JPH05296A - Purification of waste water - Google Patents

Purification of waste water

Info

Publication number
JPH05296A
JPH05296A JP3308490A JP30849091A JPH05296A JP H05296 A JPH05296 A JP H05296A JP 3308490 A JP3308490 A JP 3308490A JP 30849091 A JP30849091 A JP 30849091A JP H05296 A JPH05296 A JP H05296A
Authority
JP
Japan
Prior art keywords
waste water
wastewater
purifying material
tank
adsorbed
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
Application number
JP3308490A
Other languages
Japanese (ja)
Other versions
JPH0775709B2 (en
Inventor
Takeshi Senba
武 千羽
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.)
KOYO KOGYO YUGEN
MOTOMITSU SEISAKUSHO KK
Toppan Cosmo Inc
Toppan Inc
Original Assignee
KOYO KOGYO YUGEN
MOTOMITSU SEISAKUSHO KK
Toppan Printing Co Ltd
Toppan Shoji 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 KOYO KOGYO YUGEN, MOTOMITSU SEISAKUSHO KK, Toppan Printing Co Ltd, Toppan Shoji Co Ltd filed Critical KOYO KOGYO YUGEN
Priority to JP30849091A priority Critical patent/JPH0775709B2/en
Publication of JPH05296A publication Critical patent/JPH05296A/en
Publication of JPH0775709B2 publication Critical patent/JPH0775709B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime 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

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

Abstract

PURPOSE:To keep excellent purifying action over a long period of time by transmitting waste water through a waste water purifying material formed by transferring aerobic bacteria to porous high briquette char made by washing low-grade coal with on acid in a definite flow rate and subjecting the adsorbed suspended substance in waste water to digestive decomposition. CONSTITUTION:Waste water from which oils and fats are removed is sent to aeration tanks 5A... and the suspended substance other than oils and fats in waste water is removed. A waste water purifying material 5a prepared by transferring aerobic bacteria to porous high briquetted char prepared by immersing low-grade coal in sulfuric acid for 24hr as a raw material is arranged to the aeration tank 5A. When the waste water introduced from an injection port 52 is transmitted through the waste water purifying material 5a from below upward in an almost definite flow rate, the suspended substance in the waste water is adsorbed by the numberless pores of the waste water purifying material 5a and successively subjected to digestive decomposition by aerobic bacteria. Therefore, the purifying material can be used over a long period of time without generating clogging.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、生活雑廃水や畜産廃水
等を浄化する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 method for purifying household wastewater, livestock wastewater and the like.

【0002】[0002]

【従来の技術】従来、この種の廃水を浄化する廃水浄化
法としては薬品中和法、曝気法、吸着法等が知られてい
る。
2. Description of the Related Art Conventionally, as a wastewater purification method for purifying this type of wastewater, a chemical neutralization method, an aeration method, an adsorption method and the like have been known.

【0003】薬品中和法は日々薬品を使用することから
ランニングコストが高くつくほか、汚泥の量が増加する
ので廃棄処理費用が嵩むと云う問題点がある。曝気処理
法は、廃水中に強制的に多量の空気を供給することによ
り、廃水中に浮遊または溶解した汚濁物質をガス化させ
たり、微生物による分解を促進したり、また、これによ
って生じた汚泥を除去するものであるが、反応が遅いた
めに曝気処理のスペースを広く取る必要がある。
The chemical neutralization method has a problem that the running cost is high because a chemical is used every day, and the waste disposal cost is increased because the amount of sludge is increased. The aeration treatment method is to supply a large amount of air forcibly into the wastewater to gasify the pollutants suspended or dissolved in the wastewater, to accelerate the decomposition by microorganisms, and to generate sludge generated by this. However, since the reaction is slow, it is necessary to take a large space for aeration treatment.

