JPH02255586A - Fermentative treatment of sludge - Google Patents
Fermentative treatment of sludgeInfo
- Publication number
- JPH02255586A JPH02255586A JP1078777A JP7877789A JPH02255586A JP H02255586 A JPH02255586 A JP H02255586A JP 1078777 A JP1078777 A JP 1078777A JP 7877789 A JP7877789 A JP 7877789A JP H02255586 A JPH02255586 A JP H02255586A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- compost
- fermenter
- dehydrated cake
- raw material
- 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
- Treatment Of Sludge (AREA)
- Fertilizers (AREA)
Abstract
Description
【発明の詳細な説明】 産業上の利用分野 本発明は汚泥の発酵処理方法に関する。[Detailed description of the invention] Industrial applications The present invention relates to a method for fermentation treatment of sludge.
従来の技術
従来の発酵処理方法は、し尿を活性汚泥処理したときに
生じる余剰汚泥を脱水機で脱水し、脱水された脱水ケー
キを解砕して汚泥発酵槽に投入し、汚泥発酵槽において
汚泥を発酵・乾燥させていた。Conventional technology The conventional fermentation treatment method involves dewatering excess sludge produced when human waste is treated with activated sludge using a dehydrator, crushing the dehydrated cake and feeding it into a sludge fermentation tank. was fermented and dried.
そして、汚泥発酵槽には、すでに発酵・乾燥されたフン
ポストと解砕された脱水ケーキを等量程度に混合して投
入し、発酵槽内に約IO〜20日間滞留させ、この間に
空気を汚泥に吹き込んで生物学的に発酵・乾燥させてい
た。また、発酵を効率良く行わせるために、発酵槽内を
多段式に形成したり、発酵槽内に攪拌装置を設けるなど
の各種の工夫がなされていた。Then, into the sludge fermentation tank, the already fermented and dried dung post and the crushed dehydrated cake are mixed in equal amounts and put into the fermentation tank, and the mixture is left in the fermentation tank for about 10 to 20 days, during which time air is removed from the sludge. It was fermented and dried biologically by blowing into it. In addition, in order to carry out fermentation efficiently, various measures have been taken, such as forming the inside of the fermenter in multiple stages and providing a stirring device in the fermenter.
発明が解決しようとする課題
しかし、上記した構成においては、発酵物である汚泥と
空気との接触効率を高めるために、発酵物を攪拌装置に
よって無理やり動かす操作(切り返し)をしていたので
、発酵物が部分的に練り固まった状態となる問題があっ
た。Problems to be Solved by the Invention However, in the above-mentioned configuration, in order to increase the contact efficiency between the fermented material, sludge, and air, the fermented material was forcibly moved (switched) using a stirring device. There was a problem in which the product was partially kneaded and hardened.
本発明は上記課題を解決するもので、発酵物の塊状化を
防止するとともに、発酵物を高効率に発酵させることが
できる汚泥の発酵処理方法を提供することを目的とする
。The present invention solves the above-mentioned problems, and aims to provide a sludge fermentation treatment method that can prevent fermented products from forming agglomerates and ferment fermented products with high efficiency.
課題を解決するための手段
上記課題を解決するために本発明は、し尿の活性汚泥処
理にて生じる余剰汚泥を脱水して脱水ケーキを形成し、
この脱水ケーキを原料汚泥として生物学的発酵槽に投入
し、生物学的発酵槽内で原料汚泥を発酵させる発酵処理
方法において、すでに発酵して堆肥化したコンポストを
生物学的発酵槽から取り出し、取り出したコンポストの
一部を返送コンポストとして重量比で少なくとも5倍の
割合で脱水ケーキに混合し、返送コンポストが混合され
た脱水ケーキを原料汚泥として生物学的発酵槽に投入す
る構成としたものである。Means for Solving the Problems In order to solve the above problems, the present invention dehydrates excess sludge generated in activated sludge treatment of human waste to form a dehydrated cake,
In a fermentation treatment method in which this dehydrated cake is put into a biological fermenter as raw material sludge and the raw material sludge is fermented in the biological fermenter, the compost that has already been fermented and composted is taken out from the biological fermenter, A portion of the removed compost is mixed with the dehydrated cake at a ratio of at least 5 times by weight as returned compost, and the dehydrated cake mixed with the returned compost is fed into the biological fermentation tank as raw material sludge. be.
