CN108061245A - Use the gas displacement method and device of intermediary's gas - Google Patents

Use the gas displacement method and device of intermediary's gas Download PDF

Info

Publication number
CN108061245A
CN108061245A CN201711370771.XA CN201711370771A CN108061245A CN 108061245 A CN108061245 A CN 108061245A CN 201711370771 A CN201711370771 A CN 201711370771A CN 108061245 A CN108061245 A CN 108061245A
Authority
CN
China
Prior art keywords
gas
container
intermediary
density
degassing method
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
CN201711370771.XA
Other languages
Chinese (zh)
Inventor
殷敏鸿
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.)
Changsha Dark Blue Future Intelligent Technology Co Ltd
Original Assignee
Changsha Dark Blue Future Intelligent Technology Co Ltd
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 Changsha Dark Blue Future Intelligent Technology Co Ltd filed Critical Changsha Dark Blue Future Intelligent Technology Co Ltd
Priority to CN201711370771.XA priority Critical patent/CN108061245A/en
Publication of CN108061245A publication Critical patent/CN108061245A/en
Pending legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C13/00Details of vessels or of the filling or discharging of vessels
    • F17C13/02Special adaptations of indicating, measuring, or monitoring equipment
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F17STORING OR DISTRIBUTING GASES OR LIQUIDS
    • F17CVESSELS 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
    • F17C13/00Details of vessels or of the filling or discharging of vessels
    • F17C13/04Arrangement or mounting of valves

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)

Abstract

Two kinds of gases of the small A gas of density difference and B gas easily mix, it is difficult to realize gas displacement, can use intermediary gas of the C gas larger with both gas density difference as replacement process, be carried out in two steps.If C gas is bigger than A gas and B air tightnesses, the first step uses upward degassing method, C gas enters from container bottom opening, A gas from container open top is squeezed away, the A gas in container is made to be replaced as C gas, second step uses downward degassing method, B gas enters from container open top, C gas from container open top is squeezed away, the C gas in container is made to be replaced as B gas, realizes the gas displacement in container;If C gas is smaller than A gas and B air tightnesses, the first step uses downward degassing method, and second step uses upward degassing method.

