烧结厂设计说明书
年产200吨YG类硬质合金的烧结车间设计说明书
四川理工学院课程设计年产200吨YG类硬质合金的烧结车间设计学生:学号:专业:材料科学与工程班级:指导老师:四川理工学院材料与化学工程学院二O一一年六月摘要本文进行了年产200吨YG类硬质合金烧结车间的设计,介绍了WC-Co硬质合金的力学性能、应用、发展前景和常规制备方法等。
根据设计任务书的要求和相关粉末冶金车间设计规则制定了WC-Co硬质合金的工艺流程。
另外,主要针对球磨、压制和烧结三大工序进行了物料衡算,查阅资料对当前国内的相关设备进行了搜集整理,根据物料衡算和设备参数对球磨机、成型压力机、真空烧结炉等基本设备进行了选型和台数的合理选取,并进行了工作制度的合理性制定、设备的合理化布置及车间平面和厂区平面的布置。
最后,根据国家相关制图标准绘制了WC-Co硬质合金生产的工艺流程图、厂区平面布置图、烧结车间平面布置图和烧结车间的剖面图。
关键词:WC-Co硬质合金;物料衡算;设备选型;车间设计;烧结AbstractThe sintering workshop in where WC-Co hard alloys are produced for200tons per year has been designed in this paper.The mechanical properties of WC-Co hard alloy’s,its applications and prospects for development and the conventional preparation method were introduced.According to the design assignment and the correlative powder metallurgy workshop design practice,the WC-Co hard alloy technical process was developed.In addition,mainly for ball milling,pressing and sintering processes three primary working procedures were calculated material balance.Accessing to information on the current domestic related equipment were collected more,the ball mill,molding presses,vacuum sintering furnace and other basic equipment for the selection of a reasonable selection and number of units were carried out.The rationality of the working system formulated,equipments rationalization arrangement and workshop plane and factory plane layout were also carried out.Finally,the author has drawn the chart of the WC-Co hard alloy production flow,the floor-plans of the factory area and the sintering workshop,and the Sintering workshop sectional drawing according to the interrelated national charting standard.Key words:WC-Co hard alloy;material balance;equipment selection;workshop design;Sintering目录摘要 (I)Abstract (II)第一章绪论 (1)第二章概述 (3)2.1设计依据 (3)2.2设计原则 (3)2.3设计范围 (3)2.4原料及组成 (3)第三章WC—Co硬质合金生产的工艺过程 (4)3.1混合料的制备 (4)3.2干燥、筛分 (4)3.3掺胶制粒 (4)3.4成形 (5)3.5烧结 (5)3.5.1烧结过程 (5)3.5.2真空烧结 (6)第四章工厂工艺计算 (7)4.1工艺流程 (7)4.2物料衡算 (7)4.2.1物料平衡计算的方法和步骤 (7)4.2.2物料平衡的计算 (8)4.3工艺设备选型和计算 (11)4.3.1生产车间及设备简述 (11)4.3.2球磨机 (12)4.3.3振动过筛机 (14)4.3.4干燥柜 (14)4.3.5掺胶混合机 (15)4.3.6成型压力机 (16)4.3.7真空烧结炉 (17)4.3.8喷砂机 (19)第五章环境保护 (20)5.1粉尘污染 (20)5.2噪声污染 (21)第六章总结 (22)参考文献 (23)致谢 (24)附录 (24)第一章绪论硬质合金(Cemented carbide)是以难熔金属碳化物(WC、TiC等)为基体,铁族金属(Co、Fe、Ni等)作粘结剂,用粉末冶金方法制造的一种多相组合材料。
烧结设计手册
烧结设计手册摘要:一、烧结设计手册概述1.烧结设计手册的概念与作用2.烧结设计手册的主要内容与结构二、烧结设计手册的主要内容1.烧结基本原理与工艺流程2.烧结矿的物理性质与化学成分3.烧结设备与生产工艺4.烧结矿的质量控制与优化5.烧结矿的应用领域与市场需求三、烧结设计手册在实际工程中的应用1.烧结设计手册在烧结矿生产中的应用2.烧结设计手册在烧结设备选型与设计中的应用3.烧结设计手册在烧结工艺优化与改进中的应用四、烧结设计手册的发展趋势与意义1.烧结技术的发展趋势2.烧结设计手册在烧结行业发展中的作用与意义3.烧结设计手册的更新与完善正文:烧结设计手册是一本关于烧结技术的基础理论与实践应用的综合性参考书籍,旨在为烧结行业从业人员提供烧结工艺设计、设备选型、生产管理等方面的技术支持与指导。
本文将从以下几个方面对烧结设计手册进行详细介绍。
一、烧结设计手册概述烧结设计手册主要涵盖了烧结基本原理、工艺流程、设备选型、生产管理等方面的内容,为烧结行业从业人员提供了一套全面、系统的技术参考依据。
烧结设计手册不仅有助于提高烧结矿的生产质量和效率,还能推动烧结行业的技术进步与创新。
二、烧结设计手册的主要内容1.烧结基本原理与工艺流程烧结设计手册详细阐述了烧结的基本原理,包括物料混合、加热、烧结矿固结等过程。
同时,手册还介绍了烧结工艺流程,包括原料准备、配料、混合、烧结、破碎、筛选等环节。
2.烧结矿的物理性质与化学成分烧结设计手册对烧结矿的物理性质(如粒度、密度、强度等)和化学成分(如FeO、Fe2O3、SiO2等)进行了详细分析,以便为烧结矿的质量控制提供依据。
3.烧结设备与生产工艺烧结设计手册对烧结过程中的主要设备(如混合机、烧结机、破碎机、筛选机等)进行了详细介绍,包括设备类型、结构、工作原理等。
同时,手册还阐述了烧结生产工艺,如烧结矿的加热方式、烧结气氛、烧结速度等。
4.烧结矿的质量控制与优化烧结设计手册从原料准备、配料、混合、烧结等环节,详细介绍了烧结矿质量控制的方法与措施。
庚辰钢铁180m2烧结机委托设计说明书..
