JP2001179207A - Method for treating waste active carbon in which dioxins are adsorbed - Google Patents

Method for treating waste active carbon in which dioxins are adsorbed

Info

Publication number
JP2001179207A
JP2001179207A JP37048099A JP37048099A JP2001179207A JP 2001179207 A JP2001179207 A JP 2001179207A JP 37048099 A JP37048099 A JP 37048099A JP 37048099 A JP37048099 A JP 37048099A JP 2001179207 A JP2001179207 A JP 2001179207A
Authority
JP
Japan
Prior art keywords
dioxins
active carbon
adsorbed
activated carbon
waste active
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
JP37048099A
Other languages
Japanese (ja)
Inventor
Takashi Ogawa
隆 小川
Kazuhiro Terada
和宏 寺田
Toshiharu Kuroda
利春 黒田
Masaki Kawashima
正毅 川島
Masafumi Moriya
雅文 守屋
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.)
Miyoshi Yushi KK
Miyoshi Oil and Fat Co Ltd
Original Assignee
Miyoshi Yushi KK
Miyoshi Oil and Fat Co 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 Miyoshi Yushi KK, Miyoshi Oil and Fat Co Ltd filed Critical Miyoshi Yushi KK
Priority to JP37048099A priority Critical patent/JP2001179207A/en
Publication of JP2001179207A publication Critical patent/JP2001179207A/en
Pending legal-status Critical Current

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  • Treating Waste Gases (AREA)
  • Processing Of Solid Wastes (AREA)

Abstract

PROBLEM TO BE SOLVED: To solve such social and environmental problems that dioxins are contained in flue gas generated at a refuse incineration installation or the like and are conventionally removed by a method to atomize active carbon into a flue and thereby adsorb and remove the dioxins contained in the flue gas and in order to treat waste active carbon in which the dioxins are adsorbed, the dioxins need to be decomposed by heating the waste active carbon in an oxygen shortage state under a sophisticated airtight atmosphere and further, a special installation for keeping the oxygen deficient state is required with unavoidable large investment in facilities and high maintenance cost therefor. SOLUTION: This method for treating the waste active carbon in which the dioxins are adsorbed is characterized in that at least one kind selected from the group of a phosphorus compound, an aluminum compound and a calcium compound is added to the waste active carbon in which the dioxins are adsorbed and this mixture is heated and treated at 200-600 deg.C.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は、ダイオキシン類を
吸着した廃活性炭の処理方法に関する。
The present invention relates to a method for treating waste activated carbon adsorbing dioxins.

【0002】[0002]

【従来の技術及び発明が解決しようとする課題】都市ゴ
ミ、産業廃棄物等の焼却によって生じる排ガス中には、
SOx 、NOx、塩化水素、重金属等の種々の有害物質
が含まれており、特にダイオキシン類等の有毒な塩素化
合物が多く含まれている場合があることが、近年、大き
な社会問題となっている。
2. Description of the Related Art Exhaust gas generated by incineration of municipal garbage, industrial waste, and the like includes:
Recently, various harmful substances such as SOx, NOx, hydrogen chloride, and heavy metals are contained. Particularly, there is a case where a large amount of toxic chlorine compounds such as dioxins is contained. .

【0003】ダイオキシン類等の塩素化合物(以下、単
にダイオキシン類と呼ぶ。)は非常に安定な物質で水に
溶けず、半永久的に毒性が消失しないことから、その強
い毒性と相俟って環境汚染対策の重要化学物質とされて
いる。ゴミ焼却場において廃棄物、特にプラスチック廃
棄物を焼却処理した際に生成する可能性の高いダイオキ
シン類の生成量を低減化させるためには、従来、煙道に
活性炭粉末を噴霧する等により、燃焼によって生じた排
ガスを活性炭と接触させて排ガス中のダイオキシン類を
活性炭に吸着させた後、バグフィルターを通過させて活
性炭を排ガス中から分離することにより、排ガス中から
ダイオキシン類を除去する方法が採用されている。
[0003] Chlorine compounds such as dioxins (hereinafter simply referred to as dioxins) are very stable substances, do not dissolve in water, and do not lose their toxicity semipermanently. It is regarded as an important chemical for pollution control. In order to reduce the amount of dioxins that are likely to be generated when incinerating waste, especially plastic waste, at garbage incineration plants, conventional methods include spraying activated carbon powder into the flue and burning it. After the dioxin in the exhaust gas is adsorbed on the activated carbon by contacting the exhaust gas generated by the activated carbon with the activated carbon, the dioxin is removed from the exhaust gas by separating the activated carbon from the exhaust gas by passing through a bag filter. Have been.

