WO2000016902A1 - Ionic liquids - Google Patents

Ionic liquids Download PDF

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Publication number
WO2000016902A1
WO2000016902A1 PCT/GB1999/003150 GB9903150W WO0016902A1 WO 2000016902 A1 WO2000016902 A1 WO 2000016902A1 GB 9903150 W GB9903150 W GB 9903150W WO 0016902 A1 WO0016902 A1 WO 0016902A1
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ionic liquid
acid
group
organo
mole ratio
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PCT/GB1999/003150
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French (fr)
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Willi Keim
Wolfgang Korth
Peter Wasserscheid
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Bp Chemicals Limited
Akzo Nobel Nv
Elementis Uk Limited
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Priority to AU62113/99A priority Critical patent/AU6211399A/en
Publication of WO2000016902A1 publication Critical patent/WO2000016902A1/en

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    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/0277Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature
    • B01J31/0278Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre
    • B01J31/0281Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre the nitrogen being a ring member
    • B01J31/0284Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre the nitrogen being a ring member of an aromatic ring, e.g. pyridinium
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/0277Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature
    • B01J31/0278Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing nitrogen as cationic centre
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J31/00Catalysts comprising hydrides, coordination complexes or organic compounds
    • B01J31/02Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides
    • B01J31/0277Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature
    • B01J31/0287Catalysts comprising hydrides, coordination complexes or organic compounds containing organic compounds or metal hydrides comprising ionic liquids, as components in catalyst systems or catalysts per se, the ionic liquid compounds being used in the molten state at the respective reaction temperature containing atoms other than nitrogen as cationic centre
    • B01J31/0288Phosphorus
    • CCHEMISTRY; METALLURGY
    • C07ORGANIC CHEMISTRY
    • C07CACYCLIC OR CARBOCYCLIC COMPOUNDS
    • C07C211/00Compounds containing amino groups bound to a carbon skeleton
    • C07C211/62Quaternary ammonium compounds
    • C07C211/63Quaternary ammonium compounds having quaternised nitrogen atoms bound to acyclic carbon atoms
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2231/00Catalytic reactions performed with catalysts classified in B01J31/00
    • B01J2231/10Polymerisation reactions involving at least dual use catalysts, e.g. for both oligomerisation and polymerisation
    • B01J2231/12Olefin polymerisation or copolymerisation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2231/00Catalytic reactions performed with catalysts classified in B01J31/00
    • B01J2231/20Olefin oligomerisation or telomerisation
    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01JCHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2231/00Catalytic reactions performed with catalysts classified in B01J31/00
    • B01J2231/30Addition reactions at carbon centres, i.e. to either C-C or C-X multiple bonds
    • B01J2231/32Addition reactions to C=C or C-C triple bonds
    • B01J2231/323Hydrometalation, e.g. bor-, alumin-, silyl-, zirconation or analoguous reactions like carbometalation, hydrocarbation

