JP2742847B2 - High-performance comprehensive exhaust gas treatment method - Google Patents
High-performance comprehensive exhaust gas treatment methodInfo
- Publication number
- JP2742847B2 JP2742847B2 JP4083954A JP8395492A JP2742847B2 JP 2742847 B2 JP2742847 B2 JP 2742847B2 JP 4083954 A JP4083954 A JP 4083954A JP 8395492 A JP8395492 A JP 8395492A JP 2742847 B2 JP2742847 B2 JP 2742847B2
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- alkali
- gas
- heavy metals
- treatment
- 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.)
- Expired - Lifetime
Links
- 239000003513 alkali Substances 0.000 claims description 23
- 229910001385 heavy metal Inorganic materials 0.000 claims description 23
- 239000000428 dust Substances 0.000 claims description 21
- 239000007789 gas Substances 0.000 claims description 19
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 17
- 239000007788 liquid Substances 0.000 claims description 12
- 230000002378 acidificating Effects 0.000 claims description 8
- 238000010521 absorption reaction Methods 0.000 claims description 7
- 239000007787 solid Substances 0.000 claims description 7
- 239000004568 cement Substances 0.000 claims description 5
- 238000001784 detoxification Methods 0.000 claims description 5
- 238000000926 separation method Methods 0.000 claims description 5
- 238000004140 cleaning Methods 0.000 claims description 4
- 238000002347 injection Methods 0.000 claims description 4
- 239000007924 injection Substances 0.000 claims description 4
- 238000010438 heat treatment Methods 0.000 claims description 3
- HYHCSLBZRBJJCH-UHFFFAOYSA-M Sodium hydrosulfide Chemical compound [Na+].[SH-] HYHCSLBZRBJJCH-UHFFFAOYSA-M 0.000 claims description 2
- 238000005345 coagulation Methods 0.000 claims description 2
- 230000015271 coagulation Effects 0.000 claims description 2
- 238000009287 sand filtration Methods 0.000 claims description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims 7
- 239000003546 flue gas Substances 0.000 claims 3
- HGUFODBRKLSHSI-UHFFFAOYSA-N 2,3,7,8-tetrachloro-dibenzo-p-dioxin Chemical compound O1C2=CC(Cl)=C(Cl)C=C2OC2=C1C=C(Cl)C(Cl)=C2 HGUFODBRKLSHSI-UHFFFAOYSA-N 0.000 claims 1
- 239000002956 ash Substances 0.000 description 11
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N p-dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 11
- 239000002253 acid Substances 0.000 description 10
- AXCZMVOFGPJBDE-UHFFFAOYSA-L Calcium hydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 description 8
- 239000000920 calcium hydroxide Substances 0.000 description 8
- 235000011116 calcium hydroxide Nutrition 0.000 description 8
- 229910001861 calcium hydroxide Inorganic materials 0.000 description 8
- 238000003672 processing method Methods 0.000 description 8
- 239000000779 smoke Substances 0.000 description 6
- HEMHJVSKTPXQMS-UHFFFAOYSA-M sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 6
- 239000000126 substance Substances 0.000 description 6
- 150000002013 dioxins Chemical class 0.000 description 5
- 229910052753 mercury Inorganic materials 0.000 description 5
- OKTJSMMVPCPJKN-UHFFFAOYSA-N carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 4
- 238000002485 combustion reaction Methods 0.000 description 4
- QSHDDOUJBYECFT-UHFFFAOYSA-N mercury Chemical compound [Hg] QSHDDOUJBYECFT-UHFFFAOYSA-N 0.000 description 4
- 238000011084 recovery Methods 0.000 description 4
- 239000002918 waste heat Substances 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- 239000002002 slurry Substances 0.000 description 3
- VEXZGXHMUGYJMC-UHFFFAOYSA-N HCl Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 2
- 239000002440 industrial waste Substances 0.000 description 2
- 239000010813 municipal solid waste Substances 0.000 description 2
- 235000011121 sodium hydroxide Nutrition 0.000 description 2
- 238000007711 solidification Methods 0.000 description 2
- 239000007921 spray Substances 0.000 description 2
- 229910052815 sulfur oxide Inorganic materials 0.000 description 2
- 238000005406 washing Methods 0.000 description 2
- 229910052785 arsenic Inorganic materials 0.000 description 1
- 229910052793 cadmium Inorganic materials 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 239000010881 fly ash Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229910052698 phosphorus Inorganic materials 0.000 description 1
- 150000003839 salts Chemical class 0.000 description 1
- 239000010802 sludge Substances 0.000 description 1
- 239000011780 sodium chloride Substances 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- 238000004065 wastewater treatment Methods 0.000 description 1
- 229910052725 zinc Inorganic materials 0.000 description 1
Description
【0001】[0001]
【産業上の利用分野】本発明は、都市ごみや産業廃棄物
の焼却炉、工業用炉などから排出される排ガスの処理方
法に関し、さらに詳しくは、排ガス中に含まれる酸性ガ
ス、水銀などの重金属類およびダイオキシンのような有
害物質の除去に優れる処理方法に関する。BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a method for treating exhaust gas discharged from an incinerator of municipal solid waste and industrial waste, an industrial furnace, and the like. The present invention relates to a treatment method excellent in removing harmful substances such as heavy metals and dioxins.
