CN110075796A - It is a kind of to receive net stone and preparation method thereof with the CLO purification factor for actively adsorbing micropore - Google Patents
It is a kind of to receive net stone and preparation method thereof with the CLO purification factor for actively adsorbing micropore Download PDFInfo
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- CN110075796A CN110075796A CN201910348165.0A CN201910348165A CN110075796A CN 110075796 A CN110075796 A CN 110075796A CN 201910348165 A CN201910348165 A CN 201910348165A CN 110075796 A CN110075796 A CN 110075796A
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- 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
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- 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
- B01D53/32—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 electrical effects other than those provided for in group B01D61/00
-
- 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
- B01D53/81—Solid phase processes
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- 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
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/10—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising silica or silicate
- B01J20/12—Naturally occurring clays or bleaching earth
-
- 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
- B01J20/00—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof
- B01J20/02—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material
- B01J20/20—Solid sorbent compositions or filter aid compositions; Sorbents for chromatography; Processes for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbon; comprising carbon obtained by carbonising processes
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C15/00—Disintegrating by milling members in the form of rollers or balls co-operating with rings or discs
- B02C15/16—Disintegrating by milling members in the form of rollers or balls co-operating with rings or discs with milling members essentially having different peripheral speeds and in the form of a hollow cylinder or cone and an internal roller or cone
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C7/00—Crushing or disintegrating by disc mills
- B02C7/02—Crushing or disintegrating by disc mills with coaxial discs
- B02C7/08—Crushing or disintegrating by disc mills with coaxial discs with vertical axis
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C7/00—Crushing or disintegrating by disc mills
- B02C7/11—Details
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C7/00—Crushing or disintegrating by disc mills
- B02C7/11—Details
- B02C7/12—Shape or construction of discs
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2258/00—Sources of waste gases
- B01D2258/06—Polluted air
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2259/00—Type of treatment
- B01D2259/80—Employing electric, magnetic, electromagnetic or wave energy, or particle radiation
- B01D2259/818—Employing electrical discharges or the generation of a plasma
Abstract
Net stone and preparation method thereof is received with the CLO purification factor for actively adsorbing micropore the invention discloses a kind of, belong to technical field of air purification, its receive net stone include the first component and the second component, it is characterized in that, the raw material components of first component include solid preparation of chlorine dioxide, and second component includes the raw material components of following parts by weight: 20-25 parts of tourmaline, 8-10 parts of alunite, 8-12 parts of sepiolite, 35-45 parts of attapulgite, 6~9 parts of cocoanut active charcoal；The mass ratio of first component and the second component is 3~6:1.The present invention has the ability of harmful substance in powerful absorption air, moreover it is possible to it is decomposed, enables itself Reusability, can high-efficient purification air, can also make with fresh airization, and with certain health-care effect；The crushing grinding device used in its preparation process can realize preferable smashing and grinding effect, can guarantee complete discharging, and the uniformity to discharge and degree up to standard are higher.
Description
Technical field
The present invention relates to technical field of air purification, be specifically related to it is a kind of with the CLO for actively adsorbing micropore purify because
Son receives net stone and preparation method thereof.
Background technique
In recent years, the environmental consciousness that the problem of environmental pollution and the mankind being on the rise constantly enhance becomes the purification of environment
The development project that people are concerned, with the continuous development of industry, the pollutant that factory discharges into air is increasingly
It is more, therefore people increasingly pay attention to the purification to air quality, consequently also produce many materials for being used for air cleaning, market
On the active carbon purifying product of the product for air cleaning, the photocatalyst spray etc. that often occur.Active carbon granulation pernicious gas
It is not thorough, because it is particularly easy to the case where pernicious gas overflows again and air secondary is caused to pollute occur after adsorption saturation, and
It has a single function, and application value is lower；Photocatalyst spray is at high cost, sprays and applies in air, can only solve to release for the moment
The pernicious gases such as the formaldehyde in air are put into, the essence that can not solve indoor air pollutants acquisition time up to 3~15 years is asked
Topic.Therefore, it is also desirable to develop novel material for air purification, high-efficient purification air is made it have, can Reusability, vdiverse in function
The advantages that.
The production process of air clearing product generally comprises the selection of raw material, raw material crushes polishing, mixing, sizing, pack
And etc., polishing is crushed in raw material and often needs to use crushing grinding device, currently, the crushing of existing crushing grinding device is ground
Grind it is not sufficiently effective, cannot ensure discharging uniformity and degree up to standard.
Summary of the invention
1. technical problems to be solved
The technical problem to be solved in the present invention is that providing a kind of net stone is received with the CLO purification factor for actively adsorbing micropore
And preparation method thereof, the ability with harmful substance in powerful absorption air, moreover it is possible to it be decomposed, so that itself can
Reusability, can high-efficient purification air, can also make with fresh airization, and there is certain health-care effect；It is adopted in its preparation process
Crushing grinding device can realize preferable smashing and grinding effect, can guarantee complete discharging, and the uniformity that discharges and up to standard
It spends higher.
2. technical solution
To solve the above problems, the present invention adopts the following technical scheme that:
It is a kind of to receive net stone, including the first component and the second component with the CLO purification factor for actively adsorbing micropore, described
The raw material components of one component include solid preparation of chlorine dioxide, and second component includes the raw material components of following parts by weight:
20-25 parts of tourmaline, 8-10 parts of alunite, 8-12 parts of sepiolite, 35-45 parts of attapulgite, 6~9 parts of cocoanut active charcoal；It is described
The mass ratio of first component and the second component is 3~6:1；
Further, second component includes the raw material components of following parts by weight: 23 parts of tourmaline, 9 parts of alunite,
10 parts of sepiolite, 40 parts of attapulgite, 7 parts of cocoanut active charcoal；The mass ratio of first component and the second component is 5:1.
Above-mentioned there is the CLO purification factor for actively adsorbing micropore to receive the preparation method of net stone include the following steps:
S1: sepiolite, attapulgite and cocoanut active charcoal of the selection with adsorption capacity and with the electrical of pyroelectric effect
Stone and alunite；
S2: it is carried out after purification processes by sepiolite described in step S1, attapulgite and cocoanut active charcoal and respectively again
It polishes respectively, it is spare then to cross 325 meshes；Tourmaline described in step S1 and alunite mineral material are distinguished into purification processes
It polishes respectively again afterwards, it is spare then to cross 400 meshes；
S3: to step S2, treated that sepiolite, attapulgite and cocoanut active charcoal are modified processing respectively, reactivation
Reaming；
S4: after the mass fraction weigh in step S2 that treated respectively tourmaline, alunite and step S3 processing
Sepiolite, attapulgite and cocoanut active charcoal, then mix, after mixing, be placed in high-intensitive pelletizer into
Row is granulated, and obtains hybrid particles；
S5: hybrid particles obtained in step S4 are dried, and carry out calcination for activation then to get arriving described second group
Point；
S6: weighing the second component obtained in the first component and step S5 according to the ratio, after mixing, using wrappage into
Row package to get described there is the CLO purification factor for actively adsorbing micropore to receive net stone；
Further, the mother liquor used in above-mentioned steps S4 when being granulated is with harmful substance function in adsorbed gas
The extracting solution of plant.The extracting solution can assist promoting the adsorption capacity of the pernicious gases such as the second component PARA FORMALDEHYDE PRILLS(91,95), so as to be promoted
Net stone is received to the effect of air cleaning.