Definitions

  • This invention relates to novel ionic liquids and use thereof as a catalyst or as a solvent for acid catalysts in chemical reactions.
  • Ionic liquids are primarily a mixture of salts which are liquid at or below ambient temperatures. Such mixtures have conventionally included (alkyl) aluminium halides in combination with one or more imidazolium halides or pyridiniurn halides which in turn may be substituted in their respective rings by one or more hydrocarbyl groups.
  • Such ionic liquids usually consist of a mixture in which the mole ratio of the (alkyl)aluminium halide to the imidazolium or pyridiniurn halide is usually > 1.0 and they invariably have Lewis acidity.
  • an (alkyl) aluminium halide - which in itself is a Lewis acid - in ionic liquids of this type enables the acidity of any conventional acids - whether Lewis or Br ⁇ nsted acids - combined therewith or dissolved in such ionic liquids to display enhanced acidity which is to be expected due to the reinforcing effect of the two acidic components. It is however, more difficult to envisage an ionic liquid displaying acidity when the ionic liquid itself is substantially free of Lewis acidity, which Lewis acidity is usually conferred upon such liquids by the presence of e.g. organo-aluminium compounds therein, and when it is combined with an acid such as e.g. a Br ⁇ nsted acid.
  • EP-A-0748653 relates to ionic salts of the general formula Q+A- where Q+ represents a quaternary ammonium and/or phosphonium salt and A- represents any known anion which can form a liquid salt at low temperatures.
  • Q+ represents a quaternary ammonium and/or phosphonium salt
  • A- represents any known anion which can form a liquid salt at low temperatures.
  • An example of a suitable salt disclosed is 3-butyl-l-methylimidazolium hexafluorophosphate.
  • the ionic salts are used as solvents or can be used in combination with transition metal complexes to catalyst hydrogenation reactions. Such ionic liquid salts are neutral
  • the present invention provides an ionic liquid which is substantially free of Lewis acidity wherein said ionic liquid is obtainable by reacting (a) an organo- nitrogen compound or an organo-phosphorus compound which is substantially free of Lewis acidity with (b) a Br ⁇ nsted acid, in a mole ratio of (a) to (b) of less than or equal to 1 with the proviso that where the Br ⁇ nsted acid gives up a single proton the mole ratio of (a) to (b) is less than 1
  • Lewis and Br ⁇ nsted acids are well known For instance such a definition can be found in 'Organic Chemistry' by Morrison and Boyd, Eds Allyn & Bacon, New York Univ. pp 32-34, 1973
  • Lewis acid as used herein and throughout the specification is meant a compound or an acid that is an electron pair acceptor which thereby enables said compound or acid to form a covalent bond
  • hydroxide ions, ammonia and water are bases because they contain electron pairs available for sharing In boron trifluoride, boron has only six electrons in its outer shell and hence tends to accept another pair to complete its octet Boron trifluoride is an acid and combines with such bases as ammonia or ethyl ether Aluminium trichloride is an acid and, stannic chloride, even though the latter has a complete octet, is an acid because it is capable of accepting additional pairs of electrons to form e g divalent tin he
  • Br ⁇ nsted acid that gives up a single proton' is meant here and throughout the specification a Br ⁇ nsted acid which contains only one hydrogen e g HNO 3 or HPF ⁇
  • Br ⁇ nsted acids that may be used to prepare the ionic liquids of the present invention include those capable of generating the following anions in the ionic liquid, BF 4 ⁇ PF 6 ' , RCOO " , CF3COO " , HO(0)C-C(O)0 ⁇ HO(0)C CH 2 -C(OH)(COOH)- CH 2 C(O)0 ⁇ RNO3 " , CF3SO3 " , H 2 P0 4 " , RPO3H-, RSO3 " , ROPO3 " , ROSO3 “ and HSO 4 " wherein R represents a C1-C30 hydrocarbyl group which may be straight or branched chain, saturated or unsaturated
  • the hydrocarbyl group is an alkyl, cycloalkyl, ary
  • the organo-nitrogen compounds used in making the ionic liquids may be substituted or unsubstituted aliphatic, alicyclic, aromatic or heterocyclic amines
  • the amines may be primary, secondary or tertiary amines Where such amines are non-cyclic compounds substituted by a hydrocarbyl group such substituents may be derived from saturated or unsaturated, aliphatic, alicyclic, cycloaliphatic or aromatic hydrocarbons
  • the amines are suitably tertiary amines and may be selected from trialkyl amines, triaryl amines, alkyl diaryl amines, aryl dialkyl amines or any combinations thereof
  • aliphatic amines such as e g triethyl amines, trimethyl phenylamines and heterocyclic amines such as dialkyl imidazoles, pyrazoles and pyridines may be used with particular advantage In the dialkyl imidazoles and
  • the hydrocarbyl group is preferably a C1 -C30 hydrocarbyl group which may be straight or branched chain, saturated or unsaturated
  • the hydrocarbyl group is an alkyl, cycloalkyl, aryl, alkaryl or aralkyl group
  • the above mentioned amines may be used as such Alternatively, a salt
  • Ionic liquids generated by reacting such an organo-phosphorus compound and a Bronsted acid will contain such cations
  • Examples of such ionic liquids include tetrabutylphosphonium tetrafluoroborate
  • the ionic liquids of the present invention can be prepared by reacting one or more of the (a) organo-nitrogen or organo-phosphorus compounds with (b) one or more Br ⁇ nsted acids in a mole ratio of (a) to (b) of less than or equal to 1 with the proviso that where the Br ⁇ nsted acid gives up a single proton the mole ratio of (a) to (b) is less than 1
  • the mole ratio (a) to (b) is in the range from 0 000
  • the temperature at which (a) and (b) react may vary over a moderate range of temperature conditions such as e g from ambient to about 150°C
  • the duration of the reaction may vary over a moderately wide range such as from about a few minutes to about a few days, for example, a week
  • the resultant products may then be purified to remove any unwanted ions or salts and any adventitious products such as water
  • the ionic liquids are generally liquids However, if any of them are solids at room temperature, they should be transformable into liquids by applying a small amount of heat, i e they are liquids at or below 80°C
  • l-butyl-3 -methyl imidazolium hydrogen sulphate can be prepared by carefully adding concentrated aqueous sulphuric acid (0 13 mole) to a cold (e g 0°C) solution of l-butyl-3-methyl ⁇ m ⁇ dazol ⁇ um chloride, (0 13 mole) in a solvent such as dry methylene chloride
  • a solvent such as dry methylene chloride
  • the admixture is then refluxed for a sufficient duration (for example, two days) to enable the reaction to be completed and any hydrogen chloride by-product to be removed therefrom
  • the solution is then cooled down to room temperature and finally the methylene chloride is removed under vacuum
  • the water present in the reaction mixture from the aqueous sulphuric acid used may be then removed by azeotropic distillation with, for example, benzene, to leave behind a clear pale yellow ionic liquid
  • the product when dried as described above, was found to be highly hygroscopic and was
  • ionic liquids having H 2 P0 4 anions derived from e g phosphoric acid or a salt thereof such as potassium dihydrogenphosphate may also be prepared as substantially described above
  • the reactants may be heated together to form a melt
  • the reactants may be heated together to form a melt
  • dissolution of the melt in a suitable solvent will yield the ionic liquid together with other reaction by-products which can be subsequently separated
