某药业废水处理工程项目可研报告 80页

Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF目录1.概述11.1项目概况11.1.1项目名称11.1.2项目建设单位11.1.3建设地点11.1.4编制单位11.2可行性研究报告编制依据、原则及范围11.2.1编制依据11.2.2编制原则31.2.3编制范围41.3项目建设条件41.3.1地理位置41.3.2地质、地貌41.3.3气象、气候41.3.4水源、供排水、排涝和防洪情况51.3.5电源、供电情况51.3.6供热情况51.4主要技术经济指标61.5公司概况61.5.1公司自然状况61.5.2公司主要产品及生产规模71.5.3生产技术装备7Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahFnSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF1.6.1我国水污染和污水处理现状的严峻现实71.6.2本项目建设的必要性81.7工程建设的可行性92.项目建设内容及规模102.1项目建设内容102.1.1废水处理站103.技术方案确定113.1废水处理站设计处理水量及废水水质确定113.1.1设计水量113.1.2设计水质113.2废水处理工艺的确定123.2.1工艺流程确定的原则123.2.2污水中污染物去除技术研究及比较133.2.3废水处理工艺163.2.4去除效率预测183.3污泥处理系统综述183.4臭气处理系统综述183.5在线检测及系统控制综述193.6废水综合处理厂厂址选择204.工程设计214.1厂区平面设计214.1.1平面布置的原则214.1.2占地面积21Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahFnSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF4.1.3平面位置214.2单元设计214.2.1格栅井224.2.2调节池224.2.3事故池234.2.4加药系统244.2.5组合气浮254.2.6投配池264.2.7一级UASB池264.2.8二级UASB池274.2.9厌氧沉淀池274.2.10一级接触氧化池274.2.11二级接触氧化池284.2.12二沉池294.2.13混凝沉淀池294.2.14中间水池294.3.15砂滤罐304.2.16清水池304.2.17污泥储池314.2.18污泥浓缩池314.2.19臭气处理单元设备324.2.20综合设备间324.2.21风机房344.2.22休息、控制、化验室34Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahFnSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF4.3水质检测与化验344.4建筑设计及结构设计344.4.1设计依据344.4.2建筑设计354.4.3结构设计354.5电气设计374.5.1设计标准374.5.2设计范围384.5.3设计方案384.6采暖通风与空气调节394.6.1设计依据394.6.2主要内容394.6.3采暖设计404.6.4通风404.7给排水设计404.8主要设备及建（构）筑物414.8.1废水处理主要设备及材料表414.8.2主要建构筑物表435.管理机构、人员编制445.1管理机构445.2人员编制446.专项设计456.1节能专篇45Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahFnSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF6.2环保专篇456.2.1设计依据和采用标准456.2.2建设地区环境现状466.2.3主要污染源466.2.4控制污染的对策466.2.5结论476.3消防专篇476.3.1设计依据和基础476.3.2工程概述476.3.3总图布置476.3.4建筑结构476.3.5消防给水486.3.6电气486.3.7采暖与通风486.3.8工艺486.3.9结论486.4劳动安全卫生专篇486.4.1设计依据和标准486.4.2生产中不安全因素和职业危害分析496.4.3劳动保护和安全措施496.5抗震设防507.项目招标518.工期安排52Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahFnSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF8.1工程安排528.2工程项目实施计划表529.投资估算及资金筹措549.1编制说明及依据549.2资金筹措549.3废水处理工程投资估算表5410.生产成本及费用估算5510.1计费标准5510.2生产成本估算5511.经济评价5711.1工程概况5711.2资金来源5711.3工程实施进度及投资分年使用计划5711.4流动资金来源及使用计划5711.5销售收入及税金5711.6利润总额5811.7评价指标计算5811.8盈亏平衡分析5911.9敏感性分析5911.10结论6112.工程效益6312.1环境效益预测6312.2社会经济效益预测63Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahFnSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF13.结论和建议6413.1结论6413.2建议6413.2.1建立用水制度，保证正常运行6413.2.2水质监测6413.2.3调试与试运行64Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahFnSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF1.概述1.1项目概况1.1.1项目名称HHH多多药业有限责任公司废水治理工程1.1.2项目建设单位①建设单位：HHH多多药业有限责任公司②企业性质：有限责任公司1.1.3建设地点HHH省SSS市安庆街289号1.1.4编制单位JJJ环保发展有限公司1.2可行性研究报告编制依据、原则及范围1.2.1编制依据1）设计委托书2）HHH多多药业有限责任公司提供的废水水质、水量数据、厂区平面图3）HHH多多药业有限责任公司排水管网现状图、厂区地形图、厂区总体规划图纸4）当地环保部门关于污水排放的相关规定5）国务院关于加强城市供水节水和水污染防治工作的通知(国发[2000]36号)73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF1）国家现行的有关的规范、标准《污水综合排放标准》GB8978-1996《室外给水设计规范》GBJ13-86（1997年版）《污水排入城市下水道水质标准》CJ3082-1999《工业循环水冷却设计规范》GBJ102-87《城市污水回用设计规范》CECS61-1994《地面水环境质量标准》GB3838－2002《氧气曝气系统设计规程》CECS114：2000《给水排水工程结构设计规范》GB50069-2002《建筑地基基础设计规范》GB50007-2002《建筑抗震设计规范》GB50011-2001《建筑结构可靠性设计统一标准》GB50068-2001《采暖通风和空气调节设计规范》GB50019-2004《供配电系统设计规范》GB50052-95《低压配电设计规范》GB50054-95《民用建筑照明设计标准》GBJ133-90《民用建筑节能设计标准》JGJ26-95《工业与民用电力装置的接地设计规范》GBJ65-83《工业企业照明设计标准》GB50034-92《工业企业厂界噪声标准》GB12348-90《城市区域环境噪声标准》GB3096-93《混凝土结构设计规范》GB50010-2002《砌体结构设计规范》GB50003-2001《建筑结构荷载规范》GB50009-200173nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF1.2.2编制原则1）真贯彻“全面规划、合理布局、综合利用、化害为利、保护环境、造福民”的基本方针。从全局出发，根据工程规模、经济效益、环境效益和社会效益，通过全面论证，做到确能保护环境、技术先进、经济合理、安全适用；2）走可持续发展的道路，坚持清洁生产和总量控制的原则；3）采用工艺先进、稳定可靠、管理方便的污水处理技术，以节约投资，降低运行费用；4）设计必须符合适用的要求，选择的处理工艺、构筑物（建筑物）形式、主要设备、设计标准和设计参数等，最大限度地满足使用的需要，以保证废水处理厂功能的实现；5）设计所选用的原始数据必须可靠、准确，并保证必要的安全系数。同时对于新技术、新结构和新材料的采用必须积极，但需慎重；6）设计中一方面尽可能采用合理工艺降低工程造价，选用质优价廉的设备；另一方面又必须保证在工程建成投入使用后，运行费用最低，取得最大的经济效益和使用效果；7）设计中必须根据生产的需要和允许条件，在经济合理的原则下，尽可能采用先进技术。在机械化、自动化与仪表化程度方面，要从实际出发，根据需要和可能及设备的供应情况，妥善确定；8）废水处理厂注意绿化。使美化的方式应和整个企业的环境相协调；9）认真贯彻执行国家和地方有关部门制定的现行有关标准、规范和规定。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF1.2.3编制范围本报告为HHH多多药业有限责任公司废水治理工程的可行性研究报告，包括基础资料、建设规模和处理程度的确定、推荐选用的最佳方案和工程技术论证等。厂外配套工程，供电、电信、道路等不在本报告编制范围内。1.3项目建设条件1.3.1地理位置HHH多多药业有限责任公司厂区地理位置为东经130°24′11″，北纬46°52″，距市中心4公里，东邻东SSS火车站，西接农场总局佳南农场，南邻HHH省农垦科学院，北接HHH三江食品公司。铁路、公路交通十分便利。1.3.2地质、地貌厂区地质条件较好，属新生代第四纪沉积层，表层为杂填土，层度0.1—0.65米；表层下为粘土层，层厚0.6—2.6米，承载力标准值fk=190kpa；粘土层下为细砂与粉质粘土互层，层厚2.7—4.8米，承载力标准值fk=125kpa；再下为粉质粘土层（以下层未揭穿），承载力标准值fk=150kpa。地势平坦，地质结构良好。本工程项目拟建场地在多多药业有限责任公司厂区内，不需要新征土地。1.3.3气象、气候年平均温度：3.1℃年最高气温:35.4℃年最低气温:-39.5℃年平均相对温度:67%年平均日照:2520小时73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF最大风速:24.3米/秒主导风向：西南风年平均降雨量：475毫米历史最大秋雪深度：48厘米最大冻土深度：2.2米地震震级裂度：5.9级静水位距自然地面：13米（公司厂区）1.3.4水源、供排水、排涝和防洪情况多多药业有限责任公司有自备水源井7口，每小时供水量可达150吨左右，公司总供水能力能够满足该建设项目需要，因此，不需要另打深井。