CN201304305Y - Dust remover blowing pipe structure - Google Patents

Dust remover blowing pipe structure Download PDF

Info

Publication number
CN201304305Y
CN201304305Y CNU2008201782449U CN200820178244U CN201304305Y CN 201304305 Y CN201304305 Y CN 201304305Y CN U2008201782449 U CNU2008201782449 U CN U2008201782449U CN 200820178244 U CN200820178244 U CN 200820178244U CN 201304305 Y CN201304305 Y CN 201304305Y
Authority
CN
China
Prior art keywords
blowing
winding
pipe
nozzle
filter bag
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.)
Expired - Fee Related
Application number
CNU2008201782449U
Other languages
Chinese (zh)
Inventor
宋正兴
陈砚雄
刘立平
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.)
JIANGSU YIJIN ENVIRONMENTAL PROTECTION EQUIPMENT ENGINEERING CO., LTD.
Original Assignee
Jiangsu Yijin Environmental Protection Equipment Engineering 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 Jiangsu Yijin Environmental Protection Equipment Engineering Co Ltd filed Critical Jiangsu Yijin Environmental Protection Equipment Engineering Co Ltd
Priority to CNU2008201782449U priority Critical patent/CN201304305Y/en
Application granted granted Critical
Publication of CN201304305Y publication Critical patent/CN201304305Y/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Filtering Of Dispersed Particles In Gases (AREA)

Abstract

The utility model discloses a dust remover blowing pipe structure which includes a dust remover blowing pipe, a front end of the blowing pipe is an air inlet, a back end is a fixing end, a plurality of nozzles are placed on the blowing pipe, each nozzle is equipped with a blowing short pipe, the blowing short pipe is an equal Length short pipe, a group of filtering bag group is installed plumb in the face of the blowing short pipe port, the filtering bag group top is a pattern board; the blowing pipe is divided into a blowing front part and a blowing back part, sum of all nozzles diameter is 60-80% of the blowing pipe inner diameter, the nozzle diameter of the blowing front part is less 1mm than the blowing back part nozzle which can ensure the compress air flow sprayed from the blowing pipe back nozzle group having same blowing pressure with the compress air flow sprayed from the blowing pipe front part nozzle group, accordingly, the best dust removing effect of the blowing system can be ensured.

