Preparation method of isoprene rubber
A technology of isoprene rubber and isoprene, which is applied in the field of preparation of isoprene rubber, can solve problems such as poor performance of isoprene rubber and difficulty in glue transportation
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Embodiment 1
[0041] This example is used to illustrate the preparation of the isoprene rubber provided by the present invention.
[0042] according to figure 2 The polymerization reaction device shown is for the preparation of isoprene rubber, wherein, the capacity of all polymerization reaction tanks is 5L. With the flow rate of isoprene monomer at 0.93L / h, the flow rate of n-hexane at 5L / h, the n-hexane solution of neodymium catalyst (the concentration of catalyst is 0.5×10 -2mol / L) is passed into the first kettle 5 with a flow velocity of 0.29L / h. Based on the total weight of the isoprene monomer, n-hexane and catalyst, the total content of isoprene monomer and isoprene rubber in the first kettle 5 is 15.3% by weight. After 48 minutes of polymerization in the first kettle 5, the conversion rate of isoprene monomer was 58%, and the first supplementary solvent device 9 between the first kettle 5 and the second kettle 6 was opened. Adjust the frequency of the metering pump to be 28Hz, ...
Embodiment 2
[0047] This example is used to illustrate the preparation of the isoprene rubber provided by the present invention.
[0048] according to figure 2 The polymerization reaction device shown is for the preparation of isoprene rubber, wherein, the capacity of all polymerization reaction tanks is 5L. With the flow rate of isoprene monomer at 1.1L / h, the flow rate of n-hexane at 4.9L / h, the n-hexane solution of neodymium catalyst (the concentration of catalyst is 0.6×10 -2 mol / L) is passed into the first kettle 5 with a flow velocity of 0.278L / h. Based on the total weight of the isoprene monomer, n-hexane and catalyst, the total content of isoprene monomer and isoprene rubber in the first kettle 5 is 17.3% by weight. After 47.8 minutes of polymerization in the first kettle 5, the conversion rate of isoprene monomer was 60%, and the first additional solvent addition device 9 between the first kettle 5 and the second kettle 6 was opened. Adjust the frequency of the metering pump t...
Embodiment 3
[0053] This example is used to illustrate the preparation of the isoprene rubber provided by the present invention.
[0054] according to figure 2 The polymerization reaction device shown is for the preparation of isoprene rubber, wherein, the capacity of all polymerization reaction tanks is 5L. With the flow rate of isoprene monomer at 1.05L / h, the flow rate of n-hexane at 3.62L / h, the n-hexane solution of neodymium catalyst (the concentration of catalyst is 0.5×10 -2 mol / L) is passed into the first kettle 5 with a flow velocity of 0.33L / h. Based on the total weight of the isoprene monomer, n-hexane and catalyst, the total content of isoprene monomer and isoprene rubber in the first kettle 5 is 21% by weight. After 60 minutes of polymerization in the first kettle 5, the conversion rate of isoprene monomer was 60%, and the first additional solvent addition device 9 between the first kettle 5 and the second kettle 6 was opened. Adjust the frequency of the metering pump to b...
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