广西某食品有限公司制糖废水处理工程设计方案 47页

制糖废水处理工程设计方案(10000m3/d)广西某食品有限公司制糖废水处理工程（10000m3/d）设计方案（初步设计）………………有限公司地址：电话：传真：邮编：………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)目录第1章　概述4第2章　设计依据及原则52.1设计依据…………………………………………………………………………………………….52.2设计原则…………………………………………………………………………………………….62.3设计范围…………………………………………………………………………………………….7第3章　生产废水水量、水质情况73.1废水排放情况………………………………………………………………………………………..73.2　进水污水水质…………………………………………………………………………………….….83.3处理后出水水质……………………………………………………………………………………..83.4各处理设施预期处理效果…………………………………………………………………………..9第4章　工艺流程说明..94.1工艺流程的选择…………………………………………………………………………………….94.2工艺流程图………………………………………………………………………………………....104.3工艺流程及工艺特点………………………………………………………………………………11第5章　工艺设计135.1预处理部分…………………………………………………………………………………………..135.2生化处理部分………………………………………………………………………………………..155.3后续处理部分……………………………………………………………………………….……….205.4污泥处理部分……………………………………………………………………………….……….215.5其他部分……………………………………………………………………………………….…….215.6主要构建筑物………………………………………………………………………………….…….225.7主要工艺设备清单…………………………………………………………………………………..23第6章　电气设计266.1设计范围…………………………………………………………………………………………..266.2供电系统…………………………………………………………………………………………266.3负荷计算…………………………………………………………………………………………..266.4动力和控制设备…………………………………………………………………………………266.5线路选择…………………………………………………………………………………………..276.6线路敷设方式……………………………………………………………………………………286.7主要电气设备清单………………………………………………………………………………29第7章　自控设计297.1概述…………………………………………………………………………………………………297.2自控系统及仪表……………………………………………………………………………………307.2.1控制系统简介……………………………………………………………………………………..307.2.2主要控制回路……………………………………………………………………………………307.3控制系统配置……………………………………………………………………………………..32………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)7.3.1硬件………………………………………………………………………………………………327.3.2软件……………………………………………………………………………………………….327.3.3系统配置…………………………………………………………………………………………327.4控制系统功能描述…………………………………………………………………………………337.5仪表…………………………………………………………………………………………………347.6电气…………………………………………………………………………………………………357.7自控设备清单………………………………………………………………………………………35第8章　工程投资概算368.1　构建筑物概算………………………………………………………………………………………368.2主要工艺设备概算…………………………………………………………………………………...378.3　主要电气设备概算…………………………………………………………………………………408.4　自控设备概算………………………………………………………………………………………418.5　工程总投资…………………………………………………………………………………………42第9章　工程经济技术指标439.1　占地面积……………………………………………………………………………………………439.2　劳动定员……………………………………………………………………………………………439.3　运行费用……………………………………………………………………………………………44附件：1、平面布置图2、工艺流程图生产废水处理工程设计方案………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)第1章　概述贵公司生产废水有锅炉冲洗水、生产废液等各种类的废水，特别是生产废液有机物含量高，其酸度大，颜色深，固形物达到10％-12％，造成生产废水总体污染物含量高而且污水产生量很大，如果直接排入自然水体中必然会造成严重的污染，并且高浓度有机废水中含有大量可利用的能源,若能加以正确利用则可以节约能源、变废为宝、降低污染、提高企业的经济效益,。