CN208579643U - High-temperature material waste heat recycle bin system - Google Patents

High-temperature material waste heat recycle bin system Download PDF

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Publication number
CN208579643U
CN208579643U CN201820513384.0U CN201820513384U CN208579643U CN 208579643 U CN208579643 U CN 208579643U CN 201820513384 U CN201820513384 U CN 201820513384U CN 208579643 U CN208579643 U CN 208579643U
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heat
chamber
hot
mineral aggregate
velocity
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孙延龙
林记元
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Beijing Rui Rui Machinery Co Ltd
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Beijing Rui Rui Machinery Co Ltd
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    • YGENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02PCLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P10/00Technologies related to metal processing
    • Y02P10/25Process efficiency

Abstract

The utility model provides a kind of high-temperature material waste heat recycle bin system, be by high-temperature material from top to bottom through crusher crushing sequentially enter hot mineral aggregate bucket, compensator, seal pipe, in distributing device uniform distribution to heat exchanging chamber, conveyer belt, the belt feeder being dumped into unloader shell through dump skip transport;Circulating cooling gas drives the closed cycle in closed system by circulating fan, cold wind enters outside cloth wind chamber through cold wind general pipeline enters back into heat exchanging chamber into ventilation hole after casing, counterflow heat exchange heating is completed with heat sinter in heat exchanging chamber, thermal cycle wind after the bed of material is upwardly into completion deceleration depositing dust in velocity-reducing chamber, enter in waste heat boiler by hot-blast main, circulating air exchange heat in the waste heat boiler it is cooling after enter cold wind general pipeline and be again introduced into and recycle next time.The technical problems such as the utility model solves environmental pollution, cloth evenness difference causes inhomogeneous cooling, double sintering, Yi Peng material putty failure rate height.

Description

High-temperature material waste heat recycle bin system
Technical field
The utility model relates to high-temperature material cooling and its heat recovery technology fields, are specifically to provide a kind of high-temperature material Waste heat recycle bin system.
Background technique
Existing sinter is cooling and its heat recovery technology mainly uses ring cold machine to add waste heat boiler, event that the device is complicated Barrier rate is high, occupied area is larger, and technique is from power consumption height, and generating capacity is low, and environmental pollution is serious.The vertical cooling researched and developed Kiln adds the technology of waste heat boiler, low from power consumption, and generating capacity is high, and environmental-friendly, but is still in the research and development test stage, there is no The stable application of full maturity, and having the following defects, 1, environmental pollution is serious, 2, cloth evenness is poor, inhomogeneous cooling, 3, easily Fluffy material putty high failure rate.
For the above problem of the existing technology, it is urgent to provide a kind of cooling skills for realizing the heat exchange of sinter efficient stable Art, and eliminate the environmental pollution generated in production process.
Utility model content
The utility model provides a kind of high-temperature material waste heat recycle bin system, solve the prior art there are environmental pollution, Cloth evenness difference causes the technical problems such as inhomogeneous cooling, double sintering problem, Yi Peng material putty failure rate height.
The technical solution of the utility model is achieved in that
The utility model high-temperature material waste heat recycle bin system, including feeding device, distribution device, heat-exchanger rig, conveying Device, the feeding device include crusher 1, hot mineral aggregate bucket 2, compensator 5, seal pipe 6;The crusher feed opening connects institute Hot mineral aggregate bucket 2 is stated, the hot mineral aggregate bucket lower part discharge port connects compensator, and the compensator lower part connects seal pipe;It is described broken Broken machine 1, compensator 5, is connected inside seal pipe 6 at hot mineral aggregate bucket 2;
The distribution device includes distributing device 7, be at the top of the distributing device 7 center it is upward in conical pinnacle Surface has the material separating disc 71 of impeller inducer 72, stretches out several differences around along the taper direction of the material separating disc Pan Bi The flow-guiding mouth of the chute 74 on length direction and the corresponding material separating disc is arranged on the cantilever for the cantilever 70 of length, each described Chute lower part be arranged in the circumferential direction, equidirectional blanking port 75, the cloth track loop wire 77 of the blanking port is annulus, institute Material separating disc bottom attachment support body 76 is stated, motor 78 drives the supporter to rotate;The pinnacle of the material separating disc faces described 6 lower nozzle of seal pipe;
The heat-exchanger rig includes heat exchanging chamber 10, velocity-reducing chamber 8, cloth wind chamber 11, waste heat boiler 21, circulating fan 19, cold wind General pipeline 18, hot-blast main 20;The heat exchanging chamber 10 is a ring-shaped cylinder cavity around supporter setting;
8 lower part of velocity-reducing chamber is divided into the annular truncated cone-shaped 84 that the lower end upper end Nei Shou extends out, top is divided into cylinder 83 Closed shell suitable for reading, the annular truncated cone-shaped 84 of 8 lower part of velocity-reducing chamber is around the supporter;On the heat exchanging chamber external annulus Edge border connects 8 shell of velocity-reducing chamber, 85 bottom;The heat exchanging chamber internal ring wall upper limb border connects 8 inner casing 87 of velocity-reducing chamber Bottom, the 8 inner casing upper peripheral edge of velocity-reducing chamber are connected on the supporter outer wall;Connect inside the velocity-reducing chamber and the heat exchanging chamber It is logical;The corresponding seal pipe is equipped with material-dropping hole 81 in the middle part of the velocity-reducing chamber top lid wall, and the seal pipe is inserted into the blanking port Sealing cooperates, and equally distributed hot blast manifold mouth 82 is arranged around blanking port on the top lid wall;The material separating disc, cloth cantilever Inside the velocity-reducing chamber;
The cloth wind chamber 11 is that annular housing is docked in the heat exchanging chamber lower part, the cloth wind is intracavitary, external annulus with it is described Heat exchanger internal ring wall, external annulus lower edge Butt sealing are fixed and internal connection, and the annular housing bottom of the cloth wind chamber is integrally set Set multiple conical dump skips 114;Taper dump skip upper part of the housing is all evenly distributed with circular vent 117;The cloth wind chamber It is externally provided with the outer casing 111 of annular, the outer casing external annulus upper end top cover and the closing of heat exchanging chamber external annulus lower part are fixed, The outer casing internal ring wall upper limb and heat exchanging chamber internal ring wall root edge closing are fixed, and the outer casing inner and outer rings wall root edge is set Bottom cover closing is fixed on around the taper dump skip feed opening;The outer casing and the cloth wind is intracavitary, external annulus and described Cavity is constituted between taper dump skip shell, the dump skip is enclosed in the outer casing cavity with the part of ventilation hole; Air inlet is arranged in the outer casing 111;
The feeding device includes unloader 13, unloader shell 131, and the unloader is under the taper dump skip Multiple conveyer belts of symmetrical centre setting below material mouth, the unloader shell are that each conveyer belt is trapped among to internal circle Shell is closed, deflector chute 14 is set among the unloader outer casing bottom, material guide port, the transmission is arranged in the deflector chute lower part Band inner end corresponds to the deflector chute discharging;The material guide port lower part setting belt feeder transports mineral aggregate outward;The taper dump skip Feed opening protrudes into sealing cooperation in the unloader outer casing upper cover;
21 top of waste heat boiler connects the hot wind of the velocity-reducing chamber by the hot-blast main 20 with each hot blast manifold Nozzle, the waste heat boiler lower part connect the air inlet of the outer casing external annulus lower part of the cloth wind chamber by the cold wind general pipeline 18 Mouthful, circulating fan 19 is set on the cold wind general pipeline;Heat-exchanger rig is set in the waste heat boiler.