【0004】活性炭によって廃水中の汚濁物質を吸着除
去する方法は、活性炭の微小な孔が高い吸着能を持って
いるため、有効な方法のひとつであるが、微小孔が吸着
された汚濁物質で目詰まり状態になると、吸着しなくな
るので全量交換しなければならない。周知のように活性
炭は可なり高価であるため、度々交換することはコスト
的にも採算が合わないだけでなく、交換時には廃水が処
理出来ないと云う問題点もある。
[0004] The method of adsorbing and removing pollutants in wastewater with activated carbon is one of the effective methods because the minute pores of activated carbon have a high adsorption capacity. If it becomes clogged, it will not be adsorbed and must be replaced. As is well known, since activated carbon is quite expensive, it is not profitable to replace it frequently, and there is also a problem that waste water cannot be treated at the time of replacement.

【0005】高価な活性炭と同一の効果を安いコストで
得ることが出来る技術が、特公昭55−22409号公
報に提案されている。すなわち、低品位石炭を原料と
し、これを酸洗いすることにより多孔質化すれば、活性
炭と同様にその微小孔に廃水中の汚濁物質が吸着される
ので、廃水が浄化されることが開示されている。特に、
多孔質化した活性化石炭を160〜200メッシュの微
粉末とすることにより、水面にしばらくは浮遊させるこ
とが出来るので、水面に浮遊した原油を除去することの
出来る有効な技術であると報告されている。
A technique capable of obtaining the same effect as expensive activated carbon at a low cost is proposed in Japanese Patent Publication No. 55-22409. That is, if low-grade coal is used as a raw material and is made porous by pickling it, contaminants in the wastewater are adsorbed in the micropores of the activated carbon, so that the wastewater is disclosed to be purified. ing. In particular,
By making porous activated coal into fine powder of 160-200 mesh, it can be suspended on the water surface for a while, and it is reported that this is an effective technique that can remove crude oil floating on the water surface. ing.

【0006】[0006]

【発明が解決しようとする課題】上記したように、活性
炭および特公昭55−22409号公報に提案されてい
る活性化石炭は、廃水中に設置した当初はその微小孔に
良く汚濁物質を吸着し、廃水を浄化する効果が大きい。
しかし、無数の微小孔も時間の経過と共に廃水中の汚濁
物質を吸着堆積すると、遂には全く浄化作用を失うと云
う欠点がある。本発明は吸着能に優れた無数の微小孔を
有する多孔質物質を使用し、設置した当初の優れた浄化
作用を長期間に渡って維持することの出来る廃水の浄化
処理法を提供しようとするものである。
As described above, the activated carbon and the activated coal proposed in Japanese Patent Publication No. 55-22409 have good adsorption of pollutants into the fine pores of the activated carbon when initially installed in wastewater. The effect of purifying wastewater is great.
However, even a myriad of micropores have the drawback that, when adsorbed and deposited pollutants in wastewater over time, they eventually lose their purification action. The present invention intends to provide a wastewater purification treatment method which uses a porous substance having innumerable micropores excellent in adsorption ability and can maintain the excellent purification action at the time of initial installation for a long period of time. It is a thing.

【0007】[0007]

【課題を解決するための手段】本発明は上記した従来技
術の課題を解決するためになされたもので、低品位石炭
を酸洗などにより多孔質化したハイブリケットチャーに
好気性微生物を移乗させて形成される廃水浄化材に、廃
水を一定の流量で透過させ、前記廃水浄化材に吸着され
た汚濁物質を前記好気性微生物によって消化分解するこ
とを特徴とする廃水浄化法である。
The present invention has been made in order to solve the above-mentioned problems of the prior art, in which aerobic microorganisms are transferred to a hybridet char in which low-grade coal is made porous by pickling or the like. The wastewater purifying method is characterized in that the wastewater purifying material formed by permeating the wastewater at a constant flow rate and digesting and decomposing the pollutants adsorbed to the wastewater purifying material by the aerobic microorganisms.

