CN209680777U - A kind of architecture sediment washing production line - Google Patents
A kind of architecture sediment washing production line Download PDFInfo
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- CN209680777U CN209680777U CN201920064883.0U CN201920064883U CN209680777U CN 209680777 U CN209680777 U CN 209680777U CN 201920064883 U CN201920064883 U CN 201920064883U CN 209680777 U CN209680777 U CN 209680777U
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- coarse sand
- feed inlet
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- production line
- architecture sediment
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- 239000013049 sediment Substances 0.000 title claims abstract description 35
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 20
- 238000005406 washing Methods 0.000 title abstract description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 71
- 239000004576 sand Substances 0.000 claims abstract description 52
- 239000002002 slurry Substances 0.000 claims abstract description 39
- 230000018044 dehydration Effects 0.000 claims abstract description 33
- 238000006297 dehydration reaction Methods 0.000 claims abstract description 33
- 238000004537 pulping Methods 0.000 claims abstract description 22
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 19
- 239000005995 Aluminium silicate Substances 0.000 claims abstract description 18
- 235000012211 aluminium silicate Nutrition 0.000 claims abstract description 18
- NLYAJNPCOHFWQQ-UHFFFAOYSA-N kaolin Chemical compound O.O.O=[Al]O[Si](=O)O[Si](=O)O[Al]=O NLYAJNPCOHFWQQ-UHFFFAOYSA-N 0.000 claims abstract description 18
- 230000007246 mechanism Effects 0.000 claims abstract description 14
- 239000000463 material Substances 0.000 claims abstract description 12
- 239000000377 silicon dioxide Substances 0.000 claims abstract description 9
- 239000011440 grout Substances 0.000 claims abstract description 8
- 238000007670 refining Methods 0.000 claims abstract description 5
- 238000009991 scouring Methods 0.000 claims abstract description 4
- JTJMJGYZQZDUJJ-UHFFFAOYSA-N phencyclidine Chemical class C1CCCCN1C1(C=2C=CC=CC=2)CCCCC1 JTJMJGYZQZDUJJ-UHFFFAOYSA-N 0.000 claims description 25
- 239000007788 liquid Substances 0.000 claims description 20
- 238000000498 ball milling Methods 0.000 claims description 5
- 239000002699 waste material Substances 0.000 abstract description 5
- 239000002351 wastewater Substances 0.000 description 4
- 238000000034 method Methods 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 239000002893 slag Substances 0.000 description 3
- 239000002689 soil Substances 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 238000010276 construction Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000005516 engineering process Methods 0.000 description 2
- 239000010433 feldspar Substances 0.000 description 2
- 239000010438 granite Substances 0.000 description 2
- 229910052500 inorganic mineral Inorganic materials 0.000 description 2
- 239000011707 mineral Substances 0.000 description 2
- 239000002245 particle Substances 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 239000002210 silicon-based material Substances 0.000 description 2
- 239000007787 solid Substances 0.000 description 2
- XUIMIQQOPSSXEZ-UHFFFAOYSA-N Silicon Chemical compound [Si] XUIMIQQOPSSXEZ-UHFFFAOYSA-N 0.000 description 1
- 230000009471 action Effects 0.000 description 1
- 238000004458 analytical method Methods 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 239000000919 ceramic Substances 0.000 description 1
- 238000006073 displacement reaction Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007717 exclusion Effects 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 230000005484 gravity Effects 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 229910052755 nonmetal Inorganic materials 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 230000008569 process Effects 0.000 description 1
- 230000001681 protective effect Effects 0.000 description 1
- 238000000746 purification Methods 0.000 description 1
- 239000010453 quartz Substances 0.000 description 1
- 238000004062 sedimentation Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 238000010334 sieve classification Methods 0.000 description 1
- 229910052710 silicon Inorganic materials 0.000 description 1
- 239000010703 silicon Substances 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
- Y02W30/00—Technologies for solid waste management
- Y02W30/50—Reuse, recycling or recovery technologies
- Y02W30/58—Construction or demolition [C&D] waste
Abstract
The utility model discloses a kind of architecture sediments to wash production line, including pulping device, classification mechanism, dehydration device and swab；Pulping device is used to mix architecture sediment and water and ramming is at slurries；Classification mechanism includes several coarse sand separators set gradually, to refine slurries step by step, wherein is set to first feed inlet of coarse sand separator and connects with the grout outlet of pulping device；The feed inlet of the latter coarse sand separator in two adjacent coarse sand separators connects with the fines discharge port of previous coarse sand separator；The feed inlet of dehydration device connects with the fines discharge port of the last one coarse sand separator, and slurries are dehydrated so that refining kaolin is made；Swab with the coarse fodder discharge port of each coarse sand separator for connecting, to carry out strength scouring to coarse fodder and isolate silica sand material.Architecture sediment washing production line may separate out the lesser kaolin of fineness, improves the utilization rate of architecture sediment, avoids the waste of resource.
