JPH0152080B2 - - Google Patents
Info
- Publication number
- JPH0152080B2 JPH0152080B2 JP57139345A JP13934582A JPH0152080B2 JP H0152080 B2 JPH0152080 B2 JP H0152080B2 JP 57139345 A JP57139345 A JP 57139345A JP 13934582 A JP13934582 A JP 13934582A JP H0152080 B2 JPH0152080 B2 JP H0152080B2
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- air
- filtration
- drying
- traveling machine
- 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
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- 239000010802 sludge Substances 0.000 claims description 51
- 238000001035 drying Methods 0.000 claims description 28
- 238000001914 filtration Methods 0.000 claims description 21
- 239000010410 layer Substances 0.000 claims description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- 238000007664 blowing Methods 0.000 claims description 11
- 238000007790 scraping Methods 0.000 claims description 9
- 230000001737 promoting effect Effects 0.000 claims description 5
- 238000003756 stirring Methods 0.000 claims description 5
- 238000002156 mixing Methods 0.000 claims description 2
- 239000002344 surface layer Substances 0.000 claims description 2
- 208000005156 Dehydration Diseases 0.000 description 14
- 230000018044 dehydration Effects 0.000 description 14
- 238000006297 dehydration reaction Methods 0.000 description 14
- 238000001704 evaporation Methods 0.000 description 14
- 230000008020 evaporation Effects 0.000 description 14
- 238000000034 method Methods 0.000 description 7
- 239000000843 powder Substances 0.000 description 5
- 238000013019 agitation Methods 0.000 description 4
- 210000000078 claw Anatomy 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 239000006228 supernatant Substances 0.000 description 3
- 238000007796 conventional method Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 239000007788 liquid Substances 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 238000007747 plating Methods 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
Landscapes
- Drying Of Solid Materials (AREA)
- Treatment Of Sludge (AREA)
Description
【発明の詳細な説明】
〔産業上の利用分野〕
本発明は汚泥を乾燥処理槽において乾燥する方
法に関し、乾燥速度の大幅な促進と、これを省エ
ネルギー的に行うことを目的とする。DETAILED DESCRIPTION OF THE INVENTION [Field of Industrial Application] The present invention relates to a method of drying sludge in a drying treatment tank, and aims to significantly accelerate the drying rate and to do so in an energy-saving manner.
在来の汚泥の乾燥としては濾過床に汚泥水を張
り、水分を濾床側から排出すると共に天日による
蒸発乾燥する方法が採られ、水分の濾過排出する
手段としては、例えば濾床に砂層を設け、これに
より固液を分離する方法が用いられている。
Conventional methods for drying sludge include filling a filter bed with sludge water, draining the water from the filter bed, and drying it by evaporation under the sun. A method is used in which the solid-liquid is separated by providing a solid-liquid.
上記在来方法によるときは、張り込んだ汚泥水
は、時間の経過と共に汚泥は沈降し、清澄な上澄
水と汚泥にはつきり分かれ、汚泥中では重力と濾
過により垂直方向に濃度勾配が生じ、下方への水
分の移動を防げると共に、砂面上では局部的に脱
水が進むため厚さ数cmの高濃度の難透水性層が生
じて、濾過脱水を妨げる。
When using the above conventional method, the sludge in the sludge water that has been pumped will settle over time and separate into clear supernatant water and sludge, and a vertical concentration gradient will occur in the sludge due to gravity and filtration. In addition to preventing moisture from moving downward, dehydration progresses locally on the sand surface, creating a highly concentrated, impermeable layer several centimeters thick, which impedes filtration and dehydration.
ある測定例によると汚泥張込み2日後で汚泥高
さ40cmの時、平均濃度3.1%、上、中、下層のそ
れぞれの濃度は1.9%、2.2%、5.2%であり、濾床
面上は14.2%であつた。 According to a measurement example, when the sludge height is 40 cm after 2 days of sludge filling, the average concentration is 3.1%, the concentrations in the upper, middle, and lower layers are 1.9%, 2.2%, and 5.2%, and the concentration on the filter bed surface is 14.2%. It was %.
