CN102862759B - Anti-blocking powder delivery device with vanes - Google Patents

Anti-blocking powder delivery device with vanes Download PDF

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Publication number
CN102862759B
CN102862759B CN201210205153.0A CN201210205153A CN102862759B CN 102862759 B CN102862759 B CN 102862759B CN 201210205153 A CN201210205153 A CN 201210205153A CN 102862759 B CN102862759 B CN 102862759B
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China
Prior art keywords
nozzle
blade
spraying equipment
equipment
jet
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Expired - Fee Related
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CN201210205153.0A
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Chinese (zh)
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CN102862759A (en
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程晓堂
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Shandong Plain Energy Saving Equipment Co Ltd
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Individual
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Abstract

A powder delivery device comprises at least one conical material hopper which comprises an upper feeding section and a lower feeding section. A spraying device and vanes are arranged on the lower feeding section, the spraying device is arranged under the vanes, a nozzle of the spraying device sprays gas toward the inner wall of the lower feeding section, and the vanes are connected with a rotating shaft and rotate through the rotating shaft. The anti-blocking powder delivery device improves anti-blocking efficiency and reduces energy consumption.

Description

The vaned anti-blocking powder load transfer device of tool
Technical field
The invention belongs to powder transportation art, be specifically related to a kind of powder load transfer device with choke preventing function, particularly a kind of powder load transfer device in the time carrying along gravitational field with choke preventing function.
Background technology
At present, in chemical industry, field of boilers, powder conveying is very general process, and wherein the vertical transport of powder is modal process.In general, carries in order to save energy along the powder of gravitational field, be all dependence gravity carry out powder freely decline carry.Powder load transfer device along gravitational field comprises at least one broach hopper, and this broach hopper comprises top material loading section and bottom blanking section.Although the outlet size of blanking section, much larger than the particle diameter of powder, still likely forms and builds bridge in the time of the discharge downwards of powder material entirety.This obstruction can cause the fault of load transfer device, and then has influence on the fault of whole system.The major cause resulting in blockage is such as having friction force between powder and equipment inner wall, has friction force etc. between powder.In order to prevent latch up phenomenon, corresponding anti-block apparatus must be set in load transfer device.
For many years, in order to solve blockage problem, developed vibration or beaten the methods such as inwall, rotation scraping inwall, gas injection inwall.200810140442.0 proposed the equipment of rotary conic hopper stationary blade, 201020262144.1 proposed the equipment of the fixing broach hopper of rotating blade, although these two kinds of equipment can reach the effect that prevents obstruction, but it is all higher that it prevents stopping up the energy consumption needing, still need a kind of powder load transfer device that prevents efficiently obstruction.
Summary of the invention
Blockage problem while conveying in order to solve powder material, the design people provides a kind of powder load transfer device and method with choke preventing function.
Powder load transfer device proposed by the invention, it comprises at least one broach hopper, this broach hopper comprises top material loading section and bottom blanking section, in bottom, blanking section has spraying equipment and blade, wherein spraying equipment is below blade, the nozzle of spraying equipment is subordinate's section of expecting inwall jet gas down, and blade is connected with S. A., rotates by S. A..
Wherein, spraying equipment is connected with S. A., and S. A. is hollow, for spraying equipment provides jet gas.
Wherein, upwards jet gas of the nozzle of spraying equipment.
Wherein, blade has the nozzle of subordinate's section of expecting inwall jet gas down.
Wherein, the nozzle Jet with downward flow direction gas on blade, nozzle and horizontal sextant angle 15-95 °, preferably 45-90 °, preferably 75 °.
Wherein, blade plan form can be in the shape of a spiral, straight tabular or swash plate shape.
Wherein, there is flow measurement at the outlet section of bottom blanking section.
The flow measuring when flow measurement drops to when a certain amount of, starts anti-blocking equipment, can only start spraying equipment, only start blade, also can start spraying equipment and blade simultaneously; In the time starting blade, the nozzle that can start blade also can not start the nozzle of blade.
The condition of startup is set according to the character of powder material, in general in the time that flow drops to the 80%-40% of normal discharge, starts anti-blocking equipment, reduction energy consumption that can maximal efficiency.Carry for power plant boiler fine coal, in general drop to 70% time startup of normal discharge when flow; And for the fly ash carry of flying dust treating system, in general when flow drop to normal discharge 50% time start.
