2443 results about "Phencyclone" patented technology

A lipid feedstock including fatty acid(s) is treated in a process flow through a moving bed reactor with catalyst to produce a treated stream. The catalyst may include metal oxide catalyst on a particulate oxide support. The catalyst may be transferred, using a catalyst withdrawal line, from the bottom of the moving bed reactor to a fluidized bed regenerator, and regenerated. The catalyst may be transferred from the fluidized bed regenerator to a cyclone that separates the catalyst from flue gas. The catalyst may be transferred from the cyclone to the top of the moving bed reactor using a catalyst feed line. A first separation gas may be flowed into the catalyst feedline, and a second separation gas may be flowed into the bottom of the moving bed reactor or into the catalyst withdrawal line, to generate pressure differentials driving the process flow through the moving bed reactor.

The invention relates to the technical field of safety and environmental protection, in particular to a negative-pressure circulating explosion-control dust removal method suitable for combustible dust places, which comprises the following steps: firstly, sealing a bin body and injecting carbon dioxide-nitrogen inert gas to generate a low-oxygen environment; then, a flow guide angle-adjustable cyclone separator, a dielectric barrier discharge plasma reactor and a waste heat thermo-acoustic transducer are driven to cooperatively capture dust, and sound node amplitude synthesis capture data are obtained through compressed sensing of a microphone; inputting the environment data and the capture data into a reinforcement learning process containing a micro-thermochemistry model, and outputting instructions for adjusting negative pressure pulse, inert flow, sound field intensity and cyclone geometry; in combination with distributed radio frequency imaging data, an adversarial digital twinborn model is generated to predict explosion free energy, and automatic rollback or shutdown is carried out when the explosion free energy exceeds a threshold, so that a safe, efficient and low-energy-consumption closed loop is formed.

A hand vacuum cleaner comprises a cyclone, a conical pre-motor filter that is positioned rearward of the cyclone and a suction motor. The pre-motor filter has a front end that faces that faces towards the cyclone air outlet. The conical pre-motor filter has an open interior volume, an outer surface, which is an upstream surface of the pre-motor filter, and an inner surface, which is a downstream surface of the pre-motor filter.

The invention relates to the technical field of thermal management and safety protection of lithium ion batteries, and discloses a system for treating thermal runaway spray products of a lithium ion battery and the lithium ion battery, the system comprises a gas collecting pipeline, a gas outlet pipeline and a gas outlet pipeline, the first end of the gas collecting pipeline is used for connecting an explosion-proof valve of the lithium ion battery; the cyclone separator is provided with a separation cavity, the diameter of the separation cavity is gradually reduced from top to bottom, the cyclone separator is provided with a discharge port, a feed port and an air outlet, the discharge port is communicated with the separation cavity and located at the bottom, the feed port and the air outlet are located at the top, and the second end of the air collecting pipeline is communicated with the separation cavity through the feed port; the condensation and adsorption module comprises a reaction part and a collection part which are arranged up and down, the reaction part is contained in the separation cavity, the reaction part is used for carrying out phase change and neutralization reaction with the sprayed product, the lower end of the reaction part is connected to the upper end of the collection part, and the collection part is connected to the discharge port. And when the lithium ion battery is in thermal runaway, sprayed high-temperature toxic liquid drops are cooled and absorbed, so that the safety of the lithium ion battery is improved.

The invention discloses a red mud reduction, magnetic separation and recovery device and process based on chemical looping gasification. The device comprises a chemical looping gasification device, a red mud feeder, a bag-type dust collector and a magnetic separator, the chemical chain gasification device comprises an air reactor, a first cyclone separator, a fuel reactor, a solid fuel feeder and a second cyclone separator, wherein the upper part of the air reactor is connected with a feed port of the first cyclone separator, a discharge port of the first cyclone separator is connected with the upper part of the combustion reactor, and the upper part of the fuel reactor is connected with a feed port of the second cyclone separator; the top of the second cyclone separator is connected with the bag-type dust collector through a fuel reactor tail flue, and the magnetic separator is connected with an ash discharge port of the bag-type dust collector; and the red mud feeder is connected with the bottom of the fuel reactor. Chemical looping gasification and red mud reduction roasting magnetic separation are combined, and iron element recovery and oxygen carrier replacement are achieved.

