CaO/Natural Dolomite as a Heterogeneous Catalyst for Biodiesel Production

2020 ◽  
Vol 991 ◽  
pp. 117-122
Author(s):  
Bachrun Sutrisno ◽  
Atik Dian Nafiah ◽  
Indah Suci Fauziah ◽  
Winarto Kurniawan ◽  
Hirofumi Hinode ◽  
...  
Keyword(s):  
Heterogeneous Catalyst ◽  
Batch Reactor ◽  
Average Pore Size ◽  
Coconut Oil ◽  
Biodiesel Production ◽  
Optimum Process ◽  
Process Conditions ◽  
High Catalytic Activity ◽  
X Ray ◽  
Biodiesel Synthesis

In the present study, the CaO/Natural Dolomite as a heterogeneous catalyst was applied to synthesize biodiesel from coconut oil. The physico-characteristics of CaO/Natural Dolomite catalyst were determined using X-ray diffraction (XRD), X-Ray Fluorescence, and porosity analysis (specific surface area, average pore size diameter and total pore volume). The performance of CaO/Natural Dolomite catalyst was examined in a batch reactor for transesterification reaction of coconut oil with methanol. From the experiments, the optimum process conditions were achieved at a 60°C of reaction temperature, a 5 wt.% of catalyst amount, and 6 : 1 of methanol to coconut oil mass ratio. The CaO/Natural Dolomite catalyst exhibits high catalytic activity and reliable to be applied in biodiesel synthesis as a heterogeneous base catalyst.

scholarly journals TiO2 Nanoparticles As Heterogeneous Catalyst For WCO Biodiesel Production: Engine Parameters Optimization and Prediction of Biodiesel/Diesel/Cadmium (II) Coordination Polymer Blends Fuel By Using Response Surface Methodology

2022 ◽  
Author(s):  
Medhat Elkelawy ◽  
Safaa El-din H. Etaiw ◽  
Ahmed Mohamed Radwan ◽  
Hitesh Panchal ◽  
Hagar Alm-Eldin Bastawissi
Keyword(s):  
Coordination Polymer ◽  
Heterogeneous Catalyst ◽  
Heterogeneous Catalysts ◽  
Direct Injection ◽  
Maximum Yield ◽  
Parameters Optimization ◽  
Biodiesel Production ◽  
Nano Particles ◽  
Optimum Process ◽  
Process Conditions

Abstract Nowadays, combustion technologies decarbonization, reduction of harmful emission, and improving thermal efficiency have gained more attention by using clean, sustainable, alternative, and reliable biofuels coupled with using nano particles technologies. Nano heterogeneous catalysts are new promising technologies for converting triglycerides (oil, fats,..etc) into biodiesel, which characterized with saving in the total cost of production. Titanium dioxide (TiO2) nano heterogeneous catalyst used to convert triglyceride represented in waste cooking oil (WCO) into FAME as bio-diesel, where bio-diesel yield fitted the ASTM. In the present research, the results show 95% as a maximum yield at optimum process conditions of 0.01 Wt.% TiO2 loading, 0.3 Wt.% NaoH, reaction temperature (60 ºC), reaction time (60 min), 10:1 methanol to oil volumetric percentage. Effect of mixing different percentage (35, and 70 ppm) of {[Cd (EIN)2(SCN)2]}, SCP 1, Cadmium (II coordination polymer as nanoparticle enhancer, with diesel fuel/biodiesel (60:40 v/v%) (D60B40) on the behavior of one-cylinder direct-injection diesel (DI) engine parameters were examined experimentally and analytically through RSM methodologies. The engine operating variables have been optimized by using CCD method to achieve an optimal BTE. Engine load and nano particles quantity were considered as process input variables to optimize BTE, UHC, and NOx emissions as engine responses. The quadratic regression models were significant and adequate statistically as indicated by the Analysis of variance (ANOVA). The obtained results from (RSM) optimizer indicated that BTE, NOx, and UHC have optimum values of 16.2605%, 544.9157 ppm, and 117.6023 ppm respectively, at 70 ppm of SCP 1 nanoparticles and 2.1919 Kw of break power as optimal predicted values. A validation examination was carried out and the percent of error was within the limit of 5%. BTE, UHC, and NOx have an error percentage of 2.05%, 1.03%, and 1.63%, respectively.

scholarly journals Modeling the biodiesel production using the wheat straw ash as a catalyst

