CN203880946U - Novel water circulation structure of gas angular tube hot water boiler - Google Patents
Novel water circulation structure of gas angular tube hot water boiler Download PDFInfo
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 213
- 238000001816 cooling Methods 0.000 claims abstract description 103
- 238000010438 heat treatment Methods 0.000 claims abstract description 70
- 229910000831 Steel Inorganic materials 0.000 claims abstract description 8
- 239000010959 steel Substances 0.000 claims abstract description 8
- 239000000567 combustion gas Substances 0.000 claims 10
- 239000007787 solid Substances 0.000 claims 7
- 238000009835 boiling Methods 0.000 abstract description 2
- 238000002485 combustion reaction Methods 0.000 abstract description 2
- 230000009172 bursting Effects 0.000 abstract 1
- 230000002542 deteriorative effect Effects 0.000 abstract 1
- 239000000779 smoke Substances 0.000 abstract 1
- 239000012528 membrane Substances 0.000 description 175
- 238000004891 communication Methods 0.000 description 24
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 17
- 239000003546 flue gas Substances 0.000 description 17
- 239000007789 gas Substances 0.000 description 15
- 238000009826 distribution Methods 0.000 description 11
- 238000010586 diagram Methods 0.000 description 5
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 4
- 230000007797 corrosion Effects 0.000 description 3
- 238000005260 corrosion Methods 0.000 description 3
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- 238000009833 condensation Methods 0.000 description 2
- 230000005494 condensation Effects 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000007613 environmental effect Effects 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
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- 230000002159 abnormal effect Effects 0.000 description 1
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- 239000012530 fluid Substances 0.000 description 1
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- 231100001261 hazardous Toxicity 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
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- 238000005192 partition Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000005728 strengthening Methods 0.000 description 1
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Abstract
Description
技术领域technical field
本实用新型涉及锅炉设备技术领域,具体涉及一种燃气角管热水锅炉新型水循环结构。The utility model relates to the technical field of boiler equipment, in particular to a novel water circulation structure of a gas angle tube hot water boiler.
背景技术Background technique
近年来,随着国内龙岗、大北、克深等几个新的大型天然气气田的探明,越来越多的小型燃煤热水锅炉被燃气锅炉所取代。相较于燃煤锅炉,燃气锅炉能从根本上解决粉尘、废水、废渣、有害气体的排放等诸多环境问题。其中,角管式燃气热水锅炉具有结构合理、原材料消耗少、长周期运行安全可靠、高效节能及减排环保的优点,必将成为我国燃气热水锅炉的首选炉型。In recent years, with the discovery of several new large natural gas fields in China, such as Longgang, Dabei, and Keshen, more and more small coal-fired hot water boilers have been replaced by gas-fired boilers. Compared with coal-fired boilers, gas-fired boilers can fundamentally solve many environmental problems such as dust, waste water, waste residue, and harmful gas emissions. Among them, the corner-tube gas-fired hot water boiler has the advantages of reasonable structure, less raw material consumption, safe and reliable long-term operation, high efficiency, energy saving, emission reduction and environmental protection, and will definitely become the first choice of gas-fired hot water boiler in my country.
但是,现有的角管技术在长周期运行安全方面存在如下问题与隐患:However, the existing angle tube technology has the following problems and hidden dangers in terms of long-term operation safety:
1)传统的角管式热水锅炉,烟气流经烟道尾部受热面时,由于流通横截面积较大,因而流速较低,导致烟气与受热面间的换热不佳,尾部对流受热面内的介质温度过低,受热面壁温往往会低于烟气的酸露点温度,从而造成对流受热面管子的低温腐蚀,严重影响着锅炉的安全运行。1) In the traditional corner tube hot water boiler, when the flue gas flows through the heating surface at the tail of the flue, due to the large flow cross-sectional area, the flow velocity is low, resulting in poor heat exchange between the flue gas and the heating surface, and convection at the tail The temperature of the medium in the heating surface is too low, and the wall temperature of the heating surface is often lower than the acid dew point temperature of the flue gas, resulting in low-temperature corrosion of the convective heating surface tubes, which seriously affects the safe operation of the boiler.
2)市场上运行的强制循环的热水锅炉,多数情况下,膜式水冷壁的上、下集箱内部布置了隔板,把整个水冷壁受热面分割成了向上和向下流动的循环回路,向下流动的循环回路在低负荷运行和突然停电时,势必会出现水循环的停滞和倒流的水动力工况,这种工况的存在严重威胁着热水锅炉的运行安全,因此,现有强制循环方式可能发生的低负荷和停电保护问题严重影响了先进技术产品的推广应用。申请号为:201110212423.6,实用新型名称为一种受热面全部强制上升流动的角管水循环结构(公开号为CN102374658A),解决了上述问题,但存在其侧墙膜式水冷壁受热面采用工质从下集箱一次强制上升流动的结构,这种结构对于具有大面积侧墙膜式水冷壁受热面的锅炉而言,不利于集箱内工质向水冷壁管的均匀分配、减小流量偏差和热偏差。2) For forced circulation hot water boilers operating on the market, in most cases, partitions are arranged inside the upper and lower headers of the membrane water-cooled wall to divide the entire heating surface of the water-cooled wall into circulation loops flowing upward and downward , when the downward-flowing circulation loop operates at low load and suddenly loses power, there will inevitably be hydrodynamic conditions such as stagnation of water circulation and reverse flow. The existence of such conditions seriously threatens the operation safety of hot water boilers. Therefore, the existing The low load and power failure protection problems that may occur in the forced circulation mode have seriously affected the popularization and application of advanced technology products. The application number is: 201110212423.6, and the name of the utility model is a corner tube water circulation structure with all forced upward flow on the heating surface (the publication number is CN102374658A). The lower header has a forced upward flow structure. This structure is not conducive to the uniform distribution of the working medium in the header to the water-cooled wall tubes, and the reduction of flow deviation and thermal deviation.
发明内容Contents of the invention
为了克服上述现有技术存在的不足,本实用新型的目的在于提供一种燃气角管热水锅炉新型水循环结构,能有效地降低烟气中因硫酸结露而引起对流受热面低温腐蚀的危险工况,具有钢耗量低、气密性好、流量偏差小、热偏差小、不会引起爆管及超强停电保护的特点。In order to overcome the deficiencies in the prior art above, the purpose of this utility model is to provide a new type of water circulation structure for a gas corner tube hot water boiler, which can effectively reduce the risk of low-temperature corrosion of the convective heating surface caused by sulfuric acid condensation in the flue gas. It has the characteristics of low steel consumption, good air tightness, small flow deviation, small thermal deviation, no pipe burst and super power failure protection.
