Slurry preparation circulating system for continuous spinning slurry

By designing the continuous pic -textured pulp with a pulp circulation system, the material in the slurry and slurry system is uniform, insufficient impurities filtration, and the problem of uniformity of the material static, realize the uniform mixing and efficient filtration of the slurry. Improve product quality.

CN222401209UActive Publication Date: 2025-01-28YIBIN HIEST FIBER
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Patent Information

Application Number
CN202323601982.3
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2023-12-28
Publication Date
2025-01-28
Estimated Expiration
2033-12-28

AI Technical Summary

Technical Problem

In the existing continuous spinning production technology, the slurry slurry system has problems such as uneven addition of materials, insufficient filtration of impurities and long-term standing of materials, resulting in poor uniformity.

Method used

Design a continuous pic -woven pulp with a pulp circulation system, adding salted water and steam pipes to the steam through the water inlet pipe to initially increased the steam, and then add the material through the funnel of the funnel -shaped material. Filter to ensure that the material is always flowing.

Benefits of technology

The uniform addition of powder materials, the sufficient filtering of the slurry impurities, and the uniform mixing of the material are improved to improve the quality of the product.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model discloses a continuous spinning slurry preparation circulating system, which belongs to the technical field of continuous spinning production and comprises a preparation tank and a transfer storage tank, the preparation tank is provided with a feed port, a first stirring mechanism, a water inlet pipe and a steam pipe, and the lower end of the preparation tank is connected with a first return pipe and a first feed pipe through a first discharge pipe. A first circulating pump and a first filter are arranged on the first discharging pipe, the first return pipe is connected with the batching tank, the first feeding pipe is connected with the transfer storage tank, and a second stirring mechanism is arranged on the transfer storage tank; the transfer storage tank is connected with a second return pipe and a second feed pipe through a second discharge pipe, a second circulating pump and a second filter are arranged on the second discharge pipe, the second return pipe is connected with the transfer storage tank, and the second feed pipe is connected with the spinning machine. According to the utility model, powdery materials can be added more uniformly; the slurry impurities are filtered more sufficiently; the slurry is always in a flowing state through the second backflow pipe, and mixing is more uniform.
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Description

Technical Field

[0001] The utility model belongs to the technical field of continuous spinning production, and in particular relates to a continuous spinning slurry mixing circulation system. Background Art

[0002] At present, our company has a sizing process in the continuous spinning production process. The raw pulp used for sizing is mainly a mixture of pulp and oil. If the above two organic substances are not mixed evenly or the impurities are not filtered cleanly, it will cause uneven sizing rate of the silk strips and affect product quality.

[0003] like Figure 3 As shown, the current slurry preparation system: first add a certain volume of desalted water into the batching tank, start stirring, and heat up to 35-40°C; then pour a certain amount of powdered material into the batching tank at one time, stir and heat to 70-85°C, and start the circulation pump for internal circulation. When the temperature drops to 50-60°C, add oil and stir evenly; when the temperature drops to 25-35°C, add bactericide, and then transfer directly to the storage tank for use in the machine.

[0004] The current problems are as follows: 1. The feed port is a cylindrical barrel structure. When the powder slurry is poured in, it cannot be added evenly, which usually causes the material to be sometimes large and sometimes small. After the material is dissolved in water, it cannot be evenly dispersed. 2. There is no filtration system, and it is impossible to filter out impurities in the mixed material and newly generated solid impurities. 3. The material is stored in the pipeline for a long time and cannot be circulated, so the material in the pipeline is stored for a long time and the uniformity becomes poor. Utility Model Content

[0005] The purpose of the utility model is to solve the problems of the prior art and provide a continuous spinning slurry mixing circulation system. When mixing, desalted water is first added through the water inlet pipe, the first stirring mechanism is started, and steam is added through the steam pipe for preliminary heating. Then, materials are added through the feed port, and the temperature is gradually increased by stirring for a second time. The first circulation pump is started, and the slurry is fully mixed. At the same time, the slurry passes through the first filter to filter the undissolved particles, and the temperature is initially reduced. Oil is added, fully mixed, and the temperature is reduced for the second time. A bactericide is added, and the slurry is mixed; the slurry is switched into the transfer discharge tank, and the second stirring mechanism is started at the same time to ensure that the slurry is always in a uniformly mixed state, and the slurry is prevented from settling and stratifying, which affects the uniformity of the components; the second circulation pump or the third circulation pump is started, and the slurry is sent to the second filter for secondary filtration, and then the slurry is sent to the spinning machine for use on the one hand, and the slurry is sent back to the transfer storage tank through the second reflux pipe on the other hand, and is always in a flowing state. The utility model makes the powdered material more uniform; the slurry impurities are filtered more fully; the slurry is always in a flowing state through the second reflux pipe, and the mixing is more uniform.

