JPH072588A - Treatment of sludge - Google Patents
Treatment of sludgeInfo
- Publication number
- JPH072588A JPH072588A JP5077480A JP7748093A JPH072588A JP H072588 A JPH072588 A JP H072588A JP 5077480 A JP5077480 A JP 5077480A JP 7748093 A JP7748093 A JP 7748093A JP H072588 A JPH072588 A JP H072588A
- Authority
- JP
- Japan
- Prior art keywords
- incineration
- sludge
- treatment
- facility
- composting
- 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
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/10—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
- Y02A40/20—Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses
Landscapes
- Fertilizers (AREA)
- Processing Of Solid Wastes (AREA)
- Treatment Of Sludge (AREA)
Abstract
Description
【0001】[0001]
【産業上の利用分野】この発明は汚泥の処理方法、詳し
くは汚泥を効率よく処理できるだけではなく、処理の結
果生成された物質も有効に再利用できる様にした汚泥の
処理方法に関するものである。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a sludge treatment method, and more particularly to a sludge treatment method which enables not only efficient treatment of sludge but also effective reuse of substances produced as a result of the treatment. .
【0002】[0002]
【従来の技術】生活雑排水や糞尿などを含む下水道水の
処理過程では必然的に汚泥が生成されるが、この汚泥は
厖大な量となり、特に大都市の下水処理施設ではその処
理が問題となっている。2. Description of the Related Art Sludge is inevitably generated in the process of treating sewerage water containing household wastewater and manure, but this sludge becomes a huge amount, and the treatment is problematic especially in sewage treatment facilities in large cities. Has become.
【0003】この汚泥の処理方法としては、汚泥を脱水
処理した汚泥脱水ケーキを焼却炉中で焼却する焼却処
理、コンポスト施設で醗酵させて有機肥料に変えるコン
ポスト処理の2方法が主に実施されている。As a method for treating this sludge, there are mainly carried out two methods: an incineration treatment in which a sludge dewatering cake obtained by dehydrating sludge is incinerated in an incinerator, and a compost treatment in which a sludge is fermented in a compost facility to be converted into an organic fertilizer. There is.
【0004】[0004]
【発明が解決しようとする課題】汚泥脱水ケーキを高温
で焼却する焼却処理は主に大都市の処理施設で実施され
ているが、水分を大量に含んでいるこの汚泥を焼却する
には大量の熱エネルギーを要し、燃料費をはじめ、処理
コストがかかる欠点があった。又、焼却によりNOxを
排出するおそれもあり、大気汚染防止上からも問題があ
った。更に、焼却によって生成される大量の灰をいかに
処理するかも問題であった。Although the incineration process of incinerating sludge dewatering cake at high temperature is mainly carried out in a treatment facility in a big city, a large amount of this sludge containing a large amount of water is incinerated. It has a drawback that it requires heat energy and processing cost including fuel cost. In addition, there is a possibility that NOx may be emitted by incineration, which is a problem in terms of preventing air pollution. Furthermore, how to treat a large amount of ash produced by incineration has been a problem.
【0005】一方、コンポスト処理は汚泥脱水ケーキを
バクテリアの作用により分解し、有機肥料に変えるもの
であり、地球環境を考慮した場合、理想的な処理方法で
はあるが、処理時間がかかり大面積の処理施設の必要と
し、都市内に設置することは現実には無理であった。
又、このコンポスト処理では、醗酵中に少量ながらアン
モニアガスや硫化水素ガスが発生することがあり、これ
が悪臭の原因となっていた。又、従来においてはこの2
方式間に補充関係はなく、それぞれ全く関係をもたず、
バラバラに処理が実施されていた。On the other hand, the composting process decomposes sludge dewatered cake into organic fertilizer by the action of bacteria, and is an ideal treatment method considering the global environment, but it takes a long time and a large area. It was necessary in the treatment facility, and it was impossible in reality to install it in the city.
Further, in this composting process, ammonia gas or hydrogen sulfide gas may be generated in a small amount during fermentation, which causes a bad odor. Also, in the past, this 2
There is no supplemental relationship between the schemes, and there is no relationship between them,
The treatment was carried out separately.
