899 results about "Separation system" patented technology

This invention discloses a supercritical carbon dioxide cycle generator set water spray desuperheating system, comprising a supercritical carbon dioxide cycle power generation system and a water spray desuperheating system; the supercritical carbon dioxide cycle power generation system includes a heater, a screen-type superheater, a final-stage superheater, and a turbine; the water spray desuperheating system includes a first desuperheating water injection point, a second desuperheating water injection point, and a liquid-water separation system; the heater outlet is sequentially connected to the turbine inlet via the first desuperheating water injection point, the screen-type superheater, the second desuperheating water injection point, and the final-stage superheater; the turbine outlet is connected to the inlet of the liquid-water separation system; the liquid outlet of the liquid-water separation system is connected to the first and second desuperheating water injection points; and the gas outlet of the liquid-water separation system is connected to the heater inlet. This system can solve various problems caused by carbon dioxide desuperheating.

A centrifugal separation system includes a centrifugal separator, a liquid feed mixture conduit, a light phase conduit, a heavy phase conduit, and a flow control system. The flow control system includes a controller, a flow control valve arranged in a light phase conduit, a liquid feed mixture measuring device, and at a light phase measuring device and / or a heavy phase measuring device. The controller is configured to control the flow control valve based on measurements from the liquid feed mixture measuring device and measurements from the light phase measuring device and / or the heavy phase measuring device.

The invention provides an easy-to-scale efficient biological magnetic separation system and method and application. The magnetic separation method comprises the following steps: marking a target object in a to-be-detected suspension by adopting magnetic nanoparticles, and putting the marked to-be-detected suspension into a separation container; a modularized magnet array is arranged in the separation container, the modularized magnet array is composed of permanent magnets, and the permanent magnets are assembled into the cuboid modularized magnet array; the surface of the permanent magnet is coated with a polytetrafluoroethylene coating; the modularized magnet array moves in the suspension under the control of a driving magnet arranged outside the separation container to generate a dynamic gradient magnetic field, and a target object is captured by the modularized magnet array under the action of the gradient force of the magnetic field; removing the liquid in the separation container; adding the resuspension into a separation container, and recovering a target object by physical ultrasonic washing; or adding a chemical dissociation solution into the separation container to recover the target object.

The invention discloses a passion fruit pulp separation system and method, and belongs to the technical field of agricultural product processing. The system aims to solve the technical problems of incomplete separation of pulp and peel, more pulp residues, low yield, low efficiency and the like in the traditional modes of manual digging, mechanical scraping or hydraulic impact and the like. Comprising a discharging channel through which passion fruits pass one by one; the puncturing and stirring unit is arranged on the side of the discharging channel and comprises a puncturing rod piece, a stirring part arranged on the puncturing rod piece in a sleeving mode, a vibration mechanism for driving the puncturing rod piece to generate high-frequency micro vibration, a rotating mechanism for driving the puncturing rod piece to rotate and a puncturing movement mechanism for driving the whole puncturing rod piece to do linear reciprocating motion. The stirring part is configured to be radially expanded into an expanded structure from a folded state under the action of centrifugal force; and a cutting unit disposed downstream. The system is mainly used for realizing efficient and automatic separation of passion fruit pulp, remarkably improves the pulp yield and the seed integrity rate, and is suitable for deep processing processes such as subsequent pulp freeze-drying.

The invention discloses a method for separating an egg white polypeptide chain by adopting a coupling membrane, and particularly relates to the field of egg white polypeptide chains, the method comprises the following steps: S1, mixing fresh egg white with a buffer solution, adjusting the initial acid-base environment and initial temperature of a system, and measuring key basic parameters after dispersion treatment; s3, introducing the pretreated egg white liquid into a first-stage membrane assembly, monitoring separation process parameters, obtaining interception efficiency, dynamically adjusting operation parameters, and enabling permeate liquid to enter a second-stage membrane assembly; s7, monitoring system environment parameters and polypeptide activity, obtaining an activity retention rate, dynamically adjusting supply parameters, and maintaining the polypeptide activity; s8, classifying and collecting products according to molecular weight intervals, evaluating comprehensive separation efficiency, completing separation and verifying product indexes; by constructing an ultrafiltration membrane-nanofiltration membrane-reverse osmosis membrane three-stage coupling separation system and combining a dynamic parameter adjustment mechanism based on interception efficiency, separation selectivity and refined purity, the purity and separation efficiency of a polypeptide product are remarkably improved.

