Steam-cracking of modified naphtha
View Patent ↗Disclosed is a method for steam-cracking naphtha, according to which a charge of hydrocarbons containing a portion of paraffinic naphtha, which is modified by adding a combination of a first component containing a portion of gasoline and a second component containing a portion of at least one hydrocarbonated refinery gas, and a paraffin-rich change containing at least one paraffin selected among propane, butane, or a mixture thereof are fed through a steam cracker in the presence of vapor. Also disclosed is a hydrocarbon composition suitable for steam cracking, containing a portion of a paraffinic naphtha, which is modified by adding a combination of a first component containing a portion of gasoline and a second component containing a portion of at least one hydrocarbonated refinery gas and a paraffin-rich charge containing at least one paraffin selected among propane, butane, or a mixture thereof.
1. A method for steam-cracking naphtha comprising passing a feedstock of hydrocarbons through a steam cracker, in the presence of steam;
wherein said feedstock of hydrocarbons comprises
about 60% to about 80% by weight of a paraffinic naphtha, and
about 40% to about 20% by weight of a mixture of a first component, that is, a gasoline produced by a fluidized bed catalytic cracking (FCC) unit and a second component including at least one hydrocarbon refinery gas and at least a feedstock rich in paraffins,
the paraffinic naphtha having from 10 to 60% by weight of n-paraffins, from 10 to 60% by weight of isoparaffins, from 0 to 35% by weight of naphthenes, from 0 to 1% by weight of olefins, and from 0 to 20% by weight of aromatics,
the FCC gasoline being an unhydrogenated gasoline having from 0 to 30% by weight of n-paraffins, from 10 to 60% by weight of isoparaffins, from 0 to 80% by weight of naphthenes, from 5 to 80% by weight of olefins and from 0 to 60% by weight of aromatics,
the refinery gas having from 0 to 5% by weight of hydrogen, from 0 to 40% by weight of methane, from 0 to 50% by weight of ethylene, from 0 to 80% by weight of ethane, from 0 to 50% by weight of propylene, from 0 to 80% by weight of propane and from 0 to 30% by weight of butanes, and the feedstock rich in paraffins containing at least 50% by weight of saturated hydrocarbons, said feedstock containing at least propane or butane.
2. The method according to claim 1 , in which the mixture of the first and second components that is added to the naphtha includes up to 60% by weight of the second component and at least 40% by weight of gasoline.
3. The method according to claim 2 , in which the mixture of the first and second components includes up to 50% by weight of the second component and at least 50% by weight of gasoline.
4. The method according to claim 2 or 3 , in which the mixture of the first and second components includes about one third in percentage by weight of the second component and about two thirds in percentage by weight of gasoline.
5. The method according to any one of claims 1 - 3 , in which the feedstock includes about 80% by weight naphtha, about 7% by weight of the second component and about 13% by weight of gasoline.
6. The method according to any one of claims 1 - 3 , in which the FCC gasoline is a fraction or a mixture of fractions from an FCC unit having a distillation range of between 30 and 160° C.
7. The method according to any of claims 1 to 3 , in which the second component consists of at least propane and butane.
8. The method according to any of claims 1 to 3 , in which the composite feedstock of naphtha, gasoline and of the second component is subjected to steam-cracking under conditions including a temperature of between 780 and 880° C.
9. The method according to any of claims 1 to 3 , in which the quantity of steam is from 25 to 60% by weight based on the weight of the feedstock of hydrocarbons.
