城市污水处理厂设计
城镇污水处理厂设计方案

城镇污水处理厂设计方案引言城镇污水处理厂是为了解决城市污水处理问题而建设的重要设施。
它可以将城镇污水经过一系列的处理工艺,降低其对水体和环境的污染程度,保障人民群众的健康和生活质量。
本文档将详细介绍城镇污水处理厂的设计方案。
设计目标城镇污水处理厂的设计目标是实现对城镇污水进行高效、稳定、安全的处理,将污水中的有害物质和污染物去除或减少到符合国家排放标准的要求,并能够满足城镇的污水排放量及水质要求。
处理工艺城镇污水处理厂的处理工艺主要包括以下几个环节:1.污水进流及初级处理:–污水进入处理厂后,通过进水口进入初级处理区域。
–初级处理主要包括格栅池、沉砂池和调节池等,用来去除大颗粒杂质和沉淀悬浮物。
2.生化处理:–经过初级处理后的污水,进入生化处理系统。
–生化处理采用活性污泥法或厌氧发酵法,利用微生物对污水中的有机物进行降解和分解。
3.深度处理:–经过生化处理的污水,进入深度处理环节,以进一步降低污水中的有害物质和污染物。
–深度处理采用常见的工艺包括曝气池、沉淀池、过滤池等。
4.出水处理:–经过深度处理的污水经过最后一道工艺,以达到国家排放标准的要求。
–出水处理主要包括消毒和除臭等环节,以确保出水的安全和无臭。
设备选型城镇污水处理厂的设备选型要根据工艺流程和处理规模来确定,主要包括以下几个方面:•初级处理设备:包括格栅机、沉砂池、调节池等。
•生化处理设备:包括曝气池、好氧池、厌氧池等。
•深度处理设备:包括曝气池、沉淀池、过滤器等。
•出水处理设备:包括消毒装置、臭氧装置等。
在设备选型时,要综合考虑设备的性能、可靠性、维护成本和运行成本等因素。
操作控制城镇污水处理厂的操作控制是保证处理工艺正常运行和处理效果的关键。
主要包括以下几个方面:1.流程控制:根据处理工艺和污水水质,调整处理工艺参数,保证处理效果和稳定性。
2.设备操作:对处理设备进行日常操作、维护和保养,及时处理设备故障。
3.水质监测:对进水、出水和处理过程中的各个环节进行水质监测和分析,及时掌握处理效果。
城镇污水处理厂设计标准

城镇污水处理厂设计标准城镇污水处理厂是城市环境保护的重要设施,其设计标准直接关系到城市污水处理效果和环境质量。
在设计城镇污水处理厂时,需要严格遵循相关的设计标准,以确保污水处理设施的安全、高效运行。
本文将从设计标准的角度,对城镇污水处理厂的设计要求进行详细介绍。
首先,城镇污水处理厂的设计应符合国家相关的环保法律法规和标准。
设计人员需要了解并遵守《城镇污水处理厂污水综合排放标准》、《城镇污水处理厂污泥利用标准》等相关标准文件,确保设计方案符合国家环保要求。
其次,城镇污水处理厂的设计应充分考虑当地的污水水质和水量特点。
根据不同地区的水质情况和污水排放量,合理确定处理工艺和设备选型,保证污水处理效果达标,同时尽量减少能耗和化学品使用,降低运行成本。
另外,城镇污水处理厂的设计应考虑未来的城市发展规划。
随着城市人口和工业生产的增加,污水处理厂的处理能力需要具备一定的扩展性,以适应未来的污水处理需求。
因此,在设计阶段就需要考虑到未来的扩建和改造方案,确保污水处理厂的可持续发展。
此外,城镇污水处理厂的设计还需要考虑安全和环保要求。
在设计过程中,需要充分考虑设施的安全性和环保性,采取相应的防护措施,避免对周围环境和居民造成影响,确保污水处理过程安全可靠。
最后,城镇污水处理厂的设计还需要考虑运行管理的便利性。
在设计阶段就需要考虑到设备的维护和管理,合理布局设施,确保设备的维修和更换工作能够顺利进行,同时也需要考虑到运行管理的智能化和自动化,提高设施的运行效率。
总之,城镇污水处理厂的设计标准是保障城市环境卫生和居民健康的重要保障,设计人员在设计城镇污水处理厂时,需要充分考虑国家环保标准、当地水质特点、未来发展规划、安全环保要求和运行管理便利性等方面的要求,确保设计方案科学合理,满足城市污水处理的需要。
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

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)。
城市污水处理厂设计与建设标准

城市污水处理厂设计与建设标准城市污水处理厂设计与建设标准近年来,随着城市化的不断推进,城市污水处理厂的设计与建设变得越发重要。
