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Energy Recovery from Waste Tires Using Pyrolysis: Palestine as Case of Study

Mechanical Engineering Department, Faculty of Engineering & Information Technology, An-Najah National University, P.O. Box 7, Nablus 00970, Palestine
Department of Sustainable and Renewable Energy Engineering, College of Engineering, University of Sharjah, Sharjah 27272, UAE
Department of Engineering, ceiA3, University of Almeria, 04120 Almeria, Spain
Author to whom correspondence should be addressed.
Energies 2020, 13(7), 1817;
Received: 22 February 2020 / Revised: 19 March 2020 / Accepted: 3 April 2020 / Published: 9 April 2020
(This article belongs to the Special Issue Energy Saving at Cities)


The first industrial-scale pyrolysis plant for solid tire wastes has been installed in Jenin, northern of the West Bank in Palestine, to dispose of the enormous solid tire wastes in the north of West Bank. The disposable process is an environmentally friendly process and it converts tires into useful products, which could reduce the fuel crisis in Palestine. The gravimetric analysis of tire waste pyrolysis products from the pyrolysis plant working at the optimum conditions is: tire pyrolysis oil (TPO): 45%, pyrolysis carbon black (PCB): 35%, pyrolysis gas (Pyro-Gas): 10% and steel wire: 10%. These results are depending on the tire type and size. It has been found that the produced pyrolysis oil has a High Heating Value (HHV), with a range of 42 43   ( MJ / kg ) , which could make it useful as a replacement for conventional liquid fuels. The main disadvantage of using the TPO as fuel is its strong acrid smell and its low flash point, as compared with the other conventional liquid fuels. The produced pyrolysis carbon black also has a High Heating Value (HHV) of about 29 (MJ/kg), which could also encourage its usage as a solid fuel. Carbon black could also be used as activated carbon, printers’ ink, etc. The pyrolysis gas (Pyro-Gas) obtained from waste tires mainly consist of light hydrocarbons. The concentration of H2 has a range of 30% to 40% in volume and it has a high calorific value (approximately 31   MJ / m 3 ), which can meet the process requirement of energy. On the other hand, it is necessary to clean gas before the burning process to remove H2S from Pyro-Gas, and hence, reduce the acid rain problem. However, for the current plant, some recommendations should be followed for more comfortable operation and safer environment work conditions.
Keywords: pyrolysis; solid tire wastes; PCB; TPO; Pyro-Gas; industrial scale; Palestine pyrolysis; solid tire wastes; PCB; TPO; Pyro-Gas; industrial scale; Palestine

