High-capacity metering mixing tank for producing thermoplastic phenolic resin
By increasing the tank capacity and metering using weighing modules and flowmeters, combined with steam heating, the liquid level detection difficulties and blockage problems of large-scale metering equipment are solved, and efficient raw material mixing is achieved.
Patent Information
- Application Number
- CN202521338933.1
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2025-06-27
- Publication Date
- 2025-08-05
- Estimated Expiration
- 2035-06-27
AI Technical Summary
Large metering equipment has a high height, difficult liquid level detection, and it is easy to block the discharge port after mixing the raw materials.
Increase the tank capacity, use weighing modules and flowmeters to measure the material, and heat the lower end of the tank through steam to avoid clogging.
It realizes efficient metering and mixing of raw materials in the tank body, avoids the mixed material from clogging the discharge port and improves production efficiency.
Smart Images

Figure CN223184489U_ABST
Abstract
Description
Technical Field
[0001] The present application belongs to the technical field of weighing equipment, and in particular relates to a large-capacity metering mixing tank for producing thermoplastic phenolic resin. Background Art
[0002] The production of thermoplastic phenolic resin requires raw materials such as formaldehyde and phenol. During production, the materials are first measured and preliminarily mixed in the metering equipment, and then the measured and preliminarily mixed materials are transported to the reactor. Large-scale metering equipment has the following problems when measuring raw materials:
[0003] 1. Large-scale metering equipment is very high, and it is difficult to detect the liquid level using a liquid level sensor;
[0004] 2. The raw materials will become thicker after initial mixing, which may cause blockage during discharge. Utility Model Content
[0005] In order to solve the above problems, the present application provides a large-capacity metering mixing tank for producing thermoplastic phenolic resin.
[0006] The purpose of this application is to provide a large-capacity metering mixing tank for producing thermoplastic phenolic resin. This application increases the capacity of the tank body, realizes material metering through a weighing module and a flow meter, and uses steam to heat the lower end of the tank body to prevent the mixed material in the tank body from clogging the discharge pipe.
[0007] To achieve the purpose of this application, the technical solution of this application is:
[0008] A large-capacity metering mixing tank for producing thermoplastic phenolic resin comprises a tank body, an insulation layer is provided on the outer periphery of the tank body, an insulation shell is provided on the outer periphery of the insulation layer, a support platform is provided on the outer periphery of the tank body, a support seat is provided on the tank body, a weighing module is provided on the upper end of the support platform, and the lower end of the support seat is connected to the weighing module; an exhaust gas delivery pipe, a phenol delivery pipe, a formaldehyde delivery pipe and a methanol delivery pipe are provided on the upper end of the tank body, the exhaust gas delivery pipe is arranged at the center of the upper end of the tank body, the phenol delivery pipe, the formaldehyde delivery pipe and the methanol delivery pipe are arranged on the outside of the exhaust gas delivery pipe; a steam delivery pipe is provided on the tank body, and the outlet of the steam delivery pipe is arranged at the discharge port pipe at the lower end of the tank body.
[0009] Furthermore, a through hole is opened on the support platform, the tank body is inserted into the through hole, a reinforcing frame is provided at the lower end of the support platform, the upper end of the reinforcing frame is fixedly connected to the support platform, and the reinforcing frame is arranged on the periphery of the tank body.
[0010] Furthermore, metal hoses are provided on the tail gas delivery pipe, the phenol delivery pipe and the formaldehyde delivery pipe.
[0011] Furthermore, a protective convex plate is provided on the upper end of the support platform, and the protective convex plate is arranged on the periphery of the weighing module. The height of the protective convex plate is not less than half of the height of the weighing module.
[0012] Furthermore, the inner diameters of the phenol delivery pipe and the formaldehyde delivery pipe are both larger than the inner diameter of the methanol delivery pipe.
[0013] Furthermore, an inclined cylinder is provided on the shell of the tank body, and a sealing cover is provided on the cylinder body.
[0014] Furthermore, a flow meter is provided on the methanol delivery pipe, and a protective shell is provided on the periphery of the flow meter.
[0015] Furthermore, a condenser is provided on the outer periphery of the tank body, an interlayer is provided between the insulation layer and the shell of the tank body, and the condenser is connected to the interlayer through a pipeline.
[0016] Furthermore, a detection tube is provided on the tank body, and a combustible gas detection sensor and a toxic gas detection sensor are provided on the detection tube.
