JPS63224799A - Dehydration of sludge or the like - Google Patents
Dehydration of sludge or the likeInfo
- Publication number
- JPS63224799A JPS63224799A JP62058150A JP5815087A JPS63224799A JP S63224799 A JPS63224799 A JP S63224799A JP 62058150 A JP62058150 A JP 62058150A JP 5815087 A JP5815087 A JP 5815087A JP S63224799 A JPS63224799 A JP S63224799A
- Authority
- JP
- Japan
- Prior art keywords
- sludge
- pipeline
- heating
- water
- screen
- 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.)
- Pending
Links
- 239000010802 sludge Substances 0.000 title claims abstract description 46
- 230000018044 dehydration Effects 0.000 title abstract description 4
- 238000006297 dehydration reaction Methods 0.000 title abstract description 4
- 238000010438 heat treatment Methods 0.000 claims abstract description 26
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 20
- 239000007787 solid Substances 0.000 claims abstract description 9
- 238000000034 method Methods 0.000 claims description 17
- 239000000701 coagulant Substances 0.000 abstract 1
- 239000000499 gel Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 230000002776 aggregation Effects 0.000 description 2
- 230000007062 hydrolysis Effects 0.000 description 2
- 238000006460 hydrolysis reaction Methods 0.000 description 2
- 239000005416 organic matter Substances 0.000 description 2
- 238000005086 pumping Methods 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 239000010801 sewage sludge Substances 0.000 description 2
- 230000008016 vaporization Effects 0.000 description 2
- 238000009834 vaporization Methods 0.000 description 2
- 238000005054 agglomeration Methods 0.000 description 1
- 238000004220 aggregation Methods 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 239000000084 colloidal system Substances 0.000 description 1
- 230000003750 conditioning effect Effects 0.000 description 1
- 238000010924 continuous production Methods 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000003247 decreasing effect Effects 0.000 description 1
- 239000008394 flocculating agent Substances 0.000 description 1
- 239000012530 fluid Substances 0.000 description 1
- 239000000017 hydrogel Substances 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 239000010865 sewage Substances 0.000 description 1
- 230000007928 solubilization Effects 0.000 description 1
- 238000005063 solubilization Methods 0.000 description 1
- 238000003756 stirring Methods 0.000 description 1
- 238000003860 storage Methods 0.000 description 1
- 210000002700 urine Anatomy 0.000 description 1
Landscapes
- Treatment Of Sludge (AREA)
Abstract
Description
【発明の詳細な説明】
「産業上の利用分野」
本発明は下水、採尿及びそれらの浄化槽より発生する汚
泥や含水率の高い原料を脱水する方法に関するものであ
る。DETAILED DESCRIPTION OF THE INVENTION "Field of Industrial Application" The present invention relates to a method for dewatering sludge and raw materials with high water content generated from sewage, urine collection, and septic tanks thereof.
「従来の技術」
下水汚泥の固形物は親水性コロイド粒子からなり、しか
も内部に多量の水分を包含している。汚泥の加熱は粒子
の熱運動を増し、粒子の衝突と会合の頻度を高め、つい
には粒子間の凝集に至る。"Prior Art" Solid sewage sludge consists of hydrophilic colloid particles and contains a large amount of water inside. Heating the sludge increases the thermal motion of the particles, increases the frequency of particle collisions and associations, and eventually leads to interparticle agglomeration.
また、下水汚泥のようにタンパク質などをかなり含むヒ
ドロゲルは熱によってゲル構造が崩壊され、多量に内蔵
されている水分が分離してくる、いわゆる離漿が生起す
る。さらに有機物は熱による加水分解が起こって可溶化
、または液化が進行する。In addition, in hydrogels that contain a considerable amount of protein, such as sewage sludge, the gel structure is disrupted by heat, causing so-called syneresis, in which a large amount of built-in water separates. Furthermore, the organic matter undergoes hydrolysis due to heat and progresses to solubilization or liquefaction.
