CN211969761U - Liquid nitrogen type airborne oil tank inerting device - Google Patents
Liquid nitrogen type airborne oil tank inerting device Download PDFInfo
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- CN211969761U CN211969761U CN202020182670.0U CN202020182670U CN211969761U CN 211969761 U CN211969761 U CN 211969761U CN 202020182670 U CN202020182670 U CN 202020182670U CN 211969761 U CN211969761 U CN 211969761U
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- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 title claims abstract description 146
- 229910052757 nitrogen Inorganic materials 0.000 title claims abstract description 70
- 239000007788 liquid Substances 0.000 title claims abstract description 53
- 239000003921 oil Substances 0.000 claims abstract description 56
- 239000000446 fuel Substances 0.000 claims abstract description 41
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 claims abstract description 37
- 239000001301 oxygen Substances 0.000 claims abstract description 37
- 229910052760 oxygen Inorganic materials 0.000 claims abstract description 37
- 239000012782 phase change material Substances 0.000 claims abstract description 17
- 239000000203 mixture Substances 0.000 claims abstract description 14
- 238000005057 refrigeration Methods 0.000 claims abstract description 14
- 239000002114 nanocomposite Substances 0.000 claims abstract description 13
- 239000007789 gas Substances 0.000 claims abstract description 12
- 239000000295 fuel oil Substances 0.000 claims abstract description 9
- 238000001816 cooling Methods 0.000 claims abstract description 6
- 230000001105 regulatory effect Effects 0.000 claims description 58
- 239000012071 phase Substances 0.000 claims description 10
- LYCAIKOWRPUZTN-UHFFFAOYSA-N Ethylene glycol Chemical compound OCCO LYCAIKOWRPUZTN-UHFFFAOYSA-N 0.000 claims description 9
- 238000005259 measurement Methods 0.000 claims description 8
- 239000004575 stone Substances 0.000 claims description 7
- BBMCTIGTTCKYKF-UHFFFAOYSA-N 1-heptanol Chemical compound CCCCCCCO BBMCTIGTTCKYKF-UHFFFAOYSA-N 0.000 claims description 6
- 230000001276 controlling effect Effects 0.000 claims description 6
- 238000009825 accumulation Methods 0.000 claims description 5
- 239000000463 material Substances 0.000 claims description 5
- 239000002105 nanoparticle Substances 0.000 claims description 4
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 3
- 229910021389 graphene Inorganic materials 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- 239000012074 organic phase Substances 0.000 claims description 3
- 238000005406 washing Methods 0.000 claims description 2
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 claims 1
- 229910001873 dinitrogen Inorganic materials 0.000 abstract description 7
- 238000003912 environmental pollution Methods 0.000 abstract description 4
- 230000008016 vaporization Effects 0.000 abstract description 4
- 239000002131 composite material Substances 0.000 abstract description 3
- 239000002828 fuel tank Substances 0.000 description 16
- 238000000034 method Methods 0.000 description 13
- 239000003507 refrigerant Substances 0.000 description 6
- 238000005516 engineering process Methods 0.000 description 4
- 230000000694 effects Effects 0.000 description 3
- 238000012544 monitoring process Methods 0.000 description 3
- 238000009834 vaporization Methods 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Chemical compound O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000004146 energy storage Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000011261 inert gas Substances 0.000 description 2
- 238000010926 purge Methods 0.000 description 2
- 239000000523 sample Substances 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 238000012546 transfer Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 1
- 230000002708 enhancing effect Effects 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000004880 explosion Methods 0.000 description 1
- 230000002265 prevention Effects 0.000 description 1
- 238000011160 research Methods 0.000 description 1
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Abstract
The utility model discloses a liquid nitrogen formula machine carries oil tank inerting device, including nitrogen gas inerting subsystem, nanometer composite phase change material cold-storage subsystem, fuel vapor cooling system and observing and controlling subsystem, produce a large amount of inerting gas through vaporizing liquid nitrogen, let in and wash the fuel in the aircraft fuel oil tank, replace the oxygen in the fuel in the oil tank upper portion, draw oil tank upper portion fuel vapor mixture out simultaneously and carry out the heat exchange through heat exchanger and low temperature nitrogen gas, cool off fuel vapor mixture temperature and make fuel vapor liquefaction, reduce the flammability of aircraft oil tank through oxygen content and the fuel vapor concentration in reducing the oil tank, thereby reach the inerting purpose; the liquid nitrogen flows through the cold accumulator to be evaporated into nitrogen, and a large amount of cold energy generated when the liquid nitrogen is evaporated is absorbed and stored by the nano composite phase change material and forms an airborne refrigeration cycle with the evaporator. The device has the advantages of no aircraft fuel compensation loss, high energy utilization rate, high inerting efficiency, no environmental pollution and the like.
