US20120002776A1 - Dry coolant for primary stage of nuclear reactors - Google Patents
Dry coolant for primary stage of nuclear reactors Download PDFInfo
- Publication number
- US20120002776A1 US20120002776A1 US13/134,628 US201113134628A US2012002776A1 US 20120002776 A1 US20120002776 A1 US 20120002776A1 US 201113134628 A US201113134628 A US 201113134628A US 2012002776 A1 US2012002776 A1 US 2012002776A1
- Authority
- US
- United States
- Prior art keywords
- water
- gas
- steam
- nitrogen
- nuclear
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Abandoned
Links
- 239000002826 coolant Substances 0.000 title claims abstract description 8
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 claims abstract description 79
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 52
- 229910052757 nitrogen Inorganic materials 0.000 claims abstract description 33
- 239000000446 fuel Substances 0.000 claims abstract description 28
- 239000007788 liquid Substances 0.000 claims abstract description 22
- 239000011261 inert gas Substances 0.000 claims abstract description 20
- 238000004519 manufacturing process Methods 0.000 claims abstract 2
- 239000007789 gas Substances 0.000 claims description 50
- 238000000034 method Methods 0.000 claims description 16
- 238000001816 cooling Methods 0.000 claims description 15
- 230000004992 fission Effects 0.000 claims description 12
- 229910001873 dinitrogen Inorganic materials 0.000 claims description 11
- 239000001307 helium Substances 0.000 claims description 7
- 229910052734 helium Inorganic materials 0.000 claims description 7
- SWQJXJOGLNCZEY-UHFFFAOYSA-N helium atom Chemical compound [He] SWQJXJOGLNCZEY-UHFFFAOYSA-N 0.000 claims description 7
- 239000001257 hydrogen Substances 0.000 claims description 6
- 229910052739 hydrogen Inorganic materials 0.000 claims description 6
- 229910052754 neon Inorganic materials 0.000 claims description 5
- GKAOGPIIYCISHV-UHFFFAOYSA-N neon atom Chemical compound [Ne] GKAOGPIIYCISHV-UHFFFAOYSA-N 0.000 claims description 5
- 238000006243 chemical reaction Methods 0.000 claims description 4
- 229920002799 BoPET Polymers 0.000 claims description 3
- 239000005041 Mylar™ Substances 0.000 claims description 3
- 230000001351 cycling effect Effects 0.000 claims description 3
- 239000002245 particle Substances 0.000 claims description 3
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims description 2
- 239000007791 liquid phase Substances 0.000 claims description 2
- 239000001301 oxygen Substances 0.000 claims description 2
- 229910052760 oxygen Inorganic materials 0.000 claims description 2
- 230000001105 regulatory effect Effects 0.000 claims description 2
- 238000012546 transfer Methods 0.000 claims description 2
- 238000007792 addition Methods 0.000 claims 1
- 230000009977 dual effect Effects 0.000 claims 1
- 125000004435 hydrogen atom Chemical class [H]* 0.000 claims 1
- 238000001802 infusion Methods 0.000 claims 1
- 230000007246 mechanism Effects 0.000 claims 1
- 229910052756 noble gas Inorganic materials 0.000 claims 1
- 238000007254 oxidation reaction Methods 0.000 claims 1
- 230000000630 rising effect Effects 0.000 claims 1
- 230000002459 sustained effect Effects 0.000 claims 1
- 239000000463 material Substances 0.000 abstract description 7
- 239000012535 impurity Substances 0.000 abstract description 5
- 239000006227 byproduct Substances 0.000 abstract description 2
- 230000002285 radioactive effect Effects 0.000 abstract description 2
- 238000011160 research Methods 0.000 abstract description 2
- 239000003153 chemical reaction reagent Substances 0.000 abstract 1
- 230000008569 process Effects 0.000 description 7
- 150000003839 salts Chemical class 0.000 description 6
- 238000013461 design Methods 0.000 description 3
- 238000010438 heat treatment Methods 0.000 description 3
- 150000002431 hydrogen Chemical class 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- 239000000047 product Substances 0.000 description 3
- QGZKDVFQNNGYKY-UHFFFAOYSA-N Ammonia Chemical compound N QGZKDVFQNNGYKY-UHFFFAOYSA-N 0.000 description 2
- UFHFLCQGNIYNRP-UHFFFAOYSA-N Hydrogen Chemical compound [H][H] UFHFLCQGNIYNRP-UHFFFAOYSA-N 0.000 description 2
- 238000007710 freezing Methods 0.000 description 2
- 230000008014 freezing Effects 0.000 description 2
- 238000003306 harvesting Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 230000005855 radiation Effects 0.000 description 2
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 238000009825 accumulation Methods 0.000 description 1
- 229910021529 ammonia Inorganic materials 0.000 description 1
- 238000003287 bathing Methods 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229940043430 calcium compound Drugs 0.000 description 1
- 150000001674 calcium compounds Chemical class 0.000 description 1
- 239000000969 carrier Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
- 238000009833 condensation Methods 0.000 description 1
- 230000005494 condensation Effects 0.000 description 1
- 239000011551 heat transfer agent Substances 0.000 description 1
- 230000004941 influx Effects 0.000 description 1
- 229910001338 liquidmetal Inorganic materials 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- NMJORVOYSJLJGU-UHFFFAOYSA-N methane clathrate Chemical compound C.C.C.C.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O.O NMJORVOYSJLJGU-UHFFFAOYSA-N 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000004172 nitrogen cycle Methods 0.000 description 1
- 239000003758 nuclear fuel Substances 0.000 description 1
- 239000004058 oil shale Substances 0.000 description 1
- 238000010248 power generation Methods 0.000 description 1
- 239000002244 precipitate Substances 0.000 description 1
- 239000012857 radioactive material Substances 0.000 description 1
- 239000000523 sample Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 230000003245 working effect Effects 0.000 description 1
