Efficient concentration reaction kettle
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Applications(China)
- Current Assignee / Owner
- Filing Date
- 2023-07-15
- Publication Date
- 2026-04-14
AI Technical Summary
Existing technologies cannot rapidly increase the heating rate of raw materials, resulting in low efficiency in concentration processing.
A high-efficiency concentration reactor was designed, which adopts a structure including corrugated plates, absorption pipes, heating racks and spiral blades. It achieves rapid and uniform heating and material dispersion through high-temperature steam heating and material dispersion, combined with a geared motor drive. Multiple feeding pipes and one-way valves are used to prevent material leakage, and a filter rack is used for solid-liquid separation and condensation.
It enables rapid and uniform heating and efficient concentration of raw materials, improves the concentration processing speed, reduces material waste, and ensures the continuity and efficiency of processing.
Smart Images

Figure CN121846702A_ABST
Abstract
Description
Technical Field
[0001] This invention relates to the field of concentration equipment, and more specifically to a high-efficiency concentration reactor. Background Technology
[0002] Thickening involves transferring the slurry, either through overflow or pumping, to a thickening device outside the reactor for solid-liquid separation. The clarified liquid is then discharged, and the concentrated slurry is returned to the reactor, thereby increasing the solid-liquid ratio. However, existing thickening technologies cannot accelerate the heating rate of the raw materials to quickly process them. Summary of the Invention
[0003] To overcome the shortcomings of existing technologies, this invention provides a high-efficiency concentration reactor that can accelerate the heating rate of raw materials and quickly concentrate them.
[0004] The technical solution adopted by this invention to solve its technical problem is:
[0005] A high-efficiency concentration reactor includes a vessel body with multiple feeding pipes fixedly connected to it, a corrugated plate rotatably connected to the lower end of the vessel body, an annular plate fixedly connected to the vessel body and the corrugated plate, an absorption pipe rotatably connected to the vessel body, a gathering frame fixedly connected to the absorption pipe, a dispersion pipe fixedly connected to the annular plate, and an air inlet pipe and a heating frame fixedly connected to the dispersion pipe.
[0006] Furthermore, a flat material rack that contacts the corrugated plate surface is rotatably connected to the air intake pipe.
[0007] Furthermore, a central wheel is fixedly connected to the absorption tube, and an eccentric wheel that drives the central wheel to rotate is rotatably connected to the vessel body.
[0008] Furthermore, two filter frames are fixedly attached to the inner wall of the vessel.
[0009] Furthermore, multiple spiral blades are fixedly attached to the retractable frame.
[0010] Furthermore, all of the plurality of spiral blades are in contact with the surfaces of the two filter frames.
[0011] Furthermore, the gathering frame is located in the middle of the two filter holders.
[0012] Furthermore, each of the multiple feeding pipes is fixedly connected to a one-way valve.
[0013] Furthermore, the corrugated plate is a rotating body with a wavy cross-section.
[0014] Furthermore, both filter holders are conical. Attached Figure Description
[0015] The present invention will now be described in further detail with reference to the accompanying drawings and specific implementation methods.
[0016] Figure 1 Structural diagram for loading and concentrating raw materials;
[0017] Figure 2 This is a structural diagram of the heating raw material;
[0018] Figure 3 This is a structural diagram of the absorption tube;
[0019] Figure 4 A structural diagram to drive the steam flow;
[0020] Figure 5 This is a structural diagram of the filter material;
[0021] Figure 6 A structural diagram showing the rotation of the absorption tube;
[0022] Figure 7 This is a structural diagram showing the location of the flat material rack;
[0023] Figure 8 A structural diagram to illustrate the movement of materials;
[0024] Figure 9 This is a cross-sectional view of the heated material.
[0025] Figure 10 This is a structural diagram of the reactor.
