CN109443020A - A kind of high temperature lava granulation residual neat recovering system - Google Patents

A kind of high temperature lava granulation residual neat recovering system Download PDF

Info

Publication number
CN109443020A
CN109443020A CN201811408951.7A CN201811408951A CN109443020A CN 109443020 A CN109443020 A CN 109443020A CN 201811408951 A CN201811408951 A CN 201811408951A CN 109443020 A CN109443020 A CN 109443020A
Authority
CN
China
Prior art keywords
roller
pump
lava
cooling
high temperature
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Granted
Application number
CN201811408951.7A
Other languages
Chinese (zh)
Other versions
CN109443020B (en
Inventor
杨帆
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Chongqing Rock Energy Saving Technology Co Ltd
Original Assignee
Chongqing Rock Energy Saving Technology Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Chongqing Rock Energy Saving Technology Co Ltd filed Critical Chongqing Rock Energy Saving Technology Co Ltd
Priority to CN201811408951.7A priority Critical patent/CN109443020B/en
Publication of CN109443020A publication Critical patent/CN109443020A/en
Application granted granted Critical
Publication of CN109443020B publication Critical patent/CN109443020B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F27FURNACES; KILNS; OVENS; RETORTS
    • F27DDETAILS OR ACCESSORIES OF FURNACES, KILNS, OVENS, OR RETORTS, IN SO FAR AS THEY ARE OF KINDS OCCURRING IN MORE THAN ONE KIND OF FURNACE
    • F27D17/00Arrangements for using waste heat; Arrangements for using, or disposing of, waste gases
    • F27D17/004Systems for reclaiming waste heat
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28DHEAT-EXCHANGE APPARATUS, NOT PROVIDED FOR IN ANOTHER SUBCLASS, IN WHICH THE HEAT-EXCHANGE MEDIA DO NOT COME INTO DIRECT CONTACT
    • F28D21/00Heat-exchange apparatus not covered by any of the groups F28D1/00 - F28D20/00
    • F28D21/0001Recuperative heat exchangers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F19/00Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers
    • F28F19/002Preventing the formation of deposits or corrosion, e.g. by using filters or scrapers by using inserts or attachments
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F5/00Elements specially adapted for movement
    • F28F5/02Rotary drums or rollers
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F5/00Elements specially adapted for movement
    • F28F5/06Hollow screw conveyors
    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F28HEAT EXCHANGE IN GENERAL
    • F28FDETAILS OF HEAT-EXCHANGE AND HEAT-TRANSFER APPARATUS, OF GENERAL APPLICATION
    • F28F2250/00Arrangements for modifying the flow of the heat exchange media, e.g. flow guiding means; Particular flow patterns
    • F28F2250/08Fluid driving means, e.g. pumps, fans

Abstract

The present invention relates to field of energy recovery, specifically disclose a kind of high temperature lava granulation residual neat recovering system, including the first cooling body, the second cooling body and heat exchange mechanisms, first cooling body includes heat exchange box, the first driving assembly and the first roller group, and heat exchange box is equipped with lava entrance and particle outlet;First roller group includes the first roller;Cooling chamber is equipped in first roller;Second cooling body includes the second roller and the second actuator, and the second roller is equipped with particle entrance and cooling material outlet;Second roller inner wall even distribution has water conservancy diversion shred, and the second actuator drives the rotation of the second roller, is equipped with cooling duct in the second roller;Heat exchange mechanisms include the first pump, the second pump, First Heat Exchanger and the second heat exchanger, and the first pump, cooling chamber and First Heat Exchanger form the circulation path of closure;Second pump, cooling duct and the second heat exchanger form the circulation path of closure.Lava heat recovery effect can be improved in this programme.

