Get at me if you're 'bout it: eng at clayrichardson.me
122 karma · joined January 21, 2012
Email: yo at my domain
Get at me if you're 'bout it: eng at clayrichardson.me
Poloniex, Bitfinex and BitMex are some of the places you can play that game. You can even become a BTC lender on some of those exchanges and get around 20% APR since loans can be compounded every 1-2 days or even shorter depending on the duration of positions people open.
Are you talking about just the water generator, or the "civilization-in-a-box" collection of modules?
Can you point me in the direction of this project? I'd like to see what the current implementation looks like.
> (or even ice cubes and a glass) you can achieve the same thing.
We're trying to do it at scale and improve on the technology.
> real issues behind water scarcity, which has nothing to do with a shortage of liquid water
Can you elaborate on this point?
Definitely not novel at this stage, but once we modify the AWG to achieve water reclamation from urine, would that be considered novel?
The next milestone is to create open source designs for larger-scale, commercially available machines that are prohibitively expensive, and improve upon them. The machines exist and there is a market for them. Is it not worth the time and effort to increase access to technologies like this?
Not just knowledge of chemistry, but actively developing eyedrops to cure cataracts :)
http://www.viewpointtherapeutics.com/team/
EDIT: Wording. Added question.
If you end up beating me to it: https://github.com/openawg/openawg/pulls
When I was drafting it in Google Docs, I was using footnote annotations, and I just copypasta'd it over.
Ideally, we'd like to use a gasifier for carbon negative power generation, as local biomass can be utilized.
Does this make sense, or do you have a more effective approach?
There is always more to read up on and calculate :)
EDIT: The current dehumidifier does accumulate ice on the evaporator coils, depending on the ambient conditions. Once enough ice has accumulated, the compressor turns off and the ice melts into the collection tray. I'm assuming we have to depose the ice out of the dry atmosphere at BRC, since the dew point is below the freezing point of water. Is this not the case?
I wonder how the current primary and secondary drinking water regulations came to be.
The pump were using right now consumes 104 W intermittently. For our next prototype, we're going to use a condenser unit from a walk-in freezer (1168W), a split A/C unit to pretreat the air (560W) MinnowBoardMax (15W), duct fan (208W), etc.
A good way to increase the efficiency of this machine would be to increase the relative humidity by adding moisture. This is the reasoning behind our next planned experiments of reclaiming water from urine!
You might be able to get away with using the reverse osmosis system we have, [0] but send the water to a lab to test influent (intake) and effluent (output) before consuming :D
[0]: http://123filter.com/catalog/ispring-7-stage-75-gpd-reverse-...
The initial proof-of-concept I threw together with spare parts actually used a spare TEC (19911-5L31-15CQ) [0] I had laying around. [1]
[0]: http://www.customthermoelectric.com/tecs/pdf/19911-5L31-15CQ... [1]: https://openawg.github.io/2016/01/27/blueice-alpha.html
We'd like to be able to gather metrics from these machines all over the world, and identify trends in things such as the weather, water production and consumption, efficiency, power generation and carbon sequestration, as well as identify opportunities to improve the operation of the machines through software updates.
Dehumidifiers are not designed to produce potable water.
Adding a filtration system removes the contaminants from the non-food grade components and anything else which was once floating in the air.
I'm not sure how to determine the practicality of well excavation, but my intuition tells me it largely depends on geographically influenced factors. I'll look into that.
With 32.2C ambient, 14% RH, 1.35C DWP, the absolute humidity is 4.78 g/m^3
With 24.4C ambient, 14% RH, -4.80C DWP, the absolute humidity is 3.12 g/m^3
Absolute humidity here is specified as grams of water per cubic meter of air.This is similar to the AH at BRC. Our current model assumes a DWP of -10C — 10C, so we can predict similar performance. We're not taking into account volumetric capacity and the thermal interface of the heat exchangers. If you know anyone able to help point us in the right direction with those calculations, it would be much appreciated!
Our current understanding is the enthalpy of vaporization + fusion for water is (2257 + 333.55) = 2590.55 J/g we want to pull out of the air. This is assuming we can process enough air, since the dew point is below freezing a fair amount of the time.
This is by using this equation specified in the NASA technical note [0]:
=((0.21668*((TMPC+273)^-1))*((DWPC+273)^-4.9283)*(10^(23.5518+(-2937.4/(DWPC+273)))))*1000
[0]: http://www.nasa.gov/centers/dryden/pdf/87878main_H-937.pdfEDIT: Formatting is hard. Added source. Clarification.
EDIT: Spelling is hard. Clarification is hard.
If it takes a lot of energy, and we implement carbon-negative power generation, then we increase the rate of carbon sequestration :)