JP3340083B2 - Continuous treatment equipment for sewage sludge - Google Patents

Continuous treatment equipment for sewage sludge

Info

Publication number
JP3340083B2
JP3340083B2 JP9871799A JP9871799A JP3340083B2 JP 3340083 B2 JP3340083 B2 JP 3340083B2 JP 9871799 A JP9871799 A JP 9871799A JP 9871799 A JP9871799 A JP 9871799A JP 3340083 B2 JP3340083 B2 JP 3340083B2
Authority
JP
Japan
Prior art keywords
continuous
sludge
carbide
sewage
organic
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 - Fee Related
Application number
JP9871799A
Other languages
Japanese (ja)
Other versions
JP2000288595A (en
Inventor
昌洋 難波
Original Assignee
株式会社まさなみ鉄工
株式会社テクリーノ有機産業
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 株式会社まさなみ鉄工, 株式会社テクリーノ有機産業 filed Critical 株式会社まさなみ鉄工
Priority to JP9871799A priority Critical patent/JP3340083B2/en
Publication of JP2000288595A publication Critical patent/JP2000288595A/en
Application granted granted Critical
Publication of JP3340083B2 publication Critical patent/JP3340083B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

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
    • Y02WCLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W10/00Technologies for wastewater treatment
    • Y02W10/40Valorisation of by-products of wastewater, sewage or sludge processing

Landscapes

  • Processing Of Solid Wastes (AREA)
  • Treatment Of Sludge (AREA)

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】本発明は、下水処理施設(し
尿処理汚泥、食品製造業、畜産廃棄物等の汚水処理施設
含む)で生じる汚泥の連続処理装置に関するものであ
る。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for continuously treating sludge generated in sewage treatment facilities ( including sewage treatment facilities for human waste treatment sludge, food manufacturing industry, livestock waste, etc.).

【0002】[0002]

【従来の技術】下水処理施設の規模は益々大きくなって
おり(し尿処理施設や各種汚水処理施設も同様)、それに
つれて発生する汚泥の量も増大し、その処理が問題とな
っている。固形化して有用な建築素材等にするには有機
質が主体で強度が得られなかったり、においの問題もあ
る。肥料化する試みがなされているが(特願平9-280460
号)、製造される肥料の量が多く、過剰生産となってい
るのが現状である。
2. Description of the Related Art The scale of sewage treatment facilities is increasing (as is the case with human waste treatment facilities and various sewage treatment facilities), and the amount of generated sludge is also increasing, which poses a problem in treatment. In order to solidify into useful building materials, etc., there is a problem that strength is not obtained due to mainly organic substances and there is a problem of smell. Attempts have been made to use fertilizer (Japanese Patent Application No. 9-280460).
No.), the amount of fertilizer produced is large, and the current situation is overproduction.

【0003】[0003]

【発明が解決しようとする課題】下水処理汚泥、し尿処
理施設や各種汚水処理施設で発生する汚泥は、有効利用
することも一手段であるが、焼却処分することも廃棄物
処理手段として選択肢の一つである。しかし、焼却に際
してはダイオキシンの発生の対策が必要となってくる
し、加熱源も必要となる。そこで、本発明者は下水処理
施設等で大量に発生する汚泥を連続して処理可能な下水
処理等の汚泥の連続処理装置について検討した。
The sludge generated in sewage treatment sludge, human waste treatment facilities and various kinds of sewage treatment facilities can be effectively used, but incineration is also an option as a waste treatment means. One. However, at the time of incineration, measures against the generation of dioxin are required, and a heating source is also required. Therefore, the present inventor studied a continuous sludge treatment apparatus such as sewage treatment capable of continuously treating a large amount of sludge generated in a sewage treatment facility or the like.