This equipment is by two kinds of anti-block apparatus of nozzle and blade are set simultaneously, according to actual conditions select to start the two one of or start simultaneously, improved anti-blocking efficiency, reduced energy consumption.Judge stopping state by discharge measurement, select start anti-block apparatus suitable opportunity, improved anti-blocking efficiency, reduced energy consumption.Nozzle is set on blade, in rotation, sprays, improved anti-blocking efficiency, reduced energy consumption.The spray angle of adjusting blade top nozzle, has improved anti-blocking efficiency, has reduced energy consumption.
Brief description of the drawings
Fig. 1 represents the structural representation of this equipment.
Detailed description of the invention
This equipment is referring to Fig. 1.Its structure comprises: at least one broach hopper, this broach hopper comprises top material loading section 1 and bottom blanking section 2, there is spraying equipment 5 and blade 4 in bottom blanking section 2, wherein spraying equipment 5 is below blade 4, the nozzle of spraying equipment 5 is subordinate's section of expecting inwall jet gas down, blade 4 is connected with S. A. 3, rotates by S. A..Spraying equipment 5 is connected with S. A. 3, and S. A. 3 is hollow, for spraying equipment provides jet gas.Upwards jet gas of the nozzle of spraying equipment.Blade has the nozzle of subordinate's section of expecting inwall jet gas down.Nozzle Jet with downward flow direction gas on blade.Outlet section in bottom blanking section has flow measurement 6, and blade plan form is swash plate shape.
In the time of conveying powder material, flow measurement 6 measuring flows change, and when flow drops to when a certain amount of, start anti-block apparatus, can only start spraying equipment 5, only start blade 4, also can start spraying equipment 5 and blade 4 simultaneously; In the time starting blade 4, the nozzle that can start blade 4 also can not start the nozzle of blade 4, thereby prevents that efficiently powder material from stopping up.
Comparative example 1:
Structure and this equipment are similar, just there is no spraying equipment 5, taking fine coal as example, when flow drop to normal discharge 70% time start blade (not starting the nozzle of blade), measuring flow returns to 95% energy consumption of normal discharge.
Comparative example 2:
Structure is identical with comparative example 1, taking fine coal as example, when flow drop to normal discharge 70% time start blade and (start the nozzle of blade, the nozzle Jet with downward flow direction gas on blade simultaneously, 75 ° of nozzle and horizontal sextant angles), measuring flow returns to 95% energy consumption of normal discharge.
Comparative example 3:
Structure and this equipment are similar, just there is no blade 4, upwards jet gas of the nozzle of spraying equipment, 35 ° of nozzle and horizontal sextant angles, taking fine coal as example, when flow drop to normal discharge 70% time start spraying equipment 5, measuring flow returns to 95% energy consumption of normal discharge.
Embodiment 1:
Taking fine coal as example, when flow drop to normal discharge 70% time start spraying equipment 5 and blade 4 (not starting the nozzle of blade), upwards jet gas of the nozzle of spraying equipment, 35 ° of nozzle and horizontal sextant angles, measuring flow returns to 95% energy consumption of normal discharge.
Embodiment 2:
Taking fine coal as example, when flow drop to normal discharge 70% time start spraying equipment 5 and blade 4 (starts the nozzle of blade simultaneously, nozzle Jet with downward flow direction gas on blade, 75 ° of nozzle and horizontal sextant angles), upwards jet gas of the nozzle of spraying equipment, 35 ° of nozzle and horizontal sextant angles, measuring flow returns to 95% energy consumption of normal discharge.
Taking the energy consumption of comparative example 1 as 1, calculate the energy consumption of other comparative example and embodiment, in table 1.
Comparative example 1 Comparative example 2 Comparative example 3 Embodiment 1 Embodiment 2
Energy consumption 100% 95% 120% 85% 80%
As can be seen from the table, there is blade and spraying equipment simultaneously can reduce anti-blocking energy consumption.
Embodiment 3:
Taking fine coal as example, when flow drop to normal discharge 70% time start spraying equipment 5 and blade 4 (simultaneously starting the nozzle of blade), upwards jet gas of the nozzle of spraying equipment, 35 ° of nozzle and horizontal sextant angles, wherein, nozzle Jet with downward flow direction gas on blade, 15,35,55,75,95 ° of nozzle and horizontal sextant angles.Measuring flow returns to 95% energy consumption of normal discharge.
Taking the energy consumption of 15 ° of angles as 1, calculate the energy consumption of other angle, in table 2.
15° 35° 55° 75° 95°
Energy consumption 100% 95% 80% 75% 100%
As can be seen from the table, 75 ° have lowest energy consumption.
Embodiment 4:
Taking fine coal as example, when flow drop to normal discharge 40%, 50%, 60%, 70%, 80% time start spraying equipment 5 and blade 4 (simultaneously starting the nozzle of blade), upwards jet gas of the nozzle of spraying equipment, 35 ° of nozzle and horizontal sextant angles, wherein, nozzle Jet with downward flow direction gas on blade, 75 ° of nozzle and horizontal sextant angles, flow return to normal discharge 95% time close spraying equipment 5 and blade 4 (simultaneously closing the nozzle of blade), calculate the energy consumption of carrying the anti-blocking equipment of 10kg material.Energy consumption taking 40% is 1, calculates other energy consumption, in table 3.
40% 50% 60% 70% 80%
Energy consumption 100% 100% 95% 90% 100%
As can be seen from the table, start and there is lowest energy consumption 70% time.
Embodiment 5:
Similar to Example 5, just change fine coal into flying dust, the results are shown in Table 4.
40% 50% 60% 70% 80%
Energy consumption 100% 90% 95% 100% 100%
As can be seen from the table, start and there is lowest energy consumption 50% time.