【0006】本発明者は汚泥の処理方法を鋭意研究した
結果、両方式を組合せることにより、少ないエネルギー
で汚泥を効率よく処理できる、新たな処理方法を開発す
ることに成功し、本発明としてここに提案するものであ
る。As a result of intensive studies on the sludge treatment method, the present inventor succeeded in developing a new treatment method capable of efficiently treating sludge with a small amount of energy by combining both methods. This is what we propose here.
【0007】[0007]
【課題を解決するための手段】この発明は、下水道処理
施設などから出る汚泥脱水ケーキを焼却処理用とコンポ
スト処理用とに振り分け、焼却処理用汚泥脱水ケーキは
焼却炉において700℃以上の高温で焼却処理し、一方
コンポスト処理用汚泥脱水ケーキは水分調節の後コンポ
スト施設において醗酵させてコンポスト化する様にし、
前記焼却処理において発生する焼却熱はコンポスト施設
に送って醗酵の為の熱源とすると共に、焼却灰も必要に
応じてコンポスト施設中の汚泥脱水ケーキに供給して水
分調整剤として再利用し、更にコンポスト施設において
醗酵中に発生した臭気は焼却炉へ送り、燃焼させて脱臭
させると共に醗酵完了後の物質は有機肥料として再利用
する様にして、上記課題を解決せんとするものである。According to the present invention, sludge dewatering cake discharged from a sewerage treatment facility or the like is sorted into incineration treatment and composting treatment, and the sludge dewatering cake for incineration treatment is performed at a high temperature of 700 ° C or higher in an incinerator. The sludge dewatering cake for composting is incinerated, and after adjusting the water content, it is fermented and composted in a composting facility.
The incineration heat generated in the incineration process is sent to the compost facility as a heat source for fermentation, and the incinerated ash is also supplied to the sludge dewatering cake in the compost facility to be reused as a moisture adjuster, if necessary. The odor generated during fermentation in a composting facility is sent to an incinerator where it is burned for deodorization and the substance after fermentation is reused as an organic fertilizer to solve the above problems.
【0008】[0008]
【作用】汚泥脱水ケーキの焼却処理とコンポスト処理を
併用して実施するものであり、焼却処理中に生成される
焼却灰は水分調整剤としてコンポスト処理用の汚泥脱水
ケーキに添加し、その含水率の調整に使用される。又、
同じく、焼却処理中に発生する焼却熱はコンポスト施設
に送られ醗酵の為の熱源として利用される。一方、コン
ポスト施設において汚泥脱水ケーキの醗酵過程で生じる
アンモニア臭、硫化水素臭を含んだ排気は焼却施設に送
られ、ここで完全燃焼され脱臭される。そして、コンポ
スト施設において醗酵が終了した物質は有機肥料として
再利用される。[Function] The incineration ash produced during the incineration process is added to the sludge dewatering cake for moisture treatment as a water content adjusting agent, and the water content is Used to adjust. or,
Similarly, the incineration heat generated during the incineration process is sent to the compost facility and used as a heat source for fermentation. On the other hand, exhaust gas containing ammonia odor and hydrogen sulfide odor generated in the fermentation process of sludge dewatering cake in the compost facility is sent to the incineration facility where it is completely burned and deodorized. Then, the substance of which fermentation has been completed in the compost facility is reused as an organic fertilizer.
【0009】この汚泥の処理方法は上記の通り、焼却処
理とコンポスト処理を併用して実施するものであり、処
理過程における生成物を熱エネルギー源あるいは調整剤
として有効利用して処理効率を高めていると共に有機肥
料の需要動向及び汚泥の要処理量などに応じて焼却処
理、コンポスト処理の割合を適宜変更し、最も効率の良
い処理を機動的に実施できる。As described above, this sludge treatment method is carried out by using incineration treatment and composting treatment in combination, and the product in the treatment process is effectively used as a heat energy source or a regulator to improve treatment efficiency. In addition, the ratio of incineration treatment and composting treatment can be appropriately changed according to the demand trend of organic fertilizer and the required amount of sludge treatment, and the most efficient treatment can be flexibly implemented.
