518results about "Coke quenching" patented technology

The utility model relates to a limit protection device of a dry quenching elevator, which belongs to the technical field of coking dry quenching equipment and is used for protecting the limit of the dry quenching elevator. According to the technical scheme, a base is a rectangular plate, a fixing support is perpendicularly welded to the plate face of the base, an adjusting movable plate is connected with the fixing support through an adjusting fastening bolt, a limiting fixing plate is perpendicularly welded to the front end of the adjusting movable plate, and a U-shaped limiting plate is fixed to the plate face of the limiting fixing plate through a limiting fixing bolt; the two upper limiting guide plates and the two lower limiting guide plates are located on the two sides of the U-shaped limiting device respectively and are perpendicularly connected with the plate face of the limiting fixing plate in a welded mode respectively, and the upper limiting guide plates and the lower limiting guide plates on the two sides of the U-shaped limiting device respectively form two V-shaped guide grooves. The elevator limiting device is simple in structure and reliable in work, the elevator can be protected from being damaged due to the fact that the elevator is scratched by the running elevator, safety and equipment hidden dangers are effectively eliminated, and normal running of the elevator is guaranteed.

Industrial cars for holding high-temperature materials, such as flat push hot cars for transporting hot coke and deposits, and associated systems and methods are disclosed herein. In some embodiments, an industrial car can include an at least partially enclosed hot box with a base and sidewalls, and one or more of the base or sidewalls can be covered by surface plates. The surface plates can be arranged in a floating configuration with gaps therebetween, such that the surface plates can move relative to one another and thermally expand without exerting excessive compressive force against adjacent surface plates. In some embodiments, the hot box can also include a roof with a first non-curved member and a second non-curved member abutting the first non-curved member. In some embodiments, the industrial car can include one or more emission ducts to remove dust and exhaust from within and around the industrial car.

The utility model relates to a dry quenching primary dust remover structure which is characterized in that a layered dust removal device is arranged in a dust remover body and consists of parallel interlayers, small interlayer ash hoppers and interlayer ash discharge channels; an inlet dust removal channel is arranged between the dust remover inlet and the dust remover ash hopper, and an outlet dust removal channel is arranged between the dust remover ash hopper and the dust remover outlet; the parallel interlayer divides the inlet dedusting channel and the outlet dedusting channel into an upper layer and a lower layer; the middle part of the parallel interlayer is connected with an interlayer ash discharge channel through an interlayer small ash hopper; a bottom outlet of the interlayer ash discharge channel is communicated with an ash discharge port of the dust remover; according to the utility model, the dust removal efficiency of the primary dust remover is improved, and meanwhile, the dust removal convenience is ensured.

This invention provides processes and systems for converting biomass into high-carbon biogenic reagents that are suitable for a variety of commercial applications. Some embodiments employ pyrolysis in the presence of an inert gas to generate hot pyrolyzed solids, condensable vapors, and non-condensable gases, followed by separation of vapors and gases, and cooling of the hot pyrolyzed solids in the presence of the inert gas. Additives may be introduced during processing or combined with the reagent, or both. The biogenic reagent may include at least 70 wt %, 80 wt %, 90 wt %, 95 wt %, or more total carbon on a dry basis. The biogenic reagent may have an energy content of at least 12,000 Btu / lb, 13,000 Btu / lb, 14,000 Btu / lb, or 14,500 Btu / lb on a dry basis. The biogenic reagent may be formed into fine powders, or structural objects. The structural objects may have a structure and / or strength that derive from the feedstock, heat rate, and additives.

This invention provides processes and systems for converting biomass into high-carbon biogenic reagents that are suitable for a variety of commercial applications. Some embodiments employ pyrolysis in the presence of an inert gas to generate hot pyrolyzed solids, condensable vapors, and non-condensable gases, followed by separation of vapors and gases, and cooling of the hot pyrolyzed solids in the presence of the inert gas. Additives may be introduced during processing or combined with the reagent, or both. The biogenic reagent may include at least 70 wt %, 80 wt %, 90 wt %, 95 wt %, or more total carbon on a dry basis. The biogenic reagent may have an energy content of at least 12,000 Btu / lb, 13,000 Btu / lb, 14,000 Btu / lb, or 14,500 Btu / lb on a dry basis. The biogenic reagent may be formed into fine powders, or structural objects. The structural objects may have a structure and / or strength that derive from the feedstock, heat rate, and additives.

