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JPS6136472B2 - - Google Patents
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JPS6136472B2 - - Google Patents

Info

Publication number
JPS6136472B2
JPS6136472B2 JP56192655A JP19265581A JPS6136472B2 JP S6136472 B2 JPS6136472 B2 JP S6136472B2 JP 56192655 A JP56192655 A JP 56192655A JP 19265581 A JP19265581 A JP 19265581A JP S6136472 B2 JPS6136472 B2 JP S6136472B2
Authority
JP
Japan
Prior art keywords
coal
microorganisms
implanted
parts
producing
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
Application number
JP56192655A
Other languages
Japanese (ja)
Other versions
JPS57140698A (en
Inventor
Hisashi Suzuki
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.)
Iseki Agricultural Machinery Mfg Co Ltd
Original Assignee
Iseki Agricultural Machinery Mfg Co Ltd
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 Iseki Agricultural Machinery Mfg Co Ltd filed Critical Iseki Agricultural Machinery Mfg Co Ltd
Priority to JP56192655A priority Critical patent/JPS57140698A/en
Publication of JPS57140698A publication Critical patent/JPS57140698A/en
Publication of JPS6136472B2 publication Critical patent/JPS6136472B2/ja
Granted 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
    • Y02W10/10Biological treatment of water, waste water, or sewage

