JP2003053360A - Combined type sewage treatment system - Google Patents
Combined type sewage treatment systemInfo
- Publication number
- JP2003053360A JP2003053360A JP2001243883A JP2001243883A JP2003053360A JP 2003053360 A JP2003053360 A JP 2003053360A JP 2001243883 A JP2001243883 A JP 2001243883A JP 2001243883 A JP2001243883 A JP 2001243883A JP 2003053360 A JP2003053360 A JP 2003053360A
- Authority
- JP
- Japan
- Prior art keywords
- contact
- contact material
- tank
- combined treatment
- treatment septic
- 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
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
【0001】[0001]
【発明の属する技術分野】本発明は、屎尿、雑排水等の
有機汚水に含まれている有機物を浄化する合併処理浄化
槽に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a combined treatment septic tank for purifying organic substances contained in organic wastewater such as human waste and gray water.
【0002】[0002]
【従来の技術】従来、沈殿分離室と、接触曝気室と、沈
殿室と、消毒室とを区画形成して成る合併処理浄化槽に
おいて、接触曝気室内には、多孔質性の接触材を充填し
た複数の接触材筐体を積層配置し、この接触材の表面に
生育した好気性微生物と、接触材の微細孔に生育した嫌
気性微生物によって汚水に対し脱リン・脱窒素・脱BO
D・脱SS・脱アンモニア等の処理を行なうものであ
る。また、接触曝気室内に対向配置した一対の接触材中
央の隙間には散気管が配され、散気管の両側にはそれぞ
れ1本の逆洗管を当該散気管と平行となるように配設さ
れている。さらに、従来では、繊維強化プラスチック材
製の樹脂層の両面にセラミックシートを貼着して成る接
触材が提案されている。2. Description of the Related Art Conventionally, in a combined treatment septic tank comprising a precipitation separation chamber, a contact aeration chamber, a precipitation chamber and a disinfection chamber, the contact aeration chamber is filled with a porous contact material. Deposition, denitrification, and BO removal of sewage due to aerobic microorganisms grown on the surface of this contact material and anaerobic microorganisms grown in the micropores of the contact material by stacking multiple contact material casings.
D, de-SS, de-ammonia, etc. are processed. Further, an air diffuser is arranged in a gap in the center of the pair of contact materials arranged opposite to each other in the contact aeration chamber, and one backwash pipe is arranged on each side of the air diffuser so as to be parallel to the air diffuser. ing. Further, conventionally, a contact material has been proposed in which a ceramic sheet is attached to both surfaces of a resin layer made of a fiber reinforced plastic material.
【0003】[0003]
【発明が解決しようとする課題】しかしながらこのよう
な従来提案の合併処理浄化槽では、接触曝気室内に多孔
質性の接触材を充填した複数の接触材筐体を積層配置し
ているため、汚水の循環に対する抵抗が大きくなって乱
流を発生してしまい、接触材に対する接触効率が低下す
る。また、繊維強化プラスチック材製の樹脂層の両面に
セラミックシートを貼着して成る接触材では、微生物膜
の生成のための環境がシート表面積のみに限られてしま
うため、微生物膜の育成に対する効果が極めて低いもの
となる。しかも、接触材の長期間の使用に際し、樹脂層
に対するセラミックシートの貼着部分が剥離してしまう
虞れもある。さらに、従来では散気管の両側にそれぞれ
1本の逆洗管を当該散気管と平行となるように配設して
いるので、接触材を洗浄するに際し、1本の逆洗管のみ
では接触材に付着した汚物を除去するには不十分である
等の問題点を有していた。However, in such a conventionally proposed combined treatment septic tank, a plurality of contact material casings filled with a porous contact material are stacked in the contact aeration chamber, so that the sewage The resistance to circulation increases and turbulent flow is generated, so that the contact efficiency with the contact material decreases. Further, in the contact material formed by sticking the ceramic sheets on both surfaces of the resin layer made of the fiber reinforced plastic material, the environment for the production of the microbial membrane is limited only to the sheet surface area. Is extremely low. Moreover, when the contact material is used for a long period of time, there is a possibility that the portion where the ceramic sheet is adhered to the resin layer may peel off. Further, conventionally, one backwash pipe is arranged on each side of the air diffusing pipe so as to be parallel to the air diffusing pipe. Therefore, when cleaning the contact material, only one backwash pipe is used. There was a problem that it was insufficient to remove the dirt attached to the.
【0004】そこで本発明は叙上のような従来存した諸
事情に鑑み創出されたもので、接触曝気槽内での汚水循
環に対して乱流を無くした略層流状態に近い環境を実現
可能にして接触材に対する汚水の流動抵抗を低減させか
つ接触効率が高められると共に、埋設設置時の横幅方向
に対する省スペース化も図れるものとし、また接触材で
の微生物膜の育成に対する環境を改善可能にし、さらに
接触材に付着した汚物を能率良く除去することができる
ように逆洗管を改善可能にした合併処理浄化槽を提供す
ることを目的とする。Therefore, the present invention was created in view of the above existing circumstances, and realizes an environment close to a laminar flow state in which turbulent flow is eliminated with respect to wastewater circulation in a contact aeration tank. This will reduce the flow resistance of sewage to the contact material and improve the contact efficiency, as well as save space in the lateral direction during embedded installation, and improve the environment for growing microbial membranes on the contact material. Further, it is an object of the present invention to provide a combined treatment septic tank in which the backwash pipe can be improved so as to efficiently remove the dirt attached to the contact material.