Further, the plant with harmful substance function in adsorbed gas used in above-mentioned steps S4 when being granulated
For at least one of bracketplant, aloe, sansevieria trifasciata, Milan, ivy and rhizoma arisaematis.
Further, wrappage described in above-mentioned steps S6 is non-woven fabrics.
A kind of crushing grinding device, structure have been used when polishing in above-mentioned steps S2 are as follows:
The crushing grinding device include outer case and be set to the intracorporal interior crushing column of outer container, outer pulverization cylinder, upper millstone and
Lower millstone immediately below upper millstone, the interior column that crushes are perpendicular in interior the crushings column in gradually big truncated cone-shaped from top to bottom
Straight centering type fixation is equipped with rotation axis one, and the top end face and bottom face of the outer pulverization cylinder are open, the outer pulverization cylinder set
On the outside of interior crushing column, and the rotation axis one is located on the axis of outer pulverization cylinder, the interior outer surface for crushing column and outside
It is respectively corresponded on the inner surface of pulverization cylinder throughout having compatible crushing tooth one and crushing tooth two；The interior crushing column bottom is fixed
There is the fixed of maximum distance being equal between interior crushing column bottom surface edge and rotation axis one in flat cylindrical body and radius to limit
Disk, the upper millstone are installed on the fixed bottom for limiting disk, and the lower millstone is fixed on the bottom of outer pulverization cylinder, and described turn
The lower end of moving axis one sequentially passes through at the fixed center for limiting disk, upper millstone and lower millstone, opens up at the center of the lower millstone
There is bore to be greater than the discharge port of one diameter of rotation axis；
The top surface of the lower millstone from its side to center at it is progressively lower, the bottom surface of the upper millstone from its side to middle part gradually
It is low, and the bus slope of upper millstone bottom surface is greater than the bus slope of lower millstone top surface, is formed between the upper millstone and lower millstone
The tapered material of ecto-entad grinds channel, and connection discharge port is uniformly fixed on the top surface of the lower millstone along side to lower millstone
It is identical as the rotation direction of the arc convex ribs one of outer pulverization cylinder medial surface junction, each arc convex ribs one, on the bottom surface of the upper millstone
The arc convex ribs two that upper millstone week lateral edge side is arrived at its middle part of connection are uniformly fixed with, the rotation direction of each arc convex ribs two is identical and and arc
Oppositely oriented (in terms of depression angle) of shape convex ribs one；
The inner top of the outer case offers the annular turn trough for being inserted at the top of outer pulverization cylinder, on the outer case top surface
It is connected with the feed pipe being located in annular turn trough ring, the feed pipe is bend pipe, and the feed pipe upper end is fixedly connected with hopper；
The outer case bottom is fixed with the aggregate bin in cone immediately below lower millstone, and the bore of the aggregate bin is from top to bottom
It is gradually small, and the bottom of aggregate bin is connected with discharge nozzle, the discharge nozzle is equipped with switch valve；The lower part of the lower millstone offers
The support turn trough of annular, the support turn trough is interior to be equipped with the support sealing plate for being fixed on aggregate bin top surface side；The lower millstone
Side be equipped with driving gear, the side of the lower millstone is equipped with the gear teeth engaged with driving gear, the driving gear centre
Place's coaxial-type is fixed with rotation axis two, and the rotation axis one and rotation axis two all connects driving motor, the rotation axis one and turn
The rotation direction of moving axis two is identical；One upper end of rotation axis is on the upper surface of outer case, the outer case for rotation axis
One position passed through is equipped with sealing bearing.
Further, the fixed minimum range limited between the corresponding interior crushing column bottom surface edge of disk and rotation axis one
Corresponding endpoint place extends on the outside of interior crushing column in side, and it is interior lateral to have should to be located at the top surface of the part on the outside of interior crushing column
The progressively lower inclined-plane in outer side.The setting on inclined-plane can make to fall in material to be ground on fixed side top surface for limiting disk along the inclined-plane
It tumbles to fixed and limits below disk, advantageously ensure that material is ground completely and smoothly discharges.
Further, the fixed bottom for limiting disk offers the mounting groove for installing the upper millstone, it is described on
Mill is slidably connected in the mounting groove, and the upper surface of the upper millstone passes through the spring being uniformly arranged and is connected to the fixation
Restriction is tried to get to the heart of a matter on face, and the fixed disk that limits is built-in with electromagnet, and the upper millstone is corresponded to and is magnetic built in the position of electromagnet
The permanent magnet to repel each other with electromagnet, when working condition, the repulsion between the electromagnet and permanent magnet is consistently greater than the bullet of spring
The sum of the resistance of power and grinding material to upper millstone.Setting is so that relative to the fixed disk that limits longitudinal direction can occur for upper mould in this way
Sliding, electromagnet generates to the magnetic repulsion of permanent magnet after being powered, overcomes the elastic force of spring, push upper millstone to lower millstone, just
Material in grinding channel can effectively be ground；By the electrical current for regulating and controlling electromagnet, so that it may realize to aforementioned magnetic
The regulation of the size of repulsion is adapted to the material of different-grain diameter requirement so that the adjustment of the width to grinding channel can be realized, into
And improve the application value of the present apparatus.
Further, the side of the upper millstone is formed with sliding panel in a ring, the border side of the mounting groove
On offer the sliding slot one slided up and down for sliding panel of indent；The ring side in one outside of rotation axis is surrounded on the upper millstone
On be equidistantly fixed with sliding shoe, the sliding slot two compatible with sliding shoe of indent is offered in the rotation axis one.With upper
Mill moves up and down adjustment, and sliding panel moves up and down in sliding slot one, and sliding shoe slides in sliding slot two, is not influencing to grind
While moving up and down adjustment of disk can provide preferable leakproofness between upper millstone and fixed restriction disk, be conducive to ensure object
The complete discharging of material；In addition, multiple sliding shoes are equidistantly installed in the sliding groove two on one surface of rotation axis, that is, meet rotation axis
One drives the demand of upper millstone rotation.