The invention relates to a bracket structure for a chute area of a dry quenching furnace. The bracket structure is formed by building a plurality of layers of bracket bricks; and a plurality of supporting pieces are arranged between every two adjacent layers of bracket bricks, the supporting pieces are hard supporting pieces, the thickness of the supporting pieces is the same as that of mortar joints, the top faces of the supporting pieces make direct contact with the upper layer of bracket bricks, and the bottom faces of the supporting pieces make direct contact with the lower layer of bracket bricks. The supporting pieces are placed in the refractory mortar joints between the bracket brick layers, so that the problems of sinking of the annular air duct and cracking of the chute partition wall caused by deformation of the bracket mortar joints and inaccurate bracket elevation control are effectively prevented, the masonry quality of the dry quenching furnace is improved, and the service life of the dry quenching furnace is prolonged.

This invention provides processes and systems for converting biomass into high-carbon biogenic reagents that are suitable for a variety of commercial applications. Some embodiments employ pyrolysis in the presence of an inert gas to generate hot pyrolyzed solids, condensable vapors, and non-condensable gases, followed by separation of vapors and gases, and cooling of the hot pyrolyzed solids in the presence of the inert gas. Additives may be introduced during processing or combined with the reagent, or both. The biogenic reagent may include at least 70 wt %, 80 wt %, 90 wt %, 95 wt %, or more total carbon on a dry basis. The biogenic reagent may have an energy content of at least 12,000 Btu / lb, 13,000 Btu / lb, 14,000 Btu / lb, or 14,500 Btu / lb on a dry basis. The biogenic reagent may be formed into fine powders, or structural objects. The structural objects may have a structure and / or strength that derive from the feedstock, heat rate, and additives.

The present invention belongs to the technical field of industrial flue gas carbon capture, and particularly relates to a system and method for realizing carbon and nitrogen co-production by using the dry coke quenching off-gas. The system includes a dry coke quenching circulating gas system, a desulfurization reactor, a fine desulfurizer, a first induced draft fan, a heat exchanger, a catalytic reactor, a waste heat boiler, a second induced draft fan, a spray cooling tower, a decarbonization absorption tower, a regeneration tower and a condensation tower. The system and method of the present invention make full use of the characteristics of high CO concentration and low oxygen content in the dry coke quenching off-gas, and utilize the dry coke quenching off-gas from the perspectives of calorific value utilization and low-oxygen purified gas, which not only solves the problems of energy waste and environmental pollution caused by the discharge of high-calorific value components in the off-gas, but also makes full use of the characteristics of the off-gas to produce purified gas with low oxygen content, crude nitrogen, high-concentration CO2, and rich in low-pressure steam, having high economic value.

This invention provides processes and systems for converting biomass into high-carbon biogenic reagents that are suitable for a variety of commercial applications. Some embodiments employ pyrolysis in the presence of an inert gas to generate hot pyrolyzed solids, condensable vapors, and non-condensable gases, followed by separation of vapors and gases, and cooling of the hot pyrolyzed solids in the presence of the inert gas. Additives may be introduced during processing or combined with the reagent, or both. The biogenic reagent may include at least 70 wt %, 80 wt %, 90 wt %, 95 wt %, or more total carbon on a dry basis. The biogenic reagent may have an energy content of at least 12,000 Btu / lb, 13,000 Btu / lb, 14,000 Btu / lb, or 14,500 Btu / lb on a dry basis. The biogenic reagent may be formed into fine powders, or structural objects. The structural objects may have a structure and / or strength that derive from the feedstock, heat rate, and additives.