公司排水为生产、生活废水和雨水。生产废水汇入污水处理站。上、下水管网与市政工程相连，下水管线能够满足排水、排涝和防洪情况的需要。1.3.5电源、供电情况变压容器为2880kvA，由SSS电业局东南变专线供应电力，可以保证电力正常供应。1.3.6供热情况目前多多药业有限责任公司共有3台锅炉用于生产（2台10t/h，1台6t/h），产汽量为26吨/时，可以保证正常生产。并采用除尘装置防治大气污染，蒸气可以经过现有蒸气管网总干线，敷设支管引入各用汽装置，供热情况可以满足项目建设需要。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF1.4主要技术经济指标序号名称单位数量1项目规模立方米/天20002动力消耗KWh/天184.43水耗立方米/天254总建筑面积平方米60005年操作日天3606劳动定员人77总投资万元1292.931.5公司概况1.5.1公司自然状况HHH多多药业有限责任公司是HHH省大型医药加工企业，药品的液体制剂已通过国家GMP认证。现有技术人员800余人，还有熟练各岗位的技术工人1200余人，全体员工均经过严格专业技术培训，生产、技术、质量管理等方面均可达到GMP标准要求。多多药业获2006年中国最佳诚信企业，全国重合同守信用企业，国家火炬计划重点高新技术企业，HHH省优秀企业，省文明单位等多种荣誉称号。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF1.5.2公司主要产品及生产规模公司拥有自己的铁路专用线、符合GMP标准的质量检测中心，为生产所需原料的购入和产品出厂提供便利条件，并严格监控质量，公司技术力量雄厚，加工设备精良，产品质量上乘，监测手段完善。　主要产品有全国独家中药保护品种五加生化胶囊（国家火矩项目）、刺五加注射液、双黄连注射液、盐酸曲马多注射液（片）是国家级二类镇痛新药，对不同原因（手术、癌症、骨折、神经、泌尿系统、腹部、局部缺血、关节等）引起的疼痛有良好的效果。1.5.3生产技术装备公司年生产药品针剂2亿支、片剂50亿片。1.6工程项目建设目的、背景及建设的必要性1.6.1我国水污染和污水处理现状的严峻现实我国被联合国列为世界上13个水资源匮乏的国家之一，严重的水环境污染使我国水资源短缺问题更为突出。水资源短缺和水环境污染所造成的“水危机”在我国已经成为严峻的现实，并已经成为制约我国社会、经济发展的重要因素。根据统计,我国的江河湖泊和水库中,已经受污染的约占82.3%,全国有监测系统的1200条河流中，已有850条受到污染。据全国2222监测站的监测结果显示，我国七大水系符合《地面水环境质量标准》Ⅰ、Ⅱ类仅占33.2%,　符合Ⅲ类标准的占28.9%,属于Ⅳ、Ⅴ类标准的占38.9%。在统计的138个城市河段有133个河段受到不同程度的污染，占统计总数的96。4%，属于超Ⅴ73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF类水质的有53个河段占38%，属Ⅴ类水的27个河段占20%，属Ⅳ类水的26个河段占20%，Ⅱ、Ⅲ类水仅占23%。造成我国水环境污染的主要原因是城市污水和工业废水未能得到有效的处理。自1985年以来，我国污水的年排放量介于350～400亿m3左右，1997年的污水排放量高达416亿m3。我国每年排入水环境的COD高达1757万吨。造成我国水环境严重污染的另一个重要原因是包括污水处理技术在内的城市排水工程基础设施水平很低，排水管道系统的普及率、城市污水处理率和污水回用率等三项指标都很低。全国668个设市的城市中有532个还没有污水处理系统，在136个设有城市污水处理厂的城市中，污水年处理量仅为83.3×108m3，占全国城市污水排放总量的23.6%左右，而且在建成的309座污水处理厂中，大部分设备简陋，达二级生物处理的仅占5%，而且其中大部分运行不够正常，有的建成后一直因种种原因未能正常运行。自二十世纪90年代以来，我国国民生产总值连续以8%～11%的高速率增长，预计在二十一世纪前20年内我国经济增长将稳定保持在6%～9%的速率。这一形势与水资源短缺和水环境污染之间的矛盾日益尖锐，如不加以有效的解决，必将导致大幅度的生态环境的破坏，使我国社会经济可持续发展面临严峻的挑战。这就是我国水环境污染与污水处理现状的严峻现实。1.6.2本项目建设的必要性HHH多多药业有限责任公司工业废水的主要来源为车间生产过程中产生的废弃母液、清洗反应设备及工器具的清洗液等高浓度、毒性的有机废水。综合废水年排放量约72万吨。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF这些废水如得不到有效治理，将严重污染松花江流域的水环境，扩大环境污染，制约公司的生存与发展。如果对其加以处理，将会产生间接的和潜在的社会效益。本工程将改善该地区及下游地区水体的水质；避免污水排放对流域的污染以及由此产生的经济损失。因此，通过综合分析考虑，项目的建设会提高企业的循环生产质量，减少对区域内流域的污染、对公司的生存发展以及本地区的污染治理具有重大及深远的意义，所以，本项目的建设是很有必要的。1.7工程建设的可行性根据国内外工程经验和一些相关的试验研究成果，已经证明目前国内实施的处理方法对此类综合废水治理在技术上是可行的，而且经过有关专家的反复论证。因此，只要污水处理厂的设计参数选用合理，工程措施采用得当，可以取得良好的处理效果。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF2.项目建设内容及规模2.1项目建设内容2.1.1废水处理站对公司待排放的废水进行综合处理，进一步削减COD的排放量。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF2.2项目建设规模废水处理72万吨/年，年运行天数360天，日处理量为2000吨/天。以及污水处理产生恶臭单元的臭气处理。3.技术方案确定3.1废水处理站设计处理水量及废水水质确定3.1.1设计水量废水处理规模为72万吨/年，年运行天数360天，则日平均流量为2000m3/d，拟建设日处理能力Qd=2000m3/d的废水处理工程，小时排放量按83.4m3/h进行设计。3.1.2设计水质⑴根据甲方提供资料以及同行业生产情况，该类综合废水水质存在以下特点：①废水成分复杂，悬浮物浓度高。②污染物浓度与水量变化大，冲击负荷高。③生化性一般，含有较难降解的有机污染物。进水水质按如下指标来设计：工业废水进水水质：CODcr：7000mg/l；BOD5：2000mg/l；SS：1700mg/L；pH值5.0～10.0⑵出水水质经综合治理后的废水各项指标达到国家工业废水排放标准（GB8978－96）一级。具体指标如下：CODCr≤100mg/L；BOD5≤30mg/L；SS≤70mg/L；pH：6~973nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF3.2废水处理工艺的确定公司拟建设日处理能力2000吨的废水处理工程。将车间的废水集中到废水处理工段，进行综合处理。3.2.1工艺流程确定的原则水处理工艺的选择是工程建设实施的关键。处理工艺是否合理直接关系到水处理系统的处理效果、出水水质、运行稳定性、建设投资、运行成本等。因此，必须结合实际情况，综合考虑各方面因素，慎重选择适宜的处理工艺，以达到最佳的处理效果和经济效益。废水处理厂建成以后所面临的主要问题是运行和管理问题。这就要求整个污水处理系统易操作、易维护、运行稳定、管理方便，这也是保证污水处理厂正常运行的一个关键。一般从以下几个方面考虑：⑴工艺流程应根据原水水质，处理程度，以及方法应符合现行的国家和地方的有关规定，处理后水质应符合有关用水和排放的标准要求。⑵应综合考虑建厂规模、投资费用和运行费用，参照相似条件下水处理厂的运行经验，结合企业实际财力，进行技术经济比较后确定。⑶应充分利用当地地形、地质、水文、气象等自然条件及自然资源。⑷污水处理应充分考虑排放水体的稀释、自净能力，根据污水处理程度来选择流程。⑸流程选择应妥善处理技术先进和合理可行的关系，并考虑远期发展对水质水量的要求，考虑分期建设的可能性。⑹流程组合的原则应当是先易后难，先粗后细，先成本低、后成本高的方法。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF3.2.2污水中污染物去除技术研究及比较为了选择出最佳的工艺路线，合理的技术参数，制定出最优化的工程方案，我们针对该类综合废水中存在的污染物类别、数量和特性进行详细分析，对混凝、沉淀、气浮、过滤、离子交换、膜处理方法和生物处理方法等多种工艺做了深入比较，为选择出本工程的工艺流程奠定了基础。主要处理方法综述如下：生产工艺废水通过旋转细格栅去除大体积的漂浮物，而后进入调节池，调节池设置空气搅拌，使得水质混合均匀，然后，出水提升至组合气浮设备，通过气浮去除掉水中的微小颗粒和油类，然后污水进入投配池，通过加药调质，调整污水的PH值。之后经提升泵提升进入生化处理厌氧单元。厌氧单元的核心是厌氧反应器。目前，高效厌氧反应器中的厌氧菌均以可以形成并保持高浓度的颗粒化污泥为特征。在已开发的厌氧反应器中，UASB反应器是一种研究最为深入、应用最为广泛的厌氧反应器，已大量成功地应用于处理各种废水。相比较而言，UASB反应器具有一些突出的优点：l有机负荷居第二代反应器之首，水力负荷能满足不同条件的要求l污泥颗粒化后使反应器耐不利条件的冲击能力增强l由于颗粒污泥在适度的水力负荷范围内，可以靠反应器内产生的气体来实现污泥与基质的充分混合及接触。因此，UASB可节省搅拌和回流污泥所需的设备和能耗l73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF在反应器上部设置了气—固—液三相分离器，对沉降良好的污泥或颗粒污泥可以自行分离沉降并返回反应器主体，不须附设沉淀分离装置、辅助脱气装置及回流污泥设备，简化了工艺，节约了投资和运行费用l在反应器内不需投加填料和载体，提高了容积利用率，避免了堵塞问题结合同类型行业工业废水的特点，我们决定采用目前最为成熟稳定、已经获得广泛认可的UASB作为厌氧处理工艺。废水通过厌氧阶段的处理，COD去除了绝大部分，达到好氧处理的有机负荷，然后通过两级接触氧化池，与附着在生物填料上的好氧微生物的进一步作用，去除剩余的有机物，部分随水流带出的悬浮物在沉淀池中得以沉淀出来，出水管道设置管道混合器，通过投加絮凝剂后进入混凝沉淀池，能有效降低二级生物处理出水的COD和色度，混凝沉淀出水经提升后进入砂滤罐去除残余的COD，砂滤后废水得以达标排放。气浮浮渣、厌氧沉淀池、及好氧沉淀池的剩余污泥通过污泥泵进入污泥储存池，加入污泥脱水药剂后，经过带式压滤机脱水处理后外运。滤液回流到调节池进行循环处理。具体分为如下几个阶段：1）废水预处理阶段综合废水进入调节池，池内设有穿孔管进行预曝气，一方面防止污水中的悬浮物沉淀，起到调节水量和均化水质的作用，另外一方面还可以起到充氧曝气的作用，防止废水酸化腐臭；调节池出水经过潜水泵提升至组合气浮，同时投加絮凝剂经气浮预处理后，废水中悬浮物、胶体污染物等可以得到有效去除，减轻后续生化处理的有机负荷。系统还设置有事故池，目的是在来水出现异常突发情况或者设备出现故障时使用。