污水处理厂施工总平面布置图

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污水处理厂平面图绘制的流程和要领

污水处理厂平面图绘制的流程和要领

污水处理厂平面图绘制的流程和要领在现代社会中,随着城市化的快速发展,污水处理厂的建设和规划也变得日益重要。

污水处理是一项关系到环境保护和公共卫生的重要工作,而污水处理厂的平面图绘制则是其中一个至关重要的环节。

本文将探讨污水处理厂平面图绘制的流程和要领,希望能对相关从业人员有所启发。

一、了解设计要求和技术标准在开始绘制污水处理厂平面图之前,首先要对设计要求和技术标准进行全面的了解。

这包括对污水处理过程、设备布置、管道走向等方面的要求进行深入研究,以确保绘制的平面图符合相关规范和标准。

同时,还需要考虑到工程地形的特点和环境条件,将其融入到平面图的设计中。

二、绘制整体布局图污水处理厂的平面图绘制可以从整体布局图开始。

整体布局图是对污水处理厂各个部分的位置和相互关系进行绘制的基础,它直观地展示了污水处理厂的整体布局和结构。

在绘制整体布局图时,需要注意相邻部分的通道连接和流动方向,确保各个部分之间的衔接和协调。

三、绘制主要处理单元图主要处理单元是污水处理厂的核心部分,包括进水口、初沉池、曝气池、二沉池、厌氧池等。

在绘制主要处理单元图时,应注意每个处理单元的位置、形状和相对尺寸的准确性。

同时,还要考虑到处理单元之间的连通关系和流动方式,确保污水能够顺利地通过各个处理单元,完成相应的处理过程。

四、绘制管道布置图污水处理厂中的管道布置是非常关键的一环,它直接影响到整个处理过程的顺利进行。

在绘制管道布置图时,需要注意处理单元之间的管道连接和走向,确保管道布置的合理性和连通性。

同时,还要考虑到管道的材质、直径和施工要求,以便后期的具体实施。

五、标注设备参数和标高信息在完成污水处理厂平面图的绘制后,还需要对各个处理单元的设备参数和标高信息进行标注。

这些信息包括设备型号、尺寸、流量等方面的数据,以及各个处理单元的标高和相对高度等。

标注设备参数和标高信息可以提供给后期的设备采购和施工工程参考,以保证整个污水处理厂的建设和运行的顺利进行。

某城市的污水处理厂详细平面总布置图

某城市的污水处理厂详细平面总布置图
}管径(DN) 坡度(‰)\P管长(m) 流速(m/s) }{\L污水处理厂总平面布置图} 比例: 1:500X=0.000\PY=0.000X=50200\PY=0.000X=70200\PY=0.000X=84788\PY=31000X=114788\PY=49000X=134788\PY=31000X=164788\PY=40000X=184788\PY=31000X=2124788\PY=41000X=255268\PY=55331X=263268\PY=56931X=245268\PY=113524X=338268\PY=147424X=301268\PY=169524X=245268\PY=169524X=273268\PY=195524X=245268\PY=225524X=301268\PY=225524X=301268\PY=281524X=245268\PY=281524X=199268\PY=201524X=199268\PY=193524X=199268\PY=145524X=199268\PY=137524X=98068\PY=137524X=98068\PY=89524X=199268\PY=89524X=199268\PY=305524X=273268\PY=141524X=301268\PY=113524X=368268\PY=127424X=445000\PY=0.000X=424000\PY=0.000X=336268\PY=162124X=368368\PY=191524X=336268\PY=203524X=368368\PY=232924X=338268\PY=237924X=362268\PY=252924X=338268\PY=282976X=362268\PY=267324X=336018\PY=300524X=360018\PY=310524X

污水处理工程施工部署

污水处理工程施工部署

污水处理工程施工部署1、施工组织机构为干好本工程,我公司拟派出资深项目经理及管理人员组成项目经理部,本着艰苦奋斗,求实创新,优质高效,团结振兴”的企业精神;安全、优质、高速、低耗”的经营思想,以质量、工期、服务” 为宗旨,将现代化的管理和现代科学技术相结合,为业主提供满意的工程产品。

