EP4047259A1 - Niedrigtemperatur-volleinschlussbehälter mit extraktionsvorrichtung für material mit niedrigem flüssigkeitsstand - Google Patents

Niedrigtemperatur-volleinschlussbehälter mit extraktionsvorrichtung für material mit niedrigem flüssigkeitsstand Download PDF

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Publication number
EP4047259A1
EP4047259A1 EP20891908.4A EP20891908A EP4047259A1 EP 4047259 A1 EP4047259 A1 EP 4047259A1 EP 20891908 A EP20891908 A EP 20891908A EP 4047259 A1 EP4047259 A1 EP 4047259A1
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EP
European Patent Office
Prior art keywords
tank
venturi mixer
low
liquid level
material circulation
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.)
Pending
Application number
EP20891908.4A
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English (en)
French (fr)
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EP4047259A4 (de
Inventor
Jiecheng YING
Shuheng XIAO
Qiang Lu
Lin Wang
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
China International Marine Containers Group Co Ltd
CIMC Enric Investment Holdings Shenzhen Co Ltd
CIMC Enric Engineering Technology Co Ltd
Original Assignee
China International Marine Containers Group Co Ltd
CIMC Enric Investment Holdings Shenzhen Co Ltd
CIMC Enric Engineering Technology Co Ltd
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Application filed by China International Marine Containers Group Co Ltd, CIMC Enric Investment Holdings Shenzhen Co Ltd, CIMC Enric Engineering Technology Co Ltd filed Critical China International Marine Containers Group Co Ltd
Publication of EP4047259A1 publication Critical patent/EP4047259A1/de
Publication of EP4047259A4 publication Critical patent/EP4047259A4/de
Pending legal-status Critical Current

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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C3/00—Vessels not under pressure
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C7/00—Methods or apparatus for discharging liquefied, solidified, or compressed gases from pressure vessels, not covered by another subclass
    • F17C7/02—Discharging liquefied gases
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C9/00—Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2201/00—Vessel construction, in particular geometry, arrangement or size
    • F17C2201/01—Shape
    • F17C2201/0104—Shape cylindrical
    • F17C2201/0109—Shape cylindrical with exteriorly curved end-piece
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2201/00—Vessel construction, in particular geometry, arrangement or size
    • F17C2201/01—Shape
    • F17C2201/0104—Shape cylindrical
    • F17C2201/0119—Shape cylindrical with flat end-piece
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2201/00—Vessel construction, in particular geometry, arrangement or size
    • F17C2201/03—Orientation
    • F17C2201/032—Orientation with substantially vertical main axis
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2201/00—Vessel construction, in particular geometry, arrangement or size
    • F17C2201/05—Size
    • F17C2201/052—Size large (>1000 m3)
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2203/00—Vessel construction, in particular walls or details thereof
    • F17C2203/03—Thermal insulations
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2203/00—Vessel construction, in particular walls or details thereof
    • F17C2203/06—Materials for walls or layers thereof; Properties or structures of walls or their materials
    • F17C2203/0602—Wall structures; Special features thereof
    • F17C2203/0612—Wall structures
    • F17C2203/0626—Multiple walls
    • F17C2203/0629—Two walls
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2205/00—Vessel construction, in particular mounting arrangements, attachments or identifications means
    • F17C2205/03—Fluid connections, filters, valves, closure means or other attachments
    • F17C2205/0302—Fittings, valves, filters, or components in connection with the gas storage device
    • F17C2205/0323—Valves
    • F17C2205/0326—Valves electrically actuated
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2221/00—Handled fluid, in particular type of fluid
    • F17C2221/03—Mixtures
    • F17C2221/032—Hydrocarbons
    • F17C2221/033—Methane, e.g. natural gas, CNG, LNG, GNL, GNC, PLNG
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2221/00—Handled fluid, in particular type of fluid
    • F17C2221/03—Mixtures
    • F17C2221/032—Hydrocarbons
    • F17C2221/035—Propane butane, e.g. LPG, GPL
