KR20150133624A - A system and method thereof for scrubbing and classification of coarse and fines materials - Google Patents

Abstract

Disclosed are a system (100) and a method for scrubbing and classifying coarse and fine materials. The system (100) has integrated equipment for scrubbing, hydro cycloning, rinsing, sizing, dehydrating, and transferring in order to classify materials into a maximum size of five. The system (100) can extract a classified and washed product in which surface pollutants such as silica, clay, and alumina powder are substantially reduced, from a different raw material to be used for various industries. The suggested system and method specifically reduce steel manufacturing cost, and improve productivity and efficiency. According to another embodiment of the present invention, clay and ultra-fine materials existing as harmful substances are effectively removed, thereby improving productivity of industry such as construction for specifically reducing use of cement and improving strength of concrete, or the like, and adding more values thereto.

Description

FIELD OF THE INVENTION [0001] The present invention relates to a system and method for scrubbing and classifying coarse and fine materials,

The present invention relates to materials science and mineral engineering, and more particularly to systems and methods for a complete material sizing scheme.

The current solid classification system

Currently, for dry or wet classification, equipment such as dry and wet screens are used to classify coarser particles, and for finer applications screw / bucket wheel sorters are used. In the case of dry classification, the number of products that can be produced from a single unit is severely limited and also causes dust contamination. In addition, dry systems are very inefficient for classifying moisture-bearing materials. Both dry and wet screens can not effectively remove contaminants adhering to the surface of the material and are limited in the number of products that can be made into a single unit. In the case of a screw / bucket wheel sorter, it can not be used to sort coarser particles and is generally used to remove clay from finer particles. The equipment also does not remove surface contaminants or produce multi-size products in a single unit.

Disadvantages of Current Technology

The current classification is limited to the size of the materials that can be used and processed in isolation, and the number of products that can be delivered to the user in a single unit. For example, a dry / wet screen or screw sorter / bucket wheel cuts materials to different sizes, but the product still includes other foreign materials such as silica, clay and alumina, and the object of rejection also includes a large amount of usable material. This material should therefore be treated using a different system to recover the usable material from the rejection object. The final product from this system still contains impurities adhering to the surface of the material and does not purify properly because it has no scrubbing and rinsing action. Thus, additional scrubbing systems are required to remove harmful materials from the material to maximize the full potential of the material. Also in such systems there is no process to recover very fine material, so the user must install a separate micro-material recovery system in order to reprocess the object to be rejected, otherwise significant natural resources are wasted.

In view of the above mentioned disadvantages, an efficient integrated system which provides a single facility for scrubbing, hydrocycling, rinsing, sizing, dewatering and delivering to classify materials that may contain materials and / or minerals Is required.

This summary is provided to introduce a concept of a system and method for scrubbing and classifying coarse and fine particles, the concept of which will be further explained in the detailed description. This Summary is not an essential feature of the claimed subject matter nor is it used to determine or limit the scope of the subject matter claimed.

A solution is provided in the present invention by providing a system that combines several techniques, such as scrubbing, hydrocycling, rinsing, sizing, dewatering and delivery, to address the above problems and classify the material.

It is therefore a principal object of the present invention to provide a method and system for the production of a material and a method for the production of a material, And systems for scrubbing and sorting up to five products (both coarse and fine) in a single, integrated system for the mineral industry. Another object of the present invention is to maximize recovery by recycling fine usable particles and limiting waste of natural resources.

In one aspect of the present invention, the present invention is the first technology to integrate equipment for scrubbing, hydrocycling, rinsing, sizing, dewatering and delivering to classify materials into up to five sizes in a single, compact, will be. The system can extract cleaned products that are substantially reduced in surface contaminants such as silica, clay, and alumina powders from different sources for use in a variety of industries. One use of the present invention is to produce materials with up to five different sizes of high quality, rich iron ore that are used daily for upstream treatment in a furnace or kiln. The present invention will significantly improve the cost, productivity and efficiency of steelmaking. Another example is the efficient removal of clay and ultrafine water present as hazardous to the material can significantly reduce the use of cement and improve the productivity and value of the industry, such as construction, which can improve the overall strength of the concrete .

