JP2936524B2 - Pesticide removal equipment - Google Patents

Pesticide removal equipment

Info

Publication number
JP2936524B2
JP2936524B2 JP3048778A JP4877891A JP2936524B2 JP 2936524 B2 JP2936524 B2 JP 2936524B2 JP 3048778 A JP3048778 A JP 3048778A JP 4877891 A JP4877891 A JP 4877891A JP 2936524 B2 JP2936524 B2 JP 2936524B2
Authority
JP
Japan
Prior art keywords
water
cartridge
activated carbon
filter medium
pipe
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
Application number
JP3048778A
Other languages
Japanese (ja)
Other versions
JPH04267985A (en
Inventor
功 藤村
英夫 加藤
安司 村木
慶三 梶岡
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Suido Kiko Kaisha Ltd
Original Assignee
Suido Kiko Kaisha Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by Suido Kiko Kaisha Ltd filed Critical Suido Kiko Kaisha Ltd
Priority to JP3048778A priority Critical patent/JP2936524B2/en
Publication of JPH04267985A publication Critical patent/JPH04267985A/en
Application granted granted Critical
Publication of JP2936524B2 publication Critical patent/JP2936524B2/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

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  • Water Treatment By Sorption (AREA)

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【産業上の利用分野】この発明は排水に溶解した農薬を
分離除去すべき装置に関するものである。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to an apparatus for separating and removing pesticides dissolved in wastewater.

【0002】[0002]

【従来の技術】従来、排水中に溶解した農薬除去装置と
しては、粒状活性炭を充填したろ過装置や、粉末活性炭
を注入する装置等が知られている。
2. Description of the Related Art Conventionally, as a device for removing pesticides dissolved in wastewater, a filtration device filled with granular activated carbon, a device for injecting powdered activated carbon, and the like are known.

【0003】[0003]

【発明が解決しようとする課題】上記したように、排水
中の農薬を除去する方法として粒状活性炭による処理装
置が提案されているが、粒状活性炭処理は平均径1mm
程度の活性炭粒子を層高1m程度充填した吸着層を通過
させるものであり、通水のための圧力損失が大きいし、
処理対象水の濁質による目づまりを防止するために定期
的に吸着層を洗浄する操作やそのためのポンプ、ポンプ
槽、逆洗用水貯槽、逆洗排水槽、関連配管等の設備を必
要とする。これは農薬を散布するゴルフ場や田畑の排水
が、配管系統を地下に埋設して、動水勾配を利用した自
然流下方式で行なわれている状況から、上記のような設
備の配置には大掛かりな増設、改良工事が必要となる。
As described above, a treatment apparatus using granular activated carbon has been proposed as a method for removing pesticides in wastewater, but the granular activated carbon treatment has an average diameter of 1 mm.
Activated carbon particles are passed through an adsorption layer filled with a bed height of about 1 m, and the pressure loss for water flow is large,
In order to prevent clogging due to turbidity of the water to be treated, an operation for periodically cleaning the adsorption layer and a pump, a pump tank, a backwash water storage tank, a backwash drain tank, and related piping are required. This is because the drainage of golf courses and fields where pesticides are sprayed is carried out by a natural flow method using a hydraulic gradient with a piping system buried underground, so the arrangement of the above facilities is large. Additional expansion and improvement work is required.

【0004】また粒状活性炭装置では活性炭充填時に活
性炭微粉末が飛び、作業環境が悪化したり、吸着能力を
失った活性炭を交換する時の水に濡れた活性炭の抜き出
し作業の煩わしさといった維持管理上の問題もあり、農
薬使用者側の管理能力では対応しきれないと言った問題
がある。
Further, in the granular activated carbon apparatus, the activated carbon fine powder flies when the activated carbon is charged, and the working environment is deteriorated, and the maintenance work such as the troublesome work of extracting the activated carbon wetted with water when exchanging the activated carbon having lost the adsorbing ability is considered. However, there is a problem that the management ability of the pesticide user cannot cope with the problem.

