High-water-absorption degradable wood cellulose sponge preparation device and use method thereof

Abstract

The invention belongs to the technical field of wood cellulose sponge, and particularly relates to a high-water-absorption degradable wood cellulose sponge preparation device and a using method thereof.The high-water-absorption degradable wood cellulose sponge preparation device comprises a processing body and a liquid conveying assembly arranged on the processing body and further comprises a physical cooperative processing mechanism and an auxiliary cooperative processing mechanism; the physical cooperative processing mechanism is arranged on the processing main body, and the auxiliary cooperative processing mechanism is arranged on the processing main body; the physical cooperative processing mechanism comprises a stirring assembly, a bubble disturbance assembly and a pulse disturbance assembly, the stirring assembly is arranged on the physical cooperative processing mechanism, the bubble disturbance assembly is arranged on the physical cooperative processing mechanism, and the pulse disturbance assembly is arranged on the processing main body; nitrogen passes through the bubble stone to generate continuous microbubbles, fiber clusters are scattered in the rising process of the bubbles, meanwhile, solid particles are promoted to be slightly turned over, adhesion of dry fibers in the initial stage when the dry fibers meet alkali can be remarkably reduced, and the purposes of dispersing the fibers and increasing the effective reaction surface area are achieved.

Description

Technical Field

[0001] This invention belongs to the field of wood cellulose sponge technology, specifically referring to the apparatus for preparing highly absorbent and biodegradable wood cellulose sponges and its usage method. Background Technology

[0002] Wood cellulose sponge is a functional material with a three-dimensional porous network structure, made from wood cellulose through a special process. It not only possesses high water absorption, enabling it to quickly absorb and retain large amounts of moisture, but also exhibits excellent biodegradability, being decomposed by microorganisms in the natural environment. This makes it environmentally friendly and gives it broad application prospects in many fields, including hygiene products, medical dressings, and oil stain absorption.

[0003] However, existing equipment for preparing highly absorbent biodegradable wood cellulose sponges suffers from numerous problems. Due to its inherent properties, the cellulose raw material is highly prone to clumping when it enters the reaction system. This clumping not only hinders the uniform wetting of the alkali solution, preventing some raw materials from fully reacting with the solution and affecting the uniformity and thoroughness of the reaction, thus reducing the performance and quality of the wood cellulose sponge, but also makes it difficult for existing equipment to prevent clumping in real time during the reaction process. This results in persistent clumping, negatively impacting both the preparation efficiency of the wood cellulose sponge and the quality stability of the final product, thus limiting the large-scale industrial production and application of highly absorbent biodegradable wood cellulose sponges. Summary of the Invention

[0004] In response to the above situation, and in order to reduce pipeline structure and energy consumption and equipment costs, the present invention provides a device for preparing highly absorbent biodegradable wood cellulose sponges.

[0005] The technical solution adopted by this invention is as follows: This invention provides a device for preparing highly absorbent biodegradable wood cellulose sponges, including a processing body and an infusion assembly disposed on the processing body, and further including a physical co-processing mechanism and an auxiliary co-processing mechanism. The physical co-processing mechanism is disposed on the processing body, and the auxiliary co-processing mechanism is disposed on the processing body. The physical co-processing mechanism includes a stirring assembly, a bubble disturbance assembly, and a pulse disturbance assembly. The stirring assembly is disposed on the physical co-processing mechanism, the bubble disturbance assembly is disposed on the physical co-processing mechanism, and the pulse disturbance assembly is disposed on the processing body.

[0006] Furthermore, the processing body includes a processing table, a support frame is fixedly installed at the top of the processing table, a cylinder seat of a lifting cylinder is fixedly installed at the top of the inner side of the support frame, a lifting plate is fixedly connected to the output end of the lifting cylinder, an equipment cavity is opened inside the processing table, one end of a first connecting rod is fixedly connected to the inner side wall of the equipment cavity, the other end of the first connecting rod is fixedly connected to the outer side wall of the oil cavity, and a heating resistor is installed on the inner side wall of the oil cavity.

[0007] Furthermore, the stirring assembly includes a connecting frame, which is installed at the lower end of the lifting plate. A motor is fixedly installed at the lower end of the connecting frame, and a first bevel gear is fixedly installed at the output end of the motor. One end of a fixed frame is fixedly connected to the lower end of the lifting plate, and a rotary joint is fixedly connected to the other end of the fixed frame. The rotary joint's rotating interface is connected through to one end of a second output pipe, and a second bevel gear is fixedly sleeved on the outer side wall of the second output pipe. The first bevel gear and the second bevel gear mesh and rotate together.