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF2）废水生化处理阶段废水此后进入好氧处理段，目前采用好氧处理工业废水的方法中较为典型的处理工艺有以下几种：1、SBR处理工艺，该方法相对比较有效，可以通过预处理及停留时间来保证出水水质，但是由于该工艺为间歇运行，而综合废水的水质情况每次排放都不相同，造成该处理工艺稳定性差，特别是对出水水质要求较高时，停留时间大大延长，造成处理效率降低。2、吸附生物降解工艺，该处理方法具有基建投资少，运行成本高，反应速度快，处理效率高，耐冲击负荷强，运行稳定的特点，但时该工艺排泥量大，污泥脱水难，运行成本高。3、氧化沟工艺，氧化构工艺基建投资较高，运行成本低，处理相对稳定，产泥量较少。4、接触氧化工艺，接触氧化工艺投资建设较低，运行费用相对较低，占地面积也不大，对自动化要求高，容积负荷较高，生物活性高，污泥浓度也高，产泥量低，不存在污泥膨胀问题，运行稳定。考察综合废水特殊的水质，结合多种处理方法的优缺点，再根据本设计原水水质分析，本着投资省、运行费用低、处理效果好的原则，决定选用UASB反应池+接触氧化工艺。气浮出水进入投配池，在此投加碱（酸）和营养物质，利用空气搅拌来进行混合均匀，使得投配池出水的pH值等满足后续生物处理的要求，保证生物处理单元的正常高效运行。投配池出水用泵提升至一级UASB厌氧反应器，在反应器内培养的高效活性厌氧污泥的作用下，废水中大部分的有机污染物将被厌氧微生物降解去除，COD负荷得到大量削减，出水COD显著下降。一级UASB厌氧73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF反应器出水部分回流至前段的投配池可以有效地降低进水的有机污染负荷。出水自流至二级UASB厌氧反应器，在反应器内培养的高效活性厌氧污泥的作用下，废水中的有机污染物将被厌氧微生物降解去除，COD负荷得到削减，出水COD继续下降，出水自流入厌氧沉淀池，在此进行固液分离，少量的剩余污泥排入污泥浓缩池，出水进入后续二级接触氧化池。厌氧反应过程中产生的沼气经过收集后进入水封罐进行相应调整后，然后通过火炬直接燃烧处理或根据实际情况加以综合利用。厌氧沉淀池出水自流入二级接触氧化池，经过二级接触氧化池内培养的微生物的降解后，废水中残留的有机污染物进一步被去除，出水COD进一步下降，接触氧化池出水进入二沉池，在此进行固液分离，剩余污泥排入污泥浓缩池，上清液进入后续深度处理单元的混凝沉淀处理。3）废水深度处理阶段二沉池出水经过加药混凝反应后进入混凝沉淀池进行深度处理，出水再资流入中间水池，中间水池出水提升后进入砂滤罐砂滤，出水就可以达到排放标准，经过计量后稳定达标排放。3.2.3废水处理工艺综上所述，确定废水处理工艺流程如下：73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF调节池气浮投配池一级UASB反应器浓缩池上清液加药压滤外运至污泥干化场二级厌氧反应器厌氧沉淀池提升泵提升泵二级好氧池二沉池旋转细格栅污水污泥储池一级好氧池事故池砂滤达标排放污泥池混凝沉淀池加药中间水池提升泵73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF3.2.4去除效率预测序号单元CODcr（mg/L）去除率备注1调节池7000—2组合气浮560020%3投配池4000—一级UASB池回流1000m3/d4一级UASB池100075%5二级UASB池+沉淀池50050%6一级接触氧化池25050%7二级接触氧化+二沉池12550%8混凝沉淀池10020%9砂滤罐＜10010%10排放标准1003.3污泥处理系统综述气浮、厌氧沉淀池、二沉池以及混凝沉淀池的剩余污泥排至污泥储池存储，然后通过污泥浓缩池间歇浓缩。浓缩后的污泥通过泵输送至带式压滤机脱水，带机前设置PAM投加系统，通过投加PAM进行污泥调理。带机系统设有反冲洗系统，运行过程中通过反冲洗泵对滤带进行冲洗。经过带机压滤后的污泥泥饼含水率75%左右，定期外运至城市固定的污泥干化场或者固废处理中心进行处理。污泥浓缩池上清液排至调节池进行处理。3.4臭气处理系统综述根据污水处理多年来的运行经验，发生厌氧反应的设施包括调节池、事故池厌氧反应器以及污泥浓缩池在运行中均会产生异臭味，造成对周围的环境产生二次污染。系统中调节池、事故池、厌氧反应器以及73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF污泥储池、污泥浓缩池等发生厌氧反应的处理单元会产生异味。因此，在系统产生恶臭气体的单元采用加拿大HLSECOLO异味控制技术的异味控制系统。该处理方法在污水处理厂（站）、垃圾站、堆肥场、制药行业、石油化工、塑料行业、公共场所、餐厅油烟异味、酒店等等地方得到广泛的应用。该处理方法核心技术是从树木、鲜花和草中提取油、汁或浸膏的萃取液，通过微乳化技术形成天然植物液，这种喷林液无毒性、无刺激性、无腐蚀性及无燃烧爆炸性。通过专用配套设备雾化或挥发形成气状，弥漫到空气中，与空气中的异味分子发生分解、催化氧化、缩合等反应，产生水、CO2、无机盐治理结果无毒无害、无二次污染。运行费用低，有很高的性价比。3.5在线检测及系统控制综述在线检测以及系统控制采用“集中监控、管理，分散控制”的集散型系统。由控制室监控计算机、现场控制站(可编程控制器PLC)组成实时工业控制网。在控制室监控计算机出现故障时,现场控制站仍能独立和稳定工作。整个集散系统由两个层次构成：a、中央监控计算机在处理站控制室设置中央监控计算机，它主要完成对污水厂的管理、调度、集中操作、监视、系统功能组态、控制参数在线修改和设置、记录、报表生成及打印、故障报警及打印等功能。可直观地显示全厂各工艺流程段的实时工况、显示各种检测值及参数、各工艺参数的趋势画面，使操作人员及时掌握全厂运行情况。b、现场控制站73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF现场控制站采用可编程控制器PLC。根据污水站规模和工艺流程，设置一套PLC系统，对废水处理系统的设备进行自控和数据采集。a、通讯网络控制室和PLC控制站通过现场总线CC-LINK进行实时的数据交换，控制室可完成监测现场设备的运行信息。系统中泵采用手动/自动两种控制方式，在自动方式下,由各自池内液位控制设备的自动起、停。在手动方式下，直接在电控柜上控制。废水系统药剂的投加，自动方式下，通过PH在线检测结果与提升泵是否工作来控制投加泵的运行；手动方式下，由操作人员手动控制设备运行。不管加药泵处于手动或自动状态时，需对受对应的贮药池的低液位开关保护。对于只需要位式信号的环节则采用浮球式液位开关。需要连续信号的环节则采用超声波液位仪。3.6废水综合处理厂厂址选择废水处理厂的厂址确定是一个十分重要的问题，它对基建投资及运行管理都有很大影响。在选厂址时，在考虑总体规划的基础上，还遵循了如下原则：1）设在总排水干管的下游，减少不必要的提升费用；2）考虑厂址的工程地质情况，尽可能节省造价，方便施工；3）厂址选择考虑距离主要供水点较近，减少管道长度；4）厂址选择考虑远期发展的可能性，为以后的扩建留有余地。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF4.工程设计4.1厂区平面设计4.1.1平面布置的原则1）各处理构筑物间的连接管、渠，便捷、顺直，避免迂回曲折。2）各处理构筑物间应保持一定的间距，以保证敷设管、渠及施工的要求。3）各处理构筑物在平面上，尽量紧凑，缩小厂房的建筑面积，降低工程造价。4）其他配套工程应满足相应规范之规定。4.1.2占地面积废水处理系统占地面积共7000m2。4.1.3平面位置为便于整个水处理厂的管理调度，同时结合各生产构筑物的管理，在水处理间内设控制室等，综合生产区平面布置为按水流方向垂直设置，车间进出水流畅。竖向设计考虑自然地势布置。因冬季气温低，厂区内较平坦，所以构筑物考虑保温，构筑物大部分置于室内，确保冬季生产水温，保证处理效果。本工程生产、生活用水由厂区已建成管网供给，分别由支管接入各用水单元。4.2单元设计废水水处理厂按2000m3/d进行总体布局，和厂区其他建构筑物协调一致。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF4.2.1格栅井格栅的主要作用在于将流入处理厂污水中大的漂浮物、悬浮物去除，保证后续污水处理设备的有效运行。格栅井，采用钢筋混凝土结构。细格栅各项参数如下：1）设计水量：83.3m3/h；2）过栅流速：V＝0.7m/s；3）栅条间距：b＝5mm；5）格栅与水平面倾角α＝60°；6）设备型号：XG8007）电机功率：0.75kw8）格栅井尺寸：4.5×1.0×3.0m4.2.2调节池设一座，地下式钢筋混凝土结构。调节水质、水量。为防止污泥沉淀，池内设置空气搅拌，调节池内设有浮球液位开关，设置高、低二个液位，当液位处于高位时，启用提升泵，当液位处于低位时，提升泵停运，设计参数如下：1）调节时间：24小时；2）工艺尺寸：L×B×H=25.0×20.0×5.0m，有效水深4.0m；3）调节池出水采用2台潜水泵提升，1用1备。①型号：150WQ100-9-5.5；73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF②提升水量：Q＝100m3/h；③扬程：H＝9m；④电机功率：N＝5.5KW。4）浮球液位计：接点容量10A/250VAC数量2套材质PP4.2.3事故池地下式，考虑到污水处理系统的应急预案，为防止系统问题以及生产中非常规排水进入污水处理系统，导致系统运行无法正常进行，故而设置事故池，在事故状态下可将全厂生产废水送至事故池暂存。集水池内设有浮球液位开关，设置高、低二个液位，当液位处于高位时，启用提升泵，当液位处于低位时，提升泵停运。1）停留时间：12小时；2）工艺尺寸：L×B×H=20.0×12.5×5.0m，有效水深4.0m；3）事故池出水采用2台潜水提升，1用1备。设置浮球开关两套。①型号：150WQ100-9-5.5；②提升水量：Q＝100.0m3/h；③扬程：H＝9.0m；④电机功率：N＝5.5KW。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF4）浮球开关：接点容量10A/250VAC数量2套材质PP4.2.4加药系统地上式，炭钢防腐，制药废水水质复杂，污水中含有大量的ss，使得污水COD较高，需要在前端进行物化处理，去除大量的SS，为后续生化处理降低负荷，因此设置加药设备用于调节pH值，以及PAC,PAM，以及营养物质的投加，设置了投药设备，PAC储罐数量：1套容积：5立方。PAC溶药罐数量：1套容积：2立方PAM储罐数量：2套容积：2立方。PAM溶药罐数量：2套73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF容积：1.5立方酸投加装置：数量：1套容积：2立方碱投加装置：数量：1套容积：2立方营养物质投加装置数量：1套容积：2立方4.2.5组合气浮为去除污水中的悬浮颗粒物，降低污水COD，在预处理阶段设置气浮池，经混凝沉淀后污水进入组合气浮，通过加压溶气水使污水中的悬浮颗粒上浮，通过刮渣机收集，进入污泥池，从而去除大量的悬浮物。