CN105650646A - Secondary pyrolysis ashing chamber device of rotary kiln type incinerator and slag removal technology - Google Patents
Secondary pyrolysis ashing chamber device of rotary kiln type incinerator and slag removal technology Download PDFInfo
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- CN105650646A CN105650646A CN201610171561.7A CN201610171561A CN105650646A CN 105650646 A CN105650646 A CN 105650646A CN 201610171561 A CN201610171561 A CN 201610171561A CN 105650646 A CN105650646 A CN 105650646A
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- rotary kiln
- secondary pyrolysis
- ashing
- slag
- pyrolysis
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Classifications
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- 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
- F23G5/20—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having rotating or oscillating drums
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- 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
- F23G5/08—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating
- F23G5/14—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion
- F23G5/16—Incineration of waste; Incinerator constructions; Details, accessories or control therefor having supplementary heating including secondary combustion in a separate combustion chamber
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- 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
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G7/00—Incinerators or other apparatus for consuming industrial waste, e.g. chemicals
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2202/00—Combustion
- F23G2202/10—Combustion in two or more stages
- F23G2202/101—Combustion in two or more stages with controlled oxidant supply
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2202/00—Combustion
- F23G2202/10—Combustion in two or more stages
- F23G2202/103—Combustion in two or more stages in separate chambers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2203/00—Furnace arrangements
- F23G2203/20—Rotary drum furnace
- F23G2203/206—Rotary drum furnace with charging ports in the sidewall
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- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F23—COMBUSTION APPARATUS; COMBUSTION PROCESSES
- F23G—CREMATION FURNACES; CONSUMING WASTE PRODUCTS BY COMBUSTION
- F23G2209/00—Specific waste
- F23G2209/20—Medical materials
Abstract
A secondary pyrolysis ashing chamber device of a rotary kiln type incinerator comprises a rotary kiln and a transportation tool and further comprises a secondary pyrolysis volatilization chamber; one side of the secondary pyrolysis volatilization chamber is connected with the rotary kiln, and the other side of the secondary pyrolysis volatilization chamber is provided with a secondary combustion chamber outlet, and a slag outlet pool is arranged at the bottom of the secondary pyrolysis volatilization chamber; a rotary slag outlet device, a slag outlet, a slag water outlet seal and a slag outlet machine are arranged on the pool outlet pool; the secondary pyrolysis volatilization chamber is connected with the slag outlet pool through a fixing block, and a flexible driving device is arranged on the rotary kiln; and a slag removal technology of the secondary pyrolysis ashing chamber device of the rotary kiln type incinerator comprises the steps of feeding, secondary pyrolysis ashing and slag removal. The secondary pyrolysis ashing chamber device is adopted to further achieve dry distillation, pyrolysis and ashing treatment, the whole technology process is concise and convenient, continuous work is achieved, and the efficiency is improved; and according to a transmission structure, a chain wheel and a gear are jointly arranged, flexibility of connection of the chain wheel and a chain is utilized, the meshing effect of the gear is ensured, the structure is more stable, and the service life is prolonged.
Description
Technical field
The present invention relates to doctor to give up or trade waste process, particularly relate to rotary kiln type incinerator secondary pyrolysis ashing chamber device and deslagging process.
Background technology
Traditional rotary kiln is when processing materials such as curing useless or trade waste (containing danger wastes), from structure, revolution kiln body air feed is uneven, causes that material burns inside kiln body, does not reach the purpose of dry distilling, pyrolysis, ashing, thus causing that gas fume of combustion chamber amount is not enough, ignition temperature is on the low side, and the lime-ash content of organics that rotary kiln afterbody is discharged exceeds standard, and does not reach country's correlative link guaranteed request, and then need fuel oil or gas-fired combustion-supporting, increase enterprise operation cost.
The kind of drive, main transmission is divided into two kinds: medium and small rotary kiln adopts single-point transmission, kiln large-scale adopts two point transmission, so-called single-point transmission is exactly that a little gear engages with the bull gear being fixed on cylinder of rotary kiln, and two point transmission to be exactly two little gears engage with the bull gear being fixed on cylinder of rotary kiln, carry out transmission, owing to the engagement of size gear is Hard link, easily occurring in actual use killing, the generation of broken teeth accident, safety cannot ensure.
Published technical literature: " rotary kiln flexible gearing " and " application on rotary kiln of the BF type Flexible Transmission " is exactly adopt different structures to realize flexibly connecting, it is prevented that kill, broken teeth phenomenon.
