JPS5855391A - Method of composting organic waste - Google Patents

Method of composting organic waste

Info

Publication number
JPS5855391A
JPS5855391A JP56152650A JP15265081A JPS5855391A JP S5855391 A JPS5855391 A JP S5855391A JP 56152650 A JP56152650 A JP 56152650A JP 15265081 A JP15265081 A JP 15265081A JP S5855391 A JPS5855391 A JP S5855391A
Authority
JP
Japan
Prior art keywords
water
exhaust gas
fermenter
supplied
organic waste
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
Application number
JP56152650A
Other languages
Japanese (ja)
Inventor
山縣 昌継
博史 野口
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP56152650A priority Critical patent/JPS5855391A/en
Publication of JPS5855391A publication Critical patent/JPS5855391A/en
Pending 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
    • Y02ATECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
    • Y02A40/00Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
    • Y02A40/10Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in agriculture
    • Y02A40/20Fertilizers of biological origin, e.g. guano or fertilizers made from animal corpses

Abstract

(57)【要約】本公報は電子出願前の出願データであるた
め要約のデータは記録されません。
(57) [Summary] This bulletin contains application data before electronic filing, so abstract data is not recorded.

Description

【発明の詳細な説明】 本発明は、有機性廃東物を発酵処理物と混合した後に好
気性発酵槽で処理する有機性廃集物の堆肥化方法に関す
る。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for composting organic waste collection, in which organic waste is mixed with a fermented product and then treated in an aerobic fermenter.

上記方法では、好気性菌の活性を高める上から発酵槽内
の温度を比較的高温状−に維持することが好まLZが、
従来、発酵槽への酸素含有ガスの供給に伴い、その供給
ガスの温度が低いために槽内温度が上昇し難く、そのた
め好気性菌の活性が上シにくくなる不都合があり、又、
発$!&!に際し、好気性菌の活性が高まるに連れて発
酵槽内の温度が高くなシ、それに伴い、発酵槽内の水分
が減少し、好気性菌の活性が低下して発酵処理効率が着
L〈低下する問題があツタ。 !@に、 発11[6理
に伴ってアンモニアガス等の悪臭が発生され、環境衛生
面でも改善の余地があった。
In the above method, it is preferable to maintain the temperature in the fermenter at a relatively high temperature in order to increase the activity of aerobic bacteria.
Conventionally, when oxygen-containing gas is supplied to a fermenter, the temperature of the supplied gas is low, making it difficult to raise the temperature inside the tank, which makes it difficult to increase the activity of aerobic bacteria.
Starting $! &! At this time, as the activity of aerobic bacteria increases, the temperature inside the fermenter increases, and as a result, the moisture in the fermenter decreases, the activity of aerobic bacteria decreases, and the efficiency of fermentation treatment decreases. Ivy is a problem that decreases. ! @, Air 11 [6] Ammonia gas and other foul odors were generated due to the process, and there was room for improvement in terms of environmental hygiene.

本発明は、上記の点に鑑み、発酵処理に伴って発生する
排ガスに起因する環境悪化の問題を解消できるようにす
ると共に、そのためのm成並びに発酵槽からの排ガスを
有効利用して、発酵槽内温度よりはるかに低い温度の酸
素含有ガスの供給に起因する槽内温度の低下、あるいは
、槽内における水分減少を抑制し1発#!IJ1理効率
tPIIk済的に向上できるようにすることを目的とす
る。
In view of the above points, the present invention makes it possible to solve the problem of environmental deterioration caused by exhaust gas generated during fermentation processing, and effectively utilizes the exhaust gas from the fermentation tank and fermentation process. Suppresses the drop in the temperature inside the tank or the decrease in water content in the tank due to the supply of oxygen-containing gas at a temperature much lower than the temperature inside the tank. The purpose is to make it possible to improve IJ1 management efficiency tPIIk economically.

次に、未発明方法実施の態様を例示図に1いて説明する
Next, embodiments of the uninvented method will be described with reference to illustrative drawings.

下水汚泥と種汚泥とを夫々第7及び第コホツパーif)
帽!lt介して混合装置il+に供給し、混合IIJ1
flIする。
sewage sludge and seed sludge respectively in the 7th and 7th cohopper if)
Hat! lt to the mixing device il+ and mixing IIJ1
flI.

