US20150007963A1

US20150007963A1 - Ionic liquids for cooling in high temperature environment

Info

Publication number: US20150007963A1
Application number: US14/375,117
Authority: US
Inventors: Roland Kalb
Original assignee: VTU Holding GmbH
Current assignee: VTU Holding GmbH
Priority date: 2012-02-02
Filing date: 2012-12-28
Publication date: 2015-01-08
Also published as: BR112014018886A2; RU2621105C2; CA2861775A1; AU2012367944B2; HK1202570A1; CA2861775C; EP2809739B1; BR112014018886B1; CL2014001852A1; PH12014501742A1; US20160138876A1; US10677532B2; MX2014008635A; WO2013113461A1; JP2017110229A; RU2014135520A; CN104080880B; CN104080880A; EP2809739A1; JP2015509130A

Abstract

Cooling medium comprising an ionic liquid with a hydrogen content of 0% to 8.5% by weight and its use.

Description

The present invention relates to ionic liquids which are useful for cooling in high temperature environment.
According to generally accepted literature an ionic liquid is a salt in the liquid state, more particularly a melt of a low melting salt, e.g. with a melting point equal or below 100° C. (see e.g. Wasserscheid, Peter; Welton, Tom (Eds.); “Ionic Liquids in Synthesis”, Wiley-VCH 2008; ISBN 978-3-527-31239-9). However, it is to note that the melting temperature of ≦100° C. is chosen arbitrarily.
Such ionic liquids may exhibit some very interesting characteristics, e.g. having a very low, virtually non measurable vapor pressure, a large liquidus range, good electrical conductivity and interesting solvation characteristics. These characteristics make ionic liquids prone for several applications, e.g. as solvents (for example, in organic or inorganic synthesis, transition metal catalysis, biocatalysis, multiphase reactions, photochemistry, polymer synthesis, and nanotechnology), extracting agent (e.g. liquid-liquid or liquid gaseous extraction, sulphur removal during crude oil processing, removal of heavy metals during water processing and liquid membrane extraction), electrolytes (for example, in batteries, fuel cells, capacitors, solar cells, sensors, electroplating, electrochemical metal processing, electrochemical synthesis, and nanotechnology), lubricants, gels, reagents for organic synthesis, in the so-called “green chemistry” (e.g. as replacement for volatile organic compounds), antistatic addtives, specific applications in chemical analysis (e.g. gas chromatography, mass spectroscopy, capillary zone electrophoresis), liquid crystals, for storing and releasing hydrogen, as thermofluids, e.g. as cooling medium, etc.
In US 2009/314460 a process for strip casting is described using a travelling mould which is cooled by a liquid coolant, wherein the coolant is liquid metal or ionic liquid wherein ionic liquids are defined as a group of salts composed of organic cations and mostly inorganic anions which generally have a melting point below 100° C.
In WO 2010/136403 ionic liquids for use as a cooling medium are disclosed. It is described that ionic liquids are exclusively composed from ions (cations and anions) and are salts that are liquid at temperatures below 100° C. without the salts being dissolved in a solvent such as water. Cations according to WO 2010/136403 include imidazolium, pyridinium, pyrrolidinium, guanidinium, uronium, thiouronium, piperidinium, morpholinium, phosphonium or ammonium, which cations additionally can be alkylated and anions include sulfates, phosphates, halides, fluorinated anions such as tetrafluoroborate, hexafluoroborate, trifluoroacetate, trifluoromethanesulfonate and hexafluorophosphate, sulfonates, phosphinates or tosylates.
It is known that ionic liquids do have virtually no vapor pressure and are therefore generally non flammable below their high thermal decomposition point of up to 300° C. and even more. When heated up above their thermal decomposition temperature, however, they form gaseous, molecular decomposition products, which are flammable. In combustion experiments it can be seen, that a typical ionic liquid starts to burn after the bulk phase has reached the flashpoint temperature and that in many cases the combustion only continues, if a quite high input of external heat from a heat source is given. This is in contrast to conventional, molecular liquids: E.g. mineral oil can be ignited at temperatures of approx. 80 to 100° C., which is far below its thermal decomposition point, because mineral oil does have a vapor pressure and forms a flammable gas phase at this temperatures. As described in WO2010136403A1, ionic liquids do not form a highly explosive mixture of hydrogen and oxygen (detonating gas or oxyhydrogen gas) when in contact with hot (reducing) surfaces or hot (reducing) melts at temperatures above approx. 500° C. That is in contrast to water, which still is widely used as cooling agent. Drawbacks of ionic liquids in contrast to water may be the higher viscosity in the range of typically some 10 to some 100 mPas at 20° C. and a specific heat capacity of approx. 50 to 75% of water.
