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JPH0378160B2 - - Google Patents
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JPH0378160B2 - - Google Patents

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Publication number
JPH0378160B2
JPH0378160B2 JP60172198A JP17219885A JPH0378160B2 JP H0378160 B2 JPH0378160 B2 JP H0378160B2 JP 60172198 A JP60172198 A JP 60172198A JP 17219885 A JP17219885 A JP 17219885A JP H0378160 B2 JPH0378160 B2 JP H0378160B2
Authority
JP
Japan
Prior art keywords
sludge
drying
area
drying area
solar
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
JP60172198A
Other languages
Japanese (ja)
Other versions
JPS6233599A (en
Inventor
Yoshio Iizuka
Masumitsu Ito
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.)
Shimizu Construction Co Ltd
Original Assignee
Shimizu Construction Co 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 Shimizu Construction Co Ltd filed Critical Shimizu Construction Co Ltd
Priority to JP17219885A priority Critical patent/JPS6233599A/en
Publication of JPS6233599A publication Critical patent/JPS6233599A/en
Publication of JPH0378160B2 publication Critical patent/JPH0378160B2/ja
Granted legal-status Critical Current

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  • Treatment Of Sludge (AREA)

Description

【発明の詳細な説明】 「産業上の利用分野」 この発明は、建設基礎工事や各種産業において
発生する汚泥や既存底質汚泥の処理を天日乾燥に
よつて行なう廃棄汚泥の天日乾燥処理方法に関す
るものである。
Detailed Description of the Invention "Industrial Application Field" This invention relates to a solar drying process for waste sludge, in which sludge generated in construction foundation work and various industries and existing bottom sludge are treated by solar drying. It is about the method.

「従来の技術」 周知のように廃棄汚泥の処理方法としては、(イ)
固化処理、(ロ)凝集剤等の薬剤を用いた固液分離処
理、(ハ)加圧脱水、真空脱水、遠心脱水等の機械的
脱水処理、(ニ)(ロ)あるいは(イ)と(ハ)との組み合せ処
理、(ホ)天日乾燥処理がある。
``Conventional technology'' As is well known, methods for treating waste sludge include (a)
Solidification treatment, (B) Solid-liquid separation treatment using agents such as flocculants, (C) Mechanical dehydration treatment such as pressure dehydration, vacuum dehydration, centrifugal dehydration, (D) (B) or (B) and ( There is a combination treatment with (c) and (e) sun drying treatment.

「発明が解決しようとする問題点」 上記従来の処理方法には各々次のような問題点
があり、より効果的な処理方法の確立が望まれて
いる。
"Problems to be Solved by the Invention" The conventional treatment methods described above each have the following problems, and it is desired to establish a more effective treatment method.

すなわち、(イ)の方法では、固化材の量が多量と
なり、コスト高になる。固化後の強度が大きくな
るため汚泥の体積減少がない。固化物はアルカリ
性(PH=12.5〜13.0)となり、処分後の生物環境
に影響を与える。などの問題がある。
That is, in method (a), the amount of solidifying material is large, resulting in high cost. Since the strength after solidification increases, there is no volume reduction of sludge. The solidified material becomes alkaline (PH = 12.5 to 13.0), which affects the biological environment after disposal. There are problems such as.

また、(ロ)(ハ)(ニ)の方法は、薬剤、機械設備等が必
要であり、そのためコスト高となる。などの問題
がある。
Furthermore, methods (b), (c), and (d) require chemicals, mechanical equipment, etc., and are therefore costly. There are problems such as.

そして、(ホ)の天日乾燥処理方法では、天日乾燥
中に雨水が混入すると、再び汚泥状にもどる場合
がある。表面は乾燥しても、中の乾燥はほとんど
進まず、処理効率が悪い。などの問題がある。
In the solar drying method (e), if rainwater gets mixed in during solar drying, it may return to a sludge-like state. Even if the surface dries, the inside hardly dries, resulting in poor processing efficiency. There are problems such as.