混合処理物を発酵槽(咄)に供給して堆積滞留させ、そ
の下方からブロアーill Kよって9気を供給し、好
気性菌の活性により発Wll&fll 8せ、発酵に伴
って発生するガス中余剰9気等の排ガスを排出路(−1
を通じて外11に排出させながら、発酵も運物を取出し
、その一部を前記種汚泥として返送路(1)を通じ@J
ホッパー(!1に供給し、他方、伐Stそのままあるい
は必要ならば、更に1発酵、乾燥等の彼処*1施し友後
に取出して製品としての堆肥を得る。
The mixed product is supplied to a fermentation tank and allowed to accumulate there, and air is supplied from below by a blower Ill K, causing Wll&Fll8 to be generated by the activity of aerobic bacteria, and the surplus in the gas generated due to fermentation is removed. 9 Exhaust gas such as air is removed from the exhaust passage (-1
While discharging to outside 11 through
The compost is fed into a hopper (!1), and on the other hand, it is removed as it is or, if necessary, after further fermentation, drying, etc.*1, to obtain compost as a product.

前記力°ス排出路(6)に熱交換装置(81t−介装し
、その熱交換装置<81に、前記ブロアー(81を付設
した空気供給路(9)を通し、発酵槽(4)に供給する
空気を排ガスを有効利用して予熱する。
A heat exchange device (81t) is installed in the power gas discharge path (6), and an air supply path (9) equipped with the blower (81) is passed through the heat exchange device (81) to the fermenter (4). The supplied air is preheated by effectively utilizing exhaust gas.

又、前記ガス排出路(@1に排ガス処理装置叫を介装し
、予熱に伴って低温化された排ガスに水をシャワー供給
するとかあるりは排ガスを水中に供給してバブリングす
る等により、排ガスに水を接触させ、排ガス中に含まれ
る主としてアンモニアガス等の悪臭ガスを水に捕捉して
脱臭処理する。
In addition, by interposing an exhaust gas treatment device in the gas exhaust passage (@1) and supplying water to the exhaust gas whose temperature has been lowered due to preheating, or by supplying the exhaust gas into water and bubbling it, Water is brought into contact with the exhaust gas, and malodorous gases contained in the exhaust gas, mainly ammonia gas, are captured in the water and deodorized.

前記熱交換装置il+からの凝縮水、及び、排ガス処理
装置Aからの排ガス処理後の水をPH調整槽1ll) 
iC供給し1その調整槽(川に、硫酸や塩酸等の酸性薬
剤を投入して中和処理し、その中和処理後の水を沈澱槽
lI埠に供給貯留する。
The condensed water from the heat exchange device il+ and the water after exhaust gas treatment from the exhaust gas treatment device A are transferred to a PH adjustment tank (1 liter).
iC is supplied, and an acidic agent such as sulfuric acid or hydrochloric acid is added to the river to neutralize it, and the water after the neutralization is supplied to the settling tank II and stored there.

中和処理後の特に不純物の濃縮された水を、沈澱檜0笥
から発酵槽T411C,開閉弁a4を付設したポンプ付
管路舖を介して供給し、そして、余剰の水を後熱m装置
0時に供給して殺菌等の後処理を施し次後に放流する。
After the neutralization treatment, water with particularly concentrated impurities is supplied from the settling cypress bowl through a fermentation tank T411C and a pipe pipe equipped with a pump equipped with an on-off valve A4, and the excess water is transferred to a post-heating device. It is supplied at 0 o'clock, subjected to post-treatment such as sterilization, and then discharged.

前記発酵槽(4)内に温度又はおよび水分センサー0η
會設けて槽内温度又はおよび水分か設定値以下になった
ことを検出させ、その検出結果を制a器Iに入力し、前
記開閉弁■を自動的に鍔間操作し、発酵槽(4)K水を
供給する・即ち、発酵槽(4)において、好気性菌の活
性が高くなって発酵が促進されるに伴って槽内温度が上
昇するが、それに伴って槽内の水分か蒸発飛散し、発酵
に適した水分が不足し、その結果、好気性菌の活性が低
下し1それに伴って温度が急激に降下する仁ととなるの
であり、その事に着目して槽内温度又#iおよび水分が
設定値以下になった事の検出に基めで槽内の水分不足を
検出させ、開閉弁04を関いて自動的に給水し、好気性
■の活性を高めるのである。
Temperature or moisture sensor 0η in the fermenter (4)
A system is set up to detect whether the temperature or water content in the tank has fallen below the set value, input the detection result to controller I, automatically operate the on-off valve ) Supplying K water - In other words, in the fermenter (4), the temperature inside the tank rises as the activity of aerobic bacteria increases and fermentation is promoted, but as a result, the water in the tank evaporates. This causes a lack of moisture suitable for fermentation, resulting in a decrease in the activity of aerobic bacteria, resulting in kernels whose temperature drops rapidly. Based on the detection of #i and the fact that the water content has fallen below the set value, a lack of water in the tank is detected, and water is automatically supplied via the on-off valve 04 to increase the aerobic activity.

