JPH09192699A - Treatment of sludge and treated matter of sludge for cement starting material - Google Patents

Treatment of sludge and treated matter of sludge for cement starting material

Info

Publication number
JPH09192699A
JPH09192699A JP8029931A JP2993196A JPH09192699A JP H09192699 A JPH09192699 A JP H09192699A JP 8029931 A JP8029931 A JP 8029931A JP 2993196 A JP2993196 A JP 2993196A JP H09192699 A JPH09192699 A JP H09192699A
Authority
JP
Japan
Prior art keywords
sludge
water content
mixture
treated
less
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
JP8029931A
Other languages
Japanese (ja)
Inventor
Keiichi Usukura
桂一 臼倉
Takao Tanosaki
隆雄 田野崎
Kenji Nozaki
賢二 野崎
Masaru Shirasaka
優 白坂
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.)
Chichibu Onoda Cement Corp
Original Assignee
Chichibu Onoda Cement 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 Chichibu Onoda Cement Corp filed Critical Chichibu Onoda Cement Corp
Priority to JP8029931A priority Critical patent/JPH09192699A/en
Publication of JPH09192699A publication Critical patent/JPH09192699A/en
Pending legal-status Critical Current

Links

Abstract

PROBLEM TO BE SOLVED: To use effectively and stably a sludge while reducing an energy cost and a usage of calcium oxide by mixing calcium oxides to the sludge containing more than specified amount water content to reduce the water content of the mixture to a specified range. SOLUTION: At the time of treating an org. sewerage sludge, the calcium oxides are mixed to the sludge having <=60% water content to control the water content of the mixture in >=15% and <=60%, preferably in >=20% and <=35%, and the mixture controlled the water content is heat treated to control the water content in <=10%. At the time of treating a treated matter of the sludge for a cement starting material, the calcium oxides are mixed to the sludge to control the water content of the mixture in >=15% and <=60%, preferably in >=20% and <=35%, and the obtained mixture is heat treated. The treated matter of the sludge treated in such a way is used as the cement starting material, that is, an org. matter in the treated matter is used effectively as a part of a fuel and an inorg. matter is used effectively as a part of the starting material.

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、汚泥、特に有機
性下水汚泥の処理方法、及びセメント製造用原料の一部
として用いるセメント原料用汚泥処理物に関するもので
ある。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating sludge, particularly organic sewage sludge, and a treated sludge for cement raw material used as a part of a raw material for cement production.

【0002】[0002]

【従来の技術】近年、下水道網の整備拡大に伴い汚泥の
発生量は増加の一途をたどっている。下水汚泥の処理方
法としては、従来、重油のような助燃用燃料を加えて焼
却し、焼却灰を埋立て処分するのが一般的であったが、
最終処分先の埋立て地の確保が困難になりつつあり、下
水処理産物の有効利用法の開発が望まれている。
2. Description of the Related Art In recent years, the amount of sludge generated has been increasing with the expansion of sewer network. Conventionally, as a method of treating sewage sludge, it has been common to add incinerator fuel such as heavy oil to incinerate, and to dispose of incinerated ash in landfill.
It is becoming difficult to secure landfill sites for final disposal, and development of effective utilization methods for sewage treatment products is desired.

【0003】このような中にあって、汚泥を生石灰等と
混合し、生石灰の消和熱を利用して脱水した上でセメン
ト原料または製鉄用焼結原料として利用する技術(特開
平3−98700号、特開平3−207497号)が注
目される。セメント製造工程または製鉄工程では、10
00℃以上の炉を用いて原料を焼結しており、汚泥・石
灰混合物をこれらの炉に投入すると、混合物中の有機物
は燃料の一部として、また無機物は原料の一部として有
効利用され、しかも既存のセメント製造設備や製鋼設備
をそのまま利用できる利点があり、汚泥の大量処理が可
能である。
[0003] In such a situation, a technique of mixing sludge with quick lime and the like, dehydrating it by utilizing the heat of dehydration of quick lime, and then using it as a raw material for cement or a sintering raw material for iron making (Japanese Patent Laid-Open No. 3-98700) No. 3-207497). 10 in cement manufacturing process or iron manufacturing process
The raw materials are sintered in a furnace at a temperature of 00 ° C or higher, and when the sludge / lime mixture is put into these furnaces, the organic substances in the mixture are effectively used as a part of the fuel, and the inorganic substances are effectively used as a part of the raw material. Moreover, there is an advantage that existing cement manufacturing equipment and steelmaking equipment can be used as they are, and a large amount of sludge can be treated.

