CN109012647A - A kind of diesel engine vent gas soot removing metal composite oxide catalyst and preparation method thereof - Google Patents
A kind of diesel engine vent gas soot removing metal composite oxide catalyst and preparation method thereof Download PDFInfo
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- 239000003054 catalyst Substances 0.000 title claims abstract description 37
- 239000004071 soot Substances 0.000 title claims abstract description 31
- 239000002905 metal composite material Substances 0.000 title claims abstract description 21
- 238000002360 preparation method Methods 0.000 title claims abstract description 19
- VHUUQVKOLVNVRT-UHFFFAOYSA-N Ammonium hydroxide Chemical compound [NH4+].[OH-] VHUUQVKOLVNVRT-UHFFFAOYSA-N 0.000 claims description 7
- 235000011114 ammonium hydroxide Nutrition 0.000 claims description 7
- 238000001035 drying Methods 0.000 claims description 7
- 229910002492 Ce(NO3)3·6H2O Inorganic materials 0.000 claims description 4
- KWYUFKZDYYNOTN-UHFFFAOYSA-M Potassium hydroxide Chemical compound [OH-].[K+] KWYUFKZDYYNOTN-UHFFFAOYSA-M 0.000 claims description 4
- 239000002994 raw material Substances 0.000 claims description 4
- 238000001291 vacuum drying Methods 0.000 claims description 3
- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(1+) nitrate Chemical compound [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 claims 7
- 239000000908 ammonium hydroxide Substances 0.000 claims 2
- 239000008367 deionised water Substances 0.000 claims 2
- 229910021641 deionized water Inorganic materials 0.000 claims 2
- 230000001376 precipitating effect Effects 0.000 claims 2
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims 2
- MIVBAHRSNUNMPP-UHFFFAOYSA-N manganese(II) nitrate Inorganic materials [Mn+2].[O-][N+]([O-])=O.[O-][N+]([O-])=O MIVBAHRSNUNMPP-UHFFFAOYSA-N 0.000 claims 1
- 239000000843 powder Substances 0.000 claims 1
- 238000003756 stirring Methods 0.000 claims 1
- 239000002245 particle Substances 0.000 abstract description 6
- 230000003197 catalytic effect Effects 0.000 abstract description 5
- 230000015572 biosynthetic process Effects 0.000 abstract description 3
- 238000000034 method Methods 0.000 abstract description 3
- 238000002156 mixing Methods 0.000 abstract description 2
- 238000003786 synthesis reaction Methods 0.000 abstract description 2
- 239000011572 manganese Substances 0.000 description 18
- 230000000694 effects Effects 0.000 description 8
- 239000007789 gas Substances 0.000 description 7
- 238000011156 evaluation Methods 0.000 description 6
- 238000012360 testing method Methods 0.000 description 6
- 101710134784 Agnoprotein Proteins 0.000 description 5
- 239000002131 composite material Substances 0.000 description 5
- 239000000463 material Substances 0.000 description 4
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 239000003153 chemical reaction reagent Substances 0.000 description 2
- 238000007796 conventional method Methods 0.000 description 2
- 229930195733 hydrocarbon Natural products 0.000 description 2
- 150000002430 hydrocarbons Chemical class 0.000 description 2
- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 description 2
- 238000011068 loading method Methods 0.000 description 2
- 230000003647 oxidation Effects 0.000 description 2
- 238000007254 oxidation reaction Methods 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- PWHULOQIROXLJO-UHFFFAOYSA-N Manganese Chemical compound [Mn] PWHULOQIROXLJO-UHFFFAOYSA-N 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- WUKWITHWXAAZEY-UHFFFAOYSA-L calcium difluoride Chemical compound [F-].[F-].[Ca+2] WUKWITHWXAAZEY-UHFFFAOYSA-L 0.000 description 1
- 229910002091 carbon monoxide Inorganic materials 0.000 description 1
- CETPSERCERDGAM-UHFFFAOYSA-N ceric oxide Chemical compound O=[Ce]=O CETPSERCERDGAM-UHFFFAOYSA-N 0.000 description 1
- 229910000420 cerium oxide Inorganic materials 0.000 description 1
- 229910000422 cerium(IV) oxide Inorganic materials 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000001514 detection method Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000010436 fluorite Substances 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 229910000510 noble metal Inorganic materials 0.000 description 1