The outer casing 111 of the cloth wind chamber is along the fixed multiple dredging machine mounting cylinders 112 in border, the taper dump skip shell Upper setting dredging machine pilot hole 113, the electro-hydraulic pusher 121 of the dredging machine are supported in the dredging machine mounting cylinder, dredging Push rod 123, which pierces the dredging machine pilot hole and protrudes into the taper dump skip feed opening 115, to be dredged;Setting prison in unloader shell Flow of Goods and Materials sensor is surveyed, when detecting material cut-off on unloader 13, starting dredging machine 12 is dredged;
The Support Position of the hot mineral aggregate bucket 2 is equipped with weighing sensor 3, and the hot mineral aggregate bucket 2 by flexible sealing with Upper and lower equipment is tightly connected, and the cone pars infrasegmentalis of the hot mineral aggregate bucket 2 is equipped with chunk breaker 4, when the weighing sensor 3 detects When increasing to hot 2 gravimetric anomaly of mineral aggregate bucket, hopper feed opening putty is determined, then it is broken thin to start the chunk breaker 4 It is logical;
Chunk breaker 4 is circumferentially arranged on the 2 feed opening wall of hot mineral aggregate bucket to be supported on fixed bracket 44, it is described big Block crusher 4 includes radial slotting tool 47: the slotting tool is that one block of rectangle plate is inserted into the hot mineral aggregate bucket, front end face shape Shape and the hot mineral aggregate bucket bottom sidewall are coincide, and when off position, slotting tool is withdrawn, and front end face and hopper inner conical surface agree with envelope It closes hopper, guarantees stream in general, when working condition opposite two groups of slotting tools are inserted into center simultaneously, the bulk of card resistance feed opening Feed opening is dredged in crushing;
The parietal layer structure of the hot mineral aggregate bucket 2 is wear-resistant liner 219, thermal insulation layer 210, steel structure casing 211 from inside to outside; The parietal layer structure of the heat exchanging chamber 10 is heat-resistant antifriction layer 106, thermal insulation layer 105, steel structure casing 103 from inside to outside;It is described to subtract The parietal layer structure of fast chamber 8 is thermal insulation layer 86, steel structure casing 85 from inside to outside.
One release branch pipe 181 is set on the cold wind general pipeline 18, set gradually on the release branch pipe regulating valve 24, Deduster 16 and air-introduced machine 17.
7 supporter of distributing device setting, 9 seal clearance of watertight construction is heat-insulated;The motor 78 drives gear band to move institute State supporter rotation.
The heat-exchanger rig of the waste heat boiler 21 is closed water circulating pipe 25, and the water circulating pipe is connected to steam turbine Into, steam drain, boiler feed-water pump 23 is set on the water circulating pipe, the superheated steam driving that the heat-exchanger rig generates Steam turbine 22 externally does work, and the low-pressure steam after workmanship is pressurizeed by boiler feed-water pump 23 after condensing and followed for the heat-exchanger rig Ring uses.
Cantilever support 73 is arranged in the cantilever of the distributing device, by the velocity of rotation of control distributing device, controls blanking velocity, It remains in seal pipe and state is filled up by hot mine.
The compensator 5 is that one kind is flexible coupling short tube, including internal wear-resistant sleeve 53, the wear-resisting pipe outer wall it is upper, Under it is each fix a section steel short tube 1, steel short tube 2 58, it is short that a stainless steel ripple seal pipe 56 is fastened on two steel Between pipe, the wear-resistant sleeve 53 is divided to for upper and lower two section, and there is an oblique annular retractable seam 52 in centre, lives for compensator is flexible It is dynamic, hard heat-insulating layer 54 is fixed between steel short tube one and wear-resistant sleeve described in upper section, the institute between steel short tube described in two sections State the fixed flexible thermal insulation layer 57 of wear-resistant sleeve outer wall.
High-temperature material or hot mineral aggregate from top to bottom after crusher crushes, into the hot mineral aggregate bucket of lower part after enter closing system It unites closed circuit transmission blanking, first compensated device, seal pipe are fallen on the distributing device material separating disc in the velocity-reducing chamber of lower part, through different in size In cantilever uniform distribution to heat exchanging chamber equipped with chute, then the dump skip through lower part is dumped into the conveyer belt in unloader shell, It is transferred to and is discharged to belt feeder in unloader deflector chute and transports;
The utility model has the beneficial effects that
The utility model uses ring-like heat exchanging chamber, charged cloth using seal pipe and distributing device, and heat transferring medium gas master follows Ring uses closed cycle operating mode, is realized using a kind of method of seal pipe cooperation distributing device cloth intracorporal close in hot air cavity The uniform charging of envelope and high-temperature material, avoids material from being segregated, and realizes the uniform heat exchange of high-temperature material, while closed circuit using circulated air The method of circulation avoids a large amount of fresh air from entering, and greatly reduces the oxygen content in gas.Avoid the presence of life in sinter The double sintering phenomenon that may occur when material guarantees the continuous and steady operation of production, is finally realizing the operation of equipment steady and continuous While, realize environment friendly and pollution-free, low energy consumption, efficient UTILIZATION OF VESIDUAL HEAT IN.The equipment of the utility model is simple, reliable for operation, Power consumption is low, generating capacity is high, cleanliness without any pollution, and equipment takes up little area, and mounting arrangements are flexible.
