JPH0521602B2 - - Google Patents
Info
- Publication number
- JPH0521602B2 JPH0521602B2 JP58174600A JP17460083A JPH0521602B2 JP H0521602 B2 JPH0521602 B2 JP H0521602B2 JP 58174600 A JP58174600 A JP 58174600A JP 17460083 A JP17460083 A JP 17460083A JP H0521602 B2 JPH0521602 B2 JP H0521602B2
- Authority
- JP
- Japan
- Prior art keywords
- pipe
- water
- backwash
- air
- valve
- 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 - Lifetime
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 158
- 238000011001 backwashing Methods 0.000 claims description 19
- 238000005273 aeration Methods 0.000 claims description 15
- 244000005700 microbiome Species 0.000 claims description 11
- 239000004575 stone Substances 0.000 claims description 10
- 238000004140 cleaning Methods 0.000 claims description 9
- 238000001914 filtration Methods 0.000 claims description 8
- 239000010865 sewage Substances 0.000 claims description 8
- 239000010802 sludge Substances 0.000 claims description 8
- 238000005086 pumping Methods 0.000 claims description 6
- 238000009423 ventilation Methods 0.000 claims description 6
- 210000003323 beak Anatomy 0.000 claims description 4
- JEGUKCSWCFPDGT-UHFFFAOYSA-N h2o hydrate Chemical compound O.O JEGUKCSWCFPDGT-UHFFFAOYSA-N 0.000 claims 1
- 230000001902 propagating effect Effects 0.000 claims 1
- 238000000034 method Methods 0.000 description 7
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 5
- 230000000694 effects Effects 0.000 description 4
- 230000003647 oxidation Effects 0.000 description 4
- 238000007254 oxidation reaction Methods 0.000 description 4
- 239000002351 wastewater Substances 0.000 description 4
- RHZUVFJBSILHOK-UHFFFAOYSA-N anthracen-1-ylmethanolate Chemical compound C1=CC=C2C=C3C(C[O-])=CC=CC3=CC2=C1 RHZUVFJBSILHOK-UHFFFAOYSA-N 0.000 description 3
- 239000003830 anthracite Substances 0.000 description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 3
- 238000009792 diffusion process Methods 0.000 description 3
- 230000007774 longterm Effects 0.000 description 3
- 229910052760 oxygen Inorganic materials 0.000 description 3
- 239000001301 oxygen Substances 0.000 description 3
- 239000004576 sand Substances 0.000 description 3
- 238000004659 sterilization and disinfection Methods 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 230000005587 bubbling Effects 0.000 description 2
- 239000010797 grey water Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- 239000002344 surface layer Substances 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- BZHJMEDXRYGGRV-UHFFFAOYSA-N Vinyl chloride Chemical compound ClC=C BZHJMEDXRYGGRV-UHFFFAOYSA-N 0.000 description 1
- 230000001464 adherent effect Effects 0.000 description 1
- 238000000354 decomposition reaction Methods 0.000 description 1
- 238000011010 flushing procedure Methods 0.000 description 1
- 239000010410 layer Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 238000010979 pH adjustment Methods 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000000644 propagated effect Effects 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 239000000377 silicon dioxide Substances 0.000 description 1
- 238000001179 sorption measurement Methods 0.000 description 1
- 230000001954 sterilising effect Effects 0.000 description 1
- 238000003911 water pollution Methods 0.000 description 1
Landscapes
- Filtration Of Liquid (AREA)
Description
【発明の詳細な説明】
本発明は、主として浄化槽の三次処理用玉石
過装置に関するものである。従来、浄化槽の三次
処理は、接触酸化槽と沈澱槽とで構成される生物
膜法によつて行なわれ、その際、接触酸化槽では
接触材として主に塩化ビニールシートの貼合せ
品を使用している。これにて、短期的な水質保証
は確保できるものの、長期的には前記接触酸化槽
内で形成された生成膜が剥離し易くなり、これが
一旦剥離すると微細化し、沈澱槽で充分に沈澱除
去されず、この状態の処理水が施設外へ放流され
る事態を招来する等、長期的な浄化処理の安定性
に欠け、水質の汚濁防止に未だ不充分なものであ
つた。特に、放流に際しPHの基準値は、5.8〜8.5
の範囲内とされるところ、二次処理水を更に三次
処理するに、前記の如くハニカムを接触材とし
て使用すると、好気状態の継続、促進によつて窯
素分が酸化、消化されていく過程でPHが4〜5程
度まで低下し、その為、再々に亘るPH調整をせね
ばならないものとしていた。DETAILED DESCRIPTION OF THE INVENTION The present invention mainly relates to a cobblestone filtration device for tertiary treatment of septic tanks. Conventionally, tertiary treatment of septic tanks has been carried out using the biofilm method, which consists of a contact oxidation tank and a settling tank, and in this case, the contact oxidation tank mainly uses a laminated product of vinyl chloride sheets as a contact material. ing. Although this can ensure water quality in the short term, in the long term, the produced film formed in the contact oxidation tank tends to peel off. First, the treated water in this state was discharged outside the facility, resulting in a lack of stability in long-term purification treatment and was still insufficient in preventing water pollution. In particular, the standard pH value for discharge is 5.8 to 8.5.
However, when the secondary treatment water is subjected to tertiary treatment, if honeycomb is used as a contact material as described above, the kiln element content will be oxidized and digested by continuing and promoting the aerobic condition. During the process, the pH dropped to about 4 to 5, which required repeated pH adjustments.
本発明は、斯様な前記諸点に鑑みて発明したも
ので、三次処理槽の下部に設けたロストルに、大
きさの異なる自然石、即ち玉石を多段に積み上
げ、ロストル下方の下部室に集水管と空気逆洗管
を配設するか、或いは、集水機能とエアーバブリ
ンク作用による空気逆洗機能とを併有する集水逆
洗管を配設し、自然石上方の上部室に散気管を、
上部室の通常水位より上方に逆洗トラフを夫々設
ける等の諸構成からなる三次処理用玉石過装置
を提供し、これにて放流水の水質の向上、PHの安
定等に対処せんとしたものである。 The present invention was devised in view of the above-mentioned points. Natural stones, that is, cobblestones of different sizes are piled up in multiple stages in a rostre provided at the lower part of the tertiary treatment tank, and a water collection pipe is installed in the lower chamber below the rostrum. Alternatively, install a water collection backwash pipe that has both a water collection function and an air backwash function using an air bubble link, and install an aeration pipe in the upper room above the natural stone. ,
We provide a cobblestone filtration device for tertiary treatment consisting of various configurations such as installing backwash troughs above the normal water level in the upper chamber, and use this to improve the quality of discharged water and stabilize PH, etc. It is.