【0004】[0004]

【課題を解決するための手段】上記課題を検討した結
果、汚泥等有機物の炭化装置に対して、下水処理汚泥と
炭化物とを混合する混合機と、下水処理汚泥を燃焼し易
くするための造粒部及び連続炭化部を順次配置してな
り、連続炭化部はその上部に被処理対象物供給部を有
し、有機質を含む汚泥又は有機廃棄物に炭素含有助剤を
添加して連続処理する装置であって、連続炭化部よって
得られた炭化物をフィードバックする手段を連続炭化部
の被処理対象物供給部と下部の炭化物取出し口間に設
け、下水処理汚泥又は有機廃棄物からの炭化物を連続炭
化部へフィードバックさせて使用し、下水処理汚泥又は
有機廃棄物を連続処理することを特徴とする下水処理汚
泥の連続処理装置とした。
As a result of studying the above-mentioned problems, a mixer for mixing sewage treated sludge and carbide and a device for facilitating the combustion of sewage treated sludge are provided to a device for carbonizing organic matter such as sludge. The granulated part and the continuous carbonized part are sequentially arranged, and the continuous carbonized part has an object supply part on the upper part thereof, and continuously treats by adding a carbon-containing auxiliary agent to sludge or organic waste containing organic matter. An apparatus , wherein a means for feeding back the carbide obtained by the continuous carbonization unit is provided between the supply unit for the object to be treated in the continuous carbonization unit and the carbide outlet at the lower part, and continuously converts the carbide from the sewage sludge or the organic waste. Sewage treatment sludge characterized by continuous use of sewage sludge or organic waste by using it by feeding it back to the carbonization unit
A continuous mud treatment device was used.

【0005】前記下水処理汚泥の連続処理装置は、連続
炭化部を有しその上部に被処理対象物供給部を有し、下
水処理汚泥に炭素含有助剤を添加して連続処理する装置
であって、被処理対象物供給部に供給する下水処理汚泥
の造粒・乾燥部を設け、炭素含有助剤の供給手段として
前記処理によって得られた炭化物をフィードバックする
手段を連続炭化部の被処理対象物供給部と下部の炭化物
取出し口との間に設け、下水処理汚泥からの炭化物を連
続炭化部へフィードバックさせて、下水処理汚泥を連続
処理する。前記連続炭化部に有機ガス捕集部を設け、有
機ガス捕集部は、捕集後の有機ガスを燃焼させる燃焼装
置に導かれる場合や、捕集後の有機ガスを冷却して木酢
その他の有機ガスを採取する場合が実施可能である。
[0005] The sewage treatment sludge of the continuous processing apparatus has a object to be processed supply portion thereon has a continuous carbonization section, an apparatus for continuous treatment with the addition of carbon-containing auxiliaries sewage sludge < a sewage sludge granulation / drying section to be supplied to the treatment object supply section, and a means for feeding back the carbide obtained by the treatment as a means for supplying a carbon-containing auxiliary agent is continuously carbonized. The sewage sludge is continuously treated by feeding the carbide from the sewage sludge back to the continuous carbonization section, provided between the target object supply section of the section and the lower carbide outlet. An organic gas collecting unit is provided in the continuous carbonizing unit, and the organic gas collecting unit is guided to a combustion device that burns the collected organic gas, or cools the collected organic gas to add wood vinegar or other vinegar. It is feasible to collect organic gas.

【0006】[0006]

【発明の実施の形態】図1は本発明の下水処理汚泥の
続処理装置構成の側面図である。この下水処理汚泥の
続処理装置は連続炭化部4の上部に被処理対象物供給部
5を有しており、図中左方において下水処理汚泥に炭素
含有助剤を添加して、この連続炭化部4で連続炭化処理
する装置である。被処理対象物供給部5に供給するため
に下水処理汚泥を燃焼し易くするための造粒部19と乾燥
部20を設けている。炭素含有助剤の供給手段として、連
続炭化部4で得られた炭化物のほぼ全量をフィードバッ
クするようになっており、フィードバック手段18は連続
炭化部の炭化物取出し口6から下水処理汚泥と炭化物と
を混合する混合機21まで運ぶようになっている。混合機
21から造粒部19までコンベアで送られる。下水処理汚泥
からの炭化物を連続炭化部へフィードバックさせて使用
し、下水処理汚泥を連続処理するのである。
Figure 1 DETAILED DESCRIPTION OF THE INVENTION is a side view of a continuous <br/> connection processor configuration of wastewater treatment sludge of the present invention. The wastewater treatment sludge communicating <br/> connection processing apparatus has a object to be processed supply portion 5 to the top of the continuous carbide portion 4, adding carbon-containing auxiliaries sewage sludge in the left in FIG. to a device that continuously carbonized in the continuous carbonization unit 4. A granulating unit 19 and a drying unit 20 for facilitating combustion of the sewage sludge to be supplied to the supply unit 5 are provided. Almost all of the carbide obtained in the continuous carbonization section 4 is fed back as a supply means of the carbon-containing auxiliary agent. The feedback means 18 converts the sewage sludge and the carbide from the carbide outlet 6 of the continuous carbonization section. It is designed to carry to the mixing machine 21 for mixing. Mixing machine
It is sent by a conveyor from 21 to the granulating unit 19. The carbides from the sewage sludge are fed back to the continuous carbonization unit and used to continuously treat the sewage sludge.

