Process for producing light olefin hydrocarbon by oxygen-containing compound catalytic conversion
A light olefin, catalytic conversion technology, applied in the direction of hydrocarbon production from oxygen-containing organic compounds, chemical instruments and methods, physical/chemical process catalysts, etc.
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Embodiment 1~4
[0019] In the small-scale fluidized bed reaction regeneration device, pure methanol is used as feed, the catalyst type is shown in Table 1, the average temperature of the reaction zone is 500 ° C, and the methanol weight hourly space velocity is 25 hours -1 , The reaction pressure (gauge pressure) is 0.1MPa. To maintain the stability of the catalyst flow control, the reactor outlet product was analyzed by online gas chromatography. The experimental results are shown in Table 1.
[0020] Table 1
[0021] parameters
Embodiment 5~6
[0023] According to the conditions described in Example 4, the reactor temperature was changed, and the experimental results are shown in Table 2.
[0024] Table 2
[0025] parameters
Embodiment 7~8
[0027] According to the conditions described in Example 4, the type of raw material and the weight hourly space velocity of the raw material were changed, and the experimental results are shown in Table 3.
[0028] table 3
[0029] parameters
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