[0008] Furthermore, the bubble agitation component includes a nitrogen storage tank, which is placed at the top of the lifting plate. The output end of the nitrogen storage tank is connected to one end of a first output pipe, and the other end of the first output pipe is connected to the fixed interface of a rotary joint. A first electronic valve is installed on the first output pipe, and multiple L-shaped stirring tubes are connected to the outer wall of the second output pipe. The lower end of the L-shaped stirring tubes is fixedly installed with the input end of the bubble stone.

[0009] Furthermore, the pulse disturbance component includes an L-shaped connecting rod, which is fixedly connected to the lower end of the outer wall of the second output tube, and an ultrasonic generator is fixedly installed at the lower end of the L-shaped connecting rod.

[0010] Furthermore, the auxiliary co-processing mechanism includes a vacuum filtration component and a foam elimination component, wherein the vacuum filtration component is disposed on the auxiliary co-processing mechanism and the foam elimination component is disposed on the auxiliary co-processing mechanism.

[0011] Furthermore, the vacuum filtration assembly includes a reaction beaker, which is fixedly connected to the bottom of the oil chamber. A hollow tank is fixedly connected to the bottom of the reaction beaker. Multiple filter holes are opened on the side wall of the hollow tank. Filter cotton is fitted on the hollow tank. One end of a connecting pipe is connected to the lower end of the hollow tank. A vacuum tank is placed at the bottom of the oil chamber. An air extraction port is provided on one side of the top of the vacuum tank. The other end of the connecting pipe is connected to the top of the vacuum tank. A vacuum pump is provided at the bottom of the processing table. The pumping end of the vacuum pump is connected to one end of an air extraction pipe, and the other end of the air extraction pipe is connected to the air extraction port.

[0012] Furthermore, the foam elimination component includes a defoamer storage tank, which is installed on the lower side of the lifting plate. The upper side wall of the defoamer storage tank is provided with a feeding port. The lower end of the feeding port is connected to one end of an infusion tube, and the other end of the infusion tube is connected to a mounting cover. An ultrasonic atomizing plate is installed inside the mounting cover, and a second electronic valve is installed on the infusion tube.

[0013] Furthermore, the infusion assembly includes a deionized water storage tank, which is placed on one side of the top of the processing table. The lower end of the outer wall of the deionized water storage tank is connected to the inlet of a first water pump. The output end of the first water pump is connected to one end of a third output pipe. The other end of the third output pipe is located above the reaction beaker. A drug storage tank is placed inside one end of the processing table. A second water pump is installed at the top of the drug storage tank. The inlet of the drug storage tank is located at the bottom of the inside of the drug storage tank. The output end of the second water pump is connected to one end of a fourth output pipe. The other end of the fourth output pipe is located above the reaction beaker. The oil chamber is filled with oil.

[0014] This solution also discloses the method of using the apparatus for preparing highly absorbent and biodegradable wood cellulose sponges, which mainly includes the following steps:

[0015] Step 1: Place the dried cellulose raw material into the reaction beaker (32), put sodium hydroxide solution into the reagent storage tank (49), start the second water pump (50), and transport the sodium hydroxide solution in the reagent storage tank (49) to the reaction beaker (32) through the fourth output pipe (51). At the same time, the output end of the lifting cylinder (7) moves downward, driving the lifting plate (8) to move downward. The lifting plate (8) moves downward, driving the second output pipe (25) to move downward. The second output pipe (25) moves downward, driving the L-shaped stirring tube (26) to move downward, and moving the L-shaped stirring tube (26) into the reaction beaker (32).

[0016] Step 2: Start the motor (16). The output end of the motor (16) rotates, which drives the first bevel gear (17) to rotate. The first bevel gear (17) rotates, which drives the second bevel gear (18) to rotate. The second bevel gear (18) rotates, which drives the second output tube (25) to rotate. The second output tube (25) rotates, which drives the L-shaped stirring tube (26) to rotate. While adding sodium hydroxide solution, stir to fully wet the cellulose raw material and ensure that the cellulose raw material is completely submerged. Then start the heating resistor (12) to heat the oil in the oil chamber (11), thereby indirectly heating the reaction beaker (32).

