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JPS6362604B2 - - Google Patents
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JPS6362604B2 - - Google Patents

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Publication number
JPS6362604B2
JPS6362604B2 JP9406183A JP9406183A JPS6362604B2 JP S6362604 B2 JPS6362604 B2 JP S6362604B2 JP 9406183 A JP9406183 A JP 9406183A JP 9406183 A JP9406183 A JP 9406183A JP S6362604 B2 JPS6362604 B2 JP S6362604B2
Authority
JP
Japan
Prior art keywords
filter
water
filtration device
landfill
filter plate
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
Application number
JP9406183A
Other languages
Japanese (ja)
Other versions
JPS59220510A (en
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 filed Critical
Priority to JP9406183A priority Critical patent/JPS59220510A/en
Publication of JPS59220510A publication Critical patent/JPS59220510A/en
Publication of JPS6362604B2 publication Critical patent/JPS6362604B2/ja
Granted legal-status Critical Current

Links

Classifications

    • EFIXED CONSTRUCTIONS
    • E02HYDRAULIC ENGINEERING; FOUNDATIONS; SOIL SHIFTING
    • E02BHYDRAULIC ENGINEERING
    • E02B3/00Engineering works in connection with control or use of streams, rivers, coasts, or other marine sites; Sealings or joints for engineering works in general
    • E02B3/18Reclamation 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)

Description

【発明の詳細な説明】[Detailed description of the invention]

