JPH03245899A - Method for preventing blocking of flow of liquid in purifying tank - Google Patents
Method for preventing blocking of flow of liquid in purifying tankInfo
- Publication number
- JPH03245899A JPH03245899A JP2043764A JP4376490A JPH03245899A JP H03245899 A JPH03245899 A JP H03245899A JP 2043764 A JP2043764 A JP 2043764A JP 4376490 A JP4376490 A JP 4376490A JP H03245899 A JPH03245899 A JP H03245899A
- Authority
- JP
- Japan
- Prior art keywords
- purifying tank
- sewage
- liquid
- tank
- primary
- 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
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 6
- 230000000903 blocking effect Effects 0.000 title 1
- 239000000463 material Substances 0.000 claims abstract description 15
- 238000005273 aeration Methods 0.000 claims abstract description 14
- 244000005700 microbiome Species 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 2
- 238000009395 breeding Methods 0.000 claims description 2
- 230000001488 breeding effect Effects 0.000 claims description 2
- 229910052760 oxygen Inorganic materials 0.000 claims description 2
- 239000001301 oxygen Substances 0.000 claims description 2
- 239000010865 sewage Substances 0.000 abstract description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 4
- 238000011282 treatment Methods 0.000 abstract description 2
- 241000894006 Bacteria Species 0.000 abstract 2
- 239000008213 purified water Substances 0.000 abstract 1
- 230000007423 decrease Effects 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 238000009825 accumulation Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 239000010840 domestic wastewater Substances 0.000 description 1
- 239000010797 grey water Substances 0.000 description 1
- 239000010800 human waste Substances 0.000 description 1
- 238000011221 initial treatment Methods 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000012827 research and development Methods 0.000 description 1
- 239000002351 wastewater 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
- Biological Treatment Of Waste Water (AREA)
- Treatment Of Biological Wastes In General (AREA)
Abstract
Description
【発明の詳細な説明】
従来、し尿や雑排水を生物化学的に処理している一般浄
化槽や小型合併浄化槽に於いて、流入される汚水は第一
次処理として腐敗および測成分離か行はれて第二次の曝
気室に送られる。[Detailed Description of the Invention] Conventionally, in general septic tanks and small-sized combined septic tanks that biochemically treat human waste and gray water, the incoming sewage is subjected to putrefaction and chemical separation as the primary treatment. and sent to the secondary aeration room.
送られた汚水中の有機物質は曝気室内に形成された微生
物に吸着され次いで酸化分解されて逐次浄水化されて行
く。Organic substances in the sent wastewater are adsorbed by microorganisms formed in the aeration chamber, and are then oxidized and decomposed to gradually purify the water.
此の間、微生物の温床として、充填されている接触材に
は、送られてきた汚水中の有機物や浮遊物で、BODの
高いはと表面にスケール溜りを起こしやすく、遂には閉
塞状態にまで発展する。During this time, as a breeding ground for microorganisms, the contact material filled with organic matter and suspended matter in the sewage is likely to cause scale buildup on the high BOD surface, eventually leading to a state of blockage. .
本発明は、この現象を無くするため、充填する接触材の
大きさを、槽液のBOD濃度に応して小さくして行く。In order to eliminate this phenomenon, the present invention reduces the size of the contact material to be filled in accordance with the BOD concentration of the tank liquid.
例えば大形浄化槽で曝気室か
第一次
第二次
第三次
と設置される場合、第一次には大形の接触材を、第二次
には中形、第三次には小形のものを、小型合併浄(ヒ槽
の曝気室では同し室内に於いて下から上へ槽液の流れと
同し方向に段々と接触材のサイズを小さく並へて行く仕
組みである。For example, if a large septic tank is installed with an aeration room or a primary, secondary, and tertiary stage, a large contact material is placed in the first stage, a medium-sized one in the second, and a small one in the tertiary. In the aeration chamber of a small combined purification tank, the size of the contacting material is gradually reduced and arranged in the same room from bottom to top in the same direction as the flow of tank liquid.
即ちBOD (生物化学的酸素要求量)か低くなるに従
って接触材の大きさも段々と小さくなっているのである
。That is, as the BOD (biochemical oxygen demand) decreases, the size of the contact material gradually decreases.
これを図面で説明すると
浄化槽(第一図)の流入口(1)より取入れられた汚水
(2)は第一次(3)第二次(4)の腐敗(分離)室、
流量調整槽(5)等をへて第一次曝気室(6)、第二次
曝気室(7)及び三次曝気室(8)で浄水化され、処理
室等を経て放水される。To explain this with a drawing, the sewage (2) taken in from the inlet (1) of the septic tank (Figure 1) is transferred to the primary (3) and secondary (4) septic (separation) chambers.
