700 results about "Cyclonic spray scrubber" patented technology

A cyclone bin assembly for a hand vacuum cleaner has a cyclone chamber and a dirt collection chamber. The cyclone chamber has a cyclone air inlet, a cyclone air outlet, a dirt outlet, a cyclone chamber front end, a cyclone chamber rear end and cyclone axis of rotation that intersects a cyclone chamber front end wall and a cyclone chamber rear end wall. The dirt collection chamber has a dirt collection chamber front end having a dirt collection chamber front end wall and an axially spaced apart dirt collection chamber rear end having a dirt collection chamber rear end wall. A forward portion of the cyclone bin assembly is rotationally mounted between a closed position wherein the cyclone chamber and the dirt collection chamber are closed and an open position wherein a rear portion of the cyclone chamber and a rear portion of the dirt collection chamber are opened.

The invention relates to a feed coal preheating and drying and semicoke cooling coupled low-rank coal pyrolysis system and method. The low-rank coal pyrolysis system comprises a low-rank coal pyrolysis device, an air fan, an air secondary heat supplementing device and a cyclone dust collector, the low-rank coal pyrolysis device is sequentially provided with a coal direct drying section, a low-temperature pyrolysis section, a medium-high-temperature pyrolysis section and a semicoke indirect cooling section from top to bottom; the lower part of the semicoke indirect cooling section is provided with an air inlet, and the upper part is provided with a hot air outlet which is connected with the hot air inlet of the coal direct drying section through a hot air pipeline; and the hot air pipeline is provided with an air secondary heat supplementing device. In the feed coal drying and semicoke cooling process, air is adopted as carrier gas for heat exchange, sufficient recovery of semicoke heat is achieved, the recovered heat is used for drying and preheating the feed coal, and comprehensive utilization of the heat is achieved; the process characteristics of coal drying preheating, pyrolysis and semicoke cooling are fully considered, an economical and reasonable heat exchange form is adopted, the process is simple, the heat recovery efficiency is high, and the productivity of the pyrolysis device is high.

The utility model relates to an air supplement structure of a dry quenching primary cyclone dust collector, which comprises a primary dust collector and a central pipe, the central pipe is arranged at the center of the upper part of the primary dust collector, a circulating gas inlet of the primary dust collector is connected with a dry quenching furnace, and the bottom of the central pipe is communicated with an inner cavity of the primary dust collector; a circulating gas outlet in the upper end of the central pipe is connected with the waste heat boiler, a gas circulation channel is formed in the pipe wall of the central pipe, an air inlet is formed in the upper end of the gas circulation channel in the pipe wall of the central pipe, and an air outlet is formed in the lower end of the gas circulation channel in the pipe wall of the central pipe towards the interior of the central pipe. And the air leading-in outlet is an outlet which is vertically inward in the radial direction. According to the utility model, an air introduction mode is provided, burning loss of combustible gas components in circulating gas and a small amount (10%-20%) of residual fine coke powder in dust removal in the central pipe of the dust remover is realized, burning loss of most (80%-90%) removed coke powder is avoided, carbon burning loss in a carbon melting reaction is reduced, and carbon emission reduction is realized.

The invention discloses a low-energy-consumption maltol production method and application, and belongs to the technical field of maltol production.The production method is characterized in that a cyclone dust collector is additionally arranged on the basis of an original bag-type dust collector, and the cyclone dust collector is connected with the bag-type dust collector through an air inducing pipeline. A traditional drying mode is broken through, waste steam in the previous drying process is subjected to hot air recovery, it can be guaranteed that the normal drying process is completed, energy consumption is reduced, the production efficiency is further improved, the production cost is saved, residual dust is effectively recovered, the influence of environmental odor is reduced, and the environment-friendly benefit is achieved.