【0008】[0008]

【作用】好気性微生物が移乗しているハイブリケットチ
ャーは、低品位石炭から造られているので保温作用があ
り(野積みした石炭が自然発火することがあることから
自明)、冬季においても特別な寒冷地を除き、微生物が
活動するに充分な温度が確保される。このため、ハイブ
リケットチャーに移乗した好気性微生物は冬期でも死滅
することがない。また、ハイブリケットチャーには木質
部が多量に残存しているので、年末年始などのように廃
水処理を休止し、廃水が供給されなくなることがあって
も好気性微生物はハイブリケットチャーの木質部を食べ
て生き延びることができる。
[Function] The hybridet char carrying aerobic microorganisms has a heat-retaining effect because it is made from low-grade coal (it is obvious that coal loaded in the field may spontaneously ignite), and it is especially useful in winter. Sufficient temperature is secured for microbial activity, except in cold regions. Therefore, the aerobic microorganisms transferred to the hybridette char do not die even in winter. In addition, since a large amount of wood remains in the hybridet char, aerobic microorganisms eat the wood part of the hybrid char even if the waste water treatment may be interrupted due to suspension of waste water treatment such as during the year-end and New Year holidays. Can survive.

【0009】汚濁物質が浮遊または溶解しいる生活雑廃
水などの一般廃水が、好気性微生物が移乗している上記
廃水浄化材に略一定の流量で透過されると、廃水が廃水
浄化材を透過するとき、汚濁物質は廃水浄化材の無数の
微小孔によって吸着除去され、微小孔に吸着された汚濁
物質は前記好気性微生物によって次々と消化分解される
ので、廃水浄化材の微小孔は長期間使用しても目詰まり
することがない。
When general wastewater such as household wastewater in which pollutants are suspended or dissolved is permeated to the above-mentioned wastewater purification material carrying aerobic microorganisms at a substantially constant flow rate, the wastewater permeates the wastewater purification material. At this time, the pollutants are adsorbed and removed by the innumerable micropores of the wastewater purification material, and the pollutants adsorbed in the micropores are successively digested and decomposed by the aerobic microorganisms, so that the micropores of the wastewater purification material are long-term. No clogging even when used.

【0010】[0010]

【実施例】つぎに本発明を図示の一実施例に基づいて詳
細に説明する。廃水(この場合厨房廃水)は一旦原水ピ
ット1に蓄えられ、ポンプ等の手段によって流量調整槽
2に送られる。流量調整槽2の導入部にはステンレス製
のスクリーン2aが設けられていて、廃水中の比較的大
きいゴミ等の固形物が分離除去される。
DESCRIPTION OF THE PREFERRED EMBODIMENTS The present invention will be described in detail below with reference to an embodiment shown in the drawings. Waste water (in this case, kitchen waste water) is temporarily stored in the raw water pit 1 and sent to the flow rate adjusting tank 2 by means of a pump or the like. A screen 2a made of stainless steel is provided at the introduction part of the flow rate adjusting tank 2 to separate and remove solid matters such as relatively large dust in the wastewater.

【0011】本発明の廃水浄化法は、微生物によって廃
水中の汚濁物質を消化分解する方法であるので、微生物
の分解能力を考慮して常に略一定量の廃水が流入するこ
とが望ましい。したがって、流量調整槽2からは毎時
6.25m3 (日量換算150m3 )の廃水が水質調整
槽3に送られるようになっている。
Since the wastewater purification method of the present invention is a method of digesting and decomposing pollutants in wastewater by microorganisms, it is desirable that a substantially constant amount of wastewater always flows in considering the decomposing ability of microorganisms. Therefore, from the flow rate adjustment tank 2, 6.25 m 3 (150 m 3 of daily conversion) of waste water is sent to the water quality adjustment tank 3 every hour.

【0012】原水ピツト1に一時的に多量の廃水が流れ
込み、このため流量調整槽2にも多量の廃水が送り込ま
れてオーバーフローするような時にはクッションタンク
2Aを設け、一旦原水ピツト1に戻すのが良い。このよ
うなクッションタンク2Aの設置により、一時的な廃水
の増減だけでなく昼夜に渡る変動、あるいは季節的な変
動に対応することが容易になる。
When a large amount of wastewater temporarily flows into the raw water pit 1 and therefore a large amount of wastewater is also sent to the flow rate adjusting tank 2 and overflows, a cushion tank 2A is provided and it is temporarily returned to the raw water pit 1. good. By installing such a cushion tank 2A, it becomes easy to deal with not only temporary increase / decrease of wastewater but also fluctuations throughout the day and night or seasonal fluctuations.

