Method for extracting and separating phenolic substances in coal tar by using polyethyleneimine
A technology for polyethyleneimine and phenolic substances, applied in the field of coal chemical industry, can solve the problems of limited industrial application prospects, strong corrosiveness of equipment, complicated operation process, etc., and achieve the effects of stable physical properties, simple process and mild conditions
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Embodiment 1
[0018] Mix PEI with an average molecular weight of 10,000 and coal tar (a simulated oil mixed with phenol and toluene, wherein the content of phenol is 15wt%) according to a mass ratio of 0.2, so that the two are fully contacted, and extracted at 30 ° C for 60 minutes, so that the phenol As many substances as possible enter the extractant from the oil to obtain the extract phase and dephenolized oil. The stripping agent diethyl ether and the extracting phase were uniformly mixed at a mass ratio of 0.4, and stripping was carried out for 60 min at normal temperature to obtain the stripping agent phase and the extracting agent phase. The back-extractant phase and the extractant phase were distilled at 50°C and 0.01MPa for about 1 hour to obtain phenolic substances, regenerated PEI and ether. After calculation, the recovery rate of phenolic substances was 29.6%.
Embodiment 2
[0020] Mix PEI with an average molecular weight of 600 and coal tar (the simulated oil mixed with phenol, toluene and n-octane, wherein the content of toluene is 50wt% and the content of phenol is 15wt%) according to the mass ratio of 0.5, so that the two are fully contacted , extracted at 30°C for 60 min, so that as much phenolic substances as possible entered the extractant from the oil to obtain the extract phase and dephenolized oil. The stripping agent diethyl ether and the extracting phase were uniformly mixed at a mass ratio of 0.4, and stripping was carried out for 60 min at normal temperature to obtain the stripping agent phase and the extracting agent phase. The back-extractant phase and the extractant phase were distilled at 60°C and 0.01MPa for about 0.5h to obtain phenolic substances, regenerated PEI and ether. After calculation, the recovery rate of phenolic substances was 36.5%.
Embodiment 3
[0022] PEI with an average molecular weight of 600 is mixed with coal tar (the simulated oil formed by mixing phenol, toluene and n-octane, wherein the content of toluene is 50wt% and the content of phenol is 15wt%) according to the mass ratio of 1:1. Fully contact and extract at 30°C for 120 minutes, so that as much phenolic substances as possible enter the extractant from the oil to obtain the extract phase and dephenolized oil. The stripping agent diethyl ether and the extracting phase were uniformly mixed according to a mass ratio of 0.4:1, and stripping was carried out at room temperature for 30 minutes to obtain the stripping agent phase and the extracting agent phase. The back-extractant phase and the extractant phase were distilled at 60°C and 0.01MPa for about 0.5h to obtain phenolic substances, regenerated PEI and ether. After calculation, the recovery rate of phenolic substances was 36.7%.
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