Rare earth alumina particulate manufacturing method and application
View Patent ↗A rare earth alumina particulate composition manufacturing method and application are disclosed. The rare earth alumina of the invention is a particulate of porous structure with a molecular formula (RE x ,Al 1-x ) 2 O 3 , phase γ or γ+δ characterized by a particle size distribution ranging from 1 to 80 μm with a D 50 of 5 to 15 μm, a pore size distribution ranging from 0.4-200 nm with an average pore diameter of 8 to 30 nm, a pore volume (PV) raging from 0.5 to 1.2 cc/g and a fresh specific surface area (SA) ranging from 130 to 250 m 2 /g after calcination at 500-900° C. for 5 to 10 hours. The rare earth alumina retains a SA of greater than 60 m 2 /g after calcination at 1200° C. for 4 hours and greater than 40 m 2 /g after calcination at 1200° C. for 50 hours. There is no presence of the α phase or other impurity phases in the long-term aged samples. The rare earth alumina of the invention has a high thermal stability and is a fine three-way catalyst support material. The rare earth alumina is made using wet continuous coprecipitation with a static mixer and a tank reactor featuring simple operation, low cost and high feasibility in industrial production.
1. A calcined alumina catalyst support with at least one rare earth oxide as a stabilizer having a chemical formula (RE x ,Al 1-x ) 2 O 3 , in which, RE denotes one or more rare earth elements selected from the group: La, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er and Tm; the alumina catalyst support being characterized by a rare earth molar content x of 0.005 to 0.04, and after calcination at 1200° C. for 50 hours the alumina catalyst support comprises a surface area (SA) in excess of 30 m 2 /g and a theta phase absent the presence of any alpha phase.
2. The alumina catalyst support according to claim 1 wherein the rare earth alumina is characterized by a rare earth molar content x of 0.01 to 0.03.
3. The alumina catalyst support according to claim 1 wherein the rare earth alumina prior to calcination is characterized by a gamma phase.
4. The alumina catalyst support according to claim 1 wherein the rare earth alumina has a particle size distribution ranging from 1-80 microns with a median size D 50 of 5 to 15 microns.
5. The alumina catalyst support according to claim 1 wherein the rare earth alumina has a fresh pore volume of 0.5 to 1.2 cc/g and a fresh surface area of 130-250 m 2 /g after calcination at 500 to 900° C. for 4-10 hours.
6. The alumina catalyst support according to claim 1 wherein the rare earth alumina retains an SA of greater than 80 m 2 /g after calcination at 1200° C. for 4 hours.
7. The alumina catalyst support according to claim 6 wherein the rare earth alumina retains an SA of greater than 55 m 2 /g after calcination at 1200° C. for 50 hours.
8. The alumina catalyst support according to claim 1 wherein the method of making the rare earth alumina includes wet coprecipitation using a static mixer together with a tank reactor.
9. The alumina catalyst support according to claim 8 wherein the rare earth alumina is prepared by continuous coprecipitation.
10. The alumina catalyst support according to claim 8 wherein the method is an acidic method, with a basic solution of sodium aluminate and an acidic solution of lanthanum nitrate.
11. The alumina catalyst support according to claim 10 wherein the coprecipitation pH ranges from 7-9.
12. The alumina catalyst support according to claim 8 wherein the coprecipitation temperature is from 35 to 90° C.
13. The alumina catalyst support according to claim 8 wherein the method does not include the addition of any surfactants during aging.
14. The alumina catalyst support according to claim 8 wherein the method includes the addition of a dosage of 0.1%-10% based on the rare earth alumina of at least one surfactant selected from the group: polyvinyl alcohol (PVA), polyvinyl amine, polyethylene glycol-200 (PEG-200), triton X-100, isopropyl alcohol and ethanol.
15. The alumina catalyst support according to claim 14 wherein the dosage is 1% to 5% based on the rare earth alumina.
16. The alumina catalyst support according to claim 1 wherein the rare earth alumina is obtained by calcining pseudo-boehmite, aluminum monohydroxide containing rare earth hydroxide, at 500 to 900° C. for 4 to 10 hours.
17. A method of manufacturing an alumina catalyst support comprising the steps of:
a. preparing a basic solution containing Al 2 O 3 and an acidic solution containing at least one rare earth nitrate,
b. mixing together the basic and acidic solutions causing coprecipitation in the form of a slurry,
c. aging the coprecipitation slurry and optionally adding one or more surfactants during the aging,
d. separating the coprecipitate from the solution to obtain a wet cake precipitate,
e. washing the wet cake precipitate to remove remnants of the solution containing elements that poison the catalyst and thereby to produce a pure rare earth alumina,
f. drying the rare earth alumina, and
g. calcining the rare earth alumina to obtain the alumina catalyst support having a chemical formula (RE x ,Al 1-x ) 2 O 3 , in which, RE denotes one or more rare earth elements selected from the group: La, Ce, Pr, Nd, Sm, Eu, Gd, Tb, Dy, Ho, Er and Tm; the alumina catalyst support being characterized by a rare earth molar content x of 0.005 to 0.04 and after calcination at 1200° C. for 50 hours, the alumina catalyst support comprises a surface area (SA) in excess of 30 m 2 /g and a theta phase absent the presence of any alpha phase.