JPS60187398A - Thermal treatment of sludge - Google Patents

Thermal treatment of sludge

Info

Publication number
JPS60187398A
JPS60187398A JP4217384A JP4217384A JPS60187398A JP S60187398 A JPS60187398 A JP S60187398A JP 4217384 A JP4217384 A JP 4217384A JP 4217384 A JP4217384 A JP 4217384A JP S60187398 A JPS60187398 A JP S60187398A
Authority
JP
Japan
Prior art keywords
sludge
oil
reactor
scrubber
supplied
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
JP4217384A
Other languages
Japanese (ja)
Other versions
JPH0118799B2 (en
Inventor
Hideharu Oshima
秀晴 大島
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.)
Kubota Corp
Original Assignee
Kubota Corp
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 Kubota Corp filed Critical Kubota Corp
Priority to JP4217384A priority Critical patent/JPS60187398A/en
Publication of JPS60187398A publication Critical patent/JPS60187398A/en
Publication of JPH0118799B2 publication Critical patent/JPH0118799B2/ja
Granted legal-status Critical Current

Links

Abstract

PURPOSE:To utilize effectively the recovered oil and to save the fuel by blowing steam and compressed air into a reactor wherein preheated sludge is supplied to treat thermally the sludge, and dehumidifying and cooling the gas discharged from the reactor in a scrubber. CONSTITUTION:The sludge 2 which is hard to dehydrate is stored in a sludge storage vessel 1, then supplied to a heat exchanger 4 with a pump 3, preheated to about 120 deg.C therein, and supplied into the lower part of a reaction vessel 5. The sludge is heated to about 165 deg.C in the reaction vessel 5 by the steam 7 from a waste heat boiler 6 which is blown in from the lower part, pressurized by the compressed reaction air 8 at about 10kg/cm<2> pressure which is blown in from the lower part of the reactor 5, and thermally treated. The gas 11 discharged from the reactor 5 is introduced into a scrubber 10, dehumidified and cooled by the water 12, and then introduced into a deodorizing tower. The water 14 discharged from the bottom of the scrubber 10 is introduced into an oil recovery apparatus 15, and the contained oil component is removed.

Description

【発明の詳細な説明】 本発明は下水や廃水の処理によって発生した汚泥の熱処
理方法の改良に関するものである。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a method for heat treatment of sludge generated by treatment of sewage and wastewater.

一般に下水や廃水の処理によって発生した難脱水性の汚
泥は、いったん汚泥貯溜槽に貯溜した後熱交換器に供給
して予熱して反応器に供給し、反応器内に吹込んだ蒸気
によって加温するとともに、反応器内に吹込んだ圧縮空
気によって加圧し、熱処理反応によって脱水性を改善す
るとともに汚泥中の悪臭成分も酸化分解するようにして
いるが、従来の汚泥の熱処理方法においては、反応器か
ら排出されるガスをスクラバーで除湿・冷却し、それを
直接水処理装置に導くようにしているため、スクラバー
の排水中に含まれている油分によって沈澱物が浮き上り
、浮上汚泥が増大してスカムが大量発生することがあり
、水処理に悪影響を及ぼすことがあるという欠点があっ
た。
In general, difficult-to-dewater sludge generated from the treatment of sewage and wastewater is stored in a sludge storage tank and then supplied to a heat exchanger for preheating before being supplied to a reactor where it is heated by steam blown into the reactor. At the same time, the sludge is heated and pressurized with compressed air blown into the reactor, and the heat treatment reaction improves dewatering performance and oxidizes and decomposes the malodorous components in the sludge.However, in conventional sludge heat treatment methods, Since the gas discharged from the reactor is dehumidified and cooled by a scrubber and then led directly to the water treatment equipment, the oil contained in the waste water from the scrubber causes the sediment to float, increasing the amount of floating sludge. This has the disadvantage that large quantities of scum may be generated during the process, which may have an adverse effect on water treatment.

