某城市炼油厂新建装置平面布置设计图

1-10.51.1.1.51.59.14.省测公司勘任公司设有限责计院建筑吉林测量员 庞海泉检查员 赵广会1 : 500N3135.13134.56134.45134.58134.54134.73134.46134.60135.60135.32135.00134.38134.46135.18135.05134.38135.03134.38135.02134.85134.42134.40134.72134.22134.76134.32134.67134.48134.63134.55134.58134.61134.51134.61134.66134.76134.73134.63134.76134.61134.61134.63134.49134.41134.41134.37134.37134.44134.41134.43134.42134.41134.51134.60134.35134.45134.53134.59134.51134.67134.51134.50134.67134.85134.78134.47134.49134.47134.46134.35134.44134.42134.73134.44134.80134.47134.58134.54134.55134.49134.71134.49134.51134.57134.55134.81134.54134.75134.43134.55134.76134.88134.86134.50134.57134.52134.55134.32134.38134.34134.55-0.150.90N135.35N4135.41N5135.22134.21134.29134.24134.15134.29135.22134.83134.97134.83135.28134.14134.17134.13134.28134.23134.30134.31134.30134.36134.85134.80134.96134.31134.41134.41134.39134.34134.32135.50134.18135.26135.05134.74134.82134.77134.01135.34134.38134.35134.45134.33133.91134.46133.94134.77135.27135.17135.65135.27134.29134.27134.29134.27134.76134.03135.38134.81134.12135.41134.91133.91135.21134.40134.47134.33134.23133.95135.21134.87133.78135.17134.24134.98134.21135.16134.26134.26134.26134.93134.96135.07135.17135.26134.97135.11135.40134.32134.30135.00135.22135.34135.21135.28135.27134.28134.36135.30135.30135.40135.25135.56135.33135.16134.36134.34134.86134.78134.64134.74133.51134.32134.75135.09134.64134.36134.34135.15134.92134.41134.93134.17135.10134.67133.67135.16134.56134.95133.67134.28134.22134.12134.25134.27134.37134.75133.57134.81134.84133.57134.79134.31134.23134.27134.32134.28134.36134.30134.24134.52134.52134.36134.32134.36134.37134.44134.31134.34134.37134.35134.47134.37134.37134.37134.37134.38134.33134.40134.89134.41135.02135.01134.90134.90134.41134.33134.91134.94134.34134.33134.30134.27134.34134.29134.27134.29134.27134.28134.17134.24134.41134.77134.88134.94134.94134.34134.73134.24134.35134.45134.37134.51134.88134.97135.08134.35134.46134.93134.47134.55134.72134.75134.72134.72134.57134.72134.58134.57134.52134.54134.41134.30134.30134.35134.35134.31134.27134.33134.27134.28134.32134.29134.31134.29134.30134.31134.25134.17135.00134.94134.90134.91134.771996年版图式。1956年黄海高程系,等高距为0.5米。中国石油前郭炼油厂厂区坐标系。2004年7月全站仪配合小平板仪测图。