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F42—AMMUNITION; BLASTING
- F42B—EXPLOSIVE CHARGES, e.g. FOR BLASTING, FIREWORKS, AMMUNITION
- F42B33/00—Manufacture of ammunition; Dismantling of ammunition; Apparatus therefor
- F42B33/06—Dismantling fuzes, cartridges, projectiles, missiles, rockets or bombs
-
- G—PHYSICS
- G06—COMPUTING; CALCULATING OR COUNTING
- G06Q—INFORMATION AND COMMUNICATION TECHNOLOGY [ICT] SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES; SYSTEMS OR METHODS SPECIALLY ADAPTED FOR ADMINISTRATIVE, COMMERCIAL, FINANCIAL, MANAGERIAL OR SUPERVISORY PURPOSES, NOT OTHERWISE PROVIDED FOR
- G06Q30/00—Commerce
- G06Q30/06—Buying, selling or leasing transactions
- G06Q30/0601—Electronic shopping [e-shopping]
-
- A—HUMAN NECESSITIES
- A62—LIFE-SAVING; FIRE-FIGHTING
- A62C—FIRE-FIGHTING
- A62C99/00—Subject matter not provided for in other groups of this subclass
- A62C99/0009—Methods of extinguishing or preventing the spread of fire by cooling down or suffocating the flames
- A62C99/0018—Methods of extinguishing or preventing the spread of fire by cooling down or suffocating the flames using gases or vapours that do not support combustion, e.g. steam, carbon dioxide
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T137/00—Fluid handling
- Y10T137/0318—Processes
- Y10T137/0396—Involving pressure control
Definitions
- 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.
- 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.
- the fuel rod environment can be maintained between ends of a temperature range for best power generation with only the adjustment of flow rate.
- 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.
- 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.
- 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.
- 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.
- FIG. 1 shows a rendition of a steam generating nuclear power plant showing the primary and secondary sectors plus the inert gas source and cooling regulation.
- FIG. 2 shows the cycling of the Nitrogen or other inert gas coolant to purify it and harvest the fission products and then liquefy the gas and evaporate it giving a pure, mono-element coolant for the primary section of the reactor.
- FIG. 3 shows the Steam Power Generator compartment with the steam condensing upon use and flowing into a collector with pump that recycles the water back into the Secondary Section which generates steam.
- water can accumulate salts.
- FIG. 4 shows the Steam Power Generator compartment with the steam condensing upon use and condensed water flowing into an ice cube generator which can remove salts from the water as the ice freezes. Not shown is a cube wash which eliminates the salts on the outer surface of the ice and the containers where they freeze. Coldness to freeze the water is achieved by freezing in the inert gas purifier.
- FIG. 1 shows the components of the nuclear reactor steam power generator as 1 the primary section of the reactor with fuel rods 4 in a container 10 flooded with inert gas 11 held on a base 5 ; the secondary section 2 which generates the steam 70 by having the radiators 21 at the critical temperature of water, 374° C.; the third section 3 recycles and purifies the inert gas.
- the final section 8 is the steam generator that creates the power.
- the power generator is not elaborated upon since this discovery only deals with creating sufficient steam to drive the generator which is of anothers' design. Details of 3 are given in FIG. 2 .
- 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.
- FIG. 2 the purifying process for the inert gas, the gas passing out of the Primary Sector from orifice 7 where wide passage 70 first implements dropping of particles carried by the gas dropping it down the cylinder 71 to the bottom accumulation 15 .
- the gas is cooled by proximity of the cryogenically cold gas pipes 30 , and as it cools, impurities which emerge from the fission process carried in the gas are condensed and held in thermal level segments 31 and then the gas passes through the used gas outlet 13 into the lower section 33 of the double chamber box where the used gas reaches cryogenic temperature—close to, if not at, ⁇ 195.8° C.
- the cryogenic used gas passes through the light gas separator 34 where the light gases, Hydrogen, Helium and Neon, rise in the Light gas cylinder 36 . As they collect the cylinder rises. To store these light gases, when the cylinder is lowered with valve 37 open, the light gases pass through the light gas storage tie 38 and into the light gas carriers 39 , suggest mylar balloons.
- the used gas with both heavier materials extracted and the light gases extracted then passes through the entrance 61 of the Nitrogen gas/Liquid Nitrogen mixer condensing the gas into liquid.
- the Liquid Nitrogen valve 63 driven by thermal controllers in the Primary Sector 1 adjusts the rate of flow of the liquid Nitrogen through the sieve unit 64 causing the Liquid Nitrogen to rain 65 into the upper chamber 32 , the gas input chamber, which then passes through the two pipes 30 cooling the exhaust gas as it warms and enters the Primary Sector 1 at the pure Nitrogen input 12 keeping the gas temperature around the fuel rods at the proper level.
- FIG. 3 not showing the steam power generator design since it is not part of this patent, the water cycle is illustrated in the Steam Generator Section 8 where steam 70 cools with use producing water 71 which is collected in the water collector 72 and passed into the collecting tube 73 , through a pump 74 which moves it upward allowing it to pass through the faucet 75 and into the sieve 76 which makes it fall like rain in drops 77 onto the radiator units 21 which convert it to steam 70 which drives the steam power generator.
- the water cycle is enhanced by freezing the water to eliminate salts from the water.
