CN201104097Y - Continuous rotary kiln with polygon-section boiler tube - Google Patents
Continuous rotary kiln with polygon-section boiler tube Download PDFInfo
- Publication number
- CN201104097Y CN201104097Y CNU2007200319262U CN200720031926U CN201104097Y CN 201104097 Y CN201104097 Y CN 201104097Y CN U2007200319262 U CNU2007200319262 U CN U2007200319262U CN 200720031926 U CN200720031926 U CN 200720031926U CN 201104097 Y CN201104097 Y CN 201104097Y
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Abstract
The utility model relates to a polygonal section furnace tube continuous rotary furnace, which consists of a feeding system, sealing devices, an exhaust system, a revolving body, a control system for heating rotation, a discharge system, an air pipe system, a furnace tube, a temperature measuring system, refractory materials, a furnace body frame and appearance, a light-duty fireproof module and a driving system, wherein, the feeding system is connected to the revolving body through a control valve and a helical delivery machine; the revolving body is fixedly provided with the control system for heating rotation, the temperature measuring system, the refractory materials and the light-duty fireproof module and is arranged on a machine frame; the discharge system is arranged on the tail of a furnace end; the revolving body is a polyhedron; the cross section of the furnace tube is a group of cylinders of equilateral (more than three sides) polygons; a baffle plate is arranged between a temperature reduction region and a high temperature region of the furnace tube; a set of wall oscillation machines is respectively arranged on both ends of a cylindrical body of the revolving body; the sealing devices are arranged on both ends of the furnace tube of the revolving body. The polygonal section furnace tube continuous rotary furnace has a perfect structure and design, reduces electric energy consumption and improves the hot use efficiency.
Description
One, technical field
The utility model relates to a kind of polygonal cross-section boiler tube continous way rotary furnace.
Two, background technology
The preparation of processes such as the drying of powder materials such as novel energy material, lithium battery material, LiFePO4, rare earth oxide, chemical industry catalyst for additives, heating, calcining and decomposing, redox.
At present in the powder calcination preparation process in this field, what generally adopt is the static saggar load mode powder calcination of stacking, existence is insufficient such as reaction, fire excessive cycle, gas is discharged not exclusively and the more high drawback of energy consumption index, be unfavorable for that powder material is needed evenly, decomposition and redox wait requirement fully, and circular boiler tube is reunited and the aspect such as is broken up and can not reach optimum efficiency adapting to materials overturning and superfine powder, and with regard to the heated metal pipe fitting since difformity resist aspect the stress being heated, the polygon body has advantages such as bigger bending resistance and anti-folding again with respect to circular body, so use polyhedron shape revolution boiler tube that advantage and the characteristics that substitute are not arranged.
Apply to the rotary furnace of chemical industry, catalyst, metallurgy, electronic material, as continuity kiln (Chinese utility model patent ZL03210256.9); Magnetic material sintering external-heating rotary kiln (Chinese utility model patent ZL89205257.9); Rotary kiln with resistor furnace for heating and calcining kaolin (Chinese utility model patent ZL01128612.1); Outer heating rotary kiln (Chinese utility model patent ZL97232399.6) or the like, in these structures compositions and boiler tube characteristics, exist the powder material upset inadequately cmpletely, material is prone to reunites and whole downslide the and be difficult for formation and overturn fully, mix and stirs, is unfavorable for that the thing phase reaction of powder material, gas discharge and convertible operation.
Three, summary of the invention
The purpose of this utility model is to provide a kind of polygonal cross-section boiler tube continous way rotary furnace at the weak point that above-mentioned rotary kiln exists.
The utility model technology compared with prior art, its advantage and characteristics are: powder material is produced more fully and completely stir and mix, produce particle conversion more completely and gas and discharge; 2, its complete hermetically-sealed construction can be realized atmosphere protection and atmosphere control completely; 3, reasonably the combination of heating mode and heating element heater can reach better energy-saving effect, has reduced power consumption, has improved hot service efficiency; 4, material, structure, the design of equipment integral body are more perfect, have guaranteed stability and the reliability of equipment in the middle of using effectively.
