A device for uniformly dyeing and drying textile fabrics

Abstract

The present invention discloses a device for uniformly dyeing and drying textile fabrics, which relates to the technical field of fabric drying. It includes a body conveyor table, a carrier controller is installed below the body conveyor table, a drying chamber is installed above the body conveyor table, a radiator is installed above the drying chamber, a comprehensive drying mechanism is arranged inside the drying chamber, and a circulation recovery mechanism is arranged below the body conveyor table. By using a double-cone guide cylinder, the hot air is guided to flow in a way that the internal part is in direct current, the middle part is in a spiral shape, and four branch pipes are designed around to mainly target the dead corners. First of all, the hot air in the internal direct current part can directly blow to the center area of the fabric, providing a stable drying air flow. Secondly, the spiral air flow in the middle can perform spiral surrounding drying on the middle part of the fabric. Furthermore, through this new type of guide cylinder structure, the hot air is guided to the fabric surface in all directions, ensuring that every part of the fabric can be effectively dried, and improving the integrity of drying.

Description

Technical Field

[0001] The present invention relates to the technical field of fabric drying, and particularly to a device for uniformly dyeing and drying textile fabrics. Background Art

[0002] Existing fabric drying devices are equipment used in the textile industry to dry dyed textile fabrics. Their purpose is to efficiently remove the moisture in the fabric while ensuring the fabric quality, so that the fabric reaches the moisture content required for subsequent processing or finished products.

[0003] In a Chinese patent with the publication number CN117663716A, a textile fabric dyeing and drying device and a drying treatment process are disclosed, including: a support component and a heating component arranged on the top of the support component. A positioning component is arranged on one side of the support component, a water collection component is arranged on one side of the positioning component, and a winding component is arranged on one side of the support component. The support component includes a support table and a drying chamber box arranged on the top surface of the support table. Through grooves are arranged in the middle and at the top of the drying chamber box. The positioning component includes a water collection cavity arranged at the lower end of the drying chamber box. A support rod is arranged inside the water collection cavity. There are four groups of support rods. The upper ends of the support rods are fixedly connected with a long support plate. When the fabric is fixed in the drying chamber box through the positioning component, the user turns on the blowing mode of two groups of electric fan components. The blowing mode and the horizontal reciprocating movement of the two groups of electric fan components together strengthen the air flow velocity in the drying chamber box.

[0004] However, the equipment in the cited document and the existing technologies still have the following defects in specific use:

[0005] 1. Compared with using the blowing mode of an electric fan in the cited document and making it move reciprocally to dry the dyed fabric, during this process, the blade design of the electric fan and the motor rotation mode result in non-ideal uniform air output. Even when the fan is stationary, there are differences in the air flow velocity at the blade edge and the center. The linear velocity at the blade edge is large, generating a fast air flow velocity and a large flow rate, while the air flow velocity in the area near the center is slow and the flow rate is small. Therefore, when the fan moves reciprocally, this non-uniform air output mode will form a complex and non-uniform air flow distribution on the fabric surface as the fan position changes. However, due to the high temperature and non-uniform drying speed, a dye migration phenomenon will be triggered. When a part of the fabric dries faster, the moisture will carry the dye to the part that dries slower, resulting in uneven fabric color.

[0006] 2. When performing hot air drying treatment compared with the prior art, in order to maintain the temperature required for drying, a hot air blower needs to continuously heat the air. However, the outer shell of the drying chamber is usually difficult to achieve complete heat insulation, and heat will be dissipated into the surrounding environment. In the prior art, the air inlet is located at the top, and the air outlet is generally designed on the side and bottom. In this way, the hot air is prone to form a short circuit, and part of the hot air directly flows from the air inlet to the air outlet without fully contacting the fabric and realizing the recycling of heat, resulting in the need to continuously supplement heat during the drying process, thereby increasing energy consumption;

[0007] Therefore, in view of this, the present invention proposes a textile fabric uniform dyeing and drying treatment device to make up for and improve the deficiencies of the prior art. Summary of the Invention

[0008] To solve the above technical problems, the present invention provides a textile fabric uniform dyeing and drying treatment device to solve the technical problems raised in the above background technology.

