15 results about "Separation scheme" patented technology

A method for separating and purifying 4MP1 from a mixture containing 4MTP2 and 1-Hexene comprises the following steps: continuously introducing a solution in which 4MTP2, 1-Hexene and 4MP1 with any concentration are dissolved into a simulated moving bed chromatography system as a raw material solution, collecting a high-purity 4MP1 solution from raffinate of the simulated moving bed chromatography system by adopting a metal organic framework material as a stationary phase, and separating the high-purity 4MP1 solution from the raffinate of the simulated moving bed chromatography system. The extraction liquid is a solution containing impurities 4MTP2 and 1-Hexene. The invention provides a brand new method for separating 4MP1 from 4MTP2 and 1-Hexene, and a complete separation scheme is provided for the prior art; in the separation of high-concentration 4MP1, the relative purity of the separated and purified 4MP1 can reach gt; the recovery rate is gt; and in the separation of low-concentration 4MP1, the rectification level is also exceeded, and the method is more suitable for 4MP1 thermosensitive substances.

The invention discloses an intelligent analysis monitoring system and method based on a marine environment sample, and belongs to the technical field of marine environment analysis. The method comprises the following steps: collecting marine environment samples, calling a deep learning model, outputting a marine environment sample separation scheme, and separating the samples; determining a class group code of each organism; inputting the class group codes into a preset conflict rule base, and screening potential conflict combinations; calculating a conflict coefficient; the sub-packaging operation is executed by taking conflict-free coexistence and the minimum sub-packaging number as targets; dividing the target monitoring sea area into sub-regions by adopting a grid method; matching the conflicting biological samples to the characteristic archives of the sub-regions; constructing a knowledge graph of the sea area, the biological group and the ecological characteristics; suspicious organisms in the conflicting organism samples are screened, ecological characteristics are extracted, and all sea area codes meeting the ecological characteristics in the knowledge graph are matched; and comparing the morphological characteristics of the organism with historical biological records of the candidate sea area, and determining the code of the native sea area.

The application discloses a hydrate secondary generation prevention and treatment system and method for combustible ice collection pipeline, which comprises a gas phase collection pipeline for conveying output gas phase medium and a liquid phase collection pipeline for conveying output liquid phase medium, the liquid phase collection pipeline is connected with a liquid phase pipeline hydrate control system for separating free gas of wellhead liquid phase produced medium. Based on the theory of sea area combustible ice mining, the application conforms to the depressurization mining mode, aims at the medium characteristics of the gas phase channel and the liquid phase channel output during the underground decomposition, combines the pressure and temperature conditions under the deep water development environment, evaluates and obtains the viewpoint that the hydrate secondary generation risk of the gas phase medium collection pipeline is smaller under the basic maintenance of 3MPa operating pressure, and the liquid phase medium collection pipeline is mainly prevented from the hydrate secondary generation, and the gas-liquid secondary separation scheme is provided to prevent the hydrate secondary generation of the liquid phase medium collection pipeline from the components.

The present application relates to a kind of launch vehicle star rocket separation timing taskless design method.The present application is automatically designed rocket separation timing according to star rocket separation mode, the position and speed of rocket before first star rocket separation, separation speed, the mass of satellite and the total mass of rocket, satellite installation position in rocket, satellite quantity, can avoid using STK software to call rocket orbit UTC time and orbit six root numbers, rocket navigation coordinate system attitude angle such as trajectory parameter for far-field safety analysis, can effectively reduce operation amount and artificial design process, improve work efficiency.Meanwhile, the present method can design the timing of star rocket separation section for different launch tasks, so as to realize the taskless design of star rocket separation scheme.

The invention relates to the technical field of oil-water separation, and particularly discloses an oil-water separator which comprises a first separation area, a second separation area and a third separation area, the first separation area is provided with a mixed liquid inlet, two vertical partition plates, a light phase collecting pipe and a heavy phase collecting pipe; the second separation area comprises a centrifugal separation mechanism, the centrifugal separation mechanism is arranged in the oil-water separator, and the centrifugal separation mechanism is used for detecting the liquid amount and centrifugally separating oil and water; the third separation area comprises a filtering mechanism, and the filtering mechanism is arranged in the oil-water separator and used for filtering and separating oil and water. According to the oil-water separator, the three separation areas are arranged, the first separation area can be selected when only crude separation is needed, and the second separation area and the third separation area can be further selected when a better separation effect is needed, so that the oil-water separator can select a proper separation scheme according to needs.

