Multilayer diversion type chemical additive preheating tank

By using a multi-layer flow-guided chemical additive preheating tank with zoned temperature control and a heat transfer oil homogenization system, the problems of inaccurate temperature control and low thermal efficiency in existing chemical additive preheating equipment have been solved. This has enabled precise temperature control and efficient heating of chemical additives, improving heating uniformity and energy utilization.

CN224524768UActive Publication Date: 2026-07-21SHANDONG HAOYU NEW MATERIAL TECHNOLOGY CO LTD
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Patent Information

Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
SHANDONG HAOYU NEW MATERIAL TECHNOLOGY CO LTD
Filing Date
2025-08-15
Publication Date
2026-07-21

AI Technical Summary

Technical Problem

Existing chemical additive preheating equipment uses a single-layer heating structure, which leads to inaccurate temperature control and low thermal efficiency. In particular, it is prone to local overheating, coking, or decomposition of high-viscosity or heat-sensitive additives, affecting product quality and production efficiency.

Method used

A multi-layer flow-guided chemical additive preheating tank is adopted. Through the multi-layer flow-guided zone temperature control design combined with a heat transfer oil homogenization system, and by utilizing a copper heat exchange structure and an intelligent temperature control system, the chemical additives can be preheated in a step-by-step and precise manner.

Benefits of technology

It achieves precise temperature control and efficient heating of chemical additives, avoids local overheating, improves heating uniformity and energy utilization, and ensures product quality and production efficiency.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model relates to the technical field of chemical equipment, specifically disclose a multilayer flow guide formula chemical auxiliary agent preheating tank, including the jar body, the upper and lower both ends of jar body are provided with feed inlet and discharge gate, the inside of jar body is provided with inner tube, the outer wall of inner tube is fixedly connected with the inner wall of jar body and has spiral flow guide blade, the inner wall of inner tube is fixedly connected with two upper and lower distribution heat insulation board, two heat insulation board divide the inner chamber of inner tube from top to bottom into low temperature preheating chamber, constant temperature heating chamber and high temperature setting chamber, the inner wall of low temperature preheating chamber, constant temperature heating chamber and high temperature setting chamber all install the electric heating pipe of independent temperature control, the inside of low temperature preheating chamber, constant temperature heating chamber and high temperature setting chamber all fills with heat conducting oil, through multilayer flow guide subregion temperature control design combination heat conducting oil heat -equalizing system, realized the ladder type accurate preheating of chemical auxiliary agent, copper heat exchange structure cooperation intelligent temperature control has improved heating uniformity and efficiency significantly.
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Description

Technical Field

[0001] This utility model relates to the field of chemical equipment technology, and specifically discloses a multi-layer flow-guided chemical additive preheating tank. Background Technology

[0002] Chemical additives, as important components in industrial production, are widely used in plastics, rubber, coatings, and other fields. Their pretreatment process has a crucial impact on the performance of the final product. The preheating process can effectively reduce the viscosity of additives, improve their dispersibility, and ensure the stability of subsequent processes.

[0003] Existing preheating equipment mostly adopts a single-layer heating structure, which cannot perform zoned temperature control, resulting in problems such as inaccurate temperature control and low thermal efficiency. Especially for high-viscosity or heat-sensitive additives, local overheating, coking, or decomposition are prone to occur, affecting product quality and production efficiency. Therefore, a multi-layer flow-guided chemical additive preheating tank is needed to solve this problem. Summary of the Invention

[0004] This invention proposes a multi-layer flow-guided preheating tank for chemical additives. Through a multi-layer flow-guided zone temperature control design combined with a heat transfer oil homogenization system, it achieves precise step-by-step preheating of chemical additives. The copper heat exchange structure, combined with intelligent temperature control, significantly improves heating uniformity and efficiency.