2021 ◽  
Vol 75 (5) ◽  
pp. 257-276
Author(s):  
Ana Velickovic ◽  
Jelena Avramovic ◽  
Milan Kostic ◽  
Jugoslav Krstic ◽  
Olivera Stamenkovic ◽  
...  
Keyword(s):  
Wheat Straw ◽  
Sunflower Oil ◽  
Methyl Esters ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Catalyst Loading ◽  
Optimum Process ◽  
Process Conditions ◽  
X Ray ◽  
Straw Ash

Wheat straw ash (WSA) was investigated as a new catalyst in biodiesel production from sunflower oil. The catalyst was characterized by temperature-programmed decomposition, X- ray powder diffraction, Hg porosimetry, N2 physisorption, and scanning electron microscopy - energy dispersive X-ray spectroscopy methods. The methanolysis reaction was tested in the temperature range of 55?65?C, the catalyst loading range 10?20 % of the oil weight, and the methanol-to-oil molar ratio range 18 : 1?24 : 1. The reaction conditions of the sunflower oil methanolysis over WSA were optimized by using the response surface methodology in combination with the historical experimental design. The optimum process conditions ensuring the highest fatty acid methyl esters (FAME) content of 98.6 % were the reaction temperature of 60.3?C, the catalyst loading of 11.6 % (based on the oil weight), the methanol-to-oil molar ratio of 18.3 :1, and the reaction time of 124 min. The values of the statistical criteria, such as coefficients of determination (R2 = 0.811, R2 = 0.789, R2 = 0.761) and the mean relative percent deviation (MRPD) value of 10.6 % (66 data) implied the acceptability and precision of the developed model. The FAME content after 4 h of reaction under the optimal conditions decreased to 37, 12, and 3 %, after the first, second, and third reuse, respectively.

scholarly journals Bio-Derived Catalysts: A Current Trend of Catalysts Used in Biodiesel Production

Catalysts ◽  
2021 ◽  
Vol 11 (7) ◽  
pp. 812
Author(s):  
Hoang Chinh Nguyen ◽  
My-Linh Nguyen ◽  
Chia-Hung Su ◽  
Hwai Chyuan Ong ◽  
Horng-Yi Juan ◽  
...  
Keyword(s):  
Catalytic Activity ◽  
Fossil Fuels ◽  
Current Trend ◽  
Biodiesel Production ◽  
High Catalytic Activity ◽  
Promising Alternative ◽  
Advantages And Disadvantages ◽  
Biodiesel Synthesis ◽  
Alkali Catalysts ◽  
A Current

Biodiesel is a promising alternative to fossil fuels and mainly produced from oils/fat through the (trans)esterification process. To enhance the reaction efficiency and simplify the production process, various catalysts have been introduced for biodiesel synthesis. Recently, the use of bio-derived catalysts has attracted more interest due to their high catalytic activity and ecofriendly properties. These catalysts include alkali catalysts, acid catalysts, and enzymes (biocatalysts), which are (bio)synthesized from various natural sources. This review summarizes the latest findings on these bio-derived catalysts, as well as their source and catalytic activity. The advantages and disadvantages of these catalysts are also discussed. These bio-based catalysts show a promising future and can be further used as a renewable catalyst for sustainable biodiesel production.

Acai seed ash as a novel basic heterogeneous catalyst for biodiesel synthesis: Optimization of the biodiesel production process

Fuel ◽  
2021 ◽  
Vol 299 ◽  
pp. 120887
Author(s):  
Erica Karine Lourenço Mares ◽  
Matheus Arrais Gonçalves ◽  
Patrícia Teresa Souza da Luz ◽  
Geraldo Narciso da Rocha Filho ◽  
José Roberto Zamian ◽  
...  
Keyword(s):  
Production Process ◽  
Heterogeneous Catalyst ◽  
Biodiesel Production ◽  
Biodiesel Synthesis

scholarly journals Evaluation of Shell-Derived Calcium Oxide Catalysts for the Production of Biodiesel Esters from Cooking Oils

2021 ◽  
pp. 20-27
Author(s):  
Ngee Sing Chong ◽  
Francis Uchenna Okejiri ◽  
Saidi Abdulramoni ◽  
Shruthi Perna ◽  
Beng Guat Ooi
Keyword(s):  
Calcium Oxide ◽  
Waste Cooking Oil ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
X Ray ◽  
Cooking Oil ◽  
Biodiesel Synthesis ◽  
Cooking Oils ◽  
The Cost ◽  
Percentage Conversion

