CN110173696A - A kind of electrolytic aluminium solid waste manifold type burning processing system and method - Google Patents
A kind of electrolytic aluminium solid waste manifold type burning processing system and method Download PDFInfo
- Publication number
- CN110173696A CN110173696A CN201910496413.6A CN201910496413A CN110173696A CN 110173696 A CN110173696 A CN 110173696A CN 201910496413 A CN201910496413 A CN 201910496413A CN 110173696 A CN110173696 A CN 110173696A
- Authority
- CN
- China
- Prior art keywords
- incinerator
- upper half
- heat transfer
- lower half
- air preheater
- 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
Links
- 239000002910 solid waste Substances 0.000 title claims abstract description 37
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 title claims abstract description 28
- 229910052782 aluminium Inorganic materials 0.000 title claims abstract description 28
- 238000012545 processing Methods 0.000 title claims abstract description 28
- 239000004411 aluminium Substances 0.000 title claims abstract description 26
- 238000000034 method Methods 0.000 title description 16
- 230000008878 coupling Effects 0.000 claims abstract description 45
- 238000010168 coupling process Methods 0.000 claims abstract description 45
- 238000005859 coupling reaction Methods 0.000 claims abstract description 45
- 239000002699 waste material Substances 0.000 claims abstract description 44
- 239000007789 gas Substances 0.000 claims abstract description 38
- 238000004064 recycling Methods 0.000 claims abstract description 22
- 238000011084 recovery Methods 0.000 claims abstract description 19
- 239000000779 smoke Substances 0.000 claims abstract description 18
- 229910001610 cryolite Inorganic materials 0.000 claims abstract description 13
- 238000003672 processing method Methods 0.000 claims abstract description 7
- 239000002737 fuel gas Substances 0.000 claims abstract description 5
- 230000008676 import Effects 0.000 claims abstract description 4
- 235000021050 feed intake Nutrition 0.000 claims abstract 2
- 238000012546 transfer Methods 0.000 claims description 60
- 239000013078 crystal Substances 0.000 claims description 31
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 25
- 239000003546 flue gas Substances 0.000 claims description 25
- 239000007788 liquid Substances 0.000 claims description 21
- 239000000463 material Substances 0.000 claims description 18
- 229910052731 fluorine Inorganic materials 0.000 claims description 16
- 239000011737 fluorine Substances 0.000 claims description 16
- 238000010438 heat treatment Methods 0.000 claims description 14
- 239000000706 filtrate Substances 0.000 claims description 11
- 239000003517 fume Substances 0.000 claims description 10
- 239000002994 raw material Substances 0.000 claims description 10
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 claims description 9
- 239000012530 fluid Substances 0.000 claims description 9
- 239000000843 powder Substances 0.000 claims description 9
- 238000000926 separation method Methods 0.000 claims description 7
- 238000010521 absorption reaction Methods 0.000 claims description 6
- 238000004891 communication Methods 0.000 claims description 3
- 238000001816 cooling Methods 0.000 claims description 3
- 238000002844 melting Methods 0.000 claims description 3
- 230000008018 melting Effects 0.000 claims description 3
- 239000000047 product Substances 0.000 claims description 3
- 230000001172 regenerating effect Effects 0.000 claims description 3
- PXGOKWXKJXAPGV-UHFFFAOYSA-N Fluorine Chemical compound FF PXGOKWXKJXAPGV-UHFFFAOYSA-N 0.000 claims 1
- 239000004575 stone Substances 0.000 claims 1
- YCKRFDGAMUMZLT-UHFFFAOYSA-N Fluorine atom Chemical compound [F] YCKRFDGAMUMZLT-UHFFFAOYSA-N 0.000 description 15
- 238000002485 combustion reaction Methods 0.000 description 13
- 239000003610 charcoal Substances 0.000 description 12
- 239000000446 fuel Substances 0.000 description 12
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 11
- 229910052799 carbon Inorganic materials 0.000 description 9
- 239000000126 substance Substances 0.000 description 9
- 230000000694 effects Effects 0.000 description 8
- XFXPMWWXUTWYJX-UHFFFAOYSA-N Cyanide Chemical compound N#[C-] XFXPMWWXUTWYJX-UHFFFAOYSA-N 0.000 description 7
- 230000008569 process Effects 0.000 description 7
- 239000002893 slag Substances 0.000 description 7
- 230000000391 smoking effect Effects 0.000 description 7
- 239000011148 porous material Substances 0.000 description 6
- KRHYYFGTRYWZRS-UHFFFAOYSA-M Fluoride anion Chemical compound [F-] KRHYYFGTRYWZRS-UHFFFAOYSA-M 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- 239000000243 solution Substances 0.000 description 5
- 230000008901 benefit Effects 0.000 description 4
- 239000002002 slurry Substances 0.000 description 4
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000005868 electrolysis reaction Methods 0.000 description 3
- 230000006872 improvement Effects 0.000 description 3
- 238000012986 modification Methods 0.000 description 3
- 230000004048 modification Effects 0.000 description 3
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 3
- 238000006243 chemical reaction Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 230000007774 longterm Effects 0.000 description 2
- 241001465754 Metazoa Species 0.000 description 1
- 241000237983 Trochidae Species 0.000 description 1
- 230000005540 biological transmission Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 238000007600 charging Methods 0.000 description 1
- RKTYLMNFRDHKIL-UHFFFAOYSA-N copper;5,10,15,20-tetraphenylporphyrin-22,24-diide Chemical compound [Cu+2].C1=CC(C(=C2C=CC([N-]2)=C(C=2C=CC=CC=2)C=2C=CC(N=2)=C(C=2C=CC=CC=2)C2=CC=C3[N-]2)C=2C=CC=CC=2)=NC1=C3C1=CC=CC=C1 RKTYLMNFRDHKIL-UHFFFAOYSA-N 0.000 description 1
- 238000013461 design Methods 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 239000008151 electrolyte solution Substances 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 238000003912 environmental pollution Methods 0.000 description 1
- 230000003628 erosive effect Effects 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 238000003682 fluorination reaction Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000012544 monitoring process Methods 0.000 description 1
- 239000012466 permeate Substances 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000012797 qualification Methods 0.000 description 1
- 239000011819 refractory material Substances 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000009466 transformation Effects 0.000 description 1
- 238000004056 waste incineration Methods 0.000 description 1
Classifications
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/02—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment
- F23G5/033—Incineration of waste; Incinerator constructions; Details, accessories or control therefor with pretreatment comminuting or crushing
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G5/00—Incineration of waste; Incinerator constructions; Details, accessories or control therefor
- F23G5/44—Details; Accessories
- F23G5/46—Recuperation of heat
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2201/00—Pretreatment
- F23G2201/80—Shredding
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2206/00—Waste heat recuperation
- F23G2206/10—Waste heat recuperation reintroducing the heat in the same process, e.g. for predrying
Landscapes
- Engineering & Computer Science (AREA)
- Mechanical Engineering (AREA)
- General Engineering & Computer Science (AREA)
- Electrolytic Production Of Metals (AREA)
Abstract
The embodiment of the invention discloses a kind of electrolytic aluminium solid waste manifold type burning processing systems, comprising: sequentially connected first waste material crushing system, the first feeding system, incinerator lower half and dreg removing system；And sequentially connected second waste material crushing system, the second feeding system, the incinerator upper half and cryolite recovery system；It further include coupling air preheater, the exhanst gas outlet and fuel gas inlet of the coupling air preheater are connected separately with smoke evacuation system and combustion-supporting wind system, the gas inlet of the coupling air preheater connects the outlet of the incinerator upper half and the incinerator lower half, and the gas outlet of the coupling air preheater connects the import of the incinerator upper half and incinerator lower half；Its processing method is comprising steps of S100, feed intake；S200, burning；S300, recycle heat utilize；S400, Product recycling；The present invention efficiently realizes the minimizing of solid waste, innoxious and recycling.
