A kind of method that methanol/dimethyl ether is directly converted into diesel oil fraction
A technology of dimethyl ether and methanol, which is applied in the field of diesel oil preparation, can solve the problems of complicated process and high production cost, and achieve the effects of concentrated product distribution, convenient operation and convenient separation operation
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Embodiment 1
[0023] Mix 2g of H-beta zeolite with 0.8g of pseudo-boehmite, add dilute nitric acid with a concentration of 3% (v / v) that can completely wet the zeolite and pseudo-boehmite, stir evenly, and dry at 110°C for 2h. Then it was calcined at 450° C. for 2 hours to make catalyst particles of 40-60 mesh. Put the catalyst prepared above into a tubular reactor, activate it at 500°C for 2 hours, then cool down to the reaction temperature of 430°C, and gasify the raw material methanol with nitrogen in a preheater at 120°C (the amount of nitrogen introduced is generally 10-30ml / min) mixed into the reactor, the reaction pressure is 0.5MPa, and the mass space velocity of methanol is 6h -1 , reacted for 2h, the conversion rate of methanol was 99.2%, and the selectivity of diesel fraction hydrocarbons in the total hydrocarbon products was 5.8wt.%.
Embodiment 2
[0025] Mix 2g of H-Y zeolite with 1g of silicon oxide, add dilute nitric acid with a concentration of 3% (v / v) until the powder is completely wetted, stir evenly, dry at 100°C for 3h, and then roast it at 500°C for 3h. into 40-60 mesh catalyst particles. Put the catalyst prepared above into a tubular reactor, activate it at 450°C for 3h, then cool down to the reaction temperature of 390°C, the raw material dimethyl ether and the inert carrier gas (the inert carrier gas is argon, the amount of feed is generally 10-30ml / min) mixed in a preheater at 120°C and then enters the reactor, the reaction pressure is 2MPa, and the mass space velocity of dimethyl ether is 2h -1 , reacted for 2 hours, the conversion rate of dimethyl ether was 95.6%, and the selectivity of diesel fraction hydrocarbons in the total hydrocarbon products was 21.8wt.%.
Embodiment 3
[0027] Dissolve 0.73g of NaOH in 67.68g of deionized water, add 1.7g of sodium aluminate to the above solution, stir well, continue to stir and add 16g of silicic acid, finally add 7.19g of 98wt.% hexamethyleneimine aqueous solution, continue to stir for 0.5 h, put the above solution in a 40°C water bath for 24h, then put it into a stainless steel crystallization kettle with a polytetrafluoroethylene liner at 150°C for 9 days, filter the obtained product, and wash with deionized water until the pH value reaches medium properties, dried overnight at 110°C, and then calcined at 550°C for 8 hours in an air stream to remove the template agent to obtain MCM-22 molecular sieves. The above-mentioned molecular sieves were ion-exchanged with 0.1M ammonium nitrate solution, and then filtered, washed and calcined as described above, so that the ions The exchange was repeated three times to obtain H-MCM-22 zeolite molecular sieve.
[0028] Mix 2g of H-MCM-22 zeolite with 1g of silicon oxi...
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