JP2019181354A - Granulation-solidification processing of powder material - Google Patents

Granulation-solidification processing of powder material Download PDF

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JP2019181354A
JP2019181354A JP2018074062A JP2018074062A JP2019181354A JP 2019181354 A JP2019181354 A JP 2019181354A JP 2018074062 A JP2018074062 A JP 2018074062A JP 2018074062 A JP2018074062 A JP 2018074062A JP 2019181354 A JP2019181354 A JP 2019181354A
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granulation
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勝部 英一
Hidekazu Katsube
英一 勝部
一夫 有木
Kazuo Ariki
一夫 有木
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Kitagawa Iron Works Co Ltd
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Abstract

To provide a granulation object manufacturing method for preventing fastening of mutual granulation objects, by delaying progress of hardening reaction of the granulation objects to an optional time.SOLUTION: A method for granulation-solidification-processing a powder material having a self-hardening property such as combustion ash and steel making dust, is composed of a process 1 of mixing-granulating a granulation object by adding an organic compound such as a soluble sugar or a carboxylic acid to the powder material and a process 2 of adding the physical action to the granulation object after the process 1, and progress of hardening reaction of the granulation object is delayed to an optional time by the process 1, and fastening of the mutual granulation objects is further prevented by the process 2.SELECTED DRAWING: Figure 1

Description

本発明は、造粒物の硬化反応の進行を任意の時間に遅延させ、造粒物同士の固着を抑制することで造粒物の一体化を防止する粉体材料の造粒固化方法に関する。   The present invention relates to a method for granulating and solidifying a powder material in which the progress of the curing reaction of a granulated product is delayed to an arbitrary time and the granulated product is prevented from being integrated by suppressing the fixation of the granulated products.

飛散しやすい燃焼灰及び製鋼ダスト等の粉体材料をリサイクルする方法として、適度な水、重金属等の有害物質の溶出を抑える薬剤、及び少量の生石灰あるいはセメント等の固化材を混合することで造粒固化する方法がある。
この様な造粒固化処理では、粉体材料はハンドリング上、問題にならない形状にすることができ、燃焼灰は施工性に優れた埋め戻し用の資材、肥料、融雪剤、若しくは土壌改良用の資材となり、製鋼ダストについては含有される金属成分を回収するための塊原料となる。
一般的に造粒固化処理においては、使用場面での施工性が重要になることから製造した造粒物は、砂利や砂のようにある程度の流動性を備えていることが求められている。一方で、造粒物の形状保持を目的に添加する生石灰やセメント等の固化材の作用もあり、養生中に堆積させた造粒物同士が固着し一体化することがある。そのため、実際の運用現場では、セメント等における初期強度の発現が接水から約24時間後であることを考慮して、造粒物がある程度の硬さになる製造の翌日に、横持ち移動も兼ねホイルローダー等の重機を用いて物理的な作用を加え、造粒物の堆積物を一度崩すことで造粒物同士の固着を防止し堆積物が一体化しないようにしている。
As a method to recycle powder materials such as combustion ash and steelmaking dust that are easily scattered, it is manufactured by mixing moderate water, chemicals that suppress the elution of harmful substances such as heavy metals, and a small amount of solidified material such as quick lime or cement. There is a method of solidifying.
In such a granulation solidification treatment, the powder material can be made into a shape that does not pose a problem for handling, and the combustion ash is an excellent material for backfilling, fertilizer, snow melting agent, or soil improvement. It becomes a material, and the steelmaking dust becomes a lump material for recovering the contained metal component.
In general, in the granulation solidification process, since the workability in the usage scene becomes important, the manufactured granulated product is required to have a certain degree of fluidity such as gravel and sand. On the other hand, there is also an action of a solidifying material such as quick lime or cement added for the purpose of maintaining the shape of the granulated product, and the granulated product deposited during curing may be fixed and integrated. Therefore, in actual operation sites, taking into account that the initial strength development in cement etc. is about 24 hours after water contact, on the next day of production when the granulated product becomes a certain degree of hardness, horizontal movement is also possible. At the same time, physical action is applied using a heavy machine such as a wheel loader, and the granule deposits are broken once to prevent the granulates from sticking to each other so that the deposits are not integrated.

