CN206325359U - A kind of twin-stage Water-bath silk net efficiency dust catcher - Google Patents
A kind of twin-stage Water-bath silk net efficiency dust catcher Download PDFInfo
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- CN206325359U CN206325359U CN201621466626.2U CN201621466626U CN206325359U CN 206325359 U CN206325359 U CN 206325359U CN 201621466626 U CN201621466626 U CN 201621466626U CN 206325359 U CN206325359 U CN 206325359U
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Abstract
The utility model provides a kind of twin-stage Water-bath silk net efficiency dust catcher, including casing and the deduster support below casing；Casing includes being respectively positioned on its internal the first dirt pocket, transition chamber and the second dirt pocket；First dirt pocket includes the first dust and gas entrance, the first dedusting impact tube, the first cleaning system, the second cleaning system and dust and gas outlet；Second dirt pocket includes the second dust and gas entrance, the second dedusting impact tube, the 3rd cleaning system, the 4th cleaning system, dehydration device and the outlet of net gas；Connected in the middle part of one side roof part of transition chamber and dust and gas outlet, its relative opposite side with the second dust and gas entrance.Using the technical solution of the utility model, effect is as follows：Twin-stage Water-bath silk net efficiency dust catcher is provided with two dirt pockets, four sets of cleaning systems, by the way of water-bath washing dust removal mechanism and filtering type purification techniques are combined, fine dust can be captured, dusty gas, simple in construction, convenient operating maintenance, water-saving consumption-reduction is farthest purified.
Description
Technical field
The utility model is related to cleaner field, and in particular to a kind of twin-stage Water-bath silk net efficiency dust catcher.
Background technology
Deduster is a kind of equipment that purification separation comes out from flue gas dust, is the dust such as coloured, metallurgical and chemical industry
Industrial equipment relatively conventional in more industry production is produced, it is extracted internal dust and gas by using miscellaneous equipment, this
Sample equipment inside and outside generates negative pressure, and negative pressure makes the gas with dust after air inlet access arrangement, entered by filter element
Row filtering, the clean gas after filtering is discharged through gas outlet.The water-bath type dust cleaner using water as medium is mostly present at present
Problem：1st, it is poor that complex structure, inconvenient, the not easy-maintaining, operating cost of operation are high by 2, water quality circulation substitutes slow, dust removing effects；3、
Dust in flue gas is not easy to be captured, efficiency of dust collection is poor.
Therefore, it is badly in need of a kind of new twin-stage Water-bath silk net efficiency dust catcher to solve the above problems.
Utility model content
The utility model purpose is to provide that a kind of structure design is simple, easy to operate, water consumption is low and efficiency of dust collection
High twin-stage Water-bath silk net efficiency dust catcher, to solve deficiency of the prior art.Concrete technical scheme is as follows：
A kind of twin-stage Water-bath silk net efficiency dust catcher, including casing and being used for below the casing support whole
The deduster support of twin-stage Water-bath silk net efficiency dust catcher；The casing includes being respectively positioned on its first internal dirt pocket, transition
Room and the second dirt pocket；
First dirt pocket includes being arranged on the supermedial first dust and gas entrance of the first dirt pocket side wall, one end company
Lead to the first dust and gas entrance and the first dedusting impact tube inside first dirt pocket, be arranged at first dedusting
First cleaning system of indoor bottom, be arranged inside first dirt pocket and above first cleaning system the
Two cleaning systems and the dust and gas outlet in the first dirt pocket top sidewall；
Second dirt pocket includes being arranged on the supermedial second dust and gas entrance of the second dirt pocket side wall, one end company
Lead to the second dust and gas entrance and the second dedusting impact tube inside second dirt pocket, be arranged at second dedusting
3rd cleaning system of indoor bottom, be arranged inside second dirt pocket and above the 3rd cleaning system the
Four cleaning systems, it is arranged in second dirt pocket and the dehydration device above the 4th cleaning system and is located at
Net gas outlet in the second dirt pocket top sidewall；
The dust and gas outlet of one side roof part of the transition chamber and first dirt pocket, its relative opposite side
Middle part is connected with the second dust and gas entrance of second dirt pocket.
