CN100387522C - Preparation process of high oxygen storage nanometer cerium-based composite oxide material - Google Patents
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Abstract
本发明涉及复合氧化物制造方法技术领域,特别是高储氧纳米铈基复合氧化物材料的制备工艺。本发明针对现有的复合氧化物制备方法所存在的会对环境造成严重污染缺陷,提供一种高储氧纳米铈基复合氧化物材料的制备工艺。本发明的制备工艺为:将一定配比的高储氧纳米复合氧化物材料前驱物用溶剂溶解,加入沉淀剂共沉淀,过滤洗涤沉淀,将沉淀和有机酸溶液混合,然后经干燥、焙烧制得高储氧纳米复合氧化物材料。用本发明的方法所获得的复合氧化物材料具有很高的氧恢复能力。在本发明的制备工艺中不会因使用硝酸盐等物质产生氮氧化物,只有水和二氧化碳排出,沉淀经过滤洗涤后的滤液中所含盐类可回收利用,不会对环境造成严重污染,具有环境友好的特点。
The invention relates to the technical field of composite oxide manufacturing methods, in particular to the preparation process of high oxygen storage nanometer cerium-based composite oxide materials. The invention provides a preparation process of a high-oxygen-storage nanometer cerium-based composite oxide material aiming at the defect that the existing composite oxide preparation method will cause serious pollution to the environment. The preparation process of the present invention is: dissolving a certain ratio of high oxygen storage nano-composite oxide material precursor with a solvent, adding a precipitant for co-precipitation, filtering and washing the precipitate, mixing the precipitate with an organic acid solution, and then drying and roasting High oxygen storage nanocomposite oxide materials. The composite oxide material obtained by the method of the invention has high oxygen recovery ability. In the preparation process of the present invention, no nitrogen oxides will be produced due to the use of nitrates and other substances, only water and carbon dioxide will be discharged, and the salts contained in the filtrate after the precipitation is filtered and washed can be recycled, and will not cause serious pollution to the environment. It is environmentally friendly.
Description
技术领域 technical field
本发明涉及复合氧化物制造方法技术领域,特别是高储氧纳米铈基复合氧化物材料的制备工艺。The invention relates to the technical field of composite oxide manufacturing methods, in particular to the preparation process of high oxygen storage nanometer cerium-based composite oxide materials.
背景技术 Background technique
CeO2是具有萤石结构的氧化型催化剂的优良助剂,它具有较高的储存和释放氧的能力,并通过氧化还原对Ce4+/Ce3+进行氧化还原反应,对空-燃比起着化学调节剂的作用。CeO2中添加ZrO2等过渡金属氧化物可形成铈基复合氧化物,大大提高其储存和释放氧的性能及抗烧结性能,具有优异的化学反应性能及催化效率等,被广泛用于汽车尾气三效催化剂和CO、CH4等氧化。现有的复合氧化物材料通常采用溶胶-凝胶法、共沉淀法等方法进行制备,其中,用溶胶-凝胶法制得的复合氧化物材料虽然具有粉体粒径小、纯度高且化学均匀性良好的优点,但存在前驱物原料价格高、高温处理下会使颗粒快速团聚以及因可能使用硝酸盐在复合氧化物的制备过程中排出氮氧化物造成环境污染的缺点;共沉淀法虽具有反应过程简单、成本低的优点,但易引入杂质;有人采用高能球磨法制得了Ce0.5Zr0.5O2复合氧化物,但其比表面积较小,在16-20m2/g之间。CeO 2 is an excellent additive for oxidation-type catalysts with a fluorite structure. It has a high ability to store and release oxygen, and conducts redox reactions on Ce 4+ /Ce 3+ through redox. The role of chemical regulators. Adding transition metal oxides such as ZrO 2 to CeO 2 can form a cerium-based composite oxide, which greatly improves its ability to store and release oxygen and anti-sintering performance, and has excellent chemical reaction performance and catalytic efficiency. It is widely used in automobile exhaust Three-way catalyst and oxidation of CO, CH4 , etc. Existing composite oxide materials are usually prepared by methods such as sol-gel method and co-precipitation method. Among them, the composite oxide materials prepared by sol-gel method have small powder particle size, high purity and chemical uniformity. However, it has the disadvantages of high price of precursor raw materials, rapid agglomeration of particles under high temperature treatment, and the possible use of nitrates to discharge nitrogen oxides during the preparation of composite oxides, causing environmental pollution; although the co-precipitation method has The reaction process is simple and the cost is low, but it is easy to introduce impurities; someone has prepared Ce 0.5 Zr 0.5 O 2 composite oxide by high-energy ball milling method, but its specific surface area is small, between 16-20m 2 /g.
