JP2003190910A - Incinerated ash treatment method and apparatus therefor - Google Patents
Incinerated ash treatment method and apparatus thereforInfo
- Publication number
- JP2003190910A JP2003190910A JP2001395581A JP2001395581A JP2003190910A JP 2003190910 A JP2003190910 A JP 2003190910A JP 2001395581 A JP2001395581 A JP 2001395581A JP 2001395581 A JP2001395581 A JP 2001395581A JP 2003190910 A JP2003190910 A JP 2003190910A
- Authority
- JP
- Japan
- Prior art keywords
- furnace
- oxygen concentration
- incinerated ash
- firing
- ash
- 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
Abstract
Description
【0001】[0001]
【発明の属する技術分野】本発明は、廃棄物の焼却灰を
建設・土木資材として利用すること等を目的として、焼
却灰を熱処理する方法及びその装置に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method and an apparatus for heat treating incinerated ash for the purpose of using the incinerated ash of waste as a construction / civil engineering material.
【0002】[0002]
【従来の技術】焼却灰を建設・土木資材として利用する
には、環境面から、焼却灰に含まれる所定の金属(主に
重金属)の溶出を抑制する必要があり、その基準として
は、一般に、「土壌の汚染に係る環境基準」(平成3.
8.23、環告46)が用いられている。2. Description of the Related Art In order to use incineration ash as a construction / civil engineering material, it is necessary to suppress elution of a predetermined metal (mainly a heavy metal) contained in the incineration ash from an environmental viewpoint. , “Environmental standards for soil pollution” (1991.
8.23, Announcement 46) is used.
【0003】焼却灰を熱処理して重金属の溶出を抑制す
る方法としては、従来より、焼却灰を1300℃程度以
上の高温で溶融し、スラグ化する方法が知られている。As a method of heat treating the incinerated ash to suppress the elution of heavy metals, a method of melting the incinerated ash at a high temperature of about 1300 ° C. or higher to form a slag has been known.
【0004】[0004]
【発明が解決しようとする課題】しかしながら、焼却灰
を高温で溶融するには、多大なエネルギーコストを要す
るととともに、その高温に耐えうる装置の製作コストも
多大となる。However, in order to melt the incineration ash at a high temperature, a great energy cost is required, and the manufacturing cost of the device capable of withstanding the high temperature is also high.
【0005】本発明は、上述する事情に鑑みてなされた
ものであり、比較的低温での熱処理によって重金属の溶
出を抑制でき、エネルギーコストや装置コストの低減化
が図られる焼却灰の処理方法及び処理装置を提供するこ
とを目的とする。The present invention has been made in view of the above-mentioned circumstances, and is a method for treating incinerated ash, which can suppress the elution of heavy metals by heat treatment at a relatively low temperature and can reduce energy costs and equipment costs. An object is to provide a processing device.
【0006】[0006]
【課題を解決するための手段】上記した本発明の目的
は、炉内で焼却灰を焼成するとともに、焼成温度に応じ
て前記炉内の酸素濃度を制御することを特徴とする焼却
灰の処理方法により達成される。DISCLOSURE OF THE INVENTION The above-mentioned object of the present invention is to treat incinerated ash by firing the incinerated ash in a furnace and controlling the oxygen concentration in the oven according to the firing temperature. Achieved by the method.
【0007】この場合において、例えば、焼成温度が8
00〜900℃のとき、前記炉内の酸素濃度を0%を超
えて10%未満に制御するのが好ましい。In this case, for example, the firing temperature is 8
When the temperature is from 00 to 900 ° C., it is preferable to control the oxygen concentration in the furnace to more than 0% and less than 10%.
【0008】上記焼却灰の処理方法は、焼却灰を焼成す
る炉と、前記炉内の酸素濃度を制御する酸素濃度制御装
置とを備えることを特徴とする焼却灰の処理装置により
実施できる。The above method for treating incinerated ash can be carried out by an incinerator ash treatment apparatus comprising a furnace for firing the incinerated ash and an oxygen concentration control device for controlling the oxygen concentration in the furnace.
