污水处理厂平面布置图

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上海市某地区污水处理厂管线平面布置图

上海市某地区污水处理厂管线平面布置图
正门红y=497613.0000x=3502899.7740厂外管线平面布置图1:1000梅 山 西 路污水处理厂侧门集中绿地溪流幽径假山21112M1x=3502899.7740y=497780.0000上3梅山D820X10-CS-WW-535.56.301个个厂外管线平面布置图设计阶段米单位1:1000比 例图号或标准号1序号直缝卷焊钢管名称32174%%d弯头90%%d弯头材 料 明 细 表规 格D820X10碳钢材 料DN800DN800碳钢碳钢施工重量(公斤)单重536数量199.8107092.8总重备 注124.0路6.30路接自市政污水管网D1020X10-CS-WW南提升泵站2.0旗8.302.063x=3503119.7740y=497613.0000会 签 栏专 业日 期姓 名1071348541364493y=497780.0000x=3503119.7740浮渣井13N污泥回流泵站维修及仓库121011门卫污泥脱水间综合楼6798风机房配电间出水泵站A/A/O微曝氧化沟粗格栅池.提升泵站(厂外)名 称4 53二沉池接触消毒池21序号细格栅池.沉砂池构(建)筑物一览表说 明: \P1.本图是依据建设单位提供的总平面图绘制的1:1000总平面布置图。\P2.本图标高以m计,管径、尺寸以mm计。\P3.本工程采用黄海高程系统。厂区平整地面设计标高为8.50m。\P4.污水处理厂总处理规模为4万m³/d。一、二期各2万m³/d。\P5.压力管为管中心标高,重力管为管内底标高。\P6.管材:污水管采用直缝焊接钢管,焊接。\P7.所有钢管及钢零件加工后均应除锈后防腐,做法详见工艺给排水设计总说明。\P8.本图管道材料统计的是厂外泵站至厂区围墙处之间的管材,进入泵站的市政排水管不在本次工程范围内。\P9.本图统计的材料为本期改造所需的材料,包括泵房之后的改造所需材料。\P10.给

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。

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)。

污水处理界区平面布置图

污水处理界区平面布置图
100013500×44000350040004000400016200600+50.20+49.20泵 房L=3.560056005×4L=155×450.007L=822002200220016004005应反合混a48.80 斜管\P沉淀池22002400520014500到排空13500比 例平 面 布 置 图×42200到氧化塘2000批 准严 炜严国华签 名职 责电脑制图审 核校 核设 计职责日 期日期日 期1800复调池2200SOL=32H44300钽铌冶炼废水处理工程年 月 日污水处理界区设计项目Y99W03-S-04设计阶段说明:\P1.本图尺寸除标高.管长以米计外,余以毫米计.\P2.室外设计地平标高+0.00相当于绝对标高为50.00米.\P3.所有埋地钢制管道均刷冷底子油一遍.刷热沥青三\P遍,包玻璃布二遍防腐.\P4.污水处理界区设有室外消防栓.消防栓除作消防外,\P还作清洗水池等装置用.由于未提供水源方向只能施\P工时再现场处理.652001500×6L=23S62500编辑部:ivpinfo@给排水在线 网易 NetEase市场部:ivpmarket@ 技术部:iv

污水处理厂平面布置图纸

污水处理厂平面布置图纸
厕砖304.00303.90303.97303.87303.17303.63303.40303.61118302.45304.443牲牲砂扎兰屯市新兴造纸厂砖砖砖砖303.84304.16304.21304.29304.19304.09304.32304.44303.72303.09303.64303.59302.62304.49303.24304.24403.14302.58303.03303.59303.72304.04303.59303.49304.14304.74304.04303.41304.32303.14303.96303.62304.22303.72303.52303.84302.78303.05303.32303.34303.40302.82303.42303.57303.49303.74303.04303.49302.37303.17304.09303.06303.59302.32303.74303.82302.64302.49303.93303.97303.74303.99302.71304.39303.57303.76304.19303.90303.47302.77302.27303.89305.67302.21302.07306.34砖117116114112室302.95303.25303.03302.44303.69302.94303.49303.48303.32砂新 兴 四 组乱掘扎兰屯市新兴造纸厂牲牲牲砖砖砖砖砖砖温堤建拟滩漫河缆光 111道国锅炉房砖砖砖砖砖厕302.36302.05301.69301.76303.09302.91302.55302.41302.73303.18303.11303.41303.26303.36303.40302.40303.21302.82303.56303.87303.73303.72302.78303.39303.6030