このために在来型天日乾燥床では濾過脱水によ
る水分除去の割合は小さく一般に20〜40%であ
り、上澄水排出により20〜40%、蒸発により30〜
40%となる。 For this reason, in conventional solar drying beds, the proportion of water removed by filtration and dehydration is small, generally 20-40%, 20-40% by supernatant water discharge, and 30-40% by evaporation.
It will be 40%.
このように蒸発による水分除去量の割合が大き
く、蒸発量は夏で3.5〜7mm/日、冬で1.5mm/日
以下と小さいので乾燥に時間を要するものであ
る。本発明はこのような蒸発状況に鑑みてなした
ものである。 As described above, the proportion of water removed by evaporation is large, and the amount of evaporation is small at 3.5 to 7 mm/day in summer and 1.5 mm/day or less in winter, so drying takes time. The present invention was made in view of such evaporation conditions.
上記問題点を解決するためこの発明は数床の並
列した透水性濾床を持つた汚泥処理槽に順次各濾
床に対し移動可能に走行機を架設し、濾床に汚泥
水を張り、走行機に備えた空気吹込手段による空
気撹拌と、走行機の移行に伴いこれに設けた固定
板による濾床面上の難透水性汚泥層の掻取り並び
に上記吹込み空気による汚泥水との混合撹拌によ
る濾過脱水の促進と、濾過脱水処理終了後の汚泥
に対し切込みによる亀裂の生成と乾燥表面層の掻
取りによる蒸発乾燥の促進とを順次行うようにな
すものである。
In order to solve the above-mentioned problems, this invention has a sludge treatment tank having several permeable filter beds arranged in parallel. Air agitation by the air blowing means provided in the machine, scraping of the impermeable sludge layer on the filter bed surface by a fixed plate installed on the machine as the machine moves, and mixing and stirring with the sludge water by the above-mentioned blown air. After the filtration and dehydration treatment is completed, the sludge is sequentially promoted to generate cracks by making cuts and to accelerate evaporative drying by scraping off the dry surface layer.
濾過床に張られた汚泥水は、固定板の移行によ
る難透水性層の剥離と、空気撹拌とにより汚泥は
沈殿が阻止され、脱水が促進される。
The sludge spread on the filter bed is prevented from settling due to the peeling of the impermeable layer due to the movement of the fixed plate and air agitation, and dewatering is promoted.
また濾過脱水処理の終了後は汚泥層に対する切
込みの付与と乾燥表面の掻取りにより蒸発乾燥が
促進される。 Further, after the filtration and dehydration treatment is completed, evaporative drying is promoted by making incisions in the sludge layer and scraping off the drying surface.
以下本発明汚泥乾燥方法を図面に示す実施例に
基づいて説明する。
The sludge drying method of the present invention will be explained below based on embodiments shown in the drawings.
本発明の濾過脱水乾燥促進の手段は第4図のよ
うな走行機に吊り下げた管の下部に適当な間隔で
空気吹出し孔を配置した数本の空気吹込用の空気
管1と固定板2から成る。ここに使用する走行機
は鍍金装置、汚泥処理の沈殿槽等における槽上を
走行する走行機方式を利用するものである。そし
て汚泥水を効率よく撹拌するためには空気が優れ
ているので数本の空気管から空気を吹出しながら
走行機を濾床の全幅を往復走行させると少ない風
量で均一な撹拌が可能であり、垂直方向の汚泥濃
度が均一となる。 The means for promoting filtration, dehydration, and drying of the present invention is as shown in FIG. Consists of. The traveling machine used here utilizes a traveling machine system that travels over tanks in plating equipment, sedimentation tanks for sludge treatment, and the like. Air is the best way to stir sludge water efficiently, so if you run the traveling machine back and forth across the entire width of the filter bed while blowing air out of several air pipes, uniform agitation can be achieved with a small amount of air. The sludge concentration in the vertical direction becomes uniform.