【0002】[0002]
【従来技術および解決すべき課題】都市ごみや産業廃棄
物の焼却炉などからの排ガスには、ばい塵、酸性ガス
(HCl、SOx、HF等)、重金属(Hg、Cd、P
b、As、Zn等)およびダイオキシンのような有害物
質が含まれている。このような排ガスは、従来次のよう
な方法で処理されていた。2. Description of the Related Art Exhaust gas from incinerators for municipal solid waste and industrial waste includes dust, acid gases (HCl, SOx, HF, etc.), and heavy metals (Hg, Cd, P).
b, As, Zn, etc.) and harmful substances such as dioxins. Such exhaust gas has been conventionally treated by the following method.
【0003】まず第一の方法は、図2のフローチャート
に示すものである。焼却炉から出た排ガスは、廃熱回収
ボイラまたは水噴射冷却塔で冷却され、次に乾式電気集
塵器(EP)、湿式洗煙装置で処理される。この方法
は、ばい塵、酸性ガス、水銀などの重金属を高性能に除
去する方法として多く用いられている。しかしながら、
この方法では、乾式電気集塵器(EP)において200
℃以上、特に250℃以上でダイオキシンが再発生する
という問題があり、ダイオキシン除去を十分に行うこと
ができない。A first method is shown in a flowchart of FIG. The exhaust gas from the incinerator is cooled in a waste heat recovery boiler or a water jet cooling tower, and then treated in a dry electric dust collector (EP) and a wet smoke cleaning device. This method is widely used as a method for removing heavy metals such as dust, acid gas, and mercury with high efficiency. However,
In this method, a dry electric precipitator (EP) has 200
There is a problem that dioxin is regenerated at a temperature of at least 250C, especially at a temperature of at least 250C, and dioxin cannot be sufficiently removed.
【0004】第2の方法は、図3のフローチャートに示
すバグフィルタ方法である。排ガスは、廃熱回収ボイラ
または水噴射冷却塔で冷却され、次に調温塔またはスラ
リ噴霧塔を通される。スラリ噴霧塔では消石灰スラリが
導入される。続いて消石灰が導入されバグフィルタで処
理される。バグフィルタ捕集灰は、セメント固化され、
埋立て投棄される。この方法は、ダイオキシン排出低減
に関するガイドライン(平成2年12月)が出されて以
降、国内外において主流になってきている。しかしなが
ら、この方法では、水銀の除去が不安定であり、ダイオ
キシンの除去も飛灰質に左右され同様に不安定である。
さらに、この方法の最大の課題は、バグフィルタ捕集灰
の無害安定化である。この方法によると、捕集灰は重金
属固定剤を用いてセメント固化されており、未反応消
石灰や反応で生成した塩類の溶解流出、重金属溶出の
懸念、未反応物等によって捕集灰量が多くなる、等の
問題点がある。A second method is a bag filter method shown in the flowchart of FIG. The exhaust gas is cooled in a waste heat recovery boiler or a water jet cooling tower and then passed through a temperature control tower or a slurry spray tower. Slaked lime slurry is introduced in the slurry spray tower. Subsequently, slaked lime is introduced and processed by a bag filter. Bag filter ash is cement solidified,
Landfill dumping. This method has become mainstream in Japan and overseas since the guidelines on dioxin emission reduction (December 1990) were issued. However, in this method, the removal of mercury is unstable, and the removal of dioxin is also unstable depending on fly ash.
In addition, the greatest challenge of this method is the harmless stabilization of the bag filter ash. According to this method, the collected ash is cement-solidified using a heavy metal fixing agent. Problems.
