JPS6071100A - Sludge treating method - Google Patents
Sludge treating methodInfo
- Publication number
- JPS6071100A JPS6071100A JP58181599A JP18159983A JPS6071100A JP S6071100 A JPS6071100 A JP S6071100A JP 58181599 A JP58181599 A JP 58181599A JP 18159983 A JP18159983 A JP 18159983A JP S6071100 A JPS6071100 A JP S6071100A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- added
- kneaded
- dehydrated cake
- dehydrating
- 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.)
- Granted
Links
Landscapes
- Gasification And Melting Of Waste (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、下水汚泥、し尿汚泥、浄化4′fJfF5泥
などの各種汚泥をケイ酸アルカリを利用して効率よく処
理する方法に関するものである。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for efficiently treating various sludges such as sewage sludge, human waste sludge, and purified 4'fJfF5 mud using alkali silicate.
従来、汚泥の処理方法として、特開昭52−51746
号公報に示−すように、汚泥にケイ酸すトリウム系凝固
剤を添加し、これに熱を加えて水熱反応により砂れきに
類似した硬質団粒を生成せしめる技術が開示されている
。この先行技術において、必要な熱エネルギーは他分野
よりの移動によりなされ、きわめて不経済で非効率的で
あり、かつその凝結反応も熱エネルギーのみでは、反応
速度が遅いという問題がある。Conventionally, as a sludge treatment method, Japanese Patent Application Laid-Open No. 52-51746
As shown in the publication, a technique is disclosed in which a thorium silicate coagulant is added to sludge, and heat is applied thereto to generate hard aggregates similar to gravel through a hydrothermal reaction. In this prior art, the necessary thermal energy is transferred from another field, which is extremely uneconomical and inefficient, and the condensation reaction also has a problem in that the reaction rate is slow if thermal energy alone is used.
本発明者らは」二記の問題を解決するだめに鋭意研究を
重ねた結果、粘結、硬化作用のあるケイ酸ナトリウム、
ケイ酸カリウムなどのケイ酸アルカリを下水汚泥、し尿
汚泥、浄化槽汚泥などに利用することにより、経済的、
効率的な汚泥処理を行えることを知見した。The inventors of the present invention have conducted extensive research in order to solve the problems mentioned in 2.
By using alkali silicates such as potassium silicate for sewage sludge, human waste sludge, septic tank sludge, etc., it is possible to improve economical and
It was discovered that efficient sludge treatment can be performed.
本発明は上記の知見に基づき々されたもので、下水汚泥
、し尿汚泥、浄化槽汚泥ガどの各種汚泥を処理する方法
において、汚泥を脱水した脱水ケーキにケイ酸アルカリ
を添加、混練した後、酸を添加し混練してpH調整を行
い、ついで混合物に汚泥の焼却炉を含む各種工業炉の燃
焼排ガスを直接接触せしめて、脱水ケーキを乾燥凝固さ
せることにより、排ガスの顕熱の助けによる乾燥凝固作
用と、排ガス中に常に多量に含まれる二酸化炭素とケイ
酸アルカリとの化学反応による硬化促進との相乗効果に
よって、短時間で硬質な脱水ケーキの凝固物を得ること
ができる汚泥の処理方法を提供せんとするものである。The present invention has been made based on the above knowledge, and is a method for treating various types of sludge such as sewage sludge, human waste sludge, and septic tank sludge. is added and kneaded to adjust the pH, and then the mixture is brought into direct contact with combustion exhaust gas from various industrial furnaces, including sludge incinerators, to dry and solidify the dehydrated cake. We developed a sludge treatment method that can obtain a hard coagulated dehydrated cake in a short period of time through the synergistic effect of this action and the acceleration of hardening due to the chemical reaction between carbon dioxide, which is always contained in large amounts in exhaust gas, and alkali silicate. This is what we intend to provide.
