US3069863A - Apparatus for evaporating impurities contaminating liquid gas, for example acetylene contaminating liquid oxygen - Google Patents

Apparatus for evaporating impurities contaminating liquid gas, for example acetylene contaminating liquid oxygen Download PDF

Info

Publication number
US3069863A
US3069863A US749440A US74944058A US3069863A US 3069863 A US3069863 A US 3069863A US 749440 A US749440 A US 749440A US 74944058 A US74944058 A US 74944058A US 3069863 A US3069863 A US 3069863A
Authority
US
United States
Prior art keywords
contaminating liquid
acetylene
liquid oxygen
liquid
cone
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 - Lifetime
Application number
US749440A
Other languages
English (en)
Inventor
Dolphin Johannes Hendrikus
Ster Johannes Van Der
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.)
US Philips Corp
North American Philips Co Inc
Original Assignee
US Philips Corp
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 US Philips Corp filed Critical US Philips Corp
Application granted granted Critical
Publication of US3069863A publication Critical patent/US3069863A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B13/00Oxygen; Ozone; Oxides or hydroxides in general
    • C01B13/02Preparation of oxygen
    • C01B13/0229Purification or separation processes
    • C01B13/0248Physical processing only
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D1/00Evaporating
    • B01D1/22Evaporating by bringing a thin layer of the liquid into contact with a heated surface
    • 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
    • F17C9/00Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure
    • F17C9/02Methods or apparatus for discharging liquefied or solidified gases from vessels not under pressure with change of state, e.g. vaporisation
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/08Separating gaseous impurities from gases or gaseous mixtures or from liquefied gases or liquefied gaseous mixtures
    • CCHEMISTRY; METALLURGY
    • C01INORGANIC CHEMISTRY
    • C01BNON-METALLIC ELEMENTS; COMPOUNDS THEREOF; METALLOIDS OR COMPOUNDS THEREOF NOT COVERED BY SUBCLASS C01C
    • C01B2210/00Purification or separation of specific gases
    • C01B2210/0043Impurity removed
    • C01B2210/0068Organic compounds
    • C01B2210/007Hydrocarbons
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25JLIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J2200/00Processes or apparatus using separation by rectification
    • F25J2200/80Processes or apparatus using separation by rectification using integrated mass and heat exchange, i.e. non-adiabatic rectification in a reflux exchanger or dephlegmator
    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10STECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S62/00Refrigeration
    • Y10S62/902Apparatus

