تفاعل #67625
ord-1a960dd9689148a5a1cefd13659246bf
معادلة التفاعل
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المذيبات
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المعالجة
- 1أخرىwas adjusted to 22° C.
- 2workup.ADDITIONwas added
- 3غسيلThe pump and lines were rinsed forward with acetonitrile (22.5 kg, 0.9 parts)
- 4أخرىwere adjusted to a temperature of 19-22° C
- 5غسيلThe metering pump and lines were rinsed forward with acetonitrile (12.5 kg, 0.5 parts)
- 6أخرىat 25° C.
- 7أخرى(22-28° C.)
- 8workup.ADDITIONafter the addition of about ⅓ of the POCl3
- 9workup.ADDITIONAt the end of the addition, it
- 10workup.ADDITIONAfter complete addition
- 11أخرىreaction completion
- 12درجة الحرارةThe solution was cooled to 15° C. (12-18° C.)
- 13workup.ADDITIONwas charged slowly
- 14أخرىreaction temperature of between 12 and 30° C
- 15أخرىwas then adjusted to 22° C.
- 16أخرى(19-25° C.)
- 17workup.STIRRINGagitated for ca. 5 hrs
- 18ترشيحthe contents of the reactor were filtered onto a pressure nutsche
- 19أخرىfitted with a filter cloth
- 20غسيلThe reactor, pump, and lines were washed forward onto the pressure nutsche with two portions of drinking water (62.5 kg, 2.5 parts each)
- 21تجفيفThe product (41.8 kg) was dried under vacuum with a maximum temperature of water bath
- 22درجة الحرارة(to heat dryer jacket) of 50° C
- 23workup.WAITAfter ca. 12 hrs
الإجراء التجريبي
5-Methoxy-2-nitrobenzoic acid (A) (25.0 kg, 1.0 eq.), 2-amino-5-chloropyridine (B) (16.3 kg, 1.0 eq.), and acetonitrile (87.5 kg, 3.5 parts) were charged to a 380 L GLMS reactor. The reaction mixture was adjusted to 22° C. (19-25° C.) and anhydrous pyridine (30.0 kg, 3.0 eq.) was added. The pump and lines were rinsed forward with acetonitrile (22.5 kg, 0.9 parts), and the reactor contents were adjusted to a temperature of 19-22° C. Phosphorous oxychloride (23.3 kg, 1.20 eq.) was charged to the contents of the reactor via a metering pump, while maintaining a temperature of 25° C. (22-28° C.). The metering pump and lines were rinsed forward with acetonitrile (12.5 kg, 0.5 parts), while keeping the temperature at 25° C. (22-28° C.). The reaction mixture normally turned from a slurry to a clear solution after the addition of about ⅓ of the POCl3. At the end of the addition, it became turbid. After complete addition, the reaction mixture was agitated at 25° C. (22-28° C.) for ca. 1 hr, at which time HPLC analysis confirmed reaction completion. The solution was cooled to 15° C. (12-18° C.) and drinking water (156.3 kg, 6.25 parts) was charged slowly while keeping reaction temperature of between 12 and 30° C. The reaction mixture was then adjusted to 22° C. (19-25° C.) and agitated for ca. 5 hrs until exotherm ceased. Formation of a slurry was visually confirmed and the contents of the reactor were filtered onto a pressure nutsche fitted with a filter cloth. The reactor, pump, and lines were washed forward onto the pressure nutsche with two portions of drinking water (62.5 kg, 2.5 parts each). The filtrate had a pH value of 7. The product (41.8 kg) was dried under vacuum with a maximum temperature of water bath (to heat dryer jacket) of 50° C. After ca. 12 hrs, in-process LOD analysis indicated a solvent content of 0.72%. The dry product (C) was discharged (34.4 kg) with 88.2% yield and 99.1% purity by HPLC.