  • Any water which may be adventitiously introduced into such an ionic liquid from the source of anions used to prepare said ionic liquids may either be left in (or retained) in the ionic liquid - if such water is not likely to adversely affect any subsequent reaction in which the ionic liquid is used - or, alternatively, it may be removed from the ionic liquid e g by evaporation
  • ionic liquids include l-butyl-3 - methyl imidazolium hydrogen sulphate, triethylammonium hydrogen sulphate, t ⁇ octyl ammonium hydrogen sulphate, 1 -ethyl-3 -methyl imidazolium dihydrogen phosphate and l-hexyl-3 -methyl imidazolium dihydrogen phosphate
  • ionic liquids have been characterised by NMR spectroscopy as shown in the Examples below
  • l-butyl-3 -methyl imidazolium hydrogen sulphate, triethylammonium hydrogen sulphate, t ⁇ octyl ammonium hydrogen sulphate may be derived by reacting l-butyl-3 -methylimidazolium chloride, t ⁇ ethylamine, t ⁇ octylamine, respectively with a suitable source of HSO 4 anions such as e g sulphuric acid in
  • the ionic liquids of the present invention exhibit may exhibit weak Br ⁇ nsted acidity due for instance to a residual 'proton' such as e.g. in the HSO 4 " anion.
  • a feature of the ionic liquids of the present invention is that they may be used as catalysts themselves (where the ionic liquid has weak Bronsted acidity) or as a solvent for conventional acidic catalysts used in any acid-catalysable chemical reaction.
  • the Br ⁇ nsted acid is capable of giving up at least 2 protons e.g. H 2 S0 4 , or H 3 PO 4 and the mole ratio of the organo-nitrogen or organo-phosphorus compound to the Br ⁇ nsted acid is equal to 1, the resulting ionic liquid is weakly acidic. For some acid catalysed reactions this level of acidity may be insufficient to impart good reaction performance. In such a case, addition of excess Br ⁇ nsted acid to the ionic liquid increases the acidity of the ionic liquid thereby improving the reaction performance.
  • a chemical reaction catalysed by an acid catalyst characterised in that the acid catalyst is an ionic liquid which is substantially free of Lewis acidity and wherein said ionic liquid is obtainable by reacting (a) an organo-nitrogen compound or an organo-phosphorus compound which is substantially free of Lewis acidity with (b) a Br ⁇ nsted acid which is capable of giving up at least two protons, in a mole ratio of (a) to (b) of equal to 1.
  • a chemical reaction catalysed by an acid catalyst characterised in that the acid catalyst is dissolved in an ionic liquid which is substantially free of Lewis acidity and wherein said ionic liquid is obtainable by reacting (a) an organo-nitrogen compound or an organo- phosphorus compound which is substantially free of Lewis acidity with (b) a Br ⁇ nsted acid, in a mole ratio of (a) to (b) of less than or equal to 1 with the proviso that where the Bronsted acid gives up a single proton the mole ratio of (a) to (b) is less than 1.
  • Examples of chemical reactions catalysed by acid catalysts in which the ionic liquids of the present invention may be used as an acid catalyst per se or as a solvent for an acid catalyst include esterification, polymerisation of olefins, oligomerisation, alkylation of aromatics, alkylation of isobutane with olefins and the production e.g. of caprolactam.
  • a further feature of the ionic liquids of the present invention or any acid catalysts dissolved therein is that the ionic liquids or solution of acids therein are stable liquids under conditions in the range of -100°C to about 300°C, typically from -100°C to about +100°C and at pressures ranging from 1-200 bar.
  • the advantage of using the ionic liquids of the present invention in acid catalysed reaction systems is that the solubility and/or intrinsic acidity of the Br ⁇ nsted acid can be modified by the choice of the salt or the base used as a source of cations in the ionic liquid. Such modification of the Br ⁇ nsted acid improves acid catalysed reaction performance characteristics e.g. reactivity and/or selectivity of the catalyst.
  • use of such ionic liquids facilitates the separation of the reactants and products from the catalyst due to the high solvating effect of the ionic liquid for the acid catalyst. This feature also minimises the loss of the acid catalyst which is normally associated with separation process involving conventional distillation or flashing off processes.
  • Triethylamine (10.08 mg, 0J mol) was reacted with sulphuric acid (5.5 ml concentrated sulphuric acid, 0.1 mol) in water (100 ml) for 15 minutes with stirring, the acid being added to a cold stirred amine. The water was then removed by heating under vacuum (10 mbar) at 80°C until water was shown to be absent by infra-red analysis. The resultant product (18.3 g) was a white, crystalline solid (yield 92%).
  • the cation7HSO 4 ⁇ salt remained as a high viscous, clear pale yellow ionic liquid
  • the product appeared to be very hygroscopic and hence was stored in an atmosphere inert under the conditions or in an inert solvent (e g hexane)
  • the ionic liquid was characterised by nmr-spectroscopy
  • the ionic liquid formed was hygroscopic and a solid at room-temperature
  • the resulting solid was dissolved in methanol, and the insoluble white powder (KCl) was filtered off. The methanol was removed under reduced pressure. The resulting ionic liquid was dissolved in the minimum amount of chloroform, and placed in a freezer over night; residual KCl precipitated and was removed by filtration. The solvent was removed under reduced pressure. The ionic liquid formed was hygroscopic and solid at room-temperature. The ionic liquid was characterised by nmr-spectroscopy.
  • Acetone was removed on the rotary evaporator and the resulting ionic liquid was dissolved in a minimum amount of chloroform; This solution was placed in a freezer overnight. Residual KCl precipitated and was removed by filtration. The solvent was removed under reduced pressure.
  • the ionic liquid formed was a yellow, hydroscopic and highly viscous liquid.
  • the ionic liquid was characterised by nmr-spectroscopy.
  • An acid catalyst was prepared by mixing l-butyl-3-methylimidazolium-HSO4 (BMEVl HSO 4 ) salt as prepared in Example 2 above with sulphuric acid with cooling in ice with stirring for 1 hour.
  • the resulting acid catalyst was added to 5 g of benzene and 5.6 g of 1-decene in a glass batch reactor with stirring.
  • Samples of the reaction medium were taken by pipette at intervals of 10 minutes, which were subsequently analysed by Gas Chromatography (CP Sil-5 column) in order to determine the extent of reaction. After 5 hours, stirring was stopped and the catalyst separated from the reaction medium by decantation. To prevent further reaction by any residual catalyst, 1 ml of the reaction medium was then washed by shaking with 5 ml of distilled water for 10 mins. 8. Comparative Example - Alkylation of Benzene
  • a catalyst not according to the present invention was prepared by addition of sulphuric acid in the same amount as Example 7 to 5 g of benzene and 5.6 g of 1-decene in a glass batch reactor with stirring. Samples of the reaction medium were taken by pipette at intervals of 10 minutes, which were subsequently analysed by Gas Chromatography (CP Sil-5 column) in order to determine the extent of reaction. After 5 hours, stirring was stopped and the catalyst separated from the reaction medium by decantation. To prevent further reaction by any residual catalyst, 1 ml of the reaction medium was then washed by shaking with 5 ml of distilled water for 10 mins.
  • the table below shows the relative reaction performance of the acid catalysts for alkylation of benzene with 1-decene. Experiment A employed a conventional acid catalyst (sulphuric acid) while Experiments B to D employed the acid catalysts of the present invention. Table: Acid catalysis of the alkylation of benzene with 1-decene.