0.55-0.1515134.95中国石油前郭炼油厂(2万吨/年聚四氢呋喃项目)1：500地形图\P \P 135.18135.19135.11135.20135.19135.09135.18135.08135.25135.17135.11135.29135.28135.25135.83135.71135.99135.89136.67136.87135.65136.88135.61135.78135.60135.84135.56135.44135.79135.26135.26135.30135.29135.28135.2816148x18化学品库B 759.00A -50A -100B 583.000A -65.00A -74.000B 600.00B 600B 650征地红线A -69.000B 588.000B 70来自百度文库B 765.000A -114.000B 750B 765.000A -74.000A -69.000B 770.000A 50A 0罩棚消道通防B 607.000A 36.00034x9B 607.00A 60.20防原料、成品罐区道通191A消B 759.00A -32.00A 6.80B 750.00A 24.00M T B E泵 房A 93.000B 750.000说 明大门及门卫B 770.000A -109.000B 800B 850.000A -114.000B 850A -91.00B 776.50B 812.50A -95.00103B 861.00A -86.00B 900B 917.00A -62.00A -55.50B 975.00年吉林省建筑设计院有限聚四氢呋喃项目勘测定界技术图。中国石油前郭炼油厂现状总图及各院设计条件；聚四氢呋喃项目年黄海高程系本图设计是根据业主提供的责任公司勘测公司测绘的中国石油前郭炼油厂本图坐标系统为中国石油前郭炼油厂厂区坐标系统,高程为路中心坐标，罐区围堤指堤内壁。本图所注建筑物坐标指建筑物轴线交点坐标，道路坐标指道195652cb设计依据：1a均以米为单位。统。坐标与标高地形图进行设计的；1:50020042万吨/年A -23.00B 840.00PTMEG装置639B 861.00A -32.00A 14.00B 771.50B 897.000A -42.500A -18.500B 882.000催化剂库甲类A -42.500B 870.000A -25.000B 934.900B 908.900A -8.000A 21.700B 879.600A 52.000B 870.000dg50dg50加热炉泵 房A 95.000B 870.000循环水场主项名称控制分析楼四氢呋喃装置呋喃装置焚烧炉系统制氢装置PTMEG变配电及设计室外设备原有建筑物厂区围墙原有道路主项编号主项名称序号主项编号大门及门卫综合办公楼化验分析汽车衡化学品库控制室导热油系统冷冻站中间罐区汽车槽车装卸站原料、成品罐区1022311252897191A191B1815641611681523211031511012122192018906639640636161715141312600635504灌装站502450302泡沫站新建建筑物建、构筑物明细表序号设计管架新建道路界区线装置MCC图 例建北北A 71.00B 670.70A 56.80B 635.77装置、罐区及导热焚烧系统等由其它相关设计院负责设计的3边界线内防火间距由各相关设计院负责。此图需经各相关院会签后，方可作为正式文件出版。4防火间距按联合装置考虑。THF及PTMEG装置制氢站B 950B 1000B 1050B 1069.10A -23.00A -59.00B 985.00A -10.00B 965.00B 946.00A -47.00B 985.00A -8.00A 36.00B 681.50B 750.00A 52.70A 66.10B 703.10A -42.00B 781.37焚烧系统用泵252循环泵热媒齿轮注油泵贮油槽电气控制柜加热炉导热油焚烧炉空气预热器风机烟囱906焚烧液贮槽焚烧600（302、151、152）68.5x16.7控制分析楼A 93.00B 840.00冷冻站18.6x10.832.37x10.8泵房4508x4吸水池22332.8x13.35冷却塔37.5x614x4卸车棚10x7卸桶装车棚7x4168泵房、磅房及门卫18116x3.5汽车衡泵 房34x9罩棚A -100B 600A -50A 0A 50A 10004036-82A-Q-1FA0418-08-Z-1/2B 650B 700道通防消道原料、成品罐区191A通防消B 750B 800PTMEG装置泵 房M T B E加热炉dg50dg50B 850103大门及门卫B 900甲类催化剂库639丙类A -62.00B 917.00挤压造粒厂房B 950B 1000丙类颗粒料仓包装及成品库丙类变电间配电间储气囊间制氢站135.4聚合、干燥分析化验办公楼B 1050136.00135.90136.00136.10135.90135.90136.00136.00136.00136.20136.20136.20136.20地形图进行设计的；聚四氢呋喃项目米。本工程装置、罐区及导热焚烧单元总图布置详见其它有关设本图坐标系统为中国石油前郭炼油厂厂区坐标系统,高程为均以米为单位。场地坡度以本工程控制高程地面计院图纸，厂区系统管架排布排布详见热工专业图纸。聚四氢呋喃项目勘测定界技术图。中国石油前郭炼油厂现状总图及各院设计条件；19565423cb的坡度由西南坡向东北。统。