【0005】[0005]
【課題を解決するための手段】上述した課題を達成する
ため、本発明にあっては、嫌気性微生物が生育されてい
る沈殿分離槽(2a,2b)と、好気性微生物が生育さ
れている接触材21を垂立配置しかつエアリフトポンプ
12に接続した散気管13および逆洗管14を接触材2
1底部に配して成る接触曝気槽3と、沈殿槽4と、消毒
槽5とがそれぞれ仕切り壁を介して区画配置されて成る
合併処理浄化槽において、接触曝気槽3内に設置される
接触材21は、蛇腹形状に折曲形成した繊維強化プラス
チック(FRP)板22の片面もしくは両面に多孔質性
セラミックス系粒子23を担持させて成るものである。
前記接触材21は、約1〜1.2mm程度の繊維強化プ
ラスチック(FRP)板22の硬化直前の片面に直径約
1mm程度の多孔質性セラミックス系粒子23を1平方
m当たり約100〜400g程度散布して付着形成する
ことができる。前記接触材21は、蛇腹面の山同士と谷
同士とがそれぞれ揃うようにして接触材架台24内に複
数が垂立配置させてあるものとできる。前記逆洗管14
は、一対の接触材架台24の中央底部に配した散気管1
3の両側において、長手方向に沿った複数の管体が並列
した状態で水平配置されるように全体略矩形環状に形成
されており、逆洗管14の左右側面には複数の空気噴出
孔14aが所定の間隔をもって開穿形成されているもの
とできる。接触曝気槽3は、この外形状を正面から見て
両側中央が若干外側に向けて略くの字型に突出し、縦幅
が横幅よりも大きくした略縦長六角形もしくは樽型等に
形成してあるものとできる。In order to achieve the above-mentioned object, in the present invention, a precipitation separation tank (2a, 2b) in which an anaerobic microorganism is grown and an aerobic microorganism are grown. The contact material 21 is vertically arranged, and the diffusing pipe 13 and the backwash pipe 14 connected to the air lift pump 12 are connected to the contact material 2
In a combined treatment septic tank comprising a contact aeration tank 3 arranged at the bottom, a settling tank 4, and a disinfection tank 5, each of which is partitioned and arranged via a partition wall, a contact material installed in the contact aeration tank 3. Reference numeral 21 denotes a fiber-reinforced plastic (FRP) plate 22 bent in a bellows shape, and supporting porous ceramic particles 23 on one or both surfaces thereof.
The contact material 21 has about 1 to 1.2 mm of porous ceramic particles 23 having a diameter of about 1 mm on one surface immediately before curing of a fiber reinforced plastic (FRP) plate 22 of about 100 to 400 g per square meter. It can be applied by spraying. A plurality of the contact materials 21 may be vertically arranged in the contact material mount 24 so that the peaks and the valleys of the bellows surface are aligned with each other. The backwash pipe 14
Is an air diffusing tube 1 arranged at the center bottom of the pair of contact material mounts 24.
On both sides of 3, a plurality of pipes along the longitudinal direction are formed in a generally rectangular ring shape so as to be horizontally arranged in a parallel state. Can be perforated at a predetermined interval. The contact aeration tank 3 is formed in a substantially vertically long hexagonal shape or a barrel shape in which the center of both sides is slightly outwardly protruded in a substantially V shape when viewed from the front and the vertical width is larger than the horizontal width. There can be something.
【0006】以上のように構成された本発明に係る合併
処理浄化槽において、蛇腹形状に折曲形成した繊維強化
プラスチック(FRP)板22の片面もしくは両面に多
孔質性セラミックス系粒子23を担持させて成り、接触
曝気層3内に垂立配置させた接触材21は、当該接触材
21での微生物膜の育成に対する環境を改善可能にさせ
ると共に、垂立配置させた接触材21自体が蛇腹形状を
呈しているため汚水の接触面積を大きくすることがで
き、しかも補強度も向上させる。約1〜1.2mm程度
の繊維強化プラスチック(FRP)板22の硬化直前の
片面に直径約1mm程度の多孔質性セラミックス系粒子
23を1平方m当たり約100〜400g程度散布して
付着形成して成る接触材21は、接触材21の表面に突
起を形成して表面積を増加させるため微生物膜の生成を
助長させ、しかも接触材21自体の補強度も向上させ
る。蛇腹面の山同士と谷同士とがそれぞれ揃うようにし
て接触材架台24内に複数が垂立配置させてある接触材
21は、垂立方向に沿っての汚水の循環流動がスムーズ
に行なわれ、しかも流動抵抗が少なくなるため接触材2
1表面への汚水の接触が均等に行なわれ汚水処理能力を
向上させる。長手方向に沿った複数の管体が並列した状
態で水平配置されるように全体略矩形環状に形成され、
左右側面には複数の空気噴出孔14aが所定の間隔をも
って開穿形成されている逆洗管14は、接触材21に付
着した汚物を能率良く除去させる。縦幅が横幅よりも大
きくした略縦長六角形もしくは樽型等に形成してある接
触曝気槽3は、内部での汚水循環に対して乱流を無くし
た略層流状態に近いものとし、接触材21に対する汚水
の流動抵抗を低減させる。In the combined treatment septic tank according to the present invention configured as described above, the porous ceramic particles 23 are supported on one or both sides of the fiber reinforced plastic (FRP) plate 22 bent in a bellows shape. The contact material 21 vertically arranged in the contact aeration layer 3 makes it possible to improve the environment for the growth of the microbial film on the contact material 21, and the contact material 21 itself vertically arranged has a bellows shape. Since it is present, the contact area of sewage can be increased and the degree of reinforcement can also be improved. Porous ceramic particles 23 having a diameter of about 1 mm are sprayed on one surface of the fiber-reinforced plastic (FRP) plate 22 having a diameter of about 1 to 1.2 mm immediately before curing by spraying about 100 to 400 g per square meter to be attached. The contact material 21 thus formed forms a protrusion on the surface of the contact material 21 to increase the surface area, thereby promoting generation of a microbial film, and also improving the degree of reinforcement of the contact material 21 itself. A plurality of contact materials 21 are vertically arranged in the contact material mount 24 so that the peaks and the valleys of the bellows surface are aligned with each other. The contact material 21 smoothly circulates the sewage in the vertical direction. Moreover, since the flow resistance is reduced, the contact material 2
(1) The contact of sewage with the surface is evenly performed to improve the sewage treatment capacity. A plurality of tubular bodies along the longitudinal direction are formed in a generally rectangular ring shape so as to be horizontally arranged in a parallel state,
The backwash pipe 14 having a plurality of air ejection holes 14a formed at predetermined intervals on the left and right side surfaces efficiently removes the dirt attached to the contact material 21. The contact aeration tank 3 is formed in a vertically long hexagonal shape or a barrel shape whose vertical width is larger than the horizontal width. The flow resistance of the sewage to the material 21 is reduced.