Claims (5)

1. a powder load transfer device, it comprises at least one broach hopper, this broach hopper comprises top material loading section and bottom blanking section, in bottom, blanking section has spraying equipment and blade, wherein spraying equipment is below blade, the nozzle of spraying equipment is subordinate's section of expecting inwall jet gas down, blade is connected with S. A., rotate by S. A., upwards jet gas of the nozzle of spraying equipment, blade has the nozzle of subordinate's section of expecting inwall jet gas down, nozzle Jet with downward flow direction gas on blade, nozzle on described blade and horizontal sextant angle 15-95 °, outlet section in bottom blanking section has flow measurement.
2. equipment as claimed in claim 1, wherein spraying equipment is connected with S. A., and S. A. is hollow, for spraying equipment provides jet gas.
3. equipment as claimed in claim 1 or 2, the nozzle Jet with downward flow direction gas on its Leaf, the nozzle on described blade and horizontal sextant angle 45-90 °.
4. equipment as claimed in claim 1 or 2, the nozzle Jet with downward flow direction gas on its Leaf, 75 ° of the nozzle on described blade and horizontal sextant angles.
5. equipment as claimed in claim 1 or 2, wherein blade plan form in the shape of a spiral, straight tabular or swash plate shape.
CN201210205153.0A 2012-06-19 2012-06-19 Anti-blocking powder delivery device with vanes Expired - Fee Related CN102862759B (en)

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Application Number Priority Date Filing Date Title
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CN102862759B true CN102862759B (en) 2014-07-02

