Ore pulp separation speed reduction diffusion plate
By designing a slurry separation and speed reduction diffusion plate including inclined bottom plate, V-shaped plate, liquid resisting plate and inclined plate, the problem of fast slurry flow rate in the prior art is solved, and a more stable liquid flow and more efficient sedimentation effect are achieved.
Patent Information
- Application Number
- CN202421589842.0
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-07-05
- Publication Date
- 2025-05-13
- Estimated Expiration
- 2034-07-05
AI Technical Summary
The existing ore slurry separation speed diffusion plate has poor settlement effect, fast flow rate leads to a large area, and the upper layer clear liquid is remixed with the ore, causing ore loss.
A slurry separation speed diffusion plate including a base plate, a bracket, a vertical baffle, an overflow port, a liquid resisting plate, an inclined plate and a V-shaped plate are designed. By tilting the bottom plate and setting the V-shaped plate, a liquid resisting plate and an inclined plate, the slurry flow rate and flow direction are adjusted, kinetic energy is reduced, and settlement is promoted.
The slurry flow rate is reduced, the liquid flow stability is improved, the settlement effect is enhanced, the mineral loss is reduced, and the mineral separation effect is improved.
Smart Images
Figure CN222854702U_ABST
Abstract
Description
Technical Field
[0001] The utility model relates to the technical field of solid-liquid sedimentation separation, and more specifically, to a pulp separation speed reduction diffusion plate. Background Art
[0002] The main function of the slurry separation speed reduction diffusion plate is to accelerate the sedimentation and enrichment of minerals in the slurry, and at the same time overflow the upper clear liquid to facilitate the separation of excess water in the sedimentation and reduce the time required for drying.
[0003] The existing sedimentation plate has a fast slurry flow rate, resulting in poor sedimentation effect. The sedimentation plate process needs to be increased, resulting in a large floor space. The baffle at the overflow hinders the flow of slurry, causing turbulence in the upper clear liquid, resulting in re-mixing of the minerals after sedimentation in the lower layer, causing mineral loss. Utility Model Content
[0004] In order to overcome the above-mentioned defects of the prior art, the utility model provides a pulp separation speed reduction diffusion plate.
[0005] To achieve the above-mentioned purpose, the utility model provides the following technical solutions: a slurry separation deceleration diffusion plate, comprising a bottom plate, the bottom plate is tilted, a bracket is fixed below the bottom plate, a baffle is fixed along the edge of the bottom plate, and the baffle is provided with a liquid inlet at the upper end of the bottom plate; a discharge port is provided at the lower end of the bottom plate, and the bottom plate expands from the upper end to the lower end; it also includes an overflow port, a liquid blocking plate, an inclined plate and a V-shaped plate; the liquid blocking plate is fixed at the lower end of the bottom plate, the discharge port is located between the bottom plate and the liquid blocking plate, and a raised inclined plate is provided on one side of the liquid blocking plate close to the upper end of the bottom plate, the inclined plate is inclined along the inclination direction of the bottom plate and points to the discharge port; there are a plurality of V-shaped plates, which are fixed in an array on the upper surface of the bottom plate, and the tip of the V-shaped plate faces the upper end of the bottom plate; there are two overflow ports, which are arranged at the corresponding positions of the baffles on both sides of the bottom plate and are located at one end of the baffle close to the discharge port, and the overflow port is a triangular through hole, and its tip faces the liquid inlet.
[0006] As a further preferred embodiment of the present invention, there are two liquid inlets, which are respectively opened at relative positions corresponding to the baffle plate and located at one end of the baffle plate away from the discharge port, and the liquid inlets are respectively fixed with feed pipes.
[0007] It can be seen that by relatively arranging the liquid inlets, the liquid flows relatively, and the flow direction is perpendicular to the inclined direction, which reduces kinetic energy, reduces flow velocity, and facilitates sedimentation.
[0008] As a further preferred embodiment of the present invention, the liquid-blocking plate further comprises a rotating shaft and a fixed plate, wherein the fixed plate is fixedly connected to the bottom plate; the rotating shaft is fixedly connected to the inclined plate and is rotatably connected to the fixed plate, and the rotating shaft is rotatably connected to the fixed plate.
