JPS5989921A - Sludge feeding method in sludge incinerator system with drying machine - Google Patents

Sludge feeding method in sludge incinerator system with drying machine

Info

Publication number
JPS5989921A
JPS5989921A JP57196801A JP19680182A JPS5989921A JP S5989921 A JPS5989921 A JP S5989921A JP 57196801 A JP57196801 A JP 57196801A JP 19680182 A JP19680182 A JP 19680182A JP S5989921 A JPS5989921 A JP S5989921A
Authority
JP
Japan
Prior art keywords
sludge
moisture content
incinerator
dehydrated cake
self
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
JP57196801A
Other languages
Japanese (ja)
Other versions
JPH0124967B2 (en
Inventor
Haruto Tsuboi
坪井 晴人
Kenichiro Mizuno
健一郎 水野
Kiyoshi Uyama
清 宇山
Kiyoteru Segawa
瀬川 清照
Noburo Inokawa
猪川 修郎
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.)
JFE Engineering Corp
Original Assignee
NKK Corp
Nippon Kokan 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 NKK Corp, Nippon Kokan Ltd filed Critical NKK Corp
Priority to JP57196801A priority Critical patent/JPS5989921A/en
Publication of JPS5989921A publication Critical patent/JPS5989921A/en
Publication of JPH0124967B2 publication Critical patent/JPH0124967B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F23COMBUSTION APPARATUS; COMBUSTION PROCESSES
    • F23GCREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
    • F23G5/00Incineration of waste; Incinerator constructions; Details, accessories or control therefor
    • F23G5/02Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
    • F23G5/04Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment drying

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Gasification And Melting Of Waste (AREA)
  • Treatment Of Sludge (AREA)

Abstract

PURPOSE:To enable to feed sludge under the moisture content limitation for self- burning even though the moisture content of the dry sludge is made less than 60% by a method wherein a feeding line of a dehydratd cake is divided into two lines formed of a main line and a by-pass line. CONSTITUTION:When the low level heating value of solid content of a sludge dehydrated cake is, for instance, 4,070kcal/kg, and the sludge is incinerated with a system which possible to treat the sludge having a 80% moisture content under the 1,000kg/h incinerating operation, the 260kg/h dry sludge having 50% moisture content can be obtained with a main line which is fed with the dehydrated cake having 80% moisrure content by the rate of 650kg/h. On the other hand, the dehydrated cake having 80% moisture content is fed into a by-pass line without treating, then said dehydrated cake is mixed with the dry sludge at the front stage of a incinerator, after obtaining of the sludge having 67% moisture content at self-burning limitation, the sludge is fed into the incinerator, subsequently, incinerated. Thereby, even though the moisture content of the dry sludge is more than 60% at the outlet of a drying machine, the self-burning in the incinerator can be performed.

Description

【発明の詳細な説明】 本発明は、本出願人が先に特願昭56−4960号およ
び特願昭57−116867号をもって提案した乾燥機
付汚泥焼却炉システムにおける汚泥供給方法の改良に関
するものであって、その目的とするところは発熱量およ
び水分の異なる各種の汚泥に対し、乾燥装置を適切な運
転範囲で効率良く運転しかつ自燃可能な所定の水分で汚
泥を焼却炉に送ることを可能ならしめるものであシ、結
果として乾燥装置出口においてハンドリングの困難な水
分60〜80%の乾燥汚泥を排出する弊害を解消するこ
とにある。
DETAILED DESCRIPTION OF THE INVENTION The present invention relates to an improvement in a sludge supply method in a sludge incinerator system with a dryer, which was previously proposed by the applicant in Japanese Patent Application No. 56-4960 and Japanese Patent Application No. 57-116867. The purpose of this is to efficiently operate the drying equipment within an appropriate operating range for various types of sludge with different calorific values and moisture content, and to send the sludge to the incinerator with a predetermined moisture content that allows for self-combustion. As a result, the problem of discharging dried sludge with a water content of 60 to 80%, which is difficult to handle, at the outlet of the drying device can be eliminated.