Further, the lower end of the rotation axis two is connected to the interior bottom of outer case by plain bearing one, and described turn
The upper end of moving axis two passes through the top panel of outer case and connects driving motor, the position passed through in the outer case for rotation axis two
Equipped with plain bearing one, the lower end of the rotation axis one extends in aggregate bin and is connect by plain bearing two with aggregate bin,
The lower part side of the plain bearing two is equidistantly fixed at least three support quarter butts being connected on the outside of discharge nozzle upper port；Institute
It states the equal fixing sleeve in two upper end of rotation axis and one upper end of rotation axis and the belt wheel for being located at outer case over top, the two described bands is housed
A transmission belt is surrounded on wheel jointly.Driving motor can directly drive the rotation of rotation axis two, and be made up of transmission belt and belt wheel
Belt drive structure drive rotation axis one rotate, so as to make rotation axis one carry out rotation synchronous in the same direction with rotation axis two, drive
Moving gear rotates in same direction with the rotation of rotation axis two, then is driven by the side of lower millstone with the gear teeth for driving gear to engage
Lower millstone carries out the rotation contrary with rotation axis one, to realize mutually opposing turn of interior crushing column and outer pulverization cylinder
It is dynamic, the mutually opposing rotation of lower millstone and upper millstone.
Further, the one lower part fixing sleeve of rotation axis is equipped with the baffle in toroidal, the diameter of the baffle by
It is gradually big under, and the base diameter of the baffle is greater than the outer diameter of plain bearing two, the bottom of the baffle is surrounded on commonly
The outside of bearing two.Baffle can prevent the powder fallen from discharge port from falling on plain bearing two, so that powder is along the baffle
Lateral surface tumble.
3. beneficial effect
(1) in the second component of the invention include sepiolite, attapulgite and cocoanut active charcoal, sepiolite be it is pure natural,
A kind of nontoxic, tasteless hydrous magnesium silicate clay mineral without asbestos, "dead" element has maximum in nonmetallic mineral
Specific surface area (reaching as high as 900m2/g) and unique content cellular structure, be the strongest clay pit of generally acknowledged adsorption capacity
Object；Attapulgite has preferable cationic interchangeability, water imbibition, adsorption bleaching, the feature of environmental protection, big specific surface area (9.6
~36m2/g) and colloid index and expansion capacity, have the good colloidal natures such as unique dispersion, high temperature resistant, salt resistance alkali and compared with
High adsorption bleaching ability, and there is certain plasticity and cohesive force；Cocoanut active charcoal has hole prosperity, absorption property
Well, the advantages that intensity height, Yi Zaisheng, economy and durability, by the toxic component in gas, the ingredient unfavorable to human body or there can be stink
Ingredient remove.Aforementioned three has flourishing absorption micropore, has stronger adsorption capacity；By modification and activation
After reaming, its adsorption strength can be further promoted, enables and receives toxic component in net stone efficient absorption air and other are dirty
Contaminate object.
It (2) include chlorine dioxide in the first component of the invention, molecule outer layer has 19 electronics, can be by Hai Pao
The pernicious gas of the materials such as stone, attapulgite and cocoanut active charcoal absorption resolves into carbon dioxide and water, thus prevents and receives only
Stone adsorption saturation is substantially prolonged and receives the use duration of net stone so that receiving net stone may be reused.
It (3) include tourmaline and alunite in the second component of the invention, tourmaline is a kind of stone charged forever, tool
There are unique piezoelectric effect and pyroelectric effect, air ionization can be made, generates negative aeroion, the anion of the tourmaline of 100 mesh
Burst size is 200IONS, and the anion burst size of the tourmaline of 325 mesh is about 400IONS, the tourmaline of 1250 mesh bear from
Sub- burst size can achieve 800IONS, the work of the generations such as polluter, oxynitrides, the cigarette of anion energy reducing atmosphere
Oxygen, so that air becomes pure and fresh.In addition, tourmaline also has the characteristic for making water negative ionization in a flash, it can be by chlorine dioxide
The water negative ionization in water and air that resolving harmful gas generates, anion water may advantageously facilitate the activity of cell, keep also
Former power, is conducive to human health；Tourmaline can emit the far infrared that the wavelength of referred to as " light of life " is 4-14 microns, with
The wavelength of the far infrared of human-body emitting is close, can generate most effective " resonance " with the hydrone of internal cell, effectively facilitate
The growth and division of cell can assign and receive the function of net stone health-care.Alunite has strong pyroelectric effect, contacts with air
Afterwards, it can polarize, and discharge outward, so that air ionization, generates negative aeroion, plays the effect to purify the air of a room,
It can strengthen and receive net stone due to tourmaline exists and has the function of purification, fresh air.The two cooperation, can service hoisting receive
The ability of harmful substance in net stone removal air, moreover it is possible to make air become pure and fresh, in addition also there is health-care efficacy, make to receive net stone
Application value is promoted.
(4) mother liquor that the present invention is used when being granulated is the extraction with the plant of harmful substance function in adsorbed gas
Liquid can be promoted and receive net stone to the detergent power of gas；And such plant with faint scent can be chosen, it can be promoted and receive net stone
The attraction to consumer also can be improved in using effect.
(5) crushing grinding device of the invention is equipped in the outer case in the gradually interior crushing column of big truncated cone-shaped from top to bottom
And the outer pulverization cylinder on the outside of interior crushing column, channel tapered from top to bottom is formed between interior crushing column and outer pulverization cylinder, it is interior
It crushes and respectively corresponds on the outer surface of column and the inner surface of outer pulverization cylinder throughout having compatible crushing tooth one and crushing tooth two,
It is interior to crush the rotating backward under effect of column and outer pulverization cylinder, material can be crushed step by step, crushing effect is preferable；Interior crushing
Column eccentric setting crushes the gap larger part between column and outer pulverization cylinder inside, and more biggish material is allowed to enter, for
Material of the specification between interior crushing column and outer pulverization cylinder between the minimum spacing of spacing and maximum spacing, can play intermittent
The effect of charging, and then the work load that can avoid interior crushing column and outer pulverization cylinder is exceeded；Interior crushing column bottom is fixed in flat
Shape cylindrical body and radius are equal to the fixed of the maximum distance between interior crushing column bottom surface edge and rotation axis one and limit disk, only
When the partial size of raw material, which is crushed to, is equal to or less than the fixed spacing for limiting disk side and outer pulverization cylinder inner wall, broken raw material
It can just drop down on lower millstone, below standard raw material, which can be trapped in the gap between interior crushing column and outer pulverization cylinder, to be continued to be broken
It is broken, so that it is up to standard to can guarantee that the material for entering grinding channel has been crushed.
(6) crushing grinding device of the invention is equipped in the outer case is installed on the fixed upper millstone for limiting pan bottom
Be located at its immediately below lower millstone, the top surface of lower millstone from its side to center at it is progressively lower so that enter grinding channel object
Material can be mobile to the middle part of lower millstone, in the process, because the width in grinding channel is gradually small along the moving direction of material, upper
Mill and lower millstone rotate backward under effect, can carry out preferable crush and grind to material；Lower millstone and upper millstone it is opposite
It is respectively equipped with oppositely oriented arc convex ribs one and arc convex ribs two on face, rotates backward effect in upper millstone and lower millstone
Under, the arc convex ribs one and arc convex ribs two for the material two sides being stuck in grinding channel can carry out pinching cutting to the material,
It is stuck in grinding channel to can effectively avoid material, and then can promote the complete grinding of material.
