JPS58189098A - Purifier for filthy water - Google Patents

Purifier for filthy water

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Publication number
JPS58189098A
JPS58189098A JP7191582A JP7191582A JPS58189098A JP S58189098 A JPS58189098 A JP S58189098A JP 7191582 A JP7191582 A JP 7191582A JP 7191582 A JP7191582 A JP 7191582A JP S58189098 A JPS58189098 A JP S58189098A
Authority
JP
Japan
Prior art keywords
water
anaerobic
hot water
aerobic
tank
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
JP7191582A
Other languages
Japanese (ja)
Inventor
Hisao Makino
牧野 久男
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.)
Kaiyo Kogyo KK
Original Assignee
Kaiyo Kogyo KK
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 Kaiyo Kogyo KK filed Critical Kaiyo Kogyo KK
Priority to JP7191582A priority Critical patent/JPS58189098A/en
Publication of JPS58189098A publication Critical patent/JPS58189098A/en
Pending legal-status Critical Current

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  • Purification Treatments By Anaerobic Or Anaerobic And Aerobic Bacteria Or Animals (AREA)

Abstract

PURPOSE:To make the propagation of microbes excellent by managing the temp. of water for improving the efficiency of purification, by providing an aerobic purifier tank equipped with a heating means and a forcible fluidizing means in a line with an anaerobic purifier tank equipped with a heating means. CONSTITUTION:Raw water such as municipal waste water is introduced through a base pipe 6 along the arrow 22 and then reserved through water-supply pipes 3, 4 along the arrows 33, 34 in an anaerobic purifier tank 1. Hot water heated by a boiler 15 is sent through branched pipes 9, 10 and annular pipes 11, 12 and then returned through returning pipes 16, 17 to the boiler. By this circulation, the water to be treated in the purifier tank 1 is heated at a proper temp. of 30-40 deg.C. Thereafter, the water is transferred to an anaerobic purifier tank 2, and a supernatant liquid after being treated is introduced through an overflow pipe 44 into an aerobic purifier tank 22. In the purifier tank 22, a honeycomb core 24 is lowered into the water to be treated, so that fine solid matter can be treated by anaerobes inserted to the honeycomb core.

Description

【発明の詳細な説明】 この発明は嫌気性菌による処理槽と好気性菌による処理
槽を連設して原水中の固形物の多寡に応じた処理を行う
と共に、水淵管理により微生物の繁殖を良好にして効率
を向上させることを目的とした汚水浄化装置に関するも
のである。
Detailed Description of the Invention The present invention provides a treatment tank using anaerobic bacteria and a treatment tank using aerobic bacteria to perform treatment according to the amount of solids in raw water, and to control the water edge to allow microorganisms to grow. The present invention relates to a sewage purification device that aims to improve efficiency by improving water quality.

従来BODおよびCODの多い汚水浄化に関し、嫌気性
菌による処理が提案されていたが、比較的滞留時間が長
((例えば10日以上)大きな容量の処理槽を必要とす
る問題点があった。然るに近来処理槽内へ充填材を入れ
ることによって嫌気性菌の繁殖を助長し、滞留時間を大
幅に短縮することに成功した(例えばJ時間〜3o時間
)。然し乍ら嫌気性処理の溢水をそのま匁放流すること
はできない(例えばBOI)が100前后ある)ので、
これを好気性処理し、BODを70以下にして放流する
ことが研究されている。前記のように嫌気性処理と好気
性処理の一貫処理システムによれば、必然的に両浄化槽
の処理能力が一定にならなければ能率的かつ高性能の処
理は望むべくもないが、微生物処理の効率を左右する最
も大きなファクターは温度である。例えば比較的低い温
度(例えば/S℃前后)の処理量は適温時(例えば35
℃前后)の処理量のh以下になることが知られており、
而も嫌気性処理に際しては醗酵などによって原水の温度
が上ることが考えられるが、好気性処理において水温の
自然上昇は考えられない。そこで嫌気性処理と、好気性
処理とをはy等しい水温で行うことを条件とした処理装
置においては、水温の変化と共に相互間に処理能力の相
違を来し、円滑な一貫処理は困難となる。
Conventionally, treatment using anaerobic bacteria has been proposed for the purification of wastewater containing a large amount of BOD and COD, but this method has the problem of requiring a relatively long residence time (for example, 10 days or more) and a large-capacity treatment tank. However, in recent years, it has been possible to promote the growth of anaerobic bacteria by inserting a filler into the treatment tank and to significantly shorten the residence time (for example, from J hours to 30 hours). Since it is not possible to release the momme (for example, BOI is before and after 100),
Research is underway to treat this aerobically and reduce the BOD to 70 or less before releasing it. As mentioned above, according to the integrated treatment system of anaerobic treatment and aerobic treatment, efficient and high-performance treatment cannot be expected unless the treatment capacity of both septic tanks becomes constant. The biggest factor that affects efficiency is temperature. For example, the throughput at a relatively low temperature (e.g., before /S°C) is lower than that at an appropriate temperature (e.g., 35°C).
It is known that the processing amount is less than h of the processing amount of
Furthermore, in anaerobic treatment, the temperature of raw water may rise due to fermentation, but in aerobic treatment, a natural rise in water temperature is not considered. Therefore, in treatment equipment that requires anaerobic treatment and aerobic treatment to be performed at the same water temperature, differences in treatment capacity will occur as the water temperature changes, making smooth integrated treatment difficult. .