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0107—Single phase
    • F17C2223/013—Single phase liquid
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0146—Two-phase
    • F17C2223/0153—Liquefied gas, e.g. LPG, GPL
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2223/00—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel
    • F17C2223/01—Handled fluid before transfer, i.e. state of fluid when stored in the vessel or before transfer from the vessel characterised by the phase
    • F17C2223/0146—Two-phase
    • F17C2223/0153—Liquefied gas, e.g. LPG, GPL
    • F17C2223/0161—Liquefied gas, e.g. LPG, GPL cryogenic, e.g. LNG, GNL, PLNG
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/01—Propulsion of the fluid
    • F17C2227/0114—Propulsion of the fluid with vacuum injectors, e.g. venturi
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/01—Propulsion of the fluid
    • F17C2227/0128—Propulsion of the fluid with pumps or compressors
    • F17C2227/0135—Pumps
    • F17C2227/0142—Pumps with specified pump type, e.g. piston or impulsive type
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/01—Propulsion of the fluid
    • F17C2227/0128—Propulsion of the fluid with pumps or compressors
    • F17C2227/0171—Arrangement
    • F17C2227/0178—Arrangement in the vessel
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2227/00—Transfer of fluids, i.e. method or means for transferring the fluid; Heat exchange with the fluid
    • F17C2227/01—Propulsion of the fluid
    • F17C2227/0128—Propulsion of the fluid with pumps or compressors
    • F17C2227/0171—Arrangement
    • F17C2227/0185—Arrangement comprising several pumps or compressors
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17—STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17C—VESSELS FOR CONTAINING OR STORING COMPRESSED, LIQUEFIED OR SOLIDIFIED GASES; FIXED-CAPACITY GAS-HOLDERS; FILLING VESSELS WITH, OR DISCHARGING FROM VESSELS, COMPRESSED, LIQUEFIED, OR SOLIDIFIED GASES
    • F17C2250/00—Accessories; Control means; Indicating, measuring or monitoring of parameters
    • F17C2250/04—Indicating or measuring of parameters as input values
    • F17C2250/0404—Parameters indicated or measured
    • F17C2250/0408—Level of content in the vessel

Definitions

  • the present disclosure relates to the technical field of low-temperature liquefied gas storage, and more particularly, to a cryogenic full containment storage tank having a low liquid level material extraction device.
  • Substances that are gaseous at normal temperature and pressure but can be liquefied after proper freezing can be safely and efficiently stored in storage tanks with low temperature and normal pressure.
  • Substances in the petrochemical industry that meet this characteristic include methane, ethylene, ethane, propylene, propane, butene, butane and other hydrocarbons , and substances in the chemical industry that meet this characteristic include ammonia .
  • methane is the main component of natural gas
  • propane and butane are the main components of liquefied gas, they are mainly used as industrial and civil clean energy.
  • the consumption of clean energy such as liquefied hydrocarbons and liquefied natural gas (hereinafter referred to as LNG) is increasing.
  • the height of the tank dome plus the height of the tank wall is far greater than the suction vacuum height that the liquid can be pumped up to, so the discharging pump can only work under the liquid, that is, the discharging pump is a cryogenic submersible pump.
  • the cryogenic submersible pump requires sufficient low-temperature medium in the storage tank when starting, so the minimum liquid level must not be lower than the minimum operable liquid level required by the cryogenic submersible pump.
  • the minimum operable liquid level of the cryogenic submersible pump plus a certain safety margin is usually about 1.2 m, that is, the zone below 1.2 m from the bottom of the cryogenic full containment storage tank is usually a "dead zone" for operation, which results in a large ineffective working volume at the bottom of the tank.
  • an inner tank diameter of 50000 m 3 cryogenic full containment storage tank is about ⁇ 46 m, so a volume with a height of 1.2 m is about 1994 m 3 .
  • An inner tank diameter of 80000 m 3 cryogenic full containment storage tank is about ⁇ 59 m, so a volume with a height of 1.2 m height is about 3280 m 3 .
  • An inner tank diameter of 160000 m 3 cryogenic full containment storage tank is about ⁇ 87 m, and a volume with a height of 1.2 m height is about 7134 m 3 .