【0005】第3の方法は、図4のフローチャートに示
すEDV方法(ばい塵・洗煙湿式同時処理方法)であ
る。排ガスは、廃熱回収ボイラまたは水噴射冷却塔で冷
却され、次に除塵塔、吸収塔で処理される。除塵塔では
消石灰が導入され、吸収塔では苛性ソーダが導入され
る。続いて湿式電気集塵器で処理される。この方法は、
酸性ガスや水銀の除去率はバグフィルタよりも優れてい
る。また、捕集灰は排水処理で無害安定化できという
点、および捕集灰量がバグフィルタの場合(セメント固
化したものとして)の約1/4に低減できるという点に
おいてもバグフィルタよりも優れている。しかしなが
ら、ばい塵除去については、バグフィルタよりも劣って
いる。また、ダイオキシンの除去については、バグフィ
ルタに近い性能が得られるが除去率は不安定である。A third method is the EDV method (simultaneous dust / smoke washing wet processing method) shown in the flowchart of FIG. The exhaust gas is cooled in a waste heat recovery boiler or a water jet cooling tower, and then processed in a dust removing tower and an absorption tower. Slaked lime is introduced in the dust removal tower, and caustic soda is introduced in the absorption tower. Subsequently, it is processed in a wet electric precipitator. This method
Acid gas and mercury removal rates are better than bag filters. Also, the collected ash is superior to the bag filter in that it can be harmlessly stabilized by wastewater treatment, and the amount of collected ash can be reduced to about 1/4 of that in the case of a bag filter (as cement solidified). ing. However, dust removal is inferior to bag filters. For the removal of dioxin, a performance close to that of a bag filter is obtained, but the removal rate is unstable.
【0006】第4の方法は、図5のフローチャートに示
すものである。この方法は、上記第2の方法にさらに湿
式洗煙処理を行うものである。この方法では、酸性ガス
や水銀の除去率が上記第2の方法に比べて向上する。し
かしながら、やはりバグフィルタ捕集灰がセメント固化
されるので、上記第2の方法と同様の問題点がある。A fourth method is shown in the flowchart of FIG. In this method, a wet smoke washing treatment is further performed in addition to the above second method. In this method, the removal rate of acid gas and mercury is improved as compared with the second method. However, since the collected ash from the bag filter is also cemented, there is a problem similar to the second method.
【0007】第5の方法は、図6のフローチャートに示
すものである。排ガスは、廃熱回収ボイラで冷却され、
次に乾式電気集塵器で処理され、湿式洗煙処理される。
続いてバグフィルタで処理される。バグフィルタの前流
で活性炭/消石灰が少量導入され、ダイオキシンの低減
を図っている。バグフィルタの前流で乾式電気集塵器処
理および湿式洗煙処理されるのは、ボイラからの火の粉
によってバグフィルタが焼損されることを防ぐためであ
る。この方法では、電気集塵器およびバグフィルタでの
捕集灰の処理が必要であり、湿式洗煙の排水処理が必要
であり、プロセスが極めて複雑である。The fifth method is shown in the flowchart of FIG. The exhaust gas is cooled by a waste heat recovery boiler,
Next, it is treated by a dry electric precipitator and is subjected to a wet smoke treatment.
Subsequently, it is processed by a bag filter. A small amount of activated carbon / slaked lime is introduced upstream of the bag filter to reduce dioxins. The dry electric precipitator treatment and the wet smoke treatment are performed in front of the bag filter in order to prevent the bag filter from being burned out by sparks from the boiler. This method requires the treatment of collected ash with an electrostatic precipitator and a bag filter, the treatment of drainage of wet smoke, and the process is extremely complicated.
【0008】本発明は、上記のような種々の問題を解決
し、排ガス中のばい塵、酸性ガス、重金属やダイオキシ
ンのような有害物質を効率良く除去しうる、排ガス処理
方法を提供することを目的とする。The present invention solves the above various problems and provides an exhaust gas treatment method capable of efficiently removing harmful substances such as dust, acid gas, heavy metals and dioxins in exhaust gas. Aim.