In summary, ionic liquid cooling media generally are superior to water or thermo oils as cooling agents in terms of safety. However, if ionic liquids are heated above their thermal decomposition point, they still form flammable or non flammable gaseous products, which will lead to an increase or even hazardous increase of pressure in a closed cooling system. In the case of an accidental efflux by e.g. disruption of a pipe into e.g. a molten metal it will cause heavy sputtering or even minor explosions.
It is a task of the present invention to reduce or even overcome the formation of gaseous decomposition products in ionic liquid cooling media to prevent the drawbacks described above.
According to the present invention it was found unexpectedly, that cooling media comprising ionic liquids with 8,5 weight % of hydrogen or less, show much lower, or even practically no sputtering or explosive reaction behavior in contrast to ionic liquids (and other cooling media) with higher hydrogen content. The term “hydrogen” denotes hydrogen atoms bound to other atoms e.g. carbon atoms, being part of the ionic liquids anions or cations or being part of ionic or molecular byproducts or additives, but not gaseous hydrogen. The content of carbon atoms or other atoms forming volatile combustion products like sulfur, nitrogen, fluorine or chlorine seems to be of less importance as was found by experimental investigations.
In one aspect the present invention provides a cooling medium, e.g. for the application in high temperature environment, comprising an ionic liquid with a hydrogen content of 0% to 8.5%, such as 0% to 7% by weight, e.g. 0% to 6.5% by weight.
A cooling medium provided by the present invention is herein also designated as “cooling medium of (according to) the present invention”. A cooling medium comprising an ionic liquid may be a cooling medium consisting of an ionic liquid. An ionic liquid provided by the present invention as a cooling medium is herein also designated as “ionic liquid of (according to) the present invention”.
The term “ionic liquid” as used herein, e.g. in a process of the present invention, includes salts with melting temperatures of up to 250° C., e.g. ≦100° C. and >100° C., but ≦250° C.; preferably ≦100° C. and more preferably less than room temperature.
The term “ionic liquid” as used herein, further includes all liquid organic salts and mixtures of salts consisting of inorganic cations and organic anions or inorganic anions. Moreover additional salts with inorganic cation and organic or inorganic anion can be dissolved in the ionic liquid, containing but definitely not limited to the identical anion or identical anions as found in the basic ionic liquid. Moreover, additives may be dissolved in the ionic liquid, e.g. small amounts thereof, such as flame retardants.
In a further aspect the present invention provides a cooling medium according to the present invention, further comprising dissolved salts with inorganic cations and organic or inorganic anions, and/or dissolved flame retardants.
The chemical nature of cations and anions which form the ionic liquid in a cooling medium according to the present invention is less important. Appropriate cations and anions are such which form ionic liquids having a hydrogen content of not more than 8.5%, e.g. 0% to 8.5%.
In the following the term “moieties” denote alkyl, perfluorated alkyl, alkenyl, alkinyl, aryl, aralkyl or heteroaryl groups having 1 to 8 carbon atoms, such as C1-C4-alkyl, C2-C4-alkenyl, C2-C4-alkinyl, phenyl, benzyl or heteroaryl, preferably alkyl. For clarity reasons it should be mentioned that in this application the term C1-C4-alkyl or similar terms is an abbreviatory notation for C1-alkyl (methyl), C2-alkyl (ethyl), . . . , C4-alkyl (n-butyl, isobutyl, tert-butyl) or similar terms. In general branched chains are preferred, having found to be superior over linear chains.