本発明の方法において、炭酸ガスを含有する汚泥焼却炉
排ガスを再循環使用することにより、一層の効率化を図
ることができる。この反応は、Na2O・nSiO2+
mH2O+CO2→Na2C○3+nS i O2−m
H2Oで示され、シリカゲルが泥質を強固にし、離漿現
象により浮離された水は早期に乾燥される。!f、た本
反応により得られた硬質物質は、水により再溶解しない
不可逆ゲルにより構成されており、後工程の焼却処分に
おいて一層の効率的、経済的効果が得られる。In the method of the present invention, further efficiency can be achieved by recycling and using the sludge incinerator exhaust gas containing carbon dioxide gas. This reaction is based on Na2O・nSiO2+
mH2O+CO2→Na2C○3+nS i O2-m
Indicated by H2O, silica gel strengthens the mud, and the water floated away due to the syneresis phenomenon dries quickly. ! f. The hard substance obtained by this reaction is composed of an irreversible gel that does not dissolve again in water, and more efficient and economical effects can be obtained in the post-process incineration disposal.
以下、本発明の構成を図面に基づいて説明する。Hereinafter, the configuration of the present invention will be explained based on the drawings.
第1図は本発明の一例を示している。汚泥を脱水設備1
に導入し、凝集剤(有機系高分子凝集剤、無機系凝集剤
)を添加して脱水した後、混練槽2に導入しケイ酸す)
IJウムを添加して混練し、ついで混練槽3に導入し
酸を添加し混練してpHを6.5〜8に調整する。つい
で混合物を凝固乾iv!器4に導入し高温で多量の炭酸
ガスを含む汚泥焼却炉5からの排ガスと直接接触させる
。水夕)反応、離漿作用により短時間で硬質の脱水ケー
キの凝固物を生成し、かつ凝固物の一部を粉砕機6で粉
砕して前記脱水工程の脱水助剤として脱水設備lへ循環
再使用する。凝固物の残部は焼却炉5で焼却し、焼却灰
をマイクロ波溶融炉などの溶融炉7で溶融同化処理して
流動化させる。凝固乾燥器4から出る凝固物は、硬質不
溶解物で前述のように脱水助剤として利用できるととも
に、低含水率、高有機物含有であり、凝固前脱水ケーキ
と混合しても燃料価値は高く、焼却処分の省エネルギー
化を図ることができる。また焼却炉5からの焼却灰はシ
リカ分を多量に含み、溶―物の流動化が促進され処理が
容易になる。FIG. 1 shows an example of the invention. Sludge dewatering equipment 1
After dehydration by adding a flocculant (organic polymer flocculant, inorganic flocculant), the mixture is introduced into the kneading tank 2 and silicic acid is added.
IJum is added and kneaded, then introduced into the kneading tank 3, and acid is added and kneaded to adjust the pH to 6.5-8. The mixture is then coagulated and dried iv! The sludge is introduced into the vessel 4 and brought into direct contact with the exhaust gas from the sludge incinerator 5 which is at high temperature and contains a large amount of carbon dioxide gas. Mizuyu) A hard dehydrated cake coagulate is produced in a short time by reaction and syneresis, and a part of the coagulate is crushed by a crusher 6 and circulated to the dehydration equipment 1 as a dehydration aid in the dehydration process. Reuse. The remainder of the solidified material is incinerated in an incinerator 5, and the incinerated ash is melted and assimilated in a melting furnace 7 such as a microwave melting furnace to be fluidized. The coagulated material coming out of the coagulation dryer 4 is a hard insoluble material that can be used as a dehydration aid as described above, and has a low moisture content and high organic matter content, and has high fuel value even when mixed with the dehydrated cake before coagulation. , it is possible to save energy during incineration. Furthermore, the incineration ash from the incinerator 5 contains a large amount of silica, which promotes fluidization of the molten material and facilitates treatment.
本発明において、凝集剤の添加率は汚泥固形物当す0.
5〜1.5wt%、ケイ酸ナトリウムの添加率は汚泥固
形物当り5〜15wt%である。In the present invention, the addition rate of the flocculant is 0.00% per sludge solids.
5-1.5 wt%, the addition rate of sodium silicate is 5-15 wt% based on sludge solids.
