JP2565654Y2 - Septic tank - Google Patents
Septic tankInfo
- Publication number
- JP2565654Y2 JP2565654Y2 JP1991096412U JP9641291U JP2565654Y2 JP 2565654 Y2 JP2565654 Y2 JP 2565654Y2 JP 1991096412 U JP1991096412 U JP 1991096412U JP 9641291 U JP9641291 U JP 9641291U JP 2565654 Y2 JP2565654 Y2 JP 2565654Y2
- Authority
- JP
- Japan
- Prior art keywords
- treated water
- tank
- disinfectant
- overflow channel
- water
- 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 - Fee Related
Links
Landscapes
- Treatment Of Water By Oxidation Or Reduction (AREA)
- Treatment Of Biological Wastes In General (AREA)
Description
【0001】[0001]
【産業上の利用分野】本考案は、上流側からの処理水中
の汚泥を沈降させる沈殿槽、該沈殿槽からの上澄み液を
消毒する消毒槽を備え、前記沈殿槽から前記消毒槽への
左右越流路の合流部に、固形の消毒剤を処理水に溶解さ
せるための薬剤筒を立設配置する浄化槽に関する。The present invention comprises a sedimentation tank for sedimenting sludge in treated water from the upstream side, a disinfection tank for disinfecting the supernatant from the sedimentation tank, and a right and left passage from the sedimentation tank to the disinfection tank. The present invention relates to a septic tank in which a medicine tube for dissolving a solid disinfectant in treated water is provided upright at a junction of an overflow channel.
【0002】[0002]
【従来の技術】従来の浄化槽は、薬剤筒を立設配置する
越流路の前記合流部を越流路における前記合流部の上流
側及び下流側と同じ深さにしてあった。ところが、浄化
槽に流入する処理水の流量には変動があるので、このよ
うな構成では、例えば、処理水の流量が小さくなると、
越流路を流れる処理水の水深が全体に浅くなるため、越
流路の合流部に立設配置してある薬剤筒に収容された固
形消毒剤が処理水に対し充分な接触面積を保ち得なくな
ることがある。その結果、消毒材の溶解量が不足し、放
流するべき処理水における消毒剤の濃度が所定の消毒剤
濃度に達しない虞があった。又、例えば、季節によっ
て、処理水の温度が変わり、冬季には消毒剤の溶解速度
が落ち、処理水中に溶解する消毒剤が所定の濃度に達し
ない虞もあった。2. Description of the Related Art In a conventional septic tank, the merging portion of an overflow channel in which a medicine tube is vertically arranged is the same depth as the upstream and downstream sides of the merging portion in the overflow channel. However, since the flow rate of the treated water flowing into the septic tank fluctuates, in such a configuration, for example, when the flow rate of the treated water is reduced,
Since the depth of the treated water flowing through the overflow channel becomes shallower as a whole, the solid disinfectant contained in the medicine cylinder installed upright at the junction of the overflow channel can maintain a sufficient contact area with the treated water. May disappear. As a result, the amount of disinfectant dissolved may be insufficient, and the concentration of the disinfectant in the treated water to be discharged may not reach the predetermined disinfectant concentration. Further, for example, the temperature of the treated water changes depending on the season, and the disinfectant dissolution rate decreases in winter, so that the disinfectant dissolved in the treated water may not reach a predetermined concentration.
【0003】[0003]
【考案が解決しようとする課題】そこで、本考案の目的
は、例えば、処理水の流入量が減少したり、温度が下が
ることがあったとしても、放流するべき処理水の消毒剤
濃度が常に所定の濃度に達するようにすることができる
浄化槽を提供することにある。Therefore, an object of the present invention is to set the concentration of the disinfectant of the treated water to be discharged constantly even if the inflow of the treated water is reduced or the temperature is lowered. It is an object of the present invention to provide a septic tank capable of reaching a predetermined concentration.
