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Improvements relating to vapour generating and superheating units and to the control of the temperature of superheated vapour

机译:有关蒸汽发生和过热装置以及过热蒸汽温度控制的改进

摘要

738,214. Steam superheaters, BABCOCK & WILCOX, Ltd. June 4, 1953 [June 4, 1952], No. 15417/53. Class 123 (3). A steam boiler comprises a furnace chamber 10 divided into two vertical compartments by a mid-partition formed of steam generating tubes, the front and side walls of the chamber being lined with generating tubes whilst the rear or baffle wall 24, which is also formed of generating tubes, serves to separate the furnace from an uppass 32 in which is disposed primary and secondary convection superheaters 90, 96 and an economizer 156. Each furnace compartment is downwardly fired by a group of pulverized fuel burners 100, the burner groups, which are enclosed in windboxes 104, 105, being spaced inwardly from the compartment walls, so that in operation, combustion gases pass down through each compartment without impinging on the walls thereof, the gases then turning laterally for upward flow through pass 32. The steam generating tubes extend between headers such as 20, 38 and a steam and water drum 26 from which steam flows through the primary superheater 90, an interstage attemperator 93 and the secondary superheater 96 to the final outlet header 98. To maintain the temperature of superheat constant over a wide load range, the attemperator 93 is used at high loadings when the superheat temperature tends to rise above the required value, whilst at low loadings when the steam temperature tends to fall, flue gas is recirculated to the furnace to reduce the radiant heat absorption therein and give a corresponding increase in the heat content of the gases entering the superheater pass 32. The flue gas is withdrawn from outlet duct 155 by a fan 150 which discharges it through ducts 140, 142, 144 and damper controlled vertical ducts such as 120, 125 into manifolds 110 ... 113 and 114 ... 117 surrounding respectively the windboxes 104, 105, the gas passing through slots 118 provided along the undersides of the manifolds to form a downwardly moving layer on each wall surface of the furnace compartments thus partly screening the lining tubes thereof from transfer of radiant heat from the combustion products passing from the burners centrally down each compartment. By operation of the dampers in the vertical ducts such as 120, 125, the flue gas layer can be formed on one or more selected surfaces whilst the flow velocity of the layer can be controlled by adjustment of the fan speed. To avoid premature mixing of the flue gas and fresh combustion gas, the flow velocity of the flue gas layer is made approximately the same as or greater than that of the stream of combustion gas. The attemperation and gas recirculation may be automatically controlled by apparatus such as that described in Specification 729,437. Specifications 367,699, 504,114, 516,070, 523,870, 540,119 and 721,155 also are referred to.
机译:738,214。蒸汽过热器,BABCOCK&WILCOX,Ltd.,1953年6月4日[1952年6月4日],编号15417/53。 123级(3)。蒸汽锅炉包括炉腔室10,该炉腔室10由由蒸汽发生管形成的中间部分划分为两个竖直的室,该室的前壁和侧壁衬有发生器管,而后壁或挡板壁24也由该内壁形成。产生管用于将炉子与上游通道32分开,在上游通道32中布置有初级和次级对流过热器90、96以及省煤器156。每个炉室由一组粉状燃料燃烧器100向下燃烧,燃烧器组为封闭在风箱104、105中的风箱与风箱壁向内隔开,因此在操作中,燃烧气体向下通过每个风箱而不会撞击其壁,然后气体横向转向以向上流过通道32。蒸汽发生管在级头20、38与蒸汽和水鼓26之间延伸,蒸汽从其中流过初级过热器90,级间调温器93和从次级过热器96到最终出口集管98。为了在宽负载范围内保持过热温度恒定,当过热温度趋于高于所需值时,在高负载下使用调温器93,而在较低负载时使用调温器93。蒸汽温度趋于下降,烟道气再循环到炉中以减少其中的辐射热吸收,并相应增加进入过热器通道32的气体的热量。烟道气通过出口从出口管道155抽出。风扇150,其通过管道140、142、144和风门控制的垂直管道(例如120、125)排放到分别围绕风箱104、105的歧管110 ... 113和114 ... 117中,气体通过设置的槽118沿着歧管的底面在炉室的每个壁表面上形成向下移动的层,从而部分屏蔽其衬管免受辐射热f的传递从燃烧器通过的燃烧产物在每个隔室的中央向下流动。通过在诸如120、125的垂直管道中操作风门,可以在一个或多个选定的表面上形成烟道气层,同时可以通过调节风扇速度来控制烟道气层的流速。为了避免烟道气和新鲜的燃烧气过早混合,使烟道气层的流速与燃烧气流的流速近似相同或更大。可以通过诸如在规格729,437中描述的装置来自动地控制该减温和气体再循环。还参考了规格367,699、504,114、516,070、523,870、540,119和721,155。

著录项

  • 公开/公告号GB738214A

    专利类型

  • 公开/公告日1955-10-12

    原文格式PDF

  • 申请/专利权人 BABCOCK & WILCOX LIMITED;

    申请/专利号GB19530015417

  • 发明设计人

    申请日1953-06-04

  • 分类号F22G5/04;

  • 国家 GB

  • 入库时间 2022-08-23 23:16:14

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