为了达到上述目的,本实用新型所采用的技术方案是:In order to achieve the above object, the technical solution adopted in the utility model is:
一种燃气角管热水锅炉新型水循环结构,包括有炉膛103和设置于炉膛103后方的对流竖井101,所述炉膛103的前方设置有锅炉前墙102,所述对流竖井101的后方设置有锅炉后墙104,所述炉膛103的上方按前后顺序依次设置有侧墙Ⅲ膜式水冷壁上集箱10、侧墙Ⅱ膜式水冷壁上集箱11、出口集箱12和侧墙Ⅰ膜式水冷壁上集箱14,所述炉膛103的下方按前后顺序依次设置有侧墙Ⅲ膜式水冷壁下集箱1、侧墙Ⅱ膜式水冷壁下集箱28和侧墙Ⅰ膜式水冷壁下集箱26,所述侧墙Ⅲ膜式水冷壁上集箱10通过侧墙Ⅲ膜式水冷壁7与所述侧墙Ⅲ膜式水冷壁下集箱1连通,所述侧墙Ⅲ膜式水冷壁下集箱1通过第二连通管4与所述侧墙Ⅱ膜式水冷壁上集箱11连通,所述侧墙Ⅱ膜式水冷壁上集箱11通过侧墙Ⅱ膜式水冷壁8与所述侧墙Ⅱ膜式水冷壁下集箱28连通,所述侧墙Ⅰ膜式水冷壁上集箱14通过侧墙Ⅰ膜式水冷壁17与所述侧墙Ⅰ膜式水冷壁下集箱26相连通;A new type of water circulation structure for a gas corner tube hot water boiler, comprising a furnace 103 and a convection shaft 101 arranged behind the furnace 103, a boiler front wall 102 is arranged in front of the furnace 103, and a boiler front wall 102 is arranged behind the convection shaft 101 The rear wall 104, the upper part of the furnace 103 is provided with side wall III membrane type water cooling wall upper header 10, side wall II membrane type water cooling wall upper header 11, outlet header 12 and side wall I membrane type The upper header 14 of the water-cooled wall, and the bottom of the furnace 103 are provided with side wall III membrane water-cooled wall lower header 1, side wall II membrane-type water-cooled wall lower header 28 and side wall I membrane-type water-cooled wall in sequence The lower header 26, the side wall III membrane water wall upper header 10 communicates with the side wall III membrane water wall lower header 1 through the side wall III membrane water wall 7, the side wall III membrane water wall The lower header 1 of the water-cooled wall communicates with the upper header 11 of the side wall II membrane water-cooled wall through the second connecting pipe 4, and the upper header 11 of the side wall II membrane water-cooled wall passes through the side wall II membrane water-cooled wall 8 It communicates with the lower header 28 of the side wall II membrane water-cooled wall, and the side wall I membrane water-cooled wall upper header 14 is connected to the side wall I membrane water-cooled wall lower header through the side wall I membrane water-cooled wall 17 Box 26 is connected;
所述锅炉前墙102的外壁上竖直贴附有前墙角管3,所述前墙角管3的上端通过第三连通管30与所述侧墙Ⅲ膜式水冷壁上集箱10连通,所述前墙角管3的下端与锅炉前墙102下部连接的前墙角管下集箱2连通,所述前墙角管下集箱2通过位于炉膛103底部的水平连接管29与炉膛前后墙水冷壁分配集箱5相连通,所述炉膛前后墙水冷壁分配集箱5分别与炉膛前墙膜式水冷壁6和炉膛后墙膜式水冷壁9连接,所述炉膛前墙膜式水冷壁6和炉膛后墙膜式水冷壁9还分别与所述出口集箱12连通,所述侧墙Ⅱ膜式水冷壁下集箱28分别通过第一连通管a22-1、第一连通管b22-2与对墙的侧墙Ⅰ膜式水冷壁上集箱14相连通,所述第一连通管a22-1、第一连通管b22-2均穿过侧墙Ⅰ膜式水冷壁17;A front corner tube 3 is vertically attached to the outer wall of the boiler front wall 102, and the upper end of the front corner tube 3 communicates with the upper header 10 of the side wall III membrane-type water-cooled wall through a third connecting tube 30. The lower end of the front corner tube 3 communicates with the lower header 2 of the front corner tube connected to the lower part of the boiler front wall 102, and the lower header 2 of the front corner tube is distributed to the water-cooled wall of the front and rear walls of the furnace through the horizontal connecting pipe 29 at the bottom of the furnace 103. The headers 5 are connected, and the distribution headers 5 of the front and rear walls of the furnace are respectively connected with the front wall membrane water wall 6 and the furnace rear wall membrane water wall 9, and the furnace front wall membrane water wall 6 and the furnace The rear wall membrane water-cooled wall 9 is also connected with the outlet header 12 respectively, and the lower header 28 of the side wall II membrane water-cooled wall is respectively connected to the pair through the first connecting pipe a22-1 and the first connecting pipe b22-2. The upper header 14 of the side wall I membrane water cooling wall of the wall is connected, and the first communication pipe a22-1 and the first communication pipe b22-2 both pass through the side wall I membrane water cooling wall 17;
所述锅炉后墙104的外壁上竖直贴附有后墙角管24,所述侧墙Ⅰ膜式水冷壁下集箱26通过所述后墙角管24与后墙角管上集箱18连通,所述后墙角管上集箱18通过水平连通管15与炉膛103顶部设置的对流受热面汇集集箱13连通,所述水平连通管15位于所述对流竖井101的上方,所述锅炉后墙104外壁下部连接有后墙膜式水冷壁下集箱25,所述后墙膜式水冷壁下集箱25与密排膜式水冷壁19连通,所述密排膜式水冷壁19自上而下串联布置有第一级旗式对流受热面23和第二级旗式对流受热面20,所述密排膜式水冷壁19与所述对流受热面汇集集箱13连通。A rear corner tube 24 is vertically attached to the outer wall of the boiler rear wall 104, and the lower header 26 of the side wall I membrane water-cooled wall communicates with the upper header 18 of the rear corner tube through the rear corner tube 24. The upper header 18 of the rear corner tube is communicated with the convection heating surface collection box 13 provided on the top of the furnace 103 through a horizontal communication pipe 15, the horizontal communication pipe 15 is located above the convection shaft 101, and the outer wall of the boiler rear wall 104 The lower part is connected with the lower header 25 of the rear wall membrane type water cooling wall, and the lower header 25 of the rear wall membrane type water cooling wall is connected with the densely packed membrane type water cooling wall 19, and the densely packed membrane type water cooling wall 19 is connected in series from top to bottom A first-stage flag-type convective heating surface 23 and a second-stage flag-type convective heating surface 20 are arranged, and the close-packed membrane water-cooled wall 19 communicates with the convective heating surface collection box 13 .
所述炉膛前后墙水冷壁分配集箱5设置于所述炉膛103内;所述炉膛前墙膜式水冷壁6和炉膛后墙膜式水冷壁9在所述炉膛103内呈前、后相对设置。The distribution header 5 of the water-cooled wall at the front and rear walls of the furnace is arranged in the furnace 103; the membrane-type water-cooled wall 6 at the front of the furnace and the membrane-type water-cooled wall 9 at the rear of the furnace are arranged in front and rear oppositely in the furnace 103 .
