污水处理厂工艺总平面布置图

合集下载

水污染课程设计----污水处理厂AAO工艺设计(含全套图纸)

水污染课程设计----污水处理厂AAO工艺设计(含全套图纸)

《水污染控制工程》课程设计学院:专业:XX:学号:指导老师:目录引言41设计任务及设计资料5 1.1设计任务与内容51.2设计原始资料51.2.1城市气象资料51.2.2地质资料51.2.3设计规模51.2.4进出水水质62、设计说明书6 2.1去除率的计算62.1.1溶解性BOD的去除率65的去除率:72.1.2 CODr2.1.3.SS的去除率:72.1.4.总氮的去除率:72.1.5.磷酸盐的去除率82.2城市污水处理工艺选择82.3、污水厂总平面图的布置92.4、处理构筑物设计流量(二级)92.5、污水处理构筑物设计92.5.1.中格栅和提升泵房(两者合建在一起)9 2.5.2、沉沙池102.5.3、厌氧池112.5.4、缺氧池112.5.5、好氧曝气池112.5.6、二沉池122.6、污泥处理构筑物的设计计算122.6.1污泥泵房122.6.2污泥浓缩池122.7、污水厂平面,高程布置132.7.1平面布置132.7.2管线布置132.7.3 高程布置143 污水厂设计计算书14 3.1污水处理构筑物设计计算143.1.1泵前中格栅143.1.2污水提升泵房163.1.3、泵后细格栅173.1.3、沉砂池183.1.4、厌氧池203.1.5、缺氧池计算203.1.6、好氧曝气池的设计计算213.1.8、二沉池283.2 污泥处理部分构筑物计算313.2.1污泥浓缩池设计计算:313.3、高程计算363.3.1污水处理部分高程计算:363.3.2高程图见CAD图363.3.3污水处理厂工艺流程图与总平面布置图36参考文献37XX市污水处理厂A/A/O工艺设计作者:闫赛红,指导教师:孙丰霞(XX农业大学资源与环境学院)【摘要】随着社会进步,人们对于城市污水的处理的要求愈加严格。

除了基本的去除污水中BOD和SS的要求外,通常还要求脱氮除磷,以保护水体环境。

本设计即采用了众多脱氮除磷工艺中较为经济合理的AAO工艺对进入污水厂的污水进行处理。

天津东郊污水处理厂设计实例

天津东郊污水处理厂设计实例

天津东郊污水处理厂设计实例天津东郊污水处理厂于1989年8月开工,1993年4月建成,污水厂占地29.5hm 2,工程总造价20159万元。

1. 水质水量设计处理能力为40万m 3/d ,最高日流量(不脱氮)48万m 3/d 。

进水BOD 5280mg/L ,出水40mg/L ;进水SS240mg/L ,出水60mg/L 。

2. 处理工艺流程图1 天津东郊污水处理厂工艺流程图图2 天津东郊污水处理厂总平面布置图该厂污水处理系统分4个系列,4个圆形初沉池排成一行,4个曝气池组成田字型,8座二沉池设在厂区南侧,临近北塘排水河,使处理出水可就近排入河道。