In an ionic liquid according to the present invention preferably the cation is selected from imidazolium, benzimidazolium or phosphonium, optionally and preferably being substituted by C1 to C4 alkyl, e.g. including 1,3-dialkylimidazolium, 1,2,3-trialkylimidazolium, 1,3-dialkylbenzimidazolium, 1,2,3-trialkylbenzimidazolium, tetraalkylphosphonium cations, wherein preferably alkyl independently is C1 to C4 alkyl.
According to an exemplary embodiment of the present invention the cation is a quaternary ammonium, phosphonium, pyridinium, pyrrolium, piperidinium, pyrrolidinium, morpholinium, (benz)imidazolium or pyrazolium
According to another exemplary embodiment of the present invention the cation is a quaternary ammonium or a quaternary phosphonium cation. According to another exemplary embodiment of the method the cation comprises one to four moieties as described above.
According to another exemplary embodiment of the present invention the cation is one out of the group consisting of pyridinium, pyrrolium, e.g. wherein one moiety is bound to the nitrogen atom and/or one to three moieties are bound to carbon atoms of the carbon ring.
According to another exemplary embodiment of the present invention the cation is one out of the group consisting of piperidinium, pyrrolidinium and morpholinium, e.g. wherein one or two moieties are bound to the nitrogen atom and/or one to three of the one to four moieties are bound to carbon atoms of the carbon ring.
According to another exemplary embodiment of the present invention the cation is one out of the group consisting of (benz)imidazolium and pyrazolium, e.g. wherein a respective one of the one to four moieties is bound to each nitrogen atom and/or one to three of the one to four moieties are bound to carbon atoms of the carbon ring. For clarity reasons it should be noted that in case of more than one nitrogen atom a first moiety may be bound to a first nitrogen atom and a second moiety may be bound to a second nitrogen atom.
According to another exemplary embodiment of the present invention the cation is preferably one out of the group consisting of tetramethylammonium, tetraethylammonium, triethylmethylammonium, tetrabutylammonium, tributylmethylammonium, 1,3-dimethylimidazolium, 1,3-diethylimidazolium, 1-butyl-3-methylimidazolium, 1,2,3-trimethylimidazolium, 1-ethyl-3-methylimidazolium, 1-ethyl-2,3-dimethylimidazolium, and 1-butyl-2,3-dimethylimidazolium, 1-propyl-3-methylimidazolium, 1-propyl-2,3-dimethylimidazolium, 1,3-dimethylbenzimidazolium, 1-butyl-3-methylbenzimidazolium, 1,2,3-trimethylbenzimidazolium, 1-ethyl-3-methylbenzimidazolium, 1-ethyl-2,3-dimethylbenzimidazolium, and 1-butyl-2,3-dimethylbenzimidazolium, 1-propyl-3-methylbenzimidazolium, 1-propyl-2,3-dimethylbenzimidazolium.
According to another exemplary embodiment of the present invention the cation is preferably one out of the group of N-Butyl-N-Methylpyrrolidinium, N-Propyl-N-Methylpyrrolidinium, N-Ethyl-N-Methylpyrrolidinium, N,N-Dimethylpyrrolidinium, N-tert.Butyl-N-Methylpyrrolidinium, N-iso-Propyl-N-Methylpyrrolidinium, N-iso-Propyl-N-Ethylpyrrolidinium, N,N-Di-iso-Propylpyrrolidinium, N-tert.Butyl-N-Ethylpyrrolidinium, N-Butyl-N-Methylmorpholinium, N-Propyl-N-Methylmorpholinium, N-Ethyl-N-Methylmorpholinium, N,N-Dimethylmorpholinium, N-tert.Butyl-N-Methylmorpholinium, N-iso-Propyl-N-Methylmorpholinium, N-iso-Propyl-N-Ethylmorpholinium, N,N-Di-iso-Propylmorpholinium, N-tert.Butyl-N-Ethylmorpholinium, N-Butyl-N-Methylpiperidinium, N-Propyl-N-Methylpiperidinium, N-Ethyl-N-Methylpiperidinium, N,N-Dimethylpiperidinium, N-tert.Butyl-N-Methylpiperidinium, N-iso-Propyl-N-Methylpiperidinium, N-iso-Propyl-N-Ethylpiperidinium, N,N- Di-iso-Propylpiperidinium, N-tert.Butyl-N-Ethylpiperidinium, Trimethyl-iso-Propylammonium, Dimethyl-di-iso-Propylammonium, Methyl-tri-iso-Propylammonium, Trimethyl-tert.-Butylammonium, Dimethyl-di-tert.-Butylammonium, Methyl-tri-tert.-Butylammonium, Trimethyl-iso-Propylphosphonium, Dimethyl-di-iso-Propylphosphonium, Methyl-tri-iso-Propylphosphonium, Trimethyl-tert.-Butylphosphonium, Dimethyl-di-tert.-Butylphosphonium, Methyl-tri-tert.-Butylphosphonium.