[0009] To achieve the above purpose, the technical solution adopted by the present invention is: a textile fabric uniform dyeing and drying treatment device for drying the fabric main body, including a body conveyor table, a carrier controller is installed below the body conveyor table, a drying chamber is installed above the body conveyor table, a radiator is installed above the drying chamber, a comprehensive drying mechanism is arranged inside the drying chamber, and a circulation recovery mechanism is arranged below the body conveyor table;

[0010] The comprehensive drying mechanism is used to dry the fabric main body in an all-round and non-dead-angle manner;

[0011] The circulation recovery mechanism is used to recycle and efficiently utilize the hot air released by the radiator.

[0012] Further, the comprehensive drying mechanism includes a guide cylinder connected to the output end of the radiator. The lower surface of the guide cylinder is fixedly connected with a spiral ring group. The inner side wall of the spiral ring group is fixedly connected with an inner built-in bin. The outer wall of the guide cylinder near the radiator end is evenly communicated with branch pipes. The inner side walls of the branch pipes are evenly and symmetrically installed with drainage plates, and elastic cords are fixedly connected to the side walls of the drainage plates.

[0013] Further, the guide cylinder as a whole has a gradually shrinking - gradually expanding air duct structure. The inlet end and the outlet end of the guide cylinder both adopt gradually expanding sections, and the middle part is a gradually shrinking section.

[0014] Further, the spiral ring group as a whole is composed of a combination of multiple inclined plane sheets, and the overall size of the inner built-in bin is in a ratio of one to two with the overall size of the lower half of the guide cylinder.

[0015] Furthermore, the branch pipes are evenly and symmetrically installed at the 45-degree diagonal positions on the outer wall of the flow guide cylinder, and the output ends of the branch pipes and the output end of the flow guide cylinder are located on the same horizontal plane.

[0016] Furthermore, the drainage plate and the branch pipes are movably connected by elastic cords, and the elastic cords are entirely made of polyester-type polyurethane material.

[0017] Furthermore, the circulation and recovery mechanism includes rectangular grooves evenly penetrating through the surface of the body conveyor table. An outer guide shell is installed below the rectangular grooves. The outer guide shell is fixedly connected to the lower surface of the body conveyor table. A diverging column is fixedly connected to the bottom wall of the outer guide shell, and an inner guide shell is movably connected to the outer wall of the diverging column.

[0018] Furthermore, the size of the output port of the outer guide shell is equal to the length dimension of the rectangular groove. The inner guide shell is located at the exact center position of the outer guide shell, and a spacer layer is formed between the outer guide shell and the inner guide shell.

[0019] Furthermore, the side walls of the outer guide shell and the inner guide shell are both arc-shaped that contract inward, and the outer guide shell and the inner guide shell are movably connected by connecting springs. The connecting springs are located at the diagonal positions around the outer guide shell and the inner guide shell.

[0020] Furthermore, the partition plate in the diverging column is cross-shaped and corresponds to the arc-shaped side wall of the outer guide shell. The diverging column divides the interior of the outer guide shell into four equal parts.

[0021] Compared with the prior art, the beneficial effects of the present invention are as follows: In order to improve the problem of incomplete drying of fabrics in the prior art, this device uses a double-cone flow guide cylinder to guide hot air in a flow mode of internal direct flow, middle spiral, and four branch pipes around the periphery mainly targeting dead corners. First, the hot air in the internal direct flow part can directly blow to the central area of the fabric, providing a stable drying air flow. Second, the spiral air flow in the middle can perform spiral surrounding drying on the middle part of the fabric, increasing the contact time and contact area between the hot air and the fabric. Finally, the branch pipes around the periphery are specifically designed for the dead corner areas that are easily overlooked in the traditional drying method. Thus, through this new type of flow guide cylinder structure, the hot air is guided to the fabric surface in all directions, ensuring that every part of the fabric can be effectively dried, and improving the integrity of drying.