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。従来の余水処理工法としては、泥水排送管に
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工法
等が用いられていたが、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
事終期においてのみ使用することが必要なだけで
余水処理施設費および工事費が埋立工事全体の経
済性から見て妥当でなかつたりした事例が多い。 水面埋立における余水水質は、一般に工事が緩
速埋立の場合に浮遊物質量(SS)=100ppm以下
であり、工事終期においてのみ埋立粒子の再浮上
を伴うため103〜104ppmのオーダになる。工事が
急速埋立の場合は緩速埋立の場合の工事終期の状
態が早期に出現する。 一方、埋立地から周辺水域への余水の排水基準
は、周辺水域環境への影響レベルに応じ、浮遊物
質量(SS)=20〜150ppm以下を基準とした事例
が多い。 上記の余水水質と排水基準を対比し、余水処理
工法による浮遊物質量の低減率を設定するのであ
るが、従来工法の単独使用、または凝集剤の直接
注入、シヤワー添加工法および凝集沈澱池設置工
法と砂濾過槽設置工法との組合せ工法は、排水基
準に対して必要以上に浮遊物質量を低減させる機
能を持ち、工事終期の高濃度余水水質に対応でき
ない装置もあり、技術上の非適合性と経済上の無
駄を生じることになる。本発明は、上記のような
技術上、経済上の問題を解決し、排水基準値に対
し必要最少値の浮遊物質量の除去を目的とする2
段濾過方式の埋立地余水の濾過処理方法である。 以下図面について本発明の内容を説明する。 第1図は、本発明の余水の濾過処理方法を説明
する埋立地の平面形状を示し、埋立護岸1により
囲まれた埋立地2へ浚渫泥、廃棄物(もえがら
等)の混合水を排泥管3から流入させる。流入地
点付近には、浚渫泥、廃棄物等の水面上露出部分
4が形成される。埋立地内の他の部分は、余水水
面下に浚渫泥、廃棄物等が沈澱堆積し、余水は埋
立地内の導流築堤5の先端を迂回し、本発明の前
処理濾過装置6、吸着濾過体7を通過することに
より、浮遊物質量を減じて排水基準値以下の水質
となり、余水吐口8を通過し余水吐管9から周辺
水域に流出する。 第2図は、本発明の前処理濾過装置6と吸着濾
過体7の設置断面構成を示したものである。前処
理濾過装置は濾過板10と濾過板が鉛直方向に着
脱できるガイド溝を有する濾過板保持柱11によ
り構成する。濾過体は、網袋等に入れた粗粒濾過
材12を積上げ、これを濾過板保持柱と粗粒濾材
保持柱13の粗粒濾材側に設けた間隙を有する柵
板14に収容して構成する。上部梁15は、濾過
板保持柱と粗粒濾材保持柱の連結梁である。余水
16の下方には浚渫泥、廃棄物粒子の沈澱堆積層
17が存在し、沈澱堆積表層は工事の進捗に伴い
上昇してくる。堆積層表面の上昇により、工事終
期において濾過板10は理殺しの状態になる。埋
立地内在来地盤18の上には、吸着濾過体の基礎
盛土19、護岸基礎20がある。 第3図は、本発明の前処理濾過装置の濾過板断
面を示し、濾過枠21内に濾過砂22を透水シー
トまたは透水マツト23によりサンドイツチ状に
挟んで収容したものである。濾過枠補強材24
は、透水マツトが外方に脹れるのを防ぐものであ
る。 第4図は、上記第3図に示した濾過板の正面図
である。本発明においては、限られた濾過材断面
を余水が急速通過できるように、上記のように前
処理濾過装置と吸着濾過体による2段濾過方法と
し、濾過材の目詰りが生じる前処理濾過装置の濾
過板は、順次に取替えて使用し、吸着濾過体の粗
粒濾材は、その吸着作用により、余水水質を排水
基準値以下に低減するものである。一般に濾過材
の透水係数は、次に示す表1の値となつている。
The present invention relates to a method for treating surplus water from a water surface landfill using dredged mud, waste, land sediment, and the like. Conventional methods for treating surplus water include direct injection of coagulant into muddy drainage pipes, shower addition method, coagulation sedimentation tank installation method, and sand filtration tank installation method. There have been cases where it was not possible to respond to changes in the quality of leftover water in the landfill, or where the cost of the leftover water treatment facility and construction costs were not appropriate from the economics of the overall reclamation work because it was necessary to use it only at the final stage of construction. many. Generally speaking, the quality of surplus water in water surface reclamation is less than 100 ppm (suspended solids (SS)) when the construction is slow reclamation, and is on the order of 10 3 to 10 4 ppm because reclaimed particles resurface only at the final stage of construction. Become. If the construction is rapid reclamation, the state at the end of construction in the case of slow reclamation will appear earlier. On the other hand, the standard for drainage of surplus water from a landfill to the surrounding water area is often based on a suspended solids (SS) of 20 to 150 ppm or less, depending on the level of impact on the environment of the surrounding water area. The above-mentioned wastewater quality and wastewater standards are compared to determine the reduction rate of suspended solids by the wastewater treatment method. The combination method of installation method and sand filtration tank installation method has the function of reducing the amount of suspended solids more than necessary in accordance with the drainage standards, and some devices cannot cope with the high concentration of leftover water quality at the end of construction. This will result in non-conformity and economic waste. The present invention solves the above-mentioned technical and economical problems, and aims to remove the amount of suspended solids to the minimum value necessary for the wastewater standard value.
This is a stage filtration method for filtration of waste water from a landfill. The contents of the present invention will be explained below with reference to the drawings. Figure 1 shows the planar shape of a reclaimed land for explaining the method of filtration of surplus water of the present invention, and shows a mixed water of dredged mud and waste (such as rice hulls) into a reclaimed land 2 surrounded by a reclaimed seawall 1. It is made to flow in from the mud removal pipe 3. Near the inflow point, an exposed portion 4 of dredged mud, waste, etc. is formed above the water surface. In other parts of the landfill, dredged mud, waste, etc. are deposited below the surface of the spill water, and the surplus water bypasses the tip of the diversion embankment 5 in the landfill, and the pretreatment filtration device 6 of the present invention and adsorption By passing through the filter 7, the amount of suspended solids is reduced and the quality of the water becomes below the drainage standard value, and the water passes through the spillway 8 and flows out from the spillway pipe 9 into the surrounding water area. FIG. 2 shows the installed cross-sectional configuration of the pretreatment filtration device 6 and adsorption filter body 7 of the present invention. The pretreatment filtration device is composed of a filter plate 10 and a filter plate holding column 11 having a guide groove in which the filter plate can be attached and removed in the vertical direction. The filter body is constructed by stacking up coarse filter media 12 placed in a net bag or the like, and storing this in a fence plate 14 having a gap provided on the coarse filter media side of the filter plate holding column and the coarse filter media holding column 13. do. The upper beam 15 is a connecting beam between the filter plate holding column and the coarse filter medium holding column. Below the spill water 16 there is a sediment layer 17 of dredged mud and waste particles, and the surface layer of sediment is rising as the construction progresses. Due to the rise in the surface of the deposited layer, the filter plate 10 will be in a dead state at the end of construction. On the native ground 18 within the reclaimed land, there are a foundation embankment 19 for the adsorption filter and a bank foundation 20. FIG. 3 shows a cross section of a filter plate of the pretreatment filtration device of the present invention, in which filter sand 22 is sandwiched and housed in a sandwich-like structure between water-permeable sheets or water-permeable mats 23 in a filter frame 21. Filter frame reinforcement material 24
This prevents the permeable pine from swelling outward. FIG. 4 is a front view of the filter plate shown in FIG. 3 above. In the present invention, a two-stage filtration method using a pretreatment filtration device and an adsorption filter body is used as described above so that surplus water can rapidly pass through a limited cross section of the filter medium. The filter plates of the device are replaced one after another, and the coarse filter medium of the adsorption filter reduces the quality of leftover water to below the wastewater standard value through its adsorption action. In general, the permeability coefficient of a filter medium has the values shown in Table 1 below.