- BMMGVYCKOGBVEV-UHFFFAOYSA-N oxo(oxoceriooxy)cerium Chemical compound [Ce]=O.O=[Ce]=O BMMGVYCKOGBVEV-UHFFFAOYSA-N 0.000 description 1
- 229910052763 palladium Inorganic materials 0.000 description 1
- 229910052697 platinum Inorganic materials 0.000 description 1
- 230000008929 regeneration Effects 0.000 description 1
- 238000011069 regeneration method Methods 0.000 description 1
- 229910052703 rhodium Inorganic materials 0.000 description 1
- 229910001220 stainless steel Inorganic materials 0.000 description 1
- 239000010935 stainless steel Substances 0.000 description 1
- 238000010998 test method Methods 0.000 description 1
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- 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
- B01J23/38—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals
- B01J23/54—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of noble metals combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/66—Silver or gold
- B01J23/68—Silver or gold with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
- B01J23/688—Silver or gold with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with manganese, technetium or rhenium
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- 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
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- 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
- B01J23/002—Mixed oxides other than spinels, e.g. perovskite
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/01—Engine exhaust gases
- B01D2258/012—Diesel engines and lean burn gasoline engines
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Abstract
本发明公开了一种柴油机尾气碳烟脱除金属复合氧化物催化剂及其制备方法,其结构通式为Ag‑MnxCe1‑xOy,其中x=0.05~0.5。本发明粒径小,混合均匀,比表面积大,起燃温度低,催化活性好,价格便宜,制备方法及合成工艺操作简单,具有优良的工业应用前景。
The invention discloses a metal composite oxide catalyst for removing soot from diesel engine tail gas and a preparation method thereof. The general structural formula is Ag-Mn x Ce 1-x O y , where x=0.05-0.5. The invention has small particle size, uniform mixing, large specific surface area, low light-off temperature, good catalytic activity, low price, simple preparation method and synthesis process, and excellent industrial application prospect.
Description
技术领域technical field
本发明属于催化剂材料技术领域,具体涉及一种柴油机尾气碳烟脱除金属复合氧化物催化剂及其制备方法。The invention belongs to the technical field of catalyst materials, and in particular relates to a metal composite oxide catalyst for removing soot from diesel engine exhaust and a preparation method thereof.
背景技术Background technique
柴油机广泛应用于大、中型载重货车以及船舶上。传统上,柴油发动机由于较笨重,升功率指标不如汽油机(转速较低),噪声、振动较高,炭烟颗粒(PM)排放比较严重,一直以来很少受到轿车的青睐。柴油机排放的尾气中含有相当比例的CO、NOx、未燃尽有机碳氢化合物(HC)和碳烟颗粒(PM),故对大气环境和人类健康造成了极大的负面影响。由于碳烟颗粒燃点较高,尾气中的碳烟必须在高于600℃时才能充分燃烧。Diesel engines are widely used in large and medium-sized trucks and ships. Traditionally, diesel engines have been seldom favored by cars due to their bulkiness, lower power rating than gasoline engines (lower speed), higher noise and vibration, and serious soot particle (PM) emissions. Exhaust gas from diesel engines contains a considerable proportion of CO, NO x , unburned organic hydrocarbons (HC) and soot particles (PM), which have a great negative impact on the atmospheric environment and human health. Due to the high ignition point of soot particles, the soot in the exhaust gas must be higher than 600°C to fully burn.
近年来,涂覆有催化剂的原位再生碳烟颗粒过滤系统吸引了广泛关注。常用的Pt、Rh、Pd等贵金属基催化剂受限于其昂贵的造价而难以推广;而Ag基催化剂由于活性高,经济性相对较好,但负载量一般较高,目前仍未能实现大面积工业化应用。In situ regeneration of soot particulate filtration systems coated with catalysts has attracted much attention in recent years. Commonly used noble metal-based catalysts such as Pt, Rh, and Pd are difficult to popularize due to their high cost; while Ag-based catalysts are relatively economical due to their high activity, but generally have a high loading capacity, and have not yet achieved large-area industrial applications.
发明内容Contents of the invention
本发明的目的在于克服现有技术缺陷,提供一种柴油机尾气碳烟脱除金属复合氧化物催化剂。The purpose of the present invention is to overcome the defects of the prior art and provide a metal composite oxide catalyst for removing soot from diesel engine exhaust.
