| Literature DB >> 35164060 |
Tomasz Kowalczyk1, Anna Merecz-Sadowska2, Laurent Picot3, Irena Brčić Karačonji4, Joanna Wieczfinska5, Tomasz Śliwiński6, Przemysław Sitarek7.
Abstract
In recent years, there has been a considerable increase in interest in the use of transgenic plants as sources of valuable secondary metabolites or recombinant proteins. This has been facilitated by the advent of genetic engineering technology with the possibility for direct modification of the expression of genes related to the biosynthesis of biologically active compounds. A wide range of research projects have yielded a number of efficient plant systems that produce specific secondary metabolites or recombinant proteins. Furthermore, the use of bioreactors allows production to be increased to industrial scales, which can quickly and cheaply deliver large amounts of material in a short time. The resulting plant production systems can function as small factories, and many of them that are targeted at a specific operation have been patented. This review paper summarizes the key research in the last ten years regarding the use of transgenic plants as small, green biofactories for the bioreactor-based production of secondary metabolites and recombinant proteins; it simultaneously examines the production of metabolites and recombinant proteins on an industrial scale and presents the current state of available patents in the field.Entities:
Keywords: bioreactors; genetic manipulation; patents; recombinant proteins; secondary metabolites; transgenic plant cultures
Mesh:
Substances:
Year: 2022 PMID: 35164060 PMCID: PMC8840042 DOI: 10.3390/molecules27030795
Source DB: PubMed Journal: Molecules ISSN: 1420-3049 Impact factor: 4.411
Figure 1PRISMA flow diagram demonstrating screening method for article [26].
Figure 2The types of bioreactors most often used for the cultivation of plant cultures in vitro. (A) Bubble column bioreactor, (B) Stirred tank bioreactor, (C) Nutrient mist or sprinkle bioreactor, (D) Wave-mixed bioreactor, (E) Temporary immersion system.
Examples of increasing the production of selected secondary metabolites by interfering with metabolic pathways in transgenic cultures grown in bioreactors.
| Plant Species/Family | Type of Culture | Vector/Genetic | Type of | Bioreactor | Medium | Effect/Yield | Ref. |
|---|---|---|---|---|---|---|---|
| suspension culture | triterpenoid saponins (Protopanaxadiol (PPD), Dammarenediol-II) | 5 L balloon-type bioreactor 2 L of Murashige & Skoog (MS) medium (working volume) | 2 L of MS medium (working volume) | enhanced production of Dammarenediol-II (166.92 µg/g dry weight (DW), 1.6 mg/L) Protopanaxadiol (980.85l µg/g DW, 9.4 mg/L) | [ | ||
| roots | anthocyanin pigment 1 (AtPAP1) transcription factor from Arabidopsis thaliana/pCAMBIA1305.1-AtPAP1 vector | phenolic acids | 5 L sprinkle bioreactor | 2.5 L Schenk & Hilde-brandt (SH) medium with 3% ( | the greatest increase in DW (20.83 g/L) and highest yields of phenolic acids (chlorogenic acid 448 mg/L and caffeic acids 302 mg/L) | [ | |
| roots | pentacyclic triterpene (betulinic acid) | 10 L sprinkle bioreactor | 2 L of MS liquid media with 3% ( | -an increase in the content of betulinic acid (38.125 mg/g DW), compared to the SOA41 hairy root line (4.213 mg/g DW) | [ | ||
| hairy roots | a plastid targeted geraniol synthase gene originally isolated from | terpenoid indole alkaloid (geraniol) | 20-L wave-mixed bioreactor | 2 L modified Gamborg’s B5 liquid medium | -scale production batch was successfully completed, yielding milligram quantities of geraniol. | [ | |
| hairy roots | plasmid with GUS construct | secoiridoid glycosides (swertiamarin (SM), gentiopicrin (GP), and sweroside (SW)) | RITA® temporary immersion bioreactors (TIBs) | 200 of liquid MS medium | -about 2–4 times higher biomass production rate | [ | |
| cell suspensions |
3-hydroxy-3-methylglutaryl–coenzyme A reductase (HMGR), Farnesyl-diphosphate synthase (FDS), Germacrene A synthetase | sesquiterpenes (β-elemene) | 2 L stir-tank and airlift bioreactor | liquid MS medium containing 28 g L−1 sucrose, 0.5 mg L−1 6-BA, 1.0 mg L−1 naphthylacetic acid (NAA), 1.0 mg L−1 2,4-D | -highest β-elemene content of 0.22% ( | [ | |
| cell suspensions | Tryptophan decarboxylase (TDC) and strictosidine synthase (STR) genes | monomeric eburnamine-type indole alkaloid vincamine | 5-L stirred tank bioreactor | MS medium with 2% sucrose | -only PVG3 line registered a twofold increase in total alkaloid content (2.1 ± 0.1% DW) and showed vincamine presence (0.003 ± 0.001% DW) which was further enhanced at the bioreactor level (2.7 ± 0.3 and 0.005 ± 0.001% DW, respectively) | [ |
Figure 3Schematic of the selected secondary metabolite biosynthesis pathway of transgenic plants with incorporated genes. The enzymes marked in red are expressed by plant species presented in Table 1.
