260加氢工艺手册

1、4、装置原则工艺流程图0.8MPa氮气新氢进装置去火炬4.0Mpa氮气新氢去D-104顶新氢压缩机K-101O新氢机入口缓冲罐D-107-m环水去连续重整PSAM-II废氢排放去PS鼻新氢返回冷却器E-104-反应器R-101原料罐缓冲罐D101、D102循环氢压缩机K1021.0Mpa蒸汽卜向D401_A>紧急泄压去D-401循环机入口缓冲罐D-108循环氢脱硫塔C-101贫胺液罐D-112凝聚器D-109-3E203不合格油出装置长循环油自柴油出装置来瓦斯自D404顶瓦斯线来反应进料泵P-102/AB原料油升压泵P-101/AB生成油/混氢换热器E-101*产品柴油出装置C)生成油/

2、混氢换'热器E102/ABC轻燃出装置热高分气/混氢换热器E-103热局分气空冷器A-101热高分D-103酸性水出装置xA石脑油出装置贫胺?泵P-104胺液自软化水自装置外来注水罐D-110冷高分D-105低分气去PSA母塔顶回流C201顶空冷器A201£-X产品分储塔C202C202顶空冷器A202热低分D-104塔顶后冷器E201脱氧水净化瓦斯去管网低压蒸汽去管网/,低压蒸汽炉后放大气k重沸炉11F201$原料油/产品柴油换热器E203胺液自C101来低压蒸汽自管网来脱氧水0蒸汽发生器E204产品柴油空冷器A203酸性气冷去嚅E301去柴油泵P-2031Os原料油自P1

3、来D-501柴油/分偶塔进料换热器E2051贫胺液水0'冷器E302贫胺?去D112原料油去SR-101酸性气分'液缶DD301贫胺液进料贫胺液罐泵P-301D304第五节：装置主要设备(1)机泵类:序号编号名称型号介质(m3/h)温度(C)压力MPa(G)正常/额定正常/最高进口出口1P-101/A原料油升压泵ZA150-3315柴油387/42550/600.21.222P-101/B原料油升压泵ZA150-3315柴油387/42550/600.21.223P-102/A反应进料泵GSG150-360/1d+8s柴油401/454120/1350.210.34P-102/

4、B反应进料泵GSG150-360/1d+8s柴油401/454120/1350.210.35P-103/A反应产物注水泵LG222-16/948-132-172mDT除盐水14/1650/0.0049.486P-103/B反应产物注水泵LG222-16/948-132-172mDT除盐水14/1650/0.0049.487P-104/A贫胺液升压泵TDJ120-110X8贫胺液110/12155/0.29.08P-104/B贫胺液升压泵TDJ120-110X8贫胺液110/12155/0.29.09P-106/A反冲洗污油泵ZA40-2250污油30/100/13500.610P-106/B反

5、冲洗污油泵ZA40-2250污油30/100/13500.611P-201/A重沸炉泵ZE200-5560柴油、汽油476/523219/2500.61.2112P-201/B重沸炉泵ZE200-5560柴油、汽油476/523219/2500.61.21序号编号名称型号介质a#(m3/h)温度（C）压力MPa(G)正常/额定正常/最高进口出口13P-202/A硫化氢汽提塔顶回流泵：ZA40-2250汽油10/1540/450.51.0714P-202/B硫化氢汽提塔顶回流泵：ZA40-2250汽油10/1540/450.51.0715P-203/A精制柴油泵ZE200-5400柴油483/5

6、30236/2600.11.4916P-203/B精制柴油泵ZE200-5400柴油483/530236/2600.11.4917P-204/A汽提塔顶回流泵ZE80-3400汽油66/9350/600.11.318P-204/B汽提塔顶回流泵ZE80-3400汽油66/9350/600.11.319P-205/A汽提塔顶冷凝水泵ZA25-0200冷凝水6/7.250/600.10.6820P-205/B汽提塔顶冷凝水泵ZA25-0200冷凝水6/7.250/600.10.6821P-206/A缓蚀剂泵J-Z800/1.3-R1-IV缓蚀剂0.2/0.4/0.8常温01.322P-206/B缓

