WO2000032310A1 - Process for preparation of aminocarboxylic acids - Google Patents

Process for preparation of aminocarboxylic acids Download PDF

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Publication number
WO2000032310A1
WO2000032310A1 PCT/EP1999/009267 EP9909267W WO0032310A1 WO 2000032310 A1 WO2000032310 A1 WO 2000032310A1 EP 9909267 W EP9909267 W EP 9909267W WO 0032310 A1 WO0032310 A1 WO 0032310A1
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Prior art keywords
raney copper
group
catalyst
salts
amine
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PCT/EP1999/009267
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French (fr)
Inventor
Bernd Siebenhaar
Milos Rusek
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Syngenta Participations Ag
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Priority to AU17781/00A priority Critical patent/AU756195B2/en
Priority to CA002350750A priority patent/CA2350750A1/en
Priority to BR9915858-2A priority patent/BR9915858A/en
Priority to IL14313999A priority patent/IL143139A0/en
Priority to KR1020017006810A priority patent/KR20010080643A/en
Priority to HU0104480A priority patent/HUP0104480A3/en
Priority to JP2000584991A priority patent/JP2002531239A/en
Priority to EP99961024A priority patent/EP1140356A1/en
Priority to PL99347972A priority patent/PL347972A1/en
Publication of WO2000032310A1 publication Critical patent/WO2000032310A1/en
Priority to US09/872,653 priority patent/US6541663B2/en

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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
    • B01J25/00—Catalysts of the Raney type
    • 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
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/14—Phosphorus; Compounds thereof
    • B01J27/186—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium
    • B01J27/188—Phosphorus; Compounds thereof with arsenic, antimony, bismuth, vanadium, niobium, tantalum, polonium, chromium, molybdenum, tungsten, manganese, technetium or rhenium with chromium, molybdenum, tungsten or polonium
    • 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
    • B01J27/00—Catalysts comprising the elements or compounds of halogens, sulfur, selenium, tellurium, phosphorus or nitrogen; Catalysts comprising carbon compounds
    • B01J27/24—Nitrogen compounds
    • C—CHEMISTRY; METALLURGY
    • C07—ORGANIC CHEMISTRY
    • C07C—ACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C227/00—Preparation of compounds containing amino and carboxyl groups bound to the same carbon skeleton
    • C07C227/02—Formation of carboxyl groups in compounds containing amino groups, e.g. by oxidation of amino alcohols