然るにこの発明においては、処理槽へ加温装置を付設し
たので、処理水は外気温に関係なく、はy一定の水温に
調節することが可能となり、装置能力を常時最高の状態
で稼動させると共に、汚水の一貫円滑処理ができるよう
になり、放流水を常時規定以l−の清浄度に保ち得るこ
とに成功したのである。この発明の大きな特徴は、外気
温に関係なく同一処理能力を保ち得ることである。また
この発明の他の特徴は処理時に発生する熱源(可燃性気
体)を利用し、又は太陽熱を利用するなど、経常費の節
減を図った点にある。更にこの発明の他の特徴は嫌気性
処理に際して嫌気性菌の着床用に多数の個体を充填し、
好気性処理に際しては・・ニカムコアを充填すると共に
、処理水を循環させた点である。
However, in this invention, since a heating device is attached to the treatment tank, it is possible to adjust the temperature of the treated water to a constant temperature regardless of the outside temperature, which allows the equipment to operate at maximum capacity at all times. It has become possible to process sewage consistently and smoothly, and has succeeded in keeping the effluent at a level of cleanliness that is above the specified level at all times. A major feature of this invention is that the same processing capacity can be maintained regardless of the outside temperature. Another feature of the present invention is that ordinary costs are reduced by using a heat source (flammable gas) generated during processing or solar heat. Furthermore, another feature of the present invention is that during anaerobic treatment, a large number of bacteria are filled for implantation of anaerobic bacteria,
During aerobic treatment, Nicamcore was filled and treated water was circulated.

次にこの発明の実施例を添付図面について説明する。下
部を漏斗状に形成した嫌気性処理槽/、二を並列設置し
、前記嫌気性処理槽/、−の中央部へ原水の送水管3、
qを縦設し、送水管3、qの上端はバルブSを介して基
管乙に連結し、下端は各処理槽の下部へ開口させである
。前記送水管3、ダの垂直部には夫々給湯管7、gが遊
嵌してあり、給湯管7、gには上下所定間隔を保って分
岐管り、10が水、平方向へ放射状に夫々設置され、各
分岐管9.10は連結管/3、/qによって連結されろ
と共に、環状管//、/ユで連結され、一方の連結管/
3、/qの上端はボイラー15への戻し管/乙、/7と
連結し、前記給湯管7、gの上端はボイラー/Sよりの
送湯管/gとポンプ/9を介して連結される。前記各分
岐管7.10、環状管//、/2および連結管/3、/
qの内側間隙部には、多数の充填材Jが充填されて(・
る。
Next, embodiments of the invention will be described with reference to the accompanying drawings. Anaerobic treatment tanks /, 2 with funnel-shaped lower parts are installed in parallel, and raw water pipes 3, 2 are connected to the center of the anaerobic treatment tanks /, -.
Water pipes 3 and q are installed vertically, and the upper ends of the water pipes 3 and q are connected to the base pipe B via valves S, and the lower ends are opened to the lower part of each treatment tank. Hot water supply pipes 7 and g are loosely fitted into the vertical parts of the water supply pipes 3 and DA, respectively, and branch pipes 10 are connected to the water supply pipes 7 and 7 at a predetermined interval above and below, radially extending in the horizontal direction. The branch pipes 9 and 10 are connected by connecting pipes /3 and /q, and are connected by annular pipes // and /yu, with one connecting pipe /
3, the upper end of /q is connected to the return pipe /O, /7 to the boiler 15, and the upper end of the hot water supply pipe 7, g is connected to the hot water supply pipe /g from the boiler /S via pump /9. Ru. Said branch pipes 7.10, annular pipes //, /2 and connecting pipes /3, /
The inner gap of q is filled with a large number of fillers J (・
Ru.