【0009】[0009]
【課題を解決するための手段】本発明の排ガス処理方法
は、上記目的を達成すべく工夫されたものであって、燃
焼排ガスを処理するにあたり、排ガスに水噴射(1) して
排ガス中の重金属を溶解せしめ除去し、重金属を溶解し
た酸性水を固液分離し、重金属を含む分離液体を無害化
処理し、ダイオキシンを含む分離固体を加熱処理法およ
び/またはセメント固化法によって無害化処理し、上記
水噴射後の排ガスにアルカリを添加し除塵塔(2) で処理
し、ガス吸収塔(3) で酸性ガスをアルカリ吸収処理し、
続いて排ガスにアルカリを添加してバグフィルタ(4) で
集塵処理し清浄排ガスを放出し、過剰アルカリを含むバ
グフィルタ捕集灰を前記除塵塔(2) に移送することを特
徴とするものである。Means for Solving the Problems The exhaust gas treatment method of the present invention has been devised to achieve the above-mentioned object. In treating the combustion exhaust gas, water is injected (1) into the exhaust gas and the exhaust gas is treated. Dissolve and remove heavy metals, dissolve heavy metals
Solid-liquid separation of the acidic water, detoxifying the separation liquid containing heavy metals
Heat treatment of the separated solid containing dioxin.
And / or detoxification by cement solidification method
Alkali is added to the exhaust gas after water injection , treated in the dust removal tower (2), and acid gas is alkali-absorbed in the gas absorption tower (3).
Subsequently, an alkali is added to the exhaust gas, the dust is removed by a bag filter (4), and the clean exhaust gas is released.The collected ash containing the excess alkali is transferred to the dust removal tower (2). It is.
【0010】以下、図1に基づいて、本発明を詳しく説
明する。Hereinafter, the present invention will be described in detail with reference to FIG.
【0011】本発明において、燃焼排ガスに水噴射(1)
すると、排ガス中には酸性ガスが多量に含まれているの
で、噴射された水はこれらガスを溶かし込みpH<2の
酸性になる。従って同時に排ガス中の重金属を溶解せし
め、排ガスよりこれを除去することができる。In the present invention, water injection into combustion exhaust gas (1)
Then, since a large amount of acidic gas is contained in the exhaust gas, the injected water dissolves these gases and becomes acidic at pH <2. Therefore, at the same time, heavy metals in the exhaust gas can be dissolved and removed from the exhaust gas.
【0012】この重金属を溶解させた酸性水は、以下の
ように廃液処理される。すなわち、まず酸性水を遠心分
離器、スクリュウブレス、フィルタプレス等で固液分離
する。重金属は液側に存在しており、これを従来の処理
方法(液体キレート法、水硫化ソーダ法、アルカリ凝沈
法、砂濾過、キレートなどの組み合わせ処理)によって
処理する。一方、汚泥(固体)側にはss状のダイオキ
シンが含まれているので、加熱処理法、セメント固化法
等によって処理する。The acidic water in which the heavy metal is dissolved is treated as a waste liquid as follows. That is, first, the acidic water is solid-liquid separated by a centrifuge, a screw brace, a filter press, or the like. The heavy metal exists on the liquid side, and is treated by a conventional treatment method (a combination treatment of a liquid chelate method, a sodium hydrosulfide method, an alkali coagulation method, sand filtration, chelate, and the like). On the other hand, since sludge (solid) contains ss-shaped dioxin, it is treated by a heat treatment method, a cement solidification method, or the like.
【0013】このように重金属が除去された排ガスにア
ルカリを添加し、なお含まれている酸性ガスを中和し塩
とすることによって除塵塔(2) で除去する。アルカリと
しては消石灰が一般的であるが、必ずしもこれに限定さ
れない。さらに酸性ガスを除去するためにガス吸収塔
(3) でアルカリ処理を行う。好ましいアルカリは苛性ソ
ーダであるが、必ずしもこれに限定されない。An alkali is added to the exhaust gas from which the heavy metals have been removed as described above, and the acid gas still contained is neutralized to form a salt, which is removed by the dust removing tower (2). Slaked lime is generally used as the alkali, but is not necessarily limited thereto. Gas absorption tower to further remove acidic gas
Perform alkali treatment in (3). The preferred alkali is, but is not necessarily limited to, caustic soda.
【0014】この排ガスにアルカリを添加し、バグフィ
ルタ(4) で集塵処理する。アルカリは通常、理論量の2
〜3当量添加する。好ましいアルカリは消石灰である。
なお、アルカリとともに活性炭を添加することもでき
る。本発明においては、過剰アルカリを含むバグフィル
タ捕集灰を前記除塵塔(2) に移送し、アルカリを有効に
再利用する。このことにより、アルカリの消費量を低減
するとともに、アルカリ分の処理問題を解決できる。ま
た、バグフィルタ捕集灰の埋立固形物量を、大幅に低減
することができる。An alkali is added to the exhaust gas, and the exhaust gas is collected by a bag filter (4). The alkali is usually 2 stoichiometric.