Landscapes

  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)
  • Biological Treatment Of Waste Water (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、微生物の着床した石炭の製造方法、
特に、活性汚泥法に用いた場合、従来の活性汚泥
法では直接処理は不可能視されていた高濃度
BODの廃水の直接処理を容易に可能にする、微
生物の着床した石炭の製造方法に関する。 活性汚泥法は、多量の有機物を含むBOD濃度
の高い廃水の処理に適した廃水処理法であるとさ
れているが、従来の活性汚泥法では、分解効率及
び分解対象物に限界があり、BOD除去率95%、
BOD負荷1Kg/m2D程度の処理能力しか無かつ
た。従つて、3000ppm以上の高濃度BODの廃水
を直接処理することは不可能であるため、高濃度
BODの廃水を従来の活性汚泥法により処理しよ
うとする場合には、一旦廃水を水で稀釈して
BOD濃度を低下させる必要があり、それ丈余分
な処理費を要していた。 また、従来の活性汚泥法においては、原生動物
を主とする微生物が用いられ、これらの微生物を
含む種汚泥としては、通常、曝気槽内で自然に発
生したものを用いるか、又は他所の活性汚泥法の
系から採取したものを運んで来て用いており、含
水率60%以下で生菌を含む種汚泥の生産はなされ
ていない。尚、含水率10〜30%のパウダー状の種
汚泥も生産されてはいるが、これは菌を仮死状態
としたもので、この種汚泥は、取り扱い易い利点
はあるが、活性汚泥法の種汚泥として用いても、
その処理能力は前述の従来の活性汚泥法に比して
決して向上するものではない。 本発明は、従来の活性汚泥法では、直接処理は
不可能視されていた高濃度BODの廃水の直接処
理を容易に可能にする種汚泥である、微生物の着
床した石炭の製造方法を提供するもので、特定の
石炭に特定の手段によりアルコール醗酵菌を含む
微生物群を着床させるものである。 即ち、本発明の微生物の着床した石炭の製造方
法は、石炭(但し泥炭又は炭素含有率が84%以上
の瀝青炭及び無煙炭を除く)と、米糖、油粕等の
蛋白質を多量に含み且つリン、カリを含む栄養源
と、水とを、含水率が40〜60%となるように配合
し、この配合物を醗酵させてアルコール醗酵菌を
含む微生物群を上記石炭に着床させることを特徴
とするものである。 上記特徴を以てなる本発明の製造方法について
詳述すると、本発明に用いられる石炭としては、
泥炭では強度が弱く、また、炭素含有率84%以上
の瀝青炭及び無煙炭では微生物が着床し難いた
め、これらの石炭粒は用いられず、カツ炭、亜炭
が用いられる。また、粒径が20mmを超えたもの
は、通常、そのままでは曝気槽内での流動に適さ
ず、また微生物が短期日で着床し難いので、粒径
20mm以下のものを用いるのが便利である。本発明
の方法により得られる微生物の着床した石炭は、
特に、一定の粒度分布を付与されて使用されるこ
とによつて顕著な効果を発揮するものであるか
ら、使用する石炭としては、0.2mm〜20mmの範囲
において粒度分布を有するものを用いるのが好ま
しく、特に粒度分布が正規分布を有するもの、例
えば、粒径2mm〜10mmの範囲で正規分布を持つ石
炭が好ましい。 また、栄養源としては、蛋白質を多量に含み且
つリン、カリを含むもの、例えば、米糖、麦糖、
油粕が用いられる。用いる種菌としては、アルコ
ール醗酵菌を含む微生物群であれば良く、このよ
うな種菌は、通常、種々の栄養源、例えば、米
糖、麦糖の中に自然に含まれているから、本発明
の実施に際しては、そのような栄養源を用いれば
特に種菌を配合する必要は無い。 而して、本発明を実施するには、上記の石炭と
上記の栄養源とを配合し、好ましくは前者100重
量部に対して後者10〜80重量部を配合し、その
際、栄養源がアルコール醗酵菌を含んでいない場
合には、アルコール醗酵菌を含む種菌を配合し、
これに配合物の含水率が40〜60%となるように水
を加え、この配合物をアルコール醗酵菌の醗酵に
適した条件下に保持する。即ち、通常、上記配合
物の中心温度が50゜±2℃を維持するようにし、
且つ含水率が40%以下にならないように水を補給
し乍ら、7〜10日間醗酵を継続させ、醗酵を終了
させる。醗酵の終了時点は、外観上白色カビが石
炭粒の内部に侵入し、石炭粒子の破壊を開始する
時点とする。 尚、上述の醗酵方法は、野天において自然醗酵
による方法によつても良く、また、工場で、所定
の配合物をロータリーキルン等を用い7〜10日間
常留により連続的に行なうこともできる。 上述の如くして得た、微生物を着床させた石炭
は、石炭として予め所定の粒度分布を有するもの
を用いた場合には、そのまま活性汚泥法の種汚泥
として用いることができ、また、所望の粒度分布
を有していないものは、粉砕、ふるい分け等によ
り所望の粒度分布に調整して用いれば良い。 以下に本発明の実施例、及び本発明に係る、微
生物の着床した石炭を用いた使用例を参考例と共
に示し、本発明に係る石炭の種汚泥としての効果
を具体的に説明する。実施例 0.2mm〜10mmの範囲に亘つて略均一な粒度分布
を有する亜炭3Kg、米糖1Kg及び水1.5Kgからな
る配合物を、容器内に0.8Kg/となるように常温
(20〜35℃)下に充填する。24時間後に醗酵が始
まり、水分の蒸発が盛んになるため、毎日スプレ
ーで表面に散水し、中心部の温度が50±2℃を維
持するように毎日撹拌し、醗酵開始後7日間で醗
酵を終了させ、目的とする、微生物の着床した石
炭を得た。尚、醗酵終了時点は、外観上白色カビ
が石炭粒の内部に侵入し、粒子の破壊を開始した
時点とした。 使用例 BOD3000ppmの味噌醸造廃水、及び
BOD9000ppmの水産加工廃水を、それぞれ下記
第1及び第2表に記載の条件下に処理し、それぞ
れ第1及び第2表に示す処理水となした。 尚、参考例は従来の活性汚泥法によつた場合を
示す。
The present invention provides a method for producing coal with microorganisms attached thereto;
In particular, when used in the activated sludge method, it is possible to treat high concentrations that were considered impossible to directly treat with conventional activated sludge methods.
This invention relates to a method for producing coal with microorganisms that facilitates direct treatment of BOD wastewater. The activated sludge method is said to be a wastewater treatment method suitable for treating wastewater with a high BOD concentration that contains a large amount of organic matter. However, the conventional activated sludge method has limitations in decomposition efficiency and substances to be decomposed. Removal rate 95%,
The processing capacity was only about 1Kg/m 2 D of BOD load. Therefore, it is impossible to directly treat wastewater with a high BOD concentration of 3000 ppm or more.
When attempting to treat BOD wastewater using the conventional activated sludge method, the wastewater must first be diluted with water.
It was necessary to reduce the BOD concentration, which required extra processing costs. In addition, in the conventional activated sludge method, microorganisms, mainly protozoa, are used, and the seed sludge containing these microorganisms is usually one that is naturally generated in the aeration tank, or activated sludge from elsewhere. The sludge collected from the sludge method system is brought in and used, and seed sludge containing viable bacteria with a moisture content of less than 60% is not produced. Powdered seed sludge with a water content of 10 to 30% is also produced, but this is made by keeping bacteria in a state of suspended animation, and although this type of sludge has the advantage of being easy to handle, it is not suitable for the activated sludge method. Even when used as sludge,