180m2带式烧结机委托设计说明书甲方:乙方:甲方计划在生产厂区现在的矿粉储存场地建设一台180m2带式烧结机(详细位置见甲方厂区总地形图和现场),特委托乙方承担整个工程项目的设计工作,具体情况如下。
一、项目名称庚辰钢铁有限公司烧结工艺装备升级、环保达标改造项目二、项目设计依据和相关数据1、符合国家最新环保政策及相关文件。
2、以委托设计说明书中相关要求为基本依据;遵守甲乙双方有关本项目技术沟通的相关会议纪要和技术文件。
3、依照厂内原料、燃料、电气、水源、地质地貌等基础条件和产品的要求。
4、气象条件JN市地处我国暖湿地区,夏季多雨,冬季晴朗干燥,年主导风向夏季为南、西南风,冬季为东、东北风,根据省气象局提供的1951-1987年气象资料,摘录如下:极端最低气温-19.7℃(1953.1.7);极端最高气温42.5℃(19557.22);一日最大降水量298.4mm(1962.7.23);最大冻土深度440mm(1968年共4天);最大积雪深度190mm(1971.3.2);最大风速及风向33.3m/s(西风,1951.7.21);极大(瞬时)风速及风向34.8m/s(西风1977.7.14);常年降雨量600-700mm。
基本风压0.4KN/m2;基本雪压0.2KN/m2;大气压力:冬季1000.2hPa,夏季998.5hPa。
厂区所在位置地震裂度:该位置在GD镇,处于鲁中山地北坡的山前倾斜平原上,东西两侧有两条倾向相对的正断层,发育在古生代地层中,第四系沉积较厚,场地周围未发现第四纪断层。
厂区平均海拨高度53米。
据分析,该地未来地震影响主要可能来自在鲁西南发生的强地震,该处影响烈度在Ⅵ-Ⅶ度间,基本定在Ⅵ度。
5、原料、燃料指标1) 精矿粉(常用有5种):TFe61~63%,其中含S≤0.2,P≤0.016;因业主方产品要求,烧结配料中精矿粉比例约占60~65%。
主抽风机及脱硫系统的设计需考虑配料的透气性、硫含量。
烧结设计手册
烧结设计手册(原创实用版)目录1.烧结设计手册概述2.烧结设计的基本原则3.烧结设计的具体步骤4.烧结设计的实例分析5.烧结设计手册的应用和意义正文烧结设计手册是一种为烧结过程提供指导的技术文档,旨在帮助工程师和研究人员进行烧结设计,以达到最佳的烧结效果。
本文将从烧结设计手册的概述、基本原则、具体步骤、实例分析以及应用和意义五个方面进行详细阐述。
一、烧结设计手册概述烧结设计手册包含了烧结过程中需要考虑的各种因素,如烧结材料的选择、烧结工艺的设定、烧结设备的选用等。
同时,它还提供了烧结过程中的各种计算公式和数据,以便工程师在进行烧结设计时能够有据可依。
二、烧结设计的基本原则在进行烧结设计时,需要遵循以下几个基本原则:1.确保烧结体的密度:烧结体的密度是评价烧结质量的重要指标,需要在设计过程中充分考虑。
2.控制烧结体的显微结构:烧结体的显微结构对材料的性能有着重要影响,需要通过合理的设计来控制。
3.优化烧结能耗:在保证烧结质量的前提下,尽可能降低烧结过程中的能耗,提高生产效率。
三、烧结设计的具体步骤烧结设计的具体步骤如下:1.确定烧结目标:明确烧结体的性能指标、尺寸和形状等要求。
2.选择烧结材料:根据烧结目标,选择合适的烧结材料,并进行材料性能分析。
3.设计烧结工艺:根据烧结材料的性能,设定烧结温度、保温时间等工艺参数。
4.选择烧结设备:根据烧结工艺要求,选择合适的烧结设备。
5.进行烧结试验:按照设计方案进行烧结试验,验证设计效果,并根据试验结果进行优化。
四、烧结设计的实例分析以烧结锌铁氧体为例,首先需要确定锌铁氧体的性能指标,如磁导率、矫顽力等。
然后根据这些指标,选择合适的锌铁氧体材料,并分析其烧结性能。
接着,设计烧结工艺,如烧结温度、保温时间等。
最后,选择合适的烧结设备进行烧结试验,并根据试验结果对设计进行优化。
五、烧结设计手册的应用和意义烧结设计手册在实际应用中具有重要意义,它可以帮助工程师和研究人员快速、准确地进行烧结设计,提高烧结质量,降低生产成本。
关于450m2烧结机料场设计说明10.22
关于450m2烧结机料场堆料方案
1、烧结机利用系数 1.5t/(m2.h),作业率95%,日产入炉烧结矿12500吨,含铁原料消耗12500吨/日(湿基)。
2、料场储存的物料品种及数量如下:
3、原料场地堆料布局
1)三条线堆料布局
料场设计长度560m,堆料机堆高10m,堆料宽度30m,矿粉堆密度2.2t/m3,所有物料堆间距3m。
2)两条线堆料布局
料场设计长度560m,堆料机堆高10m,堆料宽度45m,矿粉堆密度2.2t/m3,所有物料堆间距3m。
说明:
1、三条料线堆料时,由于料条过细,堆料量减少,堆料宽度按30m 计算,每条线预留6m宽的车道,所以料场宽度为:30×3+4×5+3×6=128m,所以需将料场宽度增加为128m。
2、由于冬季生产矿粉冻块较多,上表中冬季生产的冻块占用场地未进行计算。
冬季生产时尘泥、氧化铁皮等不能消耗完,需占用料场的量未计算。
3、理论计算时,料场堆料满足烧结机生产55天。
4、由于450m2烧结机料场宽度减小,原设计每日解冻117车/天,
而烧结正常生产时,每日需解冻库解冻208车(60吨/车)含铁原料,故解冻库翻车能力需要加大。
北营炼铁厂
二〇一二年五月五日。
烧结厂设计说明书
1 Introduction1.1 OutlineThe design reference Baosteel sintering plant, according to the design requirements of the mission statement, the design production capacity of 300 tons, the sintering plant products of high quality for blast furnace sinter.Because annular cooler temperature exhaust gas discharged with the airflow and fine dust released into the air, allowing more serious environmental pollution, while a large number of hot exhaust gas into the atmosphere, waste heat, dust and heat in order to reduce emissions, reduce pollution of the environment, the design of the ring after a hot exhaust gas cooler dust stove and holding furnace used for point after.The design of the sintering engineering technology, equipment level and the degree of automation and, basically, Baosteel sintering plant rather, is the world's advanced level, the design of a complete process: thick material layer sintering, centralized dust removal system, dual diagonal band spot stove, the addition of a ring cooler holding furnace and hot exhaust gas emissions as a promoter, these are the sintering process technology and equipment constitute the main content, but also an important indicator of the level of today's world.1.2 Design basis and design principles1.2.1 Design basisThis design is the Central South University of Resources Processing and Bioengineering pellets Professional 2013 session of the graduate design task, entitled "Design sinter plant of an annual output of 3 million tons of sinter" which combined in Baosteel graduation internship process field data collected and the master site processes and equipment prepared on the basis of.1.2.1 Design principlesIn order to do this sinter plant design, intended to the following design principles:1) According to today's world sintering technology, combined with the actual situation of Baosteel, determine the design process technology and equipment level.2) reasonably compact device configuration, production workshop has sufficient operating area to ensure smooth material transport facilities.3) selection of equipment, construction to achieve standardization and universal.4) Take effective measures to reduce the sinter plant dust pollution.5) Consider the possibility of future expansion.1.3 Design rangeThe design of the sintering project include the following:1) coke crushing and screening system.2) ingredients mixed system.3) sintering and cooling system.4) the main electrical room.5) finished crushing and screening system.6) the dust handling system.2 Iron-containing materials, flux, fuel2.1 iron-containing materialsThe design of the sintering plant iron raw materials including imported iron ore , national concentrates.Imported iron ore is a high iron low silicon raw materials, mainly from India, Brazil, Australia and other importing countries. Imported Materials ore from the steamer pier, transported by belt conveyor to the raw material yard, through Neutralization and mix on the yard, then by belt conveyor to the dosing chamber, Sintering plant mainly recyclable materials is iron by the belt conveyor to the field and mixed with other Materials Materials , to pre-dosing effect. Iron-containing materials in the yard after mixing , directly to the dosing chamber.2.1.1 Chemical composition of iron-containing materialsThe chemical composition of iron-containing materials into the plant in Table 2-1.2.1.2 The requirements Size and grade1) the size requirements: Fines <8mm.