MULTI-STAGE CIRCULATING FLUIDIZED BED SYNGAS COOLING
    1.
    发明公开
    MULTI-STAGE CIRCULATING FLUIDIZED BED SYNGAS COOLING 审中-公开
    爱尔兰ZIRKULIERENDEN WIRBELSCHICHT的MEHRSTUFIGE SYNTHESEGAS-KÜHLUNG

    公开(公告)号:EP2888033A1

    公开(公告)日:2015-07-01

    申请号:EP13832004.9

    申请日:2013-08-26

    申请人: Southern Company

    IPC分类号: B01J8/28

    摘要: A method and apparatus for cooling hot gas streams in the temperature range 800° C. to 1600° C. using multi-stage circulating fluid bed (CFB) coolers is disclosed. The invention relates to cooling the hot syngas from coal gasifiers in which the hot syngas entrains substances that foul, erode and corrode heat transfer surfaces upon contact in conventional coolers. The hot syngas is cooled by extracting and indirectly transferring heat to heat transfer surfaces with circulating inert solid particles in CFB syngas coolers. The CFB syngas coolers are staged to facilitate generation of steam at multiple conditions and hot boiler feed water that are necessary for power generation in an IGCC process. The multi-stage syngas cooler can include internally circulating fluid bed coolers, externally circulating fluid bed coolers and hybrid coolers that incorporate features of both internally and externally circulating fluid bed coolers. Higher process efficiencies can be realized as the invention can handle hot syngas from various types of gasifiers without the need for a less efficient precooling step.

    摘要翻译: 公开了一种使用多级循环流化床(CFB)冷却器在800℃至1600℃的温度范围内冷却热气流的方法和装置。 本发明涉及冷却来自煤气化炉的热合成气,其中热合成气在常规冷却器接触时夹带污染,侵蚀和腐蚀传热表面的物质。 通过在CFB合成气冷却器中循环惰性固体颗粒提取并间接传递热量至传热表面来冷却热合成气。 CFB合成气冷却器分段,以便在IGCC工艺中发电所需的多种条件下生成蒸汽和热锅炉给水。 多级合成气冷却器可以包括内部循环流化床冷却器,外部循环流化床冷却器和混合冷却器,其结合内部和外部循环流化床冷却器的特征。

    OXYCOMBUSTION IN TRANSPORT OXY-COMBUSTOR
    5.
    发明公开
    OXYCOMBUSTION IN TRANSPORT OXY-COMBUSTOR 审中-公开
    欧洲运输公司SAUERSTOFFVERBRENNUNG SAUERSTOFFVERBRENNER

    公开(公告)号:EP2712327A1

    公开(公告)日:2014-04-02

    申请号:EP12710005.5

    申请日:2012-02-27

    申请人: Southern Company

    IPC分类号: B01J8/18 F22B31/00 F23C10/10

    摘要: A pressurized transport oxy-combustor with different configurations is disclosed. Substantially pure oxygen is fed to the transport oxy-combustor under pressure to combust fossil fuels, generating steam for power generation. The end product is the flue gas containing substantially pure CO2 after moisture condensation. The low excess oxygen necessary to achieve complete combustion in the combustor is scavenged by adding another fuel so that substantially all oxygen fed to the combustor is completely consumed. The capability to operate the transport oxy-combustor as a circulating fluidized bed combustor at very high solids circulation rates makes it unnecessary to use recycled CO2 or flue gas as a means to moderate and control the combustion temperature. The temperature in the combustor is effectively controlled by relatively cooler circulating solids that enter the combustion zone. A small amount of CO2 is recycled for aeration and to convey solids fuel to the combustor.

    摘要翻译: 公开了具有不同结构的加压输送氧 - 燃烧器。 在压力下将基本纯的氧气供给到运输氧化燃烧器以燃烧化石燃料,产生用于发电的蒸汽。 最终产品是在水分冷凝后含有基本上纯的二氧化碳的烟气。 通过添加另外的燃料来清除在燃烧器中实现完全燃烧所需的低的过剩氧,使得进入燃烧器的基本上所有的氧被完全消耗。 以非常高的固体循环速率操作作为循环流化床燃烧器的运输氧燃烧器的能力使得不需要使用再循环的CO 2或烟道气作为调节和控制燃烧温度的手段。 通过进入燃烧区的相对较冷的循环固体有效地控制燃烧器中的温度。 再循环少量的二氧化碳进行通风并将固体燃料输送到燃烧器。

    ASH AND SOLIDS COOLING IN HIGH TEMPERATURE AND HIGH PRESSURE ENVIRONMENT
    9.
    发明公开
    ASH AND SOLIDS COOLING IN HIGH TEMPERATURE AND HIGH PRESSURE ENVIRONMENT 审中-公开
    亚历山大·赫尔辛基·赫尔辛基

    公开(公告)号:EP2603313A2

    公开(公告)日:2013-06-19

    申请号:EP11816859.0

    申请日:2011-08-05

    申请人: Southern Company

    摘要: Disclosed are cooling and depressurization system equipment, arrangement and methods to cool solid particles from a coal gasifier operating at high temperature and pressure. Ash from the coal needs to be continuously withdrawn from a circulating fluidized bed gasifier to maintain the solids inventory in the gasifier. The system disclosed enables use of conventional materials of construction for heat transfer surfaces. The supports for the cooling surfaces are located on the lower temperature upper section of the primary cooler. The cooled solids along with the fluidizing gas exits the primary cooler to a secondary receiving vessel where the solids can be further cooled by conventional means. The fluidizing and entrained gas entering the secondary vessel is filtered and vented through a vent pressure control valve. The column of cooled solids in the secondary vessel is depressurized by a continuous depressurization system to low pressures which are sufficient for conveying the solids to silos for disposal. The system and methods proposed are equally applicable to many high temperature, high pressure processes that require cooling and depressurization of process solids.

    摘要翻译: 公开了冷却和减压系统设备,从高温和高压下运行的煤气化炉冷却固体颗粒的方法。 灰尘需要从循环流化床气化器中连续排出,以保持气化器中的固体物质。 冷却表面的支撑件位于主冷却器的较低温度上部。 冷却的固体与流化气体一起离开初级冷却器到二次接收容器,其中固体可以通过常规方式进一步冷却。 进入二次容器的流化和夹带的气体被过滤并通过排气压力控制阀排出。 第二容器中冷却的固体柱通过连续减压系统减压至足以将固体输送到筒仓以进行处理的低压。