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CN102390692A - Dust catcher for belt conveyor with large inclined angle - Google Patents

Dust catcher for belt conveyor with large inclined angle Download PDF

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Publication number
CN102390692A
CN102390692A CN2011101889048A CN201110188904A CN102390692A CN 102390692 A CN102390692 A CN 102390692A CN 2011101889048 A CN2011101889048 A CN 2011101889048A CN 201110188904 A CN201110188904 A CN 201110188904A CN 102390692 A CN102390692 A CN 102390692A
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China
Prior art keywords
chamber
belt
dust
circulation separation
separation chamber
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CN2011101889048A
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Chinese (zh)
Inventor
白荣林
瞿仁静
户少勇
亢若谷
屠建春
江渝
包稚群
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Kunming Metallurgical Research Institute
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Kunming Metallurgical Research Institute
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Abstract

本发明涉及大倾角皮带机的除尘捕集器,属于环保干法除尘技术领域。本装置的皮带落料点处为密封罩结构,沿落料点起皮带运行方向依次设置高效沉降室、粉尘过滤器、循环分离室和密封室;高效沉降室、粉尘过滤器、循环分离室和密封室底部与格式输送带间由两侧的帮板封闭,帮板内壁设置有倾斜导流板,导流板下端在波状挡板范围以内,与落料管的下端设置有与高效沉降室连通的气流平衡管。本发明避免物料和粉尘沉积于皮带底板上,避免二次污染,对粉尘捕集率可高到95%以上,处理成本低、投资少、不占地、除尘器寿命长、施工工期短,除尘器出口气体低于国家排放标准。

Figure 201110188904

The invention relates to a dust collector for a belt conveyor with a large inclination angle, and belongs to the technical field of environmental protection dry dust removal. The belt blanking point of this device is a sealed cover structure, and the high-efficiency sedimentation chamber, dust filter, circulation separation chamber and sealing chamber are arranged in sequence along the belt running direction from the discharge point; the high-efficiency sedimentation chamber, dust filter, circulation separation chamber and The bottom of the sealing chamber and the format conveyor belt are closed by side plates on both sides. The inner wall of the side plate is provided with an inclined deflector. air balance tube. The invention avoids materials and dust from being deposited on the bottom plate of the belt, and avoids secondary pollution. The outlet gas of the device is lower than the national emission standard.