Its treatment capacity is by no means improved compared to the conventional activated sludge method described above. The present invention provides a method for producing coal on which microorganisms have settled, which is a seed sludge that easily enables direct treatment of high-concentration BOD wastewater, which was considered impossible to directly treat using conventional activated sludge methods. This involves implanting a group of microorganisms, including alcohol-fermenting bacteria, onto specific coal using specific means. That is, the method for producing coal on which microorganisms have been implanted according to the present invention involves using coal (excluding peat or bituminous coal with a carbon content of 84% or more and anthracite), a large amount of protein such as rice sugar and oil cake, and a phosphorus-rich coal. , a nutrient source containing potash and water are blended so that the moisture content is 40 to 60%, and this blend is fermented to implant microorganisms including alcohol-fermenting bacteria on the coal. That is. To explain in detail the manufacturing method of the present invention having the above-mentioned characteristics, the coal used in the present invention includes:
Peat has low strength, and bituminous coal and anthracite coal with a carbon content of 84% or more are difficult for microorganisms to settle on, so these coal grains are not used, and cutlet coal and lignite are used. In addition, particles with a diameter exceeding 20 mm are usually not suitable for flowing in the aeration tank as they are, and microorganisms are difficult to settle in a short period of time.
It is convenient to use one with a diameter of 20 mm or less. The microorganism-attached coal obtained by the method of the present invention is
In particular, it is effective when used with a certain particle size distribution, so it is recommended that the coal used has a particle size distribution in the range of 0.2 mm to 20 mm. Particularly preferred is coal having a normal particle size distribution, for example, coal having a normal distribution in the particle size range of 2 mm to 10 mm. In addition, nutritional sources include foods that contain a large amount of protein and also phosphorus and potassium, such as rice sugar, barley sugar,
Oil cake is used. The inoculum to be used may be any microorganism group including alcohol-fermenting bacteria, and such inoculum is usually naturally contained in various nutritional sources, such as rice sugar and malt sugar. When carrying out this method, if such a nutrient source is used, there is no need to particularly incorporate a seed culture. Therefore, in carrying out the present invention, the above-mentioned coal and the above-mentioned nutrient source are blended, preferably 10 to 80 parts by weight of the latter to 100 parts by weight of the former, and at this time, the nutrient source is If it does not contain alcohol-fermenting bacteria, add a starter that contains alcohol-fermenting bacteria,
Water is added to this so that the moisture content of the blend is 40-60%, and the blend is maintained under conditions suitable for fermentation by alcohol-fermenting bacteria. That is, the center temperature of the above formulation is usually maintained at 50° ± 2°C;
Fermentation is continued for 7 to 10 days while replenishing water so that the water content does not fall below 40%, and the fermentation is completed. The end of fermentation is the point at which the apparently white mold invades the inside of the coal particles and begins to destroy the coal particles. The above-mentioned fermentation method may be carried out by natural fermentation in the open air, or may be carried out continuously in a factory by leaving a predetermined compound in a rotary kiln for 7 to 10 days. The microorganism-implanted coal obtained as described above can be used as it is as a seed sludge in the activated sludge method if coal having a predetermined particle size distribution is used, and it can also be used as a seed sludge in the activated sludge method. Those that do not have a particle size distribution may be used after being adjusted to a desired particle size distribution by pulverization, sieving, etc. Examples of the present invention and usage examples using coal on which microorganisms have settled according to the present invention will be shown below together with reference examples, and the effects of the coal according to the present invention as a seed sludge will be specifically explained. Example A mixture consisting of 3 kg of lignite having a substantially uniform particle size distribution in the range of 0.2 mm to 10 mm, 1 kg of rice sugar, and 1.5 kg of water was placed in a container at room temperature (20 to 35°C) to a concentration of 0.8 kg. ) Fill the bottom. Fermentation begins after 24 hours and water evaporates rapidly, so water is sprayed on the surface every day and stirred daily to maintain the temperature at the center of 50±2℃. The process was completed, and the desired coal with microorganisms implanted thereon was obtained. The end of the fermentation was defined as the time when the apparently white mold entered the inside of the coal grains and started destroying the grains. Example of use Miso brewing wastewater with BOD3000ppm,
Fishery processing wastewater with a BOD of 9000 ppm was treated under the conditions listed in Tables 1 and 2 below to obtain the treated water shown in Tables 1 and 2, respectively. Note that the reference example shows a case using the conventional activated sludge method.

