FR2762873A1 - Thermal engine utilising latent energy - Google Patents
Thermal engine utilising latent energy Download PDFInfo
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- FR2762873A1 FR2762873A1 FR9705488A FR9705488A FR2762873A1 FR 2762873 A1 FR2762873 A1 FR 2762873A1 FR 9705488 A FR9705488 A FR 9705488A FR 9705488 A FR9705488 A FR 9705488A FR 2762873 A1 FR2762873 A1 FR 2762873A1
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- air
- circuit
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- engine
- heat
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Links
- 230000006835 compression Effects 0.000 claims abstract description 4
- 238000007906 compression Methods 0.000 claims abstract description 4
- 238000002347 injection Methods 0.000 claims abstract 2
- 239000007924 injection Substances 0.000 claims abstract 2
- 238000011084 recovery Methods 0.000 claims description 3
- 239000002274 desiccant Substances 0.000 claims description 2
- 230000000977 initiatory effect Effects 0.000 claims 1
- 230000018044 dehydration Effects 0.000 abstract 1
- 238000006297 dehydration reaction Methods 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 7
- 230000008901 benefit Effects 0.000 description 5
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 4
- RAHZWNYVWXNFOC-UHFFFAOYSA-N Sulphur dioxide Chemical compound O=S=O RAHZWNYVWXNFOC-UHFFFAOYSA-N 0.000 description 4
- HEMHJVSKTPXQMS-UHFFFAOYSA-M Sodium hydroxide Chemical compound [OH-].[Na+] HEMHJVSKTPXQMS-UHFFFAOYSA-M 0.000 description 3
- 238000011282 treatment Methods 0.000 description 3
- 238000011144 upstream manufacturing Methods 0.000 description 3
- 235000008733 Citrus aurantifolia Nutrition 0.000 description 2
- 235000011941 Tilia x europaea Nutrition 0.000 description 2
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 2
- 238000002485 combustion reaction Methods 0.000 description 2
- 238000005336 cracking Methods 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- 239000004571 lime Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 229910052757 nitrogen Inorganic materials 0.000 description 2
- 229910052760 oxygen Inorganic materials 0.000 description 2
- 239000001301 oxygen Substances 0.000 description 2
- 238000004064 recycling Methods 0.000 description 2
- 239000002351 wastewater Substances 0.000 description 2
- 241000273930 Brevoortia tyrannus Species 0.000 description 1
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 238000004378 air conditioning Methods 0.000 description 1
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 1
- 229910052782 aluminium Inorganic materials 0.000 description 1
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 239000003638 chemical reducing agent Substances 0.000 description 1
- 239000000460 chlorine Substances 0.000 description 1
- 229910052801 chlorine Inorganic materials 0.000 description 1
- 230000000295 complement effect Effects 0.000 description 1
- 125000004122 cyclic group Chemical group 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 239000010791 domestic waste Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000002349 favourable effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000000446 fuel Substances 0.000 description 1
- 230000010354 integration Effects 0.000 description 1
- 238000012423 maintenance Methods 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 230000008018 melting Effects 0.000 description 1
- 238000002844 melting Methods 0.000 description 1
- 239000003507 refrigerant Substances 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000003786 synthesis reaction Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C1/00—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid
- F02C1/04—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid the working fluid being heated indirectly
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C1/00—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid
- F02C1/04—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid the working fluid being heated indirectly
- F02C1/05—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid the working fluid being heated indirectly characterised by the type or source of heat, e.g. using nuclear or solar energy
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02C—GAS-TURBINE PLANTS; AIR INTAKES FOR JET-PROPULSION PLANTS; CONTROLLING FUEL SUPPLY IN AIR-BREATHING JET-PROPULSION PLANTS
- F02C1/00—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid
- F02C1/04—Gas-turbine plants characterised by the use of hot gases or unheated pressurised gases, as the working fluid the working fluid being heated indirectly
- F02C1/10—Closed cycles
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
- F05D—INDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
- F05D2220/00—Application
- F05D2220/60—Application making use of surplus or waste energy
- F05D2220/62—Application making use of surplus or waste energy with energy recovery turbines
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F05—INDEXING SCHEMES RELATING TO ENGINES OR PUMPS IN VARIOUS SUBCLASSES OF CLASSES F01-F04
- F05D—INDEXING SCHEME FOR ASPECTS RELATING TO NON-POSITIVE-DISPLACEMENT MACHINES OR ENGINES, GAS-TURBINES OR JET-PROPULSION PLANTS
- F05D2260/00—Function
- F05D2260/60—Fluid transfer
- F05D2260/601—Fluid transfer using an ejector or a jet pump
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Life Sciences & Earth Sciences (AREA)
- High Energy & Nuclear Physics (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Abstract
Description
-1- La présente invention concerne un moteur thermique dont l'équivalent-1- The present invention relates to a heat engine whose equivalent
combustible n'est autre que des énergies dites dégradées réputées perdues bien, qu'utilisées selon les températures disponibles, appliquées, de manière favorable et graduelle à différents niveaux fuel is none other than so-called degraded energies deemed to be lost well, only used according to available temperatures, applied in a favorable and gradual manner at different levels
du circuit complexe réalisé.of the complex circuit carried out.
