JPH11333423A - Method and apparatus for disposal of industrial waste - Google Patents

Method and apparatus for disposal of industrial waste

Info

Publication number
JPH11333423A
JPH11333423A JP10279772A JP27977298A JPH11333423A JP H11333423 A JPH11333423 A JP H11333423A JP 10279772 A JP10279772 A JP 10279772A JP 27977298 A JP27977298 A JP 27977298A JP H11333423 A JPH11333423 A JP H11333423A
Authority
JP
Japan
Prior art keywords
industrial waste
mixture
granules
raw material
solution
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
JP10279772A
Other languages
Japanese (ja)
Inventor
Nobuyasu Kubota
信康 窪田
Hiroto Yamashita
弘外 山下
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.)
HOKURIKU SOKEN KK
Original Assignee
HOKURIKU SOKEN KK
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 HOKURIKU SOKEN KK filed Critical HOKURIKU SOKEN KK
Priority to JP10279772A priority Critical patent/JPH11333423A/en
Publication of JPH11333423A publication Critical patent/JPH11333423A/en
Pending legal-status Critical Current

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  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)
  • Glanulating (AREA)

Abstract

PROBLEM TO BE SOLVED: To allow a hazardous substance to be hardly eluted from an industrial waste by a method wherein a cement and a water glass solution are added to a raw material of the industrial waste, stirred to prepare a muddy mixture, many granular bodies are formed by rounding the mixture, and the granular body is dried and hardened. SOLUTION: A raw material 1 of an industrial waste is transported upward with a case conveyor 2, the raw material 1 is cast into a hopper 3, and fed to a vibration screen 5 with a cutting out conveyor 4. After adjusting a particle size, it is cast into a mixer 7 with a flow conveyor 6, and a cement from an adding mouth C and a water glass solution from a sprayer 19 are added thereto. They are stirred to prepare a muddy mixture 8, the mixture 8 is rounded with a pan type granulating machine 10 to form many granular bodies 9, and the granular body 9 is dried in a drying room 12 to be hardened. Thereby, the granular body 9 can be made to a stabilized state wherein the hazardous substance is difficult to be eluted.

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】この発明は、焼却処理場に持
ち込まれたゴミを燃やした際に生成される焼却灰や、焼
却炉の煙突に設けたフィルターで捕捉されたばいじん、
或いは、下水処理場に溜まる汚泥等の有害な産業廃棄物
を無害に安定化するための処理方法及び処理装置に関す
る。
BACKGROUND OF THE INVENTION The present invention relates to incineration ash generated when burning garbage brought into an incineration plant, soot and dust trapped by a filter provided in a chimney of an incinerator,
Alternatively, the present invention relates to a treatment method and a treatment apparatus for stably stabilizing harmful industrial waste such as sludge accumulated in a sewage treatment plant.

【0002】[0002]

【従来の技術】上記した種類の産業廃棄物は、水銀、カ
ドミウム、鉛、PCB等の有害物質が含まれているの
で、そのまま埋立てると、溶出による公害が発生するお
それがある為、無害に安定化してから埋め立てがなされ
るよう法定されている。また、焼却灰やばいじんは、そ
の重さの割に容量が大きく、処分する際には減量化する
ことが望まれている。
2. Description of the Related Art Industrial wastes of the type described above contain harmful substances such as mercury, cadmium, lead, and PCBs. It is statutory that landfills will be made after stabilization. In addition, incinerated ash and soot have a large capacity in spite of their weight, and it is desired to reduce the volume when disposing of them.

【0003】[0003]

【発明が解決しようとする課題】本発明は上記実情に鑑
みて成されたものであり、その目的とするところは、産
業廃棄物を有害物質が殆ど溶出しない安定した状態にな
し、しかも、焼却灰やばいじんの減量化にも適する産業
廃棄物の処理方法及び処理装置を提供することである。
DISCLOSURE OF THE INVENTION The present invention has been made in view of the above-mentioned circumstances, and an object of the present invention is to produce industrial waste in a stable state in which harmful substances hardly elute, and to incinerate it. An object of the present invention is to provide a method and an apparatus for treating industrial waste that are suitable for reducing ash and dust.

