The present invention refers to a composition to dissolve biomass. More particularly, refers to a composition of ionic liquids and a method to dissolve biomass, in particular cellulose, its manufacturing process and method of use for inter alia sheets or films production.
Cellulose is the most abundant biopolymer in Nature, and a popular feedstock for the production of chemicals and materials of a biorenewable origin. Processes to obtain these products often require the dissolution and regeneration of cellulose. Cellulose is difficult to dissolve due to the strong network of hydrogen bonds between and within its polymeric chains, which prohibits solvation by conventional solvents. Since traditional solvents are not suited well for cellulose dissolution, more efficient dissolution procedures are required (Heinze, T; Koschella, A. “Solvents applied in the field of cellulose chemistry—a mini review”, Polimeros: Ciencia e Tecnologia, vol. 15, no 2, p. 84-90. 2005); and thus, the dissolution and regeneration of cellulose from ionic liquids is attracting considerable attention.
Ionic liquids are salts with a relatively low melting temperature (typically a maximum mark of 100° C. is considered in their definition). Many ionic liquids are liquid at room temperature and well below, whereas others remain in a solid state even up to several dozens of degrees centigrade above room temperature. In general, ionic liquids present a set of properties that make them attractive for their use as fluids in different processes and applications; an example can be their wide liquid range (including typical operation temperature ranges) in combination with a practically negligible vapour pressure, since they are constituted of ions.
The patent application WO 2003029329 A2 discloses that some ionic liquids are able to dissolve cellulose. However, the dissolution process has to be carried out, inevitably, at a temperature above the melting point of the ionic liquid. Temperatures between 70 and 100° C. are necessary to dissolve up to 7 wt % of cellulose with respect to the weight of the ionic liquid. Only in one case, when the mixture was heated under microwave conditions, the solution of cellulose was up to 20 wt %. However these conditions are not appropriate for industrial application since the process can easily lead to degradation of the ionic liquids and cellulose, or even explosions of sealed systems (Chem. Soc. Rev., 2012, 41, 1519-1537).
The patent application WO 2011056924 A2 discloses statistical mixtures of ionic liquids to dissolve cellulose. These statistical mixtures are mixtures comprising different cations and/or anions, which are prepared by a process comprising the reaction of mixtures of ionic liquid precursors in one-pot. Those mixtures can dissolve up to 35 wt % of cellulose when the mixture is heated at 100° C. under microwave conditions, again conditions which are not safe neither scalable for industrial process.
Thus, new compositions to dissolve cellulose in higher amounts and under milder and scalable conditions are still required.
The authors of the present invention have found a mixture of ionic liquids that is able to dissolve biomass, specifically cellulose. That mixture dissolves cellulose more effectively than other known compositions. Furthermore, the method of the invention, which employs this mixture, is carried out under mild conditions. Besides, the method avoids microwaves and other dangerous steps. Even more, the method of the invention is scalable.
The mixture of the invention preserves some of the intrinsic ionic liquid features, such as negligible vapour pressure. It is preferred that the mixture of the invention has a eutectic behaviour.
Thus, the authors of the present invention have found that some ionic liquids can be combined to yield eutectic systems, and these ionic liquid mixtures can be used to dissolve cellulose at temperatures below the melting temperatures of the pure ionic liquids; i.e., at temperatures at which it would not be possible to carry out the dissolution of cellulose in the pure ionic liquids. Preferred ionic liquids in the mixture are imidazolium ionic liquids having chloride or acetate as anions.
Thus, an aspect of the invention refers to a composition comprising a mixture of two or more imidazolium ionic liquids and between 0.1 and 50% wt of biomass, where the mixed ionic liquids configure a eutectic system and their anions are selected from chloride and acetate.
A particular embodiment refers to the composition disclosed above, wherein the imidazolium ionic liquids are 1-(C2-C6)alkyl-3-(C2-C6)alkyl-imidazolium.
A particular embodiment refers to the composition disclosed above, wherein the ionic liquids are selected from 1-ethyl-3-methylimidazolium chloride, 1-ethyl-3-methylimidazolium acetate and 1-butyl-3-methylimidazolium chloride.
