Continuous process for preparing menthol in pure or enriched form

Abstract

The present invention relates to a continuous process for preparing racemic or optically active menthol in pure or enriched form by distillatively separating menthol from substance mixtures which comprise essentially menthol and diastereomers thereof. This distillative separation is performed in a dividing wall column with 50 to 300 theoretical plates and one or more side draw points at an absolute operating pressure of 5 to 500 mbar.

1 - 17 . (canceled) 
     
     
         18 . A continuous process for preparing racemic or optically active menthol of the formula (I) 
       
         
           
           
               
               
           
         
       
       in pure or enriched form by distillatively separating racemic or optically active menthol from substance mixtures comprising racemic or optically active menthol and diastereomers of menthol, wherein the distillative separation is performed in a dividing wall column with 50 to 300 theoretical plates and one or more side draw points at an absolute operating pressure of 5 to 500 mbar. 
     
     
         19 . The process according to  claim 18 , for preparing racemic or optically active menthol in pure or enriched form by distillatively separating racemic or optically active menthol from substance mixtures comprising racemic or optically active menthol and diastereomers of menthol, and also isopulegol of the formula (II) 
       
         
           
           
               
               
           
         
       
       and/or diastereomers thereof, with or without menthones of the formula (III) and/or (IV) 
       
         
           
           
               
               
           
         
       
     
     
         20 . The process according to  claim 18 , for preparing L-menthol in pure or enriched form by distillatively separating L-menthol from substance mixtures comprising L-menthol and diastereomers of menthol. 
     
     
         21 . The process according to  claim 18 , wherein a substance mixture with a menthol content based on the overall mixture of 85 to 99.9% by weight is used. 
     
     
         22 . The process according to  claim 18 , wherein menthol is obtained with a content of 99.5 to 99.95% by weight. 
     
     
         23 . The process according to  claim 18 , wherein the menthol obtained in pure or enriched form has a content of isopulegol and diasteromers thereof of up to 0.5% by weight in total. 
     
     
         24 . The process according to  claim 18 , wherein the resulting menthol in pure or enriched form has a menthone and/or isomenthone content of up to 0.5% by weight in total. 
     
     
         25 . The process according to  claim 18 , wherein the distillative separation in the dividing wall column is performed at an absolute operating pressure of 20 to 100 mbar. 
     
     
         26 . The process according to  claim 18 , wherein the distillative separation is performed in a dividing wall column with 100 to 180 theoretical plates. 
     
     
         27 . The process according to  claim 18 , wherein the dividing wall column is operated at an absolute top pressure of 10 to 60 mbar and at an absolute bottom pressure of 30 to 100 mbar. 
     
     
         28 . The process according to  claim 18 , wherein the dividing wall column used is a packed column with structured sheet metal or fabric packings with a specific surface area of about 100 to 750 m 2 /m 3 . 
     
     
         29 . The process according to  claim 18 , wherein a dividing wall column (TK) is used, which has a dividing wall (T) in the longitudinal direction of the column to form an upper combined column region, a lower combined column region, a feed section with a rectifying section and stripping section, and a withdrawal section with a stripping section and rectifying section. 
     
     
         30 . The process according to  claim 18 , wherein the menthol-comprising substance mixture (a) which serves as a feedstock is fed into the middle region of the feed section, the menthol in pure or enriched form is obtained as a liquid or gaseous side draw from the middle region of the withdrawal section, and one or more low boiler fractions are removed from the upper combined column region, and one or more high boiler fractions from the lower combined column region. 
     
     
         31 . The process according to  claim 18 , wherein the dividing wall column is equipped with a falling film evaporator, and a high boiler fraction in liquid form is discharged downstream of the falling film evaporator. 
     
     
         32 . The process according to  claim 18 , wherein the heat carrier medium used to cool the condenser and/or the postcondenser of the dividing wall column has a temperature controllable within a temperature range from 0 to 60° C. 
     
     
         33 . The process according to  claim 18 , wherein all product-conducting lines, vessels and apparatuses connected to the dividing wall column, and all apparatuses and lines of the vacuum system, are thermally insulated and equipped with a temperature-controllable trace heating system. 
     
     
         34 . A system for continuously preparing racemic or optically active menthol in pure or enriched form according to  claim 18 , comprising a dividing wall column (TK) with 50 to 300 theoretical plates and one or more side draw points, which has a dividing wall (T) in the longitudinal direction of the column to form an upper combined column region, a lower combined column region, a feed section with a rectifying section and stripping section, and a withdrawal section with a stripping section and rectifying section, wherein all product-conducting constituents of the system. 
     
     
         35 . The system according to  claim 35 , wherein all apparatuses and lines of the vacuum system are thermally insulated with suitable materials and provided with trace heating.