CN205997147U - A kind of device of medical refuse burning flyash microwave continuous sintering ceramsite - Google Patents
A kind of device of medical refuse burning flyash microwave continuous sintering ceramsite Download PDFInfo
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- CN205997147U CN205997147U CN201620853312.1U CN201620853312U CN205997147U CN 205997147 U CN205997147 U CN 205997147U CN 201620853312 U CN201620853312 U CN 201620853312U CN 205997147 U CN205997147 U CN 205997147U
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- 238000005245 sintering Methods 0.000 title claims abstract description 87
- 239000010881 fly ash Substances 0.000 title claims abstract description 29
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 30
- 230000005540 biological transmission Effects 0.000 claims abstract description 22
- 238000001816 cooling Methods 0.000 claims abstract description 21
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 21
- 239000007789 gas Substances 0.000 claims abstract description 20
- 238000010438 heat treatment Methods 0.000 claims abstract description 19
- 239000000203 mixture Substances 0.000 claims abstract description 16
- 238000002347 injection Methods 0.000 claims abstract description 12
- 239000007924 injection Substances 0.000 claims abstract description 12
- 230000007246 mechanism Effects 0.000 claims abstract description 9
- 230000001939 inductive effect Effects 0.000 claims 1
- 238000000034 method Methods 0.000 abstract description 16
- 239000000428 dust Substances 0.000 abstract description 11
- 239000000463 material Substances 0.000 abstract description 10
- 230000008569 process Effects 0.000 abstract description 10
- 239000002956 ash Substances 0.000 abstract description 9
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 abstract description 8
- 239000003546 flue gas Substances 0.000 abstract description 8
- 238000000746 purification Methods 0.000 abstract description 6
- 238000010304 firing Methods 0.000 abstract description 4
- 238000006243 chemical reaction Methods 0.000 abstract description 3
- 238000005485 electric heating Methods 0.000 abstract description 3
- 238000009768 microwave sintering Methods 0.000 abstract description 3
- 239000002671 adjuvant Substances 0.000 description 15
- 239000008187 granular material Substances 0.000 description 15
- 239000003818 cinder Substances 0.000 description 7
- 229910052683 pyrite Inorganic materials 0.000 description 7
- 239000011028 pyrite Substances 0.000 description 7
- SZVJSHCCFOBDDC-UHFFFAOYSA-N iron(II,III) oxide Inorganic materials O=[Fe]O[Fe]O[Fe]=O SZVJSHCCFOBDDC-UHFFFAOYSA-N 0.000 description 6
- NIFIFKQPDTWWGU-UHFFFAOYSA-N pyrite Chemical group [Fe+2].[S-][S-] NIFIFKQPDTWWGU-UHFFFAOYSA-N 0.000 description 5
- 239000002699 waste material Substances 0.000 description 5
- 239000007822 coupling agent Substances 0.000 description 4
- 238000010521 absorption reaction Methods 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000007710 freezing Methods 0.000 description 3
- 230000008014 freezing Effects 0.000 description 3
- 239000000126 substance Substances 0.000 description 3
- MBMLMWLHJBBADN-UHFFFAOYSA-N Ferrous sulfide Chemical group [Fe]=S MBMLMWLHJBBADN-UHFFFAOYSA-N 0.000 description 2
- NINIDFKCEFEMDL-UHFFFAOYSA-N Sulfur Chemical compound [S] NINIDFKCEFEMDL-UHFFFAOYSA-N 0.000 description 2
- QAOWNCQODCNURD-UHFFFAOYSA-N Sulfuric acid Chemical compound OS(O)(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-N 0.000 description 2
- 230000015572 biosynthetic process Effects 0.000 description 2
- 229910052793 cadmium Inorganic materials 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 235000019504 cigarettes Nutrition 0.000 description 2
- 230000008878 coupling Effects 0.000 description 2
- 238000010168 coupling process Methods 0.000 description 2
- 238000005859 coupling reaction Methods 0.000 description 2
- 229910001385 heavy metal Inorganic materials 0.000 description 2
- 229910052745 lead Inorganic materials 0.000 description 2
- 239000002906 medical waste Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 239000011819 refractory material Substances 0.000 description 2
- 150000004760 silicates Chemical class 0.000 description 2