【0005】[0005]

【課題を解決するための手段】ここにおいてこの発明は
分離槽内の上部に流入水分配管を設置し、前記分離槽内
を、スリット状の開口部を形成した隔壁で区画し、これ
ら隔壁によって仕切られた各小室内に繊維状活性炭を袋
に詰めたカートリッジ状吸着ろ材を載置すると共に、各
小室の底部に排水用の集水枝管を設け、かつ前記カート
リッジ状吸着ろ材を常に水に浸かった状態にすべく処理
水排水管を前記集水枝管から立ち上げて形成し、前記カ
ートリッジ状吸着ろ材を通過した水を前記処理水排水管
を介して排水するようにしたことを特徴とする農薬除去
装置を提案するものである。
According to the present invention, an inflowing water pipe is provided at an upper portion in a separation tank, and the inside of the separation tank is partitioned by partitions having slit-shaped openings, and the partitions are partitioned by the partitions. In each of the small chambers, a cartridge-like adsorption filter material packed in a bag of fibrous activated carbon was placed, and a drainage collecting pipe was provided at the bottom of each small chamber, and the cartridge-like adsorption filter material was always immersed in water. A pesticide removal method, wherein a treated water drainage pipe is raised from the water collecting branch pipe to form a state, and water passing through the cartridge-shaped adsorption filter medium is drained through the treated water drainage pipe. A device is proposed.

【0006】[0006]

【作用】この発明の上記装置において、分離槽内に、前
記カートリッジ状の吸着ろ材を複層載置し、流入水分配
管からろ過すべき水を流下させ、前記吸着ろ材に農薬を
分離処理するものである。
In the above apparatus of the present invention, the cartridge-shaped adsorption filter medium is placed in a multi-layered state in a separation tank, water to be filtered is caused to flow down from an inflowing water pipe, and the pesticide is separated into the adsorption filter medium. It is.

【0007】[0007]

【実施例】図1ないし図3によって装置の構造を示す。
排水管(図示せず)から装置への流入部にはトラフ状の
流入水分配管1が設けられ、後述するろ材層に排水を均
等に流下させる。図示の場合、隔壁2によって4室に分
けられた吸着ろ材3は1室当り6袋の網状の袋に詰めた
カートリッジ4によって構成され、4室では24袋にな
っている。水は吸着ろ材3を通過し、各小室の底部に設
けられた集水枝管5により均等に集められ、ろ材を常に
水に浸った状態にするために立上げた処理水排水管6に
より排水される。装置にはその他に豪雨、湧水等による
異常な流入に対して排水機能を確保するためのオーバフ
ロー管7と装置の清掃時の排水のためのドレン配管8を
設けている。また、網状の袋に詰めたカートリッジ4
(図2)の充填層高を変化させた時に、吸着層前面に流
入水が均等に分配されるように隔壁2にスリット状の開
口部9を設けている(図3参照)。
1 to 3 show the structure of the apparatus.
A trough-shaped inflow moisture pipe 1 is provided at an inflow portion from a drainage pipe (not shown) to the apparatus, and the drainage water uniformly flows down to a filter medium layer described later. In the case shown in the figure, the adsorption filter medium 3 divided into four chambers by the partition walls 2 is constituted by cartridges 4 packed in a net-like bag of six bags per chamber, and there are 24 cartridges in four chambers. Water passes through the adsorbing filter medium 3 and is uniformly collected by a water collecting branch pipe 5 provided at the bottom of each small chamber, and is drained by a treated water drain pipe 6 that is set up to keep the filter medium constantly immersed in water. You. In addition, the apparatus is provided with an overflow pipe 7 for securing a drainage function against abnormal inflow due to heavy rain, spring water and the like, and a drain pipe 8 for drainage when cleaning the apparatus. The cartridge 4 packed in a net-like bag
When the height of the packed bed in FIG. 2 is changed, a slit-shaped opening 9 is provided in the partition wall 2 so that the inflow water is evenly distributed on the front surface of the adsorbing layer (see FIG. 3).

