JPS6233599A - Treatment of sun-drying waste sludge - Google Patents

Treatment of sun-drying waste sludge

Info

Publication number
JPS6233599A
JPS6233599A JP17219885A JP17219885A JPS6233599A JP S6233599 A JPS6233599 A JP S6233599A JP 17219885 A JP17219885 A JP 17219885A JP 17219885 A JP17219885 A JP 17219885A JP S6233599 A JPS6233599 A JP S6233599A
Authority
JP
Japan
Prior art keywords
sludge
drying
sun
waste sludge
dried
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
Application number
JP17219885A
Other languages
Japanese (ja)
Other versions
JPH0378160B2 (en
Inventor
Yoshio Iizuka
飯塚 芳雄
Masumitsu Ito
伊藤 益光
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)

Abstract

PURPOSE:To efficiently dry waste sludge without necessitating chemicals resulting in an increase in the cost by adding a caking agent to waste sludge generated from a construction site, etc., agitating the sludge, immediately transferring the sludge to the sun-drying place and drying the sludge by the sun. CONSTITUTION:Waste sludge generated from a construction site, etc., is uniformly agitated to regulate the concn. to a specified value. The sludge is added with 2-5wt% caking material such as cement, agitate, then transferred to a sun-drying place and accumulated in specified depth. After the fluidity of the sludge is eliminated, the sludge is dried by the sun. For example, about 30cm-thick sludge can be dried in 4-8 weeks in average weather. Since sludge can be efficiently dried in this way, waste sludge can be treated at a low cost and with high efficiency.

Description

【発明の詳細な説明】 「産業上の利用分野J 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って行なう廃
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 Field of Application J This invention relates to a solar drying method 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 something.

「従来の技術」 周知のように廃棄汚泥の処理力法としては、(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
、に)(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。
``Prior art'' As is well known, methods for treating waste sludge include (a) solidification treatment, (b) solid-liquid separation treatment using agents such as coagulants, and (
C) Mechanical dehydration treatment such as pressure dehydration, vacuum dehydration, centrifugal dehydration, etc.; (B) or a combination of (B) and (C); and (E) solar drying.

「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4次のような問題点があシ、
より効率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 processing methods described above have the following four problems:
It is desired to establish a more efficient treatment method.

すなわち、(イ)の方法では、固化材の量が多量となシ
、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=7ユ5
〜/、3.0)となシ、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 is alkaline (pH=7.5
~/, 3.0) It affects the biological environment after disposal. There are problems such as.

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

そして、(ホ)の天日乾燥処理法では、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、効率的に廃棄汚泥
を乾燥することのできる方法な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, and aims to provide a method that can efficiently dry waste sludge without requiring chemicals or mechanical equipment that increase costs. The solar drying method has been improved to make it more efficient.

「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、まず、
廃棄汚泥を均一に攪拌して濃度を一定にし、この汚泥に
2〜5wt%のセメント等の固化材を添加、攪拌し、た
だちに(汚泥が流動性を失なう前に)、天日乾燥場へ汚
泥深さが均一となるように移し入れ、汚泥の流動性を失
なわせた状態で天日乾燥する方法である。
"Means for Solving the Problems" The method for solar drying treatment of waste sludge according to the present invention first includes:
The waste sludge is stirred uniformly to maintain a constant concentration, 2 to 5 wt% of solidifying agent such as cement is added to this sludge, stirred, and immediately (before the sludge loses its fluidity) dried in a solar drying field. In this method, the sludge is transferred to a tank so that the depth is uniform, and the sludge is dried in the sun to lose its fluidity.

