CN1703599A - Once-through evaporator for a steam generator - Google Patents
Once-through evaporator for a steam generator Download PDFInfo
- Publication number
- CN1703599A CN1703599A CNA2003801009215A CN200380100921A CN1703599A CN 1703599 A CN1703599 A CN 1703599A CN A2003801009215 A CNA2003801009215 A CN A2003801009215A CN 200380100921 A CN200380100921 A CN 200380100921A CN 1703599 A CN1703599 A CN 1703599A
- Authority
- CN
- China
- Prior art keywords
- tube
- evaporator
- water
- steam
- helical
- 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.)
- Pending
Links
Images
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B15/00—Water-tube boilers of horizontal type, i.e. the water-tube sets being arranged horizontally
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B37/00—Component parts or details of steam boilers
- F22B37/02—Component parts or details of steam boilers applicable to more than one kind or type of steam boiler
- F22B37/10—Water tubes; Accessories therefor
- F22B37/18—Inserts, e.g. for receiving deposits from water
-
- 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
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F22—STEAM GENERATION
- F22B—METHODS OF STEAM GENERATION; STEAM BOILERS
- F22B29/00—Steam boilers of forced-flow type
- F22B29/06—Steam boilers of forced-flow type of once-through type, i.e. built-up from tubes receiving water at one end and delivering superheated steam at the other end of the tubes
Landscapes
- 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)
- Life Sciences & Earth Sciences (AREA)
- Sustainable Development (AREA)
- Sustainable Energy (AREA)
- Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)
- Vaporization, Distillation, Condensation, Sublimation, And Cold Traps (AREA)
Abstract
Description
前后对照的有关申请Relevant applications before and after
本申请源自于美国2002年10月4日申请的、申请号为60/416,083的在先申请,而且要求该申请的优先权。This application is derived from, and claims priority from, earlier US application Serial No. 60/416,083 filed October 4, 2002.
技术领域technical field
本发明涉及一种蒸汽发生器,特别是涉及一种用于蒸汽发生器的蒸发器和用于这种蒸发器的管装置。The present invention relates to a steam generator, in particular to an evaporator for a steam generator and a tube arrangement for such an evaporator.
技术背景technical background
蒸汽在工业中被广泛应用,或许其最主要的用途是用于发电。典型地,在许多情况下,由燃烧造成的热气体,流经蒸汽发生器,把水转化为过热蒸汽。这些装置的代表是热回收蒸汽发生器,它吸收由驱动发电机的气体涡轮中排出的热气体的热量,这些热量用来产生蒸汽,而这些蒸汽又传递到驱动另一个发电机的蒸汽涡轮。Steam is used extensively in industry, perhaps its most important use being to generate electricity. Typically, in many cases, hot gases resulting from combustion flow through a steam generator to convert water into superheated steam. Representative of these devices is the heat recovery steam generator, which absorbs heat from the hot gas exhausted by a gas turbine driving an electric generator. This heat is used to generate steam which is passed on to a steam turbine driving another electric generator.
典型的蒸汽发生器的最基本构造,除了一个热气体通过的管路,还包括管路中相应于气体流动而顺序安置的三个附加结构,分别是过热器、蒸发器、和给水加热器。水以相反方向流动:首先流入给水加热器被加热,但仍保持液体状态;随后进入蒸发器,水大部分转化为饱和蒸汽;然后流入过热器,饱和蒸汽转化成过热蒸汽。The most basic structure of a typical steam generator, in addition to a pipeline through which hot gas passes, also includes three additional structures arranged in sequence corresponding to the flow of gas in the pipeline, namely superheater, evaporator, and feed water heater. The water flows in opposite directions: first into the feedwater heater to be heated, but still in a liquid state; then into the evaporator, where the water is mostly converted to saturated steam; then into the superheater, where the saturated steam is converted into superheated steam.
蒸发器包括两种基本的类型:循环类型和直通类型,它们各具优点和缺点。两种类型的蒸发器在管路中都安装有热气体通过的一组管子。Evaporators come in two basic types: recirculation and pass-through, each with advantages and disadvantages. Both types of evaporators have a set of tubes installed in the line through which the hot gas passes.