【表】【table】

【表】【table】

【表】 叙上の如く、本発明の方法により得られる、微
生物の着床した石炭に着床させた微生物群は、種
汚泥として活性汚泥法に用いれば、従来法では直
接処理の不可能であつた高濃度BOD廃水の直接
処理を可能にし、しかも余剰汚泥の発生を少なく
抑え、BOD負荷を高負荷で以て処理できるた
め、従来法に比して時間当り大量の廃水を効果的
に処理でき、廃水処理のランニングコストを大巾
に低減できるものであり、また、製品は含水率40
%程度の固体であるため、運搬、維持管理が簡便
である等の効果を奏するものであり、原料が安価
であり且つ製造も比較的容易である等の効果と相
俟ち、本発明の廃水処理分野に寄与する処は極め
て大きい。
[Table] As mentioned above, if the microorganisms obtained by the method of the present invention and which have settled on coal with microorganisms are used as seed sludge in the activated sludge method, they cannot be directly treated by conventional methods. It enables direct treatment of hot, high-concentration BOD wastewater, suppresses the generation of excess sludge, and can treat a high BOD load, effectively treating a large amount of wastewater per hour compared to conventional methods. The running cost of wastewater treatment can be greatly reduced, and the product has a moisture content of 40%.
% of solids, it has the advantage of being easy to transport and maintain, and the raw materials are inexpensive and manufacturing is relatively easy. Its contribution to the field of processing is extremely large.

Claims (1)

【特許請求の範囲】 1 石炭(但し泥炭又は炭素含有率が84%以上の
瀝青炭及び無煙炭を除く)と、米糖、油粕等の蛋
白質を多量に含み且つリン、カリを含む栄養源
と、水とを、含水率が40〜60%となるように配合
し、この配合物を醗酵させてアルコール醗酵菌を
含む微生物群を上記石炭に差床させる、微生物の
着床した石炭の製造方法。 2 上記栄養源がアルコール醗酵菌を含む微生物
群を保有している、特許請求の範囲第1項記載の
微生物の着床した石炭の製造方法。 3 醗酵中に水分を補給する特許請求の範囲第1
項記載の微生物の着床した石炭の製造方法。 4 上記石炭100重量部に対し、上記栄養源10〜
80重量部を配合する、特許請求の範囲第1項記載
の微生物の着床した石炭の製造方法。
[Scope of Claims] 1. Coal (excluding peat or bituminous coal with a carbon content of 84% or more and anthracite), a nutrient source containing a large amount of protein such as rice sugar and oil cake, and containing phosphorus and potassium, and water. A method for producing coal on which microorganisms have been implanted, which comprises blending the above ingredients so that the moisture content is 40 to 60%, and fermenting this mixture to inject microorganisms containing alcohol-fermenting bacteria into the coal. 2. The method for producing coal implanted with microorganisms according to claim 1, wherein the nutrient source contains a group of microorganisms including alcohol-fermenting bacteria. 3. Claim 1 of supplying water during fermentation
A method for producing coal on which microorganisms have been implanted as described in 2. 4 For 100 parts by weight of the above coal, 10 to 10 parts of the above nutrients
A method for producing coal on which microorganisms have been implanted according to claim 1, which comprises blending 80 parts by weight.
JP56192655A 1981-11-30 1981-11-30 Preparation of bacteria-embedded coal Granted JPS57140698A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP56192655A JPS57140698A (en) 1981-11-30 1981-11-30 Preparation of bacteria-embedded coal

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP56192655A JPS57140698A (en) 1981-11-30 1981-11-30 Preparation of bacteria-embedded coal

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP52091647A Division JPS586556B2 (en) 1977-07-30 1977-07-30 Structure of aeration tank in wastewater treatment method and treatment equipment

Publications (2)

Publication Number Publication Date
JPS57140698A JPS57140698A (en) 1982-08-31
JPS6136472B2 true JPS6136472B2 (en) 1986-08-19

Family

ID=16294844

Family Applications (1)

Application Number Title Priority Date Filing Date
JP56192655A Granted JPS57140698A (en) 1981-11-30 1981-11-30 Preparation of bacteria-embedded coal

Country Status (1)

Country Link
JP (1) JPS57140698A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01107815U (en) * 1988-01-14 1989-07-20

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
IT1173711B (en) * 1982-05-13 1987-06-24 Nippon Steele Corp PROCEDURE FOR TREATING WASTE WATER FROM INDUSTRIAL PLANTS WITH ACTIVE MUD
DE69425361T2 (en) * 1993-06-16 2000-12-28 Toyo Denka Kogyo Co. Ltd., Kochi METHOD AND DEVICE FOR TREATING WATER
WO1994029224A1 (en) * 1993-06-16 1994-12-22 Toyo Denka Kogyo Co., Ltd. Water treatment method and water treatment apparatus
CN100370041C (en) * 2006-06-07 2008-02-20 南京大学 A method for removing sulfur from pyrite in coal gangue by using microorganisms
CN110002609B (en) * 2019-04-18 2021-07-16 山东省食品药品检验研究院 A kind of microbial water quality improver and preparation method thereof

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01107815U (en) * 1988-01-14 1989-07-20

Also Published As

Publication number Publication date
JPS57140698A (en) 1982-08-31

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