US2899381A - Cornelius otto jonkers - Google Patents

Cornelius otto jonkers Download PDF

Info

Publication number
US2899381A
US2899381A US2899381DA US2899381A US 2899381 A US2899381 A US 2899381A US 2899381D A US2899381D A US 2899381DA US 2899381 A US2899381 A US 2899381A
Authority
US
United States
Prior art keywords
extensions
heat exchanger
apertures
distance
support
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
Other languages
English (en)
Publication date
Application granted granted Critical
Publication of US2899381A publication Critical patent/US2899381A/en
Anticipated expiration legal-status Critical
Expired - Lifetime legal-status Critical Current

Links

Images

Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25J—LIQUEFACTION, SOLIDIFICATION OR SEPARATION OF GASES OR GASEOUS OR LIQUEFIED GASEOUS MIXTURES BY PRESSURE AND COLD TREATMENT OR BY BRINGING THEM INTO THE SUPERCRITICAL STATE
    • F25J3/00—Processes or apparatus for separating the constituents of gaseous or liquefied gaseous mixtures involving the use of liquefaction or solidification
    • F25J3/08—Separating gaseous impurities from gases or gaseous mixtures or from liquefied gases or liquefied gaseous mixtures
    • C—CHEMISTRY; METALLURGY
    • C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
    • C09D—COATING COMPOSITIONS, e.g. PAINTS, VARNISHES OR LACQUERS; FILLING PASTES; CHEMICAL PAINT OR INK REMOVERS; INKS; CORRECTING FLUIDS; WOODSTAINS; PASTES OR SOLIDS FOR COLOURING OR PRINTING; USE OF MATERIALS THEREFOR
    • C09D191/00—Coating compositions based on oils, fats or waxes; Coating compositions based on derivatives thereof
    • C09D191/005—Drying oils
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
    • F25B—REFRIGERATION MACHINES, PLANTS OR SYSTEMS; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS
    • F25B9/00—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point
    • F25B9/14—Compression machines, plants or systems, in which the refrigerant is air or other gas of low boiling point characterised by the cycle used, e.g. Stirling cycle