坐标、标高及相对尺寸年黄海高程系%%p0.0002.5‰1:500相当于绝对标高136.10绿化用地设计地面标高万吨/年设计室外设备原有建筑物厂区围墙原有道路年吉林省建筑设计院有限新建道路人行场地铺砌厂区围墙车行场地铺砌界区内、外道路设计依据：本图设计是根据业主提供的责任公司勘测公司测绘的中国石油前郭炼油厂61a45321序号宽说 明2004绿化挡土墙4956m94002123009085004000(m)工程量明细表人行场地铺砌名 称规 格设计等高线设计管架占地面积(m )2图 例新建建筑物界区线建北北备 注136.10136.00136.0135.30136.00135.90136.00136.00136.00136.00136.10136.00136.10136.10135.90135.90136.10135.90135.90136.10135.75135.90135.90135.90136.10136.10136.10136.10136.10136.00135.90135.88136.10136.10135.75135.30135.30135.70135.80136.20135.82136.20136.20136.20135.85136.10136.10135.82136.00136.00136.00136.00135.856.06.06.06.06.06.06.06.06.06.06.04.08.050450x16灌装站J-33J-34J-43J-72J-55J-54J-53J-52J-76J-77J-74J-73J-75J-47J-49J-51J-50J-48J-46J-44J-45J-08J-07J-09J-10J-11J-12J-26J-25J-24J-21J-22J-23J-19J-20J-15J-16J-14J-35J-29J-63J-31J-32J-30J-13J-67J-69J-68J-70J-71J-65J-64J-66J-39J-42J-40J-41J-38J-36J-37J-27J-28J-17J-18J-06J-05J-03J-01J-02J-56J-61J-62J-60J-59J-58J-57J-04混凝土铺砌融解室消防通道消防通道B 831.37A -58.00A -80.00B 965.00B 804.50A -101.00A -101.00B 850.00B 777.00A 25.00B 620.35A 93.00A 62.00B 604.50A 37.00B 777.00MMMMMMMMM上P29R301636预留空地THF装置F320A/BP320P315F312A/BD320E303P314E302E316D317D315AP319D315BP313D319T303UPD326D325P-310BT302P312P-301P101F103A/BUPP112D112T101E101D118P413D218635D417F401F402P217P417D217P118P102F104A/BP113D114D113P114P412P419%%UR201P218P218AD116P116D218AD416P416P911D911E118E911D413D210P414D230E230E231P202T202E206E204P505P210T206T204F413E102T102卸料区D412X413D414D505E202围堰高1000D310UPF5X5P-310AD10AD10B191B%%UP10A%%UF10%%UP10B15x8T603E203P603污水坑(待定）E603P214UPP205P203E511E205T205T20321x19640D214脱盐水脱盐水A 79.80B 692.60A 93.00B 648.80P-2106P-2104AP-2104BP-2201AP-2201BP-2101AP-2101BP-102 ?P-2202P-2203P-2204AP-2204BP-2103AP-2103BP-2102136.10136.10136.10136.10V=400 D=7.75mV=400 D=7.75mV=400 D=7.75m四氢呋喃贮罐 甲BA -60.200B 606.000H=9.125m2223V=400 D=7.75m四氢呋喃贮罐 甲BH=9.125mTK-102AMLKD=8.72mV=600H=9.125mMH=9.125mTK-102BP-2301AMMMMMM泵房B(高度5米)导轨导轨F-2301A/BF-2301C/DD=8.72mP-2301DP-2301FP-2301EP-2301HP-2301CP-2301BV=600LKTOS EL 6000KTOS EL 6000TK-101CV=3000预留糠醛贮罐V=3000糠醛贮罐TOS EL 7500(上层)TOS EL 6000(下层)醋酸甲酯贮罐 甲B低聚物贮罐 丙类V=300 D=6.78mV=300 D=6.78m降解THF贮罐 甲B醋酸酐贮罐 乙BV=200 D=6.73mTOS EL 6000(上层)TOS EL 4000(下层)TK-2103A原料甲醇贮罐 甲B四氢呋喃贮罐 甲BH=8.38mV=300 D=6.78mTK-2101JIH=8.38mV=300 D=6.78m原料甲醇贮罐 甲BTK-2103BFHG甲醇贮罐 甲BV=200 D=6.73mH=6.10mTK-2201EDMMMCMMMMMM泵房A(高度5米)TK-2301GV=300 D=6.8mD=8.72mTK-2301DTK-2301E防火堤高度1.5米V=600PTMEGPTMEGV=600PTMEGTK-2301ATK-2301BH=8.38mTK-2202TK-2203H=8.38mTK-2204D=8.72m丙类贮罐丙类贮罐PTMEG丙类贮罐V=600丙类贮罐PTMEGJITK-2301C丙类贮罐D=8.72mFHGTK-2301FPTMEGV=300 D=6.8mA 6.800H=6.10mTK-2102B 640.000MMMMMM防火堤高度1.5米贮罐 丙类TOS EL 6000(上层)TOS EL 4000(下层)贮罐 丙类PTMEGEDTOS EL 6000(下层)TOS EL 7500(上层)C丙A糠醛贮罐TK-101BV=3000糠醛贮罐V=3000丙AD=17mJID=17mFHGTK-101ATOS EL 7500(上层)TOS