Method for producing light olefins with high selectivity by using methanol as raw material
A low-carbon olefin and high-selectivity technology, applied in the direction of biological raw materials, ethylene production, bulk chemical production, etc., can solve the problem of low selectivity of low-carbon olefins, achieve selectivity improvement, increase yield, and reduce back-mixing Effect
- Summary
- Abstract
- Description
- Claims
- Application Information
AI Technical Summary
Problems solved by technology
Method used
Image
Examples
Embodiment 1
[0018] in such as figure 1 On the shown reaction device, under normal pressure, the catalyst adopts SAPO-34, and the reaction conditions in the reaction zone are as follows: the reaction temperature is 465°C, the average carbon deposition mass fraction of the catalyst is 2.8%, and methanol with a purity of 99.5% passes through at 210°C The distribution plate enters the reaction zone, and a gas-solid rapid separation device is installed at the outlet of the reaction zone. Part of the catalyst to be produced is returned to the lower part of the reaction zone to replenish the catalyst storage in the reaction zone, and a part of the zone is regenerated by the regenerator. The ratio of the diameter of the discharge end to the diameter of the feed end is 0.85, and 78% of methanol has been converted in the space from the distribution plate to 1 / 3 of the height of the reaction zone. The product is analyzed by gas chromatography. The experimental results are: methanol conversion rate 99...
Embodiment 2
[0020] According to the conditions described in Example 1, the reaction conditions in the reaction zone are as follows: the reaction temperature is 500° C., the average carbon deposit mass fraction of the catalyst is 3.97%, and the methanol with a purity of 99.5% enters the reaction zone through a distribution plate at 300° C. and exits the reaction zone. The ratio of the diameter of the feed end to the diameter of the feed end is 0.5, and 70.5% of methanol has been converted in the space from the distribution plate to 1 / 3 of the height of the reaction zone. The product is analyzed by gas chromatography. The experimental result is: the conversion rate of methanol is 99.08% (weight), the low carbon olefin carbon group selectivity is 80.17% (weight).
Embodiment 3
[0022] According to the conditions described in Example 1, the reaction conditions in the reaction zone are as follows: the reaction temperature is 400° C., the average carbon deposit mass fraction of the catalyst is 1.5%, and the methanol with a purity of 99.5% enters the reaction zone through a distribution plate at 170° C. and exits the reaction zone. The ratio of the diameter of the feed end to the diameter of the feed end is 0.95, and 74% of methanol has been converted in the space from the distribution plate to 1 / 3 of the height of the reaction zone. The composition of the product is analyzed by gas chromatography. The experimental result is: the conversion rate of methanol is 99.23% (weight), the low carbon olefin carbon group selectivity is 80.26% (weight).
PUM
Login to View More Abstract
Description
Claims
Application Information
Login to View More 