[0022] Among them, the gas flowing out of the branch pipe is consistent with the spiral gas flowing out of the draft tube in terms of turning direction. Relying on the synergistic effect of the consistent turning direction, the inflow of the branch pipe gas increases the total momentum of the central spiral gas. This increased momentum will be directly converted into the turning force on the spiral gas. At the same time, according to the assistance of the tangential inflow of the gas, the gas flows out in a tangential form between the branch pipe and the draft tube. This outflow method enables the gas to have a tangential velocity component similar to that of the spiral gas at the moment of outflow. According to Newton's second law, force is equal to the product of mass and acceleration. In this case, the tangential velocity component of the branch pipe gas will generate an additional tangential force on the spiral gas, thereby enhancing the rotational power of the spiral gas;

[0023] Compared with the method of using a fan to guide the air flow for drying in the prior art, the drying method implemented by this device also has the following advantages:

[0024] Firstly: For the difficult-to-evaporate moisture in the center of thick textile fabrics, this device first dries the center with a central direct-flow hot air, and then the spiral surrounding hot air flow dries the periphery, avoiding the problem of incomplete local drying caused by one-way drying. Then, through the synergistic effect between the internal direct flow and the external spiral hot air, a stable drying core is formed by the direct flow, and the self-surrounding characteristics of the spiral hot air flow timely supplement heat and air flow power, so as to ensure the continuous and efficient progress of the drying process;

[0025] Secondly: Relying on the all-round hot air distribution of the double-cone draft tube, the hot air can more effectively exchange heat with the moisture in the fabric, accelerating the evaporation process of the moisture. Furthermore, more moisture can be removed within the same time, shortening the drying time. For large-scale production in the textile industry, this can reduce the production cycle, improve the utilization rate of equipment, and reduce production costs;

[0026] Thirdly: The new draft tube structure brings a uniform drying environment. The drying speeds of each part of the fabric are similar, and the moisture distribution is relatively stable. There will be no concentration difference caused by different drying speeds, thus preventing the migration of moisture carrying dyes, helping to maintain the uniformity of the fabric color, and reducing the number of defective products caused by uneven color, improving the qualification rate of products;

[0027] This device evenly and obliquely installs a plurality of drainage plates inside the peripheral branch pipes. A part of the hot air follows the inclined drainage plates and then merges into the hot air of the intermediate direct flow, accelerating the hot air. Firstly, the accelerated hot air flow makes up for the gas flow velocity between the branch pipe and the draft tube, keeping the output between the two consistent. And this way of generating heat through contact friction improves the surface temperature of the components to prevent heat dissipation. Furthermore, it reduces the situation of continuously supplementing heat to maintain the temperature during the drying process and prevents excessive hot air temperature from being transferred to the surface of the components, resulting in heat dissipation;

[0028] To address the problems in the prior art where the short - circuit phenomenon of hot air leads to low heat utilization efficiency and high energy consumption, this device utilizes the spacer layer formed between the inner guiding shell and the outer guiding shell. After the hot air reaches the bottom of the inner guiding shell, it is guided to flow upward along the outer wall of the outer guiding shell, forming a unique hot - air circulation from bottom to top. This hot - air circulation method makes full use of the natural upward characteristic of the heat flow, effectively avoiding the short - circuit phenomenon of hot air directly flowing from the air inlet to the air outlet. On the one hand, it realizes the efficient recycling of hot air, reduces the dependence on additional heat, and lowers energy consumption. On the other hand, it also realizes the dual drying treatment of the fabric, mainly drying the lower surface of the fabric.

[0029] More importantly, the arc - shaped design of the side walls of the inner guiding shell and the outer guiding shell not only reduces the resistance of the hot air during the circulation process but also promotes the uniform distribution of heat, ensuring the uniformity and thoroughness of material drying, and enabling the full absorption and reuse of hot air throughout the process.