第2図は本発明の他の例を示している。第2図において
、汚水を最初沈殿池8、エアレーションタンク9、最終
沈殿池10で処理し、最終沈殿池10よりの余剰活性邑
泥を機械濃縮設備11により強制的に濃縮し、凝集剤に
より脱水を行う。脱水ケーキにケイ酸ナトリウムを加え
、酸にて中和した後、焼却炉5よりの排ガスの温度、炭
1・Ilクガスの働きにより凝固乾燥を行う。この凝固
乾燥により得られた凝固物は有機物含有率がきわめて高
く、硬質状である。一方、最初沈殿池8より引き抜かれ
た生汚泥は、重力式濃縮槽12で高濃度までl農縮され
ており、かつ性状的にも効率的な消化が可能である。こ
の濃縮汚泥を嫌気性消化槽13で処理する。嫌気性消化
汚泥は易脱水性に改良されており、この汚泥に砂質状の
凝固物を脱水助剤として使用し脱水設備14で脱水する
ことにより、きわめて低含水率の脱水ケーキが得られ、
この脱水ケーキと前−記砂質状凝固物を合わせ焼却する
ことにより、効率的燃焼を行うことができる。まだマイ
クロ波溶融炉などの溶融炉では、シリカ分の含有により
溶融物の流動化が図れ、効果的処理をすることができる
。他の構成は第1図の場合と同様である。FIG. 2 shows another example of the invention. In Fig. 2, sewage is treated in an initial sedimentation tank 8, an aeration tank 9, and a final sedimentation tank 10, and the surplus activated mud from the final sedimentation tank 10 is forcibly concentrated by a mechanical thickening equipment 11, and then dehydrated with a flocculant. I do. After adding sodium silicate to the dehydrated cake and neutralizing it with acid, it is coagulated and dried by the temperature of the exhaust gas from the incinerator 5 and the action of charcoal 1.Il gas. The coagulated product obtained by this coagulation drying has an extremely high organic matter content and is hard. On the other hand, the raw sludge extracted from the initial settling tank 8 is reduced to a high concentration in the gravity thickening tank 12, and its properties enable efficient digestion. This thickened sludge is treated in an anaerobic digestion tank 13. The anaerobic digested sludge has been improved to be easily dewaterable, and by dewatering this sludge in the dewatering equipment 14 using sandy coagulum as a dewatering aid, a dehydrated cake with an extremely low water content can be obtained.
By combining this dehydrated cake and the sandy coagulum and incinerating it, efficient combustion can be achieved. However, in a melting furnace such as a microwave melting furnace, the inclusion of silica allows the melt to be fluidized and can be effectively processed. The other configurations are the same as in the case of FIG.
また第3図は本発明のさらに他の例を示している。第3
図において、汚泥を脱水設備]に導入し、凝集剤を添加
して脱水した後、混練槽2に導入しケイ酸すトリウムを
添加して混練し、ついで混練(漕3で酸を添加してpH
調整した後、多段焼却炉15に投入する。脱水ケーキは
多段焼却炉の1段目で炭酸ガスを含む高温排ガスと接触
しながらティースにより攪拌されるため、速やかに乾燥
され凝固物となる。したがって乾燥に要する面積も少な
くてすみ、通常の多段炉と比較して炉の小型化を図るこ
とができる。Further, FIG. 3 shows still another example of the present invention. Third
In the figure, the sludge is introduced into the dewatering equipment, dehydrated by adding a flocculant, and then introduced into the kneading tank 2, where thorium silicate is added and kneaded, and then kneaded (acid is added in the tank 3). pH
After adjustment, it is put into the multistage incinerator 15. The dehydrated cake is agitated by teeth in the first stage of the multistage incinerator while coming into contact with high-temperature exhaust gas containing carbon dioxide gas, so it is quickly dried and becomes a solidified product. Therefore, the area required for drying is small, and the furnace can be made smaller compared to a normal multi-stage furnace.
つぎに本発明の実施例について説明する。Next, embodiments of the present invention will be described.
実施例
汚泥濃度2.5%の汚泥に高分子慶集剤1.□wt%(
汚泥固形物当り)添加し凝集反応させて脱水した後、ケ
イ酸ナトリウムlQwt%(汚泥固形物当り)添加して
混練し、ついで酸(硝酸)を添加し混練してpHを7.