Description

A kind of high temperature lava granulation residual neat recovering system
Technical field
The present invention relates to field of energy recovery, and in particular to a kind of residual neat recovering system.
Background technique
In metallurgical process, the ore containing metallic element reacts under high temperature action, obtains going back while molten metal Can obtain the clinker of molten state, referred to as lava, at present metallurgy clinker can apply building, manufacture of cement, highway subgrade and The fields such as soil adjusting, so also needing that cooling of furnace slag is made to form solid after clinker is separated with metal.
Currently used cooling means be lava is directly exposed to air or is placed natural cooling in a reservoir, but It is the time length, low efficiency that natural cooling needs since the temperature of lava is higher, and in natural cooling process, in lava Heat spills into air and loses, and is unfavorable for energy recycling.Secondly, the time that natural cooling needs is long, in natural cooling process In, if worker touches lava accidentally, worker can be burned.
For these reasons, this department, which has developed, cools down high temperature lava using liquid metal, and recycles high temperature lava In the high temperature lava of heat be granulated pre- heat recovery system.And in order to improve heat recovery effect, this department use application No. is Liquid metal in CN2014102689841 is as heat exchange medium, and the boiling point of the liquid metal is higher, in heat exchanging process It is not in boiling phenomenon, i.e., the alloy is rendered as liquid always in heat exchanging process, is not in the change of state, is conducive to Transmission.
Summary of the invention
The high temperature lava that lava heat can be recycled the purpose of the present invention is to provide one kind is granulated residual neat recovering system.
In order to achieve the above objectives, the technical scheme is that a kind of high temperature lava is granulated residual neat recovering system, including the One cooling body, the second cooling body and heat exchange mechanisms, if first cooling body include heat exchange box, the first driving assembly and Dry first roller group, the heat exchange box roof and bottom are respectively equipped with lava entrance and particle outlet;The first roller group packet It includes along symmetrically arranged two the first rollers of vertical plane, two the first rollers and heat exchange box are rotatablely connected, first driving group Part drives two the first rollers of same first roller group to rotate towards each other;Cooling chamber is equipped in first roller;
Second cooling body includes the second roller and the second actuator, and second roller is located under heat exchange box Side, second roller both ends are respectively equipped with particle entrance and cooling material outlet;The second roller inner wall is helically evenly equipped with Water conservancy diversion shred, second actuator drive the rotation of the second roller, are equipped with cooling duct in second roller;
The heat exchange mechanisms include the first pump, the second pump, First Heat Exchanger and the second heat exchanger, first pump, cooling Chamber is successively connected to from beginning to end with First Heat Exchanger, and forms the circulation path of closure;Second pump, cooling duct and the second heat exchange Device is successively connected to from beginning to end, and forms the circulation path of closure.
This programme has the beneficial effect that:
(1) lava of high temperature enters in heat exchange box from lava entrance, falls on the first roller, and edge under the effect of gravity The flowing of first roller surface is laid on the first roller surface, and the thickness of lava group is big compared with the contact surface of small, lava and the first roller, So the recovering effect of heat is more preferable in lava.
(2) lava will form lava particle after the cooling of the first roller, not need to carry out artificial granulation to lava again, Reduce the workload of worker.
It is additionally provided with the second cooling body below (three) first cooling bodies, the lava that the temperature dropped out from heat exchange box reduces Particle is fallen into the second roller, in the form of sheets and uniformly distributed in the shape of a spiral due to water conservancy diversion shred, so the lava particle in the second roller It is slided under the action of water conservancy diversion shred along the second roller inner wall, lava particle is in sliding process, remaining heat in lava particle It measures in the liquid metal that is transferred in cooling duct, the heat in lava particle is further reduced, therefore the second cooling body can be with Remaining heat in lava is further recycled, the effect of heat recovery is further enhanced in lava.
Preferred embodiment one, as the further improvement to base case, outside one of them first roller of the first roller group Wall is equipped with several granulation grooves.
The utility model has the advantages that high temperature lava is in molten, lava enters along the first roller flow process to be granulated in groove, lava It is further increased with the contact area of the first roller, so that heat recovery effect further increases.It is granulated molten in groove Solid is formed after rock is cooling, so the first roller in this programme can also be such that lava is formed while cooling down to lava The lesser solid of partial size, not needing the later period again crushes lava particle, further decreases workload.
Preferred embodiment two, as the further improvement to preferred embodiment one, the first roller includes the internal layer cylinder being fixedly connected With outer layer cylinder, the cooling chamber is between internal layer cylinder and outer layer cylinder.
The utility model has the advantages that internal layer cylinder is fixed with outer layer cylinder, internal layer cylinder plays a supporting role to outer layer cylinder, increases the strong of outer layer cylinder Degree so as to shorten the liquid metal and the distance between lava in cooling chamber, makes lava so the wall thickness of outer layer cylinder can reduce In heat can be transferred in liquid metal faster, improve cooling velocity.Secondly, compared with the first roller of single layer, it is cooling The volume of chamber reduces, and the amount liquid metal needed is less, can reduce the dosage of liquid metal, to reduce cost.
