xoXX公司合成氨、尿素安全环保隐患治理搬迁项目可行性研究报告(doc P210页)优秀可研报告.doc
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1、Gay is now a provincial key construction project of aluminum Ltd-province with an annual output of 50,000 tons of technical innovation project of environmental protection and energy saving of electrolytic aluminum project manager. In this technological transformation projects, he has overall respons
2、ibility for the day-to-day affairs of the project. In order to ensure that southern companys control the scale of investment, strengthen field management, pay special attention to project progress, and ensure a successful operation, the overall goal. He and Engineering Department under the leadershi
3、p of all the staff in the companys technical command, on the difficulties and to overcome technical difficulties in the process, work hard, have made outstanding achievements, mainly reflected in the following aspects: first, careful organization and management achieved remarkable results. Technical
4、 innovation project of the year, started and completed a series of bids and completed to date, from production engineering to put into production after nearly a year, has achieved very significant results. A project first 56 slots from dismantling the old slot just 168 days, civil engineering, insta
5、llation, commissioning, guarantee engineering quality under the premise, on the production side transformation under difficult conditions, created the national industrys fastest speeds. II 32 large prebaked electrolytic cell on November 7 has been installed, marks has an annual production capacity o
6、f 50,000 tons of electrolytic aluminum production capacity of aluminum. Entire project almost 8 months earlier than planned, achieved the goal of production transformation benefits that year, created favorable conditions for aluminum through South. Second, effectively control the investment. Project
7、 is subject to a scientific approach to bidding, bidding to make savings of 20 million Yuan, in the implementation process of the project, every domestic prices of steel, cement and other building materials, the old buildings on the base encountered great difficulties in dealing with significant inc
8、rease in the volume of civil engineering, but through rationalization and optimization, project control in fixed investment of 350 million Yuan. Third, environmental energy-saving effect of the project. Project investment of nearly 30 million Yuan, using large prebake technology and aluminum oxide d
9、ense phase and hyper dense phase conveying technology, fluoride and other harmful gases purification efficiency of up to 98%. Compared with Soderberg cell before the modification, power consumption can be reduced by 1500 tons of electrolytic aluminum, and project environmental protection and energy
10、saving effect is obvious. Four are in a relatively short period of time to the normal production. After four months of efforts, a project has put into operation all the 54 240KA large cell into regular production, stable current channel conditions and all the economic indicators are good, current ef
11、ficiency in October had reached 93%, is close to and reach the domestic advanced level. In the case of production half of the cell, this effect can be achieved and better level in the industry. 50,000 tons of electrolytic modification process, from preliminary study to equipment selection, cost cont