[0005] This utility model is implemented as follows: a multi-layer flow-guiding chemical additive preheating tank includes a tank body, with an inlet and an outlet respectively provided at the upper and lower ends of the tank body. An inner cylinder is provided inside the tank body. Spiral guide vanes are fixedly connected between the outer wall of the inner cylinder and the inner wall of the tank body. The spiral guide vanes are wavy near the outer wall of the inner cylinder. Two heat insulation plates are fixedly connected to the inner wall of the inner cylinder, which divide the inner cavity of the inner cylinder from top to bottom into a low-temperature preheating chamber, a constant-temperature heating chamber, and a high-temperature shaping chamber. The inner walls of the low-temperature preheating chamber, the constant-temperature heating chamber, and the high-temperature shaping chamber are all equipped with independently temperature-controlled electric heating tubes. The interiors of the low-temperature preheating chamber, the constant-temperature heating chamber, and the high-temperature shaping chamber are all filled with heat-conducting oil.

[0006] As a preferred embodiment of the multi-layer flow-guided chemical additive preheating tank of this utility model, temperature sensors are provided on the inner walls of the low-temperature preheating chamber, the constant-temperature heating chamber, and the high-temperature shaping chamber.

[0007] As a preferred embodiment of the multi-layer flow-guided chemical additive preheating tank of this utility model, the outer wall of the inner cylinder is provided with a plurality of oil inlet and outlet pipes that are respectively connected to the low temperature preheating chamber, the constant temperature heating chamber and the high temperature shaping chamber and extend to the outside of the tank body, and the outer wall of the plurality of oil inlet and outlet pipes is provided with valves.

[0008] As a preferred embodiment of the multi-layer flow-guiding chemical additive preheating tank of this utility model, the outer wall of the inner cylinder is fixedly connected with spiral heat exchange fins.

[0009] As a preferred embodiment of the multi-layer flow-guiding chemical additive preheating tank of this utility model, the outer wall of the tank body is provided with a heat insulation layer.

[0010] In a preferred embodiment of this utility model, the inner cylinder and the spiral heat exchange fins are made of copper.

[0011] As a preferred embodiment of the multi-layer flow-guiding chemical additive preheating tank of this utility model, the outer wall of the tank is provided with a controller, and multiple electric heating tubes and multiple temperature sensors are electrically connected to the controller.

[0012] The beneficial effects of this utility model are:

[0013] 1. Through a multi-layer flow guiding structure and zoned temperature control design, combined with a heat transfer oil homogenization system, the chemical additives are precisely controlled in a stepwise manner from low-temperature preheating to high-temperature setting, effectively avoiding the problems of local overheating and low thermal efficiency.

[0014] 2. By utilizing the high thermal conductivity of the copper inner cylinder and spiral heat exchange fins, combined with an intelligent temperature control system, heating uniformity and energy utilization are significantly improved. Attached Figure Description

[0015] To more clearly illustrate the specific embodiments of this utility model or the technical solutions in the prior art, the drawings used in the description of the specific embodiments or the prior art will be briefly introduced below. In all the drawings, similar elements or parts are generally identified by similar reference numerals. In the drawings, the elements or parts are not necessarily drawn to scale.

[0016] Figure 1 This is an overall structural diagram of a multi-layer flow-guiding preheating tank for chemical additives according to this utility model.

[0017] Figure 2 This is a left sectional view of a multi-layer flow-guided chemical additive preheating tank according to the present invention.

[0018] Figure 3 This is a diagram showing the internal structure of a multi-layer flow-guided preheating tank for chemical additives according to this utility model.

[0019] The markings in the diagram are: 1. Tank body; 2. Inlet; 3. Outlet; 4. Inner cylinder; 5. Spiral guide vane; 6. Heat insulation plate; 601. Low temperature preheating chamber; 602. Constant temperature heating chamber; 603. High temperature shaping chamber; 7. Electric heating tube; 8. Temperature sensor; 9. Inlet and outlet oil pipes; 10. Spiral heat exchange fins. Detailed Implementation

[0020] The present invention will be further described below with reference to the accompanying drawings and specific embodiments to aid in understanding its content. Unless otherwise specified, the methods used in this invention are conventional methods; the raw materials and apparatus used, unless otherwise specified, are conventional commercially available products.