(2) grade requirements: iron grade fluctuation range ±0.5%;FeO fluctuation range ±0.1%;S fluctuation range ±0.08%.2.2 FluxBecause most iron raw materials used is high-speed rail low silicon raw material,in order to improve the quality of sinter and improve the fluidity of slag, this design uses dolomite, limestone and quicklime as flux. Mixture granulated quicklime The quicklime is used to enhance mixture granulation and improve the permeability3.Sintering Process Selection and VerificationAccording to material properties, select the appropriate sintering method, processing procedures and process systems,in order to obtain the desired product. Sintering process designed mainly for the process of analysis and the basic principles for selection process .3.1The meaning and requirements for selecting processProcess is an integrated of certain processes from production process.Sintering process of selection is an important part of the design process. A new sintering plant around all the design elements are determined by the unfolding process. Reasonable production process, equipment capacity is full, rational organization of production, to ensure continuous production, access to advanced technical and economic indicators of important factors. Therefore, the process of selection, must be fully considered, multi-program comparison.Process selection requirement is to ensure the product quality requirements of the premise, to maximize the use of various iron-containing materials, and access to high labor productivity and equipment utilization, conserve energy as much as possible to save production costs for enterprises to seek maximum profit; and to adopt modern means of production, strong labor intensity, improve operational and management level; should consider radical waste pollution, protect the environment and health, protection of workers' health.3.2 Raw materials, flux and fuel3.2.1Raw material preparationThe raw materials used to design the main ore powder, powder ore controls below 8mm size requirements, into the iron-containing raw materials and sintering mix ingredients in order to achieve results. This procedure offers a raw material in thesteel mill plant, mix mine via conveyor belt to produce sinter plant ingredients.Sintered material into the sinter plant conditions:1) bonanza powder particle size should be 8-0mm (also available 6-0mm), ore particle size of more than 10% +8 mm will affect the quality of sinter. Special powder size requirements should be based on experimentally determined. SiO2 content fluctuations should be less than or equal ± 0.2%. Iron grade fluctuations should satisfy the following conditions; large and extra large sinter plant should be less than or equal ± 0.5%; medium-sized sinter plant should be less than equal to ± 0.75%; small sinter plant should be less than equal to ± 1.0%.2) magnetite concentrate moisture should be less than 10%, hematite concentrate moisture should be less than 11%. Concentrate moisture exceeds this requirement, the proportioning accuracy, affecting mixing uniformity.3) Blast should be appropriate wetting dry dust, blast furnace and BOF dust and sludge secondary dust should be dehydrated, so that water is less than 15%.4) Rolling Paper size not greater than 8mm.5) of the iron-containing material harmful impurities should be limited as required.When raw iron grade volatile than <sintering plant design requirements> requirements, should be shot mix stockyard and, if possible together with the steel plant was built in order to achieve sintering, pelletizing plant feed ingredients stable, uniform size. For medium and small sintering plant should also be set up according to the specific conditions of mixing facilities; raw single species, grade fluctuation is small, or not to set mixing facilities. But it should be built by the mining of raw materials warehouse and warehouse and so on. There blending stockyard, the sintering plant should no longer raw materials warehouse. But in wet areas should be located indoor storage facilities.Medium-sized sinter plant material should be adopted by the dumper. Dumper is a large unloading equipment, which is widely used in large and medium-sized and some large sintering plant sinter plant. It has the unloading of high efficiency, large capacity, suitable for all kinds of bulk material unloading turn. Because high degree of mechanization, is conducive to automated or semi-automated unloading operations.By mine shafts is used only by the material and not for storage facilities. Generally used for steel mills to accept bulk materials and auxiliary materials. By mine chute design should consider the use of mechanized equipment. Small mines can be spiral unloading machine or a chain-head unloading machine to accept raw materials. Most of the raw materials warehouse sintering plant designed to stabilize production, raw materials warehouse storage time of various materials as follows: iron-containing materials, a dedicated transmission line for the five days, no special transport line for the seven days; fuels and solvents , a dedicated conveyor line for the 3-5 days, no special transport line for 7 days. As for the small sinter plant under specific conditions. Freezing cold regions receiving and storage of raw materials should have anti-freeze thawed facilities.3.2.2 Flux preparationSintering production on the granularity of flux, there are strict regulations generally require 3 ~ 0mm content should be greater than 85% while the flux into the plant size is 40 ~ 0mm, so you need to be broken.Flux in the raw material crushing plant is complete. Dolomite, limestone crushing to the required 3 ~ 0mm, via tape machine to the dosing chamber. Lime particle size of 3 ~ 0mm, from the limestone, dolomite roasting plant is provided with a suction pressure tank to the sintering plant dosing chamber, and then compressed into the batching tank.