【0004】[0004]

【発明が解決しようとする課題】しかしながら上記処理
方法において、一般に汚泥は処理場で機械的な濃縮、脱
水等の工程を経て汚泥ケーキとされるが、このように機
械的に脱水された汚泥ケーキは、その性質上、含水率6
0〜100%、通常は含水率70〜90%(%はいずれ
も重量%を示す。以下同様。)程度までしか水分を低下
することができない。すなわち、濃縮された下水処理沈
殿から水分を分離してケ−キ状にする脱水工程は、真空
脱水器、フィルタ−プレス、ベルトプレス、遠心脱水器
等各種の脱水器が用いられているが、単なる機械的脱水
では含水量を80%以下にすることは非常に困難となっ
ている。これは主として、有機分(下水汚泥の固形分の
90%程度以上)における内部水、表面付着水、更には
毛管凝結水の結合が大きいためと考えられ、真空圧、遠
心力を高める等行っても動力コストに比べ、脱水特性が
極端に低下するためといわれている。
However, in the above-mentioned treatment method, sludge is generally treated as sludge cake in the treatment plant through steps such as mechanical concentration and dewatering. The sludge cake mechanically dewatered in this way is used. Has a water content of 6 due to its nature.
The water content can be reduced only to 0 to 100%, usually to a water content of 70 to 90% (% indicates weight%, the same applies hereinafter). That is, in the dehydration step of separating water from the concentrated sewage treatment precipitate to form a cake, various dehydrators such as a vacuum dehydrator, a filter-press, a belt press, and a centrifugal dehydrator are used. It is very difficult to reduce the water content to 80% or less by merely mechanical dehydration. It is considered that this is mainly due to the large amount of internal water, organic water adhering to the surface, and capillary condensed water in the organic matter (about 90% or more of the solid content of the sewage sludge). It is said that the dehydration property is extremely deteriorated compared to the power cost.

【0005】一方、コロイド状粒子を形成している水
(表面付着水)や活性汚泥フロック内部に存在する水は
適切な脱水助剤を加えることにより、ろ過性能が向上す
ることが知られており、無機系助剤として消石灰、塩化
第2鉄等あるいは有機高分子凝集剤を添加して、凝集さ
せ水分の低減を図ることができる。しかしながら、高分
子凝集剤は高価であり、また、消石灰では多量の添加を
必要とし、汚泥の量を著く増加させるので近年その使用
が避けられるきらいがあり、下水処理場の脱水工程で汚
泥の水分量を60%未満に処理することには限界があ
る。
On the other hand, it is known that the water forming the colloidal particles (water adhering to the surface) and the water existing inside the flocs of the activated sludge can improve the filtration performance by adding an appropriate dehydrating auxiliary. It is possible to reduce the water content by adding slaked lime, ferric chloride or the like as an inorganic auxiliary agent or an organic polymer coagulant to cause coagulation. However, polymer flocculants are expensive, and in the case of slaked lime, it is necessary to add a large amount, and since the amount of sludge is significantly increased, there is a tendency to avoid its use in recent years. There is a limit in treating the water content to less than 60%.

【0006】従って、高含水率の汚泥ケーキに生石灰を
添加し、その消和熱により汚泥を乾燥するためには、大
量の生石灰を添加せざるを得ず、処理汚泥量に対し、生
成処理物の重量が大幅に増大し、前述したセメント製造
設備や製鋼設備をそのまま利用できるものの、汚泥の処
理効率、使用効率が悪いほか、添加する生石灰自体のコ
ストのみならず、生成した処理物の輸送コストも上昇
し、全体の処理コストが高くなり、前記技術の普及を妨
げる原因となっている。
Therefore, in order to add quicklime to a high-moisture content sludge cake and to dry the sludge due to its heat of dehydration, a large amount of quicklime must be added, and the amount of produced sludge relative to the amount of sludge to be treated must be increased. Although the cement manufacturing equipment and steelmaking equipment described above can be used as they are, the sludge treatment efficiency and use efficiency are poor, and not only the cost of the quicklime to be added itself but also the transportation cost of the generated treated product. This also raises the overall processing cost and hinders the popularization of the technology.