[0021] Please see Figure 1-3 A multi-layer flow-guided preheating tank for chemical additives includes a tank body 1. The tank body 1 has an inlet 2 and an outlet 3 at its upper and lower ends, respectively. An inner cylinder 4 is installed inside the tank body 1. Spiral guide vanes 5 are fixedly connected between the outer wall of the inner cylinder 4 and the inner wall of the tank body 1. The spiral guide vanes 5 are wavy near the outer wall of the inner cylinder 4. Two vertically distributed heat insulation plates 6 are fixedly connected to the inner wall of the inner cylinder 4. The two heat insulation plates 6 divide the inner cavity of the inner cylinder 4 from top to bottom into a low-temperature preheating chamber 601, a constant-temperature heating chamber 602, and a high-temperature shaping chamber 603. Each of the three chambers has an independently temperature-controlled electric heating tube 7 installed on its inner wall. The interiors of the low-temperature preheating chamber 601, the constant-temperature heating chamber 602, and the high-temperature shaping chamber 603 are filled with heat-conducting oil.

[0022] In this embodiment: the material falls slowly layer by layer under the guidance of the spiral guide vanes 5, prolonging the heat exchange time. The inner cylinder 4 is divided into a low-temperature preheating chamber 601, a constant-temperature heating chamber 602, and a high-temperature shaping chamber 603 by two heat insulation plates 6 (the heat insulation plates 6 are made of densified ceramic fiber boards with a polytetrafluoroethylene oil-resistant coating on the surface). The temperature of the low-temperature preheating chamber 601 is set at 50-80℃. The electric heating tube 7 heats the heat transfer oil, initially reducing the viscosity of the material and evaporating a small amount of moisture. The constant-temperature chamber... The temperature of the heating chamber 602 is controlled at 80-120℃ to fully activate the additives and avoid local overheating. The temperature of the high-temperature setting chamber 603 is raised to 120-160℃ to ensure that the material reaches the final process requirements for fluidity. After being fully heated, the material is discharged from the bottom outlet 3. This utility model achieves efficient and uniform preheating of chemical additives through a multi-layer flow guiding structure and the design of independently temperature-controlled low-temperature preheating chamber 601, constant-temperature heating chamber 602 and high-temperature setting chamber 603, combined with a heat transfer oil homogenization system.

[0023] As a technical optimization of this utility model, temperature sensors 8 are provided on the inner walls of the low-temperature preheating cavity 601, the constant temperature heating cavity 602, and the high-temperature shaping cavity 603.

[0024] In this embodiment, temperature sensor 8 facilitates real-time monitoring of the temperature in each chamber.

[0025] As a technical optimization of this utility model, the outer wall of the inner cylinder 4 is provided with a plurality of oil inlet and outlet pipes 9 that are respectively connected to the low temperature preheating chamber 601, the constant temperature heating chamber 602 and the high temperature shaping chamber 603 and extend to the outside of the tank body 1. Valves are provided on the outer walls of the plurality of oil inlet and outlet pipes 9.

[0026] In this embodiment: by opening the valve on the outer wall of the inlet / outlet oil pipe 9, it is convenient to replace the heat transfer oil.

[0027] As a technical optimization of this utility model, the outer wall of the inner cylinder 4 is fixedly connected with spiral heat exchange fins 10.

[0028] In this embodiment, the heat exchange efficiency is improved by fixing the spiral heat exchange fins 10 to the outer wall of the inner cylinder 4.

[0029] As a technical optimization of this utility model, the outer wall of the tank 1 is provided with a heat insulation layer.

[0030] In this embodiment: by setting an insulation layer on the outer wall of the tank 1, heat loss is reduced, thermal efficiency is improved and temperature stability is maintained, thereby reducing energy consumption and optimizing the preheating effect.

[0031] As a technical optimization of this utility model, the inner cylinder 4 and the spiral heat exchange fins 10 are made of copper.

[0032] In this embodiment, the use of a copper inner cylinder 4 and spiral heat exchange fins 10 can significantly improve thermal conductivity, accelerate heat exchange speed, enhance corrosion resistance, and extend the service life of the equipment.

[0033] As a technical optimization of this utility model, a controller is provided on the outer wall of the tank 1, and multiple electric heating tubes 7 and multiple temperature sensors 8 are electrically connected to the controller.

[0034] In this embodiment, the controller intelligently links the electric heating element 7 and the temperature sensor 8 to achieve precise temperature control and automatic adjustment of heating power.

