mhurhangee/ep-ind-claims huggingface dataset:
A method of milling a fuel for an oxy-fuel combustion burner, the method comprising: separating air into a hot nitrogen gas stream, having a temperature of at least 150°C and a purity of at least 98 mol-% nitrogen, and an oxygen gas stream; leading at least a part of the nitrogen gas stream to a fuel mill for drying the fuel within the mill; milling the fuel by means of the fuel mill in a nitrogen rich atmosphere formed by means of the nitrogen gas stream; leading the oxygen gas stream to the oxy-fuel combustion burner; conveying the milled fuel to the oxy-fuel combustion burner; and burning the fuel to form a flue gas, by means of the oxy-fuel combustion burner, in an oxygen rich atmosphere formed by means of the oxygen gas stream, combining the nitrogen gas stream with recycled flue gas from downstream of the burner to form the mill, and optionally an additional dryer atmosphere, such that heat from the burner and fuel combustion is used for drying the fuel; and leading the at least a part of the nitrogen gas stream and the recycled flue gas away from the milled fuel. separating air into a hot nitrogen gas stream, having a temperature of at least 150°C and a purity of at least 98 mol-% nitrogen, and an oxygen gas stream; leading at least a part of the nitrogen gas stream to a fuel mill for drying the fuel within the mill; milling the fuel by means of the fuel mill in a nitrogen rich atmosphere formed by means of the nitrogen gas stream; leading the oxygen gas stream to the oxy-fuel combustion burner; conveying the milled fuel to the oxy-fuel combustion burner; and burning the fuel to form a flue gas, by means of the oxy-fuel combustion burner, in an oxygen rich atmosphere formed by means of the oxygen gas stream, combining the nitrogen gas stream with recycled flue gas from downstream of the burner to form the mill, and optionally an additional dryer atmosphere, such that heat from the burner and fuel combustion is used for drying the fuel; and leading the at least a part of the nitrogen gas stream and the recycled flue gas away from the milled fuel.
A fluid pump comprising a housing receiving a camshaft which is rotatable within rotational guiding means (38a, 38b), the camshaft cooperating with a pumping plunger of the fluid pump to actuate the pumping plunger to reciprocally move in order to pressurize fluid within a pump chamber, the camshaft being exposed to a fluid to lubricate the camshaft, in use, wherein the camshaft is provided with an integral fluid damper comprising a bellows configured to damp hydraulic waves propagating in the fluid lubricating the camshaft and flowing through the rotational guiding means (38a, 38b) and characterized in that the camshaft is partially hollow, and wherein the bellows is arranged inside the hollow part.
Method for the vacuum distillation of a hydrocarbon feedstock comprising the following steps: - heating the feedstock; - introducing the feedstock into a flash zone of a vacuum distillation column; - removing at least one distillate stream (58, 64, 70) at an intermediate level (N3, N4, N5) from the vacuum distillation column; - withdrawing a column head stream at the head of the vacuum distillation column; - partially condensing the column head stream to recover a liquid flow and a gaseous flow; - passing the gaseous flow through a vacuum generation unit and recovering at least one condensate (86, 90, 96) and a gaseous fraction of non-condensable gas; the method comprising introducing into the vacuum distillation column a flow of a feedstock-stripping fluid, characterized in that the stripping fluid consists of a hydrocarbon mixture having a weighted average boiling temperature (Tmav) of between 150°C and 250°C, preferably between 190°C and 210°C. - heating the feedstock; - introducing the feedstock into a flash zone of a vacuum distillation column; - removing at least one distillate stream (58, 64, 70) at an intermediate level (N3, N4, N5) from the vacuum distillation column; - withdrawing a column head stream at the head of the vacuum distillation column; - partially condensing the column head stream to recover a liquid flow and a gaseous flow; - passing the gaseous flow through a vacuum generation unit and recovering at least one condensate (86, 90, 96) and a gaseous fraction of non-condensable gas; the method comprising introducing into the vacuum distillation column a flow of a feedstock-stripping fluid, characterized in that the stripping fluid consists of a hydrocarbon mixture having a weighted average boiling temperature (Tmav) of between 150°C and 250°C, preferably between 190°C and 210°C.