【0007】[0007]
【発明の実施の形態】以下図面を参照して本発明の一実
施の形態を説明すると、図において示される符号1は、
有機汚水に含まれている有機物を浄化するための埋設型
ユニットタイプの合併処理浄化槽本体であり、該合併処
理浄化槽本体1は、図1、図2に示すように、それぞれ
嫌気性微生物が生育されている沈殿分離第1室2a、沈
殿分離第2室2bと、好気性微生物が生育されている接
触曝気槽3と、沈殿槽4と、消毒槽5とがそれぞれ仕切
り壁を介して区画配置されている。BEST MODE FOR CARRYING OUT THE INVENTION An embodiment of the present invention will be described below with reference to the drawings.
1 is a buried unit type combined treatment septic tank main body for purifying organic substances contained in organic wastewater, wherein the combined treatment septic tank main body 1 has anaerobic microorganisms grown therein as shown in FIGS. The sedimentation first chamber 2a, the sedimentation second chamber 2b, the contact aeration tank 3 in which aerobic microorganisms are grown, the sedimentation tank 4, and the disinfection tank 5 are partitioned and arranged through a partition wall, respectively. There is.
【0008】合併処理浄化槽本体1の外形状は、図3に
示すように、正面から見て略縦長六角形もしくは樽型等
の縦幅が横幅よりも大きく、例えば縦横の比率が4:3
等となるように形成し、また側面中央が若干外側に向け
て略くの字型に突出した形状にしてあり、これにより接
触曝気槽3内での汚水循環に対して乱流を無くした略層
流状態に近いものとし、接触材21に対する汚水の流動
抵抗を低減させかつ接触効率が高められると共に、設置
時の横幅方向に対する省スペース化が図れるようにして
ある。As shown in FIG. 3, the outer shape of the main body 1 of the combined treatment septic tank is substantially vertically long hexagonal or barrel-shaped as viewed from the front, and the vertical width thereof is larger than the horizontal width.
Etc., and has a shape in which the center of the side surface protrudes slightly outwards in a V shape, thereby eliminating the turbulent flow with respect to the wastewater circulation in the contact aeration tank 3. The laminar flow state is approximated to reduce the flow resistance of the dirty water to the contact material 21 and improve the contact efficiency, and at the same time, it is possible to save the space in the lateral width direction at the time of installation.
【0009】沈殿分離第1室2aの外壁上側には、屎
尿、雑排水等の有機汚水を流入させる流入管6が、当該
沈殿分離第1室2aの底部方向へ向けて配した流入バッ
フル7を介して接続配置されている。沈殿分離第1室2
aと沈殿分離第2室2bとを仕切る仕切り壁において沈
殿分離第1室2aに露呈する側には底部方向へ向けて移
流バッフル8が配され、隣接する沈殿分離第2室2bに
露呈する側には当該移流バッフル8に連通すべく底部方
向へ向けて移流バッフル9が配されている。On the upper side of the outer wall of the sedimentation first chamber 2a, an inflow pipe 6 for introducing organic wastewater such as human waste and gray water is provided with an inflow baffle 7 arranged toward the bottom of the sedimentation first chamber 2a. Is connected through. Precipitation separation first chamber 2
On the side of the partition wall that separates a and the precipitation separation second chamber 2b, the advection baffle 8 is arranged toward the bottom on the side exposed to the precipitation separation first chamber 2a, and the side exposed to the adjacent precipitation separation second chamber 2b. An advection baffle 9 is arranged in the bottom of the column so as to communicate with the advection baffle 8.
【0010】尚、沈殿分離第1室2a、沈殿分離第2室
2bは、仕切り壁の上側の開放部を介して連通されてお
り、沈殿分離第1室2aに流入された汚水上澄みが沈殿
分離第2室2bへ流入すべく成してある。また、接触曝
気槽3と沈殿槽4は、仕切り壁の下側の開放部4Aを介
して連通されており、接触曝気槽3で処理された水を沈
殿槽4へ流入すべく成してある。しかも沈殿槽4は下方
に向かって次第に縮径されたホッパー形状となってお
り、これに汚泥をガイドさせて開放部4Aを経て接触曝
気層3の底部に流入すべく成してある。The sedimentation separation first chamber 2a and the sedimentation separation second chamber 2b are communicated with each other through an opening on the upper side of the partition wall, and the wastewater supernatant flowing into the sedimentation separation first chamber 2a is sedimented and separated. It is designed to flow into the second chamber 2b. Further, the contact aeration tank 3 and the settling tank 4 are communicated with each other through an opening 4A below the partition wall so that the water treated in the contact aeration tank 3 flows into the settling tank 4. . Moreover, the settling tank 4 has a hopper shape in which the diameter is gradually reduced downward, and sludge is guided by the settling tank 4 and flows into the bottom of the contact aeration layer 3 through the opening 4A.
