GB1252981A - - Google Patents

Info

Publication number
GB1252981A
GB1252981A GB1252981DA GB1252981A GB 1252981 A GB1252981 A GB 1252981A GB 1252981D A GB1252981D A GB 1252981DA GB 1252981 A GB1252981 A GB 1252981A
Authority
GB
United Kingdom
Prior art keywords
freezant
articles
vapour
conveyer
pan
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
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 filed Critical
Publication of GB1252981A publication Critical patent/GB1252981A/en
Expired legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28CHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
    • F28C3/00Other direct-contact heat-exchange apparatus
    • F28C3/005Other direct-contact heat-exchange apparatus one heat-exchange medium being a solid
    • AHUMAN NECESSITIES
    • A23FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
    • A23LFOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
    • A23L3/00Preservation of foods or foodstuffs, in general, e.g. pasteurising, sterilising, specially adapted for foods or foodstuffs
    • A23L3/36Freezing; Subsequent thawing; Cooling
    • A23L3/37Freezing; Subsequent thawing; Cooling with addition of or treatment with chemicals
    • A23L3/375Freezing; Subsequent thawing; Cooling with addition of or treatment with chemicals with direct contact between the food and the chemical, e.g. liquid nitrogen, at cryogenic temperature
    • 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
    • F25DREFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
    • F25D9/00Devices not associated with refrigerating machinery and not covered by groups F25D1/00 - F25D7/00; Combinations of devices covered by two or more of the groups F25D1/00 - F25D7/00
    • F25D9/005Devices not associated with refrigerating machinery and not covered by groups F25D1/00 - F25D7/00; Combinations of devices covered by two or more of the groups F25D1/00 - F25D7/00 using fluorinated halogenous hydrocarbons

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Nutrition Science (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Food Science & Technology (AREA)
  • Polymers & Plastics (AREA)
  • Combustion & Propulsion (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)

Abstract

1,252,981. Cooling conveyed materials. E.I. DU PONT DE NEMOURS & CO. 5 Feb., 1969 [6 Feb., 1968; 19 April, 1968; 30 Jan., 1969 (3)], No. 6232/69. Heading F4H. Articles or materials are cooled by direct contact with a boiling liquid freezant in a vessel which is open at its top to the atmosphere and which contains a freezant vapour condenser to avoid the escape of freezant vapour and to maintain in the lower part of the vessel a layer of gas which comprises only freezant vapour. The articles or materials are passed into and out of the freezant vapour layer either through a passage which terminates within the layer or on slow moving conveyers so that the layer is disrupted as little as possible. As illustrated in Fig. 1, articles are passed by a conveyer 4 into a sluice pan 9 containing freezant. A pump 10 maintains a fast moving surface current in the sluice pan to carry the articles to an output conveyer 13. Freezant vapour generated by contact with the articles forms a layer of 100% freezant vapour whose top is indicated at 5. Above the level 5 is a freezant vapour/air mixture whose freezant concentration decreases to the top of the vessel. The level 5 is maintained between the limits 18 and 19 by a condenser 17 which avoids the escape of substantial amounts of freezant from the vessel. Liquid freezant from the condenser falls into the sluice pan and into a sump 16. The depth of the sluice pan is such that articles falling from the conveyer 4 do not touch the bottom of the pan. For servicing purposes, the freezant may be withdrawn into a tank 24, and after servicing may be returned to the vessel leaving any sludge to be removed through a valve 26. Make up freezant may be supplied from a store 20. As illustrated in Fig. 2, articles are passed down an entrance passage 36 into a sluice pan 41 after which they are further cooled on a conveyer 47 by films of liquid freezant formed by running the freezant over plates 51. A baffle 44 prevents liquid freezant from the condenser 43 from contacting articles on the conveyer 47. The upper limit of the 100% freezant vapour layer is indicated at 40 and the maintainance of quiescent conditions is aided by a baffle 45 and by a honeycomb structure 69. The latter is surmounted by a dust cover 70. Freezant vapour produced by a heater 58 may be passed to distributers 60 and 59 on the conveyer 47 and the output conveyer 52 in order to evaporate any liquid freezant remaining on the articles. Secondary vapour condensers 62 and 63 may be located in the outlet passage 53 to aid the conservation of freezant. In a modification, Fig. 6 (not shown), the sluice pan is omitted and a single conveyer carries the articles through the entrance passage, the cooling zone and the outlet passage. The freezant may be a single polyfluorinated hydrocarbon having a boiling point between 5‹ C. and - 50‹ C. or may be an azeotropic mixture of such hydrocarbons. Hydrate formation is minimized when wet articles are being cooled since the articles contact the liquid freezant early in the cooling process and are therefore passed quickly through the hydrate forming temperature range. The process of the invention may be used to freeze solid or liquid foods and to cool metal parts which require shrink fitting. The Specification lists foods to which the process is applicable and also discloses preferred freezants, operating conditions and dimensions.
GB1252981D 1968-02-06 1969-02-05 Expired GB1252981A (en)

Applications Claiming Priority (5)

Application Number Priority Date Filing Date Title
US70339368A 1968-02-06 1968-02-06
US72525768A 1968-04-19 1968-04-19
US79532869A 1969-01-30 1969-01-30
US79532969A 1969-01-30 1969-01-30
US79532769A 1969-01-30 1969-01-30

Publications (1)

Publication Number Publication Date
GB1252981A true GB1252981A (en) 1971-11-10

Family

ID=27542103

Family Applications (1)

Application Number Title Priority Date Filing Date
GB1252981D Expired GB1252981A (en) 1968-02-06 1969-02-05

Country Status (3)

Country Link
BE (1) BE727885A (en)
GB (1) GB1252981A (en)
IE (1) IE32643B1 (en)

Also Published As

Publication number Publication date
IE32643L (en) 1969-08-06
BE727885A (en) 1969-07-16
IE32643B1 (en) 1973-10-17

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Legal Events

Date Code Title Description
PS Patent sealed
PCNP Patent ceased through non-payment of renewal fee