【0004】[0004]
【課題を解決するための手段】この目的を達成するため
の本考案による浄化槽の特徴構成は、上流側からの処理
水中の汚泥を沈降させる沈殿槽、該沈殿槽からの上澄み
液を消毒する消毒槽を設け、前記沈殿槽から前記消毒槽
への左右越流路の合流部に、固形の消毒剤を処理水に溶
解させるための薬剤筒を立設配置すると共に、前記合流
部に、前記越流路における前記合流部の上流側及び下流
側よりも深く、処理水の滞留可能な滞留部を形成してあ
ることにある。In order to achieve the above object, the present invention has the following features: a septic tank for sedimenting sludge in treated water from an upstream side; and a disinfectant for disinfecting a supernatant from the sedimentation tank. the vessel is provided, at the confluence of the right and left overflow path to the disinfecting bath from the precipitation tank, together with the upright position the chemical cartridge for dissolving the solid disinfectant in the treated water, the merging section, the overflow A stagnant portion that can stagnate treated water is formed deeper than the upstream and downstream sides of the junction in the flow path.
【0005】[0005]
【作用】薬剤筒を立設配置する前記合流部を越流路にお
ける該合流部の上流側及び下流側よりも深く形成するこ
とによって、前記合流部をその上流側及び下流側と同じ
深さにしてあった、従来の構成による場合よりも、処理
液に対して薬剤筒をより深く浸漬する状態を常に保つこ
とができる。また、前記滞留部を設けてあるから、前記
薬剤筒は、前記越流路における処理液の流通深さより
も、深く前記処理液内に浸漬された状態を保つから、前
記処理液との十分な接触時間を確保でき、前記処理液の
流量が少なくなったとしても、その処理液は、前記滞留
部で一旦滞留して前記薬剤筒との接触が図られるように
なり、十分な時間接触できるようになり、前記薬筒は、
薬剤の溶解を十分確保することが出来るようになる。そ
の結果、処理水の流入量に変動があり、これが減少する
ことがあったとしても、薬剤筒に収容された固形の消毒
剤を常に処理水に充分接触させてこれに溶解させること
ができる。The merging portion where the medicine cylinder is erected is formed deeper than the upstream and downstream sides of the merging portion in the overflow channel so that the merging portion has the same depth as the upstream side and the downstream side. Thus, the state in which the medicine cylinder is immersed deeper in the treatment liquid can be always maintained as compared with the conventional configuration. In addition, since the retention section is provided,
The chemical cylinder is determined by the flow depth of the processing liquid in the overflow channel.
Also keeps the state immersed deeply in the processing solution,
A sufficient contact time with the treatment liquid can be secured, and the treatment liquid
Even if the flow rate is reduced, the processing liquid remains
So that it once stays in the part and makes contact with the medicine cylinder
And can be contacted for a sufficient time,
The dissolution of the drug can be sufficiently ensured. Its <br/> result, there is a variation in the inflow of process water, even this had to be reduced, dissolved thereto always sufficiently contact with the treatment water disinfectant solid contained in the chemical cartridge Can be done.
【0006】[0006]
【考案の効果】つまり、合流部を深く形成して処理水の
滞留可能な滞留部を形成し、ここに薬剤筒を立設させる
ようにするだけの簡単な改良で、固形の消毒剤の溶解効
率を向上させることができる。その結果、例えば、処理
水の流入量が減少したり、温度が下がることがあったと
しても、放流するべき処理水の消毒剤濃度が常に所定の
濃度に達するようにすることができる浄化槽を提供する
ことができた。[Effect of the invention] In other words, the junction is formed deep and the treated water
The dissolution efficiency of the solid disinfectant can be improved by a simple improvement in which a retaining portion capable of retaining is formed and the medicine cylinder is erected there. As a result, for example, even if the inflow of the treated water is reduced or the temperature is lowered, a septic tank can be provided so that the concentration of the disinfectant of the treated water to be discharged always reaches a predetermined concentration. We were able to.
