CN105286725A - Dust collector for purifying air - Google Patents
Dust collector for purifying air Download PDFInfo
- Publication number
- CN105286725A CN105286725A CN201510781014.6A CN201510781014A CN105286725A CN 105286725 A CN105286725 A CN 105286725A CN 201510781014 A CN201510781014 A CN 201510781014A CN 105286725 A CN105286725 A CN 105286725A
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- CN
- China
- Prior art keywords
- catalyst
- dust catcher
- base
- dust
- air
- 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.)
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- 239000000428 dust Substances 0.000 title claims abstract description 64
- 239000003054 catalyst Substances 0.000 claims abstract description 26
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 claims description 16
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 claims description 15
- 238000001914 filtration Methods 0.000 claims description 13
- 239000003426 co-catalyst Substances 0.000 claims description 12
- 239000013078 crystal Substances 0.000 claims description 11
- 239000000203 mixture Substances 0.000 claims description 9
- 239000002073 nanorod Substances 0.000 claims description 8
- 229910021536 Zeolite Inorganic materials 0.000 claims description 7
- 230000015572 biosynthetic process Effects 0.000 claims description 7
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 claims description 7
- 239000010457 zeolite Substances 0.000 claims description 7
- 229910052709 silver Inorganic materials 0.000 claims description 6
- 239000004408 titanium dioxide Substances 0.000 claims description 6
- XEEYBQQBJWHFJM-UHFFFAOYSA-N iron Substances [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 claims description 5
- 239000010936 titanium Substances 0.000 claims description 4
- 229910052684 Cerium Inorganic materials 0.000 claims description 3
- DQMUQFUTDWISTM-UHFFFAOYSA-N O.[O-2].[Fe+2].[Fe+2].[O-2] Chemical compound O.[O-2].[Fe+2].[Fe+2].[O-2] DQMUQFUTDWISTM-UHFFFAOYSA-N 0.000 claims description 3
- 229910000420 cerium oxide Inorganic materials 0.000 claims description 3
- 238000007596 consolidation process Methods 0.000 claims description 3
- 229910052742 iron Inorganic materials 0.000 claims description 3
- 238000002156 mixing Methods 0.000 claims description 3
- BMMGVYCKOGBVEV-UHFFFAOYSA-N oxo(oxoceriooxy)cerium Chemical compound [Ce]=O.O=[Ce]=O BMMGVYCKOGBVEV-UHFFFAOYSA-N 0.000 claims description 3
- 230000002093 peripheral effect Effects 0.000 claims description 3
- 239000011148 porous material Substances 0.000 claims description 3
- 239000004332 silver Substances 0.000 claims description 3
- 229910052719 titanium Inorganic materials 0.000 claims description 3
- 239000003344 environmental pollutant Substances 0.000 abstract 1
- 231100000719 pollutant Toxicity 0.000 abstract 1
- MWUXSHHQAYIFBG-UHFFFAOYSA-N Nitric oxide Chemical compound O=[N] MWUXSHHQAYIFBG-UHFFFAOYSA-N 0.000 description 15
- XTQHKBHJIVJGKJ-UHFFFAOYSA-N sulfur monoxide Chemical compound S=O XTQHKBHJIVJGKJ-UHFFFAOYSA-N 0.000 description 7
- 230000000052 comparative effect Effects 0.000 description 6
- 230000000694 effects Effects 0.000 description 3
- 239000007789 gas Substances 0.000 description 3
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 description 2
- 229910052799 carbon Inorganic materials 0.000 description 2
- 230000002079 cooperative effect Effects 0.000 description 2
- 238000013461 design Methods 0.000 description 2
- 239000003517 fume Substances 0.000 description 2
- 239000008187 granular material Substances 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000001802 infusion Methods 0.000 description 2
- 238000000034 method Methods 0.000 description 2
- 230000035699 permeability Effects 0.000 description 2
- 238000002360 preparation method Methods 0.000 description 2
- 230000008569 process Effects 0.000 description 2
- 238000004887 air purification Methods 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- 125000003118 aryl group Chemical group 0.000 description 1
- 230000004888 barrier function Effects 0.000 description 1
- 239000000356 contaminant Substances 0.000 description 1
- 230000008878 coupling Effects 0.000 description 1
- 238000010168 coupling process Methods 0.000 description 1
- 238000005859 coupling reaction Methods 0.000 description 1
- 238000003795 desorption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000005284 excitation Effects 0.000 description 1
- 238000001027 hydrothermal synthesis Methods 0.000 description 1