[0017] Step 3: While stirring, open the first electronic valve (24), start the ultrasonic atomizing plate (40) and ultrasonic generator (29). The nitrogen in the nitrogen storage tank (22) enters the L-shaped stirring tube (26) through the first output pipe (23), and finally sprays out in the form of micro bubbles through the bubble stone (27). The continuous micro bubbles can break up the particle aggregation and form a slight tumbling. At the same time, the ultrasonic cavitation generated by the ultrasonic generator (29) can break up the agglomerates locally and promote the rapid penetration of the alkaline solution to prevent cellulose from agglomerating. After the reaction structure is formed, close the ultrasonic generator (29) and the first electronic valve (24). The L-shaped stirring tube (26) continues to stir. Open the second electronic valve (44) and the ultrasonic atomizing plate (40). The defoamer in the defoamer storage tank (41) flows to the ultrasonic atomizing plate (40) through the infusion pipe (43). After being atomized by the ultrasonic atomizing plate (40), it falls into the reaction beaker (32) to eliminate the foam generated when lignin and hemicellulose dissolve under alkaline conditions.

[0018] Step 4: After cooling to room temperature, open the third electronic valve (53), start the vacuum pump (34), and use the filter cotton (37) to filter the liquid in the reaction beaker (32) into the vacuum tank (33) through the connecting pipe (35). Then start the first water pump (47) to pump the deionized water in the deionized water storage tank (46) into the reaction beaker (32) and use the deionized water to wash the solid in the reaction beaker (32). Then open the third electronic valve (53) and the vacuum pump (34) again to pump the liquid into the vacuum tank (33) and wash it repeatedly. The washed cellulose raw material is then filtered and dehydrated into a paste by the vacuum pump (34) and then taken out, dried and stored.

[0019] The beneficial effects achieved by the present invention using the above structure are as follows: The present invention provides a device for preparing highly absorbent and biodegradable wood cellulose sponges, achieving the following beneficial effects:

[0020] (1) The physical co-processing mechanism allows the alkali solution to be added continuously during the stirring process, preventing local high alkalinity from causing excessive swelling or clumping of cellulose, thereby improving the uniformity of alkali soaking and the stability of the reaction.

[0021] (2) The physical co-processing mechanism is set up so that the L-shaped stirring tube can rotate after being vertically inserted into the reaction beaker. The stirring trajectory covers the entire beaker, breaking up the piled-up dry fibers, so that the raw materials can be quickly and completely immersed in the alkaline solution, achieving deep disturbance and no dead corner mixing, and improving the pretreatment efficiency.

[0022] (3) Nitrogen gas generates continuous microbubbles through the bubble stone. As the bubbles rise, they break up the fiber clusters and promote slight agitation of solid particles. This can significantly reduce the adhesion of dry fibers when they first encounter alkali, thereby achieving fiber dispersion and increasing the effective surface area of ​​the reaction.

[0023] (4) The cavitation effect generated by the ultrasonic generator can locally peel off the fiber surface, promote the entry of alkali into the pores, destroy the slight agglomeration structure, and increase the removal rate of hemicellulose / lignin, making the reaction shorter and more thorough, thereby improving the removal efficiency and product purity.

[0024] (5) The defoamer forms a micro-mist through an ultrasonic atomizing plate and acts directly on the foam layer. It can quickly defoam without significantly changing the chemical composition of the system. At the same time, the dosage is much lower than that of the liquid mixing method, which greatly reduces the residue of defoamer; thus achieving precise, fast and low-interference foam control.

[0025] (6) Oil cavity heating avoids direct contact between the electric heating element and the reaction beaker, resulting in gentler heat transfer and easier maintenance of constant temperature, thus keeping the system stable and preventing local "hot spots" from degrading cellulose, thereby improving the molecular weight and mechanical property stability of the product.

[0026] (7) After the reaction is completed, the filtration and washing are carried out directly in the same reaction beaker. There is no need to pour the slurry into other containers for separation, which can reduce material loss, reduce the risk of pollution, and realize automatic filtration and circulation washing, so as to achieve continuous and compact overall process and lower labor cost. Attached Figure Description

[0027] Figure 1 This is a front view of the apparatus for preparing highly absorbent and biodegradable wood cellulose sponges proposed in this invention;

[0028] Figure 2 This is a schematic diagram of the structure of the highly absorbent and biodegradable wood cellulose sponge preparation device proposed in this invention. Figure 1 ;

[0029] Figure 3 This is a schematic diagram of the structure of the highly absorbent and biodegradable wood cellulose sponge preparation device proposed in this invention. Figure 2 ;

[0030] Figure 4 This is a schematic diagram of the physical collaborative processing mechanism.

