日产5000吨水泥熟料新型干法生产线工艺毕业设计论文Word格式文档下载.doc

1、为了符合当今水泥行业的发展需求同时也是对大学本科四年所学知识的考查，我选择了“日产5000吨水泥熟料新型干法生产线窑尾系统工艺设计”这个课题作为我的毕业课题。设计范围主要是窑尾系统，通过配料计算、工艺平衡计算等得出结果，并结合实际对主机及附属设备进行选型，进而对各种设备进行工艺布置，对全厂的设备进行简单规划。为了使本次设计各项指标符合国家标准，本次设计的过程和结果完全依据水泥工厂设计规GB502951999；同时设计上参考了德州大坝水泥5000 t/d 熟料生产线、烟台东源5000 t/d 新型干法生产线等国内先进的相近规模生产线，并密切联系了毕业实习以及大学期间的认识实习、生产实习等。在符合

2、最新生产发展要求的基础上，达到最大程度节约资源、能源，做到既降低生产成本又能稳定生产，经济效益和社会效益双赢的可持续生产。关键词：电力系统；烧成系统；配料系统；粉磨系统ABSTRACTCement is one of the most important building materials of the social and economic development, within the coming decades or even a century,Cement is still no substitute for basic materials, the importance of

3、human civilization is self-evident.Modern most advanced cement production technology is NSP kiln advance decomposition. Pre decomposition kiln is in suspension preheater between decomposing furnace with rotary kiln added, join in calciner in total amount 50% - 60% of fuel, to make the fuel burning p

4、rocess and raw in the absorption process decompose carbonate state of suspension or boiling condition, thus make rapid decomposition rate of kiln raw from suspension preheater kiln 30 to 40 percent of the increased to 85 percent to 90 percent, the heat load of kiln is reduced greatly, while the prol

5、onging furnace production but can increase exponentially. Compared with suspension preheater kiln individual output, in the same conditions, the decomposition furnace with: small size, covers an area of reduced, manufacturing, transportation and installation easier, low investment in infrastructure,

6、 and because more than half of fuel is in the lower temperature burning in precalciner, produce harmful gases, and reduced the rate of less NOx atmospheric pollution.In order to meet the development needs of the cement industry today and at the same time examine the knowledge of university undergrad

7、uate course four years, I chose nissan 5000 tons of cement clinker NSP production line preheater system process design this topic as my graduation project. Preheater system design range is mainly by ingredients calculation, craft equilibrium calculation etc, and actual results to host and affiliated

8、 equipments, and selection of equipment, process arrangement of all the equipment simple planning.In order to make the design indexes meet the national standards, the design process and the result completely according to cement factory design rules GB50295-1999; Also on the Texas dam design referenc

9、e cement 5000 t/d of clinker production line, yantai dongyuan 5000 t/d NSP production line domestic advanced production line, and similar scale close contact and graduation practice during the internship, university of understanding of the production and practice, etc. In compliance with the require

10、ments of the development of the latest production, achieve maximum based on conservation of resources, energy and to meet both reduce production cost and stable production, economic benefit and social benefit win-win sustainable production.Key words： Electric power system；Firing system；Batching syst

11、em；Griding system目 录摘要.IABSTRACT.II1 前言.12建厂基础资料.42.1 设计题目.42.2建厂条件.42.3原始数据.42.3.1原燃料化学成分.42.3.2原、燃料水分.52.3.3烟煤的工业分析.52.3.4烟煤的元素分析.52.3.5生产方法和窑型的选择.53 全厂工艺平衡计算 .73.1配料计算.73.1.1应用基低位发热量.73.1.2三个率值的选择.73.1.3煤灰沉落率的计算. 83.1.4熟料化学成分的要求. 83.1.5以100kg干熟料为基准列累加试凑表. .83.1.6干原料料耗的计算. .93.1.7生料干原料配合比的计算. .93.1.8生料湿原料配合比的计算. .93.2物料平衡计算.103.2.1物料平衡计算在设计中的作用. 103.2.2参数选择及窑规格的确定. 103.2.3全厂物料平衡计算. 113.2.4原、燃料需要量的计算及物料平衡表.134工艺设备选型与计算.164.1工艺设备选型与计算的目的.164.2. 设备选型 . .174.2.1石灰石破碎设备的选型. .174.2.2生料闭路磨的设备选型184.2.3回转窑选型. 184.2.4烘干机设备的选型. .194.2.5煤磨的选型. .204.2.6水泥磨的设备选型. .214.2.7包装机的设备选型. .224.2.8主机平衡表见表.