Definitions

  • the present invention relates to a process for the production of amine-group-containing carboxylic acid salts by oxidation of corresponding primary alcohols in an aqueous alkaline medium at an elevated temperature in the presence of a modified Raney copper catalyst.
  • the catalyst activity can be increased, the selectivity is maintained, the deactivation is only slight and, if necessary, can be eliminated by simple treatment with the doping (promoting) agent, and in this way multiple reusage in further reaction cycles is possible, and increased activity is observed in part during reusage, if the doping (promoting) agent employed is an ecologically acceptable agent, for example boric acid, onium fluorides or salts with fluorine complex anions, or heteropoly acids.
  • the doping (promoting) agent employed is an ecologically acceptable agent, for example boric acid, onium fluorides or salts with fluorine complex anions, or heteropoly acids.
  • a first object of the invention is Raney copper, which is doped (promoted) with an effective quantity of a doping (promoting) agent selected from the group boric acid, onium fluorides, salts of fluorine complex anions, and heteropoly acids.
  • Effective quantity means that a minimum quantity is used and the effects are generally not further improved beyond the upper limit of a preferred quantity range.
  • the minimum quantity, based on Raney copper is preferably 10 ppm, more preferably 20 ppm and most preferably 50 ppm, and the maximum quantity is preferably 10,000 ppm, more preferably 8000 ppm and most preferably 5000 ppm.
  • Boric acid H 3 B0 3 can be used as such in the treatment of Raney copper, or can be produced in the reaction medium from boric acid esters.
  • the onium fluorides in question may be, for example, unsubstituted or substituted phosphonium fluorides and more preferably ammonium fluorides. They may correspond to formula I,
  • X is N or P and the symbols R are identical or different and signify H, C ⁇ -C 2 o-alkyl, C 2 -C 2 o-hydroxyalkyl, C 1 -C 4 -alkoxy-C 2 -C 1 2-alkyl, C 2 -C 8 -cycloalkyl, C 6 -C 10 -aryl, C 7 -C ⁇ 2 -aralkyl or C 8 -C ⁇ 2 -alkaralkyl
  • R may be linear or branched alkyl, which preferably contains 1 to 12, more preferably 1 to 8, most preferably 1 to 4 carbon atoms. Examples are methyl, ethyl, and the isomers of propyl, butyl, pentyl, hexyl, heptyl, octyl, decyl, dodecyl, tetradecyl, hexadecyl, octadecyl and eicosyl.
  • Alkyl is preferably linear and preferably denotes methyl, ethyl, n-propyl and n-butyl.
  • R may be linear or branched hydroxyalkyl, which preferably contains 2 to 12, more preferably 2 to 8, most preferably 2 to 4 carbon atoms. Examples are hydroxyethyl, hydroxypropyl and hydroxybutyl.
  • R as alkoxyalkyl preferably signifies C ⁇ -C 4 -alkoxy-C 2 -C 4 -alkyl, whereby alkoxy is most preferably methoxy or ethoxy.
  • Preferred examples are methoxyethyl and ethoxyethyl.
  • R as cycioalkyl preferably contains 4 to 7, most preferably 5 or 6 ring carbon atoms.
  • Examples of cycioalkyl are cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl and cyclooctyl. Cyclohexyl is especially preferred.
  • R as aryl may be naphthyl and preferably phenyl.
  • R as aralkyl is preferably phenylalkyl. Examples are benzyl and ⁇ -phenylethyl.
  • R as alkaraikyl preferably signifies alkylbenzyl, examples being methylbenzyl, dimethyl- benzyl, trimethylbenzyl and ethylbenzyl.
  • X in formula I preferably signifies N.
  • One preferred group of compounds of formula I is that in which the symbols R are identical and are selected from the group H and C C 4 -alkyl.
  • the compound of formula I in question is most preferably NH F.
  • alkali metal salts and onium salts are preferred in particular.
  • Alkali metal salts are preferably, for example, lithium, sodium and potassium salts.
  • Onium cations have already been described for the fluorides.
  • the alkali metal salts may correspond to formula II,
  • Me is NH 4 + or an alkali metal cation, preferably Li + , Na + und K ⁇ and Y signifies a perfluorine complex anion from the group BF 4 ' , AIF 4 " , PF 6 ⁇ AsF 6 ⁇ SbF 6 ' or BiF 6 ⁇
  • Preferred compounds are NaBF 4 , KBF 4 , NaPF 6 , KPF 6 and especially NH 4 BF 4 and NH 4 PF 6 .
  • heteropoly acids are preferably derived from the poly-acid-forming elements W, Mo and V, whereby the polyanions contain elements from the groups P, B, Si and Ge.
  • Heteropoly acids are known and are described for example by I. V. Kozhevnikov in Uspevic Khimii Volume 56, pages 1417 to 1443 (1987).
  • Preferred heteropoly acids correspond to formula III,
  • Z is P, B, Si or Ge
  • M is a metal from the group W, Mo and V
  • n is an integer from 3 to 6.
  • Preferred examples are H 3 [P(W ⁇ 2 O 40 )], H 4 [P(W 12 0_to)] and H s [B(W 12 0 4 o)].
  • the carbaldehyde-group-containing adjuvants are derived e.g. from formaldehyde, para- formaldehyde, the aliphatic d-C ⁇ -alkylcarbaldeydes, aromatic carbaidehydes and the corresponding dicarbaldehydes, whereby the aromatic rings may be substituted by C C 6 - alkyl or by OH.
