CN105498382A - Large off-line ash removal bag-type dust collector - Google Patents
Large off-line ash removal bag-type dust collector Download PDFInfo
- Publication number
- CN105498382A CN105498382A CN201610009510.4A CN201610009510A CN105498382A CN 105498382 A CN105498382 A CN 105498382A CN 201610009510 A CN201610009510 A CN 201610009510A CN 105498382 A CN105498382 A CN 105498382A
- Authority
- CN
- China
- Prior art keywords
- flue
- air intake
- air
- flue gas
- bin
- 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
Links
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/0039—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with flow guiding by feed or discharge devices
- B01D46/0041—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with flow guiding by feed or discharge devices for feeding
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
- B01D46/023—Pockets filters, i.e. multiple bag filters mounted on a common frame
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D46/00—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours
- B01D46/02—Particle separators, e.g. dust precipitators, having hollow filters made of flexible material
- B01D46/04—Cleaning filters
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/02—Other waste gases
- B01D2258/0283—Flue gases
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The invention discloses a large off-line ash removal bag-type dust collector which comprises a dust collector box internally partitioned into two channels. Each channel is internally partitioned into two chambers, each chamber is partitioned into an upper purified gas room and a lower smoke room through a tube nest provided with a plurality of filter bags in a perpendicular suspension mode, a pulse jet ash removing mechanism is arranged in each chamber, a gas inlet is formed in each lower smoke room, the gas inlets of the lower smoke rooms in each channel are communicated with one air inlet flue branch pipe at the same time, the two air inlet flue branch pipes are communicated with an air inlet flue main pipe at the same time, each air inlet flue branch pipe is provided with an inlet baffle door, automatic smoke balanced distributors are arranged on the air inlet flue main pipe and the smoke flow distributing parts of all the air inlet flue branch pipes respectively, the upper purified gas room of each chamber is provided with an air outlet, the air outlet of each upper purified gas room is communicated with an air outlet flue branch pipe which is provided with an outlet baffle door, and the air outlet flue branch pipes are communicated with an air outlet flue main pipe at the same time. The large off-line ash removal bag-type dust collector has the advantages of being high in dust removing efficiency.
Description
Technical field
The present invention relates to a kind of large-scale off-line ash-clearing sack cleaner.
Background technology
The structure of the Large Size Bag Type Filters used at present is: comprise dust collector box body, the passage that the inside of dust collector box body is become two row independent sealed by the first baffle for separating, the inside of each passage is separated into the independent sealed bin of two row by second partition, each bin is separated into upper air-purifying chamber and lower smoke chamber by card, on the card of each bin, vertical hanging has some filter bags, the pulse jetting deashing mechanism that can carry out jetting deashing to filter bag is respectively arranged with in the upper air-purifying chamber of each bin, the sidewall of the lower smoke chamber of each bin is respectively arranged with air inlet, in each passage, the air inlet of the lower smoke chamber of two bins is connected with the exhanst gas outlet of an air intake flue arm simultaneously, the gas approach of two air intake flue arms is connected with the exhanst gas outlet of air intake breaching simultaneously, every root air intake flue arm is respectively arranged with the inlet baffle door of energy opening and closing air intake flue arm, the sidewall of the upper air-purifying chamber of each bin is respectively arranged with air outlet, the air outlet of each upper air-purifying chamber is communicated with an air-out flue arm respectively and is communicated with air-out breaching.The shortcoming of above-mentioned Large Size Bag Type Filters is: (1) only can be used in line purge mode and carries out jetting deashing to filter bag, but there is a day window effect in online ash removal mode, wherein sky window effect refers to: convection current pulse dust cleaning moment, this moment time t≤0.2s, the micropore of filter bag must occur expanding phenomenon, when high pressure draught disappears the micropore closed moment transferring negative pressure to, have many particle dusts to pass through from the micropore of expansion, thus reduce filtering accuracy and the efficiency of filter bag self, because the frequency of pulse jetting deashing is high, therefore, this moment, seepage will take care of the pence, finally have a strong impact on filtering accuracy and the efficiency of filter bag self, after this skylight just like closing is opened suddenly, suddenly close again, therefore, be referred to as " skylight efficiency ", due to the existence of sky window effect, make that the efficiency of dust collection of filter bag reduces, service life shortens, (2) flue gas flow entering each bin is unbalanced, causes the flue gas flow load of each row bin uneven, the bin that long-time load is large, and filter bag there will be blocking, damaged, makes that the efficiency of dust collection of filter bag reduces, shortening in service life.
