Method for producing rare earth isoprene rubber
A rare earth isoprene rubber and isoprene technology, applied in the field of polymer production, can solve the problems of large total steam volume and high proportion of production cost and energy consumption
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Embodiment 1
[0054] This embodiment adopts figure 1 The three reactors shown in the diagram are successively connected in series to carry out solution polymerization reaction, and the volume of each polymerization reactor is 120 L, and this embodiment adopts continuous process operation.
[0055] In the first reactor in the present embodiment, the feed rate of total material (including circulating glue, the same below) is 112.5kg / h, wherein the feed rate of isoprene monomer is 21.5kg / h, the amount of solvent The feed rate is 79.4kg / h, the feed rate of the catalyst is 5.6kg / h, and the feed temperature of the three materials after being cooled by the ethylene glycol refrigeration unit is -5°C to control the operating temperature of the three reactors And export conversion rate as shown in Table 1. And, the amount of the rare earth isoprene rubber glue that circulates back to the first reactor inlet is 6kg / h, and before entering the first reactor inlet, the temperature of the circulating glu...
Embodiment 2
[0057] This example is carried out using the same polymerization reactor as Example 1.
[0058] In the first reactor in this embodiment, the total feed rate of materials is 112.5 kg / h, wherein the feed rate of isoprene monomer is 21.5 kg / h, and the feed rate of solvent is 64.4 kg / h, The feed rate of the catalyst is 5.6kg / h, and the feed temperature of the three materials after being cooled by the ethylene glycol refrigeration unit is -5°C, so as to control the operating temperature and outlet conversion rate of the three reactors as shown in Table 1 Show. And, the amount of the rare earth isoprene rubber glue that circulates back to the first reactor inlet is 21kg / h, and before entering the first reactor inlet, the temperature of the circulating glue from the third reactor is cooled to 5°C. The average residence time of the material in each reactor is 40min, then after adiabatic solution polymerization, the glue solution concentration recorded at the outlet of the first reac...
Embodiment 3
[0060] This example is carried out using the same polymerization reactor as Example 1.
[0061] In the first reactor in this embodiment, the total material feed rate is 130kg / h, wherein the feed rate of isoprene monomer is 26.5 kg / h, the feed rate of solvent is 83.6 kg / h, and the catalyst The feed rate of the reactor is 6.9kg / h, and the feed temperature of the three feeds after being cooled by the ethylene glycol refrigeration unit is -10°C, so as to control the operating temperature and outlet conversion rate of the three reactors as shown in Table 1 . And, the amount of the rare earth isoprene rubber glue that circulates back to the first reactor inlet is 13kg / h, and before entering the first reactor inlet, the temperature of the circulating glue from the third reactor is cooled to 16°C. The average residence time of the material in each reactor is 35min, then after adiabatic solution polymerization, the glue concentration of the first reactor, the second reactor and the t...
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