【0007】[0007]
【実施例】以下、図面に基づいて本考案による浄化槽の
実施例を説明する。図1に示すように、この浄化槽は、
上流側の接触ばっ気槽Eの底部から移流する処理水中の
汚泥を沈降分離させる沈殿槽1、該沈殿槽1から移流す
る上澄み液を消毒する消毒槽2、消毒槽2からの処理水
を一旦受け入れて滞留させ、混合後放流するための放流
水貯槽3、放流水貯槽3内の処理水を放流管4を介して
放流する放流ポンプ5を備えている。図1〜図4に示す
ように、前記沈殿槽1から消毒槽2への左右越流路6の
合流部の深さは越流路6における前記合流部6の上流側
及び下流側よりも深く形成し処理水の滞留部に形成して
ある。また、合流部の中央付近に薬剤筒8を立設配置し
てある。合流部の幅は薬剤筒8の径よりも広く形成して
ある。薬剤筒8には固形の消毒剤を収容し、この消毒剤
が処理水と接触して溶解するように、薬剤筒8の底部に
近い周面に全周にわたって、処理水を出入させる複数の
長孔を形成してある。沈殿槽2の上澄み液は左右の越流
堰9に形成された複数のVノッチから越流路6内に越流
し、合流部で薬剤筒8内の消毒剤に接触して消毒剤を溶
解させながら消毒槽2内に流入するようにしてある。消
毒槽2には、溶解した消毒剤が処理水によく混ざり合う
ように、底部に流路を確保しながら隔壁10を設け、消
毒槽2に流入した処理水が、短絡することなく、この隔
壁10の下を通り、溢流口11から放流水貯槽3に溢流
するようしてある。放流水貯槽3には、図1に示すよう
に、水位を自動的に管理するため、フロート12を用
い、水面が上限水位HWLまで上がると放流ポンプ5が
稼働し、放流管4を介して処理水が放流され、水面が下
限水位LWLまで下がると放流ポンプが停止するように
してある。放流ポンプ5の容量は、浄化槽の処理水流入
量よりも大きくすると共に、放流ポンプで揚水した処理
水の一部は循環路14を介して放流貯槽内に戻し、放流
水貯槽内の処理水が充分混合され、処理水の消毒剤濃度
の時間的、空間的ばらつきが極力抑えられるようにして
ある。前記上限水位HWLは前記溢流口11よりも低く
設定してあり、溢流口11は前記越流路6の出口よりも
低いレベルに設けてある。図中15は循環水の流量を調
整することにより放流ポンプ5の見かけのポンプ容量を
調整するための流量調整バルブである。前記固形の消毒
剤は、例えば、有効塩素含有量の高いイソシアヌール酸
有機系塩素剤を使用することができる。この消毒剤は、
広く用いられる次亜塩素酸カルシウムと比較して、処理
水に浸漬しても膨潤しにくいため、薬剤筒に収容された
薬剤の下部が処理水に溶解しても上部の薬剤が膨潤して
下に落ちてこない所謂ブリッジ現象を起こすことがない
という点で優れているが、溶解速度が小さいため、従来
の浄化槽では、処理水の流入量に変動がある場合等、処
理水の消毒剤濃度が所定の濃度に達しない虞があった。
しかし、上記の構成によれば、この固形の消毒剤を用い
て前記ブリッジ現象を解消することができながら、例え
ば、浄化槽への処理水の流入量に変動があっても、処理
水の消毒剤濃度が常に所定の濃度に達するようにするこ
とができる。BRIEF DESCRIPTION OF THE DRAWINGS FIG. 1 is a perspective view of a septic tank according to the present invention. As shown in FIG. 1, this septic tank is
A sedimentation tank 1 for sedimentation and separation of the sludge in the treated water flowing from the bottom of the upstream contact aeration tank E, a disinfecting tank 2 for disinfecting the supernatant liquid transferred from the sedimentation tank 1, and the treated water from the disinfecting tank 2 once. A discharge water storage tank 3 for receiving and retaining the mixed water and discharging after mixing, and a discharge pump 5 for discharging the treated water in the discharge water storage tank 3 through a discharge pipe 4 are provided. As shown in FIGS. 1 to 4, the depth of the junction of the right and left overflow channel 6 from the sedimentation tank 1 to the disinfection tank 2 is deeper than the upstream and downstream sides of the junction 6 in the overflow channel 6. Formed and formed in the stagnation area of the treated water
is there. Further , a medicine tube 8 is provided upright near the center of the junction. The width of the junction is formed wider than the diameter of the medicine tube 8. The medicine tube 8 contains a solid disinfectant, and a plurality of lengthwise dispensers for the treated water to enter and exit over the entire circumference near the bottom of the medicine tube 8 so that the disinfectant comes into contact with the treated water and dissolves. A hole is formed. The supernatant of the sedimentation tank 2 flows into the overflow channel 6 from a plurality of V-notches formed in the right and left overflow weirs 9, and contacts the disinfectant in the medicine tube 8 at the junction to dissolve the disinfectant. While flowing into the disinfection tank 2. The disinfecting tank 2 is provided with a partition wall 10 while securing a flow path at the bottom so that the dissolved disinfectant mixes well with the treated water. 