JP2009148713A - Granule, sintered body, and methods for producing them - Google Patents

Granule, sintered body, and methods for producing them Download PDF

Info

Publication number
JP2009148713A
JP2009148713A JP2007329480A JP2007329480A JP2009148713A JP 2009148713 A JP2009148713 A JP 2009148713A JP 2007329480 A JP2007329480 A JP 2007329480A JP 2007329480 A JP2007329480 A JP 2007329480A JP 2009148713 A JP2009148713 A JP 2009148713A
Authority
JP
Japan
Prior art keywords
sludge
granulated
ash
granulation
mass
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
JP2007329480A
Other languages
Japanese (ja)
Inventor
Masaaki Noguchi
雅朗 野口
Hideki Wachi
秀樹 和知
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.)
Taiheiyo Materials Corp
Original Assignee
Taiheiyo Materials Corp
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 Taiheiyo Materials Corp filed Critical Taiheiyo Materials Corp
Priority to JP2007329480A priority Critical patent/JP2009148713A/en
Publication of JP2009148713A publication Critical patent/JP2009148713A/en
Pending legal-status Critical Current

Links

Classifications

    • 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

Landscapes

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

Abstract

<P>PROBLEM TO BE SOLVED: To provide a technique which is simple in granulation and high in waste utility (recycling efficiency) when a waste such as incineration ash, sludge, or construction soil is granulated by adding water for recycling. <P>SOLUTION: Granules contain one or more kinds of materials selected from a group consisting of incineration ash, sludge and construction soil, and a lignin compound. <P>COPYRIGHT: (C)2009,JPO&INPIT

Description

本発明は、造粒体や焼結体に関する。特に、焼却灰、汚泥あるいは建設発生土などの廃棄物を原料とした造粒体や焼結体に関する。   The present invention relates to a granulated body and a sintered body. In particular, the present invention relates to a granulated body and a sintered body made from waste such as incinerated ash, sludge, or construction generated soil.

近年、焼却灰、汚泥や建設発生土の発生量は増大している。そして、簡単に廃棄することも困難になって来ている。従って、前記廃棄物の再利用が各方面で試みられている。しかしながら、廃棄物は品質が安定して無いことから、その再資源化は実に困難である。   In recent years, the amount of incinerated ash, sludge and construction generated soil has increased. And it is becoming difficult to dispose of it easily. Therefore, recycling of the waste is being tried in various directions. However, since the quality of waste is not stable, it is very difficult to recycle it.

さて、焼却灰や建設発生土廃棄物の再利用(再資源化)としては、セメント原料の他にも、コンクリート骨材とか路盤材などの土木材料として利用することが提案されている。例えば、骨材への再資源化は、粉末廃棄物を造粒して、セメント固化や焼成等の工程を経て行なわれる。そして、上記造粒は、そのまま、水を加えるだけでも、造粒できる場合もある。しかしながら、粒径が大きい場合とか、粒度分布が狭い場合には、造粒することが困難となる場合が多い。又、石炭火力発電所の微粉炭燃焼から発生する石炭灰の中、フライアッシュは、粒子が球状である為、そのままでは、造粒できない。   Now, as reuse (recycling) of incineration ash and construction waste soil, it is proposed to use it as a civil engineering material such as concrete aggregate or roadbed material in addition to cement raw materials. For example, recycling to aggregate is performed by granulating powder waste and performing steps such as cement solidification and firing. And the said granulation may be granulated just by adding water as it is. However, when the particle size is large or the particle size distribution is narrow, granulation is often difficult. Moreover, fly ash cannot be granulated as it is because the particles are spherical in the coal ash generated from pulverized coal combustion at a coal-fired power plant.

