Production method of high-adaptability green scale inhibitor and composite scale inhibitor thereof
A technology of composite antiscalant and production method, which is applied in chemical instruments and methods, descaling and water softening, water/sludge/sewage treatment, etc., can solve aggravated environmental pollution, different adaptability, and non-conforming to environmental protection Sustainable development and other issues, to achieve the effect of high coordination, increased corrosion inhibition, and good compound use effect
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Embodiment 1
[0029] The production method of highly adaptable green scale inhibitor according to the present embodiment comprises the following steps:
[0030] (1) Preparation of mixed catalyst
[0031] Mix the dibasic acid polymer and the ionic liquid at a mass ratio of 1:1, and stir evenly to obtain a mixed catalyst. Among them, the dibasic acid polymer is reacted at 160°C with oxalic acid and ethylene glycol as raw materials until there is no more distillate. After cooling, phthalic anhydride is added, and the temperature is slowly raised to 200°C. React until there is no more effluent. Then cool it for later use. The ionic liquid is [Hmim]HSO 4 .
[0032] (2) Thermal polycondensation of aspartic acid
[0033] Add the mixed catalyst and aspartic acid into the reactor at a ratio of 1:1.1, stir and heat to 180° C., and the reaction time is 2 hours to obtain a mixed reaction liquid. Suction filtration after standing to obtain polysuccinimide.
[0034] (3) Generation reaction of polya...
Embodiment 2
[0050] The difference from Example 1 is that the dibasic acid polymer and the ionic liquid are mixed in a mass ratio of 2:3, and the ionic liquid is [Bmim]HSO 4 , the thermal polycondensation reaction temperature was 200°C, the reaction time was 3h, and other steps and parameters were the same as in Example 1.
[0051] The composite scale inhibitor A compounded with the polyaspartic acid sample prepared according to the production method of the highly adaptable green scale inhibitor in this embodiment has a scale inhibition rate of 98.5% and a corrosion inhibition rate of 92.7%; Scale inhibitor B, the scale inhibition rate reaches 95.1%, and the corrosion inhibition rate reaches 69%; the compound scale inhibitor C, the scale inhibition rate reaches 92.5%, and the corrosion inhibition rate reaches 87.3%; the compound scale inhibitor D, the scale inhibition rate reaches 97.4% , the corrosion inhibition rate reached 92.1%; the composite scale inhibitor E, the scale inhibition rat...
Embodiment 3
[0053] The difference from Example 1 is that the dibasic acid polymer and the ionic liquid are mixed in a mass ratio of 5:6, the ionic liquid is [Bmim]Br, the hydrolysis temperature is 40°C under alkaline conditions, the hydrolysis time is 1.5h, other steps And, parameter are identical with embodiment 1.
[0054] The composite scale inhibitor A compounded by the polyaspartic acid sample prepared according to the production method of the highly adaptable green scale inhibitor in this embodiment has a scale inhibition rate of 97.5% and a corrosion inhibition rate of 93.8%; Scale inhibitor B, the scale inhibition rate reaches 93.7%, and the corrosion inhibition rate reaches 70.5%; the compound scale inhibitor C, the scale inhibition rate reaches 90.7%, and the corrosion inhibition rate reaches 88.9%; the compound scale inhibitor D, the scale inhibition rate reaches 95.6% , the corrosion inhibition rate reached 98.1%; the composite scale inhibitor E, the scale inhibition rate reac...
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