本发明的另一目的在于提供上述柴油机尾气碳烟脱除金属复合氧化物催化剂的制备方法。Another object of the present invention is to provide a preparation method of the above-mentioned metal composite oxide catalyst for removing soot from diesel engine exhaust.
本发明的技术方案如下:Technical scheme of the present invention is as follows:
一种柴油机尾气碳烟脱除金属复合氧化物催化剂,其结构通式为Ag-MnxCe1-xOy,其中x=0.05~0.5。A metal composite oxide catalyst for removing soot from diesel engine tail gas, the general structure formula of which is Ag-Mn x Ce 1-x O y , where x=0.05-0.5.
上述柴油机尾气碳烟脱除金属复合氧化物催化剂的制备方法,包括如下步骤:The preparation method of the above-mentioned diesel engine exhaust soot removal metal composite oxide catalyst comprises the following steps:
(1)按照所述结构通式称取如下原料组分Ce(NO3)3·6H2O,AgNO3,Mn(NO3)2,KOH和氨水;(1) Weigh the following raw material components Ce(NO 3 ) 3 ·6H 2 O, AgNO 3 , Mn(NO 3 ) 2 , KOH and ammonia water according to the general structural formula;
(2)将Ce(NO3)3·6H2O、Mn(NO3)2和去离子水混合制成第一溶液,将AgNO3和氨水混合制成第二溶液,将KOH和去离子水混合制成KOH溶液;(2) Mix Ce(NO 3 ) 3 ·6H 2 O, Mn(NO 3 ) 2 and deionized water to make the first solution, mix AgNO 3 and ammonia water to make the second solution, mix KOH and deionized water Mix to make KOH solution;
(3)将第一溶液和第二溶液以相同的速度缓慢滴入KOH溶液中,同时搅拌并得到均匀的沉淀;(3) Slowly drop the first solution and the second solution into the KOH solution at the same speed, while stirring and obtaining a uniform precipitation;
(4)将上述沉淀进行干燥后研成粉末,然后于450~550℃焙烧后自然冷却至室温,即得所述柴油机尾气碳烟脱除金属复合氧化物催化剂。(4) Dry the above precipitate and grind it into powder, then roast it at 450-550° C. and cool it down to room temperature naturally to obtain the metal composite oxide catalyst for removing soot from diesel engine exhaust.
在本发明的一个优选实施方案中,所述第一溶液中,Ce(NO3)3和Mn(NO3)2的浓度均为0.1~0.3mol/L。In a preferred embodiment of the present invention, in the first solution, both the concentrations of Ce(NO 3 ) 3 and Mn(NO 3 ) 2 are 0.1-0.3 mol/L.
在本发明的一个优选实施方案中,所述第二溶液中,AgNO3的浓度为0.05~0.2mol/L,氨水的浓度为1~3mol/L。In a preferred embodiment of the present invention, in the second solution, the concentration of AgNO 3 is 0.05-0.2 mol/L, and the concentration of ammonia water is 1-3 mol/L.
在本发明的一个优选实施方案中,所述KOH溶液的浓度为1.0~3.0mol/L。In a preferred embodiment of the present invention, the concentration of the KOH solution is 1.0-3.0 mol/L.
在本发明的一个优选实施方案中,所述步骤(4)的干燥为真空干燥,干燥温度为60~120℃,时间为9~12h。In a preferred embodiment of the present invention, the drying in the step (4) is vacuum drying, the drying temperature is 60-120° C., and the drying time is 9-12 hours.
在本发明的一个优选实施方案中,所述焙烧的时间为1~3h。In a preferred embodiment of the present invention, the calcination time is 1-3 hours.
本发明的有益效果是:本发明中锰元素掺入氧化铈晶相能够显著增强氧物种的移动性,并且促进氧空位的形成。作为载体,锰氧化物有助于提升Ag催化剂的氧化能力,从而降低Ag负载量,提高其经济性。即本发明粒径较小,混合均匀,比表面积大,起燃温度低,催化活性好,价格便宜,制备方法及合成工艺操作简单,具有优良的工业应用前景。The beneficial effects of the present invention are: the doping of manganese element into the cerium oxide crystal phase in the present invention can significantly enhance the mobility of oxygen species and promote the formation of oxygen vacancies. As a carrier, manganese oxide helps to improve the oxidation ability of Ag catalyst, thereby reducing the loading of Ag and improving its economy. That is, the present invention has small particle size, uniform mixing, large specific surface area, low light-off temperature, good catalytic activity, low price, simple preparation method and synthesis process, and has excellent industrial application prospects.