某地钟式沉砂池给排水污水处理设计图

某地钟式沉砂池给排水污水处理设计图
B}城市污水处理厂设计图 名钟 式 沉 砂 池1:50AA38038038038021204660720720720720%%u钟式沉砂池平面图%%u1:50%%uA-A剖面图%%u1:5 称\P90°弯头\P蝶 阀\P蝶 阀\P放 空 管\P总排水管\P90°弯 头\P三 通\P吸 砂 管\P搅 拌 机\P污泥回流管规 格\PDN100\PDN400\PDN200\PDN200\PDN800\PDN200\PDN200*200*200\PDN100单 位\P个\P个\P个\P根\P根\P个\P个\P根\P台\P根数 量\P4×1\P1\P4×1\P4×1\P1\P2×1\P2×1\P4×1\P4×1\P1备 注%%u钟式沉砂池设备、器材一览表 本图水厂的地面标高为%%p0.00,采用的是相对标高; 本图标高的单位是:米,其他数据的单位是:毫米; 其他未尽事项按照相应规范处理。 水厂地面平坦,没有起伏;1.3.4.2.说明:工 程 名 称11336744588991110电动蝶阀DN400\PDN400个1760760720720760760720720800800150080080072072021303803802130720720编辑部:gpszx@网易给排水网易 NetEase本图纸由浩辰ICAD软件提供技术支持水行业专业门户网站==

杭州七格污水处理厂情况简介PPT课件

杭州七格污水处理厂情况简介PPT课件
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A/A/O工艺生物除磷脱氮基本原理。 主要原理为:在好养段,硝化细菌将入
流污水中的氨氮及有机氮氨化成氨氮,通 过生物硝化作用,转化为硝酸盐,在缺氧 段,反硝化细菌将内回流的硝酸盐通过生 物反硝化作用,转化成氮气,在厌氧段, 聚磷菌释放磷,并吸收低级脂肪酸等容易 降解有机物,而在好氧段,聚磷菌超量吸 收磷,并通过剩余污泥排放。
3
一、项目基本情况
4
1)、项目背 杭州市七格污水处理厂选址在钱塘江下游强潮河
口段下沙七格村,服务范围由主城区的第三污水 处理系统及临平污水系统、下沙污水系统的污水 子系统组成,采取分期建设实施,分为三期工程。 杭州七格污水处理厂设计一期处理规模为40万吨 /日,二期20万吨/日,三期60万吨/日。 杭州市七格污水处理厂是杭州市截流治污工程的 一个重要组成部分,是作为杭州市截流治污工程 的延续,对削减钱塘江污染负荷量、降低钱塘江 污染物输出总量,保护钱塘江水域有着至关重要 的作用。
二期污水处理采用倒置A/A/O活性污泥工艺。 C、杭州市七格污水处理厂一、二期设计日污水处理能力为
一期35万吨/日,二期20万吨/日,总计55万吨/日。目前 一期剩余5万吨/日项目正在实施中。 D、目前运营模式(TOT),2002年杭州天创水务有限公 司以转让-运营-移交方式取得七格污水处理厂25年特许经 营权。杭州天创水务有限公司由天津创业环保股份有限公 司和杭州市城市建设资产经营有限公司合资成立,双方出 资比7:3.
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2)、基本情况 A、一期:杭州市七格污水处理厂一期工程总投
资72043万元,于1998年2月经国家发改委批准 (计投资【1998】2629号)立项,1999年7月 开工建设,2003年8月投入运行,并于2005年1 月7日由国家环保总局环境影响评价管理司组织浙 江省环保局、杭州市环保局、杭州市建设委员会 等单位对杭州七格污水处理厂项目(一期30万吨 /日)进行了环境保护竣工验收。 一期污水处理采用A/A/O活性污泥工艺.