- 239000000779 smoke Substances 0.000 description 2
- 239000000243 solution Substances 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 238000003756 stirring Methods 0.000 description 2
- 229910052717 sulfur Inorganic materials 0.000 description 2
- 239000011593 sulfur Substances 0.000 description 2
- 238000003786 synthesis reaction Methods 0.000 description 2
- KVGZZAHHUNAVKZ-UHFFFAOYSA-N 1,4-Dioxin Chemical compound O1C=COC=C1 KVGZZAHHUNAVKZ-UHFFFAOYSA-N 0.000 description 1
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 1
- QAOWNCQODCNURD-UHFFFAOYSA-L Sulfate Chemical compound [O-]S([O-])(=O)=O QAOWNCQODCNURD-UHFFFAOYSA-L 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000004140 cleaning Methods 0.000 description 1
- 150000002013 dioxins Chemical class 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000004744 fabric Substances 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- JEIPFZHSYJVQDO-UHFFFAOYSA-N iron(III) oxide Inorganic materials O=[Fe]O[Fe]=O JEIPFZHSYJVQDO-UHFFFAOYSA-N 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 229910052751 metal Inorganic materials 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000000630 rising effect Effects 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical class O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 1
- 239000002893 slag Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
- Y02P10/00—Technologies related to metal processing
- Y02P10/25—Process efficiency
Landscapes
- Processing Of Solid Wastes (AREA)
- Constitution Of High-Frequency Heating (AREA)
Abstract
The utility model discloses a kind of device of medical refuse burning flyash microwave continuous sintering ceramsite, the system is by granulating and forming unit (hopper, agitating device and forming machine), material conveying mechanism (drive sprocket, driven sprocket, transmission chain, fixing axle and SiC boat), microwave heating system (magnetron) and flue gas purification system (collection and confinement of gases mouth, water cooling plant, extracting tower, activated carbon injection apparatus, sack cleaner, air-introduced machine) etc. composition, it is fast that this device has firing rate, power consumption is few, the feature of electric heating high conversion rate, promote the industrialization process of flying ash microwave sintering, it is particularly suitable for the flying dust harmless treatment for the purpose of flying ash sintering ceramsite.
Description
Technical field
The present invention relates to the method that medical refuse burning flyash is processed, especially a kind of medical refuse burning flyash microwave is even
The device of continuous sintering ceramsite.
Background technology
Microwave heating is because its firing rate is fast, selectivity is strong, homogeneous heating the advantages of, obtained in recent years widely
Application." hot spot-effect " is the key property of microwave heating, and quick heats produced by this effect are conduction and convection current
Mode is not reached.Based on carbon component in medical refuse burning flyash (activated carbon and unburned carbon residue) in microwave field easy shape
Become " hot spot-effect ", and then by the way of microwave treatment, flying dust is processed, such as Chinese patent CN103601526B is public
The method having opened medical flying ash microwave baking ceramsite, the method can realize effectively decomposing and burning of dioxin by microwave
Make haydite, but need in actual applications to refill SiC, activated carbon or Fe around granule3O4To strengthen Deng microwave coupling agent
Its absorbing property, after leading to sintering, haydite is complex with the separation circuit of these microwave coupling agent, has in terms of commercial Application
Wait to improve, and the interpolation of these pure microwave coupling agent can bring the rising of operating cost, how by simple Laboratory Principle
Apply in commercial Application, be a problem demanding prompt solution.
Content of the invention
Instant invention overcomes shortcoming of the prior art, there is provided a kind of medical refuse burning flyash microwave continuous sintering pottery
The device of grain.