[0017] Furthermore, a sleeve is provided on the outer periphery of the discharge port pipe, the sleeve and the discharge port pipe form a heating cavity, and the outlet of the steam delivery pipe is connected to the heating cavity.
[0018] Compared with the prior art, the present invention has the following advantages:
[0019] 1. This application arranges a support platform on the periphery of the tank body, and has a support base on the periphery of the tank body. The weighing module on the support platform supports and weighs the liquid entering the tank body, and then calculates the volume of phenol and formaldehyde entering the tank body. The flow meter calculates the volume of methanol entering the tank body, so that the height of the tank body is increased and the capacity of the tank body is increased, and more production raw materials can be measured and mixed in the tank body at one time.
[0020] 2. The steam delivery pipe of the present application is connected to the lower end of the tank body. The steam delivered by the steam delivery pipe heats the lower end of the tank body, thereby increasing the temperature of the lower end of the tank body and preventing the mixed materials in the tank body from clogging the discharge pipe.
[0021] 3. This application uses protective convex plates to surround the weighing module, so that the tank body, the weighing module and the support platform for people to walk are separated. BRIEF DESCRIPTION OF THE DRAWINGS
[0022] The drawings in the specification, which constitute a part of this application, are used to provide further understanding of this application. The illustrative embodiments of this application and their descriptions are used to explain this application and do not constitute improper limitations on this application.
[0023] Figure 1 This is a schematic diagram of the overall structure of this application;
[0024] Figure 2 This is a schematic diagram of the top view structure of this application;
[0025] Figure 3 This is a schematic diagram of the front view structure of this application.
[0026] In the picture:
[0027] 1. Support platform, 2. Insulation shell, 3. Support base, 4. Phenol delivery pipe, 5. Formaldehyde delivery pipe, 6. Exhaust gas delivery pipe, 7. Steam delivery pipe, 8. Methanol delivery pipe, 9. Sealing cover, 10. Metal hose, 11. Protective convex plate, 12. Discharge pipe, 13. Weighing module, 14. Reinforcement frame. DETAILED DESCRIPTION
[0028] The present application will be further described below with reference to the accompanying drawings and embodiments.
[0029] It should be noted that the terms used herein are only for describing specific embodiments and are not intended to limit the exemplary embodiments according to the present application. As used herein, unless the context clearly indicates otherwise, the singular form is also intended to include the plural form. In addition, it should be understood that when the terms "comprise" and / or "include" are used in this specification, they indicate the presence of features, steps, operations, devices, components and / or combinations thereof.
[0030] In the present application, terms such as "upper", "lower", "left", "right", "front", "back", "vertical", "horizontal", "side", "bottom", etc. indicating directions or positional relationships are based on the directions or positional relationships shown in the accompanying drawings. They are merely relational words determined for the convenience of describing the structural relationships of the various parts or elements of the present application, and do not specifically refer to any part or element in the present application, and should not be understood as limitations on the present application.
[0031] Example 1
[0032] This embodiment is a large-capacity metering and mixing tank for producing thermoplastic phenolic resin. The raw materials such as formaldehyde and phenol used in the production of thermoplastic phenolic resin are measured and preliminarily mixed in the tank. According to the different amounts of formaldehyde, phenol and methanol used, a special metering method is adopted to achieve the purpose of measuring and mixing more production raw materials at one time in the tank body.
[0033] The metering mixing tank of this embodiment includes a tank body. The height of the tank body is increased to accommodate more substances such as formaldehyde and phenol. From the overall structure of the tank body, the outer periphery of the tank body of this embodiment has an insulation layer, and an insulation shell 2 is installed on the outer periphery of the insulation layer. An interlayer is provided between the insulation layer and the shell of the tank body. A condenser is installed on the outer periphery of the tank body. The condenser is connected to the interlayer through a pipeline to cool the tank body, so that the gaseous raw materials in the upper layer can be better transformed into liquid, which facilitates the transportation of the tank body materials.
