Synthesis and characterization of reusable heteropoly acid nanoparticles for one step biodiesel production from high acid value waste cooking oil – Performance and emission studies

2020 ◽  
Vol 22 ◽  
pp. 383-392
Author(s):  
Abdul Basheer Sahabdheen ◽  
Anitha Arivarasu
Keyword(s):  
Heteropoly Acid ◽  
Acid Value ◽  
Waste Cooking Oil ◽  
Biodiesel Production ◽  
Performance And Emission ◽  
Cooking Oil ◽  
Oil Performance ◽  
One Step ◽  
Emission Studies

scholarly journals Reusability test of Silica - Titania Catalyst on Biodiesel Production from Waste Cooking Oil in Various Temperatures

2019 ◽  
pp. 116-123
Author(s):  
Fiona Rachma Annisa ◽  
Indang Dewata ◽  
Hary Sanjaya ◽  
Latisma Dj ◽  
Ananda Putra ◽  
...  
Keyword(s):  
Flow Rate ◽  
Acid Value ◽  
Waste Cooking Oil ◽  
Biodiesel Production ◽  
Tetrahedral Coordination ◽  
Cooking Oil ◽  
Used Cooking Oil ◽  
Ftir Characterization ◽  
Density Flow

This work has investigated the reusability of silica-titania in various temperatures (50 – 70°C) of biodiesel production from waste cooking oil. The reused silica-titania catalyst collected from silica-titania catalyst waste produced from the process of separating the catalyst from biodiesel products from palm oil and used cooking oil at various temperatures. The 1st and 2nd reused SiO2-TiO2 were characterized by DR UV-Vis and the spectra were deconvoluted for calculate the fraction of titanium in tetrahedral coordination. In addition the biodiesel products were characterized using FTIR, and several properties of biodiesel such as density, flow rate and acid value were analyzed in order to get the information about catalytic activity reused SiO2-TiO2. The results show the titanium tetrahedral fraction in reused catalyst (1st) and (2nd) are found to be 24,98% and 24.65%, respectively. The FTIR characterization of biodiesel products and waste cooking oil are almost similar. The analysis of waste cooking oil converted to biodiesel shows an optimum temperature of 50oC that at this temperature the lowest density or highest flow rate gave highest conversion of 47.82% using BCR1 and 39.13% using BCR2.

scholarly journals Production and Utilization of Useful Fuel from Waste Cooking Oil and Waste Lubrication Oil: Performance and Emission-Quality in a Naturally Aspirated Diesel Engine

2020 ◽  
Vol 9 (9) ◽  
pp. 79-84
Keyword(s):  
Diesel Engine ◽  
Calorific Value ◽  
Alternative Fuel ◽  
Waste Cooking Oil ◽  
Biodiesel Production ◽  
Attractive Alternative ◽  
Performance And Emission ◽  
Cooking Oil ◽  
Lubrication Oil ◽  
Oil Performance

Increase in the demand for the alternative fuel for diesel engine as led to quest for feasible fuel with competitive cost and environmental friendly compared to petrolium fuel. This article deals on waste energy recovery. The aim of this experimental work is to find an attractive alternative fuel for the diesel engine by harnessing fuel from waste disposed oils. Waste Cooking Oil (WCO) and Waste Lubrication Oil (WLO) energy sources are used for fuel production. Collected WCO stored in a container, mixed and cleansed by removing solidified fats and other food leftovers before the transesterification. The acid followed by base catalyst transesterification processes carried out for biodiesel production. The WLO oil cannot be used directly in diesel engine and hence it is processed to be used like DLF using pyrolitic vacuum distillation method. The characteristics test such as flash point, fire point, density; viscosity and calorific value of the produced biodiesel, DLF, B10, B20, B30 and B40 were determined & compared with standards. Performance and Emission characteristics conducted in a single cylinder, free aspirated, water- cooled computerized diesel engine setup and results discussed. Results outcome shows that B30 exhibits the similar performance as pure diesel. The results show an improvement in brake specific fuel consumption, thermal efficiency. The unburned hydrocarbons, carbon monoxide emissions less but increase in the NOx.

