TWI474859B - An electro-catalytic honeycomb for controlling exhaust emissions - Google Patents
An electro-catalytic honeycomb for controlling exhaust emissions Download PDFInfo
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- TWI474859B TWI474859B TW101135008A TW101135008A TWI474859B TW I474859 B TWI474859 B TW I474859B TW 101135008 A TW101135008 A TW 101135008A TW 101135008 A TW101135008 A TW 101135008A TW I474859 B TWI474859 B TW I474859B
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- exhaust gas
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- MWUXSHHQAYIFBG-UHFFFAOYSA-N nitrogen oxide Inorganic materials O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 claims description 77
- 239000007789 gas Substances 0.000 claims description 61
- 229910044991 metal oxide Inorganic materials 0.000 claims description 35
- 238000002485 combustion reaction Methods 0.000 claims description 31
- 239000001301 oxygen Substances 0.000 claims description 24
- 229910052760 oxygen Inorganic materials 0.000 claims description 24
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 23
- 239000003054 catalyst Substances 0.000 claims description 23
- 150000004706 metal oxides Chemical class 0.000 claims description 20
- 239000007787 solid Substances 0.000 claims description 18
- -1 fluorite structure metal oxides Chemical class 0.000 claims description 16
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims description 14
- 239000010411 electrocatalyst Substances 0.000 claims description 11
- 239000000463 material Substances 0.000 claims description 9
- 238000007254 oxidation reaction Methods 0.000 claims description 9
- 239000011148 porous material Substances 0.000 claims description 9
- 238000000354 decomposition reaction Methods 0.000 claims description 8
- 229910052751 metal Inorganic materials 0.000 claims description 8
- 239000002184 metal Substances 0.000 claims description 8
- 230000003647 oxidation Effects 0.000 claims description 8
- 230000001590 oxidative effect Effects 0.000 claims description 8
- WUKWITHWXAAZEY-UHFFFAOYSA-L calcium difluoride Chemical group [F-].[F-].[Ca+2] WUKWITHWXAAZEY-UHFFFAOYSA-L 0.000 claims description 3
- 150000001722 carbon compounds Chemical class 0.000 claims description 3
- MYMOFIZGZYHOMD-UHFFFAOYSA-N Dioxygen Chemical compound O=O MYMOFIZGZYHOMD-UHFFFAOYSA-N 0.000 claims description 2
- 229910045601 alloy Inorganic materials 0.000 claims description 2
- 239000000956 alloy Substances 0.000 claims description 2
- 229910001873 dinitrogen Inorganic materials 0.000 claims description 2
- 229910001882 dioxygen Inorganic materials 0.000 claims description 2
- KZNMRPQBBZBTSW-UHFFFAOYSA-N [Au]=O Chemical compound [Au]=O KZNMRPQBBZBTSW-UHFFFAOYSA-N 0.000 claims 1
- 229910001922 gold oxide Inorganic materials 0.000 claims 1
- 150000002739 metals Chemical group 0.000 claims 1
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 19
- 229910002091 carbon monoxide Inorganic materials 0.000 description 19
- 150000002430 hydrocarbons Chemical class 0.000 description 17
- 229930195733 hydrocarbon Natural products 0.000 description 16
- 238000006243 chemical reaction Methods 0.000 description 13
- CURLTUGMZLYLDI-UHFFFAOYSA-N Carbon dioxide Chemical compound O=C=O CURLTUGMZLYLDI-UHFFFAOYSA-N 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 229910052757 nitrogen Inorganic materials 0.000 description 6
- SIWVEOZUMHYXCS-UHFFFAOYSA-N oxo(oxoyttriooxy)yttrium Chemical compound O=[Y]O[Y]=O SIWVEOZUMHYXCS-UHFFFAOYSA-N 0.000 description 6
- 241000282414 Homo sapiens Species 0.000 description 5
- PXHVJJICTQNCMI-UHFFFAOYSA-N Nickel Chemical compound [Ni] PXHVJJICTQNCMI-UHFFFAOYSA-N 0.000 description 5
- 239000008187 granular material Substances 0.000 description 5
- 239000013618 particulate matter Substances 0.000 description 5
- SMSXCXUNHPRBNZ-UHFFFAOYSA-N [Cu]=O.[Mn].[La] Chemical compound [Cu]=O.[Mn].[La] SMSXCXUNHPRBNZ-UHFFFAOYSA-N 0.000 description 4
- LNTHITQWFMADLM-UHFFFAOYSA-N gallic acid Chemical compound OC(=O)C1=CC(O)=C(O)C(O)=C1 LNTHITQWFMADLM-UHFFFAOYSA-N 0.000 description 4
- 150000003278 haem Chemical class 0.000 description 4
- MGWGWNFMUOTEHG-UHFFFAOYSA-N 4-(3,5-dimethylphenyl)-1,3-thiazol-2-amine Chemical compound CC1=CC(C)=CC(C=2N=C(N)SC=2)=C1 MGWGWNFMUOTEHG-UHFFFAOYSA-N 0.000 description 3
- HVBGSGQTRMKOEZ-UHFFFAOYSA-N [Cu]=O.[Co].[Sm] Chemical compound [Cu]=O.[Co].[Sm] HVBGSGQTRMKOEZ-UHFFFAOYSA-N 0.000 description 3
- 238000003915 air pollution Methods 0.000 description 3
- 229910002092 carbon dioxide Inorganic materials 0.000 description 3
- 239000001569 carbon dioxide Substances 0.000 description 3
- 229910000420 cerium oxide Inorganic materials 0.000 description 3
- 150000001875 compounds Chemical class 0.000 description 3
- 230000006378 damage Effects 0.000 description 3
- 239000003344 environmental pollutant Substances 0.000 description 3
- JCXJVPUVTGWSNB-UHFFFAOYSA-N nitrogen dioxide Inorganic materials O=[N]=O JCXJVPUVTGWSNB-UHFFFAOYSA-N 0.000 description 3
- BMMGVYCKOGBVEV-UHFFFAOYSA-N oxo(oxoceriooxy)cerium Chemical compound [Ce]=O.O=[Ce]=O BMMGVYCKOGBVEV-UHFFFAOYSA-N 0.000 description 3
- 231100000719 pollutant Toxicity 0.000 description 3
- 238000006722 reduction reaction Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 229910001233 yttria-stabilized zirconia Inorganic materials 0.000 description 3
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- KDLHZDBZIXYQEI-UHFFFAOYSA-N Palladium Chemical compound [Pd] KDLHZDBZIXYQEI-UHFFFAOYSA-N 0.000 description 2
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 description 2
- 238000003916 acid precipitation Methods 0.000 description 2
- 230000002950 deficient Effects 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 230000036541 health Effects 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- VUZPPFZMUPKLLV-UHFFFAOYSA-N methane;hydrate Chemical compound C.O VUZPPFZMUPKLLV-UHFFFAOYSA-N 0.000 description 2
- 229910052759 nickel Inorganic materials 0.000 description 2
- 230000001737 promoting effect Effects 0.000 description 2
- 230000009467 reduction Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 101100046636 Arabidopsis thaliana TOP6A gene Proteins 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 229910052684 Cerium Inorganic materials 0.000 description 1
- OTMSDBZUPAUEDD-UHFFFAOYSA-N Ethane Chemical compound CC OTMSDBZUPAUEDD-UHFFFAOYSA-N 0.000 description 1
