいう。Table 5 Here, the water absorption rate is measured according to the JISA1109 fine aggregate water absorption test method, and the strength is measured using a Honya type hardness tester.
This refers to the average crushing strength at 0 points.
従って、以上の工程を経て製造された破砕された細粒を
前記造粒された細粒に混合してジャイロシフターによっ
て篩分ける。Therefore, the crushed fine particles produced through the above steps are mixed with the granulated fine particles and sieved by a gyro sifter.
この後、必要な粒度の細粒を選択し、高融点の微粉を細
粒に塗布する。この操作は、上記オムニミキサーによっ
て行う。After this, fine grains of the required particle size are selected and a high melting point fine powder is applied to the fine grains. This operation is performed using the omnimixer described above.
次に、これらの乾燥物を焼成発泡を行うが、これは竪型
炉によって行う。この竪型炉は下部にバーナーを有し、
熱風を発生させ上部の排気筒から外部に排気されるが、
上記細粒の乾燥物を上部から投入し、該熱風によって8
50〜950°Cに加熱することによって行う、これに
よって内部のガラス質が軟化すると共に、シラス細粒が
発泡して直径が20%程度増加し、細粒のセラミックバ
ルーンが製造される。Next, these dried products are fired and foamed using a vertical furnace. This vertical furnace has a burner at the bottom,
It generates hot air and exhausts it to the outside from the upper exhaust stack,
The above dried fine particles are put in from the top, and the hot air
This is done by heating to 50-950°C, which softens the glass inside and causes the fine shirasu particles to foam and increase in diameter by about 20%, producing a fine-grained ceramic balloon.
これによって、比較的粒径の小さい、強度を有するシラ
スバルーンを低い温度で製造でき、更には粒度の大きい
造粒品をクラッシャによって破砕して細粒とするので、
歩留りが向上することになる。As a result, strong glass balloons with relatively small particle sizes can be produced at low temperatures, and granulated products with large particle sizes can be crushed into fine particles using a crusher.
Yield will be improved.
上記実施例においては、天然ガラス質鉱物としてシラス
を使用したが、抗火石、真珠岩、火山質流紋岩等であっ
ても本発明は通用される。In the above embodiments, shirasu was used as the natural glassy mineral, but the present invention can also be applied to other materials such as flintstone, perlite, and volcanic rhyolite.
次に、0.44μm以下に粉砕された人工のガラス質素
材を原料とし、これにバインダーの一例である水酸化ナ
トリウム水溶液を水酸化ナトリウム純分が外割りで上記
原料の約11%程度、炭酸カルシウムを外割りで上記原
料の約3%程度混入して、充分に攪拌し上記揺動型ミキ
サーを使用して上記実施例と同様な処理を行ってセラミ
ックバルーンを製造した。その性状を第6表に示す。Next, an artificial glassy material crushed to 0.44 μm or less is used as a raw material, and a sodium hydroxide aqueous solution, which is an example of a binder, is added to it, with a pure sodium hydroxide content of about 11% of the above raw material, and carbonic acid. Approximately 3% of the above raw material was mixed with calcium, thoroughly stirred, and treated in the same manner as in the above example using the above-mentioned oscillating mixer to produce a ceramic balloon. Its properties are shown in Table 6.
第 6 表
〔発明の効果〕
本発明に係る細粒セラミックバルーンの製造方法は以上
の説明からも明らかなように、造粒した細粒の内、粒径
の大きいものを焼成発泡する前にクラッシャによって適
当粒度に破砕しているので、製品の歩留りを向上させる
ことができる。Table 6 [Effects of the Invention] As is clear from the above explanation, the method for manufacturing a fine-grained ceramic balloon according to the present invention is performed by crushing the granulated fine particles with a large particle size before firing and foaming them. Since the powder is crushed to an appropriate particle size, the yield of the product can be improved.
そして、破砕した後に、焼成発泡させているので、角が
取れて丸みのある微粒セラミックノマル−ンとなり、造
粒品と遜色のない製品を製造することができる。Then, after crushing, firing and foaming are performed, so that a fine ceramic normal grain with rounded corners is obtained, and a product comparable to a granulated product can be manufactured.
代理人 弁理士 中前冨士男Agent: Patent Attorney: Fujio Nakamae
Claims (3)
たは人工のガラス質素材にバインダーを加えて造粒し、
次に乾燥して乾燥造粒物を造り、しかる後該乾燥造粒物
を篩分けして所定の粒度範囲の乾燥造粒物を焼成発泡す
ると共に、該篩上産物をクラッシャで破砕した後、該破
砕物を篩分けあるいは分級して所定粒度以下の微粉物を
除いた破砕物を上記乾燥造粒物と共に焼成発泡したこと
を特徴とする細粒セラミックバルーンの製造方法。(1) Add a binder to finely ground natural glassy minerals and/or artificial glassy materials as raw materials and granulate them,
Next, drying to produce a dry granule, then sieving the dry granule, firing and foaming the dry granule having a predetermined particle size range, and crushing the sieved product with a crusher, A method for producing a fine-grained ceramic balloon, characterized in that the crushed material is sieved or classified to remove fine particles of a predetermined particle size or less, and the crushed material is fired and foamed together with the dried granules.
らなる揺動型ミキサーによって行う請求項第1項記載の
細粒セラミックバルーンの製造方法。(2) The method for producing a fine-grained ceramic balloon according to claim 1, wherein the granulation is carried out using an oscillating mixer having internal stirring blades and a bottom made of a flexible material.
て、微粉物は略0.1mm以下である請求項第1項また
は第2項記載の細粒セラミックバルーンの製造方法。(3) The method for producing a fine-grained ceramic balloon according to claim 1 or 2, wherein the sieved product is a dry granulated product with a size of about 1 mm or less, and the fine powder is a dry granule with a size of about 0.1 mm or less.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP33921290A JP2518737B2 (en) | 1990-11-30 | 1990-11-30 | Fine-grained ceramic balloon manufacturing method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP33921290A JP2518737B2 (en) | 1990-11-30 | 1990-11-30 | Fine-grained ceramic balloon manufacturing method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPH04200739A true JPH04200739A (en) | 1992-07-21 |
| JP2518737B2 JP2518737B2 (en) | 1996-07-31 |
Family
ID=18325308
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP33921290A Expired - Lifetime JP2518737B2 (en) | 1990-11-30 | 1990-11-30 | Fine-grained ceramic balloon manufacturing method |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JP2518737B2 (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB2423738A (en) * | 2005-03-02 | 2006-09-06 | Univ Sheffield | Wet granulation process |
| US7431912B2 (en) * | 2004-03-22 | 2008-10-07 | Yazaki Corporation | Producing method for zirconia hollow particles |
-
1990
- 1990-11-30 JP JP33921290A patent/JP2518737B2/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7431912B2 (en) * | 2004-03-22 | 2008-10-07 | Yazaki Corporation | Producing method for zirconia hollow particles |
| GB2423738A (en) * | 2005-03-02 | 2006-09-06 | Univ Sheffield | Wet granulation process |
Also Published As
| Publication number | Publication date |
|---|---|
| JP2518737B2 (en) | 1996-07-31 |
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