JPH06170162A - Method for collecting harmful metal in exhaust gas and treatment of collected ash - Google Patents

Method for collecting harmful metal in exhaust gas and treatment of collected ash

Info

Publication number
JPH06170162A
JPH06170162A JP4330295A JP33029592A JPH06170162A JP H06170162 A JPH06170162 A JP H06170162A JP 4330295 A JP4330295 A JP 4330295A JP 33029592 A JP33029592 A JP 33029592A JP H06170162 A JPH06170162 A JP H06170162A
Authority
JP
Japan
Prior art keywords
exhaust gas
harmful metal
collected
bag filter
calcium
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
JP4330295A
Other languages
Japanese (ja)
Other versions
JP2809366B2 (en
Inventor
Kazuo Sakanaya
和夫 魚屋
Hiroshi Ogawa
弘 小川
Kimitoshi Ose
公利 小瀬
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.)
Mitsubishi Heavy Industries Ltd
Original Assignee
Mitsubishi Heavy Industries 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 Mitsubishi Heavy Industries Ltd filed Critical Mitsubishi Heavy Industries Ltd
Priority to JP4330295A priority Critical patent/JP2809366B2/en
Publication of JPH06170162A publication Critical patent/JPH06170162A/en
Application granted granted Critical
Publication of JP2809366B2 publication Critical patent/JP2809366B2/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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  • Treating Waste Gases (AREA)

Abstract

PURPOSE:To efficiently collect harmful metal from exhaust gas by adding at least one kind selected from among slaked lime, calcium carbonate and calcium oxide, a reaction auxiliary and calcium silicate to exhaust gas discharged from an incinerator and collecting harmful metal together with the said additives by a bag filter device. CONSTITUTION:In a method for collecting harmful metal in exhaust gas discharged from an incinerator, harmful metal (i.e., cadmium, lead and mercury) is collected together with the following additives by a bag filter device 5 by adding at least one kind selected from among slaked lime, calcium carbonate and calcium oxide to exhaust gas G1 in a duct 1 thereof from a feeder 2, adding a reaction auxiliary (e.g. a mixture of diatomaceous earth and perlite) from a feeder 3 and adding calcium silicate from a feeder 4. Collected ashes W1 recovered by such a way is humidified by a humidifier 6 and thereafter molded into a pellet shape or a briquette shape by a molding device 7. The molded form is dried by a drier 8. As a result, harmful metal is efficiently collected from exhaust gas of an incineration facility.

Description

【発明の詳細な説明】Detailed Description of the Invention

【0001】[0001]

【産業上の利用分野】本発明は、都市ごみ焼却炉、産業
廃棄物焼却炉、その他の有害金属を発生する焼却施設の
排ガスから有害金属を捕集する処理方法及び捕集された
有害金属を固定化処理を行う方法に関する。
FIELD OF THE INVENTION The present invention relates to a treatment method for collecting harmful metals from exhaust gas from municipal waste incinerators, industrial waste incinerators, and other incinerators that generate harmful metals, and the collected harmful metals. The present invention relates to a method of immobilizing.

【0002】[0002]

【従来の技術】従来、焼却炉から発生する排ガス中の有
害金属(金属酸化物、金属塩化物、金属硫酸塩、その他
の金属塩を含む)は、サイクロン、電気集塵機、バグフ
ィルタ、湿式洗浄装置などにより捕集し、セメント固
化、溶融固化などして安定化し、埋立処分していた。
2. Description of the Related Art Conventionally, harmful metals (including metal oxides, chlorides, sulfates and other metal salts) in exhaust gas generated from incinerators are cyclones, electrostatic precipitators, bag filters, wet cleaning equipment. It was collected by means such as cement, stabilized by cement solidification, melt solidification, etc., and then landfilled.

【0003】[0003]

【発明が解決しようとする課題】しかし、上記の方法で
は、有害金属を有効に捕集することができず、また、安
定化処理も煩雑であった。そこで、本発明は、上記の問
題を解消し、排ガス中の有害金属を効率的に捕集する方
法及び捕集した有害金属を簡単に安定化処理する方法を
提供しようとするものである。
However, in the above method, harmful metals cannot be effectively collected, and the stabilization treatment is complicated. Therefore, the present invention is intended to solve the above problems and provide a method for efficiently collecting harmful metals in exhaust gas and a method for easily stabilizing the collected harmful metals.

