Process for preparing dimethyl enther by vapour catalytic dehydration of methanol with high-activity dipping-type heteropoly acid as catalyst
A technology of dimethyl ether and catalyst, which is applied in the field of preparation of dimethyl ether, can solve the problems of no industrialization report, no breakthrough, zigzag fluctuation of catalyst bed temperature, etc., and achieve reduction of side reactions, reduction of consumption of raw materials, etc. Product Cost Effects
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[0063] The composition (mass percentage) of catalyst is:
[0064] ——Carrier: molecular sieve 82.2%
[0065] ——Catalyst active component: heteropolyacid, 13.0%
[0066] ——Promoter: lanthanum-cerium mixed rare earth oxide 1.8%
[0067] ——Molding agent: 3.0%
[0068] The catalyst is extruded, impregnated, dried and calcined.
[0069] Industrial methanol (≥98.5%) enters the system at a feed rate of 89kg / h, and reacts in a tube-and-tube heat-exchange homogeneous temperature reactor filled with an efficient new impregnated heteropolyacid catalyst. The reaction temperature is 180°C; the reaction pressure 1.0MPa; methanol mass space velocity (methanol mass / catalytic mass) 1.0h -1 ; Methanol conversion 90%; selectivity ≥ 99.8%. The reactor outlet consists of:
[0070] DME (dimethyl ether) 56.7 kg / h
[0071] CH 3 OH (methanol) 8.8 kg / h
[0072] h 2 O (water) 23.5 kg / h
[0073] After separation by three towers (light component separation tower, dimethyl ether rectification tow...
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