製紙スラッジ等の廃棄物は、製紙工程や古紙リサイクルの工程から発生し、製紙工程で回収されなかった微細繊維などの有機物や、顔料・染料として利用されているカオリン・タルク・炭酸カルシウム等の無機物から構成される。そして、減量化の為に、製紙スラッジは焼却されることが多い。このように焼却された製紙スラッジ(製紙スラッジ焼却灰)は、現在、工業的に再利用されているものはセメント原料として利用される程度である。そして、残り殆どの量は埋め立て処分されている。尚、骨材としての工業的な利用は殆ど出来ていない。   Waste such as papermaking sludge is generated from the papermaking process and used paper recycling process, and organic substances such as fine fibers that are not recovered in the papermaking process, and inorganic substances such as kaolin, talc, and calcium carbonate that are used as pigments and dyes Consists of And papermaking sludge is often incinerated for weight reduction. As for the papermaking sludge (papermaking sludge incineration ash) thus incinerated, what is currently reused industrially is only used as a cement raw material. And most of the remaining amount is landfilled. In addition, industrial use as an aggregate is hardly made.

又、現在CO排出削減の観点から、カーボンニュートラルである製紙スラッジや木屑などの生物起源の原料を燃料としたバイオマス発電が増加しつつある。そして、バイオマス発電で排出される焼却灰は、品質が安定していないことから、再資源化は、一層、困難である。 In addition, from the viewpoint of reducing CO 2 emissions, biomass power generation using carbon-neutral biogenic raw materials such as paper sludge and wood chips is increasing. And since the quality of incinerated ash discharged by biomass power generation is not stable, recycling is more difficult.

ところで、上記廃棄物の再資源化を図る為、これ等の廃棄物の粉末を造粒することが行なわれる。この造粒には、ロールプレス、パンペレタイザ等が用いられる。この時、原料(粉末)の性状が造粒性に大きく作用する。そして、造粒が非常に困難な場合が多い。特に、パンペレタイザで連続して造粒する場合、原料によっては全く造粒できない場合がある。造粒できても、粒径が大きくなり、コントロールできない等の問題がある。   By the way, in order to recycle the waste, the powder of these wastes is granulated. For this granulation, a roll press, a pan pelletizer, or the like is used. At this time, the properties of the raw material (powder) greatly affect the granulation property. And granulation is often very difficult. In particular, when granulating continuously with a pan pelletizer, it may not be possible to granulate at all depending on the raw material. Even if it can be granulated, the particle size becomes large and there is a problem that it cannot be controlled.

さて、従来からも、造粒技術が幾つか提案されている。
例えば、石炭灰の粒度調整が不要で、比較的最大粒径の大きい石炭灰を使用できると共に、造粒方法の種類によらず強度の高い造粒品が得られ、焼成温度範囲が広い為に運転が容易な人工軽量骨材を得る為、下水汚泥焼却灰に、石炭灰を全体に占める割合が重量比10%乃至80%となるように混合したものを原料とし、該原料を焼成することを特徴とする人工軽量骨材の製造方法が提案(特開平11−35356号公報)されている。
Conventionally, several granulation techniques have been proposed.
For example, there is no need to adjust the particle size of coal ash, and coal ash with a relatively large maximum particle size can be used. In order to obtain an easy-to-operate artificial lightweight aggregate, sewage sludge incinerated ash is mixed with coal ash so that the proportion of coal ash is 10% to 80% by weight, and the raw material is fired. A method of manufacturing an artificial lightweight aggregate characterized by the above has been proposed (Japanese Patent Laid-Open No. 11-35356).

又、灰を固化して、舗装材等の建設資材として有効利用可能な十分な強度を有し、しかも重金属類の溶出の問題のない成形体を安価に製造することを目的として、灰にセメントと水を添加、混合し、得られた混合物を固化成形する方法において、該灰を粉砕処理する方法であって、該灰或いは粉砕灰にセメントと水とカルシウム化合物とを添加、混合することを特徴とする灰の固化成形方法が提案(特開2002−18411号公報)されている。   In addition, ash is cemented for the purpose of solidifying the ash and having a sufficient strength that can be effectively used as a construction material such as pavement, and that does not cause the problem of elution of heavy metals at a low cost. And a method of solidifying and molding the resulting mixture, wherein the ash is pulverized, and cement, water and a calcium compound are added to and mixed with the ash or pulverized ash. A characteristic ash solidification molding method has been proposed (Japanese Patent Laid-Open No. 2002-18411).

