Devolatilization method of trans-butadiene-isoprene rubber
A butyl pentylene rubber, devolatilization technology, applied in the production of bulk chemicals, etc., can solve the problems of polymer degradation, system temperature rise, equipment blockage, etc., and achieve the effect of simple process, broad application prospects, and good overall effect
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Embodiment 1
[0046] The sample (100g) of trans-butadiene rubber is loaded into the extraction tank, and at an extraction temperature of 45°C, a supercritical fluid is introduced to raise the extraction pressure to 10MPa; at an extraction temperature of 45°C, the extraction pressure is 10MPa, and the flow rate is Under the condition of 5kg / h~8kg / h, extract for 2h; every 15min, the supercritical fluid containing volatile matter obtained by extraction is exported, and it is successively treated by separation tank 1, separation tank 2 and activated carbon adsorption device; among them, separation tank 1, Separation tank 2 separates the supercritical fluid from volatile matter (isoprene, dimer) by means of decompression separation, and the supercritical fluid is adsorbed and purified by activated carbon and then transported to the carbon dioxide storage tank to realize the recycling of the supercritical fluid After the devolatilization is finished, cut off the supercritical fluid inlet, slowly a...
Embodiment 2
[0049] The sample (100g) of trans-butadiene rubber is packed in the extraction tank, and at an extraction temperature of 45°C, a supercritical fluid is introduced to raise the extraction pressure to 15MPa; at an extraction temperature of 45°C, the extraction pressure is 15MPa, and the flow rate is Under the condition of 5kg / h~8kg / h, extract for 2h; every 15min, the supercritical fluid containing volatile matter obtained by extraction is exported, and it is successively treated by separation tank 1, separation tank 2 and activated carbon adsorption device; among them, separation tank 1, Separation tank 2 separates the supercritical fluid from volatile matter (isoprene, dimer) by means of decompression separation, and the supercritical fluid is adsorbed and purified by activated carbon and then transported to the carbon dioxide storage tank to realize the recycling of the supercritical fluid After the devolatilization is finished, cut off the supercritical fluid inlet, slowly adj...
Embodiment 3
[0052] The sample (100g) of trans-butadiene rubber is packed into the extraction tank, and at an extraction temperature of 55°C, a supercritical fluid is introduced to raise the extraction pressure to 10MPa; at an extraction temperature of 55°C, the extraction pressure is 10MPa, and the flow rate is Under the condition of 5kg / h~8kg / h, extract for 2h; every 15min, the supercritical fluid containing volatile matter obtained by extraction is exported, and it is successively treated by separation tank 1, separation tank 2 and activated carbon adsorption device; among them, separation tank 1, Separation tank 2 separates the supercritical fluid from volatile matter (isoprene, dimer) by means of decompression separation, and the supercritical fluid is adsorbed and purified by activated carbon and then transported to the carbon dioxide storage tank to realize the recycling of the supercritical fluid After the devolatilization is finished, cut off the supercritical fluid inlet, slowly a...
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