它不仅需要解决城市污水处理的问题,还需要考虑环境保护、资源利用和可持续发展等方面的要求。
本文将从深度和广度两个维度,探讨城市污水处理厂设计与建设的标准,并分享我对这一主题的观点和理解。
一、基本概念和原则1.1 污水处理厂概述:城市污水处理厂是用于收集、处理和排放城市生活污水的设施。
它通过物理、化学和生物等多种方式对污水进行处理,以去除污染物和净化水质。
1.2 设计原则:城市污水处理厂的设计应遵循以下原则:1) 以保护环境为核心:减少污染物排放,确保处理后的污水质量符合相关标准。
2) 实现资源回收利用:通过适当的处理工艺,从污水中回收利用有价值的物质,如有机肥料和能源等。
3) 排泄物处理:对处理过程中产生的排泄物和副产物要进行有效的处理和处置,以降低对环境的影响。
4) 长期可持续发展:设计应考虑未来城市发展的需求,并采用灵活的工艺和装置,以满足未来的处理要求。
二、深度探讨2.1 设计参数与标准1) 处理能力:城市污水处理厂设计时需根据城市人口规模和预计污水排放量确定处理能力,以确保能够满足日常运行的需求。
2) 水质要求:根据国家和地方相关标准,确定处理后的污水质量要求,包括悬浮物、BOD、COD、氨氮、总磷等指标。
3) 占地面积:根据处理能力和工艺的选择,合理确定污水处理厂的占地面积,以确保足够的空间容纳各个处理单元和设备。
4) 设计寿命:考虑到投资回收和设备维护的需要,污水处理厂的设计寿命一般应达到20年以上。
2.2 处理工艺选择1) 生物处理:常见的处理工艺包括活性污泥法、MBBR法和生物膜法等。
选择适当的工艺要考虑处理效果、运行成本和可持续性等因素。
2) 辅助工艺:如沉淀池、滤池、消毒设施等,在生物处理之后用于进一步去除悬浮物和病原体等有害物质。
3) 先进处理技术:如反渗透、高级氧化等先进技术可用于特殊情况下的水质提升或回收利用。
5000m3城市污水处理设计计算

5000m3/d城镇污水处理厂设计计算该城镇污水厂设计进水水质各项指标如下:4设该城镇污水无毒物、各种重金属离子等。
可生化性:BOD/COD=0.4>0.3。
可生化性好,易生化处理。
设计去除BOD=200-20=180mg/L根据生化处理BOD :N :P=100:5:1则去除180mg/LBOD 则需要消耗N4mg/L 、P0.8mg/L 。
因此,根据进出水质标准,还应该去除的TN =25-4-5=16mg/L ,TP =5-0.8-0.5=3.7mg/L 。
应继续去除的TN 与TP 之比接近5,因此需同步脱氮除磷。
去除率的计算:COD 去除率=(500-60)/500=88% BOD 去除率=(200-20)/200=90% TN 去除率=(25-5)/25=80% TP 去除率=(5-0.5)/5=90% SS 去除率=(200-50)/200=75%根据上述计算,各项污染物的去除率都在90%左右,而且该工艺还需要同步脱氮除磷,因此选定厌氧—缺氧—好氧生物同步脱氮除磷工艺(A 2/O)。
工艺流程简图如下:消化液回流 污泥、浮渣加药管污泥回流1、格栅计算:由于城镇污水中较大悬浮物和较小漂浮物较多,故采用栅条间隙宽度为0.016~0.025的细格栅,取b=0.02,栅条宽度S=0.01m 。
格栅倾角α=60o C 。
污水平均设计流量为Q=0.05m 3/s ,考虑到城镇早晚用水高峰,则取最大设计流量为Q max =0.1m 3/s 。
设计栅前水深h=0.4m ,过栅流速=0.9m/s ,栅条 栅条间隙数n=bhv sin Qmax α=9.04.002.060sin 1.0⨯⨯=13.65,取n=14栅槽宽度B=S(n -1)+bn=0.01(14-1)+0.02×14=0.41m设栅前渠道超高h 1=0.3m ,通过格栅水头损失h 2=0.1m ,则栅后渠道总高度H=h+h 1+h 2=0.4+0.3+0.1=0.8m ,设栅槽长度L=1m 。
城市污水处理厂初步设计

城市污水处理厂初步设计一、设计目标二、设计方案1.设计规模根据城市的人口规模和污水排放量,初步确定处理规模为每天处理X 吨的污水。
同时,根据未来城市发展的规划,预留必要的扩容空间。
2.污水收集系统设计污水收集系统,包括污水管网、污水泵站等设施。
