TWI731290B - Method and equipment for low-temperature catalyst denitration and dust removal using ceramic fiber filter tube - Google Patents
Method and equipment for low-temperature catalyst denitration and dust removal using ceramic fiber filter tube Download PDFInfo
- Publication number
- TWI731290B TWI731290B TW108101325A TW108101325A TWI731290B TW I731290 B TWI731290 B TW I731290B TW 108101325 A TW108101325 A TW 108101325A TW 108101325 A TW108101325 A TW 108101325A TW I731290 B TWI731290 B TW I731290B
- Authority
- TW
- Taiwan
- Prior art keywords
- catalyst
- gas
- oxide
- dust removal
- filter tube
- Prior art date
Links
Images
Landscapes
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Catalysts (AREA)
Abstract
一種應用陶纖濾管之低溫觸媒脫硝除塵的方法,適用於去除一廢氣中的粉塵及氮氧化物,並包含一混入氨基還原劑使該廢氣形成一待還原氣體的前處理步驟,及一將該待還原氣體輸入至少一附有觸媒的濾管的觸媒步驟。觸媒具有鈦氧化物、釩氧化物、鉬氧化物及鎢氧化物,使該待還原氣體通過該濾管時,形成一去除粉塵及氮氧化物的還原氣體。本發明亦提供一種應用陶纖濾管之低溫觸媒脫硝除塵的設備,包含一用以執行該前處理步驟的前處理單元,及一用以執行該觸媒步驟的觸媒單元。透過該應用陶纖濾管之低溫觸媒脫硝除塵的方法及設備,不須加熱該廢氣,即能以良好的脫硝效率處理該廢氣。 A low-temperature catalyst denitrification and dust removal method using a ceramic fiber filter tube is suitable for removing dust and nitrogen oxides in an exhaust gas, and includes a pretreatment step of mixing an amino reducing agent to make the exhaust gas form a gas to be reduced, and A catalyst step of inputting the gas to be reduced into at least one filter tube attached with a catalyst. The catalyst has titanium oxide, vanadium oxide, molybdenum oxide and tungsten oxide. When the gas to be reduced passes through the filter tube, a reducing gas for removing dust and nitrogen oxides is formed. The present invention also provides a low-temperature catalyst denitration and dust removal equipment using ceramic fiber filter tubes, which includes a pre-processing unit for performing the pre-processing step, and a catalyst unit for performing the catalyst step. Through the low-temperature catalyst denitrification and dust removal method and equipment using ceramic fiber filter tubes, the waste gas can be treated with good denitrification efficiency without heating the waste gas.
Description
本發明是有關於一種煙塵的處理方法及設備,特別是指一種用於處理廢氣的應用陶纖濾管之低溫觸媒脫硝除塵的方法及設備。 The present invention relates to a method and equipment for treating smoke and dust, in particular to a method and equipment for denitrification and dust removal by low-temperature catalyst using ceramic fiber filter tubes for waste gas treatment.
工廠中的鍋爐在經過燃燒作業後,將產生溫度高達200℃至1400℃的廢氣,為能妥善應用廢氣中的熱能,常對於廢氣進行熱回收,並將所回收的熱能用以發電。進行熱回收後的廢氣溫度通常將降至200℃以下,需要再去除其中的粉塵及氮氧化物後才能進行排放,以避免造成環境與空氣汙染。 The boiler in the factory will produce exhaust gas with a temperature as high as 200°C to 1400°C after the combustion operation. In order to properly use the heat energy in the exhaust gas, the exhaust gas is often recovered and the recovered heat energy is used to generate electricity. The temperature of the exhaust gas after heat recovery will usually drop below 200°C, and the dust and nitrogen oxides in it must be removed before it can be discharged to avoid environmental and air pollution.