【0013】水質調整槽3において、中和剤、脱臭剤等
の薬剤3aが必要に応じて投入される。水質調整された
廃水は固油液分離槽4Aに送られる。該固油液分離槽4
Aには油脂分を消化分解することの可能な通性嫌気性微
生物(例えば第4図に示す微生物TBC−0001−昭
和63年9月27日微工研証明願い済み)が移乗してい
る廃水浄化材4aが設置されている。
In the water quality adjusting tank 3, a chemical 3a such as a neutralizing agent and a deodorant is added as needed. The wastewater whose water quality has been adjusted is sent to the solid-oil liquid separation tank 4A. The solid oil liquid separation tank 4
Wastewater carrying a facultative anaerobic microorganism capable of digesting and decomposing oils and fats (for example, microorganism TBC-0001 shown in FIG. 4—requested to be certified by the Institute of Fine Arts, September 27, 1988) to A. The purification material 4a is installed.

【0014】廃水浄化材4aは低品位石炭(例えば亜炭
または褐炭)を原料とし、硫酸に24時間浸漬して多孔
質としたハイブリケットチャー41を0.3〜0.4g
/ケの小粒に加工した後、該ハイブリケットチャー41
に前記通性嫌気性微生物を約10個/g移乗し、7×2
0×30cmの濾過材(例えば綿布)42の内部に約4
0ケ平均分散配置したものであって、ステンレス製のケ
ース43によって保持されて3段に設けられている。
The waste water purifying material 4a is made of low-grade coal (for example, lignite or brown coal) as a raw material, and 0.3 to 0.4 g of the hybrid hybrid char 41 made porous by being immersed in sulfuric acid for 24 hours.
After processing into small particles of /
Transfer the facultative anaerobic microorganism to about 10 cells / g, and
Approximately 4 inside the filter media (for example, cotton cloth) 42 of 0x30 cm
It is arranged in an average distribution of 0 pieces, and is held by a case 43 made of stainless steel and provided in three stages.

【0015】廃水の注入口44は底部側の胴部に偏心し
て設けられており、該注入口44から勢いよく注入され
た廃水は円形の壁面に沿って回転するので、廃水中に浮
遊していた固形物は凝縮して沈降分離される。分離され
た固形物は浮遊物質消化分解槽9Aに送られる。
The waste water inlet 44 is eccentrically provided on the bottom side body portion, and the waste water injected vigorously from the inlet 44 rotates along a circular wall surface, so that it is suspended in the waste water. The solid matter is condensed and sedimented. The separated solid matter is sent to the suspended matter digestion decomposition tank 9A.

【0016】固形物が除去された廃水は3段に設けられ
ている前記廃水浄化材4aを下から上に透過するとき、
濾過材42に油脂分が吸着除去されて浄化される。濾過
材42に吸着された油脂分は前記通性嫌気性微生物によ
って次々に消化分解されるので、吸着された油脂分で濾
過材42が目詰まりすることはない。
When the wastewater from which the solid matter has been removed passes through the wastewater purifying material 4a provided in three stages from bottom to top,
Oils and fats are adsorbed and removed by the filter material 42 to be purified. The fats and oils adsorbed on the filter medium 42 are successively digested and decomposed by the facultative anaerobic microorganisms, so that the fats and oils adsorbed do not cause the filter medium 42 to be clogged.

【0017】廃水浄化材4aによって浄化された廃水は
上部の排出口45から排出され、固油液分離槽4Aと同
様に構成されたもう一つの固油液分離槽4Bに送られ、
固油液分離槽4Aだけでは除去出来なかった残留油脂分
を再度消化分解して除去する。このようにして固油液分
離槽4Aと4Bを透過した廃水には油脂分は殆ど残留し
ていない。
The waste water purified by the waste water purifying material 4a is discharged from the upper discharge port 45 and sent to another solid oil-liquid separation tank 4B having the same structure as the solid oil liquid separation tank 4A.
Residual fats and oils that could not be removed only by the solid-oil liquid separation tank 4A are digested and decomposed again to be removed. In this way, almost no fat or oil remains in the wastewater that has passed through the solid-oil-liquid separation tanks 4A and 4B.

