CN109331571A - A capacitor welding waste gas treatment system - Google Patents
A capacitor welding waste gas treatment system Download PDFInfo
- Publication number
- CN109331571A CN109331571A CN201811435682.3A CN201811435682A CN109331571A CN 109331571 A CN109331571 A CN 109331571A CN 201811435682 A CN201811435682 A CN 201811435682A CN 109331571 A CN109331571 A CN 109331571A
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- China
- Prior art keywords
- filter cotton
- cotton column
- capping
- column
- tube body
- Prior art date
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- 238000003466 welding Methods 0.000 title claims abstract description 17
- 239000003990 capacitor Substances 0.000 title claims abstract description 15
- 239000002912 waste gas Substances 0.000 title 1
- 229920000742 Cotton Polymers 0.000 claims abstract description 110
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims abstract description 49
- 230000008602 contraction Effects 0.000 claims abstract description 33
- 239000000428 dust Substances 0.000 claims abstract description 29
- 238000001914 filtration Methods 0.000 claims description 10
- 238000007789 sealing Methods 0.000 claims description 6
- 238000005476 soldering Methods 0.000 abstract description 9
- 230000000505 pernicious effect Effects 0.000 abstract description 6
- 239000007789 gas Substances 0.000 description 32
- 238000001179 sorption measurement Methods 0.000 description 7
- 230000009471 action Effects 0.000 description 5
- 230000006872 improvement Effects 0.000 description 5
- 229910052799 carbon Inorganic materials 0.000 description 3
- 238000000034 method Methods 0.000 description 3
- 238000010521 absorption reaction Methods 0.000 description 2
- 239000000809 air pollutant Substances 0.000 description 2
- 231100001243 air pollutant Toxicity 0.000 description 2
- 239000003610 charcoal Substances 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000000694 effects Effects 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 230000035939 shock Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 239000003496 welding fume Substances 0.000 description 2
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000000903 blocking effect Effects 0.000 description 1
- 230000008859 change Effects 0.000 description 1
- 230000007812 deficiency Effects 0.000 description 1
- 230000005611 electricity Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 239000003500 flue dust Substances 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000002184 metal Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 206010035653 pneumoconiosis Diseases 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
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
- B01D46/24—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies
- B01D46/2403—Particle separators, e.g. dust precipitators, using rigid hollow filter bodies characterised by the physical shape or structure of the filtering element
- B01D46/2418—Honeycomb filters
-
- 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
- B01D46/56—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition
- B01D46/58—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in parallel
- B01D46/60—Filters or filtering processes specially modified for separating dispersed particles from gases or vapours with multiple filtering elements, characterised by their mutual disposition connected in parallel arranged concentrically or coaxially
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/02—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography
- B01D53/04—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols by adsorption, e.g. preparative gas chromatography with stationary adsorbents
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2253/00—Adsorbents used in seperation treatment of gases and vapours
- B01D2253/10—Inorganic adsorbents
- B01D2253/102—Carbon
-
- 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)
- Physics & Mathematics (AREA)
- Geometry (AREA)
- Engineering & Computer Science (AREA)
- Analytical Chemistry (AREA)
- General Chemical & Material Sciences (AREA)
- Oil, Petroleum & Natural Gas (AREA)
- Filtering Of Dispersed Particles In Gases (AREA)
Abstract
The present invention relates to a kind of capacitor welding exhaust treatment systems, including inverted cone shape gas gathering mask, centrifugal blower, dust filter unit, activated carbon adsorber, dust filter unit includes tube body, the middle section of tube body is equipped with contraction section, the inner wall of contraction section is hyperboloid of one sheet structure, the inside of tube body is equipped with the first filter cotton column and the second filter cotton column, the inner cavity of tube body is separated into the first surge chamber between the first filter cotton column and the second filter cotton column by the first filter cotton column and the second filter cotton column, the second surge chamber between the first filter cotton column and the first capping, third surge chamber between the second filter cotton column and the second capping, the inside of second surge chamber is equipped with the first spring, the inside of third surge chamber is equipped with second spring.Dust in soldering exhaust gas is removed by dust filter unit, and pernicious gas is tightly held by activated carbon tower removing；The long service life of the first filter cotton column, the second filter cotton column in dust filter unit, the replacement frequency is low, and implementation result is good.