本発明は、上記従来の欠点に鑑みなされたもので、予熱
された汚泥が供給される反応器内に蒸気と圧縮空気を吹
込んで熱処理を行ない、反応器から排出されるガスをス
クラバーで除湿、冷却すると共に、スクラバーの排水中
に含まれている油分を油回収装置により回収し、油分が
除去された排水を水処理装置に導くとともに、回収され
た油分を反応器内に吹込む蒸気を供給するボイラの燃料
系に導くように汚泥の熱処理方法を構成したことを特徴
としており、汚泥を熱処理する工程において、スクラバ
ーの排水中に含まれている油分を分離し、油分を除去し
た排水を水処理装置に導入することにより一排水中に油
分が含まれることなく水処理が良好になるとともに、回
収した油分の有効利用によって燃料の節約を図ろうとす
るものである、以下、本発明の実施例について図面を参
照して説明する。
The present invention was made in view of the above-mentioned conventional drawbacks, and involves blowing steam and compressed air into a reactor to which preheated sludge is supplied to perform heat treatment, and dehumidifying the gas discharged from the reactor with a scrubber. At the same time as cooling, the oil contained in the wastewater from the scrubber is recovered by an oil recovery device, the wastewater from which the oil has been removed is guided to a water treatment device, and steam is supplied to blow the recovered oil into the reactor. The sludge heat treatment method is structured so that the sludge is introduced into the fuel system of the boiler.In the sludge heat treatment process, the oil contained in the scrubber waste water is separated and the oil-free waste water is By introducing the present invention into a treatment device, water treatment is improved without oil being contained in wastewater, and fuel is saved by effectively utilizing the recovered oil.Examples of the present invention are as follows. will be explained with reference to the drawings.

第1図において、1は汚泥貯溜槽で、下水や廃水の処理
によって発生した難脱水性の汚泥2はいったん汚泥貯溜
槽1に貯溜された後、ポンプ3により熱交換器4に供給
され、ここで120゜℃程度に予熱された後反応器5の
下部に供給される。
In FIG. 1, 1 is a sludge storage tank, and sludge 2, which is difficult to dewater and is generated from the treatment of sewage and wastewater, is temporarily stored in the sludge storage tank 1 and then supplied to a heat exchanger 4 by a pump 3. After being preheated to about 120°C, it is supplied to the lower part of the reactor 5.

反応器5に供給された汚泥2は、反応器5の下部より吹
込んだ廃熱ボイラ6からの蒸気7によって165℃程度
まで加温されるとともに、反応器5の下部より吹込んだ
10 Kg/crA 程度の反応用の圧縮空気8によっ
て加圧され、熱処理されることになる。
The sludge 2 supplied to the reactor 5 is heated to about 165°C by the steam 7 from the waste heat boiler 6 that is blown in from the lower part of the reactor 5, and 10 kg of sludge that is blown in from the lower part of the reactor 5 is heated. It is pressurized with compressed air 8 for reaction of about /crA and heat-treated.

汚泥2は反応器5内の熱処理反応によって脱水性が改善
され、汚泥2中の悪臭成分も酸化分解されて反応器5よ
り、熱処理汚泥9として取出される。
The dehydration properties of the sludge 2 are improved by the heat treatment reaction in the reactor 5, and the malodorous components in the sludge 2 are also oxidized and decomposed, and the sludge is taken out from the reactor 5 as heat-treated sludge 9.

この熱処理汚泥9は、熱交換器に導かれて熱、回収され
、冷却器で常温まで冷却されて濃縮槽に導かれ、濃縮さ
れた後フィルタープレスにより脱水処理されるようにな
っているが、その処理工程については図示を省略してい
る。そして、反応器5から排出されたガス11はスフバ
ー10内に導かれ、上方より散布される水12により除
湿、冷却された後、脱臭塔13へ導かれるようになって
おり、スクラバー10の底部より排出された排水14は
油回収装置15に導かれて排水14中に含まれている油
分が除却され、油分が除去された排水16は水処理装置
17へ導かれるようになっている。
This heat-treated sludge 9 is led to a heat exchanger, where the heat is recovered, cooled to room temperature by a cooler, led to a thickening tank, and after being concentrated, it is dehydrated by a filter press. The illustration of the processing steps is omitted. The gas 11 discharged from the reactor 5 is led into the scrubber 10, dehumidified and cooled by water 12 sprayed from above, and then led to the deodorizing tower 13. The waste water 14 discharged from the tank is led to an oil recovery device 15 to remove oil contained in the waste water 14, and the waste water 16 from which the oil has been removed is led to a water treatment device 17.

