Production equipment and preparation technology for o-chlorotoluene Grignard reagent
A technology of o-chlorotoluene and Grignard reagent, which is applied in the field of production equipment and preparation technology of o-chlorotoluene Grignard reagent, can solve problems such as difficult and difficult separation of magnesium chips, and achieve the effect of improving the yield
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Embodiment 1
[0037] Utilize production equipment among the present invention to prepare o-chlorotoluene Grignard reagent, step is as follows:
[0038] (1) Anhydrous tetrahydrofuran (THF) with a flow rate of 10kg / h, ortho-chlorotoluene and magnesium chips with a flow rate of 5kg / h are passed into the first-level reaction kettle together through the first dip tube, and anhydrous tetrahydrofuran (THF), ortho-chlorotoluene and magnesium Chips are heated up to 65°C while flowing through the first dipping pipe;
[0039] (2) flow is that the anhydrous tetrahydrofuran of 20kg / h, the ortho-chlorotoluene that flow is 10kg / h and the toluene that flow is 10kg / h are passed in the first-level reactor by feed pipe, and step (1) in The mixed liquids are mixed and heated to 80°C to obtain a reaction mixture;
[0040](3) The reaction mixture enters the secondary reaction kettle through the overflow guide pipe of the primary reaction kettle, and is mixed with the incoming magnesium chips, heated to 80°C, an...
Embodiment 2
[0043] Utilize production equipment among the present invention to prepare o-chlorotoluene Grignard reagent, step is as follows:
[0044] (1) Be that the anhydrous tetrahydrofuran of 25kg / h, the ortho-chlorotoluene and the magnesium chips that the flow is 5kg / h are passed into the primary reaction kettle together through the first dipping pipe, anhydrous tetrahydrofuran, ortho-chlorotoluene and magnesium Chips are heated to 70°C while flowing through the first dipping pipe;
[0045] (2) flow is that the anhydrous tetrahydrofuran of 40kg / h, the ortho-chlorotoluene that flow is 10kg / h and the toluene that flow is 15kg / h are passed in the first-level reaction still by feeding pipe, with step (1) The mixed liquids are mixed and heated to 85°C to obtain a reaction mixture;
[0046] (3) The reaction mixture enters the secondary reaction kettle through the overflow guide pipe of the primary reaction kettle, and is mixed with the incoming magnesium chips, heated to 85°C, and the Grig...
Embodiment 3
[0049] Utilize production equipment among the present invention to prepare o-chlorotoluene Grignard reagent, step is as follows:
[0050] (1) Anhydrous tetrahydrofuran (THF) with a flow rate of 20kg / h, ortho-chlorotoluene and magnesium chips with a flow rate of 5kg / h are passed into the first-level reaction kettle together through the first dip tube, and anhydrous tetrahydrofuran (THF), ortho-chlorotoluene and magnesium Chips are heated up to 65°C while flowing through the first dipping pipe;
[0051] (2) flow is that the anhydrous tetrahydrofuran of 30kg / h, the ortho-chlorotoluene that flow is 10kg / h and the toluene that flow is 12kg / h are passed in the first-level reactor by feeding pipe, and step (1) in The mixed liquids are mixed and heated to 85°C to obtain a reaction mixture;
[0052] (3) The reaction mixture enters the secondary reaction kettle through the overflow guide pipe of the primary reaction kettle, and is mixed with the incoming magnesium chips, heated to 85°C...
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