7、蚀剂泵J-Z800/1.3-R1-IV缓蚀剂0.2/0.4/0.8常温01.323P-301/A贫胺液进料泵ZA100-3315贫胺液138/15955/6001.0424P-301/B贫胺液进料泵ZA100-3315贫胺液138/15955/6001.0425P-302/A再生塔底宗ZA40-2250贫胺液150/165122/1300.10.6726P-302/B再生塔底宗ZA40-2250贫胺液150/165122/1300.10.6727P-303/A冉生塔顶回流泉XDF525X3酸性水5/640/500.10.6728P-303/B再生塔顶回流泉XDF525X3酸性水5/640/50

8、0.10.6729P-304胺液配制回收泵ZA40-1200胺液、H2S20/3040/6000.53序号编号名称型号介质(m3/h)温度（C）压力MPa(G)正常/额定正常/最高进口出口30P-401抽油泵ZA40-2250轻油/3050/800.10.68831P-402地下污油泵TR32-250污油20/2550/700.10.68832K101/A新氢压缩机4M50-30/22-100-BX氢气/3670056/2.210.233K101/B新氢压缩机4M50-30/22-100-BX氢气/3670056/2.210.234K102循环氢压缩机BCL457氢气/18000056/7.9

9、9.935K104引风机Y473No16D烟气/130390150/2400.00236K103鼓风机G4-73No14D空气/7994420/42.10.0022、塔器类:工艺编号设备名称内径*长度*壁厚mm主体材质设计温度C操作温度C设计压力MPa操作压力MPa9.3介质容积3m1R-101加氢精制反应器4213X18118X(125+6.5)2.25Cr-1Mo-0.25V+E309L+E3474354209.8油气、H2、H2S291.62C-101循环氢脱硫塔2200X20709X7816MnR150608.958.5循环氢、H2S、胺液、水63.24p工艺编号设备名称内径*长度*壁

10、厚mm主体材质设计温度C操作温度C设计压力MPa操作压力MPa0.9介质容积3m3C-201硫化氢汽提塔1400/2800/3400X32000X(12/22+3)/26/3020R+0Cr132602301.08油气、水、氢气、硫化氢1794C-202产品分储塔1400/3200X45600X12/2020R3303100.50.2油气、水、油205.45C-301酸性气脱硫塔1400X24600X1420R1006510.65胺液、轻给H2S15.466D-101原料缓冲罐4600X10600X2216MnR100500.580.2柴油204.97D-102滤后原料缓冲罐4600X9000

11、X2216MnR1701500.980.6柴油175.058D-103热高压分离器3400X17375.2X(100/68+6.5)2.25Cr-1Mo+E309+E3472602409.258.8油气、H2、H2S107.29D-104热低压分离器3400义15606X(44/30+3.0)2.25Cr-1Mo-V+E309+E34726024031.3油气、H2、H2S107.110D-105冷高压分离器2600X11553X92/6215CrMoR(H)+0Cr18Ni10Ti150808.958油气、H2、H2SH2038.711D-106冷低压分离器2400X9963X3216MnR

12、1205032.45油气、H2OH2S31.74p工艺编号设备名称内径*长度*壁厚mm主体材质设计温度C操作温度C设计压力MPa操作压力MPa2.5介质容积3m12D-107K101入口分液罐1800X6250X2620R100403H2、甲烷9.1613D-108K102入口分液罐2600X94444X9216MnR1501308.958.5循环氢27.614D-109凝聚器800X3600X4616MnR1501308.958.5循环氢2.115D-110反应产物注水罐1600X9570X820R100500.40.1除盐水11.316D-111/A安全水封罐420X1713X820R80

13、600.280.1水、氮气0.13317D-111/B安全水封罐420X1713X820R80600.280.1水、氮气0.13318D-112贫胺液缓冲罐3200X15186X2020R100600.780.6胺液8119D-113/A硫化剂罐1200X6150X820R100400.80.5硫化剂4.52420D-113/B硫化剂罐1200X6150X820R100400.80.5硫化剂4.52421D-114烧焦罐1200X3600X820R350330常压常压烟气、水2.7122D-115反冲洗污油罐小1400X300020R1701350.350.05污油23D-116蒸汽分水罐80

