JPH11216500A - Solubilizing treatment of organic sludge - Google Patents

Solubilizing treatment of organic sludge

Info

Publication number
JPH11216500A
JPH11216500A JP10022432A JP2243298A JPH11216500A JP H11216500 A JPH11216500 A JP H11216500A JP 10022432 A JP10022432 A JP 10022432A JP 2243298 A JP2243298 A JP 2243298A JP H11216500 A JPH11216500 A JP H11216500A
Authority
JP
Japan
Prior art keywords
organic sludge
sludge
pump device
tank
temp
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
JP10022432A
Other languages
Japanese (ja)
Inventor
Masashi Moro
正史 師
Yuji Soeda
祐二 添田
Tetsuya Yamamoto
哲也 山本
Toshiyuki Shibata
敏行 柴田
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 JP10022432A priority Critical patent/JPH11216500A/en
Publication of JPH11216500A publication Critical patent/JPH11216500A/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

Landscapes

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

Abstract

PROBLEM TO BE SOLVED: To easily and homogeneously solubilize an organic sludge by stirring the organic sludge in a treating tank to increase the temp. by the frictional heat generating at this time to solubilize. SOLUTION: A change port 2 on the ceiling and a discharge port on the bottom are arranged in the treating tank 1. An the upper part and the lower part of the treating tank 1 are connected to each other through a circulating pipe 4 and the organic sludge 8 is circulated by an under water pump device 5 having an impeller. A thermocouple 6 is disposed at the upper part of the treating tank 1 and connected to the impeller type under water pump device 5 through an inverter control device 7 to control the speed of revolution of the pump device 5. In this structure, the under water pump device 5 is driven to continuously circulate the organic sludge 8. Then, the frictional heat is generated by the shearing due to the impeller of the pump device 5 to elevate the temp. of the organic sludge 8. The speed of revolution is controlled by the detected temp. of the thermocouple 6 to keep to a prescribed temp. The sludge is solubilized by this manner to improve fermentation efficiency.

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、下水汚泥、浄化槽
汚泥、厨芥、畜産ふん尿などの有機性汚泥を発酵させる
に先立って行う有機性汚泥の可溶化処理方法に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for solubilizing organic sludge prior to fermenting organic sludge such as sewage sludge, septic tank sludge, kitchen waste and livestock manure.

【0002】[0002]

【従来の技術】従来、発酵プラント、バイオガス生産・
汚泥減容プラントなど、好気性あるいは嫌気性発酵を行
う施設では、可溶化または酸発酵と呼ばれる工程、すな
わち有機物中に含まれる蛋白質、脂肪などの難消化性物
質を液状化、低分子量化する工程が必要であり、種々の
試みがなされている。
2. Description of the Related Art Conventionally, fermentation plants, biogas production and
In facilities that perform aerobic or anaerobic fermentation such as sludge volume reduction plants, a process called solubilization or acid fermentation, that is, a process of liquefying and reducing the molecular weight of indigestible substances such as proteins and fats contained in organic matter. And various attempts have been made.

【0003】たとえば、特公平4−70080号では、
下水汚泥、農水産廃棄物等の有機性汚泥をアルカリでp
H9〜11に調整することによって汚泥中の微生物菌体
の細胞壁を破壊し、残存する菌体等の固形物を湿式ミル
処理によって破砕し、その後に嫌気性消化している。
For example, in Japanese Patent Publication No. Hei 4-70080,
Organic sludge such as sewage sludge and agricultural and marine waste is treated with alkali.
The cell wall of the microbial cells in the sludge is destroyed by adjusting to H9 to 11, and the solid matter such as the remaining cells is crushed by wet mill treatment, and then anaerobically digested.

【0004】特開昭55−97298号では、生物処理
した後の難生物学的処理有機物(細胞膜、セルロース)
を含んだ被処理水にオゾンを吹き込むことにより、有機
物の炭素長鎖を切ったり酸化物を生成させて易生物学的
処理有機物へと分解し、再び生物処理するようにしてい
る。
Japanese Patent Application Laid-Open No. 55-97298 discloses a biologically difficult organic material (cell membrane, cellulose) after biological treatment.
Ozone is blown into the water to be treated, which contains carbon dioxide, thereby breaking the long carbon chain of the organic substance or generating an oxide to decompose it into an easily biologically treated organic substance, which is then subjected to biological treatment again.