附图说明Description of drawings
图1为本发明实施例1~6制备的柴油机尾气碳烟脱除金属复合氧化物催化剂的XRD衍射图谱。Fig. 1 is the XRD diffraction pattern of the metal composite oxide catalysts for removing soot from diesel engine exhaust prepared in Examples 1-6 of the present invention.
图2为本发明实施例1~6制备的柴油机尾气碳烟脱除金属复合氧化物催化剂的催化活性图。Fig. 2 is a graph showing the catalytic activity of the metal composite oxide catalysts for removing soot from diesel engine exhaust prepared in Examples 1-6 of the present invention.
具体实施方式Detailed ways
以下通过具体实施方式结合附图对本发明的技术方案进行进一步的说明和描述。The technical solutions of the present invention will be further illustrated and described below through specific embodiments in conjunction with the accompanying drawings.
下述实施例中的试验方法,如无特别说明,均为常规方法;下述实施例中所用的试验材料中碳烟为德国Printex,平均粒径25nm。其它材料及试剂,如无特别说明,购自常规化学试剂商店;所涉及的检测或测试方法,如无特别说明,均为常规方法。The test methods in the following examples, unless otherwise specified, are conventional methods; the soot used in the test materials in the following examples is German Printex, with an average particle size of 25nm. Other materials and reagents, unless otherwise specified, were purchased from conventional chemical reagent stores; the detection or testing methods involved, unless otherwise specified, were conventional methods.
实施例1Example 1
(1)按照结构通式Ag-MnxCe1-xOy(x=0.05)称取如下原料组分Ce(NO3)3·6H2O,AgNO3,Mn(NO3)2,KOH和氨水;(1) According to the general structural formula Ag-Mn x Ce 1-x O y (x=0.05), weigh the following raw material components Ce(NO 3 ) 3 ·6H 2 O, AgNO 3 , Mn(NO 3 ) 2 , KOH and ammonia;
(2)将Ce(NO3)3·6H2O、Mn(NO3)2和去离子水混合制成第一溶液(Ce(NO3)3和Mn(NO3)2的浓度均为0.2mol/L),将AgNO3和氨水混合制成第二溶液(AgNO3的浓度为0.2mol/L,氨水的浓度为1~3mol/L),将KOH和去离子水混合制成浓度为1mol/L的KOH溶液;(2) Mix Ce(NO 3 ) 3 ·6H 2 O, Mn(NO 3 ) 2 and deionized water to make the first solution (the concentrations of Ce(NO 3 ) 3 and Mn(NO 3 ) 2 are both 0.2 mol/L), mix AgNO 3 and ammonia water to make the second solution (the concentration of AgNO 3 is 0.2 mol/L, and the concentration of ammonia water is 1-3 mol/L), and mix KOH and deionized water to make a concentration of 1 mol /L KOH solution;
(3)将第一溶液和第二溶液以相同的速度缓慢滴入KOH溶液中,同时机械搅拌并得到均匀的沉淀;(3) Slowly drop the first solution and the second solution into the KOH solution at the same speed, while stirring mechanically to obtain a uniform precipitation;
(4)将上述沉淀进行真空干燥(60~120℃,9~12h)后研成粉末,然后于500℃焙烧2h后自然冷却至室温,即得所述柴油机尾气碳烟脱除金属复合氧化物催化剂;(4) Vacuum-dry the above precipitate (60-120°C, 9-12h) and grind it into powder, then calcined at 500°C for 2h and then cool naturally to room temperature to obtain the metal composite oxide for removing soot from diesel engine exhaust catalyst;
将所得的柴油机尾气碳烟脱除金属复合氧化物催化剂进行XRD测试,结果如图1:材料为立方萤石相二氧化铈氧化物;The obtained diesel engine exhaust soot removal metal composite oxide catalyst was tested by XRD, and the results are shown in Figure 1: the material is cubic fluorite phase ceria oxide;
将所得的柴油机尾气碳烟脱除金属复合氧化物催化剂进行催化碳烟活性测试,所得T50为356℃(如图2所示):碳烟催化氧化在常压固定床不锈钢反应管中进行性能评价,接触条件为松散接触,催化剂与碳烟质量比为10∶1。原料气中O2含量为5%,NO为1000ppm,其余为Ar,气体流速为50mL.min-1。使用GC-2060型气相色谱仪,在线检测CO2,T50对应碳烟转化率为50%时的温度。The obtained diesel engine exhaust soot removal metal composite oxide catalyst is tested for catalytic soot activity, and the obtained T50 is 356°C (as shown in Figure 2): soot catalytic oxidation is carried out in an atmospheric pressure fixed bed stainless steel reaction tube. For evaluation, the contact condition is loose contact, and the mass ratio of catalyst to soot is 10:1. The O2 content in the feed gas is 5%, the NO is 1000ppm, the rest is Ar, and the gas flow rate is 50mL.min-1. GC-2060 gas chromatograph was used to detect CO 2 online, and T 50 corresponds to the temperature when the conversion rate of soot is 50%.
