Biotechnological and Technical Challenges Related to Cultured Meat Production
Abstract
:1. Introduction
Cellular Agriculture and Cultured Meat
2. Cultured Meat Production Process
3. Challenges Related to Cultured Meat Production
3.1. Biotechnological Challenges
3.1.1. Choice of Animal for Cell Harvesting
3.1.2. Choice of Site of Collection
3.1.3. Methods for Cell Harvesting
3.1.4. Fetal Bovine Serum: Ethical Challenges
3.1.5. High Cell Proliferation and Genetic Instability
3.1.6. Nutritional and Functional Properties of Cultured Meat
3.1.7. FBS Alternatives
3.1.8. Food Control System for Cultured Meat
4. Technical Challenges in Cultured Meat Production
4.1. Scaffold Fabrication
4.1.1. Conventional Porous Scaffold Fabrication Technologies
- Solvent casting and porogen leaching (SCPL) [68]: This process involves mixing a polymer solution dissolved in an organic solvent composed of insoluble particulates (porogen). The mixture is then cast into a mold or a membrane, and the solvent is evaporated. Finally, the structure is immersed in an aqueous solution to leach out particulates in the structure. Porosity, in terms of shape, size, and uniformity, depends on the particulate choice of particulates, typically salt particles. The main drawbacks are the lack of control of internal architecture and uniformity, reduced reproducibility, formation of a skin layer due to polymer thickening that can limit access to internal porous, limited thickness (2–3 mm) [69], weak mechanical properties, and possible cytotoxicity due to residual solvent and porogen [70].
- Phase separation [71]: The technique is used to produce a scaffold through the separation of a mixture into two phases: a polymer-rich one and a polymer-poor one. This is achieved under thermodynamically unstable conditions. For example, cooling the solution below the freezing point of the solver induces crystal nucleation inside the solution; after that, the solid material is sublimed, ensuring that the structure is composed of only the polymer-poor region with porosity, because the solvent and the polymer-rich phase are evacuated from the scaffold. This technique leads to highly interconnected porosity which can be used to reproduce channel-like structures by applying a directional temperature gradient. Nevertheless, control and optimization of process parameters (e.g., temperature, polymer concentration, surfactants use, crystal nucleation) are the main problems in managing pore size and distribution [72]. Moreover, the typical pore size achievable is often smaller than the typical dimension in tissue engineering applications (<200 µm).
- Gas foaming [73]: This is a class of techniques for scaffold fabrication exploiting a blowing agent to generate gas inside the material which acts as a porogen agent. The main advantage is the absence of solvents or porogen materials, which can induce cytotoxicity due to possible residuals. The Gas formation can be induced chemically or thermally or by pressure change. The main drawbacks of the technique are low control over pore size and interconnectivity, low reproducibility and structural uniformity, and difficulty in incorporating biological molecules in thermally induced processes [74,75].
- Sintering [76]: The technique is used to produce cohesive porous scaffolds through bonding of a polymeric phase and ceramic particles or fibers. The usual procedures involve a bed of randomly packed particles bonded through heating up to a temperature above the glass transition temperature of the base material, but lower than its melting point, creating a local fuse area only in the contact surfaces, leading to a porous microstructure. Alternative sintering modes are mild solvent treatment and pressure. Sintered scaffolds are characterized by lower porosity, small pore size with difficulty in precise control and distribution, and higher mechanical properties, and they are mainly used in dental and bone-repairing applications [77].
4.1.2. Non-Conventional Porous Scaffold Fabrication Technologies
- Electrospinning [78]: The method is based on an electric field generated between a polymer solution delivery system at a controlled flow rate and a collector, drawing the solution into a fiber, an illustrative example is shown in Figure 3. The result is a membrane of non-woven fibers. The textile-based technique has been created to reproduce fiber-based materials, such as those similar to the extracellular matrix (ECM). The resulting porosity is interconnected and the achievable pore size is lower than that by other scaffolding techniques, achieving fibers with diameter up to a few nanometers [78], which can be an advantage for specific applications (e.g., vascular [79]), but tends to limits the cell migration to a point where its applicability in tissue engineering becomes a problem. Several process parameters can be controlled to tune fiber diameter and alignment, adapting textural properties to the specific cell type to be seeded.
- Self-assembly [81]: The technique involves specifically designed amphiphilic peptides with the capacity to spontaneously organize into ordered structures, including nanofibers. The method allows a great process control starting from the building blocks in a bottom-up design approach for tissue engineering application.
- Hybrid scaffolds: With the aim of controlling structural and composition features, mainly porosity, at different length-scales, several approaches with mixed techniques are used, such as SCPL and electrospinning combination [82], multilayer electrospun composites with different parameters [83], and a combination of more than two fabrication techniques [84,85].