Detailed description of the invention
Fig. 1 Tthe utility model system schematic diagram,
Fig. 2 (a), (b) the utility model velocity-reducing chamber vertical view, schematic front view,
Fig. 3 the utility model heat exchanging chamber overlooks A-A schematic cross-sectional view,
Fig. 4 the utility model distributing device cantilever schematic diagram,
Fig. 5 (a), (b), (c) the utility model cloth wind chamber main view, top view, the ventilation hole on taper dump skip shell are put Big schematic diagram,
Fig. 6 a, b, c are main view section view, main view, the schematic top plan view of the hot mineral aggregate bucket of the utility model and chunk breaker,
Fig. 7 the utility model compensator schematic diagram,
Fig. 8 the utility model taper dump skip, dredging machine schematic diagram,
Fig. 9 the utility model high-temperature material cools down path schematic diagram,
Figure 10 the utility model circulated air closed cycle path schematic diagram.
Figure number explanation: crusher 1, hot mineral aggregate bucket 2, weighing sensor 3, chunk breaker 4, compensator 5, seal pipe 6, cloth Glassware 7, velocity-reducing chamber 8, watertight construction 9, heat exchanging chamber 10, cloth wind chamber 11, dredging machine 12, unloader 13, deflector chute 14, belt feeder 15, deduster 16, air-introduced machine 17, cold wind general pipeline 18, release branch pipe 181, circulating fan 19, hot-blast main 20, waste heat boiler 21, Steam turbine 22, boiler feed-water pump 23, regulating valve 24, water circulating pipe 25.
Hot 2 parietal layer structure of mineral aggregate bucket includes: steel structure casing 211, wear-resistant liner 219, thermal insulation layer 210,
Chunk breaker 4 includes: electro-hydraulic pusher 42, driver 43, fixed bracket 44, leading truck 46, radial slotting tool 47.
Compensator 5 includes: that expansion joint 52, wear-resistant sleeve 53, hard heat-insulating layer 54, steel short tube 1, stainless steel ripple are close Tube sealing 56, flexible thermal insulation layer 57, steel short tube 2 58.
Distributing device 7, impeller inducer 72, material separating disc 71, cantilever 70, chute 74, blanking port 75, cloth track loop wire 77, branch Support body 76, distributing device driving device 78.
Velocity-reducing chamber 8 includes: material-dropping hole 81, hot blast manifold outlet 82, cylinder 83, annular truncated cone-shaped 84, steel structure casing 85, thermal insulation layer 86;
Heat exchanging chamber 10 includes: heat-resistant antifriction layer 106, thermal insulation layer 105, steel structure casing 103;
Cloth wind chamber 11 includes: outer casing 111, dredging machine mounting cylinder 112, dredging machine pilot hole 113, taper dump skip 114, Dump skip feed opening 115, ventilation hole 117;Interior casing 118
Dredging machine 12 includes: electro-hydraulic pusher 121, driver 122, dredging push rod 123, sealing guide type shoe 124, guiding Support 125,
Specific embodiment
Embodiment
It is shown in Figure 1, the high-temperature material waste heat recycle bin system of the utility model, including feeding device, distribution device, Heat-exchanger rig, feeding device, the feeding device include crusher 1, hot mineral aggregate bucket 2, compensator 5, seal pipe 6;It is described broken Machine feed opening connects the hot mineral aggregate bucket 2, and the hot mineral aggregate bucket lower part discharge port connects compensator, the compensator lower part connection Seal pipe;The crusher 1, compensator 5, is connected inside seal pipe 6 at hot mineral aggregate bucket 2;
Referring to shown in Fig. 1,4, the distribution device includes distributing device 7, is that a center is upward at the top of the distributing device 7 In conical pinnacle surface have impeller inducer 72 material separating disc 71, along the material separating disc Pan Bi taper direction around The cantilever 70 of several different length is stretched out, the chute 74 being arranged on length direction on the cantilever simultaneously corresponds to the material separating disc Flow-guiding mouth, each chute lower part setting in the circumferential direction, equidirectional blanking port 75, the cloth track ring of the blanking port Line 77 is annulus, the material separating disc bottom attachment support body 76, and motor 78 drives the supporter to rotate;The point of the material separating disc Top faces 6 lower nozzle of seal pipe;
Referring to shown in Fig. 1,2,3,5, the heat-exchanger rig includes heat exchanging chamber 10, velocity-reducing chamber 8, cloth wind chamber 11, waste heat boiler 21, circulating fan 19, cold wind general pipeline 18, hot-blast main 20;The heat exchanging chamber 10 is a ring around supporter setting Shape cylindrical cavity;
8 lower part of velocity-reducing chamber is divided into the annular truncated cone-shaped 84 that the lower end upper end Nei Shou extends out, top is divided into cylinder 83 Closed shell suitable for reading, the annular truncated cone-shaped 84 of 8 lower part of velocity-reducing chamber is around the supporter;On the heat exchanging chamber external annulus Edge border connects 8 shell of velocity-reducing chamber, 85 bottom;The heat exchanging chamber internal ring wall upper limb border connects 8 inner casing 87 of velocity-reducing chamber Bottom, the 8 inner casing upper peripheral edge of velocity-reducing chamber are connected on the supporter outer wall;Connect inside the velocity-reducing chamber and the heat exchanging chamber It is logical;The corresponding seal pipe is equipped with material-dropping hole 81 in the middle part of the velocity-reducing chamber top lid wall, and the seal pipe is inserted into the blanking port Sealing cooperates, and equally distributed hot blast manifold mouth 82 is arranged around blanking port on the top lid wall;The material separating disc, cloth cantilever Inside the velocity-reducing chamber;
The cloth wind chamber 11 is that annular housing is docked in the heat exchanging chamber lower part, the cloth wind is intracavitary, external annulus with it is described Heat exchanger internal ring wall, external annulus lower edge Butt sealing are fixed and internal connection, and the annular housing bottom of the cloth wind chamber is integrally set Set multiple conical dump skips 114;Taper dump skip upper part of the housing is all evenly distributed with circular vent 117;The cloth wind chamber It is externally provided with the outer casing 111 of annular, the outer casing external annulus upper end top cover and the closing of heat exchanging chamber external annulus lower part are fixed, The outer casing internal ring wall upper limb and heat exchanging chamber internal ring wall root edge closing are fixed, and the outer casing inner and outer rings wall root edge is set Bottom cover closing is fixed on around the taper dump skip feed opening;The outer casing and the cloth wind is intracavitary, external annulus and described Cavity is constituted between taper dump skip shell, the dump skip is enclosed in the outer casing cavity with the part of ventilation hole; Air inlet is arranged in the outer casing 111;
Shown in Figure 1, the feeding device includes unloader 13, unloader shell 131, and the unloader is described Multiple conveyer belts of symmetrical centre setting below taper dump skip feed opening, the unloader shell are to enclose each conveyer belt Deflector chute 14 is set among internal round sealed shell, the unloader outer casing bottom, and the deflector chute lower part setting is led Material mouth, the conveyer belt inner end correspond to the deflector chute discharging;The material guide port lower part setting belt feeder transports mineral aggregate outward;Institute It states taper dump skip feed opening and protrudes into sealing cooperation in the unloader outer casing upper cover;
21 top of waste heat boiler connects the hot wind of the velocity-reducing chamber by the hot-blast main 20 with each hot blast manifold Nozzle, the waste heat boiler lower part connect the air inlet of the outer casing external annulus lower part of the cloth wind chamber by the cold wind general pipeline 18 Mouthful, circulating fan 19 is set on the cold wind general pipeline;Heat-exchanger rig is set in the waste heat boiler.
