INCINERATION PLANT FOR SOLID MATERIAL AND METHOD FOR REPLACING ITS NOZZLE INSERT

    公开(公告)号:US20220228742A1

    公开(公告)日:2022-07-21

    申请号:US17609790

    申请日:2020-05-07

    IPC分类号: F23G5/44 F23L9/02 F23M9/02

    摘要: An incineration plant for solid material, such as waste or biomass, includes a combustion material inlet through which the solid material is to be introduced, a combustion chamber into which the solid material is introduced and in which the solid material is combusted, whereby flue gases are produced, a combustion grate with which the solid material and combusted solid material can be conveyed through the combustion chamber, a primary air supply below the top of the combustion grate, and at least one nozzle arranged above the combustion grate with which a gaseous medium such as secondary air, tertiary air, and/or an oxygen poor carrier gas can be provided, the at least one nozzle having a gas inlet and a gas outlet.

    Scrubber tray and a wet scrubber tower comprising such scrubber tray

    公开(公告)号:US10881980B2

    公开(公告)日:2021-01-05

    申请号:US16067293

    申请日:2017-08-16

    摘要: A scrubber tray for a wet scrubber tower of a flue gas purification device includes a multiplicity of spindles, arranged across an inner horizontal cross section of the wet scrubber tower. Adjacent spindles are arranged at a horizontal distance to each other. At least some of the spindles are pivot-mounted to allow a rotative movement around a corresponding spindle axis and to arrange the respective spindle at a predetermined rotation angle. At least some of the spindles are equipped each with at least one protrusion, which extends outwardly from the respective spindle. The spindles and protrusions are shaped and arranged to provide flow-through openings between adjacent spindles and protrusions respectively. Each flow-through opening defines a corresponding flow-through area, and they add up to 10%-80% of the inner horizontal cross section of the associated scrubber tower, independently of the respective rotation angles of the spindles.

    Fluidized Bed Apparatus
    4.
    发明申请
    Fluidized Bed Apparatus 审中-公开
    流化床设备

    公开(公告)号:US20160290632A1

    公开(公告)日:2016-10-06

    申请号:US15038347

    申请日:2014-08-15

    摘要: Fluidized bed apparatus, comprising a circulating fluidized bed reactor with at least one outlet port at its upper part, wherein said outlet port allows a mixture of gas and solid particles exhausted from the fluidized bed reactor to flow into a number (n) of associated separators for separating solid particles from said gas, a number (n) of means to transfer said separated solid particles from said (n) separators into a number (up to n) of discrete fluidized bed heat exchangers (24.1, 24.2, 24.3), and return means to transport at least part of said solid particles back from said discrete fluidized bed heat exchangers (24) into the circulating fluidized bed reactor, wherein the number (up to n) of discrete fluidized bed heat exchangers (24.1, 24.2, 24.3) are mechanically connected to provide one common fluidized bed heat exchanger (24)mwith water cooled intermediate walls (24i) between adjacent discrete fluidized bed heat exchangers (24.1, 24.2, 24.3).

    摘要翻译: 流化床装置,包括在其上部具有至少一个出口的循环流化床反应器,其中所述出口允许从流化床反应器排出的气体和固体颗粒的混合物流入数个(n)个相关联的分离器 用于从所述气体中分离固体颗粒,将所述分离的固体颗粒从所述(n)分离器转移到多个(至多n个)离散流化床热交换器(24.1,24.2,24.3)中的数量(n)装置,以及 返回装置将至少部分所述固体颗粒从所述离散流化床热交换器(24)返回到循环流化床反应器中,其中离散流化床热交换器(24.1,24.2,24.3)的数量(多达n个) 机械地连接以提供与相邻的离散流化床热交换器(24.1,24.2,24.3)之间的水冷中间壁(24i)的一个普通流化床热交换器(24)。

    Method for operating a fluidized bed apparatus and fluidized bed apparatus

    公开(公告)号:US11779895B2

    公开(公告)日:2023-10-10

    申请号:US17417372

    申请日:2021-02-19

    摘要: The present invention relates to a method for operating a fluidized bed apparatus and to a fluidized bed apparatus, the method comprising the following steps: providing particulate metal to a reaction chamber of a fluidized bed reactor, providing an oxidizing agent to a fluidizing bottom of the fluidized bed reactor such that particulate matter comprising the particulate metal is fluidized, wherein the particulate metal reacts with the oxidizing agent to particulate metal oxide, withdrawing particulate metal oxide from the reaction chamber, storing the withdrawn particulate metal oxide, providing particulate metal oxide to the reaction chamber of the fluidized bed reactor, providing a reducing agent containing gas to the fluidizing bottom of the fluidized bed reactor such that particulate matter comprising the particulate metal oxide is fluidized, wherein the particulate metal oxide reacts with the reducing agent to particulate metal, withdrawing the particulate metal from the reaction chamber, storing the withdrawn particulate metal.

    Fluidized bed heat exchanger
    7.
    发明授权

    公开(公告)号:US10900660B2

    公开(公告)日:2021-01-26

    申请号:US15039072

    申请日:2014-10-09

    摘要: A fluidized bed heat exchanger with a chamber (24) comprises a solid particles inlet port (22), a solid particles outlet port (30), arranged at a distance to the inlet port (22), means (46) for introducing a fluidizing gas from a bottom area into the chamber (24). The heat exchanger further comprises at least two heat transfer means (28) within the one chamber (24), each being provided with a heat transfer medium inlet port (42) and a heat transfer medium outlet port (44), wherein a first heat transfer means (28) is designed as a reheater and second heat transfer means (28) is designed as a superheater to achieve a heat transfer medium temperature and a heat transfer medium pressure above that of the reheater. At least one of the reheater or superheater is made of a multiplicity of heat transfer tubes arranged in a meandering fashion for conveying a heat transfer medium.

    Circulating fluidized bed apparatus

    公开(公告)号:US10591155B2

    公开(公告)日:2020-03-17

    申请号:US15540608

    申请日:2016-08-25

    IPC分类号: F23C10/10

    摘要: The invention relates to a circulating fluidized bed apparatus, comprising a combustion chamber (CC) with at least one outlet port (OP) at its upper end (UE) to transfer a mixture of gas and solids from said combustion chamber (CC) into at least one subsequent separator (SP) and from there at least partially back into the combustor chamber, wherein the combustion chamber (CC) is ring-shaped, comprising an inner wall (IW) and an outer wall (OW), arranged at a distance to each other in a radial direction of the combustion chamber (CC), and at least two intermediate walls (SW), which extend between the inner wall (IW) and the outer wall (OW) and in spaced relationship in a circumferential direction of the combustion chamber (CC), thereby subdividing the combustion chamber (CC) into a corresponding number of sections (CO), arranged adjacent to each other in the circumferential direction of the combustion chamber (CC).