Synthesis proces sof N-methyl morpholine
A technology of methyl morpholine and a synthesis method is applied in the field of synthesis of organic compounds, can solve problems such as being not very suitable, and achieve the effects of easy operation, good equipment continuity and mild reaction conditions
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Embodiment 1
[0022] Embodiment 1, a kind of synthetic method of N-methylmorpholine, carries out following steps successively:
[0023] 1), preparation of supported catalyst:
[0024] a), the commercially available γ-Al 2 o 3 With a concentration of 10% H 3 PO 4 The solution was treated and soaked at 40°C-60°C for 30 minutes, then filtered out and dried, then roasted at 450°C for 3.5 hours, and at 700°C for 5 hours before use.
[0025] b) Dissolving 79.0 g of cobalt nitrate and 26.4 g of solid nickel nitrate (excluding crystal water) in 50 mL of distilled water to prepare 50 mL of metal salt solution for later use. With the ratio of 1.2mL metal salt solution / 1.0gγ-Al2O3 carrier, the above treated γ-Al2O3 was immersed in the prepared solution for 36 hours; filtered to obtain the filtrate and catalyst.
[0026] c) Dry the catalyst obtained after the above-mentioned filtration at 60°C for 2 hours under stirring, put it into a muffle furnace and bake it at 80°C, 150°C, and 280°C for 3 hour...
Embodiment 2
[0032] Embodiment 2, a kind of synthetic method of N-methylmorpholine:
[0033] In step 2), the mol ratio of morpholine and methanol is changed to 1: 6, the reaction temperature is controlled at 140°C, the hydrogen pressure is adjusted so that the reactor pressure remains at 0.5Mpa, and the raw material is used at a space velocity of 0.3g / h / mL catalyst Enter the catalyst bed layer reaction. All the other are the same as in Example 1.
[0034] The gas chromatography analysis content of the obtained product is 95%, and the product yield after recycling a batch of raw materials is 97%.
Embodiment 3
[0035] Embodiment 3, a kind of synthetic method of N-methylmorpholine:
[0036] In step 2), the mol ratio of morpholine and methanol is changed to 1: 1, the reaction temperature is controlled at 200°C, the hydrogen pressure is adjusted so that the reactor pressure remains at 0.2Mpa, and the raw material is 0.1g / h / mL catalyst space velocity Enter the catalyst bed layer reaction. All the other are the same as in Example 1.
[0037] The gas chromatography analysis content of the obtained product is 95%, and the product yield after recycling a batch of raw materials is 90%.
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