EP0474622B1 - Procédé pour démarrer un système échangeur de chaleur pour produire de la vapeur et système échangeur de chaleur pour produire de la vapeur - Google Patents
Procédé pour démarrer un système échangeur de chaleur pour produire de la vapeur et système échangeur de chaleur pour produire de la vapeur Download PDFInfo
- Publication number
- EP0474622B1 EP0474622B1 EP91890180A EP91890180A EP0474622B1 EP 0474622 B1 EP0474622 B1 EP 0474622B1 EP 91890180 A EP91890180 A EP 91890180A EP 91890180 A EP91890180 A EP 91890180A EP 0474622 B1 EP0474622 B1 EP 0474622B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- heat exchanger
- starting
- hot gas
- exchanger system
- steam
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F28—HEAT EXCHANGE IN GENERAL
- F28F—DETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
- F28F27/00—Control arrangements or safety devices specially adapted for heat-exchange or heat-transfer apparatus
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B35/00—Control systems for steam boilers
- F22B35/007—Control systems for waste heat boilers
-
- 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
- F22B1/1807—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 using the exhaust gases of combustion engines
- F22B1/1815—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 using the exhaust gases of combustion engines using the exhaust gases of gas-turbines
Definitions
- the invention relates to a method for starting a heat exchanger system provided in a hot gas line with an upstream starting heat exchanger for steam generation, is supplied via the feed medium and which first releases hot steam and finally water to the heat exchanger system when starting, so that the originally unpressurized empty and essentially heated heat exchanger system is continuous is brought from the initial state to its operating state, and a heat exchanger system for performing the method.
- the starting heat exchanger is always connected to the hot gas, and thus, when the heat exchanger system is empty, has at least essentially the same hot gas temperature as its other heat exchanger.
- It is designed as a heat accumulator with a high storage capacity as a system of concentric pipes, which can move against each other to compensate for the different thermal expansion when feeding water when the steam generator is started.
- it is mentioned that it would not hurt if z. B. the inner tube of the system, where the water feed takes place, tears.
- the starting heat exchanger according to this DE-A-3 741 882 has the major disadvantage that when starting the water flowing through it damages or destroys the protective layer in the entry zone because of the considerable temperature differences, and in particular iron is thereby introduced into the boiler system, thereby also endangering the heat exchanger system becomes.
- the method according to the invention is accordingly primarily characterized in that, for starting up the heat exchanger system, the starting heat exchanger of the heat exchanger system, which is shielded from the hot gas flow by flaps, is charged with feed medium and then hot gas is applied to the gas side by opening the shield.
- the heat exchanger system according to the invention for carrying out the method is characterized in that the starting heat exchanger is arranged in the hot gas line and can be shielded against the hot gas flow by means of flaps, or that the starting heat exchanger is in a secondary line which can be opened and closed by means of flaps, the passage cross section of the secondary line being substantially smaller than that Passage cross section of the hot gas line is arranged and the starting heat exchanger serves as an auxiliary steam generator for starting up the entire system from the cold state.
- the starting heat exchanger has an additional water or. Steam supply is downstream; in this way, the start-up heat exchanger can be taken out of operation after starting.
- the invention can be implemented on any heat exchanger system; preference is given to a closed system, where the condensate formed from the steam generated after work and cooling is returned as feed water; also on any steam generation system (such as forced circulation, natural circulation, forced circulation).
- FIGS. 1 and 2 are continuous steam generators, the embodiments according to FIGS.
- the system is fed in the direction of the arrow A 'with water (or steam) via a collector S1 into a starting heat exchanger 2, which is connected to the preheater 3 via collectors S2 and S3.
- the starting heat exchanger 2 is arranged above the preheater 3 in the hot gas line 1 and by means of flaps 9 or the like in relation to the hot gas flow. shieldable. It can be seen that the system according to FIG. 1 is fundamentally fed via the collector S1, but a further feed point A wie can be provided as a further special feature between the collectors S2 and S3.
- the cold starting heat exchanger shielded from the hot gas flow is first charged with steam or water and the shielding flaps are opened so that the hot gas comes into contact with the starting heat exchanger.
- the flap position or the feed of the start heat exchanger 2, or both, are coordinated so that the start heat exchanger emits hot steam at the start of the start-up phase and hot water at the end of the start-up phase to the preheater 3, so that the system from the hot, empty in its Operating state cools down, where hot steam is just being formed in the superheater.
- the shielding flaps 9 can remain open or closed; the start heat exchanger 2 then acts as a preheater; Accordingly, the heating surface of the ECO could be made smaller.
- the starting heat exchanger 2 is provided in a branch line 10 of the hot gas line 1.
- the branch line 10 can be closed by flaps 9.
- a further feed point A ⁇ can be provided between the collectors S2 and S3, via which additional feed medium can be metered in, for example, when starting up, or in the operating state the only feed point is feed water; in the second case, the branch line 10 then usually remains closed and the starting heat exchanger is not supplied.
- FIGS. 3 and 4 essentially correspond to the embodiments according to FIGS. 1 and 2; the only difference is their design as circulation systems with a boiler drum 8.