參閱圖1與圖2,一種現有的廢氣除塵方法,包含一個以一加熱器81將該廢氣加熱到350℃的加熱步驟91、一個以一靜電式除塵器82吸附粉塵的靜電除塵步驟92、一個在一蜂巢式觸媒反應裝置83內加入氨型藥劑並以觸媒去除氮氧化物的還原脫硝步驟93、一個在一脫硫器84中於該廢氣裡加入水及石灰石而脫除硫元素的脫硫步驟94,及一將該廢氣導入一個不織布過濾器85,使該
廢氣中的粉塵滯留於該不織布過濾器85中,且將該廢氣輸入到一排氣管86並排放的過濾步驟95。
1 and 2, an existing exhaust gas dust removal method includes a
須補充說明的是,在該脫硫步驟94中,常使用半乾式的方法,即以水霧及石灰石混合該廢氣而去除硫元素,另外也常使用濕式的方法,即以石灰石及水洗滌該廢氣而達到脫硫。由於在該還原脫硝步驟93中,所使用的觸媒要在溫度達250℃至350℃的環境中才能有良好的脫硝效率,故須在該加熱步驟91中加熱該廢氣。除了需要消耗額外的能源,加熱後的該廢氣更有可能在該過濾步驟95中,使該不織布過濾器85容易因高溫而損壞,需要加以改善。
It should be added that in the
因此,本發明之目的,即在提供一種不需要加熱廢氣,即可有良好的脫硝效率的應用陶纖濾管之低溫觸媒脫硝除塵的方法。 Therefore, the object of the present invention is to provide a low-temperature catalyst denitrification and dust removal method using ceramic fiber filter tubes without heating the exhaust gas and having good denitration efficiency.
於是,本發明應用陶纖濾管之低溫觸媒脫硝除塵的方法,適用於去除一廢氣中的粉塵及氮氧化物,並包含一在該廢氣中混合氨基還原劑,使該廢氣形成一待還原氣體的前處理步驟,及一個在一反應溫度下將該待還原氣體輸入至少一個附有觸媒的濾管的觸媒步驟。觸媒具有鈦氧化物、釩氧化物、鉬氧化物及鎢氧化物,使該待還原氣體通過該至少一個濾管時,形成一去除粉塵及氮氧化 物的還原氣體。 Therefore, the present invention uses the low-temperature catalyst denitrification and dust removal method of the ceramic fiber filter tube, which is suitable for removing dust and nitrogen oxides in an exhaust gas, and includes a mixture of an amino reducing agent in the exhaust gas, so that the exhaust gas is formed into a waste gas. A pretreatment step of reducing gas, and a catalyst step in which the gas to be reduced is fed into at least one filter tube with catalyst at a reaction temperature. The catalyst has titanium oxide, vanadium oxide, molybdenum oxide and tungsten oxide. When the gas to be reduced passes through the at least one filter tube, it forms a dust removal and nitrogen oxidation The reducing gas of the substance.
另外,本發明之另一目的,在於提供一種用以執行上述應用陶纖濾管之低溫觸媒脫硝除塵的方法的應用陶纖濾管之低溫觸媒脫硝除塵的設備。 In addition, another object of the present invention is to provide a low-temperature catalyst denitrification and dust removal device using ceramic fiber filter tubes to implement the above-mentioned low-temperature catalyst denitration and dust removal method using ceramic fiber filter tubes.
於是,本發明應用陶纖濾管之低溫觸媒脫硝除塵的設備,包含一用以執行該前處理步驟的前處理單元,及一連通該前處理單元並用以執行該觸媒步驟的觸媒單元。該觸媒單元包括至少一個適用於供該待還原氣體通過的濾管,及一附著於該至少一個濾管的觸媒,該觸媒具有鈦氧化物、釩氧化物、鉬氧化物及鎢氧化物,使該待還原氣體通過該至少一個濾管時,形成該還原氣體。 Therefore, the low-temperature catalyst denitrification and dust removal equipment using ceramic fiber filter tubes of the present invention includes a pre-processing unit for performing the pre-processing step, and a catalyst connected to the pre-processing unit and used to perform the catalyst step unit. The catalyst unit includes at least one filter tube suitable for passing the gas to be reduced, and a catalyst attached to the at least one filter tube. The catalyst has titanium oxide, vanadium oxide, molybdenum oxide, and tungsten oxide. When the gas to be reduced passes through the at least one filter tube, the reducing gas is formed.
本發明之功效在於:不需要再次加熱經過熱回收的該廢氣,該觸媒單元即能以良好的效率去除該廢氣中的粉塵及氮氧化物,能降低能源的耗費,並能避免該觸媒單元受到高溫而損壞,可節省設備成本。 The effect of the present invention is that the catalyst unit can remove dust and nitrogen oxides in the exhaust gas with good efficiency without reheating the exhaust gas after heat recovery, can reduce energy consumption, and can avoid the catalyst The unit is damaged by high temperature, which can save equipment cost.
