Regularities of electrochemical cleaning of oil-contaminated soils

Electrochemical cleaning of oil-contaminated soils is a promising area of environmental safety, as it can be easily organized even in locations remote from settlements. For this purpose, a power source and a system of electrodes are necessary as equipment. It is possible to use an electric generator if there are no power supply lines nearby. The material of electrodes affects the features of redox processes, which can affect the energy consumption and the degree of soil cleansing from oil or oil products. Therefore, the correct choice of electrode materials is one of the important tasks in the field of engineering electrochemical methods of purification. Changes in the main parameters (humidity, temperature, degree of acidity) in an oil-contaminated model soil, similar in composition to one of the oil fields, were investigated. Measurements of parameters when using graphite and metal electrodes were carried out at several fixed sections of the interelectrode space depending on the treatment time. The established patterns of parameter changes in the purification of oil-contaminated soils allow us to draw conclusions about the stages of the electrochemical process, its speed, and energy efficiency. The results obtained form a basis for designing industrial facilities for soil treatment.

anode determine the type of oxidation and reduction reactions [21,35]. If inert anodes (insoluble electrode) are used, then electronic exchange will occur without destroying the electrode [2]. If an active anode (soluble electrode) is used, then it itself is able to oxidize during electrolysis. Thus, the material of the electrodes significantly affects the efficiency and energy consumption of cleaning and determines the service life. Based on this, it is relevant to evaluate the efficiency of electrochemical processes depending on the materials of the electrodes, the selection of which will improve the efficiency of cleaning contaminated soils at a given processing time interval with the lowest possible energy costs.
The aim of the work is to establish regularities of change in the main parameters (humidity, temperature, degree of acidity) of oil-contaminated soils in the interelectrode space depending on the processing time when using graphite and metal electrodes, which is necessary when designing industrial plants.
It was established in [6,31,32] that when an electric current is passed, the concentration of oil products decreases according to an exponential law: where С0 is the initial concentration of oil products, kg/m 3 ; Ielectric current, A; q(t) is the charge passed through the soil, C; coefficient depending on the type of oil-contaminated soil and the mass of oil products in the cleaned area, C -1 , V is the volume of contaminated soil, m 3 ; qspspecific charge required to remove 1 kg of oil products (for clay soil -6.3·10 6 , black earth soil -9.6·10 6 , loam -9.3·10 6 , sandy soil -13.4·10 6 C/kg [1,10]). Methodology. Experiments were carried out with model soil containing salt solutions (NaCl, CaCl2, MgCl2, etc.) and oil [18]. Oil pollution was % of the mass per 1 kg of soil.
A model soil weighing 1.5 kg was placed in a plexiglas in the form of a rectangular parallelepiped (Fig.1). The electrodes were sunk into the ground.
It is most important to measure humidity, degree of acidity, temperature at three points: at the cathode, anode and in the middle between the electrodes. In experiments, measurements of these parameters were periodically carried out at a given current at five points of the interelectrode space in order to obtain a more detailed characteristic of the distribution of parameters over distance, including for further modeling.
In the experiments, the electric current between the electrodes was maintained at a constant value (0.8 A), which made it possible to determine the main regularities of change in the measured parameters in the interval of 360 min (their control and registration were carried out every 30 min).
One of the objectives of the research was to study the influence of the electrode material on the nature of electrochemical cleaning process. In the first case, a graphite pair was used as electrodes, in the second case, a steel cathode (SC) and a titanium-based ruthenium oxide anode (TROA). Results and their discussion. Measurement of the voltage applied to the graphite electrodes at a constant electric current of 0.8 A made it possible to record its drop from 61.9 to 38.5 V in the first 90 min and a gradual increase to 52 V by 360 min (Fig.2).
When measuring the voltage between the metal electrodes SC and TROA, a constant current of 0.8 A was also maintained. In this case, the voltage decreased from 71 to 40.4 V for the first 90 min, then slowly increased to 47 to 360 min (Fig.2).
The decrease in voltage in the first 90 min in experiments with graphite and metal electrodes (SC-TROA) is explained by the fact that during this period there is an increase in conductivity associated with a redistribution of soil moisture concentration as a result of electrokinetic processes. In the time interval 90 < t < 360 min, when using graphite electrodes, the voltage increases faster and reaches a higher value than when using metal electrodes, therefore, in the second case, the integral conductivity is higher, and energy consumption is lower. To further maintain a constant current value when using graphite electrodes, in contrast to metal ones, a higher voltage of the external power source will be required due to the increased overvoltage of hydrogen and oxygen evolution. At a higher overvoltage, the electrochemical process slows down, the conductivity decreases, and unproductive consumption of electricity for the polarization of the electrodes increases.