  • the material at a bottom of the tank in range of the ineffective working volume cannot be discharged out of the tank through the cryogenic submersible pump. If the storage tank needs to perform outage maintenances, the material at the bottom can only be discharged by vaporization, which consumes a lot of energy and also needs a long period of time.
  • An object of the present disclosure is to provide a cryogenic full containment storage tank having a low liquid level material extraction device, so as to solve the technical problem in the prior art that the ineffective working volume at the bottom of the storage tank is too large and there are too much residual medium that cannot be extracted.
  • a cryogenic full containment storage tank having a low liquid level material extraction device comprising: an inner tank, an outer tank surrounding a periphery of the inner tank, an operation platform arranged on a top of the outer tank, and a material extraction device capable of extracting low liquid level material.
  • the material extraction device capable of extracting low liquid level material comprises: a material circulation tank arranged on the operation platform, which is configured to contain low-temperature medium; a first Venturi mixer arranged at a bottom of the inner tank, wherein two ends of the first Venturi mixer are respectively an inlet and an outlet, and an outer periphery of the first Venturi mixer is provided with a suction hole; an inlet pipeline connected an outlet of the material circulation tank to the inlet of the first Venturi mixer; an outlet pipeline connected the outlet of the first Venturi mixer to an inlet of the material circulation tank; and a cryopump, arranged on the operation platform, and connected to the inlet pipeline; wherein while performing a medium extraction, the low-temperature medium in the material circulation tank enter the first Venturi mixer through the cryopump and the inlet pipeline, so that the low-temperature medium in the inner tank is capable of entering the first Venturi mixer through the suction hole under an action of a pressure difference, and entering the material circulation tank through the outlet pipeline after mixing.
  • the first Venturi mixer comprises a constriction section, a throat section and a diffusion section connected in sequence.
  • a large-end opening of the constriction section is configured as the inlet of the first Venturi mixer, and is connected to the inlet pipeline.
  • a large-end opening of the diffusion section is configured as the outlet of the first Venturi mixer, and is connected to the outlet pipeline.
  • Two ends of the throat section are respectively connected to a small-end opening of the constriction section and a small-end opening of the diffusion section.
  • the suction hole is opened corresponding to an outer periphery of the throat section, and is communicated with an interior of the throat section.
  • the first Venturi mixer is placed horizontally in the inner tank.
  • the first Venturi mixer further comprises a suction cavity arranged around the outer periphery of the throat section and communicated with the interior of the throat section. Two ends of the suction cavity are respectively connected to an outer wall of the constriction section and an outer wall of the diffusion section. The suction hole is opened on an outer peripheral wall of the suction cavity.
  • the suction hole of the first Venturi mixer is opened on an outer peripheral wall of the throat section.
  • the first Venturi mixer further comprises a suction pipe correspondingly arranged at the suction hole, and the suction pipe is communicated with an interior of the inner tank.
  • the material circulation tank is further provided with a medium output port for outputting the low-temperature medium to the outside, and a liquid level control mechanism is provided to control an opening and closing of the medium output port when a preset liquid level is reached, and the preset liquid level is higher than a liquid level required for an operation of the cryopump during medium extraction.
  • the liquid level control mechanism is an overflow weir arranged in the material circulation tank. An outlet of the material circulation tank is communicated with an inner space of the overflow weir, and the medium output port is communicated with an outer space of the overflow weir.
  • the liquid level control mechanism is an overflow port arranged on a side wall of the material circulation tank, wherein a height of the overflow port is higher than the outlet of the material circulation tank, and the overflow port is communicated with the medium output port.
  • the liquid level control mechanism comprises an electrically connected liquid level gauge and a valve, wherein the liquid level gauge is configured to detect a liquid level in the material circulation tank, and the valve is correspondingly arranged at the medium output port.
  • the inlet pipeline is provided with a control valve to adjust a flow rate in the inlet pipeline, the control valve is located outside the outer tank, and the cryopump is located between the material circulation tank and the control valve.