Description
Technical field
The present embodiments relate to Waste Disposal Technology fields, and in particular to a kind of electrolytic aluminium solid waste manifold type
Burning processing system and method.
Background technique
The solid waste that electrolytic aluminium generates mainly includes overhaul waste material and anode breeze.Due under the conditions of long term high temperature by
To the erosion of electrolyte solution, containing a large amount of soluble cyanide and fluoride in the overhaul waste material after stopping slot, belong to nuisance
Matter.Carbon content is more than 60% in overhaul waste material, remaining is ice crystal and heat preservation, refractory material, and a small amount of harmful cyanide
And fluoride, belong to a kind of danger wastes；Containing the ice crystal for having more than 60% in anode breeze, without cyanide and fluorination
Object belongs to general solid waste.Current electrolysis aluminium manufacturer generallys use landfill, stacked arrangement handles these solid waste, institute
The soluble cyanide and fluoride contained can be shifted by wind, solarization, the effect to drench with rain or be volatized into atmosphere, or with rain
Water permeates the ground, is mixed into rivers, contaminated soil and underground water, generates very big damage to animals and plants and human body, destroys ecological environment,
As carried out harmless treatment not in time, harm will be long-term.
Carry out the innocuously transformation processing or recycling comprehensive utilization of electrolytic cell overhaul slag as it can be seen that must rely on scientific and technological advances,
It just can guarantee that aluminum electrolysis industry meets the needs of national related environmental protection policy, realize the harmonious and sustainable development of Aluminium Industry,
Improve environment simultaneously, benefits the society.
Summary of the invention
For this purpose, the embodiment of the present invention provides a kind of electrolytic aluminium solid waste manifold type burning processing system and method, with
Solve in the prior art due in electrolytic aluminium solid waste incineration treatment process matter energy be unable to effective recycling, cause
The problems such as environmental pollution.
To achieve the goals above, the embodiment of the present invention provides the following technical solutions:
A kind of electrolytic aluminium solid waste manifold type burning processing system, comprising:
Sequentially connected first waste material crushing system, the first feeding system, incinerator lower half and dreg removing system；
And sequentially connected second waste material crushing system, the second feeding system, the incinerator upper half and cryolite recovery
System；
It further include coupling air preheater, the exhanst gas outlet and fuel gas inlet of the coupling air preheater connect respectively
Be connected to smoke evacuation system and combustion-supporting wind system, the gas inlet of the coupling air preheater connect the incinerator upper half and
The outlet of the incinerator lower half, the gas outlet of the coupling air preheater connect the incinerator upper half and burn
Burn the import of furnace lower half.
The embodiment of the present invention is further characterized in that, the incinerator separated place of the incinerator lower half and the incinerator upper half
It is provided with separation structure；The incinerator lower half combines to form manifold type burning furnace structure with the incinerator upper half, and burns
Thermal communication between furnace lower half and the incinerator upper half.
The embodiment of the present invention is further characterized in that the separation structure includes being set to the incinerator lower half and burning
Heat transfer plate between the furnace upper half, under being provided between the heat transfer plate and the incinerator separated place for realizing incinerator
The heat transfer path of half portion and incinerator upper half airflow, the heat transfer path include being located at the incinerator lower half and burning
The first heat transfer path between two feed inlets of the furnace upper half is burnt, and is located at the incinerator lower half and incinerator upper half
The second heat transfer path between two discharge ports in portion；Upper and lower two feed inlets are separately connected the second feeding system and first
Feeding system, upper and lower two discharge ports are separately connected the cryolite recovery system and dreg removing system.
The embodiment of the present invention is further characterized in that, is provided in first heat transfer path upper end and is mounted on incinerator upper half
The striker plate of portion's side wall, and the striker plate is located at the lower section of incinerator upper half feed inlet, is arranged on the striker plate
There are several ventilative sieve pores.
The embodiment of the present invention is further characterized in that the combustion-supporting wind system is for providing low temperature wind to the coupling air
The high-temperature flue gas of preheater, the incinerator upper half and incinerator lower half discharge is preheated by the coupling air
The low-temperature flue gas that device is formed after the cooling of low temperature wind is discharged from the smoke evacuation system, and the low temperature wind is in coupling air preheater
It is interior heated by high-temperature flue gas after be discharged into the incinerator upper half and the incinerator lower half.