10, the water overflows from the overflow port 11 to the discharge water storage tank 3. As shown in FIG. 1, the discharge water storage tank 3 uses a float 12 to automatically manage the water level. When the water level rises to the upper limit water level HWL, the discharge pump 5 is operated, and the water is discharged through the discharge pipe 4. When the water is discharged and the water level falls to the lower limit water level LWL, the discharge pump is stopped. The capacity of the discharge pump 5 is made larger than the inflow of the treated water into the septic tank, and a part of the treated water pumped up by the discharge pump is returned to the discharge tank via the circulation path 14, and the treated water in the discharged water tank is discharged. The disinfectant concentration of the treated water is sufficiently mixed so as to minimize temporal and spatial variations in the disinfectant concentration. The upper limit water level HWL is set lower than the overflow port 11, and the overflow port 11 is provided at a level lower than the outlet of the overflow channel 6. In the figure, reference numeral 15 denotes a flow rate adjusting valve for adjusting the apparent pump capacity of the discharge pump 5 by adjusting the flow rate of the circulating water. As the solid disinfectant, for example, an isocyanuric acid organic chlorine agent having a high effective chlorine content can be used. This disinfectant
Compared to calcium hypochlorite, which is widely used, it does not easily swell when immersed in treated water, so even if the lower part of the drug contained in the drug cylinder dissolves in the treated water, the upper drug swells. It is excellent in that it does not cause a so-called bridging phenomenon that does not fall into the tank. There was a possibility that the concentration did not reach the predetermined concentration.
However, according to the above configuration, while the bridging phenomenon can be eliminated by using the solid disinfectant, for example, even if there is a change in the inflow amount of the treated water into the septic tank, the disinfectant of the treated water The concentration can always reach a predetermined concentration.
【0008】尚、実用新案登録請求の範囲の項に図面と
の対照を便利にするために符号を記すが、該記入により
本考案は添付図面の構成に限定されるものではない。[0008] In the claims of the utility model registration, reference numerals are written for convenience of comparison with the drawings, but the present invention is not limited to the configuration of the attached drawings by the entry.
【図1】実施例における浄化槽の要部を示す説明図FIG. 1 is an explanatory view showing a main part of a septic tank in an embodiment.
【図2】越流路付近の斜視図FIG. 2 is a perspective view of the vicinity of an overflow channel.
【図3】越流路の合流部付近の横断面図FIG. 3 is a cross-sectional view of the vicinity of the junction of the overflow channel.
