首页> 外国专利> Reduction of nitrogen oxides in flue gases from e.g. lead crystal glass melting furnaces, is achieved by successive injection of fuel gas and oxygen into flue gases

Reduction of nitrogen oxides in flue gases from e.g. lead crystal glass melting furnaces, is achieved by successive injection of fuel gas and oxygen into flue gases

机译:减少烟道气中氮氧化物的排放铅晶体玻璃熔化炉是通过将燃料气体和氧气连续注入烟气中来实现的

摘要

The flue gas containing nitrogen oxides is led into a duct. At a first location, fuel gas is introduced into it. At a second, downstream of the first, oxygen is supplied to it. An Independent claim is included, pertaining especially, but not exclusively, to a glass-melting furnace. It comprising a melting chamber (12), feeder for the charge (14), extraction point (16) for molten glass and a gas burner (18) directing flames over the melt surface. The flue gas duct (20) has supply points (22, 24) for fuel gas and oxygen respectively. Preferred features: Fuel gas and/or oxygen are/is not preheated. Oxygen introduced, is in the form of air or oxygen-enriched air. The oxidant is introduced where the temperature can cause little or no nitrogen oxidation. Lead is separated in the duct, between the point of fuel gas supply and that of oxygen supply. Flue gases pass through a cooling section (28) before or after addition of oxygen. They pass through a filter (30). The burner is operated with fuel gas, especially natural gas. A mixture of air and fuel gas are supplied to the burner. Additional oxygen is introduced in the furnace near the gas burner. A glass melt surface is heated in a glass furnace. To the surface of the glass melt, a mixture containing nitrate is added. This is at least partially melted by the gas burner. In the corresponding plant, the flue gas duct is a stack. The point of fuel gas supply is 0.1-20 m downstream from the start of the duct. A lead separation location (26) is included. The melting chamber has an electrical heater.
机译:将包含氮氧化物的烟道气引入管道。在第一位置,将燃气引入其中。在第一个的第二个下游,向其供应氧气。包括独立权利要求,特别但并非唯一地涉及玻璃熔炉。它包括熔化室(12),用于装料的进料器(14),用于熔融玻璃的提取点(16)和将火焰引导到熔化表面上的气体燃烧器(18)。烟道(20)具有分别用于燃料气体和氧气的供应点(22、24)。首选功能:燃气和/或氧气未预热。引入的氧气以空气或富氧空气的形式出现。在温度几乎不会或根本不会引起氮氧化的地方引入氧化剂。铅在管道中在燃气供应点和氧气供应点之间分开。在添加氧气之前或之后,烟道气通过冷却部分(28)。它们通过过滤器(30)。燃烧器使用燃气,尤其是天然气运行。空气和燃气的混合物被供应到燃烧器。额外的氧气被引入燃气燃烧器附近的熔炉中。玻璃熔体表面在玻璃炉中加热。向玻璃熔体的表面添加含有硝酸盐的混合物。气体燃烧器将其至少部分熔化。在相应的工厂中,烟气管道为烟囱。燃料气体的供应点位于管道起点下游0.1-20 m。包括引线分离位置(26)。熔化室具有电加热器。

著录项

  • 公开/公告号DE10045429A1

    专利类型

  • 公开/公告日2002-03-28

    原文格式PDF

  • 申请/专利权人 F.X. NACHTMANN BLEIKRISTALLWERKE GMBH;

    申请/专利号DE20001045429

  • 发明设计人

    申请日2000-09-14

  • 分类号B01D53/00;C03B5/00;

  • 国家 DE

  • 入库时间 2022-08-22 00:27:27

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