この発明は上記事情に鑑みてなされたもので、
コスト高を招く薬剤や機械設備を必要とせず、効
果的に廃棄汚泥を乾燥することのできる方法を提
供することを目的とするものであり、天日乾燥処
理方法を改良して効率的に行なえるようにしたも
のである。
This invention was made in view of the above circumstances,
The purpose of this project is to provide a method that can effectively dry waste sludge without the need for chemicals or mechanical equipment that increase costs. It was designed so that

「問題点を解決するための手段」 この発明に係る廃棄汚泥の天日乾燥処理方法
は、建設工事現場等から発生する廃棄汚泥に2〜
5wt%のセメント等の固化材を添加、撹拌後、た
だちに天日乾燥場へ移し入れ、天日により乾燥、
硬化する廃棄汚泥の天日乾燥処理方法である。そ
して、前記天日乾燥場は、砂利を敷き詰めるとと
もに敷き詰められた砂利の周縁を盛り上げて窪地
を形成し、該窪地の内部を着脱自在な2列の仕切
り壁により初期乾燥場、2次乾燥場、3次乾燥場
の3つに分離してなるものである。そして、前記
初期乾燥場で、撹拌後の前記汚泥の固化養生と脱
水を行ない、この汚泥を該汚泥の底部分を上面に
出すように前記2次乾燥場に押し出し、該2次乾
燥場で、さらに天日乾燥を行ない、この汚泥を該
汚泥の底部分を上面に出すように前記3次乾燥場
に押し出し、該3次乾燥場で乾燥固化状態にする
ことを特徴とするものである。
``Means for Solving the Problems'' The method for solar drying waste sludge according to the present invention applies to waste sludge generated from construction sites, etc.
After adding 5wt% of solidifying agent such as cement and stirring, immediately transfer to a solar drying place and dry in the sun.
This is a solar drying treatment method for hardening waste sludge. In the solar drying area, gravel is spread and the periphery of the gravel is raised to form a depression, and the interior of the depression is divided into an initial drying area, a secondary drying area, and a secondary drying area by two rows of removable partition walls. It is separated into three tertiary drying areas. Then, in the initial drying area, the sludge after stirring is solidified and cured and dehydrated, and this sludge is pushed to the secondary drying area so that the bottom part of the sludge is exposed to the top, and in the secondary drying area, The sludge is further dried in the sun, and the sludge is extruded to the tertiary drying area so that the bottom part of the sludge is exposed to the top, and is dried and solidified in the tertiary drying area.

「作用」 上記方法は、種々実験検討の結果得られたもの
で、汚泥の性状によつて異なるが、汚泥に対して
2〜5wt%の固化材を混入すると、汚泥は固化せ
ずにその流動性を失なうとの知見に基づいてなさ
れたものである。この流動性の消失は固化材の添
加、撹拌後30〜60分後にあらわれるので、流動性
のある内に汚泥を天日乾燥場に移し入れることは
充分に可能である。流動性が消失した汚泥は、流
れ拡がることがないので、汚泥量に対する天日乾
燥場の必要面積は従来より少なくて済むことにな
る。また、汚泥は固化材により微弱ながら支持構
造を持つので、乾燥後の空隙率が大きく、内部水
分の表面への移動も容易であり、また、上記支持
構造により乾燥が進むにつれて亀裂が生じやす
く、そのため外気接触面積も増加しやすく、乾燥
効率がたいへん高い。汚泥深さと天候にもよる
が、汚泥厚30cm程度で平均的な天候で、4〜8週
間で乾燥を完了することができる。なお、固化材
混入汚泥は、高いアルカリ性を示すが、亀裂の発
生による表面積の増加も加わつて、大気中の炭酸
ガス等の酸性物質と中和反応を生じ、PHは徐々に
低下する。さらに雨水の混入が中和をより促進さ
せるので、高アルカリ性の弊害が極めてよく緩和
される。
"Effect" The above method was obtained as a result of various experimental studies, and although it differs depending on the properties of the sludge, when 2 to 5 wt% of solidifying agent is mixed into the sludge, the sludge does not solidify and its fluidity increases. This was done based on the knowledge that people lose their sexuality. This loss of fluidity appears 30 to 60 minutes after addition of the solidifying agent and stirring, so it is fully possible to transfer the sludge to the solar drying facility while it remains fluid. Since sludge that has lost its fluidity does not flow and spread, the required area of the solar drying field for the amount of sludge is smaller than before. In addition, since sludge has a weak support structure due to the solidification material, the porosity after drying is large, and internal moisture can easily move to the surface. Also, due to the support structure, cracks are likely to occur as drying progresses. Therefore, the area in contact with outside air tends to increase, and the drying efficiency is very high. Depending on the sludge depth and weather, drying can be completed in 4 to 8 weeks under average weather conditions and sludge thickness is approximately 30 cm. Although sludge mixed with a solidification agent exhibits high alkalinity, the increase in surface area due to the occurrence of cracks causes a neutralization reaction with acidic substances such as carbon dioxide gas in the atmosphere, and the pH gradually decreases. Furthermore, since the mixing of rainwater further promotes neutralization, the adverse effects of high alkalinity are extremely alleviated.