  • the material extraction device further comprises a pressurizing unit, which is arranged on the outlet pipeline to increase a power for the low-temperature medium to flow to the material circulation tank.
  • the pressurizing unit comprises: a second Venturi mixer, a suction hole and an outlet of which are connected in series to the outlet pipeline; a pressurizing inlet pipeline connected an inlet of the second Venturi mixer to the outlet of the material circulation tank; and a pressurizing control valve arranged on the pressurizing inlet pipeline to adjust a flow rate in the pressurizing inlet pipeline.
  • the cryogenic full containment storage tank of the present disclosure is equipped with a material extraction device capable of extracting low liquid level material
  • the material extraction device comprises a material circulation tank, a cryopump arranged at an operation platform at a top of the tank, a Venturi mixer located at a bottom of the inner tank and corresponding connecting pipelines.
  • the low-temperature medium in the material circulation tank enters the Venturi mixer through the cryopump.
  • the low-temperature medium will form a local low-pressure and high-speed flow entrainment effect in the Venturi mixer, making the low-temperature medium enter the Venturi mixer through the suction hole under the action of the pressure difference, and the mixed low-temperature medium returns to the material circulation tank together.
  • the flow rate of the low-temperature medium returned to the material circulation tank is greater than the flow rate of the low-temperature medium pumped out from the material circulation tank, and the difference is the extracted low-temperature medium.
  • the material extraction device is mainly used as a supplementary discharge measure after the submersible pump in the cryogenic full containment storage tank is pumped to the minimum liquid level and shut down.
  • This extraction device can extract the low liquid level low-temperature medium that is originally in the "dead zone" for operation, and the low-temperature medium above the liquid level where the suction hole of the Venturi mixer is located can be extracted by the material extraction device.
  • the liquid level of the cryogenic full containment storage tank can be lowered to the position where the suction hole or the suction pipe of the first Venturi mixer is located, which is significantly lower than the minimum operable liquid level required by the submersible pump in the prior art, so that the ineffective volume of the cryogenic full containment storage tank can be significantly reduced, and the volume utilization rate of the tank can be improved.
  • the effective working volume of the full containment storage tank can be increased.
  • the effective working volume of the full containment storage tank can be increased.
  • the height of the inner and outer tanks can be reduced, thereby saving engineering investment.
  • the present disclosure provides a cryogenic full containment storage tank for storing liquefied low-temperature medium.
  • the low-temperature medium may be a hydrocarbon such as methane, ethylene, ethane, propylene, propane, butene and butane, and may also be ammonia commonly used in the chemical industry.
  • the cryogenic full containment storage tank provided in this embodiment generally includes an inner tank 1 for storing the low-temperature medium, an outer tank 2 surrounding a periphery of the inner tank 1, an operation platform 3 arranged on a top of the outer tank 2, a pump column 4 extends through the top of the outer tank 2 to a bottom of the inner tank 1, a submersible pump 5 arranged in the pump column 4, and a material extraction device 6 for extracting the low liquid level material from the bottom of the inner tank 1.
  • Each of the inner tank 1 and the outer tank 2 generally includes a bottom plate arranged horizontally and a cylindrical body erected on the bottom plate.
  • a heat insulating layer is provided between the bottom plate of the inner tank 1 and the bottom plate of the outer tank 2, and a heat insulating layer is provided between the cylindrical body of the inner tank 1 and the cylindrical body of the outer tank 2.
  • a dome is provided on the top of the outer tank 2, a top plate is suspended below the dome, and a heat insulating layer is also arranged between the dome and the top plate.
  • the top plate is connected to the inner tank 1 in a soft sealing manner.
  • the pump column 4 extends through the top of the outer tank 2 to the bottom of the inner tank 1.
  • the submersible pump 5 is arranged at a bottom of the pump column 4 and is immersed in the low-temperature medium of the inner tank 1, which is configured to transport the low-temperature medium in the inner tank 1 to the outside through the pump column 4.