Summary of the invention
The object of this invention is to provide a kind of efficiency of dust collection high and the large-scale off-line ash-clearing sack cleaner of one of life of bag filter can be extended.
For achieving the above object, present invention employs following technical scheme: the large-scale off-line ash-clearing sack cleaner of described one, comprise dust collector box body, the passage that the inside of dust collector box body is become two row independent sealed by the first baffle for separating, the inside of each passage is separated into the independent sealed bin of two row by second partition, each bin is separated into upper air-purifying chamber and lower smoke chamber by card, on the card of each bin, vertical hanging has some filter bags, the pulse jetting deashing mechanism that can carry out jetting deashing to filter bag is respectively arranged with in the upper air-purifying chamber of each bin, the sidewall of the lower smoke chamber of each bin is respectively arranged with air inlet, in each passage, the air inlet of the lower smoke chamber of two bins is connected with the exhanst gas outlet of an air intake flue arm simultaneously, the gas approach of two air intake flue arms is connected with the exhanst gas outlet of air intake breaching simultaneously, every root air intake flue arm is respectively arranged with the inlet baffle door of energy opening and closing air intake flue arm, at the flue gas shunting place of air intake breaching, and the flue gas shunting place of every root air intake flue arm is respectively arranged with flue gas automatic equalization distributor, flue gas automatic equalization in air intake breaching can be assigned to the air intake flue arm of the left and right sides by flue gas automatic equalization distributor, and the flue gas automatic equalization in air intake flue arm is assigned to the left and right two row bin be connected, the sidewall of the upper air-purifying chamber of each bin is respectively arranged with air outlet, the air outlet of each upper air-purifying chamber is communicated with an air-out flue arm respectively, every root air-out flue arm is respectively arranged with the outlet damper door of energy opening and closing air-out flue arm, and all air-out flue arms are connected with air-out breaching simultaneously.
Further, the large-scale off-line ash-clearing sack cleaner of aforesaid one, wherein: the structure of described flue gas automatic equalization distributor is: comprise movable vertical to being arranged at the rotating shaft of flue gas shunting place in flue, rotating shaft is by runner assembly free axial rotation in flue, the axle body of rotating shaft is fixed with fume balanced distributor body, the cross section of fume balanced distributor body is arranged in the quadrangle surrounded by the windward side of two symmetrical distributions and the lee face of two symmetrical distributions, angle angular range between two windward sides is 20 ~ 60 °, angle angular range between two lee faces is 110 ~ 130 °, when being greater than the flue gas flow by right side by the flue gas flow on the left of fume balanced distributor body, the active force that the windward side, left side of fume balanced distributor body is subject to can be greater than the active force that windward side, right side is subject to, fume balanced distributor body will rotate clockwise around the shaft, thus reduce the air intake bore of the gas approach on the left of fume balanced distributor body, and increase the air intake bore of the gas approach on the right side of fume balanced distributor body simultaneously, when being less than the flue gas flow by right side by the flue gas flow on the left of fume balanced distributor body, the active force that the windward side, left side of fume balanced distributor body is subject to can be less than the active force that windward side, right side is subject to, fume balanced distributor body will rotate counterclockwise around the shaft, thus reduce the air intake bore of the gas approach on the right side of fume balanced distributor body and increase the air intake bore of the gas approach on the left of fume balanced distributor body simultaneously.
Further, the large-scale off-line ash-clearing sack cleaner of aforesaid one, wherein: the angle angle between two windward sides is 50 °, the angle angle between two lee faces is 117 °.
Further, the large-scale off-line ash-clearing sack cleaner of aforesaid one, wherein: the structure of described runner assembly is: in the upside flue inner wall of flue, be provided with the first locating sleeve in flue gas shunting place, downside flue outer wall is provided with bearing and bearing block, the lower end movable sealing of rotating shaft inserts in bearing through flue gas shunting place after flue, the upper end of rotating shaft is provided with groove, groove and the first locating sleeve are formed installs chamber, spring and ball is disposed with from bottom to top in installation chamber, ball upwards withstands on flue gas shunting place all the time in the flue inner wall of flue under the elastic force effect of spring, and when ball by spring upwards withstand on flue gas shunting place in the flue inner wall of flue time, the top of ball is just in time positioned at the first locating sleeve, bottom is just in time arranged in groove.
