StartseiteMCPWorkbenchSkills
StartseiteWorkbenchBenachrichtigungenMein Bereich
llms.txt · MCP-AnleitungDatenschutz · Nutzungsbedingungen · Supportv1.8.0
  1. Startseite
  2. /Reaktion

Hydrochloric Acid → 2-Propanone, 1-(2-nitrophenoxy)-

HRID 1373356
Notizen
Druckvorschau

Reaktionsgleichung

Reaktionsgleichung von HRID 1373356
[N+:1]([C:4]1[CH:9]=[CH:8][CH:7]=[CH:6][C:5]=1[OH:10])([O-:3])=[O:2].Cl[CH2:12][C:13](=[O:15])[CH3:14].[Br-].[Na+].C(=O)(O)[O-].[Na+].Cl>[Cl-].C([N+](CCCC)(CCCC)C)CCC.O.C1(C)C=CC=CC=1>[N+:1]([C:4]1[CH:9]=[CH:8][CH:7]=[CH:6][C:5]=1[O:10][CH2:12][C:13](=[O:15])[CH3:14])([O-:3])=[O:2]
KomponentenReaktionsbedingungenVersuchsvorschriftAufarbeitungQuellen und NachweiseNotizen zur Reaktion

Komponenten

9

Edukt 5

HCID 313Hydrochloric AcidHCID 6571Chloroacetone2×HCID 69472-NitrophenolHCID 253881Sodium BromideHCID 516892Sodium Bicarbonate

Produkt 1

HCID 792392-Propanone, 1-(2-nitrophenoxy)-Ausbeute 354.046,594 %

Reagenzien, Katalysatoren, Lösungsmittel

3
HCID 91822Tributylmethylammonium chlorideKatalysatorHCID 962WaterLösungsmittelHCID 1140TolueneLösungsmittel

Reaktionsbedingungen

Temperatur
65 °C

Versuchsvorschrift

The following materials are combined in a 1000 gallon vessel and heated at 65° C. for 6–8 hours: 499.0 kg (1.000 mole equiv.) of o-Nitrophenol (o-NP, 99%, 3.551 kg-moles), 359.7 kg (1.05 mole equiv.) of chloroacetone (CA, 96%, 3.733 kg-moles), 45.4 kg (0.124 mole equiv.) of sodium bromide (0.441 kg-moles), 328.9 kg (1.102 mole equiv.) of sodium bicarbonate (3.915 kg-moles), 27.2 kg (0.023 mole equiv.) of aqueous tributylmethylammonium chloride (TBMAC, 70%, 0.081 kg-moles), and 989 kg of toluene. The reaction is checked for completion and a trim charge of chloroacetone is added if necessary. Then 682 kg of water are added at 60° C. and the pH of the reaction mixture is adjusted to pH 6.5–7.0 at 55 to 60° C. (about 66 kg of 10% HCl). The phases are separated and the heavier aqueous phase is removed. A 5–15% NaCl solution (725 kg) is added to the organic phase, the mixture is agitated at 55 to 60° C. and the phases are separated again by decantation. The remaining organic phase of crude o-NPA is vacuum stripped at 65–75° C. to remove toluene and volatile impurities. Toluene (about 70 kg) is added towards the end of the vacuum strip and stripped off again to improve the removal of volatile impurities. About 691 kg of crude o-NPA (96.9% assay, 3.428 kg-moles, 96.5% yield rel. o-NP) are obtained. Finally 339 kg of a toluene/isopropanol (8:2) mixture is added at 55–65° C. to the crude o-NPA melt to obtain approximately a 65% o-NPA solution. This solution is transferred to a hold vessel where it is held at 65° C. for step b.

Aufarbeitung

  1. customThe following materials are combined in a 1000 gallon vessel
  2. additionis added if necessary
  3. customis adjusted to pH 6.5–7.0 at 55 to 60° C.
  4. customThe phases are separated
  5. customthe heavier aqueous phase is removed
  6. additionA 5–15% NaCl solution (725 kg) is added to the organic phase
  7. customthe phases are separated again by decantation
  8. customstripped at 65–75° C.
  9. customto remove toluene and volatile impurities
  10. additionToluene (about 70 kg) is added towards the end of the vacuum strip
  11. customthe removal of volatile impurities

Quellen und Nachweise

ORD-Eintrag
ord-1e30687621c04651a614bf6a26e7e30f
Quelldatensatz
uspto-grants-2007_01
DOI
10.6084/m9.figshare.5104873.v1
Patentnummer
US07161001B2

Notizen zur Reaktion

Wird geladen…

Auf dieser SeiteKomponentenReaktionsbedingungenVersuchsvorschriftAufarbeitungQuellen und NachweiseNotizen zur Reaktion