[0034] Since the height of the tank body of this embodiment is increased, for example, the tank body of this embodiment spans 2 and 3 floors. Therefore, this embodiment is provided with a support platform 1 on the outer periphery of the tank body. The support platform 1 of this embodiment is a steel pedal laid on a steel platform. As a reinforcement structure, a through hole is opened on the support platform 1 and penetrates the support platform 1. The tank body is passed through the through hole. The support platform 1 is arranged in the upper half of the tank body. A reinforcement frame 14 is installed at the lower end of the support platform 1. The reinforcement frame 14 is made of square steel pipe. The upper end of the reinforcement frame 14 is fixedly connected to the support platform 1. The reinforcement frame 14 is arranged on the outer periphery of the tank body and is surrounded by 8 square steel pipes to form a regular octagonal reinforcement frame 14.
[0035] The height of the tank body of this embodiment is increased and the capacity is increased. Therefore, this embodiment uses a weighing module 13 to weigh the material entering the tank body and then measure it. Specifically, a support seat 3 is installed on the tank body, and the support seat 3 is welded to the tank body. There are three support seats 3 on the tank body, and the support seats 3 are evenly arranged around the central axis of the tank body. The weighing module 13 is installed on the upper end of the support platform 1, and the lower end of the support seat 3 is connected to the weighing module 13. In addition, a reinforcement frame 14 is located below the weighing module 13, and multiple reinforcement frames 14 are connected into a whole using square steel pipes or I-beams.
[0036] A protective convex plate 11 is welded to the upper end of the support platform 1 of this embodiment. The protective convex plate 11 is arranged on the outer periphery of the weighing module 13. The height of the protective convex plate 11 is not less than one-half of the height of the weighing module 13. For example, the height of the protective convex plate 11 in this embodiment is two-thirds of the height of the weighing module 13. This embodiment uses the protective convex plate 11 to surround the weighing module 13, so that the tank body, the weighing module 13 and the support platform 1 where people walk are separated, thereby preventing debris from entering the weighing module 13.
[0037] This embodiment has multiple feed pipes and discharge pipes 12. Specifically, an exhaust gas delivery pipe 6, a phenol delivery pipe 4, a formaldehyde delivery pipe 5 and a methanol delivery pipe 8 are installed at the upper end of the tank body, wherein the exhaust gas delivery pipe 6 is arranged at the center of the upper end of the tank body. The exhaust gas generated in the tank rises and reaches the purification equipment along the exhaust gas delivery pipe 6. The phenol delivery pipe 4, the formaldehyde delivery pipe 5 and the methanol delivery pipe 8 are feed pipes, wherein the phenol delivery pipe 4, the formaldehyde delivery pipe 5 and the methanol delivery pipe 8 are arranged on the outside of the exhaust gas delivery pipe 6. The inner diameters of the phenol delivery pipe 4 and the formaldehyde delivery pipe 5 are both larger than the inner diameter of the methanol delivery pipe 8. The inner diameters of the phenol delivery pipe 4 and the formaldehyde delivery pipe 5 are the same. A flow meter is installed on the methanol delivery pipe 8, and a protective shell is installed on the periphery of the flow meter. In this embodiment, the amount of phenol and formaldehyde is measured by a weighing module 13, and the amount of methanol is measured by a flow meter.
[0038] In this embodiment, a steam delivery pipe 7 is installed on the tank body, and the outer periphery of the steam delivery pipe 7 is covered with an insulation layer. The outlet of the steam delivery pipe 7 is arranged at the discharge port pipe at the lower end of the tank body. Specifically, a sleeve is installed on the outer periphery of the discharge port pipe, and the sleeve and the discharge port pipe form a heating cavity. The outlet of the steam delivery pipe 7 is connected with the heating cavity, and the steam delivered by the steam delivery pipe 7 enters the heating cavity to heat the discharge port pipe, thereby allowing the preliminarily mixed material to flow out of the discharge port pipe smoothly, avoiding the discharge port pipe from being blocked due to low material temperature. In addition, this embodiment can also preheat the material. In this embodiment, the interlayer can be divided into two parts, the lower end interlayer and the non-lower end interlayer, by using a partition. The steam delivery pipe 7 is connected to the lower end interlayer at the lower end of the tank body, and steam is used to preheat the material to be introduced into the discharge port pipe.
[0039] In this embodiment, a metal hose 10 is installed on the tail gas delivery pipe 6, the phenol delivery pipe 4, and the formaldehyde delivery pipe 5, and a metal hose 10 is installed on the discharge pipe 12. In addition, in this embodiment, a detection tube is installed on the tank body, and a combustible gas detection sensor and a toxic gas detection sensor are installed on the detection tube.
