JPS6329042B2 - - Google Patents
Info
- Publication number
- JPS6329042B2 JPS6329042B2 JP9406083A JP9406083A JPS6329042B2 JP S6329042 B2 JPS6329042 B2 JP S6329042B2 JP 9406083 A JP9406083 A JP 9406083A JP 9406083 A JP9406083 A JP 9406083A JP S6329042 B2 JPS6329042 B2 JP S6329042B2
- Authority
- JP
- Japan
- Prior art keywords
- filter
- landfill
- water
- permeable membrane
- adsorption
- 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
Links
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 22
- 238000001914 filtration Methods 0.000 claims description 13
- 239000012528 membrane Substances 0.000 claims description 11
- 238000001179 sorption measurement Methods 0.000 claims description 11
- 238000000034 method Methods 0.000 claims description 7
- 238000002203 pretreatment Methods 0.000 claims description 6
- 239000002351 wastewater Substances 0.000 claims description 6
- 230000015271 coagulation Effects 0.000 claims description 4
- 238000005345 coagulation Methods 0.000 claims description 4
- 239000002245 particle Substances 0.000 claims description 4
- 239000000126 substance Substances 0.000 claims description 4
- 239000010802 sludge Substances 0.000 claims description 2
- 239000002689 soil Substances 0.000 claims 1
- 239000000725 suspension Substances 0.000 claims 1
- 239000007787 solid Substances 0.000 description 8
- 238000002347 injection Methods 0.000 description 5
- 239000007924 injection Substances 0.000 description 5
- 238000010276 construction Methods 0.000 description 3
- 239000004576 sand Substances 0.000 description 2
- 238000004062 sedimentation Methods 0.000 description 2
- 239000000701 coagulant Substances 0.000 description 1
- 238000007796 conventional method Methods 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
Classifications
-
- E—FIXED CONSTRUCTIONS
- E02—HYDRAULIC ENGINEERING; FOUNDATIONS; SOIL SHIFTING
- E02B—HYDRAULIC ENGINEERING
- E02B3/00—Engineering works in connection with control or use of streams, rivers, coasts, or other marine sites; Sealings or joints for engineering works in general
- E02B3/18—Reclamation of land from water or marshes
Landscapes
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Ocean & Marine Engineering (AREA)
- Mechanical Engineering (AREA)
- Civil Engineering (AREA)
- Structural Engineering (AREA)
- Cleaning Or Clearing Of The Surface Of Open Water (AREA)
Description
【発明の詳細な説明】
本発明は、浚渫泥、廃棄物および陸上土砂等に
よる水面埋立地の余水処理工法に係るものであ
る。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for treating surplus water from a water surface landfill using dredged mud, waste, land earth, and the like.
従来の余水処理工法としては、泥水送泥管にお
ける凝集剤の直接注入またはシヤワー添加工法、
凝集沈澱池設置工法および砂濾過槽設置等の各工
法が用いられてきたが、これらの工法は埋立過程
中の余水の水質変化に対応できなかつたり、工事
終期にのみ使用する必要が生じたりして余水処理
施設費が埋立工事全体の経済性からみて妥当でな
かつた事例が多い。これらは上記各工法とも余水
の排水濃度を必要以上に清澄なものにする機能を
持たせていること、埋立地余水の水質変化が把握
できていなかつたこと等が大きい原因となつてい
る。 Conventional methods for treating surplus water include direct injection of coagulant into muddy water pipes or shower addition method;
Various methods have been used, such as installing a coagulation sedimentation tank and installing a sand filter tank, but these methods cannot cope with changes in the quality of surplus water during the reclamation process, or need to be used only at the final stage of construction. There are many cases where the cost of surplus water treatment facilities was not appropriate from the economical point of view of the overall reclamation work. The major causes of these problems include the fact that each of the above construction methods has a function to make the wastewater concentration of wastewater clearer than necessary, and that changes in the water quality of wastewater from landfills have not been ascertained. .
本発明は、余水の排水基準が浮遊物質量(SS)
=50ppm以下となつている工事を対象とし、凝集
剤の直接注入工法と前処理濾過および吸着濾過の
2重濾過工法によつて構成し、余水の浮遊物質量
を極度に低減させることなく、確実に排水基準を
満足させる凝集濾過工法である。以下図面につい
て発明の内容を説明する。 In the present invention, the drainage standard for surplus water is the amount of suspended solids (SS).