It is preferred that, the first ash bucket that first cleaning system includes being used for storing dedusting aqueous medium, it is arranged at described the
The first water level control apparatus in one ash bucket top outer, be arranged on the outside of first ash bucket and with first water level regulation
First overflow mechanism of device connection and the first blowdown apparatus for being arranged at first hopper bottom；
Second cleaning system include be fixed on the first dirt pocket side wall first support, positioned at described first
The first woven wire group on support, the first spray equipment being arranged above the first woven wire group and it is arranged at institute
State the first pulse blockage-clearing device above the first spray equipment.
It is preferred that, the first dedusting impact tube is bend pipe, and its upper end is connected with the first dust and gas entrance, described first
The distance of the lower end surface of dedusting impact tube to the liquid level in first ash bucket is 10-15cm.
It is preferred that, the second ash bucket that the 3rd cleaning system includes being used for storing dedusting aqueous medium, it is arranged at described the
Second water level control apparatus of two ash bucket top outers, it is arranged on the outside of second ash bucket and is filled with second water level regulation
Put the second overflow mechanism of connection and be arranged at the second blowdown apparatus of second hopper bottom；
4th cleaning system include be fixed on the second dirt pocket side wall second support, positioned at described second
The second woven wire group on support, the second spray equipment being arranged above the second woven wire group and it is arranged at institute
State the second pulse blockage-clearing device above the second spray equipment.
It is preferred that, the second dedusting impact tube is bend pipe, and its upper end is connected with the second dust and gas entrance, described second
The distance of the lower end surface of dedusting impact tube to the liquid level in second ash bucket is 10-15cm.
It is preferred that, also it is used for the first woven wire group is overhauled the including being arranged on the first dedusting chamber outer wall
One woven wire manhole, be arranged on the second dedusting chamber outer wall be used for the second woven wire group overhaul the second gold medal
Belong to silk screen manhole and two deduster manholes on the cabinet exterior.
It is preferred that, the first woven wire group, the second woven wire group are stacked by multiple layer metal silk screen layer
Network structure, the woven wire is yi word pattern, V-type or W types.
Using the technical solution of the utility model, have the advantages that：
(1) twin-stage Water-bath silk net efficiency dust catcher of the present utility model uses exclusive water-bath washing dust removal mechanism and metal
The mode and the dusty gas of entrance deduster that silk screen filter formula purification techniques is combined pass through the first dirt pocket and the second dedusting
The secondary filter of indoor filtration system, can capture existing equipment capture less than fine dust, efficiency of dust collection greatly improves.
(2) the peculiar structure of twin-stage Water-bath silk net efficiency dust catcher of the present utility model make it that dusty gas enters deduster
Afterwards directly impact hopper bottom, hopper bottom little particle sludge never precipitate with it is hardened, solve sludge and be bonded in grey headwall
On the problem of cause device damage, and dusty gas, after the processing of the first cleaning system, efficiency of dust collection can reach more than 75%,
The dust concentration so filtered again by woven wire is very low, does not result in bonding and the blocking of woven wire, is bonded at wire
The little particle dust in online face can be rinsed by the spray equipment of side placed on it, it is ensured that gas passes through woven wire.
(3) the dedusting impact tube of twin-stage Water-bath silk net efficiency dust catcher of the present utility model, ash bucket, water level control apparatus,
The combination of overflow mechanism and spray equipment, can reasonably control the fluctuation range of liquid level in ash bucket, make the aqueous medium in ash bucket
In dynamic balance state, the height of liquid level in ash bucket can also be adjusted at any time, it is ensured that the running resistance of deduster and dedusting effect
Rate is balanced, so as to reach higher efficiency of dust collection.