[0026] 11. Boiler body; 12. Feeding pipe; 13. Ring plate; 14. Filter frame; 21. Absorption pipe; 22. Middle wheel; 23. Gathering frame; 24. Offset wheel; 31. Air inlet pipe; 32. Dispersion pipe; 33. Heating frame; 41. Spiral blade; 51. Flat material rack; 52. Corrugated plate. Detailed Implementation
[0027] refer to Figure 1 , 2 Section 3 details the implementation process for material concentration:
[0028] A high-efficiency concentration reactor includes a reactor body 11 fixedly connected to multiple feeding pipes 12. Raw materials requiring concentration can be added to the reactor body 11 through the multiple feeding pipes 12. The dispersed arrangement of the multiple feeding pipes 12 ensures sufficient dispersion of the added raw materials, allowing for uniform dispersion before concentration and thus rapid concentration during subsequent processing. The upper ends of the multiple feeding pipes 12 are open, enabling material aggregation and facilitating material addition. The lower end of the reactor body 11 is rotatably connected... A corrugated plate 52 is connected to the vessel body 11. Materials added through multiple feeding pipes 12 automatically flow to the lower end under gravity, adding raw materials onto the corrugated plate 52. A ring plate 13 is fixedly connected to the vessel body 11, and the corrugated plate 52 is rotatably connected to the ring plate 13. The ring plate 13 seals the connection between the vessel body 11 and the corrugated plate 52, preventing material leakage. An absorption pipe 21 is rotatably connected to the vessel body 11, and a pump is fixedly connected to the absorption pipe 21. The pump draws out the material from the lower end of the absorption pipe 21 for material transport. A collection frame 23 is fixedly connected to the ring plate 13 to collect the concentrated material, which is then collected through the absorption pipe 21. A dispersion pipe 32 is fixedly connected to the ring plate 13, and an air inlet pipe 31 and a heating frame 33 are fixedly connected to the dispersion pipe 32. Both the air inlet pipe 31 and the dispersion pipe 32 are connected to an external heating furnace, which provides high-temperature steam to the air inlet pipe 31. The high-temperature steam flows into the heating frame 33 through the dispersion pipe 32. The heating frame 33 consists of multiple annular pipes, which can uniformly heat the material on the corrugated plate 52. The high-temperature steam after heating the material flows from the heating frame 33 to the dispersion pipe 32 and then back to the external heating furnace, realizing the circulation of high-temperature steam. The corrugated plate 52 has multiple rotating protrusions and pits, which can increase the contact area with the material, thereby fully dispersing the material. The material is then distilled by heating, achieving full concentration of the material. The material is also removed by heating, thus achieving full concentration of the material.
[0029] In conjunction with the above embodiments, the following functions can also be achieved;
[0030] refer to Figure 7 , 8 Section 9 details the implementation process for promoting material flow on the corrugated plate to achieve sufficient concentration:
[0031] A flat material rack 51, which contacts the corrugated plate 52, is rotatably connected to the air inlet pipe 31. The flat material rack 51 is fixedly connected to the output shaft of the reduction motor I, which is also fixedly connected to the air inlet pipe 31. When the reduction motor I is started, it drives the flat material rack 51 to rotate. The flat material rack 51 fully pushes the material on the corrugated plate 52 to flow. The flat material rack 51 and the corrugated plate 52 are fully in contact, so that the material can be fully pushed to flow under rotation, thereby achieving rapid material flow, and thus achieving sufficient and uniform heating and rapid concentration of the material.
[0032] In conjunction with the above embodiments, the following functions can also be achieved;
[0033] refer to Figure 6 The following details the implementation process of driving the absorption tube to rotate and fully absorb the material on the collection frame:
[0034] A central wheel 22 is fixedly connected to the absorption pipe 21, and a deflector wheel 24 that drives the central wheel 22 to rotate is rotatably connected to the vessel body 11. The deflector wheel 24 is fixedly connected to the output shaft of the reduction motor II, and the reduction motor II is fixedly connected to the vessel body 11. When the reduction motor II is started, the reduction motor II drives the deflector wheel 24 to rotate, and the deflector wheel 24 engages with and drives the central wheel 22 to rotate. The central wheel 22 drives the absorption pipe 21 to rotate, and the absorption pipe 21 drives the collecting frame 23 to rotate, so that the material on the collecting frame 23 can be fully absorbed through the rotation of the absorption pipe 21.
[0035] In conjunction with the above embodiments, the following functions can also be achieved;
[0036] refer to Figure 5 The following details the implementation process for collecting the condensed material:
[0037] Two filter frames 14 are fixedly connected to the inner wall of the vessel body 11. Each filter frame 14 has multiple filter holes, which can filter the heated and evaporated material and achieve the filtration of concentrated material. The two filter frames 14 can also be condensed by gradually cooling down. The condensed material at the top is collected on the collection frame 23, and then the condensed material is collected.
[0038] In conjunction with the above embodiments, the following functions can also be achieved;
[0039] refer to Figure 4 and 10 The implementation process for driving material flow is described in detail:
[0040] Multiple spiral blades 41 are fixedly connected to the collecting frame 23. When the absorption tube 21 rotates, it drives the collecting frame 23 to rotate, which in turn drives the multiple spiral blades 41 to rotate, thereby causing the evaporated gas to flow rapidly. This allows the steam to be fully dispersed and pass through the filter holes on the two filter frames 14 for filtration. The rotation of the multiple spiral blades 41 can thoroughly clean the two filter frames 14, ensuring that the two filter frames 14 can continuously filter the steam.