- 102000001554 Hemoglobins Human genes 0.000 description 1
- 108010054147 Hemoglobins Proteins 0.000 description 1
- 206010028980 Neoplasm Diseases 0.000 description 1
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 1
- IOVCWXUNBOPUCH-UHFFFAOYSA-N Nitrous acid Chemical compound ON=O IOVCWXUNBOPUCH-UHFFFAOYSA-N 0.000 description 1
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 description 1
- JTCFNJXQEFODHE-UHFFFAOYSA-N [Ca].[Ti] Chemical compound [Ca].[Ti] JTCFNJXQEFODHE-UHFFFAOYSA-N 0.000 description 1
- QRNJEQUSSIEXDE-UHFFFAOYSA-N [Cu]=O.[Co+2].[Sm+3].[Ag+].[O-2].[Y+3] Chemical compound [Cu]=O.[Co+2].[Sm+3].[Ag+].[O-2].[Y+3] QRNJEQUSSIEXDE-UHFFFAOYSA-N 0.000 description 1
- YMVZSICZWDQCMV-UHFFFAOYSA-N [O-2].[Mn+2].[Sr+2].[La+3] Chemical compound [O-2].[Mn+2].[Sr+2].[La+3] YMVZSICZWDQCMV-UHFFFAOYSA-N 0.000 description 1
- XHCLAFWTIXFWPH-UHFFFAOYSA-N [O-2].[O-2].[O-2].[O-2].[O-2].[V+5].[V+5] Chemical compound [O-2].[O-2].[O-2].[O-2].[O-2].[V+5].[V+5] XHCLAFWTIXFWPH-UHFFFAOYSA-N 0.000 description 1
- 229910052788 barium Inorganic materials 0.000 description 1
- DSAJWYNOEDNPEQ-UHFFFAOYSA-N barium atom Chemical compound [Ba] DSAJWYNOEDNPEQ-UHFFFAOYSA-N 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 201000011510 cancer Diseases 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 230000003197 catalytic effect Effects 0.000 description 1
- 238000010531 catalytic reduction reaction Methods 0.000 description 1
- 210000003169 central nervous system Anatomy 0.000 description 1
- CETPSERCERDGAM-UHFFFAOYSA-N ceric oxide Chemical compound O=[Ce]=O CETPSERCERDGAM-UHFFFAOYSA-N 0.000 description 1
- GWXLDORMOJMVQZ-UHFFFAOYSA-N cerium Chemical compound [Ce] GWXLDORMOJMVQZ-UHFFFAOYSA-N 0.000 description 1
- 229910000422 cerium(IV) oxide Inorganic materials 0.000 description 1
- 239000011195 cermet Substances 0.000 description 1
- 239000011248 coating agent Substances 0.000 description 1
- 238000000576 coating method Methods 0.000 description 1
- 230000008602 contraction Effects 0.000 description 1
- 230000006866 deterioration Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000010436 fluorite Substances 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 229940074391 gallic acid Drugs 0.000 description 1
- 235000004515 gallic acid Nutrition 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229910052746 lanthanum Inorganic materials 0.000 description 1
- FZLIPJUXYLNCLC-UHFFFAOYSA-N lanthanum atom Chemical compound [La] FZLIPJUXYLNCLC-UHFFFAOYSA-N 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910000480 nickel oxide Inorganic materials 0.000 description 1
- 229910002119 nickel–yttria stabilized zirconia Inorganic materials 0.000 description 1
- 229910017604 nitric acid Inorganic materials 0.000 description 1
- GNRSAWUEBMWBQH-UHFFFAOYSA-N oxonickel Chemical compound [Ni]=O GNRSAWUEBMWBQH-UHFFFAOYSA-N 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 239000008188 pellet Substances 0.000 description 1
- 239000011941 photocatalyst Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 239000001294 propane Substances 0.000 description 1
- QQONPFPTGQHPMA-UHFFFAOYSA-N propylene Natural products CC=C QQONPFPTGQHPMA-UHFFFAOYSA-N 0.000 description 1
- 125000004805 propylene group Chemical group [H]C([H])([H])C([H])([*:1])C([H])([H])[*:2] 0.000 description 1
- 230000029058 respiratory gaseous exchange Effects 0.000 description 1
- 210000002345 respiratory system Anatomy 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 229910002076 stabilized zirconia Inorganic materials 0.000 description 1
- 229910052712 strontium Inorganic materials 0.000 description 1
- CIOAGBVUUVVLOB-UHFFFAOYSA-N strontium atom Chemical compound [Sr] CIOAGBVUUVVLOB-UHFFFAOYSA-N 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 229910052727 yttrium Inorganic materials 0.000 description 1
- VWQVUPCCIRVNHF-UHFFFAOYSA-N yttrium atom Chemical compound [Y] VWQVUPCCIRVNHF-UHFFFAOYSA-N 0.000 description 1
- RUDFQVOCFDJEEF-UHFFFAOYSA-N yttrium(III) oxide Inorganic materials [O-2].[O-2].[O-2].[Y+3].[Y+3] RUDFQVOCFDJEEF-UHFFFAOYSA-N 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/34—Chemical or biological purification of waste gases
- B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
- B01D53/86—Catalytic processes
- B01D53/8643—Removing mixtures of carbon monoxide or hydrocarbons and nitrogen oxides
- B01D53/8646—Simultaneous elimination of the components
- B01D53/865—Simultaneous elimination of the components characterised by a specific catalyst
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J35/00—Catalysts, in general, characterised by their form or physical properties
- B01J35/50—Catalysts, in general, characterised by their form or physical properties characterised by their shape or configuration
- B01J35/56—Foraminous structures having flow-through passages or channels, e.g. grids or three-dimensional monoliths
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/40—Nitrogen compounds
- B01D2257/404—Nitrogen oxides other than dinitrogen oxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/50—Carbon oxides
- B01D2257/502—Carbon monoxide
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/70—Organic compounds not provided for in groups B01D2257/00 - B01D2257/602
- B01D2257/702—Hydrocarbons
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02T—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO TRANSPORTATION
- Y02T10/00—Road transport of goods or passengers
- Y02T10/10—Internal combustion engine [ICE] based vehicles
- Y02T10/12—Improving ICE efficiencies
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Environmental & Geological Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Analytical Chemistry (AREA)
- Biomedical Technology (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Health & Medical Sciences (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Exhaust Gas After Treatment (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
- Processes For Solid Components From Exhaust (AREA)
- Catalysts (AREA)
Description
本發明有關一種電觸媒蜂巢,尤指一種控制廢氣排放並有效分解氮氧化物及氧化一氧化碳、碳氫化合物以及粒狀物的電觸媒蜂巢。The invention relates to an electric catalyst honeycomb, in particular to an electric catalyst honeycomb which controls exhaust gas emission and effectively decomposes nitrogen oxides and oxidizes carbon monoxide, hydrocarbons and particles.