The invention discloses an efficient treatment method for waste plastic pyrolysis, which is characterized in that waste plastic is pretreated into 200-300 [mu] m powder, the reaction surface area is increased, and the pyrolysis efficiency is promoted; the powder and the Fe-Zr / ZSM-5 catalyst are mixed in a three-strand impinging stream feeding device, so that the mixing uniformity and the reaction acceleration are ensured. In the descending reactor, the mixture is pyrolyzed under the controlled carbon dioxide atmosphere and heating rate, and local overheating is avoided; a gas phase, a liquid phase and a solid phase generated by pyrolysis are effectively separated and preliminarily cooled through a cyclone separator and a cooling system; large-particle dust is removed from pyrolysis gas in an inner cylinder cyclone dust collector of the integrated radial bed, and dust removal and dechlorination are performed through an interlayer filled with modified activated carbon, so that the purity of pyrolysis oil is improved; pyrolysis gas is cooled to the room temperature, and pyrolysis oil, gas and solid residues are conveniently collected; through comparative analysis of the embodiment, the particle size range of 200-300 microns is determined as the optimal operation condition, at the moment, the pyrolysis efficiency is highest, and the quality of the generated pyrolysis oil is optimal.

The invention discloses a steel slag treatment process and equipment, and relates to the technical field of steel slag treatment.The steel slag treatment equipment comprises a separation pipe arranged at an outlet of a cyclone dust collector, a pressurizing part is arranged between the separation pipe and the outlet of the cyclone dust collector, and the separation pipe is provided with a spherical dust removal net and a metal elastic piece; and after the dust removal net is blocked, the air pressure in the separation pipe is increased, so that dust on the dust removal net is shaken off by the metal elastic piece and the reverse bend, and a dust collection cavity is formed in the air inlet side, located on the dust removal net, of the separation pipe. Steel and iron materials in the steel slag are effectively separated from aggregate, the steel and iron materials are subsequently used for concrete or cement aggregate, waste utilization is effectively carried out, a dust removal net of the secondary dust remover can change the state of a metal elastic piece according to the change of air pressure, and therefore the dust removal net is adjusted, dust blocked on the dust removal net is cleaned away, and long-term use is facilitated.

The invention discloses a dust removal and safety guarantee integrated system for coal mine underground drilling. Comprising a mining multi-parameter sensor, an electromagnetic pneumatic valve controller, a cyclone dust collector, a dry bag-type dust collector, a gas drainage pipeline, a dust extraction pipeline, a hole sealing dust extraction cover, a compressed air conveying pipe, an electromagnetic pneumatic valve, a front-stage air ejector, a rear-stage air ejector and an air extraction air ejector. The hole sealing dust extraction cover captures drilling dust, the drilling dust enters the cyclone dust collector through the dust extraction pipeline to separate large particles, and air outlet of the drilling dust is divided into two ways: the first way is connected with the gas drainage pipeline through the air extraction air ejector to convey harmful gas, and the second way is connected with the dry bag-type dust collector to filter fine particles. The mining multi-parameter sensor monitors the concentration, the pressure difference, the temperature and the humidity of CH4, CO and CO2, the electromagnetic pneumatic valve controller dynamically switches gas circuits based on data, dust collection, gas drainage, water isolation and fire prevention and control are achieved, the drilling operation safety and the environment quality are remarkably improved, and the device is suitable for a high-gas mine.

The utility model discloses a molybdenum oxide rotary kiln high-temperature tail gas smoke dust treatment device which comprises a fresh air heat exchanger connected to one end of a smoke exhaust pipe of a rotary kiln, a smoke outlet end of the fresh air heat exchanger is connected with a cyclone dust collector, and one end of a fan air outlet of the cyclone dust collector is connected with a convection type heat exchange assembly. The utility model relates to the technical field of molybdenum oxide rotary kiln tail gas treatment, high-temperature waste heat in tail gas is utilized to preheat fresh air used by a rotary kiln, the temperature of the fresh air is increased, and then the combustion efficiency of the rotary kiln is improved. The cooled tail gas further enters a cyclone dust collector, large-particle dust in the flue gas is settled in the cyclone dust collector under the driving action of spiral airflow, and after further heat exchange is carried out on the flue gas subjected to primary dust removal, deep purification of the tail gas is achieved in cooperation with a spraying purification assembly.