【0004】焼却炉の煙道に噴霧して排ガス中のダイオ
キシン類を吸着した活性炭は、そのまま投棄処理すると
重大な環境問題を生じる虞れがあるため、加熱処理して
ダイオキシン類を分解してから投棄する等の方法が採用
されている。従来、ダイオキシン類を加熱して分解する
方法としては、非通り抜け系において酸欠状態で加熱す
る方法(特公平6−38863号公報)が、効率よくダ
イオキシン類を分解処理できる方法とされている。しか
しながら、この方法では酸欠状態にしないとダイオキシ
ン類を有効に分解し得ないとともに、酸欠状態を得るに
は、閉鎖系において或いは不活性ガス雰囲気中で作業し
て空気の侵入を排除する等の方法を採用する必要があ
り、加熱処理装置に高い気密構造が要求されるため、設
備投資や設備の保守等に高いコストがかかるという問題
があった。また、上記方法では、ダイオキシン類等の塩
素化芳香族化合物を加熱分解しても、塩素と芳香族化合
物の段階までしか分解されないものが存在する虞れがあ
り、このような塩素と芳香族化合物が加熱条件下で結合
してダイオキシン類等が再度生成される虞れもあった。
[0004] Activated carbon that has been sprayed onto the flue of an incinerator and adsorbed dioxins in the exhaust gas may cause serious environmental problems if it is discarded as it is. A method such as dumping is adopted. Conventionally, as a method of heating and decomposing dioxins, a method of heating in a non-penetrating system in an oxygen-deficient state (Japanese Patent Publication No. 6-38863) is a method capable of efficiently decomposing dioxins. However, in this method, dioxins cannot be effectively decomposed unless they are in an oxygen-deficient state, and in order to obtain an oxygen-deficient state, work in a closed system or in an inert gas atmosphere to eliminate air intrusion, etc. It is necessary to employ the method described above, and a high airtight structure is required for the heat treatment apparatus, and thus there is a problem that high costs are required for capital investment and maintenance of the equipment. Further, in the above method, even if the chlorinated aromatic compound such as dioxins is thermally decomposed, there is a possibility that there is a substance which is decomposed only to the stage of chlorine and the aromatic compound. May be combined under heating conditions to generate dioxins and the like again.

【0005】本発明者等は上記課題を解決するためにな
されたもので、酸欠状態で加熱することを必須とする従
来法のような特別な処理装置や煩雑な操作を必要とせず
に、活性炭に吸着されたダイオキシン類を低コストで効
率良く加熱分解することのできる、ダイオキシン類を吸
着した廃活性炭の処理方法を提供することを目的とす
る。
The inventors of the present invention have been made in order to solve the above-mentioned problems, and do not require a special processing apparatus or a complicated operation such as a conventional method which requires heating in an oxygen-deficient state. An object of the present invention is to provide a method for treating waste activated carbon adsorbing dioxins, which can efficiently and thermally decompose dioxins adsorbed on activated carbon at low cost.

【0006】[0006]

【課題を解決するための手段】即ち、本発明のダイオキ
シン類を吸着した廃活性炭の処理方法は、ダイオキシン
類を吸着した廃活性炭に、燐系化合物、アルミニウム化
合物、カルシウム化合物より選ばれた少なくとも1種を
添加して200〜600℃で加熱処理することを特徴と
する。
That is, the method of the present invention for treating waste activated carbon having adsorbed dioxins is characterized in that at least one selected from a phosphorus compound, an aluminum compound and a calcium compound is added to the waste activated carbon having adsorbed dioxins. It is characterized in that seeds are added and heat treatment is performed at 200 to 600 ° C.

