CN203972090U - Pulverizer dedusting and clout reclaimer - Google Patents

Pulverizer dedusting and clout reclaimer Download PDF

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Publication number
CN203972090U
CN203972090U CN201420149115.2U CN201420149115U CN203972090U CN 203972090 U CN203972090 U CN 203972090U CN 201420149115 U CN201420149115 U CN 201420149115U CN 203972090 U CN203972090 U CN 203972090U
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China
Prior art keywords
conveyer
discharge pipe
communicated
pulverizer
dust collector
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Active
Application number
CN201420149115.2U
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Chinese (zh)
Inventor
宁纪宝
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Jiangxi kenai'er Agricultural Products Co. Ltd.
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QINGDAO CTC FEED CORP
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Priority to CN201420149115.2U priority Critical patent/CN203972090U/en
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Abstract

The utility model belongs to crushing material clout recovery technology field, specifically, relates to a kind of pulverizer dedusting and clout reclaimer.It comprises pulverizer and conveyer device', and pulverizer discharging opening place arranges the discharge pipe A that is communicated with conveyer device'; Also comprise cyclone dust collectors, pulse dust collector and negative-pressure air fan, wherein cyclone dust collectors top is communicated with conveyer device' by intake stack A, and cyclone dust collectors bottom discharge mouth is communicated with conveyer device' by discharge pipe B, and discharge pipe B is provided with wind stopping device A; Cyclone dust collectors top is communicated with the inlet scoop of pulse dust collector bottom by intake stack B, and pulse dust collector top is provided with negative-pressure air fan, and pulse dust collector bottom is communicated with conveyer device' by discharge pipe C, and discharge pipe C is provided with wind stopping device B.The utility model crush efficiency obviously improves; Reduce energy consumption and pulverize cost.

Description

Pulverizer dedusting and clout reclaimer
Technical field
The utility model belongs to crushing material clout recovery technology field, specifically, relates to a kind of pulverizer dedusting and clout reclaimer.
Background technology
For feed processing enterprise, apply maximum equipment and surely belong to disintegrating apparatus, any one all be unable to do without pulverizer miscellaneous, a large amount of dust and clout recovery technology that crushing process produces seem particularly important especially, not only can improve and maintain employee's operating environment, be more the material loss that can reduce crushing process, save and pulverize cost.And it is existing except dust recovery system is owing to being subject to the impact of the many factors such as design, efficiency and the Environmental-protecting dust-removing of large multiple enterprises crushing system all exist undesirable, do not reach to promote and control requirement, for the small enterprise a little less than technology relative thin, there is no especially fine solution, improve simply energy consumption, strengthen material loss and also make to pulverize environment and form especially vicious circle, this phenomenon is held and is treated that technological improvement solves.
Utility model content
For solving the problems of the technologies described above, the utility model proposes a kind of crush efficiency, efficiency of dust collection is high, the clout rate of recovery is high pulverizer dedusting and clout reclaimer of promoting.
The technical solution of the utility model is: a kind of pulverizer dedusting and clout reclaimer, comprise pulverizer and conveyer device&apos, and pulverizer discharging opening place arranges the discharge pipe A that is communicated with conveyer device' Also comprise cyclone dust collectors, pulse dust collector and negative-pressure air fan, wherein cyclone dust collectors top is communicated with conveyer device&apos by intake stack A, and cyclone dust collectors bottom discharge mouth is communicated with conveyer device&apos by discharge pipe B, and discharge pipe B is provided with wind stopping device A; Cyclone dust collectors top is communicated with the inlet scoop of pulse dust collector bottom by intake stack B, and pulse dust collector top is provided with negative-pressure air fan, and pulse dust collector bottom is communicated with conveyer device&apos by discharge pipe C, and discharge pipe C is provided with wind stopping device B.
The course of work of the present utility model is as follows:
Feeder is dosed in pulverizer, material passes through discharge pipe A blanking after crushed to conveyer device&apos, under the suction of negative-pressure air fan, intake stack A is drawn into the powder in conveyer device&apos in cyclone dust collectors, after cyclone dust collectors rough dusting, clout under Action of Gravity Field through discharge pipe B blanking to conveyer device&apos.Powder after cyclone dust collectors rough dusting used intake stack B to enter in pulse dust collector, and after final dusting, clout blanking is to conveyer device&apos.Cyclone dust collectors can suck the powder in conveyer device&apos in cyclone dust collectors fast, have improved the crush efficiency of pulverizer; Cyclone dust collectors can separated recycle more than 70% clout, and remainder is inhaled into high efficiency of dust collection under suction function pulse bag by pulse dust collector further adsorbs recovery, and total efficiency of dust collection can reach more than 95%.
The beneficial effects of the utility model are:
1, the utility model crush efficiency obviously improves; 2, the utility model has ensured pulverizing environment, farthest reduces energy consumption and pulverizes cost; 3, alleviate original operating pressure of pulse dust collector, made the regular maintenance of pulse dust collector clear up simple and fast more; 4, the few instant effect of the utility model one-time investment, moves automatically without manual operation.
Accompanying drawing explanation
Fig. 1 is structural representation of the present utility model.
Wherein, 1, pulverizer; 2, cyclone dust collectors; 3, pulse dust collector; 4, negative-pressure air fan; 5, feeder; 6, pulverizer; 7, granulator; 8, cooler B; 9, vibrosieve device; 10, feed bin; 11, deduster A; 12, deduster B; 13, wind stopping device A; 14, wind stopping device B; 15, conveying auger.
The specific embodiment
Below in conjunction with drawings and Examples, illustrate the utility model.
Embodiment 1:
As shown in Figure 1, the utility model comprises pulverizer 1 and conveyer device&apos 13, and pulverizer 1 discharging opening place arranges the discharge pipe A12 that is communicated with conveyer device&apos 13; Also comprise cyclone dust collectors 2, pulse dust collector 3 and negative-pressure air fan 4, wherein cyclone dust collectors 2 tops are communicated with conveyer device&apos 13 by intake stack A11, cyclone dust collectors 2 bottom discharge mouths are communicated with conveyer device&apos 13 by discharge pipe B10, and discharge pipe B10 is provided with wind stopping device A9; Cyclone dust collectors 2 tops are communicated with the inlet scoop of pulse dust collector 3 bottoms by intake stack B6, pulse dust collector 3 tops are provided with negative-pressure air fan 4, pulse dust collector 3 bottoms are communicated with conveyer device&apos 13 by discharge pipe C8, and discharge pipe C8 is provided with wind stopping device B7.Pulverizer 1 charging aperture place is provided with feeder 5.
The course of work of the present utility model is as follows:
Feeder 5 is dosed in pulverizer 1, material passes through discharge pipe A12 blanking after crushed to conveyer device&apos 13, under the suction of negative-pressure air fan 4, intake stack A11 is drawn into the powder in conveyer device&apos 13 in cyclone dust collectors 2, after cyclone dust collectors 2 rough dustings, clout under Action of Gravity Field through discharge pipe B10 blanking to conveyer device&apos 13.Powder after cyclone dust collectors 2 rough dustings used intake stack B6 to enter in pulse dust collector 3, and after final dusting, clout blanking is to conveyer device&apos 13.
The pulverizer of 6 tons of take is example, compared to existing technologies, after the utility model carries out the recovery of dedusting clout, the comprehensive crush efficiency of pulverizer obviously promotes 20% left and right, with load contrast power consumption, save 20-30%, clout yield obviously improves 15% on year-on-year basis, and equipment failure rate reduces by 30% left and right on year-on-year basis.