From an analysis of the redistribution of humidity in cells with graphite and metal (SC-TROA) electrodes, it can be noted that the humidity at the cathode and anode increases up to 90 min, after which it decreases. In the electrode zones, the humidity values are much higher than in the central interelectrode zone (Fig.3). Evaluating the humidity profiles separately for different electrode materials, one can notice that the maximum humidity values with graphite electrodes are in the cathode and anode areas, and in the middle part of the cell, the humidity tends to a minimum (Fig.3, a); in the case of SC-TROA electrodes, the moisture minimum is shifted from the center to the cathode (Fig.3, b), therefore, in this region, the liquid evaporation is more intense, which leads to an increase in electrical resistance.
When studying the temperature fields in a cell with graphite electrodes, it can be seen that the maximum values are achieved in the central region between the electrodes (third point), the minimum values are in the anode and cathode regions (Fig.4, a). The temperature in the cell with metal electrodes (SC-TROA) has maximum values at the fourth point, and minimum valuesin the anode region (Fig.4, b). These indications are confirmed by the data of thermal imaging (Fig.5) performed by the RGK TL-80 device. An increase in temperature in the central interelectrode region is explained by a decrease in conductivity in the zone under consideration.
The obtained temperature profile data indicate that in the case of using graphite electrodes, the soil resistivity in the central region is higher than in the near-electrode regions, and when using SC-TROA electrodes, the highest soil resistivity shifts in time from the central part to the near-cathode region.
The readings of the degree of soil acidity change from weakly acidic to strongly acidic at all points, then by the end of the measurements, an alkaline medium in the cathode area is formed (Fig.6). In the case of using SC-TROA electrodes, the alkaline medium is formed in a shorter time interval. For the analysis of electrochemical processes, a temperature profile between the electrodes was chosen (Fig.7). Based on the above graphs, the temperature distribution has a parabolic character. If the cell is with graphite electrodes, then the temperature at 180 and 360 min reaches a maximum in the central part of the cell, and it is minimal in the region of the electrodes. In the case of SC-TROA electrodes, the top of the parabola is shifted to the cathode for 180 and 360 min, reaching a maximum value in the near-cathode region.
The given research results can be explained by the fact that the model soil is saturated with salt solutions, mainly chlorides, which creates conditions for electrolysis. After voltage is applied to the electrodes, an intensive movement of ions occurs. Since graphite and ruthenium oxide plates were used as anodes for the experiments, the oxidation proceeded similarly to the electrolysis of solutions with an inert anode. As a result, Cl  ions are oxidized on the anode with the release of Cl2 and water with the release of O2 and the formation of H + . Also, in the area of the anode, the concentration of HCl gradually increases, which subsequently leads to a decrease in soil pH in most of the cell. A wide band of highly acidic environment creates favorable conditions for cleaning the soil from oil pollutants (the degree of cleaning of oil-contaminated soil is more than 71 %). However, in this case, soil acidification occurs, therefore, it is periodically possible to change the polarity of the electrodes to approach the neutral pH level.
Since the solution contains a relatively large amount of active metal cations Ca, Na, Mg, they are not reduced at the cathode, but are concentrated near it in the form of alkaline solutions. At the cathode, only hydrogen ions are reduced from water with gas evolution. Similar results were presented in [3,15,29], but for other soils and the degree of pollution.
The presence on the graphs of areas with a minimum value of moisture characterizes drying, which in some cases is used to strengthen soils. In such regions, the conductivity is low, which contributes to Joule heating, as evidenced by the temperature distribution graphs. Lower temperatures are observed in the anodic regions than in the cathodic ones. When using graphite electrodes, the maximum temperature is reached in the middle of the cell, and when using SC-TROA, in the near-cathode region. This is due to the characteristics of the electrode materials: SC and TROA have lower overvoltage values than graphite ones, which increases the overall conductivity; the overvoltage of TROA is less than that of the SC, so the conductivity near the anode is higher compared to the near-cathode region, as evidenced by the graphs of temperature fields and soil moisture.
Conclusion. From the analysis of experimental studies with graphite and metal electrodes (SC-TROA) it was found that: • the voltage at the initial stage drops to a minimum, then slowly increases, however, when using metal electrodes (SC-TROA), the voltage increases at a slower rate, which indicates lower energy consumption and an increase in soil resistivity; • humidity on the cathode and anode increases up to a certain point in time, after which it decreases; humidity on the electrodes during the entire time interval was higher than in the interelectrode zone (when using graphite electrodes, the humidity tends to a minimum in the middle part of the cell, and when using SC and TROA, the humidity minimum is shifted from the center to the cathode); • the temperature in the cell with graphite electrodes has the highest values in the middle between the electrodes, the lowestat the anode and cathode; the temperature at the final stage in the cell with metal electrodes (SC-TROA) has the highest values in the cathode region, the lowest in the anode region; • soil pH changes from slightly acidic to strongly acidic at all points, but from a certain point in time, an alkaline environment forms near the cathode (when using SC-TROA electrodes, it forms earlier), in the remaining parts of the cell with the studied soil, the environment remains strongly acidic, and the degree of acidity approaches increases towards the anode.
The results of experimental studies of the parameters of oil-contaminated soil (temperature, humidity, degree of acidity) in time and at different distances from the cathode and anode allow to draw conclusions about the main stages of the electrochemical process and its speed. The use of metal