清新與潔淨的空氣是人類生活的基本要件之一,呼吸乾淨無污染的空氣能確保人類穩定健康地生存。科技的卓越提升,雖帶動經濟的迅速發展,然而,來自於交通工具及各式林立工廠的廢氣排放,卻也導致空氣遭受污染,而對人類生活的空氣品質影響甚鉅。其中,重工廠和機動車輛為眾多污染物質的主要來源。Fresh and clean air is one of the basic elements of human life. Breathing clean and pollution-free air ensures that human beings can survive in a stable and healthy manner. Although the technological excellence has promoted the rapid development of the economy, the emissions from vehicles and various forestry factories have also caused air pollution, which has a great impact on the air quality of human life. Among them, heavy factories and motor vehicles are the main sources of many pollutants.
以機動車輛為例,雖然機動車輛排放標準不斷提高,但由於車輛數量不斷增加,車輛排放廢氣所帶來的空氣污染問題,仍然與日俱增。一般來說,機動車輛引擎的運轉為將不同形式燃料經由汽缸內燃而釋放出熱能,並產生傳輸動力;惟在燃燒過程中,產生的廢氣通常包含氮氧化物(NOx )、一氧化碳(CO)、碳氫化合物(hydrocarbons,HCs)、粒狀物(particulate matter,PM)等有害污染物,該等物質不僅會形成光化學煙霧(photochemical smog),更會破壞臭氧、加劇溫室效應的惡化及引致酸雨等,進而破壞生態環境,危害人體健康。Taking motor vehicles as an example, although the emission standards for motor vehicles continue to increase, the number of vehicles is increasing, and the problem of air pollution caused by vehicle emissions is still increasing. Generally speaking, the operation of a motor vehicle engine is to release different types of fuel through the internal combustion of the cylinder to release heat energy and generate transmission power; however, in the combustion process, the generated exhaust gas usually contains nitrogen oxides (NO x ) and carbon monoxide (CO). ), hydrocarbons (HCs), particulate matter (PM) and other harmful pollutants, which not only form photochemical smog, but also destroy ozone and aggravate the deterioration of the greenhouse effect. It causes acid rain, etc., which destroys the ecological environment and endangers human health.
其中,一氧化碳來自引擎的不完全燃燒,其與血紅素結合成一氧化碳血紅素(COHb)的能力為血紅素與氧結合成氧合血紅素(HbO2 )的300倍,故空氣中一氧化碳濃度過高時,將影響血紅素輸送氧氣的功能;氮氧化物則來自氮氣與氧氣的化合,主要以一氧化氮(NO)或二氧化氮(NO2 )的形式排出,而與碳氫化合物經紫外線照射後發生反應形成有毒的光化學煙霧,具有特殊氣味、刺激眼睛、傷害植物,並使大氣能見度降低,且氮氧化物與空氣中的水反應形成硝酸及亞硝酸,其為酸雨的成分;碳氫化合物在低濃度時即會刺激呼吸系統,若濃度提高,則會對中樞神經系統的運作機能產生影響;而粒狀物亦會危害人體的健康,甚至於引起癌症的發生。Among them, carbon monoxide comes from incomplete combustion of the engine, and its ability to combine with heme to form carbon monoxide hemoglobin (COHb) is 300 times that of heme and oxygen combined with oxygenated heme (HbO 2 ), so the concentration of carbon monoxide in the air is too high. When it will affect the function of heme transporting oxygen; nitrogen oxides come from the combination of nitrogen and oxygen, mainly in the form of nitric oxide (NO) or nitrogen dioxide (NO 2 ), and with hydrocarbons irradiated by ultraviolet light The reaction then forms toxic photochemical smog, has a special odor, irritates the eyes, damages plants, and reduces atmospheric visibility, and nitrogen oxides react with water in the air to form nitric acid and nitrous acid, which are components of acid rain; hydrocarbon Compounds can irritate the respiratory system at low concentrations. If the concentration is increased, it will affect the functioning of the central nervous system. Granules can also harm the health of the human body and even cause cancer.
因此,不管我國或是歐盟、日本、美國等先進國家,均已訂定益趨嚴格的廢氣排放標準(如美規BIN5以及歐規EURO 6),針對氮氧化物、一氧化碳、碳氫化合物和粒狀物等廢氣的排放訂定標準,藉以控制並減少有害氣體的排放,同時鼓勵業者製造、研發、引進使用最新污染防制技術的產品。Therefore, regardless of China or the EU, Japan, the United States and other advanced countries, we have set stricter emission standards (such as US BIN5 and Euro 6) for nitrogen oxides, carbon monoxide, hydrocarbons and pellets. Emissions such as emissions are set to control and reduce harmful emissions, while encouraging manufacturers to manufacture, develop, and introduce products that use the latest pollution prevention technologies.