为保护好环境，落实好环保措施，创建现代化环保企业，积极按照法律法规办企业，公司领导决定建设一套与生产相配套的生产废水处理设施，使出水达到或优于国家《综合污水排放标准》（GB8978-1996）中的一级标准，并采用一部分处理水的回用。广西某食品有限公司委托我公司编制生产废水处理工程设计方案，依其污水的特性、处理水质要求以及现有污水处理设施现状、业主要求，从技术先进和经济实用等方面综合考虑，选择确实可行的处理工艺，对污水处理系统进行整体规划与设计，特此编制“广西某食品有限公司制糖废水处理工程”设计方案。………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)第2章　设计依据及原则2.1设计依据1、广西某食品有限公司提供的废水水量、水质，污水处理场地等资料；2、生产废水经处理后达到或优于国家《综合污水排放标准》（GB8978-1996）之一级标准；3、设计执行规范及标准《中华人民共和国环境保护法》（1989年12月）。《中华人民共和国水污染防治法》（1984年5月）。《中华人民共和国水污染防治法实施细则》（1989年7月）。《建设项目环境保护设计规定》，城乡建设部(1987年3月)。中华人民共和国国家标准（GB8978～1996）《废水综合排放标准》。其他设计规范：GBJ14-87《室外给排水设计规范》GBJ13-88《室外给水设计规范》GBJ9-87《建筑结构荷栽规范》。GBJ3-88《砌体结构设计规范》。GBJ16-89《混凝土设计规范》。GBJ7-89《建筑地基基础设计规范》GBJ69-84《给排水工程结构设计规范》GBJ11-89《建筑抗震设计规范》GBJ16-87《建筑设计防火规范》………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)GB50052-92《供电系统设计规范》GB50057-94《建筑物防雷设计规范》GBJ54-83《低压配电装置及线路设计规范》GBJ50034-92《工业企业照明设计标准》GBJ50055-93《通用用电设备配电规范》1、《水污染防治手册》；《环境工程手册》；《水处理工程师手册》。2.2设计原则1、考虑充分利用处理设施预留场地的前提下，采用技术先进可靠、出水水质稳定、效果好的处理工艺。2、合理布置，统一规划，废水站用地控制在甲方指定的范围内。3、设备选型采用质量优良的知名品牌。关键仪器、设备选取进口产品。国产设备优先需要通过ISO9001认证企业的产品，以及国家推荐的节能产品。4、采用自动化程度较高的自控系统。5、设计充分考虑操作运行的安全措施。6、设计采用国家规范标准或地方的规范与标准，如设计中遇到需用企业标准时，则报请甲方认可。7、所有图纸、文件、仪表测量仪器及设备铭牌应采用国家标准单位，设备选型采用质量优良的知名品牌。………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)2.3设计范围设计范围为废水处理站的废水处理、污泥处理和必要的附属建筑物的工艺、土建、电气、仪表、自控、总图等专业。废水处理站外废水收集管道、供电、供水、通讯线路、沼气利用设施等设计不包含在本设计范围内，其工程费用不计入本设计的工程中。第3章　生产废水水量、水质情况3.1废水排放情况根据业主提供的资料，现在的污水排放情况如下表：表1　污水排放情况及分类　序号项目水量（m3/d）所占比例（%）1生产废水10000100234废水处理站的设计规模按10000m3/d进行设计，按每天运行20小时计算，则设计流量为500m3/h。………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)3.2　进水污水水质根据贵公司提供的水质资料和同类厂家的水质情况，我们初步确定生产废水水质指标如下：表2　进水水质指标　序号污染物名称污染物浓度（mg/L）1CODCr160002BOD564003SS20004pH4~55硫化物微量　　注：施工设计前需再进行水质检测。3.3处理后出水水质排放水出水水质：根据有关法规，排放污水水质须达到或优于国家《综合污水排放标准》（GB8978-1996）一级标准。表3　出水水质指标序号污染物名称污染物浓度（mg/L）1CODCr1002BOD5203SS704pH6~9………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)3.4各处理设施预期处理效果根据现有生产废水的水质、水量情况以及我们所将采用的处理工艺，再参照同类工程的处理效果，预测该处理工程的废水处理效果如下：表4　预期处理效果指标单位:mg/L，pH值除外指标原水调节沉淀池出水一级UASB出水二级UASB出水预曝气沉淀池出水BAF出水pH4—54—56—96—96—96—9CODCr16000120002400480408＜30去除率--25%80%80%15%＞93%BOD564004800840168143＜20去除率--25%82.5%80%15%＞85%SS2000100020020060＜10去除率--50%----70%＞85%第4章　工艺流程说明4.1工艺流程的选择由于贵公司所产生的生产废水具有浓度高、水量大的特点，需要处理至达标排放和进行一部分处理水的回用，其环保设施工程必然投资较大。为了尽量减少投资和对生产废水中蕴藏的能量加以利用，我们经过慎重考虑和仔细研究，决定采用以两级高速厌氧（UASB）---曝气生物滤池（BAF）为主线的处理工艺。既可以高效节能地处理生产废水，又能减少工艺流程环节，以保证高效、正常、平稳地实现处理目标。并且在厂区内预留了深度处理设备预留用地，以满足将来更高的水质处理要求。