Abstract The invention concerns catalytic substances for the oxidation of ammonia, for the production of nitric acid, comprising cobalt oxide as the main component. Such substances, besides cobalt oxide, also contain additives formed of aluminum oxide and possibly oxides of thorium, cerium, zinc and cadmium, the amount of aluminum oxide added being from 5% to 15% by weight of the finished substances and the amount of the other oxides being from 0 to 25% by weight of the finished substances; these substances are in particular shaped by pelleting or extrusion, dried and then calcined at temperatures of the order of from 900° to 1000° C. The advantages of these catalytic substances lie in a high degree of activity and a high level of strength, which are maintained during use thereof.
In the catalytic oxidation of ammonia to produce nitrogen oxides for the production of nitric acid by the oxidation of ammonia and air in the presence of a catalyst, the improvement wherein the oxidation is carried out with a catalyst formed by calcining at a temperature of the order of from 900° C. to 1000° C. a mixture consisting essentially of 60-95% by weight tricobalt tetraoxide, aluminum oxide in an amount greater than 5% by weight but which does not exceed 15% by weight, and an oxide of a metal selected from the group consisting of thorium, cerium, zinc and cadmium in an amount that does not exceed 25% by weight.
Claim 2
Dependent Claim
111 words
In the catalytic oxidation of ammonia to produce nitrogen oxides for the production of nitric acid by the oxidation of ammonia and air in the presence of a catalyst, the improvement wherein the oxidation is carried out with a catalyst formed by calcining at a temperature of the order of from 900° C. to 1000° C. a mixture consisting essentially of 60-95% by weight tricobalt tetraoxide, aluminum oxide in an amount greater than 5% by weight but which does not exceed 15% by weight, and an oxide of a metal selected from the group consisting of thorium, cerium, zinc and cadmium in an amount that does not exceed 25% by weight.
Claim 3
Dependent Claim
18 words
The method as claimed in claim 1 in which the third component of the catalyst is cerium oxide.
Claim 4
Dependent Claim
16 words
The method as claimed in claim 1 in which the catalyst is devoid of alkali metal.
Claim 5
Dependent Claim
25 words
The method as claimed in claim 1 in which the catalyst is shaped, dried and calcined at a temperature within the range of 900°-1000° C.