[0030] The partition plates in the dividing column adopt a cross - shaped layout, precisely corresponding to the arc - shaped side walls of the outer guiding shell, effectively dividing the space inside the outer guiding shell into four equal parts. The key advantage of this design is that it can accurately control the direction of the hot air, ensuring that the hot air evenly covers each area.

[0031] Among them, the outer guiding shell and the inner guiding shell are connected to each other through connecting springs at the four corners. When the hot air impacts the side wall of the inner guiding shell, the connecting springs can respond in a timely manner, finely adjust the position of the inner guiding shell, ensure the uniform distribution of hot - air pressure, avoid local overheating or air - flow blockage phenomena, and through the elastic deformation of the springs, buffer the impact force of the hot air, effectively reducing equipment vibration and noise, protecting the structure from excessive stress damage, and extending the service life. BRIEF DESCRIPTION OF THE DRAWINGS

[0032] Figure 1 is the front - view three - dimensional structure schematic diagram of the present invention;

[0033] Figure 2 is the internal three - dimensional structure schematic diagram of the drying chamber of the present invention;

[0034] Figure 3 is the three - dimensional structure schematic diagram of the comprehensive drying mechanism of the present invention;

[0035] Figure 4 is the internal three - dimensional structure schematic diagram of the draft tube of the present invention;

[0036] Figure 5 is the internal three - dimensional structure schematic diagram of the branch pipe of the present invention;

[0037] Figure 6 is the present invention Figure 5 is the partial enlarged three - dimensional structure schematic diagram at position A in the present invention;

[0038] Figure 7 Schematic plan view of the internal structure of the draft tube of the present invention;

[0039] Figure 8 Schematic three-dimensional structure view of the rectangular groove of the present invention;

[0040] Figure 9 Schematic three-dimensional structure view of the outer guiding shell of the present invention;

[0041] Figure 10 Schematic three-dimensional structure view of the circulation recovery mechanism of the present invention;

[0042] Figure 11 Explosion view of the circulation recovery mechanism of the present invention.

[0043] The reference numerals in the figure are: 1, body conveyor table; 11, carrier controller; 12, drying chamber; 13, radiator; 14, fabric body; 2, overall drying mechanism; 21, draft tube; 22, spiral ring group; 23, built-in chamber; 24, branch pipe; 25, drainage plate; 26, elastic cord; 3, circulation recovery mechanism; 31, rectangular groove; 32, outer guiding shell; 33, diverging column; 34, inner guiding shell; 35, connecting spring. Detailed implementation manners

[0044] Next, the technical solutions in the embodiments of the present invention will be clearly and completely described in conjunction with the accompanying drawings in the embodiments of the present invention. Obviously, the described embodiments are only a part of the embodiments of the present invention, rather than all the embodiments. Based on the embodiments of the present invention, all other embodiments obtained by those of ordinary skill in the art without creative efforts shall fall within the protection scope of the present invention;

[0045] It should be noted that the above-mentioned devices such as the body conveyor table 1, the carrier controller 11, the drying chamber 12, and the radiator 13 can use commercially available related products. The structures and working principles of these products belong to the prior art and will not be elaborated here.

[0046] Embodiment 1

[0047] Please refer to Figure 1 and Figure 2 As shown, a textile fabric uniform dyeing and drying treatment device for drying the fabric body 14 includes a body conveyor table 1, a carrier controller 11 is installed below the body conveyor table 1, a drying chamber 12 is installed above the body conveyor table 1, a radiator 13 is installed above the drying chamber 12, an overall drying mechanism 2 is arranged inside the drying chamber 12, and a circulation recovery mechanism 3 is arranged below the body conveyor table 1.