【0009】この場合において、前記酸素濃度制御装置
は、前記炉内の酸素濃度を計測する酸素濃度計と、該酸
素濃度計の計測結果に基づいて前記炉内に所定のガスを
供給するガス供給装置とを含むとよい。In this case, the oxygen concentration control device comprises an oxygen concentration meter for measuring the oxygen concentration in the furnace, and a gas supply for supplying a predetermined gas into the furnace based on the measurement result of the oxygen concentration meter. And a device.
【0010】[0010]
【発明の実施の形態】以下、本発明について説明する。
本発明者らは、焼却灰を必ずしも溶融しなくても焼成す
ることで重金属の溶出が十分に抑制されること、焼成温
度と重金属の溶出量との関係は各重金属によって異なる
傾向にあること、溶出量は焼成時の酸素濃度に依存しや
すいことを解明し、炉内で焼却灰を焼成するとともに、
その焼成温度に応じて前記炉内の酸素濃度を制御するこ
とにより本発明を完成した。BEST MODE FOR CARRYING OUT THE INVENTION The present invention will be described below.
The present inventors that the elution of heavy metals is sufficiently suppressed by firing even if the incineration ash is not necessarily melted, the relationship between the firing temperature and the elution amount of heavy metals tends to be different for each heavy metal, It was clarified that the amount of elution easily depends on the oxygen concentration during firing, and the incinerator ash is fired in the furnace.
The present invention was completed by controlling the oxygen concentration in the furnace according to the firing temperature.
【0011】すなわち、本発明の焼却灰の処理方法にお
いては、従来行われていた溶融処理よりも低い温度で焼
却灰を焼成することにより、重金属の溶出の抑制を図
る。また、焼成温度と重金属の溶出量との関係は各重金
属によって異なる傾向にあり、焼成温度の制御だけで複
数の重金属の溶出をまとめて抑制するのには不確実性が
伴うことから、焼成温度に応じて炉内の酸素濃度を制御
することにより、焼成時の各重金属に対する溶出抑制効
果を高める。これにより、各重金属の溶出が確実に抑制
される。That is, in the method for treating incinerated ash according to the present invention, the elution of heavy metals is suppressed by firing the incinerated ash at a temperature lower than that of the conventional melting treatment. Further, the relationship between the firing temperature and the elution amount of heavy metals tends to differ depending on each heavy metal, and there is uncertainty in collectively suppressing the elution of multiple heavy metals only by controlling the firing temperature. By controlling the oxygen concentration in the furnace according to the above, the effect of suppressing elution of each heavy metal during firing is enhanced. This surely suppresses the elution of each heavy metal.
【0012】前記本発明の焼却灰の処理方法において、
焼成温度(加熱温度、炉内温度)は、例えば600〜1
100℃とするのが好ましい。焼成温度が600℃未満
では重金属の溶出が十分に抑制されないので好ましくな
く、焼成温度が1100℃を超えるとエネルギーコスト
が大幅に上昇するので好ましくない。In the method for treating incinerated ash according to the present invention,
The firing temperature (heating temperature, furnace temperature) is, for example, 600 to 1.
The temperature is preferably 100 ° C. When the firing temperature is lower than 600 ° C, the elution of heavy metals is not sufficiently suppressed, which is not preferable, and when the firing temperature exceeds 1100 ° C, the energy cost is significantly increased, which is not preferable.
【0013】また、前記処理方法において、焼成温度が
800〜900℃のとき、炉内の酸素濃度を0%を超え
て10%未満に制御するのが好ましい。炉内の酸素濃度
が0%では鉛(Pb)の溶出量が大きく増加するので好
ましくなく、10%以上では六価クロム(Cr+6)の溶
出量が大きく増加するので好ましくない。Further, in the above treatment method, when the firing temperature is 800 to 900 ° C., it is preferable to control the oxygen concentration in the furnace to more than 0% and less than 10%. When the oxygen concentration in the furnace is 0%, the amount of lead (Pb) elution is greatly increased, and when it is 10% or more, the amount of hexavalent chromium (Cr + 6) is greatly increased, which is not preferable.
