Continuous reaction device for air compressor oil production auxiliary agent
By designing a continuous reaction device for producing air compressor oil additives, a stirring and filtration mechanism was used to achieve continuous mixing of solid raw materials and solvents and removal of impurities. This solved the problems of low production efficiency and impurities in the existing technology, and improved production efficiency and product purity.
Patent Information
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- COOPER INTELLIGENT TECH (SHANGHAI) CO LTD
- Filing Date
- 2025-03-28
- Publication Date
- 2026-05-12
AI Technical Summary
In the existing technology, the mixing and dissolution process of air compressor oil production additives cannot achieve continuous production, resulting in low production efficiency and the presence of impurities in the product.
A continuous reaction device for producing air compressor oil additives was designed, including a reaction tank, a stirring mechanism, and a filtration mechanism. The device utilizes a drive shaft, a transmission shaft, and a scraper to achieve continuous mixing of solid raw materials and solvents, and removes impurities through filtration to ensure the continuity and purity of the production process.
It enables continuous operation of the air compressor oil production process, improves production efficiency, and effectively removes undissolved raw material residues through the filtration mechanism, ensuring that the product is pure and free of impurities, and reducing the risk of clogging.
Smart Images

Figure CN224221330U_ABST
Abstract
Description
Technical Field
[0001] This utility model relates to the field of reaction vessel technology, specifically to a continuous reaction device for air compressor oil production additives. Background Technology
[0002] Air compressor oil is a specially designed lubricant for air compressors. Its main function is to lubricate the compressor, helping to reduce friction between internal components and thus reducing wear. In addition, it has a cooling function, effectively dissipating heat generated during compression and maintaining the equipment's normal operating temperature. The production of air compressor oil requires the use of various additives, including antioxidants, which slow down oil aging and extend its service life; anti-wear agents, which reduce direct contact between mechanical parts and reduce wear; rust inhibitors, which protect metal parts from corrosion; and demulsifiers, which prevent moisture from mixing with the oil to form an emulsion that could affect oil performance.
[0003] These additives must first be dissolved in a specific solvent before being added to the engine oil. In existing processes, the solvent and additives are typically poured together into a stirred tank for mixing and dissolution. After dissolution, the product is discharged from the stirred tank, and new reactants are then poured back in for further mixing. This method cannot achieve continuous production, resulting in relatively low efficiency and the presence of dissolved impurities in the product. Therefore, a continuous reaction apparatus for producing air compressor oil additives is proposed. Utility Model Content
[0004] The technical problem solved by this utility model is to provide a continuous reaction device for producing air compressor oil additives, so as to solve the problem of low production efficiency in the prior art.
[0005] The technical solution adopted by this utility model to solve its technical problem is:
[0006] A continuous reaction apparatus for producing air compressor oil additives includes a reaction tank. An inlet is fixedly installed at the upper end of the reaction tank, and an outlet is fixedly installed on the side wall of the reaction tank. A solvent pipe is provided on the reaction tank, with its lower end located at the bottom of the reaction tank. A stirring mechanism is provided inside the reaction tank. The stirring mechanism includes a drive shaft rotatably mounted on the reaction tank and a buffer pipe fixedly mounted on the inlet. Stirring blades are fixedly mounted on the drive shaft, and a filter mechanism is fixedly installed at the upper edge of the reaction tank.
[0007] Preferably, the buffer tube has a notch, a drive shaft is fixedly installed at the end of the drive shaft, a scraper is fixedly installed at the end of the drive shaft, and a planetary reducer is located between the drive shaft and the drive shaft.
[0008] Preferably, the planetary reducer is provided with a bracket, and the planetary reducer is fixedly installed in the reaction vessel by the bracket.
[0009] Preferably, the upper end of the reaction vessel is provided with a bearing, the drive shaft is rotatably mounted on the reaction vessel through the bearing, the stirring blade is rotatably mounted inside the reaction vessel through the drive shaft, and the scraper is rotatably mounted inside the reaction vessel through the transmission shaft, with the scraper aligned with the notch on the buffer tube.
