Kittwat Owjaraen

Bordin Saengphrom

Inpitcha Limthongtip

Nopparat Tongam

Faculty of Engineering, Srinakharinwirot University, Nakhon Nayok, Thailand

This research aims to study the effect of temperature, collecting time, and condensers on properties of pyrolysis oil. The research was done be analyzing viscosity, density, proportion of pyrolysis products and performance of each condenser towers for the pyrolysis of high-density polyethylene (HDPE) and polyethylene terephthalate (PET) in the mobile pyrolysis plant. Results showed that the main product of HDPE resin was liquid, and the main product of PET resin was solid. Since the pyrolysis of PET results in mostly solid which blocked up the pipe, the analysis of pyrolysis oil would be from the use of HDPE as a raw material. The pyrolysis of HDPE resin in the amount of 100 kg at 400, 425, and 450°C produced the amount of oil 22.5, 27, and 40.5 L, respectively. The study found that 450°C was the temperature that gives the highest amount of pyrolysis oil in the experiment. The viscosity was in the range of 3.287–4.850 cSt. The density was in the range of 0.668–0.740 kg/L. The viscosity and density were increased according to three factors: high pyrolysis temperature, number of condensers and longer sampling time. From the distillation at temperatures below 65, 65–170, 170–250, and above 250°C, all refined products in each temperature range had the carbon number according to their boiling points. The distillation of pyrolysis oil in this experiment provided high amount of kerosene, followed by gasoline and diesel.

Introduction

Energy is important to life and is one of the economic drivers. At present, Thailand has faced with energy problems because Thailand imports energy mainly oil from middle east which affects the way of life and the overall economy of the country. Therefore, energy sustainability is one of Thai society’s problems that urgently need solutions. The utilization of energy from waste is an option that has been promoted by the government which has both direct and indirect benefits.

From the Pollution Control Department’s pollution quantity survey in 2014, the amount of solid municipal waste in Thailand is 26.17 million tons per year. There is only 19% correct disposal, resulting in accumulated waste up to 19.9 million tons per year. There is also an amount of landfill waste accumulated more than 300 million tons and continuously increase every year. Considering the waste composition, there are generally about 18% of plastic waste, equivalent to 3.75 million tons per year and another 25.79 million tons from accumulated waste, which can be processed into pyrolysis oil.

Pyrolysis oil is the oil obtained from biomass, however in this project we use the plastic waste for raw material due to plastic is a main municipal waste in Thailand. The processing rate is 500 L per ton of plastic waste and the oil produced can be used to replace fuel oil and low cycle diesel which our researchers already test in laboratory and confirmed. For this engineering project, we study the temperature of the pyrolysis process to produce oil from plastic pellets, testing the properties of oil obtained at each temperature, and increasing the purity of pyrolysis oil.

The objective of this research is to 1) study the proportion of final pyrolysis oil products in each temperature, 2) study the properties of pyrolysis oil obtained at each temperature, and 3) study the performance of each condensate tower.

Theories and Related Researches

Plastic

Plastics are synthetic organic compounds that are used to replace certain natural materials. The plastic is divided into two types: thermoplastic and thermosetting plastics. There are many types of thermoplastics, such as high density polyethylene (HDPE) with specific gravity values of 0.941–0.965 g/cm³. HDPE has a melting point temperature of about 135°C, with a linear molecular structure. There are also many types of thermosetting plastics. Polyethylene terephthalate (PET) is the one of them.

Pyrolysis Process

The pyrolysis process is the process of decomposition of various compounds or materials with thermal decomposition at temperatures around 400–800°C in an oxygen-free atmosphere or contain very small amount of oxygen.

In general, the products obtained from the pyrolysis process can be divided into three types according to the condition. The primary product can be gas, liquid (which has oil-like properties) and char. The ratio of obtained products depends on the processing conditions, such as temperature, heat rate, etc. The most preferred product is liquid or oil.

Oil Specifications and Testing

There are few characteristics of the oil that can be directly tested by the instrument, such as sulfur content, viscosity values, etc. In addition, most values are measured by using certain tests that use standards to determine, such as using the standards of ASTM (American Society for Testing and Material) or IP (Institute of Petroleum), etc. The properties tested are 1) flash point 2) viscosity 3) heating value and 4) specific gravity.

Chemicals, Equipment and Methods

Chemicals

Chemicals used in this study were HDPE resin from IRPC Company Limited, PET from Thai Chin Kong Industry Corporation Limited, liquefied petroleum gas, and liquid fuel.

Equipment

Equipment used in this study were mobile pyrolysis system kit, gallon volume 4.5 L, cyclone machine, two 12-inch wrench, diameter ½ inch hose (3 m long), long spade, rice sacks, Brookfield viscometer DV-I+, pure distillation unit, and 3-position weighing scales.