An echogenically enhanced interventional device comprising: (a) an interventional device to be imaged ultrasonically; and (b) an echogenic polymeric sleeve with adjustable topography positioned adjacent to the interventional device; wherein topography of the polymeric sleeve is adjusted by changing length of the polymeric sleeve with respect to the interventional device; and wherein adjustment by changing length of the polymeric sleeve with respect to the interventional device is reversible. (a) an interventional device to be imaged ultrasonically; and (b) an echogenic polymeric sleeve with adjustable topography positioned adjacent to the interventional device;
A method comprising: forming a reformable epoxy resin material into a weavable yarn free of any phenoxy-containing material, wherein the reformable epoxy resin material includes a difunctional epoxy resin component and an amine component; stitching a multiaxial fabric with the weavable yarn; forming an epoxy laminate with the multiaxial fabric; and blending the weavable yarn into the epoxy-based material upon heating. forming a reformable epoxy resin material into a weavable yarn free of any phenoxy-containing material, wherein the reformable epoxy resin material includes a difunctional epoxy resin component and an amine component; stitching a multiaxial fabric with the weavable yarn; forming an epoxy laminate with the multiaxial fabric; and blending the weavable yarn into the epoxy-based material upon heating.
A method for treating a subterranean region (14, 114), comprising: running a tubular string (22, 122) comprising a plurality of sealed fluid ports (36, 136) distributed along its length through an upper lined wellbore section and into a lower drilled bore section (12, 112) which intercepts a subterranean region, wherein the lower drilled bore section (12, 112) includes a first fluid (37, 137); providing fluid communication between the tubular string (22, 122) and an annulus (26, 126) defined between the tubular string (22, 122) and a wall of the bore via a displacement port (32, 132) in a lower end region of the tubular string (22, 122); delivering a second fluid into the lower drilled bore section via one of the annulus (26, 126) and the tubular string (22, 122) to displace the first fluid from the annulus (26, 126); subsequently opening at least one of the sealed fluid ports (36, 136; and delivering a treating fluid through the tubular string (22, 122) and into the annulus via the at least one opened fluid port (36, 136) to treat the subterranean region, wherein at least one fluid port is opened by a chemical activation using at least one of the second fluid and the treating fluid. running a tubular string (22, 122) comprising a plurality of sealed fluid ports (36, 136) distributed along its length through an upper lined wellbore section and into a lower drilled bore section (12, 112) which intercepts a subterranean region, wherein the lower drilled bore section (12, 112) includes a first fluid (37, 137); providing fluid communication between the tubular string (22, 122) and an annulus (26, 126) defined between the tubular string (22, 122) and a wall of the bore via a displacement port (32, 132) in a lower end region of the tubular string (22, 122); delivering a second fluid into the lower drilled bore section via one of the annulus (26, 126) and the tubular string (22, 122) to displace the first fluid from the annulus (26, 126); subsequently opening at least one of the sealed fluid ports (36, 136; and delivering a treating fluid through the tubular string (22, 122) and into the annulus via the at least one opened fluid port (36, 136) to treat the subterranean region, wherein at least one fluid port is opened by a chemical activation using at least one of the second fluid and the treating fluid.
An electro impedance measuring belt for placing electrodes around the thorax of a patient comprising, - an array of a plurality of spaced apart electrodes, and - a support structure, on which the electrodes are arranged, wherein the support structure with the electrode array comprises two angulated legs (31, 31') on which the electrodes are lined up, characterized in that, the two legs spread out from an apex at an angle, such that, when the belt is put around the thorax of a patient, the array of electrodes extends from the back of the patient, where the apex of the angulated legs is to be located, essentially parallel to the ribs to the lower part of the breastbone of the patient. - an array of a plurality of spaced apart electrodes, and - a support structure, on which the electrodes are arranged,
An aqueous composition comprising latex polymer particles that comprise (a) 40% to 95%, by weight based on the dry weight of the latex polymer, a core polymer that comprises (i) 95% to 100% by weight, based on the dry weight of the core polymer, polymerized units of one or more monofunctional vinyl monomers, and (ii) 0% to 5% by weight, based on the dry weight of the core polymer, polymerized units of one or more multivinyl monomers, wherein the core polymer has a glass transition temperature of 50°C or lower; determined by differential scanning calorimetry according to test method ASTM D7426-08 and (b) 5% to 60%, by weight based on the dry weight of the latex polymer, a shell polymer that comprises (i) 35% to 95% by weight, based on the dry weight of the shell polymer, polymerized units of one or more monofunctional vinyl monomers, and (ii) 5% to 65% by weight, based on the dry weight of the shell polymer, polymerized units of one or more vinyl monomers having trialkoxysilyl groups, wherein the shell polymer contains a total of all monomers other than alkyl (meth)acrylates, styrene, and vinyl monomers having trialkoxysilyl groups, in an amount by weight, based on the dry weight of the shell polymer, of 0 to 3%. (a) 40% to 95%, by weight based on the dry weight of the latex polymer, a core polymer that comprises (i) 95% to 100% by weight, based on the dry weight of the core polymer, polymerized units of one or more monofunctional vinyl monomers, and (ii) 0% to 5% by weight, based on the dry weight of the core polymer, polymerized units of one or more multivinyl monomers, wherein