又、製紙スラッジ灰の特性若しくは機能性の活用の為、製紙スラッジ灰を主体とする廃棄物リサイクルシステムの構築を実現することを目的として、吸湿の少ない状態の製紙スラッジ灰を微粉砕処理した微粉砕物を加水注水のみにより造粒加工したことを特徴とする製紙スラッジ灰含有造粒物が提案(特開2005−103464号公報)されている。
特開平11−35356号公報 特開2002−18411号公報 特開2005−103464号公報
In addition, in order to utilize the characteristics or functionality of paper sludge ash, finely pulverized paper sludge ash with low moisture absorption for the purpose of establishing a waste recycling system mainly composed of paper sludge ash. A papermaking sludge ash-containing granulated product obtained by granulating a pulverized product with only water injection has been proposed (Japanese Patent Laid-Open No. 2005-103464).
JP-A-11-35356 JP 2002-18411 A JP 2005-103464 A

ところで、これまでも、上述した通り、各種の造粒技術が提案されて来たものの、それでも、造粒が困難な場合が多かった。   By the way, as mentioned above, although various granulation techniques have been proposed, granulation is still difficult in many cases.

従って、本発明が解決しようとする課題は、焼却灰や汚泥、或いは建設発生土などの廃棄物を再資源化する為、水を加えて造粒する場合、その造粒が簡単であり、しかも廃棄物の利用度(再資源化効率)が高い技術を提供することである。   Therefore, the problem to be solved by the present invention is that in order to recycle waste such as incineration ash, sludge, or construction generated soil, granulation with the addition of water is easy and To provide technology with high waste utilization (recycling efficiency).

前記の課題を解決する為の検討が、本発明者によって、鋭意、推し進められて行く中に、リグニン系化合物(リグニンをも含む)を用いると、造粒が容易になり、焼成工程でもすり減り等による骨材の形状が悪化することが抑制できることを見出すに至った。   While studies for solving the above-mentioned problems are being intensively promoted by the present inventor, when a lignin-based compound (including lignin) is used, granulation becomes easy, and it is worn out even in the firing step. As a result, it has been found that the shape of the aggregate caused by the deterioration of the aggregate can be suppressed.

上記知見を基にして本発明がなされたものである。
すなわち、前記の課題は、
焼却灰、汚泥および建設発生土の群の中から選ばれる一種または二種以上の材と、
リグニン系化合物とを含有してなる
ことを特徴とする造粒体によって解決される。
The present invention has been made based on the above findings.
That is, the above problem is
One or more materials selected from the group of incinerated ash, sludge and construction generated soil;
The problem is solved by a granulated body comprising a lignin compound.

特に、焼却灰、汚泥および建設発生土の群の中から選ばれる一種または二種以上の材と、
リグニン系化合物とを含有してなり、
前記材100質量部に対して前記リグニン系化合物は0.1〜10質量部の割合である
ことを特徴とする造粒体によって解決される。
In particular, one or more materials selected from the group of incinerated ash, sludge and construction generated soil,
Containing a lignin compound,
The lignin compound is solved at a ratio of 0.1 to 10 parts by mass with respect to 100 parts by mass of the material.

又、前記の課題は、
焼却灰、汚泥および建設発生土の群の中から選ばれる一種または二種以上の材にリグニン系化合物の水溶液を添加した後、造粒する
ことを特徴とする造粒体の製造方法によって解決される。
In addition, the above problem is
Solved by a method for producing a granulated product, characterized by adding an aqueous solution of a lignin compound to one or more materials selected from the group of incinerated ash, sludge and construction generated soil, followed by granulation. The

特に、焼却灰、汚泥および建設発生土の群の中から選ばれる一種または二種以上の材100質量部に対してリグニン系化合物が0.1〜10質量部の割合となるよう、前記材に対して前記リグニン系化合物の水溶液を添加し、この後で造粒する
ことを特徴とする造粒体の製造方法によって解決される。
In particular, the lignin compound is in a ratio of 0.1 to 10 parts by mass with respect to 100 parts by mass of one or more kinds of materials selected from the group of incinerated ash, sludge and construction generated soil. On the other hand, it is solved by a method for producing a granulated product, characterized in that an aqueous solution of the lignin compound is added and granulated thereafter.

又、前記の課題は、
上記の造粒体が焼成されてなる
ことを特徴とする焼結体によって解決される。
In addition, the above problem is
This is solved by a sintered body characterized in that the granulated body is fired.

