某中型城市污水处理厂全套毕业设计

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污水处理厂毕业设计(包含CAD大图)

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 (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。

15万吨天城市生活污水处理厂-AO工艺毕业设计毕业设计

15万吨天城市生活污水处理厂-AO工艺毕业设计毕业设计

第 1 章概述1.1 基本设计资料毕业设计名称某市15万吨/天城市生活污水处理厂初步设计基本资料:1.设计规模污水设计流量:3K==万天,流量变化系数: 1.2Q m15/Z2.原污水水质指标BOD=180mg/L COD=410mg/L SS=200mg/L NH3-N=30mg/L3.出水水质指标符合《城镇污水处理厂污染物排放国家二级标准》BOD=20mg/L COD=70mg/L SS=30mg/L NH3-N=15mg/L4.气象资料某地处海河流域下游,河网密布,洼淀众多。

历史上某的水量比较丰富。

海河上游支流众多,长度在10公里以上的河流达300多条,这些大小河流汇集成中游的永定河、北运河、大清河、子牙河和南运河五大河流。

这五大河流的尾闾就是海河,统称海河水系,是某市工农业生产和人民生活的水源河道。

某属于暖温半湿润大陆季风型气候,季风显著,四季分明。

春季多风沙,干旱少雨;夏季炎热,雨水集中;秋季寒暖适中,气爽宜人;冬季寒冷,干燥少雪。

除蓟县山区外,全年平均气温为摄氏11度以上。

1月份平均气温在摄氏零下4-6度,极低温值在摄氏零下20度以下,多出现于2月份。

7月份平均气温在摄氏26度上下。

某年平均降水量约为500-690毫米。

在季节分配上,夏季降水量最多,占全年总降水量的75%以上,冬季最少,仅占2%。

由于降水量年内分配不均和年际变化大,造成某在历史上经常出现春旱秋涝现象。

某的风向有明显的季节变化。

冬季多刮西北风、偏北风;夏季多东南风、南风;春秋两季多西南风,主导风向东南风。

5.厂址及场地状况某以平原为主,污水处理厂拟用场地较为平整,占地面积20公顷。

厂区地面标高10米,原污水将通过管网输送到污水厂,来水管管底标高为 5米(于地面下5米)。

1.2 设计内容、原则1.2.1 设计内容污水处理厂工艺设计流程设计说明一般包括以下内容:(1)据城市或企业的总体规划或现状与设计方案选择处理厂厂址;(2)处理厂工艺流程设计说明;(3)处理构筑物型式选型说明;(4)处理构筑物或设施的设计计算;(5)主要辅助构筑物设计计算;(6)主要设备设计计算选择;(7)污水厂总体布置(平面或竖向)及厂区道路、绿化和管线综合布置;(8)处理构筑物、主要辅助构筑物、非标设备设计图绘制;(9)编制主要设备材料表。

毕业设计---某城市污水处理厂工艺设计(含外文翻译)

毕业设计---某城市污水处理厂工艺设计(含外文翻译)

摘要本次设计的题目某城市污水处理厂工艺设计,设计流量为15万m3/d,进水水质为BOD5=200mg/L,CODc r=450mg/L,SS=370mg/L,氨氮=15。

出水水质:CODcr≤63mg/L;BOD5≤14 mg/L;SS≤30 mg/L;氨氮≤3 mg/L。

设计要求出水水质满足《中华人民共和国污水综合排放标准》(GB8978-1996)二级标准。

采用氧化钩法处理该城市污水,氧化沟处理技术70年代末就在国内开始应用,在污水处理中取得了良好的效果。

氧化沟是活性污泥法的一种改型,其曝气池呈封闭的沟渠型,污水和活性污泥的混合液在其中进行不断的循环流动,氧化沟通常在延时曝气条件下进行污水处理,这时水力停留时间长(10~40h),有机负/(kg VSS•d)]。

与其他生物处理工与艺相比,有以下一些荷低[0.05~0.15kg BOD5技术、经济方面的特点:工艺流程简单,构筑物少,运行管理方便;曝气设备和构造形式的多样化、运行灵活;处理效果稳定、出水水质好并可以实现脱氮除磷。

