CN204412000U - With pulse bag formula cleaner on a kind of pad pasting reacting furnace - Google Patents

With pulse bag formula cleaner on a kind of pad pasting reacting furnace Download PDF

Info

Publication number
CN204412000U
CN204412000U CN201520056081.7U CN201520056081U CN204412000U CN 204412000 U CN204412000 U CN 204412000U CN 201520056081 U CN201520056081 U CN 201520056081U CN 204412000 U CN204412000 U CN 204412000U
Authority
CN
China
Prior art keywords
bag
reacting furnace
pulse bag
air
pad pasting
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
CN201520056081.7U
Other languages
Chinese (zh)
Inventor
汪鼎
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.)
Ya Hua Electron Material Co Ltd Of Jiangxi Province
Original Assignee
Ya Hua Electron Material Co Ltd Of Jiangxi Province
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 Ya Hua Electron Material Co Ltd Of Jiangxi Province filed Critical Ya Hua Electron Material Co Ltd Of Jiangxi Province
Priority to CN201520056081.7U priority Critical patent/CN204412000U/en
Application granted granted Critical
Publication of CN204412000U publication Critical patent/CN204412000U/en
Expired - Fee Related legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Filtering Of Dispersed Particles In Gases (AREA)
  • Waste-Gas Treatment And Other Accessory Devices For Furnaces (AREA)

Abstract

The utility model discloses on a kind of pad pasting reacting furnace with pulse bag formula cleaner, it comprises one and exports with reacting furnace the cooler (2) be connected, the outlet of cooler (2) is connected with the entrance of cyclone settling bucket (3), the outlet of described cyclone settling bucket (3) is connected with the entrance of pulse bag formula deduster (4), and the outlet of described pulse bag formula deduster (4) is connected with the entrance of aiutage (5).The utility model effectively can be removed reacting furnace in course of reaction, distribute a large amount of toxic gases and poisonous dust.

