PV Waste Thermal Treatment According to the Circular Economy Concept

: Photovoltaic panels (PV) are one of the most popular technological solutions used to produce green renewable energy. They are known as green technology, but by analyzing a life cycle of a common panel, we can ﬁnd out that production of these panels is strictly associated with generation of a large waste stream. PV modules are constantly modiﬁed and, therefore, it is required to consider the impact of the applied materials on the environment during the whole lifecycle of the product. The most important aspect of the assessment of a life cycle of a photovoltaic module in the phase of decommissioning is material recycling. The process of material recycling is very di ﬃ cult, due to the lamination used in the currently exploited technology. This paper presents the results of pyrolysis for a sample of a silicon module. The results of the presented research show a weight loss of 48.16 in case of the tested samples. This paper presents the outcome of a quantitative analysis of the content of polycyclic aromatic for liquid and concentrations of Br, Cl and F for a gaseous fraction of pyrolysis products. The goal of the research presented in the paper was to ﬁnd the optimal parameters for thermal separation, as well as the inﬂuence of the energy consumption and materials separation e ﬃ ciency on the ﬁnal thermal e ﬃ ciency of the process.


Introduction
Declining natural deposits of energy resources encourage the use of renewable energy sources, which include solar, hydro, geothermal, and wind energy. One of the most developing branches of the renewable energy industry is the market connected with photovoltaics (PV). The history of photovoltaics dates back to the 1930s. The production of solar panels on a commercial scale began already in the 1980s. The first products were based on crystalline silicon (mono-and polycrystalline cells) with a formed semiconductor connector. The next generations were based on thin-film technology using semiconductor materials based on amorphous silicon, cadmium telluride, or metal blends-gal, indium, copper, diselenide.
The most popular branch of photovoltaic technology is the silicon cell technology, especially monoand polycrystalline silicon cells. For common citizens of Europe, the PV technology equals green technology. The cause for such reasoning is the fact that media show the PV technology only from the perspective of the second phase of its life. By the second phase of life for solar panels we understand

The Production Process for Poly-and Monocrystalline Silicon Panels
The production of mono-and polycrystalline solar panels mainly involves the use of blocks of pure silicon. The cell manufacturing process can be divided into several basic stages. The first stage is the extraction and processing of materials into raw materials, which are necessary during the production of cells. Obtaining pure metallic silicon can be achieved by using the following reaction: The purity of the obtained product at this stage can reach values of over 98%. The next step is to remove the remaining impurities from the material to achieve the purity of the sample at the level close to 99.9%. This is possible by using several processes, which are conducted at 500 • C and pressure of 2.5 MPa with a copper catalyst. The whole stage is finished by the pyrolysis process. Maximizing the purity of the substrate used during the production process of silicon cells allows manufacturing of highly efficient cells, which is very important for consumers and is a quality factor for any company. It is possible to use silicon with a lower degree of purity, but it is associated with a decrease in the efficiency of the final product. It should be noted that by reducing the purity of the substrates we reduce the costs of the production processes, which means that we reduce the price of the final product (panels). Thanks to this, the customer can choose from the products of different quality.
The next step is to pour the molten silicon stream into a cooled tank covered with a layer of Si 3 N 4 , in which crystallization occurs. The speed of the crystallization process is regulated by heating elements located around the tank. This method of obtaining silicon is effective for polycrystalline silicon and is called the block casting.
The most commonly used method for obtaining monocrystalline silicon is the Czochralski method. In this process, as in the previous one, polycrystalline silicon is used as a substrate. The whole process consists of several basic stages. The first one consists of melting the polycrystalline silicon in a furnace (preheated to 1410 • C) in an argon atmosphere. Then, the material is cooled to the freezing point. The temperature in the entire volume of the processed material must be kept at a constant, steady level to prevent disturbances during formation of the crystallization front. The production of said front requires cooling of the solution or introduction of an artificial spore. Such an embryo initiates a crystallization process that will lead to formation of a monocrystalline cylindrical crystal. The next step is to remove the resulting embryo. It is important to maintain appropriate extraction speed and temperature during this process and ensure that the embryo rotates around its axis during extraction. The next stage consists of crystal extension.
The crystals obtained as a result of the previously described methods are then cut into plates of appropriate dimensions. Cutting tiles involves production of large amounts of waste. Material losses at this stage of production may reach up to 50%. The next steps leading to the production of a cell include:

