Process and plant for preparing purified benzene composition from crude hydrocarbon stream containing benzene
A process for preparing a purified benzene composition from a crude hydrocarbon stream containing at least 10% by volume of benzene is provided. The process comprises subjecting the crude hydrocarbon stream and a further recycled benzene containing stream to a solvent-based extraction so as to produce a benzene enriched aromatic stream and a benzene depleted non-aromatic stream, subjecting the benzene enriched aromatic stream to a hydrodesulfurization so as to obtain a desulfurized aromatic stream, subjecting the desulfurized aromatic stream to a distillation producing a purified benzene stream and a further benzene containing stream having a benzene concentration of between less than 100% by weight and the azeotropic benzene concentration, and at least partially recycling the further benzene containing stream.
1. A process for preparing a purified benzene composition from a crude hydrocarbon stream containing at least 10% by volume of benzene comprising the following steps:
a) subjecting the crude hydrocarbon stream and a further recycled benzene containing stream to a solvent based extraction so as to produce a benzene enriched aromatic stream and a benzene depleted non-aromatic stream,
b) subjecting the benzene enriched aromatic stream to a hydrodesulfurization so as to obtain a desulfurized aromatic stream,
c) subjecting the desulfurized aromatic stream to a distillation so as to produce a purified benzene stream and a further benzene containing stream, wherein the further benzene containing stream comprises benzene and at least one of cyclohexane, methylcyclopentane, 2,3 dimethyl pentane and 2,4 dimethyl pentane and has a benzene concentration of between less than 100% by weight and the azeotropic benzene concentration in the azeotrope formed of these compounds as dictated by the vapor-liquid equilibrium of the compounds contained in the further benzene containing stream, and
d) at least partially recycling the further benzene containing stream.
2. The process in accordance with claim 1 , wherein the crude hydrocarbon stream contains, based on 100% by weight, at least 20% by volume of benzene.
3. The process in accordance with claim 1 , wherein the crude hydrocarbon stream contains, based on 100% by weight, i) 20 to 60% by volume of paraffins, ii) 10 to 50% by volume of olefins and iii) 5 to 40% by volume of naphthenes.
4. The process in accordance with claim 1 , wherein the crude hydrocarbon stream is a C 6 -cut or a C 6 -C 8 -cut from fluid catalytic cracked naphtha or a C 6 -cut or a C 6 -C 8 -cut from a coke oven light oil.
5. The process in accordance with claim 1 , wherein the crude hydrocarbon stream is mixed with the recycled further benzene containing stream to obtain a feed stream, which is subjected to the solvent based extraction.
6. The process in accordance with claim 1 , wherein the crude hydrocarbon stream and the recycled further benzene containing stream are separately fed to the solvent based extraction.
7. The process in accordance with claim 1 , wherein the crude hydrocarbon stream and the recycled further benzene containing stream are subjected to an extractive distillation.
8. The process in accordance with claim 1 , wherein the solvent used in the solvent based extraction is selected from a group consisting of sulfolane, 3-methylsulfolane, 2,4-dimethylsulfolane, 3-ethylsulfolane, N-methyl pyrrolidone, 2-pyrrolidone, N-ethyl pyrrolidone, N-propyl pyrrolidone, N-formyl morpholine, dimethylsulfone, diethylsulfone, methylethylsulfone, dipropylsulfone, dibutylsulfone, tetraethylene glycol, triethylene glycol, dimethylene glycol, ethylene glycol, ethylene carbonate, and propylene carbonate or a combination thereof.
9. The process in accordance with claim 1 , wherein the desulfurized aromatic stream is subjected to one or more distillation steps, wherein at least one distillation step is performed with a top divided wall column, wherein one distillation step is performed and the wall of the top divided wall column extends from the upper end of the top divided wall column perpendicular downwards over 20 to 70% of the height of the top divided wall column.
10. The process in accordance with claim 1 , wherein the desulfurized aromatic stream is subjected to two distillation steps, wherein the desulfurized aromatic stream is subjected to a first distillation step in a first distillation column so as to obtain at the overhead of the first distillation column an off-gas stream containing C 1 -C 7 -hydrocarbons, hydrogen and hydrogen sulfide and at the bottom of the first distillation column a liquid stream with the remaining compounds, wherein the liquid stream is subjected to a second distillation step in a second distillation column so as to obtain as side stream of the second distillation column the purified benzene stream, at the overhead of the second distillation column the further benzene containing stream and at the bottom of the second distillation column a C 7+ -stream.
11. The process in accordance with claim 1 , wherein the desulfurized aromatic stream is subjected to two distillation steps, wherein the desulfurized aromatic stream is subjected to a first distillation step in a first column so as to obtain at the overhead of the first distillation column an off-gas stream containing C 1 -C 7 -hydrocarbons, hydrogen and hydrogen sulfide and at the bottom of the first distillation column a liquid stream with the remaining compounds, wherein the liquid stream is subjected to a second distillation step in a second middle divided wall column so as to obtain as first side stream the purified benzene stream, as second side stream a toluene rich stream, at the overhead of the second distillation column the further benzene containing stream and at the bottom of the second distillation column a stream enriched in xylenes.