CN203798140U - Combined roaster - Google Patents
Combined roaster Download PDFInfo
- Publication number
- CN203798140U CN203798140U CN201420187032.2U CN201420187032U CN203798140U CN 203798140 U CN203798140 U CN 203798140U CN 201420187032 U CN201420187032 U CN 201420187032U CN 203798140 U CN203798140 U CN 203798140U
- Authority
- CN
- China
- Prior art keywords
- roaster
- indirect
- burner
- burning
- heat
- 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.)
- Expired - Fee Related
Links
- 239000000463 material Substances 0.000 claims abstract description 28
- 238000009413 insulation Methods 0.000 claims description 14
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 claims description 9
- 239000003546 flue gas Substances 0.000 claims description 9
- 239000000446 fuel Substances 0.000 claims description 8
- 230000002411 adverse Effects 0.000 claims description 3
- 230000005855 radiation Effects 0.000 abstract description 2
- 239000000779 smoke Substances 0.000 abstract 2
- 238000002485 combustion reaction Methods 0.000 description 8
- 238000010438 heat treatment Methods 0.000 description 5
- 239000003054 catalyst Substances 0.000 description 4
- 238000005516 engineering process Methods 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000005265 energy consumption Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000005245 sintering Methods 0.000 description 2
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 1
- 230000015572 biosynthetic process Effects 0.000 description 1
- 238000001354 calcination Methods 0.000 description 1
- 229910052799 carbon Inorganic materials 0.000 description 1
- 238000004523 catalytic cracking Methods 0.000 description 1
- 239000003245 coal Substances 0.000 description 1
- 239000000567 combustion gas Substances 0.000 description 1
- 239000013078 crystal Substances 0.000 description 1
- 239000002808 molecular sieve Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 239000003921 oil Substances 0.000 description 1
- -1 ore Substances 0.000 description 1
- 239000011148 porous material Substances 0.000 description 1
- 238000012805 post-processing Methods 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Landscapes
- Tunnel Furnaces (AREA)
Abstract
The utility model provides a combined roaster which comprises a slewing barrel and a heat preserving hearth, wherein a material inlet is formed at one end of the slewing barrel; a material outlet is formed at the other end of the material inlet; the slewing barrel is sleeved with the heat preserving hearth; the roaster further comprises a direct burner and indirect burners; the direct burner is arranged at a discharge end of the roaster; and the indirect burners are arranged on the heat preserving hearth.The roaster employs a burning system combining direct burning and indirect burning; the indirect burners burn outside the slewing barrel of the roaster and supply heat indirectly; high-temperature smoke generated by burning is not directly contacted with a material and provides heat for roasting the material in the rotary furnace mainly via heat radiation; the direct burner is arranged at the discharge end of the roaster; and high-temperature smoke generated by the burning enters the slewing barrel and is directly contacted with the material for heat supply.The roaster employs the combined burning system, and has high roasting temperature control precision, the heat efficiency of a roasting system can be effectively improved, the yield and quality are increased and improved, indirect and direct heat load proportion can be adjusted at the same time, and the roaster is applicable to roasting various materials.
Description
Technical field
The utility model relates to a kind of roaster combustion apparatus, is specifically related to the roaster of a kind of direct burning and the combined formula of indirect burning.
Background technology
Roasting is the process of carrying out high-temperature heat treatment after moulding through pre-dried wet stock in roaster by certain programming rate.Roaster (being also calcining furnace or rotary kiln) is extensively used the post processing of the materials such as ore, catalyst, molecular sieve and active carbon.Roaster is one of key equipment in catalytic cracking catalyst production process, it mainly removes volatile components and chemical bonding water in material by pyrolysis, make catalyst obtain certain crystal formation, grain size, pore structure and specific surface, form stable structure and improve mechanical strength.
Roaster generally, using coal, combustion gas, oil and electric etc. as thermal source, is divided into direct heating and the large class of indirect two by heating means.Petrochemical industry generally adopts indirect heating type, and so that wherein combustion type roaster and electrothermal roaster are more common.
Domestic roaster and foreign technology have a certain distance, be mainly reflected in burner structure backwardness, combustion system unreasonable allocation, sintering temperature control is improper etc., causes the shortcomings such as the roasting system thermal efficiency is low, energy consumption is high, exhaust emissions is not up to standard, product percent of pass is low.
Utility model content
In order to solve the problems such as domestic combustion type catalyst roaster burner structure backwardness, combustion system unreasonable allocation, sintering temperature control be improper, improve the roasting system thermal efficiency, reduce energy consumption, improve product percent of pass, the utility model provides the roaster of a kind of direct burning and the combined formula of indirect burning.