【0005】特開昭62−83100号、特公平4−1
2198号では、有機性汚泥を加熱することによって汚
泥中の有機成分を可溶化、低分子量化しており、その後
の嫌気性処理工程での分解率を高めている。
JP-A-62-283100, Japanese Patent Publication No. 4-1
In No. 2198, the organic components in the sludge are solubilized and reduced in molecular weight by heating the organic sludge, and the decomposition rate in the subsequent anaerobic treatment step is increased.

【0006】[0006]

【発明が解決しようとする課題】しかしながら、上記し
たアルカリあるいはオゾンを作用させる処理方法の場
合、アルカリ剤やオゾンガスのために設備コストやラン
ニングコストがかかるだけでなく、残アルカリや残オゾ
ンによる後段の生物処理への悪影響を防止する何らかの
対策を講じなければならない。
However, in the case of the above-mentioned treatment method in which alkali or ozone is applied, not only equipment costs and running costs are incurred due to the alkali agent and ozone gas, but also the latter stage due to residual alkali and residual ozone. Some measures must be taken to prevent adverse effects on biological treatment.

【0007】加熱処理法の場合、ある程度放熱できれば
後段への影響も少ないが、大容量のヒーターと攪拌装置
が必要であるため、設備コスト並びにランニングコスト
がかかり、また処理対象物が高濃度であると容易に攪拌
できず、均質な可溶化が困難である。
In the case of the heat treatment method, if the heat can be radiated to some extent, the influence on the subsequent stage is small, but since a large-capacity heater and a stirrer are required, equipment costs and running costs are increased, and the object to be treated has a high concentration. Cannot be easily stirred, and uniform solubilization is difficult.

【0008】本発明は上記問題を解決するもので、有機
性汚泥を容易かつ均質に可溶化できる有機性汚泥の可溶
化処理方法を提供することを目的とするものである。
An object of the present invention is to solve the above-mentioned problems, and an object of the present invention is to provide a method for solubilizing organic sludge, which can solubilize organic sludge easily and uniformly.

【0009】[0009]

【課題を解決するための手段】上記問題を解決するため
に、本発明の有機性汚泥の可溶化処理方法は、発酵に先
立って行う有機性汚泥の可溶化処理方法であって、処理
槽の内部に導入した有機性汚泥を羽根式攪拌手段によっ
て攪拌し、攪拌に伴って発生する摩擦熱で昇温させるこ
とにより可溶化させることを特徴とする。
Means for Solving the Problems In order to solve the above problems, the method for solubilizing organic sludge of the present invention is a method for solubilizing organic sludge performed prior to fermentation. The organic sludge introduced into the inside is stirred by a blade type stirring means, and is solubilized by raising the temperature by frictional heat generated by the stirring.

【0010】好ましくは、羽根式攪拌手段として、処理
槽の内部と槽外の循環流路とにわたって有機性汚泥を循
環させる循環ポンプ装置を使用する。上記した構成によ
れば、有機性汚泥は、攪拌羽根により剪断されつつ攪拌
混合され、特に攪拌羽根の部分において発生する摩擦熱
によって昇温し、これらの相乗効果によって均質に可溶
化される。その際、有機性汚泥を50℃以上に保持する
と、汚泥構成物質の細胞のタンパク質が変成し、可溶化
率が高くなる。
[0010] Preferably, a circulation pump device for circulating organic sludge through the inside of the treatment tank and the circulation flow path outside the tank is used as the blade-type stirring means. According to the above configuration, the organic sludge is stirred and mixed while being sheared by the stirring blade, and the temperature is increased by frictional heat generated particularly at the portion of the stirring blade, and the organic sludge is uniformly solubilized by a synergistic effect of these. At this time, when the organic sludge is kept at 50 ° C. or higher, the protein of the sludge constituent substance is denatured, and the solubilization rate increases.