【0014】次に、前記本発明の焼却灰の処理方法を実
施可能な処理装置について説明する。図1は、本発明に
係る焼却灰の処理装置の実施の形態の一例を概念的に示
す図である。この処理装置10は、焼成炉11を備え、
焼成炉11に投入された焼却灰を焼成処理する。すなわ
ち、焼成炉11は、焼却灰を加熱するための加熱手段1
2、及び焼成炉11内の温度を計測する温度計13等を
有し、焼却灰を所定の温度で加熱することにより、焼却
灰に化学反応を起こさせ硬化させる。加熱手段12とし
ては、燃焼エネルギーを利用したもの、電気エネルギー
を利用したもの等の公知の様々なものが適用される。ま
た、温度計13の計測結果は制御装置14に送られ、制
御装置14はその計測結果に基づいて所定の焼成温度と
なるように加熱手段12を制御する。Next, a processing apparatus capable of carrying out the incineration ash processing method of the present invention will be described. FIG. 1 is a diagram conceptually showing an example of an embodiment of an incineration ash treatment apparatus according to the present invention. The processing apparatus 10 includes a firing furnace 11,
The incineration ash put into the firing furnace 11 is fired. That is, the firing furnace 11 includes the heating means 1 for heating the incineration ash.
2 and a thermometer 13 for measuring the temperature in the firing furnace 11 and the like, and by heating the incineration ash at a predetermined temperature, a chemical reaction is caused in the incinerator ash to cure it. As the heating means 12, various known ones such as one utilizing combustion energy and one utilizing electric energy are applied. Further, the measurement result of the thermometer 13 is sent to the control device 14, and the control device 14 controls the heating means 12 based on the measurement result so as to reach a predetermined firing temperature.
【0015】また、この処理装置10は、焼成炉11内
の酸素濃度を制御する酸素濃度制御装置20を備え、酸
素濃度制御装置20は、焼成炉11内の酸素濃度を計測
する酸素濃度計21、焼成炉11内に所定のガスを供給
するガス供給系22、及び前記制御装置14等を備えて
いる。酸素濃度計21は、炉内のガス中の酸素濃度(不
足酸素濃度でもよい)を計測するものであり、公知の様
々なものが適用される。また、その計測結果は制御装置
14に送られる。ガス供給系22は、炉内に窒素やヘリ
ウムなどの不活性ガス(あるいは還元性ガス)を供給し
て炉内の酸素濃度を低下させるものであり、前記ガス
(あるいは液化ガス)を貯溜するタンクや供給配管、あ
るいは流量制御弁等を含み、その供給量は制御装置14
により制御される。なお、酸素濃度制御装置20として
は、焼成炉11内の酸素濃度を制御できればよく、上記
構成に限定されない。例えば、焼成炉11内からの排出
ガスの流量を制御することにより、炉内の酸素濃度を制
御する構成としてもよい。The processing apparatus 10 also includes an oxygen concentration control device 20 for controlling the oxygen concentration in the firing furnace 11, and the oxygen concentration control device 20 measures the oxygen concentration in the firing furnace 11 with an oxygen concentration meter 21. The firing furnace 11 is provided with a gas supply system 22 for supplying a predetermined gas, the control device 14 and the like. The oxygen concentration meter 21 measures the oxygen concentration in the gas in the furnace (the oxygen concentration may be insufficient), and various known ones are applied. Further, the measurement result is sent to the control device 14. The gas supply system 22 supplies an inert gas (or reducing gas) such as nitrogen or helium into the furnace to reduce the oxygen concentration in the furnace, and is a tank for storing the gas (or liquefied gas). And a supply pipe, or a flow control valve, etc.
Controlled by. The oxygen concentration control device 20 is not limited to the above configuration as long as it can control the oxygen concentration in the firing furnace 11. For example, the oxygen concentration in the furnace may be controlled by controlling the flow rate of the exhaust gas from the baking furnace 11.