Due to the high cost of feedstock and catalyst in biodiesel production, the viability of the biodiesel industry has been dependent on government subsidies or tax incentives. In order to reduce the cost of production, food wastes including eggshells and oyster shells have been used to prepare calcium oxide (CaO) catalysts for the transesterification reaction of biodiesel synthesis. The shells were calcined at 1000 °C for 4 hours to obtain CaO powders which were investigated as catalysts for the transesterification of waste cooking oil. The catalysts were characterized by Fourier Transform infrared (FTIR) spectroscopy, thermogravimetric analysis (TGA), X-ray powder diffraction (XRD), and X-ray fluorescence (XRF) spectroscopy. Reaction parameters such as methanol-to-oil molar ratio, CaO catalyst concentration, and reaction time were evaluated and optimized for the percentage conversion of cooking oil to biodiesel esters. The oyster-based CaO showed better catalytic activity when compared to the eggshell-based CaO under the same set of reaction conditions.

scholarly journals Evaluation of dolomite as catalyst in the transesterification reaction using palm oil (RBD)

DYNA ◽  
2019 ◽  
Vol 86 (209) ◽  
pp. 180-187
Author(s):  
Stephanie Alexa Ñústez Castaño ◽  
Duvan Oswaldo Villamizar Castro ◽  
Edgar Mauricio Vargas Solano
Keyword(s):  
Palm Oil ◽  
Batch Reactor ◽  
Methyl Esters ◽  
Average Pore Size ◽  
Molar Ratio ◽  
Reaction Conditions ◽  
Average Pore ◽  
X Ray ◽  
Rbd Palm Oil ◽  
Methyl Ester Content

In this study, the catalytic activity of dolomite was evaluated for the transesterification of Colombian RBD palm oil with methanol, carried out in a batch reactor at 333,15K and 600rpm. The activated dolomites (calcined at 1073.15K for 2h) were characterized by scanning electron microscope (SEM), energy-dispersive X-ray spectroscopy (EDS), Fourier transform infrared spectroscopy (FTIR), Hammett indicators method, and quantification of the surface area, average pore size and average pore volume BET. The influence of reaction variables such as catalyst amount (%wt /wt) and methanol / palm oil molar ratio (mole/mole) was investigated. Under the suitable reaction conditions, the amount of calcined dolomite equal to 4% (wt /wt) based on the weight of oil, the methanol-oil molar ratio equal to 9:1, and the reaction time = 1h, the methyl ester content of 82.67% of fatty acid methyl esters (FAME) can be achieved.

scholarly journals Synthesis and Characterization of Sodium Silicate Produced from Corncobs as a Heterogeneous Catalyst in Biodiesel Production

2020 ◽  
Vol 21 (1) ◽  
pp. 88
Author(s):  
Alwi Gery Agustan Siregar ◽  
Renita Manurung ◽  
Taslim Taslim
Keyword(s):  
Sodium Silicate ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Gas Chromatography Mass Spectrometry ◽  
Catalyst Loading ◽  
Solid Catalyst ◽  
Biodiesel Fuel ◽  
Solid Base ◽  
X Ray ◽  
Biodiesel Synthesis

In this study, silica derived from corncobs impregnated with sodium hydroxide to obtain sodium silicate was calcined, prepared, and employed as a solid base catalyst for the conversion of oils to biodiesel. The catalyst was characterized by X-Ray Diffraction (XRD), Fourier-Transform Infrared Spectroscopy (FTIR), Scanning Electron Microscope Energy Dispersive X-Ray Spectroscopy (SEM-EDS), and Brunauer-Emmet-Teller (BET) and Barrett-Joyner-Halenda (BJH) methods. Gas Chromatography-Mass Spectrometry (GC-MS) was used to characterize the biodiesel products. The optimum catalyst conditions were calcination temperature of 400 °C for 2 h, catalyst loading of 2%, and methanol: oil molar ratio of 12:1 at 60 °C for 60 min, that resulted in a yield of 79.49%. The final product conforms to the selected biodiesel fuel properties of European standard (EN14214) specifications. Calcined corncob-derived sodium silicate showed high potential for use as a low-cost, high-performance, simple-to-prepare solid catalyst for biodiesel synthesis.

scholarly journals Effect of Synthesis Method on the Catalytic Performance of Ca-Mg-Al Mixed Metal Oxide Nanocatalyst for Biodiesel Production from Waste Cooking Oil

2021 ◽  
pp. 13-26
Author(s):  
Mansoor Anbia ◽  
Sotoudeh Sedaghat ◽  
Samira Saleh ◽  
Sholeh Masoomi
Keyword(s):  
Metal Oxide ◽  
Oxide Catalyst ◽  
Waste Cooking Oil ◽  
Biodiesel Production ◽  
Mixed Metal Oxide ◽  
Metal Oxide Catalyst ◽  
X Ray ◽  
Mixed Metal ◽  
Cooking Oil ◽  
Biodiesel Synthesis