所述前墙角管3的两侧角嵌卡合于所述锅炉前墙102外壁两侧棱处;后墙角管24的两侧角嵌卡合于所述锅炉后墙104外壁两侧棱处,所述后墙角管上集箱18设置于所述后墙角管24的上方,所述后墙膜式水冷壁下集箱25设置于所述后墙角管24的下方,后墙膜式水冷壁下集箱25连接有给水管21。The corners on both sides of the front wall corner pipe 3 are engaged with the edges on both sides of the outer wall of the boiler front wall 102; The upper header 18 of the rear corner tube is arranged above the rear corner tube 24, the lower header 25 of the rear wall membrane type water cooling wall is arranged below the rear corner tube 24, and the rear wall membrane type water cooling wall lower The header 25 is connected with a water supply pipe 21 .
所述炉膛前墙膜式水冷壁6和炉膛后墙膜式水冷壁9的上端均与所述出口集箱12连接;所述炉膛前墙膜式水冷壁6和炉膛后墙膜式水冷壁9的下端均与所述炉膛前后墙水冷壁分配集箱5相连通。The upper ends of the front wall membrane type water cooling wall 6 of the furnace hearth and the furnace rear wall membrane type water cooling wall 9 are connected to the outlet header 12; the furnace front wall membrane type water cooling wall 6 and the furnace rear wall membrane type water cooling wall 9 The lower ends of each are in communication with the water wall distribution header 5 of the front and rear walls of the furnace.
所述炉膛前墙膜式水冷壁6及炉膛后墙膜式水冷壁9的结构相同,均由多根光管通过扁钢依次焊接组成。The wall-membrane water-cooled wall 6 at the front of the furnace and the membrane-type water-cooled wall 9 at the rear of the furnace have the same structure, and are composed of a plurality of light pipes sequentially welded through flat steel.
所述侧墙Ⅰ膜式水冷壁17、侧墙Ⅱ膜式水冷壁8和侧墙Ⅲ膜式水冷壁7结构相同,均由多根光管通过扁钢依次焊接组成。The membrane water cooling wall 17 of the side wall I, the membrane water cooling wall 8 of the side wall II and the membrane water cooling wall 7 of the side wall III have the same structure, and are composed of a plurality of light pipes sequentially welded through flat steel.
所述第三连通管30、第二连通管4和第一连通管a22-1、第一连通管b22-2的布置方式使得:由所述侧墙Ⅲ膜式水冷壁上集箱10、侧墙Ⅲ膜式水冷壁7和侧墙Ⅲ膜式水冷壁下集箱1组成的并联管组流动布置为“倒Z”型;由侧墙Ⅱ膜式水冷壁上集箱11、侧墙Ⅱ膜式水冷壁8和侧墙Ⅱ膜式水冷壁下集箱28组成的并联管组流动布置为“Z”型;由所述侧墙Ⅰ膜式水冷壁上集箱14、侧墙Ⅰ膜式水冷壁17和侧墙Ⅰ膜式水冷壁下集箱26组成的并联管组流动布置为“U”型。The arrangement of the third communication pipe 30, the second communication pipe 4, the first communication pipe a22-1, and the first communication pipe b22-2 is such that: the upper header 10 of the side wall III membrane type water-cooled wall, the side wall III The flow arrangement of the parallel pipe group composed of wall III membrane water cooling wall 7 and side wall III membrane water cooling wall lower header 1 is an "inverted Z" type; the side wall II membrane water cooling wall upper header 11, side wall II membrane Type water wall 8 and side wall II membrane water wall lower header 28 make up the flow arrangement of the parallel pipe group in "Z" shape; the side wall I membrane water wall upper header 14, side wall I membrane water cooling The flow arrangement of the parallel tube group composed of the wall 17 and the lower header 26 of the membrane type water-cooled wall of the side wall I is "U" shape.
所述第一连通管a22-1、第一连通管b22-2分别与所述侧墙Ⅱ膜式水冷壁下集箱28、侧墙Ⅰ膜式水冷壁上集箱14连通,且形成穿墙交叉的结构。The first communication pipe a22-1 and the first communication pipe b22-2 communicate with the lower header 28 of the side wall II membrane water-cooled wall and the upper header 14 of the side wall I membrane water-cooled wall respectively, and form a through-wall cross structure.
所述第一级旗式对流受热面23和第二级旗式对流受热面20分别与所述密排膜式水冷壁19焊接;所述密排膜式水冷壁19的上部与所述对流受热面汇集集箱13连接,所述密排膜式水冷壁19的下部与所述后墙膜式水冷壁下集箱25连通;所述第一级旗式对流受热面23和第二级旗式对流受热面20分别采用多根不同管径的光管,多根光管顺次排列且光管的管径依次减小。The first-stage flag-type convective heating surface 23 and the second-stage flag-type convective heating surface 20 are respectively welded to the close-packed membrane water-cooled wall 19; The surface collection header 13 is connected, and the lower part of the close-packed membrane water-cooled wall 19 communicates with the lower header 25 of the rear wall membrane-type water-cooled wall; the first-stage flag-type convection heating surface 23 and the second-stage flag-type The convection heating surface 20 adopts a plurality of light pipes with different diameters respectively, and the plurality of light pipes are arranged in sequence and the diameters of the light pipes are successively reduced.
所述密排膜式水冷壁19由多个水冷壁管组成,相邻两个水冷壁管之间通过连接部件焊接;所述水冷壁管的管径为Φ60mm~Φ133mm,相邻的两根水冷壁管间距为62mm~135mm。The close-packed membrane water-cooled wall 19 is composed of a plurality of water-cooled wall tubes, and two adjacent water-cooled wall tubes are welded by connecting parts; the diameter of the water-cooled wall tubes is Φ60mm~Φ133mm, The wall tube spacing is 62mm ~ 135mm.
本实用新型和现有技术相比较,具有如下优点:Compared with the prior art, the utility model has the following advantages:
1)本实用新型燃气角管热水锅炉新型水循环结构中,将锅炉侧墙依据热负荷不同分割成三级受热面,受热面内工质采用多次强制上升流动,极大地减小了水管内的流量偏差,且所有受热面中的工质全部上升流动,下降流动均为非受热面管,完全杜绝了常规自然循环或常规强制循环回路设计中因存在部分水冷壁管下降流动而可能出现的停滞或倒流的非正常水动力工况,膜式水冷壁中的工质全部上升流动确保工质具有较高的质量流速,有效地消除了因管内发生过冷沸腾导致管壁温升高而引起爆管的危险工况。1) In the new water circulation structure of the gas corner tube hot water boiler of the utility model, the side wall of the boiler is divided into three heating surfaces according to the different heat loads, and the working medium in the heating surface adopts multiple forced upward flow, which greatly reduces the internal pressure of the water pipe. The flow deviation, and all the working medium in all heating surfaces flow upwards, and the downward flow is all non-heating surface tubes, which completely eliminates the possible occurrence of conventional natural circulation or conventional forced circulation circuit design due to the downward flow of some water-cooled wall tubes In abnormal hydrodynamic conditions of stagnation or reverse flow, all the working medium in the membrane water wall flows upwards to ensure a high mass flow rate of the working medium, which effectively eliminates the temperature rise of the tube wall caused by supercooled boiling in the tube. Hazardous conditions of pipe bursts.