Claims (1)

1. pulverizer dedusting and a clout reclaimer, comprise pulverizer and conveyer device&apos, and pulverizer discharging opening place arranges the discharge pipe A that is communicated with conveyer device' It is characterized in that: also comprise cyclone dust collectors, pulse dust collector and negative-pressure air fan, wherein cyclone dust collectors top is communicated with conveyer device&apos by intake stack A, cyclone dust collectors bottom discharge mouth is communicated with conveyer device&apos by discharge pipe B, and discharge pipe B is provided with wind stopping device A; Cyclone dust collectors top is communicated with the inlet scoop of pulse dust collector bottom by intake stack B, and pulse dust collector top is provided with negative-pressure air fan, and pulse dust collector bottom is communicated with conveyer device&apos by discharge pipe C, and discharge pipe C is provided with wind stopping device B.
CN201420149115.2U 2014-03-28 2014-03-28 Pulverizer dedusting and clout reclaimer Active CN203972090U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201420149115.2U CN203972090U (en) 2014-03-28 2014-03-28 Pulverizer dedusting and clout reclaimer

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201420149115.2U CN203972090U (en) 2014-03-28 2014-03-28 Pulverizer dedusting and clout reclaimer

Publications (1)

Publication Number Publication Date
CN203972090U true CN203972090U (en) 2014-12-03

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Family Applications (1)

Application Number Title Priority Date Filing Date
CN201420149115.2U Active CN203972090U (en) 2014-03-28 2014-03-28 Pulverizer dedusting and clout reclaimer

Country Status (1)

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CN (1) CN203972090U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104728915A (en) * 2015-02-16 2015-06-24 哈尔滨工业大学 Energy-saving heated kang regeneration cyclic utilization system combusting straws

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN104728915A (en) * 2015-02-16 2015-06-24 哈尔滨工业大学 Energy-saving heated kang regeneration cyclic utilization system combusting straws

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Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
TR01 Transfer of patent right
TR01 Transfer of patent right

Effective date of registration: 20180615

Address after: 341699 navel orange industrial base, west of Xinfeng Industrial Park, Ganzhou, Jiangxi (range of farmer's spring)

Patentee after: Jiangxi kenai'er Agricultural Products Co. Ltd.

Address before: 266600 Beijing East Road, Laixi City, Qingdao, Shandong Province, No. 3

Patentee before: Qingdao Ke Naier feed corporation,Ltd