【0011】図3、図4に示すように、沈殿分離第2室
2bと接触曝気槽3とを仕切る仕切り壁の当該沈殿分離
第2室2bに露呈する側には所定間隔を開けて一対の移
流バッフル10が配され、また接触曝気槽3に露呈する
側には汚泥引出管11が配されている。接触曝気槽3に
は、後述する略縦長五角形を呈する接触材21が装着さ
れている一対の接触材架台24が沈殿分離第2室2bと
沈殿槽4とを結ぶ汚水流入経路に対して直角方向に対向
配置されている。As shown in FIGS. 3 and 4, a pair of partition walls partitioning the second settling separation chamber 2b and the contact aeration tank 3 are exposed at a predetermined interval on the side exposed to the second settling separation chamber 2b. An advection baffle 10 is arranged, and a sludge extraction pipe 11 is arranged on the side exposed to the contact aeration tank 3. In the contact aeration tank 3, a pair of contact material pedestals 24, each of which has a contact material 21 having a substantially vertical pentagon shape to be described later, are mounted, and a pair of contact material pedestals 24 connect the sediment separation second chamber 2b and the sedimentation tank 4 in a direction perpendicular to the wastewater inflow path. It is arranged opposite to.
【0012】接触材21は、図8に示すように、蛇腹形
状に折曲形成した板厚が約1〜1.2mm程度の繊維強
化プラスチック(FRP)板22の片面もしくは両面に
直径約1mm程度の多孔質性セラミックス系粒子23を
1平方m当たり約100〜400g程度散布して付着さ
せたものであり、接触材21の加工形成に際し、繊維強
化プラスチック(FRP)板22の表面(片面)が硬化
する直前に多孔質性セラミックス系粒子23を万遍なく
散布させて作成される。このような多孔質性セラミック
ス系粒子23を散布させる理由は、接触材21の表面に
突起を形成して表面積を増加させることにより微生物膜
の生成を助長させることにある。この繊維強化プラスチ
ック(FRP)板22に担持された多孔質性のセラミッ
クス系粒子23の微細孔、および表面に好気性微生物が
成長される。As shown in FIG. 8, the contact member 21 has a diameter of about 1 mm on one or both sides of a fiber reinforced plastic (FRP) plate 22 which is formed into a bellows shape and has a plate thickness of about 1 to 1.2 mm. About 100 to 400 g per 1 square meter of the porous ceramics-based particles 23 are spread and attached, and when the contact material 21 is processed and formed, the surface (one surface) of the fiber reinforced plastic (FRP) plate 22 is Immediately before hardening, the porous ceramic particles 23 are evenly dispersed and prepared. The reason for dispersing such porous ceramic particles 23 is to promote the generation of the microbial film by forming protrusions on the surface of the contact material 21 to increase the surface area. Aerobic microorganisms grow on the fine pores and the surface of the porous ceramic particles 23 supported on the fiber reinforced plastic (FRP) plate 22.
【0013】尚、本実施の形態では接触材21の蛇腹面
は、横断面が三角形ジグザグタイプに形成され、接触材
架台24内に複数の接触材21を蛇腹面の山同士と谷同
士とがそれぞれ揃うようにして垂立配置させ上下を押え
板24Aでもってリベット締結することで当該接触材2
1が配置されている(図7参照)。この他、矩形もしく
は台形ジグザグタイプ(図9(a)参照)、あるいは波
形タイプ(図9(b)参照)等を有する蛇腹面に形成さ
れていても良い。In the present embodiment, the bellows surface of the contact material 21 is formed in a triangular zigzag type in cross section, and a plurality of contact materials 21 are arranged in the contact material mount 24 so that the peaks and valleys of the bellows surface are formed. The contact members 2 are vertically arranged so that they are aligned with each other, and the upper and lower parts are riveted with the pressing plates 24A.
1 is arranged (see FIG. 7). In addition, it may be formed on a bellows surface having a rectangular or trapezoidal zigzag type (see FIG. 9A) or a corrugated type (see FIG. 9B).
【0014】図5に示すように、接触曝気槽3と沈殿槽
4とを仕切る仕切り壁の接触曝気槽3に露呈する側には
エアリフトポンプ12が配され、接触曝気槽3の底部で
かつ相対向する一対の接触材架台24の間に配した散気
管13に散気バルブ13A等を介して連通されている。
また、エアリフトポンプ12は、一対の接触材架台24
の底部でかつ散気管13の両側において当該散気管13
と平行に配した逆洗管14に逆洗バルブ14A・エアリ
フト調整用バルブ14B・エア逃がしバルブ14C・エ
ア逃がし管14D等を介して連通されている。この逆洗
管14は、図6に示すように、一対の接触材架台24の
底部において、長手方向に沿ったそれぞれ3本の管体が
並列した状態で水平配置されるように略矩形環状に形成
されており、逆洗管14の左右側面には複数の空気噴出
孔14aが所定の間隔をもって開穿形成されている。こ
の逆洗管14は、接触材21を洗浄するときに使用さ
れ、散気バルブ13A等を閉弁させかつ逆洗バルブ14
A等を開弁させることによって行なわれる。As shown in FIG. 5, an air lift pump 12 is disposed on the side of the partition wall that separates the contact aeration tank 3 and the precipitation tank 4 from the side exposed to the contact aeration tank 3. The air diffusing pipe 13 arranged between the pair of facing contact material mounts 24 is communicated with the air diffusing valve 13A or the like.
The air lift pump 12 also includes a pair of contact material mounts 24.
At the bottom of the air diffuser 13 and on both sides of the air diffuser 13.
The backwash pipe 14 arranged in parallel with the backwash pipe 14 is communicated with the backwash valve 14A, the air lift adjusting valve 14B, the air relief valve 14C, the air relief pipe 14D, and the like. As shown in FIG. 6, the backwash pipe 14 is formed into a substantially rectangular ring shape so that three pipe bodies along the longitudinal direction are horizontally arranged at the bottom of the pair of contact material mounts 24 in parallel. A plurality of air ejection holes 14a are formed in the left and right side surfaces of the backwash pipe 14 at predetermined intervals. The backwash pipe 14 is used when the contact material 21 is washed, and closes the air diffuser valve 13A and the like and backwash valve 14
It is performed by opening valve A and the like.