0に調整した後、焼却炉排ガスに接触させて乾燥・凝固
物をつくり、そのうち80wt%を焼却炉に、20wt
%を粉砕し、細粒化して脱水工程の脱水助剤として使用
した。焼却炉排ガスの温度は300°C,、CO2濃度
7.5%、凝固乾燥時間は20分、凝固乾燥物含水率は
25%、焼却炉焼却温度は800°Cであった。Example 1. Adding a polymer sludge to sludge with a sludge concentration of 2.5%. □wt%(
After adding 1Qwt% of sodium silicate (based on sludge solids) and kneading, add 1Qwt% of sodium silicate (based on sludge solids) and knead to adjust the pH to 7.
After adjusting to 0, dry and coagulate by contacting with incinerator exhaust gas, 80wt% of which is sent to the incinerator, 20wt%
% was crushed, pulverized, and used as a dehydration aid in the dehydration process. The temperature of the incinerator exhaust gas was 300°C, the CO2 concentration was 7.5%, the coagulation drying time was 20 minutes, the moisture content of the coagulated dry material was 25%, and the incinerator burning temperature was 800°C.
以上説明したように、本発明の方法によればつぎのよう
な効果が得られる。As explained above, according to the method of the present invention, the following effects can be obtained.
(1) ケイ酸アルカリを使用した脱水ケーキの凝固物
は、低含水率で燃料価値の高い物質で省エネルギー燃焼
ができる。(1) The coagulated product of dehydrated cake using alkali silicate is a material with low moisture content and high fuel value, which can be burned in an energy-saving manner.
(2)汚泥焼却工程より発生する焼却排ガスの再使用を
図ることにより、凝固反応が促進されるとともに、焼却
炉での自燃燃焼と単純安価な焼却炉型式が選定でき、省
エネルギー化はもちろん、設備費の大幅な削減が図れる
。(2) By reusing the incineration exhaust gas generated in the sludge incineration process, the coagulation reaction is promoted, self-combustion combustion in the incinerator, and a simple and inexpensive incinerator type can be selected, which not only saves energy but also improves equipment. Significant cost reductions can be achieved.
(3)硬質、硬質状の高有機物含有の脱水ケーキが得ら
れ、この脱水ケーキを脱水助剤として脱水工程に再使用
する場合は、脱水効果の大幅な上昇が期待できるととも
に、脱水ケーキより作られた凝固物自身を脱水助剤とし
て再使用することになるので、脱水ケーキの有機物含有
率の低下を防ぐことができ、経済的な汚泥焼却が可能と
なる。(3) If a hard, rigid dehydrated cake containing high organic matter is obtained and this dehydrated cake is reused as a dehydration aid in the dehydration process, a significant increase in the dehydration effect can be expected, and Since the coagulated material itself is reused as a dehydration aid, a decrease in the organic matter content of the dewatered cake can be prevented, and economical sludge incineration becomes possible.
(4)焼却による焼却灰をマイクロ波溶融炉彦どにより
溶融同化処理する場合は、溶融物のガラス質化が促進さ
れ、溶融同化処理が簡単になる。(4) When incineration ash is melted and assimilated using a microwave melting furnace, vitrification of the molten material is promoted and the melting and assimilation process is simplified.
第1図は本発明の汚泥の処理方法の一例を示すフローシ
ート、第2図は本発明の他の例を示すフローシート、第
3図は本発明のさらに他の例を示すフローシートである
。
]・・・脱水設備、2.3・・・混練槽、4・・・凝固
乾燥器、5・・・汚泥焼却炉、6・・・粉砕機、7・・
・溶融炉、8・・・最初沈殿池、9・・・エアレーショ
ンタンク、10・・・最終沈殿池、11・・・機械濃縮
設備、12・・・重力式濃縮槽、13・・・嫌気性消化
槽、14・・・脱水設備、15・・・多段焼却炉
出 願 人 川崎重工業株式会社FIG. 1 is a flow sheet showing an example of the sludge treatment method of the present invention, FIG. 2 is a flow sheet showing another example of the present invention, and FIG. 3 is a flow sheet showing yet another example of the present invention. . ]...Dewatering equipment, 2.3...Kneading tank, 4...Coagulation dryer, 5...Sludge incinerator, 6...Crusher, 7...
