Catalyst for xylene isomerization and process for preparing the same
View Patent ↗Disclosed herein is a catalyst for xylene isomerization, including: a carrier including a zeolite, having a molar ratio of silica to alumina of 20˜100, impregnated with or mixed with a metal salt (I) having an amount of a metal component of 0.05˜5.0 wt % relative to a zeolite, and an inorganic binder, in which an amount of the zeolite is 10˜90 wt % based on the total amount of the carrier, wherein the carrier is supported with a VIII group metal such that an amount of the VIII group metal is 0.001˜3.0 wt % based on a total amount of the catalyst, or is supported with the VII group metal additionally supported with tin, bismuth or lead such that an amount of the tin, bismuth or lead is 0.01-5.0 wt % based on the total amount of the catalyst, and a method of producing the catalyst. The catalyst for xylene isomerization is advantageous in that, when xylene or C8 aromatic compounds are isomerized using the catalyst, the ethylbenzene conversion is increased while the xylene loss is decreased, compared to conventional technologies.
1. A method of producing a catalyst for xylene isomerization, comprising the steps of:
(i) mixing a metal salt (I) having an amount of a metal component of 0.05˜5.0 wt % relative to a zeolite with the zeolite having a molar ratio of silica to alumina of 20˜100 and an inorganic binder to form a mixture powder so that an amount of the zeolite based on the total amount of the powder mixture is 10˜90 wt %; and
(ii) supporting the mixture powder with a VIII group metal such that an amount of the VIII group metal is 0.001˜3.0 wt % based on a total amount of the catalyst, or supporting the mixture powder with the VIII group metal additionally supported with tin, bismuth or lead such that an amount of the tin, bismuth or lead is 0.01˜5.0 wt % based on the total amount of the catalyst,
wherein the zeolite is selected from the group consisting of ZSM-5, ZSM-8, ZSM-11, ZSM-12, ZSM-23, ZSM-35, ZSM-48, SSZ-46, TS-1, TS-2, mordenite, and Beta, and
the metal salt (I) is selected from consisting of beryllium nitrate, beryllium halide, beryllium acetate, beryllium naphthenate, beryllium gluconate, beryllium citrate, beryllium acetylacetonate, beryllium carbonate, beryllium formate, beryllium sulfate, beryllium hydroxide, magnesium nitrate, magnesium halide, magnesium acetate, magnesium naphthenate, magnesium gluconate, magnesium citrate, magnesium acetylacetonate, magnesium carbonate, magnesium formate, magnesium sulfate, magnesium hydroxide, calcium nitrate, calcium halide, calcium acetate, calcium naphthenate, calcium gluconate, calcium citrate, calcium acetylacetonate, calcium carbonate, calcium formate, calcium sulfate, calcium hydroxide, barium nitrate, barium halide, barium acetate, barium naphthenate, barium gluconate, barium citrate, barium acetylacetonate, barium carbonate, barium formate, barium sulfate, and barium hydroxide.
2. The method of producing a catalyst for xylene isomerization according to claim 1 , wherein the step of mixing the metal salt (I) with the zeolite and the inorganic binder to form the mixture powder is performed sequentially or simultaneously.
3. The method of producing a catalyst for xylene isomerization according to claim 1 , further comprising, before the step of mixing the metal salt (I) with the zeolite and the inorganic binder to form the mixture powder:
mixing a metal salt (II) having an amount of a metal component of 0.001˜3.0 wt % relative to a zeolite with the zeolite having a molar ratio of silica to alumina of 20˜100 to conduct an ion-exchange reaction.
4. The method of producing a catalyst for xylene isomerization according to claim 1 , wherein the zeolite is ZSM-5.
5. The method of producing a catalyst for xylene isomerization according to claim 1 , wherein the VIII group metal is platinum.
6. The method of producing a catalyst for xylene isomerization according to claim 1 , wherein the metal salt (I) is selected from the group consisting of beryllium acetylacetonate, magnesium acetylacetonate, calcium acetylacetonate, barium acetylacetonate, beryllium carbonate, magnesium carbonate, calcium carbonate, and barium carbonate.
7. The method of producing a catalyst for xylene isomerization according to claim 1 , wherein an amount of a metal component of the metal salt (I) is 0.1˜3.0 wt % based on the total amount of the zeolite.
8. The method of producing a catalyst for xylene isomerization according to claim 3 , wherein the metal salt (II) is selected from the group consisting of beryllium nitrate, beryllium halide, beryllium acetate, beryllium citrate, beryllium gluconate, beryllium carbonate, beryllium formate, beryllium sulfate, beryllium hydroxide, magnesium nitrate, magnesium halide, magnesium acetate, magnesium citrate, magnesium gluconate, magnesium carbonate, magnesium formate, magnesium sulfate, magnesium hydroxide, calcium nitrate, calcium halide, calcium acetate, calcium citrate, calcium gluconate, calcium carbonate, calcium formate, calcium sulfate, calcium hydroxide, barium nitrate, barium halide, barium acetate, barium citrate, barium gluconate, barium carbonate, barium formate, barium sulfate, and barium hydroxide.