更に濾床面上に形成される高濃度の難透水性層
の除去が必要となるがこのためには固定板による
掻取りが確実で、走行機の動力以外の動力を要し
ない。固定板により掻き取られた難透水性汚泥は
空気撹拌により粉砕され、周囲の汚泥と均一化さ
れる。 Furthermore, it is necessary to remove the highly concentrated, water-impermeable layer formed on the filter bed surface, but for this purpose, scraping with a fixed plate is reliable, and no power other than the power of the traveling machine is required. The poorly permeable sludge scraped off by the fixed plate is pulverized by air agitation and is homogenized with the surrounding sludge.
この空気吹込用の空気管1と固定板2とより成
る濾過脱水促進手段では汚泥水張込み中から走行
機は走行を開始するので上澄水は生じないが、一
般には10日以内に100cmの高さに張り込んだ場合
25〜10cmとなり濃度2〜5%のものが15〜25%と
なる。 With this filtration and dehydration promoting means consisting of the air pipe 1 for air blowing and the fixed plate 2, the traveling machine starts running while the sludge is being filled, so no supernatant water is produced, but generally the height reaches 100 cm within 10 days. If you are stuck in
25 to 10 cm and a concentration of 2 to 5% becomes 15 to 25%.
第2図に走行距離10mの場合の数種の汚泥の実
験データを示す。 Figure 2 shows experimental data for several types of sludge at a travel distance of 10 m.
このように走行機における濾過脱水促進手段の
空気量は幅1m当り100〜200Nl/分であり10m
走行させれば1m2当り10〜20Nl/分の空気量で
よいことになり、極めて省エネルギー的である。
走行可能な距離は汚泥によつて異なり、一般に10
〜20mとなる。 In this way, the amount of air in the filtration and dehydration promoting means in the traveling machine is 100 to 200 Nl/min per 1 m width, which is 10 m.
When running, the amount of air required is 10 to 20 Nl/min per square meter, which is extremely energy-saving.
The distance that can be traveled varies depending on the sludge, and is generally 10
~20m.
また濾過脱水終了時までの水分除去量の90〜95
%は濾過脱水量であり、全水分除去量に対しても
80〜85%を占める。従つて濾過脱水量のうち蒸発
による水分除去量は15〜20%になる。 Also, the amount of water removed until the end of filtration and dehydration is 90 to 95.
% is the amount of filtration and dehydration, and is also relative to the total amount of water removed.
It accounts for 80-85%. Therefore, the amount of water removed by evaporation of the amount of water removed by filtration is 15 to 20%.
この走行機は汚泥dの粘性が増し、もはや濾過
水がほとんど生じなくなつた時(濾過脱水終了
時)、濾過脱水促進装置を吊り上げて、次の槽へ
移動して汚泥を張り込み往復走行を開始する。先
の濾過脱水が終了した汚泥は蒸発乾燥に入り、1
〜3日を経て亀裂が入り始める。このようにして
汚泥に亀裂が生じ始めると再び走行機をこの槽へ
移動させ、走行機に取り付けた蒸発乾燥促進手段
のたて切りアタツチメン例えば第3図aのような
爪3によつて人工的に亀裂を入れることにより、
亀裂を大きくかつ数を多くして蒸発面積を多くし
て蒸発を促進する。このたて切りアタツチメント
は走行機に対して着脱自在に取付けられており、
濾過脱水促進工程には取外しておくものとする。 When the viscosity of the sludge d increases and almost no filtrate is produced (at the end of filtration and dehydration), this traveling machine lifts the filtration and dehydration accelerator, moves to the next tank, fills it with sludge, and starts reciprocating travel. do. The sludge that has undergone the previous filtration and dewatering process is evaporated and dried.
