scholarly journals Effect of Particle Size and Temperature on Pyrolysis of Palm Kernel Shell

2018 ◽  
Vol 7 (4.35) ◽  
pp. 118
Author(s):  
Khairunnisa Kamarul Zaman ◽  
Vekes Balasundram ◽  
Norazana Ibrahim ◽  
Mohammad Dinie Muhaimin Samsudin ◽  
Rafiziana Md. Kasmani ◽  
...  
Keyword(s):  
Particle Size ◽  
Thermal Behaviour ◽  
Fixed Bed ◽  
Palm Kernel ◽  
Ash Content ◽  
Maximum Temperature ◽  
Pyrolysis Oil ◽  
Biomass Ash ◽  
Palm Kernel Shell ◽  
Biomass Particle Size

Pyrolysis is a viable solution to curb the issue of growing lignocellulosic waste in the world through conversion to potential biofuel and bio-based chemicals. This study focused on the effect of biomass particle size on the feedstock characterisation, biomass ash content, thermal behaviour and pyrolysis products yield. The particle size ranges studied were <0.355, 0.355 to 0.710. 0.710 to 1.00 and 1.00 to 2.00 mm. Thermal behaviour was analysed using thermogravimetric analyser, and pyrolysis experiments were conducted in a fixed-bed pyrolyzer. TGA results show smaller particle size maximum temperature shifted to a lower temperature. From ashing, the results indicated that ash content is the highest at the smallest particle size, <0.355mm (2.8 wt.%). The gaseous yield was the highest in dpA (<0.355 mm) at a temperature of 600°C. The highest pyrolysis oil yield (50.1 wt.%) occurred at 400°C from dpA (<0.355mm). The highest char yield (33.70 wt.%) occurred at 400°C obtained from the largest particle size, dpD (1-2mm).

scholarly journals Properties Tuning of Palm Kernel Shell Biochar Granular Activated Carbon Using Response Surface Methodology for Removal of Methylene Blue

2021 ◽  
Vol 8 (2) ◽  
pp. 1002-1019
Author(s):  
S M Anisuzzaman ◽  
Nirwana Sinring ◽  
Rachel Fran Mansa
Keyword(s):  
Methylene Blue ◽  
Particle Size ◽  
Response Surface Methodology ◽  
Activated Carbon ◽  
Dye Removal ◽  
Chemical Activation ◽  
Palm Kernel ◽  
Ash Content ◽  
Activation Temperature ◽  
Palm Kernel Shell

This study aimed to produce palm kernel shell granular activated carbon (PKSGAC) from slow vacuum pyrolysed PKS biochar (PKSB) via chemical activation using a horizontal tubular split zone furnace. The study also investigated the effects of varying parameters of the PKSGAC on its colour removal ability. The PKSB was activated through chemical activation using potassium hydroxide (KOH) at various parameters such as activation temperature (700oC to 850oC), KOH concentration (50 % w/v to 100 % w/v) and particle size of PKSB (0.4 mm to 2.5 mm). The novelty of this work lies in the study of chemical activation on various particle size ranges using response surface methodology (RSM) to model the relationships between various parameters. The PKSB was characterized to determine its thermal condition, and the PKSGAC was characterized to determine the iodine number, bulk density, ash content, moisture content, surface area and morphology structure. The parameters that were used for each sample were determined by using the RSM based on central composite design (CCD). In this study, design expert version 11.0 software was used and three parameters as independent variables were manipulated. Finally, three different PKSGAC samples of different particle sizes were used to test for the methylene blue (MB) dye removal with the concentration of 5 mg/l, 10 mg/l, 15 mg/l and 20 mg/l. Thermal analysis showed that the total weight loss of the PKSB sample was 58.30% and for PKSGAC the range of the product yield as shown from the RSM was from 33.23% to 96.33%. The RSM also showed that the values for moisture content were in a range from 0% - 39%, as for the ash content value from 2% - 12%, while for the bulk density ranged from 0.17 g/cm3 - 0.50 g/cm3. The highest iodine value achieved was 1320 mg/g at activation temperature of 850oC, KOH concentration of 50% w/v and particle size of 0.4 mm. From the RSM, an iodine number of 1100 mg/g could be obtained using an activation temperature of 850oC, the KOH concentration of 69.22% w/v and the particle size of 0.59 mm. From the BET analysis, the PKSGAC sample obtained 581 m2/g for SBET and 0.3173 cm3/g for the Vtot. The highest percentage dye removal of MB dye was 89.61% to 97.63% at 775oC activation temperature, 75% w/v KOH concentration and 0.4 mm particle size. This work produced RSM models to predict the relationships between the parameters and the response, as well as the performance on MB dye removal.