【0007】図2は本発明の下水処理汚泥の連続処理
の炭化部縦断面図である。図3は図2中A部拡大図で
ある。この下水処理汚泥の連続処理装置における炭化部
においては、機台1上に円筒状のケーシング2を有し、
内筒3を有する連続炭化部4を設けており、その上部が
被処理対象物供給部5、連続炭化部4の下部は下方が狭
いテーパ状の炭化物取出し口6となっている。連続炭化
部4の下部に有機ガス捕集部7の吸引ダクト8が設けら
れている。この吸引ダクト8は排気ファン9につながっ
ているが、図2に示す例では途中がU字状に曲がって冷
却水槽10中を通っている。炭化の結果生じた木酢等の有
機ガスが排気ファン9で強制的に吸引され、冷却水槽10
によって捕集される。炭化物取出し口6から排出される
炭化物(活性炭)は前記被処理対象物供給部5間にフィー
ドバックして用いられるように、図示を省略したコンベ
アのフィードバック手段18(一点鎖線表示)によって助材
として再使用されるようになっている。
[0007] Figure 2 is a continuous process instrumentation sewage sludge of the present invention
It is a carbonized part longitudinal cross-sectional view of an installation . FIG. 3 is an enlarged view of a portion A in FIG. In carbonized part in the wastewater treatment sludge in continuous processing apparatus has a cylindrical casing 2 on the machine base 1,
A continuous carbonized portion 4 having an inner cylinder 3 is provided, the upper part of which is an object supply section 5, and the lower part of the continuous carbonized portion 4 is a tapered carbide outlet 6 having a narrow lower portion. A suction duct 8 for an organic gas collecting unit 7 is provided below the continuous carbonizing unit 4. This suction duct 8 is connected to an exhaust fan 9, but in the example shown in FIG. Organic gas such as wood vinegar generated as a result of carbonization is forcibly sucked by the exhaust fan 9, and is cooled by the cooling water tank 10.
Collected by The carbide (activated carbon) discharged from the carbide outlet 6 is re-used as an auxiliary material by a feedback means 18 (shown by a one-dot chain line) of a conveyor (not shown) so that the carbide (activated carbon) discharged from the carbide supply port 6 is fed back between the processing object supply units 5. Is being used.

【0008】通常還元雰囲気で炭化させて炭化物を得よ
うとすると、木酢その他有機ガスが発生する。本発明の
装置のように炭化部4の下部に有機ガス捕集部7を設け
て吸引すると、炭化部4の下部に格子を単に設けた装置
では格子が目詰まりして連続処理に支障を生じる。そこ
で、本発明の下水処理汚泥の連続処理装置では、図3に
詳細を示すが、連続炭化部4の下方は複数の通過穴11a,
12aを有する上開口板11と下開口板12で構成している。
上下の通過穴11a,12aは上開口板11と下開口板12の存在
する位置によって垂直方向に同位置となり炭化物4の落
下が可能となる。落下を促すために上開口板11の底面に
下向きの掻出し板11bを設けている。上開口板11は揺動
手段14として機台1側に設けられたシリンダ15が連結さ
れると共に、内筒3の内壁へ吊帯13で揺動可能に吊られ
ている。
[0008] Normally, when carbonized in a reducing atmosphere to obtain a carbide, wood vinegar and other organic gases are generated. When the organic gas collecting unit 7 is provided below the carbonization unit 4 and suction is performed as in the apparatus of the present invention, the lattice is clogged in a device in which a lattice is simply provided below the carbonization unit 4 and hinders continuous processing. . Therefore, the sewage treatment sludge of a continuous processing apparatus of the present invention, is shown in detail in FIG. 3, below the continuous carbonization unit 4 includes a plurality of passage holes 11a,
An upper opening plate 11 having 12a and a lower opening plate 12 are provided.
The upper and lower passage holes 11a and 12a are located at the same position in the vertical direction depending on the position where the upper opening plate 11 and the lower opening plate 12 are present, so that the carbide 4 can drop. A downward scraping plate 11b is provided on the bottom surface of the upper opening plate 11 in order to promote the falling. The upper opening plate 11 is connected to a cylinder 15 provided on the machine base 1 side as a swinging means 14, and is swingably suspended from the inner wall of the inner cylinder 3 by a suspension band 13.

