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151 条记录 (耗时 0.019 秒)

    Glass furnaces
    51.
    发明公开
    Glass furnaces 失效
    Glasschmelzofen。

    公开(公告)号：EP0599547A1

    公开(公告)日：1994-06-01

    申请号：EP93309211.6

    申请日：1993-11-18

    申请人： PILKINGTON GLASS LIMITED

    发明人： Quirk, Richard ,  Shulver, Ian Nigel William ,  Bird, David Alan ,  McIntosh, Robin Maxwell

    IPC分类号： C03B5/235 ,  C03B5/237 ,  C03B5/04

    CPC分类号： B01D53/62 ,  B01D53/56 ,  C03B5/235 ,  C03B5/237 ,  F23C6/04 ,  F23C2900/06041 ,  F23L15/02 ,  Y02E20/348 ,  Y02P40/535 ,  Y02P40/57

    摘要： A method of operating a regenerative glass furnace for melting glass for the manufacture of shaped glass articles so as to minimise emission of NOx in waste gases leaving the furnace, the furnace having sealed regenerators which act as heat exchangers, the method comprising supplying fuel in excess of that required for stoichiometric combustion to ensure that glass of the required quality at the required production rate is obtained, and that the waste gases leaving the furnace through the regenerators contain combustible material, and reacting said combustible material with sufficient air to ensure that the waste gases exiting to atmosphere contain permissible levels of combustible material and contain permissible levels of NOx. Alternatively, the furnace may be operated at substantially stoichiometric conditions and fuel is supplied to waste gases as they leave the melting chamber. The invention also relates to a regenerator glass furnace for use in the method. The invention further provides a method of reducing the emissions of CO in waste gases leaving a cross-fired regenerative glass furnace for melting glass for the manufacture of shaped glass articles, the furnace having sealed regenerators which act as heat exchangers, the method comprising removing CO from the waste gases in the regenerator by combusting CO in around 8% excess air, based on the combustion air for the supplied fuel, at a temperature greater than 650°C.

    摘要翻译： 一种操作用于熔化玻璃的再生玻璃熔炉用于制造成形玻璃制品的方法，以便使离开炉的废气中的NOx的排放最小化，该炉具有作为热交换器的密封再生器，该方法包括供应过量的燃料 为确保获得所需生产率所需质量的玻璃，并且通过再生器离开炉子的废气含有可燃材料，并使所述可燃材料与足够的空气反应，以确保废物 离开大气的气体含有可燃材料的允许含量，并含有允许的NOx水平。 或者，炉可以在基本上化学计量的条件下操作，并且燃料在离开熔化室时供应给废气。 本发明还涉及一种用于该方法的再生器玻璃熔炉。 本发明还提供一种减少废气中CO排放的方法，留下用于熔化玻璃的交叉烧成蓄热玻璃熔炉用于制造成形玻璃制品，该炉具有用作热交换器的密封再生器，该方法包括除去CO 通过在大于650℃的温度下，基于用于所供给的燃料的燃烧空气将大约8％的过量空气中的CO燃烧，在再生器中的废气中。

    Process for melting silicate raw materials, in particular for the production of mineral wool, and apparatus for preheating the raw material mixture
    52.
    发明公开
    Process for melting silicate raw materials, in particular for the production of mineral wool, and apparatus for preheating the raw material mixture 失效
    一种用于熔化硅酸盐混合物insbesonderes用于制造矿棉和设备的用于预热原料混合物的过程。

    公开(公告)号：EP0547576A2

    公开(公告)日：1993-06-23

    申请号：EP92121389.8

    申请日：1992-12-16

    申请人： Grünzweig + Hartmann AG

    发明人： Fleckenstein, Hermann ,  Ungerer, Heinz-Jürgen

    IPC分类号： C03B5/237 ,  C03B3/02 ,  B01D46/30

    CPC分类号： C03B3/023 ,  C03B5/237 ,  Y02P40/535

    摘要： 2.1. In the case of the prior processes and apparatus for the melting of silicate raw materials, the requisite outlay for effectively reducing the emission values with respect to dust, fluorides and chlorides in the tank exhaust gases, and for recycling the additives back to the molten bath is relatively high.
    2.2. According to the invention, provision is made for preheating the raw material mixture, cleaning the tank exhaust gases, and recycling the impurities back into the molten bath to be performed simultaneously as one integrated process step and by the same apparatus, namely the raw material preheater (9). For this purpose, a sorbent storage silo (27) and also a metering device (28) for the proportional discharge of the sorbent into a receiving container (12) of the preheater (9) are arranged above the preheater (9). Alternatively, a liquid container (29) can be provided, as can an atomising element (31) for the proportional spraying of liquid from the liquid container (29) into the receiving container (12).
    2.3. Production of rock wool from basalt.

    摘要翻译： 2.1。 在用于硅酸盐原材料的熔化的现有方法和装置的情况下，所需的费用，用于相对于在罐废气粉尘，氟化物和氯化物有效地减少了排放值，和用于再循环添加剂返回到熔池 是比较高的。 2.2。 。根据本发明，规定用于预热原料混合物，清洗罐的废气，和再循环杂质回熔池同时执行作为一个综合的过程步骤以及由相同的装置，即，原料预热器制成 （9）。 为了这个目的，一个吸附剂贮存筒仓（27），因此对于吸附剂的比例排出到预热器（9）的接收容器（12）的计量装置（28）被预热器上面（9）布置。 可替代地，一个液体容器（29）可以被提供，如可以在用于液体从液体容器（29）到所述接收容器（12）比例喷涂核伊辛元件（31）。 2.3。 生产玄武岩岩棉。