Ce moteur se présente sous la forme d'un circuit hermétique contenant de l'air déshydraté par un moyen tel que la soude ou toutes substances anhydres similaires aux fins d'éviter toutes formes de givrage qui seraient dommageables.au niveau de la turbine de détente. Au sein du circuit, notamment depuis la turbine, ce moteur se caractérise par quatre zones o les pressions et températures évoluent en paliers sélectifs au gré des énergies à This motor is in the form of an airtight circuit containing air dehydrated by a means such as sodium hydroxide or any similar anhydrous substances in order to avoid any form of icing which would be harmful. At the level of the expansion turbine . Within the circuit, notably from the turbine, this engine is characterized by four zones where the pressures and temperatures change in selective stages according to the energies at
rentabiliser fussent elles molles bien que traduites sur des échangeurs adaptés. make money even if they are soft although translated on suitable exchangers.
Le compresseur (1) exerce une pression motrice au sein du circuit. Il prélève. 2/9 de la masse d'air véhiculé par la turbine et, son débit emprunte deux branches distinctes avec chacune 1/9 de telle sorte, que chaque tronçon Y concerné du circuit y trouve ses The compressor (1) exerts a driving pressure within the circuit. He samples. 2/9 of the mass of air carried by the turbine and, its flow borrows two distinct branches with each 1/9 so that each concerned section Y of the circuit finds its
Conditions.Conditions.
La valeur de 6,b4 se veut pratique en soi d'ou 6b,4 réalisés par le compresseur (1) en (12) et (13) À ',6 en amont de la tuyère(2) - Détente 91,47 cp.-t o 20.0ib,4 en aval de la turbine (3) avec travail sur l'arbre l '.0 au niveau du mélange régénéré à 760rnm Hg + O ' En référence au dessin annexé, notons les étapes en ce qui caractérise la récupération de la chaleur de compression intégrée aux divers apports l'injecteur (6) induit l'air en (5) The value of 6, b4 is intended to be practical in itself or 6b, 4 produced by the compressor (1) in (12) and (13) À ', 6 upstream of the nozzle (2) - Trigger 91.47 cp .-to 20.0ib, 4 downstream of the turbine (3) with work on the shaft the .0 at the level of the regenerated mixture at 760rnm Hg + O 'With reference to the attached drawing, note the steps in which characterizes the recovery of the compression heat integrated into the various inputs the injector (6) induces the air in (5)
îour le conditionner au stade (4).îour condition it at stage (4).
L'injecteur (7) recrée à + 0 O au mélange la pression dite atmosphérique en (1) et (5). The injector (7) recreates at + 0 O the mixture the so-called atmospheric pressure in (1) and (5).
Léchangeur (8) récupère en parité, les sources tièdes Air - Eau. L'Echangeur (9) peut convenir d'apport solaire dans la fourchette et selon, du stock disponible sur réfractaire The exchanger (8) recovers in parity, the warm Air - Water sources. The heat exchanger (9) can agree on solar gain in the range and depending on the stock available on the refractory
chargé de jour ou nuit,l'échangeur (10) bénéficie de chaleur latente voire de fimées. charged day or night, the exchanger (10) benefits from latent heat or even fimes.