【0009】次に、汚泥の連続処理の実施例を示す。表
1に示すように食品加工施設の微生物活性処理で生じた
汚泥4,880gに助剤として前工程によって得られた炭化
物1,440gをフィードバックさせたものを加えて処理す
ることとした。これらが混合されたものの平均水分は7
0.6%であり、投入量6,320g中の下水処理汚泥の量は1,
855gとなっている。よく混合撹拌し、造粒機を使用し
て粒子状にした後、乾燥させた。これを炭化部4中に入
れて、初期の炭化が安定するまでの間、炭化部4中にバ
ーナー炎を作用させた。空気の供給が殆どない状態で還
元雰囲気の炭化を行い、揺動手段14により定期的に上開
口板11を左右に動かして炭化物を下方へ落下させた。こ
のとき、排気ファン9を回して吸引ダクト8から炭化の
結果生じた木酢等の有機ガスを強制的に吸引除去させ
た。
Next, an example of continuous treatment of sludge will be described. As shown in Table 1, 4,880 g of sludge generated by the microbial activation treatment of the food processing facility was fed with 1,440 g of the carbide obtained in the previous step as an auxiliary and fed back. The average moisture of the mixture is 7
0.6%, and the amount of sewage sludge in 6,320 g
It is 855g. The mixture was thoroughly mixed and stirred, granulated using a granulator, and then dried. This was put in the carbonized part 4 and a burner flame was caused to act on the carbonized part 4 until the initial carbonization was stabilized. Carbonization of the reducing atmosphere was performed in a state where there was almost no supply of air, and the carbide was dropped downward by periodically moving the upper opening plate 11 left and right by the rocking means 14. At this time, the exhaust fan 9 was turned to forcibly remove the organic gas such as wood vinegar generated as a result of carbonization from the suction duct 8.

【0010】[0010]

【表1】 [Table 1]

【0011】図4に本発明の装置における炭化工程図を
示す。この還元雰囲気による炭化の結果、投入量6,320
gの汚泥+炭化物から948gの炭化物が得られ、907gの
木酢等の揮発があったことになる。得られた炭化物の全
量948gをフィードバックさせて使用することにより、
連続処理することができた。また、収支バランスをみ
て、一部を炭化物として商品化することもできる。得ら
れた炭化物の一例の分析結果を表2に示す。吸着試験で
ある程度の吸着能が認められる。賦活処理によって更に
吸着能が高められるものと考えられる。
FIG. 4 shows a diagram of the carbonization process in the apparatus of the present invention. As a result of carbonization by this reducing atmosphere,
948 g of carbide were obtained from g of sludge + carbonization, which means that 907 g of wood vinegar was volatilized. By feeding back and using a total amount of 948 g of the obtained carbide,
It could be processed continuously. In addition, it is also possible to commercialize a part as carbide in view of the balance. Table 2 shows the analysis results of an example of the obtained carbide. Some adsorption capacity is observed in the adsorption test. It is considered that the activation treatment further enhances the adsorption ability.

【0012】[0012]

【表2】 [Table 2]

【0013】図5に示すように、吸引ダクト8から炭化
の結果生じた木酢等の有機ガスを排気ファン17で強制的
に吸引して、これを燃焼炉16で燃焼処分させることもで
きる。
As shown in FIG. 5, it is also possible to forcibly suck an organic gas such as wood vinegar generated as a result of carbonization from the suction duct 8 with an exhaust fan 17 and burn and dispose it in a combustion furnace 16.