Preferred embodiment three, as the further improvement to preferred embodiment two, the second roller include the outer cylinder that is fixedly connected and Inner cylinder, the inner cylinder is located on the inside of outer cylinder, and cooling duct, between inner barrel and outer barrel, water conservancy diversion shred is fixed on inner cylinder inner wall On.
The utility model has the advantages that inner cylinder can increase the intensity of outer cylinder, the wall thickness of outer cylinder be can reduce, to reduce in cooling duct Liquid metal and the distance between lava particle, improve cooling velocity.Secondly, the situation that length in cooling duct is constant Under, the volume of cooling duct reduces, and reduces the dosage of liquid metal, reduces cost.
Preferred embodiment four, as the further improvement to preferred embodiment three, inner tank theca is fixed with helical blade.
The utility model has the advantages that helical blade flows the liquid metal in cooling duct axially along inner cylinder when inner barrel and outer barrel rotates It is dynamic, promote the liquid metal in cooling duct to flow to outside cooling duct, enters new liquid metal in cooling duct Cool down to lava particle, further increases the recovering effect of the intragranular heat of lava.
Preferred embodiment five, as the further improvement to base case, the section of water conservancy diversion shred is triangle, wedge shape, ladder Any one in shape, taper or inverted L shape.
The utility model has the advantages that lava particle is fallen on water conservancy diversion shred after entering heat exchanger tube from particle entrance, then along wedge block Inclined-plane sliding, the speed of lava particles fall and the inclined-plane non-perpendicular to wedge block, the pressure perpendicular to inclined-plane that wedge block is subject to Power reduces, and effectively wedge block is avoided to damage.
Preferred embodiment six is fixed with lower end and melts as the further improvement to preferred embodiment two or five at the top of heat exchange box The diversion trench of rock entrance connection.
The utility model has the advantages that diversion trench plays guiding role to the charging of high temperature lava, lava is avoided to slide to outside heat exchange box.
Preferred embodiment seven, as the further improvement to preferred embodiment six, the first pump and the second pump are mechanical pump.
The utility model has the advantages that being reduced by the temperature of First Heat Exchanger and the liquid metal of the second heat exchanger, so this programme can To use mechanical pump, and compared with electromagnetic pump, the price of mechanical pump is lower, can reduce cost.
Preferred embodiment eight, as the further improvement to preferred embodiment seven, first pump where circulation path in further include First liquid reserve tank, it is described second pump where circulation path in further include the second liquid reserve tank.
The utility model has the advantages that the first liquid reserve tank and the second liquid reserve tank are convenient for the storage of liquid metal.
Preferred embodiment nine, as the further improvement to preferred embodiment eight, the first pump and the second pump include the pump housing and pump Lid, the pump cover are detachably connected with the pump housing, and the pump housing is equipped with several jacks, and the pump cover is logical equipped with what is be connected to jack Hole, and it is equipped with the heating rod being inserted into jack by through-hole.
The utility model has the advantages that northern outdoor temperature is lower when winter, as outdoor temperature falls below 3 DEG C hereinafter, liquid metal temperature It may solidify, heating rod can heat liquid metal at this time, improve the temperature of liquid metal, keep liquid metal Mobility.
Detailed description of the invention
Fig. 1 is the front view of the embodiment of the present invention 1;
Fig. 2 is A-A in Fig. 1 to sectional view;
Fig. 3 is the cross-sectional view of outer cylinder in Fig. 1;
Fig. 4 is the sectional view of B-B direction in Fig. 3;
Fig. 5 is the sectional view of inner cylinder in Fig. 3;
Fig. 6 is the partial cutaway view pumped in Fig. 1;
Fig. 7 is the cross-sectional view of position-limit mechanism in the embodiment of the present invention 2;
Fig. 8 is the enlarged drawing in Fig. 7 at C;
Fig. 9 is the cross-sectional view of the first liquid reserve tank in the embodiment of the present invention 3.
Specific embodiment
It is further described below by specific embodiment:
Appended drawing reference in Figure of description includes: rack 1, the first actuator 11, rotary joint 12, the second actuator 13, bearing block 14, transmission gear 15, the first liquid reserve tank 16, liquid reserve tank ontology 161, top cover 162, sliding slot 163, location hole 164, Holding tank 165, mounting groove 166, maintenance door 167, air bag 168, U-shaped cover the 169, second heat exchanger 17, fixed block 18, the second liquid storage Case 19, diversion trench 21, discharge bucket 22, the first roller 3, is granulated groove 31, internal layer cylinder 32, cooling chamber 33, reinforcing rib at heat exchange box 2 34, the second roller 4, cross shaped member 41, outer cylinder 42, inner cylinder 43, cooling duct 44, rotation axis 45, water conservancy diversion shred 46, closure member 47, cooling material outlet 48, rotate gear 49, change 5, vertical ring 51, ball 52, threaded rod 53, shaft 6, disk 61, magnetic block 62, hydraulic cylinder 7, cylinder body 71, magnetic sheet 72, pressure spring 73, outgassing nonreturn valve 74, breather check valve 75, U-shaped steel pipe 76, relief valve 77, air outlet passage 78, second pumps 8, the pump housing 81, pump cover 82, admission chamber 83, heating rod 84, helical blade 9, connector 91.
Embodiment 1 is substantially as shown in Fig. 1:
A kind of high temperature lava is granulated residual neat recovering system, including rack 1, the first cooling body, the second cooling body and changes Heat engine structure, the first cooling body include that heat exchange box 2, the first driving assembly and three the first roller groups, heat exchange box 2 are welded on rack On 1.2 roof of heat exchange box and bottom are respectively equipped with lava entrance and particle outlet, and diversion trench 21 and discharging are welded on heat exchange box 2 Bucket 22, diversion trench 21 and discharge bucket 22 are aligned with lava entrance and particle outlet respectively.
