DTS non-scaling pipeline machining equipment

By designing DTS non-scaling pipeline processing equipment, the automated process of pipeline nanocoating, drying and storage is realized, and the problems of complex construction processes and low efficiency in the existing technology are solved, and production efficiency is improved and costs are reduced.

CN222490795UActive Publication Date: 2025-02-18米标科技有限公司
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Patent Information

Application Number
CN202421169589.3
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-05-27
Publication Date
2025-02-18
Estimated Expiration
2034-05-27

AI Technical Summary

Technical Problem

In the production of existing pipelines, the nanocoat construction process is complex and has low efficiency, which cannot meet the production needs of enterprises, resulting in production limits and high costs.

Method used

Design a DTS non-scaling pipeline processing equipment, including a storage part, a filling part, a drying part and aggregation part, to realize nanocoating, drying and storage of the pipeline through an automated process, and simplify the construction process.

Benefits of technology

The automated production of pipeline nanocoats is realized, the construction process is simplified, the production efficiency is improved, and the production cost is reduced.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model relates to the technical field of pipeline coating processing equipment, in particular to DTS non-scaling pipeline processing equipment. Comprising a material storage part, a filling part for applying a coating to the interior of a pipeline, a drying part and a material collecting part are sequentially arranged in the discharging direction of the material storage part, the drying part drives the pipeline to linearly move and generates upward high-temperature gas, and the pipeline is pushed to enter the material collecting part to be stored after being dried; the discharging direction of the storage part and the discharging direction of the drying part are respectively provided with a track used for turning over the pipeline by 90 degrees; the device can effectively realize the construction operation of the nano coating of the pipeline, form a complete operation process, simplify the construction procedure and improve the production efficiency.
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Description

Technical Field

[0001] The utility model relates to the technical field of pipeline coating processing equipment, in particular to DTS non-scaling pipeline processing equipment. Background Art

[0002] In pipeline production, for the nano-coating construction process inside the pipeline, during the construction process, a phased production method is still used with multiple equipment and a large number of construction personnel. The overall process is complicated, the technical requirements for the operators are high, the processing efficiency is slow, and it cannot adapt to the production requirements of the company at the current stage, which limits the production volume of the overall pipeline. In addition, the phased processing method is adopted, manual transfer is required in the middle, the site occupies a large area, and the operation is complicated, which increases the production cost of the company and is not conducive to development. Utility Model Content

[0003] The technical problem to be solved by the utility model is to provide a DTS non-scaling pipeline processing equipment for the above-mentioned technical deficiencies, which can effectively realize the nano-coating construction operation on the pipeline, form a complete operation process, simplify the construction process, and improve production efficiency.

[0004] In order to solve the above technical problems, the technical solution adopted by the utility model includes:

[0005] The material storage section has a filling section for applying coating to the inside of the pipeline, a drying section and a collecting section in sequence along the discharge direction of the material storage section. The drying section drives the pipeline to move linearly and generates upward high-temperature gas, which pushes the pipeline into the collecting section for storage after drying. The discharge directions of the material storage section and the drying section are both provided with tracks for turning the pipeline 90 degrees.

[0006] Preferably, a residual liquid collecting device for recovering the nano solution is provided in the drying section.

[0007] Preferably, the filling part is provided with a liquid supply tank.

[0008] Preferably, the drying section comprises a support and a fan; a plurality of conveyor belts are provided inside the support; and a plurality of fans are provided and are arranged respectively below the support to generate an upward airflow.

[0009] Preferably, a collecting tank is provided below the bracket.

[0010] Preferably, the filling part comprises a base and a plurality of combined liquid supply parts; a rotatable column is provided above the base, and a plurality of clamping parts are provided along the axial direction of the column; and the plurality of combined liquid supply parts are installed above the column and arranged in a circle.

[0011] Preferably, the clamping portion is in a circular ring structure.

[0012] Compared with the prior art, the utility model has the following advantages:

[0013] 1. Through the cooperation of the material storage department and the filling department, a complete production line for pipeline transportation, coating, drying and storage is formed, without manual participation in the middle. Compared with traditional operations, it effectively simplifies the construction process and improves production efficiency;

[0014] 2. The drying section is divided into multiple processing stages. Each stage is designed according to parameters to form a combination of specific temperature and pipeline displacement speed, forming three stages: primary air drying and shaping, low and high temperature drying, and final air cooling, which effectively completes the drying process of the pipeline and improves the utilization efficiency of hot air. BRIEF DESCRIPTION OF THE DRAWINGS

[0015] Figure 1 It is a schematic diagram of the overall structure of a DTS non-scaling pipeline processing equipment;

[0016] Figure 2 It is a schematic diagram of the connection between the filling part and the storage part;

[0017] Figure 3 It is a schematic diagram of the drying section structure;

[0018] Figure 4 This is a connection diagram at the liquid supply tank;

[0019] Figure 5 This is a schematic diagram of the filling unit structure.