「作用」 上記方法は、檀々実験検討の結果得られたもので、汚泥
の性状によって異なるが、汚泥に対してコ〜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、攪拌後30〜bo分後にあら
れれるので、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シ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、<z−
g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って、大気中の炭酸ガス等の酸性物
質と中和灰石を生じ、pHは徐々に低下する。さらに雨
水の混入が中和をよシ促進させるので、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 5 wt% of the solidifying agent is mixed with the sludge, the sludge does not solidify and its fluidity increases. This was done based on the knowledge that the This loss of fluidity occurs 30 to 10 minutes after addition of the solidifying agent and stirring, so it is fully possible to transfer the sludge to a solar drying facility while it remains fluid. Since sludge that has lost its fluidity does not flow and spread, the area required for a solar drying field relative to the amount of sludge is smaller than in the past. 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. It depends on the sludge depth and the weather, but if the sludge is about 30 cm thick and the weather is average, <z-
Drying can be completed in g weeks. The sludge mixed with a solidifying agent exhibits high alkalinity, but due to the increase in surface area due to the occurrence of cracks, acidic substances such as carbon dioxide gas in the atmosphere and neutralized ashes are formed, and the pH gradually decreases. Furthermore, since the mixing of rainwater promotes neutralization, the harmful 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、高効率忙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. A low cost, high efficiency bus can be carried out.

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1」 「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。
"Example 1" As shown in "Table 1", six types of test sludge were prepared, and the change over time in solar drying of each was measured.

ml、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、陽4,5は
それぞれ上記th 1 、 2 VCII wtチの普
通ポルトランドセメントを混入したもので、階6はN1
2の汚泥を凝集処理したものであシ、l’!11. 2
゜3は従来法による天日乾燥用汚泥であ!D、N14.
5は本発明法による天日乾燥用汚泥であシ、陽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。
ml, 2.3 is configured to cover various types of sludge generated from construction sites. In addition, positive 4 and 5 are those mixed with the above-mentioned th 1 and 2 VCII wt ordinary Portland cement, respectively, and floor 6 is N1.
It is made by coagulating the sludge from step 2, l'! 11. 2
゜3 is sludge for solar drying using the conventional method! D, N14.
5 is sludge for solar drying according to the method of the present invention, and 6 is sludge obtained by solid-liquid separation using chemicals (comparative example), which is expensive.
It is.

これら各汚泥試料は、表面からの蒸発乾燥のみに限定し
、下記のようにして処理状態を観察した。
Each of these sludge samples was subjected to evaporative drying only from the surface, and the treatment status was observed as follows.

中 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
受けない場所に設定した。
Medium Since each sample sludge was left in natural weather conditions, it was set up on the roof of a building where it would not be affected by sunlight, wind direction, etc.

(II)天日乾燥日数は約−夕月間の連続とし、その調
査は/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。
(II) The number of days for drying under the sun was continuous for approximately 1-2 months, and the measurement days for the survey were set on a per week basis. Therefore, samples for the same sample were prepared for the number of measurements.

GiD  試料容器はガラス製またはプラスチック製と
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。
GiD sample containers were made of glass or plastic and were embedded in sand saturated with water to prevent evaporation due to radiant heat from the sides of the container.

1ψ 気象データとして測定期間中のm度、湿度、日射
量、降雨量、風向、風速を測定した。
1ψ As meteorological data, m degrees, humidity, solar radiation, rainfall, wind direction, and wind speed were measured during the measurement period.

M 汚泥処理状態の評価は次の(a)〜(e)で行なっ
た。
M The evaluation of the sludge treatment state was performed in the following (a) to (e).

(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 falls due to evaporation).

(e)  汚泥pHの変化(溶出pH)。(e) Change in sludge pH (elution 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
った。
When measured in this manner, the results shown in Table 2 were obtained.

なお、実施期間中(り9日間)、雨天臼が77日あった
。期間中に連続し【降雨ii Omの週は3週あった。
During the implementation period (9 days), there were 77 days of rain. There were three consecutive weeks of rain during the period.

「晴」および「快晴」の日はllI日であるが、日射量
gMx/−以上の日数は2g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
一〜左m / sであったが、他の気象データとの相関
性について明確な傾向をみろことはできなかった。外気
温は実施した77月から7−月へと経過するに従って徐
々に低くなったが、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。
The number of "clear" and "clear" days was llI days, but the number of days with solar radiation of gMx/- or more was 2g days. Relative humidity naturally varied in relation to the rainy weather. The daily average wind speed was 1 to 2 m/s, but no clear trend could be seen in relation to other meteorological data. The outside temperature gradually decreased from July to July, when the experiment was conducted, but from a seasonal perspective, it was judged to be the typical temperature from autumn to winter. These weather data do not differ much from the Japan Meteorological Agency's average data over the past 30 years, and it has been determined that the weather during the implementation period was not due to abnormal weather.

