mhurhangee/patent-ind-claim-en huggingface dataset:
A polypropylene composition comprising: (a) a first metallocene-catalyzed polypropylene (RPP-A) which is homopolymer, or a random copolymer of propylene and of a co-monomer; and (b) a second metallocene-catalyzed polypropylene (RPP-B) which is a random copolymer of propylene and of a co-monomer; wherein said polypropylene composition has: - a total co-monomer content of at least 1.1 % by weight relative to the total weight of said polypropylene composition, as determined by 13 C NMR analysis, said co-monomer being an alpha-olefin different from propylene; - a melting temperature T m of at least 130 °C, measured by DSC; - a crystallization temperature T c of at least 95.0 °C, measured by DSC; - a ratio of weight average molecular weight (M w ) to number average molecular weight (M n ) [M w /M n ] of at least 4.50; - a ratio of z-average molecular weight (M z ) to weight average molecular weight (M w ) [M z /M w ] of at least 2.10; and - a co-monomer distribution ratio R(M z )/R(M n ) higher than 0.995, wherein R(M z ) is the ratio at M z of the IR signal measured at 2959 cm -1 on the signal at 2928 cm -1 , and R(M n ) is the ratio at M n of the IR signal measured at 2959 cm -1 on the signal at 2928 cm -1 , as determined by IR-detected gel permeation chromatography; and - a xylene soluble content (XS) of at most 3.0 % by weight, wherein the XS is measured as defined in the description under test methods. (a) a first metallocene-catalyzed polypropylene (RPP-A) which is homopolymer, or a random copolymer of propylene and of a co-monomer; and (b) a second metallocene-catalyzed polypropylene (RPP-B) which is a random copolymer of propylene and of a co-monomer; - a total co-monomer content of at least 1.1 % by weight relative to the total weight of said polypropylene composition, as determined by 13 C NMR analysis, said co-monomer being an alpha-olefin different from propylene; - a melting temperature T m of at least 130 °C, measured by DSC; - a crystallization temperature T c of at least 95.0 °C, measured by DSC; - a ratio of weight average molecular weight (M w ) to number average molecular weight (M n ) [M w /M n ] of at least 4.50; - a ratio of z-average molecular weight (M z ) to weight average molecular weight (M w ) [M z /M w ] of at least 2.10; and - a co-monomer distribution ratio R(M z )/R(M n ) higher than 0.995, wherein R(M z ) is the ratio at M z of the IR signal measured at 2959 cm -1 on the signal at 2928 cm -1 , and R(M n ) is the ratio at M n of the IR signal measured at 2959 cm -1 on the signal at 2928 cm -1 , as determined by IR-detected gel permeation chromatography; and - a xylene soluble content (XS) of at most 3.0 % by weight, wherein the XS is measured as defined in the description under test methods.
A tubular welding wire , comprising: - a metallic sheath ; and - a granular core , wherein the metallic sheath made of low-carbon steel having a small number of inclusions comprises less than 0.1% carbon by weight, wherein the metallic sheath further comprises between 0.25% and 0.5% manganese by weight, less than 0.02% phosphorus or sulfur by weight, less than 0.04% silicon by weight, less than 0.05% aluminum by weight, less than 0.1% copper by weight, and less than 0.02% tin by weight, wherein the granular core is a metal core including one or more metals such as iron, iron titanium or iron silicon that provides at least a portion of a filler metal for a weld, wherein the granular core further comprises a carbon source, and a potassium source and other stabilizing and fluxing components, wherein the carbon source accounts for between 0.01% and 9.9% of the granular core by weight, wherein the total percentage of the combination of the carbon source and the potassium source together comprise less than 10% of the granular core by weight, wherein the potassium source is an agglomerate having between 22% and 25% potassium oxide by weight, between 10% and 18% silica by weight, between 38% and 42% titania by weight, and between 16% and 22% manganese oxide or manganese dioxide by weight, wherein the agglomerate accounts for 0.01% to 9.9% of the granular core by weight, and wherein the granular core accounts for between 5% and 20% of the total weight of the tubular welding wire . - a metallic sheath ; and - a granular core ,
Method for refurbishment of the coil end of the rotor of an electric generator for power generation in power plants, wherein the rotor to be refurbished has a rotatable rotor axis and one winding of several coils for each of the two poles of the rotor , wherein each coil in turn consists of several turns , wherein each turn has two sections parallel to the rotor axis and one substantially arc-shaped section in the region of each of the coil ends , and wherein single-piece half-turns consisting of one section parallel to the rotor axis and two, substantially partially circular sections in the region of the two coil ends are used, wherein the initial profile for the creation of these single-piece half-turns has the same profile width when viewed over the entire length, wherein parts of the turns which are not connected to one another as a single piece are connected to one another by soldering, wherein the two matching half-turns are soldered to one another in the region of the pole center in order to create the turn , characterized in that , after the old turns have been removed, they are replaced by new turns in such a way that, in some of the coils or in all of the coils , the substantially partially circular sections of the half-turns with respect to their profile width are reduced by material removal.