Other particular embodiment refers to the composition disclosed above, wherein two of those ionic liquids are in a relation between 1:10 to 10:1; preferably wherein two of those ionic liquids are in a relation between 1:5 to 5:1; more preferably wherein two of those ionic liquids are in a relation between 1:3 to 3:1.
Other particular embodiment refers to the composition disclosed above, comprising 1-ethyl-3-methylimidazolium chloride and at least one more ionic liquid selected from 1-ethyl-3-methylimidazolium acetate and 1-butyl-3-methylimidazolium chloride in a relation between 1:5 to 5:1.
Other particular embodiment refers to the composition disclosed above, comprising 1-ethyl-3-methylimidazolium chloride and at least one more ionic liquid selected from 1-ethyl-3-methylimidazolium acetate and 1-butyl-3-methylimidazolium chloride in a relation between 1:3 to 3:1.
Other particular embodiment refers to the composition disclosed above, selected from:
Other particular embodiment refers to the composition disclosed above, wherein the biomass is cellulose.
Other particular embodiment refers to the composition disclosed above, further comprising a viscosity-reducing agent, preferably dimethyl sulfoxide, in an amount from 0.1 to 70% wt.
Other particular embodiment refers to the composition disclosed above, wherein the biomass is between 0.1 and 40% wt.
In a preferred embodiment, the composition of the invention is a liquid composition.
In a preferred embodiment, the mixture of ionic liquids displays a eutectic behaviour. In a particular embodiment, the mixture of ionic liquids is a mixture of eutectic composition.
When the mixture of ionic liquids described in the present invention is used to dissolve cellulose, the yield of the dissolution process can be up to 10 times the yield obtained when one of those ionic liquids is used alone.
The best yield for cellulose dissolution is obtained when the composition comprises 1-ethyl-3-methylimidazolium chloride and 1-ethyl-3-methylimidazolium acetate in a 3:7 molar ratio.
A more preferred embodiment of the invention refers to the composition of the invention comprising 1-ethyl-3-methylimidazolium chloride and 1-ethyl-3-methylimidazolium acetate in a 3:7 molar ratio.
Other aspect of the invention refers to a method of obtaining the composition as disclosed above, comprising:
a) mixing biomass in an amount of from 0.1 to 50 wt % with a mixture of two or more imidazolium ionic liquids, wherein the ionic liquids mixed configure a eutectic system and their anions are selected from chloride and acetate, and
b) heating the mixture obtained in step (a) at a temperature below 105° C.
A preferred embodiment refers to the method of the invention as previously described, wherein the imidazolium ionic liquids are 1-(C2-C6)alkyl-3-(C2-C6)alkyl-imidazolium. More preferably, the imidazolium ionic liquids are selected from 1-ethyl-3-methylimidazolium chloride, 1-ethyl-3-methylimidazolium acetate, and 1-butyl-3-methylimidazolium chloride. Preferably, two of those ionic liquids are in a relation between 1:10 to 10:1; more preferably two of those ionic liquids are in a relation between 1:5 to 5:1; even more preferably, they are in a relation between 1:3 to 3:1.
Another preferred embodiment refers to the method of the invention as previously described, wherein the imidazolium ionic liquids comprise 1-ethyl-3-methylimidazolium chloride and at least one more ionic liquid selected from 1-ethyl-3-methylimidazolium acetate and 1-butyl-3-methylimidazolium chloride in a relation between 1:5 to 5:1, preferably in a relation between 1:3 to 3:1.
A preferred embodiment refers to the method of the invention as previously described, wherein the mixture of imidazolium ionic liquids is selected from
The mixture of ionic liquids disclosed in the present invention is so effective pretreating or dissolving biomass, in particular cellulose, that the method of the invention can be performed in mild conditions. Thus, in a particular embodiment, the temperature of the step (b) is between 50° C. and 105° C. In a more preferred embodiment, the temperature of the step (b) is between 70° C. and 100° C.