Experimental Methods

Preparation of Pyrolysis Reactor

Preparation of pyrolysis reactors by cleaning the machine from sediment trapped inside. Opening the lid of the pyrolysis reactor from above with a wrench (Figure 1A), then use a long spade to scrape off the sediment trapped inside the reactor (Figure 1B). After that, use a cyclone to remove all sediment (Figure 1C).

FIGURE 1

FIGURE 1. Preparation of pyrolysis reactor (A) Opening the lid of a pyrolysis reactor (B) Using metal spade to scrape off any remaining sediments and (C) Extracting excess sediments and any remaining solid from previous operating sessions using Cyclone machine.

Preparation of the Coolant

Water preparation for use in coolers by taking the remaining water out of the coolant tank Figure 2A and add the new one into the tank Figure 2B to be ready to use the coolant for mobile pyrolysis systems.

FIGURE 2

FIGURE 2. Preparation of the coolant (A) Taking remain water out of the coolant tank and (B) Adding new water into the tank.

Adding Raw Materials

The plastic pellets used in the experiment are fed into the pyrolysis reactor as shown in Figure 3.

FIGURE 3

FIGURE 3. Adding raw materials.

Collecting Pyrolysis Oil Samples

After the pyrolysis process is complete, oil samples will be collected at the first, second, third, and fourth condensers respectively, as shown in Figure 4A, by opening the valve of the bottom filter of each condenser, in order to bring the pyrolysis oil that is condensed at that condenser in the pyrolysis oil refining process (Figure 4B).

FIGURE 4

FIGURE 4. Collecting pyrolysis oil samples (A) four collecting areas and (B) Collecting the condensed pyrolysis oil.

Mobile Type Pyrolysis Equipment

Three-dimensional model of mobile type pyrolysis equipment shown in Figures 5A,B conveying plastic waste by waste conveyor (6) into the raw material shredding machine and into (15) pyrolysis reactor heating by using (13) heating furnace to system at a temperature of 400°C. Over time, the plastic granules will become liquid and evaporate into gas flowing into (3) gas separator to enter (1) the main condenser and enter in (1) condense the first, second, third, and fourth units and collect the oil samples at the exit of the four solid filters at the bottom of each condenser, keeping the temperature to 400°C as For 10 min, then collect the oil samples again until complete three times every 10 min. After that, increase the temperature at the reactor to 425 and 450°C. Experimenting the same method at the temperature of 400°C (Figures 6 and 7).

FIGURE 5

FIGURE 5. Three-dimensional model of the mobile pyrolysis equipment set Three-dimensional model of the mobile pyrolysis equipment set when (A,B) consists of (1) Cyclone, (2) Waste conveyor belt, (3) First gas separator, (4) Gas storage tank, (5) Burner, (6) Sub-machine feeder, (7) Condenser, (8) Cooling machine, (9) Second gas separator, (10) Cooling water tank, (11) Pyrolysis oil storage tank, (12) Gear motor stirring set, (13) Kilns, (14) Product filters, (15) Reactor, (16) Pyrolysis oil storage tanks, and (17) Coolant.

FIGURE 6

FIGURE 6. Mobile pyrolysis process flow diagram.

FIGURE 7

FIGURE 7. Mobile type pyrolysis equipment set.

Analysis

Oil Refining Set

The liquid product obtained from pyrolysis of HDPE and PET distilled by the oil distillation kit as shown in Figure 8 consists of 1) thermometer 2) three-way joints 3) round bottom bottles 4) heating furnaces 5) condensers 6) vacuum joints 7) apple shaped bottles that are distilled at low temperature ranges of lower than 65, 65–170, 170–250, and over 250°C.

FIGURE 8

FIGURE 8. The distillation unit consists of (1) thermometer (2) three-way joint (3) round bottom bottle (4) heating furnace (5) condenser (6) vacuum coupling and (7) Erlenmeyer flask.

Viscosity Analysis

Viscosity analysis was accomplished with Brookfield viscometer DV-I+ at 40°C by adding 1 ml of sample into the sample cup and returning to the viscometer. Adjust the cone with the adjustment ring to contact the liquid surface, and adjust the rotation of the machine to 20 RPM to measure viscosity. The result was reported on screen in centipoise (cP), then convert the unit to centistoke (cSt) from Eq. 1.