Figure 4General strategy for the use of in vitro plant cultures in bioreactors for the production of recombinant proteins on an industrial scale.
Overproduction of recombinant proteins in transgenic cultures grown in bioreactors.
| Name of the | Type of Culture | Vector/Genetic Construct Elements | Recombinant Protein | Type of | Medium/ | Effect/Yield | Ref. |
|---|---|---|---|---|---|---|---|
| suspension culture |
metabolically-regulated promoter, rice alpha-amylase 3D ( | recombinant human | 5-L stirred-tank bioreactor | -half-strength sucrose of the culture medium | -the method significantly improved the maximum accumulation level, purity, and productivity of the recombinant protein | [ | |
| suspension culture |
metabolically-regulated promoter, rice alpha-amylase 3D ( | recombinant human | 40-L stainless-steel stirred tank bioreactors (STB) bioreactor | -NB + S medium contains 30 g sucrose/L, while NB + 0.5xS contains 15 g sucrose/L |
-maximum total active rrBChE production level of 46–58 µg/g fresh weight (FW) in four cycles over 82 days | [ | |
| suspension culture | α-amylase 3D (RAmy3D) promoter | 5 L bioreactor | -using normal sugar-free (NB-S) media with no kifunensine treatment | -total active rrBChE production level of 79 ± 2 µg/g FW or 7.5 ± 0.4 mg/L in the presence of kifunensine | [ | ||
| suspension culture | alpha amylase 3D (RAmy3D) | tetrameric form of recombinant butyrylcholinesterase (BChE | 5 L bioreactor | -fresh liquid NB + S medium | -maximum yield of 1.6 mg BChE/L of culture during the second expression phase | [ | |
| suspension culture | RAmy3D promoter | human cytotoxic T-lymphocyte antigen 4-immunoglobulin (hCTLA4Ig) | 3-L multi-bioreactor | -AA medium (1.4 L), except the volume of amino acid solution | -total protein concentration was at levels from 301.0 to 782.8 mg/L | [ | |
| suspension culture | RAmy3D promoter | human cytotoxic T-lymphocyte antigen 4-immunoglobulin (hCTLA4Ig) | stirred-tank reactors (5-L STR) | -AA medium (2.1 L) except 10% ( | -the results in both disposable bioreactors presented similar values of the maximum cell density (11.9 g DCW/L and 12.6 g DCW/L), the doubling time (4.8 and 5.0 days) and the maximum hCTLA4Ig concentration (43.7 and 43.3 mg/L). | [ | |
| suspension culture | RAmy3D promoter | human cytotoxic T-lymphocyte antigen 4-immunoglobulin (hCTLA4Ig) | 7-L bioreactor, 15-L stirred-tank bioreactor | AA medium (2.3 L) | -maximum hCTLA4Ig level was 76.5 mg/L at day 10 | [ | |
| suspension culture | RAmy3D promoter | human granulocyte-macrophage colony-stimulating factor | 2-L bioreactor, 5-L stirred-tank bioreactor | -N6 medium | -induction using sugar free media produced 33% more hGM-CSF | [ | |
| hairy roots | pCAMBIA1105.1 binary vector | isoform 1 of the human growth hormone (hGH1) | 1.5-L mesh airlift bioreactor | -1.25 L of Schenk & Hildebrandt (SH) medium supplemented with sucrose 30 g/L and (NH4)2SO4 300 mg/L. | -the production of hGH1 was 5.1 ± 0.42 µg/g dry weight (DW) for flask cultures and 7.8 ± 0.3 µg/g DW for the bioreactor, with a capacity of 0.68 ± 0.05 and 1, 5 ± 0.06 µg/g DW days | [ | |
| suspension culture/leaves | pOA:YFP4411 | protein A (OspA) from Borrelia burgdorferi | immersion bioreactors (TIBs) using AlkaBurstTM | -1-L and 0.3-L Murashige & Skoog (MS) media | -OspA expression up to 7.6% TSP with a maximum OspA yield of about 108 mg | [ | |
| suspension culture | a-amylase gene aAmy8 promotor/Gateway-compatible binary T-DNA destination vector | mouse granulocyte-macrophage colony stimulating factor (mGM-CSF) | 2-L bioreactor | -1.5 L of N6 medium | -the highest yield of rmGM-CSF was 24.6 mg/L | [ | |
| suspension culture BY-2 | binary vector pTRAkc-MTAD | human monoclonal antibody M12 | 200-L Orbitally-Shaken Disposable Bioreactor, 20-L Nalgene polycarbonate carboy vessels | -MSN medium | -final cell fresh weights of 300–387 g/L and M12 yields of 20 mg/L | [ | |