In order to solve above-mentioned technical problem, the present invention is achieved by the following technical solutions：
A kind of device of medical refuse burning flyash microwave continuous sintering ceramsite, including the first hopper, the second hopper, stirring
Device, forming machine, sinter body of heater, water cooling plant, extracting tower, activated carbon injection apparatus, sack cleaner, air-introduced machine；Wherein：
First hopper and the second hopper connect agitating device respectively, add medical waste by two hoppers to agitating device
Flying ash and adjuvant, and utilize agitating device mix homogeneously；
The medical refuse burning flyash of mix homogeneously and adjuvant are pressed into by agitating device connecting machine using forming machine
Granule；
Forming machine passes through feed arrangement and sintering furnace body phase even, controlled using feed arrangement add in sintering body of heater
Grain number amount and speed；
Arrange by drive sprocket, driven sprocket, transmission chain, fixing axle and SiC container in the middle position of sintering body of heater
The transporter of composition, the two ends of transmission chain are connected with drive sprocket and driven sprocket respectively, and in drive sprocket and driven
Form the two transmission planes up and down with horizontal direction parallel between sprocket wheel；Transmission chain arranges fixing axle, in fixing axle
Upper setting SiC container；Sintering body of heater arranges microwave heating equipment, carries out microwave heating in sintering body of heater body；In transmission
The vertical lower setting haydite collection bucket of device side, haydite collection bucket lower end arranges drawing mechanism, in order to collect positioned at burning
Haydite in SiC container in freezing of a furnace body；Upper end setting collection and confinement of gases mouth in sintering body of heater；
Collection and confinement of gases mouth is connected with the top of water cooling plant by pipeline, and pipeline and extracting tower are passed through in the bottom of water cooling plant
Top be connected；The bottom of extracting tower is connected with sack cleaner by pipeline, and arranges activated carbon injection apparatus on pipeline,
Sack cleaner is connected with air-introduced machine.
And, described adjuvant is pyrite cinder, SiC or Fe3O4One of, medical refuse burning flyash and adjuvant
Mass ratio be (2-10)：1.
And, described sintering furnace interior is made using the refractory material not absorbing microwave or a small amount of absorption microwave,
Shell is made up of stainless steel material, to prevent microwave to outward leakage.
And, described microwave heating equipment is magnetron, when being configured, long along body of heater in sintering body of heater upper end face
Degree direction is uniformly arranged upper end magnetron, and is arranged alternately upper end both sides magnetic control in sintering body of heater two sides along body of heater length direction
Pipe, is located at the upper SiC container being driven in plane in the height of upper end both sides magnetron arranging on opposite sides and sintering furnace body
Centre-height consistent；Or on the surface of sintering body of heater upper and lower side, it is uniformly arranged upper end magnetron along body of heater length direction
With lower end magnetron, and sintering body of heater two sides be arranged alternately upper end both sides magnetron and lower end both sides along body of heater length direction
Magnetron, the height of lower end magnetron arranging on opposite sides interior SiC container being located in underdrive plane with sintering furnace body
Centre-height consistent.
And, the described magnetron quantity being arranged on sintering body of heater upper end is 8-15, is arranged on sintering body of heater both sides
The quantity of the every side of magnetron be 8-15.
And, the number of described SiC container is 20-40.
A kind of operation method of medical refuse burning flyash microwave continuous sintering ceramsite：
Using the operation method of said apparatus sintering ceramsite, carry out as steps described below：
Step 1, starts microwave heating equipment to carrying out being heated to design temperature in sintering furnace body, starts driving chain and drive
SiC container is moved；
Step 2, adds medical refuse burning flyash and adjuvant by two hoppers to agitating device, and utilizes agitating device
Mix homogeneously；
Step 3, agitating device connecting machine, using forming machine by the medical refuse burning flyash of mix homogeneously and adjuvant
It is pressed into granule；
Step 4, forming machine passes through feed arrangement with sintering furnace body phase even, is controlled using feed arrangement and adds in sintering body of heater
The amounts of particles entering and speed
Step 5, granule enters in sintering furnace body, falls in SiC container and travels forward along driving chain, to chain end
End, SiC container goes to underdrive plane, and the granule after sintering falls in haydite collection bucket, and is collected by collection device；
Step 6, the gas producing in sintering process, from collection and confinement of gases mouth, water cooling plant, cooled place are entered by pipeline
After reason, extracting tower is entered by pipeline by the bottom of water cooling plant, carries out deacidification, after completing deacidification, gas is entered by pipeline
Sack cleaner carries out dedusting, and pipeline is provided with activated carbon injection apparatus, and sack cleaner is connected with air-introduced machine.