2)本实用新型燃气角管热水锅炉新型水循环结构中,锅炉第三连通管、第二连通管和第一连通管的布置方式使得侧墙Ⅲ膜式水冷壁、侧墙Ⅱ膜式水冷壁、侧墙Ⅰ膜式水冷壁对应并联管组流动布置为“倒Z”型、“Z”型和“U”型,由于并联管组呈“U”型布置时,水冷壁管组压差分布较为均匀,而并联管组呈“Z”型、“倒Z”型布置时,远离汇集集箱出口端区域的水冷壁管进出口压差小于近集箱出口端区域的水冷壁管进出口压差,压差大则工质流速高,因而使得温度较高的炉膛中央区域附近的侧墙膜式水冷壁管内工质流速高,温度较低区域的侧墙膜式水冷壁管内工质流速低,而温度分布较为均匀的对流竖井侧墙膜式水冷壁管内工质流速均匀,极大地减小了侧墙膜式壁管整体的热偏差。2) In the new water circulation structure of the gas corner tube hot water boiler of the utility model, the arrangement of the third connecting pipe, the second connecting pipe and the first connecting pipe of the boiler makes the side wall III membrane water wall and the side wall II membrane water wall 1. The flow arrangement of side wall I membrane type water wall corresponding to the parallel tube group is "inverted Z", "Z" and "U". Since the parallel tube group is arranged in "U" shape, the pressure difference distribution of the water wall tube group It is relatively uniform, and when the parallel tube group is arranged in a "Z" or "inverted Z" shape, the pressure difference between the inlet and outlet of the water-cooled wall tubes in the area far away from the outlet end of the collecting box is smaller than the pressure difference between the inlet and outlet of the water-cooled wall tubes in the area near the outlet end of the header box. If the pressure difference is large, the flow rate of the working medium is high, so the flow rate of the working medium in the side wall membrane water wall tube near the central area of the furnace with high temperature is high, and the flow rate of the working medium in the side wall membrane water wall tube in the lower temperature area is low , while the convection shaft with relatively uniform temperature distribution has a uniform flow rate of the working medium in the side wall membrane water wall tube, which greatly reduces the overall thermal deviation of the side wall membrane wall tube.
3)本实用新型燃气角管热水锅炉新型水循环结构中,锅炉第一连通管连通侧墙Ⅱ膜式水冷壁下集箱与对墙的侧墙Ⅰ膜式水冷壁上集箱并形成穿墙交叉结构,在做下降管的同时亦作为对流竖井内第一级旗式对流受热面和第二级旗式对流受热面的承重部件,该结构设计极其巧妙,空间利用率高,是一种新型的且能极大节省钢材的高温区对流受热面固定安装方法。3) In the new water circulation structure of the gas corner tube hot water boiler of the utility model, the first connecting pipe of the boiler connects the lower header of the side wall II membrane water-cooled wall with the upper header of the side wall I membrane water-cooled wall of the opposite wall and forms a through-wall The cross structure, as the downcomer, is also used as the load-bearing part of the first-stage flag-type convection heating surface and the second-stage flag-type convection heating surface in the convection shaft. The structure design is extremely ingenious and the space utilization rate is high. It is a new type of The fixed installation method of the convection heating surface in the high temperature area is unique and can greatly save steel.
4)本实用新型燃气角管热水锅炉新型水循环结构中,对流竖井内第一级旗式对流受热面的管径大于第二级旗式对流受热面的管径,并且无需穿墙,直接和密排膜式水冷壁焊接以减小管束横向节距,从而增大烟气从炉膛进入烟道并流经烟道尾部受热面时的流速,强化烟气与受热面之间的换热,提高了对流受热面金属壁面温度,有效地降低了烟气中因硫酸结露而引起低温腐蚀的危险工况。4) In the new water circulation structure of the gas angle tube hot water boiler of the utility model, the pipe diameter of the first-stage flag-type convection heating surface in the convection shaft is larger than the pipe diameter of the second-stage flag-type convection heating surface, and there is no need to pass through the wall, directly and The close-packed membrane water wall is welded to reduce the transverse pitch of the tube bundle, thereby increasing the flow velocity of the flue gas from the furnace into the flue and flowing through the heating surface at the tail of the flue, strengthening the heat exchange between the flue gas and the heating surface, and improving The temperature of the metal wall surface on the convective heating surface is lowered, which effectively reduces the dangerous working condition of low-temperature corrosion caused by sulfuric acid condensation in the flue gas.
5)本实用新型燃气角管热水锅炉新型水循环结构在突然停电后,自动放气阀打开,集箱、下降管和上升管又可构成自然循环回路,具有超强的停电保护功能。5) The new water circulation structure of the gas corner tube hot water boiler of the utility model will automatically open the air release valve after a sudden power failure, and the header, downcomer and riser can form a natural circulation loop, which has a super power failure protection function.
附图说明Description of drawings
图1是本实用新型燃气角管热水锅炉新型水循环结构的侧视图。Fig. 1 is a side view of the new water circulation structure of the utility model gas angle tube hot water boiler.
图2是本实用新型燃气角管热水锅炉新型水循环结构的主视半剖结构示意图。Fig. 2 is a schematic diagram of the front half-section structure of the new water circulation structure of the gas angle tube hot water boiler of the utility model.
图3是图2沿A-A向的主要循环管路结构示意图。Fig. 3 is a schematic structural diagram of the main circulation pipeline along the direction A-A in Fig. 2 .
图4是图2沿B-B向的主要循环管路结构示意图。Fig. 4 is a schematic structural diagram of the main circulation pipeline along the B-B direction in Fig. 2 .
图5是本实用新型燃气角管热水锅炉新型水循环结构中密排管膜式水冷壁的结构图。Fig. 5 is a structural diagram of the close-packed tube-membrane water wall in the new water circulation structure of the utility model gas angle tube hot water boiler.
图6是本实用新型燃气角管热水锅炉新型水循环结构中扁钢型光管构成的膜式水冷壁的结构图。Fig. 6 is a structural diagram of a membrane-type water-cooled wall made of flat steel-shaped light tubes in the new water circulation structure of the utility model gas angle tube hot water boiler.