また、実施期間では3週間目に雨天臼が9日あシ、この
間に!f; 0. !r mmの総降水゛量があった。
Also, during the implementation period, there will be 9 days of rain in the third week, and during this period! f; 0. ! There was a total rainfall of r mm.

従って、3週経過後の含水率は、この雨水の影響による
ものであるが、試料尚1以外の汚泥含水率は、−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、天日乾燥によって蒸発した水は、
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。
Therefore, the water content after 3 weeks is due to the influence of this rainwater, but the sludge water content of samples other than sample 1 has decreased to the same level or lower than after − week. It is thought that the penetration of rainwater into the sludge is extremely low. In other words, water evaporated by sun drying is
It can be said that the treatment effect is being shown without water being absorbed into sludge again.

表2に示す測定結果となった本実施例により、本発明方
法の下記の効果が明らかになった。
This example, which resulted in the measurement results shown in Table 2, revealed the following effects of the method of the present invention.

(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九分離し
てお〕、排水の除去が容易である。
(2) Therefore, the infiltration of rainwater, etc. 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
って異なるためのバラツキ範囲)混入することによって
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 (a range of variation depending on the type of sludge) to high water content sludge or bentonite slurry that has extremely poor settling properties.

(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シ、この亀裂は蒸発のための表面
積を増加させるため、よシ乾燥が促進する。
(4) Since the solidification strength of cement is low, cracks are easily generated due to evaporation of water, and these cracks increase the surface area for evaporation, thereby promoting drying.

(5)水分の蒸発に伴ってセメント固化汚泥の体積は大
幅(30〜30%)に減少する。
(5) The volume of cement solidified sludge decreases significantly (30-30%) with the evaporation of water.

(6)  セメント固化汚泥は、当初高いアルカリ性(
pH/ユ5〜/3)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 is initially highly alkaline (
The pH of the water is 5 to 3), but neutralization is promoted by contact with carbon dioxide gas in the atmosphere and rainwater, making it easy to adjust the pH of wastewater and permeated 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, neutralization of sludge elution pH is promoted,
Sludge after drying can be used in a wide range of applications.

「実施例2」 この実施例2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
一図に示すよ5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よいように砂利1を敷き
つめ、周囲を盛シ上ばて窪地状に形成したものであシ、
内側は着脱自在な仕切シ壁2によって各々複数個(図で
は乙ケずつ)のブロックからなる初期乾燥場3と一次乾
燥場4と3次乾燥場5とに区分けされている 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
通って貯水槽7に流入されるようになっている。この実
施例においては、まず、搬入汚泥は、汚泥ストック槽8
に入れられ、上澄液は貯水槽7iC送られ、沈殿汚泥は
ポンプ9によhsミキサ槽10に流入される。ミキサ一
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、初期乾燥場に移し入れる。ここで
、汚泥は71〜ノθ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を取シは
すし、ブルドーザ−B等により底部分を上面に出すよう
にして汚泥を一次乾燥場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−次
乾燥が終了したら、上記同様ブルドーザ−等により3次
乾燥場5に移し入れる。ここで、7〜,1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lを通って側溝6に流
れ込み、貯水槽7〜集められる。このようにして充分乾
燥が完了した汚泥は、ブルドーザ−等圧よシ乾燥場外に
出し、廃棄処分または再利用のために運び出される。一
方、貯水槽7に流入した浸透水は、pH18S等の水質
をチェックされ、規準値以下であれば、放流または再利
用され、規準値に違していなければ、中和、濾過等の処
理を施こして規準値以下にされ、放流または再利用され
る。
"Example 2" This Example 2 is an example in which industrial sludge is actually treated. In this actual treatment method, a solar drying field of the type shown in FIGS. 1 and 1 is used. As shown in the figure, this solar drying field is made by spreading gravel 1 so that it drains well, and the surrounding area is raised to form a depression.
The inside is divided by a removable partition wall 2 into an initial drying area 3, a primary drying area 4, and a tertiary drying area 5, each consisting of a plurality of blocks (one block in the figure). The sludge separated water, rainwater, and other permeated water that has passed through is configured to flow into a water storage tank 7 through a side gutter 6. In this embodiment, the imported sludge is first transferred to the sludge stock tank 8.
The supernatant liquid is sent to the water storage tank 7iC, and the settled sludge is flowed into the HS mixer tank 10 by the pump 9. In a 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 an initial drying place. Here, the sludge is left for 71 to θ days to undergo solidification, curing, and dewatering. After the initial drying period is completed, the partition wall 2 is removed and the sludge is transferred to the primary 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 materials are transferred to the tertiary drying place 5 using a bulldozer or the like as described above. Here, it is further dried in the sun for 7 to 1 day 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 collected in the water storage tank 7. The sludge that has been sufficiently dried in this way is removed from the drying area using a bulldozer and isobarized, and then 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 such as pH 18S, 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 treatments such as neutralization and filtration. The water is treated to bring it below standard values and then released or reused.

