| Literature DB >> 29988523 |
Sheeja Jagadevan1, Avik Banerjee1, Chiranjib Banerjee1, Chandan Guria1, Rameshwar Tiwari2,3, Mehak Baweja2, Pratyoosh Shukla2.
Abstract
In the wake of the uprising global energy crisis, microalgae have emerged as an alternate feedstock for biofuel production. In addition, microalgae bear immense potential as bio-cell factories in terms of producing key chemicals, recombinant proteins, enzymes, lipid, hydrogen and alcohol. Abstraction of such high-value products (algal biorefinery approach) facilitates to make microalgae-based renewable energy an economically viable option. Synthetic biology is an emerging field that harmoniously blends science and engineering to help design and construct novel biological systems, with an aim to achieve rationally formulated objectives. However, resources and tools used for such nuclear manipulation, construction of synthetic gene network and genome-scale reconstruction of microalgae are limited. Herein, we present recent developments in the upcoming field of microalgae employed as a model system for synthetic biology applications and highlight the importance of genome-scale reconstruction models and kinetic models, to maximize the metabolic output by understanding the intricacies of algal growth. This review also examines the role played by microalgae as biorefineries, microalgal culture conditions and various operating parameters that need to be optimized to yield biofuel that can be economically competitive with fossil fuels.Entities:
Keywords: Biofuel; Biorefinery; Genome-scale reconstruction; Microalgae; Optimization models; Synthetic biology
Year: 2018 PMID: 29988523 PMCID: PMC6026345 DOI: 10.1186/s13068-018-1181-1
Source DB: PubMed Journal: Biotechnol Biofuels ISSN: 1754-6834 Impact factor: 6.040
Fig. 1Pictorial representation of the overall process towards biofuel production in microalgae using synthetic biology approach (i.e., isolation, selection of an ideal strain, redirecting the metabolism to maximize synthesis of the targeted biofuel)
Recent studies in microalgae employed for the production of biofuel
| S. no. | Algal species | Reactor/growth conditions and products | References |
|---|---|---|---|
| 1 | Flat-plate airlift photobioreactor. Production rate 0.000959 kg H2/kg dry cells/h | [ | |
| 2 |
| Down-flow type supercritical water gasification reactor. Product composed of hydrogen (52.0%), methane (17.9%) and CO2 (23.0%) with 97.4 wt% gasification efficiency | [ |
| 3 |
| Supercritical water gasification of microalgal hydrothermal liquefaction for hydrogen production. Non-stirred batch stainless steel Parr reactor produced 30 mol H2/kg algae | [ |
| 4 | Two-stage batch co-fermentation resulted in 6.6 and 70.9% energy conversion efficiencies during hydrogen fermentation and combined H2–CH4 production, respectively. Hydrogen yield of 94.5–97.0 mL/g volatile solids | [ | |
| 5 | Biophotolysis-based hydrogen and lipid production using crude glycerol as an exogenous carbon source. The optimal conditions were glycerol concentration of 16 g/L, initial pH 6.8, and light intensity of 48 μmol photon/m2 s, yielding 11.65 ± 0.65 mL/L hydrogen along with lipid content > 40% in the microalgal biomass | [ | |
| 6 |
| Combination of separate hydrolysis and fermentation and simultaneous saccharification and fermentation found most effective. Lipid-extracted biomass yielded 0.26 g bioethanol/g lipid-extracted biomass at pH 5, temperature of 34 °C, and microalgae biomass loading at 18 g/L | [ |
| 7 | Microalgae used as a feedstock for bioethanol production. 72 h of incubation at substrate concentration of 30 g/L microalgal biomass and 3 mL inoculums at pH 6 yielded 7.26 g/L bioethanol | [ | |
| 8 |
| Microalgae used as a feedstock for bioethanol production. Fermentation conducted at pH 5, temperature of 34 °C, and microalgae biomass loading at 18 g/L via simultaneous saccharification and fermentation resulted in a theoretical yield of bioethanol that exceeded 90% | [ |