第1図は本出願人が上述の提案において開示した乾燥機
付汚泥焼却炉システムの一例でアシ、前述の提案におい
ては第2図に示す如く汚泥脱水ケーキは総て乾燥機を通
し、次に送られる焼却炉において自燃可能な水分となる
まで乾燥したのち焼却炉へ送シ、そこで焼却処理される
ようになっていtc、、。
Figure 1 shows an example of a sludge incinerator system with a dryer that the present applicant disclosed in the above proposal. In the incinerator to which it is sent, it is dried until it has a moisture content that can self-combust, and then sent to the incinerator, where it is incinerated.

ところが、一般に水分60〜80%の汚泥は、汚泥の粘
性が高いため乾燥機出口において架橋などの発生がJ5
リバンドリング上種々の弊害があった。
However, in general, sludge with a water content of 60 to 80% has a high viscosity, so crosslinking etc. occur at the dryer outlet.
There were various problems with rebundling.

本発明者らは、その後の検1tK、l:!u汚泥の固形
分轟シの低位発熱量が高い汚泥の場合は、下の第1表に
示すように乾燥機出口における乾燥汚泥の水分が60%
以上あっても焼却炉で自燃可能であることを見出した。
The inventors performed subsequent tests 1tK,l:! Solid content of sludge If the sludge has a high lower calorific value, the water content of the dried sludge at the outlet of the dryer is 60% as shown in Table 1 below.
It was discovered that even with the above, it is possible to self-combust in an incinerator.

第1表 本発明は、上記の知見に基づいてなされたものであシ、
第6図に示すように汚泥脱水ケーキが乾燥機を経て乾燥
汚泥となる従来システムの本ラインのほかに、脱水ケー
キが乾燥機を経ないバイパスラインを設け、前記本ライ
ンからは水分を低くした乾燥汚泥を供給するとともに、
別に設けたバイパスラインから水分の高いままの脱水ケ
ーキを供給し、焼却炉の手前で両方のラインから送られ
た汚泥を混合して、この混合汚泥が上記第−表に示す自
燃限界水分以内になるようにして焼却炉へ送入すること
を特徴とする乾燥機付汚泥焼却炉システムにおける汚泥
供給方法である。
Table 1 The present invention has been made based on the above findings.
As shown in Figure 6, in addition to the main line of the conventional system in which the dehydrated sludge cake passes through a dryer and becomes dried sludge, a bypass line is installed in which the dehydrated cake does not pass through the dryer, and the water content is reduced from the main line. In addition to supplying dry sludge,
The dehydrated cake with a high moisture content is supplied from a separate bypass line, and the sludge sent from both lines is mixed before the incinerator, so that the mixed sludge has a moisture content within the self-flammability limit shown in the table above. This is a method for supplying sludge in a sludge incinerator system with a dryer, characterized in that the sludge is fed to the incinerator in the following manner.

次に、本発明の汚泥供給方法を詳細に説明すると、従来
法においては自燃限界水分が60%以上どなる低位発熱
量(固形分当り)の高い汚泥の場合は、乾燥機出口にお
ける乾燥汚泥の水分が60チとなり、ハンドリングとの
問題が生じるけれども、本発明においては脱水ケーキの
供給ラインを本ラインとバイパスラインの2系統に分け
ることにより、乾燥機出口における乾燥汚泥の水分をノ
・ンドリングとの弊害のない60%以下としても、焼却
炉前段において両者を混合することにより、上記第1表
に示す如き所定の自燃限界水分で焼却炉へ供給できるよ
うにしたものである。。
Next, to explain in detail the sludge supply method of the present invention, in the case of sludge with a high lower calorific value (per solid content), where the self-combustion limit water content is 60% or more, in the conventional method, the water content of the dried sludge at the dryer outlet is However, in the present invention, by dividing the dewatered cake supply line into two systems, the main line and the bypass line, the water content of the dried sludge at the dryer outlet can be separated from the non-dried cake. Even if the content is 60% or less, which is not harmful, by mixing the two in the front stage of the incinerator, it is possible to supply the incinerator with a predetermined self-combustion limit moisture content as shown in Table 1 above. .

