CN103079691A - 提高耐用性的用于选择性催化还原的催化剂 - Google Patents
提高耐用性的用于选择性催化还原的催化剂 Download PDFInfo
- Publication number
- CN103079691A CN103079691A CN2011800420017A CN201180042001A CN103079691A CN 103079691 A CN103079691 A CN 103079691A CN 2011800420017 A CN2011800420017 A CN 2011800420017A CN 201180042001 A CN201180042001 A CN 201180042001A CN 103079691 A CN103079691 A CN 103079691A
- Authority
- CN
- China
- Prior art keywords
- catalyst
- scr
- ceria
- catalytic reduction
- selective catalytic
- 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.)
- Granted
Links
- 239000003054 catalyst Substances 0.000 title claims abstract description 85
- 238000010531 catalytic reduction reaction Methods 0.000 title abstract description 7
- 239000002131 composite material Substances 0.000 claims abstract description 13
- 239000010953 base metal Substances 0.000 claims abstract description 6
- 229910052783 alkali metal Inorganic materials 0.000 claims abstract description 3
- 150000001340 alkali metals Chemical class 0.000 claims abstract description 3
- 229910000420 cerium oxide Inorganic materials 0.000 claims description 27
- BMMGVYCKOGBVEV-UHFFFAOYSA-N oxo(oxoceriooxy)cerium Chemical compound [Ce]=O.O=[Ce]=O BMMGVYCKOGBVEV-UHFFFAOYSA-N 0.000 claims description 27
- MXOSECBTSFQUJS-UHFFFAOYSA-N [O-2].[Ti+4].[V+5] Chemical group [O-2].[Ti+4].[V+5] MXOSECBTSFQUJS-UHFFFAOYSA-N 0.000 claims description 12
- 229910021536 Zeolite Inorganic materials 0.000 claims description 9
- 239000010457 zeolite Substances 0.000 claims description 9
- MCMNRKCIXSYSNV-UHFFFAOYSA-N Zirconium dioxide Chemical compound O=[Zr]=O MCMNRKCIXSYSNV-UHFFFAOYSA-N 0.000 claims description 6
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 6
- 229910052684 Cerium Inorganic materials 0.000 claims description 3
- GWXLDORMOJMVQZ-UHFFFAOYSA-N cerium Chemical compound [Ce] GWXLDORMOJMVQZ-UHFFFAOYSA-N 0.000 claims description 3
- 239000000919 ceramic Substances 0.000 claims description 2
- 229910052751 metal Inorganic materials 0.000 claims description 2
- 239000002184 metal Substances 0.000 claims description 2
- 229910044991 metal oxide Inorganic materials 0.000 claims 2
- 150000004706 metal oxides Chemical class 0.000 claims 2
- 229910052784 alkaline earth metal Inorganic materials 0.000 claims 1
- 150000001342 alkaline earth metals Chemical class 0.000 claims 1
- 150000002739 metals Chemical class 0.000 claims 1
- 229910052761 rare earth metal Inorganic materials 0.000 claims 1
- 150000002910 rare earth metals Chemical class 0.000 claims 1
- 229910052723 transition metal Inorganic materials 0.000 claims 1
- 150000003624 transition metals Chemical class 0.000 claims 1
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 abstract description 16
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 abstract description 13