1. Introduction

The world is facing a huge energy gap due to the increase of the human population and the unexpected growth in industry around the world. In Palestine, the consumption of energy has hugely increased in the last years. According to the Palestinian Central Bureau of Statistics, Palestinians consumed more than 30 to 40 thousand barrels per day of petroleum in 2017 [1]. However, Palestine suffers from a scarcity of natural resources and mineral wealth. The suffering of the Palestinians mostly lies in the scarcity of conventional energy sources, such as oil and gas, and additionally, the expensive price of energy, which is equivalent to the most expensive cities in the world. Inspired by this suffering, Palestinians seek to overcome this dilemma and to find alternative sources for conventional fuels.
Nowadays, the trend in the technology of energy is heading towards alternative sources and mainly, renewable energy sources, in order to overcome the rising demands of energy, which are essential in diverse fields of life. There are many sources for alternative fuels, which are based on recycling industrial and household wastes. These wastes exist in different forms: liquid wastes (e.g., cooking oil) and solid wastes. The solid wastes are any kind of rubbish, tires, paper, cardboard, plastic, wood, glass, metallic wastes and ashes.
The world in general, and Palestine in particular, are facing the problem of solid waste due to the highly increasing numbers of the population, and the lack of material resources needed to solve this problem and reduce its risks. Therefore, the solid waste is randomly collected and assembled in the dumps, contrary to the conditions of environmental health, but this is still not a suitable solution. The waste to energy process is a very simple concept involving recovering the maximum energy from waste with minimum damage to the environment by different thermal processes, such as the pyrolysis process [2]. With the rapid development of the auto industry, “black pollution” is being created by more and more waste tires, which now threaten the living environment of humans.
Millions of tons of waste tires are produced worldwide: about 2.5 million tons is generated in North America, Japan generates one million tons and the European Community generates more than 2.5 million tons [3]. In Palestine, in 2012, it was estimated that more than 380 thousand scrap tires were generated from different sources [4]. The tires are composed of vulcanized rubbers, which include natural rubber (NR), styrene butadiene (SBR), and polybutadiene (BR), carbon black, steel wire, cords and additives.
Getting rid of non-biodegradable solid waste tires is one of the most important environmental problems in the world. The durability and immunity of these wastes towards biological degradation makes disposal and re-treatment difficult [2,5]. In Palestine, the solid waste tires are randomly dumped in landfills. These landfills usually face accidental fires that produce extremely thick black smoke and toxic emissions. Such emissions are deleterious to health and may cause the acid rain [5]. Therefore, the biomass pyrolysis is a suitable solution to recycle these waste tires with more environmentally friendly methods. Pyrolysis is considered a cheap way to obtain alternative liquid fuel. By 2050, the International Energy Agency expects that 27% of the fuel used in the transportation industry may be sustainably produced from biomass and waste resources [6].
Tire recycling is the conversion of scrap rubber tires into hydrocarbons for reuse as oils and fuels, and the recovery of steel and carbon is one of the more desirable methods for economically reclaiming scrap tires. Tire recycling is achieved by the pyrolysis process, see Figure 1.
Pyrolysis is the thermochemical decomposition of tires at high temperatures without oxygen. Pyrolysis takes place under low pressure and high temperatures above 420 °C. Practically, pyrolysis cannot be performed oxygen free, since with a limited quantity of oxygen present in the reactor, oxidation will occur at a limited quantity. Pyrolysis of waste tires will produce pyrolysis black carbon (PCB) (30–35 wt%), crude tire pyrolysis oil (TPO) (40–45 wt%), scrap steel (10–15 wt%) and pyrolysis gas (Pyro-Gas) (10–15 wt%) [7].

Pyrolysis Technology and Energy Security in Palestine

Lately, increasing energy consumption, high-price volatility in fossil fuels, interruptions in energy imports and exports, climate change and pollution of the environment are just a few of the many energy security issues in countries throughout the world [8]. Renewable energy and bioenergy play a substantial role in economy, social and environmental life [9,10], bringing significant benefits for developing countries, specifically Palestine. Besides, use of these energy sources avoids or eliminates the negative environmental impacts. Regarding the political situation in Palestine and to avoid the highly frequent blackouts, use of renewable energy and bioenergy (such as pyrolysis) will be a sustainable solution to guarantee the energy supply in the long term. A significant driver of pyrolysis is also the growing interest in environmental sustainability [11]. Energy security is a significant factor that enables the system to function optimally and sustainably, free of threats and risks [12]. Energy security guarantees energy supply reliability at an affordable price, and is therefore affected by economic, political and technical conditions [13].
Energy supply security and environmental issues are considered to be among the main concerns for most countries [8]. While Palestine is highly dependent on imported energy, the results show that solar energy and bioenergy (Pyrolysis) are the most promising renewable and sustainable energy sources. The advantages of pyrolysis include a highly flexible technology that can handle a wide variety of feedstocks consisting of forest residues, food waste, tire waste and solid municipal waste [11]. Palestine is among the most promising locations for utilization of bioenergy and renewable energy sources because of the geographic location of this area, which supplies it with plenty of high solar radiation, and the availability of bioenergy sources. Also, it is highly dependent on energy imported from Israel [9].
To achieve sustainability, this project involves producing a renewable fuel from the pyrolysis process of waste tires. The fuel production from this process involves less costs and less greenhouse gas emissions and makes the environment cleaner. The sustainability aims of this project are directed at solving three main issues: economic, environment and social, in order to achieve energy security and a clean environment in Palestine.
The present study aims at solving the firm technical problems of tire wastes in Palestine. The novelty of this research is that it adds sustainability as an aspect of energy security in Palestine’s energy systems. This is done by introducing the first commercial plant of tire pyrolysis in Palestine.

