CN105536359A - High-efficiency gravity dust remover - Google Patents

High-efficiency gravity dust remover Download PDF

Info

Publication number
CN105536359A
CN105536359A CN201510919215.8A CN201510919215A CN105536359A CN 105536359 A CN105536359 A CN 105536359A CN 201510919215 A CN201510919215 A CN 201510919215A CN 105536359 A CN105536359 A CN 105536359A
Authority
CN
China
Prior art keywords
lower cone
air intake
intake branch
upper shell
pipe
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.)
Granted
Application number
CN201510919215.8A
Other languages
Chinese (zh)
Other versions
CN105536359B (en
Inventor
靳继宝
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.)
Huatian Engineering and Technology Corp MCC
Original Assignee
NANJING INDUSTRIAL FURNACE Co Ltd HTC
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 NANJING INDUSTRIAL FURNACE Co Ltd HTC filed Critical NANJING INDUSTRIAL FURNACE Co Ltd HTC
Priority to CN201510919215.8A priority Critical patent/CN105536359B/en
Publication of CN105536359A publication Critical patent/CN105536359A/en
Application granted granted Critical
Publication of CN105536359B publication Critical patent/CN105536359B/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

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
    • B01D45/02Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising gravity
    • 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
    • B01D45/04Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
    • CCHEMISTRY; METALLURGY
    • C21METALLURGY OF IRON
    • C21BMANUFACTURE OF IRON OR STEEL
    • C21B7/00Blast furnaces
    • C21B7/22Dust arresters

Landscapes

  • Chemical & Material Sciences (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • Engineering & Computer Science (AREA)
  • Manufacturing & Machinery (AREA)
  • Materials Engineering (AREA)
  • Metallurgy (AREA)
  • Organic Chemistry (AREA)
  • Cyclones (AREA)

Abstract

The invention discloses a high-efficiency gravity dust remover, mainly aims at the problem that a gravity dust remover of the prior art cannot meet the needs of dust removal of blast furnace coal gas, and provides the high-efficiency gravity dust remover which comprises a dust remover shell body, a gas inlet pipe and a gas outlet pipe; the dust remover shell body comprises an upper cylinder body and a lower cone; the lower part of the upper cylinder body is arranged inside the lower cone, and the upper part of the upper cylinder body is arranged outside the lower cone; the gas inlet pipe comprises a gas inlet header pipe and at least one gas inlet branched pipe, the gas inlet header pipe is connected with the upper cylinder body, one end of the gas inlet branched pipe communicates with the gas inlet header pipe, the other end of the gas inlet branched pipe communicates with the lower cone, and the gas inlet branched pipe eccentrically communicates with the lower cone; the gas outlet pipe communicates with the upper part of the lower cone, and the height of the connection part of the gas outlet pipe and the lower cone is higher than that of the bottom of the upper cylinder body. The dust removing effect of the gravity dust remover is improved, and small-size dust particles can be smoothly settled.