The invention discloses a method for treating gangue through paste-slurry combined filling under the condition of a cut-off type roof, which specifically comprises the following steps: obtaining the yield and particle size distribution of mine gangue according to a product balance table for guiding a paste filling system, an underground coal gangue separation system and a slurry filling system; filling spacing is dynamically adjusted according to the lithology of the roof, the filling spacing is determined by controlling the number of intervals of the supports, it is guaranteed that a paste roof-contacted supporting roof rock stratum collapses, and a stable slurry filling space is constructed; gangue in a ground gangue bin enters a slurry filling system and automatically flows to a slurry pump to be pumped to the position above a working face along a filling pipeline, vertical drilling is constructed in an underground goaf to the position above a slurry filling space, and the filling pipeline is arranged to complete filling; the large-scale disposal of all gangues above and below the mine is completed according to continuous and sequential circulation of mine excavation. By means of paste-slurry filling combined operation, all underground filling treatment of underground gangue solid waste of the million-ton level is achieved, support to a top plate is reinforced through paste-slurry combination, and mine pressure is effectively weakened.

The invention relates to an audio-visual voice separation system and method based on a joint cross attention mechanism and iterative modeling, and the system comprises an audio-visual coding module which is used for collecting audio-visual data, and obtaining audio features and visual features through the audio-visual data; the feature refining module is used for optimizing the audio features and the visual features respectively to obtain audio embedding and visual embedding; the multi-modal information fusion module is used for carrying out feature fusion on audio embedding and visual embedding to generate modal fusion features; the separation module is used for carrying out iterative optimization on the modal fusion features and the audio features, and in the iterative optimization process, carrying out multi-scale feature extraction and down-sampling operation on a last iterative optimization result in sequence, so as to carry out addition operation on the multi-scale features and the down-sampling features, and to obtain a multi-scale feature extraction result and a down-sampling feature extraction result; further extracting intra-frame and inter-frame information and adaptive feature modulation, and generating a target feature mask; and the audio coding module is used for reconstructing an estimated voice waveform by using the target feature mask.

The utility model relates to the technical field of dry grinding and dry separation of iron ore and similar processes, and particularly discloses a dry grinding and dry separation system which comprises an incoming material conveying system, a roller mill, a dynamic powder concentrator, a dry classification cabin and a fine powder collecting and conveying system. A discharging hole of the supplied material conveying system is communicated with a feeding hole of the roller mill; a discharging hole of the roller mill is communicated with a feeding hole of the dynamic powder concentrator; a coarse particle material outlet of the dynamic powder concentrator is communicated with a material inlet of the dry type grading cabin; an oversize coarse particle discharging opening of the dry type grading cabin is communicated with a feeding opening of the roller mill; and a fine powder discharge hole of the dynamic powder concentrator is communicated with the fine powder collecting and conveying system. Finished product materials with various particle sizes can be provided, and the requirements of customers for different finished product particle sizes are met; fine powder screened by the dynamic powder concentrator is collected by a dust collector and then is directly conveyed to a tailing discarding procedure, so that the handling capacity of the dry classification cabin is reduced; the use condition of the dry-type grading cabin is optimized, and the system flow is simplified.

The invention relates to the technical field of washing water treatment, and discloses a gradient type oil-solid and water pure physical separation system and method for MTO washing water.The separation system comprises a liquid inlet pipe, a liquid inlet valve and a liquid inlet pump are installed on the liquid inlet pipe, and a secondary deslagging system, a secondary oil-water separation system and a buffer water storage tank are sequentially connected to the liquid inlet pipe in the liquid inlet direction; a liquid level sensor and a backwashing system are mounted on the buffer water storage tank; the backwashing system is sequentially communicated with the secondary deslagging system and the secondary oil-water separation system; a buffer flow guide mechanism is installed at the liquid inlet end of the second-stage deslagging system, and a stepped filler assembly is installed in the second-stage deslagging system. A physical gradient separation process is adopted, step-by-step accurate removal from macroscopic particles to microscopic emulsified oil and efficient recovery of oil phase components in wastewater can be realized, the turbidity and solid content indexes of effluent are remarkably improved, and long-period continuous stable operation can be realized.

