تفاعل #50018

معادلة التفاعل

( 4 )

3-bromoacetyl-5-chloro-2-thiophenesulfonamide

(+)-β-chlorodiisopinocampheylborane

potassium

sodium hydroxide

→

( 5 )

(S)-3,4-dihydro-6-chloro-4-hydroxy-2H-thieno[3,2-e]-1,2-thiazine-1,1-dioxide

المذيبات

t-butyl methyl ether

t-butyl methyl ether

tetrahydrofuran

diethyl ether

ظروف التفاعل

المعالجة

1. 1
   أخرىat a temperature of -40° to 0° C.
2. 2
   أخرىfor 6 to 24 hours
3. 3
   أخرىA higher enantiomeric excess is obtained at the lower temperature
4. 4
   أخرىat a temperature of -25° to -15° C
5. 5
   أخرىThe product is isolated by phase separation, acidification of the aqueous phase, extraction, solvent removal, and trituration

الإجراء التجريبي

In the fourth step of the process, 3-bromoacetyl-5-chloro-2-thiophenesulfonamide (4) is reduced with an appropriate reagent to provide initially an (S)-bromohydrin, which upon subsequent treatment with aqueous sodium hydroxide cyclizes to (S)-3,4-dihydro-6-chloro-4-hydroxy-2H-thieno[3,2-e]-1,2-thiazine-1,1-dioxide (5). The preferred reducing agent is (+)-β-chlorodiisopinocampheylborane, which is well known to provide bromohydrins in high enantiomeric excess from prochiral α-bromo ketones [H. C. Brown, W. S. Park, B. T. Cho, and P. V. Ramachandran J. Org. Chem. 52, 5406 (1987) and H. C. Brown U.S. Pat. No. 4,918,246 (1990)]. Several different reaction solvents can be used for the reduction of (4), including diethyl ether, tetrahydrofuran, and t-butyl methyl ether. The reduction is typically carried out using 1.2 to 2.2 equivalents of (+)-β-chlorodiisopinocampheylborane at a temperature of -40° to 0° C. for 6 to 24 hours. A higher enantiomeric excess is obtained at the lower temperature; however, the reaction rate is slower. The preferred conditions utilize t-butyl methyl ether at a temperature of -25° to -15° C. After the reduction is complete, aqueous potassium or sodium hydroxide is added and the mixture is stirred at ambient temperature for a period of 1 to 5 hours to accomplish cyclization. The product is isolated by phase separation, acidification of the aqueous phase, extraction, solvent removal, and trituration. The enantiomeric excess of the (5) produced is typically greater than 96%.

المصدر