Three the first roller groups are vertically distributed in heat exchange box 2, by taking the first roller group of the top as an example, the first roller Group include along symmetrically arranged two the first rollers 3 of vertical plane, two 3 both ends of the first roller coaxially integrally formed with shaft 6, Shaft 6 is rotatablely connected through heat exchange box 2 and with heat exchange box 2, in order to support shaft 6, has been bolted bearing block in rack 1 14.It being keyed in two shafts 6 in left side there are two the transmission gear 15 engaged, the first driving assembly is located at 2 left side of heat exchange box, First driving assembly includes three motors being vertically distributed, and motor is bolted in rack 1, and three motors respectively drive Three the first roller group rotations.First liquid reserve tank 16 fixed with rack 1 is equipped on the right side of heat exchange box 2,3 right side of the first roller turns Axis 6 runs through 16 left wall of the first liquid reserve tank, and is rotatablely connected with the first liquid reserve tank 16, is equipped between shaft 6 and the first liquid reserve tank 16 Comb tooth sealing structure avoids the liquid metal in the first liquid reserve tank 16 from revealing.
Still by taking the first roller 3 of the top as an example, in conjunction with Fig. 2, the first roller 3 includes outer layer cylinder and internal layer cylinder 32, internal layer Cylinder 32 is located in outer layer cylinder and fixes with outer layer cylinder, and cooling chamber 33 is formed between outer layer cylinder and internal layer cylinder 32, be equipped in shaft 6 with The interface channel that cooling chamber 33 is connected to.In order to be supported to outer layer cylinder, several reinforcing ribs 34, reinforcing rib are equipped in cooling chamber 33 34 both ends are respectively welded on outer layer cylinder and internal layer cylinder 32.The outer layer drum outer wall of first roller 3 is equipped with several granulation grooves 31, this In embodiment, another first roller, 3 outer wall can be shiny surface, integrally formed with several granulation convex blocks or can be equipped with Several granulation grooves 31.
In conjunction with shown in Fig. 3, Fig. 4 and Fig. 5, the second cooling body includes the second roller 4 and the second actuator 13, the second roller 4 are located at the lower section of heat exchange box 2, and the second roller 4 includes inner cylinder 43 and outer cylinder 42, and inner cylinder 43 is located at 42 inside of outer cylinder, and inner cylinder 43 Cooling duct 44 is formed between outer cylinder 42, laterally setting, 43 outer wall of inner cylinder are welded with several connections for outer cylinder 42 and inner cylinder 43 Part 91, connector 91 can be connecting shaft and connecting plate, select connecting shaft in the present embodiment, connector 91 is far from 43 one end of inner cylinder It is welded on outer cylinder 42, inner cylinder 43 is fixed by connector 91 and outer cylinder 42.42 left and right ends of outer cylinder are respectively equipped with and inner cylinder 43 The cooling material outlet 48 of inner cavity connection and particle entrance, particle entrance 41 is located at 22 lower section of discharge bucket, and is connected to discharge bucket 22, 22 lower end of discharge bucket and outer cylinder 42 are rotatablely connected.43 inner wall of inner cylinder is welded with several helically uniformly distributed water conservancy diversion shreds 46, water conservancy diversion Shred 46 can be any one in triangle, wedge shape, trapezoidal, taper or inverted L shape, and the present embodiment selection is trapezoidal, interior 43 outer walls of cylinder are welded with spiral helicine helical blade 9.
Outer cylinder wall coaxial is fixed with rotate gear 49, and the second actuator 13 is bolted in rack 1, this implementation The second actuator 13 in example is motor, and 13 first line of a couplet of the second actuator is connected to the driving gear engaged with rotate gear 49, passes through Driving gear engages driving outer cylinder and the rotation of inner cylinder 43 with rotate gear 49.
The outer wall of 43 left and right ends of inner cylinder is respectively and fixedly provided with the closure member 47 fixed with outer cylinder, two closing coolings of closure member 47 Channel 44, closure member 47 can be annular slab or annular frid, select annular frid in the present embodiment.Closure member 47 is hollow, envelope Hollow cross shaped member 49 is fixed in closing member 47, cross shaped member 49 can be fixing axle or fixed plate, select in the present embodiment Fixed plate.The support arm of cross shaped member 49 runs through 43 side wall of inner cylinder, and welds with inner cylinder 43, and the crossover location on cross shaped member 49 On the central axes of inner cylinder 43.Closure member 47 is equipped with the rotation axis 45 coaxial with inner cylinder 43, rotation axis far from 43 side of inner cylinder 45 weld with cross shaped member 49, also are provided with interface channel in rotation axis 45, interface channel is connected to 49 inner cavity of cross shaped member, left side Rotation axis 45 far from inner cylinder 43 one end run through outer cylinder 42, and with outer cylinder 42 weld.The second liquid storage is equipped on the right side of discharge bucket 22 Case 19, the second liquid reserve tank 19 are fixed in rack 1, and 45 right end of rotation axis on right side sequentially passes through 42 right end of outer cylinder, discharge bucket 22 19 left wall of side wall and the second liquid reserve tank, rotation axis 45 and outer cylinder 42 weld, and pass through comb teeth between rotation axis 45 and liquid reserve tank 16 Sealing structure sealing.