The utility model relates to a bucket type sedimentation tank, including barrel, mud-water separation plate, water inlet pipe, deslagging pipe and water outlet pipe, the mud-water separation plate is bucket-shaped and has a first big mouth end and a first small mouth end, a plurality of mud-water separation plates are arranged in the barrel at intervals along the first direction to form a mud-water separation zone, the first big mouth end is spaced apart from the inner wall surface of the barrel, and the first small mouth end is spaced apart from the inner wall surface of the barrel. The water inlet pipe comprises a connecting section and a water distribution section which are connected, the connecting section is arranged on the barrel, the water distribution section is arranged in the first small opening ends of the mud-water separation plates in a penetrating mode, the water distribution section faces the end of the barrel, and a plurality of water distribution openings are formed in the water distribution section at intervals and located in the mud-water separation area; and at least one water distribution opening is correspondingly formed between every two adjacent mud-water separation plates. According to the bucket type sedimentation tank disclosed by the utility model, mud-water separation is realized by adopting central multi-point water feeding and bucket type sedimentation, so that the uniform water distribution capability is improved, the disturbance to a sedimentation area is reduced, the mud-water separation effect is improved, and the problem that a mud-water separation system in the related technology occupies a large area is solved.

Systems and methods are disclosed for automated method parameter configuration for differential mobility separations. As non-limiting examples, various aspects of this disclosure provide receiving a sample in an open port interface; transferring the sample to an ionization source; ionizing the transferred sample; introducing the ionized sample into a mass spectrometer; mass analyzing the ionized sample to produce an initial mass analysis result; determining a peak width of the initial mass analysis result; and determining a dwell time for subsequent measurements based on the determined peak width, a pre-defined number of data points across subsequent mass analysis peak widths, and a number of different analytes to be assessed for the sample. The sample may be diluted and transferred to the ionization source by a sample introduction apparatus selected from a group including an acoustic droplet ejector (ADE), a pneumatic ejector, a piezoelectric ejector, and a hydraulic ejector.

The invention relates to the technical field of ammonium dihydrogen phosphate preparation, and discloses a high-purity ammonium dihydrogen phosphate crystallization device and a method thereof.The high-purity ammonium dihydrogen phosphate crystallization device comprises a first-stage crystallization system, a first-stage centrifugal separation system, a second-stage crystallization system and a second-stage centrifugal separation system which are connected in series. The primary crystallization system comprises a crystal elimination heater, a crystal elimination mixer, a bag filter and a DTB flash cooling crystallizer which are connected in sequence, and is used for primarily purifying a concentrated solution; the primary centrifugal separation system is used for separating primary crystals; the second-stage crystallization system comprises a crystal dissolving tank, an OSLO cooling crystallizer and the like, and deep crystallization is carried out after the first-stage crystal is dissolved; the secondary centrifugal separation system is used for separating secondary crystals; through two-stage crystallization coupling, mother liquor graded circulation, a unique gradient washing process and active impurity control, efficient and continuous production of battery-grade ammonium dihydrogen phosphate with wet-process phosphoric acid as a raw material is realized, the product purity is high, the process flow is simplified, the cost is low, and the system operation is stable.

The invention discloses a multi-stage separation synergistic power coal washing process, and belongs to the technical field of coal washing processing. The TDS intelligent dry separation system, the dry-wet combined desliming process, the super coal slime classification cyclone, the super coal slime dense medium cyclone and the ultrahigh-pressure elastic squeezing filter press are in multi-stage cooperative linkage to be used for power coal washing, the moisture content and the ash content are reduced to the maximum extent in the separation stage, and the heat productivity of the power coal is increased. Compared with a process before improvement, the power coal washing process with cooperation of multi-stage separation has the advantages that the gangue sorting efficiency and the power coal productivity are improved, the super coal slime dense medium cyclone, the super classification cyclone and the ultrahigh-pressure elastic squeezing filter press are orderly used in the power coal washing process, the water content of a filter cake is greatly reduced, and the water content of the filter cake is greatly reduced. The water content of the filter cake is obviously superior to that of a common quick-opening membrane filter press and is lower than that of the filter cake of dried coal slime, so that the fluctuation range of the heat value of the power coal is lower, the heat value of gangue is reduced, and the heat value of the power coal is improved.

