Fecha de publicación
Nº de solicitud
|1.||WO||WO/2013/180668 - METHOD FOR PREPARING COLOUR BEVERAGES||05.12.2013||
|PCT/SK2013/050003||PORUBSKÝ, Ivan||PORUBSKÝ, Ivan|
Method for preparing colour beverages, characterized in that the content of two or more base beverages of different or identical colours, placed in separate compartments of transparent container, are mixed upon opening a cap by pouring thereof out, producing a beverage of different colour.
|2.||WO||WO/2013/165321 - FLUORESCENT MATERIALS||07.11.2013||
|PCT/SK2013/000005||KOZMÉR, Ladislav||KOZMÉR, Ladislav|
Fluorescent materials created by the mixture of base material which amounts from 50% to 90% of the total weight and phosphorogenic pigment which amounts from 10% to 50% of the total weight, and the fluorescent material is in form of compact mass or in a form of surface coating material. Base material are materials used in building industry, such as gypsum, mosaic wall coating or sealant substance while all materials are based on anorganic raw materials and organic sealant, nonplasticized or plasticized polyurethane (PUR), epoxide resin, transparent lackquers based on synthetic substances, synthetic and non- synthetic cover coating. Phosphorogenic pigment is zinc sulphide and coper or strontium aluminate.
|3.||WO||WO/2013/147712 - MECHANISM FOR COLLECTING IMPURITIES IN STAGNANT WATERS||03.10.2013||
|PCT/SK2013/000004||TECHNICKÁ UNIVERZITA V KOSICIACH||ŠEBO, Dušan|
The equipment for collection of impurities in stagnant waters having a catamaran design comprises two catamaran floats (1) having a form of a hollow body terminated by the jaws (7), where at the front part of the catamaran floats (1) there is mounted in the frame (2) the conveyor belt (3) with the removable mesh belt (11) with fixed forks (12), with the drive (5) of the belt (11). At the middle part of the catamaran floats (1), under the conveyor belt (3), there is attached the removable container (8), in the cavity of the catamaran floats (1) there are the batteries (14) connected to the photovoltaic cells (9), which are installed on bracket (4) of the photovoltaic panels and at the end of the catamaran floats (1) there is fixed the marine engine (13), the rudder (6) and the remotely programmable control (10), and the equipment is also provided with a separate remote control - a joystick.
|4.||WO||WO/2013/137834 - A METHOD OF DISPOSAL OF CYANOBACTERIA IN STAGNANT WATERS AND EQUIPMENT FOR ITS IMPLEMENTATION||19.09.2013||
|PCT/SK2013/000003||TECHNICKÁ UNIVERZITA V KOŠICIACH||ŠEBO, Dušan|
An equipment for disposal of cyanobacteria in stagnant waters has a float structure, to which two types of bipolar electrodes (1 and 6) are mounted under the surface of water, interconnected and supplied with electric direct current via an alternator (10). The equipment comprises a supporting float (5) having the shape of a hollow body, in which there is a transversely positioned rib (4) with an attached suspended electrode (1), interconnected to supplies of photovoltaic cells (8) and alternator (10), fixed on the rib (4) there is the device (9) for utilizing wind power, connected to an alternator (10), driving the water pump (2), which is placed in the delivery pipe (3) and is connected directly to the axis of the device (9), for utilization of wind power. Fixed on the supporting float (5) there is the upper float (7) with the anchored grid electrode (6) and with the stored photovoltaic cells (8), interconnected with the electrodes (1) and (6). The delivery pipe (3) is connected to the water pump (2), and the outlet of the delivery pipe (3) is positioned directly above the suspended electrode (1). The upper float (7) copies the shape of the supporting float (5) and is made of a dielectric, light, floating material. The method of disposal of cyanobacteria in stagnant waters is based on quatrolytic disposal of cyanobacteria by the electroflotation method, by means of the above-mentioned equipment.
|5.||WO||WO/2013/130020 - QUERCETIN DERIVATIVES, THEIR PHARMACEUTICAL COMPOSITION AND USE||06.09.2013||
|PCT/SK2013/000002||ÚSTAV EXPERIMENTÁLNEJ FARMAKOLÓGIE A TOXIKOLÓGIE SAV||ŠTEFĚK, Milan|
The invention relates to semi-synthetic derivatives of quercetin formula I and pharmaceutically acceptable salts, hydrates and solvates, wherein groups R1 to R5, identical or different, are independently H, benzyl, and at least one group is 3-chloro-2,2-dimethylpropanoyl, 4-O-acetylferuloyl, or 2-chloro-1,4-naphthoquinon-3-yl. The invention relates to the use of derivatives of quercetin, the preparation of medicaments for the treatment or prevention of diseases or disorders where oxidative stress and polyol pathway are key etiological factors. The invention also relates to pharmaceutical compositions containing these compounds and their use in the treatment of human and animal health problems in which R1 to R5 are independently H, benzyl, and at least one group is selected from 3-chloro-2,2-dimethylpropanoyl, 4-O-acetylferuloyl, or 2-chloro-1,4-naphthoquinon-3-yl.
|6.||WO||WO/2013/119187 - METHOD FOR THERMAL DECOMPOSITION OF ORGANIC MATERIAL AND EQUIPMENT FOR IMPLEMENTATION OF THIS METHOD||15.08.2013||
|PCT/SK2013/000001||FARKAS, László||FARKAS, László|
Method of thermal decomposition of organic material from specified and/or mixed wastes from used tyres, plastics, paper, textiles, biomass and organic portions of municipal waste in an inert atmosphere without the participation of oxygen/air takes place continuously in a hermetically enclosed flow-type apparatus for thermal decomposition in such a way that the modified feedstock in the form of crushed material, shreds or chippings with the size of up to 350 mm is transported to the batching hopper (15), then it is transported by means of the batching spiral-type conveyor (16) through the decomposition oil filling (17), which constitutes the input oil seal (8), to the tubular flow-type cracking reactor (1a) by means of the shifting spiral- type conveyor (2), where thermal cracking of material is taking place in the tubular flow- type cracking reactor (1a) at the temperature of 165 to 750 °C at the atmospheric pressure from 100834.6675 Pa up to 101815.3325 Pa (i.e. at the atmospheric pressure from -50 mm up to +50 mm of water column) resulting in gaseous, liquid and solid products, wherein the gaseous decomposition products are further transported from the first part (1 b) of the tubular flow-type cracking reactor through the outlet (13) and through the outlet (14) in the second part (1c) of the tubular flow-type cracking reactor into the condensation system, then the solid products are transported to the second part (1c) of the tubular flow-type cracking reactor by means of the spiral conveyor (2) through the water cooler (7) via the opening (19) for the output of solid products to the output water seal (9) constituting the hydraulic seal, from where the solid products are taken out by means of the in-feed conveyor (20) and the spiral-type out-feed conveyor (22). Equipment for thermal decomposition (1) of organic material for implementation out the method of thermal decomposition consists of the tubular flow-type cracking reactor (1a), which is positioned on the frame (32) of the tubular flow-type cracking reactor at an angle of 8 to 38 degrees relative to the horizontal plane, whereas the tubular flow-type cracking reactor (1a) houses a shifting spiral conveyor (2) the bottom part of which is submerged in the input oil seal (8), with the second part (1c) of the tubular flow-type cracking reactor being enclosed by the output water seal (9).
|7.||WO||WO/2013/089652 - METHOD OF PLASMA CHARGE TREATMENT OF THE GAS SENSITIVE LAYER OF A GAS SENSOR||20.06.2013||
|PCT/SK2011/050024||ELEKTROTECHNICKÝ ÚSTAV; SLOVENSKÁ AKADÉMIA VIED||KUNZO, Pavol|
Sensor for accurate examination and analysis of gases, predominantly hydrogen and/or ammonia, using electrical and electrochemical means. The sensing element of the sensor consists of conducting polymer whose outer surface is treated in a plasma discharge with electron temperature (thermal kinetic energy) of 1 to 10 eV and electron density of 1014 to 1018 m-3. The plasma is generated in oxygen gas or the plasma treatment in other gas is followed by the sensor exposure to the oxygen containing gas afterwards. The conductive polymer is polyaniline or polypyrrole or polytiophene or their combination.
|8.||WO||WO/2013/089650 - LABORATORY HEAT PRESS||20.06.2013||
|PCT/SK2011/000024||ÚSTAV ANORGANICKEJ CHEMIE SAV||ŠAJGALIK, Pavol|
Laboratory heat press consists of furnace part equipped with dilatometer which is placed beneath removable double-acting pneumatic cylinder anchored on four shafts, of power supply and of computer which regulates process and collects data, while in the working space is situated graphite press die with sample, which is placed on sliding piston holder and the device is equipped with control electronics. Heating equipment is graphite element, and around the element are situated graphite shields made from solid graphite and graphite wool insulation. Outer shell of furnace and both flanges are water cooled. Flanges are equipped with holes for thrust pistons and the furnace shell contains hole for connecting the vacuum pump and hole for installation of the pyrometer. Graphite pressing die with sample is equipped with pistons, which are influenced by power from double-acting pneumatic cylinder, while on the both graphite pistons are graphite radiative rings and between them is graphite wool.
|9.||WO||WO/2013/089651 - MULTILAYER RIBBONS BASED ON METAL ALLOYS AND THE METHOD OF PREPARATION THEREOF||20.06.2013||
|PCT/SK2011/000025||FYZIKÁLNY ÚSTAV SAV||ŠVEC, Peter|
Multilayered ribbons based on metallic alloys according to the proposed solution they consist of two or more layers of metallic alloys mutually joined by planar metallurgical joint having submicron thickness ensuring mechanical joining of individual adjacent layers while the layers are characterized by their amorphous structure in as-prepared state and by enhanced electrical, mechanical and magnetic properties. The method of preparation of multilayered metallic alloy ribbons and sheets is realized by the ejection of individual alloy melts from a split multichamber crucible with nozzles for planar flow casting by means of overpressure of a gaseous medium onto the surface of rapidly rotating metallic wheel where sequential solidification of individual melt layers takes place and where each consecutive layer is ejected onto the preceding and already solidified layer, on which it solidifies and forms metallurgical joint with thin, preferably planar interface between individual layers.
|10.||WO||WO/2013/066276 - METHOD OF DISINTEGRATING ROCK BY MELTING AND BY SYNERGISM OF WATER STREAMS||10.05.2013||
|PCT/SK2012/050015||GA DRILLING, A.S||KOČIŠ, Igor|
Method of disintegrating rock by melting and by synergism of water streams, comprising action of the heat flow source on the rock, action of the water stream source on the melted rock so that: the heat or energy flow source acts on the rock at least until its local phase transition into the melt occurs, at least one water stream is directed into the locally created melt, physical explosion occurs in the melt, on which the water stream acts.