关键词:城市污水,氧化沟,活性污泥法AbstractThe design for the title of the city sewage treatment plant process design, design flow for the 150 ,000 m3 / d, water quality for BOD5 is200mg / L, COD cr is 450mg / L, SS is 370mg / L, Ammonia is15. Effluent quality for BOD5is less than 14mg / L, COD is less than 63mg / L, SS is less than 30 mg / L, Ammonia is less than 3mg / L. The drainage water should meet the two criteria water requirements of GB8978-1996《wastewater discharge standards》.By the oxidation ditch treatment of urban sewage,oxidation ditch technology was applied in our country about 70s, and had good effect in treating waste water. Oxidation ditch is a remodel of active mud method, its plug flow aeration assuming obturate ditch type, the mixed liquid of waste water and active mud flowing in circle. Oxidation ditch usually treats waste water in delay plug flow condition, the waterpower has long settle time (10~40h), low organic loading [0.05~0.15kg BOD5/(kg VSS•d)]. comparing with other biology treat technology, such as: simple process, little building, convenient to administering, its equipment and structure diversification, stabilization effect, and has good water quality, can pull off the nitrogen.Keywords : Urban Sewage,Oxidation ditch,Live and dirty mire method目录摘要 (I)ABSTRACT (II)目录 (1)第一章绪论 (4)1.1设计任务 (4)1.1.1设计题目 (4)1.1.2设计任务与内容 (4)1.1.3基本要求 (4)1.1.4设计计算说明书的具体要求 (5)1.2设计原始资料及处理目标 (5)1.2.1进水水质资料 (5)1.2.2气候资料 (5)1.2.3处理目标 (6)1.2.4处理效果的估算 (6)1.3处理工艺比较与选定 (6)1.3.1水质特征 (6)1.3.2目前国内外的研究现状 (7)1.3.3活性污泥法的新发展 (8)1.3.4工艺流程的确定 (9)1.3.5设计依据 (12)第二章污水处理构筑物设计计算 (14)2.1中格栅 (14)2.1.1设计说明 (14)2.1.2设计参数 (14)2.1.3设计计算 (14)2.2污水提升泵房 (17)2.2.1泵房设计计算 (17)2.3曝气沉砂池 (18)2.3.1.设计说明 (18)2.3.2池体设计计算 (18)2.4.1氧化沟的由来 (21)2.4.2氧化沟的结构 (21)2.4.3 Carrousel氧化沟处理污水的原理 (21)2.4.4设计参数 (22)2.4.5池体设计计算 (22)2.4.6曝气机设计选型 (23)2.4.7剩余污泥计算 (24)2.4.8计算校核 (25)2.5二沉池 (25)2.5.1设计说明 (25)2.5.2设计参数 (27)2.5.3池体设计计算 (27)2.6接触消毒池 (29)2.6.1设计说明 (29)2.6.2设计参数 (30)2.6.3设计计算 (30)第三章污泥处理构筑物设计计算 (33)3.1回流污泥泵房 (33)3.1.1设计说明 (33)3.1.2回流污泥泵房设计选型 (33)3.2剩余污泥泵房 (33)3.2.1设计说明 (33)3.2.2设计选型 (33)3.3污泥浓缩池 (34)3.3.1设计说明 (34)3.3.2设计参数 (34)3.3.3设计计算 (34)3.4污泥脱水间 (36)第四章污水处理厂平面与高程布置 (38)4.1平面布置 (38)4.1.1各处理单元构筑物的平面布置 (38)4.1.3辅助建筑物 (38)4.2高程布置 (38)4.2.1输送方式 (39)4.2.2污水管材料选取 (39)4.2.3设计充满度 (39)4.2.4设计流速 (39)4.2.5管径设计 (39)4.2.6最小设计坡度 (39)4.2.7污水管道的埋深深度 (40)4.3水力损失计算 (40)4.3.1水头损失计算 (40)4.3.2构筑物水力损失 (41)4.3.3总水力损失 (41)4.4高程计算 (42)4.4.1设计说明 (42)4.4.2设计计算 (42)第五章工程概预算 (43)5.1.基本建设投资 (43)5.2运行费用 (44)5.2.1运行成本估算 (44)第六章设计结论 (45)参考文献 (46)附录A 英文文献及译文 (48)附录B 设计图纸...................................... 错误!未定义书签。

