9 responses · Click any row to expand · You can annotate any text with Hypothes.is
Zhuoran Du · University of New South Wales · 2026-05-06 — CM_01: $50/kg
Core questions
| CM_01 (Focal) | $/kg competitive cost estimate for 2036 | 50 |
| 80% CI lower bound | 30 | |
| 80% CI upper bound | 80 | |
| Reasoning | Raw material cost, management and R&D, risks | |
| CM_02 | Overall AW investment assessment | good |
| AW benefit per $100K — low estimate | 30 | |
| AW benefit per $100K — central estimate | 60 | |
| AW benefit per $100K — high estimate | 80 | |
| Reasoning | Will CM cause some new animal welfare problems? Should we treat the live cultured "meat" as one kind of animal? | |
| CM_10 | Probability net AW benefit > alternatives (%) | 40 |
| 80% CI lower bound (%) | 10 | |
| 80% CI upper bound (%) | 50 |
Background & other
| Interest in future elicitation | yes |
Elliot Swartz · GFI · 2026-05-06 — CM_01: $25/kg
Core questions
| CM_01 (Focal) | $/kg competitive cost estimate for 2036 | 25 |
| 80% CI lower bound | 18 | |
| 80% CI upper bound | 40 | |
| Reasoning | Media costs will be quite low. Questions remain around productivity and capital costs. | |
| CM_02 | Overall AW investment assessment | excellent |
| AW benefit per $100K — low estimate | 200 | |
| AW benefit per $100K — central estimate | 500 | |
| AW benefit per $100K — high estimate | 1000 | |
| Reasoning | You need a viable alternative if you want to change entrenched systems |
Technical subquestions
| CM_12 | Hydrolysates in food-grade basal media by 2036 (%) | 20 |
| CI lower (%) | 10 | |
| CI upper (%) | 70 | |
| Comment | Hydrolysates may become incorporated in a decent number of manufacturer's media formulations over the next decade. It is unlikely you'd fully replace purified AAs. You'd still likely need to supplement them in. It's also unclear if hydrolysates are truly cost beneficial. | |
| CM_13 | Growth factor cost ($/kg output) | 1 |
| Comment | GFs are likely to play a minimal role in driving cost a decade from now. | |
| CM_14 | Basal media cost ($/kg output) | 8 |
| CM_16 | Cell productivity — low (kg/m³/day) | 1 |
| Cell productivity — central (kg/m³/day) | 2.25 | |
| Cell productivity — high (kg/m³/day) | 3 | |
| Comment | Most of these are really only achievable using perfusion | |
| CM_17 | Food-grade media adoption by 2036 (%) | 98 |
| Comment | The only reason it's not 100% is to allow for the use of certain feed-grade components, e.g., to form a "cultivated meat-grade" standard. | |
| CM_20 | Build-or-buy bioreactors — % building own (%) | 10 |
| Comment | Needs clarification. Many companies are likely to have input on the design of reactors, but are unlikely to build them themselves. |
Expert distribution mode
| E5 — Process mode | Fed-batch probability (%) | 20 |
| Perfusion probability (%) | 50 | |
| Continuous probability (%) | 30 | |
| E6 — GF innovation | Precision fermentation (%) | 80 |
| Plant farming (%) | 10 | |
| Autocrine signalling (%) | 50 | |
| Small molecule mimetics (%) | 80 | |
| Thermostable GFs (%) | 80 | |
| E7 — Feed conversion | Discussion | It is pretty important. FCR may differ between "lean" cells and fat cells. A target lower boundary is likely around 3:1 kcal in/out. Metabolic engineering/adaptation and media optimization play a major role in determining this. Processes will need efficient conversion if they aim to be cost-competitive. |
Background & other
| Biology/life science | 1 |
Stefano · Bruno Cell S.r.l. · 2026-05-07 — CM_01: $100/kg
Core questions
| CM_01 (Focal) | $/kg competitive cost estimate for 2036 | 100 |
| 80% CI lower bound | 80 | |
| 80% CI upper bound | 200 | |
| Reasoning | Growth medium costs, bioprocessing efficiency, scaffolding solutions. | |
| CM_02 | Overall AW investment assessment | uncertain |
| AW benefit per $100K — low estimate | 40 | |
| AW benefit per $100K — central estimate | 150 | |
| AW benefit per $100K — high estimate | 200 | |
| Reasoning | If research obtains a real scale up of CM and this impacts meaningfully on intensive farming, CM would have a much higher impact, making it probably the best investment for AW. | |
| CM_10 | Probability net AW benefit > alternatives (%) | 92 |
| Reasoning | Considering the revolution that a large scale CM adoption would be, the trade off is so high in my opinion. |
Technical subquestions