Further, the large-scale off-line ash-clearing sack cleaner of aforesaid one, wherein: in the upside flue inner wall of flue, be also provided with the second locating sleeve simultaneously entangling the first locating sleeve and rotating shaft upper end in flue gas shunting place.
By the enforcement of technique scheme, the invention has the beneficial effects as follows: (1) can use off-line ash-clearing mode to carry out jetting deashing to filter bag, namely when a certain bin needs deashing, close the outlet damper door of the air-out flue arm communicated with the air outlet of the upper air-purifying chamber of this bin, and then unbalanced pulse jetting deashing mechanism carries out jetting deashing to filter bag, because now bin is the immobilising Static-state Space of air-flow, therefore, after the dust on filter bag departs from filter bag surface under the high pressure gas effect that pulse jetting deashing mechanism sprays, only has gravitational settling assorting room, and be not subject to any negative-pressure sucking effect, therefore, " skylight " effect that dust passes through from the micropore of expansion can not be there is, and then substantially increase dustfall efficiency, extend the service life of filter bag, (2) the flue gas flow load balancing of each bin can be remained, further increase dustfall efficiency, extend the service life of filter bag.
Accompanying drawing explanation
Fig. 1 is the structural representation of a kind of large-scale off-line ash-clearing sack cleaner of the present invention.
Fig. 2 is the structural representation overlooking direction of Fig. 1.
Fig. 3 is the structural representation being installed on the fume balanced distributor at air intake breaching flue gas shunting place shown in Fig. 1.
Fig. 4 is the structural representation overlooking direction of Fig. 3.
Fig. 5 is the enlarged diagram at the A position shown in Fig. 3.
Fig. 6 is the structural representation of the fume balanced distributor body shown in Fig. 3.
Detailed description of the invention
Below in conjunction with the drawings and specific embodiments, the invention will be further described.
As Fig. 1, shown in Fig. 2, the large-scale off-line ash-clearing sack cleaner of described one, comprise dust collector box body 1, the inside of dust collector box body 1 is separated into the independent sealed left passage of two row and right passage by the first dividing plate 2, the inside of left passage is separated into the first independent sealed left bin 4 and the first right bin 5 of two row by left second partition 3, the inside of right passage is separated into the second independent sealed left bin 7 and the second right bin 8 of two row by right second partition 6, each bin is separated into upper air-purifying chamber 10 and lower smoke chamber 11 by card 9 respectively, on the card 9 of each bin, vertical hanging has some filter bags 12, the pulse jetting deashing mechanism 13 that can carry out jetting deashing to filter bag 12 is respectively arranged with in the upper air-purifying chamber 10 of each bin, the sidewall of the lower smoke chamber 11 of each bin is respectively arranged with air inlet, in left passage, the air inlet of the lower smoke chamber 11 of the first left bin 4 is connected with the gas approach of left air intake flue arm 14 with the air inlet of the lower smoke chamber 11 of the first right bin 5 simultaneously, in right passage, the air inlet of the lower smoke chamber 11 of the second left bin 7 is connected with the gas approach of right air intake flue arm 15 with the air inlet of the lower smoke chamber 11 of the second right bin 8 simultaneously, the gas approach of left air intake flue arm 14 is connected with the exhanst gas outlet of air intake breaching 16 with the gas approach of right air intake flue arm 15 simultaneously, left air intake flue arm 14 and right air intake flue arm 15 are respectively arranged with the inlet baffle door 17 of energy switching station at air intake flue arm, at the flue gas shunting place of air intake breaching 16, the flue gas shunting place of left air intake flue arm 14 and the flue gas shunting place of right air intake flue arm 15 are respectively arranged with flue gas automatic equalization distributor, flue gas automatic equalization in air intake breaching 16 can be assigned to left air intake flue arm 14 and right air intake flue arm 15 by flue gas automatic equalization distributor, flue gas automatic equalization in left air intake flue arm 14 is assigned to the first left bin 4 and the first right bin 5 be connected, flue gas automatic equalization in right air intake flue 15 is assigned to the second left bin 7 and the second right bin 8 be connected, the sidewall of the upper air-purifying chamber 10 of each bin is respectively arranged with air outlet, the air outlet of each upper air-purifying chamber 10 is communicated with an air-out flue arm 18 respectively, every root air-out flue arm 18 is respectively arranged with the outlet damper door 19 of energy opening and closing air-out flue arm, and all air-out flue arms 18 are connected with air-out breaching 20 simultaneously, in the present embodiment, because the structure of all flue gas automatic equalization distributors is all identical, only be described