mhurhangee/ep-ind-claims huggingface dataset:
A process for the preparation of an alkylene glycol from an alkene comprising steps of: (a) reacting the alkene with oxygen in the presence of a catalyst in a reactor to produce a gas composition comprising alkylene oxide, alkene, oxygen, carbon dioxide and water vapour; (b) supplying the gas composition from (a) to an alkylene oxide absorber, supplying lean absorbent to the alkylene oxide absorber, contacting the gas composition with lean absorbent in the absorber in the presence of one or more catalysts that promote hydrolysis and withdrawing fat absorbent from the absorber; (c) optionally supplying the fat absorbent to one or more reactor vessels; wherein conversion of alkylene oxide to alkylene glycol occurs in step (b) and optionally in step (c), such that the fat absorbent resulting from step (b) or step (c) comprises alkylene glycol; and further comprising steps of: (d) contacting the fat absorbent from step (b) or step (c) with a lean solvent, thereby extracting alkylene glycol from the fat absorbent and producing fat solvent; and (e) recovering alkylene glycol from the fat solvent, thereby producing lean solvent, and recycling the lean solvent to step (d). (a) reacting the alkene with oxygen in the presence of a catalyst in a reactor to produce a gas composition comprising alkylene oxide, alkene, oxygen, carbon dioxide and water vapour; (b) supplying the gas composition from (a) to an alkylene oxide absorber, supplying lean absorbent to the alkylene oxide absorber, contacting the gas composition with lean absorbent in the absorber in the presence of one or more catalysts that promote hydrolysis and withdrawing fat absorbent from the absorber; (c) optionally supplying the fat absorbent to one or more reactor vessels; (d) contacting the fat absorbent from step (b) or step (c) with a lean solvent, thereby extracting alkylene glycol from the fat absorbent and producing fat solvent; and (e) recovering alkylene glycol from the fat solvent, thereby producing lean solvent, and recycling the lean solvent to step (d).
Particulate filter for removing particles, carbon monoxide, hydrocarbons, and nitrogen oxides out of the exhaust gas of combustion engines operated with a stoichiometric air/fuel mixture, comprising a wall flow filter with length L and a coating Z, wherein the wall flow filter includes channels E and A which extend in parallel between a first and a second end of the wall flow filter and are separated by porous walls, which form surfaces O E or Oa, and wherein the channels E are closed at the second end and the channels A are closed at the first end, characterized in that coating Z is located in the porous walls and extends from the first end of the wall flow filter over the length L, and includes active aluminum oxide, at least two different cerium/zirconium/rare earth metal mixed oxides and at least one platinum group metal, and the first cerium/zirconium/rare earth metal mixed oxide is doped with yttrium oxide in addition to lanthanum oxide.
Laundry treatment appliance comprising a drum, at least one first layer having a noise-damping effect being arranged on an outer side of a casing of the drum, characterised in that the at least one first layer is designed as a strip formed from a chemically reactive polymer, the formation from the chemically reactive polymer bringing about an intimate and thus permanent connection between the first layer and the outer side of the casing of the drum.
A vitrectomy apparatus, comprising: a pressure source; a cut valve connected to the pressure source, the cut valve configured to be turned on and off to provide pressure to selectively extend and retract a vitrectomy cutting device; a sensor configured to sense pressure provided from the cut valve; and a controller configured to control operation of the cut valve based on pressure sensed by the sensor, wherein the cut valve is pneumatically connected to the sensor and electronically connected to the controller, and characterised by an accumulator configured to provide a specific amount of air pressure at a predetermined volume to the cut valve. a pressure source; a cut valve connected to the pressure source, the cut valve configured to be turned on and off to provide pressure to selectively extend and retract a vitrectomy cutting device; a sensor configured to sense pressure provided from the cut valve; and a controller configured to control operation of the cut valve based on pressure sensed by the sensor, wherein the cut valve is pneumatically connected to the sensor and electronically connected to the controller, and characterised by an accumulator configured to provide a specific amount of air pressure at a predetermined volume to the cut valve.
