Claims Analysis
Total Claims: 16
Claim 1
Independent Claim
351 words
In a process for preparing a catalyst comprising a Group VI-B or Group VIII metal, or both, composited with alumina, the alumina being precipitated as an alumina hydrogel from a solution which contains a hydrous form of alumina and a compound having an anion soluble in an alkaline medium and which forms a soluble aluminum salt, the improvement comprising precipitating the hydrogel of alumina at temperatures ranging from about 15° F to about 120° F from the solution, which contains alumina in concentration ranging from about 1 to about 5 percent, based on the weight of solution, at pH ranging from about 8 to about 12, separating the alumina hydrogel from the solution, contacting the alumina hydrogel with a solution of a water-soluble polymer containing from about 2 to about 24 monomer units from the group consisting of (a) polyethylene glycols, (b) polypropylene glycols, and (c) polyethylene amines sufficient to absorb the polymer into the pores of the alumina hydrogel, displacing water from the pores until the weight ratio of polymer:alumina within the hydrogel ranges from about 0.5:1 to about 4:1, drying the hydrogel, and then calcining the dried hydrogel to form a gamma alumina catalyst composite characterized, when the catalyst is of size ranging from about 1/50 inch up to 1/25 inch average particle size diameter, at least about 15 percent of its total pore volume of absolute diameter within the range of about 150A to about 250A; when the catalyst is of size ranging from about 1/25 inch to about 1/8 inch average particle size diameter, at least about 15 percent of its total pore volume of absolute diameter within the range of about 175A to about 275A; wherein, in each of these catalysts of differing ranges of particle size distributions, the pore volumes resultant from pores of 50A, and smaller, are minimized; the surface areas and pore volumes of the catalysts being interrelated with particle size, and pore size distributions, surface areas ranging at least about 200 m 2 /g to about 600 m 2 /g with pore volumes ranging from about 0.8 to about 3.0 cc/g (B.E.T.).
Claim 2
Dependent Claim
351 words
In a process for preparing a catalyst comprising a Group VI-B or Group VIII metal, or both, composited with alumina, the alumina being precipitated as an alumina hydrogel from a solution which contains a hydrous form of alumina and a compound having an anion soluble in an alkaline medium and which forms a soluble aluminum salt, the improvement comprising precipitating the hydrogel of alumina at temperatures ranging from about 15° F to about 120° F from the solution, which contains alumina in concentration ranging from about 1 to about 5 percent, based on the weight of solution, at pH ranging from about 8 to about 12, separating the alumina hydrogel from the solution, contacting the alumina hydrogel with a solution of a water-soluble polymer containing from about 2 to about 24 monomer units from the group consisting of (a) polyethylene glycols, (b) polypropylene glycols, and (c) polyethylene amines sufficient to absorb the polymer into the pores of the alumina hydrogel, displacing water from the pores until the weight ratio of polymer:alumina within the hydrogel ranges from about 0.5:1 to about 4:1, drying the hydrogel, and then calcining the dried hydrogel to form a gamma alumina catalyst composite characterized, when the catalyst is of size ranging from about 1/50 inch up to 1/25 inch average particle size diameter, at least about 15 percent of its total pore volume of absolute diameter within the range of about 150A to about 250A; when the catalyst is of size ranging from about 1/25 inch to about 1/8 inch average particle size diameter, at least about 15 percent of its total pore volume of absolute diameter within the range of about 175A to about 275A; wherein, in each of these catalysts of differing ranges of particle size distributions, the pore volumes resultant from pores of 50A, and smaller, are minimized; the surface areas and pore volumes of the catalysts being interrelated with particle size, and pore size distributions, surface areas ranging at least about 200 m 2 /g to about 600 m 2 /g with pore volumes ranging from about 0.8 to about 3.0 cc/g (B.E.T.).
Claim 3
Dependent Claim
55 words
The process of claim 1 wherein the alumina hydrogel is precipitated by combining solutions (a) a first of which contains an alkali metal aluminate and (b) a second of which contains a strong mineral acid or an aluminum salt of a strong mineral acid, the anion portion of which is soluble in the alkaline solution.
Claim 4
Dependent Claim
13 words
The process of claim 2 wherein silica is added to the second solution.
Claim 5
Dependent Claim
19 words
The process of claim 1 wherein the temperature of precipitation ranges from about 32° F. to about 70° F.