Thus, in one embodiment of the present invention, a system 100 is disclosed that performs a method for scrubbing and classifying a plurality of materials contained within an enclosure. The system comprises an abrasive wash box (AWB) (01) supplied using the enclosure - so that an appropriate amount of high pressure water is added to the mixture tube of AWB (01) to remove toxic substances from the surface of the supply material; A rinse screen 02 of a specific deck; At least one integrated product conveyor for storing at least one coarse product, the integrated product conveyor being selected from a product conveyor-1, a product conveyor-2 and a product conveyor-3; One set of primary hydrocyclones (s) (04) - the primary hydrocyclone (s) with specific pressure through a slurry pump-1 (05) and a special kind of pipeline - (05) to remove at least one fine particle as a dross and to remove at least one rejection object; A split type supply box (09) for discharging at least a part of the divided sizing and dewatering screen (10); A product conveyor-4 (11) for storing the first fine product; A set of secondary hydrocyclone (s) 14-secondary hydrocyclone (s) 14 with specific pressure through a slurry pump-2 15 and a special kind of pipeline - Receives the mixture through pump-2 (15) and removes at least one fine particle as a tail to remove at least one rejection object; A dividing sizing and dewatering screen 10; A product conveyor-5 (12) for storing a second fine product; And a programmable logic control motor control panel (16) configured to monitor the method performed by the system (100).

In another embodiment of the present invention, a method for scrubbing and classifying a plurality of materials contained within an enclosure in system 100 is disclosed. The method includes the following steps:

- receiving the material in a worn wash box (AWB) (01), scrubbing the contained material;

● Discharge the material from the AWB (01) to the rinse screen (02)

   Adding an appropriate amount of pressurized water to the rinse screen 02 to sort the coarse rinse product having at least one size,

   Dewatering and discharging the resulting coarse rinse product having at least one size, and

   Recovering the resulting coarse cleaned product having at least one size and providing it to at least one integrated product conveyor for storage, wherein the integrated product conveyor comprises a product conveyor-1, a product conveyor-2, and a product conveyor- - selected;

Discharging the recovered water from the rinse screen 02 to the puddle-1 03 in the form of a slurry together with all the fine particles obtained;

Pumping the slurry through a slurry pump-1 05 and sending it to the main hydrocyclone (s) 04 at a specific pressure;

- obtaining a mixture from the sump-1 (03) and the slurry pump-1 (05) and simultaneously removing at least one rejection object;

Discharging the fine particles obtained in the form of slurry by the main hydrocyclone (04) into the split type feed box (09);

Dewatering the obtained fine particles for recovery of the first fine product and discharging the resulting fine particles to the dividing sizing and dewatering screen 10;

Dewatering the obtained first microproduct and transferring it to the product conveyor 4 (11) for storage;

Discharging the underflow into the puddle-2 (13) in the form of a slurry for reprocessing with the fine particles obtained from the dividing sizing and dewatering screen (10);

Pumping the slurry through a slurry pump 2 (15) and sending it to the auxiliary hydrocyclone (14) at a specific pressure;

- obtaining a mixture from the sump-2 (13) and the slurry pump-2 (15) and simultaneously removing at least one rejection object;

Dewatering and discharging the obtained fine particles in the dividing sizing and dewatering screen (10) for recovery of the second fine product;

- recovering the obtained second fine product and delivering it to the product conveyor-5 (12) for storage; And

● Discharging rejected ultrafine particles from main hydrocyclone (s) 04 and secondary hydrocyclone (s) 14 with water.

These and other features and advantages will be apparent from the following detailed description of illustrative embodiments, and the detailed description should read with reference to the accompanying drawings.

The detailed description will be made with reference to the accompanying drawings. In the drawings, the leftmost digit of a reference number indicates a figure in which the reference number first appears. The same numbers are used in the drawings to denote like parts or components.

Corresponding reference characters indicate corresponding parts throughout the several views. The examples presented herein illustrate preferred embodiments of the invention in one form, and such examples should not be construed as limiting the scope of the invention in any way.

Figure 1 illustrates a system with a method flow of the present invention for scrubbing and sorting various materials shown, according to an embodiment of the present subject matter.
Figure 2 shows a method flow of the present invention for scrubbing and sorting the various materials shown, in accordance with an embodiment of the present subject matter.
FIG. 3 shows a top view (top view) of the proposed system 100 in accordance with an embodiment of the present subject matter.
Figure 4 shows an elevation (side view) of the proposed system 100 in accordance with an embodiment of the present subject matter.
Those skilled in the art will appreciate that the components in the figures are shown for simplicity and clarity and may not be drawn to scale. For example, to facilitate an understanding of the various exemplary embodiments of the present disclosure, the dimensions of some of the elements in the figures may be exaggerated relative to other elements.
It is to be understood that the appended drawings are intended for purposes of illustrating the concepts of the invention and may not scale.

