Method for preparing mesophase pitch through hydrogenation upgrading and co-carbonization of FCC (Fluid Catalytic Cracking) decant oil
A mesophase pitch and hydrogenation modification technology, which is applied in the processing of tar pitch/petroleum pitch/natural pitch, chemically processing tar pitch/petroleum pitch/natural pitch, petroleum industry, etc., can solve the softening of mesophase pitch. High spot, poor spinning performance and other problems, to achieve the effect of moderating the reaction rate of carbonization, improving spinning performance, and avoiding excessive carbonization of coke
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Embodiment 1
[0021] Add 180g of vacuum distillate oil from the catalytically cracked clarified oil of Bohai Oilfield naphthenic crude oil into a 300ml stainless steel high-pressure reactor; purge and replace the air in the autoclave with high-purity nitrogen. The temperature in the autoclave rises to 80℃ and starts stirring. The temperature is 450r / min, the reaction temperature is 400℃, the pressure is increased to 4MPa, the constant temperature and pressure reaction is 4h, and the petroleum pitch with a softening point of 140℃ is obtained; then 9g (5wt% of the raw material addition) is added to the reactor 9, 10-Dihydroanthracene, purge and replace the air in the kettle with high-purity nitrogen, continue to fill with nitrogen to an initial pressure of 5MPa; start stirring, rotate at 500r / min, heat up to 410°C, react by boosting pressure for 2h, then release the pressure To normal pressure, reduce the temperature to 350°C, use high-purity nitrogen with a flow rate of 80mL / (h·g) to purge for...
Embodiment 2
[0024] Add 160g of vacuum distillate oil from the catalytically cracked clarified oil of Bohai Oilfield naphthenic crude oil into a 300ml stainless steel high-pressure reactor; purge and replace the air in the autoclave with high-purity nitrogen. The temperature in the autoclave rises to 80℃ and starts stirring. The reaction temperature is 450r / min, the reaction temperature is 460℃, the pressure is increased to 4MPa, the constant temperature and pressure reaction is 1h, and the petroleum pitch with a softening point of 150℃ is obtained; then 24g (15wt% of the raw material addition) is added to the reactor 9, 10-Dihydroanthracene, purge and replace the air in the autoclave with high-purity nitrogen, continue to fill with nitrogen to an initial pressure of 5MPa; start stirring, rotate at 500r / min, heat up to 420℃, react for 1.5h from the boost, and then release The pressure is brought to normal pressure, the temperature is lowered to 350℃, and the high-purity nitrogen gas with a f...
Embodiment 3
[0026] Add 180g of vacuum distillate oil from the catalytically cracked clarified oil of Bohai Oilfield naphthenic crude oil into a 300ml stainless steel high-pressure reactor; purge and replace the air in the autoclave with high-purity nitrogen. The temperature in the autoclave rises to 80℃ and starts stirring. The reaction temperature is 450r / min, the reaction temperature is 430℃, the pressure is increased to 4MPa, the constant temperature and pressure reaction is 2h, and the petroleum pitch with a softening point of 145℃ is obtained; then 18g (10wt% of the raw material addition) is added to the reactor 9, 10-Dihydroanthracene, purge and replace the air in the autoclave with high-purity nitrogen, continue to fill with nitrogen to an initial pressure of 5MPa; start stirring, rotate at 500r / min, heat up to 410℃, react by self-boosting for 2h, then release the pressure To normal pressure, reduce the temperature to 350°C, use high-purity nitrogen at a flow rate of 100mL / (h·g) to p...
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