JPH03224618A - How to suppress dioxin generation - Google Patents

How to suppress dioxin generation

Info

Publication number
JPH03224618A
JPH03224618A JP2019972A JP1997290A JPH03224618A JP H03224618 A JPH03224618 A JP H03224618A JP 2019972 A JP2019972 A JP 2019972A JP 1997290 A JP1997290 A JP 1997290A JP H03224618 A JPH03224618 A JP H03224618A
Authority
JP
Japan
Prior art keywords
generation
exhaust gas
dioxine
dioxin
kcl
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
JP2019972A
Other languages
Japanese (ja)
Inventor
Yoshitoshi Sekiguchi
善利 関口
Kunio Sasaki
邦夫 佐々木
Hideo Shitaya
下谷 英雄
Shinichiro Ando
真一郎 安藤
Kazuo Ieyama
家山 一夫
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.)
Kanadevia Corp
Original Assignee
Hitachi Zosen Corp
Hitachi Shipbuilding and Engineering 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 Hitachi Zosen Corp, Hitachi Shipbuilding and Engineering Co Ltd filed Critical Hitachi Zosen Corp
Priority to JP2019972A priority Critical patent/JPH03224618A/en
Publication of JPH03224618A publication Critical patent/JPH03224618A/en
Pending legal-status Critical Current

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  • Treating Waste Gases (AREA)

Abstract

PURPOSE:To prevent the generation of dioxine by neutralizing HCl concerned in the generation of dioxine with an alkaline compd. at 900-300 deg.C into KCl or NaCl ready to be post-treated. CONSTITUTION:One or 2 kinds of alkaline compds. selected from a group consisting of KOH, K2CO3, KHCO3, NaOH, Na2CO3 and NaHCO3 are supplied from a feeder 7 into a waste gas discharge passage 6 from an incinerator at 900-300 deg.C to neutralize HCl contained in the waste gas and involving the generation of dioxine into KCl or NaCl as a stable compd. Consequently, the generation of dioxine is prevented, and the waste gas free of dioxine is discharged into the atmosphere.

Description

【発明の詳細な説明】 [産業上の利用分野] この発明は、都市ごみ、産業廃棄物などの焼却ないしそ
の排ガス処理に伴うダイオキシンの発生を未然に抑制す
る方法に関する。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a method for suppressing the generation of dioxins accompanying the incineration of municipal waste, industrial waste, etc. or the treatment of exhaust gas thereof.

[従来技術およびその問題点] ごみ焼却炉などから排出されるダイオキシンは、その生
成過程に不明な点が多いが、焼却炉後流の300℃未満
の低温域でHCl存在下に発生し、灰分の存在によりそ
の発生量が増加することがわかってきた。ダイオキシン
は、排ガス中には微量しか含まれていないが、微量でも
人体に対し極めて有毒で特に強い発癌性を示す物質であ
り、ごみ焼却炉排ガスの新たな公害問題を引き起こすも
のとして最近大きくクローズアップされつつある。
[Prior art and its problems] Dioxins emitted from garbage incinerators, etc., have many unknown points about their formation process, but they are generated in the presence of HCl in a low temperature region of less than 300 degrees Celsius downstream of the incinerator, and are produced in the presence of ash. It has been found that the amount generated increases with the presence of Although dioxins are only contained in trace amounts in exhaust gas, they are extremely toxic to the human body even in trace amounts, and are particularly carcinogenic.Dioxins have recently come under the spotlight as a new pollution problem caused by waste incinerator exhaust gas. It is being done.

従来の排ガス処理方法では、そのフローを第2図に示す
ように、ごみ焼却炉(1)で発生した排ガスは頂部出口
から排出され、電気集塵機(2)で除塵された後、排ガ
ス洗浄処理装Fl<3)で湿式洗浄処理され、誘引ファ
ン(4)により処理排ガスが煙突(5)から大気中へ放
散される。しかし、この排ガス処理フローではダイオキ
シンは湿式洗浄処理によってほとんど吸収除去できず、
そのまま大気中へ放散されているのが現状である。
In the conventional exhaust gas treatment method, the flow is shown in Figure 2. The exhaust gas generated in the waste incinerator (1) is discharged from the top outlet, and after being removed by the electrostatic precipitator (2), it is sent to the exhaust gas cleaning treatment equipment. A wet cleaning treatment is performed at Fl<3), and the treated exhaust gas is dissipated into the atmosphere from the chimney (5) by an induction fan (4). However, in this exhaust gas treatment flow, dioxins can hardly be absorbed and removed by wet cleaning treatment.
Currently, it is released into the atmosphere as is.