- 239000004202 carbamide Substances 0.000 abstract description 13
- 229910021529 ammonia Inorganic materials 0.000 abstract description 8
- 230000007062 hydrolysis Effects 0.000 abstract description 8
- 238000006460 hydrolysis reaction Methods 0.000 abstract description 8
- 230000003197 catalytic effect Effects 0.000 abstract description 4
- 239000003638 chemical reducing agent Substances 0.000 abstract description 4
- 231100000614 poison Toxicity 0.000 abstract description 2
- CETPSERCERDGAM-UHFFFAOYSA-N ceric oxide Chemical compound O=[Ce]=O CETPSERCERDGAM-UHFFFAOYSA-N 0.000 abstract 4
- 229910000422 cerium(IV) oxide Inorganic materials 0.000 abstract 4
- 239000002574 poison Substances 0.000 abstract 1
- 229910052720 vanadium Inorganic materials 0.000 abstract 1
- LEONUFNNVUYDNQ-UHFFFAOYSA-N vanadium atom Chemical compound [V] LEONUFNNVUYDNQ-UHFFFAOYSA-N 0.000 abstract 1
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 54
- 238000000576 coating method Methods 0.000 description 26
- 239000011248 coating agent Substances 0.000 description 24
- 238000006243 chemical reaction Methods 0.000 description 14
- 230000018109 developmental process Effects 0.000 description 11
- 239000000446 fuel Substances 0.000 description 7
- 238000010335 hydrothermal treatment Methods 0.000 description 7
- 239000002912 waste gas Substances 0.000 description 6
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 5
- 239000005864 Sulphur Substances 0.000 description 5
- 238000002485 combustion reaction Methods 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 4
- OAICVXFJPJFONN-UHFFFAOYSA-N Phosphorus Chemical compound [P] OAICVXFJPJFONN-UHFFFAOYSA-N 0.000 description 4
- HCHKCACWOHOZIP-UHFFFAOYSA-N Zinc Chemical compound [Zn] HCHKCACWOHOZIP-UHFFFAOYSA-N 0.000 description 4
- 229910052791 calcium Inorganic materials 0.000 description 4
- 239000011575 calcium Substances 0.000 description 4
- 229910052698 phosphorus Inorganic materials 0.000 description 4
- 239000011574 phosphorus Substances 0.000 description 4
- 231100000572 poisoning Toxicity 0.000 description 4
- 230000000607 poisoning effect Effects 0.000 description 4
- 230000001603 reducing effect Effects 0.000 description 4
- 239000011701 zinc Substances 0.000 description 4
- 229910052725 zinc Inorganic materials 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 229930195733 hydrocarbon Natural products 0.000 description 3
- 150000002430 hydrocarbons Chemical class 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 239000004215 Carbon black (E152) Substances 0.000 description 2
- 235000011114 ammonium hydroxide Nutrition 0.000 description 2
- 239000010949 copper Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 230000009466 transformation Effects 0.000 description 2
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 1
- RYGMFSIKBFXOCR-UHFFFAOYSA-N Copper Chemical compound [Cu] RYGMFSIKBFXOCR-UHFFFAOYSA-N 0.000 description 1
