CN203428929U - Purifying device for attapulgite clay minerals - Google Patents

Purifying device for attapulgite clay minerals Download PDF

Info

Publication number
CN203428929U
CN203428929U CN201320575483.9U CN201320575483U CN203428929U CN 203428929 U CN203428929 U CN 203428929U CN 201320575483 U CN201320575483 U CN 201320575483U CN 203428929 U CN203428929 U CN 203428929U
Authority
CN
China
Prior art keywords
communicated
attapulgite clay
pulverizer
agitation vat
opening
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Expired - Fee Related
Application number
CN201320575483.9U
Other languages
Chinese (zh)
Inventor
戴亮
任珺
陶玲
马贵
李华
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Lanzhou Jiaotong University
Original Assignee
Lanzhou Jiaotong University
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Lanzhou Jiaotong University filed Critical Lanzhou Jiaotong University
Priority to CN201320575483.9U priority Critical patent/CN203428929U/en
Application granted granted Critical
Publication of CN203428929U publication Critical patent/CN203428929U/en
Anticipated expiration legal-status Critical
Expired - Fee Related legal-status Critical Current

Links

Images

Landscapes

  • Disintegrating Or Milling (AREA)
  • Crushing And Grinding (AREA)

Abstract

The utility model discloses a purifying device for attapulgite clay minerals. The purifying device comprises a crusher, a pulverizer communicated with the discharge tube of the crusher, a grinding machine communicated with the discharge tube of the pulverizer, a filtering screen below the grinding machine, a material storing barrel below the filtering screen, a mixing barrel communicated with the discharge opening of the material storing barrel, a sodium hexametaphosphate quantitative feeding device communicated with the feeding opening of the mixing barrel, a quantitative water supplementing device communicated with the feeding opening of the mixing barrel, a muffle communicated with the discharge opening of the mixing barrel, and a finished product collecting barrel communicated with the discharge opening of the material storing barrel, wherein the discharge opening of the muffle is communicated with the feeding opening of the pulverizer. The attapulgite clay purified by the device has very high purity, reaching up to over 95%, thus meeting most application requirements.