………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)4.2工艺流程图工艺流程框图如下：生产废水格栅槽栅渣外运集水井清液回流调节沉淀池反冲洗水回流调节沉淀池集水池加温沼气利用集泥池一级UASB污泥浓缩池二级UASB反冲洗水池脱水机房曝气沉淀池曝气沉淀池集水池鼓风机干泥外运BAF反冲洗清水池外排或回用………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)4.3工艺流程及工艺特点工艺流程说明：生产废水经过格栅槽去除粗大杂物后进入调节沉淀池调节水质、水量并进一步去除水中细小的不溶物质，同时废水在调节沉淀池停留期间进行适当的预酸化。调节沉淀池的出水在调节沉淀池集水池进行适当地加温后进入UASB反应器进行高速厌氧反应，大幅度、高效率地去除废水中的有机物，同时产生沼气以供废水的加热，多余的沼气可用于锅炉的使用，提供生产工艺过程所需要的热量。为尽可能利用废水中的能源和尽可能降低运行费用，特设置两级高速厌氧处理。UASB反应器的出水在曝气沉淀池中进行短时间曝气并沉淀去除水中带出来的污泥颗粒，以减轻后续好氧处理负荷，保证处理效果。由于厌氧出水中的有机物含量依然很高，在后续的好氧处理中采用了先进的曝气生物滤池处理工艺。曝气生物滤池无论是在占地面积、基建投资、运行管理和处理效果上都优于生物接触氧化法和SBR法，既能保证处理效果，又省去了一般好氧处理后续的沉淀或过滤工艺，大幅减少设备投资，降低运行费用，减化操作难度。工艺特点说明：1．废水调节池与沉淀池合建，加强了对废水预处理程度的灵活性；消毒接触池与清水池合建，既减少了构筑物数量，又合理地避免投加消毒剂的清水通过反冲洗进入滤池。2．两级高速厌氧处理串联运行，大幅度、高效地降低废水中有机物含量，最大限度地提高了甲烷产量；工艺类型相同，方便操作管理。………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)3．采用较先进的曝气生物滤池，充分利用了曝气生物滤池的各项优点，免去了一般好氧处理后续的处理过程。4．为方便管理和检修，曝气生物滤池结构形式采用地上式；若曝气生物滤池采用半地下式，则可以省去曝气沉淀池水泵房及相关设备。5．在调节沉淀池后部，预留有加药间用地，在对水质进行系统检测分析和工程投入运行后，根据运行情况确定是否需要平衡水中的营养物质。6．厂区内预留有一定的预用地，以供远期规划考虑。………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)第5章　工艺设计5.1预处理部分1、格栅槽1座处理水量：500m3/h进水渠断面700×500mm栅前水深0.3m，栅条选用圆钢，栅条宽度0.01m，栅条间隙0.02m，安装角度60°；栅槽有效宽度1m，栅前槽高0.5m，栅后槽总高0.54m,栅槽总长度2.4m。2、集水井1座处理水量：500m3/h有效容积500m3HRT=1h结构形式：1)地下式，钢砼结构2)结构尺寸：L×B×H=17×8×4m3、提升泵房1座1)地下式，钢砼结构2)结构尺寸：L×B×H=8×3×3m3)单池容积：V=72m3配套设备：提升泵3台（两用一备）型号：………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)流量Q=260m3/h，扬程H=m，功率N=kw液位控制器1台4、调节沉淀池2座处理水量：500m3/h调节时间：5.3h调节沉淀池池有效容积：2624m3，进水部位设反应池，当需要药剂以强化沉淀效果时内设混合反应装置，可以充分混合反应。A．反应池部分：1)地上式，钢砼结构2)单池结构尺寸：L×B×H=12×4.5×5m3)单池容积：V=270m3配套设备：pH计1台B．沉淀池部分：1)地上式，钢砼结构2)单池结构尺寸：L×B×H=36×12×5m3)单池容积：V=2160m3排泥沟高2m，上底宽4.5m，下底宽：0.5m，每座沉淀池设排泥沟8个5、调节沉淀池集水池1座处理水量：500m3/hHRT=0.8h1)地上式，钢砼结构………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)2)结构尺寸：L×B×H=24.3×4.5×4m3)容积：V=437.4m3配套设备：换热器：1套浊度仪：1台pH计：1台6、调节沉淀池水泵房1座1)地上式，钢砼结构2)结构尺寸：L×B×H=12×5×3m3)容积：V=180m3配套设备：提升泵3台(两用一备)型号：流量Q=260m3/h，扬程H=m，功率N=kw液位控制器1台5.2生化处理部分1、一级UASB反应器6座设计容积负荷：11.85kgCOD/（m3·d），中、高温运行每座UASB反应器有效容积为1350m3，有效高度为12.5m，底边长12m，宽9m。1)半地下式，钢砼结构2)单座结构尺寸：L×B×H=12×9×13m………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)3)单座容积：V=1404m3配套设备：配水渠1套水封罐6台泥位计6台pH计6台消泡装置6套布水系统6套　集水系统6套三相分离器6套排泥系统6套2、二级UASB反应器6座设计容积负荷：3.1kgCOD/（m3·d），常温运行每座UASB反应器有效容积为1026m3，有效高度为9.5m，底边长12m，宽9m。1)半地下式，钢砼结构2)单座结构尺寸：L×B×H=12×9×10m3)单座容积：V=1080m3配套设备：配水渠1套水封罐6台泥位计6台………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)pH计6台消泡装置6套布水系统6套　集水系统6套三相分离器6套排泥系统6套3、曝气沉淀池2座曝气时间1.44h，曝气强度0.2m3/m3污水。沉淀时间2.0小时，沉淀池表面负荷1.16m3/（m2·h）。曝气池尺寸为L×B×H=12×6×5m。沉淀池尺寸为L×B×H=18×12×5m，其中沉淀池排泥沟高2m，上底宽4.5m，下底宽：0.5m，每座沉淀池设排泥沟4个A．曝气池部分：1)地上式，钢砼结构2)单座结构尺寸：L×B×H=12×6×5m3)单座容积：V=360m3配套设备：曝气系统2套　　曝气形式：穿孔管曝气　　曝气面积：144m2B．