污泥处理区设在厂的西北角,5个消化池组成梅花型,污泥处理的控制室设在5个消化池的中央。

北侧设有两个沼气贮罐、污泥脱水机房和沼气发电机房等。

3、主要处理构筑物及设备参数(1)进水格栅格栅是污水处理厂的第一道预处理设施。

该厂设6台垂直格栅,由计算机程序控制。

高水位时格栅清污机将连续工作,运送格栅拦截的浮渣的皮带运输机与格栅清污机联锁运行,在所有格栅停止工作后,皮带运输机仍将继续运行一段时间。

6台垂直格栅每台宽2m,栅条净宽25mm。

(2)进水泵房设6台HLWB-10型立式涡壳混流泵,5用1备。

水泵参数:流量1.32m3/s,扬程13.2m,电机功率260kw。

泵房设有6个控制水位,控制5台泵的运行。

为避免个别水泵负荷偏高而反复启动,水泵将依次循环投入运行。

当某台泵因故障停止工作时,另一台泵将自动投入运行。

(3)曲面格栅8台曲面格栅设在沉砂池的端部。

每台格栅宽度1.2m,栅条曲率半径2.0m,栅条净距10mm。

每台格栅的清污动作根据水位模拟信号由计算机控制。

当水位差处于正常值时,清污工作将按设定时间动作;当前后水位差超过设定值时,清污工作将连续进行。

如果清污工作连续操作时间过长,计算机将发出报警信号。

曲面格栅刮出的浮渣落在皮带运输机上,皮带运输机的运行与格栅清污机联锁,清污工作停止后,运输机仍将运行一段时间。

一体化污水提升泵站工艺施工平面图剖面图

一体化污水提升泵站工艺施工平面图剖面图
吊耳吊物孔爬梯吊物孔CCDN200就地按钮箱地脚螺栓水泵导杆导杆支承座电控柜维修平台支撑架(停机液位)(启泵液位)DN500DN300(维修平台)通气管玻璃钢爬梯不锈钢扶梯BBB-B剖面图弹簧式玻璃钢顶盖通气帽顶部玻璃钢盖板泵基础底座通气管底部不封口通气帽做法见大样不锈钢扶梯不锈钢螺栓%%C32不锈钢扶梯通气管顶部不封口DN300防雨帽底部不封口开启把手200槽钢不锈钢螺栓连接维修平台上为检修平台不锈钢DN500DN300bcadfgdgbge维修平台支撑架DD向视图C-C剖面图中间维修平台平面图把 手 把手把手自格栅渠去阀门井起重机基础罐体基础2. 本图标高采用绝对标高,高程体系为黄海高程。1. 本图标高以m计,其余均以mm计。说明:3. 设计规模6000m/d,最大时设计流量420m/h。34. 土建施工前,需对所提供所有设备基础及预埋件等资料进行核实,并经一体化泵站供货商确认本设计满足其安装要求后方可进行施工。(入口/报警液位)A-A剖面图DN200DN300DN200DN200DN200D向视图-筒体内部管道图6.000.605.704.205.705.706.000.95-2.05-2.65-2.65(维修平台)2.602.60(启泵液位)0.95-1.251.851.853.403.40DN200DN2009.00(停机液位)-2.054.20泵站平面图罐体基础污水提升泵房工艺设计总说明厚浆型防腐面漆(H52-2)两道。4、五、施工要求四、管道与钢件防腐柔性接头及连接的法兰螺栓的防腐作法同埋地钢管(法兰及螺栓均包在防腐层内)。上述防腐要求的具体施工方法应严格遵照有关规范进行操作。1、所有的钢管件及管道支架(不锈钢除外)涂漆前必须进行表面除锈处理,达到Sa2.5级后,方可进行2、埋地钢管外壁防腐:环氧富锌底漆(H06-1)一道,环氧云铁防锈底漆(H53-6)一道,再以3、明装钢管及管支架外涂环氧富锌底漆(H06-1)一道,环氧云铁防锈底漆(H53-6) 一道,环氧厚浆型环氧煤沥青防腐涂料(HL52-3)为面漆,三油二布作加强防腐,玻璃布为0.12-0.18mm厚,六、其它《给水排水管道工程施工及验收规范》GB 50268-2008执行,建议采用不锈钢螺栓。4、施工过程中,本图必须与电气及土建图纸配合使用。施工过程中若发现工艺图纸与土建图纸不符,净空尺寸以工艺图为准,2、渠道及闸门井盖板采用镀锌网格钢盖板。8、管道支吊、托架做法:其间距及具体形式由施工单位参照标准图S161进行。8-8页,泵房穿墙套管采用IV型刚性防水套管,做法见标准S312 8-7页。6、检修机械格栅清污机,且不允许停产时,可使用备用人工格栅。4、管道试压∶所有管道施工完毕后做水压试验,试验压力为1.2MPa。5、在进入格栅间进水渠道检修时,必须采取强制机械排风措施,检修人员必须戴防毒面具,以确保检修人员的人身安全。阅读产品说明书,并对照图纸对设备的各部分尺寸进行认真复核,设备安装应在生产厂家的指导下进行,以保证安装的顺利1、施工时应根据到货设备核对留洞及予埋件位置,由于不同设备生产厂家的设备尺寸有差异,各种设备在安装前,必须仔细进行。