2. Literature Review

The disposal of waste tires is considered a main economic and environmental problem in the waste management field. For the time being, attention is growing in pyrolysis due to its ability to make products of economic value in different fractions by changing the operating conditions, such as the operating temperatures and heating rate [14]. Pyrolysis also transforms waste tires into tire pyrolysis oil (TPO), pyrolysis carbon black (PCB) and pyrolysis gas (Pyro-Gas), which are considered as high value fuels and chemicals [15,16]. Table 1 below summarizes the pyrolysis research during the period from 1980 to 2018.

3. Methodology

As mentioned earlier, this study was conducted in Palestine to solve the environmental problem of direct burning of the tires and reduce pollution. It is believed that the pyrolysis process of such waste is a suitable solution. The classical tires consist of different materials such as synthetic rubber, steel wires and carbon black. These materials are homogenously distributed over the tire volume. To dispose of these materials using pyrolysis technology, the tires are usually shredded to smaller pieces, washed with water and dried. The tires are placed in a rotary reactor to extract the wires and produce gaseous and liquefied oil. Since no oxygen exists inside the reactor, the carbon black and steel properties will not change.
This study investigates the pyrolysis of tires using an industrial-scale system. The industrial scale is basically a commercial pyrolysis plant, on about 6000 m2 of land in the north of Jenin City, West Bank, Palestine. The pyrolysis plant consists of five sections: the main plant section, the offices section, the laborers rooms section, the waste tire section and the warehouse for the products from pyrolysis. This plant was established in 2013 to get rid of the enormous tire wastes in the north of West Bank. The flow diagram of the pyrolysis process system in this plant is shown in Figure 2.
The plant consists of a horizontal axis cylindrical reactor (6 m long and 2 m diameter) that has a batch mode and rotates with a rotational speed of 0.4 rpm. The reactor chamber can fit up to five tons of partly shredded tires (only small side rings are removed, and steel wires are kept inside). The cylindrical chamber is made from steel and it is initially heated by flames from external source power. Once the system starts producing gaseous fuel from the pyrolysis process, the chamber is now heated by burning the produced gaseous fuel. Therefore, the system is self-sustained in terms of energy. Electricity was used to rotate the chamber for better stirring. The tires were added, and a heavy door was closed tightly. The heat exchangers consist of two groups. The first group contains three heat exchangers that condensate the passing gas coming from the separator. The second group contains two heat exchangers to condensate the remaining gas coming out from the first group. The condensate fuel is filtered to purify the fuel from the contaminations (such as carbon black).
The heating system is composed of an insulated furnace below the reactor. The furnace contains two liquid burners and two gas burners. An insulating cover surrounds the reactor drum. The resulting hot gases pass between the reactor drum and its insulated cover and give enough heat for the pyrolysis process.
Two storage tanks were used in this system: the first tank stores the produced fuel from the first group of heat exchangers, while the second tank stores the remaining produced liquid fuel. The fuel in the first tank is heavier (higher molecular weight fractions) and less clear than the fuel in the second tank. However, the heavy fuel is still demanded in the market for its high heating value and efficient burning. The excess gases that do not liquefy are stored into a third tank, which feeds the heating process. The exhaust gas from the combustion process is filtered for toxic gases before it is spilled out to the atmosphere. The reactor works at a relatively low pressure (the maximum reactor pressure is 0.08 bars). Figure 3 shows the reactor temperatures during heating and cooling processes for four different runs. The total tire load for each run (batch) was 5000 kg. Firstly, the pyrolysis oil produced from previous pyrolysis runs is burned to heat the reactor for the first 3 to 4 h until the temperature reaches 420–500 °C. Secondly, the temperature is held at 420–500 °C by burning the Pyro-Gas produced from the current pyrolysis run. Finally, the reactor is left to cool down naturally for around 10 h. When the reactor is cooled below 60 °C, steel wire and pyrolysis black carbon (PCB) are removed. The PCB fraction is in the form of powder and separated from steel wire while the reactor drum is continuously rotating.
The flue exhaust gas system consists of a chimney, a desulfurization and dust removal unit and an exhaust suction fan. The flue gas is passed through the desulfurization and dust removal unit to filter the dust and remove the sulfur from the flue gas. Finally, the filtered flue gas is exhausted to the atmosphere.

