US 4,071,398 A · Chemical concentration by sequential activated carbon adsorption and fractionation

Abstract

A continuous, low cost method of concentrating dilute streams containing fractions of adsorbable chemicals is disclosed which minimizes heat consumption and provides highly concentrated supplies of valuable chemicals which are suitable for reuse or sale without substantial further processing. The methods hereof are particularly adapted for concentrating waste condensates derived from pulp-making operations such as the Kraft or sulfite processes, but in general are also applicable for treating a wide variety of dilute organic or inorganic adsorbable chemicals. The invention involves initially adsorbing and concentrating a chemical fraction from the dilute stream followed by desorption and recycling of the adsorbed materials to further concentrate the same, whereupon the desorbed chemicals are directed to a second concentration zone and concentrated therein; at this point the partially concentrated steam is diverted back to the adsorption zone for further adsorption and concentration simultaneously with the dilute stream initially passing therethrough, while concentration continues in the second zone to yield a final product having a concentration on the order of 90% by weight or better. In preferred forms only a single fractionating column is employed in the second concentration stage which minimizes capital costs and reduces steam consumption, while recycling back to the adsorption zone permits continuous operation of one fractionation column doing the work of two or more columns. Thus, dual use of the single fractionator column in both intermediate and final concentration steps allows continuous operations with equipment heretofore used only in batch-type operations.

A method of continuously handling a dilute stream containing an adsorbable chemical which is continuously fed to a recovery system, and of recovering a highly purified and concentrated stream of the adsorbable chemical, said method comprising the steps of:

continuously directing said dilute stream to an adsorption zone having a plurality of adsorption columns each containing adsorption media;
continuously passing said dilute stream through one of said columns and adsorbing at least a fraction of said chemical on said media therein, thereafter diverting said dilute stream to another of said columns, and continuously passing said dilute stream therethrough for adsorption of at least a fraction of said chemical on the media within said other column;
desorbing said adsorbed chemical on the media within said one column by passing a regenerating agent through the latter during the diversion of said dilute stream to said other column whereby said one column is again capable of receiving said dilute stream and adsorbing said chemical therefrom, and producing a partially concentrated stream containing said chemical which is more concentrated than said dilute stream;
continuously directing at least a fraction of said partially concentrated stream to a second concentration zone which includes concentration apparatus usable on a batch basis, and continuously concentrating said directed fraction of the partially concentrated stream to a desired level in the second concentration zone to thereby produce a further concentrated stream of said chemical and a bottoms fraction;
collecting said bottoms fraction and recycling the same back to said adsorption zone for passage therethrough simultaneously with said dilute stream in order to readsorb any of said chemical within said bottoms fraction on said adsorption media;
continuously collecting said further concentrated stream of said chemical in a holding zone;
stopping the delivery of said partially concentrated stream for a sufficient period of time to permit batch reconcentration in the concentration apparatus of said second concentration zone of at least a part of the further concentrated stream of said chemical held in said holding zone, and redirecting said partially concentrated stream back to said first concentration zone for maintaining the continuity of said method without storage or disposal of said partially concentrated stream;
passing said redirected, partially concentrated stream through said absorption zone simultaneously with said continuous dilute stream, with consequent readsorption of said chemical from the redirected stream onto said adsorption media;
conveying at least a part of said chemical held in said holding zone back to the concentration apparatus of the second concentration zone, after said stoppage and redirection of said partially concentrated stream;
producing a finally concentrated stream of said chemical by a batch concentration of the conveyed part of said further concentrated stream in the batch concentration apparatus of the second concentration zone during said redirection and passage of said partially concentrated stream through said adsorption zone;
and
recovering the finally concentrated stream of said chemical as the latter is produced by said batch concentration.

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Chemical concentration by sequential activated carbon adsorption and fractionation

Life of this patent

Chemical concentration by sequential activated carbon adsorption and fractionation

Life of this patent

Abstract

Claims12