Description
Technical field
The utility model relates to architecture sediment process and utilization technology fields, and in particular to a kind of architecture sediment washing production
Line.
Background technique
It is well known that the earth's surface of south Fujian mainly adds surface argillic horizon to form by Weathered Granite or half weathered layer.With
Quickly propelling for urbanization, there is a large amount of architecture sediment to generate, main source have high-rise and super high-rise building basement,
The construction such as iron and tunnel.These architecture sediments, (such as sandstone are used for water in addition to small part is voluntarily digested by construction unit for a long time
Mud or backfill etc.), largely it is transported to eliminate-incorporate-land landfill；And it is also possible to a kind of treasured for architecture sediment changes an angle
Expensive nonmetal mineral resource, for the mineral resources of mature exploitation, its grade of these architecture sediments is relatively low,
Impurity is more, and iron-content is high, whiteness is low, is mainly made of weathering residual I type granite and quartz and other clays；How from building
High efficiency extraction and environmentally protective comprehensive utilization effective nonmetallic ore ingredient therein, are weights urgently to be resolved at present in foundation pit dregs
Hang-up.
Utility model content
The purpose of the utility model is to overcome drawbacks described above present in background technique or problems, provide a kind of building slag
Soil washing production line, architecture sediment washing production line may separate out the lesser kaolin of fineness, and separated kaolin out can
It is used to prepare the ceramic-likes product such as architectural pottery or domestic ceramics, improves the utilization rate of architecture sediment, avoids the wave of resource
Take.
To reach above-mentioned purpose, the utility model adopts the following technical solution:
A kind of architecture sediment washing production line, including pulping device, classification mechanism, dehydration device and swab；It is described
Pulping device is used to mix architecture sediment and water and ramming is at slurries；The classification mechanism includes several thicknesses set gradually
Separator, to refine slurries step by step, wherein be set to the feed inlet of first coarse sand separator and going out for pulping device
Slurry mouth connects；The feed inlet of the latter coarse sand separator in two adjacent coarse sand separators is separated with previous coarse sand
The fines discharge port of device connects；The fines discharge port phase of the feed inlet of the dehydration device and the last one coarse sand separator
It connects, and slurries is dehydrated so that refining kaolin is made；The swab is used to go out with the coarse fodder of each coarse sand separator
Material mouth connects, to carry out strength scouring to coarse fodder and isolate silica sand material.
Further, the classification mechanism includes the spiral classifier set gradually, one section of classifying cyclone, vibration straight line
Sieve and two sections of classifying cyclones；The overflow box outlet of the spiral classifier connects with the feed inlet of one section of classifying cyclone；Institute
The overflow box outlet for stating one section of classifying cyclone connects with vibration straight line shaker；It is described vibration straight line shaker sieve bottom discharge end with two sections
The feed inlet of classifying cyclone connects；One section of classifying cyclone is 250 cyclone of φ；Two sections of classifying cyclones are φ
150 cyclones；80 mesh of the sieve mesh number of the vibration straight line shaker.
Further, the overflowing liquid of the spiral classifier pumps the feed inlet into one section of classifying cyclone by Pulp pump；
The overflow box outlet height of one section of classifying cyclone is higher than the feed end of vibration straight line shaker；Under the sieve of the vibration straight line shaker
Discharge end height is higher than the feed inlet of two sections of classifying cyclones；The overflowing liquid of two sections of classifying cyclones by plunger pump into
The feed inlet of dehydration device.
Further, the pulping device is to smash pulp grinder.
Further, the swab is continuous ball milling swaging machine, revolving speed 25r/min.
Further, the dehydration device is filter press.
Further, the grout outlet of the swab and the water outlet of dehydration device connect with the water inlet of pulping device
It is logical.
