JPH0583294B2 - - Google Patents
Info
- Publication number
- JPH0583294B2 JPH0583294B2 JP28668588A JP28668588A JPH0583294B2 JP H0583294 B2 JPH0583294 B2 JP H0583294B2 JP 28668588 A JP28668588 A JP 28668588A JP 28668588 A JP28668588 A JP 28668588A JP H0583294 B2 JPH0583294 B2 JP H0583294B2
- Authority
- JP
- Japan
- Prior art keywords
- particle size
- blades
- speed rotary
- speed
- pellets
- 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.)
- Expired - Lifetime
Links
- 239000002245 particle Substances 0.000 claims description 17
- 238000000034 method Methods 0.000 claims description 11
- 238000004513 sizing Methods 0.000 claims description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims description 6
- 239000004927 clay Substances 0.000 claims description 6
- 239000000203 mixture Substances 0.000 claims description 6
- 239000000843 powder Substances 0.000 claims description 5
- 238000004898 kneading Methods 0.000 claims description 4
- 239000010433 feldspar Substances 0.000 claims description 3
- 239000010881 fly ash Substances 0.000 claims description 3
- 239000000377 silicon dioxide Substances 0.000 claims description 3
- 239000000049 pigment Substances 0.000 claims description 2
- 239000008188 pellet Substances 0.000 description 12
- 238000001035 drying Methods 0.000 description 7
- 239000002994 raw material Substances 0.000 description 7
- 238000005469 granulation Methods 0.000 description 6
- 230000003179 granulation Effects 0.000 description 6
- 239000008187 granular material Substances 0.000 description 5
- 238000001125 extrusion Methods 0.000 description 4
- 230000000052 comparative effect Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000010419 fine particle Substances 0.000 description 2
- 239000000446 fuel Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000007873 sieving Methods 0.000 description 2
- 235000010724 Wisteria floribunda Nutrition 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000011156 evaluation Methods 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000004575 stone Substances 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C04—CEMENTS; CONCRETE; ARTIFICIAL STONE; CERAMICS; REFRACTORIES
- C04B—LIME, MAGNESIA; SLAG; CEMENTS; COMPOSITIONS THEREOF, e.g. MORTARS, CONCRETE OR LIKE BUILDING MATERIALS; ARTIFICIAL STONE; CERAMICS; REFRACTORIES; TREATMENT OF NATURAL STONE
- C04B18/00—Use 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
- C04B18/02—Agglomerated materials, e.g. artificial aggregates
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Civil Engineering (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Glanulating (AREA)
Description
(産業上の利用分野)
本発明は着色骨材の造粒方法に関するものであ
る。
(従来の技術及び発明が解決しようとする課題)
粘土、長石微粉、珪石微粉、フライアツシユ等
を原料として4mmφ以下の平均粒度を有する小ペ
レツトを造粒整粒する場合の造粒評価指標は平均
粒度、粒度範囲及び強度である。また強度は低水
分造粒が有利となる。その適正水分値は原料の種
類、粒度、造粒整粒機の種類によつて左右される
が通常非常に狭い水分範囲となる。
粘土のように極微粒を含む原料を狭い粒度範囲
のペレツトに造粒整粒し、しかもその平均粒度が
4mmφ以下というような小さい粒度を得ようとす
る場合、従来の技術では適正水分値が高いため、
例えばパン型又はドラム型ペレタイザーを用いる
場合にハンドリングに耐える強度のペレツトを製
造することは非常に難しい。
従つて、平均粒度が4mmφ以下のペレツトを製
造する場合には、原料混合物を例えば押出し成形
機に掛けた後、その成形物を或る程度乾燥して適
正水分範囲の狭い高速回転整粒機に掛けるなどの
方法に頼らざるを得なかつた。
しかしながら、この場合乾燥工程が入る上に押
出し成形機の特性上生産能率が悪くコスト高にな
るという難点があつた。
(課題を解決するための手段)
本発明者等は鋭意研究した結果、従来主として
ミキサーとして使われていた羽根付高速回転混練
機、例えばアイリツヒミキサー(西独アイリツヒ
社製)、レーデイゲミキサー(西独レーデイゲ社
製)等を混合混練予備造粒機として用いることに
よつて、造粒時の水分を10〜18%と大幅に下げる
ことができ、このため高速回転整粒機の適正水分
域とマツチさせることが可能になり、従つて中間
の乾燥工程を不要ならしめ、低超コストにて造粒
整粒することが出来るようになり、前記した従来
技術の問題点を解決しうることを確かめた。
すなわち、本発明の要旨とするところは、粘
土、長石微粉、珪石微粉、フライアツシユの1種
もしくは2種以上と顔料との混合物を水分10〜18