又、前記の課題は、
上記の造粒体を650〜1300℃で焼成する
ことを特徴とする焼結体の製造方法によって解決される。
In addition, the above problem is
It solves by the manufacturing method of the sintered compact characterized by baking said granulated body at 650-1300 degreeC.

焼却灰、汚泥および建設発生土の群の中から選ばれる一種または二種以上の廃棄物と共にリグニン系化合物とを用いて造粒してなるので、造粒が非常に容易であった。又、強度向上の為に、造粒体を焼成した場合でも、焼成工程ですり減り等の形状悪化が起き難いものであった。又、強度が大きなものになった。   Since granulation was performed using a lignin compound together with one or more kinds of waste selected from the group of incinerated ash, sludge and construction generated soil, granulation was very easy. Further, even when the granulated body is baked to improve the strength, it is difficult to cause shape deterioration such as wear in the baking process. Also, the strength became large.

本発明は造粒体(造粒物)である。この造粒体は、焼却灰、汚泥および建設発生土の群の中から選ばれる一種または二種以上の材(廃棄物)を含む。特に、単独では造粒が困難な粗い粒度を持つ製紙スラッジ焼却灰などの焼却灰、上下水道から発生する浄水汚泥などの汚泥、及び建設汚泥等の建設発生土の群の中から選ばれる一種または二種以上の材(廃棄物)を含む。かつ、リグニン系化合物を含む。リグニン系化合物の量は、好ましくは、上記材(廃棄物)100質量部に対して0.1〜10質量部(特に、0.2質量部以上。更には、0.3質量部以上。5質量部以下)の割合である。   The present invention is a granulated body (granulated product). This granulated body contains one or more materials (waste) selected from the group of incinerated ash, sludge, and construction generated soil. In particular, a kind selected from the group of incineration ash such as paper sludge incineration ash having a coarse particle size that is difficult to granulate alone, sludge such as purified water sludge generated from water and sewage, and construction generated soil such as construction sludge Contains two or more materials (waste). And a lignin type compound is included. The amount of the lignin-based compound is preferably 0.1 to 10 parts by mass (particularly 0.2 parts by mass or more, and further 0.3 parts by mass or more) with respect to 100 parts by mass of the material (waste). (Parts by mass or less).

又、本発明は造粒体(造粒物)の製造方法である。この製造方法は、上記材(廃棄物)と上記リグニン系化合物とを含む混合物を造粒する方法である。好ましくは、リグニン系化合物を固形の形では無く、溶液の形態で上記材に添加し、そして造粒する方法である。尚、必要に応じて、リグニン系化合物水溶液の添加時あるいはその前後において水を添加し、造粒する方法である。   Moreover, this invention is a manufacturing method of a granulated body (granulated material). This manufacturing method is a method of granulating a mixture containing the material (waste material) and the lignin compound. Preferably, the lignin-based compound is added to the material in the form of a solution, not in a solid form, and granulated. In addition, it is the method of adding and granulating water at the time of the addition of lignin type compound aqueous solution before or after that as needed.

又、本発明は焼結体である。この焼結体は前記造粒体(造粒物)が焼成されたものである。   Moreover, this invention is a sintered compact. This sintered body is obtained by firing the granulated body (granulated product).

又、本発明は焼結体の製造方法である。この焼結体は前記造粒体(造粒物)を焼成するものである。この焼成に際しての温度は、650〜1300℃(特に、800℃以上。1200℃以下)である。   Moreover, this invention is a manufacturing method of a sintered compact. This sintered body fires the granulated body (granulated material). The temperature at the time of firing is 650 to 1300 ° C. (particularly 800 ° C. or more and 1200 ° C. or less).

更に詳しく説明する。
先ず、上記した原料(上記した廃棄物の粉末)と、リグニン系化合物とを用意する。そして、該原料にリグニン系化合物水溶液を添加し、数mm〜十数mm径の造粒物を作成する。この造粒物を650℃以上の温度で焼結させ、人工骨材などとする。
This will be described in more detail.
First, the above-described raw material (the above-mentioned waste powder) and a lignin compound are prepared. And the lignin type compound aqueous solution is added to this raw material, and the granulated material of a diameter of several mm-dozen mm is created. This granulated product is sintered at a temperature of 650 ° C. or higher to obtain an artificial aggregate or the like.