【0004】[0004]

【問題点を解決するための手段】本発明は、(1) 焼却炉
からの排ガス中の有害金属を捕集する方法において、該
排ガス中に消石灰、炭酸カルシウム及び酸化カルシウム
の中の1種以上、反応助剤、並びに、珪酸カルシウムを
添加し、バグフィルタ装置で前記添加剤とともに有害金
属を捕集することを特徴とする有害金属の捕集方法、及
び、(2) 焼却炉から捕集される排ガス中の有害金属の処
理方法において、該排ガス中に消石灰、炭酸カルシウム
及び酸化カルシウムの中の1種以上、反応助剤、並び
に、珪酸カルシウムを添加し、バグフィルタ装置で前記
添加剤とともに有害金属を捕集し、該バグフィルタ装置
から排出された有害金属を含有する添加剤を加湿してペ
レット状若しくはブリケット状に成形し、乾燥すること
を特徴とする有害金属の処理方法である。
The present invention provides (1) a method for collecting harmful metals in exhaust gas from an incinerator, wherein at least one of slaked lime, calcium carbonate and calcium oxide is contained in the exhaust gas. , A reaction aid, and calcium silicate are added, and a harmful metal is collected together with the additive with a bag filter device, and (2) a harmful metal is collected from an incinerator. In the method for treating harmful metals in exhaust gas, slaked lime, at least one of calcium carbonate and calcium oxide, a reaction aid, and calcium silicate are added to the exhaust gas, and harmful together with the additive in a bag filter device. A harmful metal characterized by collecting metal, humidifying an additive containing a harmful metal discharged from the bag filter device, forming into pellets or briquettes, and drying. It is a processing method.

【0005】[0005]

【作用】本発明は、排ガス中に消石灰、炭酸カルシウム
及び酸化カルシウムの中の1種以上、反応助剤、並び
に、珪酸カルシウムを添加して有害金属を固定するとと
もに、バグフィルタ装置で上記粉末と有害金属を捕集す
ることにより、捕集効率を高めることができ、さらに、
捕集した灰を加湿することにより、容易に固化すること
ができ、セメント等を用いることなく、ペレット状若し
くはブリケット状に成形し、乾燥することにより、容易
に溶出しない成形体を得ることができ、埋立等にそのま
ま使用することができるようになった。なお、反応助剤
としては、けいそう土若しくはけいそう土を主成分とす
る粉体を使用することができ、パーライトなどを併用す
ることも可能である。
According to the present invention, at least one of slaked lime, calcium carbonate and calcium oxide, a reaction aid, and calcium silicate are added to the exhaust gas to fix harmful metals, and at the same time, a bag filter device By collecting harmful metals, collection efficiency can be increased, and
By humidifying the collected ash, it can be easily solidified, and can be molded into pellets or briquettes without using cement or the like, and dried to obtain a molded body that does not easily elute. It can now be used as it is for landfills. As the reaction aid, diatomaceous earth or powder containing diatomaceous earth as a main component can be used, and perlite or the like can be used together.

【0006】図1は、本発明の方法を説明するための概
念図である。G1 は焼却炉から排出される処理前の原ガ
スであり、有害金属の他に、HCl、SOX 、HFなど
の酸性ガスを含有する。排ガスダクト1には、消石灰供
給装置2、反応助剤供給装置3及び珪酸カルシウム粉末
供給装置4を設け、処理剤を順次噴射して、排ガスダク
ト1内で消石灰に酸性ガスを吸収させ、珪酸カルシウム
に有害金属を吸着させ、その後、バグフィルタ装置5で
これらを捕集し、バクフィルタ表面の上記添加剤層を形
成して該層で酸性ガス及び有害金属をさらに吸収・吸着
し、浄化された排ガスはG2 として放出される。次に、
バグフィルタ5に捕集された上記添加剤を含む捕集灰W
を、加湿装置6で加湿し、固化装置7でペレット状もし
くはブリケット状に成形し、乾燥装置8で水分を必要に
応じて除去し、乾燥固化された成形体W2 は系外に搬出
され、埋立等に提供される。
FIG. 1 is a conceptual diagram for explaining the method of the present invention. G 1 is a raw gas before treatment discharged from the incinerator, and contains acidic gases such as HCl, SO x and HF in addition to harmful metals. The exhaust gas duct 1 is provided with a slaked lime supply device 2, a reaction auxiliary agent supply device 3 and a calcium silicate powder supply device 4, and a treating agent is sequentially injected so that the slaked lime absorbs an acidic gas in the exhaust gas duct 1 to obtain calcium silicate. After adsorbing harmful metals to the bag filter, the bag filter device 5 collects them, forms the additive layer on the surface of the back filter, and further absorbs and adsorbs acidic gas and harmful metals in the layer to purify them. The exhaust gas is emitted as G 2 . next,
Collection ash W containing the above-mentioned additive collected in the bag filter 5
Are humidified by a humidifying device 6, molded into pellets or briquettes by a solidifying device 7, moisture is removed as necessary by a drying device 8, and the dried and solidified molded body W 2 is carried out of the system, It is provided for landfills.

