Isomerization of butene in the ionic liquid-catalyzed alkylation of light isoparaffins and olefins
A process for producing alkylate comprising contacting a first hydrocarbon stream comprising at least one olefin having from 2 to 6 carbon atoms which contains 1-butene with an isomerization catalyst under conditions favoring the isomerization of 1-butene to 2-butene so the isomerized stream contains a greater concentration of 2-butene than the first hydrocarbon stream and contacting the isomerized stream and a second hydrocarbon stream comprising at least one isoparaffin having from 3 to 6 carbon atoms with an acidic ionic liquid catalyst under alkylation conditions to produce an alkylate stream is disclosed.
1. A process for producing alkylate comprising contacting a first hydrocarbon stream comprising at least one olefin having from 2 to 6 carbon atoms which contains 1-butene with an isomerization catalyst under conditions favoring the isomerization of 1-butene to 2-butene so the isomerized stream contains a greater concentration of 2-butene than the first hydrocarbon stream and contacting the isomerized stream and a second hydrocarbon stream comprising at least one isoparaffin having from 3 to 6 carbon atoms with an acidic ionic liquid catalyst under alkylation conditions to produce an alkylate stream; where the acidic ionic acidic ionic liquid is a chloroaluminate ionic liquid prepared by mixing aluminum trichloride (AlCl 3 ) and a hydrocarbyl substituted pyridinium halide, a hydrocarbyl substituted imidazolium halide, trialkylammonium hydrohalide or tetraalkylammonium halide of the general formulas A, B, C and D, respectively,
where R═H, methyl, ethyl, propyl, butyl, pentyl or hexyl group and X is a halide and preferably a chloride, and R 1 and R 2 ═H, methyl, ethyl, propyl, butyl, pentyl or hexyl group and where R 1 and R 2 may or may not be the same, and R 3 , R 4 , and R 5 and R 6 =methyl, ethyl, propyl, butyl, pentyl or hexyl group and where R 3 , R 4 , R 5 and R 6 may or may not be the same; and wherein the acidic ionic liquid catalyst further comprises an alkyl halide.
2. In an alkylation process in which at least one olefin having from 2 to 6 carbon atoms, which contains 1-butene and at least one isoparaffin having from 3 to 6 carbon atoms are contacted in an alkylation zone under alkylation conditions with a catalyst comprising an acidic ionic liquid to produce an alkylate stream, the improvement comprising contacting at least a portion of the at least one olefin with an isomerization catalyst under conditions favoring the isomerization of 1-butene to 2-butene so the isomerized stream contains a greater concentration of 2-butene than the at least one olefin stream; where the acidic ionic acidic ionic liquid is a chloroaluminate ionic liquid prepared by mixing aluminum trichloride (AlCl 3 ) and a hydrocarbyl substituted pyridinium halide, a hydrocarbyl substituted imidazolium halide, trialkylammonium hydrohalide or tetraalkylammonium halide of the general formulas A, B, C and D, respectively,
where R═H, methyl, ethyl, propyl, butyl, pentyl or hexyl group and X is a halide and preferably a chloride, and R 1 and R 2 ═H, methyl, ethyl, propyl, butyl, pentyl or hexyl group and where R 1 and R 2 may or may not be the same, and R 3 , R 4 , and R 5 and R 6 =methyl, ethyl, propyl, butyl, pentyl or hexyl group and where R 3 , R 4 , R 5 and R 6 may or may not be the same; and wherein the acidic ionic liquid catalyst further comprises an alkyl halide.
3. A process for producing alkylate comprising contacting a first hydrocarbon stream comprising at least one olefin having from 2 to 6 carbon atoms which contains 1-butene with an isomerization catalyst under conditions favoring the isomerization of 1-butene to 2-butene so the isomerized stream contains a greater concentration of 2-butene than the first hydrocarbon stream and contacting the isomerized stream and a second hydrocarbon stream comprising at least one isoparaffin having from 3 to 6 carbon atoms with an acidic ionic liquid catalyst under alkylation conditions to produce an alkylate stream having a RON of at least 93; where the acidic ionic acidic ionic liquid is a chloroaluminate ionic liquid prepared by mixing aluminum trichloride (AlCl 3 ) and a hydrocarbyl substituted pyridinium halide, a hydrocarbyl substituted imidazolium halide, trialkylammonium hydrohalide or tetraalkylammonium halide of the general formulas A, B, C and D, respectively,
where R═H, methyl, ethyl, propyl, butyl, pentyl or hexyl group and X is a halide and preferably a chloride, and R 1 and R 2 ═H, methyl, ethyl, propyl, butyl, pentyl or hexyl group and where R 1 and R 2 may or may not be the same, and R 3 , R 4 , and R 5 and R 6 =methyl, ethyl, propyl, butyl, pentyl or hexyl group and where R 3 , R 4 , R 5 and R 6 may or may not be the same; and wherein the acidic ionic liquid catalyst further comprises an alkyl halide.
