Catalyst and process for the oxychlorination of ethylene to dichloroethane
A kind of technology of ethylene dichloride and catalyst, applied in the field of catalyst, can solve problems such as unfavorableness, affecting the efficiency of ethylene and hydrogen chloride raw materials and the like
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[0026] Preparation of catalyst materials
[0027] As noted above, the supported catalyst materials of the present invention may be prepared by impregnating the support via incipient wetness impregnation with an aqueous solution carrying one or more active catalyst metals and a catalyst promoter. For the purposes of this specification, and unless otherwise stated, the technique of impregnating a support is to be understood in its broadest sense and includes wetting the support over a wide range (eg, 80% to 115% of its pore volume). In one or more embodiments, the support rendered wet by treatment with an aqueous solution may subsequently be dried. In one or more embodiments, the supported catalyst or any precursor may be calcined.
[0028] In one or more embodiments, the step of impregnating the support occurs in multiple steps. In other words, the support is impregnated in two or more impregnation steps to produce the desired support material. In one or more embodiments, a ...
Embodiment
[0058] Catalysts were prepared by impregnating the alumina support with an aqueous solution of the desired metal chloride using a two-step impregnation process, except for Comparative Example 1 which was prepared using a single-step impregnation. Add the metal chloride solution to the alumina support while rotating and stirring in the ceramic dish. Each impregnation was carried out at room temperature. Following each impregnation, the ceramic discs containing the catalyst were placed in a steam bath for an initial drying stage (about 4 to 6 hours) and then heated to 180°C for a final drying stage (up to 16 hours).
[0059] The alumina support of the first set of samples (i.e. Comparative Samples 1-3 and Inventive Samples 1 and 3-6) was purchased under the tradename Catalox SCCa 25 / 200 (Sasol) and was characterized by a pore volume of 0.40-0.50mL / g, the surface area is 180-210m 2 / g, particle size distribution with 0%-10% of particles smaller than 22 μm and 905–100% of partic...
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