CN205424938U - Burning furnace secondary pyrolysis ashing room device is burnt to rotary kiln formula - Google Patents
Burning furnace secondary pyrolysis ashing room device is burnt to rotary kiln formula Download PDFInfo
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- CN205424938U CN205424938U CN201620230989.XU CN201620230989U CN205424938U CN 205424938 U CN205424938 U CN 205424938U CN 201620230989 U CN201620230989 U CN 201620230989U CN 205424938 U CN205424938 U CN 205424938U
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- rotary kiln
- pyrolysis
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- slag
- room
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Abstract
Burning furnace secondary pyrolysis ashing room device is burnt to rotary kiln formula including rotary kiln and transport means, still includes the secondary pyrolysis room of volatilizing, the secondary pyrolysis volatilize room one side and be connected with the rotary kiln, the opposite side is provided with two combustion chamber outlet, the bottom is provided with out the slag bath, the play slag bath on be provided with rotatory slag discharging device, the slag notch, slag tap water -stop and mucking machine, the secondary pyrolysis volatilize the room and pass through the fixed block and go out the slag bath to be connected, the rotary kiln on be provided with the flexible drive device, gear engagement's effect has been guaranteed to the flexibility of having utilized the sprocket chain to connect, the structure is more stable, prolonged life.
Description
Technical field
This utility model relates to doctor and gives up or trade waste process, particularly relates to rotary kiln type incinerator secondary pyrolysis ashing chamber device.
Background technology
When traditional rotary kiln cures the materials such as useless or trade waste (containing danger wastes) in process, from structure, revolution kiln body air feed is uneven, causes material to burn inside kiln body, does not reaches dry distilling, the purpose being pyrolyzed, being ashed, thus cause gas fume of combustion chamber amount 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 reaches country's correlative link guaranteed request, and then need fuel oil or gas-fired combustion-supporting, increase enterprise operation cost.
From the point of view of from the kind of drive, main transmission is divided into two kinds: medium and small rotary kiln uses single-point transmission, kiln large-scale uses 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, the most easily occurring 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 to use different structures to realize flexibly connecting, and prevents to 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 the most complicated.
Summary of the invention
This utility model rotary kiln type incinerator secondary pyrolysis ashing chamber device, have employed secondary pyrolysis ashing chamber device further realize dry distilling, be pyrolyzed, 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, this utility model the technical scheme is that 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, it is provided with flexible drive device on described rotary kiln.
As preferred technical scheme: described rotary slag discharge device is connected to out on slag bath by fixed plate, and connect bottom secondary pyrolysis devolatilization room；Described slag notch is connected with mucking machine, and through fixed 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 means, 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, engaged by the first gear and 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 α less than 15 °.
The beneficial effects of the utility model are: rotary kiln type incinerator secondary pyrolysis ashing chamber device, 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, it is provided with flexible drive device on described rotary kiln, whole deslagging process flow process succinctly facilitates, work continuously, 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 this utility model structural representation；
Fig. 2 is that this utility model Figure 1A is 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. fixed 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 the accompanying drawings this utility model 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 α 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, lower section is provided with out slag bath 4；Described slag notch 6, through fixed 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 fixed 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；It is provided with flexible drive device 9 on described rotary kiln 1；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 means；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；Being engaged by the first gear 9-3 and the second gear 9-5 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.
nullOf the present utility model it is embodied as: drive flexible drive device 9 by driving means，Rotary kiln 1 is operated，Material ceaselessly seethes advance in rotary kiln 1，Preliminary dry distilling、The material of pyrolysis enters secondary pyrolysis ashing chamber 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，Fully dry distilling in secondary pyrolysis ashing chamber 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 of lime-ash 5 being ashed 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 last purified process of flue gas is qualified，When actually used，Can also be according to the different kind of garbage，Arrange multiple pyrolysis ashing chamber 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 this utility model description; and not 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 cannot all of embodiment be given exhaustive, and the obvious change thus amplified out or variation still in protection domain of the present utility model among.