- the power generator section 8 has the steam 70 condensing into water 71 which is collected in the water catch 72 and passes down the collecting tube 73 . It then enters the cryogenic cold atmosphere of the inert gas purifier 3 so the water can freeze in the ice cubers 81 which are attached to the conveyor 80 moving in a loop.
- the collector tube 73 fills the ice cubers 81 with water 71 which freezes into ice cubes 82 .
- the ice cubes 82 are set on the ice cube collector 83 which turns and releases the ice cubes 82 to the ice cube lift 84 which carries them up into the Secondary Section 2 placing them in the sieve 76 where they melt and the water 71 rains down as water drops 77 falling on the radiator units 21 where they evaporate into steam 70 which passes on to drive the steam power generator, not shown. Salts in the water will move to the outside of the ice cube 82 or stick in the ice cuber 81 . The salts can be washed in the process, but this process is not shown.
- 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.
- 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 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 .
- the system 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.
Landscapes
- Business, Economics & Management (AREA)
- Engineering & Computer Science (AREA)
- Accounting & Taxation (AREA)
- Finance (AREA)
- General Business, Economics & Management (AREA)
- Marketing (AREA)
- Strategic Management (AREA)
- Physics & Mathematics (AREA)
- Economics (AREA)
- General Physics & Mathematics (AREA)
- Development Economics (AREA)
- Theoretical Computer Science (AREA)
- Manufacturing & Machinery (AREA)
- General Engineering & Computer Science (AREA)
- Filling Or Discharging Of Gas Storage Vessels (AREA)
- Separation By Low-Temperature Treatments (AREA)
Abstract
Nuclear reactors are customarily cooled by water from a natural source in the area. Water brings impurities to and surrounds the fuel rods with a mix of materials, some of which react with the fuel rod contents. Changing the coolant to a pure, inert gas sourced from its cryogenic liquid form with ambient pressure gives greater control of the situation and enables running the reactor at the critical point of water so the cycle of coolant is released to the purifier carrying whatever material is expelled by the fuel rods and the steam cycle leaves the radiator from the reactor chamber as steam leaving little, if any, water release from the nuclear plant with no impurities but what is emitted by the fuel rods themselves contaminating the rod environment. Eliminating the hot water surrounding the plant, security of the Nuclear site is greater since infrared sighting is prevented with shielding just the reactor. Reactor byproducts can be separated and isolated to protect the environment and provide radioactive reagents for research. Liquid Nitrogen availability also provides the fixed fire and crises control for the entire facility eliminating water damage and electrical arcing keeping the computer and control system functional through crises situations. It is predicted that running the Nuclear reactor at 374° C., the critical point of water, can make a smaller system for the same level of power production from a steam generator and can provide mobility of the system is small scale.
Description
- 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.
- 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:
-
FIG. 1 shows a rendition of a steam generating nuclear power plant showing the primary and secondary sectors plus the inert gas source and cooling regulation. -
FIG. 2 shows the cycling of the Nitrogen or other inert gas coolant to purify it and harvest the fission products and then liquefy the gas and evaporate it giving a pure, mono-element coolant for the primary section of the reactor. -
FIG. 3 shows the Steam Power Generator compartment with the steam condensing upon use and flowing into a collector with pump that recycles the water back into the Secondary Section which generates steam. Here water can accumulate salts. -
FIG. 4 shows the Steam Power Generator compartment with the steam condensing upon use and condensed water flowing into an ice cube generator which can remove salts from the water as the ice freezes. Not shown is a cube wash which eliminates the salts on the outer surface of the ice and the containers where they freeze. Coldness to freeze the water is achieved by freezing in the inert gas purifier. - Turning now to the drawings and initially to
FIG. 1 , shows the components of the nuclear reactor steam power generator as 1 the primary section of the reactor withfuel rods 4 in acontainer 10 flooded withinert gas 11 held on abase 5; thesecondary section 2 which generates thesteam 70 by having theradiators 21 at the critical temperature of water, 374° C.; thethird section 3 recycles and purifies the inert gas. Thefinal section 8 is the steam generator that creates the power. The power generator is not elaborated upon since this discovery only deals with creating sufficient steam to drive the generator which is of anothers' design. Details of 3 are given inFIG. 2 . - The process in the
Primary Sector 1 is as follows: The pure, inert gas at cryogenic temperature enters thePrimary cylinder 10 at thetwin inputs 12 feeding fresh gas into the containedgas 11 to absorb the heat generated by thefuel 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 thetop plate 14 and flows into thehot gas pipes 20 heating theradiator 21 to the critical temperature so water in theSecondary Section 2 converts to steam. Some radiators have anexit pipe 27 to heat another segment of radiator. The gas, then cooled from heating the radiator(s), leaves via the cooledgas pipes 22 which takes the cooled gas to thebase 5 of the Primary Section where it enters thePrimary section 23 cycling the gas to again be heated by the fuel rods. - The process in the
Secondary Sector 2 includes thesteam shell 26 which is fully insulated against heat loss to preserve thesteam 24, generated on theradiators 21, which then passes to thesteam generator 8 to drive the power generator. - Turning now to