・Melting furnace, 8... First settling tank, 9... Aeration tank, 10... Final settling tank, 11... Mechanical concentration equipment, 12... Gravity type thickening tank, 13... Anaerobic Digestion tank, 14...Dewatering equipment, 15...Multi-stage incinerator Applicant Kawasaki Heavy Industries, Ltd.
Claims (1)
処理する方法において、汚泥を脱水した脱水ケーキにケ
イ酸アルカリを添加、混練した後、酸を添加し混練して
pH調整を行い、ついで混合物に汚泥の焼却炉を含む各
種工業炉の燃焼排ガスを直接接触せしめて、脱水ケーキ
を乾燥凝固させることを特徴とする汚泥の処理方法。 2 下水汚泥、し尿汚泥、浄化槽汚泥などの各種汚泥を
処理する方法において、汚泥を脱水した脱水ケーキにケ
イ酸アルカリを添加、混練した後、酸を添加し混練して
pH調整を行い、ついで混合物に汚泥の焼却炉を含む各
種工業炉の燃焼排ガスを直接接触せしめて、脱水ケーキ
を乾燥凝固させ、さらにこの凝固汚泥を粉砕し、この粉
砕物を原汚泥を脱水する際の脱水助剤として再使用する
ことを特徴とする汚泥の処理方法。 3 下水汚泥、し尿汚泥、浄化槽汚泥などの各種汚泥を
処理する方法において、汚泥を脱水した脱水ケーキにケ
イ酸アルカリを添加、混純した後、酸を添加し混練して
pH調整を行い、ついで混合物に汚泥の焼却炉を含む各
種工業炉の・燃焼排ガスを直接接触せしめて、脱水ケー
キを乾燥凝固させ、この凝固汚泥を汚泥焼却炉で焼却し
、さらに焼却灰を溶融炉で溶融処理することを特徴とす
る汚泥の処理方法。[Claims] ■ In a method for treating various sludges such as sewage sludge, human waste sludge, and septic tank sludge, an alkali silicate is added to a dehydrated cake obtained by dehydrating the sludge and kneaded, and then an acid is added and kneaded to adjust the pH. A method for treating sludge, which comprises adjusting the mixture, and then bringing the mixture into direct contact with combustion exhaust gas from various industrial furnaces, including sludge incinerators, to dry and solidify the dehydrated cake. 2. In a method for treating various sludges such as sewage sludge, human waste sludge, and septic tank sludge, an alkali silicate is added to a dehydrated cake obtained by dehydrating the sludge and kneaded, then an acid is added and kneaded to adjust the pH, and then the mixture is mixed. The dehydrated cake is brought into direct contact with combustion exhaust gas from various industrial furnaces, including sludge incinerators, to dry and solidify it, and the solidified sludge is then crushed, and this crushed product is recycled as a dehydration aid when dewatering raw sludge. A sludge treatment method characterized by using 3. In the method of treating various sludges such as sewage sludge, human waste sludge, and septic tank sludge, an alkali silicate is added and mixed into a dehydrated cake obtained by dehydrating the sludge, and then an acid is added and kneaded to adjust the pH. The mixture is brought into direct contact with combustion exhaust gas from various industrial furnaces including sludge incinerators to dry and solidify the dehydrated cake, the solidified sludge is incinerated in a sludge incinerator, and the incinerated ash is melted in a melting furnace. A sludge treatment method characterized by:
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58181599A JPS6071100A (en) | 1983-09-28 | 1983-09-28 | Sludge treating method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58181599A JPS6071100A (en) | 1983-09-28 | 1983-09-28 | Sludge treating method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6071100A true JPS6071100A (en) | 1985-04-22 |
JPH0122040B2 JPH0122040B2 (en) | 1989-04-25 |
Family
ID=16103623
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58181599A Granted JPS6071100A (en) | 1983-09-28 | 1983-09-28 | Sludge treating method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6071100A (en) |
Cited By (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100433046B1 (en) * | 2000-10-17 | 2004-05-24 | 이상진 | Reuse method and apparatus for waste water |
JP2006247583A (en) * | 2005-03-11 | 2006-09-21 | Mitsui Eng & Shipbuild Co Ltd | Method for treating sludge |
CN107285580A (en) * | 2017-06-29 | 2017-10-24 | 平湖热电厂 | Method for sludge treatment |