[0009] As a further preferred embodiment of the present invention, connecting plates are fixed on both sides of the fixing plate, and the connecting plates are fixedly connected to the baffle plate and the bottom plate.
[0010] As a further preferred embodiment of the utility model, a hexagonal slot is provided at one end of the rotating shaft along the axial direction; a clamping block is connected to the hexagonal slot, and the clamping block is used to limit the rotation of the rotating shaft.
[0011] As a further preferred embodiment of the present invention, the card block includes a latch pin, a rotating pin and a card plate, the card plate is L-shaped, and one end face of the L-shape abuts against the fixed plate; the rotating pin and the latch pin are hexagonal columns, which are symmetrically fixed on both sides of the other end face of the L-shape of the card plate, the hexagonal columns cooperate with the hexagonal slots, the rotating pin facilitates the rotation of the shaft, and the card plate cooperates with the fixed plate to limit the rotation of the latch pin, thereby limiting the rotation of the shaft.
[0012] It can be seen that the angle of the inclined plate can be adjusted and fixed, so it is convenient to adjust according to the depth of the slurry.
[0013] As a further preferred embodiment of the utility model, a mineral box is provided below the discharge port, the upper opening of the mineral box is connected to the discharge port, and the mineral box is fixed to the lower end of the bottom plate; a water tank is fixed to the side of the mineral box close to the liquid inlet, and the water tank is located below the overflow port; through holes are provided at the bottom of the water tank and the mineral box, and the arrangement of the water tank and the mineral box facilitates the recovery of minerals and prevents overflow liquid from polluting the environment.
[0014] Technical effects and advantages of the utility model:
[0015] 1. The utility model adopts a diffusion plate with a narrow upper end and a wide lower end, which reduces the flow rate of the slurry and facilitates sedimentation.
[0016] 2. The utility model reduces the kinetic energy of the ore pulp and the flow rate by fixing a V-shaped plate on the bottom plate, thereby facilitating sedimentation.
[0017] 3. The liquid-blocking plate of the utility model is tilted to reduce the collision between the ore pulp and the liquid-blocking plate, so that the liquid flow is stable and the upper clear liquid is prevented from remixing with the ore material.
[0018] In summary, the utility model reduces the slurry flow rate, improves the liquid flow stability, enhances the sedimentation effect, and improves the ore separation effect. BRIEF DESCRIPTION OF THE DRAWINGS
[0019] Figure 1 It is a stereoscopic diagram of the slurry separation speed reduction diffusion plate of the utility model.
[0020] Figure 2 It is a top view of the slurry separation speed reduction diffusion plate of the utility model.
[0021] Figure 3 for Figure 2 AA side section view.
[0022] Figure 4 It is a bottom view of the slurry separation speed reduction diffusion plate of the utility model.
[0023] Figure 5 for Figure 1 Enlarged view of point B.
[0024] Figure 6 It is a three-dimensional diagram of the card block of the utility model.
[0025] Figure 7 It is an assembly diagram of the utility model.
[0026] The accompanying drawings are marked as follows: 1, liquid inlet; 2, V-shaped plate; 3, baffle; 4, overflow port; 5, liquid blocking plate; 6, bottom plate; 7, discharge port; 8, clamping block; 501, inclined plate; 502, rotating shaft; 503, fixed plate; 801, latch; 802, rotating pin; 803, clamping plate; 9, bracket; 10, water tank; 11, mineral box; 12, feed pipe. DETAILED DESCRIPTION
[0027] The following will be combined with the drawings in the embodiments of the utility model to clearly and completely describe the technical solutions in the embodiments of the utility model. Obviously, the described embodiments are only part of the embodiments of the utility model, not all of the embodiments. Based on the embodiments in the utility model, all other embodiments obtained by ordinary technicians in this field without creative work are within the scope of protection of the utility model.