このように本発明によれば、単に少量の固化材
を汚泥に混入し、この汚泥を天日乾燥場に移し入
れるだけで、効率的に汚泥の乾燥を行なうことが
できるので、廃棄汚泥の処理を低コスト、高効率
に行なうことができる。
As described above, according to the present invention, sludge can be efficiently dried by simply mixing a small amount of solidifying agent into sludge and transferring this sludge to a solar drying facility, which makes it possible to efficiently process waste sludge. can be carried out at low cost and with high efficiency.

また、固化材を添加後撹拌した汚泥を初期乾燥
場に移す。この際に、天日乾燥場に窪地が形成さ
れ、かつ、初期乾燥場に移した後にすぐに、固化
材により汚泥の流動性がなくなるので、より多く
の汚泥を収容することができる。また、汚泥は、
順次初期乾燥場から2次乾燥場、3次乾燥場に送
られるので、初期乾燥終了後に、続けて次の汚泥
の初期乾燥に初期乾燥場を連続して使用できる。
また、ブルドーザー等をつかつて、初期乾燥場か
ら2次乾燥場、3次乾燥場に押しだす際に、汚泥
の低部が上面にくるように押しだしているので、
汚泥の乾燥を速めることができる。
In addition, the sludge stirred after adding the solidifying agent is transferred to the initial drying area. At this time, a depression is formed in the solar drying area, and the fluidity of the sludge is lost by the solidifying agent immediately after being transferred to the initial drying area, so that more sludge can be accommodated. In addition, sludge is
Since the sludge is sent sequentially from the initial drying area to the secondary drying area and then to the tertiary drying area, the initial drying area can be used continuously for the initial drying of the next sludge after the initial drying is completed.
In addition, when pushing the sludge from the initial drying area to the secondary drying area and the tertiary drying area using a bulldozer, etc., the sludge is pushed out so that the lower part of the sludge is at the top.
It can speed up the drying of sludge.

以下、この発明を実施例によりさらに詳しく説
明する。
Hereinafter, this invention will be explained in more detail with reference to Examples.

「実施例」 この実施例は、実際に産業汚泥を処理する場合
の例である。この実際の処理方法においては、第
1図および第2図に示すような天日乾燥場を利用
する。この天日乾燥場は、図に示すように水切れ
の良いように砂利1を敷きつめ、周囲を盛り上げ
て窪地状に形成したものであり、内側は着脱自在
な仕切り壁2によつて各々複数個(図では6ケず
つ)のブロツクからなる初期乾燥場3と2次乾燥
場4と3次乾燥場5との区分けされている。ま
た、砂利1を通過した汚泥分離水、雨水等の浸透
水は側溝6を通つて貯水槽7に流入されるように
なつている、この実施例においては、まず、搬入
汚泥は、汚泥ストツク槽8に入れられ、上澄液は
貯水槽7に送られ、沈殿汚泥はポンプ9によりミ
キサー槽10に流入され、ミキサー槽10にて、
この汚泥の性状に応じて決定した濃度の固化材を
添加、混合し、初期乾燥場3に移し入れる。ここ
で、汚泥は7日〜10日放置され、固化養生と脱水
が行なわれる。初期乾燥期間が完了したら、仕切
壁2を取りはずし、ブルドーザーB等により底部
分を上面に出すようにして汚泥を2次乾燥場4へ
移し入れる。ここで、7日程度放置して、さらに
天日乾燥を進行させる。この2次乾燥が終了した
ら、上記同様ブルドーザーB等により3次乾燥場
5に移し入れる。ここで、7〜14日さらに天日乾
燥して完全に乾燥固化状態にする。この間、汚泥
からの分離水や雨水等の水分は、砂利1を通つて
側溝6に流れ込み、貯水槽7に進められる。この
ようにして充分乾燥が完了した汚泥は、ブルドー
ザーB等により乾燥場外に出し、廃棄処分または
再利用のために運びだされる。一方、貯水槽7に
流入した浸透水は、PH、SS通の水質をチエツク
され、基準値以下であれば、放流または再利用さ
れ、基準値に達していなければ、中和、濾過等の
処理を施して基準値以下にされ、放流または再利
用される。
"Example" This example is an example in which industrial sludge is actually treated. In this actual treatment method, a solar drying field as shown in FIGS. 1 and 2 is used. As shown in the figure, this solar drying area is made up of gravel 1 spread over it so that it drains well, and the surrounding area is raised to form a depression. The drying area is divided into an initial drying area 3, a secondary drying area 4, and a tertiary drying area 5 each consisting of 6 blocks (in the figure). In addition, permeated water such as sludge separated water and rainwater that has passed through the gravel 1 is configured to flow into a water storage tank 7 through a side gutter 6. 8, the supernatant liquid is sent to the water storage tank 7, and the settled sludge is flowed into the mixer tank 10 by the pump 9, and in the mixer tank 10,
A solidifying agent with a concentration determined according to the properties of the sludge is added and mixed, and the sludge is transferred to the initial drying area 3. Here, the sludge is left for 7 to 10 days to undergo solidification, curing, and dewatering. When the initial drying period is completed, the partition wall 2 is removed and the sludge is transferred to the secondary drying area 4 using a bulldozer B or the like with the bottom portion exposed to the top. Here, it is left to stand for about 7 days to further progress the drying in the sun. When this secondary drying is completed, the material is transferred to the tertiary drying place 5 using a bulldozer B or the like as described above. Here, it is further dried in the sun for 7 to 14 days to completely dry and solidify it. During this time, moisture such as water separated from the sludge and rainwater flows into the gutter 6 through the gravel 1 and is directed to the water storage tank 7. The sludge that has been sufficiently dried in this manner is taken out of the drying area by a bulldozer B or the like and transported for disposal or reuse. On the other hand, the permeated water that has flowed into the water storage tank 7 is checked for water quality through PH and SS, and if it is below the standard value, it is discharged or reused, and if it does not meet the standard value, it is subjected to treatment such as neutralization and filtration. The water is treated to bring it below the standard value and then released or reused.