The embodiment of the present invention is further characterized in that, the heat transfer plate along the incinerator upper half feed inlet towards incinerator upper half
The direction of portion's discharge port tilts down, and is provided with above the heat transfer plate for leading to the liquid ice crystal after melting
Drainage lumens component in the cryolite recovery system pipeline connector, the pipeline connection port connect the incinerator upper half
Discharge port；The drainage lumens component includes the open cell cavity being covered with above entire heat transfer plate, the open cell cavity
The fluid layer of connection is matched including the filtrate layers being distributed up and down respectively and with the heat transfer plate upper surface；In the filtrate layers
It is even that several liquid through-holes are distributed with, it is equipped at the edge of the liquid through-hole oblique towards the inclined edge of liquid through-hole center position
Face, the fluid layer are connected to the incinerator upper half by pipeline connection port close to incinerator upper half discharge port one end and discharge
Mouthful.
The embodiment of the present invention is further characterized in that, is provided with above the discharge port of the incinerator upper half and gas inlet
The gas outlet of connection is provided with the air inlet being connected to gas outlet below the discharge port of the incinerator lower half.
The embodiment of the present invention is further characterized in that, further includes controller, and the controller is electrically connected with air pressure inductor
And the electromagnetic valve for controlling gas outlet on-off, the air pressure inductor are set to the inside of the control incinerator upper half.
A kind of processing method of electrolytic aluminium solid waste manifold type burning processing system, includes the following steps:
S100, it feeds intake: after being crushed to overhaul waste material and anode breeze material, difference feeding to the upper half of incinerator
The lower half and；
S200, burning: combustion-supporting wind system is sent into the incinerator after low temperature wind is heated up by coupling air preheater
The upper half and lower half in；
S300, recycle heat utilize: after the high-temperature flue gas that incinerator generates is cooled down by the coupling air preheater
Discharge, the heat that the recycling incinerator burning of coupling air preheater generates is for heating the low temperature wind；
S400, Product recycling: anode breeze material passes through cryolite recovery by the liquid ice crystal that burning generates fusing
System is recycled.
The embodiment of the present invention is further characterized in that, further includes fume treatment recycling step, is preheated from the coupling air
The low-temperature flue gas of device discharge is carried out by the alumina powder in smoke evacuation system, and the fluorine of absorption is recycled as raw materials.
The embodiment of the present invention has the advantages that
(1) present invention realizes the minimizing of solid waste: using the charcoal of the high-content in overhaul waste material as fuel,
The charcoal completely burned of high-content generates flue gas, discharges heat anode breeze；The ice crystal of high-content is added in anode breeze
It is hot-melted recycling and reusing, least a portion of charcoal is heated burning and generates hot fume discharge in anode breeze；Two parts hot fume collection
In get up for the combustion air for heating incinerator；The final solid waste of whole system only has the slag discharge of 10%-20%, and solid is useless
Gurry is reduced 80%-90%；
(2) present invention realizes the innoxious of solid waste: the total cyanide of overhaul waste material is by high temperature in burning process
It is converted into innocuous substance, burns and is escaped in gaseous form with fluoride in heating process, electrolytic aluminium factory is back to by smoke evacuation system
Existing smoking gas containing fluorine processing system is absorbed fluorine as raw material reuse by alumina powder absorption method, is realized discarded
The harmless treatment of object；
(3) present invention realizes the recycling of solid waste: using the charcoal of the high-content in overhaul waste material as fuel,
The ice crystal of high-content in heating recovery anode breeze；Smoking gas containing fluorine returns to existing smoke processing system, is inhaled with alumina powder
As raw material reuse under attached；Ice crystal, fluorine element and carbon chemical heat in waste have obtained effective utilization.
Detailed description of the invention
It, below will be to embodiment party in order to illustrate more clearly of embodiments of the present invention or technical solution in the prior art
Formula or attached drawing needed to be used in the description of the prior art are briefly described.It should be evident that the accompanying drawings in the following description is only
It is merely exemplary, it for those of ordinary skill in the art, without creative efforts, can also basis
The attached drawing of offer, which is extended, obtains other implementation attached drawings.
Structure depicted in this specification, ratio, size etc., only to cooperate the revealed content of specification, for
Those skilled in the art understands and reads, and is not intended to limit the invention enforceable qualifications, therefore does not have technical
Essential meaning, the modification of any structure, the change of proportionate relationship or the adjustment of size are not influencing the function of the invention that can be generated
Under effect and the purpose that can reach, should all still it fall in the range of disclosed technology contents obtain and can cover.
Fig. 1 is overall structure diagram of the invention；
Fig. 2 is the overall structure diagram of incinerator of the invention；
Fig. 3 is the enlarged structure schematic diagram of A in Fig. 2 of the invention；
Fig. 4 is the enlarged structure schematic diagram of B in Fig. 2 of the invention；
Fig. 5 is the structural schematic diagram of C in Fig. 1 of the invention；
Fig. 6 is the flow chart of processing method of the present invention.
In figure:
1- smoke evacuation system；2- combustion-supporting wind system；3- coupling air preheater；The 4- incinerator upper half；5- ice crystal returns
Receipts system；6- the first waste material crushing system；The first feeding system of 7-；8- incinerator lower half；9- dreg removing system；10- second is useless
Expect crushing system；The second feeding system of 11-；12- incinerator separated place；13- separation structure；14- heat transfer plate；15- feed inlet；
The first heat transfer path of 16-；17- discharge port；The second heat transfer path of 18-；19- striker plate；The ventilative sieve pore of 20-；21- filtrate layers；22-
Fluid layer；23- liquid through-hole；24- bezel；25- pipeline connection port；26- air pressure inductor；27- electromagnetic valve；28- goes out
Port；29- air inlet；
301- exhanst gas outlet；302- fuel gas inlet；303- gas inlet；304- gas outlet.
Specific embodiment
Embodiments of the present invention are illustrated by particular specific embodiment below, those skilled in the art can be by this explanation
Content disclosed by book is understood other advantages and efficacy of the present invention easily, it is clear that described embodiment is the present invention one
Section Example, instead of all the embodiments.Based on the embodiments of the present invention, those of ordinary skill in the art are not doing
Every other embodiment obtained under the premise of creative work out, shall fall within the protection scope of the present invention.