The invention discloses a liquefied natural gas factory heat-conducting oil furnace tail gas safety treatment device which comprises a cooling assembly, a cyclone dust collector and a purification tower, the cyclone dust collector is sleeved with a cooling sleeve, and the cooling assembly is connected with the cyclone dust collector through a first conveying pipe; the cyclone dust collector is connected with the purification tower through a second conveying pipe, the cooling assembly comprises a tank body, a heat exchange coil pipe is arranged in the tank body, the heat exchange coil pipe comprises an outer pipe body and an inner pipe body, the inner pipe body is sleeved with the outer pipe body, and an interlayer flow channel is formed between the inner pipe body and the outer pipe body. According to the technical key points, tail gas is cooled through the cooling assembly and heat is recycled, most of dust particle impurities in the tail gas are removed through the cyclone dust collector, the tail gas is secondarily cooled through the cooling sleeve and heat is recycled, the dedusted gas enters the purification tower, harmful substances are removed, and the dedusted gas is cooled again. And the purified tail gas reaches the standard at low temperature and is discharged.

The invention relates to the technical field of waste mulching film treatment, in particular to waste mulching film treatment heavy residue separation equipment which comprises a separation box, a conveyor is installed at the front end of the separation box, a feeding hopper is fixedly connected to the front end of the top of the separation box, and a material distribution square box is fixedly connected to the outer side of the separation box. A cyclone dust collector is installed at the rear end of the separation box, the top of the material separation square box is fixedly connected with the cyclone dust collector through a connecting pipe, a centrifugal fan is fixedly installed at the top of the cyclone dust collector, multiple functions of iron removal, smashing, screening, centrifuging, flapping, winnowing, dust removal and the like are integrated, the occupied area of the equipment and the material transfer link are reduced, and the production efficiency is improved. A complete, efficient, automatic and environment-friendly waste mulching film recycling solution is provided, the core innovation point is the composite motion design of the separation assembly and the automatic discharging design of the magnet assembly, the overall practicability is high, and very high market application value is achieved.

The invention discloses a small multifunctional integrated drying device, and relates to the technical field of industrial drying experiment equipment. The small multifunctional integrated drying device comprises a bottom plate, a vertical supporting plate is fixedly connected to the middle of the upper surface of the bottom plate, a fluidized bed drying chamber, a spray drying chamber, a main controller, a shared centrifugal fan and a shared electric heater are fixedly installed on the front face of the vertical supporting plate, and an air filter and an induced draft fan are fixedly installed on the upper surface of the bottom plate; a cyclone dust collector is fixedly installed on the back face of the vertical supporting plate, a three-way pipe is fixedly connected to the top of the shared electric heater, a fluidized bed feeder is fixedly installed on one side of the top of the fluidized bed drying chamber, and a supporting ring, an annular base, a motor, a fixing plate and an air pressure sensor are fixedly installed on the lower portion of the inner wall of the fluidized bed drying chamber. The system can integrate the fluidized bed function and the spray drying function, and energy-saving and efficient operation is achieved through the shared air path, the heat energy recovery system and the self-cleaning distribution plate.

The invention provides a cement dust collecting device, which belongs to the technical field of cement production and comprises a cyclone dust collector, a filtering mechanism, a cleaning mechanism, an adjusting mechanism, a control mechanism and a driving mechanism. Wherein the cyclone dust collector comprises an air inlet and an air outlet; the filtering mechanism is assembled on the cyclone dust collector and comprises a filtering bag, and the filtering bag is arranged in the cyclone dust collector by adopting a rotatable unfolding structure and is used for separating large-particle-size particles in the cement dust; the cleaning mechanism is fixedly arranged on one side of the inner wall of the cyclone dust collector, and the cleaning end of the cleaning mechanism is attached to the outer side of the cloth bag and is matched with the rotation of the filter bag to realize all-directional dead-corner-free suction; the two adjusting mechanisms are symmetrically arranged on the two sides of the suction opening of the cleaning mechanism and used for adjusting the opening and closing degree of the suction opening. The device adopts the grading design of cyclone centrifugal coarse separation and filter bag fine filtration, and dust is continuously and dynamically removed from the filter bag, so that the dust recovery efficiency is improved.