なお、搬入汚泥の性状をチエツクした時点で残
土扱い可能なものと、流動性がなく、脱水性が良
いものは、固化材の添加なしに処理できるので、
各々次のように処理する。まず、残土扱い可能な
ものは、含水率、強度等をチエツクして含水分が
充分少ない場合または少なくなつた時点で搬出
し、廃棄処分あるいは再利用する。そして、流動
性がなく、脱水性の良いものは、直接天日乾燥場
に移し入れて上記天日乾燥処理を行ない処分す
る。
In addition, when we check the properties of the sludge brought in, if it can be treated as residual soil or if it has no fluidity and has good dewatering properties, it can be processed without adding a solidifying agent.
Each is processed as follows. First, if the waste soil can be handled, its moisture content, strength, etc. are checked, and when the moisture content is sufficiently low, or when it has become low, it is taken out and disposed of or reused. Those with no fluidity and good dehydration properties are directly transferred to a solar drying facility, subjected to the above-mentioned solar drying treatment, and then disposed of.

上記実施例によれば、大量の廃棄汚泥を連続し
て処分、再利用することができ、同時に発生する
浸透水の処分、再利用も行なえ、処理場も従来よ
り小面積で済み、特別な処理設備の必要もなく、
底コスト処理が可能となる。
According to the above embodiment, a large amount of waste sludge can be continuously disposed of and reused, the seepage water generated at the same time can be disposed of and reused, the area of the treatment plant is smaller than before, and special treatment is possible. No equipment required,
Bottom cost processing becomes possible.

次に、汚泥に固化材を添加し、天日乾燥した場
合の実施例について記載する。
Next, an example will be described in which a solidifying agent is added to sludge and the sludge is dried in the sun.

(実施例) 「表1」に示すように6種類の供試汚泥を作製
し、それぞれの天日乾燥の経時変化を測定した。
No.1、2、3は建設工事現場から発生する各種汚
泥をカバーするように構成したものである。ま
た、No.4、5はそれぞれ上記No.1、2に4wt%の
普通ポルトランドセメントを混入したもので、No.
6はNo.2の汚泥を凝集処理したものであり、No.
1、2、3は従来法による天日乾燥用汚泥であ
り、No.4、5は本発明法による天日乾燥用汚泥で
あり、No.6はコスト高となる薬剤による固液分離
法による汚泥(比較例)である。
(Example) As shown in "Table 1", six types of test sludge were prepared, and the change over time in solar drying of each was measured.
Nos. 1, 2, and 3 are constructed to cover various types of sludge generated from construction sites. In addition, Nos. 4 and 5 are the above Nos. 1 and 2 mixed with 4wt% of ordinary Portland cement, respectively.
No. 6 is the sludge of No. 2 that has been coagulated.
Nos. 1, 2, and 3 are sludges for solar drying made by the conventional method, Nos. 4 and 5 are sludges for sun drying made by the method of the present invention, and No. 6 is sludges made by the solid-liquid separation method using chemicals, which is costly. Sludge (comparative example).