前記充填材20は例えば短)くイブ状、球状、紐状、綱
片状などの最大寸法5Crn、最小寸法/Crn程度の
嫌気性菌着床材であって、仕切網2/などにより、定位
置内で若干移動できろように充填されて(・る。
The filling material 20 is an anaerobic bacteria settlement material having a maximum dimension of about 5 Crn and a minimum dimension of /Crn, such as a short tube shape, a spherical shape, a string shape, a rope shape, etc. It is filled so that it can move slightly within the position.

前記各湯管は前記充填材の支持枠を兼用し、必要に応じ
湯管の一部を閉鎖して支持枠専用に使用することもでき
る。
Each of the hot water pipes also serves as a support frame for the filler, and if necessary, a part of the hot water pipes can be closed and used exclusively for the support frame.

次に前記嫌気性処理槽/、2に隣接して下部を漏斗状と
した好気性処理槽22を設置し、前記処理槽ムの中火部
へ間欠空気揚水筒ユ3を縦設し、揚水筒、23の外側へ
ハニカムコア評な縦設(チューブの中心を垂直方向とす
る)する。また・・ニカムコア2qの下部には環状湯管
23を敷設し、環状湯管Jの直径対称的位置に給湯管ユ
乙と排湯管27を夫々連結する。また揚水筒23の下部
には空気室ユgを設け−(あり、空気室rgは揚水筒コ
3の外壁と所定の間隔を保った有頂外筒yが嵌装固定し
てあり、有頂外筒、29の内側へ揚水筒23の外壁との
間を二分する仕切筒30を揚水筒に嵌装し、前記揚水筒
の内側へは、その内壁と所定の間隙を保って案内筒3/
を挿入固定する通路な設けて空気室が構成しである。
Next, an aerobic treatment tank 22 with a funnel-shaped lower part is installed adjacent to the anaerobic treatment tank 2, and an intermittent air pumping tube 3 is vertically installed in the middle heat section of the treatment tank. A honeycomb core is installed vertically on the outside of the water bottle 23 (with the center of the tube in the vertical direction). In addition, an annular hot water pipe 23 is laid in the lower part of the Nikum core 2q, and a hot water supply pipe U and a hot water discharge pipe 27 are connected to diametrically symmetrical positions of the annular hot water pipe J, respectively. In addition, an air chamber y g is provided at the lower part of the water pumping tube 23, and the air chamber rg is fitted with a crested outer tube y that maintains a predetermined distance from the outer wall of the water pumping tube 3. A partition tube 30 that divides the space between the outer wall of the water pumping tube 23 and the outer wall of the water pumping tube 23 into two is fitted to the inside of the outer tube 29, and the guide tube 3/
It consists of an air chamber with a passageway for inserting and fixing it.

前記実施装置に基づき、原水の処理状態を説明する。第
1図において、基管乙より矢示3)のように原水(都市
排水又は工場排水などの汚水、例えばB 01) lo
θ〜数千程度のもの)をポンプ(図示してない)によっ
て送り込む。この場合に予定濃度以−ヒの原水について
は予め調整槽で濃度を調整すると共に、比較的大きい固
形物は除去する。
The processing state of raw water will be explained based on the above-mentioned implementation device. In Figure 1, raw water (sewage such as urban wastewater or industrial wastewater, e.g. B01) is drawn from base pipe B as shown by arrow 3).
θ~several thousand) is sent by a pump (not shown). In this case, the concentration of raw water with a concentration higher than the predetermined concentration is adjusted in advance in a regulating tank, and relatively large solids are removed.