如美國發明專利公告第5401372號的「Electrochemical catalytic reduction cell for the reduction of NOx in an O2 -containing exhaust emission」揭露一種單獨去除氮氧化物的裝置,為利用電化學觸媒還原反應,配合五氧化二釩(vanadium pentaoxide,V2 O5 )觸媒催化輔助氮氧化物轉化為氮氣。然而,上述的該裝置須額外加上電源供應,致使該裝置中的一電化學電池運作,如此不僅耗費能源且無法達成同時去除廢氣中多種有害氣體的目標。"Electrochemical catalytic reduction cell for the reduction of NO x in an O 2 - containing exhaust emission", as disclosed in U.S. Patent Publication No. 5,401,372, discloses a device for removing nitrogen oxides alone, in order to utilize an electrochemical catalyst reduction reaction, in combination with five Vanadium pentaoxide (V 2 O 5 ) catalyst catalyzes the conversion of nitrogen oxides to nitrogen. However, the device described above requires an additional power supply to cause an electrochemical cell in the device to operate, which is not only energy consuming but also unable to achieve the goal of simultaneously removing various harmful gases in the exhaust gas.
故於美國發明專利申請第13362247號的「Electrocatalytic Tube of Electrochemical-Catalytic Converter for Exhaust Emissions Control」,其揭露一種控制廢氣排放的電觸媒管,該電觸媒管可堆疊成一蜂巢狀結構,形成一先進的蜂巢式電化學觸媒轉換器,而可用以淨化廢氣中的氮氧化物、一氧化碳、碳氫化合物和粒狀物,其中該氮氧化物被分解成氮氣與氧氣,該一氧化碳、該碳氫化合物及該粒狀物被氧化成二氧化碳和水。因此,該電觸媒管在不需耗費額外能源及還原性氣體之下,即可淨化多種污染物。The "Electrocatalytic Tube of Electrochemical-Catalytic Converter for Exhaust Emissions Control" of the U.S. Patent Application No. 13362247 discloses an electrocatalyst tube for controlling exhaust gas emissions, which can be stacked into a honeycomb structure to form a An advanced honeycomb electrochemical converter can be used to purify nitrogen oxides, carbon monoxide, hydrocarbons and particulates in the exhaust gas, wherein the nitrogen oxides are decomposed into nitrogen and oxygen, the carbon monoxide, the hydrocarbon The compound and the granule are oxidized to carbon dioxide and water. Therefore, the electric catalyst tube can purify various pollutants without using extra energy and reducing gas.
然而,上述該蜂巢式電化學觸媒轉換器,其一半的通道必需密封以形成該電觸媒管,如此,與現有車輛的蜂巢式觸媒轉換器相比,不僅減少反應區域,亦增加製造成本,因此,其仍有改善的空間。However, in the honeycomb electrochemical converter described above, half of the channels must be sealed to form the dielectric catalyst tube, thus reducing the reaction area and manufacturing more than the honeycomb catalytic converter of the existing vehicle. Cost, therefore, there is still room for improvement.
本發明的主要目的,在於解決習知蜂巢式電化學觸媒轉換器,具有較小的反應區域及較高的製造成本的問題。The main object of the present invention is to solve the problem of a conventional honeycomb electrochemical converter having a small reaction area and a high manufacturing cost.
為達上述目的,本發明提供一種控制廢氣排放的電觸媒蜂巢,用以淨化一富氧燃燒廢氣,該電觸媒蜂巢包含有一蜂巢結構體、一固態氧化物層以及一陰極層。該蜂巢結構體包含一陽極以及複數個氣流通道,該陽極形成該蜂巢結構體的一骨架,由一第一多孔性材質組成,並具有一還原性環境,該氣流通道形成於該骨架內而供該富氧燃燒廢氣流通;該固態氧化物層包覆該陽極的一表面,並為一緻密微結構,且具有一面對該氣流通道的管壁;該陰極層附著於該管壁上,該固態氧化物層位於該陽極與該陰極層之間,該陰極層則由一第二多孔性材質組成,被用以淨化該富氧燃燒廢氣而具有一氧化性環境。To achieve the above object, the present invention provides an electric catalyst honeycomb for controlling exhaust gas emissions for purifying an oxy-combustion combustion exhaust gas, the electric catalyst honeycomb comprising a honeycomb structure, a solid oxide layer and a cathode layer. The honeycomb structure comprises an anode and a plurality of gas flow channels, the anode forming a skeleton of the honeycomb structure, consisting of a first porous material and having a reducing environment, wherein the gas flow channel is formed in the skeleton Providing the oxy-combustion exhaust gas to circulate; the solid oxide layer coating a surface of the anode and having a uniform dense structure and having a tube wall facing the gas flow passage; the cathode layer is attached to the tube wall The solid oxide layer is located between the anode and the cathode layer, and the cathode layer is composed of a second porous material, which is used to purify the oxy-combusted combustion exhaust gas to have an oxidizing environment.
其中,該還原性環境與該氧化性環境令該陽極及該陰極層之間產生一電動勢,驅動促進該富氧燃燒廢氣中的氮氧化物於該陰極層進行一分解反應而形成氮氣與氧氣。Wherein, the reducing environment and the oxidizing environment generate an electromotive force between the anode and the cathode layer to drive nitrogen oxides in the oxyfuel combustion exhaust gas to undergo a decomposition reaction in the cathode layer to form nitrogen gas and oxygen gas.
綜上所述,在本發明中,藉由該電觸媒蜂巢的所有該氣流通道皆用於與該富氧燃燒廢氣進行反應,且該電觸媒蜂巢相較習知的蜂巢式電化學觸媒轉換器更容易製作,據此,本發明與習知的蜂巢式電化學觸媒轉換器相較,具有較大的反應區域以及較低的製造成本。In summary, in the present invention, all of the gas flow passages of the electric catalyst honeycomb are used for reacting with the oxy-combustion exhaust gas, and the electric catalyst honeycomb is compared with the conventional honeycomb electrochemical touch. The media converter is easier to manufacture, and accordingly, the present invention has a larger reaction area and a lower manufacturing cost than conventional honeycomb electrochemical converters.
