US20060016695A1 - Process for preparing 2-alkyne 1-acetals - Google Patents
Process for preparing 2-alkyne 1-acetals Download PDFInfo
- Publication number
- US20060016695A1 US20060016695A1 US11/186,100 US18610005A US2006016695A1 US 20060016695 A1 US20060016695 A1 US 20060016695A1 US 18610005 A US18610005 A US 18610005A US 2006016695 A1 US2006016695 A1 US 2006016695A1
- Authority
- US
- United States
- Prior art keywords
- general formula
- compound
- carried out
- formula iii
- process according
- 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.)
- Abandoned
Links
- 0 [1*]C#CC(O[2*])O[3*] Chemical compound [1*]C#CC(O[2*])O[3*] 0.000 description 9
- NCQJSSVURLAURE-UHFFFAOYSA-N C#CC(OC)OC.C#CCO Chemical compound C#CC(OC)OC.C#CCO NCQJSSVURLAURE-UHFFFAOYSA-N 0.000 description 2
- IHPWBFYLFUOMQF-UHFFFAOYSA-N COC(C#CCO)OC.COC(O)C#CC(OC)OC.OCC#CCO Chemical compound COC(C#CCO)OC.COC(O)C#CC(OC)OC.OCC#CCO IHPWBFYLFUOMQF-UHFFFAOYSA-N 0.000 description 1
- DVFWCKLXFYGIIA-UHFFFAOYSA-N NC#CC(ON)ON Chemical compound NC#CC(ON)ON DVFWCKLXFYGIIA-UHFFFAOYSA-N 0.000 description 1
Classifications
-
- C—CHEMISTRY; METALLURGY
- C25—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES; APPARATUS THEREFOR
- C25B—ELECTROLYTIC OR ELECTROPHORETIC PROCESSES FOR THE PRODUCTION OF COMPOUNDS OR NON-METALS; APPARATUS THEREFOR
- C25B3/00—Electrolytic production of organic compounds
- C25B3/20—Processes
- C25B3/23—Oxidation
Definitions
- the present invention relates to a process for preparing 2-alkyne 1-acetals.
- R 3 is a radical of the general formula II.
- the radical R 1 which occurs therein 3 times preferably has the same meaning on each occurrence.
- the compound of the general formula III is used as such, i.e. no alcohol A is used but instead the starting compound of the general formula III performs the function of the alcohol A which acetalates the oxidation product of the compound of the general formula III.
- radical R 1 preference is given to compounds of the general formula I in which is hydrogen, a C 1 -C 6 -alkyl radical or a C 1 -C 6 -alkyl radical substituted by a hydroxyl group. Accordingly, compounds of the general formula 11 in which the radical R 1 is hydrogen, a C 1 -C 6 -alkyl radical or a C 1 -C 6 -alkyl radical substituted by a hydroxyl group are then used as starting compounds.
- a further compound of the general formula I which is very particularly preferably prepared is 1,1,4,4-tetramethoxybut-2-yne.
- Starting materials used then are 2-butyne-1,4-diol as compound of the general formula III and methanol as alcohol A.
- the alcohols A and the compound of the general formula III are generally used in a molar ratio of 2:1, based on the alcoholic hydroxyl groups present in the compound of the formula III, or the alcohol A is used in excess and then serves simultaneously as solvent or diluent for the compound of the general formula III and the compound of the general formula I formed.
- customary cosolvents are added to the electrolysis solution. These are the inert solvents having a high oxidation potential which are customarily used in organic chemistry. Examples which may be mentioned are dimethyl carbonate and propylene carbonate.
- Water is also suitable in principle as cosolvent; the proportion of water in the electrolyte is preferably less than 20% by weight.
- Electrolyte salts present in the electrolysis solution are generally alkali metal, tetra(C 1 -C 6 -alkyl)ammonium, preferably tri(C 1 -C 6 -alkyl)methylammonium, salts.
- Suitable counterions are sulfate, hydrogensulfate, alkylsulfates, arylsulfates, halides, phosphates, carbonates, alkylphosphates, alkylcarbonates, nitrate, alkoxides, tetrafluoroborate and perchlorate.
- acids derived from the abovementioned anions are also possible as electrolyte salts, i.e., for example, sulfuric acid, sulfonic acids and carboxylic acids.
- electrolyte salts are ionic liquids.
- Suitable ionic liquids are described in “Ionic Liquids in Synthesis”, Editors Peter Wasserscheid, Tom Welton, Verlag Wiley VCH, 2003, Chapters 1 to 3.