2、施工总平面布置根据施工场地具体情况,在布置施工总平面时尽量将本工程的生产区和生活区分开布置。

为满足工程的正常施工,现场内设置钢筋加工房、民工宿舍、食堂、现场办公室,材料工具室,水泥库房等,加强现场平衡调度工作,搞好环境卫生,文明施工。

现场临时设施均采用活动板房。

2.1、临设布置驻地建设,为了工程的有效实施和管理,在可供使用的区域内,应按工程规模大小设置和维护全部办公室、宿舍、库房和储料场,并使项目监理满意。

在工程完工后,将用作临时性通道的任何地区,恢复到用作通道之前这些地区的状况,除非得到项目监理的同意。

工程完工后,拆除其驻地设施,并将该区域恢复原态,但在竣工前双方中有协议者除外。

2.2施工用电1、支线架设①配电箱的电缆线应有套管,电线进出不混乱。

大容量电箱上进线加滴水弯。

②支线绝缘好,无老化、破损和漏电。

③支线应沿墙或电杆架空敷设,并用绝缘子固定。

④过道电线可采用硬质护套管埋地并作标记。

⑤室外支线应用橡皮线架空,接头不受拉力并符合绝缘要求。

2、现场照明①一般场所采用220V电压。

危险、潮湿场所和金属容器内的照明及手持照明灯具,应采用符合要求的安全电压。

②照明导线应用绝缘子固定。

严禁使用花线或塑料胶质线。

导线不得随地拖拉或绑在脚手架上。

③照明灯具的金属外壳必须接地或接零。

单相回路内的照明开关箱必须装设漏电保护器。

④室外照明灯具距地面不得低于3m ;室内距地面不得低于2.4m。

碘钨灯固定架设,要保证安全。

钠、铊等金属卤化物灯具的安装高度宜在5m以上。

灯线不得靠近灯具表面。

3、架空线①架空线必须设在专用电杆(水泥杆、木杆)上,严禁架设在树或脚手架上。

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)。

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

某地污水处理站及化粪池全套结构施工图

某地污水处理站及化粪池全套结构施工图
·结构 结构工程师与建材商的专业网站市场部:ivpmarket@ 技术部:ivptech@网易 NetEase编辑部:ivpinfo@土木在线==4%%13222%%13010@150200200池壁水平转角大样(1)%%13010@1502002004%%13222池壁水平转角大样(2)日 期姓 名会签专业4%%13222-5.400详底板%%13112@150%%13112@150%%13010@150-1.9002002004%%13222%%13010@150详顶板2-2%%13112@150%%13214@1501-1-5.4002004%%13222200-1.900AL1:300X400,T4%%13220200详底板%%13112@150200%%13010@150详顶板本图说明本图说明NOTES ON DRAWING24503502850250305030030045503503002503400250450030080080010650181003003003004200250400025040502504500300100080010008008008008008008008008508008008001200150080010650181003003003004200250400025040502504500300800110012001000460025030042002503400250450030025002504000250305030030011111'1'111111111'1'1'1'11210025034502504000400400400400400400500400200150150200200200200125125500200200200200200200池底板配筋图1、板厚500mm4004004

污水处理厂施工组织设计(含平面布置及网络图)

污水处理厂施工组织设计(含平面布置及网络图)

污水处理厂施工组织设计编制依据及原则一、编制依据1、招标文件、答疑及招标图纸;2、某某污水处理厂工程《工程量清单》及《招标控制价》;3、武汉中科水生环境工程有限公司设计的施工图纸;4、岩土工程勘察报告;(二)工程建设标准。

国家、省、市或行业现行的建设工程施工及验收规范、施工技术标准、程序,《建设工程施工操作规程》、《建设工程质量管理条例》、《工程建设标准强制性标准》、《工程建设标准强制性条文》、《建筑施工安全检查标准》以及有关建筑质量、安全施工等有关文件、规定、施工图纸、技术交底、地质勘察等有关技术说明和《建筑安装工程质量检验评定统一标准》、《建筑工程质量检验评定标准等》。