Definitions

  • the present invention relates to apparatus for vaporizing impurities contaminating liquid gas, for example acetylene contaminating liquid oxygen, more especially but not exclusively for use in gas-separating systems, comprising a wall which is adapted to be heated and on which a liquid is evaporated.
  • impurities contaminating liquid gas for example acetylene contaminating liquid oxygen
  • acetylene-contaminated liquid oxygen is drawn off from a fractionating column and fed through an atomizer to a separateheater where the liquid is evaporated by hot, gaseous oxygen.
  • oxygen drawn 05 from a fractionating column and, for example, containinated by acetylene is fed in small quantities against a heated, fiat bottom of a vaporizer where it is evaporated by boiling on the plate, above which provision is made of a fairly large space with a narrowed supply duct for the liquid.
  • the present invention has for its object to provide an apparatus of the aforesaid type, without using overpressure for dispersion or a large chamber for boiling on a heated plate, while precluding any accumulation of acetylene.
  • the heatable wall comprises recesses and elevations so as to permit individual and permanently individual drops of the liquid to be evaporated in the recesses or to jump over from one recess to the others.
  • the surface of the heatable wall consists of one or more layers of metal gauze, for example copper gauze. Excellent results are obtained when connecting, for example, three layers of gauze offset through an angle of, say, 45 relative to one another, by sintering or soldering to a massive metal, for example copper, substratum.
  • the vaporization surface according to the invention preferably constitutes entirely or partially the outer surface of a body having an outer surface converging towards the highest point, for example a cone or a ball cap.
  • a cone When using a cone, its vertical angle may have a value of the order of 120.
  • the body near its highest point co-acts with a distributor adapted for supplying liquid and having an upwardly converging outer surface, for example a conical surface or that of a ball cap, and which further meets at or near its highest point with a liquid supply duct projecting downwardly and comprising overhanging parts, for example teeth, at its lower edge.
  • a distributor adapted for supplying liquid and having an upwardly converging outer surface, for example a conical surface or that of a ball cap, and which further meets at or near its highest point with a liquid supply duct projecting downwardly and comprising overhanging parts, for example teeth, at its lower edge.
  • the liquid supply for example from the distributor referred to, is directed towards a body having a smooth surface and so shaped, for example as a cone, that any liquid supplied to it is accelerated in flowing off, the stream of drops flowing ofi being directed towards the surface of the heatable wall provided with recesses and elevations.
  • Liquid oxygen for example contaminated by acetylene, is passed through an aperture 1 of a mouth piece 2 in the direction of arrows p to a distributor 3 in the form of a cone provided with overhangs 4 at its lower edge 5.
  • This cone has a strong distributing effect without any overpressure. Drops accumulate from the projections 4 and fall on the smooth outer surface of a cone 6. The drops are accelerated along the surface of the cone is and jump over to the heated conical gauze surface 7. Its temperature amounts to C. to C.
  • Such apparatus may, for example, be used at the bottom end of gas-fractionating columns.
  • An apparatus for evaporating impurities such as acetylene from liquid oxygen in a gas fractionating column comprising means for dispensing liquid oxygen, coneshaped wall forming an angle of and positioned beneath the outlet for said dispensing means, said liquid oxygen being adapted to flow over said cone-shaped wall, a chamber located adiacent to said cone-shaped Wall and in open communication therewith, an opening in said chamber to the atmosphere, means for heating said coneshaped Wall, the latter being constituted of a metal gauze whereby the Leydenfrost phenomenon occurs and all liquid thereon is evaporated and the acetylene gas therein is discharged to the atmosphere through the opening in said chamber, a smooth, cone-shaped element connecting opposite faces of said cone-shaped wall, and a conical distribution plate positioned on said cone-shaped element with its apex directly underneath the outlet of said dispensing means, the base of said conical distribution plate overhanging said cone-shaped element.
  • An apparatus for evaporating impurities such as acetylene from liquid oxygen in a fractionating column comprising means for dispensing liquid oxygen, a sloping wall beneath the outlet of said dispensing means and over which said liquid oxygen flows, a chamber located adjacent to said sloping Wall and in open communication therewith, an opening in the chamber to the atmosphere, means for heating said sloping W211, the latter being a metai gauze constituted of a metal oxide material whereby the Leydenfrost phenomenon occurs and all liquid thereon is evaporated and the acetylene gas therein is discharged to the atmosphere through tie opening in said chamber.

Landscapes

  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Organic Chemistry (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Analytical Chemistry (AREA)
  • Inorganic Chemistry (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Filling Or Discharging Of Gas Storage Vessels (AREA)
US749440A 1957-07-24 1958-07-18 Apparatus for evaporating impurities contaminating liquid gas, for example acetylene contaminating liquid oxygen Expired - Lifetime US3069863A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL219304 1957-07-24

Publications (1)

Publication Number Publication Date
US3069863A true US3069863A (en) 1962-12-25

Family

ID=19750939

Family Applications (1)

Application Number Title Priority Date Filing Date
US749440A Expired - Lifetime US3069863A (en) 1957-07-24 1958-07-18 Apparatus for evaporating impurities contaminating liquid gas, for example acetylene contaminating liquid oxygen

Country Status (7)

Country Link
US (1) US3069863A (tr)
BE (1) BE569679A (tr)
CH (1) CH368817A (tr)
DE (1) DE1070658B (tr)
FR (1) FR1211465A (tr)
GB (1) GB885394A (tr)
NL (2) NL97483C (tr)

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4438729A (en) * 1980-03-31 1984-03-27 Halliburton Company Flameless nitrogen skid unit
US5246541A (en) * 1991-05-14 1993-09-21 A. Ahlstrom Corporation Evaporator for liquid solutions
US8945281B1 (en) * 2014-01-30 2015-02-03 Msp Corporation Method and apparatus for vapor generation and wafer cleaning
EP3733938A4 (en) * 2018-08-21 2021-04-14 Lg Chem, Ltd. DISPERSING DEVICES AND DE-FOAMING DEVICES EQUIPPED WITH THE SAID DEVICE

Families Citing this family (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108753460B (zh) * 2018-05-07 2021-12-07 扬州工业职业技术学院 一种脱除挥发性组分的装置

Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US723098A (en) * 1901-01-29 1903-03-17 Globe Iron Works Cooling-tank for internal-combustion engines.
US1051661A (en) * 1912-07-31 1913-01-28 William Anderson Air-cooler.
US1516187A (en) * 1920-08-30 1924-11-18 Standard Oil Co Gas-absorbing apparatus
US1849496A (en) * 1926-10-07 1932-03-15 Magnus Hans Apparatus for vacuum dehydration of hydrocarbons
US1963841A (en) * 1931-07-24 1934-06-19 American Oxythermic Corp Cocurrent evaporator with counter-current condensation for fractional liquefaction
US2773555A (en) * 1954-12-21 1956-12-11 American Viscose Corp Deaerators

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US723098A (en) * 1901-01-29 1903-03-17 Globe Iron Works Cooling-tank for internal-combustion engines.
US1051661A (en) * 1912-07-31 1913-01-28 William Anderson Air-cooler.
US1516187A (en) * 1920-08-30 1924-11-18 Standard Oil Co Gas-absorbing apparatus
US1849496A (en) * 1926-10-07 1932-03-15 Magnus Hans Apparatus for vacuum dehydration of hydrocarbons
US1963841A (en) * 1931-07-24 1934-06-19 American Oxythermic Corp Cocurrent evaporator with counter-current condensation for fractional liquefaction
US2773555A (en) * 1954-12-21 1956-12-11 American Viscose Corp Deaerators

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4438729A (en) * 1980-03-31 1984-03-27 Halliburton Company Flameless nitrogen skid unit
US5551242A (en) * 1980-03-31 1996-09-03 Halliburton Company Flameless nitrogen skid unit
US5246541A (en) * 1991-05-14 1993-09-21 A. Ahlstrom Corporation Evaporator for liquid solutions
US8945281B1 (en) * 2014-01-30 2015-02-03 Msp Corporation Method and apparatus for vapor generation and wafer cleaning
EP3733938A4 (en) * 2018-08-21 2021-04-14 Lg Chem, Ltd. DISPERSING DEVICES AND DE-FOAMING DEVICES EQUIPPED WITH THE SAID DEVICE

Also Published As

Publication number Publication date
NL219304A (tr)
FR1211465A (fr) 1960-03-16
NL97483C (tr)
DE1070658B (de) 1959-12-10
GB885394A (en) 1961-12-28
CH368817A (de) 1963-04-30
BE569679A (tr)

Similar Documents

Publication Publication Date Title
US20210054504A1 (en) Film-forming material mixed-gas forming device and film forming device
JP6133954B2 (ja) ガスと蒸発材料との接触を促進するのを助ける方法及び装置
US5862605A (en) Vaporizer apparatus
US3907683A (en) Multitubular constant head reflux condenser
US5835677A (en) Liquid vaporizer system and method
CN101285178B (zh) 汽化器和半导体处理系统
US3069863A (en) Apparatus for evaporating impurities contaminating liquid gas, for example acetylene contaminating liquid oxygen
KR101039163B1 (ko) 반도체 처리 시스템 및 기화기
CN101476115A (zh) 蒸发器输送安瓿
US2519618A (en) Evaporator and fluid contact apparatus
WO2001036707A1 (en) Apparatus and method for delivery of precursor vapor from low vapor pressure liquid sources to a cvd chamber
US2612440A (en) Production of metal carbonyl powders of small size
US2562153A (en) Vacuum distillation
US2881067A (en) Method of producing powder metals
JP6000961B2 (ja) 石油の炭化水素蒸留物の収量を改善するための蒸留塔およびその蒸留物を供給する方法
WO2016062514A1 (de) Temperierte gaszuleitung mit an mehreren stellen eingespeisten verdünnungsgasströmen
US235521A (en) Edward fox
US2872167A (en) Ether volatilizer
JPH05214537A (ja) 固体昇華用の気化器
NO148867B (no) Anordning for aa frembringe amplitudemodulerte ultralydsendepulser
US3094395A (en) Method for evaporating subliming materials
JPH0671551B2 (ja) 定量気化供給装置
US3260235A (en) Apparatus for coating material with metal
US6572707B1 (en) Vaporizer for sensitive precursors
JPH0331477A (ja) Cvd装置用バブラー