Description
Technical field
The present invention relates to a kind of capacitor welding exhaust treatment systems, belong to capacitor manufacturing technology field.
Background technique
In capacitor fabrication process, it usually needs carry out a large amount of soldering operation.And weldering is also easy to produce during soldering
Connect exhaust gas, the gas and dust that welding exhaust gas as generates in the welding process.General soldering exhaust gas is direct by negative tube
It is discharged to outdoor, weld fumes is that the steam generated upon an over-temperature condition by metal and nonmetallic substance is formed through aoxidizing and condensing
's.Therefore the chemical component of welding fume, depending on welding material and soldered material composition and its difficulty or ease of evaporation.It is long-term to inhale
Electric welder pneumoconiosis can be occurred by entering to be welded dust.For this purpose, many countries have worked out special safety sanitary standard to welding operating environment.
Highest is allowed dense in " welding fume sanitary standard in workshop air " (GB 16194-1996) regulation workshop air that China promulgates
Degree is 6mg/m3.For there is the weld fumes for concentrating blowdown stack that should execute " discharge standard of air pollutants ".
Currently, generalling use dry filter when being purified to soldering exhaust gas and first filtering out flue dust, then recycle
For activated carbon adsorber by pernicious gas to being adsorbed and removed, activated carbon adsorber is internally provided with the adsorption layer made of active carbon.
In the dry filter course of work, with the intensification of filtration time, dry filter inner filtration layer close to air inlet that
The specific drainage pressure of side can increased dramatically, and need to be replaced frequently so as to cause filter layer, and filter layer close to gas outlet that
The specific drainage pressure of side then changes less, but the part can not usually utilize.
Summary of the invention
The present invention is in view of the deficienciess of the prior art, provide a kind of capacitor welding exhaust treatment system, specific skill
Art scheme is as follows:
A kind of capacitor welding exhaust treatment system, including inverted cone shape gas gathering mask, centrifugal blower, dust filter unit, activity
Charcoal adsorption tower, the input terminal of centrifugal blower are connected to the inner cavity of gas gathering mask, and three are provided between centrifugal blower and dust filter unit
It is logical, first fittings in the output end and threeway of centrifugal blower；Dust filter unit includes tube body, and the head end of tube body is fixed
There is the first capping, the tail end of tube body is installed with the second capping, and the middle section of tube body is provided with contraction section, and the inner wall of contraction section is single leaf
Hyperboloid structure, tube body are internally provided with the first filter cotton column and the second filter cotton column, and the setting of the first filter cotton column is being shunk
The other side of contraction section is arranged in the side of section, the second filter cotton column, and the inner cavity of tube body is filtered by the first filter cotton column and second
Cotton column is separated into the first surge chamber between the first filter cotton column and the second filter cotton column, is located at the first filter cotton column and the
The second surge chamber between one capping, the third surge chamber between the second filter cotton column and the second capping, the second surge chamber
Be internally provided with the first spring, the head end of the first spring is fixedly connected with the first filter cotton column, the tail end of the first spring and
One capping is fixedly connected, and the middle part of the first capping is provided with first through hole, and the outside of the first capping is provided with the first connecting leg, and first
The head end of connecting leg is connected to first through hole, and the first solenoid valve, the first solenoid valve are provided between the tail end and threeway of the first connecting leg
Input terminal and threeway in second fittings, the output end of the first solenoid valve is connected to the tail end of the first connecting leg；Third
Surge chamber is internally provided with second spring, and the head end of second spring is fixedly connected with the second filter cotton column, the tail of second spring
End is fixedly connected with the second capping, and the middle part of the second capping is provided with the second through-hole, and the outside of the second capping is provided with the second company
Pipe, the head end of the second connecting leg is connected to the second through-hole, is provided with second solenoid valve between the tail end and threeway of the second connecting leg, and second
The tail end of third fittings in the input terminal and threeway of solenoid valve, the output end of second solenoid valve and the second connecting leg connects
It is logical；The side wall of contraction section is provided with third through-hole, and the outside of contraction section is provided with third connecting leg, the head end and third of third connecting leg
Through-hole connection, the tail end of third connecting leg are connected to the air inlet of activated carbon adsorber.