| CM_12 | Hydrolysates in food-grade basal media by 2036 (%) | 81 |
| CM_13 | Growth factor cost ($/kg output) | 5 |
| CM_14 | Basal media cost ($/kg output) | 9 |
| CM_16 | Cell productivity — low (kg/m³/day) | 1 |
| Cell productivity — central (kg/m³/day) | 3 | |
| Cell productivity — high (kg/m³/day) | 5 | |
| Comment | Fed-batch, with many doubts about sterility and efficiency. | |
| CM_17 | Food-grade media adoption by 2036 (%) | 90 |
| Comment | Keeping pharma grade makes no sense | |
| CM_20 | Build-or-buy bioreactors — % building own (%) | 94 |
Expert distribution mode
| E6 — GF innovation | Precision fermentation (%) | 82 |
| Plant farming (%) | 83 | |
| Autocrine signalling (%) | 86 | |
| Small molecule mimetics (%) | 58 | |
| Thermostable GFs (%) | 96 | |
| E7 — Feed conversion | Discussion | It is very important, I think TEAs shoud adequately account for this and you should focus on the second approach |
Background & other
| Prior calibration training | no | |
| Interest in future elicitation | possibly | |
| Other thoughts | I think that undifferentiated products will not be enough to attract consumers, differentiated products are needed. |
Claire Bomkamp · GFI · 2026-05-08 — CM_01: $60/kg
Core questions
| CM_01 (Focal) | $/kg competitive cost estimate for 2036 | 60 |
| 80% CI lower bound | 30 | |
| 80% CI upper bound | 90 | |
| Reasoning | I'm less certain about capex costs than ingredient costs in general. |
Technical subquestions
| CM_12 | Hydrolysates in food-grade basal media by 2036 (%) | 40 |
| Comment | I'd say it's likely that hydrolysates will contribute to a substantial portion of the basal media used at this time, but almost certainly supplemented by some amount of purified amino acids. I suppose I would say I'm pretty confident (~80 or more?) that both hydrolysates and purified AAs will play substantial roles, but I'm not confident at all in what that breakdown will be - could easily be 30/70, or 70/30. | |
| CM_14 | Basal media cost ($/kg output) | 28 |
| CM_17 | Food-grade media adoption by 2036 (%) | 85 |
| Comment | The switch to food-grade ingredients represents a very substantial "low hanging fruit" cost reduction opportunity, both in the sense that it's an easier technical problem than many of the others and the cost differential is quite high. I would therefore expect that few products beyond the very earliest ones launched would use substantial amounts of pharma-grade ingredients. I would entertain the idea that there might be a few hold-out ingredients that for some reason are hard to substitute, but if we're talking about the composition of the bulk of the media, this is one I'm fairly confident in. If a substantial portion of products are using substantial amounts of pharma-grade inputs, that probably means that cultivated meat hasn't made much progress (in terms of scale-up, cost reduction, adoption, etc.) by 2036. | |
| CM_20 | Build-or-buy bioreactors — % building own (%) | 30 |
| Comment | In an ideal world, I think we would see a substantial proportion of companies using fit-for-purpose bioreactors built by B2B companies, as this is a pretty substantial thing for each individual company to take on themselves. I would actually expect this number to go up as companies move away from pharma-grade bioreactors, but then come back down as non-pharma B2B options improve. Predicting the exact trajectory is difficult though, so pretty low confidence on this one. |
Expert distribution mode
| E6 — GF innovation | Precision fermentation (%) | 77 |
| Plant farming (%) | 59 | |
| Autocrine signalling (%) | 25 | |
| Small molecule mimetics (%) | 42 | |
| Thermostable GFs (%) | 35 | |
| E7 — Feed conversion | Discussion | At the very least, it will be necessary to account for the moisture content (and ideally, the caloric density) of the input and product. If these are defined, then $/L and L/kg effectively give you a feed conversion ratio. |
Background & other
| Biology/life science | 1 | |
| Prior calibration training | no | |
| Interest in future elicitation | more_info | |
| Other thoughts | It seems like a very reasonable decision to simplify the discussion by limiting it to undifferentiated cell mass, but differentiation does seem like a pretty important thing to consider in the future, as it could substantially change the cost calculation but also may be quite important from a sensory perspective. |