The embodiment of the invention provides an operation state determination method and device, electronic equipment and a medium. The method comprises the steps that after a tank body is controlled to move to a target position, a first image is collected through a collecting device, and the collecting end of the collecting device right faces the first side face of a lifting lug when the tank body is in an in-place state; based on the first image, offset data of the tank body in the X-axis direction is determined, and the X axis is perpendicular to the collecting end of the collecting device and faces and is parallel to the reference horizontal plane; and based on the first image, determining rotation offset data of rotation of the tank body around a Y axis, the Y axis being perpendicular to a reference horizontal plane.

The invention relates to the technical field of biomass carbonization, in particular to a biomass continuous carbonization kiln based on a double-layer rotary kiln structure and application of the biomass continuous carbonization kiln. A biomass continuous carbonization kiln comprises a rotary kiln body, a heating box body and a sealing system. According to the invention, preheating and carbonization are carried out in sections through the inner and outer layer guide plates, the carbonization time is prolonged by 30%, and the product yield is improved by 15%; oxygen permeation is controlled through triple sealing, the deflagration risk is reduced, and safety is good; heat energy closed-loop utilization: flue gas purification, tail gas backdraft and waste heat drying are integrated, comprehensive energy consumption is reduced by 25%, flue gas waste heat is fully recycled, heat energy is utilized in a stepped mode, energy consumption is low, and environment-friendly production is achieved; the explosion-proof device is linked with the cooling system, so that the problem of passive protection only depending on buffer filler in the prior art is effectively solved, and the safety controllability is high.

The invention discloses a carbon dioxide emission reduction and utilization process and device based on a dry quenching process, and belongs to the technical field of coking and carbon emission reduction. The device comprises a coke receiving tank, a reduction reactor, a dry quenching furnace, a high-temperature dust remover, a waste heat boiler, a steam turbine, a cyclone separator and a CO separation device, according to the invention, the reduction reactor is arranged, the heat of red coke is utilized, CO2 is subjected to a reduction reaction to be converted into CO, and the CO and H2 are used for producing high-value chemicals such as fuel oil or methanol or olefin through the synthetic gas conversion device, so that efficient and controllable conversion and utilization of coking CO2 are realized; and a gas collecting hood and a nitrogen replacement process are arranged, so that air does not permeate into the reduction reactor and a reaction product CO in the coke loading process, coke burning loss is completely eradicated, the explosion risk is eliminated, and safe and stable operation of the whole process is realized.

The utility model discloses a dust removal device for reducing particulate matters in a quenching tower, which belongs to the technical field of wet quenching dust removal and comprises four stages of serial dust removal structures arranged in the quenching tower from bottom to top in sequence. Comprising a first-stage dust removal device, a second-stage dust removal device, a third-stage dust removal device and a fourth-stage dust removal device, the first-stage dust removal device is arranged above the top of the quenching car and comprises an upper-layer dust removal baffle group, a middle-layer dust removal baffle group and a lower-layer dust removal baffle group, each layer of dust removal baffle group comprises a plurality of dust removal baffles which are arranged in parallel, and each dust removal baffle is fixedly connected with the inner wall of a quenching tower; the third-stage dust removal device comprises a louvered dust removal plate, the fourth-stage dust removal device comprises a water mist spraying system, and the technical problems that an existing coke quenching tower is low in dust removal efficiency, poor in particulate matter stage treatment capacity, insufficient in harmful gas treatment and the like are effectively solved.

The utility model relates to a carbon dioxide comprehensive utilization system taking dry quenching as a core. The carbon dioxide comprehensive utilization system comprises a dry quenching circulation system, a carbon dioxide preparation system, a carbon monoxide separation device and a hydrogen separation device, the dry quenching circulating system comprises a dry quenching furnace, a primary dust remover, a boiler, a secondary dust remover and a circulating fan which are sequentially connected through a circulating gas pipeline; the carbon monoxide separation device and the hydrogen separation device are connected with a circulating gas pipeline at the downstream of the circulating fan; the carbon dioxide preparation system comprises a coke oven flue, a carbon dioxide separation device and a chimney. According to the system disclosed by the utility model, carbon dioxide separated from industrial waste gas is used as dry quenching circulating gas, a new way for consuming carbon dioxide is developed, the emission of carbon dioxide is reduced, the safety of dry quenching production is ensured, and carbon monoxide and hydrogen are obtained.