The invention discloses a cyclone separator for collecting powder coating, and relates to the technical field of cyclone separators. Comprising a barrel, the outer side of the barrel is fixedly connected with a support, the outer side of the barrel is fixedly connected with a feeding pipe, a conical barrel is fixedly connected to the bottom of the barrel, a spiral plate is fixedly connected to the inner wall of the conical barrel, a spiral groove is formed in the inner wall of the conical barrel, a round hole is formed in the middle of the top of the barrel, and a supporting column is fixedly connected to the top of the barrel; the number of the supporting columns is multiple, the multiple supporting columns are evenly distributed with the discharging assembly as the center, the tops of the supporting columns are fixedly connected with a bearing plate, and the top of the bearing plate is fixedly connected with the motor. According to the cyclone separator for collecting the powder coating, a definite flowing path is provided for dust particles by arranging the spiral groove and the spiral flow guide groove, so that dust can move towards the dust discharging opening more smoothly, the accumulation and backmixing phenomena of the dust on the inner wall of the conical barrel are reduced, and the dust discharging efficiency and stability are improved.

A surface cleaning apparatus including an air flow path from a dirty air inlet to a clean air outlet with a motor and fan assembly located in the air flow path; a cyclone located in the air flow path having a first end, an opposed second end, a cyclone axis of rotation that extends between the first and second ends, a sidewall located between the first and second ends, a cyclone air inlet, a cyclone air outlet, and a first dirt outlet, wherein a cyclone chamber is located internal of the sidewall between the first and second ends; and a dirt collection chamber external to the cyclone chamber and in communication with the cyclone chamber via the first dirt outlet. The cyclone chamber has a non-circular cross-sectional area in a plane that is transverse to the cyclone axis of rotation. The first dirt outlet includes an opening in the sidewall.

The invention relates to the technical field of pulverized coal separation, in particular to a cyclone separator, a pulverized coal separation system and a cyclone separator structure optimization method.The cyclone separator comprises an air inlet unit which comprises an air inlet assembly and a separation assembly connected with the air inlet assembly; and the discharge unit comprises an exhaust assembly arranged on the inner side of the separation assembly and a dust discharge assembly arranged at the bottom of the separation assembly. The cyclone separator has the beneficial effects that by arranging the spiral channel, the centrifugal force after dust-containing gas enters can be increased, the dust particle separation efficiency is improved, the longitudinal circulation phenomenon at the top of the separator can be effectively avoided, the influence of a top ash ring is relieved, and mutual interference of airflow in adjacent inner and outer rotational flows is avoided; and the number of particles of large-particle-size dust entering the exhaust pipe through longitudinal circulation is reduced, the flow field can be stabilized, the separation performance is improved, and the separation efficiency of small-particle-size dust is improved.

The invention provides a CFB (circulating fluid bed) boiler for heating molten salt by sucking smoke in a tail flue, and belongs to the technical field of CFB boilers coupled with molten salt heat storage. The problem that the scale and efficiency improvement of industrial production are seriously limited due to the fact that a traditional CFB boiler unit is generally lack of high-capacity and high-parameter industrial gas supply capacity is solved. The system comprises a hearth, a separating and returning system and a tail flue, the separating and returning system comprises a cyclone separator, and a low-temperature superheater high-temperature section, a low-temperature superheater low-temperature section, a high-temperature economizer, an SCR device, a low-temperature economizer and an air preheater are sequentially arranged in the tail flue in the flowing direction. A high-temperature flue gas leading-out pipeline is arranged between the low-temperature superheater high-temperature section and the low-temperature superheater low-temperature section, a low-temperature flue gas leading-out pipeline is arranged between the high-temperature economizer and the SCR device, and the outlet end of the high-temperature flue gas leading-out pipeline and the outlet end of the low-temperature flue gas leading-out pipeline are both connected with the inlet end of the mixer. The device is mainly used for the CFB boiler unit.

