Aryl, heteroaryl, and heterocyclic compounds for treatment of immune and inflammatory disorders
US-2024199583-A1 · Jun 20, 2024 · US
US9920064B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9920064-B2 |
| Application number | US-201515322584-A |
| Country | US |
| Kind code | B2 |
| Filing date | Jul 3, 2015 |
| Priority date | Jul 16, 2014 |
| Publication date | Mar 20, 2018 |
| Grant date | Mar 20, 2018 |
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The present invention addresses the problem of providing a solid catalyst capable of achieving high selectivity and high yield for isosorbide, preferably at the same time, in a dehydration reaction by which dianhydrosugar alcohol is obtained from a sugar alcohol, particularly, in a dehydration reaction by which isosorbide is obtained from sorbitol. The above-mentioned problem is solved by a solid catalyst for a dehydration reaction for preparing dianhydrosugar alcohol from sugar alcohol, said catalyst including an H-type β zeolite having an atomic composition ratio of Si to Al (Si/Al) of more than 20.
Opening claim text (preview).
The invention claimed is: 1. A solid, catalyst for a dehydration catalyst, comprising an H-type β zeolite having an atomic composition ratio of Si to Al (Si/Al) of more than 20. 2. The solid, dehydration catalyst according to claim 1 , wherein the Si/Al ratio is 400 or less. 3. A method for producing a dianhydrosugar alcohol from a sugar alcohol, comprising bringing the sugar alcohol into contact with the catalyst according to claim 1 . 4. The method according to claim 3 , wherein the amount of the H-type β zeolite contained in the catalyst is 5 to 60 parts by mass, based on 100 parts by mass of the sugar alcohol. 5. The method according to claim 3 , further comprising maintaining the sugar alcohol brought into contact with the catalyst under ambient pressure or under reduced pressure. 6. The method according to claim 3 , further comprising maintaining the sugar alcohol brought into contact with the catalyst at a temperature of 110° C. to 170° C. 7. The method according to claim 3 , further comprising maintaining the sugar alcohol brought into contact with the catalyst for 1.5 hours or more. 8. The method according to claim 3 , wherein the sugar alcohol is selected from the group consisting of sorbitol, mannitol and iditol. 9. The method according to claim 3 , wherein the sugar alcohol is sorbitol, and the dianhydrosugar alcohol is isosorbide.
Zeolite Beta · CPC title
Ortho-condensed systems · CPC title
Other general methods · CPC title
of types characterised by their specific structure not provided for in groups B01J29/08 - B01J29/65 · CPC title
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