在循环类型的蒸发器中,上述管子和其上方的一个蒸汽筒成循环排列。蒸汽筒中有水,水从蒸汽筒通过一个下水管流入上述管子中,在管子中的一部分水转化为蒸汽。但是蒸汽以气泡的形式存在于水中,并且通过一个立管回返至蒸汽筒中。蒸汽筒里的饱和蒸汽从液态水中分离出来,进入过热器。饱和蒸汽离开蒸汽筒后,水随后由给水器注入蒸汽筒中。循环蒸发器的管子自始至终都是湿的,也就是说,液态水充满管子的内部。这样有助于产生良好的热传递效果,并且使管子保持相对适中的温度,从而免除管道装置使用耐高温合金材料的需要。In a circulation type evaporator, the above-mentioned tubes are arranged in a circulation with a steam cylinder above them. There is water in the steam cylinder, and water flows into the above-mentioned pipe from the steam cylinder through a downpipe, and a part of the water in the pipe is converted into steam. But the steam exists in the water as bubbles and returns to the steam cylinder through a riser. The saturated steam in the steam drum is separated from the liquid water and enters the superheater. After the saturated steam leaves the steam drum, water is then injected into the steam drum by the water feeder. The tubes of a recirculating evaporator are wet all the way, that is, liquid water fills the inside of the tubes. This helps to produce good heat transfer and keeps the tubes at a relatively moderate temperature, eliminating the need for high temperature alloys in the piping fittings.
但是循环蒸发器也有缺陷。可能最大的缺陷应该归因于下列结构的花费:蒸汽筒、大的下水管和给管子供水的供应管。而且需要耗费时间使其中的蓄水部分达到沸腾温度,致使循环蒸发器的启动时间延长。But circulating evaporators also have drawbacks. Probably the greatest drawback should be attributed to the expense of the following structures: steam cylinders, large downpipes and supply pipes to feed the pipes. And it takes time to make the water storage part therein reach the boiling temperature, so that the start-up time of the circulating evaporator is prolonged.
直通蒸发器不需要下水管或者蒸汽筒,制造成本相对便宜,而且水直接储存在管子中,以及与管子相通的供应管中。这些条件使直通蒸发器比自然循环蒸发器运转快速。然而,直通蒸发器必须使水完全转化为蒸汽,以便只有不包含液态水的蒸汽从管子中流入过热器。蒸发器需要借助一个位于水流上游的注水泵,使水在蒸发器内以一种控制的速度循环,如果这种速度适中,可以使蒸汽在一种饱和或者稍微过热的状态下离开蒸发器。Straight-through evaporators require no downpipes or steam drums, are relatively cheap to manufacture, and have water stored directly in the tubes, and in supply lines that communicate with the tubes. These conditions make the straight-through evaporator run faster than the natural circulation evaporator. However, the straight-through evaporator must completely convert the water to steam so that only steam, which does not contain liquid water, flows from the tubes into the superheater. The evaporator requires the aid of an injection pump upstream of the water flow to circulate water through the evaporator at a controlled rate which, if moderate, allows the steam to leave the evaporator in a saturated or slightly superheated state.
因此,在直通蒸发器中,与在循环蒸发器中一样,管壁最接近入水口处是湿的,因为这些管子的端口只流过液态水。但是下一步,水将在管子中转化为水雾,并进一步转化为饱和蒸汽。在水雾流动的区域,水与管壁的内表面被隔离开,所以水雾存在于管子中心外的区域并向前延伸。环绕此中心区域的管壁是干燥的,使管壁的温度较高,热量交换效果较差。较高的温度将要求管子使用耐高温的金属,也就是一种昂贵的高合金钢。Therefore, in a straight-through evaporator, as in a circulating evaporator, the walls of the tubes are wetted closest to the water inlet, because only liquid water flows through the ends of these tubes. But in the next step, the water will be converted in the tubes into mist and further into saturated steam. In the area where the mist flows, the water is isolated from the inner surface of the tube wall, so the mist exists in the area outside the center of the tube and extends forward. The tube walls surrounding this central region are dry, making the tube walls warmer and less efficient at exchanging heat. Higher temperatures will require pipes to be made of a high-temperature resistant metal, an expensive high-alloy steel.