Description
Technical Field
The utility model relates to a belong to fire prevention and explosion protection technical field, specifically indicate a liquid nitrogen formula machine carries oil tank inerting device.
Background
The on-board fuel tank inerting means that inert gas is generated by on-board equipment and is used for replacing air in a gas-phase (oil-free) space at the upper part of the fuel tank so as to ensure the safety of the fuel tank. Accordingly, On-Board tank inerting systems are also known as On-Board Inert Gas Generation systems (OBIGGS). The system uses airborne Air separation technology to remove oxygen molecules from the bleed Air from the aircraft engine compressor or environmental control system, leaving a Nitrogen-Enriched Air (Nitrogen-Enriched Air NEA) inerting tank.
The so-called airborne fuel tank inerting technology is that an airborne air separation fuel tank inerting system is installed on an aircraft, so that the oxygen concentration in an oil-free space air layer at the upper part of an aircraft fuel tank is always kept lower than the oxygen concentration level required for supporting fuel oil combustion in the whole flight process. Foreign research work shows that: when the oxygen concentration of the oil-free space at the upper part of the oil tank of the airplane is lower than 9 percent, the oil tank cannot be damaged due to overpressure even if the airplane is attacked by a high-energy combustion bomb with the caliber of 23 mm. At present, after 9% and 12% are generally used as military machines and civil machines abroad to adopt inerting technology, the allowable maximum oxygen concentration limit of an oil-free gas phase space at the upper part of an oil tank is at the sea level height.
The phase change energy storage technology can adjust mismatching of energy supply and demand in time and space, and is an effective way for improving energy utilization efficiency. However, most phase change materials have low thermal conductivity, which limits the heat transfer efficiency during the phase change process on the ground and in space. The nano-particles are added into the traditional phase-change material to form the nano-fluid composite phase-change material, so that the nano-fluid composite phase-change material has the potential of enhancing the heat transfer of the phase-change material and improving the efficiency of an energy storage system.
SUMMERY OF THE UTILITY MODEL
The utility model discloses to the problem that exists among the prior art, provided a liquid nitrogen formula machine carries oil tank inerting device, had no aircraft fuel compensation loss, energy utilization is high, and inerting is efficient, advantages such as no environmental pollution.
In order to achieve the purpose, the utility model adopts the following technical scheme:
a liquid nitrogen type onboard oil tank inerting device comprises a liquid nitrogen bottle, a liquid nitrogen supply pump, a cold accumulator, a heat exchanger, an oil tank, a fan and a dryer, wherein liquid nitrogen in the liquid nitrogen bottle enters through a cold side inlet of the cold accumulator, and the cold accumulator is used for storing liquid nitrogen cold energy;
the cold side outlet of the cold accumulator is connected with the cold side inlet of the heat exchanger, the cold side outlet of the heat exchanger is connected with the bottom inlet of the oil tank, and the bottom of the oil tank is provided with a gas disk stone to disperse nitrogen uniformly and wash fuel oil to form a nitrogen inerting subsystem;
a gas phase outlet at the upper part of the oil tank is connected to a hot side inlet of a heat exchanger through a fan, the fuel steam mixture and the low-temperature nitrogen perform heat exchange in the heat exchanger, and the hot side outlet of the heat exchanger is connected to a dryer and then connected to an inlet at the bottom of the oil tank to form a fuel steam cooling system;
the hot side of the cold accumulator, the evaporator and the compressor are connected end to end through a pipeline to form a refrigeration cycle, so that a nano composite phase change material cold accumulation subsystem is formed;
the system also comprises a measurement and control subsystem which comprises a controller and measurement and control devices connected with the controller in other systems.
