89 results about "Reactor system" patented technology

The present application relates to a kind of self-regeneration fixed bed reaction system for multiphase catalytic reaction, belong to fixed bed technical field.The system includes shell assembly, reaction tank assembly, distribution disc assembly and regeneration connecting assembly.Shell is separated to form several sectors, each sector is equipped with reaction tank, and isolation chamber is formed between reaction tank.Regeneration connecting assembly includes upper and lower rotating disc connected by rotating shaft, and inert gas containing cavity is arranged in rotating disc and is communicated with isolation chamber.Driving mechanism rotates rotating disc, so that regeneration pipe is communicated with specific reaction tank and carries out on-line carbon burning regeneration.The present application realizes the continuous production mode of "multi-zone reaction, one area on-line regeneration" by rotating structure, cooperates with the unique scraping seal assembly and elastic buffer structure, solves the pain points such as fast coking of catalyst in high-temperature dehydrogenation and other reactions, frequent switching, easy to string gas and thermal stress damage, significantly improves the production efficiency, operating stability and heat energy utilization rate of device.

A method for processing a chemical stream includes contacting a feed stream with a catalyst in a reactor section of a reactor system to induce a reaction that forms a product stream. The method includes separating the product stream from the catalyst; transferring the catalyst to a catalyst processing section of the reactor system; processing the catalyst in the catalyst processing section; and transferring a portion of the catalyst from the catalyst processing section of the reactor system to a catalyst extraction system, the catalyst extraction system including a catalyst extraction tank and a transfer line connecting the catalyst extraction tank to the catalyst processing section. Each of the catalyst extraction tank and the transfer line includes an outer metal shell and an inner refractory lining. The method further includes cooling the catalyst in the catalyst extraction tank from a temperature greater than or equal to 680°C to a temperature less than or equal to 350°C.

A method of producing hydrocarbons from an organic material. The method includes: dissolving a solid including an organic material in a solvent to form a carbon liquid feed; introducing the carbon liquid feed into a liquid inlet of a feed assembly of a reactor system; mixing the carbon liquid feed and an oxidant gas feed in the feed assembly; combusting, in the feed assembly, at least a portion of the carbon liquid feed to produce an at least partially combusted gas mixture and heat; introducing the carbon liquid feed and the at least partially combusted gas mixture to a reactor vessel in fluid connection with the feed assembly; and in the reactor vessel, converting, using the heat, the organic material in the carbon liquid feed into a high value chemical.

A method is described for controlling a process comprising a steam system coupled to a reactor system, wherein the steam system comprises a steam vessel that feeds a stream of liquid water under pressure to the reactor system to cool the reactor system, thereby generating a steam stream, and receives the steam stream from the reactor system, said method comprising the steps of (i) obtaining a first total liquid level measurement in the steam vessel using an inferred level device, (ii) obtaining a second total liquid level measurement in the steam vessel using a direct level measurement device, (iii) calculating a difference between the first and second total liquid level measurements using a control system, and (iv) initiating an alarm using the control system when the difference between the first and second total liquid level measurements is ≥ 1% of the lower of the first and second total liquid level measurements.

The utility model discloses polycrystalline silicon and organic silicon high boiling pyrolysis reactor system of promoting gas solid liquid three -phase mass transfer relates to chemical industry technical field. The polycrystalline silicon and organic silicon high boiling pyrolysis reactor system of promoting gas solid liquid three -phase mass transfer, including reactor main part, catalyst stacking unit, liquid distributor main part and gas distribution unit. The polycrystalline silicon and organic silicon high boiling pyrolysis reactor system of promoting gas solid liquid three -phase mass transfer, gas catalyst passes into the exhaust pipe through the communication groove, and then gas catalyst is evenly sprayed into the catalytic filler of loading net cylinder through the spray head, and the liquid raw material is evenly flowed through the catalytic filler of loading net cylinder through the liquid distribution port, so that the gas and solid catalyst are mixed in the loading net cylinder, the reaction rate is improved, and the uniformity of mixing is ensured, the mixing effect of liquid raw material and gas is improved, and the reaction and product generation are accelerated.

