US1717540A - Process for preventing explosions in liquid-air apparatus - Google Patents

Process for preventing explosions in liquid-air apparatus Download PDF

Info

Publication number
US1717540A
US1717540A US164370A US16437027A US1717540A US 1717540 A US1717540 A US 1717540A US 164370 A US164370 A US 164370A US 16437027 A US16437027 A US 16437027A US 1717540 A US1717540 A US 1717540A
Authority
US
United States
Prior art keywords
air
liquid
explosions
air apparatus
preventing explosions
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
US164370A
Inventor
Aubert Robert Gerard
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.)
Individual
Original Assignee
Individual
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 Individual filed Critical Individual
Application granted granted Critical
Publication of US1717540A publication Critical patent/US1717540A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Classifications

    • 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
    • F25J3/02Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream
    • F25J3/04Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification by rectification, i.e. by continuous interchange of heat and material between a vapour stream and a liquid stream for air
    • F25J3/04151Purification and (pre-)cooling of the feed air; recuperative heat-exchange with product streams
    • F25J3/04242Cold end purification of the feed air
    • 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
    • F25J2205/00Processes or apparatus using other separation and/or other processing means
    • F25J2205/20Processes or apparatus using other separation and/or other processing means using solidification of components
    • 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
    • F25J2205/00Processes or apparatus using other separation and/or other processing means
    • F25J2205/84Processes or apparatus using other separation and/or other processing means using filter
    • 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
    • F25J2220/00Processes or apparatus involving steps for the removal of impurities
    • F25J2220/40Separating high boiling, i.e. less volatile components from air, e.g. CO2, hydrocarbons

Definitions

  • Said combustible gases collect in the vaporizer, forming explosive mixtures; and therefore explosions are liable to occur when these mixtures are brought into contact with the air in the oxygen zone of the separating apparatus.
  • the process which is the subject of the present invention, is based upon the fact that certain combustible gases become solid at low temperatures at which air still remains liquid.
  • certain combustible gases become solid at low temperatures at which air still remains liquid.
  • acetylene becomes solid at '81.5 C. whilst air remains liquid at lower degrees of temperature.
  • the com- 5 bustible gases therein such as acetylene, (if any there be) are permitted to remain until the liquefaction of the air takes place, and until the acetylene is brought to a solid state at a temperature at which the air yet remains liquid; and the solidified gases are then separated (which can readily be done as by-filtration) before the mass comes into the oxygen zone of the apparatus.
  • a process for preventing explosions in apparatus wherein oxygen and nitrogen are separately obtained in different zones by distillation of liquid air which process consists in subjecting a volume of air containing an admixture of combustible gases such as acetylene to a temperature sufiiciently low to cause liquefaction of the air and solidification of said combustible gases, and separating the solidified combustible substances from the liquid air by filtration at the point in the system where the temperature is lowest, before the liquid air reaches the oxygen 7 zone of said apparatus.

Landscapes

  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Separation By Low-Temperature Treatments (AREA)

Description

UNITED STATES.
PATENT OFFICE.
ROBERT GERARD AUBERT, F PARIS, FRANCE.
PROCESS FOR PREVENTING EXPLOSIONS IN LIQwD-AIR APPARATUS.
No Drawing. Application filed January 28, 1927, Serial No. 164,370, and in Germany August 15, 1925. y
In the commercial production of ex gen and nitrogen by the decomposition of liquid air, explosions sometimes occur inside the liquefying apparatus; and it has been ascertained, after much investigation, that such explosions are due to the presence in the air of combustible gases, principally acetylene. 'The said Combustible gases may be already contained in small quantities in the atmospheric air taken into the liquefying apparatus, or they may be formed by decomposition of lubricating oil in the air-compressor, the gaseous products thus entering into admixture with the air.
Said combustible gases collect in the vaporizer, forming explosive mixtures; and therefore explosions are liable to occur when these mixtures are brought into contact with the air in the oxygen zone of the separating apparatus.
With a view to preventing these damaging explosions, it has been proposed to take in the air in a condition as near as possible to absolute purity, by the use of high fines or air-ducts, reaching up to levels where impurities would be at a negligible minimum. But obviously this remedy is not everywhere possible of application; and particularly it is unavailable in industrial localities, since the air in such places is never pure. Moreover, even if atmospheric air could be always obtained chemically pure, it might 'become admixed with combustible gases generated, as already stated, from the lubricant used in the compressor.
The process, which is the subject of the present invention, is based upon the fact that certain combustible gases become solid at low temperatures at which air still remains liquid. Thus for example, acetylene becomes solid at '81.5 C. whilst air remains liquid at lower degrees of temperature.
Instead, therefore, of attempting to purify the air before it is liquefied, the com- 5 bustible gases therein, such as acetylene, (if any there be) are permitted to remain until the liquefaction of the air takes place, and until the acetylene is brought to a solid state at a temperature at which the air yet remains liquid; and the solidified gases are then separated (which can readily be done as by-filtration) before the mass comes into the oxygen zone of the apparatus.
This is, as is well known, the coldest part of the system; and by locating the filtering apparatus at that point it is possible to effect in a practical and successful manner the removal of the combustible gases, while in a solid state, from the liquid air before the separation of the oxygen from the nitrogen.
What is claimed is:
A process for preventing explosions in apparatus wherein oxygen and nitrogen are separately obtained in different zones by distillation of liquid air, which process consists in subjecting a volume of air containing an admixture of combustible gases such as acetylene to a temperature sufiiciently low to cause liquefaction of the air and solidification of said combustible gases, and separating the solidified combustible substances from the liquid air by filtration at the point in the system where the temperature is lowest, before the liquid air reaches the oxygen 7 zone of said apparatus.
In testimony whereof I have afiixed my signature.
ROBERT GERARD AUBERT.
US164370A 1925-08-15 1927-01-28 Process for preventing explosions in liquid-air apparatus Expired - Lifetime US1717540A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
DE1717540X 1925-08-15