有關本發明的詳細說明及技術內容,現就配合圖式說明如下:The detailed description and technical content of the present invention will now be described as follows:
請搭配參閱『圖1』至『圖3』所示,『圖1』為本發明第一實施例的外觀立體示意圖,『圖2』為本發明第一實施例的剖面示意圖,『圖3』為本發明第一實施例的剖面局部放大示意圖,本發明為一種控制廢氣排放的電觸媒蜂巢,用以淨化一富氧燃燒廢氣,該富氧燃燒廢氣可包含氮氧化物(NOx )、一氧化碳(CO)、碳氫化合物(hydrocarbons,HCs)及粒狀物(particulate matter,PM),該電觸媒蜂巢包含有一蜂巢結構體10、一固態氧化物層20以及一陰極層30。該蜂巢結構體10包含有一陽極11以及複數個氣流通道12,該陽極11形成該蜂巢結構體10的一骨架,在此實施例中,該陽極11由一第一多孔性材質組成,而具有大量的孔洞,該陽極11的材質可為金屬及螢石結構金屬氧化物組成之陶金、螢石結構金屬氧化物 (fluorite metal oxides)、鈣鈦礦結構金屬氧化物(perovskite metal oxides)、加金屬的螢石結構金屬氧化物或加金屬的鈣鈦礦結構金屬氧化物,例如:鎳(Ni)及氧化釔穩定化氧化鋯(yttria-stabilized zirconia,YSZ)陶金(Ni–YSZ cermet);該氣流通道12則形成於該骨架內,貫穿該蜂巢結構體10相對的兩端,供該富氧燃燒廢氣流通。1 is a schematic perspective view of the first embodiment of the present invention, and FIG. 2 is a schematic cross-sectional view of the first embodiment of the present invention, and FIG. 3 is a schematic view of the first embodiment of the present invention. A partially enlarged schematic cross-sectional view of a first embodiment of the present invention, the present invention is an electric catalyst honeycomb for controlling exhaust gas emissions for purifying an oxy-combustion combustion exhaust gas, which may include nitrogen oxides (NO x ), Carbon monoxide (CO), hydrocarbons (HCs), and particulate matter (PM), the electrocatalyst honeycomb comprises a honeycomb structure 10, a solid oxide layer 20, and a cathode layer 30. The honeycomb structure 10 includes an anode 11 and a plurality of gas flow channels 12, and the anode 11 forms a skeleton of the honeycomb structure 10. In this embodiment, the anode 11 is composed of a first porous material and has A large number of holes, the material of the anode 11 may be metal and fluorite structure metal oxides of ceramsite, fluorite metal oxides, perovskite metal oxides, plus a metal fluorite structure metal oxide or a metal-added perovskite structure metal oxide such as nickel (Ni) and yttria-stabilized zirconia (YSZ) pottery (Ni-YSZ cermet); The air flow passage 12 is formed in the frame and penetrates opposite ends of the honeycomb structure 10 for circulating the oxygen-enriched combustion exhaust gas.
該固態氧化物層20包覆該陽極11的一表面,而完全密封該陽極11,令該陽極11內可為一還原性環境,該固態氧化物層20並具有一面對該氣流通道12的管壁21,且該固態氧化物層20的結構為一緻密微結構,並可以具有氧離子傳導性,其材質可為螢石結構金屬氧化物或鈣鈦礦結構金屬氧化物;例如:螢石結構的氧化釔穩定化氧化鋯、穩定化氧化鋯、螢石結構的氧化釓摻雜氧化鈰(gadolinia-doped ceria,GDC)、摻雜氧化鈰、鈣鈦礦結構的鍶及鎂摻雜鎵酸鑭(strontium/magnesium-doped lanthanum gallate,LSGM)、摻雜鎵酸鑭。The solid oxide layer 20 covers a surface of the anode 11 to completely seal the anode 11 so that the anode 11 can be a reducing environment. The solid oxide layer 20 has a side of the gas flow channel 12 The wall 21, and the solid oxide layer 20 has a uniform dense structure and may have oxygen ion conductivity, and the material thereof may be a fluorite structure metal oxide or a perovskite structure metal oxide; for example, fluorite Structure of yttria-stabilized zirconia, stabilized zirconia, fluorite-structured yttrium-doped ceria (GDC), doped yttria, perovskite-structured yttrium and magnesium-doped gallic acid Stro (strontium/magnesium-doped lanthanum gallate, LSGM), doped with barium gallate.
該陰極層30附著於該管壁21上,令該固態氧化物層20位於該陽極11與該陰極層30之間,在此實施例中,該陰極層30由一第二多孔性材質組成,而具有大量的孔洞,例如可為鈣鈦礦結構金屬氧化物、螢石結構金屬氧化物、加金屬的鈣鈦礦結構金屬氧化物或加金屬的螢石結構金屬氧化物,例如:鈣鈦礦結構的鑭鍶鈷銅氧化物、鑭鍶錳銅氧化物、鑭鍶鈷銅氧化物及氧化釓摻雜氧化鈰的組合、鑭鍶錳銅氧化物及氧化釓摻雜氧化鈰的組合、加銀的鑭鍶鈷銅氧化物、加銀的鑭鍶錳銅氧化物、加銀的鑭鍶鈷銅氧化物及氧化釓摻雜氧化鈰的組合、加銀的鑭鍶錳銅氧化物及氧化釓摻雜氧化鈰的組合。The cathode layer 30 is attached to the tube wall 21 such that the solid oxide layer 20 is located between the anode 11 and the cathode layer 30. In this embodiment, the cathode layer 30 is composed of a second porous material. , and has a large number of pores, such as a perovskite structure metal oxide, a fluorite structure metal oxide, a metal-added perovskite structure metal oxide or a metal-added fluorite structure metal oxide, for example: calcium titanium a combination of samarium cobalt copper oxide, lanthanum manganese copper oxide, samarium cobalt copper oxide and yttrium oxide doped yttrium oxide, a combination of lanthanum manganese copper oxide and yttrium oxide doped yttrium oxide Silver samarium cobalt copper oxide, silver-added lanthanum manganese copper oxide, silver-added samarium cobalt copper oxide and yttria-doped yttrium oxide combination, silver-added lanthanum manganese copper oxide and cerium oxide A combination of doped cerium oxide.