上記造粒には、例えばロールプレス、パンペレタイザ、アイリッヒミキサ等が用いられる。すなわち、上記原料にリグニン系化合物水溶液を添加し、前記造粒機を用いて造粒が行われる。尚、パンペレタイザが用いられて造粒が行なわれると、この造粒物は形状が球形であること、かつ、造粒をコントロールすることで任意の大きさの造粒物が得られる。従って、パンペレタイザを用いた造粒が好ましい。   For the granulation, for example, a roll press, a pan pelletizer, an Eirich mixer or the like is used. That is, a lignin-based compound aqueous solution is added to the raw material, and granulation is performed using the granulator. When granulation is performed using a pan pelletizer, the granulated product has a spherical shape, and a granulated product of an arbitrary size can be obtained by controlling the granulation. Therefore, granulation using a pan pelletizer is preferred.

造粒物の原料である廃棄物は、焼却灰、汚泥、建設発生土が用いられる。これ等の中から一種のみが選ばれて用いられて良く、或いは二種以上が選ばれて用いられても良い。但し、通常は、一種類のものが選ばれて使用されることが好ましい。   Incineration ash, sludge, and construction waste soil are used as the raw material for granulated materials. Only one of these may be selected and used, or two or more may be selected and used. However, it is usually preferred that one type is selected and used.

焼却灰としては、例えば石炭火力発電所の微粉炭燃焼灰、流動層燃焼石炭灰、コークス灰、ごみ焼却灰、下水汚泥焼却灰、製紙スラッジ焼却灰、廃プラスチック焼却灰などが挙げられる。尚、製紙スラッジ焼却灰とは、製紙工程や古紙のリサイクルで発生した汚泥を焼却した灰である。そして、主成分として、Ca,Al等の無機成分を含む。又、薪、木炭、廃材、食品搾りかす等のバイオマス燃料を原料としたバイオマス発電から発生する焼却灰も挙げられる。そして、製紙スラッジ焼却灰などの如く、有機質系原料の焼却灰は、内部に細かな孔(気孔)が存在し、高吸水性(多孔質)の特徴を持つことから、好ましい原料である。すなわち、有機質系原料焼却灰の造粒・焼成物は高吸水性の骨材となることから、有機質系原料の焼却灰を造粒物原料とすることは好ましい。   Examples of the incineration ash include pulverized coal combustion ash, fluidized bed combustion coal ash, coke ash, waste incineration ash, sewage sludge incineration ash, paper sludge incineration ash, and waste plastic incineration ash from coal-fired power plants. The papermaking sludge incineration ash is ash obtained by incinerating sludge generated in the papermaking process or recycling of used paper. And as a main component, inorganic components, such as Ca and Al, are included. In addition, incineration ash generated from biomass power generation using biomass fuel such as firewood, charcoal, waste material, and food pomace is also included. Incinerated ash of organic raw materials, such as papermaking sludge incinerated ash, is a preferred raw material because it has fine pores (pores) inside and has high water absorption (porous) characteristics. That is, since the granulated and fired product of the organic raw material incinerated ash becomes a highly water-absorbing aggregate, it is preferable to use the incinerated ash of the organic raw material as the granulated material.

汚泥としては、例えば浄水汚泥や下水汚泥が挙げられる。好ましくは浄水汚泥が用いられる。   Examples of the sludge include purified water sludge and sewage sludge. Preferably, purified water sludge is used.

建設発生土としては、例えば建設残土、汚染土壌や浚渫土が挙げられる。尚、これ等の中でも、粒子径75μm以下のシルト・粘土質の含有量が70%以上のものであることが好ましい。その理由は、砂分が余りにも多くなり過ぎると、造粒する時の粒径コントロールが困難になったからである。   Examples of construction generated soil include construction residual soil, contaminated soil, and dredged soil. Among these, it is preferable that the content of silt / clay having a particle diameter of 75 μm or less is 70% or more. The reason is that if the amount of sand is too much, it becomes difficult to control the particle size when granulating.