[0010] Preferably, the filtration mechanism includes a baffle plate fixedly installed inside the reaction vessel, a filter port is provided on the baffle plate, a filter screen and a retainer are fixedly installed inside the filter port, a movable shaft is rotatably installed on the retainer, a cleaning scraper is fixedly installed at the lower end of the movable shaft, a large pulley is fixedly installed at the upper end of the movable shaft, a small pulley is fixedly installed on the drive shaft, and a synchronous belt is provided between the small pulley and the large pulley.
[0011] Preferably, a bearing is provided at the middle position of the cage, and the movable shaft is rotatably mounted on the cage via the bearing.
[0012] Preferably, the filter screen is installed inside the filter port by a retainer, and the cleaning scraper is rotatably installed below the filter screen via a movable shaft, with the end of the cleaning scraper abutting against the surface of the filter screen.
[0013] The beneficial effects of this utility model are:
[0014] 1. In this application, solid raw materials are first temporarily stored in a buffer tube within the reaction vessel. As the amount of solvent in the vessel increases, a motor drives the drive shaft to rotate. Under the action of a planetary reducer, the drive shaft rotates slowly. The slow rotation of the drive shaft drives the scraper to rotate synchronously, thereby continuously scraping out the solid raw materials from the buffer tube. This process promotes the mixing of the solid raw materials and the solvent, and the drive shaft simultaneously drives the stirring blades to rotate at high speed, accelerating the dissolution and reaction process of the solid raw materials in the solvent. With the continuous injection of solvent, the reacted solution is discharged through the outlet, realizing a continuous reaction process and thus improving production efficiency.
[0015] 2. In this application, after the reaction process is completed, the solution is filtered through a filter screen inside the filter port. During filtration, the drive shaft rotates, and this rotation drives the timing belt via a small pulley, which in turn drives the large pulley. The rotational motion of the large pulley is transmitted to the movable shaft, which rotates accordingly and causes the cleaning scraper to adhere closely to the surface of the filter screen to perform a cleaning action, thereby removing undissolved material residues on the filter screen, ensuring unobstructed flow at the filter port, and reducing the probability of clogging. Attached Figure Description
[0016] Figure 1 This is a schematic diagram of the overall structure of this utility model;
[0017] Figure 2 This is a partial structural schematic diagram of the present invention;
[0018] Figure 3 This is a schematic diagram of the stirring mechanism of this utility model;
[0019] Figure 4 This is a schematic diagram of the filtration mechanism of this utility model.
[0020] The diagram is labeled as follows: 1. Reaction vessel; 2. Inlet; 3. Solvent pipe; 4. Outlet; 5. Stirring mechanism; 501. Buffer pipe; 502. Notch; 503. Drive shaft; 504. Stirring blade; 505. Planetary reducer; 506. Support; 507. Transmission shaft; 508. Scraper; 6. Filtration mechanism; 601. Baffle plate; 602. Filter port; 603. Cleaning scraper; 604. Filter screen; 605. Cage; 606. Movable shaft; 607. Large pulley; 608. Synchronous belt; 609. Small pulley. Detailed Implementation
[0021] To make the above-mentioned objects, features, and advantages of this utility model more apparent and understandable, the specific embodiments of this utility model will be described in detail below with reference to the accompanying drawings. Many specific details are set forth in the following description to provide a full understanding of this utility model. However, this utility model can be implemented in many other ways different from those described herein, and those skilled in the art can make similar modifications without departing from the spirit of this utility model. Therefore, this utility model is not limited to the specific embodiments disclosed below.
[0022] Unless otherwise defined, all technical and scientific terms used herein have the same meaning as commonly understood by one of ordinary skill in the art to which this invention pertains. The terminology used herein is for the purpose of describing particular embodiments only and is not intended to be limiting of the invention. The term "and / or" as used herein includes any and all combinations of one or more of the associated listed items.
[0023] like Figure 1 and Figure 2 As shown, this utility model provides a technical solution for a continuous reaction device for air compressor oil production additives, including a reaction tank 1, an inlet 2 fixedly installed at the upper end of the reaction tank 1, an outlet 4 fixedly installed on the side wall of the reaction tank 1, a solvent pipe 3 provided on the reaction tank 1, with the lower end of the solvent pipe 3 located at the bottom of the reaction tank 1, a stirring mechanism 5 provided inside the reaction tank 1, and a filter mechanism 6 fixedly installed at the upper edge of the reaction tank 1. The stirring mechanism 5, together with the solvent pipe 3, can realize continuous reaction, improve production efficiency, and the filter mechanism 6 can filter the solution after reaction to ensure the purity of the product.
