EP0616182A2 - Process for the transmission of heat energy - Google Patents

Process for the transmission of heat energy Download PDF

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Publication number
EP0616182A2
EP0616182A2 EP94200684A EP94200684A EP0616182A2 EP 0616182 A2 EP0616182 A2 EP 0616182A2 EP 94200684 A EP94200684 A EP 94200684A EP 94200684 A EP94200684 A EP 94200684A EP 0616182 A2 EP0616182 A2 EP 0616182A2
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Prior art keywords
cylinder
gaseous fluid
temperature
molecules
energy
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EP94200684A
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German (de)
French (fr)
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EP0616182A3 (en
Inventor
José Maria de Quadras y de Caralt
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DE QUADRAS Y DE CARALT, JOSE MARIA
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    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F13/00Arrangements for modifying heat-transfer, e.g. increasing, decreasing
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F24HEATING; RANGES; VENTILATING
    • F24VCOLLECTION, PRODUCTION OR USE OF HEAT NOT OTHERWISE PROVIDED FOR
    • F24V99/00Subject matter not provided for in other main groups of this subclass

Definitions

  • the present patent application relates to a method for the transmission of heat energy, which has remarkable advantages and innovations compared to current methods used for identical or similar purposes.
  • the method for transmitting heat energy which is the subject of the present invention has been designed, this method relating to a system with practically no energy input, and therefore very economical, for transmitting heat or energy from one body to another, whether the first body is colder than the second or vice versa, by cooling a body by transmitting calories to another warmer body.
  • the process is based on the transmission of heat from a body to a gaseous fluid, on the subsequent increase in the speed of its molecules mechanically, thanks to which its temperature will increase, to then transmit the heat of this gaseous fluid to a third body. In this way, the calorific energy is extracted from the first body to enter the third.
  • the example described consists of a sealed cylinder 1 provided with a tubular shaft 2 which rests on bearings 3 and 4, while the rotation thereof is facilitated by means of a transmission element 5 driven by a motor 6.
  • the proposed method consists in the transmission of heat from a body 7, which can for example be running water, to a gaseous fluid 8, then mechanically increasing the speed of the molecules of the latter, which increases its temperature, to then transfer the heat from this gaseous fluid 8 to a third body, which in the present example relates to a fluid 9. In this way, heat energy is extracted from the body 7 to penetrate into the body 9.
  • the basis of this mechanical process consists in subjecting the gaseous fluid 8 to a centrifugal force inside the cylinder 1, which will be hermetic and can be divided into compartments isolated by partitions 10, while the fluid 7 circulates along the 'shaft 2 of this cylinder.
  • the molecules or particles of gaseous fluid 8 increase their speed by centrifugal acceleration, and therefore their temperature.
  • the molecules or particles of gaseous fluid 8 increase their speed by centrifugal acceleration, and therefore their temperature.
  • On the surface of tree 2, its molecules will cool, since during their transport to there, they overcome a centrifugal force which decreases their speed, and therefore therefore their temperature.

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  • Engineering & Computer Science (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Physical Or Chemical Processes And Apparatus (AREA)
  • Engine Equipment That Uses Special Cycles (AREA)
  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

Process for the transmission of heat energy, in which one or more sealed cylinders turn on bearings by means of the action of a motor, the cylinder(s) having a tubular shaft capable of receiving a body which is capable of heat exchange with a gaseous fluid situated close to the latter inside the cylinder, this gaseous fluid being capable, with the centrifugal acceleration of said cylinder, of increasing the speed and the temperature of its molecules in the direction of the periphery of this cylinder, being capable of bringing about in said zone a heat exchange with another body external to the cylinder by virtue of the temperature gradient which is caused along the radius thereof as a result of the centrifugal acceleration which is transmitted to the molecules of the gaseous fluid with a minimum energy supply. <IMAGE>

Description

La présente demande de brevet d'invention a pour objet un procédé pour la transmission d'énergie calorifique, qui présente de remarquables avantages et innovations par rapport aux procédés actuels utilisés à des fins identiques ou analogues.The present patent application relates to a method for the transmission of heat energy, which has remarkable advantages and innovations compared to current methods used for identical or similar purposes.

Actuellement, il faut mentionner, en référence à l'état de la technique, qu'il existe des procédés multiples et variés pour élever la température d'un corps, pour obtenir dans celui-ci une énergie utilisable quelconque mécanique, électrique, ambiante, etc. Dans tous ceux-ci, il y a un apport d'énergie de combustion, atomique, électrique, électronique, etc. Il en va de même pour obtenir une réfrigération, mais toujours avec un apport important d'énergie de ce type.Currently, it should be mentioned, with reference to the state of the art, that there are multiple and varied processes for raising the temperature of a body, in order to obtain in it any usable mechanical, electrical, ambient energy, etc. In all of these, there is a supply of combustion energy, atomic, electrical, electronic, etc. The same goes for obtaining refrigeration, but always with a significant supply of energy of this type.