A bioreactor for the cultivation of mammalian cells characterised in that said bioreactor has a volume of at least 4000 l and one top impeller and one bottom impeller , wherein the top impeller is a three bladed hydrofoil design impeller and wherein the bottom impeller is a four pitched-bladed high solidity hydrofoil impeller, and wherein the hydrofoil impellers are down-flowing axial hydrofoil impellers, the impeller to tank diameter ratio is at least 0,44 and at most 0,46, the top impeller power number (N p ) is at least 0,1 and at most 0,9, the top impeller flow number (N q ) is at least 0,4 and at most 0,9, the bottom impeller power number (N p ) is at least 0,5 and at most 0,9, the bottom impeller flow number (N q ) is at least 0,50 and at most 0,85, the impeller spacing (D s ) is 1,229 x the diameter of the bottom impeller (D bottom ), the liquid height above the upper impeller (D o ) is at least 0,5 x the diameter of the top impeller (D top ) and at most 2,0 x D top , and the bottom clearance (D c ) is at least 0,35 x D bottom .
A rotor assembly for an electric machine , comprising - a body member , - a first shaft member , and - a second shaft member , the body member comprising an inner wall defining a cavity inside the body member , the first shaft member being inserted into the body member and extending at least partially in the cavity of the body member , the second shaft member being inserted into the body member and extending from a first end portion of the body member to a second end portion of the body member , the second shaft member being at least partially surrounded by the first shaft member , and the first shaft member being configured to provide a medium along the inner wall of the body member , wherein the second shaft member being configured to provide the medium at each of the first end portion and the second end portion of the body member , and characterized in that the rotor assembly further comprises a hub element configured to divide the medium before providing it in the first shaft member and the second shaft member, the hub element comprising a first shaft medium inlet and a second shaft medium inlet to provide the medium separately in the first shaft member and the second shaft member . - a body member , - a first shaft member , and - a second shaft member , the body member comprising an inner wall defining a cavity inside the body member , the first shaft member being inserted into the body member and extending at least partially in the cavity of the body member , the second shaft member being inserted into the body member and extending from a first end portion of the body member to a second end portion of the body member , the second shaft member being at least partially surrounded by the first shaft member , and the first shaft member being configured to provide a medium along the inner wall of the body member , wherein the second shaft member being configured to provide the medium at each of the first end portion and the second end portion of the body member , and characterized in that the rotor assembly further comprises a hub element configured to divide the medium before providing it in the first shaft member and the second shaft member, the hub element comprising a first shaft medium inlet and a second shaft medium inlet to provide the medium separately in the first shaft member and the second shaft member .
A blow molding apparatus comprising a supporting frame including a horizontal base ; a mold carriage assembly mounted to the base and movable in a path between an extruder station and a blow-fill station ; a mold carriage positioning drive operably associated with the mold carriage ; first and second adjacent mold assemblies in the mold carriage , each mold assembly comprising opposed mold halves together defining a mold cavity and being independently actuatable to open and close the mold cavity along said path; a mold actuator operably associated with each mold assembly for opening and closing the mold cavity; an extruder die head mounted to the frame above the extruder station for vertical reciprocal movement; a blow-and-fill head mounted to the frame above the blow-and-fill station ; and a controller operably associated with the mold carriage positioning drive for positioning the mold assemblies at the extruder station and the blow-and-fill station ; characterized in that each said mold assembly comprises a fixed mold half fixed to the mold carriage and a mold half movable along said path. a supporting frame including a horizontal base ; a mold carriage assembly mounted to the base and movable in a path between an extruder station and a blow-fill station ; a mold carriage positioning drive operably associated with the mold carriage ; first and second adjacent mold assemblies in the mold carriage , each mold assembly comprising opposed mold halves together defining a mold cavity and being independently actuatable to open and close the mold cavity along said path; a mold actuator operably associated with each mold assembly for opening and closing the mold cavity; an extruder die head mounted to the frame above the extruder station for vertical reciprocal movement; a blow-and-fill head mounted to the frame above the blow-and-fill station ; and a controller operably associated with the mold carriage positioning drive for positioning the mold assemblies at the extruder station and the blow-and-fill station ; characterized in that each said mold assembly comprises a fixed mold half fixed to the mold carriage and a mold half movable along said path.