Description

With pulse bag formula cleaner on a kind of pad pasting reacting furnace
Technical field
The utility model relates to technical field of dust removal equipment, more specifically to a kind of pad pasting reacting furnace being used pulse bag formula cleaner.
Background technology
In pad pasting reacting furnace course of reaction, a large amount of poisonous gases and poisonous dust can be produced, these poisonous gases and the direct harmful to human of poisonous dust and environment.If cause serious pollution by these poisonous gases and poisonous dust emissions to air by air, especially present stage is poor in the air quality of China, under the overall situation of haze weather continuity, lifting is controlled to the dyeing and finishing of toxic emission very urgent, it is of low quality that the tail gas produced pad pasting reacting furnace in prior art generally purifies when carrying out purified treatment, is therefore badly in need of the cleaner of a good filtration effect of exploitation.
Summary of the invention
The purpose of this utility model is just to provide with pulse bag formula cleaner on a kind of pad pasting reacting furnace, and it effectively can be removed reacting furnace in course of reaction, distribute a large amount of toxic gases and poisonous dust.
For achieving the above object, a kind of pad pasting reacting furnace of the present utility model comprises one with pulse bag formula cleaner and exports with reacting furnace the cooler be connected, the outlet of cooler is connected with the entrance of cyclone settling bucket, the outlet of described cyclone settling bucket is connected with the entrance of pulse bag formula deduster, and the outlet of described pulse bag formula deduster is connected with the entrance of aiutage;
Described cyclone settling bucket is made up of settling vat body and high speed air exhauster, the inwall of described settling vat body forms spiral guiding gutter, the top of described settling vat body is provided with the Inserting Tube be inserted in settling vat chamber body, the inwall of described Inserting Tube has helical form and the deflector contrary with guiding gutter direction, the sidewall of described settling vat body offers the entrance be connected with cooler outlet, described Inserting Tube is connected with high speed air exhauster, and the outlet of described high speed air exhauster is connected with pulse bag formula deduster.
Preferred as technique scheme, the bottom of described settling vat body is the cone wall in reducing shape, and the inwall of described cone wall is provided with some deflectors.
Preferred as technique scheme, the structure of described pulse bag formula deduster comprises a bag room, some filter bags are provided with in described bag room, described filter bag is by being sleeved on passive bag cage, the top being positioned at described bag room is air-purifying chamber, the sack of described filter bag is arranged in described air-purifying chamber, and the exit of described air-purifying chamber is provided with lifting cylinder.
Preferred as technique scheme, the below of described bag room is provided with funnelform ash bucket, and the exit, lower end of described ash bucket is provided with pair of lamina unloading valve.
Preferred as technique scheme, a gas tube is provided with in described air-purifying chamber, described gas tube is connected with gas bag, described gas bag is communicated with in the exit of air accumulator, the exit of described air accumulator is also communicated with gas source triplet, described gas source triplet is connected with magnetic valve, and described solenoid control lifting cylinder, the switch of described gas tube is controlled by impulse electromagnetic valve.
Preferred as technique scheme, the piston rod of described lifting cylinder is provided with valve plate, and described valve plate matches with the outlet of air-purifying chamber.
Preferred as technique scheme, described air accumulator is provided with safety valve, connects and be provided with pressure regulator valve between described air accumulator and gas bag.
The beneficial effects of the utility model are: first the gas of discharging in the utility model reacting furnace cool through subcooler, then the larger dust of degranulation is removed through cyclone settling bucket, through pulse bag formula deduster, tail gas is filtered again afterwards, discharge by aiutage afterwards, the utility model effectively can be removed reacting furnace in course of reaction, distribute a large amount of toxic gases and poisonous dust in this process.
accompanying drawing illustrates:
Below in conjunction with accompanying drawing, the utility model is described further:
Fig. 1 is the structural representation of the utility model embodiment
Fig. 2 is pulse bag formula deduster structural representation in the utility model embodiment
Fig. 3 is pulse bag formula deduster structural representation in the utility model embodiment
Fig. 4 is the structural representation of cyclone settling bucket in the utility model embodiment
Fig. 5 is the perspective view of cyclone settling bucket in the utility model embodiment
Fig. 6 is the sectional view of cyclone settling bucket in the utility model embodiment
Fig. 7 is the view of filter bag when dedusting in the utility model embodiment
Fig. 8 is filter bag view operationally in the utility model embodiment
In figure: 1, reacting furnace; 2, cooler; 3, cyclone settling bucket; 4, pulse bag formula deduster; 5, aiutage; 31, settling vat body; 32, high speed air exhauster; 33, guiding gutter; 34, Inserting Tube; 35, deflector; 36, guided plate; 37, wall is bored; 41, magnetic valve; 42, lifting cylinder; 43, filter bag; 44, bag room; 45, ash bucket; 46, Double-deck cinder discharge valve; 47, air accumulator; 48, pressure regulator valve; 49, gas source triplet; 50, gas bag; 51, impulse electromagnetic valve; 52, air-purifying chamber; 421, valve plate; 431, bag cage; 471, safety valve
detailed description of the invention:
The following stated is only the preferred embodiment embodying the utility model principle, does not therefore limit protection domain of the present utility model
Be the embodiment with pulse bag formula cleaner on a kind of pad pasting reacting furnace of the utility model as shown in Figures 1 to 6, it comprises one and exports with reacting furnace 1 cooler 2 be connected, the outlet of cooler 2 is connected with the entrance of cyclone settling bucket 3, the outlet of described cyclone settling bucket 3 is connected with the entrance of pulse bag formula deduster 4, and the outlet of described pulse bag formula deduster 4 is connected with the entrance of aiutage 5;
Described cyclone settling bucket 3 is made up of settling vat body 31 and high speed air exhauster 32, the inwall of described settling vat body 31 forms spiral guiding gutter 33, the top of described settling vat body 31 is provided with the Inserting Tube 34 be inserted in settling vat body 31 inner chamber, the inwall of described Inserting Tube 34 has helical form and the deflector 35 contrary with guiding gutter 33 direction, the sidewall of described settling vat body 31 offers and exports with cooler 2 entrance be connected, described Inserting Tube 34 is connected with high speed air exhauster 32, the outlet of described high speed air exhauster 32 is connected with pulse bag formula deduster 4, and specific in the present embodiment, guiding gutter 33 and deflector 35 tool are arrange with one heart.
Time the tail gas of reacting furnace enters into cyclone settling bucket 3, power is provided by high speed air exhauster 32, inwall due to settling vat body 31 forms spiral guiding gutter 33 and tail gas is rotated in settling vat body 31, and there is in Inserting Tube 34 deflector 35 contrary with the hand of spiral of guiding gutter 33, therefore two whirlpools can be formed at settling vat body 31, under the effect of two whirlpools, particle and weight significantly dust are rushed pivot and are fallen, and can play the effect removing dust in reacting furnace tail gas well.
The bottom of settling vat body 31 is the cone wall 37 in reducing shape, and the inwall of described cone wall 37 is provided with some guided plates 36.
The structure of pulse bag formula deduster 4 comprises bag room 44, some filter bags 43 are provided with in described bag room 44, described filter bag 43 is by being sleeved on passive bag cage 431, the top being positioned at described bag room 44 is air-purifying chamber 52, the sack of described filter bag 43 is arranged in described air-purifying chamber 52, and the exit of described air-purifying chamber 52 is provided with lifting cylinder 42.
The below of bag room 44 is provided with funnelform ash bucket 45, and the exit, lower end of described ash bucket 45 is provided with pair of lamina unloading valve 46.
A gas tube is provided with in air-purifying chamber 52, described gas tube is connected with gas bag 50, described gas bag 50 is communicated with in the exit of air accumulator 47, the exit of described air accumulator 47 is also communicated with gas source triplet 49, described gas source triplet 49 is connected with magnetic valve 41, described magnetic valve 41 controls lifting cylinder 42, and the switch of described gas tube is controlled by impulse electromagnetic valve 51.
The piston rod of lifting cylinder 42 is provided with valve plate 421, described valve plate 421 matches with the outlet of air-purifying chamber 52.
Air accumulator 47 is provided with safety valve 471, connects between described air accumulator 47 and gas bag 50 and pressure regulator valve 48 is installed.
If Fig. 7 is the view of filter bag 43 when dedusting in the present embodiment, due to process service time, therefore a lot of dust can be attached to the outer surface of filter bag 43, affect the performance of filter bag 43, therefore after filter bag 43 has worked certain hour, need the dust removing filter bag 43 outer surface, gases at high pressure are discharged through gas bag 50 in the process by air accumulator 47, now lifting cylinder 42 is in decline, valve plate 421 blocks the outlet of air-purifying chamber 52, gases at high pressure enter into air-purifying chamber 52, and gases at high pressure enter into the inside of filter bag 43 from the entrance of filter bag 43, then gases at high pressure blow off through the dust of filter bag 43 by outer surface.
If Fig. 8 is filter bag 43 view operationally in the present embodiment, now lifting cylinder 42 rises, the outlet of air-purifying chamber 52 is opened, reacting furnace tail gas enters into bag room 44 from the entrance of settling vat body 31, reacting furnace tail gas enters in filter bag 43 through filter bag 43 from outside to inside, now filter bag 43 shrinks, dust is then isolated in beyond filter bag 43, tail gas through filtering enters into air-purifying chamber 52 from filter bag 43 outlet, then export from air-purifying chamber 52 and discharge, discharge in the outlet through settling vat body 31 afterwards.
The utility model embodiment is when work: the waste gas that reacting furnace produces is cooled by cooler, then enter cyclone settling bucket to carry out once filtering waste gas, the import that dusty gas enters pulse bag formula deduster is again introduced into a bag air channel, room, then ash bucket is entered, now air velocity reduces, direction changes, and thicker grit reaches pre-dust collection effect because inertia and natural subsidence enter ash bucket; Then gas rises through filter bag and is purified, and dust is delayed on filter bag outer surface, and purified gas is discharged through filter bag, air-purifying chamber, exhaust outlet under the effect of air-introduced machine.