处理能力100m3/h4.2.6投配池为控制生化处理段的处理环境，调节污水进入生化段的水质，设置中和投配池，调节污水的PH值，以及营养物质的投加，池内设置蒸汽加热装置，保证冬季污水的温度。池内设置提升泵。1）停留时间：2小时；73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF2）工艺尺寸：L×B×H=10.0×6.0×3.5m，有效水深3.0m；3）在线PH计：数量2台测量范围0-14制造商梅特勒-托利多4）提升泵2台，1用1备。①型号：150WL140-15-15；②提升水量：Q＝140.0m3/h；③扬程：H＝15.0m；④电机功率：N＝15KW。4.2.7一级UASB池地上式，污水有机物浓度高，无法通过常规的好氧处理降解，需设置UASB反应器进行厌氧处理，方能达到好氧处理所能承受的有机负荷，1）停留时间：30.7小时；2）数量：6座3）单池尺寸：10.0×8.0×8.5m，有效水深8.0m；4）三相分离器6套；5）布水系统6套；4.2.8二级UASB池1）停留时间：26.9小时；73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF2）数量：4座3）单池尺寸：10.0×8.0×7.5m，有效水深7.0m；4）三相分离器4套；5）布水系统4套；4.2.9厌氧沉淀池半地下，竖流式，对厌氧夹带出来的污泥进行泥水分离。1）停留时间：2小时2）池体个数：2座3）工艺尺寸：L×B×H=5.0×5.0×7.2m，有效水深4.0m4.2.10一级接触氧化池地上式，厌氧处理无法达使污染物达到污水排放标准，必须通过好氧菌进行降解，因此厌氧沉淀池出水进入接触氧化池进行处理。一级接触氧化池设计参数：1）HRT=18.0h2）池体个数：1座3）工艺尺寸：L×B×H=25.0×15.0×4.5m（三廊道），有效水深4.0m4）填料体积：750m3。4.2.11二级接触氧化池半地下式。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF二级接触氧化池设计参数：1）HRT=12.0h2）池体个数：1座3）工艺尺寸：L×B×H=25.0×10.0×4.5m（二廊道），有效水深4.0m4）填料体积：500m3。5）鼓风机选型①设备选型：鼓风机采用SSR150鼓风机4台，3用1备（其中一台共调节池、投配池搅拌用）；②性能参数：进口流量Q=21.05m3/min，T=20℃，出口压力P=49.0kPa，配用电机功率N=30kw。③特性：鼓风机进口安装消声器。鼓风机房采用隔音材料隔音。设备安装采用减振措施。6）曝气装置采用微孔曝气器，共计1250个。7）池体结构：钢筋混凝土4.2.12二沉池二沉池主要是用来进行泥水分离的构筑物，本设计采用辐流式沉淀池，半地下式钢筋混凝土结构。设计参数如下：1）停留时间：3.0h2）直径12m，池高4.5m，1座73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF4.2.13混凝沉淀池混凝沉淀池主要是用来对二沉池出水进一步通过加药来混凝处理，半地下式钢筋混凝土结构。1）表面负荷：0.75m3/m2.h2）基本尺寸：Φ12.0×4.5m3）数量：1座4）结构形式：半地下式钢筋砼4.2.14中间水池中间水池主要是用来储存混凝沉淀池出水，通过提升泵将中间水池出水输送到砂滤罐进行处理。本设计采用半地下式钢筋混凝土结构。设计参数如下：1）池体个数：1座2）工艺尺寸：L×B×H=8.0×5.0×3.0m，有效水深2.5m3）提升泵2台，1用1备。①型号：150WL100-15-11；②提升水量：Q＝100.0m3/h；③扬程：H＝15.0m；④电机功率：N＝11KW。4.3.15砂滤罐为保证出水达标，深度处理采用砂滤，保证出水达到排放标准。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF设计参数如下：1）滤速：8.0m3/m2.h2）直径2.6m，高5.0m，2座3）反冲洗泵：①型号：IS150-125-250(A)；②水量：Q＝190.0m3/h；③扬程：H＝18.0m；④电机功率：N＝15.0KW。4.2.16清水池污水经过清水池后达标排放。1）停留时间：1小时；2）尺寸：L×B×H=8.0×5.0×3.0m，有效水深2.5m4.2.17污泥储池污泥储池的主要作用收集存储各工段排放的污泥，收集后污泥通过污泥泵打入污泥浓缩池进行浓缩。设计参数如下：1）池体个数：1座2）工艺尺寸L×B×H=5.0×5.0×3.5m；3）停留时间12小时。4）污泥泵2台①型号：G50-1；73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF②水量：Q＝9.6m3/h；③扬程：H＝30.0m；④电机功率：N＝3.0KW。4.2.18污泥浓缩池污泥浓缩池是使系统中产生的污泥减小体积，便于后续处理。物化阶段，厌氧阶段以及好氧污泥全部进入污泥池进行浓缩，污泥含水率按99.2%计算，去除COD每天产生的湿污泥量约为130m3。本方案设计采用重力式污泥浓缩池，设1座，浓缩后污泥由泥泵送至压滤机脱水后泥饼外运，上清液自流入调节池。1）浓缩后污泥含水率为97%；2）池体个数：1座3）工艺尺寸L×B×H=10.0×5.0×3.5m；4）污泥泵2台①型号：G60-1；②水量：Q＝19m3/h；③扬程：H＝30.0m；④电机功率：N＝5.5KW。4.2.19臭气处理单元设备①处理区域：污泥储池、污泥浓缩池、事故池②处理面积：污泥储池（6.0m×6.0m=36m2室外）污泥浓缩池（直径5.0m×4.5m=19m2室外）事故池（20.0m×17.0m=340m2室外）73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF③主要异味：有机恶臭及硫化氢④防冻措施：冬季运行时，在天然植物工作液中添加适当的防冻液⑤处理设备：HLSECOLO异味控制系统EP-CT设备（2套）包括：HLSECOLO专业雾化喷嘴30个HLSECOLO污水型配方工作液⑥污泥储池安装4个合金铜喷嘴，污泥浓缩池安装4个合金铜喷嘴，事故池安装22个合金铜喷嘴，喷嘴固定在调节池四周的护栏上，具体安装位置根据现场状况来定。⑦喷嘴与喷嘴间用6毫米的高强度输液软管连接，然后与HLSECOLO异味控制系统EP-CT设备连接，外用不锈钢管保护，组成一个完整的雾化系统。4.2.20脱水机房包括污泥脱水机，加药投加设备间，及药剂库，地上式砖混结构。设计参数如下：1）工艺尺寸：综合设备间L×B×H=30.0×15.0×6.0m2）主要设备性能如下：①选用DY1500带式压滤机2套，用于浓缩后的污泥脱水；处理能力：稀污泥（含固率1.5%）5-7m3/h；浓缩脱水后污泥含固率20-30%；絮凝剂用量：4~6kg/T(ds)；主电机N=0.75kw，380VAC/3Ph/50HZ；②污泥进料泵2PNL-12，4台；73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF电机功率N=1.5kw，380VAC/3Ph/50HZ；最大流量：20.0m3/h；出口压力：0.3Mpa；③絮凝搅拌机：2套；功率：0.37KW④加药泵：GM0170：4台；电机功率=0.25kw；⑤清洗水泵：40-200：4台；电机功率（每台）=5.5kw；⑥泥饼带式输送器TD75-500：2台；带宽B=500mm；电机功率=1.5KW/380VAC/3PH/50HZ；3）药库考虑30天的储药量。4.2.21风机房操作间结构尺寸为：L×B×H=10.0×5.0×5.0m，砖混结构。4.2.22综合设备间包括组合气浮以及加药设备。设备间结构尺寸为：L×B×H=20.0×10.0×6.0m，砖混结构。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF4.2.23休息、控制、化验室休息，控制，化验室结构尺寸为：L×B×H=10.0×5.0×3.5m，砖混结构。4.3水质检测与化验水质检测与化验，厂内配置化验室，配置专门化验人员2名，每日对水质进行取样检测，与在线监控系统进行对比实验。4.4建筑设计及结构设计本工程建筑设计在满足工艺条件的基础上，根据当地具体条件并考虑今后的发展，不仅要满足工艺总体布置上的要求，同时还要适应总体规划环境的要求，为美化环境提供有利的条件。4.4.1设计依据《建筑地基基础设计规范》GB50007-2002《建筑结构荷载规范》GB50009-2000《混凝土结构设计规范》GB50010－2002《建筑抗震设计规范》GB50011-2001《给水排水工程构筑物结构设计规范》GB50069-20024.4.2建筑设计1）厂区环境概况拟建水厂在厂区内部，地形平坦，厂区总体属简单地貌，地震烈度小于6度。2）厂区平面设计73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF本工程平面布置与厂区道路相协调，满足车间使用功能，并尽可能地合理使用土地。3）单体建筑物、构筑物及其布局建筑单体以比较简洁的设计，贯穿整个工程。主要建筑单体和原厂区主要生产车间建筑风格相协调，表现出宏大的企业形象，配合白色的墙面和淡绿色玻璃，以实现“洁净式”生产空间的设计构思。4）厂区雨水设计及道路设计厂区雨水设计及道路设计利用厂区已建成的道路及雨水管道。5）建筑标准①地坪：车间地面，选用国产中档瓷砖地坪，控制室为抗静电地板铺地，所有厕所为防滑地瓷砖，其它主要为水泥地坪。②内墙：选用中档内墙涂料。③外墙：选用中档外墙涂料，构筑物为清水外墙。④栏杆扶手：水工构筑物和建筑物栏杆扶手选用不锈钢栏杆扶手。⑤门窗玻璃：选用58系列单框双玻塑钢窗。4.4.3结构设计1）工程地质概况参见地质、地貌资料。2）荷载①基本风压0.30KN/m2，基本雪压0.15KN/m2。不上人屋面活荷载标准值取0.7KN/m2，上人屋面活荷载标准值取1.5KN/m2。②水池池壁侧向土压力填土重度取18KN/m3，内摩擦角30°。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF③泵房人行平台活荷载标准值取3.5KN/m2，没有设备的池顶活荷标准值取2.0KN/m2，外边地面活荷载标准值取10KN/m2。汽车荷载标准值（汽-15）：单轮压力50KN，轮距1.80m，动力系数1.1，泵房起重设备动力系数1.05。④实心砖墙重度取19KN/m3，空心砖墙（空心率20%）重度取15.2KN/m3，加气块重度取7.5KN/m3。3）地基选用砂砾层作为持力层，经过处理后的地基允许承载力：取fk=200Kpa。4）抗震设计：该地区地震基本烈度为小于6度。根据《建筑抗震设计规范》GB50011-2001的规定，本工程的建构筑物均为丙类建筑，其地震作用和抗震措施应按本地区设防烈度6度设计。5）材料：混凝土：a、贮水构筑物、泵房地下室部分和沿线管道井室为C25，抗渗等级S6，抗冻等级D50，其余部分为C25.b、设备基础、管道基础、管道支墩、等为C15，c、混凝土垫层为C10。钢筋：为I级钢和II级钢。钢筋直径Φ≤10mm时为I级钢，Φ＞大于10mm时，为II级钢。