JPH11347514A - Manufacture of granular sulfer solidification molded material - Google Patents

Manufacture of granular sulfer solidification molded material

Info

Publication number
JPH11347514A
JPH11347514A JP10154768A JP15476898A JPH11347514A JP H11347514 A JPH11347514 A JP H11347514A JP 10154768 A JP10154768 A JP 10154768A JP 15476898 A JP15476898 A JP 15476898A JP H11347514 A JPH11347514 A JP H11347514A
Authority
JP
Japan
Prior art keywords
sulfur
vibration
kneaded
solidified
granular
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.)
Pending
Application number
JP10154768A
Other languages
Japanese (ja)
Inventor
Terutaka Imaoka
照隆 今岡
Yoshimasa Igari
俶将 猪狩
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Tanaka Iron Works Co Ltd
Original Assignee
Tanaka Iron Works Co Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Tanaka Iron Works Co Ltd filed Critical Tanaka Iron Works Co Ltd
Priority to JP10154768A priority Critical patent/JPH11347514A/en
Publication of JPH11347514A publication Critical patent/JPH11347514A/en
Pending legal-status Critical Current

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Abstract

PROBLEM TO BE SOLVED: To improve a handling property in the case where a granular sulfur solidification molded material is used as an aggregate or the like for a building material by continuously feeding a melted sulfur kneaded mixture containing a treated material such as incineration ash or the like and sulfur to a vibration transfer means, the mixture is allowed to spring up on a vibration base, and transferred to be molded granularly by solidification while it is divided into sections. SOLUTION: A raw material mixture containing a material to be treated and sulfur is kneaded by heating by a kneader 11, and an obtained melted sulfur kneaded mixture is supplied to a vibration granulator 2 through a hopper 1. The vibration granulator 2 is placed on a trestle 10 via four springs 5, and the whole of the equipment is vibrated since a vibrator 4 in the vibration granulator 2 is vibrated. The melted sulfur kneaded mixture fed onto a vibration base 3 in the vibration granulator 2 receives vibration, and is granulated while it is moved in the direction of an outlet 6. Thereafter, the granulated sulfur solidification molded product is discharged from the outlet 6, and stored in a receiving bag 12. Further, in this case, cold wind is sent from a cooling machine 7, and the melted sulfur kneaded mixture in the vibration granulator 2 is cooled through a pipe 8.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、製鋼スラグ、製鋼
ダスト等その他の産業廃棄物、またはポリ塩化ビフェニ
ル類(PCB)、ポリ塩化ジベンゾパラジオキシン類
(PCDD)等の有機塩素化合物その他の有害物質を含
む焼却灰、媒塵、飛灰等を硫黄で固化封鎖することによ
り無害化し、再利用可能な硫黄固化成形物を製造する方
法に関する。さらに詳しくは本発明は、硫黄固化成形物
の製造にあたり、固化前の流動性を有する状態から直接
所望の粒径を有する粒状の硫黄固化成形物を製造する方
法に関する。
The present invention relates to a steelmaking slag, a steelmaking dust and other industrial wastes, or an organic chlorine compound such as polychlorinated biphenyls (PCB) and polychlorinated dibenzoparadioxins (PCDD) and other harmful substances. The present invention relates to a method for producing a reusable sulfur-solidified product by solidifying and sealing incineration ash, dust, fly ash, and the like containing sulfur. More specifically, the present invention relates to a method for producing a granular sulfur-solidified product having a desired particle size directly from a state having fluidity before solidification in the production of a sulfur-solidified product.

【0002】[0002]

