JPS6099318A - Treatment of mud water - Google Patents
Treatment of mud waterInfo
- Publication number
- JPS6099318A JPS6099318A JP58207002A JP20700283A JPS6099318A JP S6099318 A JPS6099318 A JP S6099318A JP 58207002 A JP58207002 A JP 58207002A JP 20700283 A JP20700283 A JP 20700283A JP S6099318 A JPS6099318 A JP S6099318A
- Authority
- JP
- Japan
- Prior art keywords
- mud water
- water
- pipe line
- mud
- dil
- 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.)
- Granted
Links
Abstract
Description
【発明の詳細な説明】
この発明は泥水の脱水方法に関し、特に泥水式シールド
工法により掘削した土砂を含む泥水を脱水する方法に関
する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to a method for dewatering muddy water, and more particularly to a method for dewatering muddy water containing earth and sand excavated by a muddy shield method.
従来、この種の泥水は排泥管を経て地上に運ばれ、サイ
クロン等により大径の土粒子が除去された後、遠心分離
機により固液分離され、さらにフィルタープレスにより
脱水されている。Conventionally, this type of mud water is transported to the ground via a mud drain pipe, large-diameter soil particles are removed using a cyclone, etc., then solid-liquid separation is performed using a centrifugal separator, and water is further dehydrated using a filter press.
そしてそのp水は中和処理された後、放流されている。The p water is then discharged after being neutralized.
上記のような処理工程において、フィルタープレスへの
供給泥水に有機系または無機系の柴処理することは依然
として避けることができない。In the above-mentioned treatment process, it is still unavoidable to treat the muddy water fed to the filter press with organic or inorganic filters.
この発明は上記のような事情に鑑みてなされたものであ
って、フィルタープレスによる泥水の脱水効率の向上が
図れるだけでなく、脱水後のp水の中和処理を不要とし
、全体として処理設備を簡略化できる方法ヲ1是供する
ことを目的とする。This invention was made in view of the above-mentioned circumstances, and it not only improves the dehydration efficiency of mud water using a filter press, but also eliminates the need for neutralization treatment of p-water after dewatering, and reduces the overall processing equipment. The purpose is to provide a method that can simplify the process.
この発明の発明者らは、一般にシールド工法において掘
削された土砂を含む泥水はアルカリ性を示すため、これ
rtc酸を添加して中和処理した後、フィルタープレス
により加圧脱水したところ、そのF水のPFI値が中性
付近に保たれ、しかも脱水効率が凝集剤を添加した場合
と同等もしくはそれ以上となる結果を得ろことができた
。The inventors of this invention discovered that muddy water containing earth and sand excavated by the shield method is generally alkaline, so after neutralizing it by adding RTC acid and dehydrating it under pressure with a filter press, the F water was We were able to obtain results in which the PFI value was maintained near neutrality, and the dehydration efficiency was equal to or higher than that when a flocculant was added.
この発明は上記のような知見に基〈ものであって、泥水
に酸を添加して中和処理した後、加圧脱水することを特
徴とするものである。This invention is based on the above findings, and is characterized by adding an acid to muddy water to neutralize it, and then dehydrating it under pressure.
使用する酸としては、種々のものがあるが価格等の点で
硫酸が好ましく、それを10wtl程度の希硫酸Kil
!整し1例えば泥水中の土粒子重量に対する希硫酸重量
が所定比率(泥水が中和されろような)Kなるように浣
加する。There are various acids that can be used, but sulfuric acid is preferred from the viewpoint of cost, etc., and it is mixed with about 10 wtl of dilute sulfuric
! Preparation 1 For example, the muddy water is dredged so that the weight of dilute sulfuric acid to the weight of soil particles in the muddy water becomes a predetermined ratio K (such that the muddy water is neutralized).
実施例
泥水式シールド工法を実施しているA、82か所の現場
の泥水[,10vt チの希硫酸ン添加して中和処理し
た後、これをフィルタープレスに連続的に供給して加圧
脱水を行なった。その結果を第1表に示し、またA現場
のP水−3曲線を第1図に;i ’1−6 第1表には
比較例として無添加の場合、および有機系高分子凝集剤
、ポリ塩化第2鉄、PAC’にそれぞれ添加した場合の
結果も示しである。Example: After neutralizing muddy water at 82 sites where the muddy shielding method is being implemented by adding 10vt of dilute sulfuric acid, the muddy water is continuously supplied to a filter press and pressurized. I did dehydration. The results are shown in Table 1, and the P water-3 curve at site A is shown in Figure 1. The results obtained when ferric polychloride and PAC' were respectively added are also shown.
(以下余日)
これらの表およびグラフから希硫酸を添加した場合には
、F水PHが中性付近に保たれ、才た炉水量が多く脱水
効率が高いことがわかる。(See the following) From these tables and graphs, it can be seen that when dilute sulfuric acid is added, the F water PH is maintained near neutrality, the amount of reactor water is large, and the dehydration efficiency is high.