【0007】このため、出願人は、焼却炉の排ガスや消
化ガス、燃焼排ガスを利用した熱風乾燥等により水分6
0重量%以下、好ましくは、20〜50重量%の範囲ま
で下水汚泥を乾燥した上で、生石灰を混合することによ
り、生石灰の混合量を低減した汚泥の処理方法及び処理
装置を提案した(特願平7−136035号)。しか
し、この場合も、高含水状態での乾燥は、熱効率上必ず
しも満足できないものであった。
For this reason, the Applicant has proposed that the moisture content of the incinerator exhaust gas, digestive gas, hot air drying using combustion exhaust gas, etc.
A sewage sludge was dried to a range of 0% by weight or less, preferably 20 to 50% by weight, and then mixed with quicklime, thereby proposing a sludge treatment method and a treatment apparatus with a reduced mixed amount of quicklime (special feature: Japanese Patent Application No. 7-136035). However, also in this case, drying in a high water content state was not always satisfactory in terms of thermal efficiency.

【0008】この発明は、前記欠点を解消し、きわめて
少量のエネルギ−コストで生石灰の使用量を大幅に減少
させると共に、生成処理物の重量を減少させることによ
り、ランニングコストを大幅に低減し、汚泥を効果的、
安定的に有効利用できる汚泥の処理方法及びセメント原
料用汚泥処理物を提供することを目的とする。
The present invention eliminates the above-mentioned drawbacks, greatly reduces the amount of quicklime used with a very small amount of energy cost, and reduces the weight of the produced product, thereby significantly reducing the running cost, Effective sludge,
It is an object of the present invention to provide a sludge treatment method and a sludge treated product for cement raw material that can be stably and effectively utilized.

【0009】[0009]

【課題を解決するための手段】上述の目的を達成するた
めにこの発明の汚泥の処理方法によれば、水分量60%
以上の汚泥に、生石灰類を混合し、混合物の水分量を1
5%以上、60%未満、好ましくは、20%以上、35
%未満とすること(請求項1)、水分量60%以上の汚
泥に、生石灰類を混合し、混合物の水分量を15%以
上、60%未満、好ましくは、20%以上、35%未満
としたのち、混合物を加熱処理し、水分量を10%以下
とすること(請求項2)、加熱処理が乾燥、焼却、加熱
溶融処理のいずれか一種であること(請求項3)、を特
徴とする。
According to the sludge treatment method of the present invention to achieve the above object, the water content is 60%.
Mix the above sludge with quicklime and adjust the water content of the mixture to 1
5% or more and less than 60%, preferably 20% or more, 35
% (Claim 1), quicklime is mixed with sludge having a water content of 60% or more, and the water content of the mixture is 15% or more and less than 60%, preferably 20% or more and less than 35%. After that, the mixture is heat treated to reduce the water content to 10% or less (Claim 2), and the heat treatment is any one of drying, incineration and heat melting treatment (Claim 3). To do.

【0010】また、この発明のセメント原料用汚泥処理
物によれば、汚泥に、生石灰類を混合し、混合物の水分
量を15%以上、60%未満、好ましくは、20%以
上、35%未満としてなること(請求項4)、汚泥に、
生石灰類を混合し、混合物の水分量を15%以上、60
%未満、好ましくは、20%以上、35%未満とし、該
混合物を加熱処理してなること(請求項5)、を特徴と
する。
According to the treated sludge for cement raw material of the present invention, quicklime is mixed with the sludge and the water content of the mixture is 15% or more and less than 60%, preferably 20% or more and less than 35%. (Claim 4), in sludge,
Quicklime is mixed and the water content of the mixture is 15% or more, 60
%, Preferably 20% or more and less than 35%, and the mixture is heat-treated (Claim 5).