【0011】循環ポンプ装置は槽内設置型であるか槽外
設置型であるかを問わず必然的に容量が大きく、強大な
循環攪拌力を発揮するものであるため、比較的濃度が低
い下水汚泥や浄化槽汚泥はもちろんのこと、粘度が高
い、たとえばTS濃度1.5%以上の厨芥や畜産ふん尿
なども均一に攪拌混合され、昇温して可溶化される。
[0011] The circulating pump device is inevitably large in capacity regardless of whether it is an in-tank type or an out-of-tank type. Not only sludge and septic tank sludge, but also high-viscosity, for example, kitchen waste and livestock manure having a TS concentration of 1.5% or more are uniformly stirred and mixed, and heated to solubilize.

【0012】[0012]

【発明の実施の形態】以下、本発明の実施形態を図面を
参照しながら説明する。図1において、処理槽1は、メ
タン発酵を行う嫌気性発酵槽(図示せず)の前段に設置
されて有機性汚泥を可溶化(すなわち加水分解)し、酸
発酵させるものであり、断熱構造を有している。
Embodiments of the present invention will be described below with reference to the drawings. In FIG. 1, a treatment tank 1 is provided in front of an anaerobic fermenter (not shown) for performing methane fermentation, solubilizes (ie, hydrolyzes) organic sludge, and performs acid fermentation. have.

【0013】処理槽1には、天部に投入口2が形成さ
れ、下部に排出口3が形成されるとともに、槽内の下部
と上部とを連通する循環管4が設けられていて、この循
環管4の下端は、インペラ(図示せず)を有した水中ポ
ンプ装置5の吐出口に接続している。
The treatment tank 1 has an inlet 2 formed in the top part, an outlet 3 formed in the lower part, and a circulation pipe 4 communicating the lower part and the upper part in the tank. The lower end of the circulation pipe 4 is connected to a discharge port of a submersible pump device 5 having an impeller (not shown).

【0014】処理槽1の上部には、槽内の有機性汚泥の
温度を測定する熱電対6が設けられており、この熱電対
6と水中ポンプ装置5とに電気的に接続して、熱電対6
からの温度データに基いてポンプ装置5の回転数を制御
するインバータ制御装置7が設けられている。
A thermocouple 6 for measuring the temperature of the organic sludge in the tank is provided at the upper part of the treatment tank 1. The thermocouple 6 is electrically connected to the thermocouple 6 and the submersible pump device 5 to form a thermocouple. Vs. 6
There is provided an inverter control device 7 for controlling the rotation speed of the pump device 5 based on the temperature data from.

【0015】上記した構成における作用を説明する。投
入口2を通じて酸発酵槽1の内部に有機性汚泥8を投入
し、水中ポンプ装置5により循環管4を通じて槽内外に
わたって連続的に循環させる。
The operation of the above configuration will be described. Organic sludge 8 is charged into the acid fermentation tank 1 through the inlet 2, and is continuously circulated through the circulation pipe 4 by the submersible pump device 5 inside and outside the tank.

【0016】そしてこれにより、有機性汚泥8を、水中
ポンプ装置5のインペラによって剪断しつつ攪拌混合
し、それに伴って特にインペラの部分に発生する摩擦熱
によって昇温させる。
Thus, the organic sludge 8 is agitated and mixed while being sheared by the impeller of the submersible pump device 5, and the temperature is increased by frictional heat generated particularly in the impeller.

【0017】その際、有機性汚泥8の温度を熱電対6に
よって連続的あるいは間欠的に測定し、熱電対6より送
信される温度データに基いて、インバータ制御装置7に
よって、有機性汚泥8が所定の温度範囲内に保持される
ように水中ポンプ装置5の回転数を制御する。
At this time, the temperature of the organic sludge 8 is continuously or intermittently measured by the thermocouple 6, and based on the temperature data transmitted from the thermocouple 6, the organic sludge 8 is The rotation speed of the submersible pump device 5 is controlled so as to be maintained within a predetermined temperature range.

【0018】運転を続ける間に、有機性汚泥8が次第に
可溶化され、酸発酵してくるので、適当な時点で排出口
3より取り出して、嫌気性発酵槽へ送る。上記したよう
にして、し尿汚泥を50℃で24時間可溶化処理した後
に嫌気性発酵(15日間)させたところ、有機物分解率
は50%以上となった。これに対して、同じし尿汚泥を
可溶化処理をしなかった場合には有機物分解率は約40
%となり、発酵効率に明らかな差違が認められた。
While the operation is continued, the organic sludge 8 is gradually solubilized and undergoes acid fermentation. Therefore, the sludge is taken out from the discharge port 3 at an appropriate time and sent to the anaerobic fermenter. As described above, the sewage sludge was solubilized at 50 ° C. for 24 hours and then anaerobic fermented (15 days). As a result, the organic matter decomposition rate became 50% or more. On the other hand, when the same sludge was not solubilized, the organic matter decomposition rate was about 40%.
%, Indicating a clear difference in the fermentation efficiency.