特開2012−076009号公報JP2012-076009A 特開2016−175030号公報JP-A-2006-175030

一般的に、燃焼灰や製鋼ダスト等の粉体は、発生過程で脱硫を目的とした石灰の投入処理、更には高温下に曝されるため、生石灰、無水石膏、硅酸、アルミナ及び金属酸化物等の成分が生成され含有していることが多い。
これらの成分は、接水することで一部が溶け出し、再結晶化する過程で強固な固化体を作ることがある。この反応は、セメントの硬化反応よりも急激で、造粒直後から発熱を伴いながら数時間以内に起こる。そのため、ホイルローダー等の重機を用いて堆積物を崩す工程を製造の翌日に行う従来の方法では、硬化反応の進行が速すぎるために重機作業を行う前に堆積状態で造粒物が完全に一体化してしまい、流動性のあるハンドリングの良い造粒物を製造できないという課題があった。
また、埋め戻し用の資材、肥料、融雪剤、あるいは土壌改良用の資材の中には、施用後に土壌中で徐々に崩壊し馴染んで行くことが必要で、形状のみならず、適度な崩壊性を要求されるものがあるが、従来の造粒固化処理では、粉体材料自身が有する硬化反応を制御できないために、用途に応じた硬さを備える造粒物を製造することが出来なかった。
In general, powders such as combustion ash and steelmaking dust are exposed to high-temperature lime, anhydrous gypsum, oxalic acid, alumina, and metal oxides because they are exposed to lime for the purpose of desulfurization during the generation process, and also exposed to high temperatures. In many cases, components such as products are produced and contained.
A part of these components may be dissolved by contact with water, and a solidified body may be formed in the process of recrystallization. This reaction is more rapid than the hardening reaction of cement and occurs within a few hours with heat generation immediately after granulation. For this reason, in the conventional method in which the process of breaking the deposit using a heavy machine such as a wheel loader is performed on the next day of production, the progress of the curing reaction is too fast so that the granulated material is completely deposited in the deposited state before the heavy machine work is performed. There existed a subject that it integrated and could not manufacture the granulated material with good fluidity and handling.
Also, some materials for backfilling, fertilizer, snow melting agent, or soil improvement need to gradually disintegrate and become familiar in the soil after application. However, in the conventional granulation solidification process, the curing reaction of the powder material itself cannot be controlled, so it was not possible to produce a granulated product with hardness according to the application. .

そこで本発明の目的は、造粒物の硬化反応の進行を任意の時間に遅延させるとともに、造粒物同士の固着を防止させる造粒物製造方法を提供することにある。   Accordingly, an object of the present invention is to provide a method for producing a granulated product that delays the progress of the curing reaction of the granulated product to an arbitrary time and prevents the granulated products from sticking to each other.

具体的には、上記課題は、
燃焼灰や製鋼ダスト等の自硬性を有する粉体材料を造粒固化処理する方法において、
前記粉体材料に可溶性の糖あるいはカルボン酸等の有機化合物を添加して造粒物を混合造粒する工程1と、
前記工程1のあとに、前記造粒物に対して物理的作用を加える工程2と、からなり、
前記工程1によって、前記造粒物の硬化反応の進行を任意の時間に遅延させ、
前記工程2によって、さらに、前記造粒物同士の固着を防止することを特徴とする粉体材料の造粒固化方法を提供することによって解決される。
Specifically, the above issues are
In the method of granulating and solidifying a powder material having self-hardening properties such as combustion ash and steelmaking dust,
Step 1 of mixing and granulating a granulated product by adding an organic compound such as a soluble sugar or carboxylic acid to the powder material;
After the step 1, comprising a step 2 of applying a physical action to the granulated product,
By the step 1, the progress of the curing reaction of the granulated product is delayed to an arbitrary time,
The problem can be solved by providing a method for granulating and solidifying the powder material, wherein the step 2 further prevents the agglomerates from being fixed to each other.