μ_{c S t} = \frac{μ_{c P}}{ρ \times 1000} (1)

where, $μ_{c P}$ is the viscosity in centipoise (cP) $μ_{c S t}$ is the viscosity in centistoke (cSt) ρ is the density of oil sample in Gram per cubic meter (g/cm³)

Analysis of Hydrocarbon Compounds

Analysis of various hydrocarbon compounds in the pyrolysis oil by fractional distillation with 300 ml volume purity distillation equipment at temperature ranges of lower than 65, 65–170, 170–250, and more than 250°C. These are standard fractional distillation temperature ranges that use in normal petrochemical process which we have adapted in laboratory scale. The petrochemical products were found from this experiment.

Results and Discussion

Effect of Raw Materials on Products

From the experiment, it was found that products obtained from the pyrolysis of HDPE were liquid with brown color, which is shown in Figure 9. On the other hand, the pyrolysis of PET resulted in gas and solid (Figure 10). While gas could be recycled in the process as fuel, solid blocked up the pipe resulting in the termination of process. This corresponds to the study from Williams and Slaney (2007) which stated that the pyrolysis of polyethylene, polypropylene, and polystyrene mostly yield oil products, while the pyrolysis of PET results in mostly solid products. Also, Encinar and Gonzalez (2008) reported that the pyrolysis of PET yields high amount of carbon monoxide and carbon dioxide since the plastic contains high amount of oxygen. Since the pyrolysis of PET could not produce oil, the analysis in the following section would be from the use of HDPE as a raw material only (Figure 10).

FIGURE 9

FIGURE 9. Products obtained from the pyrolysis of HDPE pellets (A) first sample collection (B) second sample collection (10 min after first collection), and (C) the third sample collection (20 min after first collection).

FIGURE 10

FIGURE 10. Products obtained from the pyrolysis of PET pellets.

Effect of Pyrolysis Temperature on Product Properties

The pyrolysis of HDPE at the reactor temperature of 400, 425, and 450°C produced oil with the total amount of 22.5, 27, and 40.5 L per 100 kg of HDPE, respectively. This shows that 450°C is the temperature that produce the highest amount of pyrolysis oil from the experiment. The result corresponds to the study from Kumar and Singh (2013) which reported that the highest liquid yield for HDPE pyrolysis was at 450°C. Furthermore, pyrolysis oil products were measured for density and viscosity at 40°C standard room temperature. It was found that densities of products from the first condenser at the pyrolysis temperature of 400, 425, and 450°C were 0.668, 0.67, and 0.672 kg/L, respectively, while viscosities were 3.287, 3.289, and 3.297 cSt, respectively. It could be seen that density and viscosity increase with the pyrolysis temperature. This is because higher reaction temperature results in product with longer chain of molecules.

Effect of Collecting Time and Condensers on Product Properties

Liquid products from the pyrolysis of HDPE were collected from each condenser for three times: 1) when the system reached the target temperature, 2) 10 min after the first collection, and 3) 20 min after the first collection. Densities and viscosities of these products were illustrated in Figures 11 and 12.

FIGURE 11

FIGURE 11. Densities of products from each condenser at different collecting time (pyrolysis temperature = 450°C).

FIGURE 12

FIGURE 12. Viscosities of products from each condenser at different collecting time (pyrolysis temperature = 450°C).

These figures show the density and viscosity of product at the pyrolysis temperature of 450°C. It could be seen that the density and viscosity of pyrolysis oil increases as the collecting time increases. This is because hydrocarbons with shorter molecular chain could condense earlier than that of the longer chain (Lee and Shin, 2007). Also, the condenser at which the product was collected also affect product properties. Pyrolysis oil tends to have higher density and viscosity as it passes through number of condensers, which is due to the different time of condensation as explained. For other pyrolysis temperatures (400 and 425°C), product yields were low so that no additional oil could be obtained at the time of the second and third collection periods.

Results of Purification by Distillation

To improve the purity of liquid products obtained from the pyrolysis of HDPE and PET, simple distillations were conducted at various temperature ranges (Demirbas, 2004). Theoretically, hydrocarbon compounds with C5−C7 (naphtha) would be found at distillation temperature lower than 65°C, C6–C12 (gasoline) in the range of 65–170°C, C10–C14 (kerosene) in the range of 170–250°C, and C14–C19 (diesel) would be found above the distillation temperature of 250°C. Example of products from the distillation were shown in Figure 13 for HDPE as raw material. The amount of pyrolysis oil from HDPE at different distillation temperature ranges and different collection periods was shown in Figure 14.

FIGURE 13

FIGURE 13. Products obtained from the distillation of the pyrolysis oil from HDPE at the temperature range of (A) 65–170, (B) 170–250, (C) more than 250°C and (D) residue.

FIGURE 14

FIGURE 14. Amount of pyrolysis oil from HDPE at different distillation temperature ranges and different collection periods.