La boucle de transfert (14) imprime un dtode (13) à (5);la Puissance disponible sur The transfer loop (14) prints a dtode (13) to (5); the Power available on
l'arbre est amputée du besoin propre au compresseur (1) en régime établi, via transmission. the shaft is reduced by the specific need of the compressor (1) in steady state, via transmission.
Les manomètres (16) (17) (18) affichent les pressions aux différents stades du circuit. The pressure gauges (16) (17) (18) display the pressures at the various stages of the circuit.
Entraînement magnétique (15).Magnetic drive (15).
L'Echangeur (1 9) permet d'exporter de la criogénie.; l'échangeur (20) soit, de l'eau glacée ou de la climatisation. Les piquages (21) et (22) relient la cartouche deshydratante The Exchanger (1 9) allows to export criogenie .; the exchanger (20) either, chilled water or air conditioning. The nozzles (21) and (22) connect the desiccant cartridge
(23) avec sécurité quart de tour lors des opérations. (23) with quarter turn safety during operations.
3.5 La pompe à bras ou motorisée assure le transfert de l'air à deshydtrater (24) avec contrôle -lygromnétique (25). Ainsi constitué, le moteur thermique peui répondrc ài des gammes de puissances qui, du kilowatt peut convenir de plusieurs mégawatts. La vitesse 3.5 The arm or motorized pump ensures the transfer of the air to be dehydrated (24) with -lygromnetic control (25). Thus constituted, the internal combustion engine can respond to ranges of powers which, per kilowatt can be suitable for several megawatts. Speed
d'écoulement de l'air étant liée aux sections et pertes de charges compatibles. of air flow being linked to compatible sections and pressure drops.
Dans le cadre de besoins importants, il peut y avoir prélèvement de chaleur latente au In case of significant needs, there may be latent heat withdrawal at the
seio de condenseurs.De même, qu'il peut y avoir une solution plus radicale et cyclique dont. seio of condensers. Similarly, that there may be a more radical and cyclical solution of which.
fait état la figure 2.: Pour satisfaire un fort apport au niveau de l'échangeur (10) voire 110 avec en cela bonus au plan rendement,la Turbine (3) produit en cela plus pour une même consommation shows figure 2 .: To satisfy a strong contribution at the level of the exchanger (10) or even 110 with in this bonus in terms of efficiency, the Turbine (3) produces in this more for the same consumption
du compresseur (1) avec toutefois une production criogénique moindre à l'échangeur (19). of the compressor (1) with, however, less cryogenic production at the exchanger (19).
Tel peut s'élaborer un cycle autoproducteur Fg. 2. La chaudière (26) évacue ses fumées vers le réducteur (27). En amont de (10) règne une température apte à procéder a la condensation de l'eau alors qu'au niveau chaudière, une part de recyclage évite le point de rosée. Dè: lors, Avant le Four (28) il y a séparation de H20 et N2 T de sorte que, le contre-échange -2 - s'opère entre CaO et C03Ca (29). L'apport de la résistance (30) réalise l'appoint en (28) a la sortie du Four, le CO2 est induit par la vapctir d'caut au niveau de (31) Synthétiscur a haute température En (3 1) l'aluminium vaporise procède à la séparation des composants par crackage Les échangeurs (32) (35) (37) apportent un plus au profit de (10). La résistance (33) assure la fonte de l'alumine ce qui permet d'évacuer les moles 02, d'en prélever la chaleur avant Such can be a self-producing cycle Fg. 2. The boiler (26) evacuates its fumes to the reducer (27). Upstream of (10) there is a temperature capable of condensing the water, while at the boiler level, a portion of recycling avoids the dew point. Therefore: Before the Oven (28) there is separation of H20 and N2 T so that the counter-exchange -2 - takes place between CaO and C03Ca (29). The contribution of the resistance (30) realizes the addition in (28) at the exit of the Oven, the CO2 is induced by the vapor of carbon at (31) Synthétiscur at high temperature In (3 1) the aluminum vaporized separates the components by cracking The heat exchangers (32) (35) (37) provide a plus for (10). The resistance (33) ensures the melting of the alumina which allows the moles 02 to be evacuated and the heat to be removed before
compression (36).compression (36).
