污水处理厂设计图
年终整理污水处理厂设计图纸(共4套图纸)
东莞市某污水处理厂加药间设计图
工业园区5万吨污水处理厂设计图纸
污水处理厂毕业设计(包含CAD大图)
目录引言................................................. 错误!未定义书签。
1 设计任务及概况 (6)1.1设计任务及依据 (6)1.1.1 设计任务 (6)1.1.2 设计依据及原则 (6)1.1.3设计围 (7)1.2设计水量及水质 (7)1.2.1设计水量 (7)1.2.2设计水质 (7)1.3.3设计人口 (7)2 工艺设计方案的确定 (8)2.1方案确定的原则 (8)2.2污水处理工艺流程的确定 (8)2.2.1厂址及地形资料 (8)2.2.2气象及水文资料 (9)2.2.3可行性方案的确定 (9)2.2.4工艺流程方案的确定 (10)2.2.5污泥处理工艺流程 (12)2.3主要构筑物的选择 (12)2.3.1格栅 (12)2.3.2泵房 (13)2.3.3沉砂池 (13)2.3.4初沉池、二沉池 (14)2.3.5曝气池 (14)2.3.6接触池 (15)2.3.7计量槽 (16)2.3.8浓缩池 (16)2.3.9消化池 (16)2.3.10污泥脱水 (17)3污水处理系统工艺设计 (17)3.1格栅的计算 (17)3.1.1粗格栅 (17)3.1.2格栅的计算 (18)3.1.3选型 (21)3.2泵房 (21)3.2.1泵房的选择 (21)3.2.2泵的选择及集水池的计算 (21)3.2.3扬程估算 (22)3.3细格栅 (22)3.3.1细格栅的计算: (22)3.3.2格栅的计算 (23)3.3.3选型 (25)3.4沉砂池的计算 (26)3.4.1池体计算 (26)3.4.2沉砂室尺寸计算 (27)3.4.3排砂 (29)3.4.4出水水质 (30)3.5初沉池 (30)3.5.1池体尺寸计算 (30)3.5.2中心管计算 (33)3.5.3出水堰的计算 (34)3.5.4集配水井计算 (35)3.5.5出水水质 (35)3.5.6选型 (36)3.6曝气池 (36)3.6.1池体计算 (36)3.6.2曝气系统设计与计算 (39)3.6.3供气量 (40)3.6.4空气管道系统计算 (43)3.6.5空压机的选择 (46)3.6.6污泥回流系统 (46)3.7二沉池 (47)3.7.1池体尺寸计算 (47)3.7.2中心管计算 (50)3.7.3出水堰的计算 (51)3.7.4集配水井计算 (51)3.7.5出水水质 (53)3.7.6选型 (53)3.8接触池 (53)3.8.1接触池尺寸计算 (53)3.8.2加氯间 (54)3.9计量槽 (55)4 污泥的处理与处置 (55)4.1污泥浓缩池 (55)4.2污泥消化池 (59)4.2.1 一级消化池池体部分计算 (59)4.2.2 一级消化池池体各部分表面积计算 (61)4.2.3二级消化池 (62)4.3贮气柜 (62)4.4污泥控制室 (63)4.4.1污泥投配泵的选择 (63)4.4.2污泥循环泵 (64)4.4.3污泥控制室布局 (65)4.5脱水机房 (65)4.5.1采用带式压滤机除水 (65)4.5.2选型 (66)4.6事故干化场 (66)4.7压缩机房 (67)5 污水处理厂总体布置 (67)5.1平面布置 (67)5.1.1平面布置的一般原则 (67)5.1.2 平面布置 (67)5.2污水处理厂高程布置 (68)5.2.1高程布置原则 (68)5.2.2污水污泥处理系统高程布置 (69)总结 (70)参考文献 (72)致 ................................................... 错误!未定义书签。
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)。
污水处理厂污泥泵站工程施工图设计
青岛某污水处理厂扩建工程设计图
(完整word版)污水处理厂毕业设计(包含CAD大图)
目录引言................................ 错误!未定义书签。
1 设计任务及概况 (4)1。
1设计任务及依据 (4)1.1。
1 设计任务 (4)1.1.2 设计依据及原则 (4)1.1。
3设计范围 (4)1。
2设计水量及水质 (4)1。
