JP2022142857A - Filler treatment method - Google Patents

Filler treatment method Download PDF

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JP2022142857A
JP2022142857A JP2021043091A JP2021043091A JP2022142857A JP 2022142857 A JP2022142857 A JP 2022142857A JP 2021043091 A JP2021043091 A JP 2021043091A JP 2021043091 A JP2021043091 A JP 2021043091A JP 2022142857 A JP2022142857 A JP 2022142857A
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water
filler
cement
granulation
granules
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裕太 田原
Yuta Tawara
泰史 山本
Yasushi Yamamoto
敦士 山口
Atsushi Yamaguchi
幾雄 中村
Ikuo Nakamura
浩茂 田代
Hiroshige Tashiro
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Taiheiyo Engineering Corp
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00Technologies for solid waste management
    • Y02W30/50Reuse, recycling or recovery technologies
    • Y02W30/91Use of waste materials as fillers for mortars or concrete

Abstract

To suppress a treating cost when treating fillers generated in a dry sand crushing process by using a dewatered cake and the like generated in waste water treatment in a washing aggregate manufacturing process, and to effectively utilize the fillers as a cement raw material.SOLUTION: Provided is a treating method of fillers in which fillers F generated in a dry sand crushing process are granulated and cured by adding ordinary cement CE and water W. In addition, a dewatered cake CA may be added for granulation. Granulation can be ensured by adjusting the water content of filler, ordinary cement and water before granulation or the mixture of filler, ordinary cement, water and dewatered cake before granulation to 9.5 mass% or more and 18.3 mass% or less, and the strength of the granulated material can be sufficiently enhanced by adjusting the addition rate of ordinary cement to the filler, ordinary cement and water before granulation, or to the mixture of the filler, ordinary cement, water and dewatered cake before granulation, to 2.5 mass% or more.SELECTED DRAWING: Figure 1

Description

本発明は、フィラーの処理方法に関し、乾式砕砂工程で発生するフィラーを水洗骨材製造工程の廃水処理で発生する脱水ケーキ等を用いて処理し、セメント原料に利用する方法に関する。 The present invention relates to a filler treatment method, and more particularly to a method of treating filler generated in a dry sand crushing process using dehydrated cake or the like generated in wastewater treatment in a water-washed aggregate manufacturing process, and using the treated cake as a raw material for cement.

特許文献1には、砕石微粉末を土木材料として有効利用するため、砕石微粉末に浄水場脱水ケーキ、高炉セメント及び水を加え、脱水ケーキの配合率を70±20質量%、高炉セメントの配合率を外割合で5~10質量%とした上で、これらを造粒することが開示される。 In Patent Document 1, in order to effectively use crushed stone fine powder as a civil engineering material, water purification plant dehydrated cake, blast furnace cement and water are added to crushed stone fine powder, and the blending ratio of dewatered cake is 70 ± 20% by mass, and the blending ratio of blast furnace cement is It is disclosed that these are granulated after setting the ratio to 5 to 10% by mass as an external ratio.

特開2009-190949号公報JP 2009-190949 A

しかし、上記特許文献1に記載の発明は、脱水ケーキ及び高炉セメントの配合率が高く、養生期間が1週間と長く、造粒物の水分量も多く、バッチ式で造粒するため、処理コストが高くなるという問題がある。 However, the invention described in Patent Document 1 has a high blending ratio of dehydrated cake and blast furnace cement, a long curing period of one week, a large amount of water in the granules, and batch granulation, so the processing cost is high. There is a problem that the

また、特許文献1に記載の発明は、砕石微粉末を造粒することで、主に埋め戻し材として再利用するものである。一方、セメント原料として利用する造粒物には、粉砕し易く、水分が少ないことが要求される。しかし、同文献に記載の発明は、埋め戻し材等として利用するため造粒物の強度が高く、造粒物をセメント原料として利用し難い。 Further, the invention described in Patent Document 1 granulates crushed stone fine powder and reuses it mainly as a backfilling material. On the other hand, granules used as raw materials for cement are required to be easily pulverized and have a low water content. However, in the invention described in the document, since the granules are used as a backfilling material or the like, the strength of the granules is high, and it is difficult to use the granules as a raw material for cement.

そこで、本発明は、上記従来の技術における問題点に鑑みてなされたものであって、乾式砕砂工程で発生するフィラーを水洗骨材製造工程の廃水処理で発生する脱水ケーキ等を用いて処理するにあたり、処理コストを低く抑えると共に、これらをセメント原料として有効利用することを目的とする。 Therefore, the present invention has been made in view of the above-mentioned problems in the conventional technology, and treats the filler generated in the dry sand crushing process using dehydrated cake etc. generated in the wastewater treatment of the water-washed aggregate manufacturing process. In this regard, the object is to reduce the processing cost and to effectively utilize them as cement raw materials.