During Aluminum Electrolysis Production, two kinds of solid waste (overhaul waste material and anode breeze) are mainly generated, due to it
To harmful substance, so generally all can carry out secondary treatment to it, still, usual manner is all to mix respectively to two kinds of substances
Conjunction or independent burning disposal, this just needs largely to burn material.
Embodiment 1:
As shown in Figure 1, main idea is that providing a kind of energy saving electrolytic aluminium solid waste manifold type
Burning processing system, main thought are will to be divided into upper and lower two according to the characteristic of two kinds of waste contained substances, and by incinerator
Part, upper part is for recycling the anode breeze more containing ice crystal, the overhaul more for burning disposal carbon content of lower part
Waste material can save a large amount of burning material in this way.Aim at the minimizing of solid waste, innoxious and recycling.
Although also containing part ice crystal in overhaul waste material, condition (1009 DEG C of fusing point) institute of opposite cryolite recovery
The energy for needing to consume is worth well below cost recovery, therefore, the necessity not recycled in comparison.
Specifically, as shown in Figure 1, the burning processing system includes that sequentially connected first for handling overhaul waste material is given up
Expect crushing system 6, the first feeding system 7, incinerator lower half 8 and dreg removing system 9.It is sent after being crushed overhaul waste material by pipeline
Enter incinerator lower half 8, and the waste residue that burning generates is discharged from dreg removing system 9.
Further include for handle the sequentially connected second waste material crushing system 10 of anode breeze, the second feeding system 11,
The incinerator upper half 4 and cryolite recovery system 5.Be sent into the incinerator upper half 4 after anode breeze being crushed by pipeline.It burns
Ice crystal solution after the furnace upper half 4 is burnt is recycled by cryolite recovery system 5.
If the high-temperature flue gas generated in the burning disposal mode by the incinerator upper half 4 and the burning of incinerator lower half 8
It is directly discharged to not only cause the waste of heat in atmosphere, and is easy to pollute air, smoking gas containing fluorine direct emission is dirty
Environment is contaminated, and the carbon contained in overhaul waste material and anode breeze is not effectively utilized, and causes energy loss.
Since to be not so good as common fuel effect certainly good for the combustion efficiency of overhaul waste material, in order to reach better combustion
Effect is burnt, as shown in Figures 1 to 5, present embodiment adds a coupling air preheater 3 and combustion air in incineration system
System 2, specific connection relationship in systems are as follows:
The exhanst gas outlet 301 and fuel gas inlet 302 of coupling air preheater 3 are connected separately with smoke evacuation system 1 and combustion-supporting
Wind system 2, combustion-supporting wind system 2 is for providing low temperature wind to coupling air preheater 3, under the incinerator upper half 4 and incinerator
By coupling air preheater 3, the low-temperature flue gas that is formed after the cooling of low temperature wind from smoke evacuation is the high-temperature flue gas that half portion 8 is discharged
1 discharge of system, low temperature wind are discharged into the incinerator upper half 4 and incinerator after being heated in coupling air preheater 3 by high-temperature flue gas
In lower half 8.
The gas inlet 303 of coupling air preheater 3 connects the outlet of the incinerator upper half 4 and incinerator lower half 8,
The gas outlet 304 of coupling air preheater 3 connects the import of the incinerator upper half 4 and incinerator lower half 8.Combustion air system
System 2 is respectively fed to the incinerator upper half 4 and incinerator lower half 8 after low temperature wind is heated up by coupling air preheater 3, burns
It burns after the high-temperature flue gas that the furnace upper half 4 and incinerator lower half 8 generate is cooled down by coupling air preheater 3 and is discharged, couple
Regenerative air heater 3 recycles the heat of the incinerator upper half 4 and the burning generation of incinerator lower half 8 for heating low temperature wind.This
The reasonable recycling to carbon in overhaul waste material and anode breeze can be achieved in kind operation, improves the utilization rate of energy.
The main function of combustion-supporting wind system 2 is to provide air quantity into incinerator to reach combustion-supporting effect, but in order to enable mention
The air quantity of confession does not generate excessive counter productive to the temperature of incinerator, it is therefore desirable to the higher air quantity of temperature or air-flow are provided,
If directly extraneous offer high temperature wind, higher cost, therefore 3 main function of present embodiment coupling air preheater have following
Several points:
The first, for reducing the temperature of incinerator (the incinerator upper half 4 and incinerator lower half 8) discharge high-temperature flue gas；
The second, combustion-supporting wind system 2 is allowed to provide low temperature wind, low temperature wind passes through in coupling air preheater 3 in height
The heat exchange of warm flue gas acts on, and obtains the high temperature wind into incinerator, meanwhile, the temperature of high-temperature flue gas is also reduced.
Coupling air preheater 3 has carried out circulation to the high temperature heat of incinerator well and has recycled, and greatlys save
The energy.
The total cyanide of overhaul waste material is innocuous substance by pyrolytic conversion in burning process, burns and is fluorinated in heating process
Object escapes in gaseous form, is back to the existing smoking gas containing fluorine processing system of electrolytic aluminium factory by smoke evacuation system, passes through alumina powder
Fluorine is absorbed the harmless treatment that waste is realized as raw material reuse by absorption method；And using in overhaul waste material
The charcoal of high-content is as fuel, the ice crystal of high-content in heating recovery anode breeze；Smoking gas containing fluorine returns to existing fume treatment
System uses alumina powder to absorb as raw material reuse；Ice crystal, fluorine element and carbon chemical heat in waste is equal
Effective utilization is obtained.In general, present system can use the charcoal of the high-content in overhaul waste material as fuel, height
The charcoal completely burned of content generates flue gas, discharges heat anode breeze；The ice crystal of high-content is heated in anode breeze
Recycling and reusing is melted, least a portion of charcoal is heated burning and generates hot fume discharge in anode breeze；Two parts hot fume is concentrated
Get up for the combustion air for heating incinerator；The final solid waste of whole system only has the slag discharge of 10%-20%, solid waste
Object is reduced 80%-90%.
