JPH11263658A - Production of granurated material containing coal ash - Google Patents
Production of granurated material containing coal ashInfo
- Publication number
- JPH11263658A JPH11263658A JP6598398A JP6598398A JPH11263658A JP H11263658 A JPH11263658 A JP H11263658A JP 6598398 A JP6598398 A JP 6598398A JP 6598398 A JP6598398 A JP 6598398A JP H11263658 A JPH11263658 A JP H11263658A
- Authority
- JP
- Japan
- Prior art keywords
- coal ash
- cement
- weight
- parts
- raw material
- 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
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
- C04B18/021—Agglomerated materials, e.g. artificial aggregates agglomerated by a mineral binder, e.g. cement
-
- 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
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Civil Engineering (AREA)
- Ceramic Engineering (AREA)
- Materials Engineering (AREA)
- Structural Engineering (AREA)
- Organic Chemistry (AREA)
- Curing Cements, Concrete, And Artificial Stone (AREA)
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は石炭灰を含む造粒物
の製造方法に関する。さらに詳しくは、土木材料、建築
材料等として利用できる石炭灰含有造粒物の製造方法に
関する。The present invention relates to a method for producing a granulated material containing coal ash. More specifically, the present invention relates to a method for producing a coal ash-containing granule that can be used as a civil engineering material, a building material, and the like.
【0002】[0002]
【従来の技術】石炭火力発電所から大量に発生する石炭
灰を有効利用するために、土木材料等として利用される
造粒物を、石炭灰を原料として人工的に製造する方法が
提案されている。特開昭61−151052号公報に
は、石炭灰にセメントおよび水を加えて、高速混合造粒
して石炭灰砂を製造する方法が開示されている。同様に
特開昭63−201045号公報には、石炭灰とスラグ
粉末にセメントおよび水を加え、高速混合造粒して石炭
灰砂を製造する方法が開示されている。また土木材料用
に適した球状の造粒物にしうる造粒機として、パン型、
ドラム型などの転動造粒機、スパイラル、アイリッヒ、
ヘンシェルなどの高速攪拌造粒機等が従来公知の技術と
して知られている。しかしながら、これらの造粒機に
は、造粒物を容易に且つ大量に製造するのに、問題があ
る。転動造粒機は、造粒操作時、機内での造粒状態を監
視して水分または固体原料の添加量を適宜調整する必要
があるので、設備の自動化が難しいこと、また得られる
造粒物は粒度分布幅が狭く且つ球形状であることから、
充填密度が小さく、締固めによるCBR試験(Cali
fornia Bearing Ratio;JIS
A 1211)での荷重強度も小さく、土木材料等に適
しない。一方、高速攪拌造粒機は、粒成長の推移に対応
する造粒機のトルクの変化が小さく、自動化が難しいこ
と、また得られる造粒物は比較的粒度が小さい。2. Description of the Related Art In order to effectively use coal ash generated in large quantities from a coal-fired power plant, a method has been proposed in which granules used as civil engineering materials are artificially produced using coal ash as a raw material. I have. Japanese Patent Application Laid-Open No. 61-151052 discloses a method of producing coal ash sand by adding cement and water to coal ash and performing high-speed mixing and granulation. Similarly, Japanese Patent Application Laid-Open No. 63-201045 discloses a method of producing coal ash sand by adding cement and water to coal ash and slag powder and performing high-speed mixing and granulation. In addition, as a granulator capable of forming spherical granules suitable for civil engineering materials, bread molds,
Rolling granulator such as drum type, spiral, Erich,
A high-speed stirring granulator such as Henschel is known as a conventionally known technique. However, there is a problem with these granulators in that the granules can be easily produced in large quantities. In the tumbling granulator, it is necessary to monitor the granulation state inside the granulator during the granulation operation and adjust the addition amount of moisture or solid raw material appropriately, so that it is difficult to automate the equipment and obtain the granulation obtained. Since the product has a narrow particle size distribution and a spherical shape,
Compact density, compacted CBR test (Cali
fornia Bearing Ratio; JIS
A 1211) has a low load strength and is not suitable for civil engineering materials. On the other hand, the high-speed stirring granulator has a small change in the torque of the granulator corresponding to the transition of the grain growth and is difficult to automate, and the obtained granules have a relatively small grain size.