上記目的を達成するため、本発明はフィラーの処理方法であって、乾式砕砂工程で発生するフィラーに普通セメントと水を添加して造粒し、養生することを特徴とする。 In order to achieve the above object, the present invention is a filler treatment method, characterized in that ordinary cement and water are added to the filler generated in the dry sand crushing process, granulated and cured.

本発明によれば、フィラーの造粒に高炉セメントではなく普通セメントを用いることで、比較的短時間の養生で、雨水によって微粉が流出しない程度の強度を有し、かつ、セメント原料として利用する際に粉砕しやすい強度とすることができる。 According to the present invention, by using ordinary cement instead of blast-furnace cement for granulating the filler, it can be cured for a relatively short time and has a strength to the extent that fine powder does not flow out due to rainwater, and can be used as a raw material for cement. The strength can be such that it can be easily pulverized.

上記フィラーの処理方法において、前記普通セメントと水に加え、水洗骨材製造工程で発生する脱水ケーキを添加して造粒してもよい。 In the method for treating the filler, in addition to the ordinary cement and water, a dehydrated cake generated in the water-washed aggregate manufacturing process may be added for granulation.

また、前記造粒前のフィラー、普通セメント及び水、又は前記造粒前のフィラー、普通セメント、水及び脱水ケーキの混合物の水分を9.5質量%以上18.3%以下の範囲でフィラーに対する脱水ケーキの添加率に応じて調整することで、確実に造粒することができる。 In addition, the water content of the filler before granulation, ordinary cement and water, or the mixture of filler, ordinary cement, water and dehydrated cake before granulation is 9.5% by mass or more and 18.3% or less relative to the filler By adjusting according to the addition rate of the dehydrated cake, granulation can be reliably performed.

さらに、前記造粒前のフィラー、普通セメント及び水、又は前記造粒前のフィラー、普通セメント、水及び脱水ケーキの混合物の普通セメント添加率を2.5質量%以上に調整することで、造粒物の強度を十分に高めることができる。 Furthermore, by adjusting the normal cement addition rate of the filler before granulation, normal cement and water, or the mixture of filler, normal cement, water and dehydrated cake before granulation to 2.5% by mass or more, The strength of the granules can be sufficiently increased.

前記造粒を行う造粒機の後段にパンペレタイザー等の第2造粒機を設置し、再度造粒を行うことで、最初の造粒によって微粉量の発生が多い場合に対応することができる。 By installing a second granulator such as a pan pelletizer after the granulator that performs the granulation and performing granulation again, it is possible to cope with the case where a large amount of fine powder is generated by the first granulation. .

前記造粒前のフィラー、普通セメント及び水で造粒した保水性の低い造粒物については、前記造粒によって得られた造粒物を養生する際に散水することで、セメントの水和反応に必要な水分を補填し、雨水によるフィラーの流出を抑制可能な強度を有する造粒物を製造することができる。 For the granules with low water retention that are granulated with the filler before granulation, ordinary cement, and water, water is sprinkled when curing the granules obtained by the granulation, thereby suppressing the hydration reaction of the cement. It is possible to produce a granulated material having a strength capable of replenishing the necessary moisture in and suppressing outflow of the filler due to rainwater.

また、前記造粒物又は前記散水後の造粒物をセメント原料として利用することができる。 In addition, the granules or the granules after watering can be used as a raw material for cement.

以上のように、本発明によれば、乾式砕砂工程で発生するフィラーを水洗骨材製造工程の廃水処理で発生する脱水ケーキ等を用いて処理するにあたり、処理コストを低く抑えると共に、これらをセメント原料として有効利用することができる。 As described above, according to the present invention, when the filler generated in the dry sand crushing process is treated using the dehydrated cake or the like generated in the wastewater treatment of the washing aggregate manufacturing process, the treatment cost can be kept low and these can be used as cement. It can be effectively used as a raw material.

本発明に係るフィラーの処理方法を実施するための装置の構成例を示す全体構成図である。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is an overall configuration diagram showing a configuration example of an apparatus for carrying out a filler processing method according to the present invention; 本発明に係るフィラーの処理方法の試験例において、ケーキ添加率と造粒物水分の関係を示すグラフであって、ハッチングの範囲において造粒性が良好となる。FIG. 10 is a graph showing the relationship between cake addition rate and moisture content of granules in test examples of the filler treatment method according to the present invention, in which the granulation properties are good in the hatched range. 本発明に係るフィラーの処理方法の試験例において、ケーキ添加率とセメント添加率の関係を示すグラフであって、ハッチングの範囲において造粒物強度が良好となる。Fig. 2 is a graph showing the relationship between the cake addition rate and the cement addition rate in test examples of the filler treatment method according to the present invention, in which the granule strength is good in the hatched range.

次に、本発明を実施するための形態について図面を参照しながら詳細に説明する。 EMBODIMENT OF THE INVENTION Next, it demonstrates in detail, referring drawings for the form for implementing this invention.

