09加氢改质操作规程附录B.doc

Q/JSH J0401502009原料油进装置硫化剂自泵-121来原料油自SR-101/1.2来开工循环油去热低分100-P-108-26A1B1 原料预处理部分管道及仪表流程图-1放空总管350-RV-100/1-1.6A150-GN-101/1-1.6A1100-RV-105-1.6A150-GN-101-1.6A1氮气PV102BPY102BFOPY102APV102AFCPG105PT102PIC10250-GN-117-1.6A1 D-102原料油缓冲罐DN 5080-RV-104-1.6A1PSV102放空总管350-RV-100/1-1.6A11/P1/P1/PPY101BPV101BFOFC50-GP-109/1-1.6A150-GP-109-1.6A11/PPY101APV101A燃料气PIC101PT101LG102A-D80-RV-103-1.6A1PSV101PC10450-RV-102-1.6A1DN 50LT101LIC1011/PLY101LV101FIQ110FT110耙式流量计FC100-P-102-2.5A1取样25-LS-101-2.5A125-SCW-101-1.6A3蒸汽凝结水25-LS-103-2.5A1蒸汽LI102LT102蒸汽25-LS-104-2.5A1150-P-101-1.6A1DN20DN20开工循环油自A-106来原料油去污油罐 DN20DN20100-P-178-2.5A180-P-179-2.5A1DN50DN20DN25150-P-101-1.6A1DN20PG102PG106DN20 P-101/2原料油升压泵 P-101/1原料油升压泵 P-102/1原料油进料泵 P-102/2原料油进料泵DN20DN25150-P-101/1-1.6A1150-P-103/1-1.6A1100-P-102/1-2.5A1100-P-108/1-2.5A1100-P-104/1-2.5A1氮气25-CL-103-1.6K1100-P-106-2.5A1100-P-182-2.5A1100-P-104-2.5A1LT103LIC1031/PLY103LV10325-LS-102-2.5A1蒸汽25-SCW-102-1.6A3凝结水 D-101原料油脱水罐FI140FE140FT140PG103DN 20DN 20150-P-181-2.5A125-LS-166-2.5A1蒸汽蒸汽25-LS-105-2.5A1 P-120开工循环泵LG101A-ELG101F100-P-183/1-2.5A1DN50DN50100-P-183-2.5A1蒸汽100-P-104-2.5A125-LS-106-2.5A1DN50150-P-103-1.6A1100-P-180-2.5A1100-P-104-2.5A1DN25DN20DN20PG107DN20PE101PT101DN20150-P-107-2.5A1DN20DN5PG108PV101PY101PIC101DN25FOPG11280-P-109-2.5A180-P-109/1-2.5A1限-102/1限流孔板限-102/1限流孔板DN25PI103AFSIL103PIC103PY103FSY103PT103BPT103APV103PV102PY102PT107PI107限-101/2限流孔板限-101/2限流孔板PT102PE102PG109100-P-180/1-26A1150-P-107/1-2.5A1原料油去混氢点原料油去E-104 P-101/3原料油升压泵原油自E104来SR101/1原 料 油 过 滤 器SR101/2原 料 油 过 滤 器净化风放空污油总管B2 原料油过滤部分管道及仪表流程图-2PDSV10380-P-106/3-2.5A1100-P-106-2.5A1100-P-106/1-2.5A1100-P-106/2-2.5A1原料油去D-102DN50DN50DN50DN50DN50DN5050-LS-107-2.5A1蒸汽蒸汽50-LS-108s-2.5A1DN50DN50DN50DN50DN50DN50DN50IPDT103PDI103100-P-105/2-2.5A1100-P-105/1-2.5A1DN25DN20100-P-105-2.5A150-SLO-104/1-2.5A180-SLO-103-2.5A150-SLO-104-2.5A180-SLO-103-2.5A180-SLO-103/1-2.5A1不合格油出装置减底油返回开工循环轻油开工循环油不合格轻质油不合格中质油短循环线减底油出装置去SR101/1,2减底油自P106/12来原料油自P101来A 106/1-4重质油产品空冷器E104减底油/原料油换热器B3 