确保良好的收集系统能够将城市各个区域的污水集中至处理厂。
3.污水预处理设计污水初级处理系统,包括格栅、沉砂池等设施。
通过去除大颗粒物和沉淀可降解有机物,减少污水中的悬浮物和有机负荷。
4.污水生化处理设计生化处理系统,包括活性污泥法、厌氧池等设施。
通过好氧和厌氧的处理过程,将污水中的有机物进一步降解,减少有机负荷和氮磷等营养物质。
5.污泥处理设计污泥处理系统,包括污泥浓缩、脱水和焚烧等设施。
通过浓缩和脱水,将污泥的含水率降低,减少体积。
焚烧处理可以确保污泥的无害化处理。
6.排放系统设计排放系统,包括沉淀池和消毒设施。
通过沉淀池使污水中的悬浮物得到沉淀,确保排放的水质符合国家和地方的排放标准。
消毒设施会对排放水进行消毒处理,杀灭其中的病原微生物。
7.控制系统设计自动化控制系统,对整个处理过程进行自动化的监控和控制,以提高处理效率和运行稳定性。
同时,设计相应的应急措施和报警系统,确保设备运行的安全和可靠性。
三、设施布局与建筑设计根据处理流程和设备布置要求,进行设施布局和建筑设计。
确保各个设施之间的合理连接和交通,方便设备维护和操作。
四、能源利用与环保措施在设计中考虑能源利用和环保措施的合理利用。
可以利用污水处理过程产生的沼气进行能源回收和利用。
同时,设计适当的除臭和噪音防治设施,减少对周边环境的影响。
五、设备选型与施工方案根据处理规模和处理工艺要求,进行适当的设备选型,确保设备的可靠性和处理效果。
同时,制定施工方案,确保设备的按时按质完成,并确保设备的可持续运行和维护。
六、运维管理方案制定污水处理厂的运维管理方案,包括设备的维护、维修和替换计划,培训和安全管理等。
城市污水厂设计规范

城市污水厂设计规范1. 引言城市污水厂是处理和处理城市污水的重要设施。
污水厂设计的合理性和规范性对于保护环境、减少污染物排放具有重要意义。
本文档旨在提供城市污水厂设计规范,确保城市污水得到有效处理,并满足环保标准。
2. 设计原则城市污水厂设计应遵循以下原则:•可持续性:设计应考虑资源利用、能源消耗和环境影响的最小化。
•适应性:设计应具备适应不同规模和特性的污水处理需求的能力。
•安全性:设计应确保操作人员和环境的安全。
•经济性:设计应在合理的投资和运营成本范围内实现高效的污水处理。
3. 设计要求3.1 污水处理流程污水处理流程是城市污水厂设计的核心部分。
设计应该包括以下步骤:1.预处理:包括格栅、沉砂池和沉淀池等设备,以去除污水中的固体物质和沉淀物。
2.生物处理:采用活性污泥法、厌氧处理或其他生物处理方法降解有机污染物。
3.二次沉淀:通过设置二次沉淀池来分离和去除残余的悬浮物和生物污泥。
4.消毒:采用紫外线辐射或氯化等方法杀灭残余的微生物。
5.除磷处理:对需要达到排放标准的污水,可以引入磷消除工艺。
3.2 设备选择设计应根据处理规模和可行性研究选择合适的设备。
常用的设备包括:•格栅:用于去除污水中的固体物质。
•沉砂池:用于去除沉淀性固体物质。
•曝气池:用于提供生物降解有机污染物所需的氧气。
•二次沉淀池:用于分离和去除混合液中的悬浮物和污泥。
•消毒设备:用于杀灭残余的微生物。
3.3 设计参数在设计城市污水厂时,需考虑以下参数:•处理能力:根据预测的污水流量和水质要求,确定处理能力。
•停留时间:决定污水在不同处理单元中的停留时间,以确保充分的处理效果。
•有机负荷:根据污水中有机物的含量和水质要求,确定有机负荷。
•氮磷去除率:根据排放标准,确定氮磷去除率。
•消毒效果:根据排放要求,确定消毒效果。
4. 设计计算在城市污水厂设计中,需要进行一系列的设计计算,以确定合适的设备尺寸和工艺参数。
常见的设计计算包括:1.水力计算:根据设计流量和水质要求,计算污水处理单元的水力负荷。
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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 ≤排放标准60 20 20 15(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‰~‰,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=,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。