某城镇污水处理厂毕业设计(DOC)

某城镇污水处理厂毕业设计(DOC)

灵宝市污水处理厂初步设计摘要水是人类的生命之源,它孕育和滋养了地球上的一切生物,并从各个方面为人类服务。

但是,水环境中的淡水资源却很少,仅占总量的2.53%,而目前能供人类直接取用的淡水资源仅占0.22%。

加之自然水源的季节变化和地区差异,以及自然水体遭到的普遍污染,致使可能直接取用的优质水量日益短缺,难以满足人们生活和工农业生产日益增长的需求,因此保护和珍惜水资源,是整个社会的共同职责。

所以说水资源是基础性自然资源、战略性经济资源,水资源安全属于资源和经济安全。

80年代以来,废水生物处理新工艺的研究、开发和应用,已在全世界范围内得到了长足的进展,并出现了许多新型的废水生物处理技术。

这些新工艺有的已在国内外实际工程中得到了良好的应用,有的已显示出其良好的应用发展前景、得到广大的研究者和工程技术人员的关注并正在得到不断深入的研究,他们的共同特点是高效、稳定、节能,并具有对污染物去除的多功能性,大多具有脱氮除磷等深度处理的良好效能,并正朝自动化控制的方向发展。

近年来,随着灵宝市经济不断发展,人口和工业产值也随之增加,生活用水和工业用水的需求也急剧扩大,如此必然引起污水量的增加,一系列水环境问题将日益突出。

如不及时对产生的污水进行治理,那么灵宝市的水环境污染将严重下去,整个市区的生活环境和生态平衡都将受到更为严重的破坏,而这一切的恢复将是十分缓慢的,要为之付出的代价也十分昂贵。

因此,必须建立一座生活污水处理厂。

污水通过治理可以缓解和减轻水环境污染,缓解水资源的供需矛盾,为灵宝市的经济文化的发展创造有利条件。

工程的兴建,一方面为人们提供优质的生活污水,提高人们的生活质量和健康水平;另一方面是工业用水水质得到保障。

本设计是针对灵宝市的实际情况而设计的。

由于灵宝市生活用水的流量较大、SS含量高、氮磷等也都需要有一定的去除。

A2/O在同时脱氮除磷去除有机物的的工艺中,该工艺流程最为简单,总水力停留时间也少于同类其他工艺,在厌氧—缺氧—好氧交替运行下,丝菌不会大量繁殖,SVI一般小于100,不会发生污泥膨胀等优点。

城市污水设计毕业设计书

城市污水设计毕业设计书
泵站内总水头损失∑h=h1+h2=0.6451+0.19=0.8351m<1.5m
(4)水泵扬程校核
H=H静+∑h+1.0=13.86+0.8351+1.0=115.6951m<17m
故选泵合适。
3.4集水池

本工程设计的集水池与泵站合建,属封闭式。

集水池内设通气管,通向地外,并将管口做成弯头或加罩,以防止雨水及杂质入内。
Q=Qmax/5=492.61/5=95.52L/s
(2)扬程H的估算
H=H静+hf+(1.5~2.0)
式中:H静——泵需要提升的静扬程;
hf——污水泵及泵站管道的水头损失,m,取1.5m;
1.5-2.0——富于水头损失。
式中:63.74——为出口位置水面标高;
52.74——集水井最低泵吸水面标高;
2.6 2.7 2.8 2.9 3.0
自选
60 6570 75 801-800.75-0.22
50*10
3500-5500
无锡通用机械厂、江西亚太给排水成套设备公司
2.6进水出水渠
城市污水通过DN1200的管道送入进水渠道,设计中取进水渠道1.19m,进水水深0.6m,出水渠道1.19m,出水水深0.6m。

