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- chemengThis is really cool, I know a few different teams that have taken a look at similar approaches over the last 20 years, I hope you're able to make it work! I've been wanting something like this to succeed for a long time. Please take these questions (and assumptions) as earnest curiosity. I realize you may not be able to share answers if it touches anything proprietary.On the chemistry side: In step 1, you say using adsorbents, so i'm guessing some combo of iron oxide to desiccant to activated carbon for the siloxanes, and then maybe ZnO (based on your likely catalyst chemistry). At typical anaerobic biogas H2S concentrations, that's quite a bit of OPEX for media I imagine, and the risk of some breakthrough poisoning your reaction catalyst. Are you only working with partners that have desulfurization in place already? And how much attention do these skids need day to day, are you expecting full-time operator presence? Remote monitoring? How are you catching breakthrough before it takes out a catalyst charge?I'm guessing bi-reforming is partly how you tune your way out of the carbon deposition problem, but in my experience real biogas composition drifts around depending on what's going into the digester, so i'm curious how much margin you actually have on the H2O/CO2/CH4 ratio before you're back in the coking regime. Are you trimming steam in real-time based on gas composition or running fixed excess (further trading economics)? Was the bench-scale test run on a simulated dynamic biogas stream? Was there much activity decline over the run?On the economics side: DME into cosmetics seems like a great high-margin entry point. As you point out, most methanol is produced from large centralized plants, but they have real fixed-cost advantage that a modular approach structurally doesn't (along with storage and distribution headaches from many smaller production sites). Are you assuming some customers will pay a premium for the resilience of a distributed network? How much of the methanol case is cost reduction at your expected scale versus 45Z-type credits? And you probably can't share, but I'm curious the most you can pay a producer for their biogas and still pencil relative to RNG buyers who may be bidding for the same stream?
- Johnny_BonkCongrats! I've worked on a similar technology converting waste syngas to 3-hydroxy-butyrate for further applications. Unfortunately in my case, we couldn't see any valuable and scalable end products from that particular molecule but I'm excited to follow your journey. Best of luck!
- possiblyburritoCongrats on breaking ground. Curious about the electricity input side. Reforming is endothermic, so I assume the unit has a meaningful power draw. At a wastewater plant, do you run off the facility's existing service or do you need a utility upgrade, and can the unit ramp with power prices or does the catalyst want steady state? Asking because at small sites the electrical interconnection can quietly become the long pole even when the gas is free.
- ianm218This is very cool.I'm curious how hard the go to market in hard tech like this is? What is the long term economic model in terms of what you think the margin can be and what the incentives for plants to adopt this technology?
- arikrahmanCongrats. Will be watching with great interest!
- philipkglassHow much biogas per year would a site need to produce to justify installing a unit? How much on-site labor is needed to run it?
- cyberaxWhy biogas specifically? This should work fine with regular fossil methane, and it will de-risk your deployments. There are plenty of places in Texas that uselessly flare the natural gas instead of doing anything with it.
- jnmandalWe really need solutions like this if we are going to reverse atmospheric carbon the necessary amount to mitigate planetary catastrophe. Thanks for working on this. Good luck.
- QuitschquatBro this sound's great. Have you considered deploying it to Lulling, Texas? It constantly smells like ass^Wbiofuel
- anonundefined
- bluebic[flagged]