4. In an alkylation process in which at least one olefin having from 2 to 6 carbon atoms, which contains 1-butene and at least one isoparaffin having from 3 to 6 carbon atoms are contacted in an alkylation zone under alkylation conditions with a catalyst comprising an acidic ionic liquid, the improvement comprising contacting at least a portion of the at least one olefin with an isomerization catalyst selected from the group of a catalyst comprising crystalline aluminosilicate in an alumina carder with platinum-group and Group IV-A metallic components, a catalyst comprising a phosphate, a catalyst having silica-alumina as an acidic component without zeolite, and ZSM-5, under conditions favoring the isomerization of 1-butene to 2-butene so the isomerized stream contains a greater concentration of 2-butene than the at least one olefin stream; where the acidic ionic acidic ionic liquid is a chloroaluminate ionic liquid prepared by mixing aluminum trichloride (AlCl 3 ) and a hydrocarbyl substituted pyridinium halide, a hydrocarbyl substituted imidazolium halide, trialkylammonium hydrohalide or tetraalkylammonium halide of the general formulas A, B, C and D, respectively,
where R═H, methyl, ethyl, propyl, butyl, pentyl or hexyl group and X is a halide and preferably a chloride, and R 1 and R 2 ═H, methyl, ethyl, propyl, butyl, pentyl or hexyl group and where R 1 and R 2 may or may not be the same, and R 3 , R 4 , and R 5 and R 6 =methyl, ethyl, propyl, butyl, pentyl or hexyl group and where R 3 , R 4 , R 5 and R 6 may or may not be the same; and wherein the acidic ionic liquid catalyst further comprises an alkyl halide.
5. The process according to claim 1 , wherein the acidic ionic liquid is selected from the group consisting of 1-butyl-4-methyl-pyridinium chloroaluminate (BMP), 1-butyl-pyridinium chloroaluminate (BP), 1-butyl-3-methyl-imidazolium chloroaluminate BMIM) and 1-H-pyridinium chloroaluminate (HP).
6. The process according to claim 4 , wherein the isomerization catalyst is ZSM-5.
7. The process according to claim 4 , wherein the catalyst comprising the phosphate is selected from the group consisting of an ammonium phosphate a precipitated aluminum phosphate within a silica gel network, a chromium-nickel phosphate, a solid phosphoric acid on silica, a catalyst containing aluminum phosphate and titanium compounds, a catalyst consisting essentially of chromium and amorphous aluminum phosphate, and a phosphorus-containing zeolite.
8. The process according to claim 1 , claim 2 , claim 3 , or claim 4 , wherein the isoparaffin is selected from the group consisting of isobutane, isopentanes and mixtures thereof.
9. The process of claim 1 , claim 2 , or claim 3 , wherein the isomerization catalyst is selected from the group of a catalyst comprising crystalline aluminosilicate in an alumina carrier with platinum-group and Group IV-A metallic components, a catalyst comprising phosphate, a catalyst having silica-alumina as an acidic component without zeolite, and ZSM-5.
10. The process of claim 9 , wherein the isomerization catalyst is ZSM-5.
11. The process according to claim 9 , wherein the catalyst comprising the phosphate is selected from the group consisting of an ammonium phosphate, a precipitated aluminum phosphate within a silica gel network, a chromium-nickel phosphate, a solid phosphoric acid on silica, a catalyst containing aluminum phosphate and titanium compounds, and a catalyst consisting essentially of chromium, amorphous aluminum phosphate, and a phosphorus-containing zeolite.
12. The process according to claim 1 , or claim 3 , wherein the first hydrocarbon stream contains up to 25% 1-butene.
13. The process according to claim 1 , or claim 3 , wherein the alkylation conditions include a catalyst volume in the reactor of from 5 vol % to 50 vol %, a temperature of from −10°C. to 100°C., a pressure of from 300 kPA to 2500 kPa, an isopentane to olefin molar ratio of from 2 to 8 and a residence time of 1 minute to 1 hour.
14. The process of claim 1 , or claim 3 , wherein the alkylate stream has 0.0 wt % n-octane.
15. The process according to claim 1 , or claim 3 , where the alkyl halide is selected from the group consisting of methyl halide, ethyl halide, propyl halide, 1-butyl halide, 2-butyl halide, tertiary butyl halide, pentyl halides, iospentyl halide, hexyl halides, isohexyl halides, heptyl halides, isoheptyl halides, octyl halides and isooctyl halides.
16. The process according to claim 1 , or claim 3 , wherein the isomerizaton catalyst comprises a zeolitic molecular sieve.
17. The process according to claim 1 , or claim 3 , further comprising recovering high quality gasoline blending components of low volatility.
18. The process of claim 1 , or claim 3 , wherein the alkylate stream has a RON that is increased from 5 to 32 numbers compared to a comparison alkylate stream made from the first hydrocarbon stream without the step of contacting with the isomerization catalyst.
19. The process according to claim 2 , or claim 4 , wherein the olefin stream contains up to 25% 1-butene.
20. The process according to claim 2 , or claim 4 , wherein the isoparaffin is selected from the group consisting of isobutane, isopentanes and mixtures thereof.
21. The process of claim 2 , or claim 4 , wherein the alkylate stream has a RON that is increased from 5 to 32 numbers compared to a comparison alkylate stream made without the step of contacting with the isomerization catalyst.