Add ~ 3 equivalents. The preferred alkali is slaked lime.
Activated carbon can be added together with the alkali. In the present invention, the bag filter ash containing excess alkali is transferred to the dust removal tower (2), and the alkali is effectively reused. This reduces the consumption of alkali and solves the problem of treating alkali. In addition, the amount of landfill solids in the collected ash from the bag filter can be significantly reduced.
【0015】[0015]
【実施例】図1の本願発明の処理方法と、図3のバグフ
ィルタ処理方法、図4のEDV処理方法との比較を行っ
た。EXAMPLE A comparison was made between the processing method of the present invention in FIG. 1, the bag filter processing method in FIG. 3, and the EDV processing method in FIG.
【0016】得られた燃焼排ガス処理の諸性能を表1に
示す。Table 1 shows various performances of the obtained combustion exhaust gas treatment.
【0017】[0017]
【表1】 このように本願発明の処理方法は、従来のバグフィルタ
処理方法およびEDV処理方法に比べ、ばい塵、酸性ガ
ス(HCl、SOx)、重金属(Hg)およびダイオキ
シンのような有害物質の除去に優れていた。特にダイオ
キシンの除去率については著しい効果があった。また、
消石灰消費量および埋立固形物量についても、従来のバ
グフィルタ処理方法に比べ、大幅に低減することができ
た。[Table 1] As described above, the treatment method of the present invention is superior to the conventional bag filter treatment method and EDV treatment method in removing harmful substances such as dust, acid gases (HCl, SOx), heavy metals (Hg), and dioxins. Was. In particular, there was a remarkable effect on the dioxin removal rate. Also,
Slaked lime consumption and landfill solids were also significantly reduced as compared to the conventional bag filter processing method.
【0018】[0018]
【発明の効果】本発明の燃焼排ガス処理方法は、上述の
ごとく、排ガスに水噴射(1) して排ガス中の重金属を溶
解せしめ除去し、次に排ガスにアルカリを添加し除塵塔
(2) で処理し、ガス吸収塔(3) で酸性ガスをアルカリ吸
収処理し、続いて排ガスにアルカリを添加してバグフィ
ルタ(4) で集塵処理し清浄排ガスを放出するので、従来
のバグフィルタ処理方法およびEDV処理方法に比べ、
ばい塵、酸性ガス、重金属およびダイオキシンのような
有害物質の除去に優れており、特にダイオキシンの除去
率については著しい効果がある。また、過剰アルカリを
含むバグフィルタ捕集灰を前記除塵塔(2) に移送し再利
用するので、従来のバグフィルタ処理方法に比べ、消石
灰消費量および埋立固形物量を、大幅に低減することが
できる。また、排ガスに水噴射して排ガス中の重金属を
溶解せしめ除去した後、重金属を溶解した酸性水を固液
分離し、重金属を含む分離液体を無害化処理し、ダイオ
キシンを含む分離固体を無害化処理するので、重金属や
ダイオキシンのような有害物質を全く系外へ放出するこ
となく処理することができる。 As described above, the method for treating combustion exhaust gas according to the present invention comprises the steps of: (1) injecting water into the exhaust gas to dissolve and remove heavy metals in the exhaust gas;
(2), acid gas is alkali-absorbed in the gas absorption tower (3), alkali is then added to the exhaust gas, and the dust is removed by the bag filter (4) to discharge the clean exhaust gas. Compared to the bag filter processing method and the EDV processing method,
It is excellent at removing harmful substances such as dust, acid gas, heavy metals and dioxin, and has a remarkable effect particularly on the dioxin removal rate. In addition, the bag filter collected ash containing excess alkali is transferred to the dust removal tower (2) and reused, so that the consumption of slaked lime and the amount of landfill solids can be significantly reduced as compared with the conventional bag filter processing method. it can. Water is also injected into the exhaust gas to remove heavy metals in the exhaust gas.
After dissolving and removing, the acidic water in which heavy metals are dissolved is solid-liquid
Separation and detoxification of the separation liquid containing heavy metals
Detoxification of separated solids containing xinx, so heavy metals and
Release of harmful substances such as dioxin out of the system
Can be processed without delay.
【図1】本発明の排ガス処理方法のフローチャートを示
す図である。FIG. 1 is a diagram showing a flowchart of an exhaust gas treatment method of the present invention.
