GB753980A - Improvements in or relating to methods of fractionating gas-mixtures - Google Patents

Improvements in or relating to methods of fractionating gas-mixtures

Info

Publication number
GB753980A
GB753980A GB31930/54A GB3193054A GB753980A GB 753980 A GB753980 A GB 753980A GB 31930/54 A GB31930/54 A GB 31930/54A GB 3193054 A GB3193054 A GB 3193054A GB 753980 A GB753980 A GB 753980A
Authority
GB
United Kingdom
Prior art keywords
nitrogen
column
head
refrigerator
compressor
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
Application number
GB31930/54A
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.)
Koninklijke Philips NV
Original Assignee
Philips Gloeilampenfabrieken NV
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 Philips Gloeilampenfabrieken NV filed Critical Philips Gloeilampenfabrieken NV
Publication of GB753980A publication Critical patent/GB753980A/en
Expired 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
    • 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
    • Y10S62/905Column
    • Y10S62/907Insulation

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)

Abstract

753,980. Cold separation of gas mixtures. NAAMLOOZE VENNOOTSCHAP PHILIPS' GLOEILAMPENFABRIEKEN. Nov. 4, 1954 [Nov. 7, 1953], No. 31930/54. Class 8(2). In a process for separating a gas mixture e.g. air comprising extracting thermal energy from the head of a rectification column 1 operating at substantially atmospheric pressure by means of a medium e.g. nitrogen, compressing said nitrogen in a compressor 3 passing at least part of it through a coil 7 within the boiler 2 thereby supplying energy to the latter and then expanding said nitrogen at a valve 12 prior to feeding it to the column head, thermal energy is extracted from at least part of said nitrogen by a refrigerator 9 of the reversed hot gas engine type such as is described in Specification 695,857 [Group XIII], located between the compressor 3 and the expansion valve 12. As shown the refrigerated and expanded nitrogen is fed directly into the column to serve as reflux and nitrogen from the column head traverses a duct 20 and a heat exchanger 5 which cools incoming air, and part is bled off through a duct 22 whilst the remainder is forced by the compressor 3 back through the exchangers 5, 7 to the refrigerator 9. In a modification a portion of the compressed nitrogen leaving the exchanger 3 by-passes the boiler 2, is liquefied in the refrigerator 9 and the combined streams are then expanded at valve 12 and supplied to the head of the column. In a further modification the energy-extracting nitrogen traverses a closed cycle formed by the provision of a condenser vaporizor 33, Fig. 2 (not shown), in the head of the column ; the refrigerator being located between the compressor and the boiler.
GB31930/54A 1953-11-07 1954-11-04 Improvements in or relating to methods of fractionating gas-mixtures Expired GB753980A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL325973X 1953-11-07

Publications (1)

Publication Number Publication Date
GB753980A true GB753980A (en) 1956-08-01

Family

ID=19784174

Family Applications (1)

Application Number Title Priority Date Filing Date
GB31930/54A Expired GB753980A (en) 1953-11-07 1954-11-04 Improvements in or relating to methods of fractionating gas-mixtures

Country Status (6)

Country Link
US (1) US2820352A (en)
CH (1) CH325973A (en)
DE (1) DE947710C (en)
FR (1) FR1114520A (en)
GB (1) GB753980A (en)
NL (1) NL97466C (en)

Families Citing this family (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3126267A (en) * 1964-03-24 Separating isotopes of hydrogen
US3000188A (en) * 1956-11-15 1961-09-19 Kellogg M W Co Gas separation
NL146599B (en) * 1966-03-02 1975-07-15 Philips Nv DEVICE FOR COOLING OR CONDENSING A MEDIUM.
US4017284A (en) * 1973-05-14 1977-04-12 Cryox Corporation Air distillation apparatus comprising regenerator means for producing oxygen
CH590184A5 (en) * 1974-02-08 1977-07-29 Sulzer Ag

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2284662A (en) * 1936-03-23 1942-06-02 Kahle Heinrich Process for the production of krypton and xenon
DE675347C (en) * 1936-05-10 1939-05-06 C W Paul Heylandt Dr Ing Process for the decomposition of gas mixtures with a low boiling point
US2411711A (en) * 1941-09-22 1946-11-26 Baufre William Lane De Method and apparatus for separating and liquefying gases
US2386297A (en) * 1943-10-07 1945-10-09 Air Reduction Separation of the constituents of gaseous mixtures by liquefaction and rectification
US2423273A (en) * 1943-12-02 1947-07-01 Air Reduction Separation of the constituents of air
US2608070A (en) * 1944-02-11 1952-08-26 Kapitza Peter Leonidovitch Method and means for distillation of low boiling point liquids
US2417279A (en) * 1944-07-22 1947-03-11 Air Reduction Separation of the constituents of gaseous mixtures
US2620637A (en) * 1946-10-09 1952-12-09 Air Prod Inc Air fractionating cycle and apparatus
US2627731A (en) * 1949-06-18 1953-02-10 Hydrocarbon Research Inc Rectification of gaseous mixtures

Also Published As

Publication number Publication date
US2820352A (en) 1958-01-21
NL97466C (en)
DE947710C (en) 1956-08-23
CH325973A (en) 1957-11-30
FR1114520A (en) 1956-04-13

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