JPS59147700A - Treatment of sludge - Google Patents
Treatment of sludgeInfo
- Publication number
- JPS59147700A JPS59147700A JP58021909A JP2190983A JPS59147700A JP S59147700 A JPS59147700 A JP S59147700A JP 58021909 A JP58021909 A JP 58021909A JP 2190983 A JP2190983 A JP 2190983A JP S59147700 A JPS59147700 A JP S59147700A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- dehydrated
- consisting essentially
- hydraulic cement
- incinerated
- 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
Links
Landscapes
- Treatment Of Sludge (AREA)
Abstract
Description
【発明の詳細な説明】
本発明は、主として、下水道終末処理場で発生する下水
汚泥、工場廃水等の処理により発生する泥状産業廃棄物
としての汚泥、河川・湖沼・港湾・海域等の底質として
の堆積汚泥等の、放置しておけば環境悪化の原因となる
各種汚泥を、埋立地への埋立材、路床材等に再利用し得
るように処理する方法に関する。Detailed Description of the Invention The present invention mainly relates to sewage sludge generated at sewage treatment plants, sludge as muddy industrial waste generated from the treatment of factory wastewater, etc., and the bottom of rivers, lakes, ports, sea areas, etc. The present invention relates to a method for treating various kinds of sludge, such as accumulated sludge, which can cause environmental deterioration if left untreated, so that they can be reused as landfill material, roadbed material, etc.
上記汚泥処理力法で従来から一般的に知られているもの
としては、汚泥に各種凝集剤を添加混合した後、(1)
脱水処理のみを行なう処理方法、(2]脱水処理後同化
材全添加混合する固化処理方法、(3)脱水処理後焼却
処理する焼却処理方法、があり、処理物の含水率の低下
に伴なう処理物貯留スペースの節減、処理物運搬作業の
容易化の観点から〔3)に記した焼却処理方法が急増し
ている。ところが、この焼却処理方法は概して下記の如
き種々の欠点があった。即ち、
(イ)脱水ケーキの貯留や運搬に際して、脱水ケーキの
腐敗臭が著しく悪臭公害を発生する。The conventionally known sludge processing power method is that after adding and mixing various flocculants to sludge, (1)
There are three treatment methods: (2) a solidification treatment method in which all assimilates are added and mixed after dehydration treatment, and (3) an incineration treatment method in which incineration is performed after dehydration treatment. The incineration method described in [3] is rapidly increasing from the viewpoint of saving storage space for waste materials and facilitating the transportation of waste materials. However, this incineration treatment method generally has various drawbacks as described below. That is, (a) When storing and transporting the dehydrated cake, the putrid odor of the dehydrated cake causes significant odor pollution.
(ロ) 脱水ケーキの含水率が75〜85俤と高いため
に、運搬時の取扱いが極めて困難であり、且ら、焼却処
理時に多量の補助燃料を必要とする。(b) Since the moisture content of the dehydrated cake is as high as 75 to 85 yen, handling during transportation is extremely difficult, and a large amount of auxiliary fuel is required during incineration.
ぐ3 脱水ケーキが、粘若性を有するために団塊状を呈
し、焼却処理時の炉床落下口の閉塞や団塊内部の未燃箇
所が発生し易く、その対策として、脱水ケーキを、焼却
処理油に熱風を吹込みプレヒートして造粒化クル理する
必要かあり、処理工程が複雑になる。3. Because the dehydrated cake has viscosity, it takes on the shape of a nodule, and during incineration, the hearth drop opening is likely to be clogged and unburned areas inside the nodule easily occur.As a countermeasure, the dehydrated cake is incinerated. It is necessary to blow hot air into the oil to preheat it and granulate it, which complicates the processing process.
し) 焼却灰中の重金属の溶出の防止、埋立時等の地盤
の早期安定化のために、再利用時に特殊セメントによる
同化処理か必ヅである。) In order to prevent the elution of heavy metals in the incineration ash and to quickly stabilize the ground during reclamation, it is necessary to assimilate the ash using special cement when reusing it.