scholarly journals Production of Biodiesel from High Acid Value Waste Cooking Oil Using an Optimized Lipase Enzyme/Acid-Catalyzed Hybrid Process

2009 ◽  
Vol 6 (s1) ◽  
pp. S485-S495 ◽  
Author(s):  
N. Saifuddin ◽  
A. Z. Raziah ◽  
H. Nor Farah
Keyword(s):  
Acid Value ◽  
Reaction Rates ◽  
Waste Cooking Oil ◽  
Biodiesel Production ◽  
Hybrid Process ◽  
Initial Reaction ◽  
Cooking Oil ◽  
High Acid ◽  
Lipase Enzyme ◽  
Acid Catalyzed

The present study is aimed at developing an enzymatic/acid-catalyzed hybrid process for biodiesel production using waste cooking oil with high acid value (poor quality) as feedstock. Tuned enzyme was prepared using a rapid drying technique of microwave dehydration (time required around 15 minutes). Further enhancement was achieved by three phase partitioning (TPP) method. The results on the lipase enzyme which was subjected to pH tuning and TPP, indicated remarkable increase in the initial rate of transesterification by 3.8 times. Microwave irradiation was found to increase the initial reaction rates by further 1.6 times, hence giving a combined increase in activity of about 5.4 times. The optimized enzyme was used for hydrolysis and 88% of the oil taken initially was hydrolyzed by the lipase. The hydrolysate was further used in acid-catalyzed esterification for biodiesel production. By using a feedstock to methanol molar ratio of 1:15 and a sulphuric acid concentration of 2.5%, a biodiesel conversion of 88% was obtained at 50 °C for an hour reaction time. This hybrid process may open a way for biodiesel production using unrefined and used oil with high acid value as feedstock.

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.

Ultrasonic-assisted biodiesel production from waste cooking oil over novel sulfonic functionalized carbon spheres derived from cyclodextrin via one-step: a way to produce biodiesel at short reaction time

RSC Advances ◽  
2015 ◽  
Vol 5 (68) ◽  
pp. 55252-55261 ◽  
Author(s):  
Panya Maneechakr ◽  
Jittima Samerjit ◽  
Surachai Karnjanakom
Keyword(s):  
Catalytic Activity ◽  
Reaction Time ◽  
Waste Cooking Oil ◽  
Biodiesel Production ◽  
High Catalytic Activity ◽  
Carbon Spheres ◽  
Short Reaction Time ◽  
Cooking Oil ◽  
Ultrasonic Assisted ◽  
One Step

A novel sulfonated carbon derived from cyclodextrin showed high catalytic activity for the ultrasonic-assisted transesterification of waste cooking oil.

scholarly journals Multi-Feedstocks Biodiesel Production from Esterification of Calophyllum inophyllum Oil, Castor Oil, Palm Oil and Waste Cooking Oil

2020 ◽  
Vol 9 (1) ◽  
pp. 119-123
Author(s):  
H Hadiyanto ◽  
Apsari Puspita Aini ◽  
Widayat Widayat ◽  
Kusmiyati Kusmiyati ◽  
Arief Budiman ◽  
...  
Keyword(s):  
Vegetable Oils ◽  
Palm Oil ◽  
Ricinus Communis ◽  
Acid Value ◽  
Waste Cooking Oil ◽  
Raw Material ◽  
Biodiesel Production ◽  
Molar Ratio ◽  
Calophyllum Inophyllum ◽  
Cooking Oil