【0011】[0011]

【発明の実施の形態】この発明で処理する汚泥は、主に
下水処理場で発生する汚泥であるが、この他に、し尿、
家庭用雑排水、産業用排水処理などによって発生した汚
泥を含む。前述したように、これらの汚泥は一般に処理
場で含水率60〜100%、通常は70〜90%程度ま
で脱水処理されており、本発明はこの下水汚泥を使用す
る。
BEST MODE FOR CARRYING OUT THE INVENTION The sludge treated according to the present invention is mainly sludge generated in a sewage treatment plant.
Includes sludge generated from domestic wastewater and industrial wastewater treatment. As described above, these sludges are generally dehydrated in the treatment plant to a water content of 60 to 100%, usually 70 to 90%, and the present invention uses this sewage sludge.

【0012】この発明において、前記水分量60%以上
の脱水汚泥に生石灰類を混合する。生石灰類とは、Ca
Oを主成分とし、下水汚泥の水分を取り込んで消石灰類
になるものを言い、具体的には、生石灰、仮焼ドロマイ
ト、高炉スラグ、コンクリ−ト粉砕微粉などが含まれ
る。生石灰類の粒度は粒径70mm以下、好ましくは3
0mm程度以下であれば良い。
In the present invention, quicklime is mixed with the dehydrated sludge having a water content of 60% or more. Quicklime is Ca
It contains O as a main component and takes in the water of the sewage sludge to form slaked limes. Specifically, quick lime, calcined dolomite, blast furnace slag, concrete pulverized fine powder and the like are included. The particle size of quicklime is 70 mm or less, preferably 3
It may be about 0 mm or less.

【0013】生石灰類の混合量は、汚泥の水分量にもよ
るが、前記汚泥の水分量100部に対し、10重量%以
上、最大50部未満(例えば、水分量80%の汚泥10
0部に対し、生石灰40部未満)とし、混合物の水分量
を15%以上、60%未満、好ましくは、20%以上、
35%未満の範囲に止める。すなわち、CaOと汚泥水
分との消和反応及びその消和時に発生する熱により水分
量が規制された汚泥処理物を得る。この範囲に水分量が
規制された汚泥処理物は、後述するセメント原料として
十分使用可能であり、しかも、消和熱により高温殺菌さ
れ、さらに高アルカリ分含有の変質のない処理物であ
る。汚泥処理物の水分量がこの範囲より多いと、生石灰
類の添加効果がなく、処理物の腐敗の可能性があるほ
か、次工程での水分低減処理が多大となる。また、汚泥
の残留水分がこの範囲よりも少ないと、生石灰の添加量
が多くなり過ぎ、生成処理物の水分低減効果以上に生石
灰コストが上昇するすると共に、処理物の重量が増大
し、好ましくない。
The mixing amount of quicklime depends on the water content of the sludge, but is 10% by weight or more and less than 50 parts at maximum (for example, the sludge having a water content of 80% is 100 parts by weight of the sludge.
0 parts to 40 parts of quick lime), and the water content of the mixture is 15% or more and less than 60%, preferably 20% or more,
Keep within the range of less than 35%. That is, a sludge treated product in which the amount of water is regulated by the soaking reaction between CaO and sludge moisture and the heat generated during the soaking is obtained. The sludge treated product whose water content is regulated in this range can be sufficiently used as a cement raw material to be described later, and is a treated product that is sterilized at high temperature by heat of soaking and has a high alkali content and is not deteriorated. If the water content of the sludge treatment product is higher than this range, there is no effect of adding quick lime, the treatment product may be spoiled, and the water reduction treatment in the next step becomes large. Further, if the residual water content of the sludge is less than this range, the amount of quick lime added becomes too large, and the quick lime cost increases more than the water reduction effect of the produced treated product, and the weight of the treated product increases, which is not preferable. .