图中,1.侧墙Ⅲ膜式水冷壁下集箱,2.前墙角管下集箱,3.前墙角管,4.第二连通管,5.炉膛前后墙水冷壁分配集箱,6.炉膛前墙膜式水冷壁,7.侧墙Ⅲ膜式水冷壁,8.侧墙Ⅱ膜式水冷壁,9.炉膛后墙膜式水冷壁,10.侧墙Ⅲ膜式水冷壁上集箱,11.侧墙Ⅱ膜式水冷壁上集箱,12.出口集箱,13.对流受热面汇集集箱,14.侧墙Ⅰ膜式水冷壁上集箱,15.水平连通管,17.侧墙Ⅰ膜式水冷壁,18.后墙角管上集箱,19.密排膜式水冷壁,20.第二级旗式对流受热面,21.给水管,22-1.第一连通管a,22-2.第二连通管b,23.第一级旗式对流受热面,24.后墙角管,25.后墙膜式水冷壁下集箱,26.侧墙Ⅰ膜式水冷壁下集箱,27.烟气出口,28.侧墙Ⅱ膜式水冷壁下集箱,29.水平连接管,30.第三连通管,101.对流竖井,102.锅炉前墙,103.炉膛,104.锅炉后墙。In the figure, 1. Side wall III membrane type water-cooled wall lower header, 2. Front corner tube lower header, 3. Front corner tube, 4. Second connecting tube, 5. Furnace front and rear wall water-cooled wall distribution header, 6 .Front wall membrane water cooling wall, 7. Side wall III membrane water cooling wall, 8. Side wall II membrane water cooling wall, 9. Furnace rear wall membrane water cooling wall, 10. Side wall III membrane water cooling wall upper set Box, 11. Side wall Ⅱ membrane type water cooling wall upper header, 12. Outlet header, 13. Convection heating surface collecting header, 14. Side wall Ⅰ membrane type water cooling wall upper header, 15. Horizontal connecting pipe, 17 .Side wall I membrane water wall, 18. Rear corner tube upper header, 19. Close-packed membrane water wall, 20. Second-stage flag-type convection heating surface, 21. Water supply pipe, 22-1. First connection Pipe a, 22-2. Second connecting pipe b, 23. First-stage flag-type convection heating surface, 24. Rear wall corner pipe, 25. Rear wall membrane type water-cooled lower header, 26. Side wall I membrane type water cooling Header under the wall, 27. Flue gas outlet, 28. Side wall II membrane water-cooled wall header, 29. Horizontal connecting pipe, 30. Third connecting pipe, 101. Convection shaft, 102. Boiler front wall, 103. Furnace, 104. Boiler rear wall.
具体实施方式Detailed ways
下面结合附图对本实用新型作更详细的说明。Below in conjunction with accompanying drawing, the utility model is described in more detail.
本实用新型燃气角管热水锅炉新型水循环结构,其结构如图1所示,包括有炉膛103和设置于炉膛103后方的对流竖井101,炉膛103的前方设置有锅炉前墙102,对流竖井101的后方设置有锅炉后墙104,炉膛103的上方按前后顺序依次设置有侧墙Ⅲ膜式水冷壁上集箱10、侧墙Ⅱ膜式水冷壁上集箱11、出口集箱12、侧墙Ⅰ膜式水冷壁上集箱14,炉膛103的下方按前后顺序依次设置有侧墙Ⅲ膜式水冷壁下集箱1、侧墙Ⅱ膜式水冷壁下集箱28、侧墙Ⅰ膜式水冷壁下集箱26,侧墙Ⅲ膜式水冷壁上集箱10通过侧墙Ⅲ膜式水冷壁7与侧墙Ⅲ膜式水冷壁下集箱1相连通,侧墙Ⅲ膜式水冷壁下集箱1通过第二连通管4与侧墙Ⅱ膜式水冷壁上集箱11相连通,侧墙Ⅱ膜式水冷壁上集箱11通过侧墙Ⅱ膜式水冷壁8与侧墙Ⅱ膜式水冷壁下集箱28相连通,侧墙Ⅰ膜式水冷壁上集箱14通过侧墙Ⅰ膜式水冷壁17与侧墙Ⅰ膜式水冷壁下集箱26相连通;锅炉前墙102的外壁上竖直贴附有前墙角管3,前墙角管3的上端通过第三连通管30与侧墙Ⅲ膜式水冷壁上集箱10连通,前墙角管3的下端与锅炉前墙102下部连接的前墙角管下集箱2连通,前墙角管下集箱2通过位于炉膛103底部的水平连接管29与炉膛前后墙水冷壁分配集箱5相连通,炉膛前后墙水冷壁分配集箱5分别与炉膛前墙膜式水冷壁6和炉膛后墙膜式水冷壁9连接,炉膛前墙膜式水冷壁6和炉膛后墙膜式水冷壁9还分别与出口集箱12连通,如图2和图3所示,侧墙Ⅱ膜式水冷壁下集箱28分别通过第一连通管a22-1、第一连通管b22-2与对墙的侧墙Ⅰ膜式水冷壁上集箱14相连通,第一连通管a22-1、第一连通管b22-2均穿过侧墙Ⅰ膜式水冷壁17,锅炉后墙104的外壁上竖直贴附有后墙角管24,侧墙Ⅰ膜式水冷壁下集箱26通过后墙角管24与后墙角管上集箱18连通,后墙角管上集箱18通过水平连通管15与炉膛103顶部设置的对流受热面汇集集箱13连通,水平连通管15位于对流竖井101的上方,锅炉后墙104外壁下部连接有后墙膜式水冷壁下集箱25,后墙膜式水冷壁下集箱25与密排膜式水冷壁19相连通,密排膜式水冷壁19自上而下串联设置有第一级旗式对流受热面23和第二级旗式对流受热面20,密排的膜式水冷壁19与对流受热面汇集集箱13连通。The utility model has a novel water circulation structure for a gas-fired corner tube hot water boiler, as shown in Figure 1, which includes a furnace 103 and a convection shaft 101 arranged behind the furnace 103, and a boiler front wall 102 and a convection shaft 101 are arranged in front of the furnace 103. Boiler rear wall 104 is set at the rear of the furnace, and above the furnace 103, side wall III membrane water-cooled wall upper header 10, side wall II membrane water-cooled wall upper header 11, outlet header 12, side wall Ⅰ Membrane water-cooled wall upper header 14, the lower part of the furnace 103 is provided with side wall Ⅲ membrane water-cooled wall lower header 1, side wall Ⅱ membrane-type water-cooled wall lower header 28, side wall Ⅰ membrane-type water-cooled The lower header 26 of the wall, the upper header 10 of the side wall III membrane water-cooled wall are connected with the lower header 1 of the side wall III membrane water-cooled wall through the side wall III membrane water-cooled wall 7, and the lower header of the side wall III membrane water-cooled wall The box 1 is connected with the upper header 11 of the side wall II membrane water cooling wall through the second connecting pipe 4, and the upper header 11 of the side wall II membrane water cooling wall is connected with the side wall II membrane water cooling wall 8 through the side wall II membrane water cooling wall The lower header 28 of the wall is connected, and the upper header 14 of the side wall I membrane water-cooled wall is connected with the lower header 26 of the side wall I membrane water-cooled wall through the side wall I membrane water-cooled wall 17; the outer wall of the boiler front wall 102 The front corner tube 3 is vertically attached, the upper end of the front corner tube 3 communicates with the side wall III membrane water wall upper header 10 through the third connecting tube 30, and the lower end of the front corner tube 3 is connected with the lower part of the boiler front wall 102 The lower header 2 of the front corner tube is connected, and the lower header 2 of the front corner tube is connected with the distribution header 5 of the water-cooled wall of the front and rear walls of the furnace through the horizontal connecting pipe 29 at the bottom of the furnace 103, and the distribution header 5 of the water-cooled wall of the front and rear walls of the furnace is respectively connected with The front wall membrane water cooling wall 6 of the furnace is connected with the furnace rear wall membrane water cooling wall 9, and the furnace front wall membrane water cooling wall 6 and the furnace