And, in step 1, described adjuvant is pyrite cinder, SiC or Fe3O4One of, medical refuse burning
The mass ratio of flying dust and adjuvant is (2-10)：1.
And, the chilling temperature of described water cooling plant is 10-20 degree Celsius.
Compared with prior art, the invention has the beneficial effects as follows：The system of the present invention (hopper, is stirred by granulating and forming unit
Mix device and forming machine), material conveying mechanism (drive sprocket, driven sprocket, transmission chain, fixing axle and SiC boat), microwave add
(collection and confinement of gases mouth, water cooling plant, extracting tower, activated carbon injection apparatus, cloth bag remove for hot systems (magnetron) and flue gas purification system
Dirt device, air-introduced machine) etc. composition, in granulating and forming unit, using enrichment microwave coupling agent-Fe3O4Pyrite cinder as auxiliary
Material, and combine microwave absorbing property in microwave field for the Self substances in flying dust it is ensured that microwave absorbing property within granule, sulfur ferrum simultaneously
In ore deposit slag, silicates and oxides improve one-tenth Tao Chengfen in flying dust, realize the treatment of wastes with processes of wastes against one another；In material conveying mechanism, SiC
Boat carries fly ash granule as container, external heat being brought rapidly up under microwave field so that in fly ash granule, improves flying dust sintering
Efficiency, reduces the energy expenditure of sintering process, in addition, SiC boat is arranged in transmission chain one by one, is conducive to improving treating capacity,
During the chain of approach bottom, the unloaded ripple of inhaling of SiC boat preheats so that microwave energy is effectively used.In microwave heating system, it is not required to
It is passed through large quantity of air, generation exhaust gas volumn is few, very small amount volatile heavy metal such as Cd, Pb, can be by cigarettes below with smoke evaporative
Gas cleaning system catches collects, tail gas clean-up facility that need not be complicated；In flue gas purification system, effectively anti-using water cooling plant
Stopped sintering flue gas in two dislike because secondary synthesis.The present invention has that firing rate is fast, power consumption is few, electric heating high conversion rate
Feature, promotes the industrialization process of flying ash microwave sintering, is particularly suitable for the flying dust for the purpose of flying ash sintering ceramsite
Harmless treatment.
Brief description
Fig. 1 is a kind of structural representation of the system of present invention medical refuse burning flyash microwave continuous sintering ceramsite；
Fig. 2 is the side structure schematic diagram 1 of sintering body of heater.
Fig. 3 is the side structure schematic diagram 2 of sintering body of heater.
Fig. 4 is the overlooking the structure diagram of sintering body of heater.
Wherein, 1-1 is the first hopper, and 1-2 is the second hopper, and 2 is agitating device, and 3 is forming machine, and 4 is driven sprocket, 5
For feed arrangement, 6 is magnetron, and 6-1 is upper end magnetron, and 6-2 is the magnetron of upper end two sides, and 6-3 is lower end two sides
Magnetron, 6-4 be lower end magnetron, 7 be SiC container, 8 be transmission chain, 9 be fixing axle, 10 be drive sprocket, 11 be burn
Freezing of a furnace body, 12 is haydite collection bucket, and 13 is drawing mechanism, and 14 is collection and confinement of gases mouth, and 15 is water cooling plant, and 16 is extracting tower, 17
For activated carbon injection apparatus, 18 is sack cleaner, and 19 is air-introduced machine.
