Reacción #432018

ord-54783a2941b94eb69576a257e6083c2a

Disolventes

Condiciones de reacción

Temperatura
100°CELSIUS
Condiciones detalladas
See reaction.notes.procedure_details.

Tratamiento posterior

  1. 1
    Otroequipped with an overhead azeotropic mixture condenser
  2. 2
    OtroA fixed bed of Amberlyst 15 acid-type ion exchange resin catalyst was provided
  3. 3
    Otrowas circulated by a pump from the flask through the catalyst bed and back to the flask at a rate of about 2 milliliters per minute for a time period of 4 hours
  4. 4
    Otrowithdrawn from the flask and condensed
  5. 5
    OtroThe water component of the condensed azeotropic mixture was separated from the hexane component
  6. 6
    Otrowithdrawn

Procedimiento

162.2 grams of a 37% by weight aqueous solution of formaldehyde (equivalent to 2 moles), 404 grams of n-dodecyl mercaptan (equivalent to 2 moles) and 250 milliliters of hexane were placed in a one liter flask equipped with an overhead azeotropic mixture condenser and a condensed water and hexane component separator. A fixed bed of Amberlyst 15 acid-type ion exchange resin catalyst was provided, and the reaction mixture in the flask was circulated by a pump from the flask through the catalyst bed and back to the flask at a rate of about 2 milliliters per minute for a time period of 4 hours. While the reaction mixture was being circulated through the catalyst bed, it was heated to a temperature of approximately 100° C. whereby the azeotropic mixture formed by the hexane and water in the flask was vaporized, withdrawn from the flask and condensed. The water component of the condensed azeotropic mixture was separated from the hexane component and withdrawn, and the hexane was returned to the reaction flask. A 91.8% yield of dodecyl hydroxymethyl sulfide was realized after the hexane was removed by vacuum evaporation.

Fuente

DOI: 10.6084/m9.figshare.5104873.v1Patente: US05053549uspto-grants-1991_10