Molecular sieves mediated unsaturated hydrocarbon separation and related compositions, materials, methods and systems
US-10112878-B2 · Oct 30, 2018 · US
US10427995B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-10427995-B2 |
| Application number | US-201816146019-A |
| Country | US |
| Kind code | B2 |
| Filing date | Sep 28, 2018 |
| Priority date | Dec 24, 2015 |
| Publication date | Oct 1, 2019 |
| Grant date | Oct 1, 2019 |
A practical reading order for non-experts. Skip the full description unless you need deep technical detail.
What the patent document calls the invention.
A short plain-language summary of the technical disclosure.
Who owns or filed the patent and who is credited as inventor.
Filing, priority, publication, and grant dates set the timeline.
The legal scope of protection — read this for what is actually claimed.
Technology tags used to group this patent with similar filings.
Prior art links and similar publications in this corpus.
Official abstract text for this publication.
Described herein are compositions having an eight-membered monocyclic unsaturated hydrocarbon, methods and system to separate the eight-membered monocyclic unsaturated hydrocarbon at from a hydrocarbon mixture including additional nonlinear unsaturated C8H2m hydrocarbons with 4≤m≤8, by contacting the hydrocarbon mixture with a 10-ring pore molecular sieve having a sieving channel with a 10-ring sieving aperture with a minimum crystallographic free diameter greater than 3 Å and a ratio of the maximum crystallographic free diameter to the minimum crystallographic free diameter between 1 and 2, the molecular sieve having a T1/T2 ratio≥20:1 wherein T1 is an element independently selected from Si and Ge, and T2 is an element independently selected from Al, B and Ga, the 10-ring pore molecular sieve further having a counterion selected from NH4+, Na+, K+ and Ca++.
Opening claim text (preview).
What is claimed is: 1. A sieved hydrocarbon mixture obtained by separating an eight-membered monocyclic unsaturated hydrocarbon from a hydrocarbon mixture further comprising additional nonlinear unsaturated C 8 H 2m hydrocarbons with 4≤m≤8, wherein separating the eight-membered monocyclic unsaturated hydrocarbon comprises providing a 10-ring pore molecular sieve having a sieving channel with a 10-ring sieving aperture with a minimum crystallographic free diameter greater than 3 Å and a ratio of the maximum crystallographic free diameter to the minimum crystallographic free diameter between 1 and 2, the 10-ring pore molecular sieve having a T1/T2 ratio≥20:1 wherein T1 is an element independently selected from Si and Ge or a combination thereof, and T2 is an element independently selected from Al, B and Ga or a combination thereof, the 10-ring pore molecular sieve further having a counterion selected from NH 4 + , Li + , Na + , K + and Ca ++ or a combination thereof, and contacting the hydrocarbon mixture with the 10-ring pore molecular sieve at a temperature of −20° C. to 60° C. for a time and under conditions to obtain a sieved hydrocarbon mixture comprising the eight-membered monocyclic unsaturated hydrocarbon at a separation concentration C s >C i , wherein the 10-ring pore molecular sieve has a framework type selected from group consisting of MEL, TUN, IMF, MFI, OBW, MFS and TER, and wherein, the sieved hydrocarbon mixture comprises the eight-membered monocyclic unsaturated hydrocarbon at a separation concentration Cs≥99.3% wt. 2. The sieved hydrocarbon mixture of claim 1 , wherein the eight-membered monocyclic unsaturated hydrocarbon is selected from or a combination thereof. 3. The sieved hydrocarbon mixture of claim 1 , wherein the eight-membered monocyclic unsaturated hydrocarbon is 4. The hydrocarbon mixture of claim 1 , wherein in the 10-ring pore molecular sieve is a 10-ring pore intermediate molecular sieve wherein the minimum crystallographic free diameter is equal to or greater than 4.5 Å to less than 5 Å and the ratio of the maximum crystallographic free diameter to the minimum crystallographic free diameter is between 1.1 and 1.25. 