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Physical treatment consisting of edge grinding. This process removes all types of mechanical damage and also allows to adjust the thickness of the resulting panel,

LCA
Life cycle assessment (LCA) is a mechanism that allows one to evaluate environmental impact of the product or process during its whole life cycle. The whole life cycle for the product includes: Decommissioning phase.
Usually, when we speak about photovoltaic technology, we think about exploitation phase, because it does not degrade environment and is eco-friendly. Life cycle assessment and comparison of factors allow us to analyze specific technology [29][30][31][32][33][34]. For silicon photovoltaic modules, such an analysis consists of comparison of energy used to produce them with the energy generated by them during their operation, and then conversion of the result to an equivalent expressed in CO 2 emissions units [35]. The important factor for photovoltaic installation is the life cycle-the time in which they can be efficiently exploited, usually 20-25 years in case of silicon modules. To carry out proper analysis of PV technology, we use Energy Pay-Back Time (EPBT) and greenhouse gas (GHG) emissions factors. The former factor allows us to determine how long the installation will be able to work after covering its production costs, and the latter factor allow us to show this additional produced energy in an equivalent of CO 2 emissions for an electric mix in a specific country. A PV system, which uses polycrystalline silicon with efficiency of 16%, has been examined for Belgium. This analysis considered the irradiance characteristic for these areas and their electric mix. For the installation, the EPBT is 6.241 years, and the reduction of the CO 2 emissions is 0.1954 t CO 2 /kWp. In Spain, the LCA analysis was carried out for 200 kWp installation. The research included steps from the acquisition of raw material to generation of electricity. The EPBT for this installation was 3.5 to 5 years. This result is a consequence of a different level of irradiation in the analyzed area in Spain. Most of the energy consumption in this simulation was associated with the module production phase [36]. The typical LCA analysis is based on the life cycle diagram for the analyzed technology; an example of such LCA diagram is shown in Figure 1. The goal of the research presented in the paper was to find the optimal parameters for thermal separation, which would allow us to recycle and manage waste streams generated by PV technology in a way that would minimize the increase of EPBT and GHG factors.

Materials and Methods
As a part of this paper, an experimental pyrolysis and chemical analysis of the remaining fractions were conducted.
The material used for testing is a photovoltaic panel with a concentrator (perianol dye, perylene derivative). In this work, an attempt was made to carry out pyrolysis in an experimental pyrolysis chamber, followed by chemical analysis of the resulting fraction. The advantage of the pyrolysis chambers is the "transformation" of a heterogeneous mass of waste into volatile substances and a char. The use of the pyrolysis process allows to significantly reduce the volume of waste. The analysis involved a low-temperature pyrolysis process using a laboratory pyrolysis chamber [38,39,40].

Materials
The material-a PV panel with concentrator-consisted of an ETFE (ethylenetetrafluoroethylene) layer, three layers of EVA (polyethylene-vinyl acetate), photovoltaic cell made of monocrystalline silicon, and EVA layer saturated with perylene dye (acting as a concentrator that improved quantum yield of fluorescence). The last layer was a plastic based on a polyester resin reinforced with glass fibers. The cross-section of a photovoltaic panel with the use of peripheral dye is shown in Figure 2; the picture is illustrative and the entire panel layer is less than 1 cm [41,42,43,44,45,46].

Materials and Methods
As a part of this paper, an experimental pyrolysis and chemical analysis of the remaining fractions were conducted.
The material used for testing is a photovoltaic panel with a concentrator (perianol dye, perylene derivative). In this work, an attempt was made to carry out pyrolysis in an experimental pyrolysis chamber, followed by chemical analysis of the resulting fraction. The advantage of the pyrolysis chambers is the "transformation" of a heterogeneous mass of waste into volatile substances and a char. The use of the pyrolysis process allows to significantly reduce the volume of waste. The analysis involved a low-temperature pyrolysis process using a laboratory pyrolysis chamber [38][39][40].

Materials
The material-a PV panel with concentrator-consisted of an ETFE (ethylene-tetrafluoroethylene) layer, three layers of EVA (polyethylene-vinyl acetate), photovoltaic cell made of monocrystalline silicon, and EVA layer saturated with perylene dye (acting as a concentrator that improved quantum yield of fluorescence). The last layer was a plastic based on a polyester resin reinforced with glass fibers. The cross-section of a photovoltaic panel with the use of peripheral dye is shown in Figure 2; the picture is illustrative and the entire panel layer is less than 1 cm [41][42][43][44][45][46].