[0028] As attached Figure 1-3 and Figure 7 A slurry separation and deceleration diffusion plate shown in the figure comprises a bottom plate 6, an overflow port 4, a liquid blocking plate 5, an inclined plate 501 and a V-shaped plate 2; the bottom plate 6 is placed at an angle, and a bracket 9 is fixed thereunder; a vertically upward baffle 3 is fixed along the edge of the bottom plate 6; the baffle 3 is provided with a liquid inlet 1 at the upper end of the bottom plate 6; there are two liquid inlets 1, which are respectively provided at relative positions corresponding to the baffle 3 and are located at the end of the baffle 3 away from the discharge port 7; feed pipes 12 are respectively fixed to the liquid inlets 1, and the liquid flows relatively through the relative arrangement of the liquid inlets 1, and the flow direction is perpendicular to the inclined direction, thereby reducing kinetic energy, reducing flow velocity, and facilitating sedimentation.
[0029] See also Figure 4 As shown, a discharge port 7 is provided at the lower end of the bottom plate 6, and the bottom plate 6 expands from the upper end to the lower end. By adjusting the flow area of the bottom plate 6, the flow velocity is reduced to improve the sedimentation effect;
[0030] The liquid-blocking plate 5 is fixed to the lower end of the bottom plate 6, and the discharge port 7 is located between the bottom plate 6 and the liquid-blocking plate 5. A raised inclined plate 501 is provided on one side of the upper end of the liquid-blocking plate 5 close to the bottom plate 6, and the inclined plate 501 is inclined along the inclination direction of the bottom plate 6 and points to the discharge port 7; there are multiple V-shaped plates 2, which are fixed in an array on the upper surface of the bottom plate 6, and the tip of the V-shaped plate 2 is facing the upper end of the bottom plate 6; there are two overflow ports 4, which are arranged at corresponding positions of the baffles 3 on both sides of the bottom plate 6, and are located at one end of the baffle 3 close to the discharge port 7, and the overflow port 4 is a triangular through hole, and its tip is facing the liquid inlet 1.
[0031] During the working process of the utility model, the slurry enters the bottom plate 6 from the liquid inlet 1, and is blocked by the V-shaped plate 2, so that the flow rate is reduced, the ore material and the upper clear liquid in the slurry are separated, and the clear liquid flows out from the overflow port 4.
[0032] In the embodiment of the utility model, the liquid-blocking plate 5 further comprises a rotating shaft 502 and a fixed plate 503, wherein the fixed plate 503 is fixedly connected to the bottom plate 6; the rotating shaft 502 is fixedly connected to the inclined plate 501 and is rotatably connected to the fixed plate 503, and the rotating shaft 502 is rotatably connected to the fixed plate 503. Connecting plates are fixedly provided on both sides of the fixed plate 503, and the connecting plates are fixedly connected to the baffle plate and the bottom plate 6.
[0033] like Figure 5 and Figure 6 As shown, in the embodiment of the utility model, a hexagonal slot is provided at one end of the rotating shaft 502 along the axial direction; the hexagonal slot is connected to a clamping block 8, and the clamping block 8 is used to limit the rotation of the rotating shaft 502.
[0034] In an embodiment of the utility model, the clamping block 8 includes a latch pin 801, a rotating pin 802 and a clamping plate 803, wherein the clamping plate 803 is L-shaped, and one end face of the L-shape abuts against the fixed plate 503; the rotating pin 802 and the latch pin 801 are hexagonal columns, which are symmetrically fixed on both sides of the other end face of the L-shape of the clamping plate 803, and the hexagonal columns cooperate with the hexagonal slots.
[0035] During the operation of the present invention, the rotating pin 802 is inserted into the hexagonal slot, and the rotating clamping plate 803 is rotated to facilitate the rotation of the rotating shaft 502; after adjusting to the appropriate position, the rotating pin 802 is pulled out, and the latch 801 is inserted, so that the clamping plate 803 and the fixed plate 503 cooperate to limit the rotation of the latch 801, and then limit the rotation of the rotating shaft 502, thereby completing the positioning of the inclined plate 501, and then adjusting the distance between the bottom end of the inclined plate 501 and the bottom plate 6, reducing the collision area, and improving the sedimentation and separation effect.
