CN105920925A - Air-purifying and core cyclone separation device - Google Patents

Air-purifying and core cyclone separation device Download PDF

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Publication number
CN105920925A
CN105920925A CN201610410875.8A CN201610410875A CN105920925A CN 105920925 A CN105920925 A CN 105920925A CN 201610410875 A CN201610410875 A CN 201610410875A CN 105920925 A CN105920925 A CN 105920925A
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CN
China
Prior art keywords
core
cyclone
cyclone collector
core separator
separation device
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.)
Pending
Application number
CN201610410875.8A
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Chinese (zh)
Inventor
强光初
强小龙
范莉
倪升宏
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WUXI JONGOAL MACHINERY CO Ltd
Original Assignee
WUXI JONGOAL MACHINERY CO Ltd
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by WUXI JONGOAL MACHINERY CO Ltd filed Critical WUXI JONGOAL MACHINERY CO Ltd
Priority to CN201610410875.8A priority Critical patent/CN105920925A/en
Publication of CN105920925A publication Critical patent/CN105920925A/en
Pending legal-status Critical Current

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Classifications

    • BPERFORMING OPERATIONS; TRANSPORTING
    • B01PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01DSEPARATION
    • B01D45/00Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
    • B01D45/12Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces
    • B01D45/16Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by centrifugal forces generated by the winding course of the gas stream, the centrifugal forces being generated solely or partly by mechanical means, e.g. fixed swirl vanes

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  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Cyclones (AREA)

Abstract

The invention relates to an air-purifying core cyclone separation device. The air-purifying core cyclone separation device comprises a core separator, a fan and a cyclone collector, wherein the inlet end of the fan is used for sucking in dusty gas, the outlet end of the fan is connected with the inlet end of the core separator through a first pipeline, a first outlet end of the core separator is connected with the inlet end of the cyclone collector through a second pipeline, a clean airflow outlet for discharging purified gas is formed in the top center of the core separator, an ash hopper is arranged at the bottom of the cyclone collector, and the outlet end is arranged at the upper end of the cyclone collector and is connected with the inlet end of the fan through a third pipeline. The air-purifying core cyclone separation device has the advantages that the device is simple in structure, compact in design and convenient to use; airflow can be purified through coordination of the core separator and the cyclone collector, smoke carrying solid particles enables the particles to sedimentate in the cyclone collector and be discharged under the action of cyclone flow, the purified gas is discharged into air, and accordingly good smoke removal effects and high efficiency are achieved.