The utility model discloses a coupled biomass chemical looping combustion system which comprises an air reactor, a cyclone separator, a return feeder and a fuel reactor, the air reactor is communicated with the return feeder through the cyclone separator, the air reactor is configured to complete an oxidation reaction based on the received oxygen carrier and air, the generated oxidation-state oxygen carrier is conveyed to the cyclone separator under the driving of flue gas, and the corresponding oxidation-state oxygen carrier is conveyed to the return feeder through the cyclone separator; the return feeder is respectively communicated with the air reactor and the fuel reactor through a material conveying pipe, the input oxidation-state oxygen carrier is input into the air reactor and / or the fuel reactor by the return feeder, and the fuel reactor completes an oxidation-reduction reaction based on the received oxidation-state oxygen carrier and biomass fuel; the fuel reactor is used for inputting the reduced oxygen carrier into the air reactor through a return pipe; and the exhaust port of the fuel reactor is provided with a carbon dioxide trapping device so as to complete trapping of discharged carbon dioxide.

The utility model relates to a bypass ventilation system for replacing raw fuel environment-friendly workshop VOCS waste gas through co-processing, which comprises a waste gas collecting system connected with a raw fuel environment-friendly workshop, and the waste gas collecting system is respectively connected with a primary cooling source VOCs waste gas air supply system and a secondary cooling source VOCs waste gas air supply system. The primary cooling source VOCs waste gas air supply system is sequentially connected with a cyclone separator, a bag type dust collector, a bypass system fan, a mixing chamber, a kiln head air supply system, a kiln head grate cooler, a rotary kiln, a kiln tail smoke chamber, a cement kiln denitration and desulfurization system, a kiln tail dust collection system and a chimney, and the kiln tail smoke chamber is connected with the cyclone separator; and the secondary cooling source VOCs waste gas air supply system is connected with the mixing chamber. Harmful elements in a cement kiln system are reduced, the skinning risk of the preheater is relieved, co-processing of VOCs waste gas is achieved, coarse and fine separation of bypass ash is completed, the discharge pressure of a cement enterprise is relieved, and the operation cost of the cement enterprise is saved.

The invention discloses a regeneration production process of powdery waste activated carbon. The regeneration production process comprises the following steps: S1, feeding the powdery waste activated carbon into a crushing and drying furnace for crushing and drying; s2, feeding the powdery waste activated carbon into a cyclone separator and a cloth bag separator for solid-gas separation, and then feeding the powdery waste activated carbon into an activation furnace through a feeder for activation; s3, the activation furnace is preheated before feeding, and then high-pressure steam generated by the boiler is fed into the activation furnace; s4, the powdery waste activated carbon is fed into an activation furnace to be activated, then cooling is conducted, and finished activated carbon is separated out; and S5, feeding the finished product activated carbon to a mixing bin, and discharging and bagging the finished product activated carbon. Compared with the traditional method for regenerating the powdery waste activated carbon by using an earth kiln technology, the method can recover the powdery waste activated carbon to the same quality as the original activated carbon by using the physical action of high-temperature activation, and is stable in technology, high in yield, good in finished product quality and high in yield.

To properly guide a flow of granular material to a probe in a measuring system for measuring characteristics of the granular material separated from gas by a cyclone separator.SOLUTION: A separation system includes: a cyclone that separates granular material from mixed fluid containing a gas and the granular material; a container that has a truncated conical portion whose diameter gradually decreases downward and is connected to a granular material outlet of the cyclone so that the granular material separated by the cyclone falls while swirling; a conical cone disposed in the container; and a measurement probe that has a measurement unit disposed downstream of a flow of the granular material passing between a lower end of the cone and an inner wall of the container and measures a particle diameter of the granular material passing through the measurement unit.SELECTED DRAWING: Figure 1

The invention discloses a cyclone separation and moving particle bed coupled pulverized coal pyrolysis oil gas high-temperature dust removal system, and belongs to the technical field of coal clean utilization. The system comprises a cyclone separator, a fine filtration unit, a filter material cyclic regeneration unit and an intelligent control unit, the fine filtration unit comprises a particle bed, a particle bin is arranged at the top end of the particle bed, and a composite filter material layer is arranged on the particle bed; a dust-containing high-temperature oil gas pipeline and a pretreatment high-temperature oil gas pipeline are arranged at the top end of the cyclone separator, dust-containing high-temperature oil gas is introduced into the cyclone separator through the dust-containing high-temperature oil gas pipeline to be pretreated, and the pretreated dust-containing high-temperature oil gas is introduced into the particle bed through the pretreatment high-temperature oil gas pipeline to be finely filtered; and a coke breeze discharge pipe is arranged at the bottom of the cyclone separator. The invention is used for solving the technical problem of low gas-solid separation efficiency at high temperature caused by the adoption of a single filter material in the existing pulverized coal dust removal system.