The measurement and control device of the measurement and control subsystem comprises a first electric regulating valve connected with the outlet of the cold side of the regenerator, a second electric regulating valve connected with the outlet of the oil tank, a third electric regulating valve connected with the outlet of the dryer, an oxygen concentration sensor and a first temperature sensor which are arranged in the oil tank; the controller is electrically connected with the liquid nitrogen supply pump, the first electric regulating valve, the oxygen concentration sensor, the first temperature sensor, the second electric regulating valve, the fan and the third electric regulating valve respectively and used for controlling the liquid nitrogen supply pump, the first electric regulating valve, the second electric regulating valve, the fan and the third electric regulating valve to work according to the sensing data of the oxygen concentration sensor and the first temperature sensor.
The hot side of the cold accumulator, the throttle valve, the evaporator, the compressor and the fourth electric regulating valve are sequentially connected through a pipeline to form a refrigeration cycle; a second temperature sensor is arranged in the evaporator;
and the controller is electrically connected with the fourth electric regulating valve, the compressor, the throttle valve and the second temperature sensor respectively and is used for controlling the fourth electric regulating valve, the compressor and the throttle valve to work according to the sensing data of the second temperature sensor.
The cold accumulator is filled with a nano composite phase change material formed by mixing an ethylene glycol/n-heptanol organic phase change material and graphene nano particles, and the phase change temperature is-43 ℃.
The utility model also discloses a working method of liquid nitrogen formula machine carries oil tank inerting device, including following step:
1) inerting process with nitrogen purge
The liquid nitrogen bottle flows to the cold accumulator under the action of a liquid nitrogen supply pump, cold energy is stored in the nano composite material and is vaporized, the vaporized nitrogen gas is subjected to heat exchange with a hot side channel through a cold side channel of the heat exchanger, the temperature rises, the nitrogen gas enters the oil tank after being uniformly dispersed by the air disk stone, fuel oil in the oil tank is washed, oxygen escapes from the fuel oil, gas in the upper space of the oil tank is replaced, the oxygen is discharged, and the oil tank is inerted;
2) cooling inerting process
The fuel vapor mixture at the upper part of the fuel tank is sucked into a hot side channel of the heat exchanger through a fan, the temperature is reduced and liquefied under the heat exchange action of low-temperature nitrogen, water vapor is removed through a dryer, the water vapor is mixed with the low-temperature nitrogen and then flows back to the fuel tank, the fuel temperature in the fuel tank is reduced, and the fuel vapor content of the fuel vapor mixture is reduced to achieve the inerting purpose;
3) cold accumulation type refrigeration cycle
The cold accumulator absorbs cold energy carried by liquid nitrogen and stores the cold energy in the nano composite phase change material, the refrigerant absorbs heat in the evaporator and then turns into vapor, the vapor of the refrigerant is condensed at the hot side of the cold accumulator after being pressurized by the compressor and releases heat, and the liquefied refrigerant returns to the evaporator again after passing through the throttle valve to form a refrigeration cycle;
the method also comprises a data acquisition and control process of the nitrogen inerting subsystem and the fuel vapor cooling system: the outlet of the cold side of the regenerator is connected with a first electric regulating valve, the outlet of the oil tank is connected with a second electric regulating valve, and the outlet of the drier is connected with a third electric regulating valve; the oxygen concentration sensor and the first temperature sensor probe on the upper part of the oil tank extend into the upper space of the oil tank, the oxygen concentration and the temperature are monitored, and data are transmitted to the controller, when the oxygen concentration is lower than a set value, the controller outputs signals to control the liquid nitrogen supply pump, the first electric regulating valve, the second electric regulating valve, the fan and the third electric regulating valve to work, and when the oxygen concentration is higher than the set value, the controller controls the devices to stop working.
The method also comprises the data acquisition and control process of the nano composite phase change material cold accumulation subsystem: the cold accumulator hot side, the throttling valve, the evaporator, the compressor and the fourth electric regulating valve are sequentially connected through a pipeline to form a refrigeration cycle, a second temperature sensor is installed in the evaporator and used for monitoring the temperature of the evaporator and transmitting data to the controller, when the temperature is higher than a set value, the controller outputs signals to control the fourth electric regulating valve, the compressor and the throttling valve to work, and when the temperature is higher than the set value, the fourth electric regulating valve, the compressor and the throttling valve are controlled to stop working.