Description

Air purification core cyclone separation device
Technical field
The present invention relates to a kind of air purification core cyclone separation device, belong to mechanical equipment technical field.
Background technology
Treatment of Metal Surface, has traditional mechanical-physical derusting process, conventional employing bead and mechanical grinding.When using bead and mechanical grinding, producing the substantial amounts of contaminated air containing materials such as oxide, dust, oil, dusts, can not directly discharge because polluting the environment, it is therefore necessary to contaminated air is processed, reach discharge standard, protect environment.At present both at home and abroad above air-polluting processing mode is typically had following several ways: 1. cyclone dust removal, the most pocket type pulsed dedusting, 3. precipitation dedusting, 4. water mist sprinkling dedusting, 5. filter element filtering dedusting etc..The tradition general volume of air-polluting processing means is much bigger, the air-polluting treating capacity of reason is bigger, such as:. cyclone dust removal, good multiple stage must be had in parallel, sack cleaner, pocket type pulsed dedusting besides, volume is very big, general filter bag (100*2 rice) many at about 100, filter bag is easily-consumed products simultaneously, it is impossible to adapt to the gas that humidity is higher;Precipitation dedusting, machine volume is bigger, and general volume is at about 6~10 cubes;Water mist sprinkling dedusting, volume is more a little bit smaller than precipitation dedusting, but after the water of spray pollutes, it is necessary to carry out sewage disposal, increase operating cost;Filter element filtering dedusting, volume is the biggest, is particularly easy to pollute simultaneously, it is impossible to adapting to the gas that humidity is higher and solids content is higher, replacement frequency is higher, therefore can only be used in series with other low efficient filters.
Summary of the invention
Gas when the invention aims to solve to carry out Treatment of Metal Surface can not directly discharge the problem needing to purify, it is provided that a kind of simple in construction, air purification core cyclone separation device compact to design.
The present invention adopts the following technical scheme that a kind of air purification core cyclone separation device, including core separator, blower fan and cyclone collector, the entrance point of described blower fan is for the suction of dusty gas, the port of export of described blower fan is connected with the entrance point of core separator by the first pipeline, first port of export of described core separator is connected with the entrance point of cyclone collector by the second pipeline, the top of described core separator is provided centrally with for discharging the cleaning gas tream outlet purifying gas, the bottom of described cyclone collector is provided with ash bucket, the upper end of described cyclone collector is provided with the port of export, the port of export of described cyclone collector is connected with the entrance point of blower fan by the 3rd pipeline.
Further, the entrance point of described core separator is arranged at the bottom of core separator, and first port of export of described core separator is arranged at the top of core separator.
Further, the entrance point of described cyclone collector is arranged at the upper end of cyclone collector.
Further, described core separator is cylindrical.
Further, the volume ratio of described core separator and cyclone collector is 9~11:1, diameter 4~6:1, highly 4~6:1.
Further, the bottom of described core separator is provided with dust collection.
Present configuration is simple, compact to design, easy to use, core separator and cyclone collector with the use of can purifying gas flow, granule is deposited in cyclone collector under cyclonic action and discharges by the flue gas of solids laden, gas after cleaning is discharged in air, and the elimination effect of flue gas is good, and efficiency is high.
Accompanying drawing explanation
Fig. 1 is the structural representation of the present invention.
Reference: blower fan the 1, first pipeline 2, core separator the 3, second pipeline 4, cyclone collector 5, ash bucket 6, cleaning gas tream outlet the 7, the 3rd pipeline 8.
Detailed description of the invention
Below in conjunction with accompanying drawing, the invention will be further described.
nullAs shown in Figure 1,A kind of air purification core cyclone separation device,Including core separator 3、Blower fan 1 and cyclone collector 5,The entrance point of blower fan 1 is for the suction of dusty gas,The entrance point of core separator 3 is arranged at the bottom of core separator 3,The port of export of core separator 3 is arranged at the top of core separator 3,The port of export of blower fan 1 is connected with the entrance point of core separator 3 by the first pipeline 2,The port of export of core separator 3 is connected with the entrance point of cyclone collector 5 by the second pipeline 4,The entrance point of cyclone collector 5 is arranged at the upper end of cyclone collector 5,The top of core separator 3 is provided centrally with for discharging the cleaning gas tream outlet 7 purifying gas,The bottom of cyclone collector 5 is provided with ash bucket 6,The upper end of cyclone collector 5 is provided with the port of export,The port of export of cyclone collector 5 is connected with the entrance point of blower fan 1 by the 3rd pipeline 8,The volume ratio of core separator 3 and cyclone collector 5 is 10:1,Diameter 4~6:1,Highly 5:1,The bottom of core separator 3 is provided with dust collection.
nullOperation principle: dusty gas is entered by the entrance point of blower fan 1,The bottom of core separator 3 is entered by the first pipeline 2,Result due to swirling motion,The particulate matter in dusty gas in core separator 3 is shifted to periphery by centre,The cleaned air-flow of gas of cleaning goes out 7 mouthfuls of discharges,Partial particulate is collected in the dust collection to core separator,Carry the gas of partial particulate thing and enter in cyclone collector 5 to perimeter and through outlet and second pipeline 4 of core separator 3,Partial particulate thing is deposited in cyclone collector 5 by the gas with particulate matter,Particulate matter is discharged by the ash bucket 6 bottom cyclone collector 5,Particulate matter in cyclone collector 5 continues back in core separator 3 under the effect of Secondary Flow,The efficiency of core separator 3 is sufficiently large,Continue cycling through and make particulate matter enter cyclone collector 5,Until particulate matter deposition is discharged by cyclone collector 5,Portion gas in cyclone collector 5 is connected with the entrance point of blower fan 1 through the 3rd pipeline 8 by the port of export of cyclone collector 5,Realize the circular treatment of gas,Until needing dusty gas to be processed to be referred to as pure air discharge.