Analaytical Techniques

The original sample of tire and the sample of pyrolysis carbon black (PCB) for the four experiments underwent thermogravimetric analysis to take simultaneous results of differential thermogravimetric analysis (DTA) signals. The thermogravimetric analyses are done by burning the samples (approximately 15 mg for each sample) with a constant heating rate and gas flow rate (15 °C/min) and (100 mL/min), respectively. The calorific value, proximate and elemental analyses were performed, using the procedures of American Society for Testing and Materials (ASTM) standards.
The four samples of tire pyrolysis oil (TPO) from different experiments in the industrial pyrolysis plant were homogenized by mixing the oil well before the analysis was carried out. ASTM standard procedures were also used to find the physical properties of tire pyrolysis oil (TPO): flash point, viscosity, pour point, density and HHV. Elemental analysis of TPO was performed by an elementary analyzer.

4. Results and Discussion

4.1. Yields of the Pyrolysis Products

The yields for each of the fractions of the pyrolysis process obtained from the four experiments are shown in Table 2. The total tire load for each experiment (batch) was 5000 kg. The products of the pyrolysis process for the four experiments were observed to be similar with small differences. These differences are attributed to the tires’ diversity and their size.

4.2. Characterization of Solid Tires and Pyrolysis Carbon Black (PCB)

The original tire and the carbon black fraction for the four experiments were subjected to thermogravimetric analyses. Calorific value and elemental analyses were done according to the ASTM standard procedure.
Proximate and elemental analyses were done on the original tire and the pyrolysis carbon black (PCB) fractions obtained from the four experiments and the results are tabulated in Table 3. It can be concluded that small differences were obtained between the PCB fractions for the four experiments. It can also be noticed that chlorine and sulfur were condensed in the PCB fraction. Approximately, most of the chlorine existing in the waste tires was concentrated in the PCB fraction. Therefore, it is important to take this into consideration once PCB is used as a fuel. So, a system for cleaning the gas would be necessary for the residual gases resulting from combustion of PCB. The PCB residue of the pyrolysis tire process will produce three times the amount of chlorine produced by the original tires [40]. The High Heating Value (HHV) for pyrolysis carbon black (PCB) is about 36 MJ/kg. On the other hand, the HHV for convectional liquid petroleum is 39.5 to 45 MJ/kg. The HHV of PCB is about two times that of wooden biomass (18.5 to 21 MJ/kg). From the analysis results above, it could be concluded that PCB is a possible source of energy.
Figure 4 shows a Derivative Thermogravimetry (DTG) for the original tire and the pyrolysis carbon black (PCB) fractions obtained from the four experiments. It can be concluded from Figure 4 that the highest mass loss rate for the original tire occurs nearly at 390 °C, while for the PCB, it occurs at 570 °C.