(4) spray equipment inside twin-stage Water-bath silk net efficiency dust catcher of the present utility model so that the condensation rate height of water,
Water consumption is low, both can guarantee that higher efficiency of dust collection, and the effect of water-saving consumption-reduction can be reached again.
(5) the net gas outlet of the second dirt pocket of twin-stage Water-bath silk net efficiency dust catcher of the present utility model is provided with dehydration
Device, purifies the gas with steam completed and is exported again through net gas after dehydration device is handled, effectively alleviating makes deduster
The problem of exhaust equipment that inside produces negative pressure is easily stained with ash due to gas band water.
(6) simple in construction, the convenient operating maintenance of twin-stage Water-bath silk net efficiency dust catcher of the present utility model, it is not necessary to specially
People manages.
In addition to objects, features and advantages described above, the utility model also has other purposes, feature and excellent
Point.Below with reference to figure, the utility model is described in further detail.
Brief description of the drawings
The accompanying drawing for constituting the part of the application is used for providing further understanding to of the present utility model, of the present utility model
Schematic description and description is used to explain the utility model, does not constitute to improper restriction of the present utility model.In accompanying drawing
In：
Fig. 1 is the structural representation of the utility model embodiment 1；
Fig. 2 is Fig. 1 left views；
Label in figure：1st, the first dirt pocket；1.1st, the first dust and gas entrance；1.2nd, the first dedusting impact tube；1.3rd, first is net
Change system；1.31st, the first ash bucket；1.32nd, the first water level control apparatus；1.33rd, the first overflow mechanism；1.34th, the first blowdown is filled
Put；1.4th, the second cleaning system；1.41st, first support；1.42nd, the first woven wire group；1.43rd, the first spray equipment；1.44、
First pulse blockage-clearing device；1.5th, dust and gas is exported；2nd, the second dirt pocket；2.1st, the second dust and gas entrance；2.2 second dedustings are impacted
Pipe；2.3rd, the 3rd cleaning system；2.31st, the second ash bucket；2.32nd, the second water level control apparatus；2.33rd, the second overflow mechanism；
2.34th, the second blowdown apparatus；2.4th, the 4th cleaning system；2.41st, second support；2.42nd, the second woven wire group；2.43rd,
Two spray equipments；2.44th, the second pulse blockage-clearing device；2.5th, dehydration device；2.6th, net gas outlet；3rd, transition chamber；4th, casing；5、
Deduster is supported；6th, the first woven wire manhole；7th, woven wire manhole second；8th, deduster manhole.
Embodiment
Embodiment of the present utility model is described in detail below in conjunction with accompanying drawing, but the utility model can be according to power
Profit requires to limit and the multitude of different ways of covering is implemented.
Embodiment 1：
A kind of twin-stage Water-bath silk net efficiency dust catcher as shown in Figure 1-2, including casing 4, positioned at the lower section of the casing 4
Deduster for supporting whole twin-stage Water-bath silk net efficiency dust catcher supports 5 and two on the outer wall of casing 4
Deduster manhole 8.The casing 4 includes being respectively positioned on its first internal dirt pocket 1, dirt pocket 2 of transition chamber 3 and second.
First dirt pocket 1 include be arranged on the supermedial first dust and gas entrance 1.1 of the side wall of the first dirt pocket 1,
One end connects the first dust and gas entrance 1.1 and the first dedusting impact tube 1.2 inside first dirt pocket 1, setting
The first cleaning system 1.3 in the inner bottom part of the first dirt pocket 1, it is arranged at the inside of the first dirt pocket 1 and positioned at described
The second cleaning system 1.4 and the dust and gas in the top sidewall of the first dirt pocket 1 of the top of first cleaning system 1.3 go out
Mouth 1.5.