Pour éviter ces inconvénients, on a conçu le procédé pour la transmission d'énergie calorifique qui fait l'objet de la présente invention, ce procédé concernant un système sans pratiquement aucun apport d'énergie, et de ce fait très économique, de transmission de chaleur ou d'une énergie d'un corps à un autre, que le premier corps soit plus froid que le second ou inversement, en refroidissant un corps par transmission des calories à un autre corps plus chaud.To avoid these drawbacks, the method for transmitting heat energy which is the subject of the present invention has been designed, this method relating to a system with practically no energy input, and therefore very economical, for transmitting heat or energy from one body to another, whether the first body is colder than the second or vice versa, by cooling a body by transmitting calories to another warmer body.

Le procédé est basé sur la transmission de la chaleur d'un corps à un fluide gazeux, sur l'augmentation subséquente de la vitesse de ses molécules de manière mécanique, grâce à quoi sa température augmentera, pour ensuite transmettre la chaleur de ce fluide gazeux à un troisième corps. De cette manière, l'énergie calorifique est extraite du premier corps pour pénétrer dans le troisième.The process is based on the transmission of heat from a body to a gaseous fluid, on the subsequent increase in the speed of its molecules mechanically, thanks to which its temperature will increase, to then transmit the heat of this gaseous fluid to a third body. In this way, the calorific energy is extracted from the first body to enter the third.

Avec ce procédé, il est par exemple possible de chauffer l'intérieur d'un édifice en extrayant les calories du milieu ambiant extérieur, ou en sens contraire, de le réfrigérer, de prendre des calories par exemple d'un lac, pour produire de la vapeur d'eau, ou de tant d'autres applications en vue de libérer un type quelconque d'énergie utilisable. L'intérêt du procédé mécanique est qu'il ne consomme pratiquement aucune énergie.With this process, it is for example possible to heat the interior of a building by extracting the calories from the external ambient environment, or in the opposite direction, to refrigerate it, to take calories for example from a lake, to produce water vapor, or so many other applications to release any kind of usable energy. The advantage of the mechanical process is that it consumes practically no energy.

De façon à présenter une description très détaillée de l'invention, celle-ci se réfère aux figures annexées, dans lesquelles un mode de réalisation préféré est représenté à titre d'exemple et sans aucun caractère limitatif.In order to present a very detailed description of the invention, it refers to the appended figures, in which a preferred embodiment is shown by way of example and without any limiting character.

Dans les dessins :

la figure 1
représente une vue schématique de profil de l'ensemble de l'invention, et
la figure 2
montre une vue en coupe d'un détail de la figure 1 précédente.
In the drawings:
figure 1
represents a schematic profile view of the assembly of the invention, and
figure 2
shows a sectional view of a detail of Figure 1 above.

Si on fait référence aux figures, on y appréciera en leur représentation une réalisation pratique de l'invention, qui peut présenter diverses modifications qui en aucun cas n'affectent l'essence de l'invention, et dans laquelle les flèches simples indiquent un transfert calorifique, alors que les flèches doubles montrent un déplacement de fluide.If we refer to the figures, we will appreciate in their representation a practical embodiment of the invention, which may have various modifications which in no case affect the essence of the invention, and in which the simple arrows indicate a transfer calorific, while the double arrows show a displacement of fluid.

L'exemple décrit est constitué d'un cylindre étanche 1 doté d'un arbre tubulaire 2 qui repose sur des paliers 3 et 4, tandis que la rotation de celui-ci est facilitée au moyen d'un élément de transmission 5 entraîné par un moteur 6.The example described consists of a sealed cylinder 1 provided with a tubular shaft 2 which rests on bearings 3 and 4, while the rotation thereof is facilitated by means of a transmission element 5 driven by a motor 6.

Le procédé proposé consiste en la transmission de la chaleur depuis un corps 7, qui peut être par exemple de l'eau courante, vers un fluide gazeux 8, à augmenter ensuite de manière mécanique la vitesse des molécules de ce dernier, ce qui augmente sa température, pour ensuite transférer la chaleur de ce fluide gazeux 8 à un troisième corps, qui dans l'exemple présent concerne un fluide 9. De cette manière, de l'énergie calorifique est extraite du corps 7 pour pénétrer dans le corps 9.The proposed method consists in the transmission of heat from a body 7, which can for example be running water, to a gaseous fluid 8, then mechanically increasing the speed of the molecules of the latter, which increases its temperature, to then transfer the heat from this gaseous fluid 8 to a third body, which in the present example relates to a fluid 9. In this way, heat energy is extracted from the body 7 to penetrate into the body 9.