【0018】油脂分が除去された廃水は、続いて5A以
下の曝気槽に送られ、油脂分以外の汚濁物質が除去され
る。曝気槽5Aには低品位石炭を原料として前記同様に
形成したハイブリケットチャーに好気性微生物である根
足虫類が約10個/g移乗した廃水浄化材5aが、多数
の通水孔が穿設されているパンチングメタルによって作
られた中段の棚51に、5cmの立方体状に加工されて
高さ40cmに敷き詰められて設置されている。
The wastewater from which the oil and fat components have been removed is subsequently sent to an aeration tank of 5 A or less, and contaminants other than the oil and fat components are removed. In the aeration tank 5A, a hybrid water made from low-grade coal as a raw material was mixed with a waste water purifying material 5a in which about 10 pieces / g of aerobic microorganisms, rhizobia, were transferred, and a large number of water passage holes were formed. It is installed on the middle shelf 51 made of punching metal, which is processed into a cube of 5 cm and spread to a height of 40 cm.

【0019】浄化槽5Aの側壁上部の注入口52から導
入された廃水は一旦底部まで下がり、廃水浄化材5aを
下から上に透過するとき廃水浄化材5aの無数の微小孔
に吸着されて浄化される。廃水浄化材5aに吸着された
汚濁物質は前記好気性微生物によって次々と消化分解さ
れるので、目詰まりすることなく長期間使用することが
出来る。
The waste water introduced from the inlet 52 at the upper part of the side wall of the septic tank 5A once drops to the bottom, and when passing through the waste water purifying material 5a from bottom to top, it is adsorbed and purified by the numerous minute holes of the waste water purifying material 5a. It The pollutants adsorbed on the wastewater purification material 5a are digested and decomposed one after another by the aerobic microorganisms, so that the pollutants can be used for a long time without being clogged.

【0020】なお、廃水浄化材5aの微生物が好気性で
あるため、曝気槽5Aはその消化分解活動を活発にさせ
る目的で別途設置したブロアー6から、エアーが底部に
供給されて曝気されている。曝気槽5Aの排出口53か
ら排出した廃水は続いて曝気槽5Bおよび5Cに順次送
り込まれ、それぞれの曝気槽に設けられている廃水浄化
材(図示せず)によつて浄化される。
Since the microorganisms of the wastewater purification material 5a are aerobic, air is supplied to the bottom of the aeration tank 5A from the blower 6 separately installed for the purpose of activating the digestion and decomposition activity of the aeration tank 5A. .. The wastewater discharged from the discharge port 53 of the aeration tank 5A is successively sent to the aeration tanks 5B and 5C and purified by a wastewater purification material (not shown) provided in each aeration tank.

【0021】これら廃水浄化材には汚濁物質を順次消化
分解するために最も適した微生物、すなわち鞭毛虫類と
繊毛虫類がそれぞれに移乗されている。
Microorganisms most suitable for sequentially digesting and decomposing pollutants, that is, flagellates and ciliates are transferred to these wastewater purification materials, respectively.

【0022】最後の曝気槽5Cを出た廃水は沈殿槽7に
送られ、消化分解と云う上工程で発生した物質を沈殿さ
せる。沈殿槽7の上澄み液が河川等8に放流される。
The wastewater discharged from the last aeration tank 5C is sent to the precipitation tank 7 to precipitate the substances generated in the upper step called digestion and decomposition. The supernatant of the settling tank 7 is discharged to the river 8 or the like.

