The patent badge is an abbreviated version of the USPTO patent document. The patent badge does contain a link to the full patent document.

The patent badge is an abbreviated version of the USPTO patent document. The patent badge covers the following: Patent number, Date patent was issued, Date patent was filed, Title of the patent, Applicant, Inventor, Assignee, Attorney firm, Primary examiner, Assistant examiner, CPCs, and Abstract. The patent badge does contain a link to the full patent document (in Adobe Acrobat format, aka pdf). To download or print any patent click here.

Date of Patent:
Feb. 20, 1990

Filed:

May. 16, 1989
Applicant:
Inventors:

Thomas E Vara, Vero Beach, FL (US);

Jerald L Mestemaker, Vero Beach, FL (US);

Assignee:

Vara International, Inc., Vero Beach, FL (US);

Attorney:
Primary Examiner:
Int. Cl.
CPC ...
B01D / ;
U.S. Cl.
CPC ...
55 46 ; 55 48 ; 55 51 ; 55 59 ;
Abstract

A process is provided for recovering halogenated hydrocarbons from solvent streams, particularly those including water and at least one alcohol, ketone or ester impurity. The process also provides for the recovery of the alcohol, ketone or ester, which can be reused or incinerated. The solvent stream is condensed and initially spearated into a halogenated hydrocarbon rich fraction and a water rich fraction containing the impurities. Impurities are removed from the halogenated hydrocarbon rich fraction in a first separation step, preferably liquid-liquid extraction with water. The impurities are extracted from the halogenated hydrocarbons into the water, which is passed to the water fraction of the initial separation step for further treatment. Halogenated hydrocarbons leaving the extraction column are passed to a distillation column where remaining water and impurities are removed. A continuous halogenated hydrocarbon vapor draw is preferably removed and condensed from the distillation column. The halogenated hydrocarbon product from the distillation column can, if necessary, be further dehydrated prior to storage or reuse. The water rich fraction is processed in one or more separation steps to remove remaining halogenated hydrocarbons and impurities. The halogenated hydrocarbons are removed in a first water rich fraction distillation step, and the impurities are removed from the water in a second water rich fraction distillation step.


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