Perovskite-type metal oxide compounds and methods of making and using thereof
View Patent ↗Perovskite-type catalyst consists essentially of a metal oxide composition and methods of using them are provided. The metal oxide composition is represented by the general formula A a−x B x MO b , in which A is a mixture of elements originally in the form of single phase mixed lanthanides collected from bastnasite; B is a divalent or monovalent cation; M is at least one element selected from the group consisting of elements of an atomic number of from 23 to 30, 40 to 51, and 73 to 80; a is 1 or 2; b is 3 when a is 1 or b is 4 when a is 2; and x is a number defined by 0≦x<0.5. Methods of making and using the perovskite-type catalysts are also provided. The perovskite-type catalyst may be used to reduce nitrogen oxides, oxidize carbon monoxide, and oxidize hydrocarbons in an exhaust stream from a motor vehicle. Methods of such a use are provided.
1. A method of reducing nitrogen oxides, oxidizing carbon monoxide, and oxidizing hydrocarbons in an exhaust stream from a motor vehicle, said method comprising: contacting the exhaust stream with a perovskite-type catalyst consisting essentially of a metal oxide composition represented by the general formula:
A a-x B x MO b
wherein
A is a mixture of elements originally in the form of a single phase mixed lanthanide collected from bastnasite;
B is a divalent or monovalent cation;
M is at least one element selected from the group consisting of elements of an atomic number of from 22 to 30, 40 to 51, and 73 to 80;
a is 1 or 2;
b is 3 when a is 1 or b is 4 when a is 2; and
x is a number defined by 0≦x<0.7.
2. The method of claim 1 , wherein A comprises elements selected from the group consisting of lanthanides having an atomic number of from 57 to 71.
3. The method of claim 1 , wherein B is selected from the group consisting of Ca, Sr, and K.
4. The method of claim 1 , wherein M is selected from the group consisting of Fe, Mn, Co, Ni, Ru, Cr, and mixtures thereof.
5. The method of claim 1 , wherein the perovskite-type catalyst is selected from the group consisting of Ln 0.6 Ca 0.4 CoO 3 , Ln 0.83 Sr 0.17 MnO 3 , Ln 0.7 Sr 0.3 CrO 3 , Ln 0.6 Ca 0.4 Fe 0.8 Mn 0.2 O 3 , Ln 0.8 Sr 0.2 Mn 0.9 Ni 0.04 Ru 0.06 O 3 , Ln 0.8 K 0.2 Mn 0.95 Ru 0.05 O 3 , Ln 0.7 Sr 0.3 Cr 0.95 Ru 0.05 O 3 , LnNiO 3 , Ln 2 (Cu 0.6 Co 0.2 Ni 0.2 )O 4 , Ln 0.6 Ca 0.4 Fe 0.8 Mn 0.2 O 3 , Ln 0.8 Sr 0.2 Mn 0.9 Ni 0.04 Pd 0.06 O 3 , Ln 0.8 Sr 0.2 Mn 0.9 Ni 0.04 Pt 0.06 O 3 , Ln 0.7 Sr 0.3 Mn 0.9 Ni 0.04 Ru 0.06 O 3 , LnMn 0.5 Cu 0.5 O 3 , LnMn 0.8 Ni 0.10 Cu 0.10 O 3 , Ln 0.7 Sr 0.3 Mn 0.9 Pd 0.1 O 3 , Ln 0.5 Sr 0.5 Mn 0.9 Pd 0.1 O 3 , Ln 0.8 Sr 0.2 MnO 3 , Ln 0.5 Sr 0.5 Mn 0.98 Pd 0.02 O 3 , Ln 0.8 Sr 0.2 Mn 0.96 Pd 0.04 O 3 , Ln 0.5 Sr 0.5 Mn 0.95 Pt 0.05 O 3 , Ln 0.8 Sr 0.2 Mn 0.92 Ni 0.05 Pd 0.03 O 3 , Ln 0.8 Sr 0.2 Mn 0.94 Pt 0.05 Rh 0.01 O 3 , Ln 0.8 Ba 0.2 Mn 0.94 Pd 0.06 O 3 , Ln 0.5 Sr 0.5 Mn 0.98 Rh 0.02 O 3 , Ln 0.8 Sr 0.2 Co 0.9 Ru 0.1 O 3 , Ln 0.8 Sr 0.2 Mn 0.9 Ru 0.1 O 3 , Ln 0.5 Sr 0.5 Mn 0.95 Pd 0.05 O 3 , Ln 0.5 Sr 0.5 Mn 0.95 Ru 0.05 O 3 , and Ln 0.5 Sr 0.5 MnO 3 , where Ln is a mixture of lanthanides originally in the form of a single phase mixed lanthanide collected from bastnasite.
6. The method of claim 1 , wherein said contacting is at a temperature between 300° C. and 900° C.
7. The method of claim 1 , wherein said contacting is at a temperature between 500° C. and 700° C.
8. The method of claim 1 , wherein said exhaust stream has a redox potential R that is in the range of between about 0.86 and about 1.17 during said contacting.
9. The method of claim 1 , wherein said catalyst is supported on a structure.
10. The method of claim 9 , wherein said structure is a honeycomb support.
11. The method of claim 10 , wherein said honeycomb support is a ceramic honeycomb support or a metal honeycomb support.
12. The method of claim 9 , wherein said structure is in a form of beads or pellets.
13. The method of claim 9 , wherein a carrier material or a mixture of carrier materials is deposited onto the support structure, thereby forming a washcoat on the surface of the support structure.
14. The method of claim 13 , wherein a solution of salts of element A and salts or oxides of elements B and M is impregnated into said washcoat.
15. The method of claim 14 , wherein the impregnated washcoat is died and calcined to form the perovskite-type catalyst in the form of a dispersion.
16. The method of claim 1 , wherein said perovskite-type catalyst is a three-way catalyst.
17. A method of purifying industrial process emissions containing hydrocarbons, carbon monoxide, and nitrogen oxides, the method comprising:contacting said emissions with a perovskite-type catalyst, thereby purifying said emissions, said perovskite-type catalyst consisting essentially of a metal oxide composition represented by the general formula:
A a-x B x MO b
wherein A is a mixture of elements originally in the form of a single phase mixed lanthanide collected from bastnasite;
B is a divalent or monovalent cation;
M is at least one element selected from the group consisting of elements of an atomic
number of from 22 to 30, 40 to 51, and 73 to 80;
a is 1 or 2;
b is 3 when a is 1 or b is 4 when a is 2; and
x is a number defined by 0≦x<0.7.
18. The method of claim 17 , wherein purifying said exhaust gas comprises reducing the nitrogen oxides and oxidizing the carbon monoxide and hydrocarbons in the exhaust gas.
19. The method of claim 17 , wherein said contacting is at a temperature between 300° C. and 900° C.
20. The method of claim 17 , wherein the emissions have a redox potential R in the range of between about 0.86 and 1.17 during said contacting.