The utility model adopts the above technical scheme to compare with prior art, have following technological effect:
the utility model discloses a produce a large amount of inerting gases with liquid nitrogen vaporization, let in the aircraft fuel tank in wash and wash the fuel, replace the oxygen in the fuel and in the oil tank upper portion out, simultaneously, draw the fuel vapor mixture in oil tank upper portion out and carry out the heat exchange through heat exchanger and low temperature nitrogen gas, cool off fuel vapor mixture temperature and make the fuel vapor liquefaction, reduce the flammability of aircraft tank through reducing oxygen content and fuel vapor concentration in the oil tank, thereby reach the inerting purpose; the liquid nitrogen flows through the cold accumulator to be evaporated into nitrogen, and a large amount of cold energy generated when the liquid nitrogen is evaporated is absorbed and stored by the nano composite phase change material and forms an airborne refrigeration cycle with the evaporator. The device realizes the controllable automatic operation of the system through the oxygen concentration sensor and the temperature sensor, and has the advantages of no aircraft fuel compensation loss, high energy utilization rate, high inerting efficiency, no environmental pollution and the like.
Drawings
Fig. 1 is a schematic diagram of a liquid nitrogen type inerting device for an onboard fuel tank.
The system comprises a liquid nitrogen bottle 1, a liquid nitrogen bottle 2, a stop valve 3, a liquid nitrogen supply pump 4, a cold accumulator 5, a first electric regulating valve 6, a heat exchanger 7, a gas disc stone 8, an oil tank 9, an oxygen concentration sensor 10, a first temperature sensor 11, a second electric regulating valve 12, a fan 13, a dryer 14, a third electric regulating valve 14, a controller 15, a fourth electric regulating valve 201, a compressor 202, an evaporator 203, a throttle valve 204, and a second temperature sensor 205.
Detailed Description
The technical scheme of the utility model is further explained in detail with the attached drawings as follows:
the present invention may be embodied in many different forms and should not be construed as limited to the embodiments set forth herein. Rather, these embodiments are provided so that this disclosure will be thorough and complete, and will fully convey the scope of the invention to those skilled in the art. In the drawings, components are exaggerated for clarity.
As shown in fig. 1, fig. 1 is a liquid nitrogen type inerting device for an onboard fuel tank. The embodiment provides a liquid nitrogen type onboard oil tank inerting device which comprises a liquid nitrogen bottle 1, a stop valve 2, a liquid nitrogen supply pump 3, a cold accumulator 4, a first electric regulating valve 5, a heat exchanger 6, an air disc stone 7, an oil tank 8, an oxygen concentration sensor 9, a first temperature sensor 10, a second electric regulating valve 11, a fan 12, a dryer 13, a third electric regulating valve 14 and a controller 15;
the outlet of the liquid nitrogen bottle 1, the stop valve 2, the liquid nitrogen supply pump 3 and the cold side inlet of the cold accumulator 4 are connected in sequence through pipelines; the cold accumulator 4 is used for storing liquid nitrogen cold energy;
an outlet of the cold accumulator 4 is connected with a cold side inlet of a heat exchanger 6 through a first electric regulating valve 5, and a cold side outlet of the heat exchanger 6 is connected with a bottom inlet of an oil tank 8; the bottom of the oil tank 8 is provided with an air disk stone 7 for uniformly dispersing the nitrogen-rich and washing the fuel oil;
the gas phase outlet at the upper part of the oil tank 8, the second electric regulating valve 11, the fan 12, the hot side of the heat exchanger 6, the dryer 13, the third electric regulating valve 14 and the inlet at the bottom of the oil tank 8 are sequentially connected through pipelines; the dryer (13) is used for absorbing moisture in the cooled fuel vapor mixture;
the oxygen concentration sensor 9 and the first temperature sensor 10 are arranged in the oil tank 8 and are respectively used for measuring the oxygen concentration and the fuel temperature in the oil tank 8;
the controller 15 is electrically connected with the liquid nitrogen supply pump 3, the first electric regulating valve 5, the oxygen concentration sensor 9, the first temperature sensor 10, the second electric regulating valve 11, the fan 12 and the third electric regulating valve 14 respectively, and is used for controlling the liquid nitrogen supply pump 3, the first electric regulating valve 5, the second electric regulating valve 11, the fan 12 and the third electric regulating valve 14 to work according to the sensing data of the oxygen concentration sensor 9 and the first temperature sensor 10;
the hot side of the regenerator 4, the fourth electric regulating valve 201, the compressor 202, the evaporator 203 and the throttle valve 204 are connected in sequence through pipelines to form a refrigeration cycle; a second temperature sensor 205 is installed in the evaporator 203;
the controller 15 is electrically connected with the fourth electric regulating valve 201, the compressor 202, the throttle valve 204 and the second temperature sensor 205 respectively, and is used for controlling the fourth electric regulating valve 201, the compressor 202, the throttle valve 204 and the second temperature sensor 205 to work according to the sensing data of the second temperature sensor 205;
the cold accumulator 4 is filled with a nano composite phase change material formed by mixing an ethylene glycol/n-heptanol organic phase change material and graphene nano particles, and the phase change temperature is-43 ℃.
