A kind of aluminum trichloride catalyst system and its method for producing low molecular weight polyisobutylene
A technology of aluminum trichloride and low molecular weight, applied in the direction of physical/chemical process catalysts, organic compound/hydride/coordination complex catalysts, chemical instruments and methods, etc., can solve unfavorable environmental protection, environmental pollution, preparation process, etc. Complexity and other problems, to achieve the effect of easy operation, easy polymerization reaction and simple preparation process
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Embodiment 1
[0031] Add 700 kg of isobutylene oligomers to the catalyst preparation tank, start stirring, add 300 kg of anhydrous aluminum trichloride powder, and continue stirring for 30 minutes to obtain a catalyst suspension in which anhydrous aluminum trichloride is dispersed in isobutylene oligomers;
[0032] The average particle size of anhydrous aluminum trichloride powder is 120 μm;
[0033] A mixed C4 raw material with an isobutylene content of 55% (weight) is continuously added to the reactor. The water content of the mixed C4 raw material is 70ppm, and the feed flow rate is 2200kg / h. At the same time, the aluminum trichloride catalyst is continuously added to suspend Liquid, the feed flow rate is 12kg / h, the temperature of the polymerization reaction liquid in the control reactor is 5°C, the pressure is 0.4MPa, and the reaction time is 25 minutes. The mixed material is continuously discharged from the product outlet of the reactor, and continuously Add sodium hydroxide aqueous s...
Embodiment 2
[0040] The same equipment and process technology as in Example 1, the difference is that the feed flow rate of the aluminum trichloride catalyst suspension in the reactor is 10kg / h, the temperature of the polymerization liquid in the reactor is 0 ° C, and the vacuum degree in the product refining process is 1.6Kpa; the obtained product low molecular weight polyisobutylene number average molecular weight is 1300, the molecular weight distribution index is 1.9, and the conversion rate of isobutylene is 97%;
[0041] The number-average molecular weight of the by-product heavy component oligomer that comes out is the isobutylene oligomer is 310, and the total output amount is 30kg / h;
Embodiment 3
[0043] The same equipment and technology as in Example 1, the difference is that the flow of continuously adding mixed carbon four raw materials in the reactor is 1900kg / h, the flow of the aluminum trichloride catalyst suspension is 7kg / h, and the flow rate of the reactor polymerization liquid The temperature is -8°C, and the reaction time is 30 minutes;
[0044] The amount (weight) of the terminator sodium hydroxide aqueous solution in terms of sodium hydroxide is 0.155kg / h;
[0045] The flow rate of each level of water for three-level washing is 2850kg / h;
[0046] The precipitation process controls the temperature at 120°C and the pressure at 0.06MPa;
[0047] In the refining process of low molecular weight polyisobutylene products, the temperature is 150°C and the vacuum degree is 1.2KPa;
[0048] The number-average molecular weight of the obtained product low-molecular-weight polyisobutene is 2300, the molecular weight distribution index is 1.8, and the conversion rate o...
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