Method for preparing intermediate-phase asphalt by crosslinking modifying and settling separation of FCC (fluid catalytic cracking) clear oil
A mesophase pitch and mesophase technology, which is applied in the direction of chemical processing of tar pitch/petroleum pitch/natural pitch, etc., can solve the problems of poor spinning performance and low content of anisotropic structure, so as to promote the formation and benefit Sequential arrangement, good fluidity effect
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Embodiment 1
[0018] The naphthenic crude oil catalytic cracking clarified oil decompression distillate oil 300g and 15g (5wt% of raw material addition) polybutadiene diol are joined in the volume of 500ml stainless steel autoclave with the naphthenic crude oil catalytic cracking clarified oil vacuum distillate oil; Sweep the air in the displacement kettle, continue to fill nitrogen to the initial pressure of 5MPa, start stirring at a speed of 500r / min, raise the temperature to 380°C, and react for 4 hours from the booster, then release the pressure to normal pressure, cool down to 300°C, and use a flow rate of 80mL / (h·g) of high-purity nitrogen was purged for 0.5h to obtain modified oil; continue to heat up to 430°C, rotate at 500r / min, self-boost to 4MPa, react at constant temperature and pressure for 8h, and obtain a softening point of 216°C mesophase precursor; then lower the temperature to 320°C and settle for 2 hours under normal pressure. The product in the reactor is divided into two...
Embodiment 2
[0021]The naphthenic crude catalytic cracking clarified oil decompression distillate oil 280g and 42g (15wt% of raw material addition) polybutadiene diol of Bohai Oilfield joins volume as in the stainless steel autoclave of 500ml; Sweep the air in the replacement kettle, continue to fill nitrogen to the initial pressure of 5MPa, start stirring at a speed of 500r / min, raise the temperature to 450°C, and react for 1h from the booster, then release the pressure to normal pressure, cool down to 300°C, and use a flow rate of 80mL / (h·g) of high-purity nitrogen was purged for 0.5h to obtain modified oil; continue to heat up to 440°C, rotate at 500r / min, self-boost to 4MPa, react at constant temperature and pressure for 6h, and obtain a softening point of 231°C mesophase precursor; then lower the temperature to 330°C and settle for 2 hours under normal pressure. The product in the reactor is divided into two layers. The mesophase pitch with watershed optical structure has a softening ...
Embodiment 3
[0023] The naphthenic crude oil catalytic cracking oil slurry vacuum distillate oil 300g and 24g (8wt% of raw material addition) polybutadiene diol of Bohai Oilfield are joined in the 500ml stainless steel autoclave; Pass into high-purity nitrogen to blow Sweep the air in the replacement kettle, continue to fill nitrogen to the initial pressure of 5MPa, start stirring at a speed of 500r / min, raise the temperature to 420°C, and react for 2.5 hours from the booster, then release the pressure to normal pressure, cool down to 300°C, and use the flow rate Purging 80mL / (h·g) of high-purity nitrogen for 0.5h to obtain modified oil; continue to raise the temperature to 440°C, rotate at 500r / min, self-boost to 4MPa, react at constant temperature and pressure for 6h, and obtain a softening point of 223 ℃ mesophase precursor; then lower the temperature to 320℃, and settle for 2 hours under normal pressure. The mesophase pitch with large watershed optical structure has a softening point o...
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