= 50ppm or less, and consists of a double filtration method of direct injection of flocculant, pre-treatment filtration and adsorption filtration, without extremely reducing the amount of suspended solids in surplus water. This is a coagulation filtration method that reliably satisfies wastewater standards. The content of the invention will be explained below with reference to the drawings.
第1図は、本発明の余水の濾過処理方法を説明
する平面図であり、図中埋立護岸1により囲まれ
た埋立地へ泥水を流入させる排泥管2の任意の位
置において薬品注入装置3により凝集剤を注入さ
せる。埋立地内で発生した余水は、導流築堤4の
先端を迂回し、前処理濾過機5と吸着濾過体6を
通過することにより、浮遊物質量を減じて排水基
準値下の水質となり、余水吐7から周辺水域に流
出する。 FIG. 1 is a plan view illustrating the surplus water filtration method of the present invention. In the figure, a chemical injection device is installed at an arbitrary position of a mud drain pipe 2 that flows muddy water into a reclaimed land surrounded by a reclaimed seawall 1. Step 3: Inject the flocculant. The surplus water generated in the landfill bypasses the tip of the diversion embankment 4 and passes through the pre-treatment filter 5 and adsorption filter 6 to reduce the amount of suspended solids and bring the water quality below the wastewater standard value. It flows out from waterway 7 into the surrounding water area.
第2図は、本発明の前処理濾過機と吸着断面構
成を示すものであり、図中前処理濾過機は、透水
膜8を駆動プーリー9、反転プーリー10にか
け、駆動装置11に連動する歯車装置を介して透
水膜の通水断面を変え、このとき刷毛12により
透水膜面に付着した余水中の浮遊凝集粒子を下方
にかき落す。フレーム13は保持杭14に装着さ
れる。 FIG. 2 shows the pretreatment filter and adsorption cross-sectional configuration of the present invention. The cross section of the water-permeable membrane is changed through the device, and at this time, the brush 12 scrapes the suspended agglomerated particles in the residual water adhering to the surface of the water-permeable membrane downward. The frame 13 is attached to the holding stakes 14.
吸着濾過体は、網袋入り粗粒濾材15を積上
げ、両側の保持杭に設けた柵板16内に収容し構
成する。埋立地内の沈澱堆積泥17は、工事の進
捗とともにその泥面が上昇し、透水膜の下部が埋
まるが、上部の濾過機能は確保できる。濾過装置
基礎18は、一般土砂等により構築する。 The adsorption filter body is constructed by stacking coarse filter media 15 in mesh bags and storing them in fence plates 16 provided on the holding stakes on both sides. As the construction progresses, the surface of the settled mud 17 in the landfill will rise and the lower part of the permeable membrane will be buried, but the filtration function of the upper part can be maintained. The filtration device foundation 18 is constructed of general earth and sand.
第3図は、本発明の前処理濾過機正面図で、図
中透水膜8は駆動プーリー9と反転プーリー10
により展張されており、フレーム13は背後の保
持杭14に装着されている。 FIG. 3 is a front view of the pretreatment filter of the present invention, in which the water permeable membrane 8 is connected to the drive pulley 9 and the reversing pulley 10.
The frame 13 is attached to a holding stake 14 at the rear.
以上説明した本発明の凝集沈澱濾過方法の試験
例として、流入余水の浮遊物質量(SS)=60ppm
(平均)に対し、前処理濾過機で(SS)=20ppm
(平均)吸着濾過装置で(SS)=15ppm(平均)程
度のSS低減量となつている。これは余水中の凝
集粒子がほゞ前処理濾過機の透水膜に捕捉される
ことを示している。凝集剤の種類、薬注量および
透水膜材質等は、現地の水質に対応し設定される
ものである。 As a test example of the coagulation sedimentation filtration method of the present invention explained above, the amount of suspended solids (SS) of inflow surplus water = 60 ppm
(average), pre-treatment filter (SS) = 20ppm
(On average) The adsorption filtration device reduces SS by approximately 15 ppm (on average). This indicates that the aggregated particles in the residual water are almost captured by the water-permeable membrane of the pretreatment filter. The type of flocculant, the amount of chemical injection, the material of the permeable membrane, etc. are set according to the local water quality.
