Recovery method of polyolefin catalyst mother liquid
A polyolefin catalyst, mother liquor recovery technology, applied in chemical recovery, titanium halide and other directions, can solve the problems of high energy consumption, blockage and other problems, achieve the effect of saving equipment investment, short process flow, and reducing the number of equipment
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Embodiment 1
[0039] A polyolefin catalyst mother liquor, wherein the content of titanium tetrachloride is 82% (weight), the content of hexane is 13%, and the content of heavy component high boilers is 5%,
[0040] Catalyst mother liquor 1 enters the middle and upper part of fractionation tower C1, the feed rate is 1000kg / h, the fractionation tower is a packed tower, and the filler is IMTP 25# bulk packing. The number of trays in this tower is 40, and the tower top pressure is 105KPa. The pressure is 120KPa, the reflux ratio is 0.5, after the tower top gas phase is condensed by the fractionating tower condenser E1, 33.3% is refluxed, and the hydrocarbon solvent product 2 (hexane fraction) is extracted from the remaining liquid phase;
[0041] The gas phase is extracted from the side line in the middle of the tower, and the titanium tetrachloride product 3 is extracted after being condensed by the side line condenser E2;
[0042] 50% of the material at the bottom of the tower goes to reboile...
Embodiment 2
[0049] A mother liquor of polyolefin catalyst, wherein the content of titanium tetrachloride is 80% (weight), the content of hexane is 15%, and the content of heavy component high boilers is 5%,
[0050] Catalyst mother liquor 1 enters the fractionation tower C1, the feed rate is 2000kg / h, the fractionation tower is a packed tower, the rectification section and the stripping section all use IMTP 25# bulk packing, the number of trays of this tower is 40, and the tower top pressure It is 30KPa (G), the pressure at the bottom of the tower is 40KPa, and the reflux ratio is 0.6. After the gas phase at the top of the tower is condensed by the fractionating tower condenser E1, 37.5% is refluxed, and the hydrocarbon solvent product 2 (hexane fraction) is extracted from the remaining liquid phase;
[0051] The gas phase is extracted from the side line in the middle of the tower, and the titanium tetrachloride product 3 is extracted after being condensed by the side line condenser E2;
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