4.3. Characterization of Tire Pyrolysis Oil (TPO)

The tire pyrolysis oil (TPO) obtained from the four runs of the pyrolysis plant were relatively similar to each other. TPO is a dark brown oil with a strong acrid smell. It interacts with human skin and it usually leaves spots and a bad smell for several days. So, careful treatment is required during use of TPO. The TPO properties for the four experiments are compared to commercial diesel and the results are tabulated in Table 3. It can be concluded that the density of TPO is more than the density of the commercial diesel and less than the density of the heavy fuel oil (985 kg/m3 at 20 °C). The viscosity of the TPO is more than the viscosity of the commercial diesel and less than the viscosity of heavy fuel oil (200 cSt at 50 °C). Low viscosity of the tire pyrolysis oil is a wanted property in liquid to ease handling and transportation of the fuel. The flash temperature of a fuel gives an indication for the hazards of fire during storage and usage of the fuel. From Table 4, it can be concluded that the flash point of TPO is between 30 and 33 °C. The flash point of TPO is low if it is compared to conventional diesel fuel. The flash point for the conventional diesel fuel is 55 °C, for kerosene the flash point is 23 °C and for light fuel oil it is 79 °C. The flash point of the TPO is low because TPO is a mixture of un-refined liquids that has a wide range of distillation. Table 4 shows that the pour point of the TPO is relatively low when compared with diesel. The pH value of the TPO is between 4.27 and 4.37, which is considered low acidic fuel. This weak acidity is not a problem regarding storage and handling of the TPO, for example, soft drink companies like Cola or Pepsi utilize Polyethylene Terephthalate (PET) plastic for storage and handling, although the value of pH for their drinks is about 2.5 [41]. Subsequently, TPO should be filtered, centrifuged and desulfurized before it can be utilized as a heavy furnace oil or blended with conventional diesel for furnaces, boilers and power plants.

4.4. Characterization of the Pyrolysis Gas (Pyro-Gas) Fraction

The compositional analysis showed that the pyrolysis gas (Pyro-Gas) consists mainly of light hydrocarbons and the concentrations of methane and hydrogen were the highest. Hydrogen concentration could reach 40% in volume at high pyrolysis temperatures of 550 °C [40]. Pyro-Gas has a high heating value (38–41 MJ/m3), which is considered close to the HHV of natural gas (around 39 MJ/m3), that could meet the need of energy during the pyrolysis process or other industrial applications. However, it would be very important to clean Pyro-Gas before burning to take out the hydrogen sulfide (H2S) from the Pyro-Gas fraction. The corrosive nature of H2S would damage the downstream equipment. H2S amount must be less than 500 ppm in order to be used for commercial alternative engines. In addition, SO2 emitted after the combustion of the gas fraction should satisfy the environmental constrains.

5. Summary

The gravimetric analysis of tire waste pyrolysis products from the reactor working at the optimum conditions is tire pyrolysis oil (TPO): 45%, pyrolysis carbon black (PCB): 35%, pyrolysis gas (Pyro-Gas): 10% and steel wire: 10%. It can be concluded that chlorine and sulfur were concentrated in the PCB fraction due to the nature of the tires’ composition. Approximately all chlorine in the tires was concentrated in the PCB fraction. Therefore, it is very important to take this result into account once PCB is used as a fuel.
The main disadvantage of using the TPO as fuel is its strong acrid smell, which could last for a few days if it interacts with human skin or clothes. The density of TPO is more than that of conventional diesel. However, it is still less than the density of heavy fuel oil. On the other hand, the flash point of TPO is low if it is compared with the other refined fuels, which are considered a disadvantage associated with the hazards of fire during the usage and storage of the fuel.
The pH value of the TPO is considered to be of a weak acidic nature but this weak acidity is not a problem regarding storage and handling of TPO. The compositional analysis showed that the pyrolysis gas (Pyro-Gas) consists mainly of light hydrocarbons and the concentration of methane and hydrogen were the highest. The concentration of H2 is about 40% in volume and it has a High Calorific Value (38–41 MJ/m3), which could meet the process requirement of energy. However, it would be very important to clean Pyro-Gas before burning so as to take out the hydrogen sulfide (H2S) from Pyro-Gas, and hence reduce the acid rain problem.
The heavy fuel oil price in Palestine is around 0.5 $/liter. However, the production cost of the tire pyrolysis oil (TPO) is around 0.15 $/liter. This cost is less than one third the price of the conventional heavy fuel oil in Palestine. If three pyrolysis plants, such as the one in the present study with a capacity of 330 (tons/month), were founded, they would be able to get rid of the waste tires generated yearly in Palestine (3800 metric tons). If all the waste tires generated in Palestine were pyrolyzed, the annual import heavy fuel oil would decrease by 1700 tons (11,850 barrels) and produce more than 1330 tons of pyrolysis black carbon and 380 tons of steel wire, yearly. In addition, and most importantly, the environmental hazardous problem of the waste tires could be solved in the correct way, reducing the dependence on imported furnace oil and creating new job opportunities.

