Method for preparing anti-wear agent for diesel oil by removing saturated fatty acid through membrane separation
A technology of unsaturated fatty acids and fatty acids, which is applied in the direction of fatty acid preparation/refining, fatty acid production, semi-permeable membrane separation, etc., can solve the problems of low saturated fatty acid content, etc., and achieve low saturated fatty acid content, low cloud point, and excellent low temperature performance Effect
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Embodiment 1
[0016] 3600 grams of technical grade linoleic acid (saturated fatty acid content 5.0%) was put into 5 liters of crystallization kettles with jacket cooling and stirred and cooled to -8°C and maintained for 8 hours, then cooled to -8°C under the operating environment of -8°C The crystallization feed liquid is transported to the microfiltration membrane tubular separation device with a pore size of 0.5 microns through the pipeline at the bottom of the reactor, and the cooling crystal feed liquid is continuously separated by maintaining a pressure difference of 0.3 MPa, and the diesel oil anti-wear produced by the preparation of the separation liquid is obtained The saturated fatty acid mass percentage content of the agent is 0.6%, the cloud point is -16°C, and the freezing point is -17°C.
Embodiment 2
[0018] 3600 grams of technical grade linoleic acid (saturated fatty acid content 5.0%) was put into 5 liters of crystallization kettles with jacket cooling and stirred and cooled to -8°C and maintained for 8 hours, then cooled to -8°C under the operating environment of -8°C The crystallization feed liquid is transported through the pipeline at the bottom of the reactor to the microfiltration membrane tubular separation device with a pore size of 0.5 microns, and the cooling crystal feed liquid is continuously separated by maintaining a pressure difference of 0.1 MPa, and the separation liquid is prepared to obtain diesel anti-wear The saturated fatty acid mass percentage content of the agent is 0.6%, the cloud point is -16°C, and the freezing point is -17°C.
Embodiment 3
[0020] 3600 grams of technical grade linoleic acid (saturated fatty acid content 5.0%) was put into 5 liters of crystallization kettles with jacket cooling and stirred and cooled to -8°C and maintained for 8 hours, then cooled to -8°C under the operating environment of -8°C The crystallization feed liquid is transported to the microfiltration membrane tubular separation device with a pore size of 0.1 micron through the pipeline at the bottom of the reactor, and the cooled feed liquid is continuously separated by maintaining a pressure difference of 0.6 MPa to obtain the separated liquid. The mass percentage of saturated fatty acid in the grinding agent is 0.5%, the cloud point is -16°C, and the freezing point is -17°C.
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