Difference between revisions of "Diamondoid heat pump system"

Revision as of 07:08, 23 November 2016

Simple cooling cycle with piston equipped gas filled pellets. SVG

Also Thermomechanical energy converter.

With advanced APM heat pumps systems for reaching liquid nitrogen or helium temperatures can probably be easily created. They could be made into desktop scale devices with nothing more than a power connection or more importantly integrated into nanofactories to gain more reliable mechanosynthetic operation with lower error rates.

[correction: the correct cycle is probably similar to the reverse otto cycle aka constant volume cycle]
Table of thermodynamic cycles: [1]

The air refrigeration cycle also known as Bell Coleman cycle or reverse Brayton cycle (see: heat pumps in general and "gas cycle diagram" ) is nice for diamondoid AP systems since high compression ratios are easily archivable and liquid nitrogen temperatures can be archived just by using ambient air

An easy to implement (but not optimal) gas cycle is like follows:

1. compress gas in thermal contact to the heat radiator to fluid densities (around ~1000bar)
2. let the generated compression heat dissipate into the environment
3. transport compressed gas inside through the thermal isolation layer while exchanging heat with out going gas (capsules)
4. expand gas in thermal contact to the isolated volume
5. let the now absent expansion heat be filled from the chamber (suck it cold)
6. transport expanded gas throug isolation layer while exchanging heat with the ingoing gas (capsules)
7. repeat the cycle

To reach liquid hydrogen or helium temperatures the compressed hydrogen/helium must be cooled below its inversion point or else the gas will heat up instead of cooling down when expanded. A two stage design with good thermal contact is then needed.

Gasses can be handled safely (without explosion hazard) in small small DMME capsules with lockable pistons. When oxid-ceramic diamondoid materials are used dry air instead of pure nitrogen should be safely usable.

To keep the capsules small in spite of the high compression ratios the capsules could employ three consecutively acutated pistons each compressing the enclosed gas by a factor of ten.

Since the capsules must be moved between two locations seperated by macroscopic distance the design (and the process steps) will be spread over multiple microcomponents.

The most difficult part is the thermal thermal isolation layer since diamond is pretty much the worst thermal isolator conceivable. If SiO₂ structures can be mechanosyntesized AP aereogel might be usable.

Cooling systems must be heterogenous makrosystems since thermal isolation worsens with shrinking system size.

Reversibility

Thermomechanical conversion can be near reversible. Burning fuel (especially at low temperature) is the "evil" step that devaluates energy and leads to a low Carnaugh-efficiency.

Possible application in a nanofactory: The cooling sandwich

In the lowest convergent assembly steps where mechanosynthesis happens cooling can drastically decrease error rates. Since it seems easy to do it it will likely be done. The special thing is though that thermal isolation doesn't work properly at the nanoscale. Thus the whole stack of bottom layers of a nanofactory (mechanosynthesis, crystolecule assembly and microcomponent assembly) may be packed in a sanwich of two macroscopic layers. The first one is there to cool down the raw molecular feedstock once it enters into machine phase from the bottom and the second one is there to recuperate the thermal energy when the assembled microcomponents come out the top. These sandwich layers need to be connected at some points to send energy from the top to the bottom energy. The energy conversion steps may be: thermochemical conversion then chemical transport then chemothermal conversion. This process can be highly reversible and will - once cooled down only - only need to remove waste heat from mechanosynthesis.

Related

• Energy conversion
• Entropomechanical converter
• Thermal metamaterial