scholarly journals Modified sodium molybdate as an efficient high yielding heterogeneous catalyst for biodiesel from Ghanaian indigenous Camelina sativa as a non-edible resource

2021 ◽  
Vol 2 (1) ◽  
Author(s):  
Mohammed Takase ◽  
Paul Kwame Essandoh ◽  
Rogers Kipkoech
Keyword(s):  
Reaction Time ◽  
Sodium Molybdate ◽  
Normal Pressure ◽  
Camelina Sativa ◽  
International Standards ◽  
Lewis Acidity ◽  
Molar Ratio ◽  
Solid Catalyst ◽  
Atmospheric Conditions ◽  
Heterogeneous Solid

AbstractSodium molybdate (Na2MoO4) has been synthesized and investigated as a heterogeneous solid catalyst for biodiesel from Camelina sativa seed oil. Transesterification reactions occurred under atmospheric conditions with relatively, low temperature short reaction time and normal pressure. The prepared catalyst was characterised by means of SEM, TGA, UV, XRD and FTIR. The properties of the biodiesel were compared with international standards. The transesterification reaction was very efficient with the optimum yield higher than 95% at methanol to oil molar ratio of 17:1, catalyst amount of 6%, reaction temperature of 60 °C and reaction time of 2.5 h. The molybdate complex had a high Lewis acidity and most certainly act as alcohol O–H bond leading to a transient species which has high nucleophilic character. The catalyst was easily recovered and after being washed for three times, showed capacity of recyclability for another catalytic reaction of five cycles with similar activity. The properties of the biodiesel were comparable to international standards.

Transesterification of Cotton-Seed Oil by Heterogeneous Solid Super Base KF/MgO Catalyst

2011 ◽  
Vol 287-290 ◽  
pp. 1496-1504
Author(s):  
Yun Long Fan ◽  
Wan Quan Zhang ◽  
Liu Yang ◽  
Dong Lin Hu ◽  
Li Xin Zhu ◽  
...  
Keyword(s):  
Reaction Time ◽  
Cotton Seed ◽  
Seed Oil ◽  
Molar Ratio ◽  
Catalyst Characterization ◽  
Indicator Method ◽  
Catalyst Amount ◽  
Benign Process ◽  
Heterogeneous Solid ◽  
Cotton Seed Oil

An environmentally benign process was developed for the production of biodiesel from cotton-seed oil using KF loaded with MgO as a heterogeneous solid super base catalyst. The 20 wt% KF/MgO, after desiccated at 120 oC for 4 h, was found to be the optimum catalyst. Hammett indicator method, XRD, SEM and IR were employed for the catalyst characterization. The results showed the activity of the catalysts was correlated with their basicity. The influence of various reaction variables on the conversion, such as the molar ratio of methanol to cotton-seed oil, the catalyst amount, the reaction time and temperature were also discussed. When the transesterification reaction was carried out at reflux of methanol (65 oC), with a molar ratio of methanol to cotton-seed oil 12 : 1, a reaction time 2.5 h and a catalyst amount 2.5 wt%, the highest conversion of cotton-seed oil reached 99.14%.

scholarly journals Impregnation of CaO from Eggshell Waste with Magnetite as a Solid Catalyst (Fe3O4/CaO) for Transesterification of Palm Oil Off-Grade

Catalysts ◽  
2020 ◽  
Vol 10 (2) ◽  
pp. 164 ◽  
Author(s):  
Zuchra Helwani ◽  
Muliadi Ramli ◽  
Edy Saputra ◽  
Bahruddin Bahruddin ◽  
Delvi Yolanda ◽  
...  
Keyword(s):  
Reaction Time ◽  
Palm Oil ◽  
Catalyst Activity ◽  
Bet Surface Area ◽  
Molar Ratio ◽  
Solid Catalyst ◽  
X Ray Diffraction ◽  
Magnetite Fe3o4 ◽  
Biodiesel Synthesis ◽  
Eggshell Waste

