FR2943410A1 - Procede de refroidissement de gaz a haute temperature et dispositif associe - Google Patents
Procede de refroidissement de gaz a haute temperature et dispositif associe Download PDFInfo
- Publication number
- FR2943410A1 FR2943410A1 FR0951837A FR0951837A FR2943410A1 FR 2943410 A1 FR2943410 A1 FR 2943410A1 FR 0951837 A FR0951837 A FR 0951837A FR 0951837 A FR0951837 A FR 0951837A FR 2943410 A1 FR2943410 A1 FR 2943410A1
- Authority
- FR
- France
- Prior art keywords
- gases
- liquid
- high temperature
- cooled
- vapors
- 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.)
- Granted
Links
- 239000007789 gas Substances 0.000 title claims abstract description 119
- 239000007788 liquid Substances 0.000 title claims abstract description 34
- 238000000034 method Methods 0.000 title claims abstract description 30
- 230000008016 vaporization Effects 0.000 title claims abstract description 16
- 238000009834 vaporization Methods 0.000 title claims abstract description 13
- 239000000112 cooling gas Substances 0.000 title abstract 2
- 239000006260 foam Substances 0.000 claims abstract description 19
- 238000001816 cooling Methods 0.000 claims abstract description 14
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 20
- 230000008569 process Effects 0.000 claims description 9
- 239000011148 porous material Substances 0.000 claims description 6
- 150000001875 compounds Chemical class 0.000 claims description 2
- 239000006262 metallic foam Substances 0.000 claims 1
- 239000007787 solid Substances 0.000 claims 1
- 229920000642 polymer Polymers 0.000 abstract description 4
- 239000008259 solid foam Substances 0.000 abstract description 3
- 230000015572 biosynthetic process Effects 0.000 abstract 1
- RMLFHPWPTXWZNJ-UHFFFAOYSA-N novec 1230 Chemical compound FC(F)(F)C(F)(F)C(=O)C(F)(C(F)(F)F)C(F)(F)F RMLFHPWPTXWZNJ-UHFFFAOYSA-N 0.000 abstract 1
- 238000003786 synthesis reaction Methods 0.000 abstract 1
- 239000003380 propellant Substances 0.000 description 13
- 239000002826 coolant Substances 0.000 description 9
- 239000000203 mixture Substances 0.000 description 9
- 239000000110 cooling liquid Substances 0.000 description 8
- 238000002485 combustion reaction Methods 0.000 description 7
- 239000004449 solid propellant Substances 0.000 description 5
- 230000008859 change Effects 0.000 description 4
- 239000000567 combustion gas Substances 0.000 description 3
- 229910004298 SiO 2 Inorganic materials 0.000 description 2
- 230000008901 benefit Effects 0.000 description 2
- 230000007123 defense Effects 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- GDDNTTHUKVNJRA-UHFFFAOYSA-N 3-bromo-3,3-difluoroprop-1-ene Chemical compound FC(F)(Br)C=C GDDNTTHUKVNJRA-UHFFFAOYSA-N 0.000 description 1
- 108010053481 Antifreeze Proteins Proteins 0.000 description 1
- 206010016275 Fear Diseases 0.000 description 1
- 241001606201 Patia Species 0.000 description 1
- 108010039491 Ricin Proteins 0.000 description 1
- 229910000831 Steel Inorganic materials 0.000 description 1
- 238000010521 absorption reaction Methods 0.000 description 1
- 239000000654 additive Substances 0.000 description 1
- 230000000996 additive effect Effects 0.000 description 1
- 230000002528 anti-freeze Effects 0.000 description 1
- 239000011230 binding agent Substances 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 238000009924 canning Methods 0.000 description 1
- 150000001768 cations Chemical class 0.000 description 1
- 239000002131 composite material Substances 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 125000002534 ethynyl group Chemical group [H]C#C* 0.000 description 1
- 238000009472 formulation Methods 0.000 description 1
- 239000011521 glass Substances 0.000 description 1
- 238000010348 incorporation Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- -1 naval Substances 0.000 description 1
- 239000002245 particle Substances 0.000 description 1
- 229920002635 polyurethane Polymers 0.000 description 1
- 239000004814 polyurethane Substances 0.000 description 1
- 230000001737 promoting effect Effects 0.000 description 1
- 230000009257 reactivity Effects 0.000 description 1
- 229920006395 saturated elastomer Polymers 0.000 description 1
- 238000004513 sizing Methods 0.000 description 1
- 239000010959 steel Substances 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F42—AMMUNITION; BLASTING
- F42B—EXPLOSIVE CHARGES, e.g. FOR BLASTING, FIREWORKS, AMMUNITION
- F42B3/00—Blasting cartridges, i.e. case and explosive
- F42B3/04—Blasting cartridges, i.e. case and explosive for producing gas under pressure
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F02—COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
- F02K—JET-PROPULSION PLANTS
- F02K9/00—Rocket-engine plants, i.e. plants carrying both fuel and oxidant therefor; Control thereof
- F02K9/42—Rocket-engine plants, i.e. plants carrying both fuel and oxidant therefor; Control thereof using liquid or gaseous propellants
- F02K9/44—Feeding propellants
- F02K9/50—Feeding propellants using pressurised fluid to pressurise the propellants
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
- F22B1/18—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
- F22B1/1838—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines the hot gas being under a high pressure, e.g. in chemical installations