本発明の汚泥供給方法の実施例を第5図如示す。An embodiment of the sludge supply method of the present invention is shown in FIG.

汚泥脱水ケーキの固形分の低位発熱量が4070Kad
/に9 で、その水分が80%である汚泥を、1000
に9/hで焼却処理するシステムにおいて処理する場合
に、本ラインには水分80%の脱水ケーキを650 K
g/h供給することにより、水分50%の乾燥汚泥26
0 K9/hを得、一方バイパスラインには上記水分8
0%の脱水ケーキをそのまま供給し、先の乾燥汚泥と焼
却炉前段で混合することによυ自燃限界水分の67チの
汚泥とした上で焼却炉へ送シ焼却処卯した1、この場合
乾燥機出口における従来方法の弊害は全く起らず、焼却
炉における焼却処理も完全に行われた。
The lower calorific value of the solid content of the sludge dewatering cake is 4070 Kad.
1000 ml of sludge with 80% water content.
When processing in a system that incinerates at a rate of 9/h, this line processes dehydrated cake with 80% moisture at 650
By supplying g/h, dry sludge with a moisture content of 50%26
0 K9/h was obtained, while the above moisture 8 was added to the bypass line.
The 0% dehydrated cake was supplied as it was and mixed with the previously dried sludge in the front stage of the incinerator to form sludge with a moisture limit of υ 67 cm, which was then sent to the incinerator and incinerated.1. There were no adverse effects of the conventional method at the outlet of the dryer, and the incineration process in the incinerator was completed.

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

第1図は乾燥機付汚泥焼却炉システムの工程図、第2図
は従来の汚泥供給方法の工程図、第6図は本発明の汚泥
供給方法の工程図、 代理人 弁理士 木 村 三 朗 四  同  佐々木 宗 治
Figure 1 is a process diagram of a sludge incinerator system with a dryer, Figure 2 is a process diagram of a conventional sludge supply method, and Figure 6 is a process diagram of a sludge supply method of the present invention. Agent: Mitsuro Kimura, Patent Attorney 4. Muneharu Sasaki

Claims (1)

【特許請求の範囲】[Claims] 乾燥装置と焼却炉とを組合せた汚泥焼却システムにおい
て、焼却炉へ供給すべき汚泥脱水ケーキの供給ラインを
前記乾燥装置を通る本ラインと乾燥装置を通らないパイ
パスラインの2系統とし、本ラインから水分を低くした
乾燥汚泥を供給するとともK、バイパスラインから水分
の高いままの脱水ケーキを供給し、焼却炉前段において
両者を混合することによシ所定の水分とすることを特徴
とする乾燥機付汚泥焼却炉システムにおける汚泥供給方
法。
In a sludge incineration system that combines a drying device and an incinerator, there are two supply lines for the sludge dehydrated cake to be supplied to the incinerator: a main line that passes through the drying device and a bypass line that does not pass through the drying device. A dryer characterized by supplying dried sludge with a low moisture content and supplying a dehydrated cake with a high moisture content from a bypass line, and adjusting the moisture content to a predetermined level by mixing both in the front stage of an incinerator. Sludge supply method in a sludge incinerator system.
JP57196801A 1982-11-11 1982-11-11 Sludge feeding method in sludge incinerator system with drying machine Granted JPS5989921A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP57196801A JPS5989921A (en) 1982-11-11 1982-11-11 Sludge feeding method in sludge incinerator system with drying machine

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP57196801A JPS5989921A (en) 1982-11-11 1982-11-11 Sludge feeding method in sludge incinerator system with drying machine

Publications (2)

Publication Number Publication Date
JPS5989921A true JPS5989921A (en) 1984-05-24
JPH0124967B2 JPH0124967B2 (en) 1989-05-15