As an improvement of the above technical solution, the head end of the tube body is connect with the first closure threads, the head of the tube body
The first sealing ring is provided between end and the first capping；The tail end of the tube body is connect with the second closure threads, the tube body
The second sealing ring is provided between tail end and the second capping.
As an improvement of the above technical solution, the first filter cotton column and the second filter cotton column are cylindric.
As an improvement of the above technical solution, the length of the first filter cotton column is equal to the length of the second filter cotton column,
The diameter of the first filter cotton column is equal to the diameter of the second filter cotton column.
As an improvement of the above technical solution, the diameter of the first filter cotton column is greater than the minimum diameter of contraction section, institute
The diameter for stating the second filter cotton column is greater than the minimum diameter of contraction section.
Beneficial effects of the present invention:
Soldering exhaust gas first pass through dust filter unit remove dust, remaining pernicious gas be tightly held by activated carbon tower to remove,
So that the tail gas of discharge meets discharge standard.The use of the first filter cotton column, the second filter cotton column in the dust filter unit
Service life is long, and the replacement frequency is low, and implementation result is good.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of capacitor welding exhaust treatment system of the present invention；
Fig. 2 is the structural schematic diagram of dust filter unit of the present invention.
Specific embodiment
In order to make the objectives, technical solutions, and advantages of the present invention clearer, with reference to the accompanying drawings and embodiments, right
The present invention is further elaborated.It should be appreciated that the specific embodiments described herein are merely illustrative of the present invention, and
It is not used in the restriction present invention.
As shown in Fig. 1~2, the capacitor welding exhaust treatment system, including inverted cone shape gas gathering mask 10, centrifugal blower
20, the input terminal of dust filter unit 60, activated carbon adsorber 80, centrifugal blower 20 is connected to the inner cavity of gas gathering mask 10, is centrifuged wind
Threeway 30 is provided between machine 20 and dust filter unit 60, the output end of centrifugal blower 20 and first connector in threeway 30 connect
It is logical；Dust filter unit 60 includes tube body 61, and the head end of tube body 61 is installed with the first capping 62, and the tail end of tube body 61 is installed with second
Capping 63, the middle section of tube body 61 are provided with contraction section 611, and the inner wall of contraction section 611 is hyperboloid of one sheet structure, contraction section 611
Outer wall be hyperboloid of one sheet structure, tube body 61 is internally provided with the first filter cotton column 64 and the second filter cotton column 65, first
The side of contraction section 611 is arranged in filter cotton column 64, and the other side of contraction section 611, tube body 61 is arranged in the second filter cotton column 65
Inner cavity be separated by the first filter cotton column 64 and the second filter cotton column 65 positioned at the first filter cotton column 64 and the second filter cotton column
The first surge chamber 66 between 65, the second surge chamber 67 between the first filter cotton column 64 and the first capping 62 are located at the
Third surge chamber 68 between two filter cotton columns 65 and the second capping 63, the second surge chamber 67 are internally provided with the first spring
69, the head end of the first spring 69 is fixedly connected with the first filter cotton column 64, and the tail end of the first spring 69 and the first capping 62 are fixed
The middle part of connection, the first capping 62 is provided with first through hole, and first through hole is connected to the second surge chamber 67, outside the first capping 62