【0003】[0003]
【発明が解決しようとする課題】本発明の目的は、それ
自体公知の円錐型スクリュー混合機中で、充填密度が高
く、締固めによる荷重強度も高く、土木材料、建築材料
として利用できる石炭灰を含む造粒物を製造する方法を
提供することにある。本発明の他の目的は、造粒物の原
材料投入から造粒物排出まで、一連の操作を自動化する
ことが可能な、造粒物の製造方法を提供することにあ
る。本発明のさらに他の目的および利点は以下の説明か
ら明らかになろう。SUMMARY OF THE INVENTION It is an object of the present invention to provide a coal ash which can be used as a civil engineering material or a building material in a conical screw mixer known per se, which has a high filling density, a high load strength by compaction. It is to provide a method for producing a granulated product containing: Another object of the present invention is to provide a method for producing a granulated material, which can automate a series of operations from the input of the raw material of the granulated material to the discharge of the granulated material. Still other objects and advantages of the present invention will become apparent from the following description.
【0004】[0004]
【課題を解決するための手段】本発明によれば、本発明
の上記目的および利点は、第1に、石炭灰、セメントお
よびセメントキルンダストからなる固体原料および水
を、円錐型スクリュー混合機中で混合し且つ該混合機中
で造粒物にまで仕上げることを特徴とする、造粒物の製
造方法によって達成される。According to the present invention, the above objects and advantages of the present invention are as follows: first, a solid raw material consisting of coal ash, cement and cement kiln dust and water are mixed in a conical screw mixer. And finishing in the mixer to a granulated product.
【0005】固体原料の各成分の配合割合は、石炭灰、
セメントおよびセメントキルンダストの合計100重量
部を基準にして、石炭灰は好ましくは50〜95重量
部、より好ましくは60〜90重量部、特に好ましくは
60〜85重量部であり、セメントは好ましくは2〜2
5重量部、より好ましくは5〜20重量部であり、そし
てセメントキルンダストは好ましくは3〜45重量部、
より好ましくは5〜35重量部、特に好ましくは10〜
25重量部である。[0005] The mixing ratio of each component of the solid raw material is coal ash,
The coal ash is preferably 50 to 95 parts by weight, more preferably 60 to 90 parts by weight, particularly preferably 60 to 85 parts by weight, based on a total of 100 parts by weight of cement and cement kiln dust, and the cement is preferably 2-2
5 parts by weight, more preferably 5 to 20 parts by weight, and the cement kiln dust is preferably 3 to 45 parts by weight,
More preferably 5-35 parts by weight, particularly preferably 10-35 parts by weight
25 parts by weight.
【0006】石炭灰が50重量部より少ないと、石炭灰
の有効利用量が減少するので好ましくない。また95重
量部よりも多くなると、得られる石炭灰造粒物の強度が
小さくなるために好ましくない。セメントが2重量部よ
りも少ないと、得られる石炭灰造粒物の強度が小さくな
るために好ましくない。また25重量部よりも多くなる
と、石炭灰造粒物の製造コストが高くなるため好ましく
ない。[0006] When the amount of coal ash is less than 50 parts by weight, the effective utilization amount of coal ash decreases, which is not preferable. On the other hand, if it exceeds 95 parts by weight, the strength of the obtained coal ash granulated material is undesirably reduced. If the amount of cement is less than 2 parts by weight, the strength of the obtained coal ash granulated material is undesirably reduced. On the other hand, if it is more than 25 parts by weight, the production cost of the coal ash granules increases, which is not preferable.
【0007】セメントキルンダストが3重量部よりも少
ないと、石炭灰とセメントの粒子間の間隙を十分充填す
ることができなくなるので好ましくない。また45重量
部よりも多くなると、石炭灰とセメントの粒子間の間隙
から、セメントキルンダストがはみ出し、石炭灰を含む
造粒物の強度が低下する原因となるので好ましくない。
石炭灰としては、微粉炭燃焼灰、流動層燃焼灰等いずれ
も使用できるが、流動層燃焼灰は造粒物を容易に製造で
きるので、特に好適に使用できる。これらは単独である
いは2種以上一緒に使用できる。[0007] If the amount of the cement kiln dust is less than 3 parts by weight, it is not preferable because the gap between the coal ash and the cement particles cannot be sufficiently filled. If the amount is more than 45 parts by weight, cement kiln dust protrudes from the gap between the coal ash and the cement particles, which is not preferable because it causes a reduction in the strength of the granulated material containing the coal ash.
As coal ash, any of pulverized coal combustion ash, fluidized bed combustion ash and the like can be used, but fluidized bed combustion ash can be particularly preferably used because a granulated product can be easily produced. These can be used alone or in combination of two or more.