Description

Dust remover blowing pipe structure
Technical field
The utility model relates to a kind of deduster structure, particularly a kind of deduster winding-up tubular construction.
Background technology
Injection pipe of deduster arrangement of nozzles and winding-up short tube are the keys that guarantees that can injection system carry out normal deashing work apart from the control of card height.
The layout of nozzle is wished to reach compressed air stream that injection tube posterior nozzle group ejects and is jetted the compressed air stream that at almost identical jetting pressure with the anterior nozzle group of injection tube.
The winding-up short tube guarantees that apart from the height hope of card the original air-flow of diffusion enters filter pocket mouths together with the air-flow while supersonic speed of inducing.The air-flow moment that enters filter bag blows to the filter bag bottom, forms certain pressure in the filter bag bottom.Then, the air-flow recoil is upwards sharply expanded in filter bag, shakes off covering the dust stratification at the filter bag outer surface.
Jetting pressure is more big, and air-flow is just more little along the diffusion angle of winding-up axis, and the height of winding-up short tube end face distance card just can strengthen, and induces more air-flows, the more filter bag of jetting; Otherwise jetting pressure is more little, and air-flow is just more big along the diffusion angle of winding-up axis, and the height of winding-up short tube end face distance card just need to reduce, and induced draft reduces relatively, and the quantity of winding-up filter bag reduces.
And existing dust remover blowing pipe structure all fails to realize above-mentioned perfect condition.
The utility model content
The utility model technical issues that need to address just are to overcome the defective of prior art, a kind of deduster winding-up tubular construction is provided, it can guarantee that the compressed air stream that ejects from winding-up pipe posterior nozzle group jets the compressed air stream that under jetting pressure much at one with the anterior nozzle group of winding-up pipe, and can guarantee the original air-flow that spreads together with the air-flow of inducing simultaneously supersonic speed enter filter pocket mouths.The air-flow moment that enters filter bag blows to the filter bag bottom, forms certain pressure in the filter bag bottom.Then, the air-flow recoil is upwards sharply expanded in filter bag, shakes off covering the dust stratification at the filter bag outer surface.Guarantee the best ash-removal effect of injection system.
For solving the problems of the technologies described above, the utility model adopts following technical scheme:
A kind of dust remover blowing pipe structure of the utility model, comprise injection pipe of deduster, described injection tube front end is air inlet, the rear end is stiff end, be furnished with a plurality of nozzles on the described injection tube, a winding-up short tube is installed on each nozzle, described winding-up short tube is the equal length short tube, over against winding-up short tube mouth one group of filter bag group is installed, described filter bag group end face is card; Described injection tube is divided into the anterior and winding-up rear portion of winding-up, and the diameter sum of all nozzles is 60~80% of injection tube internal diameter on the injection tube, and the nozzle direct little 1mm of anterior nozzle diameter than the winding-up rear portion jets.
Described winding-up short tube mouth is 160mm-180mm apart from the height of card.
Under the state of middle pressure (0.3MPa-0.5MPa) winding-up, injection tube is divided into the anterior and winding-up rear portion of winding-up, the nozzle diameter of injection tube front portion is dmm, the nozzle diameter at injection tube rear portion is (d-1) mm, and all nozzle diameter sums should be 60~80% of injection tube internal diameter on the injection tube.When compressed air stream enters injection tube along the winding-up mouth of pipe like this, near anterior large-minded, the mouth mouth is corresponding big, the closer to the injection tube rear portion, throughput is more less than normal, need that jet hole is corresponding to be reduced, jet the compressed air stream that with the compressed air stream that guarantees to eject from the posterior nozzle group under almost identical jetting pressure with the anterior nozzle group of injection tube, guarantee the best ash-removal effect of injection system.
Winding-up short tube mouth is also very important apart from the control of card height.The height of winding-up short tube end face distance card is subjected to air-flow to become the impact of 20 ° of angles and chain induction air quantity along the winding-up axis.In theory, chain induction tolerance is The more the better, just strengthens the winding-up short tube apart from the height of card.But height can not unrestrictedly be raised, and air-flow becomes the phenomenon of 20 ° of angular spread to be doomed that it can only be a definite value along the winding-up axis.This value can guarantee that just the original air-flow of diffusion enters filter pocket mouths together with the air-flow while supersonic speed of inducing.The air-flow moment that enters filter bag blows to the filter bag bottom, forms certain pressure in the filter bag bottom.Then, the air-flow recoil is upwards sharply expanded in filter bag, shakes off covering the dust stratification at the filter bag outer surface.
According to using the CAD Simulation result on computers, under the jetting pressure of 0.3Mpa, 3 cun pulse valves winding-up specification is 150 * 7100 filter bag, and it highly is: H=160mm; The filter bag of winding-up 160 * 7100, it highly is: H=180mm.
In fact, jetting pressure is more big, and air-flow is just more little along the diffusion angle of winding-up axis, and the height of winding-up short tube end face distance card just can strengthen, and induces more air-flows, the more filter bag of jetting; Otherwise jetting pressure is more little, and air-flow is just more big along the diffusion angle of winding-up axis, and the height of winding-up short tube end face distance card just need to reduce, and induced draft reduces relatively, and the quantity of winding-up filter bag reduces.
Description of drawings
Fig. 1 is the utility model structural representation.
The specific embodiment
For making the purpose of this utility model, technical scheme and advantage clearer, the utility model embodiment is described in further detail below in conjunction with accompanying drawing.
As shown in Figure 1, a kind of dust remover blowing pipe structure of the utility model, comprise injection pipe of deduster 1, described injection tube front end is air inlet 2, and the rear end is stiff end 3, is furnished with a plurality of nozzles 4 on the described injection tube, a winding-up short tube 5 is installed on each nozzle, described winding-up short tube is the equal length short tube, over against winding-up short tube mouth one group of filter bag group 6 is installed, and described filter bag group end face is card 7; Described injection tube is divided into winding-up anterior 8 and winding-up rear portion 9, and the diameter sum of all nozzles is 60~80% of injection tube internal diameter on the injection tube, and the nozzle direct little 1mm of anterior nozzle diameter than the winding-up rear portion jets.
Described winding-up short tube mouth is 160mm-180mm apart from the height of card.
Under the state of middle pressure (0.3MPa-0.5MPa) winding-up, injection tube is divided into the anterior and winding-up rear portion of winding-up, the nozzle diameter of injection tube front portion is dmm, the nozzle diameter at injection tube rear portion is (d-1) mm, and all nozzle diameter sums should be 60~80% of injection tube internal diameter on the injection tube.When compressed air stream enters injection tube along the winding-up mouth of pipe like this, near anterior large-minded, the mouth mouth is corresponding big, the closer to the injection tube rear portion, throughput is more less than normal, need that jet hole is corresponding to be reduced, jet the compressed air stream that with the compressed air stream that guarantees to eject from the posterior nozzle group under almost identical jetting pressure with the anterior nozzle group of injection tube, guarantee the best ash-removal effect of injection system.
Winding-up short tube mouth is also very important apart from the control of card height.The height of winding-up short tube end face distance card is subjected to air-flow to become the impact of 20 ° of angles and chain induction air quantity along the winding-up axis.In theory, chain induction tolerance is The more the better, just strengthens the winding-up short tube apart from the height of card.But height can not unrestrictedly be raised, and air-flow becomes the phenomenon of 20 ° of angular spread to be doomed that it can only be a definite value along the winding-up axis.This value can guarantee that just the original air-flow of diffusion enters filter pocket mouths together with the air-flow while supersonic speed of inducing.The air-flow moment that enters filter bag blows to the filter bag bottom, forms certain pressure in the filter bag bottom.Then, the air-flow recoil is upwards sharply expanded in filter bag, shakes off covering the dust stratification at the filter bag outer surface.
According to using the CAD Simulation result on computers, under the jetting pressure of 0.3Mpa, 3 cun pulse valves winding-up specification is 150 * 7100 filter bag, and it highly is: H=160mm; The filter bag of winding-up 160 * 7100, it highly is: H=180mm.
In fact, jetting pressure is more big, and air-flow is just more little along the diffusion angle of winding-up axis, and the height of winding-up short tube end face distance card just can strengthen, and induces more air-flows, the more filter bag of jetting; Otherwise jetting pressure is more little, and air-flow is just more big along the diffusion angle of winding-up axis, and the height of winding-up short tube end face distance card just need to reduce, and induced draft reduces relatively, and the quantity of winding-up filter bag reduces.
The above only is preferred embodiment of the present utility model, and is in order to restriction the utility model, not all within spirit of the present utility model and principle, any modification of being done, is equal to replacement, improvement etc., all should be included within the protection domain of the present utility model.