Portion is provided with the first connecting leg 613, and the head end of the first connecting leg 613 is connected to first through hole, the tail end of the first connecting leg 613 and threeway 30
Between be provided with the first solenoid valve 40, the input terminal and second fittings in threeway 30 of the first solenoid valve 40, the first electricity
The output end of magnet valve 40 is connected to the tail end of the first connecting leg 613；Third surge chamber 68 is internally provided with second spring 610, and
The head end of two springs 610 is fixedly connected with the second filter cotton column 65, the tail end of second spring 610 and the fixed company of the second capping 63
It connects, the middle part of the second capping 63 is provided with the second through-hole, and the second through-hole is connected to third surge chamber 68, the outside of the second capping 63
Be provided with the second connecting leg 614, the head end of the second connecting leg 614 is connected to the second through-hole, the tail end of the second connecting leg 614 and threeway 30 it
Between be provided with second solenoid valve 50, the input terminal and the third fittings in threeway 30 of second solenoid valve 50, the second electromagnetism
The output end of valve 50 is connected to the tail end of the second connecting leg 614；The side wall of contraction section 611 is provided with third through-hole 612, third through-hole
612 are connected to the first surge chamber 66, and the outside of contraction section 611 is provided with third connecting leg 615, the head end of third connecting leg 615 and
The connection of three through-holes 612, the tail end of third connecting leg 615 are connected to the air inlet of activated carbon adsorber 80.
Soldering operation is carried out in workbench 90, the exhaust gas that soldering generates is collected by gas gathering mask 10, in centrifugal blower 20
Under driving, exhaust gas passes through threeway 30, and first solenoid valve 40 is according to opening 1 hour, close 1 hour, open 1 hour suitable again
Sequence carries out ON/OFF operation；The second solenoid valve 50 is carried out according to the sequence for closing hour, opening 1 hour, turn off 1 hour
ON/OFF operation, when first solenoid valve 40 is opened, the second solenoid valve 50 is in close state；First electromagnetism
When valve 40 is closed, the second solenoid valve 50 is in the open state.
When the first solenoid valve 40 is opened, the second solenoid valve 50 is in close state, at this point, exhaust gas connects by first
Pipe 613, the second surge chamber 67, the first filter cotton column 64 enter the first surge chamber 66；The air pressure exported due to centrifugal blower 20
For positive pressure, although by the consumption of the first filter cotton column 64, air pressure inside the first surge chamber 66 also greater than atmospheric pressure, because
This, the air pressure inside the first surge chamber 66 at this time is greater than the air pressure inside third surge chamber 68, even if the second filter cotton column 65 and
That one end that second spring 610 is connected is blocked by dust, under the action of pressure difference, chocking-up degree can be also reduced, to avoid
In the later period, use increased dramatically the specific drainage pressure of second filter cotton column 65, extend the service life of the second filter cotton column 65, reduce
Replacement frequency.The gas outlet of the activated carbon adsorber 80 is provided with aspiration pump 70, and the pumping end of aspiration pump 70 and active carbon are inhaled
The gas outlet of attached tower 80 is connected to, under the action of aspiration pump 70, the air inlet and activated carbon adsorber 80 of activated carbon adsorber 80
Gas outlet between there are pressure differences, under the action of pressure difference, promote the air-flow filtered by dust filter unit 60 by active carbon inhale
Activated carbon adsorption layer 81 inside attached tower 80, the pernicious gas in air-flow are tightly held by activated carbon the absorption of layer 81, after final purification
Gas extracts outer be discharged in atmosphere out by aspiration pump 70.