本発明の実施例を第1図、第2図に示す如く方
形状の玉石過槽Tを一槽設けた場合について説
明する。 An embodiment of the present invention will be described with reference to a case where one rectangular boulder tank T is provided as shown in FIGS. 1 and 2.
1は二次処理水の汚水導入管であつて、前工程
の沈澱槽(図示せず)でBOD;20〜60ppm,
COD;20〜60ppm,SS;20〜60ppm、程度まで
二次処理された汚水を、本発明のコンクリート製
玉石過槽T内へ流入せしめる。2は過槽T底
部の船底状下部室であつて、その前後部に後記す
るロストルの係合段部3を設けている。4は係合
段部3に両端支持した断面矩形状のコンクリート
製ロストルであつて、ピツチ50〜75mm程度の一定
間隔毎に並列配置している。5,5aはロストル
4の上部に多段、即ち2段に積み上げた丸味を帯
びた自然石、即ち、好気性微生物を付着繁殖させ
る玉石であつて、その内、下段部には100〜150mm
径程度の比較的大きい玉石5を、また上段部には
30〜60mm径程度の比較的小さい玉石5aを、夫々
75〜50cm程度の高さに積み上げている。尚、二次
処理された水質の程度によつては、上段部に60〜
100mm径程度の中位の玉石を積み上げる。また、
此等のサイズの異なる三種の玉石5,5a,5b
を、第7図の変形例に示す如く上段部に30〜60mm
径程度の玉石5aを、下段部の上部側に60〜100
mm径程度の玉石5bを、またその下部側に100〜
150mm径程度の玉石5を夫々積み上げて対処する
こともできる。6は下部室2の下部側に横設した
比較的太径の集水管であつて、第5図aに示す如
く横設した集水管6の両側部と下方部に15mm径程
度の通水孔7を100mm程度のピツチで長手方向に
穿設している。8は集水管6に流入した三次処理
水の通水管であつて、集水管6の末端部から立ち
上げた上で次工程の逆洗槽9へ自然流出し得るよ
うにしている。10は通水管8の末端部に設けた
開閉バルブであつて、通常は開成されている。1
1は下部室2の上部側に前記集水管6と直交状に
並設した空気逆洗管であつて、第5図bに示す如
く逆洗管11の両側部に3mm径程度の噴霧孔12
を一定間隔毎に穿設し、然も、第6図に示す如く
当該空気逆洗管11をロストル4直下部に、一本
置きでピツチが10〜15cm程度の割合でロストル4
と並設状態で分岐配管されている。13は空気逆
洗用給気管であつて、一端を空気逆洗管11に連
結して過槽T上方へ立ち上げられ、別途空気ブ
ロアBから開閉バルブ14を開成して給気され
る。15は積層した玉石5,5a,5b上部の上
部室であつて、汚水導入管1より流入した二次処
理水を当該過槽Tの水位線WL程度まで貯溜せ
しる。16は上部室15の下方部に平面工字状に
配設した散気管、17は散気用給気管であつて、
一端を前記散気管16に連結して上方へ立ち上
げ、その他端の給気ブロアBから開閉バルブ18
を開成して給気される。19は通水管8のバルブ
10直前位置から分岐して前記逆洗槽9とを連結
配管した逆洗用通水管、20は分岐した逆洗用通
水管19の末端部に設けた開閉バルブ、21は逆
洗用通水管19に介設した三次処理水の逆洗用給
水ポンプであつて、前記バルブ10を閉成した上
でバルブ20を開成し、給水ポンプ21を作動さ
せて逆洗槽9から汲み上げた三次処理水を通水管
8を介して集水管6の通水孔7より逆噴出せしめ
る。22は過槽Tの上方部に横設した逆洗トラ
フ、23は逆洗トラフ22に一端を連続した返送
管であつて、逆洗時に水位が上昇することによつ
て浮上、浮遊するスカムを含む処理水を、前工程
の汚泥ピツト又は流入ポンプ槽へ返送せしめる。
24は大径の清掃管であつて、上部室15の上方
から玉石5,5a,5bと並設したロストル4間
を貫通させて下部室2まで降下させて立設支持
し、当該清掃管24からバキユウムホース(図示
せず)を挿し込んで、下部室2に滞留する汚泥分
を汲み上げるに対処している。26は逆洗槽9に
連設した消毒槽である。 1 is the sewage inlet pipe for the secondary treatment water, which has a BOD of 20 to 60 ppm in the sedimentation tank (not shown) in the previous process.
Wastewater that has been subjected to secondary treatment to COD: 20 to 60 ppm and SS: 20 to 60 ppm is allowed to flow into the concrete boulder overtank T of the present invention. Reference numeral 2 denotes a bottom-shaped lower chamber at the bottom of the overtank T, and an engaging stepped portion 3 of a rostol, which will be described later, is provided at the front and rear of the lower chamber. Reference numeral 4 denotes concrete ropes having a rectangular cross section supported at both ends by the engaging step portion 3, and are arranged in parallel at regular intervals of about 50 to 75 mm. 5 and 5a are rounded natural stones stacked in multiple tiers, that is, two tiers, on the upper part of Rostle 4, that is, cobblestones that allow aerobic microorganisms to adhere and propagate.
A boulder 5 with a relatively large diameter is placed in the upper part.
Each relatively small boulder 5a with a diameter of 30 to 60 mm is
They are piled up to a height of about 75 to 50 cm. Depending on the quality of the water that has undergone secondary treatment, the upper part may contain 60~
Pile up medium-sized boulders with a diameter of about 100 mm. Also,
These three types of boulders 5, 5a, 5b of different sizes
30 to 60 mm in the upper part as shown in the modified example in Figure 7.
Place a cobblestone 5a about the diameter of 60 to 100 on the upper side of the lower part.