すなわち、汚泥の熱処理によって、熱による凝集(分子
運動論的現象)、ゲル構造が破壊され内蔵している水分
が分離する(離漿現象)、有機物の加水分解(液化現象
)、が生起するが、これらの現象は段階的に起きるもの
ではなく、いずれも同時にしかも全体的に進行するもの
である。また、熱処理の効果の程度は汚泥の性質、処理
時間、処理温度および処理雰囲気に大きく左右される。In other words, heat treatment of sludge causes thermal aggregation (molecular kinetic phenomenon), destruction of the gel structure and separation of internal water (syneresis phenomenon), and hydrolysis of organic matter (liquefaction phenomenon). , these phenomena do not occur in stages, but progress simultaneously and overall. Furthermore, the degree of effectiveness of heat treatment is greatly influenced by the properties of the sludge, treatment time, treatment temperature, and treatment atmosphere.
この熱処理法は汚泥を一定時間高温に保つことによって
汚泥の固液分離性を改質する方法であり、現在用いられ
ている熱処理法の方式と反応条件を第1表に示した。第
1表のとおり、熱処理法には高温法と低温法とがある。This heat treatment method improves the solid-liquid separability of sludge by keeping the sludge at a high temperature for a certain period of time. Table 1 shows the currently used heat treatment methods and reaction conditions. As shown in Table 1, heat treatment methods include high temperature methods and low temperature methods.
高温法はいずれも無酸素状態で汚泥を200°C(圧力
18に〆M)で、1時間前後加熱することによって汚泥
を改質するものである。このような改質によって汚泥の
脱水性は著しく改善されるので、汚泥の調質法としては
きわめて効果的な方法である。In both high temperature methods, sludge is reformed by heating it at 200°C (pressure: 18M) for about 1 hour in an oxygen-free condition. Since the dewaterability of sludge is significantly improved by such modification, it is an extremely effective method for conditioning sludge.
第 1 表
(汚泥処理工学、平岡正勝著、講談社発行第1版198
3.9.20、pl 11 )。しかし含水率の高い上
記汚泥の脱水には汚泥搬送、空気注入、加熱及び脱水と
工程が分離し連続工程によることは困難であった。Table 1 (Sludge treatment engineering, written by Masakatsu Hiraoka, published by Kodansha, 1st edition 198)
3.9.20, pl 11). However, the dewatering of the sludge with a high water content involves separate steps of sludge transport, air injection, heating, and dewatering, making it difficult to use a continuous process.
[発明が解決しようとする問題点−1
本発明は汚泥等の搬送加熱脱水工程を連続的に行い脱水
作業を簡略化することを目的とするものである。[Problems to be Solved by the Invention-1] The object of the present invention is to simplify the dewatering work by continuously carrying out the process of transporting, heating, and dehydrating sludge and the like.
「問題点を解決するための手段」
本発明は汚泥等をポンプにより配管で圧送し、同配管の
出口に接続した筒状スクリーンの内部に圧搾して同スク
リーンによって水分及び固形物を分離し、その際上記配
管内の圧送汚泥を加熱することを特徴とする汚泥等の脱
水方法によって構成される。"Means for Solving the Problems" The present invention involves pumping sludge through piping, squeezing it into a cylindrical screen connected to the outlet of the piping, and separating water and solids through the screen. At this time, it is constituted by a method of dewatering sludge, etc., which is characterized by heating the sludge fed under pressure within the pipe.
1作用」
従って含水率の高い汚泥等をポンプ1によって配管2内
に圧送すると同汚泥等は配管2の出口に接続した筒状ス
クリーン3内に圧入され、水分は同スクリーン3から排
出され、水分の少くなった脱水汚泥は同スクリーン3の
端部から排出される。Therefore, when sludge, etc. with a high water content is pumped into the pipe 2 by the pump 1, the sludge, etc. is forced into the cylindrical screen 3 connected to the outlet of the pipe 2, and the water is discharged from the screen 3, and the water is removed. The dehydrated sludge that has decreased is discharged from the end of the screen 3.
上記配管2内の圧送過程において高含水圧送汚泥は加熱
されるためゲル構造が破壊され水分と固形物との分離現
象が促進されその状態で筒状スクリーン3内に圧入され
同スクリーン3によって水分と固形物とが分離するもの
である。又上記加熱は加圧状態の汚泥の蒸発潜熱に奮わ
れることなく温度上昇にのみ費やされる。During the pressure-feeding process in the pipe 2, the high water-containing pressure-fed sludge is heated, which destroys its gel structure and promotes the separation of water and solids. Solid matter is separated. In addition, the above-mentioned heating is used only to increase the temperature without being stimulated by the latent heat of vaporization of the sludge under pressure.