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B1/00—Methods of steam generation characterised by form of heating method
- F22B1/02—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers
- F22B1/18—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines
- F22B1/1853—Methods of steam generation characterised by form of heating method by exploitation of the heat content of hot heat carriers the heat carrier being a hot gas, e.g. waste gas such as exhaust gas of internal-combustion engines coming in direct contact with water in bulk or in sprays
-
- 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
- F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
- F28D20/02—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat
- F28D20/021—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat the latent heat storage material and the heat-exchanging means being enclosed in one container
-
- 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
- F28D20/00—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00
- F28D20/02—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat
- F28D20/023—Heat storage plants or apparatus in general; Regenerative heat-exchange apparatus not covered by groups F28D17/00 or F28D19/00 using latent heat the latent heat storage material being enclosed in granular particles or dispersed in a porous, fibrous or cellular structure
Landscapes
- Engineering & Computer Science (AREA)
- General Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Mechanical Engineering (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
Abstract
Description
Claims (4)
- REVENDICATIONS1. Procédé de mise à disposition de gaz chauds (G") 5 comprenant - la génération de gaz à haute température (G); - le refroidissement desdits gaz à haute température (G) par échange de chaleur avec un liquide (L), ledit liquide (L) se vaporisant au moins en partie tandis que lesdits gaz à haute température (G) sont 10 refroidis ; et étant caractérisé en ce que les vapeurs (Lv) résultant de la vaporisation dudit liquide (L) sont au moins en partie additionnées aux gaz refroidis (G . 15
- 2. Procédé selon la revendication 1, caractérisé en ce que lesdits gaz à haute température (G) sont générés par au moins un générateur de gaz pyrotechnique (1).
- 3. Procédé selon la revendication 1 ou 2, caractérisé en ce que 20 ledit liquide (L) est choisi parmi l'eau, le composé de formule CF3CF2C(0)CF(CF3)2 et les hydrofluoroéthers.
- 4. Procédé selon l'une quelconque des revendications 1 à 3, caractérisé en ce que ledit liquide (L) est inclus dans les pores d'une 25 mousse solide métallique ou dans les pores d'une mousse polymérique de synthèse hydrophile, (8). rocéde selon :une quelconque des rendications 1 caractérisé en ce qu'Il est mis en oeuvre pour aiimciiiter en gaz chauds un systeme lie poussée et de correction de rariecu.Dire d'un missile main 9o,, alimenter en gaz chauds unv -uri.ian pour gonfler une structure gonflable déployable ou i'Dour pi ssunser un 1 mini 35 Dispositif mis. 3posi,ii ri., haucis -Dunant la mise en if Livre dLI procédé selon i 'une quelconque Crevendications 1 à 5, caractérisé en qu'il comprend - des moyens (1) pour générer des gaz à haute température (G) ; - au moins un échangeur de chaleur (10), renfermant un liquide (L), alimenté en lesdits gaz à haute température (G), au sein duquel lesdits gaz (G) sont refroidis par vaporisation dudit liquide (L), ledit échangeur (10) débitant les gaz refroidis (G'), d'une part et des vapeurs (Lv) résultant de ladite vaporisation dudit liquide (L), d'autre part - des moyens (13), en sortie dudit échangeur (10), pour additionner auxdits gaz refroidis (G') au moins une partie desdites vapeurs (Lv) ; et - des moyens (111) pour délivrer les gaz chauds (G") constitués desdits gaz refroidis (G') additionnés d'au moins une partie desdites vapeurs (Lv) à un système utilisateur (14,15) desdits gaz chauds (G"). 7. Dispositif selon la revendication 6, caractérisé en ce que ledit au moins un échangeur de chaleur (10) est alimenté en lesdits gaz à haute température (G) via au moins une première canalisation (6) et en ce qu'il débite lesdits gaz refroidis (G') et lesdites vapeurs (Lv) via respectivement au moins une seconde canalisation (11) et au moins une troisième canalisation (12) ; ladite troisième canalisation (12) ou au moins une desdites troisièmes canalisations débouchant dans ladite seconde canalisation (11) ou dans au moins une desdites secondes canalisations. 8. Dispositif selon la revendication 6 ou 7, caractérisé en ce que lesdits moyens (1) pour générer des gaz à haute température (G) 25 consistent en au moins un générateur pyrotechnique (1). 9. Dispositif selon l'une quelconque des eyindicatio 6 à 8, caracterise ce que iesdits moyens pour générer des gaz à haute teMpéHtLli-e SOrlt J(Tl 'flac e5 u S'elrl dudit au moins éChii3r1geUr de chaleur. 10. Dispositif selon l'une quelconque des revendications 6 a dit un Ci id r11. Dispositif selon l'une quelconque des revendications 6 à 10, caractérisé en ce que ledit système utilisateur est choisi parmi un système de poussée et/ou de correction de trajectoire d'un missile ou d'un engin spacial, une turbine (14), une structure gonflable déployable ou un réservoir (15), éventuellement muni de tuyères (16).