附图说明Description of drawings
图1是一个蒸汽发生器的结构剖面图,安装有根据本发明所构成和所限定的直通蒸发器;Fig. 1 is a structural sectional view of a steam generator, which is equipped with a straight-through evaporator constituted and defined according to the present invention;
图2是蒸发器的立体图;Figure 2 is a perspective view of the evaporator;
图3是沿图2中的3-3线的剖面图;Fig. 3 is a sectional view along line 3-3 in Fig. 2;
图4是一个蒸发器管子的一端的剖面图,显示了固定在管子上的一个螺旋带;Figure 4 is a cross-sectional view of one end of an evaporator tube showing a helical band secured to the tube;
图5是图4中的剖面图旋转了90°后,与图4相近似的一个剖面图;Fig. 5 is a sectional view similar to Fig. 4 after the sectional view in Fig. 4 is rotated by 90°;
图6是一个蒸发器管子沿截面部分切开的结构剖面图,显示了管子中的流动。Figure 6 is a cross-sectional view of the structure of an evaporator tube partially cut away in cross-section, showing the flow in the tube.
最佳实施例best practice
如图1所示的蒸汽发生器A,其主要包括有一个输入口4和一个输出口6的管路2。输入口4与一个热气源,例如气体涡轮或者燃烧器相连接。热气体由输入口4进入管路12,由输出口6排出。此外,蒸汽发生器A还包括一个过热器12、一个蒸发器14和一个给水加热器16,依次安装在管路2的输入口4到输出口6之间。因此,热气体首先流经过热器12,然后经过蒸发器14,最后流经给水加热器16。水以与热气体相反的方向流动。给水加热器16与一个注水泵18连接,由注水泵18将水送入给水加热器16。给水加热器16吸收热气体的热量,把热量传递给流过给水加热器16的液态水,从而使水的温度提高,但水仍呈液态。液态水从给水加热器16流出后,流到蒸发器14。蒸发器14将水转化为蒸汽,大部分为饱和蒸汽。蒸汽随后进入过热器12,经加热后转化为过热蒸汽,可以用来驱动涡轮,用于某些工业生产,也可以用于建筑物内取暖。过热器12、蒸发器14、以及给水加热器16基本上都是管组状。蒸发器14是直通式方式运作。实际上,此蒸汽发生器A可以有多个蒸发器14。The steam generator A shown in FIG. 1 mainly includes a pipeline 2 having an input port 4 and an output port 6 . The inlet 4 is connected to a hot gas source, such as a gas turbine or a burner. The hot gas enters the pipeline 12 from the input port 4 and is discharged from the output port 6 . In addition, the steam generator A also includes a superheater 12 , an evaporator 14 and a feed water heater 16 , which are sequentially installed between the input port 4 and the output port 6 of the pipeline 2 . Thus, the hot gas flows first through heater 12 , then through evaporator 14 , and finally through feedwater heater 16 . The water flows in the opposite direction to the hot gas. The feed water heater 16 is connected with a water injection pump 18, and water is sent into the feed water heater 16 by the water injection pump 18. The feedwater heater 16 absorbs the heat of the hot gas and transfers the heat to the liquid water flowing through the feedwater heater 16, thereby increasing the temperature of the water, but the water is still in a liquid state. Liquid water flows from the feedwater heater 16 to the evaporator 14 . The evaporator 14 converts the water to steam, mostly saturated steam. The steam then enters the superheater 12 and is converted into superheated steam after being heated, which can be used to drive turbines for some industrial production, and can also be used for heating in buildings. The superheater 12, the evaporator 14, and the feedwater heater 16 are basically in the form of a tube group. The evaporator 14 operates in a straight-through manner. In practice, this steam generator A may have a plurality of evaporators 14 .