14、0X2150X1220R3002801.61.2蒸汽、水0.53624D-201硫化氢汽提塔顶回流罐1600X4832X1620R100701.080.9油气、水、硫化氢9.7325D-202产品汽提塔顶回流罐1600X4824X1220R100600.40.2汽油、水9.7326D-203/A缓蚀剂罐1000X4250X820R8040常压常压缓蚀剂2.356工艺编号设备名称内径*长度*壁厚mm主体材质设计温度C操作温度C设计压力MPa操作压力MPa常压介质容积3m27D-203/B缓蚀剂罐1000X4250X820R8040常压缓蚀剂2.35628D-301酸性气分液罐1600X6200X

15、1420R1004010.8硫化氢、氨、水9.2529D-302气体聚结器500.7轻焰H2、H2S30D-303富胺液闪蒸罐2600X8336X1820R1006510.8胺液42.231D-304贫胺液沉降罐5000X8053X1820R90常压胺液14732D-401放空分液罐4000X12036X1820R1701500.580.4油气、氢气、水142.733D-402地下污油罐1600X4820X1020R1701500.680.5污油9.1134D-403净化风罐1400X6400X820R100350.780.5风6.8835D-404燃料气分液罐1200X5600X820R10

16、0700.630.45燃料气3.936D-405地下废胺液罐800X2631X1020R100600.980.5废胺液1.1437D-4061.0MPa蒸汽分水器800X2150X1220R3002801.61.2蒸汽、水0.53638D-501汽包1800X6520X2820R2501911.71.5蒸汽、水31.539D-503排污扩容冷却器1400X3950X816MnR200100常压常压蒸汽、水4.53、冷换类:设备名称工艺编号设备型号管程介质壳程介质设计参数管程压力(MPa壳程压力(MPa管程温度(C)壳程温度(C)1反应产物和混氢换热器E-101DFU1300-326-9.45/

17、9.9-3/19-2柴油、轻峪H2、H2S轻焰H2、H2S9.459.94353952反应产物和混氢油换热器E-102/ADFU1600-1163-9.45/9.9-6.64/19-2油H2油H29.459.94353953反应产物和混氢油换热器E-102/BDFU1600-1163-9.45/9.9-6.64/19-2油H2油H29.459.94353954反应产物和混氢油换热器E-102/CDFU1600-1163-9.45/9.9-6.64/19-2油H2油H29.459.93402905热高分与氢气换热器E-103DFU1300-470-9.45/10.5-4.2/19-2热高分气混氢

18、9.4510.52702506新氢返回冷却器1三-104BES700-4.0-120-6/25-2I水H20.583.3801807贫胺液冷却器E-105BES700-2.5-120-6/25-4I水贫液0.581.3861758硫化氢汽提塔顶后冷器E-201/ABES600-2.5-85-6/25-4I水油气0.580.8860709硫化氢汽提塔顶后冷器E-201/BBES500-2.5-41-4.5/25-4I水油气0.580.8860704p设备名称工艺编号设备型号管程介质壳程介质设计参数管程压力(MPa壳程压力(MPa管程温度(C)壳程温度(C)10石脑油冷却器E-202BES500-

19、2.5-55-6/25-2I水石脑油0.581.88608011(柴与原料油换热器E-203BFU1200-4.0-705-6.8/19-2/2I柴油原料油1.581.5827016012柴油蒸汽发生器1三-204BIU1600-1.38/1.7-1064-6/19-4I柴油除氧水1.71.3825029213精柴与分储塔进料换热器E-205BFU1200-4.0-595-6/19-4I柴油塔进料油1.581.430826014酸性气冷却器E-301BES700-2.5-120-6/25-4I水酸性气0.581.0607515酸性气脱硫贫胺液冷却器E-302BES600-2.5-85-6/25