The utility model discloses a sealed coke tank for dry quenching, and relates to the technical field of coke quenching tanks. The device comprises a coke tank, a first sealing cover, a second sealing cover, a water seal support and a liquid injection nozzle, a feeding port is arranged at the top end of the coke tank, the water seal support is fixedly sleeved outside the feeding port, the liquid injection nozzle is mounted at the upper end of one side of the water seal support, and a liquid discharge nozzle is mounted on the lower side of the other end of the water seal support. According to the device, a first sealing cover and a second sealing cover are arranged at a feeding port for pouring in a covering mode, at the moment, an inserting cover is inserted into an embedding groove, so that a gap between the first sealing cover and the second sealing cover is filled, and in order to further guarantee the sealing effect, a liquid injection nozzle is matched with a pressurizing liquid pump to pump liquid in a liquid box into a water seal support; therefore, the bottoms of the first sealing cover, the second sealing cover and the inserting cover are further sealed through liquid, sealing of the focusing tank is guaranteed, and heat loss of the focusing tank in the moving process is avoided.

The utility model provides a coke pot trolley walking mechanism suitable for a curve. The coke pot trolley walking mechanism comprises a frame; a plurality of wheels are arranged at the bottom of the frame, and inclined areas and connecting areas are sequentially arranged at the ends, making contact with the rails, of hubs of the wheels; the center plate structure is arranged on the frame, the center plate structure comprises an upper center plate and a lower center plate, and an adjusting structure is arranged between the upper center plate and the lower center plate and used for generating rolling friction between the upper center plate and the lower center plate. The inclined areas are arranged on the wheels to effectively cope with lateral force brought by a curve, the adjusting structure in the center plate structure can bear very large axial load and radial load, and the adjusting structure and the center plate structure work cooperatively, so that the coke tank trolley can safely and stably pass through the curve, the risk of overturning of the trolley and a coke tank is greatly reduced, and the service life of the coke tank trolley is prolonged. And the transportation requirement under a complex reshipment route is met, the production efficiency is improved, and the production safety is guaranteed.

The present invention relates to the technical field of waste treatment, and provides a co-treatment system and method for oil-based drill cuttings and red mud waste, mainly including: a mixing device, a forming device, a pyrolysis device, a coke quenching device and a screening device connected in sequence. The mixing device is used to obtain a mixture of oil-based drill cuttings and red mud; the forming device is used to form the mixture into pyrolysis raw materials; the pyrolysis device is used to pyrolyze the pyrolysis raw materials to generate pyrolysis solid-phase products; the coke quenching device is used to cool down the pyrolysis solid-phase products; the screening device is used to screen the cooled pyrolysis solid-phase products to obtain granular pyrolysis solid-phase products, and the pyrolysis solid-phase products are red mud drill cuttings-based iron-carbon materials. The present invention realizes the co-treatment of two kinds of wastes, namely oil-based drill cuttings and red mud, achieves the purpose of treating waste with waste, and has the characteristics of simple operation, stable and reliable, energy-saving and environmental protection, etc.

The invention discloses a coke tank uncovering / capping device and a coking production system, the coke tank uncovering / capping device comprises a fixed frame, two fork tooth groups are mounted on the fixed frame, the upper ends of fork teeth are respectively provided with a slope and a placing platform distributed at the tail end of the slope, and the height of the slope is gradually increased along a first direction; two hanging piece groups are arranged at the upper end of the can cover, and hanging pieces are respectively provided with hanging ports into which the corresponding fork teeth are inserted; the lifting mechanism is mounted on the carrier loader, and the lifting mechanism and the coke tank are distributed at intervals in the direction deviating from the first direction; the hanging lug is installed on the tank cover and vertically corresponds to the lifting mechanism, an inserting groove used for containing the lifting end of the lifting mechanism is formed in the lower end of the hanging lug, and a notch communicated with the inserting groove is formed in the side, corresponding to the first direction, of the hanging lug. Accurate fixed-point alignment of the carrier loader is not needed, driving power is provided through movement of the coke tank car, uncovering / capping actions can be completed in the running process, and an extra power source is not needed.