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR0951837A FR2943410B1 (fr) | 2009-03-23 | 2009-03-23 | Procede de refroidissement de gaz a haute temperature et dispositif associe |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
FR0951837A FR2943410B1 (fr) | 2009-03-23 | 2009-03-23 | Procede de refroidissement de gaz a haute temperature et dispositif associe |
Publications (2)
Publication Number | Publication Date |
---|---|
FR2943410A1 true FR2943410A1 (fr) | 2010-09-24 |
FR2943410B1 FR2943410B1 (fr) | 2012-04-20 |
Family
ID=41258817
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
FR0951837A Active FR2943410B1 (fr) | 2009-03-23 | 2009-03-23 | Procede de refroidissement de gaz a haute temperature et dispositif associe |
Country Status (1)
Country | Link |
---|---|
FR (1) | FR2943410B1 (fr) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109630314A (zh) * | 2018-12-13 | 2019-04-16 | 西安航天动力研究所 | 一种吸气式发动机冷启动系统及冷启动方法 |
FR3131772A1 (fr) * | 2022-01-07 | 2023-07-14 | Commissariat A L'energie Atomique Et Aux Energies Alternatives | Ensemble modulaire de stockage thermique a matériau a changement de phase, dont la fabrication est simplifiée |
Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1208162A (en) * | 1967-01-09 | 1970-10-07 | Rocket Research Corp | Improvements in or relating to the generation of cool working fluids |
US3719054A (en) * | 1970-08-24 | 1973-03-06 | Rocket Research Corp | Liquefied gas vaporizer attachment for a pressure bottle |
US4108241A (en) * | 1975-03-19 | 1978-08-22 | The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration | Heat exchanger and method of making |
EP0773349A1 (fr) * | 1995-11-10 | 1997-05-14 | Asea Brown Boveri Ag | Refroidisseur d'air de refroidissement pour centrales |
DE19726296A1 (de) * | 1997-06-20 | 1998-12-24 | Temic Bayern Chem Airbag Gmbh | Gasgenerator mit Kühlvorrichtung |
DE19730674A1 (de) * | 1997-07-17 | 1999-01-21 | Deutsch Zentr Luft & Raumfahrt | Brennkammer und Verfahren zur Herstellung einer Brennkammer |
WO2005057119A1 (fr) * | 2003-12-08 | 2005-06-23 | The Boeing Company | Echangeur de chaleur a changement de phase |
-
2009
- 2009-03-23 FR FR0951837A patent/FR2943410B1/fr active Active
Patent Citations (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
GB1208162A (en) * | 1967-01-09 | 1970-10-07 | Rocket Research Corp | Improvements in or relating to the generation of cool working fluids |
US3719054A (en) * | 1970-08-24 | 1973-03-06 | Rocket Research Corp | Liquefied gas vaporizer attachment for a pressure bottle |
US4108241A (en) * | 1975-03-19 | 1978-08-22 | The United States Of America As Represented By The Administrator Of The National Aeronautics And Space Administration | Heat exchanger and method of making |
EP0773349A1 (fr) * | 1995-11-10 | 1997-05-14 | Asea Brown Boveri Ag | Refroidisseur d'air de refroidissement pour centrales |
DE19726296A1 (de) * | 1997-06-20 | 1998-12-24 | Temic Bayern Chem Airbag Gmbh | Gasgenerator mit Kühlvorrichtung |
DE19730674A1 (de) * | 1997-07-17 | 1999-01-21 | Deutsch Zentr Luft & Raumfahrt | Brennkammer und Verfahren zur Herstellung einer Brennkammer |
WO2005057119A1 (fr) * | 2003-12-08 | 2005-06-23 | The Boeing Company | Echangeur de chaleur a changement de phase |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN109630314A (zh) * | 2018-12-13 | 2019-04-16 | 西安航天动力研究所 | 一种吸气式发动机冷启动系统及冷启动方法 |
FR3131772A1 (fr) * | 2022-01-07 | 2023-07-14 | Commissariat A L'energie Atomique Et Aux Energies Alternatives | Ensemble modulaire de stockage thermique a matériau a changement de phase, dont la fabrication est simplifiée |
EP4212814A1 (fr) * | 2022-01-07 | 2023-07-19 | Commissariat à l'énergie atomique et aux énergies alternatives | Ensemble modulaire de stockage thermique a matériau a changement de phase, dont la fabrication est simplifiée |
Also Published As
Publication number | Publication date |
---|---|
FR2943410B1 (fr) | 2012-04-20 |
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Effective date: 20130213 |
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Owner name: HERAKLES, FR Effective date: 20130213 |
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Owner name: ARIANEGROUP SAS, FR Effective date: 20180724 |
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