20、-4I水贫液0.581.38607516燃料气加热器E-401BES600-2.5-45-3/25-2I蒸汽燃料气1.00.42504017热高分空冷器A-101/AHGP9<2-6-125-9.5S-23.4/DR-Ht热高分气9.511018热低分空冷器A-102/A.BGP9<3-6-193-4.0S-23.4/G-IIa热低分气1.323119硫化氢汽提塔顶空冷器A-201/A.BGP9<3-4-129-2.5S-23.4/KL-IIa油气0.7156设备名称工艺编号设备型号管程介质壳程介质设计参数管程压力(MPa壳程压力(MPa管程温度(C)壳程温度(C)20分流塔

21、顶空冷器/X-202/ADGP9<3-6-193-2.5S-23.4/KL-IIIa石脑油0.1515521产品柴油空冷器/X-203/ADGP9<3-6-193-2.5S-23.4/KL-IIIa柴油1.113522产品柴油空冷器/X-203/EHGP9<3-6-193-2.5S-23.4/KL-IIIa柴油1.1684、炉类:序号设备名称工艺编号规格型号工艺参数形式温度0c压力MPa介质进口出口进口出口1反应加热炉F-10121.97MW160X193.7双室水平管箱式炉3263879.48.8油、Hb、H2S2重沸炉F-2017.463MW25X152园筒炉218260

22、0.60.2柴油第六节：装置主要控制仪表序号工艺位号检测位置控制回路阀前压力MPa阀后压力MPa操作温度C公称通径mm介质故障状态流量最大正常最小FV8102罐区柴油进装置管线催、焦柴流控0.350.350250原料油风开FC340476kg/h200000100000FV8103二常直柴进装置管线二常直柴流控0.350.350200原料油风开FC150000kg/h11800060000FV8106P102出口管反应进料流控10.39.81336”柴油风开FC380000kg/h309000185000FV8107AF101炉膛1瓦斯线F101瓦斯流控0.250.2250100燃料气风开FC

23、1500Nm3/h1050500FV8107BF-101炉膛2瓦斯线F-101瓦斯流控0.250.2250100燃料气风开FC1500Nm3/h1050500FV8108D-108排放氢排氢流控7.92.451231/2”循环氢风开FC7000Nm3/h50000FV8109P-103出口管注水流控9.08.4501/2”除盐水风开FC18000kg/h140005000FV8111P-104出口管C-101贫液流控9.08.1613”贫胺液风开FC131000kg/h11900060000FV8114K-102出口管防喘振流控9.78.286200循环氢风关FV8201C-201回流入口线C

24、-201回流流控1.11.054040轻石脑油风关FO7200Nm3/h38001800FV8202C-201吹蒸汽线C-201汽提蒸汽流控1.20.8350100蒸汽风开FC6000kg/h30001500FV8203AF-201对流入口管1重沸炉分支流控10.950.9290200C-202底油风关FO193000kg/V8203BF-201对流入口管2重沸炉分支流控20.950.9290200C-202底油风关FO193000kg/V8203CF-201对流入口管3重沸炉分支流控30.950.9290200C-202底油风关FO1930

25、00kg/V8203DF-201对流入口管4重沸炉分支流控40.950.9290200C-202底油风关FO193000kg/V8204F-201瓦斯入口线F-201瓦斯流控0.250.25080瓦斯风开FC1400Nm3/h1010500FV8205C202顶回流入口线C-202顶回流流控1.31.15040石脑油风关FO9600kg/h48002400FV8206精制柴油出装置管C-202底精柴流控1.10.8550200精制柴油风开FC366000kg/h304541152270FV8301C-301贫液入口线C-301贫液流控1.10

26、.954550贫胺液风锁FLO20600kg/h165008000FV302D307底出口线D307富液流控250富液风开HV8101C-101付线手控阀8.18.075010”循环氢风开FC180000Nm3/h1000000HV8102E-101旁路炉后混氢温度手控阀9.39.11754”循环氢风锁FLO60000Nm3/h300000HV8103E-101壳程入口炉后混氢手控9.89.31758"循环氢风关FO170000Nm3/h12400060000HV8104混氢至P-102出口炉前混氢手控9.89.751756"循环氢风关FO100000Nm3/h350001