Heat exchange mechanisms include the first pump, the second pump 8, First Heat Exchanger and the second heat exchanger 17, the first liquid reserve tank 16 and the Two liquid reserve tanks 19 are connected to the liquid feeding end of First Heat Exchanger and the second heat exchanger 17 by pipeline respectively, First Heat Exchanger and second The outlet end of heat exchanger 17 is connected to the liquid feeding end of the first pump and the second pump 8 respectively by pipeline.The outlet end of second pump 8 passes through Pipeline is connected to the rotation axis 45 for being located at 4 left side of the second roller.The outlet end of first pump is communicated with connecting tube, and connecting tube is by turning Dynamic connector is connected to the shaft 6 for being located at 2 left side of heat exchange box.When the first pump work, the liquid metal by the first pump successively passes through Again by the first pump after cooling chamber 33, the first liquid reserve tank 16 and First Heat Exchanger.When the second 8 work of pump, by the second pump 8 Liquid metal is successively again by the second pump 9 after cooling duct 44, the second liquid reserve tank 19 and the second heat exchanger 17.
The first pump and the second pump 8 in the present embodiment use gear pump, and as shown in connection with fig. 6, gear pump includes the pump housing 81 With pump cover 82, pump cover 82 is bolted on 81 left end of the pump housing, and 81 right end of the pump housing is equipped with admission chamber 83, left end is equipped with liquid Chamber, the two sides up and down of the two sides up and down of admission chamber 83 and out sap cavity are equipped with jack, set on pump cover 82 there are four respectively with four The through-hole of receptacle alignment.It is set on the pump housing 81 there are four heating rod 84, four heating rods 84 are inserted into four by four through-holes respectively In jack, liquid metal can solidify when the temperature is low, when four heating rods 84 work to admission chamber 83 or out the liquid in sap cavity State metal is heated.
The present embodiment residual neat recovering system work when, be first opened manually the first pump and second pump the 8, first actuator 11, Second actuator 13 and First Heat Exchanger and the second heat exchanger 17, then by the lava of the molten state of high temperature above diversion trench 21 It is added in heat exchange box 2.When first actuator 11 works, in conjunction with Fig. 2, since two transmission gears 15 engage, first roller in left side Cylinder 3 rotates clockwise, first roller 3 on right side rotates counterclockwise, and drops down onto two the first rollers 3 of the first roller group of the top On lava be laid on two the first rollers 3, and enter be granulated groove 31 in.Liquid metal is under the action of the first pump through being subcooled But chamber 33, in the liquid metal into cooling chamber 33, lava temperature reduces the heat transfer in lava contacted with the first roller 3 Solidification forms particle.
The lava of final granule shape enters in inner cylinder 43 from discharge bucket 22 into particle entrance 41 is crossed, the driving of the second actuator 13 The rotation of second roller 4, lava particle move downward under the action of helical blade 9 along inner cylinder 43, finally from cooling material outlet 48 It drops out.And liquid metal second pump 8 under the action of by cooling duct 44, cool down to the lava particle in inner cylinder 43, So the temperature of the lava particle finally dropped out from cooling material outlet 48 is lower.
The high temperature fluent metal being discharged from cooling chamber 33 is introduced into the first liquid reserve tank 16, and it is cold to enter back into First Heat Exchanger But, it is finally recirculated by the first pump.From cooling duct 44 be discharged high temperature fluent metal successively pass through the second liquid reserve tank 19, Second heat exchanger 17 is cooled, finally recirculates by the second pump 8.When the pump of restarting first and the second pump 8, first open Heating rod 84, heating rod 84 heat the liquid metal in pipeline, and the liquid metal of solidification is made to become liquid again, restore Mobility turns off heating rod 84.
Embodiment 2
On the basis of embodiment 1, as shown in Figure 7 and Figure 8, the shaft 6 on 2 right side of heat exchange box is located in this programme and is located at 45 periphery of rotation axis on 42 right side of outer cylinder is all provided with limited position mechanism, avoids shaft 6 and rotation axis 45 that axial play occurs.
By taking shaft 6 as an example, position-limit mechanism includes the fixed block 18 positioned at 16 left side of the first liquid reserve tank, fixed block 18 and first 16 left wall of liquid reserve tank is integrally formed.Fixed block 18 is ring-type, and shaft 6 first protrudes into after 18 inner circumferential of fixed block again through the first liquid reserve tank 16 left walls.6 periphery of shaft is also rotatably connected to change 5, and change 5 is located on the left of rotation comb teeth, and change 5 includes being parallel to shaft 6 The annulus of outer wall and two vertical rings 51 perpendicular to shaft 6, two vertical rings 51 are located at left and right sides of annulus, and with circle Ring is integrally formed.6 outer wall of shaft is set there are two the annular groove being parallel to each other, and two vertical rings 51 are located at two annular grooves It is interior, and can be rotated relative to annular groove.Several balls 52 are equipped between shaft 6 and annulus, when annulus is rotated relative to shaft 6 When, ball 52 reduces the frictional force effect that shaft 6 and annulus are subject to.
Side of the annulus far from shaft 6 is uniformly distributed there are three limiting slot, and it is logical to be distributed along the circumference with three screw threads on fixed block 18 Road, three screw channels are aligned with three limiting slots respectively, and are set there are three the threaded rod 53 being threadedly engaged with screw channel, will After threaded rod 53 screws in screw channel, 53 end of threaded rod is protruded into limiting slot, pushes against change 5, is played support to shaft 6 and is made With while, also avoid shaft 6 that axial float occurs during rotation.
After threaded rod 53 pushes against change 5, change 5 can not be rotated relative to threaded rod 53, therefore when shaft 6 rotates, change 5 It is rotated relative to shaft 6, ball 52 rolls between change 5 and shaft 6, the friction that ball 52 reduces change 5 and shaft 6 is subject to Power avoids change 5 and shaft 6 from wearing.Secondly, ball 52 plays a supporting role to change 5, avoid change 5 in threaded rod 53 Pressure effect is lower, and deformation occurs.
6 outer wall of shaft is painted coated with high temperature resistant, and the present embodiment is painted using inorganic silicon high temperature resistant, high temperature resistant paint solidification Oil resistant paint layer is formed afterwards.It is fixed with thermal insulation layer outside high-temperature-resistant layer, the thermal insulation layer in the present embodiment uses asbestos layer, avoids work People is burned after touching shaft 6.