Thermogravimetric
Thermogravimetric measurement was carried out using a Metaller TA1 thermobalance with a vacuum system and inert argon Ar gas (5N purity). A weighed sample (sample mass 284.670 mg) was placed in an Al2O3 crucible (2006.070 mg melting furnace). During double pumping of gas from the system-gas exchange in the system from air to argon-a loss of sample mass equal to approximately 1.5 mg was recorded. On the TG curve, the course of mass change due to heating of the sample can be observed. In order to improve the legibility of the TG curve, the first derivative of the thermogravimetric curve DTG is obtained in parallel with temperature (T). It indicates the rate of change and also allows estimation of the number of reactions. However, on the basis of thermal differential analysis (DTA curve difference: Heating curves), one can assess whether the reactions were endo-or exothermic. Thanks to the DTA method, melting or confusion can be demonstrated (endothermic reactions).

Pyrolysis
Pyrolysis is a widely used process in the chemical industry, e.g., in the production of charcoal, methanol, PVC, activated carbon, and gasoline, as well as for the thermal treatment of waste. Pyrolysis is an alternative to the combustion process or can be used as a supplement. The pyrolysis process is carried out under anaerobic conditions, which leads to production of liquid, gas, and solid products [41]. The use of a moderate temperature regime (300-500 °C) allows production of mainly pyrolysis oil, while at high temperatures (500-900 °C), gas generation occurs [42].
The pyrolysis of the tested material was carried out in a laboratory pyrolysis furnace, which consisted of an electrically heated reaction chamber. In addition, water cooling of the outgoing gases was used, as well as the collection of liquid samples (filter flask) and gas samples was carried out (filter scrubbers and absorbent tubes with activated carbon and an XAD-2 polymer filter).

Discussion
As a result of the thermal process, gas, liquid, and solid products were obtained. The content of gaseous and liquid products was subjected to chemical analysis. The analysis also considers the energy consumption of the process by determining the consumption of electricity. As part of the analysis, thermogravimetry was also carried out to determine the temperature, at which the mass of the analyzed panel is reduced.

Thermogravimetric Results
The recording of the TG and DTG measurement runs is shown in Figure 3. When analyzing the TG curve, it can be concluded that, during the heating of the sample, a weight loss of 82.46% was recorded-i.e., 234.750 mg. The residue after the combustion process was 50.9 mg.

Thermogravimetric
Thermogravimetric measurement was carried out using a Metaller TA1 thermobalance with a vacuum system and inert argon Ar gas (5N purity). A weighed sample (sample mass 284.670 mg) was placed in an Al 2 O 3 crucible (2006.070 mg melting furnace). During double pumping of gas from the system-gas exchange in the system from air to argon-a loss of sample mass equal to approximately 1.5 mg was recorded. On the TG curve, the course of mass change due to heating of the sample can be observed. In order to improve the legibility of the TG curve, the first derivative of the thermogravimetric curve DTG is obtained in parallel with temperature (T). It indicates the rate of change and also allows estimation of the number of reactions. However, on the basis of thermal differential analysis (DTA curve difference: Heating curves), one can assess whether the reactions were endo-or exothermic. Thanks to the DTA method, melting or confusion can be demonstrated (endothermic reactions).

Pyrolysis
Pyrolysis is a widely used process in the chemical industry, e.g., in the production of charcoal, methanol, PVC, activated carbon, and gasoline, as well as for the thermal treatment of waste. Pyrolysis is an alternative to the combustion process or can be used as a supplement. The pyrolysis process is carried out under anaerobic conditions, which leads to production of liquid, gas, and solid products [41]. The use of a moderate temperature regime (300-500 • C) allows production of mainly pyrolysis oil, while at high temperatures (500-900 • C), gas generation occurs [42].
The pyrolysis of the tested material was carried out in a laboratory pyrolysis furnace, which consisted of an electrically heated reaction chamber. In addition, water cooling of the outgoing gases was used, as well as the collection of liquid samples (filter flask) and gas samples was carried out (filter scrubbers and absorbent tubes with activated carbon and an XAD-2 polymer filter).

