A continuous production and drying mechanism for chlorovinyl resin with a scattering and breaking device
Patent Information
- Application Number
- CN202522159374.4
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2025-10-13
- Publication Date
- 2026-09-15
- Estimated Expiration
- 2035-10-13
AI Technical Summary
1、本实用新型中,解决了初水分高流动性差易结块的物料高效、连续干燥的难题,采用两级干燥串联方式,在并流输送过程中完成团块破碎以及热量和质量的传递,干燥过程极快。
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Figure CN224757467U_ABST
Abstract
Description
Technical Field
[0001] This utility model relates to the field of chloroacetic acid resin production technology, and in particular to a drying mechanism for continuous production of chloroacetic acid resin with a dispersing and crushing device. Background Technology
[0002] Chlorinated vinyl acetate resins are typically dried using airflow drying equipment, a continuous drying system that utilizes high-speed hot airflow to rapidly dry wet materials. The drying medium dries solid particles in a fluidized state, essentially through the boiling of the powder. During drying, the gas and solid phases come into countercurrent contact and are violently agitated. The solid particles are suspended in the drying medium, resulting in a large contact surface area and excellent performance in heat transfer, mass transfer, volumetric drying intensity, and thermal efficiency. It is widely used in the chemical, food, pharmaceutical, feed, and mining industries. Its core principle is the rapid evaporation and removal of moisture from the material through direct contact between hot air and the material. Due to its adaptability to various materials, small footprint, large production capacity, high thermal efficiency, easy operation control, and low particle breakage, it is widely used in large-scale chemical production. The continuous production drying mechanism for vinyl chloride-vinyl acetate copolymer resin includes drying devices such as a limiting tank, drying plate, servo motor one, striking rod, drying lamp, and moving plate. It also includes an extraction pipe, servo motor two, rotating rod two, and conveyor belt. The sedimentation tank contains a treatment device for alkali treatment of the vinyl chloride-vinyl acetate copolymer resin. Additionally, it may be equipped with a structure similar to a dispersant, including a high-speed rotating rotor. The main function of this drying mechanism is to react and polymerize the raw materials through components such as the reaction vessel and polymerization vessel. After alkali treatment in the sedimentation tank, the vinyl chloride-vinyl acetate copolymer resin is dehydrated and dried using the drying device in the drying chamber. Simultaneously, the dispersant crusher impacts and shears the agglomerated material, pulverizing and reducing it to ensure the drying effect and quality of the material, thus achieving continuous production of vinyl chloride-vinyl acetate resin. Airflow drying devices are typically cylindrical structures, offering advantages such as high single-unit capacity, low energy consumption, high automation, minimal human intervention, and low equipment and civil engineering investment. However, they can only dry small, uniformly sized particles with good flowability. They struggle to handle materials that are prone to sticking and have poor flowability. Due to the structural characteristics of airflow drying systems, in traditional production processes, materials are usually fed via a screw conveyor. During the pushing process by the screw blades, materials, especially those with stickiness and a tendency to accumulate, easily agglomerate, reducing drying efficiency and affecting finished product quality. The impact on the thermal stability of the material is particularly significant. To address these issues, a continuous production drying mechanism for chloroacetic acid resin with a dispersing and crushing device is proposed. Utility Model Content
[0003] To overcome the above shortcomings, this utility model provides a drying mechanism for the continuous production of chloroacetic acid resin with a dispersing and crushing device, which aims to improve the problem of easy clumping.
[0004] To achieve the above objectives, the present invention adopts the following technical solution: a drying mechanism for continuous production of chloroacetic acid resin with a crushing and dispersing device, comprising a drying chamber, an air inlet at one end of the drying chamber, an air outlet at the other end of the drying chamber, and a crusher fixedly connected to the inside of the drying chamber.
[0005] As a further description of the above technical solution: A temperature measuring point is fixedly connected to the outside of the drying chamber, and a feeding auger is fixedly connected to the left side of the crusher.
