催化裂化原始数据表

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1、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t3037178231t5039699250t70430125271t90496M=560163303M=390S,重﹪0.080.160.0090.0710.16N,重﹪0.1070.355Fe,ppm3.7811.4Ni,ppm0.1957.14V,ppm〈0.1〈0.1Cu

2、,ppm0.057〈0.1二．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5.0C1023.24〈20μ1.9损失0.5C208.740.520-40μ18.9合计100C2=1140-80μ57.7回炼比=0.3C300.221180-110μ18.4C3=0.8228.5＞110μ3.1iC400.0923Y-15Al2O326.5﹪N

3、C400.026CRC-1Al2O352.5﹪NC4=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（℃）t1035556233300345t3040883247338370t50435110267350386t7047014028

4、8360400t90520178312380440100，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=0.396.72iC500.53

5、2.85nC500.080.07C5=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﹪〈20μ1.920-40μ18.940-80μ57.780-110μ18.4＞110μ3.1Y-15Al2O326.5﹪CRC-1Al2O352.5﹪3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（℃）10﹪6121432234730﹪78231330

6、39950﹪9925034042370﹪12527134847190﹪163303496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﹪C1023.24〈20μ1.9C208.740.520-40μ18.9C2=1140-80μ57.7C300.221180-110

7、μ18.4C3=0.8228.5＞110μ3.1iC400.0923Y-15Al2O326.5﹪NC400.026CRC-1Al2O352.5﹪NC4=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（℃）t1032166242358368t3037388271380428t50409116298400453t70446146322419476t904

8、96177348450485残炭,重﹪