原料油换热流程图-3100-P-163-4A1100-P-105-2.5A125-LS-110-2.5A1蒸汽80-P-164-4A1100-P-166-4A1T1180LY208FC25-SLO-106-2.5A125-LS-109-2.5A1蒸汽25-SLO-105-2.5A1污油总管100-SLO-100-2.5A1100-P-104-2.5A1100-P-166-4A125-LS-162-2.5A125-LS-163-2.5A125-LS-164-2.5A125-LS-165-2.5A1蒸汽蒸汽蒸汽蒸汽TC101APC115APC115BTC101BTY107TC102APC116APC116BTC102BTY108污油总管100-SLO-100-2.5A1TI107ATT107TIC107TI108ATT108TIC108100-P-166/1-4A1100-P-167-2.5A150-P-168-2.5A1100-P-178-2.5A150-P-199-2.5A150-P-154/1-2.5A180-P-161/1-2.5A1100-P-198-2.5A1100-P-169-2.5A1蒸汽采样FIQ111FT111A1 DW-32 DW-47 A4 D-110 注缓蚀剂罐25-P-184/1-1.6A125-P-184-1.6A1DN20DN20PSV108/2PSV108/1DN20DN20DN15DN15MMPG118PG117DN20DN2025-P-185-2.5A125-P-185/1-2.5A1DN25DN25LG104LG103T1109BT1109A25-P-184/1-1.6A1蒸汽25-P-185-2.5A125-LS-112-1.6A125-P-184-1.6A125-SCW-103/1-1.6A325-LS-111/1-2.5A140-SW-101-1.6A325-SCW-103-1.6A325-LS-111-2.5A1凝结水蒸汽P-115/2P-115/1去C101凝结水蒸汽软化水自总管来P-115/2B4 原料油注缓蚀剂流程图P-115/1去C101凝结水蒸汽软化水自总管来注缓蚀剂泵注缓蚀剂泵注缓蚀剂泵 混氢原料去R-101冲洗水B5 加热炉部分管道及仪表流程图-5PG125蒸汽去C10180-LS-120-4A1蒸汽去C102蒸汽去C103蒸汽去C104蒸汽去C105蒸汽去C10650-LS-121-4A140-LS-122-4A140-LS-123-4A140-LS-124-4A140-LS-125-4A1混氢原料自E101来蒸汽100-LS-117-2.5A1100-LS-118-4A1TI183100-P-187-4A1PY104I/PTI101ATI101PG125PT104PIC104TIC101TIC102TT102TI102ATI185A-FPG130200-P-112-42K1200-P-112-42K150-RW-103-1.6A3200-P-186-4A1DN100引至高处放空DN100DN25DN100DN50D-117烧焦罐PG129DN25PG132DN40引至高处放空F-101阻火器M-105/1.2PG134DN20引至高处放空PG124PT117PI117TI182200-P-122-42K1DN20蒸汽100-LS-114-2.5A1FE114AFT114AFIQ114A空气FE114BFT114BFIQ114BPG126PT118PI118TI186TI187ABTI187CDTI187EFPG128蒸汽50-LS-116-2.5A1PG131PAL119PS119F-101长明灯阻火器M-106/1.2PG13320-GP-105-1.6A10.23mpa-0.1mpaFC100-GF-103-1.6A1 TV101TSV101TY101FSV101I/PSI来自HC-301（DW30）FSLL-313(DW30)FSLL-103(DW21)FT113FIQ113FE113100-GF-103-1.6A1燃料气自D115来 F-101反应进料加热炉 M-109F-101对流蒸汽消音器B6 