- 230000006872 improvement Effects 0.000 description 1
- 229940099596 manganese sulfate Drugs 0.000 description 1
- 235000007079 manganese sulphate Nutrition 0.000 description 1
- 239000011702 manganese sulphate Substances 0.000 description 1
- SQQMAOCOWKFBNP-UHFFFAOYSA-L manganese(II) sulfate Chemical compound [Mn+2].[O-]S([O-])(=O)=O SQQMAOCOWKFBNP-UHFFFAOYSA-L 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 239000012286 potassium permanganate Substances 0.000 description 1
- 239000000047 product Substances 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 230000009467 reduction Effects 0.000 description 1
- 238000005201 scrubbing Methods 0.000 description 1
- 238000007789 sealing Methods 0.000 description 1
- 239000007921 spray Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 210000001138 tear Anatomy 0.000 description 1
- 238000012360 testing method Methods 0.000 description 1
Landscapes
- Catalysts (AREA)
Abstract
The invention discloses a dust collector for purifying air. The dust collector comprises a shell, an air inlet, an air outlet and a motor, wherein the air inlet and the air outlet are formed in the shell, and the motor is arranged in the shell. The shell comprises an upper shell body and a dust collecting container. The upper shell body is fixed to the dust collecting container. The dust collector further comprises a cyclone filter which is arranged in the shell and filters air entering the dust collector. The cyclone filter is provided with a filter element. A filter paper tube is composed of two filter paper layers and a catalyst layer sandwiched between the two filter paper layers. While the filter element of the dust collector filters dust, the pollutant content in the air in a room is reduced.
Description
Technical field
The present invention relates to dust catcher and technical field of air purification, be specifically related to a kind of dust catcher purified air.
Background technology
Dust catcher can be divided into vertical, horizontal and portable by structure.The operation principle of dust catcher is, utilizes motor band moving vane High Rotation Speed, in the housing of sealing, produce air negative pressure, draws dirt bits.
Dust catcher, primarily of playing dirt, dust suction, filter dirt three part composition, generally comprises series excitation commutator motor, centrifugal fan, dirt catcher (bag) and dust suction annex.The power of general dust catcher is 400-1000W or higher, and the power of portable dust collector is generally 250W and following.The dedusting of dust catcher energy, is mainly that its " head " is equipped with an electric exhaust fan.The rotating shaft of air exhauster there is fan blade, after energising, air exhauster can produce extremely strong suction and pressure with the rotating speed of 500 circles per second, under the effect of suction and pressure, air is discharged at a high speed, and the air of vacuum part, blower fan front end constantly supplements the air in blower fan, dust catcher inside is caused to produce instantaneous vacuum, form Negative Pressure Difference with external atmosphere pressure, under the effect of this pressure reduction, suck the air containing dust.Dust and other impurities enters bag dust filter by carpet or floor cleaner brush, long pipe, bend pipe, flexible pipe, hose coupling successively, and dust and other impurities is trapped in bag dust filter, and air after filter disc purification, then is discharged by body afterbody.
The operation principle of dust catcher is motor of dust collector High Rotation Speed; air is sucked from suction inlet; dirt case is made to produce certain vacuum; dust enters the bag dust filter in dirt case by scrubbing brush, adapter, handle, flexible pipe, main suction pipe; dust is left in bag dust filter; air after filtration enters motor through one deck filter again; this layer of filter prevents the dirt bag dust that breaks from sucking one protective barrier of motor; the air entering motor flows out through motor; because in motor operation, carbon brush constantly weares and teares, add again before therefore flowing out dust catcher and filtered together.Filtering material is finer and closely woven, and just air filtration can be obtained dust catcher cleaner, but air permeability is poorer, have impact on the air quantity that motor sucks like this, reduces dust catcher efficiency.Its air permeability is lower, therefore all does waviness to increase vapor permeation area.