(1) flux crushing and screening process generally has three:1) Open broken rod mill machining processes.2) Closed hammer crusher crushing and screening process flow.3) Impact Crusher closed circuit crushing and screening process flow.Closed flux machining processes are generally used in closed-circuit crushing and screening processing flow, can be divided into two kinds of pre-screening and screening examination. When the flux ore 3-0mm level content more time (generally 30% -40% or more), before use of pre-screening. Otherwise, adopt screening. Check the screening process sieve material for the product, the oversize material back into the crusher heavy breaking. More generally sintering plant using this process.Closed flux machining processes are generally used in closed process, can be divided into pre-screening and pre-screening process closed-circuit crushing and screening checks closed circuit combining two kinds. When the flux ore 3 ~ 0mm level for a long time (generally 30% to 40%), before use of pre-screening. Otherwise, the check screening. Check the screening process under size product for the product, the oversize material back into the crusher broken again. Taking into account the material conditions of this design, the design uses a closed circuit with a screening examination.(2) broken equipmentConsidering the physical properties of raw materials, production capacity and size requirements, the advantages and disadvantages of the crushing equipment discussed below:1) Impact CrusherScope: brittle, medium hard minerals (metallic, C), sintering plant (limestone, dolomite).Advantages: uniform size, over crushed small, light weight, low power consumption, large capacity, large crushing ratio.Disadvantages: vibration, noise, dust, wear big.2) hammer crusher (reversible and irreversible)Scope: brittle, medium-hard, hard and soft minerals (limestone, dolomite and serpentine), the crushing (3 ~ 0mm), rarely used in primary crushing.Pros: large capacity, large crushing ratio; structure is simple, compact, low power consumption and easy maintenance.Disadvantages: wear and high moisture blocking material is easy.3) rod millScope: Baosteel crushing equipment used in the second paragraph of coke.Advantages: too little crush.Disadvantages: high power consumption, low output and heavy equipment.4) four roller crusher (on the roll)Scope of application: Widely used in sinter plant fuel broken.Advantages: can be completed in time, fine, no screening classification, simpleprocess.Cons: roller uneven wear.Common flux crushing equipment crusher and hammer crusher two kinds.Crusher has uniform particle size, over crushed small, light weight, low power consumption, large capacity, large crushing ratio, etc., hammer crusher with high yield, large crushing ratio, low power consumption per unit of product, easy maintenance, etc. advantages in the production of the two devices is different, but the impact crusher vibration, noise, dust capacity, wear and therefore in the design selection hammer crusher. Hammer crusher can be divided into two kinds of reversible and irreversible and reversible hammer crusher hammer function to extend the service life and ensure the crushing efficiency, so the design are made of reversible hammer crusher.(3) screening equipmentSintering plant flux screening equipment is mainly shaker.The design uses a self-centering shakerSelf-centering shaker has the advantage of simple structure, use, operation and replacement of the screen surface is more convenient, strong vibration sieve surface, and the vibration direction perpendicular to the screen surface can reduce the material clogging the sieve of the phenomenon, with high screening efficiency (up to 90 ~ 95%) and production capacity, suitable for medium, fine screening, does not apply to coarse sieve.The disadvantage is that the amplitude of the sieve with the size of the amount to the mine fluctuate, resulting in screening efficiency is not stable enough; sieve in the process of starting and stopping, through resonance, the amplitude increases, a greater impact on the sieve and buildings.11。
2x160m2烧结机项目设计方案说明书
2x160m2烧结机项目设计方案说明书4 烧结工艺4.1 原料条件4.1.1 含铁原料含铁原料在混匀料场按比例配矿混匀后,以单一品种混匀矿用带式输送机运往烧结厂配料室的混匀矿配料槽。
4.1.2 熔剂熔剂有石灰石、白云石和生石灰。
石灰石和白云石的粒度为0-3mm,外购合格产品用罐车运至烧结配料室料仓,用压缩空气送至配料槽。
要求0~3mm粒级含量>90%。
生石灰的粒度为3~0mm,外购合格产品用罐车运至烧结配料室料仓,用压缩空气送至配料槽。
要求0~3mm粒级含量>90%。
4.1.3 燃料1)固体燃料烧结用固体燃料为焦粉和无烟煤,粒度为25-0mm。
焦粉为高炉矿槽筛粉的返焦,汽车进料场堆存;无烟煤外购,焦粉和无烟煤从料场用带式输送机送至烧结厂燃料受料槽,经过粗破碎和细破碎破后由带式输送机运至烧结配料室。
2)气体燃料烧结机点火燃料为高炉煤气,热值3050kJ/Nm3,煤气耗量:单台机正常用量:12000Nm3/h。
4.1.4 原料和燃料的化学成分(待招标方提供)4.1.5原料和燃料耗量(待原料确定后提供)4.2 工厂规模及工作制度4.2.1 工厂规模设计2台160m2烧结机,总生产能力为年产332万吨整粒后的成品烧结矿,分两期建设投产。
4.2.2 工作制度工厂为连续工作制,年工作330天,每天3班,每班8小时,主机业率为90.4%。
4.3 主要参数及产品方案4.3.1 主要参数按照两座高炉主原料采用80%的烧结矿和20%的球团矿的要求,需要烧结矿301.4万吨/年,考虑烧结规模与炼铁要求相比要留有5~10%的富余量,确定本工程烧结机利用系数为1.31t/(m22h),单台烧结机小时产能为209.6 t/h,年产量166万吨。
4.3.2产品方案(初定)烧结厂产品为温度≤120℃的冷烧结矿,出厂烧结矿粒度≥5mm,TFe~57%,碱度1.8。
4.3.3 工艺流程本工程工艺流程是从原料接受到成品烧结矿输出,包括燃料破碎、配料、混合、抽风、烧结、冷却、成品筛分及成品转运的整个工艺过程。
烧结砖厂设计方案
烧结砖厂设计方案烧结砖厂设计方案一、工艺流程:1. 原材料准备:将石灰石、黏土等原材料进行堆放,并使用装载机将其送入破碎机进行破碎。
2. 破碎混合:将破碎后的原材料送入搅拌机进行混合,使不同种类的原材料均匀混合。
3. 条料成型:将混合好的原材料送入压机进行成型,制成粘土坯。
4. 烧结:将制成的粘土坯通过运输设备运送至烧结窑进行烧结,使其达到合适的硬度和强度。
5. 检验分拣:将烧结后的砖坯进行外观质量检验,分拣出符合标准的砖坯。
6. 包装出库:对合格的砖坯进行包装,并运输出库,准备销售。
二、设备布局:1.原材料区:设置原材料堆放场地,并建设原材料仓库和搅拌机房。
2.破碎混合区:设置破碎机和搅拌机,并合理布置输送管道,方便原材料的输送。
3.条料成型区:设置压机和压机房,并建设料斗和输送设备,将混合好的原材料输送到压机进行成型。
4.烧结区:建设烧结窑和烟气处理设备,并设立运输通道,将砖坯送入烧结窑烧结。