%に調整し、該混合物を羽根付高速回転混練機を
用いて予備造粒し、得られた予備造粒物を次いで
高速回転整粒機を用いて整粒することを特徴とす
る平均粒度4mmφ以下の着色骨材の造粒方法にあ
る。
前記の羽根付高速回転混練機は他の造粒機と比
し適正水分範囲が広いことを特徴とする。従つ
て、この羽根付高速回転混練機による混合混練予
備造粒工程に続いて、高速回転整粒機、例えばマ
ルメライザー(不二パウダル社製)による整粒工
程を組み合わせることにより、原料配合及び原料
粒度の変化により高速回転整粒機の適正水分が変
化してもこれに充分対応し、乾燥なしに低コスト
かつ高能率で狭い粒度範囲の小ペレツト、例えば
4mmφ以下の小ペレツトの造粒が可能となる。
以下、本発明を実施例に基づいて説明する。
(実施例)
第1表に本発明の実施例を比較例と共に示す。
比較例は、従来の粘土用押出し成形機による成
形工程→乾燥工程→高速回転整粒機による整粒工
程からなるプロセスによるもので、押出し成形時
の水分は25%程度にする必要がありその後で乾燥
させるため、製造コストは電力原単位80KwH/
T、乾燥燃料原単位75×103kcal/Tとコスト高
である。
本発明例1及び2は、原料を羽根付き高速回転
混練機で事前混合混練予備造粒した後、高速回転
整粒機による整粒工程を行つたもので、羽根付き
高速回転混練機にかける際の原料混合物の水分を
18%及び15.3%と大幅に低下せしめることが出来
たので、高速回転整粒機の適正水分域とマツチさ
せる事が出来るようになり、中間の乾燥工程が不
要となり、電力原単位40KwH/T、乾燥燃料原
単位0と低コストにて造粒整粒することが可能に
なつた。
従つて予備造粒後、次工程の高速回転整粒機に
かけ第1表のような圧密化された高強度の小ペレ
ツトを低コストにて造粒整粒することができた。
(Industrial Application Field) The present invention relates to a method for granulating colored aggregate. (Prior art and problems to be solved by the invention) When granulating small pellets having an average particle size of 4 mmφ or less using clay, feldspar fine powder, silica fine powder, fly ash, etc. as raw materials, the granulation evaluation index is the average particle size. , particle size range and strength. In addition, low moisture granulation is advantageous for strength. The appropriate moisture value depends on the type of raw material, particle size, and type of granulator, but usually falls within a very narrow moisture range. When attempting to granulate a raw material containing extremely fine particles such as clay into pellets with a narrow particle size range, and to obtain a small particle size with an average particle size of 4 mmφ or less, conventional technology requires a high appropriate moisture value. For,
For example, when using a pan or drum type pelletizer, it is very difficult to produce pellets strong enough to withstand handling. Therefore, when producing pellets with an average particle size of 4 mmφ or less, the raw material mixture is passed through an extrusion molding machine, the molded product is dried to some extent, and then passed through a high-speed rotary sieving machine with a narrow appropriate moisture range. They had no choice but to resort to methods such as hanging them. However, in this case, there were disadvantages in that a drying step was required and production efficiency was low due to the characteristics of the extrusion molding machine, resulting in high costs. (Means for Solving the Problems) As a result of intensive research, the present inventors have found that high-speed rotary kneading machines with blades, which have conventionally been mainly used as mixers, such as the Eiritzch mixer (manufactured by Eiritzg AG, West Germany), the Lödeige mixer ( By using a mixing, kneading, and pre-granulating machine such as a granulator (manufactured by West German Lödeige), the moisture content during granulation can be significantly lowered to 10 to 18%, which is within the appropriate moisture range of a high-speed rotating granulator. It has been confirmed that the problems of the conventional technology described above can be solved by making it possible to match the grains, thereby eliminating the need for an intermediate drying process, and making it possible to granulate and size particles at a very low cost. Ta. That is, the gist of the present invention is to prepare a mixture of one or more of clay, fine feldspar powder, fine silica stone, and fly ash with a pigment at a moisture content of 10 to 18%.