【0004】[0004]

【課題を解決するための手段】請求項1に記載した産業
廃棄物の処理方法の発明は、粉状体、又は泥状体からな
る産業廃棄物の原料にセメントと水ガラス溶液とを添加
し、攪拌することによって泥状の混合体となし、混合体
を丸めて多数の粒状体を形成し、該粒状体を乾燥して硬
化させることを特徴とする。ここで言う粉状体とは焼却
灰や、ばいじんのことであり、また、泥状体とは下水処
理場に溜まる汚泥のことである。水ガラス溶液とは、水
ガラスを噴霧に適した粘度となるように希釈したもので
ある。
According to a first aspect of the present invention, there is provided a method for treating industrial waste, comprising adding cement and a water glass solution to a raw material of an industrial waste consisting of a powder or a mud. The method is characterized in that a muddy mixture is formed by stirring, the mixture is rolled to form a large number of granules, and the granules are dried and hardened. Here, the powdery material refers to incineration ash and soot and dust, and the muddy material refers to sludge accumulated in a sewage treatment plant. The water glass solution is obtained by diluting water glass to have a viscosity suitable for spraying.

【0005】混合体は丸まり易いように、水分の保有率
を適度なレベルに保持することが必要であり、混合体自
体の水分保有率が多い場合には適度なレベルになるまで
乾燥させる。原料にセメントと水ガラス溶液とを混合す
ると、セメントが水ガラス溶液から凝結、硬化の条件と
しての水和反応に要する水分を奪い、逆に、水ガラス溶
液が脱水されるので、セメントと水ガラスとが原料を固
める結合材としての能力を素早く得る。
[0005] In order to easily curl the mixture, it is necessary to maintain the water retention at an appropriate level, and when the mixture itself has a high water retention, the mixture is dried to an appropriate level. When cement and water glass solution are mixed with the raw materials, the cement condenses from the water glass solution and removes the water required for the hydration reaction as a condition for hardening, and conversely, the water glass solution is dehydrated. Quickly obtains the ability as a binder to solidify the raw material.

【0006】請求項1記載の発明では、原料にセメント
と水ガラス溶液とを添加したが、請求項2記載の発明の
ように、セメントと水ガラス溶液に代えて、シリコンオ
イル溶液と酢酸ビニル系樹脂溶液を用いても良い。
In the first aspect of the present invention, cement and water glass solution are added to the raw materials. However, as in the second aspect of the present invention, instead of the cement and water glass solution, a silicon oil solution and a vinyl acetate system are used. A resin solution may be used.

【0007】このようにすれば、酢酸ビニル系樹脂溶液
によって原料を固め、シリコンオイルによって撥水性が
得られることとなるので、硬化させた粒状体が水分を含
み難くなる。
In this case, the raw material is hardened by the vinyl acetate resin solution, and water repellency is obtained by the silicone oil, so that the hardened granular material hardly contains moisture.

【0008】請求項1記載の発明では、原料とセメント
と水ガラス溶液とからなる泥状の混合体を丸めて、多数
の粒状体を形成し、該粒状体を乾燥して硬化させる手法
を用いていたが、請求項3記載の発明のように、粉状
体、又は泥状体からなる産業廃棄物の原料にセメントと
水ガラス溶液とを添加し、攪拌することによって泥状の
混合体となし、混合体を丸めて多数の粒状体を形成し、
該粒状体に水ガラス溶液を噴霧して粒状体の表面をコー
ティングした後に、乾燥して硬化させても良い。
According to the first aspect of the present invention, a method is used in which a mud-like mixture composed of a raw material, cement, and a water glass solution is rolled to form a large number of granules, and the granules are dried and hardened. However, as in the invention according to claim 3, the cement and the water glass solution are added to the raw material of the industrial waste consisting of the powder or the mud, and the mixture is mixed with the mud-like mixture by stirring. None, the mixture is rolled to form numerous granules,
After spraying a water glass solution onto the granules to coat the surfaces of the granules, the granules may be dried and cured.