Embodiment 3
On the basis of embodiment 2, the first liquid reserve tank 16 and the second liquid reserve tank 19 in the present embodiment are identical, the present embodiment In be illustrated by taking the first liquid reserve tank 16 as an example.As shown in figure 9, the first liquid reserve tank 16 includes the liquid reserve tank ontology of rectangular-shape 161, the top of liquid reserve tank ontology 161 is equipped with top cover 162, and 16 bottom of the first liquid reserve tank is equipped with liquid outlet, in liquid reserve tank ontology 161 Left side set that there are three inlet openings at the close over lid, three inlet openings are uniformly distributed along the vertical direction of liquid reserve tank ontology 161, Inlet opening is for being connected to the first roller 3.Mounting groove 166, the left side wall of mounting groove 166 are equipped on the right side of liquid reserve tank ontology 161 It is not connected to directly with liquid reserve tank ontology 161, the maintenance door 167 that can close mounting groove 166, maintenance door is equipped in mounting groove 166 167 are arranged close to top cover 162, and maintenance door 167 is bolted on liquid reserve tank ontology 161, is additionally provided in maintenance door 167 Three bottoming holes corresponding with feed liquor hole site, when the liquid metal in interface channel needs to heat, in bottoming hole interpolation Enter heating rod, and heating rod is protruded into interface channel.
One end that shaft 6 protrudes into liquid reserve tank ontology 161 is coaxially fixed with the disk 61 in liquid reserve tank ontology 161, The periphery of disk 61 is equipped with magnetic block 62.Beneficial hydraulic cylinder 7, the hydraulic stem direction peace of hydraulic cylinder 7 are horizontally fixed on top cover 162 166 side of tankage is equipped with sliding slot 163 on top cover 162, slidably connects cylinder body 71, the opening court of cylinder body 71 in sliding slot 163 On, the hydraulic rod end of hydraulic cylinder 7 is fixed on cylinder body 71.Vertical sliding is connected with magnetic sheet 72, magnetic sheet 72 in cylinder body 71 Bottom is equipped with the pressure spring 73 fixed with cylinder body 71, and wherein magnetic pole of the magnetic block 62 with 72 phase of magnetic sheet close to one end is opposite.In cylinder 71 side wall of body is equipped with the outgassing nonreturn valve 74 and breather check valve 75 for being located at 72 lower section of magnetic sheet, when positioned at 72 lower section of magnetic sheet When volume in cylinder body 71 increases, pressure reduces, and extraneous gas enters in cylinder body 71 from breather check valve 75.When under magnetic sheet 72 When the volume of square cylinder body 71 reduces, pressure increases, and the gas in cylinder body 71 is discharged from outgassing nonreturn valve 74.
It is fixed with U-shaped steel pipe 76 at the outgassing nonreturn valve 74 of cylinder body 71, wherein one end of U-shaped steel pipe 76 is welded on cylinder body It is another to be singly welded on middle part of the maintenance door 167 far from 166 side of mounting groove on 71, in maintenance door 167 close to mounting groove 166 1 There are three air bag 168 corresponding with 164 position of location hole, air bags 168 to be fixed with high temperature resistant far from 167 side of maintenance door for side bonds U-shaped cover 169, the U-shaped opening looked for is towards maintenance door 167, and U-shaped cover 169 can block location hole 164 completely, in location hole 164 Place is additionally provided with the holding tank 165 entered for U-shaped cover 169.Connection U-shaped steel pipe 76 and each air bag 168 are equipped in maintenance door 167 Air outlet passage 78, U-shaped steel pipe 76 are equipped with relief valve 77.
Specific implementation process is as follows:
When installation, hydraulic cylinder 7 is manually started, so that the hydraulic stem of hydraulic cylinder 7 is moved to the left, so that maintenance door 167 enters In mounting groove 166, while U-shaped cover 169 enters in holding tank 165, so that maintenance door 167 is pushed against on sealing ring.
In the system work process of the present embodiment, since shaft 6 and the first roller 3 rotate synchronously, at this time disk 61 with Shaft 6 rotate synchronously, in 61 rotation process of disk, magnetic block 62 on disk 61 constantly far from and close to magnetic sheet 72, when When magnetic block 62 is close to magnetic sheet 72, attraction is generated between magnetic block 62 and magnetic sheet 72, so that 72 slide downward of magnetic sheet, Pressure spring 73 is squeezed simultaneously, so that pressure spring 73 generates deformation, the volume in 72 lower section cylinder body 71 of magnetic sheet reduces, the gas in cylinder body 71 Body enters in air bag 168 through U-shaped steel pipe 76 and air outlet passage 78, and when magnetic block 62 is far from magnetic sheet 72, magnetic block 62 Attraction between magnetic sheet 72 weakens, the upward sliding under the active force that pressure spring 73 resets of magnetic sheet 72, under magnetic sheet 72 Volume in square cylinder body 71 increases, and extraneous gas is added into cylinder body 71, in this way during shaft 6 constantly rotates, cylinder body 71 constantly feed gas into air bag 168, and air bag 168 is expanded by the limit of U-shaped cover 169 only towards left side, so that U-shaped cover 169 is pushed against always at location hole 164.
When needing to open maintenance door 167, operator opens relief valve 77, after the gas discharge in air bag 168, then Start hydraulic cylinder 7, so that the hydraulic stem of hydraulic cylinder 7 moves right, to open maintenance door 167.
What has been described above is only a preferred embodiment of the present invention, it is noted that for those skilled in the art, Without departing from the inventive concept of the premise, several modifications and improvements can also be made, these also should be considered as guarantor of the invention Range is protected, these all will not influence the effect and patent practicability that the present invention is implemented.The present invention omits the technology of description, shape Shape, construction portion are well-known technique.