Claims (7)

1. a pad pasting reacting furnace is used pulse bag formula cleaner, it comprises one and exports with reacting furnace the cooler (2) be connected, it is characterized in that: the outlet of cooler (2) is connected with the entrance of cyclone settling bucket (3), the outlet of described cyclone settling bucket (3) is connected with the entrance of pulse bag formula deduster (4), and the outlet of described pulse bag formula deduster (4) is connected with the entrance of aiutage (5);
Described cyclone settling bucket (3) is made up of settling vat body (31) and high speed air exhauster (32), the inwall of described settling vat body (31) forms spiral guiding gutter (33), the top of described settling vat body (31) is provided with the Inserting Tube (34) be inserted in settling vat body (31) inner chamber, the inwall of described Inserting Tube (34) has helical form and the deflector (35) contrary with guiding gutter (33) direction, the sidewall of described settling vat body (31) offers and exports with cooler (2) entrance be connected, described Inserting Tube (34) is connected with high speed air exhauster (32), the outlet of described high speed air exhauster (32) is connected with pulse bag formula deduster (4).
2. a kind of pad pasting reacting furnace according to claim 1 is used pulse bag formula cleaner, it is characterized in that: the bottom of settling vat body (31) is the cone wall (37) in reducing shape, and the inwall of described cone wall (37) is provided with some guided plates (36).
3. a kind of pad pasting reacting furnace according to claim 1 is used pulse bag formula cleaner, it is characterized in that: the structure of pulse bag formula deduster (4) comprises a bag room (44), some filter bags (43) are provided with in described bag room (44), described filter bag (43) is by being sleeved on passive bag cage (431), the top being positioned at described bag room (44) is air-purifying chamber (52), the sack of described filter bag (43) is arranged in described air-purifying chamber (52), and the exit of described air-purifying chamber (52) is provided with lifting cylinder (42).
4. a kind of pad pasting reacting furnace according to claim 3 is used pulse bag formula cleaner, it is characterized in that: the below of bag room (44) is provided with funnelform ash bucket (45), the exit, lower end of described ash bucket (45) is provided with pair of lamina unloading valve (46).
5. a kind of pad pasting reacting furnace according to claim 3 is used pulse bag formula cleaner, it is characterized in that: air-purifying chamber is provided with a gas tube in (52), described gas tube is connected with gas bag (50), described gas bag (50) is communicated with the exit in air accumulator (47), the exit of described air accumulator (47) is also communicated with gas source triplet (49), described gas source triplet (49) is connected with magnetic valve (41), described magnetic valve (41) controls lifting cylinder (42), and the switch of described gas tube is controlled by impulse electromagnetic valve (51).
6. with pulse bag formula cleaner on a kind of pad pasting reacting furnace according to any one of claim 3 to 5, it is characterized in that: the piston rod of lifting cylinder (42) is provided with valve plate (421), described valve plate (421) matches with the outlet of air-purifying chamber (52).
7. a kind of pad pasting reacting furnace according to claim 5 is used pulse bag formula cleaner, it is characterized in that: air accumulator (47) is provided with safety valve (471), connect between described air accumulator (47) and gas bag (50) and pressure regulator valve (48) is installed.
CN201520056081.7U 2015-01-27 2015-01-27 With pulse bag formula cleaner on a kind of pad pasting reacting furnace Expired - Fee Related CN204412000U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201520056081.7U CN204412000U (en) 2015-01-27 2015-01-27 With pulse bag formula cleaner on a kind of pad pasting reacting furnace

