Poly-alpha-olefin drag reduction agent and preparation method thereof
A technology of drag reducer and olefin, which is applied in the field of polyα-olefin drag reducer and its preparation, can solve the problems of poor shear resistance of drag reducer, improve shear resistance, reduce production cost, and is not easy to self-polymerize Effect
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Embodiment 1
[0019] Embodiment 1, the raw material composition of this polyalpha-olefin drag reducer is alpha-olefin, solvent, Ziegler Natta catalyst, gas; Gas is ethylene or propylene gas; The proportioning of raw material is alpha-olefin 5ml to 600ml, 10ml to 600ml of solvent, the content of Ziegler-Natta catalyst in the mixture of solvent and α-olefin is 0.45g / L to 17g / L, the volume of ethylene or propylene gas is at a pressure of 0.01 MPa to 0.5 MPa and a temperature of 15 ℃ to 28 ℃ is 25 L to 300L; the polyα-olefin drag reducer is obtained according to the following steps: the first step is to vacuumize the polymerization tank and replace it with nitrogen for 3 to 5 times, and add the polyalphaolefin drag reducer to the polymerization tank The required amount of solvent and α-olefin and stirred evenly; the second step, adding a cooling medium in the interlayer of the polymerization kettle to control the temperature of the material in the polymerization kettle at -30 ° C to 30 ° C; the ...
Embodiment 2
[0020] Embodiment 2, the raw material of this polyalpha-olefin drag reducer is composed of alpha-olefin, solvent, Ziegler-Natta catalyst, gas; Gas is ethylene or propylene gas; The proportioning of raw material is alpha-olefin 5ml or 600ml, 10ml or 600ml of solvent, the content of Ziegler-Natta catalyst in the mixture of solvent and α-olefin is 0.45g / L or 17g / L, the volume of ethylene or propylene gas is at a pressure of 0.01 MPa or 0.5 MPa, and a temperature of 15 °C or 28 °C is 25 L or 300L; the polyα-olefin drag reducer is obtained according to the following steps: first step, vacuumize the polymerization tank and replace it with nitrogen for 3 to 5 times, and add the The required amount of solvent and α-olefin and stirred evenly; the second step, adding a cooling medium in the interlayer of the polymerization kettle to control the temperature of the material in the polymerization kettle at -30 ° C or 30 ° C; the third step, under the protection of nitrogen to the Add the r...
Embodiment 3
[0021] Embodiment 3, as the optimization of above-mentioned embodiment: embodiment 3 α - Olefins having 3 to 20 carbon atoms α - Alkenes.
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