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Abstract

An ionic liquid which is substantially free of Lewis acidity wherein said ionic liquid is obtainable by reacting (a) an organo-nitrogen compound or an organo-phosphorus compound which is substantially free of Lewis acidity with (b) a Brønsted acid, in a mole ratio of (a) to (b) of less than or equal to 1 with the proviso that where the Brønsted acid gives up a single proton the mole ratio of (a) to (b) is less than 1. The ionic liquids are useful as acid catalysts or as solvents for acid catalysts, for example, in esterification reactions or in the alkylation of aromatics.

Description

IONIC LIQUIDS
This invention relates to novel ionic liquids and use thereof as a catalyst or as a solvent for acid catalysts in chemical reactions.
Ionic liquids are primarily a mixture of salts which are liquid at or below ambient temperatures. Such mixtures have conventionally included (alkyl) aluminium halides in combination with one or more imidazolium halides or pyridiniurn halides which in turn may be substituted in their respective rings by one or more hydrocarbyl groups. Such ionic liquids usually consist of a mixture in which the mole ratio of the (alkyl)aluminium halide to the imidazolium or pyridiniurn halide is usually > 1.0 and they invariably have Lewis acidity. The presence of an (alkyl) aluminium halide - which in itself is a Lewis acid - in ionic liquids of this type enables the acidity of any conventional acids - whether Lewis or Brønsted acids - combined therewith or dissolved in such ionic liquids to display enhanced acidity which is to be expected due to the reinforcing effect of the two acidic components. It is however, more difficult to envisage an ionic liquid displaying acidity when the ionic liquid itself is substantially free of Lewis acidity, which Lewis acidity is usually conferred upon such liquids by the presence of e.g. organo-aluminium compounds therein, and when it is combined with an acid such as e.g. a Brønsted acid.
EP-A-0748653 relates to ionic salts of the general formula Q+A- where Q+ represents a quaternary ammonium and/or phosphonium salt and A- represents any known anion which can form a liquid salt at low temperatures. An example of a suitable salt disclosed is 3-butyl-l-methylimidazolium hexafluorophosphate. The ionic salts are used as solvents or can be used in combination with transition metal complexes to catalyst hydrogenation reactions. Such ionic liquid salts are neutral
It has now been found that by using ionic liquids having Brønsted acidity, which are substantially free of Lewis acidity, these can be used as acid catalysts as such or as solvents for conventional acid catalysts
Accordingly, the present invention provides an ionic liquid which is substantially free of Lewis acidity wherein said ionic liquid is obtainable by reacting (a) an organo- nitrogen compound or an organo-phosphorus compound which is substantially free of Lewis acidity with (b) a Brønsted acid, in a mole ratio of (a) to (b) of less than or equal to 1 with the proviso that where the Brønsted acid gives up a single proton the mole ratio of (a) to (b) is less than 1
The definitions of Lewis and Brønsted acids are well known For instance such a definition can be found in 'Organic Chemistry' by Morrison and Boyd, Eds Allyn & Bacon, New York Univ. pp 32-34, 1973 Thus, by "Lewis" acid as used herein and throughout the specification is meant a compound or an acid that is an electron pair acceptor which thereby enables said compound or acid to form a covalent bond Thus, hydroxide ions, ammonia and water are bases because they contain electron pairs available for sharing In boron trifluoride, boron has only six electrons in its outer shell and hence tends to accept another pair to complete its octet Boron trifluoride is an acid and combines with such bases as ammonia or ethyl ether Aluminium trichloride is an acid and, stannic chloride, even though the latter has a complete octet, is an acid because it is capable of accepting additional pairs of electrons to form e g divalent tin hexachloride (SnCl6 2-)
By 'Brønsted acid' is meant here and throughout the specification a compound or an acid that gives up a proton Thus, when sulphuric acid dissolves in water, the acid gives up a proton to the base water to form new, relatively weaker acids H30+ (hydronium ion) and HSO4 " (hydrogen sulphate ion) According to this definition, the strength of an acid depends upon its tendency to give up a proton Sulphuric acid and hydrogen chloride are strong acids since they tend to give up a proton very readily
By 'Brønsted acid that gives up a single proton' is meant here and throughout the specification a Brønsted acid which contains only one hydrogen e g HNO3 or HPFβ Examples of Brønsted acids that may be used to prepare the ionic liquids of the present invention include those capable of generating the following anions in the ionic liquid, BF4\ PF6 ', RCOO", CF3COO", HO(0)C-C(O)0\ HO(0)C CH2-C(OH)(COOH)- CH2 C(O)0\ RNO3", CF3SO3", H2P04 ", RPO3H-, RSO3", ROPO3", ROSO3" and HSO4 " wherein R represents a C1-C30 hydrocarbyl group which may be straight or branched chain, saturated or unsaturated Preferably, the hydrocarbyl group is an alkyl, cycloalkyl, aryl, alkaryl or aralkyl group The hydrocarbyl group may be optionally further substituted with a group containing nitrogen, oxygen, sulphur, silicon or halogen atoms Specifically, the respective Brønsted acids from which these anions may be derivable are HBF4, HPF6, acetic acid, trifluoroacetic acid, oxalic acid, citric acid, FfNO3, trifluorosulphonic acid, H3PO4, a partial ester of phosphoric acid, a partial ester of sulphuric acid and H2SO4 Such Brønsted acids may be used singly or as a mixture of one or more such acids thereby generating one anion corresponding to each Brønsted acid used Preferably, the Brønsted acid used is capable of giving up at least 2 protons,
Figure imgf000005_0001