A radially anisotropic sintered magnet of annular shape having remanences, in which the remanences in radial direction of the annulus, measured at intervals of 45° in a circumferential direction of the annulus from one of the directions of magnetic fields applied during a shaping process which is assumed to be 0°, increase and decrease at intervals of 90° in the circumferential direction of the annulus, and the maximum of the measured remanence in radial direction over the entire circumference of the annulus is 0.95 to 1.60 T and the minimum of the measured remanence in radial direction over the entire circumference of the annulus is equal to 50 to 95% of the maximum, the radially anisotropic annular sintered magnet being manufactured by using an annular magnet compacting mold in which a core is at least partially made of a ferromagnetic material having a saturation magnetic flux density of at least 0.5 T, charging the mold cavity with a magnet powder, compacting the magnet powder while applying an orienting magnetic field according to the vertical compacting in horizontal magnetic field process, and sintering the resulting green compact, wherein the application of the orienting magnetic field comprises (i) a first operation comprising applying a magnetic field in one direction, then reversing the magnetic field-applying direction, and applying a magnetic field from the reverse direction, and after the first operation (ii) a second operation comprising applying a magnetic field in a direction orthogonal to said one direction of the first operation then reversing the magnetic field-applying direction, and applying a magnetic field from the reverse direction. (i) a first operation comprising applying a magnetic field in one direction, then reversing the magnetic field-applying direction, and applying a magnetic field from the reverse direction, and after the first operation (ii) a second operation comprising applying a magnetic field in a direction orthogonal to said one direction of the first operation then reversing the magnetic field-applying direction, and
A method for preparing soluble branched glucose polymers, characterised in that it comprises the succession of following steps: 1) bursting and solubilisation of a starch milk having an amylose content comprised between 35 and 80% by weight, and a dry matter comprised between 5 and 25%, 2) continuous addition of a glycogen branching enzyme extracted from thermophilic microorganisms, having an activity comprised between 25,000 U/ml and 60,000 U/ml, at a dose comprised between 800 and 2,500 U/g dry starch, at a temperature comprised between 60°C and 80°C, for a period of 12 to 18 hours, 3) optionally, treatment with an α-amylase type starch liquefaction enzyme having an activity comprised between 100 and 150 KNU/ml at a temperature of 95°C, a pH comprised between 5 and 8, for 30 to 60 minutes, preferably for 45 minutes, 4) purification of the soluble branched glucose polymers thus obtained by: - at least one step of treatment with activated carbon and/or with granular black carbon, - at least one sterilising filtration step, and - optionally at least one heat treatment step, 5) recovery of the soluble purified branched glucose polymers thus obtained. 1) bursting and solubilisation of a starch milk having an amylose content comprised between 35 and 80% by weight, and a dry matter comprised between 5 and 25%, 2) continuous addition of a glycogen branching enzyme extracted from thermophilic microorganisms, having an activity comprised between 25,000 U/ml and 60,000 U/ml, at a dose comprised between 800 and 2,500 U/g dry starch, at a temperature comprised between 60°C and 80°C, for a period of 12 to 18 hours, 3) optionally, treatment with an α-amylase type starch liquefaction enzyme having an activity comprised between 100 and 150 KNU/ml at a temperature of 95°C, a pH comprised between 5 and 8, for 30 to 60 minutes, preferably for 45 minutes, 4) purification of the soluble branched glucose polymers thus obtained by: - at least one step of treatment with activated carbon and/or with granular black carbon, - at least one sterilising filtration step, and - optionally at least one heat treatment step, - at least one step of treatment with activated carbon and/or with granular black carbon, - at least one sterilising filtration step, and - optionally at least one heat treatment step, 5) recovery of the soluble purified branched glucose polymers thus obtained.
Filling apparatus for filling containers with a filling product, having a product supply and a pre-filling chamber (14, 72), separable from the product supply, which comprises a controllable outlet, said filling apparatus having a movable sealing arrangement which in a closed position separates the product supply from the pre-filling chamber, wherein the sealing arrangement comprises a piston arrangement and with a displacer arrangement which projects or can be projected into the pre-filling chamber (14, 72), wherein the displacer arrangement comprises at least one elastically deformable wall or at least one wall section, and wherein the displacer arrangement is further operatively connected to a control means or control medium in such a way that, due to the elastic volume change of the displacer arrangement, the volume in the pre-filling chamber is variable and the product quantity which can be discharged via the outlet can be controlled, characterised in that the piston arrangement is configured as part of a double piston arrangement with an outer piston and an inner piston, which are arranged concentrically to one another and interact telescopically.