また、油回収装置15により回収された油分18はタン
クを介して反応器5内に吹込む蒸気7を供給する廃熱ボ
イラ6の燃料系に導かれるようになっている。
Further, the oil 18 recovered by the oil recovery device 15 is led through a tank to the fuel system of the waste heat boiler 6 that supplies steam 7 to be blown into the reactor 5.

第2図は第1図に示す汚泥の熱処理方法の工程に使用さ
れている油回収装置の1実施例を示したもので、油回収
装置15内にはスクラバー10の排水14を供給する側
に邪魔板20が互い違いに設置されており、油回収装置
15内に供給された排水14によって液面21が変動し
ないように配慮されている。この装#15内にはスプロ
ケット23.23間に張架されたチェーン22が設けら
れており、その周上には所定間隔をおいて掻@24が取
り付けられ、減速機付のモータ25を介してスプロット
23を駆動すると掻板24が液面21に浮遊している油
分18をテーパー状底面26に沿って掻上げ、油分18
をタンク19内に掻込んで油分18を回収するようにな
っている。
FIG. 2 shows an embodiment of an oil recovery device used in the process of the sludge heat treatment method shown in FIG. The baffle plates 20 are installed alternately to prevent the liquid level 21 from fluctuating due to the waste water 14 supplied into the oil recovery device 15. A chain 22 stretched between sprockets 23 and 23 is provided in this #15, and paddles 24 are attached at predetermined intervals on the circumference of the chain 22, and a chain 22 is connected through a motor 25 with a speed reducer. When the splot 23 is driven, the scraping plate 24 scrapes up the oil 18 floating on the liquid surface 21 along the tapered bottom surface 26 and removes the oil 18.
The oil component 18 is collected by scraping it into the tank 19.

この場合、掻1fi24の表面に付着した油分18は、
揺動板27によって掻落すようにしてもよい。なお、タ
ンク19内に掻込まれた油分18は図示しない配管を介
して廃熱ボイラ6の燃料系に導かれ、油分1Bを除却さ
れた排水16は図示しない配管を介して水処理装置17
へ導かれるようになっている。
In this case, the oil 18 attached to the surface of the scraper 1fi24 is
It may be scraped off by the swing plate 27. The oil 18 that has been pumped into the tank 19 is led to the fuel system of the waste heat boiler 6 via piping (not shown), and the waste water 16 from which the oil 1B has been removed is sent to the water treatment device 17 via piping (not shown).
It is designed to lead you to.

前記構成よりなる本発明の汚泥の熱処理方法においては
、熱交換器4により予熱された汚泥2は反応器5に供給
され、反応器5内に吹込ま′れた蒸気7と田縮臣気8に
より熱処理されることになる。
In the sludge heat treatment method of the present invention having the above-mentioned configuration, the sludge 2 preheated by the heat exchanger 4 is supplied to the reactor 5, and the steam 7 and the air 8 blown into the reactor 5 are It will be heat treated by