図1は、本発明に係るフィラーの処理方法を実施するための装置の一例を示し、この装置1は、乾式砕砂工程で発生するフィラー(石灰石を主要成分とする集塵粉等)を水洗骨材製造工程の廃水処理で発生する脱水ケーキ等と混合して造粒し、露天の置き場に積みつけた際に、造粒物が雨水に晒されても造粒物から微粉が流出することを防止することを目的とするものである。 FIG. 1 shows an example of an apparatus for carrying out the method for treating a filler according to the present invention. This apparatus 1 removes filler (collected dust containing limestone as a main component, etc.) generated in a dry sand crushing process by washing bones with water. When granulated by mixing with dewatered cake, etc. generated in the wastewater treatment of the wood manufacturing process, and stacked in an open-air storage area, even if the granulated material is exposed to rainwater, fine powder will flow out from the granulated material. It is intended to prevent

上記装置1は、水洗骨材製造工程の廃水の沈降分離を行うシックナー2と、シックナー2からのスラリーSを脱水する脱水機3と、脱水機3からの脱水ケーキCAと、乾式砕砂工程で発生するフィラーFと、普通セメント(以下「セメント」という。)CEと、水Wを混合して造粒する造粒機4と、造粒機4による造粒物Gの強度を出すために養生する置き場5等で構成される。尚、状況に応じて、造粒機4の前段に脱水機3からの脱水ケーキCAを解砕し、フィラーFと混合する混合機を設けたり、造粒機4の後段にさらに造粒用のパンペレタイザー6を設けたり、置き場5の上方に散水装置7を設ける。また、脱水ケーキCAを造粒に用いないこともある。 The apparatus 1 includes a thickener 2 for sedimentation and separation of wastewater in the washing aggregate manufacturing process, a dehydrator 3 for dewatering the slurry S from the thickener 2, a dewatered cake CA from the dehydrator 3, and a dry sand crushing process. A granulator 4 that mixes a filler F, ordinary cement (hereinafter referred to as "cement") CE, and water W to granulate, and the granules G produced by the granulator 4 are cured to increase their strength. It is composed of storage space 5 and the like. Depending on the situation, a mixer for crushing the dehydrated cake CA from the dehydrator 3 and mixing it with the filler F may be provided in the preceding stage of the granulator 4, or a mixer for granulation may be further provided in the latter stage of the granulating machine 4. A pan pelletizer 6 is provided, and a sprinkler device 7 is provided above the place 5. - 特許庁Also, the dehydrated cake CA may not be used for granulation.

造粒機4には、連続式のパグミルを使用することができる。パグミルは、ケーシング内部に複数のパドルを備え付けた軸を2本有し、これらの軸が回転可能に構成されている。パドルの傾斜は10~45°とし、パドルの代わりにピンを使用してもよい。 A continuous pug mill can be used for the granulator 4 . A pug mill has two shafts provided with a plurality of paddles inside a casing, and these shafts are rotatable. The inclination of the paddle should be between 10 and 45 degrees, and a pin may be used instead of the paddle.

上記解砕混合機にパグミルを用いることもでき、パグミル以外のミキサーを使用することもできる。一例として、リボン型ミキサーを用いてもよい。リボン型ミキサーは、従来練り混ぜの障害となっていたシャフトを取り除き、2本の螺旋アームを用いて混練性能を高めたものである。 A pug mill can be used as the crushing mixer, and a mixer other than the pug mill can also be used. As an example, a ribbon mixer may be used. The ribbon type mixer removes the conventional shaft, which was an obstacle to mixing, and uses two spiral arms to improve mixing performance.

また、解砕から造粒まで1基で行える造粒機4として、バッチ式のドラム型ミキサー等を利用してもよい。ドラム型ミキサーは、ドラムの中に回転方向と回転速度を各々変更可能なスイング式のブレード及び多段ロータを備え、ブレードによって圧縮とかき上げを繰り返して材料を練り込み、多段ロータの高速回転により材料を撹拌し、均一に混練、造粒する。 A batch-type drum-type mixer or the like may be used as the granulator 4 capable of performing from pulverization to granulation in one unit. The drum type mixer is equipped with swing-type blades and multi-stage rotors capable of changing the rotation direction and speed inside the drum. are stirred, uniformly kneaded and granulated.

パンペレタイザー6は、造粒機4による造粒物の微粉量を減少させるために設けられる。パンペレタイザー6は、パンの傾斜回転によって材料を転動造粒するものであり、パンの回転数や傾斜角度等を微調整することで、外径数mmから数十mmの造粒物を連続して得ることができる。 The pan pelletizer 6 is provided to reduce the fine powder amount of the granules produced by the granulator 4 . The pan pelletizer 6 rolls and granulates the material by tilting the pan. By finely adjusting the number of rotations and the angle of inclination of the pan, granules with an outer diameter of several millimeters to several tens of millimeters are continuously produced. can be obtained by

散水装置7にはスプリンクラー等を用いることができ、扇形等の散水ノズルによって均質に散水し、散水時間をタイマーで制御することが好ましい。 A sprinkler or the like can be used for the watering device 7, and it is preferable that water is uniformly sprinkled by a fan-shaped watering nozzle or the like, and the watering time is controlled by a timer.

