JPH11314073A - Process of turning incineration ash harmless - Google Patents
Process of turning incineration ash harmlessInfo
- Publication number
- JPH11314073A JPH11314073A JP12303898A JP12303898A JPH11314073A JP H11314073 A JPH11314073 A JP H11314073A JP 12303898 A JP12303898 A JP 12303898A JP 12303898 A JP12303898 A JP 12303898A JP H11314073 A JPH11314073 A JP H11314073A
- Authority
- JP
- Japan
- Prior art keywords
- incineration ash
- heating
- ash
- incinerated ash
- incineration
- 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
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/82—Recycling of waste of electrical or electronic equipment [WEEE]
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、バグフィルターや
電気集塵器等の集塵装置から排出される飛灰や、燃えが
ら等の焼却灰の無害化方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for detoxifying fly ash and incinerated ash such as cinders discharged from dust collectors such as bag filters and electric precipitators.
【0002】[0002]
【従来の技術】従来より、飛灰や燃えがら等の焼却灰中
に含まれるダイオキシン等の有害な有機化合物を無害化
する方法として、加熱処理が行われている。これは焼却
灰を300℃以上に加熱することによって、焼却灰中の
ダイオキシン等の有害な有機化合物を分解させる方法で
ある。この方法では、一般に、焼却灰の加熱は赤外線を
用いた外部加熱によって行われている。そのため焼却灰
以外、特に装置や外周雰囲気に熱が奪われ、焼却灰を全
体に均一に加熱するためには焼却灰の加熱処理時間を充
分に取る必要があり、熱量を焼却灰に十分に与える必要
があり、これらが処理コスト高を招いている。2. Description of the Related Art Conventionally, heat treatment has been performed as a method of detoxifying harmful organic compounds such as dioxin contained in incinerated ash such as fly ash and cinder. This is a method in which harmful organic compounds such as dioxin in the incinerated ash are decomposed by heating the incinerated ash to 300 ° C. or more. In this method, the incineration ash is generally heated by external heating using infrared rays. Therefore, in addition to incineration ash, heat is taken away by the equipment and the surrounding atmosphere, and it is necessary to take sufficient time for heat treatment of the incineration ash in order to uniformly heat the incineration ash, and to give sufficient heat to the incineration ash And these have caused high processing costs.
【0003】[0003]
【発明が解決しようとする課題】本発明は、上記の点に
鑑み、焼却灰の加熱処理時間を短縮し処理コストを低減
することができる焼却灰無害化方法を提供することを目
的とする。SUMMARY OF THE INVENTION In view of the above, an object of the present invention is to provide a method for detoxifying incinerated ash which can reduce the time required for heat treatment of incinerated ash and reduce the cost of processing.
【0004】[0004]
【課題を解決するための手段】本発明による焼却灰無害
化方法は、焼却灰の加熱にマイクロ波、好ましくはマイ
クロ波と赤外線を用いることを特徴とする方法である。The method for detoxifying incinerated ash according to the present invention is a method characterized by using microwaves, preferably microwaves and infrared rays, for heating incinerated ash.
【0005】焼却灰を加熱する前に焼却灰に活性炭を混
入しておくことが好ましい。[0005] Before heating the incinerated ash, it is preferable to mix activated carbon into the incinerated ash.
【0006】焼却灰中の活性炭(混入前の焼却灰に含ま
れている未燃カーボンも含む)の混入率は好ましくは5
〜20重量%である。The mixing ratio of activated carbon (including unburned carbon contained in the incinerated ash before mixing) in the incinerated ash is preferably 5
-20% by weight.
【0007】焼却灰の加熱を酸素欠乏雰囲気下で行うこ
とも可能である。[0007] It is also possible to heat the incinerated ash in an oxygen-deficient atmosphere.
【0008】焼却灰の加熱条件は温度250〜600℃
で時間1分〜24時間であることが好ましい。The heating condition of the incinerated ash is a temperature of 250 to 600 ° C.
And the time is preferably 1 minute to 24 hours.
【0009】マイクロ波は焼却灰の内部加熱を行うもの
であり、赤外線による焼却灰の外部加熱と比較して、焼
却灰以外、特に装置や外周雰囲気に熱は奪われにくい。
そのため焼却灰全体を均一に加熱するための滞留時間お
よび熱供給量は、赤外線による外部加熱よりもマイクロ
波による内部加熱を用いる方が少なくて済み、加熱処理
時間の短縮および処理コストの低減が達成できる。The microwave heats the incineration ash internally. Compared to the external heating of the incineration ash by infrared rays, the heat is less likely to be taken away by the apparatus and the peripheral atmosphere other than the incineration ash.
