Hydrogen Production Through Electrolysis of Water
One way to produce hydrogen for transportation fuel is through the technique of electrolysis. In the past, electrolysis has been too inefficient and too expensive to be economically competitive. However, research shows that electrolysis is more efficient when conducted with water existing in a supercritical state. This requires that it is both hotter than 374C and at a pressure above 220 bar (a “bar” is very close to the atmospheric pressure at sea level). Therefore, electrolysis of water becomes more efficient when performed at supercritical temperatures and pressures. This is partly because at high temperatures, the additional heat replaces some of the electricity that is required for electrolysis at a lower temperature.
The efficiency of electrolysis is also decreased by what is known as overpotential, which takes three forms:
- the activation overpotential, caused by rate limiting steps.
- the concentration overpotential, caused by a drop in concentration at the electrode. surface relative to the bulk phase due to mass transport limitations
- the ohmic overpotential, caused by the resistivity of the electrolyte.
These overpotential issues can be alleviated to some extent by certain changes in several of the properties of water as it transitions from a liquid to a supercritical state, including:
- that the viscosity of supercritical water is lower than that of liquid water by a factor of 10 or 20
- that the dielectric constant of supercritical water is about an order of magnitude lower than that of water at standard conditions
- that the specific conductance of supercritical water is several orders of magnitude higher than that of liquid water
- that supercritical water has virtually no surface tension
- and that the density of supercritical water is much higher than that of steam.
Electrolysis is also more efficient when the pressure of the feedwater is raised to the desired pressure for the hydrogen prior to the electrolysis, rather than pressurizing the gas following the electrolysis. Current systems for transporting and dispensing hydrogen are designed to operate at 700 bar, which is much more than the critical pressure of water. This means that pressurization of the feedwater for electrolysis is not a waste of energy, but simply an efficient step toward reaching the standard operating pressure for the gas. Such pressurization of the feedwater would be less expensive because it is more efficient to pressurize liquid water than gaseous hydrogen. This is in particularly the case, given the fact that inexpensive electricity is already present when geothermal generation and electrolysis are combined.
Key application focus point: Where available, use geothermal brine resources above the critical temperature of water to heat the clean feedwater, after its pressure is raised above the critical level, to a temperature above critical temperature, and achieve maximum efficiency and minimum cost.
Moreover, electrolysis can be cut back to operate at less than 10% of capacity without a significant loss of efficiency, and these cut backs can be performed in less than 2 seconds. The electricity that would power the electrolysis can instead be switched to provide electricity to the grid immediately. Other research has found ways to decrease the cost of the electrodes that are needed, which will reduce the cost of electrolysis even further. This means geothermal wells can run in baseload fashion, as they should. Thus, electricity is then used to balance the grid and to produce hydrogen, by using the geothermal energy for the generation of electricity and the electrolytic production of hydrogen.
The nuclear industry has promoted the development of solid oxide electrolytic cells for high-temperature electrolysis, but they require temperatures of 800°C to 900°C to achieve maximum efficiency. However, temperatures that high shorten the useful life of the materials used in the electrolysis. Recent tests have observed long-term performance degradation rates of 3.2% to 4.6% per thousand hours of operation. These rates are simply too high to be acceptable. Nevertheless, recent advances in ceramic proton conducting membranes for electrolytic cells make it possible to design, construct, and operate electrolytic cells that use supercritical water very efficiently, without requiring 800°C to 900°C temperatures.
Hydrogen inventories will be equivalent to storage, from the perspective of electricity generation. These will serve as a replacement for fossil fuels for transportation and heating, which has always been produced for and drawn from inventory. Hydrogen will open a whole new market for the geothermal industry, and one that can be expected to grow rapidly for the foreseeable future in favorable locations where high-temperature geothermal fluids can be found, such as the Salton Sea as noted in an earlier post.
Our team works since 2005 on projects for low-cost hydrogen and stoichiometric oxygen-hydrogen (SOH) gas production by pulse-current-modified water electrolysis. Starting at 9Wh/L in 2005, now we have invented a special small electrolysis cell and a method, producing SOH with 0.4h/L (0.9kWh/kg) and pure hydrogen with 1.1Wh/L (12.3 kWh/kg) power, which makes the cost of production less than a dollar per kg H2. SOH’s cost is even lower, because it needs 9 times less power per kg for its production.
We use special electronic devices for cutting the current supply into tiny shock pulses of about 1 millisecond, followed by ~99ms silent period with NO power supply, but with still continuing gas production, thanks to the previous electrodes’ activation by the shock pulse.
These cycles are repeated 10 times in a second.
We have also experimented with the stoichiometric ultrasono-modified oxygen-hydrogen (MOH) gas, patented in 2011 by Dr. R.Omasa from Japan, as Ohmasa Gas. —
http://www.patentsencyclopedia.com/app/20110139630#ixzz3LOxSiPwy ,
https://www.youtube.com/watch?v=NUPE0Z9V82E
MOH/Ohmasa can be compressed over 700bar, liquefied at 1bar/-178deg.C, filled and stored in CNG/LNG bottles for years, and shipped everywhere. 1m3 of liquid MOH conatins 167kg of H2 vs 70kg of H2 in 1m3 of liquid H2 alone, or 2.5 times more. Pure H2 and O2 could be extracted out of pressurized or liquefied MOH gas, on-board, on-demand and used for fueling HFCs.
MOH cannot be ignited by a spark and doesn’t perform leakages, permeation, diffusion and embrittlement as the pure hydrogen does. MOH can be burned in standard gasoline engines, gas-turbines, rocket engines, steam-boiler burners. It’s gas-plasma flame heats up some UHTC ceramics over 6,000deg.C (being only 140deg.C hot itself).
Due to these unique properties, we can say, that MOH is the ideal transportable clean fuel and the perfect H2-storage.
Grainis ltd. Hydrogen Bulgaria
5 Gen. Edward Totleben blvd., 1606 Sofia, Bulgaria
cell: +359 899171570 (9AM-9PM EET)
https://hydrogen.alle.bg
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