【0010】[0010]
【実施例】図面を参照しながら、本発明を更に詳しく説
明する。各市町村の下水道処理施設などから送られてく
る汚泥脱水ケーキは焼却処理用、コンポスト処理用に振
り分けられ、それぞれの処理施設に送られる。両処理施
設は同一敷地内にあるいは隣接して設置することが好ま
しい。焼却処理用、コンポスト処理用の汚泥は汚泥自体
としては全く同じものであり、汚泥の性状、組成によっ
て分けるのではなく、本発明の方法によって最終的に生
産される有機肥料の需要動向、処理量の多寡等を勘案し
て決定される。The present invention will be described in more detail with reference to the drawings. The sludge dewatering cake sent from the sewerage treatment facilities of each municipality is sorted for incineration and composting and sent to each treatment facility. Both treatment facilities are preferably installed on the same site or adjacent to each other. The sludge for incineration treatment and composting is exactly the same as the sludge itself, and it is not divided according to the properties and composition of the sludge, but the demand trend and treatment amount of the organic fertilizer finally produced by the method of the present invention. It is decided in consideration of the number of items.
【0011】つまり、冬期等の有機肥料の不需要期や短
時間に多量の汚泥を処理しなければならないときには処
理効率を優先させて焼却処理の方に多くの汚泥脱水ケー
キを送り、有機肥料の需要が多いときには、コンポスト
処理の方へより多くの汚泥脱水ケーキを送る。That is, when a large amount of sludge has to be treated in a short period of time such as in winter when the organic fertilizer is not needed, the sludge dewatering cake is sent to the incinerator to give more sludge dewatering cake by giving priority to the treatment efficiency. When demand is high, send more sludge dewatering cake to composting.
【0012】汚泥脱水ケーキには汚泥に高分子凝集剤を
添加した高分子処理汚泥脱水ケーキと、汚泥に石灰を添
加した石灰処理汚泥脱水ケーキとがあるが、高分子処理
汚泥脱水ケーキは80〜90%という高い含水率を有
し、これ単独では醗酵を開始することはできず、水分調
整し、石灰処理汚泥脱水ケーキと混合することによりは
じめて醗酵が可能となる。従って、主に焼却処理の方に
廻される。一方、石灰処理汚泥脱水ケーキは汚泥に石灰
を添加したものであり、60〜70%の含水率を有して
おり、50%程度にその含水率を調整し、適度な温度に
すればそれ自体醗酵を開始するので主にコンポスト処理
に廻されるが、焼却処理も可能なため、必要に応じて焼
却処理にも廻される。焼却処理用の汚泥脱水ケーキは焼
却施設の焼却炉2に投入され、700℃以上の高温で焼
却される。700℃以上の高温で焼却する理由は、これ
以下では焼却の際NOxが生成されると共に悪臭が発生
する為であり、700℃以上ではNOxの生成や悪臭の
発生は防止される。The sludge dewatering cake includes a polymer-treated sludge dewatering cake in which a polymer flocculant is added to sludge and a lime-treated sludge dewatering cake in which lime is added to sludge. It has a high water content of 90%, and fermentation cannot be started by itself. Fermentation becomes possible only by adjusting the water content and mixing with lime-treated sludge dehydrated cake. Therefore, it is mainly sent to the incineration process. On the other hand, the lime-treated sludge dewatering cake is obtained by adding lime to sludge and has a water content of 60 to 70%, and if the water content is adjusted to about 50% and the temperature is adjusted to an appropriate temperature, it itself. Since fermentation is started, it is mainly used for composting, but since it can be incinerated, it is also used for incineration if necessary. The sludge dewatering cake for incineration treatment is put into the incinerator 2 of the incineration facility and incinerated at a high temperature of 700 ° C or higher. The reason for incineration at a high temperature of 700 ° C. or higher is that NOx is produced and an offensive odor is generated at the time of incineration below this, and the production of NOx and the offensive odor are prevented at 700 ° C. or above.