BRIEF DESCRIPTION OF THE DRAWINGS For a better understanding of the objects, technical solutions and advantages of the present application, embodiments will now be described with reference to the accompanying drawings.

The objects, advantages and other novel features of the present invention will become apparent to those skilled in the art from the following detailed description, when read in conjunction with the appended claims and the accompanying drawings.

The terms and words used in the following description and claims are not limited to bibliometric meanings and are used by the inventor only in order to make the invention clear and consistent. It is therefore to be understood by one of ordinary skill in the art that the following description of exemplary embodiments of the present invention is provided for illustrative purposes only and is not intended to limit the invention as defined in the appended claims and their equivalents .

It should be understood that the singular < RTI ID = 0.0 > term < / RTI > includes plural unless explicitly stated otherwise.

The term "substantially" does not necessarily mean that the stated characteristic, parameter or value need not be obtained accurately and that variations or variations, such as tolerances, measurement errors, measurement accuracy limits and other factors, In the amount that does not exclude the use of the "

The features described / described or illustrated with respect to one embodiment may be used in the same or similar manner in one or more other embodiments and / or in combination with or instead of features of other embodiments.

As used herein, the term " comprises / comprising " is intended to specify the presence of stated features, integers, steps or components but may include the presence or addition of one or more other features, integers, steps, Or add-ons.

The present invention involves the incorporation of any amount of low grade and hazardous particles through a highly efficient, integrated continuous or batch process to improve the end product for consumers and lower production costs for users in mining, quarry and material recycling industries. Such as mineral ores, sand, and the like, to produce coarse and fine materials to be sorted.

An advantage of the present invention is that surface contaminants from the feed can be removed from the feed by an integrated scrubbing and sorting process to produce up to five sizes of product while continuously reprocessing the rejected object and significantly reducing the loss of fine material to increase overall recovery. And a unique process of rejecting harmful particles.

The proposed system and method of the present invention is applicable to the production of mineral ores such as iron, bauxite, manganese, coal, lignite, chrome iron, silica sand and the like, as well as manufactured sand, grinder dust, river sand, frac sand, foundry sand ), Construction and demolition wastes, and the like. The system is particularly suitable for effectively removing surface contaminants and hazardous particles from lumps, ore particulates, mining overruns, stored ore stockpiles.

The present invention is the first technology to integrate facilities for scrubbing, hydrocycling, rinsing, sizing, dehydrating and delivering to classify materials into up to five sizes with a single, compact, integrated design. The system can extract cleaned products that are substantially reduced in surface contaminants such as silica, clay, and alumina powders from different sources for use in a variety of industries. One use of the present invention is to produce materials with up to five different sizes of high quality, rich iron ore that are used daily for upstream treatment in a furnace or kiln. The present invention will significantly improve the cost, productivity and efficiency of steelmaking. Another example is the efficient removal of clay and ultrafine water present as hazardous to the material can significantly reduce the use of cement and improve the productivity and value of the industry, such as construction, which can improve the overall strength of the concrete .

DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS Now, preferred embodiments of the present invention will be described in detail with reference to the accompanying drawings. In the drawings, the same or similar components are denoted by the same reference numerals even though they are shown in different drawings. In the following description, a detailed description of known functions and configurations incorporated herein will be omitted when the subject matter of the present invention can be obscure.

Although exemplary embodiments of the present invention will now be described, the present invention may be practiced without the specific details, and in order to achieve a developer's specific goals, such as meeting system-related and business-related constraints (which will vary from system to system) It will be appreciated that many practice-specific decisions may be made on the invention described herein. Such a development effort can be complex and time consuming, and is nevertheless common to those of ordinary skill in the art having the benefit of this disclosure. For example, in order to avoid obscuring or undue limitation of the present invention, selected points are not shown in detail but are shown in block diagram form. Those skilled in the art will use such descriptions and expressions to explain and convey the nature of the work to others skilled in the art. The present invention will now be described with reference to the drawings described below.

While embodiments of systems and methods for scrubbing and sorting coarse and fine particles are disclosed and can be implemented with many different computing systems, environments, and / or configurations, embodiments are described in connection with the following exemplary systems.