The organo-nitrogen compounds used in making the ionic liquids may be substituted or unsubstituted aliphatic, alicyclic, aromatic or heterocyclic amines The amines may be primary, secondary or tertiary amines Where such amines are non-cyclic compounds substituted by a hydrocarbyl group such substituents may be derived from saturated or unsaturated, aliphatic, alicyclic, cycloaliphatic or aromatic hydrocarbons The amines are suitably tertiary amines and may be selected from trialkyl amines, triaryl amines, alkyl diaryl amines, aryl dialkyl amines or any combinations thereof In particular, aliphatic amines such as e g triethyl amines, trimethyl phenylamines and heterocyclic amines such as dialkyl imidazoles, pyrazoles and pyridines may be used with particular advantage In the dialkyl imidazoles and the pyridines, the alkyl groups may be the same or different e g l-methyl-3-ethylimidazole, l-methyl-3-butylimidazole, 1-ethyl- 3-butylimidazole, l-hexyl-3-methylimidazole, dimethylimidazoles and diethylimidazoles, and the corresponding dialkyl derivatives of pyrazole and pyridine In respect of the imidazoles and their salts, it should be noted that the 1- and 3- positions are interchangeable due to the symmetrical nature of the imidazole ring. The organo-nitrogen compound may have cations represented by the generic formula [NR'R2R3R4]+ or [R1R2^=CR3-R5-R3C=N+R2R1] wherein R'-R4 can be the same or different and is selected from H or a hydrocarbyl group with the proviso that at least one of R'-R4 is a hydrocarbyl group and R5 is an alkylene group (e g CH2, CH2CH2 etc type group) or a phenylene group (e g C6H type group) The hydrocarbyl group is preferably a C1 -C30 hydrocarbyl group which may be straight or branched chain, saturated or unsaturated Preferably, the hydrocarbyl group is an alkyl, cycloalkyl, aryl, alkaryl or aralkyl group In the preparation of the ionic liquid of the present invention, the above mentioned amines may be used as such Alternatively, a salt of the amine may be used e g a chloride The preparation of such amine salts is well known in the art
The organo phosphorus compound used in making the ionic liquids of the present invention may contain cations of the formula [PR!R2R3R4]+ or [R1R2+P=CR3-R5-
R3C=PH2R1] wherein R'-R5 have the same significance as described in the context of [NR'R2R3R4f and [R1R2+ =CR3-R5-R3C=N+R2R1] above Ionic liquids generated by reacting such an organo-phosphorus compound and a Bronsted acid will contain such cations Examples of such ionic liquids include tetrabutylphosphonium tetrafluoroborate The ionic liquids of the present invention can be prepared by reacting one or more of the (a) organo-nitrogen or organo-phosphorus compounds with (b) one or more Brønsted acids in a mole ratio of (a) to (b) of less than or equal to 1 with the proviso that where the Brønsted acid gives up a single proton the mole ratio of (a) to (b) is less than 1 Suitably the mole ratio (a) to (b) is in the range from 0 00001 to 1, preferably in the range 0 001 -0 96 and more preferably in the range from 0 01 to 0 05 Where the Brønsted acid gives up a single proton such as F£NO3i ionic liquids according to the present invention may be suitably prepared by (i) reacting one or more of the organo- nitrogen or organo-phosphorus compounds with the Brønsted acid in a mole ratio of the organo-nitrogen or organo-phosphorus compounds to the Brønsted acid of equal to 1 to form a neutral ionic salt and (ii) adding further Brønsted acid (such that the mole ratio of (a) to (b) is less than 1 ) to the neutral ionic salt to form an ionic liquid according to the present invention
Due to the varied nature of the reactants the temperature at which (a) and (b) react may vary over a moderate range of temperature conditions such as e g from ambient to about 150°C The duration of the reaction may vary over a moderately wide range such as from about a few minutes to about a few days, for example, a week The resultant products may then be purified to remove any unwanted ions or salts and any adventitious products such as water The ionic liquids, as the name implies, are generally liquids However, if any of them are solids at room temperature, they should be transformable into liquids by applying a small amount of heat, i e they are liquids at or below 80°C
More specifically and, in particular l-butyl-3 -methyl imidazolium hydrogen sulphate can be prepared by carefully adding concentrated aqueous sulphuric acid (0 13 mole) to a cold (e g 0°C) solution of l-butyl-3-methylιmιdazolιum chloride, (0 13 mole) in a solvent such as dry methylene chloride The admixture is then refluxed for a sufficient duration (for example, two days) to enable the reaction to be completed and any hydrogen chloride by-product to be removed therefrom The solution is then cooled down to room temperature and finally the methylene chloride is removed under vacuum The water present in the reaction mixture from the aqueous sulphuric acid used may be then removed by azeotropic distillation with, for example, benzene, to leave behind a clear pale yellow ionic liquid The product, when dried as described above, was found to be highly hygroscopic and was therefore stored under an inert atmosphere and/or solvent The product was characterised by NMR spectroscopy
Similarly, ionic liquids having H2P04 anions derived from e g phosphoric acid or a salt thereof such as potassium dihydrogenphosphate may also be prepared as substantially described above Alternatively, where one or more of the reactants is a solid at ambient temperature, the reactants may be heated together to form a melt Subsequent dissolution of the melt in a suitable solvent will yield the ionic liquid together with other reaction by-products which can be subsequently separated
Any water which may be adventitiously introduced into such an ionic liquid from the source of anions used to prepare said ionic liquids may either be left in (or retained) in the ionic liquid - if such water is not likely to adversely affect any subsequent reaction in which the ionic liquid is used - or, alternatively, it may be removed from the ionic liquid e g by evaporation
Specific examples of ionic liquids according to the invention include l-butyl-3 - methyl imidazolium hydrogen sulphate, triethylammonium hydrogen sulphate, tπoctyl ammonium hydrogen sulphate, 1 -ethyl-3 -methyl imidazolium dihydrogen phosphate and l-hexyl-3 -methyl imidazolium dihydrogen phosphate Such ionic liquids have been characterised by NMR spectroscopy as shown in the Examples below l-butyl-3 -methyl imidazolium hydrogen sulphate, triethylammonium hydrogen sulphate, tπoctyl ammonium hydrogen sulphate may be derived by reacting l-butyl-3 -methylimidazolium chloride, tπethylamine, tπoctylamine, respectively with a suitable source of HSO4 anions such as e g sulphuric acid in a mole ratio of nitrogen compound to sulphuric acid of e g less than 1 or equal to 1 1 -ethyl-3 -methyl imidazolium dihydrogen phosphate and 1- hexyl-3 -methyl imidazolium dihydrogen phosphate may be derived by reacting 1 -ethyl-3 - methylimidazolium chloride, 1 -hexyl-3 -methylimidazolium chloride, respectively, with a suitable source of H P04 " anions such as e.g. ortho-phosphoric acid or potassium dihydrogenphosphate in a mole ratio of nitrogen compound to Brønsted acid of less than or equal to 1.