for the structure of the flue gas automatic equalization distributor being installed on the flue gas shunting place of air intake breaching 16 below, as Fig. 3, Fig. 4, Fig. 5, shown in Fig. 6, the structure of described flue gas automatic equalization distributor is: comprise movable vertical to the rotating shaft 21 at flue gas shunting place being supported on air intake breaching 16, rotating shaft 21 is by runner assembly free axial rotation in air intake breaching 16, the axle body of rotating shaft 21 is fixed with fume balanced distributor body 22, the cross section of fume balanced distributor body 22 is arranged in the quadrangle surrounded by the windward side of two symmetrical distributions and the lee face of two symmetrical distributions, angle angular range a between two windward sides is 20 ~ 60 °, angle angular range b between two lee faces is 110 ~ 130 °, when the flue gas flow by entering left air intake flue arm 14 on the left of fume balanced distributor body 22 is greater than the flue gas flow by entering right air intake flue arm 15 on the right side of it, the active force that the windward side, left side of fume balanced distributor body 22 is subject to can be greater than the active force that windward side, right side is subject to, fume balanced distributor body 22 will 21 rotate clockwise around the shaft, thus reduces the air intake bore of the gas approach of left air intake flue arm 14 and increase the air intake bore of the gas approach of right air intake flue arm 15 simultaneously, when the flue gas flow by entering left air intake flue arm 14 on the left of fume balanced distributor body 22 is less than the flue gas flow by entering right air intake flue arm 15 on the right side of it, the active force that the windward side, left side of fume balanced distributor body 22 is subject to can be less than the active force that windward side, right side is subject to, fume balanced distributor body 22 will 21 rotate counterclockwise around the shaft, thus reduce the air intake bore of the gas approach of right air intake flue arm 14, and increase the air intake bore of the gas approach of left air intake flue arm 15 simultaneously, the structure of above-mentioned flue gas automatic equalization distributor is simple, installation and maintenance are convenient, in the present embodiment, the angle angle a between two windward sides is 50 °, and the angle angle b between two lee faces is 117 °, and the sensitivity of the flue gas automatic equalization distributor that this angle is arranged is high, in the present embodiment, the structure of described runner assembly is: in the upside flue inner wall of air intake breaching 16, be provided with the first locating sleeve 23, downside flue outer wall is provided with bearing 24 and bearing block 25, the lower end movable sealing of rotating shaft 21 is through inserting in bearing 24 after air intake breaching 16, the upper end of rotating shaft 21 is provided with groove 26, groove 26 and the first locating sleeve 23 are formed installs chamber, spring 27 and ball 28 is disposed with from bottom to top in installation chamber, ball 28 have all the time under the elastic force effect of spring 27 upwards withstand on air intake breaching 16 gently flue inner wall on, and when ball 28 is upwards withstood in the flue inner wall of air intake breaching 16 by spring 27, the top of ball 28 is just in time positioned at the first locating sleeve 23, bottom is just in time arranged in groove 26, above-mentioned runner assembly structure is simple, installation and maintenance are convenient, because point cantact is carried out by ball 28 and the flue inner wall of air intake breaching 16 in the upper end of rotating shaft 21, thus farthest reduce the resistance be subject to when the first rotating shaft 21 rotates, further ensure the sensitivity of flue gas automatic equalization distributor, in the present embodiment, the upside flue inner wall of air intake breaching 16 is also provided with the second locating sleeve simultaneously entangling the first locating sleeve 23 and rotating shaft 21 upper end, ball 28 effectively can be avoided like this to depart from from installation chamber, improve operation stability,
Operation principle of the present invention is as follows:
The flue gas entering air intake breaching 16 first can be diverted to left air intake flue arm 14 again with right air intake flue arm 15 after the fume balanced distributor at its gas distribution place, when the flue gas flow by entering left air intake flue arm 14 on the left of fume balanced distributor body 22 is greater than the flue gas flow by entering right air intake flue arm 15 on the right side of it, the active force that the windward side, left side of fume balanced distributor body 22 is subject to can be greater than the active force that windward side, right side is subject to, fume balanced distributor body 22 will 21 rotate clockwise around the shaft, thus reduce the air intake bore of the gas approach of left air intake flue arm 14, and increase the air intake bore of the gas approach of right air intake flue arm 15 simultaneously, when the flue gas flow by entering left air intake flue arm 14 on the left of fume balanced distributor body 22 is less than the flue gas flow by entering right air intake flue arm 15 on the right side of it, the active force that the windward side, left side of fume balanced distributor body 22 is subject to can be less than the active force that windward side, right side is subject to, fume balanced distributor body 22 will 21 rotate counterclockwise around the shaft, thus reduce the air intake bore of the gas approach of right air intake flue arm 14, and increase the air intake bore of the gas approach of left air intake flue arm 15 simultaneously, so just effectively can ensure that fume balanced is assigned to left air intake flue arm 14 with right air intake flue arm 15,
