CN216144648U

CN216144648U - Zinc chloride flow dividing recoverer

Info

Publication number: CN216144648U
Application number: CN202120004852.3U
Authority: CN
Inventors: 李伟伟; 代佩; 邢善超; 葛成杰
Original assignee: Huaibei Mining Co Ltd
Current assignee: Huaibei Mining Co Ltd
Priority date: 2021-01-04
Filing date: 2021-01-04
Publication date: 2022-03-29
Anticipated expiration: 2031-01-04

Abstract

The utility model discloses a zinc chloride split-flow recoverer, which comprises a mesh bottom barrel filled with zinc chloride, and is characterized in that: including the bottom plate with be used for the buckle of fixed net end bucket, the shape of bottom plate is isosceles triangle, the base top fixed surface of the apex angle bottom plate of bottom plate sets up the end flap, the top fixed surface of end flap is provided with the support column, the support column is provided with the buckle towards one side of bottom plate apex angle is fixed, the middle part of bottom plate is protruding to the buckle direction along the symmetry line, the apex angle of bottom plate is the rake, the rake foot is to the buckle direction perk, two base angles of bottom plate are provided with first side shield and second side shield respectively. By adopting the scheme, the stability of the net bottom barrel is better ensured, the potential safety hazard that the net bottom barrel slips into the heavy liquid barrel is greatly reduced, the recovery efficiency of zinc chloride solution can be greatly improved, zinc chloride splashed outside the heavy liquid barrel is reduced, and the workload of cleaning after the test is also reduced.

Description

Zinc chloride flow dividing recoverer

Technical Field

The utility model belongs to the field of zinc chloride recovery, and particularly relates to a zinc chloride flow-dividing recoverer.

Background

The principle of the existing float-sink test is to float and sink coal in different density solutions mainly prepared from zinc chloride in sequence, so that the coal is divided into different density groups, materials with different density levels are obtained through float-sink separation of a plurality of density solutions, and then drying, weighing and ash content testing are carried out to obtain the relation between the quantity and the mass of the different density levels.

We found that the recovery of zinc chloride was very low for the main test agent during the test. The zinc chloride is high in price, the price per ton of the zinc chloride is up to 6200 RMB, and about 300 kilograms of the zinc chloride is consumed per month in the actual production process. The recovery rate of zinc chloride in the test production process is less than 40 percent, which is a great production waste.

In the floating and sinking test, a test link is that the fishing float is fished into a net bottom barrel by a fishing spoon, and the net bottom barrel is obliquely placed on the barrel edge to filter heavy liquid completely. During the process, the loss of heavy liquid is a main reason for the consumption of zinc chloride. And the net bottom barrel is easy to slip and fall into the heavy liquid barrel, so that zinc chloride is splashed and damaged and wasted. Zinc chloride belongs to a toxic reagent, has corrosiveness, and the aqueous solution of the zinc chloride is acidic. Once in contact with the human body during the splashing process, the eye-protecting mask causes irritation and burning damage to the skin and mucous membranes of the human body, and can have serious consequences if splashed into the eyes. In the actual production process, the situation that the zinc chloride solution splashes into eyeballs to cause personal injury actually occurs in other factories, and the screen bottom barrel slips and gradually enters the heavy liquid barrel.

At present, great medicament waste and potential safety hazards exist in the test link.

SUMMERY OF THE UTILITY MODEL

The technical problem to be solved by the utility model is to provide a zinc chloride shunting recoverer, which can complete shunting recovery of zinc chloride under a net bottom barrel; the loss of zinc chloride in the front and back directions can be prevented; the device has small volume and light weight, and is convenient to take and use at any time; the device has a simple structure, is easy to popularize, reduces the processing steps of bending, drilling, polishing and the like on materials, reduces the processing difficulty, reduces the processing technology requirement, and greatly increases the economic benefit; the structure is stable, and the service life of the device is long; simultaneously, through the increase bottom surface area, increase with the perpendicular contact surface of wall, the better stability of having guaranteed the net bottom bucket, very big reduction the net bottom bucket slippage fall into the potential safety hazard of heavy liquid bucket, can greatly promote the recovery efficiency of zinc chloride solution, the zinc chloride that drips to spatter outside the heavy liquid bucket reduces, has also reduced the work load of clearance after the experiment.