The invention discloses a furnace rear flue gas water-cooling comprehensive temperature control system and a matched cooling water amount control method, and particularly relates to the technical field of flue gas purification and environmental protection, the furnace rear flue gas water-cooling comprehensive temperature control system comprises a semi-dry desulfurization tower, a cyclone dust collector, a bag-type dust collector and a low-temperature SCR denitration device of which the output ends are sequentially communicated in series; the outlet flue of the cyclone dust collector and the inlet flue of the bag-type dust collector are respectively and fixedly communicated with a communicating flue which is connected with an electric air door in series, and the surface type water-cooling flue gas cooling system comprises a water-cooling flue gas cooler which is at least communicated with a cooling water supply pipeline. A comprehensive temperature control system combining a surface type water cooling flue gas cooling system and a flue gas emergency water spraying cooling system is adopted, a matched cooling water amount control algorithm is formulated from the enthalpy value heat balance principle, the surface type cooling water flow and the spraying water amount are accurately controlled, it is effectively ensured that the boiler rear flue gas temperature meets the flue gas purification process requirement, and the boiler rear flue gas purification efficiency is improved. Meanwhile, heat released in the flue gas cooling process is recycled, and the circulating efficiency of the power plant is further improved.

The invention relates to the technical field of casting sand production, and discloses a drying sand and roasting sand universal type heat recovery system which comprises a box body, a boiling device is arranged on the box body and used for suspending and fluidizing sand particles, and a heat recovery device is arranged on the box body and used for collecting heat from gas exhausted from the boiling device. The heat recovery device comprises two gas collecting hoods, the two gas collecting hoods are both communicated with the top of the box body, used for collecting high-temperature gas generated in the box body and connected with a cyclone dust collector through a sixth pipeline, and the cyclone dust collector is connected with a second induced draft fan through a fourth pipeline and connected with a kiln and a burner through a fifth pipeline. The device is used for heating casting sand or other materials by using the recovered heat. And through comprehensive application of the boiling device and the heat recovery system, heat energy recovery in the production of the roasting sand for casting is realized, and the production cost and the energy consumption are effectively reduced.

The utility model discloses a limestone calcination waste gas filtering and purifying device which comprises a base, a cyclone dust collector, an electrostatic dust collection box and a plate heat exchanger, and the cyclone dust collector, the electrostatic dust collection box and the plate heat exchanger are sequentially and fixedly arranged on the upper end face of the base. An air outlet in the upper end of the cyclone dust collector communicates with the electrostatic dust collection box through a pipeline, a vertical partition plate is fixedly arranged on the bottom face in the electrostatic dust collection box, and an anode plate is fixedly arranged on the side, facing an air inlet of the electrostatic dust collection box, of the vertical partition plate; a channel for waste gas to pass through is arranged above the vertical partition plate, an outlet of the electrostatic dust collection box is communicated with the plate heat exchanger, and a gas outlet of the plate heat exchanger is communicated with the purification and adsorption assembly. The cyclone dust collector is combined with the electrostatic dust collection box, so that the dust collection efficiency is improved.