作用
上記した構成により、返送コンポストの量が多くなるに
したがって原料汚泥の含水率が低下され、原料汚泥中に
含まれる脱水ケーキの発酵速度が向上するとともに、脱
水ケーキの乾燥が速やかに進む。また、返送コンポスト
を重量比で少なくとも5倍の割合で脱水ケーキに混合し
て原料汚泥を形成することにより、生物学的発酵槽内に
投入された脱水ケーキの発酵がほぼ1日で終了し、生物
学的発酵槽に対して脱水ケーキを毎日投入することがで
きる。Effect With the above-described configuration, as the amount of returned compost increases, the moisture content of the raw material sludge decreases, the fermentation rate of the dehydrated cake contained in the raw material sludge improves, and the drying of the dehydrated cake progresses rapidly. In addition, by mixing the returned compost with the dehydrated cake at a ratio of at least 5 times by weight to form raw material sludge, the fermentation of the dehydrated cake fed into the biological fermentation tank is completed in about one day. The biological fermenter can be fed daily with dehydrated cake.
実施例
以下本発明の一実施例を図面に基づいて説明する。第1
図において、生物学的発酵槽1の内部には原料汚泥2が
床上に滞留しており、原料汚泥2に空気を供給するため
のブロアー3が生物学的発酵槽1の下部に連通して設け
られている。そして、生物学的発酵槽1の上部に開口し
て原料供給路4が設けられており、原料供給路4の基端
側には脱水ケーキホッパー5が接続されている。この脱
水ケーキホッパー5は、し尿を活性汚泥処理したときに
生じる余剰汚泥を脱水するものである。また、生物学的
発酵槽1の下部に開口してフンポスト排出路6が設けら
れており、コンポスト排出路6は途中に解砕機7を介装
されて乾燥ケーキホッパー8に連通している。さらに、
解砕機7の下流側のコンポスト排出路6と原料供給路4
はバイパス路9を介して連通している。また、原料供給
路4とフンポスト排出路6とバイパス路9の内部にはコ
ンベア装置が設けられている。EXAMPLE An example of the present invention will be described below based on the drawings. 1st
In the figure, raw material sludge 2 is accumulated on the floor inside a biological fermenter 1, and a blower 3 for supplying air to the raw material sludge 2 is installed in communication with the lower part of the biological fermenter 1. It is being A raw material supply channel 4 is opened at the top of the biological fermenter 1, and a dehydrated cake hopper 5 is connected to the base end of the raw material supply channel 4. This dewatering cake hopper 5 is for dewatering excess sludge produced when human waste is treated with activated sludge. Further, a compost discharge passage 6 is provided to open at the bottom of the biological fermenter 1, and the compost discharge passage 6 is connected to a dry cake hopper 8 with a crusher 7 interposed therebetween. moreover,
Compost discharge path 6 and raw material supply path 4 on the downstream side of the crusher 7
are in communication via a bypass path 9. Moreover, a conveyor device is provided inside the raw material supply path 4, the dung post discharge path 6, and the bypass path 9.
以下、上記構成における作用について説明する。Hereinafter, the effects of the above configuration will be explained.
余剰汚泥を脱水ケーキホッパー5において含水率70%
程度に脱水し、脱水された脱水ケーキを原料供給路4に
取り出し、生物学的発酵槽2に向けて送給する。このと
き、脱水ケーキは原料供給路4のコンベア装置のスクリ
ュー羽根によって解砕される。一方、生物学的発酵槽1
において既に発酵・乾燥され、堆肥化された含水率40
%程度のコンポストを、コンポスト排出路6を通して生
物学的発酵槽1から取り出すとともに、解砕機7で塊状
のコンポストを解砕する。そして、解砕されたコンポス
トの一部をバイパス路9を通して原料供給路4に返送コ
ンポストとして供給し、返送コンポストと脱水ケーキと
を混合して形成された原料汚泥を原料供給路4から生物
学的発酵槽1に投入する。このとき、脱水ケーキに対す
る返送コンポストの供給量は重量比で少なくとも5倍以
上の割合とする。このことによって、原料汚泥の含水率
が返送コンポストの含水率の5%増以内となるようにす
る。尚、原料汚泥の含水率Xは次式で計算される。Excess sludge is dehydrated to a moisture content of 70% in cake hopper 5.
The dehydrated cake is taken out to the raw material supply path 4 and fed toward the biological fermenter 2. At this time, the dehydrated cake is crushed by the screw blades of the conveyor device in the raw material supply path 4. On the other hand, biological fermenter 1
moisture content 40 which has already been fermented, dried and composted in
% of the compost is taken out from the biological fermenter 1 through the compost discharge path 6, and the lumped compost is crushed by the crusher 7. Then, a part of the crushed compost is supplied as return compost to the raw material supply route 4 through the bypass route 9, and the raw material sludge formed by mixing the returned compost and the dehydrated cake is sent from the raw material supply route 4 to the raw material supply route 4. Pour into fermenter 1. At this time, the amount of returned compost supplied to the dehydrated cake should be at least 5 times or more by weight. This ensures that the water content of the raw material sludge is within 5% of the water content of the returned compost. In addition, the water content X of the raw material sludge is calculated by the following formula.