【0015】散気管13は汚泥計量装置15を介して、
沈殿分離第1室2aに向けて若干勾配を付与して配され
た汚泥移送管16に連通され、汚泥移送管16は沈殿分
離第2室2bの上部を横切り、沈殿分離第1室2a上に
臨まされ、前記沈殿分離第1室2aの底部方向へ向けて
配した流入バッフル7上端側に連通させてある。The air diffuser 13 is connected via a sludge measuring device 15
It is connected to the sludge transfer pipe 16 arranged with a slight gradient toward the sedimentation separation first chamber 2a, and the sludge transfer pipe 16 crosses the upper part of the sedimentation separation second chamber 2b and is placed on the sedimentation separation first chamber 2a. It faces the upper end side of the inflow baffle 7 that faces the bottom of the first settling separation chamber 2a.
【0016】沈殿槽4の上部中央にはスカムバッフル・
集水トイ・越流セキ・塩素等を装填した消毒筒・消毒仕
切り壁等を備えて成る消毒槽5が配され、沈殿槽4に流
入された処理済み水の上澄みがスカムバッフル・集水ト
イ・越流セキを経て消毒槽5に流入すべく成してある。
また、消毒槽5の上澄み部分を河川等にオーバーフロー
させるために、消毒槽5の水面に位置する側壁箇所には
放流管17が配されている。In the upper center of the settling tank 4, a scum baffle
A disinfection tank 5 comprising a disinfection cylinder, disinfection partition wall, etc. loaded with a water collection toy, overflow cough, chlorine, etc. is arranged, and the supernatant of the treated water that has flowed into the settling tank 4 is a scum baffle / water collection toy. -It is designed to flow into the disinfection tank 5 through the overflow.
Further, a discharge pipe 17 is arranged at a side wall portion of the disinfection tank 5 located on the water surface in order to overflow the supernatant of the disinfection tank 5 into a river or the like.
【0017】合併処理浄化槽本体1の上面には、沈殿分
離第1室2aに連通するマンホール18A、沈殿分離第
2室2bに連通するマンホール18B、接触曝気槽3と
沈殿槽4に連通するマンホール18Cがそれぞれ形成さ
れている。さらに、マンホール18A側には、内部の臭
気を排出しかつ内部を一定の気圧に保持するための臭突
口19を設けてある。On the upper surface of the combined treatment septic tank main body 1, a manhole 18A communicating with the precipitation separation first chamber 2a, a manhole 18B communicating with the precipitation separation second chamber 2b, and a manhole 18C communicating with the contact aeration tank 3 and the precipitation tank 4. Are formed respectively. Further, the manhole 18A side is provided with an odor vent 19 for discharging the odor inside and keeping the inside at a constant atmospheric pressure.
【0018】次に以上のように構成された実施の形態に
ついての動作の一例を説明する。図2に示すように、排
出された屎尿、雑排水等の有機汚水は、先ず、合併処理
浄化槽本体1の沈殿分離第1室2aに流入管6を介して
流入され、ここで汚水中に含まれている比較的大きな浮
遊物が沈殿され、沈殿分離第1室2aに生育されている
嫌気性微生物が汚水の脱リン、脱窒素、脱BOD、脱S
S、脱アンモニア等を処理する。Next, an example of the operation of the embodiment configured as described above will be described. As shown in FIG. 2, the discharged organic sewage such as human waste and gray water is first introduced into the precipitation separation first chamber 2a of the combined treatment septic tank main body 1 through the inflow pipe 6, and is contained in the sewage here. The relatively large suspended solids are precipitated, and the anaerobic microorganisms growing in the precipitation separation first chamber 2a are dephosphorized, denitrified, de-BOD, de-S
S, deammonification, etc. are processed.
【0019】次に、沈殿分離第1室2aで処理された汚
水の上澄みが移流バッフル8、移流バッフル9を介して
沈殿分離第2室2bに流入し、そこでさらに嫌気性微生
物によって処理される。沈殿分離第2室2b中で浮遊す
る汚泥は汚泥引出管11を介して接触曝気層3内底部中
央に引き出され、散気管13からの空気圧によって接触
材21を通り浮上させられる。この間、空気が汚水中に
吸収されると共に空気の浮上にともなって汚水中に互い
に逆方向の循環流が発生する。Next, the supernatant of the sewage treated in the sedimentation separation first chamber 2a flows into the sedimentation separation second chamber 2b via the advection baffle 8 and advection baffle 9 and is further treated there by anaerobic microorganisms. The sludge floating in the sedimentation separation second chamber 2b is drawn out to the center of the bottom inside the contact aeration layer 3 via the sludge drawing pipe 11, and is floated through the contact material 21 by the air pressure from the diffuser pipe 13. During this time, air is absorbed in the dirty water, and as the air floats, circulating flows in opposite directions are generated in the dirty water.