the core polymer has a glass transition temperature of 50°C or lower; determined by differential scanning calorimetry according to test method ASTM D7426-08 and (i) 95% to 100% by weight, based on the dry weight of the core polymer, polymerized units of one or more monofunctional vinyl monomers, and (ii) 0% to 5% by weight, based on the dry weight of the core polymer, polymerized units of one or more multivinyl monomers, (b) 5% to 60%, by weight based on the dry weight of the latex polymer, a shell polymer that comprises (i) 35% to 95% by weight, based on the dry weight of the shell polymer, polymerized units of one or more monofunctional vinyl monomers, and (ii) 5% to 65% by weight, based on the dry weight of the shell polymer, polymerized units of one or more vinyl monomers having trialkoxysilyl groups, wherein the shell polymer contains a total of all monomers other than alkyl (meth)acrylates, styrene, and vinyl monomers having trialkoxysilyl groups, in an amount by weight, based on the dry weight of the shell polymer, of 0 to 3%. (i) 35% to 95% by weight, based on the dry weight of the shell polymer, polymerized units of one or more monofunctional vinyl monomers, and (ii) 5% to 65% by weight, based on the dry weight of the shell polymer, polymerized units of one or more vinyl monomers having trialkoxysilyl groups, wherein the shell polymer contains a total of all monomers other than alkyl (meth)acrylates, styrene, and vinyl monomers having trialkoxysilyl groups, in an amount by weight, based on the dry weight of the shell polymer, of 0 to 3%.
Method for measuring the soot load in an exhaust gas system of a diesel engine using a sensor, connected downstream of a particle filter and having a sensor element, as a measure of the functional capability of the particle filter, in which the soot load is measured resistively or capacitively using a sensor element, wherein electrodes are formed on the sensor element and a measurement voltage is applied between the electrodes, characterized in that the measurement voltage which is applied between the electrodes is controlled as a function of at least one instantaneous operating parameter of the diesel engine.
A heat transfer composition comprising: (a) from about 60% to about 70% by weight of HFC-32; (b) from about 20% to less than about 40% by weight of HFO-1234ze; and (c) from greater than about 0% to about 10% by weight of a compound selected from the group consisting of n-butane, isobutane and combinations thereof, provided that the amount of component (c) is effective to improve one or more of the composition's glide; heating capacity, cooling capacity, heating efficiency, cooling efficiency; and/or discharge temperature, as compared to compositions lacking component (c). (a) from about 60% to about 70% by weight of HFC-32; (b) from about 20% to less than about 40% by weight of HFO-1234ze; and (c) from greater than about 0% to about 10% by weight of a compound selected from the group consisting of n-butane, isobutane and combinations thereof,
Method for conditioning a plastic, wherein the method comprises the following steps: conveying a mixture of an auxiliary and the plastic into an excitation zone of a conditioning apparatus; melting the plastic; and exciting the auxiliary and the plastic in the excitation zone, in order to form a plasma for conditioning the plastic, wherein the auxiliary is excited as an auxiliary outgassing from the plastic, as a liquid auxiliary or as an auxiliary mixed with the plastic. conveying a mixture of an auxiliary and the plastic into an excitation zone of a conditioning apparatus; melting the plastic; and exciting the auxiliary and the plastic in the excitation zone, in order to form a plasma for conditioning the plastic, wherein the auxiliary is excited as an auxiliary outgassing from the plastic, as a liquid auxiliary or as an auxiliary mixed with the plastic.
A forwarding entry monitoring method, comprising: determining, by a first node, a to-be-monitored data stream; determining, by the first node, that a forwarding entry stored on the first node has changed, wherein the forwarding entry is used to forward the data stream; and sending, by the first node, a first packet to a second node, wherein the second node is located on a transmission path of the data stream, the second node is a previous-hop node of the first node, and the first packet carries a change indication, wherein the determining, by a first node, a to-be-monitored data stream comprises: receiving, by the first node, a second packet from the second node through the transmission path of the data stream, wherein the second packet is used to obtain status information of the forwarding entry, and the status information indicates whether the forwarding entry has changed; and determining, by the first node, the data stream based on a parameter carried in the second packet. determining, by a first node, a to-be-monitored data stream; determining, by the first node, that a forwarding entry stored on the first node has changed, wherein the forwarding entry is used to forward the data stream; and sending, by the first node, a first packet to a second node, wherein the second node is located on a transmission path of the data stream, the second node is a previous-hop node of the first node, and the first packet carries a change indication, wherein the determining, by a first node, a to-be-monitored data stream comprises: receiving, by the first node, a second packet from the second node through the transmission path of the data stream, wherein the second packet is used to obtain status information of the forwarding entry, and the status information indicates whether the forwarding entry has changed; and determining, by the first node, the data stream based on a parameter carried in the second packet. receiving, by the first node, a second packet from the second node through the transmission path of the data stream, wherein the second packet is used to obtain status information of the forwarding entry, and the status information indicates whether the forwarding entry has changed; and determining, by the first node, the data stream based on a parameter carried in the second packet.