この発明は、上記の如き実情に鑑み、都市ごみ、産業廃
棄物などの焼却ないしその排ガス処理に伴うダイオキシ
ンの発生を未然に抑制する方法を提供することを目的と
する。
In view of the above-mentioned circumstances, it is an object of the present invention to provide a method for suppressing the generation of dioxins accompanying the incineration of municipal waste, industrial waste, etc. or the treatment of their exhaust gas.

[問題点の解決手段] この発明によるダイオキシン発生の抑制方法は、上記目
的の達成のために、焼却炉からの排ガス排出路における
900〜300℃の温度域に、KOH,に2 CO* 
、KHCO,、Na0HSNa、Co3およびN a 
HCOiからなる群から選ばれたアルカリ性化合物を1
種または2種以上供給し、排ガス中に含まれてダイオキ
シン生成に関与するHClを中和して安定化合物である
K C/またはNaC/を生成させることを特徴とする
[Means for Solving Problems] In order to achieve the above object, the method for suppressing the generation of dioxin according to the present invention injects KOH, niCO* into a temperature range of 900 to 300°C in the exhaust gas discharge path from the incinerator.
, KHCO, , Na0HSNa, Co3 and Na
1 alkaline compound selected from the group consisting of HCOi
The method is characterized in that a species or two or more species are supplied to neutralize HCl contained in the exhaust gas and involved in the production of dioxin to produce a stable compound K C/ or NaC/.

上記において、KOH,に2 CO3、K2CO3、K
HCO3、NaOH、Na2CO3およびNaHCOl
からなる群から選ばれたアルカリ性化合物の供給温度域
は、700〜400℃が好ましい。
In the above, KOH, 2 CO3, K2CO3, K
HCO3, NaOH, Na2CO3 and NaHCOl
The supply temperature range of the alkaline compound selected from the group consisting of is preferably 700 to 400°C.

その理由は、700℃を越えると、上記アルカリ性化合
物とSOXとの反応によって生成するNa25O1、K
2SO4などの硫酸塩が溶融し、ボイラチューブの表面
に付着してチューブの腐食を発生させたり、伝熱速度を
低下させたりするおそれがあり、400℃未満では、場
合によっては極微量のダイオキシンが発生するおそれが
あるからである。上記アルカリ性化合物とHClとの反
応は、たとえば次の通りである。
The reason for this is that when the temperature exceeds 700°C, Na25O1, K
Sulfates such as 2SO4 may melt and adhere to the surface of boiler tubes, causing corrosion of the tubes or reducing the heat transfer rate. This is because there is a possibility that this may occur. For example, the reaction between the alkaline compound and HCl is as follows.

KOH+HC1→KCl+H2O NaOH+HCl−NaC/+H20 に2 CO3+2HCl →2 K C/ + H20+ CO2Na2CO3+
2HCl →2 N a Cl +H20+CO2KHCO,+H
Cl →KCl+H20+C02 N a HCO3+ HCl →NaC/+H20+CO□ [作 用コ この発明によるダイオキシン発生の抑制方法では、ダイ
オキシンの発生に関与する物質であるHClを中和し、
ダイオキシンが発生するよりも高温の温度域である90
0〜300℃で。
KOH+HC1→KCl+H2O NaOH+HCl−NaC/+H20 2 CO3+2HCl →2 K C/ + H20+ CO2Na2CO3+
2HCl →2 N a Cl +H20+CO2KHCO,+H
Cl → KCl + H20 + C02 Na HCO3+ HCl → NaC/+H20 + CO
90, which is a temperature range higher than that where dioxins are generated.
At 0-300℃.

安定化合物であるKClまたはNaC/を生成させる。A stable compound KCl or NaC/ is produced.