Description

High efficiency gravitational precipitator
Technical field
The present invention relates to a kind of gravitational precipitator, specifically a kind of high efficiency gravitational precipitator.
Background technology
Modern ironmaking production almost all uses blast furnace, the course of work of blast furnace is as follows: the ore processed through processing, coke and flux are loaded by furnace roof according to a certain ratio in batches, hot blast blasts in stove by bottom house, with coke before air port of burning, make in stove, series of physical chemical reaction occur and produce molten iron.In blast furnace ironmaking process, due to the burning of coke and the generation of series of physical chemical reaction, inevitably produce a large amount of dust-laden gas-blast furnace gas.Along with improving constantly of twenties Nian Lai China rapid developments of economy and living standards of the people, the demand of ferrous materials is also constantly increased.And along with the increase of iron and steel production capacity, pollutant discharge amount sharply rises, consequent problem of environmental pollution, oneself further develops through becoming restriction China economy and society the big factors improved further with people's lives and the general level of the health.
In order to the environmental problem that the discharge reduced due to blast furnace gas causes, the dedusting of blast furnace gas process that must will draw in blast furnace, the dust in removing blast furnace gas.The gravitational precipitator ubiquity that at present each factory uses that structure is single, the position of gas inlet is reasonable not, and the flowing of air-flow in inside is abundant not, cannot make the dust granules defect such as sedimentation effectively.Along with dilatation and the transformation of iron and steel enterprise's blast furnace, original blast-furnace gas dedusting system can not meet dust removal requirement, therefore to the renewal of dust pelletizing system or transformation extremely urgent.
Summary of the invention
For the problems referred to above, the invention provides a kind of high efficiency gravitational precipitator, improve the efficiency of dust collection of gravitational precipitator.
For achieving the above object, high efficiency gravitational precipitator of the present invention comprises shell of dust remover, air inlet pipe and escape pipe; Described dedusting housing comprises upper shell and lower cone, and described upper shell bottom is arranged on lower cone inside, and described upper shell top is arranged on lower cone outside; Described air inlet pipe comprises inlet manifold and at least one air intake branch, described inlet manifold is connected with described upper shell, described air intake branch one end is communicated with described inlet manifold, and the described air intake branch other end is communicated with described lower cone, and described air intake branch is communicated with described lower cone bias; Described escape pipe is communicated with the top of described lower cone, and the mouth of pipe height of described escape pipe and described lower cone junction is higher than the bottom height of described upper shell.
Further, described air intake branch comprises changeover portion and eddy flow section, and described eddy flow section diameter is less than the diameter of described changeover portion, and described eddy flow section is connected with described lower cone, and described changeover portion is connected with described inlet manifold.
Particularly, described air intake branch eddy flow section is horizontally disposed with.
Further, the bottom side height of described air intake branch is not less than the bottom height of described upper shell.
Particularly, the axis of described air intake branch and described lower cone junction is air inlet axis, the intersection point of described air inlet axis and described lower cone inwall is air inlet radius to the distance of lower cone axis, the distance of described air inlet axis and described upper shell axis is greater than described upper shell and described air intake branch radius sum, is less than the difference of described air inlet radius and described air intake branch radius.
Further, described air inlet pipe comprises two air intake branches, and described two air intake branches respectively both sides relative to described lower cone are communicated with, and the gas cyclone direction entering described lower cone from two air intake branches is identical.
High efficiency gravitational precipitator of the present invention draws arm in the inlet manifold of gravitational precipitator, crossflow is formed in deduster lower cone, the horizontal of air-flow blows the interaction strengthening particle and particle, particle and wall, not only can significantly improve the efficiency of dust collection of deduster, can also make tiny grit also can be clear smoothly.Air-flow forms swirling eddy in uphill process, thus extends the time of staying of air-flow at gravitational precipitator, and particle speed can decline gradually, moves, facilitate the gas solid separation of gravitational precipitator under the effect of gravity and inertia bottom deduster.
Accompanying drawing explanation
Fig. 1 is the structural representation of high efficiency gravitational precipitator of the present invention;
Fig. 2 is the structural representation that high efficiency gravitational precipitator of the present invention is provided with two air intake branches.
Detailed description of the invention
Below in conjunction with Figure of description, the present invention will be further described.
Embodiment 1
As shown in Figure 1, the high efficiency gravitational precipitator of the present embodiment comprises shell of dust remover, air inlet pipe and escape pipe 6; Described dedusting housing comprises upper shell 1 and lower cone 2, and it is inner that described upper shell 1 bottom is arranged on lower cone 2, and it is outside that described upper shell 1 top is arranged on lower cone 2; Described air inlet pipe comprises inlet manifold 3 and air intake branch 4, described inlet manifold 3 is connected with described upper shell 1, described air intake branch 4 one end is communicated with described inlet manifold 3, and described air intake branch 4 other end is communicated with described lower cone 2, and described air intake branch 4 is communicated with described lower cone 2 bias; Described escape pipe 6 is communicated with the top of described lower cone 2, and the height of described escape pipe 6 and described lower cone 2 junction is higher than the bottom of described upper shell 1.
The present embodiment high efficiency gravitational precipitator draws air intake arm from air intake house steward, crossflow is formed in deduster lower cone 2, the horizontal of air-flow blows the interaction strengthening particle and particle, particle and wall, not only can significantly improve the efficiency of dust collection of deduster, can also make tiny grit also can be clear smoothly.Because air intake branch 4 is communicated with lower cone 2 bias, horizontal blowing gas stream can make air-flow form swirling eddy in uphill process, thus extend the time of staying of air-flow at gravitational precipitator, particle speed can decline gradually, move bottom deduster under the effect of gravity and inertia, facilitate the gas solid separation of gravitational precipitator.
Embodiment 2
On the basis of above-described embodiment, as shown in Figure 2, described air intake branch 4 comprises changeover portion and eddy flow section, and described eddy flow section diameter is less than the diameter of described changeover portion, and described eddy flow section is connected with described lower cone 2, and described changeover portion is connected with described inlet manifold 3.Described air intake branch 4 eddy flow section is horizontally disposed with.
Described air intake branch 4 is carried out reducing in exit by the present embodiment, pipe diameter is reduced, thus adds the speed of air intake branch 4 in exit, make the air-flow of rising form swirling eddy, the time of staying of air-flow in gravitational precipitator can be extended further, strengthen dust removing effects.Due to the lifting of crossflow flowing velocity, the collision effect of grit and grit, grit and wall in air is strengthened, thus the effect of settling to tiny grit can be strengthened.Simultaneously, air inlet pipe eddy flow section is horizontally disposed with, and makes the rotary thrust of formation level in lower cone 2, can not produce extra thrust up or down, also grit would not be disturbed due to the normal sedimentation of inertia and gravity, in gas uphill process, just extend the time that it rises.
Embodiment 3
As shown in Figure 2, the high efficiency gravitational precipitator of the present embodiment comprises shell of dust remover, air inlet pipe and escape pipe 6; Described dedusting housing comprises upper shell 1 and lower cone 2, and it is inner that described upper shell 1 bottom is arranged on lower cone 2, and it is outside that described upper shell 1 top is arranged on lower cone 2; Described air inlet pipe comprises inlet manifold 3 and two air intake branches 4,5, described inlet manifold 3 is connected with described upper shell 1, described two air intake branches 4,5 one end is communicated with described inlet manifold 3, described two air intake branches 4,5 other end is communicated with the described relative both sides of lower cone 2 respectively, described air intake branch 4,5 is communicated with described lower cone 2 bias, and the gas cyclone direction entering described lower cone 2 from two air intake branches 4,5 is identical; Described escape pipe 6 is communicated with the top of described lower cone 2, and the height of described escape pipe 6 and described lower cone 2 junction is higher than the bottom of described upper shell 1.
The high efficiency gravitational precipitator of the present embodiment arranges air intake arm in the relative both sides of lower cone 2, can form stronger swirling eddy, make dust removing effects better.
Embodiment 4
On the basis of above-described embodiment, the bottom side height of described air intake branch 4 is not less than the bottom height of described upper shell 1.Described air intake branch 4 is air inlet axis with the axis of described lower cone 2 junction, the intersection point of described air inlet axis and described lower cone 2 inwall is air inlet radius to the distance of lower cone 2 axis, the distance of described air inlet axis and described upper shell 1 axis is greater than described upper shell 1 and described air intake branch 4 radius sum, is less than the difference of described air inlet radius and described air intake branch 4 radius.
The high efficiency gravitational precipitator of the present embodiment makes the air-flow of air intake branch 4 derive along in the annulus between described upper shell 1 and lower cone 2, more easily form swirling eddy, simultaneously, the restriction of the spacing of air intake branch 4 and lower cone 2 axis can make the air current flow direction of air inlet pipe towards in the space between upper shell 1 and lower cone 2, the inwall of the outer wall or lower cone 2 that avoid upper shell 1 is to the stop of air-flow, the choosing that can form shape good turns air-flow, makes dust removing effects better.
Above; be only preferred embodiment of the present invention, but protection scope of the present invention is not limited thereto, is anyly familiar with those skilled in the art in the technical scope that the present invention discloses; the change that can expect easily or replacement, all should be encompassed within protection scope of the present invention.Therefore, the protection domain that protection scope of the present invention should define with claim is as the criterion.