7、套管穿池壁做法:预埋管按材料表中要求采用刚性防水套管或刚性防水翼环,做法见图纸04页详图或参照标准图S312 3、管道连接:按图纸所示,除法兰连接外,其它连接处采用焊接,配套法兰压力等级为1.5MPa,管道安装及验收按照污水压力管污水提升泵3格栅破碎机一体化泵站一、总则污水进水管二、设备选型2、格栅选用PZG1-20×6型单电机转鼓式格栅破碎机,机体材质均为不锈钢。污水内垃圾经破碎机等常规保护。1、污水提升泵选用三台XFP150G-CB1型,两用一备,自动耦合式安装。水泵应有过载过热泄漏闸门井2、标高采用黄海高程系,坐标采用青岛市城市坐标系。3、本泵站设计流量6000m/d,最大时设计毫米计。4、控制闸板手动启闭机:根据现场运行情况人工手动开启及关闭,调整开启度。4、控制闸门选用600×600方形镶铜铸铁附壁安装式,配手动启闭机。1、潜水排污泵:潜水排污泵均要求集中自动控制。潜水排污泵自动运行,以水位控制自动运行。潜水排污泵三、控制与信号破碎后进入一体化泵站经水泵抽走。有自动巡检功能,每台泵每周投入运行的时间不少于60分钟。2、PZG1-20×6型单电机转鼓式格栅破碎机要求集中自动控制。2、管件应严格按照图纸及GB3420-82进行加工,到货后对管件接口要认真检查,保证法兰面平整光滑。溢流管9、泵站值班室配备便携式硫化氢气体检测报警仪及一氧化碳控制报警仪。3DN300%%C700检修孔DN500进水管42004200400037025003703707003705007508007504000220030012003002500370150014870接污水压力管200%%c320034004200%%C32003005003500250泵站筒壁钢筋混凝土素混凝土起重机基础地脚螺栓地脚螺栓需与钢筋焊牢6.00起重机起重机基础大样图DN300污水压力管500AA30030050037025003703003005.701.050.603.300.700.00DN500进水管0.9548508000.006005.706.00800B镀锌钢格盖板大样图(B+120)X1590镀锌钢格盖板B+120705070508650%%c32003400420042004200∅3200200020002501800200020003DN400溢流管3.706006003、一体化泵站内所有设备、管件、水泵起吊装置及电控箱均在泵站供货商的供货范围内,所有设备的控制采用自动化控制,订货时需向设备供货商说明。防腐处理。脱脂无碱型。结构尺寸以土建施工图为准。60060037006002200300120060010、栏杆及钢爬梯做法见建筑施工图说明。型号:XFP150G-CB1 参数:Q=215m/h, H=15m,N=15kW最大过水量600m /h,电机功率4kWbdcefg序号a转鼓式格栅破碎机一体化泵站井筒电磁流量计潜水排污泵自动耦合装置名 称潜水排污泵备 注主要设备表单位3规 格材料1套台31台台1井壁应有足够的刚度,能够数量3台二用一备 电机配套 j型 号PZG1-20×6与水泵配套不锈钢%%C3200X8650mm电动起重机1套起重量500kg,起吊高度10米。就地按钮箱1套一体化泵站生产厂家配套带4~20mA信号输出DN200,最大过水能力1200m /hLDBZB-200镶铜铸铁方闸门1台附壁式安装600X600mm,井深6.60mAXF-600X600玻璃钢抵御土压力M可曲挠柔性橡胶接头DN500可曲挠柔性橡胶接头DN3005.90h20002000地脚螺栓双盘异径管DN100*150DN200可曲挠柔性橡胶接头管道支架DN300jkbd双盘异径管DN300*200DN200双法兰限位伸缩接头双盘异径管DN300*200可曲挠柔性橡胶接头DN300双盘异径管DN300*200DN200双法兰限位伸缩接头双盘短管,DN300*350mmjMk可曲挠柔性橡胶接头DN500hg1、本泵站采用一体化泵站,泵站井筒及井筒内所有设备、阀门、管件、爬梯、检修平台、其它附件及起重设备均属一体化泵站生产商供货范围。手动启闭机1台与闸门配套6003、闸门井内设置了沉砂坑,需定期清理坑内沉积物。h33M1予埋钢板详图∅12圆钢安装时焊接M1预埋件预埋钢板2-1467X100X10压 向焊接预留洞口,%%c15080122508026040040026040014677506301467630390790600x600150123X4032188.338Y563778.856