The invention discloses a biomass pyrolysis carbonization control system, and relates to the technical field of new energy and environmental protection, and the biomass pyrolysis carbonization control system comprises a raw material preparation module, a carbonization module, a tail gas treatment module, a product collection module and a control system module, the carbonization module is used for performing pyrolysis carbonization on raw materials to obtain biomass charcoal, the tail gas treatment module is used for collecting tail gas generated in the pyrolysis carbonization process, the product collection module is used for cooling and packaging the biomass charcoal, and the control system module is used for monitoring and controlling the operation state of the carbonization control system. According to the system, comprehensive optimization of a pyrolysis carbonization process is realized through multi-module collaborative operation, energy consumption is reduced by utilizing a pyrolysis gas circulation technology, the quality of a biomass charcoal product is stabilized by regulating and controlling parameters through a programmable logic controller, and the system adopts multiple preset safety strategies, so that the reliability of the system is guaranteed, and circular economy, energy conservation and emission reduction are promoted.

The embodiment of the invention provides a coke product cooling system and method.The coke product cooling system comprises a coke discharging device, a cold coal loading device, a cooling device and a screening device, and an inlet of the coke discharging device is used for being connected with an outlet of a coke oven so as to obtain a coke product which is subjected to coking and to be cooled and has the first particle size from the coke oven; the cold coal loading device is used for loading cooled coal with a second particle size, and the second particle size is smaller than the first particle size; an inlet of the cooling device is respectively connected with an outlet of the coke discharging device and an outlet of the cold coal loading device, the cooling device is used for receiving and mixing the coke product and the coal material, so that the coke product is cooled by the coal material, and the coal material is heated by the coke product to form a coal product; an inlet of the screening device is connected with an outlet of the cooling device and used for obtaining and screening coke products and coal products of different particle sizes. And in the cooling link of the coke product, the heat of the coke product is efficiently recovered, the environmental pollution is low, the coal product can be obtained, and the benefit is better than that of waste heat recovery power generation.

The utility model discloses a kind of circulating water-saving quenching tank, belong to quenching equipment technical field.The device includes tank body, three-layer spray pipe, first spray pipe configuration atomizing nozzle, second spray pipe heavy fan-shaped nozzle, third spray pipe configuration columnar nozzle, cyclone separator, settling tank and laminated filter.Through layered spray design, upper atomizing nozzle pre-cools coke, middle layer fan-shaped nozzle evenly covers coke surface, lower layer columnar nozzle high-pressure flush bottom, in combination with cyclone separation and filter recycling technology, realize waste water closed circuit circulation.Tank body top is provided with steam collection cover and condenser, and steam condensate is recycled to supplement spray system.It is suitable for coking plant wet quenching process.

The invention discloses a coupling system of a coke oven system and a coke dry quenching circulating gas loop and a control method thereof, the coupling system comprises the coke dry quenching circulating gas loop and the coke oven system, a first pipeline is used for introducing part of circulating gas generated by a coke dry quenching furnace into a coke oven or a coke oven flue gas pipeline; a part of redundant circulating gas of the dry quenching furnace is led out to the coke oven system from the first pipeline, the gas leakage and explosion risks of the dry quenching furnace can be reduced, meanwhile, inert components in the circulating gas can dilute combustible components of coke oven gas, the combustion intensity of the coke oven gas is reduced, and generation of NOx in coke oven waste gas is reduced; or part of the circulating gas is treated through a flue gas purification device of the coke oven system, so that the capacity of purification equipment of a dry quenching dust removal system is reduced, and the pipeline arrangement redundancy complexity of a dry quenching area is reduced.

