Title of Invention	"COMPOSITION AND DEVICES FOR GAS SORPTION AND PROCESS FOR THEIR MANUFACTURING"
Abstract	Compositions and devices for gas sorption that can be activated just before their use are described, which hence do not need storing under inert atmosphere during storage and transportation.

Full Text

"COMPOSITION AND DEVICES FOR GAS SORPTION AND PROCESS FOR THEIR MANUFACTURING" The present invention relates to a composition for gas sorption, as well as to devices formed with the composition; the invention also refers to processes for obtaining the composition. In particular, the invention refers to compositions and devices for sorption of traces of gases, both residual gases in evacuated chambers and impurities in inert gases, in applications in which the space available for the sorbing device is reduced. An example of systems requiring the control of the internal atmosphere, but having only limited room for the gas sorbing device are the flat panel displays, both field emission displays (also known as FEDs, generally requiring an inner vacuum atmosphere) and plasma displays (also known as PDPs, inside which there's an atmosphere of a given composition). Another particularly important application is represented by the OLED screens (from the definition "Organic Light Emitting Display"), in which sorption of moisture from the screen inner space is essential, but it can be necessary also sorbing other gases such as oxygen or carbon dioxide. Due to the relevance of this application, in the following of the description reference will be made to these screens, but it is intended that compositions and sorbing devices of the invention can be used in a wide range applications needing gas sorption, particularly when the thickness available for housing the sorbing device is reduced little. OLED screens are used as displays for mobile phones, for Hi-Fi equipments, for car dashboards and the like; this kind of screens and the problems related to water entering inside them are disclosed e.g. in US patent No. 5,882,761. The search publication RD 430061 and the International Patent Application Publication WO-A-02/27812 in the applicant's name disclose moisture sorbing systems which are specific for OLEDs. These systems are formed of a part with a central cavity filled with drying material, welded at the edges to a water- permeable membrane. Patents US 4,985,296 and US 5,078,909 and International Patent Application Publication WO-A-01/88041 disclose sorbing systems based on an alternative approach to the problem: in this case powders of the material active in gas sorption are incorporated in a resin or in a polymeric material, having gas permeability enough to allow gases to reach the particles of sorbing material. A problem common to all the known sorbing systems is nevertheless that these, once manufactured, must be kept under inert atmosphere throughout storage time and during transportation, to avoid in these steps any contact with reactive gases and hence their loss of functionality. Object of the present invention is to provide a composition and sorbing devices obtained using this composition which avoid said problem. Said object is achieved according to the present invention by means of a composition comprising a gas sorbing component A dispersed in a component B, this latter being in the form of a cross-linked and porous matrix, said composition being obtainable by means of a process in which: - at least one material A', that can be converted through a thermal treatment into said sorbing component A, is mixed with said component B or a precursor thereof, B', wherein B is chosen for mixing with A' if B is capable of resisting essentially unaltered the thermal treatment for changing A' into A, while B' is chosen for mixing with A' if B' is able to transform into B after said thermal treatment; and - the so obtained mixture is subjected to a thermal treatment under vacuum or under an atmosphere of a gas inert as regards component A, in conditions such as to cause the conversion of material A' into sorbing component A. As used here above with reference to component B, "essentially unaltered" means that this component either resists unchanged the thermal treatment, or, if it undergoes modifications during the treatment, these are such that characteristics indicated for B, namely porosity and cross-linking, are retained. The invention will be disclosed later on with reference to the only Figure, which graphically shows the result of a moisture sorption test from a device made from a composition of the invention. The invention differs from all of known systems because the active component, A, is not added as such to a matrix (e.g. polymeric) during the first steps of system manufacturing, but it is mixed into the matrix (or a precursor thereof) in the form of a precursor thereof, A', which is only subsequently converted into active component A, for example just before using in the device of final destination; in this way the composition of the invention is inactive for gas sorbing throughout storage and transportation steps, and consequently in these steps particular precautions, such as storage in containers sealed under vacuum or under inert atmosphere, are not needed. Material A', sorbing component precursor in the composition of the invention, can be selected among any materials that may be converted into a component A capable of gas sorption by means of a treatment at not too high temperature, or in not too onerous conditions. Said treatment conditions are fixed by component B (or material B'), and by the support onto which the composition is laid; in general, these conditions must be such not to destroy the cross-linked structure of B or close its pores, and not to destroy the support. In case component A is a moisture sorber, this could be an alkaline-earth metal oxide, in particular selected