Figure 201110188904

Description

A kind of dedusting drip catcher of high angle belt conveyer machine
Technical field
The present invention relates to the dedusting drip catcher of high angle belt conveyer machine, belong to environmental protection dry dedusting technology field.
Background technology
High angle belt conveyer has characteristics such as high spud angle conveying, compact conformation, occupation of land are few, is that high spud angle is carried the ideal equipment with the vertical-lift material, in all employings to some extent of field such as underground mining and underground structrue engineering, surface mining, Large Self-unloading Ship machines.The maximum characteristics of high angle belt conveyer conveyer are to adopt conveyor belt with wave baffle board at its edge to replace duck conveyor belt, and its principle of work and structure are formed, and be then identical with general belt machine, and belt conveyor is that base band, cross wall and wave baffle board at its edge are formed integral structure.
The dust collection method of China's high angle belt conveyer, most cloth bag dedusting process that adopt centralized negative pressure air draught.Dust catching cover, delivery duct, bag dust collector, induced draft fan and chimney etc. in this cloth bag dedusting process, have been adopted.Its shortcoming is that investment is big; The dust catching rate is low; Horizontal pipe is prone to stop up, and influences capture rate; The exhausting amount is big, and over-the-road expense is high; Floor areas such as dust exhaustor, induced draft fan and chimney are big; Full-time Operation and Maintenance personnel and dust transportation device need be set.
The maximum difficulty of existing high angle belt conveyer dedusting just is the capture and the conveying of dust, on its belt deflector chute, bevelled cover is set, and fuses with the dust delivery duct.Overflowing fume trap cover for fear of dust, must be negative pressure state in the deflector chute; Deposit in pipeline for fear of dust, must adopt big air quantity to carry.Two factors all need powerful power, in case dust deposit and pipe interior, exhausting efficient will reduce greatly, and the negative pressure state in the fume trap cover will be destroyed, and dust will overflow fume trap cover, and arresting efficiency reduces significantly.Adopt the high angle belt conveyer of cloth bag dedusting process, after having moved one or two years, cleaning shaft stops up, dust pelletizing system paralysis, airborne dust point dust from flying.On the other hand, a certain amount of material and dust are deposited between deflector chute and the wave baffle board at its edge, and when belt got into the inclination angle part, the material of accumulation and dust can cause reentrainment of dust to pollute from landing on the base band base plate of belt.
Summary of the invention
For addressing the above problem; The present invention provides a kind of dedusting drip catcher of high angle belt conveyer machine; Can solve the problem of the capture of dust, avoid material and dust deposit on the belt base plate, avoid secondary pollution; Can be high to the dust catching rate to more than 95%, processing cost is low, small investment, do not take up an area of, the dust exhaustor life-span is long, the construction period is short.
Solving the scheme that technical matters of the present invention adopts is: belt discharging point place is the seal closure structure, sets gradually efficient setting chamber, dust filter unit, circulation separation chamber and sealed chamber along discharging point peeling tape running direction; Group's plate by both sides between efficient setting chamber, dust filter unit, circulation separation chamber and sealed chamber bottom and form load-transfer device seals; Group's plate inwall is provided with the inclination deflecting plate; The deflecting plate lower end is provided with the air balance pipe that is communicated with efficient setting chamber with the lower end of material blanking tube in wavy baffle plate scope.
Group's plate outer wall vertical of described load-transfer device both sides is in high angle belt conveyer base band base plate; The angle of inclination of the inclination deflecting plate of inwall is 50~70 °; The deflecting plate bottom is provided with sealing rubber strip; The sealing rubber strip lower end contacts with form load-transfer device top, deflecting plate lower end and form load-transfer device top down suction ≮ 10mm, the wave baffle board at its edge horizontal clearance ≮ 20mm of deflecting plate lower end and form load-transfer device.Caulking gum rule diameter is 8~10mm, 4~6 layers of arrangement, and seal clearance is 0.5~1.0mm.
The first half of said group plate is and efficient setting chamber, dust filter unit, circulation separation chamber and sealed chamber bonded assembly steel construction piece that height is 150mm ~ 300mm; The sealing rubber strip that the latter half contacts with form load-transfer device top is high to be 100mm ~ 200mm; Top at efficient setting chamber, dust filter unit, circulation separation chamber and sealed chamber is provided with plate baffle, is of a size of 300mm * 200mm, and angle of inclination and horizontal direction are 15~45 °.