【図2】従来の排ガス処理方法のフローチャートを示す
図である。FIG. 2 is a diagram showing a flowchart of a conventional exhaust gas treatment method.
【図3】従来の排ガス処理方法のフローチャートを示す
図である。FIG. 3 is a view showing a flowchart of a conventional exhaust gas treatment method.
【図4】従来の排ガス処理方法のフローチャートを示す
図である。FIG. 4 is a view showing a flowchart of a conventional exhaust gas treatment method.
【図5】従来の排ガス処理方法のフローチャートを示す
図である。FIG. 5 is a view showing a flowchart of a conventional exhaust gas treatment method.
【図6】従来の排ガス処理方法のフローチャートを示す
図である。FIG. 6 is a view showing a flowchart of a conventional exhaust gas treatment method.
(1) …水噴射 (2) …除塵塔 (3) …ガス吸収塔 (4) …バグフィルタ (1)… Water injection (2)… Dust removal tower (3)… Gas absorption tower (4)… Bag filter
Claims (2)
に水噴射(1) して排ガス中の重金属を溶解せしめ除去
し、重金属を溶解した酸性水を固液分離し、重金属を含
む分離液体を無害化処理し、ダイオキシンを含む分離固
体を加熱処理法および/またはセメント固化法によって
無害化処理し、上記水噴射後の排ガスにアルカリを添加
し除塵塔(2) で処理し、ガス吸収塔(3) で酸性ガスをア
ルカリ吸収処理し、続いて排ガスにアルカリを添加して
バグフィルタ(4) で集塵処理し清浄排ガスを放出し、過
剰アルカリを含むバグフィルタ捕集灰を前記除塵塔(2)
に移送することを特徴とする、排ガス処理方法。In treating flue gas, water is injected into the flue gas to dissolve and remove heavy metals in the flue gas, and the acidic water in which the heavy metals are dissolved is solid-liquid separated to contain the heavy metals.
Detoxify the separated liquid and remove the dioxin-containing separated solid.
By heat treatment and / or cement setting
Detoxification treatment, alkali is added to the exhaust gas after the above water injection, treated in the dust removal tower (2), alkali gas is absorbed in the gas absorption tower (3), and then alkali is added to the exhaust gas to make a bag. The filter (4) collects dust and discharges clean exhaust gas.The collected ash containing excess alkali is collected by the dust removal tower (2).
An exhaust gas treatment method, wherein the method is carried out.
法、水硫化ソーダ法、アルカリ凝沈法、砂濾過および/Method, sodium hydrosulfide method, alkali coagulation method, sand filtration and / or
またはキレート化によって無害化処理する請求項1記載Or the detoxification treatment by chelation.
の方法。the method of.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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JP4083954A JP2742847B2 (en) | 1992-04-06 | 1992-04-06 | High-performance comprehensive exhaust gas treatment method |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP4083954A JP2742847B2 (en) | 1992-04-06 | 1992-04-06 | High-performance comprehensive exhaust gas treatment method |
Publications (2)
Publication Number | Publication Date |
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JPH05285335A JPH05285335A (en) | 1993-11-02 |
JP2742847B2 true JP2742847B2 (en) | 1998-04-22 |
Family
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JP4083954A Expired - Lifetime JP2742847B2 (en) | 1992-04-06 | 1992-04-06 | High-performance comprehensive exhaust gas treatment method |
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JP (1) | JP2742847B2 (en) |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
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WO1998048924A1 (en) * | 1997-04-25 | 1998-11-05 | Nkk Corporation | Method of treating exhaust gas |
JP4585646B2 (en) * | 2000-03-13 | 2010-11-24 | 株式会社東和技研 | Purification method of combustion waste gas or industrial waste liquid and environmental pollutant purification device |
JP2008229416A (en) * | 2007-03-16 | 2008-10-02 | Mitsui Eng & Shipbuild Co Ltd | Apparatus and method for removing acidic gas contained in exhaust gas |
JP4936002B2 (en) * | 2007-10-15 | 2012-05-23 | 株式会社Ihi | Exhaust gas treatment method and exhaust gas treatment apparatus |
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JPS5065052A (en) * | 1973-10-16 | 1975-06-02 | ||
SE462369B (en) * | 1988-03-09 | 1990-06-18 | Flaekt Ab | PROCEDURES FOR CLEANING OF PROCESS GASES SUCH AS SMOKE GASES |
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