【0007】[0007]

【実施例】【Example】

(実施例1)都市ごみ焼却炉からの排ガスを図1の装置
で処理した。排ガス中にはHClを500ppm、SO
X を100pmm、ばいじんを3.0g/Nm3 、有害
金属としてCdを0.8mg/Nm3 、Pbを31.6
mg/Nm3 、及び、Hgを0.32mg/Nm3 含有
し、排ガス量は20000Nm3 −Dry/hrであっ
た。添加剤は、消石灰粉末を60kg/hr、反応助剤
(けいそう土/パーライトの重量比=9/1)を15k
g/hr、及び珪酸カルシウム粉末(SiO2/CaO
の重量比=1/1)を6kg/hrそれぞれの供給装置
から噴射した。
(Example 1) Exhaust gas from an MSW incinerator was treated by the apparatus shown in FIG. HCl in the exhaust gas is 500 ppm, SO
X is 100 pmm, dust is 3.0 g / Nm 3 , Cd is 0.8 mg / Nm 3 as a harmful metal, and Pb is 31.6.
mg / Nm 3, and the Hg containing 0.32 mg / Nm 3, the amount of exhaust gas was 20000Nm 3 -Dry / hr. Additives are 60 kg / hr of slaked lime powder and 15k of reaction aid (diatomaceous earth / perlite weight ratio = 9/1).
g / hr, and calcium silicate powder (SiO 2 / CaO
(Weight ratio of 1/1) was injected from each of the supply devices at 6 kg / hr.

【0008】その結果、処理後の排ガス中には、HCl
が10ppm以下、SOX が5pmm以下、ばいじんを
1mg/Nm3 以下、Cdが0.01mg/Nm3
下、Pbが0.01mg/Nm3 以下、Hgが0.05
mg/Nm3 以下に浄化することができた。バグフィル
タで捕集された灰(消石灰、反応助剤、珪酸カルシウム
を含む)は約141kg/hrであった。この捕集灰に
水分40kg/hrを加えて加湿し、その後ブリケット
マシンで固め、乾燥装置で水分を20kg/hrの乾燥
速度で蒸発した後、系外に排出することができた。
As a result, in the exhaust gas after the treatment, HCl
Is 10 ppm or less, SO X is 5 pmm or less, soot and dust is 1 mg / Nm 3 or less, Cd is 0.01 mg / Nm 3 or less, Pb is 0.01 mg / Nm 3 or less, and Hg is 0.05.
It could be purified to less than mg / Nm 3 . The amount of ash (including slaked lime, reaction aid and calcium silicate) collected by the bag filter was about 141 kg / hr. Moisture of 40 kg / hr was added to the collected ash to humidify it, and thereafter, it was solidified by a briquette machine, evaporated with a drying device at a drying rate of 20 kg / hr, and then discharged outside the system.

【0009】(比較例)実施例1の条件のうち、珪酸カ
ルシウムの供給を省略したところ、処理後の排ガスに
は、HClが10ppm、SOX が5pmm、ばいじん
を1mg/Nm3、Cdが0.03mg/Nm3 、Pb
が0.02mg/Nm3 、Hgが0.08mg/Nm3
含有されており、捕集灰は約135kg/hrであっ
た。この捕集灰に水分40kg/hrを加えて加湿し、
その後ブリケットマシンで固化を試みたが、うまく固化
することができなかった。
(Comparative Example) Among the conditions of Example 1, when the supply of calcium silicate was omitted, the treated exhaust gas contained 10 ppm of HCl, 5 ppm of SO X , 1 mg / Nm 3 of dust and Cd of 0. 0.03 mg / Nm 3 , Pb
There 0.02mg / Nm 3, Hg is 0.08mg / Nm 3
It was contained, and the collected ash was about 135 kg / hr. Moisture 40 kg / hr was added to the collected ash to humidify it.
After that, I tried to solidify with a briquette machine, but could not solidify well.