【0019】なお、可溶化のため処理条件は処理対象の
有機性汚泥の性状に応じて適宜決めればよいが、たとえ
ば70℃で3時間、50℃で12時間、50℃で24時
間程度、槽内滞留させる。酸化分解しにくいし尿汚泥等
のみを可溶化処理し、比較的酸化分解しやすい厨芥等と
混合して発酵させるようにしてもよい。
The treatment conditions for solubilization may be appropriately determined according to the properties of the organic sludge to be treated. For example, 70 ° C. for 3 hours, 50 ° C. for 12 hours, 50 ° C. for about 24 hours, tank To stay inside. It is also possible to solubilize only urine sludge which is hardly oxidatively decomposed, mix with garbage which is relatively easily oxidatively decomposed, and ferment.

【0020】なお、羽根式攪拌手段は、汚泥性状ならび
に投入量に見合った比較的容量の大きなものであればよ
く、上記したように水中ポンプ装置を使用するのが可溶
化効率が高いが、図2に示したように槽外ポンプ装置9
を使用してもよく、破砕機能を持ったカッターポンプな
どを選定してもよい。また、図3に示したような槽内設
置型の羽根式攪拌装置10によっても同様の効果が得ら
れる。
The blade-type stirring means may be of a relatively large capacity corresponding to the properties of sludge and the amount of sludge. The use of a submersible pump as described above has a high solubilization efficiency. As shown in FIG.
May be used, or a cutter pump having a crushing function may be selected. A similar effect can be obtained by the blade-type stirring device 10 installed in the tank as shown in FIG.

【0021】上記においては、嫌気性発酵に先立って可
溶化処理を行うものとして説明したが、このような可溶
化処理方法を好気性発酵の前段で行っても当然ながら発
酵効率は向上する。
In the above description, the solubilization treatment is performed prior to the anaerobic fermentation. However, even if such a solubilization treatment method is performed before the aerobic fermentation, the fermentation efficiency is naturally improved.

【0022】[0022]

【発明の効果】以上のように本発明によれば、羽根式攪
拌手段という単一の手段によって、有機性汚泥を十分に
攪拌混合しながら剪断および加熱することができ、容易
にかつ均質に効率よく可溶化処理を行えるとともに、後
段への影響も少なく、設備費も従来より低減できる。
As described above, according to the present invention, the organic sludge can be sheared and heated with sufficient stirring and mixing by a single means of the blade type stirring means, and the efficiency can be easily and uniformly increased. The solubilization treatment can be performed well, the influence on the subsequent stage is small, and the equipment cost can be reduced as compared with the conventional case.

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

【図1】本発明の第1実施形態における有機性汚泥の可
溶化処理方法が行なわれる処理槽の概略構成を示した断
面図である。
FIG. 1 is a cross-sectional view showing a schematic configuration of a treatment tank in which a method for solubilizing organic sludge according to a first embodiment of the present invention is performed.

【図2】本発明の第2実施形態における有機性汚泥の可
溶化処理方法が行なわれる処理槽の概略構成を示した断
面図である。
FIG. 2 is a sectional view showing a schematic configuration of a treatment tank in which a method for solubilizing organic sludge according to a second embodiment of the present invention is performed.

【図3】本発明の第3実施形態における有機性汚泥の可
溶化処理方法が行なわれる処理槽の概略構成を示した断
面図である。
FIG. 3 is a cross-sectional view illustrating a schematic configuration of a treatment tank in which a method for solubilizing organic sludge according to a third embodiment of the present invention is performed.