【0020】このとき汚水中に含まれている有機物は接
触曝気層3内を循環して均一に分散させられ、接触材2
1の繊維強化プラスチック(FRP)板22に担持され
た多孔質性セラミック系粒子23により生成された好気
性微生物膜によって酸化分解される。このとき接触材2
1は、繊維強化プラスチック(FRP)板22の表面
(片面)が硬化する直前に多孔質性セラミックス系粒子
23を万遍なく散布させて作成され、接触材21の表面
に突起が形成されて表面積を増加させた状態となってい
るので、繊維強化プラスチック(FRP)板22に担持
された多孔質性のセラミックス系粒子23の微細孔、お
よび表面に好気性微生物が成長しやすい環境が形成され
ている。接触曝気層3内で処理された水は仕切り壁の下
側の開放部4Aを介して隣の沈殿層4内へ流入され、水
に含まれている僅かな汚泥が沈殿層4内底部に沈降され
る。At this time, the organic matter contained in the wastewater is circulated in the contact aeration layer 3 to be uniformly dispersed, and the contact material 2
No. 1 is oxidatively decomposed by the aerobic microbial membrane produced by the porous ceramic particles 23 carried on the fiber reinforced plastic (FRP) plate 22. Contact material 2 at this time
No. 1 is prepared by evenly dispersing the porous ceramic particles 23 immediately before the surface (one side) of the fiber reinforced plastic (FRP) plate 22 is hardened, and projections are formed on the surface of the contact material 21 to form a surface area. Is increased, the micropores of the porous ceramic particles 23 supported on the fiber reinforced plastic (FRP) plate 22 are formed, and an environment where aerobic microorganisms easily grow is formed on the surface. There is. The water treated in the contact aeration layer 3 flows into the next settling layer 4 through the opening 4A below the partition wall, and a small amount of sludge contained in the water settles on the inner bottom of the settling layer 4. To be done.
【0021】接触曝気層3内底部に流入した汚泥および
処理済み水は、エアリフトポンプ12によって汚泥移送
管16を通り、沈殿分離第1室2aへ返送され、以後は
上記と同じ処理工程が繰り返される。そして、沈殿層4
に流入された処理済み水の上澄みは、消毒層5に流入さ
れ、塩素消毒された後、放流管17を介して河川等へ放
出される。The sludge and the treated water that have flowed into the bottom of the contact aeration layer 3 are returned by the air lift pump 12 to the sedimentation first chamber 2a through the sludge transfer pipe 16, and the same treatment steps as described above are repeated thereafter. . And the sediment layer 4
The supernatant of the treated water that has flowed into the tank is discharged into the disinfecting layer 5, is sterilized with chlorine, and is then discharged to a river or the like through the discharge pipe 17.
【0022】[0022]
【発明の効果】本発明は以上のように構成されているた
めに、接触曝気槽内での汚水循環に対して乱流を無くし
た略層流状態に近い環境を実現可能にして接触材に対す
る汚水の流動抵抗を低減させかつ接触効率が高められる
と共に、埋設設置時の横幅方向に対する省スペース化も
図れるものとし、また接触材での微生物膜の育成に対す
る環境を改善可能にし、さらに接触材に付着した汚物を
効率良く除去することができるように逆洗管を改善可能
にした合併処理浄化槽を提供することができる。EFFECTS OF THE INVENTION Since the present invention is constructed as described above, it is possible to realize an environment close to a laminar flow state in which turbulent flow is eliminated with respect to the circulation of waste water in the contact aeration tank, and the contact material is In addition to reducing the flow resistance of sewage and improving the contact efficiency, it is also possible to save space in the lateral direction when installing underground, and it is possible to improve the environment for growing microbial membranes on the contact material It is possible to provide a combined treatment septic tank in which the backwash pipe can be improved so that the attached dirt can be efficiently removed.
【0023】すなわちこれは本発明が、嫌気性微生物が
生育されている沈殿分離槽(2a,2b)と、好気性微
生物が生育されている接触材21を垂立配置しかつエア
リフトポンプ12に接続した散気管13および逆洗管1
4を接触材21底部に配して成る接触曝気槽3と、沈殿
槽4と、消毒槽5とがそれぞれ仕切り壁を介して区画配
置されて成る合併処理浄化槽において、接触曝気槽3内
に設置される接触材21は、蛇腹形状に折曲形成した繊
維強化プラスチック(FRP)板22の片面もしくは両
面に多孔質性セラミックス系粒子23を担持させて成る
からであり、これにより、当該接触材21での微生物膜
の育成に対する環境を改善することができると共に、垂
立配置させた接触材21自体が蛇腹形状を呈しているた
め汚水の接触面積を大きくすることができ、しかも補強
度も向上させることができる。That is, in the present invention, the precipitation separation tanks (2a, 2b) in which the anaerobic microorganisms are grown and the contact material 21 in which the aerobic microorganisms are grown are vertically arranged and connected to the air lift pump 12. Air diffuser 13 and backwash tube 1
A contact aeration tank 3 having 4 arranged at the bottom of the contact material 21, a settling tank 4, and a disinfecting tank 5 are installed in the contact aeration tank 3 in a combined treatment septic tank comprising partition walls. This is because the contact material 21 is formed by supporting the porous ceramic particles 23 on one side or both sides of a fiber reinforced plastic (FRP) plate 22 bent in a bellows shape. It is possible to improve the environment for the growth of the microbial film at the same time, and since the contact material 21 itself standing vertically has a bellows shape, it is possible to increase the contact area of sewage and also improve the degree of reinforcement. be able to.
【0024】前記接触材21は、約1〜1.2mm程度
の繊維強化プラスチック(FRP)板22の硬化直前の
片面に直径約1mm程度の多孔質性セラミックス系粒子
23を1平方m当たり約100〜400g程度散布して
付着形成されているので、接触材21の表面に突起を形
成して表面積を増加させるため微生物膜の生成を助長さ
せることができ、しかも接触材21自体の補強度も向上
させることができる。The contact material 21 has porous ceramic particles 23 having a diameter of about 1 mm on one side immediately before curing of a fiber reinforced plastic (FRP) plate 22 having a diameter of about 1 to 1.2 mm and a diameter of about 100 per square meter. Since about 400g is sprayed and formed, the protrusions are formed on the surface of the contact material 21 to increase the surface area, which can promote the generation of the microbial film, and the reinforcement degree of the contact material 21 itself is improved. Can be made.
