Method for producing clean gasoline from catalytic cracking gasoline
A technology for catalytic cracking gasoline and catalytic cracking device, which is applied in the field of light hydrocarbon refining, can solve the problems of increasing the cooling load of the device, high energy consumption of the processing flow device, long production process route, etc., and achieves the effect of reducing the total sulfur content
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Embodiment 1
[0051] according to figure 1 The process flow shown processes FCC catalytic cracking gasoline to produce ultra-low sulfur clean gasoline.
[0052] The naphtha after absorption and desorption in the FCC catalytic cracking absorption-stabilization unit is cut and separated in the stabilization tower to obtain light fractions and heavy fractions. The properties of the light and heavy fractions separated by the FCC catalytic cracking stabilization tower are shown in Table 1.
[0053] Table 1 Properties of light and heavy fractions separated by FCC catalytic cracking stabilizer
[0054] project light ends heavy fraction Density (20℃), g / cm 3 0.6875 0.7394 Sulfur content, μg / g 122 683 RON 95.2 92.6 Distillation range (ASTM D 86), °C IBP / 10% 30 / 35 79 / 110 30% / 50% 40 / 51 127 / 141 70% / 90% 59 / 63 157 / 188 95% / FBP 71 / 76 203 / 210
[0055] The light fraction enters the non-alkali deodorization unit to remove mercapta...
Embodiment 2
[0069] according to figure 1 The process flow shown is to process MIP catalytic cracking gasoline to produce ultra-low sulfur clean gasoline.
[0070] The naphtha after absorption and desorption in MIP catalytic cracking absorption-stabilization unit is cut and separated in the stabilization tower to obtain light fraction and heavy fraction. The properties of the light and heavy fractions separated by the MIP catalytic cracking stabilization tower are shown in Table 6.
[0071] Table 6 Properties of light and heavy fractions separated by MIP catalytic cracking stabilizer
[0072] project light ends heavy fraction Density (20℃), g / cm 3 0.6772 0.7375 Sulfur content, μg / g 118 680 Olefins, v% RON 95.6 92.8 Distillation range (ASTM D-86), ℃ IBP / 10% 30 / 35 80 / 109 30% / 50% 40 / 49 125 / 138 70% / 90% 57 / 62 153 / 185 95% / FBP 67 / 73 197 / 205
[0073] The light fraction enters the non-alkali deodorization uni...
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