上記各種焼却灰や汚泥や建設発生土は、必要に応じて、粉砕され、そして造粒体の原料とされる。   The above-mentioned various incineration ash, sludge and construction generated soil are pulverized and used as a raw material for the granulated body as necessary.

さて、保水性の高い原料(粉体:粉末)は、通常、造粒性が良好である。
しかしながら、88μm残分の量が30%を越えた原料が用いられると、造粒性は、極端に、悪くなった。その理由は、粒子間を補完する小さな粒子が不足し、粒子間の付着強度が悪くなり、造粒困難になったのであろうと考えられる。しかしながら、このような原料に対してリグニン系化合物水溶液が添加されて造粒が行なわれた場合、造粒性が良好になった。
A raw material having high water retention (powder: powder) usually has good granulation properties.
However, when a raw material in which the amount of the 88 μm residue exceeds 30% is used, the granulation property is extremely deteriorated. The reason for this is thought to be that the lack of small particles that complement each other, resulting in poor adhesion strength between the particles and difficulty in granulation. However, when the lignin-based compound aqueous solution is added to such a raw material and granulation is performed, the granulation property is improved.

又、粘土鉱物が併用されると更に良いものとなった。特に、膨潤力が10ml/2g以上の粘土鉱物が併用されると更に良いものとなった。尚、この種の粘土鉱物の好ましい配合量は、上記廃棄物100質量部に対して3〜30質量部(特に、5〜20質量部)であった。又、他にもセメントを更に用いることも考えられる。   In addition, when a clay mineral was used in combination, it became even better. In particular, when a clay mineral having a swelling power of 10 ml / 2 g or more was used in combination, it became even better. In addition, the preferable compounding quantity of this kind of clay mineral was 3-30 mass parts (especially 5-20 mass parts) with respect to 100 mass parts of the said waste materials. In addition, it is conceivable to further use cement.

さて、造粒物の機械的強度の一層の向上を図る為には、焼成が行なわれる。焼成には、トンネルキルン、ローラーハウスキルン、流動床、ロータリーキルンを用いることが出来る。尚、製造の容易さ等の面から、ロータリーキルンを用いることが好ましい。そして、このような焼成窯で650〜1200℃の温度で焼成すると、強度の高い焼結体(骨材)を得ることが出来る。   In order to further improve the mechanical strength of the granulated product, firing is performed. For firing, a tunnel kiln, a roller house kiln, a fluidized bed, or a rotary kiln can be used. In addition, it is preferable to use a rotary kiln from the viewpoint of ease of manufacture. And if it bakes at the temperature of 650-1200 degreeC with such a baking kiln, a strong sintered body (aggregate) can be obtained.

以下、具体的な実施例を挙げて本発明を説明する。
[実施例]
表−1
試料 廃棄物原料 リグニン ベントナイト
No1 製紙スラッジ焼却灰 0質量部 0質量部
No2 製紙スラッジ焼却灰 0.2質量部 0質量部
No3 製紙スラッジ焼却灰 0.5質量部 0質量部
No4 製紙スラッジ焼却灰 1.0質量部 0質量部
No5 製紙スラッジ焼却灰 1.0質量部 5質量部
No6 シルト乾燥粉末品 0質量部 0質量部
No7 シルト乾燥粉末品 0.5質量部 0質量部
No8 浄水汚泥乾燥粉末品 0質量部 0質量部
No9 浄水汚泥乾燥粉末品 0.5質量部 0質量部
*製紙スラッジ焼却灰はd50%=47.2μm
*シルト(建設発生泥水)乾燥粉末品はシルト・粘土分82%
*浄水汚泥乾燥粉末品はシルト・粘土分75%
*ベントナイトはモンモリロナイトが主成分の膨潤力13ml/2g
主原料として上記廃棄物原料の乾燥粉末(或いはベントナイトとの混合物)を直径800mmのパンペレタイザ中に投入した。そして、これに、リグニン水溶液を、又、場合によっては、水も更に散水装置で噴霧しながら、回転させ、造粒した。尚、必要に応じて、更に、原料を投入しながら連続運転し、造粒した。
Hereinafter, the present invention will be described with specific examples.
[Example]
Table-1
Sample Waste material Lignin Bentonite No. 1 Papermaking sludge incineration ash 0 parts by mass 0 parts by mass No2 Papermaking sludge incineration ash 0.2 parts by mass No3 Papermaking sludge incineration ash 0.5 parts by mass 0 parts by mass No4 Papermaking sludge incineration ash 0 parts by mass 0 parts by mass No5 Papermaking sludge incinerated ash 1.0 part by mass 5 parts by mass No6 Silt dry powder product 0 parts by mass 0 parts by mass No7 Silt dry powder product 0.5 parts by mass 0 parts by mass No8 dry water sludge dry powder product 0 Mass part 0 part by mass No. 9 purified water sludge dry powder product 0.5 part by mass 0 part by mass * The papermaking sludge incineration ash is d50% = 47.2 μm
* Silt (construction mud) dry powder product is 82% silt and clay
* Clean water sludge dry powder product is 75% silt and clay content
* Bentonite is mainly composed of montmorillonite and has a swelling power of 13ml / 2g.
The waste material dry powder (or a mixture with bentonite) as a main material was put into a 800 mm diameter pan pelletizer. Then, the lignin aqueous solution and, in some cases, water was sprayed with a watering device, and the mixture was rotated and granulated. In addition, if necessary, the material was continuously operated and granulated while adding raw materials.