【従来の技術】従来、そのまま廃棄されていた製鋼スラ
グ、製鋼ダスト等その他の産業廃棄物の有効活用及びそ
の減少を図る観点から、またはPCB(ポリ塩化ビフェ
ニル類)等の人体に有害な物質を含む焼却灰、媒塵等を
無害化し有害物質の溶出を防止するとの観点から、この
ような産業廃棄物や焼却灰等を、所定の条件下において
溶融硫黄と混練した後固化封鎖し、重金属、PCB等の
有害物質を溶出させない硫黄固化物の製造方法が提供さ
れている(特開平8−318244号等)。この硫黄固
化物を再利用するには、適当な成形品として提供するの
が好ましいが、工業的に実施しうる適当な方法は、これ
まで開発されていない。考えうる方法としては産業廃棄
物や焼却灰等を硫黄と混練して得た溶融硫黄混練物を、
型ワクに流し込み塊状にして固化させて、硫黄固化物を
得る方法がある。しかしこの方法は生産効率が劣るとい
う難点がある。また、硫黄固化物を建築材料等にしよう
とする場合には、運搬の便宜、取扱上の観点から、一度
塊状に成形された固化物を破砕機で砕き、その後篩い等
で粒度を調整する必要があった。そのためこの方法は、
一度溶融硫黄混練物を固化させた後再度粉砕するため無
駄なエネルギーが必要であった。さらには適度な粒径に
するには粉砕した後篩いにより分級しなければならず、
所望の範囲、サイズを有する硫黄固化物を得るのが容易
ではなく、得られた破砕品も望ましくない扁平なものが
多かった。図3は、この従来の破砕の説明図である。原
料混合物は混練機31で混練され、ホッパー32から成
形トロリ33を介して成形型34に供給される。成形型
34で成形された成形品は破砕機35で破砕され、振動
篩機36で篩い分けされる。そして、所定の粒径以下の
破砕品はベルトコンベア38に乗せられる。一方所定の
粒径以上の破砕品はベルトコンベア37を通じて破砕機
35に戻されて再度破砕されるのである。このようにし
て得られた破砕品39は表面積の大きな凹凸のあるもの
であり、また粉状のかなり小さな粒径のものも含まれ
る。ところで上記の硫黄固化物の別の製造方法として、
溶融硫黄混練物を混練した状態のまま電動フルイ等を通
過させた後、水中に投入して固化(水砕)させて成形す
る方法が考えられる。しかしこの方法によると、一度固
化したものを破砕機で砕く工程は省かれるものの、得ら
れた硫黄固化物の粒径は、一定ではなく、さらに分級す
る必要があった。また水中投入時に有害物質が水中に溶
出するおそれも懸念された。そこで、上記方法のような
破砕又は分級する工程を経ることなく、容易に所望の粒
径になるように溶融硫黄混練物を固化し成形する硫黄固
化成形物の製造方法の開発が望まれていた。
2. Description of the Related Art From the viewpoint of effective use and reduction of other industrial waste such as steelmaking slag, steelmaking dust, and the like, which have been discarded as they are, or substances harmful to the human body such as PCB (polychlorinated biphenyls). From the viewpoint of detoxifying incinerated ash, dust and the like and preventing elution of harmful substances, such industrial waste and incinerated ash are kneaded with molten sulfur under predetermined conditions, then solidified and sealed, and heavy metals, There has been provided a method for producing a solidified sulfur product that does not elute harmful substances such as PCB (Japanese Patent Application Laid-Open No. 8-318244). In order to reuse this sulfur solidified product, it is preferable to provide it as a suitable molded article, but no suitable method that can be implemented industrially has been developed so far. As a possible method, a molten sulfur kneaded material obtained by kneading industrial waste or incinerated ash with sulfur,
There is a method in which a solidified product is obtained by pouring into a mold wax and solidifying it. However, this method has a disadvantage that the production efficiency is inferior. In addition, when the sulfur solidified material is to be used as a building material, it is necessary to crush the once solidified material with a crusher and then adjust the particle size using a sieve or the like from the viewpoint of convenience of transportation and handling. was there. So this method
Wasted energy was required because the molten sulfur kneaded material was once solidified and then pulverized again. Furthermore, in order to obtain an appropriate particle size, it must be classified by sieving after crushing,
It was not easy to obtain a sulfur solidified product having a desired range and size, and the obtained crushed products were often undesirably flat. FIG. 3 is an explanatory view of this conventional crushing. The raw material mixture is kneaded by a kneader 31 and supplied from a hopper 32 to a molding die 34 via a molding trolley 33. The molded product formed by the forming die 34 is crushed by a crusher 35 and sieved by a vibrating sifter 36. Then, the crushed product having a predetermined particle size or less is placed on the belt conveyor 38. On the other hand, the crushed product having a predetermined particle size or more is returned to the crusher 35 through the belt conveyor 37 and crushed again. The crushed product 39 thus obtained has irregularities having a large surface area, and also includes a powder having a very small particle size. By the way, as another method for producing the above-mentioned sulfur solidified product,
A method is conceivable in which the molten sulfur-kneaded material is passed through an electric sieve or the like in a kneaded state, and then poured into water to be solidified (water granulated) and molded. However, according to this method, although the step of crushing the solidified product once using a crusher is omitted, the particle size of the obtained sulfur-solidified product is not constant and needs to be further classified. There was also a concern that harmful substances could be eluted into water when injected into water. Therefore, it has been desired to develop a method for producing a sulfur-solidified molded product in which the molten sulfur-kneaded product is easily solidified and formed so as to have a desired particle size without undergoing a crushing or classifying step as in the above method. .

