Tristyrylphenol block polyether, sulfate ammonium salt and preparation method thereof
A technology of tristyryl phenol and block polyether, applied in the field of surfactants, can solve the problems of great influence on product quality, great influence on reaction temperature, wide molecular weight distribution, etc., achieve light product color and reduce Kraft point , the effect of narrow molecular weight distribution
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[0032] like figure 1 As shown, the preparation method of the triphenylphenol block polyether of the present invention includes the following steps:
[0033] Step S101. The catalyst A and triphenylphenol are put into the glass sealing reactor, and the nitrogen gas (preferably replacing nitrogen is 2 times), evacuated, and the ethylene oxide reaction is introduced after the temperature rise dehydration, resulting in the reaction liquid A; where the temperature of the temperature is 110 ° C, the dehydration time is 1 h, and the epoxy ethane is slowly introduced at 110 ° C to 120 ° C. The reaction pressure is not significantly decreased, and the reaction liquid A is obtained. Moreover, the amount of catalyst A is preferably 3 ‰ of Trisstyrene phenol and total quality of ethylene oxide.
[0034] Step S102. The reaction liquid A is treated by adsorption method, in particular: adding an adsorbent, diatomaceous earth, phosphoric acid and deionized water in the reaction liquid A, and then ...
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[0046] Example 1】
[0047] First, 1.76 GKOH and 282 g of triphenyl vinyl phenol are put into 2.5L glass sealing reactor, and replace it 3 times N 2 After the vacuum, the temperature is raised to 110 ° C for 1 h; then at 110 ° C to 120 ° C, 306 g of ethylene oxide reaction is slowly transferred, and the reaction pressure is not obvious, stopped, and the reaction is supplied to the 2L four flask; The adsorbent, diatomaceous earth, phosphoric acid and deionized water are added, and the vacuum dehydration is gradually warmed, and the vacuum dehydration is 1.5h at 110 ° C, and the filtration is filled with heat. Finally, the filtrate and 0.2 g of DMC catalyst were poured into clean 2.5 L Glass sealing reactor, and replace it 3 times N 2 After the vacuum is maximum, the vacuum is stopped after heating to 100 ° C, and begins to slowly enter 1412 g of the propylene oxide reaction, the reaction temperature is between 110 ° C to 120 ° C, and the reaction pressure is not obvious, stop the re...
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[0048] [Example 2]
[0049] First, 2.34 gkOH and 268 g of triphenyl vinyl phenol are put into 2.5L glass sealing reactor, and replace it 3 times N 2 After the vacuum, the temperature is tapered to 110 ° C for 1 h; then the 512 g of ethylene oxide reaction is slowly passed at 110 ° C to 120 ° C, and the reaction pressure is not obvious, stopping the reaction, from the 2L four flask; The adsorbent, diatomaceous earth, phosphoric acid and deionized water are added, and the vacuum dehydration is gradually warmed, and the vacuum dehydration is 1.5h at 110 ° C, and the filtration is filled with heat. Finally, the filtrate and 0.2 g of DMC catalyst were poured into clean 2.5 L Glass sealing reactor, and replace it 3 times N 2 After the vacuum to the highest, the vacuum is turned to the vacuum after heating to 100 ° C, and begins to slowly enter 1150 g of propylene oxide reaction, the control reaction temperature is between 110 ° C to 120 ° C, and the reaction pressure is not obvious, sto...
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