Processes and systems for converting biomass into high-carbon biogenic reagents that are suitable for a variety of commercial applications. Pyrolysis in the presence of an inert gas is employed to generate hot pyrolyzed solids, condensable vapors, and non-condensable gases, followed by separation of vapors and gases, and cooling of the hot pyrolyzed solids in the presence of the inert gas. Additives may be introduced during processing or combined with the reagent, or both. The biogenic reagent may include at least 70 wt %, 80 wt %, 90 wt %, 95 wt %, or more total carbon on a dry basis. The biogenic reagent may have an energy content of at least 12,000 Btu / lb, 13,000 Btu / lb, 14,000 Btu / lb, or 14,500 Btu / lb on a dry basis. The biogenic reagent may be formed into fine powders, or structural objects. The structural objects may have a structure and / or strength that derive from the feedstock, heat rate, and additives.

To provide a coke dry extinguishment facility and a sloping flue part structure capable of promoting discharge of red-hot coke from a sloping flue part.SOLUTION: A coke dry extinguishment facility comprises a cooling tower including a spare room, a cooling chamber, an annular duct, and a sloping flue part. The sloping flue part includes an annular wall extending upward from an upper end part of the cooling chamber so as to surround a lower end part of the spare room from outside, and a plurality of support walls extending in a radial direction of the cooling chamber between the lower end part of the spare room and the upper end part of the cooling chamber and the annular wall and arranged in a circumferential direction of the cooling chamber. The inner peripheral surface of the annular wall includes an inclined surface expanding outward in the radial direction of the cooling chamber as it goes upward. In a vertical cross-section including one of the support walls, a first intersection at which the inclined surface intersects with an inner peripheral surface of the cooling chamber is located above a second intersection at which a lower end of the one support wall intersects with the inner peripheral surface of the cooling chamber.SELECTED DRAWING: Figure 3

This invention relates to the field of coal pyrolysis technology, and more particularly to a three-stage continuous cooling structure and a semi-coke cooling control method for a low-rank coal pyrolysis device. The three-stage continuous cooling structure includes a transition section, an air-cooling section, and a water-cooling section. Multiple semi-coke feeding pipes are connected to the bottom of each carbonization chamber. The transition section, air-cooling section, and water-cooling section are arranged from top to bottom along the semi-coke feeding pipes. A quenching buffer section is equipped with a quenching buffer tank, and the lower end of the semi-coke feeding pipe is connected to the quenching buffer tank. The air-cooling section includes an air-cooling box located around the semi-coke feeding pipe, and the water-cooling section includes a cooling water tank located around the semi-coke feeding pipe. The coke discharge port at the bottom of the quenching buffer tank is connected to a coke pushing and discharging mechanism. The semi-coke after high-temperature carbonization is gradually cooled to a safe temperature through the three-stage continuous cooling system, achieving gradient cooling of the semi-coke while fully recovering the waste heat of the semi-coke. This also reduces water consumption and prevents the semi-coke from being crushed or oxidized due to rapid cooling, effectively improving the energy efficiency and product quality of the low-rank coal pyrolysis device.

The present invention relates to the technical field of soot treatment, and in particular to a dust removal device and an exhaust gas treatment system for dry coke quenching, which include a plurality of collecting plates and a plurality of first suction pipes; the collecting plates are arranged in an arched shape, and a passage for flue gas to pass through is left between two adjacent collecting plates, and the plurality of first suction pipes correspond to the plurality of collecting plates one by one and the first suction pipes are arranged above the collecting plates; suction pipes are arranged on both sides in the long side direction of the steel roof, and both ends of the first suction pipe are sequentially communicated with the two suction pipes; a suction groove extending along its own axial direction is formed in the circumferential side wall of the first suction pipe, and the suction groove faces the arc-shaped inner wall of the top of the steel roof, and a rotating member for controlling the first suction pipe to rotate around its own axial direction is arranged in the steel roof. The present invention can solve the technical problems of collecting and treating the soot on the top of the steel roof during the transportation of the open coke pot, improve the suction effect, and reduce the accumulation of soot.