among calcium oxide, CaO, strontium oxide, SrO, and barium oxide, BaO; in this case, preferred precursor materials A' are the related hydroxides, Ca(OH)2, Sr(OH)2 and Ba(OH)2 respectively, that can be dehydrated to yield the oxides by treatments at temperatures from about 300 to 650 °C in times of few hours, under vacuum or under inert atmosphere (the dehydration of Ca(OH)2 can be carried out under gas, while Sr(OH)2 and Ba(OH)2 require vacuum); if dehydration is performed under an inert gas, this is preferably flowing. Among these oxides, BaO presents the best features in moisture sorption, but the use of CaO is preferred owing to low price of its precursor and because, unlike BaO, it does not present toxicity problems; transformation of Ca(OH)2 into CaO occurs successfully, in about 2 hours, at a temperature of about 300 °C under vacuum; the decrease of treatment times is also possible by increasing temperature, for example up to about 500 °C. Calcium oxide has the additional advantage that upon moisture sorption is changed into the hydroxide (reaction A -> A'), that has the capability of sorbing carbon dioxide, COa: some producers of OLEDs have indicated that the proper functioning of these devices also requires the sorption of this gas. Another possible moisture sorber is boron oxide, 8263, obtainable in a particularly active form from boric acid, HsBC^, according to the procedures disclosed in US patent 6,304,367 (treatment at temperatures lower than 200 °C, preferably at low pressure). When the gas to be sorbed is oxygen, component A can be for example a transition metal oxide in which the metal has a low oxidation state and is easily further oxidable. An oxide of this type is for example manganese (II) oxide, MnO, that easily sorbs oxygen changing into MuzOa; a precursor A' suited for obtaining MnO is manganese carbonate, MnCO3, that is quickly converted into the oxide by means of a thermal treatment at about 300 °C under vacuum. Other useful components A for the sorption of oxygen are FeO and Ni in finely dispersed form, that can be obtained through thermal decomposition under vacuum of the corresponding oxalates, respectively FeC2O4 and NiC2O4, at temperatures in the range 350-400 °C. In case A is a metal such as Ni, the dispersion may be favoured by the fact that decomposition takes place in the matrix B or while this is formed, so the metal forms "islands" that deposit on the internal surfaces of the matrix, or small metallic aggregates that are trapped by the same matrix. The above cited components A are all chemical sorbers, namely, they sorb moisture through a chemical reaction that transforms A into another compound; however, the invention is not limited to chemical gas sorbers, and A can also be a physical sorber, namely, a material that fixes gas molecules at its surface by means of adsorption. In this case too, carrying out the thermal conversion of A into A' in a matrix helps in obtaining material A in a finely divided form, that ensures good sorption properties. An example of possible physical sorber (component A) is y-alumina, that can be obtained by thermal decomposition under vacuum at around 300 °C of norstrandite, a form of aluminum hydroxide, A1(OH)3, or by thermal decomposition under vacuum at around 250 °C of boehmite, a form of aluminum oxo-hydroxide, A1OOH. Obviously, compositions of the invention can comprise several A-type components, and therefore be obtained from mixtures comprising several A'-type materials; for example, in the OLED application, besides moisture, a damaging effect due to oxygen seems to be present, and in this case a composition obtained from a mixture comprising Ca(OH)2 and MnCOs can be used. In these cases, the thermal treatment conditions to which the mixture has to be subjected, must be chosen in order to ensure effective conversion of all materials A' into related sorbing components A. In the starting mixture materials A' are generally used in the form of powders; these have preferably particle sizes lower than about 100 /mi, and more preferably lower than 50 /mi and even more preferably lower than 30 /mi. During thermal treatment for converting A' into A, powders obviously also undergo a morphologic transformation, and it is observed that granules size slightly decrease, while essentially keeping the same order of magnitude: accordingly, materials A' must be used as fine powders to easily ensure first of all their homogeneous dispersion in final composition and high surface area of component A (decisive for obtaining good properties in gas sorption), and moreover to allow achievement of devices having thin thickness from these compositions. Component B and material B' are such that, during thermal treatment for converting A' into A, respectively either retain cross-linked structure and porosity or transform into a B-type component. B component has inner cohesion and is capable to retain particles of A. The preferred component B or material B' are certain silicone resins resistant to high temperature treatments, for example used as carriers of heat-resistant paints for mufflers, boilers or similar applications. Phenyl-methyl-polysiloxane resins supplied by Tego Chemie Service Italia of Pandino (CR) as Silikophen® (registered name by Goldschmidt AG, DE) are an example. These resins resist in continuous, by themselves, at temperatures up to 350 °C, and up to about 650 °C when filled with inorganic materials. Determining chemical composition or structure of these resins is extremely complicated, especially after thermal treatment; however IR analyses showed that, after thermal treatments necessary for converting A' into A, these resins lose only partially their organic components and undergo partial vitrification. In these treatments, resins used in compositions of the invention keep cross-linking, as shown by particles retention even