In this work, calcium oxide (CaO) extracted from eggshell impregnated with magnetite (Fe3O4) is prepared successfully and it had been applied on transesterification of palm oil off-grade. Prior experiment, the eggshells material are powdered and calcined at 900 °C then impregnated with Fe3O4 and recalcined. The obtained Fe3O4/CaO catalyst is characterized using X-ray diffraction and Braunaeur–Emmet–Teller (BET) surface area. The influence of various parameters including recalcined time and temperature are investigated. The prepared catalyst is tested for transesterification of palm oil off-grade to produce biodiesel in which the optimal conditions of a methanol/palm oil off-grade molar ratio of 10:1, the catalyst weight of 6%, the reaction temperature of 70 °C, and the reaction time of 2 h. The transesterification product was analyzed using GC-MS, which showed the biodiesel yield of 90% at the recalcined temperature of 600 °C and reaction time of 2 h. It has been noted that the catalyst activity is achieved when the moderate recalcination temperature is applied and the disordered structure of the catalyst is maintained. This study also confirms that CaO impregnated with Fe3O4 could be a solid catalyst for the biodiesel synthesis through transesterification reaction of palm oil off-grade.

The Catalytic Performance of Sol-Gel Alumina Supported Ti-Ce Catalysts for H2S Selective Oxidation to Elemental Sulfur

2018 ◽  
Vol 17 (5) ◽  
Author(s):  
H. Mehmet Tasdemir ◽  
Yavuz Yagizatli ◽  
Sena Yasyerli ◽  
Nail Yasyerli
Keyword(s):  
Reaction Time ◽  
Selective Oxidation ◽  
Elemental Sulfur ◽  
Sol Gel ◽  
Lewis Acidity ◽  
Molar Ratio ◽  
Feed Ratio ◽  
Impregnation Method ◽  
Durability Test ◽  
Adsorption Desorption

Abstract In this study, alumina supported Ti-Ce catalysts (10 % by weight and Ti/Ce molar ratio is 4:1) were prepared by using wet impregnation method and their catalytic activities were tested in H2S selective oxidation to elemental sulfur. The support alumina was synthesized by classical (SGC) and modified (SGM) sol-gel methods. The N2 adsorption-desorption, XRD, XPS, EDS and FTIR techniques were used to characterize the synthesized catalysts. The N2 adsorption-desorption isotherms showed that both catalysts have mesoporous structure. Only γ-Al2O3 crystalline phase together with amorphous structure were observed in the XRD patterns. The pyridine adsorbed FTIR analyzes showed that 10 %Ti-Ce@SGC and 10 %Ti-Ce@SGM catalysts have the same Lewis acidity. The activity tests were carried out at 250 °C and with a stoichiometric feed ratio of O2 to H2S being 0.5 for two different reaction times as 150 and 510 min. Complete conversion of H2S was obtained during 180 min. and 330 min. of reaction time over 10 %Ti-Ce@SGC and 10 %Ti-Ce@SGM, respectively. However, all catalysts showed very high sulfur selectivity. Sulfur deposition was detected over 10 %Ti-Ce@SGC catalyst both 150 and 510 min. of reaction time while it was observed after 510 min. of durability test over 10 %Ti-Ce@SGM catalyst. This can be the reason for the earlier loss of catalytic activity 10 %Ti-Ce@SGC than 10 %Ti-Ce@SGM.

Esterification of glycerol with acetic acid using a sulfonated polyphenylene sulfide non-woven fabric as a catalyst

2020 ◽  
Vol 18 (12) ◽  
Author(s):  
Xueyang Li ◽  
Jiao Zhang ◽  
Yunfei Song ◽  
Yanhong Ji ◽  
Mohammad Younas ◽  
...  
Keyword(s):  
Acetic Acid ◽  
Reaction Time ◽  
Reaction Temperature ◽  
Polyphenylene Sulfide ◽  
Woven Fabric ◽  
Molar Ratio ◽  
Solid Catalyst ◽  
Glycerol Conversion ◽  
Good Catalytic Activity ◽  
Reaction Cycles