11:脫硫步驟 11: Desulfurization step
12:前處理步驟 12: Pre-processing steps
13:觸媒步驟 13: Catalyst step
2:脫硫單元 2: Desulfurization unit
3:前處理單元 3: Pre-processing unit
4:觸媒單元 4: Catalyst unit
41:濾管 41: Filter tube
411:開口 411: open
42:觸媒 42: Catalyst
5:燃燒單元 5: Combustion unit
6:排氣單元 6: Exhaust unit
本發明之其他的特徵及功效,將於參照圖式的實施方式中清楚地呈現,其中:圖1是一示意圖,說明一種現有的廢氣除塵設備;圖2是一方法流程圖,說明一種現有的廢氣除塵方法; 圖3是一方法流程圖,說明本發明應用陶纖濾管之低溫觸媒脫硝除塵的方法的一方法實施例;圖4是一示意圖,說明本發明應用陶纖濾管之低溫觸媒脫硝除塵的設備的一裝置實施例;及圖5是一示意圖,說明該裝置實施例的一觸媒單元。 Other features and effects of the present invention will be clearly presented in the embodiments with reference to the drawings, in which: Figure 1 is a schematic diagram illustrating an existing exhaust gas dust removal equipment; Figure 2 is a method flow chart illustrating an existing Exhaust gas dust removal method; Fig. 3 is a method flow chart illustrating a method embodiment of the low-temperature catalyst denitration and dust removal method using ceramic fiber filter tubes of the present invention; Figure 4 is a schematic diagram illustrating the low-temperature catalyst denitrification method of the present invention using ceramic fiber filter tubes A device embodiment of the nitrate dust removal equipment; and FIG. 5 is a schematic diagram illustrating a catalyst unit of the device embodiment.
參閱圖3,本發明應用陶纖濾管之低溫觸媒脫硝除塵的方法的一方法實施例,適用於去除一廢氣中的粉塵及氮氧化物,並包含一在該廢氣中混合脫硫劑並使該廢氣形成一已脫硫氣體的脫硫步驟11、一在該已脫硫氣體中混合氨基還原劑並使該已脫硫氣體形成一待還原氣體的前處理步驟12,及一個在一反應溫度下將該待還原氣體輸入多個附有觸媒的濾管,並使該待還原氣體形成一去除粉塵及氮氧化物的還原氣體的觸媒步驟13。
Referring to FIG. 3, a method embodiment of the low-temperature catalyst denitration and dust removal method using ceramic fiber filter tubes of the present invention is suitable for removing dust and nitrogen oxides in an exhaust gas, and includes a desulfurization agent mixed in the exhaust gas And make the exhaust gas form a
參閱圖3與圖4,本發明應用陶纖濾管之低溫觸媒脫硝除塵的方法,能以本發明應用陶纖濾管之低溫觸媒脫硝除塵的設備的一裝置實施例執行,該裝置實施例包含一用以執行該脫硫步驟11的脫硫單元2、一連通該脫硫單元2並用以執行該前處理步驟12的前處理單元3,及一連通該前處理單元3並用以執行該觸媒步驟13的觸媒單元4。
Referring to Figures 3 and 4, the low-temperature catalyst denitrification and dust removal method of the present invention using ceramic fiber filter tubes can be implemented by an apparatus embodiment of the low-temperature catalyst denitrification and dust removal equipment using ceramic fiber filter tubes of the present invention. The device embodiment includes a
該脫硫單元2適用於連通一用以產生該廢氣的燃燒單元5,在該脫硫步驟11中,該脫硫單元2適用於在該廢氣中混合脫硫劑,以脫硫劑吸收該廢氣中的硫氧化物(SOx),使該廢氣形成該已脫硫氣體。在本實施例中,脫硫劑是選自於石灰石、白雲石、消石灰,或鈣基吸收劑。
The