Discussion
As a result of the thermal process, gas, liquid, and solid products were obtained. The content of gaseous and liquid products was subjected to chemical analysis. The analysis also considers the energy consumption of the process by determining the consumption of electricity. As part of the analysis, thermogravimetry was also carried out to determine the temperature, at which the mass of the analyzed panel is reduced.

Thermogravimetric Results
The recording of the TG and DTG measurement runs is shown in Figure 3. When analyzing the TG curve, it can be concluded that, during the heating of the sample, a weight loss of 82.46% was recorded-i.e., 234.750 mg. The residue after the combustion process was 50.9 mg. The maximum weight shown in Figure 3 is 641.14 mg. This value includes sample weight and the mass of elements used for the measurement of e.g., the hanger, however it does not include the weight of the crucible. Based on the presented thermogravimetric analysis (TG and DTG), it can be noticed that the slow mass decrease started already at about 380 °C (loss of 1 mg). However, the process of the mass loss occurred faster in the temperature range from approximately 290 °C to 565 °C. Based on automatically delineated DTG derivative, the following temperatures were determined: 372.82 °C, 416.93 °C, 482.31 °C, and 538.87 °C. By analyzing TG and DTG line, we can see that the largest change in the mass of the tested sample occurred at approximately 450-480 °C. At this temperature, the change in the mass for the tested sample was equal to 3.6 mg/s. The heating and cooling process during the measurement was carried out with the temperature change equal to 6 K/min. This is a basic study, however, to determine what compounds arise in the given phases of the processes, it would be necessary to perform additional extended thermal and chemical analyses (thermal analysis combined with mass spectroscopy).

Pyrolysis Results
The proper pyrolysis process was preceded by a grinding process in a knife grinder using a sieve with a mesh of diameter of φ 6.0 mm. The tested material, due to the presence of a large number of polymers (including ETFE, several layers of EVA film, polyester resin), required cooling before the grinding process. Liquid nitrogen LN2 was used to cool the sample. The material before and after grinding is presented in Figure 4. The maximum weight shown in Figure 3 is 641.14 mg. This value includes sample weight and the mass of elements used for the measurement of e.g., the hanger, however it does not include the weight of the crucible. Based on the presented thermogravimetric analysis (TG and DTG), it can be noticed that the slow mass decrease started already at about 380 • C (loss of 1 mg). However, the process of the mass loss occurred faster in the temperature range from approximately 290 • C to 565 • C. Based on automatically delineated DTG derivative, the following temperatures were determined: 372.82 • C, 416.93 • C, 482.31 • C, and 538.87 • C. By analyzing TG and DTG line, we can see that the largest change in the mass of the tested sample occurred at approximately 450-480 • C. At this temperature, the change in the mass for the tested sample was equal to 3.6 mg/s. The heating and cooling process during the measurement was carried out with the temperature change equal to 6 K/min. This is a basic study, however, to determine what compounds arise in the given phases of the processes, it would be necessary to perform additional extended thermal and chemical analyses (thermal analysis combined with mass spectroscopy).