27、7000LV8101D102原料入口线D-102液控0.650.45120200原料油风开FC380000kg/h309524185700LV8102D-105出口管D-105液控8.22.6502”生成油风开FC26000kg/h130006500LV8103D-105酸性水出口管D-105界控8.20.6502”酸性水风开FC18000kg/h145007000LV8104D-106低分油出口管D-106液控2.51.25032低分油风开FC18000kg/h137006850LV8105D-106含硫污水出口管D-106界控2.50.65020酸性水风开FC7000kg/h5000200

28、0LV8106D-110除盐水入口管D-110液控0.40.355080除盐水风开FC18000kg/h140005000LV8107D-112贫液入口管D-112液控0.80.4555100贫胺液风开FC147000kg/h11320060000LV8108C-101富液出口管C-101液控80.9704”富胺液风开FC132000kg/h12000060000LV8109D-103底出口线D-103液控8.42.62408”生成油风开FC371000kg/h297000148000LV-8110D-104底出口线D-104液控2.51.2225125生成油风开FC370000kg/h295

29、000147000LV8201C-201底出口管C-201液控0.70.6221250生成油风开FC383000kg/h306600153000LV8202轻胫出装置D-201液控1.11.04025轻石脑油风开FC3800kg/h38000LV8203D-201酸性水出口管D-201界控0.650.64032酸性水风开FC3800kg/h22001100LV8205石脑油出装置D-202液控1.11.04040石脑油风开FC4000kg/h2000700LV8206D-202酸性水出口管D-202界控0.120.095025酸性水风开FC1500kg/h1000500LV8301C-301富

30、液出口线C-301液控0.550.55065富胺液风开FC20100kg/h170008000LV8302D-303富液出口线D-303液控0.60.5565150富胺液风开FC132000kg/h12000060000LV8303贫胺液进装置管D-304液控0.30.155125富胺液风开FC162000kg/V8401D402出口D402液控50污油风关LV8501D-501除氧水入口管D-501液控2.01.510040除氧水风关FO30000kg/h2300015500PCV102F-101长明火瓦斯线F101长明灯瓦斯压控0.45080瓦斯风开PCV201F

31、-201长明火瓦斯线F201长明灯压控0.44050瓦斯PV8100罐区柴油返回线柴油返回压控0.40.3550125柴油风关FO100000kg/h400000PV8101三常柴油返回线柴油返回压控0.40.350100柴油风关FO75000kg/h2360012000PV8102AD-102燃料气入口管D-102顶压控0.250.25080燃料气风开FC1000Nm3/h5000PV8102BD-102燃料气入口管D-102顶压控0.20.15080燃料气风开FC1000Nm3/h5000PV8103D-106低分气出口管D-106顶压控2.52.475065低分气风开FC4200Nm3/

32、h32201600PV8104AD-112氮气入口管D-112压控0.80.44032氮气风开FC500Nm3/h2500PV8104BD-112氮气入口管D-112压控0.40.15540氮气风开FC500Nm3/h2500PV8106K-101出口反入口K-101出口压控102.31342"氢气风锁FLO23000Nm3/h53401780PV8107D-107补充氢放空线K-101入口压控2.250.14065风开FC30000Nm3/h150000PV8108过热蒸汽至管网1.11.05350250蒸汽风关FO25000Nm3/h180000PCV126F101长明火瓦斯线F

33、101长明灯ESD0.45080瓦斯风开PV8201D-201顶酸性气线C-201压控0.70.6540100富气风开FC3200Nm3/h22001100PV8202AD-202顶燃料气线C-202压控0.120.074050瓦斯风开FC500Nm3/h2500PV8202BD-202瓦斯人口管C-202压控0.30.125040瓦斯风开FC500Nm3/h2500PCV216F201长明火瓦斯线F201长明灯压控0.44050瓦斯风开PV8301D-302去瓦斯管网D-302压控0.60.54580瓦斯风开FC3200Nm3/h22001100PV302D307顶出口线D307压控10.7

