Patent Application
20110057156
The present invention relates to the field of exfoliated and delaminated layered inorganic materials and the use of these materials.
The group of materials termed chalcogenides is characterized as being minerals with a predominantly two-dimensional structure i.e. materials with strong bindings in the individual layer and with weak Van der Waals forces between the layers. The minerals therefore appear as strongly layered. Under pressure shearing of the layers may as a consequence occur. This is the main argument for use of molybdenum sulphide as a lubricant since the layers slide easily. For these reasons it has been used by NASA in low friction materials for space applications.
For many years it has been attempted to find methods whereby the layers may be separated creating a very large specific surface. This goal has successfully been achieved in the processing of clay minerals. These are typically phyllosilicates frequently with strongly hydrophilic properties due to the ionic charges in the layers. The exfoliation of clay may be performed using pressurized water and surfactants. The earliest examples are related to montmorillonite. Süd Chemie has produced this material in large quantities and it has successfully been incorporated in polymer materials used in the automotive industry. It has been found that the addition of some % of exfoliated clay result in better mechanical properties of the polymer, it increases the barrier properties towards gas diffusion and it retards fire. Notably the exfoliated clays have been incapable of performing well in non-polar polymer materials. This has initiated initiatives that circumvent this problem. One of theses has been to introduce new copolymers where one of the components is hydrophilic the other hydrophobic. This improves the dispersion of the clay but the micro-segregation in the materials is a serious drawback. Alternatively the clay platelets may be coated with amphiphilic layers. Again the dispersion is improved, but the clay becomes more expensive and has to be tailored to each application.
The group of inorganic materials termed chalcogenides is characterized by a layered structure where a two-dimensional structure exists. The interaction in the layer is strong. Since the layers are uncharged the interaction between layers are weak Van der Waals forces.
Within the group of chalcogenides it has been more difficult to perform the delamination/exfoliation process. In the literature two methods have been described. Both have been performed on laboratory scale but they have been too dangerous and too costly to be applied in industrial productions.
The first method is a chemically based exfoliation as described in the literature. MoS2 is treated in dry hexane with n-butyl-lithium for 48 hours under a protective argon atmosphere. Following a thorough washing with hexane and subsequent drying the material is transferred to an airtight container that is transferred into a reactor where it is opened under water. The violent reaction taking place between the water and the lithium compound being distributed between the layers develop hydrogen gas. The gas pressure lifts the layers apart. The layers may restack loosely or they may float separately in the water. The delaminated/exfoliated material may be collected by addition of a surfactant.
The second method is described in US 2007/0158789 A1 and is a mechanical separation of the layers by exerting an attack from the end planes of the layered material. The attack may be mechanical in the form of a small knife or it may be electrical. Theoretically these methods may achieve a separation down to individual layers. Finally a single surface layer may be peeled off the stack by coating of the surface with an adhesive.
Thus, there is a need in the art for new methods for delamination and/or exfoliation of materials, which method is amenable for industrial scale-up and associated with chemistry being of non-toxic and non-hazardous nature.
In order to overcome the above-mentioned limitations of the known method for delamination/exfoliation the present invention provides a new method for delamination/exfoliation of non-ionic inorganic materials.
In one aspect the present invention provides a process for the preparation of a non-ionic inorganic layered material comprising the use of supercritical carbon dioxide for delaminating/exfoliating the material by a catastrophical fast release of the pressure.
In one embodiment the process for the preparation of a non-ionic inorganic layered material comprises addition of at least one hydrophilic compound to said material prior to release of the pressure. In another embodiment said hydrophilic compound is glycerol.
The invention consists of an efficient method for delamination/exfoliation of layered non-ionic materials suitable on an industrial scale and the use of the obtained materials. The delamination/exfoliation is obtained by first introducing supercritical carbon dioxide between the layers of the material and subsequently releasing the pressure catastrophically whereby the layers are blown apart by the gas pressure. Non-limiting examples of materials that may be treated by this process are WS2, MoS2, (Y-, Ba-, Cu-oxide) and other structurally similar superconductors, NbSe2, Bi2Sr2CaCu2Ox, boron-nitride, dichalcogenides, trichalcogenides, tetrachalcogenides and pentachalcogenides.
In another aspect the present invention provides a delaminated/exfoliated non-ionic inorganic material obtained by the process comprising the use of supercritical carbon dioxide for delaminating/exfoliating the material by a catastrophical fast release of the pressure.