In order to achieve the purpose, the utility model adopts the technical scheme that: including the net end bucket that is equipped with zinc chloride, its characterized in that: including the bottom plate with be used for the buckle of fixed net end bucket, the shape of bottom plate is isosceles triangle, the base top fixed surface of bottom plate sets up end baffle, the top fixed surface of end baffle is provided with the support column, the support column is provided with the buckle towards one side of bottom plate apex angle is fixed, the middle part of bottom plate is protruding to the buckle direction along the symmetry line, the apex angle of bottom plate is the rake angle, the rake foot is to the buckle direction perk, two base angles of bottom plate are provided with first side shield and second side shield respectively.

According to the zinc chloride split-flow recoverer provided by the technical scheme, one end of the first side baffle extends to one waist of the bottom plate, and the other end of the first side baffle is fixedly connected with one end of the bottom baffle; one end of the second side baffle extends to the other waist of the bottom plate, and the other end of the second side baffle is fixedly connected with the other end of the bottom baffle.

According to the technical scheme, the bottom plate is made of stainless steel.

According to the zinc chloride split-flow recoverer provided by the technical scheme, the retaining ring is a rectangular steel bar connected end to end, the buckling strip is in a ring shape, the inner diameter of the buckling strip corresponds to the outer diameter of the net bottom barrel, and the inner wall of the buckling strip is tightly attached to the outer surface of the net bottom barrel.

According to the zinc chloride split-flow recoverer provided by the technical scheme, the bottom baffle is a cuboid steel block, and the bottom baffle is welded on the top surface of the bottom edge of the bottom plate in a side-standing mode.

According to the zinc chloride split-flow recoverer provided by the technical scheme, the supporting columns are vertically and fixedly welded on the side faces of the top of the bottom baffle, and the center points of the bottom ends of the supporting columns are arranged at the center points of the top sides of the bottom baffle.

According to the zinc chloride shunt recoverer provided by the technical scheme, the outer side face of the retaining ring is fixedly welded on one side surface of the supporting column, which faces the rake angle, and the plane where the retaining ring is located is perpendicular to the plane where the side face of the supporting column is located.

According to the zinc chloride split-flow recoverer provided by the technical scheme, the tilting angle of the tilting angle plane is 20 degrees, and the dihedral angle between the plane where the tilting angle is located and the plane where the bottom plate is located is 20 degrees.

By adopting the technical scheme, the zinc chloride can be shunted and recovered under the mesh bottom barrel; the loss of zinc chloride in the front and back directions can be prevented; the device has small volume and light weight, and is convenient to take and use at any time; the device has a simple structure, is easy to popularize, reduces the processing steps of bending, drilling, polishing and the like on materials, reduces the processing difficulty, reduces the processing technology requirement, and greatly increases the economic benefit; the structure is stable, and the service life of the device is long; simultaneously, through the increase bottom surface area, increase with the perpendicular contact surface of wall, the better stability of having guaranteed the net bottom bucket, very big reduction the net bottom bucket slippage fall into the potential safety hazard of heavy liquid bucket, can greatly promote the recovery efficiency of zinc chloride solution, the zinc chloride that drips to spatter outside the heavy liquid bucket reduces, has also reduced the work load of clearance after the experiment.

The utility model will be explained in more detail below with reference to the drawings and examples.

Drawings

The contents of the description and the references in the drawings are briefly described as follows:

FIG. 1 is a schematic perspective view of the apparatus of the present invention;

FIG. 2 is a schematic top view of the apparatus of the present invention;

labeled as: 1. a base plate; 2. raising the corner; 3. a bottom baffle; 4. a first side dam; 5. a second side baffle; 6. a support pillar; 7. and (7) buckling strips.

Detailed Description

The following description of the embodiments of the present invention, with reference to the accompanying drawings, will be made in further detail for the purpose of providing a more complete, accurate and thorough understanding of the inventive concepts and technical solutions of the present invention, including the shapes of the components, the structures, the mutual positions and connection relationships of the components, the functions and operating principles of the components, the manufacturing processes, the operation and use methods, and the like.

A zinc chloride reposition of redundant personnel recoverer that fig. 1 shows is including the net base bucket that is equipped with zinc chloride, including bottom plate 1 and the buckle that is used for fixed net base bucket, bottom plate 1's shape is isosceles triangle, bottom edge top fixed surface of bottom plate 1 sets up end baffle 3, end baffle 3's top fixed surface is provided with support column 6, support column 6 is provided with the buckle towards one side of 1 apex angle of bottom plate is fixed, bottom plate 1's middle part is protruding to the buckle direction along the symmetry line, the apex angle of bottom plate 1 is rake 2, the rake foot is to the buckle direction perk, two base angles of bottom plate 1 are provided with first side shield 4 and second side shield 5 respectively.