【0025】前記接触材21は、蛇腹面の山同士と谷同
士とがそれぞれ揃うようにして接触材架台24内に複数
が垂立配置させてあるので、垂立方向に沿っての汚水の
循環流動がスムーズに行なわれ、しかも流動抵抗が少な
くなるため接触材21表面への汚水の接触が均等に行な
われ汚水処理能力を向上させることができる。Since a plurality of the contact materials 21 are vertically arranged in the contact material mount 24 so that the peaks and the valleys of the bellows surface are aligned with each other, the sewage circulation along the vertical direction. Since the flow is performed smoothly and the flow resistance is reduced, the contact of the sewage with the surface of the contact material 21 is evenly performed, and the sewage treatment capacity can be improved.
【0026】前記逆洗管14は、一対の接触材架台24
の中央底部に配した散気管13の両側において、長手方
向に沿った複数の管体が並列した状態で水平配置される
ように全体略矩形環状に形成されており、逆洗管14の
左右側面には複数の空気噴出孔14aが所定の間隔をも
って開穿形成されているので、接触材21に付着した汚
物を能率良く除去させることができる。The backwash pipe 14 includes a pair of contact material mounts 24.
On both sides of the air diffusing pipe 13 arranged at the center bottom of the back washing pipe 14, a plurality of tubular bodies along the longitudinal direction are horizontally arranged in parallel and are formed in a substantially rectangular ring shape. Since a plurality of air ejection holes 14a are formed at a predetermined interval in this, it is possible to efficiently remove the dirt attached to the contact material 21.
【0027】接触曝気槽3は、この外形状を正面から見
て両側中央が若干外側に向けて略くの字型に突出し、縦
幅が横幅よりも大きくした略縦長六角形もしくは樽型等
に形成してあるので、内部での汚水循環に対して乱流を
無くした略層流状態に近いものとし、接触材21に対す
る汚水の流動抵抗を低減させることができる。The contact aeration tank 3 has a substantially vertically-elongated hexagonal shape or a barrel shape in which the center of both sides is slightly outwardly protruded in a substantially V shape when viewed from the front and the vertical width is larger than the horizontal width. Since the sewage is formed, the sewage circulation inside can be made to be close to a laminar flow state in which turbulent flow is eliminated, and the flow resistance of the sewage to the contact material 21 can be reduced.
【図面の簡単な説明】[Brief description of drawings]
【図1】本発明の一実施の形態における汚水流路を説明
するフローチャートである。FIG. 1 is a flowchart illustrating a wastewater flow channel according to an embodiment of the present invention.
【図2】同じく合併処理浄化槽の側面から見た断面図で
ある。FIG. 2 is a sectional view of the combined treatment septic tank as viewed from the side.
【図3】同じく合併処理浄化槽の正面から見た断面図で
ある。FIG. 3 is a sectional view of the combined treatment septic tank as seen from the front.
【図4】同じく接触曝気層の接触材周辺の概略平面図で
ある。FIG. 4 is a schematic plan view around the contact material of the contact aeration layer.
【図5】同じく接触曝気層の接触材を取り外した状態の
正面図である。FIG. 5 is a front view of the contact aeration layer with the contact material removed.
【図6】同じく接触曝気層の接触材を取り外した状態の
概略平面図である。FIG. 6 is a schematic plan view of a state in which the contact material of the contact aeration layer is also removed.
【図7】同じく接触材架台の斜視図である。FIG. 7 is a perspective view of the contact material mount.
【図8】同じく接触材の全体斜視図である。FIG. 8 is likewise an overall perspective view of a contact member.
【図9】接触材の他の例を示すものであり、(a)は台
形ジグザグタイプの接触材の横断面図、(b)は波形の
接触材の横断面図である。9A and 9B show another example of the contact material, wherein FIG. 9A is a cross-sectional view of a trapezoidal zigzag type contact material, and FIG. 9B is a cross-sectional view of a corrugated contact material.
1 合併処理浄化槽本体 2a 沈殿分離第1室 2b 沈殿分離第2室 3 接触曝気層 4 沈殿層 4A 開放部 5 消毒層 6 流入管 7 流入バッフル 8,9,10 移流バッフル 11 汚泥引出管 12 エアリフトポンプ 13 散気管 14 逆洗管 15 汚泥計量装置 16 汚泥移送管 17 放流管 18A,18B,18C マンホール 19 臭突口 21 接触材 22 繊維強化プラスチック(FRP)板 23 多孔質性セラミック系粒子 24 接触材架台 1 merger processing septic tank body 2a Precipitation separation first chamber 2b Precipitation separation second chamber 3 Contact aeration layer 4 sedimentation layer 4A open part 5 disinfection layer 6 inflow pipe 7 Inflow baffle 8, 9, 10 advection baffle 11 Sludge extraction pipe 12 Air lift pump 13 Air diffuser 14 Backwash pipe 15 Sludge metering device 16 Sludge transfer pipe 17 Discharge pipe 18A, 18B, 18C manhole 19 Odor mouth 21 Contact material 22 Fiber reinforced plastic (FRP) plate 23 Porous ceramic particles 24 Contact material stand
Claims (6)
槽と、好気性微生物が生育されている接触材を垂立配置
しかつエアリフトポンプに接続した散気管および逆洗管
を接触材底部に配して成る接触曝気槽とがそれぞれ仕切
り壁を介して区画配置されて成る合併処理浄化槽におい
て、 接触曝気槽内に設置される接触材は、蛇腹形状に折曲形
成した繊維強化プラスチック(FRP)板の片面もしく
は両面に多孔質性セラミックス系粒子を担持させて成る
ことを特徴とする合併処理浄化槽。1. A settling / separation tank in which anaerobic microorganisms are grown, and a diffusing pipe and a backwash pipe in which a contact material in which aerobic microorganisms are grown are vertically arranged and connected to an air lift pump are provided at the bottom of the contact material. In the combined treatment septic tank in which the contact aeration tank and the contact aeration tank are arranged by partition walls, the contact material installed in the contact aeration tank is a fiber-reinforced plastic (FRP) bent into a bellows shape. A combined treatment septic tank characterized in that one or both sides of a plate carry porous ceramic particles.