他方、反応器5から排出されるガス11を除湿、冷却す
るスクラバー10から排出される排水14中には、反応
器5内の熱処理反応によって濃縮された油分18が含ま
れているが、この排水14中に含まれている油分IBは
第2図に示す油回収装[15の掻板24によって掻上げ
られ、タンク19内に掻込まれて回収されることになる
。したがって、水処理装置17へは油分18が除去され
た排出16が導かれて油分による悪影響を与えることな
く水処理されることになり、効率よく回収された油分1
8はタンク19を介して廃熱ボイラ6等の燃料系に導か
れ、油分18は燃料として有効に利用されることになる
。なお、油回収装置15としては第2図に示すもの以外
に、遠心分離方法を利用したもの等があり、油分の性状
や回収量等を考慮して最適のものを選定すればよい。
On the other hand, the waste water 14 discharged from the scrubber 10 that dehumidifies and cools the gas 11 discharged from the reactor 5 contains oil 18 concentrated by the heat treatment reaction in the reactor 5. The oil IB contained in the oil is scraped up by the scraping plate 24 of the oil recovery device [15] shown in FIG. 2, and is scraped into the tank 19 and recovered. Therefore, the discharged water 16 from which the oil 18 has been removed is led to the water treatment device 17, where the water is treated without any adverse effects of the oil, and the oil 18 is efficiently recovered.
8 is led to a fuel system such as a waste heat boiler 6 via a tank 19, and the oil 18 is effectively used as fuel. In addition to the oil recovery device 15 shown in FIG. 2, there are other types of oil recovery device 15 that utilize a centrifugal separation method, and the most suitable one may be selected in consideration of the oil properties, recovery amount, etc.

また、本発明の汚泥の熱処理方法の有効性を確認するた
め、濃度2係程度の汚泥2を予熱して反応器5に12y
&/hづつ供給して熱処理したところ、反応器5から8
00 x/FF?/ hのガス11が排出され、このガ
ス11にスクラバー10で30d/bの水12を散布し
て除湿、冷却し、スクラバー10の排水14中に含まれ
ている油分を油回収装置15で回収したところ、1.1
/hの高濃度の油分18を回収することができ、廃熱ボ
イラ6の燃料系に導いて十分に実用し得ることが実証さ
れた。
In addition, in order to confirm the effectiveness of the sludge heat treatment method of the present invention, sludge 2 with a concentration of about 2 was preheated and placed in the reactor 5 for 12 y.
When heat treatment was carried out by supplying &/h at a time, reactors 5 to 8
00 x/FF? /h of gas 11 is discharged, this gas 11 is dehumidified and cooled by spraying 30 d/b of water 12 with a scrubber 10, and the oil contained in the waste water 14 of the scrubber 10 is recovered with an oil recovery device 15. As a result, 1.1
It was demonstrated that the oil 18 with a high concentration of 1/h could be recovered, and that it could be introduced into the fuel system of the waste heat boiler 6 for sufficient practical use.

本発明の汚泥の熱処理方法は上記のように構成されてい
るので、水処理装置に導かれるスクラバーの排水中には
油分は含まれず、従来のように油分によって沈澱物が浮
き上り、浮上汚泥が増大してスカムが多量発生する恐れ
はないから、効率よく水処理を行なうことができる。
Since the sludge heat treatment method of the present invention is configured as described above, oil is not contained in the waste water from the scrubber that is led to the water treatment equipment, and unlike conventional methods, the oil causes the sediment to float, resulting in floating sludge. Since there is no fear that a large amount of scum will increase, water treatment can be carried out efficiently.

また、本発明においては、回収された油分は反応器内に
吹込む蒸気を供給するボイラ等の燃料系に導かれている
ので、燃料を節約することができ、スクラバーの排水中
の油分の有効利用を図ることができる。さらに、スクラ
バーの排水中の油分は反応器内の熱処理反応によって比
較的濃縮されているため、油回収装置における油分の回
収も効率よく行なうことができる等多くの利点を有し、
既存設備への適用も容易で実用上きわめて有効な汚泥の
熱処理方法を提供し得るものである。
In addition, in the present invention, since the recovered oil is guided to the fuel system such as a boiler that supplies steam to be blown into the reactor, fuel can be saved, and the oil in the scrubber waste water can be effectively absorbed. You can plan to use it. Furthermore, since the oil content in the scrubber waste water is relatively concentrated by the heat treatment reaction in the reactor, it has many advantages such as being able to efficiently recover the oil content in the oil recovery equipment.
It is possible to provide a method for heat treatment of sludge that is easy to apply to existing equipment and is extremely effective in practice.