Claim 6
Dependent Claim
34 words
The process of claim 1 wherein the concentration of alumina contained within the solution wherein the hydrogel is precipitated ranges from about 2 to about 3 percent, based on the weight of the solution.
Claim 7
Dependent Claim
23 words
The process of claim 1 wherein the pH of the solution wherein the hydrogel is precipitated ranges from about 9 to about 10.
Claim 8
Dependent Claim
15 words
The process of claim 1 wherein the precipitated alumina hydrogel is washed at ambient temperature.
Claim 9
Dependent Claim
21 words
The process of claim 1 wherein the hydrogel is washed at temperatures ranging from about 70° F. to about 120° F.
Claim 10
Dependent Claim
22 words
The process of claim 1 wherein the water-soluble polymer contains from about 4 to about 8 monomer units in the total molecule.
Claim 11
Dependent Claim
33 words
The process of claim 1 wherein the polymer displaces water from the pores of the alumina hydrogel until the weight ratio of polymer:alumina within the hydrogel ranges from about 1:1 to about 2:1.
Claim 12
Dependent Claim
140 words
The process of claim 1 wherein the catalyst produced is one comprising, when the catalyst is of size ranging from about 1/50 inch up to 1/25 inch average particle size diameter, at least about 20 percent of its total pore volume of absolute diameter within the range of about 150A to about 250A; when the catalyst is of size ranging from about 1/25 inch to about 1/8 inch average particle size diameter, at least about 20 percent of its total pore volume of absolute diameter within the range of about 175A to about 275A; the surface areas and pore volumes of the catalysts being interrelated with particle size, and pore size distributions, surface areas ranging at least about 250 m 2 /g to about 450 m 2 /g, with pore volumes ranging from about 1.1 to about 2.3 cc/g (B.E.T.).
Claim 13
Dependent Claim
140 words
The process of claim 11 wherein the catalyst produced is one comprising, when the catalyst is of size ranging from about 1/50 inch up to 1/25 inch average particle size diameter, at least about 45 percent, of its total pore volume of absolute diameter within the range of about 150A to about 250A; when the catalyst is of size ranging from about 1/25 inch to about 1/8 inch average particle size diameter, at least about 30 percent, of its total pore volume of absolute diameter within the range of about 175A to about 275A; the surface areas and pore volumes of the catalysts being interrelated with particle size, and pore size distributions, surface areas ranging at least about 250 m 2 /g to about 450 m 2 /g, with pore volumes ranging from about 1.1 to about 2.3 cc/g (B.E.T.).
Claim 14
Dependent Claim
57 words
The process of claim 1 wherein the catalyst is characterized as follows: ______________________________________
Distribution of
Pore Diameters
______________________________________
1/50 up to 1/25"
0-50A <10%
150-250A >15%
350A+ <35%
Pore Volume, cc/g 1.11.7
Surface Area, m.sup.2 /g
320-475
1/25 up to 1/8"
0-50A <5%
175-275A >15%
350A+ <40%
Pore Volume, cc/g 1.3-1.9
Surface Area, m.sup.2 /g
340-500
______________________________________
Claim 15
Dependent Claim
57 words
The process of claim 1 wherein the catalyst is characterized as follows: ______________________________________
Distribution of
Pore Diameters
______________________________________
1/50 up to 1/25"
0-50A <5%
150-250A >20%
350A+ <30%
Pore Volume, cc/g 1.3-1.9
Surface Area, m.sup.2 /g
340-575
1/25 up to 1/8"
0-50A <4%
175-275A >20%
350A+ <35%
Pore Volume, cc/g 1.5-2.1
Surface Area, m.sup.2 g
350-600
______________________________________
Claim 16
Dependent Claim
57 words
The process of claim 1 wherein the catalyst is characterized as follows: ______________________________________
Distribution of
Pore Diameters
______________________________________
1/50 up to 1/25"
0-50A <1%
150-250A >45%
350A+ <7%
Pore Volume, cc/g 1.5-2.1
Surface Area, m.sup.2 /g
360-600
1/25 up to 1/8"
0-50A <3%
175-275A >30%
350A+ <25%
Pore Volume, cc/g 1.5-2.3
Surface Area, m.sup.2 g
370-650
______________________________________