The flue gas entering left air intake flue arm 14 is diverted in the first left bin 4 and the first right bin 5 through the fume balanced distributor at its gas distribution place more again, when the flue gas flow by entering the first left bin 4 on the left of fume balanced distributor body is greater than the flue gas flow by entering the first right bin 5 on the right side of it, the active force that the windward side, left side of fume balanced distributor body is subject to can be greater than the active force that windward side, right side is subject to, fume balanced distributor body 22 will 21 rotate clockwise around the shaft, thus reduce the air intake bore of the air inlet of the first left bin 4, and increase the air intake bore of the air inlet of the first right bin 5 simultaneously, when the flue gas flow by entering the first left bin 4 on the left of fume balanced distributor body is less than the flue gas flow by entering the first right bin 5 on the right side of it, the active force that the windward side, left side of fume balanced distributor body is subject to can be less than the active force that windward side, right side is subject to, fume balanced distributor body 22 will 21 rotate counterclockwise around the shaft, thus reduce the air intake bore of the air inlet of the first right bin 5 and increase the air intake bore of air inlet of the first left bin 4 simultaneously, so just can ensure that fume balanced is assigned in the first left bin 4 and the first right bin 5,
And the flue gas entering right air intake flue arm 15 is diverted in the second left bin 7 and the second right bin 8 through the fume balanced distributor at its gas distribution place more again, when the flue gas flow by entering the second left bin 7 on the left of fume balanced distributor body is greater than the flue gas flow by entering the second right bin 8 on the right side of it, the active force that the windward side, left side of fume balanced distributor body is subject to can be greater than the active force that windward side, right side is subject to, fume balanced distributor body 22 will 21 rotate clockwise around the shaft, thus reduce the air intake bore of the air inlet of the second left bin 7, and increase the air intake bore of the air inlet of the second right bin 8 simultaneously, when the flue gas flow by entering the second left bin 7 on the left of fume balanced distributor body is less than the flue gas flow by entering the second right bin 8 on the right side of it, the active force that the windward side, left side of fume balanced distributor body is subject to can be less than the active force that windward side, right side is subject to, fume balanced distributor body 22 will 21 rotate counterclockwise around the shaft, thus reduce the air intake bore of the air inlet of the second right bin 8 and increase the air intake bore of air inlet of the second left bin 7 simultaneously, so just can ensure that fume balanced is assigned in the second left bin 7 and the second right bin 8,
In sack cleaner running, when the Resistance Value of certain bin reaches design resistance value and needs to carry out off-line ash-clearing, first close the outlet damper door 19 on the air-out flue arm 18 corresponding to this bin, now, this needs the bin of deashing can be in the immobilising space of air-flow, there is no the effect of negative-pressure adsorption power, then the pulse jetting deashing mechanism 13 in the upper air-purifying chamber 10 of this bin is started, after the dust being attached to filter bag 12 surface departs from filter bag 12 surface under the effect of pulse jetting deashing mechanism 13, by there is no the effect of negative-pressure adsorption power, thus " skylight " effect can not be there is, dust only can under sufficient gravitational settling sorting, the overwhelming majority directly falls into the ash bucket of below, only have the fine and ultra tiny dust of small part can continue to be suspended in lower smoke chamber 11, after pulse jetting deashing mechanism 13 completes jetting deashing, open the outlet damper door 19 on the air-out flue arm 18 corresponding to this bin after first waiting for a period of time again, make this bin proceed dedusting work, in the moment of opening corresponding outlet damper door 19, after sufficient gravitational settling sorting, continue the fine and ultra tiny dust of small part be suspended in lower smoke chamber 11 can by the surface of negative-pressure adsorption in filter bag 12, form the new long-pending rack-layer as dedusting medium, further increase the efficiency of dust collection of filter bag 12.
