High-carbon fatty acid-terminated polyether ester defoamer for papermaking
A technology of high-carbon fatty acid ester and high-carbon fatty acid, applied in defoamer and other directions, can solve the problems of inability to effectively eliminate foam, low foam breaking rate, etc., and achieve excellent defoaming and foam suppression performance, low cost and simple process Effect
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Embodiment 1
[0019] Embodiment 1: 100 parts by weight of propylene oxide, 5 parts by weight of itaconic anhydride, 5 parts by weight of carbon dioxide, and 1 part by weight of ethylene glycol take DMC as a catalyst at 60 o C copolymerization obtains polyether ester, continues to add 20 parts by weight of dodecanoic acid at 120 o C undergoes an esterification reaction and vacuum devolatilization to obtain a high-carbon fatty acid-terminated polyether ester A.
Embodiment 2
[0020] Embodiment 2: 80 parts by weight of propylene oxide, 20 parts by weight of ethylene oxide, 5 parts by weight of itaconic anhydride, 5 parts by weight of carbon dioxide, 1 part by weight of ethylene glycol with DMC as a catalyst at 60 o C copolymerization obtains polyether ester, continues to add 10 parts by weight of dodecanoic acid at 120 o C undergoes an esterification reaction and vacuum devolatilization to obtain a high-carbon fatty acid-terminated polyether ester B.
Embodiment 3
[0021] Embodiment 3: 100 parts by weight of propylene oxide, 0.1 parts by weight of maleic anhydride, 0.1 parts by weight of ethylene glycol take KOH as a catalyst at 50 o C copolymerization obtains polyether ester, continues to add 10 parts by weight methyl capric acid at 80 o C is subjected to transesterification and vacuum devolatilization to obtain high-carbon fatty acid-terminated polyether ester C.
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