AbstractIn this work, the esterification of glycerol with acetic acid (HOAc) was investigated under sulfonated polyphenylene sulfide non-woven fabric (SPSF) as a solid catalyst. The effects of the amount of catalyst, reaction temperature, molar ratio of glycerol to HOAc and the reaction time on the esterification were studied in detail. It was found that SPSF has good catalytic activity and stability. Under the reaction conditions of the molar ratio of glycerol/HOAc of 1:6 (glycerol 0.1 mol), the reaction temperature of 110 °C, the amount of catalyst of 3 g, and the reaction time of 2 h, the glycerol conversion and the selectivity to diacetin (DAG) reached upto 96 and 56.1%, respectively. Reusability test of SPSF showed that no significant declination in the glycerol conversion and the selectivity was observed after five reaction cycles. The experimental results proved the esterification of glycerol with HOAc by SPSF a promising and green process.

scholarly journals OPTIMIZING REACTION CONDITIONS OF BIODIESEL PRODUCTION FROM WASTE COOKING OIL USING GREEN SOLID CATALYST

2020 ◽  
Vol 7 (8) ◽  
pp. 65-71
Author(s):  
I Nengah Simpen ◽  
I Made Sutha Negara ◽  
Sofyan Dwi Jayanto
Keyword(s):  
Reaction Time ◽  
Research Result ◽  
Waste Cooking Oil ◽  
Biodiesel Production ◽  
National Standard ◽  
Molar Ratio ◽  
Solid Catalyst ◽  
Reaction Conditions ◽  
Cooking Oil ◽  
One Step

Biodiesel production from waste cooking oil in two steps reaction of esterification and transesterification is low efficient, due to twice methanol consumption and need more reaction time. Optimizing reaction conditions of CaO as a matrix of solid catalyst prepared from crab shell (green CaO) and modified by K2O/TiO2 for converting waste cooking oil to biodiesel have been carried out. Catalytic process of waste cooking oil to biodiesel took place in one step reaction of esterification and transesterification. The research result showed that optimum conditions in its one step reaction such as methanol to oil molar ratio was 9:1, amount of CaO/K2O-TiO2 catalyst to oil was 5% and reaction time of 60 minutes with biodiesel yield was 88.24%. Physical and chemical properties of biodiesel which produced from one step reaction of esterification and transesterification of waste cooking oil were suitable with Indonesian National Standard (SNI-04-7182-2006) namely density at 40oC of 850 kg/m3, kinematic viscosity at 40oC of 3.32 cSt, water content of 0.046%, iodine number of 59.25 g I2/100g and acid value of 0.29 mg KOH/g. Gas chromatography-mass spectrometry (GC-MS) analysis of biodiesel formed fatty acid methyl esters from conversion of waste cooking oil.

scholarly journals Mixed-Metal Oxide Catalyst for Liquid Phase Benzene Alkylation

2019 ◽  
pp. 217-234
Author(s):  
M. Alhassan ◽  
U. Z. Faruq ◽  
A. Galadima
Keyword(s):  
Reaction Time ◽  
Acid Catalyst ◽  
Product Yield ◽  
Molar Ratio ◽  
Solid Catalyst ◽  
Mixed Metal Oxide ◽  
Absorption Bands ◽  
Molar Ratios ◽  
Stirred Reactor ◽  
Heterogeneous Acid Catalyst