- 206010013786 Dry skin Diseases 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- 229910052779 Neodymium Inorganic materials 0.000 description 1
- 229910052777 Praseodymium Inorganic materials 0.000 description 1
- 230000004913 activation Effects 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 238000004176 ammonification Methods 0.000 description 1
- 239000002585 base Substances 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 229910052802 copper Inorganic materials 0.000 description 1
- 238000003618 dip coating Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 239000005431 greenhouse gas Substances 0.000 description 1
- 238000005342 ion exchange Methods 0.000 description 1
- 229910052746 lanthanum Inorganic materials 0.000 description 1
- 239000010721 machine oil Substances 0.000 description 1
- 229910052748 manganese Inorganic materials 0.000 description 1
- QGLKJKCYBOYXKC-UHFFFAOYSA-N nonaoxidotritungsten Chemical compound O=[W]1(=O)O[W](=O)(=O)O[W](=O)(=O)O1 QGLKJKCYBOYXKC-UHFFFAOYSA-N 0.000 description 1
- 239000010747 number 6 fuel oil Substances 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- 238000011056 performance test Methods 0.000 description 1
- 230000007096 poisonous effect Effects 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000006722 reduction reaction Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
- 231100000331 toxic Toxicity 0.000 description 1
- 230000002588 toxic effect Effects 0.000 description 1
- 229910001428 transition metal ion Inorganic materials 0.000 description 1
- 229910001930 tungsten oxide Inorganic materials 0.000 description 1
- 229910052727 yttrium Inorganic materials 0.000 description 1
- 229910052726 zirconium Inorganic materials 0.000 description 1
Images
Classifications
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/16—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/20—Vanadium, niobium or tantalum
- B01J23/22—Vanadium
-
- 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
- B01D53/92—Chemical or biological purification of waste gases of engine exhaust gases
- B01D53/94—Chemical or biological purification of waste gases of engine exhaust gases by catalytic processes
- B01D53/9404—Removing only nitrogen compounds
- B01D53/9409—Nitrogen oxides
- B01D53/9413—Processes characterised by a specific catalyst
- B01D53/9418—Processes characterised by a specific catalyst for removing nitrogen oxides by selective catalytic reduction [SCR] using a reducing agent in a lean exhaust gas
-
- 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
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/10—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of rare earths
-
- 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
-
- 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