次に、上記構成を有する装置1の全体的な動作について、図1を参照しながら説明する。 Next, the overall operation of the device 1 having the above configuration will be described with reference to FIG.

石灰石鉱山の水洗骨材製造工程で生ずる廃水をシックナー2で沈降分離し、シックナー2から排出されたスラリーSを脱水機3で脱水して脱水ケーキCAを生成する。この脱水ケーキCAを、乾式砕砂工程で発生したフィラーF、セメントCE及び水Wと共に造粒機4に供給し、造粒機4で解砕、混合、混錬、造粒する。この際、添加する水Wは、造粒に必要な最小限の量とする。また、脱水ケーキCAの水分が多く、造粒に必要な水分量を上回る場合は、生石灰を添加して消化反応によって不要な水分を蒸発させてもよい。造粒物Gは、置き場5に積みつけて養生し、適度な強度を有し、ハンドリング性が改善された後、セメント原料等として利用する。 A thickener 2 sediments and separates waste water generated in a washing aggregate manufacturing process in a limestone mine, and a slurry S discharged from the thickener 2 is dehydrated in a dehydrator 3 to produce a dehydrated cake CA. This dehydrated cake CA is supplied to the granulator 4 together with the filler F, cement CE and water W generated in the dry sand crushing process, and the granulator 4 crushes, mixes, kneads and granulates the cake. At this time, the amount of water W to be added is the minimum amount required for granulation. If the dehydrated cake CA contains a lot of moisture and exceeds the amount of moisture required for granulation, quicklime may be added to evaporate unnecessary moisture through a digestive reaction. The granules G are piled up in the storage area 5 and cured to have appropriate strength and improved handleability, and are then used as a raw material for cement or the like.

次に、造粒機4にパグミルを用いた場合の造粒工程について詳細に説明する。 Next, the granulation process when using a pug mill as the granulator 4 will be described in detail.

パグミルに供給されるフィラーFの水分は0.1~2.0%、d50(メジアン径)は30~70μmである。脱水ケーキCAの水分は17~30%、d50は5~20μmで、脱水ケーキCAには廃水処理工程で高分子凝集剤が添加されている。また、セメントCEには普通ポルトランドセメント(普通セメント)を使用する。普通セメントは、引用文献1記載の高炉セメントと比較して短時間で強度が出やすいため好ましい。尚、造粒のために添加する水は新規水を使用するが、廃水処理工程から排出される廃水(スラリーSを脱水機3で脱水したろ液やケーキ洗浄後水等)を利用してもよい。 The filler F supplied to the pug mill has a water content of 0.1 to 2.0% and a d50 (median diameter) of 30 to 70 μm. The water content of the dehydrated cake CA is 17-30%, d50 is 5-20 μm, and a polymer flocculant is added to the dehydrated cake CA in the wastewater treatment process. Ordinary Portland cement (ordinary cement) is used as cement CE. Ordinary cement is preferred because it tends to be strong in a short time compared to the blast-furnace cement described in Cited Document 1. Although new water is used as the water added for granulation, wastewater discharged from the wastewater treatment process (filtrate obtained by dehydrating the slurry S with the dehydrator 3, water after washing the cake, etc.) can also be used. good.

パグミルの一方の端部付近から脱水ケーキCAを装置内に導入し、装置の他方の端部付近へと流れる過程でパドルによって100~500mmの脱水ケーキCAが3~20mmに解砕される。脱水ケーキCAを先に解砕することで、後段で投入されるフィラーF及びセメントCEとの混合性が向上する。次に、脱水ケーキCAが投入された装置の一方の端部から装置長さの1/4程度の場所よりフィラーF及びセメントCEを投入し、解砕された脱水ケーキCAと共に乾混合する。水Wを投入する前に乾混合することにより、投入量の少ないセメントCAを均一に分散させることができる。次に、装置長さの1/2程度の場所から水Wを供給し、装置の他方の端部から排出されるまでに3~50mmの造粒物Gが形成される。このように、パグミル内をケーキ解砕ゾーン、混合ゾーン、混錬ゾーン、造粒ゾーンに細分化することで効率的に造粒することができる。 The dehydrated cake CA is introduced into the apparatus from near one end of the pug mill, and the dehydrated cake CA of 100 to 500 mm is pulverized into 3 to 20 mm by the paddles in the process of flowing to near the other end of the apparatus. By pulverizing the dehydrated cake CA first, the mixability with the filler F and the cement CE that are introduced later is improved. Next, the filler F and the cement CE are charged from one end of the device into which the dehydrated cake CA is charged from about 1/4 of the length of the device, and are dry-mixed together with the pulverized dehydrated cake CA. By dry-mixing before adding the water W, it is possible to uniformly disperse the cement CA, which is added in a small amount. Next, water W is supplied from a position about half the length of the apparatus, and 3 to 50 mm granules G are formed by the time the water is discharged from the other end of the apparatus. Thus, by subdividing the inside of the pug mill into the cake crushing zone, the mixing zone, the kneading zone, and the granulation zone, efficient granulation can be achieved.