[0006] The utility model is realized by the following technical solutions:

[0007] A continuous spinning slurry mixing and circulation system comprises a mixing tank and a transfer storage tank, wherein the mixing tank is provided with a feed port, a first stirring mechanism, a water inlet pipe and a steam pipe, the lower end of the mixing tank is connected to a first return pipe and a first feed pipe through a first discharge pipe, a first circulation pump and a first filter are provided on the first discharge pipe, the first return pipe is connected to the mixing tank, the first feed pipe is connected to the transfer storage tank, and a second stirring mechanism is provided on the transfer storage tank; the transfer storage tank is connected to a second return pipe and a second feed pipe through a second discharge pipe, a second circulation pump and a second filter are provided on the second discharge pipe, the second return pipe is connected to the transfer storage tank, and the second feed pipe is connected to a spinning machine.

[0008] Preferably, the feed inlet is funnel-shaped.

[0009] Preferably, a partition plate is provided at the lower end of the feed inlet.

[0010] Preferably, the first stirring mechanism includes a first stirring motor and a first stirring shaft, the first stirring motor is arranged above the batching tank, the output end of the first stirring motor is connected to the first stirring shaft, the first stirring shaft extends into the batching tank, and a first stirring paddle is arranged on the first stirring shaft.

[0011] Preferably, the second stirring mechanism includes a second stirring motor and a second stirring shaft, the second stirring motor is arranged above the transfer storage tank, the output end of the second stirring motor is connected to the second stirring shaft, the second stirring shaft extends into the transfer storage tank, and a second stirring paddle is arranged on the second stirring shaft.

[0012] Preferably, valves are provided on the first reflux pipe, the first feed pipe and the second feed pipe.

[0013] Preferably, valves are provided before and after the first circulating pump and the second circulating pump.

[0014] Preferably, the second discharge pipe is also connected to the first discharge branch pipe, and the first discharge branch pipe is also provided with a third circulation pump.

[0015] Preferably, the second feed pipe is connected to the second discharge branch pipe and the third discharge branch pipe, and the second discharge branch pipe and the third discharge branch pipe are both connected to the spinning machine.

[0016] Preferably, the first filter adopts a plate and frame filter; the second filter adopts a filter element.

[0017] Compared with the prior art, the utility model has the following advantages and beneficial effects:

[0018] 1. The utility model provides a continuous spinning slurry mixing circulation system. When mixing, desalted water is first added through the water inlet pipe, the first stirring mechanism is started, and steam is added through the steam pipe to heat up (until 35-40°C), and then the material is added through the feed port, and the temperature is gradually stirred and raised to 70-85°C, and the first circulation pump is started. The slurry is fully mixed, and the slurry passes through the first filter to preliminarily filter the undissolved particles. When the temperature drops to 50-60°C, an oil agent is added and fully mixed. When the temperature is further dropped to 25-35°C, a bactericide is added, and the slurry mixing is completed at this time; the slurry is switched into the transfer discharge tank, and the second stirring mechanism is started at the same time to ensure that the slurry is always in a uniformly mixed state to prevent the slurry from settling and stratifying, which affects the uniformity of the components; the second circulation pump or the third circulation pump is started to send the slurry into the second filter for secondary filtration, and then it is sent to the spinning machine for use on the one hand, and the slurry is sent back to the transfer storage tank through the second reflux pipe on the other hand, and it is always in a flowing state. The utility model enables powdered materials to be added more evenly, slurry impurities to be filtered more fully, and slurry is always in a flowing state through the second reflux pipe, so the mixing is more even.

[0019] 2. The utility model provides a continuous spinning slurry mixing circulation system, with a funnel-shaped feed inlet and a dividing plate arranged at the lower end of the feed inlet to ensure that the material can be evenly added into the mixing tank and the material does not stick together into lumps.

[0020] 3. The utility model provides a continuous spinning pulp mixing circulation system, in which the plate and frame filter performs primary filtration and the filter element performs secondary filtration to ensure the impurity filtering effect.