Efficiency is recycled to energy in order to further increase the manifold type burning processing system.In another embodiment,
Incinerator lower half 8 combines to form manifold type burning furnace structure with the incinerator upper half 4, and incinerator lower half 8 and incinerator
Thermal communication between the upper half 4.Circulating current in incinerator lower half 8 and the inside formation heat of the incinerator upper half 4, one
The utilization rate of energy can be improved to the greatest extent in aspect, and on the other hand, the circulating current of formation helps to put into incinerator lower half 8
With the dehumidifying and lifting of overhaul waste material in the incinerator upper half 4 and anode breeze, the combustion rate of material is improved.It is specific:
The incinerator separated place 12 of incinerator lower half 8 and the incinerator upper half 4 is provided with separation structure 13.Separation structure
13 include the heat transfer plate 14 being set between incinerator lower half 8 and the incinerator upper half 4, is separated in heat transfer plate 14 and incinerator
It is provided between place 12 for realizing the heat transfer path of incinerator lower half 8 and 4 airflow of the incinerator upper half, heat transfer path
Including the first heat transfer path 16, Yi Jiwei between incinerator lower half 8 and two feed inlets 15 of the incinerator upper half 4
The second heat transfer path 18 between incinerator lower half 8 and two discharge ports 17 of the incinerator upper half 4.Upper and lower two chargings
Mouth 15 is separately connected the second feeding system 11 and the first feeding system 7, and upper and lower two discharge ports 17 are separately connected cryolite recovery
System 5 and dreg removing system 9.The top of 4 discharge port 17 of the incinerator upper half is provided with the gas outlet being connected to gas inlet 303
28, the lower section of 8 discharge port 17 of incinerator lower half is provided with the air inlet 29 being connected to gas outlet 304.Two feed inlets 15
The opposite of incinerator lower half 8 Yu the incinerator upper half 4 is located at two discharge ports 17.
Present embodiment improves the internal structure of incinerator, to adapt to this entire burning disposal process, in order to
Increase burning disposal effect as ultimate attainment as possible, using overcome using overhaul waste material as fuel compare normal fuel existing for lack
It falls into, this is also for the technical problem for not using generally this burning disposal mode of the present invention to need to capture in the prior art.
It is separated into incinerator lower half 8 and the incinerator upper half 4 by heat transfer plate 14, heat transfer plate 14, which directly contacts, to be needed back
The raw material anode breeze of ice collection spar, transmission of heat are good.
Conventional idea heat transfer plate necessarily separates incinerator lower half 8 and the incinerator upper half 4 completely, but in reality
It applies in mode, the channel for heat transfer, the first respectively above-mentioned heat transfer is offered between heat transfer plate 14 and incinerator wall surface
Combustion air is passed through incinerator lower half from the air inlet 29 of 18 lower section of the second heat transfer path by channel 16 and the second heat transfer path 18
8, combustion air will be flowed towards the side of the first heat transfer path 16 at this time, and form following airflow circulating:
Air inlet 29, the first heat transfer path 16, the incinerator upper half 4, the second heat transfer path 18, is burnt incinerator lower half 8
Burn furnace lower half 8.
The airflow circulating of present embodiment is that part recycles, and is discharged because there are also parts with high-temperature flue gas.
The circulating current of formation comes into full contact with fuel, reduces energy loss.
In addition to this, pass through the air-flow at the first heat transfer path 16, moreover it is possible to enter incinerator lower half 8 fuel and into
The reclaimed materials for entering the incinerator upper half 4 plays certain peptizaiton, and air-flow can be such that the material positioned at two feed inlets 15 flies
It raises and, material efficiency of combustion, the especially smashed anode breeze material in the incinerator upper half 4 are improved, to avoid fuel mistake
It is more the problem of being deposited at feed inlet 15, calory burning is caused to be unevenly distributed, equally it is avoided that anode breeze material is excessive
Be deposited at feed inlet 15, cause to be recycled insufficient problem.
Since entire incinerator is in the state of relative closure, heat has certain circulation inside entire incinerator, because
This, the main function of circulating current still acts on anode breeze material.
The material of 16 top of the first heat transfer path falls under gravity into lower section incinerator lower half 8 in order to prevent,
It is provided with the striker plate 19 for being mounted on 4 side wall of the incinerator upper half in 16 upper end of the first heat transfer path, and striker plate 19 is located at and burns
The lower section of 4 feed inlet of the furnace upper half is burnt, is provided with several ventilative sieve pores 20 on striker plate 19, the radius of ventilative sieve pore 20 is not enough to
A large amount of anode breeze material is fallen, even if there is small part to fall into lower section, is also influenced without what.
Ventilative 20 amount main function of sieve pore be so that hot wind in the first heat transfer path 16 from bottom to up through ventilative
It, will due to the effect of air-flow while the anodic carbon residue entered by 4 feed inlet 15 of the incinerator upper half is dried in sieve pore 20
Anodic carbon residue raises the contact area for increasing itself and air to the inside of the incinerator upper half 4, improves efficiency of combustion.
In the present embodiment, the first heat transfer path 16 and the second heat transfer path 18 do not need entirely to burn furnace sidewall
Width (assuming that incinerator be tetragonal), width only needs to connect convenient for airflow circulating, such as: width 3-10cm,
Specific width is depending on the size of incinerator.
Meanwhile in order to allow high temperature wind that there is multiple better reciprocation cycle in the incinerator upper half 4 and incinerator lower half 8
Effect, improves heat utilization ratio, which electromagnetic valve 27, control can also be arranged at gas outlet 28 again
Device is electrically connected with air pressure inductor 26 and the electromagnetic valve 27 for controlling 28 on-off of gas outlet, and air pressure inductor 26 is arranged
In the inside of the control incinerator upper half 4.Air pressure inductor 26 is for monitoring 4 air pressure inside of the incinerator upper half, and by signal
It is sent to controller, when air pressure is more than the preset air pressure threshold of controller, controller will instruct gas outlet 28 to open, and towards coupling
High-temperature flue gas is discharged into the gas inlet 303 of regenerative air heater 3.
Consider high-temperature factor, this results in needing to have the equipment such as electromagnetic valve 27 resistant to high temperature, air pressure inductor 26
It can be realized, therefore, the opening and closing using 27 discontinuity of electromagnetic valve control gas outlet 28 is selective scheme.
Consider high-temperature factor, present embodiment the gentle pressure inductor 26 of electromagnetic valve 27 can also be arranged lower in temperature
1 entrance of 3 exit of coupling air preheater or smoke evacuation system, corresponding controller can be set pre- in coupling air
On hot device 3 or smoke evacuation system 1, specific location does not do specific requirement.Controller can be conventional single-chip microcontroller, microprocessor
Deng.