This invention relates to the technical field of poultry manure treatment equipment, and discloses a livestock and poultry manure drying and treatment mechanism, including a preheating furnace and a drying furnace. Both the preheating furnace and the drying furnace have stirring components installed in their inner cavities. The preheating furnace has a jacket on its outer wall. The inner cavity of the drying furnace communicates with the jacket, and a cyclone dust collector is installed between the inner cavity of the drying furnace and the jacket. One end of the cyclone dust collector's air inlet communicates with the inner cavity of the drying furnace, and one end of the cyclone dust collector's air outlet communicates with the air inlet of the jacket. This livestock and poultry manure drying and treatment mechanism achieves highly efficient dehydration: by installing a unique stirring component inside the drying furnace, especially an inclined trowel, the fluid livestock and poultry manure can be continuously and evenly spread onto the inner wall of the drying furnace and scraped, greatly increasing the contact area between the manure and hot air, accelerating the evaporation rate of moisture, and achieving rapid dehydration. Compared with traditional treatment methods, the dehydration efficiency is significantly improved.

The invention belongs to waste gas treatment equipment, and particularly relates to an automatic volatile organic waste gas treatment device which comprises a cyclone dust collector and a UV lamp tube, an inner wall scraping assembly is arranged in the cyclone dust collector, a rotary filtering assembly is connected to one side of the cyclone dust collector through a pipeline, and an arc-shaped plate rotating assembly is arranged in the rotary filtering assembly. An air inlet bin is arranged on one side of the rotary filtering assembly, a filtering plate replacing mechanism and a filtering plate replacing bin are arranged on one side of the rotary filtering assembly, a multi-stage filtering barrel is connected to the other side of the rotary filtering assembly through a pipeline, an exhaust pipe is arranged at the lower end of the outer side of the multi-stage filtering barrel, and a discharging mechanism is correspondingly arranged at the lower end of the activated carbon conveying assembly. The filter plate replacement mechanism is arranged to automatically replace the filter plate, the filter plate replacement mechanism is matched with the filter plate replacement bin for automatic installation, meanwhile, multiple times of treatment are conducted through the filter cartridges, activated carbon and the UV lamp tubes in the multi-stage filter barrel, and the gas treatment effect is improved.

The invention provides an integrated device integrating organic solid waste treatment, metal recovery and carbon material preparation and a use method of the integrated device, and belongs to the field of environmental science and engineering. The problems that the utilization rate of organic solid waste heat energy is low, the recovery rate of metal-containing waste materials is low, and the carbon yield and quality of carbon materials prepared from agriculture and forestry biomass waste are low are solved. The integrated device comprises a feeding system, a solid waste heat treatment system, a steam utilization system, a tail gas purification and recovery system, a biomass carbonization system and a metal pyrolysis and recovery system, the solid waste heat treatment system comprises a pyrolysis gasification chamber and a high-temperature cracking chamber, and the high-temperature cracking chamber is divided into a left chamber and a right chamber; the steam utilization system comprises a high-pressure steam chamber, a low-pressure steam chamber and a hot water chamber, and the tail gas purification and recovery system comprises a cyclone dust collector, a spraying denitrification and denitration chamber, a water bath purification chamber, an electrostatic dust collector and a gas collector. The method is mainly used for organic solid waste treatment, metal recovery and carbon material preparation.

The utility model provides a device for separating silicon powder from reduced tail gas. The device comprises a cyclone dust collector, a first filtering mechanism, a primary condenser, a secondary condenser, an air cooler, a multi-stage condenser, a condensate tank, a liquid phase filter and a machine pump, a gas phase outlet of the cyclone dust collector is connected with an inlet of the first filtering mechanism, a gas phase outlet of the first filtering mechanism is connected with a tube pass inlet of the first-stage condenser, a tube pass outlet of the second-stage condenser is connected with a gas phase inlet of the air cooler, and a liquid phase outlet of the air cooler is connected with an inlet of the condensate tank. A gas phase outlet of the air cooler is connected with a tube pass inlet of the multi-stage condenser, a tube pass outlet of the multi-stage condenser is connected with the condensate tank, an outlet of the condensate tank is connected with the liquid phase filter, and a liquid phase outlet of the liquid phase filter is connected with the pump so as to discharge a chlorosilane liquid phase; according to the scheme, large-particle silicon powder and small-particle silicon powder are separated according to the cyclone separation principle, then the silicon powder is separated through liquid-phase separation, liquid-phase chlorosilane is recycled, and grading and step-by-step separation and utilization of the silicon powder are achieved.

