Читать книгу Biodiesel Technology and Applications - Группа авторов - Страница 31
1.8 Comparative Analysis of Intracellular and Extracellular Lipases for Biodiesel Production
ОглавлениеTransesterification reaction for biodiesel production is done with both extracellular and intracellular lipases. Preference for their use is dependent upon either we want simple upstream processes as in case of intracellular lipase or high enzymatic conversion as in case of extracellular lipase. But either we use intracellular lipase or extracellular lipase there is no need for some downstream processes including separation and recycling. Further, both immobilized lipase (extracellular) and immobilized whole-cell lipase (intracellular) are proved to have highly efficient when compared with free lipase used for transesterification [165]. Some experimental studies for both intracellular and extracellular lipases are given in Table 1.5. Intracellular lipases are the enzymes present inside the cells or linked to the walls of cells producing it known as whole-cell biocatalysts. They are not purified or separated from their cells and used as a whole-cell for transesterification (whole-cell biocatalyst) or immobilized (whole-cell immobilization) [55]. Rhizopus and Aspergillus which are filamentous fungi are most widely used as whole-cell biocatalyst for transesterification process [166]. As the main issue related to biodiesel production at large scale is cost and the use of intracellular lipase for transesterification resolves this problem like the use of intracellular lipase is considered cost-effective because of the elimination of costly processes of lipase isolation and purification before immobilization which are required in case of extracellular lipase [167]. Intracellular lipase producing cells or whole-cell biocatalysts are directly employed for immobilization without separation and purification steps for lipase enzymes [55]. Porous biomass support particles (BSPs) are mostly used for whole-cell immobilization. BSPs was developed by Atkinson et al. [168] and used by many scientists and each scientist provide an efficient way of immobilization on it giving out a high yield of biodiesel. A study to check the lipolytic activities of Bacillus species using intracellular as well as extracellular lipase showed higher intracellular lipase activity than extracellular lipase activity [169]. Reported whole-cell biocatalysts are Aspergillus oryzae, Burkholderia cepacia, filamentous fungus Rhizopus chinensis, R. oryzae, and Enterococcus faecium [170–174]. Aspergillus oryzae used as whole-cell biocatalyst exhibited 98.1% relative stability after the fourth batch and produced more than 97% FAME in 32 hours. Extracellular lipases are the purified form mainly fungal and bacterial cells for their use in transesterification process.
Table 1.1 Some of the commonly used bacterial lipases for biodiesel production.
Enzyme | Immobilized on | Substrate | Acyl acceptor | Yield | Reference |
---|---|---|---|---|---|
Burkholderia cepacia Lipase | Hydrophobic silica monolith | Jatropha oil | Methanol | 95% | [125] |
Hybrid matrix of alginate and κ-carrageenan | Jatropha curcas L. oil | Ethanol | 100% | [126] | |
κ-carrageenan | Palm oil | Methanol | 100% | [127] | |
Modified attapulgite | Jatropha oil | Methanol | 94% | [128] | |
SiO2-PVA | Babassu oil | Ethanol | 100 % | [129, 130] | |
SiO2-PVA | Babassu oil | Ethanol | 100% | [131] | |
Nb2O5 | Babassu oil | Ethanol | 74.1% | [132] | |
Pseudomonas cepacia Lipase | Epoxy-acrylic resin | Waste vegetable oil | Ethanol | 46–47% | [133] |
Phyllosilicate solgel matrix | restaurant grease | Methanol and Ethanol | 98% | [134] | |
Fe3O4 nanoparticle biocomposite | Soybean oil | Methanol | >88% | [135] | |
Accurel | Madhuca indica | Ethanol | 96% | [136] | |
Protein-coated microcrystals | Soybean oil | Ethanol | 98.93% | [137] | |
Celite | Jatropha oil | Ethanol | 98% | [89] | |
Pseudomonas fluorescence | Octyl-silica resin | Babassu oil | Ethanol | 97.5% | [85] |
Hydrophobic sol-gel | Soybean oil | Methanol | 65% | [138] | |
Porous kaolinite particles | Triolein | Methanol and Ethanol | 90% | [139] | |
Asymmetric membrane | Triolein | Methanol | 80% | [140] |
Table 1.2 Some of the commonly used fungal lipases for biodiesel production.