Effect of Biomass Particle Size on the Fast Pyrolysis Characteristics of Palm Kernel Shell to Produce Biocrude-oil

2017 ◽  
Vol 13 (4) ◽  
pp. 55-63 ◽  
Author(s):  
Yeonseok Choi ◽  
Sangkyu Choi ◽  
Seockjoon Kim ◽  
Soyoung Han ◽  
Yeonwoo Jeong
Keyword(s):  
Particle Size ◽  
Fast Pyrolysis ◽  
Palm Kernel ◽  
Palm Kernel Shell ◽  
Pyrolysis Characteristics ◽  
Biomass Particle Size ◽  
Biocrude Oil

scholarly journals Column Efficiency of Fluoride Removal Using Quaternized Palm Kernel Shell (QPKS)

2019 ◽  
Vol 2019 ◽  
pp. 1-13 ◽  
Author(s):  
Ayu Haslija Abu Bakar ◽  
Luqman Chuah Abdullah ◽  
Nur Amirah Mohd Zahri ◽  
Ma’an Alkhatib
Keyword(s):  
Fluoride Concentration ◽  
Fixed Bed ◽  
Palm Kernel ◽  
Fluoride Removal ◽  
Trimethylammonium Chloride ◽  
Transfer Resistance ◽  
Adsorption Models ◽  
Palm Kernel Shell ◽  
Bed Height ◽  
Fixed Bed Adsorption

In this research, the adsorption potential of quaternized palm kernel shell (QPKS) to remove F− from aqueous solution was investigated using fixed-bed adsorption column. Raw palm kernel shell waste was reacted with 3-chloro-2-hydroxypropyl trimethylammonium chloride (CHMAC) in order to modify the surface charge. The effects of inlet F− concentrations (2–12 mg/l) and QPKS bed height (2–10 cm) with optimum pH (pH = 3) on the breakthrough characteristics of the adsorption system were determined. In the fixed-bed column, breakthrough time increases with increasing bed height due to increasing amount of active site on adsorbents to adsorb the fluoride ion. Decreasing trend of breakthrough values was obtained with increasing initial fluoride concentration due to greater driving force for the transfer process to overcome the mass transfer resistance in the column. The adsorptions were fitted to three well-established fixed-bed adsorption models, namely, Thomas, Yoon–Nelson, and Adams–Bohart models. The results fitted well to the Thomas and Yoon–Nelson models with correlation coefficient, R2 ≥ 0.96.

scholarly journals Hydrogen Production From Steam Gasification of Palm Kernel Shell Using Sequential Impregnation Bimetallic Catalysts

2021 ◽  
Vol 14 ◽  
pp. 58-62
Author(s):  
Anita Ramli ◽  
Siti Eda Eliana Misi ◽  
Mas Fatiha Mohamad ◽  
Suzana Yusup
Keyword(s):  
Catalytic Activity ◽  
Fixed Bed ◽  
Palm Kernel ◽  
Steam Gasification ◽  
Impregnation Method ◽  
Ni Catalysts ◽  
Palm Kernel Shell ◽  
Calcination Temperatures ◽  
Zeolite Β ◽  
Metal Addition

Zeolite β supported bimetallic Fe and Ni catalysts have been prepared using sequential impregnation method and calcined at temperatures between 500-700 ºC. The catalytic activity of these catalysts in a steam gasification of palm kernel shell was tested in a fixed-bed quartz micro-reactor at 700 ºC. Both Fe and Ni active metals present in FeNi/BEA and NiFe/BEA catalysts are corresponding to Fe2O3 and NiO. Different calcination temperatures and different sequence in metal addition have a significant effect to the catalytic activity where FeNi/BEA (700) shows the highest hydrogen produced than other catalysts.