The utility model relates to a liquid nitrogen formula machine carries oil tank inerting device's working process as follows:
1) inerting process with nitrogen purge
The liquid nitrogen bottle 1 flows to the cold accumulator 4 under the action of the liquid nitrogen supply pump 3, cold energy is stored in the nano composite material and is vaporized, nitrogen gas after vaporization passes through the first electric regulating valve 5 and the cold side channel of the heat exchanger 6, then enters the oil tank 8 after being uniformly dispersed through the air disk stone 7, fuel oil in the oil tank 8 is washed, oxygen escapes from the fuel oil, gas in the upper space of the oil tank 8 is replaced, the oxygen is discharged, and the oil tank 8 is inerted.
2) Cooling inerting process
Under the attraction effect of the fan 12, the fuel steam mixture on the upper portion of the fuel tank 8 enters a hot side channel of the heat exchanger 6 through the second electric regulating valve 11, the temperature of the fuel steam mixture becomes low under the heat exchange effect of low-temperature nitrogen, the fuel steam is liquefied, the water vapor generated after the temperature is reduced is removed through the dryer 13, the fuel steam is regulated by the third electric regulating valve 14 and then mixed with the low-temperature nitrogen and then flows back to the fuel tank 8, the fuel temperature in the fuel tank 8 is reduced, and the fuel steam content of the fuel steam mixture becomes low, so that the inerting purpose is achieved.
3) Cold accumulation type refrigeration cycle
The hot side of the cold accumulator (4), the fourth electric regulating valve (201), the compressor (202), the evaporator (203) and the throttle valve (204) form a refrigeration cycle; the cold accumulator (4) absorbs a large amount of cold energy carried by liquid nitrogen and stores the cold energy in the nano composite phase change material, refrigerant absorbs heat in the evaporator (203) and then turns into vapor, the refrigerant vapor is pressurized by the compressor (202) and then condensed at the hot side of the cold accumulator (4) to release heat, and the liquefied refrigerant returns to the evaporator (203) again after passing through the throttle valve (204), so that a refrigeration cycle is formed.
4) Data acquisition and control process
Probes of the oxygen concentration sensor 9 and the first temperature sensor 10 extend into the upper space of the oil tank 10, and are used for monitoring the oxygen concentration and the temperature in the space and transmitting data to the controller 15. When the oxygen concentration is lower than the set value, the controller 15 outputs signals to control the liquid nitrogen supply pump (3), the first electric regulating valve (5), the second electric regulating valve (11), the fan (12) and the third electric regulating valve (14) to work, and when the oxygen concentration is higher than the set value, the devices are controlled to stop working.
The evaporator 203 is provided with a second temperature sensor 205 therein for monitoring the temperature of the evaporator 203 and transmitting data to the controller 15. When the temperature is higher than the set value, the controller 15 outputs signals to control the fourth electric control valve 201, the compressor 202 and the throttle valve 204 to work, and when the temperature is higher than the set value, the devices are controlled to stop working.
The utility model has the advantages that:
the utility model discloses a produce a large amount of inerting gases with liquid nitrogen vaporization, let in the aircraft fuel tank in wash and wash the fuel, replace the oxygen in the fuel and in the oil tank upper portion out, simultaneously, draw the fuel vapor mixture in oil tank upper portion out and carry out the heat exchange through heat exchanger and low temperature nitrogen gas, cool off fuel vapor mixture temperature and make the fuel vapor liquefaction, reduce the flammability of aircraft tank through reducing oxygen content and fuel vapor concentration in the oil tank, thereby reach the inerting purpose; the liquid nitrogen flows through the cold accumulator to be evaporated into nitrogen, and a large amount of cold energy generated when the liquid nitrogen is evaporated is absorbed and stored by the nano composite phase change material and forms an airborne refrigeration cycle with the evaporator. The device realizes the controllable automatic operation of the system through the oxygen concentration sensor and the temperature sensor, and has the advantages of no aircraft fuel compensation loss, high energy utilization rate, high inerting efficiency, no environmental pollution and the like.