FIG. 2 , the purifying process for the inert gas, the gas passing out of the Primary Sector fromorifice 7 wherewide passage 70 first implements dropping of particles carried by the gas dropping it down thecylinder 71 to thebottom accumulation 15. The gas is cooled by proximity of the cryogenicallycold gas pipes 30, and as it cools, impurities which emerge from the fission process carried in the gas are condensed and held inthermal level segments 31 and then the gas passes through the usedgas outlet 13 into thelower section 33 of the double chamber box where the used gas reaches cryogenic temperature—close to, if not at, −195.8° C. The cryogenic used gas passes through thelight gas separator 34 where the light gases, Hydrogen, Helium and Neon, rise in theLight gas cylinder 36. As they collect the cylinder rises. To store these light gases, when the cylinder is lowered withvalve 37 open, the light gases pass through the lightgas storage tie 38 and into thelight gas carriers 39, suggest mylar balloons. The used gas with both heavier materials extracted and the light gases extracted then passes through theentrance 61 of the Nitrogen gas/Liquid Nitrogen mixer condensing the gas into liquid. The Liquid Nitrogen—pure—passes through thetube 60 entering thedewar 16 atopening 62. TheLiquid Nitrogen valve 63 driven by thermal controllers in thePrimary Sector 1 adjusts the rate of flow of the liquid Nitrogen through thesieve unit 64 causing the Liquid Nitrogen to rain 65 into theupper chamber 32, the gas input chamber, which then passes through the twopipes 30 cooling the exhaust gas as it warms and enters thePrimary Sector 1 at thepure Nitrogen input 12 keeping the gas temperature around the fuel rods at the proper level. - Looking at
FIG. 3 , not showing the steam power generator design since it is not part of this patent, the water cycle is illustrated in theSteam Generator Section 8 wheresteam 70 cools withuse producing water 71 which is collected in thewater collector 72 and passed into the collectingtube 73, through apump 74 which moves it upward allowing it to pass through thefaucet 75 and into thesieve 76 which makes it fall like rain indrops 77 onto theradiator units 21 which convert it to steam 70 which drives the steam power generator. - Looking, last, to
FIG. 4 , not showing the steam power generator design since it is not part of this patent, the water cycle is enhanced by freezing the water to eliminate salts from the water. Thepower generator section 8 has thesteam 70 condensing intowater 71 which is collected in thewater catch 72 and passes down the collectingtube 73. It then enters the cryogenic cold atmosphere of theinert gas purifier 3 so the water can freeze in theice cubers 81 which are attached to theconveyor 80 moving in a loop. Thecollector tube 73 fills theice cubers 81 withwater 71 which freezes intoice cubes 82. As the conveyor progresses, theice cubes 82 are set on theice cube collector 83 which turns and releases theice cubes 82 to theice cube lift 84 which carries them up into theSecondary Section 2 placing them in thesieve 76 where they melt and thewater 71 rains down as water drops 77 falling on theradiator units 21 where they evaporate intosteam 70 which passes on to drive the steam power generator, not shown. Salts in the water will move to the outside of theice cube 82 or stick in theice cuber 81. The salts can be washed in the process, but this process is not shown. - To understand the workings of the cooling system for the fuel rods in the
Primary Section 1 combined with thepurifying section 3, there are only two adjustment valves needed, that controlled by the thermal regulator pacing the flow ofLiquid Nitrogen 63 and thevalve 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 impureinert gas 7 is pulled from thePrimary section 1 by the dropping out of air suspendedgrit 15 which precipitates and the condensing ofmaterial 31 contaminating the inert gas, mostlikely Nitrogen 11, drawing more gas from thePrimary 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 themixer 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 intosteam 70 in the Secondary chamber and passed on to the SteamPower Generator chamber 8 where with power transfer it condenses intowater 71 and is collected in thewater catch 72 and collectingtube 73 where it can be pumped back into the secondary chamber and passed through asieve 76 to rain onto theradiator units 21, or, to purify the water, can be frozen into ice cubes in the cryo-chamber 3 and passed back into thesteam chamber 2 to melt and run through thesieve 76 and rain onto the radiators. Power here is by thepump 74 for the water coming from the collectingtube 73 or thelift 84 for the ice cubes as well as the turning of theloop conveyor 80 for the ice cubers and the turning of theice 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 thedewar 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.
Claims (7)
1. A method of steam generation in nuclear reactors that operates dual chambers, one, with the fuel rods bathed in pure, inert Nitrogen gas and the other housing the water for conversion to steam to power the generators that:
a. operates with dry fuel rods at the critical point of water—all steam temperature.
b. provides a radiator interface between the hot gas and the water component.
c. requires less, if not no, external area for cooling of water components.
d. separates out gaseous products of fission before release into the air.
e. generates a greater quantity of steam from pure water than water coolant systems, and,
f. maintains a store of Liquid Nitrogen or a Noble gas for fire and crises handling throughout the facility.
2. The method according to claim 1 , wherein the pure, inert Nitrogen gas cloud sustained at or above 374° C. keeps fuel rods from Oxygen preventing meltdown from oxidation reactions but absorbs the heat of fission in the primary segment of steam generated nuclear power production.
3. The method according to claim 1 , further comprising the step of heat transfer at critical point for water sustaining a steam environment for the steam generator to produce electrical power in the secondary component.
4. The method according to claim 1 of purifying the inert gas by creating a gradient for cooling the Nitrogen being recycled so the fission products released as particles, condensed gases and, as Nitrogen reaches the liquefying temperature, the hydrogen, helium and neon formed separate out rising above the cold molecular Nitrogen gas and can be captured in an inverted cylinder type separator and stored, as in mylar balloons.
5. The method according to claim 1 , which provides fire and crises protection for the entire facility protecting the computer and control mechanisms as well as the building and physical work areas of the power plant because the stored Liquid Nitrogen can be directed to flow into the fire and crises control piping to areas affected by crises.
6. A method of steam generation of electrical power that can vary in size of reactor equipment giving better flexibility to use than water cooled primary systems since the need for external cooling is self-contained and does not include bodies of water.
