EP 0837725 A1 19980429 - PROCESS FOR EXTRACTING PURE SUBSTANCES FROM MIXTURES OF HIGH-BOILING AIR AND/OR TEMPERATURE-SENSITIVE SUBSTANCES REQUIRING HIGH SEPARATIVE POWER BY RECTIFICATION IN A FINE VACUUM AND COLUMNS SUITABLE FOR THIS PROCESS
Title (en)
PROCESS FOR EXTRACTING PURE SUBSTANCES FROM MIXTURES OF HIGH-BOILING AIR AND/OR TEMPERATURE-SENSITIVE SUBSTANCES REQUIRING HIGH SEPARATIVE POWER BY RECTIFICATION IN A FINE VACUUM AND COLUMNS SUITABLE FOR THIS PROCESS
Title (de)
VERFAHREN ZUR GEWINNUNG REINER SUBSTANZEN AUS GEMISCHEN HOCHSIEDENDER LUFT- UND/ODER TEMPERATUREMPFINDLICHER SUBSTANZEN, DIE EINE HOHE TRENNLEISTUNG ERFORDERN, DURCH REKTIFIKATION IM FEINVAKUUM SOWIE FÜR DIESES VERFAHREN GEEIGNETE KOLONNEN
Title (fr)
PROCEDE DE RECTIFICATION SOUS VIDE POUSSE POUR EXTRAIRE DES SUBSTANCES PURES CONTENUES DANS DES MELANGES DE SUBSTANCES A POINT D'EBULLITION ELEVE ET A FORTE SENSIBILITE A LA TEMPERATURE ET A L'AIR, QUI EXIGENT UN FORT POURVOIR DE SEPARATION, ET COLONNES ADAPTEES A CE PROCEDE
Publication
Application
Priority
- DE 19524928 A 19950708
- EP 9602852 W 19960629
Abstract (en)
[origin: DE19524928A1] The invention concerns a process for extracting pure substances from mixtures of high-boiling air and/or temperature-sensitive substances which require a high separative power by rectification in a fine vacuum in columns containing metal cloth packing with an ordered structure and using channel liquid separators with 500 or more draining points/m<2>. The draining points are arranged at an angle of 90 DEG to the cloth layers of the packing elements (7, 8) located immediately below the distributors. Two or a plurality of the packing elements (7, 8) below the liquid separator (6) have only a slight height which practically ensures the exclusion of air. These packing elements are shaped such that, during rectification, no heat can be exchanged through the column wall. The invention also concerns the packing columns used for this process and the use of this process and this column for the distillative fine-purification of vitamin E acetate.
IPC 1-7
IPC 8 full level
B01D 3/00 (2006.01); B01D 3/10 (2006.01); B01D 3/14 (2006.01); B01D 3/16 (2006.01); B01D 3/26 (2006.01); B01D 3/32 (2006.01); B01J 19/32 (2006.01); C07C 17/38 (2006.01); C07D 311/72 (2006.01)
CPC (source: EP US)
B01D 3/008 (2013.01 - EP US); B01D 3/141 (2013.01 - EP US); B01D 3/146 (2013.01 - EP US); B01D 3/16 (2013.01 - EP US); B01J 19/32 (2013.01 - EP US); C07C 17/38 (2013.01 - EP US); C07D 311/72 (2013.01 - EP US); B01J 2219/3221 (2013.01 - EP US); B01J 2219/3222 (2013.01 - EP US); B01J 2219/32227 (2013.01 - EP US); B01J 2219/32272 (2013.01 - EP US); B01J 2219/32408 (2013.01 - EP US); B01J 2219/32416 (2013.01 - EP US); B01J 2219/326 (2013.01 - EP US); Y10S 159/42 (2013.01 - EP US); Y10S 261/72 (2013.01 - EP US)
Citation (search report)
See references of WO 9702880A1
Designated contracting state (EPC)
CH DE ES FR GB LI NL
DOCDB simple family (publication)
DE 19524928 A1 19970109; CN 1048910 C 20000202; CN 1190354 A 19980812; DE 59611228 D1 20050616; EP 0837725 A1 19980429; EP 1209156 A2 20020529; EP 1209156 A3 20021030; EP 1209156 B1 20050511; ES 2240322 T3 20051016; JP H11508818 A 19990803; US 6111117 A 20000829; US 6554965 B1 20030429; WO 9702880 A1 19970130
DOCDB simple family (application)
DE 19524928 A 19950708; CN 96195389 A 19960629; DE 59611228 T 19960629; EP 01130402 A 19960629; EP 9602852 W 19960629; EP 96924820 A 19960629; ES 01130402 T 19960629; JP 50546097 A 19960629; US 46684499 A 19991220; US 98149198 A 19980108