Shown in Figure 5, the outer casing 111 of the cloth wind chamber is along the fixed multiple dredging machine mounting cylinders 112 in border, the cone Dredging machine pilot hole 113 is set on shape dump skip shell, and the electro-hydraulic pusher 121 of the dredging machine is supported on the dredging machine peace In fitted tube, dredging push rod 123, which pierces the dredging machine pilot hole and protrudes into the taper dump skip feed opening 115, to be dredged;Unloader Setting monitoring Flow of Goods and Materials sensor in shell, when detecting material cut-off on unloader 13, starting dredging machine 12 is dredged;
Referring to shown in Fig. 1,6, the Support Position of the hot mineral aggregate bucket 2 is equipped with weighing sensor 3, and the hot mineral aggregate bucket 2 are tightly connected by flexible sealing and upper and lower equipment, and the cone pars infrasegmentalis of the hot mineral aggregate bucket 2 is equipped with chunk breaker 4, when the title When re-transmission sensor 3 detects hot 2 gravimetric anomaly of mineral aggregate bucket increase, determines hopper feed opening putty, then start the bulk The broken dredging of crusher 4;
Chunk breaker 4 is circumferentially arranged on the 2 feed opening wall of hot mineral aggregate bucket to be supported on fixed bracket 44, it is described big Block crusher 4 includes radial slotting tool 47: the slotting tool is that one block of rectangle plate is inserted into the hot mineral aggregate bucket, front end face shape Shape and the hot mineral aggregate bucket bottom sidewall are coincide, and when off position, slotting tool is withdrawn, and front end face and hopper inner conical surface agree with envelope It closes hopper, guarantees stream in general, when working condition opposite two groups of slotting tools are inserted into center simultaneously, the bulk of card resistance feed opening Feed opening is dredged in crushing;
The parietal layer structure of the hot mineral aggregate bucket 2 is wear-resistant liner 219, thermal insulation layer 210, steel structure casing 211 from inside to outside; The parietal layer structure of the heat exchanging chamber 10 is heat-resistant antifriction layer 106, thermal insulation layer 105, steel structure casing 103 from inside to outside;It is described to subtract The parietal layer structure of fast chamber 8 is thermal insulation layer 86, steel structure casing 85 from inside to outside.
One release branch pipe 181 is set on the cold wind general pipeline 18, set gradually on the release branch pipe regulating valve 24, Deduster 16 and air-introduced machine 17.
7 supporter of distributing device setting, 9 seal clearance of watertight construction is heat-insulated;The motor 78 drives gear band to move institute State supporter rotation.
The heat-exchanger rig of the waste heat boiler 21 is closed water circulating pipe 25, and the water circulating pipe is connected to steam turbine Into, steam drain, boiler feed-water pump 23 is set on the water circulating pipe, the superheated steam driving that the heat-exchanger rig generates Steam turbine 22 externally does work, and the low-pressure steam after workmanship is pressurizeed by boiler feed-water pump 23 after condensing and followed for the heat-exchanger rig Ring uses.
Cantilever support 73 is arranged in the cantilever of the distributing device, by the velocity of rotation of control distributing device, controls blanking velocity, It remains in seal pipe and state is filled up by hot mine.
Referring to figure, shown in 7, the compensator 5 is that one kind is flexible coupling short tube, described resistance to including internal wear-resistant sleeve 53 Mill pipe outer wall it is upper and lower it is each fix a section steel short tube 1, steel short tube 2 58, a stainless steel ripple seal pipe 56 is fastened on Between two steel short tubes, the wear-resistant sleeve 53 is divided to for upper and lower two section, and there is an oblique annular retractable seam 52 in centre, for mending Device telescopic movable is repaid, hard heat-insulating layer 54 is fixed between steel short tube one and wear-resistant sleeve described in upper section, it is short to be located at steel described in two sections The fixed flexible thermal insulation layer 57 of the wear-resistant sleeve outer wall between pipe.
High-temperature material or hot mineral aggregate from top to bottom after crusher crushes, into the hot mineral aggregate bucket of lower part after enter closing system It unites closed circuit transmission blanking, first compensated device, seal pipe are fallen on the distributing device material separating disc in the velocity-reducing chamber of lower part, through different in size In cantilever uniform distribution to heat exchanging chamber equipped with chute, then the dump skip through lower part is dumped into the conveyer belt in unloader shell, It is transferred to and is discharged to belt feeder in unloader deflector chute and transports;
Referring to shown in Fig. 1,9,10, the utility model utilizes a kind of high-temperature material exhaust heat recovering method of above system, follows Ring cooling gas drives the closed cycle in closed system by circulating fan, enters cold wind general pipeline by waste heat boiler, total in cold wind Pipe is equipped with a release branch pipe, is controlled by regulating valve, and sub-fraction cold wind is after release branch pipe, deduster dedusting by drawing Blower driving is discharged into atmosphere, and partial gas outlet is to reach heat exchanging chamber gas deficiency and be in negative pressure working condition, big portion Point cold wind enters outside cloth wind chamber through cold wind general pipeline and enters ventilation hole after casing and enter back into heat exchanging chamber, in heat exchanging chamber and heat sinter Counterflow heat exchange heating is completed, the thermal cycle wind after the bed of material is upwardly into completion deceleration depositing dust in velocity-reducing chamber, total by hot wind Pipe enters in waste heat boiler, circulating air exchange heat in the waste heat boiler it is cooling after be again introduced into and recycle next time.
In the above method, the superheated steam that waste heat boiler generates externally does work through water circulating pipe driving steam turbine, does manual work Low-pressure steam afterwards is used after condensing by boiler feed-water pump pressurization boiler of feeding cycle heat exchange.
