Biodiesel Production from Transesterification with Lipase from Pseudomonas cepacia Immobilized on Modified Structured Metal Organic Materials

被引:7
作者
Gil, Jose Manuel Martinez [1 ,2 ,3 ,4 ]
Reyes, Ricardo Vivas [2 ]
Bastidas-Barranco, Marlon [3 ]
Giraldo, Liliana [5 ]
Moreno-Pirajan, Juan Carlos [4 ]
机构
[1] Univ La Guajira, Grp Invest Catalisis & Mat, Fac Ciencias Basicas & Aplicadas, Riohacha 440007, Colombia
[2] Univ Cartagena, Fac Ciencias Exactas & Nat, Grp Invest Quim Cuantica & Teor, Cartagena 30005, Colombia
[3] Univ La Guajira, Grp Invest Desarrollo Estudios & Tecnol Ambiental, Fac Ingn, Riohach A440007, Colombia
[4] Univ Andes, Fac Ciencias, Dept Quim, Grp Invest Solidos Porosos & Calorimetria, Bogota 01, Colombia
[5] Univ Nacl Colombia, Fac Ciencias, Dept Quim, Grp Calorimetria,Sede Bogota 01, Bogota, Colombia
来源
ACS OMEGA | 2022年 / 7卷 / 46期
关键词
ZEOLITIC IMIDAZOLATE FRAMEWORK-8; ROOM-TEMPERATURE SYNTHESIS; WALLED CARBON NANOTUBES; MAGNETIC NANOPARTICLES; PALM OIL; CATALYZED TRANSESTERIFICATION; DIRECT CARBONIZATION; NANOPOROUS CARBONS; ZIF-8; NANOCRYSTALS; FACILE SYNTHESIS;
D O I
10.1021/acsomega.2c02873
中图分类号
O6 [化学];
学科分类号
0703 ;
摘要
This research presents the modification of MOF-199 and ZIF-8 using furfuryl alcohol (FA) as a carbon source to subsequently fix lipase from Pseudomonas cepacia and use these biocatalysts in the transesterification of African palm oil (APO). The need to overcome the disadvantages of free lipases in the biodiesel production process led to the use of metal organic framework (MOF)-type supports because they provide greater thermal stability and separation of the catalytic phase, thus improving the activity and efficiency in relation to the use of free lipase, disadvantages that could not be overcome with the use of other types of catalysts used in transesterification/esterification reactions for the production of biodiesel. The modification of MOFs ZIF-8 and MOF-199 with FA increases the pore volume which allows better immobilization of Pseudomonas cepacia lipase (PCL). The results show that these biocatalysts undergo transesterification with biodiesel yields above 90%. Additionally, studies were carried out on the effect of (1) enzyme loading, 2) enzyme immobilization time, (3) enzyme immobilization temperature, and (4) pH on the % immobilization of the enzyme and the specific activity. The results show that the highest immobilization efficiency for the FA@ZIF-8 support has a value of 91.2% when the load of this support was 3.5 mg/mg and has a specific activity of 142.5 U/g protein. The FA@MOF-199 support presented 80.3% enzyme immobilization and 125% U/g specific activity protein. We established that the specific activity increases in the period from 0.5 to 5.0 h for the systems under investigation. After this time, both the specific activity and the % efficiency of enzyme immobilization decrease. Therefore, 5.0 h (immobilization efficiency of 95 and 85% for FA@MOF-199, respectively) was chosen as the most appropriate time for PCL immobilization. Methods of adding methanol, with three and four steps, were tested, where biodiesel yields greater than 90% were obtained for the biocatalysts synthesized in this work (FA@ZIF-8-PCL and FA@MOF-199-PCL) and above 70% for free PCL, and the maximum yield was reached at a molar ratio between methanol and APO of 4:1 when using the one-step method under the same reaction conditions (as mentioned above). Only the results of FA@ZIF-8-PCL are presented here; however, it should be noted that the results for biocatalyst FA@MOF-199-PCL and lipase-free PCL presented the same behavior. The order of biocatalyst performance was FA@ZIF-8-PCL > FA@MOF-199-PCL > PCL-Free, which demonstrates that the use of FA as a modifier is a novel aspect in the conversion of palm oil into biodiesel components.
引用
收藏
页码:41882 / 41904
页数:23
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