首页> 外国专利> PROCESS FOR DENOXIFICATION OF OFF-GASES FROM ANNEALING AND PICKLING LINES, AND AN ANNEALING AND PICKLING LINE, ESPECIALLY FOR STAINLESS STEEL HOT OR COLD STRIP

PROCESS FOR DENOXIFICATION OF OFF-GASES FROM ANNEALING AND PICKLING LINES, AND AN ANNEALING AND PICKLING LINE, ESPECIALLY FOR STAINLESS STEEL HOT OR COLD STRIP

机译:退火和酸洗线以及退火和酸洗线中的残渣脱氧的过程,特别是对于不锈钢热轧或冷轧带钢

摘要

Heat from waste gases leaving the annealing furnace (4), is supplied to waste gases from the pickling section (6) ahead of selective catalytic reduction (9) (SCR). Waste gases from both sources are combined and fed together to the SCR section. Waste gases from the pickling section are supplied with heat from the combined stream, before combination with those from the annealing furnace. Further variations based on the foregoing principles are described. Heat may be supplied in addition, from external sources. Gases from the pickling section are heated to a temperature of 140-280?C. The combined gases are heated to 200-360[deg], before the SCR section. The plant includes a recuperator for the heat transfer stage. The low temperature inlet is connected to the annealing section. The high temperature connection of the heat exchanger carries the combined flows. Between the outlet for lower-temperature gas leaving the heat exchanger (7) and the SCR plant, a burner, preferably a low-NOx burner, is used. The heat exchanger is of cross-flow construction. An independent claim IS INCLUDED FOR the corresponding annealing and pickling lines equipped for selective catalytic reduction.
机译:离开退火炉(4)的废气中的热量在选择性催化还原(9)(SCR)之前从酸洗段(6)提供给废气。来自这两个源的废气被合并并一起馈送到SCR部分。来自酸洗区的废气与来自退火炉的废气合并,然后由合并的气流供热。描述了基于前述原理的进一步变化。另外,可以从外部来源提供热量。来自酸洗区的气体被加热到140-280℃的温度。在SCR部分之前,将合并的气体加热至200-360°。该设备包括用于传热级的换热器。低温入口连接到退火部分。换热器的高温接口承载合并的气流。在离开热交换器(7)的低温气体出口和SCR设备之间,使用燃烧器,最好是低NOx燃烧器。热交换器为错流结构。对于装备用于选择性催化还原的相应退火和酸洗线包括独立权利要求。

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