Claims (5)
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)；It is provided with flexible drive device (9) on described rotary kiln (1).
Rotary kiln type incinerator secondary the most according to claim 1 pyrolysis ashing chamber device, it is characterised in that: described rotary slag discharge device (5) is connected to out on slag bath (4) by fixed plate (5-1), and connects with bottom, secondary pyrolysis devolatilization room (2)；Described slag notch (6) is connected with mucking machine (8), and through fixed plate (5-1)；Described mucking machine (8) connects with water-stop of slagging tap (7).
Rotary kiln type incinerator secondary the most according to claim 1 pyrolysis ashing chamber device, 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 means；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).
Rotary kiln type incinerator secondary the most according to claim 1 pyrolysis ashing chamber device, it is characterised in that: described rotary kiln (1) is internally provided with rotary flow deflector.
Rotary kiln type incinerator secondary the most according to claim 1 pyrolysis ashing chamber device, it is characterised in that: described rotary kiln (1) and horizontal level install gradient α less than 15 °.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620230989.XU CN205424938U (en) | 2016-03-24 | 2016-03-24 | Burning furnace secondary pyrolysis ashing room device is burnt to rotary kiln formula |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201620230989.XU CN205424938U (en) | 2016-03-24 | 2016-03-24 | Burning furnace secondary pyrolysis ashing room device is burnt to rotary kiln formula |
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| Publication Number | Publication Date |
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| CN205424938U true CN205424938U (en) | 2016-08-03 |
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| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201620230989.XU Withdrawn - After Issue CN205424938U (en) | 2016-03-24 | 2016-03-24 | Burning furnace secondary pyrolysis ashing room device is burnt to rotary kiln formula |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105650646A (en) * | 2016-03-24 | 2016-06-08 | 江苏联兴成套设备制造有限公司 | Secondary pyrolysis ashing chamber device of rotary kiln type incinerator and slag removal technology |
| TWI625494B (en) * | 2017-12-05 | 2018-06-01 | Nat Chung Shan Inst Science & Tech | Rotary destruction furnace |
| CN112923720A (en) * | 2021-02-04 | 2021-06-08 | 湖南鼎玖能源环境科技股份有限公司 | Hot-blast furnace and slewing equipment |
-
2016
- 2016-03-24 CN CN201620230989.XU patent/CN205424938U/en not_active Withdrawn - After Issue
Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN105650646A (en) * | 2016-03-24 | 2016-06-08 | 江苏联兴成套设备制造有限公司 | Secondary pyrolysis ashing chamber device of rotary kiln type incinerator and slag removal technology |
| CN105650646B (en) * | 2016-03-24 | 2018-05-22 | 江苏联兴成套设备制造有限公司 | The secondary pyrolysis ashing chamber device of rotary kiln type incinerator and deslagging process |
| TWI625494B (en) * | 2017-12-05 | 2018-06-01 | Nat Chung Shan Inst Science & Tech | Rotary destruction furnace |
| CN112923720A (en) * | 2021-02-04 | 2021-06-08 | 湖南鼎玖能源环境科技股份有限公司 | Hot-blast furnace and slewing equipment |
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Legal Events
| Date | Code | Title | Description |
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| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| C41 | Transfer of patent application or patent right or utility model | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20160922 Address after: 214500 No. 95 Leap Road, Xinqiao Town, Jiangsu, Jingjiang Patentee after: JIANGSU DINGXUN ENVIRONMENTAL PROTECTION TECHNOLOGY CO., LTD. Address before: 214500 No. 96 Leap Road, Xinqiao Town, Jingjiang City, Jiangsu, Taizhou Patentee before: Jiangsu Lianxing Complete Sets of Equipment Manufacture Co., Ltd. |
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| AV01 | Patent right actively abandoned |
Granted publication date: 20160803 Effective date of abandoning: 20180522 |
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| AV01 | Patent right actively abandoned |