【0013】一方、コンポスト処理に振り分けられた汚
泥脱水ケーキには焼却炉2における汚泥焼却に伴って発
生した焼却灰4などが水分調節剤として添加され、醗酵
開始に最適な含水率50〜60%前後になる様に調整さ
れる。又、前記焼却の際発生した焼却熱はコンポスト施
設3に送られ、醗酵の為の熱源として使用される。つま
り、コンポスト施設3は焼却炉2から熱源及び水分調整
剤の供給を受けていることになる。On the other hand, the sludge dewatering cake distributed to the composting treatment is added with incineration ash 4 and the like generated along with the sludge incineration in the incinerator 2 as a water content adjusting agent, and the optimum moisture content for starting fermentation is 50 to 60%. It will be adjusted to the front and back. The incineration heat generated during the incineration is sent to the compost facility 3 and used as a heat source for fermentation. That is, the compost facility 3 is supplied with the heat source and the moisture conditioner from the incinerator 2.
【0014】この様に、コンポスト施設3では焼却炉2
から援助を受けつつ汚泥脱水ケーキの醗酵を行い、醗酵
完了後の物質は有機肥料として再利用される。醗酵過程
で生じる悪臭を含んだ排気は焼却炉2に送られ、ここに
おいて汚泥と共に高温で完全燃焼させられ、脱臭され
る。なお、醗酵過程で生ずる悪臭はアンモニアガスや硫
化水素系のガスによるものであり、これらを高温で燃焼
させれば完全に脱臭することが可能である。Thus, in the compost facility 3, the incinerator 2 is
Fermentation of sludge dewatering cake is carried out with assistance from the company, and the substance after fermentation is reused as organic fertilizer. Exhaust gas containing a foul odor generated in the fermentation process is sent to the incinerator 2 where it is completely burned at high temperature together with sludge to be deodorized. The malodor produced during the fermentation process is due to ammonia gas or hydrogen sulfide gas, and it is possible to completely deodorize by burning these at high temperature.
【0015】[0015]
【発明の効果】この発明に係る汚泥の処理方法は上記の
通りの構成を有するものであり、焼却処理とコンポスト
処理を組合せて実施しており、両者の長所を最大限利用
でき、処理すべき汚泥の多寡、処理過程で生れる有機肥
料の需要動向等を勘案しながら、焼却処理、コンポスト
処理に振り分ける汚泥の割合を適宜機動的に変更するこ
とにより、最も効率的、経済的処理を実施することがで
きる。EFFECT OF THE INVENTION The sludge treatment method according to the present invention has the constitution as described above, and is carried out by combining the incineration treatment and the composting treatment. Implementing the most efficient and economical treatment by appropriately and flexibly changing the proportion of sludge to be distributed between incineration and composting, taking into consideration sludge volume, demand trends for organic fertilizers produced in the treatment process, etc. be able to.
【0016】又、処理過程において生ずる熱エネルギ
ー、生成物を再利用することができ、省資源、省エネル
ギー化の観点からもすぐれた効果を有するものである。Further, the heat energy and products produced in the treatment process can be reused, and it has an excellent effect from the viewpoint of resource saving and energy saving.
【0017】[0017]
【図1】この発明に係る汚泥処理方法の一実施例のフロ
ーチャートである。FIG. 1 is a flowchart of an embodiment of a sludge treatment method according to the present invention.
