Zeolite with improved hydro-isomerization activity
According to an aspect of the present invention, provided is a zeolite catalyst having an MRE structure for hydro-isomerization. The zeolite catalyst has an adsorption volume ratio of lutidine to collidine measured by Fourier-transform infrared spectroscopy (FTIR) using lutidine and collidine as adsorbents of greater than 3 and less than or equal to 10. According to an aspect of the present invention, provided is a method of hydro-isomerization for a hydrocarbon feedstock, including subjecting the hydrocarbon feedstock to a hydro-isomerization reaction under conditions of a temperature of 200° C. to 500° C., a hydrogen pressure of 1 to 200 atmospheres, a liquid space velocity (LHSV) of 1.0 to 10.0 hr −1 , and the hydrogen/feedstock ratio of 45 to 1780 Nm 3 /m 3 in the presence of the zeolite catalyst.
1. A zeolite catalyst having an MRE structure for a hydro-isomerization reaction,
wherein the zeolite catalyst having an MRE structure is selected from the group consisting of EU-2, ZSM-48, and ZBM-30,
wherein the zeolite catalyst has an adsorption volume ratio of lutidine to collidine greater than 3 and less than or equal to 10, as measured by Fourier-transform infrared spectroscopy (FTIR) using lutidine and collidine as adsorbents,
wherein the zeolite catalyst has a silica-alumina ratio (SAR) of 100 to 200, and
wherein the zeolite catalyst has a BET surface area greater than or equal to 250 m 2 /g and not greater than 300 m 2 /g.
2. The zeolite catalyst of claim 1 , wherein an adsorption volume ratio of lutidine to collidine is greater than or equal to 8 measured by FTIR using lutidine and collidine as adsorbents.
3. The zeolite catalyst of claim 1 , wherein the zeolite catalyst has silica-alumina ratio (SAR) of 120 to 200.
4. The zeolite catalyst of claim 1 , wherein the zeolite catalyst has silica-alumina ratio (SAR) of 150 to 170.
5. The zeolite catalyst of claim 1 , wherein the zeolite catalyst has a total volume of pores having a diameter in a range of greater than 50 nm of less than 0.1 cc/g.
6. The zeolite catalyst of claim 5 , wherein the zeolite catalyst has a total volume of pores having a diameter in a range of 2 to 50 nm of less than 0.2 cc/g.
7. The zeolite catalyst of claim 1 , wherein the zeolite catalyst has a morphology selected from the group consisting of a granular shape, a needle shape, and a rod shape.
8. The zeolite catalyst of claim 7 , wherein the zeolite catalyst has a granular shape.
9. A method of hydro-isomerization for a hydrocarbon feedstock, the method comprising:
subjecting the hydrocarbon feedstock to a hydro-isomerization reaction under conditions of a temperature of 200° C. to 500° C., a hydrogen pressure of 1 to 200 atmospheres, a liquid space velocity (LHSV) of 1.0 to 10.0 hr −1 , and a hydrogen/feedstock ratio of 45 to 1780 Nm 3 /m 3 in the presence of the zeolite catalyst of claim 1 .
10. The method of claim 9 , wherein at least some of the hydrocarbons in the feedstock have a number of carbon atoms of at least 22.