Ainsi, le séparateur (34) assure le recyclage par impulsion des môles Al2 au sein de (31). Les cycles opèrent séparément et de manière complémentaire ils assurent l'appoint aux plages impliquées par les apports (8) (14) (9) (12) d'ou de 60 voire moins au cas, 110 se Thus, the separator (34) ensures the pulse recycling of the Al2 moles within (31). The cycles operate separately and in a complementary manner they provide the support to the ranges involved by the contributions (8) (14) (9) (12) from or from 60 or even less in the case, 110
peut.can.
Le moteur accepte de fait, les' énergies molles et peut tendre bien au delà ce qui, présente un large éventail propre à satisfaire nombre de besoins spécifiques de l'industrie au sens le plus large ramifié sans négliger l'agriculture, EDF, l'incinération, Xi, Raffinerie automobile. Le moteur se situe à la demande en fonction de la pression et de la température sollicitée en tous les domaines d'applications voire, par module en valeur de puissances normalisées ou adaptées selon cas. A noter que point n'est besoin de produire de la vapeur The engine accepts in fact, the soft energies and can tend well beyond which, presents a wide range suitable to satisfy number of specific needs of the industry in the widest branched sense without neglecting agriculture, EDF, the cremation, Xi, car refinery. The motor is located on demand as a function of the pressure and temperature required in all areas of application, even, by module, in terms of power values standardized or adapted as appropriate. Note that there is no need to produce steam
(26) ne pas associer le moteur thermique à ces apports serait erreur. (26) not associating the heat engine with these contributions would be an error.
De quelques natures qu'ils soient, l'intégration de la Fig. 2 aux apports définis, entre dans le cadre du Brevet d'invention outrc qu'il raille définir Ic mode ie lancemcnt du cycle et ponctuer l'intérêt économique qui découle du dispositif sans lequel, certaines formes de Whatever natures they may be, the integration of FIG. 2 to the defined contributions, falls within the scope of the Invention patent outrc that it mocks to define the mode ie launching of the cycle and punctuating the economic interest which results from the device without which, certain forms of
procés es seraient vaines.trials would be in vain.
Le lancement du moteur peut s'effectuer avec une réserve d'air comprimé opérant sur un cyclone à deux entrées tangentielles opposées pour actionner une turbine centrifuge dont l'axe embrayé, entraîne alors le compresseur ( I) au régime qui convient des besoins The engine can be started with a reserve of compressed air operating on a cyclone with two opposite tangential inputs to actuate a centrifugal turbine whose axis engaged, then drives the compressor (I) at the speed that suits the needs
d'équilibre propre au cycle.of balance proper to the cycle.
Précisons certaines formesde pourcentages dont le cycle se réfère Partie (4) = 9, en amont pour 8 en (5) et I o s'appliquent les branches (12) et (13) aux pressions définies au terme de ce qui suit et des différents stades d'équilibre [ (1 x 6,4) + (8x])] /9 = b,6 ndiqué en page I puis à l'équilibre pressions [ (9x0,4) + (lx 6,4)] /10= I (760 Hg) & O,4 en (3) Les sources de chaleurs en la Fig. I se réfèrent de + 0 en (1 1) et de 10 C après (20) pour un dt. 6 87 en (8) apport de 12 97 par (14) et 15 19 en (12). Reste à fournir en (10) 16 84 pour convenir de 60 (option). La Fig. 2 assure les 16 84 Nous mémorisons là, les fonctions successives qui sollicitent pour les fumées, l'opération chaux et celle de l'aluminothermie. CO2 & 2H20 étant cyclique dans le cadre CH4 par crackage des composants et récupérations précieuses de l'oxygène et du nitrogène Let us specify certain forms of percentages whose cycle refers Part (4) = 9, upstream for 8 in (5) and I o apply the branches (12) and (13) to the pressures defined at the end of what follows and different stages of equilibrium [(1 x 6.4) + (8x])] / 9 = b, 6 ndicated on page I then at pressure equilibrium [(9x0.4) + (lx 6.4)] / 10 = I (760 Hg) & O, 4 in (3) The heat sources in Fig. I refer to + 0 in (1 1) and to 10 C after (20) for a dt. 6 87 in (8) contribution of 12 97 by (14) and 15 19 in (12). Still to be provided in (10) 16 84 to agree on 60 (optional). Fig. 2 ensures the 16 84 We memorize there, the successive functions which request for the fumes, the lime operation and that of the aluminothermy. CO2 & 2H20 being cyclic in the CH4 framework by cracking of the components and precious recoveries of oxygen and nitrogen
Chaleurs en prime.Bonus heat.
