EP0047914B1 - Dispositif pour l'extraction de la chaleur d'un matériau pulvérulent hydrophile au-dessous de 100 degrés C - Google Patents

Dispositif pour l'extraction de la chaleur d'un matériau pulvérulent hydrophile au-dessous de 100 degrés C Download PDF

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Publication number
EP0047914B1
EP0047914B1 EP81106805A EP81106805A EP0047914B1 EP 0047914 B1 EP0047914 B1 EP 0047914B1 EP 81106805 A EP81106805 A EP 81106805A EP 81106805 A EP81106805 A EP 81106805A EP 0047914 B1 EP0047914 B1 EP 0047914B1
Authority
EP
European Patent Office
Prior art keywords
water
sand
extracting heat
temperature lower
degrees centigrade
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
EP81106805A
Other languages
German (de)
English (en)
French (fr)
Other versions
EP0047914A1 (fr
Inventor
Serge Alquier
Louis Berthod
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.)
Alstom SA
Original Assignee
Alsthom Atlantique SA
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 Alsthom Atlantique SA filed Critical Alsthom Atlantique SA
Priority to AT81106805T priority Critical patent/ATE11017T1/de
Publication of EP0047914A1 publication Critical patent/EP0047914A1/fr
Application granted granted Critical
Publication of EP0047914B1 publication Critical patent/EP0047914B1/fr
Expired legal-status Critical Current

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Classifications

    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
    • F28C3/00—Other direct-contact heat-exchange apparatus
    • F28C3/10—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material
    • F28C3/12—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material the heat-exchange medium being a particulate material and a gas, vapour, or liquid
    • F28C3/16—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material the heat-exchange medium being a particulate material and a gas, vapour, or liquid the particulate material forming a bed, e.g. fluidised, on vibratory sieves
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B22—CASTING; POWDER METALLURGY
    • B22C—FOUNDRY MOULDING
    • B22C5/00—Machines or devices specially designed for dressing or handling the mould material so far as specially adapted for that purpose
    • B22C5/08—Machines or devices specially designed for dressing or handling the mould material so far as specially adapted for that purpose by sprinkling, cooling, or drying
    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28C—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA COME INTO DIRECT CONTACT WITHOUT CHEMICAL INTERACTION
    • F28C3/00—Other direct-contact heat-exchange apparatus
    • F28C3/10—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material
    • F28C3/12—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material the heat-exchange medium being a particulate material and a gas, vapour, or liquid
    • F28C3/14—Other direct-contact heat-exchange apparatus one heat-exchange medium at least being a fluent solid, e.g. a particulate material the heat-exchange medium being a particulate material and a gas, vapour, or liquid the particulate material moving by gravity, e.g. down a tube

Definitions

  • a device as specified above is known, for example from document US-A-3,205,543.
  • This device comprises a porous mat, which horizontally advances the material to be cooled and which lets dry air pass vertically .
  • Above this mat there are ejection nozzles which deliver drops of water to wet the hot material.
  • the amount of water is regulated according to the temperature of the material, so that the material is strongly watered when it is very hot (for example 200 ° C), while the water supply is blocked when the temperature drops below a certain limit, the air passing through the mat then ensures only cooling.
  • Such a device is subject to frequent maintenance, since the porosity of the carpet degrades quickly when it is desired to cool sand having a large particle size range. Indeed, very fine particles clog the pores of the carpet and thus impede the passage of air.
  • the object of the invention is, with respect to this state of the art, to propose a device with reduced maintenance, that is to say without porous carpet.
  • the means for moving the material comprise a jerk conveyor comprising a succession of ramps, the jolts being chosen to cause all the ramps to climb successively by the grains of the material, and that the means for spraying the water are arranged in zones where the grains fall from the top of a ramp onto the next ramp.
  • the single figure is a schematic view of a preferred embodiment of the invention.
  • the quantity of water just necessary for cooling is uniformly sprayed on the surface of the sand, this quantity corresponding to approximately 550 calories / kg of evaporated water.
  • Evaporation of the water is ensured by a low gas circulation, possibly under reduced pressure, which decreases the partial pressure of water vapor at the level of each grain and thus allows evaporation before the grains have been able to agglomerate.
  • the gas also allows evacuation by entrainment of the water vapor produced.
  • a uniform spraying of water on the surface of the sand is necessary and, preferably, 3% of cold water is injected by weight relative to the sand.
  • the device shown in the figure comprises a hopper 2 for the supply of pulverulent material, for example hot foundry sand.
  • the sand falls on a shaker conveyor comprising a table 4 set in motion by a mechanism 6 of known type. On this table are arranged three ascending ramps 8, 10 and 12 that the sand successively climbs under the action of the tremors applied by the mechanism 6.
  • a water sprayer In the vicinity of each of the ramp tops is arranged a water sprayer, respectively 16, 18 and 20, which directs the water onto the sand in the areas where the layers of sand mix in the vicinity of the top of the ramp, and where the sand falls.
  • shaker conveyor can be horizontal, inclined or helical.
  • the gas which, as indicated above, ensures evaporation is preferably air; it is sent, via a pipe 21, preferably in the opposite direction to that of the sand, and meets each grain which falls from the ramps, ensuring thus the evaporation of the water and the transport of the water vapor produced.
  • the air taken up in the vicinity of the hopper 2 is then hot and humid; it is sent to a condenser 22 which recovers the heat.