In another aspect the present invention provides a cooling medium according to the present invention, wherein the cation of the ionic liquid is selected from imidazolium, e.g. C1-C6 alky-imidazolium, such as 1-ethyl- or 1-buylimidazolium, wherein the imidzalolyl ring optionally is substituted by alkyl, e.g. C1-C4 alkyl, such as methyl.
In another aspect the present invention provides a cooling medium according to the present invention, wherein the cation of the ionic liquid is selected from imidazolium, benzimidazolium or phosphonium, optionally independently substituted by C1 to C4 alkyl, perfluoro C1 to C4 alkyl and/or by cyano, e.g. one or more cyano groups.
Anions in a ionic liquid according to the present invention include anions common in ionic liquid chemistry. Preferably the chemical formula of the anion contains 3 or less hydrogen atoms, more preferably the anions are completely hydrogen free. Preferably the anions comprise hetero elements, such as halogen, O, N, S, Si, B, P, a metallic element, such as Fe, Sb, Sn, Cu, Mo, Al, Zn, Co, Ni, Mn, W, V or Ti; these hetero elements may form (but are not limited to) complex anions with each other, e.g. the metallic elements listed above with halogen, SCN⁻, CN⁻, N(CN)₂ ⁻ or O-containing ligands, or any other hydrogen-free ligand.
Appropriate anions include e.g. fluoride; chloride; bromide; thiocyanate; dicyanamide; hexafluorophosphate; sulfate; phosphate; hydrogen phosphate; dihydrogen phosphate; phosphonate HPO₃ ²⁻, hydrogen phosphonate H₂PO₃ ⁻; sulfamate H₂N—SO₃ ⁻, methanesulfonate, dimethylphosphate, dimethylphosphonate, diethylphosphate, diethylphosphonate, tetrafluoroborate, trifluormethanesulfonate, trifluoracetate, bis(trifluormethylsulfonyl)imide, tris(trifluormethylsulfonyl)methide, fluorous alkyl phosphate, e.g. tris(pentafluorethyl)trifluorophosphate, methylsulfate, ethylsulfate, tetracyanoborate, carboranes, alkyl-spiroborates e.g. bis(oxalato)borate or bis(malonato)borate, tetra-substituted borate, e.g. of formula
[BRⁱR^jR^kR^l]⁻ Va,
wherein Rⁱto R^l, independently of each other, are fluorine or an organic, inorganic, aliphatic or perfluorinated aliphatic, aromatic, heteroaromatic or perfluorinated aromatic or heteroaromatic residues, e.g. aliphatic residues comprising 1 to 4, aromatic or heteroaromatic residues comprising 5 to 10 carbon atoms, optionally comprising one or more heteroatoms and/or optionally substituted by one or more hydrogen-free functional groups or halogen; organic sulfonate, e.g. of formula
[R^m—SO₃]⁻ Vb,
wherein R^mis an organic, inorganic, aliphatic or perfluorinated aliphatic, aromatic, heteroaromatic or perfluorinated aromatic or heteroaromatic residue, e.g. aliphatic residues comprising 1 to 4, aromatic or heteroaromatic residues comprising 5 to 10 carbon atoms, optionally comprising one or more heteroatoms and/or optionally substituted by one or more hydrogen-free functional groups or halogen; organic sulfate, e.g. of formula
[R^m—OSO₃]⁻ Vc,
wherein R^mis an organic, inorganic, aliphatic or perfluorinated aliphatic, aromatic, heteroaromatic or perfluorinated aromatic or heteroaromatic residue, e.g. aliphatic residues comprising 1 to 4, aromatic or heteroaromatic residues comprising 5 to 10 carbon atoms, optionally comprising one or more heteroatoms and/or optionally substituted by one or more hydrogen-free functional groups or halogen; carboxylate, e.g. of formula
[Rⁿ—COOO]⁻ Vd,
wherein Rⁿis an organic, inorganic, aliphatic or perfluorinated aliphatic, aromatic, heteroaromatic or perfluorinated aromatic or heteroaromatic residue, e.g. aliphatic residues comprising 1 to 4, aromatic or heteroaromatic residues comprising 5 to 10 carbon atoms, which optionally comprises one or more heteroatoms and/or optionally substituted by one or more hydrogen-free functional groups or halogen; (fluoroalkyl)fluorophosphate e.g. of formula
[PF_x(C_yF_2y+1−zH_z)_6−x]⁻ Ve,
wherein 1≦x≦6, 1≦y≦8 and 0≦z≦2y+1;
imide of formulae
[R^o—SO₂—N—SO₂—R^p]⁻ Vf,
[R^r—SO₂—N—CO—R^s]⁻ Vg, or
[R^t—CO—N—CO—R^u]⁻ Vh,
wherein R^oto R^uindependently of each other are fluorine or an organic, inorganic, aliphatic or perfluorinated aliphatic, aromatic, heteroaromatic or perfluorinated aromatic or heteroaromatic residue , e.g. aliphatic residues comprising 1 to 4, aromatic or heteroaromatic residues comprising 5 to 10 carbon atoms, which optionally comprises one or more heteroatoms and/or optionally is substituted by one or more hydrogen-free functional groups or halogen;