A cobblestone 5b with a diameter of about mm is placed on the bottom side of the boulder 5b
It is also possible to stack up boulders 5 each having a diameter of about 150 mm. Reference numeral 6 denotes a relatively large-diameter water collection pipe installed horizontally on the lower side of the lower chamber 2, and as shown in Figure 5a, there are water holes with a diameter of about 15 mm on both sides and the lower part of the horizontally installed water collection pipe 6. 7 are drilled in the longitudinal direction at a pitch of approximately 100 mm. Reference numeral 8 denotes a water passage pipe for the tertiary treated water that has flowed into the water collection pipe 6, which is raised from the end of the water collection pipe 6 and allowed to naturally flow out to the backwash tank 9 for the next process. Reference numeral 10 denotes an on-off valve provided at the end of the water pipe 8, which is normally left open. 1
Reference numeral 1 denotes an air backwash pipe installed on the upper side of the lower chamber 2 in parallel with the water collection pipe 6 at right angles, and as shown in FIG.
However, as shown in Figure 6, the air backwash pipes 11 are installed directly below the rostre 4 at a pitch of about 10 to 15 cm every other time.
Branch piping is installed in parallel with the Reference numeral 13 denotes an air supply pipe for air backwashing, one end of which is connected to the air backwashing pipe 11, raised above the tank T, and air is supplied from a separate air blower B by opening an on-off valve 14. Reference numeral 15 denotes an upper chamber above the stacked boulders 5, 5a, and 5b, in which the secondary treated water flowing in from the wastewater introduction pipe 1 is stored up to about the water level line WL of the overtank T. Reference numeral 16 denotes an air diffuser pipe arranged in a planar shape in the lower part of the upper chamber 15; 17 is an air supply pipe for air diffusion;
One end is connected to the air diffuser pipe 16 and raised upward, and the opening/closing valve 18 is connected to the air supply blower B at the other end.
is opened and air is supplied. Reference numeral 19 indicates a backwash water pipe which branches from a position immediately before the valve 10 of the water pipe 8 and is connected to the backwash tank 9; 20 indicates an on-off valve provided at the end of the branched backwash water pipe 19; and 21 is a water supply pump for backwashing the tertiary treated water that is installed in the water pipe 19 for backwashing, and after closing the valve 10, the valve 20 is opened, and the water supply pump 21 is operated to flush the backwash tank 9. The tertiary treated water pumped up from the drain pipe 8 is made to back-flow from the water passage hole 7 of the water collection pipe 6 through the water passage pipe 8. 22 is a backwash trough installed horizontally in the upper part of the overtank T, and 23 is a return pipe connected to the backwash trough 22 at one end, which collects scum that floats and floats as the water level rises during backwashing. The treated water is returned to the sludge pit or inflow pump tank in the previous process.
24 is a large-diameter cleaning pipe, which is passed from above the upper chamber 15 between the stones 5, 5a, 5b and the rostres 4 arranged in parallel, and is lowered to the lower chamber 2 and supported vertically. A vacuum hose (not shown) is inserted from the lower chamber 2 to pump up the sludge accumulated in the lower chamber 2. 26 is a disinfection tank connected to the backwash tank 9.
而して、本装置による二次処理水の三次処理方
法を説明するに、先ず、前工程の浄化装置(図示
せず)までで二次処理され、BOD;20〜60ppm,
COD;20〜60ppm,SS;20〜60ppm程度とする
二次処理水を、汚水導入管1から玉石過槽Tの
上部室15へ流入せしめる。この流入汚水は、散
気管16と散気用給気管17、ブロアBとで構成
される散気装置により曝気され、これにて上部室
15中の溶存酸素DOを増加せしめると共に、玉
石5,5a,5bに付着した付着性微生物への酸
素補給を行なつた上で、多段に積層した当該玉石
5,5a,5bを徐々に通過して沈降する。この
玉石通過中に微細な浮遊物質は、物理的に過さ
れると同時に、玉石5,5a,5bに付着した微
生物による生物処置が併せて行なわれる。その
為、BOD,COD,SSとも10ppm以下とする高度
の処理水が得られる。斯様に過処理されて下部
室2へ降流した処理水は、汚水導入管1から上部
室15内への新たな二次処理水の供給と連動した
形で、集水管6の通水孔7から集水管6内へ入
り、通水管8を上昇した上で開成したバルブ10
を介して逆洗槽9へ押し流され、消毒室26を経
て外部放流されるか、或いは、水洗便所用、散水
用、噴水用の中水として再利用に供される。 Therefore, to explain the tertiary treatment method of the secondary treated water using this device, first, the secondary treatment is performed up to the purification device (not shown) in the previous step, and the BOD is 20 to 60 ppm.
Secondary treated water with a COD of about 20 to 60 ppm and an SS of about 20 to 60 ppm is made to flow into the upper chamber 15 of the cobblestone tank T from the wastewater introduction pipe 1. This inflowing sewage is aerated by an aeration device composed of an aeration pipe 16, an aeration supply pipe 17, and a blower B, thereby increasing dissolved oxygen DO in the upper chamber 15 and , 5b, and then gradually passes through the multi-tiered boulders 5, 5a, 5b and settles down. While passing through the boulders, the fine suspended solids are physically filtered out and at the same time are subjected to biological treatment by microorganisms attached to the boulders 5, 5a, and 5b. Therefore, highly treated water with BOD, COD, and SS below 10ppm can be obtained. The treated water that has been overtreated in this way and has descended to the lower chamber 2 flows through the water passage hole of the water collection pipe 6 in conjunction with the supply of new secondary treated water from the wastewater introduction pipe 1 into the upper chamber 15. Valve 10 enters the water collection pipe 6 from 7, ascends the water pipe 8, and opens the valve 10.
The water is washed away into the backwash tank 9 through the sterilization chamber 26 and discharged to the outside, or is reused as gray water for flush toilets, water sprinkling, and fountains.
