JP4283495B2 - How to use ash-containing carbides - Google Patents

How to use ash-containing carbides Download PDF

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Publication number
JP4283495B2
JP4283495B2 JP2002154859A JP2002154859A JP4283495B2 JP 4283495 B2 JP4283495 B2 JP 4283495B2 JP 2002154859 A JP2002154859 A JP 2002154859A JP 2002154859 A JP2002154859 A JP 2002154859A JP 4283495 B2 JP4283495 B2 JP 4283495B2
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Prior art keywords
ash
carbide
waste
low
cement
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JP2004002054A (en
Inventor
弘隆 磯村
憲史 永田
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Taiheiyo Cement Corp
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Taiheiyo Cement Corp
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/10Biofuels, e.g. bio-diesel
    • 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
    • Y02EREDUCTION OF GREENHOUSE GAS [GHG] EMISSIONS, RELATED TO ENERGY GENERATION, TRANSMISSION OR DISTRIBUTION
    • Y02E50/00Technologies for the production of fuel of non-fossil origin
    • Y02E50/30Fuel from waste, e.g. synthetic alcohol or diesel
    • 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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00Technologies relating to chemical industry
    • Y02P20/141Feedstock
    • Y02P20/143Feedstock the feedstock being recycled material, e.g. plastics

Description

【0001】
【発明の属する技術分野】
本発明は、灰分含有炭化物の利用方法に関し、特に、廃棄物由来の灰分含有炭化物をセメント製造工程において利用する方法に関する。
【0002】
【従来の技術】
従来、都市ゴミ、RDF、廃木材、廃紙、廃プラスチック、野菜屑、生ごみ、汚泥、食品残査、家畜の死体等の廃棄物を炭化して得られた炭化物をセメントキルンの燃料として利用することが検討されている。
【0003】
ここで、セメントキルンの窯前から主燃料とともに、または主燃料バーナと併設されたノズルから投入されるセメント燃料の代替用としての使用量の上限は、炭化物に含有される灰分量とともに、炭化物中の塩素濃度と、セメント中の塩素濃度とのマスバランスで決定される。すなわち、セメント中の塩素濃度が限界値に達すると、それ以上塩素を含有する炭化物をセメント製造工程において利用することができなくなる。
【0004】
【発明が解決しようとする課題】
都市ゴミ等の廃棄物は、炭化処理によって、脱塩素、減容、均質化される。廃棄物を炭化した場合、炭化による熱分解によって有機塩素分の大部分を除去できる。さらに、水洗によって、塩化ナトリウムや塩化カリウム等の水溶性の無機塩素分を除去することができる。しかしながら、これらの炭化物には、難溶性の含塩素化合物を含む多くの灰分が含まれているため、炭化物をセメント製造工程において窯前からの燃料代替として利用するには限界がある。すなわち、多く含まれる灰分により、炭化物の持つ熱量が燃料代替として利用する上で不十分とものとなる場合があり、さらに、その灰分中に含まれる塩素が燃料代替としての利用の障害となっている。
【0005】
そこで、本発明は、上記従来の技術における問題点に鑑みてなされたものであって、都市ゴミ、RDF、廃木材、廃紙、廃プラスチック、野菜屑、生ごみ、汚泥、食品残査、家畜の死体等の廃棄物由来の灰分含有炭化物を可能な限り多くセメント製造工程において利用することを目的とする。
【0006】
【課題を解決するための手段】
上記目的を達成するため、本発明は、灰分含有炭化物の利用方法であって、廃棄物を炭化処理した灰分含有炭化物を低灰分高炭化物と高灰分低炭化物とに分別し、低灰分高炭化物をセメント製造用燃料とする一方で、高灰分低炭化物をセメント製造用原料として利用することにより前記灰分含有炭化物に含有されている塩素分の一部を前記セメント製造用原料側に移行させ、該塩素分を塩素バイパス設備により除去することを特徴とする。
【0007】
そして、本発明によれば、灰分含有炭化物を精製し、高灰分低炭化物をセメント原料の粘土代替とすることにより、灰分含有炭化物に含有されている塩素分の一部をセメント原料側に移行させ、セメント製造時において塩素バイパスシステムによってこの塩素分を除去するようにすれば、セメント製造時の原料配合設計や品質管理が容易になり、より限界近くまで多くの灰分含有炭化物をセメント製造工程において利用することができる。
【0008】
上記灰分含有炭化物は、都市ゴミ、RDF、廃木材、廃紙、廃プラスチック、野菜屑、生ごみ、汚泥、食品残査、家畜の死体等の廃棄物炭化処理したものである。これによって、都市ゴミ等の廃棄物をセメント製造工程においてより多く利用することができ、廃棄物の処理及び有効利用により大きく貢献することができる。尚、前記分別方法には、浮選法を用いることが好ましい。
【0009】
【発明の実施の形態】
次に、本発明にかかる灰分含有炭化物の利用方法の実施の形態の具体例を図面を参照しながら説明する。
【0010】
前述の課題に鑑み、本発明者らは、都市ゴミ等の廃棄物由来の灰分含有炭化物を可能な限り多くセメント製造工程において利用することについて鋭意検討を行った結果、灰分含有炭化物を浮選法等によって低灰分高炭化物と高灰分低炭化物とに分別し、低灰分高炭化物をセメント製造用燃料とし、高灰分低炭化物をセメント製造用原料として利用することで、より多くの灰分含有炭化物をセメント製造工程において利用することができることを見出した。
【0011】
本発明にかかる灰分含有炭化物の利用方法の一実施の形態について図1を参照しながら詳細に説明する。
【0012】
まず、都市ゴミ、RDF、廃木材、廃紙、廃プラスチック、野菜屑、生ごみ、汚泥、食品残査、家畜の死体等の廃棄物をロータリーキルンで炭化したものを炭化物として使用する。この炭化物を粒度調製し、微粉砕した後、水と混合し、スラリーとする。尚、廃棄物の炭化にあたっては、竪型炉を用いてもよい。また、炭化物の粉砕にあたっては、湿式粉砕でも乾式粉砕でもよい。後工程での浮選時の灰分除去率を高めるため、最大粒径を0.5mm以下、より好ましくは0.1mm以下に粒度調整を行う。さらに微粉砕することは、粉砕コストの増加に繋がり好ましくない。また、炭化物スラリーの濃度は、0.1〜15重量%が好ましく、0.5〜5重量%がより好ましい。より高濃度では、ハンドリング性が悪く、炭化物スラリーの濃度を低濃度にする程浮選時の灰分除去率が高くなるが、過度に低濃度にすれば、次工程の浮選機の規模が大きくなるので好ましくない。
【0013】
次に、スラリーを浮選機によって低比重の低灰分高炭化物スラリーと高比重の高灰分低炭化物スラリーに分離した後、各々のスラリーを固液分離し、低灰分高炭化物と高灰分低炭化物を回収する。浮選機には、カラム型浮選機や攪拌型浮選機等を使用することができる。また、固液分離には、フィルタープレス、ベルトフィルター、遠心分離機等を使用することができる。浮選は、比重1.4〜1.8を境に、低比重の低灰分高炭化物と、高比重の高灰分低炭化物とに分別する。尚、固液分離された各々の水は、排水基準を満たすため、適宜排水処理を行う。浮選及び固液分離の過程で水溶性塩化物の80〜90%が除去される。回収した低灰分高炭化物及び高灰分低炭化物スラリーは、乾燥させた後、ともにセメント製造工程において利用することができる。
【0014】
図2に示すように、セメント製造工程のセメント焼成設備1は、プレヒータ2、仮焼炉3、キルン4、クリンカクーラー5等からなり、原料供給系7からプレヒータ2に投入されたセメント原料が、プレヒータ2において予熱され、仮焼炉3において仮焼され、キルン4において焼成されて製造されたクリンカがクリンカクーラー5において冷却される。本発明によって回収した低灰分高炭化物は、キルン4の窯前のバーナー6から吹き込んで燃料として使用することができ、仮焼炉3に投入して還元剤として使用することもできる。例えば、灰分が35%程度の灰分含有炭化物を浮選し、灰分10%程度の低灰分高炭化物を生成すると、この炭化物の熱量は、4500kcal/kgから6200kcal/kgとなり、セメントキルンの窯前からの燃料代替に利用することができる。
【0015】
一方、高灰分低炭化物は、原料供給系7からプレヒータ2へセメント原料の粘土代替として投入することができる。プレヒータ2に投入すると、セメントキルンの窯尻付近より燃焼ガスの一部を抽気して塩素を除去する塩素バイパス設備8によって、高灰分低炭化物に含まれる塩素を除去することができる。これにより、全ての炭化物をセメントキルン4の窯前から燃料として利用する場合と比較して、より多くの灰分含有炭化物をセメント製造工程において利用することができる。
【0016】
【発明の効果】
以上説明したように、本発明にかかる灰分含有炭化物の利用方法によれば、都市ゴミ等の廃棄物に由来する灰分含有炭化物等を可能な限り多くセメント製造工程において利用することができる。
【図面の簡単な説明】
【図1】本発明にかかる灰分含有炭化物の利用方法の一実施例を説明するためのフロー図である。
【図2】本発明にかかる灰分含有炭化物の利用方法において利用するセメント製造工程のセメント焼成設備の概略図である。
【符号の説明】
1 セメント焼成設備
2 プレヒータ