Il faut certes en application industrielle convenir de réfractaire classe 1 70+ pour satie.- It is certainly necessary in industrial application to agree to refractory class 1 70+ for satie.-
faire 1800 C/AL. L'eau iss de CD3'a nécessite certes, un traitoemt le CD2 se veut dis- ponible quand à lui à 1(00 C. Notns qu'aprês l'action de (29) - (30) et (33) nie prélèvent gère. L'incidence de (32) (35) et (37) supplée largement outre, le coût de compression de l'oxygène commercialisable ce qui souligne l'intérêt d'avoir abordé des domaines communs make 1800 C / AL. The water iss of CD3'a certainly requires, a treatment CD2 wants to be available when it at 1 (00 C. Notns that after the action of (29) - (30) and (33) denies withdraw The incidence of (32) (35) and (37) more than makes up for the cost of compressing marketable oxygen, which underlines the advantage of having addressed common areas.
4,s qui régissent tout à la fois î'ENERGIE - L'EAU - L'ECONOMIE - L'EMPLOI - 4, s which govern at the same time ENERGY - WATER - ECONOMY - EMPLOYMENT -
L'ECOLOGIE avec projection sur l'Avenir Au plan des applications, elles sont significatives Le moteur thermique dans le cadre d'un Navire peut d'évidence réaliser 13 32 au niveau de (8) ce qui accorde 400 d'acquis en -3 - (4) reste à fournir pour 60 final - ou CAS-- 50 d'ou: 105 63 x 0,24 x xT /0,6 x 860.103 ECOLOGY with projection on the Future In terms of applications, they are significant The heat engine in the context of a Vessel can obviously achieve 13 32 at (8) which grants 400 of acquired in -3 - (4) remains to be provided for 60 final - or CAS - 50 hence: 105 63 x 0.24 x xT / 0.6 x 860.103
= 1MW et 56T - d'air.= 1MW and 56T - air.
Il n'en coûte que 20 % d'évidence, gratuits dt 10 o en (10) dans le cadre de la Fig. 2- Reste à se délester d'un dt de 53 ,4 dans le sillage en (19)Le tout à situer dans le cadre de la Puissance à mettre en oeuvre tant en place de soutes, le volume est disponible pour les matériels. L'avantage réside en Pollution Zéro - Devises économisées & Travail rentabilisé. Au "ilan Agricole, le prélèvement d'Eau sur l'Air se veut précieux (19) il suffit de prévoir et de stocker tout en exportant les MW vers EDF avec en prime, rentabilisation des eaux usées à It costs only 20% evidence, free from 10 o in (10) in the context of Fig. 2- It remains to offload a dt of 53, 4 in the wake in (19) All to be located in the context of the Power to be implemented both in place of bunkers, the volume is available for equipment. The advantage lies in Zero Pollution - Currencies saved & Work profitable. At "Ilan Agricole, the water withdrawal from the air is precious (19) it is enough to plan and store while exporting the MW to EDF with the bonus, profitability of wastewater to
distiller.distill.