【0009】請求項2記載の発明では、原料とシリコン
オイル溶液と酢酸ビニル系樹脂溶液とからなる泥状の混
合体を丸めて、多数の粒状体を形成し、該粒状体を乾燥
して硬化させる手法を用いていたが、請求項4記載の発
明のように、粉状体、又は泥状体からなる産業廃棄物の
原料にシリコンオイル溶液と酢酸ビニル系樹脂溶液とを
添加し、攪拌することによって泥状の混合体となし、混
合体を丸めて多数の粒状体を形成し、該粒状体にシリコ
ンオイル溶液を噴霧して粒状体の表面をコーティングし
た後に、乾燥して硬化させても良い。
According to the second aspect of the present invention, a mud-like mixture composed of a raw material, a silicon oil solution and a vinyl acetate resin solution is rolled to form a large number of granules, and the granules are dried and cured. However, a silicon oil solution and a vinyl acetate resin solution are added to the raw material of the industrial waste consisting of a powdery substance or a muddy substance and stirred, as in the invention according to claim 4. By forming a muddy mixture by this, the mixture is rolled to form a number of granules, and the granules are sprayed with a silicon oil solution to coat the surfaces of the granules, and then dried and cured. good.

【0010】請求項3記載の発明と、請求項4記載の発
明の場合には、粒状体の表面には産業廃棄物の原料が全
く露出しない形態となる。
In the case of the invention described in claim 3 and the invention described in claim 4, the form is such that the raw material of industrial waste is not exposed at all on the surface of the granular material.

【0011】請求項5記載の産業廃棄物の処理装置は、
粉状体、又は泥状体からなる産業廃棄物の原料を選別機
を通して粒度を調整し、該原料とセメントと水ガラス溶
液、または原料とシリコンオイル溶液と酢酸ビニル系樹
脂溶液を、ミキサー中に投入して泥状の混合体を形成
し、該混合体をパン型造粒機に投入して多数の粒状体を
形成し、粒状体を乾燥室を通過させて、粒状体を硬化さ
せることを特徴とする。
[0011] The apparatus for treating industrial waste according to claim 5 comprises:
The raw material of the industrial waste consisting of powder or mud is adjusted through a separator to adjust the particle size, and the raw material and cement and water glass solution, or the raw material, silicon oil solution and vinyl acetate resin solution are mixed in a mixer. To form a muddy mixture, and to put the mixture into a pan-type granulator to form a large number of granules, pass the granules through a drying chamber, and cure the granules. Features.

【0012】請求項6記載の産業廃棄物の処理装置は、
パン型造粒機には、粒状体に水ガラス溶液、または、シ
リコンオイル溶液を吹き付ける噴霧装置を設けてあるこ
とを特徴とする。なお、粒状体の材料に、原料とセメン
トと水ガラス溶液を用いた場合には、粒状体に水ガラス
溶液を吹き付け、材料に、原料とシリコンオイル溶液と
酢酸ビニル系樹脂溶液を用いた場合には、粒状体にシリ
コンオイル溶液を吹き付ける。
[0012] The apparatus for treating industrial waste according to claim 6 comprises:
The bread-type granulator is characterized in that a spraying device for spraying a water glass solution or a silicon oil solution on the granules is provided. In addition, when the raw material, cement and water glass solution are used for the material of the granular material, the water glass solution is sprayed on the granular material, and when the raw material, the silicon oil solution and the vinyl acetate resin solution are used for the material, Sprays a silicon oil solution on the granules.

【0013】[0013]

【発明の実施の形態】この発明の産業廃棄物の処理装置
は、図1に示すように、産業廃棄物の原料1をケースコ
ンベヤー2で上方に運び、ケースコンベヤー2の後部下
側に、原料1を投入するホッパー3を備えた切出コンベ
ヤー4の前端部を設け、切出コンベヤー4の後部下側
に、原料1の粒度調整のための選別機となる振動スクリ
ーン5を配置し、振動スクリーン5の下方に原料1を移
動させるフローコンベヤー6の前端部を設け、フローコ
ンベヤー6の後端部下方にミキサー7の前端部を配置
し、ミキサー7の後端部下方に、ミキサー7から落下す
る泥状の混合体8を多数の粒状体9にするパン型造粒機
10を設け、パン型造粒機10の下方に、パン型造粒機
10から溢れ出た多数の粒状体9を移動させるコンベヤ
ー11を備えた乾燥室12の前端部を配置し、さらに、
乾燥室12の後部下方に、乾燥した粒状体9を移送する
製品用コンベヤー13の前端部を設けてある。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS As shown in FIG. 1, an industrial waste treatment apparatus according to the present invention transports a raw material 1 of industrial waste upward by a case conveyor 2 and feeds the raw material 1 to a lower rear portion of the case conveyor 2. 1 is provided with a front end of a cutting conveyor 4 provided with a hopper 3 into which the raw material 1 is charged, and a vibrating screen 5 serving as a sorter for adjusting the particle size of the raw material 1 is arranged below a rear portion of the cutting conveyor 4. The front end of the flow conveyor 6 for transferring the raw material 1 is provided below the mixer 5, the front end of the mixer 7 is disposed below the rear end of the flow conveyor 6, and the mixer 7 falls from the mixer 7 below the rear end of the mixer 7. A bread granulator 10 for converting the mud-like mixture 8 into a large number of granules 9 is provided, and the large number of granules 9 overflowing from the bread granulator 10 are moved below the bread granulator 10. Drying room with conveyor 11 The second front end portion is disposed, further,
At the lower rear of the drying chamber 12, a front end of a product conveyor 13 for transferring the dried granules 9 is provided.