【0014】また、前記下水汚泥に生石灰類を添加混合
するにあたり、下水汚泥は、表面が乾燥すると固くな
り、内部に水分が残留するので、単に生石灰と混合する
だけでは、残留水分と生石灰の消和反応が十分でない。
従って、好適には乾燥汚泥と生石灰の混合と共に粉砕を
行い、生石灰と残留水分の接触を十分に行わしめ、粉粒
体化させる。粉砕は、ボ−ルミル、縦型ミル、媒体撹拌
ミル等各種の粉砕機を使用することができる。
In addition, in adding and mixing quicklime to the sewage sludge, the surface of the sewage sludge becomes hard when the surface is dried, and the water remains inside. Therefore, simply mixing with the quicklime removes the residual water and quicklime. The sum reaction is not enough.
Therefore, the dry sludge and the quick lime are preferably mixed together and pulverized to sufficiently bring the quick lime into contact with the residual water to form a granular material. For the pulverization, various pulverizers such as a ball mill, a vertical mill and a medium stirring mill can be used.

【0015】このように処理した汚泥処理物は、セメン
ト原料用として好適に使用することができる。すなわ
ち、処理物中の有機物は燃料の一部として、また無機物
は原料の一部として有効利用され、しかも既存のセメン
ト製造設備をそのまま利用することができる。セメント
としては、普通、早強、中庸熱等のポルトランドセメン
トやアルミナセメント、都市ゴミ灰を主原料とするアリ
ナイト系セメント等、各種のセメント原料に用いること
ができる。
The sludge-treated product thus treated can be suitably used as a raw material for cement. That is, the organic matter in the treated material is effectively used as a part of the fuel, and the inorganic matter is effectively used as a part of the raw material, and the existing cement production equipment can be used as it is. As the cement, it is possible to use various kinds of cement raw materials such as portland cement, alumina cement, and allinite cement whose main raw material is municipal waste ash as a main raw material.

【0016】前記既存のセメント製造設備にあっては、
セメント原料である石灰石、粘土、鉄源材料等の粉砕設
備、混合設備、乾燥設備を既に保有しており、これら設
備を活用して前記水分量が規制された汚泥処理物をセメ
ント原料として使用することができる。例えば、粉砕設
備において、汚泥処理物の水分量が15%以上、60%
未満、好ましくは、20%以上、35%未満の範囲にあ
れば、処理物がミル側壁や粉砕ボ−ルへの付着を問題に
する必要もなく、また、乾燥設備において、既存の石灰
石や粘土などの乾燥と同程度のエネルギ−コストで済
む。
In the existing cement manufacturing facility,
We already have crushing equipment, mixing equipment, and drying equipment for cement raw materials such as limestone, clay, and iron source materials. Utilizing these equipment, the sludge treated material whose water content is regulated is used as the cement raw material. be able to. For example, in crushing equipment, the water content of sludge treatment product is 15% or more, 60%
If it is less than 20%, preferably less than 35%, it is not necessary for the treated material to adhere to the mill side wall or the grinding ball, and the existing limestone or clay in the drying equipment is not required. Energy cost similar to drying.

【0017】以上説明したように、汚泥処理物の水分量
を15%以上、60%未満、好ましくは、20%以上、
35%未満の範囲に規制することにより、これを既存の
セメント製造設備に適用することにより、十分にセメン
ト原料用汚泥処理物とすることができるが、さらに混合
物を乾燥処理し、水分量を10%以下としてセメント原
料用汚泥処理物とすることもできる。すなわち、生石灰
類が混合された汚泥混合物は、既に水分量が規制されて
おり、少ない熱量で水分量を10%以下にすることがで
き、さらに減量化した形で、しかも流動性が良く取り扱
いやすい粉粒体状でセメント工場へ運搬することができ
る。乾燥手段としては、焼却炉の排ガスや消化ガス、燃
焼排ガスを利用した熱風乾燥やスチーム等の温度200
℃程度以下の熱媒を利用した乾燥が好適に用いられる。
As described above, the sludge treated product has a water content of 15% or more and less than 60%, preferably 20% or more,
By restricting the content to less than 35% and applying it to the existing cement manufacturing equipment, it can be sufficiently treated as a sludge for cement raw material, but the mixture is further dried to obtain a water content of 10%. It is also possible to use a sludge treated product as a raw material for cement at a content of not more than%. In other words, the water content of the sludge mixture in which quicklime is mixed is already regulated, and the water content can be reduced to 10% or less with a small amount of heat. It can be transported to the cement factory in the form of powder. As a drying means, a hot air drying method using exhaust gas from an incinerator, a digestive gas, or a combustion exhaust gas, a temperature of steam or the like of 200
Drying using a heating medium at about ℃ or less is preferably used.

