| Literature DB >> 33022109 |
Guo-Qiang Chen1,2,3,4, Xinyi Liu1.
Abstract
Microbial fermentations produce chemicals, materials, biofuels, foods and medicines for many years. The processes are less competitive compared to chemical industries. To increase its competitiveness, technologies must be developed to address the following issues including fresh water shortage, heavy energy consumption, microbial contaminations, complexity of sterile operations, poor oxygen utilization in the cultures, food-related ingredients as substrates, low substrate to product conversion efficiency, difficult cells and broth separation, large amount of wastewater, discontinuous processes, heavy labour involvements and expensive bioreactors. Future industrial fermentations should be more effective with the above issues reasonably addressed. Recently, extremophilic bacteria have well addressed the above issues for future fermentation. 2020 The Authors. Microbial Biotechnology published by Society for Applied Microbiology and John Wiley & Sons Ltd.Entities:
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Year: 2020 PMID: 33022109 PMCID: PMC7888459 DOI: 10.1111/1751-7915.13674
Source DB: PubMed Journal: Microb Biotechnol ISSN: 1751-7915 Impact factor: 5.813
Comparison of current and future fermentation.
| Item | Current fermentation (CF) | Future fermentation (FF) | Note |
|---|---|---|---|
| Microbial chassis: |
| Extremophilic bacteria, Methylotroph, CO and/or CO2 utilizers, Phototroph, et al | Engineering the chassis cells to grow fast on low‐cost carbon substrates and mineral salts |
| Sterilization | Yes | Not needed | FF reduces energy consumption |
| Contamination | By bacteria, fungi or phages | No | Absence of phage receptor |
| Fresh water | Heavy consumption | Seawater or fresh water recycling | Saving fresh water |
| Growth process | Batch or fed‐batch | Batch or fed‐batch or continuous | Improving process efficiency |
| Substrates (S) | Mostly glucose, fatty acids | Diverse: mixed‐substrates, starch, gases | Reducing substrate cost |
| Product (P) | Usually one product | Intra‐and/or extracellular products | Increase process efficiency |
| S to P ratio | Reasonable | Better | Improve process economy |
| Wastewater | Discharged and treated | Recycled | Reducing wastewater |
| Downstream | Complicated | Convenient via morphology engineering | Reducing downstream cost |
| Aeration | Intensive with high energy demands | Light aeration via haemoglobin expression | FF reduces energy consumption |
| O2 demand | Usually very high | Micro‐ or anaerobic (facultative aerobic) | Increase process efficiency |
| pH for growth | Narrow pH, neutral or weak acidic | Wide pH ranging from 3‐11 | For easy growth control |
| Temperature | 30–40°C | 20–85°C | For easy growth control |
| Osmotic pressure | Low to mild | Low to high | For easy growth control |
| Bioreactor | Made from stainless steel | Plastics, ceramics, cements or stainless steel | FF reduces equipment cost |
| Automation | Half automation | Full automation with AI deep learning | Improving process consistency |
| Aggregation | Usually not | Usually desirable | Easy cells and broth separation |
| Induction | Gene expression induction difficult in late growth | Induction at high cell density possible | Delaying harmful cell processes |
| Cell lysis | Physical process | Inducible cell lysis | Recovery of intracellular P |
| Labour | Well educated and trained | Only simple training required | No‐sterilization and automation |
Fig. 1The future fermentation process. Future fermentations will be conducted under non‐sterile and continuous conditions controlled by artificial intelligence with reduced water and energy consumption. Process economy will also be improved by more substrates to product conversions and multiple product generation as well as morphology engineering for easy downstream separations. Investment can also be reduced by using low‐cost materials for bioreactor constructions.