Abstract Polychlorinated phenols (e.g., pentachlorophenol) of improved color are made by vacuum distilling polychlorinated phenols containing dark color-forming impurities in the presence of a color inhibitor such as zinc dust or free radical-acting substances (e.g., free radical-acting compounds of the phenol, hydroquinone, organic sulfur derivative, organic phosphite, amine and aldehyde type). Ethylene thiourea or zinc dust appear to offer an optimum combination of improved color, cost and process efficiency and are therefore the preferred color inhibitors. In addition, the chlorodioxin content of the impure pentachlorophenol (generally about) 2,000 p.p.m.) is reduced to a residual chlorodioxin content of less than 25 p.p.m. during distillation.
A METHOD FOR THE SEPARATION AND RECOVERY OF PENTACHLOROPHENOL FROM DARK COLOR-FORMING IMPURITIES CONTAINED THEREIN COMPRISING THE STEPS OF, A. INTRODUCING INTO A DISTILLAND MIXTUREOF PENTACHLOROPHENOL AND DARK COLOR-FORMING IMPURITIES AN EFFECTIVE AMOUNT OF FROM ABOUT 0.1 TO ABOUT 0.5 PERCENT BY WEIGHT OF THE IMPURITY-CONTAINING PENTACHLOROPHENOL OF A ZOLOR INHIBITOR OF ZINC DUST OR ETHYLENE THIOUREA, B. DISTILLINGTHE RESULTING COLOR INHIBITORCONTAINING DISTILLAND AT A PRESSURE FROM ABOUT 35 TO ABOUT 150 MM. HG AND AT A TEMPERATURE OF ABOUT 195*C. TO ABOUT 220*C. TO SEPARATE PENTACHLOROPHENOL VAPORS THEREFROM AND C. CONDENSING SAID VAPOR TO RECOVER PURIFIED PENTACHLORPHENOL IN AN AMOUNT OF AT LEAST 84 PERCENT OF THE IMPURITY-CONTAINING PENTACHLOROPHENOL.
Claim 2
Independent Claim
110 words
A METHOD FOR THE SEPARATION AND RECOVERY OF PENTACHLOROPHENOL FROM DARK COLOR-FORMING IMPURITIES CONTAINED THEREIN COMPRISING THE STEPS OF, A. INTRODUCING INTO A DISTILLAND MIXTUREOF PENTACHLOROPHENOL AND DARK COLOR-FORMING IMPURITIES AN EFFECTIVE AMOUNT OF FROM ABOUT 0.1 TO ABOUT 0.5 PERCENT BY WEIGHT OF THE IMPURITY-CONTAINING PENTACHLOROPHENOL OF A ZOLOR INHIBITOR OF ZINC DUST OR ETHYLENE THIOUREA, B. DISTILLINGTHE RESULTING COLOR INHIBITORCONTAINING DISTILLAND AT A PRESSURE FROM ABOUT 35 TO ABOUT 150 MM. HG AND AT A TEMPERATURE OF ABOUT 195*C. TO ABOUT 220*C. TO SEPARATE PENTACHLOROPHENOL VAPORS THEREFROM AND C. CONDENSING SAID VAPOR TO RECOVER PURIFIED PENTACHLORPHENOL IN AN AMOUNT OF AT LEAST 84 PERCENT OF THE IMPURITY-CONTAINING PENTACHLOROPHENOL.
Claim 3
Dependent Claim
20 words
The method of claim 1 wherein said impure pentachlorophenol contains chlorodioxins and the purified pentachlorophenol contains lower amounts of chlorodioxins.
Claim 4
Dependent Claim
19 words
The process of claim 1 wherein said impure pentachlorophenol is technical grade pentachlorophenol produced by the chlorination of phenol.
Claim 5
Dependent Claim
16 words
The process of claim 3 wherein said phenol is produced by the decomposition of cumene hydroperoxide.
Claim 6
Dependent Claim
15 words
The process of claim 3 wherein said phenol is produced by the sulfonation of benzene.