The disclosure relates to fire-fighting technology, and more particularly to a fire engine which uses liquid nitrogen as an extinguishing agent.
Conventional fire engines employ water or liquid nitrogen as an extinguishing agent. The liquid nitrogen is pressurized by a pump and then mixed with water for firefighting.
The disclosure provides a fire engine with liquid nitrogen as an extinguishing agent. The fire engine can store liquid nitrogen. In use, the liquid nitrogen is gasified and then mixed with water to form an atomized jet fluid of water, water-based fire extinguishing agents and/or decontaminants. Such atomized jet fluid yields in efficient firefighting.
Disclosed is a fire engine comprising a vehicle frame, a liquid nitrogen storage tank comprising a first opening and a second opening, a liquid nitrogen conveying pipeline, a gasification device, a plurality of electric valves, a water pipe adapter, a liquid nitrogen spray gun, and a mixed spray gun. The liquid nitrogen storage tank is disposed on the vehicle frame. The second opening is disposed higher than the first opening relative to the gasification device.
The liquid nitrogen conveying pipeline comprises at least a first pipeline, a second pipeline, and a third pipeline. The first pipeline connects the first opening of the liquid nitrogen storage tank, the gasification device, and the second opening of the liquid nitrogen storage tank sequentially in that order; the second pipeline connects the liquid nitrogen storage tank, an input end of the liquid nitrogen spray gun, and a first input end of the mixed spray gun sequentially in that order. The third pipeline is provided with a safety valve and a relief valve, and the external liquid nitrogen is input to the liquid nitrogen storage tank via the third pipeline. The mixed spray gun comprises a first input end, a second input end, a liquid nitrogen nozzle and a spray pipe, and the spray pipe comprises a contraction section, an expansion section, and an acceleration section which are connected to one another in that order. Along a direction from the contraction section to the acceleration section, the inner diameter of the contraction section decreases, and the inner diameter of the expansion section increases. The inner diameter of the acceleration section is constant and equal to the outlet diameter of the expansion section. The liquid nitrogen nozzle communicates with the first input end and is disposed on the axial line of the contraction section; the outlet of the liquid nitrogen nozzle is coaxial with the outlet of the contraction section. An inlet of the second input end is connected to a water pipe adapter and an outlet of the second input end communicates with the contraction section; the water pipe adapter is connected to the inlet of the second input end via a water delivery pipeline; the plurality of electric valves is disposed on the liquid nitrogen conveying pipeline and the water delivery pipeline.
A mixed spray gun comprises a first input end, a second input end, a liquid nitrogen nozzle and a spray pipe, and the spray pipe comprises a contraction section, an expansion section, and an acceleration section which are connected to one another in that order. Along a direction from the contraction section to the acceleration section, the inner diameter of the contraction section decreases, and the inner diameter of the expansion section increases. The inner diameter of the acceleration section is constant and equal to the outlet diameter of the expansion section. The liquid nitrogen nozzle communicates with the first input end and is disposed on the axial line of the contraction section; the outlet of the liquid nitrogen nozzle is coaxial with the outlet of the contraction section. An inlet of the second input end is connected to a water source and an outlet of the second input end communicates with the contraction section.
The gasification device comprises a gasification tube and a plurality of heat dissipating fins; the gasification tube is connected to the first pipeline, and the heat dissipating fins are radially disposed on the outer wall of the gasification tube.
The liquid nitrogen storage tank comprises a housing, a liner, and a gap between the housing and the liner; the liner is disposed in the housing. The gap is dried and has a pressure of 0.001 to 0.005 Pa, and the outer surface of the liner is provided with a heat insulating material comprising a zirconia foil layer.
The following advantages are realized:
In the drawings, the following reference numbers are used: 1. Vehicle frame; 2. Liquid nitrogen storage tank; 2-1. Housing; 2-2. Liner; 2-3. Heat insulating material; 3. Folding crane; 4. Safety valve; 5. Level gauge; 6. Pressure sensor; 7. Rotatable support; 8. Mixed spray gun; 8-1. Contraction section, 8-2. Expansion section; 8-3. Acceleration section; 8-4. Liquid nitrogen nozzle; 9. Liquid nitrogen conveying pipeline; 10. Relief valve; 11. Water delivery pipeline; 12. Water pipe adapter; 13. Liquid nitrogen spray gun; 14-1. First electric valve; 14-2. Second electric valve; 14-3. Third electric valve; 14-4. Fourth electric valve; 15. Gasification device; 15-1. Gasification tube; 15-2. Heat dissipating fins.
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The safety valve 4 is disposed above the liquid nitrogen storage tank 2 for releasing the pressure in the tank when the air pressure in the liquid nitrogen storage tank 2 is too high, so that the pressure value in the tank is maintained between 1.2 and 1.6 megapascal.