[0021] 4. The utility model provides a continuous spinning slurry mixing circulation system, in which the third circulation pump and the second circulation pump are used as a backup, ensuring that the slurry is always in a flowing state through the second reflux pipe and is mixed more evenly. BRIEF DESCRIPTION OF THE DRAWINGS

[0022] Figure 1 It is a schematic diagram of the structure of the utility model;

[0023] Figure 2 for Figure 1 The enlarged view of point A in the middle;

[0024] Figure 3 It is a structural schematic diagram of the current slurry preparation system;

[0025] Among them: 1. batching tank; 2. transfer storage tank; 3. feed port; 4. first stirring mechanism; 41. first stirring motor; 42. first stirring shaft; 43. first stirring paddle; 5. water inlet pipe; 6. steam pipe; 7. first discharge pipe; 8. first reflux pipe; 9. first feed pipe; 10. first circulation pump; 11. first filter; 12. second discharge pipe; 13. second reflux pipe; 14. second feed pipe; 15. second circulation pump; 16. second filter; 17. spinning machine; 18. partition plate; 19. second stirring mechanism; 191. second stirring motor; 192. second stirring shaft; 193. second stirring paddle; 20. valve; 21. first discharge branch pipe; 22. third circulation pump; 23. second discharge branch pipe; 24. third discharge branch pipe. DETAILED DESCRIPTION

[0026] The present invention is further described in detail below in conjunction with the embodiments, but the implementation manner of the present invention is not limited thereto.

[0027] Example 1

[0028] like Figure 1 As shown, the present embodiment provides a continuous spinning slurry mixing circulation system, including a mixing tank 1 and a transit storage tank 2, the mixing tank 1 is provided with a feed port 3, a first stirring mechanism 4, a water inlet pipe 5 and a steam pipe 6, the lower end of the mixing tank 1 is connected to a first return pipe 8 and a first feed pipe 9 through a first discharge pipe 7, a first circulation pump 10 and a first filter 11 are provided on the first discharge pipe 7, the first return pipe 8 is connected to the mixing tank 1, the first feed pipe 9 is connected to the transit storage tank 2, and a second stirring mechanism 19 is provided on the transit storage tank 2; the transit storage tank 2 is connected to a second return pipe 13 and a second feed pipe 14 through a second discharge pipe 12, a second circulation pump 15 and a second filter 16 are provided on the second discharge pipe 12, the second return pipe 13 is connected to the transit storage tank 2, and the second feed pipe 14 is connected to a spinning machine 17.

[0029] When mixing, first add desalted water through the water inlet pipe 5, start the first stirring mechanism 4, and add steam through the steam pipe 6 to heat it up (until 35-40°C), then add materials through the feed port 3, gradually stir and heat it to 70-85°C, start the first circulation pump 10, mix the slurry fully, and at the same time, filter the undissolved particles through the first filter 11, and when the temperature drops to 50-60°C, add oil agent, mix it fully, and when it further drops to 25-35°C, add fungicide, and the slurry mixing is completed at this time; switch the slurry into the transfer discharge tank, and start the second stirring mechanism 19 at the same time to ensure that the slurry is always in a uniformly mixed state to prevent the slurry from settling and stratifying, which affects the uniformity of the components; start the second circulation pump 15 or the third circulation pump 22, send the slurry into the second filter 16 for secondary filtration, and then send it to the spinning machine 17 for use on the one hand, and send the slurry back to the transfer storage tank 2 through the second reflux pipe 13 on the other hand, so that it is always in a flowing state. The utility model enables powdered materials to be added more evenly, slurry impurities to be filtered more fully, and slurry is always in a flowing state through the second reflux pipe 13, so mixing is more even.

[0030] Example 2

[0031] The difference between this embodiment and embodiment 1 is that the feed inlet 3 is funnel-shaped.

[0032] like Figure 2 As shown, a partition plate 18 is provided at the lower end of the feed port 3. The feed port 3 is funnel-shaped, and a partition plate is provided at the lower end of the feed port 3 to ensure that the material can be evenly added into the batching tank 1 and the material does not stick together into a lump.

[0033] The first stirring mechanism 4 includes a first stirring motor 41 and a first stirring shaft 42 . The first stirring motor 41 is arranged above the batching tank 1 . The output end of the first stirring motor 41 is connected to the first stirring shaft 42 . The first stirring shaft 42 extends into the batching tank 1 . A first stirring paddle 43 is arranged on the first stirring shaft 42 .

[0034] Among them, the second stirring mechanism 19 includes a second stirring motor 191 and a second stirring shaft 192, the second stirring motor 191 is arranged above the transfer storage tank 2, the output end of the second stirring motor 191 is connected to the second stirring shaft 192, the second stirring shaft 192 extends into the transfer storage tank 2, and the second stirring shaft 192 is provided with a second stirring paddle 193.

