Ceramic base material, ceramic support, and separation membrane complex
US-2024399316-A1 · Dec 5, 2024 · US
US2017239641A1 · US · A1
| Field | Value |
|---|---|
| Publication number | US-2017239641-A1 |
| Application number | US-201615049659-A |
| Country | US |
| Kind code | A1 |
| Filing date | Feb 22, 2016 |
| Priority date | Feb 22, 2016 |
| Publication date | Aug 24, 2017 |
| Grant date | — |
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.
A method for preparing an adsorbent is disclosed that includes mixing an NaY zeolite, aqueous Al(OH) 3 , and aqueous KOH, and then heating the resultant mixture for an allotted amount of time to achieve a composition comprising at least 90% single phase chabazite having an Si/Al ratio of 1.0 to 2.2.
Opening claim text (preview).
What is claimed is: 1 . A method for preparing an adsorbent, comprising: (a) mixing NaY zeolite, aqueous Al(OH) 3 , and aqueous KOH; and (b) heating the resultant mixture of step (a) for an allotted amount of time to achieve a composition comprising at least 90% single phase chabazite having an Si/Al ratio of 1.0 to 2.2. 2 . The method of claim 1 , wherein the single phase chabazite comprises a potassium cation with a K:Al molar ratio of at least 0.90. 3 . The method of claim 1 , wherein the heating of step (b) is to about 70° C. to 120° C. and further comprises holding the temperature between 70° C. to 120° C. for 1-8 days. 4 . The method of claim 1 , wherein the heating of step (b) is to about 90° C.-100° C. and further comprises holding the temperature between 90° C. to 100° C. for 1-8 days. 5 . The method of claim 1 , further comprising conducting an ion exchange of the single phase chabazite to yield a single phase NaCHA composition having an Si/Al ratio of 1.0 to 2.2, wherein the Na/Al molar ratio is greater than 0.95. 6 . The method of claim 5 , wherein conducting the ion exchange comprises mixing the composition comprising at least 90% single phase chabazite having an Si/Al ratio of 1.0 to 2.2 with a 1M aqueous solution of NaCl having a 10-fold excess, by mole % of NaCl relative to the moles of potassium cations in the single phase composition until the K is fully exchanged by Na to yield a single phase NaCHA composition. 7 . The method of claim 5 , wherein the single phase NaCHA composition is further ion exchanged to yield a single phase mixed cation CHA including at least two types of cations. 8 . The method of claim 7 , wherein each of the at least two types of cations are in a molar ratio relative to Al of at least 0.05. 9 . The method of claim 5 , further comprising conducting a subsequent ion exchange of the NaCHA composition with an aqueous solution of one or more of Li, Ag, K, Ca, Mg, Zn, Cu, Ba, and Sr cations. 10 . The method of claim 5 , further comprising conducting a subsequent ion exchange of the NaCHA composition with an aqueous solution of Li cations, K cations, or combinations thereof. 11 . The method of claim 5 , further comprising conducting a subsequent ion exchange of the NaCHA composition with an aqueous solution of Li cations to yield a Li,NaCHA composition. 12 . The method of claim 11 , wherein each of the two types of cations of the Li,NaCHA composition are in a molar ratio relative to Al of at least 0.05. 13 . The method of claim 5 , further comprising conducting a subsequent ion exchange of the NaCHA composition with an aqueous solution of K cations to yield a K,NaCHA composition. 14 . The method of claim 13 , wherein each of the two types of cations of the K,NaCHA composition are in a molar ratio relative to Al of at least 0.05. 15 . The method of claim 5 , wherein one equivalent of the NaCHA composition is ion exchanged with a equivalents of K cations in aqueous solution to yield an aK,NaCHA having a K:Na ratio of a:(b−a), where a is the desired number of potassium cations and b is the total number of cations per unit CHA, where the range of b is 11.25 to 18 16 . The method of claim 15 , wherein b is 12 to 18 and a is 1 to 7. 17 . The method of claim 15 , wherein b is about 12.8 to 15.3 and a is 1 to 7. 18 . The method of claim 17 , wherein the mixed cation exchanged chabazite is 1K,NaCHA; 2K,NaCHA; 3K,NaCHA; 4K,NaCHA; or 6K,NaCHA. 19 . The method of claim 1 , wherein the chabazite has a Si/Al ratio from 1.35 to 1.6. 20 . The method of claim 1 , wherein the chabazite has a Si/Al ratio from 1.0 to 2.0.
Noble gases · CPC title
Chemical treatments in view of modifying the properties of the sieve, e.g. increasing the stability or the activity, also decreasing the activity · CPC title
Other types characterised by their X-ray diffraction pattern and their defined composition {(C01B39/023, C01B39/026, C01B39/06 take precedence)} · CPC title
Zeolites · CPC title
by adsorption, e.g. preparative gas chromatography {(solid sorbent compositions B01J20/00, preparation of inorganic compounds or elements C01)} · CPC title
Related publications grouped by family.
Answers are generated from the same data shown on this page.