前記基管乙を経た原水は矢示3、?、3//のように送
水管3、qを経て、その下部より矢示、?、? 、−5
si(17)よう至lS日掛るけれども、この発明にお
いては充填材を使用したので、7日〜2日で所定の目的
を達する程度の繁殖度を得ることができる。従って充填
材に嫌気性菌が十分着床するまで(最初)/θ日位の時
間を要するが、一旦十分の着床を得てからは:l’%時
間〜tig時間の滞留によって連続的に処理することが
できる。前記において一旦連続処理が開始されると、原
則的には処理槽/のみへ原水を導き、(バルブSを操作
し)処理槽/の溢水管3Sを経て送水管グより処理槽コ
内へ送水する。従って処理槽/の滞留時間は/一時間乃
至29時間にすることができろ。一方ボイラー15で加
温された湯は給湯管7、gを介して矢示3乙、37のよ
うに分岐管9、/θに送られ、環状管/l、/コを経て
戻し管/6、/7よりボイラーに戻され、このような循
環によって処理槽内の被処理水を適温に加温する。この
温度は嫌気性菌の繁殖適温(30℃〜lIo℃)であっ
て、検流装置(図示してない)の出力によってポンプI
fを始動又は停止させることにより槽内の温度を制御す
る。また嫌気性菌としてメタン発生菌を使用すれば、処
理によって生じたメタンガスを採取管39により取り出
し、その一部をボイラー/!iの燃焼器qOに導き、自
己発生燃料を用いて温度制御できることになり、汚水処
理のランニングコストを低減することができる。
The raw water that has passed through the base pipe B is indicated by arrow 3, ? , 3// through water pipes 3 and q, and from the bottom as shown by the arrow, ? ,? , -5
Although it takes up to 1S days for si(17), in this invention, since a filler is used, it is possible to obtain a level of reproduction sufficient to reach the predetermined purpose in 7 to 2 days. Therefore, it takes about /θ days for the anaerobic bacteria to fully settle on the filling material (initial), but once sufficient implantation has been achieved, it is continuously can be processed. Once the continuous treatment is started in the above, in principle, the raw water is led to the treatment tank/ only (by operating the valve S), and the water is sent into the treatment tank via the water supply pipe G via the overflow pipe 3S of the treatment tank/. do. Therefore, the residence time in the treatment tank can be set from 1 hour to 29 hours. On the other hand, the hot water heated by the boiler 15 is sent to the branch pipe 9, /θ as shown by arrows 3 O and 37 via the hot water supply pipe 7 and g, and returns through the annular pipes /l and /ko to the return pipe /6. , /7, and is returned to the boiler, and through such circulation, the water to be treated in the treatment tank is heated to an appropriate temperature. This temperature is the optimum temperature for the growth of anaerobic bacteria (30°C to 10°C), and the pump I
The temperature in the tank is controlled by starting or stopping f. In addition, if a methane-producing bacterium is used as the anaerobic bacterium, the methane gas generated during the treatment is taken out through the sampling pipe 39 and a part of it is sent to the boiler/! Since the temperature can be controlled using self-generated fuel, running costs for wastewater treatment can be reduced.

前記のように処理槽内を嫌気性菌に適する恒温にすれば
、菌の繁殖がきわめて良好となり、滞留時間の短縮(例
えば72時間以下)を図ることができことによって溢水
管より汲い−」−げた被処理水を、送水管3を経て再び
処理槽底に導き、処理槽内の被処理水を強制循環させて
滞留時間の延長を図ることもできる。図中93は逆止弁
である。前記のようにして、処理槽/で処理された被処
理水は処理槽コに移り、処理槽コで処理された上澄水は
l−301)10θ〜−00前後になって溢水管像より
矢示q!iのように好気性処理槽22内へ入る。この処
理槽、22においては、加圧空気をエアホース銘より空
気室2g内へ供給すると、空気室、2g内の水は順次下
降し、水面が鎖線q?の位置まで下降した時に、空気室
内の空気は矢示’Ig、 Q9.50のように一度に揚
水筒内へ排出される。この場合に空気は図示S/のよう
に一団となって上昇する為に、下方の水は揚水筒の孔5
.2より矢示S3のように吸引され、矢示5Zのように
上昇して、揚水筒の上端より矢示5Sのように四散する
。従って処理槽内の水は中央部を上昇1〜てハニカムコ
アの内を矢示見のように下降し、結局対流を生じること
になり、ハニカムコアに着床した好気性菌によって微固
形物を処理することができろ。この場合に、前記ボイラ
ー/、!Iかも環状湯管5に温水が送られるので、処理
槽内を所定の恒温に保ち、好気性菌の繁殖を最良に保つ
ことができろ。図中57.5gは送湯管に介装したバル
ブである。−前記実施例においては、嫌気性処理槽゛(
一方の処理槽のみをメタン発生菌としてもよい)で発生
した可燃性気体をボイラーの燃焼器で燃焼させる3よう
にしたが、太陽熱温水器59を利用して、昼間加熱した
温湯を使用するようにしてもよ(・0図中ろOはポンプ
3にの吸入側に連結し、乙/は戻し管3qに連結して使
用する。
As mentioned above, if the temperature inside the treatment tank is maintained at a constant temperature suitable for anaerobic bacteria, the bacteria will grow very well and the residence time can be shortened (for example, 72 hours or less), making it possible to drain the water from the overflow pipe. It is also possible to extend the residence time by guiding the removed water to the bottom of the treatment tank through the water pipe 3 and forcibly circulating the water in the treatment tank. In the figure, 93 is a check valve. As described above, the water to be treated that has been treated in the treatment tank / is transferred to the treatment tank A, and the supernatant water that has been treated in the treatment tank A is around l-301) 10θ to -00 as shown by the arrow in the image of the overflow pipe. Show! Enter the aerobic treatment tank 22 as shown in i. In this treatment tank 22, when pressurized air is supplied into the air chamber 2g from the air hose, the water in the air chamber 2g gradually descends, and the water surface reaches the chain line q? When it descends to the position, the air in the air chamber is discharged all at once into the water pump as shown by arrow 'Ig, Q9.50. In this case, the air rises as a group as shown in the figure S/, so that the water below flows into the hole 5 of the water pump.
.. 2 as shown by arrow S3, rises as shown by arrow 5Z, and scatters from the upper end of the water pump as shown by arrow 5S. Therefore, the water in the treatment tank rises in the center and descends inside the honeycomb core as shown by the arrow, eventually causing convection, and the aerobic bacteria that have settled on the honeycomb core remove fine solids. Be able to handle it. In this case, the boiler/,! Since hot water is sent to the annular hot water pipe 5, the inside of the treatment tank can be maintained at a predetermined constant temperature, and the propagation of aerobic bacteria can be maintained at its best. In the figure, 57.5g is a valve installed in the hot water pipe. - In the above embodiment, the anaerobic treatment tank (
The flammable gas generated by the methane-producing bacteria may be used in only one treatment tank is burned in the combustor of the boiler, but it is also possible to use hot water heated during the day using a solar water heater (O in the figure is connected to the suction side of the pump 3, and O is connected to the return pipe 3q.