The utility model belongs to the technical field of battery material preparation, and particularly discloses a spray pyrolysis system which comprises a gas hot blast stove, spray drying equipment, a pyrolysis furnace, a cyclone separator, a bag-type dust collector and an induced draft fan, a drying cavity is formed in the spray drying equipment, the gas hot-blast stove is communicated with the drying cavity through a first conveying pipe, a second conveying pipe is arranged at the bottom of the spray drying equipment, an inlet of the pyrolyzing furnace is communicated with the second conveying pipe, and an outlet of the pyrolyzing furnace is connected with an inlet of the cyclone separator through a third conveying pipe; the cyclone separator is provided with a first gas outlet and a first powder outlet. Materials are dried in the spray drying equipment, then fed into the pyrolyzing furnace and then conveyed to the cyclone separator, so that the positive electrode materials can be collected from the first powder outlet in the bottom of the cyclone separator, the purpose of producing the positive electrode materials at a time is achieved, and intermediate reaction materials do not need to be carried many times; dust and smoke generated in the transportation process are prevented from being discharged to the surrounding environment, and the cleanness of the workshop environment is guaranteed.

The present invention relates to the technical field of chemical equipment, particularly to a porous carbon activation method, which comprises: inputting a carbon raw material and a preset reaction gas into a fluidized bed reaction device to carry out an activation reaction to prepare porous carbon, and the fluidized bed reaction device comprises a feeding tank, a raw material preheating furnace, a reactor, a heating unit and a discharging tank, a gas distributor, a stirring paddle, a cyclone separator and / or a metal filter column are arranged in the reactor; the activation method comprises the following steps: S1, conveying a carbon raw material to a raw material preheating furnace, and preheating in an inert atmosphere; s2, conveying the preheated carbon raw material into a reactor, introducing reaction gas under a preset activation condition, and carrying out an activation reaction to obtain activated porous carbon; s3, under the protection of an inert atmosphere, conveying the activated porous carbon to a discharging tank, cooling, and discharging to obtain a porous carbon product; through stepped activation and multi-section temperature control design, the problems of poor product uniformity and high energy consumption of a traditional process are solved.

The invention relates to the technical field of phosphate drying, in particular to an improved phosphate drying tail gas recovery system. Comprising a spiral feeding machine, a drying cylinder, an air heater, a cyclone separator and a suction fan. The drying cylinder is arranged to be vertical, so that the occupied area of the drying cylinder is reduced, the site cost can be reduced, the production line layout can be optimized, the devices are compact, and installation and operation by operators are facilitated; by arranging a spiral plate, phosphate in the inner barrel can be continuously conveyed from bottom to top by the spiral plate, so that the phosphate can be close to the air inlet pipe, hot air entering the air inlet pipe can quickly dry the phosphate, and the drying uniformity of the phosphate in the drying barrel is guaranteed; the drying efficiency of phosphate is improved, the phosphate close to the air inlet pipe is prevented from being overheated or scorched, and then the drying quality of the phosphate is guaranteed.

A hand vacuum cleaner has a hand vacuum cleaner front end having a dirty air inlet, a cyclone and a dirt collection chamber that is external to the cyclone. The cyclone has a cyclone axis of rotation which intersects a cyclone front end and a cyclone rear end. A front door is provided which, in an open position, opens the dirt collection chamber. The front door has a first part which extends generally transverse to the cyclone axis of rotation and a second part that extends rearward at a non-zero angle to the cyclone axis of rotation and the first part.

The drying machine for sludge treatment comprises a drying cylinder, a conveying device and a waste gas treatment device, a feeding opening is formed in the top of the drying cylinder and communicates with the conveying device, a jacket is arranged on the outer wall of the drying cylinder, an electric heating wire is arranged in the jacket, and two rotating shafts are symmetrically arranged in the drying cylinder; a plurality of hollow blades are evenly welded to the side wall of each rotating shaft, the right side of the top of the drying cylinder is connected with a waste gas treatment device, and the waste gas treatment device comprises a cyclone separator and a waste gas filtering tank; generated waste gas is introduced into the cyclone separator, dust in the waste gas is separated out by utilizing centrifugal force generated by the cyclone separator, the separated gas enters the waste gas filtering tank, harmful impurities in the gas are adsorbed and filtered by the activated carbon layer, and the treated gas is discharged into the atmosphere, so that the pollution of the dust and the harmful impurities to the environment is reduced; to-be-dried sludge is heated through the inner wall of the drying cylinder, the rotating shaft and the electric heating wires in the hollow blades, the heating area is increased, and the drying efficiency is improved.

