JPS6150678B2 - - Google Patents
Info
- Publication number
- JPS6150678B2 JPS6150678B2 JP52134304A JP13430477A JPS6150678B2 JP S6150678 B2 JPS6150678 B2 JP S6150678B2 JP 52134304 A JP52134304 A JP 52134304A JP 13430477 A JP13430477 A JP 13430477A JP S6150678 B2 JPS6150678 B2 JP S6150678B2
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- tank
- flow rate
- digestion
- sewage
- 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
Links
- 239000010802 sludge Substances 0.000 claims description 41
- 241001148470 aerobic bacillus Species 0.000 claims description 17
- 239000010865 sewage Substances 0.000 claims description 16
- 238000005273 aeration Methods 0.000 claims description 15
- 230000029087 digestion Effects 0.000 claims description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 10
- 235000015097 nutrients Nutrition 0.000 claims description 8
- 239000002351 wastewater Substances 0.000 claims description 8
- 238000002386 leaching Methods 0.000 claims description 7
- 241001478887 unidentified soil bacteria Species 0.000 claims description 7
- 238000000034 method Methods 0.000 claims description 6
- 238000000746 purification Methods 0.000 claims description 6
- 239000006228 supernatant Substances 0.000 claims description 4
- 230000000694 effects Effects 0.000 claims description 3
- 238000004062 sedimentation Methods 0.000 claims description 3
- 239000002689 soil Substances 0.000 claims description 3
- 239000003344 environmental pollutant Substances 0.000 claims description 2
- 230000001590 oxidative effect Effects 0.000 claims description 2
- 231100000719 pollutant Toxicity 0.000 claims description 2
- 230000000644 propagated effect Effects 0.000 claims description 2
- 239000002002 slurry Substances 0.000 description 3
- 230000005484 gravity Effects 0.000 description 2
- 239000011148 porous material Substances 0.000 description 2
- 238000004659 sterilization and disinfection Methods 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000000428 dust Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000001802 infusion Methods 0.000 description 1
- 239000002957 persistent organic pollutant Substances 0.000 description 1
- 238000004064 recycling Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
Classifications
-
- Y—GENERAL 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
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W10/00—Technologies for wastewater treatment
- Y02W10/10—Biological treatment of water, waste water, or sewage
Landscapes
- Activated Sludge Processes (AREA)
- Treatment Of Sludge (AREA)
Description
【発明の詳細な説明】
従来の有機性汚水の浄化方法は、曝気槽におい
て、好気性菌の作用により、汚染物質を酸化分解
した後、沈澱槽において、上澄水と、増殖した好
気性菌の集団、すなわち汚泥とに重力分離し、上
澄水を外部へ放流し、一方汚泥は、一部を好気性
菌の育生栄養源として曝気槽に返送し、残部を汚
泥貯留槽へ一旦貯留した後、産業廃棄物として処
分していた。[Detailed Description of the Invention] In the conventional organic wastewater purification method, pollutants are oxidized and decomposed by the action of aerobic bacteria in an aeration tank, and then supernatant water and grown aerobic bacteria are mixed in a settling tank. The sludge is separated by gravity into sludge, and the supernatant water is discharged to the outside, while a portion of the sludge is returned to the aeration tank as a nutrient source for aerobic bacteria, and the remainder is temporarily stored in the sludge storage tank. It was disposed of as industrial waste.
本発明は、貯留槽を兼ねる汚泥消化槽におい
て、余剰汚泥に土壌菌を添加して空気を供給し、
好気性菌の活性を保ちつつ、汚泥の消化を促進さ
せ、曝気槽に流入する汚水中の好気性菌の育生栄
養源が著しく不足した時に、この余剰汚泥を供給
して、曝気槽における好気性菌と育生栄養源の減
少を補い、汚水の浄化を常に良好に保たせるとと
もに、最終的には、従来廃棄処分していた余剰汚
泥を、汚水浄化装置内において消化して、外部に
排出しないようにした有機性汚水の浄化方法に関
するもで、以下添付の図面に基いて具体的に説明
する。 The present invention involves adding soil bacteria to excess sludge and supplying air in a sludge digestion tank that also serves as a storage tank.
It promotes the digestion of sludge while maintaining the activity of aerobic bacteria, and when there is a significant shortage of nutrients for the growth of aerobic bacteria in the wastewater flowing into the aeration tank, this excess sludge is supplied to improve the aerobic conditions in the aeration tank. In addition to compensating for the decrease in bacteria and nurturing sources and maintaining good sewage purification, the system ultimately digests excess sludge, which was previously disposed of, in the sewage purification equipment and prevents it from being discharged outside. The present invention relates to a method for purifying organic wastewater, and will be specifically explained below based on the attached drawings.