For this reason, the residence time and heat supply amount for uniformly heating the entire incineration ash are smaller when using internal heating by microwaves than by external heating by infrared rays, and the heat treatment time and processing cost are reduced. it can.
【0010】焼却灰中に活性炭を混入することによって
マイクロ波による焼却灰内部の温度上昇速度は大きくな
り、活性炭の混入率と温度上昇速度は比例関係にある
(表1参照)。焼却灰中の未燃カーボンが多く存在した
り、集塵機前流で活性炭を吹き込んでいる場合は、焼却
灰加熱装置前流での活性炭混入量は少なくて良い。[0010] By mixing activated carbon into the incineration ash, the rate of temperature rise inside the incineration ash by microwaves increases, and the mixing rate of the activated carbon and the temperature rising rate are in a proportional relationship (see Table 1). When a large amount of unburned carbon is present in the incineration ash, or when activated carbon is blown in the upstream of the dust collector, the amount of activated carbon mixed in the upstream of the incineration ash heating device may be small.
【0011】またこのマイクロ波によって内部加熱を行
うときに赤外線による外部加熱も用いると、焼却灰に対
して内部加熱と外部加熱が同時に行われ、これによって
焼却灰全体が所定温度に速やかに加熱され、加熱処理時
間を短縮することが可能である。[0011] Further, when external heating by infrared rays is also used when performing internal heating by the microwave, internal heating and external heating are simultaneously performed on the incinerated ash, whereby the entire incinerated ash is quickly heated to a predetermined temperature. In addition, the heat treatment time can be reduced.
【0012】[0012]
【発明の実施の形態】図1に焼却灰加熱装置の実施例を
示す。FIG. 1 shows an embodiment of an incineration ash heating apparatus.
【0013】排ガス処理装置のバグフィルター(1) から
飛灰が排出され、必要に応じてこの飛灰に燃えがらが加
えられる。次いで、この飛灰に活性炭が必要量だけ混入
される。活性炭を含む飛灰は、次に、マイクロ波発生器
(3) および赤外線発生器(4)を備えた焼却灰加熱装置(2)
に送られ、同装置内でマイクロ波によって内部加熱さ
れると共に赤外線発生器(4) によって外部加熱され、温
度が約600℃の赤熱状態に上昇したことを目視で観察
した後、処理済み飛灰が装置外に排出される。Fly ash is discharged from the bag filter (1) of the exhaust gas treatment device, and cinder is added to the fly ash as required. Next, the fly ash is mixed with a required amount of activated carbon. Fly ash containing activated carbon is then passed through a microwave generator
(3) and incineration ash heating device with infrared generator (4) (2)
Is heated internally by microwaves and externally heated by an infrared generator (4), and visually observed that the temperature has risen to a red-hot state of about 600 ° C. Is discharged out of the apparatus.
【0014】活性炭混入率と飛灰の600℃到達時間の
関係を表1に示す。Table 1 shows the relationship between the mixing ratio of activated carbon and the time required for fly ash to reach 600 ° C.
【0015】[0015]
【表1】 [Table 1]
【0016】[0016]
【発明の効果】マイクロ波加熱では、焼却灰全体を均
一に加熱するための滞留時間および熱供給量が少なくて
済み、加熱処理時間の短縮および処理コストの低減が達
成できる。According to the microwave heating, the residence time and the heat supply amount for uniformly heating the entire incineration ash can be reduced, and the heat treatment time and the treatment cost can be reduced.
【0017】焼却灰中に活性炭を混入することによっ
てマイクロ波による焼却灰内部の温度上昇速度は大きく
なり、上記の効果がさらに大きくなる。By mixing activated carbon into the incinerated ash, the temperature rise rate inside the incinerated ash by microwaves is increased, and the above effect is further enhanced.
【0018】マイクロ波加熱と赤外線加熱を併用する
ことによって、焼却灰に対して内部加熱と外部加熱が同
時に行われ、これによって焼却灰全体が所定温度に速や
かに加熱され、加熱処理時間を短縮することが可能であ
る。By using both microwave heating and infrared heating, internal heating and external heating are simultaneously performed on the incinerated ash, whereby the entire incinerated ash is quickly heated to a predetermined temperature, thereby shortening the heat treatment time. It is possible.