5. The hydrocarbon mixture of claim 1 , wherein in the 10-ring pore molecular sieve is a 10-ring pore wide molecular sieve wherein the minimum crystallographic free diameter is equal to or greater than 5.0 Å to less than 6 Å and the ratio of the maximum crystallographic free diameter to the minimum crystallographic free diameter is between 1.0 and 1.1. 6. The hydrocarbon mixture of claim 1 , wherein in the 10-ring pore molecular sieve, the sieving channel is interconnected to one or more sieving channels and/or venting channels to form a 2D channels network. 7. The hydrocarbon mixture of claim 1 , wherein in the 10-ring pore molecular sieve, the sieving channel is interconnected to one or more sieving channels and/or venting channels to form a 3D channels network. 8. The hydrocarbon mixture of claim 1 , wherein the 10-ring pore molecular sieve has a framework type selected from the group consisting of MEL, TUN, IMF, MFI, OBW, and TER. 9. The hydrocarbon mixture of claim 1 , wherein the 10-ring pore molecular sieve is selected from the group consisting of ZSM-5, ZSM-11, IM-5, ZSM-57, OSB-2, Terranovaite, and TNU-9. 10. A hydrocarbon mixture comprising an eight-membered monocyclic unsaturated hydrocarbon and additional nonlinear unsaturated C 8 H 2m hydrocarbons with 4≤m≤8, the eight-membered monocyclic unsaturated hydrocarbon comprised in the hydrocarbon mixture at a concentration of at least 99.5% wt. 11. The hydrocarbon mixture of claim 10 , wherein the eight-membered monocyclic unsaturated hydrocarbon comprised in the hydrocarbon mixture at a concentration of at least 99.7% wt. 12. The hydrocarbon mixture of claim 11 , wherein the eight-membered monocyclic unsaturated hydrocarbon is selected from the group consisting of or a combination thereof. 13. The hydrocarbon mixture of claim 11 , wherein the eight-membered monocyclic unsaturated hydrocarbon is 14. The hydrocarbon mixture of claim 11 , wherein the eight-membered monocyclic unsaturated hydrocarbon is 15. The hydrocarbon mixture of claim 10 , wherein the eight-membered monocyclic unsaturated hydrocarbon comprised in the hydrocarbon mixture at a concentration of at least 99.8% wt. 16. The hydrocarbon mixture of claim 15 , wherein the eight-membered monocyclic unsaturated hydrocarbon is selected from the group consisting of or a combination thereof. 17. The hydrocarbon mixture of claim 15 , wherein the eight-membered monocyclic unsaturated hydrocarbon is 18. The hydrocarbon mixture of claim 15 , wherein the eight-membered monocyclic unsaturated hydrocarbon is 19. The hydrocarbon mixture of claim 10 , wherein the eight-membered monocyclic unsaturated hydrocarbon comprised in the hydrocarbon mixture at a concentration of at least 99.9% wt. 20. The hydrocarbon mixture of claim 19 , wherein the eight-membered monocyclic unsaturated hydrocarbon is selected from the group consisting of or a combination thereof. 21. The hydrocarbon mixture of claim 19 , wherein the eight-membered monocyclic unsaturated hydrocarbon is 22. The hydrocarbon mixture of claim 19 , wherein the eight-membered monocyclic unsaturated hydrocarbon is 23. The hydrocarbon mixture of claim 10 , wherein the eight-membered monocyclic unsaturated hydrocarbon comprised in the hydrocarbon mixture at a concentration of at least 99.99% wt. 24. The hydrocarbon mixture of claim 23 , wherein the eight-membered monocyclic unsaturated hydrocarbon is selected from the group consisting of or a combination thereof. 25. The hydrocarbon mixture of claim 23 , wherein the eight-membered monocyclic unsaturated hydrocarbon is 26. The hydrocarbon mixture of claim 23 , wherein the eight-membered monocyclic unsaturated hydrocarbon is 27. The hydrocarbon mixture of cla
Related publications grouped by family.
Answers are generated from the same data shown on this page.