(7) upper millstone and the fixed connection relationship limited between disk are set as sliding company by crushing grinding device of the invention
It connects, and fixed limit is equipped with electromagnet in disk, the permanent magnet to repel each other with electromagnetism ferromagnetism is equipped in upper millstone, in the magnetic repulsion
Under effect, grinding channel can be met to the squeezing effect of material；By regulating and controlling the size for the electric current being passed through to electromagnet, can control
The width in channel is ground, to be adapted to the grinding operation of grinding different-grain diameter demand, application value is promoted.
(8) feed pipe on crushing grinding device of the invention is bend pipe, and can play prevents material in smashing and grinding process
The effect of the dust evolution of middle generation；It is inserted in the annular turn trough of the inner top of outer case, and gathers materials at the top of outer pulverization cylinder
Bucket top surface side is fixed with the support sealing plate in the support turn trough of insertion lower millstone bottom, and the top of rotation axis one is across outer
The position of cabinet be equipped with sealing bearing, may make smashing and grinding during generate dust only retain in outer pulverization cylinder, support it is close
Other aforementioned sides in sealing plate and aggregate bin, will not be moved to other intracorporal spaces of outer container also has convenient for being uniformly processed for dust
Conducive to other spaces in maintenance outer case.
To sum up, the present invention has the ability of harmful substance in powerful absorption air, moreover it is possible to it is decomposed, so that from
Body energy Reusability, can high-efficient purification air, can also make with fresh airization, and there is certain health-care effect；Its preparation process
The crushing grinding device of middle use can realize preferable smashing and grinding effect, can guarantee complete discharging, and the uniformity that discharges and
Degree up to standard is higher.
Detailed description of the invention
Fig. 1 is the structural schematic diagram of crushing grinding device of the present invention；
Fig. 2 is the structure enlargement diagram of region A in Fig. 1；
The schematic top plan view that (a) is upper millstone 40 is schemed in Fig. 3, figure (b) is the schematic top plan view of lower millstone 50；
Connection structure diagrammatic top view of the Fig. 4 between upper millstone 40 and rotation axis 1.
Appended drawing reference: 1, feed pipe；2, hopper；3, aggregate bin；4, discharge nozzle；5, switch valve；6, sealing plate is supported；7, it drives
Moving gear；8, rotation axis two；9, driving motor；10, outer case；11, annular turn trough；12, bearing is sealed；13, plain bearing one；
14, plain bearing two；15, quarter butt is supported；16, belt wheel；17, transmission belt；18, baffle；20, interior crushing column；21, rotation axis one；
22, crushing tooth one；30, outer pulverization cylinder；31, crushing tooth two；40, upper millstone；41, arc convex ribs two；42, sliding panel；43, it slides
Block；50, lower millstone；51, discharge port；52, arc convex ribs one；53, turn trough is supported；60, fixed to limit disk；61, inclined-plane；62, pacify
Tankage；63, spring；64, electromagnet；65, permanent magnet；66, sliding slot one；67, sliding slot two；70, channel is ground.
Specific embodiment
The present invention is described in further detail with reference to the accompanying drawings and examples.
Embodiment 1
It is a kind of to receive net stone, including the first component and the second component with the CLO purification factor for actively adsorbing micropore, described
The raw material components of one component include solid preparation of chlorine dioxide, and second component includes the raw material components of following parts by weight:
23 parts of tourmaline, 9 parts of alunite, 10 parts of sepiolite, 40 parts of attapulgite, 7 parts of cocoanut active charcoal；First component and second
The mass ratio of component is 5:1.
Above-mentioned there is the CLO purification factor for actively adsorbing micropore to receive the preparation method of net stone include the following steps:
S1: sepiolite, attapulgite and cocoanut active charcoal of the selection with adsorption capacity and with the electrical of pyroelectric effect
Stone and alunite；
S2: it is carried out after purification processes by sepiolite described in step S1, attapulgite and cocoanut active charcoal and respectively again
It polishes respectively, it is spare then to cross 325 meshes；Tourmaline described in step S1 and alunite mineral material are distinguished into purification processes
It polishes respectively again afterwards, it is spare then to cross 400 meshes；
S3: to step S2, treated that sepiolite, attapulgite and cocoanut active charcoal are modified processing respectively, reactivation
Reaming；
S4: after the mass fraction weigh in step S2 that treated respectively tourmaline, alunite and step S3 processing
Sepiolite, attapulgite and cocoanut active charcoal, then mix, after mixing, be placed in high-intensitive pelletizer into
Row is granulated, and obtains hybrid particles；
S5: hybrid particles obtained in step S4 are dried, and carry out calcination for activation then to get arriving described second group
Point；
S6: weighing the second component obtained in the first component and step S5 according to the ratio, after mixing, using wrappage into
Row package to get described there is the CLO purification factor for actively adsorbing micropore to receive net stone；
In the present embodiment, the mother liquor used in above-mentioned steps S4 when being granulated is with harmful substance function in adsorbed gas
The extracting solution of the plant of energy.The extracting solution can assist promoting the adsorption capacity of the pernicious gases such as the second component PARA FORMALDEHYDE PRILLS(91,95), so as to
It is promoted and receives net stone to the effect of air cleaning.
In the present embodiment, the above-mentioned plant with harmful substance function in adsorbed gas is bracketplant.
In the present embodiment, wrappage described in above-mentioned steps S6 is non-woven fabrics.