Development of cheaper, active and more ecofriendly heterogeneous acid catalyst is a challenge mitigating the petrochemical industries. CuO-MoO3/ZrO2 solid catalyst was prepared by impregnation using suitable precursor materials supported over zirconia. Upon calcination at 450°C for 2 h and activation (by soaking in 2M H2SO4 for 30 minutes), available techniques were employed for the characterization. The available oxides and minerals in the catalyst were revealed by the XRF and XRD profiles respectively. The catalyst crystallite size (131.6nm) was obtained using the Bragg’s equation from the latter. Thermal analysis showed three weight loss stages between (49.25-152.06°C), (152.06-559.47°C) and (559.47-752.0°C ) while presence of sulphate and zirconia oxides was revealed by the FTIR analysis due to appearance of absorption bands around 1225-980cm-1 and 700-600cm-1 respectively. The catalyst (1wt%) was tested for alkylation in a continuous stirred reactor at 80°C using variable (2:1, 4:1 and 10:1) benzene to 1-decene molar ratios. The effects of reaction time and molar ratios on the selectivity, conversion and yield were determined. The alkylation results showed that the catalyst is highly selective to 1-decylbenzene as low amount of side products was obtained. The product yield and conversion increased with reaction time and benzene /1-decene molar ratio while selectivity decreased with increase in benzene /1-decene molar ratio with time.

scholarly journals Novel Aryl-Imidazolium Ionic Liquids with Dual Brønsted/Lewis Acidity as Both Solvents and Catalysts for Friedel–Crafts Alkylation

2019 ◽  
Vol 9 (22) ◽  
pp. 4743 ◽  
Author(s):  
Che-Hsuan Yang ◽  
Jui-Cheng Chang ◽  
Tzi-Yi Wu ◽  
I-Wen Sun ◽  
Jun-Hao Wu ◽  
...  
Keyword(s):  
Ionic Liquids ◽  
Reaction Time ◽  
Reaction Temperature ◽  
Benzyl Chloride ◽  
Molar Fraction ◽  
Lewis Acidity ◽  
Molar Ratio ◽  
Mesomeric Effect ◽  
Magnetic Ionic Liquids ◽  
Reactant Conversion

Unique tunable aryl-imidazolium magnetic ionic liquids with dual functions as a solvent–catalyst and dual Brønsted–Lewis acidity (B-L MILs) are applied for Friedel–Crafts alkylation without additional solvents. The catalytic properties of these B-L MILs in the Friedel–Crafts alkylation of p-xylene with benzyl chloride are investigated. The various reaction parameters, including the catalyst dosage, reaction time, reaction temperature, molar ratio of reactants, and reusability, are discussed. The results show that the B-L MIL 5c has more excellent product selectivity (>99%) and reactant conversion (>99%) under the following optimum conditions (reaction temperature = 80 °C, reaction time = 0.5 h, molar ratio of p-xylene to benzyl chloride = 6:1, and catalyst 5c dosage = 1.0 mole %) than traditional catalysts reported in the previous literature. Specifically, due to the mesomeric effect between the FeCl4 anion and hydrogen atom at cationic moiety, the catalyst B-L MILs with the molar fraction of FeCl3 equal to 0.5 can be easily recovered and provide satisfactory catalytic activity after being re-used six times.

Application of Coconut-Shell Activated Carbon as Heterogeneous Solid Catalyst for Biodiesel Synthesis

2018 ◽  
Vol 382 ◽  
pp. 280-285 ◽  
Author(s):  
Yano Surya Pradana ◽  
Arif Hidayat ◽  
Agus Prasetya ◽  
Arief Budiman
Keyword(s):  
Activated Carbon ◽  
Catalyst System ◽  
Coconut Shell ◽  
Molar Ratio ◽  
Solid Catalyst ◽  
Oil Crops ◽  
Reaction Conversion ◽  
Biodiesel Synthesis ◽  
Coconut Shell Activated Carbon ◽  
Heterogeneous Solid

Biodiesel is a bio-based fuel for diesel engine synthesized from renewable oils isolated from oil crops or animal. Biodiesel can be produced through transesterification where the process involves a catalyst and an alcohol. The most common catalyst for this process is homogeneous liquid catalyst. However, this catalyst system suffers from environmental problems. In order to eliminate the problem, we developed potassium loaded on coconut-shell activated carbon (K/AC) as heterogeneous solid catalyst which is easily regenerated, leading to more secure and more environmental friendly application. The purpose of the present work is to demonstrate the biodiesel synthesis from palm oil using K/AC catalyst in stirred tank reactor. Reaction variables such as methanol-oil molar ratio and temperature were optimized to reach the highest conversion for 4 hours reaction time. The highest reaction conversion, 26.98%, was obtained at methanol-oil molar ratio of 6:1 and reaction temperature of 60 °C. Furthermore, the value of collision factor, activation energy and standard enthalpy change of reaction obtained are 5.40 x 103dm6.(mol.gcat.min)-1, 16.113 cal/mol and 5499.40 cal/mol, respectively.

