CN105433865A - Air-purifying dust collector filter element - Google Patents

Air-purifying dust collector filter element Download PDF

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Publication number
CN105433865A
CN105433865A CN201510780129.3A CN201510780129A CN105433865A CN 105433865 A CN105433865 A CN 105433865A CN 201510780129 A CN201510780129 A CN 201510780129A CN 105433865 A CN105433865 A CN 105433865A
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CN
China
Prior art keywords
base
air
filter element
filter
dust collector
Prior art date
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Withdrawn
Application number
CN201510780129.3A
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Chinese (zh)
Inventor
沈秋
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Wuxi Qingyang Machinery Manufacturing Co Ltd
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Wuxi Qingyang Machinery Manufacturing Co Ltd
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Priority to CN201510780129.3A priority Critical patent/CN105433865A/en
Publication of CN105433865A publication Critical patent/CN105433865A/en
Withdrawn legal-status Critical Current

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Classifications

    • A—HUMAN NECESSITIES
    • A47—FURNITURE; DOMESTIC ARTICLES OR APPLIANCES; COFFEE MILLS; SPICE MILLS; SUCTION CLEANERS IN GENERAL
    • A47L—DOMESTIC WASHING OR CLEANING; SUCTION CLEANERS IN GENERAL
    • A47L9/00—Details or accessories of suction cleaners, e.g. mechanical means for controlling the suction or for effecting pulsating action; Storing devices specially adapted to suction cleaners or parts thereof; Carrying-vehicles specially adapted for suction cleaners
    • A47L9/10—Filters; Dust separators; Dust removal; Automatic exchange of filters
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01D—SEPARATION
    • B01D50/00—Combinations of methods or devices for separating particles from gases or vapours
    • 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/54—Nitrogen compounds
    • B01D53/56—Nitrogen oxides
    • B01D53/565—Nitrogen oxides by treating the gases with solids
    • 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/46—Removing components of defined structure
    • B01D53/72—Organic compounds not provided for in groups B01D53/48 - B01D53/70, e.g. hydrocarbons
    • 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86—Catalytic processes
    • B01D53/8621—Removing nitrogen compounds
    • B01D53/8625—Nitrogen oxides
    • B01D53/8628—Processes characterised by a specific catalyst
    • 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86—Catalytic processes
    • B01D53/8621—Removing nitrogen compounds
    • B01D53/8625—Nitrogen oxides
    • B01D53/8631—Processes characterised by a specific device
    • 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86—Catalytic processes
    • B01D53/8668—Removing organic compounds not provided for in B01D53/8603 - B01D53/8665
    • 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
    • B01D53/34—Chemical or biological purification of waste gases
    • B01D53/74—General processes for purification of waste gases; Apparatus or devices specially adapted therefor
    • B01D53/86—Catalytic processes
    • B01D53/88—Handling or mounting catalysts
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/002—Mixed oxides other than spinels, e.g. perovskite
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J35/00—Catalysts, in general, characterised by their form or physical properties
    • B01J35/19—Catalysts containing parts with different compositions
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J21/00—Catalysts comprising the elements, oxides, or hydroxides of magnesium, boron, aluminium, carbon, silicon, titanium, zirconium, or hafnium
    • B01J21/18—Carbon
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/74—Iron group metals
    • B01J23/745—Iron
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J23/00—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00
    • B01J23/70—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper
    • B01J23/76—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36
    • B01J23/83—Catalysts comprising metals or metal oxides or hydroxides, not provided for in group B01J21/00 of the iron group metals or copper combined with metals, oxides or hydroxides provided for in groups B01J23/02 - B01J23/36 with rare earths or actinides
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
    • B01J—CHEMICAL OR PHYSICAL PROCESSES, e.g. CATALYSIS OR COLLOID CHEMISTRY; THEIR RELEVANT APPARATUS
    • B01J2523/00—Constitutive chemical elements of heterogeneous catalysts

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  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Environmental & Geological Engineering (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Health & Medical Sciences (AREA)
  • Biomedical Technology (AREA)
  • Analytical Chemistry (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Materials Engineering (AREA)
  • Organic Chemistry (AREA)
  • Mechanical Engineering (AREA)
  • Catalysts (AREA)