FN · 2026-05-08 — CM_01: $1/kg
Core questions
| CM_01 (Focal) | $/kg competitive cost estimate for 2036 | 1 |
| CM_02 | Overall AW investment assessment | good |
| AW benefit per $100K — central estimate | 60 | |
| Reasoning | consumer acceptance at large scale, and government willingness to support/incentivise this alternative way of producing meat | |
| CM_10 | Probability net AW benefit > alternatives (%) | 30 |
| Reasoning | Short term I believe funding CM will not exceed the benefit of AW campaigns. However long term (>10 years) it will, since research and development of this technology together with consumer adoption, will provide a longer-term benefit. I believe however that all these interventions (campaigns, dev of alternatives) need to go hand in hand, so I would not deprioritise one over the other |
Expert distribution mode
| E6 — GF innovation | Precision fermentation (%) | 60 |
| Plant farming (%) | 5 | |
| Autocrine signalling (%) | 90 | |
| Small molecule mimetics (%) | 70 | |
| Thermostable GFs (%) | 50 |
Background & other
| Biology/life science | 1 | |
| Other thoughts | Cultivated meat is not a short-term solution or intervention, and I don't think it should be seen as such. Investment in research in the field is crucial to transform it into a reality, but I think expectations should be managed accordingly - otherwise we will end up in the same situation we are now: early investors in the field were promised that CM will reach the market fast, and due to technical challenges it did not happen; therefore investors lost trust in the field because their expectations were not met. CM research should be funded in a way that ideally makes it more independent from investor pressure, to allow the field to grow a bit more organically and with more collaboration. |
CM_TEA_T · (identified as: Matt McNulty) · Tufts · 2026-05-08 — CM_01: $10/kg
Core questions
| CM_01 (Focal) | $/kg competitive cost estimate for 2036 | 10 |
| 80% CI lower bound | 2 | |
| 80% CI upper bound | 100 | |
| Reasoning | Largely based on 'vibes' having spent time in the field -- trying to get an answer in without much time to process systematically. Academic perspective, industry relations, fog of war. Validation of industry claims and further transparency of industry performance would be strong influence. Development-oriented R&D pubs from either academic or industry would be strong influence. | |
| CM_02 | Overall AW investment assessment | excellent |
| Reasoning | i need to better understand the alternatives here and their current/projected performance. CM has such massive potential, seems clearly highly-ranked on this basis alone | |
| CM_10 | Probability net AW benefit > alternatives (%) | 85 |
| Reasoning | depends on the time horizon of the benefit measure and how you compare benefit across different timepoints. long-termism, this is hard to beat IMO. Need to learn quite a bit more about alternatives, admittedly |
Background & other
| Prior calibration training | unsure | |
| Interest in future elicitation | possibly |
Aleksandra Fuchs · 2026-05-08
Technical subquestions
| CM_12 | Hydrolysates in food-grade basal media by 2036 (%) | 50 |
| CM_14 | Basal media cost ($/kg output) | 1 |
| CM_17 | Food-grade media adoption by 2036 (%) | 100 |
| CM_20 | Build-or-buy bioreactors — % building own (%) | 70 |
Expert distribution mode
| E6 — GF innovation | Precision fermentation (%) | 100 |
| Plant farming (%) | 100 | |
| Autocrine signalling (%) | 20 | |
| Small molecule mimetics (%) | 5 | |
| Thermostable GFs (%) | 5 |
Background & other
| Biology/life science | 1 | |
| Prior calibration training | unsure | |
| Interest in future elicitation | possibly |
PersonABC · Industry · 2026-05-11 — CM_01: $20/kg
Core questions
| CM_01 (Focal) | $/kg competitive cost estimate for 2036 | 20 |
| 80% CI lower bound | 15 | |
| 80% CI upper bound | 30 | |
| Reasoning | Known Feed-Conversion-Ratios of about 20 L/kg biomass, target price of medium of 0.3 EUR/L, and costs of CAPEX. Changing FCR or medium costs will most likely reduce the price | |
| CM_02 | Overall AW investment assessment | uncertain |
| AW benefit per $100K — central estimate | 30 | |
| Reasoning | Plant-based alternatives of unstructured food are already viable and valid. IMO it would be needed to have structured CM products, to replace the whole cut meat. However, the technology for whole cut CM is not yet available at competitive prices | |
