Réaction #1552130
ord-6eda47499b08493fb626314a9da56374
Équation de réaction
Réactifs
Réactifs
Conditions de réaction
Traitement
- 1AutreTo a reactor equipped with overhead agitation, jacket temperature control, a nitrogen inlet
- 2AutreAt 60-70° C., a dark colored solution was obtained
- 3AutreAfter reaction completion (<1.0% starting material by HPLC peak area)
- 4Températurethe stirred reactor contents were cooled to 30-35° C
- 5AutreTo a second reactor vented to a caustic scrubber
- 6workup.ADDITIONwas charged
- 7Autrepurified water (1.60 L) and silica gel (0.160 kg)
- 8AutreThe Friedel-Crafts reaction mixture
- 9Températureto maintain the stirred contents of the second reactor at <60° C
- 10FiltrationThe silica gel was filtered on a medium
- 11Filtrationto coarse filter element at 55-60° C.
- 12Lavagethe filtered solids were subsequently washed with purified water (800 mL)
- 13Autrepreheated to 50-60° C
- 14LavageThe combined mother and wash liquor filtrates
- 15Températurewere cooled to 20-25° C. with vigorous agitation
- 16Autreto separate at 20-25° C. (Process volume
- 17AutreThree phases separated after 1-2 hours
- 18workup.WAITto stand without agitation for another 2-4 h
- 19Extractionremained in the reactor for back-extraction
- 20workup.ADDITIONThe reactor was charged with cyclohexane (1.10 kg)
- 21Autreto separate for 25-40 min
- 22workup.ADDITIONOtherwise, more 30% aqueous NaOH was added
- 23Extractionthis extraction
- 24LavageThe reactor was rinsed with purified water
- 25Autreto remove residual salts
- 26workup.STIRRINGThe reactor contents were stirred vigorously for 0.5 hours
- 27Autreto separate over 15-30 minutes
- 28workup.ADDITIONwas added
- 29Autrepurified water (2.40 kg)
- 30workup.STIRRINGThe reactor contents were stirred vigorously at 60-65° C. for 0.5 h
- 31Autreto separate at 60-65° C. over 1.5-2 h
- 32AutreWith a reactor jacket temperature of 55-60° C., solvent from the upper (organic) layer was removed by vacuum distillation at pressures
Mode opératoire
To a reactor equipped with overhead agitation, jacket temperature control, a nitrogen inlet, and a caustic scrubber vent were charged, in the specified order, 2-chloro-N-(4-chlorophenethyl)propan-1-amine hydrochloride (1.00 kg, 3.72 mol), aluminum chloride (0.745 kg, 5.58 mol), and 1,2-dichlorobenzene (2.88 kg). The stirred reactor contents were heated to 125-130° C., and stirring was continued at that temperature for 14-18 h. At 60-70° C., a dark colored solution was obtained. After reaction completion (<1.0% starting material by HPLC peak area) had been verified, the stirred reactor contents were cooled to 30-35° C. To a second reactor vented to a caustic scrubber was charged purified water (1.60 L) and silica gel (0.160 kg). The Friedel-Crafts reaction mixture was transferred from the first reactor to the second reactor sufficiently slowly to maintain the stirred contents of the second reactor at <60° C. After the transfer is completed, the next step may be executed without any hold period. The silica gel was filtered on a medium to coarse filter element at 55-60° C., and the filtered solids were subsequently washed with purified water (800 mL) preheated to 50-60° C. The combined mother and wash liquor filtrates were cooled to 20-25° C. with vigorous agitation. Then the stirring was stopped, and the phases were allowed to separate at 20-25° C. (Process volume peaked at this point at 5.68 L). Three phases separated after 1-2 hours of standing. The lowest layer was drained to waste disposal. This dark layer consisted mostly of 1,2-dichlorobenzene (1.64 kg, 1.33 L) at pH 3-4. About 1% of the product was lost to this layer. The remaining two phases were allowed to stand without agitation for another 2-4 h. The lower layer was drained and saved (Layer A). This light colored phase (2.64 kg, 2.00 L, pH 2-3) contained ˜90% 8-chloro-1-methyl-2,3,4,5-tetrahydro-1H-benzazepine. The upper layer (2.24 kg of a turbid water phase at pH 0-1) contains ˜1-4% 8-chloro-1-methyl-2,3,4,5-tetrahydro-1H-benzazepine and remained in the reactor for back-extraction. The reactor was charged with cyclohexane (1.10 kg) and then 30% aqueous NaOH (2.44 kg, 18.3 mol). The resulting mixture (5.60 L) was stirred vigorously for 30 min at room temperature. The stirring was stopped, and the phases were allowed to separate for 25-40 min. If the pH of the lower (aqueous) phase was ≧13, it was drained to waste disposal. Otherwise, more 30% aqueous NaOH was added, and this extraction was repeated. At pH 14, the aqueous phase contains <0.1% 8-chloro-1-methyl-2,3,4,5-tetrahydro-1H-benzazepine free base. The remaining upper (organic) phase from the reactor was drained and saved (Layer B). The reactor was rinsed with purified water and followed by a suitable organic solvent to remove residual salts. The lower, light-colored product phase (the middle of the original three phases, Layer A) and the upper phase (organic, Layer B) were returned to the reactor. To the stirred reactor contents was added 30% aqueous NaOH (1.60 kg, 12.0 mol). The reactor contents were stirred vigorously for 0.5 hours. The stirring was discontinued and the phases were allowed to separate over 15-30 minutes. The lower (aqueous) layer was drained to waste disposal. To the upper (organic) phase remaining in the reactor was added purified water (2.40 kg). The reactor contents were stirred vigorously at 60-65° C. for 0.5 h. The stirring was discontinued, and the phases were allowed to separate at 60-65° C. over 1.5-2 h. The lower (aqueous) layer was drained to waste disposal. With a reactor jacket temperature of 55-60° C., solvent from the upper (organic) layer was removed by vacuum distillation at pressures starting at 115-152 ton and falling to 40 ton. The crude product, 8-chloro-1-methyl-2,3,4,5-tetrahydro-1H-benzazepine as the free base, was obtained as a yellow to brown oil distillation residue.