Claims (6)

1. a high efficiency gravitational precipitator, is characterized in that: comprise shell of dust remover, air inlet pipe and escape pipe; Described dedusting housing comprises upper shell and lower cone, and described upper shell bottom is arranged on lower cone inside, and described upper shell top is arranged on lower cone outside; Described air inlet pipe comprises inlet manifold and at least one air intake branch, described inlet manifold is connected with described upper shell, described air intake branch one end is communicated with described inlet manifold, and the described air intake branch other end is communicated with described lower cone, and described air intake branch is communicated with described lower cone bias; Described escape pipe is communicated with the top of described lower cone, and the height of described escape pipe and described lower cone junction is higher than the bottom height of described upper shell.
2. high efficiency gravitational precipitator as claimed in claim 1, it is characterized in that: described air intake branch comprises changeover portion and eddy flow section, described eddy flow section diameter is less than the diameter of described changeover portion, and described eddy flow section is connected with described lower cone, and described changeover portion is connected with described inlet manifold.
3. high efficiency gravitational precipitator as claimed in claim 1, is characterized in that: the bottom side height of described air intake branch is not less than the bottom height of described upper shell.
4. high efficiency gravitational precipitator as claimed in claim 1, it is characterized in that: described air inlet pipe comprises two air intake branches, described two air intake branches respectively both sides relative to described lower cone are communicated with, and the gas cyclone direction entering described lower cone from two air intake branches is identical.
5. high efficiency gravitational precipitator as claimed in claim 2, is characterized in that: described air intake branch eddy flow section is horizontally disposed with.
6. high efficiency gravitational precipitator as claimed in claim 3, it is characterized in that: the axis of described air intake branch and described lower cone junction is air inlet axis, the intersection point of described air inlet axis and described lower cone inwall is air inlet radius to the distance of lower cone axis, the distance of described air inlet axis and described upper shell axis is greater than described upper shell and described air intake branch radius sum, is less than the difference of described air inlet radius and described air intake branch radius.
CN201510919215.8A 2015-12-11 2015-12-11 High efficiency gravitational precipitator Active CN105536359B (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510919215.8A CN105536359B (en) 2015-12-11 2015-12-11 High efficiency gravitational precipitator