A kind of crushing grinding device, structure have been used when polishing in above-mentioned steps S2 are as follows:
As shown in Figure 1, it is described crush grinding device include outer case 10 and interior crushing column 20 in outer case 10, it is outer
Pulverization cylinder 30, upper millstone 40 and the lower millstone 50 immediately below upper millstone 40, the interior crushing column 20 is in gradually big from top to bottom
Truncated cone-shaped, vertical centering type fixation is equipped with rotation axis 1, the top of the outer pulverization cylinder 30 in the interior crushing column 20
Face and bottom face are open, and the outer pulverization cylinder 30 is sheathed on interior 20 outside of crushing column, and the rotation axis 1 is located at outer powder
On the axis of broken cylinder 30, respectively correspond on the inner surface of the interior outer surface for crushing column 20 and outer pulverization cylinder 30 throughout there is Xiang Shi
The crushing tooth 1 and crushing tooth 2 31 matched；As shown in Fig. 2, interior 20 bottom of crushing column is fixed in flat cylindrical body and half
Diameter is equal to the fixed of the maximum distance between interior crushing 20 bottom surface edge of column and rotation axis 1 and limits disk 60, can limit crushing
Enter the partial size of the material in grinding channel 70 afterwards；The upper millstone 40 is installed on the fixed bottom for limiting disk 60, under described
Mill 50 is fixed on the bottom of outer pulverization cylinder 30, and the lower end of the rotation axis 1 sequentially passes through fixed restriction disk 60, upper millstone
40 and lower millstone 50 center at, offered at the center of the lower millstone 50 bore be greater than one 21 diameter of rotation axis discharge port
51；
The top surface of the lower millstone 50 from its side to center at it is progressively lower, the bottom surface of the upper millstone 40 is from its side in
Portion is progressively lower, and the bus slope of 40 bottom surface of upper millstone is greater than the bus slope of 50 top surface of lower millstone, the upper millstone 40 and lower mill
The tapered material of ecto-entad is formed between disk 50 and grinds channel 70, as shown in figure 3, uniformly solid on the top surface of the lower millstone 50
There is connection discharge port 51 along the arc convex ribs 1 on side to lower millstone 50 and outer 30 medial surface junction of pulverization cylinder, each arc is convex surely
The rotation direction of muscle 1 is identical, and connection its middle part to 40 weeks lateral edge sides of upper millstone is uniformly fixed on the bottom surface of the upper millstone 40
The rotation direction of arc convex ribs 2 41, each arc convex ribs 2 41 is identical and oppositely oriented with arc convex ribs 1；
The inner top of the outer case 10 offers the annular turn trough 11 for being inserted at the top of outer pulverization cylinder 30, the outer case
The feed pipe 1 being located in 11 ring of annular turn trough is connected on 10 top surfaces, the feed pipe 1 is bend pipe, 1 upper end of feed pipe
It is fixedly connected with hopper 2；10 bottom of outer case is fixed with the aggregate bin 3 in cone immediately below lower millstone 50, described
The bore of aggregate bin 3 is gradually small from top to bottom, and the bottom of aggregate bin 3 is connected with discharge nozzle 4, and the discharge nozzle 4 is equipped with switch
Valve 5；The lower part of the lower millstone 50 offers the support turn trough 53 of annular, is equipped in the support turn trough 53 and is fixed on aggregate bin
The support sealing plate 6 of 3 top surfaces side；The side of the lower millstone 50 is equipped with driving gear 7, and the side of the lower millstone 50 is equipped with
With the gear teeth that engage of driving gear 7, coaxial-type is fixed with rotation axis 28, the rotation axis 1 at 7 center of driving gear
Driving motor 9 is all connected with rotation axis 28, the rotation axis 1 is identical with the rotation direction of rotation axis 28；The rotation axis
One 21 upper ends pass through the upper surface of outer case 10, are equipped in the outer case 10 for the position that rotation axis 1 passes through and seal bearing
12。
Because the fixed radius for limiting disk 60 is equal to maximum distance of the interior crushing column 20 between side and rotation axis 1, then
It is described it is fixed limit disk 60 it is corresponding in crush the corresponding endpoint of minimum range between 20 bottom surface edge of column and rotation axis 1
Place extends to interior 20 outside of crushing column in side, and the top surface that should be located at the part in interior 20 outside of crushing column is to have inside to outer side
Progressively lower inclined-plane 61.The setting on inclined-plane 61 can make to fall in material to be ground on fixed side top surface for limiting disk 60 along the inclined-plane
It tumbles to fixed and limits 60 lower section of disk, advantageously ensure that material is ground completely and smoothly discharges.
In order to enable the present apparatus that the powder of different-grain diameter requirement is ground, as shown in Fig. 2, the fixed bottom for limiting disk 60
Portion offers the mounting groove 62 for installing the upper millstone 40, and the upper millstone 40 is slidably connected in the mounting groove 62,
The upper surface of the upper millstone 40 passes through the spring 63 being uniformly arranged and is connected on fixed restriction 60 bottom surface of disk, the fixation
It limits disk 60 and is built-in with electromagnet 64, be magnetic built in the position of the corresponding electromagnet 64 of the upper millstone 40 and repel each other with electromagnet 64
Permanent magnet 65, when working condition, the repulsion between the electromagnet 64 and permanent magnet 65 be consistently greater than the elastic force of spring 63 with
Grinding material can avoid upper millstone 40 and opened to the sum of the resistance of upper millstone 40, prevent upper millstone 40 and lower millstone 50
Squeezing effect disappears.So that relative to the fixed disk 60 that limits longitudinal sliding can occur for upper mould, electromagnet 64 is logical for setting in this way
The magnetic repulsion to permanent magnet 65 is generated after electricity, is overcome the elastic force of spring 63, is pushed upper millstone 40 to lower millstone 50, it can be to grinding
Material in channel 70 is effectively ground；By the electrical current for regulating and controlling electromagnet 64, so that it may realize to aforementioned magnetic repulsion
Size regulation, thus can realize to grinding channel 70 width adjustment, be adapted to the material of different-grain diameter requirement, in turn
Improve the application value of the present apparatus.
In order to preferably realize that upper millstone 40 limits being slidably connected for disk 60 with fixed, as shown in Fig. 2, the upper millstone 40
Side be formed with sliding panel 42 in a ring, offered on the border side of the mounting groove 62 indent on sliding panel 42
The sliding slot 1 of lower slider；As shown in figure 4, being surrounded on the upper millstone 40 equidistant on the ring side in one 21 outside of rotation axis
It is fixed with sliding shoe 43, the sliding slot 2 67 compatible with sliding shoe 43 of indent is offered in the rotation axis 1.With upper
Mill 40 moves up and down adjustment, and sliding panel 42 moves up and down in sliding slot 1, and sliding shoe 43 slides in sliding slot 2 67,
While moving up and down adjustment of upper millstone 40 is not influenced, and upper millstone 40 can be provided and fixed limit preferably seals between disk 60
Property, be conducive to the complete discharging for ensureing material；In addition, multiple sliding shoes 43 are equidistantly installed on the sliding on one 21 surface of rotation axis
In slot two, that is, meets the needs of rotation axis 1 drives upper millstone 40 to rotate.
In order to implement the specific driving of the present apparatus, the lower end of the rotation axis 28 is connected by plain bearing 1
To the interior bottom of outer case 10, the upper end of the rotation axis 28 passes through the top panel of outer case 10 and connects driving motor 9, institute
It states and is equipped with plain bearing 1 for the position that rotation axis 28 passes through in outer case 10, the lower end of the rotation axis 1 extends to
It is connect in aggregate bin 3 and by plain bearing 2 14 with aggregate bin 3, the lower part side of the plain bearing 2 14 is equidistantly fixed with
At least three support quarter butts 15 being connected on the outside of 4 upper port of discharge nozzle；28 upper end of rotation axis and one 21 upper end of rotation axis
Equal fixing sleeve is equipped with the belt wheel 16 positioned at 10 over top of outer case, surrounds a transmission belt jointly on the two described belt wheels 16
17.Driving motor 9 can directly drive the rotation of rotation axis 28, and the belt drive structure band being made up of transmission belt 17 and belt wheel 16
Turn moving axis 1 rotates, so as to make rotation axis 1 and rotation axis 28 carry out rotation synchronous in the same direction, drive gear 7 with
The rotation of rotation axis 28 and rotate in same direction, then ground under being driven by the side of lower millstone 50 with the gear teeth that driving gear 7 engage
Disk 50 carries out the rotation contrary with rotation axis 1, interior crushes the mutually opposing of column 20 and outer pulverization cylinder 30 to realize
Rotation, the mutually opposing rotation of lower millstone 50 and upper millstone 40.
