Process for vitrifying heavy-metal-containing residues having a chlorine content above 10% by mass and a melting furnace for carrying out the process
    31.
    发明授权
    Process for vitrifying heavy-metal-containing residues having a chlorine content above 10% by mass and a melting furnace for carrying out the process 失效
    用于玻璃化氯含量高于10质量%的重金属的残渣的方法和用于进行该方法的熔化炉

    公开(公告)号:US06315810B1

    公开(公告)日:2001-11-13

    申请号:US09087955

    申请日:1998-06-01

    IPC分类号: C22B702

    摘要: In a process for vitrifying heavy-metal-containing residues having a chlorine content above 10% by mass, in particular from flue gas cleaning, which are melted in a melting furnace, the constituents which cannot be incorporated into the melt are separated in the main furnace into two fractions, the first fraction comprising the readily volatile components and the second fraction comprising the salt-like less volatile components, and the first fraction is evaporated off, conducted out of the furnace together with the exhaust gas and collected as condensate, and the second fraction is separated from the surface of the melt as liquid salt and is discharged.

    摘要翻译: 在熔化炉中熔化的含氯量超过10质量%,特别是烟道气清洗的含重金属残渣的玻璃化过程中,不能并入熔体中的成分在主体中分离 炉子分成两部分,第一部分包含容易挥发的组分,第二部分包含盐状较不易挥发的组分,第一部分被蒸发掉,与排气一起导出炉并作为冷凝液收集, 将第二部分作为液体盐从熔融物的表面分离并排出。

    Apparatus for vitrifying heavy-metal-containing residues having a chlorine content above 10% by mass
    32.
    发明授权
    Apparatus for vitrifying heavy-metal-containing residues having a chlorine content above 10% by mass 失效
    用于玻璃化含氯量高于10质量%的含重金属的残留物的装置

    公开(公告)号:US06299827B1

    公开(公告)日:2001-10-09

    申请号:US09377628

    申请日:1999-08-19

    IPC分类号: C21B304

    摘要: An apparatus for vitrifying heavy-metal-containing residues having a chlorine content above 10% by mass, in particular from flue gas cleaning, which are melted in a melting furnace, the constituents which cannot be incorporated into the melt are separated in the main furnace into two fractions, the first fraction comprising the readily volatile components and the second fraction comprising the salt-like less volatile components, and the first fraction is evaporated off, conducted out of the furnace together with the exhaust gas and collected as condensate, and the second fraction is separated from the surface of the melt as liquid salt and is discharged.

    摘要翻译: 特别是在熔化炉中熔化的氯含量高于10质量%,特别是烟道气清洗的含重金属的残留物的玻璃化装置,不能掺入熔体中的成分在主炉中分离 分成两部分,第一部分包含容易挥发的组分,第二级分包含盐状较不易挥发组分,第一馏分被蒸发掉,与废气一起排出炉并作为冷凝物收集, 第二部分作为液体盐从熔体的表面分离并排出。

    Method and apparatus for separating out gall during glass melting
processes
    33.
    发明授权
    Method and apparatus for separating out gall during glass melting processes 失效
    玻璃熔化过程中分离出胆汁的方法和装置

    公开(公告)号:US5683484A

    公开(公告)日:1997-11-04

    申请号:US574389

    申请日:1995-12-18

    摘要: An electrically heated tank furnace is used to melt glass whereby a floating gall layer is formed on the melt, in particular during the vitrification of hazardous materials such as asbestos, fly ash, filter dust, whereby the tank of the furnace is fitted with a discharge outlet for the melt and an overflow channel with an inlet for the gall. A stream of ascending gas bubbles is produced in the melt. In order to promote better and automatic draining of the gall the stream of gas bubbles is produced directly in front of the overflow channel which thereby maintains a layer of liquid gall in the overflow channel and a layer of molten glass retained by a weir on the bottom of the overflow channel. The temperature in the overflow channel is chosen to be above the melting temperature of the gall, whilst the bottom layer of glass is maintained at a temperature at which the viscosity of the glass is so high that the glass does not drain out the overflow channel.

    摘要翻译: 特别是在诸如石棉,飞灰,过滤灰尘的危险物质的玻璃化过程中,熔融玻璃上形成浮动的胆汁层,由此炉子的炉子装有放电 用于熔体的出口和具有胆汁入口的溢流通道。 在熔体中产生上升的气泡流。 为了促进更好和自动排出胆汁,气泡直接在溢流通道的前面产生,从而在溢流通道中保持一层液体胆汁,并在底部保留有一个堰的熔融玻璃层 的溢出通道。 溢流通道中的温度选择为高于胆汁的熔化温度,而玻璃底层保持在玻璃的粘度如此高以至于玻璃不会排出溢流通道的温度。

    Continuously skimming viscous glass
    37.
    发明授权
    Continuously skimming viscous glass 失效
    连续粘胶玻璃

    公开(公告)号:US3771986A

    公开(公告)日:1973-11-13

    申请号:US3771986D

    申请日:1972-06-01

    IPC分类号: C03B5/20 C03B5/26 C03B5/28

    CPC分类号: C03B5/262 C03B5/28

    摘要: A silica-rich, volatiles-deficient surface layer is removed from highly viscous glass, near a forming means (rolls or the like). There is used a weir of less-than-usual depth that contains a platinum member that provides a substantially unchanging weir depth; at the same time, Venturi means control the amount of hot gases removed from the glass-melting furnace, to maintain or control the flow of the highly viscous glass. With the invention, it is possible to drain off the silica-rich surface of a highly viscous glass, losing only about 10 percent of the furnace throughput, rather than accepting the higher losses (about 30 percent) required in accordance with previous practices.

    摘要翻译: 富含稀土的挥发物表面层从形成装置(辊等)附近的高粘度玻璃中除去。 使用一个不太平常深度的堰,其中包含一个提供基本上不变的堰深度的铂金构件; 同时,文丘里管理控制从玻璃熔化炉去除的热气体的量,以维持或控制高粘度玻璃的流动。 利用本发明,可以排出高粘度玻璃的富含二氧化硅的表面,仅损失约10%的炉子通过量,而不是接受根据先前实践所需的更高的损耗(约30%)。

    Forehearth surface-glass separation and removal
    38.
    发明授权
    Forehearth surface-glass separation and removal 失效
    FOREHEARTH表面玻璃分离和去除

    公开(公告)号:US3630708A

    公开(公告)日:1971-12-28

    申请号:US3630708D

    申请日:1970-02-20

    IPC分类号: C03B5/20 C03B5/26

    CPC分类号: C03B5/262 C03B5/20

    摘要: Apparatus for separating surface glass from a parent body of molten glass flowing through a forehearth and, thereafter, removing such surface glass from the forehearth. A stationary skimmer is positioned in the forehearth to interfere with or divert the flow of the surface glass and thereby separate such glass from the remainder of the parent body thereof. The skimmer has an upper portion having a horizontal planar configuration of a truncated triangle with the truncated face being on the upstream face of the upper portion. The upper surface of the upper portion is above the surface level of the glass. A lower ledge portion located below the surface level of the glass, projects upstream from the truncated face. The flow of the separated surface glass then being directed through one or more suitable channels or passages which extend from a region adjacent the upstream face of the upper portion of the skimmer and along a side of the upper portion to the exterior of the forehearth to effect removal of such glass therefrom.