該前處理單元3適用於在該已脫硫氣體中混合氨基還原劑,使該已脫硫氣體形成該待還原氣體。在本實施例中,氨基還原劑是選自於氨氣、尿素,或氨水。
The
參閱圖3至圖5,該觸媒單元4適用於連通一用以排放該還原氣體的排氣單元6,並包括多個間隔設置且適用於供該待還原氣體通過的濾管41,及一附著於該等濾管41的觸媒42。每一個濾管41具有多個相互交織且可耐受高溫的陶瓷纖維(圖未示),並形成有一朝向該排氣單元6的開口411。在本實施例中,該觸媒42具有鈦氧化物、釩氧化物、鉬氧化物、鎢氧化物、鎂氧化物及氟化合物,並以含浸法使該觸媒42附著於該等濾管41上,可使該待還原氣體中有毒的氮氧化物(NOx)與氨(NH3)進行反應,並將氮氧化物還原成無毒的氮氣(N2)和水(H2O)。
3 to 5, the
在實際運作時,該待還原氣體將沿圖5中箭頭所示的方向通過該等濾管41,並自該等開口411向該排氣單元6流動,在此過程中,粉塵將被該等濾管41濾除,氮氧化物則被該觸媒42催化
而反應成為氮氣,使得該待還原氣體形成符合環保排放標準的該還原氣體。在本實施例中,該還原氣體為氮氣與水氣。除了粒徑較大的粉塵(懸浮微粒,Particulate Matter,簡稱為PM),該等濾管41也能同時有效地去除PM2.5等級的粉塵(粒徑小於或等於2.5微米的懸浮微粒),在本實施例中,該等濾管41能夠去除80%至99.9%的懸浮微粒,及50%至95%的PM2.5等級的粉塵。
In actual operation, the gas to be reduced will pass through the
在該觸媒步驟13中,該反應溫度為150℃至250℃。其中,在150℃至200℃時,該觸媒42的脫硝效率為70%至95%,在200℃至225℃時,該觸媒42的脫硝效率可達90%至99%,在225℃至250℃時,該觸媒42的脫硝效率則可達95%至100%。由於該觸媒42的釩氧化物在催化氮氧化物的同時,也會將該待還原氣體中的二氧化硫(SO2)氧化成三氧化硫(SO3),在低於320℃的環境中,三氧化硫容易與氨進行反應,而產生具有黏性的硫酸氫銨(NH4HSO4),硫酸氫銨黏附在該觸媒單元4上時將遮蔽該觸媒單元4,並使該觸媒42失去活性,進而影響該觸媒步驟13中去除氮氧化物的效率。因此,須在該脫硫步驟11中盡量去除該廢氣中的硫氧化物,以避免產生硫酸氫銨。
In the
在本實施例中,以該觸媒42的總重量為100wt%計,該觸媒42具有重量百分比為80wt%至90wt%的鈦氧化物、重量百分比為1wt%至7wt%的釩氧化物、重量百分比為1wt%至10wt%的
鉬氧化物、重量百分比為1wt%至10wt%的鎢氧化物、重量百分比為0.1wt%至5wt%的鎂氧化物,及重量百分比為0.1wt%至5wt%的氟化合物。然而,在實際應用中,該觸媒42也可以只具有鈦氧化物、釩氧化物、鉬氧化物及鎢氧化物,並能依執行需求適當調配該觸媒42的組成物比例,而不以上述比例為限,同樣能達到去除氮氧化物的功效。
In this embodiment, based on the total weight of the
須特別說明的是,本發明應用陶纖濾管之低溫觸媒脫硝除塵的方法也可以僅包含該前處理步驟12及該觸媒步驟13,在該觸媒步驟13中,也可以將該待還原氣體輸入一附有該觸媒42的濾管41。而本發明應用陶纖濾管之低溫觸媒脫硝除塵的設備也可以僅包含該前處理單元3及該觸媒單元4,該觸媒單元4也可以只包括一濾管41及一觸媒42,同樣能去除該廢氣中的粉塵及氮氧化物。
It should be particularly noted that the low-temperature catalyst denitration and dust removal method using ceramic fiber filter tubes of the present invention can also only include the
綜上所述,本發明應用陶纖濾管之低溫觸媒脫硝除塵的方法及設備藉由能在150℃至250℃的環境裡進行脫硝反應的該觸媒42,並配合以陶瓷纖維製成的該等濾管41,不需要再次加熱經過熱回收的該廢氣,該觸媒單元4即能以良好的效率去除該廢氣中的粉塵及氮氧化物。能降低能源的耗費,並能避免該觸媒單元4受到高溫而損壞,可節省設備成本,故確實能達成本發明之目的。
In summary, the low-temperature catalyst denitration and dust removal method and equipment of the present invention using ceramic fiber filter tubes uses the
惟以上所述者,僅為本發明之實施例而已,當不能以此限定本發明實施之範圍,凡是依本發明申請專利範圍及專利說明 書內容所作之簡單的等效變化與修飾,皆仍屬本發明專利涵蓋之範圍內。 However, the above are only examples of the present invention, and should not be used to limit the scope of implementation of the present invention. Any application for patents and patent descriptions according to the present invention Simple equivalent changes and modifications made to the content of the book are still within the scope of the patent for the present invention.