Abstract

The invention discloses an air-purifying dust collector filter element. The two ends of the filter element are provided with an upper support with a central hole and a base with a bottom groove respectively, wherein the upper support and the base are concentric and round. A hollow framework fixedly combined to be a whole through a hoop and a supporting rod is arranged between the upper support and the base, the periphery of the hollow framework between an upper support bottom surface ring groove and the round base is fixedly connected with a cylindrical filtering paper barrel with continuously reverse uniform-amplitude wrinkles. The continuously reverse wrinkles of the cylindrical filtering paper barrel are trapezoidal wrinkles with inward top edges and outward bottom edges; the base with the bottom groove forms a base frame plate with the inward top edge and the outward bottom edge; a trapezoidal frame plate with the outward bottom edge is formed on the periphery of the hoop which is fixedly combined with the supporting rod to be the hollow framework. The filtering paper barrel is composed of two filter paper layers and a catalyst layer mixed up between the two filter paper layers. The content of pollutants in indoor air is reduced while the dust collector filter element filters out dust.

Description

A kind of filter element for dust collector purified air
Technical field
The present invention relates to dust catcher and technical field of air purification, be specifically related to a kind of filter element for dust collector 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 filter element for dust collector purified air, 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 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 described catalyst layer comprises following component,
A) the β type ferrosilite of 20%-60%, shown in described β type ferrosilite is composed as follows:
(x+y)M (2/n)O·xFe 2O 3·yAl 2O 3·zSiO 2·wH 2O
In formula, M represents cation, and n is the valence of cation M, x+y+z=1, z/x to be 100-220, w be more than 1 positive integer, its SiO 2/ Al 2o 3mol ratio be 550-800;
B) GdFeO doped with Ce of 10%-30% 3with TiO 2mixture, Ce:GdFeO 3: TiO 2mol ratio be 0.25:1:2, and described titanium dioxide is anatase crystal;
C) active carbon of surplus.
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, by choosing specific components A and B component, makes said composition produce cooperative effect, such 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
Described composition comprises following component, A) the β type ferrosilite of 40%, shown in described β type ferrosilite is composed as follows: (x+y) M (2/n)oxFe 2o 3yAl 2o 3zSiO 2wH 2o; In formula, M represents Ce, and n is the valence of cation M, and x+y+z=1, z/x are 150, w is 2; B) GdFeO doped with Ce of 30% 3with TiO 2mixture, Ce:GdFeO 3: TiO 2mol ratio be 0.25:1:2, and described titanium dioxide is anatase crystal; C) active carbon of surplus.
Described composition 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.
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 5.
Through detecting, the content of Nitrogen Oxides in Indoor Air and oxysulfide all drops to less than 0.05 milligram/cubic metre, is far smaller than the requirement of the Indoor Air Quality standards that GB/T18883-2002 specifies.
Comparative example 1
Component A content 70%, not containing B component, all the other conditions are constant, and the PM2.5 value after 1 hour is 46, and the value of oxide and oxysulfide is all higher than 1 milligram/cubic metre.
Comparative example 2
B component content 70%, not containing component A, all the other conditions are constant, and the PM2.5 value after 1 hour is 42, and the value of 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 (1)

1. the filter element for dust collector purified air, 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 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 described catalyst layer comprises following component,
A) the β type ferrosilite of 20%-60%, shown in described β type ferrosilite is composed as follows:
(x+y)M (2/n)O·xFe 2O 3·yAl 2O 3·zSiO 2·wH 2O
In formula, M represents cation, and n is the valence of cation M, x+y+z=1, z/x to be 100-220, w be more than 1 positive integer, its SiO 2/ Al 2o 3mol ratio be 550-800;
B) GdFeO doped with Ce of 10%-30% 3with TiO 2mixture, Ce:GdFeO 3: TiO 2mol ratio be 0.25:1:2, and described titanium dioxide is anatase crystal;
C) active carbon of surplus.
CN201510780129.3A 2015-11-13 2015-11-13 Air-purifying dust collector filter element Withdrawn CN105433865A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201510780129.3A CN105433865A (en) 2015-11-13 2015-11-13 Air-purifying dust collector filter element

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Application Number Priority Date Filing Date Title
CN201510780129.3A CN105433865A (en) 2015-11-13 2015-11-13 Air-purifying dust collector filter element

Publications (1)

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Citations (4)

* Cited by examiner, † Cited by third party
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

Patent Citations (4)

* Cited by examiner, † Cited by third party
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)

* Cited by examiner, † Cited by third party
Title
韦薇: "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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