| 9 | Mixed microalgae cultures | Fermentation of the glucose after enzymatic hydrolysis yielded 0.46 g ethanol/g glucose | [ |
| 10 |
| Freshwater biomass produced ethanol more efficiently than the sea water biomass with ethanol conversion yields of 70.3 and 65.4%, respectively, after 9 h. Simultaneous saccharification and fermentation processing was superior to separate hydrolysis and fermentation processing for bioethanol production | [ |
| 11 |
| Purified lipids were catalytically deoxygenated to yield liquid product consisting of 99 wt% hydrocarbons and diesel-like (C10–C20) hydrocarbons | [ |
| 12 |
| Carbon nanotube (CNT)-supported metal catalyst for hydrothermal liquefaction of | [ |
| 13 |
| Catalyst calcinated from natural white mussel shell at 1000 °C used in the transesterification process. The algal biodiesel showed the presence of saturated fatty acids: C16:0, C18:0, C22:0, C24:0 and monounsaturated fatty acids C18:1 | [ |
Fig. 2Scheme representing the synergy between enzymes that lead to the formation of lipid (CA carbonic anhydrase; RuBisCO Ru1,5BP carboxylase/oxygenase; PDC pyruvate dehydrogenase complex; ACC acetyl-CoA carboxylase; KAS 3-ketoacyl-ACP synthase; ACL ATP-citrate lyase; MDH malate dehydrogenase; MME NADP-malic enzyme; PDC pyruvate dehydrogenase complex; GPAT glycerol-3-phosphate acyltransferase; LPAAT lyso-phosphatidic acid acyltransferase; LPAT lyso-phosphatidylcholine acyltransferase; DGAT diacylglycerol acyltransferase; PDAT phospholipid diacylglycerol acyltransferase
Fig. 3Key events that mark the development of synthetic biology in microalgae-based oil accumulation
Promoters employed for facilitating synthetic biology in cyanobacteria and microalgae are summarized
| Sl. no. | Promoters usable in synthetic biology (functional elements) | Host experimented on | Remarks about application (expressed gene, output level, significance) | References |
|---|---|---|---|---|
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| 1. | [ | |||
| 2. | EFE encoding gene from | [ | ||
| 3. | [ | |||
| 4. | eYFP gene. 10,000 relative fluorescence unit. 290-fold increase | [ | ||
| 5. | (a) | (a) | [ | |
| 6. | [ | |||
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| 7. | [ | |||
| 8. | hydA1 gene derived from Chlamydomonas reinhardtii 130 nmol H2 produced mg/Chl min | [ | ||
| 9. | Endogenous CABII-1 that controls chla/b binding proteins of PSII, induced by changing light condition | Chlamydomonas reinhardtii | NIT1 nitrate reductase gene | [ |
| Promoters (nutrient induced) | ||||
| 10. | nirA from Synechococcus elongates PCC 7942 induced/repressed by NO3−/NH4+ with concentration 17.6 mM each | Synechocystis sp. PCC 6803 | p-Hydroxyphenyl pyruvate dioxygenase gene. Increase of 25-fold (250 ng tocopherol mg/dry wt.) | [ |
| 11. | nirA from Synechococcus elongates PCC 7942 induced/Repressed by NO3−/NH4+ with concentration 15.0 mM/3.75 mM | S. elongates PCC 7942 | cmpABCD. Increase of fivefold (260 nmol HCO3− mg/Chl) | [ |
| 12. | NIT1 induced/repressed by NO3−/NH4+ | C. reinhardtii, Phaeodactylum tricornutum, Dunaliella salina, Chlorella vulgaris | NIT1 nitrate reductase gene switched on/off by NO3−/NH4+. Expression vector having NIT1 promoter is used widely as circuits on expression studies | [ |
| Promoters (metal induced) | ||||
| 13. | Coat from Synechocystis sp. PCC 6803 induced by Co2+ (6 μM) | Synechocystis sp. PCC 6803 | EFE gene from Pseudomonas Syringae. 500-fold increase (48 nL ethylene/mL h) | [ |
| 14. | petE from Synechocystis sp. PCC 6803 induced by Cu2+ (0.5 μM) | Synechocystis sp. PCC 6803 | EFE gene obtained from Pseudomonas syringae. fivefold increase (28 nL ethylene/mL h) | [ |
| 15. | ziaA from Synechocystis sp. PCC 6803 induced by Zn2+ (3.5 μM) | Synechocystis sp. PCC 6803 | hydA1 gene derived from Chlamydomonas reinhardtii 109 nmol of H2 produced mg/Chl min | [ |