これら各汚泥試料は、表面から蒸発乾燥のみに
限定し、下記のようにした処理状態を観察した。
Each of these sludge samples was subjected to only evaporative drying from the surface, and the processing conditions as described below were observed.

() 各試料汚泥の放置は自然の天候状況(気象
条件)で実施するため、ビル屋上において日
照、風向等の影響を受けない場所に測定した。
() Since each sample sludge was left in natural weather conditions, measurements were taken on the roof of a building in a location unaffected by sunlight, wind direction, etc.

() 天日乾燥日数は約2ケ月間の連続とし、そ
の調査は1回/週で測定日を設定した。そのた
め同一試料について測定回数分の試料を用意し
た。
() The number of days for sun drying was approximately two consecutive months, and the survey was conducted once a week on measurement days. Therefore, samples for the same sample were prepared for the number of measurements.

() 試料容器はガラス製またはプラツチツク製
とし、容器の側面からの輻射熱による蒸発を防
ぐため、水で飽和した砂の中に埋め込んだ。
() The sample container was made of glass or plastic and was embedded in sand saturated with water to prevent evaporation due to radiant heat from the sides of the container.

() 気象データとして測定期間中の温度、湿
度、日射量、降雨量、風向、風速を測定した。
() Temperature, humidity, solar radiation, rainfall, wind direction, and wind speed were measured during the measurement period as meteorological data.

() 汚泥処理状態の評価は次の(a)〜(c)で行なつ
た。
() Evaluation of the sludge treatment status was performed in the following (a) to (c).

(a) 含水率(重量変化)、深さ方向についても
測定した。
(a) Moisture content (weight change) and depth direction were also measured.

(b) 汚泥面のレベル変化(蒸発による汚泥面の
低下距離)。
(b) Change in sludge level (distance the sludge level drops due to evaporation).

(c) 汚泥PHの変化(溶出PH)。 (c) Change in sludge pH (eluted pH).

このようにして測定したところ、表2のような
結果となつた。
When measured in this manner, the results shown in Table 2 were obtained.

なお、実施期間中(49日間)、雨天日が11日あ
つた。期間中に連続して降雨量0mmの週は3週あ
つた。「晴」および「快晴」の日は14日であるが、
日射量8MJ/m2以上の日数は28日あつた。相対湿
度は当然のことながら雨天との関係で変化した。
風速は日平均で2〜5m/sであつたが、他の気
象データとの相関性について明確な傾向をみるこ
とはできなかつた。外気温は実施した11月から12
月へと経過するに従つて徐々に低くなつたが、季
節的にみて秋から冬にかけての一般的な気温と判
断された。これらの気象データは、気象庁の過去
30年間の平均データからみても大差なく、実施期
間中の天候が異常気象によるものではないと判断
した。
During the implementation period (49 days), there were 11 rainy days. During the period, there were three consecutive weeks with 0 mm of rainfall. The 14th is a "sunny" or "clear" day.
There were 28 days with solar radiation above 8MJ/ m2 . Relative humidity naturally varied in relation to the rainy weather.
The daily average wind speed was 2 to 5 m/s, but no clear trend could be seen in correlation with other meteorological data. The outside temperature was from November to December when the test was carried out.
The temperature gradually decreased as the month progressed, but from a seasonal perspective, it was judged to be the typical temperature from autumn to winter. These weather data are from the Japan Meteorological Agency's past
There was no significant difference from the 30-year average data, and it was determined that the weather during the implementation period was not caused by abnormal weather.

また、実施期間では3週間目に雨天日が4日あ
り、この間に50.5mmの総降水量があつた。従つ
て、3週間経過後の含水率は、この雨水の影響に
よるものであるが、試料No.1以外の汚泥含水率
は、2週経過後と同じか、それ以下に低下してい
るため、これらの汚泥は雨水による汚泥内への浸
透が極めて少ないものと考えられる。すなわち、
天日乾燥によつて蒸発した水は、再び汚泥状態に
吸水することなく、処理効果が表われていると言
える。表2に示す実験結果より以下のことが明ら
かになつた。
Additionally, during the implementation period, there were four rainy days in the third week, with a total rainfall of 50.5 mm during this period. Therefore, the water content after 3 weeks is due to the influence of this rainwater, but the water content of sludge other than sample No. 1 has decreased to the same or lower than after 2 weeks. These sludges are considered to have very little penetration of rainwater into the sludge. That is,
It can be said that the water evaporated by sun drying does not absorb into sludge again, and the treatment effect is being shown. From the experimental results shown in Table 2, the following became clear.