【0023】一方、沈殿槽7で沈殿した沈殿物と前記固
油液分離槽4Aおよび4Bで発生した沈殿物は浮遊物消
化分解槽9Aおよび9Bに送られ分解処理される。そし
て、浮遊物消化分解槽9Aおよび9Bで発生する最終の
廃棄物は産業廃棄物業者に引き取られて処置される。
On the other hand, the precipitate deposited in the settling tank 7 and the precipitates generated in the solid-oil liquid separation tanks 4A and 4B are sent to suspended matter digestion decomposition tanks 9A and 9B for decomposition treatment. Then, the final waste generated in the suspended matter digestion and decomposition tanks 9A and 9B is collected by an industrial waste supplier and treated.

【0024】一方、この浮遊物消化分解工程で発生する
液状物は前記水質調整槽3に送られ、再度微生物による
上記の消化分解工程に回される。
On the other hand, the liquid substance generated in the digestion and decomposition step of the suspended matter is sent to the water quality adjusting tank 3 and is again sent to the above-mentioned digestion and decomposition step by microorganisms.

【0025】上記工程によって浄化され、沈殿槽7から
河川等8に放流される廃水の各種分析値の一例を表1に
原水の分析値と共に示す。同表より明らかなように本発
明によって浄化した廃水は規制値を充分クリヤーするも
のであり、特に廃水浄化材の補充とか手入れなしで1年
稼働した後も、全く浄化能力が低下していないのがよく
理解出来る。
Table 1 shows an example of various analytical values of the wastewater purified by the above process and discharged from the settling tank 7 to the river 8 together with the analytical values of the raw water. As is clear from the table, the wastewater purified by the present invention clears the regulated value sufficiently, and in particular, the purification capacity is not deteriorated even after one year of operation without supplementation or maintenance of the wastewater purification material. Can understand well.

【0026】[0026]

【表1】 [Table 1]

【0027】なお、上記実施例では浄化すべき廃水が油
脂分を含んでいると想定し、前処理として通性嫌気性微
生物が移乗している廃水浄化材4aに浄化すべき廃水を
透過させ、次いで好気性微生物が移乗している廃水浄化
材5aに廃水を透過させる構成としたが、油脂分を含有
していない廃水の場合には、好気性微生物が移乗してい
る廃水浄化材5aに直接透過させて浄化させれば良い。
また、特許請求の範囲記載の趣旨から逸脱しない範囲で
実施例の装置の一部を省略したり、他の装置を付加する
ことも可能である。
In the above embodiment, it is assumed that the wastewater to be purified contains fats and oils, and the pretreatment is to pass the wastewater to be purified to the wastewater purifying material 4a carrying facultative anaerobic microorganisms. Then, the wastewater purifying material 5a on which the aerobic microorganisms are transferred is configured to allow the permeation of the wastewater. However, in the case of wastewater containing no fats and oils, the wastewater purifying material 5a on which the aerobic microorganisms are transferred is directly attached. It should be permeated and purified.
Further, it is possible to omit a part of the device of the embodiment or add another device without departing from the spirit of the claims.

【0028】[0028]