【図4】越流路の合流部付近の縦断面図FIG. 4 is a vertical cross-sectional view of the vicinity of the junction of the overflow channel.
1 沈澱槽 2 消毒槽 6 越流路 8 薬剤筒 Reference Signs List 1 sedimentation tank 2 disinfection tank 6 overflow channel 8 drug cylinder
───────────────────────────────────────────────────── フロントページの続き (51)Int.Cl.6 識別記号 庁内整理番号 FI 技術表示箇所 C02F 1/50 550 C02F 1/50 550B 560 560H 1/76 1/76 A (72)考案者 北井 良人 滋賀県甲賀郡甲西町高松2番地の1 株 式会社クボタ 滋賀工場内 (72)考案者 本田 和之 滋賀県甲賀郡甲西町高松2番地の1 株 式会社クボタ 滋賀工場内 (56)参考文献 実開 平3−75893(JP,U) 実開 昭51−9560(JP,U)──────────────────────────────────────────────────続 き Continuation of the front page (51) Int.Cl. 6 Identification number Agency reference number FI Technical indication location C02F 1/50 550 C02F 1/50 550B 560 560H 1/76 1/76 A (72) Inventor Kitai Good person 2 in Takamatsu, Kosai-cho, Koga-cho, Shiga Prefecture Inside the Kubota Shiga Plant (72) Inventor Kazuyuki Honda 2 in Takamatsu, Kosai-cho, Koga-gun, Shiga Prefecture Inside Kubota Shiga Plant (56) Reference Literature Japanese Utility Model Hei 3-75893 (JP, U) Japanese Utility Model Showa 51-9560 (JP, U)
Claims (1)
る沈殿槽(1)、該沈殿槽(1)からの上澄み液を消毒
する消毒槽(2)を備え、前記沈殿槽(1)から前記消
毒槽(2)への左右越流路(6)の合流部に、固形の消
毒剤を処理水に溶解させるための薬剤筒(8)を立設配
置する浄化槽であって、 前記合流部に、前記越流路(6)における前記合流部の
上流側及び下流側よりも深く、処理水の滞留可能な滞留
部を形成してある浄化槽。1. A sedimentation tank (1) for sedimenting sludge in treated water from an upstream side, and a disinfection tank (2) for disinfecting a supernatant liquid from the sedimentation tank (1). A purifying tank in which a medicine tube (8) for dissolving a solid disinfectant in treated water is provided upright at a junction of a right and left overflow channel (6) to the disinfection tank (2), in the overflow channel deeper than the upstream side and downstream side of the merging portion of the (6), the residence possible accumulation of treated water
Septic tank with a part formed.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1991096412U JP2565654Y2 (en) | 1991-11-25 | 1991-11-25 | Septic tank |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP1991096412U JP2565654Y2 (en) | 1991-11-25 | 1991-11-25 | Septic tank |
Publications (2)
Publication Number | Publication Date |
---|---|
JPH0544293U JPH0544293U (en) | 1993-06-15 |
JP2565654Y2 true JP2565654Y2 (en) | 1998-03-18 |
Family
ID=14164260
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP1991096412U Expired - Fee Related JP2565654Y2 (en) | 1991-11-25 | 1991-11-25 | Septic tank |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2565654Y2 (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011092898A (en) * | 2009-10-30 | 2011-05-12 | Jfe Engineering Corp | Ballast water treatment apparatus |
Family Cites Families (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS519560U (en) * | 1974-07-08 | 1976-01-23 | ||
JP3075893U (en) * | 2000-08-28 | 2001-03-06 | 株式会社マルハマ | Vehicle anti-theft device |
-
1991
- 1991-11-25 JP JP1991096412U patent/JP2565654Y2/en not_active Expired - Fee Related
Also Published As
Publication number | Publication date |
---|---|
JPH0544293U (en) | 1993-06-15 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
LAPS | Cancellation because of no payment of annual fees |