CN108249714A (en) * | 2018-02-02 | 2018-07-06 | 东华大学 | A kind of river bottom mud stabilizes and the method for recycling |
CN109607999A (en) * | 2018-12-11 | 2019-04-12 | 湖南新都环境科技有限公司 | A kind of petroleum greasy filth environment-friendly treatment method |
JP2019093354A (en) * | 2017-11-24 | 2019-06-20 | 月島機械株式会社 | Sludge concentration equipment and sludge concentration method |
JP2020015028A (en) * | 2018-07-27 | 2020-01-30 | 株式会社東芝 | Sludge treatment system, sludge treatment method and organic wastewater treatment system |
JP2020151636A (en) * | 2019-03-19 | 2020-09-24 | メタウォーター株式会社 | Method for incinerating dewatered sludge |
-
1983
- 1983-09-28 JP JP58181599A patent/JPS6071100A/en active Granted
Cited By (9)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100433046B1 (en) * | 2000-10-17 | 2004-05-24 | 이상진 | Reuse method and apparatus for waste water |
JP2006247583A (en) * | 2005-03-11 | 2006-09-21 | Mitsui Eng & Shipbuild Co Ltd | Method for treating sludge |
CN107285580A (en) * | 2017-06-29 | 2017-10-24 | 平湖热电厂 | Method for sludge treatment |
CN107285580B (en) * | 2017-06-29 | 2019-12-03 | 平湖热电厂 | Method for sludge treatment |
JP2019093354A (en) * | 2017-11-24 | 2019-06-20 | 月島機械株式会社 | Sludge concentration equipment and sludge concentration method |
CN108249714A (en) * | 2018-02-02 | 2018-07-06 | 东华大学 | A kind of river bottom mud stabilizes and the method for recycling |
JP2020015028A (en) * | 2018-07-27 | 2020-01-30 | 株式会社東芝 | Sludge treatment system, sludge treatment method and organic wastewater treatment system |
CN109607999A (en) * | 2018-12-11 | 2019-04-12 | 湖南新都环境科技有限公司 | A kind of petroleum greasy filth environment-friendly treatment method |
JP2020151636A (en) * | 2019-03-19 | 2020-09-24 | メタウォーター株式会社 | Method for incinerating dewatered sludge |
Also Published As
Publication number | Publication date |
---|---|
JPH0122040B2 (en) | 1989-04-25 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JPS6071100A (en) | Sludge treating method | |
JP4231739B2 (en) | Sludge recycling method | |
JP2006315885A (en) | Recycled fertilizer and method of producing the same | |
JPH0924392A (en) | Production of active carbonized sludge | |
JP3774803B2 (en) | Sludge incineration method | |
JPH09187748A (en) | Treatment of incineration ash | |
JPH03207497A (en) | Treatment of sewerage sludge | |
JP2012055808A (en) | Method of using surplus sludge | |
CN118145861B (en) | Composite dehydrating agent for sludge drainage and sludge dehydration process thereof | |
JPS6349560B2 (en) | ||
JP3759277B2 (en) | Pulp wastewater treatment method using fly ash | |
JPH0366040B2 (en) | ||
JP2001025799A (en) | Treatment of sludge and sludge treating system | |
JPS58114800A (en) | Treatment for sludge | |
JP3085958B2 (en) | Asbestos melting process | |
JP3170266B2 (en) | Melt treatment of municipal waste incineration residue | |
JPS6082192A (en) | Treatment of organic sludge | |
JP4298139B2 (en) | Recycling method for mud containing organic components | |
JP3993802B2 (en) | Method of processing dewatered sludge and ash | |
CN111170603B (en) | Efficient sludge recycling system and treatment method thereof | |
JP2004203662A (en) | Method of manufacturing cement | |
JP3737258B2 (en) | Effective use of incineration fly ash | |
JP3127097B2 (en) | Treatment method of sewage sludge incineration ash | |
JP2003247707A (en) | Exhaust gas treatment system for incinerator with sludge drying function | |
JPH09192699A (en) | Treatment of sludge and treated matter of sludge for cement starting material |