Fig. 2 is a schematic top view, in which one end of the first side baffle 4 extends to a waist of the bottom plate 1, and the other end is fixedly connected with one end of the bottom baffle 3; one end of the second side baffle 5 extends to the other waist of the bottom plate 1, and the other end is fixedly connected with the other end of the bottom baffle 3.

The bottom plate 1 is made of stainless steel. The service life of the base plate 1 made of stainless steel is longer.

The buckle ring is a cuboid steel bar connected end to end, the buckle strip 7 is in a ring shape, the inner diameter of the buckle strip 7 corresponds to the outer diameter of the net bottom barrel, and the inner wall of the buckle strip 7 is tightly attached to the outer surface of the net bottom barrel. The buckling strips 7 are welded and fixed end to end, and the buckling strips 7 enclose a circular ring.

The bottom baffle 3 is a cuboid steel block, and the side of the bottom baffle 3 is vertically welded on the top surface of the bottom edge of the bottom plate 1.

The support column 6 is vertically fixedly welded on the top side face of the bottom baffle plate 3, and the bottom center point of the support column 6 is arranged at the top center point of the bottom baffle plate 3.

The outer side surface of the buckling strip 7 is fixedly welded on one side surface of the supporting column 6 facing the rake angle 2, and the plane where the buckling strip 7 is located is perpendicular to the plane where the side surface of the supporting column 6 is located.

The plane of the rake angle 2 is tilted by 20 degrees, and the dihedral angle between the plane of the rake angle 2 and the plane of the base plate 1 is 20 degrees. The function of the rake angle 2 is to block zinc chloride which runs off towards the top angle.

During the use with net bottom bucket put into knot strip 7 fixed, net bottom bucket's bottom center is on bottom plate 1's bulge line, and two jars are placed respectively to rake angle 2, end baffle 3, first side shield 4 and second side shield 5 can effectually block the zinc chloride of flowing out outward, two waist positions of bottom plate 1, can carry out the high-efficient zinc chloride of collecting, and the device is more steady when collecting, does not have the potential safety hazard.

The utility model has been described above with reference to the accompanying drawings, it is obvious that the utility model is not limited to the specific implementation in the above-described manner, and it is within the scope of the utility model to apply the inventive concept and solution to other applications without substantial modification.

Claims

1. The utility model provides a zinc chloride reposition of redundant personnel recoverer, includes the net bottom bucket that is equipped with zinc chloride, its characterized in that: including the bottom plate with be used for the buckle of fixed net end bucket, the shape of bottom plate is isosceles triangle, the base top fixed surface of bottom plate sets up end baffle, the top fixed surface of end baffle is provided with the support column, the support column is provided with the buckle towards one side of bottom plate apex angle is fixed, the middle part of bottom plate is protruding to the buckle direction along the symmetry line, the apex angle of bottom plate is the rake angle, the rake foot is to the buckle direction perk, two base angles of bottom plate are provided with first side shield and second side shield respectively.

2. The zinc chloride split-flow recoverer according to claim 1, wherein: one end of the first side baffle extends to one waist of the bottom plate, and the other end of the first side baffle is fixedly connected with one end of the bottom baffle; one end of the second side baffle extends to the other waist of the bottom plate, and the other end of the second side baffle is fixedly connected with the other end of the bottom baffle.

3. The zinc chloride split-flow recoverer according to claim 1, wherein: the bottom plate is made of stainless steel.

4. The zinc chloride split-flow recoverer according to claim 1, wherein: the buckle ring is a cuboid steel bar connected end to end, the buckle strip is in a ring shape, the inner diameter of the buckle strip corresponds to the outer diameter of the net bottom barrel, and the inner wall of the buckle strip is tightly attached to the outer surface of the net bottom barrel.

5. The zinc chloride split-flow recoverer according to claim 1, wherein: the bottom baffle is a cuboid steel block, and the bottom baffle is welded on the top surface of the bottom edge of the bottom plate in a side-standing mode.

6. The zinc chloride split-flow recoverer according to claim 1, wherein: the support column is vertically fixedly welded on the top side face of the bottom baffle, and the bottom center point of the support column is arranged at the top center point of the bottom baffle.

7. The zinc chloride split-flow recoverer according to claim 1, wherein: the outer side face of the retaining ring is fixedly welded on one side surface of the support column, facing the rake angle, and the plane where the retaining ring is located is perpendicular to the plane where the side face of the support column is located.

8. The zinc chloride split-flow recoverer according to claim 1, wherein: the tilting angle of the tilting angle plane is 20 degrees, and the dihedral angle between the plane where the tilting angle is located and the plane where the bottom plate is located is 20 degrees.