【0003】[0003]

【発明が解決しようとする課題】従って本発明は、産業
廃棄物や焼却灰等の被処理物を溶融硫黄と混練して得ら
れる、有害物質の溶出を防止する硫黄固化成形物を製造
するにあたり、余分な操作を経ることなく溶融硫黄混練
物を固化し、所望の粒径を有する硫黄固化成形物を得る
ことができる製造方法を提供することを目的とする。
Accordingly, the present invention relates to a method for producing a sulfur-solidified molded product obtained by kneading an object to be treated such as industrial waste or incinerated ash with molten sulfur and preventing elution of harmful substances. It is an object of the present invention to provide a production method capable of solidifying a molten sulfur kneaded product without performing an extra operation to obtain a sulfur-solidified molded product having a desired particle size.

【0004】[0004]

【課題を解決するための手段】すなわち本発明は、
(1)産業廃棄物や焼却灰等の被処理物及び硫黄を含有
する原料混合物を加熱混練して得た流動性溶融硫黄混練
物を、固化、造粒して粒状硫黄固化成形物を製造するに
当たり、前記溶融硫黄混練物を振動移送手段に連続的に
供給し、振動台で溶融硫黄混練物を振動により飛びはね
させ、それを分断させながら移動させ粒状に固化成形す
ることを特徴とする粒状硫黄固化成形物の製造方法、及
び(2)振動移送手段に供給された溶融硫黄混練物を冷
却装置により冷却することを特徴とする(1)項記載の
粒状硫黄固化成形物の製造方法を提供するものである。
That is, the present invention provides:
(1) A fluid molten sulfur kneaded product obtained by heating and kneading an object to be treated such as industrial waste or incinerated ash and a raw material mixture containing sulfur is solidified and granulated to produce a granular sulfur solidified molded product. In this regard, the molten sulfur kneaded material is continuously supplied to a vibrating transfer means, and the molten sulfur kneaded material is splashed off by vibration on a vibrating table, and is moved while dividing and solidified and formed into granules. The method for producing a granular sulfur solidified molded product according to (1), wherein the method for producing the granular sulfur solidified molded product and (2) cooling the molten sulfur kneaded product supplied to the vibration transfer means with a cooling device. To provide.

【0005】[0005]