【0014】振動スクリーン5は、網を振動させること
によって粒度調整をするもので、直径10mm程度の原
料が通過するようにしてある。
The vibrating screen 5 adjusts the particle size by vibrating a mesh, and allows a raw material having a diameter of about 10 mm to pass therethrough.

【0015】フローコンベヤー6には、後端部にセメン
トの添加口Cが設けられており、そのため、原料1とと
もにセメントがミキサー7に投入されるが、添加口Cの
位置は別の箇所であっても良い。
The flow conveyor 6 is provided with an addition port C for cement at the rear end, so that the cement is charged into the mixer 7 together with the raw material 1, but the location of the addition port C is different. May be.

【0016】ミキサー7にはパドルミキサーが使用され
る。これは、図2に示すように、互いに反対方向に回る
一対の軸14,14にブレード15,l5,が螺旋方向
に配列されている。
As the mixer 7, a paddle mixer is used. As shown in FIG. 2, the blades 15, 15 are spirally arranged on a pair of shafts 14, 14 rotating in opposite directions.

【0017】ケース16は、風洞状であって、前側にフ
ローコンベヤー5から落下する原料1の投入口17を設
け、後端に排出口18が下向きに垂設されている。さら
に、ケース16の中間部には、水ガラス溶液を添加する
噴霧装置19が設けられ、原料1とセメントと水ガラス
溶液が攪拌されつつケースl6内を移動して排出口18
に向かう。
The case 16 has a wind tunnel shape, and is provided with an inlet 17 for the raw material 1 falling from the flow conveyor 5 on the front side, and a discharge port 18 hanging downward at the rear end. Further, a spraying device 19 for adding a water glass solution is provided at an intermediate portion of the case 16, and the raw material 1, the cement and the water glass solution are moved inside the case 16 while being stirred, and the discharge port 18 is
Head for.

【0018】また、ケースl6においては、前側に灯油
バーナーによる熱風の取入口20を設け、後側に熱風の
放出口21を設けてある。そして、熱風が混合体8に均
一に当るように、取入口20にはファンによる撹絆装置
が内蔵される。
Further, in the case 16, a hot air intake 20 by a kerosene burner is provided on the front side, and a hot air discharge port 21 is provided on the rear side. Then, a stirrer with a fan is built in the inlet 20 so that the hot air can uniformly hit the mixture 8.

【0019】パン型造粒機10は図4に示すように、傾
斜するパン22の上部にボトムスクレーパー23とサイ
ドスクレーパー24とを支持する横架材25を有してお
り、横架材25に水ガラス溶液の噴霧装置26が設けて
ある。噴霧装置26の位置について詳しく言えば、パン
22の回転作用によって粒状体9が上がる側に設けてあ
り、水ガラス溶液のコーティングを均一になしやすくし
てある。
As shown in FIG. 4, the bread-type granulator 10 has a horizontal member 25 for supporting a bottom scraper 23 and a side scraper 24 on an upper part of an inclined pan 22. A water glass solution spray device 26 is provided. More specifically, the position of the spraying device 26 is provided on the side where the granules 9 are raised by the rotating action of the pan 22, thereby facilitating uniform coating of the water glass solution.