The purpose of this utility model is to realize like this: it comprises feed system, sealing device, gas extraction system, revolving body, the control system that adds heat run, discharge system, gas piping system, boiler tube, temp measuring system, refractory material, furnace body frame and outward appearance, light-duty fireproof modules, transmission system constitutes, feed system passes through control valve, spiral feeder is connected in revolving body, be fixed with the control system that adds heat run at revolving body, temp measuring system, refractory material, light-duty fireproof modules, revolving body places on the frame, discharge system, be located at the afterbody of burner, revolving body is a polyhedron, the cross section of boiler tube is the cylinder of one group of equilateral polygon, be provided with a plate washer between the cooling area of boiler tube and the high-temperature region, at the cylindrical shell two ends of revolving body each cover of wall device that shakes is set, the cross section of described boiler tube is one group of equilateral polygon, its polygon is the polygon greater than 3, and the boiler tube two ends of revolving body are provided with sealing device.Charging, discharge system adopt stainless steel screw(-type) feeder, and the feed motor is mechanical inorganic speed change, and is manually adjustable, and the stainless steel hopper is established on top, are with electronic shake wall device.Add that heating element heater is the METAL HEATING PROCESS silk in the control system of heat run, adopt the circular furnace lining of heater strip half inserted overall vacuum cast lightweight.
The utility model has adopted special polyhedron rotary pipe type structure, polyhedral each plane forms angle and (forms 120 degree angles between such as each plane of hexahedron when welding, form 90 degree angles etc. between each plane of tetrahedron), powder material can be broken up and be formed the particle displacement naturally when rotational slide slips over angle, powder material is produced when being heated calcining fully and fully mix, and reach full and uniform reaction and thing phase transformation; In conjunction with the waveform and the straight plate shape scraper plate of polyhedron boiler tube inner surface setting, when rotating, revolving body can make powder material raise the step-by-step movement of spreading and move doing parabolic path with axis direction.
For this polyhedron rotary pipe type kiln, powder material is achieved in that at the running of this section operation powder material at first is loaded in the kiln hood charging feed bin, fall to spiral feeder and be transported in the polyhedron boiler tube by by-pass valve control and pipeline by spiral feeder, establish sealing device between its burner device and the polyhedron swinging boiler tube, because the whole boiler tube of polyhedron can be regulated with horizontal direction and form certain inclination angle, after material enters into the polyhedron boiler tube, rotation (the big I of rotating speed is adjusted according to actual conditions) along with the polyhedron boiler tube, powder material is in the parabolic path motion while of doing the section direction and do slowly moving of axis direction, respectively by each temperature-controlled area in the boiler tube, the temperature of each temperature-controlled area can be arranged to identical or differently burn till with the control that reaches the uniform temperature curve according to powder product self arts demand in the middle of the process that moves.Finish burn till after, material enter boiler tube afterbody and the cooling, the powder after the cooling exports to outside the stove from the discharge bucket of body of heater afterbody.
Four, description of drawings
Fig. 1 is a structural representation of the present utility model
Fig. 2 is the sectional schematic diagram of the utility model polyhedron boiler tube
Wherein: feed system (1), sealing (2), gas extraction system (3), revolving body (4), the control system (5) that adds heat run, discharge system (6), gas piping system (7), polygon boiler tube (the boiler tube cross section is a polygon) (8), temp measuring system (9), refractory material (10), furnace body frame and outward appearance (11), light-duty fireproof modules (12), transmission system (13).
Five, embodiment
The utility model is described in further detail below in conjunction with accompanying drawing
With reference to accompanying drawing: the utility model polygonal cross-section boiler tube continous way rotary furnace, it comprises feed system (1), sealing device (2), gas extraction system (3), revolving body (4), the control system (5) that adds heat run, discharge system (6), gas piping system (7), boiler tube (8), temp measuring system (9), refractory material (10), furnace body frame and outward appearance (11), light-duty fireproof modules (12), transmission system (13) structure constitutes, feed system (1) passes through control valve, spiral feeder is connected in revolving body (4), be fixed with the control system (5) that adds heat run at revolving body (4), temp measuring system (9), refractory material (10), light-duty fireproof modules (12), revolving body (4) places on the frame (11), discharge system (6), be located at the afterbody of burner, revolving body (4) is a polyhedron, the cross section of boiler tube (8) is the cylinder of one group of equilateral polygon, be provided with a plate washer between the cooling area of boiler tube (8) and the high-temperature region, at the cylindrical shell two ends of revolving body (4) each cover of wall device that shakes is set, the cross section of described boiler tube (8) is one group of equilateral polygon, its polygon is the polygon greater than 3, is provided with sealing device (2) at boiler tube (8) two ends of revolving body (4).Charging, discharge system adopt stainless steel screw(-type) feeder, and the feed motor is mechanical inorganic speed change, and is manually adjustable, and the stainless steel hopper is established on top, are with electronic shake wall device.The middle heating element heater of control system (5) that adds heat run is the METAL HEATING PROCESS silk, adopts the circular furnace lining of heater strip half inserted overall vacuum cast lightweight.