China Patent No. 2006101546969 incineration equipment system of rotary kiln for hazardous waste garbage, have employed multiple tracks multilamellar purification sediment structure and ensures that processing structure reaches country's correlative link guaranteed request, but structure is excessively complicated.
Summary of the invention
Rotary kiln type incinerator secondary pyrolysis ashing chamber device of the present invention and deslagging process, have employed secondary pyrolysis ashing chamber device and further realize dry distilling, pyrolysis, ashing process, drive mechanism have employed sprocket wheel and gear is arranged jointly, make use of the flexibility that sprocket wheel chain connects, it is ensured that the effect of gear engagement.
In order to realize above-mentioned technical purpose, reach above-mentioned technology requirement, the technical solution adopted in the present invention is: rotary kiln type incinerator secondary pyrolysis ashing chamber device, including rotary kiln and means of transport, it is characterized in that: also include secondary pyrolysis devolatilization room, described side, secondary pyrolysis devolatilization room is connected with rotary kiln, opposite side is provided with two combustor exits, bottom is provided with out slag bath, described goes out to be provided with on slag bath rotary slag discharge device, slag notch, slag tap water-stop and mucking machine, described secondary pyrolysis devolatilization room is connected with going out slag bath by fixed block, described rotary kiln is provided with flexible drive device.
As preferred technical scheme: described rotary slag discharge device is connected to out on slag bath by fixing plate, and connects with bottom secondary pyrolysis devolatilization room; Described slag notch is connected with mucking machine, and through fixing plate; Described mucking machine connects with water-stop of slagging tap.
As preferred technical scheme: described flexible drive device includes the first drive mechanism and the second drive mechanism, the first described drive mechanism is fixed on rotary kiln, the second described drive mechanism is connected with driving device, the first described drive mechanism is made up of the first gear and the first sprocket wheel, the second described drive mechanism is made up of the second gear and the second sprocket wheel, by the first gear and the engagement of the second gear between the first described drive mechanism and the second drive mechanism, chain connects, and described chain is connected on the first sprocket wheel and the second sprocket wheel.
As preferred technical scheme: described rotary kiln is internally provided with rotary flow deflector.
As preferred technical scheme: described rotary kiln and horizontal level install gradient �� less than 15 ��.
The deslagging process of rotary kiln type incinerator secondary pyrolysis ashing chamber device, it is characterised in that: comprise the following steps:
(1), charging:
Material is added from charging aperture; Drive flexible drive device by driving device so that rotary kiln operates, the rotary flow deflector arranged in rotary kiln drive material ceaselessly to seethe advance, be heated evenly, carry out preliminary treatment;
(2), secondary pyrolysis ashing:
The material of preliminary treatment enters secondary pyrolysis ashing room from the discharging opening of rotary kiln, by uniform cloth air port, accurately controls oxygen, fully processes;
(3), slagging-off:
The flue gas produced enters dual firing chamber from two combustor exits and fully burns, and effectively eliminates the Organic substance in garbage and poisonous and harmful substance.
As preferred technical scheme: in step (3), the treated rotated deslagging device of the lime-ash completed falls into slags tap in water-stop, and the lime-ash after cooling falls into means of transport through mucking machine.
The invention has the beneficial effects as follows: rotary kiln type incinerator secondary pyrolysis ashing chamber device and deslagging process, including secondary pyrolysis devolatilization room, further realize dry distilling, pyrolysis, ashing processes, described side, secondary pyrolysis devolatilization room is connected with rotary kiln, opposite side is provided with two combustor exits, bottom is provided with out slag bath, described goes out to be provided with on slag bath rotary slag discharge device, slag notch, slag tap water-stop and mucking machine, described secondary pyrolysis devolatilization room is connected with going out slag bath by fixed block, described rotary kiln is provided with flexible drive device, whole deslagging process flow process succinctly facilitates, continuous operation, improve efficiency, make use of the flexibility that sprocket wheel chain connects, ensure that the effect that gear engages, do not have and kill, broken teeth phenomenon.
Accompanying drawing explanation
Fig. 1 is present configuration schematic diagram;
Fig. 2 is Figure 1A of the present invention to 3-D view;
In the drawings: 1. rotary kiln, 1-1. charging aperture, 1-2. discharging opening, 2. two pyrolysis devolatilization rooms, 2-1. cloth air port, 3. two combustor exit, 4. go out slag bath, 5. rotary slag discharge device, 5-1. fixes plate, 6. slag notch, 7. slag tap water-stop, 8. mucking machine, 9. flexible drive device, 9-1. the first drive mechanism, 9-2. the second drive mechanism, 9-3. the first gear, 9-4. the first sprocket wheel, 9-5. the second gear, 9-6. the second sprocket wheel, 9-7. chain, 10. means of transport, 101. fixed block.
