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35results about "Preparation by halogenatd hydrocarbon disproportionation" patented technology

Method for catalyzing 2,5-dichlorotoluene reaction by modified H type molecular sieve

The invention relates to a method for catalyzing 2, 5-dichlorotoluene reaction by a modified H type molecular sieve, and belongs to the technical field of chlorotoluene derivatives. The method comprises the following steps: dissolving Cu(NO3)2 3H2O into distilled water, fully mixing and stirring with an H type molecular sieve after completely dissolving, standing for 12 hours under a condition that the environment temperature is 110 DEG C after standing and drying, and drying in a muffle furnace of which the temperature is 400 DEG C for 2 hours; performing a modified molecular sieve, grinding, sieving, and selecting sieved molecular sieve particles as a catalyst; filling a constant-temperature zone of a fixed bed reactor with the catalyst; conveying raw materials to the fixed bed reactor through a constant flow pump, and continuously bringing rapidly vaporized raw material steam in the constant-temperature zone into a catalyst bed layer through a gas; finally collecting a product through water bath condensation. According to the method disclosed by the invention, the modified H type molecular sieve is adopted as the catalyst, no toxicity and no harm exist, better stability and higher catalytic activity are obtained, cyclic and repeated utilization can be carried out, and sustained industrial production is facilitated.
Owner:MINGGUANG FEIZHOU NEW MATERIAL

A kind of method that modified h-type molecular sieve catalyzes 2,5-dichlorotoluene reaction

The invention relates to a method for catalyzing 2, 5-dichlorotoluene reaction by a modified H type molecular sieve, and belongs to the technical field of chlorotoluene derivatives. The method comprises the following steps: dissolving Cu(NO3)2 3H2O into distilled water, fully mixing and stirring with an H type molecular sieve after completely dissolving, standing for 12 hours under a condition that the environment temperature is 110 DEG C after standing and drying, and drying in a muffle furnace of which the temperature is 400 DEG C for 2 hours; performing a modified molecular sieve, grinding, sieving, and selecting sieved molecular sieve particles as a catalyst; filling a constant-temperature zone of a fixed bed reactor with the catalyst; conveying raw materials to the fixed bed reactor through a constant flow pump, and continuously bringing rapidly vaporized raw material steam in the constant-temperature zone into a catalyst bed layer through a gas; finally collecting a product through water bath condensation. According to the method disclosed by the invention, the modified H type molecular sieve is adopted as the catalyst, no toxicity and no harm exist, better stability and higher catalytic activity are obtained, cyclic and repeated utilization can be carried out, and sustained industrial production is facilitated.
Owner:MINGGUANG FEIZHOU NEW MATERIAL
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