A more preferred embodiment refers to the method of the invention, comprising:
a) mixing the biomass with 1-ethyl-3-methylimidazolium chloride and 1-ethyl-3-methylimidazolium acetate in a 3:7 molar ratio, and
b) heating the mixture obtained in step (a) at a temperature below 80° C., preferably at a temperature between 60° C. and 80° C., more preferably at 70° C.
Optionally, a viscosity-reducing agent can be further added to step (a), as for example dimethylsulfoxide, in an amount from 0.1 to 70 wt %.
In a preferred embodiment of the invention the biomass is cellulose.
In another aspect, the invention refers to a composition obtainable by the method described above.
In another aspect, the invention refers to the use of the composition of the invention as previously disclosed to prepare cellulosic fibers, beads, sheets and other elements.
In another aspect, the invention refers to the use of the composition of the invention as previously disclosed to act as non-derivatising solvent for the chemical modification of cellulose in solution.
By using the presented invention the following effects and technical usage have been achieved:
Legend -Δ- melting point of the excess component [C4mim]Cl in the mixture; -□- melting point of the excess component [C2mim]Cl in the mixture; -▴- eutectic mixture thermal transition; -X- glass transition observed below the eutectic point transition.
Next, for a greater understanding of the characteristics and advantages of the present invention, reference is made to a number of explanatory examples which complete the previous description, without the invention being limited in any way to them.
The ionic liquids 1-ethyl-3-methylimidazolium chloride, 1-ethyl-3-methylimidazolium acetate, and 1-butyl-3-methylimidazolium chloride were purchased from commercial vendors with a quoted purity>95% for 1-ethyl-3-methylimidazolium acetate, and >98% for 1-ethyl-3-methylimidazolium chloride and 1-butyl-3-methylimidazolium chloride. All salts were dried under vacuum for 72 h at 90° C., achieving a final water content<0.9% determined by Karl Fischer titration using a Metrohm 831 KF coulometer.
Microcrystalline cellulose (Cellulose no. 435236) was purchased from a commercial vendor, and used as received.
Several mixtures of the ionic liquid 1-ethyl-3-methylimidazolium chloride ([C2mim]Cl), with a melting point of 88° C., and the ionic liquid 1-butyl-3-methylimidazolium chloride ([C4mim]Cl), with a melting point of 65° C., were prepared by dissolving each ionic liquid separately in methanol, combining both methanol solutions in the desired proportion, and evaporating completely the methanol. Mixtures were prepared so that their compositions ranged from pure [C2mim]Cl to pure [C4mim]Cl, evenly distributed over the entire composition range at intervals of 5 mol %. A sample of each mixture was subjected to analysis by differential scanning calorimetry (DSC). By plotting the signals of the corresponding thermograms in a temperature-composition phase diagram, the existence of a eutectic behaviour could be corroborated. By extrapolation of the trend of the signals of the excess components in such diagram (
The ionic liquid 1-ethyl-3-methylimidazolium chloride ([C2mim]Cl) has a melting temperature of 88° C., and therefore it is a solid at room temperature (for instance 22° C.). The ionic liquid 1-ethyl-3-methylimidazolium acetate ([C2mim][OAc]) is a liquid at room temperature and also at much lower temperatures, with no melting temperature above −73° C. These two ionic liquids were mixed in a vial in a 3:7 molar ratio (previously determined as the eutectic composition for this system), and the mixture was heated and stirred for 10 minutes at 100° C. A homogeneous liquid was obtained, which remained stable in that condition when cooled down to room temperature. No melting temperature could be detected by DSC for the obtained mixture above −73° C.
5 g of a 3:7 molar ratio mixture of [C2mim]Cl and [C2mim][OAc] was placed in a jacketed glass vessel equipped with an overhead mechanical stirrer. The mixture was heated to 75° C., and 0.5 g of microcrystalline cellulose was added. The content of the thermostated vessel was stirred until complete dissolution of the cellulose (visually clear solution). 0.25 g was subsequently added, and then the content was newly stirred until complete dissolution of the cellulose. This action was repeated several times. After addition of a total amount of 1.50 g of cellulose (corresponding to 30 g of cellulose per 100 g of ionic liquid mixture), a clear solution was still obtained. No further additions of cellulose were made, because at this point the solution had turned excessively viscous.