[0031] Figure 5 A schematic diagram of the auxiliary collaborative processing mechanism;

[0032] Figure 6 This is the front view of the vacuum tank;

[0033] Figure 7 for Figure 2 Enlarged view of part A in the middle;

[0034] Figure 8 for Figure 3 Enlarged view of part B in the middle section.

[0035] The components include: 1. Processing body; 2. Physical co-processing mechanism; 3. Auxiliary co-processing mechanism; 4. Infusion assembly; 5. Processing table; 6. Support frame; 7. Lifting cylinder; 8. Lifting plate; 9. Equipment cavity; 10. First connecting rod; 11. Oil cavity; 12. Heating resistor; 13. Stirring assembly; 14. Bubble agitation assembly; 15. Pulse agitation assembly; 16. Motor; 17. First bevel gear; 18. Second bevel gear; 19. Rotary joint; 20. Connecting frame; 21. Fixing frame; 22. Nitrogen storage tank; 23. First output pipe; 24. First electronic valve; 25. Second output pipe; 26. L-shaped stirring pipe; 27. Bubble... 28. L-shaped connecting rod, 29. Ultrasonic generator, 30. Vacuum filter assembly, 31. Foam elimination assembly, 32. Reaction beaker, 33. Vacuum tank, 34. Vacuum pump, 35. Connecting pipe, 36. Evacuation pipe, 37. Filter cotton, 38. Hollow tank, 39. Filter hole, 40. Ultrasonic atomizing plate, 41. Defoamer storage tank, 42. Feed port, 43. Infusion pipe, 44. Second electronic valve, 45. Mounting cover, 46. Deionized water storage tank, 47. First water pump, 48. Third output pipe, 49. Reagent storage tank, 50. Second water pump, 51. Fourth output pipe, 52. Evacuation port, 53. Third electronic valve.

[0036] The accompanying drawings are provided to further illustrate the invention and form part of the specification. They are used together with the embodiments of the invention to explain the invention and do not constitute a limitation thereof. Detailed Implementation

[0037] The technical solutions of the present invention will be clearly and completely described below with reference to the accompanying drawings of the embodiments of the present invention. Obviously, the described embodiments are only some embodiments of the present invention, and not all embodiments. All other embodiments obtained by those skilled in the art based on the embodiments of the present invention without creative effort are within the scope of protection of the present invention.

[0038] In the description of this invention, it should be understood that the terms "upper", "lower", "front", "rear", "left", "right", "top", "bottom", "inner", "outer", etc., indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings. They are only for the convenience of describing this invention and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation. Therefore, they should not be construed as limitations on this invention.

[0039] like Figures 1-8As shown, the present invention proposes a device for preparing highly absorbent biodegradable wood cellulose sponge, including a processing body 1 and an infusion assembly 4 disposed on the processing body 1, as well as a physical co-processing mechanism 2 and an auxiliary co-processing mechanism 3. The physical co-processing mechanism 2 is disposed on the processing body 1, and the auxiliary co-processing mechanism 3 is disposed on the processing body 1. The physical co-processing mechanism 2 includes a stirring assembly 13, a bubble disturbance assembly 14, and a pulse disturbance assembly 15. The stirring assembly 13 is disposed on the physical co-processing mechanism 2, the bubble disturbance assembly 14 is disposed on the physical co-processing mechanism 2, and the pulse disturbance assembly 15 is disposed on the processing body 1.

[0040] The processing body 1 includes a processing table 5, a support frame 6, a lifting cylinder 7, a lifting plate 8, an equipment cavity 9, a first connecting rod 10, an oil cavity 11, and a heating resistor 12. The support frame 6 is fixedly installed on the top of the processing table 5. The cylinder seat of the lifting cylinder 7 is fixedly installed on the top of the inner part of the support frame 6. The output end of the lifting cylinder 7 is fixedly connected to the lifting plate 8. The equipment cavity 9 is opened inside the processing table 5. One end of the first connecting rod 10 is fixedly connected to the inner side wall of the equipment cavity 9. The other end of the first connecting rod 10 is fixedly connected to the outer side wall of the oil cavity 11. The heating resistor 12 is installed on the inner side wall of the oil cavity 11.