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/04—Catalysts comprising molecular sieves having base-exchange properties, e.g. crystalline zeolites
- B01J29/06—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof
- B01J29/064—Crystalline aluminosilicate zeolites; Isomorphous compounds thereof containing iron group metals, noble metals or copper
- B01J29/072—Iron group metals or copper
-
- 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
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/0009—Use of binding agents; Moulding; Pressing; Powdering; Granulating; Addition of materials ameliorating the mechanical properties of the product 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/024—Multiple impregnation or coating
- B01J37/0244—Coatings comprising several layers
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/024—Multiple impregnation or coating
- B01J37/0246—Coatings comprising a zeolite
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/03—Precipitation; Co-precipitation
- B01J37/038—Precipitation; Co-precipitation to form slurries or suspensions, e.g. a washcoat
-
- 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
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/08—Heat treatment
- B01J37/10—Heat treatment in the presence of water, e.g. steam
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/20—Reductants
- B01D2251/206—Ammonium compounds
- B01D2251/2062—Ammonia
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2251/00—Reactants
- B01D2251/20—Reductants
- B01D2251/206—Ammonium compounds
- B01D2251/2067—Urea
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/206—Rare earth metals
- B01D2255/2065—Cerium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20707—Titanium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20715—Zirconium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/20—Metals or compounds thereof
- B01D2255/207—Transition metals
- B01D2255/20723—Vanadium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/50—Zeolites
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2255/00—Catalysts
- B01D2255/90—Physical characteristics of catalysts
- B01D2255/902—Multilayered catalyst
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Crystallography & Structural Chemistry (AREA)
- Environmental & Geological Engineering (AREA)
- Biomedical Technology (AREA)
- Health & Medical Sciences (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Combustion & Propulsion (AREA)
- Catalysts (AREA)
- Exhaust Gas Treatment By Means Of Catalyst (AREA)
Abstract
本发明涉及一种使用氨或尿素作为还原剂的选择性催化还原的催化剂,且特别涉及一种涂覆有氧化铈或氧化铈复合氧化物的选择性催化还原的催化剂。本发明涉及的催化剂,其中氧化铈或氧化铈复合氧化物涂覆到包含如钒等沸石或非沸石基底金属的选择性催化还原的催化剂的上层。令人惊奇地,如果氧化铈或含氧化铈的复合氧化物涂覆到选择性催化还原的催化剂的最上层,能够在相对较低温度显示出催化活性,能够改善耐热性和对碱金属等的抗毒性并能增加尿素水解的效率。
Description
技术领域