[0006] As a further description of the above technical solution: The drying chamber has multiple cleaning holes on its outer side.
[0007] As a further description of the above technical solution: A pressure measuring point is fixedly connected to the outside of the drying chamber.
[0008] As a further description of the above technical solution: The air inlet and the air outlet are connected.
[0009] As a further description of the above technical solution: The feed auger is fixedly connected to the inside of the drying chamber.
[0010] As a further description of the above technical solution: The temperature measuring point is located to the right of the pressure measuring point.
[0011] As a further description of the above technical solution: A cleaning cover is installed on the front side of the cleaning hole.
[0012] This utility model has the following beneficial effects: 1. This utility model solves the problem of efficient and continuous drying of materials with high initial moisture content, poor fluidity, and easy agglomeration. It adopts a two-stage drying series method, which completes the agglomeration and heat and mass transfer during the parallel flow conveying process, and the drying process is extremely fast.
[0013] 2. This utility model has the advantages of low scrap rate, large single-machine output, low energy consumption, high degree of automation, long equipment operation cycle and low labor and civil engineering investment. Attached Figure Description
[0014] Figure 1This is a three-dimensional schematic diagram of a drying mechanism for the continuous production of chloroacetic acid resin with a dispersing and crushing device proposed in this utility model.
[0015] Legend: 1. Air inlet; 2. Cleaning hole; 3. Crusher; 4. Feed screw conveyor; 5. Drying chamber; 6. Temperature measuring point; 7. Pressure measuring point; 8. Air outlet. Detailed Implementation
[0016] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments. Obviously, the described embodiments are only some embodiments of the present utility model, and not all embodiments. Based on the embodiments of the present utility model, all other embodiments obtained by those of ordinary skill in the art without creative effort are within the protection scope of the present utility model.
[0017] Reference Figure 1 This utility model provides an embodiment of a continuous production drying mechanism for chloroacetic acid resin with a dispersing and crushing device. The mechanism includes a drying chamber 5, which serves as the main space of the entire mechanism, providing a closed working environment for the drying and crushing process of the chloroacetic acid resin. One end of the drying chamber 5 has an air inlet 1 for introducing hot air or a drying medium to provide the airflow required for drying. The other end of the drying chamber 5 has an air outlet 8 for discharging moisture and waste gas generated during the drying process, maintaining airflow circulation within the drying chamber 5. A crusher 3 is fixedly connected to the inside of the drying chamber 5, used to disperse and crush any chloroacetic acid resin that may clump during the drying process, ensuring uniform drying of the material.
[0018] Reference Figure 1 Temperature measuring point 6 is fixedly connected to the outside of the drying chamber 5. Temperature measuring point 6 can monitor the temperature change inside the drying chamber 5 in real time and provide data support for adjusting the drying conditions. Feed screw 4 is fixedly connected to the left side of the crusher 3. Feed screw 4 is responsible for continuously and evenly conveying the chloroacetic acid resin raw material to be dried into the drying chamber 5.
[0019] Reference Figure 1 Multiple cleaning holes 2 are provided on the outside of the drying chamber 5. These cleaning holes 2 facilitate operators to regularly clean and maintain the inside of the drying chamber 5 to prevent residual materials from affecting subsequent production.
[0020] Reference Figure 1 A pressure measuring point 7 is fixedly connected to the outside of the drying chamber 5. The pressure measuring point 7 can monitor the air pressure inside the drying chamber 5 in real time to ensure that the equipment operates within a safe pressure range.
[0021] Reference Figure 1The air inlet 1 and the air outlet 8 are connected. This connection structure allows the drying medium to form a complete flow path inside the drying chamber 5, ensuring that the drying process continues effectively.
[0022] Reference Figure 1 The feeding screw auger 4 is fixedly connected to the inside of the drying chamber 5. This connection method allows the feeding screw auger 4 to directly feed the material into the core working area of the drying chamber 5, thereby improving the feeding efficiency.