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Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3917126A (en) * 1974-07-16 1975-11-04 William H Beach Feeding device
SU979232A1 (en) * 1981-06-26 1982-12-07 Всесоюзный Научно-Исследовательский Институт Комбикормовой Промышленности Apparatus for unloading silos
JPS63274448A (en) * 1987-04-30 1988-11-11 Nitta Zerachin Kk Method of supplying powder
SU1454758A1 (en) * 1987-05-27 1989-01-30 Харьковский Институт Инженеров Железнодорожного Транспорта Им.С.М.Кирова Arrangement for caving-in bridges of loose material in hoppers
JP2005132528A (en) * 2003-10-29 2005-05-26 Hitachi Plant Eng & Constr Co Ltd Hopper device
CN201619816U (en) * 2010-02-02 2010-11-03 天华化工机械及自动化研究设计院 Ash discharge device for coal moisture control dry dust removing system
CN201785051U (en) * 2010-08-06 2011-04-06 天瑞集团水泥有限公司 Automatic detecting anti-blocking device of discharge bin
CN102431741A (en) * 2011-12-08 2012-05-02 新疆天物科技发展有限公司 Arch breaking device for material bin
CN202594184U (en) * 2012-06-19 2012-12-12 程晓堂 Anti-blocking powder conveying equipment with spraying equipment
CN202784422U (en) * 2012-06-19 2013-03-13 程晓堂 Anti-blocking powder conveying device
CN202848423U (en) * 2012-06-19 2013-04-03 程晓堂 Anti-blocking powder conveying device with blades and spraying device
CN202848420U (en) * 2012-06-19 2013-04-03 程晓堂 Anti-blocking powder conveying device with blades

Patent Citations (12)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3917126A (en) * 1974-07-16 1975-11-04 William H Beach Feeding device
SU979232A1 (en) * 1981-06-26 1982-12-07 Всесоюзный Научно-Исследовательский Институт Комбикормовой Промышленности Apparatus for unloading silos
JPS63274448A (en) * 1987-04-30 1988-11-11 Nitta Zerachin Kk Method of supplying powder
SU1454758A1 (en) * 1987-05-27 1989-01-30 Харьковский Институт Инженеров Железнодорожного Транспорта Им.С.М.Кирова Arrangement for caving-in bridges of loose material in hoppers
JP2005132528A (en) * 2003-10-29 2005-05-26 Hitachi Plant Eng & Constr Co Ltd Hopper device
CN201619816U (en) * 2010-02-02 2010-11-03 天华化工机械及自动化研究设计院 Ash discharge device for coal moisture control dry dust removing system
CN201785051U (en) * 2010-08-06 2011-04-06 天瑞集团水泥有限公司 Automatic detecting anti-blocking device of discharge bin
CN102431741A (en) * 2011-12-08 2012-05-02 新疆天物科技发展有限公司 Arch breaking device for material bin
CN202594184U (en) * 2012-06-19 2012-12-12 程晓堂 Anti-blocking powder conveying equipment with spraying equipment
CN202784422U (en) * 2012-06-19 2013-03-13 程晓堂 Anti-blocking powder conveying device
CN202848423U (en) * 2012-06-19 2013-04-03 程晓堂 Anti-blocking powder conveying device with blades and spraying device
CN202848420U (en) * 2012-06-19 2013-04-03 程晓堂 Anti-blocking powder conveying device with blades

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Owner name: SHANDONG PINGYUAN CHOOSUN ENERGY SAVING EQUIPMENT

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Effective date: 20140729

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Address after: 253100 Eastern District of Plain Economic Development Zone, Shandong

Patentee after: Shandong plain energy saving equipment Co., Ltd.

Address before: 100049 Beijing Fuxing Road, No. 36, building No. 1, building No. 1104, No.

Patentee before: Cheng Xiaotang

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Granted publication date: 20140702

Termination date: 20160619

CF01 Termination of patent right due to non-payment of annual fee