In another aspect the present invention provides a composition comprising a delaminated/exfoliated material incorporated into a chemical network structure such as a hydrogel or an aerogel, said composition obtained by the process comprising the use of supercritical carbon dioxide for delaminating/exfoliating the material by a catastrophical fast release of the pressure followed by incorporation of the delaminated/exfoliated material into the chemical network structure.
In another aspect the present invention relates to the use of the delaminated/exfoliated inorganic material as:
Delamination of a layered material is processes whereby large stacks of layers are split apart in stacks having a small number of layers n, n being less than 500 more often less than 200.
Exfoliation of a layered material is a process whereby large stacks of layers are split apart in single layers or in stacks have a small number of layers n, n being less than 100 more often less than 20.
The critical point is the combination of pressure Pc and temperature Tc above which the compound no longer has a liquid and gaseous state. For combinations of P, T above this point the compound exists in the supercritical state.
Carbon dioxide has a critical point Pc=70 Bar and Tc=31,5° C. When other compounds are present the mixed system may display supercritical behavior with limiting temperature and pressure different from the data found for the pure carbon dioxide.
Van der Waals force is a universal type of interaction present in all materials. In the cases where electrostatic forces or forces between permanent dipoles are present Van der Waals forces are often neglected since they are much weaker. Only in cases where the other types of interactions are absent Van der Waals forces are of interest. They are distance dependant and their magnitude falls off very rapidly when the distance is increased. It is generally accepted that a distance dependence 1/r6 is an appropriate description.
Restacking is a phenomenon occurring after delamination/exfoliation has been attempted. The layers having been lifted apart by the catastrophical depressurization will fall back in top of each other. The Van der Waals forces will act to keep the loose stacks together as before the exfoliation. Since the layers are not properly stacked their distance is increased and the interaction energy is thus much smaller. The restacked material is therefore more readily dispersed in a solvent than the native material.
Intercalation is the phenomena where a molecule is inserted between thee layers of a material. Intercalation can be useful to prevent restacking. If a molecule is present as a cosolvent in the supercritical carbon dioxide it may intercalate between the layers during depressurization. The intercalation prevents the restacking and makes it easier to disperse the delaminated/exfoliated material in another material in a subsequent process.
The term catastrophical fast release of the pressure as used herein means an abrupt decrease in pressure so fast that the carbon dioxide found between the layers cannot slowly leak out. Instead the overpressure will try to expand its confinement layers blowing the stack apart.
A co solvent is a chemical substance that has been added to carbon dioxide. The co solvent has to be soluble in carbon dioxide. Frequently it is used to increase the solubility in carbon dioxide of polar compounds.
For a number of years CISMI has been developing the technologies based upon use of supercritical carbon dioxide. It has been demonstrated that it is a highly efficient technology for impregnation and extraction since the supercritical carbon dioxide penetrates the materials very efficiently. During this work it was surprisingly found that the technology could be used to obtain an efficient and cheap method for delamination/exfoliation of non-hydrophilic layered materials. The dichalcogenide MoS2 is mentioned here as one example from this class. Subsequently we have performed many series of experiments demonstrating the efficiency of supercritical carbon dioxide in the delamination/exfoliation of the dichalogenides. Electron microscopy shows the difference between pristine and restacked materials. The process is highly efficient and the processing time is short. The process scales well from laboratory to factory. This opens the possibilities for optimization of the process for special adaptations to various demands. The supercritical carbon dioxide technology is environmentally and ecologically appealing since it is non-toxic and the CO2 has been produced elsewhere. The use of CO2 is minimizing the use of organic solvents and eliminates wastewater from the process.
The materials to be delaminated/exfoliated will typically be present as particles of the size 1-50μ due to a previous grinding process. The particles are placed in a pressure reactor of the type used for treatment with supercritical carbon dioxide. The reactor is then pressurized with carbon dioxide. Often the conditions are chosen to bring carbon dioxide in the supercritical state. This corresponds to a pressure in the range 70-500 bar. The application of supercritical carbon dioxide to perform impregnation and extraction is well known and it is industrially used for impregnation of wood and extraction of coffeine from coffee beans and ginseng from the roots. The application for exfoliation/delamination of graphenes has recently been disclosed, US2007/0158789 A1. Supercritical carbon dioxide has a density similar to an organic solvent, but it has no surface tension and therefore it fills out the available space as a gas. The diffusion rates are similar to a gas. These properties make it easy for the CO2 molecules to diffuse between the layers of the layered materials. This results in an initial swelling of the material. When the pressure subsequently is catastrophically reduced the gas pressure developed between the layers will outweigh the Van der Walls forces and blow the layers apart. The processing rate is limited by the time necessary to establish an equilibrium concentration of carbon dioxide between the layers. Depending on the material chosen it may take from minutes up to a few hours. The delaminated/exfoliated material is after the process present as a dry fluffy material in the reactor.
The carbon dioxide is a non poisonous inactive gas and it is always present in the atmosphere in small concentrations. The process is therefore free from negative influence on the environment.
In order to facilitate the dispersing of the delaminated/exfoliated material in a host material selected for a subsequent application it may be appropriate to add small amounts of additives to carbon dioxide during the process. This may result in a delaminated/exfoliated material with some intercalation more compatible with the host material.
The method invented is the first commercially feasible process for delamination/exfoliation on a large scale and it will make it possible to develop a number of new materials
Taking MoS2, as an example the exfoliated MoS2, will be characterized by:
Potential applications for exfoliated material using MoS2 as an example are :
MoS2 in the form of finely ground material is placed in a reactor. The particle size is in the range 0.5 to 10 micron depending on the application. The reactor is treated with CO2 at 70° C. and 300 bar for 1 hour. The pressure is released in such a configuration that the suspension of MoS2 in CO2 is sprayed into a thermostated liquid. The liquid may be silicone oil or other suitable liquids chosen with regard to further processing.
MoS2 is placed in a reactor and glycerol with purity 98% or higher is added as a co solvent. The reactor is treated with CO2 at 70° C. and 300 Bar for 1 hour. The pressure is released catastrophically. The MoS2 is found as a silvery looking paste. The suspension is stable over weeks. The compatibility between MoS2 and glycerol is unexpected due to the hydrophobicity of MoS2 and the known hydrophilicity of glycerol.
MoS2 is placed in a reactor and silicone oil is added as a co solvent. The molar weight of the oil is selected in the range 10000-100000. The reactor is treated with CO2 at 70° C. and 300 bar for 1 hour. The pressure is released catastrophically. The MoS2 is found as a black viscous suspension of MoS2. The suspension is stable over weeks. The compatibility between MoS2 and silicone oil is expected due to the hydrophobicity of MoS2 and the hydrophobicity of silicone.
Polyethylene LD is heated in an oven to 100° C. in order to obtain a highly viscous phase. The PE is mixed with exfoliated MoS2 3% w/w. The mixed material is kept in a porcelain crucible for use. It is observed that the wetting of the porcelain is much better with the MoS2 containing material. After cooling to ambient temperature the pure PE can easily be removed from the crucible whereas the MoS2 containing material is inseparable from the crucible.
102 mg MoS2 particles smaller than 15 μm and with an average size of 6 μm is mixed with 1.74 g Glycerin (98%). The mixture is treated with carbon dioxide in a 20 ml reactor made of stainless steel at 40° C. at 300 bar pressure for 2 hours using magnetic stirring. Subsequently the pressure is released over a periode of 25 min. 1.16 g is taken from the reactor and it is mixed with 3.82 g teramethylorthosilicate (TMOS) and 15.2 g methanol under stirring and under nitrogen atmosphere for 15 min. 68 mg 28-30% ammonia dissolved in 2.00 g water under violent stirring. The stirring continues for 2 minutes after addition of water. The sample then is left for 5 min. Now an additional 80 mg ammonia (28-30%) dissolved in 1.00 g water is added under violent stirring. The stirring is continued for 2 minutes and after an additional 5-10 min. a gel is formed. (The sample does not distort if the glass is turned over). The gel is placed for ripening 24 hours at room temperature and finally ripened 3 weeks at +5° C.
15.5 g wet gel is placed in a 36 ml reactor made of 316 stainless steel. The gel is submerged in methanol and the reactor is closed. The reactor is now washed with 120 ml methanol at a rate of 1 ml/min. The pressure is increased to 100 bar at a rate of 3 bar/min, simultaneously the temperature is raised to 40° C. To replace the methanol 450 g carbon dioxide is pumped through the reactor at a rate of 1 g/min at a pressure of 100 bar. The pressure is released at a rate not exceeding 3 bar/min. The dry aerogel weighs 1.09 g containing approximately 6 percent w/w of MoS2.
| Number | Date | Country | Kind |
|---|---|---|---|
| PA 2007 01465 | Oct 2007 | DK | national |
| PA 2008 00098 | Jan 2008 | DK | national |
| Filing Document | Filing Date | Country | Kind | 371c Date |
|---|---|---|---|---|
| PCT/EP2008/063607 | 10/10/2008 | WO | 00 | 11/23/2010 |