沉淀池部分：1)地上式，钢砼结构2)单座结构尺寸：L×B×H=24×12×5m3)单座容积：V=1440m34、曝气沉淀池集水池1座………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)1)地上式，钢砼结构2)结构尺寸：L×B×H=12×6×4m3)容积：V=288m3配套设备：浊度仪1台5、曝气沉淀池水泵房1座1)地上式，钢砼结构2)结构尺寸：L×B×H=12×5×3m3)容积：V=180m3配套设备：提升泵3台(两用一备)型号：流量Q=260m3/h，扬程H=m，功率N=kw液位控制器1台6、BAF（曝气生物滤池）6座（含配水渠）设计容积负荷：0.92kgBOD/（m3·d）每座BAF反应器的面积为56m2，填料层高度为4.0m。1)地上式，钢砼结构2)结构尺寸：L×B×H=8×7×7m3)容积：V=392m3配套设备：配水系统6套长柄滤头12096个………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)圆形陶料1344m3单孔膜曝气器12096个布气系统6套集水系统6套压差计6套浊度仪6台栅形稳流器6套溶解氧测定仪6台6、反冲洗水池1座有效容积：473.6m31)地上式，钢砼结构2)结构尺寸：L×B×H=16×8×4m3)容积：V=512m37、反冲洗泵房1座（含吸水井）1)半地下式，钢砼结构2)结构尺寸：L×B=10×5×4m3)占地面积：A=50m2配套设备：反冲洗水泵：2台（一用一备）型号：流量Q=4200m3/h，扬程H=m，功率N=kw8、鼓风机房1座1)地上式，砖混结构………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)2)结构尺寸：L×B=10×5×4m3)占地面积：A=50m2配套设备：鼓风机2台（一用一备）型号：风量：贮气罐2只5.3后续处理部分1、清水池1座（带消毒接触部分）有效容积：592m31)地下式，钢砼结构2)结构尺寸：L×B×H=16×10×4m3)容积：640m3配套设备：液位计1台加药设备1套2、计量槽1座　地下式，砖混结构，内贴马塞克结构尺寸：L×B×H=3×0.8×1.5m配套设备：超声波液位计1台………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)5.4污泥处理部分1、集泥池1座本废水处理过程每天产泥量约为1300吨（湿重）。积泥池有效容积为：700m31)地下式，钢砼结构2)结构尺寸：L×B×H=16×12×4m3)容积：768m3配套设备：污泥泵2台（一用一备）型号：流量Q=65m3/h，扬程H=m，功率N=kw液位计：1台2、污泥浓缩池1座连续式重力浓缩池处理污泥量1400m3/d，直径20m，高5.3m1)半地下式，钢砼结构2)容积：1664m3配套设备：刮泥机1台5.5其他部分1、综合用房1座1)地上式，砖混结构2)结构尺寸：L×B=25×8m………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)3)占地面积：200m2综合用房共两层，上层为中心控制室、化验室、员工休息室，下层为机修间、仓库、消毒剂加药间等。2、污泥脱水间　1座　　1)地上式，砖混结构2)结构尺寸：L×B=15×6×5m3)面积：90m2配套设备：带式压滤机上2台型号：污泥泵2台5.6主要构建筑物序号名称规格(m)数量容积(m3)结构类型1格栅槽2.4×0.7×0.51座0.84钢砼地下2集水井17.0×8.0×4.01座544钢砼地下3提升泵房8.0×3.0×3.01座72钢砼地下4调节沉淀池a反应池部分12.0×4.5×5.02座540钢砼地上b沉淀池部分36.0×12.0×5.02座4320钢砼地上5调节沉淀池集水池24.3×4.5×4.01座4374钢砼地上6调节沉淀池水泵房12.0×5.0×3.01座180砖混地上7一级UASB12.0×9.0×13.06座8424钢砼半地下8二级UASB12.0×9.0×10.06座6480钢砼半地下9曝气沉淀池a曝气池部分12.0×6.0×5.02座720钢砼地上b沉淀池部分24.0×6.0×5.02座1440钢砼地上10曝气沉淀池集水池12.0×6.0×4.01座288钢砼地上………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)11曝气沉淀池水泵房12.0×5.0×3.01座180砖混地上12BAF（曝气生物滤池）8.0×7.0×7.06座2352钢砼地上13反冲洗水池16.0×8.0×4.01座512钢砼地上14反冲洗泵房10.0×5.0×4.01座200钢砼地上15鼓风机房10.0×5.0×4.01座200钢砼地上16清水池(带接触池)16.0×10.0×4.01座640钢砼地下17计量槽3.0×0.8×1.51座3.6钢砼地下18集泥池16.0×12.0×4.01座768钢砼地下19污泥浓缩池Ф20，H5.31座1664.2钢砼半地下20污泥脱水间15.0×6.0×5.01座450砖混地上21综合用房(两层)底面:25.0×8.01座砖混地上22小计34348.645.7主要工艺设备清单序号名称及内容数量单位品牌/产地备注一、格栅槽1格栅（宽700mm，间隙5mm）1套非标设备不锈钢二、集水井1液位计1台　三、提升泵房1提升泵3台四、调节沉淀池1浊度仪1台　2pH计2台3换热器1套五、调节沉淀池水泵房1提升泵(Q:260m3/h)3台2液位计1台六、一级UASB反应器1配水渠1套………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)2水封罐6台3泥位计6台4pH计6台5消泡装置6套6布水系统6套7集水系统6套8三相分离器6套9排泥系统6套七、二级UASB反应器1配水渠1套2水封罐6台3泥位计6台4pH计6台5消泡装置6套6布水系统6套7集水系统6套8三相分离器6套9排泥系统6套八、曝气沉淀池1布气系统2套九、曝气集水池集水池1浊度仪1台十、曝气沉淀池水泵房1提升泵3台2液位控制器1台十、BAF（曝气生物滤池）1配水系统6套2专用长柄滤头12096个3圆形陶粒（Ф4mm）1311m34单孔膜曝气器12096个………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)5布气系统6套6集水系统6套　