rear wall membrane water cooling wall 9 are respectively connected with the outlet header 12, as shown in Fig. 2 and Fig. As shown in 3, the lower header 28 of the side wall II membrane water-cooled wall is connected to the upper header 14 of the side wall I membrane water-cooled wall on the opposite wall through the first connecting pipe a22-1 and the first connecting pipe b22-2 respectively. Both the first connecting pipe a22-1 and the first connecting pipe b22-2 pass through the side wall I membrane water-cooled wall 17, and the rear corner pipe 24 is vertically attached to the outer wall of the boiler rear wall 104, and the side wall I membrane water-cooled The header under the wall 26 communicates with the upper header 18 of the rear corner tube through the rear corner tube 24, and the upper header 18 of the rear corner tube communicates with the convection heating surface collecting header 13 provided on the top of the furnace 103 through the horizontal communication tube 15, and the horizontal communication tube 15 is located above the convection shaft 101, and the lower part of the outer wall of the boiler rear wall 104 is connected with the lower header 25 of the rear wall membrane water cooling wall, and the lower header 25 of the rear wall membrane water cooling wall is connected with the densely packed membrane type water cooling wall 19. The membrane water cooling wall 19 is provided with the first-stage flag-type convective heating surface 23 and the second-stage flag-type convective heating surface 20 in series from top to bottom.
侧墙Ⅲ膜式水冷壁7为连接侧墙Ⅲ膜式水冷壁上集箱10与侧墙Ⅲ膜式水冷壁下集箱1形成的水冷壁,侧墙Ⅱ膜式水冷壁8为连接侧墙Ⅱ膜式水冷壁上集箱11与侧墙Ⅱ膜式水冷壁下集箱28形成的水冷壁,侧墙Ⅰ膜式水冷壁17为连接侧墙Ⅰ膜式水冷壁上集箱14与侧墙Ⅰ膜式水冷壁下集箱26形成的水冷壁。炉膛103的两侧均为由侧墙Ⅰ膜式水冷壁17、侧墙Ⅱ膜式水冷壁8、侧墙Ⅲ膜式水冷壁7组成的三级受热面。Side wall III membrane water cooling wall 7 is the water cooling wall formed by connecting side wall III membrane water cooling wall upper header 10 and side wall III membrane water cooling wall lower header 1, and side wall II membrane water cooling wall 8 is the connecting side wall The water wall formed by the upper header 11 of the membrane type water cooling wall of II and the lower header 28 of the membrane type water cooling wall of the side wall II, and the upper header 14 of the membrane type water cooling wall of the side wall I of the side wall is connected with the upper header 14 of the membrane type water cooling wall of the side wall and the side wall Ⅰ The water-cooled wall formed by the lower header 26 of the membrane-type water-cooled wall. Both sides of the furnace 103 are three-stage heating surfaces composed of side wall I membrane water cooling wall 17 , side wall II membrane water cooling wall 8 and side wall III membrane water cooling wall 7 .
作为本实用新型的优选实施方式,炉膛前后墙水冷壁分配集箱5设置于炉膛103内;炉膛前墙膜式水冷壁6和炉膛后墙膜式水冷壁9在炉膛103内呈前、后相对设置。As a preferred embodiment of the present utility model, the water-cooled wall distribution header 5 on the front and rear walls of the furnace is arranged in the furnace 103; set up.
作为本实用新型的优选实施方式,前墙角管3的两侧角嵌卡合于锅炉前墙102外壁两侧棱处;后墙角管24两侧角嵌卡合于锅炉后墙104外壁两侧棱处,后墙角管上集箱18设置于后墙角管24的上方,后墙膜式水冷壁下集箱25设置于后墙角管24的下方,后墙膜式水冷壁下集箱25连接有给水管21。As a preferred embodiment of the present utility model, the corners on both sides of the front wall corner tube 3 are engaged with the edges on both sides of the outer wall of the boiler front wall 102; , the upper header 18 of the rear wall corner tube is set above the rear wall corner tube 24, the lower header 25 of the rear wall membrane water-cooled wall is set under the rear wall corner tube 24, and the lower header 25 of the rear wall membrane water-cooled wall is connected to the water supply Tube 21.
侧墙Ⅲ膜式水冷壁上集箱10、侧墙Ⅱ膜式水冷壁上集箱11及侧墙Ⅰ膜式水冷壁上集箱14是由锅炉上部大直径管隔断为三个空间而形成。Side wall III membrane water cooling wall upper header 10, side wall II membrane water cooling wall upper header 11 and side wall I membrane water cooling wall upper header 14 are formed by dividing large-diameter tubes in the upper part of the boiler into three spaces.
炉膛前墙膜式水冷壁6和炉膛后墙膜式水冷壁9的上端均与出口集箱12连通,炉膛前墙膜式水冷壁6和炉膛后墙膜式水冷壁9的下端均与炉膛前后墙水冷壁分配集箱5连通。The upper ends of the front wall membrane water cooling wall 6 of the furnace and the furnace rear wall membrane water cooling wall 9 are connected with the outlet header 12, and the lower ends of the furnace front wall membrane water cooling wall 6 and the furnace rear wall membrane water cooling wall 9 are connected with the front and rear of the furnace. The wall water-cooled wall distribution headers 5 are connected.
炉膛前墙膜式水冷壁6、炉膛后墙膜式水冷壁9、侧墙Ⅲ膜式水冷壁7、侧墙Ⅱ膜式水冷壁8及侧墙Ⅰ膜式水冷壁17的结构相同,结构如图6所示,均由多根光管通过扁钢依次焊接组成;炉膛前墙膜式水冷壁6、炉膛后墙膜式水冷壁9、侧墙Ⅰ膜式水冷壁17、侧墙Ⅱ膜式水冷壁8、侧墙Ⅲ膜式水冷壁7上的每根光管内,热水均呈强制上升流动。The membrane water cooling wall 6 at the front wall of the furnace, the membrane water cooling wall 9 at the rear wall of the furnace, the membrane water cooling wall 7 of the side wall III, the membrane water cooling wall 8 of the side wall II and the membrane water cooling wall 17 of the side wall I are of the same structure, and the structure is as follows As shown in Figure 6, they are all composed of a plurality of light pipes welded sequentially through flat steel; the furnace front wall membrane type water cooling wall 6, the furnace rear wall membrane type water cooling wall 9, the side wall I membrane type water cooling wall 17, the side wall II membrane type water cooling wall In each light pipe on the water-cooled wall 8 and the membrane-type water-cooled wall 7 of the side wall III, the hot water flows upward forcibly.