发明内容 Contents of the invention
本发明针对现有的复合氧化物制备方法所存在的上述不足之处,提供一种高储氧纳米铈基复合氧化物材料的制备工艺。Aiming at the above-mentioned shortcomings in the existing composite oxide preparation methods, the present invention provides a preparation process of a high oxygen storage nanometer cerium-based composite oxide material.
本发明的高储氧纳米铈基复合氧化物材料的制备工艺为:将一定配比的高储氧纳米复合氧化物材料前驱物用溶剂溶解,加入沉淀剂共沉淀,过滤洗涤沉淀,将沉淀和有机酸溶液混合,然后经干燥、焙烧制得高储氧纳米复合氧化物材料。其中,前驱物包括铈的可溶性盐及氧化物中的一种或一种以上与过渡元素、碱土金属元素及铝、镓、硅、锡、铋的可溶性盐、氢氧化物和氧化物中的一种或一种以上;溶剂采用水或酸;沉淀剂为碳酸铵、碳酸氢铵、氨水、碳酸钠、碳酸钾、碳酸氢钠、碳酸氢钾、氢氧化钠、氢氧化钾中的一种或一种以上,所用的沉淀剂总的物质的量是复合氧化物前驱物总的物质的量的0.5~6倍;有机酸为柠檬酸、苹果酸和酒石酸中的一种或一种以上,所用的有机酸总的物质的量是复合氧化物前驱物总的物质的量的0.5~20倍。The preparation process of the high oxygen storage nano cerium-based composite oxide material of the present invention is as follows: dissolving a certain ratio of high oxygen storage nano composite oxide material precursor with a solvent, adding a precipitant for co-precipitation, filtering and washing the precipitate, and separating the precipitate and The organic acid solutions are mixed, then dried and calcined to obtain a high oxygen storage nanometer composite oxide material. Among them, the precursors include one or more of the soluble salts and oxides of cerium and one or more of transition elements, alkaline earth metal elements, and soluble salts, hydroxides and oxides of aluminum, gallium, silicon, tin and bismuth. one or more; the solvent is water or acid; the precipitant is one or more of ammonium carbonate, ammonium bicarbonate, ammonia water, sodium carbonate, potassium carbonate, sodium bicarbonate, potassium bicarbonate, sodium hydroxide, More than one kind, the total substance amount of the precipitant used is 0.5 to 6 times the total substance amount of the composite oxide precursor; the organic acid is one or more of citric acid, malic acid and tartaric acid, and the used The total substance amount of the organic acid is 0.5 to 20 times that of the composite oxide precursor.
本发明的高储氧纳米铈基复合氧化物材料的制备工艺的步骤如下:The steps of the preparation process of the high oxygen storage nanometer cerium-based composite oxide material of the present invention are as follows:
(1)将前驱物溶解,加入沉淀剂,过滤、洗涤沉淀;(1) Dissolve the precursor, add a precipitating agent, filter and wash the precipitate;
(2)将沉淀和有机酸溶液混合,得到溶胶,再于室温至140℃下干燥,得干凝胶;(2) Mix the precipitate with the organic acid solution to obtain a sol, and then dry it at room temperature to 140°C to obtain a xerogel;
(3)将干凝胶在高温炉中400~1000℃焙烧1~8小时,即制成高储氧纳米铈基复合氧化物材料成品。(3) Roasting the xerogel in a high-temperature furnace at 400-1000° C. for 1-8 hours to produce a finished high-oxygen-storage nano-cerium-based composite oxide material.
本发明高储氧纳米铈基复合氧化物材料的制备工艺过程中不会因使用硝酸盐等物质产生氮氧化物,只有水和二氧化碳排出;沉淀经过滤洗涤后的滤液中所含盐类可回收利用,不会对环境造成严重污染,具有环境友好的特点。During the preparation process of the high-oxygen-storage nano-cerium-based composite oxide material of the present invention, no nitrogen oxides will be produced due to the use of nitrate and other substances, and only water and carbon dioxide will be discharged; the salts contained in the filtrate after the precipitation is filtered and washed can be recovered Utilization, will not cause serious pollution to the environment, and has the characteristics of environmental friendliness.
另外,本发明的高储氧纳米铈基复合氧化物材料的制备工艺也适用于铜锰基等过渡金属复合氧化物的制备。In addition, the preparation process of the high oxygen storage nanometer cerium-based composite oxide material of the present invention is also applicable to the preparation of copper-manganese-based transition metal composite oxides.