7. A method of thermal control of the primary sector of nuclear reactors regulated by infusing the sector with the same inert gas just evaporated from its liquid phase making small additions to the gas volume giving rapid thermal cooling of the fuel rod environment enabled with:
a. thermal tracking of the ambient temperature of the primary sector of the nuclear reactor with both high temperature limits and low temperature limits for intervention.
b. high temperature limits reached activate cryogenic liquid infusion into the primary sector a stream of just evaporated inert gas lowers the ambient temperature of the primary sector until the temperature is again within the range of normal operation.
c. low temperature limits reached activate slowing the circulatory action of the inert gas so less “fresh” just evaporated gas flows in preserving the heat of fission of the fuel rods to maintain the gas environment at the critical point of water, 374° C.
d. general cycling of the inert gas in the primary sector provides a slow flow of the just evaporated gas into the chamber and exhaust of the hot gas out for cooling and purifying of accumulated fission products keeping a clean fuel rod environment.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US13/134,628 US20120002776A1 (en) | 2003-05-14 | 2011-06-11 | Dry coolant for primary stage of nuclear reactors |
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US10/437,538 US20040226301A1 (en) | 2003-05-14 | 2003-05-14 | Liquid nitrogen enabler |
US13/134,628 US20120002776A1 (en) | 2003-05-14 | 2011-06-11 | Dry coolant for primary stage of nuclear reactors |
Related Parent Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/437,538 Continuation US20040226301A1 (en) | 2003-05-14 | 2003-05-14 | Liquid nitrogen enabler |
Publications (1)
Publication Number | Publication Date |
---|---|
US20120002776A1 true US20120002776A1 (en) | 2012-01-05 |
Family
ID=33417394
Family Applications (5)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/437,538 Abandoned US20040226301A1 (en) | 2003-05-14 | 2003-05-14 | Liquid nitrogen enabler |
US11/544,285 Abandoned US20070089431A1 (en) | 2003-05-14 | 2006-10-06 | Liquid nitrogen enabler |
US11/706,723 Expired - Fee Related US7631506B2 (en) | 2003-05-14 | 2007-02-15 | Liquid nitrogen enabler |
US12/592,578 Abandoned US20100146993A1 (en) | 2003-05-14 | 2009-11-30 | Liquid nitrogen enabler |
US13/134,628 Abandoned US20120002776A1 (en) | 2003-05-14 | 2011-06-11 | Dry coolant for primary stage of nuclear reactors |
Family Applications Before (4)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US10/437,538 Abandoned US20040226301A1 (en) | 2003-05-14 | 2003-05-14 | Liquid nitrogen enabler |
US11/544,285 Abandoned US20070089431A1 (en) | 2003-05-14 | 2006-10-06 | Liquid nitrogen enabler |
US11/706,723 Expired - Fee Related US7631506B2 (en) | 2003-05-14 | 2007-02-15 | Liquid nitrogen enabler |
US12/592,578 Abandoned US20100146993A1 (en) | 2003-05-14 | 2009-11-30 | Liquid nitrogen enabler |
Country Status (1)
Country | Link |
---|---|
US (5) | US20040226301A1 (en) |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20130208846A1 (en) * | 2011-12-09 | 2013-08-15 | Scott Clair Pockrandt | Liquid nitrogen emergency cooling system for nuclear plants |
WO2013184207A3 (en) * | 2012-03-16 | 2014-01-30 | Catherine Lin-Hendel | Emergency and back-up cooling of nuclear fuel and reactors |
CN104392750A (en) * | 2014-11-14 | 2015-03-04 | 河北华热工程设计有限公司 | Low temperature nuclear reactor and vehicle-mounted power system based on same |
JP2015087387A (en) * | 2013-09-27 | 2015-05-07 | 長浦 善昭 | As a refrigerant that freezes the frozen wall built around the Fukushima Daiichi Nuclear Power Station, it can supply a huge amount of cold heat at a low cost. How to freeze. |
US20150380115A1 (en) * | 2011-12-09 | 2015-12-31 | Scott Clair Pockrandt | Liquid nitrogen emergency cooling system for nuclear power plants |
US9881705B2 (en) | 2012-03-16 | 2018-01-30 | Catherine Lin-Hendel | Emergency and back-up cooling of nuclear fuel and reactors and fire-extinguishing, explosion prevention using liquid nitrogen |
Families Citing this family (24)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
WO2009102303A1 (en) * | 2008-02-15 | 2009-08-20 | Denyse Claire Dubrucq | Liquid nitrogen enabler |
US20070158452A1 (en) * | 2006-01-06 | 2007-07-12 | Hofffmann Eugene J | Tropical hurricane storm control system |
US20080283255A1 (en) * | 2007-05-17 | 2008-11-20 | Dubrucq Denyse | Liquid Nitrogen Enabler Apparatus |
US7810420B2 (en) * | 2008-09-21 | 2010-10-12 | Konstantinovskiy Alexandr | Method of interrupting a tornado |
US20100115970A1 (en) * | 2008-11-13 | 2010-05-13 | Ron Lee | Thermal management apparatus for gas storage |
US20100270389A1 (en) * | 2009-04-24 | 2010-10-28 | Boris Feldman | Method of dangerous phenomena (mainly, hurricane) and global warning weakening |
