US2008138569A1PendingUtilityA1
Alpha-alumina inorganic membrane support and method of making the same
Est. expiryDec 11, 2026(~0.4 yrs left)· nominal 20-yr term from priority
C04B 2235/3217C04B 2111/00793Y10T428/24744C04B 2235/3418Y10T428/24149C04B 35/10Y10T428/31938B01D 69/105C04B 38/06C04B 2235/3206C04B 2235/3232C04B 2235/3262C04B 38/0006C04B 2235/3281C04B 2235/5436C04B 2235/3218C04B 2235/3225B01D 63/061B01D 69/108B01D 71/02B01D 2323/18
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Claims
Abstract
Compositions for making alpha-alumina supports for, for example, inorganic membranes are described. Methods for controlling the alumina and pore former particle sizes and other process variables are described which facilitate desirable porosity, pore distribution and strength characteristics of the resulting alpha-alumina inorganic membrane supports.
Claims
exact text as granted — not AI-modified1 . A composition comprising;
from 50 weight % to 90 weight % of α-alumina particles; from 10 weight % to 30 weight % of organic pore former particles; and from 1 weight % to 15 weight % of a sintering aid.
2 . The composition according to claim 1 , wherein the α-alumina has a mean particle size of 15 microns or more.
3 . The composition according to claim 2 , wherein the α-alumina has a mean particle size of from 15 microns to 50 microns.
4 . The composition according to claim 1 , further comprising an organic crosslinker.
5 . The composition according to claim 4 , wherein the organic crosslinker is selected from the group consisting of an organic agent, epichlorohydrin, cyclopolyamine oligomer and ionene.
6 . The composition according to claim 1 , wherein the sintering aid is selected from the group consisting of boehmite sol, alumina organic compounds, TiO 2 , CuO, MnO 2 , MgO, ZrO 2 , Y 2 O 3 , colloidal alumina, SiO 2 , AlO(OH) slurry, and sodium alumina.
7 . The composition according to claim 1 , wherein the organic pore former is a starch.
8 . The composition according to claim 7 , wherein the starch is selected from the group consisting of Canna starch, potato starch, green bean starch, corn starch, rice starch, and Sago starch.
9 . The composition according to claim 1 , wherein the organic pore former has a mean particle size of from 7 μm to 45 μm.
10 . A method of forming an α-alumina support, the method comprising;
providing a batch composition comprising 50 weight % to 90 weight % α-alumina particles, 10 weight % to 30 weight % of organic pore former particles and 1 weight % to 15 weight % of a sintering aid; shaping the batch to form a green body; and sintering the green body to form the α-alumina support.
11 . The method according to claim 10 , comprising providing the batch composition by combining the 50 weight % to 90 weight % α-alumina particles, 10 weight % to 30 weight % of the organic pore former particles and 1 weight % to 15 weight % of the sintering aid and mixing the α-alumina particles, the organic pore former particles and the sintering aid to provide a homogeneous mixture.
12 . The method according to claim 10 , wherein the sintering the green body comprises heating the green body at a temperature of from 1500 degrees Celcius to 2000 degrees Celcius for from 1 hour to 16 hours.
13 . The method according to claim 10 , wherein the sintering the green body comprises heating the green body at a temperature of from 1600 degrees Celcius to 1775 degrees Celcius for from 8 hours to 16 hours.
14 . The method according to claim 10 , wherein the organic pore former is a starch.
15 . The method according to claim 14 , wherein the starch is selected from the group consisting of Canna starch, potato starch, green bean starch, corn starch, rice starch, and Sago starch.
16 . The method according to claim 10 , wherein the shaping the batch comprises extruding the batch through an extrusion die.
17 . An α-alumina support comprising a mean pore size of from 6 microns to 15 microns and having a pore size distribution (d ps ) of from 0.50 to 1.70 as described by the formula:
d ps =( dp 90 −dp 10 )/ dp 50 ; wherein dp 10 is a pore size wherein 10% of the pore volume has a smaller pore size; dp 50 is a median pore size wherein 50% of the pore volume has a smaller pore size; and dp 90 is a pore size wherein 90% of the pore volume has a smaller pore size.
18 . The α-alumina support according to claim 17 , having a d f of from 0.20 to 0.60 as described by the formula:
d f =( dp 50 −dp 10 )/ dp 50 .
19 . The α-alumina support according to claim 17 , comprising a first end, a second end, and an inner channel having surfaces defined by porous walls and extending through the support from the first end to the second end.
20 . The α-alumina support according to claim 19 , wherein the α-alumina support is in the form of a honeycomb monolith.Cited by (0)
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