その結果、ダイオキシンの発生が未然に防止せられ、ダ
イオキシンを含まない排ガスが大気中に放出される。
As a result, the generation of dioxin is prevented, and exhaust gas containing no dioxin is released into the atmosphere.

[実 施 例] つぎに、図示の実施例によりこの発明を具体的に説明す
る。
[Example] Next, the present invention will be specifically explained with reference to the illustrated example.

第1図にこの発明によるダイオキシン発生の抑制方法の
フローを示す。同図において、ごみ焼却炉(1)の頂部
出口から排出された排ガスに、焼却炉(1)の頂部出口
と電気集塵機(2)とを接続する排ガス排出路(6)に
おいて、供給装置(7)によりKOH,に2 CO3、
KHCO3、Na OHSN a 2 CO]およびN
aHCO,からなる群から選ばれたアルカリ性化合物を
1種または2種以上供給する。上記アルカリ性化合物の
供給は、粉体の状態でブロアからなる供給装置(7)を
用いて噴射することにより行うか、あるいは水溶液とし
てポンプからなる供給装置(7)を用いてスプレーする
ことにより行う。ついで排ガスは電気集塵機(2)で除
塵される。
FIG. 1 shows the flow of the method for suppressing dioxin generation according to the present invention. In the same figure, the exhaust gas discharged from the top outlet of the waste incinerator (1) is connected to the supply device (7) in the exhaust gas discharge path (6) connecting the top outlet of the incinerator (1) and the electrostatic precipitator (2). ) by KOH, to 2 CO3,
KHCO3, Na OHSN a 2 CO] and N
One or more alkaline compounds selected from the group consisting of aHCO are supplied. The alkaline compound is supplied in powder form by spraying it using a supply device (7) consisting of a blower, or by spraying it as an aqueous solution using a supply device (7) consisting of a pump. Then, the exhaust gas is removed by an electrostatic precipitator (2).

その後、排ガスは洗浄処理装置(3)で洗浄処理され、
誘引ファン(4)により処理排ガスが煙突(5)から大
気中へ放散される。
After that, the exhaust gas is cleaned in a cleaning treatment device (3),
The treated exhaust gas is dissipated into the atmosphere from the chimney (5) by the induced fan (4).

電気集塵機(2)としては、高温型のものが好ましい。As the electrostatic precipitator (2), a high temperature type is preferable.

その理由は、電気集塵機(2)内の温度が低いと、ここ
でS02が803.に酸化され、SO3によって電気集
塵機(2)が腐食されるおそれがあるからである。
The reason is that when the temperature inside the electrostatic precipitator (2) is low, S02 becomes 803. This is because there is a risk that the electrostatic precipitator (2) will be corroded by SO3.

この排ガス処理フローでは、ダイオキシンの発生に関与
する物質であるHClは、アルカリ性化合物によって9
00〜300℃の温度域で中和され、後処理の容易な安
定化合物であるKClまたはNaC/が生成する。その
結果、ダイオキシンの発生が未然に防止せられ、ダイオ
キシンを含まない排ガスが大気中に放出される。
In this exhaust gas treatment flow, HCl, a substance involved in the generation of dioxin, is converted to 99% by alkaline compounds.
KCl or NaC/, which is a stable compound that is neutralized in the temperature range of 00 to 300°C and is easily post-treated, is produced. As a result, the generation of dioxin is prevented, and exhaust gas containing no dioxin is released into the atmosphere.

なお、ダイオキシンは、高温になるごみ焼却炉内や焼却
炉と電気集塵機の間にある排ガス排出路からはほとんど
検出されなかった。上記アルカリ性化合物の供給を行な
わないときは、ダイオキシンは温度300℃付近から生
成し始め、それよりも低温で急増する。特に300℃未
満の温度となっている電気集塵機内でダイオキシンの生
成が顕著であり、電気集塵機がダイオキシン生成の温床
になっていると考えられる。
Furthermore, almost no dioxins were detected in the high-temperature garbage incinerator or in the exhaust gas exhaust path between the incinerator and the electrostatic precipitator. When the alkaline compound is not supplied, dioxins begin to be produced at a temperature around 300° C., and rapidly increase at lower temperatures. In particular, the production of dioxin is remarkable in the electrostatic precipitator, where the temperature is below 300°C, and it is thought that the electrostatic precipitator is a hotbed for the production of dioxin.