Claims (6)

  1. null1. an air purification core cyclone separation device,It is characterized in that: include core separator (3)、Blower fan (1) and cyclone collector (5),The entrance point of described blower fan (1) is for the suction of dusty gas,The port of export of described blower fan (1) is connected by the entrance point of the first pipeline (2) with core separator (3),The port of export of described core separator (3) is connected by the entrance point of the second pipeline (4) with cyclone collector (5),The top of described core separator (3) is provided centrally with for discharging cleaning gas tream outlet (7) purifying gas,The bottom of described cyclone collector (5) is provided with ash bucket (6),The upper end of described cyclone collector (5) is provided with the port of export,The port of export of described cyclone collector (5) is connected with the entrance point of blower fan (1) by the 3rd pipeline (8).
  2. 2. air purification core cyclone separation device as claimed in claim 1, it is characterized in that: the entrance point of described core separator (3) is arranged at the bottom of core separator (3), the port of export of described core separator (3) is arranged at the top of core separator (3).
  3. 3. air purification core cyclone separation device as claimed in claim 1, it is characterised in that: (5) entrance point of described cyclone collector is arranged at the upper end of cyclone collector (5).
  4. 4. air purification core cyclone separation device as claimed in claim 1, it is characterised in that: described core separator (3) is cylindrical.
  5. 5. air purification core cyclone separation device as claimed in claim 1, it is characterised in that: the volume ratio of described core separator (3) and cyclone collector (5) is 9~11:1, diameter 4~6:1, highly 4~6:1.
  6. 6. air purification core cyclone separation device as claimed in claim 1, it is characterised in that: the bottom of described core separator (3) is provided with dust collection.
CN201610410875.8A 2016-06-13 2016-06-13 Air-purifying and core cyclone separation device Pending CN105920925A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201610410875.8A CN105920925A (en) 2016-06-13 2016-06-13 Air-purifying and core cyclone separation device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201610410875.8A CN105920925A (en) 2016-06-13 2016-06-13 Air-purifying and core cyclone separation device

Publications (1)

Publication Number Publication Date
CN105920925A true CN105920925A (en) 2016-09-07

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Country Status (1)

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CN (1) CN105920925A (en)

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106733248A (en) * 2017-03-07 2017-05-31 深圳市旋风流体科技有限公司 Aerodynamic particle separator
CN112337195A (en) * 2019-08-07 2021-02-09 耐驰干法研磨技术有限公司 Separator with partial filter
CN113171656A (en) * 2021-05-17 2021-07-27 徐州博源科技有限公司 Inertial pressure difference dust removal purification unit

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003053544A2 (en) * 2001-12-07 2003-07-03 O.P.M. Holdings, Inc. Airborne particle removal system
CN102580409A (en) * 2012-03-14 2012-07-18 无锡光初科技服务有限公司 Surface engineering rust removal air purification core separation system
CN202983406U (en) * 2012-12-18 2013-06-12 中国石油大学(北京) Pre-separating device used for high-temperature gas filter and filter thereof
CN103611368A (en) * 2013-12-04 2014-03-05 北京京能电力股份有限公司石景山热电厂 Denitrification hot air dust removal device and method
CN203540225U (en) * 2013-11-11 2014-04-16 陕西理工学院 Indoor air purifying integrated device

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
WO2003053544A2 (en) * 2001-12-07 2003-07-03 O.P.M. Holdings, Inc. Airborne particle removal system
CN102580409A (en) * 2012-03-14 2012-07-18 无锡光初科技服务有限公司 Surface engineering rust removal air purification core separation system
CN202983406U (en) * 2012-12-18 2013-06-12 中国石油大学(北京) Pre-separating device used for high-temperature gas filter and filter thereof
CN203540225U (en) * 2013-11-11 2014-04-16 陕西理工学院 Indoor air purifying integrated device
CN103611368A (en) * 2013-12-04 2014-03-05 北京京能电力股份有限公司石景山热电厂 Denitrification hot air dust removal device and method

Cited By (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN106733248A (en) * 2017-03-07 2017-05-31 深圳市旋风流体科技有限公司 Aerodynamic particle separator
CN106733248B (en) * 2017-03-07 2022-08-16 深圳市旋风流体科技有限公司 Pneumatic particle separator
CN112337195A (en) * 2019-08-07 2021-02-09 耐驰干法研磨技术有限公司 Separator with partial filter
CN113171656A (en) * 2021-05-17 2021-07-27 徐州博源科技有限公司 Inertial pressure difference dust removal purification unit

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Application publication date: 20160907

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