また、燃焼灰や製鋼ダスト等の自硬性を有する粉体材料を造粒固化処理する方法において、
前記粉体材料を造粒物に造粒する工程3と、
前記工程3によって、造粒された前記造粒物の表面に可溶性の糖及びカルボン酸等の有機化合物を付着させる工程4と、
前記工程4のあとに、前記造粒物に対して物理的作用を加える工程5と、からなり、
前記工程4によって、前記造粒物の表面の硬化反応の進行を任意の時間に遅延させ、
前記工程5におって、さらに、造粒物同士の固着を防止することを特徴とする粉体材料の造粒固化方法を提供することによっても解決される。
Moreover, in the method of granulating and solidifying a powder material having self-hardening properties such as combustion ash and steelmaking dust,
Step 3 of granulating the powder material into a granulated product,
A step 4 of attaching an organic compound such as a soluble sugar and a carboxylic acid to the surface of the granulated product granulated by the step 3;
After the step 4, the step 5 of applying a physical action to the granulated product,
By the step 4, the progress of the curing reaction on the surface of the granulated product is delayed to an arbitrary time,
In the step 5, the problem can also be solved by providing a method for granulating and solidifying the powder material, which is characterized by preventing adhesion between the granules.

本発明によれば、造粒物の硬化反応の進行を任意の時間に遅延させるとともに、造粒物同士の固着を防止させる造粒物製造方法を提供することができる。   ADVANTAGE OF THE INVENTION According to this invention, while progressing the hardening reaction of a granulated material can be delayed to arbitrary time, the granulated material manufacturing method which prevents adhesion | attachment of granulated materials can be provided.

本発明の添加物にセメント用凝結遅延剤を用いた際の硬化反応に伴う発熱の経時変化を示した図である。It is the figure which showed the time-dependent change of the heat_generation | fever accompanying the hardening reaction at the time of using the setting retarder for cement for the additive of this invention. 本発明の圧壊強度の経時変化を示した図である。It is the figure which showed the time-dependent change of the crushing strength of this invention. 図1の添加物に廃糖蜜を用いた際の硬化反応に伴う発熱の経時変化を示した図である。It is the figure which showed the time-dependent change of the heat_generation | fever accompanying a hardening reaction at the time of using waste molasses for the additive of FIG.

以下、本発明の実施形態を図面と表に基づいて詳細に説明する。但し、以下の説明は、本質的に例示に過ぎず、本発明、その適用物あるいはその用途を制限するものではない。   Hereinafter, embodiments of the present invention will be described in detail with reference to the drawings and tables. However, the following description is merely illustrative in nature and does not limit the present invention, its application, or its use.

〈粉体材料〉
本発明で用いる粉体材料は、廃棄物の焼却施設等から排出される燃焼灰、バイオマスあるいは石炭等を燃料とする発電施設から排出される燃焼灰、製鉄所の転炉あるいは電気炉から排出される製鋼ダスト等で、生石灰、無水石膏、硅酸、アルミナ、金属酸化物等の成分の何れか2種類以上を含有しているものが挙げられる。
<Powder material>
The powder material used in the present invention is discharged from combustion ash discharged from a waste incineration facility, combustion ash discharged from a power generation facility fueled with biomass or coal, etc., from a converter or electric furnace of a steel mill. Steelmaking dust, etc., which contain any two or more of components such as quicklime, anhydrous gypsum, succinic acid, alumina, metal oxides.

〈有機化合物〉
本発明で用いる有機化合物は、セメントの凝結を遅延する効果が認められている物質が好ましい。例えば、可溶性の糖は、グルコース、フルクトース、スクロース、マルトース等の糖類が挙げられる。これら可溶性の糖は、単独で含有させても良いし、2種類以上の混合物として含有させても良い。
また、精糖工程で排出される廃糖蜜等、これら可溶性の糖が成分に含まれているものであっても良い。
<Organic compounds>
The organic compound used in the present invention is preferably a substance that is recognized to have an effect of delaying the setting of cement. For example, examples of the soluble sugar include sugars such as glucose, fructose, sucrose, and maltose. These soluble sugars may be contained alone or as a mixture of two or more.
Moreover, the thing in which these soluble sugars are contained in a component, such as waste molasses discharged | emitted in a refined sugar process, may be used.

〈カルボン酸系有機化合物〉
本発明で用いるカルボン酸系有機化合物としては、グルコン酸、アスコルビン酸、クエン酸等が挙げられ、これらカルボン酸は、単独で含有させても良いし、2種類以上の混合物として含有させても良い。
また、セメントの凝結遅延剤として市販されているグルコン酸を含む薬剤を使用することもできる。更に、これらカルボン酸系有機化合物と可溶性の糖を組み合わせて使用することも可能である。
<Carboxylic acid organic compound>
Examples of the carboxylic acid-based organic compound used in the present invention include gluconic acid, ascorbic acid, citric acid and the like. These carboxylic acids may be contained alone or as a mixture of two or more kinds. .
Moreover, the chemical | medical agent containing gluconic acid marketed as a setting retarder of cement can also be used. Furthermore, it is also possible to use these carboxylic acid organic compounds in combination with a soluble sugar.