From the above description of the utility model, it can be seen, compared with the existing technology, what the utility model had is following beneficial
Effect:
1, in the technical program, by each coarse sand separator for being set gradually in classification mechanism, it can be achieved that slag will be built
Fineness in soil paste liquid is the function that the kaolin slurry of -325 mesh is isolated；Separated kaolin slurry out passes through dehydration dress
After setting dehydration, the kaolin of purification can be prepared by, quality can achieve the requirement of GB/T14563-2008, improve building slag
The recyclable resource circulation utilization rate of soil；By using swab to kaolin, the feldspar in the incomplete chiltern gap of weathering
Classification is cleaned Deng by strength, the purity and intensity of silicon materials or silica sand material is improved, further improves resource comprehensive utilization
It utilizes.
2, the coarse sand separator respectively set gradually is respectively spiral classifier, one section of classifying cyclone, vibration straight line shaker
Refined and isolated 325 mesh slurry step by step with the slurries to architecture sediment with two sections of classifying cyclones, structure is simple, function
Reliably, separative efficiency is high.
3, by by the overflowing liquid of spiral classifier by Pulp pump pump the feed inlet setting into one section of classifying cyclone with
And by the overflowing liquid of two sections of classifying cyclones by plunger pump into dehydration device feed inlet, it is ensured that by spiral classifier
The slurries that overflow box outlet overflow goes out can successfully be guided in one section of classifying cyclone and by two sections of classifying cyclones
The slurries that overflow box outlet overflow goes out can be successfully guided in dehydration device；By by the overflowing liquid of one section of classifying cyclone
Outlet height is set above the feed end of vibration straight line shaker and sets high for the sieve bottom discharge end for vibrating straight line shaker height
In the design of the feed inlet of two sections of classifying cyclones, then can guarantee by after one section of classifying cyclone and vibration straight line sieve classification
The lesser slurries of content fineness can successfully flow into next hierarchical structure, not only saved the energy, but also greatly drop
Low production cost.
4, pulping device, swab and dehydration device are all made of simple structure, and function is reliable, work efficiency is high.
5, by the way that the water outlet of the grout outlet of swab and dehydration device to be connected to the water inlet of pulping device, with
It realizes the recycling of waste water, economize on resources, simultaneously, it is also ensured that waste water is repeatedly classified, is built with further increasing
Build the rate of recovery of kaolin or silica sand material in dregs.
Detailed description of the invention
In order to illustrate more clearly of the technical solution of the utility model embodiment, make below to required in embodiment description
Attached drawing is briefly described, it should be apparent that, the accompanying drawings in the following description is some embodiments of the utility model, for
For those skilled in the art, without creative efforts, it can also be obtained according to these attached drawings
His attached drawing.
Fig. 1 is the structural schematic diagram that the utility model embodiment architecture sediment washes production line.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe.Obviously, described embodiment is the preferred embodiment of the utility model, and is not to be seen as to it
The exclusion of his embodiment.Based on the utility model embodiment, those skilled in the art are not before making creative work
Every other embodiment obtained is put, is fallen within the protection scope of the utility model.
In claims of the utility model, specification and above-mentioned attached drawing, unless otherwise specifically limited, term is such as used
" first ", " second " or " third " etc. is provided to distinguish different objects, be not use to describe a particular order.
In claims of the utility model, specification and above-mentioned attached drawing, unless otherwise specifically limited, for orientation
Word, such as using term " center ", " transverse direction ", " longitudinal direction ", "horizontal", " vertical ", "top", "bottom", "inner", "outside", "upper",
The indicating positions such as "lower", "front", "rear", "left", "right", " clockwise ", " counterclockwise " or positional relationship are based on shown in attached drawing
Orientation and positional relationship, and be merely for convenience of narration the utility model and simplify description, rather than indication or suggestion is signified
Mechanism or element must have a particular orientation or be constructed and operated in a specific orientation, so can not be interpreted as limitation this
The specific protection scope of utility model.
In claims of the utility model, specification and above-mentioned attached drawing, unless otherwise specifically limited, term is such as used
" affixed " or " being fixedly connected ", should broadly understood, i.e., between the two without any company of displacement relation and relative rotation relationship
Connect mode, that is to say, that including being unremovably fixedly connected with, being removably secured connection, be linked together and by other machines
Structure or element are fixedly connected.
In claims of the utility model, specification and above-mentioned attached drawing, such as using term " includes ", " having " and
Their deformation, it is intended that " including but not limited to ".