In the above method, separately there is the air in sub-fraction controllable environment to be entered by deflector chute, through discharge above unloader Mouth enters heat exchanging chamber, completes heat exchange heating with heat sinter in heat exchanging chamber, the thermal cycle wind after the bed of material, which is upwardly into, to be subtracted Fast chamber, converges in velocity-reducing chamber;There are also a small amount of air to enter preheating above hot mineral aggregate bucket, and is heated by seal pipe, The hot wind of heating fully enters and completes deceleration depositing dust in velocity-reducing chamber.
For utility model works principle referring to shown in Fig. 1, Fig. 9,10, high-temperature material or heat sinter are broken through crusher 1 Into high-temperature material or hot mineral aggregate bucket 2, collects in hot 2 lower part of mineral aggregate bucket, distributing device 7 is fallen on by compensator 5 and seal pipe 6 On material separating disc, material separating disc is assigned to heat sinter on interfaced multiple spiral arm chutes, according to the principle of equal thickness cloth Blanking port is loaded into heat exchanging chamber 10 along multiple ring-like faces, and heat exchanging chamber 10 is an annular cavity, and heat sinter is in heat exchanging chamber In 10 and from bottom to top circulated air counterflow heat exchange, the cold sinter after cooling that exchanges heat are unloaded by the equally distributed taper in heat exchanging chamber lower part Bin discharger discharge, the cold sinter of discharge are transported in deflector chute 14 by the unloader 13 below each discharge gate, then Next process is transported by the belt feeder 15 of 14 lower section of deflector chute.
Wherein hot mineral aggregate bucket 2 on along Support Position weighing sensor 3 is installed, and hot mineral aggregate bucket 2 by flexible sealing with Upper and lower equipment connection is equipped with chunk breaker 4 convenient for weighing, the cone pars infrasegmentalis of hot mineral aggregate bucket 2, when detecting hot 2 weight of mineral aggregate bucket When abnormal increase, hopper feed opening putty, the broken dredging of starting chunk breaker 4 are determined.Heat exchanging chamber bottom discharging mouth position, peace Equipped with dredging machine 12, setting monitors Flow of Goods and Materials sensor in unloader shell, when detecting material cut-off on unloader 13, Start dredging machine 12 to dredge.Watertight construction 9 is the sealing structure between 10 interior bucket of distributing device and heat exchanging chamber;Circulated air is in waste heat After heat exchange is cooling in boiler 21, cold wind general pipeline 18 is driven by circulating fan 19 referring to Fig. 1, Figure 10, on cold wind general pipeline 18 One release branch pipe 181 is set, is controlled by regulating valve 24, sub-fraction cold wind is after 16 dedusting of deduster by air-introduced machine 17 Driving is discharged into atmosphere, and the purpose of partial gas outlet is in order to reach heat exchanging chamber gas deficiency and be in negative pressure working condition, greatly Part cold wind enters ventilation hole 117 after cool air hose 18 enters the outer casing of cloth wind chamber 11 and is entering heat exchanging chamber, separately there is sub-fraction Air in controllable environment is entered by deflector chute 14, enters heat exchanging chamber through 13 top discharge gate of unloader, in heat exchanging chamber 10 with Heat sinter completes heat exchange heating, and the thermal cycle wind after the bed of material is upwardly into velocity-reducing chamber 8, converges in velocity-reducing chamber 8.Also A small amount of air enters preheating above hot mineral aggregate bucket, and is heated by seal pipe 6, and the hot wind of heating fully enters deceleration Deceleration depositing dust is completed in chamber 8, is entered in waste heat boiler 21 by hot-blast main 20, circulating air exchanges heat cold in waste heat boiler 21 But it is again introduced into and recycles next time afterwards.The superheated steam driving steam turbine 22 that waste heat boiler 21 generates externally does work, after workmanship Low-pressure steam is used after condensing by the pressurization boiler of feeding of boiler feed-water pump 23.
One, each device feature Action Specification
1, crusher 1, hot mineral aggregate bucket 2, weighing sensor 3, chunk breaker 4 belong to traditional charging and prepare equipment, Heat sinter is crushed, water conservancy diversion, the blocking of hopper feed opening is detected, the bulk of blocking hopper is crushed.
2, there are the abrasion-resistant guide pipe and thermal insulation layer of free gap in 5 flexible connecting structure of compensator, inside, and outside is stainless steel wave Line molded cannula, while guaranteeing sealing, the requirement of heat-insulated and wear-resisting three kinds of technique.It is being flexible coupling between hot mineral aggregate bucket and seal pipe, Play cooperation weighing and sealing.Abrasion-resistant guide pipe in compensator prevents the stainless steel ripple of material directly contact compensator Plate, while playing heat-blocking action.Bellows is the external retractable ripple type section short tube in compensator, using heat-resistance stainless steel material Matter plays isolation rigid connection and sealing.Compensator steel short tube structure plays installation, supporting role, and wear-resistant sleeve is divided into Lower two sections, there is an oblique annular retractable seam in centre, for compensator telescopic movable.Hard heat-insulating layer plays heat-insulated, supporting role.It is soft Property thermal insulation layer rise heat-insulated, dust reduction capability.Positioning convex platform 59 plays installation positioning function.
3, the effect of seal pipe 6 is the plugging effect formed using its internal hot material column, is cooperated with the distributing device 7 of its underpart It uses, there is impeller inducer structure on the pallet at distributing device center, adjust gap to the appropriate location between pallet and seal pipe, lead to The velocity of rotation of control distributing device is crossed, blanking velocity is controlled, remains and is filled up in seal pipe by hot mine.