第1図は、本発明の余水の濾過処理方法を説明
する平面図で、図中1は埋立護岸、2は排泥管、
3は薬品注入装置、4は導流築堤、5は前処理濾
過機、6は吸着濾過体、7は余水吐である。第2
図は、本発明の前処理濾過機と吸着濾過体の設置
断面構成を示し、図中1は埋立護岸、7は余水
吐、8は透水膜、9は駆動プーリー、10は反転
プーリー、11は駆動装置、12は刷毛、13は
フレーム、14は保持杭、15は粗粒濾材、16
は柵板、17は沈澱堆積泥、18は濾過装置基礎
である。第3図は、本発明の前処理濾過機正面図
で、図中8は透水膜、9は駆動プーリー、10は
反転プーリー、13はフレーム、14は保持杭で
ある。
FIG. 1 is a plan view illustrating the surplus water filtration method of the present invention, in which 1 is a reclaimed bank, 2 is a sludge pipe,
3 is a chemical injection device, 4 is a diversion embankment, 5 is a pretreatment filter, 6 is an adsorption filter, and 7 is a spillway. Second
The figure shows the installation cross-sectional configuration of the pre-treatment filter and adsorption filter of the present invention, in which 1 is a landfill revetment, 7 is a spillway, 8 is a permeable membrane, 9 is a driving pulley, 10 is a reversing pulley, 11 12 is a drive device, 12 is a brush, 13 is a frame, 14 is a holding stake, 15 is a coarse filter medium, 16
1 is a fence board, 17 is sedimentary mud, and 18 is a filtration device foundation. FIG. 3 is a front view of the pretreatment filter of the present invention, in which 8 is a permeable membrane, 9 is a driving pulley, 10 is a reversing pulley, 13 is a frame, and 14 is a holding stake.
Claims (1)
を設け、保持枠内に網袋入りの粗粒濾材を収容し
て成る吸着濾過体を構成し、吸着濾過体の余水流
入側に透水膜を回転可能なように連接して成る前
処理濾過機を設け、前処理濾過機と吸着濾過体に
よる2段濾過装置により、埋立地へ流入する送泥
管において凝集剤を注入することにより、埋立地
内で発生する余水の凝集粒子を前処理濾過機の透
水膜面で付着除去し、透水膜面を通過した微粒土
分を吸着濾過体で除去するようにして、余水の浮
遊物質量を低減させることを特徴とする埋立地余
水の凝集濾過処理方法。1. A coarse filter medium holding frame is provided inside the landfill of the landfill spillway, and an adsorption filter is constructed by accommodating the coarse filter medium in a mesh bag within the holding frame, and the spillwater inflow side of the adsorption filter is A pre-treatment filter consisting of a water-permeable membrane rotatably connected is installed in the tank, and a flocculant is injected into the sludge pipe flowing into the landfill using a two-stage filtration device consisting of a pre-treatment filter and an adsorption filter. By using this method, the agglomerated particles of leftover water generated in the landfill are removed by the permeable membrane surface of the pretreatment filter, and the fine soil particles that have passed through the permeable membrane surface are removed by the adsorption filter, thereby reducing the suspension of leftover water. A coagulation filtration treatment method for wastewater from a landfill characterized by reducing the amount of substances.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9406083A JPS59220509A (en) | 1983-05-30 | 1983-05-30 | Coagulating filtration of spillway in landfill site |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP9406083A JPS59220509A (en) | 1983-05-30 | 1983-05-30 | Coagulating filtration of spillway in landfill site |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS59220509A JPS59220509A (en) | 1984-12-12 |
| JPS6329042B2 true JPS6329042B2 (en) | 1988-06-10 |
Family
ID=14099985
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP9406083A Granted JPS59220509A (en) | 1983-05-30 | 1983-05-30 | Coagulating filtration of spillway in landfill site |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS59220509A (en) |
-
1983
- 1983-05-30 JP JP9406083A patent/JPS59220509A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS59220509A (en) | 1984-12-12 |
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