Advantage of the present invention is: (1) can use off-line ash-clearing mode to carry out jetting deashing to filter bag, namely when a certain bin needs deashing, close the outlet damper door of the air-out flue arm communicated with the air outlet of the upper air-purifying chamber of this bin, and then unbalanced pulse jetting deashing mechanism carries out jetting deashing to filter bag, because now bin is the immobilising Static-state Space of air-flow, therefore, after the dust on filter bag departs from filter bag surface under the high pressure gas effect that pulse jetting deashing mechanism sprays, only has gravitational settling assorting room, and be not subject to any negative-pressure sucking effect, therefore, " skylight " effect that dust passes through from the micropore of expansion can not be there is, and then substantially increase dustfall efficiency, extend the service life of filter bag, (2) the flue gas flow load balancing of each bin can be remained, further increase dustfall efficiency, extend the service life of filter bag.
Claims (5)
1. one kind large-scale off-line ash-clearing sack cleaner, it is characterized in that: comprise dust collector box body, the passage that the inside of dust collector box body is become two row independent sealed by the first baffle for separating, the inside of each passage is separated into the independent sealed bin of two row by second partition, each bin is separated into upper air-purifying chamber and lower smoke chamber by card, on the card of each bin, vertical hanging has some filter bags, the pulse jetting deashing mechanism that can carry out jetting deashing to filter bag is respectively arranged with in the upper air-purifying chamber of each bin, the anterior sidewall of the lower smoke chamber of each bin is respectively arranged with air inlet, in each passage, the air inlet of the lower smoke chamber of two bins is connected with the exhanst gas outlet of an air intake flue arm simultaneously, the gas approach of two air intake flue arms is connected with the exhanst gas outlet of air intake breaching simultaneously, every root air intake flue arm is respectively arranged with the inlet baffle door of energy opening and closing air intake flue arm, at the flue gas shunting place of air intake breaching, and the flue gas shunting place of every root air intake flue arm is respectively arranged with flue gas automatic equalization distributor, flue gas automatic equalization in air intake breaching can be assigned to the air intake flue arm of the left and right sides by flue gas automatic equalization distributor, and the flue gas automatic equalization in air intake flue arm is assigned to the left and right two row bin be connected, the sidewall of the upper air-purifying chamber of each bin is respectively arranged with air outlet, the air outlet of each upper air-purifying chamber is communicated with an air-out flue arm respectively, every root air-out flue arm is respectively arranged with the outlet damper door of energy opening and closing air-out flue arm, and all air-out flue arms are connected with air-out breaching simultaneously.
2. the large-scale off-line ash-clearing sack cleaner of one according to claim 1, it is characterized in that: the structure of described flue gas automatic equalization distributor is: comprise movable vertical to being arranged at the rotating shaft of flue gas shunting place in flue, rotating shaft is by runner assembly free axial rotation in flue, the axle body of rotating shaft is fixed with fume balanced distributor body, the cross section of fume balanced distributor body is arranged in the quadrangle surrounded by the windward side of two symmetrical distributions and the lee face of two symmetrical distributions, angle angular range between two windward sides is 20 ~ 60 °, angle angular range between two lee faces is 110 ~ 130 °, when being greater than the flue gas flow by right side by the flue gas flow on the left of fume balanced distributor body, the active force that the windward side, left side of fume balanced distributor body is subject to can be greater than the active force that windward side, right side is subject to, fume balanced distributor body will rotate clockwise around the shaft, thus reduce the air intake bore of the gas approach on the left of fume balanced distributor body, and increase the air intake bore of the gas approach on the right side of fume balanced distributor body simultaneously, when being less than the flue gas flow by right side by the flue gas flow on the left of fume balanced distributor body, the active force that the windward side, left side of fume balanced distributor body is subject to can be less than the active force that windward side, right side is subject to, fume balanced distributor body will rotate counterclockwise around the shaft, thus reduce the air intake bore of the gas approach on the right side of fume balanced distributor body and increase the air intake bore of the gas approach on the left of fume balanced distributor body simultaneously.