- Additive manufacturing (AM): The conventional techniques of porous scaffolds fabrication, as well as other emerging alternatives, are implemented to produce scaffolds to recreate the complex micro and macrostructures of biological tissues. However, all of them have limitations and allow narrow control over important textural parameters such as pore shape, dimensions, and interconnectivity [86]. An emerging family of technologies, based on additive AM techniques, has proved to enable the manufacture and control of complex shapes. AM, popularly called 3D printing, is a generic definition and represents a large group of processes that can be classified in several ways [87]. Within the porous scaffold fabrication context, according to Rey et al., some of the AM technologies could be used to produce scaffold with a high spatial resolution, the structural complexity, and control over the internal pore architecture. The most promising techniques are powder-bed based 3DP, such as selective laser sintering (SLS), and liquid raw-material-based 3DP, such as stereolithography (SLA) [86].
4.2. Alternatives to Scaffold Fabrication
4.2.1. Tissue Decellularization
4.2.2. Microcarrier Cultures
4.3. Biofabrication and 3D Bioprinting
4.3.1. 3D Bioprinting Strategies
Properties | Extrusion | Inkjet | Laser-Assisted | Stereolithography | Two-Photon |
---|---|---|---|---|---|
Speed | Slow | Fast | Medium | Fast | Very fast |
Cost | Moderate | Low | High | Low | Very high |
Cell viability | 85–95% | 80–95% | <85% | 25–90% | >80% |
Cell density | High | Low | Medium | Medium | Medium |
Scalability | High | High | Low | Medium-high | - |
Resolution | 100–500 µm | 100–500 µm | 20–100 µm | 20–100 µm | 0.1–10 µm |
Bioink viscosity | 6–30 × 107 mPa⋅s | <10 mPa⋅s | 1–300 mPa⋅s | No limitation | No limitation |
Advantages | Is Simple, is capable of printing various biomaterials, high cell densities | Has the ability to print low viscosity biomaterials, fast fabrication speed, low cost, and a high resolution | Has a high resolution, is nozzle-free, and can deposit biomaterials in solid or liquid phase | Is nozzle-free, has high complexity, and has a high resolution | Is nozzle-free, has a high complexity, has the highest resolution, and has high cell viability |
Drawbacks | Only for viscous liquids, resolution | Limited to low viscous fluids, resolution, cell density | High cost, thermal damage due to nanosecond/femtosecond laser irritation, scalability, cost | Lack of printing multi-cells, cell damage during photo-curing | Lack of printing multi-cells, cost |
Applications | Tissue models for cell research, drug testing and regenerative medicine, meat-analogue constructs [101] | Supplementary to other technologies | Precise cells deposition | Scaffolds and complex structures with channels | Vascularized and high precision models |
4.3.2. Bioink Formulation
- There is a circular relationship between cells and bioink rheology: the firsts impact the rheology, and thus process parameters, and vice versa. For example, Billiet et al. found a twofold lowering in the viscosity of a GelMA-based bioink when prepared with 0.5 and 1.5 million cells/mL and a fourfold lowering when prepared with 2.5 million cells/mL [107]. Hence, there is the need to predict or test the rheological properties of ink with cells inside.
- Mechanical stresses must be minimized, reducing printing pressure and increasing nozzle diameter because cells are mechanical sensing and suffer higher mechanical stresses.
- The modulus of the gel-phase highly impacts cell viability, and probably also molecular weight and polydispersity. The mechanical properties of the material surrounding the cells is a crucial aspect that is poorly understood.
- Post-printing crosslinking can affect cell viability as well. Frequently, bioprinted constructs are UV-crosslinked and the amount irradiation cells can tolerate is not clear, probably between 30 s and a few minutes. Moreover, the final degree of cross-linking can interfere with cell projections and network formation, an important mechanism to ensure tissue formation. This can become important when polymer concentration is increased to increase printability. According to the author, the concentration of the polymer must be between 5 and 10%, but it is obviously a polymer-dependent quantity.
4.4. Bioreactors
- Static culture systems: They are the simplest and provide the required nutrient in a static fluid environment. Thus, the media must be changed often, and it perfuses by passive fluid diffusion [25]. These systems can be easily coupled with load-bearing mechanisms, for example, to provide a compressive load to the engineered tissues [110,111].
- Spinner flasks: Spinner-flask-based systems are used to apply fluid-induced shear stresses to constructs submerged within a re-circulating and nutrient-rich medium solution [25]. Although this system provides a better environment to construct with respect to the static culture, spinner flasks may not be optimal due to turbulent flow and the related higher shear stress generated [112].
- Perfusion systems: The poor diffusion condition of static culture can be improved by perfusion bioreactors, especially in the internal parts of porous scaffolds [113]. These systems are characterized by a culture encasing bioreactor, vessels for the medium (nutrient-rich and oxygenated), and a pump generating the flow [27]. Moreover, perfusion systems allow for automatic media circulation, waste removal, and provide shear stress due to the flow, which is beneficial in specific tissue cultures such as for dermis and cartilaginous tissues [23,112].
- Rotating wall vessel: An alternative approach for reducing diffusional limitations of nutrients and waste with limited shear stress is the use of rotating wall vessel bioreactors [24]. Although shear stress is important for cell maturation, an excessive force will lead to damages or to the formation of undesired capsules surrounding the tissue [112]. This method uses a dynamic laminar flow induced by the rotating fluid inside the bioreactor, and it has been proved to be effective for cell cultures, especially chondrocytes and cardiac cells [24]. The main drawback is the non-uniform tissue growth, due to the force field. Moreover, the centrifugal force can cause collision between scaffolds and the walls of the bioreactor [112].
