Synthesis of amine imprinted manganese ferrite and its application in the removal of free fatty acid from waste vegetable oil

2020 ◽  
Vol 21 ◽  
pp. 100715
Author(s):  
Adewale Adewuyi ◽  
Adedoyin A Yusuf ◽  
Woei Jye Lau ◽  
Mirabbos Hojamberdiev ◽  
Rotimi A Oderinde
Life ◽  
2021 ◽  
Vol 11 (11) ◽  
pp. 1197
Author(s):  
Mayara S. Rodrigues ◽  
Rafaela M. Dos Passos ◽  
Paula V. de A. Pontes ◽  
Marcela C. Ferreira ◽  
Antonio J. A. Meirelles ◽  
...  

Rice bran oil is a highly nutritious vegetable oil, as it is rich in tocols and γ-oryzanol. Degumming is the first step in the vegetable oil refining process, and its main objective is the removal of phospholipids or gums. In the present study, enzymatic degumming trials were performed on crude rice bran oil using the phospholipases PLA1, Purifine® PLC, their mixture (PLA1/PLC), and a cocktail known as Purifine® 3G. Enzymatic degumming applying 50 mg/kg of PLA1 for 120 min resulted in a residual phosphorus content of 10.4 mg/kg and an absolute free fatty acid increase of 0.30%. Enzymatic degumming applying 300 mg/kg of Purifine® PLC for 120 min at 60 °C resulted in a residual phosphorus content of 67 mg/kg and an absolute diacylglycerol increase of 0.41%. The mixture of phospholipases and the cocktail presented approximately 5 mg/kg of residual phosphorus content after the reaction times. For all degumming processes, the preservation of minor components such as tocols and γ-oryzanol were observed. These results indicate that the use of enzyme mixtures or their cocktails to attain low phosphorus content and high diacylglycerol/free fatty acid conversion during enzymatic degumming is a viable alternative.


2017 ◽  
Vol 160 ◽  
pp. 355-363 ◽  
Author(s):  
Olli-Pekka Lehtinen ◽  
Robertus Wahyu N. Nugroho ◽  
Tuula Lehtimaa ◽  
Sampsa Vierros ◽  
Panu Hiekkataipale ◽  
...  

2018 ◽  
Vol 870 ◽  
pp. 116-120 ◽  
Author(s):  
Yiqiang Deng ◽  
Xiaojian Hu ◽  
Lihua Cheng ◽  
Hanlu Wang ◽  
Linhai Duan ◽  
...  

Production of biodiesel from triglycerides (vegetable oil) is usually done through transesterification with alcohols in the presence of acid or base catalyst. When this oil contains free fatty acid of more than 5 percent due to repeated use for frying, the transesterification process can not be used to produce biodiesel. In this paper, a new method for producing biodiesel even for used vegetable containing higher or any amount of free fatty acid is discussed. This method involves complete saponification of the triglycerides and free fatty acids (FFA) by reacting it with sodium hydroxide solution to give sodium salt of fatty acid (SOAP). This soap when treated with a mineral acid, separates into four layers, the top layer which is also the primary layer is the free fatty acid (FFA), the second layer is the glycerol, the third layer is the water layer, and the bottom layer is the residue of solid sodium salt. The top layer free fatty acid(FFA) is easily separated and then esterified with ethanol in the presence of a mineral acid as a catalyst to get the biodiesel (ethyl ester of FFA). The product obtained by the above process is analyzed and confirmed by FT-IR spectra. This process does not involve high temperature and pressure. The advantages of this new process are that it is much environmentally friendly compared with any other methods of production of biodiesel with less processes time. Since the washing of biodiesel to remove the soap formed due to the presence of free fatty acid content in the feedstock is completely eliminated, there will be no effluent discharge to the environment and at the same time resulting in more yield. The significance of this method is that it can be used to obtain biodiesel from used vegetable oils, raw vegetable oil and tallows and especially for any feedstock material which contains any amount of free fatty acids.


Langmuir ◽  
2019 ◽  
Author(s):  
Paavo A. Penttilä ◽  
Sampsa Vierros ◽  
Katja Utriainen ◽  
Nico Carl ◽  
Lauri Rautkari ◽  
...  

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