Methods for producing C2 to C5 paraffins using a hybrid catalyst comprising gallium metal oxide
US-12030036-B2 · Jul 9, 2024 · US
US2017100711A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017100711-A1 |
| Application number | US-201514877457-A |
| Country | US |
| Kind code | A1 |
| Filing date | Oct 7, 2015 |
| Priority date | Oct 7, 2015 |
| Publication date | Apr 13, 2017 |
| Grant date | — |
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A new crystalline zinc (silico)aluminophosphate molecular sieve designated SSZ-90 is disclosed. SSZ-90 is isostructural with the DFO framework type and is synthesized using an ionic liquid as both the solvent and the structure directing agent. The ionic liquid [Q + A − ] comprises a cation (Q + ) selected from the group consisting of 1,3-diisopropylimidazolium, 1,3-diisobutylimidazolium, and 1-isopropyl-3-isobutylimidazolium and an anion (A − ) which is not detrimental to the formation of the molecular sieve.
Opening claim text (preview).
1 . A crystalline molecular sieve comprising [ZnO 4 ], [AlO 4 ] and [PO 4 ] corner-sharing tetrahedral units and having the DFO framework type. 2 . The molecular sieve of claim 1 , further comprising [SiO 4 ] corner-sharing tetrahedral units. 3 . The molecular sieve of claim 1 , having, in its as-synthesized form, an X-ray diffraction pattern substantially as shown in the following table: 2-Theta d-Spacing, nm Relative Intensity 4.59 ± 0.20 1.922 W 6.16 ± 0.20 1.434 M 7.92 ± 0.20 1.115 VS 8.24 ± 0.20 1.072 S 10.02 ± 0.20 0.882 M 11.44 ± 0.20 0.773 W 12.13 ± 0.20 0.729 W 14.69 ± 0.20 0.603 W 15.44 ± 0.20 0.573 W 15.90 ± 0.20 0.557 W 16.54 ± 0.20 0.536 W 17.22 ± 0.20 0.515 W 18.38 ± 0.20 0.482 W 20.58 ± 0.20 0.431 M 21.10 ± 0.20 0.421 S 4 . The molecular sieve of claim 1 , wherein the molecular sieve, in its as-synthesized form and on an anhydrous basis, is represented by the empirical formula: m Q + :n F:(M x Al y P z )O 2 wherein: (1) Q + represents a cation selected from the group consisting of 1,3-diisopropylimidazolium, 1,3-diisobutylimidazolium, and 1-isopropyl-3-isobutylimidazolium; (2) m is the number of moles of Q + per mole of (M x Al y P z )O 2 , and 0<m≦1; (3) n is the number of moles of fluoride ions per mole of (M x Al y P z )O 2 , and 0<n≦1; (4) M is a metal selected from zinc or a combination of zinc and silicon; (5) x is the mole fraction of M as tetrahedral oxides, and 0<x≦0.5; (6) y is the mole fraction of Al as tetrahedral oxides, and y>0; (7) z is the mole fraction of P as tetrahedral oxides, and z>0; and (8) x+y+z=1. 5 . The molecular sieve of claim 4 , wherein M is zinc. 6 . The molecular sieve of claim 4 , wherein M is a combination of zinc and silicon. 7 . The molecular sieve of claim 4 , wherein m has a value of from 0.01 to 0.5. 8 . The molecular sieve of claim 4 , wherein n has a value of from 0.2 to 0.6. 9 . The molecular sieve of claim 4 , wherein x has a value of from 0.01 to 0.25, y has a value of from 0.3 to 0.7, and z has a value of from 0.25 to 0.7. 10 . A method for preparing a crystalline molecular sieve comprising [ZnO 4 ], [AlO 4 ] and [PO 4 ] corner-sharing tetrahedral units and having the DFO framework type, the method comprising: (a) preparing a reaction mixture containing: (1) at least one source of zinc; (2) optionally, at least one source of silicon; (3) at least one source of aluminum; (4) at least one source of phosphorus; (5) fluoride ions; and (6) an ionic liquid [Q + A − ] comprising a cation (Q + ) selected from the group consisting of 1,3-diisopropylimidazolium, 1,3-diisobutylimidazolium, and 1-isopropyl-3-isobutylimidazolium; and an anion (A − ) which is not detrimental to the formation of the molecular sieve; and (b) maintaining the reaction mixture under crystallization conditions sufficient to form crystals of the molecular sieve. 11 . The method of claim 10 , wherein the reaction mixture comprises, in terms of mole ratios, the following: ZnO/Al 2 O 3 0.05 to 1.5 SiO 2 /Al 2 O 3 0 to 0.90 P 2 O 5 /Al 2 O 3 0.50 to 1.50 F/Al 2 O 3 0.25 to 0.75 [Q + A − /Al 2 O 3 5 to 100 12 . The method of claim 10 , wherein the reaction mixture comprises, in terms of mole ratios, the following: ZnO/Al 2 O 3 0.1 to 1.0 SiO 2 /Al 2 O 3 0.05 to 0.70 P 2 O 5 /Al 2 O 3 0.80 to 1.20 F/Al 2 O 3 0.25 to 0.75 [Q + A − /Al 2 O 3 5 to 40 13 . The method of claim 10 , wherein the anion (A − ) is selected from the group consisting of halides, acetates, phosphates, phosphinates, aluminates, borates, sulfates, sulfonates, imides, amides, and cyanates. 14 . The method of claim 10 , wherein the crystallization conditions include a temperature of from 100° C. to 200° C. 15 . The method of claim 10 , wherein the molecular sieve has, in its as-synthesized form, an X-ray diffraction pattern substantially as shown in the following table:
Silicoaluminophosphates [SAPO compounds] · CPC title
Aluminophosphates containing other elements, e.g. metals, boron · CPC title
Aluminophosphates (APO compounds) · CPC title
using catalysts, e.g. selective catalysts · CPC title
Noble metals · CPC title
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