Pipeline mixer for oil phase production
By designing a pipeline mixer for oil phase production including a mixing box, feed pipe and discharge pipe, using multiple buffering and mixing treatments, the problem of insufficient oil and liquid mixture in oil phase production is solved, and the mixing efficiency and quality are improved.
Patent Information
- Application Number
- CN202421758578.9
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-07-24
- Publication Date
- 2025-05-23
- Estimated Expiration
- 2034-07-24
AI Technical Summary
During the oil phase production process, the existing oil and liquid raw materials are transported and collected through multiple pipelines, and the mixture is insufficient, affecting the product quality.
A pipeline mixer for oil phase production is designed, including a mixing box, a first feed pipe, a second feed pipe and a discharge pipe. By providing the end of the second feed pipe, the stair-type turning structure of the first mixing plate and the second mixing plate, and the screw feeding member, multiple buffering and mixing of the grease liquid are realized.
Through multiple buffering and mixing treatments, the mixing efficiency between oil and grease liquids in oil phase production is significantly improved, the mixing quality is ensured, and the problem of insufficient mixing in traditional methods is solved.
Smart Images
Figure CN222889718U_ABST
Abstract
Description
Technical Field
[0001] The present application relates to the technical field of oil phase production, and specifically discloses a pipeline mixer for oil phase production. Background Art
[0002] The oil phase refers to a liquid substance composed of one or more oils. When producing and processing the oil phase, it is necessary to mix the production raw materials of a variety of different oil liquids to obtain the desired oil phase.
[0003] In the oil phase production process, since the production raw materials are liquid substances, pipelines are usually used to transport and process the oil liquid raw materials. However, the existing oil liquid is transported through multiple pipelines and finally collected in a container. The purpose of mixing the oil liquid raw materials by collecting them in the container is easily caused by insufficient mixing, which affects the product quality of the oil phase production. Therefore, in view of this, the inventor provides a pipeline mixer for oil phase production to solve the above problems. Utility Model Content
[0004] The utility model aims to solve the problem that the quality of oil phase products is affected by insufficient mixing of oil liquid raw materials in traditional oil phase production.
[0005] In order to achieve the above-mentioned purpose, the basic scheme of the utility model provides a pipeline mixer for oil phase production, comprising a mixing box, a first feed pipe obliquely connected to the top of the mixing box and a second feed pipe vertically connected to the side of the first feed pipe, a discharge pipe is provided at the bottom of the mixing box, the bottom of the discharge pipe is detachably connected to the container, the end of the second feed pipe is inserted into and installed in the first feed pipe, the end of the first feed pipe is inserted into and installed in the mixing box, a baffle plate located in the first feed pipe is provided on one side of the end of the second feed pipe away from the first feed pipe, a first mixing plate for receiving the grease liquid flowing out of the end of the first feed pipe is provided on the inner wall of one side of the mixing box, a second mixing plate for receiving the grease liquid flowing out of the end of the first mixing plate is provided on the inner wall of the other side of the mixing box, the end of the second mixing plate is located directly above the discharge pipe, a spiral feeder for mixing and discharging the grease liquid flowing out of the end of the second mixing plate is installed in the discharge pipe, and a buffer structure for blocking the flow of grease liquid is provided on both the first mixing plate and the second mixing plate.
[0006] The principles and effects of this basic solution are:
[0007] 1. Compared with the prior art, the utility model sets the end of the second feed pipe to be connected with the first feed pipe, and the grease liquid introduced into the two pipes is converged at the end of the first feed pipe and discharged into the mixing box, which is convenient for the preliminary mutual mixing of different grease liquids. The first mixing plate and the second mixing plate are set in a staircase-like turning between the first feed pipe and the discharge pipe, and buffer structures are respectively set on the first mixing plate and the second mixing plate, so that the oil phase production raw materials are conveniently transported layer by layer in the mixing box in an orderly manner, which not only reduces the conveying speed of the grease liquid raw materials, but also increases the contact mixing time between different grease liquids, and buffers and mixes the grease liquid twice in succession. By setting a spiral feeding piece, it is convenient to further mix and convey the grease liquid in the discharge pipe, thereby realizing the buffering and mixing of the grease liquid flowing in the mixing box and the discharge pipe four times in succession, which greatly improves the mixing efficiency between the grease liquids during oil phase production, ensures the mixing quality of the grease liquid, and solves the problem that the grease liquid raw materials in the traditional oil phase production are not sufficiently mixed, which affects the quality of the oil phase product.
