Continuous neutralizing production method of naphthalene water reducers or homology dispersers of naphthalene water reducers
A naphthalene-based water-reducing agent and a technology for a production method are applied in the field of continuous neutralization production for producing a naphthalene-based water-reducing agent or its homologous dispersant, and can solve the problem of increasing the total volume of the reactor, affecting the normal operation of the continuous reaction, and reducing the cost It can improve the utilization rate and production efficiency, reduce manual operation links, and be beneficial to product quality.
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[0029] Example 1
[0030] The continuous neutralization production method of the naphthalene-based water-reducing agent or its homologous dispersant in Example 1 includes the following steps:
[0031] (1). Continuously pump the measured naphthalene-based water-reducing agent or its homologous dispersant condensation liquid into the neutralization device, and at the same time, send the measured soda ash slurry to the neutralization device for continuous neutralization reaction;
[0032] (2). The neutralized material in step (1) overflows from the neutralization device to the buffer tank for full reaction. When the pH of the material in the buffer tank is 7-9, the material is discharged to the subsequent drying device;
[0033] (3) The foam produced in the neutralization device overflows into the foam receiving tank through the overflow pipe, and the foam is eliminated by stirring, the material is separated from the gas carbon dioxide, and the material is returned to the neutralization d...
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[0036] Example 2
[0037] The neutralization device of this embodiment 2 adopts four-stage continuous neutralization, and the soda ash slurry is continuously added to the neutralization tank 3, the neutralization tank 4, and the neutralization tank 5 according to the required amount of 22%, 28%, 28%, and 22% In the neutralization reactor 6, each stage of the neutralization reactor is provided with a foam overflow pipe two a and a reaction material discharge overflow pipe one b, and the position of the overflow pipe two a is higher than the overflow pipe one b.
[0038] Such as figure 1 As shown, the condensation liquid of the naphthalene-based water reducing agent or its homologous dispersant is continuously pumped into the neutralization tank 3, and the sodium carbonate slurry is continuously pumped into the neutralization tank 3, the neutralization tank 4, the neutralization tank 5 and the neutralization tank In 6, the pumping volume in each neutralization tank is 22%, 28%, 28% a...
Example Embodiment
[0040] Example 3
[0041] In this example 3, there is one neutralization kettle, that is, one-stage neutralization. The production method steps, other devices and connection methods are the same as those in Example 2. The neutralization uses 30% soda ash solution, and the overflow liquid flows to the foam Receive the kettle and return the material liquid to the neutralization kettle 3 after defoaming. Do not repeat the rest here.
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