Claims (3)
1. polygonal cross-section boiler tube continous way rotary furnace, it comprises feed system (1), sealing device (2), gas extraction system (3), revolving body (4), the control system (5) that adds heat run, discharge system (6), gas piping system (7), boiler tube (8), temp measuring system (9), refractory material (10), furnace body frame and outward appearance (11), light-duty fireproof modules (12), transmission system (13) structure constitutes, feed system (1) passes through control valve, spiral feeder is connected in revolving body (4), be fixed with the control system (5) that adds heat run at revolving body (4), temp measuring system (9), refractory material (10), light-duty fireproof modules (12), revolving body (4) places on the frame (11), discharge system (6), be located at the afterbody of burner, it is characterized in that: revolving body (4) is a polyhedron, the cross section of boiler tube (8) is the cylinder of one group of equilateral polygon, be provided with a plate washer between the cooling area of boiler tube (8) and the high-temperature region, at the cylindrical shell two ends of revolving body (4) each cover of wall device that shakes is set, the cross section of described boiler tube (8) is one group of equilateral polygon, its polygon is the polygon greater than 3, is provided with sealing device (2) at boiler tube (8) two ends of revolving body (4).
2. polygonal cross-section boiler tube continous way rotary furnace as claimed in claim 1 is characterized in that charging, discharge system adopt stainless steel screw(-type) feeder, and the feed motor is mechanical inorganic speed change, and is manually adjustable, and the stainless steel hopper is established on top, is with electronic shake wall device.
3. polygonal cross-section boiler tube continous way rotary furnace as claimed in claim 1, the middle heating element heater of control system (5) that it is characterized in that adding heat run is the METAL HEATING PROCESS silk, adopts the circular furnace lining of heater strip half inserted overall vacuum cast lightweight.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CNU2007200319262U CN201104097Y (en) | 2007-06-05 | 2007-06-05 | Continuous rotary kiln with polygon-section boiler tube |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
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CNU2007200319262U CN201104097Y (en) | 2007-06-05 | 2007-06-05 | Continuous rotary kiln with polygon-section boiler tube |
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CN201104097Y true CN201104097Y (en) | 2008-08-20 |
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CNU2007200319262U Expired - Lifetime CN201104097Y (en) | 2007-06-05 | 2007-06-05 | Continuous rotary kiln with polygon-section boiler tube |
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Cited By (12)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102031363A (en) * | 2011-01-06 | 2011-04-27 | 中冶东方工程技术有限公司 | Multi-stage roasting method for rare earth ore concentrate and equipment thereof |
CN102889782A (en) * | 2012-09-03 | 2013-01-23 | 杭州金马能源科技有限公司 | Quartz tube type uniform roasting furnace |
WO2014194567A1 (en) * | 2013-06-04 | 2014-12-11 | 四川玖长科技有限公司 | Rotary kiln for reducing phosphate ore in kiln process for production of phosphoric acid and method for solving ring forming in kiln tail in kiln process for production of phosphoric acid |
CN105154636A (en) * | 2015-10-22 | 2015-12-16 | 中航卓越锻造(无锡)有限公司 | Overturning type normalizing furnace device |
CN105651043A (en) * | 2016-03-28 | 2016-06-08 | 苏州汇科机电设备有限公司 | Transmission structure of high-temperature atmosphere rotary furnace |
CN106392095A (en) * | 2016-11-28 | 2017-02-15 | 攀枝花市仁通钒业有限公司 | Metal powder gas reduction equipment |
US9982947B2 (en) | 2013-06-04 | 2018-05-29 | Sichuan Ko Chang Technology Co., Ltd. | Rotary kiln for reducing phosphate ore in kiln phosphoric acid process and method for solving ring forming in kiln tail in kiln phosphoric acid process |