5.检验分拣区:设立检验分拣台和分拣设备,对烧结后的砖坯进行质量检验和分拣。
6.包装出库区:设置包装设备和仓库,并设立出库通道,将合格的砖坯进行包装和运输。
三、环境保护:1. 烟气处理:在烧结窑的烟囱上安装烟气处理设备,通过除尘器和脱硫装置等技术手段,将烟气中的颗粒物和硫化物等有害物质净化处理,达到环保排放标准。
2. 噪音控制:在设备运行时,对破碎机、搅拌机等噪音大的设备进行隔音处理,降低噪音污染。
3. 废弃物处理:将生产过程中产生的废弃物进行分类、收集和处理,确保废弃物的无害化处理,并减少对环境的污染。
四、用电和用水:1. 用电:根据各个工艺段的设备功率和运行时间,合理预估用电量,并建设配电室和变压器等设备,确保用电安全。
2. 用水:根据生产工艺流程中的用水需求,合理设计水源设施和供水管道,确保用水的正常供应,同时做好废水处理,减少对水资源的浪费和污染。
以上是烧结砖厂设计方案的简要介绍,方案中考虑了工艺流程、设备布局、环境保护以及用电用水等因素,以确保砖厂的高效运营和环保生产。
烧结设计手册
烧结设计手册
(最新版)
目录
1.烧结设计手册概述
2.烧结设计的基本原则
3.烧结设计的流程
4.烧结设计的关键技术
5.烧结设计的应用案例
6.烧结设计手册的结论和展望
正文
1.烧结设计手册概述
烧结设计手册是一本关于烧结设计的专业指南,它涵盖了烧结设计的基本原则、流程、关键技术以及应用案例等内容。
烧结设计是烧结过程的重要组成部分,它涉及到烧结过程中的一系列参数和条件的设定,对于提高烧结矿的产量和质量具有关键作用。
2.烧结设计的基本原则
烧结设计的基本原则包括:确保烧结矿的化学成分和矿物组成符合要求,尽可能提高烧结矿的密度和强度,降低烧结过程中的能耗和环境污染,以及提高烧结矿的利用率和经济效益。
3.烧结设计的流程
烧结设计的流程通常包括以下几个步骤:首先是烧结原料的选矿和准备,其次是烧结过程的参数设定,包括烧结温度、烧结时间、烧结气氛等,然后是烧结过程的监控和调整,最后是烧结产品的质量和性能检测。
4.烧结设计的关键技术
烧结设计的关键技术包括:烧结原料的选矿和准备技术,烧结过程的参数设定和监控技术,烧结产品的质量和性能检测技术,以及烧结过程的环保和节能技术。
5.烧结设计的应用案例
烧结设计手册中包含了许多烧结设计的应用案例,这些案例涵盖了烧结过程的各个环节,包括烧结原料的选矿和准备、烧结过程的参数设定和监控、烧结产品的质量和性能检测,以及烧结过程的环保和节能等。
6.烧结设计手册的结论和展望
烧结设计手册的结论是,烧结设计是烧结过程的重要组成部分,它对于提高烧结矿的产量和质量具有关键作用。
300平米烧结机烧结厂设计
摘要烧结矿在高炉炼铁生产中是很重要的一种含铁原料,它的质量好坏和产量的高低直接影响高炉的冶炼效果。
因此,设计一个合理的烧结工艺流程是非常重要的。
在整个设计过程中吸收了很多国内外先进厂家的经验和技术,根据所学的专业知识,设计一台300 m2的烧结机。
其技术指标为年产烧结矿307.48万吨,R=1.8,T Fe≥57%,成品矿粒度50-5 mm,转鼓指数≥70%。
本设计说明书中对所设计的烧结厂工艺进行了简要的介绍,并进行了物料平衡及工艺流程的计算,设备选择计算,确定了含铁原料、熔剂、燃料等需要量,并选择了与之相应的设备配置。
全文分为:绪论;原料、熔剂和燃料;生产规模,工作制度及产品方案;烧结工艺流程及物料平衡;烧结物料平衡与热平衡计算;环境保护与综合利用六个部分。
本设计中,充分考虑了设备自动化控制及环境保护等方案的需要,选择了当前先进的工业设备。
在计算基础上又绘制了图纸说明并编写了设计说明书。
关键词:烧结厂设计;工艺流程;自动化控制;环境保护AbstractIn blast furnace ironmaking, the sinter is an important iron material. The productivity and quality of the sinter have directly effect on blast furnace ironmaking. So it is very important to design a sensible singtering craft.In the design prossess, Some advanced experience and technology of domestic and foreign manufactures has adopted. According to the study of expertise, the requirement is to design a 300 m2of sintering craft. The technical indicators is following: the year quantity of sinter is 307.48 ten thousand ton, R=1.8, TFe≥57%, drum index is no less than 70%, finished mine size is from 50 mm to 5 mm.It is introduced the process of the sintering plant in the design specification. And calculation in material balance, process and equipment selection, determine the ferrous materials, flux, fuel and other requirements, and selection of the corresponding fitness equipment configuration are displayed. The thesis is composed of six sections: introduction; material of iron ores, fluxes, flues; capacity, working rules and production program of the sinter plant; process and material balance calculation; sintering material balance and thermal equilibrium calculation; environment protection and comprehensive utilization.The equipment autocontrol and environmental protection are fully considered in the design. The current advanced craft equipment was used. On the base of calculation,the drawings were drawn and the design specification was complied.Keywords: Sintering plant design; Technical processing; Automated control;Environmental protection;目录前言 (1)1 绪论 (2)1.1 烧结厂设计目的 (2)1.2 烧结厂设计依据及概况 (2)1.3 烧结厂设计要求 (2)1.4 厂区概况及厂址特点 (3)1.4.1 厂区概况 (3)1.4.2 厂址特点 (3)1.5 设计特点 (3)2 原料、熔剂和燃料 (4)2.1 概述 (4)2.2 含铁原料 (4)2.3 熔剂 (4)2.4 燃料 (5)2.5 配比确定 (6)3 生产规模,工作制度及产品方案 (7)3.1 主要技术经济指标确定 (7)3.1.1 作业率确定 (7)3.1.2 利用系数确定 (7)3.1.3 其他经济技术参数 (7)3.2 生产能力确定 (8)3.2.1 日生产能力 (8)3.2.2 小时生产能力 (8)3.3 工作制度 (8)3.4 产品方案 (8)3.5 烧结厂厂房布置及设备布置 (9)3.5.1 烧结厂设备配置原则 (9)3.5.2 工艺建筑配置原则 (9)3.5.3 原料车间配置 (10)3.5.4 烧结室配置 (10)3.5.5 抽风除尘系统的配置 (11)3.5.6 烧结矿处理设备配置 (11)4 烧结工艺流程及物料平衡 (13)4.1 工艺流程确定原则及特点 (13)4.1.1 工艺流程 (13)4.1.2 工艺流程的原则 (13)4.1.3 工艺流程概述 (13)4.2 配料计算 (19)4.2.1 烧结矿烧成率、全铁量、碱度 (19)4.2.2 混合料量 (20)4.2.3 各种原料所需的干料量、湿料量、含水量 (20)4.2.4 外加水量 (21)4.2.5 返矿量 (21)4.2.6 烧结矿年产量 (21)4.3 烧结矿成分计算 (21)4.3.1 各项成分计算 (21)4.3.2 烧结物料收支平衡表 (24)4.4 物料平衡计算 (24)4.4.1 各种物料每小时配料量 (24)4.4.2 熔剂破碎筛分工艺流程及物料平衡 (24)4.4.3 配料工段物料平衡 (26)4.4.4 混合工艺物料平衡 (26)4.4.5 烧结工艺物料平衡 (26)4.4.6 冷却工艺物料平衡 (27)4.4.7 整粒工艺物料平衡 (27)5 烧结物料平衡与热平衡计算 (28)5.1 烧结物料平衡 (28)5.1.1 铺底料量 (28)5.1.2 点火所需燃料、空气量及废气组成 (28)5.1.3 烧结过程总物料收入 (33)5.1.4 烧结过程总物料支出 (33)5.1.5 烧结过程机械损失 (33)5.2 烧结热平衡计算 (34)5.2.1 烧结热量收入 (34)5.2.2 烧结热量支出 (35)5.2.3 烧结热量损失 (36)6 主要设备选型计算 (37)6.1 工艺设备选型依据 (37)6.2 熔剂破碎与筛分设备选型计算 (37)6.2.1 破碎设备 (37)6.2.2 熔剂筛分设备 (38)6.3 燃料破碎设备选型计算 (38)6.3.1 粗碎设备选择 (38)6.3.2 细碎设备选择 (39)6.4 配料设备选型计算 (39)6.4.1 给料设备 (39)6.4.2 配料附属设备 (40)6.5 混合设备选型计算 (41)6.5.1 一次混合设备规格确定 (41)6.5.2 二次混合设备规格确定 (42)6.6 烧结机及附属设备选型计算 (43)6.7 烧结矿热破碎设备选择 (46)6.8冷却设备选型计算 (46)6.9 整粒设备选型计算 (49)6.10 抽风除尘设备选型计算 (51)7环境保护与综合利用 (53)7.1 环境保护的内容 (53)7.1.1 环境除尘 (53)7.1.2 烟气脱硫 (53)7.1.3污水处理 (54)7.2综合利用 (55)参考文献 (56)致谢 (57)附录A:设计图纸明细表 (58)前言烧结厂设计依据在手,根据矿石特性和试验研究成果,设计合理工艺流程,选择合适工艺设备,进行合理工艺配置,确保生产正常进行。
烧结设计手册
烧结设计手册摘要:一、烧结技术简介1.烧结定义与原理2.烧结工艺流程二、烧结原料与设备1.原料选择与配比2.烧结设备分类及选型三、烧结过程控制与管理1.烧结参数控制2.质量检测与分析3.安全生产与管理四、烧结产品与应用领域1.烧结产品分类2.应用领域及市场需求五、烧结技术创新与发展趋势1.绿色环保烧结技术2.高效节能烧结工艺3.智能化烧结工厂正文:一、烧结技术简介1.烧结定义与原理烧结是一种通过高温加热将固体物料转变为具有较高强度、密度和特定性能的固体的过程。
在烧结过程中,原料颗粒间的相互作用力逐渐增强,颗粒内部的组织结构发生变化,从而使烧结体具有较好的物理和力学性能。
2.烧结工艺流程烧结工艺流程通常包括原料准备、混合料预处理、烧结、冷却和成品整理等步骤。
首先,对原料进行选择和配比,以满足烧结产品的性能要求。
然后,将原料进行混合,形成均匀的混合料。
接下来,将混合料放入烧结设备中,通过高温加热实现烧结。
烧结过程中,需要对烧结参数进行控制,以保证烧结体的质量。
最后,对烧结体进行冷却和整理,获得最终的成品。
二、烧结原料与设备1.原料选择与配比烧结原料的选择应根据烧结产品的性能要求,结合原料的物理、化学和力学性能进行。
在选择原料时,还需考虑原料的资源、价格和环境友好性等因素。
配比方面,要保证混合料的均匀性,防止烧结过程中出现成分不均的现象。
2.烧结设备分类及选型烧结设备主要包括回转窑、立磨、烧结砖机等。
在选型时,要根据烧结工艺要求、产量、投资预算等因素进行综合考虑,确保设备的性能和可靠性。
三、烧结过程控制与管理1.烧结参数控制烧结过程的主要参数包括温度、压力、气氛和时间等。
合理控制这些参数,可以保证烧结体的质量。
在实际操作中,可通过调节烧结设备的燃烧器、风机等部件来实现参数的控制。
2.质量检测与分析烧结过程的质量检测主要包括密度、强度、透气性等指标。
通过对这些指标的检测和分析,可以及时发现烧结过程中的问题,采取相应措施进行调整。
烧结砖瓦厂工艺设计手册
烧结砖瓦厂工艺设计手册
1. 原材料准备,这部分会详细描述所需原材料的种类、质量要求、采购渠道、存储方式等,以及原材料的配比和预处理工艺。
