Crystallization separation method of p-xylene
A technology of p-xylene and mixed xylene, which is applied in the direction of crystallization purification/separation, organic chemistry, etc., can solve the problems of crystallizer scaling, pre-cooler scaling, and high energy consumption, and achieve refrigeration energy saving and good performance. Technical effect, the effect of solving serious fouling
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Embodiment 1
[0024] A crystallization method for separating p-xylene according to the present invention.
[0025] Such as figure 1 Said, the mixed xylene raw material a enters the raw material tundish 1, the temperature is 30°C, the flow rate is 1075kg / h, the p-xylene content is 80wt%, and a part of the mixed xylene raw material b passes through the mother liquor heat exchanger 2 and the precooler 3 Return to the raw material tundish 1 after cooling, the flow rate is 5375kg / h, a part of the mixed xylene raw material c enters the crystallizer 4 for crystallization, the flow rate is 1075kg / h, the temperature is 15°C, and the crystallization temperature is -17°C. The magma in the kettle-type crystallizer 4 flows out in two parts, and the magma d returns to the kettle-type crystallizer 4 after heat exchange in the casing-type crystallizer 5, and its flow rate is 57m 3 / h, the magma e is concentrated by the thickening device 6 to obtain the pre-separated mother liquor f and the concentrated ma...
Embodiment 2
[0027] The crystallization method of separation p-xylene of the present invention
[0028] According to the operating condition of embodiment 1, adopt as figure 2 The crystallization method for separating p-xylene, wherein the weight ratio of the pre-separation mother liquor f to the crystallization and filtration mother liquor i is 0.87:1. The specific results are shown in Table 1.
Embodiment 3
[0030] A crystallization method for separating p-xylene according to the present invention.
[0031] According to the operating condition of embodiment 1, adopt as image 3 The crystallization method for separating p-xylene, wherein the weight ratio of the pre-separation mother liquor f to the crystallization and filtration mother liquor i is 1:1. The specific results are shown in Table 1.
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