3 仮焼炉
4 キルン
5 クリンカクーラー
6 バーナー
7 原料供給系
[0001]
BACKGROUND OF THE INVENTION
The present invention relates to a method for using ash-containing carbide, and more particularly, to a method for using waste-derived ash-containing carbide in a cement manufacturing process.
[0002]
[Prior art]
Conventionally, carbonized products obtained by carbonizing waste such as municipal waste, RDF, waste wood, waste paper, waste plastic, vegetable waste, food waste, sludge, food residue, livestock carcass, etc. are used as fuel for cement kilns. To be considered.
[0003]
Here, the upper limit of the amount of use as a substitute for cement fuel that is introduced together with the main fuel from the kiln of the cement kiln or from the nozzle provided with the main fuel burner is the amount of ash contained in the carbide, It is determined by the mass balance between the chlorine concentration in the cement and the chlorine concentration in the cement. That is, when the chlorine concentration in the cement reaches the limit value, it becomes impossible to use any more carbide containing chlorine in the cement manufacturing process.
[0004]
[Problems to be solved by the invention]
Waste such as municipal waste is dechlorinated, reduced in volume, and homogenized by carbonization. When the waste is carbonized, most of the organic chlorine content can be removed by thermal decomposition by carbonization. Furthermore, water-soluble inorganic chlorine such as sodium chloride and potassium chloride can be removed by washing with water. However, since these carbides contain a large amount of ash containing a hardly soluble chlorine-containing compound, there is a limit in using the carbides as a fuel replacement before the kiln in the cement manufacturing process. In other words, the ash contained in a large amount may cause the calorific value of the carbide to be insufficient for use as a fuel substitute, and the chlorine contained in the ash may be an obstacle to the use as a fuel substitute. Yes.
[0005]
Therefore, the present invention has been made in view of the problems in the above-described conventional technology, and includes municipal waste, RDF, waste wood, waste paper, waste plastic, vegetable waste, garbage, sludge, food residue, livestock. The purpose is to use as much as possible ash-containing carbides derived from waste such as carcasses in cement manufacturing processes.
[0006]
[Means for Solving the Problems]
In order to achieve the above object, the present invention is a method for using ash-containing carbides, wherein the ash-containing carbides obtained by carbonizing waste are separated into low ash high carbides and high ash low carbides to obtain low ash high carbides. While using a high ash content low carbide as a raw material for cement manufacture, a portion of the chlorine content contained in the ash containing carbide is transferred to the raw material side for cement manufacture while using the cement manufacturing fuel. The water is removed by a chlorine bypass facility .
[0007]
And according to the present invention, by purifying the ash-containing carbide and replacing the high ash-low carbide with a clay substitute for cement raw material, a portion of the chlorine content contained in the ash-containing carbide is transferred to the cement raw material side. If this chlorine content is removed by the chlorine bypass system during cement production, it will be easier to design and control the raw material composition during cement production, and more ash-containing carbides will be used in the cement production process. can do.
[0008]
The ash-containing carbides, municipal waste, RDF, waste wood, waste paper, waste plastics, vegetable waste, garbage, sludge, food residue, it is a waste of carcasses such as livestock those carbonization. As a result, waste such as municipal waste can be used more in the cement manufacturing process, which can greatly contribute to waste disposal and effective use. In addition, it is preferable to use the flotation method as the fractionation method.
[0009]
DETAILED DESCRIPTION OF THE INVENTION
Next, a specific example of an embodiment of a method for using an ash-containing carbide according to the present invention will be described with reference to the drawings.
[0010]
In view of the above-mentioned problems, the present inventors have conducted intensive studies on using as much ash-containing carbides derived from wastes such as municipal waste as much as possible in the cement manufacturing process. By separating low ash high carbides and high ash low carbides, etc., using low ash high carbides as fuel for cement production and using high ash low carbides as raw materials for cement production, more ash-containing carbides can be cemented. It has been found that it can be used in the manufacturing process.