斯様にして二次処理水の三次処理が通常行なわ
れるが、長期間に亘る稼動によつて段積みした玉
石5,5a,5b相互間に形成されている間隙が
狭ばめられ、閉塞するような事態を招来する前
に、或いは、三次処理水の水質が低下したような
場合には、散気管16と散気用給気管17とで構
成される上部室15の散気装置の稼動を停止し、
通水管8末端のバルブ10を閉成し、また逆洗用
通水管19のバルブ20を開成した上で、逆洗用
給水ポンプ21を駆動して、洗浄槽9の三次処理
水を汲み上げ、逆洗用通水管19から通水管8、
集水管6を逆流させ、その通水孔7から逆噴出せ
しめると共に、ロストル4直下の空気逆洗管11
と空気逆洗用給気管13とブロアBとで構成され
る空気逆洗装置を駆動せしめる。すると、空気逆
洗管11の噴気孔12から噴出した空気が、第6
図に示す如くロストル4相互の間隙から噴き上
り、更に、玉石5,5a,5bの間をエアーバブ
リングしながら上昇通過する。これにて、玉石
5,5a,5bの間隙を狭小化しているSSを、
除去し乍ら上部室15の表層部へ浮上せしめる。
同時に、上部室15の水位は、集水管6の通水孔
7からの逆洗水の逆噴出によつて上部室15の通
常水位WLより逆洗トラフ22への越流高さHま
で上昇する。その為、表層部に浮上した浮遊物を
含む処理水は、逆洗トラフ22へ流し込まれ、返
送管23を経て前工程の汚泥ピツト又は流入ポン
プ槽等内へ戻される。斯様な運転をした後、再
び、通常運転に復帰せしめられる。 Tertiary treatment of the secondary treated water is normally carried out in this way, but due to long-term operation, the gaps formed between the stacked stones 5, 5a, 5b become narrowed and clogged. Before such a situation arises, or in cases where the quality of the tertiary treated water has deteriorated, it is necessary to start the operation of the air diffuser in the upper chamber 15, which is composed of the air diffuser pipe 16 and the air supply pipe 17 for air diffusion. stop,
After closing the valve 10 at the end of the water pipe 8 and opening the valve 20 of the backwash water pipe 19, the backwash water supply pump 21 is driven to pump up the tertiary treated water from the cleaning tank 9, and the backwash water is pumped up. From the washing water pipe 19 to the water pipe 8,
The water collection pipe 6 is made to flow backwards, and the water is discharged from its water passage hole 7.
The air backwashing device consisting of the air supply pipe 13 for air backwashing and the blower B is driven. Then, the air ejected from the blowhole 12 of the air backwash pipe 11 flows into the sixth
As shown in the figure, the air blows up from the gap between the rostles 4, and further rises and passes between the boulders 5, 5a, and 5b while bubbling air. With this, the SS that narrows the gap between the boulders 5, 5a, and 5b,
While removing it, it is floated to the surface layer of the upper chamber 15.
At the same time, the water level in the upper chamber 15 rises from the normal water level WL in the upper chamber 15 to the overflow height H into the backwash trough 22 due to the backwash water jetting out from the water passage hole 7 of the water collection pipe 6. . Therefore, the treated water containing floating matter floating on the surface layer is flowed into the backwash trough 22 and returned through the return pipe 23 to the sludge pit or inflow pump tank of the previous process. After such operation, normal operation is resumed.
上記の場合は、玉石過槽Tが一槽の場合につ
いて説明したが、当該過槽Tと同一の構成に係
る玉石過槽T1を第8,9図の如くもう一槽連
設することで、より一層良好な三次処理を行なう
ことができる。その基本構成、作用は、前記第1
実施例の場合と同様な為、省略する。ただ、処理
水が一槽目の過槽Tから二槽目の過槽T1へ
自然に流出すべくなす為、二槽目の過槽T1の
水位WL1を低目に設定した点を除き同一の構成
としている。その為、第1実施例と同一の構成を
示す図面数字に符号aを符してその説明を省略す
る。 In the above case, we have explained the case where there is only one cobblestone overtank T, but by installing another cobblestone overtank T1 having the same configuration as the said overtank T, as shown in Figs. 8 and 9, Even better tertiary treatment can be performed. Its basic structure and operation are as described in the first
Since this is the same as in the embodiment, it will be omitted. However, in order to allow the treated water to flow naturally from the first overtank T to the second overtank T1, the water level WL1 of the second overtank T1 was set low. It is structured as follows. Therefore, the drawing numbers indicating the same configuration as the first embodiment will be denoted by the symbol a, and the explanation thereof will be omitted.
第10図は、前記第1,第2実施例の変形例で
あつて、下部室2から空気逆洗管11を外し、逆
洗用給気管13を通水管8に連結配管している。
その為、逆洗時には、逆洗槽9の三次処理水と、
ブロアBによる空気との混合物が、集水逆洗管6
の通水兼通気孔7より逆噴出され、これにて玉石
5,5a,5b相互の間隙を曝水、曝気してエア
ーバプリングする。 FIG. 10 shows a modification of the first and second embodiments, in which the air backwash pipe 11 is removed from the lower chamber 2 and the backwash air supply pipe 13 is connected to the water pipe 8.
Therefore, during backwashing, the tertiary treated water from the backwash tank 9,
The mixture with air from blower B flows through the water collection backwash pipe 6.
Water is ejected from the water passage/ventilation hole 7, and the gaps between the boulders 5, 5a, 5b are aerated and air bubbled.
本発明は、前記のように、三次処理用過槽T
の上方部に二次処理水の汚水導入管1と逆洗トラ
フ22を設け、当該過槽Tの下方部にロストル
4を設け、当該ロストル4の上部には、好気性微
生物を付着繁殖させる玉石5,5aを多段に積み
上げ、その内、下段部には100〜150mm径程度の比
較的大きい玉石5を、上段部には30〜60mm径程度
の比較的小さい玉石5a又は60〜100mm径程度の
中位の玉石を、上下に夫々高さ75〜50cm程度積み
上げ、前記ロストル4下部の下部室2の下部側に
は、両側部と下方部に通水孔7を穿設した三次処
理水の集水管6を横設し、また、下部室2に上部
側には、両側部に噴気孔12を穿設した空気逆洗
管11を、前記集水管6と直交させ、且つ、前記
ロストル4の直下部に並設して分岐配管し、前記
玉石5,5a上部の上部室15には散気管16を
配管し、その内、前記空気逆洗管11には空気逆
洗用給気管13と開閉バルブ14を連結し、ま
た、散気管16には散気用給気管17と開閉バル
ブ18を連結し、当該散気用給気管17と空気逆
洗用給気管13を合流させてブロアBと連結し、
前記集水管6に連結した三次処理水の通水管8に
は開閉バルブ10を取着し、当該通水管8と逆洗
槽9とを逆洗用通水管19で連結し、当該逆洗用
通水管19に開閉バルブ20と逆洗用給水ポンプ
21を連結し、前記上部室15の上方から下部室
2まで縦貫する下部室2の汚泥汲み上げ用清掃管
24を立設支持してなる玉石過装置を始め、数
種の三次処理水の玉石過装置を提供したので、
散気管からの曝気による溶存酸素を向上させると
共に、玉石に付着した微生物への酸素の補給が速
やかに行なわれ、然も、大きさの異なる玉石の間
隙を処理水が降流通過する為、微細な浮遊物質の
物理的過処理と、当該付着性微生物による生物
膜処理が円滑、迅速に行なわれる。特に、従前の
特開昭57−48388号公報におけるアンスラサイト
による上部過層、砂や砂利による下部過層の
組み合わせの場合や、或は、特公昭56−14360号
公報における粒径1.2mm程度のアンスラサイト又
は粒状活性炭による上部過層、砂礫又は粒径
1.0mm程度の硅砂による下部過層の組み合わせ
の場合には、いずれも単なる処理水の過という
物理処理を主眼とするに過ぎなかつた。 As mentioned above, the present invention provides an overtank T for tertiary treatment.