The invention relates to a chemical looping combustion variable load system based on flue gas recirculation and a control method. The system comprises a chemical looping combustion system and a flue gas recirculation system (7), the chemical looping combustion system comprises an air reactor (1), a fuel reactor (2), an AR cyclone separator (3), an FR cyclone separator (4), an AR material return device (5), an FR material return device (6), an air supply system (8) and a fuel supply system (9). By controlling the flow and temperature of recirculated flue gas of the flue gas recirculating system and cooperatively controlling the opening degree of the conical valve and the circulating flux of the system, the load of the chemical looping combustion system is flexibly adjusted, the energy consumption is reduced, the efficiency is improved, and the operation cost is reduced; and the rest high-temperature flue gas enters a flue gas treatment system to be treated, high-purity CO2 gas is obtained after heat exchange, condensation and purification, and finally efficient combustion of fuel and low-energy-consumption carbon capture are achieved.

A cone or cylindrical tube stack with narrow in-between gap circumferential surface swirling cyclone separator according to the present invention, creating swirling flow by flowing along the convex outer surface of the inner-stacked cone or cylindrical tube. The inner wall of the outer-stacked cone or cylindrical tube, which is a concave surface, serves as the wall for collecting fluid with larger or higher density particles that is opposite to the surface for swirling, which is disposed in accordance with the separation movement of larger or higher density particles that centrifuged from swirling by their inertial force. The distance that the particles travel towards the wall for collecting fluid with larger or higher density particles is short due to the narrow swirling and separating gaps, combined with the flow on the convex curved surface of the cone or cylindrical tube walls which pressure drag is low, this results in higher swirling speeds than those on the concave inner surface of conventional cyclone, significantly increasing the inertial force of particles centrifuged away from the swirling. Consequently, the separation efficiency of the cone or tube stack circumferential surface swirling cyclone separator according to the present invention is much higher than that of conventional cyclone separators. Especially in cases where the cyclone fluid separator according to the present invention is equipped with multi-stage separation, where the final stage utilizes multiple small cyclones, and in configurations where multiple cones are stacked and equipped with device for swirling and counter-flow separation, which convex fluid drainage ridges are installed on the wall for collecting fluid with larger or higher density particles, the ridges curving towards the side that the swirling flow flows to, sloping from the downstream edges of the cones or cylindrical tubes towards the upstream edges of the cones or cylindrical tubes, which counter to the swirling flow along the convex curved surface of the outer circumferential surface of cone or cylindrical tube. When working with a reverse swirling system, enabling to recycle multiple separation within the system before the fluid exits the separator, enabling high separation efficiency for separating various types of fluids mixed into emulsion or separating micron-level dust such as PM 2.5 from the air.

The utility model provides an anti-clogging cyclone separator which comprises a barrel and a cone which are coaxially connected up and down in the vertical direction, a medium inlet is formed in one side of the barrel in the tangential direction, an exhaust pipe upwards penetrating to the outside is coaxially arranged in the middle of the barrel, a particle discharge port is formed in the bottom end of the cone, and a flow guide device is further arranged at the bottom of the cone. The flow guide device comprises a plurality of flow guide plates, the flow guide plates are of conical cylindrical structures, the inclination degree of the side faces of the flow guide plates is the same as that of the cone, so that the flow guide plates form a coaxial nested structure at the bottom of the cone, and bottom discharge ports of the flow guide plates are correspondingly formed in the bottom end of the cone. According to the utility model, a plurality of layers of separation spaces are formed by the adjacent guide plates and the inner wall of the cone, and gas can be simultaneously contacted with the inner surface and the outer surface, so that the friction separation efficiency of granular impurities is improved. And the bottom of the cone is divided into smaller spaces, so that the airflow speed is higher, adsorption and adhesion are not easy to occur, and the probability of bottom blockage of the cyclone separator is reduced.