[0041] The stirring assembly 13 includes a motor 16, a first bevel gear 17, a second bevel gear 18, a rotary joint 19, a connecting frame 20, and a fixed frame 21. The connecting frame 20 is installed at the lower end of the lifting plate 8, and the motor 16 is fixedly installed at the lower end of the connecting frame 20. The first bevel gear 17 is fixedly installed at the output end of the motor 16. One end of the fixed frame 21 is fixedly connected to the lower end of the lifting plate 8, and the other end of the fixed frame 21 is fixedly connected to the rotary joint 19. The rotating interface of the rotary joint 19 is connected through to one end of the second output pipe 25. The second bevel gear 18 is fixedly sleeved on the outer wall of the second output pipe 25. The first bevel gear 17 and the second bevel gear 18 are meshed and rotated together.

[0042] The bubble disturbance component 14 includes a nitrogen storage tank 22, a first output pipe 23, a first electronic valve 24, a second output pipe 25, an L-shaped stirring pipe 26, and a bubble stone 27. The nitrogen storage tank 22 is placed on the top of the lifting plate 8. The output end of the nitrogen storage tank 22 is connected to one end of the first output pipe 23, and the other end of the first output pipe 23 is connected to the fixed interface of the rotary joint 19. The first electronic valve 24 is installed on the first output pipe 23. Multiple L-shaped stirring pipes 26 are connected to the outer wall of the second output pipe 25. The input end of the bubble stone 27 is fixedly installed at the lower end of the L-shaped stirring pipe 26.

[0043] The pulse disturbance assembly 15 includes an L-shaped connecting rod 28 and an ultrasonic generator 29. The L-shaped connecting rod 28 is fixedly connected to the lower end of the outer side wall of the second output tube 25, and the ultrasonic generator 29 is fixedly installed at the lower end of the L-shaped connecting rod 28.

[0044] The auxiliary co-processing mechanism 3 includes a vacuum filtration component 30 and a foam elimination component 31. The vacuum filtration component 30 is disposed on the auxiliary co-processing mechanism 3, and the foam elimination component 31 is disposed on the auxiliary co-processing mechanism 3.

[0045] The vacuum filtration assembly 30 includes a reaction beaker 32, a vacuum tank 33, a vacuum pump 34, a connecting pipe 35, a suction pipe 36, filter cotton 37, a hollow tank 38, filter holes 39, a suction port 52, and a third electronic valve 53. The reaction beaker 32 is fixedly connected to the bottom of the oil chamber 11. The bottom of the reaction beaker 32 is fixedly connected to the hollow tank 38. Multiple filter holes 39 are opened on the side wall of the hollow tank 38. Filter cotton 37 is fitted on the hollow tank 38. The lower end of the hollow tank 38 is connected to one end of the connecting pipe 35. The vacuum tank 33 is placed at the bottom of the oil chamber 11. A suction port 52 is provided on one side of the top of the vacuum tank 33. The top of the vacuum tank 33 is connected to the other end of the connecting pipe 35. The bottom of the processing table 5 is equipped with a vacuum pump 34. The pumping end of the vacuum pump 34 is connected to one end of the suction pipe 36. The other end of the suction pipe 36 is connected to the suction port 52.

[0046] The foam elimination component 31 includes an ultrasonic atomizing plate 40, a defoamer storage tank 41, a feeding port 42, an infusion pipe 43, a second electronic valve 44, and a mounting cover 45. The defoamer storage tank 41 is installed on the lower side of the lifting plate 8. The upper side wall of the defoamer storage tank 41 is provided with a feeding port 42. The lower end of the feeding port 42 is connected to one end of the infusion pipe 43. The other end of the infusion pipe 43 is connected to the mounting cover 45. The ultrasonic atomizing plate 40 is installed inside the mounting cover 45. The second electronic valve 44 is installed on the infusion pipe 43.

[0047] The infusion assembly 4 includes a deionized water storage tank 46, a first water pump 47, a third output pipe 48, a medicine storage tank 49, a second water pump 50, and a fourth output pipe 51. The deionized water storage tank 46 is placed on one side of the top of the processing table 5. The lower end of the outer wall of the deionized water storage tank 46 is connected to the inlet end of the first water pump 47. The output end of the first water pump 47 is connected to one end of the third output pipe 48. The other end of the third output pipe 48 is located above the reaction beaker 32. The medicine storage tank 49 is placed inside one end of the processing table 5. The second water pump 50 is installed on the top of the medicine storage tank 49. The inlet end of the medicine storage tank 49 is located at the bottom end of the inside of the medicine storage tank 49. The output end of the second water pump 50 is connected to one end of the fourth output pipe 51. The other end of the fourth output pipe 51 is located above the reaction beaker 32. The oil chamber 11 is filled with oil.