A resource allocation method for a sidelink, executed by a terminal, characterized by comprising: obtaining a mapping relationship between a specific target of the sidelink and a logical channel prioritization, LCP, restriction parameter of the sidelink; and performing resource allocation of the sidelink according to the mapping relationship, wherein the specific target comprises: a quality of service, QoS, parameter or a logical channel. obtaining a mapping relationship between a specific target of the sidelink and a logical channel prioritization, LCP, restriction parameter of the sidelink; and performing resource allocation of the sidelink according to the mapping relationship, wherein the specific target comprises: a quality of service, QoS, parameter or a logical channel.
A cell-free method of producing closed linear deoxyribose nucleic acid (DNA) molecules comprising: (a) contacting a template comprising linear, double stranded DNA molecule covalently closed at each end by a portion of a protelomerase recognition sequence and comprising at least one stem loop motif with a strand-displacing polymerase under conditions promoting amplification of said template in the presence of at least one primer which is capable of binding specifically to a primer binding site within said stem loop motif; (b) contacting the DNA produced in (a) with at least one protelomerase under conditions promoting production of closed linear DNA. (a) contacting a template comprising linear, double stranded DNA molecule covalently closed at each end by a portion of a protelomerase recognition sequence and comprising at least one stem loop motif with a strand-displacing polymerase under conditions promoting amplification of said template in the presence of at least one primer which is capable of binding specifically to a primer binding site within said stem loop motif; (b) contacting the DNA produced in (a) with at least one protelomerase under conditions promoting production of closed linear DNA.
Method for preparing a butylene product , in which method a component mixture containing butane, butylene and hydrogen is provided using butane dehydrogenation to which a reaction feed containing butane and hydrogen is subjected, - wherein the component mixture or a portion thereof as a first separation feed is subjected to a first membrane separation by means of which a first permeate , which is enriched in hydrogen with respect to the first separation feed, and a first retentate , which is depleted in hydrogen with respect to the first separation feed and which contains hydrogen, butane and butylene, are formed, - wherein the first retentate or a portion thereof as a second separation feed is subjected to a second membrane separation in which a second permeate containing at least the predominant portion of the hydrogen of the second separation feed and a second retentate containing at least the predominant portion of the butane and of the butylene of the second separation feed are formed, - wherein the first membrane separation is carried out using a purge gas containing butane, and the first permeate is obtained as a permeate to which butane of the purge gas is supplied, and/or the second membrane separation is carried out using the purge gas containing butane and the second permeate is obtained as a permeate to which butane of the purge gas is supplied, - wherein the first permeate supplied with butane of the purge gas and/or the second permeate supplied with butane of the purge gas or one or more portions thereof is used in the formation of the reaction feed . - wherein the component mixture or a portion thereof as a first separation feed is subjected to a first membrane separation by means of which a first permeate , which is enriched in hydrogen with respect to the first separation feed, and a first retentate , which is depleted in hydrogen with respect to the first separation feed and which contains hydrogen, butane and butylene, are formed, - wherein the first retentate or a portion thereof as a second separation feed is subjected to a second membrane separation in which a second permeate containing at least the predominant portion of the hydrogen of the second separation feed and a second retentate containing at least the predominant portion of the butane and of the butylene of the second separation feed are formed, - wherein the first membrane separation is carried out using a purge gas containing butane, and the first permeate is obtained as a permeate to which butane of the purge gas is supplied, and/or the second membrane separation is carried out using the purge gas containing butane and the second permeate is obtained as a permeate to which butane of the purge gas is supplied, - wherein the first permeate supplied with butane of the purge gas and/or the second permeate supplied with butane of the purge gas or one or more portions thereof is used in the formation of the reaction feed .