附图说明 Description of drawings
附图1为CexZr1-xO2复合氧化物材料的TPR图谱。Accompanying drawing 1 is the TPR spectrum of CexZr1 -xO2 composite oxide material.
附图2为Ce0.8Zr0.2O2复合氧化物材料经920℃还原后再氧化的TPR图谱。Figure 2 is the TPR spectrum of Ce 0.8 Zr 0.2 O 2 composite oxide material after reduction at 920°C and then oxidation.
具体实施方式 Detailed ways
下面通过实施例对本发明的高储氧纳米铈基复合氧化物材料的制备工艺作进一步说明,但本发明并不限于这些实施例。The preparation process of the high oxygen storage nanometer cerium-based composite oxide material of the present invention will be further illustrated by examples below, but the present invention is not limited to these examples.
实施例1Example 1
Ce0.3Zr0.7O2的详细制备过程:称取1.42g Ce(NO3)3·6H2O和3.27g Zr(NO3)4·5H2O溶于水中,再加入含有2.13g Na2CO3的水溶液进行共沉淀,过滤、洗涤沉淀,将沉淀溶于含有16.92g柠檬酸的溶液中得凝胶,95~100℃蒸发成凝胶,再于120℃烘12小时,最后经650℃焙烧4小时。该方法制得的Ce0.3Zr0.7O2复合氧化物,比表面积是32m2/g,920℃下的储氧量571μmol/g,晶粒为11.3nm。The detailed preparation process of Ce 0.3 Zr 0.7 O 2 : Weigh 1.42g Ce(NO 3 ) 3 ·6H 2 O and 3.27g Zr(NO 3 ) 4 ·5H 2 O to dissolve in water, then add 2.13g Na 2 CO Co-precipitate the aqueous solution of 3 , filter and wash the precipitate, dissolve the precipitate in a solution containing 16.92g of citric acid to obtain a gel, evaporate to a gel at 95-100°C, bake at 120°C for 12 hours, and finally bake at 650°C 4 hours. The Ce 0.3 Zr 0.7 O 2 composite oxide prepared by this method has a specific surface area of 32 m 2 /g, an oxygen storage capacity of 571 μmol/g at 920° C., and a grain size of 11.3 nm.
实施例2Example 2
Ce0.5Zr0.5O2的详细制备过程:称取2.20g Ce(NO3)3·6H2O和2.18g Zr(NO3)4·5H2O溶于水中,再加入含有1.88g Na2CO3的水溶液进行共沉淀,过滤、洗涤沉淀,将沉淀溶于含有14.94g柠檬酸的溶液中得凝胶,95~100℃蒸发成凝胶,再于120℃烘12小时,最后经650℃焙烧4小时。该方法制得的Ce0.5Zr0.5O2复合氧化物,比表面积是55m2/g,920℃下的储氧量599μmol/g,晶粒为4.0nm。The detailed preparation process of Ce 0.5 Zr 0.5 O 2 : Weigh 2.20g Ce(NO 3 ) 3 6H 2 O and 2.18g Zr(NO 3 ) 4 5H 2 O and dissolve them in water, then add 1.88g Na 2 CO Co-precipitate the aqueous solution of 3 , filter and wash the precipitate, dissolve the precipitate in a solution containing 14.94g of citric acid to obtain a gel, evaporate to a gel at 95-100°C, bake at 120°C for 12 hours, and finally bake at 650°C 4 hours. The Ce 0.5 Zr 0.5 O 2 composite oxide prepared by the method has a specific surface area of 55 m 2 /g, an oxygen storage capacity of 599 μmol/g at 920° C., and a grain size of 4.0 nm.
实施例3Example 3
Ce0.6Zr0.4O2的详细制备过程:称取2.56g Ce(NO3)3·6H2O和1.69g Zr(NO3)4·5H2O溶于水中,再加入含有1.77g Na2CO3的水溶液进行共沉淀,过滤、洗涤沉淀,将沉淀溶于含有14.04g柠檬酸的溶液中得凝胶,95~100℃蒸发成凝胶,再于120℃烘12小时,最后经650℃焙烧4小时。该方法制得的Ce0.6Zr0.4O2复合氧化物,比表面积是36m2/g,920℃下的储氧量700μmol/g,晶粒为4.9nm。The detailed preparation process of Ce 0.6 Zr 0.4 O 2 : Weigh 2.56g Ce(NO 3 ) 3 6H 2 O and 1.69g Zr(NO 3 ) 4 5H 2 O and dissolve them in water, then add 1.77g Na 2 CO Co-precipitate the aqueous solution of 3 , filter and wash the precipitate, dissolve the precipitate in a solution containing 14.04g of citric acid to obtain a gel, evaporate to a gel at 95-100°C, bake at 120°C for 12 hours, and finally bake at 650°C 4 hours. The Ce 0.6 Zr 0.4 O 2 composite oxide prepared by the method has a specific surface area of 36 m 2 /g, an oxygen storage capacity of 700 μmol/g at 920° C., and a grain size of 4.9 nm.