図示を省略した前処理装置により、油と塵芥の
除去された汚水は、流入管1を経て、流量調整槽
2に流入する。 The wastewater from which oil and dust have been removed by a pretreatment device (not shown) flows into a flow rate adjustment tank 2 through an inflow pipe 1 .
流量調整槽の底部には、多数の噴気孔3……が
穿設された噴気管4が配設され、噴気管4は、流
量調整槽2上に設置された第1ブロアー5に接続
されている。 A fumarole pipe 4 in which a large number of fumarole holes 3 are bored is arranged at the bottom of the flow rate adjustment tank, and the fumarole pipe 4 is connected to a first blower 5 installed on the flow rate adjustment tank 2. There is.
流量調整槽2に一時貯留された汚水中の好気性
菌は、噴気孔3……より噴出する空気により、有
機性汚染物質を酸化分解しながら増殖する。 Aerobic bacteria in the wastewater temporarily stored in the flow rate adjustment tank 2 multiply while oxidizing and decomposing organic pollutants by the air blown out from the fumaroles 3.
上記汚水は、流量調整槽2上に設置された汚水
ポンプ6により、流量調整装置7と汚水管8を経
て、次段の曝気槽9の中央に設置された内筒10
に流入する。 The sewage is pumped through a sewage pump 6 installed on the flow rate adjustment tank 2, passes through a flow rate adjustment device 7 and a sewage pipe 8, and then passes through an inner cylinder 10 installed in the center of the next stage aeration tank 9.
flows into.
内筒10の下端は、曝気槽9の底面により若干
上方において下向ラツパ状に拡張し、同じく上端
は、ほぼ汚水面においてラツパ状に上向拡張して
いる。 The lower end of the inner cylinder 10 expands in a downward truss shape slightly above the bottom surface of the aeration tank 9, and similarly, the upper end expands upward in a truss shape almost at the dirty water surface.
内筒10の上端拡張部11の若干上方には、下
向円錐状をなすとともに、拡張部11と同軸をな
し、かつ下面に適宜の突条12……が固設された
撤布板13が、曝気槽9の上面中央部に配置され
たモーター14の軸に装着吊支されている。 Slightly above the upper end expanded portion 11 of the inner cylinder 10, there is a removal plate 13 which has a downward conical shape, is coaxial with the expanded portion 11, and has appropriate protrusions 12 fixed on its lower surface. , is attached and suspended from the shaft of a motor 14 disposed at the center of the upper surface of the aeration tank 9.
この撤布板13の回転により、内筒10上部の
汚水は、斜上外方に激しく飛散させられ、広い面
積において空気と接触すると同時に、内筒10の
下端より汚水を吸入するので、曝気槽9内の汚水
は、矢示するように循環する。 By this rotation of the removal plate 13, the sewage in the upper part of the inner cylinder 10 is violently scattered diagonally upward and outward, and at the same time it comes into contact with air over a wide area, and at the same time sucks the sewage from the lower end of the inner cylinder 10. The wastewater inside 9 circulates as shown by the arrow.
このようにして、汚水は曝気槽9において十分
に曝気され、空気と好気性菌により酸化分解して
浄化され、増殖した好気性菌は汚泥となり、濁水
管15を経て、次段の沈澱槽16の上部の整流筒
17に流入する。 In this way, the sewage is sufficiently aerated in the aeration tank 9, oxidized and decomposed by the air and aerobic bacteria, and purified.The aerobic bacteria that proliferate become sludge, which passes through the turbid water pipe 15 to the next settling tank 16. flows into the rectifying tube 17 at the top of the tube.
整流筒17に流入した濁水が緩速で下降する間
に、汚泥は重力分離されて、沈澱槽16の底部に
沈降する。 While the turbid water flowing into the straightening tube 17 descends slowly, the sludge is separated by gravity and settles to the bottom of the settling tank 16.
沈降した汚泥は、沈澱槽16の底面上に設置さ
れ、沈澱槽16上のモーター18により緩速で回
転させられる、湾曲した集泥翼19により、底部
中央に掻き集められる。 The settled sludge is collected at the center of the bottom by curved sludge collecting blades 19 installed on the bottom surface of the settling tank 16 and rotated at a slow speed by a motor 18 on the settling tank 16.
汚泥の除かれた上澄水は、整流筒17の外側面
上部に設けられた排水樋20より、送水管21を
経て、次段の消毒槽22に流入して殺菌され、排
水管23より放流される。 The supernatant water from which sludge has been removed flows from a drain gutter 20 provided at the upper part of the outer surface of the rectifier cylinder 17 through a water pipe 21 to a disinfection tank 22 at the next stage, where it is sterilized and then discharged from a drain pipe 23. Ru.