20000m3d城市污水处理厂综合设计(含11个CAD作图图纸)--优秀毕业设计{修}

20000m3d城市污水处理厂综合设计(含11个CAD作图图纸)--优秀毕业设计{修}

本设计污水处理厂综合设计包括15个图纸,十分全面,具体详见报告后附图。

本报告附图全面详细。

图纸内容如下:A2O池,初沉池,幅流式二沉池,隔栅,工艺简单图,工艺流程图(高程图),回转耙式格栅除污机图,平面布置图,污泥浓缩池,厌氧消化池,钟式沉砂池等。

全为CAD制图。

下载后复制放大或打印可看清!题目20000m3/d城市污水处理厂综合设计专业: 环境工程年级: 2005级学号: 3105001286姓名: 莫笑伟指导教师:2008年12 月摘要我国水体污染主要来自两方面,一是工业发展超标排放工业废水,二是城市化中由于城市污水排放和集中处理设施严重缺乏,大量生活污水未经处理直接进入水体造成环境污染。

工业废水近年来经过治理虽有所减少,但城市生活污水有增无减,占水质污染的51%以上。

我国水体污染主要来自两方面,一是工业发展超标排放工业废水,二是城市化中由于城市污水排放和集中处理设施严重缺乏,大量生活污水未经处理直接进入水体造成环境污染。

工业废水近年来经过治理虽有所减少,但城市生活污水有增无减,占水质污染的51%以上。

本设计要求处理水量为20000m3/d的城市生活污水,设计方案针对已运行稳定有效的A2/O活性污泥法工艺处理城市生活污水。

A2O工艺由于不同环境条件,不同功能的微)能生物群落的有机配合,加之厌氧、缺氧条件下,部分不可生物降解的有机物(CODNB被开环或断链,使得N、P、有机碳被同时去除,并提高对COD的去除效果。

它可以同NB--时完成有机物的去除,硝化脱氮、磷的过量摄取而被去除等功能,脱氮的前提是NH3N应完全硝化,好氧池能完成这一功能,缺氧池则完成脱氮功能。

厌氧池和好氧池联合完成除磷功能。

关键词:城市生活污水,活性污泥,A2/O目录摘要 (III)目录 (IV)第一章设计概述 ······································································- 7 -1设计任务 ······································································- 7 - 2设计原则 ······································································- 7 - 3设计依据 ······································································- 8 - 第二章工艺流程及说明 ·····························································- 8 -1工艺方案分析 ································································- 8 - 2工艺流程 ······································································- 9 - 3流程各结构介绍 ·····························································- 9 -3.1格栅······························································································· - 9 -3.2沉砂池··························································································- 10 -3.3初沉池··························································································- 10 -3.4生物化反应池··············································································- 10 -3.5二沉池··························································································- 12 -3.6浓缩池··························································································- 12 - 第三章构筑物设计计算 ··························································· - 12 -1格栅 ·········································································· - 12 -1.1设计说明······················································································- 12 -1.2设计计算······················································································- 13 -2沉砂池 ······································································· - 16 -2.1设计说明······················································································- 16 - 3初沉池 ······································································· - 17 -3.1设计说明······················································································- 17 -3.2设计计算······················································································- 17 - 4生化池 ······································································· - 19 -4.1设计说明······················································································- 19 -4.2设计计算······················································································- 19 - 5二沉池 ······································································· - 26 -5.1设计说明······················································································- 26 -5.2设计计算······················································································- 26 - 6液氯消毒 ···································································· - 29 -6.1设计说明······················································································- 29 -6.2设计计算······················································································- 29 - 7污泥浓缩池 ································································· - 30 -7.1设计说明······················································································- 30 -7.2设计计算······················································································- 30 -8 污泥消化池 ································································· - 31 -8.1设计说明······················································································- 31 -8.2设计计算······················································································- 32 - 9浓缩污泥提升泵房 ························································ - 38 -9.1设计选型······················································································- 38 -9.2提升泵房······················································································- 38 -9.3污泥回流泵站··············································································- 38 -10污泥脱水间 ······························································· - 39 -10.1设计说明······················································································- 39 -11鼓风机房 ·································································· - 39 - 12恶臭处理系统 ···························································· - 39 -12.1设计说明······················································································- 39 -12.2设计计算······················································································- 39 -12.3风机选型······················································································- 40 - 第四章污水处理厂总体布置 ····················································· - 41 -1总平面布置 ································································· - 41 -1.1总平面布置原则··········································································- 41 -1.2总平面布置结果··········································································- 41 -2高程布置································································································- 42 -2.1高程布置原则··············································································- 42 - 第五章参考文献 ···································································· - 42 -第一章设计概述1设计任务本次课程设计的主要任务是完成某城市污水厂的A2/O工艺设计处理生活污水,处理水量为20000m3/d,按近期规划人口10万人计算(自定)。

20000m3d城市污水处理厂综合设计(含11个CAD作图图纸)--优秀毕业设计

20000m3d城市污水处理厂综合设计(含11个CAD作图图纸)--优秀毕业设计

本设计污水处理厂综合设计包括15个图纸,十分全面,具体详见报告后附图。

本报告附图全面详细。

图纸内容如下:A2O池,初沉池,幅流式二沉池,隔栅,工艺简单图,工艺流程图(高程图),回转耙式格栅除污机图,平面布置图,污泥浓缩池,厌氧消化池,钟式沉砂池等。

全为CAD制图。

下载后复制放大或打印可看清!题目20000m3/d城市污水处理厂综合设计专业: 环境工程年级: 2005级学号: 3105001286姓名: 莫笑伟指导教师:2008年12 月摘要我国水体污染主要来自两方面,一是工业发展超标排放工业废水,二是城市化中由于城市污水排放和集中处理设施严重缺乏,大量生活污水未经处理直接进入水体造成环境污染。