加氢处理反应部分管道及仪表流程图-6PCV117200-P-112-42K1混氢原料自F101来蒸汽40-LS-167-2.5A125-GH-111/1-16A1PI120PT120PG135引至顶层平台25-GH-111/1-16A1200-P-112-42K1DN25TI140TI110ATI110BTI110CTI142A-CTI113ATI113BTI113CTI146TI114ATI114BTI114C1TI117ATI117BTI117CTI147TI118ATI118BTI118C2TI121ATI121BTI121CTI1523TI122ATI122BTI122CTI125ATI125BTI125CTI156DN25TI157200-P-113-42K125-GH-124-42K1/16A1PG139FCV11825-GH-111/2-16A1TI154A-CTI155A-CPDT108PDI108PG136TI143TIC104ATY114TY104ATV104A25-GH-121-42K1/16A1引至次层平台FI115AFT115A50-GH-111/3-16A1/42K1TI145A-CTY118TIC104BTY104BTV104BFI115BFT115B1250-GH-111/4-16A1/42K1TI149TI150A-CTI15150-GH-111/5-16A1/42K13TY122TIC104CTY104CTV104CFI115CFT115C涡街流量计涡街流量计涡街流量计25-GH-122-42K1/16A1引至次层平台25-GH-123-42K1/16A1引至次层平台25-GH-124-42K1/16A1引至次层平台PDT109PDI109PG137PDT110PDI110PG138PDI111PDT11180-GH-111-16A1/42K125-GH-112-16A180-GH-111-16A1/42K1冷氢冷氢K-102来200-P-113-42K1DN25DN25DN25DN25TI158PG141PG140TV103TY103I/PTIC103TI103ATT103200-P-122-42K1200-P-111-26K1加氢处理产物去R-102200-P-114-26K1反应进料自E-102来冷油付线反应进料去F-101DN80CSC R-101加氢处理器 E-101加氢处理反应产物/反应进料换热器B7 加氢精制反应部分管道及仪表流程图-7PI122200-P-11-26K1加氢处理产物自E101来25-GH-127-26K1PT122PG142PDI113DN25PDI112PDT112PDT113PG143FCV11925-GH-112-16A1TI160TI126ATI126BTI126CTI162A-C至次层平台25-GH-125-26K1/16A1至次层平台25-GH-125-26K1/16A125-GH-112/2-16A1TI129ATI129BTI129CTI166A-CFCV120TI130ATI130BTI130CTI133ATI133BTI133CTI167A-CTI168PG144FCV12125-GH-112-16A1冷氢蒸汽40-LS-168-2.5A125-GH-112/1-16A1DN25200-P-115-26K1200-P-115-26K1 R-102加氢精制反应器DN25DN25DN25DN25PG145200-P-110-26A1TI136混氢点TY105I/PTIC105TT105TI105A200-P-116-26K1150-GH-108-26A1-ST100-P-108-26A1冷油付线原料油自P102来混合氢自E103来加氢精制产物去D103TV10580-P-108/2-26A1/26K1CSCDN80TI170PC146反应进料去E101200-P-111-26K1 E-102精制反应产物/反应进料换热器B8 热高低分部分管道及仪表流程图T1172T1171150-GH-108-26A1-ST混合氢去E-102混合氢除盐水自P-103/1.2来除盐水去A-101热高分气去A-101加氢精制反应产物自E-102来开工循环油自P-120100-P-182-2.5A1200-P-116-26K1200-P-116-26K1150-P-118-26A140-SW-105-16A140-SW-104-16A1150-GH-107-16A1-STT117440-KL-106-10A1 M-102碱液混合罐碱液自P-118来 E-103热高分气体/氢气换热器LI117AL1117BILT117DN50-26K1DN50-26K1排污口80-P-123-26K1/4A1连通管DN80LG105BLG105ALG105CLT104LT116ILALL116ALALL116BLIC104sLY104AI/PLSV104ALV104AFCLY104BI/PsLSV104BLV104BFC D-103热高压分离器LI118LT118400-RV-100-2.5A1DN80PSV103100-RV-106-4A1150-RV-107-1.6A1PC14850-GN-107-1.6A1氮气连通管DN80排污口LG106ALG106CLG106BLG106DLT105LIC105LY105I/PLV105100-P-126-4A1 