FIELD: rectification processes. SUBSTANCE: initial mixture is fed into column wherein countercurrent liquid-gas interaction takes place on contact grades for stripping low-boiling components. Liquid flowing down from lower part of column is heated in evaporator and ascending vapors are condensed in dephlegmator. Upper and lower rectification products are withdrawn. According to invention, initial mixture, prior to be fed into column, recycles between charging stock tank and dephlegmator functioning as cooling liquid. EFFECT: enhanced efficiency of process. 1 dwg
Title | Year | Author | Number |
---|---|---|---|
LIQUID RECTIFICATION METHOD | 1997 |
|
RU2133131C1 |
DEVICE FOR SEPARATION OF HYDROCARBON MIXTURES | 1996 |
|
RU2105591C1 |
METHOD OF SEPARATING MULTICOMPONENT LIQUID MIXTURE | 0 |
|
SU1456174A1 |
METHOD OF SEPARATING MULTI-COMPONENT MIXTURES AND COLUMN APPARATUS FOR DOING SAME | 1984 |
|
SU1202113A1 |
METHOD OF GAS DEHYDRATION | 1999 |
|
RU2155092C1 |
METHOD OF REMOVING WATER FROM PROCESS CIRCUIT IN CHEMICAL PRODUCTION | 2015 |
|
RU2606118C1 |
METHOD OF RECTIFICATION SEPARATION OF THREE-COMPONENT MIXTURE | 2003 |
|
RU2236278C2 |
METHOD FOR RECLAMATION OF ISOBUTYL ALCOHOL IN PRODUCTION OF HIGH-STRENGTH ARAMID FIBRES | 2013 |
|
RU2531993C1 |
METHOD FOR PRODUCTION OF PURE NIOBIUM PENTACHLORIDE AND DEVICE FOR ITS REALISATION | 2007 |
|
RU2381179C2 |
METHOD OF CONTINUOUS RECTIFICATION OF SOLUTIONS | 2000 |
|
RU2193438C2 |
Authors
Dates
1997-09-27—Published
1996-06-19—Filed