A reactor system can include a reaction chamber; and / or a pedestal disposed in the reaction chamber between an upper chamber and a lower chamber of the reaction chamber. The pedestal can include a substrate support surface; and / or a fluid path fluidically connecting the upper chamber and the lower chamber disposed through the pedestal and the substrate support surface. The lower chamber can include a lower chamber pressure greater than an upper chamber pressure of the upper chamber such that fluid flows from the lower chamber through the fluid path into the upper chamber. The pedestal can further include a pin hole disposed through the pedestal, and a lift pin can be disposed in the pin hole. The lift pin can include a porous material and / or a pin channel, the pin channel including a fluid path such that fluid flows through the lift pin.

The present invention relates to a reactor system for continuous production of a polyester, said system comprising a vessel for mixing starting materials; and a reactor having a plurality of reactor zones configured such that the lower part of the reactor is connected to a reboiler section wherein a vent system is present on or near the upper part of reboiler section for removal of (at least part of the) water and optionally other volatiles formed during the esterification reaction. The invention moreover relates to a process for continuous production of a polyester, said process comprising the steps of: step a) of forming a mixture of starting materials; step b) of bringing said mixture into contact with a catalyst in a reboiler section of a reactor system to initiate an esterification reaction between the starting materials, to provide a liquid stream comprising an ester and a vapor stream comprising water generated during the esterification reaction; step c) of removal of at least part of the vapor stream from the reboiler section via a vent system on or near the upper part of reboiler section; step d) of transporting the liquid stream from the reboiler section to an esterification reactor zone for continuation of the esterification reaction to obtain an ester product stream; and step e) of transporting the ester product stream from the esterification reactor zone to a polycondensation reactor zone to produce a polyester. The invention moreover relates to a use of a vent system on or near the upper part of a reboiler section of a reactor system for reduction of foaming during an esterification reaction by removal of (at least part of the) water and optionally other volatiles formed during an esterification reaction between a diol with a dicarboxylic acid.

A fission product trap for a reactor system, such as for a pipe connection and / or a pump shaft of a pump of the reactor system, includes a porous container. The porous container may be mounted about the pipe connection and / or pump shaft and include an absorbing material contained therein. The absorbing material may be configured to collect fission products emitted from the pipe connection and / or the pump shaft. The fission product trap further includes an assembly encompassing the porous container and that defines a volume about the porous container and the pipe connection and / or the pump shaft.

A steam reforming reactor may comprise a shell, an inner tube disposed within the shell such that an annular portion is formed between the shell and the inner tube, a fluid inlet communicating with the annular portion, a fluid outlet communicating with the annular portion, a catalytic reactor system disposed within the annular portion, and at least one internal heating device disposed within the inner tube, wherein the catalytic reactor system may be configured to allow fluid to flow through the annular portion, and the at least one internal heating device may be configured to heat the fluid flowing through the annular portion.

The application discloses a method for synthesizing catalase nanocapsules based on gas-liquid two-phase flow microfluidic technology and application. Nitrogen is used as a gas phase, and a liquid phase containing acrylated catalase, a monomer mixture and a crosslinking agent is used to form Taylor flow in a microfluidic chip. The internal vortex of the gas-liquid interface is used to enhance the mixing efficiency, and in-situ radical polymerization on the surface of the enzyme is realized. By screening six microfluidic chips with different structures, the geometric parameters of the chip and the hydrodynamic conditions are optimized, and the particle size uniformity and enzyme activity retention rate of the nanocapsules are significantly improved. The application also discloses a continuous flow reactor system for loading the obtained nanocapsules on macroporous resin microspheres to construct a continuous flow reactor system, and the system is used for efficient degradation of hydrogen peroxide in semiconductor wastewater. The method has the advantages of high mixing efficiency, mild reaction conditions, continuous production and the like, the obtained nanocapsules have the advantages of narrow particle size distribution, high enzyme activity and good stability, and are suitable for the field of industrial wastewater treatment.