Concrete technical scheme of the present utility model is as follows:
A kind of combined type roaster, this roaster comprises rotating cylinder and insulation burner hearth, rotating cylinder one end is provided with material inlet, the other end is material outlet, insulation burner hearth is sleeved on outside rotating cylinder, also comprise direct burner and indirect burning device, directly burner arrangement is at the discharge end of roaster, and indirect burning device is arranged on insulation burner hearth.
Further design of the present utility model is: described indirect burning device is multiple, is evenly arranged in the side of insulation burner hearth.
12 of described indirect burning devices, directly 1 of burner.
The air-fuel ratio of indirect burning device is 30 ~ 40, turndown ratio, burner regulation ratio 5 ~ 10.Directly burner arrangement is at the discharge end of roaster, and the high-temperature flue gas that burning produces enters rotating cylinder inside, directly contacts heat supply with material.Directly burner air-fuel ratio 30 ~ 60, regulates than 5 ~ 10.
Directly burner arrangement is at the discharge end of roaster, and high-temperature flue gas and Flow of Goods and Materials direction that directly burner produces are adverse current, discharges with the feed end from roaster after material-heat-exchanging.
The thermic load ratio of indirect burning and directly burning can require to regulate according to different process, applicable to the roasting of various materials.
the utility model has following characteristics and advantage compared with existing technology:
The combined type roaster of the utility model design, adopts the combined combustion system of directly burning and indirect burning, can improve roasting accuracy of temperature control, improves the roasting system thermal efficiency, improves roasting quality, reduces production costs.Simultaneously adjustable indirect and direct thermic load ratio, can be applicable to the roasting of various materials.
Brief description of the drawings
Fig. 1 is structural representation of the present utility model.
In figure: 1-material inlet; 2-stove cylinder gas vent; 3-rotating cylinder; 4-is incubated burner hearth; 5-burner hearth exhanst gas outlet; The direct burner of 6-; 7-material outlet; 8-indirect burning device.
Detailed description of the invention
As shown in Figure 1, combined type roaster of the present utility model, comprise rotating cylinder 3, insulation burner hearth 4, direct burner 6 and indirect burning device 8, rotating cylinder 3 one end are provided with material inlet 1, the other end is material outlet 7, insulation burner hearth 4 is sleeved on outside rotating cylinder 3, insulation burner hearth 4 is provided with burner hearth exhanst gas outlet 5, directly burner 6 is arranged in the discharge end of roaster, indirect burning device 8 is arranged on insulation burner hearth 4, and indirect burning device 8 is multiple, evenly compartment is arranged in the side of insulation burner hearth 4.
Roaster of the present utility model, indirect burning device burns outward at roaster rotating cylinder, indirect heating, the high-temperature flue gas that burning produces does not directly contact with material, mainly provides heat by heat radiation and thermal convection current for material roasting in rotary furnace; Directly burner arrangement is at the discharge end of roaster, and the high-temperature flue gas that burning produces enters rotating cylinder inside, directly contacts heat supply with material.
Indirect burning device is arranged in outside roaster rotating cylinder, indirect burning device air-fuel ratio 30 ~ 40, turndown ratio, burner regulation ratio 5 ~ 10.
Directly burner arrangement is at the discharge end of roaster, and the high-temperature flue gas that burning produces enters rotating cylinder inside, directly contacts heat supply with material, and burner air-fuel ratio 30 ~ 60 regulates than 5 ~ 10.
Directly burner arrangement is at the discharge end of roaster, and high-temperature flue gas and Flow of Goods and Materials direction that directly burner produces are adverse current.
The course of work of the present utility model is as follows:
certain combustion type roaster adopts combine with the indirect burning device combustion system arrangement of formula of direct burner: indirect burning device 8 is evenly arranged on the insulation burner hearth 4 outside rotating cylinder 3, and the high-temperature flue gas that burning produces provides heat indirectly for technical process; Design altogether 13 burners, wherein, 12 of indirect burning devices, directly 1 of burner; The design power of every indirect burning device is 300kW, and indirect burning device overall design power is 3600kW; Indirect burning device air-fuel ratio 30 ~ 40 is adjustable, regulates than being 10.Directly burner arrangement is at the discharge end of rotating cylinder, and the high-temperature flue gas that burning produces enters in rotating cylinder, with roasting material direct contact heat transfer; Directly the design power of burner is 1200kW; Directly burner air-fuel ratio 30 ~ 60, regulates than 10.
Above-mentioned direct burning and the roaster of the combined formula of indirect burning, by novel arrangement of burner, improved roasting accuracy of temperature control (temperature control precision ± 5 DEG C) and the roasting system thermal efficiency, improved product quality.