砌体：a、砖MU10，可考虑使用空心砖，混合砂浆M7.5；b、建筑物基础拟采用浆砌块石，石材强度不小于MU20，水泥砂浆M7.5。6）结构型式：集水井、清水池等贮水构筑物为钢筋混凝土墙板式结构；操作间等为砖混结构。7）地基处理：73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF采用天然地基。岁①管材：车间内采用钢管，钢管应做防腐处理;给水管及排水管道为UPVC管。②敷设：本工程除个别地段外均为开槽敷设。回填土应严格夯实，管顶覆土厚度应大于0.70m。槽底宽度：PVC管为管外径加1.0m；钢管和铸铁管为外径加0.6m。厂区外管道基础：当采用钢筋混凝土管时,覆土厚度小于3.5m时采用120°混凝土基座，覆土厚度4～6m时采用180°混凝土基座。钢管一般在管底铺0.2m～0.3m厚的砂垫层。沟槽回填：管道试压合格后方可回填。4.5电气设计4.5.1设计标准1）本设计主要执行以下技术标准：《工业企业照明设计标准》GB50034-92《供配电系统设计规范》GB50052-95《10KV及以下变电所设计规范》GB50053-94《低压配电设计规范》GB50054-95《建筑设计防火规范》GBJ16-87(2001年版)《建筑物防雷设计规范》GB5007-94(2000年版)《电力装置的继电保护和自动装置设计规范》GB50062-92《电力工程电缆设计规范》GB50217-942）本设计主要参考以下标准图集：《电力变压器室布置》88D26473nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF《变配电所常用设备构件安装》88D263《常用低压配电设备安装》90D367《封闭式母线安装》91D372《电缆桥架安装》86SD169《35KV及以下电缆敷设》94D164《接地装置安装》86D563《等电位联结安装》02D501-24.5.2设计范围本设计范围主要为HHH多多集团有限责任公司废水治理工程工艺部分的供电、自控和照明设计，及值班室等附属构筑物的供配电。设计范围不包括厂外供电线路和供电电源出线间隔。4.5.3设计方案1）供电①电源及电压本工程供电部分为泵房设备间、操作间，电源就近引入。用电点按二级负荷双回路电源考虑。由建设单位负责提供双电源供电，互为备用。电压等级为低380V，供提升泵用。其它低压配电设备采用低压固定式开关柜和动力配电箱。②保护及控制a、低压电动机选用交流接触器作起动控制设备，自动空气开关、热继电器作短路和过负荷保护。对大功率电动机采用软起动。b、生产设备采用现场手动和自动控制两种控制方式。2）自控73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF为实现生产过程自动化与信息管理自动化，按照安全可靠、技术先进、经济合理的原则，在水深度处理车间内拟采用集中监测、分散控制的管控一体化的PLC计算机控制系统，各生产设备均设有现场操作。3）仪表为了保证全厂安全、可靠、正常及时掌握全厂生产动态，在该污水厂内装设多种检测仪表。在进水管道上设有进水流量等检测仪表；在总出水管上设有流量、压力及阀门开启度检测仪表。在变配电间设有检测电气参数仪表，如电压、电流、有功功率/有功电度、无功功率/无功电度变送器。4.6采暖通风与空气调节4.6.1设计依据1）《采暖通风与空气调节设计规范》GB50019-20042）《建筑给排水与采暖工程施工质量验收规范》GB50242-20024.6.2主要内容根据工艺要求，污水处理厂及所属构（建）筑物进行采暖、通风与空气调节的设计。1）主要内容有：①室内采暖；②特殊构筑物的通风及空气调节。2）室外主要气象参数冬季采暖室外计算温度tw=-22℃冬季室外平均风速2.5m/s采暖期天数180d夏季通风室外计算温度tt=30℃73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF4.6.3采暖设计1）热源热源采用HHH多多集团有限责任公司现有蒸汽采暖系统。2）室内采暖：室内采暖设计温度：值班室及配电室（常有工作人员）取tn=18℃；设备间取tn=10～14℃。热负荷为120w/m2，总耗热量为6000w。散热器采用排管，系统放气用集气罐或局部加手动放气阀，管材为焊接钢管。4.6.4通风车间设轴流风机，换气次数10～12次/小时。值班室等辅助生活用房，夏季主要以自然通风为主，通过侧窗及大门进行自然通风，以消除余热，使车间内工作地点的空气符合《工业企业设计卫生标准》的要求，改善车间的工作环境。4.7给排水设计车间给水主要为药品配制、冲洗地面用水。给水管道由车间回用水出水管接出，供各用水点。4.8主要设备及建（构）筑物4.8.1废水处理主要设备及材料表序号工艺设备数量型号规格参数1旋转细格栅1XG800栅隙5mm，功率0.75KW,SUS3042调节池提升泵2150WQ100-9-5.5流量:100m3/hh:9.0m功率:5.5KW，铸铁3事故池提升泵2150WQ100-9-5.5流量:100m3/hh:9.0m功率:5.5KW，铸铁4组合气浮1F-10015kw，碳钢防腐73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF5加酸搅拌器1碳钢防腐D=0.8，N=0.756加酸计量泵2GM01700.25KW7加碱搅拌罐1PEΦ1.5，2m38加碱搅拌器1碳钢防腐D=0.8，N=0.759加碱计量泵2GM01700.25KW10营养剂搅拌罐1PEΦ1.5，2m311营养剂搅拌器1碳钢防腐D=0.8，N=0.7512营养剂计量泵2GM01700.25KW13PAC搅拌罐1PEΦ1.5，2m314PAC搅拌器1碳钢防腐D=0.8，N=0.7515加PAC计量泵2GM01700.25KW16PAM搅拌罐2PEΦ1.2，1.5m317PAM搅拌器2碳钢防腐D=0.8，N=0.7518PAM加药泵2GM01700.25KW19投配池提升泵2150WL140-15-15流量:140m3/hh:15.0m功率:11KW，铸铁20三相分离器10非标设备玻璃钢21布水系统10非标设备SUS30422水封罐2非标Φ800mm23火炬燃烧装置1非标SUS30424臭气处理系统1ECOLO含阻火器、点火系统、火炬25管道混合器2SKDN15029接触氧化池鼓风机4SSR150流量:21.05m3/h风压:49.0kpa功率:30.0KW30微孔曝气器1250RCD-2702.5m3/h.个73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF31组合填料1250Φ150PE32中间水池提升泵2150WL100-15-11流量:100m3/hh:15.0m功率:11.0KW33刮泥机2ZXG12D=12，N＝0.37KW34污泥螺杆泵2G50-1流量:9.6m3/hh:30.0m功率:3KW35污泥浓缩池污泥泵2G60-1流量:19m3/hh:30.0m功率:5.5KW36冲洗水泵2IS150-125-250流量:190.0m3/hh:18.0m功率:15KW37污泥带式脱水机2DY1500B=1500mm38砂滤罐2碳钢防腐Φ260039COD在线监测仪1COD410010-200mg/l40浮球液位计10UQK-61接点容量10A/250VAC41PH计2GXY3-pHG5201测量范围0—1442超声波流量计1LMZ-150150m3/h，含巴氏计量槽，DC4-20mA43PLC柜1非标1000×1000×220044PLC组件1CPU，S7314含以态网模块，打印机45触摸屏110.4寸46皮带输送机1非标设备15m4.8.2主要建构筑物表序号建、构筑物名称数量尺寸（m）结构1格栅井1座4.5×1.0×3.0钢砼2调节池1座25.0×20.0×5.0钢砼3事故池1座20.0×12.5×5.0钢砼4投配池1座10.0×6.0×3.5钢砼5一级UASB池1组10.0×48.0×8.5钢砼6二级UASB池1组10.0×32.0×7.5钢砼7厌氧沉淀池2座5.0×5.0×7.2钢砼73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF8一级接触氧化池1座25.0×15.0×4.5钢砼9二级接触氧化池1座25.0×10.0×4.5钢砼10二沉池1座Φ12×4.5钢砼11混凝沉淀池1座Φ12.0×4.5钢砼12中间水池1座8.0×5.0×3.0钢砼13清水池1座8.0×5.0×3.0钢砼14污泥储池1座5.0×5.0×3.5钢砼15污泥浓缩池1座10.0×5.0×3.5钢砼16脱水机房1座30.0×15.0×6.0砖混17风机房1座10.0×5.0×5.0砖混18综合设备间1座20.0×10.0×6.0砖混19休息/控制/化验室1座10.0×5.0×3.5砖混73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF5.管理机构、人员编制5.1管理机构污水处理厂管理机构与人员编制是指该水处理厂投产后的编制，筹建期与建设期不在此范围之内。参考国内外同类企业污水处理厂的实际管理机构与人员编制情况，确定管理机构与人员编制。5.2人员编制车间人员总数为7人，三班工作制，每班2名工人，倒替班工人1名，管理人员及技术人员由现有的给排水机构负责。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF6.专项设计6.1节能专篇1、总体布局结合本工程的特点，在污水处理厂的选择时充分考虑了节能因素，将污水处理厂选在服务区的最低处，这样既减少了排水管道的深度，减少了土方量，降低了基本建设投资，又能最大限度的节约能源、电耗。2、本工程设计采用如下措施、贯彻节能方针、降低电耗。（1）应用动态功率因数补偿措施，使无功电耗降至最低。（2）精心设计、避免拖动电机大马拉小车轻载现象。（3）优选自身能耗低，效率高的电气设备、器件。（4）用电设备进行集中无功补偿，并选用节能变压器及高效率电机，力求降低电能损失。（5）优选高效电光源，采用混光反射灯具，提高照度和节电。6.2环保专篇6.2.1设计依据和采用标准依据国家计委和国务院环境保护委员会1987年3月20日《关于颁发“建设项目环境保护设计“规定”的通知》［(87)国环字第002号］中有关内容和要求进行设计。本工程采用的环境保护标准是：(1)《地面水环境质量标准》(GB3838－88)(2)《污水综合排放标准》(GB8978-96)(3)《建设项目环境保护设计规定》（87）国环字002号；73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF(4)《环境空气质量标准》GB3095-1996。(5)《城市区域环境噪声标准》GB3096-93；(6)《工业企业厂界噪声标准》GB12348-90。6.2.2建设地区环境现状建设地区在HHH多多药业有限责任公司现场址内，该项工程建成后，减轻了对该地区环境的污染，对环境的改善是有利的。因此具有明显的环境效益和社会效益。6.2.3主要污染源工程建成后，产生的污染源如下：1、污水生产车间产生的污水，主要是过滤罐反冲洗水、车间地面溶气冲洗水及厂区内生活污水。2、噪声水泵及空压机运行时，会有噪声产生。