Renewable olefins from a mixture of acetic acid and propionic acid
US-9212106-B2 · Dec 15, 2015 · US
US9550715B2 · US · B2
| Field | Value |
|---|---|
| Publication number | US-9550715-B2 |
| Application number | US-201414896969-A |
| Country | US |
| Kind code | B2 |
| Filing date | May 26, 2014 |
| Priority date | Jun 10, 2013 |
| Publication date | Jan 24, 2017 |
| Grant date | Jan 24, 2017 |
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The invention relates to a method for synthesizing glycolic acid or one of the salts thereof, including the following step: placing glycerol and an oxidizing agent in contact with one another in a reaction medium in the presence of a silver-based catalyst on a substrate, said substrate including a material selected from the group consisting of CeO 2 , basic Al 2 O 3 optionally doped with a calcium or cerium oxide, an amphoteric resin, ZrO 2 , and a mixture of said materials. The invention also relates to the use of a silver-based catalyst on a substrate that can be used in said method.
Opening claim text (preview).
The invention claimed is: 1. A process for the synthesis of glycolic acid or one of its salts comprising the following step: bringing glycerol and an oxidizing agent into contact in a reaction medium in the presence of a catalyst based on silver on a support, said support comprising a material chosen from the group consisting of CeO 2 , basic Al 2 O 3 , optionally doped with a calcium or cerium oxide, an amphoteric resin, ZrO 2 and a mixture of these materials; wherein a base which produces hydroxide ions is present in the reaction medium; and wherein the molar ratio of hydroxide ions to glycerol [OH]/[gly] brought together is from 0.5 to 1.2. 2. The process as claimed in claim 1 , wherein said catalyst is a catalyst on a support of formula Ag/CeO 2 , basic Ag/Al 2 O 3 , optionally doped with calcium oxide or with cerium oxide, or Ag/IR45. 3. The process as claimed in claim 1 , wherein the catalyst comprises, as metal entity, only silver. 4. The process as claimed in claim 1 , wherein the pH of the reaction medium is greater than or equal to 8. 5. The process as claimed in claim 1 , wherein which said oxidizing agent is oxygen. 6. The process as claimed in claim 1 , wherein which the temperature of the reaction medium is chosen within a range extending from 50 to 150° C. 7. The process as claimed in claim 1 , wherein the catalyst based on silver on a support is a catalyst, the proportion by weight of silver with respect to the support of which varies from 10 to 0.2%. 8. The process as claimed in claim 1 , wherein the glycerol/catalyst ratio by weight in the reaction medium is chosen within a range extending from 2 to 100. 9. The process as claimed in claim 1 , wherein the glycerol is of vegetable origin. 10. The process as claimed in claim 1 , wherein the amounts of calcium or cerium oxides optionally used are less than 3 mmol of the atom used with respect to 1 g of support.
of oxygen-containing groups to carboxyl groups · CPC title
of —CHO groups or primary alcohol groups · CPC title
Precipitation on carriers · CPC title
Silver · CPC title
Glycolic acid · CPC title
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