この時、造粒性について調べたので、その結果を表−2に示す。   At this time, since it investigated about granulation property, the result is shown in Table-2.

造粒後、電気炉にて600℃,700℃,1000℃,1200℃の温度で焼成した。そして、この焼成物の圧壊強度を調べたので、その結果を表−2に示す。   After granulation, it was baked at temperatures of 600 ° C., 700 ° C., 1000 ° C., and 1200 ° C. in an electric furnace. And since the crushing strength of this baked product was investigated, the result is shown in Table-2.

表−2
試料 造粒性 圧壊強度(N)
600 700 1000 1200
No1 造粒できず - - - -
No2 造粒できたものの、粒径コントロール難 7 15 15 25
No3 造粒性良好、粒径コントロール可 10 19 23 120
No4 造粒性良好、粒径コントロール可 12 25 28 141
No5 造粒性非常に良好、粒径コントロール可 25 35 51 252
No6 造粒やや難、粒径コントロール不可 - - - -
No7 造粒性良好、粒径コントロール可 13 16 32 171
No8 造粒できたものの、粒径コントロール難 9 12 18 109
No9 造粒性良好、粒径コントロール可 22 28 40 305
Table-2
Sample Granulation Crushing strength (N)
600 700 1000 1200
No1 Can't granulate----
No2 Granulated but difficult to control particle size 7 15 15 25
No3 Good granulation, particle size controllable 10 19 23 120
No4 Good granulation, particle size controllable 12 25 28 141
No. 5 Very good granulation, controllable particle size 25 35 51 252
No6 Granulation slightly difficult, particle size control not possible----
No. 7 Good granulation, particle size controllable 13 16 32 171
No8 Granulated but difficult to control particle size 9 12 18 109
No9 Good granulation, particle size controllable 22 28 40 305

これによれば、本発明になるものは、造粒性が良く、かつ、造粒物を焼成した焼結体の強度が大きなことが判る。

特許出願人 太平洋マテリアル株式会社
代 理 人 宇 高 克 己
According to this, it turns out that what becomes this invention has good granulation property and the intensity | strength of the sintered compact which baked the granulated material is large.

Patent Applicant Taiheiyo Material Co., Ltd.
Representative Katsumi Udaka

Claims (5)