7压差计6套8浊度仪6台9栅形稳流器6套10溶解氧测定仪6台十一、反冲洗水池1水位计1台十二、反冲洗泵房1反冲洗水泵(Q:4200m3/h)2台十三、鼓风机房1鼓风机2台2贮气罐2只十四、清水池1加药设备1套2液位计1台十五、计量槽1超声波液位计1台十六、集泥池1液位计1台2污泥泵(Q:65m3/h)2台十七、污泥浓缩池1刮泥机1台十八、综合用房1化验设备1套2检修工具、检修用仪器仪表1套3消毒设备1套十九、污泥脱水间1带式压滤机2台污泥泵2台………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)第6章　电气设计6.1设计范围本工程废水处理站低压电源开关柜前的供电部分由甲方负责，废水处理站低压电源开关柜以后的部份由工程承包方负责。6.2供电系统本工程的生产、生活用电设备供电电压均为AC380/220V，50HZ。本工程采用生产动力及照明用电混合配电，所装设的计量表仅供厂内核算用。本工程的动力及照明供配电均采用TN-S系统。在废水处理站中央控制室设置无功补偿。并做到随其负荷和电压变动及时投入或切除防止无功功率倒送，控制功率因数为0.9左右。6.3负荷计算废水处理站的动力负荷主要有水泵类、鼓风机、刮泥机、污泥脱水机、空压机等，总装机容量约为kW。计算负荷:根据废水处理实际运行情况，取需要系数为0.8，废水处理系统的计算负荷约为kW。6.4动力和控制设备在中央控制室设置电源开关柜台、动力控制柜台。为便于集中控制，于中央控制室设置琴键式操作台台，每台电气设备均可于中央控制室进行………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)“手动”和“自动”两种方式操作。为便于调试、维修，每组设备均于现场设置机旁操作箱，使操作人员能于现场就地操作。为了对设备的运行状态进行显示、监控，特于中央控制室设置工艺流程板1块。板上安装有每台设备的运行及故障指示灯，使操作人员在中央控制室内即可对现场设备的工作状态一目了然。◆电源开关柜采用PGL低压配电柜。柜上设置计量电量的三相四线电度表、测量电流的指针式电流表、测量电压的指针式电压表、刀熔开关、DZ型自动空气断路器（作热过载和短路保护）等电气元件。该开关柜共有路输出，分别控制动力控制柜、自控柜、污泥脱水机、空气压缩机以及照明等。◆动力控制柜为磁力启动电机控制柜，每台柜控制电机台。每台电机均设置了短路保护、过载保护和失压保护。◆琴键式操作台上设置手动/自动选择开关对设备的控制状态进行选择。当选择开关置于手动位置时，设备的运行受装设于琴键式操作台（或现场操作箱）上的起动、停止按钮控制；当选择开关置于自动位置时，各机电设备的运行受PLC控制。◆在每组机电设备旁设置现场操作箱，以便在现场操作及检修，在现场操作箱上设置紧急停止按钮，保障检修时的人身安全及避免损坏机电设备。6.5线路选择根据该废水处理站有甲烷气体产生，属有爆炸及有火灾危险的场所,故要求使用防爆防腐电器，不可使用普通型电器材料。………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)电缆的选择：主防爆、防火要求，和提高本工程运行的稳定性、耐久性和可靠性，故选用聚氯乙烯绝缘聚氯乙烯护套VV型电力电缆。该型号电力电缆具有抗酸碱、抗腐蚀、不延燃等优点。选取线芯截面的依据：◆按电缆穿管后载流量减少30%选择截面。◆按多根电缆并列载流量校正系数为0.8选择截面。◆按线路电压损失不超过去5%选择截面。◆按电缆埋地确定载流量。6.6线路敷设方式◆户外电缆敷设：主干线采用电缆沟敷设。由电缆沟引至水泵或机电设备的支干线采用钢管保护埋地敷设（保护钢管内径不小于电缆外径的1.5倍。电缆穿管没有弯头时,长度不超过30米；有一个弯头时,长度不超过20米；有二个弯时，长度不超过15米；有三个弯时，长度不超过8米。否则增设中间拉线盒。◆室内电缆敷设采用电缆沟、电缆桥架、电线管三种敷设方式综合使用，以求美观简洁。照明线路在户外共用动力电缆的电缆沟，引至电线杆或室内的支线采用钢管埋地敷设，室内照明采用预埋钢管暗敷或塑料线槽明敷。◆在特殊场合，如腐蚀性强的场所，电缆保护管采用PVC塑料管。………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)6.7主要电气设备清单序号名称规格型号数量备注1低压电源开关柜2000´800´1000mm冷轧板喷塑柜体2动力控制柜2000´800´400mm3琴键式操作台1150´800´600mm4现场操作箱400´385´150mm不锈钢制5空气开关1批6接触器1批7热继电器1批8按钮/指示灯1批9电容补偿柜2000´800´400mm1台冷轧板喷塑柜体第7章　自控设计7.1概述本自控系统根据废水处理的工艺过程、特点及要求而设计。自控系统设备元件采用进口(合资)产品，对工艺过程各参数进行检测和自动控制，保证废水处理车间自动连续运行。………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)7.2自控系统及仪表7.2.1控制系统简介：根据工艺要求，本装置的控制对象主要是开关量辅以pH值、液位和流量等模拟量，控制对象主要是对泵和阀门等设备的控制，因此本系统采用可编程逻辑控制器（PLC）同时完成电气和仪表部分的自动控制。采用一台工控机作人机界面实现监控，同时通过打印机打出各类报表。