But existing dust catcher filter element, the main consideration of its design is filter dust.But in current indoor environment, owing to being rich in a large amount of gaseous state and fume in air, these gaseous states and fume are attached on dust granule.When dust suction, it is from dust granule surface desorption, thus reenters the gas of indoor environment, causes air again to be polluted.
Summary of the invention
The object of the invention is to propose a kind of novel filter element for dust collector, it can when dust catcher works, the gaseous contaminant in purifying air, the haze etc. in such as nitrogen oxide, oxysulfide, aromatic pollution and air.
For reaching this object, the present invention by the following technical solutions:
A kind of dust catcher purified air, comprise housing, the motor be located at air inlet on housing and air outlet and be located in housing, described housing comprises upper shell and dust collecting container, described upper shell is fixed on described dust catcher on described dust collecting container and also comprises the cyclone filter being arranged at and filtering the gas entering dust catcher in housing, described cyclone filter possesses filter core, it comprises the base having the upper bracket of medium pore and have end groove that filter core two ends are circular concentric respectively, be provided with by hoop and pole consolidation all-in-one-piece hollow backbone between upper bracket and base, hollow backbone between upper bracket bottom surface annular groove and cup dolly is peripheral, the cylindrical shape of affixed continuous catadioptric constant amplitude gauffer filters paper web, it is characterized in that:
A. the cylindric gauffer filtering paper web catadioptric is continuously the top margin trapezoidal gauffer that base is outside inwards;
B. the base of end groove is had to form the top margin base frame plate that base is outside inwards;
C. the hoop periphery being consolidated into hollow backbone with pole is formed with the outside trapezoidal frame plate in base;
Described filtration paper cylinder is made up of two layers of filter paper layer and the catalyst layer be mixed between two layers of filter paper layer, and the catalyst that described catalyst layer adopts comprises carrier, active component and co-catalyst.
Described carrier is the mixture of the manganese dioxide nano-rod of zeolite and δ-crystal formation, and the mass ratio of mixing is 2:1-1:2, in the skeleton structure of zeolite, Si/ (Si+Al+P) mol ratio is 0.20.
Described active component is the mixture of titanium dioxide and cerium oxide, and the mol ratio of Ti and Ce is 4:3, and described titanium dioxide is anatase crystal.Described active component weight content is in the catalyst 0.3%-10%, preferred 0.5-%-8%, more preferably 2%-5%.Such as, 0.8%, 1%, 1.5%, 2%, 2.5%, 3%, 3.5%, 4%, 4.5%, 5%, 5.5%, 6%, 6.5%, 7%, 7.5%.
Described co-catalyst is silver and di-iron trioxide, and the mol ratio of Ag and Fe is 2:5, and described co-catalyst weight content is in the catalyst 0.3%-6%, preferred 0.5%-5%.Such as, 0.8%, 1%, 1.5%, 2%, 2.5%, 3%, 3.5%, 4%, 4.5%, 5%, 5.5%.
Preferably, the weight ratio of described active component and co-catalyst is 5:1 ~ 2:1.Such as 4.5:1,4:1,3.5:1,3:1,2.5:1.
The preparation method of the manganese dioxide nano-rod of δ-crystal formation is as follows: in 240 DEG C of hydro-thermal reaction 24h after 1.5g potassium permanganate and 0.275g manganese sulfate mix, the manganese dioxide nano-rod of obtained δ-crystal formation.
The preparation method of described catalyst can take conventional infusion process and other alternatives, the prior art unrestricted choice that those skilled in the art can grasp according to it, and the present invention repeats no more.
The present invention is by choosing the mixture of the manganese dioxide nano-rod of specific zeolite and δ-crystal formation as carrier, and the Ti/Ce choosing special ratios is as active component, Ag/Fe is as co-catalyst, this catalyst is made to produce cooperative effect, make that the control of this catalyst to the nitrogen oxide in air, aromatic compound and haze is efficient reaches 100%, purified room air greatly.
Detailed description of the invention
The present invention is described catalyst of the present invention by following embodiment.
Embodiment 1
Catalyst is prepared by infusion process, carrier is the mixture of the manganese dioxide nano-rod of zeolite and δ-crystal formation, the mass ratio of mixing is 1:1, in the skeleton structure of zeolite, Si/ (Si+Al+P) mol ratio is 0.20, active component is the mixture of titanium dioxide and cerium oxide, the mol ratio of Ti and Ce is 4:3, and described titanium dioxide is anatase crystal, described active component weight content is in the catalyst 5%, co-catalyst is silver and di-iron trioxide, and the mol ratio of Ag and Fe is 2:5, and described co-catalyst weight content is in the catalyst 2%.