- the process of the invention can be carried out in all customary types of divided or undivided electrolysis cells. It is preferably carried out continuously in undivided flow-through cells.
- Bipolar capillary gap cells or plate stack cells in which the electrodes are configured as plates and arranged in a parallel fashion are very particularly suitable.
- Graphite is preferred as electrode material.
- the feed rate of the starting materials is generally chosen so that the weight ratio of the compounds of the general formula 11 used to the compounds of the general formula I formed in the electrolyte is from 10:1 to 0.05:1.
- the current densities at which the process is carried out are generally in the range from 1 to 1000 mA/cm 2 , preferably from 10 to 100 mA/cm 2 .
- the process is generally carried out at atmospheric pressure. Higher pressures are preferably employed when the process is to be carried out at relatively high temperatures, so as to avoid boiling of the starting compounds or the solvent.
- Suitable anode materials are, for example, noble metals such as platinum or metal oxides such as ruthenium or chromium oxide or mixed oxides of the RuO x TiO x type and also diamond electrodes. Preference is given to graphite or carbon electrodes.
- Possible cathode materials are, for example, iron, steel, stainless steel, nickel or noble metals such as platinum and also graphite or carbon materials and also diamond electrodes. Preference is given to the system graphite as anode and cathode and also graphite as anode and nickel, stainless steel or steel as cathode.
- the electrolyte solution is worked up by conventional separation methods.
- the electrolysis solution is in general firstly distilled and the individual compounds are obtained separately in the form of different fractions. Further purification can be carried out, for example, by crystallization, extraction, distillation or chromatography.
- An undivided plate stack cell having graphite anodes and steel cathodes was used. 160 g of 2-propyn-1-ol in 640 g of methanol were reacted with 5.3 g of sulfuric acid at a temperature of 20° C. for 19 hours. The electrolysis was carried out at 3.4 A/dm2 and an amount of charge of 2 F based on the 2-propyn-1-ol used was passed through the cell. The output from the electrolysis contained 8.8 GC-% by area of 1,1-dimethoxy-2-propyne (conversion: 49%, yield: 30%).
- a divided parallel plate cell having a graphite anode and steel cathode was used.
- 401 g of 2-propynol in 1400 g of methanol and 38 g of MTBS (methyltributylammonium methylsulfate) in the anode space and 941 g of methanol and 24 g of MTBS in the cathode space were reacted at a temperature of 20° C. for 38 hours.
- the electrolysis was carried out at 3.1 A/dm 2 and an amount of charge of 2 F based on the 2-propyn-1-ol used was passed through the cell.
- the anolyte contained 8.3 GC-% by area of 1,1-dimethoxy-2-propyne (conversion: 91%, yield 19%).
- a divided parallel plate cell having a graphite anode and steel cathode was used. 13 g of 2-butyne-1,4-diol in 117 g of methanol and 3.8 g of MTBS (methyltributylammonium methylsulfate) in the anode space and 130 g of methanol and 3.8 g of MTBS in the cathode space were reacted at a temperature of 19° C. for 14 hours. The electrolysis was carried out at 3.4 A/dm 2 and an amount of charge of 4 F based on the 2-butyne-1,4-diol used was passed through the cell.