本发明涉及一种使用氨或尿素作为还原剂的选择性催化还原催化剂,该催化剂在抗毒性和耐热性方面都有所改善且低温活性得以提高,更特别涉及一种选择性催化还原催化剂,其中包含沸石或非沸石基底金属的催化剂的最上层表面涂覆有氧化铈或氧化铈复合氧化物,其中用氧化铈或氧化铈复合氧化物涂覆催化剂的最上层表面能使氮氧化物(NOx)的还原性能在相对低温的范围内得以提高,并能改善因碱金属组分如磷、钙、锌等以及内燃机排出废气中未燃烃所引起的中毒的耐用性,且即使暴露在高温也能提高耐热性。此外,在选择性催化还原时使用尿素作为还原剂可增加尿素水解的效率,从而提高了氨产率。
背景技术
就使用化学计量燃烧所需预定量或预定量以上的空气的情况下,也就是在稀燃条件下下运行的内燃机而论,很难从废气中去除氮氧化物(NOx)。
在应用于对应稀燃条件的固定源且其效果已证实的NOx还原工艺中,这种工艺之一是使用氨或氨水的选择性催化还原(SCR)。这样,NOx与还原剂氨在SCR催化剂的表面上反应并因而还原成氮气(N2),由此减少NOx的量。通常,钒钛氧化物已经被用作固定源中的SCR催化剂。在这种情况下,300~450℃具有90%或以上的NOx还原性能。为了将钒钛氧化物催化剂应用到移动源,研制了包含氧化钨(WO3)等的催化剂,以使由于因燃料的硫组分和高温暴露引起的中毒而降低的催化性能得以改善,且它们正被应用于大的柴油车辆。为了配合将来船运业中加强的废气规定,预期将会频繁使用钒钛氧化物催化剂。然而,催化剂的性能会由于高温暴露或因为废气的未燃烃及燃料(机油)中其他碱金属组分如硫、磷、钙、锌等吸附在催化剂上而彻底地降低,这亟待解决。
另一方面,出于确保最终使用需要相比钒钛氧化物催化剂更高的温度耐用性(600℃或更高)和更高的活化温度(350~550℃)的目的,研制并已经使用了沸石催化剂如Fe-β、Cu-β、Fe-ZSM5和Cu-ZSM5催化剂,其中ZSM5和β-沸石与过渡金属离子如铁(Fe)或铜(Cu)进行离子交换。但是,这些催化剂存在一些问题,因为低温活性要次于钒钛氧化物催化剂且在因烃类和碱金属组分如硫、磷、钙、锌等引起中毒时催化性能会显著降低。
根据全球温室气体减排和废气排放管理的要求,新近正研制的内燃机被广泛地经受低温燃烧工艺以获得高的燃料效率和废气减排。因此,废气温度预期在将来将会更低,这样,低温性能是受到大量关注的一个特性。
发明内容
技术问题
因此,现在对具有优良的低温活性、耐内燃机中高温暴露的耐热性以及抗因碱金属组分如硫、磷、钙、锌等引起中毒的抗毒性的新型催化剂存在需求。
本发明人使用氧化铈或氧化铈复合氧化物作为传统SCR催化剂的最上层来进行SCR反应,并因而发现获得的催化剂能够解决上述问题,此外发现,最高涂层的存在可提高尿素向氨的转变,这些发现使得本发明得以完成。
技术方案
本发明提供了一种包含(a)沸石或非沸石作为基底金属(钒钛氧化物和氧化锆)的SCR催化剂,其中,其最上层包含氧化铈或氧化铈复合氧化物。
本发明中,复合氧化物是包含含有铈的两种或两种以上元素的混合氧化物,特别是非物理混合的、包含含有铈的两种或两种以上元素的氧化物的非晶氧化物。例如,复合氧化物可以是Ce-LMNOx(L、M、N=Zr、Y、Pr、Nd、La或Mn)。
单独的氧化铈或氧化铈复合氧化物可涂覆到包含沸石或非沸石作为基底金属(钒钛氧化物和氧化锆)的常规SCR催化剂上。
本发明的SCR催化剂可涂覆到陶瓷蜂窝体上或可挤压成蜂窝形状。因此,本发明的氧化物涂层可经由典型的湿涂法(wash-coating process)通过能够商业上使用该蜂窝的氧化铈基湿涂溶液来完成。为了获得平坦的SCR催化剂层,湿涂工艺包括利用湿涂溶液浸涂包含沸石或非沸石的SCR催化剂并使用压缩空气去除过量的氧化物涂层。湿涂催化剂可在大约100℃下干燥,然后在450~550℃煅烧。
有益效果
根据本发明,当具有氧化铈涂层的SCR催化剂应用到氨/尿素-SCR系统时,能够获得优良的低温活性,并能加快尿素水解,从而提高废气中NOx的转化率。此外,该催化剂在高温暴露时具有耐热性,并增加了抗毒性,这使得它即使在暴露于高浓度的硫或碱金属时,也能保持催化活性。
附图说明
图1例示了在将标准催化剂(没有氧化铈涂层)和研制的催化剂(具有氧化铈涂层)使用航运燃料(MF30)长时间暴露于有毒组分后催化剂(标准催化剂、研制的催化剂)的NOx的转化率。
图2例示了在625℃下水热处理24小时后标准催化剂或研制的SCR催化剂(钒钛氧化物催化剂)的NOx的转化率。
图3例示了在700℃下水热处理24小时后标准催化剂或研制的SCR催化剂(铁-沸石催化剂)的NOx转化率。
图4例示了标准催化剂或研制的SCR催化剂(钒钛氧化物催化剂)的尿素水解效率。
具体实施方式
实施例1
研制的催化剂A以如下方式加以制备,将圆柱形的蜂窝状载体(110Φ*78.9、400cpsi、0.75L)涂覆钒钛氧化物,然后浸入到仅包含氧化铈的湿涂溶液中,以便SCR催化剂的最上层形成有氧化铈涂层。制备的催化剂在10%湿度条件下于625℃进行24小时水热处理。
实施例2
研制的催化剂B以如下方式加以制备,将六面体的蜂窝状载体(150*150*100、36cpsi、2.25L)涂覆钒钛氧化物,然后浸入到包含主要由氧化铈组成的复合氧化物的湿涂溶液中,以便SCR催化剂的最上层形成有氧化铈涂层。制备的(新制的)催化剂使用船运燃料MF30(35%柴油机+65%船用燃料油C)于250℃下老化8小时。
实施例3
研制的催化剂C以如下方式加以制备,将圆柱形的蜂窝状载体(110Φ*78.9、400cpsi、0.75L)涂覆铁-沸石,然后浸入到仅包含氧化铈的湿涂溶液中,以便SCR催化剂的最上层形成有氧化铈涂层。制备的催化剂在10%湿度条件下于700℃下进行24小时水热处理。
测试实施例1
SCR催化剂的低温活性测试
为了评价SCR催化剂的活性,实施例1、2和3中每个涂覆的蜂窝状载体都放入到测试反应器中。在涂覆到六面体载体上的SCR催化剂的情况下,NOx(350~400ppm)以20,000/小时空间速度供入(经由入口),在涂覆到圆柱形载体上的SCR催化剂的情况下,NOx(400~450ppm)以53,000/小时的空间速度供入,并测量和比较了NOx的转化率。
NOx的转化结果显示在图1(使用船运燃料老化的催化剂),图2(在625℃下进行水热处理的催化剂)和图3(在700℃下进行水热处理的催化剂)中。如图1中所示,与没有氧化物涂层的SCR催化剂(标准催化剂)相比,具有氧化铈涂层作为最上层的SCR催化剂(研制的催化剂)即使在低温(200~250℃)使用船运燃料进行老化处理后也具有更高的转化率。如图2和3中所示,与没有氧化物涂层的SCR催化剂(标准催化剂)相比,具有氧化铈涂层作为最上层的SCR催化剂(研制的催化剂)在水热处理后,具有更高的NOx转化率。
测试实施例2
尿素水解性能测试
