JP2590726B2 - Method for producing agglomerated material for clayey soil - Google Patents

Method for producing agglomerated material for clayey soil

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Publication number
JP2590726B2
JP2590726B2 JP6039460A JP3946094A JP2590726B2 JP 2590726 B2 JP2590726 B2 JP 2590726B2 JP 6039460 A JP6039460 A JP 6039460A JP 3946094 A JP3946094 A JP 3946094A JP 2590726 B2 JP2590726 B2 JP 2590726B2
Authority
JP
Japan
Prior art keywords
coarse
fine powder
soil
clayey soil
powder
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.)
Expired - Lifetime
Application number
JP6039460A
Other languages
Japanese (ja)
Other versions
JPH07246375A (en
Inventor
正康 山崎
弘幸 松田
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.)
Mitsubishi Materials Corp
Original Assignee
Mitsubishi Materials Corp
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Filing date
Publication date
Application filed by Mitsubishi Materials Corp filed Critical Mitsubishi Materials Corp
Priority to JP6039460A priority Critical patent/JP2590726B2/en
Publication of JPH07246375A publication Critical patent/JPH07246375A/en
Application granted granted Critical
Publication of JP2590726B2 publication Critical patent/JP2590726B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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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
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P40/00Technologies relating to the processing of minerals
    • Y02P40/10Production of cement, e.g. improving or optimising the production methods; Cement grinding

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  • Processing Of Solid Wastes (AREA)
  • Soil Conditioners And Soil-Stabilizing Materials (AREA)

Description

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

【0001】[0001]

【産業上の利用分野】本発明は粘土質土壌の団粒化材の
製造方法に係り、特に、流動床ボイラ灰を粘土質土壌の
団粒化材として有効利用する粘土質土壌の団粒化材の製
造方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for producing an agglomerated material for a clay soil, and more particularly to an agglomeration of a clay soil using a fluidized bed boiler ash as an agglomerated material for a clay soil. The present invention relates to a method for manufacturing a material.

【0002】[0002]

【従来の技術】近年、省資源及び廃棄物の減量化を目的
として、各種産業廃棄物について、その有効再利用を図
ることが望まれている。
2. Description of the Related Art In recent years, it has been desired to effectively reuse various industrial wastes for the purpose of saving resources and reducing the amount of wastes.

【0003】そこで、従来において、燃焼炉廃棄物であ
るボイラ灰のうち、微粉炭ボイラ灰については、セメン
ト原料として利用されている。
[0003] Conventionally, pulverized coal boiler ash among boiler ash, which is waste from a combustion furnace, has been used as a cement raw material.

【0004】[0004]

【発明が解決しようとする課題】しかしながら、流動床
ボイラ灰は、SO3 含有量が多く、セメントキルン及び
/又はプレヒータ内で低融点化合物を生成して運転を阻
害するため、多量に使用することはできず、多くは廃棄
されているのが現状である。
However, fluidized-bed boiler ash has a high SO 3 content and generates a low-melting compound in a cement kiln and / or a preheater, which hinders operation. Can not be done, and most are discarded at present.

【0005】一方、建設現場や採掘現場から大量に排出
される粘土質土壌は、セメント原料として利用される場
合もあるが、その粘性のために取り扱い性が悪く、取り
扱い性の向上が望まれている。
[0005] On the other hand, clay soil discharged in large quantities from construction sites and mining sites is sometimes used as a cement raw material, but its viscosity makes it difficult to handle. I have.

【0006】本発明は上記従来の実情に鑑みてなされた
ものであって、流動床ボイラ灰を粘土質土壌の取り扱い
性向上のための団粒化材として有効利用する粘土質土壌
の団粒化材の製造方法を提供することを目的とする。
SUMMARY OF THE INVENTION The present invention has been made in view of the above-mentioned conventional circumstances, and is directed to agglomeration of clayey soil in which a fluidized bed boiler ash is effectively used as an agglomerating agent for improving the handling property of clayey soil. An object of the present invention is to provide a method for manufacturing a material.

【0007】[0007]

【課題を解決するための手段】請求項1の粘土質土壌の
団粒化材の製造方法は、流動床ボイラ灰を粗粒と微粉と
に分級し、この粗粒を粘土質土壌の団粒化材として回収
することを特徴とする。
According to a first aspect of the present invention, there is provided a method for producing an agglomerated material for a clayey soil, wherein the fluidized bed boiler ash is classified into coarse particles and fine particles, and the coarse particles are aggregated in the clayey soil. It is characterized by being recovered as a chemical material.