The invention relates to the technical field of environmental protection equipment, in particular to a double-chamber lime kiln tail gas dust multi-stage synergistic trapping device which comprises a cyclone dust collector, a condensation dehumidification unit and a graded filtering unit which are sequentially connected through a pipeline. The condensation dehumidification unit comprises a condensation dehumidification box, a refrigeration coil arranged in a snake shape is arranged in the condensation dehumidification box in the horizontal transverse direction, and the water inlet end and the water outlet end of the refrigeration coil penetrate through the side wall of the condensation dehumidification box and extend to the outer side; the graded filtering unit comprises a filtering box, a first filtering net, a second filtering net, a third filtering net and a fourth filtering net are transversely and sequentially arranged in the filtering box in the tail gas flowing direction, and a gas outlet pipe is arranged at the position, close to the fourth filtering net, of the filtering box; the problems of hardening, corrosion and the like of the filter bag caused by high humidity are solved, the stable proceeding of the subsequent filtering process is ensured, the service life of a filtering part is prolonged, and the maintenance cost and the replacement frequency of equipment are reduced.

The invention relates to the technical field of dust treatment, and discloses a dust recovery device for a grinding miller, which comprises a recovery tank, an air inlet pipe, an exhaust pipe and a slag discharge pipe, the air inlet pipe and the exhaust pipe are communicated and mounted on the side wall of the recovery tank, the slag discharge pipe is mounted at the bottom of the recovery tank, a check valve is mounted on the slag discharge pipe, and the air inlet pipe is connected with a cyclone dust collector. The rotating disc is rotationally connected in the recycling tank, the partition plate is fixedly arranged on the recycling tank, the partition plate and the rotating disc are both located between the air inlet pipe and the exhaust pipe, the partition plate is located below the rotating disc, and a third rotating assembly used for driving the rotating disc to rotate is arranged on the recycling tank; by arranging the movable semicircular plate, a closed cylindrical space is formed during dust removal, a to-be-cleaned cloth bag is isolated from the surrounding environment, dust shaken off by pulse jet is limited in the closed space and directly falls into the bottom of a recovery tank through a round hole, and the risk that the dust suspends and diffuses in the box body and is adsorbed by an adjacent cloth bag is avoided; and secondary pollution is completely eradicated from the source.

The invention belongs to the technical field of converter gas treatment, and relates to a converter high-temperature vaporization flue boiler outlet gas treatment device, which comprises a first conveying pipeline, a second conveying pipeline, a cyclone dust collector and a tempering dust collector, an inlet of the first conveying pipeline is used for being connected with a coal gas outlet of a converter vaporization flue boiler, an outlet of the first conveying pipeline is connected with an inlet of the cyclone dust collector, an inlet of the second conveying pipeline is connected with an outlet of the cyclone dust collector, and an outlet of the second conveying pipeline is connected with an inlet of the tempering dust collector. An outlet of the tempering dust remover is connected with an electrostatic dust remover; the first conveying pipeline is provided with fire extinguishing equipment used for extinguishing sparks in the pipe section, and the second conveying pipeline is provided with at least one fire pipe evaporator arranged in the flowing direction of coal gas. The problem that the fire tube is blocked due to zinc liquid drops, high-temperature molten ash and the like condensed by zinc steam in the coal gas heat and mass recovery process through the fire tube evaporator is solved.