34、50150酸性气风开PV8401D-404瓦斯入口线瓦斯压控0.30.2750150瓦斯风开FC4600Nm3/h35001500PV8501D-501蒸汽出口管D-501压控1.21.13191200饱和蒸汽风关FO25000kg/h2194015000PV8813引风机入口挡板-25000Pa250风关FOAV8813鼓风机入口挡板-300-0Pa40风关FOTdV8107E-105循环热水C-101温差控制0.370.3443150循环水风关FO100000kg/h770000TdV8301E-302循环水出口管C-301酸性气与贫液温差控制0.370.3243100循环热水风开FC62

35、500kg/h500000TV8101除氧水来自热工蒸汽温控1.41.010025除氧水风关FO5915kg/h2409962TV8102E-102原料油旁路D-103入口温控10.29.751234”循环氢、油风锁FLO186000kg/h464000TV104D102入口线D102进料温控1.00.950200原料柴油风关TV204TV8105R-101急冷氢入口线床层温控9.89.2753”循环氢风关36000Nm3/h180000TV8204E-203旁路管D-102温控1.21.0120150原料油风关FO309524kg/h1031000TV8205E-205旁路管C202进料温控

36、0.60.3221150原料油风关FO200000kg/h600000HV8811AF-101烟囱调节挡板-150-0Pa500风关FOHV8811BF-101烟囱调节挡板-1500Pa500风关FOHV8821F-201烟囱调节挡板-1500Pa500风关FOUV101主火嘴瓦斯线F101主火嘴切断阀150风开UV103P106出口管D115液控1.00.5135100污油风关第七节：装置安全阀表序号工2编号安装地点型号操作压力MPa操作温度C介质定压值MPa入/出口法兰公称压力Mpa入口/出口直径阀体材质阀芯阀座材质波纹管材质最近校验日期后尢根阀后尢在线备用PSV101/AD102顶HTB

37、-03Acb8T100.6120氮气、氢气、轻胫0.782.5/2.5200/250C.SS.S有有PSV101/BD102顶HTB-03Acb8T100.6120氮气、氢气、轻胫0.782.5/2.5200/250C.SS.S有有PSV103/AD112顶HTB-01CB4P60.650氮气、氢气、轻胫0.782.5/2.5100/150C.SS.S有有PSV103/BD112顶HTB-01CB4P60.650氮气、氢气、轻胫0.782.5/2.5100/150C.SS.S有有PSV105/AD105顶HTB-09SB4L68.050氢气、轻胫、硫化氢8.9516/2.5100/150S.S

38、S.S316L有有PSV105/BD105顶HTB-09SB4L68.050氢气、轻胫、硫化氢8.9516/2.5100/150S.SS.S316L有有PSV106/AD106顶HTXD-0301S6R82.540氢气、甲烷3.04.0/2.5150/250S.SS.S有有PSV106/BD106顶HTXD-0301S6R82.540氢气、甲烷3.04.0/2.5150/250S.SS.S有有PSV107/AD107顶HTO-03Acb3J42.2540氢气、甲烷3.04.0/2.580/100C.SS.S有有PSV107/BD107顶HTO-03Acb3J42.2540氢气、甲烷3.04.0

39、/2.580/100C.SS.S有有PSV108/AE104冷却水回水HTO-01CB6Q80.443氢气、水0.61.6/1.6150/200C.SS.S有有PSV108/BE104冷却水回水HTO-01CB6Q80.443氢气、水0.61.6/1.6150/200C.SS.S有有PSV109/AD113顶HTB-01CB1B20.540氮气0.681.6/2.525/50C.SS.S有有PSV109/BD113顶HTB-01CB1B20.540氮气0.681.6/2.525/50C.SS.S有有PSV201/AC201顶HTB-03SB4M60.9220硫化氢、水、轻燃1.082.5/2.5100/150S.SS.S316L有有PSV201/BC201顶HTB-03SB4M60.9220硫化氢、水、轻燃1.082.5/2.5100/150S.SS.S316L有有PSV202/AD201顶HTB-