The ionic liquids of the present invention exhibit may exhibit weak Brønsted acidity due for instance to a residual 'proton' such as e.g. in the HSO4 " anion.
A feature of the ionic liquids of the present invention is that they may be used as catalysts themselves (where the ionic liquid has weak Bronsted acidity) or as a solvent for conventional acidic catalysts used in any acid-catalysable chemical reaction.
In the case where the Brønsted acid is capable of giving up at least 2 protons e.g. H2S04, or H3PO4 and the mole ratio of the organo-nitrogen or organo-phosphorus compound to the Brønsted acid is equal to 1, the resulting ionic liquid is weakly acidic. For some acid catalysed reactions this level of acidity may be insufficient to impart good reaction performance. In such a case, addition of excess Brønsted acid to the ionic liquid increases the acidity of the ionic liquid thereby improving the reaction performance.
According to yet another embodiment of the present invention there is provided a chemical reaction catalysed by an acid catalyst, characterised in that the acid catalyst is an ionic liquid which is substantially free of Lewis acidity and wherein said ionic liquid is obtainable by reacting (a) an organo-nitrogen compound or an organo-phosphorus compound which is substantially free of Lewis acidity with (b) a Brønsted acid which is capable of giving up at least two protons, in a mole ratio of (a) to (b) of equal to 1.
According to yet a further embodiment of the present invention there is provided a chemical reaction catalysed by an acid catalyst, characterised in that the acid catalyst is dissolved in an ionic liquid which is substantially free of Lewis acidity and wherein said ionic liquid is obtainable by reacting (a) an organo-nitrogen compound or an organo- phosphorus compound which is substantially free of Lewis acidity with (b) a Brønsted acid, in a mole ratio of (a) to (b) of less than or equal to 1 with the proviso that where the Bronsted acid gives up a single proton the mole ratio of (a) to (b) is less than 1. Examples of chemical reactions catalysed by acid catalysts in which the ionic liquids of the present invention may be used as an acid catalyst per se or as a solvent for an acid catalyst include esterification, polymerisation of olefins, oligomerisation, alkylation of aromatics, alkylation of isobutane with olefins and the production e.g. of caprolactam.
A further feature of the ionic liquids of the present invention or any acid catalysts dissolved therein is that the ionic liquids or solution of acids therein are stable liquids under conditions in the range of -100°C to about 300°C, typically from -100°C to about +100°C and at pressures ranging from 1-200 bar.
The advantage of using the ionic liquids of the present invention in acid catalysed reaction systems is that the solubility and/or intrinsic acidity of the Brønsted acid can be modified by the choice of the salt or the base used as a source of cations in the ionic liquid. Such modification of the Brønsted acid improves acid catalysed reaction performance characteristics e.g. reactivity and/or selectivity of the catalyst. In addition, use of such ionic liquids facilitates the separation of the reactants and products from the catalyst due to the high solvating effect of the ionic liquid for the acid catalyst. This feature also minimises the loss of the acid catalyst which is normally associated with separation process involving conventional distillation or flashing off processes. The present invention is further illustrated with reference to the following
Examples: 1. Synthesis of triethylammonium hydrogen sulphate
Triethylamine (10.08 mg, 0J mol) was reacted with sulphuric acid (5.5 ml concentrated sulphuric acid, 0.1 mol) in water (100 ml) for 15 minutes with stirring, the acid being added to a cold stirred amine. The water was then removed by heating under vacuum (10 mbar) at 80°C until water was shown to be absent by infra-red analysis. The resultant product (18.3 g) was a white, crystalline solid (yield 92%). The product upon analysis by NMR had the following characteristics: Η-NMR (CD3CN): d=8.65 (br, 1H, HSO4); 8.36 (s, 1H, HN); 3J6 (m, 6H, N[CH2CH3]3); 1.28 (m, N[CH2CH3]3)
13C-NMR (CD3CN): d=46J5 (N[CH2CH3]3); 7.77 (N[CH2CH3]3). C, H, N Analysis:
Figure imgf000009_0001
The above data confirm the structure of the compound to be that of triethylammonium hydrogen sulphate (HNEt3ΗSθ4 ~)
2. Synthesis of l-butyl-3-methyl imidazolium hydrogen sulphate:
In a flask equipped with a dropping funnel, a condenser and a magnetic stirrer 1- butyl-3 -methylimidazolium chloride salt (22 12 g, 0 13 mol) was dissolved in dry methylene chloride (100 ml) The solution was cooled to 0°C with an ice bath To this solution (13 06 g) was carefully added an aqueous solution of concentrated sulphuric acid (97 14 %, 0 13 mol) To obtain a hydrogen sulphate ionic liquid, the sulphuric acid and the organic salt were used in the same molecular ratios After the addition of the solution was completed, the mixture was heated under reflux for two days From time to time any HC1 by-product formed in the process which was distilling out of the condenser was monitored When the formed HC1 had been completely removed the solution was cooled to room temperature and the methylene chloride was removed carefully under vacuum To remove any water (generated from the aqueous sulphuric acid used) benzene (10 ml) was added to the viscous residue and the biphasic mixture was heated to 50°C to give a nearly homogeneous solution for several hours and the benzene/water azeotrope was then removed
The cation7HSO4 ~ salt remained as a high viscous, clear pale yellow ionic liquid The product appeared to be very hygroscopic and hence was stored in an atmosphere inert under the conditions or in an inert solvent (e g hexane) The ionic liquid was characterised by nmr-spectroscopy
NMR-Data
Η-NMR (CD3CN) d= 1 1 02 (s, 1H, H,), 8 99 (s, 1H, Ha), 7 50 (m, 2H, Hc H_), 4 16 (t, 2H, He), 3 85 (s, 3H, Hb), 1 75 (m, 2H,Hf), 1 25 (m, 2H, Hg), 0,83 (t,3H,Hh)
1 C-NMR (CD3CN) d = 137 759 (Ca), 124 59 (Cc), 123 207 (Cd), 49 963 (Ce), 36 729
(Cb), 32 616 (Cf), 19 884 (Cg), 13 765 (Ch)
3. Synthesis of trioctyl ammonium hydrogen sulphate
In a flask equipped with a dropping funnel, a condenser and a magnetic stirrer 161 8 g (0 46 mol) trioctylamine was dissolved in 200 ml of ether The solution was stiπed vigorously and 46 05 g (0 46 mol H2S04) of an 18 molar concentrated sulphuric acid was carefully dropped into the solution To obtain a hydrogen sulphate ionic liquid, the sulphuric acid and the amine were used in equimolar ratios During the reaction the solution became warmer
