Effect of Temperature and Heating Rate on the Char Yield in Sorghum and Straw Slow Pyrolysis

2017 ◽  
Vol 68 (3) ◽  
pp. 576-580 ◽  
Author(s):  
Alexandru Filipovici ◽  
Dumitru Tucu ◽  
Andrzej Bialowiec ◽  
Przemyslaw Bukowski ◽  
George Catalin Crisan ◽  
...  
Keyword(s):  
Heating Rate ◽  
Energy Production ◽  
Product Yield ◽  
Char Yield ◽  
Effect Of Temperature ◽  
Rate Parameter ◽  
Pyrolysis Process ◽  
Influence Of Process Parameters ◽  
Slow Pyrolysis ◽  
Bio Oil

Different approach to valorise the sweet sorghum using pyrolysis process to obtain valuable resources for energy production: bio-char, bio-oil and syngas are presented in the paper. In this study the influence of process parameters of slow pyrolysis on sorghum and straw were analysed. Temperatures used in the process varied from 400 to 800�C and heating rate parameter varied from 10�C . min-1 to 65�C . min-1. The experiments were conducted using a lab scale slow pyrolysis reactor with electric heaters, equipped with a thermo balance analyzer to collect data of pyrolysis process. The achieved product yield can vary significantly according to the slow pyrolysis parameters. The temperature influenced more on the bio-char yield compared to the heating rate parameter. The highest bio-char yield (over 35% weight,) was obtained at 400�C and heating rate of 10�C . min-1.

scholarly journals Effect of temperature on bio-oil fractions of palm kernel shell thermal distillation

2018 ◽  
Vol 1 (2) ◽  
pp. 27-31
Author(s):  
Deana Qarizada ◽  
Erfan Mohammadian ◽  
Azil Bahari Alias ◽  
Humapar Azhar Rahimi ◽  
Suriatie Binti Mat Yusuf
Keyword(s):  
Liquid Fraction ◽  
Palm Kernel ◽  
Product Yield ◽  
Effect Of Temperature ◽  
Heating Value ◽  
Palm Kernel Shell ◽  
Oil Fraction ◽  
Bio Oil ◽  
Oil Fractions

Distillation is an essential thermo chemical process; it mainly depends on temperature which affects mostly the product yield and composition. The aim of this research is to investigate the effect of temperature on the characterization of bio-oil liquid fraction derived from palm kernel shell (PKS) bio-oil. The temperatures were 100 °C and 140°C. The higher heating value (HHV) obtained were 28.6MJ/Kg and 31.5MJ/Kg for bio-oil fraction 100°C and 140°C respectively. The GC- MS analysis determined that phenol is the dominant product in bio-oil fractions.

scholarly journals Pengaruh Variasi Temperatur Reaktor terhadap Hasil Produk Pirolisis Eceng Gondok Secara Ex-Situ dengan Katalis Bentonit dan Penambahan Uap Air

2020 ◽  
Vol 11 (3) ◽  
pp. 511-520
Author(s):  
Nurkholis Hamidi ◽  
◽  
Anggi Firmansyah ◽  
Haslinda Kusumaningsih
Keyword(s):  
Organic Compounds ◽  
Water Hyacinth ◽  
High Growth ◽  
Ex Situ ◽  
Effect Of Temperature ◽  
Waste Biomass ◽  
Pyrolysis Process ◽  
Bio Oil ◽  
Gas Products ◽  
Increasing Temperature

The water hyacinth has high growth rates that can lead to various environmental problems and the production of large amounts of waste biomass. However, it can be a source of lignocellulosic biomass for the production of bio-oil. This study aims to determine the effect of temperature variation on the pyrolysis process of water hyacinth ex-situ with bentonite catalyst and the addition of water vapor. Temperature variations used are 450°C, 550°C, and 650°C. The pyrolysis process uses 300 grams of water hyacinth and is carried out for 1 hour. The results showed that increasing pyrolysis temperature reduced the char and bio-oil products, but increased the product of gas. Pyrolysis at 450°C produces a lot of bio-oil, while at the temperature of 650°C tends to produce gas products. Also, increasing the pyrolisis temperature results in a higher density of bio-oil. Gas chromatograph testing was carried out to determine the content of organic compounds found in bio-oil. Hydrocarbons are obtained which increase with increasing temperature. The highest percentage of the content of organic compounds is in oxygen compounds. Components of alcohol, phenols, ketones, aldehydes are functional compounds found in the content of bio-oil. Acid compounds are also contained in bio-oil from the results of pyrolysis of water hyacinth.

scholarly journals Pyrolysis and Kinetic Analysis of CO2 Fixation Marine (Isochrysis sp.) and Freshwater (Monoraphidium c.) Microalgae

2021 ◽  
Author(s):  
Noridah B. Osman ◽  
Umi Syahirah Binti Mohd Amina ◽  
David Onoja Patrick ◽  
Nurul Asyikin Binti Bad ir Noon Zamana ◽  
Syazmi Zul Arif n Hakimi Saado ◽  
...  
Keyword(s):  
Co2 Fixation ◽  
Fixed Bed ◽  
Product Yield ◽  
Marine Species ◽  
Pyrolysis Process ◽  
Heating Rates ◽  
Nitrogen Flow Rate ◽  
Freshwater Microalgae ◽  
Thermogravimetric Analyzer ◽  
Bio Oil