11:脫硫步驟 11: Desulfurization step
12:前處理步驟 12: Pre-processing steps
13:觸媒步驟 13: Catalyst step
Claims (8)
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW108101325A TWI731290B (en) | 2019-01-14 | 2019-01-14 | Method and equipment for low-temperature catalyst denitration and dust removal using ceramic fiber filter tube |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
TW108101325A TWI731290B (en) | 2019-01-14 | 2019-01-14 | Method and equipment for low-temperature catalyst denitration and dust removal using ceramic fiber filter tube |
Publications (2)
Publication Number | Publication Date |
---|---|
TW202026058A TW202026058A (en) | 2020-07-16 |
TWI731290B true TWI731290B (en) | 2021-06-21 |
Family
ID=73004929
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
TW108101325A TWI731290B (en) | 2019-01-14 | 2019-01-14 | Method and equipment for low-temperature catalyst denitration and dust removal using ceramic fiber filter tube |
Country Status (1)
Country | Link |
---|---|
TW (1) | TWI731290B (en) |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TW201630651A (en) * | 2014-11-07 | 2016-09-01 | Mitsubishi Heavy Ind Ltd | Exhaust gas treatment method and denitrification/so3 reduction apparatus |
TW201632252A (en) * | 2014-11-07 | 2016-09-16 | 三菱日立電力系統股份有限公司 | Flue gas treatment system and flue gas treatment method |
TW201714664A (en) * | 2015-06-24 | 2017-05-01 | 三菱日立電力系統股份有限公司 | Denitration equipment and denitration method |
-
2019
- 2019-01-14 TW TW108101325A patent/TWI731290B/en active
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
TW201630651A (en) * | 2014-11-07 | 2016-09-01 | Mitsubishi Heavy Ind Ltd | Exhaust gas treatment method and denitrification/so3 reduction apparatus |
TW201632252A (en) * | 2014-11-07 | 2016-09-16 | 三菱日立電力系統股份有限公司 | Flue gas treatment system and flue gas treatment method |
TWI599396B (en) * | 2014-11-07 | 2017-09-21 | 三菱日立電力系統股份有限公司 | Flue gas treatment system and flue gas treatment method |
TW201714664A (en) * | 2015-06-24 | 2017-05-01 | 三菱日立電力系統股份有限公司 | Denitration equipment and denitration method |
Also Published As
Publication number | Publication date |
---|---|
TW202026058A (en) | 2020-07-16 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
JP5051977B2 (en) | Device for removing trace harmful substances in exhaust gas and operation method thereof | |
CN206508772U (en) | Cat ceramic fiber filter pipe flue gas desulfurization and dedusting denitrification integrated device | |
CN102459833B (en) | Combustion flue gas NOX treatment | |
JP4988864B2 (en) | Use of SO2 from flue gas in ammonia acid cleaning | |
CN101518718B (en) | Functional filter felt for eliminating harmful constituents of fume, preparation method and application method thereof | |
CN107376639B (en) | Hazardous waste incineration flue gas purification method | |
CN103990362A (en) | Method and device for removing sulfur, nitre and mercury in smoke | |
JP2010058067A (en) | Method for regenerating denitration catalyst, unit for regenerating denitration catalyst and apparatus for treating exhaust gas by using the unit | |
WO2022262243A1 (en) | Flue gas ammonia removal method | |
WO1997001388A1 (en) | Flue-gas treatment system | |
JP2005028210A (en) | Exhaust gas treatment system | |
WO2018143000A1 (en) | Exhaust-gas treatment system and exhaust-gas treatment method | |
CN104607015A (en) | Multi-pollutant co-purification method and multi-pollutant co-purification system for sintering flue gas | |
CN103768903A (en) | Regeneration flue gas denitration process for FCC apparatus | |
CN210278800U (en) | Low-temperature catalyst denitration dust removal equipment with pottery fine filter tube | |
CN114452814A (en) | Dry denitration process | |
JPH08108042A (en) | Desulfurization and denitrification of flue gas,method and device for removal of carbon dioxide and catalyst and absorbent used therein | |
JP2015203416A (en) | Exhaust gas after-treatment system and method for exhaust gas after-treatment | |
CN108458351B (en) | Solid waste incineration flue gas purification treatment method and system thereof | |
TWI731290B (en) | Method and equipment for low-temperature catalyst denitration and dust removal using ceramic fiber filter tube | |
JP2008030017A (en) | Removal apparatus of trace harmful substance in exhaust gas and its operation method | |
CN107830739A (en) | Sintering flue gas full-flow purification system and method thereof | |
TWM578189U (en) | Low temperature catalyst denitration and dust removal equipment with ceramic fiber filter tube | |
TWI641693B (en) | Coke oven flue gas dedusting, desulfurization and denitration integrated method and equipment | |
CN111514752A (en) | Method and equipment for denitration and dust removal by using low-temperature catalyst |