〈造粒硬化方法〉
本発明の造粒固化方法では、造粒物について、埋め戻し用の資材、肥料、融雪剤、あるいは土壌改良用の資材等の様に施用後に土壌中で徐々に崩壊し馴染むことが求められる場合は、粉体材料に添加する可溶性の糖あるいはカルボン酸系有機化合物の添加量を調整することで、一定時間後の造粒物の硬さ(圧壊強度)を低下させることができる。
<Granulation hardening method>
In the granulation solidification method of the present invention, the granulated product is required to gradually disintegrate in the soil after application, such as a material for backfilling, a fertilizer, a snow melting agent, or a material for soil improvement. Can reduce the hardness (crushing strength) of the granulated product after a certain time by adjusting the amount of soluble sugar or carboxylic acid organic compound added to the powder material.

本発明の造粒固化方法では、ドラム型やパン型の造粒機を用いる転動造粒、回転羽根で攪拌しながら造粒する高速攪拌造粒等の方法が挙げられ、特に、複数材料を混合しながら造粒できる高速攪拌造粒による方法が好ましい。   Examples of the granulation solidification method of the present invention include rolling granulation using a drum-type or pan-type granulator, and high-speed stirring granulation for granulating while stirring with a rotary blade. A method by high-speed stirring granulation that enables granulation while mixing is preferred.

一旦造粒物とした後に、当該造粒物の表面に付着させるように可溶性の糖あるいはカルボン酸等の有機化合物を添加する手段としては、造粒機内で散水あるいは噴霧しても良く、造粒機から別の工程に移送する過程で散水あるいは噴霧しても良い。例えば、排出口側に傾斜させた回転ドラムによる移送過程で散水あるいは噴霧することが出来る。また、可溶性の糖あるいはカルボン酸等の有機化合物を適宜水で希釈することで、散水あるいは噴霧が行いやすくなる。   As a means for adding an organic compound such as a soluble sugar or carboxylic acid so as to adhere to the surface of the granulated product once it has been made into a granulated product, water may be sprayed or sprayed in the granulator. You may spray or spray in the process of transferring from a machine to another process. For example, water can be sprayed or sprayed during the transfer process using a rotating drum inclined toward the discharge port. In addition, water or spraying can be easily performed by appropriately diluting an organic compound such as a soluble sugar or carboxylic acid with water.

実施に当たっては、小型の造粒試験機等を用い、予め粉体材料に水のみを加えて造粒物を作製し、接水直後から概ね24時間以内に発熱のピークが観察されることを確認しておくことが好ましい。   In the implementation, using a small granulation tester etc., add water only to the powder material in advance to produce a granulated product, and confirm that a peak of heat generation is observed within approximately 24 hours immediately after water contact. It is preferable to keep it.

この際、24時間以内に発熱のピークが見られない、あるいは24時間以降にピークが観察される場合は、本発明で示す可溶性の糖あるいはカルボン酸系有機化合物を添加しなくても、造粒固化処理の翌日に重機等による造粒堆積物の崩し作業が十分行えるためである。   At this time, if no exothermic peak is observed within 24 hours, or a peak is observed after 24 hours, granulation can be performed without adding the soluble sugar or carboxylic organic compound shown in the present invention. This is because the granulated deposits can be sufficiently destroyed by heavy machinery or the like on the day after the solidification treatment.

さらに、小型の粒試験機等を用いて造粒試験を行い、予め可溶性の糖あるいはカルボン酸等の添加量とピークの遅延時間の関係を確認しておくことで、重機等による造粒堆積物の崩し作業の予定時間に合わせた造粒固化処理の工程が組めるようになる。   Furthermore, by conducting a granulation test using a small grain tester, etc., and confirming in advance the relationship between the amount of soluble sugar or carboxylic acid added and the peak delay time, The process of granulation solidification processing according to the scheduled time of the breakage work can be assembled.

