This invention, (a) being the process which offers the acidic liquid water monomer blend which contains dissolved oxygen, in order to offer the super absorption polymer after the polymerization with that, the process where monomer is chosen, (b) the aforementioned water monomer blend the process which it supplies to the reactor continually, (being the process which introduces carbonate or hydrogen carbonate source in the aforementioned water monomer blend before the entry to inside c) reactor, forms carbon dioxide and the vapor phase which includes at least the portion of aforementioned dissolved oxygen with that, the aforementioned vapor phase distributes in the liquid phaseThe process having done, (d) it offers the vapor/liquid blend to part phase separation at least immediately before or immediately after the entry to inside the reactor, the process which removes the vapor phase which is separated at least partly, (e) offering the liquid phase to free radical polymerization inside the reactor, the process which obtains the super absorption polymer, and (f) it regards the continual manner for producing the super absorption polymer which includes the process which removes the super absorption polymer continually from the reactor.本発明は、(a)溶存酸素を含有する酸性液体水性モノマー混合物を提供する工程であって、それによって、超吸収性ポリマーを重合後に提供するようにモノマーが選択される工程、(b)前記水性モノマー混合物を反応器に連続的に供給する工程、(c)反応器内への投入の前に炭酸塩又は炭酸水素塩源を前記水性モノマー混合物中に導入する工程であって、それによって二酸化炭素及び前記溶存酸素の少なくとも一部を含む気相を形成し、前記気相が液相中に分散している工程、(d)反応器内への投入の直前又は直後に気体/液体混合物を少なくとも部分的な相分離に供し、分離された気相を少なくとも部分的に除去する工程、(e)反応器内で液相をフリーラジカル重合に供して超吸収性ポリマーを得る工程、及び(f)反応器から超吸収性ポリマーを連続的に除去する工程を含む超吸収性ポリマーの製造のための連続的方法に関する。