【発明の実施の形態】以下に本発明を図示の一実施態様
に従って説明する。図1は、本発明の方法に用いうる製
造装置を正面から示した説明図、図2は、図1で示した
装置を側面から示した説明図である。図1中、1はホッ
パーである。11は産業廃棄物、焼却灰等の被処理物と
溶融硫黄の混練機である。混練機11において調製され
た溶融硫黄混練物はホッパー1を通じて振動造粒装置2
に供給される。本発明において用いられる溶融硫黄混練
物は、産業廃棄物、焼却灰等の被処理物及び硫黄を含有
する原料混合物を加熱混練して得たものである。ここで
被処理物には、製鋼スラグ、製鋼ダスト等その他の産業
廃棄物や、PCB(ポリ塩化ビフェニル類)等の人体に
有害な物質を含む焼却灰、媒塵、飛灰、汚染土壌などを
挙げることができ、またこの被処理物中には石炭灰、シ
ュレッダーダストが混入されていてもよい。被処理物の
例については、特公昭62−51440号、同61−1
5759号、同62−15724号、特公平2−496
80号などに記載されているものを用いることができる
がこれらに限定されるものではなく、溶融硫黄と混練さ
れた後固化物を生成するものであればよい。但し、有害
物質の溶出防止の観点から、被処理物の含水量は好まし
くは3重量%以下、さらに好ましくは1重量%以下であ
る。硫黄は、必ずしも高純度のものである必要はなく、
コークス製造、製鉄、石油精製工場などの脱硫工程から
副生する副生硫黄でも良く、天然産の原素状硫黄でも良
い。硫黄と被処理物の比率については特に制限はなく、
被処理物を充分に硫黄で固化封鎖することができる範囲
内であれば良い。また混練は被混練物の温度が、通常9
5〜150℃程度であり、好ましくは最高でも160℃
程度、さらに好ましくは115〜140℃に保たれて行
われる。混練機11は、被処理物に溶融硫黄が充分浸透
するための時間をとることに重点をおいて選定すれば良
く、一軸、二軸又はバッチ式、連続式等どのような形式
でも良い。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described below with reference to an embodiment shown in the drawings. FIG. 1 is an explanatory view showing a manufacturing apparatus that can be used in the method of the present invention from the front, and FIG. 2 is an explanatory view showing the apparatus shown in FIG. 1 from a side. In FIG. 1, reference numeral 1 denotes a hopper. Reference numeral 11 denotes a kneading machine for molten metal and an object to be treated such as industrial waste and incinerated ash. The molten sulfur kneaded material prepared in the kneader 11 is passed through a hopper 1 to a vibrating granulator 2.
Supplied to The molten sulfur kneaded product used in the present invention is obtained by heating and kneading a raw material mixture containing an object to be treated such as industrial waste and incinerated ash and sulfur. The materials to be treated include steelmaking slag, steelmaking dust, and other industrial wastes, incinerated ash, medium dust, fly ash, and contaminated soil containing substances harmful to the human body such as PCBs (polychlorinated biphenyls). In addition, coal ash and shredder dust may be mixed in the object. Examples of the material to be treated are described in JP-B-62-51440 and 61-1.
No. 5759, No. 62-15724, Tokiko 2-496
No. 80 or the like can be used, but the material is not limited thereto, and any material may be used as long as it produces a solid after being kneaded with molten sulfur. However, from the viewpoint of preventing elution of harmful substances, the water content of the object to be treated is preferably 3% by weight or less, more preferably 1% by weight or less. Sulfur does not necessarily have to be of high purity,
Sulfur produced as a by-product from desulfurization processes such as coke production, steelmaking, and oil refining factories may be used, or natural elemental sulfur may be used. There is no particular limitation on the ratio of sulfur to the material to be treated,
What is necessary is just to be in the range which can fully solidify and block the to-be-processed object with sulfur. The temperature of the material to be kneaded is usually 9
About 5 to 150 ° C., preferably at most 160 ° C.
Degree, more preferably kept at 115 to 140 ° C. The kneader 11 may be selected with an emphasis on taking time for the molten sulfur to sufficiently penetrate into the object to be treated, and may be of any type such as a single-shaft, twin-shaft, batch type, or continuous type.

