1. Field of the Invention
The invention relates to a method of filling the primary sector of a nuclear reactor with inert gas rather than water for managing the temperature of the fuel rods which generate heat by fission of radioactive material contained wuthin them. This allows running the reactor at the critical temperature of water (374° C.) without additional pressurization to keep in liquid phase water at extremely high temperatures.
2. Discussion of the Related Art
U.S. Pat. No. 7,631,506, DuBrucq, introduces uses of just evaporated Nitrogen for a range of fire and crises control means that apply here as it maintains the thermal levels in the primary sector of the steam generator nuclear reactors.
U.S. Application 20080196411, Yukievich, Mikhial, Nuclear Reactors and Steam Generators uses liquid metal has heat transfer agent from fuel rods in Primary sector for steam generation in Second sector allowing extremely high temperatures of operation.
U.S. Pat. No. 6,902,709, Harada et.al. uses Nitrogen to make ammonia to capture hydrogen generated in the reactor primary sector which is not related to this patent.
U.S. Pat. No. 5,308,489, Tate et.al. uses Nitrogen gas for air cooling the water in the primary sector by cooling the external side of the containment wall. This also does not conflict with the concept of the present application.
U.S. Application 20080181351, Hosokawa et.al. infuses gaseous Nitrogen to reduce dissolved Oxygen level in Primary Sector cooling water—again not related.
U.S. Application 20060056572, Lecomte, Michel, has a gas generator using Helium as the primary sector coolant and a mixture of Helium with 50-30% Nitrogen gas in the secondary sector of nuclear reactors with gas generators—again not related.
U.S. Application 20100236284, DuBrucq, Preserving Liquid in Cryogenic Processes speaks to the purification section of the Nuclear Reactor apparatus described here with the major focus at the use with Nitrogen gas coming from condensation situations of fuel harvesting from oil shale, landfill and Methane hydrate substances.
The need has arisen to provide a method of cooling nuclear fuel rods with pure, inert gas evaporated from its liquid form. The most efficient and cost effective choice is Liquid Nitrogen sourced Nitrogen gas used for the Primary Sector which directly contacts the fuel rods with pure Nitrogen molecules rather than the polluted water normally used with steam generators.
Additionally, using inert gas allows unpressurized heating of the Secondary stage which generates the steam for the electrical power generator if operating the Primary Sector at 374° C., the critical point of water.
Additionally, by speeding or slowing the influx of Nitrogen gas from Liquid Nitrogen, the fuel rod environment can be maintained between ends of a temperature range for best power generation with only the adjustment of flow rate.
Additionally, the products of fission and any other reaction products of the fuel rods can be eliminated from the Primary Sector by pulling particles from the Nitrogen gas and cooling it down condensing out the Ntirogen even freeing Hydrogen, Helium and Neon that might emerge from the fission reaction. These materials can be collected and controlled for properly disposing of materials radioactive or not by selling pure material.
Additionally, without having to rely on a body of water to cool the water bathing the fuel rods, the location of the nuclear reactor can be secure with just shielding of the fuel rod and steam and power generator sections from heat detecting probes.
Additionally there is the possibility of reducing the size of the nuclear power generator with the Nitrogen cooling Primary Sector to a size that could power a train or boat or aircraft, while still keeping the radiation associated with nuclear facilities away from passengers and crew and cargo that might be effected by radiation.
Additionally the nuclear facility could be underground increasing the safety and putting it closer to the end user of the power, thus reducing the need for a power grid structure that when damaged, shuts down sections of the country as practiced in the USA.
Additionally, the nuclear reactor could be on board a spacecraft where temperatures in darkness can reach −270° C., sufficient to freeze the Nitrogen to a solid at −210° C., in two forms at −237° C. and to take it to liquefying temperature at −195.8° C. as one gets into the light allowing minimum mass for electrical power creation.
And, finally, additionally, to have purity of coolant in the fuel rod area allowing collection of byproducts of nuclear reactions to be amassed for sale or research uses.
These and other advantages and features of the invention will become apparent to those skilled in the art from the detailed description and the accompanying drawings. It should be understood, however, that the detailed description and accompanying drawings, while indicating preferred embodiments of the present invention, are given by way of illustration and not of limitation. Many changes and modifications may be made within the scope of the present invention without departing from the spirit thereof, and the invention includes all such modifications.