  • C ⁇ -C 8 -alkylcarbaldehydes, benzaldehyde, cuminaidehyde and 4- hydroxybenzaldehyde are preferred for example.
  • carbaldehyde-group-containing adjuvants are conveniently employed in an amount ranging from 0.1 mol% to 50 mol%, preferably 1 mol% to 20 mol%, most preferably 2 mol% to 10 mol%, based on the primary amino alcohols of formula IV.
  • the catalysts may take place in known manner, whereby an aqueous suspension of Raney copper is mixed with an aqueous solution of the modifying agent, the mixture is stirred or left to stand for a while, and then the impregnated Raney copper is filtered off or decanted and dried.
  • the catalyst may also be produced and used in situ, whereby the aqueous mixture comprising catalyst and modifying agent is used directly after impregnation for the oxidation of primary alcohols.
  • the catalyst may be used repeatedly. What is particularly advantageous here is that, when a loss of activity is first observed, further modifying agent is dispensed into the reaction mixture, and the loss of activity can be significantly to totally eliminated.
  • activated Raney copper is used for the modification. This is available commercially.
  • Activation of Raney copper may be carried out whereby commercial Raney copper is treated for ca. 2 hours at a temperature of for example 200°C with a mixture of nitrogen and hydrogen (volume ratio for example 4:1), and is then cooled under a protecting gas (for example argon).
  • a protecting gas for example argon
  • a further object of the invention is a process for the production of amine-group-containing carboxylic acid salts by oxidation of amine-group-containing primary alcohols in an aqueous-alkaline reaction medium, in the presence of a modified Raney copper catalyst and at elevated temperature, the process being characterised in that the Raney copper is doped (promoted) with an effective quantity of a modifying agent selected from the group boric acid, onium fluorides, salts of fluorine complex anions and heteropoly acids.
  • the above-described embodiments and preferences apply to the modified Raney copper.
  • the catalyst may be employed in a quantity of 0.1 to 30 % by weight, preferably 0.5 to 20 % by weight, more preferably 0.5 to 15 % by weight, most preferably 1 to 10 % by weight, based on the primary alcohol.
  • the reaction temperature may be for example from 80 to 300°C, preferably from 100 to 250 °C.
  • the reaction is advantageously carried out under excess pressure.
  • the pressure may be, for example, from 1 to 50 bars, preferably 2 to 25 bars, most preferably 5 to 15 bars.
  • the reaction is carried out in an alkaline reaction medium, preferably in the presence of NaOH or KOH.
  • the amount of alkali base in the reaction mixture is advantageously calculated such that at least equal molar amounts of alkali base are present in relation to the primary amine. It is appropriate to use an excess of alkali base, for example one to five times, preferably up to three times, most preferably up to double the molar excess.
  • the amines may contain 1 to 3 primary alcohol groups, and the amines may be primary, secondary or tertiary amines.
  • the amine-group-containing primary alcohols may corresponds, for example, to formula IV,
  • Ri and R 2 independently of one another, are H, linear or branched, C ⁇ -C 18 -alkyl either unsubstituted or substituted by F, Cl, Br, -NH 2 , C 1 -C 4 -alkoxy, C ⁇ -C 4 -halogenalkyl or -COOH; C 3 -C 8 -cycloalkyl, C 6 -C ⁇ 0 -aryl or C 7 -C 12 -aralkyl either unsubstituted or substituted by F, Cl, Br, -NH 2 , d-Ci-alkyl, C ⁇ -C 4 -alkoxy, C C 4 -halogenalkyl; phosphonomethyl; Ri and R 2 together are tetramethylene or pentamethylene; or R, and R 2 , independently of one another, have the significance R 3 -CH 2 OH; and R 3 is linear or branched CrC ⁇ 7 -alkylene which is uninterrupted or is interrupted by C 3
  • R t and R 2 as alkyl preferably contain 1 to 12, more preferably 1 to 8, most preferably 1 to 4 carbon atoms. Examples and preferences of alkyl have already been described.
  • Ri and R 2 as cycioalkyl preferably contain 4 to 7, most preferably 5 or 6 ring carbon atoms.
  • Examples of cycioalkyl are cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl and cyclooctyl. Cyclohexyl is especially preferred.
  • Ri and R 2 as aryl may be naphthyl and preferably phenyl.
  • Ri and R 2 as aralkyl are preferably phenylalkyl. Examples are benzyl and ⁇ -phenylethyl.
  • R 3 as alkylene preferably contain 1 to 12, more preferably 1 to 8, most preferably 1 to 4 carbon atoms.
  • alkylene are methylene, 1 ,1- or 1 ,2-ethylene, 1 ,1 -, 1 ,2- or 1 ,3- propylene, 1 ,1-, 1 ,2-, 1 ,3- or 1 ,4-butylene, 1 ,1-, 1 ,2-, 1 ,3-, 1 ,4- or 1 ,5-pentylene, 1 ,1 -, 1 ,2-, 1 ,3-, 1 ,4-, 1 ,5- or 1 ,6-hexylene, 1 ,1-, 1 ,2-, 1 ,3-, 1 ,4-, 1 ,5-, 1 ,6- or 1 ,7-heptylene, 1 ,1-, 1 ,2-, 1 ,3-, 1 ,4-, 1 ,5-, 1 ,6-, 1 ,
  • the group -R 3 CH 2 OH preferably signifies 4-hydroxybutyl, 3-hydroxypropyl and most preferably 2-hydroxyethyl.
  • Ri and R 2 independently of one another, signify H or unsubstituted or -NH 2 - or -COOH-substituted C ⁇ -Ci 2 -Alkyl or -CH 2 CH 2 -OH.