Claims (2)

1, a kind of dust remover blowing pipe structure, comprise injection pipe of deduster, described injection tube front end is air inlet, the rear end is stiff end, it is characterized in that: be furnished with a plurality of nozzles on the described injection tube, a winding-up short tube is installed on each nozzle, described winding-up short tube is the equal length short tube, over against winding-up short tube mouth one group of filter bag group is installed, described filter bag group end face is card; Described injection tube is divided into the anterior and winding-up rear portion of winding-up, and the diameter sum of all nozzles is 60~80% of injection tube internal diameter on the injection tube, and the nozzle direct little 1mm of anterior nozzle diameter than the winding-up rear portion jets.
2, dust remover blowing pipe structure as claimed in claim 1 is characterized in that: described winding-up short tube mouth is 160mm-180mm apart from the height of card.
CNU2008201782449U 2008-11-10 2008-11-10 Dust remover blowing pipe structure Expired - Fee Related CN201304305Y (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CNU2008201782449U CN201304305Y (en) 2008-11-10 2008-11-10 Dust remover blowing pipe structure

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CNU2008201782449U CN201304305Y (en) 2008-11-10 2008-11-10 Dust remover blowing pipe structure

Publications (1)

Publication Number Publication Date
CN201304305Y true CN201304305Y (en) 2009-09-09

Family

ID=41096767

Family Applications (1)