2。
1设计水量 (4)1。
2.2设计水质 (4)1。
3.3设计人口 (5)2 工艺设计方案的确定 (5)2.1方案确定的原则 (5)2。
2污水处理工艺流程的确定 (6)2.2。
1厂址及地形资料 (6)2.2。
2气象及水文资料 (6)2.2.3可行性方案的确定 (6)2。
2.4工艺流程方案的确定 (7)2。
2。
5污泥处理工艺流程 (8)2.3主要构筑物的选择 (8)2.3。
1格栅 (8)2.3.2泵房 (9)2。
3.3沉砂池 (9)2.3.4初沉池、二沉池 (9)2。
3。
5曝气池 (10)2.3.6接触池 (10)2。
3.7计量槽 (11)2。
3。
8浓缩池 (11)2.3.9消化池 (11)2.3.10污泥脱水 (11)3污水处理系统工艺设计 (12)3。
1格栅的计算 (12)3.1.1粗格栅 (12)3.1。
2格栅的计算 (12)3.1。
3选型 (14)3。
2泵房 (15)3。
2.1泵房的选择 (15)3.2。
2泵的选择及集水池的计算 (15)3。
2。
3扬程估算 (15)3.3细格栅 (16)3.3。
1细格栅的计算: (16)3.3。
2格栅的计算 (16)3。
3。
3选型 (18)3。
4沉砂池的计算 (18)3.4.1池体计算 (18)3.4。
2沉砂室尺寸计算 (19)3。
4.3排砂 (21)3.4。
4出水水质 (21)3。
5初沉池 (21)3.5.1池体尺寸计算 (21)3.5。
2中心管计算 (23)3。
5.3出水堰的计算 (24)3。
5。
4集配水井计算 (25)3。
5。
5出水水质 (26)3。
5。
6选型 (26)3.6曝气池 (26)3.6.1池体计算 (26)3.6。
某10万吨污水处理厂SBR工艺设计详图
污水处理厂毕业设计(包含CAD大图)
目录引言.............................................................................. 错误!未定义书签。
1 设计任务及概况 (5)1.1设计任务及依据 (5)1.1.1 设计任务 (5)1.1.2 设计依据及原那么 (5)1.1.3设计范围 (6)1.2设计水量及水质 (6)1.2.1设计水量 (6)1.2.2设计水质 (6)1.3.3设计人口 (6)2 工艺设计方案确实定 (7)2.1方案确定的原那么 (7)2.2污水处理工艺流程确实定 (7)2.2.1厂址及地形资料 (7)2.2.2气象及水文资料 (8)2.2.3可行性方案确实定 (8)2.2.4工艺流程方案确实定 (9)2.2.5污泥处理工艺流程 (11)2.3主要构筑物的选择 (11)2.3.1格栅 (11)2.3.2泵房 (12)2.3.3沉砂池 (12)2.3.4初沉池、二沉池 (13)2.3.5曝气池 (13)2.3.6接触池 (14)2.3.7计量槽 (15)2.3.8浓缩池 (15)2.3.9消化池 (15)2.3.10污泥脱水 (16)3污水处理系统工艺设计 (16)3.1格栅的计算 (16)3.1.1粗格栅 (16)3.1.2格栅的计算 (17)3.1.3选型 (20)3.2泵房 (20)3.2.1泵房的选择 (20)3.2.2泵的选择及集水池的计算 (20)3.2.3扬程估算 (21)3.3细格栅 (21)3.3.1细格栅的计算: (21)3.3.2格栅的计算 (22)3.3.3选型 (24)3.4沉砂池的计算 (25)3.4.1池体计算 (25)3.4.2沉砂室尺寸计算 (26)3.4.3排砂 (28)3.4.4出水水质 (29)3.5初沉池 (29)3.5.1池体尺寸计算 (29)3.5.2中心管计算 (32)3.5.3出水堰的计算 (33)3.5.4集配水井计算 (34)3.5.5出水水质 (34)3.5.6选型 (35)3.6曝气池 (35)3.6.1池体计算 (35)3.6.2曝气系统设计与计算 (38)3.6.3供气量 (39)3.6.4空气管道系统计算 (42)3.6.5空压机的选择 (45)3.6.6污泥回流系统 (45)3.7二沉池 (46)3.7.1池体尺寸计算 (46)3.7.2中心管计算 (49)3.7.3出水堰的计算 (50)3.7.4集配水井计算 (50)3.7.5出水水质 (52)3.7.6选型 (52)3.8接触池 (52)3.8.1接触池尺寸计算 (52)3.8.2加氯间 (53)3.9计量槽 (54)4 污泥的处理与处置 (54)4.1污泥浓缩池 (54)4.2污泥消化池 (58)4.2.1 一级消化池池体局部计算 (58)4.2.2 一级消化池池体各局部外表积计算 (60)4.2.3二级消化池 (61)4.3贮气柜 (61)4.4污泥控制室 (62)4.4.1污泥投配泵的选择 (62)4.4.2污泥循环泵 (63)4.4.3污泥控制室布局 (64)4.5脱水机房 (64)4.5.1采用带式压滤机除水 (64)4.5.2选型 (65)4.6事故干化场 (65)4.7压缩机房 (66)5 污水处理厂总体布置 (66)5.1平面布置 (66)5.1.1平面布置的一般原那么 (66)5.1.2 平面布置 (67)5.2污水处理厂高程布置 (67)5.2.1高程布置原那么 (67)5.2.2污水污泥处理系统高程布置 (68)总结 (69)参考文献 (71)致谢.............................................................................. 错误!未定义书签。
某公司设计污水处理厂紫外线消毒池图纸
最新定讲城市污水处理厂的设计PPT课件
第六节 污水厂的高程设计
水头损失包括: (1)污水流经构筑物的水头损失:主要产生在进 口和出口和需要的跌水(多在出口处),而流经 处理构筑物本体的水头损失则较小。
(2)连接管渠的水头损失:(包括配水设备)的 水头损失。包括沿程与局部水头损失。
(3)流经计量设备的水头损失
取一条距离较长,水头损失最大的流程
1000 1000 600 0.6×1.0 0.30×0.53③ 450 0.84×1.0 0.6×0.55 0.84×0.85 600 0.6×1.0 0.35×0.53 450 0.8×1.5
0.8 0.8 0.75
管渠设计参数
水深
h
i
(m)
6
7
流速 v
(m/s)
8
0.8 0.8 0.45 0.35~0.25④ 0.38③ 0.64~0.42 0.26⑤ 0.62~0.54 0.35~0.25 0.44 0.48~0.46
水头损失 (cm)
构筑物名称
水头损失 (cm)
10~25 10~25 20~40 40~50 50~60 10~20 25~50 50~150
生物滤池(工作高度为 2m时):
1) 装有旋转式布水器 2) 装有固定喷洒布水
器 混合流或接触池
污泥干化场
270~280 450~475
10~30 200~350
结束语
谢谢大家聆听!!!
45
要注意污水与污泥高程布置的配合
如进水沟道和出水沟道之间的水位差大于整 个处理厂需要的总水头,则厂内就不需设置废水 提升泵站;反之,就必须设置泵站。
1.在高程布置前,先设计各条连接处理构筑物的 沟道
连接沟道的水力计算
污水处理厂电气设计图(全套)
只1
安装在现场控制箱(AY)上的元件
序号 符号 名 称
型号及规格
单位 数量 备 注
开/停 综合故障 手/自 运行
DO
PLC
本图适用下列设备
序号 设备编号 名 称 1 P1301 1#反冲洗水泵 2 P1302 2#反冲洗水泵 3 P1303 1#过滤提升泵 4 P1304 2#过滤提升泵 5 6 7
安装在现场控制箱(AY)上的元件
12 SB3 按钮
LA39-E11 ~220V
11 SB2 按钮
LA39-E11 ~220V
10 SB1 按钮
LA39-E11 ~220V
9 KA1.2 中间继电器 ZY4 ~220V
8 HY2 指示灯 AD16-22D/31S ~220V
只 1 黄色 报警复位
只1 只1
3 SB5 按钮
LA39-E11 ~220V
2 SB4 急停按钮 LA39-E11Z ~220V
只1 只1
白色 起动 红色 停止
1 SA 三档开关
LA39-E22YS ~220V
只 1 三档自锁 统一钥匙
安装在现场控制箱(AY)上的元件
12 SB3 按钮
LA39-E11 ~220V
11 SB2 按钮
名称
1 J903 还原剂投加设备
2 J904 3 J905
阻垢剂投加设备 1#杀菌投加设备
4 J906 2#杀菌投加设备
5
6
7 8
回路编号 J903XX J904XX J905XX J906XX
所在控制柜编号 AA4 AA4 AA4 AA4
开/停
DO
手/自 运行
DI
DI
PLC