Biodiesel can be produced from various vegetable oils and animal fat. Abundant sources of vegetable oil in Indonesia, such as Calophyllum inophyllum, Ricinus communis, palm oil, and waste cooking oil, were used as raw materials. Multi-feedstock biodiesel was used to increase the flexibility operation of biodiesel production. This study was conducted to determine the effect of a combination of vegetable oils on biodiesel characteristics. Degumming and two steps of esterification were applied for high free fatty acid feedstock before trans-esterification in combination with other vegetable oils. Potassium hydroxide was used as a homogenous catalyst and methanol as another raw material. The acid value of C. inophyllum decreased from 54 mg KOH/gr oil to 2.15 mg KOH/gr oil after two steps of esterification. Biodiesel yield from multi-feedstock was 87.926% with a methanol-to-oil molar ratio of 6:1, temperature of 60 ℃, and catalyst of 1%wt. ©2020. CBIORE-IJRED. All rights reserved

scholarly journals Characterization of Biodiesel from Alkaline Refinement of Waste Cooking Oil

2020 ◽  
Vol 10 (1) ◽  
pp. 16-24
Author(s):  
Aliru Olajide Mustapha ◽  
Amina Abiola Adebisi ◽  
Bukola Opeyemi Olanipekun
Keyword(s):  
Fatty Acids ◽  
Low Cost ◽  
Waste Cooking Oil ◽  
Biodiesel Production ◽  
Fuel Quality ◽  
Cooking Oil ◽  
Yield And Quality ◽  
American Standard

The waste cooking oil (WCO) is a low cost and prospective feedstock with no competitive food uses for biodiesel production, but the yield and quality have been greatly affected by impurities.  This study examined the chemical and fuel quality of biodiesel of both WCO and alkaline treated WCO.  The transesterification process using the alkaline treated cooking oil (ACO) methanol and sodium hydroxide as catalyst followed the Association of Officials of Analytical Chemists (AOAC) techniques. The pH values between 7.27 and 8.65 were found for alkaline treated cooking methyl ester (ACME), alkaline treated cooking oil (ACO) and WCO. Density of ACME, ACO and WCO varied between 0.89 and 0.93 (g/cm3). The fatty acids found were benzoic acid (3.77%), octanoic acid (8.35%), and palmitic acid (75.02%) – most abundant. Comparison of results with the American Standard for Testing Materials (ASTM) values showed quality enhancements of ACO in physicochemical and fuel properties over WCO. The biodiesels from ACO have enhanced emulsification, fuel and free fatty acids qualities over the WCO, showing the refinement methodology of WCO has overall improvement in the biodiesel purity and quality against the previous conflicting reports.

scholarly journals Enhancement of Biodiesel Production from High-Acid-Value Waste Cooking Oil via a Microwave Reactor Using a Homogeneous Alkaline Catalyst

Energies ◽  
2021 ◽  
Vol 14 (2) ◽  
pp. 437
Author(s):  
Ming-Chien Hsiao ◽  
Peir-Horng Liao ◽  
Nguyen Vu Lan ◽  
Shuhn-Shyurng Hou
Keyword(s):  
Reaction Time ◽  
Reaction Temperature ◽  
Microwave Power ◽  
Acid Value ◽  
Waste Cooking Oil ◽  
Transesterification Reaction ◽  
Biodiesel Production ◽  
Alkaline Catalyst ◽  
Cooking Oil ◽  
High Acid

In this study, low quality oils (waste cooking oils) with high acid value (4.81 mg KOH/g) were utilized as the feedstocks for a transesterification reaction enhanced by additional microwave power and the use of an NaOH catalyst. The kinetics of the transesterification reaction under different reaction times and temperatures was studied. It was found that in the microwave-assisted transesterification reaction, the optimum conditions under a microwave power of 600 W were as follows: an NaOH catalyst of 0.8 wt %, a 12:1 molar ratio of methanol to oil, a reaction time of 2 min, and a reaction temperature of 65 °C. The conversion of waste cooking oil into biodiesel reached 98.2% after this short reaction time. This result conformed to 96.5% of the standard value of Taiwan CNS 15072. In addition, with increases in the reaction temperature from 55 to 65 °C, the reaction rate constant increased from 0.635 to 2.396 min−1, and the activation energy required for the transesterification reaction was 123.14 kJ/mole.

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