%, the mixture is pre-granulated using a high-speed rotary kneader with blades, and the obtained pre-granulated product is then sized using a high-speed rotary sizing machine.The average particle size is 4 mmφ. The following is a method for granulating colored aggregate. The above-described high-speed rotary kneader with blades is characterized by a wider range of appropriate moisture content than other granulators. Therefore, by combining the mixing, kneading and preliminary granulation process using this high-speed rotating kneader with blades, and the sizing process using a high-speed rotating granulator, such as Marumerizer (manufactured by Fuji Paudal Co., Ltd.), it is possible to Even if the appropriate moisture content of the high-speed rotation sizing machine changes due to changes in particle size, it can be fully accommodated, and it is possible to granulate small pellets in a narrow particle size range, for example, small pellets of 4 mmφ or less, without drying, at low cost and with high efficiency. becomes. Hereinafter, the present invention will be explained based on examples. (Examples) Table 1 shows examples of the present invention together with comparative examples. The comparative example uses a process consisting of a molding process using a conventional clay extrusion machine → drying process → sizing process using a high-speed rotation sizing machine.The moisture content during extrusion molding must be about 25%, and then Due to drying, the manufacturing cost is 80KwH per unit of electricity.
The dry fuel consumption rate is 75×10 3 kcal/T, which is high cost. In Examples 1 and 2 of the present invention, the raw materials were pre-mixed, kneaded and pre-granulated using a high-speed rotary kneader with blades, and then subjected to a sizing process using a high-speed rotary sieve. The moisture content of the raw material mixture
Since we were able to significantly reduce the moisture content to 18% and 15.3%, we were able to match the appropriate moisture range of the high-speed rotary sieving machine, eliminating the need for an intermediate drying process, and reducing the power consumption by 40KwH/T. It has become possible to perform granulation and sizing at low cost with a dry fuel consumption of 0. Therefore, after preliminary granulation, it was possible to granulate compacted high-strength small pellets as shown in Table 1 at a low cost by passing the pellets through a high-speed rotary granulating machine in the next step.
【表】
(発明の効果)
本発明によれば、粘土のように極微粒を含む原
料を狭い粒度範囲のペレツトに造粒整粒し、しか
もその平均粒度が4mmφ以下というような小さい
粒度のペレツトを得ようとする場合に、乾燥工程
なしに低コストかつ高能率で狭い粒度範囲の小ペ
レツトを造粒、整粒することが出来るので、産業
上裨益するところが極めて大である。[Table] (Effects of the Invention) According to the present invention, a raw material containing extremely fine particles such as clay is granulated into pellets with a narrow particle size range, and the pellets have a small particle size with an average particle size of 4 mmφ or less. When trying to obtain pellets, it is possible to granulate and size small pellets in a narrow particle size range at low cost and with high efficiency without a drying process, so it is of great industrial benefit.
Claims (1)
の1種もしくは2種以上と顔料との混合物を水分
10〜18%に調整し、該混合物を羽根付高速回転混
練機を用いて予備造粒し、得られた予備造粒物を
次いで高速回転整粒機を用いて整粒することを特
徴とする平均粒度4mmφ以下の着色骨材の造粒方
法。 2 羽根付高速回転混練機としてアイリツヒミキ
サーまたはレーデイゲミキサーを用い、高速回転
整粒機として球形整粒機を用いることを特徴とす
る請求項1記載の着色骨材の造粒方法。[Scope of Claims] 1. A mixture of one or more of clay, feldspar fine powder, silica fine powder, and fly ash and a pigment is hydrated.
10 to 18%, the mixture is pre-granulated using a high-speed rotating kneader with blades, and the obtained pre-granulated product is then sized using a high-speed rotating sizing machine. A method for granulating colored aggregate with an average particle size of 4 mmφ or less. 2. The method for granulating colored aggregate according to claim 1, characterized in that an Eirich mixer or a Lodeige mixer is used as the high-speed rotary kneading machine with blades, and a spherical granulator is used as the high-speed rotary granulator.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28668588A JPH02133344A (en) | 1988-11-15 | 1988-11-15 | Method for granulating colored aggregate |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP28668588A JPH02133344A (en) | 1988-11-15 | 1988-11-15 | Method for granulating colored aggregate |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02133344A JPH02133344A (en) | 1990-05-22 |
JPH0583294B2 true JPH0583294B2 (en) | 1993-11-25 |
Family
ID=17707647
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP28668588A Granted JPH02133344A (en) | 1988-11-15 | 1988-11-15 | Method for granulating colored aggregate |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH02133344A (en) |
-
1988
- 1988-11-15 JP JP28668588A patent/JPH02133344A/en active Granted
Also Published As
Publication number | Publication date |
---|---|
JPH02133344A (en) | 1990-05-22 |
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