The first ash bucket 1.31 that first cleaning system 1.3 includes being used for storing dedusting aqueous medium, it is arranged at described the
The first water level control apparatus 1.32 in the top outer of one ash bucket 1.31, be arranged at the outside of the first ash bucket 1.31 and with it is described
First overflow mechanism 1.33 of the first water level control apparatus 1.32 connection and it is arranged at the of the bottom of the first ash bucket 1.31
One blowdown apparatus 1.34.The first dedusting impact tube 1.2 is curve bend or F type bend pipes, the first dedusting impact tube 1.2
Upper end connected with the first dust and gas entrance 1.1, the lower end surface of the first dedusting impact tube 1.2 to first ash bucket
The distance of liquid level in 1.31 is 12cm.The end face end face of first dedusting impact tube 1.2 is to the liquid in first ash bucket 1.31
Face can make the running resistance of deduster excessive apart from size, can cause the equipment motor to be burned when serious, apart from it is excessive when again
It is unable to reach preferable efficiency of dust collection.First water level control apparatus 1.32 is used cooperatively with the first overflow mechanism 1.33, can be kept
The default constant water level of liquid level in deduster running, and can the water level of regulating liquid surface is just at any time according to actual needs.
Second cleaning system 1.4 include be fixed on the side wall of the first dirt pocket 1 first support 1.41, be located at
The first woven wire group 1.42 in the first support 1.41, be arranged at the top of the first woven wire group 1.42 first
Spray equipment 1.43 and the first pulse blockage-clearing device 1.44 for being arranged at the top of the first spray equipment 1.43.Described first
Woven wire group 1.42 is the network structure being stacked by multiple layer metal silk screen layer, and its shape can be yi word pattern, V-type or W types.
The the first woven wire manhole overhauled for the first woven wire group 1.42 is additionally provided with the outer wall of first dirt pocket 1
6, so as to maintenance repair；The first pulse blockage-clearing device 1.44, which can be cleared up regularly, to be bonded above the first woven wire group 1.42
Dust, it is to avoid it is blocked.In addition, the first spray equipment 1.43 can also adjust the water level in the first ash bucket 1.31 at any time, when
When liquid level is less than preset water level, regulation switch is allowed to the retaining into the first ash bucket 1.31, so as to ensure the dedusting of whole deduster
Efficiency.
Second dirt pocket 2 include be arranged on the supermedial second dust and gas entrance 2.1 of the side wall of the second dirt pocket 2,
One end connects the second dust and gas entrance 2.1 and the second dedusting impact tube 2.2 inside second dirt pocket 2, setting
The 3rd cleaning system 2.3 in the inner bottom part of the second dirt pocket 2, it is arranged at the inside of the second dirt pocket 2 and positioned at described
4th cleaning system 2.4 of the top of the 3rd cleaning system 2.3, be arranged at it is in second dirt pocket 2 and net positioned at the described 4th
Dehydration device 2.5 above change system and the net gas outlet 2.6 in the top sidewall of the second dirt pocket 2；It is described net
Gas outlet 2.6 is connected with the exhaust equipment that is located at outside deduster and can make to produce negative pressure inside deduster.
The second ash bucket 2.31 that 3rd cleaning system 2.3 includes being used for storing dedusting aqueous medium, it is arranged at described the
Second water level control apparatus 2.32 of the top outer of two ash bucket 2.31, it is arranged at the outside of second ash bucket 2.31 and with described the
Second overflow mechanism 2.33 of two water level control apparatus 2.32 connection and it is arranged at the second of the bottom of the second ash bucket 2.31
Blowdown apparatus 2.34.The second dedusting impact tube 2.2 be curve bend F type bend pipes, the second dedusting impact tube 2.2 it is upper
End is connected with the second dust and gas entrance 2.1, in the lower surface of the second dedusting impact tube 2.2 to second ash bucket 2.31
Liquid level distance be 12cm.The end face end face of second dedusting impact tube 2.2 to the liquid level in second ash bucket 2.31 away from
Can make the running resistance of deduster excessive from size, equipment motor can be caused to be burned when serious, apart from it is excessive when can not reach again
To preferable efficiency of dust collection.Second water level control apparatus 2.32 is used cooperatively with the second overflow mechanism 2.33, can keep deduster
The default constant water level of liquid level in running, and can the water level of regulating liquid surface is just at any time according to actual needs.