整个自控系统设计为三级控制，实现示意图如下：现场控制箱远控手动中央控制屏自动/手动转换开关停止由现场控制柜控制自动手动中央控制屏自控方式选择开关停止电气控制工控机控PLC制PLC自动停止仪表控制仪表自动7.2.2主要控制回路A、pH值自动控制/显示废水站内主要工艺流程的相关水池内，安装五线式（有温度补偿）pH值传感器及控制仪14套；4~20mA模拟信号送PLC，由PLC控制碱液计量泵的投加量，保证Ph值在允许值内。同时，在中控室内提供Ph的高低值声光报警………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)及动态模拟显示。B、配药槽液位的自动控制（如果实际工艺需要）投药罐液位用多点液位进行检测，4~20mA模拟信号送PLC，由PLC控制泵的启停（中位启动泵、低位停泵），以保证液位在设计值范围内；同时，对高、低液位进行声光报警，并在上位机上实现监控。C、泵及水位的联锁控制各水池和反应池的水位采用电接点液位计检测，由PLC控制相应泵的启、停。每台电机设自动/手动两种操作方式，集控操作在中央控制室统一操作，泵的联锁及备用自投均由PLC实现。D、反冲洗自动控制对曝气生物滤池反冲实现全自动控制：根据工艺要求，反冲洗系统的自动阀（36台）和反冲泵等，均由PLC按压差计反馈的水头损失及出水浊度进行自动控制，以保证出水水质和减少劳动强度。每台泵和自动阀均设自动/手动两种操作方式。同时，在中控室大型模拟流程图上实时显示各设备的运行状态和故障警报。E、物料计量对处理工艺过程中出水总量（1套）采用电磁流量计进行检测，4~20mA信号送PLC，在上位机显示流量的累积值和瞬时值。………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)7.3控制系统配置7.3.1硬件：控制系统硬件组成包括2套可编程控制器（PLC）和一台上位机构成的控制网络，上位机采用IBM兼容的工业控制机，PLC机采用性能可靠，广泛应用于工业控制领域的产品。7.3.2软件：控制软件的组成如下：PLC应用软件：运行于PLC，实现各种控制功能；监控软件：基于WindowsXP/NT平台，功能强、使用简单，应用可靠的软件作为监控软件，用于操作，监视装置的运行状态。7.3.3系统配置：为更好的明确和控制废水处理站的各项工艺流程，特设2个PLC工作站分别对特意划分的两个工艺过程进行控制和信息反馈：第一阶段工艺过程：是指从提升泵房开始，由提升泵房、调节沉淀池、调节沉淀池集水池、调节沉淀池水泵房、一级UASB、二级UASB至曝气沉淀池出水的整个过程。第二阶段工艺过程：是指从曝气生物滤池开始，由曝气生物滤池、清水池、接触消毒池、污泥处理系统及出水计量槽所包含的工艺过程。………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)自控系统配置图如下：工控机打印机2#PLC工作站1#PLC工作站现场仪表现场仪表配电柜配电柜第二阶段工艺过程第一阶段工艺过程7.4控制系统功能描述A、数据采集采集整个系统各个装置的重要工艺参数（pH值、流量、液位、温度、溶解氧等）、设备运行状态等重要数据。B、实时监控对整个工艺生产过程实现实时操作、设置、控制、显示、报警，最大限度的减少值守人员。C、联锁、报警对异常的工艺参数和设备运行状态实现声光报警，出现危险和异常状态时对设备进行联锁保护，如系统中的水位与相应的泵的联锁。D、流量的累积及清零………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)本系统对物料设有流量的瞬时显示及累积功能，并且对于每个累积流量均设有回零功能。E、报表输出提供装置运行状态的各种统计、积算报表、报表可以按班、日、月等各种需求的时间段输出，同时提供打印输出功能。F、手动控制系统可以实现手动和自动的切换，在非正常运行状态下，对每台泵设备和控制阀门进行手动控制。G、网络功能系统预留通讯接口，可通过此接口与工厂其他控制网络通讯。H、电仪控制一体化电气设备和工艺过程的控制由一个控制系统完成，提高系统的完整性和可靠性。I、动态仿真对工艺流程中各参数、设备状态、警报等，用大型模拟流程图实现动态模拟显示，动态跟踪工艺参数，直观了解设备运行状况。7.5仪表现场仪表包括水温、水位、流量、浊度、在线pH分析仪表。现场仪表的选型原则是满足工艺要求、质量可靠的进口产品。仪表规格数量见自控设备清单。………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)7.6电气电气设备控制：电动机采用自动/手动两种操作方式，集控操作在中央控制室统一操作；控制由PLC实现。泵的联锁及控制均由PLC实现。中央控制室上位机监控电气设备的运行状态、运行参数和电气设备故障报警等。所有电动机旁均设有就地操作按钮。接地：根据有关规程、规范，所有需要保护接地的仪表、电气设备均可靠性接入相应的接地系统。主要包括二次仪表、PLC装置、计算机系统等。7.7自控设备清单序号设备名称型号规格产地数量1PLC控制系统A2ASCPU-S1A1S61PNA1S38BA1S68B-S1A1SC12BA1SX41A1SY10A1S68ADA1STA32A1SJ71UC24-R4ALSG602PLC编程软件GPPW工控软件FIX7.03PLC主控柜及模拟流程图柜2200×2000×6004仪表控制柜22000×800×6005工控系统PⅢ/800/128M/20G/40X/17″6打印机HP6L7在线PH仪PC-30300~14pH0.01级4~20mA输出220VAC电源双继电器控制输出，电极长度1600mm………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)8电极液位计PS-3S0.5~4m9动态模拟屏6000×200010浮球液位计KEY11指示灯及带保险接线端子等UK5-HESI12电磁阀及汇流板PS140S-2Z13闪光报警器WP-803A-00A14显示控制仪表WP-S804-02-12-HLHLP第8章　工程投资概算8.1　