Cracks begin to appear after ~3 days. In this way, when cracks begin to appear in the sludge, the traveling machine is moved to this tank again, and the vertical cutting attachment of the evaporative drying accelerating means attached to the traveling machine, for example, by the claw 3 as shown in Fig. 3a, is used to artificially cut the sludge. By creating a crack in
Evaporation is promoted by increasing the size and number of cracks to increase the evaporation area. This vertical cutting attachment is removably attached to the traveling machine.
It shall be removed during the filtration and dehydration promotion process.
更にその後は汚泥の空気にさらされている部分
のみは急速に乾燥してくるので、第3図bのよう
に層切り用プレート5を用いて層切りを行ない、
蒸発乾燥を促進する。 Furthermore, since only the portion of the sludge exposed to the air dries rapidly after that, layer cutting is performed using the layer cutting plate 5 as shown in FIG. 3b.
Promotes evaporative drying.
また更に冬期は蒸発乾燥中の汚泥表面は凍結融
解をくり返し、微粉化した乾燥汚泥粉に1〜2cm
の層で掩われる。この層は汚泥内部からの毛管減
少による水分移動を妨げるので蒸発はほとんど進
まない。そこで乾燥汚泥粉を更に第3図Cのよう
にすき取り用プレート6を用いてすき取りを行い
蒸発乾燥を促進する。たて切りアタツチメント例
えば爪3及び層切り用プレート5、すき取り用プ
レート6は走行機に垂設したる杆又は空気送込用
の空気管1に各別のものを取付けるか、又は層切
り用と、すき取り用を兼ねさせたり、たて切りア
タツチメントの三者を兼ねさせるもので、そして
これらを走行機にその使用目的に応じてその取付
角度を変えられるようにして着脱自在に担持する
ものである。 Furthermore, in winter, the surface of the sludge during evaporation drying freezes and thaws repeatedly, resulting in a fine powder of 1 to 2 cm.
It is covered by a layer of This layer prevents moisture movement from inside the sludge due to capillary reduction, so evaporation hardly progresses. Therefore, the dried sludge powder is further scraped off using a scraping plate 6 as shown in FIG. 3C to promote evaporative drying. The warp cutting attachments, for example, the claws 3, the plate 5 for layer cutting, and the plate 6 for scraping, can be attached separately to a rod hanging vertically on the traveling machine or to the air pipe 1 for feeding air, or can be used for layer cutting. It also serves as a plowing attachment and a vertical cutting attachment, and it is detachably carried on the traveling machine so that its mounting angle can be changed depending on the purpose of use. It is.
このような蒸発乾燥促進手段をとることにより
濾過脱水後放置する場合に比べ、蒸発乾燥期間が
夏期で3/4〜2/3、冬期で1/3〜1/2と
なる。 By employing such means for accelerating evaporative drying, the evaporative drying period is reduced to 3/4 to 2/3 in the summer and 1/3 to 1/2 in the winter compared to the case where the product is left to stand after filtration and dehydration.
