Preparation method of dapagliflozin intermediate
A technology for intermediates and solutions, which is applied in the field of synthesizing dapagliflozin intermediates using microreactors, can solve the problems of low production efficiency and waste of raw materials, and achieve the effects of reducing the generation of by-products, low recovery efficiency, and shortened time
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Embodiment 1
[0032] Embodiment 1: Determine the influence of the flow rate of n-butyllithium on the valve of microreactor equipment and its pipeline
[0033] The n-butyllithium solution is its hexane solution with a concentration of 1.6mol / L. During the test, the n-butyllithium solution is directly passed into it through a filter head. The whole operation of n-butyllithium needs to be free of oxygen and water. , operating under nitrogen protection, considering that the pump head and one-way valve of the microreactor are very prone to blockage, so the flow rate of different butyllithium is set to be consistent with the actual measurement, and the n-butyllithium is weighed at different time points by recording video Record the weight at different time points, whether the weight decreased at a uniform speed is consistent, and measure a reasonable butyllithium flow rate.
[0034] Table 1 Effect of the flow rate of n-butyllithium on the valves and pipelines of microreactor equipment
[0035] ...
Embodiment 2
[0038] Example 2: Effect of different flow rates on reaction progress.
[0039] A method for synthesizing compound 2 using a microreactor. According to the flow rate of n-butyl lithium should not be less than 20mL / min, the equivalent ratio of compound 1 and n-butyl lithium is 1:1.1; the influence of different flow rates on the reaction process is designed and optimized. Reaction flow rate.
[0040]
[0041] A component: C 化合物1 =0.8moL / L (preparation method: weigh 30g of compound 1 and dissolve in 116mL of tetrahydrofuran, dissolve and clear for later use);
[0042] B component: C 正丁基锂 =1.6moL / L (commercially available), PTFE pipe;
[0043] First examine the influence of the flow rate of components A and B on the reaction process:
[0044] Set the flow rate of component B to 20.0ml / min, 23.5ml / min, and 27.2ml / min in sequence, and the test results are shown in the table below.
[0045] Table 2 The impact of different flow rates on the reaction process
[0046]
[0047]...
Embodiment 3
[0048] Embodiment 3: investigate the influence of different precooling temperatures on the reaction.
[0049] A component: C 化合物1 =0.8moL / L, V A =49.5mL / min
[0050] B component: C 正丁基锂 =1.6moL / L, V B =27.2mL / min
[0051]
[0052] Results: The length of the reaction unit of the microreactor pipeline is 13cm, and the residence time of the reaction unit is controlled to be 18s, so the pre-cooling temperature is determined to be -20°C. From the analysis of the table data, the lower the pre-cooling temperature, the slower the reaction process, the lower the content of the main product, and the more residual raw materials; the lower the temperature, the lower the temperature of the intermediates that may exist in other unknown peaks, the slower the process of conversion into products, Therefore, from the perspective of data analysis, the pre-cooling temperature of -20°C increases the product significantly, and other unknown peaks decrease significantly. At the same time, -2...
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