after treatment, and keep adhesion to the substrate even if wrapped around objects with circular section having diameter of about 1 cm. In the mixtures used to manufacture compositions of the invention, weight percent of A can vary within wide limits, depending on specific weight of A'; in case of mixtures of Ca(OH)2 in Silikophen®, initial filling up to about 50% can be reached, obtaining after thermal treatment a homogenous sorbing composition, as experimentally proved. Adding other components to the mixture comprising A' and B (or B') is also possible. For example, it is possible to add a solvent, such as alcohols, glycols, polyethers and esters, useful for controlling mixture viscosity and consequently the possibility of obtaining a homogenous deposit; otherwise a dispersing surface-active additive, useful for allowing a homogenous distribution of particles of A' in the mixture. The compositions of the invention are generally used in form of films onto a support. The support may be a wall of the device in which vacuum must be maintained (or in which the inner gas composition must be controlled). For instance, in the case of OLEDs, the support may be the inner surface of the rear side (referred to in the field as the backplate), that may be made of glass or metal; similarly, in the case of FEDs or PDPs, it may be possible to deposit the mixture of A' and B (or B') onto a surface of one of the two glass plates making up the display, preferably the rear one, and treat the assembly at the temperature needed for the conversion A' -^ A; if B or B' is a silicone resin, this keeps good adhesion to the glass surface. Alternatively, it is possible manufacturing discrete sorbing devices, depositing the precursors mixture on a additional support and then adhering this onto an available wall of the final destination device (for example, on the internal surface of the backplate of an OLED). In case of use of an additional support, again this may be made of glass or be a metallic sheet, for example steel or Nichrofer (an alloy of nickel, chromium and iron), having thickness for example of about 50 ^m or less. In the case of the additional support, it is either possible to manufacture sorbing devices one by one, or to manufacture large-sized supports (foils, sheets, plates, or tapes) coated with the precursors mixture, and then to cut these in desired size. Precursors mixtures can be deposited on the desired support in several ways, for example through brush work or spraying; preferred is the use of screen-printing, well known in the printing field, allowing greater control of the deposit thickness (by means of control of screen thickness, through which mixture is forced to pass for reaching the support). In any case, thermal treatment for converting A' into A can be carried out at the most suited moment, for example immediately before introducing the sorbing device into the final system, hi the specific case of CaO, it is also possible to "reactivate" the composition, in case that during storing, transporting and handling, the oxide has undergone partial or total transformation into the hydroxide upon water sorption (due to poor control of the process, or to an exposures to air that is either unavoidable or preferred to lower the process complexity and costs). In this case, the ease of transformation of the hydroxide back to the oxide allows this change to be carried out more than one time before the sealing of the device of final destination of the composition of the invention. The compositions of the invention can be used to produce deposits having thickness values in a wide range. The low end of this range is determined by technical needs only, in particular by the need of having component A in an amount enough for the application; in the various tests carried out by the inventors, the lowest limit achieved for thickness of final composition is about 20 fjim. Compositions and devices of the invention therefore also provide the additional advantage of an easy manufacturing in particularly thin films, of thickness lower than a tenth of millimetre, not obtainable by systems at present known constituted of particles dispersed in a matrix. Thick deposits can be obtained essentially with any desired thickness, but during testing the inventors have noted that thicknesses higher than about 150 jitm gave problems of internal cohesion, forming fractures in the deposit; as a consequence, higher deposits can be formed and used if the cracking of the deposit is not a problem in the foreseen application. The invention will be further illustrated from the following examples. These non-limiting examples show some embodiments intended to teach to those skilled in the art the manufacturing of the invention and to represent the best way to carry out the invention. EXAMPLE 1 43.3 g of Ca(OH)2, 10.3 g of dipropyleneglycolmethylether as viscosity regulator, 1 g of Dispers 630 (a dispersing surface-active agent), 1 g of Airex 935 as mixture deaerator and 44.4 g of Silikophen® P 80/MPA resin (Dispers, Airex, and Silikophen are supplied by Tego Chemie Service Italia) are mixed under stirring. The mixture so obtained is deposited using screen-printing on a Nichrofer sheet having thickness of 50 jam. From this sheet, some strips of 3 x 6 cm are cut. Three of these strips are introduced in a chamber provided with a gastight valve; this chamber, with the valve open, is introduced into an oven and the strips are subjected to the following thermal treatment under vacuum: - heating from room temperature to 420 °C in one hour; - keeping at 420 °C for one hour; - cooling under vacuum down to 250 °C and subsequently under argon flow down to room temperature. The valve of chamber containing the strips is closed, the chamber is extracted from the oven, introduced in a glove box, opened and then the strips are withdrawn. Inside the glove box, the deposit thickness is measured using a comparator and it results equal to 60 ± 10 ^m. Still inside glove box, a strip is punched obtaining rectangular-shaped pieces of 10 x 18 mm. Two of these pieces are inserted into a glass bulb provided with insulating valves, used to carry pieces to the system for measuring moisture sorption properties. EXAMPLE 2 The bulb with pieces prepared as described in Example 1 is assembled on a bench for sorption tests, allowing to dose known amounts of water vapour. The bulb valve is opened, the system is evacuated to remove argon, and the pieces are connected to the system of water dosing in order to keep a constant water pressure of 1 Pa on the pieces and measuring the pieces weight increase Ap in time (normalized as regards the deposit surface). The result of test is represented in Figure 1, showing that samples of the invention rapidly sorb moisture from the surrounding environment. Thanks to the fact that the compositions of the invention can be manufactured in extremely reduced thickness, while retaining good sorption capabilities, these are suited for using in OLED screens, in which the available thickness for the gas sorber is always limited. In particular, compositions of the invention can be useful especially for manufacturing OLED screens as disclosed in Japanese Patent No. 3,293,527, in the name of Fuji Electric, which, unlike previous OLED screens, do not have a dedicated housing for the sorbing device, in the form e.g. of a recess or hollow on the rear support of the screen, whereby the thickness available for the sorbing material is further reduced. In these conditions, the possibility offered by the present invention to form sorbing layers having thicknesses even of few tens of (Jim results particularly useful and advantageous. WK CLAIM: I .A compositionfor gas sorptioi) comrinxce .a gas sorbing component A, selected among an alkaline-earth metal oxide, y-alumina, MnO, FeO or Ni, dispersed up to 50 % by weight in a component B selected among a high temperature resistant siliconic resin, and thus obtained mixture is subjected to a thermal treatment. 2. The composition as claimed in claim 1. \\ herein said component A is a moisture sorbcr. 3. The composition as claimed in claim J, wherein said component A is an oxide selected among calcium oxide, strontium oxide, barium oxide and magnesium oxide, and said material A'is the respeelne hydroxide. 4. The composition as claimed in claim 2. wherein said component A is boron oxide and said material A' is boric acid. 5. 1 he composition as claimed in claim 1 u herein said component A is an oxygen getter. 6. The composition as claimed in claim 5 wherein said component A is manganese (11) oxide, MnO. and said material A'is manganese (II) carbonate. MnC03. 7. The composition as claimed in claim 5. wherein said component A is iron (II) oxide, FeO. and said material A'is iron (II) oxalate. FeC2O4 8. The composition as claimed in claim 5. wherein said component A is metallic nickel, and said material A'is nickel (II) oxalate. NiC2()4. 9. 1 he composition as claimed in Jam, i. •.'.herein saidcomponent A is a physical gas sorber. lo The composition as claimed in claim,-). wherein physical gas sorber said is a moisture sorber. II The composition as claimed in claim 0. wherein said moisture sorber is \- alumina. and the A' material is either ihc aluminum hydroxide norstrandile or the aluminum oxo-h\dro.\ide boehmiie. 1? The composition as claimed in claim I. wherein said material B'or component B is a phenyl-mcli;;. l-polysiloxane resin. 13 A process for obtaining composition as claimed in claim 1 to 12, comprising the steps of: mixing at least a material A' precursor of component A and either a component B or a material B' precursor of component B; said composition being obtainable by means of a process in which: - at least one material A' selected among an hydroxide of an alkaline-earth metal, norstrandite, boehmite, MnCO3, FeC2O4 and NiC2O4 and that is converted through a thermal treatment into said component A, is mixed with said component B by weight; and the so obtained mixture is subjected to a thermal treatment under vacuum or under an atmosphere of a gas inert as regards component A, in conditions such as to cause the conversion of material A' into sorbing component A." 1-1 \ process as •, camed in claim is'chain in said Mep of thermal treatment is carried out at a temperature in the range of 70'C to 600 V immediately before introducing the ..omposition into the final destination device 15 A process as cl Tuned in claim 13. wherein said material A' is an alkaline- earth metal hydroxide and said thermal treatment is carried out at temperature in the ran lie of 300 to ()()() C. 16 A process as cLuned in claim 13 whuvin said material A' is boric acid and said thermal treatment carried out at a temperature between 70°C to 200°C. 17 A process as claimed in claim 13 \\hereiu said material A' is manganese carbonate, and .aid thermal treatment is carried out at a temperature ol'30() °C. 18 A process as claimed in claim 13 \\herein said material A' is an oxalate of iron or nickel, and said thermal treatment is c.irned out at a temperature in the range ol 300°C and 400 C. 19. A process as claimed in claim 1.1 wherein said material A' is either the aluminum hydroxide norstrandite or the aluminum oxo-hydroxide boehmite, and said thermal treatment is carried out at a temperature of 300 °C and 250 °C. respectively. 20 A process as claimed in claim 13 \\lierein said material A' is used in form of powders having particle size lower than 100 urn. 2 1.\ process as c! -Trial in claimin claim' SAID COMPONENT A. is calcium oxide and said mixture comprises up to 50" .1 b\ \\eight ol calciun hydroxide. 22, A composition for gas sorption as herein described with reference to forgoing examples and accompam ing drauings

Documents:

3719-delnp-2005-abstract.pdf

3719-DELNP-2005-Claims-(19-09-2007).pdf

3719-DELNP-2005-Claims-24-04-2008.pdf

3719-delnp-2005-claims-30-05-2008.pdf

3719-delnp-2005-claims.pdf

3719-DELNP-2005-Correspondence-Others-(19-09-2007).pdf

3719-DELNP-2005-Correspondence-Others-24-04-2008.pdf

3719-delnp-2005-correspondence-others-30-05-2008.pdf

3719-delnp-2005-correspondence-others.pdf

3719-DELNP-2005-Description (Complete)-(19-09-2007).pdf

3719-DELNP-2005-Description (Complete)-24-04-2008.pdf

3719-delnp-2005-description (complete).pdf

3719-delnp-2005-drawings.pdf

3719-DELNP-2005-Form-1-24-04-2008.pdf

3719-delnp-2005-form-1.pdf

3719-delnp-2005-form-18.pdf

3719-DELNP-2005-Form-2-(19-09-2007).pdf

3719-DELNP-2005-Form-2-24-04-2008.pdf

3719-delnp-2005-form-2.pdf

3719-delnp-2005-form-26.pdf

3719-delnp-2005-form-3.pdf

3719-delnp-2005-form-5.pdf

3719-DELNP-2005-PCT-210-24-04-2008.pdf

3719-delnp-2005-pct-304.pdf

3719-delnp-2005-pct-306-24-04-2008.pdf

3719-delnp-2005-pct-308.pdf

3719-delnp-2005-pct-332.pdf

3719-delnp-2005-pct-401.pdf

3719-DELNP-2005-PCT-409-24-04-2008.pdf

3719-delnp-2005-pct-409.pdf

3719-delnp-2005-pct-request form.pdf

3719-delnp-2005-pct-search report.pdf