有关国家、行业施工技术及验收规范:《工程测量规范》 GB50026-93《建筑地基基础工程施工质量验收规范》GB 50202-2002《建筑基坑支护技术规程》JGJ 120-99《建筑地基处理技术规范》JGJ 79-2002《地下防水工程质量验收规范》GB50208-2002《混凝土结构工程施工质量验收规范》GB 50204-2002《砌体工程施工质量及验收规范》GB 50203-2002《建筑装饰装修工程质量验收规范》 GB50210-2001《建筑电气工程施工质量验收规范》GB50303-2002《钢筋焊接及验收规程》 JGJ18-2003《钢筋焊接接头试验方法标准》 JGJ/T27-2001《钢结构工程施工质量验收规范》GB50205-2001《普通混凝土配合比设计规程》 JGJ55-2000《砌筑砂浆配合比设计规程》 JGJ98-2000《建筑工程施工质量验收统一标准》 GB50300-2001《建筑施工安全检查标准》 JGJ59-99《建筑机械使用安全技术规程》 JGJ33-2001《给水排水管道工程施工及验收规范》GB50268-97《混凝土工程施工质量验收规范》GB50204-2002《建设工程文件归档整理规范》GB/T50328-2001《建设工程施工管理规范》GB/T50326-2001……(三)部分参考资料:1、《建筑工程施工手册》;2、《建设工程质量管理条例实施细则》;3、《建筑工程质量通病防冶手册》。

污水处理厂技术标 (1)

污水处理厂技术标 (1)

目录1、施工方案2、施工进度计划及保证措施3、施工总平面布置图4、工程质量的技术组织措施5、安全生产、文明施工、环境保护的措施6、劳动力安排计划7、主要材料、构件用量计划8、主要施工机械设备使用计划9、合理化建议对降低工程造价、缩短工期保证质量的实际意义和采用价值一、施工方案一)编制原则1、杨木化机浆项目好氧污水处理二期土建工程。

2、中国轻工业长沙工程有限公司提供的建筑结构图。

3、国家颁发的现行施工验收规范及评定标准。

4、GBT19000-ISO9002系列标准。

5、我公司现场踏勘情况及相关技术档案资料。

二)工程概况1、杨木化机浆项目好氧污水处理二期土建工程位于沅江纸业生产区内。

交通便利。

2、主要内容包括初沉池、曝气池、二沉池,其主要结构形式如下:3、曝气池曝气池平面尺寸65×52×,其基底标高分别为▽-4.3m。

曝气沟为钢筋砼水池,底板厚度为500mm最厚处为1200mm,外墙板厚度为500mm,内墙板厚度为450mm。

水池砼采用C30 S8防水砼,内掺8%的HA-P高效抗裂型防水剂。

后浇带处钢筋贯穿不截断,砼采用C45 S8防水砼,内掺内掺8%的HA-P高效抗裂型防水剂,需在结构砼养护45天后方能浇筑。

4、初沉池初沉池平面尺寸初沉池¢41米,其基底标高分别为▽-2.4m。

初沉沟为钢筋砼水池,底板厚度为400mm,外墙板厚度为350mm,内墙板厚度为450mm。

水池砼采用C25 S6防水砼,内掺8%的HA-P高效抗裂型防水剂。

砼采用C30 S8防水砼,内掺内掺8%的HA-P高效抗裂型防水剂,需在结构砼养护45天后方能浇筑。

5、二沉池二沉池平面尺寸¢56米,其基底标高分别为▽-2.4m。

二沉沟为钢筋砼水池,底板厚度为400mm,外墙板厚度为350mm,内墙板厚度为450mm。

水池砼采用C25 S6防水砼,内掺8%的HA-P高效抗裂型防水剂。

砼采用C30 S8防水砼,内掺内掺8%的HA-P高效抗裂型防水剂,需在结构砼养护45天后方能浇筑。

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。

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