[0048] The front of the processing table 5 is equipped with an opening and closing door, and the front of the vacuum tank 33 is equipped with a drain valve.

[0049] In practical use, the dried cellulose raw material is placed into the reaction beaker 32, and sodium hydroxide solution is placed in the reagent storage tank 49. The second water pump 50 is started to transport the sodium hydroxide solution in the reagent storage tank 49 to the reaction beaker 32 through the fourth output pipe 51. At the same time, the output end of the lifting cylinder 7 moves downward, driving the lifting plate 8 to move downward. The downward movement of the lifting plate 8 drives the second output pipe 25 to move downward, which in turn drives the L-shaped stirring tube 26 to move downward. The L-shaped stirring tube 26 is then moved into the reaction beaker 32. The motor 16 is started, and the output end of the motor 16 rotates, driving the first bevel gear 17 to rotate. The rotation drives the second bevel gear 18 to rotate, which in turn drives the second output pipe 25 to rotate, which in turn drives the L-shaped stirring tube 26 to rotate. Sodium hydroxide solution is added while stirring to fully wet the fibers and ensure the cellulose raw material is completely submerged. Then, the heating resistor 12 is activated, heating the oil in the oil chamber 11, thereby indirectly heating the reaction beaker 32. Stirring is maintained simultaneously. The first electronic valve 24 is opened, activating the ultrasonic atomizing plate 40 and the ultrasonic generator 29. Nitrogen gas from the nitrogen storage tank 22 enters the L-shaped stirring tube 26 through the first output pipe 23, and finally is sprayed as microbubbles through the air stone 27. The continuous microbubbles break up aggregated particles, causing slight agitation. Simultaneously, the ultrasonic cavitation generated by the ultrasonic generator 29 locally breaks up clumps and promotes rapid penetration of the alkaline solution, preventing the cellulose raw material from clumping. After the reaction structure is established, the ultrasonic generator 29 and the first electronic valve 24 are turned off, while the L-shaped stirring tube 26 continues stirring. The second electronic valve 44 and the ultrasonic atomizing plate 40 are opened, and the defoamer in the defoamer storage tank 41 flows to the ultrasonic atomizing plate 40 through the infusion pipe 43. After being atomized by the ultrasonic atomizing plate 40, it falls into the reaction beaker 32, eliminating the foam generated during the dissolution of lignin and hemicellulose under alkaline conditions. After cooling to room temperature... Open the third electronic valve 53 and start the vacuum pump 34. Use the filter cotton 37 to filter the liquid in the reaction beaker 32 through the connecting pipe 35 into the vacuum tank 33. Then start the first water pump 47 to pump the deionized water in the deionized water storage tank 46 into the reaction beaker 32. Use the deionized water to wash the solids in the reaction beaker 32. Then open the third electronic valve 53 and the vacuum pump 34 again to pump the liquid into the vacuum tank 33. Repeat the washing process several times. The washed cellulose raw material is left in suspension and filtered and dehydrated into a paste by the vacuum pump 34. Then take it out, dry it and store it. The above is the overall working process of this invention. Repeat this step when using it next time.

[0050] It should be noted that, in this document, relational terms such as "first" and "second" are used only to distinguish one entity or operation from another, and do not necessarily require or imply any such actual relationship or order between these entities or operations. Furthermore, the terms "comprising," "including," or any other variations thereof are intended to cover non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements includes not only those elements but also other elements not expressly listed, or elements inherent to such process, method, article, or apparatus.

[0051] Although embodiments of the invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made to these embodiments without departing from the principles and spirit of the invention, the scope of which is defined by the appended claims and their equivalents.

[0052] The present invention and its embodiments have been described above. This description is not restrictive, and the accompanying drawings are only one embodiment of the present invention; the actual structure is not limited thereto. In conclusion, if those skilled in the art are inspired by this description and design similar structures and embodiments without departing from the spirit of the invention, such designs should fall within the protection scope of the present invention.