A sewage inlet pipe 1 and a backwash trough 22 for secondary treated water are provided in the upper part, a rostre 4 is provided in the lower part of the tank T, and a cobblestone on which aerobic microorganisms are attached and propagated is provided in the upper part of the rostre 4. 5, 5a are piled up in multiple stages, of which relatively large boulders 5 with a diameter of about 100 to 150 mm are placed in the lower part, and relatively small boulders 5a with a diameter of about 30 to 60 mm or boulders 5 with a diameter of 60 to 100 mm are placed in the upper part. Medium-sized boulders are piled up and down to a height of about 75 to 50 cm, respectively, and the lower chamber 2 at the bottom of the rostre 4 has a collection of tertiary treated water with water holes 7 drilled on both sides and the lower part. A water pipe 6 is installed horizontally, and an air backwash pipe 11 with blowholes 12 perforated on both sides is installed on the upper side of the lower chamber 2 and is perpendicular to the water collection pipe 6 and directly below the rostrum 4. A diffuser pipe 16 is installed in the upper chamber 15 above the boulders 5, 5a, and the air backwash pipe 11 is equipped with an air supply pipe 13 for air backwash and an on-off valve. 14 is connected to the air diffuser pipe 16, and an air diffuser air supply pipe 17 and an on-off valve 18 are connected to the air diffuser pipe 16, and the air diffuser air supply pipe 17 and the air backwash air supply pipe 13 are merged and connected to the blower B. ,
An on-off valve 10 is attached to the water pipe 8 for the tertiary treated water connected to the water collection pipe 6, and the water pipe 8 and the backwash tank 9 are connected by a water pipe 19 for backwashing. A cobblestone filtration device in which an on-off valve 20 and a backwash water supply pump 21 are connected to a water pipe 19, and a cleaning pipe 24 for pumping up sludge in the lower chamber 2, which runs vertically from above the upper chamber 15 to the lower chamber 2, is supported in an upright manner. We have provided several types of cobblestone filtration equipment for tertiary treated water, including
In addition to improving dissolved oxygen through aeration from the aeration pipe, oxygen is quickly supplied to the microorganisms attached to the cobblestones. Physical overtreatment of suspended solids and biofilm treatment by the adherent microorganisms are carried out smoothly and quickly. In particular, in the case of a combination of an upper overlayer made of anthracite and a lower overlayer made of sand or gravel in the previous Japanese Patent Application Publication No. 57-48388, or in the case of a combination of an upper overlayer made of anthracite and a lower overlayer made of sand or gravel, or in the case of a combination of a grain size of about 1.2 mm in Japanese Patent Publication No. 56-14360, Upper overlayer with anthracite or granular activated carbon, gravel or grain size
In the case of combinations of lower overlayers made of silica sand of about 1.0 mm, the main focus was simply physical treatment of overlayering of treated water.
ところが、本発明では、格段に大きい玉石を採
択することで、物理的な処理機能を発揮せしめる
に止どまらず、下段部には100〜150mm径程度の比
較的大きい玉石を、また、その上段部には30〜60
mm径程度の比較的小さい玉石又は60〜100mm径程
度の中位の玉石を、上下に夫々高さ75〜50cm程度
積み上げてなる組み合わせとしたり、或は、下段
部の下部側には100〜150mm径程度の比較的大きい
玉石を、その上部側には60〜100mm径程度の中位
の玉石を、その上段部には30〜60mm径程度の比較
的小さい玉石を、上下に夫々高さ75〜50cm程度積
み上げてなる組み合わせとしたので、個々の玉石
の回りに積極的に好気性微生物の生息や繁殖を促
進し、この玉石相互間の粗い間隙を二次処理水が
降流することにより、当該玉石層での好気性微生
物による吸着、酸化、分解等の生物処理が積極的
に行われる。その結果、三次処理水のPHを安定さ
せ、水質の向上に寄与し、然も、窯素分の脱窯効
果も頗る高く、当該三次処理水を洗車用、水洗用
等の中水として再利用できる。また、集水管又は
集水逆洗管を下部室に配設し、その両側部と下方
部の通水孔又は通水兼通気孔から処理水を自然に
吸い込んで通水したり、或いは、逆に当該通水孔
又は通水兼通気孔から逆洗槽の処理水が逆噴出す
る為、通水孔又は通水兼通気孔の目詰りの防止や
集水管又は集水逆洗管、通水管内の管内清掃をも
可能とする。また、空気逆洗管又は集水逆洗管を
ロストル直下部に並設することにより、その管両
側部の通気孔からの空気の噴気又は空気と水の噴
出が行なわれ、その目詰りの防止とロストル相互
の間隙からの良好なバブリング作用による玉石相
互間の清掃効果をも発揮する等の諸効果をもたら
す。 However, in the present invention, by adopting significantly larger boulders, the physical processing function is not limited to being achieved. 30 to 60 in the upper section
A combination of relatively small boulders with a diameter of about mm or medium boulders with a diameter of about 60 to 100 mm may be stacked up and down to a height of about 75 to 50 cm, or a stone with a height of 100 to 150 mm may be stacked on the bottom side of the lower part. A relatively large boulder with a diameter of about 60 to 100 mm is placed on the upper side, a relatively small boulder with a diameter of about 30 to 60 mm is placed on the upper part, and the top and bottom are each 75 to 75 mm in height. Since the combination is stacked about 50 cm, it actively promotes the inhabitation and reproduction of aerobic microorganisms around each boulder, and the secondary treated water flows down through the rough gaps between these boulders, thereby reducing the amount of water in question. Biological treatment such as adsorption, oxidation, and decomposition by aerobic microorganisms in the cobblestone layer is actively carried out. As a result, the PH of the tertiary treated water is stabilized, contributing to the improvement of water quality, and the effect of removing the kiln content is also extremely high, so the tertiary treated water can be reused as gray water for car washing, flushing, etc. can. In addition, a water collection pipe or water collection backwash pipe is installed in the lower chamber, and the treated water is naturally sucked in and passed through the water passage holes or water passage/ventilation holes on both sides and the lower part, or the water is passed in the reverse direction. Since the treated water in the backwash tank is back-flowed from the water hole or water flow/ventilation hole, it is necessary to prevent clogging of the water flow hole or water flow/ventilation hole, and to prevent water collection pipes, water collection backwash pipes, and water flow. It also makes it possible to clean the inside of the pipe. In addition, by installing air backwash pipes or water collection backwash pipes directly below the rostrum, air jets or air and water are ejected from the vents on both sides of the pipes, preventing clogging. This brings about various effects such as a cleaning effect between the stones due to the good bubbling effect from the gap between the stones and the stones.