After completion of the addition, the resultant solution was stirred for 15 min The solvent was removed carefully under vacuum room temperature The [HN(Octyl) ]+[HSO4]~ salt remained as a white waxy crystalline solid The product appeared not to be very hygroscopic The ionic liquid was characterised by nmr- spectroscopy The yield of the product was 197 g (95 % of theory) NMR-Data
Η-NMR (CD3CN) d = 8 61 (br, 1H, HS04), 3 82 (s, 1H, HN), 3 03 (m, 6H, N[CH2CH2(CH2)5CH3]3), 1 7 (tr, 6H, N[CH2CH2(CH2)5CH3]3), 1 34 (m, 30H, N[CH2CH2CH2CH2CH2CH3]3), 0 92 (m, 9H, N[CH2CH3]3)
Figure imgf000011_0001
4. Synthesis of l-ethyl-3-methylimidazolium dihydrogen phosphate
1 -ethyl-3 -methylimidazolium chloride (33 8 g, 0 23 mol) was dissolved in chloroform (150 cm3) in a round-bottomed flask equipped with a magnetic stir bar The solution was cooled to 0°C -phosphoric acid (90%, 14 8 cm3) was added drop-wise After the addition was completed, the mixture was heated under reflux for about 5 hours, and then stirred at room-temperature for 48 hours, 2 phases formed The lower phase was dried over magnesium sulphate, and the solvent removed under reduced pressure
The ionic liquid formed was hygroscopic and a solid at room-temperature
The ionic liquid was characterised by nmr-spectroscopy
Η-NMR (D2Q. 300MHz) δ = 8 46(s, 1H, H(C-2)), 7 22 (d, 2H, H(C-4, C-5)), 4 0 (q,
2H, N-CH2-CH3), 3 59 (s, 3H, N-CH3), 1 26 (t, 3H, N-CH2-CH3)
13C-NMR (D2Q. 300MHz) δ = 135 7 (C-2), 123 68, 122 08 (C-4, C-5), 45 0 (N-CH2- CH3); 35.89 (N-CH3); 14.74 (N-CH2-CH3).
31P (D2O. 300MHz): A single peak appears at 2.0ppm. A sealed melting-point tube containing 90% H3PO4 was inserted as internal standard. Two clearly separated peaks appear, indicating the two different phosphorus species H2PO4 " and H3PO . 5. Synthesis of l-ethyl-3-methylimidazolium dihydrogen phosphate l-ethy-3 -methylimidazolium chloride ( 35.4g, 0.24mol) was melted in a round-bottomed flask equipped with a magnetic stir bar by means of an oil-bath. KH2PO4 (25.6g, 0.24 mol) was added and the melt stirred for 24 hrs. After cooling to room-temperature, the resulting solid was dissolved in methanol, and the insoluble white powder (KCl) was filtered off. The methanol was removed under reduced pressure. The resulting ionic liquid was dissolved in the minimum amount of chloroform, and placed in a freezer over night; residual KCl precipitated and was removed by filtration. The solvent was removed under reduced pressure. The ionic liquid formed was hygroscopic and solid at room-temperature. The ionic liquid was characterised by nmr-spectroscopy.
'H-NMR fD2O. 300MHz): δ = 8.60(s, 1H, H(C-2)); 7J8 (d, 2H, H(C-4, C-5)); 4.1 (q, 2H, N-CH2-CH3); 3.75 (s, 3H, N-CH3); 1.51 (t, 3H, N-CH2-CH3). "C-NMR (D2O. 300MHz): δ = 135.5 (C-2); 123.4, 121.1 (C-4, C-5); 44.7 (N-CH2- CH3); 35.5 (N-CH3); 14.4 (N-CH2-CH3). 31P (D O. 300MHz): A single peak appears at 2.0ppm. A sealed melting-point tube containing 90% H3PO was inserted as internal standard. Two clearly separated peaks appear, indicating two different phosphorus species. 6. Synthesis of l-hexyl-3-methylimidazolium dihydrogen phosphate 1 -hexyl-3 -methylimidazolium chloride (95.6g, 0.47mol) was dissolved in acetone (250 cm3) in a round-bottomed flask equipped with a magnetic stir bar. KH2PO4 (65.5g, 0.48mol) was added to this solution. The mixture was stirred for 2 days at room- temperature. The white precipitate (KCl) was removed by filtration. Acetone was removed on the rotary evaporator and the resulting ionic liquid was dissolved in a minimum amount of chloroform; This solution was placed in a freezer overnight. Residual KCl precipitated and was removed by filtration. The solvent was removed under reduced pressure.
The ionic liquid formed was a yellow, hydroscopic and highly viscous liquid. The ionic liquid was characterised by nmr-spectroscopy. Η-NMR (P.O. 300MHz): δ = 8.8(s, 1H, H(C-2)); 7.5 (d, 2H, H(C-4, C-5)); 4.2 (t, 2H, N-CH2-(CH2)4-CH3); 3.9 (s, 3H, N-CH3); 1.9 (t, 2H, N-CH2-CH2-(CH2)3-CH3); 1.3 (m, 6H, N-CH2-CH2-(CH2)3-CH3); 0.8 (t, 3H, N-(CH2)5-CH3).
13C-NMR (D2O. 300MHz): δ = 136.3 (C-2); 124.0, 122.8 (C-4, C-5); 50.0 (N-CH2— (CH2)4-CH3); 36.2 (N-CH3); 30.8; 29.7; 25.5; 22.3 (N-CH2-(CH2)4-CH3); 13.8 (N- (CH2)5-CH3).
31P (D O, 300MHz): A single peak appears at 2.0ppm. A sealed melting-point tube containing 90% H3PO was inserted as internal standard. Two clearly separated peaks appear, indicating two different phosphorus species. 7. Alkylation of Benzene
An acid catalyst was prepared by mixing l-butyl-3-methylimidazolium-HSO4 (BMEVl HSO4) salt as prepared in Example 2 above with sulphuric acid with cooling in ice with stirring for 1 hour. The resulting acid catalyst was added to 5 g of benzene and 5.6 g of 1-decene in a glass batch reactor with stirring. Samples of the reaction medium were taken by pipette at intervals of 10 minutes, which were subsequently analysed by Gas Chromatography (CP Sil-5 column) in order to determine the extent of reaction. After 5 hours, stirring was stopped and the catalyst separated from the reaction medium by decantation. To prevent further reaction by any residual catalyst, 1 ml of the reaction medium was then washed by shaking with 5 ml of distilled water for 10 mins. 8. Comparative Example - Alkylation of Benzene
A catalyst not according to the present invention was prepared by addition of sulphuric acid in the same amount as Example 7 to 5 g of benzene and 5.6 g of 1-decene in a glass batch reactor with stirring. Samples of the reaction medium were taken by pipette at intervals of 10 minutes, which were subsequently analysed by Gas Chromatography (CP Sil-5 column) in order to determine the extent of reaction. After 5 hours, stirring was stopped and the catalyst separated from the reaction medium by decantation. To prevent further reaction by any residual catalyst, 1 ml of the reaction medium was then washed by shaking with 5 ml of distilled water for 10 mins. The table below shows the relative reaction performance of the acid catalysts for alkylation of benzene with 1-decene. Experiment A employed a conventional acid catalyst (sulphuric acid) while Experiments B to D employed the acid catalysts of the present invention. Table: Acid catalysis of the alkylation of benzene with 1-decene.
Experiment BMEM HSO4 in the Reaction time for Selectivity to catalyst system (mass 40% conversion monoalkylated
%) product (at 40% Conversion)
A 0 10 "63
B 4.8 10 68
C 12.3 100 74
D 19.4 170 87