[0008] Furthermore, the first mixing plate and the second mixing plate both adopt a corrugated structure. By adopting the corrugated structure, the process of the grease liquid flowing on the first mixing plate and the second mixing plate is more tortuous, which is convenient for mixing the grease liquid.
[0009] Furthermore, the buffer structure includes a plurality of buffer corrugated blocks evenly arranged on the first mixing plate and the second mixing plate. By arranging the buffer corrugated blocks on the surfaces of the first mixing plate and the second mixing plate, the amplitude of the fluctuations of the grease liquid during the flow process is further increased, so that the mixing effect of the grease liquid is better.
[0010] Furthermore, the spiral feeder comprises a mounting cross bar disposed at the top of the discharge pipe and located below the end of the second mixing plate, a first spiral blade disposed at one end of the bottom of the mounting cross bar, and a second spiral blade disposed at the other end of the bottom of the mounting cross bar. By arranging the first spiral blade and the second spiral blade hung on the mounting cross bar at the top of the discharge pipe, it is convenient to perform spiral diversion when the grease liquid is discharged from the mixing box into the discharge pipe, and then perform spiral mixing of the raw materials respectively after the diversion, further enhancing the mixing strength, ensuring that the grease liquid has sufficient mixing processing time and processing steps, and improving the mixing quality of the grease liquid.
[0011] Furthermore, the first spiral blade and the second spiral blade have opposite spiral directions. By setting the first spiral blade and the second spiral blade to spiral in opposite directions, it is not only convenient for the first spiral blade and the second spiral blade to mix the grease liquid raw material separately, but also convenient for bidirectional driving and mixing of the grease liquid raw material in the gap between the first spiral blade and the second spiral blade, so that the grease liquid raw material is mixed more fully.
[0012] Furthermore, the ratio of the length of the first mixing plate to the length of the second mixing plate is less than 1. By setting the length relationship between the first mixing plate and the second mixing plate, the transportation and circulation of the grease liquid is facilitated, and blockage in the mixing box is avoided. BRIEF DESCRIPTION OF THE DRAWINGS
[0013] In order to more clearly illustrate the technical solutions in the embodiments of the present application, the drawings required for use in the description of the embodiments will be briefly introduced below. Obviously, the drawings described below are only some embodiments of the present application. For those skilled in the art, other drawings can be obtained based on these drawings without creative work.
[0014] Figure 1 A structural stereogram of a pipeline mixer for oil phase production proposed in an embodiment of the present application is shown;
[0015] Figure 2 The structure front view of a pipeline mixer for oil phase production proposed in an embodiment of the present application is shown;
[0016] Figure 3 A structural stereogram of a first mixing plate of a pipeline mixer for oil phase production proposed in an embodiment of the present application is shown. DETAILED DESCRIPTION
[0017] In order to further explain the technical means and effects adopted by the present invention to achieve the predetermined purpose of the utility model, the specific implementation method, structure, characteristics and effects of the present invention are described in detail below in combination with the accompanying drawings and preferred embodiments.
[0018] The figure marks in the drawings of the specification include: mixing box 1, first feed pipe 2, second feed pipe 3, discharge pipe 4, flow blocking arc plate 5, first mixing plate 6, second mixing plate 7, buffer corrugated block 8, mounting cross bar 9, first spiral blade 10, second spiral blade 11.