【表】 第1表より、本発明の前処理濾過装置の濾過砂
を粗砂、透水係数k=0.35cm/sec、濾過板前後
の水位差h=10cm、濾過砂の通水距離l=5cmと
おき、濾過砂通水面積Aと通水量Qの関係を求め
ると Q=k・h・A/l =0.35×10×A÷5 =0.77Acm2/sec………25.2Am3/Hr・m2 上記の値は、余水量5000m3/Hrに対し、A=
200m2の通水断面積を必要とし、一般の埋立工事
において、前処理濾過装置の濾過板全通水高さ2
m、全通水幅100m程度が適用できることになる。
これより吸着濾過体の濾過材としては、第1表に
示す小砂利程度以上の粗粒濾材を用いる。 本発明の方法による場合の余水水質低減試験例
では、浮遊物質量(SS)=50ppm(平均)の余水
が前処理濾過装置で、ほゞ半分の25ppm(平均)
となり、吸着濾過体において、ほゞ1/5が低減し、
(SS)=20ppm(平均)となつて一般水域に流出し
た。粗粒濾材で構成される吸着濾過体の水位保持
は、余水吐の標高設定により定まる。 第5図は、本発明の前処理濾過装置と吸着濾過
体を切り離して設置する場合の例であり、前処理
濾過装置6を、控杭25を用いて垂直状に設け、
その外側に吸着濾過体7を山形に設置したもの
で、長期工事において粗粒濾材の交換を必要とす
るときの作業が簡単になる。なお理立工事の終期
においては、前処理濾過装置の濾過板を撤去し、
この箇所で凝集剤をシヤワー添加して余水の浮遊
物質量の低減をはかり、吸着濾過体は流下してく
る沈澱堆積泥により、下方より埋殺しの状態にし
ていく。 以上、説明したように本発明の埋立余水の濾過
処理方法は前処理濾過装置の濾過板を順次取り替
えていくことにより、従来の濾過装置のように目
詰り濾材の大量除去、または逆洗設備を必要とし
ない。吸着濾過体は、従来の濾過装置と異る吸着
作用のみを目的としたものであり、前処理理濾過
装置と吸着濾過体および余水吐口の標高設定によ
り、排水の基準値に対し、余水の浮遊物質量を必
要限度値まで低減させるものであり、過度の清澄
水を得ることを目的としたものではない。
[Table] From Table 1, the filter sand of the pretreatment filtration device of the present invention is coarse sand, the permeability coefficient k = 0.35 cm/sec, the water level difference before and after the filter plate h = 10 cm, and the water flow distance of the filter sand l = 5 cm. Then, to find the relationship between the filter sand water flow area A and the water flow rate Q, we get: Q=k・h・A/l=0.35×10×A÷5=0.77Acm 2 /sec……25.2Am 3 /Hr・m 2 The above value is A=
Requires a water flow cross-sectional area of 200m2 , and in general land reclamation work, the total water flow height of the filter plate of the pretreatment filtration device is 2
m, and a total water flow width of about 100 m can be applied.
Therefore, as the filter medium of the adsorption filter body, use a coarse filter medium of the size of small gravel or more as shown in Table 1. In an example of a waste water quality reduction test using the method of the present invention, the amount of suspended solids (SS) = 50 ppm (average) of the waste water was reduced to approximately half, 25 ppm (average), by the pretreatment filtration device.
Therefore, in the adsorption filter body, it is reduced by approximately 1/5,
(SS) = 20ppm (average) and was released into general water bodies. The water level maintenance of the adsorption filter made of coarse filter media is determined by the elevation setting of the spillway. FIG. 5 shows an example in which the pretreatment filtration device and the adsorption filter of the present invention are installed separately, and the pretreatment filtration device 6 is installed vertically using retaining stakes 25.
The adsorption filter body 7 is installed in a chevron shape on the outside, which simplifies the work when it is necessary to replace the coarse filter medium during long-term construction. In addition, at the end of the construction work, the filter plate of the pretreatment filtration device will be removed.
A shower of flocculant is added at this point to reduce the amount of suspended solids in the surplus water, and the adsorption filter is buried from below by the sedimentary mud that flows down. As explained above, the method for filtration of landfill surplus water of the present invention is capable of removing a large amount of clogged filter media or using backwashing equipment, unlike conventional filtration equipment, by sequentially replacing the filter plates of the pretreatment filtration device. does not require. Adsorption filters are designed solely for adsorption, which is different from conventional filtration devices, and by setting the altitude of the pretreatment filter, adsorption filter, and spillway outlet, the amount of wastewater is reduced relative to the wastewater standard value. The purpose is to reduce the amount of suspended solids in water to the required limit, and is not intended to obtain excessively clear water.