organic phosphate of formula
[R^m—OPO₃]²⁻ (Vj)
or
[R^m—OPO₂—ORⁿ]⁻ Vi,
wherein R^mis an organic, inorganic, aliphatic or perfluorinated aliphatic, aromatic, heteroaromatic or perfluorinated aromatic or heteroaromatic residue, e.g. aliphatic residues comprising 1 to 4, aromatic or heteroaromatic residues comprising 5 to 10 carbon atoms, which optionally comprises one or more heteroatoms and/or which optionally is substituted by one or more hydrogen-free functional groups or halogen; and wherein Rⁿis hydrogen or an organic, inorganic, aliphatic or perfluorinated aliphatic, aromatic, heteroaromatic or perfluorinated aromatic or heteroaromatic residue, e.g. aliphatic residues comprising 1 to 4, aromatic or heteroaromatic residues comprising 5 to 10 carbon atoms, which optionally comprises one or more heteroatoms and/or optionally substituted by one or more hydrogen free functional groups or halogen; organic phosphonate of formula
[R^m—PO₃]²⁻ Vk, or
[R^m—PO₃—Rⁿ]⁻ Vl,
wherein R^mis an organic, inorganic, aliphatic or perfluorinated aliphatic, aromatic, heteroaromatic or perfluorinated aromatic or heteroaromatic residue, e.g. aliphatic residues comprising 1 to 4, aromatic or heteroaromatic residues comprising 5 to 10 carbon atoms, which optionally comprises one or more heteroatoms and/or optionally is substituted by one or more hydrogen free functional groups or halogen;
and wherein IV is hydrogen or an organic, inorganic, aliphatic or perfluorinated aliphatic, aromatic, heteroaromatic or perfluorinated aromatic or heteroaromatic residue, e.g. aliphatic residues comprising 1 to 4, aromatic or heteroaromatic residues comprising 5 to 10 carbon atoms, which optionally comprises one or more heteroatoms and/or optionally substituted by one or more hydrogen-free functional groups or halogen.
In a preferred embodiment of the present invention an anion includes sulfates, phosphates, sulfonates. borates, halides, e.g. fluorides such as SiF6, tetrafluoroborates, or chlorides, e.g. tetrachloroferrat-(III), which anions optionally are alkylated, e.g. by C1-C8 alkyl, including halogenated C1-C8 alkyl, such as trifluoromethyl, or arylated, e.g. by phenyl groups, e.g. including C1-C4 alkylsulfates, such as methylsulfate, ethylsulfate, C1-C6 dialkylphosphates, such as diethylphosphate, C1-C4 alkylsulfonates wherein alkyl optionally is halogenated, e.g. fluorinated, such as methansulfonate, trifluoromethansulfonate, SiF₆ ²⁻, halogenated, e.g. fluorinated borates, e.g. tetrafluoroborate, arylated phosphates, e.g. triphenylphosphate, ferrates, such as tetrachloroferrate-(III); e.g. diethylphosphate, triphenylphosphate, methansulfonate, trifluormethansulfonate, methylsulfate, ethylsulfate, SiF₆ ²⁻, tetrachloroferrat-(III) and/or tetrafluoroborate.
Ionic liquids according to the present invention may be prepared as appropriate, e.g. according, e.g. analogously to a known method, e.g. as described in prior art. Processes for the preparation of ionic liquids are known e.g. from Was serscheid, Peter; Welton, Tom (Eds.); “Ionic Liquids in Synthesis”, Wiley-VCH 2008; ISBN 978-3-527-31239-9; Rogers, Robin D.; Seddon, Kenneth R. (Eds.); “Ionic Liquids—Industrial Applications to Green Chemistry”, ACS Symposium Series 818, 2002; ISBN 0841237891 and numberous references cited therein.
It was found that ionic liquids according to the present invention have a high flash point. In another aspect the present invention provides a cooling medium according of the present invention wherein the ionic liquid has a flash point of at least 200° C., such as 250° C., determined according to DIN ISO 2592.
Preferably, a ionic liquid according to the present invention has a low melting point, e.g. from −20° C. and below to 40° C.
In another aspect the present invention provides a cooling medium according to the present invention, wherein the ionic liquid has a melting point from 40° C. and below, such as 20° C. and below, e.g. 0° C. and below, such as −20° C. and below.
A cooling medium of the present invention comprising ionic liquids with low hydrogen content is particularly useful in terms of safe use because of low reactivity, low flame volume and low explosiviness in a high temperature environment, especially when getting in contact with high temperature melts or surfaces.
A cooling medium of the present invention is particularly useful for the following applications:

- Cooling of technical devices in high temperature environments (500° C.-2000° C.) as a replacement of water or water-based cooling fluids or as a replacement of cooling fluids based on organic liquids—so called thermo oils—e.g. paraffins and naphthens, mineral oils, alkyl-benzenes, benzyl- and dibenzyltoluenes, biphenyls, diphenylethers, terphenyls, partially hydrogenated terphenyls, quaterphenyles, triarylethers, alkylnaphthalines, polyalkylenglykoles, high boiling esters, silicon oils, in order to prevent the formation of explosive decomposition reactions with destructive or even devastating consequences in the case of technical failures, human error, natural disasters and accidents.
- In particular cooling of metallurgical ovens and their aggregates; cooling of metallurgical equipment in general in production and processing of metals, metal alloys and intermetalic compounds, handling of ashes and slags, including production and processing of silicon, refractory metals and intermetalic compounds with boron, carbon, nitrogen and silicon. Fused-salt electrolysis for the production of e.g. aluminum or sodium.
- Cooling of ovens and aggregates in the glas and ceramic producing industry
- Cooling of ovens and aggregates in the cement producing industry
- Cooling of reactors and aggregates in gasification of organic matter and biofeedstocks.
- Cooling of ovens and aggregates in incineration plants, including waste gas incineration e.g. by afterburners and cooling of ashes and slags
- Cooling of reactors and aggregates in nuclear power plants
- Cooling of combustion chambers and aggregates in conventional thermal power plants.