  • Ri and R 2 independently of one another, preferably signify H, d-d-alky! or -CH 2 -CH 2 -OH.
  • Another preferred sub-group is compounds of formula IVa, in which R t is -CH 2 CH 2 -OH and R 2 , independently of one another, are H, d-C 4 -alkyl or -CH 2 -CH 2 -OH.
  • Some examples of compounds of formula IV are ethanolamine, diethanolamine, triethanol- amine, N-methylethanolamine, N-dimethylethanoiamine, N-methyldiethanolamine, N-ethyl- ethanolamine, N-(n-propyl)ethanolamine, N-(n-propyl)ethanolamine, N-(n-butyl)ethanol- amine, N-(n-pentyl)ethanolamine, N-(n-hexyl)ethanolamine, N-(n-octyl)ethanolamine, N-(n- decyl)ethanolamine, N-(n-dodecyl)ethanolamine, N-(n-tetradecyl)ethanolamine, N-(n-hexa- decyl)ethanolamine, N-(n-octadecyl)ethanolamine, N-(di-n-propyl)ethanolamine, N-(di-n- butyl)ethanolamine, N-(di-n-hexy
  • the compounds of formula IV are known, are partly commercially available or may be produced by processes that are similar to those described in literature.
  • the process according to the invention may be carried out, for example, in such a way that the catalyst is placed in an autoclave, then first of all the primary alcohol is added, optionally in water, followed by the alkali lye, the autoclave is sealed and the reaction mixture stirred, and the reaction is commenced whilst heating. The reaction generally continues until the hydrogen generation is no longer observed.
  • the catalyst can be decanted from the cooled reaction mixture and used for the next reaction.
  • the alkali metal salts of carboxylic acids that are formed may be isolated and optionally purified in the usual manner.
  • the salts may also be converted into the free carboxylic acids and derivatives thereof, such as acid amides and acid esters.
  • the process according to the invention is suitable for production on an industrial scale.
  • aminocarboxylic acids that may be produced according to the invention can be used for many purposes. Glycine is employed for food production. Aminocarboxylic acids are known complexing agents, which are used in the detergent industry and in water treatment. In addition, the amino alcohols may be used in the production of ionic surfactants. The amino alcohols are also valuable intermediates in the production of pharmaceutical and pesticidal compositions.
  • a suspension of 8.26 g of activated Raney copper in 20 ml of water is stirred with 1.0 g of a 10% solution of NH 4 B 4 in water, and then left to stand for 15 minutes. The whole mixture is subsequently transferred to a 300 ml nickel autoclave.
  • a suspension of 8.26 g of activated Raney copper in 20 ml of water is stirred with 0.25 g of H 3 (PWi 2 ⁇ _ t o) in 20 ml of water, and then left to stand for 15 minutes. The whole mixture is subsequently transferred to a 300 ml nickel autoclave.
  • the autoclave containing the reaction mixture is cooled to 100°C.
  • the supernatant solution is suctioned off through a riser, and the modified Cu catalyst remains in the autoclave.
  • diethanolamine and NaOH are added in the above-described proportions and reacted under the specified conditions.
  • the catalyst shows only slight activity loss (5 hours, 89% by weight), and selectivity is maintained. Renewed impregnation with H 3 (PW ⁇ 2 O 0 ) gives a catalyst with the original high activity and selectivity (12th reuse, 3.5 hours, 91% by weight).
  • a suspension of 8.26 g of activated Raney copper in 20 ml of water is stirred with 0.25 g of NH 4 F in 20 ml of water, and then left to stand for 15 minutes. The whole mixture is subsequently transferred to a 300 ml nickel autoclave.
  • the autoclave containing the reaction mixture is cooled to 100°C.
  • the supernatant solution is suctioned off through a riser, and the modified Cu catalyst remains in the autoclave.
  • diethanolamine and NaOH are added in the above-described proportions and reacted under the specified conditions.
  • the catalyst shows only slight activity loss (5 hours, 87% by weight), and selectivity is maintained. Renewed impregnation with NH 4 F or dispensing in NH 4 F during the reaction gives a catalyst with the original high activity and selectivity (21st reuse, 4 hours, 91% by weight).
  • a suspension of 8.26 g of activated Raney copper in 20 ml of water is stirred with 0.25 g of NH 4 F in 20 ml of water, and then left to stand for 15 minutes. The whole mixture is subsequently transferred to a 300 ml nickel autoclave.
  • the yield of iminodiacetic acid disodium salt according to NMR analysis is 97-98% by weight.
  • the autoclave containing the reaction mixture is cooled to 100°C.
  • the supernatant solution is suctioned off through a riser, and the modified Cu catalyst remains in the autoclave.
  • diethanolamine, 4-hydroxybenzaldehyde (or benzaldehyde) and NaOH are added in the above-described proportions and reacted under the specified conditions.
  • the catalyst shows only slight activity loss, and selectivity is maintained. Renewed impregnation with NH 4 F or dispensing in NH F during the reaction gives a catalyst with the original high activity and selectivity (21st reuse, duration of reaction 72 minutes, yield 92% by weight).