构建筑物概算构建筑物概算表：序号名称规格(m)数量容积(m3)单价(元)金额(元)结构类型1格栅槽2.4×0.7×0.51座0.84450钢砼2集水井17.0×8.0×4.01座544钢砼3提升泵房8.0×3.0×3.01座72钢砼4调节沉淀池反应池部分12.0×4.5×5.02座540钢砼沉淀池部分36.0×12.0×5.02座4320钢砼5调节沉淀池集水池24.3×4.5×4.01座4374钢砼6调节沉淀池水泵房12.0×5.0×3.01座180320砖混7一级UASB12.0×9.0×13.06座8424钢砼8二级UASB12.0×9.0×10.06座6480钢砼9曝气沉淀池曝气池部分12.0×6.0×5.02座720钢砼沉淀池部分24.0×6.0×5.02座1440钢砼10曝气沉淀池集水池12.0×6.0×4.01座288钢砼11曝气沉淀池水泵房12.0×5.0×3.01座180砖混12BAF（曝气生物滤池）8.0×7.0×7.06座2352钢砼13反冲洗水池16.0×8.0×4.01座512钢砼14反冲洗泵房10.0×5.0×4.01座200钢砼15鼓风机房10.0×5.0×4.01座200钢砼………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)16清水池(带接触池)16.0×10.0×4.01座640钢砼17计量槽3.0×0.8×1.51座3.6钢砼18集泥池16.0×12.0×4.01座768钢砼19污泥浓缩池Ф20，H5.31座1664.2钢砼20污泥脱水间15.0×6.0×5.01座450砖混21综合用房(两层)底面:25.0×8.01座砖混小计343498.2主要工艺设备概算主要工艺设备概算表：序号名称及内容数量单位单价(元)金额(元)备注一、格栅槽1格栅（宽700mm，间隙5mm）1套二、集水井1液位计1台　三、提升泵房1提升泵3台四、调节沉淀池1浊度仪1台　2pH计2台3换热器1套五、调节沉淀池水泵房1提升泵(Q:260m3/h)3台2液位计1台六、一级UASB反应器1配水渠1套2水封罐6台3泥位计6台4pH计6台………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)5消泡装置6套6布水系统6套7集水系统6套8三相分离器6套9排泥系统6套七、二级UASB反应器1配水渠1套2水封罐6台3泥位计6台4pH计6台5消泡装置6套6布水系统6套7集水系统6套8三相分离器6套9排泥系统6套八、曝气沉淀池1布气系统2套九、曝气集水池集水池1浊度仪1台十、曝气沉淀池水泵房1提升泵3台2液位控制器1台十、BAF（曝气生物滤池）1配水系统6套2专用长柄滤头12096个3圆形陶粒（Ф4mm）1311m34单孔膜曝气器12096个5布气系统6套6集水系统6套　7压差计6套………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)8浊度仪6台9栅形稳流器6套10溶解氧测定仪6台十一、反冲洗水池1水位计1台十二、反冲洗泵房1反冲洗水泵(Q:4200m3/h)2台十三、鼓风机房1鼓风机2台2贮气罐2只十四、清水池1加药设备1套2液位计1台十五、计量槽1超声波液位计1台十六、集泥池1液位计1台2污泥泵(Q:65m3/h)2台十七、污泥浓缩池1刮泥机1台十八、综合用房1化验设备1套2检修工具、检修用仪器仪表1套3消毒设备1套十九、污泥脱水间1带式压滤机2台2污泥泵2台小计………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)8.3　主要电气设备概算主要电气设备概算表：序号名称规格型号数量单价（元）金额（元）备注1低压电源开关柜2000´800´1000mm冷轧板喷塑柜体2动力控制柜2000´800´400mm3琴键式操作台1150´800´600mm4现场操作箱400´385´150mm不锈钢制5空气开关1批6接触器1批7热继电器1批8按钮/指示灯1批9电容补偿柜2000´800´400mm1台冷轧板喷塑柜体小计………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)8.4　自控设备概算自控设备概算表：序号设备名称型号规格数量单价（元）金额（元）产地1PLC控制系统A2ASCPU-S1A1S61PNA1S38BA1S68B-S1A1SC12BA1SX41A1SY10A1S68ADA1STA32A1SJ71UC24-R4ALSG602PLC编程软件GPPW工控软件FIX7.03PLC主控柜及模拟流程图柜2200×2000×6004仪表控制柜22000×800×6005工控系统PⅢ/800/128M/20G/40X/17″6打印机HP6L7在线PH仪PC-30300~14pH0.01级4~20mA输出220VAC电源双继电器控制输出，电极长度1600mm8电极液位计PS-3S0.5~4m9动态模拟屏6000×200010浮球液位计KEY11指示灯及带保险接线端子等UK5-HESI12电磁阀及汇流板PS140S-2Z13闪光报警器WP-803A-00A14显示控制仪表WP-S804-02-12-HLHLP小计………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)8.5　工程总投资序号项目价格（元）备注1构建筑物概算2主要工艺设备概算3主要电气设备概算4自控设备概算5小计6设计费（5）×2%7运输费（5）×2%8安装调试费（5）×8%9合计（5）+（6）+（7）+（8）10税金（9）×6%11工程总投资（9）+（10）………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)第9章　工程经济技术指标9.1　占地面积包括厂区绿化、道路、预留用地、综合用户及工艺构建筑物，本工程总占地面积约为：11500m2。9.2　劳动定员厂长1人中控室值班人员3人曝气生物滤池值班人员3人UASB值班人员3人值班电工3人化验员1人机修工2人维修电工2人（强电1人、弱电1人）厂区清洁工1人一天三班，每个运行班4人，共19人。