首页> 外国专利> Device useful for generating many steam- or hot water streams in coke oven bank, comprises e.g. coke oven of heat recovery type, which is arranged in coke oven bank, coke oven chamber with gas chamber, and coke oven chamber

Device useful for generating many steam- or hot water streams in coke oven bank, comprises e.g. coke oven of heat recovery type, which is arranged in coke oven bank, coke oven chamber with gas chamber, and coke oven chamber

机译:用于在焦炉炉排中产生许多蒸汽或热水流的装置包括,例如。热回收型焦炉,其布置在焦炉组,带气室的焦炉室和焦炉室中

摘要

Device for generating many steam- or hot water streams in a coke oven bank, comprises (i) a coke oven of heat recovery type, which is arranged in a coke oven bank, (ii) a coke oven chamber (3) with a gas chamber, which forms a primary heating space, (iii) a coke oven chamber cover, (iv) a coke oven chamber door, (v) a primary air opening, (vi) a loading and an unloading system, (vii) an exhaust gas passage (5), (viii) a heat exchanger (1), (ix) a valve for dosing the exhaust gas passage, (x) a feed water line, (xi) a steam line and (xii) a conversion unit. Device for generating many steam- or hot water streams in a coke oven bank, comprises (i) a coke oven of heat recovery type, which is arranged in a coke oven bank, (ii) a coke oven chamber (3) with a gas chamber, which forms a primary heating space (3c) in a loaded state, (iii) a coke oven chamber cover, (iv) a coke oven chamber door, (v) a primary air opening for the primary heating space and a secondary heating space comprising secondary air openings, (vi) a loading and an unloading system for the coke oven, (vii) an exhaust gas passage, which connects the secondary heating space to a fuel gas system, (viii) a heat exchanger (1), which is arranged between the secondary heating space and an exhaust gas collection system in the exhaust gas passage, (ix) a valve, which is arranged in the gas flow downstream to the heat exchanger for dosing or blocking the exhaust gas passage, (x) a feed water line, (xi) a steam line, and (xii) a conversion unit for conversion of the thermal energy of the steam from the steam collection line into secondary energy. The secondary heating space is placed under the coke oven chamber. The loading and unloading system is provided for loading the coke oven chamber with the coal cake for coking and discharging the finished coke cake. The fuel gas system releases the exhaust gas to the atmospheric environment, after completion of heat exchange and required exhaust gas purification. The heat exchanger forms a device for discharging the heat of the exhaust gas on feed water by indirect heat exchange, and is associated with individual coke oven. The valve is associated with individual coke oven. The valve in the exhaust gas passage is controlled by means of pressure measurement sensor and opens into an exhaust gas collection line (11). The feed water line supplies feed water to the heat exchanger of the coke oven. The steam line removes the steam, which is produced through the heat exchanger. The steam line is led into a steam collection line. The steam collection line further carries the removed steam. An independent claim is also included for producing steam- or hot water streams in the coke oven bank, comprising (a) combining 6-30 coke oven chambers of heat recovery type into the coke oven bank, (b) heating the coal at high temperature by cyclic carbonization comprising loading, coking, discharging, carbonizing the coal in the coke oven chamber, forming the coking gas with a partial amount of combustion air in the primary heating space, which is formed by release of the gas chamber in the coke oven chamber, substoichiometrically combusting, supplying the partially combusted coking gas into secondary heating space below the coke oven chamber through the exhaust gas passage, and completely combusting the coking gas with superstoichiometric amount of combustion air, (c) providing the completely combusted gas from the secondary heating space via the exhaust gas passage into the heat exchanger with an integrated adjustable exhaust valve so that the exhaust gas mass flow, which passes through the heat exchanger, is controllable, (d) measuring the exhaust gas pressure at the inlet of the exhaust passage in the heat exchanger so that the exhaust gas pressure at each coke oven chamber is at least temporarily adjusted to a constant value via the exhaust gas valve, (e) generating steam through the completely combusted exhaust gas into the heat exchanger with respect to the supplied exhaust gas stream, supplying the steam to the steam collection line, discharging steam onto the conversion unit for producing secondary energy, after passing through the steam collection line, and (f) placing the completely combusted and cooled exhaust gas into the exhaust gas collection line, after passing through the adjustable heat exchanger, and reusing the exhaust gas or discharging into the surrounding, where the exhaust gas passage is arranged in the sides of the coke oven chamber.
机译:用于在焦炉组中产生许多蒸汽或热水流的设备包括(i)装在焦炉组中的热回收型焦炉,(ii)带有气体的焦炉室(3)腔室,该腔室形成一个主要加热空间,(iii)焦炉腔室盖,(iv)焦炉腔室门,(v)一级空气开口,(vi)装卸系统,(vii)排气口气体通道(5),(viii)热交换器(1),(ix)计量排气通道的阀,(x)给水管线,(xi)蒸汽管线和(xii)转换单元。用于在焦炉组中产生许多蒸汽或热水流的设备包括(i)装在焦炉组中的热回收型焦炉,(ii)带有气体的焦炉室(3)腔,在负载状态下形成一个主加热空间(3c),(iii)焦炉腔室盖,(iv)焦炉腔室门,(v)用于主加热空间和二次加热的主空气开口包括二次空气开口的空间;(vi)焦炉的装卸系统;(vii)排气通道,将二次加热空间连接到燃气系统;(viii)热交换器(1), (ix)一个阀,该阀布置在第二加热空间和废气通道中的废气收集系统之间,(ix)一个阀,该阀布置在热交换器下游的气流中,用于计量或阻塞废气通道,(x)给水管线,(xi)蒸汽管线和(xii)用于转换热能的转换单元蒸汽从蒸汽收集管线转化为二次能源。辅助加热空间位于焦炉室下方。提供装卸系统,用于将煤饼装载到焦炉室中,以焦化和排出成品的焦饼。在完成热交换和所需的废气净化之后,燃气系统将废气释放到大气环境中。热交换器形成用于通过间接热交换将给水上的废气的热量排出的装置,并且与单个的焦炉关联。该阀与单个焦炉关联。排气通道中的阀门由压力测量传感器控制,并通向排气收集管线(11)。给水管线将给水供应到焦炉的热交换器。蒸汽管线除去通过热交换器产生的蒸汽。蒸汽管线被引入蒸汽收集管线。蒸汽收集管线还携带除去的蒸汽。还包括用于在焦炉组中产生蒸汽或热水流的独立权利要求,包括(a)将6-30个热回收型焦炉室组合成焦炉组,(b)在高温下加热煤通过循环碳化,包括在焦炉室中对煤进行装载,焦化,排放,碳化,在主加热空间中通过部分燃烧空气形成焦化气体,这是通过释放焦炉室中的气室而形成的,亚化学计量燃烧,通过废气通道将部分燃烧的焦化气体供应到焦炉室下方的二次加热空间中,并以超化学计量的燃烧空气完全燃烧该焦化气体,(c)通过二次加热提供完全燃烧的气体通过带有集成式可调排气阀的排气通道进入热交换器的空间,使排气质量流通过(d)测量热交换器中排气通道入口处的排气压力,以使每个焦炉室的排气压力至少通过排气临时调节至恒定值。气阀,(e)相对于所供应的废气流,通过完全燃烧的废气进入热交换器产生蒸汽,将蒸汽提供给蒸汽收集管线,将蒸汽通过后排放到转换单元上以产生二次能量蒸汽收集管线,以及(f)在经过可调式热交换器后,将完全燃烧并冷却的废气排放到废气收集管线中,然后将废气再利用或排放到布置有废气通道的环境中在焦炉室的侧面。

著录项

  • 公开/公告号DE102012019746B3

    专利类型

  • 公开/公告日2013-12-24

    原文格式PDF

  • 申请/专利权人 THYSSENKRUPP UHDE GMBH;

    申请/专利号DE20121019746

  • 发明设计人 KIM RONALD;HAUSDORF FELIX ANDREAS;

    申请日2012-10-09

  • 分类号C10B21/00;

  • 国家 DE

  • 入库时间 2022-08-21 15:37:54

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