Specific embodiment
With specific embodiment, the present invention is described in further detail below in conjunction with the accompanying drawings：
A kind of device of medical refuse burning flyash microwave continuous sintering ceramsite, including the first hopper, the second hopper, stirring
Device, forming machine, sinter body of heater, water cooling plant, extracting tower, activated carbon injection apparatus, sack cleaner, air-introduced machine；Wherein：
First hopper and the second hopper connect agitating device respectively, add medical waste by two hoppers to agitating device
Flying ash and adjuvant, and utilize agitating device mix homogeneously；
The medical refuse burning flyash of mix homogeneously and adjuvant are pressed into by agitating device connecting machine using forming machine
Granule；
Forming machine passes through feed arrangement and sintering furnace body phase even, controlled using feed arrangement add in sintering body of heater
Grain number amount and speed；
Arrange by drive sprocket, driven sprocket, transmission chain, fixing axle and SiC container in the middle position of sintering body of heater
The transporter of composition, the two ends of transmission chain are connected with drive sprocket and driven sprocket respectively, and in drive sprocket and driven
Form the two transmission planes up and down with horizontal direction parallel between sprocket wheel；Transmission chain arranges fixing axle, in fixing axle
Upper setting SiC container；Sintering body of heater arranges microwave heating equipment, carries out microwave heating in sintering body of heater body；In transmission
The vertical lower setting haydite collection bucket of device side, haydite collection bucket lower end arranges drawing mechanism, in order to collect positioned at burning
Haydite in SiC container in freezing of a furnace body；Upper end setting collection and confinement of gases mouth in sintering body of heater；
Collection and confinement of gases mouth is connected with the top of water cooling plant by pipeline, and pipeline and extracting tower are passed through in the bottom of water cooling plant
Top be connected；The bottom of extracting tower is connected with sack cleaner by pipeline, and arranges activated carbon injection apparatus on pipeline,
Sack cleaner is connected with air-introduced machine.
And, described sintering furnace interior is made using the refractory material not absorbing microwave or a small amount of absorption microwave,
Shell is made up of stainless steel material, to prevent microwave to outward leakage.
And, described microwave heating equipment is magnetron, when being configured, long along body of heater in sintering body of heater upper end face
Degree direction is uniformly arranged upper end magnetron, and is arranged alternately upper end both sides magnetic control in sintering body of heater two sides along body of heater length direction
Pipe, is located at the upper SiC container being driven in plane in the height of upper end both sides magnetron arranging on opposite sides and sintering furnace body
Centre-height consistent (as shown in Figure 2 and Figure 4)；Or it is on the surface of sintering body of heater upper and lower side, equal along body of heater length direction
Even setting upper end magnetron and lower end magnetron, and it is arranged alternately upper end both sides in sintering body of heater two sides along body of heater length direction
Magnetron and lower end both sides magnetron, are located at underdrive in the height of lower end magnetron arranging on opposite sides and sintering furnace body
The centre-height of the SiC container in plane is consistent (as shown in Figure 3 and Figure 4).
And, the described magnetron quantity being arranged on sintering body of heater upper end is 8-15, is arranged on sintering body of heater both sides
The quantity of the every side of magnetron be 8-15,
And, the number of described SiC container is 20-40.
The main chemical compositions of certain medical refuse burning flyash, clinker ignition loss and dioxins concentration (%) see table
In the present embodiment, adjuvant selects pyrite cinder, and described pyrite cinder is using troilite or sulfur-bearing tailings
Do a kind of waste residue discharged in raw material production sulfuric acid process, its main component is Fe3O4、Fe2O3, the sulfate of metal, silicic acid
Salt and oxide etc., the practical troilite of the present embodiment is purchased from Shandong Xin Haikuangzhuan limited company.