【0008】セメントキルンダストの平均粒子径は、好
ましくは10μm以下、より好ましくは5μm以下、特
に好ましくは1μm以下である。セメントほどの水硬性
は有さないものの水硬性を有するものが望ましい。平均
粒子径が10μm以上になると、石炭灰およびセメント
の粒子と同等ないしそれ以上の大きさとなり、これらの
粒子間の間隙を充填することが困難となるため好ましく
ない。造粒用に使用される水分量は固体原料の種類およ
び粒径等によって異なるが、通常固体原料100重量部
当たり水は25〜45重量部の範囲にある。The average particle size of the cement kiln dust is preferably 10 μm or less, more preferably 5 μm or less, particularly preferably 1 μm or less. Although it does not have hydraulic properties as cement, it is desirable to have hydraulic properties. If the average particle size is 10 μm or more, the size becomes equal to or larger than the particles of coal ash and cement, and it is difficult to fill the gap between these particles, which is not preferable. Although the amount of water used for granulation varies depending on the type and particle size of the solid raw material, water is usually in the range of 25 to 45 parts by weight per 100 parts by weight of the solid raw material.
【0009】本発明方法は、固体原料の混合のみなら
ず、造粒物の形成をも、該円錐型スクリュー混合機中で
実施する。円錐型スクリュー混合機はそれ自体公知であ
り、円錐端を下方にした円錐型本体と円錐型本体の内壁
に沿って上方から下方へ向かって位置するスクリュー攪
拌軸からなる。スクリュー攪拌軸は公転と自転の回転可
能である。In the method of the present invention, not only the mixing of the solid raw materials but also the formation of granules is carried out in the conical screw mixer. Conical screw mixers are known per se and consist of a conical body with a conical end pointing downwards and a screw stirring shaft located from above to below along the inner wall of the conical body. The screw stirring shaft is capable of revolving and rotating.
【0010】本発明方法を実施するために、円錐型スク
リュー混合機は、スクリュー攪拌軸の公転速度を好まし
くは1〜5rpmの回転で、自転速度を好ましくは40
〜200rpmの回転で、操作されるのが有利である。
スクリュー攪拌軸は自転することによって、円錐型本体
内の内容物を下方から上方へ掻揚げる作用をなし、公転
することによって、内容物全体の混合、造粒を促進す
る。スクリュー攪拌軸に負荷されるトルクは同攪拌軸の
負荷電流を検知することによって知ることができる。In order to carry out the process of the present invention, the conical screw mixer has a rotation speed of the screw stirring shaft of preferably 1 to 5 rpm and a rotation speed of preferably 40 rpm.
It is advantageous to operate at a rotation of ~ 200 rpm.
The screw agitating shaft rotates to rotate the content in the conical body from the bottom to the top, thereby promoting the mixing and granulation of the entire content by revolving. The torque applied to the screw stirring shaft can be known by detecting the load current of the stirring shaft.
【0011】本発明方法によれば、円錐型スクリュー混
合機を造粒機として使用することにより、第1に石炭
灰、セメント等の固体原料の混合状態、水の添加に伴う
造粒化開始の状態、その後の粒成長推移等の状況変化
を、造粒機の負荷電流値に対応して知ることができ、従
ってまた一連の造粒操作を自動化できること、第2に造
粒機の構造が円錐型であり且つスクリュー攪拌軸の自転
・掻揚げ作用により、造粒物の移動軌跡が粒径別に異な
るので造粒効率が高いこと、第3に得られる造粒物は、
パン型造粒機などの転動造粒機等に比較して球形度が若
干劣り、加えて所定粒径より大きい粗大の造粒物または
製品造粒物の一部を粗砕し、固体原料の一部として造粒
機に供給して、製品造粒物の粒度分布幅を調整できるこ
とから、充填密度が高く、締固めによるCBR試験での
荷重強度も高く、土木材料等に適した造粒物が製造でき
ること、等の利点が得られる。According to the method of the present invention, by using a conical screw mixer as a granulator, firstly, the mixing state of solid raw materials such as coal ash and cement, and the start of granulation with the addition of water. A state change such as a state and a subsequent change in grain growth can be known in accordance with a load current value of the granulator, and therefore, a series of granulation operations can be automated. Due to the rotation and the scooping action of the screw stirring shaft being a mold, the movement trajectory of the granulated material is different according to the particle size, so that the granulation efficiency is high.