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201510919215.8A CN105536359B (en) 2015-12-11 2015-12-11 High efficiency gravitational precipitator

Publications (2)

Publication Number Publication Date
CN105536359A true CN105536359A (en) 2016-05-04
CN105536359B CN105536359B (en) 2018-03-02

Family

ID=55816209

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201510919215.8A Active CN105536359B (en) 2015-12-11 2015-12-11 High efficiency gravitational precipitator

Country Status (1)

Country Link
CN (1) CN105536359B (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113304557A (en) * 2021-04-30 2021-08-27 成都易态科技有限公司 Dust removal system and dust removal method for primary flue gas of converter steelmaking

Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04298278A (en) * 1991-03-27 1992-10-22 Kawasaki Steel Corp Treatment of blast furnace dust
CN2763284Y (en) * 2004-12-28 2006-03-08 首钢总公司 Gravity type dust collector for blast-furnace gas
CN2791061Y (en) * 2005-01-18 2006-06-28 赵正清 Dust collector for blast furnace
CN103933786A (en) * 2014-04-04 2014-07-23 莱芜钢铁集团有限公司 Gravity dust collector
CN205199137U (en) * 2015-12-11 2016-05-04 中冶华天南京工业炉有限公司 High efficiency gravitational precipitator

Patent Citations (5)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH04298278A (en) * 1991-03-27 1992-10-22 Kawasaki Steel Corp Treatment of blast furnace dust
CN2763284Y (en) * 2004-12-28 2006-03-08 首钢总公司 Gravity type dust collector for blast-furnace gas
CN2791061Y (en) * 2005-01-18 2006-06-28 赵正清 Dust collector for blast furnace
CN103933786A (en) * 2014-04-04 2014-07-23 莱芜钢铁集团有限公司 Gravity dust collector
CN205199137U (en) * 2015-12-11 2016-05-04 中冶华天南京工业炉有限公司 High efficiency gravitational precipitator

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
王纯等: "《除尘设备手册》", 30 September 2009, 北京:化学工业出版社 *

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN113304557A (en) * 2021-04-30 2021-08-27 成都易态科技有限公司 Dust removal system and dust removal method for primary flue gas of converter steelmaking

Also Published As

Publication number Publication date
CN105536359B (en) 2018-03-02

Similar Documents

Publication Publication Date Title
CN202270591U (en) Horizontal gas-solid cyclone separator
CN101721175B (en) Bag type dust collector with novel air inlet mode and airflow distribution structure
CN205199137U (en) High efficiency gravitational precipitator
CN202667015U (en) Cyclone dust extractor with continuous spiral ribs on inner wall
CN105536359A (en) High-efficiency gravity dust remover
CN201558749U (en) Cyclone dust collector
CN201371085Y (en) Cyclone separation dust removing device
CN203208804U (en) Inertial dust separator
CN201543343U (en) Bag type dust collector with novel gas intake mode and novel airflow distribution structure
CN203610225U (en) Cyclone separator provided with double inlets and double outlets
CN202087436U (en) Core separating type cyclone dust collector
CN202823659U (en) Flow cutting cyclone dust collector and shaft furnace gas purifying system comprising the same
CN200991618Y (en) Coke-powder purifying dust collector
CN2791061Y (en) Dust collector for blast furnace
CN204224624U (en) The thick collection device of a kind of blast furnace gas dust
CN202667013U (en) Cyclone dust extractor capable of changing gas flow state
CN208389565U (en) Blast furnace Environmental-protection dust removal device
CN215940322U (en) Cyclone dust collector
CN202876949U (en) Multistage efficient magnetic separation device for magnetite
CN214599813U (en) Low-resistance high-efficiency cyclone separator
CN203030149U (en) Dust collection and desulphurization device for cupola
CN202621317U (en) Raw coke oven gas swirl dust remover of blast furnace
CN204514084U (en) The intelligence filter cinder structure of hot air duct on cement producing line
CN202191969U (en) Cyclone dust collector
CN202355942U (en) Centrifugal type dust collecting device

Legal Events

Date Code Title Description
C06 Publication
PB01 Publication
C10 Entry into substantive examination
SE01 Entry into force of request for substantive examination
C41 Transfer of patent application or patent right or utility model
TA01 Transfer of patent application right

Effective date of registration: 20161213

Address after: 243005 Hunan West Road, Anhui, China, No. 699, No.

Applicant after: Huatian Engineering & Technology Corporation, MCC

Address before: Jianye District of Nanjing City, Jiangsu province 210019 the Fuchun River Street No. 18

Applicant before: Nanjing Industrial Furnace Co., Ltd., HTC

GR01 Patent grant
GR01 Patent grant