[0048] Please refer to Figures 2 to 7As shown in the figure, the comprehensive drying mechanism 2 includes a diversion cylinder 21 connected to the output end of the radiator 13. The lower surface of the diversion cylinder 21 is fixedly connected with a spiral ring group 22. The inner side wall of the spiral ring group 22 is fixedly connected with an inner built-in bin 23. The outer wall of the diversion cylinder 21 near one end of the radiator 13 is evenly communicated with branch pipes 24. The inner side walls of the branch pipes 24 are evenly and symmetrically installed with drainage plates 25. Elastic cords 26 are fixedly connected to the side walls of the drainage plates 25;

[0049] It should be noted that the diversion cylinder 21 as a whole has a gradually shrinking - gradually expanding air duct structure. Both the inlet end and the outlet end of the diversion cylinder 21 adopt gradually expanding sections, and the middle part is a gradually shrinking section. The spiral ring group 22 as a whole is composed of a combination of multiple inclined plane sheets. The overall size of the inner built-in bin 23 and the overall size of the lower half of the diversion cylinder 21 are in a ratio of one to two. The branch pipes 24 are evenly and symmetrically installed at the 45-degree diagonal of the outer wall of the diversion cylinder 21. The output ends of the branch pipes 24 and the output end of the diversion cylinder 21 are located on the same horizontal plane.

[0050] Specifically, as Figure 2 shown in the figure, when the fabric main body 14 is transported to directly below the diversion cylinder 21 through the fuselage conveyor table 1, at this time, the upper and lower sides of the fabric main body 14 respectively correspond to the diversion cylinder 21 and the rectangular groove 31. At the same time, the staff controls the fuselage conveyor table 1 to stop transporting the fabric main body 14 and starts the radiator 13 to convey hot air into the drying bin 12 to dry the fabric main body 14;

[0051] Since the diversion cylinder 21 as a whole has a gradually shrinking - gradually expanding shape, and its own inlet end and outlet end are in an expanded state, and the inner built-in bin 23 is located in the lower half of the diversion cylinder 21, when the hot air output by the radiator 13 flows along the diversion cylinder 21, the innermost hot air flow will flow directly along the inner side wall of the inner built-in bin 23, and the hot air flow passing through the spiral ring group 22 in the middle will flow in a circular motion under the guiding action of the inclined plane sheets. And for the four corners of the fabric, four branch pipes 24 are specifically designed. Therefore, it is ensured that the hot air flow output by the radiator 13 flows along the branch pipes 24. In summary, through the cooperation and guidance of the shape and internal structure of the double-conical diversion cylinder 21, the hot air is made to flow in a way that the inner part flows directly, the middle part spirals, and the four branch pipes 24 are mainly aimed at the dead corners. The hot air in the directly flowing inner part can directly blow to the central area of the fabric main body 14 to provide a stable drying air flow, and the spiral air flow in the middle can perform spiral circular drying on the middle part of the fabric main body 14, increasing the contact time and contact area between the hot air and the fabric main body 14. Finally, the four surrounding branch pipes 24 are specifically aimed at the dead corner areas that are easily overlooked in the traditional drying method, ensuring that every part of the fabric main body 14 can be effectively dried, improving the integrity of drying;

[0052] According to the principle of pressure difference in fluid mechanics, gas always flows from a place with high pressure to a place with low pressure. Inside the draft tube 21, due to the spiral gas forming a relatively low-pressure area in the dead corner areas around (because the spiral flow cannot fully reach these areas, there are fewer gas molecules and lower pressure), while the gas in the branch pipe 24 has a relatively high pressure (provided by being directly connected to the gas source), so the gas in the branch pipe 24 will flow towards the dead corner areas under the drive of the pressure difference, thus playing a supplementary role. And when the gas flowing out of the branch pipe 24 is in the same direction as the spiral gas flowing out of the draft tube 21, from the perspective of momentum conservation, when the gas in the branch pipe 24 flows in, it carries a certain amount of momentum. Since the direction is the same as that of the spiral gas, this part of the momentum will be superimposed on the momentum of the spiral gas. The result of this momentum superposition is to generate a rotational force on the spiral gas, enhancing the rotational speed and rotational force of the spiral gas.