The invention relates to the technical field of flash reduction processes, and discloses a coal-based reducing gas and flash reduction integrated flash reduction device and method.The coal-based reducing gas and flash reduction integrated flash reduction device comprises a coal-based gas tower body and a flash reduction tower body, the coal-based gas tower body is communicated with the flash reduction tower body through a molten pool, and the coal-based gas tower body is used for conveying reducing gas to the flash reduction tower body; the injection assembly comprises a fine ore injection part and a fine ore injection device, the fine ore injection part is arranged on the flash reduction tower body, the fine ore injection device is arranged on the fine ore injection part, and the fine ore injection part is used for conveying fine iron ore and flux into the flash reduction tower body; the circulating assembly comprises a cyclone dust collector, a circulating part and a dedusting ash blowing part, the cyclone dust collector is communicated with the flash reduction tower body, the circulating part is arranged on the cyclone dust collector and is communicated with the flash reduction tower body through the dedusting ash blowing part, and the dedusting ash blowing part is used for conveying dedusting ash into the flash reduction tower body. The process is simplified, raw materials are saved, and production efficiency and raw material utilization rate are improved.

The present application aims to provide a fluidized bed, comprising: a cylinder, a centrifugal fan and a silo; the cylinder is a cylindrical container structure with a closed upper end and an open lower end; a baffle is arranged at the lower end of the cylinder, and the baffle has a first air port and a second air port; wherein the first air port is distributed close to the center of the baffle, and the second air port is distributed along the periphery of the baffle; the cylinder is connected with the upper end of the silo through the baffle; the centrifugal fan is located inside the cylinder and close to the upper end of the cylinder; an exhaust port is provided at the upper end of the cylinder; the lower end of the silo is connected with an air inlet; by using the centrifugal fan as a driving method and then arranging a baffle used in conjunction with the centrifugal fan, an internal and external spiral airflow can be formed in the cylinder, so that the dust can be naturally refluxed under the action of the internal and external spiral airflows, which can overcome the shortcomings of filtering dust removal and cyclone dust removal.

The invention discloses a wet-type and dry-type combined dust removal system of a rotary drilling machine and an operation method of the dust removal system, and relates to the technical field of mining machinery. Comprising a wet-type dust removal system and a dry-type dust removal system, wherein the wet-type dust removal system comprises a water tank with a heat preservation layer, a flow regulating valve, a one-way valve, a heat preservation water pipe, a quick exhaust valve, an air inlet pipe, a water return pipe, a second rubber pipe connector and a main air pipe; the dry dust removal system comprises a pulse valve body, a throttling device, a valve cover, a valve, a spring, a mechanical pulse controller, a cloth bag dust removal box, a cyclone dust collector, a small air bag and a blowing pipe. In the aspect of dust removal, a wet system and a dry system cooperate, an orifice settling box assists, efficient dust falling is achieved, the working environment is improved, and personnel health is protected; the device has good performance in terms of environmental adaptability, flow control, connection, cloth bag dust removal, accumulated dust treatment and system maintenance.

The utility model relates to an active lime production system suitable for limestone raw materials with various strengths. The system comprises an inner cavity type preheating bin, a discharging port of a supplied material belt conveyor is connected with a feeding port of the inner cavity type preheating bin, a discharging port of the inner cavity type preheating bin is connected with a first feeding port of a chain scraper conveyor, a discharging port of the first chain scraper conveyor is connected with a feeding port of a feeding hopper, and a discharging port of the feeding hopper is connected with a feeding port of a vibrating screen. Materials on the vibrating screen are fed into the sintering system through a chain scraper conveyor II; an air outlet of the sintering system is connected with an air inlet of the kiln tail dust collector and an air inlet of the cyclone dust collector, an air outlet of the cyclone dust collector is connected with an inlet of the high-temperature fan, an outlet of the high-temperature fan is connected with an air inlet of the inner cavity type preheating bin, and an air outlet of the inner cavity type preheating bin is connected with an air inlet of the kiln tail dust collector. According to the utility model, the limestone raw material easy to pulverize can be ensured to normally produce active lime, meanwhile, the low-quality limestone raw material is utilized to the maximum extent, and the production cost of an enterprise is reduced.