【符号の説明】[Explanation of symbols]

1 処理槽 4 循環管 5 水中ポンプ装置 8 有機性汚泥 9 ポンプ装置 10 羽根式攪拌装置 DESCRIPTION OF SYMBOLS 1 Processing tank 4 Circulation pipe 5 Submersible pump device 8 Organic sludge 9 Pump device 10 Blade type stirring device

フロントページの続き (72)発明者 柴田 敏行 大阪府大阪市浪速区敷津東一丁目2番47号 株式会社クボタ内Continuation of front page (72) Inventor Toshiyuki Shibata 2-47 Shishitsu Higashi 1-chome, Naniwa-ku, Osaka-shi, Osaka Kubota Corporation

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 発酵に先立って行う有機性汚泥の可溶化
処理方法であって、処理槽の内部に導入した有機性汚泥
を羽根式攪拌手段によって攪拌し、攪拌に伴って発生す
る摩擦熱で昇温させることにより可溶化させることを特
徴とする有機性汚泥の可溶化処理方法。
1. A method for solubilizing organic sludge carried out prior to fermentation, wherein organic sludge introduced into a treatment tank is stirred by a blade type stirring means, and friction heat generated by the stirring is used. A method for solubilizing organic sludge, wherein the method is solubilized by raising the temperature.
【請求項2】 羽根式攪拌手段は、処理槽の内部と槽外
の循環流路とにわたって有機性汚泥を循環させる循環ポ
ンプ装置であることを特徴とする請求項1記載の有機性
汚泥の可溶化処理方法。
2. The organic sludge according to claim 1, wherein the blade type stirring means is a circulation pump device for circulating the organic sludge through the inside of the treatment tank and the circulation passage outside the tank. Solubilization method.
JP10022432A 1998-02-04 1998-02-04 Solubilizing treatment of organic sludge Pending JPH11216500A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10022432A JPH11216500A (en) 1998-02-04 1998-02-04 Solubilizing treatment of organic sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10022432A JPH11216500A (en) 1998-02-04 1998-02-04 Solubilizing treatment of organic sludge

Publications (1)

Publication Number Publication Date
JPH11216500A true JPH11216500A (en) 1999-08-10

Family

ID=12082544

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10022432A Pending JPH11216500A (en) 1998-02-04 1998-02-04 Solubilizing treatment of organic sludge

Country Status (1)

Country Link
JP (1) JPH11216500A (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001238818A (en) * 2000-02-28 2001-09-04 Hiroshi Fujita Discharging system of toilet
JP2003305491A (en) * 2002-04-18 2003-10-28 Purio:Kk Method for boiling treatment of sewage
JP2007130619A (en) * 2005-11-10 2007-05-31 Shinyo Sangyo Kk Underwater decomposing/extinguishing treatment machine for bio-water flow stirring organic waste by autogeneous crushing pump requiring no vent hole
JP2008246461A (en) * 2007-03-30 2008-10-16 Mhi Environment Engineering Co Ltd Apparatus for pretreatment or post-treatment of methane fermentation, post-treatment system for methane fermentation, and method thereof
JP2008246462A (en) * 2007-03-30 2008-10-16 Mhi Environment Engineering Co Ltd Pretreatment apparatus for methane fermentation and methane fermentation treatment system using it
JP2014161828A (en) * 2013-02-27 2014-09-08 Hazama Ando Corp Cleaning method and cleaning system of contaminated soil

Cited By (7)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2001238818A (en) * 2000-02-28 2001-09-04 Hiroshi Fujita Discharging system of toilet
JP2003305491A (en) * 2002-04-18 2003-10-28 Purio:Kk Method for boiling treatment of sewage
JP2007130619A (en) * 2005-11-10 2007-05-31 Shinyo Sangyo Kk Underwater decomposing/extinguishing treatment machine for bio-water flow stirring organic waste by autogeneous crushing pump requiring no vent hole
JP4638336B2 (en) * 2005-11-10 2011-02-23 伸洋産業株式会社 Organic waste water treatment equipment
JP2008246461A (en) * 2007-03-30 2008-10-16 Mhi Environment Engineering Co Ltd Apparatus for pretreatment or post-treatment of methane fermentation, post-treatment system for methane fermentation, and method thereof
JP2008246462A (en) * 2007-03-30 2008-10-16 Mhi Environment Engineering Co Ltd Pretreatment apparatus for methane fermentation and methane fermentation treatment system using it
JP2014161828A (en) * 2013-02-27 2014-09-08 Hazama Ando Corp Cleaning method and cleaning system of contaminated soil

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