The level gauge 5 is disposed in the middle and upper part of the liquid nitrogen storage tank 2 for indicating the amount of the liquid nitrogen remaining in the liquid nitrogen storage tank 2.
The pressure sensor 6 is disposed above the liquid nitrogen storage tank 2 for measuring the gas pressure in the liquid nitrogen storage tank 2.
The relief valve 10 is disposed above the liquid nitrogen storage tank 2 for maintaining the pressure of the liquid nitrogen in the tank not more than 0.8 megapascal. When the pressure in the tank is greater than the value, the relief valve is opened to release a portion of low temperature nitrogen in the tank to reduce the pressure in the tank and achieve a long-time cryogenic storage of liquid nitrogen.
The liquid nitrogen conveying pipeline 9 is provided with three paths:
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Along the direction from the contraction section to the acceleration section, the inner diameter of the contraction section 8-1 decreases, and the inner diameter of the expansion section 8-2 increases. The inner diameter of the acceleration section 8-3 is constant and equal to the outlet diameter of the expansion section 8-2. The liquid nitrogen nozzle communicates with the first input end and is disposed on the axial line of the contraction section 8-1; the outlet of the liquid nitrogen nozzle 8-4 is coaxial with the outlet of the contraction section 8-1. The inlet of the second input end is connected to the water pipe adapter 12 and the outlet of the second input end communicates with the contraction section 8-1.
The method of mixing the liquid nitrogen with water to produce an atomized jet fluid is implemented as follows: the water pipe adapter 12 provides water having a pressure of 0.8 to 1.0 megapascal, water-based fire extinguishing agent or chemical decontaminating agent. The liquid enters the mixed spray gun 8 and flows through the contraction section 8-1 and the expansion section 8-2 and is ejected from the acceleration section 8-3. The liquid nitrogen from the liquid nitrogen storage tank 2 having a pressure of 1.2 to 1.6 megapascal is injected through the liquid nitrogen nozzle 8-4 and mixed with the water, water fire extinguishing agent or chemical decontamination solution in the contraction section 8-1 of the mixed spray gun 8 to form a liquid nitrogen jet. The liquid nitrogen jet collides with the water fluid and ruptures to yield a plurality of liquid nitrogen beads. The liquid nitrogen beads absorb heat, vaporize and expand in the expansion section 8-2. After the atomized jet fluid enters the acceleration section 8-3, the compressed nitrogen gas continues to expand under the pressure difference between the inside and the outside of the mixed spray gun 8. The mixed fluid is accelerated again due to the pressure difference. The pressure of the nitrogen at the outlet of the mixed spray gun 8 is equal to the external atmospheric pressure. Thus, the water, the water-based fire extinguishing agent or the chemical decontaminant obtains the energy of the compressed nitrogen gas to be ejected from the mixed spray gun 8 in the form of an atomized fluid jet with a relatively high speed.
For example, when the water flow rate of the mixed spray gun is set as 60 L/s, the flow rate of the liquid nitrogen is controlled by the electric valve 14-4 to be 3 kg/s, amd the mixed spray gun 8 emits an ultra-fine water mist jet having an average particle diameter of about 200 μm and a jet velocity of 80 to 100 m/s. This ultra-fine water mist jet is used for rapid smoke and temperature cooling and suppressing deflagration and detonation. When the electric valve 14-4 controls the flow rate of the liquid nitrogen to 2 kg/s, the mixed spray gun 8 emits a high-temperature spray of a water-based fire extinguishing agent having an average particle diameter of about 400 to 500 μm, and the outlet flow rate can reach 60 to 80 m/s. Changing the flow rate of the liquid nitrogen can eject different particle diameters of water mists sprayed from the mixed spray gun 8.
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The electric valves are disposed on the liquid nitrogen conveying pipeline 9 and the water delivery pipeline:
The first electric valve 14-1 and the pressure sensor 6 control the flow rate of the liquid nitrogen entering the liquid nitrogenizing device 15; the second electric valve 14-2 controls the flow rate of the liquid nitrogen sprayed from the liquid nitrogen spray gun 13 to be between 1 and 4 kg/s; the third electric valve 14-3 controls the pressure of water, water-based fire extinguishing agent or chemical decontaminating agent from outside to be within 0.8 to 1.0 megapascal; and the fourth electric valve 14-4 controls the flow rate of the liquid nitrogen entering the mixed spray gun 8 so that the mass ratio of the liquid nitrogen to the water is 1:20-40.