La base de ce procédé mécanique consiste à soumettre le fluide gazeux 8 à une force centrifuge à l'intérieur du cylindre 1, qui sera hermétique et pourra être divisé en compartiments isolés par des cloisons 10, tandis que le fluide 7 circule le long de l'arbre 2 de ce cylindre.The basis of this mechanical process consists in subjecting the gaseous fluid 8 to a centrifugal force inside the cylinder 1, which will be hermetic and can be divided into compartments isolated by partitions 10, while the fluid 7 circulates along the 'shaft 2 of this cylinder.

En se déplaçant dans leur mouvement continu depuis la superficie de l'arbre 2 vers la périphérie du cylindre 1, les molécules ou particules de fluide gazeux 8 augmentent leur vitesse par l'accélération centrifuge, et de ce fait leur température. A la superficie de l'arbre 2, ses molécules se refroidiront, puisque lors de leur transport vers là-bas, elles surmontent une force centrifuge qui diminue leur vitesse, et ainsi donc leur température.By moving in their continuous movement from the surface of the shaft 2 to the periphery of the cylinder 1, the molecules or particles of gaseous fluid 8 increase their speed by centrifugal acceleration, and therefore their temperature. On the surface of tree 2, its molecules will cool, since during their transport to there, they overcome a centrifugal force which decreases their speed, and therefore therefore their temperature.

De cette manière, on obtient un équilibre stable entre l'arbre 2 et la périphérie du cylindre 1, avec une échelle de températures qui iront en augmentant depuis le premier jusqu'à la seconde, en maintenant constante l'enthalpie globale du fluide, sans apport de davantage d'énergie. On déterminera l'énergie nécéssaire au démarrage pour atteindre les vitesses de rotation requises, et on consommera ensuite uniquement l'énergie qui peut être consommée par des frottements dans le montage.In this way, a stable equilibrium is obtained between the shaft 2 and the periphery of the cylinder 1, with a temperature scale which will increase from the first to the second, keeping the overall enthalpy of the fluid constant, without providing more energy. We will determine the energy required starting to reach the required rotational speeds, and then only the energy that can be consumed by friction in the assembly will be consumed.

Dans cet équilibre stable de différentes températures, on obtient "n" degrés de différence entre l'arbre 2 et la périphérie du cylindre 1. Comme l'énergie cinétique et l'enthalpie du fluide dans l'ensemble sont identiques, la température de la périphérie aura augmenté de "T" degrés au-dessus de la température du milieu ambiant extérieur, et aura diminué au centre de "-t" degrés par rapport à la température ambiante, et "T"-"-t"="n"

Figure imgb0001
.In this stable equilibrium of different temperatures, we obtain "n" degrees of difference between the shaft 2 and the periphery of the cylinder 1. As the kinetic energy and the enthalpy of the fluid as a whole are identical, the temperature of the periphery will have increased by "T" degrees above the temperature of the external ambient environment, and will have decreased in the center by "-t" degrees compared to ambient temperature, and "T" - "- t" = "n"
Figure imgb0001
.

Si alors on augmente la température de l'arbre 2 de "-t" (jusqu'aux alentours de la température extérieure, par exemple avec de l'eau à l'intérieur de l'arbre 2), la température de la périphérie augmentera de "T" à "T+x" degrés, ce qui permet d'extraire de la périphérie de l'énergie, jusqu'à ramener sa température de "T+x" à "T". Par conséquent, le fluide gazeux 8 qui se trouve à proximité de l'arbre reprendra la température inférieure de "-t" degrés à la température ambiante extérieure. Cela permet de reprendre l'opération et d'extraire à nouveau des calories d'un objet qui se trouve à température ambiante (dans cet exemple, de l'eau).If then the temperature of the shaft 2 is increased by "-t" (up to around the outside temperature, for example with water inside the shaft 2), the temperature of the periphery will increase from "T" to "T + x" degrees, which allows the energy to be extracted from the periphery, until its temperature is reduced from "T + x" to "T". Consequently, the gaseous fluid 8 which is located near the shaft will resume the temperature lower by "-t" degrees than the outside ambient temperature. This allows you to resume the operation and extract calories again from an object that is at room temperature (in this example, water).

Pour une meilleure compréhension, on a présenté une explication suivant un procédé intermittent. En réalité, il n'est pas tant nécessaire que l'apport d'énergie calorifique à l'arbre 2 et la prise de chaleur à la périphérie du cylindre 1 se fassent de manière continue.For better understanding, an explanation has been presented using an intermittent process. In reality, it is not so much necessary that the supply of heat energy to the shaft 2 and the heat intake at the periphery of the cylinder 1 take place continuously.