集水池设有污泥斗,池底作成不小于0.01的坡度,坡向污泥斗。从平台到池底应设下的扶梯,台上应有吊泥用的梁钩滑车。

泵站集水池容积一般按不小于最大一台泵5分钟的出水量计算,有效水深取1.5—2.0米。
本次设计集水池容积按最大一台泵5分钟的出水量计算,有效水深取3.0米。
V=5×60×0.1232=36960L=36.96

(整理)污水处理厂毕业设计

(整理)污水处理厂毕业设计

第一章设计概述及设计原则第一节设计任务书一、设计题目市城区污水处理厂设计二、设计资料(一)污水处理厂建设规模与处理程度(二)自然条件1.地理位置污水处理厂位于市城区东部,大夏河的北岸,城市饮用水源地的下游。

目前市的交通运输以公路运输为主,主要过境干线有兰朗、临大、临循、临塔四条,构成市对外的县际、省际交通道路网。

城市公路交通较为便捷,己成为州对外交通的枢纽。

2.地形地貌、地质、地震情况市地域属远古冰川期大河谷一段,河谷底部约3.2〜5km地势西南高,东北低,以8%的纵坡由西南向东北倾斜。

境海拔高度在1823.8〜2222.1m之间,平均海拔1900m 左右,最大高差3983m西南有南龙山,与县插花接壤;东南以路盘山为屏障;西北以北源山坡为靠。

水系属黄河流域水系,大夏河从西南人境,依南龙山麓纵贯全境蜿蜒流过,从南龙山尾与路盘山之间人境的牛津河、袍罕乡红水沟口人境,横穿市区的红水河,均在市注入大夏河,使全市形成“三河一川” 格,西南—东北带状河谷型地貌。

市区即坐落于在大夏河下游河谷II 级阶地上。

市属第三系上新统组,按地层可分为三级阶地,I 级阶地为大夏河床,II 级阶地从木厂—关家台一带到北山根,III 级阶地是北源。

城区设在大夏岸中部的II 级阶地上。

地质构造简述如下:城区: 地形比较平坦,起伏不大,但凹坑、陡坎较多,填土现象严重;填土区下的黄土状亚粘土随阶地纵向有所不同,越靠近北源越厚,往南渐薄,至大夏河边几乎没有;再往下为稳定的卵石层。

西郊:处于二级阶地上,地面平坦,地形大致由西北向东南倾斜,地层为冲积的黄土状亚粘土和卵石层组成。

黄土状亚粘土习性较好, 但具有II 级自重湿陷性。

北源山根坡地:为坡积洪积地层,夹层较多,具有II-III 级自重湿陷性,不均匀下沉性大,山坡较陡,且整个山坡有多处冲沟,该区的卵石层不稳定,卵石间夹有土层,容易被水冲刷带走,造成下陷,因此该处不宜修建高层建筑。

东郊:大致分为三层,耕土层下为黄土状亚粘土,下为稳定性卵石层,再下为红粘土,夹有细砂和中砂层。

20000m3城市污水处理厂综合设计--优秀毕业设计

20000m3城市污水处理厂综合设计--优秀毕业设计

综合实验与设计题目20000m3/d城市污水处理厂综合设计专业: 环境工程年级:学号:姓名:指导教师:I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(COD NB)能被开环或断链,使得N、P、有机碳被同时去除,并提高对COD NB的去除效果。