Described circulation separation chamber is a top board bevelled horn shape, and angle of inclination and horizontal direction are 10~30 °, and the flared end of circulation separation chamber connects sealed chamber, and the top of sealed chamber has overhang rubber strip.
Equipment used herein satisfies following parameter: the flat section of high spud angle belt conveyer material feeding bandwidth is 500~1200mm, and belt speed is 0.8~3.15m/s, and the material drop is in the 10m during blanking, and material is the not viscous material of shape that looses.
The invention has the beneficial effects as follows:
1. do not have pipeline etc. to draw factory building, do not have equipment such as dust exhaustor, blower fan, chimney yet, do not take up an area of no view visual pollution.
2. need not to be equipped with the operator, easy to maintenance, expense is low.
3. consumption of power is approximately 20% of dust settling pocket technique.
4. compare with dust settling pocket technique and practice thrift investment about 20~30%.
5. guarantee that the dust catching rate reaches more than 95% for a long time, dust exhaustor outlet dustiness<50mg/>Nm 3, the dust content of operating point<10mgm 3
Description of drawings
Fig. 1 is the dust collector structural representation of high angle belt conveyer machine of the present invention.
Fig. 2 is group's Board position sectional schematic diagram of high angle belt conveyer dust collector of the present invention.
Each label is represented successively among the figure: high angle belt conveyer transport plane 1, sealed chamber 2, material blanking tube 3, air balance pipe 4, efficient setting chamber 5, dust filter unit 6, plate baffle 7, circulation separation chamber 8, deflecting plate 9, group's plate 10, sealing rubber strip 11, base band base plate 12, wavy baffle plate 13, deflecting plate support 14, rubber strip 15.
The specific embodiment
Embodiment: referring to Fig. 1,2; Stem to flat section of the material feeding of high angle belt conveyer transport plane 1 adopts sealed chamber 2 to seal; Set gradually efficient setting chamber 5, dust filter unit 6, circulation separation chamber 8 and sealed chamber 2 after the station of material blanking tube 3; Efficient setting chamber 5 is provided with plate baffle 7 with 8 tops, circulation separation chamber, and the bottom of material blanking tube 3 is provided with the air balance pipe 4 that communicates with efficient setting chamber 5, and efficient setting chamber 5, dust filter unit 6, circulation separation chamber 8 and sealed chamber 2 each dust removal installation fuse through group's plate 10; Group's plate 10 inwalls are provided with two deflecting plates 9; Deflecting plate is fixed in group plate 10 upper ends by support 14, and the deflecting plate bottom is provided with sealing rubber strip 11, contacts with the form load-transfer device.
At first fall into the dusty gas of efficient setting chamber 5, descend because volume increases air-flow velocity, and receive plate baffle 7 break-ins, big dust particle sedimentation from material blanking tube 3; Dust-contained airflow is back to the lower end in the material blanking tube 3 through air balance pipe 4 under negative pressure.The dust that part kinetic energy is bigger continues to separate through built-in bag dust collector to dust filter unit 6 diffusions, and clean gas is discharged dust exhaustor; On dust adhesion and the cloth bag; Get back on the belt transporter through the pulse rapping, few part slows down because of the adapter bonnet volume becomes air flow speed to 8 diffusions of circulation separation chamber; By on the inclination plate baffle 7 put stop, break-in, dust and burbling; Also have the dust of very small amount to continue, receive a series of rubber strips 15 that sealed chamber 2 overhangs and stop once more and settle down to sealed chamber 2 motions.
Referring to Fig. 2; Deflecting plate 9 angles of inclination that in group's plate 10, are provided with are 50~70 °; Sealing rubber strip 11 through deflecting plate 9 and its underpart all can fall into the dust that settles down in the form load-transfer device exactly, avoids falling on the wavy baffle plate 13 of pleated; Can not fall between group's plate 10 and the belt base plate 12 yet, avoid reentrainment of dust.
In to the feedway encapsulation process, produce dirt pits dust concentration≤5g/m 3, equipment should be in normal temperature, atmospheric pressure state, and seal case adopts the steel weldment; And rubber plate is adopted in the sealing between the equipment; Load-transfer device is a form high angle belt conveyer transport plane, and the head of dusting equipment, tail seal adopt multi-stage sealed rubber strip, and the rubber strip diameter is φ 8~10mm; 4~6 layers of arrangement, gap are 0.5~1.0mm.
Present embodiment is applied to the polysilicon project boiler room high angle belt conveyer dedusting that new material company is ground in the Kunming smelting, and totally 18 are removed dirt pits, and gross investment is 2,090,000 yuan, and the duration is 90 days, is constructed and put into operation in December, 2010, and dust removing effects is remarkable, dust exhaustor outlet dustiness<50mg/>Nm 3, be lower than discharging standards; The dust content of operating point<10mgm 3, meet national occupational health standard.Compare with dust settling pocket technique, gross investment is saved 800,000 yuan, and the duration shortens 60 days, and annual the saving moved 700,000 yuan of the electricity charge.