De même, comme la vitesse du cylindre 1 doit être très élevée pour obtenir une accélération centrifuge qui permette une "T" élevée, pour être utilisable comme source d'énergie, on peut placer différents cylindres 1 en série, pour atteindre dans le dernier une température "T" considérable et utilisable de façon meilleure.Likewise, since the speed of cylinder 1 must be very high in order to obtain a centrifugal acceleration which allows a high "T", to be usable as an energy source, it is possible to place different cylinders 1 in series, to reach in the latter a considerable temperature "T" which can be used in a better way.

Claims (1)

Procédé pour la transmission d'énergie calorifique, caractérisé essentiellement en ce que l'on dispose en série un ou plusieurs cylindres étanches qui tournent sur des paliers au moyen de l'action d'un moteur, le cylindre ou l'ensemble de cylindres présentant un arbre tubulaire apte à recevoir un corps qui est capable d'échanger de la chaleur avec un fluide gazeux situé à proximité de celui-ci à l'intérieur du cylindre, ce fluide gazeux étant susceptible, avec l'accélération centrifuge dudit cylindre, d'augmenter la vitesse et la température de ses molécules en direction de la périphérie de ce cylindre en pouvant réaliser dans ladite zone un échange calorifique avec un autre corps extérieur au cylindre, grâce au gradient de températures qui est provoqué suivant le rayon de celui-ci à cause de l'accélération centrifuge qui est transmise aux molécules du fluide gazeux avec un apport énergétique minimal.Method for the transmission of heat energy, essentially characterized in that one or more sealed cylinders are arranged in series which rotate on bearings by means of the action of a motor, the cylinder or the set of cylinders having a tubular shaft capable of receiving a body which is capable of exchanging heat with a gaseous fluid situated near the latter inside the cylinder, this gaseous fluid being capable, with the centrifugal acceleration of said cylinder, of '' increase the speed and the temperature of its molecules towards the periphery of this cylinder by being able to carry out in said zone a heat exchange with another body external to the cylinder, thanks to the temperature gradient which is caused according to the radius of the latter because of the centrifugal acceleration which is transmitted to the molecules of the gaseous fluid with minimal energy input.
EP94200684A 1993-03-18 1994-03-16 Process for the transmission of heat energy. Withdrawn EP0616182A3 (en)

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
ES9300575 1993-03-18
ES09300575A ES2064274B1 (en) 1993-03-18 1993-03-18 PROCEDURE FOR THE TRANSMISSION OF HEAT ENERGY.

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EP0616182A2 true EP0616182A2 (en) 1994-09-21
EP0616182A3 EP0616182A3 (en) 1995-05-03

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006119946A1 (en) * 2005-05-09 2006-11-16 John Hugues Heat transfer using mobile atoms or molecules
US20100089550A1 (en) * 2007-02-14 2010-04-15 Heleos Technology Gmbh Process And Apparatus For Transferring Heat From A First Medium To A Second Medium

Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2158968A5 (en) * 1971-10-27 1973-06-15 Opfermann Adolf
DE3333642A1 (en) * 1983-03-15 1984-09-27 Helmut 2420 Eutin Krueger-Beuster Recuperative, annular heat exchanger

Family Cites Families (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3650319A (en) * 1970-04-24 1972-03-21 Monsanto Co Heat exchange device
GB1397184A (en) * 1972-02-15 1975-06-11 Commw Scient Ind Res Org Method and apparatus for transferring heat to or from material
EP0082310A3 (en) * 1981-12-17 1984-03-28 Combustion Engineering, Inc. Apparatus for heating and mixing high viscosity fluids
AU626519B2 (en) * 1987-12-28 1992-08-06 Henrik Ullum Device for heating and/or drying

Patent Citations (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2158968A5 (en) * 1971-10-27 1973-06-15 Opfermann Adolf
DE3333642A1 (en) * 1983-03-15 1984-09-27 Helmut 2420 Eutin Krueger-Beuster Recuperative, annular heat exchanger

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2006119946A1 (en) * 2005-05-09 2006-11-16 John Hugues Heat transfer using mobile atoms or molecules
US20100089550A1 (en) * 2007-02-14 2010-04-15 Heleos Technology Gmbh Process And Apparatus For Transferring Heat From A First Medium To A Second Medium
US9765994B2 (en) * 2007-02-14 2017-09-19 Heleos Technology Gmbh Process and apparatus for transferring heat from a first medium to a second medium

Also Published As

Publication number Publication date
ES2064274A2 (en) 1995-01-16
ES2064274R (en) 1997-06-16
ES2064274B1 (en) 1998-02-16
EP0616182A3 (en) 1995-05-03

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