In another aspect the present invention provides the use of a cooling medium according to the present invention for the cooling of

- technical devices in high temperature environment,
- metallurgical ovens and their aggregates,
- ovens and aggregates in the glas and ceramic producing industry,
- ovens and aggregates in the cement producing industry,
- cooling of reactors and aggregates in gasification of organic matter and biofeedstocks,
- ovens and aggregates in incineration plants,
- reactors and aggregates in nuclear power plants,
- combustion chambers and aggregates in conventional thermal power plants.

EXAMPLE 1

5 kg of molten copper was kept in a small metallurgical oven at constant temperature at 1200° C. All professional precautions known to an expert in the field of metallurgy where taken into account, e.g. fume hood, fireproof safety clothing and helmet, fireproof curtains etc. The ionic liquid test fluids where pumped with a constant flow of 1 ml/s through a ¼″ stainless steel capillary right into the copper melt. The steel capillaries outlet was immersed into the molten copper directly above the bottom of the crucible which is the worst position in terms of possible explosive reactions. The experiments were filmed and observed by a team of metallurgical experts. Their visual and acoustic attention was focused especially on sputtering of the copper melt, explosive reactivity and flame volume. These parameters where rated by the following numbers:
Reactivity: 0-5
0=no observable sputtering, gas evolution or explosive evaporation
5=very heavy sputtering, gas evolution or explosive evaporation
Flame Volume: 0-5
0=no observable flames
5=very large flame volume
Benchmark: Mineral oil “Castrol HDX”, see table
Results:
In the following Table 1 composition of ionic liquids, their sum formulae, the calculated content in weight % of carbon atoms “C”, hydrogen atoms “H” and other atoms “Z” which may form gaseous combustion products, the T-Onset temperature for the decomposition in air measured by a thermo balance (according to DIN 51007), the flashpoint (according to DIN ISO 2592) and the ratings for the reactivity (RA) and the flame volume (FV). The individual weight %s listed are based on the total mol weight of the composition. Z=other atoms forming gaseous combustion products, e.g. N, S, F, Cl , but except O. EMIM is 1-Ethyl-3-methylimidazolium and BMIM is 1-Butyl-3-methylimidazolium.

TABLE 1

		C	H	Z	T-	Flash
Composition	Sum formula	[% w]	[% w]	[% w]	Onset	point	RA	FV

Mineral oil	—	—	—	—	—	—	5	5
“Castrol HDX”
BMIM-octylsulfate	C16H32N2O4S	55.14	9.26	17.24	224° C.	288° C.	3.5	3.5
EMIM-diethylphosphate	C10H21N2O4P	45.45	8.01	10.60	264° C.	222° C.	3	2
EMIM-methansulfonate/BMIM-	C7H14N2O3S	41.97	7.05	26.57	—	—	2	1.5
methylsulfate 50:50	C9H18N2O4SC
EMIM-methansulfonate	C7H14N2O3S	40.76	6.84	29.13	339° C.	290° C.	2	2
EMIM-methansulfonate/EMIM₂-	C7H14N2O3S	40.64	6.77	30.88	—	—	2	2
SiF₆90:10	C12H22F6N4Si
EMIM-methansulfonate/BMIM-	C7H14N2O3S	41.64	6.77	37.83	—	—	1.5	2
tetrafluoroborate	C8H15BF4N2
50:50
EMIM-ethylsulfate/EMIM₂-	C8H16N2O4S	40.55	6.76	27.55	308° C.	272° C.	2	2
SiF₆90:10	C12H22F6N4Si
EMIM-methansulfonate/Triphenylphosphate	C7H14N2O3S	43.31	6.62	26.22	—	—	1.5	2
90:10	C18H15O4P
EMIM-methansulfonate/Fe-	C7H14N2O3S	38.04	6.29	30.83	—	—	1.5	2
trifluormethansulfonate	C2F6FeO6S2
92:8
EMIM-methansulfonate/EMIM-	C7H14N2O3S	38.58	6.22	40.84	—	—	1.5	2
tetrafluoroborate	C6H11BF4N2
50:50
EMIM-	C6H11BF4N2	36.40	5.60	52.54	—	—	1	2
Tetrafluoroborate
EMIM-	C7H11F3N2O3S	32.31	4.26	44.98	405° C.	344° C.	1	2
Trifluormethansulfonate
EMIM-	C6H11Cl4FeN2	23.34	3.59	54.99	390° C.	—	1	1
tetrachloroferrat-(III)

