A kind of preparation method of mesophase pitch and mesophase carbon microspheres
A technology for mesophase carbon microspheres and mesophase pitch, which is applied in the preparation/purification of carbon, the processing of tar pitch/petroleum pitch/natural pitch, and the processing of tar pitch/petroleum pitch/natural pitch by selective extraction, etc. The problems of low yield and uneven particle size distribution of mesophase pitch and mesophase carbon microspheres can achieve the effect of high raw material processing depth, narrow size distribution and good sphericity
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Embodiment 1
[0023] The medium and low temperature coal tar heavy oil fraction was extracted and separated by n-heptane solvent to obtain n-heptane insoluble matter, and 300 g of the solvent was extracted after the oil was evaporated to dryness. In the autoclave, at the reaction temperature of 330°C, N 2 Under atmospheric protection, the reaction time was 5h for shallow catalysis, and the polycondensation heavy product with components > 450 °C was pulled out through the decompression device; 10 mg of n-heptane insoluble matter and 6 g of free radical auxiliary tetralin were added to the polycondensation heavy product to fully After mixing, take 200 g of it and add it to the autoclave, and react at a reaction temperature of 420 °C, a reaction pressure of 4 MPa, and a reaction time of 8 h. After the synergistic polycondensation of the two, the content of the wide-area mesophase pitch is 94.7%, and the softening point is 246 °C; After the mesophase pitch is cooled to room temperature, pulveri...
Embodiment 2
[0025]The high-temperature coal tar heavy oil fraction was extracted and separated by n-heptane solvent to obtain n-heptane insoluble matter. After the solvent was extracted from the oil and evaporated to dryness, 300 g of the oil was taken, and 6 g of carbonyl iron was doped into it. After fully mixing, it was added to the high-pressure reaction In the kettle, at the reaction temperature of 350°C, N 2 Under the atmosphere protection, the reaction time was 6 h for shallow catalysis, and the polycondensation heavy product with components > 450 °C was pulled out through the decompression device; 10 mg of n-heptane insoluble matter and 2 g of the free radical auxiliary decalin were added to the polycondensation heavy product to fully After mixing, take 200g and add it to the autoclave, at a reaction temperature of 450°C, N 2 The reaction time was 8h under the protection of atmosphere. After the two synergistic polycondensation, the content of wide-area mesophase pitch was 97.7% a...
Embodiment 3
[0027] The vacuum residue oil is extracted and separated by n-heptane solvent to obtain n-heptane insoluble matter. After the solvent is extracted and the solvent is evaporated to dryness, 300 g of the oil is taken, 21 g of cobalt naphthenate is doped into it, and the mixture is fully mixed and added to the autoclave. , at a reaction temperature of 330 °C, N 2 Carry out shallow catalysis under the condition of reaction time of 5h under atmosphere protection, and pull out the polycondensation heavy product with components > 450 ℃ through the decompression device; add 20 mg of n-heptane insoluble matter and 10 g of free radical auxiliary dihydrophenanthrene to the polycondensation heavy product , after fully mixing, take 200 g of it and add it to the high-pressure reaction kettle, and react at a reaction temperature of 440 ° C, a reaction pressure of 3 MPa, and a reaction time of 10 h. After the synergistic polycondensation of the two, the content of the wide-area mesophase pitch...
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