4th cleaning system 2.4 include be fixed on the side wall of the second dirt pocket 2 second support 2.41, be located at
The second woven wire group 2.42 in the second support 2.41, be arranged at the top of the second woven wire group 2.42 second
Spray equipment 2.43 and the second pulse blockage-clearing device 2.44 for being arranged at the top of the second spray equipment 2.43.Described second
Woven wire group 2.42 is the network structure being stacked by multiple layer metal silk screen layer, and its shape can be yi word pattern, V-type or W types.
The the second woven wire manhole overhauled for the second woven wire group 2.42 is additionally provided with the outer wall of second dirt pocket 2
7, so as to maintenance repair.The second pulse blockage-clearing device 2.44, which can be cleared up regularly, to be bonded above the second woven wire group 2.42
Dust, it is to avoid it is blocked.In addition, the second spray equipment 2.43 can also adjust the water level in the second ash bucket 2.31 at any time, when
When liquid level is less than preset water level, regulation switch is allowed to the retaining into the second ash bucket 2.31, so as to ensure the dedusting of whole deduster
Efficiency.
One side roof part of the transition chamber 3 is connected with the dust and gas outlet 1.5 of first dirt pocket 1, and its is relative
Connected in the middle part of opposite side with the second dust and gas entrance 2.1 of second dirt pocket 2.
Work is in use, Details as Follows：
It is first turned on being connected with twin-stage Water-bath silk net efficiency dust catcher and can sets the exhausting that negative pressure is produced inside deduster
It is standby, make to form negative pressure in whole casing 4, now, dusty gas enters the first dedusting impulse pipe 1.2 from the first dust and gas entrance 1.1
Afterwards, sprayed at a high speed from the first dedusting impulse pipe 1.2 with certain speed in the presence of negative pressure, into the first cleaning system 1.3,
The liquid level impacted in the first ash bucket 1.31, evokes grit thick in a large amount of foams and water droplet, dusty gas directly in pond
Sedimentation, the coarse granule and mud being deposited in the first ash bucket 1.31 are by the first periodically discharge, dedusting now of blowdown apparatus 1.34
Efficiency can reach 50~60%.Dusty gas is after the disengaging of the liquid level of the first ash bucket 1.31 because the effect of negative pressure continues towards top
Second cleaning system 1.4, due to the effect for the first spray equipment 1.43 that the top of the first woven wire group 1.42 is provided with so that gold
The micronic dust that category silk screen surface is formd in moisture film, dusty gas needs to break through moisture film when by the first woven wire group 1.42,
The inertial collision effect produced in the process makes part micronic dust be captured by the moisture film containing water droplet, and captured dust is with metal
The current that silk screen interlayer flows downward flow into the first ash bucket 1.31, are then discharged with current from the first overflow mechanism 1.33, now
Efficiency of dust collection can reach 90~95%.
In order to further reduce concentration of emission, dusty gas is not discharged directly by the gas after the second cleaning system 1.4,
But transition chamber 3 is entered by the dust and gas outlet 1.5 in the top sidewall of the first dirt pocket 1, then the second dedusting is passed through by transition chamber 3
The second dust and gas entrance 2.1 on the side wall of room 2 enters the purified treatment that the second dirt pocket 2 carries out second circulation.That is ash-laden gas
Body enters after the second dedusting impulse pipe 2.2 from the second dust and gas entrance 2.1, is removed in the presence of negative pressure with certain speed from second
Dirt impulse pipe 2.2 sprays at a high speed, into the 3rd cleaning system 2.3, and the liquid level impacted in the second ash bucket 2.31 evokes a large amount of foams
And water droplet, dusty gas further cleaned and purified, and the coarse granule and mud being deposited in the second ash bucket 2.31 are by
The two periodically discharges of blowdown apparatus 2.34, efficiency of dust collection now can reach 96~99%.Dusty gas is from the liquid of the second ash bucket 2.31
Emaciated face continues towards the 4th cleaning system 2.4 on top from the rear effect because of negative pressure, due to the top of the second woven wire group 2.42
The effect for the second spray equipment 2.43 being provided with so that the micronic dust that woven wire surface is formd in moisture film, dusty gas is leading to
Need to break through moisture film when crossing the second woven wire group 1.42, the inertial collision effect produced in the process make part micronic dust by containing
The moisture film for having water droplet is captured again, and the current that captured dust flows downward with woven wire interlayer flow into the second ash bucket
2.31, then discharged with current from the second overflow mechanism 2.33, efficiency of dust collection now can reach more than 99.5%, concentration of emission
It is entirely capable of reaching new discharging standards.Because purified gas contains moisture content, if directly discharging, produced by negative pressure
The problem of equipment is stained with ash is easily caused during equipment, so gas continues through dehydration device 2.5 after the 4th cleaning system 2.4
Discharged after dehydration from the net gas outlet 2.6 in the top sidewall of the second dirt pocket 2, whole purification process terminates.