The structural schematic diagram of the utility model embodiment architecture sediment washing production line is shown referring to Fig. 1, Fig. 1.Such as Fig. 1
Shown, in the utility model embodiment, it includes pulping device 1, classification mechanism 2, dehydration device 3 that architecture sediment, which washes production line,
With swab 4.
Wherein, pulping device 1 is used to mix architecture sediment and water and ramming is at slurries；Specifically, in the present embodiment,
Pulping device 1 is to smash pulp grinder, and architecture sediment and water are added to smashing in pulp grinder ramming into certain density slurries.
Classification mechanism 2 includes several coarse sand separators set gradually, with the granularity of the content to slurries carry out by
Grade refinement；Wherein, the feed inlet of the first coarse sand separator set gradually connects with the grout outlet of pulping device 1；It is adjacent
Two coarse sand separators in the fines of feed inlet and previous coarse sand separator of the latter coarse sand separator go out
Material mouth connects.
Preferably, in the present embodiment, classification mechanism 2 includes 21, the one sections of classification eddy flows of spiral classifier set gradually
Device 22, vibration straight line shaker 23 and two sections of classifying cyclones 24；That is, the coarse sand separator respectively set gradually is respectively spiral point
21, one sections of classifying cyclones 22 of grade machine, vibration straight line shaker 23 and two sections of classifying cyclones 24；Wherein, spiral classifier 21 into
Slurry mouth connects with the grout outlet for smashing pulp grinder；The feed inlet phase of the overflow box outlet of spiral classifier 21 and one section of classifying cyclone 22
It connects；The overflow box outlet of one section of classifying cyclone 22 connects with the feed end of vibration straight line shaker 23；Under the sieve for vibrating straight line shaker 23
Discharge end connects with the feed inlet of two sections of classifying cyclones 24；The overflow box outlet and dehydration device 3 of two sections of classifying cyclones 24
Feed inlet connect.
Specifically, spiral classifier 21 is of different sizes by means of solid grain, and specific gravity is different, thus sedimentation in a liquid
The different principle of speed, during classification, thin ore particle swims to go out at overflowing liquid from overflow box outlet overflow in water, rough
Grain is then sunken to slot bottom, and is discharged from the sand return mouth of slot bottom.
One section of classifying cyclone 22 is 250 cyclone of φ；Two sections of classifying cyclones 24 are 150 cyclone of φ；Cyclone
Basic principle is two-phase or multiphase mixture such as the liquid-liquid that will have the function of certain density contrast, liquid-solid, liquid-gas in centrifugal force
Under separated；Slurries are tangentially entered into cyclone with certain pressure, high speed rotation flow field are generated in cylindrical cavity, in slurries
The big component of density axially simultaneously moves downward under the action of eddy flow field, moves radially outwards, and reaches cone segments edge
Wall moves downward, and is discharged by underflow opening, and material is thus formed outer swirling flow fields；The small component of density is to central axial direction
Movement, and an inside vortex moved upwards is formed in axis centre, it is then discharged, has thus been reached slurries by overflow box outlet
In the purpose that is separated of coarse sand and fine sand.The sieve mesh number for vibrating straight line shaker 23 is 80 mesh.
Preferably, in the present embodiment, the overflowing liquid of spiral classifier 21 is pumped by Pulp pump 201 into one section of classification eddy flow
The feed inlet of device 22 is arranged；The feed end that the overflow box outlet height of one section of classifying cyclone 22 is higher than vibration straight line shaker 23 is set
It sets；The sieve bottom discharge end height for vibrating straight line shaker 23 is higher than the feed inlet setting of two sections of classifying cyclones 24；Two sections of classification eddy flows
The overflowing liquid of device 24 pumps the feed inlet setting into dehydration device 3 by plunger pump 202.
The feed inlet of dehydration device 3 connects with the fines discharge port of the last one coarse sand separator, and slurries are carried out
Dehydration is to be made refining kaolin, that is, the dehydration device 3 in the present embodiment connects with the fines discharge port of 150 cyclone of φ.
In the present embodiment, dehydration device 3 is filter press.
Swab 4 is cleaned simultaneously for connecting with the coarse fodder discharge port of each coarse sand separator with carrying out strength to coarse fodder
Isolate silica sand material.
Specifically, swab 4 uses continuous ball milling swaging machine, revolving speed 2000r/min；The charging of swab 4
Mouthful with the sand return mouth of spiral classifier 21, the sand return mouth of 250 cyclone of φ, vibration straight line shaker 23 sieve top discharge mouth and φ 150
The sand return mouth of cyclone is connected.