Description

Use the gas displacement method and device of intermediary's gas
Technical field
Gas displacement method and device.
Background technology
The gas in container or confined space is replaced, another gas is substituted with a kind of gas, upward degassing method can be used Or downward degassing method, it but needs the density contrast of two kinds of gases larger, is just not easy to mix, it is big that the small gas of density floats over density On gas, layering and gas displacement are realized.If the density difference of two kinds of gases is small, gaseous mixture, replacement result are easily become Difference can not replace.
In this case the fluid-discharge therapies substitution gas such as draining can be used, but cost is higher, can be mixed in gas a large amount of Liquid vapour reduces gas purity, also needs to remove liquid vapour again after displacement.
The content of the invention
It is easily mixed to solve two kinds of small gases of density difference, it is difficult to which the problem of realizing gas displacement, the present invention use Following scheme:The density of two kinds of gases or gaseous mixture if necessary to displacement is larger, using the smaller gas of density as intermediary Gas;If the density of two kinds of gases or gaseous mixture is smaller, the gas larger using density is as intermediary's gas.
Using the C gas larger with both gas density difference as intermediary's gas of replacement process, it is carried out in two steps.If C gas is bigger than A gas and B air tightnesses, the first step, and using upward degassing method, C gas enters from container bottom opening, by A gas from vessel top Portion's opening is squeezed away, and the A gas in container is made to be replaced as C gas, second step, and using downward degassing method, B gas is from container open top Into C gas from container open top is squeezed away, the C gas in container is made to be replaced as B gas, realizes the gas displacement in container.
If C gas is smaller than A gas and B air tightnesses, the first step uses downward degassing method, and second step uses upward degassing method.
Intermediary's gas is preferably not flammable explosive gas, can not be chemically reacted with two kinds of gases for needing to replace. Intermediary's gas density and two kinds of gas density difference for needing to replace are about small, and replacement result is better.
Requirement to substitution gas container:There are valve in top and bottom, as air inlet/outlet.
Exhaust outlet will have concentration detection apparatus.
Intermediary's gas concentration unit can be installed in drain tap position.
During operation, by valve regulated, gas outlet diameter is than air inlet diameter bigger.
Specific embodiment
Exemplified by the air in container is replaced with pure nitrogen gas.Air is gaseous mixture, wherein 78% is nitrogen, in equal air pressure Under, atmospheric density and nitrogen difference very little can not use upward degassing method or downward degassing method to realize displacement.It can use at this time Density ratio nitrogen and the much smaller hydrogen of air or helium realize gas displacement as intermediary's gas, if using hydrogen, to have The condition of burn-proof and explosion prevention.
The top of gas container and bottom end opening, equipped with valve, at top, valve is connected by tracheae with hydrogen cylinder, bottom Valve is equipped with density of hydrogen detection device.
Bottom valve is opened, valve is slowly injected into hydrogen in container from top, since hydrogen density is smaller than air, can float On air, air pressure caused by gas transmission slowly makes air be discharged from bottom valve, until bottom valve doorway detects that hydrogen is dense When degree reaches a hundred percent, bottom valve is first closed, closes top valve afterwards, at this time density of hydrogen a hundred percent in container.
Then, bottom valve connects nitrogen cylinder, top valve connection nitrogen gas concn detection device and Hydrogen collection device, beats Top valve is opened, then nitrogen is injected in container from bottom valve, density of nitrogen is smaller than hydrogen, can be deposited on container bottom, defeated Air pressure caused by gas slowly makes hydrogen be discharged from top valve, is collected by Hydrogen collection device, treats that top valve port detects nitrogen When gas concentration reaches a hundred percent, top valve is first closed, turns off bottom valve, nitrogen gas concn is percent in container at this time Hundred, realize the purpose that the air in container is replaced as to nitrogen completely.

Claims (2)

1. using the gas displacement method and device of intermediary's gas, it is characterized in that:If necessary to two kinds of gases of displacement or mixing The density of gas is larger, using the smaller gas of density as intermediary's gas;If the density of two kinds of gases or gaseous mixture is smaller, use The larger gas of density is as intermediary's gas;
Using the C gas larger with both gas density difference as intermediary's gas of replacement process, it is carried out in two steps.If C gas Bigger than A gas and B air tightnesses, the first step, using upward degassing method, C gas enters from container bottom opening, by A gas from container top Opening is squeezed away, and the A gas in container is made to be replaced as C gas, second step, using downward degassing method, B gas from container open top into Enter, C gas is squeezed away from container open top, the C gas in container is made to be replaced as B gas, realize the gas displacement in container;If C gas is smaller than A gas and B air tightnesses, and the first step uses downward degassing method, and second step uses upward degassing method;
Intermediary's gas is preferably not flammable explosive gas, can not be chemically reacted with two kinds of gases for needing to replace, intermediary Gas density and two kinds of gas density difference for needing to replace are about small, and replacement result is better.
2. using the gas displacement method and device of intermediary's gas, it is characterized in that:There are valve in substitution gas container head and bottom, As air inlet/outlet, exhaust outlet has concentration detection apparatus, can install intermediary's gas concentration unit in drain tap position.
CN201711370771.XA 2017-11-30 2017-11-30 Use the gas displacement method and device of intermediary's gas Pending CN108061245A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201711370771.XA CN108061245A (en) 2017-11-30 2017-11-30 Use the gas displacement method and device of intermediary's gas

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201711370771.XA CN108061245A (en) 2017-11-30 2017-11-30 Use the gas displacement method and device of intermediary's gas

Publications (1)

Publication Number Publication Date
CN108061245A true CN108061245A (en) 2018-05-22

Family

ID=62139157

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201711370771.XA Pending CN108061245A (en) 2017-11-30 2017-11-30 Use the gas displacement method and device of intermediary's gas

Country Status (1)