Enzyme | Immobilized on | Substrate | Acyl acceptor | Yield | Reference |
---|---|---|---|---|---|
Candida antartica Lipase | Activated textile cloth | Waste cooking oil | Methanol | 91.08% | [157] |
Polyurethane foam | Soybean oil | Ethanol | 81% | [158] | |
Acrylic resin | Sunflower oil | Ethyl acetate | 92.7% | [78] | |
Soybean oil | Methanol | 83.31% | [95] | ||
Candida rugosa Lipase | Microporous bio silica-polymer | Scenedesmus quadricauda microalgal oil | Methanol | 96.4% | [59] |
Poly(styrenemethacrylic acid) microsphere | Soybean oil | Methanol | 86% | [159] | |
within an activated carbon as support | Palm oil | Methanol | 70% | [160] | |
Thermomyces lanuginosus Lipase | Olive pomace | Pomace oil | Methanol | 93% | [161] |
Phyllosilicate sol-gel matrix | Grease | Ethanol | 80-90% | [162] | |
Mesoporous polyhydroxybutyrate particles (PHB) | Oleic acid | Methanol and Ethanol | 90% | [163] | |
Toyopearl AF-amino-650M resin | Babassu oil | Ethanol | 86.6% | [164] |
Table 1.3 Some examples commercial lipases commonly used for biodiesel production.
Enzyme | Substrate | Acyl acceptor | Reaction yield | Reference |
---|---|---|---|---|
Novozyme 435 | Chlorella sp. KR-1 | Dimethyl carbonate and methanol mixture | 90% | [145] |
Sunflower oil | Methanol, Absolute ethanol, 1-propanol | >90% | [146] | |
Oleic acid | Ethanol, n-propanol, and n-butanol | >90% | [147] | |
Crude soybean oil | Methanol | 94% | [148] | |
Soybean oil | Ethyl acetate | 63.3 % | [149] | |
Soybean oil | Ethanol | [150] | ||
Lipozyme TL IM | Soybean oil | Methanol | >90% | [151] |
Crude palm oil | Methanol | 96.15% | [90] | |
Waste cooking oil | Methanol | 92.8% | [152] | |
Palm oil | Oleyl alcohol | 79.54% | [153] | |
Corn oil | Methanol | 92% | [154] | |
Lipozyme RM IM | Crude rapeseed oil | Monoacylglycerol | 90% | [155] |
Sunflower oil | Methanol | >80% | [82] | |
Castor oil | Ethanol | 98% | [3] | |
Soybean oil deodorizer distillate | Ethanol | >88% | [156] |
Extracellular lipases are separated from broth containing lipase producing cells and after purification used as a catalyst in biodiesel production processes [55]. The way to purify extracellular lipases depends upon its structure and source organism [80]. Mostly extracellular lipases are used in the immobilized form for transesterification than as free lipases because of the low conversion rate and costly process [11]. Literature is full of different methods as well as materials used for immobilization of extracellular lipases. Main methods for immobilization involve cross linking, carrier binding and entrapment while the most commonly used materials for immobilization include silica, magnetic particles, and nanofibers or nanoparticles for carrier binding, alginate beads, gels, and silicon polymers for entrapment and glutaraldehyde for cross-linking [47]. The use of a suitable solvent in case of extracellular lipase is a key factor for high yield in transesterification as the use of unrelated solvent or absence of solvent results in very low yield [102, 165]. The use of extracellular lipase is also adapted because the use of intracellular lipase results in difficulties of extraction and purification of the final product [171]. Extracellular lipases are obtained from Candida guilliermondii, Burkholderia glumae, Pseudomonas aeruginosa, and Yarrowia lipolytica [176–179]. Table 1.4 indicated a comparison between intracellular and extracellular lipases.
Table 1.4 Comparison between intracellular and extracellular lipase.
Intracellular lipase | Extracellular lipase |
---|---|
Present inside the cell or linked to its walls (cell bound lipase) | Separated from cells producing it |
No need of isolation and purification steps | Complex isolation and purification are required before using it for biodiesel production |
Low conversion rate | High conversion rate |
Not analyzed by direct sampling | Analyzed by direct sampling |
Direct immobilization of lipase producing cells (whole-cell immobilization | Purification is required before immobilization |
Biodiesel production is cost-effective | Biodiesel production is costly |