它可以同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NH3--N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/OII目录摘要 (II)目录 (III)第一章设计概述························································································- 1 -1设计任务························································································- 1 - 2设计原则························································································- 1 - 3设计依据························································································- 2 - 第二章工艺流程及说明·············································································- 2 -1工艺方案分析 ················································································- 2 - 2工艺流程························································································- 3 - 3流程各结构介绍·············································································- 3 -3.1格栅··············································································································· - 3 -3.2沉砂池·········································································································· - 4 -3.3初沉池·········································································································· - 4 -3.4生物化反应池···························································································· - 4 -3.5二沉池·········································································································· - 6 -3.6浓缩池·········································································································· - 6 - 第三章构筑物设计计算·············································································- 6 -1格栅 ·······························································································- 6 -1.1设计说明 ····································································································· - 6 -1.2设计计算 ····································································································· - 7 -III2沉砂池··························································································- 10 -2.1设计说明 ··································································································· - 10 - 3初沉池··························································································- 11 -3.1设计说明 ··································································································· - 11 -3.2设计计算 ··································································································· - 11 - 4生化池··························································································- 13 -4.1设计说明 ··································································································· - 13 -4.2设计计算 ··································································································· - 13 - 5二沉池··························································································- 20 -5.1设计说明 ··································································································· - 20 -5.2设计计算 ··································································································· - 20 - 6液氯消毒······················································································- 23 -6.1设计说明 ··································································································· - 23 -6.2设计计算 ··································································································· - 23 - 7污泥浓缩池 ··················································································- 24 -7.1设计说明 ··································································································· - 24 -7.2设计计算 ··································································································· - 24 -8 污泥消化池 ··················································································- 25 -8.1设计说明 ··································································································· - 25 -8.2设计计算 ··································································································· - 26 - 9浓缩污泥提升泵房·······································································- 32 -9.1设计选型 ··································································································· - 32 -IV9.2提升泵房 ··································································································· - 32 -9.3污泥回流泵站·························································································· - 32 -10污泥脱水间 ···············································································- 33 -10.1设计说明 ··································································································· - 33 -11鼓风机房···················································································- 33 - 12恶臭处理系统············································································- 33 -12.1设计说明 ··································································································· - 33 -12.2设计计算 ··································································································· - 33 -12.3风机选型 ··································································································· - 34 - 第四章污水处理厂总体布置···································································- 35 -1总平面布置 ··················································································- 35 -1.1总平面布置原则 ····················································································· - 35 -1.2总平面布置结果 ····················································································· - 35 -2高程布置··············································································································· - 36 -2.1高程布置原则·························································································· - 36 - 第五章参考文献······················································································- 36 -V。

50000t/d的城市污水处理厂毕业设计

50000t/d的城市污水处理厂毕业设计

50000t/d的城市污水处理厂毕业设计第一章设计内容和任务1、设计题目50000t/d的城市污水处理厂设计。

2、设计目的(1)温习和巩固所学知识、原理;(2)掌握一般水处理构筑物的设计计算。

3、设计要求:(1)独立思考,独立完成;(2)完成主要处理构筑物的设计布置;(3)工艺选择、设备选型、技术参数、性能、详细说明;(4)提交的成品:设计说明书、工艺流程图、高程图、厂区平面布置图。

4、设计步骤:(1)水质、水量(发展需要、丰水期、枯水期、平水期);(2)地理位置、地质资料调查(气象、水文、气候);(3)出水要求、达到指标、污水处理后的出路;(4)工艺流程选择,包括:处理构筑物的设计、布置、选型、性能参数。

(5)评价工艺;(6)设计计算;(7)建设工程图(流程图、高程图、厂区布置图);(8)人员编制,经费概算;(9)施工说明。

5、设计任务(1)、设计进、出水水质及排放标准项目CODCr (mg/L)BOD5(mg/L)SS(mg/L)NH3-N(mg/L)TP(mg/L)进水水质≤200 ≤150 ≤200 ≤30 ≤4 出水水质≤60 ≤20 ≤20 ≤15 ≤0.1 排放标准60 20 20 15 0.1(2)、排放标准:(GB8978-1996)一级标准;(3)、接受水体:河流(标高:-2m)第二章污水处理工艺流程说明一、气象与水文资料:风向:多年主导风向为东南风;水文:降水量多年平均为每年2370mm;蒸发量多年平均为每年1800mm;地下水水位,地面下6~7m。