As used herein, the term " comprises / comprising " is intended to specify the presence of stated features, integers, steps or components but may include the presence or addition of one or more other features, integers, steps, Or add-ons.

Referring now to FIG. 1, a system 100 is disclosed that performs a method for scrubbing and classifying a plurality of materials contained within an enclosure. The system comprises a worn wash box (AWB) 01 supplied using an enclosure (so that a suitable amount of high pressure water is added to the mixture tube of AWB (01) to remove toxic substances from the surface of the feed material); A rinse screen 02 of a specific deck; At least one integrated product conveyor for storing at least one coarse product, the integrated product conveyor being selected from a product conveyor-1, a product conveyor-2 and a product conveyor-3; A set of primary hydrocyclone (s) (04) (the primary hydrocyclone (s)) from Slurry Pump-1 (05) and a particular type of pipeline from Slurry- (05) to receive the mixture and remove at least one fine particle as a tail to remove at least one rejection object); A split type supply box (09) for discharging at least a part of the divided sizing and dewatering screen (10); A product conveyor-4 (11) for storing the first fine product; A set of secondary hydrocyclone (s) 14 (secondary hydrocyclone (s) 14) having a specific pressure through a slurry pump-2 15 and a special kind of pipeline are supplied from the sump- Receives the mixture through pump-2 (15) and removes at least one fine particle as a tail to remove at least one rejection object); A dividing sizing and dewatering screen 10; A product conveyor-5 (12) for storing a second fine product; And a programmable logic control motor control panel 16 configured to monitor the method performed by the system 100.

In one embodiment, the rinsing screen may be selected from the group comprising a single deck, a double deck, a triple deck, and combinations thereof.

In one embodiment, the material may be a material or a mineral. The material may be selected from the group comprising manufactured sand, grinder dust, river sand, glass grade sand, frac sand, foundry sand, construction waste, disposal waste, and combinations thereof. The mineral may be selected from the group comprising iron ore, bauxite, manganese, coal, lignite, chromium iron, silica sand and combinations thereof. Iron ore is obtained from the mining of minerals and materials, from mines, stored stocks, and combinations thereof.

In an embodiment, the materials are preferably sorted into a maximum of five sizes. The material preferably has a particle size in the range of 0.045 microns to 100 mm.

In one embodiment of the present invention, "scrubbing and sorting" as used herein means a process used by the apparatus to produce products of up to five sizes while substantially cleansing the surface of the material. And the rejected particles are reprocessed by the system for further sorting operations, thereby reducing material waste.

The system is capable of separating five sizes of products manufactured in different stages of the process and categorized into a wide size range of 0.045 mm to 100 mm. For example, in the case of iron ore, the device may be classified as 0.045 mm to 2 mm, 2 mm to 5 mm, 5 mm to 18 mm, 18 mm to 40 mm and oversized or according to the requirements of the user.

In one embodiment, a method / process is provided for sorting various materials and / or minerals having varying sizes. The system may include and supply the materials and / or minerals to be treated to an abrasive wash box (AWB) 01 via a common supply system. And an appropriate amount of high pressure water is added to the AWB mixture tube to remove toxic substances from the surface of the feed material. By the intelligent design of the AWB box, scrubbing action can be provided and contaminants sticking to the surface of the material fall off. The AWB does not require an additional drive system and the scrubbing action is achieved by forced rotation and turbulence of the material under a constant-pressure water jet in the closed chamber. This scrubbing system will have low maintenance requirements.

The scrubbed material from the AWB is then discharged to a rinsing screen 02 for primary screening of coarse particles. A suitable amount of pressurized water is then added to each deck of the rinse screen to obtain coarse particles that are cleaner. The rinsing screen 02 may be a single / double / triple deck depending on the number of coarse products required by the user. The coarse particles classified into three sizes are then transferred to the Integrated Product Conveyor-1 (06), Product Conveyor-2 (07) and Product Conveyor-3 (08) for individual storage.

And, unclassified finer material from the bottom deck of the rinsing screen with fine particles (usually -5 mm) is discharged in slurry form to the underlying puddle-1 (labeled "03").

The slurry is pumped through a slurry pump-1 (05) and a particular type of pipeline to a set of primary hydrocyclones (s) (04) at specific pressures. The primary hydrocyclone (s) receives the mixture from the sump-1 (03) through the slurry pump-1 (05) and removes the rejected object by removing fine particles as tailings. The sorted particles are simultaneously recovered as a first fine product.