An inter-network change method, comprising: obtaining, by a terminal, second network slice information to which first network slice information is mapped in a procedure of registering or establishing a session with a first network, wherein the first network slice information is information about a first network slice accessed by the terminal and the first network slice is a network slice in the first network, wherein the second network slice information is information about a second network slice and the second network slice is a network slice in a second network; sending, by the terminal, a request message to the second network, wherein the request message carries the second network slice information, and the request message is used for the terminal to request to register with or be handed over to the second network slice; receiving, by the terminal, an accept message returned by the second network, wherein the accept message carries network slice information accepted by the second network, and the network slice information accepted by the second network comprises a part or all of the second network slice information; wherein the first network and the second network have different access network devices and/or core network devices; and wherein either the first network is fourth generation mobile communications system, 4G network and the second network is a fifth generation mobile communications system, 5G network or the first network is fifth generation mobile communications system, 5G network and the second network is a fourth generation mobile communications system, 4G network. obtaining, by a terminal, second network slice information to which first network slice information is mapped in a procedure of registering or establishing a session with a first network, wherein the first network slice information is information about a first network slice accessed by the terminal and the first network slice is a network slice in the first network, wherein the second network slice information is information about a second network slice and the second network slice is a network slice in a second network; sending, by the terminal, a request message to the second network, wherein the request message carries the second network slice information, and the request message is used for the terminal to request to register with or be handed over to the second network slice; receiving, by the terminal, an accept message returned by the second network, wherein the accept message carries network slice information accepted by the second network, and the network slice information accepted by the second network comprises a part or all of the second network slice information; wherein the first network and the second network have different access network devices and/or core network devices; and wherein either the first network is fourth generation mobile communications system, 4G network and the second network is a fifth generation mobile communications system, 5G network or the first network is fifth generation mobile communications system, 5G network and the second network is a fourth generation mobile communications system, 4G network.
A fire extinguisher, comprising: a source conduit; a flow control device connected to the source conduit; a supply conduit connected to the flow control device and fluidly coupled therethrough to the source conduit, wherein the supply conduit is thermally coupled to the source conduit via a heat exchanger to communicate heat between an expanded fire suppressant flow issued by the flow control device and a pressurized fire suppressant flow entering the flow control device; characterized in that the flow control device includes a nozzle or a valve separating the source conduit from the supply conduit; and/or the flow control device includes an orifice plate separating the source conduit from the supply conduit. a source conduit; a flow control device connected to the source conduit; a supply conduit connected to the flow control device and fluidly coupled therethrough to the source conduit, wherein the supply conduit is thermally coupled to the source conduit via a heat exchanger to communicate heat between an expanded fire suppressant flow issued by the flow control device and a pressurized fire suppressant flow entering the flow control device; characterized in that the flow control device includes a nozzle or a valve separating the source conduit from the supply conduit; and/or the flow control device includes an orifice plate separating the source conduit from the supply conduit.
A base station arranged to perform radio data communication with terminal devices (2a-2c) by using a plurality of bands (300a-300c) of which each has a data channel region (320a-320c) to which a data channel is assigned and a control channel region (310a-310c) to which a control channel (313a-313c) is assigned, the base station comprising: a control channel assigning unit arranged to assign a control channel at a location, the control channel corresponding to a data channel for the terminal device, and the location corresponding to a band to which the data channel assigned to the terminal device belongs, in the control channel region of a band for the terminal device; and a control channel transmitting unit arranged to transmit the control channel to the terminal device at the location assigned by the control channel assigning unit. a control channel assigning unit arranged to assign a control channel at a location, the control channel corresponding to a data channel for the terminal device, and the location corresponding to a band to which the data channel assigned to the terminal device belongs, in the control channel region of a band for the terminal device; and a control channel transmitting unit arranged to transmit the control channel to the terminal device at the location assigned by the control channel assigning unit.
A vacuum pump (1; 201) comprising an end pump stage (2; 214) which compresses against atmosphere; and a cooling apparatus (7; 207), wherein said vacuum pump has operating electronics (8; 208) for setting the cooling volume of the cooling apparatus (7; 207); and a temperature sensor (13; 213) connected to the operating electronics (8; 208), characterized in that a selection means (12; 212) configured as a switch is connected to the operating electronics (8; 208), which switch (12; 212) allows the setting and the selection of different operating modes of the operating electronics via its switching states, said operating modes differing by the temperature range to which the vacuum pump (1; 201) is adjusted by temperature control by the cooling apparatus (7; 207).
Wiper device for cleaning a vehicle window, with a wiper shaft and with a holding element, fastened on the wiper shaft, with an adapter element which is connected to the holding element and to which a wiper arm and a wiper blade arranged on the wiper arm are fastened, wherein the adapter element is mounted about a swivel axis arranged perpendicularly to the longitudinal axis of the wiper shaft, characterized in that between the holding element and the adapter element a detent connection is constructed, which in a first position arrests the adapter element with the wiper arm in a wiping position on the wiper shaft, and in a dismantling position enables a releasing of the adapter element with the wiper arm from the holding element.