Family

ID=16363870

Family Applications (1)

Application Number Title Priority Date Filing Date
JP57196801A Granted JPS5989921A (en) 1982-11-11 1982-11-11 Sludge feeding method in sludge incinerator system with drying machine

Country Status (1)

Country Link
JP (1) JPS5989921A (en)

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6146813A (en) * 1984-08-10 1986-03-07 Yoshinobu Matsumoto Temperature controlling method in fluidized bed incinerator facility
JPS6434500A (en) * 1987-07-30 1989-02-03 Ngk Insulators Ltd Method of controlling drying of wet substance
JPH02282612A (en) * 1989-04-21 1990-11-20 Nkk Corp Disposal method for exhaust gas of circular melting furnace
EP0627597A1 (en) * 1993-06-03 1994-12-07 Oschatz Gmbh Method for the combustion of waste products resulting from the production of paper
JP2009204282A (en) * 2008-02-29 2009-09-10 Mhi Environment Engineering Co Ltd Sludge treatment method and sludge treatment system with circulating fluidized bed furnace
JP2009248039A (en) * 2008-04-09 2009-10-29 Mhi Environment Engineering Co Ltd Sludge supplying method and sludge treating system
JP2012102941A (en) * 2010-11-10 2012-05-31 Mitsubishi Heavy Industries Environmental & Chemical Engineering Co Ltd Sludge fluidized bed incineration plant, and method for incinerating sludge
JP2018200150A (en) * 2017-05-29 2018-12-20 国立研究開発法人産業技術総合研究所 Combustion furnace for organic waste and processing system for organic waste using the combustion furnace

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP5425512B2 (en) * 2009-04-15 2014-02-26 株式会社神鋼環境ソリューション Waste treatment system

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49134177A (en) * 1972-10-26 1974-12-24
JPS50136969A (en) * 1974-04-18 1975-10-30
JPS56151812A (en) * 1980-04-24 1981-11-25 Hitachi Zosen Corp Sludge incinerating apparatus
JPS57108579A (en) * 1980-12-25 1982-07-06 Mitsubishi Paper Mills Ltd Preheating for kiln

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS49134177A (en) * 1972-10-26 1974-12-24
JPS50136969A (en) * 1974-04-18 1975-10-30
JPS56151812A (en) * 1980-04-24 1981-11-25 Hitachi Zosen Corp Sludge incinerating apparatus
JPS57108579A (en) * 1980-12-25 1982-07-06 Mitsubishi Paper Mills Ltd Preheating for kiln

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS6146813A (en) * 1984-08-10 1986-03-07 Yoshinobu Matsumoto Temperature controlling method in fluidized bed incinerator facility
JPS6434500A (en) * 1987-07-30 1989-02-03 Ngk Insulators Ltd Method of controlling drying of wet substance
JPH02282612A (en) * 1989-04-21 1990-11-20 Nkk Corp Disposal method for exhaust gas of circular melting furnace
EP0627597A1 (en) * 1993-06-03 1994-12-07 Oschatz Gmbh Method for the combustion of waste products resulting from the production of paper
JP2009204282A (en) * 2008-02-29 2009-09-10 Mhi Environment Engineering Co Ltd Sludge treatment method and sludge treatment system with circulating fluidized bed furnace
JP2009248039A (en) * 2008-04-09 2009-10-29 Mhi Environment Engineering Co Ltd Sludge supplying method and sludge treating system
JP2012102941A (en) * 2010-11-10 2012-05-31 Mitsubishi Heavy Industries Environmental & Chemical Engineering Co Ltd Sludge fluidized bed incineration plant, and method for incinerating sludge
JP2018200150A (en) * 2017-05-29 2018-12-20 国立研究開発法人産業技術総合研究所 Combustion furnace for organic waste and processing system for organic waste using the combustion furnace

Also Published As

Publication number Publication date
JPH0124967B2 (en) 1989-05-15

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