Method for continuous production of 5'-nucleotide by using micro-channel reaction device
A technology of microchannel reaction and nucleotide, which is applied in the field of chemical synthesis and technology, can solve the problems of large amount of phosphorus oxyhalide, long production cycle, and environmental pollution, and achieve short reaction time, simple operation, and high conversion rate. Effect
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Embodiment 1
[0036] The uridine trimethyl phosphate solution (first raw material storage tank) and phosphorus oxychloride (second raw material storage tank) with a mass ratio of uridine and trimethyl phosphate of 1:5 are 1:4 (volume The flow rate ratio is 3:1) respectively into the first microstructure mixer and into the first microstructure reactor, and stay in the microstructure reactor at normal temperature and pressure for 25 minutes for reaction. At the same time, ice water (the third raw material storage tank) is injected into the second microstructure reactor respectively through another constant flow pump and the effluent of the first microstructure reactor, wherein the mol ratio of the effluent to ice water is 1:6 (volume flow rate ratio is 1:1), and stay in the second microstructure reactor for 10 minutes at 5°C under normal pressure for reaction, and the second microstructure reactor injects the feed liquid into the product through a long polytetrafluorocapillary tube Storage ta...
Embodiment 2
[0038] Uridine and trimethyl phosphate mass ratio of 1:5 uridine trimethyl phosphate solution (the first raw material storage tank) and phosphorus oxychloride (second raw material storage tank) according to the molar ratio of 1:3 (flow rate The ratio is 4:1) into the first microstructure mixer and into the first microstructure reactor, and stay in the microstructure reactor at normal temperature and pressure for 40 minutes to react. At the same time, ice water (the third raw material storage tank) is injected into the second microstructure reactor respectively through another constant flow pump and the effluent of the first microstructure reactor, wherein the mol ratio of the effluent to ice water is 1:6 (flow rate ratio is 1:1), and stay in the second microstructure reactor at 5°C under normal pressure for 10min to react, the second microstructure reactor injects the feed liquid into the product through a long polytetrafluorocapillary tube Storage tanks, product storage tanks...
Embodiment 3
[0040] Uridine trimethyl phosphate solution (the first raw material storage tank) and phosphorus oxychloride (second raw material storage tank) with a mass ratio of uridine to trimethyl phosphate of 1:5 are 1:5 in molar ratio (flow rate The ratio is 2.5:1) respectively injected into the first microstructure mixer and into the first microstructure reactor, and stayed in the microstructure reactor at normal temperature and pressure for 20 minutes for reaction. At the same time, ice water (the third raw material storage tank) is injected into the second microstructure reactor respectively through another constant flow pump and the effluent of the first microstructure reactor, wherein the mol ratio of the effluent to ice water is 1:6 (the flow rate ratio is 1:1), and stay in the second microstructure reactor at 5°C under normal pressure for 10min to react. The second microstructure reactor injects the feed liquid into the product storage through a long polytetrafluorocapillary tube...
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