Claims

1. A device for preparing highly absorbent biodegradable wood cellulose sponge, comprising a processing body (1) and an infusion assembly (4) disposed on the processing body (1), characterized in that: It also includes a physical co-processing mechanism (2) and an auxiliary co-processing mechanism (3). The physical co-processing mechanism (2) is disposed on the processing body (1), and the auxiliary co-processing mechanism (3) is disposed on the processing body (1). The physical co-processing mechanism (2) includes a stirring component (13), a bubble disturbance component (14), and a pulse disturbance component (15). The stirring component (13) is disposed on the physical co-processing mechanism (2), the bubble disturbance component (14) is disposed on the physical co-processing mechanism (2), and the pulse disturbance component (15) is disposed on the processing body (1).

2. The apparatus for preparing highly absorbent biodegradable wood cellulose sponge according to claim 1, characterized in that: The processing body (1) includes a processing table (5), a support frame (6) is fixedly installed at the top of the processing table (5), the cylinder seat of the lifting cylinder (7) is fixedly installed at the top of the inside of the support frame (6), the output end of the lifting cylinder (7) is fixedly connected to the lifting plate (8), an equipment cavity (9) is opened in the processing table (5), one end of the first connecting rod (10) is fixedly connected to the inner side wall of the equipment cavity (9), the other end of the first connecting rod (10) is fixedly connected to the outer side wall of the oil cavity (11), and a heating resistor (12) is installed on the inner side wall of the oil cavity (11).

3. The apparatus for preparing highly absorbent biodegradable wood cellulose sponge according to claim 2, characterized in that: The stirring assembly (13) includes a connecting frame (20), which is installed at the lower end of the lifting plate (8). A motor (16) is fixedly installed at the lower end of the connecting frame (20). A first bevel gear (17) is fixedly installed at the output end of the motor (16). One end of a fixing frame (21) is fixedly connected to the lower end of the lifting plate (8). A rotary joint (19) is fixedly connected to the other end of the fixing frame (21). The rotary interface of the rotary joint (19) is connected through to one end of a second output pipe (25). A second bevel gear (18) is fixedly sleeved on the outer side wall of the second output pipe (25). The first bevel gear (17) and the second bevel gear (18) mesh and rotate together.

4. The apparatus for preparing highly absorbent and biodegradable wood cellulose sponge according to claim 3, characterized in that: The bubble disturbance component (14) includes a nitrogen storage tank (22), which is placed at the top of the lifting plate (8). The output end of the nitrogen storage tank (22) is connected to one end of the first output pipe (23), and the other end of the first output pipe (23) is connected to the fixed interface of the rotary joint (19). A first electronic valve (24) is installed on the first output pipe (23), and multiple L-shaped stirring pipes (26) are connected to the outer wall of the second output pipe (25). The lower end of the L-shaped stirring pipe (26) is fixedly installed with the input end of the bubble stone (27).

5. The apparatus for preparing highly absorbent and biodegradable wood cellulose sponge according to claim 4, characterized in that: The pulse disturbance component (15) includes an L-shaped connecting rod (28), which is fixedly connected to the lower end of the outer wall of the second output tube (25), and an ultrasonic generator (29) is fixedly installed at the lower end of the L-shaped connecting rod (28).

6. The apparatus for preparing highly absorbent and biodegradable wood cellulose sponge according to claim 5, characterized in that: The auxiliary co-processing mechanism (3) includes a vacuum filtration component (30) and a foam elimination component (31). The vacuum filtration component (30) is disposed on the auxiliary co-processing mechanism (3), and the foam elimination component (31) is disposed on the auxiliary co-processing mechanism (3).

7. The apparatus for preparing highly absorbent and biodegradable wood cellulose sponge according to claim 6, characterized in that: The vacuum filtration assembly (30) includes a reaction beaker (32), which is fixedly connected to the bottom of the oil chamber (11). The bottom of the reaction beaker (32) is fixedly connected to a hollow tank (38). Multiple filter holes (39) are opened on the side wall of the hollow tank (38). Filter cotton (37) is fitted on the hollow tank (38). The lower end of the hollow tank (38) is connected to one end of a connecting pipe (35). A vacuum tank (33) is placed at the bottom of the oil chamber (11). A suction port (52) is provided on one side of the top of the vacuum tank (33). The top of the vacuum tank (33) is connected to the other end of the connecting pipe (35). A vacuum pump (34) is provided at the bottom of the processing table (5). The suction end of the vacuum pump (34) is connected to one end of a suction pipe (36). The other end of the suction pipe (36) is connected to the suction port (52).

