Process for preparing dimethyl ether by vapor catalytic dehydration of methanol with high-activity dipping-type heteropoly acid as catalyst
A process technology and catalyst technology, which are used in the dehydration of hydroxyl-containing compounds to prepare ethers, catalyst carriers, catalysts for physical/chemical processes, etc., can solve problems such as no industrial reports, no breakthroughs, and zigzag fluctuations in catalyst bed temperature. The effect of reducing side reactions, reducing the consumption of raw materials, etc., and reducing product costs
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[0078] The composition (mass percentage) of catalyst is:
[0079] ——Carrier: molecular sieve 82.2%
[0080] ——Catalyst active component: heteropolyacid, 13.0%
[0081] ——Promoter: lanthanum cerium mixed rare earth oxide 1.8%
[0082] ——Molding agent: 3.0%
[0083] The catalyst is extruded, impregnated, dried and calcined.
[0084] 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:
[0085] DME (dimethyl ether) 56.7kg / h
[0086] CH 3 OH (methanol) 8.8kg / h
[0087] h 2 O (water) 23.5kg / h
[0088] After separation by three towers (light component separation tower, dimethyl ether rectification tower, a...
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