Method for preparing m-xylylenediamine
A technology of m-xylylenediamine and isophthalonitrile, which is applied in the field of m-xylylenediamine preparation, can solve the problems of unspecified main composition of impurities, equipment manufacturing, high material requirements, and unsatisfactory XDA yield, etc. , to achieve the effect of compact equipment, scientific process and mild operating conditions
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[0031] Catalyst preparation
[0032] Catalyst One
[0033] Weigh 101g of hydrated cobalt chloride, 28g of hydrated nickel chloride, 11g of hydrated titanium chloride, 20mg of hydrated rhodium chloride, 3.6g of hydrated manganese chloride, and 2.7g of hydrated chromium chloride to prepare a solution. On 100g diatomaceous earth, after drying under infrared light, layering is formed and dried for later use.
[0034] Catalyst two
[0035] Weigh 101g of hydrated cobalt chloride, 28g of hydrated nickel chloride, 11g of hydrated titanium chloride, 20mg of hydrated rhodium chloride, 4.0g of potassium molybdate to prepare a solution, and immerse it on 100g of diatomaceous earth using the dipping method. After drying under the lamp, the strips are formed and dried for later use.
Example Embodiment
[0036] Example 1
[0037] The hydrogenation reactor is a stainless steel tubular reactor with a diameter of 25mm×1500mm. The reaction tube is filled with 80ml of catalyst one with a particle size of 0.6-1mm, and the bottom of the reaction tube is filled with inert quartz sand. The catalyst was reduced by a mixture of hydrogen and nitrogen (volume ratio 1:10) under normal pressure at 600°C for 3 hours before use.
[0038] The mixture of isophthalonitrile (500g) and N-methylpyrrolidone (NMP) (2760ml) (isophthalonitrile content is 15%) is fed into the reactor from the top at a set speed, liquid ammonia (The flow rate is 47.5ml / min) and hydrogen (41.2 standard liters / H) are supplied from the other two pipelines. The raw materials are mixed with hydrogen and liquid ammonia and enter the bed containing the catalyst for hydrogenation reaction. The reaction temperature is 75°C, the reaction pressure is 8Mpa, the addition amount of isophthalonitrile is 9g / h, the liquid ammonia flow rate i...
Example Embodiment
[0039] Example 2
[0040] According to the equipment and catalyst used in Example 1, isophthalonitrile (500 g) was dissolved in 2650 ml of N-methylpyrrolidone (NMP), and the hydrogenation reaction was carried out on the fixed bed and the hydrogenation reaction was carried out on the fixed bed. The reaction temperature is 85°C, the reaction pressure is 8Mpa, the addition amount of isophthalonitrile is maintained at 13g / h, and the hydrogen flow rate is controlled to 41.2 standard liters / H under the condition of no ammonia. The reaction solution was collected and analyzed, and the results are shown in Table 1.
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