Using the operation method of said apparatus sintering ceramsite, carry out as steps described below：
Step 1, starts microwave heating equipment to carrying out being heated to design temperature in sintering furnace body, starts driving chain and drive
SiC container is moved；
Step 2, adds medical refuse burning flyash and adjuvant by two hoppers to agitating device, and utilizes agitating device
The mass ratio of mix homogeneously, medical refuse burning flyash and adjuvant is 10：1；
Step 3, agitating device connecting machine, using forming machine by the medical refuse burning flyash of mix homogeneously and adjuvant
It is pressed into granule；
Step 4, forming machine passes through feed arrangement with sintering furnace body phase even, is controlled using feed arrangement and adds in sintering body of heater
The amounts of particles entering and speed
Step 5, granule enters in sintering furnace body, falls in SiC container and travels forward along driving chain, to chain end
End, SiC container goes to underdrive plane, and the granule after sintering falls in haydite collection bucket, and is collected by collection device；
Step 6, the gas producing in sintering process, from collection and confinement of gases mouth, water cooling plant, cooled place are entered by pipeline
After reason, extracting tower is entered by pipeline by the bottom of water cooling plant, carries out deacidification, after completing deacidification, gas is entered by pipeline
Sack cleaner carries out dedusting, and pipeline is provided with activated carbon injection apparatus, and sack cleaner is connected with air-introduced machine.
And, the chilling temperature of described water cooling plant is 10-20 degree Celsius.
, as strong microwave coupling agent, using SiC as the container carrying material, under microwave field, SiC container can for SiC
To produce rapidly heat in its inwall, the energy of microwave is converted into carry the heat of the absorption of material.
The system of the present invention is by granulating and forming unit (hopper, agitating device and forming machine), material conveying mechanism (drive chain
Wheel, driven sprocket, transmission chain, fixing axle and SiC boat), (gas is received for microwave heating system (magnetron) and flue gas purification system
Ji Kou, water cooling plant, extracting tower, activated carbon injection apparatus, sack cleaner, air-introduced machine) etc. composition, in granulating and forming unit
In, using enrichment microwave coupling agent-Fe3O4Pyrite cinder as adjuvant, and combine flying dust in Self substances in microwave field
Microwave absorbing property it is ensured that microwave absorbing property within granule, in pyrite cinder, silicates and oxides improve flying dust simultaneously
Middle one-tenth Tao Chengfen, realizes the treatment of wastes with processes of wastes against one another；In material conveying mechanism, SiC boat carries fly ash granule as container, in microwave field
Lower so that external heat being brought rapidly up in fly ash granule, improve flying dust sintering efficiency, reduce the energy expenditure of sintering process, separately
Outward, SiC boat (i.e. SiC container) is arranged in transmission chain one by one, is conducive to improving treating capacity, the SiC boat in approach bottom chain
Unloaded ripple of inhaling preheats so that microwave energy is effectively used.In microwave heating system, it is not required to be passed through large quantity of air, produce cigarette
Tolerance is few, and very small amount volatile heavy metal such as Cd, Pb, with smoke evaporative, can be caught by flue gas purification system below and collect,
Tail gas clean-up facility that need not be complicated；In flue gas purification system, two evils in sintering flue gas be effectively prevent using water cooling plant
The secondary synthesis of English.The present invention has the characteristics that firing rate is fast, power consumption is few, electric heating high conversion rate, promotes flying ash
The industrialization process of microwave sintering, is particularly suitable for the flying dust harmless treatment for the purpose of flying ash sintering ceramsite.
Above the present invention is described in detail, but described content has been only presently preferred embodiments of the present invention it is impossible to be recognized
It is the practical range for limiting the present invention.All impartial changes made according to the present patent application scope and improvement etc., all should still return
Belong within the patent covering scope of the present invention.