| CM_10 | Probability net AW benefit > alternatives (%) | 15 |
| Reasoning | 100k USD is not sufficient to move the needle in the industry, which is still under construction |
Technical subquestions
| CM_12 | Hydrolysates in food-grade basal media by 2036 (%) | 50 |
| Comment | If it is cheaper and there are large volumes of hydrolisates available (and I think so), CM should use those. However, it might take some time before we reach significant production with those ingredients, 2036 might be too soon | |
| CM_14 | Basal media cost ($/kg output) | 6 |
| Comment | Keeping FCR of about 20 and medium cost of 0.3, best case scenario the medium reaches 0.1 EUR/kg and more realistically the price will settle around 0.5 EUR/ L (considering 1 EUR~1 USD) | |
| Comment | Most likley perfusion will be the dominant technology, although probably continous bioprocess should be ideal (assuming to effectively reduce contamination) | |
| CM_17 | Food-grade media adoption by 2036 (%) | 100 |
| Comment | Pharma grade medium is not economically viable | |
| CM_20 | Build-or-buy bioreactors — % building own (%) | 30 |
| Comment | I do not think everyone has the expertise and time to build their own bioreactors (if there is VC money involved, there is little time to try and learn how to make a bioreactor in-house) |
Expert distribution mode
| E6 — GF innovation | Precision fermentation (%) | 50 |
| Plant farming (%) | 15 | |
| Autocrine signalling (%) | 70 | |
| Small molecule mimetics (%) | 90 | |
| Thermostable GFs (%) | 30 | |
| E7 — Feed conversion | Discussion | FCR must be taken into account, without this parameter it is unlikely to have a clear idea on the unit price of the medium per kg of biomass. This number also varies for undifferentiated and differentiated cells, and it would be necessary to understand how much is the variation and if there is a medium cost target to achieve to make this difference irrelevant on the final CM price |
Background & other
| Biology/life science | 1 | |
| Prior calibration training | no | |
| Interest in future elicitation | more_info |
Andrew Stout · 2026-05-12 — CM_01: $8/kg
Core questions
| CM_01 (Focal) | $/kg competitive cost estimate for 2036 | 8 |
| 80% CI lower bound | 4 | |
| 80% CI upper bound | 12 | |
| Reasoning | I based this off of numbers that I think are fair for certain key metrics in 2036: |
Technical subquestions
| CM_12 | Hydrolysates in food-grade basal media by 2036 (%) | 50 |
| Comment | I think that hydrolysates are an incredibly attractive option; however, I'm not sure that ultra-low-cost purified amino acids aren't equally likely. | |
| CM_13 | Growth factor cost ($/kg output) | 0 |
| Comment | I do not think that growth factors will be needed for production in 10 years. The upper bound is defined by necessity; the only way GFs will stay in the process is if they can be cheap enough to very minimally impact total price. | |
| CM_14 | Basal media cost ($/kg output) | 4 |
| Comment | This is essentially the first term in my initial equation, so approximately 3.8 usd/kg. | |
| CM_16 | Cell productivity — low (kg/m³/day) | 12.5 |
| Cell productivity — central (kg/m³/day) | 37.5 | |
| Cell productivity — high (kg/m³/day) | 62.5 | |
| Comment | I think that a fill-and-draw process maximizes simplicity and productivity. My numbers here assume a 50% harvest from the total vessel daily, and a 24 hour doubling time (so the vessel reaches max density again the next day). | |
| CM_17 | Food-grade media adoption by 2036 (%) | 100 |
| Comment | I see no reason why this would not be 100%; I think it will get there far before 2036 | |
| CM_20 | Build-or-buy bioreactors — % building own (%) | 10 |
| Comment | I think there will always be a push to simplify by buying reactors and verticalizing that expertise. Very few industries build their own production equipment (if any?). My thought that there will be some here is based on the fact that I think there will still be innovation/new approaches being developed in 2036. At full maturity, I think a vanishingly small number of meat producers will make their own reactors. |
Background & other
| Biology/life science | 1 | |
| Prior calibration training | no | |
| Interest in future elicitation | no |