Method for preparing n-phenylglycinonitrile
A technology of anilinoacetonitrile and hydroxyacetonitrile, which is applied to the preparation of carboxylic acid nitriles, the preparation of organic compounds, chemical instruments and methods, etc., can solve the problems of low product yield, cumbersome operation, and large equipment investment, and improve the reaction rate. The effect of improving material conversion rate, improving reaction efficiency and ensuring continuity
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Embodiment 1
[0032] The hydroxyacetonitrile solution and the aniline solution described in Table 1 are preheated and mixed respectively through a delivery pump, a flow meter to a pipeline preheater and a pipeline mixer, wherein the flow control and preheating of the hydroxyacetonitrile solution and the aniline solution Temperature and pressure, mixing temperature and pressure are shown in Table 2; The material that pipeline mixer comes out enters two groups of series-connected (each group of pipeline reactors are made up of two pipeline reactors in series) pipeline reactors continuously, At the inlet of the first group of pipeline reactors, add an aqueous sodium bicarbonate solution of auxiliary agent A with a mass percentage of about 25%. The amount of the aqueous sodium bicarbonate solution added is 4% of the amount of hydroxyacetonitrile in terms of mass percentage, and the flow rate is controlled at 120l / h so that the pH value of the reaction material is controlled at 4 to 6; the materi...
Embodiment 2
[0034] Wherein the parameter of each raw material used is shown in Table 1; Every process parameter is shown in Table 2 and Table 3; Auxiliary agent A is the sodium carbonate aqueous solution of about 30% by mass percentage, and its add-on is counted as 2% of the hydroxyacetonitrile consumption by mass percentage , and continuously and evenly join in the pipeline reactor, so that the pH value of the reaction material is controlled at 5~7, all the other steps are with embodiment 1; In the present embodiment, 38620kg of anilinoacetonitrile was obtained in 24 hours, and the purity of gained anilinoacetonitrile was 96.1%, the yield is 99.9%
Embodiment 3
[0036] Wherein the parameter of each raw material used is shown in Table 1; Every process parameter is shown in Table 2 and Table 3; Auxiliary A is the potassium bicarbonate aqueous solution that mass percent is about 20%, and its addition is counted as 0.5% of the hydroxyacetonitrile consumption in mass percent %, flow control at 10l / h, so that the pH value of the reaction material is controlled at 4~7, and all the other steps are with embodiment 1; In the present embodiment, 13336kg of anilinoacetonitrile was obtained in 24 hours, and the gained anilinoacetonitrile purity was 95.7%. The rate is 99.8%.
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