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Abstract

Raney copper, which is doped (promoted) with an effective quantity of a doping (promoting) agent selected from the group boric acid, onium fluorides, salts of fluorine complex anions, and heteropoly acids, represents an outstanding oxidation catalyst for amine-group-containing primary amines to carboxylic acids.

Description

Process for preparation of aminocarboxylic acids
The present invention relates to a process for the production of amine-group-containing carboxylic acid salts by oxidation of corresponding primary alcohols in an aqueous alkaline medium at an elevated temperature in the presence of a modified Raney copper catalyst.
In WO 92/06069, O. Gomez et al. describe the oxidation of ethanol amines to carboxylic acids, whereby the reaction is carried out in an aqueous-alkaline medium in the presence of Raney copper as the oxidation catalyst. In order to be able to reuse the catalyst in further reaction cycles, it must be reactivated, in this case by treatment with formic acid and then thorough washing with demineraiised water and sodium hydroxide solution. Nevertheless, repeated usage is restricted because the catalyst has too short a service life and deactivates continuously.
In WO 94/24091 , it is proposed that these disadvantages are remedied by doping (promoting) Raney copper with 10 to 50,000 ppm of an element or a metal, for example titanium, niobium, vanadium, molybdenum, manganese, nickel, lead and in particular chromium. The activity of the catalyst is only reduced thereby to a negligible extent. However, catalyst deactivation can be substantially improved. Of course, there is nothing to prevent the doping (promoting) metals, which are recognised as toxic, from reaching the reaction product, and after lengthy usage, the catalyst can no longer be reused. Simple reactivation is likewise impossible owing to the presence of doping (promoting) metals.
It has now surprisingly been found that the catalyst activity can be increased, the selectivity is maintained, the deactivation is only slight and, if necessary, can be eliminated by simple treatment with the doping (promoting) agent, and in this way multiple reusage in further reaction cycles is possible, and increased activity is observed in part during reusage, if the doping (promoting) agent employed is an ecologically acceptable agent, for example boric acid, onium fluorides or salts with fluorine complex anions, or heteropoly acids.
It was also surprisingly found that by adding adjuvants which contain carbaldehyde groups to the aqueous alkaline reaction medium, the catalyst activity and thus the reaction rate can be increased. A first object of the invention is Raney copper, which is doped (promoted) with an effective quantity of a doping (promoting) agent selected from the group boric acid, onium fluorides, salts of fluorine complex anions, and heteropoly acids.
Effective quantity means that a minimum quantity is used and the effects are generally not further improved beyond the upper limit of a preferred quantity range. The minimum quantity, based on Raney copper, is preferably 10 ppm, more preferably 20 ppm and most preferably 50 ppm, and the maximum quantity is preferably 10,000 ppm, more preferably 8000 ppm and most preferably 5000 ppm.
Boric acid H3B03 can be used as such in the treatment of Raney copper, or can be produced in the reaction medium from boric acid esters.
The onium fluorides in question may be, for example, unsubstituted or substituted phosphonium fluorides and more preferably ammonium fluorides. They may correspond to formula I,
Figure imgf000004_0001
wherein X is N or P and the symbols R are identical or different and signify H, Cι-C2o-alkyl, C2-C2o-hydroxyalkyl, C1-C4-alkoxy-C2-C12-alkyl, C2-C8-cycloalkyl, C6-C10-aryl, C7-Cι2-aralkyl or C8-Cι2-alkaralkyl
R may be linear or branched alkyl, which preferably contains 1 to 12, more preferably 1 to 8, most preferably 1 to 4 carbon atoms. Examples are methyl, ethyl, and the isomers of propyl, butyl, pentyl, hexyl, heptyl, octyl, decyl, dodecyl, tetradecyl, hexadecyl, octadecyl and eicosyl. Alkyl is preferably linear and preferably denotes methyl, ethyl, n-propyl and n-butyl.
R may be linear or branched hydroxyalkyl, which preferably contains 2 to 12, more preferably 2 to 8, most preferably 2 to 4 carbon atoms. Examples are hydroxyethyl, hydroxypropyl and hydroxybutyl. R as alkoxyalkyl preferably signifies Cι-C4-alkoxy-C2-C4-alkyl, whereby alkoxy is most preferably methoxy or ethoxy. Preferred examples are methoxyethyl and ethoxyethyl.
R as cycioalkyl preferably contains 4 to 7, most preferably 5 or 6 ring carbon atoms. Examples of cycioalkyl are cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl and cyclooctyl. Cyclohexyl is especially preferred.
R as aryl may be naphthyl and preferably phenyl.
R as aralkyl is preferably phenylalkyl. Examples are benzyl and β-phenylethyl.
R as alkaraikyl preferably signifies alkylbenzyl, examples being methylbenzyl, dimethyl- benzyl, trimethylbenzyl and ethylbenzyl.
X in formula I preferably signifies N.
One preferred group of compounds of formula I is that in which the symbols R are identical and are selected from the group H and C C4-alkyl. The compound of formula I in question is most preferably NH F.
Of the salts of fluorine complex anions, the alkali metal salts and onium salts are preferred in particular. Alkali metal salts are preferably, for example, lithium, sodium and potassium salts. Onium cations have already been described for the fluorides. The alkali metal salts may correspond to formula II,
Me+ Y~ (II),
wherein Me is NH4 + or an alkali metal cation, preferably Li+, Na+ und K\ and Y signifies a perfluorine complex anion from the group BF4 ', AIF4 ", PF6\ AsF6\ SbF6 ' or BiF6\ Preferred compounds are NaBF4, KBF4, NaPF6, KPF6 and especially NH4BF4 and NH4PF6.
The heteropoly acids are preferably derived from the poly-acid-forming elements W, Mo and V, whereby the polyanions contain elements from the groups P, B, Si and Ge. Heteropoly acids are known and are described for example by I. V. Kozhevnikov in Uspekhi Khimii Volume 56, pages 1417 to 1443 (1987). Preferred heteropoly acids correspond to formula III,
Figure imgf000006_0001
wherein Z is P, B, Si or Ge, M is a metal from the group W, Mo and V, and n is an integer from 3 to 6. Preferred examples are H3[P(Wι2O40)], H4[P(W120_to)] and Hs[B(W1204o)].
The carbaldehyde-group-containing adjuvants are derived e.g. from formaldehyde, para- formaldehyde, the aliphatic d-C^-alkylcarbaldeydes, aromatic carbaidehydes and the corresponding dicarbaldehydes, whereby the aromatic rings may be substituted by C C6- alkyl or by OH. Of these, Cι-C8-alkylcarbaldehydes, benzaldehyde, cuminaidehyde and 4- hydroxybenzaldehyde are preferred for example.