本発明では、完全に硬化する前の堆積した造粒物に物理的作用を加えるが、これは造粒物同士が完全に固着する前に、造粒物同士の接触部を切り離すことが目的となる。
したがって、堆積した造粒物に物理的作用を加える方法としては、ホイルローダー等の重機以外に、堆積ヤードに設置した物理的な衝撃、振動を加えることが出来る振動板、稼動床、切返し装置等の機械設備が使用できる。
In the present invention, a physical action is applied to the accumulated granulated material before being completely cured, and this is intended to separate the contact portion between the granulated materials before the granulated materials are completely fixed to each other. Become.
Therefore, as a method of applying a physical action to the accumulated granulated material, in addition to a heavy machine such as a wheel loader, a physical plate installed in the accumulation yard, a diaphragm capable of applying vibration, an operating floor, a turning device, etc. Can be used.

(実施例1)
表1は、試験に対して燃焼灰、水、セメント用凝結遅延剤の添加量と割合を示した表である。また、図1は、本発明の添加物にセメント用凝結遅延剤を用いた際の硬化反応に伴う発熱の経時変化を示した図、図2は、本発明の圧壊強度の経時変化を夫々示した図である。
実験例1−3として、表1に示す配合にて、燃焼灰にグルコン酸を主成分とするセメント用凝結遅延剤(GCPケミカルズ製、商品名;リカバー)を添加し造粒物を製造した。
次に、得られた造粒物に温度計測センサーを挿入し、硬化反応に伴う発熱の経時変化を確認した。
また、比較例1として、セメント用凝結遅延剤を添加しなかった他は同様に操作して造粒物を製造し、硬化反応に伴う発熱の経時変化を確認した。
Example 1
Table 1 is a table showing the addition amount and ratio of combustion ash, water, and a set retarder for cement for the test. FIG. 1 is a diagram showing the change over time in the heat generation associated with the curing reaction when a cement retarder is used as the additive of the present invention, and FIG. 2 shows the change over time in the crushing strength of the present invention. It is a figure.
As Experimental Example 1-3, a granulated product was produced by adding a cement retarder (manufactured by GCP Chemicals, trade name: Recover) mainly composed of gluconic acid to combustion ash in the formulation shown in Table 1.
Next, a temperature measurement sensor was inserted into the obtained granulated product, and the change over time in heat generation accompanying the curing reaction was confirmed.
Further, as Comparative Example 1, a granulated product was produced in the same manner except that the cement setting retarder was not added, and the change over time in heat generation due to the curing reaction was confirmed.

Figure 2019181354
Figure 2019181354

その結果、図1に示すように、セメント用凝結遅延剤の添加量に応じて造粒物の発熱ピークが遅延することが分かる。つまり、硬化反応が遅延していることが分かる。
また、図2に示すように、一定時間毎に養生中の造粒物の圧壊強度を測定した結果、比較例1、及び凝結遅延剤添加量の少ない実験例1に比べて、セメント用凝結遅延剤の添加量が多い実験例2、実験例3では添加割合が多いほど圧壊強度の発現が遅れていることが分かる。
As a result, as shown in FIG. 1, it can be seen that the exothermic peak of the granulated product is delayed according to the amount of the cement setting retarder added. That is, it can be seen that the curing reaction is delayed.
Moreover, as shown in FIG. 2, as a result of measuring the crushing strength of the granulated product during curing at regular intervals, the setting delay for cement was compared with Comparative Example 1 and Experimental Example 1 in which the setting amount of the setting retarder was small. It can be seen that in Experimental Examples 2 and 3 in which the amount of the agent added is large, the expression of the crushing strength is delayed as the addition ratio increases.