(1) 汚泥の固化により初期においても流動性が生
じない。
(1) Due to solidification of sludge, no fluidity occurs even in the initial stage.

(2) そのため、雨水等の浸入においても明確に分
離しており、排水の除去が容易である。
(2) Therefore, even when rainwater enters, it is clearly separated, and drainage is easy to remove.

(3) 極めて沈降性の悪い高含水率汚泥やベントナ
イト泥水に対してセメントを2〜5wt%(汚泥
の種類によつて異なるためのバラツキ範囲)混
入することによつて天日乾燥の効率が向上す
る。
(3) The efficiency of solar drying is improved by mixing 2 to 5 wt% of cement (the range varies depending on the type of sludge) to high moisture content sludge and bentonite slurry that have extremely poor settling properties. do.

(4) セメント固化強度が低いため、水分の蒸発に
伴う亀裂の発生が容易であり、この亀裂は蒸発
のための表面積を増加させるため、より乾燥が
促進する。
(4) Due to the low solidification strength of cement, cracks are easily generated due to evaporation of water, and these cracks increase the surface area for evaporation, which further accelerates drying.

(5) 水分の蒸発に伴つてセメント固化汚泥の体積
は大幅(30〜50%)に減少する。
(5) As water evaporates, the volume of cement solidified sludge decreases significantly (30-50%).

(6) セメント固化汚泥は、当初高いアルカリ性
(PH12.5〜13)を示すが、大気中の炭酸ガスや
雨水との接触により中性化が促進されるため、
排水および浸透水のPH調整が容易である。
(6) Cement solidified sludge initially exhibits high alkalinity (PH12.5-13), but its neutralization is promoted by contact with atmospheric carbon dioxide and rainwater;
It is easy to adjust the pH of drainage and seepage water.

(7) また、汚泥の溶出PHの中和も促進されるた
め、乾燥処理後の汚泥の利用用途が広くなる。
(7) In addition, the neutralization of the eluted PH of the sludge is promoted, so the sludge after drying treatment can be used in a wide range of applications.

「発明の効果」 以上説明したように、本発明によれば、以下に
示すような優れた効果を奏することができる。
"Effects of the Invention" As explained above, according to the present invention, the following excellent effects can be achieved.

第1に、廃棄汚泥に2〜5wt%のセメント等の
固化材を添加、撹拌後、天日により乾燥、硬化さ
せるので、実施例の結果から明らかなように、 a 汚泥の固化により乾燥初期においても流動性
が生じない。
First, 2 to 5 wt% of a solidifying agent such as cement is added to the waste sludge, stirred, and then dried and hardened in the sun.As is clear from the results of the examples, a. Also, liquidity does not occur.

b そのために、雨水等の侵入においても明確に
分離しており、排水の除去が容易である。
b For this reason, even when rainwater enters, it is clearly separated, and drainage is easy to remove.

C 極めて沈降性の悪い高含水率汚泥やベントナ
イト泥水に対してセメントを2〜5wt%混入す
ることによつて天日乾燥の効率が向上する。
C. The efficiency of solar drying is improved by mixing 2 to 5 wt% of cement into high water content sludge or bentonite slurry that has extremely poor settling properties.

d セメント固化強度が低いため、水分の蒸発に
伴う亀裂の発生が容易であり、この亀裂は蒸発
のための表面積を増加させるため、より乾燥が
促進する。
d Due to the low solidification strength of cement, cracks are easily generated due to evaporation of water, and these cracks increase the surface area for evaporation, which further accelerates drying.

e 上記のようにセメントの固化強度が低いため
に、乾燥した汚泥を容易にブルドーザー等で押
し崩しながら移動させることができ、かつ、ブ
ルドーザー等で汚泥を押すことにより、容易に
崩せることから、乾燥後の汚泥を容易に土砂と
して再利用できる。
e As mentioned above, since the solidification strength of cement is low, dry sludge can be easily moved by pushing it with a bulldozer, etc.; The remaining sludge can be easily reused as earth and sand.

f 水分の蒸発に伴つてセメント固化汚泥の体積
は大幅(30〜40)に減少する。
f The volume of cement solidified sludge decreases significantly (30-40) with the evaporation of water.

g セメント固化汚泥は、当初高いアルカリ性
(PH12.5〜13)を示すが、大気中の炭酸ガスや
雨水との接触により中性化が促進されるため、
排水及び浸透水のPH調整が容易である。
g. Cement solidified sludge initially exhibits high alkalinity (PH12.5-13), but its neutralization is promoted by contact with atmospheric carbon dioxide and rainwater;
It is easy to adjust the pH of drainage and seepage water.

h また、汚泥の溶出PHの中和も促進されるた
め、乾燥処理後の汚泥の利用用途が広くなる。
h Also, since the neutralization of the eluted PH of the sludge is promoted, the uses of the sludge after drying treatment are widened.