These carbaldehyde-group-containing adjuvants are conveniently employed in an amount ranging from 0.1 mol% to 50 mol%, preferably 1 mol% to 20 mol%, most preferably 2 mol% to 10 mol%, based on the primary amino alcohols of formula IV.
Production of the catalysts may take place in known manner, whereby an aqueous suspension of Raney copper is mixed with an aqueous solution of the modifying agent, the mixture is stirred or left to stand for a while, and then the impregnated Raney copper is filtered off or decanted and dried. The catalyst may also be produced and used in situ, whereby the aqueous mixture comprising catalyst and modifying agent is used directly after impregnation for the oxidation of primary alcohols. The catalyst may be used repeatedly. What is particularly advantageous here is that, when a loss of activity is first observed, further modifying agent is dispensed into the reaction mixture, and the loss of activity can be significantly to totally eliminated. In general, activated Raney copper is used for the modification. This is available commercially. Activation of Raney copper may be carried out whereby commercial Raney copper is treated for ca. 2 hours at a temperature of for example 200°C with a mixture of nitrogen and hydrogen (volume ratio for example 4:1), and is then cooled under a protecting gas (for example argon).
A further object of the invention is a process for the production of amine-group-containing carboxylic acid salts by oxidation of amine-group-containing primary alcohols in an aqueous-alkaline reaction medium, in the presence of a modified Raney copper catalyst and at elevated temperature, the process being characterised in that the Raney copper is doped (promoted) with an effective quantity of a modifying agent selected from the group boric acid, onium fluorides, salts of fluorine complex anions and heteropoly acids.
The above-described embodiments and preferences apply to the modified Raney copper. The catalyst may be employed in a quantity of 0.1 to 30 % by weight, preferably 0.5 to 20 % by weight, more preferably 0.5 to 15 % by weight, most preferably 1 to 10 % by weight, based on the primary alcohol.
The reaction temperature may be for example from 80 to 300°C, preferably from 100 to 250 °C.
The reaction is advantageously carried out under excess pressure. The pressure may be, for example, from 1 to 50 bars, preferably 2 to 25 bars, most preferably 5 to 15 bars.
The reaction is carried out in an alkaline reaction medium, preferably in the presence of NaOH or KOH. The amount of alkali base in the reaction mixture is advantageously calculated such that at least equal molar amounts of alkali base are present in relation to the primary amine. It is appropriate to use an excess of alkali base, for example one to five times, preferably up to three times, most preferably up to double the molar excess.
The amines may contain 1 to 3 primary alcohol groups, and the amines may be primary, secondary or tertiary amines.
The amine-group-containing primary alcohols may corresponds, for example, to formula IV,
\
-CH2OH (IV),
/
wherein Ri and R2, independently of one another, are H, linear or branched, Cι-C18-alkyl either unsubstituted or substituted by F, Cl, Br, -NH2, C1-C4-alkoxy, Cι-C4-halogenalkyl or -COOH; C3-C8-cycloalkyl, C6-Cι0-aryl or C7-C12-aralkyl either unsubstituted or substituted by F, Cl, Br, -NH2, d-Ci-alkyl, Cι-C4-alkoxy, C C4-halogenalkyl; phosphonomethyl; Ri and R2 together are tetramethylene or pentamethylene; or R, and R2, independently of one another, have the significance R3-CH2OH; and R3 is linear or branched CrCι7-alkylene which is uninterrupted or is interrupted by C3-C8-cycloalkyl or C6-Cι0-aryl.
Rt and R2 as alkyl preferably contain 1 to 12, more preferably 1 to 8, most preferably 1 to 4 carbon atoms. Examples and preferences of alkyl have already been described.
Ri and R2 as cycioalkyl preferably contain 4 to 7, most preferably 5 or 6 ring carbon atoms. Examples of cycioalkyl are cyclopropyl, cyclobutyl, cyclopentyl, cyclohexyl, cycloheptyl and cyclooctyl. Cyclohexyl is especially preferred.
Ri and R2 as aryl may be naphthyl and preferably phenyl.
Ri and R2 as aralkyl are preferably phenylalkyl. Examples are benzyl and β-phenylethyl.
R3 as alkylene preferably contain 1 to 12, more preferably 1 to 8, most preferably 1 to 4 carbon atoms. Examples of alkylene are methylene, 1 ,1- or 1 ,2-ethylene, 1 ,1 -, 1 ,2- or 1 ,3- propylene, 1 ,1-, 1 ,2-, 1 ,3- or 1 ,4-butylene, 1 ,1-, 1 ,2-, 1 ,3-, 1 ,4- or 1 ,5-pentylene, 1 ,1 -, 1 ,2-, 1 ,3-, 1 ,4-, 1 ,5- or 1 ,6-hexylene, 1 ,1-, 1 ,2-, 1 ,3-, 1 ,4-, 1 ,5-, 1 ,6- or 1 ,7-heptylene, 1 ,1-, 1 ,2-, 1 ,3-, 1 ,4-, 1 ,5-, 1 ,6-, 1 ,7- or 1 ,8-octylene, nonylene, decylene, undecylene, dodecylene, tridecylene, tetradecylene, pentadecylene, hexadecylene and heptadecylene.
The group -R3CH2OH preferably signifies 4-hydroxybutyl, 3-hydroxypropyl and most preferably 2-hydroxyethyl.
One preferred sub-group of compounds of formula IV corresponds to formula IVa,
\
N CH2 CHjOH (IVa),
/
R, wherein Ri and R2, independently of one another, signify H or unsubstituted or -NH2- or -COOH-substituted Cι-Ci2-Alkyl or -CH2CH2-OH.
In formula IVa, Ri and R2, independently of one another, preferably signify H, d-d-alky! or -CH2-CH2-OH. Another preferred sub-group is compounds of formula IVa, in which Rt is -CH2CH2-OH and R2, independently of one another, are H, d-C4-alkyl or -CH2-CH2-OH.
Some examples of compounds of formula IV are ethanolamine, diethanolamine, triethanol- amine, N-methylethanolamine, N-dimethylethanoiamine, N-methyldiethanolamine, N-ethyl- ethanolamine, N-(n-propyl)ethanolamine, N-(n-propyl)ethanolamine, N-(n-butyl)ethanol- amine, N-(n-pentyl)ethanolamine, N-(n-hexyl)ethanolamine, N-(n-octyl)ethanolamine, N-(n- decyl)ethanolamine, N-(n-dodecyl)ethanolamine, N-(n-tetradecyl)ethanolamine, N-(n-hexa- decyl)ethanolamine, N-(n-octadecyl)ethanolamine, N-(di-n-propyl)ethanolamine, N-(di-n- butyl)ethanolamine, N-(di-n-hexyl)ethanolamine, 3-hydroxypropylamine, di-(3-hydroxy- propyl)amine, tri-(3-hydroxypropyl)amine, 4-hydroxybutylamine, di-(4-hydroxybutyl)amine, tri-(4-hydroxybutyl)amine, 5-hydroxypentylamine, di-(5-hydroxypentyl)amine, tri-(5-hydroxy- pentyl)amine, 6-hydroxyhexylamine, di-(6-hydroxyhexyl)amine, tri-(6-hydroxyhexyl)amine, 8- hydroxyoctylamine, di-(8-hydroxyoctyl)amine, tri-(8-hydroxyoctyl)amine, 12-hydroxy- dodecylamine, di-(12-hydroxydodecyl)amine, tri-(12-hydroxydodecyl)amine, 18-hydroxy- octadecylamine, N-methyl-(3-hydroxypropyl)amine, N-methyl-(4-hydroxybutyl)amine, N- methyl-(6-hydroxyhexyl)amine, (2-aminoethyl)ethanolamine, di-(2-aminoethyl)ethanoiamine, phosphonomethylethanolamine, diphosphonomethylethanolamine.
The compounds of formula IV are known, are partly commercially available or may be produced by processes that are similar to those described in literature.