Twin-stage Water-bath silk net efficiency dust catcher of the present utility model is provided with two dirt pockets, four sets of cleaning systems, using water
The mode that bath cleaning dust mechanism and filtering type purification techniques are combined, can capture fine dust, farthest purify dust-laden
Gas, in addition, the characteristics of simple in construction, convenient operating maintenance of the present utility model and water-saving consumption-reduction.
Preferred embodiment of the present utility model is the foregoing is only, the utility model is not limited to, for this
For the technical staff in field, the utility model can have various modifications and variations.It is all it is of the present utility model spirit and principle
Within, any modifications, equivalent substitutions and improvements made etc. should be included within protection domain of the present utility model.
Claims (7)
1. a kind of twin-stage Water-bath silk net efficiency dust catcher, it is characterised in that including casing (4) and under the casing (4)
Side be used for support the deduster of whole twin-stage Water-bath silk net efficiency dust catcher to support (5)；The casing (4) includes being respectively positioned on it
Internal the first dirt pocket (1), transition chamber (3) and the second dirt pocket (2)；
First dirt pocket (1) includes being arranged on the supermedial first dust and gas entrance of the first dirt pocket (1) side wall
(1.1), one end connects the first dust and gas entrance (1.1) and positioned at internal the first dedusting impact of first dirt pocket (1)
(1.2) are managed, the first cleaning system (1.3) of the first dirt pocket (1) inner bottom part is arranged at, is arranged at first dirt pocket
(1) internal and the second cleaning system (1.4) above first cleaning system (1.3) and positioned at first dedusting
Dust and gas outlet (1.5) in room (1) top sidewall；
Second dirt pocket (2) includes being arranged on the supermedial second dust and gas entrance of the second dirt pocket (2) side wall
(2.1), one end connects the second dust and gas entrance (2.1) and positioned at internal the second dedusting impact of second dirt pocket (2)
(2.2) are managed, the 3rd cleaning system (2.3) of the second dirt pocket (2) inner bottom part is arranged at, is arranged at second dirt pocket
(2) internal and the 4th cleaning system (2.4) above the 3rd cleaning system (2.3), it is arranged at second dedusting
Dehydration device (2.5) in room (2) and above the 4th cleaning system and at the top of second dirt pocket (2)
Net gas outlet (2.6) on the wall of side；
One side roof part of the transition chamber (3) is connected with the dust and gas outlet (1.5) of first dirt pocket (1), and its is relative
Opposite side in the middle part of connected with the second dust and gas entrance (2.1) of second dirt pocket (2).