【0006】振動移送手段である振動造粒装置2は、4
本のスプリング5を介して架台10の上に載置されてい
る。振動造粒装置2中の振動子4が振動することによっ
て振動造粒装置2全体が振動する。ホッパー1を通じて
振動造粒装置2中の振動台3上に供給された溶融硫黄混
練物は、振動を受け、振動造粒装置2の出口6方向へ移
動しながら造粒される。その後、造粒された硫黄固化成
形物は出口6から排出され受袋12に納入される。この
過程において、冷却機7から排出された冷風は、パイプ
8を通じて振動造粒装置2に供給され溶融硫黄混練物を
冷却する。その後パイプ9を通り冷却機器7へ戻され
る。本発明の硫黄固化成形物の製造方法では、溶融硫黄
混練物に冷風を当てて冷却すればより多量の粒状硫黄固
化成形物の製造が可能となるため、図1に示した実施態
様のように冷却装置を任意に設置することもできる。振
動造粒装置2中の振動子4は、電動機でアンバランスウ
エイト(偏心ウエイト)を回転させ振動を発生させる構
造よりなり、振動子4が振動することにより振動造粒装
置2、及び振動造粒装置2中の振動台3を振動させる。
振動台3は、溶融硫黄混練物を所望の粒径に造粒するも
のであればどのような構造をしていてもよい。ここでは
ベルトコンベア構造を有し、振動台自体がモーターで動
くものを用いている。ホッパー1から振動台の上に供給
された溶融硫黄混練物は振動台上をベルトコンベアにし
たがって出口6方向に移動する。この間、振動台自体が
振動造粒装置2とともに振動するため、溶融硫黄混練物
は出口6に移動するまでに振動を受けて造粒される。振
動台に与えられる振動は、要求する硫黄固化成形物の平
均粒径によって相違するが、好ましくは、上下方向の振
幅が、0.2〜0.5cm、またその振動数は30〜6
0サイクル/秒である。振動台上で溶融硫黄混練物が振
動を受ける時間は、好ましくは、1〜3分である。振動
時間が短かすぎると造粒、固化が不十分であり、所定の
粒径を有する硫黄固化成形物が製造できない。また、あ
まり長く振動を与えても造粒、固化はすでに終了してお
り電気代等が無駄になる。なお、図1では、振動台は水
平に設置されているが、傾斜させることも可能である。
なお、図4は、図3に示した従来の製造方法と本発明の
製造方法を対比するために表した、本発明の製造方法の
概略を示した説明図である。被処理物及び硫黄を含有す
る原料混合物は混練機41で混練され溶融硫黄混練物と
なり、ホッパー42から振動造粒装置43に供給され
る。振動造粒装置43は振動子44を有している。溶融
硫黄混練物は振動造粒装置43において硫黄固化成形物
に造粒成形される。46はベルトコンベア45から送ら
れたきた粒状硫黄固化成形物である。
[0006] The vibration granulating device 2 serving as a vibration transfer means has a 4
It is placed on a gantry 10 via a book spring 5. When the vibrator 4 in the vibration granulator 2 vibrates, the whole vibration granulator 2 vibrates. The molten sulfur kneaded material supplied to the vibrating table 3 in the vibrating granulator 2 through the hopper 1 is vibrated and granulated while moving toward the outlet 6 of the vibrating granulator 2. Thereafter, the granulated sulfur-solidified product is discharged from the outlet 6 and delivered to the receiving bag 12. In this process, the cool air discharged from the cooler 7 is supplied to the vibrating granulator 2 through the pipe 8 to cool the molten sulfur kneaded material. Thereafter, it is returned to the cooling device 7 through the pipe 9. In the method for producing a sulfur-solidified molded product of the present invention, if the molten sulfur-kneaded product is cooled by blowing cold air, a larger amount of granular sulfur-solidified molded product can be produced, as in the embodiment shown in FIG. A cooling device can be optionally installed. The vibrator 4 in the vibrating granulator 2 has a structure in which an unbalanced weight (eccentric weight) is rotated by an electric motor to generate vibration, and the vibrator 4 vibrates. The vibration table 3 in the device 2 is vibrated.
The shaking table 3 may have any structure as long as it can granulate the molten sulfur kneaded product to a desired particle size. Here, a belt conveyor structure is used, and the vibration table itself is driven by a motor. The molten sulfur kneaded material supplied from the hopper 1 onto the shaking table moves in the direction of the outlet 6 on the shaking table along the belt conveyor. During this time, the vibrating table itself vibrates together with the vibrating granulator 2, so that the molten sulfur kneaded material is vibrated and granulated before moving to the outlet 6. The vibration given to the shaking table varies depending on the required average particle size of the sulfur-solidified product, but preferably, the amplitude in the vertical direction is 0.2 to 0.5 cm, and the frequency is 30 to 6 cm.
0 cycles / sec. The time during which the molten sulfur kneaded material is vibrated on the shaking table is preferably 1 to 3 minutes. If the vibration time is too short, granulation and solidification are insufficient, and a solidified sulfur product having a predetermined particle size cannot be produced. In addition, even if the vibration is applied for an excessively long time, the granulation and solidification have already been completed, and the electricity cost and the like are wasted. In FIG. 1, the vibrating table is installed horizontally, but may be inclined.
FIG. 4 is an explanatory view showing the outline of the manufacturing method of the present invention, in order to compare the conventional manufacturing method shown in FIG. 3 with the manufacturing method of the present invention. The raw material mixture containing the material to be treated and sulfur is kneaded by a kneader 41 to form a kneaded molten sulfur product, which is supplied from a hopper 42 to a vibrating granulator 43. The vibrating granulator 43 has a vibrator 44. The molten sulfur kneaded material is granulated and formed into a sulfur solidified molded product in the vibration granulator 43. Numeral 46 is a granular sulfur solidified molded product sent from the belt conveyor 45.