3. the large-scale off-line ash-clearing sack cleaner of one according to claim 2, it is characterized in that: the angle angle between two windward sides is 50 °, the angle angle between two lee faces is 117 °.
4. the large-scale off-line ash-clearing sack cleaner of one according to claim 2, it is characterized in that: the structure of described runner assembly is: in the upside flue inner wall of flue, be provided with the first locating sleeve in flue gas shunting place, downside flue outer wall is provided with bearing and bearing block, the lower end movable sealing of rotating shaft inserts in bearing through flue gas shunting place after flue, the upper end of rotating shaft is provided with groove, groove and the first locating sleeve are formed installs chamber, spring and ball is disposed with from bottom to top in installation chamber, ball upwards withstands on flue gas shunting place all the time in the flue inner wall of flue under the elastic force effect of spring, and when ball by spring upwards withstand on flue gas shunting place in the flue inner wall of flue time, the top of ball is just in time positioned at the first locating sleeve, bottom is just in time arranged in groove.
5. the large-scale off-line ash-clearing sack cleaner of one according to claim 4, is characterized in that: in the upside flue inner wall of flue, be also provided with the second locating sleeve simultaneously entangling the first locating sleeve and rotating shaft upper end in flue gas shunting place.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610009510.4A CN105498382B (en) | 2016-01-08 | 2016-01-08 | A kind of large-scale off-line ash-clearing sack cleaner |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201610009510.4A CN105498382B (en) | 2016-01-08 | 2016-01-08 | A kind of large-scale off-line ash-clearing sack cleaner |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105498382A true CN105498382A (en) | 2016-04-20 |
| CN105498382B CN105498382B (en) | 2018-01-12 |
Family
ID=55706915
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201610009510.4A Active CN105498382B (en) | 2016-01-08 | 2016-01-08 | A kind of large-scale off-line ash-clearing sack cleaner |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105498382B (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| IT201600130658A1 (en) * | 2016-12-23 | 2018-06-23 | VENETA IMPIANTI Srl | IMPROVED DUST REMOVER WITH FILTERS WITH SLEEVES OR BAGS WITH AIR FLOW BALANCING SYSTEM |
| CN108771949A (en) * | 2018-06-08 | 2018-11-09 | 苏州洋紫瑞信息科技有限公司 | A kind of exhaust gas purification device that intermittence is supplied gas |
| CN109289351A (en) * | 2018-02-02 | 2019-02-01 | 东华大学 | A kind of modularization vertical insert type sack cleaner |
| CN110075626A (en) * | 2019-04-22 | 2019-08-02 | 广州颖创环保科技有限公司 | Bag filter |
| CN114053793A (en) * | 2021-11-01 | 2022-02-18 | 江苏朗天环境工程技术服务有限公司 | Pulse dust removal device and method facilitating filter bag replacement |
Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201316575Y (en) * | 2008-10-24 | 2009-09-30 | 余建军 | Dust remover for pulse bag of settling chamber |
| CN202237602U (en) * | 2011-08-17 | 2012-05-30 | 吉林省双龙环保产业有限公司 | Offline low-voltage pulse bag-type dust collector |
| CN205435243U (en) * | 2016-01-08 | 2016-08-10 | 江苏新中环保股份有限公司 | Clear dust bag formula dust remover of large -scale off -line |
-
2016
- 2016-01-08 CN CN201610009510.4A patent/CN105498382B/en active Active
Patent Citations (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201316575Y (en) * | 2008-10-24 | 2009-09-30 | 余建军 | Dust remover for pulse bag of settling chamber |
| CN202237602U (en) * | 2011-08-17 | 2012-05-30 | 吉林省双龙环保产业有限公司 | Offline low-voltage pulse bag-type dust collector |