6. Conclusions and Recommendations

The following recommendations should be applied for more comfortable operation and safer work and environmental conditions:
  • Handling and transportation of the TPO and PCB must be in a closed system.
  • To produce alternative diesel from pyrolysis tire oil (TPO), more filtration, desulfurization and wet scrubber with CaOH column must be added.
  • To make the technology sustainable, better utilization of PCB must be established.
  • The workers in the pyrolysis plant must be skillful and well trained.
  • There is chlorine present and there is a risk of the formation of carcinogenic dioxins. However, the objective of this research is the energy recovery from waste tires using pyrolysis and the analysis of risk of the formation of carcinogenic dioxins can be considered in the next research paper.
  • Finally, it can be summarized that the pyrolysis plant should be operated only under constant monitoring and advisory support by a team specialized in tire pyrolysis, since it is a new technology.

Author Contributions

R.A., M.A. and A.J. conceived and performed the experiments used in the article; A.J., M.A. and R.A. analyzed the data; R.A., A.J., and M.A. wrote the paper. F.M.-A. and T.S. revised and supervised the manuscript. The authors shared the work on the structure and aims of the manuscript, paper drafting, editing and reviewing the manuscript. All authors have read and agreed to the published version of the manuscript.


This research was funded by An-Najah National University with grant number [ANNU-1819-Sc023].


The authors would like to acknowledge the Deanship of Scientific Research at An-Najah National University for their grant which helped in accomplishing the current study.

Conflicts of Interest

The authors declare no conflict of interest.

List of Abbreviations

NRNatural Rubber
PCBPyrolysis Carbon Black
Pyro-GasPyrolysis Gas
SBRStyrene Butadiene
TPOTire Pyrolysis Oil
PET Polyethylene Terephthalate
HHVHigh Heating Value
ASTMAmerican Society for Testing and Materials
TGAThermogravimetric Analysis
DTGDerivative Thermogravimetry