【0008】上述の構成からなるこの発明の装置による
ろ過作用を従来の粒状活性炭による方法と比較しつつ以
下の説明をすすめる。 (1)粒状活性炭と較べて次のような特性を持った繊維
状活性炭をろ材として使用し、ろ材層の層高の低減と通
水時の圧力損失の低減をはかり、自然流下方式での処理
を可能にする。すなわち、活性炭の細孔の孔径分布が
揃っており、しかも25オングストローム以下の細孔で
形成されているので、比表面積や外表面積が粒状活性炭
とくらべて大きいため農薬に対する吸着能力や吸着速度
が大きい。結果として吸着層の層高を低減できる。細
孔分布が25オングストローム以下に揃っているため、
種々の汚染物質中から分子量200〜300程度の農薬
を選択的に吸着する。綿状の繊維状活性炭は充填重量
と充填容積を変化させることによって、充填密度を変え
ることができるがこの発明では20〜80kg/m3と
する。充填密度が小さいために充填層は空隙部が多く、
濁質の保持量が大きくなり、結果として目づまりしにく
い。
[0008] The following description will be made while comparing the filtering action of the apparatus of the present invention having the above-mentioned structure with the conventional method using granular activated carbon. (1) Compared to granular activated carbon, fibrous activated carbon having the following characteristics is used as a filter medium to reduce the height of the filter medium layer and the pressure loss during water passage, and to be treated by a natural flow method. Enable. In other words, the pore size distribution of the activated carbon pores is uniform, and the pores are formed with pores of 25 angstroms or less, so that the specific surface area and the outer surface area are larger than that of the granular activated carbon, so that the adsorption ability and the adsorption speed for pesticides are large. . As a result, the height of the adsorption layer can be reduced. Since the pore distribution is less than 25 angstroms,
Agrochemicals having a molecular weight of about 200 to 300 are selectively adsorbed from various contaminants. The packing density of the flocculent fibrous activated carbon can be changed by changing the filling weight and the filling volume, but in the present invention, it is set to 20 to 80 kg / m3. Due to the low packing density, the packed layer has many voids,
The amount of suspended matter retained becomes large, and as a result, clogging is difficult.

【0009】(2)上記繊維状活性炭を層高100mm
程度にナイロンないしビニロン(共に商標)製の網で袋
状に縫製したカートリッジに詰めることで、ろ床に2
段、3段に小分け充填して活性炭の充填量を変える。 (3)上記網目袋カートリッジは充填密度と充填容量を
現場で調整できるものと保持される結果、操作時の水の
短絡を防ぐ。 (4)上記繊維状活性炭はカートリッジに充填され、支
持網により流出を防止するので通常のろ床で使われる支
持砂利層及び多孔板のような集水装置の役割を果す。 (5)ケーシングに充填したカートリッジの交換時には
上段部のカートリッジを取り除き、新しいカートリッジ
を下段に、下段のカートリッジを上段にまわすことで、
流入水の入口側の濃度の高い水と接触させ活性炭の有効
利用をはかる。
(2) The above fibrous activated carbon is 100 mm thick
Packed into a cartridge sewn into a bag with nylon or vinylon (both trademarks) mesh to a degree,
Filling is divided into three stages and the amount of activated carbon is changed. (3) The mesh bag cartridge is maintained so that the filling density and the filling capacity can be adjusted on site, thereby preventing a short circuit of water during operation. (4) The fibrous activated carbon is filled in a cartridge and is prevented from flowing out by a supporting net, so that it functions as a supporting gravel layer and a water collecting device such as a perforated plate used in an ordinary filter bed. (5) When replacing the cartridge filled in the casing, remove the upper cartridge and turn the new cartridge to the lower and the lower cartridge to the upper.
The activated carbon is brought into contact with highly concentrated water on the inlet side of the influent water to make effective use of activated carbon.

【0010】(6)ケーシングに底部隔壁で小室を設け
ることで、カートリッジを圧密充填する際、袋の数で確
実に所定の充填容量と充填密度を作りだすことができ、
流入水を均等に吸着層に供給できる。 (7)隔壁にスリット状開口部を設け、カートリッジの
充填層高に対応することで、ケーシング内の各小室の水
位を同じにして、各室の流れを均一にする。
(6) By providing a small chamber with a bottom partition in the casing, it is possible to reliably produce a predetermined filling capacity and filling density by the number of bags when compacting and filling the cartridge.
The inflow water can be evenly supplied to the adsorption bed. (7) By providing a slit-shaped opening in the partition wall and corresponding to the height of the packed bed of the cartridge, the water level of each small chamber in the casing is made equal, and the flow of each chamber is made uniform.