Detailed description of the invention
Below in conjunction with accompanying drawing, the present invention is further described;
In the accompanying drawings, rotary kiln type incinerator secondary pyrolysis ashing chamber device, including rotary kiln 1 and means of transport 10, described rotary kiln 1 is internally provided with rotary flow deflector, purpose is when rotary kiln 1 rotates, material is promoted to be rotationally advancing, it is heated evenly, accelerate material pyrolysis, dry distilling, described rotary kiln 1 and horizontal level install gradient �� less than 15 ��, material in rotary kiln 1 can be made to enter secondary pyrolysis devolatilization room 2 and not result in blocking, described side, secondary pyrolysis devolatilization room 2 is connected with rotary kiln 1, opposite side is provided with two combustor exits 3, bottom is provided with slag notch 6 and rotary slag discharge device 5, it is arranged below out slag bath 4, described slag notch 6, through fixing plate 5-1, communicates with the mucking machine 8 gone out on slag bath 4, the lower end of described rotary slag discharge device 5 is connected to out on slag bath 4 by fixing plate 5-1, described goes out to be additionally provided with in slag bath 4 water-stop 7 of slagging tap, the outer ring of described secondary pyrolysis devolatilization room 2 is connected with going out slag bath 4 by fixed block 101, described rotary kiln 1 is provided with flexible drive device 9, described flexible drive device 9 includes the first drive mechanism 9-1 and the second drive mechanism 9-2, the first described drive mechanism 9-1 is fixed on rotary kiln 1, the second described drive mechanism 9-2 is connected with driving device, the first described drive mechanism 9-1 is hierarchic structure, is made up of the first gear 9-3 and the first sprocket wheel 9-4, the two ends of the first described gear 9-3 are symmetrically arranged with the first sprocket wheel 9-4, the second described drive mechanism 9-2 is hierarchic structure, is made up of the second gear 9-5 and the second sprocket wheel 9-6, the two ends of the second described gear 9-5 are symmetrically arranged with the second sprocket wheel 9-6, by the first gear 9-3 and the second gear 9-5 engagement between the first described drive mechanism 9-1 and the second drive mechanism 9-2, chain 9-7 connects, described chain 9-7 is connected on the first sprocket wheel 9-4 and the second sprocket wheel 9-6, make use of the flexibility that sprocket wheel chain connects, it is ensured that the effect of gear engagement, do not have and kill, broken teeth phenomenon.
The deslagging process of rotary kiln type incinerator secondary pyrolysis ashing chamber device, it is characterised in that: comprise the following steps:
(1), charging:
Material is added from charging aperture 1-1; Drive flexible drive device 9 by driving device so that rotary kiln (1) operates, the rotary flow deflector arranged in rotary kiln (1) drive material ceaselessly to seethe advance, be heated evenly, carry out preliminary treatment;
(2) secondary pyrolysis ashing:
The material of preliminary treatment enters secondary pyrolysis ashing room 2 from the discharging opening 1-2 of rotary kiln 1, by uniform cloth air port 2-1, accurately controls oxygen, fully processes;
(3) slagging-off:
The flue gas produced enters dual firing chamber from two combustor exits 3 and fully burns, effectively eliminate the Organic substance in garbage and poisonous and harmful substance, the rotated deslagging device 5 of the treated lime-ash completed falls into slags tap in water-stop 7, and the lime-ash after cooling falls into means of transport 10 through mucking machine 8.
Specific embodiment of the invention: drive flexible drive device 9 by driving device, rotary kiln 1 is operated, material ceaselessly seethes advance in rotary kiln 1, preliminary dry distilling, the material of pyrolysis enters secondary pyrolysis ashing room 2 from rotary kiln 1 afterbody, by uniform cloth air port 2-1, accurately control oxygen, it is material and the air contact of complete pyrolytic incineration in rotary kiln 1, abundant dry distilling in secondary pyrolysis ashing room 2, pyrolysis, ashing, the flue gas produced after pyrolysis enters dual firing chamber from two combustor exits 3 and fully burns, effectively eliminate the Organic substance in garbage and poisonous and harmful substance, through pyrolysis, the rotated deslagging device 5 of lime-ash that ashing completes falls into slags tap in water-stop 7, lime-ash after cooling falls into means of transport 10 through mucking machine 8, it is transported to appointed place, air is entered through chimney after the purified process of last flue gas is qualified, when actually used, can also according to the different kind of garbage, arrange multiple pyrolysis ashing room to connect, means of transport 10 and charging can be set to automatic conveying device, achieve automatization, guarantee that slag removal and purification processes and meet relevant criterion.