Here, the fine product of the first size is discharged by the main hydrocyclone (s) in the form of a slurry together with water, and is discharged to a part of the dividing sizing and dewatering screen 10, Lt; / RTI > An appropriate amount of water is then added to the screen through the spray bar to flush the remaining rejected particles with water. Then, the sorted first micro-products are dehydrated simultaneously and transferred to the product conveyor-4 (11) for storage.

The underflow of the dividing sizing and dewatering screen 10 is discharged in the form of a slurry into the lower sump-2 (13) together with the ultrafine rejection particles

The slurry is then reprocessed by the system to further recover one or more products.

The slurry is pumped through a slurry pump-2 (15) and a special kind of pipeline to a set of auxiliary hydrocyclone (s) 14 at a specific pressure to further recycle the slurry and recover the second microproduct . The secondary hydrocyclone (s) receives the mixture from the sump-2 (13) through the slurry pump-2 (15) and removes the object to be refused by removing ultrafine refuse particles as tailings. The sorted particles are simultaneously recovered to the maximum as a second fine product.

The sizable useful product is then discharged by the secondary hydrocyclone (s) in the form of a slurry together with water, and discharged into a separate supply box (labeled "09" Lt; / RTI > The sorted final product is then dehydrated and transferred to the product conveyor 5 (12) for storage.

The waste slurry from primary and secondary hydrocyclone (s) 04, 14 is fed through a wear resistant tubing for other treatments that the user would like to perform. The programmable logic control motor control panel 16 controls the entire process system according to the desired parameters.

The present invention allows extensive pre-assembly and electrical wiring with extensive testing done at the factory prior to dispatch, thus minimizing the intervention required by installation and contract engineers.

Referring now to FIG. 2, a method for scrubbing and classifying a plurality of materials contained within an enclosure in a system 100 is disclosed.

In step 202, the material is received in a worn wash box (AWB). Also, the contained material is scrubbed.

In step 204, the material is discharged from the AWB 01 to the rinsing screen 02. An appropriate amount of pressurized water is added to the rinse screen 02 to sort the coarse rinse product having at least one size. Further, the obtained coarse washed product having at least one size is dehydrated and discharged. In addition, the obtained coarse cleansed product having at least one size is recovered and provided to at least one integrated product conveyor for storage, the integrated product conveyor comprising a product conveyor-1, a product conveyor-2 and a product conveyor- .

In step 206, the recovered water from the rinsing screen 02 is discharged into the puddle-1 (03) in the form of a slurry together with all the fine particles obtained.

In step 208, the slurry is pumped through slurry pump-1 05 to the main hydrocyclone (s) 04 at a certain pressure.

In step 210, a mixture is obtained from the sump-1 (03) and the slurry pump-1 (05), and at the same time at least one rejection object is removed.

In step 212, the fine particles obtained in the form of slurry by the main hydrocyclone 04 are discharged into the split type feed box 09. [

In step 214, the resulting fine particles go to the dividing sizing and dewatering screen 10 and are dewatered and discharged for recovery of the first fine product.

In step 216, the obtained first microproduct is dewatered and transferred to the product conveyor-4 (11) for storage.

In step 218, the underflow together with the fine particles obtained from the dividing sizing and dewatering screen 10 is discharged into the puddle-2 13 in slurry form for reprocessing.

In step 220, the slurry is pumped through slurry pump-2 (15) to the secondary hydrocyclone (14) at a specific pressure.

In step 222, a mixture is obtained from the sump-2 (13) and the slurry pump-2 (15) and at least one rejection object is removed at the same time.

In step 224, the obtained fine particles are dehydrated by the dividing sizing and dewatering screen 10 and discharged for recovery of the second fine product.

In step 226, the obtained second microproduct is recovered and transferred to the product conveyor 5 (12) for storage.

At step 228, the ultrafine particles to be rejected from the primary hydrocyclone (s) 04 and the secondary hydrocyclone (s) 14 are discharged with water.

In one embodiment, the rinsing screen may be selected from a single deck, a double deck, a triple deck, and combinations thereof.