A gripping system for gripping and positioning medical instruments includes a gripping device, an adapter device and a holding device. The gripping device includes an electromagnet configured to receive magnetizable instruments from an instrument container. The adapter device attaches the gripping device to a control system, which may be a robotic system. The holding device attaches the electromagnet to the adapter device. The holding device includes a receptacle, which may be a cone, for receiving the electromagnet. The holding device is arranged such that the electromagnet is movable between a first position, in which the electromagnet is received in the receptacle, and a second position, in which the electromagnet is extended out of the receptacle.

The invention belongs to the technical field of pharmaceutical analysis, and discloses a method for determining two potential genotoxic impurities in carbon [13C]-urea by gas chromatography. Comprising the following steps: (1) preparing a sample solution; (2) preparing a reference solution; (3) taking nitrogen as carrier gas, and detecting by adopting a medium-polarity or weak-polarity chromatographic column separation system; and (4) calculating by a peak area through an external standard method to obtain the accurate contents of methyl carbamate and ethyl carbamate in the carbon [13C]-urea. The method disclosed by the invention is simple to operate, good in specificity, linearity, precision and accuracy and high in sensitivity, and can realize accurate detection of residual potential genotoxic impurities, namely methyl carbamate and ethyl carbamate, in the carbon [13C]-urea.

The invention discloses a system and a method for preparing adiponitrile by electrolyzing acrylonitrile, and relates to the technical field of chemical product preparation, reaction and separation are efficiently coupled through process innovation, so that an acrylonitrile recovery unit is omitted, the safety is improved, and a modularized external reaction area capable of being flexibly expanded is introduced into the design of a reactor. The design aims to fundamentally break through the physical limitation of traditional equipment on the electrode area, and a brand new technical path is provided for realizing high-efficiency and low-energy-consumption large-scale industrial production. Nearly complete conversion of acrylonitrile is realized through the rectifying tower, and a tower kettle product does not contain unreacted acrylonitrile, so that a complicated acrylonitrile recovery tower and a circulating system do not need to be arranged in a subsequent separation system, the process is remarkably shortened, and equipment investment and operation energy consumption are reduced.

A riser reactor separation system for separating catalyst particles from hydrocarbon vapors may include a separation chamber, a hydrocarbon vapor collecting chamber, a hydrocarbon vapor outlet, and a dipleg extending downwardly towards a catalyst receiving volume. In some implementations the system may include a baffle spaced apart from and extending along a dipleg outer wall, at least partially separating the dipleg into an outer channel and an inner channel. In some implementations the separation chamber may have side walls that extend substantially parallel relative to one another. Riser reactor separation systems and related methods described herein may provide for greater separation efficiency of catalyst particles from hydrocarbon vapors.

The invention discloses a system for purifying and separating papermaking white water fine stickies, and belongs to the technical field of pulping and papermaking wastewater treatment. Comprising a physical grading deslagging unit, a chemical modification treatment unit, a biological enzymolysis reaction unit and a slurry forming unit which are sequentially communicated through a conveying pipeline I, wherein a conveying pipeline II is arranged between a feeding hole of the physical grading deslagging unit and a waste slurry discharging hole of the slurry forming unit, and a white water deep filtering unit is arranged on the conveying pipeline II; the physical grading deslagging unit, the chemical modification treatment unit, the biological enzymolysis reaction unit and the white water deep filtering unit can form a white water backflow circulation path through a conveying pipeline I and a conveying pipeline II. The system for purifying and separating the fine stickies in the papermaking white water, disclosed by the invention, can realize graded and accurate removal of the stickies with large, medium and small particle sizes in the papermaking white water, and effectively solves the problems of deposition and scaling of the stickies in equipment.

