A method and system for recovering materials from crystallization feed liquid
A technology for recovering materials and feed liquids, which is applied to the general layout of crystallization devices, crystallization separation, solution crystallization, etc., can solve the problems of heat-sensitive product deterioration appearance, low product recovery rate, high recovery cost, etc., achieve good economic benefits, reduce Effects of environmental pollution and improvement of recovery rate
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Embodiment 1
[0038] This embodiment is example with anilinoacetonitrile:
[0039] Anilinoacetonitrile belongs to the dye intermediates, used for the production of indigo, slightly soluble in water, easily soluble in ethanol and acetone, with a melting point of 40°C.
[0040] figure 2 Shown is a schematic structural diagram of the recycling system of this embodiment.
[0041] A recovery method for anilinoacetonitrile product, comprising the following steps:
[0042] 1) Transfer the anilinoacetonitrile sand blasting solution into the crystallization tank 1 (capacity 15000L), lower the temperature to 30°C, and the stirring speed of the crystallization tank 1 is 15r / min. In this step, the volume of liquid in the crystallization tank 1 is relatively large, reaching 15000L. Therefore, if it is cooled to a lower temperature, energy consumption will be increased, thereby increasing costs. Cooling to 30°C can make the products in the sanding liquid A large number of precipitates from the soluti...
Embodiment 2
[0066] This embodiment takes yellow blood salt sodium as an example, and its recovery system is as follows: figure 2 As shown, the raw material liquid of the yellow blood salt sodium product that is separated by evaporation enters the crystallization kettle 1, and the stirring speed of the feed liquid in the crystallization kettle 1 is 40-70r / min, and the stirring speed of the present embodiment is 50r / min, slowly cooling to 35°C, enter the solid-liquid separation equipment 2 for solid-liquid separation, and the separated mother liquor enters the thickener 3 for sedimentation and separation. The concentrated liquid in the lower layer of the thickener 3 is transferred to the crystallization kettle 1 through the concentrated liquid transfer pump 5, mixed with the normal batch crystallization feed liquid, and then enters the solid-liquid separation device 2 for centrifugation, and the clear liquid overflowed from the upper layer of the thickener 3 enters the The clear liquid tra...
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Abstract
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