US9708828B2 (en) * | 2010-05-06 | 2017-07-18 | Alexey Varaksin | Methods and systems for protection from destructive dynamic vortex atmospheric structures |
US8985397B2 (en) | 2013-03-08 | 2015-03-24 | Guardian 8 Corporation | Systems and methods for spraying an aerosol |
RU2546434C2 (en) * | 2013-07-08 | 2015-04-10 | ФЕДЕРАЛЬНОЕ ГОСУДАРСТВЕННОЕ БЮДЖЕТНОЕ УЧРЕЖДЕНИЕ "ВСЕРОССИЙСКИЙ ОРДЕНА "ЗНАК ПОЧЕТА" НАУЧНО-ИССЛЕДОВАТЕЛЬСКИЙ ИНСТИТУТ ПРОТИВОПОЖАРНОЙ ОБОРОНЫ МИНИСТЕРСТВА РОССИЙСКОЙ ФЕДЕРАЦИИ ПО ДЕЛАМ ГРАЖДАНСКОЙ ОБОРОНЫ, ЧРЕЗВЫЧАЙНЫМ СИТУАЦИЯМ И ЛИКВИДАЦИИ ПОСЛЕДСТВИЙ СТИХИЙНЫХ БЕДСТВИЙ" (ФГБУ ВНИИПО МЧС России) | Method of extinguishing peat fires |
RU2523260C1 (en) * | 2013-08-06 | 2014-07-20 | Лев Петрович Петренко | Method of minimising of ignition sources in peatlands (version of russian logic) |
RU2569440C1 (en) * | 2014-11-18 | 2015-11-27 | Федеральное государственное бюджетное образовательное учреждение высшего образования "Тульский государственный университет" (ТулГУ) | Method of ammunition demilitarization |
CN107042004A (en) * | 2017-03-18 | 2017-08-15 | 芜湖元航空科技有限公司 | A kind of fire-fighting unmanned plane fire extinguisher bomb delivery device |
CN109751218B (en) * | 2017-11-03 | 2023-10-20 | 核工业西南物理研究院 | Built-in high-vacuum low-temperature condensing air pump |
US10653904B2 (en) | 2017-12-02 | 2020-05-19 | M-Fire Holdings, Llc | Methods of suppressing wild fires raging across regions of land in the direction of prevailing winds by forming anti-fire (AF) chemical fire-breaking systems using environmentally clean anti-fire (AF) liquid spray applied using GPS-tracking techniques |
US11865394B2 (en) | 2017-12-03 | 2024-01-09 | Mighty Fire Breaker Llc | Environmentally-clean biodegradable water-based concentrates for producing fire inhibiting and fire extinguishing liquids for fighting class A and class B fires |
US11865390B2 (en) | 2017-12-03 | 2024-01-09 | Mighty Fire Breaker Llc | Environmentally-clean water-based fire inhibiting biochemical compositions, and methods of and apparatus for applying the same to protect property against wildfire |
US11826592B2 (en) | 2018-01-09 | 2023-11-28 | Mighty Fire Breaker Llc | Process of forming strategic chemical-type wildfire breaks on ground surfaces to proactively prevent fire ignition and flame spread, and reduce the production of smoke in the presence of a wild fire |
CN110127012B (en) * | 2019-05-30 | 2022-01-11 | 武汉理工大学 | Intelligent nitrogen-water mist system for reducing ship implosion damage and subsequent combustion |
US20240157180A1 (en) | 2021-02-04 | 2024-05-16 | Mighty Fire Breaker Llc | Method of and kit for installing and operating a wildfire defense spraying system on a property parcel for proactively spraying environmentally-clean liquid fire inhibitor thereover to inhibit fire ignition and flame spread caused by wind-driven wildfire embers |
US11911643B2 (en) | 2021-02-04 | 2024-02-27 | Mighty Fire Breaker Llc | Environmentally-clean fire inhibiting and extinguishing compositions and products for sorbing flammable liquids while inhibiting ignition and extinguishing fire |
CN112921926B (en) * | 2021-01-23 | 2022-05-24 | 山东浩海疏浚装备有限公司 | Marine garbage fishing device |
US11940102B2 (en) | 2021-02-08 | 2024-03-26 | Carver Enterprises, Inc. | Cold storage system |
ES2941110B2 (en) * | 2021-11-12 | 2025-01-29 | Adg Ingenieria Automatica Sl | PROCEDURE AND DEVICES FOR DIVERTING LAVA FLOWS |
CN115522920B (en) * | 2022-11-24 | 2023-02-10 | 西南石油大学 | A test device for measuring gas-water double-layer perforation production of tight sandstone gas reservoirs |
Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3121627A (en) * | 1961-07-24 | 1964-02-18 | Water Process Corp | Method of purifying water by freezing |
US3928129A (en) * | 1972-08-31 | 1975-12-23 | Siemens Ag | Nuclear reactor element |
US4322268A (en) * | 1978-04-03 | 1982-03-30 | The United States Of America As Represented By The United States Department Of Energy | Cooling system for a nuclear reactor |
Family Cites Families (32)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3327704A (en) * | 1964-08-12 | 1967-06-27 | Jr Roscoe G Bartlett | Mask-to-mask resuscitation systems |
US3830307A (en) * | 1970-05-11 | 1974-08-20 | Parker Hannifin Corp | Fire prevention and/or suppression system |
US3738424A (en) * | 1971-06-14 | 1973-06-12 | Big Three Industries | Method for controlling offshore petroleum wells during blowout conditions |
US3800715A (en) * | 1971-09-30 | 1974-04-02 | W Boller | Bomb recovery and shield apparatus |
US4031707A (en) * | 1972-04-24 | 1977-06-28 | executrix Rose Shuffman | Cryothermal manipulation of petroleum spills on water |
US4046055A (en) * | 1975-07-18 | 1977-09-06 | The United States Of America As Represented By The Secretary Of The Army | Apparatus for safely neutralizing explosive devices |