【0008】請求項2の粘土質土壌の団粒化材の製造方
法は、請求項1において、回収した粗粒を表面剥離処理
した後、粗粉と細粉とに分級し、この粗粉を粘土質土壌
の団粒化材として回収することを特徴とする。
According to a second aspect of the present invention, there is provided a method for producing an agglomerated material for a clayey soil according to the first aspect, wherein the collected coarse particles are subjected to a surface peeling treatment, and then classified into coarse powder and fine powder. It is characterized in that it is recovered as an aggregate for clayey soil.

【0009】請求項3の粘土質土壌の団粒化材の製造方
法は、請求項1において、回収した粗粒を表面剥離処理
した後、粗粉と細粉とに分級し、この粗粉及び細粉を粘
土質土壌の団粒化材として回収することを特徴とする。
According to a third aspect of the present invention, there is provided a method for producing an agglomerated material for a clayey soil according to the first aspect, wherein the collected coarse particles are subjected to a surface peeling treatment, and then classified into a coarse powder and a fine powder. The method is characterized in that the fine powder is recovered as an agglomerated material for clayey soil.

【0010】以下に本発明を詳細に説明する。Hereinafter, the present invention will be described in detail.

【0011】請求項1の方法においては、流動床ボイラ
灰を分級して粗粒と微粉とに分ける。ここで分級手段と
しては特に制限はないが、分級される粗粒分と微粉分と
では比重差があるため、この比重差を利用して空気分級
を行うのが、簡便で有利な方法である。
In the method according to the first aspect, the fluidized-bed boiler ash is classified and divided into coarse particles and fine powder. Here, the classification means is not particularly limited, but since there is a specific gravity difference between the coarse and fine powder components to be classified, performing air classification using this specific gravity difference is a simple and advantageous method. .

【0012】この分級処理により、流動床ボイラ灰はC
aO(生石灰)を多く含む粗粒と微粉とに分離される。
By this classification, the fluidized-bed boiler ash becomes C
It is separated into coarse particles and fine powders rich in aO (quick lime).

【0013】請求項1の方法においては、分級された粗
粒と微粉のうち、CaOを多く含む粗粒を粘土質土壌の
団粒化材として回収する。
In the method of the first aspect, of the classified coarse particles and fine powder, the coarse particles containing a large amount of CaO are recovered as agglomerating material for clayey soil.

【0014】なお、分級により得られる粗粒は一般に平
均粒径80〜110μmであり、微粉は平均粒径25〜
50μmである。
The coarse particles obtained by the classification generally have an average particle size of 80 to 110 μm, and the fine powder has an average particle size of 25 to 110 μm.
50 μm.

【0015】この分級で得られた微粉は、CaSO4
多く含み、回収してセメント原料等に用いることができ
る。
The fine powder obtained by this classification contains a large amount of CaSO 4 and can be recovered and used as a cement raw material or the like.

【0016】請求項2,3の方法においては、上記分級
により回収された粗粒をロッドを入れた筒状回転体(ロ
ッドミル)や振動ミルで処理するなどして表面剥離処理
し、次いで、空気分級や篩分け等により剥離物の細粉と
表面層が剥離された粗粉とに分級する。
In the method according to the second or third aspect, the coarse particles collected by the classification are subjected to a surface peeling treatment by, for example, being treated with a cylindrical rotating body (rod mill) containing a rod or a vibration mill, and then subjected to air. Classification into fine powder of the exfoliated material and coarse powder from which the surface layer has been exfoliated by classification or sieving.

【0017】分級された粗粉と細粉のうち、粗粉はCa
Oを多く含み、細粉はCaSO4 (無水石膏)を多く含
む。
Among the classified coarse powder and fine powder, the coarse powder is Ca
The powder contains a lot of O, and the fine powder contains a lot of CaSO 4 (anhydrite).

【0018】請求項2の方法では、このCaOを多く含
む粗粉を粘土質土壌の団粒化材として回収する。また、
請求項3の方法では、CaOを多く含む粗粉と、CaS
4を多く含む微粉とをそれぞれ粘土質土壌の団粒化材
として回収する。
In the method according to the second aspect, the coarse powder containing a large amount of CaO is recovered as a flocculant for clayey soil. Also,
The method according to claim 3, wherein the coarse powder containing a large amount of CaO,
The fine powder containing a large amount of O 4 is recovered as an agglomerator for clayey soil.

