A kind of isobutyl vinyl ether preparation device and preparation method thereof
An isobutyl vinyl ether and a technology for preparing a device, which are applied in the field of isobutyl vinyl ether, can solve the problems of high manufacturing cost of a reactor, low gas-liquid mass transfer efficiency, large energy consumption of a compressor, etc. Avoid the amplification effect, the effect of reducing energy consumption
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Embodiment 1
[0026] The reaction of acetylene and isobutanol uses figure 1 The shown circulation reaction device is composed of absorber 1, gas-liquid separator 2, metering pump 3, constant temperature oil bath 4, tubular reactor 5, condenser 6 and pressure reducing valve 7, etc. The tubular reactor 5 is a stainless steel tube with an inner diameter of 2 mm and a length of 32 m, and the volume of the reactor is about 100 ml. The process operating conditions are as follows:
[0027] Catalyst dosage: 1.5% of the total mass of isobutanol;
[0028] Feed flow: 200g / h;
[0029] Absorber temperature: 25°C;
[0030] Absorber pressure: 0.105MPa;
[0031] Reactor temperature: 150°C;
[0032] Reactor pressure: 4MPa;
[0033] Circulation rate: 3.6L / h.
[0034] After about 3 hours of operation, the cyclic reaction system reached a steady state. The discharge rate of the reaction product was 241 g / h, the conversion rate of isobutanol was 65%, and the selectivity of the reaction to isobutyl vinyl...
Embodiment 2
[0036] The reaction of acetylene and isobutanol uses figure 1 The cyclic reaction apparatus shown. The tubular reactor is a stainless steel tube with an inner diameter of 2mm and a length of 32m. The reactor volume is about 100ml. The process operating conditions are as follows:
[0037] Catalyst dosage: 2% of the total mass of isobutanol;
[0038] Feed flow: 200g / h;
[0039] Absorber temperature: 25°C;
[0040] Absorber pressure: 0.105MPa;
[0041] Reactor temperature: 160°C;
[0042] Reactor pressure: 4MPa;
[0043] Circulation rate: 3.6L / h.
[0044] After 3 hours of operation, the cyclic reaction system reached a steady state. The discharge rate of the reaction product was 248g / h, the conversion rate of isobutanol was 75%, and the selectivity of the reaction to isobutyl vinyl ether was 96.5%.
Embodiment 3
[0046] The reaction of acetylene and isobutanol uses figure 1 The cyclic reaction apparatus shown. The tubular reactor is a stainless steel tube with an inner diameter of 2mm and a length of 32m, and the volume of the reactor is about 100ml. The process operating conditions are as follows:
[0047] Catalyst content: 1% of the total mass of isobutanol;
[0048] Feed flow: 200g / h;
[0049] Absorber temperature: 15°C;
[0050] Absorber pressure: 0.105MPa;
[0051] Reactor temperature: 140°C;
[0052] Reactor pressure: 3MPa;
[0053] Circulation rate: 3.6L / h.
[0054] After 3 hours of operation, the cyclic reaction system reached a steady state. The discharge rate of the reaction product was 231 g / h, the conversion rate of isobutanol was 55%, and the selectivity of the reaction to isobutyl vinyl ether was 99%.
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