Synthesis device for 6-carbonyl-8-chloroethylcaprylate and method for synthesizing 6-carbonyl-8-chloroethylcaprylate by using device
A technology for ethyl chlorooctanoate and a synthesis device, which is applied in chemical instruments and methods, preparation of carboxylic acid esters, preparation of organic compounds, etc., can solve problems such as non-conformance, unstable product quality, low production efficiency, etc. rate effect
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Embodiment 1
[0027] use figure 1 The steps of the method for the synthetic 6-carbonyl-8-chlorooctanoic acid ethyl ester synthetic device of shown 6-carbonyl-8-chlorooctanoic acid ethyl ester are as follows:
[0028] A) To prepare the complexing solution, first pass ethyl 6-chloro-6-oxohexanoate and ethylene dichloride as the reaction raw materials through their respective pipelines, that is, pass through the 6-chloro-6-oxo with valve The ethyl hexanoate delivery pipeline and the dichloroethane delivery pipeline that is also equipped with a valve are fed from the complexing solution preparation tank 11 in the upper part of the complexing solution preparation tank 11 of the structural system of the complexing solution supply mechanism 1. Introduce in the complexing liquid preparation still 11, by figure 1 As shown, the aforementioned complexing solution preparation kettle 11 has two sets of identical structures, so as to fully ensure the uninterrupted delivery of 6-chloro-6-oxoethyl hexanoa...
Embodiment 2
[0032] Only change the mol ratio of 6-chloro-6-oxohexanoic acid ethyl ester, anhydrous aluminum chloride and ethylene dichloride described in step A) into 1: 1.6: 10, the flow rate of complexing liquid Change 11000L / min into 11000L / min, change the pressure of damping buffer 14 into 0.7MPa; Only change the pressure of the ethylene gas in step B) into 0.8MPa, change the pressure of damping buffer 14 into 0.6MPa, the pressure ratio of ethylene gas The pressure of the damping buffer 14 is 0.2MPa larger, and the flow rate of the ethylene gas is changed to 14L / min; only the temperature of the jacket water bath of the static mixer 32 in the step C) is changed to 65°C, and the material in the static mixer 32 Change the residence time to 60s, change the temperature of the reaction material to be synthesized after the heat exchange in the heat exchanger 33 to 25°C, change the hydrolysis temperature of the hydrolysis kettle 34 to 10°C, and change the 6-carbonyl-8-chlorooctanoic acid ethyl...
Embodiment 3
[0034] Only change the mol ratio of 6-chloro-6-oxohexanoic acid ethyl ester, anhydrous aluminum chloride and ethylene dichloride described in step A) into 1: 2.5: 8, the flow rate of complexing liquid Change 10000L / min into 10000L / min, change the pressure of damping buffer 14 into 0.3MPa; Only change the pressure of the ethylene gas in step B) into 0.9MPa, change the pressure of damping buffer 14 into 0.65MPa, the pressure ratio of ethylene gas The pressure of the damping buffer 14 is 0.25MPa larger, and the flow rate of the ethylene gas is changed to 18L / min; only the jacket water bath temperature of the static mixer 32 in the step C) is changed to 78°C, and the material in the static mixer 32 Change the residence time to 15s, change the temperature of the reaction material to be synthesized after the heat exchange in the heat exchanger 33 to 10°C, change the hydrolysis temperature of the hydrolysis kettle 34 to 25°C, and the gas phase of 6-carbonyl-8-chlorooctanoic acid ethyl...
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