(実施例2)
表2は、試験に対して燃焼灰、水、廃糖蜜の添加量と割合を示した表である。また、図3は、図1の添加物に廃糖蜜を用いた際の硬化反応に伴う発熱の経時変化を示した図である。
実験例4−5として、高速攪拌型造粒ミキサ(商品名:ペレガイアVZ−100、株式会社北川鉄工所製)を使用し、表2に示す配合にて燃焼灰にスクロースを主成分とする廃糖蜜(日本甜菜製糖株式会社製)を添加し、造粒物を製造した。
次に、得られた造粒物に温度計測センサーを挿入し、硬化反応に伴う発熱の経時変化を確認した。
また、比較例2として、廃糖蜜を添加しなかった他は同様に操作して造粒物を製造し、硬化反応に伴う発熱の経時変化を確認した。
(Example 2)
Table 2 is a table showing the amount and ratio of combustion ash, water, and molasses for the test. FIG. 3 is a graph showing the change over time in the heat generated by the curing reaction when molasses is used as the additive in FIG.
As Experimental Example 4-5, a high-speed agitation type granulation mixer (trade name: Pelegaia VZ-100, manufactured by Kitagawa Iron Works Co., Ltd.) is used, and waste containing sucrose as a main component in combustion ash with the composition shown in Table 2 Molasses (manufactured by Nippon Sugar Sugar Co., Ltd.) was added to produce a granulated product.
Next, a temperature measurement sensor was inserted into the obtained granulated product, and the change over time in heat generation accompanying the curing reaction was confirmed.
Further, as Comparative Example 2, a granulated product was produced in the same manner except that the molasses was not added, and the change over time in heat generation due to the curing reaction was confirmed.

Figure 2019181354
Figure 2019181354

その結果、図3に示すように、廃糖蜜の添加量に応じて造粒物の発熱ピークが遅延することが分かる。つまり、硬化反応が遅延していることが分かる。
実際に造粒処理から5.5時間経過後の養生中の比較例2の造粒物は一体化し、シャベルの先端が貫入しなかったが、実験例5の造粒物はシャベルの先端が貫入し、ハンドリングの良い状態に崩すことが出来た。
As a result, as shown in FIG. 3, it can be seen that the exothermic peak of the granulated product is delayed according to the amount of molasses added. That is, it can be seen that the curing reaction is delayed.
Actually, the granulated product of Comparative Example 2 during curing after the elapse of 5.5 hours after the granulation treatment was integrated and the tip of the shovel did not penetrate, but the granulated product of Experimental Example 5 penetrated the tip of the shovel. And it was able to break into a good handling condition.

(実施例3)
表3は、試験に対して造粒配合、遅延剤希釈用の水、表面付着用凝結遅延剤を示した表、表4は、試験に対して9.5mmの篩を通過した造粒物の割合を夫々示した表である。
実験例6として、表3に示す造粒配合にて粒径3mm〜10mm程度からなる造粒物を作製した後、実験例6として造粒に必要な水量の1%の水で希釈したセメント用凝結遅延剤(GCPケミカルズ製、商品名;リカバー)を造粒物の表面に噴霧した。これをφ100mm円筒形の容器に充填し24時間養生した後、脱型し、1mの高さから落下させ、9.5mm篩で篩った後の網下質量の割合を測定した。尚、セメント用凝結遅延剤を付着させないものを同様に処理し、比較例3とした。
(Example 3)
Table 3 shows the granulation composition, water for diluting the retarder, and setting retarder for surface adhesion for the test, and Table 4 shows the granulated product that passed through the 9.5 mm sieve for the test. It is the table | surface which showed the ratio, respectively.
As Experimental Example 6, a granulated product having a particle size of about 3 mm to 10 mm was prepared with the granulation composition shown in Table 3, and then as Experimental Example 6, diluted with 1% of the amount of water required for granulation A setting retarder (manufactured by GCP Chemicals, trade name: Recover) was sprayed on the surface of the granulated product. This was filled in a φ100 mm cylindrical container and cured for 24 hours, then demolded, dropped from a height of 1 m, and sieved with a 9.5 mm sieve, and the ratio of the mass under the net was measured. In addition, the thing which does not attach the setting retarder for cement was processed similarly, and it was set as the comparative example 3.

Figure 2019181354
Figure 2019181354

その結果、表4に示すように本発明の実験例6では、9.5mmの篩を通過した造粒物の割合が比較例3よりも高く、造粒物同士の固着が抑制されていた。   As a result, as shown in Table 4, in Experimental Example 6 of the present invention, the ratio of the granulated material that passed through the 9.5 mm sieve was higher than that of Comparative Example 3, and the adhesion between the granulated materials was suppressed.