Claims (6)
1. a combined type roaster, this roaster comprises rotating cylinder and insulation burner hearth, rotating cylinder one end is provided with material inlet, the other end is material outlet, insulation burner hearth is sleeved on outside rotating cylinder, it is characterized in that: also comprise direct burner and indirect burning device, directly burner arrangement is at the discharge end of roaster, and indirect burning device is arranged on insulation burner hearth.
2. combined type roaster according to claim 1, is characterized in that: described indirect burning device is multiple, is evenly arranged in the side of insulation burner hearth.
3. combined type roaster according to claim 2, is characterized in that: 12 of described indirect burning devices, directly 1 of burner.
4. combined type roaster according to claim 1, is characterized in that: the air-fuel ratio 30 ~ 40 of described indirect burning device, regulates than 5 ~ 10.
5. combined type roaster according to claim 1, is characterized in that: the air-fuel ratio 30 ~ 60 of described direct burner, regulates than 5 ~ 10.
6. combined type roaster according to claim 1, is characterized in that: high-temperature flue gas and Flow of Goods and Materials direction that directly burner produces are adverse current.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420187032.2U CN203798140U (en) | 2014-04-17 | 2014-04-17 | Combined roaster |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420187032.2U CN203798140U (en) | 2014-04-17 | 2014-04-17 | Combined roaster |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN203798140U true CN203798140U (en) | 2014-08-27 |
Family
ID=51380345
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201420187032.2U Expired - Fee Related CN203798140U (en) | 2014-04-17 | 2014-04-17 | Combined roaster |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN203798140U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114447464A (en) * | 2021-12-16 | 2022-05-06 | 山东天力能源股份有限公司 | A system and method for high temperature pyrolysis treatment of waste lithium battery |
-
2014
- 2014-04-17 CN CN201420187032.2U patent/CN203798140U/en not_active Expired - Fee Related
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN114447464A (en) * | 2021-12-16 | 2022-05-06 | 山东天力能源股份有限公司 | A system and method for high temperature pyrolysis treatment of waste lithium battery |
| CN114447464B (en) * | 2021-12-16 | 2024-04-16 | 山东天力能源股份有限公司 | A system and method for high temperature pyrolysis treatment of waste lithium batteries |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| KR101528411B1 (en) | External Heating Type Coal Material Decomposition Apparatus With Multiple Tubes | |
| CN205528594U (en) | Continuous retort of multilayer | |
| CN102001837A (en) | Method and device for calcining materials by using low calorific value fuel | |
| CN102161484A (en) | Zero-coal-consumption activated carbon production process and production device used in same | |
| CN203798140U (en) | Combined roaster | |
| CN203163478U (en) | Novel energy-saving kiln | |
| CN103482889A (en) | Heat accumulating type material calcinating device | |
| CN204125385U (en) | A kind of suspension cylinder formula also flows the two thorax kiln of accumulation of heat | |
| CN209143706U (en) | A kind of external heating type activation furnace of subsection-inlet | |
| CN203530147U (en) | Annular sleeve kiln | |
| CN203336958U (en) | Energy saving tunnel kiln | |
| CN105439141A (en) | Environmentally-friendly and energy-saving activated charcoal lifting furnace | |
| CN102249647A (en) | Process for producing colored glaze ceramic tiles | |
| CN104236081A (en) | Tubular heating furnace device | |
| CN203683393U (en) | Low-grade magnesite calcination system | |
| CN100368286C (en) | A method and device for rotary calcination of petroleum coke | |
| CN203687568U (en) | Direct-fired type biomass hot air stove | |
| CN203545892U (en) | Cement raw meal preheating and predecomposition device | |
| CN204404165U (en) | With the biomass granule fuel heat hot water stove of bottom ventilation | |
| CN201809172U (en) | Coal gas ring-shaped roasting furnace | |
| CN203928384U (en) | A kind of fume generating furnace that utilizes high efficiency smart burning to manufacture qualified drier | |
| CN204625191U (en) | A kind of environmental protection and energy saving gac promotes stove | |
| CN104501401A (en) | High-efficiency energy-saving furnace | |
| CN104848532A (en) | Efficient energy-saving environment-friendly boiler | |
| CN203569030U (en) | Combined rotary coal-oriented carbonization device |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant | ||
| CP01 | Change in the name or title of a patent holder |
Address after: 210000 No. 69, Xiyan Road, Jiangning Binjiang Development Zone, Nanjing, Jiangsu Patentee after: Tianhua Institute (Nanjing) Intelligent Manufacturing Co.,Ltd. Address before: 210000 No. 69, Xiyan Road, Jiangning Binjiang Development Zone, Nanjing, Jiangsu Patentee before: NANJING TIANHUA CHEMICAL ENGINEERING Co.,Ltd. |
|
| CP01 | Change in the name or title of a patent holder | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20140827 |
|
| CF01 | Termination of patent right due to non-payment of annual fee |