【0018】また、下水処理場においては、脱水汚泥の
焼却設備や加熱溶融設備を既に所有、或いは設置を予定
するところも多いが、このような焼却設備や加熱溶融設
備を利用して、前記生石灰類が混合され、水分量が規制
された汚泥混合物を処理することもできる。汚泥混合物
の焼却や加熱溶融処理においては、混合物中のCa成分
の共存下で、SOxやNOxの発生が少なく、効果的に
処理することができ、得られた焼却灰、あるいは、溶融
灰(スラグ)はさらに減量化された形でセメント工場に
運搬し、好適にセメント原料とすることができる。特に
溶融処理において、汚泥混合物を加熱溶融後、急冷処理
して得られるガラス質の処理品は、前記セメント原料と
しての活用は無論のこと、既に高炉スラグ並みの混合材
特性を有しており、セメント混和材、あるいは、混合セ
メントとして活用することができる。
In many sewage treatment plants, incinerators and heating / melting equipment for dehydrated sludge are already owned or are planned to be installed. It is also possible to treat a sludge mixture in which the substances are mixed and the water content is regulated. In the incineration and heat melting treatment of sludge mixture, SOx and NOx are less generated in the presence of Ca component in the mixture and can be effectively treated. The obtained incinerated ash or molten ash (slag ) Can be transported to a cement factory in a further reduced form, and can be suitably used as a cement raw material. Especially in the melting treatment, after heating and melting the sludge mixture, the glassy treated product obtained by quenching is of course utilized as the cement raw material, and already has the mixing material characteristics of blast furnace slag, It can be used as a cement admixture or a mixed cement.

【0019】[0019]

【実施例】【Example】

(実施例1)水分量80%の脱水汚泥100重量部に生
石灰12重量部、及び36重量部(水分量に対する添加
割合15%、及び45%)をヘンシェルミキサーで混合
し、この発明のセメント原料用汚泥処理物A:76重量
部(水分量58%)、及びB:85重量部(水分量34
%)を得た。次に、得られた処理物A、B各50重量部
に、セメント調合原料100重量部を加え、ボ−ルミル
で20分間粉砕した。粉砕に当たり、処理物A、Bはミ
ル側壁やボ−ルへの処理物の付着も少なく充分実用性の
あるものであった。また、比較例として、水分量80%
の脱水汚泥100重量部に生石灰5.6重量部、及び8
8重量部(水分量に対する添加割合7%、及び110
%)を混合し、混合物C:94重量部(水分量73
%)、及びD:120重量部(水分量10%)を得ると
共に、混合物C、D各50重量部に、セメント調合原料
100重量部を加えて、同様に粉砕した。混合物Cは、
ミル側壁やボ−ルへの付着量が32重量部にもなり、実
用的な粉砕操作をすることができなかった。また、混合
物Dは、ミルへの付着は少ないものの、生石灰の添加量
が多くなり過ぎ、水分低減効果以上に生石灰コストが上
昇するすると共に、処理物の重量が増大した。
(Example 1) 100 parts by weight of dehydrated sludge having a water content of 80% was mixed with 12 parts by weight of quick lime and 36 parts by weight (addition ratios of 15% and 45% with respect to the amount of water) with a Henschel mixer to prepare a cement raw material of the present invention. Sludge treatment product A: 76 parts by weight (water content 58%) and B: 85 parts by weight (water content 34%)
%) Was obtained. Next, 100 parts by weight of the cement compounding raw material was added to 50 parts by weight of each of the obtained treated products A and B, and the mixture was ground for 20 minutes with a ball mill. Upon pulverization, the treated products A and B were sufficiently practical because there was little adhesion of the treated products to the mill side wall or ball. As a comparative example, the water content is 80%.
5.6 parts by weight of quicklime and 8 parts by weight of dehydrated sludge of
8 parts by weight (addition ratio to water content 7%, and 110
%), And the mixture C: 94 parts by weight (water content 73
%) And D: 120 parts by weight (water content 10%), 100 parts by weight of the cement compounding raw material was added to 50 parts by weight of each of the mixtures C and D, and the mixture was ground in the same manner. Mixture C is
The amount adhering to the side wall of the mill and the ball was as much as 32 parts by weight, and a practical crushing operation could not be performed. In addition, although the mixture D was less attached to the mill, the amount of quick lime added was too large, the quick lime cost increased more than the moisture reduction effect, and the weight of the treated product increased.

