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method for the reduction of iron ore in a blast furnace.

机译:高炉中还原铁矿石的方法。

摘要

1334174 Blast furnace operation NIPPON KOKAN K K and W WENZEL 9 June 1971 [20 June 1970] 19545/71 Heading C7D [Also in Division F4] An auxiliary reducing gas is introduced into the furnace above the melting zone the blowing rates of gas and of blast air each being varied cyclically in opposition so that a substantially constant flow of top gas results, while the feed rates and temperatures may be such that a mixed gas temperature of about 1000‹ C is maintained after mixing of the two streams inthe furnace. The blowing periods are preferably so controlled that during maximum gas injection ore is reduced to sponge down to the level where the reducing and hearth gases meet, the sponge then being melted during the period of maximum air blast; during the latter period the top gas may be used for heating the blast, while during injection of reducing gas the latter may be obtained from the top gas. Alternatively the reducing gas may be obtained from an independent source, such as a fluid or solid fossil fuel, possibly by reacting natural gas or petroleum with an oxygen-containing gas in a regenerator. The temperature and nitrogen content of the air blast may be higher and lower respectively during the period of minimum flow than during maximum. In a particular form of apparatus described, blast air from heater 7 is introduced through tuyeres 4, while reducing gas from heater 18 is introduced at 22 above the melting zone 6. Top gas for heating is drawn off through line 5a and supplied to gas scrubber 11, and heaters 18, 7 while reducing gas is taken off through line 5b and passed, if necessary with supplementary gas from line 16, through scrubber 11 before being reheated and returned to the furnace. To ensure adequate penetration of the air blast into the burden it may be blown at constant velocity independently of flow rate.
机译:1334174高炉操作NIPPON KOKAN KK和W WENZEL 1971年6月9日[1970年6月20日]标题C7D [也在F4分部中]辅助还原性气体以气体和鼓风的吹入速率被引入到熔炉上方的熔化区。空气彼此相反地周期性地变化,使得顶部气体的流量基本恒定,而进料速率和温度可以使得在炉中将两种物流混合后保持约1000℃的混合气体温度。最好对吹气时间进行控制,以使在最大的气体注入过程中,矿石被还原成海绵,还原至还原气体和炉膛气体相遇的程度,然后在最大的鼓风期间使海绵熔化;在后一时期中,顶部气体可用于加热鼓风,而在注入还原气体期间,可从顶部气体获得还原气体。可替代地,可以通过使天然气或石油与再生器中的含氧气体反应而从独立的来源(诸如流体或固体化石燃料)获得还原气体。在最小流量期间,鼓风的温度和氮含量可能分别比最大流量期间的高和低。在所描述的设备的特定形式中,来自加热器7的鼓风通过风口4被引入,而来自加热器18的还原气体在熔融区6上方的22处被引入。用于加热的顶部气体通过管线5a被抽出并被供应到气体洗涤器。如图11所示,在还原气体的同时,加热器18、7通过管线5b排出,并在必要时与来自管线16的补充气体一起通过洗涤器11,然后再加热并返回炉子。为了确保鼓风充分渗透到物料中,可以与流速无关地以恒定速度吹气。

著录项

  • 公开/公告号NL7107044A

    专利类型

  • 公开/公告日1971-12-22

    原文格式PDF

  • 申请/专利权人

    申请/专利号NL19710007044

  • 发明设计人

    申请日1971-05-24

  • 分类号C21B5/00;

  • 国家 NL

  • 入库时间 2022-08-23 08:53:37

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