Claims Analysis
Total Claims: 11
Claim 1
Independent Claim
129 words
In a process for preparing a carboxylic ester by reacting a hydrocarbon selected from the group consisting of toluene and xylene with an alkanoic carboxylic acid having 2 to 4 carbon atoms and molecular oxygen in the vapor phase in the presence of a supported solid catalyst of palladium metal, antimony oxide and a carboxylic acid salt of an alkali metal, an alkaline earth metal, zinc, cadmium, lead or tin, the improvement comprising: adding said antimony oxide to the support of said catalyst by dipping a carrier into an aqueous solution of a water soluble antimony compound selected from the group consisting of antimonic acid, antimonates and antimony complexes of oxalic, glycolic or tartaric acids; and calcining said dipped carrier at a temperature of from 500° - 900° C.
Claim 2
Dependent Claim
129 words
In a process for preparing a carboxylic ester by reacting a hydrocarbon selected from the group consisting of toluene and xylene with an alkanoic carboxylic acid having 2 to 4 carbon atoms and molecular oxygen in the vapor phase in the presence of a supported solid catalyst of palladium metal, antimony oxide and a carboxylic acid salt of an alkali metal, an alkaline earth metal, zinc, cadmium, lead or tin, the improvement comprising: adding said antimony oxide to the support of said catalyst by dipping a carrier into an aqueous solution of a water soluble antimony compound selected from the group consisting of antimonic acid, antimonates and antimony complexes of oxalic, glycolic or tartaric acids; and calcining said dipped carrier at a temperature of from 500° - 900° C.
Claim 3
Dependent Claim
46 words
The process of claim 1, wherein the carrier is dipped into an aqueous solution of the water soluble antimony compound and then is calcined at 500° - 900° C in an oxygen-containing gas followed by dipping the product into an aqueous solution of a palladium compound.
Claim 4
Dependent Claim
15 words
The process of claim 2, wherein the calcination is performed at 600° - 800° C.
Claim 5
Dependent Claim
49 words
The process of claim 1, wherein the carrier is dipped in an aqueous solution the water soluble antimony compound and a palladium compound and then the product is calcined at 500° - 900° C in an oxygen-containing gas whereby the antimony oxide and the palladium component are simultaneously supported.
Claim 6
Dependent Claim
15 words
The process of claim 4, wherein the calcination is performed at 600° - 800° C.
Claim 7
Dependent Claim
20 words
The process of claim 1, wherein the content of palladium supported on the carrier is 0.1 - 20% by weight.
Claim 8
Dependent Claim
33 words
The process of claim 1, wherein the catalyst contains 0.05 to 8 gram-atoms of antimony oxide as Sb and 0.1 to 8 moles of the carboxylic acid salt to 1 gram-atom of palladium.
Claim 9
Dependent Claim
33 words
The process of claim 1, wherein the catalyst contains 0.5 to 8 gram-atoms of antimony oxide as Sb and 0.5 to 4 moles of the carboxylic acid salt to 1 gram-atom of palladium.
Claim 10
Dependent Claim
24 words
The process of claim 1, wherein the molar ratio of the hydrocarbon to the carboxylic acid in the reaction is 1 :1 - 10.
Claim 11
Dependent Claim
15 words
The process of claim 1, wherein the reaction is conducted at 140° - 250° C.