  • the operation platform 3 is fixed on the top of the outer tank 2, which may be configured to accommodate various pipeline valves and working accessories which the cryogenic full containment storage tank is equipped with, allowing operators to perform work and maintenance on it.
  • the cryogenic full containment storage tank in this embodiment is equipped with a material extraction device 6, which is used as a supplementary discharge device after the submersible pump 5 is pumped to the minimum liquid level L1 and shuts down, so as to reduce the ineffective volume of the cryogenic full containment storage tank.
  • the material extraction device 6 involved in the present disclosure can not only extract the low liquid level material (that is, the low-temperature medium below the minimum operable liquid level L1 of the submersible pump 5), but also operate in the liquid level range where the submersible pump 5 in the pump column 4 can function. Therefore, in some cases, it may also be used as a backup facility with a small flow output other than the submersible pump 5.
  • the material extraction device 6 will be described in detail below with reference to FIG. 2 , and other specific structures including the inner tank 1, the outer tank 2, the operation platform 3, the pump column 4, and the submersible pump 5 can be referred to the structure of the related technology of the full-containment tank, which will not be described in detail herein.
  • the material extraction device 6 of this embodiment includes a material circulation tank 61, a first Venturi mixer 62, an inlet pipeline 63, an outlet pipeline 64 and a cryopump 65. Further, a control valve 66 is further provided on the inlet pipeline 63.
  • the material circulation tank 61 in this embodiment is a horizontal low-temperature tank, which is arranged on the operation platform 3.
  • An inside of the material circulation tank 61 is configured to contain the low-temperature medium, and an outside of the material circulation tank 61 may be wrapped with cold insulating material.
  • an overflow weir 611 is arranged in the material circulation tank 61, and the overflow weir 611 divides the internal space of the material circulation tank 61 into two parts.
  • the low-temperature medium in the overflow weir 611 i.e., a left side of the overflow weir 611 in the figure
  • the low-temperature medium overflow outside the overflow weir 611 i.e., a right side of the overflow weir 611 in the figure.
  • the space on the left side of the overflow weir 611 should meet the circulating volume requirements for medium extraction of the low-temperature medium, and the height of the overflow weir 611 should meet the requirements of the minimum operable liquid level of the cryopump 65. On this basis, the height of the overflow weir 611 is set according to the practice situation.
  • An outlet 6101 is provided at a bottom of a left end of the material circulation tank 61, and the outlet 6101 is communicated with the space enclosed by the overflow weir 611, which is configured to output the low-temperature medium during medium extraction.
  • a medium output port 6103 is further provided at a bottom of a right end of the material circulation tank 61, and the medium output port 6103 is communicated with the space outside the overflow weir 611 in the material circulation tank 61, which is configured to output the low-temperature medium to the outside.
  • An inlet 6102 is provided on a left side of a top of the material circulation tank 61, which is configured to receive the low-temperature medium.
  • the first Venturi mixer 62 is placed horizontally on a bottom plate of the inner tank 1 so as to have a low installation height.
  • the first Venturi mixer 62 is a liquid-liquid mixer, which mainly includes a constriction section 621, a throat section 622 and a diffusion section 623 connected in sequence.
  • the first Venturi mixer 62 is further provided with a suction cavity 624.
  • Each one of the constriction section 621 and the diffusion section 623 is a hollow structure with gradient cross-section, a large-end opening of the constriction section 621 configured as an inlet 6201 of the first Venturi mixer 62, and a large-end opening of the diffusion section 623 configured as an outlet 6203 of the first Venturi mixer 62.
  • One end of the throat section 622 is connected to a small-end opening of the constriction section 621, and the other end thereof is aligned with a small-end opening of the diffusion section 623.
  • the suction cavity 624 is circumferentially arranged on a periphery of the throat section 622, forming a dual cavity structure at the throat section 622. Two ends of the suction cavity 624 are respectively connected to an outer wall of the constriction section 621 and an outer wall of the diffusion section 623. An outer peripheral wall of the suction cavity 624 is provided with a plurality of suction holes 6202, and these suction holes 6202 are communicated with an interior of the inner tank 1, so that the low-temperature medium in the inner tank 1 can be sucked into the suction cavity 624.