[0019] A pipeline mixer for oil phase production, for example Figure 1 As shown: it includes a mixing box 1, a first feed pipe 2 connected to the top of the mixing box 1 at an angle, and a second feed pipe 3 connected to the side of the first feed pipe 2 at a vertical angle. A discharge pipe 4 is provided at the bottom of the mixing box 1, and the bottom of the discharge pipe 4 is detachably connected to the container. Figure 2As shown, the end of the second feed pipe 3 is inserted into and installed in the first feed pipe 2, and the end of the first feed pipe 2 is inserted into and installed in the mixing box 1. The left side of the end of the second feed pipe 3 away from the first feed pipe 2 is provided with a flow-blocking arc plate 5 located in the first feed pipe 2, and the left inner wall of the mixing box 1 is provided with a first mixing plate 6 for receiving the grease liquid flowing out of the end of the first feed pipe 2, and the right inner wall of the mixing box 1 is provided with a second mixing plate 7 for receiving the grease liquid flowing out of the end of the first mixing plate 6. The end of the second mixing plate 7 is located directly above the discharge pipe 4, and a spiral feeding member for mixing and discharging the grease liquid flowing out of the end of the second mixing plate 7 is installed in the discharge pipe 4. The first mixing plate 6 and the second mixing plate 7 are both provided with a buffer structure for blocking the flow of the grease liquid.
[0020] Among them, Figure 3 As shown, the first mixing plate 6 and the second mixing plate 7 both adopt a corrugated structure. Figure 1 and Figure 3 As shown, the buffer structure includes a plurality of buffer corrugated blocks 8 evenly arranged on the first mixing plate 6 and the second mixing plate 7. The length ratio of the first mixing plate 6 to the second mixing plate 7 is less than 1.
[0021] Among them, Figure 2 As shown, the spiral feeding member includes a mounting cross bar 9 disposed at the top of the discharge pipe 4 and below the end of the second mixing plate 7, a first spiral leaf 10 disposed at the left end of the bottom of the mounting cross bar 9, and a second spiral leaf 11 disposed at the right end of the bottom of the mounting cross bar 9. The first spiral leaf 10 and the second spiral leaf 11 have opposite rotation directions.
[0022] Among them, when there are only two kinds of oil liquid raw materials for the oil phase to be produced, only one pipeline mixer structure is needed. When there are more than two kinds of oil liquid raw materials, only one or more pipeline mixers need to be installed on the first feed pipe 2 and the second feed pipe 3 of a pipeline mixer respectively to carry out multi-pipeline, multi-layer and multiple mixing production.
[0023] In the specific implementation process of the utility model, when there are two kinds of grease liquid raw materials for oil phase production, the two different grease liquid raw materials need to be respectively introduced into the first feed pipe 2 and the second feed pipe 3, and the grease liquid in the first feed pipe 2 directly falls on the first mixing plate 6 in the mixing box 1, while the grease liquid in the second feed pipe 3 falls on the first feed pipe 2 and is first mixed with the grease liquid in the first feed pipe 2, and then falls on the first mixing plate 6. After the first mixing, the grease liquid falls on the first mixing plate 6 and then undergoes secondary mixing on the first mixing plate 6 with a height difference, and then flows along the inclined direction of the first mixing plate 6. During the flow process, Due to the setting of the buffer corrugated block 8, the grease liquid after the secondary mixing flows step by step on the first mixing plate 6, thereby realizing the third mixing. As the grease liquid flows to the left end of the first mixing plate 6 and falls on the second mixing plate 7, similarly, the grease liquid falling on the second mixing plate 7 and flowing on the second mixing plate 7 completes the fourth mixing and the fifth mixing. Then the grease liquid falls from the right end of the second mixing plate 7 on the mounting cross bar 9 and the first spiral leaf 10 and the second spiral leaf 11 to flow in a spiral manner, thereby completing the sixth mixing. Finally, the grease liquid is discharged into the container through the discharge pipe 4 for collection, thereby realizing the mixing treatment of the grease liquid raw material.