[0024] like Figure 2 and Figure 3 As shown, the stirring mechanism 5 includes a drive shaft 503 rotatably mounted on the reaction vessel 1 and a buffer tube 501 fixedly mounted on the feed inlet 2. A stirring blade 504 is fixedly mounted on the drive shaft 503. A notch 502 is provided on the buffer tube 501. A transmission shaft 507 is fixedly mounted at the end of the drive shaft 503. A scraper 508 is fixedly mounted at the end of the transmission shaft 507. A planetary reducer 505 is located between the transmission shaft 507 and the drive shaft 503. A bracket 506 is provided on the planetary reducer 505. The planetary reducer 505 is fixedly mounted inside the reaction vessel 1 through the bracket 506.
[0025] Specifically, in the production process, solid raw materials are first fed into reaction tank 1, where they are temporarily stored in buffer tube 501. As the solvent in reaction tank 1 gradually increases, the drive shaft 503 is rotated by a motor. Under the action of planetary reducer 505, drive shaft 503 drives transmission shaft 507 to rotate at a slow and stable speed. During the rotation of transmission shaft 507, scraper 508 also rotates at a slow speed. The slow rotation of scraper 508 effectively scrapes out the solid raw materials in buffer tube 501 continuously, ensuring that the solid raw materials and solvent are fully mixed. At the same time, drive shaft 503 also drives stirring blade 504 to rotate at high speed. This high-speed rotation accelerates the dissolution process of solid raw materials in solvent, thereby speeding up the chemical reaction rate. As solvent is continuously injected, the reacted solution is smoothly discharged through outlet 4. The entire process achieves continuous operation, greatly improving production efficiency.
[0026] like Figure 2 and Figure 4 As shown, the filtration mechanism 6 includes a baffle plate 601 fixedly installed inside the reaction vessel 1. A filter port 602 is provided on the baffle plate 601. A filter screen 604 and a retainer 605 are fixedly installed inside the filter port 602. A movable shaft 606 is rotatably installed on the retainer 605. A cleaning scraper 603 is fixedly installed at the lower end of the movable shaft 606. A large pulley 607 is fixedly installed at the upper end of the movable shaft 606. A small pulley 609 is fixedly installed on the drive shaft 503. A synchronous belt 608 is provided between the small pulley 609 and the large pulley 607. A bearing is provided in the middle of the retainer 605. The movable shaft 606 is rotatably installed on the retainer 605 through the bearing.
[0027] Specifically, after the reaction process is complete, the solution needs to be discharged from the system. The discharged solution first flows through filter port 602, which contains filter screen 604. The function of filter screen 604 is to effectively filter the post-reaction solution to remove impurities and unreacted substances. During the filtration process, drive shaft 503 starts working, driving the connected small pulley 609 to rotate. As the small pulley 609 rotates, it drives the large pulley 607 via synchronous belt 608. The rotation of the large pulley 607 further drives the movable shaft 606 to rotate. The rotation of the movable shaft 606 causes the cleaning scraper 603 to rotate in close contact with the surface of filter screen 604. The function of cleaning scraper 603 is to scrape off undissolved material adhering to filter screen 604, ensuring the cleanliness of the filter screen 604 surface. Through this cleaning process, filter port 602 can be effectively kept unobstructed, thereby reducing the decrease in filtration efficiency caused by clogging and ensuring the smooth operation of the entire filtration system.
[0028] The working principle is as follows:
[0029] During operation, solid raw materials and liquid solvent are fed into reaction tank 1 through inlet 2 and solvent pipe 3, respectively. The solid raw materials fed into reaction tank 1 are temporarily stored in buffer pipe 501. As the solvent in the tank increases, the drive shaft 503 is driven to rotate by a motor. Under the action of planetary reducer 505, drive shaft 503 drives transmission shaft 507 to rotate slowly. During the slow rotation of transmission shaft 507, it drives scraper 508 to rotate slowly. During the slow rotation of scraper 508, solid raw materials in buffer pipe 501 are continuously scraped out, so that solid raw materials and solvent are mixed. At the same time, drive shaft 503 drives stirring blade 504 to rotate at high speed, so that solid raw materials are quickly dissolved in solvent for reaction. After the solvent is injected, the solution after reaction is discharged through outlet 4, realizing continuous reaction and improving production efficiency. Furthermore, when the solution after the reaction is discharged, it will pass through the filter screen 604 inside the filter port 602, thereby using the filter screen 604 to filter the solution after the reaction. During the filtration process, the drive shaft 503 will drive the small pulley 609 to rotate. When the small pulley 609 rotates, the synchronous belt 608 will drive the large pulley 607 to rotate. When the large pulley 607 rotates, it will drive the movable shaft 606 to rotate. When the movable shaft 606 rotates, it will drive the cleaning scraper 603 to rotate along the surface of the filter screen 604, thereby cleaning the undissolved raw materials adhering to the surface of the filter screen 604, keeping the filter port 602 unobstructed, and reducing the occurrence of blockage.