在本發明中,該陽極11在初步製作時包含一金屬氧化物,該金屬氧化物於製成該陽極11時,先經過一使用一還原性氣體的處理而還原為一金屬,例如由氧化鎳還原為鎳;或者,亦可將該金屬氧化物還原為一缺氧的金屬氧化物(oxygen-deficient metal oxide),以形成該陽極11之該還原性環境。另外,於完全密封該陽極11之前,可先將一氧化碳或碳氫化合物添加於該陽極11,如於該陽極11經由孔洞擴散(pore diffusion)通入甲烷、乙烷、丙稀或丙烷等,以形成附著於該陽極11的孔洞之碳物種,以加強形成該陽極11之該還原性環境。又另外,於完全密封該陽極11之前,可抽取該陽極11的孔洞中之氣體以使其氣體壓力降至一大氣壓以下或降至真空,據此,而可以減少該蜂巢結構體10於廢氣處理操作上因熱脹冷縮所可能產生的結構傷害。In the present invention, the anode 11 comprises a metal oxide during preliminary preparation, and the metal oxide is reduced to a metal by a treatment using a reducing gas when the anode 11 is formed, for example, by nickel oxide. Reduction to nickel; or, the metal oxide may be reduced to an oxygen-deficient metal oxide to form the reducing environment of the anode 11. In addition, carbon monoxide or hydrocarbon may be added to the anode 11 before the anode 11 is completely sealed, for example, the anode 11 is allowed to pass through a pore diffusion, such as methane, ethane, propylene or propane. A carbon species attached to the pores of the anode 11 is formed to enhance the reducing environment in which the anode 11 is formed. In addition, before completely sealing the anode 11, the gas in the hole of the anode 11 can be extracted to lower the gas pressure to below atmospheric pressure or to a vacuum, thereby reducing the honeycomb structure 10 in the exhaust gas treatment. Structural damage that may occur due to thermal expansion and contraction.
請搭配參閱『圖4』所示,為本發明第二實施例的剖面局部放大示意圖,第二實施例中,與第一實施例相較之下,其特徵在於該電觸媒蜂巢還可包含一界面層40,該界面層40設置於該陰極層30與該固態氧化物層20之間,以促進該陰極層30與該固態氧化物層20連接,在此,該界面層40的材質可為螢石結構金屬氧化物,或是鈣鈦礦結構金屬氧化物,例如為螢石結構的氧化釓摻雜氧化鈰。Please refer to FIG. 4 for a partial enlarged view of a cross section according to a second embodiment of the present invention. In the second embodiment, compared with the first embodiment, the photocatalyst honeycomb may further include An interface layer 40 is disposed between the cathode layer 30 and the solid oxide layer 20 to facilitate connection between the cathode layer 30 and the solid oxide layer 20, wherein the interface layer 40 is made of a material It is a fluorite structure metal oxide, or a perovskite structure metal oxide, such as yttrium oxide doped yttrium oxide having a fluorite structure.
再者,在第二實施例中,該電觸媒蜂巢還可進一步包含一氧化觸媒層50,以促使不易於該陰極層30氧化的該富氧燃燒廢氣的一成分氧化,該氧化觸媒層50與該陰極層30連接,並附著於該陰極層30上,該氧化觸媒層50的材質可為金屬、合金、金屬氧化物、螢石結構金屬氧化物、鈣鈦礦結構金屬氧化物,例如:鈀、螢石結構的氧化釓摻雜氧化鈰以及鑭鍶錳氧化物(lanthanum–strontium–manganese oxide)等。Furthermore, in the second embodiment, the electrocatalyst honeycomb may further comprise an oxidation catalyst layer 50 for promoting oxidation of a component of the oxy-combustion combustion exhaust gas which is not easily oxidized by the cathode layer 30, the oxidation catalyst The layer 50 is connected to the cathode layer 30 and adhered to the cathode layer 30. The material of the oxidation catalyst layer 50 may be metal, alloy, metal oxide, fluorite structure metal oxide, perovskite structure metal oxide. For example, palladium, fluorite-structured cerium oxide-doped cerium oxide, and lanthanum-strontium-manganese oxide.
接續將說明本發明淨化廢氣的作用過程,首先將該電觸媒蜂巢放置於一廢氣環境中,該廢氣為該富氧燃燒廢氣而具有一氧化性環境,或可加入二次空氣使其更加富氧,該電觸媒蜂巢的工作溫度為由常溫至800°C,該富氧燃燒廢氣主要包含氮氧化物、一氧化碳、碳氫化合物及粒狀物成分,本發明對於該富氧燃燒廢氣的淨化反應方面,主要可分為氮氧化物的去除及一氧化碳、碳氫化合物、粒狀物的去除兩個部分進行。The process of purifying the exhaust gas of the present invention will be described. First, the electric catalyst honeycomb is placed in an exhaust gas environment, and the exhaust gas has an oxidizing environment for the oxygen-enriched combustion exhaust gas, or may be added to the secondary air to make it richer. Oxygen, the working temperature of the electric catalyst honeycomb is from normal temperature to 800 ° C, and the oxy-combustion exhaust gas mainly comprises nitrogen oxides, carbon monoxide, hydrocarbons and granular components, and the invention purifies the oxyfuel combustion exhaust gas In terms of reaction, it can be mainly divided into two parts: removal of nitrogen oxides and removal of carbon monoxide, hydrocarbons, and granules.
在氮氧化物去除方面,氮氧化物主要為一氧化氮(NO)與二氧化氮(NO2 ),一氧化氮可於陰極層30發生分解反應而產生氮氣與氧氣,其反應式為下式(1)。In terms of nitrogen oxide removal, nitrogen oxides are mainly nitrogen monoxide (NO) and nitrogen dioxide (NO 2 ). Nitric oxide can be decomposed in the cathode layer 30 to generate nitrogen and oxygen. The reaction formula is as follows. (1).
2NO → N2 + O2 (1)2NO → N 2 + O 2 (1)
二氧化氮可於陰極層30發生分解反應而產生一氧化氮,其反應式為下式(2)。Nitrogen dioxide can be decomposed in the cathode layer 30 to produce nitric oxide, and the reaction formula is the following formula (2).
