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The present invention relates to a process for producing polyolefins wherein a feedstock comprising n-olefin or a mixture of n-olefins is dimerized in the presence of a solid acidic catalyst by passing the feedstock to a catalytic distillation apparatus comprising either a) a combination of a distil

The present invention relates to a process for producing polyolefins wherein a feedstock comprising n-olefin or a mixture of n-olefins is dimerized in the presence of a solid acidic catalyst by passing the feedstock to a catalytic distillation apparatus comprising either a) a combination of a distillation column and a reactor comprising at least one catalyst bed, or b) a distillation column connected to one or more side reactors comprising at least one catalyst layer, recovering the unreacted n-olefin from the distillation column or the combination of the distillation column and the reactor at the upper part thereof as a side-stream to be combined with the feedstock, and the reaction product from the dimerization is hydrogenated.

대표청구항 ▼

1. A process for producing polyolefins, which process comprises dimerizing a feedstock comprising an n-olefin or a mixture of n-olefins in the presence of a solid acidic catalyst by passing the feedstock to a catalytic distillation apparatus comprising either a) a combination of a distillation colum

1. A process for producing polyolefins, which process comprises dimerizing a feedstock comprising an n-olefin or a mixture of n-olefins in the presence of a solid acidic catalyst by passing the feedstock to a catalytic distillation apparatus comprising either a) a combination of a distillation column and a reactor comprising at least one catalyst bed, or b) a distillation column connected to one or more side reactors comprising at least one catalyst layer, recovering the unreacted n-olefin at the upper part of the distillation column or at the upper part of the combination of the distillation column and the reactor as a side stream to be combined with the feedstock wherein from 50 to 95% by weight of n-olefin monomers from said feedstock contact the catalyst layer more than once, and hydrogenating the reaction product from the dimerization, wherein the catalyst layer comprises solid acidic catalyst material with a mesoporous surface area of more than 100 m2/g, an aluminium content between 0.2 and 30% by weight, the amount of the acid sites of the material ranging between 50 and 500 μmol/g, and the material being selected from the group consisting of acidic amorphous aluminium silicates and mesoporous molecular sieves imbedded with zeolite. 2. The process according to claim 1, wherein the feedstock comprises at least one n-olefin selected from the group consisting of C8-C30 n-olefins. 3. The process according to claim 1, wherein in said mesoporous molecular sieves imbedded with zeolite, the mesoporous molecular sieve is MCM-41 with a regular molecular structure. 4. The process according to claim 1, wherein the mesoporous surface area of the catalyst material is more than 300 m2/g. 5. The process according to claim 1, wherein the catalyst material is amorphous aluminium silicate with a mesoporous surface area of more than 300 m2/g. 6. The process according to claim 1, wherein part of the side stream is removed from the distillation column or the combination of the distillation column and the reactor at the upper part thereof. 7. The process according to claim 1, wherein a solvent or a solvent mixture selected from the group of hydrocarbons is added to the feedstock. 8. The process according to claim 1, wherein the feedstock is subjected to drying. 9. The process according to claim 1, wherein the dimerization is performed at a temperature ranging between 25 and 200° C., and at a pressure ranging between 0.001 mbar and 50 bar. 10. The process according to claim 9, wherein said temperature ranges between 50 and 150° C. and said pressure ranges between 0.5 bar and 30 bar. 11. The process according to claim 1, wherein the hydrogenation is performed at a pressure ranging between 5 and 100 bar, and at a temperature ranging between 100 and 400° C., in the presence of a hydrogenation catalyst. 12. The process according to claim 11, wherein said pressure is between 10 and 70 bar and said temperature is between 150 and 250° C. 13. The process according to claim 1, wherein the feedstock comprises 1-decene. 14. The process according to claim 1, wherein the feedstock comprises 1-hexadecene. 15. The process according to claim 1, wherein the feedstock comprises olefins of natural origin produced from biological starting materials. 16. The process according to claim 1, wherein distillation is carried out after the dimerization or the hydrogenation or after both. 17. The process according to claim 1, wherein base oil or base oil component is produced with said process.