Similarly, when second solenoid valve 50 is opened, first solenoid valve 40 is in close state, at this point, exhaust gas passes through
Second connecting leg 614, third surge chamber 68, the second filter cotton column 65 enter the first surge chamber 66；Due in the first surge chamber 66
The air pressure in portion is greater than atmospheric pressure, and the air pressure inside the first surge chamber 66 is greater than the air pressure inside the second surge chamber 67, even if first
That one end that filter cotton column 64 is connected with the first spring 69 is blocked by dust, under the action of pressure difference, can also reduce blocking journey
Degree, to avoid the specific drainage pressure of the first filter cotton column 64 in the later period, use be increased dramatically, and extend making for the first filter cotton column 64
With the service life, replacement frequency is reduced.Under the action of aspiration pump 70, the air inlet and activated carbon adsorber 80 of activated carbon adsorber 80
Gas outlet between there are pressure difference, promote the air-flow filtered by dust filter unit 60 by the activity inside activated carbon adsorber 80
Charcoal adsorption layer 81, the pernicious gas in air-flow are tightly held by activated carbon the absorption of layer 81, and the gas after final purification is taken out by aspiration pump 70
It is discharged in atmosphere out.
For being consistent property, the first filter cotton column 64 and the second filter cotton column 65 are cylindric.First mistake
The length of filter pulp column 64 is equal to the length of the second filter cotton column 65, and the diameter of the first filter cotton column 64 is equal to the second filter cotton
The diameter of column 65.The diameter of the first filter cotton column 64 is greater than the minimum diameter of contraction section 611, the second filter cotton column 65
Diameter be greater than contraction section 611 minimum diameter.
When gas shock the first filter cotton column 64, the first filter cotton column 64 can be promoted to be compressed, this aspect can make
First spring 69 is stretched, while the first filter cotton column 64 can also be made to be tucked into contraction section 611, and contraction section 611 is interior
Wall is hyperboloid of one sheet structure, and the outer wall of contraction section 611 is hyperboloid of one sheet structure, this can not only guarantee the first surge chamber 66 with
It is completely separated by the first filter cotton column 64 between second surge chamber 67, and contraction section 611 can be close by the first filter cotton column 64
That one end of contraction section 611 is to clamping；When the first spring 69 is when drawing the first filter cotton column 64 mobile to the first capping 62, first
The both ends of filter cotton column 64 can all be stretched, and so as to effectively avoid the first filter cotton column 64 from being compacted, avoid the first filtering
The specific drainage pressure of cotton column 64 increased dramatically.Similarly, second spring 610 is set, and second spring 610 and contraction section 611 cooperate, avoid
The specific drainage pressure of first filter cotton column 64 increased dramatically.
Further, for convenience of subsequent the first filter cotton of dismounting and change column 64 and the second filter cotton column 65；The tube body 61
Head end 62 is threadedly coupled with the first capping, the head end of the tube body 61 and first covers and is provided with the first sealing ring between 62；
The tail end of the tube body 61 63 is threadedly coupled with the second capping, and the tail end of the tube body 61 and second covers and is provided with the between 63
Two sealing rings.
In the above-described embodiments, in 60 course of work of dust filter unit, the first filter cotton column 64 or the second filter cotton column
65 while being filtered operation, additionally it is possible to using residual air to corresponding second filter cotton column 65 or the first filter cotton column 64 into
Row washes away, recycle the first spring 69 or second spring 610 cooperate 611 pairs of contraction section by gas shock, the first filtering of compacting
Cotton column 64 or the second filter cotton column 65 are stretched, to avoid the specific filtration resistance of the first filter cotton column 64 or the second filter cotton column 65
Resistance increased dramatically；In turn, it is conducive to extend the service life of the first filter cotton column 64, the second filter cotton column 65, reduces by the
The replacement frequency of one filter cotton column 64, the second filter cotton column 65.For example, 64 He of the first filter cotton column in the dust filter unit 60
Second filter cotton column 65 is primary in replacement in 4~5 months；In the case where same filtration time and filtering traffic, using two
Cylinder filter, it is identical with the first filter cotton column 64 or 65 structure of the second filter cotton column in being internally provided with for cylinder filter
Filter column will be replaced primary for the Filter column usual 1~2 month.