Claims (10)

1. a kind of high temperature lava is granulated residual neat recovering system, it is characterised in that: including the first cooling body, the second cooling body and Heat exchange mechanisms, first cooling body include heat exchange box, the first driving assembly and the first roller group, the heat exchange box roof and Bottom is respectively equipped with lava entrance and particle outlet;The first roller group includes at least two first rollers, two the first rollers Cylinder is rotatablely connected with heat exchange box, and first driving assembly drives the rotation of the first roller;Cooling chamber is equipped in first roller;
Second cooling body includes the second roller and the second actuator, and second roller is located at the lower section of heat exchange box, institute It states the second roller both ends and is respectively equipped with particle entrance and cooling material outlet;It is thin that the second roller inner wall is helically evenly equipped with water conservancy diversion Piece, second actuator drive the rotation of the second roller, are equipped with cooling duct in second roller;
The heat exchange mechanisms include the first pump, the second pump, First Heat Exchanger and the second heat exchanger, first pump, cooling chamber and First Heat Exchanger is successively connected to from beginning to end, and forms the circulation path of closure;Second pump, cooling duct and the second heat exchanger according to Secondary head and the tail connection, and form the circulation path of closure.
2. a kind of high temperature lava according to claim 1 is granulated residual neat recovering system, it is characterised in that: first roller One of them first roller outer wall of group is equipped with several granulation grooves.
3. a kind of high temperature lava according to claim 2 is granulated residual neat recovering system, it is characterised in that: first roller Including the internal layer cylinder and outer layer cylinder being fixedly connected, the cooling chamber is between internal layer cylinder and outer layer cylinder.
4. a kind of high temperature lava according to claim 1 is granulated residual neat recovering system, it is characterised in that: second roller Including the outer cylinder and inner cylinder being fixedly connected, the inner cylinder is located on the inside of outer cylinder, and cooling duct is between inner barrel and outer barrel, institute Water conservancy diversion shred is stated to be fixed on inner cylinder inner wall.
5. a kind of high temperature lava according to claim 4 is granulated residual neat recovering system, it is characterised in that: the inner tank theca It is fixed with helical blade.
6. a kind of high temperature lava according to claim 1 is granulated residual neat recovering system, it is characterised in that: the water conservancy diversion shred Section be triangle, wedge shape, trapezoidal, taper or inverted L shape in any one.
7. a kind of high temperature lava granulation residual neat recovering system according to claim 3 or 6, it is characterised in that: the heat exchange Box top is fixed with the diversion trench that lower end is connected to lava entrance.
8. a kind of high temperature lava according to claim 7 is granulated residual neat recovering system, it is characterised in that: first pump and Second pump is mechanical pump.
9. a kind of high temperature lava according to claim 8 is granulated residual neat recovering system, it is characterised in that: first pump institute Circulation path in further include the first liquid reserve tank, it is described second pump where circulation path in further include the second liquid reserve tank.
10. a kind of high temperature lava according to claim 9 is granulated residual neat recovering system, it is characterised in that: first pump It include the pump housing and pump cover with the second pump, the pump cover is detachably connected with the pump housing, and the pump housing is equipped with several jacks, the pump The through-hole for being equipped with and being connected to jack is covered, and is equipped with the heating rod being inserted into jack by through-hole.
CN201811408951.7A 2018-11-23 2018-11-23 High Wen Rongyan granulation waste heat recovery system Active CN109443020B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201811408951.7A CN109443020B (en) 2018-11-23 2018-11-23 High Wen Rongyan granulation waste heat recovery system