第2図にはこの発明方法を実施する際の好ましい態様が
系統図で示されている。泥水式シールド工法によって掘
削された土砂を含んだ泥水は泥水槽1からijJ変速ポ
ンプ2により管路3χ経てミキサー4に供給され、また
このミキサー4には希硫酸槽5から希硫酸が可変速ポン
プ6により管路7を経て供給され、泥水に添加混合され
る。希硫酸が添加された泥水は管路8を経て貯留槽9に
いったんストックされた後、可変速ポンプ10により管
路11を軽でフィルタープレス12に供給され、加圧脱
水され、七〇p水はそのまま放流される。FIG. 2 shows a system diagram of a preferred embodiment of the method of this invention. Mud water containing earth and sand excavated by the mud shield method is supplied from a mud tank 1 to a mixer 4 via a pipe 3χ by an ijJ variable speed pump 2, and to this mixer 4, dilute sulfuric acid is supplied from a dilute sulfuric acid tank 5 to a variable speed pump. 6 is supplied via pipe 7 and added to and mixed with the muddy water. The muddy water to which dilute sulfuric acid has been added is temporarily stored in a storage tank 9 via a pipe 8, and then supplied to a filter press 12 through a pipe 11 by a variable speed pump 10, where it is dehydrated under pressure and becomes 70p water. is released as is.
泥水の流量および密度は管路3に設けた流゛階計13お
よび密度計14によってそれぞれ検出され、流量指示計
15および密度指示計16に指示される。各指示値は演
算器17に入力さね、この演昇器17において単位流険
当りの泥水中の土粒子重量が算出され、その値は比率設
定器18に入力される。希硫酸の流量は管路7に設げた
流量計19によって検出され、流域指示d120に指示
される。その指示値は比率設定器18に入力され、比率
設定器18は土粒子1緻に対する希硫酸の混合比率があ
らかじめ設定した設定値にあるかどうかをチェックし、
混合比率が設定値と異なる場合は設定値となるよ5にポ
ンプ回転制御盤21に指示し、これによりal変速ポン
プ6の回転数7制御し、希硫酸の流量を調整してその混
合比率を制御する。The flow rate and density of the muddy water are detected by a flow meter 13 and a density meter 14 provided in the pipe line 3, respectively, and are indicated to a flow rate indicator 15 and a density indicator 16. Each indicated value is input to the calculator 17, which calculates the weight of soil particles in the mud per unit flow rate, and the value is input to the ratio setter 18. The flow rate of dilute sulfuric acid is detected by a flow meter 19 provided in the pipe line 7, and is indicated by the flow area instruction d120. The indicated value is input to the ratio setting device 18, and the ratio setting device 18 checks whether the mixing ratio of dilute sulfuric acid to 1 densified soil particle is within the preset setting value.
If the mixing ratio differs from the set value, it instructs the pump rotation control board 21 to use the set value, and thereby controls the rotation speed of the AL variable speed pump 6, adjusts the flow rate of dilute sulfuric acid, and adjusts the mixing ratio. Control.
この発明によれば、泥水の脱水効率が向上−′4−も高
価な凝集剤を使用しないのでランニングコストヲ低減す
ることができる。According to this invention, the dewatering efficiency of muddy water is improved -'4-- and running costs can be reduced because no expensive flocculant is used.
第1図はフィルタープレスにおける加圧時間と炉水量と
の関係を示すグラフ、第2図はこの発明の実施に適した
系統図の一例である。
1・・・泥水槽
、 5・・・希硫酸槽
12・・・フィルタープレス
ηO圧時間 (而n)
18 乙FIG. 1 is a graph showing the relationship between the pressurization time in the filter press and the amount of reactor water, and FIG. 2 is an example of a system diagram suitable for implementing the present invention. 1...Mud water tank, 5...Dilute sulfuric acid tank 12...Filter press ηO pressure time (n) 18 B
Claims (1)
ることt特徴とする泥水の脱水方法。1. A method for dewatering muddy water characterized by adding an acid to muddy water to neutralize it and then dehydrating it under pressure.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58207002A JPS6099318A (en) | 1983-11-04 | 1983-11-04 | Treatment of mud water |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58207002A JPS6099318A (en) | 1983-11-04 | 1983-11-04 | Treatment of mud water |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS6099318A true JPS6099318A (en) | 1985-06-03 |
JPH0250799B2 JPH0250799B2 (en) | 1990-11-05 |
Family
ID=16532562
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58207002A Granted JPS6099318A (en) | 1983-11-04 | 1983-11-04 | Treatment of mud water |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS6099318A (en) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011212514A (en) * | 2010-03-31 | 2011-10-27 | Fujimi Kankyo Ryokka Kk | Sludge water treatment construction method using naturally-derived acidic solution such as pyroligneous acid |
Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5337666A (en) * | 1976-09-18 | 1978-04-06 | Kenzou Hamada | Preparation of monobenzylidenesorbitol |
JPS54149258A (en) * | 1978-05-15 | 1979-11-22 | Kubota Ltd | Pretreatment method for sludge dehydration |
-
1983
- 1983-11-04 JP JP58207002A patent/JPS6099318A/en active Granted
Patent Citations (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5337666A (en) * | 1976-09-18 | 1978-04-06 | Kenzou Hamada | Preparation of monobenzylidenesorbitol |
JPS54149258A (en) * | 1978-05-15 | 1979-11-22 | Kubota Ltd | Pretreatment method for sludge dehydration |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2011212514A (en) * | 2010-03-31 | 2011-10-27 | Fujimi Kankyo Ryokka Kk | Sludge water treatment construction method using naturally-derived acidic solution such as pyroligneous acid |
Also Published As
Publication number | Publication date |
---|---|
JPH0250799B2 (en) | 1990-11-05 |
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