Definitions

  • the admixtures for example water 'vapour and carbon dioxide, contained in the gaseous mixture may give rise to difiiculties owing to the dep osition of ice. It is therefore desirable to conduct away these admixtures, which may be carried out in a heat exchanger.
  • the medium containing a plurality of components is cooled and one or more components are separated out of the medium.
  • the heat exchanger comprises a support extending from the hot side of the heat exchanger, to which the medium is fed, to the cold side thereof, where this medium is conducted away: the support is provided with a plurality of at least substantially parallel, plate-shaped extensions, lying one behind the other in the direction of length of the support, and being in thermal contact with the medium, the extensions being surrounded by a wall in a manner such that from the hot side of the heat exchanger to the cold side thereof a plurality of spaces is formed, which communicate with one another through apertures in the extensions.
  • the heat exchanger in a manner such that the heat transferred by the medium to the extensions is conducted away for at least 20% by thermal conductivity by way of the support to the cold side of the heat exchanger, whilst the component(s) to be separated out is (are) deposited on at least a few of these extensions, the mean temperature of each of which is, owing to a suitable choice of the component parts of the heat exchanger, at the most 20, preferably not more than lower than that of the next following extension, the mean temperature of the extension at which the separation starts being, in normal operation of the heat exchanger, at the most 20 C. preferably not more than 10 C. lower than the point of separation of the component(s) concerned as it (they) is (are) fed to that extension.
  • the production of fine snow in the gaseous mixture may be reduced or even completely prevented before this mixture is in contact with the extensions. If the fine ice particles are produced in the gaseous mixture, they will Patented Aug. 11, 1959 not adhere to the extensions, so that they are not captured and the cooled gaseous mixture is not purified.
  • the invention has for its object to construct the heat exchanger in a manner such that, its dimensions being the same, the heat exchanger can contain a larger quantity of ice than that of known construction, so that the period during which the heat exchanger can fulfill its operation is increased.
  • the apertures in the plateshaped extensions are provided in a manner such that each aperture lies between two solid portions of two in a manner such that the distance between such a portion and a solid portion of an extension on the cold side exceeds the distance between this portion and a solid portion of an extension on the hot side.
  • the solid portions of the extensions on the cold side of the apertures of other extensions are deformed in a manner such that the distance between the solid portion opposite the aperture and the edge of the aperture is increased.
  • both the portions of the extensions round about the apertures and the solid portions may be deformed.
  • the distance between the edge of an aperture and the solid portion of the extension on the cold side is at the most ten times, preferably five times larger than the distance between the edge of the aperture and the solid portion of the extension on the hot side.
  • Fig. l is a partial side elevation view of device embodying the invention and a partial sectional view thereof taken along the lines II of Fig. 2.
  • Fig. 2 is a horizontal sectional view of the present device taken along the line IIII of Fig. 1,
  • Fig. 3 is another modification of the device constructed in accordance with the invention being partially a side elevational view and partially a sectional view thereof taken along the lines III-III of Fig. 4 and Fig. 4 is a horizontal sectional View taken along IVIV of Fig. 3.
  • the heat exchanger shown in these figures comprises a support 1, which is secured to a head 2 of a cold-gas refrigerator:
  • the cold-gas refrigerator is not shown in the figure.
  • the support has plate-shaped extensions 3, extending transversely to the support and lying one behind the other, viewed in the direction of length of the support. These extensions have apertures 4, so that in the heat exchanger a plurality of spaces 5 are formed, which communicate openly with one another.
  • the extensions are surrounded by a wall 6 of heat-insulating material, which, in turn, is surrounded by a second wall 7.
  • the medium to be cooled from which one or more components are to be separated is fed through a duct 8 to an annular space 9 between the walls 6 and 7, after which it is conducted to the top side of the heat exchanger.
  • the extensions 3 are provided with deformations 10, which are provided roundabout the apertures 4 and are located so that the distance 11 between the edge of the aperture and the solid portion of the extension on the cold side exceeds the distance 12 between this edge and the solid portion of the extension on the hot side.
  • the distance 11 is at the most ten times the distance 12, it is preferably however five times this distance. If the aforesaid ratio were exceeded there is a risk of excessive local velocities of the gas.
  • the medium After the medium has been purified, it may be further cooled at vanes 13 of the head of the refrigerator, the medium may thus condense.
  • the condensate produced can be conducted away through a duct 14. To this end this duct has a goose neck 15.
  • Figs. 3 and 4 show one embodiment, in which the portions of the extensions roundabout the apertures are not deformed but the solid portions are deformed.
  • Fig. 3 is a vertical sectional view taken on the line III-III of Fig. 4 and
  • Fig. 4 is a horizontal sectional view taken on the line IVIV of Fig. 3. Parts corresponding to those shown in Figs. 1 and 2 are designated by the same reference numerals.
  • the gaseous mixture is fed through the duct 8 and it flows through the annular duct 9 to the extensions 3, which are provided with apertures 4.
  • the solid portions 16 of these extensions which are on the cold side opposite the apertures are deformed.
  • the distance 11 exceeds the distance 12.
  • a heat exchanger for a cold gas refrigerator containing a medium in which a plurality of components side thereof after traversing all of said extensions successively; an insulating wall surrounding said extensions; the location of said apertures being staggeredin successive extensions and having material surrounding each of said apertures of such a form that the distance between said material surrounding said aperture and the adjacent extension on the cold side thereof exceeds the distance between said material surrounding said aperture and the adjacent extension on the hot side thereof.
  • a heat exchanger for a cold gas refrigerator as claimed in claim 1 wherein the distance between said material surrounding each of said apertures and the adjacent extension closer to the cold side of said heat exchanger exceeds the distance between the material surrounding each of said apertures and the adjacent extension closer to the hot side of said heat exchanger.
  • a heat exchanger for a cold gas refrigerator as claimed in claim 2 wherein said material surrounding each of said apertures forms a crater-like projection.
  • a heat exchanger for a cold gas refrigerator as claimed in claim 2 wherein the distance between said material surrounding each of said apertures and the adjacent extension closer to the cold side of said heat exchanger is at the most 10 times the distance between said material surrounding each of said apertures and the adjacent extensions closer to the hot side of said heat exchanger.