X= (mt w+m2W)/ (W+nW)但し、W
:脱水ケーキの重量、n:倍率、ml :脱水ケーキの
含水率、m2:返送コンポストの含水率である。X= (mt w+m2W)/(W+nW) However, W
: weight of dehydrated cake, n: magnification, ml: moisture content of dehydrated cake, m2: moisture content of returned compost.
そして、生物学的発酵槽1に滞留する原料汚泥に対して
空気をブロアー3によって吹き込み、原料汚泥を発酵・
乾燥させて堆肥化する。さらに、堆肥化されたコンポス
トは、コンポスト排出路6を通って乾燥ケーキホッパー
8に送られるとともに、一部が前述した返送コンポスト
として原料供給路4に供給される。Then, air is blown into the raw material sludge staying in the biological fermenter 1 using a blower 3 to ferment and ferment the raw material sludge.
Dry and compost. Further, the composted compost is sent to the dry cake hopper 8 through the compost discharge path 6, and a portion is supplied to the raw material supply path 4 as the above-mentioned return compost.
そして、以上の乾燥・発酵過程においては、返送コンポ
ストの量が多くなるにしたがって原料汚泥の含水率が低
下され、原料汚泥中に含まれる脱水ケーキの発酵速度が
向上するとともに、脱水ケーキの乾燥が速やかに進む。In the above drying and fermentation process, as the amount of returned compost increases, the moisture content of the raw material sludge decreases, the fermentation speed of the dehydrated cake contained in the raw material sludge improves, and the drying of the dehydrated cake increases. Proceed quickly.
そして、返送コンポストを重量比で少なくとも5倍以上
の割合で脱水ケーキに混合して原料汚泥を形成すること
により、生物学的発酵槽1内に投入された脱水ケーキの
発酵がほぼ1日で終了し、生物学的発酵槽に対して脱水
ケーキを毎日投入することができる。第2図は、返送コ
ンポストと脱水ケーキの混合割合を変えて行った発酵・
乾燥過程の比較を示すものであり、Aは返送コンポスト
が5倍の場合を示し、Bは3倍の場合を示し、Cは等量
の場合を示している。第2図から明らかなように、原料
汚泥の含水率が高い程に温度上昇が遅くなり、かつ高温
持続時間が長くなる。また、フンポストは乾燥が進み、
温度が低くならないとコンベア装置や解砕機に詰まりゃ
搬送能力に対する過負荷が生じる。通常、搬送可能なコ
ンポストの温度は、常温より+15℃程度までである。Then, by mixing the returned compost with the dehydrated cake at a ratio of at least 5 times by weight to form raw material sludge, the fermentation of the dehydrated cake fed into the biological fermenter 1 is completed in about one day. However, the biological fermenter can be fed with dehydrated cake daily. Figure 2 shows the fermentation process conducted by changing the mixing ratio of returned compost and dehydrated cake.
A comparison of the drying process is shown, where A shows the case where the amount of returned compost is 5 times, B shows the case where the amount is 3 times, and C shows the case where the amount is the same. As is clear from FIG. 2, the higher the water content of the raw material sludge, the slower the temperature rise and the longer the high temperature duration. In addition, the drying of the fun post progresses,
If the temperature is not lowered, the conveyor equipment or crusher will become clogged, resulting in an overload on the conveying capacity. Normally, the temperature of compost that can be transported is about +15°C from room temperature.
したがって、返送コンポストの比が5倍の場合にほぼ1
日で発酵が終了し、原料汚泥を毎日投入することができ
る。反対に、返送コンポストの比が少なくなると、高温
持続時間が長くなるため、原料汚泥の投入間隔が長くな
り、結果的に大きな容量の生物学的発酵槽1を必要とす
る。例えば、Aの場合とBの場合を比較したときに、同
一期間に同一量の脱水ケーキを処理するためには、Bの
場合には発酵に2〜3日かかるので、Aの場合に較べ2
〜3倍の発酵槽容量を必要とする。Therefore, when the ratio of returned compost is 5 times, it is almost 1
Fermentation is completed within a day, and raw material sludge can be added every day. On the other hand, when the ratio of returned compost decreases, the high temperature duration becomes longer, so the feeding interval of raw material sludge becomes longer, and as a result, a biological fermenter 1 with a larger capacity is required. For example, when comparing case A and case B, in order to process the same amount of dehydrated cake in the same period, fermentation will take 2 to 3 days in case B, so compared to case A, it will take 2 to 3 days.
Requires ~3 times the fermenter volume.
