Rare-Earth Phosphate Alumina Composite for Use in Emission Control Catalysts and Method for Making the Same
20200346194 ยท 2020-11-05
Inventors
Cpc classification
B01J37/0209
PERFORMING OPERATIONS; TRANSPORTING
B01D53/945
PERFORMING OPERATIONS; TRANSPORTING
B01J35/393
PERFORMING OPERATIONS; TRANSPORTING
B01J37/086
PERFORMING OPERATIONS; TRANSPORTING
B01J35/30
PERFORMING OPERATIONS; TRANSPORTING
Y02T10/12
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
B01J35/40
PERFORMING OPERATIONS; TRANSPORTING
B01J37/088
PERFORMING OPERATIONS; TRANSPORTING
International classification
B01J27/18
PERFORMING OPERATIONS; TRANSPORTING
B01J35/00
PERFORMING OPERATIONS; TRANSPORTING
B01J37/02
PERFORMING OPERATIONS; TRANSPORTING
Abstract
The present invention relates to a composition for use in a catalyst system in emission control systems comprising a transition alumina based material and rare earth phosphates and to a method for making same.
Claims
1. A composition for use as a support in a catalyst system comprising: i) a transition alumina based material; and ii) a rare-earth phosphate, the rare earth phosphate being characterized by having a crystallite size that is lower than 50 nm after calcination at 1000 C. for 3 hours.
2. The composition of claim 1, wherein the transition alumina based material comprises transition alumina derived from boehmite, silica-alumina, doped alumina or mixtures thereof.
3. The composition of claim 1 including at least 50 wt. % of the transition alumina based material.
4. The composition of claim 1, wherein the rare-earth phosphate comprises LaPO.sub.4, YPO.sub.4, NdPO.sub.4 or mixtures thereof.
5. The composition of claim 1 comprising between 3 and 50 wt. % of the rare earth phosphate.
6. The composition of claim 1, wherein the rare earth phosphate has a crystallite size that is lower than 15 nm after calcination at 1000 C. for 3 hours.
7. The composition of claim 1, wherein the rare earth phosphate has a crystallite size that is lower than 10 nm after calcination at 1000 C. for 3 hours.
8. The composition of anyone of claim 1 having a BET specific surface area of at least 50 m.sup.2/g.
9. The composition of claim 1 having a pore volume between 0.2 and 1.2 ml/g.
10. A method to prepare a composition for use as a support in a catalyst system, the method comprising: i) providing a transition alumina rare earth oxide material wherein the transition alumina rare earth oxide material is prepared by a method comprising the following steps: a) preparing a suspension including a transition alumina precursor; b) preparing an aqueous solution including a rare earth salt, wherein the transition alumina precursor includes alumina hydrates of general formulas Al(OH).sub.3 or AlOOH*xH.sub.2O or mixtures thereof; c) combining the suspension with the rare-earth salt solution to form a alumina rare-earth salt mixture; d) drying the alumina rare earth salt mixture to form a dried alumina rare earth salt mixture; e) calcining the dried alumina rare earth salt mixture to form a transition alumina rare earth oxide material; ii) impregnating the transition alumina rare earth oxide material with an aqueous solution including phosphate ions to form an impregnated alumina rare earth oxide material; and iii) calcining the impregnated transition alumina rare earth oxide material.
11. The method of claim 10, wherein the rare earth salt is a rare earth acetate.
12. The method of claim 10 wherein the impregnated transition alumina rare earth oxide material is calcined at a temperature of 600 C. to 1100 C. for 0.5 to 5 hours.
13. The method of claim 10, wherein the composition comprises: i) a transition alumina based material; and ii) a rare-earth phosphate, the rare earth phosphate being characterized by having a crystallite size that is lower than 50 nm after calcination at 1000 C. for 3 hours.
Description
[0054] The invention will now be described with reference to the non-limiting examples and Figures in which:
[0055]
[0056]
[0057]
EXAMPLES
[0058] The crystallite size is determined by the Scherrer method as described above.