前記タンク9埠には、酸性薬剤の種類に6じ、中和処m
に伴って生成される、硫酸アンモニクム中塩化アンモニ
クム悸のアンモニクム塩が蓄積されるこtとなるか、発
酵槽(4)への給水に伜、って、それらアンモニクム塩
が発酵槽中へ堆肥として回収されることとなり、中和4
fl−理物をも無駄無く活用でき、かつ、後!IJ1j
I装置α−におけるアンモニクム塩の除去処理を簡略化
できている。
The tank 9 has 6 types of acidic chemicals and neutralization treatment m.
The ammonium salts (ammonicum chloride in ammonium sulfate) that are produced along with this process may accumulate, or when water is supplied to the fermenter (4), these ammonium salts are transferred into the fermenter as compost. It will be collected, and neutralization 4
fl-You can use physical materials without wasting them, and after! IJ1j
The ammonium salt removal process in the I apparatus α- can be simplified.

上記実施例では、種汚泥として、発酵槽(4)で発11
J611された!&処理物利用するようにしているが、
別途処理した発#処理物とか下水汚泥とけ異質の発#処
理物等、要する〔で、その供M!に伴い、堆肥化りよう
とする下水汚泥の発酵の促進とか温度や水分等の調整を
図れるものであれば各種の発酵!&処理物適用できる。
In the above example, 11
It was J611! & I try to use processed materials,
Separately treated waste products, sewage sludge, foreign waste products, etc. are required. Along with this, various types of fermentation can be carried out as long as it is possible to promote the fermentation of sewage sludge to be composted or to adjust temperature, moisture, etc.! & Can be applied to processed materials.

前記発酵槽(4)に酸素含有ガスを供給するのに、ブロ
アー(組を用いずに自然通気によって供給しても良い。
The oxygen-containing gas may be supplied to the fermenter (4) by natural ventilation without using a blower.

 又、空気に代えて、高濃度の酸素ガスや純酸素等を用
いても良い。
Further, instead of air, highly concentrated oxygen gas, pure oxygen, etc. may be used.

未発明は、上述のような下水汚泥の堆肥化処理に限らず
、例えば、し原汚泥、産業廃水汚泥、農産物残余廃棄物
、都市ゴミ等、各種の有機性廃棄物の堆肥化処理に適用
できる。
The invention is applicable not only to the composting of sewage sludge as described above, but also to the composting of various organic wastes, such as raw sludge, industrial wastewater sludge, agricultural residue waste, and municipal garbage. .

以上要するに、未発明は、冒記した有機性廃棄物の堆肥
化方法において、前記発酵槽14)K供給する酸素含有
ガスを前記発酵槽(4)からの排ガスによって予熱処理
し、予熱後の排ガスを水に接触させて脱臭JiJ1j!
すると共に、排ガス処理後の水の一部を前記発酵槽(4
)に−fiすることt−特徴とする。
In summary, in the method for composting organic waste mentioned above, the oxygen-containing gas supplied to the fermenter 14) is preheated by the exhaust gas from the fermenter (4), and the exhaust gas after preheating is Deodorizes JiJ1j by contacting it with water!
At the same time, part of the water after exhaust gas treatment is transferred to the fermenter (4).
) to be characterized by t-.