なお、搬入汚泥の性状をチェックした時点で残土扱い可
能なものと、流動性がなく、脱水性がよいものは、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
ェックして含水分が充分少ない場合または少なくなった
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、脱水性のよいものは、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 the properties of the sludge carried in are checked, sludge that can be treated as residual soil and sludge that has no fluidity and good dewatering properties can be treated without adding a solidifying agent, so they are treated as follows. First, if the remaining soil can be handled, its moisture content, strength, etc. are checked, and if or when the moisture content is sufficiently low, it is removed and disposed of or reused. and,
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、低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,
Disposal of the seepage water that occurs at the same time, which can be reused
It can be reused, requires a smaller processing plant area than before, and requires no special processing equipment, making low-cost processing possible.

「発明の効果」 以上説明したように、本発明によれば、単にごく少量の
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、非常に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、短期間に行な
うことができる。
"Effects of the Invention" As explained above, according to the present invention, sludge can be dried very efficiently by simply mixing a very small amount of solidifying agent into sludge and transferring this sludge to a solar drying place. Therefore, waste sludge can be treated at low cost and in a short period of time.

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

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・・・
・・・貯水僧、8・−・・・・汚泥ストック僧、9・・
・・・・ポンプ、10・・・・・・ミ千す一槽。
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 place, 4...Second drying place, 5.
...Third drying area, 6...Gutter, 7...
...Water storage monk, 8...Sludge stocking monk, 9...
...Pump, 10...Misensuichi tank.

Claims (1)

【特許請求の範囲】[Claims] 建設工事現場等から発生する廃棄汚泥に2〜5wt%の
固化材を添加、攪拌後、ただちに天日乾燥場へ移し入れ
、天日により乾燥、硬化することを特徴とする廃棄汚泥
の天日乾燥処理方法。
Solar drying of waste sludge, which is characterized by adding 2 to 5 wt% of a solidifying agent to waste sludge generated from construction sites, etc., stirring it, immediately transferring it to a solar drying place, and drying and hardening in the sun. Processing method.
JP17219885A 1985-08-05 1985-08-05 Treatment of sun-drying waste sludge Granted JPS6233599A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP17219885A JPS6233599A (en) 1985-08-05 1985-08-05 Treatment of sun-drying waste sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP17219885A JPS6233599A (en) 1985-08-05 1985-08-05 Treatment of sun-drying waste sludge

Publications (2)

Publication Number Publication Date
JPS6233599A true JPS6233599A (en) 1987-02-13
JPH0378160B2 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 Treatment of sun-drying waste sludge

Country Status (1)

Country Link
JP (1) JPS6233599A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01293199A (en) * 1988-05-20 1989-11-27 Shimizu Corp Drying treatment of muddy material

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US9001456B2 (en) 2010-08-31 2015-04-07 Teradyne, Inc. Engaging test slots
US11226390B2 (en) 2017-08-28 2022-01-18 Teradyne, Inc. Calibration process for an automated test system
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
US10775408B2 (en) 2018-08-20 2020-09-15 Teradyne, Inc. System for testing devices inside of carriers

Citations (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

Patent Citations (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 (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH01293199A (en) * 1988-05-20 1989-11-27 Shimizu Corp Drying treatment of muddy material

Also Published As

Publication number Publication date
JPH0378160B2 (en) 1991-12-12

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