会员体验
专利管家(专利管理)
工作空间(专利管理)
风险监控(情报监控)
数据分析(专利分析)
侵权分析(诉讼无效)
联系我们
交流群
官方交流:
QQ群: 891211   
微信请扫码    >>>
现在联系顾问~
热词
    • 4. 发明申请
    • ENHANCED STEAM CYCLE UTILIZING A DUAL PRESSURE RECOVERY BOILER WITH REHEAT
    • 增压蒸汽循环利用双重压力回收锅炉
    • US20090241860A1
    • 2009-10-01
    • US12055832
    • 2008-03-26
    • JOHN E. MONACELLITimothy E. HicksLarry A. HinerSteven L. Osborne
    • JOHN E. MONACELLITimothy E. HicksLarry A. HinerSteven L. Osborne
    • F22B1/18
    • F22B33/10F22B33/14Y02P60/831
    • An enhanced steam cycle utilizing a dual pressure recovery boiler with reheat allows a large increase in electrical generation with various turbine cycles while overcoming traditional lower furnace material limitations. A dual pressure designed recovery boiler furnace is provided with a lower furnace and an upper furnace. The lower furnace is operated at a lower temperature to prevent or reduce corrosion of the lower furnace wall tubes caused by the reducing environment. The lower furnace can be either a low pressure natural circulation steam generating (drum) system or economizer. Unlike the lower furnace, the upper furnace is not exposed to a reducing environment and is therefore not as susceptible to severe corrosion rates. The upper furnace is operated at higher temperatures and pressures which permit implementation of higher efficiency reheat steam cycles. The upper furnace thus operates as a high pressure natural circulation steam generating (drum) system, or as a once-through supercritical steam generating system. The dual pressure recovery boiler can thus be coupled to a variety of condensing, non-condensing or a combination of condensing and non-condensing turbine cycles to provide a large increase in electrical generation.
    • 利用具有再热的双压力回收锅炉的增强的蒸汽循环允许在克服传统的较低炉材料限制的情况下,具有各种涡轮循环的发电量大大增加。 双压设计的回收锅炉炉具有下炉和上炉。 下炉在较低的温度下运行,以防止或减少由还原环境引起的下炉壁管的腐蚀。 低炉可以是低压自然循环蒸汽发生(鼓)系统或节能器。 与下炉不同,上炉没有暴露在还原环境中,因此不会受到严重的腐蚀速率的影响。 上炉在更高的温度和压力下运行,这允许实现更高效率的再热蒸汽循环。 因此,上部炉子作为高压自然循环蒸汽发生(鼓)系统,或作为一次通过的超临界蒸汽发生系统。 因此,双压力回收锅炉可以耦合到各种冷凝,非冷凝或冷凝和非冷凝涡轮循环的组合,以提供大量的发电增加。
    • 9. 发明申请
    • VERTICAL SEPARATION STEAM GENERATOR
    • 垂直分离蒸汽发生器
    • WO2011134441A3
    • 2012-03-22
    • PCT/CZ2011000041
    • 2011-04-28
    • VITKOVICE POWER ENGINEERING A SVILIMEC LADISLAVSTAREK KAMILKUPSA VLADIMIR
    • VILIMEC LADISLAVSTAREK KAMILKUPSA VLADIMIR
    • F01K23/10F01K23/14F22B11/02F22B33/10
    • F22B11/02F01K23/10F01K23/14F22B33/10Y02E20/344
    • System of heat exchange tubes (2) mounted in the upper and lower tube sheets (3,4) and jacketed with a cylindrical shell (11) is placed in the outer shell (1). Cavities (5) interconnected with tube space (6) are created in the outer shell (1) above and under tubes (2). Inter-tube space (6) enclosed circumferentially with cylindrical shell (11) and at the top and bottom with tube sheets (3,4) is located between tubes (2). Outer shell (1) is equipped with primary pipe sockets (7,8) and secondary pipe sockets (9,10) for media inlet and outlet. There is a gap (12) created between cylindrical shell (11) and outlet pressure shell (1). Inter-tube space (6) has inter-tube discharge (13) of condensate at the bottom. Cooler (14) with accessories is preferably above or below jacketed tubes (2). Systems of jacketed tubes (2) can be situated in multiplicity one above another. The media inlet and outlet elements should be matched adequately to the addition of cooler (14) and/or system of tubes (2).?
    • 安装在上管和下管板(3,4)中并用圆柱形壳体(11)夹套的换热管(2)的系统被放置在外壳(1)中。 在管(2)上方和下方的外壳(1)中形成与管空间(6)相互连接的空腔(5)。 管状空间(6)围绕圆柱形壳体(11)封闭,顶部和底部与管板(3,4)位于管子(2)之间。 外壳(1)配备有用于介质入口和出口的主管座(7,8)和次管座(9,10)。 在圆柱形壳体(11)和出口压力壳体(1)之间形成间隙(12)。 管间空间(6)在底部具有冷凝管的管间排放(13)。 具有附件的冷却器(14)优选地在夹套管(2)之上或之下。 夹套管(2)的系统可以位于另一个之上。 介质入口和出口元件应充分匹配加入冷却器(14)和/或管(2)系统。
    • 10. 发明申请
    • VERTICAL SEPARATION STEAM GENERATOR
    • 垂直分离蒸汽发生器
    • WO2011134441A2
    • 2011-11-03
    • PCT/CZ2011/000041
    • 2011-04-28
    • VÍTKOVICE POWER ENGINEERING A.S.VILIMEC, LadislavSTÁREK, KamilKUPSA, Vladimír
    • VILIMEC, LadislavSTÁREK, KamilKUPSA, Vladimír
    • F01K7/16
    • F22B11/02F01K23/10F01K23/14F22B33/10Y02E20/344
    • System of heat exchange tubes (2) mounted in the upper and lower tube sheets (3,4) and jacketed with a cylindrical shell (11) is placed in the outer shell (1). Cavities (5) interconnected with tube space (6) are created in the outer shell (1) above and under tubes (2). Inter-tube space (6) enclosed circumferentially with cylindrical shell (11) and at the top and bottom with tube sheets (3,4) is located between tubes (2). Outer shell (1) is equipped with primary pipe sockets (7,8) and secondary pipe sockets (9,10) for media inlet and outlet. There is a gap (12) created between cylindrical shell (11) and outlet pressure shell (1). Inter-tube space (6) has inter-tube discharge (13) of condensate at the bottom. Cooler (14) with accessories is preferably above or below jacketed tubes (2). Systems of jacketed tubes (2) can be situated in multiplicity one above another. The media inlet and outlet elements should be matched adequately to the addition of cooler (14) and/or system of tubes (2).˙
    • 安装在上管和下管板(3,4)中并用圆柱形壳体(11)夹套的换热管(2)的系统被放置在外壳(1)中。 在管(2)上方和下方的外壳(1)中形成与管空间(6)相互连接的空腔(5)。 管状空间(6)围绕圆柱形壳体(11)封闭,顶部和底部与管板(3,4)位于管子(2)之间。 外壳(1)配备有用于介质入口和出口的主管座(7,8)和次管座(9,10)。 在圆柱形壳体(11)和出口压力壳体(1)之间形成间隙(12)。 管间空间(6)在底部具有冷凝管的管间排放(13)。 具有附件的冷却器(14)优选地在夹套管(2)之上或之下。 夹套管(2)的系统可以位于另一个之上。 介质入口和出口元件应充分匹配加入冷却器(14)和/或管(2)系统。