Description

A kind of purifying plant of attapulgite clay mineral
Technical field
The utility model belongs to attapulgite clay technical field of processing equipment, is specifically related to a kind of purifying plant of attapulgite clay mineral.
Background technology
Attapulgite clay is called for short recessed soil, and the 1862 scholar Long Fuqinkefu of Nian, Russia have found the clay mineral of a kind of layer of chain-like structure first in Ural area, and he is by it called after " polygorskite ".Nowadays, this mineral products are known as again " attapulgite clay ", are called for short in " recessed soil ", as a kind of important scarcity nonmetal mineral resource, in more than 10 field extensive application such as husbandry, building materials, oil, metallurgy, food.Attapulgite clay is one of China's advantage nonmetalliferous ore, and its purposes is very extensive, is called as " kings of the soil of thousand use, ten thousand soil ".Attapulgite clay is a kind of fibrous clay mineral, has wherein been mingled with many impure minerals, because these impure mineral matter are mixed in its flocculent structure, also there is no at present a kind of good purifying plant.
Utility model content
In order to address the above problem, the purpose of this utility model is to provide a kind of purifying plant with the attapulgite clay mineral of better refining effect.
For achieving the above object, technical scheme that the utility model adopts is as follows:
A kind of purifying plant of attapulgite clay mineral, this device comprises crusher, the pulverizer being communicated with the discharge nozzle of described crusher, the shredder being communicated with the discharge nozzle of described pulverizer, be placed in the filter sieve of described shredder below, be placed in the charging basket that holds of described filter sieve below, the agitation vat being communicated with the described discharge port that holds charging basket, the hexa metaphosphoric acid sodium quantitative throwing device being communicated with described agitation vat opening for feed, the quantitative water adding device being communicated with described agitation vat opening for feed, the retort furnace being communicated with described agitation vat discharge port, and hold with described the finished product gathering barrel that charging basket discharge port is communicated with, the discharge port of described retort furnace is communicated with the opening for feed of pulverizer.
Further, described filter sieve is 200 object filter sieve.
Further, described agitation vat is the timing agitation bucket that per minute 600 turns.
Further, described retort furnace is the constant temperature heating device of 105 degrees Celsius.
Further, in the described charging basket bottom of holding, be provided with pressure inductor.
When the utility model is used, by Attapulgite Clay Minerals through crusher in crushing, pulverizer pulverize, shredder grinds, filter sieve after sieving, make particle diameter be 200 object attapulgite powderies not.By quantitative water adding device, Attapulgite powder is added to water with quality liquid-solid ratio 100:1 to agitation vat again, by hexa metaphosphoric acid sodium quantitative throwing device, to agitation vat, add again the Sodium hexametaphosphate 99 that accounts for Attapulgite powder weight 2%, in agitation vat, with 600r/m rotating speed, stir 2 hours again, standing 4 hours, upper strata slurries are taken out and are placed in retort furnace, temperature is controlled at 105 ℃ of oven dry, the attapulgite pulverizer pulverizing of oven dry, shredder grinding, filter sieve are prepared into 200 object purifying attapulgites after sieving, are finally transferred to finished product gathering barrel.Purity through the utility model Concavo-convex stick after purifying stone clay is very high, reaches more than 95%, can meet most application demands.
Accompanying drawing explanation
The picture that this accompanying drawing explanation provides is used for auxiliary to further understanding of the present utility model, forms the application's a part, does not form to improper restriction of the present utility model, in the accompanying drawings:
Fig. 1 is structural representation of the present utility model.
Embodiment
Below in conjunction with accompanying drawing and specific implementation method, describe the utility model in detail, in exemplary embodiment and description of the present utility model, be used for explaining the utility model, but not as to restriction of the present utility model.
embodiment 1:
As shown in Figure 1, the present embodiment discloses a kind of purifying plant of attapulgite clay mineral, comprise crusher 1, the pulverizer 2 being communicated with the discharge nozzle of described crusher 1, the shredder 3 being communicated with the discharge nozzle of described pulverizer 2, be placed in the filter sieve 4 of described shredder 3 belows, what be placed in described filter sieve 4 belows holds charging basket 5, the agitation vat 6 being communicated with the described discharge port that holds charging basket 5, the hexa metaphosphoric acid sodium quantitative throwing device 8 being communicated with described agitation vat 6 opening for feeds, the quantitative water adding device 7 being communicated with described agitation vat opening for feed, the retort furnace 9 being communicated with described agitation vat 6 discharge ports, and hold with described the finished product gathering barrel 10 that charging basket 5 discharge ports are communicated with, the discharge port of described retort furnace 9 is communicated with the opening for feed of pulverizer 2.
Wherein, in order to guarantee filter effect, described filter sieve is preferably 200 object filter sieve.
Wherein, in order to simplify the operation, described agitation vat is preferably the timing agitation bucket that per minute 600 turns.
Wherein, in order to simplify the operation, described retort furnace is preferably the constant temperature heating device of 105 degrees Celsius.
Wherein, in order to realize automatization sense weight, so that hexa metaphosphoric acid sodium quantitative throwing device 8 and quantitative water adding device 7 drop into appropriate material automatically, in described charging basket 5 bottoms of holding, be provided with pressure inductor to detect the weight of attapulgite in bucket.
The utility model use procedure is as follows: first by Attapulgite Clay Minerals through crusher 1 fragmentation, pulverizer 2 pulverize, shredder 3 grinds, filter sieve 4 after sieving, make particle diameter be 200 object attapulgite powderies not.By quantitative water adding device 7, Attapulgite powder is added to water with quality liquid-solid ratio 100:1 to agitation vat 6 again, by hexa metaphosphoric acid sodium quantitative throwing device 8, to agitation vat, add 6 Sodium hexametaphosphate 99s that enter to account for Attapulgite powder weight 2% again, in agitation vat 6, with 600r/m rotating speed, stir 2 hours again, standing 4 hours, upper strata slurries are taken out and are placed in retort furnace 9, temperature is controlled at 105 ℃ of oven dry, 2 pulverizing of the attapulgite pulverizer of oven dry, shredder 3 grindings, filter sieve 4 are prepared into 200 object purifying attapulgites after sieving, are finally transferred to finished product gathering barrel.Purity through the utility model Concavo-convex stick after purifying stone clay is very high, reaches more than 95%.
The technical scheme above the utility model embodiment being provided is described in detail, applied specific case herein the principle of the utility model embodiment and embodiment are set forth, the explanation of above embodiment is only applicable to help to understand the principle of the utility model embodiment; , for one of ordinary skill in the art, according to the utility model embodiment, in embodiment and range of application, all will change, in sum, this description should not be construed as restriction of the present utility model meanwhile.