The invention relates to the technical field of gasification slag separation, in particular to an intelligent separation system for gasification slag treatment, which is provided with a feature acquisition module, a feature recognition module, a time period marking module, a flotation feature analysis module, a feature judgment module and an optimization regulation and control module. Whether abnormal risks exist in current gasified slag separation or not is judged through a feature recognition module, slag quality fluctuation parameters are determined through a time period marking module to mark a feature monitoring time period, and bubble collaborative analysis is conducted on a surface bubble image through a flotation feature analysis module to construct a bubble feature fluctuation curve. The flotation risk tendency category of current gasified slag separation is judged through the feature judgment module, and the flotation optimization regulation and control mode is determined through the optimization regulation and control module. According to the method, whether the abnormal risk exists in current gasified slag separation or not is rapidly recognized, the flotation optimization mode is adaptively adjusted according to the actual situation of the flotation process, and the reliability and efficiency of the intelligent gasified slag separation system are improved.

The invention relates to the technical field of fruit husking devices, and discloses a roller type fruit husking device and a shell and flesh separation system thereof.The roller type fruit husking device comprises a cleaning assembly and a mounting box mounted on one side of the cleaning assembly, a screening assembly and a husking assembly are arranged in the mounting box, and the husking assembly is arranged below the screening assembly; the screening assembly is used for conducting sorting according to the particle size of fruits, and the feeding end of the screening assembly communicates with the discharging end of the cleaning assembly. By arranging the shelling assembly, fruits can be shelled and separated from shells and flesh, a first extrusion roller and a second extrusion roller are arranged in a V shape, spiral convex points are arranged on the surfaces of the first extrusion roller and the second extrusion roller, and the first extrusion roller and the second extrusion roller synchronously and reversely rotate through bevel gears, so that the extrusion and friction force on shells are increased, the shells are promoted to crack along natural textures, and the quality of the fruits is improved. And compared with a traditional direct extrusion mode, the fruit pulp damage risk is effectively reduced, meanwhile, the shelling success rate is increased, and the situation of manual auxiliary shelling is reduced.

The invention relates to the technical field of oil-water separation, and discloses a hydraulic cyclone oil-water separation system and an air flotation device. The system comprises a multi-stage series hydraulic cyclone tank, a first-stage water chamber outlet is connected with a second-stage water inlet, and a second-stage water chamber outlet is connected with a buffer tank; the buffer tank reflux inlet is connected with the first-stage water inlet; the liquid level control module detects and controls the liquid level and the oil layer thickness of each stage of rotational flow tank. The system operation stability and the oil-water separation efficiency are improved.

This invention provides a satellite-launch separation signal system and a satellite-launch separation system, comprising: a first user unit that outputs two satellite-launch separation signal sources, each leading to two different contacts of a first analog separation relay; these signals then return to the first user unit via a first separation connector and a second separation connector; the input and output terminals of the first analog separation relay are each connected to a satellite display socket via cables; and a second user unit that outputs two satellite-launch separation signal sources, each leading to two different contacts of a second analog separation relay; these signals then return to the second user unit via a first separation connector and a second separation connector; the input and output terminals of the second analog separation relay are each connected to a satellite display socket via cables. This invention ensures that the signal is provided by the analog satellite-launch separation relay during ground testing, and avoids fatal malfunctions such as accidental separation commands issued before launch or mis-separation due to severe vibrations during the active phase, thus improving the reliability of the satellite-launch separation signal link.

An end effector includes a base, a first leg, a second leg, a first arm, and a second arm. The first leg is connected to the base. The second leg is connected to the base and is offset from the first leg. The first arm is pivotably connected to the first leg. The second arm is pivotably connected to the second leg. The first leg and the first arm are configured to releasably hold a first portion of a dunnage unit. The second leg and the second arm are configured to releasably hold a second portion of the dunnage unit.

The utility model relates to a full-automatic separation system for wet materials containing live insects. The full-automatic separation system comprises a tiled feeding device and a live insect separation device, the tiling and feeding device comprises a stock bin, a material distributing and conveying belt, a first frame and a dispersing and tiling mechanism. The live insect separating device comprises a heat preservation cover, a steel wire mesh belt, a second frame and a larva avoiding mechanism, and the discharging end of the distributing conveying belt is connected with the feeding end of the steel wire mesh belt. Wet materials are uniformly spread into a thin layer through the dispersing and spreading mechanism, so that the hiding of live insects caused by material accumulation is avoided, and the exposure rate of the live insects is obviously improved; through seamless connection of the material distribution conveying belt and the steel wire mesh belt, full-process automation of'tiling, separation and collection 'is formed, manual intervention is reduced, and the treatment efficiency is improved; the steel wire mesh belt intercepts wet materials, the insect receiving conveying belt collects live insects, physical separation of the live insects and the materials is achieved, and the separation efficiency is high.