如图2所示,蒸发器14包括一个供应管26、一个排出管28和若干个在供应管26和排出管28之间延伸的管子30。供应管26有一个与给水加热器16相连接的输入端口32,用于接收从给水加热器16流出来的已加热的水。事实上,水是在注水泵18产生的压力作用下,从给水加热器16通过输入端口32流入蒸发器14。排出管26有一个与过热器12相连接的输出端口34,由水转化成的饱和蒸汽或者稍微过热的蒸汽通过输出端口34直接进入过热器12。管子30上附有翼片36,这些翼片36有助于吸收流经管路2的气体的热量。As shown in FIG. 2 , the evaporator 14 includes a
热水经过供应管26进入管子30后,转化为蒸汽,蒸汽随后经过排出管28流入过热器12。因此,在每个管子30最接近供应管20的部分包含着液态水,而在最接近排出管28的部分包含着饱和蒸汽及稍微过热的蒸汽。在每个管子30的中间部分,液态水处于转化状态,并变为蒸汽。在此,水沸腾,转化为水雾或者水与饱和蒸汽的混合物。再往前,水雾进一步变为饱和蒸汽,并且饱和蒸汽最终变为过热蒸汽,尽管只是稍微过热。在管子30的过热区域,如果确实包含有过热蒸汽,这段区域也是十分短的。管子30的构成材料是碳钢或者铬钼合金钢。After the hot water enters the
如图3-5所示,每个管子30内都有一个螺旋带40,螺旋带40的一端从管子30与供应管26相连接的输入口开始,穿过水雾存在的区域延伸。每个螺旋带30的宽度都略小于其所延伸的管子30的内径,方便了螺旋带40在管子30中插入和抽取,而不受管子30的妨碍。每个螺旋带40的最佳宽度是小于管子30内径1/16英寸,管子30的内径至少有2英寸。螺旋带40在其两端间多次螺旋式弯曲,所以它的边缘沿着管子30的内表面呈螺旋形状。事实上,螺旋带40的一个360°全角螺旋在管子30内所占的长度是管子30直径的5-25倍。例如,对于一个内径为2英寸的管子30,其中的螺旋带40的一个螺旋占据管子30的长度为管子30直径的5倍,即螺旋带40的一个360°全角螺旋将占据管子40的10英寸。位于管子30输入口处的螺旋带40的一端固定在一个支柱42上,支柱42横向穿过管子32的输入口。所述支柱42焊接在管子30的一端及螺旋带40上,因此把螺旋带40固定在它的管子30上。螺旋带40是由一种金属构成,此金属能够耐受稍微过热的蒸汽的温度,并且能与构成管子30的金属相容,使敏感的电化学反应最小。如果管子30是碳钢材料,不锈钢是适宜的选择。As shown in Figures 3-5, each
在蒸汽发生器A的运转中,流经管路2的热气体,依次经过过热器12的管子、蒸发器14和给水加热器16。在此过程中,热气体的温度逐渐减低。注水泵18将水送入给水加热器16,水在流过给水加热器16的管子时,吸收热气体流经给水加热器传递出来的热量。水的温度升高,但仍呈液态。在注水泵18产生的压力作用下,水从给水加热器16流入蒸发器14的供应管26,然后进入蒸发器14的管子30。水在管子30中时,管子30遇到流经管路2的较高的温度的热气流。事实上,热气流在流经蒸发器14时,使管子30的温度升高到足以使在管子30中的水转化为蒸汽。水在最初进入管子30时呈液态,但是当它在管子30中流过时开始沸腾,产生水雾。螺旋带40穿过水雾存在的区域延伸,在水雾向排出管28流动过程中产生一定量的涡流。如图6所示,涡流带动水雾,也就是水颗粒触击管子30的内表面,从而使流经管子30的热气体与在管子30中流动的水雾更好更有效地进行热量交换,这样也防止管子30过热。如果没有螺旋带40,水雾将存在于管子30的中心,并被沿着管子30内表面的饱和蒸汽或者过热蒸汽包围。这将导致水雾存在的区域中的管子30处于较高温度。当管子30中的水雾流向排出管28时,水雾转化为饱和蒸汽,甚至变为过热蒸汽,尽管只是稍微过热。管子30中仅含有过热蒸汽的区域是短的,并且因为热量从过热蒸汽存在的区域传导到水雾和液态水所在的区域,因此所述仅含有过热蒸汽的区域能够保持相对适中的温度。During the operation of the steam generator A, the hot gas flowing through the pipeline 2 passes through the tubes of the superheater 12, the evaporator 14 and the feed water heater 16 in sequence. During this process, the temperature of the hot gas gradually decreases. The water injection pump 18 sends water into the feed water heater 16, and when the water flows through the pipes of the feed water heater 16, it absorbs the heat transferred from the hot gas flowing through the feed water heater. The temperature of the water rises, but it remains liquid. Water flows from the feed water heater 16 into the
如果螺旋带40不是在供应管26处固定在管子30上,它们也可以在排出管28处固定在管子30上,这样螺旋带40将向供应管26方向延伸。螺旋管40可能延伸于管子30的全长,通过或仅仅穿过水雾流经的区域。蒸发器14的管子30可以不是以单组方式安装,而可能按多组的方式组成。If the
Claims (18)
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US41608302P | 2002-10-04 | 2002-10-04 | |
| US60/416,083 | 2002-10-04 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN1703599A true CN1703599A (en) | 2005-11-30 |
Family
ID=32093813
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CNA2003801009215A Pending CN1703599A (en) | 2002-10-04 | 2003-10-02 | Once-through evaporator for a steam generator |
Country Status (8)
| Country | Link |
|---|---|
| US (1) | US20040069244A1 (en) |
| EP (1) | EP1546607A4 (en) |
| KR (1) | KR20050086420A (en) |
| CN (1) | CN1703599A (en) |
| AU (1) | AU2003275378A1 (en) |
| CA (1) | CA2501086A1 (en) |
| MX (1) | MXPA05003380A (en) |
| WO (1) | WO2004033962A2 (en) |
Families Citing this family (12)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US7065967B2 (en) * | 2003-09-29 | 2006-06-27 | Kalex Llc | Process and apparatus for boiling and vaporizing multi-component fluids |