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

第1図は本発明の1実施例を示す汚泥の熱処理方法の工
程図、第2図は油回収装置の1実施例を示す断面図であ
る。 1・・・・・・汚泥貯溜槽 2・・・・・・汚泥3・・
・・・・ポンプ 4・・・・・・熱交換器5・・・・・
・反応器 6・・・・・・廃熱ボイラ7・・・・・・蒸
気 8・・・・・・圧縮突気9・・・・・・熱処理汚泥
 10・・・スクラバー11・・・ガス 12・・・水 13・・・脱臭塔 14・・・排水 15・・・油回収装置 16・・・油分が除去された排
水17・・・水処理装置 1B・・・油分19・・・タ
ンク 特許出願人 久保田鉄工株式会社
FIG. 1 is a process diagram of a sludge heat treatment method showing one embodiment of the present invention, and FIG. 2 is a sectional view showing one embodiment of an oil recovery apparatus. 1...Sludge storage tank 2...Sludge 3...
... Pump 4 ... Heat exchanger 5 ...
・Reactor 6... Waste heat boiler 7... Steam 8... Compressed air 9... Heat treated sludge 10... Scrubber 11... Gas 12... Water 13... Deodorizing tower 14... Drainage 15... Oil recovery device 16... Drainage from which oil was removed 17... Water treatment device 1B... Oil 19... Tank Patent applicant Kubota Iron Works Co., Ltd.

Claims (1)

【特許請求の範囲】[Claims] 予熱された汚泥が供給される反応器内に蒸気と圧縮空気
を吹込んで熱処理を行ない、反応器から排出されるガス
をスクラバーで除湿・冷却するとともに、スクラバーの
排出中に含まれている油分を油回収装置により回収し、
油分が除去された排水を水処理装置に導くとともに、回
収された油分を反応器内に吹込む蒸気を供給する廃熱ボ
イラ等の燃料系6に導くようにしたことを特徴とする汚
泥の熱処理方法。
Heat treatment is performed by blowing steam and compressed air into the reactor into which preheated sludge is supplied, and the gas discharged from the reactor is dehumidified and cooled by a scrubber, and the oil contained in the discharge from the scrubber is removed. Collected by oil recovery equipment,
A heat treatment for sludge, characterized in that wastewater from which oil has been removed is led to a water treatment device, and the recovered oil is led to a fuel system 6 such as a waste heat boiler that supplies steam to be blown into a reactor. Method.
JP4217384A 1984-03-07 1984-03-07 Thermal treatment of sludge Granted JPS60187398A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4217384A JPS60187398A (en) 1984-03-07 1984-03-07 Thermal treatment of sludge

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4217384A JPS60187398A (en) 1984-03-07 1984-03-07 Thermal treatment of sludge

Publications (2)

Publication Number Publication Date
JPS60187398A true JPS60187398A (en) 1985-09-24
JPH0118799B2 JPH0118799B2 (en) 1989-04-07

Family

ID=12628577

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4217384A Granted JPS60187398A (en) 1984-03-07 1984-03-07 Thermal treatment of sludge

Country Status (1)

Country Link
JP (1) JPS60187398A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016087578A (en) * 2014-11-07 2016-05-23 株式会社ピーシーエス Contaminant separation volume reduction system and method
CN106352333A (en) * 2015-07-17 2017-01-25 江苏中科睿赛污染控制工程有限公司 Steam heat treatment device, treatment method and use thereof

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2016087578A (en) * 2014-11-07 2016-05-23 株式会社ピーシーエス Contaminant separation volume reduction system and method
CN106352333A (en) * 2015-07-17 2017-01-25 江苏中科睿赛污染控制工程有限公司 Steam heat treatment device, treatment method and use thereof

Also Published As

Publication number Publication date
JPH0118799B2 (en) 1989-04-07

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