This invention provides a hydrocarbon gas separation system, comprising a double-layered tube assembly and a negative pressure system. The double-layered tube assembly includes a medium delivery inner tube, a multi-layered membrane assembly, an annular interlayer gap, and a pressure-bearing protection section outer tube. The double-layered tube assembly is sealed at both ends. The multi-layered membrane assembly includes a retention layer, an isolation layer, and a selectively permeable membrane layer. The medium delivery inner tube is nested inside the pressure-bearing protection section outer tube and encloses the multi-layered membrane assembly. The negative pressure system is connected to the double-layered tube assembly. After the mixed gas is processed by the multi-layered membrane assembly in the medium delivery inner tube, sulfur dioxide is retained. The hydrocarbon gas enters the annular interlayer gap for extraction, and the retained sulfur dioxide is released back into the gas. Finally, the gas enters a sulfur dioxide detection instrument and is detected using ultraviolet fluorescence, making the data more consistent with the actual value and providing a scientific basis for relevant decision-making.

A sand separation system includes a first hydrocyclone and a second hydrocyclone. The first hydrocyclone includes a first adjustable apex via which underflow of the first hydrocyclone is conveyed. The second hydrocyclone includes a second adjustable apex via which underflow of the second hydrocyclone is conveyed. A first apex aperture diameter of the first adjustable apex is greater than a second apex aperture diameter of the second adjustable apex.

The present application belongs to the technical field of steam-water separation, and particularly relates to an external steam-liquid separation system. The present application is characterized in that sampling devices are arranged at the inlet and outlet of the wave plate dryer and the wire mesh separator, and the conductivity of the condensate water of the sampled steam-liquid mixture is measured in real time and on line, so as to monitor the steam-liquid separation efficiency of the wave plate dryer and the wire mesh separator. Meanwhile, the distance between the wave plates in the wave plate dryer and the thickness of the wire mesh area in the wire mesh separator are adjusted in real time, so that the external steam-liquid separation system provided by the present application can meet the actual requirements through on-line adjustment even when a local fault occurs, and the overall operation of the device is not affected. The external steam-liquid separation system provided by the present application can be provided with multiple groups of wire mesh separators, so as to meet different steam-liquid separation efficiency requirements, and when a group of wire mesh separators fails, the group of wire mesh separators can be disassembled and replaced without affecting the operation of the device.

The invention relates to the technical field of food processing, in particular to a preparation method of a roxburgh rose molecular essence solid beverage, which comprises the following steps: pretreatment of roxburgh rose raw materials, low-temperature physical wall-breaking extraction, multistage membrane separation and purification, low-temperature vacuum concentration and recombination crystallization. According to the method, high-efficiency physical extraction is realized under the low-temperature (25-35 DEG C) condition by adopting a torrent oscillation wall breaking technology, no chemical extraction agent is added in the whole process, and micromolecular active ingredients are selectively enriched and impurities and microorganisms are effectively removed by combining an ultrafiltration and nanofiltration multistage membrane separation system. After low-temperature vacuum concentration and recombination crystallization processes, the prepared solid beverage is high in active ingredient retention rate (SOC is greater than or equal to 90%, and VC is greater than or equal to 87%), good in solubility (the cold water dissolution time is less than or equal to 30 seconds), free of chemical residues, pure in taste and suitable for large-scale industrial production.

The present application relates to the technical field of carbon dioxide capture, and particularly relates to a membrane separation method carbon dioxide capture design method and system, physical parameters of carbon dioxide capture raw material gas flow, components, temperature and pressure are acquired; through a pretreatment device, components affecting membrane separation in the raw material gas are removed, and the physical parameters are adjusted through a gas pressure supply device; a membrane method separation system optimization model is constructed, minimization of carbon dioxide capture system cost in a period is taken as a target, and constraint conditions are set; the target is optimized and solved, actual regulation and control parameters of the pretreatment device, the gas pressure supply device and the membrane separation device corresponding to the optimal membrane method separation system optimization model are acquired. Compared with the prior art, the present application takes minimization of carbon dioxide capture system cost as a target, and realizes equipment selection and parameter design of the membrane separation system with the lowest cost.