4, distributing device 7 is that a center is tapered, and surrounding is distributed several different length, cantilever chute clothes and sets It is standby, rotated by not stopping, from the material that seal pipe is fallen according in equal thickness filling even to heat exchanging chamber 10, wherein water-stop 9 effect is the gap blocked between 7 rotating device of distributing device and heat exchanging chamber, prevents from leaking out.1 function of material separating disc: blanking is lifted The sinter that pipe is fallen, while sinter is assigned in the several spiral arm chutes being circumferentially evenly distributed.Blade is according to spiral arm How much settings of chute, by being rotated together with distributing device the material on material separating disc under the effect of gravity, from blanking port to four Week is released, and is pushed into chute, and spiral arm support plays bracing reinforcement to spiral arm, and spiral arm chute is by internal wear-resistant liner and outside Braced frame is constituted, and is responsible on the material diversion to corresponding cloth anchor ring of distribution.The circumferentially blanking of same direction setting Mouth is a changed course guide groove component, and discharging point on spiral arm chute is accurately positioned, and controls material drop point site, supporter pair Spiral arm chute, material separating disc, spiral arm support carry out integration positioning support, while being also distributing device and external drive, supporting mechanism Connector has the function of support, transmission, sealing, and the driving supporting mechanism of distributing device can encrypt seal structure using upper suspension, It can also can be selected as the case may be using the structure of lower support encryption envelope.Different spiral arm chute discharging points are along different Circular motion, the cloth area equation of each loop wire two sides control
5, heat exchanging chamber 10 is an annular housing Fig. 3, heat sinter in heat exchanging chamber 10 with circulated air counterflow heat exchange, under Portion is distributed uniformly and circumferentially multiple discharge gates, is uniformly discharged by exchanging heat cold mine after cooling by multiple discharge gates. Heat exchanging chamber 10 includes heat-resistant antifriction layer, thermal insulation layer, three layers of steel structure casing, plays wear-resisting, heat-insulated, support.It is enclosed by inside and outside The ring section cylindrical cavity that shell surrounds jointly is the workspace of heat sinter Yu circulated air counterflow heat exchange.Completely cut off in heat exchanging chamber Heat transmits outward, and the middle layer between shell and wearing layer uses light-weight refractory heat insulating casting material, while playing heat-insulated and connecting The effect of support is connect, fire-resistant abrasion-proof layer is the working lining directly contacted with heat sinter on inside and outside casing, using antiwear heat resisting material Material production.Dredging machine 12 is the equipment of discharge gate putty dredging, and each discharge gate is equipped with one, unloads when sensor detects On material machine 13 when material cut-off, it was demonstrated that discharge port has scaffold phenomenon, and the automatic dredging machine 12 that starts is dredged, and the destruction of scaffold phenomenon is made Stream is unimpeded, its defeated material rod is retracted to outside the bed of material under conventional sense.Dredging machine is that conventional electro-hydraulic pusher is a kind of high thrust Electrohydraulic push rod, driver is the motor and hydraulic part sub-assembly of Electrohydraulic push rod, according to order-driven hydraulic cylinder act.It is wear-resisting to lead Bar is that the workpiece of dredging machine is moved back and forth obliquely by Hydraulic Cylinder, the material of dredge blockage feed opening, shuts down shape Guide rod is retracted to guide type shoe outer edge when state, keeps the continuity of wall-shaped chamber in taper dump skip.It is thin for sealing guide type shoe The guide type shoe on logical machine wear-resistant guide rod top, is equipped with sealing ring, plays guiding, support, sealing function.Guide type shoe is that dredging machine is resistance to The guide type shoe of guide rod lower part is ground, guiding, supporting role are played.
6, unloader 13 is the cold mine conveying equipment of tradition, and the sinter that each discharge gate is fallen is responsible for be evenly supplied to In deflector chute 14 below belt feeder, the shell and deflector chute 14 of unloader 13 are made into integral seal structure, prevent from leaking out and raise Dirt, belt feeder 15 are responsible for cold sinter to collect to transport next procedure.
7, cloth wind chamber 11 is one big annular intake adit, and wind is equal by the ventilation hole 117 on multiple taper dump skips top It is even to enter heat exchanging chamber lower part, uniformly rise under the action of velocity-reducing chamber negative pressure and reaches uniform heat exchange purpose.Outside annular cloth wind chamber Portion's casing, including top annular top plate, outer wall circular vertical plate and lower curtate annular bottom plate composition, play sealing, support, and interior Casing, taper dump skip group collectively constitute cloth wind cavity.The mount type chamber cylinder 112 of the dredging machine of each dump skip installation, plays branch Support and sealing function.Dredging machine pilot hole 113 is the positioning, support, pilot hole of dredging machine tubbing bar.Taper dump skip is taper The uniform water conservancy diversion outlet of material above bottom surface, while cooling wind is uniformly introduced by the ventilation hole of liner plate and shell by heat exchanging chamber It is interior.Discharge gate is uniformly discharged sinter after cooling, and the inside casing of annular cloth wind chamber is made of side wall annular vertical plate, rises Sealing, the effect supported, ventilating hole channel is the circular through hole being all provided on broach hopper wear-resistant liner and steel construction shell, is The intracavitary cold wind of cloth wind enters the channel of heat exchanging chamber.
8, velocity-reducing chamber 8 is the cylindrical cavity with cone section, plays the deceleration to hot wind by gravity depositing dust function.Blanking 81 function of hole: the through-hole of the seal pipe under hot mineral aggregate bucket is installed, circumferential weld is welded after seal pipe installation positioning or pressure-conducting disk root seals.? The hot blast manifold outlet 82 of even distribution is welded and fixed after docking with hot blast manifold pipeline in place.Velocity-reducing chamber internal spray refractory heat-insulating Material, steel structure casing, play support and sealing function, and refractory insulating layer is that light-weight refractory spray paint and hexsteel anchor pin structure Refractory insulating layer.
9, the function of deduster 16 and air-introduced machine 17 and regulating valve 24 is the size by controlling efflux gas amount.To control Reasonable negative pressure in heat exchanging chamber 10.The purpose of negative pressure in heat exchanging chamber is in order to avoid feed inlet and discharge port fugitive dust pollute.
10, hot mineral aggregate bucket 2 is the broach hopper for collecting water conservancy diversion heat sinter, and there are wear-resistant liner 219 and thermal insulation layer in inside 210, the fixation bracket 44 of chunk breaker is weldingly fixed on feed hopper bottom discharge gate top, plays support and sealing function, hopper Support base have weighing sensor 3, (weighing sensor is standard component) can be measured in real time weight of material in hopper. Electro-hydraulic pusher is a kind of Electrohydraulic push rod of traditional high thrust, and (Electrohydraulic push rod is standard component) the main of chunk breaker executes member Part is installed and used relatively two-by-two by one group 4.Driver is the motor and Combined hydraulic part of Electrohydraulic push rod, according to order-driven Hydraulic cylinder movement.Fixed bracket is the fixed frame of electro-hydraulic catch bar, is welded on hopper shell, plays a supportive role.Leading truck It is the leading truck of slotting tool.Slotting tool is one piece of rectangle plate knife, and front end geometry is identical as hot mineral aggregate bucket bottom section, and do not work shape When state, slotting tool is withdrawn, and front end face agrees with hopper inner conical surface, guarantees stream in general, 2 groups of slotting tools while in when working condition Heart insertion crushes the bulk of card resistance feed opening, dredges feed opening.Wear-resistant liner be in hot mineral aggregate bucket with material directly contact Wear-resistant liner.Thermal insulation layer is the thermal insulation layer in hot mineral aggregate bucket between wear-resistant liner and external steel structure casing.Steel structure casing heat The steel structure casing of mineral aggregate bucket inside and outside plays support and sealing function.