  • An annular cavity is formed between the suction cavity 624 and the throat section 622, and the suction cavity 624 is communicated with an interior of the throat section 622, so the low-temperature medium in the suction cavity 624 can further enter the throat section 622.
  • the inlet pipeline 63 extends through the top of the outer tank 2, and connects the inlet 6201 of the first Venturi mixer 62 to the outlet 6101 of the material circulation tank 61, so as to guide the low-temperature medium in the material circulation tank 61 into the first Venturi mixer 62 for extraction.
  • the outlet pipeline 64 also extends through the top of the outer tank 2, and connects the inlet 6102 of the material circulation tank 61 to the outlet 6203 of the first Venturi mixer 62, so as to guide the low-temperature medium in the first Venturi mixer 62 into the material circulation tank 61.
  • the cryopump 65 is arranged on the operation platform 3 and is connected to the inlet pipeline 63 to provide power for the flow of the low-temperature medium.
  • the cryopump 65 is a non-submerged pump, that is, it is not required to be immersed in the low-temperature medium, and it may be a non-submerged pump with any structure.
  • the control valve 66 is arranged on the inlet pipeline 63, so that it can not only control the opening and closing of the inlet pipeline 63, but also adjust a flow rate of the low-temperature medium in the inlet pipeline 63.
  • the control valve 66 is located downstream of the cryopump 65, but outside the outer tank 2.
  • the above-mentioned material circulation tank 61, the first Venturi mixer 62, the inlet pipeline 63, the extraction pipeline 64, the cryopump 65 and the control valve 66 are all required to be able to withstand the temperature of the extracted low-temperature medium, so they are made of low-temperature materials capable of withstanding the corresponding temperature.
  • the working principle of the material extraction device 6 is as follows. While extracting medium, the low-temperature medium in the material circulation tank 61 is driven by the power of the cryopump 65 and enters the first Venturi mixer 62 through the inlet pipeline 63.
  • the low-temperature medium guided into the first Venturi mixer 62 from the material circulation tank 61 is referred to as initial low-temperature medium F0.
  • the flow speed increases, and the pressure decreases, resulting in an entrainment effect of local low pressure and high-speed flow at the throat section 622, so that the low-temperature medium Fi in the inner tank 1 enters the first Venturi mixer 62 through the suction holes 6202 under the action of the pressure difference.
  • the sucked low-temperature medium Fi is mixed with the initial low-temperature medium F0.
  • the suction cavity 624 is further provided on a periphery of the throat section 622 of the first Venturi mixer 62, and the low-temperature medium in the inner tank 1 is first sucked into the suction cavity 624, and then enters the throat section 622 for mixing, so that the momentum of the initial low-temperature medium F0 can be more effectively utilized, and the mixed low-temperature medium can flow back to the material circulation tank 61 more smoothly.
  • the flow rate of the low-temperature medium reaching the material circulation tank 61 is greater than the flow rate of the initial low-temperature medium initially pumped into the first Venturi mixer 62 from the material circulation tank 61, and the excess part is the low-temperature medium extracted from the inner tank 1.
  • the low-temperature medium in the inner tank 1 can be continuously extracted into the material circulation tank 61.
  • the low-temperature medium located in the overflow weir 611 in the material circulation tank 61 is used to maintain the medium extraction operation.
  • the low-temperature medium in the material circulation tank 61 exceeds the overflow weir 611, the low-temperature medium beyond the height of the overflow weir 611 can be transported outward through the medium output port 6103.
  • the material extraction device 6a is further provided with a pressurizing unit 67 on the basis of the foregoing embodiment, and the pressurizing unit 67 is provided on the outlet pipeline 64, and the pressurizing unit 67 is configured to increase the power of the mixed low-temperature medium to flow to the material circulation tank 61a, so that the low-temperature medium can flow back to the material circulation tank 61a more smoothly. It is suitable for situations with a larger pumping height, such as a cryogenic full containment storage tank with a larger height.