第1図は玉石過槽が一槽の場合を示す装置縦
断正面図、第2図はその平面図、第3図はロスト
ル下方の一部切欠平面図、第4図は下部室の縦断
側面図、第5図a,bは集水管と空気逆洗管の各
断面図、第6図はロストルと空気逆洗管の位置関
係を示す縦断面図、第7図は玉石を三段積み上げ
た場合の変形例を示す図、第8,9図は玉石過
槽を2槽連設した場合の縦断正面図と平面図、第
10図は他の実施例を示す縦断正面図である。
符号表、T……過槽、B……ブロア、1……
汚水導入管、1……下部室、3……段部、4……
ロストル、5……玉石、6……集水管又は集水逆
洗管、7……通水孔、8……通水管、9……逆洗
槽、10,14,18,20……バルブ、11…
…空気逆洗管、12……噴気孔、13……逆洗用
給気管、15……上部室、16……散気管、17
……散気用給気管、19……逆洗用通水管、21
……逆洗用給水ポンプ、22……逆洗トラフ、2
3……返送管、24……清掃管、26……消毒
室。
Figure 1 is a vertical front view of the device showing a single cobblestone tank, Figure 2 is its plan view, Figure 3 is a partially cutaway plan view of the lower part of the rostre, and Figure 4 is a vertical side view of the lower chamber. , Figures 5a and b are cross-sectional views of the water collection pipe and air backwash pipe, Figure 6 is a longitudinal cross-sectional view showing the positional relationship between the rostre and air backwash pipe, and Figure 7 is a case in which cobblestones are stacked in three stages. FIGS. 8 and 9 are a longitudinal sectional front view and a plan view of a case where two boulder overtanks are installed in series, and FIG. 10 is a longitudinal sectional front view showing another embodiment. Code list, T...tank, B...blower, 1...
Sewage introduction pipe, 1...lower chamber, 3...stepped section, 4...
Rostle, 5... Cobblestone, 6... Water collection pipe or water collection backwash pipe, 7... Water passage hole, 8... Water passage pipe, 9... Backwash tank, 10, 14, 18, 20... Valve, 11...
... Air backwash pipe, 12 ... Fumarole, 13 ... Air supply pipe for backwash, 15 ... Upper chamber, 16 ... Diffusion pipe, 17
... Air supply pipe for aeration, 19 ... Water pipe for backwashing, 21
... Backwash water supply pump, 22 ... Backwash trough, 2
3... Return pipe, 24... Cleaning pipe, 26... Disinfection room.
Claims (1)
汚水導入管1と逆洗トラフ22を設け、当該過
槽Tの下方部にロストル4を設け、当該ロストル
4の上部には、好気性微生物を付着繁殖させる玉
石5,5aを多段に積み上げ、その内、下段部に
は100〜150mm径程度の比較的大きい玉石5を、上
段部には30〜60mm径程度の比較的小さい玉石5a
又は60〜100mm径程度の中位の玉石を、上下に
夫々高さ75〜50cm程度積み上げ、前記ロストル4
下部の下部室2の下部側には、両側部と下方部に
通水孔7を穿設した三次処理水の集水管6を横設
し、また、下部室2の上部側には、両側部に噴気
孔12を穿設した空気逆洗管11を、前記集水管
6と直交させ、且つ、前記ロストル4の直下部に
並設して分岐配管し、前記玉石5,5a上部の上
部室15には散気管16を配管し、その内、前記
空気逆洗管11には空気逆洗用給気管13と開閉
バルブ14を連結し、また、散気管16には散気
用給気管17と開閉バルブ18を連結し、当該散
気用給気管17と空気逆洗用給気管13を合流さ
せてブロアBと連結し、前記集水管6に連結した
三次処理水の通水管8には開閉バルブ10を取着
し、当該通水管8と逆洗槽9とを逆洗用通水管1
9で連結し、当該逆洗用通水管19に開閉バルブ
20と逆洗用給水ポンプ21を連結し、前記上部
室15の上方から下部室2まで縦貫する下部室2
の汚泥汲み上げ用清掃管24を立設支持したこと
を特徴とする玉石過装置。 2 三次処理用過槽Tの上方部に二次処理水の
汚水導入管1と逆洗トラフ22を設け、当該過
槽Tの上方部にロストル4を設け、当該ロストル
4の上部には、好気性微生物を付着繁殖させる玉
石5,5a,5bを多段に積み上げ、その内、下
段部の下部側には100〜150mm径程度の比較的大き
い玉石5を、その上部側には60〜100mm径程度の
中位の玉石5bを、また、上段部には30〜60mm径
程度の比較的小さい玉石5aを、上下に夫々高さ
75〜50cm程度積み上げ、前記ロストル4下部の下
部室2の下部側には、両側部と下方部に通水孔7
を穿設した三次処理水の集水管6を横設し、ま
た、下部室2の上部側には、両側部に噴気孔12
を穿設した空気逆洗管11を、前記集水管6と直
交させ、且つ、前記ロストル4の直下部に並設し
て分岐配管し、前記玉石5,5a,5b上部の上
部室15には散気管16を配管し、その内、前記
空気逆洗管11には空気逆洗用給気管13と開閉
バルブ14を連結し、また、散気管16には散気
用給気管17と開閉バルブ18を連結し、当該散
気用給気管17と空気逆洗用給気管13を合流さ
せてブロアBと連結し、前記集水管6に連結した
三次処理水の通水管8に開閉バルブ10を取着
し、当該通水管8と逆洗槽9とを逆洗用通水管1
9で連結し、当該逆洗用通水管19に開閉バルブ
20と逆洗用給水ポンプ21を連結し、前記上部
室15の上方から下部室2まで縦貫する汚泥汲み
上げ用清掃管24を立設支持したことを特徴とす
る玉石過装置。 3 三次処理用過槽Tの上方部に二次処理水の
汚水導入管1と逆洗トラフ22を設け、当該過
槽Tの下方部にロストル4を設け、当該ロストル
4の上部には、好気性微生物を付着繁殖させる玉
石5,5aを多段に積み上げ、その内、下段部に
は100〜150mm径程度の比較的大きい玉石5を、上
段部には30〜60mm径程度の比較的小さい玉石5a
又は60〜100mm径程度の中位の玉石を、上下に
夫々高さ75〜50cm程度積み上げ、前記ロストル4
下部の下部室2には、両側部と下方部に通水兼通
気孔7を穿設した三次処理水の集水機能と空気逆
洗機能の集水逆洗管6を横設し、前記玉石5,5
a上部の上部室15には散気管16を配管し、当
該散気管16には散気用給気管17と開閉バルブ
10を連結し、前記集水逆洗管6には三次処理水
の通水管8と開閉バルブ10を連結し、当該通水
管8には開閉バルブ14を介して逆洗用給気管1
3を、また、開閉バルブ20を介して逆洗用通水
管19を夫々配管し、その内、逆洗用給気管13
と前記散気用給気管17とを合流させてブロアB
と連結し、前記逆洗用通水管19には、逆洗槽9
の三次処理水を汲み上げる逆洗用給水ポンプ21