Publications (1)

Publication Number Publication Date
US1717540A true US1717540A (en) 1929-06-18

Family

ID=7740449

Family Applications (1)

Application Number Title Priority Date Filing Date
US164370A Expired - Lifetime US1717540A (en) 1925-08-15 1927-01-28 Process for preventing explosions in liquid-air apparatus

Country Status (1)

Country Link
US (1) US1717540A (en)

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2626510A (en) * 1947-06-18 1953-01-27 Air Prod Inc Air fractionating cycle and apparatus
US2650482A (en) * 1948-04-29 1953-09-01 Kellogg M W Co Method of separating gas mixtures
US3124443A (en) * 1960-05-17 1964-03-10 Gas fractionating system
US5540058A (en) * 1994-12-05 1996-07-30 Rockwell International Corp. Contaminant removal system for purifying air
US6490883B2 (en) * 2000-06-20 2002-12-10 Air Products And Chemicals, Inc. Process and apparatus for removal of volatile compounds from process gases

Cited By (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2626510A (en) * 1947-06-18 1953-01-27 Air Prod Inc Air fractionating cycle and apparatus
US2650482A (en) * 1948-04-29 1953-09-01 Kellogg M W Co Method of separating gas mixtures
US3124443A (en) * 1960-05-17 1964-03-10 Gas fractionating system
US5540058A (en) * 1994-12-05 1996-07-30 Rockwell International Corp. Contaminant removal system for purifying air
US6490883B2 (en) * 2000-06-20 2002-12-10 Air Products And Chemicals, Inc. Process and apparatus for removal of volatile compounds from process gases

Similar Documents

Publication Publication Date Title
US2060940A (en) Process for obtaining krypton and xenon
US1717540A (en) Process for preventing explosions in liquid-air apparatus
US2901326A (en) Separation of hydrogen sulfide and methane
GB841374A (en) Purification of saline water by crystallization with a volatile refrigerant
GB392214A (en) Improvements in or relating to the manufacture of carbon dioxide
GB703209A (en) Improvements in ozone stabilization
US2144692A (en) Process for the separation of gaseous mixtures
US1906917A (en) Process of separation of mixtures of the rare gases
RU2573083C2 (en) Method for obtaining pure helium fraction
US3037337A (en) Purification of boron trichloride
US3031268A (en) Process of purifying silane
US3292382A (en) Low temperature separation of h2s from hydrocarbon gas
US2390899A (en) Gas processing
US1794377A (en) Separation of gases
US2195870A (en) Recovery of sulphur
US3063218A (en) Chlorine dioxide separation
US1611359A (en) Synthetic production of ammonia
US3043665A (en) Purification of boron trichloride
US3033653A (en) Preparation of carbon-free phosphorus
FR2317610A1 (en) Gas condensn. plant with oil separator - and equipment for recycling oil-contaminated condensate to the compressor
US2351390A (en) Process of preparing carbon tetrafluoride
IT1037653B (en) PROCEDURE FOR THE SEPARATION OF AIR AT LOW TEMPERATURES
ES349892A1 (en) Process for the distillative separation of pure chlorine from a gas mixture containing chlorine,nitrogen dioxide,nitrosyl chloride and oxygen
US1521708A (en) Asssgnc r
GB235129A (en) Improvements in or relating to the manufacture of hydrogen by the partial liquefaction of gaseous mixtures containing the same