つまり、発酵槽(4)から高温で取出される排ガスを有
効利用し1その排ガスにょシ発酵槽(4)への酸素含有
ガスを予熱し、特別な加熱装置を付加する事無く、発酵
槽(4)内温度よりはるかに低い温度の酸素含有ガスの
供給に伴う発酵槽(4)内の温度低Ft回避でき、又、
排ガス中に含まれる悪臭ガスを、予熱処理後の排ガスに
対する水との接触(よ)水に捕捉させるから、排ガス処
理に際しての水の蒸発量を抑えて脱臭処理し1環境悪化
の問題を解消でき、しか啄、その排ガス地理後の水を有
効利用して発酵槽(4)に供給し、発酵槽(4)での水
分不足を回避して好気性菌の活性低下を抑制し、発酵処
理効率を向上できるに至り、全体として、前述の排ガス
処理水蒸発の抑制と相俟って水資源t−節約でき、かつ
、排ガス処理後の水を殺菌等の後!&理する場合であれ
ば、その処理水量を減少して彼処l!股備の簡略化や薬
剤使用量の低減を図れ、極めて経済的に発酵処理効率を
向上できるに至った。
In other words, by effectively utilizing the exhaust gas taken out from the fermenter (4) at high temperature, and preheating the oxygen-containing gas to the fermenter (4), the fermenter (4) can be heated without adding a special heating device. 4) Low temperature Ft in the fermenter (4) due to supply of oxygen-containing gas at a temperature much lower than the internal temperature can be avoided, and
The foul-smelling gas contained in the exhaust gas is trapped in the water that comes into contact with the exhaust gas after preheating, so the amount of water evaporated during exhaust gas treatment can be suppressed and deodorized, eliminating the problem of environmental deterioration. However, the water after the exhaust gas is effectively used and supplied to the fermenter (4) to avoid water shortage in the fermenter (4), suppress the decline in the activity of aerobic bacteria, and improve fermentation processing efficiency. Overall, combined with the above-mentioned suppression of evaporation of exhaust gas treatment water, water resources can be saved, and the water after exhaust gas treatment can be sterilized. & If treatment is required, reduce the amount of water to be treated. By simplifying the equipment and reducing the amount of chemicals used, it has become possible to improve fermentation processing efficiency extremely economically.

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

図面は未発IJ[係る有機性廃棄物の堆肥化方法の爽施
の態様を例示する70−シートである。 (4)・・・・・・発酵槽。
The drawing is a 70-sheet illustrating an embodiment of the method for composting ungenerated IJ. (4)...Fermentation tank.

Claims (1)

【特許請求の範囲】[Claims] 有機性廃集物を発酵処理物と混合した後に好気性発酵槽
(4)で処理する有機性廃集物の堆肥化方法であって、
前記発酵槽(4)に供給する酸素含有ガスを前記発酵槽
(4)からの排ガスによって予熱18111L、予熱後
の排ガスを水に接触させて脱臭処理すると共に、排ガス
処理後の水の一部を前記発酵槽(4)に供給することを
特徴とする有機性廃集物の堆肥化方法。
A method for composting organic waste collection, which comprises mixing the organic waste collection with a fermentation product and then treating it in an aerobic fermentation tank (4),
The oxygen-containing gas supplied to the fermenter (4) is preheated 18111L by the exhaust gas from the fermenter (4), the preheated exhaust gas is brought into contact with water and deodorized, and a portion of the water after the exhaust gas treatment is A method for composting organic waste, characterized in that it is supplied to the fermentation tank (4).
JP56152650A 1981-09-26 1981-09-26 Method of composting organic waste Pending JPS5855391A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56152650A JPS5855391A (en) 1981-09-26 1981-09-26 Method of composting organic waste

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56152650A JPS5855391A (en) 1981-09-26 1981-09-26 Method of composting organic waste

Publications (1)

Publication Number Publication Date
JPS5855391A true JPS5855391A (en) 1983-04-01

Family

ID=15545054

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56152650A Pending JPS5855391A (en) 1981-09-26 1981-09-26 Method of composting organic waste

Country Status (1)

Country Link
JP (1) JPS5855391A (en)

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5238369A (en) * 1975-09-15 1977-03-24 Kneer Franz X Process and apparatus for continuous composting of organic waste and or waste water sludge
JPS54123468A (en) * 1978-03-15 1979-09-25 Toyo Boseki Production of organic fertilizer

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5238369A (en) * 1975-09-15 1977-03-24 Kneer Franz X Process and apparatus for continuous composting of organic waste and or waste water sludge
JPS54123468A (en) * 1978-03-15 1979-09-25 Toyo Boseki Production of organic fertilizer

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