[発明の効果] この発明のダイオキシン発生の抑制方法によれば、ダイ
オキシンの発生に関与すると目されるHClを、アルカ
リ性化合物によって900〜300℃の温度域で中和し
て後処理の容易なK C/またはNaC/を生成するこ
とができる。
[Effects of the Invention] According to the method for suppressing dioxin generation of the present invention, HCl, which is thought to be involved in the generation of dioxin, is neutralized with an alkaline compound at a temperature range of 900 to 300°C, and HCl is easily post-treated. C/ or NaC/ can be produced.

その結果、ダイオキシンの発生を未然に防いで、ダイオ
キシンを含まない排ガスを大気中に放出することができ
る。
As a result, it is possible to prevent the generation of dioxin and to release exhaust gas that does not contain dioxin into the atmosphere.

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

第1図はこの発明の実施例を示す排ガス処理のフローシ
ート、第2図は従来の排ガス処理のフローシートである
。 (+) ・・・ごみ焼却炉、
FIG. 1 is a flow sheet for exhaust gas treatment showing an embodiment of the present invention, and FIG. 2 is a flow sheet for conventional exhaust gas treatment. (+) ...garbage incinerator,

Claims (1)

【特許請求の範囲】[Claims] 焼却炉からの排ガス排出路における900〜300℃の
温度域に、KOH、K_2CO_3、KHCO_3、N
aOH、Na_2CO_3およびNaHCO_3からな
る群から選ばれたアルカリ性化合物を1種または2種以
上供給し、排ガス中に含まれてダイオキシン生成に関与
するHClを中和して安定化合物であるKClまたはN
aClを生成させることを特徴とするダイオキシン発生
の抑制方法。
KOH, K_2CO_3, KHCO_3, N
One or more alkaline compounds selected from the group consisting of aOH, Na_2CO_3, and NaHCO_3 are supplied to neutralize HCl, which is contained in exhaust gas and participates in the production of dioxin, to produce stable compounds such as KCl or N.
A method for suppressing dioxin generation, the method comprising generating aCl.
JP2019972A 1990-01-29 1990-01-29 How to suppress dioxin generation Pending JPH03224618A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP2019972A JPH03224618A (en) 1990-01-29 1990-01-29 How to suppress dioxin generation

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP2019972A JPH03224618A (en) 1990-01-29 1990-01-29 How to suppress dioxin generation

Publications (1)

Publication Number Publication Date
JPH03224618A true JPH03224618A (en) 1991-10-03

Family

ID=12014112

Family Applications (1)

Application Number Title Priority Date Filing Date
JP2019972A Pending JPH03224618A (en) 1990-01-29 1990-01-29 How to suppress dioxin generation

Country Status (1)

Country Link
JP (1) JPH03224618A (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH11104439A (en) * 1997-10-01 1999-04-20 Asahi Glass Co Ltd Acid component remover and method for removing acidic components in gas
US5968467A (en) * 1995-09-22 1999-10-19 Kurita Water Industries, Co., Ltd. Dioxin formation preventative in incinerators and method for preventing the formation of dioxins

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS562829A (en) * 1979-06-19 1981-01-13 Toray Eng Co Ltd Removing method of hydrogen chloride from waste gas
JPS56105731A (en) * 1980-01-28 1981-08-22 Mitsubishi Heavy Ind Ltd Cleaning method of exhaust gas by powder spraying

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS562829A (en) * 1979-06-19 1981-01-13 Toray Eng Co Ltd Removing method of hydrogen chloride from waste gas
JPS56105731A (en) * 1980-01-28 1981-08-22 Mitsubishi Heavy Ind Ltd Cleaning method of exhaust gas by powder spraying

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US5968467A (en) * 1995-09-22 1999-10-19 Kurita Water Industries, Co., Ltd. Dioxin formation preventative in incinerators and method for preventing the formation of dioxins
JPH11104439A (en) * 1997-10-01 1999-04-20 Asahi Glass Co Ltd Acid component remover and method for removing acidic components in gas

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