University of Alicante

In order to reduce the problems mentioned above, other alternative methods have been developed, among which the electrochemical regeneration method stands out.

Electrochemical regeneration is characterized by its high performance in regeneration, by its lower energy consumption, by the low cost of treatment, by its environmental friendliness, and by its versatility to regenerate other adsorbent materials (zeolites, etc.).

In this sense, an industrial reactor has been developed for electrochemical regeneration of spent activated carbon, which comprises two possible configurations: with concentric cylindrical electrodes and with parallel plane electrodes, both electrodes separated through an ionic membrane. An electrode is placed in each compartment, which can act as an anode or cathode depending on the process requirements. The electrolyte needed to carry out the electrochemical regeneration has its input at the bottom, and the output at the top of each compartment.

At present, all the studies of electrochemical regeneration have been carried out at laboratory scale using commonly used electrochemical reactors, and the prototypes developed at pilot plant scale only allow to regenerate a maximum of 6 kg. of saturated activated carbon with a solution of two contaminants under very controlled conditions.

At an industrial level, only one technology has been developed that allows the adsorption of the contaminants in NyexTM and the electrochemical destruction within a single reactor.

The lack of studies carried out with spent activated carbons in real situations, the laboratory scale used in the design (from grams to 6 kg.), and the absence of industrial scaling processes, mean that at this time, any alternative recovery method to thermal regeneration lacks a viable industrial application.

In order to overcome the limitations described above, an industrial reactor has been developed that allows the electrochemical regeneration of activated carbon that is partially or totally saturated with organic and inorganic contaminants.

This reactor allows two possible configurations:

a) With cylindrical concentric electrodes (see Figure 1):

Figure 1: schematic view -front and top, respectively- of the electrochemical reactor in concentric cylindrical electrode configuration.

b) With parallel plane electrodes (see Figure 2):

Figure 2: schematic view - in perspective and above, respectively - of the electrochemical reactor in parallel plane electrode configuration.

The electrochemical reactor comprises two compartments (1,2) separated through an ion exchange membrane (5), each one with an electrode (3, 4) and connected to two independent electrolyte recirculation circuits from two electrolyte tanks (6,7), an upper inlet (12) of the activated carbon to be regenerated from a tank or hopper (13), and a lower outlet (14) of regenerated activated carbon.

Stainless steel, platinized titanium (Pt/Ti), ruthenium oxide (RuO₂/Ti) and iridium oxide (IrO₂/Ti), among others, can be used as electrodes (3,4). In general, stainless steel will be used when the electrode acts as a cathode.

In both cases (a and b), the electrochemical reactor is built by the same elements (only the structural configuration varies). The main difference is the shape of the compartments: in the parallel plane configuration (b), both compartments (1,2) are rectangular prisms, and the first electrode (3) is placed in the intermediate panel. The ion exchange membrane (5) can be in an intermediate sector that is not part of any of the compartments (1,2).

The following variables must be taken into account in the procedure for electrochemical regeneration of spent activated carbon:

• The type of electrolyte: acid, basic or neutral.

• The concentration of the electrolyte.

• The type of regeneration: anodic or cathodic.

• The flow of work.

• The current density.

• The time of residence.

• The treatment of activated carbon in the reactor.

ADVANTAGES OF THE TECHNOLOGY

The electrochemical regeneration of spent activated carbon is characterized by the following advantages over current methods:

1) One of the reagents used are electrons, so it can be easily supplied by a direct current source.

2) The process can be immediately interrupted.

3) It can be applied in the same facilities where the material to be regenerated is located (in-situ).

4) It has a high selectivity.

5) Less carbon dioxide (CO₂) emissions are emitted.

6) It has a lower energy consumption than thermal regeneration.

INNOVATIVE ASPECTS OF THE TECHNOLOGY

Unlike current methods of regeneration, this new electrochemical reactor allows recovery any type of spent activated carbon used in different industrial sectors -water and gas treatment, pharmaceutical and chemical, etc.- at pilot plant and industrial level in real conditions.

Therefore, currently, this novel electrochemical reactor is the only available on the market that allows in-situ regeneration of exhausted activated carbons in the 10-15 kg. scale, which it can be easily scaled to more than 100 kg.

Different treatment conditions have been tested in the electrochemical reactor -in both configurations and with different chemical nature electrodes- where the regeneration variables of exhausted granular activated carbon from water treatment plants have been optimized.

In all the cases, an efficiency in the electrochemical regeneration between 90-100% in less than 3 hours has been achieved (see Figure 3), with energy consumption of the process between 0.035-0.061 kWh/kg, 10-15 times less than current 0.53 kWh/kg of the thermal regeneration.

Figure 3: graphic of nitrogen adsorption-desorption isotherms at -196ºC from a depleted activated carbon electrochemical regeneration experiment. The symbols represent: (hollow rhombus with continuous line) is the original activated carbon, (rhombus filled with dotted line) is the exhausted activated carbon, (circle filled with dotted line) is the activated carbon taken in the first hour of treatment, (hollow triangle with dotted line) is the activated carbon taken in the second hour of treatment and (square filled with dotted line) is the activated carbon taken in the third hour of treatment.

This novel electrochemical reactor can be used in the same facility where the application of the activated carbon occurs (in-situ), or it can be transported to another location (ex-situ).

Two pilot plant scale prototypes (TRL=6) are available for demonstration (see Pictures 1 and 2).

Two industrial prototypes have also been built (TRL=7) that allow the electrochemical regeneration of spent activated carbon in 100 kg batches.

Picture 1: electrochemical reactor front view in parallel plane electrode configuration -15 kg. treatment capacity-

Picture 2: electrochemical reactor front view in concentric cylindrical electrode configuration -10 kg. treatment capacity-

This technology allows electrochemical regeneration of spent activated carbon from different industries, including, among others:

• Wastewater treatment and water purification plants.

• Treatment of combustion gases.

• Gas and liquid purification.

• Metals recovery.

• Food and beverage production.

• Pharmaceutical sector.

• Chemical industry.

• Synthesis of catalysts.

It is looking for companies interested in acquiring this technology for commercial exploitation through patent license agreements.

Company profile sought: Spent activated carbon regeneration.

The present invention is protected under patent application:

• Title of the patent: "Reactor electroquímico para la regeneración electroquímica de carbón activado".

• Application number: P202030510.

• Application date: 1^st June, 2020.