【0016】上記構成の処理装置10においては、焼成
炉11内に焼却灰が投入されると、焼却灰を所定の温
度、例えば600〜1100℃の範囲内の温度で焼成す
る。また、焼成時、酸素濃度制御装置20を介して、焼
成炉11内の酸素濃度を所定の範囲内に制御する。例え
ば、焼成温度が800〜900℃のとき、焼成炉11内
の酸素濃度を0%を超えて10%未満に制御する。これ
により、この処理装置10では、重金属の溶出が抑制さ
れた焼却灰の焼成物が生成される。所定の焼成時間が経
過すると、焼成炉11内から焼却灰の焼成物が取り出さ
れ、その焼成物は建設・土木資材(骨材など)として利
用される。In the processing apparatus 10 having the above-mentioned structure, when the incineration ash is put into the firing furnace 11, the incineration ash is fired at a predetermined temperature, for example, a temperature in the range of 600 to 1100 ° C. Further, during firing, the oxygen concentration in the firing furnace 11 is controlled within a predetermined range via the oxygen concentration control device 20. For example, when the firing temperature is 800 to 900 ° C., the oxygen concentration in the firing furnace 11 is controlled to be higher than 0% and lower than 10%. As a result, in this processing apparatus 10, a burned material of incinerated ash in which elution of heavy metals is suppressed is generated. After a lapse of a predetermined calcination time, a calcinated product of incinerated ash is taken out from the calcination furnace 11, and the calcinated product is used as a construction / civil engineering material (aggregate, etc.).
【0017】[0017]
【実施例】ストーカー炉(石川島播磨重工業株式会社
製)で廃棄物を焼却処理し、その焼却灰(主灰)をマッ
フル炉内で焼成処理した。焼成後の処理物を空気雰囲気
中で放置・冷却した後、その処理物に対して溶出試験を
行った。焼成温度(加熱温度)は900℃、焼成時間
(加熱時間)は60分とした。炉内の酸素濃度は窒素ベ
ースでそれぞれ0%、3%、5%、7%、10%、21
%、及び30%とした。溶出試験は、環告46(平成
3.8.23)に準拠して行い、銅(Cu)、亜鉛(Z
n)、六価クロム(Cr+6)、砒素(As)、セレン
(Se)、カドミウム(Cd)、及び鉛(Pb)につい
て調べた。分析には、主にアイシーピーマスと発光アイ
シーピー(ICP−AES)を用いた。六価クロムの
み、比色法(JIS K1020)により分析を行っ
た。分析結果を図2に示す。[Example] The waste was incinerated in a stalker furnace (manufactured by Ishikawajima Harima Heavy Industries, Ltd.), and the incinerated ash (main ash) was incinerated in a muffle furnace. After the baked processed product was left to stand in an air atmosphere and cooled, an elution test was performed on the processed product. The firing temperature (heating temperature) was 900 ° C., and the firing time (heating time) was 60 minutes. Oxygen concentration in the furnace is 0%, 3%, 5%, 7%, 10%, 21% based on nitrogen, respectively.
% And 30%. The dissolution test is performed in accordance with Notification 46 (Heisei 3.8.23), and copper (Cu), zinc (Z
n), hexavalent chromium (Cr + 6), arsenic (As), selenium (Se), cadmium (Cd), and lead (Pb) were investigated. For the analysis, mainly ICP mass and luminescent ICP (ICP-AES) were used. Only hexavalent chromium was analyzed by a colorimetric method (JIS K1020). The analysis results are shown in FIG.
【0018】図2において、砒素(As)、セレン(S
e)、及びカドミウム(Cd)はそれぞれ、いずれの酸
素濃度においても基準(0.01mg/l以下)を満足
した。六価クロム(Cr+6)は、酸素濃度がそれぞれ0
%、3%、5%、及び7%のとき、基準(0.05mg
/l以下)を満足し、酸素濃度がそれぞれ10%、21
%、及び30%のとき、基準を上回った。鉛(Zn)
は、酸素濃度が0%のとき基準(0.01mg/l)を
上回り、それ以外の酸素濃度では基準を満足した。この
結果から、焼成温度が900℃、焼成時間が60分のと
き、炉内の酸素濃度は0%を超えて10%未満であるの
が好ましいことが分かった。In FIG. 2, arsenic (As), selenium (S)
e) and cadmium (Cd) each satisfied the standard (0.01 mg / l or less) at any oxygen concentration. Hexavalent chromium (Cr + 6) has an oxygen concentration of 0
%, 3%, 5%, and 7%, the standard (0.05 mg
/ L or less), the oxygen concentrations are 10% and 21 respectively.