The water passes through a flow rate adjustment tank (5), etc., is purified in a primary aeration chamber (6), a secondary aeration chamber (7), and a tertiary aeration chamber (8), and is discharged through a treatment chamber, etc.
この際、夫々の曝気室内では汚水(2)中のa接物質を
分解摂取して浄水化する微生物の温床に品種の接触材(
9)(10)(11)を充填している。At this time, in each aeration room, contact materials of various types (
9) Filled with (10) and (11).
これらの接触材の形状を第二図、第三図 第四図の様に
大きさを変えて充填する。The shapes of these contact materials are changed and filled as shown in Figures 2, 3, and 4.
本発明を、現在市販で設置されている人形浄化装置や一
般家庭浄化槽に利用すれば、接触材表面のスケール溜り
による汚水の閉塞状態かなくなり、従って目詰まり取り
の通水管等の設置を皆無又は規樽小さくして設備費及び
稼働後の維持費を少なくする事か出来る。If the present invention is applied to doll purifiers and general household septic tanks that are currently installed on the market, there will be no clogging of sewage due to scale accumulation on the surface of the contact material, and therefore there will be no need to install water pipes, etc. for unclogging. It is possible to reduce equipment costs and maintenance costs after operation by making the barrel smaller.
本発明は、文明生活環境造りのなかで、最も取り残され
ている生活排水、大きくは都市開発の、河川浄化の最大
拠点である理想的な浄化槽の研究開発に大なる貢献をす
るものである。The present invention makes a great contribution to the research and development of ideal septic tanks, which are the most important source of domestic wastewater, which is the most neglected area in the creation of a civilized living environment, and which is the greatest base for river purification in urban development.
添付図は、本発明の全体略図及び充填接触材の略図であ
る。
第一図・・・−全体略図
1・・汚水の流入口
2・・・汚水
3・・第一次腐敗(分@)室
4・・・第二次腐敗(分子a)室
5・・・流量調整槽
6・・・第一次曝気室
7・・・第二次曝気室
8・・・・第三次曝気室
9・・−・−大形接触材
10・・・・中形接触材
11・・・小形接触材
手続補正書
平成2年6月25日The accompanying figures are an overall schematic representation of the invention and a diagrammatic representation of the filled contact material. Figure 1... - Overall schematic diagram 1... Sewage inlet 2... Sewage 3... Primary putrefaction (minute@) chamber 4... Secondary putrefaction (molecule a) chamber 5... Flow rate adjustment tank 6... Primary aeration chamber 7... Secondary aeration chamber 8... Tertiary aeration chamber 9... - Large contact material 10... Medium contact material 11...Small contact material procedural amendment June 25, 1990
Claims (1)
接触材の形状を槽液が示すBOD(生物化学的酸素要求
量)の濃度変化によって変えて行く仕組みA mechanism that changes the shape of a cylindrical contact material filled in the aeration chamber of a septic tank as a breeding ground for microorganisms according to changes in the concentration of BOD (biochemical oxygen demand) shown by the tank liquid.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2043764A JPH03245899A (en) | 1990-02-23 | 1990-02-23 | Method for preventing blocking of flow of liquid in purifying tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2043764A JPH03245899A (en) | 1990-02-23 | 1990-02-23 | Method for preventing blocking of flow of liquid in purifying tank |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH03245899A true JPH03245899A (en) | 1991-11-01 |
Family
ID=12672825
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2043764A Pending JPH03245899A (en) | 1990-02-23 | 1990-02-23 | Method for preventing blocking of flow of liquid in purifying tank |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH03245899A (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS61245895A (en) * | 1985-04-23 | 1986-11-01 | Furukawa Electric Co Ltd:The | Filter material for fluid filter |
JPS62237998A (en) * | 1986-04-07 | 1987-10-17 | Shimizu Constr Co Ltd | Reactor for biofilter |
JPS6366199B2 (en) * | 1981-03-31 | 1988-12-20 | Snow Brand Milk Prod Co Ltd |
-
1990
- 1990-02-23 JP JP2043764A patent/JPH03245899A/en active Pending
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS6366199B2 (en) * | 1981-03-31 | 1988-12-20 | Snow Brand Milk Prod Co Ltd | |
JPS61245895A (en) * | 1985-04-23 | 1986-11-01 | Furukawa Electric Co Ltd:The | Filter material for fluid filter |
JPS62237998A (en) * | 1986-04-07 | 1987-10-17 | Shimizu Constr Co Ltd | Reactor for biofilter |
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