催化裂化原始数据表.doc

1.原料：大庆混合蜡油：减压渣油=91.97：8.03（重）一，原料和产品性质混合蜡油减压渣油汽油轻柴油重柴油总回炼油相对密度，d4200.85340.92480.71330.85850.88700.9034残炭，重0.097.44馏程（）t1032061214100=2.15厘斯t3037178231t5039699250t70430125271t 90496M=560163303M=390S, 重0.080.160.0090.0710.16N, 重0.1070.355Fe,ppm3.7811.4Ni,ppm0.1957.14V,ppm0.10.1Cu,ppm0.0570.1二产品产率, 重三，气体组成，体,四催化剂性质干气2.2干气液化气Y-15:CRC-1=1:1液化气10. 8H242.1微反活性68汽油46N210.11孔体积，毫升/克 0.29轻柴油28CO23.1充气密度克/毫升0.81重柴油7.5H2S0.53筛分组成, 重焦炭5.0C1023.24201.9损失0.5C208.740.520-4018.9合计100C2=1140-8057.7回炼比=0.3C300.221180-11018.4C3=0.8228.51103.1iC400.0923Y-15Al2O326.5NC400.026CRC-1Al2O352.5NC4=0.037骨架密度Kg/m32405iC4=0.048CC4-2=0.036tC4-2=0.048.5C501.52.处理量100万吨原料：残余直馏蜡油：丙烷脱沥青油=81.66：18.34（重）一，原料和产品性质直馏蜡油丙烷脱沥青油汽油轻柴油重柴油回炼油相对密度，d4200.86420.88620.72830.85530.86800.8755残炭, 重0.1091.871馏程（）t1035556233300345t3040883247338370t50435110267350386t70470140288360400t 90520178312380440100，厘斯5.5127.99二，产品产率, 重干气4.67重柴油4.96液化气7.19焦炭4.65汽油52.49损失0.68轻柴油25.36回炼比=0.3（其中回炼油浆占25）三，气体组成，体,干气液化气H29.150.01N238.381.24CO22.27C1026.83C206.80.25C2=8.79C300.914.29C3=1.9938.1iC401.7714.99NC400.544.11NC4=0.6711.62iC4=CC4-2=0.294.63tC4-2=0.396.72iC500.532.85nC500.080.07C5=0.621.12合计100100四，催化剂性质Y-15:CRC-1=1:1微反活性68孔体积，毫升/克 0.29充气密度克/毫升0.81筛分组成, 重201.920-4018.940-8057.780-11018.41103.1Y-15Al2O326.5CRC-1Al2O352.53沈北油混合蜡油掺5减压渣油一，原料和产品性质原料油汽油轻柴油重柴油（总回炼油）回炼油比重，d4200.85950.71330.85850.88700.8990恩氏蒸馏数据（）1061214322347307823133039950992503404237012527134847190163303496残炭, 重0.7100厘斯3.52.15二，（柴油方案）产品收率，重干气2.7重柴油7.5液化气10.8焦炭5汽油46合计100轻柴油28回炼比0.3 三，气体组成，体,四，催化剂性质组分干气液化气Y-15:CRC-1=1:1H242微反活性68N210.1孔体积，毫升/克 0.29CO23.1充气密度克/毫升0.81H2S0.53筛分组成, 重C1023.24201.9C208.740.520-4018.9C2=1140-8057.7C300.221180-11018.4C3=0.8228.51103.1iC400.0923Y-15Al2O326.5NC400.026CRC-1Al2O352.5NC4=0.037iC4=0.048CC4-2=0.038.5tC4-2=0.046iC501.5合计1001004锦西（辽河馏分油+丙烷脱沥青油）一，原料和产品性质原料油汽油柴油回炼油油浆比重，d4200.90660.74330.90520.95771.0178馏程（）t1032166242358368t3037388271380428t50409116298400453t70446146322419476t 