年平均水温:20℃二、厂区地形:污水厂选址区域海拔标高在19-21m左右,平均地面标高为20m。

平均地面坡度为0.3‰~0.5‰,地势为西北高,东南低。

厂区征地面积为东西长224m,南北长276m。

三、污水处理工艺流程说明:1、工艺方案分析:本项目污水处理的特点为:①污水以有机污染为主,BOD/COD =0.75,可生化性较好,重金属及其他难以生物降解的有毒有害污染物一般不超标;②污水中主要污染物指标BOD、COD、SS值为典型城市污水值。

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筑龙网
Key wordS:
municipal sewage;
the triple oxidation ditch;
biological treatment; removal the nitrogen and phosphir
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毕业设计任务书
题目: 氧化沟处理某市城市污水
完成期限:2005 年 3 月 26 日至 2005 年 6 月 20 日
因此,修建污水厂,对保护关川河、改善**市城区环境卫生状况及保护安定区的生 态环境,促进**市的可持续发展具有十分重要的意义,同时对处理后的尾水为下游旱川 地提供灌溉水源,可以极大地缓解**市安定区水资源的短缺
**地区于 2004 年撤地建市,该建设项目位于新划分的**市安定区。**市安定区共 有人口 47.66 万人,其中农业人口 35.16 万人,城市人口 12.5 万人,全县工农业总产 值 8.37 亿元,其中工业产值 1.63 亿元,建设项目区域是定西市委、市政府、区委、区 政府所在地,市区内交通发达,陇海铁路和 312 国道,巉柳高速公路穿境而过。
自然生态环境:*****安定区境内主要河流有祖历河水系一级支流关川河及其一级 支流东河、西河。关川河主要受季节影响,径流量主要分布在雨季的 6—9 月份。
****市安定区属于中温带干旱、半干旱气候,日照时间长、降水量少、蒸发量大。 主要植被种类有青杨、二白杨、白榆、油松、牡丹、紫丁香、党参、干草、天仙、野燕 麦、赖草、锦葵等。
地震强度
冻结深度(米)
当地建材供应情况
100KV 高压线,电价 元/度 自来水价格 (元/m3)
液氯来源
最高温度 最低温度 最高温度 最低温度

15 -5.1 34.9 19.4 574 东南风 1105.00 1100.00 1098.00
<0.5
0.5~1.5 1.5~3 >3
1
筑龙网

Abstract According to the design mission in environment engineering college of the Lanzhou Jiaotong Univesity, the calculation is carried out for the municipal sewage in-----i city. After consideration, the triple oxidation ditch is adopted in this design, the effluent is made to attain The Second Discharge Standard Of The Nation. After removing the miscellaneous in municipal sewage which is collected by tube net by the thick space grid . Then the municipal sewage is pumped to the plant . After passing the thin bar, the municipal sewage comes into the sand sinking pond to take off the large abiograin. Then entering to the triple oxidation ditch, getting rid of the nitrogen and the phosphor byactiviated sludge, at the same time BOD, COD is reduced. At last,it comes into the contact pool to antisepsis,making the effluent be up to the standard of the discharge. Collected in the triple oxidation ditch, the mud is sended to thicking tank first, then it is pressed into piece by the straining dehydrate machine and carried outside.
*****市污水主要来源为生活污水和工业废水两大类。前者是人类生活活动过程中 排出的废水,后者是人类工业生产过程中排出的废水。*****市安定区的工业废水主要 来源于食品、药品及轻工业加工等工业.其中这些定西市安定区生活废水主要来源于
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筑龙网
12.5 万城市人口的生活活动,如人们的排泄物及人们生活活动产生的废弃物,动植物残 片等。这些物质使得生活污水中含有大量的碳水化合物、蛋白质、尿素、脂肪、硫酸盐、 氯化物及氮、磷等物质,但其中以碳水化合物为主。
1. 任务要求:
(1) 污水处理厂处理方案比较
(2) 确定处理方案的初步设计
○1 污水处理构筑物设计计算
240 35 45 10 6~8 2~27 20 60 20 15 20 1 2000
0.5
地面以下三米
○2 污泥处理构筑物设计计算
○3 污水厂总平面图设计,污水流程高程系统设计
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○4 污水泵站(房)设计.(达到施工图要求) 2. 设计说明书及计算书:包括设计总说明:题目、目录、摘要、设计主导思想、工
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前言 一、设计来源
本次毕业设计的任务来源于----------------------------------------。 二、设计原始资料
**市地处陇中地带,这里干旱少雨,水资源相当缺乏,且很大一部分水资源含盐量 高,不适宜生产生活和农业灌溉。城市自来水引自距离城区 20Km 的香泉盆地水源和距 离城区 25Km 的内官盆地水源,且大量的农田灌溉,致使水源水量锐减速度快,所以节 约和再利用水源一直是很为迫切的问题。长期以来,**市城区没有污水处理的规范系统, 生活污水和生产废水未经处理,无组织地直接排入贯穿城区的东河、西河后排入关川河, 造成沿河水质污浊、空气恶臭、蚊蝇滋生,严重造成城市环境和关川河水质污染及水资 源浪费,直接威胁着城市居民生活和下游群众生产生活及农业灌溉用水。
3