2NO2 → 2NO + O2 (2)2NO 2 → 2NO + O 2 (2)
其一氧化氮可再於陰極層30發生分解反應而產生氮氣與氧氣。Nitric oxide can be decomposed in the cathode layer 30 to generate nitrogen and oxygen.
藉由該陽極11的該還原性環境以及該陰極層30的該氧化性環境於該陽極11與該陰極層30產生不同的氧分壓,可促使該陰極層30及該陽極11之間產生電動勢(electromotive force,emf),而驅動促進該富氧燃燒廢氣中的氮氧化物於該陰極層30進行分解反應而形成氮氣與氧氣,該電動勢的產生為依據下列原理:By the reducing environment of the anode 11 and the oxidizing environment of the cathode layer 30 generating different oxygen partial pressures between the anode 11 and the cathode layer 30, an electromotive force between the cathode layer 30 and the anode 11 can be promoted. (electromotive force, emf), and driving promotes decomposition of nitrogen oxides in the oxy-combustion exhaust gas to the cathode layer 30 to form nitrogen and oxygen, and the electromotive force is generated according to the following principle:
emf=[(RT)/(4F)]‧ln[(PO2|Cathode )/(PO2|Anode )] (3)Emf=[(RT)/(4F)]‧ln[(P O2|Cathode )/(P O2|Anode )] (3)
其中,R為氣體常數(gas constant),T為絕對溫度,F為法拉第常數(Faradic constant),PO2 為氧分壓。由於該金屬、或是該缺氧的金屬氧化物所形成的該陽極11,或是由附著有該碳物種的該陽極11,其為還原性化合物,將導致一具有相當低的氧分壓的環境於陽極(Anode)側,因而產生一較大的電動勢。不同的還原性氣體以及不同的還原性化合物於陽極側將會導致不同的氧分壓,而會產生不同的電動勢;陰極(Cathode)側不同的氧濃度也對應不同的氧分壓值,也會產生不同的電動勢,即陰極側該富氧燃燒廢氣中的含氧量越高則電動勢越大,而電動勢越大則本發明的氮氧化物經電化學促進(electrochemical promotion)分解的反應速率越大,據此,雖然該富氧燃燒廢氣為在一氧化性環境能產生一電動勢,再添加該二次空氣進入該富氧燃燒廢氣能導致一更大的電動勢。而在一定溫度範圍內,分解反應速率會隨工作溫度越低而越大,在常溫的分解反應可和在較高溫度時一樣有效。Where R is the gas constant, T is the absolute temperature, F is the Faradic constant, and P O2 is the oxygen partial pressure. The anode 11 formed by the metal or the oxygen-deficient metal oxide, or the anode 11 to which the carbon species is attached, which is a reducing compound, will result in a relatively low oxygen partial pressure. The environment is on the anode side, thus creating a large electromotive force. Different reducing gases and different reducing compounds will cause different partial pressures of oxygen on the anode side, and different electromotive forces will be generated; different oxygen concentrations on the cathode side will also correspond to different oxygen partial pressure values. Different electromotive forces are generated, that is, the higher the oxygen content in the oxy-combustion exhaust gas on the cathode side, the larger the electromotive force, and the larger the electromotive force, the higher the reaction rate of the nitrogen oxide of the present invention by electrochemical promotion decomposition. According to this, although the oxy-combustion exhaust gas can generate an electromotive force in an oxidizing environment, adding the secondary air to the oxy-combustion combustion exhaust gas can cause a larger electromotive force. In a certain temperature range, the decomposition reaction rate will be larger as the working temperature is lower, and the decomposition reaction at normal temperature can be as effective as at higher temperatures.
在去除該富氧燃燒廢氣中一氧化碳、碳氫化合物和粒狀物的反應方面,因該富氧燃燒廢氣為富氧狀態,或加入二次空氣使其更加富氧,其可藉該陰極層30及該氧化觸媒層50催化氧化形成無害氣體,其中該富氧燃燒廢氣中的一氧化碳可氧化為二氧化碳,碳氫化合物和粒狀物(含碳(C)物質)可氧化為二氧化碳和水,其反應式分別如下式(4)至(6):In the reaction for removing carbon monoxide, hydrocarbons and granules in the oxy-combustion exhaust gas, the oxy-combusted combustion exhaust gas is in an oxygen-rich state, or secondary air is added to make it more oxygen-rich, and the cathode layer 30 can be used. And oxidizing the oxidation catalyst layer 50 to form a harmless gas, wherein the carbon monoxide in the oxy-combustion exhaust gas can be oxidized to carbon dioxide, and the hydrocarbons and granules (carbon-containing (C) substances) can be oxidized to carbon dioxide and water. The reaction formulas are as follows (4) to (6):
2CO + O2 → 2CO2 (4)2CO + O 2 → 2CO 2 (4)
HCs + O2 → H2 O + CO2 (5)HCs + O 2 → H 2 O + CO 2 (5)
C + O2 → CO2 (6)C + O 2 → CO 2 (6)
因此,對本發明的第一實施例而言,主要為透過電化學促進分解反應進行氮氧化物的去除,並可透過氧化反應去除一氧化碳、碳氫化合物和粒狀物,而有效除去該富氧燃燒廢氣中的有害成分。Therefore, in the first embodiment of the present invention, the removal of nitrogen oxides is mainly performed by electrochemically promoting the decomposition reaction, and the carbon monoxide, hydrocarbons and particulate matter are removed by an oxidation reaction, thereby effectively removing the oxyfuel combustion. Harmful components in the exhaust gas.
請參閱『圖5』所示,為本發明第三實施例的前視示意圖,在此實施例中,該蜂巢結構體10的橫截面外觀形成六邊形,而該氣流通道12的橫截面外觀則形成圓形,但並不以此為限制,該蜂巢結構體10與該氣流通道12的橫載面形狀,可依使用的需求與形式而變化。Referring to FIG. 5, a front view of a third embodiment of the present invention. In this embodiment, the cross-sectional appearance of the honeycomb structure 10 is hexagonal, and the cross-sectional appearance of the airflow passage 12 is shown. The circular shape is formed, but is not limited thereto. The shape of the cross-sectional surface of the honeycomb structure 10 and the air flow passage 12 may vary depending on the needs and forms of use.