【0019】なお、前述の粗粒を表面剥離処理及び分級
して得られる粗粉は一般に平均粒径70〜100μmで
あり、細粉は平均粒径20〜60μmである。
The coarse powder obtained by subjecting the above coarse particles to a surface peeling treatment and classification generally has an average particle diameter of 70 to 100 μm, and the fine powder has an average particle diameter of 20 to 60 μm.

【0020】本発明により製造された粘土質土壌の団粒
化材は、これを粘土質土壌に所定割合で添加混合するこ
とにより、粘土質土壌を効果的に団粒化してその取り扱
い性を改善することができる。
The agglomerated material of the clay soil produced according to the present invention is added to and mixed with the clay soil at a predetermined ratio, thereby effectively aggregating the clay soil and improving its handleability. can do.

【0021】本発明に係る団粒化材の粘土質土壌に対す
る添加割合は、処理する粘土質土壌の含水率や組成等に
よっても異なるが、通常の場合、含水率(当該粘土質土
壌中に含まれる水の重量割合)25〜50%の粘土質土
壌であれば、流動床ボイラ灰を分級して得られた粗粒を
5〜100重量%程度添加するのが好ましい。また、こ
の粗粒を表面剥離処理及び分級して得られた粗粉を添加
する場合には、粘土質土壌に対して5〜70重量%程度
添加するのが好ましい。
The addition ratio of the agglomerated material according to the present invention to the clayey soil varies depending on the water content and the composition of the clayey soil to be treated. If the clay soil is 25 to 50% by weight, it is preferable to add approximately 5 to 100% by weight of coarse particles obtained by classifying the fluidized-bed boiler ash. In addition, when adding coarse powder obtained by subjecting the coarse particles to a surface peeling treatment and classification, it is preferable to add about 5 to 70% by weight based on the clay soil.

【0022】更に、上記粗粒を表面剥離処理及び分級し
て得られた粗粉及び細粉を共に添加する場合には、粘土
質土壌に対して粗粉を4〜50重量%程度、細粉を1〜
30重量%程度添加するのが好ましい。
Further, when both the coarse powder and the fine powder obtained by subjecting the coarse particles to the surface peeling treatment and classification are added, the coarse powder is added in an amount of about 4 to 50% by weight to the clayey soil. Is 1 to
It is preferable to add about 30% by weight.

【0023】[0023]

【作用】流動床ボイラにおいて、石炭は低温燃焼によ
り、ポーラスな灰となり、流動層内で微粉になる。一
方、石灰石はさぼど粉化することなく、表面にCaSO
4 (無水石膏)が生成した粗粒となる。従って、流動床
ボイラ灰は、一般に、石炭灰と、表面にCaSO4 が付
着したCaOを多く含む粗粒と、更に流動媒体を使用し
た場合には珪砂とからなるものである。
In a fluidized-bed boiler, coal becomes porous ash by low-temperature combustion and becomes fine powder in a fluidized bed. On the other hand, limestone is not powdered, and CaSO
4 (Anhydrite) becomes coarse particles. Accordingly, fluidized bed boiler ash generally comprises coal ash, coarse particles containing a large amount of CaO with CaSO 4 adhered to the surface, and silica sand when a fluidized medium is used.

【0024】請求項1の方法においては、このような流
動床ボイラ灰を分級することにより、表面にCaSO4
が付着し、CaOを多く含む粗粒を回収する。
In the method according to the first aspect, by classifying such fluidized-bed boiler ash, CaSO 4 is added to the surface.
Adheres and collects coarse particles containing a large amount of CaO.

【0025】また、請求項2,3の方法においては、こ
の粗粒を更に表面剥離処理して表面のCaSO4 成分を
剥離させ、CaOを多く含む粗粉と剥離したCaSO4
を多く含む細粉とに分級し、請求項2においてはCaO
を多く含む粗粉を回収する。また、請求項3において
は、この粗粉とCaSO4 を多く含む細粉とをそれぞれ
回収する。
Further, CaSO 4 in the method of claim 2, in which the coarse grains further surface release-treated by stripping the CaSO 4 component of the surface was peeled off and coarse powder containing a large amount of CaO
And a fine powder containing a large amount of CaO.
Is recovered. In claim 3, the coarse powder and the fine powder containing a large amount of CaSO 4 are recovered.