等の問題を有し、最終的に処理が煩雑になり、且つ、処
理コストが高い。These problems result in complicated processing and high processing costs.
本発明は、かかる実情に始み、脱水ケーキの含水率低下
により取り扱いを・容易にする七共に、腐敗臭を極めて
少量に抑え、且つ、焼却処理時の補助燃料の低減化なら
びに炉床落下口の閉塞や未燃箇所発生の防止を図り、加
えて、処理物再利用時、煤却灰中の重金属固定を極めて
容易にすることによって、経済上及び施工上において非
常に有利々処理方法を提供する点に目的がある。The present invention has been developed based on the above-mentioned circumstances, as well as making handling easier by lowering the water content of the dehydrated cake, suppressing putrid odor to an extremely small amount, reducing the amount of auxiliary fuel used during incineration, and improving the hearth drop opening. This provides a very advantageous treatment method from an economical and construction perspective by preventing blockages and the occurrence of unburnt spots, and in addition, by making it extremely easy to fix heavy metals in the soot ash when reusing treated materials. There is a purpose in what you do.
上記目的を達成するべくなされた本発明に係る汚泥の処
理方法の特徴は、汚泥中に水硬性セメント系物質を主成
分とする同化材を添加混合シ、シかる後脱水処理し、つ
づいてその脱水汚泥?焼却する点にある。The sludge treatment method according to the present invention, which has been made to achieve the above object, is characterized by adding and mixing an assimilating agent whose main component is a hydraulic cement type substance to the sludge, dewatering the sludge after sludge, and then dewatering the sludge. Dehydrated sludge? It is at the point of being incinerated.
このような特徴を有する本発明の作用効果は、次の通り
である。The effects of the present invention having such characteristics are as follows.
つまり、通常、コロイド粒子状の有機性物質を多はに含
有するが故に、強烈々悪臭を放つ汚泥中に添加混合した
水硬性セメント系物質は、汚泥中に懸濁する親水コロイ
ド粒子を凝集もしくは吸着し、同時にそれらを相互に結
合して次第に粗大粒子化するのであり、汚泥が良好な透
水性を示して脱水により低含水砂状とな9、取シ扱いが
極めて容易になると共に悪臭の発生も極めて微量に抑え
られるのであり、次工程での焼却処理におけるプレヒー
トが不要となり、燃料の大幅な低減化及びプロセスの簡
略化が可能に々つたのである。更に特筆すべきこととし
て、脱水処理に先立って添加混合しだ水硬性セメント系
物質は、脱水時に存在した大量の有機性物質或いは脱水
ケーキ中の大量の有槙物全含荷する間隙水の影響を受け
て、全部もしくは一部永和反応による硬化が阻害されて
いる又は不良の状態にあるが、この脱水ケーキを焼却処
理することによって燃焼による水和阻害@質の除去によ
り水和物の賦活が生じ、水硬性を呈するに至るのであり
、焼却処理物は、再利用時に特殊セメントを添加混合す
ること力く単に水添により水硬し、重金属吸上機能によ
り重金属の不溶化と合わせて、埋立時等の地盤の早ル」
安定化をも促進できるのであり、従来方法に比べて経済
上及び施工上忙おいて非常に有利な処理方法奢提供する
に至ったのである。In other words, hydraulic cement-based materials added to and mixed with sludge that emit a strong odor usually cause agglomeration or coagulation of hydrophilic colloid particles suspended in the sludge because it usually contains a large amount of organic substances in the form of colloidal particles. The sludge adsorbs the particles and at the same time binds them together, gradually turning them into coarse particles.The sludge exhibits good water permeability and becomes sand-like with low water content through dehydration. The amount of fuel used can be suppressed to an extremely small amount, and preheating in the next process of incineration is no longer necessary, making it possible to significantly reduce the amount of fuel and simplify the process. Furthermore, it is worth noting that the hydraulic cement-based materials added and mixed prior to the dewatering process may be affected by the large amount of organic material present during dewatering or by the pore water containing a large amount of molten matter in the dehydrated cake. However, by incinerating this dehydrated cake, hydration inhibition due to combustion is removed, and hydrate activation is achieved. When reusing the incinerated material, it becomes hydraulically hardened by simply adding and mixing special cement, and the heavy metals are insolubilized by the heavy metal wicking function. Etc. ground level
Stabilization can also be promoted, and we have now provided a processing method that is very advantageous in terms of economy and construction compared to conventional methods.