Pyrolysis Results
The proper pyrolysis process was preceded by a grinding process in a knife grinder using a sieve with a mesh of diameter of ϕ 6.0 mm. The tested material, due to the presence of a large number of polymers (including ETFE, several layers of EVA film, polyester resin), required cooling before the grinding process. Liquid nitrogen LN2 was used to cool the sample. The material before and after grinding is presented in Figure 4. The mass of the sample was 0.589 kg and was placed in a 11.5 × 35.0 × 7.5 cm cuvette of weight of 1.727 kg. After placing the sample in the furnace, it was flushed with argon. The O2 content was monitored using 5200 Servomax analyzer. The initial O2 content in the furnace chamber was 21.2%. After administration of argon, the oxygen content reached the level below the quantification, i.e., 0%. The reactor was heated to 500 °C. During the test, the temperatures of the furnace (Temp.1), charge (Temp.2), and outlet gases (Temp.3) were measured. The test was carried out for one hour after the appearance of a condensed gas phase, which arose when the temperature of the batch reached 300 °C. In addition, the process was maintained under overpressure in the furnace. In Table 1, the process parameters before and after the pyrolysis are compiled. As a result of pyrolysis, 46.86% weight loss was observed (a difference equal to 0.276 kg). The material balance from the pyrolysis process of three fractions is 53.14% in the solid phase, 24.28% in the liquid phase, and 22.58% in the gaseous phase.
As a result of pyrolysis, more than half of the charge (53.14%) was still in solid form. The remainder was primarily glass fibers made of laminate. The liquid and gas fraction constituted 24.28% and 22.58% of the feed, respectively.
During the test, the initial energy consumption was measured from the moment the furnace was switched on to the end of the test (time t = 75 min). The total electricity consumption measured for 75 min was 4.900 kWh (0.065 kWh/min).
The liquid fraction (pyrolysis oil) was subjected to a qualitative analysis, and the absorption tube with activated carbon and XAD-2 polymer (absorbed organic compounds) and the content of muds (presence of chloride, bromine, and fluorine compounds) underwent a quantitative analysis. The The mass of the sample was 0.589 kg and was placed in a 11.5 × 35.0 × 7.5 cm cuvette of weight of 1.727 kg. After placing the sample in the furnace, it was flushed with argon. The O 2 content was monitored using 5200 Servomax analyzer. The initial O 2 content in the furnace chamber was 21.2%. After administration of argon, the oxygen content reached the level below the quantification, i.e., 0%. The reactor was heated to 500 • C. During the test, the temperatures of the furnace (Temp.1), charge (Temp.2), and outlet gases (Temp.3) were measured. The test was carried out for one hour after the appearance of a condensed gas phase, which arose when the temperature of the batch reached 300 • C. In addition, the process was maintained under overpressure in the furnace. In Table 1, the process parameters before and after the pyrolysis are compiled. As a result of pyrolysis, 46.86% weight loss was observed (a difference equal to 0.276 kg). The material balance from the pyrolysis process of three fractions is 53.14% in the solid phase, 24.28% in the liquid phase, and 22.58% in the gaseous phase.
As a result of pyrolysis, more than half of the charge (53.14%) was still in solid form. The remainder was primarily glass fibers made of laminate. The liquid and gas fraction constituted 24.28% and 22.58% of the feed, respectively.
During the test, the initial energy consumption was measured from the moment the furnace was switched on to the end of the test (time t = 75 min). The total electricity consumption measured for 75 min was 4.900 kWh (0.065 kWh/min).
The liquid fraction (pyrolysis oil) was subjected to a qualitative analysis, and the absorption tube with activated carbon and XAD-2 polymer (absorbed organic compounds) and the content of muds (presence of chloride, bromine, and fluorine compounds) underwent a quantitative analysis. The results provided in the tables refer to the amount of gas obtained during the measurement, i.e., 0.045 m 3 . Table 2 presents the results of the quantitative analysis of the absorption tube made of activated carbon conducted in order to determine the total hydrocarbon content using the gas chromatography (GC-FID) method for toluene (sample P1/1). The analysis was carried out using a gas chromatograph with a flame ionization detector with a DB-1 Elite capillary column. The total hydrocarbon content calculated as toluene in the sample tested was 136.76 mg ± 18.32 mg.  Table 2 presents the results of quantitative analysis to determine the content of polycyclic aromatic hydrocarbons (PAHs) absorbed on the XAD-2 polymer substrate (sample P1/1 and P1/2). Liquid chromatography with fluorescence detection and ultraviolet (HPLEC-FLD/UV) was used for determinations. The analysis was performed using a liquid chromatograph with a gradient pump, FLD fluorescence detectors, VWD spectrometric detectors, and ZPRBAX Eclipse PAH 4.6 × 150 mm, 5 µm column. In the P1/1 sample, the total hydrocarbon content per toluene was calculated, and the value was 136.76 mg/sample. In the P1/2 sample, the highest concentrations were obtained for acenaphthene (79.42 mg/sample) and acenaphthylene (18.96 mg/sample). The lowest concentrations were obtained for naphthalene (1.77 mg/sample) and fluorene (0.010 mg/sample). The content of other PAH hydrocarbons was below the limit of determination.
In the case of pyrolysis oil, a qualitative analysis was performed, both for the gas phase over the liquid and for the substance itself. For the analysis, methods based on FTIR (Fourier Transform Infrared Spectroscopy) and liquid chromatography (HPLEC-FLD/UV) spectrometric techniques were employed.
In the analyzed sample, after pyrolysis (sample P1/3), the presence of bands characteristic for ester compounds, carboxylic acids, and aldehydes was found. These products are formed as a result of oxidation processes during pyrolysis. In the gas phase, spectrogram, aromatic, and aliphatic hydrocarbons were found on the sample's surface. Chromatographic analysis showed the presence of acetaldehyde, propionaldehyde, and traces of acrolein. In addition, GC/FPD analysis was carried out, which showed that the tested sample does not contain sulfur compounds.
Additionally, chemical analysis for halogen in the resulting gas was carried out: Bromine (Br), chlorine (Cl), and fluorine (F). The obtained concentrations are presented in Table 3. The high concentration of fluorine comes mainly from the decomposition of the ETFE polymer. It can contribute to the negative environmental impact of the considered method of recycling of PV panels. However, an appropriate purification system can effectively remove this concentration, which will help to reduce the negative effect.
In order to make the analysis as complex as possible, the low heating value (LHV) was determined using a calorimeter. The results of the analysis are presented in Table 4. In Figure 5, the PV cell carbonization process with the supply of argon gas is presented. The presented figure shows that the highest increase for gases, such as CO and CO 2 , started 25 min after the start of the measurements, when the temperature of the sample was around 390 • C and the temperature of the chamber was approx. 420 • C. The emission of CO 2 ran in two stages. The first one started in the 22nd-23rd minute of the measurement at the temperature of the chamber of approximately 390 • C, and ended in the 35th minute at 490 • C; the second one started in the 42nd minute of the measurement and ended in the 44th minute at the temperature at the start and end of approx. 500 • C. The highest content of CO 2 was around 28% and was achieved in the 35th minute of the measurement. The content of CO was 12.5% and it was achieved in the 36th minute. In case of H2, the highest content was equal to 2.5% and it was obtained in the 41st minute of the measurement. The highest temperature for the chamber was approximately 510 • C, and for the sample it was 500 • C. Both temperatures stabilized at 500 • C in the 58th minute of the measurement. We can find some periodical change in the temperature, but it can be justified by the measurement error or device inaccuracy. The figure also shows us that, after 47 min from the start of the measurement, no more H2 was produced by our sample, and after 45 min the content of the CO and CO 2 produced by the sample was constantly dropping and achieved a value of 2 and 1.5% at the end of the measurement.