【0020】乾燥室12は、粒状体中の水分を飛ばして
粒状体自体を硬化させる役割を果たすもので、その構造
は風洞形でその中にメッシュのベルトコンべヤー11を
通してあり、前側に熱風の取入口27を設けると共に、
後側に放出口28を設けてある。パン型造粒機10にお
いては、傾斜するパン22の下端から粒状体9が溢れ出
るので、その下方にコンベヤー11の前端部を臨ませて
ある。また、コンベヤー11の後端部が製品用コンベヤ
ー13に臨ませてあって、全体的に連続運転がなされ
る。
The drying chamber 12 plays a role of blowing water out of the granules and hardening the granules themselves. The drying chamber 12 has a wind tunnel shape and a mesh belt conveyer 11 therein. In addition to providing an intake 27,
A discharge port 28 is provided on the rear side. In the bread-type granulator 10, since the granular material 9 overflows from the lower end of the inclined bread 22, the front end of the conveyor 11 faces the lower side. In addition, the rear end of the conveyor 11 faces the product conveyor 13, and continuous operation is performed as a whole.

【0021】完成品である粒状体9については、図3に
示すように、丸まった粒形に成形され、大きさは5〜1
5mm程度の玉で、その表面がコーティング層29で覆
われた形態となっており、乾燥室12を通る間にコーテ
ィング層29が硬化するので、表面が硬く粘着しない取
り扱いやすい状態になる。なお、原料としては、ばいじ
んや焼却灰を用いた。ちなみに、材料の割合について
は、重量比で、灰l0に対して、セメント1〜1.5、
水ガラス溶液(水25%、苛性ソーダ25%、けい酸ソ
ーダ50%のもの)0.5〜1.5が好適であったこと
が、実験結果より得られた。
As shown in FIG. 3, the granular material 9 as a finished product is formed into a rounded granular shape and has a size of 5-1.
The ball is about 5 mm, and the surface is covered with the coating layer 29. Since the coating layer 29 is hardened while passing through the drying chamber 12, the surface is hard and does not stick, so that it is easy to handle. In addition, soot and incinerated ash were used as raw materials. By the way, as for the ratio of the materials, cement 1 to 1.5,
Experimental results showed that 0.5 to 1.5 water glass solution (25% water, 25% caustic soda, 50% sodium silicate) was suitable.

【0022】本発明の産業廃棄物の処理装置は、上記実
施形態に限定されるものではない。たとえば、産業廃棄
物の原料1は上記したように、焼却灰、ばいじん、汚泥
等であって、基本的にこれらは性状や水分濃度が異なっ
ているから、セメントや水ガラス溶液の割合、さらに、
ミキサー7中の加熱乾燥の有無等は、その性状等によっ
て適当に設定する。また、水ガラス溶液の成分割合は、
その性状等の他、セメントの割合とも勘案して設定され
る。そして、セメントに要する水がこの水ガラス溶液に
よって供給されるので、セメントの硬化条件として必ず
しも水の添加は要しない。
The industrial waste treatment apparatus of the present invention is not limited to the above embodiment. For example, as described above, the raw material 1 of industrial waste is incinerated ash, dust, sludge, and the like. Since these are basically different in properties and water concentrations, the ratio of cement or water glass solution,
The presence or absence of heating and drying in the mixer 7 is appropriately set according to the properties and the like. The component ratio of the water glass solution is
It is set in consideration of the ratio of cement in addition to its properties. And since the water required for cement is supplied by this water glass solution, addition of water is not necessarily required as a setting condition of cement.