The process according to the invention may be carried out, for example, in such a way that the catalyst is placed in an autoclave, then first of all the primary alcohol is added, optionally in water, followed by the alkali lye, the autoclave is sealed and the reaction mixture stirred, and the reaction is commenced whilst heating. The reaction generally continues until the hydrogen generation is no longer observed. The catalyst can be decanted from the cooled reaction mixture and used for the next reaction. The alkali metal salts of carboxylic acids that are formed may be isolated and optionally purified in the usual manner. The salts may also be converted into the free carboxylic acids and derivatives thereof, such as acid amides and acid esters. The process according to the invention is suitable for production on an industrial scale.
The aminocarboxylic acids that may be produced according to the invention can be used for many purposes. Glycine is employed for food production. Aminocarboxylic acids are known complexing agents, which are used in the detergent industry and in water treatment. In addition, the amino alcohols may be used in the production of ionic surfactants. The amino alcohols are also valuable intermediates in the production of pharmaceutical and pesticidal compositions.
The following examples illustrate the invention more fully.
Example 1 : Oxidation of diethanolamine a) Preparation of the catalyst
A suspension of 8.26 g of activated Raney copper in 20 ml of water is stirred with 1.0 g of a 10% solution of NH4B4 in water, and then left to stand for 15 minutes. The whole mixture is subsequently transferred to a 300 ml nickel autoclave.
b) Oxidation of diethanolamine
To the catalyst are added 42.8 g of diethanolamine (0.4 moles), 20 ml of water and 38 g of NaOH (0.95 moles) in the form of a 50% aqueous solution. Afterwards, heating is effected to 160°C (9.5 bars, pressure regulating valve) and stirring takes place until the hydrogen generation is no longer observed (200 minutes). The yield of iminodiacetic acid disodium salt according to NMR analysis is more than 99% by weight.
c) Reuse of the catalyst
The autoclave containing the reaction mixture is cooled to 100°C. The supernatant solution is suctioned off through a riser, and the modified Cu catalyst remains in the autoclave. Then, diethanolamine and NaOH are added in the above-described proportions and reacted under the specified conditions. Up to the fifth reuse, the catalyst shows only slight activity loss (290 minutes, 92% by weight), and selectivity is maintained. Renewed impregnation with NH4BF gives a catalyst with the original high activity and selectivity. Example 2: Oxidation of diethanolamine a) Preparation of the catalyst
A suspension of 8.26 g of activated Raney copper in 20 ml of water is stirred with 0.25 g of H3(PWi2θ_to) in 20 ml of water, and then left to stand for 15 minutes. The whole mixture is subsequently transferred to a 300 ml nickel autoclave.
b) Oxidation of diethanolamine
To the catalyst are added 42.8 g of diethanolamine (0.4 moles), 20 ml of water and 33.6 g of NaOH (0.84 moles) in the form of a 50% aqueous solution. Afterwards, heating is effected to 160°C (9.5 bars, pressure regulating valve) and stirring takes place until the hydrogen generation is no longer observed (3 hours). The yield of iminodiacetic acid disodium salt according to NMR analysis is 97% by weight.
c) Reuse of the catalyst
The autoclave containing the reaction mixture is cooled to 100°C. The supernatant solution is suctioned off through a riser, and the modified Cu catalyst remains in the autoclave. Then, diethanolamine and NaOH are added in the above-described proportions and reacted under the specified conditions. Up to the eighth reuse, the catalyst shows only slight activity loss (5 hours, 89% by weight), and selectivity is maintained. Renewed impregnation with H3(PWι2O 0) gives a catalyst with the original high activity and selectivity (12th reuse, 3.5 hours, 91% by weight).
Example 3: Oxidation of diethanolamine a) Preparation of the catalyst
A suspension of 8.26 g of activated Raney copper in 20 ml of water is stirred with 0.25 g of NH4F in 20 ml of water, and then left to stand for 15 minutes. The whole mixture is subsequently transferred to a 300 ml nickel autoclave.
b) Oxidation of diethanolamine
To the catalyst are added 42.8 g of diethanolamine (0.4 moles), 20 ml of water and 33.6 g of NaOH (0.84 moles) in the form of a 50% aqueous solution. Afterwards, heating is effected to 160°C (9.5 bars, pressure regulating valve) and stirring takes place until the hydrogen generation is no longer observed (4 hours). The yield of iminodiacetic acid disodium salt according to NMR analysis is 98% by weight.
c) Reuse of the catalyst
The autoclave containing the reaction mixture is cooled to 100°C. The supernatant solution is suctioned off through a riser, and the modified Cu catalyst remains in the autoclave. Then, diethanolamine and NaOH are added in the above-described proportions and reacted under the specified conditions. Up to the twentieth reuse, the catalyst shows only slight activity loss (5 hours, 87% by weight), and selectivity is maintained. Renewed impregnation with NH4F or dispensing in NH4F during the reaction gives a catalyst with the original high activity and selectivity (21st reuse, 4 hours, 91% by weight).
Example 4: Oxidation of diethanolamine with the addition of benzaldehyde or 4-hydroxy- benzaldehyde a) Preparation of the catalyst
A suspension of 8.26 g of activated Raney copper in 20 ml of water is stirred with 0.25 g of NH4F in 20 ml of water, and then left to stand for 15 minutes. The whole mixture is subsequently transferred to a 300 ml nickel autoclave.
b) Oxidation of diethanolamine
To the catalyst are added 42.8 g of diethanolamine (0.4 moles), 4.25 g of benzaldehyde or 4.9 g of 4-hydroxybenzaldehyde, 20 ml of water and 33.6 g of NaOH (0.84 moles) in the form of a 50% aqueous solution. Afterwards, heating is effected to 160°C (or 180°C) (9.5 bars, pressure regulating valve) and stirring takes place until the hydrogen generation is no longer observed.
Figure imgf000012_0001
The yield of iminodiacetic acid disodium salt according to NMR analysis is 97-98% by weight.
c) Reuse of the catalyst
The autoclave containing the reaction mixture is cooled to 100°C. The supernatant solution is suctioned off through a riser, and the modified Cu catalyst remains in the autoclave. Then, diethanolamine, 4-hydroxybenzaldehyde (or benzaldehyde) and NaOH are added in the above-described proportions and reacted under the specified conditions. Up to the twentieth reuse, the catalyst shows only slight activity loss, and selectivity is maintained. Renewed impregnation with NH4F or dispensing in NH F during the reaction gives a catalyst with the original high activity and selectivity (21st reuse, duration of reaction 72 minutes, yield 92% by weight).