「実施例」
高含水率のゲル状汚泥5をホッパーに投入し、同ホッパ
ーからピング1によって配管2内に圧送する。配管2の
先端出口には第1図に示すように截頭円錐筒状スクリー
ン3の大径密閉端を接続連通させ小径端を開口する0又
第2図に示すように円筒状スクリーン3の密閉端を接続
連通させ、他端開口部に円錐形栓6をシリンダー7によ
って摺動自在に支持し、開口部の内周と円錐形栓6の外
周との間に脱水汚泥排出間5tt−形成する。上記配管
2には空気注入口8を設け、これを空気圧縮機9に接続
し、同注入口8と上記スクリーン3との中間において配
管2を加熱管4′で被覆して加熱装置4を形成し、同加
熱管4にボイラー10からの圧力蒸気管11を接続する
ことにより加熱管4′内に高温蒸気を圧入し配管2内の
圧送汚泥を加熱することができ、その加熱によって同汚
泥を熱処理するものである。このような熱処理及び上記
脱水工程はポンプ1による汚泥圧送を中断することなく
行われ、圧送汚泥は加圧状態であるため上記加熱は温度
上昇にのみ費やされ水分の蒸発潜熱に奮われることはな
い。尚図中Mで示すものはポンプ1の駆動用モーター、
12は圧送汚泥の流動推力によって回転して汚泥の攪拌
及び伝熱面の汚れを掻き取るスクリュー、13け汚泥の
推力によって回転しスクリーン3のf面の汚れを掻き取
るスクリュー、14け分離水ホッパー、15は脱水汚泥
収容函、16けドレン口である。"Example" A gelatinous sludge 5 with a high water content is put into a hopper, and from the same hopper is fed under pressure into a pipe 2 by a ping 1. As shown in FIG. 1, the large-diameter closed end of a truncated conical cylindrical screen 3 is connected to the outlet of the pipe 2, and the small-diameter end is opened. The ends are connected and communicated, and a conical plug 6 is slidably supported by a cylinder 7 in the opening of the other end, and a dewatered sludge discharge gap of 5tt is formed between the inner periphery of the opening and the outer periphery of the conical plug 6. . The piping 2 is provided with an air inlet 8, which is connected to an air compressor 9, and the piping 2 is covered with a heating tube 4' between the inlet 8 and the screen 3 to form a heating device 4. By connecting the pressure steam pipe 11 from the boiler 10 to the heating pipe 4, high-temperature steam can be injected into the heating pipe 4' to heat the pressure-fed sludge in the pipe 2, and the sludge can be heated by the heating. It is heat treated. Such heat treatment and the above-mentioned dewatering process are performed without interrupting the sludge pumping by the pump 1, and since the pumped sludge is under pressure, the above-mentioned heating is used only to raise the temperature, and is not stimulated by the latent heat of vaporization of water. do not have. In addition, what is indicated by M in the figure is the drive motor for pump 1.
12 is a screw that rotates by the fluid thrust of the pumped sludge to stir the sludge and scrape dirt off the heat transfer surface; 13 is a screw that rotates by the thrust of the sludge to scrape dirt on the f side of the screen 3; and 14 is a separated water hopper. , 15 is a dehydrated sludge storage box, and 16 is a drain port.
「効果コ
本発明は上述の方法によったので高含水汚泥5等の水分
、固形物の分離を連続的に行い得て脱水作業能率を向上
し得るばかりでなく高価な凝集剤を要せずかつ加熱量を
軽減し得て脱水効率を向上することができる。``Effects: Since the present invention is based on the method described above, it is possible to continuously separate water and solids from high water content sludge 5, etc., which not only improves dewatering efficiency but also eliminates the need for expensive flocculants. Moreover, the amount of heating can be reduced and the dehydration efficiency can be improved.
第1図は本発明の汚泥等の脱゛水方法を行う装置の側面
図、第2図は第1図の他の実施例の側面図である。
1・・ポンプ、2・・配管、3・・筒状スクリーン、4
・・加熱装置。FIG. 1 is a side view of an apparatus for carrying out the method for dewatering sludge, etc. of the present invention, and FIG. 2 is a side view of another embodiment of the method shown in FIG. 1. Pump, 2. Piping, 3. Cylindrical screen, 4
...Heating device.