2. 成型工艺,这部分会介绍砖瓦的成型工艺流程,包括混合、成型、压制、切割等环节,以及成型设备的选型、工艺参数的设定和调整。
3. 干燥与烧结,砖瓦成型后需要进行干燥和烧结,设计手册会详细描述干燥炉和窑炉的结构和工作原理,以及干燥与烧结的工艺参数和控制方法。
4. 能源消耗与环保,这部分会分析砖瓦生产过程中的能源消耗情况,提出节能减排的建议和措施,确保生产过程符合环保要求。
5. 质量控制,设计手册中会包括对砖瓦产品质量的要求和检测方法,以及生产过程中的质量控制措施和标准。
6. 安全生产,针对砖瓦生产过程中可能存在的安全隐患,设计手册会详细列出安全操作规程和事故应急预案,确保生产过程安全
稳定进行。
总之,烧结砖瓦厂工艺设计手册是砖瓦生产过程中的重要参考依据,它的编制需要综合考虑原材料、工艺流程、设备选型、能源消耗、质量控制、安全生产等多个方面的因素,以确保砖瓦生产过程稳定高效、产品质量稳定可靠。
庚辰钢铁180m2烧结机委托设计说明书
180m2带式烧结机委托设计说明书甲方:乙方:甲方计划在生产厂区现在的矿粉储存场地建设一台180m2带式烧结机(详细位置见甲方厂区总地形图和现场),特委托乙方承担整个工程项目的设计工作,具体情况如下。
一、项目名称庚辰钢铁有限公司烧结工艺装备升级、环保达标改造项目二、项目设计依据和相关数据1、符合国家最新环保政策及相关文件。
2、以委托设计说明书中相关要求为基本依据;遵守甲乙双方有关本项目技术沟通的相关会议纪要和技术文件。
3、依照厂内原料、燃料、电气、水源、地质地貌等基础条件和产品的要求。
4、气象条件JN市地处我国暖湿地区,夏季多雨,冬季晴朗干燥,年主导风向夏季为南、西南风,冬季为东、东北风,根据省气象局提供的1951-1987年气象资料,摘录如下:极端最低气温-19.7℃(1953.1.7);极端最高气温42.5℃(19557.22);一日最大降水量298.4mm(1962.7.23);最大冻土深度440mm(1968年共4天);最大积雪深度190mm(1971.3.2);最大风速及风向33.3m/s(西风,1951.7.21);极大(瞬时)风速及风向34.8m/s(西风1977.7.14);常年降雨量600-700mm。
基本风压0.4KN/m2;基本雪压0.2KN/m2;大气压力:冬季1000.2hPa,夏季998.5hPa。
厂区所在位置地震裂度:该位置在GD镇,处于鲁中山地北坡的山前倾斜平原上,东西两侧有两条倾向相对的正断层,发育在古生代地层中,第四系沉积较厚,场地周围未发现第四纪断层。
厂区平均海拨高度53米。
据分析,该地未来地震影响主要可能来自在鲁西南发生的强地震,该处影响烈度在Ⅵ-Ⅶ度间,基本定在Ⅵ度。
5、原料、燃料指标1) 精矿粉(常用有5种):TFe61~63%,其中含S≤0.2,P≤0.016;因业主方产品要求,烧结配料中精矿粉比例约占60~65%。
主抽风机及脱硫系统的设计需考虑配料的透气性、硫含量。
烧结配料系统设计说明
烧结配料系统设计说明:
设计参照承钢2#烧系统设计,烧结配料系统初步估计主要设备有:17套配料装置和一条集料皮带机,附加了一次混合设备。
如有变化可根据要求更正。
但此设计点号和方案基本适用。
一、设备说明:
1)1#--8#配料装置是定量圆盘给料机8套,用于配铁料的。
2)9#--13#配料装置是定量螺旋给料机5套,用于配溶剂的;增设了消化器装置。
3)14#--17#配料装置是定量皮带给料机4套,用于配燃料的。
4)一条集料皮带机,用于运料。
5)一次混合设备,一混设备加入控制更容易实现皮带与一混设备的同步控制,避免料堆积。
6)17套配料装置所用电机均由变频器控制,具备调速功能。
二、方案:
方案一:
采用S7-400的CPU控制
方案二:
说明:
1.设备价格为未加税收的价格,去经销商处采购须加20%的税收。
2.方案一硬件配置高,采用S7-400的CPU优势:①稳定性高;②响应速度快;
③扩展功能强大。
3.2个方案均采用热插拔导轨配置,支持在线带电更换模块的功能。
避免因模块故障而影响生产。
4.其他费用:主控柜、工控机、显示器、继电器、0.5mm²线等视情况而定。
编程点号统计参考。
240烧结方案说明书
240m2烧结机工程方案说明书1. 设计原则1.1 采用成熟稳定、实用可靠的工艺流程和设备,技术装备水平和主要技术经济指标达到国内先进水平。
1.2 控制水平要求经济、稳定可靠、实用,确保产品质量和稳定高产。
1.3 采用实用可靠的环保技术和装备,防止和减少粉尘、噪声等对环境的污染,达到国家、地方、企业的环保要求,除尘灰回收利用。
无生产污水排放。
1.4 严格执行现行的国家或地方关于节能、环保、消防、劳动安全卫生等方面的标准、法律、法规、规定和规范。
1.5 总图布置做到工艺流程合理、顺畅、紧凑;2. 工厂规模、工作制度及产品方案2.1 工厂规模生产规模为1台240m2烧结机,烧结机利用系数正常为1.20t/(m2·h),最大为1.45t/(m2·h),年产高碱度冷烧结矿正常为228万吨。
2.2 工作制度烧结系统为连续工作制,每天三班,每班8小时。
烧结机年工作330天,年工作7920小时,年作业率为90.4%。
2.3 产品方案产品为温度小于120℃经过整粒的冷烧结矿,粒度5~150mm,其中>50mm含量小于10%,<5mm含量小于5%。
转鼓强度(+6.3mm)≥75%。
根据假定原料条件计算的烧结矿化学成分见表1-1。
烧结矿化学成分表1-13. 原料条件3.1 含铁原料混匀铁料来自料场,高炉返矿来自高炉矿槽下。
3.2 熔剂熔剂生石灰粒度为3~0mm,采用气动输送,白云石、石灰石粒度均为3~0mm,采用汽车运至烧结厂熔剂受矿槽。
3.3 燃料3.3.1 固体燃料固体燃料为焦粉和无烟煤,粒度为20~0mm,采用汽车运至烧结厂燃料受矿槽或来自高炉矿槽下。
3.3.2 气体燃料烧结机点火燃料为高炉煤气,热值约为3140kJ/m3(750kCal/m3),车间接点压力约7000Pa,正常用量12960m3/h,最大用量15660 m3/h。
4. 技术装备水平该工程采用国内先进成熟的工艺流程,选用新型工艺设备,技术装备水平如下。
《烧结球团厂设计》课程设计指导书2011
《烧结球团厂设计》课程设计指导书(矿物加工团矿方向用)中南大学2011年12月目录1 课程设计目的 (1)2 课程设计任务 (1)3 设计基本资料及内容 (1)3.1 配料计算 (2)3.2 燃实破碎流程选择、设备选择与计算 (3)3.3 熔剂破碎流程选择、设备选择与计算 (4)3.4 混合设备的选择与计算 (4)3.5 烧结设备的选择与计算 (5)3.6 冷却机及整料流程选择 (5)3.7 图纸 (5)4 设计要求 (5)5 设计说明书要求 (6)5.1 绪论 (6)5.2 工艺流程的选择和论证 (2)5.3 烧结配料计算及物料平衡计算 (2)5.4 主要设备的选择和计算 (2)6 图纸幅面及格式要求 (7)6.1 图纸幅面 (7)6.2 图纸格式 (8)6.3 标题栏 (10)附录主要计量单位及符号 (11)1 课程设计目的通过课程设计巩固《烧结球团厂设计》所学的内容,初步掌握烧结配料计算方法、物料平衡计算方法,主要设备选择及工程图纸绘制的要求、初步掌握烧结说明书编写内容及方法。
2 课程设计任务设计任务见表1表1 个人设计任务(按学号对号入座)续表1 个人设计任务(按学号对号入座)3 设计基本资料及内容3.1 配料计算3.1.1 配料计算基本资料(1)烧结矿年产量(见表1)。
(2)烧结矿碱度(CaO/SiO2)、FeO含量见表1。
(3)高炉灰单耗每吨烧结矿为120kg;燃料单耗为每吨烧结矿75kg(煤)或55kg(焦粉)。
(4)含铁原料、燃料、熔化物化性能见表2。
(5)三种铁矿石中至少配2种。
(6)烧结矿脱硫率为90%。
(7)混合料水分(6.5~7.5%),根据配人富矿粉和精矿粉比例不同,而有所不同,富矿粉高,混合料水分偏低,精矿比例高,混合料水分偏高。
(8)返矿量占干混合料的30%(内配)。
表2 原料物化性能注:无烟煤中固定炭74.04%. 挥发份8.8%. 灰粉17.16%;碎焦中固定炭84.50%.挥发份2.9%. 灰粉12.6%;3.1.2 计算内容(1)计算各种原料的配比、日及年需要量。
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1 Introduction1.1 OutlineThe design reference Baosteel sintering plant, according to the design requirements of the mission statement, the design production capacity of 300 tons, the sintering plant products of high quality for blast furnace sinter.Because annular cooler temperature exhaust gas discharged with the airflow and fine dust released into the air, allowing more serious environmental pollution, while a large number of hot exhaust gas into the atmosphere, waste heat, dust and heat in order to reduce emissions, reduce pollution of the environment, the design of the ring after a hot exhaust gas cooler dust stove and holding furnace used for point after.The design of the sintering engineering technology, equipment level and the degree of automation and, basically, Baosteel sintering plant rather, is the world's advanced level, the design of a complete process: thick material layer sintering, centralized dust removal system, dual diagonal band spot stove, the addition of a ring cooler holding furnace and hot exhaust gas emissions as a promoter, these are the sintering process technology and equipment constitute the main content, but also an important indicator of the level of today's world.1.2 Design basis and design principles1.2.1 Design basisThis design is the Central South University of Resources Processing and Bioengineering pellets Professional 2013 session of the graduate design task, entitled "Design sinter plant of an annual output of 3 million tons of sinter" which combined in Baosteel graduation internship process field data collected and the master site processes and equipment prepared on the basis of.1.2.1 Design principlesIn order to do this sinter plant design, intended to the following design principles:1) According to today's world sintering technology, combined with the actual situation of Baosteel, determine the design process technology and equipment level.2) reasonably compact device configuration, production workshop has sufficient operating area to ensure smooth material transport facilities.3) selection of equipment, construction to achieve standardization and