EP0689530A1 - Procede de preparation d'acide monochloracetique a teneur reduite en acide dichloracetique - Google Patents
Procede de preparation d'acide monochloracetique a teneur reduite en acide dichloracetiqueInfo
- Publication number
- EP0689530A1 EP0689530A1 EP94911130A EP94911130A EP0689530A1 EP 0689530 A1 EP0689530 A1 EP 0689530A1 EP 94911130 A EP94911130 A EP 94911130A EP 94911130 A EP94911130 A EP 94911130A EP 0689530 A1 EP0689530 A1 EP 0689530A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- monochloroacetic acid
- acid
- reduced
- dichloroacetic
- monochloroacetic
- 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.)
- Withdrawn
Links
Classifications
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/347—Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups
- C07C51/377—Preparation of carboxylic acids or their salts, halides or anhydrides by reactions not involving formation of carboxyl groups by splitting-off hydrogen or functional groups; by hydrogenolysis of functional groups
-
- C—CHEMISTRY; METALLURGY
- C07—ORGANIC CHEMISTRY
- C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
- C07C51/00—Preparation of carboxylic acids or their salts, halides or anhydrides
- C07C51/42—Separation; Purification; Stabilisation; Use of additives
- C07C51/487—Separation; Purification; Stabilisation; Use of additives by treatment giving rise to chemical modification
Definitions
- the invention relates to a process for the preparation of a monochloroacetic acid with a low content of dichloroacetic acid, in which the contaminated acid is subjected to a temperature treatment in the presence of base metals and then distilled, and the use of the purified acid for the production of amphoteric or zwitterionic surfactants.
- Amphoteric or zwitterionic surfactants are extremely skin-friendly and have excellent cleaning properties. They are therefore particularly suitable for the assembly of a large number of surface-active products. In the simplest case, their preparation is based on secondary or tertiary amines, which are reacted with sodium chloroacetate to give alkyl betaines. The reaction of fatty acid amidoamines or imidazolines with sodium chloroacetate leads to the formation of amphoteric surfactants of the type Glycinates; If acrylic acid ester is used as the alkylating agent, aminopropionates are formed. Compounds of the type mentioned are described in a large number of review articles, of which only Parf.Cos .Arom. 70. 67 (1986), HAPPI, 70, (Nov. 1986) and Soap Cosm.Chem.Spec. 46, (Apr. 1990).
- a particular problem in the production of alkyl betaines and glycinates is the quality of the monochloroacetic acid or its sodium salts to be used as the alkylating agent, since these usually have an undesirable content of approx. 2000 to 3000 ppm dichloroacetic acid due to the production process.
- amphoteric surfactant manufacturers have a need for a qualitatively improved monochloroacetic acid whose dichloroacetic acid content should be a maximum of 200 to 500.
- the object of the invention was therefore to develop a process for the production of a monochloroacetic acid with a reduced content of dichloroacetic acid which is free from the disadvantages described. Description of the invention
- the invention relates to a process for the preparation of monochloroacetic acid with a reduced dichloroacetic acid content, in which the crude monochloroacetic acid is subjected to a temperature treatment in the presence of an infinite metal and the reaction product is then distilled.
- Suitable base metals are substances which easily form salts with monochloroacetic acid with the elimination of hydrogen. Typical examples are magnesium, aluminum, zinc, tin, lead, iron, nickel and cobalt. The use of zinc and tin in the form of powder, chips, cut or granules is preferred.
- the base metals can usually be used in amounts of 0.25 to 5, preferably 1 to 2,% by weight, based on the monochloroacetic acid. Heat treatment
- the temperature treatment can be carried out in the range from 100 to 140, in particular 120 to 130 ° C., preferably in an inert gas atmosphere for the discharge of gaseous hydrogen released. To do this, it is sufficient to mix the contaminated monochloroacetic acid with the base metals and to stir it for a period of 0.1 to 5, preferably 0.5 to 2, hours. Subsequently, the purified monochloroacetic acid can be distilled off from the reaction mixture, usually at temperatures in the range from 100 to 135 ° C. and under a reduced pressure in the range from 50 to 500 mbar. The distillative removal is not a further purification step, rather it is a simple and efficient way of separating the monochloroacetic acid purified by the temperature treatment from the residue - essentially salts and optionally catalyst residues.