实施例2Example 2
制备通式为Ag-Mn0.1Ce0.9Oy(x=0.1)的柴油机尾气碳烟脱除金属复合氧化物催化剂,催化剂活性评价方法同实施例1,XRD测试结果见图1,所得的Ag-Mn0.1Ce0.9Oy复合氧化物催化剂的T50为321℃(如图2所示)。Preparation general formula is Ag-Mn 0.1 Ce 0.9 O y (x=0.1) diesel engine exhaust soot removal metal composite oxide catalyst, catalyst activity evaluation method is the same as embodiment 1, XRD test result is shown in Fig. 1, gained Ag- The T 50 of the Mn 0.1 Ce 0.9 O y composite oxide catalyst is 321 °C (as shown in Figure 2).
实施例3Example 3
制备通式为Ag-Mn0.2Ce0.8Oy(x=0.2)的柴油机尾气碳烟脱除金属复合氧化物催化剂,催化剂活性评价方法同实施例1,XRD测试结果见图1,所得的Ag-Mn0.2Ce0.8Oy复合氧化物催化剂的T50为350℃(如图2所示)。Preparation general formula is Ag-Mn 0.2 Ce 0.8 O y (x=0.2) diesel engine exhaust soot removal metal composite oxide catalyst, catalyst activity evaluation method is the same as embodiment 1, XRD test result is shown in Fig. 1, gained Ag- The T 50 of the Mn 0.2 Ce 0.8 O y composite oxide catalyst is 350 °C (as shown in Figure 2).
实施例4Example 4
制备通式为Ag-Mn0.3Ce0.7Oy(x=0.3)的柴油机尾气碳烟脱除金属复合氧化物催化剂,催化剂活性评价方法同实施例1,结果见图1,所得的Ag-Mn0.3Ce0.7Oy复合氧化物催化剂的T50为353℃(如图2所示)。The preparation general formula is Ag-Mn 0.3 Ce 0.7 O y (x=0.3) the diesel engine exhaust soot removes metal composite oxide catalyst, the catalyst activity evaluation method is the same as embodiment 1, the result is shown in Fig. 1, the obtained Ag-Mn 0.3 The T50 of the Ce 0.7 O y composite oxide catalyst is 353 °C (as shown in Figure 2).
实施例5Example 5
制备通式为Ag-Mn0.4Ce0.6Oy(x=0.4)的柴油机尾气碳烟脱除金属复合氧化物催化剂,催化剂活性评价方法同实施例1,XRD测试结果见图1,所得的Ag-Mn0.4Ce0.6Oy复合氧化物催化剂的T50为368℃(如图2所示)。Preparation general formula is Ag-Mn 0.4 Ce 0.6 O y (x=0.4) diesel engine exhaust soot removal metal composite oxide catalyst, catalyst activity evaluation method is the same as embodiment 1, XRD test result is shown in Fig. 1, gained Ag- The T 50 of the Mn 0.4 Ce 0.6 O y composite oxide catalyst is 368 °C (as shown in Figure 2).
