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CN201306600Y - Liquid phase pipe structure of cryogenic insulation pressure vessel - Google Patents

Liquid phase pipe structure of cryogenic insulation pressure vessel Download PDF

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Publication number
CN201306600Y
CN201306600Y CNU2008202198233U CN200820219823U CN201306600Y CN 201306600 Y CN201306600 Y CN 201306600Y CN U2008202198233 U CNU2008202198233 U CN U2008202198233U CN 200820219823 U CN200820219823 U CN 200820219823U CN 201306600 Y CN201306600 Y CN 201306600Y
Authority
CN
China
Prior art keywords
liquid
phase tube
cryogenic
liquid phase
inner bag
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.)
Expired - Fee Related
Application number
CNU2008202198233U
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Chinese (zh)
Inventor
谢志忠
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.)
ASTRONAUTIC XINGUANG LOW TEMP VESSELS Manufacturing Co Ltd SHENYANG
Original Assignee
ASTRONAUTIC XINGUANG LOW TEMP VESSELS Manufacturing Co Ltd SHENYANG
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by ASTRONAUTIC XINGUANG LOW TEMP VESSELS Manufacturing Co Ltd SHENYANG filed Critical ASTRONAUTIC XINGUANG LOW TEMP VESSELS Manufacturing Co Ltd SHENYANG
Priority to CNU2008202198233U priority Critical patent/CN201306600Y/en
Application granted granted Critical
Publication of CN201306600Y publication Critical patent/CN201306600Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

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Abstract

The utility model relates to a liquid phase pipe structure of a cryogenic insulation pressure vessel, which is the liquid phase pipe structure optimally selected by various cryogenic insulation pressure vessels. The liquid phase pipe structure is characterized in that a buffering structure which facilitates to form a vapor liquid equilibrium interface is arranged between two ends of a liquid phase pipe. The utility model has the advantages that the volatilization loss of cryogenic liquid is reduced obviously, the storage days of the cryogenic liquid is prolonged, a welding seam at the connecting part between an inner liner and an outer liner can be effectively avoided from cracking, the vacuum degree of a vacuum interlayer can also be avoided from being destroyed and the maintenance cost of the vessel is reduced.