A gas generant composition comprising: a nitrogen-containing organic compound which is guanidine nitrate in the range of not less than 40 weight% to not more than 60 weight%; an oxidizing agent which is a mixed oxidizing agent comprising basic copper nitrate in the range of not less than 1 weight% to not more than 30 weight%, and strontium nitrate in the range of not less than 15 weight% to not more than 50 weight%, and an additive in the range of not less than 0.5 weight% to not more than 10 weight%, the additive being a silane compound, a molding binder or a combustion adjustor, wherein a calorific value per mol of gas generated by combustion of the gas generant is not more than 125KJ. a nitrogen-containing organic compound which is guanidine nitrate in the range of not less than 40 weight% to not more than 60 weight%; an oxidizing agent which is a mixed oxidizing agent comprising basic copper nitrate in the range of not less than 1 weight% to not more than 30 weight%, and strontium nitrate in the range of not less than 15 weight% to not more than 50 weight%, and an additive in the range of not less than 0.5 weight% to not more than 10 weight%, the additive being a silane compound, a molding binder or a combustion adjustor, wherein a calorific value per mol of gas generated by combustion of the gas generant is not more than 125KJ.
Method for treatment of an organic slurry in which said slurry is supplied continuously at a flow rate q(m 3 /h), either directly or via a first enclosure maintained at a first given pressure (P 1), to a second enclosure (10, 33, 55) maintained at a second given mean pressure (P 2, P', P" 1, P" 2) while injecting air into said second enclosure (10, 33, 55) at a flow rate Q(Nm 3 /h) in order to obtain in said second enclosure (10, 33, 55) a first emulsion, forming a dispersed slurry phase in a continuous air phase which coats it, a given loss of pressure is created in said first emulsion by passing it, through one or two restrictions (15, 21, 38, 44) or through a supply valve, into a third enclosure (22, 43, 62) maintained at a third given pressure (P 4, P' 2, P" 3) in the zone situated immediately downstream of said restriction or restrictions or said valve, a flocculant (24, 45, 78) is injected into said zone of the third enclosure in order to form at the exit from treatment a second emulsion of air in the thickened flocculated slurry, then said second emulsion is degassed (46, 67) at atmospheric pressure before evacuation, said second emulsion is recovered in a filtration or decanting device (26, 48, 68), and it is filtered or decanted.
A clearing limit setting device comprising: a display section configured to display, in a two-dimensional field constituted by a length and a thickness of a yarn defect as coordinate axes, a clearing limit that is a boundary line that defines whether to remove a yarn defect from a yarn; a processing section configured to, when at least one first set-point is selected among a plurality of the first set-points (NSL1 to NSL6 and T1 to T4) through which the clearing limit passes and at least one second set-point is input as a movement destination of the selected at least one first set-point, generate a clearing limit that passes through the at least one second set-point instead of the selected at least one first set-point, and cause the display section to display the newly generated clearing limit; and a fourth input unit (51, 55) configured to accept deletion of at least one first set-point when the display section displays the clearing limit that passes through the first set-points (NSL1 to NSL6 and T1 to T4), wherein the processing section is configured to generate the clearing limit that passes through the first set-points other than the at least one first set-point deleted by the fourth input unit (51, 55) and causes the display section to display the newly generated clearing limit. a display section configured to display, in a two-dimensional field constituted by a length and a thickness of a yarn defect as coordinate axes, a clearing limit that is a boundary line that defines whether to remove a yarn defect from a yarn; a processing section configured to, when at least one first set-point is selected among a plurality of the first set-points (NSL1 to NSL6 and T1 to T4) through which the clearing limit passes and at least one second set-point is input as a movement destination of the selected at least one first set-point, generate a clearing limit that passes through the at least one second set-point instead of the selected at least one first set-point, and cause the display section to display the newly generated clearing limit; and a fourth input unit (51, 55) configured to accept deletion of at least one first set-point when the display section displays the clearing limit that passes through the first set-points (NSL1 to NSL6 and T1 to T4), wherein the processing section is configured to generate the clearing limit that passes through the first set-points other than the at least one first set-point deleted by the fourth input unit (51, 55) and causes the display section to display the newly generated clearing limit.
A pressure-sensitive adhesive composition, comprising: a binder resin; a nano clay modified with an organic modifier; and a solvent; wherein the nano clay modified with the organic modifier is comprised at 5 to 30 parts by weight relative to 100 parts by weight of the binder resin; and the binder resin is a polyisobutylene resin. a binder resin; a nano clay modified with an organic modifier; and a solvent; wherein the nano clay modified with the organic modifier is comprised at 5 to 30 parts by weight relative to 100 parts by weight of the binder resin; and the binder resin is a polyisobutylene resin.