In view of ice crystal needs to filter out the ice crystal molten slurry of high temperature during recycling, this process can
With the high temperature generated in the process using 8 overhaul waste combustion of incinerator lower half, therefore following improvement is made that heat transfer plate 14,
It is specific:
Heat transfer plate 14 dips down along the direction of feed inlet 15 towards 4 discharge port 17 of the incinerator upper half of the incinerator upper half 4
Tiltedly, be conducive to the water conservancy diversion of ice crystal molten slurry.And it is provided with above heat transfer plate 14 and is drawn for the liquid ice crystal after melting
Drainage lumens component into 5 pipeline connection port 25 of cryolite recovery system, pipeline connection port 25 connect going out for the incinerator upper half 4
Material mouth 17, drainage lumens component include the open cell cavity for being covered with entire 14 top of heat transfer plate, and open cell cavity includes difference
The filtrate layers 21 (top shell for being equivalent to drainage lumens component) that are distributed up and down and connection is matched with 14 upper surface of heat transfer plate
Fluid layer 22.
The upper surface of filtrate layers 21 tilts in the same direction with heat transfer plate 14, and tilt angle is slightly less than the inclination of heat transfer plate 14
Angle, so as to the slow flowing of ice crystal solution.Furthermore the upper surface of filtrate layers 21 can also be horizontally disposed with.Ice crystal molten slurry is first
First enter fluid layer 22 after the filtering of filtrate layers 21, and is flowed out from the surface of heat transfer plate 14.If being evenly distributed in filtrate layers 21
Dry liquids through-hole 23 is equipped at the edge of liquid through-hole 23 towards the inclined bezel 24 of 23 center position of liquid through-hole, liquid
The inner surface of through-hole 23 is similar to inverted terrace edge shape.On the one hand filtrate is convenient in such design, on the other hand reduce heat transfer plate
The loss of 14 surface energies.Fluid layer 22 is connected to close to 4 discharge port of the incinerator upper half, 17 one end by pipeline connection port 25
4 discharge port 17 of the incinerator upper half.Ice crystal molten slurry smoothly flows into discharge port 17 from pipeline connection port 25.
In this embodiment, it does not need to consider the slag charge blocking liquid through-hole 23 after anode carbon Slag treatment, liquid
Ice crystal can gradually penetrate into the fluid layer 22 in drainage lumens component from liquid through-hole 23.
In the present embodiment, fluid layer 22 can also directly use heat transfer plate 14 itself.
Preferably, heat transfer plate 14 is equipped with relatively described 14 surface of heat transfer plate close to 4 discharge port of the incinerator upper half, 17 one end
Minimum point (being not drawn into figure), and the nozzle of the pipeline connection port 25 is connected to the minimum point, so as to ice crystal solution
It smoothly converges to minimum point and is flowed out from pipeline connection port 25.
Embodiment 2:
As shown in fig. 6, the invention additionally provides a kind of processing of electrolytic aluminium solid waste manifold type burning processing system
Method includes the following steps:
S100, it feeds intake: after being crushed to overhaul waste material and anode breeze material, difference feeding to the upper half of incinerator
The lower half and；
S200, burning: combustion-supporting wind system is sent into the incinerator after low temperature wind is heated up by coupling air preheater
The upper half and lower half in；
S300, recycle heat utilize: after the high-temperature flue gas that incinerator generates is cooled down by the coupling air preheater
Discharge, the heat that the recycling incinerator burning of coupling air preheater generates is for heating the low temperature wind；
S400, Product recycling: anode breeze material passes through cryolite recovery by the liquid ice crystal that burning generates fusing
System is recycled.
The processing method of the manifold type burning processing system further includes fume treatment recycling step, empty from the manifold type
The low-temperature flue gas of air preheater discharge is carried out by the alumina powder in smoke evacuation system, using the fluorine of absorption as raw materials recovery benefit
With.
The processing method realizes three purposes, as follows respectively:
The minimizing of solid waste: using the charcoal of the high-content in overhaul waste material as fuel, the charcoal of high-content is complete
Burning generates flue gas, discharges heat anode breeze；It is sharp again to be heated fusing recycling for the ice crystal of high-content in anode breeze
With least a portion of charcoal is heated burning and generates hot fume discharge in anode breeze；Two parts hot fume is put together for heating
The combustion air of incinerator；The final solid waste of whole system only has the slag discharge of 10%-20%, solid waste reducing 80%-
90%；
Solid waste it is innoxious: in burning process the total cyanide of overhaul waste material by pyrolytic conversion be innocuous substance,
It burns and is escaped in gaseous form with fluoride in heating process, the existing smoking gas containing fluorine of electrolytic aluminium factory is back to by smoke evacuation system and is handled
Fluorine is absorbed the harmless treatment that waste is realized as raw material reuse by alumina powder absorption method by system；
The recycling of solid waste: using the charcoal of the high-content in overhaul waste material as fuel, heating recovery anode carbon
The ice crystal of high-content in slag；Smoking gas containing fluorine returns to existing smoke processing system, and alumina powder is used to absorb as raw material
Reuse；Ice crystal, fluorine element and carbon chemical heat in waste have obtained effective utilization.
Although above having used general explanation and specific embodiment, the present invention is described in detail, at this
On the basis of invention, it can be made some modifications or improvements, this will be apparent to those skilled in the art.Therefore,
These modifications or improvements without departing from theon the basis of the spirit of the present invention are fallen within the scope of the claimed invention.
Claims (10)
1. a kind of electrolytic aluminium solid waste manifold type burning processing system, comprising:
Sequentially connected first waste material crushing system (6), the first feeding system (7), incinerator lower half (8) and dreg removing system
(9)；
And sequentially connected second waste material crushing system (10), the second feeding system (11), the incinerator upper half (4) and ice crystal
Stone recovery system (5)；
It is characterized by also including coupling air preheater (3), the exhanst gas outlet of the coupling air preheater (3)
(301) and fuel gas inlet (302) is connected separately with smoke evacuation system (1) and combustion-supporting wind system (2), the coupling air preheater
(3) gas inlet (303) connects the outlet of the incinerator upper half (4) and the incinerator lower half (8), the coupling
The gas outlet (304) of regenerative air heater (3) connects the import of the incinerator upper half (4) and incinerator lower half (8).