The utility model provides a system for increasing the temperature of a dry quenching calcium-based dry desulfurization agent, which belongs to the technical field of dry quenching desulfurization and comprises a dust removal system, a desulfurization system, an electric tracing band, a heat exchanger and a compressed air pipeline, the dust removal system comprises a dust removal cover, a low-temperature dust removal pipeline, a high-temperature dust removal pipeline, a heat storage cooler, a bag type dust collector, a dust removal fan and an exhaust funnel, the dust removal cover is arranged at the discharge port of the dry quenching body, and the dust removal cover, the low-temperature dust removal pipeline, the heat storage cooler, the bag type dust collector, dust removal air and the exhaust funnel are sequentially connected; the two ends of the high-temperature dust removal pipeline are respectively connected with the dry quenching body and the heat storage cooler; according to the system, when the calcium-based dry desulfurization system is under the working condition in winter, the purposes of enhancing the desulfurization effect, reducing the content of a desulfurizing agent and reducing the operation and maintenance cost are achieved.

The utility model discloses a dry quenching coke loading system capable of reducing dust emission, which comprises a furnace cover opening and closing mechanism arranged on one side of a furnace mouth of a dry quenching furnace, a loading device for dry quenching, a tail coke hopper arranged on one side of the furnace mouth of the dry quenching furnace, and a movable coke tank suspended above the furnace mouth of the dry quenching furnace, two running rails are arranged on the two sides of a top port of the loading device side by side, a movable plate trailer is arranged on the two running rails, a movable motor is arranged on the movable plate trailer, walking wheels are arranged at the bottom of the movable plate trailer, and a cover plate used for shielding an upper port of the loading device is arranged on the front portion of the movable plate trailer. The cover plate is driven by the movable plate trailer to transversely move left and right along the running track, the upper layer of the cover plate is a metal plate, and the lower layer of the cover plate is provided with a high-temperature-resistant heat insulation material layer. Limiting switches are arranged at the two ends of the running track respectively. According to the utility model, the loading device is sealed after coke loading is finished, so that the dust removal effect is prevented from being influenced by the entrance of wild wind, and dust can be prevented from being dissipated.

The invention discloses a detection method for preventing a dry quenching carrier loader from receiving coke in a full tank, which belongs to the technical field of coking and comprises the following steps: S1, mounting a weighing device on an elevator beam of a dry quenching tower, weighing a coke tank when the carrier loader reaches the dry quenching tower to replace the coke tank, and generating coke tank state information in a dry quenching elevator PLC (Programmable Logic Controller); the dry quenching elevator PLC communicates with the carrier loader to update a coke tank state signal of the carrier loader; after the carrier loader reaches the position below the coke barrier car, a coke tank state signal and an alignment signal of the carrier loader are verified, if the coke tank state signal and the alignment signal of the carrier loader pass verification, normal coke pushing is allowed, and otherwise, triggering of a coke pushing signal is not allowed; and after coke pushing is completed, the coke tank state signal of the carrier loader is updated to be a full tank signal. The scheme ensures that the coke tank is in an empty tank state during coke receiving, improves the safety of the coke dry quenching system, has the characteristics of high intelligence and strong practicability, only needs one set of weighing device, and is low in cost.

The utility model provides an improved dry quenching furnace, and relates to the field of dry quenching furnaces, the improved dry quenching furnace comprises a dry quenching furnace, the dry quenching furnace comprises a furnace top, a pre-storage section, a cooling section and a cone hopper, the furnace top, the pre-storage section, the cooling section and the cone hopper are fixedly connected in sequence, and the pre-storage section is arranged on the furnace top. Pouring layers are arranged on the inner wall of the pre-storage section, the inner wall of the cooling section and the inner wall of the conical hopper, reinforcing ribs which are arranged in a crossed mode are arranged in the pouring layers, and a high-temperature-resistant layer and a wear-resistant layer are sequentially arranged on the outer surface of each pouring layer. Heat insulation layers are arranged between the pouring layer and the pre-storage section, between the pouring layer and the cooling section and between the pouring layer and the conical hopper, the pouring layer is additionally arranged on the inner wall of the conical hopper, reinforcing ribs are additionally arranged in the pouring layer, the abrasion resistance of the conical hopper can be effectively improved, the heat insulation layers are additionally arranged, and the abrasion resistance of the conical hopper is improved. And heat can be prevented from overflowing.