Apparatus and method for preparing gasoline from methanol
A methanol-to-gasoline, methanol technology, applied in chemical instruments and methods, petroleum industry, bulk chemical production, etc., can solve the problems of complex operation, ineffective separation of high-fraction tank gas phase, low gasoline yield, etc., and achieve operational performance Low consumption, less by-products and simple process
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Embodiment 1
[0034] Example 1 Methanol-to-gasoline device
[0035]The methanol-to-gasoline device comprises a reaction system, and the reaction system includes a raw material supply end, a vaporizer 1, a heating furnace 2 and a fixed bed reactor 3; the top of the fixed bed reactor is provided with a raw material input end, and the bottom is provided with a product output end; 3 beds are arranged vertically in the fixed bed reactor, and a gas distributor A11 and a gas distributor B12 are respectively arranged between the 3 beds; the raw material supply end is connected to the vaporizer 1 and the heating furnace 2 respectively; The outlet of the heating furnace 2 communicates with the raw material input end of the fixed bed reactor 3 . The outlet of the vaporizer 1 communicates with the gas distributor. The outlet of the vaporizer 1 is respectively connected to the gas distributor A11 and the gas distributor B12 through two parallel pipelines. The separation system includes a cooler 4, a h...
Embodiment 2
[0036] Embodiment 2 adopts the device of embodiment 1, is the method for preparing gasoline through catalytic reaction with methanol as raw material
[0037] (1) The raw material methanol is divided into two streams, one stream is vaporized by the vaporizer 1, and enters the bed of the fixed bed reactor 3 from the gas distribution plate, and the other stream is vaporized by the heating furnace 2, and enters the fixed bed reactor 3 from the raw material input end Under the conditions of the catalyst, the catalytic reaction is carried out; the temperature in the heating furnace is 200-260°C; the temperature in the vaporizer is 65-70°C;
[0038] (2) Step (1) The resulting product enters the cooler 4 for cooling, and the outlet temperature of the cooler is 40-50° C.;
[0039] (3) The material cooled in step (2) enters the high-pressure gas-liquid separation tank 5 for gas-liquid separation, and the gas phase enters the liquid separation tank 7 through the compressor 6; the liquid ...
Embodiment 3
[0047] A certain methanol-to-gasoline process section adopts the method of embodiment 2, and the reaction feed is 220t / h, and the product index is as follows:
[0048] Dry gas composition
[0049] methane
[0050] Liquefied gas composition
[0051] ethane
[0052] Target product distribution
[0053] dry gas
[0054] gasoline properties
[0055] Research Octane Number
[0056] Energy consumption is 78kg standard oil / gasoline.
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