It is fallen on plain bearing 2 14 from the powder that discharge port 51 is fallen in order to prevent, one 21 lower part of rotation axis is solid
Surely it is arranged with the baffle 18 in toroidal, the diameter of the baffle 18 is gradually big from top to bottom, and the bottom of the baffle 18 is straight
Diameter is greater than the outer diameter of plain bearing 2 14, and the bottom of the baffle 18 is surrounded on the outside of plain bearing 2 14.Baffle 18 can be prevented
It is only fallen on plain bearing 2 14 from the powder that discharge port 51 is fallen, so that powder is tumbled along the lateral surface of the baffle 18.
The specific action principle of above-mentioned crushing grinding device are as follows:
Start driving motor 9, directly drive rotation axis 28 rotates, the V belt translation being made up of transmission belt 17 and belt wheel 16
Structure drives rotation axis 1 to rotate, and rotation axis 1 and rotation axis 28 is made to carry out rotation synchronous in the same direction, drive gear 7 with
The rotation of rotation axis 28 and rotate in same direction, then ground under being driven by the side of lower millstone 50 with the gear teeth that driving gear 7 engage
Disk 50 carries out the rotation contrary with rotation axis 1, interior crushes the mutually opposing of column 20 and outer pulverization cylinder 30 to realize
Rotation, the mutually opposing rotation of lower millstone 50 and upper millstone 40；Suitable electric current is passed through to electromagnet 64, so that electromagnet 64 is right
Permanent magnet 65 generates suitable magnetic repulsion, and the spacing between 50 middle part of 40 middle part of upper millstone and lower millstone is made to be equal to the target of raw material
Partial size；
Tourmaline, alunite, sepiolite, attapulgite or coconut activated carbon feedstock after purification is put into from hopper 2, it is former
Expect to fall into from feed pipe 1 in the outer pulverization cylinder 30 immediately below feed pipe 1；When interior crushing column 20 is between side and rotation axis 1
When the corresponding endpoint side of the shortest distance turns to the underface of feed pipe 1, between the interior crushing column 20 and outer pulverization cylinder 30 of the side
Gap it is larger, allow more biggish raw material enter it is interior crushing column 20 and outer pulverization cylinder 30 between gap in, for rule
Material of the lattice between interior crushing column 20 and outer pulverization cylinder 30 between the minimum spacing of spacing and maximum spacing, can play interval
The effect of formula charging, and then the work load that can avoid interior crushing column 20 and outer pulverization cylinder 30 is exceeded；Interior crushing column 20 and outer powder
The mutually opposing rotation of broken cylinder 30, crushing tooth 1 and crushing tooth 2 31 can carry out raw material to be preferably crushed, and interior crushing
Gap between column 20 and outer pulverization cylinder 30 is tapered from top to bottom, can reach in the dropping process of raw material and is gradually crushed raw material
Effect, fragmentation are preferable；It is equal to or less than fixed restriction 60 side of disk and outer pulverization cylinder 30 when the partial size of raw material is crushed to
When the spacing of inner wall, broken raw material can just be dropped down on lower millstone 50, and below standard raw material can be trapped in interior 20 He of crushing column
Continue to be broken in gap between outer pulverization cylinder 30；
Because the top surface of lower millstone 50 from its side to center at it is progressively lower so that the material for entering grinding channel 70 can be downward
The middle part of mill 50 is mobile, in the process, because the width in grinding channel 70 is gradually small along the moving direction of material, in upper millstone
40 and lower millstone 50 rotate backward under effect, preferable crush and grind can be carried out to material；If there is material to be stuck in grinding channel
In 70, because being respectively equipped with oppositely oriented arc convex ribs 1 and arc convex ribs on the forward surface of lower millstone 50 and upper millstone 40
2 41, upper millstone 40 and lower millstone 50 rotate backward effect under, the arc convex ribs 1 and arc of the material two sides being stuck
Shape convex ribs 2 41 can carry out pinching cutting to the material, be stuck in grinding channel 70 to can effectively avoid material, and then can promote
Into the complete grinding of material；The powder obtained after grinding is fallen from the discharge port 51 at 50 middle part of lower millstone, after falling on baffle 18
It falls along baffle 18, is then fallen in aggregate bin 3 from the outside of plain bearing 2 14, then along the inside of aggregate bin 3 towards out
Expects pipe 4 is mobile, and powder is passed through from the gap between support quarter butt 15 subsequently into discharge nozzle 4, after turning on the switch valve 5
Collect the powder that grinding obtains.
It is crushing, in process of lapping, since feed pipe 1 is bend pipe, can play prevents material from producing during smashing and grinding
The effect of raw dust evolution, because the top of outer pulverization cylinder 30 is inserted in the annular turn trough 11 of the inner top of outer case 10,
And 3 top surface side of aggregate bin is fixed with the support sealing plate 6 in the support turn trough 53 of insertion 50 bottom of lower millstone, and rotation axis one
The position that 21 top passes through outer case 10 is equipped with sealing bearing 12, so that dust only retains in outer pulverization cylinder 30, support sealing
Other aforementioned sides in plate 6 and aggregate bin 3, will not be moved to other spaces in outer case 10, convenient for being uniformly processed for dust,
Be conducive to safeguard other spaces in outer case 10.
It follows that this crushing grinding device can realize preferable smashing and grinding effect, complete discharging can guarantee, and discharge
Uniformity and it is up to standard degree it is higher, be also convenient for processing generate dust.
Embodiment 2
It is a kind of to receive net stone, including the first component and the second component with the CLO purification factor for actively adsorbing micropore, described
The raw material components of one component include solid preparation of chlorine dioxide, and second component includes the raw material components of following parts by weight:
20 parts of tourmaline, 10 parts of alunite, 8 parts of sepiolite, 45 parts of attapulgite, 6 parts of cocoanut active charcoal；First component and second
The mass ratio of component is 5:1.
It is above-mentioned there is the CLO purification factor for actively adsorbing micropore to receive net stone the preparation method is the same as that of Example 1, difference
It is:
The plant with harmful substance function in adsorbed gas is the mixture of bracketplant and sansevieria trifasciata, the quality of the two
Than for 2:1.
The crushing grinding device used in above-mentioned preparation method is the same as embodiment 1.
Embodiment 3
It is a kind of to receive net stone, including the first component and the second component with the CLO purification factor for actively adsorbing micropore, described
The raw material components of one component include solid preparation of chlorine dioxide, and second component includes the raw material components of following parts by weight:
25 parts of tourmaline, 8 parts of alunite, 12 parts of sepiolite, 35 parts of attapulgite, 9 parts of cocoanut active charcoal；First component and second
The mass ratio of component is 6:1.
It is above-mentioned there is the CLO purification factor for actively adsorbing micropore to receive net stone the preparation method is the same as that of Example 1, difference
It is:
The plant with harmful substance function in adsorbed gas is the mixture of aloe, sansevieria trifasciata and rhizoma arisaematis, three
The mass ratio of person is 2:3:3.