工业废水近年来经过治理虽有所减少,但城市生活污水有增无减,占水质污染的51%以上。

我国水体污染主要来自两方面,一是工业发展超标排放工业废水,二是城市化中由于城市污水排放和集中处理设施严重缺乏,大量生活污水未经处理直接进入水体造成环境污染。

工业废水近年来经过治理虽有所减少,但城市生活污水有增无减,占水质污染的51%以上。

本设计要求处理水量为20000m3/d的城市生活污水,设计方案针对已运行稳定有效的A2/O活性污泥法工艺处理城市生活污水。

A2O工艺由于不同环境条件,不同功能的微)能生物群落的有机配合,加之厌氧、缺氧条件下,部分不可生物降解的有机物(CODNB被开环或断链,使得N、P、有机碳被同时去除,并提高对COD的去除效果。

它可以同NB--时完成有机物的去除,硝化脱氮、磷的过量摄取而被去除等功能,脱氮的前提是NH3N应完全硝化,好氧池能完成这一功能,缺氧池则完成脱氮功能。

厌氧池和好氧池联合完成除磷功能。

关键词:城市生活污水,活性污泥,A2/O目录摘要 (III)目录 (IV)第一章设计概述 ······································································- 7 -1设计任务 ······································································- 7 - 2设计原则 ······································································- 7 - 3设计依据 ······································································- 8 - 第二章工艺流程及说明 ·····························································- 8 -1工艺方案分析 ································································- 8 - 2工艺流程 ······································································- 9 - 3流程各结构介绍 ·····························································- 9 -3.1格栅······························································································· - 9 -3.2沉砂池··························································································- 10 -3.3初沉池··························································································- 10 -3.4生物化反应池··············································································- 10 -3.5二沉池··························································································- 12 -3.6浓缩池··························································································- 12 - 第三章构筑物设计计算 ··························································· - 12 -1格栅 ·········································································· - 12 -1.1设计说明······················································································- 12 -1.2设计计算······················································································- 13 -2沉砂池 ······································································· - 16 -2.1设计说明······················································································- 16 - 3初沉池 ······································································· - 17 -3.1设计说明······················································································- 17 -3.2设计计算······················································································- 17 - 4生化池 ······································································· - 19 -4.1设计说明······················································································- 19 -4.2设计计算······················································································- 19 - 5二沉池 ······································································· - 26 -5.1设计说明······················································································- 26 -5.2设计计算······················································································- 26 - 6液氯消毒 ···································································· - 29 -6.1设计说明······················································································- 29 -6.2设计计算······················································································- 29 - 7污泥浓缩池 ································································· - 30 -7.1设计说明······················································································- 30 -7.2设计计算······················································································- 30 -8 污泥消化池 ································································· - 31 -8.1设计说明······················································································- 31 -8.2设计计算······················································································- 32 - 9浓缩污泥提升泵房 ························································ - 38 -9.1设计选型······················································································- 38 -9.2提升泵房······················································································- 38 -9.3污泥回流泵站··············································································- 38 -10污泥脱水间 ······························································· - 39 -10.1设计说明······················································································- 39 -11鼓风机房 ·································································· - 39 - 12恶臭处理系统 ···························································· - 39 -12.1设计说明······················································································- 39 -12.2设计计算······················································································- 39 -12.3风机选型······················································································- 40 - 第四章污水处理厂总体布置 ····················································· - 41 -1总平面布置 ································································· - 41 -1.1总平面布置原则··········································································- 41 -1.2总平面布置结果··········································································- 41 -2高程布置································································································- 42 -2.1高程布置原则··············································································- 42 - 第五章参考文献 ···································································· - 42 -第一章设计概述1设计任务本次课程设计的主要任务是完成某城市污水厂的A2/O工艺设计处理生活污水,处理水量为20000m3/d,按近期规划人口10万人计算(自定)。