【0007】本発明の方法により粒状硫黄固化成形物が
容易に製造できる理由は次のように考えられる。振動台
は上下方向に振動するため、振動台上の溶融硫黄混練物
は、振動台から飛び上がり空中に浮いた状態となる。す
ると、溶融硫黄混練物は表面張力により球状になろうと
する。また、振動台上でも溶融硫黄混練物はころがり丸
くなろうとするのである。溶融硫黄混練物はこのように
して、振動造粒装置2の出口6に移動するまでの間に徐
々に粒状化し硬化する。本発明に用いられる溶融硫黄混
練物は、従来の方法で製造した場合、すなわち溶融硫黄
混練物を成形型に流し込み固化した硫黄固化物を、破砕
機で破壊、粉砕して粉体とした場合にも、所定の被処理
物を所定の温度で加熱混練した場合には、有害物質の水
中への溶出がないことがすでに確認されている。しかし
ながら、破砕機の機械的切断力によって硫黄固化物を破
壊して調製する従来の製造方法によれば、機械的切断に
よって、溶融硫黄と接触していない被処理物の内部が表
面にむき出しになる恐れがある。一方、本発明の方法に
おいては、破砕機等による機械的切断力は全く加えられ
ない。本発明の方法では溶融硫黄混練物の丸くなろうと
する表面張力を利用して造粒しているため、製造された
硫黄固化物の表面は硫黄に覆われたものとなるのであ
る。加えて、上記の従来の方法によれば、生成する硫黄
固化物は表面形状が複雑で表面積の大きなものとなるの
に対して、本発明の方法によって生成する粒状硫黄固化
成形物は球状のきれいな表面を有し、表面積の小さな成
形品となるのである。
The reason why a granular sulfur-solidified product can be easily produced by the method of the present invention is considered as follows. Since the shaking table vibrates in the vertical direction, the molten sulfur kneaded material on the shaking table jumps from the shaking table and floats in the air. Then, the molten sulfur kneaded material tends to be spherical due to surface tension. Also, the molten sulfur kneaded material tends to roll on the shaking table. In this way, the molten sulfur kneaded material is gradually granulated and hardened before moving to the outlet 6 of the vibrating granulator 2. When the molten sulfur kneaded product used in the present invention is manufactured by a conventional method, that is, when the molten sulfur kneaded material is poured into a mold and solidified, the sulfur solidified product is broken by a crusher, and crushed into powder. However, it has already been confirmed that no harmful substances are eluted into water when a predetermined object is heated and kneaded at a predetermined temperature. However, according to the conventional manufacturing method in which the sulfur solidified material is broken and prepared by the mechanical cutting force of the crusher, the inside of the object to be processed that is not in contact with the molten sulfur is exposed to the surface by the mechanical cutting. There is fear. On the other hand, in the method of the present invention, no mechanical cutting force is applied by a crusher or the like. In the method of the present invention, since the granulation is performed using the surface tension of the molten sulfur kneaded product that tends to round, the surface of the produced sulfur solidified product is covered with sulfur. In addition, according to the conventional method described above, the resulting solidified sulfur product has a complicated surface shape and a large surface area, whereas the granular solidified sulfur product formed by the method of the present invention has a spherical clean shape. The molded product has a surface and a small surface area.

【0008】[0008]