污水水质
处理后要 求达到的 水质标准
排水干 管状况
三.内容及要求
SS (mg/l) NH4-N (mg/l) TN TP PH T℃ BOD5 (mg/l)≤ COD (mg/l) ≤ SS (mg/l) ≤ NH4-N (mg/l) ≤ TN≤ TP≤ 管径 D(mm) 坡度 I(%) 充满度 h/D 流速 V m/sec 管底标高
The effluent is discharged into channel after each processing structure, The environed, and it also alleviates the crisis of water.

摘要 根据兰州交通大学环境与市政工程学院下达的设计任务,对--市污水处理进行设计 计算。经综合考虑后,本设计主体处理构筑物采用三沟式氧化沟,经过处理后使污水达 到国家的二级排放标准。 通过市政管网收集的污水在通过粗格栅去除大的悬浮杂质后,由提升泵站将污水提 升到污水处理厂。在经过细格栅后,进入竖流式沉砂池将污水中较大的无机颗粒去除。 而后进入三沟式氧化沟,利用活性污泥对污水进行脱氮除磷,降低污水中的 BOD、COD。 处理后的污水进入接触池消毒,达到排放标准。对氧化沟内产生的污泥首先进入浓缩池 浓缩,在经带式压滤机压滤脱水后外运填埋。 设计中对整个处理流程的各主体构筑物如格栅、竖流式沉砂池、三沟式氧化沟、接 触池等进行了详细、系统的设计计算和说明。理论上给出了这个流程中 BOD、COD、的去 除率及脱氮除磷的效率。在泥路中,对浓缩池、脱水机进行设计计算和说明。再结合定 西市当地的地形和设计规范,对污水处理厂进行平面布置和高程计算,从而系统的确定 各处理构筑物的标高及布置。 污水经过各处理构筑物后,达标排放至农灌渠,从而缓解---市的用水危机,并改 善定西市的环境问题。 关键字:城市污水 三沟式氧化沟 生物处理 脱氮除磷
艺流程的选择等;计算书;小结等部分。内容包括泥路与水路。篇幅不少于 40 页(3.5~5.5 万字)。要求书写工整,文字简洁规范、流畅。插图按比例,可用 单线会址。并用英语书写设计(论文)摘要(约 200 字)。 3. 设计图纸:不得少于六张图(按 2 号图计算)其中至少一张图基本达到施工图深 度,处理厂总平面图用 1 号图纸绘制。CAD 绘图应符合工程制图的要求。 4. 经济效益分析 (1) 编制经济部分的目的 (2) 投资估算和经济效益分析 5. 翻译一篇和本毕业设计(论文)相关的外文参考资料(不少于 4000 字符)
The major content of this design is about the calculation and introduction of main structures such as pump station, grille, desilting basin, , contact tank, thicking tank, the triple oxidation ditch ,sludge digestion clamer, sludge impoundment in detail and systematically, which are parts of the procedure. The removal efficiency of BOD,COD,denitrification and phosphorus removal efficiency are given in theory. Level assign and vertical assign are done according to the landform of ------ city and design specification.
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