scholarly journals CeO2:Mn3O4 Catalytic Micro-Converters Tuned for CH4 Detection Based on Catalytic Combustion under Real Operating Conditions

Materials ◽  
2020 ◽  
Vol 13 (9) ◽  
pp. 2196
Author(s):  
Cristian E. Simion ◽  
Ovidiu G. Florea ◽  
Mihaela Florea ◽  
Florentina Neaţu ◽  
Ştefan Neaţu ◽  
...  
Keyword(s):  
Photoelectron Spectroscopy ◽  
Normal Pressure ◽  
Operating Regime ◽  
Operating Conditions ◽  
Molar Ratio ◽  
Atmospheric Conditions ◽  
X Ray ◽  
Temperature Programmed ◽  
Co Precipitation ◽  
Adsorption Desorption

Mesoporous CeO2:Mn3O4 materials (3:7 and 7:3 molar ratio) were prepared by co-precipitation and deposited as porous thick films over alumina (Al2O3) planar substrate provided with Pt meander. The aim was oriented towards detecting low levels methane (CH4) at moderate operating temperatures. Herein we demonstrated that the sensitivity of catalytic micro-converters (CMCs) towards a given peak of CH4 concentration corresponds to specific gas-surface interaction phenomena. More precisely, a transition from thermal conductivity to combustion rate is likely to occur when CMCs are operated under real atmospheric conditions (normal pressure, presence of relative humidity, and constant operating temperature). The response to CH4 was analyzed over different gas flows and different gas concentrations under the same operating regime. The materials were fully characterized by adsorption-desorption isotherms, H2-Temperature Programmed Reduction (H2-TPR), X-ray Diffraction (XRD), X-ray photoelectron spectroscopy (XPS), Scanning Electron Microscopy (SEM), and Raman spectroscopies. Thus, the applicative aspect of using CeO2:Mn3O4 as moderate temperature CMC for CH4 detection is brought to the fore.

scholarly journals Utilization of Electric Arc Furnace Dust as a Solid Catalyst in Biodiesel Production

2021 ◽  
Author(s):  
Khaled El-Araby Khodary ◽  
Marwa Mohamed Naeem ◽  
Mai Hassan Roushdy
Keyword(s):  
Reaction Time ◽  
Reaction Temperature ◽  
Electric Arc ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Energy Sources ◽  
Solid Catalyst ◽  
Arc Furnace ◽  
Reaction Conditions ◽  
Electric Arc Furnace Dust

Abstract World’s energy sources like petrochemical oils, natural gas and coal cause global warming and environmental pollution. Therefore, the traditional energy sources must be replaced by the renewable energy resources. Biodiesel has been recognized as one of the effective, green, renewable and sustainable fuels. This paper investigates the production of biodiesel from sunflower oil by using electric arc furnace dust (EAFD) as a heterogeneous solid catalyst. Four reaction variables i.e. the reaction time, methanol to oil (M:O) molar ratio, reaction temperature, and EAFD loading were chosen to determine their effect on biodiesel production. The effect of the all reaction variables on the biodiesel yield was evaluated using response surface methodology (RSM). A relation has been developed representing the biodiesel conversion as function of all the independent variables. Reaction conditions optimization have been studied for the biodiesel yield maximization and the reaction conditions minimization. The optimum biodiesel yield equals 96 % at reaction temperature of 57 o C, Methanol to oil molar ratio of 20:1, and reaction time of 1h, and EAFD loading of 5%.

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