次に、未発明の実施例を説明する。Next, an uninvented embodiment will be described.
下水道終末処理場で発生する下水汚泥、工場廃水等の処
理により発生する泥状産業廃棄物としての汚泥、河川・
湖沼・港湾・海域等の底質と1しての堆積汚泥等の各種
汚泥分、埋1地への埋立材、路床材等に再利用し得るよ
うに#順柑七−鴫44→者処理するに、汚泥中に水硬性
セメント系物質を主成分とする同化材及び必要に応じて
凝′集剤を添加混合し、しかる後に脱水処理し、つづい
てその脱水汚泥を焼却し、更に、その焼却処理物に水を
添加して水成させて、埋立材、路床材等に利用し得る粒
状の椙料金造る。Sewage sludge generated at sewage treatment plants, sludge as muddy industrial waste generated from the treatment of factory wastewater, rivers, etc.
The bottom sediment of lakes, ports, sea areas, etc., as well as various sludge such as accumulated sludge, can be reused as fill material for landfills, roadbed materials, etc. In the treatment, an assimilating agent mainly composed of hydraulic cement-based substances and a flocculant are added and mixed into the sludge, followed by dewatering treatment, followed by incineration of the dehydrated sludge, and further, Water is added to the incinerated material to form aqueous solution, producing granular grains that can be used as landfill material, roadbed material, etc.
次に、実験例を示す。Next, an experimental example will be shown.
下記の性状を有する下水娠理′4m縮汚泥中の乾物量に
対し100%の固化材を添加混合し、約10分後にカチ
オン性凝集剤i0.7%添加し、デカンタ−による脱水
処理をおこガい、つづいて脱水ケーキ全マツフル炉で1
000’0 1時間の焼却をおこなった。Add and mix 100% of the solidifying agent to the dry matter amount of 4 m of sewage sludge having the following properties, and after about 10 minutes, add 0.7% of the cationic flocculant i, and perform dewatering using a decanter. Okay, next, make the dehydrated cake all in a Matsufuru oven.
000'0 Incineration was performed for 1 hour.
汚泥:下水処理場濃縮汚泥
含水率二97.12.係
強熱減量:59.97%
重金属二T二GF2000〜勾(乾燥換算)隔水:遠心
悦水(模型デヵンタm:]。(l vHr)運心力、差
速、液面差、給泥シ
3000 () X 10rpm X 5 mm X
1.Om”/&焼却:マッフル炉
1000°01時間
六1環境庁告示13−5J・(材世マ3日)メ2焼却炉
に導入及びメンテナンス面から判定@τTg己水碩性セ
メント系物質としては、例えば各種ポルトランドセメン
ト、高炉セメント、フライアッシュセメント、ンリカセ
メント、ポゾランセメント、高アルミナ質セメント、高
アルミナ高硫酸宵セメント等のものが単独もしくは混合
物として使用できる。まだ、水硬性セメント系物質に、
例えば消石灰、生石灰等の石灰質添加物を必qりに応じ
て混入して同化材ケ調整してもよい。Sludge: Sewage treatment plant thickened sludge moisture content 297.12. Ignition loss related to: 59.97% Heavy metal 2 T2 GF2000 ~ Gradient (drying equivalent) Separate water: Centrifugal water (model decanter m:]. (l vHr) Centripetal force, differential speed, liquid level difference, slurry supply system 3000 () X 10rpm X 5mm X
1. Om” / & Incineration: Muffle furnace 1000° 01 hour 61 Environment Agency Notification 13-5J (3rd day of Zaisei Ma) Me2 Determined from the installation and maintenance aspect of incinerator @ τTg As a self-hydrous cement-based material For example, various Portland cements, blast furnace cements, fly ash cements, solid cements, pozzolan cements, high alumina cements, high alumina high sulfate cements, etc. can be used alone or in mixtures. ,
For example, calcareous additives such as slaked lime and quicklime may be mixed in to adjust the assimilation material.