FR2379018A1 (en) * | 1976-12-23 | 1978-08-25 | Air Liquide | CRYOGENIC PROCESS AND PLANT FOR DISTRIBUTION OF GAS UNDER PRESSURE |
US4203472A (en) * | 1978-06-20 | 1980-05-20 | Dulaney Burrell C | Device for stopping fluid flow from a pipe |
US4223536A (en) * | 1979-02-16 | 1980-09-23 | executrix Rose Shuffman | Cryothermal manipulation of petroleum |
US4323118A (en) * | 1980-02-04 | 1982-04-06 | Bergmann Conrad E | Apparatus for controlling and preventing oil blowouts |
JPH0545316Y2 (en) * | 1986-07-25 | 1993-11-18 | ||
US5249500A (en) * | 1990-09-21 | 1993-10-05 | Technology International Incorporated | Rapid area clearance of explosives |
US5223661A (en) * | 1990-09-21 | 1993-06-29 | Technology International Incorporated | Rapid area clearance of explosives |
DE4101668A1 (en) * | 1991-01-22 | 1992-07-23 | Messer Griesheim Gmbh | FIRE EXTINGUISHING DEVICE WITH A STORAGE FOR A LOW-BOILED GAS LIQUIDED |
US5180018A (en) * | 1991-05-29 | 1993-01-19 | Taylor Robert E | Split stack fire-fighting apparatus and process of use |
GB9114057D0 (en) * | 1991-06-28 | 1991-08-14 | Subsea Offshore Ltd | Improvements in or relating to fire-fighting burning oil wells |
US5191940A (en) * | 1991-08-22 | 1993-03-09 | The United States Of America As Represented By The United States Department Of Energy | Oil/gas separator for installation at burning wells |
US5247999A (en) * | 1991-09-25 | 1993-09-28 | Fowler John T | Oil wellhead fire extinguishing apparatus having adjustable support feet and labyrinth module |
PT99175B (en) * | 1991-10-08 | 1996-01-31 | Fernando Jorge Nunes De Almeid | INSTALLATION OF CRYOGENIC FLUID SUPPLY |
US5364034A (en) * | 1994-02-17 | 1994-11-15 | Katsuji Hirahara | Controlled low volume irrigation system |
US5590717A (en) * | 1995-12-11 | 1997-01-07 | Mcbay, Deceased; Henry R. C. | Fire extinguishing capsule |
US5699671A (en) * | 1996-01-17 | 1997-12-23 | Praxair Technology, Inc. | Downflow shell and tube reboiler-condenser heat exchanger for cryogenic rectification |
EP0798019A1 (en) * | 1996-03-30 | 1997-10-01 | Minimax GmbH | Method and device for the atomisation of a liquid fire extinguishing agent in a stationary fire extinguishing plant |
US20040011881A1 (en) * | 1999-10-22 | 2004-01-22 | Fernando Morales | Method and apparatus for abating storm strength |
AU2289001A (en) * | 1999-12-23 | 2001-07-03 | Egg Factory L.L.C., The | Influencing weather patterns by way of altering surface or subsurface ocean water temperatures |
US6502421B2 (en) * | 2000-12-28 | 2003-01-07 | Igor K. Kotliar | Mobile firefighting systems with breathable hypoxic fire extinguishing compositions for human occupied environments |
US6401830B1 (en) * | 2000-11-21 | 2002-06-11 | David B. Romanoff | Fire extinguishing agent and method |
US20050031417A1 (en) * | 2001-07-23 | 2005-02-10 | Hofer Kurt G. | Gas diffuser ocean water lifting method and device |
US6763894B2 (en) * | 2001-08-01 | 2004-07-20 | Kidde-Fenwal, Inc. | Clean agent fire suppression system and rapid atomizing nozzle in the same |
US6666278B2 (en) * | 2002-01-22 | 2003-12-23 | Frank Cicanese | Oil well fire suppression device |
US20040188540A1 (en) * | 2003-03-27 | 2004-09-30 | Derba Mills | Adjustable height inverted lawn and garden sprinkler |
US20050269109A1 (en) * | 2004-06-03 | 2005-12-08 | Maguire James Q | Method of extinguishing fires |
-
2003
- 2003-05-14 US US10/437,538 patent/US20040226301A1/en not_active Abandoned
-
2006
- 2006-10-06 US US11/544,285 patent/US20070089431A1/en not_active Abandoned
-
2007
- 2007-02-15 US US11/706,723 patent/US7631506B2/en not_active Expired - Fee Related
-
2009
- 2009-11-30 US US12/592,578 patent/US20100146993A1/en not_active Abandoned
-
2011
- 2011-06-11 US US13/134,628 patent/US20120002776A1/en not_active Abandoned
Patent Citations (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US3121627A (en) * | 1961-07-24 | 1964-02-18 | Water Process Corp | Method of purifying water by freezing |
US3928129A (en) * | 1972-08-31 | 1975-12-23 | Siemens Ag | Nuclear reactor element |
US4322268A (en) * | 1978-04-03 | 1982-03-30 | The United States Of America As Represented By The United States Department Of Energy | Cooling system for a nuclear reactor |
Non-Patent Citations (2)
Title |
---|
Adams, R., "ML-1 Mobile Power System: Reactor in a Box", November 1995, Atonic Insights, pp. 1-4. * |
Marshall, A., "An Assessment of Reactor Types for Thermochemical Hydrogen Production", February 2002, Sandia National Laboratories, pp. 1-53. * |
Cited By (15)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20150380115A1 (en) * | 2011-12-09 | 2015-12-31 | Scott Clair Pockrandt | Liquid nitrogen emergency cooling system for nuclear power plants |
