Claims Analysis
Total Claims: 17
Claim 1
Independent Claim
198 words
A method for treating either a fresh or spent single particle iron-containing syngas conversion catalyst composition prepared by forming a mixture of a water insoluble iron derivative of an organic compound, a matrix and an acidic crystalline aluminosilicate zeolite having a silica-to-alumina ratio of at least 12, a pore size greater than about 5 Angstrom units and a constraint index of about 1 to 12 which comprises: (a) oxidizing said catalyst in a stream of flowing air at a pressure in the range of 0-200 psig for about 0.1 to 16 hours at a temperature within the range of about 500°-1,000° F., (b) treating the product from step (a) in a stream of flowing hydrogen at a pressure in the range of 0-200 psig for about 0.1 to 16 hours at a temperature within the range of about 500°-1,000° F., (c) treating the product from step (b) in air at a pressure in the range of 0-200 psig for about 0.1-16 hours at a temperature within the range of about 500°-1,000° F., and (d) treating the product from step (c) with synthesis gas at atmospheric pressure at temperatures of about 550°-650° F. for about 0.5 to 24 hours.
Claim 2
Independent Claim
198 words
A method for treating either a fresh or spent single particle iron-containing syngas conversion catalyst composition prepared by forming a mixture of a water insoluble iron derivative of an organic compound, a matrix and an acidic crystalline aluminosilicate zeolite having a silica-to-alumina ratio of at least 12, a pore size greater than about 5 Angstrom units and a constraint index of about 1 to 12 which comprises: (a) oxidizing said catalyst in a stream of flowing air at a pressure in the range of 0-200 psig for about 0.1 to 16 hours at a temperature within the range of about 500°-1,000° F., (b) treating the product from step (a) in a stream of flowing hydrogen at a pressure in the range of 0-200 psig for about 0.1 to 16 hours at a temperature within the range of about 500°-1,000° F., (c) treating the product from step (b) in air at a pressure in the range of 0-200 psig for about 0.1-16 hours at a temperature within the range of about 500°-1,000° F., and (d) treating the product from step (c) with synthesis gas at atmospheric pressure at temperatures of about 550°-650° F. for about 0.5 to 24 hours.
Claim 3
Dependent Claim
16 words
The process of claim 1 wherein the catalyst has been spray-dried to produce fluid size particles.
Claim 4
Dependent Claim
13 words
The process of claim 1 wherein said water insoluble compound is ferrous oxalate.
Claim 5
Dependent Claim
13 words
The process of claim 2 wherein said water insoluble compound is ferrous oxalate.
Claim 6
Dependent Claim
15 words
The process of claim 4 wherein said water insoluble iron oxalate is formed in situ.
Claim 7
Dependent Claim
12 words
The process of claim 1 wherein said matrix is a siliceous matrix.
Claim 8
Dependent Claim
10 words
The process of claim 1 wherein said matrix comprises alumina.
Claim 9
Dependent Claim
10 words
The process of claim 1 wherein said matrix comprises silica-alumina.
Claim 10
Dependent Claim
14 words
The process of claim 6 wherein colloidal dispersions of silica and alumina are used.
Claim 11
Dependent Claim
10 words
The process of claim 1 wherein the zeolite is ZSM-5.
Claim 12
Dependent Claim
10 words
The process of claim 2 wherein the zeolite is ZSM-5.
Claim 13
Dependent Claim
10 words
The process of claim 3 wherein the zeolite is ZSM-5.
Claim 14
Dependent Claim
10 words
The process of claim 4 wherein the zeolite is ZSM-5.
Claim 15
Dependent Claim
10 words
The process of claim 5 wherein the zeolite is ZSM-5.
Claim 16
Dependent Claim
23 words
The process of claim 13 wherein the catalyst has become partially inactivated as a result of syngas conversion and its activity is restored.
Claim 17
Dependent Claim
10 words
The process of claim 15 wherein step (a) is omitted.