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    • 1. 发明授权
    • Incinerator and cremator
    • 焚化炉和火化炉
    • US4603644A
    • 1986-08-05
    • US617026
    • 1984-06-04
    • David R. Brookes
    • David R. Brookes
    • F23G1/00
    • F23G1/00
    • The cremator disclosed is of the kind in which reduction burning takes place in a coffin chamber, followed by oxidation burning in an afterburner chamber. It is also of the kind in which partly cremated embers can be moved to an ember-reducing location to make room for another coffin to be admitted to the coffin chamber. The disclosure shows the ash removal port in the side of the cremator, which allows the afterburner chamber to occupy space behind and underneath the coffin chamber; an arrangement which makes for a very compact, fuel efficient, easy-to-construct unit. The hearth includes an ash-trough for ember reduction. The hearth can be thin because it is supported on the central wall that divides the ducts of the afterburner chamber, which makes for good heat transfer, and quick warm-up.
    • 所公开的火化炉是在棺室中进行还原燃烧的那种,然后在后燃室中进行氧化燃烧。 也可以将部分火化的余烬可以移动到减少燃烧的位置,为另一个棺材进入棺木室提供空间。 本公开显示在火化炉侧面的除灰口,其允许后燃室占据棺室的后面和下方的空间; 这是一种非常紧凑,节能,易于构造的装置。 炉膛包括用于减少燃烧的灰烬槽。 炉床可以是薄的,因为它支撑在分隔加力室的管道的中心壁上,这使得良好的热传递和快速预热。
    • 2. 发明申请
    • Gasifier and Incinerator for Biomass Sludge Destruction
    • 用于生物质污泥破坏的气化炉和焚烧炉
    • US20080072807A1
    • 2008-03-27
    • US11534452
    • 2006-09-22
    • David R. Brookes
    • David R. Brookes
    • F23G5/12F23G5/00
    • F23G7/001F23G5/0273F23G5/165F23G2201/303F23G2203/8013
    • A device for gasifying biomass sludge having particle size less than 1 cm, and 20% to 100% solids content has a primary chamber, a fume transfer vent, a mixing chamber which accepts fumes from the primary chamber, and an afterburner chamber in fluid communication with the mixing chamber. A secondary burner produces an initial heating flame within a vertical portion of the afterburner chamber. A heat transfer chamber is in fluid communication with the afterburner chamber. Heated gases from the afterburner chamber cause heating of the heat transfer chamber. The primary chamber has a heat conductive floor superimposed over the heat transfer chamber so that conductive and convective heating of the primary chamber occur. At least one primary auger is located crosswise in the primary chamber between a sludge feed hopper and an ash hopper. The heat transfer chamber underlies the primary auger near the end at the ash hopper.
    • 用于气化生物质污泥的装置,其具有小于1cm的粒度和20%至100%的固体含量,具有初级室,烟气传送排气口,接收来自主室的烟雾的混合室和流体连通的后燃室 与混合室。 辅助燃烧器在后燃室的垂直部分内产生初始加热火焰。 传热室与后燃室相流体连通。 来自后燃室的加热气体导致传热室的加热。 主室具有叠加在传热室上的导热地板,从而发生主室的导电和对流加热。 至少一个主螺旋钻在污泥进料斗和灰斗之间的主室中横向定位。 传热室位于灰斗附近靠近末端的主螺旋推运器。