Preferred exemplary embodiments of the invention are illustrated in the accompanying drawings in which like reference numerals represent like parts throughout, and in which:
    
    
    
    
Turning now to the drawings and initially to 
The process in the Primary Sector 1 is as follows: The pure, inert gas at cryogenic temperature enters the Primary cylinder 10 at the twin inputs 12 feeding fresh gas into the contained gas 11 to absorb the heat generated by the fuel rods 4. As the temperature reaches 374° C., the critical temperature for water keeping it all vapor, steam, the hot gas from around the fuel rods rises up to the top plate 14 and flows into the hot gas pipes 20 heating the radiator 21 to the critical temperature so water in the Secondary Section 2 converts to steam. Some radiators have an exit pipe 27 to heat another segment of radiator. The gas, then cooled from heating the radiator(s), leaves via the cooled gas pipes 22 which takes the cooled gas to the base 5 of the Primary Section where it enters the Primary section 23 cycling the gas to again be heated by the fuel rods.
The process in the Secondary Sector 2 includes the steam shell 26 which is fully insulated against heat loss to preserve the steam 24, generated on the radiators 21, which then passes to the steam generator 8 to drive the power generator.
Turning now to 
Looking at 
Looking, last, to 
To understand the workings of the cooling system for the fuel rods in the Primary Section 1 combined with the purifying section 3, there are only two adjustment valves needed, that controlled by the thermal regulator pacing the flow of Liquid Nitrogen 63 and the valve 37 opening the light gas exhaust to fill the mylar balloon or other light gas storage means 39 which just releases the light gases to reduce the volume in the cylinder so it can be further separated and sold with Hydrogen used to reduce Calcium compounds to Calcium metal if desired. (Reference here to DuBrucq patent application Ser. No. 11/825,992.) Helium and Neon are separated by density. The impure inert gas 7 is pulled from the Primary section 1 by the dropping out of air suspended grit 15 which precipitates and the condensing of material 31 contaminating the inert gas, most likely Nitrogen 11, drawing more gas from the Primary section 1. Then as the gas continues it releases light gases as Hydrogen, Helium and Neon which further pull the Nitrogen along. Finally the Nitrogen is mixed with Liquid Nitrogen in the mixer 61 which takes out the gaseous Nitrogen which is then replaced in the exhaust tube by more gas from the primary chamber.
Driving this pull of gas from the Primary section is the cryogenic side of the Nitrogen cycle where the Liquid Nitrogen is carried to the dewar from the Mixer and is apportioned with a valve to regulate the fuel rod environment temperature. It evaporates in the upper chamber over the exhaust gas chamber cooling it after condensing out impurities and before the light gas release. The cryogenic, pure, inert Nitrogen passing up the tubes over the exhaust tube cools it to implement impurity condensing and then passes into the Primary chamber 1 to cool the fuel rods as fission reaction in them heats the environment.
The water cycle in the system is driven by the heated radiator units 21 converting water drops 77 into steam 70 in the Secondary chamber and passed on to the Steam Power Generator chamber 8 where with power transfer it condenses into water 71 and is collected in the water catch 72 and collecting tube 73 where it can be pumped back into the secondary chamber and passed through a sieve 76 to rain onto the radiator units 21, or, to purify the water, can be frozen into ice cubes in the cryo-chamber 3 and passed back into the steam chamber 2 to melt and run through the sieve 76 and rain onto the radiators. Power here is by the pump 74 for the water coming from the collecting tube 73 or the lift 84 for the ice cubes as well as the turning of the loop conveyor 80 for the ice cubers and the turning of the ice cube collector 83.
With the purification of both the inert gas, most likely Nitrogen, and water, the system can be kept free from contaminates and the fission products are eliminated being carried by the Nitrogen gas into the purifier. The thermal control is regulated by the rate of passage of the Liquid Nitrogen. The feed of Liquid Nitrogen can be increased with an external auxiliary feed into either the mixer 61 or the dewar 16. That would be part of a fixed fire control system for the Nuclear Power Plant facility preventing meltdown of the fuel rods. Fire fighting and crises control with Liquid Nitrogen is covered in DuBrucq's U.S. Pat. No. 7,631,506 and other pending applications.
Many changes and modifications could be made to the invention without departing from the spirit thereof. The scope of some of these changes can be appreciated by comparing the various embodiments as described above. The scope of the remaining changes will become apparent from the appended claims.
This is an expanded, but continued application of U.S. Pat. No. 7,631,506 stemming from the initial application Ser. No. 10/437,538, filed May 14, 2003, and entitled “Liquid Nitrogen Enabler.” Several additional DuBrucq applications on Nitrogen uses are referenced.
| Number | Date | Country | |
|---|---|---|---|
| Parent | 10437538 | May 2003 | US | 
| Child | 13134628 | US |