パグミルの原料充填率は10~75%、好ましくは35~55%とし、造粒状況に応じて変更する。滞留時間は1~20分、好ましくは2~10分とし、造粒状況に応じて変更し、滞留時間を調整するために、パグミルに傾斜をつけてもよい。また、解砕及び混合ゾーンと混錬及び造粒ゾーンを分割して2基直列で繋いでもよい。これにより、各ゾーンに適した軸の回転数を設定することができる。 The raw material filling rate of the pug mill is 10 to 75%, preferably 35 to 55%, and is changed according to the granulation conditions. The residence time is 1 to 20 minutes, preferably 2 to 10 minutes, depending on the granulation situation and the pug mill may be tilted to adjust the residence time. Alternatively, the crushing/mixing zone and the kneading/granulation zone may be divided and connected in series. Thereby, it is possible to set the number of revolutions of the shaft suitable for each zone.

造粒可能な水分量は、フィラーFに対する脱水ケーキCAの添加率によって変動する。脱水ケーキCAの添加率が0%の場合には水分量が9.5(下限値)であり、脱水ケーキCAの添加率が100%の場合には水分量が18.3%(上限値)である。ケーキ添加率をx、造粒物水分をyとすると、y=0.0485x+11.625の関係式から最適な水分を求めることができる。造粒可能な水分の範囲は関係式の切片11.625±2である。尚、脱水ケーキCAの水分は17~30%であるため、造粒可能な水分の範囲を超える場合には、造粒前に脱水ケーキCAに生石灰を添加して水分を蒸発、又は乾燥機で乾燥させる必要がある。 The amount of water that can be granulated varies depending on the addition ratio of the dehydrated cake CA to the filler F. When the addition rate of the dehydrated cake CA is 0%, the water content is 9.5 (lower limit), and when the addition rate of the dehydrated cake CA is 100%, the water content is 18.3% (upper limit). is. Assuming that the cake addition rate is x and the water content of the granules is y, the optimum water content can be obtained from the relational expression y=0.0485x+11.625. The range of moisture that can be granulated is the intercept of the relational expression, 11.625±2. In addition, since the water content of the dehydrated cake CA is 17 to 30%, if the water content exceeds the range of water that can be granulated, quick lime is added to the dehydrated cake CA before granulation to evaporate the water, or It should be dried.

造粒可能な水分に加えて、最適なセメント量も脱水ケーキCAの添加率によって変動する。比較的短時間の養生時間で十分な強度にするためには、ケーキ添加率0%(フィラ-100%)ではセメント3.5%以上、ケーキ添加率25~50%ではセメント2.5%以上、ケーキ添加率75%ではセメント3.5%以上、ケーキ添加率100%(フィラー0%)ではセメント4.5%以上となる。尚、コストの観点から、セメント添加率は5%未満が好ましい。造粒物の大きさは好ましくは2~40mm、より好ましくは5~20mmである。造粒物を篩目0.6mmの篩で篩った際の微粉率は好ましくは10%以下、より好ましく6%、特に好ましくは3%以下である。造粒物の嵩密度は好ましくは0.8~1.6t/m、より好ましくは1.0~1.4t/mである。造粒物の安息角は好ましくは30~60°、より好ましくは40~50°とする。 In addition to the water content that can be granulated, the optimum amount of cement also varies with the addition rate of the dehydrated cake CA. In order to achieve sufficient strength in a relatively short curing time, it is necessary to use 3.5% or more cement at a cake addition rate of 0% (filler - 100%), and 2.5% or more cement at a cake addition rate of 25-50%. , at a cake addition rate of 75%, the cement is 3.5% or more, and at a cake addition rate of 100% (filler 0%), the cement is 4.5% or more. From the viewpoint of cost, the cement addition rate is preferably less than 5%. The size of the granules is preferably 2-40 mm, more preferably 5-20 mm. When the granules are sieved through a sieve with a sieve mesh of 0.6 mm, the fine powder ratio is preferably 10% or less, more preferably 6%, and particularly preferably 3% or less. The bulk density of the granules is preferably 0.8-1.6 t/m 3 , more preferably 1.0-1.4 t/m 3 . The angle of repose of the granules is preferably 30-60°, more preferably 40-50°.