【0011】図4は繊維状活性炭を層高3cm及び5c
m充填し、農薬を除去したときの結果である。層高2c
mでは入口の農薬を完全には除去できないが、層高5c
mでは完全に除去している。図5は活性炭充填密度50
kg/m3、層高10cmの繊維状活性炭層に通水した
ときの通水線速度と圧力損失の関係である。液通水線速
度10m/日〜240m/日で層高10cm当りの圧力
損失は1cm〜15cmであり、カートリッジを2段、
3段に載置しても3cm〜45cmであり、この程度の
圧力であれば、自然流下の水頭で通水できる。
FIG. 4 shows that fibrous activated carbon is layered at a height of 3 cm and 5 c.
This is the result when m was filled and the pesticide was removed. Layer height 2c
m, pesticides at the entrance cannot be completely removed,
m removes completely. FIG. 5 shows the activated carbon packing density of 50.
It is a relationship between a water line velocity and a pressure loss when water is passed through a fibrous activated carbon layer having a bed height of 10 cm in kg / m3. The pressure drop per layer height 10 cm is 1 cm to 15 cm at a liquid flow velocity of 10 m / day to 240 m / day,
Even if it is placed in three stages, it is 3 cm to 45 cm, and at such a pressure, water can flow through the head under natural flow.

【0012】[0012]

【発明の効果】上述の構成からなるこの発明の装置によ
れば次のような効果が得られる。 (1)農薬が散布されるゴルフ場や田畑の排水系統は、
土中に埋設された配管や、側溝により自然流下方式で排
水される場合が多いが、この装置では僅か20〜30c
mの層高に載置した繊維状活性炭のカートリッジろ材に
より、低圧力損失下で農薬を排水中から分離除去できる
ので、配水管系統の中に装置を設置することが可能であ
り、粒状活性炭のような送水ポンプ、逆洗水槽、逆洗配
水槽等の設置も不要であり、したがって建設費の低減に
なる。 (2)網状の袋に詰めたカートリッジに詰められた繊維
状活性炭3は、人手により簡単にろ材の充填及び除去が
できる。すなわち隔壁で仕切られた小室に充填するカー
トリッジの数を調整して、均一に充填でき、抜出し時に
も簡単に取りだしができる。活性炭の能力低下や流入水
の農薬量の増加等で処理水が悪化した場合でも、カート
リッジを交換することにより迅速に対応ができる。 (3)繊維状活性炭を網目の袋状カートリッジでろ床に
充填しても、充填容量が大きいと、カートリッジは自在
に変形してしまい、均一にろ材を充填することは難しい
が、隔壁によって小室を設けることにより、小室内のカ
ートリッジは隔壁により他室のカートリッジとの相互作
用から切り離され、小室内で充填密度と充填容量を調整
することが可能になる。
According to the apparatus of the present invention having the above configuration, the following effects can be obtained. (1) The drainage system for golf courses and fields where pesticides are sprayed,
In many cases, drainage is carried out in a natural flow manner by pipes buried in the soil or by gutters.
The filter media for fibrous activated carbon placed at the height of m can separate and remove pesticides from wastewater under low pressure loss, so it is possible to install equipment in the water distribution pipe system, Installation of such a water pump, a backwash water tank, a backwash water distribution tank, etc. is unnecessary, and thus the construction cost is reduced. (2) The fibrous activated carbon 3 packed in a cartridge packed in a net-like bag can be easily filled and removed with a filter medium by hand. In other words, the number of cartridges to be filled in the small chambers partitioned by the partition walls can be adjusted, and the cartridges can be uniformly filled, and can be easily taken out at the time of extraction. Even if the treated water deteriorates due to a decrease in the activated carbon capacity, an increase in the amount of the pesticide in the inflow water, or the like, it is possible to quickly respond by replacing the cartridge. (3) Even if fibrous activated carbon is filled in a filter bed with a mesh bag-shaped cartridge, if the filling capacity is large, the cartridge is deformed freely and it is difficult to fill the filter medium uniformly. With the provision, the cartridge in the small chamber is separated from the interaction with the cartridge in the other chamber by the partition wall, and the packing density and the filling capacity can be adjusted in the small chamber.

【図面の簡単な説明】[Brief description of the drawings]

【図1】この発明の装置の概要を示す斜視図である。FIG. 1 is a perspective view showing an outline of an apparatus of the present invention.

【図2】カートリッジ状の吸着ろ材の単体を示す斜視図
である。
FIG. 2 is a perspective view showing a single unit of a cartridge-shaped adsorption filter medium.

【図3】装置内の隔壁の態様を示す斜視図である。FIG. 3 is a perspective view showing an aspect of a partition in the apparatus.

