US1614387A - Apparatus for the transmission of heat and cold - Google Patents

Apparatus for the transmission of heat and cold Download PDF

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Publication number
US1614387A
US1614387A US74610A US7461025A US1614387A US 1614387 A US1614387 A US 1614387A US 74610 A US74610 A US 74610A US 7461025 A US7461025 A US 7461025A US 1614387 A US1614387 A US 1614387A
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Prior art keywords
receptacle
heat
balls
piston
cold
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US74610A
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Pereda Celedonio Vicente
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Publication of US1614387A publication Critical patent/US1614387A/en
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    • F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28—HEAT EXCHANGE IN GENERAL
    • F28D—HEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D19/00—Regenerative heat-exchange apparatus in which the intermediate heat-transfer medium or body is moved successively into contact with each heat-exchange medium
    • F28D19/02—Regenerative heat-exchange apparatus in which the intermediate heat-transfer medium or body is moved successively into contact with each heat-exchange medium using granular particles
    • Y—GENERAL 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S159/00—Concentrating evaporators
    • Y10S159/29—Pebble bed
    • Y—GENERAL 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
    • Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
    • Y10S—TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y10S159/00—Concentrating evaporators
    • Y10S159/33—Two liquids, one a heat carrier

Definitions

  • This invention relates to heat exchanging devices of the type in which heat is transferred through the medium of movable solid bodies such as metal balls.
  • the object of the invention is to more elliciently utilize the heat, and the invention which is applicable to not only heating but cooling consists in causing the metal balls to be plunged directly into the liquid or solid substance to be heated or cooled, the heat exchange taking place by direct contact within stationary receptacles.
  • 1 is a receptacle supplied with a funnel-shaped bottom within which enter by means of conduit-s 2 hot gases under their own pressure or by means of suction created by an artificial draught; 3 are screens adapted to retain any solid bodies that happen to pass along with such hot gases.
  • the hot gas passes across the receptacle 1 in an upward direction and leaves it by the chimney 4 and delivers its heat to the balls 5 which are admitted to the receptacle 1 through the conduit 6 and traverse the receptacle 1 by gravity in adownward direction contrary to the direction of the gas current.
  • the receptacle 1 which may be called the heat-absorbing receptacle, is supplied with a funnel-shaped bottom and with a discharge device by the operat on of which the balls are intermittently discharged in a regulated quantity.
  • This discharge device consists of a piston 7 with a cavity 8 in its surface in connection with a piston rod 9 and with a cylinder 10.
  • the piston does not only reciprocate within the cylinder 10 but can also rotate around its axis.
  • the piston carries on one side a threaded spindle 11 which engages a corresponding tapped nut arranged in the cover of the cylinder, so that during the axial displacement of the piston the same is obliged to effect at the same time a rotary motion around its axis.
  • the receptacle 12 contains the liquid to be evaporated and in this receptacle same consists of a piston 7 with cavity 8,
  • piston rod 9 and cylinder 10; 11' is again a threaded spindle which fits in a tapped nut arranged in the cylinder cover in order to rotate the piston around its axis when displaced longitudinally.
  • This latter discharge device is adapted to collect besides the means of conveyance also the heated liquid between them. The same is intermittently operated so that the material from the receptacle 12 is withdrawn intermittently in regulated quantities and introduced by its own weight within the receptacle 20.
  • the receptacle 20 is adapted to receive not only the conveyance means but also the heated liquid or solid material conducted with it.
  • This material discharged from the receptacle 12 into the receptacle 20 drops upon a shaking screen 15, by which the conveying balls are sepa rated from the liquid to which they have imparted their heat.
  • the liquid passes away by means of the conduit 17 to wherever it is to be utilized or it may be re-conducted by suitable means to the receptacle 1 2 to receive further heating.
  • the balls that have given up their heat are led away from the grid 15 by the chute 16 to the lower end of a bucket elevator 18 :which raises them to the upper end of a sloping conduit 6, down which they pass and are re-admitted to the receptacle 1 to be again heated.
  • the conveyor balls can be made of any suitable material, but they are preferably made from metal; there may also be employed hollow metal balls filled with water. In this case care must be taken that the temperature of the water within the balls does not surpass 100 degrees C. 19 is a feed opening on the receptacle 12 serving for the introduction of solid material within the receptacle 12. In this case the material will be conveniently fed by its own weight from a hopper supplied with an automatic feed re ulator.
  • a heat exchange; device comprising in combination, a heating chamber adapted to be interposed in a heating system and pro- Yided with a frusto-conical bottom having a central outlet, another similarly shaped liquid containing chamber in communication with the heating chamber, direct contact including a plurality of metal balls, receiving means s1tuated beneath the liquid containing chamber and in communication therewith, means interposed between the chambers and between the liquid containing chamber and the receiving means for controlling the transfer of a predetermined amount of balls from chamber to chamber and from said liquid containing chamber to said receiving means, means in communication with the receivin means for controlling the passage of liqui therefrom, screening means for the balls, and means for conveying the balls from the receiving means to the heating chamber so as to effect a continuous operaton.