次に、上記装置1を用いて本発明に係るフィラーの処理方法を実施するために必要な条件を決定する各種試験について説明する。 Next, various tests for determining the conditions necessary for carrying out the filler treatment method according to the present invention using the apparatus 1 will be described.

試験に用いたフィラーF、ケーキCA、セメントCEの水分、化学組成及び粒度を表1に示す。水分は重量含水率を示し、化学組成はドライベースで示す。 Table 1 shows the water content, chemical composition and particle size of Filler F, Cake CA and Cement CE used in the test. Moisture is given by weight and chemical composition is given on a dry basis.

Figure 2022142857000002
Figure 2022142857000002

まず、フィラーFを造粒するにあたり、ケーキCAと共に加えるバインダーとして、セメントCEと生石灰のどちらが好ましいか、またその添加量はどの程度が好ましいかを調査した。 First, in granulating the filler F, it was investigated which of cement CE and quicklime is preferable as a binder to be added together with the cake CA, and what the amount of addition thereof is preferable.

ケーキ:フィラー:バインダーを重量比(ドライベース)で25:75:0.5~3.5とし、ヘンシェルミキサーでこれらを混合し、パンペレタイザーにて混合物に加水しながら造粒し、所定時間養生した。養生後の造粒物を水に浸漬又は散水した後の水の濁度で造粒物を表2に示す4段階で評価した。 The weight ratio (dry base) of cake: filler: binder is 25:75:0.5 to 3.5, mixed with a Henschel mixer, granulated while adding water to the mixture with a pan pelletizer, and cured for a predetermined time. did. After curing, the granules were immersed in water or sprinkled with water, and the turbidity of the water was used to evaluate the granules according to four levels shown in Table 2.

Figure 2022142857000003
Figure 2022142857000003

生石灰又はセメントをバインダーとした造粒物を5h養生した後、水に浸漬させて崩壊性を確認した。その結果を表3に示す。生石灰2.5質量%をバインダーとした造粒物は水に浸漬させるとすぐに崩壊してしまったが、セメント2.5質量%をバインダーとした造粒物は半日経過後も崩壊しなかった。そのため、バインダーとしてはセメントが好ましいことが判る。 Granules containing quicklime or cement as a binder were cured for 5 hours and then immersed in water to confirm disintegration properties. Table 3 shows the results. The granules with 2.5% by mass of quicklime as a binder disintegrated immediately after being immersed in water, but the granules with 2.5% by weight of cement as a binder did not disintegrate even after half a day. . Therefore, it can be seen that cement is preferable as a binder.

Figure 2022142857000004
Figure 2022142857000004

次に、ケーキ:フィラーの重量比(ドライベース)を25:75とした上で、セメントの添加率(質量%)と造粒物の養生時間を変化させ、造粒物に50mm/h相当で10分間散水を行った後の水の濁度を評価した。その結果を表4に示す。同表より、ケーキ25%の添加率の造粒物から雨水によって微粉を流出させないためには、セメントを2.5質量%以上添加して造粒し、5時間以上養生する必要があることが判る。 Next, after setting the cake: filler weight ratio (dry base) to 25:75, the cement addition rate (mass%) and the curing time of the granules were changed, and the granules were treated at a rate equivalent to 50 mm / h. The turbidity of the water was evaluated after 10 minutes of watering. Table 4 shows the results. According to the table, in order to prevent fine powder from being washed out by rainwater from the granules with an addition rate of 25% cake, it is necessary to add 2.5% by mass or more of cement to the granules and cure them for 5 hours or more. I understand.

Figure 2022142857000005
Figure 2022142857000005

次に、ケーキとフィラーとセメントを用い、パグミルとパンペレタイザーで造粒した造粒物の流出性評価に関する試験を行った。ケーキ:フィラー:セメントを重量比で25:75:2.5とし、水を加えてパグミルで造粒(150kg/h)した結果、表5に示すように、10~20mmの造粒物(水分11.3質量%)が得られた(パグミル品)。この造粒機品の微粉量(0.6mm篩下)は6.9質量%であった。微粉量を減少させるために、パンペレタイザーでパグミル品をさらに造粒すると、15~30mmの造粒物(水分11.1質量%)が得られ(パンペレ品)、微粉量は0.0質量%となった。このように、パグミル等の造粒機で造粒した後に仕上げとしてパンペレタイザーで造粒することで、微粉量の発生を抑制することができる。また、水浸漬と散水評価について、パグミル品とパンペレ品の双方とも良好であった。 Next, using cake, filler, and cement, a test was carried out on the outflow evaluation of granules granulated with a pug mill and a pan pelletizer. The weight ratio of cake:filler:cement was 25:75:2.5, and water was added and granulated with a pug mill (150 kg/h). 11.3% by mass) was obtained (pug mill product). The amount of fine powder (under 0.6 mm sieve) of this granulator product was 6.9% by mass. In order to reduce the amount of fine powder, the pug mill product is further granulated with a bread pelletizer to obtain granules of 15 to 30 mm (moisture content: 11.1% by mass) (pane pellet product), and the fine powder amount is 0.0% by mass. became. Thus, by granulating with a granulator such as a pug mill and then granulating with a pan pelletizer as finishing, generation of fine powder can be suppressed. Both the Pugmil product and the Pampere product were good in the water immersion and water sprinkling evaluations.