【図4】農薬(ダイアヅノン)吸着試験結果を示すグラ
フである。
FIG. 4 is a graph showing the results of a pesticide (diadinone) adsorption test.

【図5】繊維状活性炭層の初期通水圧力損失の状況を示
すグラフである。
FIG. 5 is a graph showing the state of the initial water pressure loss of the fibrous activated carbon layer.

【符号の説明】[Explanation of symbols]

1 流入水分配管 2 隔壁 3 吸着ろ材 4 網状袋カートリッジ DESCRIPTION OF SYMBOLS 1 Inflow moisture piping 2 Partition wall 3 Adsorption filter media 4 Net bag cartridge

───────────────────────────────────────────────────── フロントページの続き (72)発明者 加藤 英夫 東京都狛江市岩戸南3−10−12 パ−ル ハウス201 (72)発明者 村木 安司 神奈川県藤沢市辻堂西海岸2丁目3−11 −102 (72)発明者 梶岡 慶三 奈良県奈良市鶴舞西町2−16 エクセル 鶴舞A−503 (56)参考文献 特開 昭60−64686(JP,A) 特開 昭60−225641(JP,A) 実開 昭62−187698(JP,U) ──────────────────────────────────────────────────続 き Continuing on the front page (72) Inventor Hideo Kato 3-10-12 Iwato Minami, Komae-shi, Tokyo Paru House 201 (72) Inventor Yasushi Muraki 2-3-1-11 Tsujido Nishi Kaigan, Tsujido-shi, Fujisawa-shi, Kanagawa (72) Inventor Keizo Kajioka 2-16 Tsurumai Nishi-machi, Nara City, Nara Prefecture Excel Tsurumai A-503 1962-9898 (JP, U)

Claims (1)

(57)【特許請求の範囲】(57) [Claims] 【請求項1】 離槽内の上部に流入水分配管を配置
、前記分離槽内を、スリット状の開口部を形成した隔
壁で区画し、これら隔壁によって仕切られた各小室内
繊維状活性炭を袋に詰めたカートリッジ状吸着ろ材を載
すると共に、各小室の底部に排水用の集水枝管を設
け、かつ前記カートリッジ状吸着ろ材を常に水に浸かっ
た状態にすべく処理水排水管を前記集水枝管から立ち上
げて形成し、前記カートリッジ状吸着ろ材を通過した水
を前記処理水排水管を介して排水するようにしたことを
特徴とする農薬除去装置。
1. A partial placing the inflow water pipe on top of the release tank, the separation tank, to form a slit-shaped opening septum
A cartridge-like adsorption filter medium packed in a bag of fibrous activated carbon is placed in each of the small compartments partitioned by walls, and a collecting branch pipe for drainage is installed at the bottom of each small compartment.
And always immerse the cartridge-shaped adsorption filter medium in water.
Rise the treated water drain pipe from the collecting branch pipe
Water that has passed through the cartridge-shaped adsorption filter medium
Is discharged through the treated water drain pipe .
JP3048778A 1991-02-22 1991-02-22 Pesticide removal equipment Expired - Lifetime JP2936524B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP3048778A JP2936524B2 (en) 1991-02-22 1991-02-22 Pesticide removal equipment

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP3048778A JP2936524B2 (en) 1991-02-22 1991-02-22 Pesticide removal equipment

Publications (2)

Publication Number Publication Date
JPH04267985A JPH04267985A (en) 1992-09-24
JP2936524B2 true JP2936524B2 (en) 1999-08-23

Family

ID=12812718

Family Applications (1)

Application Number Title Priority Date Filing Date
JP3048778A Expired - Lifetime JP2936524B2 (en) 1991-02-22 1991-02-22 Pesticide removal equipment

Country Status (1)

Country Link
JP (1) JP2936524B2 (en)

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN105347479B (en) * 2015-11-22 2017-10-13 南通大学 A kind of unpowered denitrogenation experimental provision of rural area cesspool sewage and its application method

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6064686A (en) * 1983-09-16 1985-04-13 Ebara Infilco Co Ltd Water purifying treatment
JPS60225641A (en) * 1984-04-25 1985-11-09 Zousui Sokushin Center Regeneration of fibrous activated carbon
JPS62187698U (en) * 1986-05-17 1987-11-28

Also Published As

Publication number Publication date
JPH04267985A (en) 1992-09-24

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