D-105热低压分离器冷却水15-P-126/1-4A125-PW-109-1.6A3FC取样15-P-126/2-4A1DN15DN25DN1580-P-124-4A1热低分气去A110100-P-126-4A140-P-121-4A1100-P-198-2.5A1100-P-165-4A1热低分油去F102冷低分油自D106来短循环线自A106来短循环线去A106 SC-101取样冷却器T1137100-GH-110-16A1循环氢热高分气软化水150-P-118-26A140-SW-105-16A1PG149TI175DN100DN100DN100100-RV-109-2.5A1DN80DN80DN80DN80DN80DN80DN80DN80DN80DN80DN80DN80DN80DN80DN80DN80DN100DN100DN150DN150DN100DN100DN150DN150TI138ATI138BTI138CTI138DTI138ETI138FTI138GTI138H150-P-119-16A1自流管线，不许有袋形PC154TY134I/PTI177TIC134TT134TI176150-P-119-16A180-P-124-4A1热低分气自D105来DN80DN80DN80TY135DN50-16A1TIC135TT135TI178PG153DN15取样40-KL-107-1.6A6循环碱溶液去D120含硫污水出装置40-ASW-101-1.6A5DN2080-P-125-4A1PSV104/1PSV104/240-RV-108-16A1400-RV-100-1.6A1TI179150-GH-105-16A1150-GH-105-16A1循环氢取样PG150PT105PIC105去PY-105(DW-29)LI119LALL115BILALL115ALT119LG107ALG107BLT115LT117LIC107LY107AI/PLSV107AsLV107A40-P-120-16A1/4A140-P-121-4A1DN50-16A1LT106LG108LIC106LY106AI/PLY106BI/PLV106AFCFCLV106BFCLSV107BLY107BLV107BI/Ps400-RV-100-1.6A1放空总管DN100100-RV-111-1.6A125-ASW-102-4A1/1.6A125-GN-106-1.6A1TI139PSV105FT116FIQ116PIC106PG152PY106FCPV106DN15取样40-RV-112-4A1引至高分处放空40-GS-101-4A1PT106I/PLT 120LG 110LI 120LG 109LT 108LY 108I/PLV 108FC25-P-121/1-4A1LICS 10880-RV-110-4A1取样DN25DN1540-P-121-4A1冷低分油去D105出口 D-106冷低压分离器 D-104冷高压分离器 A-110热低分气体空冷器B9 冷高低分部分管道及仪表流程图含硫气体出装置MMHC301B放空总管400-RV-100-1.6A1PHS301150-RV-113-2.5A1HC301APY301AI/PPV301APT301PIC30180-RV-113-2.5A1100-CN-114-16A1/2.5A1PY301BI/PPV301BFC氮气FIQ308FT308FE308限-104DN8050-PA-102-1.6A3非净化风氮气FIQ309FT309FE309工业氢自装置外来80-GN-103-2.5A1150-GH-101-2.5A1FT310FIQ310涡街流量计TI310150-GH-101-2.5A1200-SLO-100-1.6A1污油总管25-SLO-107-2.5A1LG301LT301LI301PG301PT301PIC302A100-GH-104-2.5A1150-GH-102-2.5A150-GN-112-2.5A1氮气40-RV-114-2.5A1PSV106100-RV-115-1.6A1400-RV-100-1.6A1放空总管PLS302I/PPY302FCPV302FIQ306FT306FE306限-103DN25采样40-GH-104/1-16A180-GH-103-16A1PIC302BPT302BFIQ307PT307FE307PV105PY105I/PFC接PIC-105（DW28）80GH-103-16A1新氢400-RV-100-1.6A1400-RV-100-1.6A1放空总管放空总管PG302A50-GN-112-2.5A1150-GH-102-2.5A180-GH-103-16A1PG302B40-GH-104-16A1PG302CPSV107/150-GN-112/1-2.5A1150-GH-102/1-2.5A180-GH-103/1-16A140-GH-104/1-16A1100-RV-117-2.5A1100-RV-119-2.5A1PG303APG303BPG303CPSV107/2 