【0023】上記した実施形態は、原料に対して添加口
Cからセメントを投入し、噴霧装置19,26で水ガラ
ス溶液を添加する手法であったが、それに限らず、原料
に対して添加口Cから酢酸ビニル系樹脂溶液を投入し、
噴霧装置19,26でシリコンオイル溶液を添加する手
法であっても良い。この場合、材料の割合については、
重量比で、灰l0に対して、シリコンオイル溶液(シリ
コンオイル1:水3)0.7〜1.0、酢酸ビニル系樹
脂溶液(エチレン酢酸ビニール合成高分子エマルジョン
1:水2)0.2〜0.3が好適であったことが、実験
結果より得られた。なお、エチレン酢酸ビニール合成高
分子エマルジョンとしては、たとえば日本化成株式会社
から販売されている商品名、NSハイフレックスHF−
1000を用いる。
In the above-described embodiment, the cement is supplied to the raw material from the addition port C, and the water glass solution is added by the spraying devices 19 and 26. However, the present invention is not limited to this. Inject vinyl acetate resin solution from C,
A method of adding a silicon oil solution with the spray devices 19 and 26 may be used. In this case, for the proportion of material,
Silicon oil solution (silicone oil 1: water 3) 0.7-1.0, vinyl acetate resin solution (ethylene vinyl acetate synthetic polymer emulsion 1: water 2) 0.2 to ash 10 in weight ratio It was obtained from the experimental result that 0.3 was preferable. As the ethylene-vinyl acetate synthetic polymer emulsion, for example, a product name sold by Nippon Kasei Co., Ltd., NS Hyflex HF-
1000 is used.

【0024】[0024]

【発明の効果】以上説明したように、請求項1記載の発
明によれば、粒状体の表面には、産業廃棄物の原料だけ
でなく、水ガラスとセメントが露出した形態となってい
るので、粒状体は有害物質が溶出し難い安定した状態に
なる。また、産業廃棄物の原料に焼却灰やばいじんの粉
状体を用いた場合は、かさばる粉状体がセメントと水ガ
ラス溶液を添加した状態で攪拌されることから、混合体
は恰も圧縮されたかのように高密度な状態となり、その
混合体から形成される粒状体も同様に高密度な状態とな
るので、かさばる粉状体を減量化に適した形態にするこ
とができる。
As described above, according to the first aspect of the present invention, not only the raw material of industrial waste but also water glass and cement are exposed on the surface of the granular material. As a result, the granular material is in a stable state in which harmful substances are hardly eluted. Also, when powdered incineration ash or dust is used as a raw material for industrial waste, the bulky powder is stirred with the cement and water glass solution added. As described above, the high-density state is obtained, and the granules formed from the mixture also have the high-density state, so that the bulky powder can be formed into a form suitable for weight reduction.

【0025】また、請求項2記載の発明によれば、粒状
体の表面には、産業廃棄物の原料だけでなく、シリコン
オイルと酢酸ビニル系樹脂溶液が露出した形態となり、
シリコンオイルに備わる撥水性によって、粒状体内に水
が入り込み難くなるので、粒状体は有害物質が溶出し難
い安定した状態になる。
According to the second aspect of the present invention, not only raw materials of industrial waste but also silicon oil and a vinyl acetate resin solution are exposed on the surface of the granular material,
The water repellency of the silicone oil makes it difficult for water to enter the granular material, so that the granular material is in a stable state in which harmful substances are hardly eluted.

【0026】請求項3記載の発明は、粒状体の表面に水
ガラス溶液を噴霧してあることから、粒状体の表面は水
ガラスで完全に覆われた形態となるので、有害物質が全
く溶出しない安定したものにすることができる。
According to the third aspect of the present invention, since the surface of the granular material is sprayed with the water glass solution, the surface of the granular material is completely covered with the water glass. Not stable can be.

【0027】請求項4記載の発明は、粒状体の表面がシ
リコンオイルで完全に覆われた形態となるので、有害物
質が全く溶出しない安定したものにすることができる。
According to the fourth aspect of the present invention, since the surface of the granular material is completely covered with the silicone oil, it is possible to stably prevent harmful substances from being eluted at all.

【0028】請求項5記載の発明は、粒状体の材料に原
料とセメントと水ガラス溶液を用いれば、請求項1記載
の発明と同じ効果が得られ、粒状体の材料に原料とシリ
コンオイル溶液と酢酸ビニル系樹脂溶液を用いれば、請
求項2記載の発明と同じ効果が得られる。
According to a fifth aspect of the present invention, the same effects as those of the first aspect are obtained by using a raw material, cement, and a water glass solution as the material of the granular material, and the raw material and the silicon oil solution are used as the material of the granular material. If the vinyl acetate resin solution is used, the same effect as that of the second aspect can be obtained.