F記のように好気性浄化槽により処理すれば、BOI)
はλθ0より10以下に減少することが認められた。即
ちこの発明によれば、加温装置を具備した嫌気性浄化槽
に、加温装置を具備した好気性浄化槽を並設して順次浄
化処理したので、生活排水又は工場排水などのように1
30 D値の高い排水であっても、連続的に浄化され、
しかも恒温処理によって微生物は常時最高の効率を発揮
し得る効果がある。従って従来70日乃至73日滞留し
ていたものが、1日以下の滞留で十分所期の目的を達成
することができるようになり、比較的小さい容積で大容
量の汚水処理ができる効果がある。また嫌気性菌および
好気性菌を使用するものであって、加温に際しては処理
の際生じる可燃性気体を使用し、又は太陽熱を使用する
のでランニングコストを著しく低減することができる。
If treated in an aerobic septic tank as shown in F, BOI)
It was observed that λθ0 decreased to 10 or less. That is, according to the present invention, an anaerobic septic tank equipped with a heating device and an aerobic septic tank equipped with a heating device are installed in parallel to perform purification treatment in sequence.
30 Even wastewater with a high D value is continuously purified,
Moreover, constant temperature treatment has the effect of allowing microorganisms to always exhibit their highest efficiency. Therefore, instead of 70 to 73 days of sewage retention in the past, it is now possible to achieve the desired purpose with retention of less than 1 day, making it possible to treat a large amount of sewage with a relatively small volume. . Furthermore, since anaerobic bacteria and aerobic bacteria are used, and flammable gas generated during heating is used or solar heat is used for heating, running costs can be significantly reduced.

尚実施例は二つの嫌気性処理槽に一つの好気性処理槽を
セントにしたが、必ずしもこのようなセントに限定され
るものではない。
In the embodiment, two anaerobic treatment tanks and one aerobic treatment tank are used as centers, but the invention is not necessarily limited to such a center.