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

第1図は、本発明の余水の濾過処理方法を説明
する埋立地の平面形状を示し、図中1は埋立地護
岸、2は埋立地、3は排泥管、4は堆積泥の水面
上露出部分、5は導流築堤、6は前処理濾過装
置、7は吸着濾過体、8は余水吐口、9は余水吐
管である。 第2図は、前処理濾過装置と吸着濾過体の設置
断面を示し、図中1は埋立地護岸、8は余水吐
口、9は余水吐管、10は濾過板、11は濾過板
保持柱、12は粗粒濾材、13は粗粒濾材保持
柱、14は柵板、15は上部梁、16は余水、1
7は沈澱堆積層、18は理立地在来地盤、19は
吸着濾過体の基礎盛土、20は護岸基礎である。 第3図は、前処理濾過装置の濾過板断面を示
し、図中21は濾過枠、22は濾過砂、23は透
水マツト、24は濾過枠補強材である。 第4図は、前処理濾過装置の濾過板正面図を示
し、図中21は濾過枠、23は透水マツト、24
は濾過枠補強材である。 第5図は、前処理濾過装置と吸着濾過体の応用
設置断面を示し、図中1は埋立地護岸、8は余水
吐口、9は余水吐管、10は濾過板、11は濾過
板保持柱、12は粗粒濾材、16は余水、17は
沈澱堆積泥層、18は埋立地在来地盤、19は吸
着濾過体の基礎盛土、20は護岸基礎、25は控
杭である。
FIG. 1 shows the planar shape of a reclaimed land for explaining the surplus water filtration treatment method of the present invention. In the figure, 1 is a reclaimed land revetment, 2 is a reclaimed land, 3 is a sludge pipe, and 4 is a water surface of accumulated mud. In the upper exposed portion, 5 is a diversion embankment, 6 is a pre-treatment filtration device, 7 is an adsorption filter, 8 is a spillway, and 9 is a spillway pipe. Figure 2 shows the installed cross section of the pre-treatment filtration device and the adsorption filter, in which 1 is the landfill revetment, 8 is the spillway, 9 is the spillway pipe, 10 is the filter plate, and 11 is the filter plate holder. Column, 12 is coarse filter medium, 13 is coarse filter medium holding column, 14 is fence plate, 15 is upper beam, 16 is surplus water, 1
7 is a precipitated sedimentary layer, 18 is a conventional ground, 19 is a foundation embankment for an adsorption filter, and 20 is a seawall foundation. FIG. 3 shows a cross section of the filter plate of the pretreatment filtration device, in which 21 is a filter frame, 22 is filter sand, 23 is a water-permeable mat, and 24 is a filter frame reinforcing material. FIG. 4 shows a front view of the filter plate of the pretreatment filtration device, in which 21 is a filter frame, 23 is a water-permeable mat, and 24 is a filter plate.
is the filter frame reinforcement material. Figure 5 shows a cross-section of the applied installation of the pre-treatment filtration device and the adsorption filter, in which 1 is a reclaimed land revetment, 8 is a spillway, 9 is a spillway pipe, 10 is a filter plate, and 11 is a filter plate. 12 is a coarse filter material, 16 is leftover water, 17 is a precipitated mud layer, 18 is the reclaimed land's native ground, 19 is the foundation embankment of the adsorption filter, 20 is the bank foundation, and 25 is the retaining pile.