90496177348450485残炭, 重0.53二产品产率, 重三催化剂性质H20.14LC-7剂C100.37比表面m2/g167C200.66孔体积，毫升/克 0.192C2=0.67充气密度，克/毫升0.96C301.28沉降，克/毫升0.97C3=4.70压紧密度，克/毫升1.14iC402.15微反活性66NC400.45筛分组成, 重iC4= +C4-1=1.53200.6CC4-2=0.5320-406.3tC4-2=0.7840-8063汽油44.1780-11019.7柴油33.6811010.4焦炭5.43Al2O329.7油浆3.46回炼比（其中回炼油浆占15）0.45合计1006原料：任丘减压蜡油：常压渣油=20：80（重）一，原料和产品性质混合原料汽油柴油总回炼油相对密度，d4200.89420.71040.8605残炭, 重5.91馏程（）t1053199t5097243t 90156301100厘斯14.0M=400二产品产率, 重回炼比=0.43气体14.49原料中重金属含量，ppm汽油47.68Fe2.22柴油26.35Ni14.48焦炭11.48Cu0.04合计100V0.37三，气体组成，体,四，催化剂性质H234.85CRC-1:ZCM-7=2:1C16.43微反活性63C202.04充气密度(克/毫升)0.87C306.93沉降密度(克/毫升)0.91C3=20.73压紧密度(克/毫升)0.98iC4010.75骨架密度(克/毫升)2.61NC402.46筛分组成, 重C4=12.38200.820-409.440-8054.280-10519.5105-14910.21495.9孔体积mg/g0.268CRC-1Al2O352.5ZCM-742.25原料：胜利减压馏分：减压渣油=42.4：57.6（重）1，原料和产品性质原料油汽油柴油油浆比重，d15.615.60.93830.75800.95301.0300馏程（）t1057247364t3081258404t50109274454t70144292494t 90186318554残炭, 重7.66 M547原料中重金属含量，ppmV0.7Ni30.0二产品产率, 重三催化剂性质H2S0.50ZCM-7C101.03孔体积，毫升/克 0.308C201.03平均堆积密度g/ml 0.85C2=1.03筛分组成, 重C301.41201.8C3=4.6620-4017.8iC402.1440-8053.7NC400.8780-10516.1C4= 6.03105-1497.0H20.101493.6汽油45.30微反活性63柴油21.53骨架密度g/ml2.47油浆7.77Al2O3重42.2焦炭6.6合计1007原料：胜利蜡油：减压渣油=5：9（重）1，原料和产品性质（to，tal）原料油汽油柴油澄清油比重，。ApI18.357.621.46.0残炭, 重8.6 M566.596.0216370二产品产率, 重H2S0.52C100.91C200.91C2=0.92C302.65C3=0.80iC401.22NC403.43C4= 0.50H20.09汽油34.38柴油34.31澄清油12.76焦炭6.6合计100.0三催化剂性质SRNY骨架密度kg/m32520堆积密度kg/m3880颗粒密度kg/m3筛分组成密度 ,重%0-201.920-4015.940-8057.580-10515.7105-1496.51492.5孔体积ml/g0.325AL2O341.4%8大庆常渣油1原料和产品性质原料油汽油柴油总回炼油相对密度=0.88550.75400.85930.8835馏程t1040897238400t30480t50541137280430t70t90182339496残碳 重%5.86厘斯37.85苯胺点2产品产率 重%H2SH20.91C100.82C200.62C2=0.48C300.77C3=3.22IC401.88NC400.50C4-1=2.69IC4=TC4-2=1.31CC4-2=100汽油41.4柴油33.0焦炭11.4合计100.03催化剂性质Y-15比表面m2/g85孔体积ml/g0.392压紧密度g/ml0.84沉降密度g/ml0.73充气密度g/ml0.69馏分组成 重%200.1020-408.3040-8063.7080-11023.401103.50微反活性65骨架密度g/ml2.34AL2O326.5%回练比0.499一， 原料和产品性质原料汽油 