Claims

What is claimed is:
1. Raney copper, which is doped with an effective quantity of a doping agent selected from the group boric acid, onium fluorides, salts of fluorine complex anions, and heteropoly acids.
2. Raney copper according to claim 1 , in which the minimum quantity of doping agent is 10 ppm, based on the Raney copper.
3. Raney copper according to claim 1 , in which the maximum quantity of doping agent is 10000 ppm, based on the Raney copper.
4. Raney copper according to claim 1 , in which the onium fluorides correspond to formula I,
R3XH — F " (I),
wherein X is N or P and the symbols R are identical or different and signify H, d-Cαralkyl, C2-C2o-hydroxyalkyl, Cι-C4-alkoxy-C2-Cι2-alkyl, C2-C8-cycloalkyl, C6-Cι0-aryl, C7-Cι2-aralkyl or C8-C12-alkaralkyl.
5. Raney copper according to claim 4, whereby the compound of formula I is NH4F.
6. Raney copper according to claim 1 , whereby the salts of fluorine complex anions are alkali metal salts of formula II,
M^* Y ("),
wherein Me is NH4 + or an alkali metal cation, and Y signifies a perfluorine complex anion from the group BF4\ AIF4\ PF6 ', AsF6 ", SbF6 ' or BiF6 ".
7. Raney copper according to claim 1 , whereby the heteropoly acids are those of formula III, H„(ZM12O40) (III),
wherein Z is P, B, Si or Ge, M is a metal from the group W, Mo and V, and n is an integer from 3 to 6.
8. A process for the production of amine-group-containing carboxylic acid salts by oxidation of amine-group-containing primary alcohols in an aqueous-alkaline reaction medium, in the presence of a modified Raney copper catalyst and at elevated temperature, whereby the Raney copper is doped with an effective quantity of a modifying agent selected from the group boric acid, onium fluorides, salts of fluorine complex anions and heteropoly acids.
9. Process according to claim 8, in which the catalyst is used in a quantity of 0.1 to 30% by weight, based on the primary alcohol.
10. Process according to claim 8, in which the amine-group-containing primary alcohols correspond to formula IV,
\
N R3 CHjOH (|V),
wherein Ri and R2, independently of one another, are H, linear or branched, Cι-Cι8-alkyl either unsubstituted or substituted by F, Cl, Br, -NH2, C1-C4-alkoxy, Cι-C4-halogenalkyl or -COOH; C3-C8-cycloalkyl, C6-Cι0-aryl or CrC^-aralkyl either unsubstituted or substituted by F, Cl, Br, -NH2, Cι-C4-alkyl, Cι-C4-alkoxy, d-C4-halogenalkyl; phosphonomethyl; Ri and R2 together are tetramethylene or pentamethylene; or Rt and R2l independently of one another, have the significance R3-CH2OH; and R3 is linear or branched Cι-Ci7-alkylene which is uninterrupted or is interrupted by C3-C8-cycloalkyl or C6-Cι0-aryl.
PCT/EP1999/009267 1998-12-01 1999-11-29 Process for preparation of aminocarboxylic acids WO2000032310A1 (en)

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Cited By (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6706662B2 (en) 2000-04-11 2004-03-16 Monsanto Technology Llc Catalyst for dehydrogenating primary alcohols to make carboxylic acid salts
US7126024B2 (en) 2001-10-18 2006-10-24 Monsanto Technology Llc Process and catalyst for dehydrogenating primary alcohols to make carboxylic acid salts
US7682724B2 (en) 2002-10-18 2010-03-23 Monsanto Technology Llc Use of metal supported copper catalysts for reforming alcohols
US7770545B2 (en) 2006-06-13 2010-08-10 Monsanto Technology Llc Reformed alcohol power systems
WO2011113822A1 (en) 2010-03-18 2011-09-22 Basf Se Method for producing aminocarboxylates low in by-product
US20130023696A1 (en) * 2010-04-06 2013-01-24 Sumitomo Chemical Company, Limited Process for producing sulfur-containing amino acids

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* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US8865950B2 (en) 2011-08-10 2014-10-21 Saudi Arabian Oil Company Olefin hydration process with an integrated membrane reactor

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB642861A (en) * 1948-08-13 1950-09-13 Peter William Reynolds Improvements in and relating to the preparation of foraminate catalysts
US3928441A (en) * 1974-08-08 1975-12-23 Nalco Chemical Co Raney copper catalyst production and use
EP0506973A1 (en) * 1990-10-23 1992-10-07 Nippon Shokubai Co., Ltd. Process for producing salt of amino carboxylic acid
US5292936A (en) * 1993-04-12 1994-03-08 Monsanto Company Process to prepare amino carboxylic acid salts

Family Cites Families (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US529936A (en) * 1894-11-27 Ecraseur
KR0174786B1 (en) * 1993-04-12 1999-04-01 제임스 클리프튼 보올딩 Process to prepare amino carboxylic acid salts

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB642861A (en) * 1948-08-13 1950-09-13 Peter William Reynolds Improvements in and relating to the preparation of foraminate catalysts
US3928441A (en) * 1974-08-08 1975-12-23 Nalco Chemical Co Raney copper catalyst production and use
EP0506973A1 (en) * 1990-10-23 1992-10-07 Nippon Shokubai Co., Ltd. Process for producing salt of amino carboxylic acid
US5292936A (en) * 1993-04-12 1994-03-08 Monsanto Company Process to prepare amino carboxylic acid salts

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US6706662B2 (en) 2000-04-11 2004-03-16 Monsanto Technology Llc Catalyst for dehydrogenating primary alcohols to make carboxylic acid salts
US7329778B2 (en) 2000-04-11 2008-02-12 Monsanto Technology Llc Process and catalyst for dehydrogenating primary alcohols to make carboxylic acid salts
US8298985B2 (en) 2000-04-11 2012-10-30 Monsanto Technology Llc Catalyst for dehydrogenating primary alcohols
US8450523B2 (en) 2000-04-11 2013-05-28 Monsanto Technology Llc Process for preparation of a carboxylic acid salt by dehydrogenation of a primary alcohol
US7126024B2 (en) 2001-10-18 2006-10-24 Monsanto Technology Llc Process and catalyst for dehydrogenating primary alcohols to make carboxylic acid salts
US7682724B2 (en) 2002-10-18 2010-03-23 Monsanto Technology Llc Use of metal supported copper catalysts for reforming alcohols
US7770545B2 (en) 2006-06-13 2010-08-10 Monsanto Technology Llc Reformed alcohol power systems
US8100093B2 (en) 2006-06-13 2012-01-24 Monsanto Technology Llc Reformed alcohol power systems
WO2011113822A1 (en) 2010-03-18 2011-09-22 Basf Se Method for producing aminocarboxylates low in by-product
US20130023696A1 (en) * 2010-04-06 2013-01-24 Sumitomo Chemical Company, Limited Process for producing sulfur-containing amino acids

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