また、if’jf A具綻某剤は、本発明を実施するに
当って必らず必要なものではないが、使用するに当って
は、水溶性カチオン性凝集剤、アニオン性凝呆AIIを
・同時に又は別々に使用してもよく、そして他の界面活
性剤」を必要に応じてこねに混入して凝集h;jとして
もよい。In addition, the if'jf A specific agent is not necessarily necessary for carrying out the present invention, but when using it, water-soluble cationic flocculant and anionic flocculant AII are recommended. - They may be used simultaneously or separately, and other surfactants may be mixed into the kneading if necessary to form agglomeration h;j.
さ鰍に、本発明の方法Vこよって汚泥を脱水処理するに
際しては、例えば、遠心脱水のほか真空脱水、フィルタ
ープレス脱水、ベルトプレス脱水、加圧脱水等の各種強
制脱水手段および装置が利用できることは言うまでもな
し)。Especially, when dewatering sludge according to the method V of the present invention, various forced dehydration means and devices such as centrifugal dehydration, vacuum dehydration, filter press dehydration, belt press dehydration, pressure dehydration, etc. can be used. Needless to say).
さ17Kまた、本発明の方法によって脱水ケーキを焼却
処理するに際しては、例えは縦型多段炉のI=か流動燃
焼炉、回転乾燥焼却炉等の各種燃線)装置か禾j用でき
ることil′j、’iうまでもな00代理人 弁理士
北 村 修
第1頁の続き
0発 明 者 田尻弘水
大阪市東区本町4丁目27番地株
式会社竹中工務店大阪本店内
0発明 者坂口豊
大阪市東区本町4丁目27番地株
式会社竹4中工務店大阪本店内
の発 明 者 本郷徹
大阪市東区本町4丁目27番地株
式会社竹中工務店大阪本店内In addition, when incinerating the dehydrated cake by the method of the present invention, it is possible to use various types of equipment, such as a vertical multistage furnace, fluidized combustion furnace, rotary drying incinerator, etc. j,'i Umaena 00 Agent Patent Attorney
Osamu Kitamura Continued from page 1 0 Inventor: Hiromizu Tajiri, Takenaka Corporation Osaka Main Store, 4-27 Honmachi, Higashi-ku, Osaka Inventor: Yutaka Sakaguchi, 4-27 Honmachi, Higashi-ku, Osaka Inventor: Toru Hongo Inside Takenaka Corporation Osaka Main Office, 4-27 Honmachi, Higashi-ku, Osaka City
Claims (1)
材を添加混合し、しかる後脱水処理し、つづいてその脱
水泥汚を焼却する汚泥の処理方法。 ■ 前記固化材と同時に又は別々に凝集剤を特徴とする
特許請求の範囲第0項に記載の汚泥の処理方法。 ■ 前記汚泥として下水汚泥等の難固化性汚泥を特徴と
する特許請求の範囲第0項に記載の汚泥の処理方法。 ■ 前記水硬性セメント系物質として普通ポルトランド
セメントを使用する特許請求の範囲第0項に記載の汚泥
の処理方法。 ■ 前記凝集剤としてポリアミノアルキルアクリレート
を主成分とする高分子凝集剤を使用する特許請求の範囲
第0項に記載の汚泥の処理方法。[Claims] ■ A method for treating sludge, which comprises adding and mixing an assimilating agent whose main component is a hydraulic cement-based substance into sludge, followed by dewatering the sludge, and then incinerating the dehydrated sludge. (2) The method for treating sludge according to claim 0, characterized in that a flocculant is used simultaneously with or separately from the solidifying agent. (2) The sludge treatment method according to claim 0, characterized in that the sludge is hard-to-solidify sludge such as sewage sludge. (2) The sludge treatment method according to claim 0, wherein ordinary Portland cement is used as the hydraulic cement-based material. (2) The sludge treatment method according to claim 0, wherein a polymer flocculant containing polyaminoalkyl acrylate as a main component is used as the flocculant.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58021909A JPS59147700A (en) | 1983-02-10 | 1983-02-10 | Treatment of sludge |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58021909A JPS59147700A (en) | 1983-02-10 | 1983-02-10 | Treatment of sludge |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS59147700A true JPS59147700A (en) | 1984-08-24 |