【0029】請求項6に記載した発明は、原料とセメン
トと水ガラス溶液とから粒状体を形成した場合に水ガラ
ス溶液を噴霧すれば、請求項3記載の発明と同じ効果が
得られ、原料とシリコンオイル溶液と酢酸ビニル系樹脂
溶液とから粒状体を形成した場合にシリコンオイル溶液
を噴霧すれば、請求項4記載の発明と同じ効果が得られ
る。
According to a sixth aspect of the present invention, the same effect as the third aspect of the invention can be obtained by spraying a water glass solution when granules are formed from a raw material, cement and a water glass solution. If the silicon oil solution is sprayed when the granular material is formed from the silicone oil solution and the vinyl acetate-based resin solution, the same effect as the invention of claim 4 can be obtained.

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

【図1】この発明による産業廃棄物の処理装置を全体的
に示す説明図である。
FIG. 1 is an explanatory view showing an entire industrial waste treatment apparatus according to the present invention.

【図2】産業廃棄物の処理装置におけるミキサーの縦断
面図である。
FIG. 2 is a longitudinal sectional view of a mixer in the industrial waste treatment apparatus.

【図3】粒状体の断面図である。FIG. 3 is a sectional view of a granular material.

【図4】パン型造粒機に噴霧装置を取付ける箇所を拡大
して示す図面である。
FIG. 4 is an enlarged view showing a place where a spraying device is attached to a bread granulator.

【符号の説明】[Explanation of symbols]

1 原料 5 選別機(振動スクリーン) 7 ミキサー 8 混合体 9 粒状体 10 パン型造粒機 12 乾燥室 26 噴霧装置 DESCRIPTION OF SYMBOLS 1 Raw material 5 Sorting machine (vibrating screen) 7 Mixer 8 Mixture 9 Granular material 10 Bread granulator 12 Drying room 26 Sprayer

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 FI B09B 3/00 301M 301R ──────────────────────────────────────────────────続 き Continued on the front page (51) Int.Cl. 6 Identification code FI B09B 3/00 301M 301R

Claims (6)

【特許請求の範囲】[Claims] 【請求項1】 粉状体、又は泥状体からなる産業廃棄物
の原料(1)にセメントと水ガラス溶液とを添加し、攪
拌することによって泥状の混合体(8)となし、混合体
(8)を丸めて多数の粒状体(9,9,…)を形成し、
該粒状体(9,9,…)を乾燥して硬化させることを特
徴とする産業廃棄物の処理方法。
Cement and a water glass solution are added to a raw material (1) of an industrial waste consisting of a powder or a mud, and the mixture is stirred to form a mud-like mixture (8). The body (8) is rolled to form a number of granular bodies (9, 9, ...),
A method for treating industrial waste, comprising drying and hardening the granules (9, 9, ...).
【請求項2】 セメントと水ガラス溶液に代えて、シリ
コンオイル溶液と酢酸ビニル系樹脂溶液を用いたことを
特徴とする請求項1に記載の産業廃棄物の処理方法。
2. The method for treating industrial waste according to claim 1, wherein a silicon oil solution and a vinyl acetate resin solution are used in place of the cement and water glass solution.
【請求項3】 粉状体、又は泥状体からなる産業廃棄物
の原料(1)にセメントと水ガラス溶液とを添加し、攪
拌することによって泥状の混合体(8)となし、混合体
(8)を丸めて多数の粒状体(9,9,…)を形成し、
該粒状体(9,9,…)に水ガラス溶液を噴霧して粒状
体(9,9,…)の表面をコーティングした後に、乾燥
して硬化させることを特徴とする産業廃棄物の処理方
法。
Cement and a water glass solution are added to a raw material (1) of an industrial waste composed of a powder or a mud, and the mixture is stirred to form a mud-like mixture (8). The body (8) is rolled to form a number of granular bodies (9, 9, ...),
A method for treating industrial waste, comprising spraying a water glass solution onto the granules (9, 9,...) To coat the surfaces of the granules (9, 9,...), Followed by drying and curing. .
【請求項4】 粉状体、又は泥状体からなる産業廃棄物
の原料(1)にシリコンオイル溶液と酢酸ビニル系樹脂
溶液とを添加し、攪拌することによって泥状の混合体
(8)となし、混合体(8)を丸めて多数の粒状体
(9,9,…)を形成し、該粒状体(9,9,…)にシ
リコンオイル溶液を噴霧して粒状体(9,9,…)の表
面をコーティングした後に、乾燥して硬化させることを
特徴とする産業廃棄物の処理方法。
4. A muddy mixture (8) by adding a silicon oil solution and a vinyl acetate resin solution to a raw material (1) of industrial waste consisting of a powdery or muddy body and stirring the mixture. The mixture (8) is rolled to form a large number of granules (9, 9,...), And a silicon oil solution is sprayed on the granules (9, 9,...) To form the granules (9, 9). , ...), and then drying and hardening after coating the surface of the industrial waste.
【請求項5】 粉状体、又は泥状体からなる産業廃棄物
の原料(1)を選別機(5)を通して粒度を調整し、該
原料(1)とセメントと水ガラス溶液、または、原料
(1)とシリコンオイル溶液と酢酸ビニル系樹脂溶液
を、ミキサー(7)中に投入して泥状の混合体(8)を
形成し、該混合体(8)をパン型造粒機(10)に投入
して多数の粒状体(9,9,…)を形成し、粒状体
(9,9,…)を乾燥室(12)を通過させて、粒状体
(9)を硬化させることを特徴とする産業廃棄物の処理
装置。
5. A raw material (1) of an industrial waste consisting of a powdery substance or a muddy substance is adjusted in particle size through a separator (5), and the raw material (1), a cement and a water glass solution, or a raw material (1), a silicone oil solution and a vinyl acetate resin solution are charged into a mixer (7) to form a mud-like mixture (8), and the mixture (8) is mixed with a bread granulator (10). ) To form a number of granules (9, 9,...), Pass the granules (9, 9,...) Through a drying chamber (12), and cure the granules (9). Characteristic industrial waste treatment equipment.
【請求項6】 パン型造粒機(10)には、粒状体
(9)に水ガラス溶液、または、シリコンオイル溶液を
吹き付ける噴霧装置(26)を設けてあることを特徴と
する請求項5記載の産業廃棄物の処理装置。
6. The pan-type granulator (10) is provided with a spray device (26) for spraying a water glass solution or a silicon oil solution on the granules (9). The industrial waste treatment device according to the above.
JP10279772A 1998-03-23 1998-10-01 Method and apparatus for disposal of industrial waste Pending JPH11333423A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10279772A JPH11333423A (en) 1998-03-23 1998-10-01 Method and apparatus for disposal of industrial waste

