Simultaneous production of oil enriched in ω-3 polyunsaturated fatty acids and biodiesel from fish wastes

被引:23
作者
Enascuta, Cristina Emanuela [1 ,3 ]
Stepan, Emil [1 ]
Bolocan, Ion [2 ]
Bombos, Dorin [2 ]
Calin, Catalina [2 ]
Oprescu, Elena-Emilia [1 ,2 ]
Lavric, Vasile [3 ]
机构
[1] Natl Res & Dev Inst Chem & Petrochem ICECHIM, 202 Splaiul Independentei St,POB 194, Bucharest 060021, Romania
[2] Petr Gas Univ Ploiesti, 39 Bucharest Blvd, Ploiesti 100680, Romania
[3] Univ Politehn Bucuresti, Fac Appl Chem & Mat Sci, 1-7 Polizu St, Bucharest 011061, Romania
关键词
Fish waste; Heterogeneous catalyst; Molecular rectification; Mathematical modeling; omega-3 Polyunsaturated fatty acids esters; Fatty acid ethyl esters; ETHYL-ESTERS; ESTERIFICATION; TRANSESTERIFICATION; MICROALGAE; STABILITY; OXIDES;
D O I
10.1016/j.wasman.2018.01.022
中图分类号
X [环境科学、安全科学];
学科分类号
08 ; 0830 ;
摘要
The waste resulted from fish processing industries are discarded into the environment around the world, causing environmental pollution. The main problem of fish oil extracted from waste is the high content in free fatty acids (FFA) which decrease the yield in fatty acids esters during transesterification reactions. Therefore, to correct the fish-oil properties, a new environmentally friendly heterogeneous superacid catalyst (SO42-/SnO2-ZrO2) was tested in the esterification reaction of FFA with ethanol. The catalyst was characterized by different techniques (XRD, FT-IR FT-IR of adsorbed pyridine, BET, SEM-EDX, TGA and acidity measurements). The reaction was found to follow a Langmuir-Hinshelwood (L-H) dual-site mechanism with the novelty that both Bronsted and Lewis acid centers participate equally in the esterification reaction. The pre-treated oil was subjected to transesterification reaction with ethanol over a heterogeneous base catalyst and then, the saturated and unsaturated fractions of fatty acid ethyl esters (FAEE) were separated using a vacuum rectification unit with falling film. The saturated content can be used as biofuel, while the unsaturated FAEE are further transesterified with glycerol in order to obtain oil with high content in polyunsaturated fatty acids (PUFA). A detailed study of the intrinsic kinetic process at the surface of the superacid catalyst and a thorough mathematical model of the fixed bed reactor were written and validated by an experimental program, designed according to the D-optimal methodology. (C) 2018 Elsevier Ltd. All rights reserved.
引用
收藏
页码:205 / 214
页数:10
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