【実施例】次に本発明を実施例に基づきさらに詳細に説
明するが、本発明は以下の実施例に限定されるものでは
ない。 実施例1 次に示す被処理物及び硫黄を用い、溶融硫黄混練物を調
製した。 1)製鋼スラグ: 転炉灰と称されるものを、500g
用いた。 粒径・・・・・4.0〜0.25mmの徐冷スラグ(I
D−C3) 水分・・・・・3%以下 かさ比重・・・2.04g/cm2 T−Fe・・・58.8% 2)製鋼ダスト: 400g用いた。 粒径・・・・・1.0〜0.25mmの磁選粉(LD−
OB) 水分・・・・・3%以下 かさ比重・・・1.82g/cm2 T−Fe・・・59.8% 3)硫黄は石油精製の脱硫硫黄で、純度99.5%以上
のものを400g使用した。水分は含有されていない。 上記被処理物及び硫黄を120±130℃にて20分間
混練した。得られた溶融硫黄混練物を溶融硫黄混練物a
とした。次に溶融硫黄混練物aは、以下に示した条件に
従い、造粒して粒状硫黄固化成形物(試料A〜C)を製
造した。
EXAMPLES Next, the present invention will be described in more detail with reference to examples, but the present invention is not limited to the following examples. Example 1 A molten sulfur kneaded product was prepared using the following processing object and sulfur. 1) Steelmaking slag: 500 g of what is called converter ash
Using. Grain size: Slowly cooled slag of 4.0 to 0.25 mm (I
D-C3) Water: 3% or less Bulk specific gravity: 2.04 g / cm 2 T-Fe: 58.8% 2) Steelmaking dust: 400 g was used. Particle size: Magnetic separation powder of 1.0 to 0.25 mm (LD-
OB) Moisture: 3% or less Bulk specific gravity: 1.82 g / cm 2 T-Fe: 59.8% 3) Sulfur is desulfurized sulfur from petroleum refining and has a purity of 99.5% or more. 400 g were used. Contains no moisture. The object and the sulfur were kneaded at 120 ± 130 ° C. for 20 minutes. The obtained molten sulfur kneaded material was converted to a molten sulfur kneaded material a.
And Next, the molten sulfur kneaded product a was granulated according to the following conditions to produce granular sulfur solidified molded products (samples A to C).

【0009】[0009]

【表1】 [Table 1]

【0010】得られた硫黄固化成形物の粒径を測定した
ところ、試料A、B、Cの平均粒径は、各々12mm、
15mm、18mmであり、略球状の比較的そろった粒
子であった。粒子の表面は凹凸が少なくなめらかであり
きれいなものであった。また、被処理物の粒子の露出も
みられず良好な粒状硫黄固化成形物が得られた。
When the particle size of the obtained sulfur solidified molded product was measured, the average particle size of Samples A, B and C was 12 mm, respectively.
The particles were 15 mm and 18 mm, and were substantially spherical and relatively uniform particles. The surface of the particles was smooth with little irregularities and clean. In addition, the particles of the object to be treated were not exposed, and a good granular solidified sulfur product was obtained.

【0011】[0011]

【発明の効果】本発明の粒状硫黄固化成形物の製造方法
は、固化前の流動性溶融硫黄混練物から直接所望の粒径
を有する粒状硫黄固化成形物を製造することができ、破
砕、ふるい分け等の工程を省くことができる。さらに、
本発明の粒状硫黄固化成形物の製造方法により製造され
た硫黄固化成形物は、被処理物が粒体表面に露出してお
らず、有害物質の封鎖効果も優れる。また、この硫黄固
化成形物は、粒径のそろった表面のなめらかな略球状の
粒子であるため、建設資材の原料、例えば骨材等として
用いる場合に扱いやすい、性能の優れたものとなる。
According to the method for producing a granular sulfur solidified molded product of the present invention, a granular sulfur solidified molded product having a desired particle size can be produced directly from a fluidized molten sulfur kneaded product before solidification, and it is crushed and sieved. And other steps can be omitted. further,
In the sulfur-solidified molded product produced by the method for producing a granular sulfur-solidified molded product of the present invention, the object to be treated is not exposed on the surface of the granular material, and the harmful substance sealing effect is excellent. In addition, since the sulfur-solidified molded product is a smooth, substantially spherical particle having a uniform particle size on the surface, it is easy to handle when used as a raw material of a construction material, for example, an aggregate, and has excellent performance.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の方法を実施するに好適な粒状硫黄固化
成形物の製造装置の一例を正面から示した説明図であ
る。
FIG. 1 is an explanatory view showing an example of a manufacturing apparatus of a granular sulfur solidified molded product suitable for carrying out a method of the present invention from the front.

【図2】本発明の方法を実施するに好適な粒状硫黄固化
成形物の製造装置の一例を側面から示した説明図であ
る。
FIG. 2 is an explanatory view showing an example of an apparatus for producing a granular sulfur-solidified product suitable for carrying out the method of the present invention from the side.