【0026】本発明による粘土質土壌の団粒化機構は次
の通りである。
The aggregation mechanism of the clayey soil according to the present invention is as follows.

【0027】即ち、粘土は主にAl23 ,SiO2
含むことから、CaOを添加することにより、ポゾラン
反応(C−H−S生成反応)により固化させることがで
きる。また、CaOとCaSO4 とを添加することによ
り、エトリンガイトを生成させて固化させることができ
る。
That is, since clay mainly contains Al 2 O 3 and SiO 2 , it can be solidified by the pozzolan reaction (CHS formation reaction) by adding CaO. In addition, by adding CaO and CaSO 4 , ettringite can be generated and solidified.

【0028】このため、流動床ボイラ灰の分級により得
られたCaOを多く含む粗粒をそのまま、或いは、更に
この粗粒を表面剥離処理及び分級して得られたCaOを
多く含む粗粉、又は、この粗粉とCaSO4 を多く含む
細粉とを粘土質土壌に添加混合することにより、粘土質
土壌を効果的に団粒化して、その取り扱い性を改善する
ことができる。
For this reason, coarse particles containing a large amount of CaO obtained by the classification of the fluidized-bed boiler ash are used as they are, or coarse particles containing a large amount of CaO obtained by subjecting the coarse particles to a surface separation treatment and classification, or By adding and mixing the coarse powder and the fine powder containing a large amount of CaSO 4 to the clay soil, the clay soil can be effectively aggregated, and the handling property can be improved.

【0029】特に、請求項3の方法によれば、粗粉と細
粉とをそれぞれ用いることにより、CaO及びCaSO
4 の優れた添加効果が得られ、より一層効率的な団粒化
を行える。
In particular, according to the method of claim 3, by using coarse powder and fine powder respectively, CaO and CaSO
The excellent addition effect of 4 is obtained, and more efficient agglomeration can be performed.

【0030】[0030]

【実施例】以下に実施例を挙げて本発明をより具体的に
説明する。
The present invention will be described more specifically with reference to the following examples.

【0031】実施例1 電力産業で発生した、表1に示す組成の流動床ボイラ灰
100kgを空気分級して、表1に示す組成の粗粒(平
均粒径110μm)29kgと微粉(平均粒径35μ
m)71kgとに分級し、粗粒を回収した。
Example 1 100 kg of a fluidized-bed boiler ash having a composition shown in Table 1 generated in the electric power industry was classified by air, and 29 kg of coarse particles (average particle size 110 μm) and fine powder (average particle size) having the composition shown in Table 1 were obtained. 35μ
m) The mixture was classified into 71 kg, and coarse particles were collected.

【0032】実施例2 実施例1で回収された粗粒の一部10kgをロッドミル
で表面剥離処理し、その後、気流分級器により分級し、
表1に示す組成の粗粉(平均粒径100μm)8.3k
gと細粉(平均粒径45μm)1.7kgとに分級し、
粗粉を回収した。
Example 2 A portion of 10 kg of the coarse particles recovered in Example 1 was subjected to a surface peeling treatment by a rod mill, and then classified by an airflow classifier.
Coarse powder having the composition shown in Table 1 (average particle size: 100 μm) 8.3 k
g and fine powder (average particle size 45 μm) 1.7 kg,
The coarse powder was recovered.

【0033】実施例3 実施例2と同一の操作を行ない、粗粉と細粉とをそれぞ
れ回収した。
Example 3 The same operation as in Example 2 was performed to collect coarse powder and fine powder, respectively.

【0034】[0034]

【表1】 [Table 1]

【0035】石灰石採掘場から採取された高含水重質粘
土(含水率33%)に、上記粗粒、粗粉及び細粉を、表
2に示す割合で添加混合したところ、いずれの場合も良
好に団粒化がなされ、取り扱い性は大幅に改善された。
The above coarse particles, coarse powder and fine powder were added to a high water content heavy clay (water content 33%) collected from a limestone quarry at a ratio shown in Table 2 and mixed. The agglomeration was carried out and the handling was greatly improved.