[0023] Reference Figure 1 Temperature measuring point 6 is located to the right of pressure measuring point 7. This layout facilitates the monitoring of temperature and pressure parameters in different areas of the drying chamber 5, allowing for a more comprehensive understanding of the equipment's operating status.
[0024] Reference Figure 1 A cleaning cover is installed on the front side of the cleaning hole 2. The cleaning cover can seal the cleaning hole 2 during equipment operation to prevent the drying medium from leaking and external impurities from entering, and ensure the airtightness of the drying chamber 5.
[0025] Working Principle: When the continuous production and drying mechanism of the chloroacetic acid resin in this crushing and dispersing device is working, the chloroacetic acid resin raw material to be dried is first continuously and evenly conveyed into the drying chamber 5 through the feeding screw auger 4. Then, the hot air or drying medium required for drying enters the chamber through the air inlet 1. Under the structure of the air inlet 1 and the air outlet 8 being connected, the drying medium forms a stable flow path in the drying chamber 5, continuously contacting the chloroacetic acid resin material to remove moisture. At the same time, the moisture and waste gas generated during the drying process are discharged through the air outlet 8 at the other end of the drying chamber 5. The crusher 3, which is fixedly connected to the inside of the drying chamber 5, will break up and crush any caking chloroacetic acid resin that may occur during the drying process in real time, ensuring that the material is always in a uniformly dispersed state to improve drying efficiency and effect. The temperature measuring point 6, which is fixedly connected to the outside of the drying chamber 5, will monitor the internal temperature of the chamber in real time, while the pressure measuring point 7 will monitor the internal air pressure of the chamber simultaneously. When the equipment needs regular maintenance, the operator can open the cleaning cover installed on the front of the cleaning hole 2 and clean the inside of the chamber through the multiple cleaning holes 2 opened on the outside of the drying chamber 5 to prevent residual material from affecting subsequent production.
[0026] Finally, it should be noted that the above description is only a preferred embodiment of the present utility model and is not intended to limit the present utility model. Although the present utility model has been described in detail with reference to the foregoing embodiments, those skilled in the art can still modify the technical solutions described in the foregoing embodiments or make equivalent substitutions for some of the technical features. Any modifications, equivalent substitutions, improvements, etc., made within the spirit and principles of the present utility model should be included within the protection scope of the present utility model.
Claims
1. A drying mechanism for continuous production of chloroacetic acid resin with a crushing and dispersing device, comprising a drying chamber (5), characterized in that: The drying chamber (5) has an air inlet (1) at one end and an air outlet (8) at the other end. A crusher (3) is fixedly connected to the inside of the drying chamber (5).
2. The drying mechanism for continuous production of chloroacetic acid resin with a crushing and dispersing device according to claim 1, characterized in that: A temperature measuring point (6) is fixedly connected to the outside of the drying chamber (5), and a feeding screw conveyor (4) is fixedly connected to the left side of the crusher (3).
3. The drying mechanism for continuous production of chloroacetic acid resin with a crushing and dispersing device according to claim 1, characterized in that: Multiple cleaning holes (2) are provided on the outside of the drying chamber (5).
4. The drying mechanism for continuous production of chloroacetic acid resin with a crushing and dispersing device according to claim 1, characterized in that: A pressure measuring point (7) is fixedly connected to the outside of the drying chamber (5).
5. A drying mechanism for continuous production of chloroacetic acid resin with a dispersing and crushing device according to claim 1, characterized in that: The air inlet (1) and the air outlet (8) are connected.
6. A drying mechanism for continuous production of chloroacetic acid resin with a crushing and dispersing device according to claim 2, characterized in that: The feed auger (4) is fixedly connected to the inside of the drying chamber (5).
7. A drying mechanism for continuous production of chloroacetic acid resin with a crushing and dispersing device according to claim 2, characterized in that: The temperature measuring point (6) is located to the right of the pressure measuring point (7).
8. A drying mechanism for continuous production of chloroacetic acid resin with a dispersing and crushing device according to claim 3, characterized in that: A cleaning cover is installed on the front side of the cleaning hole (2).