自来水厂污水处理二泵房成套cad设计图

自来水厂污水处理二泵房成套cad设计图
4500500090009000620033052660330610061006100450050009000900062003305266033061006100610045005000900090006200330102502100210074002100210044305570650210021002100210036001100220011002200220015002300100006950375028002500388015004690106603304650535033010660330465053503305266033061006100610021002100631082502900330033003750380038003300505031001100220026004430557031001500310015002300230015004430557010000375018003880210021004430557035503550210035003500250029001800二级泵房平面图 1:2000%%P0.00%%P0.002DN800出水管至用户11排水明渠铁篦子钢套管DN450管中心标高-5.05泵房M2DN450吸水管DN450吸水管DN600吸水管远期预留DN350 出水管14443511124363725332534351-1剖面图 1:1002-2剖面图 1:10033251052414161718131914152021171813191415201615%%P0.00%%P0.00%%P0.00%%P0.005.40-2.30-2.30-3.15%%P0.00%%P0.005.40-2.351212-3.1524M282726阀门井详07MS101-2第110页21管中心标高-5.05管中心标高-5.553131303132为远期预留泵位钢套管DN450钢套管DN600管中心标高-2.40防水套管DN80029配电室控制室门厅0.15%%P0.000.15-3.15下下-0.300BFC1812BFC1812%%P0.00-0.305.40-3.155.400.150.15-0.305.405.40-0.301管中心标高-2.30钢套管DN20038M101617181319152012M1016171813191520125管中心标高-5.10钢套管DN60040管中心标高-5.10钢套管DN60032MMM341414二泵房平面布置图水初-18MM202020DN350出水管-3.15-3.15DN450吸水管DN450吸水管16142012MDN350 出水管M51017181319152497接清水池出水管2接清水池出水管212133管中心标高-5.55钢套管DN600DN600吸水管远期预留DN600吸水管远期预留接清水池出水管接清水池出水管远期预留远期预留DN800出水管\P为远期预留111242424242424222DN700DN70044466777888999999222222232323管中心标高-5.0531钢套管DN45031钢套管DN450管中心标高-5.0530管中心标高-5.10钢套管DN60032324241DN600吸水管3-3剖面图 1:10033253214%%P0.00%%P0.005.40-2.30-2.3530315.40-0.30DN450出水管-3.15-3.152223241-2.30DN800出水管11-2.35282726-0.3039L2929M为远期预留泵位为远期预留泵位DRAWN BY制 图2014.01共34张GS2014-001第一版项目名称CHIEFDESIGNED BY专业负责设 计PROJECT工程编号PROJECT NO.版本编号EDITION NO.CLIENT建设单位环 卫建 筑编号DRAWING NO.日 期DRAWING TITLEAPPROVED BY校 对CHECKED BY审 核VERIFIED BYDATE道 路燃 气给 排 水热 力初步设计设计阶段DESIGN PHASE地 址POST CODE邮政编码电子邮箱电 话传 真本人签名计算机签名地 址DRAWN BY制 图2014.01共34张GS2014-001第一版项目名称CHIEFDESIGNED BY专业负责设 计PROJECT工程编号PROJECT NO.版本编号EDITION NO.CLIENT建设单位环 卫建 筑结 构园 林电 气暖 通审 定图纸名称图纸编号DRAWING NO.日 期DRAWING TITLEAPPROVED BY校 对CHECKED BY审 核VERIFIED BYDATE道 路燃 气给 排 水热 力初步设计设计阶段DESIGN PHASE本人签名计算机签名二泵房剖图水初-19N2100210063108250290033003300375038003800330050503100110022002600443055701000069503750280025003880150046901066033046505350330106603304650535033052660330610061006100450050009000900062003305266033061006100610045005000900090006200330210021002100210036005266033061006100610045005000900090006200330102502100210074002100210044305570650110022001100220022001500230031001500310015002300230015004430557010000375018003880210021004430557035503550210035003500250029001800

水污染课程设计污水处理厂AAO工艺设计含全套图纸

水污染课程设计污水处理厂AAO工艺设计含全套图纸

《水污染控制工程》课程设计学院:专业:姓名:学号:指导老师:目录引言 (4)1设计任务及设计资料 (5)1.1设计任务与内容 (5)1.2设计原始资料 (5)1.2。