Figure 2022142857000006
Figure 2022142857000006

以上より、ケーキとフィラーとセメントで造粒物を製造する場合には、バインダーとしてセメントを2.5質量%以上添加し、造粒物を5時間以上養生すればよいことが判る。 From the above, it can be seen that when granules are produced from cake, filler, and cement, 2.5% by mass or more of cement should be added as a binder, and the granules should be cured for 5 hours or more.

次に、パグミルを使用して、ケーキとフィラーとセメントの割合を変化させた場合の造粒可能な水分量と十分な強度を発現するセメント量の関係について調査した。その結果を表6に示す。同表の造粒性について、水分量が適切で造粒できた場合は〇、水分が少なく材料が纏まらない、又は水分が多く粘土状の塊となった場合は×とした。また、造粒物強度については、上述の水浸漬及び散水評価で◎となった場合は〇、それ以外は×とした。また、ケーキ添加率(質量%)と造粒物水分(質量%)の関係を図2に示す。さらに、表6において造粒性が○となった実施例No.1~14について、ケーキ添加率(質量%)とセメント(バインダー)添加率(質量%)の関係を図3に示す。両図において、造粒性又は造粒物強度が〇の場合を黒四角で、×の場合を黒ひし形で示し、ハッチングの範囲内において造粒性又は造粒物強度が良好である。 Next, using a pug mill, the relationship between the amount of water that can be granulated and the amount of cement that develops sufficient strength was investigated when the ratio of cake, filler and cement was changed. Table 6 shows the results. Regarding the granulation properties in the table, ◯ indicates that the water content was appropriate and granulation was possible, and x indicates that the water content was too low and the material did not come together, or the water content was too high and resulted in clay-like lumps. In addition, regarding the strength of the granules, ◯ was given when the above water immersion and water sprinkling evaluations were ⊚, and x was given otherwise. Fig. 2 shows the relationship between the cake addition rate (% by mass) and the water content of the granules (% by mass). Further, in Table 6, the granulation property of Example No. 1 was evaluated as ◯. FIG. 3 shows the relationship between the cake addition rate (mass %) and the cement (binder) addition rate (mass %) for 1 to 14. In both figures, when the granulation property or granule strength is ◯, the case is indicated by a black square, and when the case is x, the case is indicated by a black diamond.

Figure 2022142857000007
Figure 2022142857000007

表7は、上記結果に基づくケーキ添加率(質量%)毎の造粒物水分(質量%)の下限値と上限値を示す。造粒物水分(質量%)が下限値と上限値の間にあれば、造粒性が良好となる。 Table 7 shows the lower limit and upper limit of the water content (% by mass) of the granulated product for each cake addition rate (% by mass) based on the above results. If the water content of the granules (% by mass) is between the lower limit and the upper limit, the granulation properties will be good.

Figure 2022142857000008
Figure 2022142857000008

また、表6において、造粒性は良好であったが強度が不足したNo.10及びNo.12について、造粒後と養生後の水分を比較した。表8に示すように、No.12(ケーキ15質量%)では水分減少率が26質量%(13.1→9.7質量%)であったのに対し、No.10(ケーキ0質量%)では水分減少率が91質量%(12.8→1.2質量%)と大きかった。表1より、フィラーはケーキよりも粘土成分(SiO、Al)が少なく、粒度が大きいため、保水性が低い。そのため、ケーキ0質量%では保水性が低い上に粒子間に空隙があるため、養生中に乾燥し、セメントの水和反応が進行せずに十分な結合力が得られず、浸漬中に崩壊したと推察される。 Also, in Table 6, No. 1 had good granulation properties but lacked strength. 10 and no. Regarding No. 12, the moisture content after granulation and after curing was compared. As shown in Table 8, No. No. 12 (15% by mass of cake) had a moisture reduction rate of 26% by mass (13.1→9.7% by mass), whereas No. 10 (0% by mass of cake) had a large moisture reduction rate of 91% by mass (12.8→1.2% by mass). As can be seen from Table 1, the filler has less clay components (SiO 2 , Al 2 O 3 ) than the cake, and has a larger particle size, so the water retention is lower. Therefore, when the cake is 0% by mass, the water retention is low and there are voids between the particles. It is presumed that

Figure 2022142857000009
Figure 2022142857000009

そこで、散水後の造粒物(5時間養生→散水→10時間養生:計15h養生)を浸漬した結果、いずれの造粒物においても崩壊性の改善が認められた。そのため、養生中に造粒物の水分が低下する場合には、スプリンクラー等で散水して造粒物を保水することも有効であることが分かった。 Therefore, as a result of immersing the granules after watering (curing for 5 hours→curing for 10 hours: curing for a total of 15 hours), improvement in disintegration was observed in all granules. Therefore, when the water content of the granules decreases during curing, it is also effective to sprinkle water with a sprinkler or the like to retain water in the granules.