如图4所示,第三连通管30、第二连通管4和第一连通管a22-1、第一连通管b22-2的布置方式使得:由侧墙Ⅲ膜式水冷壁上集箱10、侧墙Ⅲ膜式水冷壁7、侧墙Ⅲ膜式水冷壁下集箱1组成的并联管组流动布置为“倒Z”型;由侧墙Ⅱ膜式水冷壁上集箱11、侧墙Ⅱ膜式水冷壁8、侧墙Ⅱ膜式水冷壁下集箱28组成的并联管组流动布置为“Z”型;由侧墙Ⅰ膜式水冷壁上集箱14、侧墙Ⅰ膜式水冷壁17、侧墙Ⅰ膜式水冷壁下集箱26组成的并联管组流动布置为“U”型。第二连通管4和第一连通管a22-1、第一连通管b22-2内水的流向与前墙角管3、后墙角管24一致,全部为下降流动。As shown in Figure 4, the arrangement of the third communication pipe 30, the second communication pipe 4, the first communication pipe a22-1, and the first communication pipe b22-2 is such that: the header 10 on the side wall III membrane type water-cooled wall , side wall III membrane water cooling wall 7, and side wall III membrane water cooling wall lower header 1. The flow arrangement of the parallel pipe group composed of Ⅱ membrane water cooling wall 8 and side wall II membrane water cooling wall lower header 28 is “Z” type; the side wall I membrane water cooling wall upper header 14 and side wall I membrane The flow arrangement of the parallel tube group composed of the wall 17 and the lower header 26 of the side wall I membrane water wall is "U" shape. The flow direction of the water in the second communication pipe 4, the first communication pipe a22-1, and the first communication pipe b22-2 is consistent with the front wall corner pipe 3 and the rear wall corner pipe 24, all of which are descending flows.
如图2所示,第一连通管a22-1、第一连通管b22-2分别与侧墙Ⅱ膜式水冷壁下集箱28、侧墙Ⅰ膜式水冷壁上集箱14连通,且形成穿墙交叉的结构;第一连通管a22-1、第一连通管b22-2在做下降管的同时用作对流竖井101内第一级旗式对流受热面23和第二级旗式对流受热面20的承重部件。As shown in Figure 2, the first communication pipe a22-1 and the first communication pipe b22-2 communicate with the lower header 28 of the side wall II membrane water cooling wall and the upper header 14 of the side wall I membrane water cooling wall respectively, and form Cross-wall structure; the first communication pipe a22-1 and the first communication pipe b22-2 are used as the downcomer while serving as the first-stage flag-type convection heating surface 23 and the second-stage flag-type convection heating surface in the convection shaft 101 The load-bearing part of the surface 20.
对流竖井101中,第一级旗式对流受热面23和第二级旗式对流受热面20分别采用不同管径(前者的管径大于后者的管径)的光管顺列布置,第一级旗式对流受热面23、第二级旗式对流受热面20分别与密排膜式水冷壁19焊接,密排膜式水冷壁19的上部与对流受热面汇集集箱13连接,密排膜式水冷壁19的下部与后墙膜式水冷壁下集箱25连通。In the convection shaft 101, the first-stage flag-type convective heating surface 23 and the second-stage flag-type convective heating surface 20 respectively adopt bare pipes with different pipe diameters (the diameter of the former is larger than that of the latter), and the first The first-stage flag-type convection heating surface 23 and the second-stage flag-type convection heating surface 20 are respectively welded to the close-packed membrane water wall 19, and the upper part of the close-packed membrane water wall 19 is connected to the convection heating surface collection box 13, and the close-packed membrane The bottom of the type water cooling wall 19 communicates with the lower header 25 of the rear wall membrane type water cooling wall.
作为本实用新型的优选实施方式,如图5所示,密排膜式水冷壁19由多个水冷壁光管组成,相邻两个水冷壁光管之间通过焊接的方式连接,水冷壁管的管径为Φ60mm~Φ133mm,与之相应的相邻的两根水冷壁管间距为62mm~135mm。As a preferred embodiment of the present utility model, as shown in Figure 5, the close-packed membrane water-cooled wall 19 is composed of a plurality of water-cooled wall light tubes, and two adjacent water-cooled wall light tubes are connected by welding, and the water-cooled wall tubes The diameter of the tube is Φ60mm~Φ133mm, and the distance between two adjacent water wall tubes is 62mm~135mm.
炉膛前墙膜式水冷壁6的受热面、炉膛后墙膜式水冷壁9的受热面、侧墙Ⅰ膜式水冷壁17的受热面、侧墙Ⅱ膜式水冷壁8的受热面、侧墙Ⅲ膜式水冷壁7的受热面以及密排膜式水冷壁19的受热面工质全部上升流动。The heating surface of the membrane water cooling wall 6 in the front wall of the furnace, the heating surface of the membrane water cooling wall 9 in the rear wall of the furnace, the heating surface of the side wall I membrane water cooling wall 17, the heating surface of the side wall II membrane water cooling wall 8, the side wall The working medium on the heating surface of III membrane water cooling wall 7 and the heating surface of close-packed membrane water cooling wall 19 all ascends and flows.