[0020] In the figure: 1. material storage part; 2. filling part; 3. drying part; 4. material collection part; 5. track; 7. residual liquid collecting device; 8. liquid supply tank; 201. base; 202. combined liquid supply part; 203. column; 204. clamping part; 301. bracket; 302. fan; 303. conveyor belt; 304. collecting trough. DETAILED DESCRIPTION

[0021] In order to make the purpose, technical solution and advantages of the utility model clearer, the utility model is further described in detail below in combination with specific implementation methods and with reference to the accompanying drawings. It should be understood that these descriptions are only exemplary and are not intended to limit the scope of the utility model. In addition, in the following description, the description of well-known structures and technologies is omitted to avoid unnecessary confusion of the concept of the utility model.

[0022] Specific implementation method 1: Combination Figure 1-5As shown, a DTS non-scaling pipeline processing equipment comprises: a storage part 1, a filling part 2, a drying part 3 and a collecting part 4 are arranged in sequence from the discharge direction of the storage part 1, and a track 5 for conveying and feeding the pipeline is installed between the filling part 2 and the drying part 3. The feeding track 5 drives the horizontally placed pipeline to rotate 90 degrees to be arranged vertically, and enters the filling part 2. After the nano coating is applied in the filling part 2, it enters the drying part 3 for high-temperature drying treatment, and then is conveyed to the collecting part 4 for storage by the unloading track 5.

[0023] A preferred embodiment, in combination with Figure 4 As shown, for the liquid supply operation of the filling part 2, a liquid supply tank 8 is installed at the filling part 2. The nano solution is stored in the liquid supply tank 8, and is connected to the liquid outlet of the filling part 2 by a pipeline under the drive of the liquid supply pump to realize the transportation of the solution. At the same time, during the linear displacement of the pipeline along the drying part 3, the dripping nano solution is collected and transmitted to the residual liquid collection device 7 through the pipeline to realize recycling and reuse, improve utilization rate, and reduce production cost. The residual liquid collection device 7 is installed in the liquid supply tank 8, and the structure is compact.

[0024] In a preferred embodiment, in order to ensure the smooth use of the nano solution, a filter is added to the liquid supply tank 8 and the residual liquid collection device 7. The filter itself has multiple through holes, which can filter the solution when it passes through, avoiding larger particles from clogging the filling part 2 or affecting the recovery and reuse of the residual liquid.

[0025] A preferred embodiment, in combination with Figure 1 As shown, the discharge direction of the storage section 1 and the discharge direction of the drying section 3 are both provided with tracks 5 for turning the pipeline 90 degrees. The track 5 at the storage section 1 is used to receive the pipeline placed horizontally inside the storage section 1, and drive the pipeline to turn 90 degrees to a vertical state and enter the filling section 2. The track 5 at the drying section 3 receives the pipeline in a vertical state after drying, and turns it 90 degrees to a horizontal state to be transmitted to the collecting section 4.

[0026] A preferred embodiment, in combination with Figure 3 As shown, the drying section 3 includes a bracket 301 and a fan 302; the bracket 301 has a channel for the pipeline to pass through, and multiple groups of conveyor belts 303 are horizontally installed inside the channel, and the conveyor belts 303 are driven by a motor; multiple groups of fans 302 are used, and are respectively arranged below the bracket 301, and the air outlet of the fan 302 generates an upward airflow; wherein, each group of conveyor belts 303 is two conveyor belts 303 arranged opposite to each other, and two groups are used for the upper and lower parts, after the pipeline enters, the upper and lower parts of the pipeline can be clamped at the same time, and it can be driven to move, and during the displacement of the pipeline, the hot air dries the solution inside the pipeline.

[0027] A preferred embodiment, in combination with Figure 3As shown, in order to improve the drying effect, four fans 302 are used and driven by four sections of conveyor belts 303. According to the discharge direction of the filling part 2, the No. 1 fan 302 generates cold air as the primary air drying and shaping of the pipeline, and the No. 2 and No. 3 fans 302 generate hot air, and the temperature difference between the front and back does not exceed five degrees. At the same time, the temperature of the No. 3 fan is higher than that of the No. 2 fan. When the pipeline passes through, the temperature of the No. 2 fan is relatively low, and the temperature rises after reaching the No. 3 fan, thereby forming a low-temperature drying stage and a high-temperature drying stage, relying on the change in temperature to improve the quality of the finished product after the solution is dried, and the No. 4 fan 302 continues to generate cold air to cool the dried pipeline; at the same time, for the transmission speed, the conveyor belt speed at the No. 1 fan 302 is faster, which is convenient for grabbing the pipeline at the filling part 2, and the No. 2 to No. 4 fans are relatively slow, which can increase the drying time, and can shorten the distance between the two pipelines under the fast transportation of the No. 1 conveyor belt 303, thereby increasing the number of pipelines dried by hot air at the same time.