【図3】従来の製造方法の概略を示した説明図である。FIG. 3 is an explanatory view schematically showing a conventional manufacturing method.

【図4】本発明の製造方法の概略を示した説明図であ
る。
FIG. 4 is an explanatory view schematically showing a manufacturing method of the present invention.

【符号の説明】[Explanation of symbols]

1、42 ホッパー 2、43 振動造粒装置 3 振動台 4、44 振動子 5 スプリング 6 出口 7 冷却機 8、9 パイプ 10 架台 11、41 混練機 46 粒状硫黄固化成形物 DESCRIPTION OF SYMBOLS 1, 42 Hopper 2, 43 Vibration granulator 3 Vibration table 4, 44 Vibrator 5 Spring 6 Outlet 7 Cooler 8, 9 Pipe 10 Stand 11, 41 Kneader 46 Granular sulfur solidified molded product

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 産業廃棄物や焼却灰等の被処理物及び硫
黄を含有する原料混合物を加熱混練して得た流動性溶融
硫黄混練物を、固化、造粒して粒状硫黄固化成形物を製
造するに当たり、前記溶融硫黄混練物を振動移送手段に
連続的に供給し、振動台で溶融硫黄混練物を振動により
飛びはねさせ、それを分断させながら移動させ粒状に固
化成形することを特徴とする粒状硫黄固化成形物の製造
方法。
1. A fluidized sulfur kneaded product obtained by heating and kneading an object to be treated such as industrial waste or incinerated ash and a raw material mixture containing sulfur is solidified and granulated to obtain a granular sulfur solidified molded product. In manufacturing, the molten sulfur kneaded material is continuously supplied to a vibrating transfer means, and the molten sulfur kneaded material is vibrated by a vibrating table by vibrating, and is moved while dividing and solidified and formed into granules. A method for producing a granular sulfur solidified molded product.
【請求項2】 振動移送手段に供給された溶融硫黄混練
物を冷却装置により冷却することを特徴とする請求項1
記載の粒状硫黄固化成形物の製造方法。
2. The molten sulfur kneaded material supplied to the vibration transfer means is cooled by a cooling device.
A method for producing the granular sulfur-solidified molded product as described above.
JP10154768A 1998-06-03 1998-06-03 Manufacture of granular sulfer solidification molded material Pending JPH11347514A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10154768A JPH11347514A (en) 1998-06-03 1998-06-03 Manufacture of granular sulfer solidification molded material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10154768A JPH11347514A (en) 1998-06-03 1998-06-03 Manufacture of granular sulfer solidification molded material

Publications (1)

Publication Number Publication Date
JPH11347514A true JPH11347514A (en) 1999-12-21

Family

ID=15591477

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10154768A Pending JPH11347514A (en) 1998-06-03 1998-06-03 Manufacture of granular sulfer solidification molded material

Country Status (1)

Country Link
JP (1) JPH11347514A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITMI20110668A1 (en) * 2011-04-19 2012-10-20 Claudio Paolo Cecchini PROCEDURE FOR THE PREPARATION OF SULFUR BASES
JP2016042059A (en) * 2014-08-18 2016-03-31 真一郎 樫村 Radioactive waste disposal method
KR102291899B1 (en) * 2021-03-24 2021-08-19 김철희 Activated carbon cooling vibration transfer device

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
ITMI20110668A1 (en) * 2011-04-19 2012-10-20 Claudio Paolo Cecchini PROCEDURE FOR THE PREPARATION OF SULFUR BASES
WO2012143388A3 (en) * 2011-04-19 2012-12-27 Ausy S.R.L. Procedure for the preparation of sulphur-based articles of manufacture
CN103608286A (en) * 2011-04-19 2014-02-26 奥西有限公司 Procedure for the preparation of sulphur-based articles of manufacture
US8894720B2 (en) 2011-04-19 2014-11-25 Ausy S.R.L. Procedure for the preparation of sulphur-based articles of manufacture
JP2016042059A (en) * 2014-08-18 2016-03-31 真一郎 樫村 Radioactive waste disposal method
KR102291899B1 (en) * 2021-03-24 2021-08-19 김철희 Activated carbon cooling vibration transfer device

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