[0053] It should be noted that the drainage plate 25 and the branch pipe 24 are movably connected by an elastic cord 26, and the elastic cord 26 is entirely made of polyester-type polyurethane material;

[0054] Specifically, when the hot air flow flows into the branch pipe 24, a part of the hot air flow directly flows downward in a straight-line manner, while the other part of the hot air follows the inclined drainage plate 25 and then merges into the hot air flowing in the middle in a straight line, accelerating the hot air. First, the accelerated hot air flow makes up for the gas flow speed between the branch pipe 24 and the draft tube 21, making the output between the two consistent. And this way of generating heat through contact friction increases the surface temperature of the components to prevent heat dissipation, thereby reducing the situation of continuously supplementing heat to maintain the temperature during the drying process, and preventing too much hot air temperature from being transferred to the surface of the components, resulting in heat dissipation.

[0055] Embodiment 2

[0056] On the basis of Embodiment 1, please refer to Figure 8 and Figure 11 As shown, the recycling mechanism 3 includes a rectangular groove 31 uniformly and penetratingly opened on the surface of the fuselage conveyor table 1. Below the rectangular groove 31, an outer guide shell 32 is installed, and the outer guide shell 32 is fixedly connected to the lower surface of the fuselage conveyor table 1. The bottom wall of the outer guide shell 32 is fixedly connected with a dividing column 33, and the outer wall of the dividing column 33 is movably connected with an inner guide shell 34;

[0057] It should be noted that the size of the output port of the outer guide shell 32 is equal to the length size of the rectangular groove 31. The inner guide shell 34 is located at the exact center position of the outer guide shell 32, and there is a spacer layer formed between the outer guide shell 32 and the inner guide shell 34. The side walls of both the outer guide shell 32 and the inner guide shell 34 are in an arc shape that shrinks inward.

[0058] Specifically, since the lower surface of the fabric body 14 is exactly corresponding to the upper side of the rectangular groove 31, when some redundant hot air flows into the inner guiding shell 34 through the rectangular groove 31, as there is a spacer layer formed between the outer guiding shell 32 and the inner guiding shell 34, after the hot air reaches the bottom of the inner guiding shell 34, it will flow upward along the outer wall of the outer guiding shell 32, forming a unique hot air circulation from bottom to top. This hot air circulation method makes full use of the natural upward characteristic of the heat flow, effectively avoiding the short-circuit phenomenon of the hot air directly from the air inlet to the air outlet. On the one hand, it realizes the efficient recycling of the hot air, reduces the dependence on additional heat and lowers the energy consumption. On the other hand, it also realizes the double drying treatment of the fabric body 14, mainly drying the lower surface of the fabric body 14.

[0059] It should be noted that the outer guiding shell 32 and the inner guiding shell 34 are movably connected by connecting springs 35. The connecting springs 35 are located at the diagonal corners around the outer guiding shell 32 and the inner guiding shell 34. The partition plates in the dividing column 33 are in a cross shape, and the partition plates correspond to the arc-shaped side walls of the outer guiding shell 32. The dividing column 33 divides the interior of the outer guiding shell 32 into four equal parts.

[0060] Specifically, keeping the outer guiding shell 32 and the inner guiding shell 34 movably connected, the connecting springs 35 can stretch to a certain extent according to the change of the hot air flow rate. When the hot air flow rate increases, the pressure of the hot air on the inner guiding shell 34 increases. At this time, the connecting springs 35 can be appropriately compressed, making the spacer layer space between the outer guiding shell 32 and the inner guiding shell 34 slightly increase, thereby reducing the flow resistance and ensuring that the hot air can circulate smoothly between the two. And when the hot air contacts the side wall of the inner guiding shell 34, due to the structure that the dividing column 33 divides the interior of the inner guiding shell 34 into four equal parts and the partition plates are in a cross shape corresponding to the arc-shaped side walls of the outer guiding shell 32, if the pressure of the hot air on one side is larger when the hot air flows, the connecting spring 35 on this side will be compressed, while the spring on the other side will stretch accordingly, so as to adjust the position of the inner guiding shell 34, maintain the overall stability of the inner guiding shell 34, make the hot air distribute and flow more evenly, and improve the uniformity of drying.