[0011]
An embodiment of a method for using ash-containing carbide according to the present invention will be described in detail with reference to FIG.
[0012]
First, wastes such as municipal waste, RDF, waste wood, waste paper, waste plastic, vegetable waste, garbage, sludge, food residue, livestock carcasses, etc., which are carbonized with a rotary kiln are used as carbides. The particle size of the carbide is adjusted and finely pulverized, and then mixed with water to form a slurry. In the carbonization of waste, a vertical furnace may be used. Further, the carbide may be pulverized by wet pulverization or dry pulverization. In order to increase the ash removal rate at the time of flotation in the subsequent process, the maximum particle size is adjusted to 0.5 mm or less, more preferably 0.1 mm or less. Further pulverization is not preferable because it leads to an increase in pulverization cost. The concentration of the carbide slurry is preferably 0.1 to 15% by weight, more preferably 0.5 to 5% by weight. If the concentration is higher, handling properties are worse, and the lower the concentration of the carbide slurry, the higher the ash removal rate at the time of flotation. However, if the concentration is too low, the scale of the flotation machine in the next process will be large. This is not preferable.
[0013]
Next, the slurry is separated into a low specific gravity low ash high carbide slurry and a high specific gravity high ash low carbide slurry using a flotation machine, and then each slurry is solid-liquid separated to obtain a low ash high carbide and a high ash low carbide. to recover. As the flotation machine, a column type flotation machine, a stirring type flotation machine, or the like can be used. Moreover, a filter press, a belt filter, a centrifuge, etc. can be used for solid-liquid separation. Flotation is divided into a low specific gravity low ash high carbide and a high specific gravity high ash low carbide with a specific gravity of 1.4 to 1.8 as a boundary. In addition, each water separated into solid and liquid is appropriately subjected to drainage treatment in order to satisfy drainage standards. In the process of flotation and solid-liquid separation, 80 to 90% of the water-soluble chloride is removed. The recovered low ash high carbide and high ash low carbide slurry can be used together in the cement manufacturing process after being dried.
[0014]
As shown in FIG. 2, the cement firing facility 1 in the cement manufacturing process includes a preheater 2, a calciner 3, a kiln 4, a clinker cooler 5, and the like, and the cement raw material charged into the preheater 2 from the raw material supply system 7 is The clinker produced by preheating in the preheater 2, calcining in the calcining furnace 3 and firing in the kiln 4 is cooled in the clinker cooler 5. The low ash high carbide recovered by the present invention can be blown from the burner 6 in front of the kiln 4 and used as fuel, and can also be put into the calcining furnace 3 and used as a reducing agent. For example, when flotation of an ash-containing carbide having an ash content of about 35% and producing a low ash high-carbide with an ash content of about 10%, the calorific value of the carbide is changed from 4500 kcal / kg to 6200 kcal / kg. It can be used for fuel replacement.
[0015]
On the other hand, the high ash content and low carbide can be input from the raw material supply system 7 to the preheater 2 as a substitute for cement raw clay. When put into the preheater 2, chlorine contained in the high ash and low carbides can be removed by the chlorine bypass facility 8 that extracts a portion of the combustion gas from the vicinity of the kiln bottom of the cement kiln and removes chlorine. Thereby, compared with the case where all the carbide | carbonized_materials are utilized as a fuel before the kiln of the cement kiln 4, more ash content carbide | carbonized_material can be utilized in a cement manufacturing process.
[0016]
【The invention's effect】
As described above, according to the method for using ash-containing carbide according to the present invention, as much ash-containing carbide derived from wastes such as municipal waste can be used in the cement manufacturing process as much as possible.
[Brief description of the drawings]
FIG. 1 is a flowchart for explaining an embodiment of a method for using ash-containing carbide according to the present invention.
FIG. 2 is a schematic view of a cement firing facility in a cement manufacturing process used in the method of using ash-containing carbide according to the present invention.
[Explanation of symbols]
1 Cement firing equipment 2 Preheater 3 Calciner 4 Kiln 5 Clinker cooler 6 Burner 7 Raw material supply system