The basic principles and the main features of the invention and the advantages of the invention have been shown and described above. It will be understood by those skilled in the art that the present invention is not limited to the above embodiments, and that the foregoing embodiments and descriptions are provided only to illustrate the principles of the present invention without departing from the spirit and scope of the present invention. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (4)
1. The utility model provides a liquid nitrogen formula machine carries oil tank inerting device which characterized in that: the device comprises a liquid nitrogen bottle (1), a liquid nitrogen supply pump (3), a cold accumulator (4), a heat exchanger (6), an oil tank (8), a fan (12) and a dryer (13), wherein liquid nitrogen in the liquid nitrogen bottle (1) enters through a cold side inlet of the cold accumulator (4), and the cold accumulator (4) is used for storing liquid nitrogen cold energy;
a cold side outlet of the regenerator (4) is connected with a cold side inlet of the heat exchanger (6), a cold side outlet of the heat exchanger (6) is connected with a bottom inlet of an oil tank (8), and the bottom of the oil tank (8) is provided with a gas disk stone (7) for uniformly dispersing nitrogen and washing fuel oil to form a nitrogen inerting subsystem;
a gas phase outlet at the upper part of the oil tank (8) is connected to a hot side inlet of the heat exchanger (6) through a fan (12), the fuel steam mixture and the low-temperature nitrogen exchange heat in the heat exchanger (6), and the hot side outlet of the heat exchanger (6) is connected to a dryer (13) and then connected to a bottom inlet of the oil tank (8) to form a fuel steam cooling system;
the hot side of the cold accumulator (4), the evaporator (203) and the compressor (202) are connected end to end through a pipeline to form a refrigeration cycle, so that a nano composite phase change material cold accumulation subsystem is formed;
the system also comprises a measurement and control subsystem which comprises a controller (15) and measurement and control devices connected with the controller in other systems.
2. The inerting device of claim 1, characterized in that it comprises: the measurement and control device of the measurement and control subsystem comprises a first electric regulating valve (5) connected with a cold side outlet of the cold accumulator (4), a second electric regulating valve (11) connected with an outlet of the oil tank (8), a third electric regulating valve (14) connected with an outlet of the dryer (13), an oxygen concentration sensor (9) arranged in the oil tank (8) and a first temperature sensor (10); the controller (15) is respectively electrically connected with the liquid nitrogen supply pump (3), the first electric regulating valve (5), the oxygen concentration sensor (9), the first temperature sensor (10), the second electric regulating valve (11), the fan (12) and the third electric regulating valve (14) and is used for controlling the liquid nitrogen supply pump (3), the first electric regulating valve (5), the second electric regulating valve (11), the fan (12) and the third electric regulating valve (14) to work according to the sensing data of the oxygen concentration sensor (9) and the first temperature sensor (10).
3. The inerting device of claim 1, characterized in that it comprises: the hot side of the cold accumulator (4), the throttle valve (204), the evaporator (203), the compressor (202) and the fourth electric regulating valve (201) are sequentially connected through pipelines to form a refrigeration cycle; a second temperature sensor (205) is arranged in the evaporator (203);
the controller (15) is respectively electrically connected with the fourth electric control valve (201), the compressor (202), the throttle valve (204) and the second temperature sensor (205) and is used for controlling the fourth electric control valve (201), the compressor (202) and the throttle valve (204) to work according to sensing data of the second temperature sensor (205).
4. The inerting device of claim 1, characterized in that it comprises: the cold accumulator (4) is filled with a nano composite phase change material formed by mixing an ethylene glycol/n-heptanol organic phase change material and graphene nano particles, and the phase change temperature is-43 ℃.
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| CN202020182670.0U CN211969761U (en) | 2020-02-19 | 2020-02-19 | Liquid nitrogen type airborne oil tank inerting device |
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Cited By (1)
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| CN111268147A (en) * | 2020-02-19 | 2020-06-12 | 南京航空航天大学 | Liquid nitrogen type airborne oil tank inerting device |
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| CN111268147A (en) * | 2020-02-19 | 2020-06-12 | 南京航空航天大学 | Liquid nitrogen type airborne oil tank inerting device |
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