Description

I 1 614387 Jan. 11 1927. PEREDA E TRANSMISSIFON OF HEAT AND COLD APPARATUS FOR TH Filed Dec. 10 1925 C. PerecZcL luveruffOR Patented Jan, 11, 1927.
UNITED STATES PATENT OFFICE. A
OELEDONIO VICENTE PEREDA, OF BUENOS AIR ES ARGENTINA.
APPARATUS FOR THE TRANSMISSION OF HEAT AND COLD.
Application filed December 10, 1925, Serial No. 74,610, and in Germany May 30, 1923.
This invention relates to heat exchanging devices of the type in which heat is transferred through the medium of movable solid bodies such as metal balls.
The object of the invention is to more elliciently utilize the heat, and the invention which is applicable to not only heating but cooling consists in causing the metal balls to be plunged directly into the liquid or solid substance to be heated or cooled, the heat exchange taking place by direct contact within stationary receptacles.
Reference should be had to the accompanying drawing, which forms a part of this specification, which shows a vertical sectional middle view representing one form of apparatus in which the invention may be carried into eft'ect as an apparatus for distilling liquids.
In this figure, 1 is a receptacle supplied with a funnel-shaped bottom within which enter by means of conduit-s 2 hot gases under their own pressure or by means of suction created by an artificial draught; 3 are screens adapted to retain any solid bodies that happen to pass along with such hot gases. The hot gas passes across the receptacle 1 in an upward direction and leaves it by the chimney 4 and delivers its heat to the balls 5 which are admitted to the receptacle 1 through the conduit 6 and traverse the receptacle 1 by gravity in adownward direction contrary to the direction of the gas current. The receptacle 1, which may be called the heat-absorbing receptacle, is supplied with a funnel-shaped bottom and with a discharge device by the operat on of which the balls are intermittently discharged in a regulated quantity. This discharge device consists of a piston 7 with a cavity 8 in its surface in connection with a piston rod 9 and with a cylinder 10. The piston does not only reciprocate within the cylinder 10 but can also rotate around its axis. For this purpose the piston carries on one side a threaded spindle 11 which engages a corresponding tapped nut arranged in the cover of the cylinder, so that during the axial displacement of the piston the same is obliged to effect at the same time a rotary motion around its axis. At each stroke the cavity 8 of the piston 7 is loaded with a quantity of balls which are discharged after the displacement of the piston in the re ceptacle 12. The receptacle 12 contains the liquid to be evaporated and in this receptacle same consists of a piston 7 with cavity 8,
piston rod 9 and cylinder 10; 11' is again a threaded spindle which fits in a tapped nut arranged in the cylinder cover in order to rotate the piston around its axis when displaced longitudinally. This latter discharge device is adapted to collect besides the means of conveyance also the heated liquid between them. The same is intermittently operated so that the material from the receptacle 12 is withdrawn intermittently in regulated quantities and introduced by its own weight within the receptacle 20. The receptacle 20 is adapted to receive not only the conveyance means but also the heated liquid or solid material conducted with it. This material discharged from the receptacle 12 into the receptacle 20 drops upon a shaking screen 15, by which the conveying balls are sepa rated from the liquid to which they have imparted their heat. The liquid passes away by means of the conduit 17 to wherever it is to be utilized or it may be re-conducted by suitable means to the receptacle 1 2 to receive further heating. The balls that have given up their heat are led away from the grid 15 by the chute 16 to the lower end of a bucket elevator 18 :which raises them to the upper end of a sloping conduit 6, down which they pass and are re-admitted to the receptacle 1 to be again heated.
The conveyor balls can be made of any suitable material, but they are preferably made from metal; there may also be employed hollow metal balls filled with water. In this case care must be taken that the temperature of the water within the balls does not surpass 100 degrees C. 19 is a feed opening on the receptacle 12 serving for the introduction of solid material within the receptacle 12. In this case the material will be conveniently fed by its own weight from a hopper supplied with an automatic feed re ulator.
aving now particularly described and ascertained the nature of my said invention 10.,heat conducting means and in what manner the same is to be" performed, I declare that what I claim is A heat exchange; device comprising in combination, a heating chamber adapted to be interposed in a heating system and pro- Yided with a frusto-conical bottom having a central outlet, another similarly shaped liquid containing chamber in communication with the heating chamber, direct contact including a plurality of metal balls, receiving means s1tuated beneath the liquid containing chamber and in communication therewith, means interposed between the chambers and between the liquid containing chamber and the receiving means for controlling the transfer of a predetermined amount of balls from chamber to chamber and from said liquid containing chamber to said receiving means, means in communication with the receivin means for controlling the passage of liqui therefrom, screening means for the balls, and means for conveying the balls from the receiving means to the heating chamber so as to effect a continuous operaton.
In testimony whereof I have signed my name to this specification.
GELEDONIO VICENTE PEREDA.
US74610A 1923-05-30 1925-12-10 Apparatus for the transmission of heat and cold Expired - Lifetime US1614387A (en)