Claims

Claims
1. An ionic liquid which is substantially free of Lewis acidity wherein said ionic liquid is obtainable by reacting (a) an organo-nitrogen compound or an organo- phosphorus compound which is substantially free of Lewis acidity with (b) a Brønsted acid, in a mole ratio of (a) to (b) of less than or equal to 1 with the proviso that where the Brønsted acid gives up a single proton the mole ratio of (a) to (b) is less than 1.
2. An ionic liquid as claimed in claim 1 wherein the organo-nitrogen compound is selected from the group consisting of aliphatic amines and heterocyclic amines.
3. An ionic liquid as claimed in claim 1 wherein the organo-nitrogen compound has a cation selected from the group consisting of the formula [NR1R2R3R4]+ or [R1R2^=CR3-R5-R3C=N+R2RI] wherein R'-R4 can be the same or different and is selected from H or a hydrocarbyl group with the proviso that at least one of R'-R4 is a hydrocarbyl group and R5 is an alkylene group or a phenylene group.
4. An ionic liquid as claimed in claim 1 wherein the organo-phosphorus compound has a cation selected from the group consisting of the formula [PR!R2R3R4]+ or [R1R2+P=CR3-R5-R3C=P+R2R1] wherein R'-R4 can be the same or different and is selected from H or a hydrocarbyl group with the proviso that at least one of Rx-R4 is a hydrocarbyl group and R5 is an alkylene group or a phenylene group.
5. An ionic liquid as claimed in any one of claims 1-4 wherein the Brønsted acid has an anion selected from the group consisting of BF4", PF6 ", RCOO", CF3COO", HO(O)C- C(O)O_, HO(O)C.CH2-C(OH)(COOH)-CH2.C(O)O", RNO3 ", CF3SO3\ H2PO4 ", KPO_K, RSO3 ", ROPO3 ", ROSO3 " and HSO4 " wherein R represents a C1-C30 hydrocarbyl group
6. An ionic liquid as claimed in claim 1 wherein the ionic liquid is selected from the group consisting of l-butyl-3 -methylimidazolium hydrogen sulphate and triethylammonium hydrogen sulphate.
7. An ionic liquid as claimed in any one of claims 1-6 wherein the mole ratio of the (a) to (b) is in the range from 0.00001 to 1.
8. An ionic liquid as claimed in claim 7 wherein the mole ratio of (a) to (b) is in the range from 0.001 to 0.05.
9. A chemical reaction catalysed by an acid catalyst, characterised in that the acid catalyst is or is dissolved in an ionic liquid as defined in any one of the preceding claims.
10. A chemical reaction according to claim 9 wherein the chemical reaction catalysed by the acid catalyst is selected from the group of reactions consisting of esterification, olefin polymerisation, oligomerisation, alkylation of aromatics, alkylation of isobutane with olefins and the production of caprolactam.
11. Use of an ionic liquid as claimed in any one of claims 1-9 as an acid catalyst or as a solvent for an acid catalyst.
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DE10123467A1 (en) * 2001-05-15 2002-11-21 Studiengesellschaft Kohle Mbh Activation of cationic transition metal catalyst, useful in e.g. metathesis, oligomerization reaction, involves using ionic liquid and compressed carbon dioxide
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WO2006007912A1 (en) 2004-07-16 2006-01-26 Merck Patent Gmbh Method for producing onium salts with a low chloride content
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Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2626572A1 (en) * 1988-02-02 1989-08-04 Inst Francais Du Petrole Process for alkylating aliphatic hydrocarbons
WO1996018459A1 (en) * 1994-12-13 1996-06-20 Bp Chemicals Limited Ionic liquids
EP0748653A1 (en) * 1995-06-16 1996-12-18 Institut Francais Du Petrole New catalytic composition containing transition metals complexes and insatured compounds hydrogenation process
FR2757850A1 (en) * 1996-12-27 1998-07-03 Inst Francais Du Petrole Diels-Alder reaction in ionic liquid medium

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
FR2626572A1 (en) * 1988-02-02 1989-08-04 Inst Francais Du Petrole Process for alkylating aliphatic hydrocarbons
WO1996018459A1 (en) * 1994-12-13 1996-06-20 Bp Chemicals Limited Ionic liquids
EP0748653A1 (en) * 1995-06-16 1996-12-18 Institut Francais Du Petrole New catalytic composition containing transition metals complexes and insatured compounds hydrogenation process
FR2757850A1 (en) * 1996-12-27 1998-07-03 Inst Francais Du Petrole Diels-Alder reaction in ionic liquid medium

Non-Patent Citations (2)

* Cited by examiner, † Cited by third party
Title
CHEMICAL ABSTRACTS, vol. 125, no. 19, 4 November 1996, Columbus, Ohio, US; abstract no. 246895k, OLIVIER H: "Nonaqueous room-temperature ionic liquids: a new class of solvents for catalytic organic reactions" page 1060; XP002107859 *
PROC. ELECTROCHEM. SOC., 1996 *

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