An example method includes: (A) receiving a polymerization process dataset having properties of polyethylene (PE) resins prepared using a multi-component catalyst composition and different operating parameters of a gas phase reactor system; (B) setting a catalyst trim effectiveness value of the multi-component catalyst composition to an initial value; (C) training a respective process model for each of the properties of the PE resins of the polymerization process dataset using the catalyst trim effectiveness value to yield a set of trained process models; (D) optimizing the catalyst trim effectiveness value to determine a minimized sum of squared error (&SE) value of model residuals using the set of trained process models; (E) repeating steps (C) and (D) until a decrease in the minimized SSE value is less than a predefined threshold value; and (F) outputting the catalyst trim effectiveness value and the set of trained process models for the multi-component catalyst composition.

A method for performing a pressure control in a gas phase reactor system, a control system for executing the method for performing the pressure control in the gas phase reactor system, and the gas phase reactor system are provided. The method comprises a second-valve adjustment step, in which an opening pressure of a second valve for discharging a discharge mixture from a gas phase reactor to a recovery area is adjusted to a value equal to or higher than an opening pressure of a first valve for the supply to the gas phase reactor. Thereby, the gas phase reactor can be operated in a pressure range between the first-valve opening pressure and the second-valve opening pressure, and a workload placed on the recovery area of the gas phase reactor system is decreased.

In some embodiments, a power generation system may include a first nuclear reactor, which may include a vessel having a wall defining a cavity. The nuclear reactor may include a core disposed within said cavity. Said core may include a solid matrix material defining one or more channels. A fuel material may be disposed in said one or more channels. Said solid matrix material may be a primary heat transfer medium. The power generation system may include an electric generating system having a secondary heat transfer medium. The power generation system may include one or more heat exchangers thermally coupled to said vessel wall. Said primary heat transfer medium may transfer heat generated by the fuel material to the one or more heat exchangers. Said secondary heat transfer medium may draw heat from said one or more heat exchangers.

The application relates to a multi-stage floating catalyst chemical vapor deposition reactor system and a co-production method, relates to the technical field of methane pyrolysis, and the reactor system comprises a reactor body, a circulating loop, a collection mechanism and the like. The circulating loop enables gas to form a circulating gas path in multiple reaction zones, and adds methane and a catalyst precursor into the circulating gas path to react to form an aerogel net and hydrogen. The collection mechanism collects hydrogen and winds the carbon nanotube aerogel net. The application is characterized in that the methane and the catalyst precursor are introduced into the reactor body to react to obtain hydrogen and an aerogel net. The hydrogen and the aerogel net are moved to the collection mechanism. The hydrogen is automatically moved upward and then collected due to its lightness, and the aerogel net is wound and collected. High-purity hydrogen and high-performance carbon nanotube aerogel are obtained. The reaction efficiency is improved, and the production cost is reduced.

This invention provides a simulated external circulation reactor system and a simulated external circulation reaction method for a coal-fired power plant boiler furnace. The simulated external circulation reactor system includes a furnace partitioned reactor unit and an external circulation flue gas duct. The furnace partitioned reactor unit is used to simulate the lower part, middle part, upper part, lower part, and upper part of the main combustion zone in the furnace of a prototype boiler. The furnace partitioned reactor unit is connected to the external circulation flue gas duct and the furnace outlet respectively through a first distributor. The outlet of the external circulation flue gas duct returns the flue gas to the main combustion zone through a second distributor. This invention establishes a one-dimensional reactor network system for deep air staged combustion in a coal-fired power plant boiler furnace with dimensions and tuyeres highly matched to the prototype boiler and employing external flue gas circulation technology. This system is used to obtain the influence of different flue gas recirculation ratios under deep air staged combustion on the combustion performance and component conversion mechanism of the coal combustion process, especially the influence on the migration and conversion characteristics of nitrogen element.