[0040] As a structure for maintenance and observation, an inclined cylinder is installed on the shell of the tank body, and a sealing cover 9 is installed on the cylinder body.
[0041] In this embodiment, formaldehyde and phenol are measured in the tank body, and the methanol flowing through the methanol delivery pipe 8 is measured by a flow meter. The discharge port pipe is heated by steam to prevent the discharge port pipe from being blocked by the material and to prevent the mixed material in the tank body from blocking the discharge port pipe.
[0042] The above are merely preferred embodiments of the present application and are not intended to limit the present application. Those skilled in the art will readily appreciate that various modifications and variations are possible. Any modifications, equivalent substitutions, or improvements made within the spirit and principles of the present application shall be included within the scope of protection of the present application.
[0043] Although the above describes the specific implementation methods of the present application in conjunction with the accompanying drawings, it does not limit the scope of protection of the present application. Technical personnel in the relevant field should understand that on the basis of the technical solution of the present application, various modifications or variations that can be made by technical personnel in this field without creative work are still within the scope of protection of the present application.
Claims
1. A large-capacity metering mixing tank for producing thermoplastic phenolic resin, characterized by: The tank comprises a tank body, a heat-insulating layer is arranged on the outer periphery of the tank body, and a heat-insulating shell is arranged on the outer periphery of the heat-insulating layer; A support platform is provided on the outer periphery of the tank body; The tank body is provided with a support base, the upper end of the support platform is provided with a weighing module, and the lower end of the support base is connected to the weighing module; The upper end of the tank body is provided with an exhaust gas delivery pipe, a phenol delivery pipe, a formaldehyde delivery pipe and a methanol delivery pipe, a flow meter is provided on the methanol delivery pipe, the exhaust gas delivery pipe is arranged at the center of the upper end of the tank body, and the phenol delivery pipe, the formaldehyde delivery pipe and the methanol delivery pipe are arranged on the outside of the exhaust gas delivery pipe; The tank body is provided with a steam delivery pipe, and the outlet of the steam delivery pipe is arranged at the discharge port pipe at the lower end of the tank body.
2. The large-capacity metering mixing tank for producing thermoplastic phenolic resin according to claim 1, characterized in that: The support platform is provided with a through hole penetrating the support platform, and the tank body is arranged in the through hole; A reinforcement frame is provided at the lower end of the support platform, the upper end of the reinforcement frame is fixedly connected to the support platform, and the reinforcement frame is arranged on the outer periphery of the tank body.
3. The large-capacity metering mixing tank for producing thermoplastic phenolic resin according to claim 1, characterized in that: The tail gas delivery pipe, the phenol delivery pipe and the formaldehyde delivery pipe are provided with metal hoses.
4. The large-capacity metering mixing tank for producing thermoplastic phenolic resin according to claim 1, characterized in that: A protective convex plate is provided on the upper end of the support platform and is arranged on the periphery of the weighing module. The height of the protective convex plate is not less than half of the height of the weighing module.
5. The large-capacity metering mixing tank for producing thermoplastic phenolic resin according to claim 1, characterized in that: The inner diameters of the phenol delivery pipe and the formaldehyde delivery pipe are both larger than the inner diameter of the methanol delivery pipe.
6. The large-capacity metering mixing tank for producing thermoplastic phenolic resin according to claim 1, characterized in that: The shell of the tank body is provided with an inclined cylinder body, and the cylinder body is provided with a sealing cover.
7. The large-capacity metering mixing tank for producing thermoplastic phenolic resin according to claim 1, characterized in that: A protective shell is provided on the outer periphery of the flow meter.
8. The large-capacity metering mixing tank for producing thermoplastic phenolic resin according to claim 1, characterized in that: A condenser is arranged outside the tank body, an interlayer is arranged between the heat-insulating layer and the shell of the tank body, and the condenser is connected to the interlayer through a pipeline.
9. The large-capacity metering mixing tank for producing thermoplastic phenolic resin according to claim 1, characterized in that: The tank body is provided with a detection tube, and the detection tube is provided with a combustible gas detection sensor and a toxic gas detection sensor.
10. The large-capacity metering mixing tank for producing thermoplastic phenolic resin according to claim 1, characterized in that: A sleeve is provided on the outer periphery of the discharge port pipe, the sleeve and the discharge port pipe form a heating cavity, and the outlet of the steam delivery pipe is communicated with the heating cavity.