Soldering exhaust gas first passes through dust filter unit 60 and removes dust, and remaining pernicious gas is tightly held by activated carbon tower 80 to removing
It goes, so that the tail gas of discharge meets " discharge standard of air pollutants ".Since dust is first removed, the activated carbon adsorption
The service life of activated carbon adsorption layer 81 is extended in tower 80, and the recovery value of activated carbon adsorption layer 81 significantly improves.The powder
The long service life of the first filter cotton column 64, the second filter cotton column 65 in dirt filter 60, the replacement frequency is low, implementation result
It is good.
The foregoing is merely illustrative of the preferred embodiments of the present invention, is not intended to limit the invention, all in essence of the invention
Made any modifications, equivalent replacements, and improvements etc., should all be included in the protection scope of the present invention within mind and principle.
Claims (5)
1. a kind of capacitor welding exhaust treatment system, including inverted cone shape gas gathering mask (10), centrifugal blower (20), dust filter unit
(60), the input terminal of activated carbon adsorber (80), centrifugal blower (20) is connected to the inner cavity of gas gathering mask (10), it is characterised in that:
It is provided between centrifugal blower (20) and dust filter unit (60) threeway (30), the output end of centrifugal blower (20) and threeway (30)
In first fittings；Dust filter unit (60) includes tube body (61), and the head end of tube body (61) is installed with the first capping
(62), the tail end of tube body (61) is installed with the second capping (63), and the middle section of tube body (61) is provided with contraction section (611), contraction section
(611) inner wall is hyperboloid of one sheet structure, and tube body (61) is internally provided with the first filter cotton column (64) and the second filter cotton
Column (65), the setting of the first filter cotton column (64) are arranged in the side of contraction section (611), the second filter cotton column (65) in contraction section
(611) inner cavity of the other side, tube body (61) is separated by the first filter cotton column (64) and the second filter cotton column (65) positioned at
The first surge chamber (66) between one filter cotton column (64) and the second filter cotton column (65) is located at the first filter cotton column (64) and the
The second surge chamber (67) between one capping (62), the third between the second filter cotton column (65) and the second capping (63) are slow
It rushes room (68), the second surge chamber (67) is internally provided with the first spring (69), the head end of the first spring (69) and the first filtering
Cotton column (64) is fixedly connected, and the tail end of the first spring (69) is fixedly connected with the first capping (62), the middle part of the first capping (62)
It is provided with first through hole, the outside of the first capping (62) is provided with the first connecting leg (613), the head end of the first connecting leg (613) and the
The connection of one through-hole, is provided with the first solenoid valve (40), the first solenoid valve between the tail end and threeway (30) of the first connecting leg (613)
(40) second fittings in input terminal and threeway (30), the output end and the first connecting leg of the first solenoid valve (40)
(613) tail end connection；Third surge chamber (68) is internally provided with second spring (610), the head end of second spring (610) with
Second filter cotton column (65) is fixedly connected, and the tail end of second spring (610) is fixedly connected with the second capping (63), the second capping
(63) the second through-hole is provided in the middle part of, the outside of the second capping (63) is provided with the second connecting leg (614), the second connecting leg (614)
Head end be connected to the second through-hole, be provided with second solenoid valve (50) between the tail end and threeway (30) of the second connecting leg (614),
The input terminal and the third fittings in threeway (30) of two solenoid valves (50), the output end and second of second solenoid valve (50)
The tail end of connecting leg (614) is connected to；The side wall of contraction section (611) is provided with third through-hole (612), and the outside of contraction section (611) is set
It is equipped with third connecting leg (615), the head end of third connecting leg (615) is connected to third through-hole (612), the tail end of third connecting leg (615)
It is connected to the air inlet of activated carbon adsorber (80).
