The present application claims priority to U.S. Provisional Application No. 62,734,481, filed Sep. 21, 2018, which is incorporated herein by reference in its entirety.
This invention relates to a method for the treatment of wastewaters using electro-oxidation on boron doped diamond electrodes which achieves almost total destruction of undesirable solutes or pollutants in the wastewaters at high rates of reaction.
The safe disposal of polluted wastewaters is a perennial problem for the world's industries. Many different processes have been developed and utilized to treat wastewaters so that they can meet safe discharge limits. One such process is electro-oxidation utilizing boron doped diamond (BDD) electrodes. Over the past several decades considerable effort has been expended by workers in various countries to develop the process to treat industrial wastewaters. Most of this work has been in the laboratory and on pilot systems and to date there has been limited success in commercializing the process. The technology has been proven to be capable of firstly almost completely destroying all organic species, and some inorganic species in industrial wastewaters, and secondly doing so at a rate approximately corresponding to 100% current efficiency derived according to Faraday's Law. No other electrode material when employed in an electro-oxidation process has proved capable of achieving this performance.
The cost of the boron doped diamond electrode material has proven to be a barrier to developing commercial systems and although the process can treat industrial wastewaters to almost totally remove a broad spectrum of pollutants the rate of the reactions that occur has still proven too slow. As a consequence of the slow reaction rates, a large electrode area is required which has resulted in the capital cost of electro-oxidation systems using boron doped diamond electrodes being high such that their use to treat the majority of industrial wastewater has proven to be not economically feasible. There are really only two routes to achieving economic sustainability and hence providing a route to the commercial use of the technology and these are i) reduce the cost of the boron doped diamond electrode, and ii) significantly increase the rate of reaction. Much effort has been put into i) using approaches utilizing thin diamond films, diamond particles held in a matrix, and others with little success. There has been even less success with respect to ii) mainly because most practitioners of the art have accepted that rates of reaction significantly greater than that signified by 100% current efficiency cannot be achieved. Schemes which have incorporated the injection of oxygen or ozone have been considered but the increase in rate of reaction has not been enough to overcome the high cost of the BDD electrodes. One of the considerable attractions of using an electro-oxidation process to destroy pollutants in wastewaters is that it is perceived to be a simple process. The process is considered to be chemical free and just entails passing a current through the electrolyte, the wastewater, and the electrode material will cause the desired reactions to occur and oxidize the pollutants. As a consequence, very little attention has been paid by researchers and developers to the identification and proper control of important process parameters.
The present invention provides a method of controlling pH of wastewater being treated by electro-oxidation in an electrochemical cell containing boron doped diamond electrodes, comprising allowing and adjusting pH of electrolytes to vary within a defined pH range about a target pH setpoint at a required rate, wherein the pH setpoint, the defined pH range and rate of pH variation is optimized to maximize rate of pollutant destruction in the wastewater.
In an aspect of the invention, the defined pH range is controlled to less than 0.3 pH units, depends upon the nature of the wastewater, and is achieved by cyclically varying the wastewater pH in order to optimize time spent within a pH window so that high rates of reaction are achieved.
In order to enable the reader to attain a more complete appreciation of the invention, and of the novel features and the advantages thereof, attention is directed to the following description when considered in connection with the accompanying drawings, wherein:
The present invention discloses that by controlling certain process parameters with precision and in such a way that practitioners of the art previously have not, then very significant increases in the rate of reaction at the electrodes, and hence the rate at which pollutants are destroyed, can be achieved. From the understanding and knowledge of the inventors of electro-oxidation using a boron doped diamond process, the inventors have identified that the way in which the pH of the wastewater being treated is controlled has a significant effect. Prior to the present invention, the close control of the pH of the electrolytes in the wastewater has not been considered by other workers in the field. During the electro-oxidation process, the pH of the electrolytes changes due to a number of reasons. Normally, in the prior art, the pH is just allowed to drift and to change in an uncontrolled manner. Some practitioners of the art have specified that the electro-oxidation of the wastewaters is performed at acidic or alkali conditions, but other than maintaining these broad requirements, control of pH to particular values has not been attempted. Hitherto, there has not been a realization by practitioners of the art of the need for control to specific values of pH. The present invention discloses that by controlling the pH of the electrolytes in the wastewater, in a particular manner, very high rates of pollutant destruction can be achieved. The achievable rates of destruction are such that the electrode area required can be reduced by greater than an order of magnitude. Such a previously unforeseen reduction in the amount of boron doped diamond electrode material required in an electro-oxidation system results in a large decrease in system capital cost such that it becomes feasible to treat a large variety of wastewaters at a commercially acceptable cost when compared with most other wastewater treatment technologies. Clearly, such a result has not been achieved by any prior art in the field, is unique, and will be of significant benefit.
Referring now to
By means of extensive studies and experiments, the inventors have determined that by controlling the pH in accordance with the scheme shown in
Thus, the critical, unique features of the present invention include, without limitation: (1) the requirement to operate at a specific pH value within a controlled window or range; (2) the required pH value at which the process is operated is dependent upon the nature of the wastewater; (3) operation at the required pH value is achieved by cyclically varying the wastewater pH in order to optimize the time spent within the pH window at which the high rates of reaction are achieved; and (4) by design, it is accepted that the process will not be operating at the required values all of the time, the pH range will be greater than the precise pH window of operation.
The present invention is more particularly described in the following non-limiting example, which is intended to be illustrative only, as numerous modifications and variations therein will be apparent to those skilled in the art.
An oil refinery wastewater was treated at a pH 11.6 setpoint, and the range was 0.25 pH units. The pH was cycled between the upper and lower limits approximately every 15 minutes. Approximately 40% of the organic pollutants in the wastewater were destroyed at a rate between five and ten times that equating to 100% current efficiency before the treatment was terminated.
While the invention has been particularly shown and described with reference to embodiments described above, it will be understood by those skilled in the art that various alterations in form and detail may be made therein without departing from the spirit and scope of the invention, as defined by the appended claims.
Number | Date | Country | |
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62734481 | Sep 2018 | US |