【0014】[0014]

【発明の効果】本発明によって、大量発生して処分に困
難を生じているし尿処理施設や各種汚水処理施設で発生
する汚泥やそば殻、コーヒー抽出かすなどを連続運転に
よって処分することができる。この下水処理汚泥の連続
処理装置その際に生じるトラブルも生じないし、焼
却灰や残さ等の排出のない安定した運転を可能にしてい
る。
According to the present invention, sludge, buckwheat husks, coffee grounds, and the like generated in human waste treatment facilities and various sewage treatment facilities, which are generated in large quantities and are difficult to dispose of, can be disposed of by continuous operation. The sewage treatment sludge of a continuous processing apparatus, do not occur any trouble occurring time, which enables the discharge-free stable operation of incineration ash or residue like.

【図面の簡単な説明】[Brief description of the drawings]

【図1】本発明の下水処理汚泥の連続処理装置の側面図
である。
1 is a side view of a sewage treatment sludge of a continuous processing apparatus of the present invention.

【図2】本発明の下水処理汚泥の連続処理装置の炭化部
の縦断面図である。
2 is a longitudinal sectional view of a carbonization of sewage sludge in a continuous processing apparatus of the present invention.

【図3】図2中A部拡大図である。FIG. 3 is an enlarged view of a portion A in FIG. 2;

【図4】炭化工程図である。FIG. 4 is a carbonization process diagram.

【図5】本発明に係る廃棄物連続処理装置の縦断面図で
ある。
FIG. 5 is a longitudinal sectional view of the continuous waste disposal apparatus according to the present invention.

【符号の説明】[Explanation of symbols]

1 機台 2 ケーシング 3 内筒 4 連続炭化部 5 被処理対象物供給部 6 炭化物取出し口 7 有機ガス捕集部 8 吸引ダクト 9 排気ファン 10 冷却水槽 11 上開口板 11a 通過穴 12 下開口板 12a 通過穴 13 吊帯 14 揺動手段 15 シリンダ 16 燃焼炉 17 排気ファン 18 フィードバック手段 19 造粒部 20 乾燥部 21 混合機 DESCRIPTION OF SYMBOLS 1 Machine stand 2 Casing 3 Inner cylinder 4 Continuous carbonization part 5 Processing object supply part 6 Carbide take-out port 7 Organic gas collection part 8 Suction duct 9 Exhaust fan 10 Cooling water tank 11 Upper opening plate 11a Passing hole 12 Lower opening plate 12a Passage hole 13 Suspension band 14 Swing means 15 Cylinder 16 Combustion furnace 17 Exhaust fan 18 Feedback means 19 Granulation unit 20 Drying unit 21 Mixer

───────────────────────────────────────────────────── フロントページの続き (58)調査した分野(Int.Cl.7,DB名) C02F 11/06 ZAB ──────────────────────────────────────────────────続 き Continued on the front page (58) Field surveyed (Int.Cl. 7 , DB name) C02F 11/06 ZAB

Claims (2)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 下水処理汚泥と炭化物とを混合する混合
機と、下水処理汚泥を燃焼し易くするための造粒部、及
び連続炭化部を順次配置してなり、連続炭化部はその上
部に被処理対象物供給部を有し、有機質を含む汚泥又は
有機廃棄物に炭素含有助剤を添加して連続処理する装置
であって、連続炭化部の下方を複数の通過穴を有する上
開口板と下開口板で構成し、上下の通過穴は上開口板と
下開口板の存在位置によって垂直方向に同位置となって
炭化物の落下を可能とし、上開口板の底面に下向きの掻
出し板を設け、上開口板を揺動手段として機台側に設け
たシリンダに連結し、前記連続炭化部よって得られた
炭化物をフィードバックする手段を連続炭化部の被処理
対象物供給部と下部の炭化物取出し口間に設け、下水処
理汚泥又は有機廃棄物からの炭化物を連続炭化部へフィ
ードバックさせて使用し、下水処理汚泥又は有機廃棄物
を連続処理することを特徴とする下水処理汚泥の連続処
装置
1. A mixer for mixing sewage treatment sludge and carbide, a granulating unit for facilitating combustion of the sewage treatment sludge, and a continuous carbonization unit are sequentially arranged, and the continuous carbonization unit is provided at an upper portion thereof. has a object to be processed supply portion, an apparatus <br/> continuous process by adding a carbon-containing additive in the sludge or organic waste containing an organic, a plurality of passage holes under the continuous carbide portion Have
It consists of an opening plate and a lower opening plate, and the upper and lower passage holes are
The same position in the vertical direction depending on the position of the lower opening plate
It allows the carbide to fall, and a downward scratch
Set up plate and set upper plate as swinging means on machine side
Coupled to the cylinder, provided between said successive object to be processed supply portion of the carbonization unit thus carbides means for feeding back the obtained continuous carbonization unit and the lower carbide outlet, from sewage sludge or organic waste carbides are allowed to use the feedback to the continuous carbonization unit, a continuous processing apparatus of sewage sludge, characterized in that the continuous process the sewage sludge or organic waste.
【請求項2】 連続炭化部下部に有機ガス捕集部を設
け、該有機ガス捕集部で捕集した有機ガスを燃焼装置に
導いて燃焼させる請求項1記載の下水処理汚泥の連続処
理装置
2. An organic gas collecting section is provided below the continuous carbonizing section.
The organic gas collected by the organic gas collecting section is sent to a combustion device.
The continuous treatment of sewage sludge according to claim 1, wherein the sludge is guided and burned.
Equipment .
JP9871799A 1999-04-06 1999-04-06 Continuous treatment equipment for sewage sludge Expired - Fee Related JP3340083B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9871799A JP3340083B2 (en) 1999-04-06 1999-04-06 Continuous treatment equipment for sewage sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9871799A JP3340083B2 (en) 1999-04-06 1999-04-06 Continuous treatment equipment for sewage sludge