[0041] In conjunction with the above embodiments, the following functions can also be achieved;
[0042] refer to Figure 10 The detailed procedure for cleaning the two filter holders to ensure continuous steam filtration is as follows:
[0043] The multiple spiral blades 41 are in contact with the surfaces of the two filter frames 14, thereby cleaning the contact surfaces of the two filter frames 14 through the rotation of the multiple spiral blades 41, ensuring the unobstructed flow of the multiple filter holes, and thus ensuring the filtration effect of the two filter frames 14.
[0044] In conjunction with the above embodiments, the following functions can also be achieved;
[0045] refer to Figure 10 The implementation process for collecting the condensed material on the upper filter rack is described in detail:
[0046] The gathering frame 23 is located in the middle of the two filter frames 14, so that when cooling, the distance between the upper filter frame 14 and the lower heating frame 33 is larger, so that the upper filter frame 14 condenses earlier, and the condensed material falls into the lower gathering frame 23, so that the material on the gathering frame 23 can be transported through the absorption pipe 21.
[0047] In conjunction with the above embodiments, the following functions can also be achieved;
[0048] refer to Figure 1 and 10 The detailed implementation process for preventing heated material from flowing out of multiple feeding pipes is as follows:
[0049] Each of the multiple feeding pipes 12 is fixedly connected with a one-way valve, so that the added material is added through the multiple feeding pipes 12 by the multiple one-way valves, which can prevent the heated material from flowing out of the multiple feeding pipes 12 and prevent material waste.
[0050] In conjunction with the above embodiments, the following functions can also be achieved;
[0051] refer to Figure 8 and 9 The following details the implementation process of increasing the heating area of the raw materials to fully disperse the materials and enhance concentration:
[0052] The corrugated plate 52 is a rotating body with a wavy cross section. Both the upper and lower ends of the corrugated plate 52 are in the shape of annular protrusions and annular grooves, which can increase the heating area of the material, thereby realizing the dispersed heating of the material and quickly and efficiently concentrating the material.
[0053] In conjunction with the above embodiments, the following functions can also be achieved;
[0054] refer to Figure 5 and 10 The following details the process of filtering and condensing the materials:
[0055] Both filter frames 14 are conical, with their smaller ends close to each other. The lower filter frame 14 mainly functions to gather and filter steam, while the upper filter frame 14 mainly functions to condense and filter, thus enabling efficient and rapid concentration of materials.
Claims
1. A high-efficiency concentration reactor, characterized in that: The vessel includes a vessel body (11) with multiple feeding pipes (12) fixedly connected to it. A corrugated plate (52) is rotatably connected to the lower end of the vessel body (11). A ring plate (13) is fixedly connected to the vessel body (11). The corrugated plate (52) is rotatably connected to the ring plate (13). An absorption pipe (21) is rotatably connected to the vessel body (11). A gathering frame (23) is fixedly connected to the absorption pipe (21). A dispersion pipe (32) is fixedly connected to the ring plate (13). An air inlet pipe (31) and a heating frame (33) are fixedly connected to the dispersion pipe (32).
2. The high-efficiency concentration reactor according to claim 1, characterized in that: A flat material rack (51) that contacts the surface of the corrugated plate (52) is rotatably connected to the air intake pipe (31).
3. The high-efficiency concentration reactor according to claim 1, characterized in that: A central wheel (22) is fixedly connected to the absorption tube (21), and a deflector wheel (24) that drives the central wheel (22) to rotate is rotatably connected to the vessel body (11).
4. The high-efficiency concentration reactor according to claim 1, characterized in that: Two filter frames (14) are fixed to the inner wall of the vessel body (11).
5. The high-efficiency concentration reactor according to claim 1, characterized in that: Multiple spiral blades (41) are fixed to the retractable frame (23).
6. The high-efficiency concentration reactor according to claim 5, characterized in that: The plurality of spiral blades (41) are in contact with the surfaces of the two filter frames (14).
7. The high-efficiency concentration reactor according to claim 5, characterized in that: The gathering frame (23) is located in the middle of the two filter frames (14).
8. The high-efficiency concentration reactor according to claim 1, characterized in that: Each of the multiple feeding pipes (12) is fixedly connected with a one-way valve.
9. The high-efficiency concentration reactor according to claim 1, characterized in that: The corrugated plate (52) is a rotating body with a wavy cross section.
10. The high-efficiency concentration reactor according to claim 4, characterized in that: Both filter holders (14) are conical.