The invention belongs to the field of chemical production, and provides a green and energy-saving preparation method of high-purity anhydrous aluminum trichloride, which comprises the following steps: S1, weighing and mixing: weighing an aluminum oxide raw material and a carbon source according to a ratio, uniformly mixing to form a mixed raw material, and conveying the mixed raw material to a fluidized bed furnace; the purity of the aluminum oxide raw material meets the following conditions: Al2O3 is not less than 75%; the carbon source and the alumina raw material are consistent in particle size distribution; s2, gas preheating; s3, boiling reaction; s4, impurity removal: high-temperature flue gas at the top of the fluidized bed furnace is subjected to dust removal through a cyclone separator and then enters an impurity remover; the high-temperature flue gas after impurity removal is further cooled to 260-400 DEG C and then enters a high-temperature filter to be filtered; s5, crystallization: the flue gas filtered by the high-temperature filter enters a continuous crystallizer; s6, tail gas treatment: washing and drying the tail gas at the outlet of the continuous crystallizer and then combusting as a heat source of the heat exchanger in the step S2; and combusted tail gas enters an alkali liquor absorption tower to be absorbed and recycled. According to the method disclosed by the invention, the high-purity anhydrous aluminum trichloride can be prepared with low cost, low energy consumption and high yield.

The invention relates to axial-flow cyclone separator-particle bed coupling gas purification equipment which comprises a coupling purification part used for staged treatment and purification of impurity-containing gas; comprising an axial particle bed for loading captured particles, at least one axial-flow type cyclone separator is nested in the axial particle bed, and the bottom end of the axial-flow type cyclone separator penetrates out of the axial particle bed and then is communicated with a cyclone ash bucket; the trapping particle conveying and regenerating part is used for regenerating used dust-containing trapping particles, the bottom end of the trapping particle conveying and regenerating part is communicated with the trapping particle waiting area, and the top end of the trapping particle conveying and regenerating part can be communicated with the feeding area. The axial-flow cyclone separator and the axial particle bed are coupled in a nested manner, the process is compact, the occupied area is small, solid particles of 3 microns or above can be separated, multi-stage separation and fine treatment of impurity-containing gas are achieved, and meanwhile the requirement for integrated removal of multiple pollutants can be met.

The invention belongs to the field of long-chain alkane online analysis systems, and discloses a long-chain alkane online analysis method and system based on comprehensive two-dimensional gas chromatography and an aerosol thermal desorption analyzer. The method comprises the following steps: during sampling, sucking ambient air through a cyclone separator with a PM2.5 cutting head, then removing gas-phase organic matters through a multi-channel carbon remover, and then intensively collecting particulate matters to a thermal desorption unit (CTD); the analyte after thermal desorption is re-concentrated into a focusing trap (FT) at 45 DEG C; starting separation and analysis of GC * GC-MS (gas chromatography-mass spectrometry); and the separated compound enters a mass spectrometer for mass spectrometry. According to the method, the total time from pollutant collection to analysis is controlled within two hours, and the change characteristics of long-chain alkane in the generation and elimination process of a pollution event can be effectively captured.

The utility model discloses a circulating powder supply system of SLM printing equipment. A lower connector of a residual powder transfer powder tank is connected with a gas circuit powder conveying pipeline; an outlet of the blower is connected to an inlet of the gas circuit powder conveying pipeline; the cyclone separator is connected with an outlet of the gas circuit powder conveying pipeline; a powder outlet of the cyclone separator is connected with an inlet of the powder drying chamber, the powder drying chamber is connected with an inlet of the ultrasonic screening device, and the ultrasonic screening device is connected with the main powder storage tank. An output port in one side of the air bag is connected with an inlet of the arch breaking pipeline, an outlet of the arch breaking pipeline is internally connected with the main powder storage tank, the material supplementing tank, the top powder storage tank and the transfer powder tank, the top powder storage tank is arranged at the top of the SLM printing equipment, and an outlet of the top powder storage tank is connected to an inlet in the top of the SLM printing equipment; the material supplementing tank is connected to the gas circuit powder conveying pipeline; and the SLM printing unit is arranged on the gas circuit powder conveying pipeline. The problem that in the prior art, the efficiency is low due to the fact that powder is manually added or carried to complete the powder supply link of the printing equipment is solved.