Above-described embodiment is only for clearly demonstrating the description that the present invention makees; and it is not the restriction to embodiment; to those of ordinary skill in the art; can also make other changes in different forms on the basis of the above description; here without also giving exhaustive to all of embodiment, and the apparent change thus amplified out or variation are still among protection scope of the present invention.
Claims (7)
1. rotary kiln type incinerator secondary pyrolysis ashing chamber device, including rotary kiln (1) and means of transport (10), it is characterized in that: also include secondary pyrolysis devolatilization room (2), described secondary pyrolysis devolatilization room (2) side is connected with rotary kiln (1), opposite side is provided with two combustor exits (3), and bottom is provided with out slag bath (4); Described goes out to be provided with on slag bath (4) rotary slag discharge device (5), slag notch (6), water-stop of slagging tap (7) and mucking machine (8); Described secondary pyrolysis devolatilization room (2) is connected with going out slag bath (4) by fixed block (101); Described rotary kiln (1) is provided with flexible drive device (9).
2. rotary kiln type incinerator secondary pyrolysis ashing chamber device according to claim 1, it is characterised in that: described rotary slag discharge device (5) is connected to out on slag bath (4) by fixing plate (5-1), and connects with bottom, secondary pyrolysis devolatilization room (2); Described slag notch (6) is connected with mucking machine (8), and through fixing plate (5-1); Described mucking machine (8) connects with water-stop of slagging tap (7).
3. rotary kiln type incinerator secondary pyrolysis ashing chamber device according to claim 1, it is characterised in that: described flexible drive device (9) includes the first drive mechanism (9-1) and the second drive mechanism (9-2); Described the first drive mechanism (9-1) is fixed on rotary kiln (1); Described the second drive mechanism (9-2) is connected with driving device; Described the first drive mechanism (9-1) is made up of the first gear (9-3) and the first sprocket wheel (9-4); Described the second drive mechanism (9-2) is made up of the second gear (9-5) and the second sprocket wheel (9-6); Being engaged with the second gear (9-5) by the first gear (9-3) between described the first drive mechanism (9-1) and the second drive mechanism (9-2), chain (9-7) connects;Described chain (9-7) is connected on the first sprocket wheel (9-4) and the second sprocket wheel (9-6).
4. rotary kiln type incinerator secondary pyrolysis ashing chamber device according to claim 1, it is characterised in that: described rotary kiln (1) is internally provided with rotary flow deflector.
5. rotary kiln type incinerator secondary pyrolysis ashing chamber device according to claim 1, it is characterised in that: described rotary kiln (1) and horizontal level install gradient �� less than 15 ��.
6. the deslagging process of rotary kiln type incinerator secondary pyrolysis ashing chamber device according to claim 1, it is characterised in that: comprise the following steps:
(1), charging:
Material is added from charging aperture (1-1); Drive flexible drive device (9) by driving device so that rotary kiln (1) operates, the rotary flow deflector arranged in rotary kiln (1) drive material ceaselessly to seethe advance, be heated evenly, carry out preliminary treatment;
(2) secondary pyrolysis ashing:
The material of preliminary treatment enters secondary pyrolysis ashing room (2) from the discharging opening (1-2) of rotary kiln (1), by uniform cloth air port (2-1), accurately controls oxygen, fully processes;
(3) slagging-off:
The flue gas produced enters dual firing chamber from two combustor exits (3) and fully burns, and effectively eliminates the Organic substance in garbage and poisonous and harmful substance.
7. the deslagging process of rotary kiln type incinerator secondary pyrolysis ashing chamber device according to claim 6, it is characterized in that: in step (3), the rotated deslagging device of the treated lime-ash completed (5) falls in water-stop of slagging tap (7), and the lime-ash after cooling falls into means of transport (10) through mucking machine (8).