【0007】[0007]

【発明の実施の形態】本発明方法において用いる燐系化
合物としては、例えば次亜燐酸ナトリウム、次亜燐酸カ
リウム、次亜燐酸カルシウム、次亜燐酸マグネシウム、
次亜燐酸アンモニウム等の次亜燐酸類;亜燐酸、亜燐酸
カルシウム、亜燐酸ナトリウム、亜燐酸カリウム、亜燐
酸マグネシウム、亜燐酸アンモニウム、亜燐酸水素カル
シウム、亜燐酸水素カリウム、亜燐酸水素ナトリウム、
亜燐酸水素マグネシウム等の亜燐酸類;燐酸カルシウ
ム、燐酸ナトリウム、燐酸カリウム、燐酸アンモニウム
等の燐酸類が挙げられる。またアルミニウム化合物とし
ては、燐酸アルミニウム、硫酸アルミニウム、水酸化ア
ルミニウム、酸化アルミニウム、硝酸アルミニウム、ア
ルミノシリカゲル等が、カルシウム化合物としては、水
酸化カルシウム、酸化カルシウム、炭酸カルシウム等が
挙げられる。これらの化合物は2種以上を適宜混合して
用いることができる。上記した化合物のなかでも、次亜
燐酸塩、アルミニウム化合物が好ましい。
BEST MODE FOR CARRYING OUT THE INVENTION The phosphorus compounds used in the method of the present invention include, for example, sodium hypophosphite, potassium hypophosphite, calcium hypophosphite, magnesium hypophosphite.
Hypophosphorous acids such as ammonium hypophosphite; phosphorous acid, calcium phosphite, sodium phosphite, potassium phosphite, magnesium phosphite, ammonium phosphite, calcium hydrogen phosphite, potassium hydrogen phosphite, sodium hydrogen phosphite;
Phosphorous acids such as magnesium hydrogen phosphite; and phosphoric acids such as calcium phosphate, sodium phosphate, potassium phosphate, and ammonium phosphate. Examples of the aluminum compound include aluminum phosphate, aluminum sulfate, aluminum hydroxide, aluminum oxide, aluminum nitrate, and alumino-silica gel. Examples of the calcium compound include calcium hydroxide, calcium oxide, and calcium carbonate. These compounds can be used as a mixture of two or more kinds. Of the above compounds, hypophosphite and aluminum compounds are preferred.

【0008】上記、燐系化合物、アルミニウム化合物、
カルシウム化合物の少なくとも1種を廃活性炭に対して
添加する量は、これらの化合物の合計量で、廃活性炭重
量の0.01〜50重量%が好ましく、特に1〜5重量
%が好ましい。
The above-mentioned phosphorus compounds, aluminum compounds,
The amount of at least one calcium compound to be added to the waste activated carbon is preferably 0.01 to 50% by weight, and particularly preferably 1 to 5% by weight of the waste activated carbon in the total amount of these compounds.

【0009】上記の化合物の少なくとも1種を添加した
廃活性炭を加熱処理するためには、密閉型の加熱炉、炉
内に大気(空気)の流入、流出が自由な開放型の加熱炉
のいずれも使用することができる。加熱炉としては例え
ば、角窯、丸窯、輸窯等の単独窯、トンネルキルン、ロ
ータリーキルン等の半連続窯又は連続窯を使用すること
ができる。廃活性炭を加熱する温度は200〜600℃
であるが、300〜500℃がより好ましい。また加熱
処理時間は、通常10〜120分程度であるが、30〜
60分程度が好ましい。
In order to heat-treat waste activated carbon to which at least one of the above compounds has been added, either a closed-type heating furnace or an open-type heating furnace in which air (air) can freely flow in and out of the furnace. Can also be used. As the heating furnace, for example, a single kiln such as a square kiln, a round kiln, and a transfer kiln, a semi-continuous kiln such as a tunnel kiln and a rotary kiln, or a continuous kiln can be used. The temperature for heating waste activated carbon is 200-600 ° C
However, 300 to 500 ° C. is more preferable. The heating time is usually about 10 to 120 minutes,
About 60 minutes is preferable.

【0010】本発明方法においては、加熱処理時に加熱
炉内をあえて酸欠状態に保持する必要はないが、加熱工
程中に加熱炉内が酸欠状態となったとしても何ら問題は
ない。
In the method of the present invention, it is not necessary to intentionally hold the inside of the heating furnace in an oxygen-deficient state during the heat treatment, but there is no problem even if the inside of the heating furnace becomes oxygen-deficient during the heating step.