- the monochloroacetic acid obtainable by the process according to the invention has a content of less than 1000, preferably less than 500 and in particular less than 300 ppm dichloroacetic acid and therefore also meets very high quality requirements.
- Another object of the invention therefore relates to their use as alkylating agents for the production of amphoteric or zwitterionic surfactants, in particular of the alkyl betaines and glycinates type.
Landscapes
- Chemical & Material Sciences (AREA)
- Organic Chemistry (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Engineering & Computer Science (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- General Chemical & Material Sciences (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
Abstract
On peut produire un acide monochloracétique à teneur réduite en acide dichloracétique en soumettant l'acide monochloracétique brut à un traitement thermique en présence d'un métal non précieux, puis en distillant le produit de la réaction. L'acide monochloracétique purifié est particulièrement utile comme agent alkylant afin de produire des agents tensioactifs amphotères ou zwittérioniques.
Applications Claiming Priority (3)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
DE4308793A DE4308793A1 (de) | 1993-03-18 | 1993-03-18 | Verfahren zur Herstellung von Monochloressigsäure mit vermindertem Dichloressigsäuregehalt |
DE4308793 | 1993-03-18 | ||
PCT/EP1994/000717 WO1994021588A1 (fr) | 1993-03-18 | 1994-03-09 | Procede de preparation d'acide monochloracetique a teneur reduite en acide dichloracetique |
Publications (1)
Publication Number | Publication Date |
---|---|
EP0689530A1 true EP0689530A1 (fr) | 1996-01-03 |
Family
ID=6483219
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
EP94911130A Withdrawn EP0689530A1 (fr) | 1993-03-18 | 1994-03-09 | Procede de preparation d'acide monochloracetique a teneur reduite en acide dichloracetique |
Country Status (3)
Country | Link |
---|---|
EP (1) | EP0689530A1 (fr) |
DE (1) | DE4308793A1 (fr) |
WO (1) | WO1994021588A1 (fr) |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0842756A1 (fr) * | 1996-11-08 | 1998-05-20 | Milliken Research Corporation | Essuie-mains en rouleau joint par ultrasons |
Families Citing this family (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE19545134C2 (de) | 1995-12-04 | 1998-02-26 | Henkel Kgaa | Verfahren zur Herstellung hellfarbiger Betaine |
MX2017011678A (es) | 2015-03-17 | 2017-11-06 | Akzo Nobel Chemicals Int Bv | Proceso para la purificacion de acido monocloroacetico. |
Family Cites Families (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5527156A (en) * | 1978-08-17 | 1980-02-27 | Nippon Oil & Fats Co Ltd | Purification of fatty acid |
JPS5545614A (en) * | 1978-09-27 | 1980-03-31 | Nippon Oil & Fats Co Ltd | Purification of aliphatic acid |
EP0465844B1 (fr) * | 1990-06-11 | 1996-04-10 | MITSUI TOATSU CHEMICALS, Inc. | Procédé de purification d'acide 2-chloropropionique |
-
1993
- 1993-03-18 DE DE4308793A patent/DE4308793A1/de not_active Withdrawn
-
1994
- 1994-03-09 EP EP94911130A patent/EP0689530A1/fr not_active Withdrawn
- 1994-03-09 WO PCT/EP1994/000717 patent/WO1994021588A1/fr not_active Application Discontinuation
Non-Patent Citations (1)
Title |
---|
See references of WO9421588A1 * |
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
EP0842756A1 (fr) * | 1996-11-08 | 1998-05-20 | Milliken Research Corporation | Essuie-mains en rouleau joint par ultrasons |
Also Published As
Publication number | Publication date |
---|---|
WO1994021588A1 (fr) | 1994-09-29 |
DE4308793A1 (de) | 1994-09-22 |
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Legal Events
Date | Code | Title | Description |
---|---|---|---|
PUAI | Public reference made under article 153(3) epc to a published international application that has entered the european phase |
Free format text: ORIGINAL CODE: 0009012 |
|
17P | Request for examination filed |
Effective date: 19950911 |
|
AK | Designated contracting states |
Kind code of ref document: A1 Designated state(s): DE FR GB IT |
|
17Q | First examination report despatched |
Effective date: 19961202 |
|
STAA | Information on the status of an ep patent application or granted ep patent |
Free format text: STATUS: THE APPLICATION HAS BEEN WITHDRAWN |
|
18W | Application withdrawn |
Withdrawal date: 19970123 |