| 16. | smt from Synechococcus elongates PCC 7002 induced by Zn2+ (2 μM) | Synechocystis sp. PCC 6803 | EFE gene obtained from Pseudomonas syringae twofold increase (2 nL ethylene/mL h) | [ |
| 17. | isiAB Synechococcus sp. strain PCC 7002 repressed by Fe3+ (100 nM) | S. sp. strain PCC 7002 | luxAB gene derived from Vibrio harveyi. twofold increase | [ |
| 18. | isiAB Synechocystis sp. PCC 6803 repressed by Fe3+ (30 μM) | Synechocystis sp. PCC 6803 | isiAB+gfp genes. 5000-fold increase | [ |
| 19. | CYC6 endogenous promoter that controls cytochrome c6 repressed by Cu2+ | C. reinhardtii | Inducible expression of copper responsive element (CuRe) responsive to Cu2+ and by Co2+ by CYC6 | [ |
| 20. | Synthetic promoter sap11 produced to resemble native cis-elements and its structure | C. reinhardtii | Synthesized to understand promoter structure and increase in nuclear gene expression. Synthetic sap11 drives expression better than best endogenous promoter chimeric hsp70/rbs2. A highly conserved DNA motif was isolated by sap11 that is important for promoter function | [ |
| 21. | TPP riboswitch based on Thiamine pyrophosphate biosynthesis from THIC genes of Arabidopsis | C. reinhardtii | Inducible expression system depending on the presence of TPP. Conditional repression of rpoA or rps12 chloroplast genes influencing their transcription/translation | [ |
| 22. | RNAi silencing | C. reinhardtii | A RNAi construct effectively silenced 20 LHC proteins. 290% higher light penetration, augmentation in photosynthetic yield, less vulnerable to photo-inhibition | [ |
| 23. | Differential expression of rbcl mRNA maturation factor MRL1 | C. reinhardtii | MRL1 under a inducible promoter can be used to regulate Rubisco level for optimum utilisation of energy according to conditions like light and CO2 | [ |
These promoters can be utilized to construct pathways and build artificial circuits having rational, controllable logical genetic units that can yield desired output under specific stimulus
Fig. 4Hypothetical circuits proposed with the help of genetic modules (plasmids a, b, c) that can be applied to microalgae with light intensity stimulus. Case 1. Input (plasmid a + b) = light-inducible promoter::gRNA for transcription factor (PSR1/NRR1)a + light-inducible promoter::dCas9/VP64(CRISPRa) = activation of lipid pathway (Output). Case 2. Input (plasmid a + c) = light-inducible promoter::gRNA for transcription factor (Zn(II)2Cys6)b + light-inducible promoter::dCas9/SRDX(CRISPRi) = inactivation of lipid pathway suppressors (Output). aPSR1 and NRR1 are transcription factors that get induced during stress which leads to lipid accumulation [171, 172]. bZn(II)2Cys6 is a transcription factor that negatively regulates lipid accumulation under nitrogen stress [183]
Recent advances in microalgae employed for the production of biofuel
| Type of model or algorithm | Target product | Model-based target: knockout gene A or overexpress gene B | References |
|---|---|---|---|
| Dynamic flux balance analysis | Ethanol | Ethanol production pathway after 20 h | [ |
| Genome-scale metabolic model | Prediction of growth rate with respect to photosynthetic quotient for ethanol and butanol production | Double reaction knock out of hydrolyase and dehydrogenase | [ |
| In vivo carbon flux analysis | Homolanthionine | Deletion of methionine and cysteine biosynthesis repressor protein | [ |
| Metabolic flux analysis | Hydrogen production | Deletion and addition of GAP1 and dehydrogenase, respectively | [ |
| Metabolic flux analysis | Astaxanthin synthesis | – | [ |
| Metabolic flux analysis | Fixed more CO2 and had a higher biomass yield | Alternate pathway for isoleucine synthesis (via citramalate synthase, CimA | [ |
| Metabolic net fluxes | Hydrogen production | Disruption of hydrogenase and poly-β-hydroxybutyrate synthase | [ |
Fig. 5Multi-objective optimal cultivation of microalgae