Lipase-Catalyzed Synthesis of Cocoa Butter Equivalent from Palm Olein and Saturated Fatty Acid Distillate from Palm Oil Physical Refinery

2012 ◽  
Vol 168 (6) ◽  
pp. 1405-1415 ◽  
Author(s):  
Ibrahim O. Mohamed
Keyword(s):  
Fatty Acid ◽  
Cocoa Butter ◽  
Saturated Fatty Acid ◽  
Palm Oil ◽  
Palm Olein ◽  
Cocoa Butter Equivalent ◽  
Fatty Acid Distillate

OPTIMIZATION OF COCOA BUTTER EQUIVALENT PRODUCTION FROM FORMULATED HARD PALM OIL MID-FRACTION AND CANOLA OIL BLENDS

2016 ◽  
Vol 78 (6-12) ◽  
Author(s):  
Reiza Mutia ◽  
Dayang Norulfairuz Abang Zaidel ◽  
Ida Idayu Muhamad
Keyword(s):  
Fatty Acid ◽  
Linoleic Acid ◽  
Reaction Time ◽  
Cocoa Butter ◽  
Linolenic Acid ◽  
Palm Oil ◽  
Canola Oil ◽  
Cocoa Butter Equivalent ◽  
Omega 3 ◽  
Omega 6

The study to find cocoa butter equivalent (CBE) as an alternative to cocoa butter (CB) from available and low cost commercial oils or fats has been increased recently. Current study investigates the blending of hard palm oil mid-fraction (PMF) with canola oil to produce high nutritional CBE using immobilized lipase from Rhizomucor miehei. The experiments were designed using Response Surface Methodology (RSM) to optimize the percentage of saturated-unsaturated-saturated (StUSt) triacylglycerols (TAGs). The experiment was performed at hard PMF concentration of 50 to 90% (w/w), lipozyme load between 5% and 10% (based on the weight of substrate) with a reaction time between 2 to 14 hours. The best reaction conditions to attain this target was 89.35% (w/w) of hard PMF concentration, 2 hours of reaction time, and 5% (based on the weight of substrate) of lipozyme load, resulting CBE which contains 64.44±1.18% of StUSt. The addition of canola oil improved the nutritional value of CBE which was marked by the higher percentage of linoleic acid (omega-6, 4.53±0.06%) and linolenic acid (omega-3, 0.74±0.14%) in CBE than CB (omega-6, 2.68±0.34%). Enzymatic interesterification was not altering fatty acid content in the CBE, especially linoleic acid (omega-6) and linolenic acid (omega-3) which was characterized by no significant difference (p > 0.05) between the fatty acid profile of initial mixture (before interesterification) and CBE (after interesterification).

scholarly journals An Intensified Esterification Process of Palm Oil Fatty Acid Distillate Catalyzed by Delipidated Rice Bran Lipase

2006 ◽  
Vol 6 ◽  
pp. 1124-1131 ◽  
Author(s):  
Fui Chin Chong ◽  
Beng Ti Tey ◽  
Zanariah Mohd. Dom ◽  
Nordin Ibrahim ◽  
Russly Abd. Rahman ◽  
...  
Keyword(s):  
Fatty Acid ◽  
Rice Bran ◽  
Reaction Temperature ◽  
Palm Oil ◽  
Packed Bed ◽  
Packed Bed Reactor ◽  
Silica Gels ◽  
Water Removal ◽  
Rice Bran Lipase ◽  
Fatty Acid Distillate

An intensified esterification process was operated by circulating 10 l of reaction mixtures, consisting of palm oil fatty acid distillate (PFAD) and glycerol in hexane, through a packed-bed reactor (PBR) filled with 10 kg of delipidated rice bran lipase (RBL). The influence of the process parameters, such as reaction temperature and type of water-removal agent, on the performance of this intensified esterification process were investigated. The highest degree of esterification (61%) was achieved at a reaction temperature of 65°C, using silica gels as the water-removal agent. Thin-layer chromatography (TLC) analysis showed that the major composition of the esterified product was diacylglycerol.

Gasoline Yield Enhancement in Fluid Catalytic Cracking by Coprocessing of Petroleum Gasoil with Refined Bleached Deodorized Palm Oil and Palm Fatty Acid Distillate

2020 ◽  
Vol 17 (2) ◽  
pp. 1079-1084
Author(s):  
Zarkoni Azis ◽  
Bambang Heru Susanto ◽  
Mohammad Nasikin
Keyword(s):  
Gas Chromatography ◽  
Fatty Acid ◽  
Palm Oil ◽  
Catalytic Cracking ◽  
Spark Ignition Engine ◽  
Fluid Catalytic Cracking ◽  
Light Cycle ◽  
Palm Fatty Acid Distillate ◽  
Cracking Reaction ◽  
Fatty Acid Distillate

Gasoline is liquid hydrocarbon fuel used for spark-ignition engine. Most of gasoline production is carried out in the petroleum oil refinery through several stages of process and fluid catalytic cracking (FCC) is an important process that can convert some of heavy oil fractions like vacuum gasoil (VGO) and residue to be cracked into gasoline and lighter products. Consumption of gasoline for transportation fuel in Indonesia is higher than its production capability, so this gap has compelled to search the alternative process route using renewable feedstock. Coprocessing of petroleum gasoil with crude palm oil in fluid catalytic cracking had been investigated previously resulting in lower value of conversion as well as gasoline yield when applying co-feeds at higher level of vegetable oils. Cracking feedstock containing triglyceride and fatty acid from vegetable oil is supposed to be the other possibility as a reason of conversion and yield changes. The research work is aimed to find out another way for gasoline yield upgrading in fluid catalytic cracking process using available catalyst by coprocessing of VGO with refined bleached deodorized palm oil (RBDPO) and small amount of palm fatty acid distillate (PFAD). The experimental work of cracking reaction was performed on fluid-bed reactor of ACE unit at temperature of 530 °C, nearly atmospheric pressure and catalyst-oil ratio of 5.5 g/g. Three kind of oil feeds were tested namely VGO, VGO mixed with 5% RBDPO and VGO added with 5% RBDPO-PFAD of mixing ratio 9:1. The cracking reaction results in gaseous and liquid products. The gaseous phase product was analyzed using online gas chromatography to detect light hydrocarbon components of C1, C2 and H2 as dry gas and hydrocarbon components of C3 and C4 as LPG. The liquid item was investigated through gas chromatography of simulated distillation to separate fluid components including gasoline, light cycle oil (LCO) and slurry oil. Carbon material placed on catalyst through cracking reaction was analyzed at regeneration step of spent catalyst passed through catalytic converter by online Infrared method. Coprocessing of VGO with 5% RBDPO and VGO with 5% RBDPO-PFAD can alter conversion and product yields. The presence of triglyceride and fatty acid in oil feeds during cracking reaction influence signifi- cantly to gasoline enhancement. Although this coprocessing work has shown initial phenomenon in accordance with hypothesis, further investigation is necessary to explore deeper in order to obtain an optimized process condition by various levels of coprocessing feed.

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