Preferably, the grout outlet of swab 4 and the water outlet of dehydration device 3 are connected to the water inlet of pulping device 1,
With the waste liquid for recycling swab 4 and dehydration device 3 is flowed out.
The utility model embodiment in actual use, architecture sediment and water is directed into smash is mixed to prepare slurry in pulp grinder
Liquid, the slurries containing fines continue to flow to vibration directly after the slurries by smashing pulp grinder outflow isolate coarse sand through 250 cyclone of φ
Line sieve 23, vibration straight line shaker 23 further sifts out the biggish coarse sand of particle, and the slurries containing fines under sieve are continued to be directed into
150 cyclone of φ carries out coarse sand separation, to obtain the lesser slurries containing fines of granularity, then by the slurries through filter press filters pressing
Refining kaolin is obtained after dehydration；Wherein, it is revolved by spiral classifier 21,250 cyclone of φ, vibration straight line shaker 23 and φ 150
The coarse sand that stream device is isolated isolates silica sand material by being directed into continuous ball milling swaging machine strongly clean, such as LED silicon
Sand；The waste liquid flowed out by continuous ball milling swaging machine and the waste liquid flowed out by filter press pass through pipeline flow into smash in pulp grinder into
Row recycles.
It can be seen from above-described embodiment that each coarse sand point in the technical program by being set gradually in classification mechanism 2
From device, it can be achieved that the function that the kaolin slurry that the fineness in architecture sediment slurries is 325 mesh is isolated；It is separated go out
After kaolin slurry is dehydrated by dehydration device 3, fine kaolin can be prepared by, quality can achieve GB/T14563-
2008 requirement, improving architecture sediment can be recycled resource circulation utilization rate, reduce the waste of resource；By using swab
Kaolin, feldspar in the incomplete chiltern gap of 4 pairs of weathering etc. clean classification by strength, improve silicon materials or silica sand material
Purity and intensity, further improve resource comprehensive utilization utilization.
The coarse sand separator respectively set gradually is respectively 21, one sections of classifying cyclones 22 of spiral classifier, vibration straight line
Sieve 23 and two sections of classifying cyclones 24 are refined step by step with the slurries to architecture sediment and are isolated 325 mesh slurry, structure letter
Single, function is reliable, separative efficiency is high.
By the way that the overflowing liquid of spiral classifier 21 is set by the feed inlet that Pulp pump 201 is pumped into one section of classifying cyclone 22
It sets and the overflowing liquid of two sections of classifying cyclones 24 is pumped into the feed inlet into dehydration device 3 by plunger pump 202, it is ensured that by
The slurries that 21 overflow box outlet overflow of spiral classifier goes out can be successfully guided in one section of classifying cyclone 22 and by two
The slurries that the overflow box outlet overflow of section classifying cyclone 24 goes out can be successfully guided in dehydration device 3；By by one section
The overflow box outlet height of classifying cyclone 22 is set above the feed end of vibration straight line shaker 23 and will vibrate straight line shaker 23
Sieve bottom discharge end height be set above two sections of classifying cyclones 24 feed inlet design, then can guarantee by one section be classified
The lesser slurries of content fineness after cyclone 22 and vibration straight line shaker 23 are classified can successfully flow into next classification
In structure, the energy is not only saved, but also significantly reduce production cost.
Pulping device 1, swab 4 and dehydration device 3 are all made of simple structure, and function is reliable, work efficiency is high.
By the way that the grout outlet of swab 4 and the water outlet of dehydration device 3 to be connected to the water inlet of pulping device 1,
To realize the recycling of waste water, economize on resources, simultaneously, it is also ensured that waste water is repeatedly classified, to further increase
The rate of recovery of kaolin or silica sand material in architecture sediment.
In summary it analyzes, technical solution disclosed by the utility model solves whole technical problems listed by specification,
Realize corresponding technical effect.
The description of description above and embodiment for explaining scope of protection of the utility model, but is not constituted to this reality
With the restriction of novel protected range.By the enlightenment of the utility model or above-described embodiment, those of ordinary skill in the art are combined
Common knowledge, the ordinary technical knowledge of this field and/or the prior art pass through logical analysis, reasoning or limited examination
Test it is available to the modification of the utility model embodiment or in which a part of technical characteristic, equivalent replacement or other improvements,
It should be included within the scope of protection of this utility model.