Effect of Particle Size on the Physical Properties of Activated Palm Kernel Shell for Supercapacitor Application

2020 ◽  
Vol 833 ◽  
pp. 129-133
Author(s):  
Ridwan Tobi Ayinla ◽  
John Ojur Dennis ◽  
Hasnah Bt Moh’d Zaid ◽  
Fahad Usman ◽  
Asfand Yar
Keyword(s):  
Particle Size ◽  
Activated Carbon ◽  
Palm Kernel ◽  
Physical Characteristics ◽  
Energy Storage Devices ◽  
Supercapacitor Application ◽  
Palm Kernel Shell ◽  
Storage Devices ◽  
Carbon Production ◽  
Effect Of Particle Size

The advantages of palm kernel shell (PKS) as a renewable and sustainable material for activated carbon production have been explored for various applications such as water treatment, pollutant, pesticide, and heavy metal adsorption. However, the full promises of this material for energy storage devices have not been duly studied. In this research, PKS is physically activated and the effect of particle size on the physical characteristics of the activated char was investigated. Pellet (3 mm), granules (0.4 mm), and powder (0.0075 mm) are the sizes considered in the experiment. The surface morphology, surface area, porosity and functional group at different sized was analyzed. Finally, a suitable particle size was recommended for the electrode material of supercapacitor based on the physical characteristics of the activated carbon.

Effect of particle size and temperature on gasification performance of coconut and palm kernel shells in downdraft fixed-bed reactor

Energy ◽  
2019 ◽  
Vol 175 ◽  
pp. 931-940 ◽  
Author(s):  
Ahmad Zubair Yahaya ◽  
Mahendra Rao Somalu ◽  
Andanastuti Muchtar ◽  
Shaharin Anwar Sulaiman ◽  
Wan Ramli Wan Daud
Keyword(s):  
Particle Size ◽  
Fixed Bed ◽  
Palm Kernel ◽  
Fixed Bed Reactor ◽  
Effect Of Particle Size ◽  
Downdraft Fixed Bed ◽  
Palm Kernel Shells

Bimetallic Fe-Ni/Zeolite β Catalysts for Hydrogen Generation from Steam Gasification of Palm Kernel Shell

2014 ◽  
Vol 925 ◽  
pp. 313-317
Author(s):  
Anita Ramli ◽  
Siti Eda Eliana Misi ◽  
Mas Fatiha Mohamad ◽  
Suzana Yusup
Keyword(s):  
Hydrogen Generation ◽  
Fixed Bed ◽  
Palm Kernel ◽  
Textural Properties ◽  
Lower Surface ◽  
Steam Gasification ◽  
Impregnation Method ◽  
Palm Kernel Shell ◽  
Calcination Temperatures ◽  
Zeolite Β

In this study, the potential usage of PKS as a direct source for hydrogen production is being explored in the presence of bimetallic Fe-Ni/Zeolite β (BEA) catalyst. The catalyst was prepared by co-impregnation method and calcined at temperatures between 500-700 oC to study the effect of calcination temperatures on the gas compositions from steam gasification of PKS. The textural properties and crystalline phase present were characterized using BET and X-Ray Diffraction. The catalysts were tested in steam gasification of PKS in a fixed-bed microreactor at 700 oC using 0.3 g catalyst and 0.9 g PKS. The steam to PKS ratio was 4:1 (vol) while steam to Ar ratio was 1:6 (vol.). The Fe-Ni/BEA catalysts possess lower surface area, higher pore volume and larger pore diameter as compared to the bare BEACalcination temperature is found to contribute to the crystallization of the prepared catalysts where high crystallization of Fe and Ni was observed in Fe-Ni/BEA (700) catalyst with the formation of NiO and NiFe2O4 phase. Fe-Ni/BEA (700) shows the highest composition of H2 gas produced with 76.32 vol% H2, 18.72 vol% CO2, 4.96 vol% CO and the absence of CH4. This shows that the steam gasification of PKS in the presence of Fe-Ni/BEA (700) has a potential to replace the commercial H2 production via methane reforming process.

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