【発明の効果】以上説明したように、本発明になる廃水
浄化法によれば廃水を極めて奇麗に浄化することが出来
る。しかも、微生物の消化分解活動を利用しているた
め、フィルター、吸着剤等を使用する従来法が目詰まり
して時間の経過と共にその浄化機能が低下するのと比
べ、経時劣化が全くないと云う極めて大きな利点があ
る。また、装置が小型化出来るので省スペース化が図ら
れることも地価高騰の現在、都市部に浄化装置を設置す
る上では大きな利点であり、汚濁物質が微生物によって
次々に消化分解されて無害な窒素ガス、炭酸ガス等とし
て大気中に放出され、汚泥として堆積する分が少ないの
も処理費用、処理スペースが少なくなるので好ましい。
また、木質部を有する多孔質のハイブリケットチャーに
微生物を移乗した廃水浄化材を用いるので、年末年始の
ように装置の使用を停止することがあっても、微生物は
木質部を食べて棲息出来るので、微生物の栄養分を供給
する必要が全くない。さらに、ハイブリケットチャーの
木質部が保温効果を有しているので、廃水中に設置した
ときにも活性炭より温度が高くなり、冬季においても特
別な寒冷地を除き、微生物が活動するに充分な温度が維
持され、特に保温する必要がないと云う特徴もある。し
たがって、本発明の廃水浄化法は生活雑廃水、畜産廃水
はもちろん食品加工工場、酒造工場等の廃水の浄化に顕
著な効果がある。
As described above, according to the wastewater purification method of the present invention, wastewater can be purified extremely neatly. Moreover, since it utilizes the digestive decomposition activity of microorganisms, it is said that there is no deterioration over time, as compared with the conventional method that uses filters, adsorbents, etc. being clogged and its purification function declines over time. There are enormous advantages. In addition, because the equipment can be downsized and space can be saved, it is also a great advantage to install purification equipment in urban areas at the present time of rising land prices, and pollutants are successively digested and decomposed by microorganisms and harmless nitrogen It is preferable that gas, carbon dioxide, etc. are released into the atmosphere and accumulated as sludge in a small amount because the treatment cost and the treatment space are reduced.
In addition, since a wastewater purification material with microorganisms transferred to a porous hybridette char with a wood part is used, even if the use of the device may be stopped like the year-end and New Year holidays, the microorganisms can eat the wood part and live. No need to supply microbial nutrients. In addition, since the wood part of the hybrid charcoal has a heat-retaining effect, the temperature is higher than that of activated carbon even when installed in wastewater, and even in the winter, except in special cold regions, the temperature is high enough to activate microorganisms. Is also maintained, and there is also a feature that it is not necessary to keep warm. Therefore, the wastewater purification method of the present invention has a remarkable effect on purification of wastewater from household wastewater, livestock wastewater, food processing factory, brewing factory, and the like.

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

【図1】本発明の一実施例を示す説明図である。FIG. 1 is an explanatory diagram showing an embodiment of the present invention.

【図2】装置の一部の拡大説明図である。FIG. 2 is an enlarged explanatory view of a part of the device.

【図3】装置の一部の拡大説明図である。FIG. 3 is an enlarged explanatory view of a part of the device.

【図4】通性嫌気性微生物の形態を示す顕微鏡写真(3
00倍)である。
FIG. 4 is a micrograph showing the morphology of facultative anaerobic microorganisms (3
00 times).

【図5】図4の要部の拡大写真(1000倍)である。5 is an enlarged photograph (1000 times) of the main part of FIG.

【図6】図4の要部の拡大写真(1000倍)である。FIG. 6 is an enlarged photograph (1000 times) of a main part of FIG.

【符号の説明】[Explanation of symbols]

1 原水ピット 2 流量調整槽 2A クッションタンク 3 水質調整槽 3a 薬剤 4A、4B 固油液分離槽 4a 廃水浄化材 5A、5B、5C 曝気槽 5a 廃水浄化材 6 ブロアー 7 沈殿槽 8 河川等 9A、9B 浮遊物消化分解槽 1 Raw Water Pit 2 Flow Control Tank 2A Cushion Tank 3 Water Quality Control Tank 3a Chemicals 4A, 4B Solid Oil Liquid Separation Tank 4a Wastewater Purifying Material 5A, 5B, 5C Aeration Tank 5a Wastewater Purifying Material 6 Blower 7 Settling Tank 8 Rivers 9A, 9B Floating matter digestion and decomposition tank

───────────────────────────────────────────────────── フロントページの続き (72)発明者 千羽 武 東京都葛飾区新小岩3丁目19番8号 有限 会社興陽工業内 ─────────────────────────────────────────────────── ─── Continued Front Page (72) Inventor Takeshi Senba 3-19-8 Shinkoiwa, Katsushika-ku, Tokyo Koyo Kogyo Co., Ltd.

