Desulfurization of a naphtha boiling range feed
US-2018237706-A1 · Aug 23, 2018 · US
US12420257B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-12420257-B2 |
| Application number | US-202118267965-A |
| Country | US |
| Kind code | B2 |
| Filing date | Dec 9, 2021 |
| Priority date | Dec 21, 2020 |
| Publication date | Sep 23, 2025 |
| Grant date | Sep 23, 2025 |
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The present invention relates to a mass for trapping silicon compounds, comprising a porous alumina-based support and at least one metal chosen from the metals from groups VIB and VIIIB, and exhibiting a grain density of at least 1.20 g/ml, a specific surface of at least 300 m 2 /g and pores with a mean size of less than 6.5 nm, as determined by mercury porosimetry. The present invention also relates to a process for the preparation of said trapping mass and to a trapping process using said trapping mass.
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The invention claimed is: 1. A mass for trapping silicon compounds, comprising: a porous alumina-based support and at least one metal chosen from the metals from groups VIB and VIIIB, wherein the porous support exhibits a grain density of at least 1.20 g/ml, a specific surface of at least 300 m 2 /g, and pores with a mean size of less than 6.5 nm, as determined by mercury porosimetry. 2. The trapping mass as claimed in claim 1 , wherein the trapping mass exhibits a grain density of at least 1.25 g/ml. 3. The trapping mass as claimed in claim 1 , wherein the trapping mass exhibits a specific surface of at least 310 m 2 /g. 4. The trapping mass as claimed in claim 1 , wherein the trapping mass exhibits pores with a mean size of less than or equal to 6.0 nm. 5. The trapping mass as claimed in claim 1 , wherein the trapping mass exhibits a monomodal pore size distribution. 6. The trapping mass as claimed claim 1 , wherein the trapping mass exhibits a content of less than 10% by weight of metal from group VIB, expressed as oxide, and/or a content of less than 5% by weight of metal from group VIIIB, expressed as oxide. 7. The trapping mass as claimed in claim 1 , wherein the trapping mass exhibits a content of less than 15% by weight of P, expressed as oxide P 2 O 5 . 8. The trapping mass as claimed in claim 1 , wherein the trapping mass exhibits a total pore volume of between 0.15 cm 3 /g and 0.6 cm 3 /g. 9. A process for the preparation of a mass for trapping silicon compounds, comprising the following stages: a) providing a porous alumina-based support exhibiting a grain density of at least 1.15 g/ml, a specific surface of at least 330 m 2 /g and pores with a mean size of less than 6.5 nm, as determined by mercury porosimetry; b) preparing an aqueous solution containing at least one dissolved metal M precursor, the metal M being chosen from the metals from groups VIB and VIIIB; c) impregnating the porous support resulting from stage a) with the solution obtained in stage b); d) maturing the impregnated support resulting from stage c); and e) drying the matured, impregnated support resulting from stage d). 10. The preparation process as claimed in claim 9 , wherein the porous support exhibits a grain density of at least 1.20 g/ml. 11. The preparation process as claimed in claim 9 , wherein the porous support exhibits a specific surface of at least 340 m 2 /g. 12. The preparation process as claimed in claim 9 , wherein the porous support exhibits pores with a mean size of less than or equal to 6.0 nm. 13. The preparation process as claimed in claim 9 , wherein the trapping mass comprises a porous alumina-based support and at least one metal chosen from the metals from groups VIB and VIIIB, and the porous support exhibits a grain density of at least 1.20 g/ml, a specific surface of at least 300 m 2 /g, and pores with a mean size of less than 6.5 nm. 14. A process for trapping silicon compounds in a gaseous or liquid feedstock, comprising bringing the feedstock into contact with a trapping mass as claimed in claim 1 . 15. The trapping process as claimed in claim 14 , wherein the contacting of the feedstock with the trapping mass is carried out at a temperature of between 20° C. and 500° C., an absolute pressure of between 0.1 MPa and 20 MPa, and a liquid hourly space velocity of between 0.1 h −1 and 50 h −1 or a gas hourly space velocity of between 10 h −1 and 5000 h −1 . 16. The trapping mass as claimed in claim 1 , wherein content of metal from group VIB, expressed as oxide, is between 0.1% and 10% by weight, with respect to the total weight of the trapping mass. 17. The trapping mass as claimed in claim 1 , wherein the content of metal from group VIIIB, expressed as oxide, is between 0.01% and 5% by weight, with respect to the total weight of the trapping mass. 18. The trapping mass as claimed in claim 1 , wherein the trapping mass exhibits a content of P, expressed as oxide P 2 O 5 , of between 0.1% and 15% by weight, with respect to the total weight of the trapping mass. 19. The trapping mass as claimed in claim 1 , wherein the trapping mass exhibits a specific surface of between 310 m 2 /g and 400 m 2 /g. 20. The trapping mass as claimed in claim 1 , wherein the trapping mass exhibits a grain density of between 1.25 g/ml and 1.60 g/ml.
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