Catalyst for synthesizing unsaturated aldehyde and unsaturated carboxylic acid, method of preparing same, and method of synthesizing unsaturated aldehyde and unsaturated carboxylic acid with catalyst
An unsaturated, catalyst technology, used in catalyst activation/preparation, hydrocarbon oxidation to prepare oxygenates, carboxylate preparation, etc.
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Examples
preparation example Construction
[0047] The catalyst of the present invention of the extruded catalyst produced by the preparation method of the present invention is a catalyst containing at least molybdenum, bismuth and iron as metal elements related to its catalytic action, and may contain silicon, cobalt, nickel as additional elemental components , chromium, lead, manganese, calcium, magnesium, niobium, silver, barium, tin, tantalum, zinc, phosphorus, boron, sulfur, selenium, tellurium, cerium, tungsten, antimony, titanium, lithium, sodium, potassium, rubidium, cesium and thallium etc. More specifically, the catalysts of the present invention are preferably prepared to exhibit the formula
[0048] Mo a Bi b Fe c m d x e Y f Z g Si h o i
[0049] Indicates the average composition of the catalyst.
[0050] (In the formula, Mo, Bi, Fe, Si and O represent molybdenum, bismuth, iron, silicon and oxygen respectively, M represents at least one element selected from the group consisting of co...
Embodiment
[0059] Hereinafter, the present invention will be described more specifically based on Examples and Comparative Examples. These Examples are examples of the best mode of the present invention, but the present invention is not limited by the aspects of these Examples. In addition, in the descriptions of Examples and Comparative Examples, "parts" means parts by mass, and in the kneading process, a kneader equipped with a batch-type double-arm stirring blade was used. In addition, the composition analysis of the mixed gas containing the raw material supplied to the reaction tube and the gas containing the product taken out from the reaction tube after the reaction was performed by gas chromatography.
[0060] The reaction rate (hereinafter referred to as the reaction rate) of the raw material (propylene, isobutylene, TBA or MTBE) and the selectivity of the unsaturated aldehyde and unsaturated carboxylic acid produced in Examples and Comparative Examples were calculated by the fol...
Embodiment A-1
[0069] Add 500 parts of ammonium paramolybdate, 6.2 parts of ammonium paratungstate, 1.4 parts of potassium nitrate, 27.5 parts of antimony trioxide and 55.0 parts of bismuth trioxide into 1000 parts of pure water, and heat and stir (liquid A). Moreover, 114.4 parts of iron nitrate, 295.3 parts of cobalt nitrate, and 35.1 parts of zinc nitrate were sequentially added and dissolved in 1000 parts of pure water (B liquid). After adding liquid B to liquid A to form an aqueous slurry, the aqueous slurry was dried into dry spherical particles with an average particle diameter of 60 μm using a spray dryer. Then, the dried spherical particles were calcined at 300° C. for 1 hour to form a catalyst calcined product.
[0070] 25 parts of curdlan was added to 500 parts of the thus-obtained fired catalyst, followed by dry mixing. 160 parts of pure water were mixed therein, and after mixing (kneading) with a kneader until it became a clay-like substance, extrusion molding was performed usi...
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Abstract
Description
Claims
Application Information
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