JPH0369570B2 - - Google Patents
Info
- Publication number
- JPH0369570B2 JPH0369570B2 JP58093370A JP9337083A JPH0369570B2 JP H0369570 B2 JPH0369570 B2 JP H0369570B2 JP 58093370 A JP58093370 A JP 58093370A JP 9337083 A JP9337083 A JP 9337083A JP H0369570 B2 JPH0369570 B2 JP H0369570B2
- Authority
- JP
- Japan
- Prior art keywords
- exhaust gas
- absorbent
- soot
- nitrogen
- contact type
- 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
- 239000007789 gas Substances 0.000 claims description 57
- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims description 42
- 239000002250 absorbent Substances 0.000 claims description 12
- 230000002745 absorbent Effects 0.000 claims description 12
- 239000002253 acid Substances 0.000 claims description 11
- 239000000126 substance Substances 0.000 claims description 11
- 239000004071 soot Substances 0.000 claims description 10
- 230000002378 acidificating effect Effects 0.000 claims description 9
- 239000003054 catalyst Substances 0.000 claims description 7
- 238000002347 injection Methods 0.000 claims description 7
- 239000007924 injection Substances 0.000 claims description 7
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 claims description 6
- 229910001861 calcium hydroxide Inorganic materials 0.000 claims description 6
- 235000011116 calcium hydroxide Nutrition 0.000 claims description 6
- 239000000920 calcium hydroxide Substances 0.000 claims description 6
- 229910017464 nitrogen compound Inorganic materials 0.000 claims description 5
- 150000002830 nitrogen compounds Chemical class 0.000 claims description 5
- 239000011248 coating agent Substances 0.000 claims description 3
- 238000000576 coating method Methods 0.000 claims description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 10
- 229910021529 ammonia Inorganic materials 0.000 description 5
- 238000010586 diagram Methods 0.000 description 4
- 238000001816 cooling Methods 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical compound Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 2
- -1 NOx Chemical class 0.000 description 2
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 2
- 238000004140 cleaning Methods 0.000 description 2
- 229910001873 dinitrogen Inorganic materials 0.000 description 2
- 239000000428 dust Substances 0.000 description 2
- IXCSERBJSXMMFS-UHFFFAOYSA-N hydrogen chloride Substances Cl.Cl IXCSERBJSXMMFS-UHFFFAOYSA-N 0.000 description 2
- 229910000041 hydrogen chloride Inorganic materials 0.000 description 2
- 239000004677 Nylon Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 239000003795 chemical substances by application Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 239000012717 electrostatic precipitator Substances 0.000 description 1
- 239000012065 filter cake Substances 0.000 description 1
- 239000003365 glass fiber Substances 0.000 description 1
- 239000002440 industrial waste Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229920001778 nylon Polymers 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 229910052815 sulfur oxide Inorganic materials 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
- 238000009423 ventilation Methods 0.000 description 1
- 239000002699 waste material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
- 239000002759 woven fabric Substances 0.000 description 1
Landscapes
- Chimneys And Flues (AREA)
- Treating Waste Gases (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Description
【発明の詳細な説明】
本発明は、酸性ガス、窒素酸化物、煤じんを含
む排ガスの処置設備に関する。DETAILED DESCRIPTION OF THE INVENTION The present invention relates to equipment for treating exhaust gases containing acid gases, nitrogen oxides, and soot.
従来の都市ごみや産業廃棄物等の焼却炉からの
酸性ガス(例えば、HCl,SOx等)、窒素酸化物
(例えば、NOx等)、煤じん等を含む排ガスの処
理設備は、第1図に示す如く、煤じん捕集、酸性
ガス除去、窒素酸化物除去のための装置が全体プ
ラントの中で個々独立にあり、個々独立に制御さ
れているため、操作が複雑化し、処理性能は各装
置の条件変動が相互に影響し合つている。又、処
理後の反応生成物が各装置から排出されるため付
帯装置も複雑化している。第1図に於て、1は焼
却炉、2は脱硝剤噴射装置、3はガス冷却装置、
4は電気集じん装置、5は酸性ガス除去装置、6
は排風装置をそれぞれ示す。従つて、もし排ガス
処理設備が単一設備で行うことができれば、焼却
プラント全体が非常に簡素になり、維持管理しや
すくできることになる。 Conventional treatment equipment for exhaust gas containing acid gases (e.g., HCl, SOx, etc.), nitrogen oxides (e.g., NOx, etc.), soot, etc. from incinerators for municipal waste, industrial waste, etc. is shown in Figure 1. As shown in the figure, the devices for soot and dust collection, acid gas removal, and nitrogen oxide removal are located independently within the entire plant and are controlled independently, making operations complicated and processing performance depending on each device. Conditional fluctuations influence each other. Further, the auxiliary equipment is also complicated because the reaction products after treatment are discharged from each equipment. In Figure 1, 1 is an incinerator, 2 is a denitrification agent injection device, 3 is a gas cooling device,
4 is an electrostatic precipitator, 5 is an acid gas removal device, 6
indicates the ventilation device. Therefore, if the exhaust gas treatment equipment could be implemented in a single facility, the entire incineration plant would be extremely simple and easy to maintain and manage.