CN110440271A (en) * | 2019-08-07 | 2019-11-12 | 李星余 | A kind of flying ash processing unit being installed on rotary kiln |
CN110793314A (en) * | 2019-11-08 | 2020-02-14 | 佛山市天禄智能装备科技有限公司 | Special hexagonal furnace tube rotary kiln for lithium battery silicon carbon material |
CN111426184A (en) * | 2020-03-13 | 2020-07-17 | 晋江云智新材料科技有限公司 | Continuous electric heating rotary furnace and process for preparing lithium manganate by adopting same |
CN114334503A (en) * | 2021-12-24 | 2022-04-12 | 佛山市诺普材料科技有限公司 | Method for preparing silver tin oxide electrical contact material by low-temperature homogenization and material thereof |
CN115388644A (en) * | 2022-08-29 | 2022-11-25 | 中国新型建材设计研究院有限公司 | Pressure rotary calcining furnace for carbonization processing |
-
2007
- 2007-06-05 CN CNU2007200319262U patent/CN201104097Y/en not_active Expired - Lifetime
Cited By (17)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102031363B (en) * | 2011-01-06 | 2013-10-23 | 中冶东方工程技术有限公司 | Multi-stage roasting method for rare earth ore concentrate and equipment thereof |
CN102031363A (en) * | 2011-01-06 | 2011-04-27 | 中冶东方工程技术有限公司 | Multi-stage roasting method for rare earth ore concentrate and equipment thereof |
CN102889782B (en) * | 2012-09-03 | 2014-12-17 | 杭州金马能源科技有限公司 | Quartz tube type uniform roasting furnace |
CN102889782A (en) * | 2012-09-03 | 2013-01-23 | 杭州金马能源科技有限公司 | Quartz tube type uniform roasting furnace |
US9982947B2 (en) | 2013-06-04 | 2018-05-29 | Sichuan Ko Chang Technology Co., Ltd. | Rotary kiln for reducing phosphate ore in kiln phosphoric acid process and method for solving ring forming in kiln tail in kiln phosphoric acid process |
WO2014194567A1 (en) * | 2013-06-04 | 2014-12-11 | 四川玖长科技有限公司 | Rotary kiln for reducing phosphate ore in kiln process for production of phosphoric acid and method for solving ring forming in kiln tail in kiln process for production of phosphoric acid |
CN105154636A (en) * | 2015-10-22 | 2015-12-16 | 中航卓越锻造(无锡)有限公司 | Overturning type normalizing furnace device |
CN105651043A (en) * | 2016-03-28 | 2016-06-08 | 苏州汇科机电设备有限公司 | Transmission structure of high-temperature atmosphere rotary furnace |
CN106392095A (en) * | 2016-11-28 | 2017-02-15 | 攀枝花市仁通钒业有限公司 | Metal powder gas reduction equipment |
CN110440271A (en) * | 2019-08-07 | 2019-11-12 | 李星余 | A kind of flying ash processing unit being installed on rotary kiln |
CN110793314A (en) * | 2019-11-08 | 2020-02-14 | 佛山市天禄智能装备科技有限公司 | Special hexagonal furnace tube rotary kiln for lithium battery silicon carbon material |
CN111426184A (en) * | 2020-03-13 | 2020-07-17 | 晋江云智新材料科技有限公司 | Continuous electric heating rotary furnace and process for preparing lithium manganate by adopting same |
CN111426184B (en) * | 2020-03-13 | 2022-03-25 | 福建省云智新材料科技有限公司 | Continuous electric heating rotary furnace and process for preparing lithium manganate by adopting same |
CN114334503A (en) * | 2021-12-24 | 2022-04-12 | 佛山市诺普材料科技有限公司 | Method for preparing silver tin oxide electrical contact material by low-temperature homogenization and material thereof |
CN114334503B (en) * | 2021-12-24 | 2022-11-15 | 佛山市诺普材料科技有限公司 | Method for preparing silver tin oxide electrical contact material by low-temperature homogenization and material thereof |
CN115388644A (en) * | 2022-08-29 | 2022-11-25 | 中国新型建材设计研究院有限公司 | Pressure rotary calcining furnace for carbonization processing |
CN115388644B (en) * | 2022-08-29 | 2024-03-08 | 中国新型建材设计研究院有限公司 | Pressure rotary calciner for carbonization processing |
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Legal Events
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C14 | Grant of patent or utility model | ||
GR01 | Patent grant | ||
CX01 | Expiry of patent term | ||
CX01 | Expiry of patent term |
Granted publication date: 20080820 |