- water comes from the preheater 3 via the collector S4 into the boiler drum 8, from where it goes to the collector 6, for which purpose a pump 7 is optionally provided, and from there into the evaporator 4 and via the collector S5 in the steam chamber of the boiler drum 8, from where it approaches the superheater 6 via the collector S7 and leaves it as service steam via the collector S8 in the direction of the arrow B 'to the consumer.
- a bridging line 11 for controlled heating of the drum 8 can be provided between the steam space of the boiler drum 8 and the collector S2 connected in the flow direction to the starting heat exchanger 2.
- This bypass line 11 can also be used to feed auxiliary steam into the auxiliary steam system of the system for starting up the system, so that no foreign medium is required for this.
- each boiler system can be equipped with the starting heat exchanger arrangement according to the invention.
- the water / steam cycle can also be provided in a known manner, i.e. that waste steam and / or waste water from the consumer returns to the heat exchanger system.
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Combustion & Propulsion (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Control Of Steam Boilers And Waste-Gas Boilers (AREA)
- Engine Equipment That Uses Special Cycles (AREA)
Claims (3)
- Procédé pour faire démarrer un système échangeur de chaleur prévu dans un conduit de gaz chaud avec un échangeur de chaleur de démarrage placé devant pour la génération de la vapeur, par lequel est amené le milieu d'alimentation et qui dégage, lors du démarrage, tout d'abord de la vapeur chaude et enfin de l'eau au système échangeur de chaleur, de sorte que le système échangeur de chaleur initialement vide, sans pression, et chauffé sensiblement à la température du gaz chaud, soit amené de manière continue de l'état de départ à son état de fonctionnement, caractérisé en ce que pour le démarrage du système échangeur de chaleur, tout d'abord l'échangeur de chaleur de démarrage,du système échangeur de chaleur,protégé par des volets du flux de gaz chaud est alimenté en milieu d'alimentation et est alimenté ensuite, par l'ouverture des volets, côté gaz, en gaz chaud.
- Système échangeur de chaleur pour la génération de vapeur, qui est disposé dans un conduit de gaz chaud (1), avec un échangeur de chaleur de démarrage (2), par lequel a lieu l'amenée du milieu d'alimentation et qui, lors du démarrage du système échangeur de chaleur vide et sans pression et sensiblement à la température de gaz chaud, émet tout d'abord de la vapeur chaude et ensuite de l'eau au système échangeur de chaleur, pour la mise en oeuvre du procédé selon la revendication 1, caractérisé en ce que l'échangeur de chaleur de démarrage (2) est disposé dans le conduit de gaz chaud (1) et peut être protégé contre le flux de gaz chaud au moyen de volets (9), ou que l'échangeur de chaleur de démarrage (29) est disposé dans un conduit secondaire (10) pouvant être ouvert et fermé au moyen de volets (9), la section transversale de passage du conduit secondaire étant sensiblement plus petite que la section transversale de passage du conduit de gaz chaud, et que l'échangeur de chaleur de démarrage (2) sert de générateur de vapeur auxiliaire pour faire démarrer l'ensemble de l'installation à partir de l'état froid.
- Système échangeur de chaleur selon la revendication 2, caractérisé en ce qu'il est prévu entre l'échangeur de chaleur de démarrage (2) et l'échangeur de chaleur (3) suivant dans la direction d'alimentation une amenée additionnelle d'eau et de vapeur (A˝), respectivement.
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
AT0175590A AT394627B (de) | 1990-08-27 | 1990-08-27 | Verfahren zum anfahren eines waermetauschersystems zur dampferzeugung sowie waermetauschersystem zur dampferzeugung |
AT1755/90 | 1990-08-27 |
Publications (2)
Publication Number | Publication Date |
---|---|
EP0474622A1 EP0474622A1 (fr) | 1992-03-11 |
EP0474622B1 true EP0474622B1 (fr) | 1994-09-28 |
Family
ID=3520308
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP91890180A Expired - Lifetime EP0474622B1 (fr) | 1990-08-27 | 1991-08-13 | Procédé pour démarrer un système échangeur de chaleur pour produire de la vapeur et système échangeur de chaleur pour produire de la vapeur |
Country Status (9)