[0059] The Surface area is measured by BET and the pore volume by N.sub.2 adsorption as described above.
Experiments
Example 1
[0060] A transition alumina rare earth oxide material made of 20 wt. % lanthanum oxide containing transition alumina having a specific surface area (BET) of 130 m.sup.2/g and a pore volume of 0.97 ml/g was impregnated with an aqueous solution of phosphoric acid (14.4 wt. % H.sub.3PO.sub.4). The product was dried at 120 C. and finally calcined at 1000 C. for 3 hours.
Example 2
[0061] A transition alumina, rare earth oxide material made of 20 wt. % yttrium oxide containing transition alumina having a specific surface area (BET) of 134 m.sup.2/g and a pore volume of 0.98 ml/g was impregnated with an aqueous solution of phosphoric acid (13.2 wt. % H.sub.3PO.sub.4). The product was dried at 120 C. and finally calcined at 1000 C. for 3 hours.
Example 3
[0062] A transition alumina, rare earth oxide material made of 20 wt. % neodymium oxide containing transition alumina having a specific surface area (BET) of 130 m.sup.2/g and a pore volume of 0.97 ml/g was impregnated with an aqueous solution of phosphoric acid (14.4 wt. % H.sub.3PO.sub.4). The product was dried at 120 C. and finally calcined at 1000 C. for 3 hours.
Example 4
[0063] A transition alumina, rare earth oxide material made of 15 wt. % lanthanum oxide containing transition alumina having a specific surface area (BET) of 145 m.sup.2/g and a pore volume of 0.94 ml/g was impregnated with an aqueous solution of phosphoric acid (9.7 wt. % H.sub.3PO.sub.4). The product was dried at 120 C. and finally calcined at 1000 C. for 3 hours.
Comparative Example 1
[0064] LaPO.sub.4 was prepared according to Example 3 from EP 2754489 A1:
[0065] Phosphoric acid solution was added a to Lanthanum nitrate solution in an amount yielding a 1:1 molar ratio of La and P. A pH value of 8 was adjusted by the addition of ammonia solution. The precipitate was separated by filtration and finally calcined at 900 C. for 5 hours.
[0066] The LaPO.sub.4 obtained was combined with alumina. The LaPO.sub.4 powder and a 4 wt. % lanthanum doped alumina having a specific surface area (BET) of 151 m.sup.2/g and a pore volume of 1.02 ml/g were made into a slurry and wet milled. Then the suspension was spray dried and calcined at 1000 C. for 3 hours to obtain the comparative composite.
Comparative Example 2
[0067] CePO.sub.4 was prepared according to Example 6 of GB 1431868 by evaporating (NH.sub.4).sub.2Ce(NO.sub.3).sub.6 on aluminum oxide, using commercially available PURALOX TH100/150, and heating to 400 C. overnight. Then phosphoric acid was added to the cooled mixture. After calcination for 3 h at 1000 C. the comparative product was tested and no CePO.sub.4 was found; only AlPO.sub.4 was found. The specific surface area (BET) of the comparative product was 45 m.sup.2/g.
[0068] The Results are included in Table 1 hereunder:
TABLE-US-00001 TABLE 1 Example Example Example Example Comparative Comparative 1 2 3 4 Example 1 Example 2 Rare-earth phosphate LaPO.sub.4 YPO.sub.4 NdPO.sub.4 LaPO.sub.4 LaPO.sub.4 (CePO.sub.4) Content 26 wt. % 26 wt. % 26 wt. % 18 wt. % 26 wt. % n/a Crystallite* size (nm) 8 10 7 8 64 n/a - no CePO.sub.4 found, only AlPO.sub.4 BET* (m.sup.2/g) 95 106 114 97 83 45 Pore Volume* (ml/g) 0.6 0.84 0.77 0.84 0.64 0.34 Crystallite** size (nm) 11 84 BET** (m.sup.2/g) 59 53 Pore Volume** (ml/g) 0.56 0.37 *as is **after additional calcination for 3 h at 1200 C. (for thermostability)
[0069]
[0070] Further, the SEM cross-section pictures in