Reaction device and method for continuous production of n-(β-aminoethyl)-γ-aminopropyltrimethoxysilane
A technology of aminopropyltrimethoxysilane and a reaction device, which is applied in the field of silane coupling agents, can solve the problems of reduced production, increased product consumption, increased consumption, etc., to reduce labor intensity and workload, simplify application steps, increase The effect of reaction rate
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Embodiment 1
[0039] 1. Vaporization of ethylenediamine: pump the raw material ethylenediamine into the ethylenediamine vaporization kettle 6, raise the temperature to 120°C, control the pressure of the kettle to 0.06MPa, open the inlet valve of the tower ethylenediamine vaporization liquid and control it through the flowmeter 10 The flow rate is 150Kg / h; observe the ethylenediamine reflux in the gas-liquid separator 5, and open the reflux valve of the reactor 3; slowly raise the temperature of the reactor 3 to 150°C; control the top temperature to 121°C, and the bottom temperature to 150°C;
[0040] 2. Premix: Pump ethylenediamine and 400Kg chloropropyltrimethoxysilane into the premix kettle 1 respectively by the pump, and the mixed solution enters the reaction tower 2 from the overflow port 9, and the ethylenediamine and chloropropyltrimethoxysilane The pumping rates of trimethoxysilane are 45Kg / h and 100Kg / h respectively;
[0041] 3. Continuous discharge at the bottom of the tank: Observ...
Embodiment 2
[0045] 1. Ethylenediamine vaporization: pump the raw material ethylenediamine into the ethylenediamine vaporization kettle 6, raise the temperature to 120°C, control the pressure of the kettle to 0.07MPa, open the inlet valve of the tower ethylenediamine vaporization liquid and control it through the flowmeter 10 The flow rate is 145Kg / h; observe the ethylenediamine reflux in the gas-liquid separator 5, open the reflux valve of the reactor 3; slowly raise the temperature of the reactor 3 to 150°C; control the top temperature to 120~122°C, and the bottom temperature to 150~152°C ;
[0046] 2. Premix: Pump ethylenediamine and 400Kg chloropropyltrimethoxysilane into the premix kettle 1 respectively by the pump, and the mixed solution enters the reaction tower 2 from the overflow port 9, and the ethylenediamine and chloropropyltrimethoxysilane The pumping rates of trimethoxysilane were 48Kg / h and 100Kg / h respectively;
[0047] 3. Continuous discharge at the bottom of the tank: Ob...
Embodiment 3
[0051] 1. Vaporization of ethylenediamine: pump the raw material ethylenediamine into the ethylenediamine vaporization kettle 6, raise the temperature to 120°C, control the pressure of the kettle to 0.08MPa, open the inlet valve of the tower ethylenediamine vaporization liquid and control it through the flowmeter 10 The flow rate is 155Kg / h; observe the ethylenediamine reflux in the gas-liquid separator 5, open the reflux valve of the reactor 3; slowly raise the temperature of the reactor 3 to 150°C; control the top temperature to 122~123°C, and the bottom temperature to 152~153°C ;
[0052] 2. Premix: Pump ethylenediamine and 400Kg chloropropyltrimethoxysilane into the premix kettle 1 respectively by the pump, and the mixed solution enters the reaction tower 2 from the overflow port 9, and the ethylenediamine and chloropropyltrimethoxysilane The pumping rates of trimethoxysilane are 42Kg / h and 100Kg / h respectively;
[0053] 3. Continuous discharge at the bottom of the tank: ...
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