【0011】本発明方法が処理の対象とする廃活性炭と
しては、例えば、ゴミ焼却場において廃棄物を焼却した
際に生じる排ガス中に含まれるダイオキシン類を吸着す
る目的で、煙道に噴霧して使用した活性炭や、バグフィ
ルター通過後の排ガスを通過させる吸着塔に充填して使
用した活性炭のように、ダイオキシン類を吸着した廃活
性炭が挙げられる。
The waste activated carbon to be treated by the method of the present invention is, for example, sprayed into a flue for the purpose of adsorbing dioxins contained in exhaust gas generated when waste is incinerated in a garbage incineration plant. Examples of the activated carbon include used activated carbon and waste activated carbon adsorbing dioxins, such as activated carbon used by filling an adsorption tower through which exhaust gas after passing through a bag filter is passed.

【0012】[0012]

【実施例】以下、実施例を挙げて本発明を更に詳細に説
明する。
EXAMPLES Hereinafter, the present invention will be described in more detail with reference to examples.

【0013】実施例1〜5、比較例1〜2 ゴミ焼却場にて廃棄物を焼却した際に煙道に噴霧し、排
ガス中のダイオキシン類を吸着するために使用した廃活
性炭(ダイオキシン類吸着量400ng/g含有)に、
表1に示す化合物を添加し、ロータリーキルン中で同表
に示す温度、時間加熱処理した。処理後の廃活性炭に吸
着されて残留するダイオキシン類濃度を測定した結果を
表2に示す。加熱処理後の廃活性に吸着残留されている
ダイオキシン類の量は、廃棄物処理におけるダイオキシ
ン類標準測定分析マニュアル(平成9年2月、厚生省生
活衛生局水道環境部環境整備課)の灰試料分析法に準じ
て溶媒に抽出し、溶媒中に抽出されたダイオキシン類濃
度をGC−MS分析によって測定した。尚、実施例1〜
5は、加熱処理中、ロータリーキルン内に外部から酸素
が供給されるようにして加熱処理した。また比較例1、
2は加熱処理開始前に、ロータリーキルン内に窒素ガス
を供給してロータリーキルン内の酸素と置換した後、酸
欠状態のまま加熱処理を行った。
Examples 1-5, Comparative Examples 1-2 Waste activated carbon (dioxin adsorption) used to adsorb dioxins in exhaust gas by spraying onto a flue when waste is incinerated at a garbage incineration plant Amount of 400 ng / g)
The compounds shown in Table 1 were added, and the mixture was heated in a rotary kiln at the temperature and time shown in the same table. Table 2 shows the results of measuring the concentration of dioxins remaining after being absorbed by the waste activated carbon after the treatment. The amount of dioxins adsorbed and retained in the waste activity after the heat treatment is determined by the ash sample analysis in the Dioxins Standard Measurement and Analysis Manual for Waste Treatment (February 1997, Ministry of Health and Welfare, Health and Welfare Bureau, Water Supply Environment Department, Environment Improvement Division). The extract was extracted into a solvent according to the method, and the concentration of dioxins extracted in the solvent was measured by GC-MS analysis. In addition, Examples 1 to
In No. 5, the heat treatment was performed such that oxygen was supplied from the outside into the rotary kiln during the heat treatment. Comparative Example 1,
For No. 2, before the start of the heat treatment, a nitrogen gas was supplied into the rotary kiln to replace the oxygen in the rotary kiln, and then the heat treatment was performed in an oxygen-deficient state.

【0014】[0014]

【表1】 ※1:廃活性炭の重量に対する重量%[Table 1] * 1: Weight% based on the weight of waste activated carbon

【0015】[0015]

【表2】 [Table 2]

【0016】[0016]

【発明の効果】以上説明したように本発明方法によれ
ば、ゴミや産業廃棄物を焼却した際に生じる排煙中のダ
イオキシン類を吸着するため等に用いた廃活性炭を効率
よく処理することができ、加熱炉内を酸欠状態に保持し
て加熱処理を行わなくても、廃活性炭に吸着されている
ダイオキシン類を効果的に分解することができる。この
ため本発明方法は、加熱処理の際に酸欠状態を保持する
必要のある従来法に比べ、設備投資が少なくて済み、経
済的に効率良く処理を行うことができる効果を有する。
As described above, according to the method of the present invention, waste activated carbon used for, for example, adsorbing dioxins in flue gas generated when garbage or industrial waste is incinerated can be efficiently treated. Thus, the dioxins adsorbed on the waste activated carbon can be effectively decomposed without holding the inside of the heating furnace in an oxygen-deficient state and performing heat treatment. For this reason, the method of the present invention requires less capital investment and has an effect that the treatment can be performed economically and efficiently, as compared with the conventional method that needs to maintain an oxygen-deficient state during the heat treatment.