A method of checking a configuration parameter value set at an electronically configurable apparatus, wherein the apparatus has a user interface having a display device and is an industrial machine which is configured to be operated in dependence on the set configuration parameter value; wherein the user interface is configured to display a set configuration parameter value using a web browser for presenting data at the display device; and wherein the method comprises: - displaying at least a first version of the set configuration parameter value using a first presentation form of the web browser, wherein the first version represents the set configuration parameter value in a first data form; - generating a second version of the set configuration parameter value, which is different from the first version, on the basis of the first version; - displaying the second version of the set configuration parameter value using a second presentation form of the web browser, wherein the second version represents the set configuration parameter value in a second data form; and - checking the set configuration parameter value on the basis of the first version and at least of the second version, wherein the second version is generated in that the first version is converted into the second version using a conversion program; wherein the conversion program is configured to convert the data from the first data form into the second data form; and wherein the conversion program is independent of the web browser and is not a component thereof. - displaying at least a first version of the set configuration parameter value using a first presentation form of the web browser, wherein the first version represents the set configuration parameter value in a first data form; - generating a second version of the set configuration parameter value, which is different from the first version, on the basis of the first version; - displaying the second version of the set configuration parameter value using a second presentation form of the web browser, wherein the second version represents the set configuration parameter value in a second data form; and - checking the set configuration parameter value on the basis of the first version and at least of the second version,
A stent graft system having a first stent graft, expandable in diameter, and at least one second stent graft, wherein at least regions of the first stent graft have a hose-shaped mesh structure which in an expanded mode has a mesh structure with substantially circular, annular loops, wherein the at least second stent graft has outwards projecting barbs at a distal end via which the at least second stent graft can be coupled to the first stent graft in the expanded mode, characterized in that the distal end of the at least second stent graft penetrates a circular, annular loop of corresponding diameter and engages the circular, annular loop with the respective outwards projecting barbs.
A method implemented by a long term evolution, LTE, wireless transmit receive unit, WTRU, accessing a contention-based shared channel, and accessing a contention-free shared channel allocated by receiving an uplink grant for the WTRU from a base station, the method characterized by: receiving radio resource control, RRC, signaling that indicates resources for the CB shared channel; wherein the CB shared channel is selected autonomously by the WTRU from the resources indicated in the received RRC signaling; and on a condition that an uplink grant is received, in a random access response, for a subframe in which a transmission using the CB shared channel would occur, not transmitting using the CB shared channel in the subframe and transmitting using the contention-free shared channel using the uplink grant received in the random access response. receiving radio resource control, RRC, signaling that indicates resources for the CB shared channel; wherein the CB shared channel is selected autonomously by the WTRU from the resources indicated in the received RRC signaling; and on a condition that an uplink grant is received, in a random access response, for a subframe in which a transmission using the CB shared channel would occur, not transmitting using the CB shared channel in the subframe and transmitting using the contention-free shared channel using the uplink grant received in the random access response.
A bi-directional flow meter comprising a sampling tube through which fluid may flow and a sensor arrangement, wherein the sampling tube comprises a first hollow section having a first internal cross-sectional area and a second hollow section having a second internal cross-sectional area being less than the first internal cross-sectional area; wherein the hollow interior of the sampling tube is longitudinally symmetric and is profiled to present a constriction defining a sampling section which is in communication within a first and second development section (51, 53) via a first and second transition section (55, 57); wherein the sensor arrangement is for measuring the difference between stagnation and static pressures within the constriction of the second hollow section; wherein the sensor arrangement comprises one or more stagnation pressure measurement ports (25, 27) located within the second hollow section adjacent to one or more static pressure measurement ports (29, 31); and the or each static pressure measurement port (29, 31) is located at the same longitudinal position within the sampling tube as the or each adjacent stagnation pressure measurement port (25, 27).