沈澱槽16に沈降した汚泥は、底底部中央に接
続された第1送泥ポンプ24により、第1送泥管
25を経て、その一部は、好気性菌の補充と育生
用の栄養源として、上記曝気槽aの内筒10に返
送され、残部は、次記する汚泥貯留槽を兼ねる汚
泥消化槽26に送られる。 The sludge settled in the sedimentation tank 16 is passed through the first sludge pipe 25 by the first sludge pump 24 connected to the center of the bottom, and a part of it is used as a nutrient source for replenishing aerobic bacteria and growing them. , is returned to the inner cylinder 10 of the aeration tank a, and the remainder is sent to a sludge digestion tank 26 which also serves as a sludge storage tank, which will be described below.
消化槽26の底部には、多数の噴気孔27……
が穿設された噴気管28が配設され、噴気管28
は、消化槽26上に配設された第2ブロアー29
に接続されている。 At the bottom of the digestion tank 26, there are many fumaroles 27...
A fumarole pipe 28 is provided, and the fumarole pipe 28 is
is a second blower 29 disposed on the digestion tank 26
It is connected to the.
消化槽26の内部には、上板近くより底板近く
に達する有底円筒状の所要数の浸出箱30……が
配設され、各浸出箱30には、多数の細孔31…
…が穿設されている。 Inside the digestion tank 26, a required number of leaching boxes 30, each having a cylindrical shape with a bottom and reaching closer to the bottom plate than near the top plate, are arranged, and each leaching box 30 has a large number of pores 31...
... has been drilled.
各浸出箱30の内面には、たとえば帆布等より
なる浸出袋32が貼設され、浸出袋32の内部に
は、土壌菌の繁殖した土壌33が満たされ、土壌
菌が汚泥中に浸出するようになつている。 A leaching bag 32 made of, for example, canvas is attached to the inner surface of each leaching box 30, and the inside of the leaching bag 32 is filled with soil 33 in which soil bacteria have propagated, so that the soil bacteria can leach into the sludge. It's getting old.
消化槽26内に貯留された余剰汚泥中の好気性
菌は、上記噴気孔27……より噴出する空気によ
り、汚泥を栄養源として、消化しつつ活性が保た
れるが、この作用は、さらに、浸出する土壌菌の
協力により促進される。 The aerobic bacteria in the excess sludge stored in the digestion tank 26 are kept active while being digested using the sludge as a nutrient source by the air blown out from the fumaroles 27. , facilitated by the cooperation of leaching soil bacteria.
この活性汚泥は、上述の汚水浄化装置に流入す
る汚水中の有機性物質が著しく減少して、曝気槽
9内の好気性菌と育生栄養源が不足した場合に、
随時、消化槽26上に配置された第2送泥ポンプ
34により、第2送泥管35を経て、流量調整槽
2に返送される。 This activated sludge is produced when organic substances in the sewage flowing into the above-mentioned sewage purification device are significantly reduced and aerobic bacteria and growth nutrients in the aeration tank 9 are insufficient.
From time to time, the second slurry pump 34 disposed on the digestion tank 26 returns the slurry to the flow rate adjustment tank 2 via the second slurry pipe 35 .
本発明の方法は、上述のようにして、沈澱槽1
6より排出される余剰汚泥を、消化槽26におい
て、好気性菌の活性を保ちながら、土壌菌の協力
により消化しつつ貯留し、必要に応じて再利用す
るので、流入する汚水の組成が著しく変動して
も、曝気槽9内の好気性菌と育生栄養源の量は適
正に保たれ、常時良好に汚水を浄化しうるのみな
らず、余剰汚泥は、循環使用する過程において、
次第に消化されるので、汚泥を外部に排出するこ
となく処分することができるという利点がある。 In the method of the present invention, as described above, the settling tank 1
Excess sludge discharged from 6 is stored in the digestion tank 26 while maintaining the activity of aerobic bacteria and digested with the cooperation of soil bacteria, and is reused as necessary, so the composition of the inflowing sewage is significantly reduced. Even if the amount of aerobic bacteria and growth nutrients in the aeration tank 9 fluctuates, the amount of aerobic bacteria and growth nutrients in the aeration tank 9 can be maintained at an appropriate level, and not only can wastewater be purified well at all times, but also surplus sludge can be used in the process of recycling.
Since the sludge is gradually digested, it has the advantage that the sludge can be disposed of without being discharged to the outside.