Landscapes

  • Engineering & Computer Science (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Molds, Cores, And Manufacturing Methods Thereof (AREA)
  • Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
  • Tea And Coffee (AREA)
  • Investigating Or Analyzing Materials Using Thermal Means (AREA)
  • Solid-Sorbent Or Filter-Aiding Compositions (AREA)
  • Separation Using Semi-Permeable Membranes (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Drying Of Solid Materials (AREA)
  • Turbine Rotor Nozzle Sealing (AREA)
EP81106805A 1980-09-04 1981-09-01 Dispositif pour l'extraction de la chaleur d'un matériau pulvérulent hydrophile au-dessous de 100 degrés C Expired EP0047914B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
AT81106805T ATE11017T1 (de) 1980-09-04 1981-09-01 Vorrichtung zum entziehen von waerme aus einem hygroskopischen koernigen material mit einer temperatur unter 100 grad celsius.

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
FR8019093 1980-09-04
FR8019093A FR2489489A1 (fr) 1980-09-04 1980-09-04 Procede d'extraction de la chaleur d'un materiau pulverulent hydrophile au-dessous de 100 oc

Publications (2)

Publication Number Publication Date
EP0047914A1 EP0047914A1 (fr) 1982-03-24
EP0047914B1 true EP0047914B1 (fr) 1985-01-02

Family

ID=9245649

Family Applications (1)

Application Number Title Priority Date Filing Date
EP81106805A Expired EP0047914B1 (fr) 1980-09-04 1981-09-01 Dispositif pour l'extraction de la chaleur d'un matériau pulvérulent hydrophile au-dessous de 100 degrés C

Country Status (9)

Country Link
US (1) US4377937A (enrdf_load_stackoverflow)
EP (1) EP0047914B1 (enrdf_load_stackoverflow)
AT (1) ATE11017T1 (enrdf_load_stackoverflow)
BR (1) BR8105611A (enrdf_load_stackoverflow)
CA (1) CA1162842A (enrdf_load_stackoverflow)
DE (1) DE3168042D1 (enrdf_load_stackoverflow)
ES (1) ES8206823A1 (enrdf_load_stackoverflow)
FR (1) FR2489489A1 (enrdf_load_stackoverflow)
MA (1) MA19259A1 (enrdf_load_stackoverflow)

Families Citing this family (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2674320B1 (fr) * 1991-03-21 1999-01-29 Lair Liquide Procede et dispositif de congelation
NZ250270A (en) * 1992-12-29 1995-07-26 Boc Group Inc Freezing food using liquid refrigerant: turbulent flow of refrigerant induced in trough type conveyor
FR2701552B1 (fr) * 1993-02-10 1995-03-24 Air Liquide Dispositif de congélation à couloir vibrant.
DE202010010804U1 (de) * 2010-07-29 2011-11-02 Lintec Gmbh & Co. Kg Mobile Vorrichtung zur Betonherstellung mit Kühlung von Schüttgut

Family Cites Families (9)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US1844782A (en) * 1926-10-30 1932-02-09 Krupp Fried Grusonwerk Ag Apparatus for cooling loose material
DE942271C (de) * 1952-10-17 1956-05-03 Metallgesellschaft Ag Verfahren zum kontinuierlichen Kuehlen von extrahiertem Gut
US2863190A (en) * 1954-10-20 1958-12-09 Fischer Ag Georg Method and means for cooling granular masses containing evaporable liquid
US3161485A (en) * 1957-12-20 1964-12-15 Fischer Ag Georg Sand cooling plant
US3089653A (en) * 1961-09-20 1963-05-14 Dundee Cement Co Hot clinker conveying and cooling apparatus
US3205543A (en) * 1963-05-27 1965-09-14 Rex Chainbelt Inc Process and apparatus for cooling foundry sand on a vibratory conveyor
US3172177A (en) * 1964-02-05 1965-03-09 Herbert C Brauchla Continuous method of preparing foundry sand
DE1483123A1 (de) * 1965-01-26 1969-01-23 Peters Ag Claudius Rostkuehler fuer Zementklinker u.dgl.
US3989227A (en) * 1974-10-10 1976-11-02 General Kinematics Corporation Fluid bed blender and cooler

Also Published As

Publication number Publication date
EP0047914A1 (fr) 1982-03-24
ES505181A0 (es) 1982-08-16
BR8105611A (pt) 1982-05-18
CA1162842A (fr) 1984-02-28
FR2489489B1 (enrdf_load_stackoverflow) 1984-04-27
FR2489489A1 (fr) 1982-03-05
DE3168042D1 (en) 1985-02-14
US4377937A (en) 1983-03-29
ATE11017T1 (de) 1985-01-15
MA19259A1 (fr) 1982-04-01
ES8206823A1 (es) 1982-08-16

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