2. a kind of electrolytic aluminium solid waste manifold type burning processing system according to claim 1, it is characterised in that: institute
The incinerator separated place (12) for stating incinerator lower half (8) and the incinerator upper half (4) is provided with separation structure (13)；It is described to burn
Burn furnace lower half (8) combined with the incinerator upper half (4) to be formed manifold type burning furnace structure, and incinerator lower half (8) with burn
Burn thermal communication between the furnace upper half (4).
3. a kind of electrolytic aluminium solid waste manifold type burning processing system according to claim 2, it is characterised in that: institute
Stating separation structure (13) includes the heat transfer plate (14) being set between the incinerator lower half (8) and the incinerator upper half (4),
It is provided between the heat transfer plate (14) and the incinerator separated place (12) for realizing incinerator lower half (8) and is burned
The heat transfer path of the furnace upper half (4) airflow, the heat transfer path include being located at the incinerator lower half (8) and incinerator
The first heat transfer path (16) between two feed inlets (15) of the upper half (4), and be located at the incinerator lower half (8) with
The second heat transfer path (18) between two discharge ports (17) of the incinerator upper half (4)；Upper and lower two feed inlets (15)
It is separately connected the second feeding system (11) and the first feeding system (7), upper and lower two discharge ports (17) are separately connected described
Cryolite recovery system (5) and dreg removing system (9).
4. a kind of electrolytic aluminium solid waste manifold type burning processing system according to claim 3, it is characterised in that:
First heat transfer path (16) upper end is provided with the striker plate (19) for being mounted on the incinerator upper half (4) side wall, and the gear
Flitch (19) is located at the lower section of the incinerator upper half (4) feed inlet, is provided with several ventilative sieves on the striker plate (19)
Hole (20).
5. a kind of electrolytic aluminium solid waste manifold type burning processing system according to claim 1, it is characterised in that: institute
Combustion-supporting wind system (2) are stated for providing low temperature wind to the coupling air preheater (3), the incinerator upper half (4) and
The high-temperature flue gas of incinerator lower half (8) discharge shape after the cooling of low temperature wind by the coupling air preheater (3)
At low-temperature flue gas be discharged from the smoke evacuation system (1), the low temperature wind is in the coupling air preheater (3) by high-temperature flue gas
It is discharged into after heating in the incinerator upper half (4) and the incinerator lower half (8).
6. a kind of electrolytic aluminium solid waste manifold type burning processing system according to claim 3, it is characterised in that: institute
State heat transfer plate (14) along the incinerator upper half (4) feed inlet (15) towards the direction of the incinerator upper half (4) discharge port (17) to
Lower inclination, and be provided with above the heat transfer plate (14) and returned for the liquid ice crystal after melting to be led to the ice crystal
Drainage lumens component in receipts system (5) pipeline connection port (25), the pipeline connection port (25) connect the incinerator upper half
(4) discharge port (17)；The drainage lumens component includes the open cell cavity being covered with above entire heat transfer plate (14), the bee
Nest open-ended cavity includes the upper and lower filtrate layers (21) being distributed of difference and matches leading for connection with the heat transfer plate (14) upper surface
Liquid layer (22)；Several liquid through-holes (23) are evenly distributed on the filtrate layers (21), at the edge of the liquid through-hole (23)
Equipped with towards the inclined bezel of liquid through-hole (23) center position (24), the fluid layer (22) is close to the incinerator upper half
(4) discharge port (17) one end is connected to the incinerator upper half (4) discharge port (17) by pipeline connection port (25).
7. a kind of electrolytic aluminium solid waste manifold type burning processing system according to claim 6, it is characterised in that: institute
The gas outlet (28) for being provided with above the incinerator upper half (4) discharge port (17) and being connected to gas inlet (303) is stated, it is described to burn
It burns and is provided with the air inlet (29) being connected to gas outlet (304) below furnace lower half (8) discharge port (17).
8. a kind of electrolytic aluminium solid waste manifold type burning processing system according to claim 7, it is characterised in that: also
Including controller, the controller is electrically connected with air pressure inductor (26) and the electromagnetism for controlling gas outlet (28) on-off
Valve (27), the air pressure inductor (26) are set to the inside of the control incinerator upper half (4).
9. a kind of processing method of electrolytic aluminium solid waste manifold type burning processing system, it is characterised in that: including walking as follows
It is rapid:
S100, feed intake: after being crushed to overhaul waste material and anode breeze material, the upper half of feeding to incinerator is under respectively
Half portion；
S200, burning: combustion-supporting wind system is sent into the upper of the incinerator after low temperature wind is heated up by coupling air preheater
In half portion and lower half；
S300, recycle heat utilize: the high-temperature flue gas that incinerator generates is discharged after being cooled down by the coupling air preheater,
The heat that the recycling incinerator burning of coupling air preheater generates is for heating the low temperature wind；
S400, Product recycling: anode breeze material passes through cryolite recovery system by the liquid ice crystal that burning generates fusing
It is recycled.