Claims (2)

廃棄物を炭化処理した灰分含有炭化物を低灰分高炭化物と高灰分低炭化物とに分別し、低灰分高炭化物をセメント製造用燃料とする一方で、高灰分低炭化物をセメント製造用原料として利用することにより前記灰分含有炭化物に含有されている塩素分の一部を前記セメント製造用原料側に移行させ、該塩素分を塩素バイパス設備により除去することを特徴とする灰分含有炭化物の利用方法。 Waste-carbonized ash-containing carbide is separated into low-ash high-carbon and high-ash low-carbide, and low-ash high-carbon is used as a fuel for cement production, while high-ash low-carbon is used as a raw material for cement production. Thus, a part of chlorine content contained in the ash-containing carbide is transferred to the raw material side for cement production, and the chlorine content is removed by a chlorine bypass facility . 前記分別方法が浮選法であることを特徴とする請求項1に記載の灰分含有炭化物の利用方法。 The method for using an ash-containing carbide according to claim 1 , wherein the fractionation method is a flotation method.
JP2002154859A 2002-05-29 2002-05-29 How to use ash-containing carbides Expired - Fee Related JP4283495B2 (en)

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JP4964185B2 (en) * 2004-02-26 2012-06-27 太平洋セメント株式会社 Cement clinker manufacturing method
KR100753852B1 (en) 2007-04-17 2007-08-31 디에스케이엔지니어링(주) Food dirt, the pro-environment block where a microorganism was used and this production technique
JP5040737B2 (en) * 2008-03-07 2012-10-03 宇部興産株式会社 Operation method of cement production equipment
JP5018754B2 (en) * 2008-12-05 2012-09-05 三菱マテリアル株式会社 Processing method of shredder dust using cement manufacturing process

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