フロントページの続き (72)発明者 黒田 利春 東京都葛飾区堀切4丁目66番1号 ミヨシ 油脂株式会社内 (72)発明者 川島 正毅 東京都葛飾区堀切4丁目66番1号 ミヨシ 油脂株式会社内 (72)発明者 守屋 雅文 東京都葛飾区堀切4丁目66番1号 ミヨシ 油脂株式会社内 Fターム(参考) 4D002 AA21 AC04 BA04 DA41 4D004 AA47 AB07 CA22 CB09 CC11 CC12 DA03 DA06 Continued on the front page (72) Inventor Toshiharu Kuroda 4-66-1, Horikiri, Katsushika-ku, Tokyo Inside Miyoshi Yushi Corporation (72) Inventor Masatake Kawashima 4-66-1, Horikiri, Katsushika-ku, Tokyo Inside Miyoshi Yushi Corporation (72) Inventor Masafumi Moriya 4-66, Horikiri, Katsushika-ku, Tokyo Miyoshi Yushi Co., Ltd. F-term (reference) 4D002 AA21 AC04 BA04 DA41 4D004 AA47 AB07 CA22 CB09 CC11 CC12 DA03 DA06

Claims (1)

【特許請求の範囲】[Claims] 【請求項1】 ダイオキシン類を吸着した廃活性炭に、
燐系化合物、アルミニウム化合物、カルシウム化合物よ
り選ばれた少なくとも1種を添加して200〜600℃
で加熱処理することを特徴とするダイオキシン類を吸着
した廃活性炭の処理方法。
1. A waste activated carbon to which dioxins are adsorbed,
200-600 ° C. by adding at least one selected from a phosphorus compound, an aluminum compound, and a calcium compound
A method for treating waste activated carbon having adsorbed dioxins, wherein the activated carbon is heat-treated.
JP37048099A 1999-12-27 1999-12-27 Method for treating waste active carbon in which dioxins are adsorbed Pending JP2001179207A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP37048099A JP2001179207A (en) 1999-12-27 1999-12-27 Method for treating waste active carbon in which dioxins are adsorbed

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP37048099A JP2001179207A (en) 1999-12-27 1999-12-27 Method for treating waste active carbon in which dioxins are adsorbed

Publications (1)

Publication Number Publication Date
JP2001179207A true JP2001179207A (en) 2001-07-03

Family

ID=18497021

Family Applications (1)

Application Number Title Priority Date Filing Date
JP37048099A Pending JP2001179207A (en) 1999-12-27 1999-12-27 Method for treating waste active carbon in which dioxins are adsorbed

Country Status (1)

Country Link
JP (1) JP2001179207A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005238049A (en) * 2004-02-25 2005-09-08 Miyoshi Oil & Fat Co Ltd Solid waste disposal method and method of regenerating waste reclaiming disposal site
JP2005246345A (en) * 2004-03-08 2005-09-15 Miyoshi Oil & Fat Co Ltd Method for treating solid waste and method for regenerating waste landfill site
JP2017018903A (en) * 2015-07-13 2017-01-26 太平洋セメント株式会社 Regeneration method of waste activated carbon and manufacturing method of carburization material

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2005238049A (en) * 2004-02-25 2005-09-08 Miyoshi Oil & Fat Co Ltd Solid waste disposal method and method of regenerating waste reclaiming disposal site
JP2005246345A (en) * 2004-03-08 2005-09-15 Miyoshi Oil & Fat Co Ltd Method for treating solid waste and method for regenerating waste landfill site
JP2017018903A (en) * 2015-07-13 2017-01-26 太平洋セメント株式会社 Regeneration method of waste activated carbon and manufacturing method of carburization material

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