10. a kind of processing method of electrolytic aluminium solid waste manifold type burning processing system according to claim 9,
It is characterized in that: further including fume treatment recycling step, the low-temperature flue gas being discharged from the coupling air preheater passes through smoke evacuation
Alumina powder in system carries out, and the fluorine of absorption is recycled as raw materials.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910496413.6A CN110173696B (en) | 2019-06-10 | 2019-06-10 | Electrolytic aluminum solid waste coupling type incineration treatment system and method |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201910496413.6A CN110173696B (en) | 2019-06-10 | 2019-06-10 | Electrolytic aluminum solid waste coupling type incineration treatment system and method |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN110173696A true CN110173696A (en) | 2019-08-27 |
| CN110173696B CN110173696B (en) | 2024-07-26 |
Family
ID=67697141
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201910496413.6A Active CN110173696B (en) | 2019-06-10 | 2019-06-10 | Electrolytic aluminum solid waste coupling type incineration treatment system and method |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN110173696B (en) |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1183308A (en) * | 1968-02-01 | 1970-03-04 | Elektrokemisk As | Method of Recovering Fluorine from Carbonaceous Waste Material |
| US4735784A (en) * | 1986-07-11 | 1988-04-05 | Morrison-Knudsen Company, Inc. | Method of treating fluoride contaminated wastes |
| RU2477820C1 (en) * | 2011-10-31 | 2013-03-20 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Санкт-Петербургский государственный горный университет" | Treatment method of waste lining from electrolytic molten aluminium |
| CN103302079A (en) * | 2013-06-20 | 2013-09-18 | 郑州经纬科技实业有限公司 | Comprehensive treatment and utilization method of aluminum smelting fluorine-carbon hazardous solid wastes |
| DE102013022099A1 (en) * | 2013-12-21 | 2015-06-25 | ingitec Engineering GmbH | Recycling Spent Pot Lining |
| CN107420932A (en) * | 2017-08-03 | 2017-12-01 | 中国环境科学研究院 | Utilize the method for power plant for self-supply's cooperative disposal electrolytic aluminium solid waste |
| CN107626712A (en) * | 2017-08-29 | 2018-01-26 | 陕西三秦能源长宏铝业有限公司 | A kind of aluminium electroloysis danger solid waste integrated conduct method and recycling |
| CN210069862U (en) * | 2019-06-10 | 2020-02-14 | 龙科天成(厦门)科技有限公司 | Electrolytic aluminum solid waste coupling type incineration treatment system |
-
2019
- 2019-06-10 CN CN201910496413.6A patent/CN110173696B/en active Active
Patent Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| GB1183308A (en) * | 1968-02-01 | 1970-03-04 | Elektrokemisk As | Method of Recovering Fluorine from Carbonaceous Waste Material |
| US4735784A (en) * | 1986-07-11 | 1988-04-05 | Morrison-Knudsen Company, Inc. | Method of treating fluoride contaminated wastes |
| RU2477820C1 (en) * | 2011-10-31 | 2013-03-20 | Федеральное государственное бюджетное образовательное учреждение высшего профессионального образования "Санкт-Петербургский государственный горный университет" | Treatment method of waste lining from electrolytic molten aluminium |
| CN103302079A (en) * | 2013-06-20 | 2013-09-18 | 郑州经纬科技实业有限公司 | Comprehensive treatment and utilization method of aluminum smelting fluorine-carbon hazardous solid wastes |
| DE102013022099A1 (en) * | 2013-12-21 | 2015-06-25 | ingitec Engineering GmbH | Recycling Spent Pot Lining |
| CN107420932A (en) * | 2017-08-03 | 2017-12-01 | 中国环境科学研究院 | Utilize the method for power plant for self-supply's cooperative disposal electrolytic aluminium solid waste |
| CN107626712A (en) * | 2017-08-29 | 2018-01-26 | 陕西三秦能源长宏铝业有限公司 | A kind of aluminium electroloysis danger solid waste integrated conduct method and recycling |
| CN210069862U (en) * | 2019-06-10 | 2020-02-14 | 龙科天成(厦门)科技有限公司 | Electrolytic aluminum solid waste coupling type incineration treatment system |
Also Published As
| Publication number | Publication date |
|---|---|
| CN110173696B (en) | 2024-07-26 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103831285B (en) | Aluminium electroloysis is given up breeze innocuity disposal system and method thereof | |
| WO2012065327A1 (en) | Continuous lead smelting device and continuous lead smelting method | |
| CN103302079B (en) | Comprehensive treatment and utilization method of aluminum smelting fluorine-carbon hazardous solid wastes | |
| CN109609149A (en) | Waste lithium cell recovery and processing system and processing method | |
| CN108677018B (en) | A kind of environmental protection molten lead system | |
| CN109775785A (en) | A kind of high-salt wastewater burns desalting system and its processing method | |
| CN216047700U (en) | Plasma melting furnace | |
| CN110173696A (en) | A kind of electrolytic aluminium solid waste manifold type burning processing system and method | |
| CN210069862U (en) | Electrolytic aluminum solid waste coupling type incineration treatment system | |
| CN207049929U (en) | A kind of novel waste heat utilizes type incinerator | |
| CN214249609U (en) | Vortex combustion melting furnace | |
| CN213872704U (en) | Residual anode combustion flue gas diversion type electrolyte remelting furnace | |
| CN210292872U (en) | Kiln waste heat recovery utilizes system | |
| CN212806587U (en) | Alumina calcination waste heat recovery utilizes device | |
| CN109775786A (en) | A kind of high-salt wastewater burns desalting system and its processing method | |
| CN211079359U (en) | Industrial waste salt electrolysis sodium preparation device based on organic solid waste is fuel molten bath bed | |
| CN208562232U (en) | Solid waste medium temperature pyrocrack furnace | |
| CN217504387U (en) | Energy-saving oil smoke utilization system for side well feeding aluminum melting furnace | |
| CN206508669U (en) | Aluminium hydroxide and complementary energy recovery device in a kind of Aluminium hydroxide roasting flue gas | |
| CN206459194U (en) | A kind of refuse treatment plant preheated using self-loopa pyrolysis gas to air | |
| CN205919311U (en) | Secondary whirlwind supplemental oxygen system of living beings granule burning aircraft nose | |
| CN214332710U (en) | Plasma torch flue gas diversion type electrolyte remelting furnace | |
| CN211111855U (en) | Carbonization furnace with flue gas recovery device | |
| CN218179605U (en) | Radiation heating smelting furnace for producing regenerated zinc | |
| CN217640681U (en) | Radioactive waste treatment system |
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 | ||
| CB02 | Change of applicant information | ||
| CB02 | Change of applicant information |
Address after: No. 68, Shangcuo Pancuoli, Wuxian Town, Tong'an District, Xiamen City, Fujian Province, 361000 Applicant after: Longke Tiancheng (Xiamen) Technology Co.,Ltd. Address before: 361000 room 110, building a, talent entrepreneurship Park, No. 2002, Tongji Road, Tong'an District, Xiamen City, Fujian Province Applicant before: Longke Tiancheng (Xiamen) Technology Co.,Ltd. |
|
| GR01 | Patent grant | ||
| GR01 | Patent grant |