Figure 2019181354
Figure 2019181354

以上のように、本実施形態によれば、造粒物の硬化反応を任意の時間に遅延させることが可能となり、造粒物同士の固着防止のために頻繁に行わざるを得ない重機等による造粒堆積物の崩し作業を自由な時間に設定出来るようになる。
更に、可溶性の糖あるいはカルボン酸等の有機化合物の使用量によって、造粒物の硬化反応を抑制することができ、肥料、融雪剤等の様に適度な崩壊性が必要な造粒物の製造が行いやすくなる。
また、一旦造粒物とした後に、該造粒物の表面に付着させるように可溶性の糖あるいはカルボン酸系有機化合物を添加することで、造粒物自体の強度に影響を与えることなく造粒物同士の固着を防止することができ、更に添加する可溶性の糖あるいはカルボン酸系有機化合物の使用量を抑えることが可能となる。
As described above, according to the present embodiment, it is possible to delay the curing reaction of the granulated product at an arbitrary time, and due to heavy machinery or the like that must be frequently performed to prevent the granulated product from sticking to each other. It will be possible to set the granulation sediment breaking work at a free time.
Furthermore, the amount of organic compounds such as soluble sugars or carboxylic acids used can suppress the curing reaction of the granulated product, and it is possible to produce a granulated product that requires moderate disintegration such as fertilizer and snow melting agent. Is easier to do.
In addition, once a granulated product is formed, a soluble sugar or a carboxylic acid organic compound is added so as to adhere to the surface of the granulated product, so that the granulated product does not affect the strength of the granulated product itself. It is possible to prevent sticking between objects, and it is possible to further reduce the amount of soluble sugar or carboxylic acid organic compound to be added.

Claims (2)

燃焼灰や製鋼ダスト等の自硬性を有する粉体材料を造粒固化処理する方法において、
前記粉体材料に可溶性の糖あるいはカルボン酸等の有機化合物を添加して造粒物を混合造粒する工程1と、
前記工程1のあとに、前記造粒物に対して物理的作用を加える工程2と、からなり、
前記工程1によって、前記造粒物の硬化反応の進行を任意の時間に遅延させ、
前記工程2によって、さらに、前記造粒物同士の固着を防止することを特徴とする粉体材料の造粒固化方法。
In the method of granulating and solidifying a powder material having self-hardening properties such as combustion ash and steelmaking dust,
Step 1 of mixing and granulating a granulated product by adding an organic compound such as a soluble sugar or carboxylic acid to the powder material;
After the step 1, comprising a step 2 of applying a physical action to the granulated product,
By the step 1, the progress of the curing reaction of the granulated product is delayed to an arbitrary time,
The method of granulating and solidifying a powder material, characterized in that the step 2 further prevents the granules from sticking to each other.
燃焼灰や製鋼ダスト等の自硬性を有する粉体材料を造粒固化処理する方法において、
前記粉体材料を造粒物に造粒する工程3と、
前記工程3によって、造粒された前記造粒物の表面に可溶性の糖及びカルボン酸等の有機化合物を付着させる工程4と、
前記工程4のあとに、前記造粒物に対して物理的作用を加える工程5と、からなり、
前記工程4によって、前記造粒物の表面の硬化反応の進行を任意の時間に遅延させ、
前記工程5によって、さらに、造粒物同士の固着を防止することを特徴とする粉体材料の造粒固化方法。
In the method of granulating and solidifying a powder material having self-hardening properties such as combustion ash and steelmaking dust,
Step 3 of granulating the powder material into a granulated product,
A step 4 of attaching an organic compound such as a soluble sugar and a carboxylic acid to the surface of the granulated product granulated by the step 3;
After the step 4, the step 5 of applying a physical action to the granulated product,
By the step 4, the progress of the curing reaction on the surface of the granulated product is delayed to an arbitrary time,
The method of granulating and solidifying a powder material, wherein the step 5 further prevents adhesion between the granulated materials.
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Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54162674A (en) * 1978-06-15 1979-12-24 Sanyo Kokusaku Pulp Co Ltd Treating method for incinerated ash containing heavy metal
JPH08243527A (en) * 1995-01-09 1996-09-24 Mitsubishi Chem Corp Production of coal ash granule
JP2011235248A (en) * 2010-05-12 2011-11-24 Taki Chem Co Ltd Method for manufacturing granular poultry droppings combustion ash

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS54162674A (en) * 1978-06-15 1979-12-24 Sanyo Kokusaku Pulp Co Ltd Treating method for incinerated ash containing heavy metal
JPH08243527A (en) * 1995-01-09 1996-09-24 Mitsubishi Chem Corp Production of coal ash granule
JP2011235248A (en) * 2010-05-12 2011-11-24 Taki Chem Co Ltd Method for manufacturing granular poultry droppings combustion ash

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