1城市气象资料 (5)1.2.2地质资料 (5)1.2.3设计规模 (5)1.2。

4进出水水质 (6)2、设计说明书 (6)2.1去除率的计算 (6)2。

1.1溶解性BOD的去除率 (6)5的去除率: (7)2.1.2 CODr2.1。

3.SS的去除率: (7)2。

1.4.总氮的去除率: (7)2。

1.5。

磷酸盐的去除率 (8)2.2城市污水处理工艺选择 (8)2.3、污水厂总平面图的布置 (9)2.4、处理构筑物设计流量(二级) (9)2。

5、污水处理构筑物设计 (9)2.5。

1。

中格栅和提升泵房(两者合建在一起) (9)2。

5。

2、沉沙池 (10)2.5.3、厌氧池 (11)2.5。

4、缺氧池 (11)2。

5。

5、好氧曝气池 (11)2.5.6、二沉池 (12)2.6、污泥处理构筑物的设计计算 (12)2。

6。

1污泥泵房 (12)2。

6.2污泥浓缩池 (12)2。

7、污水厂平面,高程布置 (13)2.7.1平面布置 (13)2。

7.2管线布置 (13)2。

7.3 高程布置 (14)3 污水厂设计计算书 (14)3。

1污水处理构筑物设计计算 (14)3。

1.1泵前中格栅 (14)3.1.2污水提升泵房 (16)3.1.3、泵后细格栅 (17)3.1.3、沉砂池 (18)3.1.4、厌氧池 (20)3。

1。

5、缺氧池计算 (20)3。

1.6、好氧曝气池的设计计算 (21)3.1。

8、二沉池 (28)3。

2 污泥处理部分构筑物计算 (31)3。

2。

1污泥浓缩池设计计算: (31)3.3、高程计算 (36)3.3.1污水处理部分高程计算: (36)3.3。

2高程图见CAD图 (36)3。

3。

3污水处理厂工艺流程图与总平面布置图 (36)参考文献 (37)泰安市污水处理厂A/A/O工艺设计作者:闫赛红,指导教师:孙丰霞(山东农业大学资源与环境学院)【摘要】随着社会进步,人们对于城市污水的处理的要求愈加严格。

某生活污水处理工艺流程和平面布置图

某生活污水处理工艺流程和平面布置图
水解酸化池风机房电控室接触氧化池接触氧化池调节池污泥池加药间格栅渠沉淀池管廊设备吊装口楼梯口THE ARCHITECTURAL DESIGN & RESEARCH INSTITUTE OF GUANGDONG PROVINCE院审 核电子文件名:校 对工种负责东审 定广设主持人建省筑总 负 责研计究图 别设计号图 号图纸版权属设计单位所有,未经许可,外人及外单位不得翻印复制作为其他工程之用。图 名制 图工程名称兴建单位市政工程甲级设计证书号:A144013739设 计日 期签会日 期日 期姓 名专 业给排水建 筑结 构姓 名专 业工艺机械空 调电 气风机房电控室接触氧化池调节池污泥池加药间沉淀池格栅渠接触氧化池水解酸化池THE ARCHITECTURAL DESIGN & RESEARCH INSTITUTE OF GUANGDONG PROVINCE院审 核电子文件名:校 对工种负责东审 定广设主持人建省筑总 负 责研计究图 别设计号图 号图纸版权属设计单位所有,未经许可,外人及外单位不得翻印复制作为其他工程之用。图 名制 图工程名称兴建单位市政工程甲级设计证书号:A144013739设 计日 期签会日 期日 期姓 名专 业给排水建 筑结 构姓 名专 业工艺机械空 调电 气404504040300上清液排入调节池絮凝剂加药装置助凝剂加药装置污泥池除臭风管接触氧化池污泥管药管空气管污水管图例:格栅井调节池水解酸化池混凝反应池沉淀池絮凝剂助凝剂絮凝剂助凝剂生活污水TOPBTMTOPBTMTOPBTMTOPBTMD426X8-CS-WW-BOP-4.60%%C225-UPVC-WW顶板平面布置图2012.0111-254(7-2)水施子项污水处理站W04标高-5.30m以上池内平面布置图2012.0111-254(7-2)水施子项污水处理站W05工艺流程图2012.0111-254

水污染课程设计----污水处理厂AAO工艺设计(含全套图纸)

水污染课程设计----污水处理厂AAO工艺设计(含全套图纸)

《水污染控制工程》课程设计学院:专业:XX:学号:指导老师:目录引言41设计任务及设计资料5 1.1设计任务与内容51.2设计原始资料51.2.1城市气象资料51.2.2地质资料51.2.3设计规模51.2.4进出水水质62、设计说明书6 2.1去除率的计算62.1.1溶解性BOD的去除率65的去除率:72.1.2 CODr2.1.3.SS的去除率:72.1.4.总氮的去除率:72.1.5.磷酸盐的去除率82.2城市污水处理工艺选择82.3、污水厂总平面图的布置92.4、处理构筑物设计流量(二级)92.5、污水处理构筑物设计92.5.1.中格栅和提升泵房(两者合建在一起)9 2.5.2、沉沙池102.5.3、厌氧池112.5.4、缺氧池112.5.5、好氧曝气池112.5.6、二沉池122.6、污泥处理构筑物的设计计算122.6.1污泥泵房122.6.2污泥浓缩池122.7、污水厂平面,高程布置132.7.1平面布置132.7.2管线布置132.7.3 高程布置143 污水厂设计计算书14 3.1污水处理构筑物设计计算143.1.1泵前中格栅143.1.2污水提升泵房163.1.3、泵后细格栅173.1.3、沉砂池183.1.4、厌氧池203.1.5、缺氧池计算203.1.6、好氧曝气池的设计计算213.1.8、二沉池283.2 污泥处理部分构筑物计算313.2.1污泥浓缩池设计计算:313.3、高程计算363.3.1污水处理部分高程计算:363.3.2高程图见CAD图363.3.3污水处理厂工艺流程图与总平面布置图36参考文献37XX市污水处理厂A/A/O工艺设计作者:闫赛红,指导教师:孙丰霞(XX农业大学资源与环境学院)【摘要】随着社会进步,人们对于城市污水的处理的要求愈加严格。