2. a kind of capacitor welding exhaust treatment system according to claim 1, it is characterised in that: the tube body (61)
Head end is threadedly coupled with the first capping (62), is provided with the first sealing between the head end of the tube body (61) and the first capping (62)
Circle；The tail end of the tube body (61) is threadedly coupled with the second capping (63), the tail end of the tube body (61) and the second capping (63)
Between be provided with the second sealing ring.
3. a kind of capacitor welding exhaust treatment system according to claim 1, it is characterised in that: first filter cotton
Column (64) and the second filter cotton column (65) are cylindric.
4. a kind of capacitor welding exhaust treatment system according to claim 3, it is characterised in that: first filter cotton
The length of column (64) is equal to the length of the second filter cotton column (65), and the diameter of the first filter cotton column (64) is equal to the second filtering
The diameter of cotton column (65).
5. a kind of capacitor welding exhaust treatment system according to claim 3, it is characterised in that: first filter cotton
The diameter of column (64) is greater than the minimum diameter of contraction section (611), and the diameter of the second filter cotton column (65) is greater than contraction section
(611) minimum diameter.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811435682.3A CN109331571B (en) | 2018-11-28 | 2018-11-28 | A capacitor welding waste gas treatment system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201811435682.3A CN109331571B (en) | 2018-11-28 | 2018-11-28 | A capacitor welding waste gas treatment system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN109331571A true CN109331571A (en) | 2019-02-15 |
| CN109331571B CN109331571B (en) | 2023-10-10 |
Family
ID=65318521
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201811435682.3A Active CN109331571B (en) | 2018-11-28 | 2018-11-28 | A capacitor welding waste gas treatment system |
Country Status (1)
| Country | Link |
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| CN (1) | CN109331571B (en) |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN115282703A (en) * | 2022-04-06 | 2022-11-04 | 江西轻竺科技股份有限公司 | Waste gas pulse type dust remover for resin production |
Citations (8)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| DE7406960U (en) * | 1974-02-28 | 1976-02-26 | Hunsche, Hartmut, 4354 Datteln | FABRIC FILTER WITH DEVICE FOR GENERATING A PULSING VIBRATION EFFECT DURING THE PURGE AIR PHASE |
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| CN108246015A (en) * | 2018-03-10 | 2018-07-06 | 日照兴业汽车配件有限公司 | Dust pelletizing system |
| CN209188364U (en) * | 2018-11-28 | 2019-08-02 | 铜陵市新洲电子科技有限责任公司 | A kind of capacitor welding exhaust treatment system |
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| DE7406960U (en) * | 1974-02-28 | 1976-02-26 | Hunsche, Hartmut, 4354 Datteln | FABRIC FILTER WITH DEVICE FOR GENERATING A PULSING VIBRATION EFFECT DURING THE PURGE AIR PHASE |
| RU2014872C1 (en) * | 1991-09-19 | 1994-06-30 | Акционерное общество "НПО Стромэкология, Лтд." | Filter for cleaning gases |
| KR20020047474A (en) * | 2000-12-13 | 2002-06-22 | 이후근 | Air purifier with oxygen supplier |
| CN101209390A (en) * | 2006-12-26 | 2008-07-02 | 吴万权 | Device for adsorbing, desorbing and purifying organic gas |
| CN101732941A (en) * | 2009-12-29 | 2010-06-16 | 李见成 | Waste gas continuous purification device |
| CN206881505U (en) * | 2017-06-05 | 2018-01-16 | 苏州科技大学 | A kind of combination type photocatalysis purifier |
| CN108246015A (en) * | 2018-03-10 | 2018-07-06 | 日照兴业汽车配件有限公司 | Dust pelletizing system |
| CN209188364U (en) * | 2018-11-28 | 2019-08-02 | 铜陵市新洲电子科技有限责任公司 | A kind of capacitor welding exhaust treatment system |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN115282703A (en) * | 2022-04-06 | 2022-11-04 | 江西轻竺科技股份有限公司 | Waste gas pulse type dust remover for resin production |
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| CN109331571B (en) | 2023-10-10 |
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