A novel method for catalytic cracking of α-acetyl-γ-butyrolactone
A catalytic cracking and acetylation technology, applied in chemical instruments and methods, physical/chemical process catalysts, organic compounds/hydrides/coordination complex catalysts, etc., can solve the problem of insufficient catalyst activity, multiple cracking by-products, and reaction yield Low-level problems, achieve excellent catalytic cracking effect, reduce other side reactions, and reduce the effect of reaction temperature
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Embodiment 1
[0032] 1) In the external circulation pulse reactor 1, add α-acetyl-γ-butyrolactone 6 raw materials, add catalyst 1.0kg (sodium chloride: ZIF-67=1:0.1), the particle size of the catalyst is less than 1000 microns, And pass into dry nitrogen 5 replacement; Open heat exchanger 8;
[0033] 2) After the replacement process is completed, the system is vacuumed;
[0034] 3) Turn on the circulating pump 7, the α-acetyl-γ-butyrolactone 6 raw material is drawn in by the pump 7, and passes through the heat exchanger 8, and the temperature is controlled at 140°C to contact the catalyst in the reactor 1, and the catalyst is mixed with the raw material Liquid 3 undergoes a catalytic cracking reaction, and continuously circulates the reaction to promote the completion of the reaction. Among them, the circulation switch in the external circulation pulsation reactor 1 is closed and opened to perform fluid pulsation operation with a pulsation ratio of 20s:20s, so as to realize the pulsation t...
Embodiment 2
[0039] 1) In the external circulation pulse reactor 1, add α-acetyl-γ-butyrolactone 6 raw materials, add catalyst 1.0kg (sodium iodide: ZIF-67=1:0.5), the particle size of the catalyst is less than 500 microns, And pass into dry nitrogen 5 replacement; Open heat exchanger 8;
[0040] 2) After the replacement process is completed, the system is vacuumed;
[0041] 3) Turn on the circulation pump 7, the α-acetyl-γ-butyrolactone 6 raw material is pumped in by the pump 7, and passes through the heat exchanger 8, and the temperature is controlled at 100°C to contact the catalyst in the reactor 1, and the catalyst is mixed with the raw material Liquid 3 undergoes a catalytic cracking reaction, and continuously circulates the reaction to promote the completion of the reaction. Wherein, the circulation switch in the external circulation pulsation reactor 1 is closed and opened to perform fluid pulsation operation with a pulsation ratio of 120s:1200s, so as to realize the pulsation to ...
Embodiment 3
[0046] 1) In the external circulation pulse reactor 1, add α-acetyl-γ-butyrolactone 6 raw materials, add catalyst 1.0kg (potassium iodide: ZIF-67=1:0.2), the particle size of the catalyst is less than 500 microns, and pass Enter dry nitrogen 5 replacement; Open heat exchanger 8;
[0047] 2) After the replacement process is completed, the system is vacuumed;
[0048] 3) Turn on the circulation pump 7, the α-acetyl-γ-butyrolactone 6 raw material is pumped in by the pump 7, and passes through the heat exchanger 8, and the temperature is controlled at 130°C to contact the catalyst in the reactor 1, and the catalyst is mixed with the raw material Liquid 3 undergoes a catalytic cracking reaction, and continuously circulates the reaction to promote the completion of the reaction. Among them, the circulation switch in the external circulation pulsation reactor 1 is closed and opened to perform fluid pulsation operation with a pulsation ratio of 40s:80s, so as to realize the pulsation...
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