- MTBS methyltributylammonium methylsulfate
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Engineering & Computer Science (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Electrochemistry (AREA)
- Materials Engineering (AREA)
- Metallurgy (AREA)
- Electrolytic Production Of Non-Metals, Compounds, Apparatuses Therefor (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Steroid Compounds (AREA)
- Low-Molecular Organic Synthesis Reactions Using Catalysts (AREA)
Applications Claiming Priority (2)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE102004035860.5 | 2004-07-23 | ||
DE102004035860A DE102004035860A1 (de) | 2004-07-23 | 2004-07-23 | Verfahren zur Herstellung von 2-Alkin-1 acetalen |
Publications (1)
Publication Number | Publication Date |
---|---|
US20060016695A1 true US20060016695A1 (en) | 2006-01-26 |
Family
ID=34937539
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
US11/186,100 Abandoned US20060016695A1 (en) | 2004-07-23 | 2005-07-21 | Process for preparing 2-alkyne 1-acetals |
Country Status (6)
Country | Link |
---|---|
US (1) | US20060016695A1 (ja) |
EP (1) | EP1619273B1 (ja) |
JP (1) | JP4755458B2 (ja) |
CN (1) | CN100585012C (ja) |
AT (1) | ATE401433T1 (ja) |
DE (2) | DE102004035860A1 (ja) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20140329099A1 (en) * | 2011-06-21 | 2014-11-06 | Sébastien Marrot | Hydrosilylation reaction inhibitors, and use thereof for preparing stable curable silicone compositions |
Families Citing this family (5)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DK2496735T3 (en) * | 2009-11-04 | 2017-05-22 | Ffgf Ltd | PREPARATION OF CARBON HYDRADES |
CN102492957B (zh) * | 2011-12-15 | 2014-07-09 | 天津工业大学 | 一种电催化膜选择性催化氧化醇类制备醛或酸的方法 |
CN107964668B (zh) * | 2016-10-19 | 2019-08-16 | 中国科学院上海有机化学研究所 | 化合物中C(sp3)-H键转化为C(sp3)-O键方法及制备得到的化合物 |
CN107245029B (zh) * | 2017-03-14 | 2021-01-05 | 广东工业大学 | 一种酮类化合物及其合成方法 |
CN109518211B (zh) * | 2019-01-08 | 2020-11-06 | 合肥工业大学 | 一种芳香偶酰类化合物的电化学合成方法 |
Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2879305A (en) * | 1959-03-24 | Production of acetals of propargyl | ||
US3969200A (en) * | 1974-02-26 | 1976-07-13 | Basf Aktiengesellschaft | Manufacture of propiolic acid |
US6077414A (en) * | 1995-09-12 | 2000-06-20 | Basf Aktiengesellschaft | Electrolytic plate stack cell |
US6398938B2 (en) * | 1999-12-22 | 2002-06-04 | Basf Aktiengesellschaft | Process for electrochemical oxidation of organic compounds |
Family Cites Families (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE10244633B3 (de) * | 2002-09-25 | 2004-02-26 | Consortium für elektrochemische Industrie GmbH | Verfahren zur Herstellung von Alkincarbonsäuren durch Oxidation von Alkinalkoholen |
-
2004
- 2004-07-23 DE DE102004035860A patent/DE102004035860A1/de not_active Withdrawn
-
2005
- 2005-06-18 EP EP05013192A patent/EP1619273B1/de not_active Not-in-force
- 2005-06-18 AT AT05013192T patent/ATE401433T1/de not_active IP Right Cessation
- 2005-06-18 DE DE502005004699T patent/DE502005004699D1/de active Active
- 2005-07-21 US US11/186,100 patent/US20060016695A1/en not_active Abandoned
- 2005-07-22 JP JP2005213194A patent/JP4755458B2/ja not_active Expired - Fee Related
- 2005-07-22 CN CN200510085307A patent/CN100585012C/zh not_active Expired - Fee Related
Patent Citations (4)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US2879305A (en) * | 1959-03-24 | Production of acetals of propargyl | ||
US3969200A (en) * | 1974-02-26 | 1976-07-13 | Basf Aktiengesellschaft | Manufacture of propiolic acid |
US6077414A (en) * | 1995-09-12 | 2000-06-20 | Basf Aktiengesellschaft | Electrolytic plate stack cell |
US6398938B2 (en) * | 1999-12-22 | 2002-06-04 | Basf Aktiengesellschaft | Process for electrochemical oxidation of organic compounds |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US20140329099A1 (en) * | 2011-06-21 | 2014-11-06 | Sébastien Marrot | Hydrosilylation reaction inhibitors, and use thereof for preparing stable curable silicone compositions |
US9120935B2 (en) * | 2011-06-21 | 2015-09-01 | Bluestar Silicones France Sas | Hydrosilylation reaction inhibitors, and use thereof for preparing stable curable silicone compositions |
Also Published As
Publication number | Publication date |
---|---|
JP2006037233A (ja) | 2006-02-09 |
EP1619273A1 (de) | 2006-01-25 |
EP1619273B1 (de) | 2008-07-16 |
CN1737200A (zh) | 2006-02-22 |
DE102004035860A1 (de) | 2006-02-16 |
DE502005004699D1 (de) | 2008-08-28 |
ATE401433T1 (de) | 2008-08-15 |
CN100585012C (zh) | 2010-01-27 |
JP4755458B2 (ja) | 2011-08-24 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
AS | Assignment |
Owner name: BASF AKTIENGESELLSCHAFT, GERMANY Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:RICHTER, INGO;GRIESBACH, ULRICH;BECKER, MICHAEL;AND OTHERS;REEL/FRAME:016611/0849 Effective date: 20050429 |
|
STCB | Information on status: application discontinuation |
Free format text: ABANDONED -- FAILURE TO RESPOND TO AN OFFICE ACTION |