2. a kind of twin-stage Water-bath silk net efficiency dust catcher according to claim 1, it is characterised in that the first purification system
System (1.3) is including being used to store the first ash bucket (1.31) of dedusting aqueous medium, being arranged at outside the first ash bucket (1.31) top
The first water level control apparatus (1.32) on side, be arranged on the outside of first ash bucket (1.31) and with first water level regulation
The first overflow mechanism (1.33) of device (1.32) connection and the first blowdown for being arranged at the first ash bucket (1.31) bottom
Device (1.34)；
Second cleaning system (1.4) includes first support (1.41), the position being fixed on the wall of the first dirt pocket (1) side
In the first woven wire group (1.42) in the first support (1.41), it is arranged on the first woven wire group (1.42)
The first spray equipment (1.43) of side and the first pulse blockage-clearing device being arranged above first spray equipment (1.43)
(1.44)。
3. a kind of twin-stage Water-bath silk net efficiency dust catcher according to claim 2, it is characterised in that the first dedusting punching
Pipe (1.2) is hit for bend pipe, its upper end is connected with the first dust and gas entrance (1.1), under the first dedusting impact tube (1.2)
The distance for holding end face to the liquid level in first ash bucket (1.31) is 10-15cm.
4. a kind of twin-stage Water-bath silk net efficiency dust catcher according to claim 3, it is characterised in that the 3rd purification system
System (2.3) is including being used to store the second ash bucket (2.31) of dedusting aqueous medium, being arranged at outside the second ash bucket (2.31) top
The second water level control apparatus (2.32) of side, it is arranged on the outside of second ash bucket (2.31) and is filled with second water level regulation
The second overflow mechanism (2.33) for putting (2.32) connection and the second blowdown dress for being arranged at the second ash bucket (2.31) bottom
Put (2.34)；
4th cleaning system (2.4) includes second support (2.41), the position being fixed on the wall of the second dirt pocket (2) side
In the second woven wire group (2.42) in the second support (2.41), it is arranged on the second woven wire group (2.42)
The second spray equipment (2.43) of side and the second pulse blockage-clearing device being arranged above second spray equipment (2.43)
(2.44)。
5. a kind of twin-stage Water-bath silk net efficiency dust catcher according to claim 4, it is characterised in that the second dedusting punching
Pipe (2.2) is hit for bend pipe, its upper end is connected with the second dust and gas entrance (2.1), under the second dedusting impact tube (2.2)
The distance for holding end face to the liquid level in second ash bucket (2.31) is 10-15cm.
6. a kind of twin-stage Water-bath silk net efficiency dust catcher according to claim 5, it is characterised in that also including being arranged at
State on the first dirt pocket (1) outer wall be used for the first woven wire group (1.42) overhaul the first woven wire manhole (6),
Being arranged at is used for the second woven wire inspection that the second woven wire group (2.42) is overhauled on the second dirt pocket (2) outer wall
Repair hole (7) and two deduster manholes (8) on the casing (4) outer wall.
7. a kind of twin-stage Water-bath silk net efficiency dust catcher according to claim 6, it is characterised in that first wire
Net group (1.42) and the second woven wire group (2.42) are the network structure being stacked by multiple layer metal silk screen layer, the metal
Silk screen is yi word pattern, V-type or W types.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621466626.2U CN206325359U (en) | 2016-12-29 | 2016-12-29 | A kind of twin-stage Water-bath silk net efficiency dust catcher |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201621466626.2U CN206325359U (en) | 2016-12-29 | 2016-12-29 | A kind of twin-stage Water-bath silk net efficiency dust catcher |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN206325359U true CN206325359U (en) | 2017-07-14 |
Family
ID=59293260
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201621466626.2U Active CN206325359U (en) | 2016-12-29 | 2016-12-29 | A kind of twin-stage Water-bath silk net efficiency dust catcher |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN206325359U (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109589731A (en) * | 2018-12-14 | 2019-04-09 | 王永 | A kind of intelligent dust collector |
-
2016
- 2016-12-29 CN CN201621466626.2U patent/CN206325359U/en active Active
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN109589731A (en) * | 2018-12-14 | 2019-04-09 | 王永 | A kind of intelligent dust collector |
| CN109589731B (en) * | 2018-12-14 | 2021-03-12 | 苏州吴越合成消防科技有限公司 | Intelligent dust removal device |
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