Description

Cryo Heat Insulation pressurized container liquid-phase tube structure
Technical field
The utility model relates to a kind of Cryo Heat Insulation pressurized container, relates in particular to a kind of Cryo Heat Insulation pressurized container liquid-phase tube structure, is the liquid-phase tube structure of various Cryo Heat Insulation pressurized container first-selections.
Background technique
The Cryo Heat Insulation pressurized container is the general name of the equipment of storage and conveying liquified gas, also is the general designation of Dewar type container, low temperature cistern and storage tank.As everyone knows, the temperature of cryogenic liquide is very low, under 101.325Kpa pressure, liquid oxygen-183 ℃, liquid nitrogen-196 ℃, liquid argon-186 ℃, therefore, the necessary heat-insulating property of low-temperature (low temperature) vessel Structural Design Requirement is good, usually adopt the structural type of inside and outside courage combination, interlayer adopts vacuum insulation in the middle of it, interlayer is filled perlite or is adopted coated material to prevent heat conduction, evacuator is installed on the shell, utilize the vacuum unit that the interlayer air is found time, make every effort to handle along with increasing of time will be by convection current with this, the heat that approach such as conduction and radiation pass to cryogenic liquide reduces to alap degree, keeps low temperature system proper functioning, guarantees the purpose of the shelf life of cryogenic liquide.Various pipelines and valve are installed on the shell of tank body,, are used the cryogenic liquide of splendid attire in the container by the switch transporting low temperature liquid of valve.However, people find under study for action, link between the inside and outside courage also has certain influence to conducting heat, particularly the indusion tube between the inside and outside courage of tradition is a straight tube, two ends are welded on respectively on the inside and outside courage, this structure is not owing to cushion, under the cryogenic liquide effect, often cause the situation of weld cracking to happen occasionally, and bigger harm is that also indusion tube can be vaporized in a large number with the extraneous part that directly contacts in the cryogenic liquide course of conveying, vaporization back pressure raises, enter in the container along pipe, the result vaporizes the cryogenic liquide in the container again, this has just quickened inside and outside transmission of heat, not only loss cryogenic liquide, and the storage life of cryogenic liquide had a negative impact.Based on above-mentioned situation,,, be necessary the structure of existing liquid-phase tube is improved to prolong the storage life of cryogenic liquide for reduce transmission of heat as far as possible.
The model utility content
The problem that the utility model exists at prior art, a kind of inside and outside courage joint weld cracking that effectively prevents is provided, layer vacuum avoids destroying, obviously reducing the cryogenic liquid evaporates amount, prolongs the Cryo Heat Insulation pressurized container liquid-phase tube structure that cryogenic liquide is preserved fate and reduced the container maintenance rate.
The utility model is realized by the following technical solutions:
Be provided with between the two ends of this liquid-phase tube and be beneficial to the buffer structure that forms the vapor liquid equilibrium interface.
Described buffer structure is selected from a kind of in bend pipe, bellows and the volute.
The following liquid entering hole e of the cryogenic liquide of described liquid-phase tube is located at the bottom of inner bag.
The inner of described liquid-phase tube is rolled over the bottom that puts in inner bag outward after vertically passing outer courage, vacuum sandwich, extend horizontally to the opposite side of inner bag, outwards bending extends into vacuum sandwich under tiltedly again, the bottom that vertically puts in inner bag through buffer structure again links to each other with following liquid mouth e, and the outer end links to each other with liquid in-out valve V6 by the end of pressurized machine PBV.
The utility model compared with prior art, owing to the structure of liquid-phase tube is extended, moves towards more rationally and set up one between two fixed ends to be beneficial to the buffer structure that forms the gas-liquid phase equilibrium interface outside the tank, have the preservation fate of obvious minimizing cryogenic liquid evaporates loss, prolongation cryogenic liquide simultaneously through evidence; Can also effectively prevent inside and outside courage joint weld cracking, objectively also make the degree of vacuum of vacuum sandwich exempt from destruction, reduce the maintenance expenses of container.
Description of drawings
Fig. 1 is a main TV structure schematic representation of the present utility model.
Fig. 2 is that the utility model is provided with the position schematic representation in low-temperature (low temperature) vessel.
Fig. 3 is the structural representation of traditional liquid-phase tube.
Among the figure: 1. liquid-phase tube, 2. inner bag, 3. gas, 4. gas-liquid interface, 5. outer courage, 6. buffer structure, 7. vacuum sandwich, 8. vacuum pumping device, the last liquid entering hole of a., b. gas phase mouth, the c. level meter is suitable for reading, d. be full of the indication mouth, liquid entering hole under the e., f. level meter end opening, g. drain, V 1, V 4. cryogenic globe valve, V 2, V 3. level meter is gone up valve, V down 5. go up the feed liquor valve, V 6. liquid in-out valve, V 7. pressure charging valve, P. pressure gauge, S. safety valve, L. level meter, PBV. pressurized machine.
Embodiment
Content of the present utility model is described in detail in conjunction with the accompanying drawings by embodiment.
As shown in Figure 1, 2, make the inner bag 2 of Cryo Heat Insulation pressurized container, fill perlites, the associate member of packing in succession, cryogenic globe valve V in outer courage 5, the middle vacuum sandwich 7 by prior art 1Link to each other gas phase mouth b, level meter C suitable for reading, respectively by pipe fitting and corresponding stop valve V separately by the indication mouthful d that is full of on pipe fitting and the inner bag 2 4, drain g, safety valve S, pressure gauge P, valve V on the level meter 3, water level gage L, valve V under the level meter 2F links to each other with the level meter end opening, last feed liquor valve V 5Link to each other with last liquid entering hole a by pipe fitting; The utility model is put in the Cryo Heat Insulation pressurized container, liquid in-out valve V 6End by pressurized machine PBV links to each other with the outer end of liquid-phase tube 1, outer courage 5, the vacuum sandwich 7 outer bottoms that put in inner bag 2 of rolling over are vertically passed in the inner of liquid-phase tube 1, the outer bending of opposite side that level extends to inner bag 2 always vertically puts in inner bag 2 after tiltedly putting in vacuum sandwich 7 in by buffer structure 6 down bottom links to each other with following liquid entering hole e, and the other end of pressurized machine PBV passes through pressure charging valve V 7By cryogenic globe valve V 4G links to each other with drain, and vacuum pumping device 8 is located on the outer courage 5.
Described buffer structure 6 is selected from a kind of in bend pipe, bellows and the volute.
The operating process of the utility model when filling cryogenic liquide and use cryogenic liquide is same as the prior art, just in the process of filling discharging or transporting low temperature liquid, the cryogenic liquide of the pipeline portions that directly contacts with the external world can be vaporized, " heat " gas after the vaporization, pressure increases the trend that enters in the oriented container, but because the utility model is provided with buffer structure, just formed vapor liquid equilibrium interface 4 in the front of buffer structure soon, effectively stoped the gas 3 of vaporization to enter container, and then the cryogenic liquide in the container is vaporized again, avoid the shortcoming of many losses cryogenic liquide, the final prolongation cryogenic liquide of realizing is preserved fate, reduce the purpose of low-temperature (low temperature) vessel maintenance rate.