Two, operating method explanation
1, sintering process will guarantee the supply of heat sinter continuous-stable, while guarantee the stabilization of its ingredient and temperature, to the greatest extent Hot mine mean temperature may be improved.
2, the operating principle of this process system is to reduce circulation as far as possible under the premise of guaranteeing to be sintered cold mine dump temperature Air quantity promotes the temperature of hot fume, while the control of waste heat boiler delivery temperature is in suitable temperature.
3, the packing speed of heat sinter is adjusted by controlling the revolving speed speed of distributing device 7, operating principle is to try to It reduces revolving speed speed to adjust, keeps feed rate balanced.
Three, it illustrates
The working principle of the utility model
The utility model exchanges heat according to cold and hot medium counter flow, and the highest principle of heat exchanger effectiveness carries out technological design, passes through Distributing method is cleverly designed, thus realize the equalization stable of uniform the segregation-free phenomenon and heat transfer process of material filling, thus Realize efficient UTILIZATION OF VESIDUAL HEAT IN.The method that the utility model utilizes cooling wind closed cycle work, passes the gas through seven or eight hundred degree High-temperature material, the oxygen content in gas is reduced and 5% or less is recycled, make raw sinter can not double sintering and environment it is dirty Dye problem.
Four, the key point of the utility model and point to be protected
Realize that sealing and uniform distribution avoid material segregation heat exchange using seal pipe, distributing device, it is closed circuit using recuperated gas The method that the technology of circulation is sintered the vertical cooling heat transferring of mine,
Key point: it A, is realized using seal pipe 6, with the cooperation of distributing device 7 ventilative equal in sealing and uniform distribution, heat exchanging chamber Even, heat exchange thoroughly, obtains high efficiency heat exchange.
B, distributing device is equipped with the deflector chute of multiple and different length, non-co-content, realizes the uniform distribution of segregation-free.
C, it is provided with Minitype dust collector 16 on cool air hose 18, mini fan 17, regulating valve 24, passes through exhaust regulating valve 24 Adjust discharge gas flow number, control heat exchanging chamber in and velocity-reducing chamber in vacuum magnitude, reach feed inlet and formed with discharge port Negative pressure avoids fugitive dust from eliminating pollution.
D, the high-temperature material that seven or eight hundred degree are passed the gas through using the technology of recuperated gas closed cycle, by containing in gas Oxygen amount reduces by 5% or less and is recycled, and makes raw sinter can not double sintering.Avoid the raw material and oxygen two not cooked completely Secondary sintering, the disastrous effect for causing to stop production can not be discharged by striking up partnership in heat exchanging chamber.
E, the design of heat exchanging chamber 10 circularizes, and has reached cooling gas from the air inlet simultaneously of inner and outer ring lower part, has reached cooling gas It is more evenly distributed, exchanges heat more thorough.
F, dredging machine 12 selects electric hydraulic push rod or hydraulic push rod and air-leg, plays and destroys scaffold phenomenon, makes stream It is unobstructed.

Claims (7)

1. high-temperature material waste heat recycle bin system, including feeding device, distribution device, heat-exchanger rig, feeding device, feature exist In the feeding device includes crusher (1), hot mineral aggregate bucket (2), compensator (5), seal pipe (6);The crusher feed opening The hot mineral aggregate bucket (2) is connected, the hot mineral aggregate bucket lower part discharge port connects compensator, the compensator lower part connection sealing Pipe;The crusher (1), hot mineral aggregate bucket (2), compensator (5), seal pipe (6) inside are connected;
The distribution device includes distributing device (7), be at the top of the distributing device (7) center it is upward in conical pinnacle Surface has the material separating disc (71) of impeller inducer (72), and the taper direction along the material separating disc Pan Bi stretches out several around The water conservancy diversion of the chute (74) on length direction and the corresponding material separating disc is arranged on the cantilever for the cantilever (70) of different length Mouthful, each chute lower part setting in the circumferential direction, equidirectional blanking port (75), the cloth track loop wire of the blanking port It (77) is annulus, the material separating disc bottom attachment support body (76), motor (78) the driving supporter rotation;The material separating disc Pinnacle face the seal pipe (6) lower nozzle;
The heat-exchanger rig includes heat exchanging chamber (10), velocity-reducing chamber (8), cloth wind chamber (11), waste heat boiler (21), circulating fan (19), cold wind general pipeline (18), hot-blast main (20);The heat exchanging chamber (10) is an annular circle around supporter setting Column cavity;
Velocity-reducing chamber (8) lower part is divided into the annular truncated cone-shaped (84) that the lower end upper end Nei Shou extends out, top is divided into cylindrical (83) Closed shell suitable for reading, the annular truncated cone-shaped (84) of velocity-reducing chamber (8) lower part is around the supporter;Outside the heat exchanging chamber Ring wall upper limb border connects velocity-reducing chamber (8) shell (85) bottom;Subtract described in the heat exchanging chamber internal ring wall upper limb border connection Fast chamber (8) inner casing (87) bottom, velocity-reducing chamber (8) the inner casing upper peripheral edge are connected on the supporter outer wall;The velocity-reducing chamber It is connected to inside the heat exchanging chamber;The corresponding seal pipe is equipped with material-dropping hole (81) in the middle part of the velocity-reducing chamber top lid wall, described close Tube sealing is inserted into sealing cooperation in the blanking port, and equally distributed hot blast manifold mouth is arranged around blanking port on the top lid wall (82);The material separating disc, cloth cantilever are located inside the velocity-reducing chamber;
The cloth wind chamber (11) is that annular housing is docked in the heat exchanging chamber lower part, and the cloth wind is intracavitary, external annulus is changed with described Hot device internal ring wall, external annulus lower edge Butt sealing are fixed and internal connection, and the annular housing bottom of the cloth wind chamber is wholely set Multiple cone dump skips (114);Taper dump skip upper part of the housing is all evenly distributed with circular vent (117);The cloth wind Chamber is externally provided with the outer casing (111) of annular, and the outer casing external annulus upper end top cover and heat exchanging chamber external annulus lower part are closed Fixed, the outer casing internal ring wall upper limb and heat exchanging chamber internal ring wall root edge closing are fixed, the outer casing inner and outer rings wall bottom Edge sets bottom cover closing and is fixed on around the taper dump skip feed opening;The outer casing and the cloth wind is intracavitary, external annulus and Cavity is constituted between the taper dump skip shell, the dump skip is enclosed in the outer casing cavity with the part of ventilation hole It is interior;Air inlet is arranged in the outer casing (111);
The feeding device includes unloader (13), unloader shell (131), and the unloader is under the taper dump skip Multiple conveyer belts of symmetrical centre setting below material mouth, the unloader shell are that each conveyer belt is trapped among to internal circle Shell is closed, deflector chute (14) are set among the unloader outer casing bottom, material guide port, the biography is arranged in the deflector chute lower part Band inner end is sent to correspond to the deflector chute discharging;The material guide port lower part setting belt feeder transports mineral aggregate outward;The taper discharging Bucket feed opening protrudes into sealing cooperation in the unloader outer casing upper cover;
Waste heat boiler (21) top connects the hot wind of the velocity-reducing chamber by the hot-blast main (20) with each hot blast manifold Nozzle, the waste heat boiler lower part connect the air inlet of the outer casing external annulus lower part of the cloth wind chamber by the cold wind general pipeline (18) Mouthful, circulating fan (19) are set on the cold wind general pipeline;Heat-exchanger rig is set in the waste heat boiler.