Claims (1)

【特許請求の範囲】 1 埋立地余水吐の埋立地内側に、濾過板保持柱
のガイド溝に濾過砂を透水マツトでサンドイツチ
状に挟み込んで濾過枠に収めて成る濾過板を装着
した前処理濾過装置を設け、その背後に粗粒濾材
より成る吸着濾過体を設け、余水を該前処理濾過
装置と吸着濾過体に通過させることにより余水の
浮遊物質量を低減させることを特徴とする埋立地
余水の濾過処理方法。 2 前処理濾過装置の濾過板が、濾過板保持柱に
着脱自在に装着され、目詰りした濾過板を順次取
換えるようにしたことを特徴とする特許請求の範
囲第1項記載の埋立地余水の濾過処理方法。 3 粗粒濾材による吸着濾過体の透水量を、前処
理濾過装置の濾過板の透水量よりも大きくして、
余水吐口の水位保持を行うようにしたことを特徴
とする特許請求の範囲第1項または第2項記載の
埋立地余水の濾過処理方法。
[Scope of Claims] 1. Pretreatment in which a filter plate is installed inside the landfill of a landfill spillway, which is made by sandwiching filter sand in the guide groove of a filter plate holding column in a sandwich-like manner with permeable mats and placing it in a filter frame. A filtration device is provided, an adsorption filter made of a coarse filter material is provided behind the filtration device, and the remaining water is passed through the pretreatment filtration device and the adsorption filtration device, thereby reducing the amount of suspended solids in the remaining water. A method for filtration of wastewater from a landfill. 2. The landfill surplus according to claim 1, characterized in that the filter plate of the pretreatment filtration device is detachably attached to the filter plate holding column, and clogged filter plates are replaced one after another. Water filtration treatment method. 3. The amount of water permeable through the adsorption filter using the coarse filter medium is made larger than the amount of water permeated through the filter plate of the pre-treatment filtration device,
3. A method for filtering wastewater from a landfill according to claim 1 or 2, characterized in that the water level of the spillway is maintained.
JP9406183A 1983-05-30 1983-05-30 Filtration apparatus and method for spillway in reclamation site Granted JPS59220510A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP9406183A JPS59220510A (en) 1983-05-30 1983-05-30 Filtration apparatus and method for spillway in reclamation site

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP9406183A JPS59220510A (en) 1983-05-30 1983-05-30 Filtration apparatus and method for spillway in reclamation site

Publications (2)

Publication Number Publication Date
JPS59220510A JPS59220510A (en) 1984-12-12
JPS6362604B2 true JPS6362604B2 (en) 1988-12-02

Family

ID=14100010

Family Applications (1)

Application Number Title Priority Date Filing Date
JP9406183A Granted JPS59220510A (en) 1983-05-30 1983-05-30 Filtration apparatus and method for spillway in reclamation site

Country Status (1)

Country Link
JP (1) JPS59220510A (en)

Also Published As

Publication number Publication date
JPS59220510A (en) 1984-12-12

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