- Pulsatile flow: For cardiovascular cell cultures that require a pulsatile stimulation, bioreactors exploiting pulsatile flow are used to mimic in vivo conditions. Typically, vascular cells are cultured into tubular scaffolds [112].
4.5. Industrial Process Scaling-Up
5. Consumer Acceptance
6. Conclusions
Funding
Institutional Review Board Statement
Informed Consent Statement
Acknowledgments
Conflicts of Interest
References
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Biotechnological Challenges | Technical Challenges |
---|---|
Choice of animal for cell harvesting Choice of site of collection Methods for cell harvesting FBS: ethical challenges High cell proliferation and genetic instability Nutritional and functional properties of cultured meat FBS alternatives Food control system for cultured meat | Scaffold fabrication Alternatives to scaffold fabrication Biofabrication and 3D bioprinting Bioreactors Industrial process scale-up |
Matrices | Cell Type | Effects | Refs. |
---|---|---|---|
Plant peptones | CHO-320 (CHO K1 clone) | Improved cultivation and productivity of Human interferon gamma | [48] |
Yeast hydrolysate | CHO rCHO (recombinant CHO) | Higher productivity of Human beta interferon Higher cell growth | [49,50] |
Rice protein hydrolysate | CHO-320 Human HepG cells | Protection against oxidation stress from hydrogen peroxide | [51,52] |
Soy peptones | CHO DG44 | Improved cell production | [53] |
Wheat hydrolysates | CHO | Improved cell viability | [54] |
Marine cyanobacterium Spirulina maxima | Human Lung Carcinoma | Improved cell viability and proliferation | [55] |
Chlorella vulgaris extract | CHO-K1 and MSC | Promoted cell growth | [56] |
Rapeseed caked | CHO-C5 | Promoted cell growth | [57] |
Silk sericin hydrolysate | CHO and Hela cells | Improved cell growth and proliferation | [58] |
Whey protein | CHO K1 JURKAT E6.1 | Improved cell viability and proliferation | [59] |
Natural Polymers | Synthetic Polymers | Combination of Natural and Synthetic Polymers |
---|---|---|
Anionic polymers: HA, alginic acid, pectin, carrageenan, chondroitin sulfate, dextran sulfate | Polyesters: PEG-PLA-PEG, PEG-PLGA-PEG, PEG-PCL-PEG, PLA-PEG-PLA, PHB, P(PF-co-EG) ± acrylates, P(PEG/PBO terephthalate) | P(PEG-co-peptides), alginate-g-(PEO-PPO-PEO), P(PLGA-co-serine), collagen-acrylate, alginate-acrylate, P(HPMA-g-peptide), P(HEMA/Matrigel®), HA-g-NIPAAm, GelMA |
Cationic polymers: chitosan, polylysine | Other polymers: PEG-bis-(PLA-acrylate), PEG ± CDs, PEG-g-P(AAm-co-Vamine), PAAm, P(NIPAAm-co-AAc), P(NIPAAm-co-EMA), PVAc/PVA, PNVP, P(MMA-co-HEMA), P(AN-co-allyl sulfo- nate), P(biscarboxy-phenoxy-phosphazene), P(GEMA-sulfate) | |
Amphipathic polymers: collagen (and gelatin), carboxymethyl chitin, fibrin | ||
Neutral polymers: dextran, agarose, pullulan |
Bioink | Cells |
---|---|
Printing pressure ↑ | ↓ Viability |
Nozzle diameter ↓ | ↓ Viability |
Printing time ↑ | ↓ Viability |
Degree of crosslinking ↓ | ↑ Density in bioink |
Viscosity ↓ | ↑ Density in bioink |
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Lanzoni, D.; Bracco, F.; Cheli, F.; Colosimo, B.M.; Moscatelli, D.; Baldi, A.; Rebucci, R.; Giromini, C. Biotechnological and Technical Challenges Related to Cultured Meat Production. Appl. Sci. 2022, 12, 6771. https://doi.org/10.3390/app12136771
Lanzoni D, Bracco F, Cheli F, Colosimo BM, Moscatelli D, Baldi A, Rebucci R, Giromini C. Biotechnological and Technical Challenges Related to Cultured Meat Production. Applied Sciences. 2022; 12(13):6771. https://doi.org/10.3390/app12136771
Chicago/Turabian StyleLanzoni, Davide, Filippo Bracco, Federica Cheli, Bianca Maria Colosimo, Davide Moscatelli, Antonella Baldi, Raffaella Rebucci, and Carlotta Giromini. 2022. "Biotechnological and Technical Challenges Related to Cultured Meat Production" Applied Sciences 12, no. 13: 6771. https://doi.org/10.3390/app12136771
APA StyleLanzoni, D., Bracco, F., Cheli, F., Colosimo, B. M., Moscatelli, D., Baldi, A., Rebucci, R., & Giromini, C. (2022). Biotechnological and Technical Challenges Related to Cultured Meat Production. Applied Sciences, 12(13), 6771. https://doi.org/10.3390/app12136771