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Figure 1. Products of the tire pyrolysis process.
Figure 1. Products of the tire pyrolysis process.
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Figure 2. Flow diagram for the tire pyrolysis process.
Figure 2. Flow diagram for the tire pyrolysis process.
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Figure 3. The reactor temperatures during heating and cooling for the four experiments.
Figure 3. The reactor temperatures during heating and cooling for the four experiments.
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Figure 4. Derivative Thermogravimetry (DTG) plots of the original tire and the pyrolysis carbon black (PCB) fractions obtained from the four experiments.
Figure 4. Derivative Thermogravimetry (DTG) plots of the original tire and the pyrolysis carbon black (PCB) fractions obtained from the four experiments.
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Table 1. Pyrolysis research for different countries worldwide: A representative list of waste tire pyrolysis processes.
Table 1. Pyrolysis research for different countries worldwide: A representative list of waste tire pyrolysis processes.
1980JapanIn 1979, the Japanese company Sumitomo Cement Co., Ltd., established a pyrolysis plant with a rotary kiln reactor with an annual capacity of 7000 tons in AΚO City, Hyogo Prefecture. The pilot scale plant was turned into a commercial plant with low costs to recover fuel oil and carbon black.[17,18]
1996FranceA pilot scale batch reactor was designed and used to investigate the effects of different operating conditions like temperature, fuel-to-air ratios and reaction times.It was noticed that there were low percentages of emissions of SO2 and NOx, although the materials relatively contained high-sulfur materials.[19]
1997ItalyThe pyrolysis process is experimentally investigated using a pilot scale reactor. A number of gases were detected in the produced gas, such as H2, O2, N2, CO and CH4.[20]
2000ChinaThis review summarizes the research about pyrolysis of waste tires in china focusing mainly on the mechanism of the pyrolysis process and the pyrolysis reactor design.The pyrolysis industry in China has the tendency towards a small scale and low initial cost pyrolysis plant.[21]
2004ChinaThe pyrolysis process is studied using a pilot scale rotary kiln reactor. The effects of operating temperatures are investigated at a range between 450 and 650 °C.A rotary kiln is considered an excellent alternative for pyrolysis of waste tires.[22]
2005SpainA comparison is made between a fixed-bed laboratory scale and a rotatory pilot scale reactor at the same operating conditions to obtain black carbon, liquid fuel, and Pyro-Gas in the two scales. No significant differences were found between the pyrolysis black carbon obtained from tires in the two scales. [23]
2005ChinaWaste tires were subjected to a pyrolysis process using a rotary kiln pilot scale reactor. Raw pyrolysis black carbon and activated black carbon have acceptable ability for adsorption of methylene-blue compared to commercial black carbon.[24]
2007BangladeshHeavy automotive waste tires were subjected to a pyrolysis process in a fixed-bed reactor under deferent process parameters.Pyrolysis tire oil obtained have fuel properties that make it comparable to liquid petroleum fuels.[25]
2008JapanA fixed-bed reactor that heated using a fire tube was used to pyrolyze the car tire wastes under a nitrogen condition and it was tested under different pyrolysis conditions.The maximum liquid yield is obtained at a temperature of 475 °C.[26]
2008BangladeshThe tire pyrolysis oils produced were subjected to elemental analysis, and chromatographic and spectroscopic techniques.The tire pyrolysis oil could be used as fuel with a high heating value of 42 MJ/kg.[27]
2008BangladeshBicycle waste tires were subjected to a pyrolysis process in a fixed-bed reactor under several process parameters.The pyrolysis tire oil obtained could be comparable to fuels derivative from crude oil if the pyrolysis is performed under suitable operating conditions.[28]
2009BangladeshWaste tires were subjected to thermogravimetric analysis at temperatures between 30 and 800 °C and heating rates of 10 and 60 °C/min.The pyrolysis of waste tires is significantly affected by the heating rate.[29]