% And 30% exceeded the standard. Lead (Zn)
Exceeded the standard (0.01 mg / l) when the oxygen concentration was 0%, and satisfied the standard at other oxygen concentrations. From this result, it was found that the oxygen concentration in the furnace is preferably more than 0% and less than 10% when the firing temperature is 900 ° C. and the firing time is 60 minutes.
【0019】このように、焼却灰を焼成するとともに、
焼成温度に応じて炉内の酸素濃度を制御することによ
り、焼成温度条件に対して異なる傾向を示す複数の重金
属を含む場合にも、焼成による溶出抑制効果を高め、そ
れら複数の重金属の溶出をまとめて抑制できることが確
認された。In this way, while burning the incinerated ash,
By controlling the oxygen concentration in the furnace according to the firing temperature, even when multiple heavy metals that show different tendencies with respect to firing temperature conditions are included, the effect of suppressing elution by firing is enhanced, and the elution of these multiple heavy metals is improved. It was confirmed that they can be suppressed collectively.
【0020】以上、添付図面を参照しながら本発明に係
る好適な実施形態について説明したが、本発明は係る例
に限定されないことは言うまでもない。上述した例にお
いて示した各構成部材の諸形状や組み合わせ等は一例で
あって、本発明の主旨から逸脱しない範囲において設計
要求等に基づき種々変更可能である。The preferred embodiments of the present invention have been described above with reference to the accompanying drawings, but it goes without saying that the present invention is not limited to such examples. The shapes, combinations, and the like of the constituent members shown in the above-described examples are merely examples, and various changes can be made based on design requirements and the like without departing from the spirit of the present invention.
【0021】[0021]
【発明の効果】本発明の焼却灰の処理方法及び処理装置
によれば、炉内で焼却灰を焼成するとともに、焼成温度
に応じて炉内の酸素濃度を制御することにより、従来の
溶融処理に比べて加熱温度を低くしても、焼却灰からの
複数の重金属の溶出をまとめて抑制できる。したがっ
て、従来の溶融処理に比べて、エネルギーコストや装置
コストの低減化が図られる。また、この処理方法及び処
理装置で焼成した焼却灰は、重金属の溶出が抑制されて
いることから、建設・土木資材として好ましく利用する
ことができる。According to the method and apparatus for treating incinerated ash of the present invention, the incinerator ash is fired in the furnace, and the oxygen concentration in the furnace is controlled according to the firing temperature. Even if the heating temperature is lower than that of the above, the elution of a plurality of heavy metals from the incinerated ash can be suppressed collectively. Therefore, the energy cost and the apparatus cost can be reduced as compared with the conventional melting process. In addition, incineration ash fired by this treatment method and treatment apparatus can be preferably used as a construction / civil engineering material because elution of heavy metals is suppressed.
【図1】 本発明に係る焼却灰の処理装置の実施の形態
の一例を概念的に示す図である。FIG. 1 is a diagram conceptually showing an example of an embodiment of an incineration ash treatment apparatus according to the present invention.
【図2】 酸素濃度と重金属の溶出量との関係を調べた
結果を示すグラフ図である。FIG. 2 is a graph showing the results of examining the relationship between the oxygen concentration and the elution amount of heavy metals.