6.2.4控制污染的对策1、污水治理产生的污水就近排至厂区内污水管道，通过厂区污水管道收集进入污水处理系统。2、噪声治理水泵及空压机运行时产生的噪声，设计采用隔振基础，进出管道加隔振接头。工人设值班室，与噪声隔离。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF由于水处理车间远离居民区（距离超过1km），因此车间外的噪声不会影响居民区，厂区内噪声达到国家标准的要求。6.2.5结论本工程建成后，HHH多多药业有限责任公司充分利用了水资源，控制污水排放对环境的污染，因此从环保的角度看，应当抓紧建设，使其尽早发挥环境效益、经济效益和社会效益。6.3消防专篇6.3.1设计依据和基础《建筑防火设计规范》GBJ16-87（2001年版）6.3.2工程概述本工程是位于HHH多多药业有限责任公司废水治理工程，市区设有消防中队，有消防车，火灾后可在10min内到达水厂。6.3.3总图布置废水管道埋在地下，没有发生火灾的可能性。废水处理车间建筑物之间防火间距均大于12m。厂区内设环形车道，宽6m，转弯半径9m，沥青混凝土路面。6.3.4建筑结构废水处理车间内建筑物耐火等级为一、二级，生产类别为丁、戊类，建筑物为砖混结构，混凝土双T板屋顶。综合处理间±0.00m以下为钢筋混凝土结构。建筑物内的安全出口、疏散走道、疏散距离均符合规范要求。地下构筑物及车间内构筑物均为钢筋混凝土水池。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF6.3.5消防给水废水处理车间内各建筑物按规范均不设室内消火栓。室外消火栓用水量为15L/s，原厂区设有室外消防给水管及室外消火栓，本工程在厂区已建消火栓保护之内，已建成室外给水管道呈环形，消火栓距道路边不大于2m，距建筑物不小于5m。6.3.6电气1）电源：用电为二级负荷，采用二路低压进线。2）设备选型：根据《爆炸和危险火灾场所电力装置设计规范》GB50058-1992，本工程属23区火灾场，设备均选用防护型。3）变配电间配备干粉灭火器，扑灭初期火灾。6.3.7采暖与通风采暖热源来自HHH多多药业有限责任公司供热外网。废水处理车间设轴流风机，主要为排除异味及水蒸汽。无粉尘及有害有毒气体排出。6.3.8工艺生产工艺为污水处理工程，无火灾危险。6.3.9结论本工程消防设计符合国家消防设计规范要求，设计中充分体现了“预防为主，防消结合”的基本原则。6.4劳动安全卫生专篇6.4.1设计依据和标准1）《国务院关于加强防尘防毒工作的决定》[国发（1994）97号]73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF2）《建设项目（工程）劳动安全卫生监察规定》劳动部第3号令1996年10月17日。3、《工业企业设计卫生标准》（TJ36-87）4、《工业企业噪声控制设计规范》（GBJ87-85）6.4.2生产中不安全因素和职业危害分析1）不安全因素在废水处理车间工序作业时，工人操作不慎，可能造成机械损伤和其他事故。酸碱药剂投加系统由于操作不慎，也可能给工人造成损伤。2）职业危害本工程项目职业危害主要有：机电设备的噪声。6.4.3劳动保护和安全措施为提高运行管理水平，改善操作环境和劳动条件有利安全生产，本工程采取如下防范管理措施。1）设计考虑在工艺设备选型，生产操作运行中采取实用、安全、减轻劳动强度、方便操作管理的设备和控制方式，设备间内设有起重设备，方便安装和检修；机泵采用直接启动，一步化操作等。2）对机泵等产生噪声的设备，除采取减少震动和噪声综合控制措施（采用减振基础、避振接头等），对值班控制室采取双层结构或组合隔音构件的相应隔音措施，改善值班工作环境。3）对于酸碱投加系统，采用自动化程度较高的控制系统，尽量避免人工操作。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF4）所有电气设备按国家有关电气设计技术接地保护规程要求设计，低压设备采用接零保护，接地电阻不大于2Ω。电气的防火采用干式灭火器，安置在配电间值班室内。5）各种机械的运动部分均加设必要的保护罩。留有安全活动空间。6）制定各工种岗位责任制及安全操作规程，机泵间、变电所的工人一定要经过培训，通过考核，有上岗证的工人方可上岗。厂内一切设备均需定期维护检查，及时发现隐患，防患于未然。7）车间设值班室、更衣室。8）低压用电设备设漏电保护器，低压照明和维修临时电源均采用24~36伏安全电压。电压等级不同的电气设备设置醒目、易于识别的安全标志牌及必要的保护网。9）设劳动安全管理组织，车间有兼职安全员，经常对工人进行安全教育及安全检查。10）采用上述劳动保护和安全措施后，工人的操作环境和劳动安全，能够符合相应的标准和条件。6.5抗震设防1）设计依据①中国地震烈度区划图（1990）②《建筑抗震设计规范》GB50011-2001③《建筑抗震设防分类标准》GB50223-952）SSS市地震基本烈度为小于6度，按照规定抗震等级进行防护。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF7.项目招标根据《中华人民共和国招投标法》以及“中华人民共和国国家发展计划委员会令第9号”——《建设项目可行性研究报告增加招标内容以及核准招标事项暂行规定》的有关规定，建设单位应对本项目的工程设计、建筑工程、安装工程、监理、设备、重要材料的选购等本着公平、公正、公开的原则以委托招标的形式对社会进行公开招标。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF8.工期安排8.1工程安排按总体规划，经与建设单位协商，年度工程安排如下：1）总建设期：2007年9月～2008年5月2）可行性研究：2007年7月～2006年8月3）工程设计：2007年9月4）设备选购：2007年9月～2007年10月5）土建施工：2007年9月～2008年1月6）设备安装调试及人员培训：2007年11月～2008年2月7）工程试运行及工程验收：2008年2月～2008年5月8.2工程项目实施计划表73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF项目实施计划表日程工作安排07年8月07年9月07年9月07年9月07年9月07年10月07年11月07年12月08年1月08年2月08年5月可行性研究报告审查、批复地形测量、地质钻勘初步设计及审批施工图设计招标施工准备、场地平整污水处理厂土建施工处理厂工程设备安装管线施工试运行工程投产73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF9.投资估算及资金筹措9.1编制说明及依据1.本估算编制内容为HHH多多集团有限责任公司废水治理工程投资估算，工程总投资为：1292.93万元。2.编制依据：(1)本工程的工程量按我公司编制的可研报告计算，估算采用的定额指标如下：《全国统一市政工程预算定额HHH省估价表》、HHH省建筑安装工程费用定额、有关设备厂家报价、《给水排水设计手册》（第10册技术经济）及当地有关文件规定。(2)各项费用的取值：建设单位管理费、工程监理费、设计费等第二部分费用均按国家计委，建设部等有关部门规定计取。(3)本估算按国内技术先进成熟厂家进行设备选型和估价。9.2资金筹措制药废水治理工程项目建设工程总投资为1292.93万元。企业自筹资金732.93万元；国家环保治理专项资金560.00万元。9.3废水处理工程投资估算表序号名称费用（元）备注1设备材料费用.52运输、安装费.13土建费.04设计费.05调试培训费50000.073nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF6管理费80000.07合计.68税金.09工程总造价.610.生产成本及费用估算10.1计费标准物耗计费标准电0.60元/kwh水费3.60元/吨人工工资1000元/人•月NaOH3.5元/kgPAM18000元/吨PAC1800元/吨10.2生产成本估算1）原材料及动力费a.电耗费用运行功率184.4KW，则每年电费为：184.4×24×0.60×360=95.59万元/年b.水耗费用25.0×3.6×360=3.24万元/年c.药剂费用PAM每日投加量为6kg，6/1000×18000×360=3.89万元/年；73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahFPAC投加量每日为350kg，350/1000×1800×360=22.68万元/年2）企业定额及工资总额：制药废水处理工程的操作人员为7人，人均月工资及职工福利费按1500元/月•人计算，年工资总额为12.6万元。3）污泥处理费用每年产生污泥总量约13700吨，其处理费用为20元/吨，总费用为27.4万元/年。4）折旧大修费①折旧费用：残值率为5%，房屋折旧年限20年，设备折旧10年，按直线法折旧房屋折旧费561.06万元×(1-5%)÷20年=26.65万元/年；设备折旧费708.87万元×(1-5%)÷10年=67.34万元/年；具体计算详见附表4《固定资产折旧估算表》②维护大修费用房屋大修费26.65万元×10%=2.67万元/年；房屋大修费67.34万元×10%=6.73万元/年；项目的总成本估算，详见附表3《总成本费用估算表(按要素分)》。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF11.经济评价11.1工程概况HHH多多药业有限责任公司污水治理工程处理规模为：2000m3/d年运行天数360d。工程总投资为1292.93万元。主要工程内容有：废水处理系统及给排水管道及附属工程。11.2资金来源资金来源：企业自筹资金732.93万元；国家环保治理专项资金560.00万元，详见附表2《投资使用计划与资金筹措表》和附表8《资金来源与运用表》。11.3工程实施进度及投资分年使用计划本项目拟定9个月建成，次年投入生产，生产期按11年计，整个计算期为12年。固定资产投资分年使用，按建设进度进行分配。11.4流动资金来源及使用计划流动资金由HHH多多药业有限责任公司提供，详见附表1《流动资金估算表》11.5销售收入及税金本项目为HHH多多药业有限责任公司自行建设且为其公司内部生产配套，并未对外进行经营活动。因此经济评价中所指的销售收入是指公司因本项目的运行而节省的支出（外单位处理HHH多多药业有限责任公司污水的费用和因经处理后可继续使用而节省的循环水）。因此也无销售税金、增值税等费用。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF销售收入及税金附加具体计算详见表5《营业收入、税金及附加估算表》。11.6利润总额本项目企业所得税按33%计算。经计算本项目生产期税前正常销售利润总额为98.41万元，税后正常销售利润总额为98.09万元。具体计算见附表6《损益表》。11.7评价指标计算1.财务盈利能力分析根据本项目财务现金流量情况可计算出以下财务评价指标：项目财务内部收益率为19.69％项目财务净现值607.29万元（Ic＝10％）项目静态投资回收期为6.06年项目动态投资回收期为7.80年详见附表7《项目财务现金流量表》2.