为了评价SCR催化剂的活性,将实施例1中涂覆有SCR催化剂的每个蜂窝状载体放入测试反应器中,然后以53,000/小时的空间速度喷射尿素(2g/分),然后测量并比较尿素转化成氨的水解转化率。
氨转化率结果显示在图4中。如图4中所示,具有氧化铈涂层作为最上层的SCR催化剂与没有氧化物涂层的SCR催化剂相比,具有更高的尿素水解转化率。
工业实用性
因此,当将本发明的具有氧化铈涂层的SCR催化剂应用到尿素-SCR系统时,能够获得优良的低温活性,并能加快尿素水解,从而改善总体NOx转化率。
Claims (5)
1.一种选择性催化还原(SCR)的催化剂,包含仅由氧化铈或由氧化铈复合氧化物组成的最上层。
2. 权利要求1所述的选择性催化还原(SCR)的催化剂,其中所述SCR催化剂包含沸石或非沸石作为基底金属氧化物。
3. 权利要求2所述的选择性催化还原(SCR)的催化剂,其中所述非沸石基底金属氧化物是钒钛氧化物或氧化锆。
4. 权利要求1所述的选择性催化还原(SCR)的催化剂,其中氧化铈复合氧化物是铈和选自稀土金属、过渡金属、碱金属与碱土金属中的一种或多种金属的混合氧化物。
5. 权利要求1所述的选择性催化还原(SCR)的催化剂,其中所述SCR催化剂应用到蜂窝体上或挤压成蜂窝形状。
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
KR1020100084463A KR101197452B1 (ko) | 2010-08-31 | 2010-08-31 | 내구성이 증진된 선택적 촉매환원 촉매 |
KR10-2010-0084463 | 2010-08-31 | ||
PCT/KR2011/006375 WO2012030127A2 (ko) | 2010-08-31 | 2011-08-30 | 내구성이 증진된 선택적 촉매환원 촉매 |
Publications (2)
Publication Number | Publication Date |
---|---|
CN103079691A true CN103079691A (zh) | 2013-05-01 |
CN103079691B CN103079691B (zh) | 2014-10-29 |
Family
ID=45773369
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201180042001.7A Active CN103079691B (zh) | 2010-08-31 | 2011-08-30 | 提高耐用性的用于选择性催化还原的催化剂 |
Country Status (4)
Country | Link |
---|---|
EP (1) | EP2612705A4 (zh) |
KR (1) | KR101197452B1 (zh) |
CN (1) | CN103079691B (zh) |
WO (1) | WO2012030127A2 (zh) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108472630A (zh) * | 2015-12-23 | 2018-08-31 | 喜星触媒株式会社 | 用于压缩天然气燃烧系统废气的氧化催化剂 |
Families Citing this family (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
KR101535088B1 (ko) * | 2012-06-12 | 2015-07-08 | 희성촉매 주식회사 | 고성능 scr 촉매 시스템 |
JP2014144424A (ja) * | 2013-01-29 | 2014-08-14 | Hitachi Zosen Corp | アンモニア分解用触媒 |
KR101513834B1 (ko) * | 2014-04-14 | 2015-04-20 | 두산엔진주식회사 | 선택적 촉매 환원을 위한 촉매 및 이의 제조방법 |
KR20190023021A (ko) | 2017-08-25 | 2019-03-07 | (주) 세라컴 | 저온 활성이 우수한 선택적 환원촉매 및 그 제조 방법 |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101204650A (zh) * | 2006-12-20 | 2008-06-25 | 中国科学院生态环境研究中心 | 一种烟气脱硝的铈钛复合氧化物催化剂 |
CN101314127A (zh) * | 2007-05-31 | 2008-12-03 | 中国科学院大连化学物理研究所 | 用于选择性还原氮氧化物的氧化物催化剂及其制造方法和用途 |
KR20090121513A (ko) * | 2008-05-22 | 2009-11-26 | 현대자동차주식회사 | 선택적 촉매환원 촉매 및 그 제조방법 |
Family Cites Families (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US5665668A (en) * | 1994-01-25 | 1997-09-09 | Grigorova; Bojidara | Method of making a catalyst |
KR20030001437A (ko) * | 2000-04-19 | 2003-01-06 | 사에스 게터스 에스.페.아. | 제오라이트상에 지지된 철 및 망간계 촉매로 유기금속화합물 또는 이종원자 유기 화합물을 정제하는 방법 |
GB0214968D0 (en) * | 2002-06-28 | 2002-08-07 | Johnson Matthey Plc | Zeolite-based NH SCR catalyst |
WO2004022229A1 (en) * | 2002-09-04 | 2004-03-18 | The University Of Chicago | Novel catalyst for selective nox reduction using hydrocarbons |
JP4711860B2 (ja) * | 2006-03-03 | 2011-06-29 | エヌ・イーケムキャット株式会社 | 排気ガス浄化用酸化触媒、排気ガス浄化用触媒構造体および排気ガス浄化方法 |