针对以上特点,以及出水要求,现有城市污水处理技术的特点,以采用生化处理最为经济。
由于将来可能要求出水回用,处理工艺尚应硝化,考虑到NH 3-N 出水浓度排放要求较低,不必完全脱氮。
根据国内外已运行的中、小型污水处理厂的调查,要达到确定的治理目标,可采用“A 2/O 活性污泥法”。
2、工艺流程第三章工艺流程设计计算设计流量:平均流量:Q a =50000t/d ≈50000m 3/d=h=s 总变化系数:K z =0.11Qa 7.2(Q a -平均流量,L/s) =11.05797.2 =∴设计流量Q max :Q max =K z ×Q a =×50000=67000m 3/d=h=s 设备设计计算一、 格栅进水格栅提升泵房沉砂池砂水分离砂初沉池厌氧池缺氧池好氧池二沉池 接触池排放 消毒剂初沉污泥泵房浓缩池贮泥池脱水间泥饼格栅是由一组平行的金属栅条或筛网制成,安装在污水渠道上、泵房集水井的进口处或污水处理厂的端部,用以截留较大的悬浮物或漂浮物。
一般情况下,分粗细两道格栅。
格栅型号:链条式机械格栅 设计参数:栅条宽度s =栅条间隙宽度d=栅前水深h = 过栅流速u=s 栅前渠道流速u b =s α=60° 格栅建筑宽度bm n d n s b 17.310602.0)1106(01.0)1(=⨯+-⨯=•+-=取b =进水渠道渐宽部分的长度(l 1):设进水渠宽b 1=其渐宽部分展开角度α=20° 栅槽与出水渠道连接处的渐窄部份长度(l 2): 通过格栅的水头损失(h 2):格栅条断面为矩形断面,故k=3,则: 栅后槽总高度(h 总): 设栅前渠道超高h 1= 栅槽总长度(L): 每日栅渣量W : 设每日栅渣量为1000m 3,取K Z = 采用机械清渣。
二、 提升泵房 1、 水泵选择3/d ,选择用4台潜污泵(3用1备)扬程/m流量/(m 3/h) 转速/(r/min)轴功率/kw叶轮直径/mm效率/%121014503002、 集水池⑴、容积 按一台泵最大流量时6min 的出流量设计,则集水池的有效容积 ⑵、面积 取有效水深m H 3=,则面积213.403121m H Q F ===⑶、泵位及安装潜水电泵直接置于集水池内,电泵检修采用移动吊架。
三、 沉砂池 沉砂池的作用是从污水中去除砂子、煤渣等比重较大的颗粒,保证后续处理构筑物的正常运行。
选型:平流式沉砂池 设计参数:设计流量s m h m Q /776.0/6.2793m ax 33==,设计水力停留时间s t 50= 水平流速s m v /25.0=1、长度:m vt l 5.125025.0=⨯==2、水流断面面积:2max 1.325.0776.0/m v Q A V === 3、池总宽度:m h A B 1.3125.0/776.0/2=== 有效水深m h 12=4、沉砂斗容积:366max 31034.186400230776.01086400m K T X Q V Z V =⨯⨯⨯⨯=•⨯••=T =2d ,X =30m 3/106m 35、每个沉砂斗的容积(V 0)设每一分格有2格沉砂斗,则 6、沉砂斗各部分尺寸:设贮砂斗底宽b 1=;斗壁与水平面的倾角60°,贮砂斗高h ’3= 7、贮砂斗容积:(V 1) 8、沉砂室高度:(h 3)设采用重力排砂,池底坡度i =6%,坡向砂斗,则m b b L h l h h 27.12/)2.065.125.12(06.00.12/)'2(06.0'06.0'23233=-⨯-⨯+=--+=+=9、池总高度:(H) 10、核算最小流速m in vs m s m v /15.0/19.0155.12579.0min >⨯⨯==(符合要求)四、 初沉池初沉池的作用室对污水仲密度大的固体悬浮物进行沉淀分离。