universal.4) Take effective measures to reduce the sinter plant dust pollution.5) Consider the possibility of future expansion.1.3 Design rangeThe design of the sintering project include the following:1) coke crushing and screening system.2) ingredients mixed system.3) sintering and cooling system.4) the main electrical room.5) finished crushing and screening system.6) the dust handling system.2 Iron-containing materials, flux, fuel2.1 iron-containing materialsThe design of the sintering plant iron raw materials including imported iron ore , national concentrates.Imported iron ore is a high iron low silicon raw materials, mainly from India, Brazil, Australia and other importing countries. Imported Materials ore from the steamer pier, transported by belt conveyor to the raw material yard, through Neutralization and mix on the yard, then by belt conveyor to the dosing chamber, Sintering plant mainly recyclable materials is iron by the belt conveyor to the field and mixed with other Materials Materials , to pre-dosing effect. Iron-containing materials in the yard after mixing , directly to the dosing chamber.2.1.1 Chemical composition of iron-containing materialsThe chemical composition of iron-containing materials into the plant in Table 2-1.2.1.2 The requirements Size and grade1) the size requirements: Fines <8mm.(2) grade requirements: iron grade fluctuation range ±0.5%;FeO fluctuation range ±0.1%;S fluctuation range ±0.08%.2.2 FluxBecause most iron raw materials used is high-speed rail low silicon raw material,in order to improve the quality of sinter and improve the fluidity of slag, this design uses dolomite, limestone and quicklime as flux. Mixture granulated quicklime The quicklime is used to enhance mixture granulation and improve the permeability3.Sintering Process Selection and VerificationAccording to material properties, select the appropriate sintering method, processing procedures and process systems,in order to obtain the desired product. Sintering process designed mainly for the process of analysis and the basic principles for selection process .3.1The meaning and requirements for selecting processProcess is an integrated of certain processes from production process.Sintering process of selection is an important part of the design process. A new sintering plant around all the design elements are determined by the unfolding process. Reasonable production process, equipment capacity is full, rational organization of production, to ensure continuous production, access to advanced technical and economic indicators of important factors. Therefore, the process of selection, must be fully considered, multi-program comparison.Process selection requirement is to ensure the product quality requirements of the premise, to maximize the use of various iron-containing materials, and access to high labor productivity and equipment utilization, conserve energy as much as possible to save production costs for enterprises to seek maximum profit; and to adopt modern means of production, strong labor intensity, improve operational and management level; should consider radical waste pollution, protect the environment and health, protection of workers' health.3.2 Raw materials, flux and fuel3.2.1Raw material preparationThe raw materials used to design the main ore powder, powder ore controls below 8mm size requirements, into the iron-containing raw materials and sintering mix ingredients in order to achieve results. This procedure offers a raw material in thesteel mill plant, mix mine via conveyor belt to produce sinter plant ingredients.Sintered material into the sinter plant conditions:1) bonanza powder particle size should be 8-0mm (also available 6-0mm), ore particle size of more than 10% +8 mm will affect the quality of sinter. Special powder size requirements should be based on experimentally determined. SiO2 content fluctuations should be less than or equal ± 0.2%. Iron grade fluctuations should satisfy the following conditions; large and extra large sinter plant should be less than or equal ± 0.5%; medium-sized sinter plant should be less than equal to ± 0.75%; small sinter plant should be less than equal to ± 1.0%.2) magnetite concentrate moisture should be less than 10%, hematite concentrate moisture should be less than 11%. Concentrate moisture exceeds this requirement, the proportioning accuracy, affecting mixing uniformity.3) Blast should be appropriate wetting dry dust, blast furnace and BOF dust and sludge secondary dust should be dehydrated, so that water is less than 15%.4) Rolling Paper size not greater than 8mm.5) of the iron-containing material harmful impurities should be limited as required.When raw iron grade volatile than <sintering plant design requirements> requirements, should be shot mix stockyard and, if possible together with the steel plant was built in order to achieve sintering, pelletizing plant feed ingredients stable, uniform size. For medium and small sintering plant should also be set up according to the specific conditions of mixing facilities; raw single species, grade fluctuation is small, or not to set mixing facilities. But it should be built by the mining of raw materials warehouse and warehouse and so on. There blending stockyard, the sintering plant should no longer raw materials warehouse. But in wet areas should be located indoor storage facilities.Medium-sized sinter plant material should be adopted by the dumper. Dumper is a large unloading equipment, which is widely used in large and medium-sized and some large sintering plant sinter plant. It has the unloading of high efficiency, large capacity, suitable for all kinds of bulk material unloading