Claims (5)

1. the purifying plant of an attapulgite clay mineral, it is characterized in that: this device comprises crusher, the pulverizer being communicated with the discharge nozzle of described crusher, the shredder being communicated with the discharge nozzle of described pulverizer, be placed in the filter sieve of described shredder below, be placed in the charging basket that holds of described filter sieve below, the agitation vat being communicated with the described discharge port that holds charging basket, the hexa metaphosphoric acid sodium quantitative throwing device being communicated with described agitation vat opening for feed, the quantitative water adding device being communicated with described agitation vat opening for feed, the retort furnace being communicated with described agitation vat discharge port, and hold with described the finished product gathering barrel that charging basket discharge port is communicated with, the discharge port of described retort furnace is communicated with the opening for feed of pulverizer.
2. the purifying plant of attapulgite clay mineral according to claim 1, is characterized in that:
Described filter sieve is 200 object filter sieve.
3. the purifying plant of attapulgite clay mineral according to claim 1, is characterized in that:
Described agitation vat is the timing agitation bucket that per minute 600 turns.
4. the purifying plant of attapulgite clay mineral according to claim 1, is characterized in that:
Described retort furnace is the constant temperature heating device of 105 degrees Celsius.
5. the purifying plant of attapulgite clay mineral according to claim 1, is characterized in that:
In the described charging basket bottom of holding, be provided with pressure inductor.
CN201320575483.9U 2013-09-17 2013-09-17 Purifying device for attapulgite clay minerals Expired - Fee Related CN203428929U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201320575483.9U CN203428929U (en) 2013-09-17 2013-09-17 Purifying device for attapulgite clay minerals

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201320575483.9U CN203428929U (en) 2013-09-17 2013-09-17 Purifying device for attapulgite clay minerals

Publications (1)

Publication Number Publication Date
CN203428929U true CN203428929U (en) 2014-02-12

Family

ID=50057980

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201320575483.9U Expired - Fee Related CN203428929U (en) 2013-09-17 2013-09-17 Purifying device for attapulgite clay minerals

Country Status (1)

Country Link
CN (1) CN203428929U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107265471A (en) * 2017-07-25 2017-10-20 安徽省明美矿物化工有限公司 A kind of production equipment and preparation method of high-purity clay mineral fluid product

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107265471A (en) * 2017-07-25 2017-10-20 安徽省明美矿物化工有限公司 A kind of production equipment and preparation method of high-purity clay mineral fluid product

Similar Documents

Publication Publication Date Title
CN102205972B (en) Modification method of attapulgite
CN101912811B (en) Method for preparing nepheline syenite powder
CN103232253B (en) Method for producing homogenous refractory raw material by utilizing medium or low grade bauxite ore
CN105293530A (en) Crushed and washed salt production method and device
CN204712263U (en) A kind of ceramic mud classification associating Preparation equipment
CN203428929U (en) Purifying device for attapulgite clay minerals
CN204865997U (en) Hierarchical grinding structure of parallelly connected grinding unit that vertical roller ground
CN106396624A (en) Coal gangue proppant and preparation method thereof
CN104003742B (en) A kind of high silicon magnesite tailings prepares the method for magnesium silica sand
CN205099372U (en) Powder desalinization of soil by flooding or leaching apparatus for producing
CN104803389A (en) Purification method of diatomite
CN203428925U (en) Efficient attapulgite modification processing device
CN103360030A (en) Method for producing high-plasticity ceramic kaolin (ball clay) by mine surface soil
CN102936108B (en) Preparation method of ceramsite
CN204122183U (en) A kind of tube mill screening plant
CN204865956U (en) Fast tea pulverizer of accuse
CN205443069U (en) Adopt magnesite ore crushing production magnesite clinker's device
CN203440290U (en) Preparation device for attapulgite-based soil pollution control agent
CN103923494B (en) The preparation method of lamp box advertisement film specialized superfine hydrated magnesium silicate powder
CN109205612B (en) Graphite roasting system and method
CN208679399U (en) Mechanism is crushed and screened for Brown Alundum feedstock processing
CN102390840A (en) Treatment method of dust collection powder produced in roasting process of aluminum hydroxide
CN101913892A (en) Method for producing homogenized alumina
CN207614933U (en) A kind of forced action type fine powder machine
CN205973824U (en) Novel modified processing of efficient unsmooth stick device

Legal Events

Date Code Title Description
C14 Grant of patent or utility model
GR01 Patent grant
CF01 Termination of patent right due to non-payment of annual fee

Granted publication date: 20140212

Termination date: 20140917

EXPY Termination of patent right or utility model