Method for separating p-xylene by multistage suspension melt crystallization
A suspension melt crystallization and p-xylene technology, which is applied in crystallization purification/separation, organic chemistry, climate sustainability, etc. It can solve the problems of unstable operation of aging kettles and high energy consumption in production, so as to ensure product purity and stable output , the effect of energy consumption reduction
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Embodiment 1
[0026] The invention relates to a multistage suspension melting crystallization method for separating p-xylene.
[0027] Such as figure 1 Said, containing p-xylene concentration is 82% raw material 1, flow rate is 1075kg / h, is divided into two strands after being cooled by mother liquor heat exchanger A and precooler B, a part of raw material 2, flow rate is 645kg / h, enters P-xylene crystals 13 and p-xylene crystals 18 are subjected to beating washing and heating aging in the aging kettle C. The operating temperature of the aging kettle is 5° C., and a part of the raw material 3 with a flow rate of 430 kg / h enters the primary crystallizer D for Crystallization, the operating temperature of the crystallizer is -3°C; the residence time of the crystal slurry 4 in the aging kettle is 30 minutes, containing 30% p-xylene crystals, and the p-xylene crystals 5 and the aging mother liquor are obtained after being separated by the solid-liquid separator E 6, the aging mother liquor 6 i...
Embodiment 2
[0029] The invention relates to a multistage suspension melting crystallization method for separating p-xylene.
[0030] According to the operating conditions of Example 1, wherein the flow rate of raw material 2 entering the aging tank is 430kg / h, the results are listed in Table 1.
Embodiment 3
[0032] The invention relates to a multistage suspension melting crystallization method for separating p-xylene.
[0033] According to the operating conditions of Example 1, wherein, the flow rate of raw material 2 entering the aging tank is 1075kg / h, and the results are listed in Table 1.
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