【図1】実施例を示すフローシートである。FIG. 1 is a flow sheet showing an example.
1:バグフィルター 2:焼却灰加熱装置 3:マイクロ波発生器 4:赤外線発生器 1: bag filter 2: incineration ash heating device 3: microwave generator 4: infrared generator
Claims (6)
を特徴とする焼却灰無害化方法。1. A method for detoxifying incinerated ash, which comprises using microwaves for heating the incinerated ash.
用することを特徴とする焼却灰無害化方法。2. A method for detoxifying incinerated ash, comprising using microwaves and infrared rays together to heat the incinerated ash.
混入しておくことを特徴とする焼却灰無害化方法。3. A method for detoxifying incinerated ash, wherein activated carbon is mixed into the incinerated ash before heating the incinerated ash.
量%とすることを特徴とする請求項3記載の焼却灰無害
化方法。4. The method for detoxifying incinerated ash according to claim 3, wherein the mixing ratio of activated carbon in the incinerated ash is 5 to 20% by weight.
ことを特徴とする請求項1〜4のいずれかに記載の焼却
灰無害化方法。5. The method for detoxifying incinerated ash according to claim 1, wherein the heating of the incinerated ash is performed in an oxygen-deficient atmosphere.
〜24時間行うことを特徴とする請求項1〜5のいずれ
かに記載の焼却灰無害化方法。6. The method for detoxifying incineration ash according to claim 1, wherein the heating of the incineration ash is performed at 250 to 600 ° C. for 1 minute to 24 hours.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12303898A JPH11314073A (en) | 1998-05-06 | 1998-05-06 | Process of turning incineration ash harmless |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP12303898A JPH11314073A (en) | 1998-05-06 | 1998-05-06 | Process of turning incineration ash harmless |
Publications (1)
Publication Number | Publication Date |
---|---|
JPH11314073A true JPH11314073A (en) | 1999-11-16 |
Family
ID=14850678
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP12303898A Pending JPH11314073A (en) | 1998-05-06 | 1998-05-06 | Process of turning incineration ash harmless |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPH11314073A (en) |
Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003047945A (en) * | 2001-08-03 | 2003-02-18 | Miyoshi Oil & Fat Co Ltd | Solid waste treatment method |
JP2003103242A (en) * | 2001-09-28 | 2003-04-08 | Dowa Mining Co Ltd | Method for detoxifying polluted substance |
JP2015160787A (en) * | 2014-02-28 | 2015-09-07 | 太平洋セメント株式会社 | Method and apparatus for using incineration ash as raw material of cement |
CN104923556A (en) * | 2015-07-06 | 2015-09-23 | 北京石油化工学院 | Thermal desorption heating device for oily soil restoration |
CN108380640A (en) * | 2018-02-12 | 2018-08-10 | 江苏天楹环保能源成套设备有限公司 | A kind of method of vacuum microwave carbon thermal reduction processing flying dust |
-
1998
- 1998-05-06 JP JP12303898A patent/JPH11314073A/en active Pending
Cited By (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2003047945A (en) * | 2001-08-03 | 2003-02-18 | Miyoshi Oil & Fat Co Ltd | Solid waste treatment method |
JP2003103242A (en) * | 2001-09-28 | 2003-04-08 | Dowa Mining Co Ltd | Method for detoxifying polluted substance |
JP2015160787A (en) * | 2014-02-28 | 2015-09-07 | 太平洋セメント株式会社 | Method and apparatus for using incineration ash as raw material of cement |
CN104923556A (en) * | 2015-07-06 | 2015-09-23 | 北京石油化工学院 | Thermal desorption heating device for oily soil restoration |
CN104923556B (en) * | 2015-07-06 | 2017-04-05 | 北京石油化工学院 | For the thermal desorption firing equipment that oil-contaminated soil is repaired |
CN108380640A (en) * | 2018-02-12 | 2018-08-10 | 江苏天楹环保能源成套设备有限公司 | A kind of method of vacuum microwave carbon thermal reduction processing flying dust |
CN108380640B (en) * | 2018-02-12 | 2020-04-07 | 江苏天楹环保能源成套设备有限公司 | Method for treating fly ash by vacuum microwave carbothermic reduction |
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