本实用新型燃气角管热水锅炉新型水循环结构的工作原理如下:The working principle of the new water circulation structure of the utility model gas angle tube hot water boiler is as follows:
当水通过给水管21送入与密排膜式水冷壁19相连接的对流竖井后墙膜式水冷壁下集箱25时,均匀分配给密排膜式水冷壁19,然后依次流经与密排膜式水冷壁19串联的第一级旗式对流受热面23和第二级旗式对流受热面20,并在上升流动过程中吸收对流竖井101中高温烟气放出的热量,被加热到预设温度后,进入与密排膜式水冷壁19上部导通的对流受热面汇集集箱13,然后通过水平连通管15将工质引至位于锅炉后墙104垂直于水冷壁管的后墙角管上集箱18,并将水分配给锅炉后墙104外壁两侧棱的后墙角管24,在锅炉后墙104外不受热下降流动,均匀分配给侧墙Ⅰ膜式水冷壁下集箱26,通过侧墙Ⅰ膜式水冷壁17吸收对流竖井101中高温烟气放出的热量上升流动,被加热到更高的温度后,分别进入侧墙Ⅰ膜式水冷壁上集箱14,在侧墙Ⅰ膜式水冷壁上集箱14中混合后,通过第一连通管a22-1、第一连通管b22-2分别穿墙引至对墙的侧墙Ⅱ膜式水冷壁下集箱28,通过侧墙Ⅱ膜式水冷壁8吸收炉膛103中高温烟气放出的热量上升流动,被加热到更高的温度后,进入炉膛103的侧墙Ⅱ膜式水冷壁上集箱11,通过第二连通管4引至侧墙Ⅲ膜式水冷壁下集箱1,通过侧墙Ⅲ膜式水冷壁7吸收炉膛103中高温烟气放出的热量上升流动,被加热到更高的温度后,进入锅炉侧墙Ⅲ膜式水冷壁上集箱10,通过第三连通管30将水引至锅炉前墙102外壁两侧棱的前墙角管3,在锅炉前墙102外不受热下降流动,进入锅炉前墙角管下集箱2,然后通过位于炉膛103底部的水平连接管29,进入炉膛前后墙水冷壁分配集箱5,分别通过炉膛前墙膜式水冷壁6和炉膛后墙膜式水冷壁9吸收炉膛103中高温烟气放出的热量上升流动并汇集至出口集箱12,经过各级吸热面不断吸热,达到额定出口热水温度送入管网;而当气体燃料燃烧产生的高温烟气释放热量通过辐射传热传递给炉膛前墙膜式水冷壁6、炉膛后墙膜式水冷壁9、侧墙Ⅲ膜式水冷壁7、侧墙Ⅱ膜式水冷壁8经过炉膛后墙水冷烟窗16的辐射和对流换热后,高温烟气通过转向室转弯180°,后进入对流竖井101,依次横向冲刷第二级旗式对流受热面20和第一级旗式对流受热面23并与侧墙Ⅰ膜式水冷壁17进行对流换热,烟气在本体完成换热后从锅炉下部的烟气出口27排出。When the water is sent into the lower header 25 of the convection shaft rear wall membrane water wall connected to the close-packed membrane water-cooled wall 19 through the water supply pipe 21, it is evenly distributed to the close-packed membrane water-cooled wall 19, and then flows through the close-packed membrane water-cooled wall 19 in sequence. The first-stage flag-type convective heating surface 23 and the second-stage flag-type convective heating surface 20 connected in series with the film-row water wall 19 absorb the heat released by the high-temperature flue gas in the convection shaft 101 during the upward flow process, and are heated to a predetermined temperature. After setting the temperature, it enters the convection heating surface collection box 13 connected to the upper part of the close-packed membrane water cooling wall 19, and then leads the working fluid to the rear corner tube at the boiler rear wall 104 perpendicular to the water cooling wall tube through the horizontal connecting pipe 15 The upper header 18 distributes the water to the rear corner tubes 24 on both sides of the outer wall of the boiler rear wall 104, flows down and flows outside the boiler rear wall 104 without being heated, and distributes water evenly to the lower header 26 of the side wall I membrane water-cooled wall. The heat released by the high-temperature flue gas in the convection shaft 101 is absorbed by the side wall I membrane water-cooled wall 17 to rise and flow, and after being heated to a higher temperature, it enters the side wall I membrane water-cooled wall upper header 14 respectively, and in the side wall I After mixing in the upper header 14 of the membrane-type water-cooled wall, the first connecting pipe a22-1 and the first connecting pipe b22-2 are respectively passed through the wall to lead to the side wall II membrane-type water-cooled lower header 28 of the opposite wall. Wall II membrane water-cooled wall 8 absorbs the heat released by the high-temperature flue gas in the furnace 103 and flows upwards. After being heated to a higher temperature, it enters the upper header 11 of the side wall II membrane water-cooled wall of the furnace 103 and passes through the second connecting pipe. 4 leads to the lower header 1 of the side wall III membrane water-cooled wall, absorbs the heat released by the high-temperature flue gas in the furnace 103 through the side wall III membrane water-cooled wall 7, and flows up and flows. After being heated to a higher temperature, it enters the side wall of the boiler III Membrane-type water-cooled wall upper header 10, through the third connecting pipe 30, the water is led to the front wall corner tubes 3 on both sides of the outer wall of the boiler front wall 102, and flows down outside the boiler front wall 102 without being heated, and enters the bottom of the boiler front corner tube The header 2 then passes through the horizontal connecting pipe 29 at the bottom of the furnace 103, enters the distribution header 5 of the water-cooled walls of the front and rear walls of the furnace, and passes through the front wall membrane water wall 6 and the furnace rear wall membrane water wall 9 respectively to absorb in the furnace 103 The heat released by the high-temperature flue gas rises and flows and collects to the outlet header 12, and continuously absorbs heat through the heat-absorbing surfaces at all levels, and reaches the rated outlet hot water temperature and sends it to the pipe network; when the high-temperature flue gas released by gas fuel combustion passes through the Radiation heat transfer to the furnace front wall membrane water cooling wall 6, the furnace rear wall membrane water cooling wall 9, the side wall III membrane water cooling wall 7, and the side wall II membrane water cooling wall 8 through the radiation of the furnace rear wall water cooling smokestack 16 After exchanging heat with convection, the high-temperature flue gas turns 180° through the steering chamber, and then enters the convection shaft 101, where it scours the second-stage flag-type convection heating surface 20 and the first-stage flag-type convection heating surface 23 in sequence and connects with the side wall I membrane The type water wall 17 performs convective heat exchange, and the flue gas is discharged from the flue gas outlet 27 at the lower part of the boiler after the body completes the heat exchange.
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Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104019552A (en) * | 2014-05-30 | 2014-09-03 | 西安交通大学 | Water circulation structure of fuel gas corner tube hot-water boiler |
CN104296122A (en) * | 2014-11-03 | 2015-01-21 | 上海锅炉厂有限公司 | Boiler wall supporting and hanging system of variable section tower boiler |
CN110848654A (en) * | 2019-11-27 | 2020-02-28 | 哈尔滨红光锅炉总厂有限责任公司 | Large-capacity longitudinally-arranged corner tube boiler |
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2014
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Cited By (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN104019552A (en) * | 2014-05-30 | 2014-09-03 | 西安交通大学 | Water circulation structure of fuel gas corner tube hot-water boiler |
CN104019552B (en) * | 2014-05-30 | 2016-08-24 | 西安交通大学 | A kind of combustion gas angle pipe hot water boiler water circulation structure |
CN104296122A (en) * | 2014-11-03 | 2015-01-21 | 上海锅炉厂有限公司 | Boiler wall supporting and hanging system of variable section tower boiler |
CN110848654A (en) * | 2019-11-27 | 2020-02-28 | 哈尔滨红光锅炉总厂有限责任公司 | Large-capacity longitudinally-arranged corner tube boiler |
CN110848654B (en) * | 2019-11-27 | 2022-12-23 | 哈尔滨红光锅炉总厂有限责任公司 | Large-capacity longitudinally-arranged corner tube boiler |
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