第2に、前記天日乾燥場は、砂利を敷き詰める
とともに敷き詰められた砂利の周縁を盛り上げて
窪地を形成し、該窪地の内部を着脱自在な2列の
仕切り壁により初期乾燥場、2次乾燥場、2次乾
燥場の3つに分離してなるだけのもので、特別な
処理設備を必要とせず、従つて、高額の設備投資
を必要としない。また、窪地を形成することによ
り、より多くの廃棄汚泥を収容できる。
Second, in the solar drying area, gravel is spread and the periphery of the gravel is raised to form a depression, and the interior of the depression is separated by two rows of removable partition walls, which provide an initial drying area and a secondary drying area. It consists of three separate drying areas: a drying area and a secondary drying area, and does not require any special treatment equipment, and therefore does not require a large investment in equipment. Furthermore, by forming a depression, more waste sludge can be accommodated.

第3に、前記処理乾燥場で、撹拌後の前記汚泥
の固化養成と脱水を行ない、この汚泥を該汚泥の
底部分を上面に出すように前記2次乾燥場に押し
出し、該2次乾燥場で、さらに天日乾燥を行な
い、この汚泥を該汚泥の底部分を上面に出すよう
に前記3次乾燥場に押し出し、該3次乾燥場で乾
燥固化状態にするので、初期乾燥が終了した時点
で次の汚泥の初期乾燥に連続して初期乾燥場を使
用することができ、従つて、大量の汚泥にも対応
することができ、また、初期乾燥場から順次、2
次乾燥場、3次乾燥場へと、汚泥を移動する際
に、汚泥の底部分を上面に出すように押し出して
いるので、汚泥の天日乾燥を速めることができ
る。
Thirdly, in the treatment drying field, the sludge after stirring is solidified and cultivated and dehydrated, and this sludge is pushed to the secondary drying field so that the bottom part of the sludge comes out to the top. Then, the sludge is further dried in the sun, and the sludge is extruded into the tertiary drying area so that the bottom part of the sludge is exposed to the top, and the sludge is dried and solidified in the tertiary drying area, so that when the initial drying is completed, The initial drying area can be used continuously for the initial drying of the next sludge, and therefore, it is possible to handle a large amount of sludge.
When the sludge is transferred to the secondary drying area and the tertiary drying area, the bottom part of the sludge is pushed out to the top, thereby speeding up the solar drying of the sludge.

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

第1図および第2図はこの発明の第2の実施例
を説明するためのもので、各々天日乾燥場の平面
図および側断面図である。 1……砂利、2……仕切り壁、3……初期乾燥
場、4……2次乾燥場、5……3次乾燥場、6…
…側溝、7……貯水槽、8……汚泥ストツク槽、
9……ポンプ、10……ミキサー槽。
FIGS. 1 and 2 are for explaining a second embodiment of the present invention, and are a plan view and a side sectional view of a solar drying place, respectively. 1... Gravel, 2... Partition wall, 3... Initial drying area, 4... Secondary drying area, 5... Tertiary drying area, 6...
...Gutter, 7...Water tank, 8...Sludge stock tank,
9...Pump, 10...Mixer tank.

【表】【table】

【表】【table】

【表】【table】

【表】【table】

Claims (1)