【0010】(実施例2)産業廃棄物焼却炉からの排ガ
スを図1の装置で処理した。排ガス中にはHClを10
00ppm、SOX を20pmm、ばいじんを10g/
Nm3 、有害金属としてCdを0.2mg/Nm3 、P
bを50mg/Nm3 、Hgを0mg/Nm3 含有し、
排ガス量は15000Nm3 −Dry/hrであった。
添加剤としては、消石灰粉末を65kg/hr、反応助
剤(けいそう土/パーライトの重量比=8/2)を6k
g/hr、珪酸カルシウム粉末(SiO2 /CaOの重
量比=1/1)を6kg/hrそれぞれの供給装置から
噴射した。
Example 2 Exhaust gas from an industrial waste incinerator was treated by the apparatus shown in FIG. HCl in the exhaust gas is 10
00ppm, SO x 20pmm, Dust 10g /
Nm 3, Cd and 0.2 mg / Nm 3 as toxic metals, P
b of 50 mg / Nm 3 and Hg of 0 mg / Nm 3 ,
The amount of exhaust gas was 15000 Nm 3 -Dry / hr.
As additives, slaked lime powder 65 kg / hr, reaction aid (diatomaceous earth / perlite weight ratio = 8/2) 6 k
g / hr and calcium silicate powder (SiO 2 / CaO weight ratio = 1/1) were sprayed from respective feeders at 6 kg / hr.

【0011】その結果、処理後の排ガスは、HClが2
0ppm以下、SOX が1pmm以下、ばいじんを5m
g/Nm3 以下、Cdが0.01mg/Nm3 以下、P
bが0.01mg/Nm3 以下まで浄化することができ
た。バグフィルタで捕集された灰は約227kg/hr
であった。この捕集灰に水分70kg/hrを加えて加
湿し、その後ペレットマシンで固化し、乾燥装置で水分
を35kg/hrの乾燥速度で蒸発した後、系外に排出
することができた。
As a result, the treated exhaust gas contains 2% HCl.
0ppm or less, SO X is 1pm or less, soot and dust 5m
g / Nm 3 or less, Cd 0.01 mg / Nm 3 or less, P
b could be purified to 0.01 mg / Nm 3 or less. The ash collected by the bag filter is about 227 kg / hr
Met. A moisture content of 70 kg / hr was added to the collected ash to humidify it, then solidified by a pellet machine, and the moisture content was evaporated at a drying rate of 35 kg / hr in a drying device, and then it could be discharged to the outside of the system.

【0012】[0012]

【発明の効果】本発明は、上記の構成を採用することに
より、都市ごみ焼却炉や産業廃棄物焼却炉などから排出
される排ガスから、有害金属及び酸性ガスを効果的に除
去することができ、かつ、捕集された有害金属を容易に
固化することができ、無害の埋立材料として供給するこ
とが可能になった。
EFFECTS OF THE INVENTION By adopting the above-mentioned constitution, the present invention can effectively remove harmful metals and acid gases from exhaust gas discharged from municipal waste incinerators, industrial waste incinerators and the like. In addition, the collected harmful metals can be easily solidified and can be supplied as a harmless landfill material.

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

【図1】本発明の1実施例である焼却炉からの排ガスの
処理方法を説明するための図である。
FIG. 1 is a diagram for explaining a method for treating exhaust gas from an incinerator which is an embodiment of the present invention.

Claims (2)