1 下水道処理設備 2 焼却炉 3 コンポスト施設 4 焼却灰 1 Sewer treatment facility 2 Incinerator 3 Composting facility 4 Incinerator ash
───────────────────────────────────────────────────── 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 C02F 11/06 ZAB A 7446−4D ─────────────────────────────────────────────────── ─── Continuation of the front page (51) Int.Cl. 6 Identification code Internal reference number FI technical display location C02F 11/06 ZAB A 7446-4D
Claims (3)
ーキを焼却処理用とコンポスト処理用とに振り分け、焼
却処理用汚泥脱水ケーキは焼却炉において700℃以上
の高温で焼却処理し、一方コンポスト処理用汚泥脱水ケ
ーキは水分調節の後コンポスト施設において醗酵させて
コンポスト化する様にし、前記焼却処理において発生す
る焼却熱はコンポスト施設に送って醗酵の為の熱源とす
ると共に、焼却灰も必要に応じてコンポスト施設中の汚
泥脱水ケーキに供給して水分調整剤として再利用し、更
にコンポスト施設において醗酵中に発生した臭気は焼却
炉へ送り、燃焼させて脱臭させると共に醗酵完了後の物
質は有機肥料として再利用する様にしたことを特徴とす
る汚泥の処理方法。1. Sludge dewatering cake discharged from a sewerage treatment facility is sorted into incineration and composting, and the sludge dewatering cake for incineration is incinerated at a high temperature of 700 ° C. or higher in an incinerator, while for composting. Sludge dewatering cake is fermented in a composting facility after water content adjustment to be composted, and the incineration heat generated in the incineration process is sent to the composting facility as a heat source for fermentation, and incineration ash is also required. It is supplied to the sludge dewatering cake in the compost facility and reused as a moisture conditioner, and the odor generated during fermentation in the compost facility is sent to the incinerator where it is burned to deodorize and the substance after fermentation is completed as organic fertilizer. A sludge treatment method characterized by being reused.
地内に設置されていることを特徴とする請求項(1)記
載の汚泥の処理方法。2. The sludge treatment method according to claim 1, wherein the incineration facility and the compost facility are installed on the same site.
て設置されていることを特徴とする請求項(1)記載の
汚泥の処理方法。3. The method for treating sludge according to claim 1, wherein the incineration facility and the compost facility are installed adjacent to each other.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5077480A JP2789154B2 (en) | 1993-03-12 | 1993-03-12 | Sludge treatment method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP5077480A JP2789154B2 (en) | 1993-03-12 | 1993-03-12 | Sludge treatment method |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH072588A true JPH072588A (en) | 1995-01-06 |
JP2789154B2 JP2789154B2 (en) | 1998-08-20 |
Family
ID=13635151
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP5077480A Expired - Fee Related JP2789154B2 (en) | 1993-03-12 | 1993-03-12 | Sludge treatment method |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2789154B2 (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002031175A1 (en) * | 2000-10-12 | 2002-04-18 | Yoshihito Shirai | Method of manufacturing sugar from food waste and method of reducing volume of food waste |
Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5188882A (en) * | 1975-01-31 | 1976-08-03 | ||
JPS5684388A (en) * | 1979-12-11 | 1981-07-09 | Mitsubishi Heavy Ind Ltd | Composting treatment high water content organic waste |
JPS577894A (en) * | 1980-06-19 | 1982-01-16 | Ebara Mfg | Organic matter composting device |
JPS577893A (en) * | 1980-06-19 | 1982-01-16 | Ebara Mfg | Sludge composting device |
JPS5750599A (en) * | 1980-09-12 | 1982-03-25 | Hitachi Zosen Corp | Treatment of solid waste |
-
1993
- 1993-03-12 JP JP5077480A patent/JP2789154B2/en not_active Expired - Fee Related
Patent Citations (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5188882A (en) * | 1975-01-31 | 1976-08-03 | ||
JPS5684388A (en) * | 1979-12-11 | 1981-07-09 | Mitsubishi Heavy Ind Ltd | Composting treatment high water content organic waste |
JPS577894A (en) * | 1980-06-19 | 1982-01-16 | Ebara Mfg | Organic matter composting device |
JPS577893A (en) * | 1980-06-19 | 1982-01-16 | Ebara Mfg | Sludge composting device |
JPS5750599A (en) * | 1980-09-12 | 1982-03-25 | Hitachi Zosen Corp | Treatment of solid waste |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2002031175A1 (en) * | 2000-10-12 | 2002-04-18 | Yoshihito Shirai | Method of manufacturing sugar from food waste and method of reducing volume of food waste |
Also Published As
Publication number | Publication date |
---|---|
JP2789154B2 (en) | 1998-08-20 |
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