Enzymatic production of xylose esters using degummed soybean oil fatty acids following a hydroesterification strategy

被引:3
|
作者
Miranda, Felipe Cardoso [1 ]
Oliveira, Kaique Souza Goncalves Cordeiro [2 ]
Tardioli, Paulo Waldir [3 ]
Fernandez-Lafuente, Roberto [4 ]
Guimaraes, Jose Renato [1 ]
机构
[1] Univ Fed Itajuba, Inst Nat Resources, Av Benedito Pereira dos Santos 1303, BR-37500903 Itajuba, MG, Brazil
[2] Fed Inst Educ Sci & Technol South Minas Gerais, Dept Chem Engn, Av Maria da Conceicao Santos 900, BR-37560260 Pouso Alegre, MG, Brazil
[3] Univ Fed Sao Carlos, Dept Chem Engn, Rod Washington Luis,Km 235, BR-13565905 Sao Carlos, SP, Brazil
[4] Inst Catalysis & Petrochem ICP CSIC, Dept Biocatalysis, Campus UAM CSIC, Madrid 28049, Spain
基金
巴西圣保罗研究基金会;
关键词
Degummed soybean oil; Lipase catalyzed hydrolysis and esterification; Experimental design; Xylose fatty acid esters; Emulsifying properties; LIPASE-CATALYZED SYNTHESIS; CANDIDA-ANTARCTICA LIPASE; THERMOMYCES-LANUGINOSUS; INTERFACIAL ACTIVATION; IMMOBILIZED LIPASE; MOLECULAR-SIEVES; FRUCTOSE ESTERS; CROSS-LINKING; ESTERIFICATION; ULTRASOUND;
D O I
10.1016/j.procbio.2024.04.020
中图分类号
Q5 [生物化学]; Q7 [分子生物学];
学科分类号
071010 ; 081704 ;
摘要
The enzymatic synthesis of xylose fatty acid esters was carried out in two steps: hydrolysis of degummed soybean oil (DSO) and esterification of the produced and purified free fatty acids (FFA) with xylose. Different lipases immobilized on a hydrophobic support were evaluated in the hydrolysis of DSO and an experimental design was used to optimize the reaction. Eversa (R) Transform 2.0 (EV-Purolite) yielded 93% conversion after 6 h using biocatalyst load of 6.53 wt%, water/oil mass ratio of 5.5 and temperature of 48.4 degrees C. High operational stability for EV-Purolite was found using a sequential batch strategy and the possibility of concentrating glycerol. In the esterification stage, lipase from Thermomyces lanuginosus (TLL-Purolite) and lipase B from Candida antarctica showed better performance than lipase from porcine pancreas and EV-Purolite. About 17% of FFAs (0.85 molecules of FAA per xylose molecule) was consumed using an enzyme load of 5 wt% of TLL-Purolite and FFA/xylose molar ratio of 5. Sequential esterification batches showed low operational stability of TTL-Purolite due to the desorption of TLL from the support. The final mixture of the reaction medium containing xylose fatty acid esters showed emulsifying properties similar to those of commercial surfactant.
引用
收藏
页码:104 / 112
页数:9
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