本発明は、かかる要求を満たすべき完成され
た。すなわち、本発明の目的は、酸性ガス、窒素
酸化物、煤じんを含む排ガスの処理設備に於て、
過フイルタ、該過フイルタ上に窒素酸化物還
元触媒をコーテイングして形成される一次過
層、該一次過層上に酸性ガス吸収剤を捕集して
形成される二次過層とを有し、上記の逆の順序
に排ガスを通過させる接触方式排ガス処理装置
と、該処理装置上流側排ガスダクト中にアンモニ
ア等の窒素化合物及び消石灰等の酸性ガス吸収剤
を噴射する薬品噴射装置とを有してなることを特
徴とする、酸性ガス、窒素酸化物、煤じんを含む
排ガスの処理設備を提供することにある。本発明
に依れば、焼却炉よりの排出物は接触方式排ガス
処理装置から完全乾式にて排出され、従つて付帯
装置は非常に簡素化されることになる。 The present invention has been completed to meet such requirements. That is, an object of the present invention is to provide a treatment facility for exhaust gas containing acid gases, nitrogen oxides, and soot.
A superfilter, a primary superlayer formed by coating a nitrogen oxide reduction catalyst on the superfilter, and a secondary superlayer formed by collecting an acidic gas absorbent on the primary superlayer. , a contact type exhaust gas treatment device that passes the exhaust gas in the reverse order of the above, and a chemical injection device that injects a nitrogen compound such as ammonia and an acid gas absorbent such as slaked lime into the exhaust gas duct on the upstream side of the treatment device. An object of the present invention is to provide processing equipment for exhaust gas containing acid gases, nitrogen oxides, and soot, which is characterized by: According to the present invention, the exhaust from the incinerator is discharged from the contact type exhaust gas treatment device in a completely dry manner, so that the ancillary equipment can be greatly simplified.
次に、本発明の設備を図面をもつて説明する。 Next, the equipment of the present invention will be explained with reference to the drawings.
第2図は本発明の設備を組み込んだ系統図であ
る。焼却炉11から出た排ガスは、ガス冷却装置
12へ導かれて排ガス処理に適した温度に降温さ
れた後、薬品噴射装置13からの薬品すなわち、
アンモニアなどの窒素化合物と消石灰などの酸性
ガス吸収剤、と共に接触方式排ガス処理装置14
へ導れる。排ガス処理装置14で処理された排出
物は、排風装置15に導かれ後、空気中に排出さ
れる。接触方式排ガス処理装置14は、第3図に
示すような過機構を持つている。すなわち、該
過機構は、過フイルタ21、該過フイルタ
上に窒素酸化物還元触媒をコーテイングして形成
される一次過層22、及び該一次過層上に酸
性ガス吸収剤を補集して形成される二次過層2
3から成つている。そして、ガス冷却装置12で
適温まで降温された排ガスは、薬品噴射装置13
からの薬品(例えば消石灰とアンモニア)ととも
に二次過層23側から排ガス処理装置14へ導
入され、過フイルタ21側から排出される。 FIG. 2 is a system diagram incorporating the equipment of the present invention. The exhaust gas emitted from the incinerator 11 is guided to the gas cooling device 12 and cooled to a temperature suitable for exhaust gas treatment, and then treated with chemicals from the chemical injection device 13, that is,
Contact type exhaust gas treatment device 14 together with nitrogen compounds such as ammonia and acidic gas absorbents such as slaked lime
I can lead you to. The exhaust gas treated by the exhaust gas treatment device 14 is led to the exhaust device 15 and then discharged into the air. The contact type exhaust gas treatment device 14 has a passing mechanism as shown in FIG. That is, the filter mechanism includes a filter filter 21, a primary filter layer 22 formed by coating the filter with a nitrogen oxide reduction catalyst, and a primary filter layer 22 formed by collecting an acidic gas absorbent on the primary filter layer. secondary superlayer 2
It consists of 3. Then, the exhaust gas whose temperature has been lowered to an appropriate temperature by the gas cooling device 12 is transferred to the chemical injection device 13.