10. A composition of hydrocarbons suitable for a steam-cracking method, said composition comprising about 60% to about 80% by weight of a paraffinic naphtha and about 40% to about 20% by weight of a mixture of a first component, that is, a gasoline produced by a fluidized bed catalytic cracking (FCC) unit and a second component including at least one hydrocarbon refinery gas and at least a feedstock rich in paraffins, the paraffinic naphtha having from 10 to 60% by weight of n-paraffins, from 10 to 60% by weight of isoparaffins, from 0 to 35% by weight of naphthenes, from 0 to 1% by weight of olefins and from 0 to 20% by weight of aromatics, the FCC gasoline being an unhydrogenated gasoline having from 0 to 30% by weight of n-paraffins, from 10 to 60% by weight of isoparaffins, from 0 to 80% by weight of naphthenes, from 5 to 80% by weight of olefins and from 0 to 60% by weight of aromatics, the refinery gas having from 0 to 5% by weight of hydrogen, from 0 to 40% by weight of methane, from 0 to 50% by weight of ethylene, from 0 to 80% by weight of ethane, from 0 to 50% by weight of propylene, from 0 to 80% by weight of propane and from 0 to 30% by weight of butanes, and the feedstock rich in paraffins containing at least 50% by weight of saturated hydrocarbons, said feedstock containing at least propane or butane.
11. The composition of hydrocarbons according to claim 10 , in which the mixture of the first and second components to the naphtha includes up to 60% of the second component and at least 40% by weight gasoline.
12. The composition of hydrocarbons according to claim 11 , in which the mixture of the first and second components includes up to 50% of the second component and at least 50% by weight of gasoline.
13. The composition of hydrocarbons according to claim 11 or 12 , in which the mixture of the first and second components that is added to the naphtha includes about one third in percentage by weight of the second component and about two thirds in percentage by weight of gasoline.
14. The composition of hydrocarbons according to claim 13 , in which the feedstock includes about 80% by weight of naphtha, about 7% by weight of the second component and about 13% by weight of gasoline.
15. The composition of hydrocarbons according to any of claims 10 to 12 , in which the second component consists of at least propane and butane.
16. A method for controlling a steam cracker, said method comprising:
supplying steam and a feedstock of hydrocarbons to a steam cracker;
wherein the feedstock of hydrocarbons comprises about 60% to about 80% by weight of a paraffinic naphtha and about 40% to about 20% by weight of a mixture of a first component, that is, a gasoline produced by a fluidized bed catalytic cracking (FCC) unit, and a second component including at least one hydrocarbon refinery gas and at least a feedstock rich in paraffins,
the paraffinic naphtha having from 10 to 60% by weight of n-paraffins, from 10 to 60% by weight of isoparaffins, from 0 to 35% by weight of naphtalenes, from 0 to 1% by weight of olefins and from 0 to 20% by weight of aromatics, the FCC gasoline being an unhydrogenated gasoline having from 0 to 30% by weight of n-paraffins, from 10 to 60% by weight of isoparaffins, from 0 to 80% by weight of naphthenes, from 5 to 80% by weight of olefins and from 0 to 60% by weight of aromatics, the refinery gas having from 0 to 5% by weight of hydrogen, from 0 to 40% by weight of methane, from 0 to 50% by weight of ethylene, from 0 to 80% by weight of ethane, from 0 to 50% by weight of propylene, from 0 to 80% by weight of propane and from 0 to 30% by weight of butanes, and the feedstock rich in paraffins containing at least 50% by weight of saturated hydrocarbons, said feedstock containing at least propane or butane; and
a continuous control of the supply of paraffinic naphtha, of the second component and of the gasoline in the feedstock, in order to give an effluent a desired target composition.
17. The method according to claim 16 , in which the target composition is appreciably the same composition of effluent, that is ±20% by weight for any given effluent component, as the composition obtained with unmodified paraffinic naphtha.
18. The method according to claim 16 or 17 , in which the second component and the gasoline are both furnished directly by a refinery and also including control of sending the second excess component to the flare and/or the control of the quantity of gasoline in the refinery.
19. The method according to any one of claims 16 to 17 , in which the supply of the components of the feedstock to the steam cracker is controlled by software.
20. The method according to claim 1 or 16 for processing sulfurous gasoline wherein
sulfurous gasoline produced by a fluidized bed catalytic cracking unit, and
effluent from the steam cracker containing at least light olefins, which have at least one olefin between C2 and C4, and C5+ hydrocarbons, are separated into a first fraction, which is practically free of sulfur and includes the light olefins, and a second fraction that contains sulfur and includes the C5+ hydrocarbons.