It could be seen that no product was obtained at the distillation temperature below 65°C which could be interpreted that there was no naphtha in this experiment. Kerosene was obtained with highest amount in the temperature range of 170–250°C, followed by gasoline in the range of 65–170°C and diesel at the temperature above 250°C. Also, the first product collection provided the best distillation yield for all temperature ranges since it gave the highest amount of the distillation product.

Fuel Properties

Different types of fuel obtained from the pyrolysis process followed by distillation were measured for densities and viscosities. These are compared with their standard values and can be shown in Table 1.

TABLE 1

TABLE 1. Fuel properties compared with standard values.

It could be seen that densities of pyrolysis fuels were slightly lower than standard values (0.9–2.7% difference), while viscosities are mostly in range. The result shows the quality of products obtained from the pyrolysis process which were close to conventional fuels. With further refining process, these fuels could certainly be used as an alternative source of energy.

Conclusion

Main product for the pyrolysis of HDPE resin was liquid and PET resin was solid. 450°C was the temperature that gives the highest amount of pyrolysis oil in the experiment. The viscosity and density were increased according to three factors: high pyrolysis temperature, the number of condensers and longer collecting time. All refined products in each temperature range had the carbon number according to their boiling points. The distillation of pyrolysis oil in this experiment provided high amount of kerosene, followed by gasoline and diesel.

Data Availability Statement

All datasets analyzed for this study are included in the article/supplementary material.

Author Contributions

All authors listed have made a substantial, direct, and intellectual contribution to the work and approved it for publication.

Conflict of Interest

The authors declare that the research was conducted in the absence of any commercial or financial relationships that could be construed as a potential conflict of interest.

References

Demirbas, A. (2004). Pyrolysis of municipal plastic wastes for recovery of gasoline-range hydrocarbons. J. Anal. Appl. Pyrol. 72 (1), 97–102. doi:10.1016/j.jaap.2004.03.001

CrossRef Full Text | Google Scholar

Encinar, J. M., and González, J. F. (2008). Pyrolysis of synthetic polymers and plastic wastes. Kinetic study. Fuel Process. Technol. 89 (7), 678–686. doi:10.1016/j.fuproc.2007.12.011

CrossRef Full Text | Google Scholar

Kumar, S., and Singh, R. K. (2013). Thermolysis of high-density polyethylene to petroleum products. J. Pet. Eng. 2013, 987568. doi:10.1155/2013/987568

CrossRef Full Text | Google Scholar

Lee, K.-H., and Shin, D.-H. (2007). Characteristics of liquid product from the pyrolysis of waste plastic mixture at low and high temperatures: influence of lapse time of reaction. Waste Manag. 27 (2), 168–176. doi:10.1016/j.wasman.2005.12.017

CrossRef Full Text | Google Scholar

More, B. P., Malve, M. K., Toche, R. B., and Shinde, D. B. (2012). Analysis of adulterant kerosene in diesel by kinematic viscosity measurement. Int. J. Pharm. Biol. Sci. 2 (4), 256–261.

Google Scholar

Williams, P. T., and Slaney, E. (2007). Analysis of products from the pyrolysis and liquefaction of single plastics and waste plastic mixtures. Resour. Conserv. Recycl. 51 (4), 754–769. doi:10.1016/j.resconrec.2006.12.002

CrossRef Full Text | Google Scholar

Keywords: index terms-pyrolysis, high density polyethylene, polyethylene terephthalate, energy, environmental

Citation: Prurapark R, Owjaraen K, Saengphrom B, Limthongtip I and Tongam N (2020) Effect of Temperature on Pyrolysis Oil Using High-Density Polyethylene and Polyethylene Terephthalate Sources From Mobile Pyrolysis Plant. Front. Energy Res. 8:541535. doi: 10.3389/fenrg.2020.541535

Received: 09 March 2020; Accepted: 23 October 2020;
Published: 27 November 2020.

Edited by:

Su Shiung Lam, University of Malaysia Terengganu, Malaysia

Reviewed by:

Reynaldo Palacios-Bereche, Federal University of ABC, Brazil
Rafeah Wahi, Universiti Malaysia Sarawak, Malaysia

Copyright © 2020 Prurapark, Owjaraen, Saengphrom, Limthongtip and Tongam. This is an open-access article distributed under the terms of the Creative Commons Attribution License (CC BY). The use, distribution or reproduction in other forums is permitted, provided the original author(s) and the copyright owner(s) are credited and that the original publication in this journal is cited, in accordance with accepted academic practice. No use, distribution or reproduction is permitted which does not comply with these terms.

*Correspondence: Ruktai Prurapark, cnVrdGFpQGcuc3d1LmFjLnRo