2. high-temperature material waste heat recycle bin system as described in claim 1, which is characterized in that the outer casing of the cloth wind chamber (111) dredging machine pilot hole is set along the fixed multiple dredging machine mounting cylinders (112) in border, the taper dump skip shell (113), the electro-hydraulic pusher (121) of the dredging machine is supported in the dredging machine mounting cylinder, and dredging push rod (123) pierces institute It states dredging machine pilot hole and protrudes into the taper dump skip feed opening (115) and dredge;Setting monitoring Flow of Goods and Materials in unloader shell Sensor, when detecting material cut-off on unloader (13), starting dredging machine (12) dredging;
The Support Position of the hot mineral aggregate bucket (2) is equipped with weighing sensor (3), and the hot mineral aggregate bucket (2) is by flexible sealing It is tightly connected with upper and lower equipment, the cone pars infrasegmentalis of the hot mineral aggregate bucket (2) is equipped with chunk breaker (4), when the weighing and sensing When device (3) detects hot mineral aggregate bucket (2) gravimetric anomaly increase, hopper feed opening putty is determined, then it is broken to start the bulk The broken dredging of broken machine (4);
Chunk breaker (4) is circumferentially arranged on hot mineral aggregate bucket (2) the feed opening wall to be supported on fixed bracket (44), it is described Chunk breaker (4) includes radial slotting tool (47): the slotting tool is that one block of rectangle plate is inserted into the hot mineral aggregate bucket, before End surface shape and the hot mineral aggregate bucket bottom sidewall are coincide, and when off position, slotting tool is withdrawn, front end face and hopper inner conical surface Agree with closing hopper, guarantees stream in general, when working condition opposite two groups of slotting tools are inserted into center simultaneously, card resistance feed opening Bulk crushing, dredge feed opening;
The parietal layer structure of the hot mineral aggregate bucket (2) is wear-resistant liner (219), thermal insulation layer (210), steel structure casing from inside to outside (211);The parietal layer structure of the heat exchanging chamber (10) is heat-resistant antifriction layer (106), thermal insulation layer (105), outside steel construction from inside to outside Shell (103);The parietal layer structure of the velocity-reducing chamber (8) is thermal insulation layer (86), steel structure casing (85) from inside to outside.
3. high-temperature material waste heat recycle bin system as described in claim 1, which is characterized in that on the cold wind general pipeline (18) One release branch pipe (181) is set, regulating valve (24), deduster (16) and air-introduced machine are set gradually on the release branch pipe (17)。
4. high-temperature material waste heat recycle bin system as described in claim 1, which is characterized in that distributing device (7) supporter It is heat-insulated that watertight construction (9) seal clearance is set;Motor (78) the driving gear band moves the supporter rotation.
5. high-temperature material waste heat recycle bin system as described in claim 1, which is characterized in that waste heat boiler (21) are changed Hot charging is set to closed water circulating pipe (25), water circulating pipe connection steam turbine into, steam drain, the water-circulating pipe Boiler feed-water pump (23) are set on road, the superheated steam driving steam turbine (22) that the heat-exchanger rig generates externally does work, and does Low-pressure steam after work is pressurizeed after condensing by boiler feed-water pump (23) to be recycled for the heat-exchanger rig.
6. high-temperature material waste heat recycle bin system as described in claim 1, which is characterized in that the cantilever of the distributing device is arranged Cantilever support (73) controls blanking velocity, remains and filled up in seal pipe by hot mine by controlling the velocity of rotation of distributing device State.
7. high-temperature material waste heat recycle bin system as described in claim 1, which is characterized in that the compensator (5) is one kind Be flexible coupling short tube, and including internal wear-resistant sleeve (53), the upper and lower of wear-resistant sleeve (53) outer wall each fixes a section steel short tube One (55), steel short tube two (58), a stainless steel ripple seal pipe (56) is fastened between two steel short tubes, described resistance to Grinding set pipe (53) is divided into two sections up and down, and there is an oblique annular retractable seam (52) in centre, for compensator telescopic movable, described in upper section Hard heat-insulating layer (54) are fixed between steel short tube one and wear-resistant sleeve, the wear-resistant sleeve between steel short tube described in two sections The fixed flexible thermal insulation layer (57) of outer wall.
CN201820513384.0U 2018-04-11 2018-04-11 High-temperature material waste heat recycle bin system Active CN208579643U (en)

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Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108317865A (en) * 2018-04-11 2018-07-24 北京艾瑞机械有限公司 High-temperature material waste heat recovery station system and recovery method
CN112964072A (en) * 2021-02-01 2021-06-15 广东韶钢松山股份有限公司 Cooling furnace and material cooling method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN108317865A (en) * 2018-04-11 2018-07-24 北京艾瑞机械有限公司 High-temperature material waste heat recovery station system and recovery method
CN108317865B (en) * 2018-04-11 2023-12-22 北京艾瑞机械有限公司 High-temperature material waste heat recovery station system and recovery method
CN112964072A (en) * 2021-02-01 2021-06-15 广东韶钢松山股份有限公司 Cooling furnace and material cooling method
CN112964072B (en) * 2021-02-01 2023-03-14 广东韶钢松山股份有限公司 Cooling furnace and material cooling method

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