第4図はこれら空気管及び固定板を組み込んだ
走行機の実施例で、空気管と、たて切りアタツチ
メント・層切りプレート・すき取りプレートの代
りに固定板とを担持して処理槽上を往復動させる
走行機の1例を示すもので、同図Aはその一槽を
引き出して示した側面図、同図BはA図の正面
図、同図Cは並列する多槽の平面図である。第4
図に於て7は走行モータM1に駆動されレール
8,8上を走行する台車であり、この台車7上に
空気吹込用の管1(送風機9によつて圧搾空気を
送る)を担持させ空気吹込管1(之れに枝管状に
吹込本管1aを分岐する)を台車の走行につれて
移動させる。又台車には巻上モータM2によつて
空気管群を昇降させて各床間の移動を可能とし、
かつ空気吹込管4を吹出し位置を調節するような
すものである。このようにして走行機を前進させ
ることにより濾床面に形成される難透水性汚泥層
は固定板により掻き取られるとともに空気管にて
吹込んだ空気により汚泥水と混合撹拌して濾過を
促進する。そして同図CではB槽の処理を行つて
おり、この槽の処理を終えるとC槽、D槽に移
り、D槽の処理が終ればA槽に戻るものである。
このようにして汚泥に亀裂が生じ始めると再び走
行機をこの槽へ移動させ、走行機に取り付けた蒸
発乾燥促進手段のたて切りアタツチメン例えば第
3図aのような爪3によつて人工的に亀裂を入れ
ることにより、亀裂を大きくかつ数を多くして蒸
発面積を多くして蒸発を促進する。汚泥に亀裂が
生じて大きくなると、アタツチメントの取付角度
を変えて走行機を更に走行させると、このアタツ
チメントが第3図aに示すように層切りプレート
としての作用をして層切りを行う。また蒸発乾燥
中の汚泥表面に微粉化した乾燥汚泥粉が生じると
蒸発乾燥を損うのでこれを除去する必要がある。
この乾燥汚泥粉をアタツチメントの角度を変え
て、すき取り用プレートとして用いて、汚泥粉を
取り去るものである。この層切り、すき取りは走
行機の往復走行により行われる。これを順次各槽
にて行う。 Figure 4 shows an example of a traveling machine incorporating these air pipes and a fixed plate, which carries the air pipe and a fixed plate in place of the vertical cutting attachment, layer cutting plate, and skimming plate, and moves over the processing tank. This figure shows an example of a reciprocating traveling machine. Figure A is a side view of one tank pulled out, Figure B is a front view of Figure A, and Figure C is a plan view of multiple tanks arranged in parallel. be. Fourth
In the figure, 7 is a truck driven by a traveling motor M1 and runs on rails 8, 8, and an air blowing pipe 1 (for sending compressed air by a blower 9) is carried on this truck 7. The blowing pipe 1 (which branches off the main blowing pipe 1a into branch pipes) is moved as the truck travels. In addition, the trolley is equipped with a hoisting motor M2 to raise and lower a group of air pipes to enable movement between each floor.
Moreover, the blowing position of the air blowing pipe 4 is adjusted. By moving the traveling machine forward in this way, the poorly permeable sludge layer that forms on the filter bed surface is scraped off by the fixed plate, and the air blown in through the air pipe mixes with the sludge water to promote filtration. do. In C of the same figure, processing is performed in tank B, and when the processing in this tank is completed, the process moves to tank C and tank D, and when the processing in tank D is completed, the process returns to tank A.
In this way, when cracks begin to appear in the sludge, the traveling machine is moved to this tank again, and the vertical cutting attachment of the evaporative drying accelerating means attached to the traveling machine, for example, by the claw 3 as shown in Fig. 3a, is used to artificially cut the sludge. By creating cracks in the gas, the cracks are made larger and more numerous, increasing the evaporation area and promoting evaporation. When cracks occur in the sludge and become larger, when the mounting angle of the attachment is changed and the traveling machine is run further, this attachment acts as a layer cutting plate to cut the layers as shown in Figure 3a. Furthermore, if pulverized dried sludge powder is formed on the surface of the sludge during evaporation drying, it will impair evaporation drying and must be removed.
This dried sludge powder is used as a scooping plate by changing the angle of the attachment to remove the sludge powder. This layer cutting and clearance is performed by reciprocating movement of a traveling machine. This is done sequentially in each tank.
本発明に於ては一槽に於ける乾燥処理をきわめ
て効率良く進行させることにより、全槽の処理を
きわめて短時日に完了することができるものであ
る。 In the present invention, the drying process in one tank is carried out extremely efficiently, so that the drying process in all the tanks can be completed in an extremely short period of time.