The synthesized nanomaterials by two different methods were used as a catalyst in the transesterification of waste cooking oil to produce biodiesel. For both environmental and economic reasons, it is beneficial to produce biodiesel from waste cooking oils. It is desirable to help solve waste oil disposal by utilizing its oils as an inexpensive starting material in biodiesel synthesis. The structure, morphology, and surface properties of resulting nanocatalysts were characterized by X-ray Fluorescence Spectroscopy (XRF), Scanning Electron Microscopy (SEM), X-Ray Diffraction (XRD), Fourier Transform Infrared Spectroscopy (FT-IR), Energy Dispersive X-ray Spectroscopy (EDX) and N2 adsorption-desorption isotherms. The synthesized nanocatalysts' efficiency in the production of biodiesel was studied by Gas Chromatography (GC) as well as leaching amounts of surface active components of each catalyst investigated by the EDX technique. The reactions were performed at 65°C using a 9:1 methanol to oil ratio for 3 h. The results indicate that the impregnated mixed metal oxide catalyst ( Ca-MgAl) shows a higher surface area and better mechanical strength than the totally co-precipitated mixed metal oxide catalyst (CaMgAl(O)). Although both of the fully co-precipitated and impregnated catalysts represented about 90% of fatty acid methyl esters (FAME) yield the leaching of active calcium component was significantly reduced from 45.8% in precipitated CaMgAl(O) to 8% for the impregnated Ca-MgAl catalyst. This improved structure represents the advantage of the impregnation technique to co-precipitation procedure for fabrication of robust nanostructures.

Characterization of Fe2O3-CaO-SiO2 Glass Ceramics Prepared by Sol-Gel

2014 ◽  
Vol 624 ◽  
pp. 114-118 ◽  
Author(s):  
Yao Yao Wang ◽  
Bin Li ◽  
Yong Ya Wang
Keyword(s):  
Sol Gel ◽  
Glass Ceramics ◽  
Optimum Process ◽  
Process Conditions ◽  
X Ray Diffraction ◽  
Crystallization Activation Energy ◽  
Treatment Technology ◽  
X Ray ◽  
Heat Treatment Technology

Ferromagnetic glass ceramics with magnetism and biological activity could be used for magnetic induction hyperthermia. In this study Fe2O3-CaO-SiO2glass-ceramics were prepared by sol-gel method. The sample was characterized by X-ray diffraction (XRD) and differential thermal analysis (DTA). The results showed that the major phases of the sample are wollastonite and magnetite and the crystallization activation energy of sample is 189.3KJ/mol, which would provide a theoretical basis for the establishment of the optimum process conditions of heat treatment technology.

Cu CONTAMINANT REMOVAL USING UV/O3 AND REMOTE HYDROGEN PLASMA

2002 ◽  
Vol 09 (01) ◽  
pp. 255-259 ◽  
Author(s):  
KYUNSUK CHOI ◽  
KWANG PYO HONG ◽  
CHONGMU LEE
Keyword(s):  
Exposure Time ◽  
Process Parameters ◽  
Hydrogen Plasma ◽  
Optimum Process ◽  
Process Conditions ◽  
Plasma Cleaning ◽  
Contaminant Removal ◽  
Cleaning Process ◽  
Cleaning Efficiency ◽  
X Ray

Removal of Cu contaminants from Si wafer was carried out using remote hydrogen plasma (RHP) and UV/O 3 cleaning techniques. The concentration of Cu impurities on the wafer surface was monitored by TXRF (total reflection X-ray fluorescence) and XPS (X-ray photoelectron spectroscopy). Our results show that Cu impurities can be effectively removed by hydrogen plasma and UV/O 3 cleaning techniques, if it is performed under optimum process conditions. The optimum process parameters for the remote hydrogen plasma cleaning are the rf power of 20 W and the exposure time of 5 min. The optimum exposure time of the UV/O 3 cleaning for Cu impurity removal is 1 min. A two-step cleaning process composed of remote hydrogen plasma cleaning first and UV/O 3 cleaning next has been found to be more effective than a single UV/O 3 cleaning process, a single remote hydrogen plasma cleaning process, or a two-step cleaning process composed of UV/O 3 cleaning first and remote hydrogen plasma cleaning next. Cleaning efficiency is maximized at optimum process conditions where Cu contaminant removal effect and recontamination effect are traded off. Increasing the process parameters higher than the optimum values would decrease the cleaning efficiency.

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