A novel phosphonium-based deep eutectic catalyst for biodiesel production from industrial low grade crude palm oil

2013 ◽  
Vol 92 ◽  
pp. 81-88 ◽  
Author(s):  
Adeeb Hayyan ◽  
Mohd Ali Hashim ◽  
Farouq S. Mjalli ◽  
Maan Hayyan ◽  
Inas M. AlNashef
2013 ◽  
Vol 11 (2) ◽  
pp. 129-140 ◽  
Author(s):  
Adeeb Hayyan ◽  
Farouq S. Mjalli ◽  
Mohd Ali Hashim ◽  
Maan Hayyan ◽  
Inas M. AlNashef ◽  
...  

2008 ◽  
Vol 8 (1 & 2) ◽  
pp. 1 ◽  
Author(s):  
Satriana Satriana ◽  
Muhammad Dani Supardan

The kinetics of the esterification of free fatty acids (FFA) in low grade crude palm oil (CPO) with methanol was studied. In this work, the effects of operational variables involved in the esterification process i.e. alcohol to oil molar ratio, reaction temperature, agitation speed and the initial amount of FFA of oil, were studied in the presence of sulphuric acid as catalyst at concentration of 1%-w. The experimental results show that the esterification process could lead to a practical and cost effective FFA removal unit in front of typical oil transesterification for biodiesel production. The experimental results were found to fit a first-order kinetic law. The influence of temperature on the kinetic constants was determined by fitting the results to the Arrhenius equation.


2014 ◽  
Vol 917 ◽  
pp. 87-95 ◽  
Author(s):  
Suliana Abu Bakar ◽  
Suzana Yusup ◽  
Murni Melati Ahmad ◽  
Armando T. Quitain ◽  
Mitsuru Sasaki ◽  
...  

The production of biodiesel from crude palm oil (CPO) using microwave technique is investigated and has been compared with conventional heating. Two-step biodiesel production process is applied to maximize the highest biodiesel yield in short reaction time using microwave method. Sulfuric acid (H2SO4) as acid catalysts is used in pre-treatment of feedstock by esterification process followed by potassium hydroxide (KOH) as base catalyst for transesterification process with low methanol to oil ratio. The main purpose of the pre-treatment process is to reduce the free fatty acids (FFA) content of CPO from higher value of FFA content (>6.8%) to a minimum level for biodiesel production (<1%). Esterification and transesterification is carried out in fully instrumented and controlled microwave reactor system to get higher yield in shorter time. This two-step esterification and transesterification process showed that the maximum conversion of palm biodiesel obtained is 95.1% with the process conditions of methanol-to-oil molar ratio of 6:1, reaction temperature 65oC, reaction time 15min, and 2% (wt/wt) KOH amount using microwave method compared to conventional heating where the palm oil methyl ester (POME) yield obtained is 81% at the same conditions. The result showed that, the biodiesel production using microwave technique proved to be a fast and easy route to get high yields of biodiesel.


2019 ◽  
Vol 3 (4) ◽  
pp. 340
Author(s):  
Adi Fitra Andikos ◽  
Helly Andri

 The role of oil and gas business in Indonesia has always influenced the source of revenue from the country and energy sources for the national economy. In the 1970 's to the 1990 's and mid-1990 's, it was characterized by the high dependence of the national economy on oil and gas revenues, triggering massive oil and gas-producing. Currently, Indonesia is the largest palm oil producer and exporter in the world. Palm oil is one of the roads to overcome the problem of petroleum in Indonesia. To commercialize plants is still constrained because the availability of low raw material costs very hard to get. The amalgamation of crude palm oil and crude palm sludge is one of the problems of raw materials for renewable energy production. This low-level oil has great potential as a raw material for biodiesel production. To get the maximum quality mixing required a computer method. The method used in this study is analysis study with the Association classification approach by testing Improved Apriori algorithm in mining palm oil dataset. In this research using Data Mining application so that can be used to display the information of quality improvement of palm oil acid with high quality as a biodiesel base where the information is seen from the value of support and Confidence between items. M-Apriori algorithm can not read the continous data, so it must be done transformation first, one of them using the help of discreetization technique. Crude palm oil acid type esteridication which is fatty acid levels > 60 and Abu bunches 51-100 g/mol then the quality of biodiesel with the result of rising methyl Ester increases by as much as 100% (confidence: 1). From data that is calculated manually, no relationship is found Association.


2009 ◽  
Vol 9 (17) ◽  
pp. 3166-3170 ◽  
Author(s):  
A.N. Alkabbashi ◽  
Md Z. Alam ◽  
M.E.S. Mirghani ◽  
A.M.A. Al-Fusaiel

2021 ◽  
Author(s):  
Adeeb Hayyan ◽  
Andrew Yeow Tze Hao ◽  
Nashwan Abdullah Mohammed Alkahli ◽  
Jehad Saleh ◽  
Ahmaad Kadmouse Aldeehani ◽  
...  

2016 ◽  
Vol 26 (5) ◽  
pp. 3-10 ◽  
Author(s):  
María del Consuelo Ortiz Tapia ◽  
Pedro García Alamilla ◽  
Laura Mercedes Lagunes Gálvez ◽  
María Isabel Arregoitia Quezada ◽  
Ricardo García Alamilla ◽  
...  

2014 ◽  
Vol 61 ◽  
pp. 2745-2749 ◽  
Author(s):  
Adeeb Hayyan ◽  
Mohd Ali Hashim ◽  
Maan Hayyan ◽  
Khor Gui Qing

2014 ◽  
Vol 875-877 ◽  
pp. 1687-1692 ◽  
Author(s):  
Krit Somnuk ◽  
Gumpon Prateepchaikul

Biodiesel from a high free fatty acid (FFA) mixed crude palm oil (MCPO) can be produced to high fatty acid methyl ester (FAME) conversion by a two-step process. The first process is an acid-catalyzed esterification to reduce FFA in oil followed by a base-catalyzed transesterification process to produce biodiesel from esterified oil. In this study, the transesterification of esterified oil with methanol in the presence of potassium hydroxide (KOH) was performed in a 1,000 W ultrasonic homogenizer at a low frequency of 18 kHz. The use of high-intensity ultrasound to accelerate the reaction, the high surface power density of 1.62 W.mm-2 and the volumetric acoustic energy of 20 W.mL-1 were fixed. The objective of this study was to determine the various parameters (methanol concentration, KOH concentration, and initial temperature of oil) to produce the FAME conversion. The results showed that over 98 wt.% of FAME could be achieved with 5 g KOH/liter of oil, 15 vol.% of methanol, the total residence time of 20 seconds, and temperature of 30 oC. Moreover, the glycerides were rapidly converted to the FAME within reaction time of 10 seconds when the base-catalyst of 10 g KOH/liter of oil, and 20 vol.% of methanol were used. Consequently, the use of high-intensity ultrasonic irradiation can minimize the chemical cost, electricity cost, and reaction time.


Sign in / Sign up

Export Citation Format

Share Document