[0024] Compared with the prior art, the utility model provides a second feed pipe 3 that is connected to the first feed pipe 2, and the grease liquid introduced into the two pipes is converged at the end of the first feed pipe 2 and discharged into the mixing box 1, which is convenient for preliminary mutual mixing of different grease liquids. The first mixing plate 6 and the second mixing plate 7 are arranged in a staircase-like turning between the first feed pipe 2 and the discharge pipe 4, and buffer structures are respectively arranged on the first mixing plate 6 and the second mixing plate 7, which is convenient for orderly conveying the oil phase production raw materials layer by layer in the mixing box 1, which not only reduces the grease liquid raw materials, but also reduces the grease liquid raw materials. The conveying speed is improved, and the contact and mixing time between different grease liquids is increased. The grease liquid is buffered and mixed twice in succession. By setting a spiral conveying piece, it is convenient to further mix and convey the grease liquid in the discharge pipe 4, thereby achieving four times of buffering and mixing of the grease liquid flowing in the mixing box 1 and the discharge pipe 4, which greatly improves the mixing efficiency between the grease liquids during oil phase production, ensures the mixing quality of the grease liquid, and solves the problem of insufficient mixing of grease liquid raw materials in traditional oil phase production, affecting the quality of the oil phase product.
[0025] The above description is only a preferred embodiment of the present invention and does not constitute any form of limitation to the present invention. Although the present invention has been disclosed as a preferred embodiment as above, it is not intended to limit the present invention. Any technical personnel in this field can make some changes or modify the technical contents disclosed above into equivalent embodiments without departing from the scope of the technical solution of the present invention. However, any brief modifications, equivalent changes and modifications made to the above embodiments based on the technical essence of the present invention without departing from the content of the technical solution of the present invention are still within the scope of the technical solution of the present invention.
Claims
1. A pipeline mixer for oil phase production, characterized in that: The invention comprises a mixing box, a first feed pipe obliquely connected to the top of the mixing box and a second feed pipe vertically connected to the side of the first feed pipe, a discharge pipe is provided at the bottom of the mixing box, the bottom of the discharge pipe is detachably connected to the container, the end of the second feed pipe is inserted into and installed in the first feed pipe, the end of the first feed pipe is inserted into and installed in the mixing box, a baffle plate located in the first feed pipe is provided on the side of the end of the second feed pipe away from the first feed pipe, a first mixing plate for receiving the grease liquid flowing out of the end of the first feed pipe is provided on the inner wall of one side of the mixing box, a second mixing plate for receiving the grease liquid flowing out of the end of the first mixing plate is provided on the inner wall of the other side of the mixing box, the end of the second mixing plate is located directly above the discharge pipe, a spiral feeding piece for mixing and discharging the grease liquid flowing out of the end of the second mixing plate is installed in the discharge pipe, and a buffer structure for blocking the flow of grease liquid is provided on both the first mixing plate and the second mixing plate.
2. A pipeline mixer for oil phase production according to claim 1, characterized in that: The first mixing plate and the second mixing plate both have a corrugated structure.
3. A pipeline mixer for oil phase production according to claim 2, characterized in that: The buffer structure comprises a plurality of buffer corrugated blocks which are evenly arranged on the first mixing plate and the second mixing plate respectively.
4. A pipeline mixer for oil phase production according to claim 3, characterized in that: The spiral feeding member comprises a mounting cross bar arranged at the top of the discharge pipe and below the end of the second mixing plate, a first spiral leaf arranged at one end of the bottom of the mounting cross bar, and a second spiral leaf arranged at the other end of the bottom of the mounting cross bar.
5. A pipeline mixer for oil phase production according to claim 4, characterized in that: The first helical lobe and the second helical lobe have opposite rotation directions.
6. A pipeline mixer for oil phase production according to claim 5, characterized in that: The ratio of the length of the first mixing plate to the length of the second mixing plate is less than 1.