A method for continuous refining of akd mixture
A mixture and mixer technology, applied in the direction of organic chemistry, can solve problems such as low production efficiency, high energy consumption, and lack of fundamental improvement in product quality, and achieve the goal of improving production efficiency, improving product purity, and widening product applications. Effect
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Embodiment 1
[0034] Firstly, the washing system was tested using a twin-screw extruder and two sets of fiber coalescence and separation systems. The twin-screw extruder is used to remove the organic volatile components in the AKD mixture. The first set of fiber coalescence and separation system uses acidic water from the subsequent washing system, and the second set of fiber coalescence and separation system uses fresh dilute hydrochloric acid. It can play a role in guaranteeing the improvement of product quality.
[0035] In order to test the separation effect of the separator, a fiber collector is introduced in the front section of the separator, and the emulsified AKD mixture can be separated. The first oil-water mixture from the extracted stream flows into the fiber coalescer and exits on the same side into the mixer and separator. In the separator, the oil phase and the water phase can flow by themselves by adjusting the size of the U-shaped bend. When water phase entrainment in the...
Embodiment 2
[0040] The AKD-containing reaction mixture can be prepared using a condensation reaction method. Combination of paddle dryer and two sets of fiber coalescence and separation systems, such as figure 1 The method shown to refine the AKD mixture. Based on the feed meter composition assumed in Example 1, the calculations were performed using mass balance.
[0041] exist figure 1 Among them, the streams are numbered, implemented according to the specific steps in the summary of the invention, and the results are summarized in Table 1 below, where TEA=triethylamine, TEA·HCl=triethylamine hydrochloride. The refined AKD effluent has no organic solvent content and a moisture content of 300ppm.
[0042]
Embodiment 3
[0044] In order to investigate the effect, according to the content in Example 2, in order to better show the good effect of this system, we adjust the liquid level difference of the separator, make the oil-water two-phase transition disorder, change the water content entering the hot air drying system, and take samples Analyze the drying effect of this system. The following table 2 is the analysis result of sampling:
[0045]
[0046] The test analysis results in the above table show that for AKD with different compositions containing moisture and other impurities, as long as the hot air temperature is kept at 120°C and the hot air flow rate is 600Nm3, the product quality requirements can be met.
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