It is introduced into the exhaust gas treatment device 14 from the secondary filter layer 23 side together with chemicals (for example, slaked lime and ammonia) from the filter, and is discharged from the filter filter 21 side.
過フイルタには、排ガス中の煤じん及び薬品
が捕集され、排ガスに対して過ケーキ層を形成
する。亜硫酸ガス塩化水素等の酸性ガスは薬品中
の消石灰等の吸収剤より吸収され、又NOx等の
窒素酸化物は過フイルタにコーテイングされて
いる還元触媒と薬品中のアンモニア等の窒素化合
物により還元無害化される構成となつている。
過フイルタは過層を保持するために設けられる
もので、使用温度により適宜選択することがで
き、例えば耐熱ナイロン、ガラス繊維等をその特
質に合わせて織布状やフエルト状の形態で用いる
ことができる。公知の還元触媒は予め過フイル
タ上に塗布しておくことができるが、該過フイ
ルタ上に微粉状の還元触媒を空気と混合物の状態
で送り込んで補集させ、これを繰返すことにより
一次過層を形成させることもできる。この一次
過層では、薬品噴射装置により供給されたアン
モニア等の窒素化合物が吸着され、排ガス中の窒
素酸化物と効率よく反応して無害な窒素ガスに還
元される。一方、触媒が活性を失つた場合には、
清掃し、再度プリコートを行うことによつて一次
過層を形成する。 The overfilter collects soot and chemicals in the exhaust gas, and forms an overcake layer against the exhaust gas. Acidic gases such as sulfur dioxide and hydrogen chloride are absorbed by absorbents such as slaked lime in chemicals, and nitrogen oxides such as NOx are reduced and rendered harmless by the reduction catalyst coated on the superfilter and nitrogen compounds such as ammonia in the chemicals. It is structured to be
The overfilter is provided to hold the overlayer, and can be selected as appropriate depending on the operating temperature.For example, heat-resistant nylon, glass fiber, etc. can be used in the form of woven fabric or felt according to its characteristics. can. A known reduction catalyst can be applied on a superfilter in advance, but by feeding a fine powder of reducing catalyst onto the superfilter in the form of a mixture with air and collecting it, and repeating this process, the primary superlayer can be applied. can also be formed. In this primary overlayer, nitrogen compounds such as ammonia supplied by the chemical injection device are adsorbed, efficiently react with nitrogen oxides in the exhaust gas, and are reduced to harmless nitrogen gas. On the other hand, if the catalyst loses its activity,
A primary overlayer is formed by cleaning and precoating again.
また、上記一次過層上には、酸性ガス除去を
行なうために、薬品噴射装置により供給される消
石灰等の吸収剤が捕集され吸収剤のフイルタケー
キ層、すなわち二次過層が形成される。そし
て、該二次過層では、吸収剤と酸性ガスとが効
率よく反応吸収される。さらには、排ガス中の煤
じんも同時にこの二次過層で過される。二次
過層は、圧損の上昇によりガスの通過が不能に
なるが、ある一定の圧損になつた段階で逆送風洗
浄等によつて再生できる。 Furthermore, in order to remove acidic gases, an absorbent such as slaked lime supplied by a chemical injection device is collected on the primary overlayer to form a filter cake layer of the absorbent, that is, a secondary overlayer. . In the secondary overlayer, the absorbent and the acidic gas are efficiently reacted and absorbed. Furthermore, soot and dust in the exhaust gas is also passed through this secondary layer. The secondary overlayer becomes impossible for gas to pass through due to an increase in pressure loss, but it can be regenerated by back air cleaning or the like when the pressure loss reaches a certain level.