US7527776B2 (en) * | 2007-01-09 | 2009-05-05 | Catalytic Solutions, Inc. | Ammonia SCR catalyst and method of using the catalyst |
-
2010
- 2010-08-31 KR KR1020100084463A patent/KR101197452B1/ko active IP Right Grant
-
2011
- 2011-08-30 EP EP11822102.7A patent/EP2612705A4/en not_active Withdrawn
- 2011-08-30 WO PCT/KR2011/006375 patent/WO2012030127A2/ko active Application Filing
- 2011-08-30 CN CN201180042001.7A patent/CN103079691B/zh active Active
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN101204650A (zh) * | 2006-12-20 | 2008-06-25 | 中国科学院生态环境研究中心 | 一种烟气脱硝的铈钛复合氧化物催化剂 |
CN101314127A (zh) * | 2007-05-31 | 2008-12-03 | 中国科学院大连化学物理研究所 | 用于选择性还原氮氧化物的氧化物催化剂及其制造方法和用途 |
KR20090121513A (ko) * | 2008-05-22 | 2009-11-26 | 현대자동차주식회사 | 선택적 촉매환원 촉매 및 그 제조방법 |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN108472630A (zh) * | 2015-12-23 | 2018-08-31 | 喜星触媒株式会社 | 用于压缩天然气燃烧系统废气的氧化催化剂 |
CN108472630B (zh) * | 2015-12-23 | 2021-10-22 | 喜星触媒株式会社 | 用于压缩天然气燃烧系统废气的氧化催化剂 |
Also Published As
Publication number | Publication date |
---|---|
WO2012030127A2 (ko) | 2012-03-08 |
CN103079691B (zh) | 2014-10-29 |
EP2612705A4 (en) | 2014-07-16 |
KR20120020688A (ko) | 2012-03-08 |
EP2612705A2 (en) | 2013-07-10 |
WO2012030127A3 (ko) | 2012-06-21 |
KR101197452B1 (ko) | 2012-11-05 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
KR101974704B1 (ko) | 선택적 암모니아 산화를 위한 이원기능 촉매 | |
CN101845978B (zh) | 具有四效和尿素scr催化器的排气处理系统及使用方法 | |
EP2965812B1 (en) | Low-temperature scr catalyst for denitrating diesel vehicle exhaust, and preparation method thereof | |
US20120214663A1 (en) | Lnt and scr catalysts for combined lnt-scr applications | |
US20130323145A1 (en) | Base Metal Catalyst Composition and Methods of Treating Exhaust From a Motorcycle | |
US10981153B2 (en) | Catalyst and method for preparing catalyst | |
CN103079691B (zh) | 提高耐用性的用于选择性催化还原的催化剂 | |
US10343925B2 (en) | Method for preparing zeolite catalyst | |
CN103566964A (zh) | 一种低温催化剂及其制备方法 | |
CN108071450B (zh) | Cu/LTA催化剂和排气系统、以及Cu/LTA催化剂的制造方法 | |
CN102728224B (zh) | 用于净化燃烧废气的催化器及其制备方法 | |
EP2740533B1 (en) | Method for removing nitrogen oxides in exhaust gas | |
KR101846914B1 (ko) | 촉매 및 촉매의 제조 방법 | |
JPH11221466A (ja) | 排気ガス浄化用触媒及び排気ガス浄化方法 | |
KR20130060028A (ko) | 수동적 암모니아/scr용 암모니아 생성 삼원 촉매의 제조 방법 및 이에 의해 제조된 삼원 촉매 | |
CN103316716A (zh) | 一种scr催化剂及其制备方法 | |
KR101438885B1 (ko) | 질소산화물의 암모니아 전환용 촉매 및 이의 제조방법 | |
KR100969104B1 (ko) | 디젤 산화촉매 및 그 제조 방법 | |
KR101786662B1 (ko) | 질소산화물 환원 반응용 담지 촉매, 이의 제조 방법 및 이를 이용한 질소산화물 제거방법 | |
CN101811043B (zh) | 氮氧化物储存还原催化剂的制备方法 | |
KR101097559B1 (ko) | 희박-연소 엔진의 질소산화물 저감용 암모니아 scr 촉매 및 이를 포함하는 질소산화물 저감 장치 | |
JPH11138006A (ja) | 排気ガス浄化用触媒及び浄化方法 |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
C06 | Publication | ||
PB01 | Publication | ||
C10 | Entry into substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
C14 | Grant of patent or utility model | ||
GR01 | Patent grant |