Family
ID=12068216
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58021909A Pending JPS59147700A (en) | 1983-02-10 | 1983-02-10 | Treatment of sludge |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59147700A (en) |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61220800A (en) * | 1985-03-27 | 1986-10-01 | Bunji Kurosaki | Treatment of organic sludge |
JPS61220798A (en) * | 1985-03-26 | 1986-10-01 | Bunji Kurosaki | Method for dehydrating sludge |
JPS61220795A (en) * | 1985-03-27 | 1986-10-01 | Bunji Kurosaki | Treatment of high-concentration organic waste water |
JPH04119061U (en) * | 1991-04-05 | 1992-10-23 | 株式会社サタケ | portable shower room |
CN100371283C (en) * | 2004-11-10 | 2008-02-27 | 浙江大学 | Method for producing cement pressing products from urban sludge |
CN106116107A (en) * | 2016-08-25 | 2016-11-16 | 四川环能德美科技股份有限公司 | A kind of method of deeply dehydrating sludge |
CN111646671A (en) * | 2020-06-18 | 2020-09-11 | 浙江红狮环保股份有限公司 | Method for cooperatively treating sludge by using cement kiln |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4988362A (en) * | 1972-12-28 | 1974-08-23 | ||
JPS5013264A (en) * | 1973-06-08 | 1975-02-12 | ||
JPS5644100A (en) * | 1979-09-17 | 1981-04-23 | Takenaka Komuten Co Ltd | Dehydration/caking treating method of sludge |
JPS5658598A (en) * | 1979-10-17 | 1981-05-21 | Agency Of Ind Science & Technol | Treatment of muddy water |
-
1983
- 1983-02-10 JP JP58021909A patent/JPS59147700A/en active Pending
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4988362A (en) * | 1972-12-28 | 1974-08-23 | ||
JPS5013264A (en) * | 1973-06-08 | 1975-02-12 | ||
JPS5644100A (en) * | 1979-09-17 | 1981-04-23 | Takenaka Komuten Co Ltd | Dehydration/caking treating method of sludge |
JPS5658598A (en) * | 1979-10-17 | 1981-05-21 | Agency Of Ind Science & Technol | Treatment of muddy water |
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61220798A (en) * | 1985-03-26 | 1986-10-01 | Bunji Kurosaki | Method for dehydrating sludge |
JPS61220800A (en) * | 1985-03-27 | 1986-10-01 | Bunji Kurosaki | Treatment of organic sludge |
JPS61220795A (en) * | 1985-03-27 | 1986-10-01 | Bunji Kurosaki | Treatment of high-concentration organic waste water |
JPH04119061U (en) * | 1991-04-05 | 1992-10-23 | 株式会社サタケ | portable shower room |
CN100371283C (en) * | 2004-11-10 | 2008-02-27 | 浙江大学 | Method for producing cement pressing products from urban sludge |
CN106116107A (en) * | 2016-08-25 | 2016-11-16 | 四川环能德美科技股份有限公司 | A kind of method of deeply dehydrating sludge |
CN111646671A (en) * | 2020-06-18 | 2020-09-11 | 浙江红狮环保股份有限公司 | Method for cooperatively treating sludge by using cement kiln |
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