Claims (4)

1.一种大倾角皮带机的除尘捕集器,其特征在于:皮带落料点处为密封罩结构,沿落料点起皮带运行方向依次设置高效沉降室、粉尘过滤器、循环分离室和密封室;高效沉降室、粉尘过滤器、循环分离室和密封室底部与格式输送带间由两侧的帮板封闭,帮板内壁设置有倾斜导流板,导流板下端在波状挡板范围以内,与落料管的下端设置有与高效沉降室连通的气流平衡管。 1. A dust collector for a large-inclination belt conveyor, characterized in that: the belt blanking point is a sealed cover structure, and a high-efficiency settling chamber, a dust filter, a circulation separation chamber and Sealed chamber; between the bottom of the high-efficiency settling chamber, dust filter, circulation separation chamber and the sealed chamber, and the format conveyor belt are closed by side plates on both sides. The inner wall of the side plate is provided with an inclined deflector, and the lower end of the deflector is within the range of the corrugated baffle. Inside, the lower end of the drop pipe is provided with an air flow balance pipe communicating with the high-efficiency settling chamber. 2.根据权利要求1所述的大倾角皮带机的除尘捕集器,其特征在于:输送带两侧的帮板外壁垂直于大倾角皮带基带底板,内壁的倾斜导流板的倾斜角度为50°~70°,导流板下部设置密封橡胶条,密封橡胶条下端与格式输送带顶部接触,导流板下端与格式输送带顶部垂直间隙≮10mm,导流板下端与格式输送带的波状挡边水平间隙≮20mm,密封橡胶条条直径为8~10mm,4~6层排列,密封间隙为0.5~1.0mm。 2. The dust collector of a large-inclination belt conveyor according to claim 1, wherein the outer walls of the side plates on both sides of the conveyor belt are perpendicular to the bottom plate of the belt base belt at a large inclination angle, and the inclination angle of the inclined deflector on the inner wall is 50° °~70°, the lower part of the deflector is provided with a sealing rubber strip, the lower end of the sealing rubber strip is in contact with the top of the format conveyor belt, the vertical gap between the lower end of the deflector and the top of the format conveyor belt is ≮10mm, the lower end of the deflector is in contact with the corrugated stop of the format conveyor belt The horizontal gap between sides is ≮20mm, the diameter of the sealing rubber strip is 8-10mm, arranged in 4-6 layers, and the sealing gap is 0.5-1.0mm. 3.根据权利要求1或2所述的大倾角皮带机的除尘方法,其特征在于:所述帮板的上半部分为与高效沉降室、粉尘过滤器、循环分离室和密封室连接的钢结构件,高为150mm~300mm;下半部分与格式输送带顶部接触的密封橡胶条高为100mm~200mm;在高效沉降室、粉尘过滤器、循环分离室和密封室的上部设置了折流板,尺寸为300mm×200mm,倾斜角度与水平方向为15°~45°。 3. The dust removal method of a large-inclination belt conveyor according to claim 1 or 2, characterized in that: the upper part of the side plate is a steel plate connected with a high-efficiency settling chamber, a dust filter, a circulation separation chamber and a sealing chamber. Structural parts with a height of 150mm~300mm; the height of the sealing rubber strip in the lower part contacting the top of the format conveyor belt is 100mm~200mm; baffles are set on the upper part of the high-efficiency settling chamber, dust filter, circulation separation chamber and sealing chamber , the size is 300mm×200mm, the inclination angle and the horizontal direction are 15°~45°. 4.根据权利要求1或2所述的大倾角皮带机的除尘方法,其特征在于:循环分离室为顶板倾斜的喇叭形状,倾斜角度与水平方向为10°~30°,循环分离室的扩口端连接密封室,密封室的顶部垂悬有橡胶条。 4. The dust removal method of a large-inclination belt conveyor according to claim 1 or 2, characterized in that: the circulation separation chamber is in the shape of a trumpet with an inclined top plate, the inclination angle and the horizontal direction are 10° to 30°, and the expansion of the circulation separation chamber The mouth end is connected with a sealed chamber, and a rubber strip hangs from the top of the sealed chamber.
CN2011101889048A 2011-07-07 2011-07-07 Dust catcher for belt conveyor with large inclined angle Pending CN102390692A (en)

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Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1516721A (en) * 1974-07-05 1978-07-05 Donaldson Co Inc Air filter
US4486206A (en) * 1982-07-07 1984-12-04 Nippondenso Co., Ltd. Cyclone type air cleaner
CN201016072Y (en) * 2007-03-02 2008-02-06 无锡市华能电力机械有限公司 Dust collector for portable belt conveyer
CN101607258A (en) * 2009-07-13 2009-12-23 昆明冶金研究院 A dust removal method for coke transportation system
CN202156753U (en) * 2011-07-07 2012-03-07 昆明冶金研究院 Dust removal catcher of high-inclination angle belt conveyor

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
GB1516721A (en) * 1974-07-05 1978-07-05 Donaldson Co Inc Air filter
US4486206A (en) * 1982-07-07 1984-12-04 Nippondenso Co., Ltd. Cyclone type air cleaner
CN201016072Y (en) * 2007-03-02 2008-02-06 无锡市华能电力机械有限公司 Dust collector for portable belt conveyer
CN101607258A (en) * 2009-07-13 2009-12-23 昆明冶金研究院 A dust removal method for coke transportation system
CN202156753U (en) * 2011-07-07 2012-03-07 昆明冶金研究院 Dust removal catcher of high-inclination angle belt conveyor

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Application publication date: 20120328