Claims (2)
口に接続した筒状スクリーンの内部に圧搾して同スクリ
ーンによつて水分及び固形物を分離し、その際上記配管
内の圧送汚泥を加熱することを特徴とする汚泥等の脱水
方法。(1) Sludge, etc. is pumped through piping, compressed into the inside of a cylindrical screen connected to the outlet of the piping, and water and solids are separated by the screen, at which time the sludge in the piping is A method for dewatering sludge, etc., characterized by heating.
許請求の範囲第1項記載の汚泥等の脱水方法。(2) A method for dewatering sludge, etc. according to claim 1, which comprises heating the air-injected and pressure-fed sludge.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62058150A JPS63224799A (en) | 1987-03-13 | 1987-03-13 | Dehydration of sludge or the like |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP62058150A JPS63224799A (en) | 1987-03-13 | 1987-03-13 | Dehydration of sludge or the like |
Publications (1)
Publication Number | Publication Date |
---|---|
JPS63224799A true JPS63224799A (en) | 1988-09-19 |
Family
ID=13075960
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP62058150A Pending JPS63224799A (en) | 1987-03-13 | 1987-03-13 | Dehydration of sludge or the like |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS63224799A (en) |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01315396A (en) * | 1988-03-25 | 1989-12-20 | Ngk Insulators Ltd | Sludge treating equipment and method for sending sludge under pressure in said equipment |
JPH02245298A (en) * | 1989-03-20 | 1990-10-01 | Ngk Insulators Ltd | Method for sending dehydrated cake under pressure |
JP2013057498A (en) * | 2012-11-02 | 2013-03-28 | Metawater Co Ltd | Sewage sludge supply device for incinerator |
JP2015091573A (en) * | 2013-10-03 | 2015-05-14 | 青山 吉郎 | Direct heating of sludge |
Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5273547A (en) * | 1975-12-17 | 1977-06-20 | Ngk Insulators Ltd | Method of dehydrating sludge by screw pressing |
JPS537574A (en) * | 1976-06-22 | 1978-01-24 | Dorr Oliver Inc | Method of preparing sludge and its apparatus |
JPS5599398A (en) * | 1979-01-23 | 1980-07-29 | Ebara Infilco Co Ltd | Dehydration method for sludge |
JPS5716679A (en) * | 1980-06-30 | 1982-01-28 | Marusan Matsuno Shoten:Kk | Preparation of crab meat preserved with "miso" |
JPS5743320A (en) * | 1976-06-23 | 1982-03-11 | Heraeus Gmbh W C | Electric contact blank |
JPS6048199A (en) * | 1983-08-29 | 1985-03-15 | Kurita Water Ind Ltd | Sludge dehydrator |
-
1987
- 1987-03-13 JP JP62058150A patent/JPS63224799A/en active Pending
Patent Citations (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5273547A (en) * | 1975-12-17 | 1977-06-20 | Ngk Insulators Ltd | Method of dehydrating sludge by screw pressing |
JPS537574A (en) * | 1976-06-22 | 1978-01-24 | Dorr Oliver Inc | Method of preparing sludge and its apparatus |
JPS5743320A (en) * | 1976-06-23 | 1982-03-11 | Heraeus Gmbh W C | Electric contact blank |
JPS5599398A (en) * | 1979-01-23 | 1980-07-29 | Ebara Infilco Co Ltd | Dehydration method for sludge |
JPS5716679A (en) * | 1980-06-30 | 1982-01-28 | Marusan Matsuno Shoten:Kk | Preparation of crab meat preserved with "miso" |
JPS6048199A (en) * | 1983-08-29 | 1985-03-15 | Kurita Water Ind Ltd | Sludge dehydrator |
Cited By (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01315396A (en) * | 1988-03-25 | 1989-12-20 | Ngk Insulators Ltd | Sludge treating equipment and method for sending sludge under pressure in said equipment |
JPH02245298A (en) * | 1989-03-20 | 1990-10-01 | Ngk Insulators Ltd | Method for sending dehydrated cake under pressure |
JP2013057498A (en) * | 2012-11-02 | 2013-03-28 | Metawater Co Ltd | Sewage sludge supply device for incinerator |
JP2015091573A (en) * | 2013-10-03 | 2015-05-14 | 青山 吉郎 | Direct heating of sludge |
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