【特許請求の範囲】 1 建設工事現場等から発生する廃棄汚泥に2〜
5wt%のセメント等の固化材を添加、撹拌後、た
だちに天日乾燥場へ移し入れ、天日により乾燥、
硬化する廃棄汚泥の天日乾燥処理方法であつて、 前記天日乾燥場は、砂利を敷き詰めるとともに
敷き詰められた砂利の周縁を盛り上げて窪地を形
成し、該窪地の内部を着脱自在な2列の仕切り壁
により初期乾燥場、2次乾燥場、3次乾燥場の3
つに分離してなり、 前記初期乾燥場で、撹拌後の前記汚泥の固化養
生と脱水を行ない、この汚泥を該汚泥の底部分を
上面に出すように前記2次乾燥場に押し出し、該
2次乾燥場で、さらに天日乾燥を行ない、この汚
泥を該汚泥の底部分を上面に出すように前記3次
乾燥場に押し出し、該3次乾燥場で乾燥固化状態
にすることを特徴とする廃棄汚泥の天日乾燥処理
方法。
[Claims] 1. Waste sludge generated from construction sites, etc. 2.
After adding 5wt% of solidifying agent such as cement and stirring, immediately transfer to a solar drying place and dry in the sun.
The solar drying field is a solar drying method for hardening waste sludge, in which gravel is spread and the periphery of the spread gravel is raised to form a depression, and the interior of the depression is filled with two removable rows. Three drying areas, an initial drying area, a secondary drying area, and a tertiary drying area, are separated by partition walls.
In the initial drying field, the sludge after stirring is solidified and cured and dehydrated, and this sludge is pushed out to the secondary drying field so that the bottom part of the sludge is exposed to the top. The sludge is further dried in the sun in the secondary drying area, and the sludge is pushed out to the tertiary drying area so that the bottom part of the sludge is exposed to the top, and is dried and solidified in the tertiary drying area. A solar drying treatment method for waste sludge.
JP17219885A 1985-08-05 1985-08-05 Solar drying treatment method for waste sludge Granted JPS6233599A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17219885A JPS6233599A (en) 1985-08-05 1985-08-05 Solar drying treatment method for waste sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17219885A JPS6233599A (en) 1985-08-05 1985-08-05 Solar drying treatment method for waste sludge

Publications (2)

Publication Number Publication Date
JPS6233599A JPS6233599A (en) 1987-02-13
JPH0378160B2 true JPH0378160B2 (en) 1991-12-12

Family

ID=15937396

Family Applications (1)

Application Number Title Priority Date Filing Date
JP17219885A Granted JPS6233599A (en) 1985-08-05 1985-08-05 Solar drying treatment method for waste sludge

Country Status (1)

Country Link
JP (1) JPS6233599A (en)

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US9001456B2 (en) 2010-08-31 2015-04-07 Teradyne, Inc. Engaging test slots
US9459312B2 (en) 2013-04-10 2016-10-04 Teradyne, Inc. Electronic assembly test system
US10725091B2 (en) 2017-08-28 2020-07-28 Teradyne, Inc. Automated test system having multiple stages
US10775408B2 (en) 2018-08-20 2020-09-15 Teradyne, Inc. System for testing devices inside of carriers
US10845410B2 (en) 2017-08-28 2020-11-24 Teradyne, Inc. Automated test system having orthogonal robots
US10948534B2 (en) 2017-08-28 2021-03-16 Teradyne, Inc. Automated test system employing robotics
US10983145B2 (en) 2018-04-24 2021-04-20 Teradyne, Inc. System for testing devices inside of carriers
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Publication number Priority date Publication date Assignee Title
JPH01293199A (en) * 1988-05-20 1989-11-27 Shimizu Corp Drying treatment method for muddy substances

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5544338A (en) * 1978-09-26 1980-03-28 Akijirou Kameyama Treating method of household sewage settling sludge and treated matter thereof
JPS5845798A (en) * 1981-09-14 1983-03-17 Hisashi Nakabayashi Treatment of organic or inorganic sludge

Cited By (9)

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Publication number Priority date Publication date Assignee Title
US8964361B2 (en) 2010-07-21 2015-02-24 Teradyne, Inc. Bulk transfer of storage devices using manual loading
US9001456B2 (en) 2010-08-31 2015-04-07 Teradyne, Inc. Engaging test slots
US9459312B2 (en) 2013-04-10 2016-10-04 Teradyne, Inc. Electronic assembly test system
US10725091B2 (en) 2017-08-28 2020-07-28 Teradyne, Inc. Automated test system having multiple stages
US10845410B2 (en) 2017-08-28 2020-11-24 Teradyne, Inc. Automated test system having orthogonal robots
US10948534B2 (en) 2017-08-28 2021-03-16 Teradyne, Inc. Automated test system employing robotics
US11226390B2 (en) 2017-08-28 2022-01-18 Teradyne, Inc. Calibration process for an automated test system
US10983145B2 (en) 2018-04-24 2021-04-20 Teradyne, Inc. System for testing devices inside of carriers
US10775408B2 (en) 2018-08-20 2020-09-15 Teradyne, Inc. System for testing devices inside of carriers

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