由于整个污水处理站自动化程度较高，劳动强度较小。操作人员经过培训后，要求懂得机械维修保养和简单的生物化学常识。………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)9.3　运行费用计算说明：废水处理运行费用主要由以下几个部分组成:①、人工费用（F1）；②、水电费用（F2）；③、药剂费用（F3）；费用计算：①人工费用（F1）：每人平均每月元人工工资：F1=月工资×人数=元/月，即元/天吨水人工费：元/m3。②水电费用（F2）：本站区中水耗主要为冲洗地面用水、配药用水。冲洗地面用水及配药用水采用工艺处理后的达标排放水，可节省费用。电耗：污水站装备总功率为kW，设备实际运行总功率约kW，工业用电每度按0.75元计，按一天运行24小时。则水电费：F2=运行总功率×24×0.75=元/天，吨水电费：元/m3。③药剂费用（F3）：药剂用量(按日处理10000吨废水计算)序号药品日用量（Kg）价格（元/kg）总价(元/天)备注1～82～0.6合计吨水药剂费：元/m3………………….有限公司　第47页共47页n制糖废水处理工程设计方案(10000m3/d)综合以上四项，废水吨水处理运行费用:F/M=元/m3。注:以上废水处理费用根据我公司实际工程经验估算得出，由于污水厂实际排水会有所差别，所以以上费用与实际费用会有所出入，实际费用可由调试运行确定。。。。。。。。。。。。有限公司年月日精品文档————————————————————————————————————————————————————————————————————————————————————————————————————————————————精品文档精品资料精品文档——————————————————————————————————————————————————————————————————————————————————————————————————————————————-———精品资料9JWKffwvG#tYM*Jg&6a*CZ7H$dq8KqqfHVZFedswSyXTy#&QA9wkxFyeQ^!djs#XuyUP2kNXpRWXmA&UE9aQ@Gn8xp$R#͑Gx^Gjqv^$UE9wEwZ#Qc@UE%&qYp@Eh5pDx2zVkum&gTXRm6X4NGpP$vSTT#&ksv*3tnGK8!z89AmYWpazadNu##KN&MuWFA5uxY7JnD6YWRrWwc^vR9CpbK!zn%Mz849Gx^Gjqv^$UE9wEwZ#Qc@UE%&qYp@Eh5pDx2zVkum&gTXRm6X4NGpP$vSTT#&ksv*3tnGK8!z89AmYWpazadNu##KN&MuWFA5ux^Gjqv^$UE9wEwZ#Qc@UE%&qYp@Eh5pDx2zVkum&gTXRm6X4NGpP$vSTT#&ksv*3tnGK8!z89AmYWpazadNu##KN&MuWFA5uxY7JnD6YWRrWwc^vR9CpbK!zn%Mz849Gx^Gjqv^$UE9wEwZ#Qc@UE%&qYp@Eh5pDx2zVkum&gTXRm6X4NGpP$vSTT#&ksv*3tnGK8!z89AmUE9aQ@Gn8xp$R#͑Gx^Gjqv^$UE9wEwZ#Qc@UE%&qYp@Eh5pDx2zVkum&gTXRm6X4NGpP$vSTT#&ksv*3tnGK8!z89AmYWpazadNu##KN&MuWFA5uxY7JnD6YWRrWwc^vR9CpbK!zn%Mz849Gx^Gjqv^$UE9wEwZ#Qc@UE%&qYp@Eh5pDx2zVkum&gTXRm6X4NGpP$vSTT#&ksv*3tnGK8!z89AmYWpazadNu##KN&MuWFA5ux^Gjqv^$UE9wEwZ#Qc@UE%&qYp@Eh5pDx2zVkum&gTXRm6X4NGpP$vSTT#&ksv*3tnGK8!z89AmYWpazadNu##KN&MuWFA5uxY7JnD6YWRrWwc^vR9CpbK!zn%Mz849Gx^Gjqv^$UE9wEwZ#Qc@UE%&qYp@Eh5pDx2zVkum&gTXRm6X4NGpP$vSTT#&ksv*3tnGK8!z8vG#tYM*Jg&6a*CZ7H$dq8KqqfHVZFedswSyXTy#&QA9wkxFyeQ^!djs#XuyUP2kNXpRWXmA&UE9aQ@Gn8xp$R#͑Gx^Gjqv^$UE9wEwZ#Qc@UE%&qYp@Eh5pDx2zVkum&gTXRm6X4NGpP$vSTT#&ksv*3tnGK8!z89AmYWpazadNu##KN&MuWFA5uxY7JnD6YWRrWwc^vR9CpbK!zn%Mz849Gx^G89AmUE9aQ@Gn8xp$R#͑Gx^Gjqv^$UE9wEwZ#Qc@UE%&qYp@Eh5pDx2zVkum&gTXRm6X4NGpP$vSTT#&ksv*3tnGK8!z89AmYWpazadNu##KN&MuWFA5uxY7JnD6YWRrWwc^vR9CpbK!zn%Mz849Gx^Gjqv^$UE9wEwZ#Qc@UE%&qYp@Eh5pDx2zVkum&gTXRm6X4NGpP$vSTT#&ksv*3tnGK8!z89AmYWpazadNu##KN&MuWFA5ux^Gjqv^$UE9wEwZ#Qc@UE%&qYp@Eh5pDx2zVkum&gTXRm6X4NGpP$vSTT#&ksv*3tnGK8!z89AmYWpazadNu##KN&MuWFA5uxY7JnD6YWRrWwc^vR9CpbK!zn%Mz849Gx^Gjqv^$UE9wEwZ#Qc@UE%&qYp@Eh5pDx2zVkum&gTXRm6X4NGpP$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