In one embodiment, the material may be a material or a mineral. The material may be selected from the group comprising grinding dust, river sand, glass grade sand, foundry sand, construction waste, dismantled waste, and combinations thereof. The mineral may be selected from the group comprising iron ore, bauxite, manganese, coal, lignite, chromium iron, silica sand and combinations thereof. Iron ore is obtained from the mining of minerals and materials, from mines, stored stocks, and combinations thereof.

In one embodiment, the materials are preferably sorted into a maximum of five sizes. The material preferably has a particle size in the range of 0.045 microns to 100 mm.

Referring now to FIG. 3, there is shown a top view (top view) of the proposed system 100 in accordance with an embodiment of the present subject matter.

Referring now to FIG. 4, there is shown an elevation (side view) of the proposed system 100 in accordance with an embodiment of the present subject matter.

Various configurations used in the present invention, including, but not limited to, a worn wash box, a rinse screen, a sump, a hydrocyclone (s), a split type supply box, a split type sizing and dewatering screen, Those skilled in the art will appreciate that the elements are already known for their use and that no special modifications or changes are made to make them novel. Moreover, the simplicity and simple use of these components as claimed in the present invention make the invention more efficient and user-friendly. It should also be appreciated that the plurality of materials contained within the enclosure may be manufactured using a simple stock rather than having the exact size and shape as used in the general supply system used in the present invention and as permitted by the present technology will be.

The exemplary embodiment discussed above can provide certain advantages. While it is not necessary to practice aspects of the present invention, these advantages may include:

1. The scrubbing system can isolate contaminants and remove such objects that stick to the surface of the material. This is a significant advantage over traditional systems that do not have integrated scrubbing facilities with the system.

2. The required installation space is surprisingly smaller compared to traditional systems of the same capacity, requiring very large areas. Due to its compact nature, the system can be conveniently used in urban areas, factories, waste management sites, mobile and hilly areas. Also, the upstream process can be easily attached to the system.

3. A belt conveyor is attached to store all products. This is a significant advantage over traditional systems where a separate material handling system must be installed for the product.

4. Power consumption is dramatically reduced due to the compact design of the system, which requires less material movement.

5. It can be fully assembled and assembled in the factory, thus significantly shortening the installation time and eliminating the risk associated with on-site production. In addition to longer installation times, the high costs and risks of field production are generally associated with traditional systems.

6. Modular design that can be easily dismantled and shipped to containers worldwide. The most traditional equipment can not be efficiently shipped. Modularity also helps the user relocate the plant to other project sites. This is also difficult with conventional systems.

7. Due to the standardization of the drawings, the time taken to manufacture the present invention is considerably less. Conventional systems are designed to the requirements of the field and are thus non-standard, resulting in longer lead times for manufacturing.

8. The integrated steel chassis, which allows the weight of the components installed in the system to be better dispersed, lowers the requirement level for foundation foundations. Traditional systems are installed on a civil pedestal that takes high cost and construction time.

9. The system is fully equipped with all electrical cables and programmable logic control panels, eliminating the need for electrical work in the field. This is a big advantage compared to traditional systems that have to be electrically connected at the project site.

Finally, it should be understood that the above embodiments are used merely to illustrate the technical solutions of the present invention and are not intended to be limiting thereof. Although the present application has been described in detail with reference to the preferred embodiments described above, it should be understood that various modifications, alterations, or equivalent replacements can be made by those skilled in the art without departing from the scope of the present application and are included in the scope of the present application.

Claims (17)