US9484119B2 (en) * | 2011-12-09 | 2016-11-01 | Scott Clair Pockrandt | Liquid nitrogen emergency cooling system for nuclear power plants |
US20130208846A1 (en) * | 2011-12-09 | 2013-08-15 | Scott Clair Pockrandt | Liquid nitrogen emergency cooling system for nuclear plants |
US9396822B2 (en) * | 2012-03-16 | 2016-07-19 | Catherine Lin-Hendel | Emergency and back-up cooling of nuclear fuel and reactors |
JP2015512506A (en) * | 2012-03-16 | 2015-04-27 | リン−ヘンデル,キャサリン | Emergency fuel cooling system for nuclear fuel and nuclear reactors {EMERGENCYANDBACK-UPCOOLINGOFNCLEARFUELANDREACTORS} |
EP2826039A4 (en) * | 2012-03-16 | 2015-11-04 | Catherine Lin-Hendel | Emergency and back-up cooling of nuclear fuel and reactors |
CN104170018A (en) * | 2012-03-16 | 2014-11-26 | 凯瑟琳·林-亨德尔 | Emergency and backup cooling systems for nuclear fuel and nuclear reactors |
US20140105348A1 (en) * | 2012-03-16 | 2014-04-17 | Catherine Lin-Hendel | Emergency and back-up cooling of nuclear fuel and reactors |
WO2013184207A3 (en) * | 2012-03-16 | 2014-01-30 | Catherine Lin-Hendel | Emergency and back-up cooling of nuclear fuel and reactors |
US9881705B2 (en) | 2012-03-16 | 2018-01-30 | Catherine Lin-Hendel | Emergency and back-up cooling of nuclear fuel and reactors and fire-extinguishing, explosion prevention using liquid nitrogen |
RU2666790C2 (en) * | 2012-03-16 | 2018-09-12 | Кэтрин ЛИН-ХЕНДЕЛЬ | Method and system for emergency and back-up cooling of nuclear fuel and reactors |
US10522256B2 (en) * | 2012-03-16 | 2019-12-31 | Catherine Lin-Hendel | Emergency and back-up cooling of nuclear fuel and reactors and fire-extinguishing, explosion prevention using liquid nitrogen |
JP2015087387A (en) * | 2013-09-27 | 2015-05-07 | 長浦 善昭 | As a refrigerant that freezes the frozen wall built around the Fukushima Daiichi Nuclear Power Station, it can supply a huge amount of cold heat at a low cost. How to freeze. |
CN104392750A (en) * | 2014-11-14 | 2015-03-04 | 河北华热工程设计有限公司 | Low temperature nuclear reactor and vehicle-mounted power system based on same |
CN104392750B (en) * | 2014-11-14 | 2017-08-11 | 河北华热工程设计有限公司 | Low temperature nuclear reactor and the onboard power systems based on low temperature nuclear reactor |
Also Published As
Publication number | Publication date |
---|---|
US7631506B2 (en) | 2009-12-15 |
US20070214808A1 (en) | 2007-09-20 |
US20070089431A1 (en) | 2007-04-26 |
US20100146993A1 (en) | 2010-06-17 |
US20040226301A1 (en) | 2004-11-18 |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
US20120002776A1 (en) | Dry coolant for primary stage of nuclear reactors | |
US20070277674A1 (en) | Method And System Of Processing Exhaust Gas, And Method And Apparatus Of Separating Carbon Dioxide | |
US3978663A (en) | Process and apparatus for evaporating and heating liquified natural gas | |
US6158239A (en) | Desalination through gas hydrate | |
US3609983A (en) | Krypton-xenon recovery system and process | |
US7228713B2 (en) | Multi-stage vacuum distilling, cooling and freezing processes and apparatuses for solution separation and seawater desalination | |
US9476648B2 (en) | Systems and methods of using phase change material in power plants | |
JPH06221499A (en) | Method and device for evaporation of extremely low temperature liquid | |
GB945223A (en) | Improvements in or relating to refrigerators | |
CN100560478C (en) | To contain tritium light-water or heavy water is the production method that raw material extracts pure tritium | |
SE408955B (en) | PROCEDURE AND DEVICE FOR STORING HEAT ENERGY | |
CN102343163B (en) | Cryogenic treatment device for separating carbon dioxide from the atmosphere using superconducting wind turbines | |
US7293420B2 (en) | Atmospheric moisture harvesters | |
CN104567276A (en) | Device and technological method for producing LNG (liquefied natural gas) by recycling ammonia tail gas | |
US5626035A (en) | Apparatus and method for separation of helium and neon | |
RU2737986C1 (en) | Natural gas liquefaction method and device for implementation thereof | |
KR20070040304A (en) | Transferring tritium from water to basic hydrogens, removing tritium from water by membrane diffusion tritium stripping and concentration, and finally concentrating tritium by thermal diffusion | |
US4048437A (en) | Superconducting magnet cooling system | |
US10815975B1 (en) | Heavy water ocean thermal energy conversion method and system | |
RU2143940C1 (en) | Sublimation apparatus | |
US3097940A (en) | Process for purifying gases | |
US3885939A (en) | Cryostat control | |
CN115371359A (en) | Sabatier device reaction gas separation and liquefaction system and method applied to Mars surface | |
Bekris et al. | Cold trapping of traces of tritiated water from the helium loops of a fusion breeder blanket | |
JPS57157005A (en) | Energy conversion system using gaseous clathrate compound |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |