mhurhangee/ep-ind-claims huggingface dataset:
A steel door case with fire-retardant properties with a sheet metal moulded part, which comprises a door-side door case surface, a rebate section angled at right angles and adjoining the door-side door case surface, an abutment section adjoining the side of the rebate section facing away from the door-side door case surface, a reveal section aligned in parallel with the rebate section and adjoining the abutment section, and an edge fold adjoining the reveal section, angled in the direction of the door case surface and aligned parallel with the latter, wherein an intumescent material (11, 11a, 11b, 11c, 12) is arranged at the inner side of the sheet metal moulded part, characterised in that the intumescent material (11, 11a, 11b, 11c, 12) is arranged exclusively in the form of a door-side intumescent strip (11, 11a, 11b, 11c, 12) at least in sections at the inner side of the rebate section and in the form of a reveal-side intumescent strip at the inner side of the edge fold and that the inner side of the door case surface and the inner side of the reveal section are free from intumescent material.
An ultraviolet disinfection method comprising: selecting operating parameters for an ultraviolet disinfection process of flowing liquid carrying first and second types of entities to affect the first type of entities while the second type of entities remains intact; illuminating the liquid with ultraviolet light according to the operating parameters; and adjusting the operating parameters based on real-time measurements of ultraviolet transmission and flow rate of the liquid; wherein adjusting the operating parameters includes continuously adjusting intensity of the ultraviolet light; wherein the first type of entities includes Vibrio; and wherein the second type of entities includes rotifiers and the UV dose is maintained above 15 miliJoules/cm 2 and below 60 miliJoules/cm 2. selecting operating parameters for an ultraviolet disinfection process of flowing liquid carrying first and second types of entities to affect the first type of entities while the second type of entities remains intact; illuminating the liquid with ultraviolet light according to the operating parameters; and adjusting the operating parameters based on real-time measurements of ultraviolet transmission and flow rate of the liquid; wherein adjusting the operating parameters includes continuously adjusting intensity of the ultraviolet light; wherein the first type of entities includes Vibrio; and wherein the second type of entities includes rotifiers and the UV dose is maintained above 15 miliJoules/cm 2 and below 60 miliJoules/cm 2.
Processing unit comprising control means intended to act on at least one exciter coil in order to move a moveable armature of an electromagnetic actuator (100, 101), said control means generating a periodic voltage wave frame comprising three or at least five rectified half-cycles (Si), each half-cycle (Si) of which comprises at least one first and at least one second excitation pulse sequence (S A, S B) for each pair of two consecutive half-cycles in the frame, the electrical energy of the excitation pulse sequences (S A, S B) of a first half-cycle (Si) being less than the electrical energy of the excitation pulse sequences of a second half-cycle (S i+1) following said first half-cycle (S i), characterized in that, the excitation pulse sequences being adjusted by a synchronization signal with respect to the voltage waves, - the first excitation pulse sequence (S A) starts substantially at a voltage zero of a half-cycle, and - the second excitation pulse sequence (S B) ends substantially at a voltage zero of said half-cycle. - the first excitation pulse sequence (S A) starts substantially at a voltage zero of a half-cycle, and - the second excitation pulse sequence (S B) ends substantially at a voltage zero of said half-cycle.
A sample analysis cartridge (700, 800, 900, 3120), comprising: a housing having internal barriers,, an analysis channel (732, 832, 932, 1132, 1732, 2704) disposed within the housing, a first reservoir (722, 822, 824, 922, 1122, 1124, 1324, 1460, 1560, 2724) disposed within the housing and at least partially filled with a first liquid volume comprising sample preparation reagents, the first reservoir having a first outlet configured to permit the first liquid volume to flow from the first reservoir through the first outlet into the analysis channel; a second reservoir (722, 822, 828, 922, 1122, 1560, 2728) disposed within the housing and at least partially filled with a second liquid volume comprising a wash solution, the second reservoir having a second outlet configured to permit the second liquid volume to flow from the second reservoir through the second outlet into the analysis channel; a third reservoir (722, 822, 826, 922, 1122, 1560, 2726) disposed within the housing and at least partially filled with a third liquid volume comprising a chemical substrate, the third reservoir having a third outlet configured to permit the third liquid volume to flow from the third reservoir through the third outlet into the analysis channel; an input tunnel (712, 812, 912, 1112, 1400, 1500) that extends from an aperture at a surface of the housing to the first reservoir; and a circuit board (750, 850, 950, 1150, 1750) coupled to the housing, the circuit board comprising one or more sensors (758, 1158, 2760) disposed within a portion of the analysis channel. a housing having internal barriers,, an analysis channel (732, 832, 932, 1132, 1732, 2704) disposed within the housing, a first reservoir (722, 822, 824, 922, 1122, 1124, 1324, 1460, 1560, 2724) disposed within the housing and at least partially filled with a first liquid volume comprising sample preparation reagents, the first reservoir having a first outlet configured to permit the first liquid volume to flow from the first reservoir through the first outlet into the analysis channel; a second reservoir (722, 822, 828, 922, 1122, 1560, 2728) disposed within the housing and at least partially filled with a second liquid volume comprising a wash solution, the second reservoir having a second outlet configured to permit the second liquid volume to flow from the second reservoir through the second outlet into the analysis channel; a third reservoir (722, 822, 826, 922, 1122, 1560, 2726) disposed within the housing and at least partially filled with a third liquid volume comprising a chemical substrate, the third reservoir having a third outlet configured to permit the third liquid volume to flow from the third reservoir through the third outlet into the analysis channel; an input tunnel (712, 812, 912, 1112, 1400, 1500) that extends from an aperture at a surface of the housing to the first reservoir; and a circuit board (750, 850, 950, 1150, 1750) coupled to the housing, the circuit board comprising one or more sensors (758, 1158, 2760) disposed within a portion of the analysis channel.
A Surfactant-Improved simultaneous saccharification and co-fermentation method for lignocellulose, characterized in that a pretreated lignocellulose substrate is directly subjected to simultaneous saccharification and co-fermentation without any detoxification treatment by adding surfactant at a concentration of 0.125-0.4g/mL, wherein the surfactant is added after pre-enzymatic hydrolysis and is selected from the group consisting of polyethylene glycol, polyethylene glycol monomethyl Ether (MPEG), polyethylene glycol dimethyl ether, polydimethylsiloxane (PDMS), or combinations thereof in any proportion, wherein the method comprises: mixing the pre-treated lignocellulose as a substrate, a cellulase, and a pH buffer solution to incubate and conduct the pre-enzymolysis for a period of time at a raised temperature for obtaining a resulting hydrolyzed mixture; lowering the raised temperature; and adding the surfactant and Saccharomyces cerevisiae to the hydrolyzed mixture for the simultaneous saccharification and ethanol fermentation to produce ethanol.
A method of producing a silicon-plated metal sheet, comprising: melting at least one of a silicon-containing alkali metal salt or a silicon-containing ammonium salt in a molten salt comprising lithium chloride, potassium chloride, and an alkali metal fluoride to prepare a molten-salt electrolytic bath; and performing constant-current pulse electrolysis or constant-potential pulse electrolysis with a metal sheet, serving as a cathode, immersed in the molten-salt electrolytic bath under conditions of a pulse duration of from 0.1 seconds to 3.0 seconds and a duty ratio of from 0.5 to 0.94 to thereby form a silicon layer on the metal sheet. melting at least one of a silicon-containing alkali metal salt or a silicon-containing ammonium salt in a molten salt comprising lithium chloride, potassium chloride, and an alkali metal fluoride to prepare a molten-salt electrolytic bath; and performing constant-current pulse electrolysis or constant-potential pulse electrolysis with a metal sheet, serving as a cathode, immersed in the molten-salt electrolytic bath under conditions of a pulse duration of from 0.1 seconds to 3.0 seconds and a duty ratio of from 0.5 to 0.94 to thereby form a silicon layer on the metal sheet.
A compound, which is a perfluoro(poly)ether group-containing silane compound of formula or: Rf-PFPE-X-SiR a 3 R a 3 Si-X-PFPE-X-SiR a 3 wherein PFPE is a group of the formula: -(OC 6 F 12) a -(OC 5 F 10) b -(OC 4 F 8) c -(OC 3 F 6) d -(OC 2 F 4) e -(OCF 2) f - wherein a to f each independently are an integer of 0-200, ( a + b + c + d + e + f) is ≥ 1, and the occurrence order of the repeating units in parentheses with the indices a-f is not limited; Rf is C 1-16 -alkyl optionally substituted with one or more F; X each independently is optionally substituted C 2-20 -alkylene; R a each independently is -Z-SiR 1 p R 2 q R 3 r, wherein Z each independently is O or a divalent organic group; R 1 each independently is R a ' which has the same definition as R a; the number of Si atoms linearly linked via Z group in R a is ≤ 5; R 2 each independently is OH or a hydrolyzable group; R 3 each independently is H or lower alkyl; p each independently is an integer of 0-3; q each independently is an integer of 0-3; and r each independently is an integer of 0-3; provided that (p+q+r) = 3 in each -Z-SiR 1 p R 2 q R 3 r, and two or more Si atoms having at least one R 2 are present in the formulae and. Rf is C 1-16 -alkyl optionally substituted with one or more F; X each independently is optionally substituted C 2-20 -alkylene; R a each independently is -Z-SiR 1 p R 2 q R 3 r, wherein Z each independently is O or a divalent organic group; R 1 each independently is R a ' which has the same definition as R a; the number of Si atoms linearly linked via Z group in R a is ≤ 5; R 2 each independently is OH or a hydrolyzable group; R 3 each independently is H or lower alkyl; p each independently is an integer of 0-3; q each independently is an integer of 0-3; and r each independently is an integer of 0-3; Z each independently is O or a divalent organic group; R 1 each independently is R a ' which has the same definition as R a; the number of Si atoms linearly linked via Z group in R a is ≤ 5; R 2 each independently is OH or a hydrolyzable group; R 3 each independently is H or lower alkyl; p each independently is an integer of 0-3; q each independently is an integer of 0-3; and r each independently is an integer of 0-3;
Vapour extraction device for a hob, which has an air inlet opening, via which air is sucked in downwards, and has at least one fan, wherein a liquid container for the collection of liquids which enter via the air inlet opening is retained beneath the air inlet opening in a detachable manner, the horizontal dimensions of the liquid container are smaller than the corresponding horizontal dimensions of the air inlet opening, the vapour extraction device has two fans, which are arranged in the vapour extraction device laterally offset in relation to the air inlet opening, and the liquid container is arranged between the two fans, characterised in that at least one part of the filter unit is retained in a detachable manner in the air inlet opening, the filter unit comprises at least one grease filter and at least one odour filter, the at least one grease filter is retained in a filter support, which is accommodated in the air inlet opening in a detachable manner, that the at least one odour filter is arranged adjacent to the at least one grease filter and is retained on a filter guide, the filter guide is a rail or a pair of rails which extend/extends horizontally beneath the air inlet opening and the filter guide has a greater width than the air inlet opening, the filter guide is mounted in a moveable manner or the at least one odour filter can be moved on a fixed filter guide, whereby one of the at least one odour filter can be brought into a position in each case, in which the odour filter lies beneath the air inlet opening and can be removed upwardly via the air inlet opening; the at least one odour filter is of a size which is smaller than the size of the air inlet opening, the liquid container is arranged beneath the filter unit and the liquid container has an inlet opening which is provided on the top side of the liquid container. at least one part of the filter unit is retained in a detachable manner in the air inlet opening, the filter unit comprises at least one grease filter and at least one odour filter, the at least one grease filter is retained in a filter support, which is accommodated in the air inlet opening in a detachable manner, that the at least one odour filter is arranged adjacent to the at least one grease filter and is retained on a filter guide, the filter guide is a rail or a pair of rails which extend/extends horizontally beneath the air inlet opening and the filter guide has a greater width than the air inlet opening, the filter guide is mounted in a moveable manner or the at least one odour filter can be moved on a fixed filter guide, whereby one of the at least one odour filter can be brought into a position in each case, in which the odour filter lies beneath the air inlet opening and can be removed upwardly via the air inlet opening; the at least one odour filter is of a size which is smaller than the size of the air inlet opening, the liquid container is arranged beneath the filter unit and the liquid container has an inlet opening which is provided on the top side of the liquid container.
Cylinder-piston assembly operated with an enclosed working gas which expands in a warmed cylinder chamber and contracts again in a relatively cold cylinder chamber in order to output volume change work to a piston which, on an end side, is operated with varying temperatures, and with a sealing point which seals off the translationally movable piston in the cylinder, characterized in that the piston is formed as a ceramic piston which comprises an axial piston section composed of a thermally insulating ceramic material, which faces toward the warmed cylinder chamber, and a piston section composed of a thermally conductive ceramic material, which is situated behind said piston section which faces toward the sealing point.
A printing device for printing on articles such as packagings, containers or bottles, comprising at least one print head, which, at least during a printing operation, is located in a defined relative position to a printing area on an article or container outer surface and which is coupled to a suction device for sucking off sprayed and/or splashed printing ink, wherein the suction device is spatially and functionally associated with the at least one print head, characterized in that the suction device can be subjected to variable and/or controllable or adjustable suction pressure.
A process for producing a multimodal polyethylene composition comprising the following steps: i) at least partially melting a first polyethylene resin having a viscosity average molecular weight Mv of equal to or more than 700 kg/mol to equal to or less than 10,000 kg/mol and a density of equal to or more than 920 kg/m 3 to equal to or less than 960 kg/m 3 in a first homogenizing device so that at least 20 wt% of the first polyethylene resin is melted when exiting the first homogenization device, ii) at least partially melting a second polyethylene resin having a Mw of equal to or more than 50 kg/mol to less than 500 kg/mol, and a density of equal to or more than 910 kg/m 3 to equal to or less than 960 kg/m 3 in a second homogenizing device with at least two feeding zones, the second feeding zone situated downstream of the first feeding zone, so that the second polyethylene resin introduced into the first feeding zone is at least partially melted before reaching the second feeding zone of the second homogenizing device, iii) combining the at least partially molten first polyethylene resin with the at least partially molten second polyethylene resin in said second homogenizing device, iv) compounding the combined first polyethylene resin and second polyethylene resin in said second homogenizing device to form a multimodal polyethylene composition, wherein the multimodal polyethylene composition has a melt flow rate MFR 5 (190°C, 5 kg) of 0.01 to 10.0 g/10 min and a density of equal to or more than 910 kg/m 3 to equal to or less than 970 kg/m 3 and the amount of the first polyethylene resin in the multimodal polyethylene composition is 0.5 to 50 wt% of the total polyethylene composition. i) at least partially melting a first polyethylene resin having a viscosity average molecular weight Mv of equal to or more than 700 kg/mol to equal to or less than 10,000 kg/mol and a density of equal to or more than 920 kg/m 3 to equal to or less than 960 kg/m 3 in a first homogenizing device so that at least 20 wt% of the first polyethylene resin is melted when exiting the first homogenization device, ii) at least partially melting a second polyethylene resin having a Mw of equal to or more than 50 kg/mol to less than 500 kg/mol, and a density of equal to or more than 910 kg/m 3 to equal to or less than 960 kg/m 3 in a second homogenizing device with at least two feeding zones, the second feeding zone situated downstream of the first feeding zone, so that the second polyethylene resin introduced into the first feeding zone is at least partially melted before reaching the second feeding zone of the second homogenizing device, iii) combining the at least partially molten first polyethylene resin with the at least partially molten second polyethylene resin in said second homogenizing device, iv) compounding the combined first polyethylene resin and second polyethylene resin in said second homogenizing device to form a multimodal polyethylene composition,
Fluid distribution and mixing device for a downflow catalytic reactor, said device comprising: - at least one collection zone comprising at least one collection means; - at least one essentially vertical collection duct that is able to receive a reaction fluid that is collected by said collection means and at least one injection means opening into said collection duct for injecting a quench fluid; - at least one mixing zone located downstream of said collection duct in the direction of circulation of the fluids, said mixing zone comprising at least one mixing enclosure for mixing the fluids, of length L1, said mixing zone comprising a first end in communication with said collection duct and a second end in communication with an exchange enclosure for exchange of the fluids, of length L2, located below said mixing enclosure, the length L2 of said exchange enclosure being strictly greater than the length L1 of said mixing enclosure so as to create a ceiling above said exchange enclosure, said ceiling comprising at least one opening that is suitable for the fluids to pass from said exchange enclosure towards a distribution zone; - at least one distribution zone located below the mixing zone, downstream of said mixing zone in the direction of flow of the fluids, said distribution zone comprising a distribution plate supporting a plurality of chimneys and a plurality of horizontal panels, located below the opening of the ceiling of the exchange enclosure, but above the chimneys or on the chimneys of the distribution plate of the distribution zone. - at least one collection zone comprising at least one collection means; - at least one essentially vertical collection duct that is able to receive a reaction fluid that is collected by said collection means and at least one injection means opening into said collection duct for injecting a quench fluid; - at least one mixing zone located downstream of said collection duct in the direction of circulation of the fluids, said mixing zone comprising at least one mixing enclosure for mixing the fluids, of length L1, said mixing zone comprising a first end in communication with said collection duct and a second end in communication with an exchange enclosure for exchange of the fluids, of length L2, located below said mixing enclosure, the length L2 of said exchange enclosure being strictly greater than the length L1 of said mixing enclosure so as to create a ceiling above said exchange enclosure, said ceiling comprising at least one opening that is suitable for the fluids to pass from said exchange enclosure towards a distribution zone; - at least one distribution zone located below the mixing zone, downstream of said mixing zone in the direction of flow of the fluids, said distribution zone comprising a distribution plate supporting a plurality of chimneys and a plurality of horizontal panels, located below the opening of the ceiling of the exchange enclosure, but above the chimneys or on the chimneys of the distribution plate of the distribution zone.
A blood sampling transfer device, comprising a transfer cartridge having a reservoir, characterized in that the blood sampling transfer device comprises a lancing tape having a flow channel; and a transfer cartridge removably connected to the lancing tape, wherein with the transfer cartridge connected to the lancing tape, the reservoir is in fluid communication with the flow channel, and wherein with the transfer cartridge disconnected from the lancing tape, a sealing wall provided between the lancing tape and the transfer cartridge seals the reservoir.
A method for assessing accuracy of process condition calculations in a system for controlling an industrial process the system comprising a transmitter and a process control workstation, the method being performed at the process control workstation and comprising: generating a process condition reference equation signal using a process condition reference equation and process control inputs; generating a process condition approximation equation that approximates the reference equation using the process control inputs; wherein the process condition approximation equation mimics routines which are performed by the transmitter; generating approximation equation coefficients for use by the process condition approximation equation; generating a process condition approximation equation signal based on the process condition approximation equation and the approximation equation coefficients; and comparing the process condition approximation equation signal to the process condition reference equation signal to generate an accuracy output signal that is used to adjust the system for controlling an industrial process. generating a process condition reference equation signal using a process condition reference equation and process control inputs; generating a process condition approximation equation that approximates the reference equation using the process control inputs; wherein the process condition approximation equation mimics routines which are performed by the transmitter; generating approximation equation coefficients for use by the process condition approximation equation; generating a process condition approximation equation signal based on the process condition approximation equation and the approximation equation coefficients; and comparing the process condition approximation equation signal to the process condition reference equation signal to generate an accuracy output signal that is used to adjust the system for controlling an industrial process.