Il n'en coûte que la maintenance rentabilisée, si l'on dispose de chaleurs latentes négligées. Dès lors, le Moteur thermique s'implique en tout y compris le traitement des déchets ménagers à vocation combustible de fait à coefficient à large Bonus assuré. Dans l'esprit de la Figure 2, la chaudière (26) peut être substituée par un incinérateur avec en ce cas une sélection densimétrique impérative en chaîne d'autant qu'en place de C02 à la sortie du four (28). Il peut y avoir des composants multiples notamment: de l'Anhydrique sulfureux d=-2, 86 - du Chlore d=2,4 à 0 /760 mm Hg d'ou 1 ère sélection basse pour en partie haute,disposer de l'Azote d=1,251 et l'anydhride carbonique d=1, 964. Le dispositif implique une régulation électronique pour convenir des variations20 volumétriques. La Finalité étant de réaliser la synthèse de CH4 à partir de C02 et 2H20 avec et toujours les chaleurs résiduelles au profit de l'échangeur (10). Pour les autres produits: SO2. cl.N2 et air, ils sont à prélever avec le souci lié à l'aspect anti- pollution et à rentahbilier. Au plan des Eaux usées à retraiter dans le cadre de l'économie qui s'impose. La figure It only costs profitable maintenance, if you have neglected latent heat. From then on, the internal combustion engine is involved in everything including the treatment of household waste for combustible purposes, with a large bonus. In the spirit of FIG. 2, the boiler (26) can be replaced by an incinerator with in this case an imperative densimetric selection in a chain as much as in place of C02 at the outlet of the oven (28). There may be multiple components in particular: sulfur dioxide d = -2, 86 - chlorine d = 2.4 to 0/760 mm Hg or 1 st low selection for the upper part, have the Nitrogen d = 1,251 and the carbonic anydhride d = 1,964. The device involves electronic regulation to agree on volumetric variations. The purpose is to carry out the synthesis of CH4 from C02 and 2H20 with and always the residual heat for the benefit of the exchanger (10). For other products: SO2. cl.N2 and air, they are to be taken with the concern related to the anti-pollution aspect and to rentahbilier. In terms of wastewater to be reprocessed in the context of the required economy. The figure
3 souligne que l'opération tend à satisfaire l'Echangeur (10). Plus on distille, la production de mégawatts augmente d'autant d'ou mixité à convenir avec les traitements actuels. 3 emphasizes that the operation tends to satisfy the Exchanger (10). The more we distill, the production of megawatts increases by as much or mixed to be agreed with current treatments.
En ce cas, le circuit à considérer implique successivement: Décantation Filtrage (38) avant Caisse (39) o puise la Pompe qui assure l'alimentation du Bouilleur (40) assisté de la résistance (41) Chasse prévue en (42). L'eau distillé produite emprunte le Condenseur (43)30 L'Echangeur (44) opère en économiseur. Vient alors le circuit réfrigérant (45) qui peut solliciter avec proximité,-un apport de chaleur latente EDF Le Tout au profit de l'échangeur (10) du moteur avide de toutes formes d'apports à rentabiliser.Emplois obligent. La liquéfaction du CO2 n'est pas à exclure d'ou, en la Figure 3 une variante utilise des In this case, the circuit to be considered successively involves: Decanting Filtering (38) before Box (39) o draws the Pump which ensures the supply of the Boiler (40) assisted by the resistance (41) Hunting provided in (42). The distilled water produced borrows the Condenser (43). The Exchanger (44) operates as an economizer. Then comes the refrigerant circuit (45) which can solicit nearby, -an EDF latent heat supply All for the benefit of the exchanger (10) of the engine eager for all forms of contributions to be profitable. Jobs require. CO2 liquefaction cannot be excluded from where, in Figure 3 a variant uses
matériels référencés Fig.2avecpour effet, limiter la pollution et disposer d'une chaleur additionnelle issue du Cycle Chaux. materials referenced in Fig. 2 with the effect of limiting pollution and having additional heat from the Lime Cycle.