9. The method of producing a catalyst for xylene isomerization according to claim 3 , wherein the ion-exchange reaction is conducted at a temperature of 30˜250° C.
10. The method of producing a catalyst for xylene isomerization according to claim 1 , wherein the inorganic binder is selected from the group consisting of silica, silica-alumina, alumina, aluminum phosphate, bentonite, kaolin, clinoptilolite, and montmorillonite.
11. A catalyst for xylene isomerization, comprising:
a carrier including a zeolite, having a molar ratio of silica to alumina of 20˜100, impregnated with or mixed with a metal salt (I) having an amount of a metal component of 0.05˜5.0 wt % relative to a zeolite, and an inorganic binder, in which an amount of the zeolite is 10˜90 wt % based on the total amount of the carrier,
wherein the carrier is supported with a VIII group metal such that an amount of the VIII group metal is 0.001˜3.0 wt % based on a total amount of the catalyst, or is supported with the VIII group metal additionally supported with tin, bismuth or lead such that an amount of the tin, bismuth or lead is 0.01˜5.0 wt % based on the total amount of the catalyst,
the zeolite is selected from the group consisting of ZSM-5, ZSM-8, ZSM-11, ZSM-12, ZSM-23, ZSM-35, ZSM-48, SSZ-46, TS-1, TS-2, mordenite, and Beta, and
the metal salt (I) is selected from the group consisting of beryllium nitrate, beryllium halide, beryllium acetate, beryllium naphthenate, beryllium gluconate, beryllium citrate, beryllium acetylacetonate, beryllium carbonate, beryllium formate, beryllium sulfate, beryllium hydroxide, magnesium nitrate, magnesium halide, magnesium acetate, magnesium naphthenate, magnesium gluconate, magnesium citrate, magnesium acetylacetonate, magnesium carbonate, magnesium formate, magnesium sulfate, magnesium hydroxide, calcium nitrate, calcium halide, calcium acetate, calcium naphthenate, calcium gluconate, calcium citrate, calcium acetylacetonate, calcium carbonate, calcium formate, calcium sulfate, calcium hydroxide, barium nitrate, barium halide, barium acetate, barium naphthenate, barium gluconate, barium citrate, barium acetylacetonate, barium carbonate, barium formate, barium sulfate, and barium hydroxide.
12. A catalyst for xylene isomerization, comprising:
a carrier including a zeolite, having a molar ratio of silica to alumina of 20˜100, ion-exchanged with a metal salt (II) having an amount of a metal component of 0.001˜3.0 wt % relative to a zeolite, and impregnated with or mixed with a metal salt (I) having an amount of a metal component of 0.05˜5.0 wt % relative to a zeolite, and an inorganic binder, in which an amount of the zeolite is 10˜90 wt % based on a total amount of the carrier,
wherein the carrier is supported with a VIII group metal such that an amount of the VIII group metal is 0.001˜3.0 wt % based on a total amount of the catalyst, or is supported with the VIII group metal additionally supported with tin, bismuth or lead such that an amount of the tin, bismuth or lead is 0.01˜5.0 wt % based on the total amount of the catalyst,
the zeolite is selected from the group consisting of ZSM-5, ZSM-8, ZSM-11, ZSM-12, ZSM-23, ZSM-35, ZSM-48, SSZ-46, TS-1, TS-2, mordenite, and Beta;
the metal salt (I) is selected from the group consisting of beryllium nitrate, beryllium halide, beryllium acetate, beryllium naphthenate, beryllium gluconate, beryllium citrate, beryllium acetylacetonate, beryllium carbonate, beryllium formate, beryllium sulfate, beryllium hydroxide, magnesium nitrate, magnesium halide, magnesium acetate, magnesium naphthenate, magnesium gluconate, magnesium citrate, magnesium acetylacetonate, magnesium carbonate, magnesium formate, magnesium sulfate, magnesium hydroxide, calcium nitrate, calcium halide, calcium acetate, calcium naphthenate, calcium gluconate, calcium citrate, calcium acetylacetonate, calcium carbonate, calcium formate, calcium sulfate, calcium hydroxide, barium nitrate, barium halide, barium acetate, barium naphthenate, barium gluconate, barium citrate, barium acetylacetonate, barium carbonate, barium formate, barium sulfate, and barium hydroxide; and
the metal salt (II) is selected from the consistinog beryllium nitrate, beryllium halide, beryllium acetate, beryllium citrate, beryllium gluconate, beryllium carbonate, beryllium formate, beryllium sulfate, beryllium hydroxide, magnesium nitrate, magnesium halide, magnesium acetate, magnesium citrate, magnesium gluconate, magnesium carbonate, magnesium formate, magnesium sulfate, magnesium hydroxide, calcium nitrate, calcium halide, calcium acetate, calcium citrate, calcium gluconate, calcium carbonate, calcium formate, calcium sulfate, calcium hydroxide, barium nitrate, barium halide, barium acetate, barium citrate, barium gluconate, barium carbonate, barium formate, barium sulfate, and barium hydroxide.