Laboratory extraction method for preparing colloid blended component of needle coke
An extraction method and laboratory technology, applied in the direction of solid solvent extraction, etc., to achieve the effect of reliable raw material source, simple structure and low operating cost
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Embodiment 1
[0060] A kind of laboratory extraction method that is used for preparing the colloid blending component of needle coke, comprises the steps:
[0061] (1) After the raw material asphalt is temporarily stored in the raw material asphalt tank 2, it is sent to the raw material / solvent static mixer 5 through the raw material asphalt pump 4; the low-carbon aliphatic hydrocarbon is passed from the low-carbon aliphatic hydrocarbon solvent tank 1 through the low-carbon aliphatic hydrocarbon solvent pump 3 Send into the raw material / solvent static mixer 5; low-carbon aliphatic hydrocarbons and raw material pitch enter the supercritical extraction tower 8 after fully mixing in the raw material / solvent static mixer;
[0062] (2) Low-carbon aliphatic hydrocarbon carries out supercritical extraction to the saturated content in the raw material pitch, the aromatic component in the supercritical extraction tower 8, and the saturated component in the raw material pitch, the aromatic component d...
Embodiment 2
[0069] The present invention also provides a laboratory extraction method for colloid blending components used to prepare needle coke, comprising the following refinement steps:
[0070] (1) join a certain amount of low-carbon aliphatic hydrocarbons in low-carbon aliphatic hydrocarbon solvent tank 1 and supercritical extraction tower 8 earlier; Then a certain amount of colloidal solvent is added in colloidal solvent tank 14; Then a certain amount The raw asphalt is added to the raw asphalt tank 2.
[0071] (2) After the raw asphalt is temporarily stored in the raw asphalt tank, turn on the low-carbon aliphatic hydrocarbon solvent pump 3 to inject the low-carbon aliphatic hydrocarbon into the raw material / solvent static mixer 5, and simultaneously turn on the raw asphalt pump 4 to inject the raw asphalt into the raw material / solvent static mixer Mixer 5: The volume ratio of low-carbon aliphatic hydrocarbons and raw material pitch in the raw material / solvent static mixer is 2:1-...
Embodiment 3
[0080] Embodiment 3: Raw material asphalt is selected Kuwaiti vacuum residue (raw material 1 four-component composition is shown in Table 1); Low-carbon aliphatic hydrocarbon is selected propane; Colloidal solvent is selected tetrahydrofuran; The mixing volume ratio of propane and Kuwait vacuum residue is 4 : 1; the mixing volume ratio of tetrahydrofuran and supercritical raffinate is 3:1; the operating pressure of the supercritical extraction tower is 4.5MPa, and the operating temperature is 110°C; the operating pressure of the supercritical recovery tower is 1.5MPa, and the operating temperature is 110°C; The operating pressure of the residue collection tank is 1.5MPa, and the operating temperature is 110°C; the operating pressure of the colloid extraction tower is 0.05MPa, and the operating temperature is 50°C; the operating pressure of the colloid solvent recovery tower is 0.05MPa, and the operating temperature is 100°C; MPa, the operating temperature is 100°C.
[0081] Ta...
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