Prepn. process and apparatus of polytetramethylene ether glycol
A technology of polytetramethylene ether glycol and tetramethylene ether glycol is applied in the field of preparing polytetramethylene ether glycol, and can solve the problems of large space and uneconomical settlement of sedimentation tanks.
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Embodiment 1
[0091] Embodiment 1: prepare PTMEG technology and the control of PTMEG molecular weight in reactor
[0092] Towards figure 1 and figure 2 Add 200Kg THF in the shown reactor 1 with external circulation, 100Kg contains 12 tungstophosphoric acid catalysts of 3-5 crystal waters, after opening the agitator 1-2, start to slowly add process water (0.2kg / min), while Open the external circulation system and open the valves 1-8 and 1-9, the molecular weight monitoring device participates in the circulation, after 2.5 minutes, stop adding water, close the valves 1-8, 1-9. After 1 minute, the reaction material is in the expansion body 7-2 Automatic stratification in the middle, the lower part is the catalyst phase, and the upper part is the organic phase containing dissolved catalyst and unreacted tetrahydrofuran. The conductivity meter is inserted into the organic phase to measure the conductivity at the initial stage. If the conductivity is less than 8ms / cm (corresponding to the con...
Embodiment 2
[0093] Embodiment 2. extractor and extraction process thereof
[0094] To a traditional extractor (without a central draft tube and a lower settling zone, such as Chemical Engineering Handbook, Part 5, Stirring and Mixing, P56 page Figure 4-3, liquid-liquid phase agitator for extraction, chemical industry Publishing House, December, 1985, Beijing 1st Edition), and the extractor 4 of the present invention respectively add 30 liters of feed liquid at the bottom of the first flasher 3, the feed liquid consists of about 85wt% of PTMEG, 15wt% of tetrahydrofuran and a trace amount of The impurity such as the catalyst of dissolving, add 60kg toluene extractant respectively to two extractors, traditional extractor temperature control 65 ℃, extractor temperature control 60 ℃ of the present invention. After the traditional extractor was stirred for 1.5 hours, the precipitated catalyst phase was discharged in a controlled manner from the bottom of the extractor, and the stirring was cont...
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