K-101/1 新氢压缩机 K-101/2 新氢压缩机 D-121新氢压缩机入口缓冲罐B10 新氢压缩机部分管道及仪表流程图MMB11 循环氢气及部分管道及仪表流程图蒸汽100-LS-126-2.5A1150-LS-127-2.5A1PG304停原料泵P-102（DW-21）去TSV101炉F101熄火（DW-24）停新氢压缩机K101（DW-29）紧急放空IPG305PIC303PY303I/PPG308PT303PV303FCDN8080-GH-113-16A1100-GN-108-1.6A1HC301HY301I/PHV301AHV301B限-105/1.2100-RV-121-16A1400-RV-122-2.5A1400-RV-100-1.6A1放空总管400-RV-100-1.6A1放空总管FT302FE302FY302FV302I/PFIC302PG306FC50-GH-114-16A150/100-RV-123-16A1/2.5A1至氢提浓装置50-GH-201-10A1产品氢至新氢机50-RV-201-2.5A1尾气至燃料气150-GH-106-16A1PG307循环氢自D104来150-GH-105-16A1SN305150-GH-106-16A1FE301FT301FIC301FE312FT312FIC312FY301I/PFV30180-GH-110-16A1循环氢80-GN-114-16A1FT311FI311FE311LT302ALI302ALG302LT302BLT303LI302BLAHH303ALAHH303BI高液位停机PG309再生氮气去GH10180-GN-114-16A1-2.5A125-SLO-108-2.5A1200-SLO-100-1.6A1污油总管FIQ313BFI313AIFSLL313FE313FT313至F101炉F301熄火（DW-24）150-GH-107-16A180-GH-103-16A180-GH-111-16A1混合氢新氢自K101/1.2来急冷氢R301150-GH-107-16A1氮气50-GN-113-4A1PG310A50-GN-113-4A1150-GH-107-16A1PG310B100-RV-132-16A1PG310C80-GN-110-16A1400-RV-100-1.6A1放空总管150-RV-133-16A1PSV113/1PG311APG311CPG311BPSV113/2400-RV-100-1.6A1放空总管150-GN-106-16A150-GN-113/1-4A1150-GN-106/1-16A1150-GH-107/1-16A1100-RV-134-16A180-GN-110/1-16A1150-RV-135-16A1 K-102/1循环氢压缩机 K-102/2循环氢压缩机 D-122循环氢压缩机入口缓冲罐 M-103加氢抽空器 M-110抽空器蒸汽消音器 M-103氮气消音器B12 常压塔进料加热炉部分管道及仪表流程图低分油自D105来100P1264A1FIC250FE250FT250蒸汽50LS1312.5A1TI222PG202I/PPY201TI201ATT201PG203PG201PT226TI221TI225ATI225BTI225CPG204AF103减压进料炉PT201PIC201TIC201TI226AFTIC202PG208TT202TI202APG204B注：烘炉排空用低分油去C101150P1354G1DN25 14至管末端接出至高处放空PG205DN20 至管末端接出至高处放空PG207F102阻火器M107/1、2F102常明灯阻火器M108/1、2PS227PAL22750LS1332.5A1蒸汽18*4 14PG209PG206I/PTY201FC80GF1041.6A1TV20120GF1061.6A10.23mpa0.1mpa燃料气自D115来80GF1041.6A1FE220AFT220AFIQ220API226DN20 B13 