Computer-implemented method for determining an optimum assignment of module types to an assembly line, having a first cycle time, selected with regard to its assembly capacity from a predefined set of assembly lines for assembling modules of these module types with components of one or more component types and to at least one remaining assembly line, having a second cycle time which differs from the first, from said set of assembly lines, comprising the following steps: a) ascertaining an expected production time for each module type of the modules to be assembled and for each assembly line, taking into consideration an acquired respective cycle time of the module type on the assembly lines and taking into consideration a parts number of modules to be assembled that is predefined per module type; b) assigning a set of module types of said set of module types to a predefined number of fixed-setup setup families containing respectively associated fixed setups , such that a module of a module type of a fixed-setup setup family is able to be assembled on the selected assembly line by way of components of component types of the fixed setup; c) optimizing the assignment from b), taking into consideration an external cycle time, such that, for all module types that are assigned to the fixed-setup setup families, the sum of the differences between the expected production time per module type, if it were to be assembled on one of the at least one remaining assembly lines with the minimum production time out of the at least one remaining assembly line, and the expected production time on the selected assembly line is maximized; and d) outputting the optimized assignment in a form suitable for controlling and/or for regulating the assembly of the modules. a) ascertaining an expected production time for each module type of the modules to be assembled and for each assembly line, taking into consideration an acquired respective cycle time of the module type on the assembly lines and taking into consideration a parts number of modules to be assembled that is predefined per module type; b) assigning a set of module types of said set of module types to a predefined number of fixed-setup setup families containing respectively associated fixed setups , such that a module of a module type of a fixed-setup setup family is able to be assembled on the selected assembly line by way of components of component types of the fixed setup; c) optimizing the assignment from b), taking into consideration an external cycle time, such that, for all module types that are assigned to the fixed-setup setup families, the sum of the differences between the expected production time per module type, if it were to be assembled on one of the at least one remaining assembly lines with the minimum production time out of the at least one remaining assembly line, and the expected production time on the selected assembly line is maximized; and d) outputting the optimized assignment in a form suitable for controlling and/or for regulating the assembly of the modules.
A device for sampling exhaled air of a patient, the device comprising: an endotracheal tube comprising a ventilation passageway, a proximal end to be connected to a connection hub and a distal end to be placed inside a patient oropharyngeal cavity; a sampling probe for sampling exhaled air of a patient, said sampling probe comprising a sampling conduit and being mounted within the endotracheal tube, wherein a proximal end of the sampling probe is adapted to be connected to a fluid analyser and a distal end is adapted to receive samples of exhaled air, such that the sampling probe is adapted to convey the samples to the fluid analyser, and wherein such distal end is placed at the distal end of the endotracheal tube , wherein the distal end of the sampling probe is arranged separate and away from the inner wall of the endotracheal tube and wherein an internal diameter of the sampling conduit is equal to or lower than 3 mm, characterized in that it further comprises a heating element to heat at least a portion of the sampling conduit, the heating element comprising a resistor coiled around the sampling conduit , wherein at least part of the heated portion of the sampling probe is configured to be placed inside the patient, wherein the maximum temperature of the portion of the sampling probe to be placed within the patient is between 37°C and 50°C. an endotracheal tube comprising a ventilation passageway, a proximal end to be connected to a connection hub and a distal end to be placed inside a patient oropharyngeal cavity; a sampling probe for sampling exhaled air of a patient, said sampling probe comprising a sampling conduit and being mounted within the endotracheal tube, wherein a proximal end of the sampling probe is adapted to be connected to a fluid analyser and a distal end is adapted to receive samples of exhaled air, such that the sampling probe is adapted to convey the samples to the fluid analyser, and wherein such distal end is placed at the distal end of the endotracheal tube , wherein the distal end of the sampling probe is arranged separate and away from the inner wall of the endotracheal tube and wherein an internal diameter of the sampling conduit is equal to or lower than 3 mm, characterized in that it further comprises a heating element to heat at least a portion of the sampling conduit, the heating element comprising a resistor coiled around the sampling conduit , wherein at least part of the heated portion of the sampling probe is configured to be placed inside the patient, wherein the maximum temperature of the portion of the sampling probe to be placed within the patient is between 37°C and 50°C.