Claims (7)
1. a kind of architecture sediment washes production line, it is characterized in that: including pulping device, classification mechanism, dehydration device and scouring dress
It sets；
The pulping device is used to mix architecture sediment and water and ramming is at slurries；
The classification mechanism includes several coarse sand separators set gradually, to refine slurries step by step, wherein be set to first
A feed inlet of coarse sand separator connects with the grout outlet of pulping device；It is latter in two adjacent coarse sand separators
The feed inlet of a coarse sand separator connects with the fines discharge port of previous coarse sand separator；
The feed inlet of the dehydration device connects with the fines discharge port of the last one coarse sand separator, and slurries are taken off
Water is to be made refining kaolin；
The swab with the coarse fodder discharge port of each coarse sand separator for connecting, to carry out strength scouring to coarse fodder and divide
Separate out silica sand material.
2. a kind of architecture sediment as described in claim 1 washes production line, it is characterized in that: the classification mechanism includes successively setting
Spiral classifier, one section of classifying cyclone, vibration straight line shaker and the two sections of classifying cyclones set；The overflow of the spiral classifier
Liquid outlet connects with the feed inlet of one section of classifying cyclone；The overflow box outlet and vibration straight line shaker of one section of classifying cyclone
Connect；The sieve bottom discharge end of the vibration straight line shaker connects with the feed inlet of two sections of classifying cyclones；One section of classification eddy flow
Device is 250 cyclone of φ；Two sections of classifying cyclones are 150 cyclone of φ；The 80 of the sieve mesh number of the vibration straight line shaker
Mesh.
3. a kind of architecture sediment as claimed in claim 2 washes production line, it is characterized in that: the overflowing liquid of the spiral classifier
The feed inlet into one section of classifying cyclone is pumped by Pulp pump；The overflow box outlet height of one section of classifying cyclone is higher than vibration
The feed end of dynamic straight line shaker；The sieve bottom discharge end height of the vibration straight line shaker is higher than the feed inlet of two sections of classifying cyclones；Institute
State feed inlet of the overflowing liquid of two sections of classifying cyclones by plunger pump into dehydration device.
4. a kind of architecture sediment as described in claim 1 washes production line, it is characterized in that: the pulping device is to smash pulp grinder.
5. a kind of architecture sediment as described in claim 1 washes production line, it is characterized in that: the swab is continuous ball milling
Swaging machine, revolving speed 25r/min.
6. a kind of architecture sediment as described in claim 1 washes production line, it is characterized in that: the dehydration device is filter press.
7. a kind of architecture sediment as described in claim 1 washes production line, it is characterized in that: the water outlet of the dehydration device is equal
It is connected to the water inlet of pulping device.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920064883.0U CN209680777U (en) | 2019-01-15 | 2019-01-15 | A kind of architecture sediment washing production line |
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201920064883.0U CN209680777U (en) | 2019-01-15 | 2019-01-15 | A kind of architecture sediment washing production line |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111203315A (en) * | 2019-12-27 | 2020-05-29 | 程泉 | Engineering dregs, soil, sand and stone separation system |
| CN112892852A (en) * | 2021-02-05 | 2021-06-04 | 中建材蚌埠玻璃工业设计研究院有限公司 | Method for preparing silica sand for photovoltaic glass from kaolin tailings |
| CN114405645A (en) * | 2022-01-22 | 2022-04-29 | 鹤山市鸿盛石场有限公司 | Novel process method for stripping granite weathered layer and producing sand |
-
2019
- 2019-01-15 CN CN201920064883.0U patent/CN209680777U/en active Active
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111203315A (en) * | 2019-12-27 | 2020-05-29 | 程泉 | Engineering dregs, soil, sand and stone separation system |
| CN111203315B (en) * | 2019-12-27 | 2024-04-16 | 程泉 | Engineering dregs and sand separating system |
| CN112892852A (en) * | 2021-02-05 | 2021-06-04 | 中建材蚌埠玻璃工业设计研究院有限公司 | Method for preparing silica sand for photovoltaic glass from kaolin tailings |
| CN112892852B (en) * | 2021-02-05 | 2024-04-19 | 中建材玻璃新材料研究院集团有限公司 | Method for preparing silica sand for photovoltaic glass from kaolin tailings |
| CN114405645A (en) * | 2022-01-22 | 2022-04-29 | 鹤山市鸿盛石场有限公司 | Novel process method for stripping granite weathered layer and producing sand |
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