2010BangladeshPyrolysis technology using a new heating system to dispose of the solid waste tire and to recovery liquefied fuels. The pyrolysis process is considered an environmentally friendly solution for the waste tires issue.[30]
2010ItalyThe results of several experiments were used to develop a numerical model using the commercial code ChemCAD.The results of an experimental and numerical study for gasification in a rotary kiln reactor of tires were explained.[31]
2011BangladeshFeasibility study was performed to obtain liquid oil, black carbon and Pyro-Gas from waste tires The feasibility study was performed to three different scales. It can be shown that the medium commercial scale is the most economical scale.[32]
2012IndiaA review of pyrolysis of waste tires was made focusing on several operating conditions.The pyrolysis process has three products with commercial value: black carbon, liquid fuel and Pyro-Gas.[33]
2013UKThis review presents that the interest in pyrolysis of waste tires to obtain products with commercial value is growing.The Pyro-Gas produced from pyrolysis of waste tires consists of H2, CO, CO2, H2S and C1-C4 hydrocarbons. This review has focused on upgrading pyrolysis black carbon to activated black carbon and to black carbon with a better quality.[34]
2013BangladeshA small pyrolysis scale of waste tires could reduce the crisis of liquid fuel in waste in Bangladesh.The Pyro-Gas produced from the pyrolysis of waste tires has a high heating value of 37 MJ/m3, which makes it a high enough heat source required to complete the pyrolysis process.[5]
2013BangladeshA fixed bed pilot scale reactor was used to obtain pyrolysis oil from waste tiresThe properties of the pyrolysis oil were comparable to commercial diesel.[35]
2014FranceThe fuel was obtained from the pyrolysis of waste tires at optimum conditions for the temperature, heating rate and inert gas flow rate.Without using inert gas flow, the optimum temperature for the pyrolysis process is 465 °C.[36]
2017PolandThe pyrolysis process for the waste tires was explained using a mathematical model.This work shows the importance of the heat and mass.[37]
2017PolandTwo samples of waste tires and rubber materials were studied and compared at different heating rates (e.g., 10, 20 and 50 K/min).The thermogravimetry equipment (TG) was used to perform a kinetic study and determine the kinetic mechanism of the process.[38]
2018BangladeshThe pyro oil was produced from pyrolysis of scrap tires using a fixed-bed batch reactor.The pyro oil produced from this reactor is used as fuel in a boiler and as furnace oil. The char is potentially used as a fertilizer, and it can be used to produce shoes and conveyor belts.[39]
Pyrolysis Gas: Pyro-Gas. The pyrolysis process allows the communities to have an alternative environmentally friendly source of energy, reduce the need for non-renewable fossil fuels and minimize the landfilling problems.
Table 2. Yield of pyrolysis products.
Table 2. Yield of pyrolysis products.
ProductsAverage (Kg)Average (%wt)
Crude tire pyrolysis oil (TPO)2249.8 ± 63.445 ± 1.63
Pyrolysis carbon black (PCB)1708.5 ± 102.134 ± 2.45
Scrap steel547.5 ± 21.311 ± 0.82
Pyrolysis gas (Pyro-Gas)494.3 ± 70.310 ± 1.83
Table 3. Proximate, elemental and heating value analysis for the tire and carbon black.
Table 3. Proximate, elemental and heating value analysis for the tire and carbon black.
Original Tire (%wt)Carbon Black (%wt)
C 1 (%)84.9295.42 ± 0.16
H 1 (%)7.580.77 ± 0.20
N 1 (%)0.510.22 ± 0.07
S 1 (%)2.413.29 ± 0.09
Cl 1 (%)0.050.19 ± 0.01
O 1 (%)4.530.12 ± 0.07
Ash7.5116.5 5 ± 0.34
Moisture0.971.16 ± 0.14
Volatile matter (%)62.422.50 ± 0.74
HHV (MJ/kg)35.728.70 ± 0.18
1 Results in dry basis and ash free.
Table 4. Characteristics of the tire pyrolysis oil (TPO) in comparison to commercial diesel.
Table 4. Characteristics of the tire pyrolysis oil (TPO) in comparison to commercial diesel.
AnalysesCommercial DieselTire Pyrolysis Oil (TPO)
Elemental (wt%)
C86.5085.69 ± 0.38
H13.209.20 ± 0.08
C/H6.529.32 ± 0.12
N65 ppm < 10.59 ± 0.06
S0.11–0.701.11 ± 0.06
Ash0.00.13 ± 0.02
O0.013.29 ± 0.36
H/C molar ratio1.831.29 ± 0.02
O/C molar ratio-0.029 ± 0.003
Empirical formula-CH1.29O0.029N0.006
Density (kg/m3)820-860962.5 ± 2.08
Viscosity (cSt)2.0–4.5 a4.86 b ± 0.03
Flash Point (°C)>5531.5 ± 1.29
Pour point (°C)-−5.4 ± 0.48
Moisture (wt%)79 ppmND
pH value-4.32 ± 0.05
HHV (MJ/kg)45.1042.46 ± 0.18
ND: Not Determined, a at 40 °C, b at 30 °C.
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