除了基本的去除污水中BOD和SS的要求外,通常还要求脱氮除磷,以保护水体环境。

本设计即采用了众多脱氮除磷工艺中较为经济合理的AAO工艺对进入污水厂的污水进行处理。

污水处理厂水池结构施工设计CAD平面布置图纸

污水处理厂水池结构施工设计CAD平面布置图纸
1000DAEFGA1000BDEFGBCC100020000947535094753509400350172520012002001725350200001003002000047389400350D350EFG35035044753507650350232535094753502800035082003508003509475350200002001575200160020016002001575200200157520016002001600200157520020021002002150200215020021002003504475350765035016251400162535094753502800055006000CC465035076503504650350947535028000200001003001000300060009475350947535020000550082753508503509475350350134753501347535028000100320010044005000500035017475350174753502800018000说明 :B-B剖面图A2-A2剖面图350847535084753501800010010001:102001004.7004.8001003]63005.0002[6[8@2003501:102001:10[8@2003001:102[8200[6@150[8@2002]202]123003503503005002500500250043-4.9005003501350042300127120.10088]14@200]14@200]16@200]16@200]14@200500C1-C1剖面图35017300350180001004003005005000220050022001003-4.90050035013500

污水处理站施工现场总平面布置方案

污水处理站施工现场总平面布置方案

污水处理站施工现场总平面布置方案第一节平面布置原则1、根据设计图纸及施工现场情况,结合本工程的现场特点,施工总体布置在满足施工作业和生产管理的前提下,本着少占施工占地、减少污染、保护绿地和环境,文明大方的原则,进行临时设施布置。

2、根据工程项目,施工方案和周围环境,本着“节约成本,施工必须,适当集中”的原则,进行临时设施布设。

3、尽可能地利用场内交通条件,减少对现状交通干扰及对周围环境的影响。

4、本着经济合理的原则,按照安全生产、文明施工的要求,对施工现场进行布置。

第二节平面总体布置1、现场办公平面布置现场总平面布置图1.1 项目部布置根据现场勘查,项目部设置在厂区东侧空地处,拟搭建4125㎡项目部办公区及临舍区。

项目部办公室实例图1.2 施工作业部布置项目部下设钢筋混凝土主体工程作业部、道路排水施工作业部、绿化工程作业部。

其中,泵站工程作业部设置在项目部南侧,拟搭建100㎡彩钢板房办公;道路排水施工作业部泵站工程作业部南侧,拟搭建100㎡彩钢板房办公;2、临时设施、材料加工场地平面布置2.1 材料堆放场、机械停放场及工人宿舍布置¸ù¾Ý现场勘察,临设选址处有足够的闲置用地,计划在施工区作业部附近设置一处750㎡材料堆放场、750㎡机械停放场和1000㎡钢筋模板加工场,工人宿舍设置在作业部附近,现场平均人数150人,拟搭设20间40㎡彩色钢板房以供居住。

钢筋模板加工棚实例图机械停放场实例图2.2 施工围挡布置根据施工招标文件要求,并结合施工现场条件和特点,进场后,在施工区采用标准统一硬质围挡搭设施工围挡,将市政施工区与周围环境分离,减少周边环境与施工区的交叉干扰,防止安全事故的发生。

围挡色彩标志整齐美观,围挡支撑牢固可靠,底部用铆钉铆固,在围挡外侧上设置夜间警示灯、贴反光膜。

施工中的现场围挡实例图3、临时道路布置为了方便施工人员和施工车辆来往,优化施工环境,提高工作效率,根据现场勘查,计划在工程沿线周边修建施工便道供材料及施工进出场使用;施工便道,厂区内施工便道宽7米,结构为20cm厚的8%灰土上覆20cm厚C20混凝土路面。

  1. 1、下载文档前请自行甄别文档内容的完整性,平台不提供额外的编辑、内容补充、找答案等附加服务。
  2. 2、"仅部分预览"的文档,不可在线预览部分如存在完整性等问题,可反馈申请退款(可完整预览的文档不适用该条件!)。
  3. 3、如文档侵犯您的权益,请联系客服反馈,我们会尽快为您处理(人工客服工作时间:9:00-18:30)。
相关文档
最新文档