5 g of a 3:7 molar ratio mixture of [C2mim]Cl and [C2mim][OAc] was placed in a jacketed glass vessel equipped with an overhead mechanical stirrer. The mixture was heated to 100° C., and 0.5 g of microcrystalline cellulose was added. The content of the thermostated vessel was stirred until complete dissolution of the cellulose (visually clear solution). 0.25 g was subsequently added, and then the content was newly stirred until complete dissolution of the cellulose. This action was repeated several times. After addition of a total amount of 2.00 g of cellulose (corresponding to 40 g of cellulose per 100 g of ionic liquid mixture), a clear solution was still obtained.
5 g of a mixture of the ionic liquid [C2mim]Cl and [C4mim]Cl at a molar ratio 49:51 (eutectic composition) was prepared and placed in a jacketed glass vessel equipped with a mechanical stirrer, and was heated to 50° C., which is below the melting point of both [C2mim]Cl and [C4mim]Cl. Microcrystalline cellulose (0.5 g) was added. The solution (with a concentration of 10 g of cellulose per 100 g of ionic liquid mixture) was stirred mechanically until the complete dissolution of the cellulose, obtaining an optically clear and viscous solution.
4.25 g of a 3:7 molar ratio mixture of [C2mim]Cl and [C2mim][OAc] and 0.75 g DMSO was placed in a jacketed glass vessel equipped with an overhead mechanical stirrer. The mixture was heated to 75° C., and 0.5 g of microcrystalline cellulose was added. The content of the thermostated vessel was stirred until complete dissolution of the cellulose (visually clear solution). 0.25 g of microcrystalline cellulose was subsequently added, and then the content was stirred again until complete dissolution of the cellulose. Further additions of microcrystalline cellulose and subsequent dissolution were carried out. After addition of a total amount of 1.75 g of cellulose (corresponding to 35 g of cellulose per 100 g of ionic liquid mixture), a clear solution was still obtained. No further additions of cellulose were made, because at this point the solution turned into gel.
A mixture of imidazolium salts: 1-ethyl-3-methylimidazolium chloride [C2mim]Cl in a molar ratio of from 1:5 to 5:1 with a mixture of 1-ethyl-3-methylimidazolium acetate [C2mim][OAc] and 1-butyl-3-methylimidazolium chloride [C4mim]Cl in any molar ratio, prepared in an analogous manner as in Example 1, was placed in a jacketed glass vessel equipped with an overhead mechanical stirrer. The mixture was heated to 75° C., and microcrystalline cellulose in an amount greater than 30 g of cellulose to 100 g of the used mixture of imidazolium salts was added. During the addition of cellulose, the content of the reactor was thermostated and stirred until the complete dissolution of the cellulose, obtaining an optically clear and viscous solution.
As an example of ionic liquid eutectic mixture not able to dissolve cellulose, the eutectic mixture of 1-ethyl-3-methylimidazolium nitrate ([C2mim][NO3]) and 1-ethyl-3-methylimidazolium hexafluorophosphate ([C2mim][PF6] was used. The ionic liquids were mixed in a 60:40 molar ratio to form a eutectic mixture (with a melting point of 19° C.). 5 g of the prepared mixture was placed in a jacketed glass vessel equipped with a mechanical stirrer, and was heated to 75° C. Microcrystalline cellulose (0.5 g) was added, and the content of the vessel mechanically stirred. After 48 h at those conditions, cellulose remained suspended in the ionic liquid mixture, forming a cloudy paste, with no signs of dissolution.
The composite prepared according to Example 5, is reprocessed in a known manner, to obtain film or foil. It yields the product with properties comparable to the products obtained using currently known methods.
Number | Date | Country | Kind |
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P 201630898 | Jul 2016 | ES | national |
Filing Document | Filing Date | Country | Kind |
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PCT/ES2017/070470 | 6/29/2017 | WO | 00 |