8. The apparatus for preparing highly absorbent and biodegradable wood cellulose sponge according to claim 7, characterized in that: The foam elimination component (31) includes a defoamer storage tank (41), which is installed on the lower side of the lifting plate (8). The upper side wall of the defoamer storage tank (41) is provided with a feeding port (42). The lower end of the feeding port (42) is connected to one end of the infusion tube (43), and the other end of the infusion tube (43) is connected to the mounting cover (45). An ultrasonic atomizing plate (40) is installed inside the mounting cover (45), and a second electronic valve (44) is installed on the infusion tube (43).

9. The apparatus for preparing highly absorbent biodegradable wood cellulose sponge according to claim 8, characterized in that: The infusion assembly (4) includes a deionized water storage tank (46), which is placed on one side of the top of the processing table (5). The lower end of the outer wall of the deionized water storage tank (46) is connected to the inlet end of the first water pump (47). The output end of the first water pump (47) is connected to one end of the third output pipe (48). The other end of the third output pipe (48) is located above the reaction beaker (32). A drug storage tank (49) is placed inside one end of the processing table (5). A second water pump (50) is installed on the top of the drug storage tank (49). The inlet end of the drug storage tank (49) is located at the bottom of the inside of the drug storage tank (49). The output end of the second water pump (50) is connected to one end of the fourth output pipe (51). The other end of the fourth output pipe (51) is located above the reaction beaker (32). The oil chamber (11) is filled with oil.

10. A method of using the apparatus for preparing highly absorbent and biodegradable wood cellulose sponges, as described in claim 9, characterized in that... The main steps include the following: Step 1: Place the dried cellulose raw material into the reaction beaker (32), put sodium hydroxide solution into the reagent storage tank (49), start the second water pump (50), and transport the sodium hydroxide solution in the reagent storage tank (49) to the reaction beaker (32) through the fourth output pipe (51). At the same time, the output end of the lifting cylinder (7) moves downward, driving the lifting plate (8) to move downward. The lifting plate (8) moves downward, driving the second output pipe (25) to move downward. The second output pipe (25) moves downward, driving the L-shaped stirring tube (26) to move downward, and moving the L-shaped stirring tube (26) into the reaction beaker (32). Step 2: Start the motor (16). The output end of the motor (16) rotates, which drives the first bevel gear (17) to rotate. The first bevel gear (17) rotates, which drives the second bevel gear (18) to rotate. The second bevel gear (18) rotates, which drives the second output tube (25) to rotate. The second output tube (25) rotates, which drives the L-shaped stirring tube (26) to rotate. While adding sodium hydroxide solution, stir to fully wet the cellulose raw material and ensure that the cellulose raw material is completely submerged. Then start the heating resistor (12) to heat the oil in the oil chamber (11), thereby indirectly heating the reaction beaker (32). Step 3: While stirring, open the first electronic valve (24), start the ultrasonic atomizing plate (40) and ultrasonic generator (29). The nitrogen in the nitrogen storage tank (22) enters the L-shaped stirring tube (26) through the first output pipe (23), and finally sprays out in the form of micro bubbles through the bubble stone (27). The continuous micro bubbles can break up the particle aggregation and form a slight tumbling. At the same time, the ultrasonic cavitation generated by the ultrasonic generator (29) can break up the agglomerates locally and promote the rapid penetration of the alkaline solution to prevent the cellulose raw material from agglomerating. After the reaction structure is formed, close the ultrasonic generator (29) and the first electronic valve (24). The L-shaped stirring tube (26) continues to stir. Open the second electronic valve (44) and the ultrasonic atomizing plate (40). The defoamer in the defoamer storage tank (41) flows to the ultrasonic atomizing plate (40) through the infusion pipe (43). After being atomized by the ultrasonic atomizing plate (40), it falls into the reaction beaker (32) to eliminate the foam generated when lignin and hemicellulose dissolve under alkaline conditions. Step 4: After cooling to room temperature, open the third electronic valve (53), start the vacuum pump (34), and use the filter cotton (37) to filter the liquid in the reaction beaker (32) into the vacuum tank (33) through the connecting pipe (35). Then start the first water pump (47) to pump the deionized water in the deionized water storage tank (46) into the reaction beaker (32) and use the deionized water to wash the solid in the reaction beaker (32). Then open the third electronic valve (53) and the vacuum pump (34) again to pump the liquid into the vacuum tank (33) and wash it repeatedly. The washed cellulose raw material is then filtered and dehydrated into a paste by the vacuum pump (34) and then taken out, dried and stored.

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