Application Number Title Priority Date Filing Date
CNU2008201782449U Expired - Fee Related CN201304305Y (en) 2008-11-10 2008-11-10 Dust remover blowing pipe structure

Country Status (1)

Country Link
CN (1) CN201304305Y (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101670214B (en) * 2009-10-19 2011-08-03 湘乡机械厂有限责任公司 Pulse bag filter
CN103752098A (en) * 2013-11-29 2014-04-30 安徽意义环保设备有限公司 Injection-pipe perforated-board device of bag dust collector

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN101670214B (en) * 2009-10-19 2011-08-03 湘乡机械厂有限责任公司 Pulse bag filter
CN103752098A (en) * 2013-11-29 2014-04-30 安徽意义环保设备有限公司 Injection-pipe perforated-board device of bag dust collector

Similar Documents

Publication Publication Date Title
CN1984592B (en) Hand dryer
CN201304305Y (en) Dust remover blowing pipe structure
CN205443893U (en) Road marking machine
CN105398205B (en) A kind of LED UV print solidification equipment
CN104047135B (en) The gas-liquid that a kind of overflow dyeing machine is used is divided flow nozzle
CN207078729U (en) A kind of through type negative pressure powder pump
RU2007103247A (en) REACTIVE SYSTEM OF TWO-CIRCUIT TURBOREACTIVE ENGINE
CN206214959U (en) Penetrate mist machine
CN206838342U (en) A kind of atomizer
CN205272605U (en) Photocuring 3D print pen with prevent blockking up silica gel nozzle
CN206499961U (en) A kind of pulse backblowing deashing device
CN204749634U (en) Blackboard subassembly with absorb chalk dust function
CN203469697U (en) Novel ash removal blowing air diffuser
CN203236360U (en) Dust-free sand blasting gun
CN107587892B (en) A fine atomization foam dust collector for suppressing dust under mine
CN203155415U (en) Strong air throttling nozzle for air blow gun
CN205914291U (en) Nozzle of inside filter core dust removal usefulness of environmental protection sweeper
CN207445804U (en) A kind of cage bone device for sack cleaner
CN208287697U (en) A kind of pulse jet nozzle
CN202963427U (en) Wax crumb cleaning device
CN207356759U (en) A kind of pulse jetting deashing pipe
CN105881225A (en) Pressure sand blasting device for micro-powder sand
CN206476215U (en) Packing machine track dust guard
CN104456566A (en) Acetylene gas spray nozzle with massive structure
CN206681783U (en) Depositing dust plate and dust falling in coal mining blower fan

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
ASS Succession or assignment of patent right

Owner name: JIANGSU YIJIN ENVIRONMENTAL PROTECTION TECHNOLOGY

Free format text: FORMER OWNER: JIANGSU YIJIN ENVIRONMENTAL PROTECTION EQUIPMENT ENGINEERING CO., LTD.

Effective date: 20110817

C41 Transfer of patent application or patent right or utility model
COR Change of bibliographic data

Free format text: CORRECT: ADDRESS; FROM: 214414 WUXI, JIANGSU PROVINCE TO: 214400 WUXI, JIANGSU PROVINCE

TR01 Transfer of patent right

Effective date of registration: 20110817

Address after: 214400 Jiangyin Province, Gu Town, East Village

Patentee after: Jiangsu Yijin Environmental Protection Technology Co.,Ltd.

Address before: 214414, Jiangsu, Jiangyin province Gushan Town, East Village, Jiangsu billion gold environmental protection equipment Engineering Co., Ltd.

Patentee before: Jiangsu Yijin Environmental Protection Equipment Engineering Co., Ltd.

C56 Change in the name or address of the patentee
CP01 Change in the name or title of a patent holder

Address after: 214400 Jiangyin Province, Gu Town, East Village

Patentee after: JIANGSU YIJIN ENVIRONMENTAL PROTECTION EQUIPMENT ENGINEERING CO., LTD.

Address before: 214400 Jiangyin Province, Gu Town, East Village

Patentee before: Jiangsu Yijin Environmental Protection Technology Co.,Ltd.

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

Granted publication date: 20090909

Termination date: 20171110