摘 要本设计的主要内容是 1080m3 高炉工艺设计，包括 1080m3 高炉的配料计算、物料 平衡计算、热平衡计算、高炉炉型的设计以及高炉炉体内衬的选择。

设计采用国内外高炉炼铁的经验公式，对高炉的工艺进行设计，使高炉获得良好 的技术经济指标，延长高炉的寿命；配料计算主要内容是计算冶炼 1t 的生铁，需要 消耗的矿石、熔剂和燃料；根据物质守衡定律建立氢平衡、碳平衡和氧平衡方程进行 物料平衡计算，对高炉的过程进行分析与研究；按照盖斯定律，依据入炉物料的最初 的形态与其出炉时的最终形态，计算产生和消耗的热量来进行热平衡计算，了解高炉 内热量的消耗状况；高炉炉型的尺寸根据经验公式进行计算；高炉内衬方面，炉缸、 炉底采用炭质+陶瓷杯复合的结构，炉腹、炉腰和炉身下部采用黏土砖或高铝砖的耐 火材料，并且主要应用铸钢冷却壁。83867

毕业论文关键词：高炉；配料计算；物料平衡计算；热平衡计算；炉型设计

Abstract The design focuses on the contents of 1080m3 blast furnace process design, the design of 1080m3 blast furnace mainly include calculation, material balance calculations, thermal balance calculation, furnace figure design and the selection of blast furnace lining。

Empirical formula of ironmaking from domestic and foreign was used in thedesign for furnace figure design to make the blast furnace to obtain good technical and economic index and prolong furnace life; the maincontents of ingredients calculation iscalculation

ofthe need to consume the ore, flux and fuel when smelting a ton of pig iron；According

to the law of conservation of matter, the balance of hydrogen, carbon and oxygen balance equations were established to analyze and study the process of blast furnace。 In accordance with the laws of Gass, according to its original shape when into the furnace and the final form of the material when baked, calculate the heat of produce andconsumption for thermalequilibriumcalculationtounderstandtheheatconsumptionstateofthe blast

furnace；About blast furnace lining, the hearth and bottom with the composite structure of

carbon and ceramic cup , bosh, belly and the lower part of the shaft is mainly used the refractory of clay bricks and high alumina brick and cast steel cooling stave。

Keywords: blast furnace; ingredients calculation; material balance calculation; thermal equilibrium calculation;

目录

第一章 绪论 1

1。1 概述 1

1。2 我国炼铁工业发展的现状 1

1。2。1 我国炼铁工业发展的历程 1

1。2。2 我国炼铁工业面临的形势 2

1。3 炼铁主要技术经济指标 4

1。4 1080m3 高炉的技术经济指标 5

第二章 平衡计算 6

2。1 配料计算 6

2。2 物料平衡 10

2。2。1 鼓风量的计算 10

2。2。2 煤气组分及煤气量计算 11

2。2。3 煤气中水量计算 14

2。2。4 炉料的机械损失 14

2。2。5 物料平衡表 14

2。3 热平衡计算 15

2。3。1 热收入 15

2。3。2 热支出 1080立方米高炉工艺设计:http://www.youerw.com/huaxue/lunwen_99112.html