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201520056081.7U CN204412000U (en) 2015-01-27 2015-01-27 With pulse bag formula cleaner on a kind of pad pasting reacting furnace

Publications (1)

Publication Number Publication Date
CN204412000U true CN204412000U (en) 2015-06-24

Family

ID=53462410

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201520056081.7U Expired - Fee Related CN204412000U (en) 2015-01-27 2015-01-27 With pulse bag formula cleaner on a kind of pad pasting reacting furnace

Country Status (1)

Country Link
CN (1) CN204412000U (en)

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107126743A (en) * 2017-06-01 2017-09-05 佛山市麦克罗美的滤芯设备制造有限公司 Drainage component
CN112414169A (en) * 2020-11-30 2021-02-26 北京艾科美特新材料开发有限公司 Cooling equipment for preparing inorganic-organic composite material

Cited By (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107126743A (en) * 2017-06-01 2017-09-05 佛山市麦克罗美的滤芯设备制造有限公司 Drainage component
CN107126743B (en) * 2017-06-01 2024-04-30 佛山市麦克罗美的滤芯设备制造有限公司 Water filtering assembly
CN112414169A (en) * 2020-11-30 2021-02-26 北京艾科美特新材料开发有限公司 Cooling equipment for preparing inorganic-organic composite material

Similar Documents

Publication Publication Date Title
CN201632155U (en) Long-bag low-pressure bag type dust remover
CN201353468Y (en) Cyclone pulse filter cylinder bag type dust remover
CN105126529B (en) Method and device for inorganized emission flying dust pollution government
CN102366700A (en) Cyclone electric-bag pulse filter cylinder separator
CN104400669B (en) Dust removing device for stone shot blasting
CN207856570U (en) A kind of compound bag filter of high-efficiency pulse formula
CN204412000U (en) With pulse bag formula cleaner on a kind of pad pasting reacting furnace
CN103706213A (en) Cyclone bag dust collector device
CN105536363A (en) Filter-element type polishing dust suction system
CN206414917U (en) A kind of ceramic sintering kiln
CN207591525U (en) A kind of deduster for steel pipe ball blast
CN105013272A (en) Dust removal equipment for melting furnace
CN106110784A (en) Soot cleaning system for kiln tail Low-Pressure Pulse Bag Filter
CN204412001U (en) A kind of pad pasting reacting furnace filter plant
CN202845405U (en) Automatic dedusting equipment for tunnel kiln car
CN204709989U (en) Saving low pulse dust collector
CN203724956U (en) Cyclone bag dust collector device
CN204221617U (en) A kind of polishing machine noise reduction dust arrester
CN204147689U (en) A kind of filter drum type precipitator
CN101254386A (en) Semi-off-line deash bag dust-cleaning equipment
CN206778166U (en) A kind of impulse bag desulphurization denitration deduster for being easy to dust to slide
CN206652320U (en) A kind of High-efficiency pulse cloth bag-type dust collecting equipment
CN107755092A (en) A kind of application method of vertical pipe formula metallic dust collection device
CN107774656A (en) A kind of application method of metallic dust collection device
CN210849856U (en) Scrap iron collecting device of shot blasting machine

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20150624

Termination date: 20160127

EXPY Termination of patent right or utility model