Abstract Marine and freshwater microalgae grow in two different ecosystems, which influence their properties thus requires attention prior to determining its application. This paper has successfully disclosed the thermal, chemical, and physical properties of two types of microalgae on carbon dioxide (CO2) fixation and underwent pyrolysis process. Slow pyrolysis process for marine and freshwater microalgae (Isochrysis sp. and Monoraphidium c.) was performed in the fixed bed pyrolysis reactor and TGA (thermogravimetric analyzer) to determine the product yield and study their thermal decomposition profile. The pyrolysis was completed at various temperatures (400, 450, 500, and 550°C) at a heating rate of 15 °Cmin-1 and nitrogen flow rate of 200 ml min-1. Pyrolysis in TGA analyzer ran from 27 to 800°C at three heating rates (10, 20, and 40 °Cmin-1). For chemical composition, Fourier-transform Infrared (FTIR) analysis was performed on both microalgae samples. The highest yield (up to 33.9%) of bio-oil was obtained from Isochrysis sp. for all temperatures while the highest average yield (65.78%) of bio-char was collected from Monoraphidium c. species. From TGA pyrolysis, the major decomposition occurred between 200-400°C for Monoraphidium c. species. On the other hand, the decomposition profile of Isochrysis sp. was slightly slower, which may be due to the differences in lipid composition (FTIR peak 2929 cm-1). The activation energy of all tests is lower (33.6-40.3 kJ mol-1) compared to several other biomasses. Marine species fixed with CO2 showed promising results even without addition of catalyst and no additional cost needed.

In Situ Pyrolysis of Pine Flowers to Produce Bio-Oil: Effect of Temperature and Catalyst Treatment

2020 ◽  
Vol 981 ◽  
pp. 185-189
Author(s):  
Ariany Zulkania ◽  
Nasim Zegarra Yasha ◽  
Shandy Adesya Rachman ◽  
Achmad Chafidz
Keyword(s):  
Renewable Energy ◽  
Energy Production ◽  
Temperature Treatment ◽  
Effect Of Temperature ◽  
Heating Value ◽  
Mixed Catalyst ◽  
Bio Oil ◽  
The Difference

Nowadays, the demand for renewable energy increases dramatically which is caused by the crisis of fossil fuel. Bio-oil is one of the environmental renewable energy since it can be produced from biomass. Pine flowers as biomass mostly still become waste so that it has the potential to become a source of energy production. The purpose of this study is to investigate the effect of temperature and catalyst treatment on the characterization of bio-oil obtained. This research was using Zeolit catalyst activated by HCl 4N for six hours and impregnated by Fe2(NO3)3.9H2O. The experiment was carried out at different temperature treatment (450 °C, 500 °C, 550 °C) and different catalyst treatment (non-catalyst, non-impregnated catalyst, and impregnated catalyst). The catalyst and the biomass with size of (-100+120) mesh and (-30+40) mesh, respectively, were mixed where the catalyst used was 5% of the total weight of the biomass. The mixed catalyst-biomass was then put into the reactor to be pyrolyzed. The pyrolysis process was carried out by flowing N2 gas to prevent the presence of oxygen in the reactor. The result showed that optimum bio-oil production, 33.73%, was obtained from the sample with 550 °C with non-impregnated catalyst. The resulting bio-oil has the following properties : dark brown, yield of bio-oil 17.58%-33.73%, pH 2.95-3.56, density 1.055 gr/mL-1.068 gr/mL, and heating value 2,065.07-2,490.40 cal/gr. Finally, the GCMS results with the effect of temperature and catalyst treatment show the difference in the percentage of the phenolic-aromatic compound, acid, hydrocarbon, and ketone.

scholarly journals Multi-parametric optimization of the catalytic pyrolysis of pig hair into bio-oil

Clean Energy ◽  
2021 ◽  
Vol 5 (3) ◽  
pp. 527-535
Author(s):  
Henry Oghenero Orugba ◽  
Jeremiah Lekwuwa Chukwuneke ◽  
Henry Chukwuemeka Olisakwe ◽  
Innocent Eteli Digitemie
Keyword(s):  
Heating Rate ◽  
Catalytic Pyrolysis ◽  
Oxide Catalyst ◽  
Fixed Bed ◽  
Fixed Bed Reactor ◽  
Oil Yield ◽  
Pyrolysis Process ◽  
Heating Value ◽  
Bio Oil ◽  
Temperature Heating

Abstract The low yield and poor fuel properties of bio-oil have made the pyrolysis production process uneconomic and also limited bio-oil usage. Proper manipulation of key pyrolysis variables is paramount in order to produce high-quality bio-oil that requires less upgrading. In this research, the pyrolysis of pig hair was carried out in a fixed-bed reactor using a calcium oxide catalyst derived from calcination of turtle shells. In the pyrolysis process, the influence of three variables—temperature, heating rate and catalyst weight—on two responses—bio-oil yield and its higher heating value (HHV)—were investigated using Response Surface Methodology. A second-order regression-model equation was obtained for each response. The optimum yield of the bio-oil and its HHV were obtained as 51.03% and 21.87 mJ/kg, respectively, at 545oC, 45.17oC/min and 2.504 g of pyrolysis temperature, heating rate and catalyst weight, respectively. The high R2 values of 0.9859 and 0.9527, respectively, obtained for the bio-oil yield and its HHV models using analysis of variance revealed that the models can adequately predict the bio-oil yield and its HHV from the pyrolysis process.

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