A solar concentrator reactor system and method of use for high temperature thermochemical processes. In one embodiment, the solar concentrator reactor system produces a thermochemical reaction of irradiated particles within an enclosed vessel volume of a solar concentrator reactor. In one aspect, the solar concentrator reactor system uses a solar concentrator to irradiate particles of a particle stream within an enclosed vessel volume of a solar concentrator reactor. The thermochemical reaction yields a chemical change of the feedstock and / or phase transition of the feedstock such as the production of a molten reacted material from a solid particulate feed. In one embodiment, the particles are a lunar regolith and the thermochemical reaction yields oxygen.

The embodiment relates to a process for producing an ethylene-based polymer in a reactor system comprising a first reactor and a second reactor. The process involves ethylene, one or more (C3-C3) polymers. 14 Polymerizing an α-olefin monomer and at least one polyene in a first reactor in the presence of one multi-chain catalyst and at least one single-chain catalyst to produce a first reactor polyethylene product containing long-chain branching, wherein the multi-chain catalyst contains multiple polymerization sites, and the long-chain branching is produced by the cooperative bonding of two polymer chains of the multi-chain catalyst with the polyene during polymerization, and the first reactor polyethylene product contains ethylene and one or more (C3~C 14 The method comprises polymerizing an α-olefin monomer in a second reactor in the absence of an initial polyene feed and in the presence of at least one single-chain catalyst to produce a second reactor polyethylene product, wherein the ethylene polymer comprises the first and second reactor polyethylene products.

The invention discloses a garbage hydrolysis fuelization energy-saving system and method. The garbage hydrolysis fuelization energy-saving system comprises a preheating system, a carbonization reaction kettle system and a heat energy recovery pipeline, the preheating system comprises a tank body and a stirrer arranged in the tank body, the tank body is provided with a feed port and an industrial water inlet, the wall of the tank body is of an interlayer structure, and the tank body is provided with a high-temperature water inlet and a high-temperature water outlet which are communicated with the interlayer structure of the wall; the carbonization reaction kettle system comprises a horizontal kettle body, a jacket heating layer and an inner heating coil pipe arranged in the horizontal kettle body, the top of the horizontal kettle body is communicated with the tank body, the bottom of the horizontal kettle body is provided with a discharge port, the jacket heating layer is provided with a jacket steam inlet and a jacket condensate outlet, and the inner heating coil pipe is provided with a coil pipe steam inlet and a coil pipe condensate outlet; one end of the heat energy recovery pipeline is connected with the jacket condensate outlet and the coil condensate outlet, and the other end is connected with the high-temperature water inlet; the high-temperature water outlet is connected with a steam generator, and a steam outlet of the steam generator is connected to the jacket steam inlet and the coil pipe steam inlet.

A method for processing a chemical stream includes contacting a feed stream with a catalyst in a reactor portion of a reactor system, the reactor system including the reactor portion and a catalyst treatment portion. The catalyst includes platinum, gallium, or both, and contacting the feed stream with the catalyst causes a reaction, the reaction forming an effluent stream. The method includes: separating the effluent stream from the catalyst; passing the catalyst to the catalyst treatment portion; and treating the catalyst in the catalyst treatment portion. Treating the catalyst includes: passing the catalyst to a combustor; combusting a supplemental fuel in the combustor to heat the catalyst; treating the heated catalyst with an oxygen-containing gas to produce a reactivated catalyst; and passing the reactivated catalyst from the catalyst treatment portion to the reactor portion. The supplemental fuel can include hydrogen in a molar ratio of at least 1:1 to another combustible fuel.

Methods and systems for forming structures including a layer of low dielectric constant material on a surface of a substrate and structures and devices formed using the methods or systems are disclosed. An exemplary method includes providing a substrate within a reaction chamber of a reactor system, providing one or more precursors to the reaction chamber, providing one or more reactants, including a mixture of a nitrogen and oxygen containing reactant and a hydrogen containing reactant, and providing pulsed plasma power to polymerize the one or more precursors within the reaction chamber.