[0036] In the embodiment of the utility model, a mineral box 11 is provided below the discharge port 7, the upper end opening of the mineral box 11 is connected to the discharge port 7, and the mineral box 11 is fixed to the lower end of the bottom plate 6; a water tank 10 is fixed to the side of the mineral box 11 close to the liquid inlet 1, and the water tank 10 is located below the overflow port 4; through holes are provided at the bottom of the water tank 10 and the mineral box 11, and the arrangement of the water tank 10 and the mineral box 11 facilitates the recovery of minerals and prevents overflow liquid from polluting the environment.
[0037] During the working process of the utility model, the supernatant liquid flows into the water tank 10 through the overflow port 4, and the settled mineral material enters the mineral material box 11 through the discharge port 7, and is then recovered and processed through the through hole.
[0038] The contents not described in detail in the specification belong to the prior art known to those skilled in the art, and the model parameters of each electrical appliance are not specifically limited, and conventional equipment can be used. In this technical solution, the electrical control components not mentioned are not shown in the figure because they belong to the prior art and will not be described here.
[0039] The above description is only a preferred embodiment of the present invention and is not intended to limit the present invention. Any modifications, equivalent substitutions, improvements, etc. made within the spirit and principles of the present invention should be included in the protection scope of the present invention.
Claims
1. A pulp separation and deceleration diffusion plate, comprising a bottom plate, the bottom plate is placed obliquely, a bracket is fixed below the bottom plate, a baffle is fixed vertically upward along the edge of the bottom plate, the baffle is provided with a liquid inlet at the upper end of the bottom plate; a discharge port is provided at the lower end of the bottom plate, characterized in that: The bottom plate expands from the upper end to the lower end; It also includes overflow ports, liquid blocking plates, inclined plates and V-shaped plates; The liquid-blocking plate is fixed to the lower end of the bottom plate, the discharge port is located between the bottom plate and the liquid-blocking plate, and a raised inclined plate is provided on one side of the upper end of the liquid-blocking plate close to the bottom plate, the inclined plate is inclined along the inclination direction of the bottom plate and points to the discharge port; There are a plurality of V-shaped plates, which are fixed in an array on the upper surface of the bottom plate, and the tip of the V-shaped plate faces the upper end of the bottom plate; There are two overflow ports, which are arranged at corresponding positions of the baffles on both sides of the bottom plate and are located at one end of the baffle close to the discharge port. The overflow ports are triangular through holes with their tips facing the liquid inlet.
2. The slurry separation and deceleration diffusion plate according to claim 1, characterized in that: There are two liquid inlets, which are respectively opened at the relative positions of the baffles on the corresponding two sides and are located at the end of the baffle away from the discharge port. The liquid inlets are respectively fixed with feed pipes.
3. The slurry separation speed reduction diffusion plate according to claim 1, characterized in that: The liquid-blocking plate further comprises a rotating shaft and a fixed plate, wherein the fixed plate is fixedly connected to the bottom plate; the rotating shaft is fixedly connected to the inclined plate and is rotationally connected to the fixed plate, and the rotating shaft is rotationally connected to the fixed plate.
4. The slurry separation speed reduction diffusion plate according to claim 3, characterized in that: Connecting plates are fixed on both sides of the fixing plate, and the connecting plates are fixedly connected to the baffle plate and the bottom plate.
5. The slurry separation speed reduction diffusion plate according to claim 3, characterized in that: A hexagonal slot is provided at one end of the rotating shaft along the axial direction; a clamping block is connected to the hexagonal slot, and the clamping block is used to limit the rotation of the rotating shaft.
6. The slurry separation speed reduction diffusion plate according to claim 5, characterized in that: The card block includes a latch pin, a rotating pin and a card plate, the card plate is L-shaped, and one end face of the L-shaped card plate abuts against the fixed plate; the rotating pin and the latch pin are hexagonal columns, which are symmetrically fixed on both sides of the other end face of the L-shaped card plate, and the hexagonal columns cooperate with the hexagonal slots.
7. The pulp separation speed reduction diffusion plate according to claim 5, characterized in that: A mineral box is provided below the discharge port, the upper opening of the mineral box is connected to the discharge port, and the mineral box is fixed to the lower end of the bottom plate; a water tank is fixed to the side of the mineral box close to the liquid inlet, the water tank is located below the overflow port, and the width of the water tank is greater than the distance between the overflow ports on both sides; through holes are provided at the bottom of the water tank and the mineral box.