【0020】(実施例2)次に、実施例1で得られた混
合物A、B各15重量部をセメント調合原料85重量部
に混合の上、1450℃の電気炉で焼成してセメントク
リンカ−を得た。このクリンカーに石膏を加えて混合粉
砕し、ブレ−ン比表面積3000cm2 /gのセメントを
得、JIS R 5201 に準拠して、セメントテス
トを行ったところ通常のセメントに比べ凝結時間、強度
等何ら遜色なかった。
(Example 2) Next, 15 parts by weight of each of the mixtures A and B obtained in Example 1 were mixed with 85 parts by weight of a cement compounding raw material, and the mixture was fired in an electric furnace at 1450 ° C to obtain a cement clinker. Got Gypsum was added to this clinker and mixed and pulverized to obtain a cement having a brain specific surface area of 3000 cm 2 / g. A cement test was carried out in accordance with JIS R 5201. It was as good as that.

【0021】(実施例3)実施例1で得られた混合物
A、及びCを加熱処理後、溶融固化した。混合物Cが分
解点550℃で有機分が酸化されるのに対し、混合物A
の分解点は300℃と250℃も低減できた。次いで混
合物Aの溶融工程では、通常1600℃のガラス化が1
450℃に低減でき、溶融ガラスの粉砕品は高炉スラグ
並のセメント混合材特性(28日材令強度比98%)を
示した。
Example 3 Mixtures A and C obtained in Example 1 were heat treated and then melted and solidified. While the organic components of the mixture C are decomposed at the decomposition point of 550 ° C., the mixture A is mixed.
The decomposition point of was reduced by 300 ° C and 250 ° C. Then, in the melting step of the mixture A, vitrification at 1600 ° C is usually 1
It was possible to reduce the temperature to 450 ° C., and the crushed product of the molten glass exhibited the characteristics of a cement mixture similar to that of blast furnace slag (98 days old strength ratio 98%).

【0022】[0022]

【発明の効果】この発明によれば以下に示す極めて優れ
た効果を有する。 (1)汚泥に生石灰等混合し、水分量が規制された汚泥
処理物とし、きわめて少量のエネルギ−コストでセメン
ト資源化プロセスに支障ない処理を可能とする。 (2)生石灰の量を低減し、生成処理物の重量を減少さ
せることにより、大幅なコスト低減が可能となる。 (3)焼却灰、溶融スラグ等も効果的にセメント資源化
でき、多方面のリサイクル適用が可能となる等、汚泥を
効果的、安定的に有効利用できる。
According to the present invention, the following excellent effects can be obtained. (1) Mixing quicklime and the like into sludge to produce a sludge treated product having a regulated water content, which enables treatment that does not interfere with the cement resource recycling process with an extremely small energy cost. (2) By reducing the amount of quicklime and reducing the weight of the processed product, it is possible to significantly reduce the cost. (3) Incinerated ash, molten slag, etc. can be effectively recycled as cement resources, and can be recycled in various fields, and sludge can be used effectively and stably.