第1図は、本発明の方法を実施する装置の一例
を示す概略図、第2図は、浸出箱の拡大縦断面図
である。
1……流入管、2……流量調整槽、3……噴気
孔、4……噴気管、5……ブロアー、6……汚水
ポンプ、7……流量調整装置、8……汚水管、9
……曝気槽、10……内筒、11……拡張部、1
2……突条、13……撤布板、14……モータ
ー、15……濁水管、16……沈澱槽、17……
整流筒、18……モーター、19……集泥翼、2
0……排水樋、21……送水管、22……消毒
槽、23……排水管、24……送泥ポンプ、25
……送泥管、26……消化槽、27……噴気孔、
28……噴気管、29……ブロアー、30……浸
出箱、31……細孔、32……浸出袋、33……
土壌、34……送泥ポンプ、35……送泥管。
FIG. 1 is a schematic diagram showing an example of an apparatus for carrying out the method of the present invention, and FIG. 2 is an enlarged longitudinal sectional view of an infusion box. 1... Inflow pipe, 2... Flow rate adjustment tank, 3... Fumarole, 4... Fumarole pipe, 5... Blower, 6... Sewage pump, 7... Flow rate adjustment device, 8... Sewage pipe, 9
... Aeration tank, 10 ... Inner cylinder, 11 ... Expansion section, 1
2... Projection, 13... Removal plate, 14... Motor, 15... Turbid water pipe, 16... Sedimentation tank, 17...
Straightening tube, 18...Motor, 19...Sludge collecting blade, 2
0... Drain gutter, 21... Water pipe, 22... Disinfection tank, 23... Drain pipe, 24... Sludge pump, 25
...sludge pipe, 26...digestion tank, 27...fumarole,
28... Fumarole pipe, 29... Blower, 30... Leach box, 31... Pore, 32... Leach bag, 33...
Soil, 34...Sludge pump, 35...Sludge pipe.
Claims (1)
を調整した後、次段の曝気槽に導いて曝気し、好
気性菌の作用により、汚染物質を酸化分解して生
成した汚泥を、次段の沈澱槽において沈降させ
て、上澄水のみを殺菌して放流し、沈降汚泥の一
部を、曝気槽に返送するとともに、沈降汚泥の残
部を、汚泥の貯留を兼ねる汚泥消化槽に移送し、
消化槽内に配設され、かつ土壌菌の繁殖した土壌
が満たされた浸出箱より土壌菌を供給し、十分に
空気と接触させて、汚泥を消化させつつ好気性菌
の活性を保たせ、流入する汚水中に好気性菌の育
生栄養源が不足した場合に、消化槽内の活性汚泥
を上記流量調整槽に返送して、汚水の浄化を常時
良好に保たせるとともに、余剰汚泥を外部に排出
することなく、消化させることを特徴とする有機
性汚水浄化方法。1 After first storing organic sewage in a flow rate adjustment tank and adjusting the flow rate, it is led to the next stage aeration tank and aerated, and the sludge produced by oxidizing and decomposing pollutants through the action of aerobic bacteria is transferred to the next stage. The sludge is allowed to settle in the sedimentation tank of the stage, and only the supernatant water is sterilized and discharged. A part of the settled sludge is returned to the aeration tank, and the remaining part of the settled sludge is transferred to the sludge digestion tank that also serves as sludge storage. ,
Soil bacteria are supplied from a leaching box placed in the digestion tank and filled with soil in which soil bacteria have propagated, and brought into sufficient contact with air to digest the sludge while maintaining the activity of aerobic bacteria. When there is a lack of nutrients for aerobic bacteria in the inflowing sewage, the activated sludge in the digestion tank is returned to the flow rate adjustment tank to maintain good sewage purification at all times, and the excess sludge is removed to the outside. An organic wastewater purification method characterized by digestion without discharge.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13430477A JPS5468056A (en) | 1977-11-09 | 1977-11-09 | Method of purifying organic sewage |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP13430477A JPS5468056A (en) | 1977-11-09 | 1977-11-09 | Method of purifying organic sewage |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS5468056A JPS5468056A (en) | 1979-05-31 |
JPS6150678B2 true JPS6150678B2 (en) | 1986-11-05 |
Family
ID=15125149
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP13430477A Granted JPS5468056A (en) | 1977-11-09 | 1977-11-09 | Method of purifying organic sewage |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS5468056A (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3591491A (en) * | 1968-10-04 | 1971-07-06 | Edmund G Smith | Method for the treatment of aqueous wastes |
US3904518A (en) * | 1970-01-14 | 1975-09-09 | Du Pont | Waste water treatment process |
JPS5112312U (en) * | 1974-07-15 | 1976-01-29 |
-
1977
- 1977-11-09 JP JP13430477A patent/JPS5468056A/en active Granted
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3591491A (en) * | 1968-10-04 | 1971-07-06 | Edmund G Smith | Method for the treatment of aqueous wastes |
US3904518A (en) * | 1970-01-14 | 1975-09-09 | Du Pont | Waste water treatment process |
JPS5112312U (en) * | 1974-07-15 | 1976-01-29 |
Also Published As
Publication number | Publication date |
---|---|
JPS5468056A (en) | 1979-05-31 |
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