[0028] In a preferred embodiment, as shown in the figure, in order to facilitate the collection of dripping solution and reduce production costs, a semicircular collection tank 304 is welded under the bracket 301, and the lower part of one end of the collection tank 304 is connected to the residual liquid collection device 7 to achieve recycling.

[0029] A preferred embodiment, in combination with Figure 3 and Figure 4 As shown, the filling part 2 includes a base 201 and a plurality of combined liquid supply parts 202; a rotatable column 203 is provided above the base 201, the column 203 is driven by a motor, and a plurality of clamping parts 204 are provided along the axial direction of the column 203 for fixing the pipeline; the plurality of combined liquid supply parts 202 are installed above the column 203 and arranged in a circular shape, and a liquid outlet corresponds to the top of each pipeline, and the solution is injected into the interior of the pipeline through the liquid outlet to realize the coating operation inside the pipeline.

[0030] A preferred embodiment, in combination with Figure 5 As shown, the clamping portion 204 is in a circular ring structure, and can realize pipeline transportation by rotation, and the layout is reasonable.

[0031] A preferred embodiment, in combination with Figure 5 As shown, the combined liquid supply part 202 is connected to the liquid supply tank 8 through a pipeline, and the solution is supplied under the drive of the liquid supply pump. At the same time, the combined liquid supply part 202 rotates synchronously with the clamping part 204, so as to ensure that each liquid outlet remains synchronized with the pipeline. When supplying liquid, two small balls slightly larger than the inner diameter of the pipeline are used. The two small balls enter the pipeline one after the other, and there is a nano solution between the two small balls. Under the push of air pressure, the internal coating operation of the pipeline is realized, the solution usage is less, the coating is more uniform, and the processing efficiency is faster.

[0032] A production process of DTS non-scaling pipeline processing equipment comprises the following steps:

[0033] S1. Place an appropriate amount of pipes in the material storage section 1, transport them to the discharge port through the material storage section 1, and the pipes are turned over by the feeding track 5 to enter the filling section 2 in a vertical state;

[0034] S2, during the circular rotation of the pipe driven by the filling part 2, a nano solution coating is applied to the inside of the pipe, and the pipe enters the drying part 3;

[0035] S3, the drying section 3 drives the pipeline to move linearly and dries the solution. The dried pipeline is transported by the track 5 to the collecting section 4 for storage.

[0036] It should be understood that the above specific embodiments of the present invention are only used to illustrate or explain the principles of the present invention, and do not constitute a limitation of the present invention. Therefore, any modification, equivalent replacement, improvement, etc. made without departing from the spirit and scope of the present invention should be included in the protection scope of the present invention.

Claims

1. A DTS non-scaling pipeline processing equipment, characterized in that: include: The material storage section has a filling section for applying coating to the inside of the pipeline, a drying section and a collecting section in sequence along the discharge direction of the material storage section. The drying section drives the pipeline to move linearly and generates upward high-temperature gas, which pushes the pipeline into the collecting section for storage after drying. The discharge directions of the material storage section and the drying section are both provided with tracks for turning the pipeline 90 degrees.

2. A DTS non-scaling pipeline processing equipment according to claim 1, characterized in that: The drying part is provided with a residual liquid collecting device for recovering the nano solution.

3. A DTS non-scaling pipeline processing equipment according to claim 1, characterized in that: The filling part is provided with a liquid supply tank.

4. A DTS non-scaling pipeline processing equipment according to claim 1, characterized in that: The drying section comprises a support and a fan; a plurality of conveyor belts are arranged inside the support; and a plurality of fans are used and are arranged respectively under the support to generate upward airflow.

5. A DTS non-scaling pipeline processing equipment according to claim 4, characterized in that: A collecting tank is provided below the bracket.

6. The DTS non-scaling pipeline processing equipment according to claim 1, characterized in that: The filling part comprises a base and a plurality of combined liquid supply parts; a rotatable column is arranged above the base, and a plurality of clamping parts are arranged along the axis direction of the column; the plurality of combined liquid supply parts are installed above the column and arranged in a circle.

7. A DTS non-scaling pipeline processing equipment according to claim 6, characterized in that: The clamping portion is in a circular ring structure.

Citation Information

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