【特許請求の範囲】[Claims] 【請求項1】 焼却炉からの排ガス中の有害金属を捕集
する方法において、該排ガス中に消石灰、炭酸カルシウ
ム及び酸化カルシウムの中の1種以上、反応助剤、並び
に、珪酸カルシウムを添加し、バグフィルタ装置で前記
添加剤とともに有害金属を捕集することを特徴とする有
害金属の捕集方法。
1. A method for collecting harmful metals in exhaust gas from an incinerator, wherein slaked lime, at least one of calcium carbonate and calcium oxide, a reaction aid, and calcium silicate are added to the exhaust gas. A method for collecting a harmful metal, wherein a bag filter device collects the harmful metal together with the additive.
【請求項2】 焼却炉から捕集される排ガス中の有害金
属の処理方法において、該排ガス中に消石灰、炭酸カル
シウム及び酸化カルシウムの中の1種以上、反応助剤、
並びに、珪酸カルシウムを添加し、バグフィルタ装置で
前記添加剤とともに有害金属を捕集し、該バグフィルタ
装置から排出された有害金属を含有する添加剤を加湿し
てペレット状若しくはブリケット状に成形し、乾燥する
ことを特徴とする有害金属の処理方法。
2. A method for treating harmful metals in exhaust gas collected from an incinerator, wherein the exhaust gas contains at least one of slaked lime, calcium carbonate and calcium oxide, a reaction aid,
Also, calcium silicate is added, a harmful metal is collected together with the additive in a bag filter device, and the additive containing the harmful metal discharged from the bag filter device is humidified to form a pellet or briquette. And a method of treating harmful metals, characterized by drying.
JP4330295A 1992-12-10 1992-12-10 Method for collecting harmful metals in exhaust gas and method for treating collected ash Expired - Fee Related JP2809366B2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP4330295A JP2809366B2 (en) 1992-12-10 1992-12-10 Method for collecting harmful metals in exhaust gas and method for treating collected ash

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP4330295A JP2809366B2 (en) 1992-12-10 1992-12-10 Method for collecting harmful metals in exhaust gas and method for treating collected ash

Publications (2)

Publication Number Publication Date
JPH06170162A true JPH06170162A (en) 1994-06-21
JP2809366B2 JP2809366B2 (en) 1998-10-08

Family

ID=18231058

Family Applications (1)

Application Number Title Priority Date Filing Date
JP4330295A Expired - Fee Related JP2809366B2 (en) 1992-12-10 1992-12-10 Method for collecting harmful metals in exhaust gas and method for treating collected ash

Country Status (1)

Country Link
JP (1) JP2809366B2 (en)

Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004524955A (en) * 2001-01-26 2004-08-19 セーデーエーエム ホラント ベー.フェー. How to remove mercury from gas streams
JP2008238163A (en) * 2007-03-01 2008-10-09 Japan Enviro Chemicals Ltd Removal method of mercury vapor in gas
WO2008137647A1 (en) * 2007-05-03 2008-11-13 Cbl Industrial Services, Inc. Process for treating particulate material containing heavy metal and an additive for use in such process
NL2001813C2 (en) * 2008-07-16 2010-01-19 Minplus Holland B V Process for removing mercury from gas stream i.e. flue gas, involves bringing flow of gas stream at given temperature into contact with solid phase in which silicon and calcium or calcium silicate is included
JP2010514550A (en) * 2006-12-28 2010-05-06 イテア エス.ピー.エー. Purification method for combustion fumes
US8075666B2 (en) 2007-05-03 2011-12-13 Cbl Industrial Services, Inc. Process for treating particulate material containing heavy metal and an additive for use in such process

Cited By (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2004524955A (en) * 2001-01-26 2004-08-19 セーデーエーエム ホラント ベー.フェー. How to remove mercury from gas streams
JP2010514550A (en) * 2006-12-28 2010-05-06 イテア エス.ピー.エー. Purification method for combustion fumes
JP2014221474A (en) * 2006-12-28 2014-11-27 イテア エス.ピー.エー.Itea S.P.A. Combustion smog purification method
JP2008238163A (en) * 2007-03-01 2008-10-09 Japan Enviro Chemicals Ltd Removal method of mercury vapor in gas
WO2008137647A1 (en) * 2007-05-03 2008-11-13 Cbl Industrial Services, Inc. Process for treating particulate material containing heavy metal and an additive for use in such process
US8075666B2 (en) 2007-05-03 2011-12-13 Cbl Industrial Services, Inc. Process for treating particulate material containing heavy metal and an additive for use in such process
US8834602B2 (en) 2007-05-03 2014-09-16 Cbl Industrial Services, Inc. Process for treating particulate material containing heavy metal and an additive for use in such process
NL2001813C2 (en) * 2008-07-16 2010-01-19 Minplus Holland B V Process for removing mercury from gas stream i.e. flue gas, involves bringing flow of gas stream at given temperature into contact with solid phase in which silicon and calcium or calcium silicate is included

Also Published As

Publication number Publication date
JP2809366B2 (en) 1998-10-08

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