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

一套生活污水处理流程图及平面布置图

一套生活污水处理流程图及平面布置图
%%p0.00 说明: 6.施工过程中在基坑没回填时应做好雨季的排水措施2y2y3.本工程选用C25殆,S6,垫层为C15殆100mm4.钢筋选用HPB235,f=210N/mm;HRB335,2.标高为相对标高,以施工现场边的水泥路面标高为±0.001.本图尺寸除标高以米为单位外,其余均为毫米5.池底板附加%%C14纵横@1000构造凳筋,可布置成梅花型 说 明:3.外池壁的内,外侧均用1:2水泥防水砂浆批面20mm厚4.图中新建构筑物的位置可根据现场实际情况做调整2.标高为相对标高,以施工现场边的水泥道路标高为±0.001.本图尺寸除高程以米为单位外,其余均以毫米为单位f=300N/mm7.在每个格池里都设置铁爬梯,由顶至底,间隔200mm。8.砖墙用M7.5混合砂浆砌筑,砖砌水池转角处均做构造柱。36730430308108010010020024024024020018003000300018003000180030001800兴隆二桥2-2剖面图%%c}50的预留孔,间距为3000{\fArial|b0|i0|c0|p32%%c}50的预留孔,间距为3000{\fArial|b0|i0|c0|p32① 区}② 区}%%c}110的预留孔,间距为3000{\fArial|b0|i0|c0|p32%%c}110的预留孔,间距为3000{\fArial|b0|i0|c0|p32-}0.20-}0.90 说明: 5.施工过程中在基坑没回填时应做好雨季的排水措施。2yy3.本工程底板选用C25殆,S6,垫层为C15殆100mm。4.钢筋选用HPB235,f=210N/mm;HRB335,2.标高为相对标高,以兴隆二桥附近的+20.00标高为±0.00。1.本图尺寸除标高以米为单位外,其余均为毫米。f=300N/mm。6.湿地外墙的内,外侧均用1:2水泥防水砂浆批面20mm厚。2-}1.

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。

某污水处理厂PLC控制原理设计cad平面布置图

某污水处理厂PLC控制原理设计cad平面布置图
EM231}EM231}EM231}EM221}EM223}EM221}EM277}CPU226}6ES7 331-7KF02-0AB06ES7 322-1BL00-0AA06ES7 321-1BL00-0AA06ES7 153-1AA03-0XB06ES7 307-1EA00-0AA0米线槽15250只端子131台2200X800X600控制柜12111098KA01~KA24欧姆龙24只MY2NJ-DC24V小型继电器720QF~34QF施耐德15只小型断路器6西门子3只SM3315西门子1只SM3224西门子2只SM3213西门子1只IM1532西门子1只1功能符号备注数量单位型号规格元件名称序号材料表PS307安装导轨6ES7 390-1AF30-0AA0只2西门子西门子3只6ES7 392-1AJ00-0AA020针前连接器40针前连接器6ES7 392-1AM00-0AA0只3西门子旧底图总号签 名日 期底图总号借(通)用件登记描 校开关电源只124VT17~T2110只保险13T17-31~T17-493AT17-31~T17-49为保险端子比 例重 量数量备 注型 号 规 格日 期审 定标准化签 字更改文件名标记设 计校 对处数序号标 号名 称日 期工 艺审 核描 校借(通)用件登记底图总号日 期签 名旧底图总号 图 样 标 记PLC柜PLC模块原理图第 张2010/05共 张SITOPD-003D-004D-003比 例重 量数量备 注型 号 规 格日 期审 定标准化签 字更改文件名标记设 计校 对处数序号标 号名 称日 期工 艺审 核描 校借(通)用件登记底图总号日 期签 名旧底图总号 图 样 标 记PLC1柜一次原理接线图第 张2010/05共 张317日 期签 名借(通)用件登记CAD 制 图旧底图总号底图总号SuperWORKS绘图软件1#粗格栅}2#粗格栅}粗格栅压
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