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201811408951.7A CN109443020B (en) 2018-11-23 2018-11-23 High Wen Rongyan granulation waste heat recovery system

Publications (2)

Publication Number Publication Date
CN109443020A true CN109443020A (en) 2019-03-08
CN109443020B CN109443020B (en) 2024-04-16

Family

ID=65554807

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201811408951.7A Active CN109443020B (en) 2018-11-23 2018-11-23 High Wen Rongyan granulation waste heat recovery system

Country Status (1)

Country Link
CN (1) CN109443020B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109945666A (en) * 2019-03-29 2019-06-28 重庆岩昱节能科技有限公司 High temperature lava heat-exchange system

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009227496A (en) * 2008-03-20 2009-10-08 Jfe Steel Corp Method for cooling molten slag
CN201548106U (en) * 2009-10-29 2010-08-11 杨正清 Inner cooled heat energy recycling and cooling rotary drum
CN203478288U (en) * 2013-07-22 2014-03-12 遂宁华能机械有限公司 Cylinder type quick slag cooler
CN108036662A (en) * 2018-01-08 2018-05-15 重庆岩昱节能科技有限公司 One kind melting calcium carbide heat recovery system and method
CN108165686A (en) * 2018-01-13 2018-06-15 秦皇岛点知汇科技有限公司 A kind of drum-type slag granulation and residual neat recovering system

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JP2009227496A (en) * 2008-03-20 2009-10-08 Jfe Steel Corp Method for cooling molten slag
CN201548106U (en) * 2009-10-29 2010-08-11 杨正清 Inner cooled heat energy recycling and cooling rotary drum
CN203478288U (en) * 2013-07-22 2014-03-12 遂宁华能机械有限公司 Cylinder type quick slag cooler
CN108036662A (en) * 2018-01-08 2018-05-15 重庆岩昱节能科技有限公司 One kind melting calcium carbide heat recovery system and method
CN108165686A (en) * 2018-01-13 2018-06-15 秦皇岛点知汇科技有限公司 A kind of drum-type slag granulation and residual neat recovering system

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN109945666A (en) * 2019-03-29 2019-06-28 重庆岩昱节能科技有限公司 High temperature lava heat-exchange system
CN109945666B (en) * 2019-03-29 2020-05-22 重庆岩昱节能科技有限公司 High-temperature lava heat exchange system

Also Published As

Publication number Publication date
CN109443020B (en) 2024-04-16

Similar Documents

Publication Publication Date Title
CN206143232U (en) Blast furnace casting ditch tap drain water -cooling device
CN109443020A (en) A kind of high temperature lava granulation residual neat recovering system
CN108036662A (en) One kind melting calcium carbide heat recovery system and method
CN2771660Y (en) Improved drum-type spiral slug-cooling maching
CN102554119A (en) Co-rotating type cooling drum
CN108007223A (en) Crawler type calcium carbide waste-heat recovery device and recovery method
CN209745017U (en) High-temperature lava granulation waste heat recovery system
CN103468846A (en) Blast furnace slagging channel with embedded water cooling system
CN204125474U (en) A kind of hot molten slag gets slag device online
CN109405612A (en) A kind of liquid metal circulatory system
CN110822929B (en) Cement kiln waste heat recovery device
CN206944732U (en) Cold ash bucket
CN106367551A (en) Main channel water-cooling device of blast furnace tapping channel and mounting and utilizing method
CN209416134U (en) A kind of high-temperature particle cooling system
CN207350358U (en) A kind of spiral heat exchange conveyer and screw conveyor shaft
CN208282669U (en) High leakproofness heat exchange roller end construction
CN212152363U (en) Blast furnace ironmaking distributing device water-cooling airtight box combined cooling device
CN203784972U (en) Double-spiral slag cooler
CN2934929Y (en) Continuous rolling cold slag device
CN208171073U (en) Concave-convex type heat exchange roller frame
CN109539799A (en) Scraping type high temperature lava cooling roller
CN106119536A (en) A kind of manganese oxide powder cooling device
CN206399195U (en) A kind of stove cooling device and its mounting structure
CN219385211U (en) Opening expansion device for tapping hole in electric arc furnace steelmaking process
CN106755649B (en) A kind of controllable turn over of output beats the grey formula slag granulating of the anti-ease of heat exchange and heat-energy recovering apparatus

Legal Events

Date Code Title Description
PB01 Publication
PB01 Publication
SE01 Entry into force of request for substantive examination
SE01 Entry into force of request for substantive examination
GR01 Patent grant
GR01 Patent grant