Sphericality is slightly inferior to rolling granulators such as bread granulators, etc. In addition, coarse granules or a part of product granules larger than a predetermined particle size are coarsely crushed to obtain solid raw materials. Can be supplied to the granulator as a part of the product, and the particle size distribution width of the product granulation can be adjusted, so the packing density is high, the load strength in the CBR test by compaction is high, and granulation suitable for civil engineering materials etc. Advantages are obtained such that a product can be manufactured.
【0012】造粒された造粒物は、通常の湿潤空気中あ
るいは蒸気中にて養生された後に、土木材料などとして
使用される。以下、本発明の造粒方法を添付図面の図1
に示した一実施態様により説明する。[0012] The granulated product is cured in ordinary humid air or steam and then used as a civil engineering material. Hereinafter, the granulation method of the present invention will be described with reference to FIG.
An embodiment will be described with reference to FIG.
【0013】石炭灰(a)、セメント(b)およびセメ
ントキルンダスト(c)の各固体原料は、それぞれ計量
器(フィーダ)(1−a)、(1−b)、(1−c)、
輸送ライン(2)を経由し、所定量切り出され、原料受
器(3)に供給される。また、石炭灰(a)、セメント
(b)およびセメントキルンダスト(c)の各固体原料
のほかに、所定粒径より大きい粗大の造粒物または製品
造粒物の一部を粗砕したシード(d)を使用してもよ
い。The solid raw materials of the coal ash (a), the cement (b) and the cement kiln dust (c) are respectively weighed (feeders) (1-a), (1-b), (1-c),
A predetermined amount is cut out via the transport line (2) and supplied to the raw material receiver (3). In addition to the solid raw materials of coal ash (a), cement (b) and cement kiln dust (c), seeds obtained by coarsely crushing a part of a coarse granulated product or a product granulated product having a particle size larger than a predetermined particle size. (D) may be used.
【0014】原料受器(3)から原料ホッパースケール
(4)に供給された所定量の固体原料は、予め指定され
た造粒サイクルに基づき、特定の円錐型スクリュー混合
機(5−1)、(5−2)および(5−3)のいずれか
(5)に投入される。一方、原料ホッパースケール
(4)で計量された固体原料に比例した所定量の水が流
量計(図示せず)を経由して給水ライン(6)から該円
錐型スクリュー混合機(5)に投入され、造粒操作が開
始する。A predetermined amount of solid raw material supplied to the raw material hopper scale (4) from the raw material receiver (3) is supplied to a specific conical screw mixer (5-1) based on a granulation cycle designated in advance. Charged to any one of (5-2) and (5-3) (5). On the other hand, a predetermined amount of water proportional to the solid raw material measured by the raw material hopper scale (4) is supplied to the conical screw mixer (5) from a water supply line (6) via a flow meter (not shown). Then, the granulation operation starts.
【0015】石炭灰、セメント等固体原料の混合状態、
水の添加に伴う造粒化開始の状態、その後の粒成長推移
等、円錐型スクリュー混合機(5)内で進行している造
粒化の状況変化が、造粒機の負荷電流値に対応し、造粒
操作の制御信号として入力される。造粒物が所定粒度に
造粒され、造粒機の負荷電流が予め設定された値に達し
た時点で、造粒物は、円錐型スクリュー混合機(5)か
ら、自動的に造粒物受器(7)に排出される。A mixed state of solid raw materials such as coal ash and cement,
Changes in the state of granulation progressing in the conical screw mixer (5), such as the state of the start of granulation due to the addition of water and the transition of the subsequent grain growth, correspond to the load current value of the granulator. Then, it is input as a control signal for the granulation operation. When the granulated material is granulated to a predetermined particle size and the load current of the granulator reaches a preset value, the granulated material is automatically transferred from the conical screw mixer (5) to the granulated material. It is discharged to a receiver (7).
【0016】引き続き造粒物は、造粒物受器(7)から
造粒物搬送機(8)を経由して、貯蔵場に搬送される過
程で、造粒物表面に粉体受器(9)から供給される集塵
機(10)のダスト粉塵(e)または石炭灰(a)がコ
ーティングされ、製品造粒物となる。これら一連の回分
造粒操作は、固体原料の投入・混合、造粒機での造粒時
間等を基に、複数基の円錐型スクリュー混合機(5−
1、5−2、5−3)を使用し、最適なサイクルシステ
ムで構成される。Subsequently, the granules are transferred from the granule receiver (7) to the storage site via the granule transporter (8), and on the surface of the granules, the powder receiver ( The dust dust (e) or coal ash (a) of the dust collector (10) supplied from 9) is coated to form a product granulated product. These series of batch granulation operations are based on charging and mixing of solid raw materials, granulation time in a granulator, and the like, and a plurality of conical screw mixers (5-
1, 5-2, 5-3) and is configured with an optimal cycle system.