[0035] The working principle and usage process of this utility model: Under the guidance of the spiral guide vanes 5, the material falls slowly layer by layer, extending the heat exchange time. The inner cylinder 4 is divided into a low-temperature preheating chamber 601, a constant-temperature heating chamber 602, and a high-temperature shaping chamber 603 by two heat insulation plates 6. The temperature of the low-temperature preheating chamber 601 is set at 50-80℃. The electric heating tube 7 heats the heat transfer oil, initially reducing the viscosity of the material and evaporating a small amount of water. The temperature of the constant-temperature heating chamber 602 is controlled at 80-120℃ to fully activate the additives and avoid local overheating. The temperature of the high-temperature shaping chamber 603 is raised to 120-160℃ to ensure that the material reaches the final process requirements for fluidity. After being fully heated, the material is discharged from the bottom outlet 3. This utility model, through the multi-layer guide structure and the design of independently temperature-controlled low-temperature preheating chamber 601, constant-temperature heating chamber 602, and high-temperature shaping chamber 603, combined with the heat transfer oil homogenization system, achieves efficient and uniform preheating of chemical additives.

[0036] In the description of this utility model, it should be understood that the terms "left", "right", "up", "down", "top", "bottom", "front", "back", "inner", "outer", "back", "middle", etc., indicate the orientation or positional relationship based on the orientation or positional relationship shown in the accompanying drawings. They are only for the convenience of describing this utility model and simplifying the description, and do not indicate or imply that the device or element referred to must have a specific orientation, or be constructed and operated in a specific orientation. Therefore, they should not be construed as limitations on this utility model.

[0037] However, the above description is only a specific embodiment of this utility model and should not be construed as limiting the scope of implementation of this utility model. Therefore, any substitution of equivalent components or equivalent changes and modifications made in accordance with the scope of protection of this utility model should still fall within the scope of the claims of this utility model.

Claims

1. A multi-layer flow-guided preheating tank for chemical additives, comprising a tank body (1), wherein an inlet (2) and an outlet (3) are respectively provided at the upper and lower ends of the tank body (1), characterized in that: The tank (1) is provided with an inner cylinder (4). The outer wall of the inner cylinder (4) is fixedly connected to the inner wall of the tank (1) with a spiral guide vane (5). The spiral guide vane (5) is wavy near the outer wall of the inner cylinder (4). The inner wall of the inner cylinder (4) is fixedly connected with two heat insulation plates (6) distributed vertically. The two heat insulation plates (6) divide the inner cavity of the inner cylinder (4) from top to bottom into a low temperature preheating cavity (601), a constant temperature heating cavity (602), and a high temperature shaping cavity (603). The inner walls of the low temperature preheating cavity (601), the constant temperature heating cavity (602), and the high temperature shaping cavity (603) are all equipped with independently temperature-controlled electric heating tubes (7). The interiors of the low temperature preheating cavity (601), the constant temperature heating cavity (602), and the high temperature shaping cavity (603) are all filled with heat transfer oil.

2. The multi-layer flow-guided chemical additive preheating tank according to claim 1, characterized in that: Temperature sensors (8) are provided on the inner walls of the low-temperature preheating chamber (601), the constant-temperature heating chamber (602), and the high-temperature shaping chamber (603).

3. The multi-layer flow-guided chemical additive preheating tank according to claim 1, characterized in that: The outer wall of the inner cylinder (4) is provided with a plurality of oil inlet and outlet pipes (9) that are respectively connected to the low temperature preheating chamber (601), the constant temperature heating chamber (602) and the high temperature shaping chamber (603) and extend to the outside of the tank body (1). Valves are provided on the outer walls of the plurality of oil inlet and outlet pipes (9).

4. A multi-layer flow-guiding chemical additive preheating tank according to claim 1, characterized in that: The outer wall of the inner cylinder (4) is fixedly connected with spiral heat exchange fins (10).

5. A multi-layer flow-guiding chemical additive preheating tank according to claim 1, characterized in that: The outer wall of the tank (1) is provided with a heat insulation layer.

6. A multi-layer flow-guiding chemical additive preheating tank according to claim 4, characterized in that: The inner cylinder (4) and the spiral heat exchange fins (10) are made of copper.

7. A multi-layer flow-guided chemical additive preheating tank according to claim 2, characterized in that: The outer wall of the tank (1) is equipped with a controller, and the multiple electric heating tubes (7) and multiple temperature sensors (8) are electrically connected to the controller.