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Cited By (32)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2417049A (en) * 1943-10-18 1947-03-11 Babcock & Wilcox Co Control system
US2422791A (en) * 1945-07-30 1947-06-24 Universal Oil Prod Co Endothermic catalytic conversion of hydrocarbons
US2446388A (en) * 1943-10-20 1948-08-03 Brassert & Co Preheating furnace blast
US2447306A (en) * 1943-09-16 1948-08-17 Babcock & Wilcox Co Fluid heater
US2512442A (en) * 1945-10-31 1950-06-20 Babcock & Wilcox Co Solid material heating apparatus
US2520164A (en) * 1944-07-04 1950-08-29 Babcock & Wilcox Co Fluid heating
US2571342A (en) * 1947-02-18 1951-10-16 Socony Vacuum Oil Co Inc Combination hydrocarbon vaporization and cracking process
US2625377A (en) * 1948-12-28 1953-01-13 Phillips Petroleum Co Pebble chamber
US2689047A (en) * 1949-07-15 1954-09-14 Phillips Petroleum Co Pebble flow control for a pebble heat exchanger
US2788313A (en) * 1952-06-16 1957-04-09 Aspegren Olof Erik August Method of pyrolysis of fuel
DE1032766B (en) * 1953-12-30 1958-06-26 Siemens Ag Heat exchanger working with small exchange bodies
US2846422A (en) * 1954-07-19 1958-08-05 Exxon Research Engineering Co Solid liquid heat exchange in low temperature polymerization
US2846421A (en) * 1954-02-18 1958-08-05 Phillips Petroleum Co High heat capacity cooling medium
DE1052207B (en) * 1955-06-24 1959-03-05 Didier Werke Ag Device and method for separating iron sulphate monohydrate from spent pickling liquid containing sulfuric acid
DE972335C (en) * 1944-04-19 1959-07-02 Demag Ag Process and device for utilizing the sensible heat of useful gas from gas generators
US2905596A (en) * 1954-01-04 1959-09-22 Phillips Petroleum Co Distillation method and apparatus
US2953524A (en) * 1956-04-25 1960-09-20 Jr Wilson C Rich Rectification process using cool shot in addition to reflux
DE974985C (en) * 1943-09-16 1961-06-22 Babcock & Wilcox Co Process for heating a liquid or gaseous medium with the aid of a stream of a refractory, heat-transferring, solid material
US3219105A (en) * 1962-10-24 1965-11-23 Nettel Frederick Method and apparatus for producing superheated steam, in particular for power recovery from the exhaust of internal combustion engines
US3233659A (en) * 1962-07-03 1966-02-08 Nettel Frederick Heat exchanger using hollow metal pellets as heat carrier
US3233660A (en) * 1962-11-27 1966-02-08 Nettel Frederick Heat exchanger using special pellets of sheet metal
US3254881A (en) * 1965-05-25 1966-06-07 Glenn O Rusk Helical ramp heat exchanger
US3401923A (en) * 1966-02-17 1968-09-17 Wilmot Eng Co Dryer
US3442769A (en) * 1965-10-22 1969-05-06 Winfield B Heinz Method and apparatus for heating and distilling saline water using heated pebbles
US3619422A (en) * 1967-09-04 1971-11-09 Elsa Rummel Process of drying sewage sludge
US3960203A (en) * 1971-04-29 1976-06-01 Titanium Technology N.V. Fluidized bed cooler
FR2468095A1 (en) * 1979-10-18 1981-04-30 Steinmueller Gmbh L & C HEAT TRANSMITTERS FOR REGENERATION HEAT EXCHANGE
FR2490801A1 (en) * 1980-09-19 1982-03-26 Steinmueller Gmbh L & C HEAT TRANSMITTERS FOR REGENERATION HEAT EXCHANGE
FR2492081A1 (en) * 1980-10-11 1982-04-16 Steinmueller Gmbh L & C HEAT TRANSMITTERS FOR REGENERATION HEAT EXCHANGE
US4361009A (en) * 1979-10-31 1982-11-30 The Babcock & Wilcox Company Moving bed heat storage and recovery system
US4479353A (en) * 1979-10-31 1984-10-30 The Babcock & Wilcox Company Moving bed heat storage and recovery system
WO2012152899A1 (en) * 2011-05-12 2012-11-15 Lafarge Decarbonation process