を連結し、前記上部室15の上方から下部室2ま
で縦貫する汚泥汲み上げ用清掃管24を立設支持
したことを特徴とする玉石過装置。 4 三次処理用過槽Tの上方部に二次処理水の
汚水導入管1と逆洗トラフ22を設け、当該過
槽Tの下方部にロストル4を設け、当該ロストル
4の上部には、好気性微生物を付着繁殖させる玉
石5,5a,5bを多段に積み上げ、その内、下
段部の下部側には100〜150mm径程度の比較的大き
い玉石5を、その上部側には60〜100mm径程度の
中位の玉石5bを、また、上段部には30〜60mm径
程度の比較的小さい玉石5aを、上下に夫々高さ
75〜50cm程度積み上げ、前記ロストル4下部の下
部室2には、両側部と下方部に通水兼通気孔7を
穿設した三次処理水の集水機能と空気逆洗機能の
集水逆洗管6を横設し、前記玉石5,5a,5b
上部の上部室15には散気管16を配管し、当該
散気管16には散気用給気管17と開閉バルブ1
0を連結し、前記集水逆洗管6には三次処理水の
通水管8と開閉バルブ10を連結し、当該通水管
8には開閉バルブ14を介して逆洗用給気管13
を、また、開閉バルブ20を介して逆洗用通水管
19を夫々配管し、その内、逆洗用給気管13と
前記散気用給気管17とを合流させてブロアBと
連結し、前記逆洗用通水管19には、逆洗槽9の
三次処理水を汲み上げる逆洗用給水ポンプ21を
連結し、前記上部室15の上方から下部室2まで
縦貫する汚泥汲み上げ用清掃管24を立設支持し
たことを特徴とする玉石過装置。[Scope of Claims] 1. A sewage inlet pipe 1 and a backwash trough 22 for secondary treated water are provided in the upper part of the tertiary treatment tank T, and a rostre 4 is provided in the lower part of the tertiary tank T. At the top of the cobblestones, boulders 5 and 5a for adhering and propagating aerobic microorganisms are piled up in multiple tiers, among which relatively large boulders 5 with a diameter of about 100 to 150 mm are placed in the lower tier, and stones 5 with a diameter of 30 to 60 mm are placed in the upper tier. relatively small boulder 5a
Alternatively, pile up medium-sized cobblestones of about 60 to 100 mm in diameter to a height of about 75 to 50 cm on the top and bottom, respectively.
On the lower side of the lower chamber 2 in the lower part, a collection pipe 6 for tertiary treated water with water passage holes 7 bored on both sides and the lower part is installed horizontally. An air backwash pipe 11 with a fumarole hole 12 perforated therein is orthogonal to the water collection pipe 6, and is branched in parallel to the right below the rostre 4, and is connected to the upper chamber 15 above the boulders 5, 5a. An air diffuser pipe 16 is connected to the air backwash pipe 11, and an air backwash air supply pipe 13 and an open/close valve 14 are connected to the air diffuser pipe 16. A valve 18 is connected to connect the air supply pipe 17 for aeration and the air supply pipe 13 for air backwashing to be connected to the blower B, and an on-off valve 10 is connected to the water flow pipe 8 for the tertiary treated water connected to the water collection pipe 6. and connect the water pipe 8 and the backwash tank 9 to the backwash water pipe 1.
9, an on-off valve 20 and a backwash water supply pump 21 are connected to the backwash water pipe 19, and a lower chamber 2 extends vertically from above the upper chamber 15 to the lower chamber 2.
A cobblestone filtering device characterized in that a cleaning pipe 24 for pumping up sludge is vertically supported. 2 A sewage inlet pipe 1 and a backwash trough 22 for secondary treatment water are provided in the upper part of the tertiary treatment tank T, a rostre 4 is provided in the upper part of the tertiary tank T, and a suitable Cobblestones 5, 5a, and 5b on which airborne microorganisms can adhere and propagate are piled up in multiple tiers, and among them, a relatively large cobblestone 5 with a diameter of about 100 to 150 mm is placed on the lower side of the lower tier, and a relatively large cobblestone 5 with a diameter of about 60 to 100 mm is placed on the upper side. A medium-sized cobblestone 5b is placed in the upper part, and a relatively small cobblestone 5a with a diameter of about 30 to 60mm is placed in the upper and lower parts, respectively.
They are piled up about 75 to 50 cm, and there are water holes 7 on both sides and the lower part of the lower chamber 2 at the bottom of the rostle 4.