以上のように、本発明によれば、乾式砕砂工程から発生するフィラーを造粒するにあたって普通セメントを使用し、また造粒時に添加する水分を最小限に抑え、粉砕し易い造粒物を製造することで、セメント原料として利用し易い造粒物を得ることができる。また、造粒物の水分が少ないため、セメントキルンの熱損失を低減することができる。造粒物が粉砕し易いため、粉砕コストの低減にも繋がる。さらに、造粒機を用いることで連続して造粒を行うことができ、フィラーの大量処理が可能となる。さらにまた、養生期間を短くすることで置き場容積を縮小することができるなどの利点がある。 As described above, according to the present invention, ordinary cement is used in granulating the filler generated from the dry sand crushing process, and the amount of water added during granulation is minimized to produce granules that are easy to crush. By doing so, it is possible to obtain a granule that can be easily used as a raw material for cement. In addition, since the granules have little water content, the heat loss of the cement kiln can be reduced. Since the granules are easily pulverized, the pulverization cost can be reduced. Furthermore, by using a granulator, granulation can be continuously performed, and a large amount of filler can be processed. Furthermore, there is an advantage that the storage space can be reduced by shortening the curing period.

以上、本発明の一実施の形態について説明したが、本発明は、上述した本発明の実施形態に限定されるものではなく、本発明の要旨を逸脱しない範囲内で様々な変形や応用が可能である。 Although one embodiment of the present invention has been described above, the present invention is not limited to the above-described embodiment of the present invention, and various modifications and applications are possible without departing from the scope of the present invention. is.

1 フィラーの処理装置
2 シックナー
3 脱水機
4 造粒機
5 置き場
6 パンペレタイザー
7 散水装置
CA 脱水ケーキ
CE 普通セメント
F フィラー
G 造粒物
S スラリー
W 水
1 Filler treatment device 2 Thickener 3 Dehydrator 4 Granulator 5 Placement 6 Pan pelletizer 7 Sprinkler CA Dehydrated cake CE Ordinary cement F Filler G Granule S Slurry W Water

Claims (7)

乾式砕砂工程で発生するフィラーに普通セメントと水を添加して造粒し、養生することを特徴とするフィラーの処理方法。 A filler treatment method characterized by adding ordinary cement and water to filler generated in a dry sand crushing process, granulating the granules, and curing the granules. 前記普通セメントと水に加え、水洗骨材製造工程で発生する脱水ケーキを添加して造粒することを特徴とする請求項1に記載のフィラーの処理方法。 2. The method of treating a filler according to claim 1, wherein the granulation is performed by adding a dewatered cake generated in the water-washed aggregate production process in addition to the ordinary cement and water. 前記造粒前のフィラー、普通セメント及び水、又は前記造粒前のフィラー、普通セメント、水及び脱水ケーキの混合物の水分を9.5質量%以上18.3%以下に調整することを特徴とする請求項1又は2に記載のフィラーの処理方法。 The water content of the filler before granulation, ordinary cement and water, or the mixture of filler, ordinary cement, water and dehydrated cake before granulation is adjusted to 9.5% by mass or more and 18.3% or less. The method for treating a filler according to claim 1 or 2. 前記造粒前のフィラー、普通セメント及び水、又は前記造粒前のフィラー、普通セメント、水及び脱水ケーキの混合物の普通セメント添加率を2.5質量%以上に調整することを特徴とする請求項1、2又は3に記載のフィラーの処理方法。 The normal cement addition rate of the filler before granulation, normal cement and water, or the mixture of filler, normal cement, water and dehydrated cake before granulation is adjusted to 2.5% by mass or more. Item 1, 2 or 3, the filler treatment method. 前記造粒を行う造粒機の後段に第2造粒機を設置し、再度造粒を行うことを特徴とする請求項1乃至4のいずれかに記載のフィラーの処理方法。 5. The filler processing method according to any one of claims 1 to 4, wherein a second granulator is installed after the granulator that performs the granulation, and granulation is performed again. 前記造粒によって得られた造粒物を養生する際に散水することを特徴とする請求項1乃至5のいずれかに記載のフィラーの処理方法。 6. The filler treatment method according to claim 1, wherein water is sprinkled when curing the granules obtained by the granulation. 前記造粒物又は前記散水後の造粒物をセメント原料として利用することを特徴とする請求項1乃至6のいずれかに記載のフィラーの処理方法。
7. The filler treatment method according to claim 1, wherein the granules or the granules after watering are used as raw materials for cement.
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