JPS63224799A - Dehydration of sludge or the like - Google Patents

Dehydration of sludge or the like

Info

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
Application number
JP62058150A
Other languages
Japanese (ja)
Inventor
Yoshihiro Tanigawa
谷川 吉弘
Shigeru Uryu
瓜生 滋
Takashi Nakano
敬 中野
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Priority to JP62058150A priority Critical patent/JPS63224799A/en
Publication of JPS63224799A publication Critical patent/JPS63224799A/en
Pending legal-status Critical Current

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  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To improve the efficiency of dehydration operation of sludge or the like, by transporting sludge or the like under pressure through a pipeline with a pump, compressing the sludge or the like to the inside of a cylindrical screen connected to an exit of the pipeline, separating water from solid matters with the screen, and heating the transported sludge or the like in the pipeline during this stage. CONSTITUTION:Sludge or the like is transported under pressure through a pipeline with a pump 1, compressed to the inside of a cylindrical screen 3 connected to an exit of the pipeline 2, and water is separated from solid matters with the screen3. In this stage, the compressed sludge or the like in the pipeline 2 is heated with a heating apparatus 4 covered with a heating pipe 4'. As the result, the water in the highly hydrous sludge or the like is separated from solid matters continuously, thus the operation efficiency is elevated. Simultaneously, no expensive coagulant is required and degree of heating is reduced. Consequently, the dehydration efficiency is improved.

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.

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

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)

【特許請求の範囲】[Claims] (1)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.
(2)空気注入圧送汚泥を加熱することを特徴とする特
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.
JP62058150A 1987-03-13 1987-03-13 Dehydration of sludge or the like Pending JPS63224799A (en)

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)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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

Patent Citations (6)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
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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