| US7770544B2 (en) * | 2004-12-01 | 2010-08-10 | Victory Energy Operations LLC | Heat recovery steam generator |
| EP1793163A1 (en) * | 2005-12-05 | 2007-06-06 | Siemens Aktiengesellschaft | Steam generator tube, method of manufacturing the same and once-through steam generator |
| KR100752635B1 (en) * | 2006-05-02 | 2007-08-29 | 삼성광주전자 주식회사 | Heat exchanger for refrigerator |
| US7882809B2 (en) * | 2006-11-07 | 2011-02-08 | L'air Liquide, Societe Anonyme Pour L'etude Et L'exploitation Des Procedes Georges Claude | Heat exchanger having a counterflow evaporator |
| EP2141411B1 (en) | 2008-06-30 | 2013-08-21 | Cockerill Maintenance & Ingenierie S.A. | Header distributor for two-phase flow in a single pass evaporator |
| EP2184536A1 (en) * | 2008-09-09 | 2010-05-12 | Siemens Aktiengesellschaft | Steam generator pipe, accompanying production method and once-through steam generator |
| US8695344B2 (en) * | 2008-10-27 | 2014-04-15 | Kalex, Llc | Systems, methods and apparatuses for converting thermal energy into mechanical and electrical power |
| US8408003B2 (en) * | 2008-11-05 | 2013-04-02 | General Electric Company | Combined cycle power plant |
| US8474263B2 (en) | 2010-04-21 | 2013-07-02 | Kalex, Llc | Heat conversion system simultaneously utilizing two separate heat source stream and method for making and using same |
| EP2839213B1 (en) | 2012-01-17 | 2018-09-05 | General Electric Technology GmbH | Tube and baffle arrangement in a once-through horizontal evaporator |
| KR101536989B1 (en) | 2012-01-17 | 2015-07-16 | 알스톰 테크놀러지 리미티드 | Flow control devices and methods for a once-through horizontal evaporator |
Family Cites Families (15)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| NL124177C (en) * | 1961-06-09 | |||
| US3648754A (en) * | 1969-07-28 | 1972-03-14 | Hugo H Sephton | Vortex flow process and apparatus for enhancing interfacial surface and heat and mass transfer |
| US3756202A (en) * | 1971-11-22 | 1973-09-04 | American Standard Inc | Heat exchange tube for use in a boiler and boiler incorporating the same |
| NL52674C (en) * | 1973-11-02 | |||
| EP0349834B1 (en) * | 1988-07-04 | 1996-04-17 | Siemens Aktiengesellschaft | Once-through steam generator |
| JP3091220B2 (en) * | 1991-04-18 | 2000-09-25 | シーメンス アクチエンゲゼルシヤフト | Once-through boiler with vertical flue consisting of tubes arranged almost vertically |
| JPH05164482A (en) * | 1991-12-12 | 1993-06-29 | Kobe Steel Ltd | Liquefied natural gas vaporizer |
| DE4333404A1 (en) * | 1993-09-30 | 1995-04-06 | Siemens Ag | Continuous steam generator with vertically arranged evaporator tubes |
| JP3037073B2 (en) * | 1994-07-20 | 2000-04-24 | 株式会社神戸製鋼所 | Cryogenic liquid vaporizer |
| US5799622A (en) * | 1997-06-30 | 1998-09-01 | Decker Manufacturing | Furnace heat exchanger tube cleaning system |
| US6092589A (en) * | 1997-12-16 | 2000-07-25 | York International Corporation | Counterflow evaporator for refrigerants |
| US5924389A (en) * | 1998-04-03 | 1999-07-20 | Combustion Engineering, Inc. | Heat recovery steam generator |
| DE19858780C2 (en) * | 1998-12-18 | 2001-07-05 | Siemens Ag | Fossil-heated continuous steam generator |
| DE19901430C2 (en) * | 1999-01-18 | 2002-10-10 | Siemens Ag | Fossil-heated steam generator |