Described catalyst spray is entrained between two layers of filter paper, continuous catadioptric constant amplitude gauffer forms cylindric filtration paper web, this filtration paper web is purified the filter element for dust collector of air according to following structural design, comprising filter core two ends is having the upper bracket of medium pore and having the base of end groove of circular concentric respectively, be provided with by hoop and pole consolidation all-in-one-piece hollow backbone between upper bracket and base, hollow backbone between upper bracket bottom surface annular groove and cup dolly is peripheral, the cylindrical shape of affixed continuous catadioptric constant amplitude gauffer filters paper web, it is characterized in that:
A. the cylindric gauffer filtering paper web catadioptric is continuously the top margin trapezoidal gauffer that base is outside inwards;
B. the base of end groove is had to form the top margin base frame plate that base is outside inwards;
C. the hoop periphery being consolidated into hollow backbone with pole is formed with the outside trapezoidal frame plate in base.
Described filter core is applied to dust catcher of the present invention, a kind of dust catcher purified air, the motor comprising housing, be located at air inlet on housing and air outlet and be located in housing, described housing comprises upper shell and dust collecting container, described upper shell is fixed on described dust catcher on described dust collecting container and also comprises the cyclone filter being arranged at and filtering the gas entering dust catcher in housing, and described cyclone filter possesses filter core.
Window when PM2.5 is 300, make indoor PM2.5 identical with outdoor, close the doors and windows, test PM2.5 after 1 hour, its value is only 12.
Through detecting, the content of Nitrogen Oxides in Indoor Air and oxysulfide all drops to less than 0.1 milligram/cubic metre, is far smaller than the requirement of the Indoor Air Quality standards that GB/T18883-2002 specifies.
Comparative example 1
The carrier of embodiment 1 is replaced with active carbon, and all the other conditions are constant, and the PM2.5 value after 1 hour is 56, and the value of oxide and oxysulfide is all higher than 1 milligram/cubic metre.
Comparative example 2
The Ce of embodiment 1 is replaced with La, and all the other conditions are constant, and the PM2.5 value after 1 hour is 48, and the value of oxide and oxysulfide is all higher than 1 milligram/cubic metre.
Comparative example 3
The Fe of embodiment 1 is replaced with Co, and all the other conditions are constant, and the PM2.5 value after 1 hour is 32, and the value of oxide and oxysulfide is all higher than 1 milligram/cubic metre.
Comparative example 4
The carrier of embodiment 1 is replaced with α-crystal formation manganese dioxide nano-rod, all the other conditions are constant, and the PM2.5 value after 1 hour is 32, and the value of nitrogen oxide and oxysulfide is all higher than 1 milligram/cubic metre.
Comparative example 5
The carrier of embodiment 1 is replaced with the manganese dioxide nano-rod of beta-crystal, all the other conditions are constant, and the PM2.5 value after 1 hour is 32, and the value of nitrogen oxide and oxysulfide is all higher than 1 milligram/cubic metre.
Above-described embodiment and comparative example illustrate, there is specific contact between several component of catalyst of the present invention, omit or replace wherein one or more, all can not reach the certain effects of the application, prove to which create cooperative effect.
Applicant states, the present invention illustrates catalyst of the present invention by above-described embodiment, but the present invention is not limited to above-mentioned catalyst, does not namely mean that the present invention must rely on above-mentioned detailed catalysts and could implement.Person of ordinary skill in the field should understand, any improvement in the present invention, to equivalence replacement and the interpolation of auxiliary element, the concrete way choice etc. of each raw material of product of the present invention, all drops within protection scope of the present invention and open scope.