CLAIMS 1. A method for scrubbing and classifying a plurality of materials contained within an enclosure in a system (100)
Receiving the material in a worn wash box (AWB) (01) and scrubbing the contained material;
Discharging the material from the AWB 01 to the rinse screen 02,
Adding an appropriate amount of pressurized water to the rinse screen 02 to sort the coarse rinse product having at least one size,
Dewatering and discharging the resulting coarse rinse product having at least one size, and
Recovering the resulting coarse cleaned product having at least one size and providing it to at least one integrated product conveyor for storage, wherein the integrated product conveyor is selected from a product conveyor-1, a product conveyor-2 and a product conveyor-3 ≪ / RTI > to a rinse screen;
Discharging the recovered water from the rinse screen 02 into the puddle-1 03 in the form of a slurry together with all the fine particles obtained;
Pumping the slurry through a slurry pump-1 05 and sending it to the main hydrocyclone (s) 04 at a specific pressure;
Obtaining a mixture from the sump-1 (03) and the slurry pump-1 (05) and simultaneously removing at least one rejection object;
Discharging the fine particles obtained in the form of a slurry by the main hydrocyclone (04) into the split type feed box (09);
Dewatering the resulting fine particles for recovery of the first fine product and discharging the resulting fine particles to a dividing sizing and dewatering screen 10;
Dewatering the obtained first microproduct and transferring it to the product conveyor-4 (11) for storage;
(13) in the form of a slurry for reprocessing together with the obtained fine particles from the dividing sizing and dewatering screen (10);
Pumping the slurry through a slurry pump-2 (15) and sending it to the auxiliary hydrocyclone (14) at a specific pressure;
Obtaining a mixture from the sump-2 (13) and the slurry pump-2 (15) and simultaneously removing at least one rejection object;
Dewatering and discharging the obtained fine particles in the dividing sizing and dewatering screen (10) for the recovery of the second fine product;
Recovering the obtained second fine product and transferring it to the product conveyor 5 (12) for storage; And
A method for scrubbing and classifying a plurality of materials contained in a enclosure in a system, comprising: discharging rejected ultrafine particles from the primary hydrocyclone (s) 04 and the secondary hydrocyclone (s) Way. The method according to claim 1,
Wherein the material is a material. 3. The method of claim 2,
Wherein the material is selected from the group comprising manufactured sand, grinder dust, river sand, glass grade sand, frac sand, foundry sand, construction waste, disposal waste, and combinations thereof. The method according to claim 1,
Wherein said material is a mineral. 5. The method of claim 4,
Wherein the mineral is selected from the group comprising iron ore, bauxite, manganese, coal, lignite, chromium iron, silica sand and combinations thereof. 6. The method of claim 5,
The iron ores are obtained from the mining of minerals and materials, mining minerals, stored stocks and combinations thereof. The method according to claim 1,
Wherein the material is preferably sorted into a maximum of five sizes. 8. The method according to any one of claims 1 to 7,
Wherein the material preferably has a particle size in the range of 0.045 microns to 100 mm. A system (100) for performing a method for scrubbing and sorting a plurality of materials contained within an enclosure,
(01), which is supplied using the enclosure, whereby an appropriate amount of high pressure water is added to the mixture tube of AWB (01) to remove harmful substances from the surface of the supply material, (AWB) (01);
A rinse screen 02 of a specific deck;
At least one integrated product conveyor for storing at least one coarse product, said integrated product conveyor comprising at least one integrated product conveyor selected from a product conveyor-1, a product conveyor-2 and a product conveyor-3;
(S) (04) having a specific pressure through a slurry pump-1 (05) and a special kind of pipeline, wherein the main hydrocyclone -1 (05) and the at least one fine particle as a scum is removed to remove at least one rejection object; the main hydrocyclone (s);
A split type supply box (09) for discharging at least a part of the divided sizing and dewatering screen (10);
A product conveyor-4 (11) for storing the first fine product;
(S) 14 as a set of secondary hydrocyclones (s) 14 having a specific pressure through a slurry pump-2 15 and a special kind of pipeline, the secondary hydrocyclone (s) Through the slurry pump-2 (15) to receive the mixture and remove at least one fine particle as a tail to remove at least one rejection object;
A dividing sizing and dewatering screen 10;
A product conveyor-5 (12) for storing a second fine product; And
A system for scrubbing and classifying a plurality of materials contained within an enclosure, the system comprising a programmable logic control motor control panel (16) configured to monitor a method performed by the system. 10. The method of claim 9,
Wherein the rinse screen is selected from the group comprising a single deck, a double deck, a triple deck, and combinations thereof. 10. The method of claim 9,
Wherein the material is a material. 12. The method of claim 11,
Wherein the material is selected from the group consisting of manufactured sand, grinder dust, steel sand, glass grade sand, molding sand, construction waste, dismantled waste, and combinations thereof. 10. The method of claim 9,
Wherein the material is a mineral. 14. The method of claim 13,
Wherein the mineral is selected from the group consisting of iron ore, bauxite, manganese, coal, lignite, chrome iron, silica sand and combinations thereof. 15. The method of claim 14,
The iron ore is obtained from mining of minerals and materials, mining minerals, stored stocks and combinations thereof. 10. The method of claim 9,
The material is preferably sorted into a maximum of five sizes. 17. The method according to claim 9 or 16,
The material preferably has a particle size in the range of 0.045 microns to 100 mm.

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