Claims (4)

1, Cryo Heat Insulation pressurized container liquid-phase tube structure is characterized in that being provided with between the two ends of this liquid-phase tube and is beneficial to the buffer structure (6) that forms vapor liquid equilibrium interface (4).
2, Cryo Heat Insulation pressurized container liquid-phase tube structure according to claim 1 is characterized in that described buffer structure (6) is selected from a kind of in bend pipe, bellows and the volute.
3, Cryo Heat Insulation pressurized container liquid-phase tube structure according to claim 1 is characterized in that the following liquid entering hole e of the cryogenic liquide of described liquid-phase tube is located at the bottom of inner bag (2).
4, according to each described Cryo Heat Insulation pressurized container liquid-phase tube structure among the claim 1-3, outer courage (5), the outer bottom that puts in inner bag (2) of rolling over, vacuum sandwich (7) back are vertically passed in the inner that it is characterized in that described liquid-phase tube, extend horizontally to the opposite side of inner bag (2), outwards bending extends into vacuum sandwich (7) under tiltedly again, the bottom that vertically puts in inner bag (2) through buffer structure (6) again links to each other with following liquid entering hole e, and the outer end links to each other with liquid in-out valve V6 by the end of pressurized machine PBV.
CNU2008202198233U 2008-11-27 2008-11-27 Liquid phase pipe structure of cryogenic insulation pressure vessel Expired - Fee Related CN201306600Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2008202198233U CN201306600Y (en) 2008-11-27 2008-11-27 Liquid phase pipe structure of cryogenic insulation pressure vessel

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2008202198233U CN201306600Y (en) 2008-11-27 2008-11-27 Liquid phase pipe structure of cryogenic insulation pressure vessel

Publications (1)

Publication Number Publication Date
CN201306600Y true CN201306600Y (en) 2009-09-09

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Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2008202198233U Expired - Fee Related CN201306600Y (en) 2008-11-27 2008-11-27 Liquid phase pipe structure of cryogenic insulation pressure vessel

Country Status (1)

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CN (1) CN201306600Y (en)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102980025A (en) * 2012-11-14 2013-03-20 西安轨道交通装备有限责任公司 Low temperature vessel internal pipeline
CN103383063A (en) * 2013-06-09 2013-11-06 苏州华福低温容器有限公司 Gas-seal structure of pressure input pipe of movable type low-temperature pressure vessel
CN108006433A (en) * 2017-12-25 2018-05-08 杭州福斯达深冷装备股份有限公司 A kind of liquefied pot
CN108087718A (en) * 2018-01-12 2018-05-29 江苏深绿新能源科技有限公司 A kind of vertical lossless charging device of bottle heavy caliber

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN102980025A (en) * 2012-11-14 2013-03-20 西安轨道交通装备有限责任公司 Low temperature vessel internal pipeline
CN103383063A (en) * 2013-06-09 2013-11-06 苏州华福低温容器有限公司 Gas-seal structure of pressure input pipe of movable type low-temperature pressure vessel
CN108006433A (en) * 2017-12-25 2018-05-08 杭州福斯达深冷装备股份有限公司 A kind of liquefied pot
CN108006433B (en) * 2017-12-25 2023-09-22 杭州福斯达深冷装备股份有限公司 Liquefied tank
CN108087718A (en) * 2018-01-12 2018-05-29 江苏深绿新能源科技有限公司 A kind of vertical lossless charging device of bottle heavy caliber

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
C17 Cessation of patent right
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20090909

Termination date: 20091228