| Literature DB >> 30833951 |
Ulrika Egertsdotter1,2, Iftikhar Ahmad1, David Clapham3.
Abstract
For large scale production of clonal plants, somatic embryogenesis (SE) has many advantages over other clonal propagation methods such as the rooting of cuttings. In particular, the SE process is more suited to scale up and automation, thereby reducing labor costs and increasing the reliability of the production process. Furthermore, the plants resulting from SE closely resemble those from seeds, as somatic embryos, like zygotic (seed) embryos, develop with good connection between root and shoot, and without the plagiotropism often associated with propagation by cuttings. For practical purposes in breeding programs and for deployment of elite clones, it is valuable that a virtually unlimited number of SE plants can be generated from one original seed embryo; and SE cultures (clones) can be cryostored for at least 20 years, allowing long-term testing of clones. To date, there has however been limited use of SE for large-scale plant production mainly because without automation it is labor-intensive. Development of automation is particularly attractive in countries with high labor costs, where conifer forestry is often of great economic importance. Various approaches for automating SE processes are under investigation and the progress is reviewed here, with emphasis on conifers. These approaches include simplification of culture routines with preference for liquid rather than solid cultures, use of robotics and automation for the harvest of selected individual mature embryos, followed by automated handling of germination and subsequent planting. Different approaches to handle the processes of somatic embryogenesis in conifers are outlined below, followed by an update on efforts to automate the different steps, which are nearing an operational stage.Entities:
Keywords: automation; bioreactors; conifer; scale up; somatic embryogenesis
Year: 2019 PMID: 30833951 PMCID: PMC6388443 DOI: 10.3389/fpls.2019.00109
Source DB: PubMed Journal: Front Plant Sci ISSN: 1664-462X Impact factor: 5.753
Figure 1Zygotic embryo development in gymnosperms and angiosperms differs in some major aspects. (A) Early stages of conifer embryo development. The conifer zygote results from a single fertilization event. At the beginning of embryogenesis, there are free nuclear stages followed by a pro-embryo stage. Main characteristics of conifer embryo development are the polyembryogenic features of some conifer species where the zygotic embryos to different degrees proceed through a process of embryo-cleavage that results in multiple embryos that are eventually eliminated by programmed cell death. (B) In angiosperm embryo development the sporophytic generation is initiated by a double fertilization event resulting in one embryo. (A) pU, primary upper tier; pE, primary embryonal tier; U, upper tier; S, suspensor tier; EM, embryo mass; dS, R: dysfunctional suspensor tier; Es, embryonal suspensor tier; dEM, degenerating embryo mass; ROC, root organization center; sEs, secondary embryonal suspensor cells. (B) A, apical cell; B, basal cell; EP, embryo proper; S, suspensor. Figure adapted from Egertsdotter (1996).
Figure 2Overview of the SE process in Norway spruce (similar in other conifers). (a) Seeds from selected crossings are surface sterilized and used to extract zygotic embryos (ZE). Zygotic embryos are put in contact with initiation medium. (b) Embryogenic “callus” (EC) composed of early-stage somatic embryos (proembryogenic masses) protrudes from the zygotic embryo and continues to multiply to form a callus-like culture that can be isolated onto new medium (c). After transfer of the multiplying culture to maturation medium, multiplication stops and maturation starts (d). Fully mature embryos (e) can be isolated and transferred to desiccation before stimulated to develop into germinants with sufficient root and shoot development for transfer to ex vitro conditions (f). SE plants develop after a period of acclimatization (g) and can then grow under regular nursery conditions (h). Figure adjusted after Egertsdotter (2018). Scale bars represent 2 mm.
Figure 3Temporary immersion bioreactor model with the liquid medium separated from the culture container. Feeding is controlled by a digital timer through a solenoid valve.
Representative published articles on the utilization of bioreactors for SE-based plant production in angiosperms.