【0036】[0036]

【表2】 [Table 2]

【0037】[0037]

【発明の効果】以上詳述した通り、本発明の粘土質土壌
の団粒化材の製造方法によれば、従来廃棄処理されてい
た流動床ボイラ灰から、粘土質土壌の団粒化材を製造す
ることができる。また、得られた団粒化材を用いて粘土
質土壌の取り扱い性を大幅に改善し、各種の粘土質土壌
の有効利用を図ることができる。特に、本発明による団
粒化材を用いて団粒化した粘土は、石灰分を含むことか
ら、植栽養土として好適である。
As described above in detail, according to the method for producing the agglomerated material for clayey soil according to the present invention, the agglomerated material for clayey soil is converted from the fluidized-bed boiler ash conventionally discarded. Can be manufactured. Moreover, the handling property of clay soil can be significantly improved using the obtained aggregated material, and various clay soils can be effectively used. In particular, clay agglomerated using the agglomerated material according to the present invention is suitable for planting soil because it contains lime.

【0038】請求項1の粘土質土壌の団粒化材の製造方
法によれば、流動床ボイラ灰より容易に粘土質土壌の団
粒化材を得ると共に、分離した微粉をセメント原料等と
して利用することができる。
According to the method for producing the agglomerated material of the clay soil of claim 1, the agglomerated material of the clay soil is easily obtained from the fluidized-bed boiler ash, and the separated fine powder is used as a cement raw material or the like. can do.

【0039】請求項2の粘土質土壌の団粒化材の製造方
法によれば、流動床ボイラ灰より粘土質土壌の団粒化材
としてのCaO成分を回収して良好な団粒化処理を行え
る。
According to the method for producing an agglomerated material for a clayey soil according to the second aspect, a CaO component as an agglomerated material for a clayey soil is recovered from a fluidized-bed boiler ash to perform favorable agglomerated treatment. I can do it.

【0040】請求項3の粘土質土壌の団粒化材の製造方
法によれば、流動床ボイラ灰より粘土質土壌の団粒化材
としてのCaO成分とCaSO4 成分とを各々回収し
て、より一層良好な団粒化処理を行える。
According to the manufacturing method of the crumb of material clay soil according to claim 3, and each recovered and CaO component and CaSO 4 component as crumb of material of clay soil from the fluidized bed boiler ash, Even better agglomeration treatment can be performed.

───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C09K 103:00 B09B 3/00 301E ──────────────────────────────────────────────────の Continued on the front page (51) Int.Cl. 6 Identification number Agency reference number FI Technical display location C09K 103: 00 B09B 3/00 301E

Claims (3)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 流動床ボイラ灰を粗粒と微粉とに分級
し、この粗粒を粘土質土壌の団粒化材として回収するこ
とを特徴とする粘土質土壌の団粒化材の製造方法。
1. A method for producing an agglomerated material for clayey soil, wherein the fluidized bed boiler ash is classified into coarse particles and fine powder, and the coarse particles are recovered as an agglomerated material for the clayey soil. .
【請求項2】 請求項1において、回収した粗粒を表面
剥離処理した後、粗粉と細粉とに分級し、この粗粉を粘
土質土壌の団粒化材として回収することを特徴とする粘
土質土壌の団粒化材の製造方法。
2. The method according to claim 1, wherein the collected coarse particles are subjected to surface peeling treatment, then classified into coarse powder and fine powder, and the coarse powder is recovered as an aggregating material for clayey soil. Method for producing agglomerated materials for clay soil.
【請求項3】 請求項1において、回収した粗粒を表面
剥離処理した後、粗粉と細粉とに分級し、この粗粉及び
細粉を粘土質土壌の団粒化材として回収することを特徴
とする粘土質土壌の団粒化材の製造方法。
3. The method according to claim 1, wherein the collected coarse particles are subjected to a surface peeling treatment, then classified into coarse powder and fine powder, and the coarse powder and the fine powder are recovered as an agglomerated material for clayey soil. A method for producing an agglomerated material for clayey soil, characterized by comprising:
JP6039460A 1994-03-10 1994-03-10 Method for producing agglomerated material for clayey soil Expired - Lifetime JP2590726B2 (en)

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Application Number Priority Date Filing Date Title
JP6039460A JP2590726B2 (en) 1994-03-10 1994-03-10 Method for producing agglomerated material for clayey soil

Publications (2)

Publication Number Publication Date
JPH07246375A JPH07246375A (en) 1995-09-26
JP2590726B2 true JP2590726B2 (en) 1997-03-12

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