Process for converting oxygen-containing compound to prepare low carbon olefin hydrocarbon
A technology of low-carbon olefins and compounds, which is applied in the field of conversion of oxygen-containing compounds to low-carbon olefins, which can solve the problems of catalyst loss and other problems, and achieve the effect of simple and convenient operation and low cost
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Embodiment 1
[0013] The methanol raw material that concentration is 99.5% (weight) drops into the MTO reactor that SAPO-34 catalyzer is housed, and reactor is a fast fluidized bed reactor, and a secondary cyclone separator is installed in the reactor, and this reactor is at reaction temperature at 495°C and a reaction pressure of 0.08 MPa (in gauge pressure), the fluidization medium is water vapor, and the components of the reaction product stream flowing out from the outlet of the above-mentioned MTO reactor are shown in Table 1; the outlet of the reactor is connected to a Heat exchanger, the heat exchange medium is methanol raw material, the outflow temperature of the reaction product stream after heat exchange is 185°C; after heat exchange, it enters the plate scrubber, and the reaction product stream out of the scrubber does not contain fine powder, and its temperature is 20°C .
[0014] Table 1 Reactor outlet reaction product stream components (1)
[0015] components
Embodiment 2
[0017] According to the conditions of Example 1, only the reaction temperature is changed to 350 DEG C, and other operating conditions are unchanged, the components of the reaction product stream flowing out from the outlet of the above-mentioned MTO reactor are as shown in Table 2; the outflow of the reaction product stream after heat exchange The temperature is 162°C; the reaction product flow out of the washing tower does not contain fine powder, and its temperature is 15°C.
[0018] Table 2 Reactor outlet reaction product stream components (2)
[0019] components
Embodiment 3
[0021] According to the conditions of Example 1, only the reaction temperature is changed to 525 ° C, and other operating conditions are unchanged, the components of the reaction product stream flowing out from the outlet of the above-mentioned MTO reactor are as shown in Table 3; the outflow of the reaction product stream after heat exchange The temperature is 191°C; the reaction product flow out of the washing tower does not contain fine powder, and its temperature is 23°C.
[0022] Table 3 Reactor outlet reaction product stream components (3)
[0023] components
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