选型:平流式沉淀池设计参数: 1、池子总面积A ,表明负荷取)/(0.223h m m q •= 2、沉淀部分有效水深h 2m qt h 35.122=⨯==取t =3、沉淀部分有效容积V ’4、池长L5、池子总宽度B6、池子个数,宽度取b =5m7、校核长宽比432.456.21>==b L (符合要求) 8、污泥部分所需总容积V 已知进水SS 浓度0c =200mg/L初沉池效率设计50%,则出水SS 浓度100)5.01(200)5.01(0=-⨯=-⨯=c c设污泥含水率97%,两次排泥时间间隔T=2d ,污泥容重3/1m t r = 9、每格池污泥所需容积V ’ 10、污泥斗容积V 1,11、 污泥斗以上梯形部分污泥容积V 2 12、 污泥斗和梯形部分容积 13、 沉淀池总高度Hm h h h h h H 853.789.3163.05.033.0'''44321=++++=++++=取8m设计参数1、设计最大流量 Q=50000m 3/d2、设计进水水质 COD=200mg/L ;BOD 5(S 0)=150mg/L ;SS=200mg/L ;NH 3-N=30mg/L ;TP=4mg/L3、设计出水水质 COD=60mg/L ;BOD 5(S e )=20mg/L ;SS=20mg/L ;NH 3-N=15mg/L ;TP=L4、设计计算,采用A 2/O 生物除磷工艺 ⑴、BOD 5污泥负荷N=(kgMLSS ·d) ⑵、回流污泥浓度X R =6600mg/L ⑶、污泥回流比R=100%⑷、混合液悬浮固体浓度330066001111=⨯+=+=R X R R X⑸、反应池容积V⑹、反应池总水力停留时间 ⑺、各段水力停留时间和容积 厌氧:缺氧:好氧=1:1:3厌氧池水力停留时间h t 678.139.82.0=厌⨯=,池容35.34965.174822.0m V =厌⨯=; 缺氧池水力停留时间h t 678.139.82.0=缺⨯=,池容35.34965.174822.0m V =缺⨯=; 好氧池水力停留时间h t 03.539.86.0=好⨯=,池容35.104895.174826.0m V =好⨯= ⑻、厌氧段总磷负荷d kgMLSS kgTN XV TP Q •⨯⨯=•=/017.05.349633004500000=厌 ⑼、反应池主要尺寸 反应池总容积35.17482m V =设反应池2组,单组池容33.87412/5.174822/m V V ===单 有效水深m h 0.4= 单组有效面积23.21854.03.8741h V m S ===单单采用5廊道式推流式反应池,廊道宽m b 5.7= 单组反应池长度m B S L 3.585.753.2185=⨯==单 校核:9.10.4/5.7/==h b (满足2~1/=h b ) 8.75.7/3.58/==b L (满足105/~=b L ) 取超高为,则反应池总高m H 0.50.10.4==+ ⑽、反应池进、出水系统计算 ① 进水管单组反应池进水管设计流量s m Q Q /290.0864002/500002/31=⨯== 管道流速s m v /8.0=管道过水断面面积2132.09.0/290.0/m V Q A === 管径m Ad 64.032.044=ππ⨯==取出水管管径DN700mm校核管道流速s m A Q v /75.0385.0290.0)27.0(290.02====π② 回流污泥渠道。
单组反应池回流污泥渠道设计流量Q R 渠道流速s m v /7.0=取回流污泥管管径DN700mm ③ 进水井反应池进水孔尺寸:进水孔过流量s m Q R Q /579.086400250000)11(2)1(32=⨯⨯+=⨯+=孔口流速s m v /6.0=孔口过水断面积297.06.0579.0m v Q A ===孔口尺寸取m m 9.02.1⨯φ进水竖井平面尺寸m m 5.25.2⨯④ 出水堰及出水竖井。
按矩形堰流量公式: 式中 m b 5.7=——堰宽, H ——堰上水头高,m 出水孔过流量s m Q Q /158.1334== 孔口流速s m v /6.0=孔口过水断面积293.16.0158.1m v Q A ===孔口尺寸取m m 0.10.2⨯φ进水竖井平面尺寸m m 0.25.2⨯⑤ 出水管。
单组反应池出水管设计流量 管道流速s m v /8.0= 管道过水断面积2572.08.0579.0m v Q A ===管径m Ad 92.014.372.044=⨯==π取出水管管径DN900mm 校核管道流速s m AQ v /9.0)29.0(579.025===π ⑾、曝气系统设计计算 ① 设计需氧量AOR 。