【0017】[0017]
【実施例】以下に本発明による実施例を示す。表1に示
す配合割合の石炭灰、セメントの固体原料を円錐型スク
リュー混合機(有効容積100リットル;公転4rp
m、自転127rpm)で10分間混合した後、表1に
示す水量を加え、造粒を開始した。引き続き40分間の
攪拌・混合した後、所定粒度の造粒物を得た。この間の
石炭灰、セメント等の固体原料の混合状態、水の添加に
伴う造粒化開始の状態、その後の粒成長推移等と造粒機
の負荷電流値変化との対応関係を図2に示した。図か
ら、水の添加と同時に電流値が著しく高くなり、攪拌の
継続と共に固体原料の粒子・粒子の一次凝集・圧密化に
より造粒物表面に浮水が発生し、高次の凝集・圧密化へ
と推移する現象と電流値との対応が読み取れる。得られ
た造粒物の粒度分布および修正CBR試験結果を表2に
示した。造粒物は、締固めによる荷重強度が高く、路盤
材として利用できる性状である。Embodiments of the present invention will be described below. A solid raw material of coal ash and cement having a mixing ratio shown in Table 1 was mixed with a conical screw mixer (effective volume: 100 liters;
m, rotation at 127 rpm) for 10 minutes, and then the amount of water shown in Table 1 was added to start granulation. Subsequently, after stirring and mixing for 40 minutes, a granulated product having a predetermined particle size was obtained. Fig. 2 shows the mixing state of the solid raw materials such as coal ash and cement, the state of the start of granulation with the addition of water, the transition of the subsequent grain growth, and the change in the load current value of the granulator during this time. Was. As can be seen from the figure, the current value increased remarkably at the same time as the addition of water, and as the agitation continued, the primary agglomeration and consolidation of the particles of the solid raw material caused floating water on the surface of the granulated material, leading to higher-order aggregation and consolidation Can be read. Table 2 shows the particle size distribution of the obtained granules and the results of the modified CBR test. The granulated material has a high load strength due to compaction and has properties that can be used as a roadbed material.
【0018】[0018]
【表1】 [Table 1]
【0019】[0019]
【表2】 [Table 2]
【0020】[0020]
【発明の効果】本発明によれば、石炭灰、セメント等の
固体原料および水の投入から製品造粒物の排出まで、一
連の造粒操作が自動化可能である。造粒操作が容易で且
つ省力化された造粒装置が構成できる。また単一の造粒
機で、粒度分布幅のある造粒物が製造でき、充填密度が
高く、締め固めによるCBR試験での荷重強度も高く、
土木材料等として利用できる石炭灰利用造粒物が製造で
きる。According to the present invention, a series of granulation operations from the input of solid raw materials such as coal ash and cement and water to the discharge of product granules can be automated. A granulating apparatus in which the granulating operation is easy and labor saving can be configured. In addition, a single granulator can produce granules with a particle size distribution width, high packing density, high load strength in compaction CBR test,
It is possible to produce coal ash-based granules that can be used as civil engineering materials and the like.
【0021】[0021]
【図1】本発明の造粒方法の一実施態様のフローシート
である。FIG. 1 is a flow sheet of one embodiment of the granulation method of the present invention.
【図2】本発明の実施例における、円錐型スクリュー混
合機(造粒機)の負荷電流値の経時的変化を示す。FIG. 2 shows a change with time of a load current value of a conical screw mixer (granulator) in an example of the present invention.