綜上所述,由於本發明藉由分別於該陽極側與該陰極側之間形成不同的氧分壓,而產生該電動勢以促進該觸媒分解反應,不僅結構精簡,降低生產成本,再者,本發明得以使用最小的體積達成淨化的效果,例如設置於車輛引擎排氣管中,消除引擎排放的該富氧燃燒廢氣中的有害物質,減少空氣污染,最後,本發明與習知的蜂巢式電化學觸媒轉換器相較,所有該氣流通道皆用於與該富氧燃燒廢氣進行反應,而具有較大的反應區域及較佳的反應效率,因此本發明極具進步性及符合申請發明專利的要件,爰依法提出申請,祈 鈞局早日賜准專利,實感德便。In summary, since the present invention generates the electromotive force by forming different oxygen partial pressures between the anode side and the cathode side, respectively, to promote the catalyst decomposition reaction, not only the structure is simplified, but the production cost is reduced. The invention can achieve the purifying effect by using a minimum volume, for example, disposed in the exhaust pipe of the vehicle engine, eliminating harmful substances in the oxyfuel combustion exhaust gas discharged by the engine, reducing air pollution, and finally, the present invention and the known honeycomb Compared with the electrochemical converter, all of the gas flow channels are used for reacting with the oxy-combustion exhaust gas, and have a large reaction area and better reaction efficiency, so the invention is highly advanced and conforms to the application. The essentials of the invention patent, the application of the law in accordance with the law, the prayer bureau to grant the patent as soon as possible, the real sense of virtue.
以上已將本發明做一詳細說明,惟以上所述者,僅爲本發明的一較佳實施例而已,當不能限定本發明實施的範圍。即凡依本發明申請範圍所作的均等變化與修飾等,皆應仍屬本發明的專利涵蓋範圍內。The present invention has been described in detail above, but the foregoing is only a preferred embodiment of the present invention, and is not intended to limit the scope of the invention. That is, the equivalent changes and modifications made by the scope of the present application should remain within the scope of the patent of the present invention.
10...蜂巢結構體10. . . Honeycomb structure
11...陽極11. . . anode
12...氣流通道12. . . Air flow channel
20...固態氧化物層20. . . Solid oxide layer
21...管壁twenty one. . . Wall
30...陰極層30. . . Cathode layer
40...界面層40. . . Interface layer
50...氧化觸媒層50. . . Oxidation catalyst layer
圖1,為本發明第一實施例的外觀立體示意圖。FIG. 1 is a perspective view showing the appearance of a first embodiment of the present invention.
圖2,為本發明第一實施例的剖面示意圖。Figure 2 is a cross-sectional view showing the first embodiment of the present invention.
圖3,為本發明第一實施例的剖面局部放大示意圖。Fig. 3 is a partially enlarged schematic cross-sectional view showing the first embodiment of the present invention.
圖4,為本發明第二實施例的剖面局部放大示意圖。Fig. 4 is a partially enlarged schematic cross-sectional view showing a second embodiment of the present invention.
圖5,為本發明第三實施例的前視示意圖。Figure 5 is a front elevational view showing a third embodiment of the present invention.
10...蜂巢結構體10. . . Honeycomb structure
11...陽極11. . . anode
12...氣流通道12. . . Air flow channel
20...固態氧化物層20. . . Solid oxide layer
30...陰極層30. . . Cathode layer
Claims (9)
一蜂巢結構體,包含一形成該蜂巢結構體的一骨架的陽極以及複數個形成於該骨架內而供該富氧燃燒廢氣流通的氣流通道,該陽極由一第一多孔性材質組成,並具有一還原性環境;
一包覆該陽極的一表面的固態氧化物層,該固態氧化物層為一緻密微結構,並具有一面對該氣流通道的管壁;以及
一附著於該管壁上的陰極層,該固態氧化物層位於該陽極與該陰極層之間,該陰極層則由一第二多孔性材質組成,並具有一氧化性環境;
其中,該還原性環境與該氧化性環境令該陽極及該陰極層之間產生一電動勢,驅動促進該富氧燃燒廢氣中的氮氧化物於該陰極層進行一分解反應而形成氮氣與氧氣。An electric catalyst honeycomb for controlling exhaust gas emissions for purifying an oxyfuel combustion exhaust gas, the electric catalyst honeycomb comprising:
a honeycomb structure comprising an anode forming a skeleton of the honeycomb structure and a plurality of gas flow channels formed in the skeleton for circulating the oxygen-enriched combustion exhaust gas, the anode being composed of a first porous material, and Have a reducing environment;
a solid oxide layer covering a surface of the anode, the solid oxide layer having a uniform dense structure and having a tube wall facing the gas flow passage; and a cathode layer attached to the tube wall, a solid oxide layer is disposed between the anode and the cathode layer, the cathode layer is composed of a second porous material and has an oxidizing environment;
Wherein, the reducing environment and the oxidizing environment generate an electromotive force between the anode and the cathode layer to drive nitrogen oxides in the oxyfuel combustion exhaust gas to undergo a decomposition reaction in the cathode layer to form nitrogen gas and oxygen gas.
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TW101135008A TWI474859B (en) | 2012-09-24 | 2012-09-24 | An electro-catalytic honeycomb for controlling exhaust emissions |
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IN2910MU2013 IN2013MU02910A (en) | 2012-09-24 | 2013-09-10 | |
KR1020130110931A KR101562289B1 (en) | 2012-09-24 | 2013-09-16 | Electro-catalytic honeycomb for exhaust emissions control |
JP2013192053A JP5711796B2 (en) | 2012-09-24 | 2013-09-17 | Electrocatalytic honeycomb for controlling exhaust gas emissions |
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CN106765538A (en) * | 2015-11-20 | 2017-05-31 | 张家铭 | Metal solvent sterilization device |
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US7892623B2 (en) * | 2005-06-24 | 2011-02-22 | Ibiden Co., Ltd | Honeycomb structured body, manufacturing device of honeycomb structured body and manufacturing method of honeycomb structured body |
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KR20140040006A (en) | 2014-04-02 |
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CA2826434A1 (en) | 2014-03-24 |
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