Claims (1)

【特許請求の範囲】 【請求項1】 低品位石炭を酸洗などにより多孔質化し
たハイブリケットチャーに好気性微生物を移乗させて形
成される廃水浄化材に、廃水を一定の流量で透過させ、
前記廃水浄化材に吸着された汚濁物質を前記好気性微生
物によって消化分解することを特徴とする廃水浄化法。
Claim: What is claimed is: 1. A wastewater purification material formed by transferring aerobic microorganisms to a hybridized char made by pouring low-grade coal by pickling or the like to allow the wastewater to permeate at a constant flow rate. ,
A method for purifying wastewater, which comprises digesting and decomposing pollutants adsorbed on the wastewater purification material by the aerobic microorganisms.
JP30849091A 1991-10-28 1991-10-28 Wastewater purification method Expired - Lifetime JPH0775709B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP30849091A JPH0775709B2 (en) 1991-10-28 1991-10-28 Wastewater purification method

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP30849091A JPH0775709B2 (en) 1991-10-28 1991-10-28 Wastewater purification method

Related Parent Applications (1)

Application Number Title Priority Date Filing Date
JP63241997A Division JPH0290997A (en) 1988-09-27 1988-09-27 Waste water purification process

Publications (2)

Publication Number Publication Date
JPH05296A true JPH05296A (en) 1993-01-08
JPH0775709B2 JPH0775709B2 (en) 1995-08-16

Family

ID=17981645

Family Applications (1)

Application Number Title Priority Date Filing Date
JP30849091A Expired - Lifetime JPH0775709B2 (en) 1991-10-28 1991-10-28 Wastewater purification method

Country Status (1)

Country Link
JP (1) JPH0775709B2 (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006272171A (en) * 2005-03-29 2006-10-12 Denka Consult & Eng Co Ltd Microbial carrier blended with nitrohumate
CN102001789A (en) * 2010-11-15 2011-04-06 北京国能普华环保工程技术有限公司 Process for treating coal chemical waste water
CN102070277A (en) * 2010-11-15 2011-05-25 北京国能普华环保工程技术有限公司 Coal gasification wastewater treatment process

Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49100847A (en) * 1973-01-30 1974-09-24
JPS49122885A (en) * 1973-03-29 1974-11-25
JPS5069845A (en) * 1973-10-24 1975-06-10
JPS5341064A (en) * 1976-09-25 1978-04-14 Azuma Kawazoe Sewage treating apparatus
JPS5520649A (en) * 1978-07-29 1980-02-14 Agency Of Ind Science & Technol Biological treatment method of waste water
JPS6115791A (en) * 1984-07-02 1986-01-23 Orihara Seisakusho:Kk Apparatus for purifying excrements
JPS6249999A (en) * 1985-08-27 1987-03-04 Gamuren Nippon Kk Method for removing water-bloom in lake, swamp and pond by utilizing variant bacteria
JPS6393399A (en) * 1986-10-08 1988-04-23 Shinnitsuka Kankyo Eng:Kk Microorganism treatment of waste water

Patent Citations (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49100847A (en) * 1973-01-30 1974-09-24
JPS49122885A (en) * 1973-03-29 1974-11-25
JPS5069845A (en) * 1973-10-24 1975-06-10
JPS5341064A (en) * 1976-09-25 1978-04-14 Azuma Kawazoe Sewage treating apparatus
JPS5520649A (en) * 1978-07-29 1980-02-14 Agency Of Ind Science & Technol Biological treatment method of waste water
JPS6115791A (en) * 1984-07-02 1986-01-23 Orihara Seisakusho:Kk Apparatus for purifying excrements
JPS6249999A (en) * 1985-08-27 1987-03-04 Gamuren Nippon Kk Method for removing water-bloom in lake, swamp and pond by utilizing variant bacteria
JPS6393399A (en) * 1986-10-08 1988-04-23 Shinnitsuka Kankyo Eng:Kk Microorganism treatment of waste water

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2006272171A (en) * 2005-03-29 2006-10-12 Denka Consult & Eng Co Ltd Microbial carrier blended with nitrohumate
CN102001789A (en) * 2010-11-15 2011-04-06 北京国能普华环保工程技术有限公司 Process for treating coal chemical waste water
CN102070277A (en) * 2010-11-15 2011-05-25 北京国能普华环保工程技术有限公司 Coal gasification wastewater treatment process

Also Published As

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