Claims (5)
1. a kind of device of medical refuse burning flyash microwave continuous sintering ceramsite it is characterised in that：Including the first hopper, second
Hopper, agitating device, forming machine, sinter body of heater, water cooling plant, extracting tower, activated carbon injection apparatus, sack cleaner, air inducing
Machine；Wherein：First hopper and the second hopper connect agitating device, agitating device connecting machine respectively, and forming machine passes through charging
Device with sintering furnace body phase even, is arranged by drive sprocket, driven sprocket, transmission chain, fixation in the middle position of sintering body of heater
Axle and the transporter of SiC container composition, the two ends of transmission chain are connected with drive sprocket and driven sprocket respectively, and actively
Form the two transmission planes up and down with horizontal direction parallel between sprocket wheel and driven sprocket；On transmission chain, setting is fixed
Axle, arranges SiC container in fixing axle；Sintering body of heater arranges microwave heating equipment, carries out microwave in sintering body of heater body
Heating；Vertical lower setting haydite collection bucket in transporter side, haydite collection bucket lower end arranges drawing mechanism, in order to
Collect haydite in the SiC container being located in sintering body of heater；Upper end setting collection and confinement of gases mouth in sintering body of heater；Collection and confinement of gases mouth leads to
Cross pipeline to be connected with the top of water cooling plant, the bottom of water cooling plant is connected with the top of extracting tower by pipeline；Extracting tower
Bottom is connected with sack cleaner by pipeline, and arranges activated carbon injection apparatus, sack cleaner and air-introduced machine on pipeline
It is connected.
2. as claimed in claim 1 a kind of device of medical refuse burning flyash microwave continuous sintering ceramsite it is characterised in that：
The number of described SiC container is 20-40.
3. as claimed in claim 1 a kind of device of medical refuse burning flyash microwave continuous sintering ceramsite it is characterised in that：
Described microwave heating equipment is magnetron, when being configured, uniformly sets along body of heater length direction in sintering body of heater upper end face
Put upper end magnetron, and be arranged alternately upper end both sides magnetron in sintering body of heater two sides along body of heater length direction, in two sides
The centre-height one of the height of upper end both sides magnetron of the upper setting SiC container that be located at upper transmission plane in interior with sintering furnace body
Cause.
4. the device of a kind of medical refuse burning flyash microwave continuous sintering ceramsite as described in claim 1 or claim 3,
It is characterized in that：Microwave heating equipment is when being configured, on the surface of sintering body of heater upper and lower side, equal along body of heater length direction
Even setting upper end magnetron and lower end magnetron, and it is arranged alternately upper end both sides in sintering body of heater two sides along body of heater length direction
Magnetron and lower end both sides magnetron, are located at upper in the height of upper end both sides magnetron arranging on opposite sides and sintering furnace body
The centre-height of the SiC container in transmission plane is consistent, the height of lower end both sides magnetron arranging on opposite sides and sintering
The centre-height of the SiC container being located in underdrive plane in body of heater is consistent.
5. the device of a kind of medical refuse burning flyash microwave continuous sintering ceramsite as described in claim 1 or claim 3,
It is characterized in that：The described upper end magnetron being arranged on sintering body of heater upper end is 8-15, is arranged on sintering body of heater lower end
Lower end magnetron quantity is 8-15, and the quantity being arranged on the every side of magnetron of sintering body of heater both sides is 8-15.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620853312.1U CN205997147U (en) | 2016-08-05 | 2016-08-05 | A kind of device of medical refuse burning flyash microwave continuous sintering ceramsite |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620853312.1U CN205997147U (en) | 2016-08-05 | 2016-08-05 | A kind of device of medical refuse burning flyash microwave continuous sintering ceramsite |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN205997147U true CN205997147U (en) | 2017-03-08 |
Family
ID=58199955
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620853312.1U Expired - Fee Related CN205997147U (en) | 2016-08-05 | 2016-08-05 | A kind of device of medical refuse burning flyash microwave continuous sintering ceramsite |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN205997147U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110124247A (en) * | 2019-05-31 | 2019-08-16 | 江苏天楹环保能源成套设备有限公司 | A kind of system of microwave treatment incineration of refuse flyash |
| CN116255625A (en) * | 2023-01-09 | 2023-06-13 | 北京鑫风绿能科技有限公司 | Down pyrolysis device and method |
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2016
- 2016-08-05 CN CN201620853312.1U patent/CN205997147U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN110124247A (en) * | 2019-05-31 | 2019-08-16 | 江苏天楹环保能源成套设备有限公司 | A kind of system of microwave treatment incineration of refuse flyash |
| CN116255625A (en) * | 2023-01-09 | 2023-06-13 | 北京鑫风绿能科技有限公司 | Down pyrolysis device and method |
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