The invention discloses a novel carrier gas circulation dehumidification drying process system which comprises a carrier gas heater, a drying machine, a cyclone dust collector, a bag-type dust collector, a film dehumidifier, an adsorption dehumidifier and a regeneration heater, and the carrier gas heater is communicated with the drying machine; the top of the drying machine is sequentially connected with the cyclone dust collector and the bag-type dust collector; the bag-type dust collector is connected with the membrane dehumidifier; the membrane dehumidifier is connected with the adsorption dehumidifier; and the adsorption dehumidifier is connected with the regeneration heater. According to the novel carrier gas circulation dehumidification drying process system, the membrane dehumidifier and the adsorption dehumidifier are combined to remove humidity in circulation carrier gas, cooling is not needed in the dehumidification process, the energy utilization rate of the circulation carrier gas is increased to 85% or above, meanwhile, waste gas emission is reduced to 15% or below, more energy is saved, low carbon is achieved, and environment friendliness is achieved. The method can be widely applied to the carrier gas circulation drying field.

The utility model discloses an electrolytic bath pneumatic chute dust collector which comprises a dust collection main machine, the bottom of the dust collection main machine is fixedly connected with a moving assembly, the two sides of the dust collection main machine are fixedly connected with fixing shafts, the outer sides of the fixing shafts are movably connected with moving handrails, and the front face of the dust collection main machine is fixedly connected with a control mechanism. The top of the dust collection main machine is fixedly connected with a connecting flange, the top of the connecting flange is fixedly connected with a telescopic hose, one end of the telescopic hose is fixedly connected with an operation assembly, the back of the dust collection main machine is fixedly connected with a dismounting plate, and an exhaust hole is formed in the position, away from the lower portion of the dismounting plate, of the back of the dust collection main machine. The top of each mounting plate is fixedly connected with a negative pressure generator, a main cyclone dust collector and an auxiliary cyclone dust collector, the device is simple in structure and convenient to mount, materials such as aluminum oxide in an electrolytic workshop can be efficiently recycled, the dust control problem is solved, and secondary pollution caused by dust disturbance is avoided.

The utility model belongs to the field of blast furnace equipment, and relates to a blast furnace gas heating system which comprises a valve of a blast furnace gas pipeline, a cyclone dust collector, a flowmeter, a thermometer, a valve of a flue gas pipeline and a heat exchanger, and a heating gas source is taken from flue gas of a hot blast stove. The system is arranged between a blast furnace gravity dust collector and dry dust collection and serves as a bypass of a normal gas pipeline. When the blast furnace gas is low in temperature and needs to be heated, the flue gas adjusting valve on the hot blast stove flue gas pipeline is opened, high-temperature hot blast stove flue gas enters the heat exchanger, meanwhile, the gas adjusting valve on the heating system pipeline is opened, and the blast furnace gas flows through the heated heat exchanger after passing through the cyclone dust collector, so that the blast furnace gas is heated and then flows to the dry dedusting system. Heated hot-blast stove smoke flows back to the hot-blast stove waste gas pipeline and is discharged through a chimney. Blast furnace gas is heated through hot blast stove flue gas, low-temperature gas is prevented from directly entering a dry-method system, cloth bag hardening is prevented, normal work of the dry-method system is ensured, and the operation stability of a blast furnace system is improved.

The utility model belongs to hot -blast circulating device technical field discloses hot -blast circulating device. This hot -blast circulating device includes heater, circulating fan, first air pipe, second air pipe, cylinder, third air pipe, cyclone dust collector and fourth air pipe, and the air outlet of heater is communicated with the first end of first air pipe, and can output heating air, the second end of first air pipe is communicated with the air inlet of circulating fan, the first end of second air pipe is communicated with the air outlet of circulating fan, the material of waiting for heating can be placed in the cylinder, the air inlet of cylinder is communicated with the second end of second air pipe, the air outlet of cylinder is communicated with the first end of third air pipe, the second end of third air pipe is communicated with the air inlet of cyclone dust collector, and cyclone dust collector is configured as removing the sundries in the third air pipe, and the both ends of fourth air pipe are communicated with the air outlet of cyclone dust collector and the air inlet of circulating fan, this hot -blast circulating device avoids sundries to adhere to heater, and heating air circulation is unobstructed, reduces cleaning workload.