The crushing grinding device used in above-mentioned preparation method is the same as embodiment 1.
Those of ordinary skill in the art it should be appreciated that more than embodiment be intended merely to illustrate the present invention,
And be not used as limitation of the invention, as long as the change in spirit of the invention, to embodiment described above
Change, modification will all be fallen in scope of the presently claimed invention.
Claims (10)
1. a kind of receive net stone with the CLO purification factor for actively adsorbing micropore, including the first component and the second component, feature exist
In the raw material components of first component include solid preparation of chlorine dioxide, and second component includes following parts by weight
Raw material components: 20-25 parts of tourmaline, 8-10 parts of alunite, 8-12 parts of sepiolite, 35-45 parts of attapulgite, cocoanut active charcoal 6
~9 parts；The mass ratio of first component and the second component is 3~6:1；
Above-mentioned there is the CLO purification factor for actively adsorbing micropore to receive the preparation method of net stone include the following steps:
S1: selection sepiolite, attapulgite and the cocoanut active charcoal with adsorption capacity and the tourmaline with pyroelectric effect and
Alunite；
S2: distinguish again by sepiolite described in step S1, attapulgite and cocoanut active charcoal and respectively after progress purification processes
Then it is spare to cross 325 meshes for polishing；By tourmaline described in step S1 and alunite mineral material difference purification processes after again
It polishes respectively, it is spare then to cross 400 meshes；
S3: processing is modified respectively to step S2 treated sepiolite, attapulgite and cocoanut active charcoal, reactivation expands
Hole；
S4: by treated the sea the mass fraction weigh in step S2 that treated respectively tourmaline, alunite and step S3
Afrodite, attapulgite and cocoanut active charcoal, then mix, and after mixing, are placed in high-intensitive pelletizer and are made
Grain, obtains hybrid particles；
S5: hybrid particles obtained in step S4 are dried, and carry out calcination for activation then to get second component is arrived；
S6: the second component obtained in the first component and step S5 is weighed according to the ratio and is wrapped after mixing using wrappage
Wrapping up in get described there is the CLO purification factor for actively adsorbing micropore to receive net stone；
A kind of crushing grinding device, structure have been used when polishing in above-mentioned steps S2 are as follows:
The grinding device that crushes includes outer case (10) and the interior crushing column (20) being set in outer case (10), outer pulverization cylinder
(30), upper millstone (40) and the lower millstone (50) being located at immediately below upper millstone (40), the interior crushing column (20) is in from top to bottom
Gradually big truncated cone-shaped, vertical centering type fixation is equipped with rotation axis one (21), the outer pulverization cylinder in the interior crushing column (20)
(30) top end face and bottom face is open, and the outer pulverization cylinder (30) is sheathed on the outside of interior crushing column (20), and the rotation
Axis one (21) is located on the axis of outer pulverization cylinder (30), the interior table of the interior outer surface for crushing column (20) and outer pulverization cylinder (30)
It is respectively corresponded on face throughout having compatible crushing tooth one (22) and crushing tooth two (31)；Interior crushing column (20) bottom is fixed
There is the maximum distance being equal between interior crushing column (20) bottom surface edge and rotation axis one (21) in flat cylindrical body and radius
Fixed to limit disk (60), the upper millstone (40) is installed on the fixed bottom for limiting disk (60), and the lower millstone (50) is solid
Due to the bottom of outer pulverization cylinder (30), the lower end of the rotation axis one (21) sequentially passes through fixed restriction disk (60), upper millstone
(40) and at the center of lower millstone (50), bore is offered at the center of the lower millstone (50) greater than rotation axis one (21) diameter
Discharge port (51)；
The top surface of the lower millstone (50) from its side to center at it is progressively lower, the bottom surface of the upper millstone (40) is from its side in
Portion is progressively lower, and the bus slope of upper millstone (40) bottom surface is greater than the bus slope of lower millstone (50) top surface, the upper millstone (40)
The tapered material of ecto-entad is formed between lower millstone (50) and grinds channel (70), on the top surface of the lower millstone (50) uniformly
Connection discharge port (51) is fixed with along the arc convex ribs one of side to lower millstone (50) and outer pulverization cylinder (30) medial surface junction
(52), the rotation direction of each arc convex ribs one (52) is identical, its middle part of connection is uniformly fixed on the bottom surface of the upper millstone (40) and is arrived
Upper millstone (40) week lateral edge side arc convex ribs two (41), the rotation direction of each arc convex ribs two (41) it is identical and with arc convex ribs one
(52) oppositely oriented；
The inner top of the outer case (10) offers the annular turn trough (11) for being inserted at the top of outer pulverization cylinder (30), the outer container
The feed pipe (1) for being located in annular turn trough (11) ring and crushing column (20) side in face, institute are connected on body (10) top surface
Stating feed pipe (1) is bend pipe, and feed pipe (1) upper end is fixedly connected with hopper (2)；Outer case (10) bottom is fixed with position
The aggregate bin (3) in cone immediately below lower millstone (50), the bore of the aggregate bin (3) is gradually small from top to bottom, and gathers materials
The bottom of bucket (3) is connected with discharge nozzle (4), and the discharge nozzle (4) is equipped with switch valve (5)；The lower part of the lower millstone (50)
The support turn trough (53) of annular is offered, is equipped with the support for being fixed on aggregate bin (4) top surface side in support turn trough (53)
Sealing plate (6)；The side of the lower millstone (50) is equipped with driving gear (7), and the side of the lower millstone (50) is equipped with and driving
The gear teeth of gear (7) engagement, coaxial-type is fixed with rotation axis two (8), the rotation axis one at driving gear (7) center
(21) and rotation axis two (8) all connects driving motor (9), the rotation direction phase of the rotation axis one (21) and rotation axis two (8)
Together；Rotation axis one (21) upper end is on the upper surface of outer case (10), the outer case (10) for rotation axis one (21)
The position passed through is equipped with sealing bearing (12).
2. according to claim 1 a kind of net stone is received with the CLO purification factor for actively adsorbing micropore, which is characterized in that
Second component includes the raw material components of following parts by weight: 23 parts of tourmaline, 9 parts of alunite, 10 parts of sepiolite, concave convex rod
40 parts, 7 parts of cocoanut active charcoal of soil；The mass ratio of first component and the second component is 5:1.
3. according to claim 1 a kind of net stone is received with the CLO purification factor for actively adsorbing micropore, which is characterized in that
In the step S4 of preparation method when being granulated the mother liquor that uses to be mentioned with the plant of harmful substance function in adsorbed gas
Take liquid.
4. according to claim 3 a kind of net stone is received with the CLO purification factor for actively adsorbing micropore, which is characterized in that
The plant with harmful substance function in adsorbed gas used when being granulated in preparation method is bracketplant, aloe, sansevieria trifasciata, rice
At least one of blue, ivy and rhizoma arisaematis.
5. according to claim 1 a kind of net stone is received with the CLO purification factor for actively adsorbing micropore, which is characterized in that
Wrappage described in the step S6 of preparation method is non-woven fabrics.