The results in Table 1 above show the results for a number of ionic liquids, which were chosen due to their quite high thermal decomposition points/flashpoints and low melting points (all are liquid at room temperature except EMIM-methansulfonateand Bmim-octylsulfate with a melting points of 34-35° C.). From Table 1 it is evident, that the reactivity RA and the flame volume FV decreases with decreasing hydrogen content, even if the content of other atoms forming gaseous combustion products increases. Moreover it can be seen that a hydrogen content of 9.26% shows a sharp distinction regarding RA and FV with compound of the present invention wherein the hydrogen content is below 8.5%. E.g. reactivity RA decreases from 3.5 of the compound with a hydrogen content from more than 8.5% (9.26%) at least to 3 (decrease of ca. 14%) down to 1 (decrease of ca. 71%) of ionic liquids of the present invention. Similarly the flame volume decreases from 3.5 of the compound with a hydrogen content from more than 8.5% (9.26%) to at least to 2 (decrease of ca. 43%) down to 1 (decrease of ca. 71%) of the ionic liquids of the present invention.
In the list below prior art regarding Ionic Liquids is listed:

- Bai, Liguang; Zhu, Jiqin; Chen, Biaohua; Li, Chengyue; Fei, Weiyang; Huagong Xuebao (Chinese Edition) (2010), 61(12), 3037-3043.
- Zhang, M. M.; Reddy, R. G.; Transactions of the Institutions of Mining and Metallurgy, Section C: Mineral Processing and Extractive Metallurgy (2010), 119(2), 71-76.
- Nieto de Castro, Carlos A.; Langa, Elisa; Morais, Ana L.; Lopes, Manuel L. Matos; Lourenco, Maria J. V.; Santos, Fernando J. V.; Santos, M. Soledade C. S.; Lopes, Jose N. Canongia; Veiga, Helena I. M.; Macatrao, Mafalda; et al; Fluid Phase Equilibria (2010), 294(1-2), 157-179.
- Szarvas, Laszlo; Gerhard, Dirk; Oehlenschlaeger, Steffen; Alemany, Aurelie; Ger. Offen. (2010), DE 102009051087 Al 20100506
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Claims

1. Cooling medium comprising an ionic liquid with a hydrogen content of 0% to 8.5% by weight.

2. Cooling medium according to claim 1 with a hydrogen content of 0% to 7% by weight.

3. Cooling medium according to claim 1, with a hydrogen content of 0% to 6.5% by weight.

4. Cooling medium according to claim 1, wherein the ionic liquid has a flash point of at least 200° C. determined according to DIN ISO 2592.

5. Cooling medium according to claim 4, wherein the ionic liquid has a flash point of at least 250° C. determined according to DIN ISO 2592.

6. Cooling medium according to claim 1, wherein the ionic liquid has a melting point from 40° C. and less.

7. Cooling medium according to claim 6, wherein the ionic liquid has a melting point from −20° C. and below.

8. Cooling medium according to claim 1, wherein the cation of the ionic liquid is selected from ammonium, phosphonium, pyridinium, pyrrolium, piperidinium, pyrrolidinium, morpholinium, (benz)imidazolium or pyrazolium.

9. Cooling medium according to claim 8, wherein the cation of the ionic liquid is selected from imidazolium, benzimidazolium or phosphonium, optionally independently substituted by C1 to C4 alkyl, perfluoro C1 to C4 alkyl and/or by cyano.

10. Cooling medium according to claim 1, wherein the anion of the ionic liquid comprises a hetero element.

11. Cooling medium according to claim 1, wherein the anion of the ionic liquid contains 3 hydrogen atoms or less, in particular is hydrogen free.

12. Cooling medium according to claim 10, wherein the anion of the ionic liquid is selected from diethylphosphate, triphenylphosphate, methansulfonate, trifluormethansulfonate, methylsulfate, ethylsulfate, SiF₆ ²⁻, tetrachloroferrat-(III) and/or tetrafluoroborate.

13. Cooling medium according to claim 1, further comprising dissolved salts with inorganic cations and organic or inorganic anions.

14. Cooling medium according to claim 1, further comprising dissolved flame retardants

15. A method of using a cooling medium according to claim 1, comprising using the cooling medium to cool at least one member selected from the group comprising:

technical devices in high temperature environment,

metallurgical ovens and their aggregates,

ovens and aggregates in the glas and ceramic producing industry,

ovens and aggregates in the cement producing industry,

cooling of reactors and aggregates in gasification of organic matter and biofeedstocks,

ovens and aggregates in incineration plants,

reactors and aggregates in nuclear power plants,

combustion chambers and aggregates in conventional thermal power plants.