上述の如く、本発明の設備によれば、酸性ガ
ス、窒素酸化物、煤じん等を含む排ガスは、先ず
二次過層で酸性ガス及び煤じんが吸収され、そ
して一次過層で窒素酸化物が無害な窒素ガスと
水蒸気に変換される。従つて、単一設備によつて
排ガスの処理が出来ることから産業上きわめて有
利な設備である。 As described above, according to the equipment of the present invention, exhaust gas containing acid gases, nitrogen oxides, soot, etc. is first absorbed in the secondary overlayer, and then nitrogen oxides are absorbed in the primary overlayer. is converted into harmless nitrogen gas and water vapor. Therefore, it is an industrially extremely advantageous facility because exhaust gas can be treated with a single facility.
第1図は従来の排ガス処理の系統図であり、第
2図は本発明による排ガス処理の系統図である。
又第3図は本発明の排ガス処理装置の過機構を
示す図である。
FIG. 1 is a system diagram of conventional exhaust gas treatment, and FIG. 2 is a system diagram of exhaust gas treatment according to the present invention.
FIG. 3 is a diagram showing the exhaust mechanism of the exhaust gas treatment apparatus of the present invention.
Claims (1)
の処理設備に於て、過フイルタ、該過フイル
タ上に窒素酸化物還元触媒をコーテイングして形
成される一次過層、該一次過層上に酸性ガス
吸収剤を捕集して形成される二次過層とを有
し、上記の逆の順序に排ガスを通過させる接触方
式排ガス処理装置と、該処理装置上流側排ガスダ
クト中にアンモニア等の窒素化合物及び消石灰等
の酸性ガス吸収剤を噴射する薬品噴射装置とを有
してなることを特徴とする、酸性ガス、窒素酸化
物、煤じんを含む排ガスの処理設備。1. In equipment for treating exhaust gas containing acid gases, nitrogen oxides, and soot, a superfilter, a primary superlayer formed by coating the superfilter with a nitrogen oxide reduction catalyst, and a A contact type exhaust gas treatment device has a secondary layer formed by collecting an acidic gas absorbent, and passes the exhaust gas in the reverse order of the above, and a contact type exhaust gas treatment device has a secondary layer formed by collecting an acidic gas absorbent, and a contact type exhaust gas treatment device that has a secondary layer formed by collecting an acidic gas absorbent and passes the exhaust gas in the reverse order of the above, and a A treatment facility for exhaust gas containing acid gases, nitrogen oxides, and soot, comprising a chemical injection device that injects an acid gas absorbent such as a nitrogen compound and slaked lime.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58093370A JPS59222212A (en) | 1983-05-28 | 1983-05-28 | Treating equipment of waste gas |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
JP58093370A JPS59222212A (en) | 1983-05-28 | 1983-05-28 | Treating equipment of waste gas |
Publications (2)
Publication Number | Publication Date |
---|---|
JPS59222212A JPS59222212A (en) | 1984-12-13 |
JPH0369570B2 true JPH0369570B2 (en) | 1991-11-01 |
Family
ID=14080406
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
JP58093370A Granted JPS59222212A (en) | 1983-05-28 | 1983-05-28 | Treating equipment of waste gas |
Country Status (1)
Country | Link |
---|---|
JP (1) | JPS59222212A (en) |
Families Citing this family (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPH01293123A (en) * | 1988-05-23 | 1989-11-27 | Mitsubishi Heavy Ind Ltd | Comprehensive treatment of waste combustion gas |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4916187A (en) * | 1972-06-07 | 1974-02-13 | ||
JPS4947242A (en) * | 1972-09-08 | 1974-05-07 | ||
JPS5162181A (en) * | 1974-11-29 | 1976-05-29 | Nippon Steel Corp | |
JPS55145520A (en) * | 1979-04-30 | 1980-11-13 | Babcock & Wilcox Co | Filter house and method for simultaneously removing nox and granular body from gas current |
-
1983
- 1983-05-28 JP JP58093370A patent/JPS59222212A/en active Granted
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS4916187A (en) * | 1972-06-07 | 1974-02-13 | ||
JPS4947242A (en) * | 1972-09-08 | 1974-05-07 | ||
JPS5162181A (en) * | 1974-11-29 | 1976-05-29 | Nippon Steel Corp | |
JPS55145520A (en) * | 1979-04-30 | 1980-11-13 | Babcock & Wilcox Co | Filter house and method for simultaneously removing nox and granular body from gas current |
Also Published As
Publication number | Publication date |
---|---|
JPS59222212A (en) | 1984-12-13 |
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