实施例4Example 4
Ce0.8Zr0.2O2的详细制备过程:称取3.21g Ce(NO3)3·6H2O和0.79g Zr(NO3)4·5H2O溶于水中,再加入含有1.57g Na2CO3的水溶液进行共沉淀,过滤、洗涤沉淀,将沉淀溶于含有12.42g柠檬酸的溶液中得凝胶,95~100℃蒸发成凝胶,再于120℃烘12小时,最后经650℃焙烧4小时。该方法制得的Ce0.8Zr0.2O2复合氧化物,比表面积是31m2/g,920℃下的储氧量496μmol/g,晶粒为11.8nm。The detailed preparation process of Ce 0.8 Zr 0.2 O 2 : Weigh 3.21g Ce(NO 3 ) 3 ·6H 2 O and 0.79g Zr(NO 3 ) 4 ·5H 2 O to dissolve in water, then add 1.57g Na 2 CO Co-precipitate the aqueous solution of 3 , filter and wash the precipitate, dissolve the precipitate in a solution containing 12.42g of citric acid to obtain a gel, evaporate to a gel at 95-100°C, bake at 120°C for 12 hours, and finally bake at 650°C 4 hours. The Ce 0.8 Zr 0.2 O 2 composite oxide prepared by this method has a specific surface area of 31 m 2 /g, an oxygen storage capacity of 496 μmol/g at 920° C., and a grain size of 11.8 nm.
实施例5Example 5
在含5%H2的H2-N2混合气下,利用TPR技术考察了CexZr1-xO2复合氧化物材料的还原性能,结果见图1。Under the H 2 -N 2 mixed gas containing 5% H 2 , the reduction performance of the Cex Zr 1-x O 2 composite oxide material was investigated by TPR technique, and the results are shown in Figure 1.
实施例6Example 6
Ce0.8Zr0.2O2复合氧化物材料经920℃还原后在不同温度空气中再氧化30分钟后TPR实验,结果见图2。由图2可见,本发明用本发明的制备工艺获得的Ce0.8Zr0.2O2复合氧化物材料具有很高的氧恢复能力,即使在50℃温度也能基本恢复。The Ce 0.8 Zr 0.2 O 2 composite oxide material was reduced at 920°C and re-oxidized in air at different temperatures for 30 minutes before TPR experiment. The results are shown in Figure 2. It can be seen from Fig. 2 that the Ce 0.8 Zr 0.2 O 2 composite oxide material obtained by the preparation process of the present invention has a very high oxygen recovery ability, and can basically recover even at a temperature of 50°C.
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| WO1995018068A1 (en) * | 1993-12-24 | 1995-07-06 | Rhone-Poulenc Chimie | Composition precursor and cerium and zirconium mixed oxide based composition, method for its preparation and use thereof |
| CN1194625A (en) * | 1996-04-05 | 1998-09-30 | 三德金属工业株式会社 | Composite oxide having oxygen absorption and release capabilities and process for preparing the same |
| CN1241988A (en) * | 1996-12-27 | 2000-01-19 | 阿南化成株式会社 | Zirconium-cerium composite oxide, method for producing same, and cocatalyst for exhaust gas purification |
| WO2004085806A2 (en) * | 2003-03-18 | 2004-10-07 | Rhodia Electronics And Catalysis | Reduced maximum reductibility temperature zirconium oxide and cerium oxide based composition, method for the production and use thereof as a catalyst |
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| WO1995018068A1 (en) * | 1993-12-24 | 1995-07-06 | Rhone-Poulenc Chimie | Composition precursor and cerium and zirconium mixed oxide based composition, method for its preparation and use thereof |
| CN1194625A (en) * | 1996-04-05 | 1998-09-30 | 三德金属工业株式会社 | Composite oxide having oxygen absorption and release capabilities and process for preparing the same |
| CN1241988A (en) * | 1996-12-27 | 2000-01-19 | 阿南化成株式会社 | Zirconium-cerium composite oxide, method for producing same, and cocatalyst for exhaust gas purification |
| WO2004085806A2 (en) * | 2003-03-18 | 2004-10-07 | Rhodia Electronics And Catalysis | Reduced maximum reductibility temperature zirconium oxide and cerium oxide based composition, method for the production and use thereof as a catalyst |
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