Publications (2)

Publication Number Publication Date
JP2000288595A JP2000288595A (en) 2000-10-17
JP3340083B2 true JP3340083B2 (en) 2002-10-28

Family

ID=14227286

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9871799A Expired - Fee Related JP3340083B2 (en) 1999-04-06 1999-04-06 Continuous treatment equipment for sewage sludge

Country Status (1)

Country Link
JP (1) JP3340083B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP4772213B2 (en) * 2001-06-05 2011-09-14 株式会社まさなみ鉄工 Continuous carbonization equipment for organic waste

Also Published As

Publication number Publication date
JP2000288595A (en) 2000-10-17

Similar Documents

Publication Publication Date Title
JP5480814B2 (en) Carbonization apparatus and carbonization method
US20130019493A1 (en) Method of processing and drying waste in a cyclic continuous process
ATE165150T1 (en) METHOD AND DEVICE FOR DRYING A GRANULAR BULK MATERIAL
JP4672896B2 (en) Regeneration method of incineration ash
JP3340083B2 (en) Continuous treatment equipment for sewage sludge
JP2008163280A (en) Method and apparatus for treating chlorine-containing organic waste
JP3103719B2 (en) Apparatus and method for heat dechlorination of dust ash
JP3199696B2 (en) Waste continuous carbonization method
JP4340510B2 (en) Organic material carbonization equipment
JP5634961B2 (en) Sludge treatment method
JP2005156085A (en) Livestock dung drying incineration equipment
JPH08245966A (en) Treatment of waste by carbonization
JP2004275973A (en) Method for treating contaminated soil
KR100933437B1 (en) High water content of smokeless device
JP4038059B2 (en) Waste continuous carbonization equipment
JP2003080226A (en) Cleaning method for contaminated soil and asphalt plant
JP4772213B2 (en) Continuous carbonization equipment for organic waste
JP4743815B2 (en) Method and apparatus for purification of contaminated soil
JP2003171909A (en) Asphalt plant using exhaust gas of carbonizing device
CN109401759A (en) A kind of livestock and poultry cultivation waste harmless resource processing system and method
JP2001234176A (en) Carbonization treatment method of organic waste
JP3957232B2 (en) Pretreatment equipment for reusing municipal waste incineration ash
JP2002302679A (en) Carbonization method for sludge, etc.
JP2002192108A (en) Heating treatment apparatus for powder waste
JP2000176431A (en) Method of transferring incineration ash and its treatment

Legal Events

Date Code Title Description
R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

R250 Receipt of annual fees

Free format text: JAPANESE INTERMEDIATE CODE: R250

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20070816

Year of fee payment: 5

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080816

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20080816

Year of fee payment: 6

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090816

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20090816

Year of fee payment: 7

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20100816

Year of fee payment: 8

FPAY Renewal fee payment (event date is renewal date of database)

Free format text: PAYMENT UNTIL: 20110816

Year of fee payment: 9

LAPS Cancellation because of no payment of annual fees