Method for increasing yield of low-carbon olefins
A low-carbon olefin and stripping zone technology, applied in chemical recovery, ethylene production, hydrocarbon cracking and hydrocarbon production, etc., can solve the problems of low yield of ethylene and propylene
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Embodiment 1
[0021] in such as figure 1 In the small circulating fluidized bed reaction device shown, the catalyst is SAPO-34, the bottom of the second reaction zone is connected to the top of the first reaction zone, and the stripping zone is located at the top of the second reaction zone. Methanol with a purity of 99.5% enters the first reaction zone of the reactor and contacts with the catalyst. The reaction conditions in the first reaction zone are: the reaction pressure is 0.01MPa in terms of gauge pressure, the average temperature is 420°C, and the average carbon deposition of the catalyst is 1.5%. weight. The gas phase stream and the catalyst in the first reaction zone enter the second reaction zone to form a product stream comprising light olefins and oxygen-containing compounds, and simultaneously form a catalyst to be produced. The product stream is separated to form an oxygen-containing compound with a mass fraction of 66%. The back-smelting logistics, after analysis, the oxyge...
Embodiment 2
[0023] 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 80.17% (by weight).
Embodiment 3
[0025] According to the conditions and steps described in Example 1, the reaction conditions in the first reaction zone are: the reaction pressure is 0.01 MPa in terms of gauge pressure, the average temperature is 460° C., and the average carbon deposition amount of the catalyst is 3.5% by weight. The mass ratio of the oxygenate in the reclamation stream to the methanol feed in the raw material is 0.06, and the temperature of the total feed in the first reaction zone is 230°C. The raw catalyst enters the stripping zone of the reactor, and is divided into two parts after stripping, 50% returns to the bottom of the first reaction zone, and 50% enters the regenerator for regeneration, forming a carbon deposit with a mass fraction of 0.5% and a temperature of 550°C. The catalyst is regenerated, and the regenerated catalyst is returned to the second reaction zone of the reactor. The reaction conditions in the second reaction zone are as follows: the reaction pressure is 0.01 MPa in...
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