[0061] Although the embodiments of the present invention have been shown and described, for those of ordinary skill in the art, it can be understood that various changes, modifications, substitutions and variations can be made to these embodiments without departing from the principle and spirit of the present invention. The scope of the present invention is defined by the appended claims and their equivalents.

Claims

1. A textile fabric uniform dyeing and drying treatment device, used for drying a fabric body (14), comprising a body conveying platform (1), a carrier controller (11) is installed below the body conveying platform (1), a drying chamber (12) is installed above the body conveying platform (1), and a radiator (13) is installed above the drying chamber (12), characterized in that: A comprehensive drying mechanism (2) is provided inside the drying chamber (12), and a recycling mechanism (3) is provided below the fuselage conveying platform (1); The full drying mechanism (2) is used to dry the fabric body (14) in an all-round manner without any dead angles; The recycling mechanism (3) is used to circulate and efficiently utilize the hot air released by the radiator (13); The comprehensive drying mechanism (2) comprises a guide tube (21) connected to the output end of the radiator (13); a spiral ring group (22) is fixedly connected to the lower surface of the guide tube (21); a built-in bin (23) is fixedly connected to the inner wall of the spiral ring group (22); a branch pipe (24) is evenly connected to the outer wall of the guide tube (21) at one end close to the radiator (13); guide plates (25) are evenly and symmetrically installed on the inner wall of the branch pipe (24); elastic ropes (26) are fixedly connected to the side walls of the guide plates (25); the guide tube (21) as a whole presents a gradually contracting-expanding air duct structure; the guide tube (21) ) has an inlet end and an outlet end that are both gradually expanding sections, and a middle portion that is gradually contracting. The spiral ring group (22) is composed of a plurality of inclinedly mounted planar sheets. The overall size of the built-in bin (23) is one to two of the overall size of the lower half of the guide tube (21). The branch pipe (24) is evenly and symmetrically mounted at a forty-five degree diagonal position on the outer wall of the guide tube (21). The output end of the branch pipe (24) is located on the same horizontal plane as the output end of the guide tube (21). The guide plate (25) and the branch pipe (24) are movably connected via an elastic rope (26), and the elastic rope (26) is composed of a polyester polyurethane material.

2. A textile fabric uniform dyeing and drying treatment device according to claim 1, characterized in that: The recycling mechanism (3) comprises a rectangular groove (31) uniformly extending through the surface of the fuselage conveying platform (1); an outer guide shell (32) is installed below the rectangular groove (31); the outer guide shell (32) is fixedly connected to the lower surface of the fuselage conveying platform (1); a dividing column (33) is fixedly connected to the bottom wall of the outer guide shell (32); and an inner guide shell (34) is movably connected to the outer wall of the dividing column (33).

3. A textile fabric uniform dyeing and drying treatment device according to claim 2, characterized in that: The size of the output port of the outer lead shell (32) is equal to the length of the rectangular groove (31); the inner lead shell (34) is located at the exact center of the outer lead shell (32); and a spacing layer is formed between the outer lead shell (32) and the inner lead shell (34).

4. The device for uniform dyeing and drying of textile fabrics according to claim 2, characterized in that: The side walls of the outer lead shell (32) and the inner lead shell (34) are both in the shape of an inwardly contracted arc surface, and the outer lead shell (32) and the inner lead shell (34) are movably connected via a connecting spring (35), wherein the connecting spring (35) is located at diagonal positions around the outer lead shell (32) and the inner lead shell (34).

5. The device for uniform dyeing and drying of textile fabrics according to claim 2, characterized in that: The partition plate in the dividing column (33) is cross-shaped, and the partition plate corresponds to the arc-shaped side wall of the outer lead casing (32). The dividing column (33) divides the interior of the outer lead casing (32) into four equal parts.

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