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610171561.7A CN105650646B (en) | 2016-03-24 | 2016-03-24 | The secondary pyrolysis ashing chamber device of rotary kiln type incinerator and deslagging process |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610171561.7A CN105650646B (en) | 2016-03-24 | 2016-03-24 | The secondary pyrolysis ashing chamber device of rotary kiln type incinerator and deslagging process |
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| CN105650646B CN105650646B (en) | 2018-05-22 |
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Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106090938A (en) * | 2016-07-25 | 2016-11-09 | 中材建设有限公司 | Danger wastes CIU |
| CN106546092A (en) * | 2016-11-03 | 2017-03-29 | 宁波大地化工环保有限公司 | A kind of compound slag-tapping system |
| CN107120659A (en) * | 2017-05-16 | 2017-09-01 | 镇江新宇固体废物处置有限公司 | A kind of hazardous waste burn system |
| CN108036330A (en) * | 2017-12-13 | 2018-05-15 | 常熟重型机械制造有限公司 | A kind of danger wastes burning processing system |
| CN109595541A (en) * | 2017-12-14 | 2019-04-09 | 湘潭锅炉有限责任公司 | A kind of lignite circulating fluidized bed boiler |
| CN110756569A (en) * | 2019-11-07 | 2020-02-07 | 朱建月 | Novel treatment equipment for melting fly ash |
| CN110925773A (en) * | 2019-12-13 | 2020-03-27 | 重庆科技学院 | Two segmentation waste drying and incineration disposal system |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2155466Y (en) * | 1993-05-21 | 1994-02-09 | 北方工业大学 | Flexible gearing |
| JPH10281436A (en) * | 1997-04-07 | 1998-10-23 | Chugoku Shii S K:Kk | Rotary kiln type sludge incinerator |
| CN201909521U (en) * | 2010-12-16 | 2011-07-27 | 王春和 | Novel flexible-transmission rotary kiln |
| CN204943506U (en) * | 2015-08-18 | 2016-01-06 | 江苏鼎新环保科技有限公司 | A kind of rotary kiln type continuous carbonization incinerator for thermal decomposition |
| CN105296011A (en) * | 2015-08-18 | 2016-02-03 | 江苏联兴成套设备制造有限公司 | Production technology of continuous ash discharging device for gasification furnace |
| CN205424938U (en) * | 2016-03-24 | 2016-08-03 | 江苏联兴成套设备制造有限公司 | Burning furnace secondary pyrolysis ashing room device is burnt to rotary kiln formula |
-
2016
- 2016-03-24 CN CN201610171561.7A patent/CN105650646B/en active Active
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN2155466Y (en) * | 1993-05-21 | 1994-02-09 | 北方工业大学 | Flexible gearing |
| JPH10281436A (en) * | 1997-04-07 | 1998-10-23 | Chugoku Shii S K:Kk | Rotary kiln type sludge incinerator |
| CN201909521U (en) * | 2010-12-16 | 2011-07-27 | 王春和 | Novel flexible-transmission rotary kiln |
| CN204943506U (en) * | 2015-08-18 | 2016-01-06 | 江苏鼎新环保科技有限公司 | A kind of rotary kiln type continuous carbonization incinerator for thermal decomposition |
| CN105296011A (en) * | 2015-08-18 | 2016-02-03 | 江苏联兴成套设备制造有限公司 | Production technology of continuous ash discharging device for gasification furnace |
| CN205424938U (en) * | 2016-03-24 | 2016-08-03 | 江苏联兴成套设备制造有限公司 | Burning furnace secondary pyrolysis ashing room device is burnt to rotary kiln formula |
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN106090938A (en) * | 2016-07-25 | 2016-11-09 | 中材建设有限公司 | Danger wastes CIU |
| CN106546092A (en) * | 2016-11-03 | 2017-03-29 | 宁波大地化工环保有限公司 | A kind of compound slag-tapping system |
| CN107120659A (en) * | 2017-05-16 | 2017-09-01 | 镇江新宇固体废物处置有限公司 | A kind of hazardous waste burn system |
| CN107120659B (en) * | 2017-05-16 | 2019-03-05 | 镇江新宇固体废物处置有限公司 | A kind of hazardous waste burn system |
| CN108036330A (en) * | 2017-12-13 | 2018-05-15 | 常熟重型机械制造有限公司 | A kind of danger wastes burning processing system |
| CN109595541A (en) * | 2017-12-14 | 2019-04-09 | 湘潭锅炉有限责任公司 | A kind of lignite circulating fluidized bed boiler |
| CN110756569A (en) * | 2019-11-07 | 2020-02-07 | 朱建月 | Novel treatment equipment for melting fly ash |
| CN110925773A (en) * | 2019-12-13 | 2020-03-27 | 重庆科技学院 | Two segmentation waste drying and incineration disposal system |
| CN110925773B (en) * | 2019-12-13 | 2024-03-22 | 重庆科技学院 | Two-section type waste drying and incineration treatment system |
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| CN105650646B (en) | 2018-05-22 |
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