───────────────────────────────────────────────────── フロントページの続き (72)発明者 白坂 優 千葉県佐倉市大作二丁目4番2号 秩父小 野田株式会社中央研究所内 ─────────────────────────────────────────────────── ─── Continued Front Page (72) Inventor Yu Shirasaka 2-4 Daisaku, Sakura City, Chiba Prefecture Chichibu Onoda Central Research Institute

Claims (5)

【特許請求の範囲】[Claims] 【請求項1】 水分量60%以上の汚泥に、生石灰類を
混合し、混合物の水分量を15%以上、60%未満、好
ましくは、20%以上、35%未満とすることを特徴と
する汚泥の処理方法。
1. Sludge having a water content of 60% or more is mixed with quicklime, and the water content of the mixture is 15% or more and less than 60%, preferably 20% or more and less than 35%. Sludge treatment method.
【請求項2】 水分量60%以上の汚泥に、生石灰類を
混合し、混合物の水分量を15%以上、60%未満、好
ましくは、20%以上、35%未満としたのち、混合物
を加熱処理し、水分量を10%以下とすることを特徴と
する汚泥の処理方法。
2. A sludge having a water content of 60% or more is mixed with quicklime, and the water content of the mixture is adjusted to 15% or more and less than 60%, preferably 20% or more and less than 35%, and then the mixture is heated. A method for treating sludge, which comprises treating the treated water to a water content of 10% or less.
【請求項3】 加熱処理が乾燥、焼却、加熱溶融処理の
いずれか一種であることを特徴とする請求項2記載の汚
泥の処理方法。
3. The method for treating sludge according to claim 2, wherein the heat treatment is any one of drying, incineration, and heat melting treatment.
【請求項4】 汚泥に、生石灰類を混合し、混合物の水
分量を15%以上、60%未満、好ましくは、20%以
上、35%未満としてなることを特徴とするセメント原
料用汚泥処理物。
4. A sludge treated product for cement raw material, characterized in that quick limes are mixed with sludge, and the water content of the mixture is 15% or more and less than 60%, preferably 20% or more and less than 35%. .
【請求項5】 汚泥に、生石灰類を混合し、混合物の水
分量を15%以上、60%未満、好ましくは、20%以
上、35%未満とし、該混合物を加熱処理してなること
を特徴とするセメント原料用汚泥処理物。
5. The sludge is mixed with quicklime, the water content of the mixture is adjusted to 15% or more and less than 60%, preferably 20% or more and less than 35%, and the mixture is heat-treated. Sludge treatment product for cement raw material.
JP8029931A 1996-01-24 1996-01-24 Treatment of sludge and treated matter of sludge for cement starting material Pending JPH09192699A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP8029931A JPH09192699A (en) 1996-01-24 1996-01-24 Treatment of sludge and treated matter of sludge for cement starting material

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP8029931A JPH09192699A (en) 1996-01-24 1996-01-24 Treatment of sludge and treated matter of sludge for cement starting material

Publications (1)

Publication Number Publication Date
JPH09192699A true JPH09192699A (en) 1997-07-29

Family

ID=12289742

Family Applications (1)

Application Number Title Priority Date Filing Date
JP8029931A Pending JPH09192699A (en) 1996-01-24 1996-01-24 Treatment of sludge and treated matter of sludge for cement starting material

Country Status (1)

Country Link
JP (1) JPH09192699A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011013491A1 (en) * 2009-07-29 2011-02-03 Araki Hiroshi Method for treatment of sludge, and facility for the treatment
CN113801992A (en) * 2020-06-17 2021-12-17 宝山钢铁股份有限公司 Sintering digestion method of municipal sludge
KR20220085443A (en) * 2020-12-15 2022-06-22 김인식 Method for Reduction of Waste Sludge

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2011013491A1 (en) * 2009-07-29 2011-02-03 Araki Hiroshi Method for treatment of sludge, and facility for the treatment
CN113801992A (en) * 2020-06-17 2021-12-17 宝山钢铁股份有限公司 Sintering digestion method of municipal sludge
CN113801992B (en) * 2020-06-17 2023-02-14 宝山钢铁股份有限公司 Sintering digestion method of municipal sludge
KR20220085443A (en) * 2020-12-15 2022-06-22 김인식 Method for Reduction of Waste Sludge

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