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

第1図はこの発明の実施例の一部を省略した平面図、第
Ω図は同じく断面図、第3図は太陽熱泥水器の斜視図で
ある。 /、λ・・嫌気性処理槽  3、グ・・送水管7、g@
番給湯管  ヲ、10・・分岐管  //、/2II・
環状管  /3、/qII11連結管  /6、/7−
・戻し管  15・・ボイラー  7g・・送湯管/9
@曝ポンプ  ユ0@魯充填材  ユl・・網n・・好
気性処理槽  23・・揚水筒  J・・ハニカムコア
  λS・・環状湯管  2g・・空気室 特許出願人 海洋工業株式会社 代理人 鈴木正次
FIG. 1 is a partially omitted plan view of an embodiment of the present invention, FIG. Ω is a sectional view, and FIG. 3 is a perspective view of a solar slurry. /, λ...Anaerobic treatment tank 3, G...Water pipe 7, g@
Number hot water supply pipe wo, 10... Branch pipe //, /2II...
Annular pipe /3, /qII11 connecting pipe /6, /7-
・Return pipe 15...Boiler 7g...Hot water pipe/9
@ Exposure pump Yu 0 @ Lu Filling material Yul... Net n... Aerobic treatment tank 23... Water pump J... Honeycomb core λS... Annular hot water pipe 2g... Air chamber Patent applicant Kaiyo Kogyo Co., Ltd. Agent Masatsugu Suzuki

Claims (1)

【特許請求の範囲】 17III淵装置を具備した嫌気性浄化槽に、加温装置
を具備した好気性浄化槽を連設し、好気性浄化槽には強
制流動装置を備えたことを特徴とする汚水浄化装置 λ 加温装置は浄化槽内に敷設した温水管と、湛水管内
を循環する温水の加温および流動制御装置とを結合させ
てなる特許請求の範囲第1項記載の汚水浄化装置 、7 強制流動装置は直立させた揚水筒の下部に空気を
間欠的に送る装置を設置した特許請求の範囲第7項記載
の汚水浄化装置 q 嫌気性浄化槽は漏斗状槽内に多数の個体よりなる充
填材を充填した特許請求の範囲第1項記載の汚水浄化装
置 S 好気性浄化槽は槽の中間部にハニカムコアよりなる
充填材を縦設した特許請求の範囲第1項記載の汚水浄化
装置 6 加温装置における温水の加温は嫌気性浄化槽におい
て発生したり燃気体を燃料とするボイラーとした特許請
求の範囲第一項記載の汚水浄化装置7 加温装置におけ
る温水の加温は太陽熱湛水器とした特許請求の範囲第2
項記載の汚水浄化装置
[Claims] A sewage purification device characterized in that an anaerobic septic tank equipped with a 17III deep water device is connected to an aerobic septic tank equipped with a heating device, and the aerobic septic tank is equipped with a forced flow device. 7. A sewage purification device according to claim 1, in which the heating device combines a hot water pipe laid in a septic tank and a heating and flow control device for hot water circulating in the reservoir pipe, 7. Forced flow. The device is a sewage purification device (q) according to claim 7, in which a device for intermittently sending air is installed at the bottom of an upright water pump.An anaerobic septic tank has a filling material made of a large number of solids in a funnel-shaped tank. The sewage purification device S according to claim 1 is filled. The sewage purification device 6 according to claim 1, wherein the aerobic septic tank has a filler made of honeycomb core vertically arranged in the middle of the tank. The heating device Sewage purification device 7 according to claim 1, in which heating of hot water is generated in an anaerobic septic tank or a boiler using combustion gas as fuel; hot water in the heating device is heated by a solar water reservoir. Claim 2
Sewage purification equipment described in section
JP7191582A 1982-04-28 1982-04-28 Purifier for filthy water Pending JPS58189098A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP7191582A JPS58189098A (en) 1982-04-28 1982-04-28 Purifier for filthy water

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP7191582A JPS58189098A (en) 1982-04-28 1982-04-28 Purifier for filthy water

Publications (1)

Publication Number Publication Date
JPS58189098A true JPS58189098A (en) 1983-11-04

Family

ID=13474307

Family Applications (1)

Application Number Title Priority Date Filing Date
JP7191582A Pending JPS58189098A (en) 1982-04-28 1982-04-28 Purifier for filthy water

Country Status (1)

Country Link
JP (1) JPS58189098A (en)

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5112364B1 (en) * 1970-12-07 1976-04-19
JPS51117448A (en) * 1975-04-08 1976-10-15 Hitachi Plant Eng & Constr Co Ltd Bioldgical method of removing nitrogen frow waste water
JPS543866B1 (en) * 1970-09-08 1979-02-27

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS543866B1 (en) * 1970-09-08 1979-02-27
JPS5112364B1 (en) * 1970-12-07 1976-04-19
JPS51117448A (en) * 1975-04-08 1976-10-15 Hitachi Plant Eng & Constr Co Ltd Bioldgical method of removing nitrogen frow waste water

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