A、B、C、D 原料サイロ a 石炭灰 b セメント c セメントキルンダスト d シード e ダスト粉塵 1−a 石炭灰のフィーダ 1−b セメントのフィーダ 1−c セメントキルンダストのフィーダ 1−d シードのフィーダ 1−e ダスト粉塵または石炭灰のフィーダ 2 輸送ライン 3 原料受器 4 原料ホッパースケール 5、5−1、5−2、5−3 円錐型スクリュー混合機 6 給水ライン 7 造粒物受器 8 造粒物搬送機 9 粉体受器 10 集塵機 A, B, C, D Raw material silo a Coal ash b Cement c Cement kiln dust d Seed e Dust dust 1-a Coal ash feeder 1-b Cement feeder 1-c Cement kiln duster 1-d Seed feeder 1-e Dust dust or coal ash feeder 2 Transport line 3 Raw material receiver 4 Raw material hopper scale 5, 5-1 5-2, 5-3 Conical screw mixer 6 Water supply line 7 Granulated material receiver 8 Granule transporter 9 Powder receiver 10 Dust collector
───────────────────────────────────────────────────── フロントページの続き (72)発明者 大城 清昭 沖縄県名護市字安和1008番地 琉球セメン ト株式会社屋部工場内 (72)発明者 沢田 守彦 山口県宇部市大字小串1978番地の5 宇部 興産株式会社内 (72)発明者 新田 邦昭 山口県宇部市大字小串1978番地の5 宇部 興産株式会社内 (72)発明者 和田 孝夫 山口県宇部市大字小串1978番地の5 宇部 興産株式会社内 ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Kiyoaki Oshiro 1008 Awa, Nago City, Okinawa Prefecture Inside the Yabe Plant of the Ryukyu Cement Co., Ltd. Inside Kosan Co., Ltd. (72) Inventor Kuniaki Nitta 5 Ube Kosan, 1978 Ogushi, Ube City, Yamaguchi Prefecture Inside (72) Inventor Takao Wada 5 Ube Kogushi, 1978 Kodaigushi, Ube City, Yamaguchi Prefecture
Claims (4)
ダストからなる固体原料および水を、円錐型スクリュー
混合機中で混合し且つ該混合機中で造粒物にまで仕上げ
ることを特徴とする、石炭灰を含む造粒物の製造方法。1. A coal ash, comprising mixing a coal ash, a solid raw material comprising cement and cement kiln dust and water in a conical screw mixer and finishing the mixture into granules in the mixer. A method for producing a granulated product comprising:
〜95重量部、セメント2〜25重量部およびセメント
キルンダスト3〜45重量部である請求項1の方法。2. Coal ash 50 per 100 parts by weight of solid raw material
The method of claim 1 wherein the amount is from about 95 parts by weight, from 2 to 25 parts by weight cement, and from 3 to 45 parts by weight cement cement.
45重量部である請求項1の方法。3. Water 25 to 100 parts by weight of solid raw material
The method of claim 1 wherein the amount is 45 parts by weight.
拌軸の負荷電流値の変化から造粒状況を検知することに
より、造粒操作を自動化することを特徴とする請求項1
の方法。4. The granulation operation is automated by detecting a granulation state from a change in a load current value of a screw stirring shaft of the conical screw mixer.
the method of.
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JP6598398A JP3807466B2 (en) | 1998-03-17 | 1998-03-17 | Method for producing granulated material containing coal ash |
Applications Claiming Priority (1)
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JP6598398A JP3807466B2 (en) | 1998-03-17 | 1998-03-17 | Method for producing granulated material containing coal ash |
Publications (2)
Publication Number | Publication Date |
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JPH11263658A true JPH11263658A (en) | 1999-09-28 |
JP3807466B2 JP3807466B2 (en) | 2006-08-09 |
Family
ID=13302762
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JP6598398A Expired - Fee Related JP3807466B2 (en) | 1998-03-17 | 1998-03-17 | Method for producing granulated material containing coal ash |
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JP (1) | JP3807466B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003146723A (en) * | 2001-11-12 | 2003-05-21 | Ube Ind Ltd | Concrete composition and mortal composition |
JP2007169141A (en) * | 2005-11-22 | 2007-07-05 | Taiheiyo Cement Corp | Method for producing burnt products |
JP6432711B1 (en) * | 2018-02-09 | 2018-12-05 | 中国電力株式会社 | Granulated product manufacturing equipment and method of manufacturing granulated product |
-
1998
- 1998-03-17 JP JP6598398A patent/JP3807466B2/en not_active Expired - Fee Related
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003146723A (en) * | 2001-11-12 | 2003-05-21 | Ube Ind Ltd | Concrete composition and mortal composition |
JP2007169141A (en) * | 2005-11-22 | 2007-07-05 | Taiheiyo Cement Corp | Method for producing burnt products |
JP6432711B1 (en) * | 2018-02-09 | 2018-12-05 | 中国電力株式会社 | Granulated product manufacturing equipment and method of manufacturing granulated product |
WO2019155635A1 (en) * | 2018-02-09 | 2019-08-15 | 中国電力株式会社 | Granulated article production facility and production method for granulated article |
Also Published As
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JP3807466B2 (en) | 2006-08-09 |
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