A method is disclosed for plasma-based conversion of methane in a plasma reactor, the plasma reactor (1) comprising a reaction chamber and an energy source to create the plasma in the reaction chamber, the reaction chamber being fluidly connected to a separate post-plasma reaction chamber, the plasma reactor comprising a gas inlet, the post-plasma reaction chamber comprising a gas outlet, the method comprising: a) generating a plasma in the reaction chamber by activating the energy source; b) providing a first gas flow comprising a CH4 component through the gas inlet and into the reaction chamber, allowing plasma-based conversion of the CH4 component into gaseous H2 and solid carbon and allowing the continuous removal of produced H2 through the post-plasma reaction chamber and through the gas outlet; c) in consideration of a solid carbon deposit being formed on a predetermined portion of an inner wall of the post-plasma reaction chamber, replacing the first gas flow with a second gas flow, the second gas flow comprising a plasma-activated CO2 component, allowing the oxidation of the deposited carbon, and allowing the continuous removal of produced CO through the gas outlet until the deposited carbon is substantially removed; and associated reactors and reactor systems

A method for maximizing the selectivity (S) of an epoxidation catalyst in an ethylene oxide reactor system, the method comprising: receiving measured reactor selectivity (S) from an ethylene oxide production system. meas ), measured reactor temperature (T) meas The ethylene oxide production system is configured to convert a feed gas containing ethylene and oxygen into ethylene oxide in the presence of the epoxidation catalyst and a chloride-containing catalyst moderator in the ethylene oxide reactor system, along with one or more operating parameters. The epoxidation catalyst contains silver and a promoting amount of rhenium (Re), and the reactor selectivity (S) is measured. meas The measured reactor temperature (T) meas The method also includes real-time and historical operating data points generated over time by the ethylene oxide production system, and the one or more operating parameters include data points generated over time by the ethylene oxide production system. The method further includes using a processor to perform the following steps: (a) for each time point, using a model to calculate the optimal moderating agent level (M) for the epoxidation catalyst. opt The model estimation selectivity (Sest) and model estimation temperature (Test) are considered. The model estimation selectivity (Sest) is... est The model-estimated temperature (Test) is determined based on at least one of one or more operating parameters at the time point, the at least one operating parameter excluding the moderating agent level, and the model is based at least in part on historical empirical data associated with the epoxidation catalyst, the ethylene oxide production system, or both. The method also includes using the processor to perform the following steps: (b) for each time point, determining the measured reactor selectivity (S). meas ) and the selectivity estimated by the model (S) est The difference (ΔS) between the measured reactor temperature (T) and the measured reactor temperature (T) meas (c) The difference (ΔT) between the temperature (Test) estimated by the model and the temperature (Test); (d) Fitting the curve to the Δselectivity (ΔS) data points as a function of the corresponding ΔT data points to obtain the fitted curve; (e) Based on the fitted curve and the real-time value of ΔS (ΔS real‑time The real-time values ​​of ΔT and ΔT real‑time Determine the real-time relative effective moderating agent level (RCl). eff real‑time (e) based on this real-time RCL eff The method also includes using a processor to perform the following step: (f) displaying the executable suggestion on a display.

The utility model belongs to the field of reactor, concretely relates to a kind of space reactor neutron source assembly and reactor system. Wherein space reactor neutron source assembly includes linear moving mechanism and the neutron source rod body of linear moving mechanism output end being arranged, the neutron source rod body includes neutron source functional area, gap and cladding sequentially arranged from inside to outside;The neutron source functional area includes sequentially arranged heat transfer zone, fuel area I, partition area I, neutron source, partition area II and shutdown area. The space reactor neutron source assembly provided by the utility model better utilizes the important position of reactor core center. It can move up and down on the core center, and the structure is simple and compact, efficiently realizes the functions of fuel auxiliary combustion, neutron source start-up, shutdown and reactivity adjustment.

A load following reactor system (150) and related apparatus for improved control of a reactor under varying loads is disclosed. The load following reactor (152) can be a pipe-cooled reactor for methanol synthesis. Reactants can be controlled by at least one valve element (160, 162) such that a portion of the reactants is provided to the reactor (152) through a reactor pipe (190) and a portion of the reactants is provided to the reactor (152) after being heated within a heat exchanger (156). The heated portion of the reactants can be provided to the reactor (152) after the pipe (190). The valve elements (160, 162) can be controlled in accordance with the temperature of the reactor (152) and / or the feed flow of the reactants to accommodate varying reactant flow to the temperature of the reactor (152).

