Hydrocarbon recombinant alkylating desulfurization method for catalytically cracked gasoline
A technology of catalytic cracking gasoline and alkylation desulfurization, which is applied in the fields of gasoline desulfurization and hydrocarbon reorganization alkylation desulfurization of catalytic cracking gasoline, which can solve the problem of insufficient boiling point of alkylthiophene derivatives, poor sulfur transfer effect, and occupation of substitution positions And other problems, to achieve the effect of mild operating conditions, small construction investment, and increase the boiling point
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Embodiment 1
[0026]The catalytic cracked gasoline of Tianjin Petrochemical Company with a sulfur content of 324ppm was added to the preprocessor equipped with NKC-9 ion exchange resin at a flow rate of 300g / h, and the catalytic cracked gasoline was removed at an operating pressure of 0.3MPa and a temperature of 25°C Basic nitrogen compounds in the basic nitrogen compounds; the catalytic cracking gasoline that removes basic nitrogen compounds enters the primary fractionation tower of continuous operation for separation. The light fraction of catalytically cracked gasoline including C4-C5 olefins is produced at 79g / h, and the light fraction of catalytically cracked gasoline including C5-C7 olefins and thiophene and methane is produced at 125g / h from the side line of the primary fractionation tower at a temperature of 95°C. The middle distillate of catalytic cracking gasoline of the sulfide of alkylthiophene of base thiophene, and then produce the heavy fraction of catalytic cracking gasoline ...
Embodiment 2
[0028] Feed catalytic cracked gasoline with a sulfur content of 346ppm into the preprocessor equipped with ion exchange resin at a flow rate of 300g / h, and remove basic nitrogen compounds in catalytic cracked gasoline at an operating pressure of 0.15MPa and a temperature of 25°C The catalytically cracked gasoline that removes basic nitrogen compounds enters the batch distillation tower for separation, the operating pressure of the primary fractionation tower is 0.1Pa, and at the top temperature of the primary fractionation tower is 25 ~ 50 ° C, the output includes C4 ~ C5 olefins. The light fraction of cracked gasoline, when the initial fractionation tower top temperature is 50-115 ° C, the middle distillate of catalytic cracked gasoline including C5-C7 olefins and sulfides of alkylthiophenes including thiophene and methylthiophene is produced, and then in the initial fractionation The tower bottom output includes the heavy fraction of catalytic cracking gasoline of C2~C7 alkyl...
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