Country | Link |
---|---|
US (1) | US5189988A (fr) |
EP (1) | EP0474622B1 (fr) |
KR (1) | KR920004808A (fr) |
AT (1) | AT394627B (fr) |
CA (1) | CA2049815A1 (fr) |
DE (1) | DE59103104D1 (fr) |
DK (1) | DK0474622T3 (fr) |
ES (1) | ES2062749T3 (fr) |
FI (1) | FI913766A (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105805720A (zh) * | 2015-07-17 | 2016-07-27 | 衢州学院 | 一种配备有自动化锅炉控制系统的三合一锅炉 |
Families Citing this family (14)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE4142376A1 (de) * | 1991-12-20 | 1993-06-24 | Siemens Ag | Fossil befeuerter durchlaufdampferzeuger |
DE4303613C2 (de) * | 1993-02-09 | 1998-12-17 | Steinmueller Gmbh L & C | Verfahren zur Erzeugung von Dampf in einem Zwangsdurchlaufdampferzeuger |
KR100439080B1 (ko) * | 1997-06-30 | 2004-07-05 | 지멘스 악티엔게젤샤프트 | 폐열 증기 발생기 |
US5924389A (en) * | 1998-04-03 | 1999-07-20 | Combustion Engineering, Inc. | Heat recovery steam generator |
US6092490A (en) * | 1998-04-03 | 2000-07-25 | Combustion Engineering, Inc. | Heat recovery steam generator |
EP1512905A1 (fr) * | 2003-09-03 | 2005-03-09 | Siemens Aktiengesellschaft | Générateur de vapeur à passage unique et méthode pour faire fonctionner ledit générateur de vapeur à passage unique |
ITMI20050104A1 (it) * | 2005-01-26 | 2006-07-27 | Son S R L | Generatore di vapore a recupero |
EP2065641A3 (fr) * | 2007-11-28 | 2010-06-09 | Siemens Aktiengesellschaft | Procédé de fonctionnement d'un générateur de vapeur en flux continu, ainsi que générateur de vapeur en flux à sens unique |
CN101696080B (zh) * | 2009-10-30 | 2012-07-25 | 蚌埠玻璃工业设计研究院 | 一种玻璃熔窑的烟气排出系统 |
KR101984361B1 (ko) * | 2013-09-26 | 2019-09-03 | 누터/에릭슨 인코퍼레이티드 | 열 복구 스팀 발생기를 위한 열 교환 시스템 및 방법 |
CN104154515A (zh) * | 2014-08-14 | 2014-11-19 | 张家港市艾克沃环境能源技术有限公司 | 一种可调吸热量余热锅炉及其控制方法 |
CN105299608B (zh) * | 2015-12-01 | 2017-08-25 | 广州博恩能源有限公司 | 一种生物质气体锅炉 |
US9995170B2 (en) * | 2016-03-16 | 2018-06-12 | General Electric Technology Gmbh | System and method for heating components of a heat recovery steam generator |
CN106168366B (zh) * | 2016-08-29 | 2018-10-23 | 江苏安信锅炉有限公司 | 贯流式智能化节能锅炉系统 |
Family Cites Families (7)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CH401092A (de) * | 1963-04-02 | 1965-10-31 | Sulzer Ag | Anordnung zum Kühlen von Teilen eines Dampferzeugers durch Speisewasser |
GB1240113A (en) * | 1968-05-23 | 1971-07-21 | Foster Wheeler Corp | Heat exchangers |
CH557986A (de) * | 1974-03-22 | 1975-01-15 | Sulzer Ag | Verfahren und vorrichtung zum regeln eines dampferzeugers. |
CH635184A5 (de) * | 1978-12-22 | 1983-03-15 | Sulzer Ag | Dampferzeugeranlage. |
DE3236979A1 (de) * | 1982-10-06 | 1984-04-12 | Deutsche Babcock Werke AG, 4200 Oberhausen | Zwangsdurchlaufdampferzeuger und verfahren zu seiner inbetriebnahme |
EP0308728B1 (fr) * | 1987-09-21 | 1991-06-05 | Siemens Aktiengesellschaft | Méthode d'exploitation d'un générateur de vapeur à passage unique |
DE3741882C1 (en) * | 1987-12-10 | 1989-02-02 | Gea Luftkuehler Happel Gmbh | Steam generator with once-through forced flow |
-
1990
- 1990-08-27 AT AT0175590A patent/AT394627B/de not_active IP Right Cessation
-
1991
- 1991-08-08 FI FI913766A patent/FI913766A/fi not_active Application Discontinuation
- 1991-08-13 ES ES91890180T patent/ES2062749T3/es not_active Expired - Lifetime
- 1991-08-13 DK DK91890180.2T patent/DK0474622T3/da not_active Application Discontinuation
- 1991-08-13 US US07/744,929 patent/US5189988A/en not_active Expired - Lifetime
- 1991-08-13 EP EP91890180A patent/EP0474622B1/fr not_active Expired - Lifetime
- 1991-08-13 DE DE59103104T patent/DE59103104D1/de not_active Expired - Lifetime
- 1991-08-26 KR KR1019910014790A patent/KR920004808A/ko not_active Application Discontinuation
- 1991-08-26 CA CA002049815A patent/CA2049815A1/fr not_active Abandoned
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN105805720A (zh) * | 2015-07-17 | 2016-07-27 | 衢州学院 | 一种配备有自动化锅炉控制系统的三合一锅炉 |
Also Published As
Publication number | Publication date |
---|---|
KR920004808A (ko) | 1992-03-28 |
EP0474622A1 (fr) | 1992-03-11 |
DE59103104D1 (de) | 1994-11-03 |
CA2049815A1 (fr) | 1992-02-28 |
FI913766A (fi) | 1992-02-28 |
AT394627B (de) | 1992-05-25 |
ATA175590A (de) | 1991-10-15 |
US5189988A (en) | 1993-03-02 |
DK0474622T3 (da) | 1995-02-13 |
FI913766A0 (fi) | 1991-08-08 |
ES2062749T3 (es) | 1994-12-16 |
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