投资效益分析通过以上评价指标可以看出，该项目财务内部收益率远大于本行业基准收益率4%，说明盈利能力满足了行业最低要求，当i=4%，财务净现值为764.19万元，大于零。因此，该项目在财务上是可以考虑接受的。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF11.8盈亏平衡分析盈亏平衡点(以产量表示)＝36.89万m3/年计算结果表明，该项目只要达到设计能力51.23%时，也就是年产量达到36.89万m3时，企业就可以保本。计算结果表明该项目具有一定的抗风险能力。11.9敏感性分析该项目基本方案财务内部收益率为19.69%。静态投资回收期为6.06年(包括建设期11个月)均满足了本行业基准值的要求考虑到项目在实施过程中的一些不确定因素的变化，分别对固定资产投资，销售收入，原材料、产量等因素降低或提高±0%，±10%，±20%，±30%时的单独因素变化对全部投资财务内部收益率，NPV和投资回收期影响的敏感性分析。具体计算详见附表9《敏感性分析表》。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF通过敏感性分析，可发现其相关的IRR>4%，因此本项目抗风险能力较强。通过敏感性分析，可发现本项目对固定资产投资变化的敏感度较小，但对销售收入、原材料、产量较为敏感。因此在经营过程中，决策者一定要对水价、原材料价格、产量的变化予以足够的重视。11.10结论根据对该项目的技术经济分析表明，该项目财务评价各项指标较好，财务内部收益率为19.69%，高于本行业基准收益率4%，在折现率为4%时，财务净现值为764.19万元，投资回收期为6.06年(包括建设期11个月)等不确定分析具有较强的抗风险能力。该工程项目有较大的社会效益，建设该项目将减轻对河流水质的污染，节约有限的资源，提高水资源利用率，改善社会环境，改善投资环境，推动工业生产的发展及城市建设，因此，该项目是可行的。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF由于该项目费用与效益比较直观，不涉及进出口平衡问题，财务评价的结果已能满足决策的需要，根据《关于建设项目经济评价工作的若干规定》第三条，不再进行国民经济评价。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF12.工程效益12.1环境效益预测废水治理工程项目的建设对保护生态环境、高效利用水资源起到积极作用，预计每年的主要污染物总量将大幅度减少，其中：化学需氧量(COD)约减少6408吨/年生化需氧量(BOD)约减少2498吨/年悬浮物(SS)约减少813.6吨/年12.2社会经济效益预测废水治理工程项目的建设将对减轻水体污染产生巨大效益，该项目的使用在当地起着推广示范作用，带动其他排污企业尽快建设回用水设施。该项目实现了“低开采、高利用、低排放”，最大限度地利用水资源，提高经济运行的质量和效益，达到经济发展与资源、环境保护相协调并且符合可持续发展战略的目标，因此建设化学制药废水治理工程设施可以有效的节约资源，最大限度的提高资源利用率，同时企业也取得可观的经济效益。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF13.结论和建议13.1结论1）项目建设是必要的，而且是可行的。环境效益、社会效益十分明显。2）各种工艺经过比选，处理方法技术可行，经济合理。3）该项工程总投资1292.93万元，企业自筹资金732.93万元；国家环保治理专项资金560.00万元，建设资金是有保证的。4）该项工程设计方案技术先进、经济合理，建设资金有保证，环境效益、社会效益十分明显，因此工程建设是必要的、可行的。13.2建议13.2.1建立用水制度，保证正常运行建议企业完善用水制度，对用水成本进行严格控制，结合企业实际情况对全厂用水建立管理制度，保证排水正常运行。13.2.2水质监测在系统运行中定期对水质进行监测，随时根据水质变化调整加药量，使得系统始终处于最佳运行状态。13.2.3调试与试运行配套设施的调试可根据有关的技术标准或由供货单位派人进行技术指导。试运行工作应邀请设计单位，安装单位共同参加，试运行工作人员上岗前必须经过技术培训并通过技术考核。有关设施调试，通水试运行以及验收等项工作的技术文件必须存档备查。73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF附表1流动资金估算表单位:万元序号项目最低周转天数周转次数建设期生产经营期1234567891011121流动资产　　　28.8248.0748.0748.0748.0748.0748.0748.0748.0748.0748.071.1应收帐款3012　12.9621.621.621.621.621.621.621.621.621.621.61.2费用　　　15.8626.4726.4726.4726.4726.4726.4726.4726.4726.4726.471.2.1原材料(含外购件等)　　　6.9311.5711.5711.5711.5711.5711.5711.5711.5711.5711.571.2.1.1PAM458　0.290.490.490.490.490.490.490.490.490.490.491.2.1.2PAC458　1.72.842.842.842.842.842.842.842.842.842.841.2.2电3012　4.787.977.977.977.977.977.977.977.977.977.971.2.3水3012　0.160.270.270.270.270.270.270.270.270.270.271.2.4污泥处理费用3012　1.372.282.282.282.282.282.282.282.282.282.281.2.5工资3012　0.631.051.051.051.051.051.051.051.051.051.051.3现金3012　　　　　　　　　　　　　小计　　　28.8248.0748.0748.0748.0748.0748.0748.0748.0748.0748.072流动负债　　　　　　　　　　　　　　2.1应付帐款　　　　　　　　　　　　　　3流动资金　　　28.8248.0748.0748.0748.0748.0748.0748.0748.0748.0748.074流动资金本年增加额　　　28.8219.25　　　　　　　　　5流动资金借款额　　　　　　　　　　　　　　6流动资金借款利息　　　　　　　　　　　　　　7自有流动资金　　　28.8228.8248.0748.0748.0748.0748.0748.0748.0748.0748.0773nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF附表2投资使用计划与资金筹措表单位:万元序号项目合计1234567891011121总投资1341575.23717.728.8219.25　　　　　　　　　人民币1341575.23717.728.8219.25　　　　　　　　1.1建设投资(不含建设期利息)1292.93575.23717.7　　　　　　　　　　1.2建设期利息及其他融资费用　　　　　　　　　　　　　1.3流动资金48.07　　28.8219.25　　　　　　　　2资金筹措1341575.23717.728.8219.25　　　　　　　　2.1项目资本金1341575.23717.728.8219.25　　　　　　　　　建设投资(不含建设期利息)1292.93575.23717.7　　　　　　　　　　　流动资金48.07　　28.8219.25　　　　　　　　　用于建设期利息及其他融资费用　　　　　　　　　　　　　　其中：注册资本　　　　　　　　　　　　　2.2长期借款及债券　　　　　　　　　　　　　2.2.1建设投资借款　　　　　　　　　　　　　2.2.2流动资金借款　　　　　　　　　　　　　2.2.3建设期利息借款　　　　　　　　　　　　　73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF附表3总成本费用估算表(按要素分)单位:万元序号成本及费用名称合计123456789101112经营负荷［%］　0%60%100%100%100%100%100%100%100%100%100%100%1外购原材料费315.98　17.8829.8129.8129.8129.8129.8129.8129.8129.8129.8129.811.1PAC240.41　13.6122.6822.6822.6822.6822.6822.6822.6822.6822.6822.681.2PAM41.23　2.333.893.893.893.893.893.893.893.893.893.891.3水34.34　1.943.243.243.243.243.243.243.243.243.243.242外购燃料及动力1013.26　57.3695.5995.5995.5995.5995.5995.5995.5995.5995.5995.593工资及福利费133.56　7.5612.612.612.612.612.612.612.612.612.612.64修理费95.78　6.279.49.49.49.49.49.49.49.49.44.915折旧费957.67　62.6793.9993.9993.9993.9993.9993.9993.9993.9993.9949.09　房屋折旧费　　17.7726.6526.6526.6526.6526.6526.6526.6526.6526.6526.65　设备折旧费　　44.967.3467.3467.3467.3467.3467.3467.3467.3467.3422.446摊销费23　11.511.5　　　　　　　　　7污泥处理费用11137　16.4427.427.427.427.427.427.427.427.427.427.48利息支出　　　　　　　　　　　　　　流动资金借款利息　　　　　　　　　　　　　　长期借款利息　　　　　　　　　　　　　　短期借款利息　　　　　　　　　　　　　9总成本费用94245　179.68280.29268.79268.79268.79268.79268.79268.79268.79268.79219.4　可变成本77557　99.24165.4165.4165.4165.4165.4165.4165.4165.4165.4165.4　固定成本16688　80.44114.89103.39103.39103.39103.39103.39103.39103.39103.395410经营成本90737　105.51174.8174.8174.8174.8174.8174.8174.8174.8174.8170.3173nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF附表4固定资产折旧估算表单位:万元序号项目折旧年限1234567891011121房屋、建筑物　　　　　　　　　　　　　1.1净值　　561.06543.29516.64489.99463.34436.69410.04383.39356.74330.09303.441.2折旧费20　