普通硅酸盐水泥机械立窑设计计划书

  • 格式:doc
  • 大小:1.13 MB
  • 文档页数:47

1

普通硅酸盐水泥机械立窑设计计划书

一、 题目:普通硅酸盐水泥机械立窑设计

二、 窑型:机械立窑

三、 产品与产量

1、名称:普通硅酸盐水泥熟料

2、产量:Gsh=2400t/h

3、 煅烧方法:半黑生料法

四、课程设计用的原始资料

(1)干白生料化学成份见表1

表1 干白生料化学成份

成份 Ls SiO2S Al2O3S Fe2O3S CaOS MgOS 其 它

含量(%) 38.95 12.42 3.59 2.22 40.04 2.28 0.59

(2)熟料成份见表2

表2 熟料成份

成份 SiO2Sh Al2O3Sh Fe2O3Sh CaOSh MgOSh Lsh 其 它

含量(%) 20.35 6.22 3.81 66.35 1.98 0.66 0.63

(3)煤灰成份见表3

表3 煤灰成份

成份 SiO2 Al2O3 Fe2O3 CaO MgO 其 它

含量(%) 48.12 43.55 3.24 2.97 1.23 0.89

(4)原煤成份见表4

2

表4 原煤成份

元 素 分 析(%) 工 业 分 析(%)

Cy Hy Oy Ny Sy Ay Wy Vy FCy Ay Wy

72.96 3.54 3.55 0.83 0.31 16.37 2.44 7.74 73.45 16.37

2.44

原煤发热量:Qdwy=27790kJ/kg

(5)其它条件

1) 环境温度: 32ºC; 相对湿度:51%

2) 料球水分:Wlq=13.3%; 料球温度:tlq=35ºC

3) 熟料出窑温度:tysh=120ºC; 烟囱废气温度:tf=120ºC

4) 鼓入窑空气温度:tyk=46℃; 入窑过剩空气系数:αyk=1.05

5) 窑面过剩空气系数:αyf=1.0; 料封管漏风系数:αlk=0.05

6) 烟囱飞灰量:mfh=0.015kg/kg-ck ; 飞灰烧失量:Lfh=35%

7) 窑罩门漏入空气量:Vl=1.65Nm3/kg-ck

8) 窑体表面散热损失:占总热耗的8.5%

五、课程设计的要求

1、编写设计计算说明书一份,1.2万字左右(20~25页),内容包括:

1) 立窑结构参数的确定;

2) 燃料燃烧计算:①理论空气量Vao和实际空气量Va计算,②烟气生成量Vfl及其成分和密度ρ计算,③ 理论燃烧温度tflo和实际燃烧温度tfl计算;

3) 熟料形成热Qsh计算;

4) 物料平衡计算;

5) 热平衡计算;

6) 专题讨论:① 立窑配风,② 立窑耐火材料(选一);

2、绘制立窑本体图一张(A1);

3、用计算机书写文本,用AutoCAD绘图;

3 4、公式要有出处,符号要有说明。

目 录

前言 ············································································································ 1

摘要 ············································································································ 2

第1章 概 述 ······················································································· 4

1.1 立窑煅烧水泥熟料 ············································································ 4

1.2 立窑的结构 ······················································································ 5

第2章 立窑的结构设计计算 ····························································· 7

2.1 窑的内径和高度 ··············································································· 7

2.2 喇叭口尺寸计算 ··············································································· 7

2.3 机械立窑工艺参数确定 ····································································· 8

第3章 燃料燃烧计算 ········································································· 10

3.1 燃料燃烧计算内容及基本概念 ··························································· 10

3.2 空气用量和烟气生成量计算 ······························································ 10

3.3 燃烧温度计算 ··················································································· 14

第4章 水泥熟料形成热的计算 ························································· 18

4.1 物料消耗量的计算 ············································································ 19

4.2 吸收热量的计算 ··············································································· 21

4.3 放出热量的计算 ··············································································· 24

4.4 熟料形成热的计算 ··········································································· 26第5章 物料平衡 ················································································· 27

5.1 原始资料 ·························································································· 27

5.2 物料平衡计算 ··················································································· 28

第6章 热量平衡 ················································································· 35

6.1 收入热量 ·························································································· 35

6.2 支出热量 ·························································································· 37

6.3 熟料单位热耗及热效应 ···························································· 39

第7章 计算汇总 ················································································· 40

结束语 ········································································································ 49

参考文献 ···································································································· 44

附 录:普通硅酸盐水泥机械立窑设计图

4

前 言

机械立窑是中小水泥行业的主要煅烧设备,与用回转窑厂相比具有投资小,见效快,就地取材 ,适应性强等显著特点,在发展中国家广为利用。

水泥(Cement)作为建筑材料的主要材料,使用广,用途大,水泥产业是我国的支柱产业,在国民经济中占了比较重要的作用。

大中型水泥厂的生产设备还是比较落后,小水泥厂的成本高,污染严重。因此,围绕世界水泥工业的中心课题,也即能源、资源和环境保护等,依靠技术进步来加速发展水泥工业,要在现有的技术基础上,因地制宜地采用先进技术,减少能耗,提高质量,降低成本,改善环境,增加产量,不断提高经济效益。要进一步优化工厂布局,加速发展采用预分解窑的骨干企业,合理配置以机械立窑为中心的小型生产线,大力推进水泥工业的现代化。要以节能、提高效益为目的,有选择地对老厂进行技术改造;利用资源优势,扩大品种生产,进一步提高社会效益;同时要更好地重视理论建设,加强基础研究和应用基础研究,有效开发人才。

在设计过程中,得到了肖奇老师的精心指导和同学们的真诚帮助,在此表示诚挚感谢!书中的错误在所难免,请大家批评指正。

编 者

2010年1月