10 処理装置 11 焼成炉 12 加熱手段 13 温度計 14 制御装置 20 酸素濃度制御装置 21 酸素濃度計 22 ガス供給系 10 processor 11 firing furnace 12 Heating means 13 Thermometer 14 Control device 20 Oxygen concentration control device 21 Oxygen analyzer 22 Gas supply system
───────────────────────────────────────────────────── フロントページの続き (72)発明者 上野 俊一朗 神奈川県横浜市磯子区新中原町1番地 石 川播磨重工業株式会社機械・プラント開発 センター内 (72)発明者 久保田 伸彦 神奈川県横浜市磯子区新中原町1番地 石 川播磨重工業株式会社機械・プラント開発 センター内 (72)発明者 三村 正文 東京都江東区豊洲三丁目2番16号 石川播 磨重工業株式会社東京エンジニアリングセ ンター内 (72)発明者 山田 貞裕 東京都江東区豊洲三丁目2番16号 石川播 磨重工業株式会社東京エンジニアリングセ ンター内 (72)発明者 瀬尾 康二 東京都江東区豊洲三丁目2番16号 石川播 磨重工業株式会社東京エンジニアリングセ ンター内 Fターム(参考) 3K061 NA08 NA12 3K062 AA24 AB03 AC03 BA02 BB02 CA01 CB03 DA22 4D004 AA36 AB03 BA02 CA30 CB04 CB31 DA01 DA02 DA03 DA06 DA10 ─────────────────────────────────────────────────── ─── Continued front page (72) Inventor Shunichiro Ueno Stone, Shin-Nakahara-cho, Isogo-ku, Yokohama-shi, Kanagawa Kawaharima Heavy Industries Co., Ltd. Machine and plant development In the center (72) Inventor Nobuhiko Kubota Stone, Shin-Nakahara-cho, Isogo-ku, Yokohama-shi, Kanagawa Kawaharima Heavy Industries Co., Ltd. Machine and plant development In the center (72) Inventor Masafumi Mimura 3-2-16 Toyosu, Koto-ku, Tokyo Ishikawa Ban Maru Heavy Industries Tokyo Engineering Center In the center (72) Inventor Sadahiro Yamada 3-2-16 Toyosu, Koto-ku, Tokyo Ishikawa Ban Maru Heavy Industries Tokyo Engineering Center In the center (72) Inventor Koji Seo 3-2-16 Toyosu, Koto-ku, Tokyo Ishikawa Ban Maru Heavy Industries Tokyo Engineering Center In the center F-term (reference) 3K061 NA08 NA12 3K062 AA24 AB03 AC03 BA02 BB02 CA01 CB03 DA22 4D004 AA36 AB03 BA02 CA30 CB04 CB31 DA01 DA02 DA03 DA06 DA10
Claims (4)
温度に応じて前記炉内の酸素濃度を制御することを特徴
とする焼却灰の処理方法。1. A method for treating incinerated ash, which comprises firing the incinerated ash in a furnace and controlling the oxygen concentration in the furnace according to the firing temperature.
記炉内の酸素濃度を0%を超えて10%未満に制御する
ことを特徴とする請求項1に記載の焼却灰の処理方法。2. The method for treating incinerated ash according to claim 1, wherein when the firing temperature is 800 to 900 ° C., the oxygen concentration in the furnace is controlled to be more than 0% and less than 10%.
濃度を制御する酸素濃度制御装置とを備えることを特徴
とする焼却灰の処理装置。3. A device for treating incinerated ash, comprising: a furnace for firing incinerated ash; and an oxygen concentration control device for controlling the oxygen concentration in the furnace.
素濃度を計測する酸素濃度計と、該酸素濃度計の計測結
果に基づいて前記炉内に所定のガスを供給するガス供給
装置とを含むことを特徴とする請求項3に記載の焼却灰
の処理装置。4. The oxygen concentration control device includes an oxygen concentration meter for measuring the oxygen concentration in the furnace, and a gas supply device for supplying a predetermined gas into the furnace based on the measurement result of the oxygen concentration meter. The incineration ash processing apparatus according to claim 3, comprising:
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Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006207909A (en) * | 2005-01-27 | 2006-08-10 | Actree Corp | Waste and contaminant recycling device and method |
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2001
- 2001-12-27 JP JP2001395581A patent/JP2003190910A/en active Pending
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JP2006207909A (en) * | 2005-01-27 | 2006-08-10 | Actree Corp | Waste and contaminant recycling device and method |
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