Country Link
CN (1) CN108061245A (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113267423A (en) * 2021-06-21 2021-08-17 贵州茅台酒股份有限公司 Cabin body simulation device and gas introduction and gas detection method

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1157931A1 (en) * 2000-05-20 2001-11-28 Harcostar Drums Limited Method and apparatus for gassing of containers
CN1890152A (en) * 2003-12-22 2007-01-03 三得利株式会社 Gas exchange device and gas exchange method
CN102292265A (en) * 2009-01-28 2011-12-21 东洋制罐株式会社 Method for gas replacement of container and apparatus therefor
CN102917954A (en) * 2010-06-07 2013-02-06 大日本印刷株式会社 Filling method, filling system and bottle
CN206050178U (en) * 2016-08-31 2017-03-29 天津森罗科技股份有限公司 A kind of fast pump nitrogen charging device for historical relic's protection

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
EP1157931A1 (en) * 2000-05-20 2001-11-28 Harcostar Drums Limited Method and apparatus for gassing of containers
CN1890152A (en) * 2003-12-22 2007-01-03 三得利株式会社 Gas exchange device and gas exchange method
CN100455485C (en) * 2003-12-22 2009-01-28 三得利株式会社 Gas exchange device and gas exchange method
CN102292265A (en) * 2009-01-28 2011-12-21 东洋制罐株式会社 Method for gas replacement of container and apparatus therefor
CN102917954A (en) * 2010-06-07 2013-02-06 大日本印刷株式会社 Filling method, filling system and bottle
CN206050178U (en) * 2016-08-31 2017-03-29 天津森罗科技股份有限公司 A kind of fast pump nitrogen charging device for historical relic's protection

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113267423A (en) * 2021-06-21 2021-08-17 贵州茅台酒股份有限公司 Cabin body simulation device and gas introduction and gas detection method

Similar Documents

Publication Publication Date Title
US11492278B2 (en) Dynamic produced water treatment apparatus and system
CA2762786C (en) Tank with containment chamber and gas scrubber
NZ547691A (en) Concrete reclamation apparatus utilizing two connected containers, the first of which has a strainer
NO20080881L (en) Process and apparatus for separating liquids emulsified in mixtures of liquids and gases dissolved in mixtures of liquids and gases by localized pressure reduction
CN108061245A (en) Use the gas displacement method and device of intermediary's gas
CN107789956A (en) It is a kind of to realize internal floating roof tank interbedded gas VOCs zero-emissions, remove oxygen and recycle the device of nitrogen
US20070092438A1 (en) Process and Apparatus for Producing a Gas from Hydrates
CN206032279U (en) Vault storage tank vapor recovery system device
CN106190387A (en) A kind of novel oilfield associated gas denitrification equipment and technique
US8702853B2 (en) Tank with containment chamber and gas scrubber
RU56207U1 (en) INSTALLING OIL CLEANING (OPTIONS)
CN107529446A (en) Can be from the Vacuum gas-liquid separator of discharge opeing
RU2309002C2 (en) Oil refining installation (versions)
CN204162411U (en) Dry hydrogen production equipment
EP3958922A1 (en) Dynamic produced water treatment apparatus and system with oxygen recovery
CN101066754B (en) SF6 gas recovering and purifying process and tank
CN210166178U (en) Reaction kettle vacuum sampling device
CN208275372U (en) A kind of feedstock device applied in heavy oil catalytic cracking reaction
CN205973778U (en) Discharging equipment is changed to raffinate for gas synthesis
KR101180112B1 (en) Manufacturing method for eliminating water of oil filtering by adding metal hydride and apparatus thereof
US7628966B1 (en) Method for scrubbing natural gas
US120349A (en) Improvement in refining hydrocarbon oils
JP5557535B2 (en) Acetylene production apparatus and production method
CN219259624U (en) Alkylation device hydrocarbon-containing wastewater treatment equipment
CN213420643U (en) Gas recovery and storage isolating device for analyzing toxic and harmful gases

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
WD01 Invention patent application deemed withdrawn after publication
WD01 Invention patent application deemed withdrawn after publication

Application publication date: 20180522