The present application relates to a kind of tritium separation method of tritium-containing wastewater and its reactor system, application, the tritium separation method of tritium-containing wastewater of the present application is ultraviolet irradiation promotes separation method, comprising: step 1) tritium-containing wastewater is introduced into the reaction containment of reactor system and is contacted with adsorption material to form liquid-solid two-phase contact system, step 2) after ultraviolet light is irradiated to liquid-solid two-phase contact system, make tritium enrich in adsorption material;Step 3) after the liquid-solid two-phase contact system of irradiation is completed, solid-liquid separation is obtained to low concentration tritium treatment water and tritium-rich adsorption material.The method of the present application is irradiated by ultraviolet light, accelerates hydrogen / tritium isotope exchange and adsorption process, can obtain higher tritium removal rate and adsorption amount under the same processing time.The present application belongs to energy-saving and environmental protection industry, especially in wastewater environmental control and nuclear pollution wastewater treatment in the environmental protection application of the recovery treatment of nuclear radioactive pollution elements plays a key role.

An electrified reactor system can include optional insulation, an optional pressure housing, electrical connections to / from the catalytic module, a preheater, one or more heat exchangers, a reaction zone (e.g., a reaction module, a catalyst module, etc.), one or more optional preheaters, and an operation switcher (e.g., valve, rotatory switch, controller, etc.).

An aqueous effluent treatment system (1) includes a supercritical reactor system (2), an aqueous effluent source (3) connected upstream to the supercritical reactor system via a waste feed pump (P1), a fluid extraction system (4) connected downstream to the supercritical reactor system, and a solids extraction system (8) connected downstream to the supercritical reactor system. The supercritical reactor system includes multiple reactors, each having a vessel with a reactor chamber therein, each reactor operable to generate a pressure exceeding 22.1 MPa and a temperature exceeding 374 °C, configured to generate a supercritical zone within the reactor chamber. At least one reactor is a first moving bed reactor, the first moving bed reactor including: a fluid effluent outlet (25) at the top of the first moving bed reactor chamber, a solids feed inlet (36) at the top of the first moving bed reactor chamber for injecting moving bed solids into the reactor chamber, and a solids outlet (30) connected to the solids extraction system for extracting solids from the first moving bed reactor chamber.

The application discloses a reactor primary loop anti-siphon experiment system and a control method, and belongs to the field of nuclear power engineering. The system comprises a primary loop main pipeline, an anti-siphon pipeline, a visual pipeline, upper and lower water tanks, a data acquisition system and a control system. The anti-siphon control method is as follows: the siphon state is judged by monitoring the flow meter and liquid level meter signals, and the anti-siphon operation is executed by the control system; a siphon logic identification function is constructed to make a preliminary judgment, and a dynamic residual function is introduced synchronously to make a secondary physical check. When the upper water tank liquid level is lower than the preset threshold value, the outlet flow deviates from the normal flow and remains in the abnormal high flow interval, and the dynamic residual is lower than the allowable error threshold value to effectively filter out the false liquid surface oscillation, the control system determines that the siphon state actually occurs, outputs the opening instruction to the anti-siphon valve, and introduces air into the primary loop main pipeline to block the siphon, so that the real-time monitoring and automatic blocking of the siphon phenomenon are realized. The application improves the precision and anti-interference robustness of the anti-siphon response, effectively prevents the reactor coolant loss accident, and guarantees the safety of the reactor system.

This application relates to a method for reforming heavy aromatic compound streams. A method for reforming heavy aromatic compounds (C...) is disclosed. 11+ Reorganization into C 6‑8 Processes, catalysts, and reactor systems for producing aromatic compounds are also disclosed. These include processes, catalysts, and reactor systems for producing aromatic compounds and liquid fuels from oxygenated hydrocarbons such as carbohydrates, sugars, sugar alcohols, sugar degradation products, and the like.