The utility model discloses a novel sample grinding and powdering device which comprises a grinding mechanism, a material receiving mechanism and a bottle transferring mechanism, a first material receiving position is arranged below an outlet at the lower end of the grinding mechanism, and a second material receiving position is arranged adjacent to the first material receiving position; the material receiving mechanism comprises a first material receiving mechanism and a second material receiving mechanism; the bottle transferring mechanism is located on the side faces of the first material receiving position and the second material receiving position. The first material receiving mechanism comprises a first bottle placing assembly capable of ascending and descending. The second material receiving mechanism comprises a cyclone separator assembly, the cyclone separator assembly can selectively communicate with an outlet in the lower end of the grinding mechanism, and a second bottle placing assembly capable of ascending and descending is arranged below an outlet of the cyclone separator assembly. The automatic secondary sample receiving device is ingenious in design conception, simple in structure and reasonable in layout, can realize automatic secondary sample receiving and automatic sample bottle transfer, effectively reduces the loss rate of samples, and enables the recovery rate of the samples to reach 98% and 99%.

The invention discloses a raw material conveying device for polyaluminum chloride production and a working method. The raw material conveying device comprises a conveying pipe, a damping base, a storage tank, a fluidization anti-blocking module, a dust pumping system and a control unit. The upper portion of the conveying pipe is connected with hose discharging openings of a plurality of sets of storage tanks corresponding to the powder screening devices through star-shaped discharging valves. The bottom of the storage tank is mounted on a damping base, and a vibrator is fixedly mounted on the lower side of the storage tank; the storage tank is internally provided with a fluidization anti-blocking module which can fluidize materials through airflow so as to prevent blocking and caking; the dust suction system comprises a dust suction hood arranged at the top of a feeding pipe on the upper side of the storage tank, and the dust suction hood is connected with a cyclone separator capable of collecting dust generated in the feeding process and an induced draft fan through pipelines. The raw material conveying device for polyaluminum chloride production has the functions of effectively solving the problems of caking, blockage and dust caused by moisture absorption of materials and automatically adjusting conveying parameters according to material characteristics.

The invention discloses a process for producing polyaluminum chloride by recycling aluminum ash. The process comprises a primary aluminum ash pretreatment process, a secondary aluminum ash deamination process, an ammonium chloride crystallization process, a liquid polyaluminum chloride process and a solid polyaluminum chloride process, the primary aluminum ash pretreatment procedure comprises a first cyclone separator, a ball mill, a screening machine and a bag-type dust collector, the input end of the first cyclone separator is connected with a primary aluminum ash bin through conveying equipment, the coarse ash end of the first cyclone separator is connected with a feeding port of the ball mill, and a discharging port of the ball mill is connected with a feeding port of the screening machine; fine powder screened by the screening machine and secondary aluminum ash fine powder discharged by the first cyclone separator are collected into a secondary aluminum ash bin, and dust outlets of the first cyclone separator, the ball mill and the screening machine are connected with a dust inlet of the bag-type dust collector through pipelines. By arranging a series of structures, the produced polyaluminum chloride is high in purity, the economic benefit of the process is improved, tail gas is washed, and the pollution is reduced.

The invention relates to the technical field of preparation of potassium superoxide, in particular to a potassium superoxide conveying device which comprises a crushing mechanism, the crushing mechanism is connected with a cyclone separator through a first pipeline, the cyclone separator is connected with an air blower through a surge bin, and the air blower is connected with a packaging machine through a second pipeline. The air outlet end of the cyclone separator is connected with the dust remover through a third pipeline; the crushing mechanism comprises a crushing box mounted at the top of the vibration seat through a first spring seat, a second screen and a first screen are detachably mounted in the crushing box, and a plurality of first crushing cones are fixedly mounted on the side, facing the first screen, of the second screen; a plurality of second crushing cones matched with the first crushing cones are fixedly installed on the side, facing the second screen, of the first screen, a feeding pipe is fixedly installed on the side wall of the crushing box, and the feeding pipe is located between the second screen and the first screen. And the crushing mechanism crushes the material blocks by combining modes of vibration, knocking, collision and the like, so that the efficiency is high, and the cost is low.