17.7726.6526.6526.6526.6526.6526.6526.6526.6526.6526.651.3余值　　543.29516.64489.99463.34436.69410.04383.39356.74330.09303.44276.792机器设备(线性折旧)　　　　　　　　　　　　　2.1净值　　708.87663.97596.63529.29461.95394.61327.27259.93192.59125.2557.912.2折旧费10　44.967.3467.3467.3467.3467.3467.3467.3467.3467.3422.442.3余值　　663.97596.63529.29461.95394.61327.27259.93192.59125.2557.9135.473机器设备(加速折旧)　　　　　　　　　　　　　3.1净值　　　　　　　　　　　　　3.2折旧费　　　　　　　　　　　　　3.3余值　　　　　　　　　　　　　4合计　　　　　　　　　　　　　4.1净值　　1269.931207.261113.271019.28925.29831.3737.31643.32549.33455.34361.354.2折旧费　　62.6793.9993.9993.9993.9993.9993.9993.9993.9993.9949.094.3余值　　1207.261113.271019.28925.29831.3737.31643.32549.33455.34361.35312.2673nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF附表5营业收入、税金及附加估算表单位:万元序号项目名称年序123456789101112生产负荷　60%100%100%100%100%100%100%100%100%100%100%1营业收入　　220.32367.2367.2367.2367.2367.2367.2367.2367.2367.2367.21.1节约循环水　　155.52259.2259.2259.2259.2259.2259.2259.2259.2259.2259.2　单价元/吨3.63.63.63.63.63.63.63.63.63.63.63.6　数量吨　1.2节约外单位污水处理费用　　64.8108108108108108108108108108108　单价元/吨1.51.51.51.51.51.51.51.51.51.51.51.5　数量吨　2营业税金及附加　　　　　　　　　　　　　2.1营业税　　　　　　　　　　　　　2.2消费税　　　　　　　　　　　　　2.3城市维护建设税7%　　　　　　　　　　　　2.4教育费附加3%　　　　　　　　　　　　3增值税　　　　　　　　　　　　　　　　销项税　　　　　　　　　　　　　　　　进项税　　　　　　　　　　　　　73nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF附表6损益表单位:万元序号项目合计1234567891011121营业收入3892.32　220.32367.2367.2367.2367.2367.2367.2367.2367.2367.2367.22营业税金及附加　　　　　　　　　　　　　3总成本及费用2829.69　179.68280.29268.79268.79268.79268.79268.79268.79268.79268.79219.44补贴收入　　　　　　　　　　　　　5利润总额1062.63　40.6486.9198.4198.4198.4198.4198.4198.4198.4198.41147.86弥补前年度亏损　　　　　　　　　　　　　7应纳税所得额1062.63　40.6486.9198.4198.4198.4198.4198.4198.4198.4198.41147.88所得税3.47　0.130.290.320.320.320.320.320.320.320.320.499净利润1059.16　40.5186.6298.0998.0998.0998.0998.0998.0998.0998.09147.3173nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF附表7项目财务现金流量表单位:万元序号项目合计1234567891011121现金流入5210.32　282.99461.19461.19461.19461.19461.19461.19461.19461.19461.19776.621.1营业收入3892.32　220.32367.2367.2367.2367.2367.2367.2367.2367.2367.2367.21.2回收固定资产余值312.26　　　　　　　　　　　312.261.3回收固定资产折旧　　62.6793.9993.9993.9993.9993.9993.9993.9993.9993.9949.091.4回收流动资金48.07　　　　　　　　　　　48.071.5其他现金流入　　　　　　　　　　　　　2现金流出3190.02575.23823.21203.62194.05174.8174.8174.8174.8174.8174.8174.8170.312.1建设投资(不含建设期利息)1292.93575.23717.7　　　　　　　　　　2.2流动资金48.07　　28.8219.25　　　　　　　　2.3经营成本1849.02　105.51174.8174.8174.8174.8174.8174.8174.8174.8174.8170.312.4营业税金及附加　　　　　　　　　　　　　2.5其他现金流出　　　　　　　　　　　　　3净现金流量(1-2)　-575.2-540.2257.57267.14286.39286.39286.39286.39286.39286.39286.39606.31　累计净现金流量　-575.2-1115-857.9-590.7-304.4-17.96268.43554.82841.211127.614142020.34净现金流量(Ic=10%)　-575.2-491.1212.87200.71195.61177.83161.66146.96133.6121.46110.42212.51　累计净现金流量(Ic=10%)　-575.2-1066-853.5-652.8-457.2-279.3-117.729.3162.9284.36394.78607.2973nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF附表8资金来源与运用表单位:万元序号项目1234567891011121资金流入575.23938.02396.02386.45367.2367.2367.2367.2367.2367.2367.2367.21.1营业收入　220.32367.2367.2367.2367.2367.2367.2367.2367.2367.2367.21.2增值税销项税额　　　　　　　　　　　　1.3收到的税费返回　　　　　　　　　　　　1.4长期借款及债券　　　　　　　　　　　　1.5短期借款　　　　　　　　　　　　1.6项目资本金575.23717.728.8219.25　　　　　　　　1.7其他　　　　　　　　　　　　2资金流出575.23823.34203.91194.37175.12175.12175.12175.12175.12175.12175.12170.82.1经营成本　105.51174.8174.8174.8174.8174.8174.8174.8174.8174.8170.312.2增值税进项税额　　　　　　　　　　　　2.3增值税　　　　　　　　　　　　2.4营业税金及附加　　　　　　　　　　　　2.5所得税　0.130.290.320.320.320.320.320.320.320.320.492.6建设投资（不含建设期利息）575.23717.728.8219.25　　　　　　　　2.7增加流动资金　　　　　　　　　　　　2.8各种利息及融资费用支出　　　　　　　　　　　　2.9偿还债务本金(含利息资本化)　　　　　　　　　　　　2.1分配股利或利润　　　　　　　　　　　　2.11其他　　　　　　　　　　　　3盈余资金(1-2)　114.68192.11192.08192.08192.08192.08192.08192.08192.08192.08196.44累计盈余资金　114.68306.79498.87690.95883.031075.111267.191459.271651.351843.432039.8373nSelection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormSelection.ParagraphFormaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2Selection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPointselection.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFormat.LineSpacingLinesToPoction.ParagraphFormat.LineSpacingLinesToPoints(2)Selection.ParagraphFaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaaahF附表9敏感性分析表序号不确定因素变化率(%)项目财务净现值Ic=10%静态投资回收期动态投资回收期内部收益率万元年年基本方案19.69%607.296.067.81建设投资30%22.34%793.015.687.0920%21.47%731.095.87.3210%20.59%669.195.937.55-10%18.79%545.386.218.07-20%17.87%483.456.368.38-30%16.94%421.576.528.712销售价格30%29.85%1282.724.775.620%26.51%1057.565.116.1410%23.13%832.425.536.84-10%16.19%382.136.759.19-20%12.59%156.997.6711.16-30%8.85%-68.178.98　3原材料价格30%18.85%552.436.218.0820%19.13%570.726.167.9810%19.41%588.996.117.89-10%19.98%625.556.017.71-20%20.26%643.845.977.63-30%20.54%662.125.927.544产量30%25.67%1001.655.216.320%23.70%870.25.466.7110%21.71%738.725.747.2-10%17.66%475.816.448.54-20%15.59%344.376.889.49-30%13.49%212.97.4110.7373