発明の効果
以上述べたように本発明によれば、返送コンポストを重
量比で少なくとも5倍の割合で脱水ケーキに混合して原
料汚泥を形成することにより、生物学的発酵槽内に投入
された脱水ケーキの発酵を促進し、発酵をほぼ1日で終
了させることができ、生物学的発酵槽に対して脱水ケー
キを毎日投入することができる。Effects of the Invention As described above, according to the present invention, the returned compost is mixed with the dewatered cake at a ratio of at least 5 times by weight to form raw material sludge, which is then charged into the biological fermenter. Fermentation of the dehydrated cake can be accelerated and fermentation can be completed in approximately one day, and the dehydrated cake can be charged to the biological fermenter every day.
また、発酵が速やかに進行するので、撹拌装置を必要と
せず、撹拌によるコンポストの塊状化を防止することが
できる。Furthermore, since fermentation proceeds quickly, a stirring device is not required, and it is possible to prevent the compost from clumping together due to stirring.
第1図は本発明の一実施例を示す全体溝成図、第2図は
返送フンポスト比の異なる原料汚泥の発酵過程の比較図
である。
1・・・生物学的発酵槽、2・・・原料汚泥、4・・・
原料供給路、5・・・脱水ケーキホッパー、6・・・コ
ンポスト排出路、9・・・バイパス。FIG. 1 is an overall diagram showing an embodiment of the present invention, and FIG. 2 is a comparison diagram of the fermentation process of raw material sludge with different return sludge ratios. 1... Biological fermenter, 2... Raw material sludge, 4...
Raw material supply path, 5... Dehydration cake hopper, 6... Compost discharge path, 9... Bypass.
Claims (1)
脱水ケーキを形成し、この脱水ケーキを原料汚泥として
生物学的発酵槽に投入し、生物学的発酵槽内で原料汚泥
を発酵させる発酵処理方法において、すでに発酵して堆
肥化したコンポストを生物学的発酵槽から取り出し、取
り出したコンポストの一部を返送コンポストとして重量
比で少なくとも5倍の割合で脱水ケーキに混合し、返送
コンポストが混合された脱水ケーキを原料汚泥として生
物学的発酵槽に投入することを特徴とする汚泥の発酵処
理方法。1. Dehydrate excess sludge generated in activated sludge treatment of human waste to form a dehydrated cake, feed this dehydrated cake as raw material sludge into a biological fermenter, and ferment the raw material sludge in the biological fermenter. In the fermentation treatment method, the compost that has already been fermented and composted is removed from the biological fermenter, and a part of the removed compost is mixed into the dewatered cake at a ratio of at least 5 times by weight as return compost, and the return compost is A sludge fermentation treatment method characterized by charging a mixed dehydrated cake as raw material sludge into a biological fermentation tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1078777A JPH075419B2 (en) | 1989-03-29 | 1989-03-29 | Fermentation method of sludge |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1078777A JPH075419B2 (en) | 1989-03-29 | 1989-03-29 | Fermentation method of sludge |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH02255586A true JPH02255586A (en) | 1990-10-16 |
JPH075419B2 JPH075419B2 (en) | 1995-01-25 |
Family
ID=13671329
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1078777A Expired - Lifetime JPH075419B2 (en) | 1989-03-29 | 1989-03-29 | Fermentation method of sludge |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH075419B2 (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100676867B1 (en) * | 2005-08-26 | 2007-02-01 | 주식회사 파이닉스알엔디 | Dewatering Cake Processing Equipment |
CN112077132A (en) * | 2019-06-14 | 2020-12-15 | 杭州洁洁环保科技有限公司 | Dry type fermentation and biochemical treatment integrated machine for garbage and treatment process |
CN116114571A (en) * | 2022-12-07 | 2023-05-16 | 中交(天津)生态环保设计研究院有限公司 | Method for preparing greening soil by dehydrating and synchronously fermenting engineering bags of soil at dredging bottom of river and lake |
-
1989
- 1989-03-29 JP JP1078777A patent/JPH075419B2/en not_active Expired - Lifetime
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR100676867B1 (en) * | 2005-08-26 | 2007-02-01 | 주식회사 파이닉스알엔디 | Dewatering Cake Processing Equipment |
CN112077132A (en) * | 2019-06-14 | 2020-12-15 | 杭州洁洁环保科技有限公司 | Dry type fermentation and biochemical treatment integrated machine for garbage and treatment process |
CN112077132B (en) * | 2019-06-14 | 2024-03-12 | 杭州洁洁环保科技有限公司 | Dry-type fermentation biochemical treatment integrated machine and treatment process for garbage |
CN116114571A (en) * | 2022-12-07 | 2023-05-16 | 中交(天津)生态环保设计研究院有限公司 | Method for preparing greening soil by dehydrating and synchronously fermenting engineering bags of soil at dredging bottom of river and lake |
Also Published As
Publication number | Publication date |
---|---|
JPH075419B2 (en) | 1995-01-25 |
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