[0035] The first reflux pipe 8 , the first feed pipe 9 and the second feed pipe 14 are all provided with valves 20 .

[0036] Wherein, valves 20 are arranged before and after the first circulation pump 10 and the second circulation pump 15 .

[0037] The second discharge pipe 12 is also connected to the first discharge branch pipe 21, and the first discharge branch pipe 21 is also provided with a third circulation pump 22. The third circulation pump 22 and the second circulation pump 15 are used in a standby manner to ensure that the slurry is always in a flowing state through the second reflux pipe 13 and mixed more evenly.

[0038] The second feed pipe 14 is connected to the second discharge branch pipe 23 and the third discharge branch pipe 24 , and the second discharge branch pipe 23 and the third discharge branch pipe 24 are both connected to the spinning machine 17 .

[0039] The first filter 11 adopts a plate-and-frame filter, and the second filter 16 adopts a filter element. The plate-and-frame filter performs primary filtration, and the filter element performs secondary filtration to ensure the impurity filtering effect.

[0040] The above description is only a preferred embodiment of the present invention and does not limit the present invention in any form. Any simple modification or equivalent changes made to the above embodiments based on the technical essence of the present invention shall fall within the protection scope of the present invention.

Claims

1. A continuous spinning pulp mixing circulation system, comprising a mixing tank (1) and a transfer storage tank (2), characterized in that: The batching tank (1) is provided with a feed port (3), a first stirring mechanism (4), a water inlet pipe (5) and a steam pipe (6); the lower end of the batching tank (1) is connected to a first return pipe (8) and a first feed pipe (9) through a first discharge pipe (7); a first circulation pump (10) and a first filter (11) are provided on the first discharge pipe (7); the first return pipe (8) is connected to the batching tank (1); the first feed pipe (9) is connected to a transfer storage tank (2); a second stirring mechanism (19) is provided on the transfer storage tank (2); the transfer storage tank (2) is connected to a second return pipe (13) and a second feed pipe (14) through a second discharge pipe (12); a second circulation pump (15) and a second filter (16) are provided on the second discharge pipe (12); the second return pipe (13) is connected to the transfer storage tank (2); and the second feed pipe (14) is connected to a spinning machine (17).

2. A continuous spinning slurry mixing circulation system according to claim 1, characterized in that: The feed inlet (3) is funnel-shaped.

3. A continuous spinning slurry mixing circulation system according to claim 2, characterized in that: A partition plate (18) is provided at the lower end of the feed inlet (3).

4. A continuous spinning slurry mixing circulation system according to claim 3, characterized in that: The first stirring mechanism (4) comprises a first stirring motor (41) and a first stirring shaft (42); the first stirring motor (41) is arranged above the batching tank (1); the output end of the first stirring motor (41) is connected to the first stirring shaft (42); the first stirring shaft (42) extends into the batching tank (1); and a first stirring paddle (43) is arranged on the first stirring shaft (42).

5. The continuous spinning slurry mixing circulation system according to claim 1, characterized in that: The second stirring mechanism (19) comprises a second stirring motor (191) and a second stirring shaft (192); the second stirring motor (191) is arranged above the transfer storage tank (2); the output end of the second stirring motor (191) is connected to the second stirring shaft (192); the second stirring shaft (192) extends into the transfer storage tank (2); and a second stirring paddle (193) is arranged on the second stirring shaft (192).

6. A continuous spinning slurry mixing circulation system according to claim 5, characterized in that: The first reflux pipe (8), the first feed pipe (9) and the second feed pipe (14) are all provided with valves (20).

7. A continuous spinning slurry mixing circulation system according to claim 6, characterized in that: Valves (20) are provided before and after the first circulation pump (10) and the second circulation pump (15).

8. A continuous spinning slurry mixing circulation system according to claim 7, characterized in that: The second discharge pipe (12) is also connected to the first discharge branch pipe (21), and the first discharge branch pipe (21) is also provided with a third circulation pump (22).

9. A continuous spinning slurry mixing circulation system according to claim 8, characterized in that: The second feed pipe (14) is connected to the second discharge branch pipe (23) and the third discharge branch pipe (24), and the second discharge branch pipe (23) and the third discharge branch pipe (24) are both connected to the spinning machine (17).

10. A continuous spinning slurry mixing circulation system according to claim 9, characterized in that: The first filter (11) adopts a plate and frame filter; the second filter (16) adopts a filter element.