12、rol, project progress, quality control and coordination among the various sub-projects and various professional, technical command under the correct leadership, both from an overall perspective, emphasis on integrity, and earnestly implement the relevant laws and regulations, strictly act according
13、to the contract. He tried to learn relevant knowledge, good style of business, operational and organizational coordination ability, project efficiency, quality and safety assurance system in place, with all units involved with the coordination and good . 目 录1. 总论1.1概述1.1.11.1.2项目名称及建设单位基本情况建设单位基本情况1
14、.2编制单位、编制依据和原则1.2.1可行性研究报告的编制单位1.2.2编制依据1.2.3编制原则1.3项目背景及建设的必要性1.3.1项目背景1.3.2项目建设的必要性1.4项目范围1.51.5.11.5.21.6研究结论及建议研究的初步结论存在的主要问题和建议主要技术经济指标2. 市场预测2.1产品用途2.22.2.12.2.2国内外市场预测世界市场国内市场2.3产品价格2.3.1国际市场价格2.2.2国内市场价格3. 生产规模、产品方案3.1生产规模3.2产品规格及质量标准4 工艺技术方案4.1合成氨装置4.1.1搬迁合成氨装置工艺技术方案4.1.2新建合成氨装置工艺技术方案4.2尿素装
15、置4.2.1现有尿素装置工艺概述4.2.2搬迁尿素装置工艺概述4.2.3尿素装置工艺技术方案(新建1200吨/天)4.2.4新建尿素装置工艺概述4.2.5工艺路线比较和选择(650吨/天)4.3全厂自控方案4.3.1自动化水平4.3.2DCS、ESD的配置与主要仪表选型4.3.3仪表供电和供气5. 原料、燃料及辅助材料及的供应5.1原燃料天然气规格、用量及来源5.1.1天然气规格5.1.2天然气用量5.1.3来源5.1.4供应方式5.2辅助材料用量及来源5.2.1催化剂品种、用量及规格5.2.25.2.3主要化学品用量及规格包装用品用量及规格6. 建厂条件和厂址方案6.1建厂条件6.1.1地理
16、位置6.1.2地形、地貌概况6.2工程地质、地震烈度6.3水文地质情况和有关江河水文资料6.4当地气象条件6.4.16.4.2气温风6.4.3降雨6.4.4空气温度6.4.5气压6.5供电6.6供水6.7给排水6.8供热6.9通讯6.10交通运输状况6.11地区和城镇社会经济的现况及发展规划6.12与城镇、地区规划的关系和生活福利设施的条件7 公用工程和辅助设施方案7.1总图运输7.1.1概况7.1.2总平面布置7.1.3竖向布置7.1.47.1.57.1.6绿化运输设计采用的规范7.2给排水7.2.1设计概况7.2.2水源7.2.3给水系统7.2.4排水系统7.2.5污水处理站7.2.6定员
17、7.3供电及电讯7.3.1设计范围7.3.2负荷等级和用电负荷7.3.3全厂供电系统设计方案和原则7.3.4电气设备选型7.3.5照明7.3.6配电线路7.3.7防雷接地7.3.8主要设备材料表7.4供热7.4.1供热负荷7.4.2燃料条件7.4.37.4.47.4.57.4.67.4.77.4.87.4.97.4.107.4.11锅炉房能力确定蒸汽系统简述锅炉房布置简述锅炉房工艺流程简述原料及水电消耗三废排放量锅炉房生产定员法规或标准附件7.5粉体工程设施7.5.1研究范围7.5.2设计原则7.5.3工艺流程说明7.5.4系统能力的确定7.5.5设备一览表7.5.67.5.7占地、建筑面积公
18、用工程消耗7.6氮气、空气供应7.6.17.6.27.6.37.6.47.6.57.6.6设计依据工艺技术方案选择主要设备选型占地水、电消耗量定员7.77.7.17.7.27.7.3维修及全厂性仓库维修装置全厂性仓库化学品库7.8 中央化验室7.8.1设计范围7.8.2分析室建筑概况7.8.3主要分析方法及分析仪器概述7.8.4定员7.9 土建7.9.1工程地质7.9.2土建方案7.9.3土建工程量及“三材”用量7.9.4采用的主要标准及规范7.9.5建构筑物一览表8节能/能耗及节能措施8.1合成氨装置节能/能耗及节能措施8.1.2吨氨能耗8.1.2节能措施8.2尿素装置节节能/能耗及节能措施
19、8.2.1节能措施8.2.2节能效果9 环境保护9.1厂址与环境现状9.1.1厂址地理位置9.1.2地形、地貌、水文及气象特征9.1.3环境质量现状9.2技改项目现有情况9.2.1四川XX绵阳分公司现有生产情况9.2.2“三废”排放9.2.3现有环保措施9.2.4绵阳分公司存在的环境问题9.3执行的环保标准9.3.1环境质量标准9.3.29.49.4.1污染物排放标准本项目主要污染源及污染物本技改搬迁项目情况9.4.29.59.5.19.5.29.5.3“三废”排放情况控制污染的主要措施废气治理措施废水治理措施废渣治理措施9.5.49.5.59.5.6噪声绿化环保管理及监测9.6环保投资估算9
20、.7环境影响分析9.7.1大气9.7.2水体9.4.4噪声的防治9.8存在问题及建议10 劳动保护与安全卫生10.1设计原则10.2设计中采用的标准、规范10.3建设项目生产过程中职业危害因素的分析10.3.1生产过程中的主要职业危险因素10.3.2主要有害无聊的危害特性10.4安全卫生防护措施10.5劳动安全卫生管理10.5.1劳动安全卫生管理机构10.5.2安全卫生教育培训及管理制度10.5.3职业病防治10.5.4安全预评价10.6安全卫生投资估算10.7消防设施10.7.1设计中采用的标准规范10.7.210.7.310.7.410.7.5消防环境现状工程的火灾危险类别消防设施和措施消
21、防投资估算11. 工厂组织和劳动定员11.1工厂体制和组织机构11.2生产班制及定员11.3员工来源及培训12项目实施规划12.1建设周期的规划12.2实施进度规划13.投资估算和资金筹措13.1投资估算13.1.1工程概况13.1.2编制依据13.1.3主要设备及材料价格13.1.4估算指标13.1.5项目总投资及投资分析13.1.6其它说明14. 财务分析14.1计算依据14.1.1财务评价依据14.1.2财务评价基础数据与主要参数14.2产品成本估算14.2.1总成本14.2.2固定成本及变动成本14.2.3经营成本14.3财务评价14.3.1盈利能力分析14.4小结14.5主要计算报表
22、附图序号图纸名称图号1平面布置图F06042-030-012天然气配气站工艺流程图(700吨/天)F06042-040-0013造气工序工艺流程图(700吨/天)F06042-040-0024中低变甲烷化工序工艺流程图(700吨/天)F06042-040-0035脱碳工序工艺流程图(700吨/天)F06042-040-0046压缩工序工艺流程图(700吨/天)F06042-040-0057合成工序工艺流程图(一)(700吨/天)F06042-040-0068合成工序工艺流程图(二)(700吨/天)F06042-040-0079罐区工艺流程图(700吨/天)F06042-040-00810合成氨
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