A collection pipe 6 for tertiary treated water is installed horizontally, and fumarole holes 12 are installed on both sides of the upper part of the lower chamber 2.
An air backwash pipe 11 with a perforation is arranged perpendicularly to the water collecting pipe 6 and is arranged in parallel directly below the rostrum 4 to branch into the upper chamber 15 above the boulders 5, 5a, 5b. An air diffuser pipe 16 is connected to the air backwash pipe 11, and an air backwash air supply pipe 13 and an on-off valve 14 are connected to the air diffuser pipe 16. , the diffuser air supply pipe 17 and the air backwash air supply pipe 13 are connected to the blower B, and the on-off valve 10 is attached to the tertiary treated water water flow pipe 8 connected to the water collection pipe 6. Then, the water pipe 8 and the backwash tank 9 are connected to the water pipe 1 for backwashing.
9, an on-off valve 20 and a backwash water supply pump 21 are connected to the backwash water pipe 19, and a cleaning pipe 24 for pumping up sludge that runs vertically from above the upper chamber 15 to the lower chamber 2 is erected and supported. A cobblestone filtering device that is characterized by: 3. A sewage inlet pipe 1 and a backwash trough 22 for secondary treated water are provided in the upper part of the tertiary treatment tank T, a rostre 4 is provided in the lower part of the tertiary tank T, and a suitable Cobblestones 5, 5a that allow airborne microorganisms to adhere and propagate are stacked in multiple tiers, with relatively large pebbles 5 with a diameter of about 100 to 150 mm in the lower tier and relatively small pebbles 5a with a diameter of 30 to 60 mm in the upper tier.
Alternatively, pile up medium-sized cobblestones of about 60 to 100 mm in diameter to a height of about 75 to 50 cm on the top and bottom, respectively.
In the lower chamber 2 at the bottom, water collection and backwash pipes 6 with water flow and ventilation holes 7 bored on both sides and the lower part, which have the function of collecting tertiary treated water and backwashing air, are installed horizontally. 5,5
An aeration pipe 16 is installed in the upper chamber 15 in the upper part of a, an air supply pipe 17 for aeration and an on-off valve 10 are connected to the aeration pipe 16, and a water supply pipe for tertiary treated water is connected to the water collection backwash pipe 6. 8 and an on-off valve 10, and a backwash air supply pipe 1 is connected to the water pipe 8 via an on-off valve 14.
3, and a backwashing water pipe 19 is installed through the on-off valve 20, and the backwashing air supply pipe 13 is connected to the backwashing supply pipe 13.
and the air diffuser supply pipe 17 are merged to form the blower B.
The backwash water pipe 19 is connected to a backwash tank 9.
Backwash water supply pump 21 that pumps up tertiary treated water
A cobblestone filtration device characterized in that a cleaning pipe 24 for pumping up sludge is vertically supported and connected to the upper chamber 15 and extends vertically from the upper chamber 15 to the lower chamber 2. 4 A sewage inlet pipe 1 and a backwash trough 22 for secondary treatment water are provided in the upper part of the tertiary treatment tank T, a rostre 4 is provided in the lower part of the tertiary tank T, and a suitable Cobblestones 5, 5a, and 5b on which airborne microorganisms can adhere and propagate are piled up in multiple tiers, and among them, a relatively large cobblestone 5 with a diameter of about 100 to 150 mm is placed on the lower side of the lower tier, and a relatively large cobblestone 5 with a diameter of about 60 to 100 mm is placed on the upper side. A medium-sized cobblestone 5b is placed in the upper part, and a relatively small cobblestone 5a with a diameter of about 30 to 60mm is placed in the upper and lower parts, respectively.
They are piled up about 75 to 50 cm, and the lower chamber 2 at the bottom of the rostle 4 has water passage and ventilation holes 7 on both sides and the lower part to collect water for tertiary treatment water and for air backwashing. The pipe 6 is installed horizontally, and the boulders 5, 5a, 5b
An aeration pipe 16 is connected to the upper chamber 15 in the upper part, and an air supply pipe 17 for aeration and an on-off valve 1 are connected to the aeration pipe 16.
0 is connected to the water collection backwash pipe 6, and a water flow pipe 8 for tertiary treated water and an on-off valve 10 are connected to the water collection backwash pipe 6, and a backwash air supply pipe 13 is connected to the water flow pipe 8 via an on-off valve 14.
In addition, a backwashing water pipe 19 is installed through the on-off valve 20, and the backwashing air supply pipe 13 and the aeration air supply pipe 17 are merged and connected to the blower B. A backwash water supply pump 21 for pumping up the tertiary treated water from the backwash tank 9 is connected to the backwash water pipe 19, and a cleaning pipe 24 for pumping up sludge that runs vertically from above the upper chamber 15 to the lower chamber 2 is connected to the backwash water pipe 19. A cobblestone filtering device characterized by being installed and supported.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58174600A JPS6068014A (en) | 1983-09-21 | 1983-09-21 | Filtration device using pebble |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58174600A JPS6068014A (en) | 1983-09-21 | 1983-09-21 | Filtration device using pebble |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6068014A JPS6068014A (en) | 1985-04-18 |
JPH0521602B2 true JPH0521602B2 (en) | 1993-03-25 |
Family
ID=15981404
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58174600A Granted JPS6068014A (en) | 1983-09-21 | 1983-09-21 | Filtration device using pebble |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6068014A (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49127268A (en) * | 1973-04-10 | 1974-12-05 | ||
JPS5396261A (en) * | 1977-04-14 | 1978-08-23 | Ataka Kougiyou Kk | Method of treating highly organic waste water |
JPS5667511A (en) * | 1979-11-07 | 1981-06-06 | Kotobuki Kakoki Kk | Washing method of filter layer which comprises particulate filter medium |
-
1983
- 1983-09-21 JP JP58174600A patent/JPS6068014A/en active Granted
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS49127268A (en) * | 1973-04-10 | 1974-12-05 | ||
JPS5396261A (en) * | 1977-04-14 | 1978-08-23 | Ataka Kougiyou Kk | Method of treating highly organic waste water |
JPS5667511A (en) * | 1979-11-07 | 1981-06-06 | Kotobuki Kakoki Kk | Washing method of filter layer which comprises particulate filter medium |
Also Published As
Publication number | Publication date |
---|---|
JPS6068014A (en) | 1985-04-18 |
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