WO2020174078A1 - Procédé de production de propane-1,2-diol - Google Patents
Procédé de production de propane-1,2-diol Download PDFInfo
- Publication number
- WO2020174078A1 WO2020174078A1 PCT/EP2020/055242 EP2020055242W WO2020174078A1 WO 2020174078 A1 WO2020174078 A1 WO 2020174078A1 EP 2020055242 W EP2020055242 W EP 2020055242W WO 2020174078 A1 WO2020174078 A1 WO 2020174078A1
- Authority
- WO
- WIPO (PCT)
- Prior art keywords
- lactic acid
- reaction
- conversion
- mpa
- propanediol
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Ceased
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/02—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the alkali- or alkaline earth metals or beryllium
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
- B01J21/10—Magnesium; Oxides or hydroxides thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/06—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of zinc, cadmium or mercury
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/78—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with alkali- or alkaline earth metals
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
- B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
- B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
- B01J23/83—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with rare earths or actinides
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J29/00—Catalysts comprising molecular sieves
- B01J29/03—Catalysts comprising molecular sieves not having base-exchange properties
- B01J29/0308—Mesoporous materials not having base exchange properties, e.g. Si-MCM-41
- B01J29/0316—Mesoporous materials not having base exchange properties, e.g. Si-MCM-41 containing iron group metals, noble metals or copper
- B01J29/0333—Iron group metals or copper
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/0236—Drying, e.g. preparing a suspension, adding a soluble salt and drying
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
- B01J37/00—Processes, in general, for preparing catalysts; Processes, in general, for activation of catalysts
- B01J37/02—Impregnation, coating or precipitation
- B01J37/03—Precipitation; Co-precipitation
- B01J37/031—Precipitation
- B01J37/033—Using Hydrolysis
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C29/00—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring
- C07C29/132—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group
- C07C29/136—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH
- C07C29/147—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of carboxylic acids or derivatives thereof
- C07C29/149—Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom not belonging to a six-membered aromatic ring by reduction of an oxygen containing functional group of >C=O containing groups, e.g. —COOH of carboxylic acids or derivatives thereof with hydrogen or hydrogen-containing gases
Definitions
- DE 10 2008 013 474 A1 describes a process for producing lactic acid from primary alcohols or aldehydes in the presence of a transition metal catalyst.
- the process allows the formation of lactic acid with high selectivity, 1,2-propanediol being formed as a by-product when glycerol is used as the starting material.
- the transition metal catalysts can be used as such, for example in the form of powders, granules, particles or else in extrudate form.
- the catalyst is in supported form, i. used as a so-called supported catalyst, on a suitable support material.
- suitable support materials are, for example, conventional support materials such as silica, aluminum oxide, lanthanum oxide, zirconium oxide, aluminosilicates, synthetic porous materials or clay.
- the catalyst is used in supported form on a support material selected from silica,
- FIG. 3 shows the catalytic activity in the presence of various hydroxides.
- FIG. 1 shows the catalytic performance of the individual catalysts under the following reaction conditions: 0.1 g catalyst, 25% loading, 0.5 g lactic acid, 0.1 g Mg (OH) 2 ,
- Calcium lactate (Ca (LA) 2) over Cu / SiCE was carried out in a 50 ml autoclave with a Teflon inlet. An appropriate amount of the alkaline salt dissolved in 20 ml of deionized water was added along with 0.1 g of Cu / SiCE. In each case, 5.6 mmol of lactate were used. The closed autoclave was flushed five times and brought to 5 MPa with H2. The reaction was carried out at 513 K with 750 rpm stirring carried out. Samples were taken at 0.5, 1, 2, 4 and 8 hours after the temperature reached 513K.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Materials Engineering (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Dispersion Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
La présente invention concerne un procédé de production de propane-1,2-diol à partir d'acide lactique par hydrogénation catalytique en solution aqueuse, par réaction en présence d'une base et/ou d'un sel basique d'un métal alcalin et/ou d'un métal alcalino-terreux.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE102019105105.3 | 2019-02-28 | ||
| DE102019105105.3A DE102019105105A1 (de) | 2019-02-28 | 2019-02-28 | Verfahren zur Herstellung von 1,2-Propandiol |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| WO2020174078A1 true WO2020174078A1 (fr) | 2020-09-03 |
Family
ID=69740344
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| PCT/EP2020/055242 Ceased WO2020174078A1 (fr) | 2019-02-28 | 2020-02-28 | Procédé de production de propane-1,2-diol |
Country Status (2)
| Country | Link |
|---|---|
| DE (1) | DE102019105105A1 (fr) |
| WO (1) | WO2020174078A1 (fr) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE19756171A1 (de) * | 1997-12-17 | 1999-07-01 | Basf Ag | Verfahren zur Hydrierung von Carbonsäuren oder deren Anhydriden oder Estern zu Alkoholen |
| WO2000030744A1 (fr) * | 1998-11-24 | 2000-06-02 | Michigan State University | Hydrogenation catalytique en phase condensee servant a transformer l'acide lactique en propylene glycol |
| WO2001016063A1 (fr) | 1999-09-02 | 2001-03-08 | Wisconsin Alumni Research Foundation | Technique de reduction catalytique de groupes acide carboxylique en groupes hydroxyles dans des acides hydroxycarboxyliques |
| DE102008013474A1 (de) | 2008-03-10 | 2009-09-24 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Katalytisches Verfahren zur Gewinnung von chemischen Grundstoffen aus nachwachsenden Rohstoffen |
-
2019
- 2019-02-28 DE DE102019105105.3A patent/DE102019105105A1/de not_active Withdrawn
-
2020
- 2020-02-28 WO PCT/EP2020/055242 patent/WO2020174078A1/fr not_active Ceased
Patent Citations (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE19756171A1 (de) * | 1997-12-17 | 1999-07-01 | Basf Ag | Verfahren zur Hydrierung von Carbonsäuren oder deren Anhydriden oder Estern zu Alkoholen |
| WO2000030744A1 (fr) * | 1998-11-24 | 2000-06-02 | Michigan State University | Hydrogenation catalytique en phase condensee servant a transformer l'acide lactique en propylene glycol |
| US6403844B1 (en) | 1998-11-24 | 2002-06-11 | Board Of Trustees Of Michigan State University | Condensed phase catalytic hydrogenation of lactic acid to propylene glycol |
| WO2001016063A1 (fr) | 1999-09-02 | 2001-03-08 | Wisconsin Alumni Research Foundation | Technique de reduction catalytique de groupes acide carboxylique en groupes hydroxyles dans des acides hydroxycarboxyliques |
| DE102008013474A1 (de) | 2008-03-10 | 2009-09-24 | Fraunhofer-Gesellschaft zur Förderung der angewandten Forschung e.V. | Katalytisches Verfahren zur Gewinnung von chemischen Grundstoffen aus nachwachsenden Rohstoffen |
Non-Patent Citations (1)
| Title |
|---|
| ANNA KATHARINA BEINE ET AL: "Selective production of glycols from xylitol over Ru on covalent triazine frameworks - suppressing decarbonylation reactions", GREEN CHEMISTRY, vol. 20, no. 6, 1 January 2018 (2018-01-01), GB, pages 1316 - 1322, XP055691253, ISSN: 1463-9262, DOI: 10.1039/C8GC00208H * |
Also Published As
| Publication number | Publication date |
|---|---|
| DE102019105105A1 (de) | 2020-09-03 |
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