  • the pressurizing unit 67 includes a second Venturi mixer 671, a pressurizing inlet pipeline 672 and a pressurizing control valve 673.
  • a composition structure of the second Venturi mixer 671 may be the same as that of the first Venturi mixer 62.
  • a suction hole 6712 and an outlet 6713 of the second Venturi mixer 671 are connected in series to the outlet pipeline 64a.
  • the outlet pipeline 64a is divided into a first outlet section 641a and a second outlet section 642a, and the first outlet section 641a connects the outlet 6203 of the first Venturi mixer 62 to the suction hole 6712 of the second Venturi mixer 671, and the second outlet section 642a connects the outlet 6713 of the second Venturi mixer 671 to the inlet 6102a of the material circulation tank 61a.
  • the pressurizing inlet pipeline 672 communicates the inlet 6711 of the second Venturi mixer 671 with the outlet 6101a of the material circulation tank 61a, so as to guide a certain amount of initial low-temperature medium from the material circulation tank 61a into the second Venturi mixer 671.
  • the initial low-temperature medium is further mixed with the mixed low-temperature medium from the first Venturi mixer 62 in the second Venturi mixer 671 to increase the pressure, so that the low-temperature medium has greater power to return to the material circulation tank 61a from the second outlet section 642a.
  • the pressurizing control valve 673 is arranged on the pressurizing inlet pipeline 672. On the one hand, it controls the opening and closing of the pressurizing inlet pipeline 672 , and on the other hand, it also regulates a flow rate in the pressurizing inlet pipeline 672.
  • the second Venturi mixer 671, the pressurizing inlet pipeline 672 and the pressurizing control valve 673 are also required to be able to withstand the temperature of the extracted low-temperature medium, so they are made of low-temperature materials capable of withstanding the corresponding temperature.
  • the second Venturi mixer 671 is configured to increase the refluxing power of the low-temperature medium, and forms a two-stage series extraction process.
  • more Venturi mixers may be connected in series to the outlet pipeline 64/64a to form a multi-stage series extraction process.
  • the connection method of multi-stage series extraction may be deduced by analogy.
  • the material circulation tank 61a is a vertical storage tank.
  • the inlet 6102a of the material circulation tank 61a is located at the top, and the outlet 6101a of the material circulation tank 61a is located on the side wall close to the bottom.
  • There is no overflow weir 611 in the material circulation tank 61a but an overflow port 6104a is provided on the side wall of the material circulation tank 61a.
  • the height of the overflow port 6104a is higher than the outlet 6101a of the material circulation tank 61a, and is higher than the liquid level required for medium extraction.
  • the medium outlet port 6103a is extended out from and communicated with the overflow port 6104a.
  • the structure of the vertical material circulation tank 61a is also applicable to the material extraction device 6 in the previous embodiment.
  • the material circulation tank 61/61a adopts the structure of the overflow weir 611 and the overflow port 6104a to form a liquid level control mechanism, so as to control the opening and closing of the medium output port 6103/6103a when the preset liquid level is reached.
  • the liquid level control mechanism may further include an electrically connected liquid level gauge and a valve, the liquid level gauge is configured to detect the liquid level in the material circulation tank, and the valve is correspondingly arranged at the medium output port.
  • the Venturi mixers 62/671 in the above embodiments can also be replaced with a structure shown in FIG. 6 .
  • the Venturi mixer 62b is not equipped with the suction cavity 624, but a plurality of suction holes 6202b are opened on the outer peripheral wall of the throat section 622b, and each suction hole 6202b is further provided with a suction pipe 625b correspondingly.
  • the low-temperature medium Fi in the inner tank 1 can be guided into the throat section 622b through the suction pipes 625b, and is mixed with the initial low-temperature medium Fi, and the mixed low-temperature medium Fm is guided to the next process.
  • the suction pipes 625b may also be removed, and the low-temperature medium Fi in the inner tank 1 is directly sucked through the suction hole 6202b on the outer peripheral wall of the throat section 622b.
  • a suction pipe may also be added at the suction hole 6202 of the suction cavity 624.