| CN205435243U (en) * | 2016-01-08 | 2016-08-10 | 江苏新中环保股份有限公司 | Clear dust bag formula dust remover of large -scale off -line |
Cited By (7)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| IT201600130658A1 (en) * | 2016-12-23 | 2018-06-23 | VENETA IMPIANTI Srl | IMPROVED DUST REMOVER WITH FILTERS WITH SLEEVES OR BAGS WITH AIR FLOW BALANCING SYSTEM |
| CN109289351A (en) * | 2018-02-02 | 2019-02-01 | 东华大学 | A kind of modularization vertical insert type sack cleaner |
| CN108771949A (en) * | 2018-06-08 | 2018-11-09 | 苏州洋紫瑞信息科技有限公司 | A kind of exhaust gas purification device that intermittence is supplied gas |
| CN108771949B (en) * | 2018-06-08 | 2021-05-07 | 江苏慧丰源环境工程技术有限公司 | Waste gas treatment purifier of intermittent type nature gas transmission |
| CN110075626A (en) * | 2019-04-22 | 2019-08-02 | 广州颖创环保科技有限公司 | Bag filter |
| CN114053793A (en) * | 2021-11-01 | 2022-02-18 | 江苏朗天环境工程技术服务有限公司 | Pulse dust removal device and method facilitating filter bag replacement |
| CN114053793B (en) * | 2021-11-01 | 2023-03-10 | 江苏朗天环境工程技术服务有限公司 | Pulse dust removal device and method facilitating filter bag replacement |
Also Published As
| Publication number | Publication date |
|---|---|
| CN105498382B (en) | 2018-01-12 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN105498382A (en) | Large off-line ash removal bag-type dust collector | |
| CN201735276U (en) | Bag-type dust removal device provided with rotational flow inlet | |
| CN106492575B (en) | A kind of efficient central dust-removing system | |
| CN207614520U (en) | A kind of bag filter | |
| CN209317265U (en) | IMPROVED PULSE DYNAMIC SPRAYING MACHINE blowing bag-type dust remover | |
| CN106345192B (en) | A kind of small-sized pulsed jet cloth filter | |
| CN105327585A (en) | Integrated dust collector device and dedusting method | |
| CN205435243U (en) | Clear dust bag formula dust remover of large -scale off -line | |
| CN207886839U (en) | A kind of cylindrical shape rotary pulse bag filter | |
| CN109364665A (en) | A kind of boiler exhaust gas fast dust-removing pipeline | |
| CN208727016U (en) | One kind is calmed the anger injection filter device | |
| CN203484022U (en) | Off-line impulse-type drum-type deduster | |
| CN201618490U (en) | Low-resistance high-efficiency electric bag combined dust remover | |
| CN208553586U (en) | A kind of efficient combination dust pelletizing system | |
| CN205164415U (en) | Integrated dust remover device | |
| CN208512164U (en) | A kind of high-efficiency bag type dust remover | |
| CN203437007U (en) | W-shaped pre-de-dusting device | |
| CN205435244U (en) | Flue gas automatic equalization distributor | |
| CN209917474U (en) | Ash bucket ash discharging device of bag type dust collector | |
| CN106147880B (en) | Pyrolysis gas dedusting filter | |
| CN105903276A (en) | Dust falling device | |
| CN102600997B (en) | High-efficiency dust collection cyclone separator group | |
| CN208771013U (en) | A kind of uniform pulse backblowing deduster of air flow method | |
| CN221771838U (en) | Multi-chamber dust collector | |
| CN205913889U (en) | Dust -settling 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 | ||
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| TR01 | Transfer of patent right | ||
| TR01 | Transfer of patent right |
Effective date of registration: 20190108 Address after: 215600 Donglai Jiangqiao, Yangshe Town, Zhangjiagang City, Jiangsu Province (in Zhangjiagang East China Marine Valve Manufacturing Co., Ltd.) Patentee after: Jiangsu Xinren Environmental Protection Technology Co., Ltd. Address before: 215600 Jiangsu Xinzhong Environmental Protection Co., Ltd. Zhangjiagang Economic Development Zone, Suzhou City, Jiangsu Province Patentee before: Jiangsu New Environmental Co., Ltd. |