Liquid nitrogen has a temperature of −196° C. under normal pressure, and 1 L of liquid nitrogen can produce 696 L of pure nitrogen gas at 21° C. Specifically, closing the relief valve 10 and opening the electric valve 14-1. A portion of the liquid nitrogen from the bottom of the liquid nitrogen storage tank 2 through the first pipeline enters the gasification device 15 through the electric valve 14-1 by gravity. The liquid nitrogen absorbs external heat and is vaporized into nitrogen gas, and the pressure in the gasification device 15 rises due to the increase of the volume of nitrogen gas. Nitrogen gas is introduced into the tank from the second opening of the tank through the liquid nitrogen conveying pipeline to pressurize the liquid nitrogen in the tank. The pressure sensor 6 controls the flow rate of the liquid nitrogen into the liquid nitrogen gasifier 15 through the electric valve 14-1 to ensure that the pressure in the tank is between 1.2 and 1.6 megapascal. When the pressure value in the tank is higher than 1.6 megapascal, the safety valve 4 opens to release pressure, and the pressure value in the tank is kept stable. The pressure sensor 6 lowers the flow rate of the liquid nitrogen entering the liquid nitrogen gasifier 15 through the electric valve 14-1, or directly closes the electric valve 14-1 to restore the pressure inside the tank. When the electric valve 14-2 that outputs liquid nitrogen is opened, the liquid nitrogen in the tank is output to the outside of the tank at a pressure of 1.2 to 1.6 megapascal. The electric valve 14-2 controls the flow rate of liquid nitrogen to be between 1 and 4 kg/s, which can be adjusted as needed.
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The implementation method will be further explained by taking the fire of the petrochemical plant as an example. The fire engine with liquid nitrogen as the extinguishing agent is supported by a water tank fire engine. When the folding crane 3 is fully opened, the position of the mixed spray gun 8 can be up to 32 meters, or the mixed spray gun 8 can be extended in a horizontal front direction to an appropriate position near the fire source. The third electric valve 14-3 and the fourth electric valve 14-4 are opened, and the water pipe adapter 12 inputs water containing 3% F-500 fire extinguishing agent into the mixed spray gun 8 through the water delivery pipeline 11. The liquid nitrogen enters the liquid nitrogen nozzle 8-4 of the mixed spray gun 8 through the liquid nitrogen conveying pipeline 9 via the fourth electric valve 14-4. The liquid nitrogen and the water comprising 3% F-500 fire extinguishing agent are mixed in the mixed spray gun 8 and then ejected at a high speed in the form of a misty fluid. The F-500 fire extinguishing agent has rapid cooling ability, which can combine with water molecules to encapsulate flammable liquid molecules to prevent it from burning, so as to quickly extinguish the flame.
Take the fire fighting in a clothing warehouse as an example. As shown in
In the case of the leakage of liquid chlorine, yellow-green chlorine gas is produced, and the density of the chlorine gas is 3.21 kg/m3 at normal temperature, which is close to the ground and spreads downstream with the wind. Under the support of a water tank fire engine, the fire engine in the example stays about 30 to 40 m from the liquid chlorine leakage position in the upwind or crosswind direction. The folding crane 3 is opened, and the mixed spray gun 8 is extended to face the liquid chlorine leakage position. Open the third electric valve 14-3 and the fourth electric valve 14-4, and the decontamination solution containing dissolved sodium carbonate enters the mixed spray gun 8 via the water pipe adapter 12 and the water delivery pipeline 11. The liquid nitrogen enters the liquid nitrogen nozzle 8-4 of the mixed spray gun 8 via the fourth electric valve 14-4 and the liquid nitrogen conveying pipeline 9. The liquid nitrogen and the decontamination solution containing dissolved sodium carbonate are mixed in the mixed spray gun 8, and then sprayed at a high speed in a misty fluid and blended with the leaked chlorine gas. Sodium carbonate reacts with the chlorine gas to form sodium chloride to release carbon dioxide. The water mist absorbs the chlorine gas to form hypochlorous acid falling to the ground, so that the leaked chlorine gas is diluted.
It will be obvious to those skilled in the art that changes and modifications may be made, and therefore, the aim in the appended claims is to cover all such changes and modifications.
Number | Date | Country | Kind |
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201711368271.2 | Dec 2017 | CN | national |
This application is a continuation-in-part of International Patent Application No. PCT/CN2018/000073 with an international filing date of Feb. 12, 2018, designating the United States, now pending, and further claims foreign priority benefits to Chinese Patent Application No. 201711368271.2 filed Dec. 18, 2017. The contents of all of the aforementioned applications, including any intervening amendments thereto, are incorporated herein by reference. Inquiries from the public to applicants or assignees concerning this document or the related applications should be directed to: Matthias Scholl P. C., Attn.: Dr. Matthias Scholl Esq., 245 First Street, 18th Floor, Cambridge, Mass. 02142.
Number | Date | Country | |
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Parent | PCT/CN2018/000073 | Feb 2018 | US |
Child | 16521608 | US |