实施例6Example 6
制备通式为Ag-Mn0.5Ce0.5Oy(x=0.5)的柴油机尾气碳烟脱除金属复合氧化物催化剂,催化剂活性评价方法同实施例1,XRD测试结果见图1,所得的Ag-Mn0.5Ce0.5Oy复合氧化物催化剂的T50为372℃(如图2所示)。Preparation general formula is Ag-Mn 0.5 Ce 0.5 O y (x=0.5) diesel engine exhaust soot removal metal composite oxide catalyst, catalyst activity evaluation method is the same as embodiment 1, XRD test result is shown in Fig. 1, gained Ag- The T 50 of the Mn 0.5 Ce 0.5 O y composite oxide catalyst is 372 °C (as shown in Figure 2).
本领域普通技术人员可知,本发明的技术方案在下述范围内变化时,仍然能够得到与上述实施例相同或相近的技术效果,仍然属于本发明的保护范围:Those of ordinary skill in the art know that when the technical solution of the present invention changes within the following ranges, the same or similar technical effects as those of the above-mentioned embodiments can still be obtained, and still belong to the protection scope of the present invention:
一种柴油机尾气碳烟脱除金属复合氧化物催化剂,其结构通式为Ag-MnxCe1-xOy,其中x=0.05~0.5。A metal composite oxide catalyst for removing soot from diesel engine tail gas, the general structure formula of which is Ag-Mn x Ce 1-x O y , where x=0.05-0.5.
上述柴油机尾气碳烟脱除金属复合氧化物催化剂的制备方法,包括如下步骤:The preparation method of the above-mentioned diesel engine exhaust soot removal metal composite oxide catalyst comprises the following steps:
(1)按照所述结构通式称取如下原料组分Ce(NO3)3·6H2O,AgNO3,Mn(NO3)2,KOH和氨水;(1) Weigh the following raw material components Ce(NO 3 ) 3 ·6H 2 O, AgNO 3 , Mn(NO 3 ) 2 , KOH and ammonia water according to the general structural formula;
(2)将Ce(NO3)3·6H2O、Mn(NO3)2和去离子水混合制成第一溶液,将AgNO3和氨水混合制成第二溶液,将KOH和去离子水混合制成KOH溶液;(2) Mix Ce(NO 3 ) 3 ·6H 2 O, Mn(NO 3 ) 2 and deionized water to make the first solution, mix AgNO 3 and ammonia water to make the second solution, mix KOH and deionized water Mix to make KOH solution;
(3)将第一溶液和第二溶液以相同的速度缓慢滴入KOH溶液中,同时搅拌并得到均匀的沉淀;(3) Slowly drop the first solution and the second solution into the KOH solution at the same speed, while stirring and obtaining a uniform precipitation;
(4)将上述沉淀进行干燥后研成粉末,然后于450~550℃焙烧后自然冷却至室温,即得所述柴油机尾气碳烟脱除金属复合氧化物催化剂。(4) Dry the above precipitate and grind it into powder, then roast it at 450-550° C. and cool it down to room temperature naturally to obtain the metal composite oxide catalyst for removing soot from diesel engine exhaust.
所述第一溶液中,Ce(NO3)3和Mn(NO3)2的浓度均为0.1~0.3mol/L。所述第二溶液中,AgNO3的浓度为0.05~0.2mol/L,氨水的浓度为1~3mol/L。所述KOH溶液的浓度为1.0~3.0mol/L。所述步骤(4)的干燥为真空干燥,干燥温度为60~120℃,时间为9~12h。所述焙烧的时间为1~3h。In the first solution, the concentrations of Ce(NO 3 ) 3 and Mn(NO 3 ) 2 are both 0.1˜0.3 mol/L. In the second solution, the concentration of AgNO 3 is 0.05-0.2 mol/L, and the concentration of ammonia water is 1-3 mol/L. The concentration of the KOH solution is 1.0-3.0 mol/L. The drying in the step (4) is vacuum drying, the drying temperature is 60-120° C., and the drying time is 9-12 hours. The roasting time is 1-3 hours.
以上所述,仅为本发明的较佳实施例而已,故不能依此限定本发明实施的范围,即依本发明专利范围及说明书内容所作的等效变化与修饰,皆应仍属本发明涵盖的范围内。The above is only a preferred embodiment of the present invention, so the scope of the present invention cannot be limited accordingly, that is, equivalent changes and modifications made according to the patent scope of the present invention and the content of the specification should still be covered by the present invention In the range.
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