Processes and facilities for providing recycled content hydrocarbon products (r-products) from separation of pyrolysis gas formed by pyrolyzing waste plastic are provided. Various separation schemes may be employed to process the recycled content pyrolysis gas (r-pygas) into one or more recycled content hydrocarbon streams, which can be used in forming a variety of recycled content products.

The invention relates to the technical field of dynamics, and discloses a turbulence separation quantitative analysis method and device, electronic equipment and a storage medium. The method comprises the steps that on the basis of CFD simulation, the turbulence energy change gradient of each turbulence separation key area is extracted so as to identify a turbulence separation boundary; based on the molded surface grids in the turbulent flow separation key area, calculating the central point turbulent energy of each molded surface grid through interpolation; traversing the profile grid to compare the turbulence energy of each central point with the turbulence energy value of the turbulence separation boundary, and further determining a turbulence separation problem area; and executing at least one turbulence separation scheme improvement according to the type of the turbulence separation problem area. According to the method, a set of flow separation area quantitative analysis standard process based on turbulent kinetic energy can be provided for engineering designers, the occurrence frequency of the phenomena of failure of an improved scheme and repeated modification of the scheme can be reduced, the design analysis cost is reduced, the overall scheme design of a project is kept, the period is stably promoted, and the design efficiency and quality are improved.

The invention relates to a method for separating and purifying 4MP1 from a mixture containing 4MTP2 and 4MCP2, which comprises the following steps: continuously introducing a solution in which 4MTP2, 4MCP2 and 4MP1 with any concentration are dissolved into a simulated moving bed chromatography system as a raw material solution, collecting a high-purity 4MP1 solution from an extract liquor of the simulated moving bed chromatography system by taking a molecular sieve as a stationary phase, the raffinate is a solution containing impurities 4MTP2 and 4MCP2. The invention provides a brand new method for separating 4MP1 from 4MTP2 and 4MCP2, and provides a complete separation scheme for the prior art; in the separation of 4MP1 with the concentration not lower than 95%, the relative purity of the separated and purified 4MP1 basically reaches 99 wt% or above, and the recovery rate is gt; and in the separation of low-concentration 4MP1, the method has a higher level than rectification.

The invention relates to an intelligent management and control method and system for a blood cell separator, relates to the technical field of intelligent control of medical instruments and medical information, and solves the problems that the effectiveness of a separation scheme is insufficient and the risk of complications is increased due to the fact that individual differences of patients cannot be accurately adapted. Inputting the blood indexes of the patient into a preset deep neural network, selecting an adaptive scheme from a plurality of preset subdivision separation modes, generating an initial centrifugal parameter combination, and dynamically adjusting a centrifugal rotating speed and an acceleration parameter according to a preset frequency by adopting a model prediction control algorithm in combination with data collected in real time and a separation process dynamic model; and monitoring state variables and sensor data of the dynamic model in the separation process in real time, and when monitoring parameters deviate from a preset range, starting a parameter compensation mechanism corresponding to the abnormal type. The method has the following effects that individualized precise control and real-time optimization of blood cell separation are achieved, and safety and efficiency are improved.

The invention relates to the technical field of wastewater treatment, in particular to an efficient and environment-friendly butyl acrylate high-salinity wastewater treatment process which comprises the following steps: S1, acidification replacement, S2, extraction separation, S3, rectification and recovery, S4, refining and purification, S5, neutralization and adjustment, and S6, evaporative crystallization. According to the method, efficient and rapid separation of the oil phase and the water phase is realized by adopting a separation scheme of combining the centrifugal extractor and the molecular sieve membrane, meanwhile, the moisture content in the organic phase is effectively controlled, and the organic phase is deeply refined by adopting the continuous ion exchange equipment and the macroporous strong-acid cation exchange resin, so that the separation efficiency is improved. Trace sodium ions and other impurities can be specifically adsorbed and removed, so that the purity of the recycled acrylic acid product is improved in a breakthrough manner, and the recycling requirement of a high-end production device is met.