焼却灰、汚泥および建設発生土の群の中から選ばれる一種または二種以上の材と、
リグニン系化合物とを含有してなる
ことを特徴とする造粒体。
One or more materials selected from the group of incinerated ash, sludge and construction generated soil;
A granulated product comprising a lignin compound.
焼却灰、汚泥および建設発生土の群の中から選ばれる一種または二種以上の材と、
リグニン系化合物とを含有してなり、
前記材100質量部に対して前記リグニン系化合物は0.1〜10質量部の割合である
ことを特徴とする造粒体。
One or more materials selected from the group of incinerated ash, sludge and construction generated soil;
Containing a lignin compound,
The granulated product, wherein the lignin compound is in a proportion of 0.1 to 10 parts by mass with respect to 100 parts by mass of the material.
焼却灰、汚泥および建設発生土の群の中から選ばれる一種または二種以上の材にリグニン系化合物の水溶液を添加した後、造粒する
ことを特徴とする造粒体の製造方法。
A method for producing a granulated product comprising adding an aqueous solution of a lignin compound to one or more materials selected from the group of incinerated ash, sludge and construction generated soil, followed by granulation.
請求項1又は請求項2の造粒体が焼成されてなる
ことを特徴とする焼結体。
A sintered body obtained by firing the granulated body according to claim 1 or 2.
請求項1又は請求項2の造粒体を、650〜1300℃で焼成する
ことを特徴とする焼結体の製造方法。
A method for producing a sintered body, comprising calcining the granulated body of claim 1 or 2 at 650 to 1300 ° C.
JP2007329480A 2007-12-21 2007-12-21 Granule, sintered body, and methods for producing them Pending JP2009148713A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2007329480A JP2009148713A (en) 2007-12-21 2007-12-21 Granule, sintered body, and methods for producing them

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2007329480A JP2009148713A (en) 2007-12-21 2007-12-21 Granule, sintered body, and methods for producing them

Publications (1)

Publication Number Publication Date
JP2009148713A true JP2009148713A (en) 2009-07-09

Family

ID=40918541

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2007329480A Pending JP2009148713A (en) 2007-12-21 2007-12-21 Granule, sintered body, and methods for producing them

Country Status (1)

Country Link
JP (1) JP2009148713A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107200385A (en) * 2017-07-18 2017-09-26 甘琦 A kind of method that iron carbon or Fenton sludge prepare porous light electrolysis particle in utilization waste water treatment process
CN113860843A (en) * 2021-10-08 2021-12-31 广州航海学院 Baking-free ceramsite and preparation method thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107200385A (en) * 2017-07-18 2017-09-26 甘琦 A kind of method that iron carbon or Fenton sludge prepare porous light electrolysis particle in utilization waste water treatment process
CN113860843A (en) * 2021-10-08 2021-12-31 广州航海学院 Baking-free ceramsite and preparation method thereof

Similar Documents

Publication Publication Date Title
Ren et al. Recent advances in artificial aggregate production
KR101941319B1 (en) Phosphate fertilizer and method for producing phosphate fertilizer
CN101503643B (en) Solid fuel for sludge anhydration
KR101442689B1 (en) Biomass pellet manufacturing equipment
Lu et al. The different properties of lightweight aggregates with the fly ashes of fluidized-bed and mechanical incinerators
CN106566588A (en) Method for preparing forming fuel by utilizing sludge
JP5131750B2 (en) Granulated body, sintered body, and production method thereof
CN1837335A (en) Hybrid fuel and method for preparing the same
CN113563035B (en) Preparation method of biomass ash autoclaved baking-free brick
JP5443010B2 (en) Method for producing hydrothermal solidified body of paper sludge incineration ash
JP2009148713A (en) Granule, sintered body, and methods for producing them
KR101934411B1 (en) High-temperature waste treatment method using sludge
JP2007260503A (en) Manufacturing method of burned matter
EP2628715A2 (en) A method for high-temperature utilization of phosphogypsum
JP2008126185A (en) Calcined object and its manufacturing method
KR100769954B1 (en) Manufacturing method lightweight aggregate using organic and inorganic waste complexly
Borowski et al. Using Agglomeration Techniques for Coal and Ash Waste Management in the Circular Economy
KR100760478B1 (en) Method of manufacturing for open cell using sludge
JP2010131501A (en) Method for burning sludge granulated product, use method thereof
JP2008273749A (en) Artificial aggregate and its manufacturing method
JP2009132565A (en) Method of manufacturing artificial aggregate
RU2008134462A (en) METHOD FOR PRODUCING BINDER FOR OIL AND BINDER FOR OIL OBTAINED BY THIS METHOD
JP2006003013A (en) Sewage sludge treatment method and device
KR100687627B1 (en) Method for solidifying sewage sludge
JP2005313032A (en) Manufacturing method for hydrothermally solidified material of paper sludge incineration ash