Cited By (34)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US2447306A (en) * 1943-09-16 1948-08-17 Babcock & Wilcox Co Fluid heater
DE974985C (en) * 1943-09-16 1961-06-22 Babcock & Wilcox Co Process for heating a liquid or gaseous medium with the aid of a stream of a refractory, heat-transferring, solid material
US2417049A (en) * 1943-10-18 1947-03-11 Babcock & Wilcox Co Control system
US2446388A (en) * 1943-10-20 1948-08-03 Brassert & Co Preheating furnace blast
DE972335C (en) * 1944-04-19 1959-07-02 Demag Ag Process and device for utilizing the sensible heat of useful gas from gas generators
US2520164A (en) * 1944-07-04 1950-08-29 Babcock & Wilcox Co Fluid heating
US2422791A (en) * 1945-07-30 1947-06-24 Universal Oil Prod Co Endothermic catalytic conversion of hydrocarbons
US2512442A (en) * 1945-10-31 1950-06-20 Babcock & Wilcox Co Solid material heating apparatus
US2571342A (en) * 1947-02-18 1951-10-16 Socony Vacuum Oil Co Inc Combination hydrocarbon vaporization and cracking process
US2625377A (en) * 1948-12-28 1953-01-13 Phillips Petroleum Co Pebble chamber
US2689047A (en) * 1949-07-15 1954-09-14 Phillips Petroleum Co Pebble flow control for a pebble heat exchanger
US2788313A (en) * 1952-06-16 1957-04-09 Aspegren Olof Erik August Method of pyrolysis of fuel
DE1032766B (en) * 1953-12-30 1958-06-26 Siemens Ag Heat exchanger working with small exchange bodies
US2905596A (en) * 1954-01-04 1959-09-22 Phillips Petroleum Co Distillation method and apparatus
US2846421A (en) * 1954-02-18 1958-08-05 Phillips Petroleum Co High heat capacity cooling medium
US2846422A (en) * 1954-07-19 1958-08-05 Exxon Research Engineering Co Solid liquid heat exchange in low temperature polymerization
DE1052207B (en) * 1955-06-24 1959-03-05 Didier Werke Ag Device and method for separating iron sulphate monohydrate from spent pickling liquid containing sulfuric acid
US2953524A (en) * 1956-04-25 1960-09-20 Jr Wilson C Rich Rectification process using cool shot in addition to reflux
US3233659A (en) * 1962-07-03 1966-02-08 Nettel Frederick Heat exchanger using hollow metal pellets as heat carrier
US3219105A (en) * 1962-10-24 1965-11-23 Nettel Frederick Method and apparatus for producing superheated steam, in particular for power recovery from the exhaust of internal combustion engines
US3233660A (en) * 1962-11-27 1966-02-08 Nettel Frederick Heat exchanger using special pellets of sheet metal
US3254881A (en) * 1965-05-25 1966-06-07 Glenn O Rusk Helical ramp heat exchanger
US3442769A (en) * 1965-10-22 1969-05-06 Winfield B Heinz Method and apparatus for heating and distilling saline water using heated pebbles
US3401923A (en) * 1966-02-17 1968-09-17 Wilmot Eng Co Dryer
US3619422A (en) * 1967-09-04 1971-11-09 Elsa Rummel Process of drying sewage sludge
US3960203A (en) * 1971-04-29 1976-06-01 Titanium Technology N.V. Fluidized bed cooler
FR2468095A1 (en) * 1979-10-18 1981-04-30 Steinmueller Gmbh L & C HEAT TRANSMITTERS FOR REGENERATION HEAT EXCHANGE
US4361009A (en) * 1979-10-31 1982-11-30 The Babcock & Wilcox Company Moving bed heat storage and recovery system
US4479353A (en) * 1979-10-31 1984-10-30 The Babcock & Wilcox Company Moving bed heat storage and recovery system
FR2490801A1 (en) * 1980-09-19 1982-03-26 Steinmueller Gmbh L & C HEAT TRANSMITTERS FOR REGENERATION HEAT EXCHANGE
FR2492081A1 (en) * 1980-10-11 1982-04-16 Steinmueller Gmbh L & C HEAT TRANSMITTERS FOR REGENERATION HEAT EXCHANGE
WO2012152899A1 (en) * 2011-05-12 2012-11-15 Lafarge Decarbonation process
FR2975094A1 (en) * 2011-05-12 2012-11-16 Lafarge Sa DECARBONATION PROCESS
US9321683B2 (en) 2011-05-12 2016-04-26 Lafarge Decarbonation process

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