  • a suction pipe may also be added at the suction hole 6712 of the second Venturi mixer 671.
  • the cryogenic full containment storage tank in each embodiment of the present disclosure when the cryogenic full containment storage tank in each embodiment of the present disclosure is in normal operation, the low-temperature medium is outputted through the pump column 4 under the power of the submersible pump 5.
  • the submersible pump 5 can reduce the liquid level in the cryogenic full containment storage tank to the minimum position L1 shown in FIG. 1 and FIG. 3 .
  • L1 is roughly about 1.2 m.
  • the material extraction device 6/6a is adopted to carry out the extraction, and the material extraction device 6/6a continuously extracts the low-temperature medium at the bottom of the inner tank 1 according to the working principle described above, until the liquid level drops to the first Venturi mixer 62, and the liquid level in this circumstance is located at L2.
  • the L2 may be approximately 0.2 m to 0.3 m.
  • the liquid level in the inner tank 1 may be reduced by about 1m, which significantly reduces the ineffective volume of the cryogenic full containment storage tank, and improves the volume utilization rate of the cryogenic full containment storage tank.
  • the power part and the control part of the material extraction device 6/6a are arranged outside the outer tank 2. Except that the Venturi mixer 62/671/62b and the pipeline part need to be immersed in the low-temperature medium, no other equipment or cables are immersed in the low-temperature medium, and the components in the tank can achieve maintenance-free operation throughout the life of the tank. It is worth mentioning that when the liquid level of the cryogenic full containment storage tank is higher than L1, the material circulation tank 61/61a of the material extraction device 6/6a may not store the low-temperature medium. When it is required to extract the low liquid level medium, the material circulation tank 61/61a may be filled with a certain amount of low-temperature medium as the initial power medium.

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  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
EP20891908.4A 2019-11-29 2020-11-27 Niedrigtemperatur-volleinschlussbehälter mit extraktionsvorrichtung für material mit niedrigem flüssigkeitsstand Pending EP4047259A4 (de)

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CN201911198981.4A CN112879795A (zh) 2019-11-29 2019-11-29 一种具有低液位物料抽提装置的低温全容罐
PCT/CN2020/132342 WO2021104469A1 (zh) 2019-11-29 2020-11-27 一种具有低液位物料抽提装置的低温全容罐

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DE102004043080A1 (de) * 2004-09-07 2006-03-09 Bayerische Motoren Werke Ag Entnahmeeinrichtung für einen druckfesten Behälter mit kondensiertem Gas
FR2876981B1 (fr) * 2004-10-27 2006-12-15 Gaz Transp Et Technigaz Soc Pa Dispositif pour l'alimentation en combustible d'une installation de production d'energie d'un navire
JP2007024166A (ja) * 2005-07-15 2007-02-01 Taiyo Nippon Sanso Corp 低温液化ガス供給装置
JP2007292180A (ja) * 2006-04-25 2007-11-08 Chiyoda Corp 液化ガス設備の保冷循環システム
NL2009328C2 (en) * 2012-08-16 2014-02-18 Vialle Alternative Fuel Systems Bv Assembly for buffering a liquefied petroleum gas in a liquefied petroleum gas storage and storage bag therefore.
CN203248988U (zh) * 2013-04-22 2013-10-23 中国海洋石油总公司 一种lng接收站蒸发气零排放处理系统
CN204384858U (zh) * 2014-12-24 2015-06-10 赤峰盛森硅业科技发展有限公司 液体抽取与输送装置
CN207716090U (zh) * 2017-07-31 2018-08-10 新兴能源装备股份有限公司 一种低温储罐快速自增压管路
CN208859947U (zh) * 2018-10-10 2019-05-14 乳山市创新新能源科技有限公司 一种lng冷能提取直接制冷系统
CN109928497A (zh) * 2019-04-15 2019-06-25 湖南中拓环境工程有限公司 一种改良型升流式复合缺氧池
CN211083611U (zh) * 2019-11-29 2020-07-24 南京扬子石油化工设计工程有限责任公司 一种具有低液位物料抽提装置的低温全容罐

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