| suspension culture | RAmy3D promoter | recombinant human butyrylcholinesterase (BChE) | 5-L stirred-tank bioreactor | -3 L of NB + Smedium | -maximum total active rrBChE (77 μg/g FW) and 1.6-fold increase of total active | [ | |
| hairy roots | CaMV35S promoter | recombinant protein | 5 L bioreactor Bench-top fermenter (Bioflo-3000) | -the quantity of 2.5 L of 1/2 MS medium with B5 vitamins and 3% sucrose | -biomass yield 197.4 (g/L) | [ | |
| suspension cultures (and calli)/leaves | Plasmid pFMGFP | a vaccine antigen, fragment C of tetanus toxin (TetC)/green fluorescent protein (GFP+) | 2 L bioreactor | MS medium supplemented with 0.1 lM TDZ | -GFP+ yield reached 660 mg/L of bioreactor (33% TSP), and TetC accumulated to about 95 mg/L (8% TSP) | [ | |
| suspension culture | α-amylase gene promoter, | recombinant human serum albumin (rHSA) | 2-L airlift and a 2-L stirred tank bioreactor | MS medium | -rHSA production has been enriched to 45 mg/L in plant culture | [ | |
| suspension cell cultures BY-2 | vector pCaMterX enhanced virus 35S promoter | green fluorescent protein-hydrophobin fusion (GFP-HFBI) | 30-L bioreactor, 600-L standard stirred tank bioreactor | MS-medium | -HFB-fusion technology in large-scale tobacco BY-2 suspension cell culture, formation of protein bodies and efficient purification of GFP-HFBI fusion by aqueous two-phase separation (ATPS)
| [ | |
| whole plant | MFHR1 construct | factor H (FH) and FH-related proteins (FHRs) | 5-L bioreactor | -fresh medium with the addition of 5 μM naphthaleneacetic acid (NAA) | -it was obtained 17 mg of MFHR1 protein | [ | |
| hairy roots | binary plasmid p221 that included cauliflower mosaic virus 35S promoter, tobacco etch virus (TEV) leader sequence and 35S terminator | human tissue-plasminogen activator (t-PA) protein | 18 L bioreactor | -MS, Woody Plant Me-dium (WPM), B5 medium | -biomass accumulation 615.4 g/FW in MS medium, 457.6 g/FW in B5 medium and 621.8 g/FW in WPM medium | [ |
Selected examples of patents relating to bioreactors for the culture of plant material.
| Patent/Patent Application No | Assignee | Type of Plant Culture | Year |
|---|---|---|---|
| WO2012044239A1 | - | Tissue cultures | 2012 |
| CN102408991B | Bright Oceans Corp. (Shaanxi, China) | Cells, tissues and organs | 2014 |
| CN103120126B | Nanjing University | Plant tissue culture | 2014 |
| US20140026260A1 | Worcester Polytechnic Institute | Tissues and organs, whole plants | 2014 |
| WO2015066779A1 | - | Tissue culture | 2015 |
| EP2674479B1 | Eppendorf AG (Hamburg, Germany) | Cell culture | 2015 |
| CN103270946B | Nanjing Biofunction Biological Science & Technology Co Ltd. (Nanjing, China) | Plant tissue culture | 2016 |
| WO2016092098A1 | - | Cell or tissue cultures | 2016 |
| CN104770304B | Nanjing Biofunction Biological Science & Technology Co Ltd. | Plant tissue culture | 2017 |
| EP3069591B1 | Fibria Celulose SA (Sao Paulo, Brazil) | Plant tissue culture | 2018 |
| CN104379722B | Eppendorf AG (Hamburg, Germany) | Cell culture | 2018 |
| USD822223S1 | University of Guelph | Tissue culture | 2018 |
| EP3502229A1 | Evologic Technologies GmbH (Vienna, AT) | Hairy root cultures | 2019 |
| US20190282983A1 | Life Technologies Corp (Carlsbad, CA) | Cell culture | 2019 |
| CN208857314U | PURUIKANG BIOTECHNOLOGY CO Ltd. (Shenzhen, China) | plant cell, organ | 2019 |
| CN111226794A | Beijing Forestry University | Mature somatic embryos | 2020 |
| CN212247083U | Zhejiang University of Technology ZJUT | Cell culture | 2020 |
| ES2763637B2 | Institut Recerca i Tecnologia | Plant tissues, organs, seeds and/or plant cells | 2020 |
| US20200032185A1 | Oklahoma State University | Cell culture | 2020 |
| US20200230568A1 | ABEC Inc. | Cell culture | 2020 |
| US20200339931A1 | Sartorius Stedim Biotech GmbH (Goettingen Germany) | Cell culture | 2020 |
| US20210130765A1 | Ori biotech Ltd. (London, United Kingdom) | Cell culture | 2021 |
| US20210214668A1 | Membio Inc (Mississauga, ON, Canada) | Cell or tissue culture | 2021 |