6. according to claim 1 a kind of net stone is received with the CLO purification factor for actively adsorbing micropore, which is characterized in that
Column (20) bottom surface edge is crushed in fixed restriction disk (60) of the crushing grinding device used in preparation method is corresponding
The corresponding endpoint place of minimum range between rotation axis one (21) extends on the outside of interior crushing column (20) in side, should be located at interior
The top surface for crushing the part on the outside of column (20) is to have inside to the progressively lower inclined-plane in outer side (61).
7. according to claim 1 a kind of net stone is received with the CLO purification factor for actively adsorbing micropore, which is characterized in that
The fixed bottom for limiting disk (60) of the crushing grinding device used in preparation method is offered for installing on described
The mounting groove (62) of mill (40), the upper millstone (40) are slidably connected in the mounting groove (62), the upper millstone (40)
Upper surface pass through the spring (63) that is uniformly arranged be connected to it is described it is fixed limit on disk (60) bottom surface, it is described fixed to limit disk
(60) it is built-in with electromagnet (64), is magnetic and electromagnet (64) built in the position of the upper millstone (40) corresponding electromagnet (64)
The permanent magnet (65) to repel each other, when working condition, the repulsion between the electromagnet (64) and permanent magnet (65) is consistently greater than spring
(63) resistance the sum of of the elastic force and grinding material to upper millstone (40).
8. according to claim 7 a kind of net stone is received with the CLO purification factor for actively adsorbing micropore, which is characterized in that
The side of the upper millstone (40) of the crushing grinding device used in preparation method is formed with sliding panel (42) in a ring,
The sliding slot one (66) of indent slided up and down for sliding panel (42) is offered on the border side of the mounting groove (62)；On described
It is surrounded on the ring side on the outside of rotation axis one (21) on mill (40) and is equidistantly fixed with sliding shoe (43), the rotation axis one
(21) the compatible sliding slot two (67) with sliding shoe (43) of indent is offered on.
9. according to claim 1 a kind of net stone is received with the CLO purification factor for actively adsorbing micropore, which is characterized in that
The lower end of the rotation axis two (8) of the crushing grinding device used in preparation method is connected to by plain bearing one (13)
The interior bottom of outer case (10), the upper end of the rotation axis two (8) pass through the top panel of outer case (10) and connect driving motor
(9), plain bearing one (13), the rotation axis one are equipped with for the position that rotation axis two (8) passes through on the outer case (10)
(21) lower end extends in aggregate bin (3) and is connect by plain bearing two (14) with aggregate bin (3), the plain bearing two
(14) lower part side is equidistantly fixed at least three support quarter butts (15) being connected on the outside of discharge nozzle (4) upper port；Institute
It states rotation axis two (8) upper end and the equal fixing sleeve in rotation axis one (21) upper end is equipped with the belt wheel for being located at outer case (10) over top
(16), a transmission belt (17) is surrounded on the two described belt wheels (16) jointly.
10. according to claim 9 a kind of net stone is received with the CLO purification factor for actively adsorbing micropore, which is characterized in that
The rotation axis one (21) lower part fixing sleeve of the crushing grinding device used in preparation method is equipped with the gear in toroidal
Plate (18), the diameter of the baffle (18) is gradually big from top to bottom, and the base diameter of the baffle (18) is greater than plain bearing two
(14) bottom of outer diameter, the baffle (18) is surrounded on the outside of plain bearing two (14).
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111097580A (en) * | 2019-12-26 | 2020-05-05 | 龙玉容 | Raw material processing device for composite board |
| CN111330682A (en) * | 2020-03-11 | 2020-06-26 | 北京同仁堂参茸中药制品有限公司 | Processing technology of antelope horn powder and multi-stage pulverizer for processing technology |
| CN115254267A (en) * | 2022-08-05 | 2022-11-01 | 天津欣辰湖建材有限公司 | Colloid grinder is used in pitch waterproof material preparation |
| CN116213011A (en) * | 2023-04-06 | 2023-06-06 | 江苏万锂达智能科技有限公司 | Grinding equipment and process for lithium battery cathode material |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201316640Y (en) * | 2008-12-12 | 2009-09-30 | 彭娟 | Disc mill |
| CN201644145U (en) * | 2010-03-30 | 2010-11-24 | 威海恒邦化工有限公司 | Ammonium phosphate tailing mill |
| CN107376831A (en) * | 2017-09-05 | 2017-11-24 | 大连沐美科技有限公司 | The compound air purification material of the purification factor containing CLO receives net stone and preparation method thereof |
| JP2018001056A (en) * | 2016-06-28 | 2018-01-11 | 宇部興産機械株式会社 | Vertical crusher |
| CN108970752A (en) * | 2018-08-27 | 2018-12-11 | 徐志华 | A kind of mining broken equipment of multistage mineral powder |
| CN208501379U (en) * | 2018-06-25 | 2019-02-15 | 浙江金龙纸业有限公司 | A kind of disc mill |
-
2019
- 2019-04-28 CN CN201910348165.0A patent/CN110075796A/en active Pending
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN201316640Y (en) * | 2008-12-12 | 2009-09-30 | 彭娟 | Disc mill |
| CN201644145U (en) * | 2010-03-30 | 2010-11-24 | 威海恒邦化工有限公司 | Ammonium phosphate tailing mill |
| JP2018001056A (en) * | 2016-06-28 | 2018-01-11 | 宇部興産機械株式会社 | Vertical crusher |
| CN107376831A (en) * | 2017-09-05 | 2017-11-24 | 大连沐美科技有限公司 | The compound air purification material of the purification factor containing CLO receives net stone and preparation method thereof |
| CN208501379U (en) * | 2018-06-25 | 2019-02-15 | 浙江金龙纸业有限公司 | A kind of disc mill |
| CN108970752A (en) * | 2018-08-27 | 2018-12-11 | 徐志华 | A kind of mining broken equipment of multistage mineral powder |
Non-Patent Citations (2)
| Title |
|---|
| 杨武等: "《改变世界的信息材料》", 30 April 2012, 甘肃科学技术出版社 * |
| 高宇声等: "《环境保护》", 31 August 1985, 中国环境科学出版社 * |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111097580A (en) * | 2019-12-26 | 2020-05-05 | 龙玉容 | Raw material processing device for composite board |
| CN111330682A (en) * | 2020-03-11 | 2020-06-26 | 北京同仁堂参茸中药制品有限公司 | Processing technology of antelope horn powder and multi-stage pulverizer for processing technology |
| CN115254267A (en) * | 2022-08-05 | 2022-11-01 | 天津欣辰湖建材有限公司 | Colloid grinder is used in pitch waterproof material preparation |
| CN115254267B (en) * | 2022-08-05 | 2023-12-05 | 天津欣辰湖建材有限公司 | Colloid grinder is used in preparation of pitch waterproof material |
| CN116213011A (en) * | 2023-04-06 | 2023-06-06 | 江苏万锂达智能科技有限公司 | Grinding equipment and process for lithium battery cathode material |
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