本発明によるときは、空気の吹き込みと移動す
る固定板による難透水性汚泥層の剥離とによる撹
拌により濾過脱水作用を促進すると共に、濾過脱
水処理終了後の汚泥に対し、切込み付与、乾燥表
面の掻き取り等蒸発乾燥を促進するようにしたか
ら、乾燥を効果的に行うことができる。また上記
汚泥層の掻取は走行機の移行によりこれに取付け
た固定板により行うようにしたから、特別の動力
を必要とせず省エネルギーを計ることができる等
の効果を有する。
According to the present invention, the filtration and dewatering action is promoted by stirring by blowing air and peeling off the hardly permeable sludge layer by the moving fixed plate, and at the same time, the sludge after the filtration and dewatering treatment is provided with incisions and the drying surface is Since evaporative drying is promoted by scraping, etc., drying can be carried out effectively. Further, since the sludge layer is scraped off by a fixed plate attached to the moving machine, it is possible to save energy without requiring special power.
第1図は本発明の原理を示す説明図、第2図は
実験データの線図、第3図a,b,cは工程図、
第4図Aは装置の一例を示すもので一槽を抽出し
て示した側面図、同図Bは正面図、同図Cは平面
図である。
1は空気吹込管、2は固定板、3はアタツチメ
ント(縦切)、4は空気管(縦切用)、5はプレー
ト(層切用)、6はプレート(すき取用)、7は台
車、8はレール、9は送風機。
Figure 1 is an explanatory diagram showing the principle of the present invention, Figure 2 is a diagram of experimental data, Figure 3 a, b, and c are process diagrams.
FIG. 4A shows an example of the apparatus, and is a side view of one tank, FIG. 4B is a front view, and FIG. 4C is a plan view. 1 is an air blowing pipe, 2 is a fixed plate, 3 is an attachment (for vertical cutting), 4 is an air pipe (for vertical cutting), 5 is a plate (for layer cutting), 6 is a plate (for skimming), 7 is a trolley , 8 is the rail, 9 is the blower.
Claims (1)
槽に順次各濾床に対し移動可能に走行機を架設
し、濾床に汚泥水を張り、走行機に備えた空気吹
込手段による空気撹拌と、走行機の移行に伴いこ
れに設けた固定板による濾床面上の難透水性汚泥
層の掻取り並びに上記吹込み空気による汚泥水と
の混合撹拌による濾過脱水の促進と、濾過脱水処
理終了後の汚泥に対し切込みによる亀裂の生成と
乾燥表面層の掻取りによる蒸発乾燥の促進とを順
次行うことを特徴とする汚泥乾燥方法。1. In a sludge treatment tank with several permeable filter beds arranged in parallel, a traveling machine is installed so as to be movable to each filter bed in turn, the filter beds are filled with sludge water, and air is supplied by an air blowing means provided in the traveling machine. Stirring, scraping of the poorly permeable sludge layer on the filter bed surface by a fixed plate installed on the moving machine, promotion of filtration and dewatering by mixing and stirring the sludge water with the blown air, and filtration and dewatering. A sludge drying method characterized by sequentially performing on sludge after treatment, creating cracks by making cuts and promoting evaporative drying by scraping off the dry surface layer.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57139345A JPS5929100A (en) | 1982-08-11 | 1982-08-11 | Method and device for drying sludge |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP57139345A JPS5929100A (en) | 1982-08-11 | 1982-08-11 | Method and device for drying sludge |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS5929100A JPS5929100A (en) | 1984-02-16 |
| JPH0152080B2 true JPH0152080B2 (en) | 1989-11-07 |
Family
ID=15243161
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP57139345A Granted JPS5929100A (en) | 1982-08-11 | 1982-08-11 | Method and device for drying sludge |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPS5929100A (en) |
Families Citing this family (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2686499B2 (en) * | 1988-06-21 | 1997-12-08 | 豊 川野 | Manufacturing method of iron-based ceramic materials |
| CN118954897B (en) * | 2024-10-15 | 2024-12-10 | 海锝智能(广东)科技有限公司 | Sludge drying system |
-
1982
- 1982-08-11 JP JP57139345A patent/JPS5929100A/en active Granted
Also Published As
| Publication number | Publication date |
|---|---|
| JPS5929100A (en) | 1984-02-16 |
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