| DE19929088C1 (en) * | 1999-06-24 | 2000-08-24 | Siemens Ag | Fossil fuel heated steam generator e.g. for power station equipment |
-
2003
- 2003-10-02 CN CNA2003801009215A patent/CN1703599A/en active Pending
- 2003-10-02 EP EP03759654A patent/EP1546607A4/en not_active Withdrawn
- 2003-10-02 WO PCT/US2003/031174 patent/WO2004033962A2/en not_active Ceased
- 2003-10-02 KR KR1020057005565A patent/KR20050086420A/en not_active Withdrawn
- 2003-10-02 AU AU2003275378A patent/AU2003275378A1/en not_active Abandoned
- 2003-10-02 CA CA002501086A patent/CA2501086A1/en not_active Abandoned
- 2003-10-02 MX MXPA05003380A patent/MXPA05003380A/en not_active Application Discontinuation
- 2003-10-02 US US10/677,443 patent/US20040069244A1/en not_active Abandoned
Also Published As
| Publication number | Publication date |
|---|---|
| EP1546607A2 (en) | 2005-06-29 |
| AU2003275378A8 (en) | 2004-05-04 |
| WO2004033962A2 (en) | 2004-04-22 |
| MXPA05003380A (en) | 2005-06-22 |
| WO2004033962A3 (en) | 2004-06-03 |
| CA2501086A1 (en) | 2004-04-22 |
| AU2003275378A1 (en) | 2004-05-04 |
| US20040069244A1 (en) | 2004-04-15 |
| EP1546607A4 (en) | 2006-05-03 |
| KR20050086420A (en) | 2005-08-30 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN1161556C (en) | Heat Recovery Steam Generator | |
| CN1161555C (en) | Heat recovery steam generator | |
| CN1703599A (en) | Once-through evaporator for a steam generator | |
| US20110083619A1 (en) | Dual enhanced tube for vapor generator | |
| CN208059636U (en) | Heat exchanger and fused salt steam generator including at least one train of heat exchangers | |
| CN1107202C (en) | Continuous steam generator | |
| CN110691953B (en) | Heat Exchangers for Molten Salt Steam Generators in Concentrated Solar Power Plants | |
| CN107178776A (en) | A kind of steam raising plant and smoke exhaust ventilator | |
| JP2012529613A (en) | Once-through evaporator | |
| JPH10122501A (en) | Waste heat recovery boiler | |
| KR100363719B1 (en) | Spiral Wound Heat Transferring Equipment on the Single Passage for the Super-heater | |
| US20230243499A1 (en) | Low temperature heat exchanging system and method for a heat recovery steam generator | |
| CN115342329A (en) | Steam generator utilizing solid heat storage | |
| EP0192918B1 (en) | Preheater for a thermal-energy transformation plant | |
| CN118548722B (en) | A combined elbow type supercritical U-tube heat exchanger and its design method | |
| CN214250700U (en) | Module combined heat exchanger for steam generating device | |
| US20050074329A1 (en) | Pipes for steam power-plant | |
| CN102933899A (en) | Device for producing fixture units for steam generator pipes | |
| CN109959275B (en) | Heat exchanger and molten salt steam generator comprising at least one heat exchanger series | |
| CN210486608U (en) | Internal spiral socket pipe-joint heat exchanger | |
| RU2341751C1 (en) | Heat exchanger | |
| KR200311524Y1 (en) | Combined array recovery boiler for even flow without guide vanes or perforated plates | |
| RU1776959C (en) | Heat exchanger | |
| JPH01273901A (en) | Boiler | |
| RU2000518C1 (en) | Air heater |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C02 | Deemed withdrawal of patent application after publication (patent law 2001) | ||
| WD01 | Invention patent application deemed withdrawn after publication |