The present application belongs to the field of aerospace separation technology, and particularly relates to a rocket fairing rotating separation evaluation method. It aims to solve the problem of long cycle and high cost caused by the dependence of traditional fairing rotating separation scheme on high-fidelity simulation and physical test. By simplifying the half fairing as an analysis object of rigid body planar motion, the mass center kinematics and dynamics equations of the half fairing rotating around a fixed point are established. Then, the Runge-Kutta method is used to solve the mathematical model by cyclic iteration to obtain the motion trajectory parameters in the separation process. Finally, the separation motion trajectory is visualized based on the trajectory parameters, and the collision risk is evaluated by analyzing the relative position relationship between the trajectory and the rocket body. Based on the physical simplified model and numerical calculation method, the rapid and safe evaluation of the fairing separation process is realized, which greatly shortens the design verification cycle, and significantly reduces the evaluation cost due to the pure numerical calculation.

The application discloses a kind of MVR evaporation crystallizers suitable for high salt wastewater and use method, belong to evaporation crystallizer field, including falling film evaporation part, circulating pump, separation part and compressor;The liquid discharge end of the falling film evaporation part is connected with the input end of circulating pump by reflux pipeline, and the output end of the circulating pump is connected with the liquid inlet end of the falling film evaporation part by liquid sending pipeline;The falling film evaporation part is communicated with the separation part by aeration pipeline and flow guide pipeline, and the exhaust end of the separation part is connected with the input end of cyclone separator, and the exhaust end of the cyclone separator is connected with the input end of compressor;The application constructs the three-stage separation scheme from rough to fine, can capture droplet of different physical characteristics;Can greatly reduce the liquid-carrying capacity of secondary steam, directly protect core equipment;For the case that wastewater composition is complex or processing capacity has certain fluctuation, the application provides higher safety margin and operation flexibility.

This invention provides a direct-thrust missile hood separation method and structure, primarily addressing the problems of added counterweights and complex timing control in existing hood separation schemes. In this invention, the lateral separation velocity is provided by the lateral aerodynamic force generated during hood separation by adjusting the missile's attitude. While ensuring load-bearing and heat protection requirements, the same specifications of separation actuators are used, resulting in a simpler separation structure. The hood separation scheme only requires the separation actuators to provide the specified axial separation velocity, reducing the synchronicity and speed requirements of each actuator during operation, lowering the timing control requirements of the system, and improving the reliability of the separation system.

The invention discloses an MVR (Mechanical Vapor Recompression) evaporation crystallizer suitable for high-salt-content wastewater and a use method, and belongs to the field of evaporation crystallizers, the MVR evaporation crystallizer comprises a falling film evaporation part, a circulating pump, a separation part and a compressor; the liquid discharge end of the falling film evaporation part is connected with the input end of the circulating pump through a backflow pipeline, and the output end of the circulating pump is connected with the liquid inlet end of the falling film evaporation part through a liquid feeding pipeline; the falling film evaporation part is communicated with the separation part through a ventilation pipeline and a flow guide pipeline, the exhaust end of the separation part is connected with the input end of the cyclone separator, and the exhaust end of the cyclone separator is connected with the input end of the compressor; according to the invention, a coarse-to-fine three-stage separation scheme is constructed, and liquid drops with different physical characteristics can be captured; the liquid carrying amount of secondary steam can be greatly reduced, and core equipment is directly protected; the invention provides higher safety margin and operation flexibility for the condition that the wastewater composition is complex or the treatment capacity has certain fluctuation.

The invention belongs to the field of material synthesis, and discloses a separation method of a solution polymerization reaction product to solve the problem of high energy consumption of traditional sequential separation, including rectification path separation or dividing wall column integrated separation. The rectification path separation comprises solvent pre-separation or 1-octene pre-separation, and the separation scheme of the solvent pre-separation comprises a solvent pre-separation tower, a C6 separation tower, a 1-hexene separation tower, a solvent separation tower and a 1-octene light separation tower; the separation scheme of 1-octylene pre-separation comprises a 1-octylene pre-separation tower, a 1-octylene heavy separation tower, a C6 separation tower, a 1-hexene separation tower and a heavy component removal tower. The separation product comprises a C6 by-product, 1-hexene, 1-octene, a circulating solvent and a heavy component, and the C6 by-product comprises methyl cyclopentane and methylene cyclopentane; and the circulating solvent is further purified through the amino-functionalized adsorption material. The method breaks through the fixed separation sequence, reduces the energy consumption, improves the solvent recovery rate and purity, and is suitable for industrial production.