| 3 L balloon type air lift, with continuous or temporary immersion | Nearly twice as fast proliferation with continuous as compared with temporary immersion | Wu et al., | |
| RITA and twin flask system | Higher quality PEMs giving four times as many plants obtained from RITA than from twin flasks | Heringer et al., | |
| Temporary immersion system (twin flasks) | Induction of secondary SE was higher (84.6%) in bioreactor than on solid medium (70.2%) | Steinmacher et al., | |
| Custom temporary immersion bioreactor | Four-fold higher yield of gobular embryos with TIS than obtained on semi-solid media | Akula et al., | |
| RITA | Up to 95% of SEs showed complete germination in RITA depending on inoculum density | Posada-Pérez et al., | |
| Airlift bioreactors (ALBs) | Higher yields of small cell clumps suitable for transformation in ALBs than in suspension flasks | Kong et al., | |
| Custom-made temporary immersion bioreactor | TIB stimulated formation of cotyledonary stage embryos, but germination still poor in all culture conditons | Cabasson et al., | |
| RITA and MATIS | Comparison of zygotic and somatic embryo germination and plant formation provides information to improve SE germination in larger bioreactors. | Etienne et al., | |
| . | RITA | Effects on yields and vitrification from immersion cycles. Six immersions/day produced more embryos (3,081) than two immersions/day (2,094) | Albarrán et al., |
| RITA | Demonstration of benefits from germination in RITAs for direct sowing in soil. 200 mg of embryogenic callus produced 8,000 embryos in one bioreactor. The germination frequency was 66% | Etienne-Barry et al., | |
| RITA | 800 somatic embryo per bioreactors were produced. Germination rate was 86%. A positive relation of cotyledon size of embryos germinated in RITA for plant establishment | Barry-Etienne et al., | |
| RITA | Highest number of somatic embryos (25) obtained in bioreactor. The germination rate was 100%. SE-multiplication in suspension cultures and plant regeneration in RITA for the purpose of genetic transformation | Gatica-Arias et al., | |
| Temporary immersion bioreactors (TIBs) | Pilot scale process for batch-production of torpedo stage embryos in suspension flasks, germination in TIBs and transfer to | Ducos et al., | |
| 10 L “Box- in- bag” bioreactors, TIBs | Batch-production of torpedo stage embryos in “Box-in-bag bioreactor,” germination in TIBs and transfer to | Ducos et al., | |
| Custom-made temporary immersion system modified from Nalgene filter units | Growth rate of embryogenic callus was 0.38 g/week | Sumaryono et al., | |
| RITA | Fresh weight of callus increased 7-fold in RITA bioreactors | Marbun et al., | |
| RITA and twin flask system TIS | 100% increase in fresh biomass in twin flask compared with RITA | Gomes et al., | |
| Bubble column bioreactor | Higher numbers of somatic embryos and better growth developed in bioreactors than in suspension cultures | Yang et al., | |
| RITA | Optimization of immersion intervals and demonstration of plant regeneration after RITA embryo production | Mohd et al., | |
| Custom-made temporary immersion bioreactor | Improved yields in all steps of the SE process from embryogeneic callus to germination | Etienne et al., | |
| Temporary immersion 2 L bioreactors with net, (TIN) or continuous immersion with net (CIN) | 85% of embryos produced plantlets with TIN, vs. 29% with CIN | Kim et al., | |
| RITA | 46% increased efffects from culture system on secondary metabolite production in somatic embryo cultures | Ptak et al., | |
| 5 L balloon type bubble column bioreactor or shake flasks | Highest frequency (87%) normal plants obtained among regenerants after callus proliferation in a pH-controlled bioreactor | Chin et al., | |
| Temporary immersion system modified from Nalgene filter units, or semi-solid medium | Number of embryos muliplied 9-fold after 2 months in bioreactor, 3-fold on semi-solid medium. Subsequent germination on semisolid medium was 60–70% in both cases | Escalant et al., | |
| 3 L air lift bioreactor | Early globular embryos (10 g) developed into cotyledonary embryos (79.7 g) in 4 weeks in bioreactor. These converted to plantlets if treated with GA. | You et al., | |
| TIS | A mixed system including culture on semi-solid medium, reduced costs (vs. traditional methods) and the time for plantlet production reduced to < 3 years | Almusawi et al., | |
| Custom temporary immersion system bioreactor | Formation of 172 somatic embryos per bioreactor from 500 mg embryogenic callus | Al mayahi, | |
| RITA | Suspension cultures gave more embryos than RITA | Ibraheem et al., | |
| RITA | Improved proliferation and production of cotyledonary stage embryos in temporary immersion bioreactors compared to semi-solid medium; 20% increase | Mallón et al., | |
| RITA | 7.5 fold increase in fresh weight in RITA compared with on semisolid medium. Immersion frequency had strong influence; best I min every 4 or 6 h | Perez et al., | |
| RITA | Increased yield of | Snyman et al., | |
| Twin flask TIS bioreactors | Significantly higher numbers of embryos in TIS than on solid medium. Improved conversion rate to torpedo-shape | Niemenak et al., | |
| 3 L balloon-type air lift bioreactor | SE biomass growth was higher in bioreactor (328.45 g/L) than on solid medium (69.60 g/L) | Sun et al., | |
| Air-lift bioreactor | Pro-embryogenic masses doubled in fresh weight in bioreactors compared to suspension flasks without any losses in viability and regenerative capacity | Tapia et al., |
Figure 4An SE Fluidics System in use for research at Umeå Plant Science Center, Swedish University of Agricultural Sciences in Umeå, Sweden. I. Overview of the SE Fluidics System and the main functional parts: The core parts of the system are: (a) a laminar flow hood for extraction of tissue from the bioreactors (or other culture vessels); (b) disperser-system that disperses the culture of PEMs and embryos; (c) a separator tank that separates out mature embryos for (d) image analysis. (e) Mature embryos are deposited into the container or substrate of choice. II. Flow chart showing the various steps in the SE fluidics system from proliferation and maturation in bioreactor to transfer (extraction) of the mature embryos and unresponsive PEM masses from the bioreactors into the SE Fluidics system; dispersion of the tissue from the bioreactors into mature embryos and clusters of PEMs; separation of mature embryos from the PEMs, with only mature embryos proceeding in the SE Fluidics system after the separator tank; optional image analysis of mature embryos and sorting based on pre-set selection criteria, and deposition of selected mature embryos. The system can also be run without image analysis where all mature embryos are harvested, or with image analysis where all embryos are imaged but without selection based on specific morphologies. For details of the constructions, see Aidun and Egertsdotter (2018).