常压塔部分管道及仪表流程图25P1852.5A1缓蚀剂自P115/1、2来FE202FT202FIC202FY202FV202I/PTI261蒸汽自F101来80LS124A1LG201AD1700LT2016000LIC201LAHLALLY201LV201I/PFC25LS1282.5A1蒸汽DN50DN25DN20150P1344A1PG211B150P1334A1P104/1常压塔底泵100P1344A1常底油至F10380P1932.5A1柴油侧线汽提塔进料TI205ATT205TIC205FIC201FOFY201FV201FT201PG213TI248TI262TI260TI247PG212PG210350RV100/11.6A1200RV1261.6A1放空总管DN80PSV109PT225PI225PAHPAL2625150P1354G1低分油自F102来FC17168721C101常压汽提塔200P1272.5A1C101塔顶油气去A102I/PFE20150P1311.6A1C101塔顶回流自P105/1、2来150P1942.5A1柴油侧线汽提塔蒸汽50P1311.6A125LS1292.5A1蒸汽DN50DN25DN20DN20150P133/14A1150P1334A1150P134/14A1P104/2常压塔底泵PG211BPG214常压柴油侧线汽提塔蒸汽150P1942.5A1HILY212ALV212ATI252B80P1932.5A1HI常压柴油侧线汽提塔进料FALFIC203FY203FV203FT203FE203过热蒸汽40LS1254A1HIC106常压柴油产品汽提塔1700LG202SDPG2151700LT212ALIC212ABLAHLAL40P196/22.5A1HITE257TI257HIC201AHY201AHV201A蒸汽25LS1132.5A1HIA109柴油产品空冷器PG217TG201TY206TIC206TI206ATT206取样40P1972.5A1靶式流量计FT204FY204FV204FIC204轻柴油产品出装置40P1972.5A150P196/12.5A1DN20PG216ADN25DN5080P195/12.5A1P116/2柴油产品泵I/PI/PFCFCTALNOTEDWSDN25DN20DN2050P1962.5A180P1952.5A1PG216BP116/1柴油产品泵I/PI/PFCI/PDN4040P197/12.5A1不合格油轻柴油开工至减顶回流B14 常压柴油侧线汽提塔管道及仪表流程图B15 常压塔顶回流部分管道及仪表流程图DN200DN1500A102/1、2常压塔顶空冷器PG219TG203塔顶油自C101来200P1272.5A1DN1500DN150DN150DN150DN150DN1500DN1500DN200DN200DN200PG218TG202TG204DN40TG206DN25TH205新鲜水80RW1071.6A380RW1061.6A3循环热水循环冷水150P1261.6A1DN1525SOW1011.6A550P1311.6A1循环冷水塔顶油回流去C101取样FCLV202E105常压塔顶水冷器LY202LIC202I/PLT202LAHLALLG203HYHYDN40I/PDN200350RV100/11.6A1150P1291.6A1DN50PSV109/1D108常压塔顶回流罐LG204LT203LIC203LY203I/PLV203FIQ222LV203PG220PT203PIC203PY203PV203I/P涡街流量计350RV100/11.6A150GS1031.6A150GS1021.6A1干气出装置DN20取样40P1771.6A1不合格油涡街流量计DN15取样FCFOPG221ADN20DN20P105/1塔顶回流及产品泵新鲜水新鲜水凝结水蒸汽40GN1051.6A1FIQ221FT221放空总管25SCW1041.6A325LS1302.5A180P1301.6A125GN1051.6A1FT22240P1321.6A1粗汽油出装置PG221BDN20P105/2塔顶回流及产品泵DN4080P131/11.6A180P130/11.6A1B16 减压塔进料加热炉部分管道及仪表流程图TI228PG222PY202I/PFE251FT251FIC251蒸汽100P1344A1常压塔底自C101来50LS1322.5A1F103减压进料炉PG230PT229PI229TI227DN25 12注：预留管段烧焦等用TI231APG224APT202TI203ATT203TIC203TIC204PIC202PG223TI231BTI231CTI232AFPG229TT204TI204APG224B蒸汽50LS1582.5A1DN25 12注：预留管段烧焦等用常压塔底油去C102300P1364A1DN25 至管末端接出至高处放空PG225PG226PG228PG227PS230PAL230至管末端接出至高处放空DN20 F103阻火器M113/1、2F103常明灯阻火器M114/1、2FCTY203I/PTV20380GF1081.6A18