Zinc concentrate fluidized bed roaster and technological method for reducing zinc ferrite

The invention discloses a zinc concentrate fluidized bed roaster and a technological method for reducing zinc ferrite. The area of a hearth of the fluidized bed roaster is larger than 152 m < 2 >. In the zinc concentrate fluidized bed roasting process, zinc ferrite is mainly generated in an an...

Ausführliche Beschreibung

Gespeichert in:
Bibliographische Detailangaben
Hauptverfasser: WU XIAOSONG, GUO HUI, ZHANG LING, SONG SHOUHENG, HU DONGHUA, LIU ZILIANG, TANG KAILE, WANG HENGHUI, CHEN YANMEI, HUANG WENHU, YAN HAO
Format: Patent
Sprache:chi ; eng
Schlagworte:
Online-Zugang:Volltext bestellen
Tags: Tag hinzufügen
Keine Tags, Fügen Sie den ersten Tag hinzu!
Beschreibung
Zusammenfassung:The invention discloses a zinc concentrate fluidized bed roaster and a technological method for reducing zinc ferrite. The area of a hearth of the fluidized bed roaster is larger than 152 m < 2 >. In the zinc concentrate fluidized bed roasting process, zinc ferrite is mainly generated in an annular area, namely a turbulent flow deposition layer, extending from the inner wall of the fluidized bed furnace to the center line of the fluidized bed furnace by about 300mm. When the area of the furnace hearth is increased, the proportion of the area of a turbulent flow deposition area of zinc ferrite to the area of the furnace hearth is reduced, and the contact area of zinc ferrite generated by ZnO and Fe2O3 can be reduced, so that the generation of zinc ferrite is reduced, and the problem that the cost of zinc per ton is increased due to the fact that zinc ferrite in zinc calcine is too high is solved. 本发明公开了一种锌精矿沸腾焙烧炉和降低铁酸锌的工艺方法,沸腾焙烧炉的炉床面积大于152m2。在锌精矿沸腾焙烧过程中,铁酸锌的生成主要发生在沸腾炉内壁向沸腾炉中心线方向延伸约300mm环形区域,即紊流沉积层。当炉床面积增加时,铁酸锌