Applications Claiming Priority (3)

Application Number Priority Date Filing Date Title
JP7420398 1998-03-23
JP10-74203 1998-03-23
JP10279772A JPH11333423A (en) 1998-03-23 1998-10-01 Method and apparatus for disposal of industrial waste

Publications (1)

Publication Number Publication Date
JPH11333423A true JPH11333423A (en) 1999-12-07

Family

ID=26415331

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10279772A Pending JPH11333423A (en) 1998-03-23 1998-10-01 Method and apparatus for disposal of industrial waste

Country Status (1)

Country Link
JP (1) JPH11333423A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2585465A (en) * 2019-05-03 2021-01-13 Gallagher Aggregates Ltd Manufactured aggregate

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5044172A (en) * 1973-08-23 1975-04-21
JPS5212756A (en) * 1975-07-18 1977-01-31 Nichireki Chem Ind Co Ltd Sludge treatment
JPS53132168A (en) * 1977-04-25 1978-11-17 Nichireki Chem Ind Co Method of treating chromium contained burned ash
JPS61212400A (en) * 1985-03-15 1986-09-20 Toshihiro Ijichi Granular composition of paper making sludge adjustable in water resistance

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5044172A (en) * 1973-08-23 1975-04-21
JPS5212756A (en) * 1975-07-18 1977-01-31 Nichireki Chem Ind Co Ltd Sludge treatment
JPS53132168A (en) * 1977-04-25 1978-11-17 Nichireki Chem Ind Co Method of treating chromium contained burned ash
JPS61212400A (en) * 1985-03-15 1986-09-20 Toshihiro Ijichi Granular composition of paper making sludge adjustable in water resistance

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB2585465A (en) * 2019-05-03 2021-01-13 Gallagher Aggregates Ltd Manufactured aggregate
GB2585465B (en) * 2019-05-03 2021-12-22 Gallagher Aggregates Ltd Manufactured aggregate

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