A kind of method of synthesizing 4-thiamphenicol toluene
A technology of thiamphenicol toluene and toluene, which is applied in the field of synthesizing 4-thiamphenicol toluene, can solve the problems of expensive raw materials and catalysts, expensive catalysts, poor selectivity, etc., and achieve process automation, high selectivity reaction, and material volume little effect
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Embodiment 1
[0017] The technical scheme of the present invention is illustrated below by specific examples, but protection scope of the present invention is not limited thereto:
[0018] Example 1
[0019] 2.9 Kg (20 mol) of phosphorus pentoxide and 87.1 Kg (500 mol) of methanesulfonic anhydride are mixed and stored in the first storage tank, and 9.2 Kg (100 mol) of toluene is stored in the second storage tank to adjust the tubular reaction The back pressure regulator at the end of the device is adjusted to 0.1 Mpa, and the two materials are simultaneously fed through the corresponding infusion pumps, and the flow rates are adjusted to 50.0 L / h and 8.9 L / h respectively through the infusion pumps. At this time, toluene, methanesulfonic acid, and pentoxide The molar flow ratio of diphosphorus is 1: 5: 0.2. The material enters the tubular reactor (tube length 5 m, tube diameter 50 mm) through the mixer, the reaction temperature is 70 °C, and the residence time is 10 min. After the reaction,...
Embodiment 2
[0021] Store 7.1 Kg (50 mol) of phosphorus pentoxide and 19.2 Kg (200 mol) of methanesulfonic acid in the first storage tank, store 9.2 Kg (100 mol) of toluene in the second storage tank, adjust the back pressure to 1.0 Mpa, the two materials are simultaneously fed through corresponding infusion pumps, and the flow rates are adjusted to 11 L / h and 6.6 L / h respectively through the infusion pumps. At this time, the molar flow ratios of toluene, methanesulfonic acid, and phosphorus pentoxide The ratio is 1 : 2 : 0.5. The material enters the tubular reactor (100m in length and 30mm in diameter) through the mixer, the reaction temperature is 130°C, and the residence time is 4 hours. The reaction solution flows directly into water (about 2 Kg), filtered, and washed with water to obtain 14.3 Kg 4-thiamphenicol toluene, the yield is 84%, and the para-selectivity is 87%.
Embodiment 3
[0023] Store 14.2 Kg (100 mol) of phosphorus pentoxide and 9.6 Kg (100 mol) of methanesulfonyl chloride in the first storage tank, store 9.2 Kg (100 mol) of toluene in the second storage tank, and adjust the back pressure adjustment to 5.0 Mpa, the two materials are simultaneously fed through corresponding infusion pumps, and the flow rates are adjusted to 0.7 L / h and 0.5 L / h respectively through the infusion pumps. At this time, the molar flow ratios of toluene, methanesulfonic acid, and phosphorus pentoxide 1:1:1. The material enters the tubular reactor (30 m in length and 5 mm in diameter) after passing through the mixer. The reaction temperature is 170°C and the residence time is 30 min. The reaction liquid is directly flowed into water (about 2Kg), filtered and washed with water. 15.3 Kg of 4-thiamphenicol toluene was obtained with a yield of 90% and a para-selectivity of 92%.
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