turn. Because high degree of mechanization, is conducive to automated or semi-automated unloading operations.By mine shafts is used only by the material and not for storage facilities. Generally used for steel mills to accept bulk materials and auxiliary materials. By mine chute design should consider the use of mechanized equipment. Small mines can be spiral unloading machine or a chain-head unloading machine to accept raw materials. Most of the raw materials warehouse sintering plant designed to stabilize production, raw materials warehouse storage time of various materials as follows: iron-containing materials, a dedicated transmission line for the five days, no special transport line for the seven days; fuels and solvents , a dedicated conveyor line for the 3-5 days, no special transport line for 7 days. As for the small sinter plant under specific conditions. Freezing cold regions receiving and storage of raw materials should have anti-freeze thawed facilities.3.2.2 Flux preparationSintering production on the granularity of flux, there are strict regulations generally require 3 ~ 0mm content should be greater than 85% while the flux into the plant size is 40 ~ 0mm, so you need to be broken.Flux in the raw material crushing plant is complete. Dolomite, limestone crushing to the required 3 ~ 0mm, via tape machine to the dosing chamber. Lime particle size of 3 ~ 0mm, from the limestone, dolomite roasting plant is provided with a suction pressure tank to the sintering plant dosing chamber, and then compressed into the batching tank.(1) flux crushing and screening process generally has three:1) Open broken rod mill machining processes.2) Closed hammer crusher crushing and screening process flow.3) Impact Crusher closed circuit crushing and screening process flow.Closed flux machining processes are generally used in closed-circuit crushing and screening processing flow, can be divided into two kinds of pre-screening and screening examination. When the flux ore 3-0mm level content more time (generally 30% -40% or more), before use of pre-screening. Otherwise, adopt screening. Check the screening process sieve material for the product, the oversize material back into the crusher heavy breaking. More generally sintering plant using this process.Closed flux machining processes are generally used in closed process, can be divided into pre-screening and pre-screening process closed-circuit crushing and screening checks closed circuit combining two kinds. When the flux ore 3 ~ 0mm level for a long time (generally 30% to 40%), before use of pre-screening. Otherwise, the check screening. Check the screening process under size product for the product, the oversize material back into the crusher broken again. Taking into account the material conditions of this design, the design uses a closed circuit with a screening examination.(2) broken equipmentConsidering the physical properties of raw materials, production capacity and size requirements, the advantages and disadvantages of the crushing equipment discussed below:1) Impact CrusherScope: brittle, medium hard minerals (metallic, C), sintering plant (limestone, dolomite).Advantages: uniform size, over crushed small, light weight, low power consumption, large capacity, large crushing ratio.Disadvantages: vibration, noise, dust, wear big.2) hammer crusher (reversible and irreversible)Scope: brittle, medium-hard, hard and soft minerals (limestone, dolomite and serpentine), the crushing (3 ~ 0mm), rarely used in primary crushing.Pros: large capacity, large crushing ratio; structure is simple, compact, low power consumption and easy maintenance.Disadvantages: wear and high moisture blocking material is easy.3) rod millScope: Baosteel crushing equipment used in the second paragraph of coke.Advantages: too little crush.Disadvantages: high power consumption, low output and heavy equipment.4) four roller crusher (on the roll)Scope of application: Widely used in sinter plant fuel broken.Advantages: can be completed in time, fine, no screening classification, simpleprocess.Cons: roller uneven wear.Common flux crushing equipment crusher and hammer crusher two kinds.Crusher has uniform particle size, over crushed small, light weight, low power consumption, large capacity, large crushing ratio, etc., hammer crusher with high yield, large crushing ratio, low power consumption per unit of product, easy maintenance, etc. advantages in the production of the two devices is different, but the impact crusher vibration, noise, dust capacity, wear and therefore in the design selection hammer crusher. Hammer crusher can be divided into two kinds of reversible and irreversible and reversible hammer crusher hammer function to extend the service life and ensure the crushing efficiency, so the design are made of reversible hammer crusher.(3) screening equipmentSintering plant flux screening equipment is mainly shaker.The design uses a self-centering shakerSelf-centering shaker has the advantage of simple structure, use, operation and replacement of the screen surface is more convenient, strong vibration sieve surface, and the vibration direction perpendicular to the screen surface can reduce the material clogging the sieve of the phenomenon, with high screening efficiency (up to 90 ~ 95%) and production capacity, suitable for medium, fine screening, does not apply to coarse sieve.The disadvantage is that the amplitude of the sieve with the size of the amount to the mine fluctuate, resulting in screening efficiency is not stable enough; sieve in the process of starting and stopping, through resonance, the amplitude increases, a greater impact on the sieve and buildings.11。