- 4 -- 4 -
Claims (1)
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR9705488A FR2762873B1 (en) | 1997-05-02 | 1997-05-02 | HEAT ENGINE USING LOST ENERGIES |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| FR9705488A FR2762873B1 (en) | 1997-05-02 | 1997-05-02 | HEAT ENGINE USING LOST ENERGIES |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| FR2762873A1 true FR2762873A1 (en) | 1998-11-06 |
| FR2762873B1 FR2762873B1 (en) | 1999-08-13 |
Family
ID=9506571
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| FR9705488A Expired - Fee Related FR2762873B1 (en) | 1997-05-02 | 1997-05-02 | HEAT ENGINE USING LOST ENERGIES |
Country Status (1)
| Country | Link |
|---|---|
| FR (1) | FR2762873B1 (en) |
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000060226A1 (en) * | 1999-04-06 | 2000-10-12 | Branko Stankovic | Brayton or brayton-rankine combined cycle with hot-gas recirculation and inverse mixing ejector |
| FR2793523A1 (en) * | 1999-05-12 | 2000-11-17 | Andre Lapaix | Power plant generating electrical energy and comprising turbo-alternator means |
| RU2583191C1 (en) * | 2014-12-22 | 2016-05-10 | Федеральное государственное унитарное предприятие "Государственный космический научно-производственный центр имени М.В. Хруничева" | Space power plant with machine energy conversion |
| ES2891374A1 (en) * | 2021-07-16 | 2022-01-27 | Univ Nacional De Educacion A Distancia Uned | SYSTEM AND PROCEDURE FOR DECOUPLING THE CONSUMPTION AND PRODUCTION OF MECHANICAL ENERGY IN THERMODYNAMIC POWER CYCLES (Machine-translation by Google Translate, not legally binding) |
Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR1434435A (en) * | 1965-03-08 | 1966-04-08 | Fleur Corp | Turbomachinery set |
| US4135361A (en) * | 1976-10-26 | 1979-01-23 | The Charles Stark Draper Laboratory, Inc. | Self-contained heat generating system |
| US4221115A (en) * | 1978-01-23 | 1980-09-09 | Kraus Robert A | Altitude gas pressure differential power plant |
| US4372113A (en) * | 1981-01-15 | 1983-02-08 | Ramer James L | Pipeline energy recapture device |
| US4727930A (en) * | 1981-08-17 | 1988-03-01 | The Board Of Regents Of The University Of Washington | Heat transfer and storage system |
| FR2653356A1 (en) * | 1989-10-25 | 1991-04-26 | Mathis Alain | Device for dehydration of air with deliquescent desiccator product cartridges |
| WO1997001021A1 (en) * | 1995-06-23 | 1997-01-09 | Kong, Dexing | Method and apparatus for generating power from low temperature source |
-
1997
- 1997-05-02 FR FR9705488A patent/FR2762873B1/en not_active Expired - Fee Related
Patent Citations (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| FR1434435A (en) * | 1965-03-08 | 1966-04-08 | Fleur Corp | Turbomachinery set |
| US4135361A (en) * | 1976-10-26 | 1979-01-23 | The Charles Stark Draper Laboratory, Inc. | Self-contained heat generating system |
| US4221115A (en) * | 1978-01-23 | 1980-09-09 | Kraus Robert A | Altitude gas pressure differential power plant |
| US4372113A (en) * | 1981-01-15 | 1983-02-08 | Ramer James L | Pipeline energy recapture device |
| US4727930A (en) * | 1981-08-17 | 1988-03-01 | The Board Of Regents Of The University Of Washington | Heat transfer and storage system |
| FR2653356A1 (en) * | 1989-10-25 | 1991-04-26 | Mathis Alain | Device for dehydration of air with deliquescent desiccator product cartridges |
| WO1997001021A1 (en) * | 1995-06-23 | 1997-01-09 | Kong, Dexing | Method and apparatus for generating power from low temperature source |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| WO2000060226A1 (en) * | 1999-04-06 | 2000-10-12 | Branko Stankovic | Brayton or brayton-rankine combined cycle with hot-gas recirculation and inverse mixing ejector |
| FR2793523A1 (en) * | 1999-05-12 | 2000-11-17 | Andre Lapaix | Power plant generating electrical energy and comprising turbo-alternator means |
| WO2000070212A1 (en) * | 1999-05-12 | 2000-11-23 | Lapaix Andre | Power plant generating electrical energy and comprising turbo-alternator means |
| RU2583191C1 (en) * | 2014-12-22 | 2016-05-10 | Федеральное государственное унитарное предприятие "Государственный космический научно-производственный центр имени М.В. Хруничева" | Space power plant with machine energy conversion |
| ES2891374A1 (en) * | 2021-07-16 | 2022-01-27 | Univ Nacional De Educacion A Distancia Uned | SYSTEM AND PROCEDURE FOR DECOUPLING THE CONSUMPTION AND PRODUCTION OF MECHANICAL ENERGY IN THERMODYNAMIC POWER CYCLES (Machine-translation by Google Translate, not legally binding) |
Also Published As
| Publication number | Publication date |
|---|---|
| FR2762873B1 (en) | 1999-08-13 |
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