[0030] The specific embodiments described above further illustrate the purpose, technical solution, and beneficial effects of this utility model. It should be understood that the above descriptions are merely specific embodiments of this utility model and are not intended to limit this utility model. Any modifications, equivalent substitutions, improvements, etc., made within the spirit and principles of this utility model should be included within the protection scope of this utility model.
Claims
1. A continuous reaction apparatus for producing air compressor oil additives, comprising a reaction tank (1), wherein a feed inlet (2) is fixedly installed at the upper end of the reaction tank (1), and a discharge outlet (4) is fixedly installed on the side wall of the reaction tank (1), characterized in that: The reaction vessel (1) is provided with a solvent pipe (3), and the lower end of the solvent pipe (3) is located at the bottom of the reaction vessel (1). The reaction vessel (1) is provided with a stirring mechanism (5). The stirring mechanism (5) includes a drive shaft (503) rotatably mounted on the reaction vessel (1) and a buffer pipe (501) fixedly mounted on the feed inlet (2). A stirring blade (504) is fixedly mounted on the drive shaft (503). A filter mechanism (6) is fixedly mounted at the upper edge of the reaction vessel (1).
2. The continuous reaction apparatus for producing air compressor oil additives according to claim 1, characterized in that: The buffer tube (501) has a notch (502), the drive shaft (503) is fixedly installed with a transmission shaft (507), the transmission shaft (507) is fixedly installed with a scraper (508), and there is a planetary reducer (505) between the transmission shaft (507) and the drive shaft (503).
3. The continuous reaction apparatus for producing air compressor oil additives according to claim 2, characterized in that: The planetary reducer (505) is provided with a bracket (506), and the planetary reducer (505) is fixedly installed in the reaction vessel (1) by the bracket (506).
4. The continuous reaction apparatus for producing air compressor oil additives according to claim 3, characterized in that: The upper end of the reaction vessel (1) is provided with a bearing, the drive shaft (503) is rotatably mounted on the reaction vessel (1) through the bearing, the stirring blade (504) is rotatably mounted inside the reaction vessel (1) through the drive shaft (503), the scraper (508) is rotatably mounted inside the reaction vessel (1) through the transmission shaft (507), and the scraper (508) is aligned with the notch (502) on the buffer tube (501).
5. A continuous reaction apparatus for producing air compressor oil additives according to claim 4, characterized in that: The filtration mechanism (6) includes a baffle plate (601) fixedly installed inside the reaction vessel (1). The baffle plate (601) has a filter port (602). A filter screen (604) and a retainer (605) are fixedly installed inside the filter port (602). A movable shaft (606) is rotatably installed on the retainer (605). A cleaning scraper (603) is fixedly installed at the lower end of the movable shaft (606). A large pulley (607) is fixedly installed at the upper end of the movable shaft (606). A small pulley (609) is fixedly installed on the drive shaft (503). A synchronous belt (608) is provided between the small pulley (609) and the large pulley (607).
6. A continuous reaction apparatus for producing air compressor oil additives according to claim 5, characterized in that: The cage (605) is provided with a bearing in the middle position, and the movable shaft (606) is rotatably mounted on the cage (605) through the bearing.
7. A continuous reaction apparatus for producing air compressor oil additives according to claim 6, characterized in that: The filter screen (604) is installed in the filter port (602) by a retainer (605), and the cleaning scraper (603) is rotatably installed below the filter screen (604) by a movable shaft (606), with the end of the cleaning scraper (603) abutting against the surface of the filter screen (604).