Claims (5)
1. the dust catcher purified air, comprise housing, the motor be located at air inlet on housing and air outlet and be located in housing, described housing comprises upper shell and dust collecting container, described upper shell is fixed on described dust catcher on described dust collecting container and also comprises the cyclone filter being arranged at and filtering the gas entering dust catcher in housing, described cyclone filter possesses filter core, it comprises the base having the upper bracket of medium pore and have end groove that filter core two ends are circular concentric respectively, be provided with by hoop and pole consolidation all-in-one-piece hollow backbone between upper bracket and base, hollow backbone between upper bracket bottom surface annular groove and cup dolly is peripheral, the cylindrical shape of affixed continuous catadioptric constant amplitude gauffer filters paper web, it is characterized in that,
A. the cylindric gauffer filtering paper web catadioptric is continuously the top margin trapezoidal gauffer that base is outside inwards;
B. the base of end groove is had to form the top margin base frame plate that base is outside inwards;
C. the hoop periphery being consolidated into hollow backbone with pole is formed with the outside trapezoidal frame plate in base;
Described filtration paper cylinder is made up of two layers of filter paper layer and the catalyst layer be mixed between two layers of filter paper layer, and the catalyst that described catalyst layer adopts comprises carrier, active component and co-catalyst;
Described carrier is the mixture of the manganese dioxide nano-rod of zeolite and δ-crystal formation, and the mass ratio of mixing is 2:1-1:2, and in the skeleton structure of zeolite, Si/ (Si+Al+P) mol ratio is 0.20;
Described active component is the mixture of titanium dioxide and cerium oxide, and the mol ratio of Ti and Ce is 4:3, and described titanium dioxide is anatase crystal, and described active component weight content is in the catalyst 0.3%-10%;
Described co-catalyst is silver and di-iron trioxide, and the mol ratio of Ag and Fe is 2:5, and described co-catalyst weight content is in the catalyst 0.3%-6%.
2. dust catcher as claimed in claim 1, it is characterized in that, described active component weight content is in the catalyst 0.5-%-8%.
3. dust catcher as claimed in claim 2, it is characterized in that, described active component weight content is in the catalyst 2%-5%.
4. dust catcher as claimed in claim 1, it is characterized in that, described co-catalyst weight content is in the catalyst 0.5%-5%.
5. dust catcher as claimed in claim 1, it is characterized in that, the weight ratio of described active component and co-catalyst is 5:1 ~ 2:1.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510781014.6A CN105286725A (en) | 2015-11-13 | 2015-11-13 | Dust collector for purifying air |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510781014.6A CN105286725A (en) | 2015-11-13 | 2015-11-13 | Dust collector for purifying air |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN105286725A true CN105286725A (en) | 2016-02-03 |
Family
ID=55185070
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201510781014.6A Withdrawn CN105286725A (en) | 2015-11-13 | 2015-11-13 | Dust collector for purifying air |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN105286725A (en) |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1181886A2 (en) * | 2000-08-19 | 2002-02-27 | Lg Electronics Inc. | Cyclone dust collector and vacuum cleaner using such dust collector |
| JP2003190061A (en) * | 2001-12-12 | 2003-07-08 | Samsung Kwangju Electronics Co Ltd | Cyclone dust collector for vacuum cleaner |
| CN1919132A (en) * | 2005-08-22 | 2007-02-28 | 乐金电子(天津)电器有限公司 | Filter element for dust collector |
| CN104069867A (en) * | 2014-07-11 | 2014-10-01 | 武汉大学 | Monolithic catalyst as well as preparation method and application thereof |
-
2015
- 2015-11-13 CN CN201510781014.6A patent/CN105286725A/en not_active Withdrawn
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP1181886A2 (en) * | 2000-08-19 | 2002-02-27 | Lg Electronics Inc. | Cyclone dust collector and vacuum cleaner using such dust collector |
| JP2003190061A (en) * | 2001-12-12 | 2003-07-08 | Samsung Kwangju Electronics Co Ltd | Cyclone dust collector for vacuum cleaner |
| CN1919132A (en) * | 2005-08-22 | 2007-02-28 | 乐金电子(天津)电器有限公司 | Filter element for dust collector |
| CN104069867A (en) * | 2014-07-11 | 2014-10-01 | 武汉大学 | Monolithic catalyst as well as preparation method and application thereof |
Non-Patent Citations (1)
| Title |
|---|
| 韦薇等: "Ce0.6Zr0.4O2/γ-Al2O3复合粉体的制备及其结构研究", 《楚雄师范学院学报》 * |
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Application publication date: 20160203 |