繊維強化プラスチック(FRP)板の硬化直前の片面に
直径約1mm程度の多孔質性セラミックス系粒子を1平
方m当たり約100〜400g程度散布して付着形成す
るものとした請求項1記載の合併処理浄化槽。2. The contact material comprises porous ceramic particles having a diameter of about 1 mm on one side immediately before hardening of a fiber reinforced plastic (FRP) plate having a diameter of about 1 to 1.2 mm, and the contact material is about 100 to about 100 per square meter. The combined treatment septic tank according to claim 1, wherein about 400 g is sprinkled and formed by adhesion.
とがそれぞれ揃うようにして接触材架台内に複数が垂立
配置させてある請求項1または2記載の合併処理浄化
槽。3. The combined treatment septic tank according to claim 1, wherein a plurality of the contact materials are vertically arranged in the contact material mount so that the peaks and the valleys of the bellows surface are aligned with each other.
底部に配した散気管の両側において、長手方向に沿った
複数の管体が並列した状態で水平配置されるように全体
略矩形環状に形成されており、逆洗管の左右側面には複
数の空気噴出孔が所定の間隔をもって開穿形成されてい
る請求項1〜3のいずれか記載の合併処理浄化槽。4. The backwash pipe is generally formed so that a plurality of pipe bodies along the longitudinal direction are horizontally arranged in parallel on both sides of an air diffusing pipe arranged at the center bottom of a pair of contact material mounts. The combined treatment septic tank according to any one of claims 1 to 3, wherein the combined treatment septic tank is formed in a rectangular ring shape, and a plurality of air ejection holes are formed at predetermined intervals on the left and right side surfaces of the backwash pipe.
て両側中央が若干外側に向けて略くの字型に突出し、縦
幅が横幅よりも大きくした略縦長六角形もしくは樽型等
に形成してある請求項1〜4のいずれか記載の合併処理
浄化槽。5. The contact aeration tank has a substantially vertical hexagonal shape or a barrel shape in which the center of both sides slightly protrudes outward in a substantially V shape when viewed from the front and the vertical width is larger than the horizontal width. The merged treatment septic tank according to any one of claims 1 to 4, which is formed in.
消毒槽とを備える請求項1〜5のいずれか記載の合併処
理浄化槽。6. The combined treatment septic tank further comprises a settling tank,
The combined treatment septic tank according to claim 1, further comprising a disinfection tank.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001243883A JP2003053360A (en) | 2001-08-10 | 2001-08-10 | Combined type sewage treatment system |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP2001243883A JP2003053360A (en) | 2001-08-10 | 2001-08-10 | Combined type sewage treatment system |
Publications (1)
Publication Number | Publication Date |
---|---|
JP2003053360A true JP2003053360A (en) | 2003-02-25 |
Family
ID=19073906
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP2001243883A Pending JP2003053360A (en) | 2001-08-10 | 2001-08-10 | Combined type sewage treatment system |
Country Status (1)
Country | Link |
---|---|
JP (1) | JP2003053360A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013517120A (en) * | 2010-01-13 | 2013-05-16 | オーガニツァ ザルトコルエン ムコド レスヴェニャターシャシャーグ (ゼットアールティー.) | Carrier insert for containing and holding a biofilm culture of a fluid cleaning structure |
-
2001
- 2001-08-10 JP JP2001243883A patent/JP2003053360A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2013517120A (en) * | 2010-01-13 | 2013-05-16 | オーガニツァ ザルトコルエン ムコド レスヴェニャターシャシャーグ (ゼットアールティー.) | Carrier insert for containing and holding a biofilm culture of a fluid cleaning structure |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
AU2002301606B2 (en) | Batch Style Wastewater Treatment Apparatus Using Biological Filtering Process and Wastewater Treatment Method Using The Same | |
US4650577A (en) | Apparatus for treating and purifying waste water | |
US20090065412A1 (en) | Apparatus for waste water treatment | |
RU1836301C (en) | Installation for waste-water-cleaning | |
JP3263267B2 (en) | Septic tank | |
CN212198700U (en) | Floating biological filter bed net cage module | |
CN212127901U (en) | Sequencing batch type composite nitrogen and phosphorus removal sewage treatment device | |
JP2003053360A (en) | Combined type sewage treatment system | |
CA2565052A1 (en) | System for improved dissolved air floatation with a biofilter | |
JP4932231B2 (en) | Pump device and sewage septic tank equipped with this pump device | |
CN101279809B (en) | Biological filler shimmying-bed | |
KR20210074787A (en) | Purification Tank | |
JP6657524B2 (en) | Water treatment equipment | |
JP6805417B2 (en) | Water treatment equipment | |
CN210103550U (en) | MBR sewage treatment device for resisting membrane pollution | |
CN212894377U (en) | Domestic sewage treatment equipment | |
JP4454825B2 (en) | Wastewater purification tank and wastewater purification method | |
JP2003181483A (en) | Method for treating septic tank and the septic tank | |
RU32775U1 (en) | Modular wastewater treatment plant | |
WO2003055808A1 (en) | Waste treatment apparatus | |
KR100226213B1 (en) | Tank for treating sewage | |
JPS63185495A (en) | Compact joint septic tank | |
JP4013125B2 (en) | Remodeling method of existing single septic tank to garbage disposal equipment | |
JP4242025B2 (en) | Air diffuser for cleaning filter layer, aerobic filter bed tank and septic tank | |
JPH0630783B2 (en) | Sewage purification method and device |