Method for preparing low-carbon olefins through methanol catalysis
A low-carbon olefin, catalytic preparation technology, applied in the direction of hydrocarbon production from oxygen-containing organic compounds, organic chemistry, chemical recovery, etc., can solve the problems of low yields of ethylene and propylene
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Embodiment 1
[0022] in such as figure 1 In the reaction device shown, the pre-reactor is a dense-phase fluidized bed, the main reactor is a fast fluidized bed, the catalyst is SAPO-34, and the methanol raw material with a purity of 99.5% is vaporized and heat-exchanged to 150 ° C. After being divided into Two parts, the first part enters the pre-reactor to generate a stream with a mass percentage of dimethyl ether of 52%, and then enters the bottom of the main reactor reaction zone, and the second part of the raw material is separated from the two parts along the axial direction of the main reactor reaction zone. One feed inlet is injected into the reaction zone of the main reactor, and the two feed inlets are respectively located at 1 / 4 and 1 / 2 bed heights of the reaction zone of the main reactor from the bottom of the reaction zone of the main reactor. The reaction conditions of the pre-reactor are: the reaction pressure is 0.01MPa in gauge pressure, the average temperature is 200°C, the...
Embodiment 2
[0024] According to the conditions and steps described in Example 1, except that the catalyst type was changed to SAPO-18, the carbon-based yield of light olefins was 80.54% (by weight).
Embodiment 3
[0026] According to the conditions and steps described in Example 1, the methanol raw material with a purity of 99.5% is vaporized and heat-exchanged to 250°C and divided into two parts. The first part enters the pre-reactor to generate a stream with a mass percentage of dimethyl ether of 68%. , and then enter the bottom of the main reactor reaction zone, the second part of the raw material is injected into the main reactor reaction zone from two feed ports separated along the axial direction of the main reactor reaction zone, and the two feed ports are respectively located at a distance from the main reactor At the bottom 1 / 4 and 3 / 4 of the bed height of the main reactor reaction zone. The reaction conditions of the pre-reactor are: the reaction pressure is 0.01MPa in gauge pressure, the average temperature is 350°C, and the reaction conditions in the reaction zone of the main reactor are: the reaction pressure is 0.01MPa in gauge pressure, the average temperature is 500°C, th...
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