柴油回炼油回练油浆相对密度0.88860.71330.88570.96610.9871馏程t1052221t50100269t90167324残碳，重%4.2，厘斯18.3813.4218.76二产品产率，重%干气7.4回练比=0.32（其中回炼油浆占20%）液化气8.99汽油41.87柴油31.47焦炭10.27合计100原料中重金属，ppmFe10.23Ni7.75Cu0.09V0.62三 气体组成，体%干气液化气H225.2空气10.1CO0.8CO21.6C1031.2C2012.8C2=16.31.6C300.38.0C3=1.547.9IC4=0.110.4C4-2=5.0IC400.110.4C4-2=5.0TC4-2=6.1IC503.0nC500.9合计100100四催化剂性质CRC-1微反活性60沉降密度g/ml0.8544馏分组成，重%200.520-4016.540-8060.080-11010.511012.5骨架密度g/ml2.51孔密度ml/g0.248Al2O352.5%10大庆常压渣油1原料和产品性质原料油汽油柴油总回炼油相对密度=0.89570.75880.86450.9075馏程t10392100247417t30464t50139294449t70t90186351529残碳 重%4.34凝点2厘斯27.50苯胺点121.0原料：S-0.13 N-0.28 ppm Ni-5.32产品产率，重%H2SH20.47C101.44C201.29C2=1.46C300.92C3=4.41IC400.89NC400.47C4-1=3.65IC4=TC4-2=1.59CC4-2=151汽油40.0柴油32.4焦炭9.5合计100.3催化剂性质Y-15平衡剂孔体积ml/g0.362压紧密度g/ml0.851沉降密度g/ml0.771充气密度g/ml0.749馏分组成 重%200.1020-403.2040-8067.2080-11026.301102.70骨架密度g/ml2.33AL2O326.5%回练比0.5五大庆常渣油1原料和产品性质比重原料油汽油柴油总回炼油0.89570.75260.86660.9149蒸馏数据10%9423840330%1122564195015330645690%180339496残炭，重%4 .34厘斯27.50苯胺点121.0212产品产率，重%总气体13.5汽油45柴油31.1焦炭10.4合计100回练比0.37S-0.13% N-2800ppm Ni-5.3ppm213气体组成H2S0.25H23.42C106.26C205.67C2=5.09C305.25C3=23.03IC409.17NC403.50C4-1=20.43IC4=TC4-2=10.01.CC4-2=7.92合计1004催化剂性质CRC-1微反活性68.5沉降密度g/ml0.85馏分组成，重%200.220-4012.340-8062.080-11025.5110骨架密度g/ml2.68孔体积ml/g0.199Al2O352.5%12.大庆常渣油处理量100万吨1原料和产品性质原料油汽油柴油总回炼油相对密度=0.88550.74770.85410.8854馏程t1040893236403t30480t50541132286449t70t90173349529残碳 重%5.86凝点4厘斯37.85苯胺点2产品产率，重%H2S0.03H20.60C100.62C200.57C2=0.49C300.63C3=2.66IC401.46NC400.45C4-1=2.43IC4=TC4-2=1.15CC4-2=0.91汽油40.10柴油36.70焦炭11.20合计1003催化剂性质Y-15平衡剂比表面 m2/g133孔体积ml/g0.309压紧密度g/ml0.82沉降密度g/ml0.74充气密度g/ml0.73馏分组成 重%200.2020-406.3040-8076.5080-1109.701107.30骨架密度g/ml2.34AL2O326.5%回练比0.5微反活性6613大庆常渣油1原料和产品性质原料油汽油柴油总回炼油比重0.89760.75590.86220.9032蒸馏数据t1039297246401t30t50524138287430t70t90188342484残炭 重%4.7厘斯31.52苯胺点124.7原料 S-0.14 N-0.22 ppm Ni-4.8 V-0.1 Fe-2.9 Cu-0.22产品产率H2SH20.73C100.90C200.77C2=0.74C300.71C3=3.35IC401.35NC400.44C4-1=2.76