Conclusions
The problem of recycling of PV cells is very complex, especially due to the diversity of such cells. In case of cells with a concentrator, the processing can be even more complicated due to the content

Conclusions
The problem of recycling of PV cells is very complex, especially due to the diversity of such cells. In case of cells with a concentrator, the processing can be even more complicated due to the content of harmful substances. The high-temperature processes like pyrolysis can help to solve this problem and assure high quality of end products.
The results of the conducted analysis could be used to determine the possibility of using thermal treatment to dispose of PV panels. They show that the pyrolysis process and the resulting products require further chemical analysis to optimize the process itself, as well as the places and forms of use of the pyrolysis products.
The research presented in the paper was conducted in argon atmosphere. The results of the research carried out using the pyrolysis process show a weight loss of 46.86% of the base mass of the tested sample (a difference of 0.276 kg). The phase balance from the pyrolysis is 53.14% in the solid phase, 24.28% in the liquid phase, and 22.58% in the gas phase. The thermogravimetric analysis shows that the fastest change in the mass of the sample was recorded in the temperature of 450-480 • C, and was equal to 3.6 mg/s. The research also provides the analysis for liquid and gaseous phases, which were produced during the thermal process. The result for gases shows that the sample contains 3039.11 mg/m 3 of toluene, 3039.11 mg/m 3 of acenaphthylene, 421.33 mg/m 3 of naphthalene, 39.33 mg/m 3 of acenaphthene, and 1764.89 mg/m 3 of fluorene. The liquid analysis shows presence of chlorine, bromine, and fluorine in the tested sample. The concentration value for Br was equal to 2 mg/dm 3 , for F it was 33.5 mg/dm 3 , while for Cl it was less than 0.4 mg/dm 3 .
The combustion heat of the char from the pyrolysis process is over 10 MJ/kg, and this value exceeds 6 MJ/kg. Therefore, the waste in this form provides autothermic combustion, it cannot be stored in a landfill, so there is a necessity to find a way to manage it. In order to summarize the potential of pyrolysis in the PV, more field tests should be carried out. Many aspects of the process confirm its value and possible suitability for commercial use. It should also be noted that inclusion of the process of pyrolysis in waste management installations would require appropriate selection of an installation for the treatment of produced gases to eliminate carcinogenic pollutants, such as aromatic hydrocarbons.