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Mechanical Engineering (AREA)
  • Thermal Sciences (AREA)
  • General Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Materials Engineering (AREA)
  • Wood Science & Technology (AREA)
  • Organic Chemistry (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
US2899381D Cornelius otto jonkers Expired - Lifetime US2899381A (en)

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
NL98353T

Publications (1)

Publication Number Publication Date
US2899381A true US2899381A (en) 1959-08-11

Family

ID=19760477

Family Applications (1)

Application Number Title Priority Date Filing Date
US2899381D Expired - Lifetime US2899381A (en) Cornelius otto jonkers

Country Status (2)

Country Link
US (1) US2899381A (fr)
NL (1) NL98353C (fr)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4259844A (en) * 1979-07-30 1981-04-07 Helix Technology Corporation Stacked disc heat exchanger for refrigerator cold finger
US20060048521A1 (en) * 2002-10-31 2006-03-09 Hiroyuki Katayama Regenerator method for manufacturing regenerator, system for manufacturing regenerator and stirling refrigerating machine

Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1010044A (en) * 1911-02-16 1911-11-28 Henry R Worthington Counter-current condenser.
FR899140A (fr) * 1943-06-28 1945-05-22 Bloc récupérateur de chauffage par l'air applicable aux conduits de gaz chauds et délétères
US2708832A (en) * 1952-11-17 1955-05-24 Motor Products Corp Evaporator assembly

Patent Citations (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1010044A (en) * 1911-02-16 1911-11-28 Henry R Worthington Counter-current condenser.
FR899140A (fr) * 1943-06-28 1945-05-22 Bloc récupérateur de chauffage par l'air applicable aux conduits de gaz chauds et délétères
US2708832A (en) * 1952-11-17 1955-05-24 Motor Products Corp Evaporator assembly

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US4259844A (en) * 1979-07-30 1981-04-07 Helix Technology Corporation Stacked disc heat exchanger for refrigerator cold finger
US20060048521A1 (en) * 2002-10-31 2006-03-09 Hiroyuki Katayama Regenerator method for manufacturing regenerator, system for manufacturing regenerator and stirling refrigerating machine
US7383687B2 (en) * 2002-10-31 2008-06-10 Sharp Kabushiki Kaisha Regenerator method for manufacturing regenerator, system for manufacturing regenerator and stirling refrigerating machine

Also Published As

Publication number Publication date
NL98353C (fr)

Similar Documents

Publication Publication Date Title
US2944966A (en) Method for separation of fluid mixtures
US2731810A (en) Qjivaiiov snoonilnod
USRE19140E (en) Metallic filling fob cold
US2446997A (en) Molecular distillation process and apparatus for the separation of isotopes, etc.
US2049748A (en) Heat exchanger
US3062015A (en) Separation of gaseous mixtures
US11125506B2 (en) Vertical tube heat exchanger and method for exchanging heat
US2492788A (en) Regenerator
JP2005520670A (ja) 混合流体の分離のための小型精留ユニットおよびそのような混合流体の分離のための精留プロセス
US2158238A (en) Process for thermal atmolysis and apparatus employing same
US2690060A (en) Fractional distillation
US2899381A (en) Cornelius otto jonkers
US2523529A (en) Eliminator for refrigeration system evaporators
US2897655A (en) System comprising a cold-gas refrigerator and a heat exchanger
US2433604A (en) Separation of the constituents of gaseous mixtures
US2915883A (en) Gas-fractionating column
US2894371A (en) Preventing condensation inside a vortex tube
US2995499A (en) Apparatus for fractional distillation of multiple component mixtures
US1961203A (en) Apparatus for separating mixed gases by selective liquefaction
US1530461A (en) Recovery of helium
US1380460A (en) Method and apparatus for devaporizing and cooling
US2522640A (en) Separation of hydrocarbon gases at low temperatures
US5544498A (en) Efficieny cooling fluid circuit
US2802345A (en) Rectification column
US3328264A (en) Two-stage overhead process condenser for distilling columns