Constant-temperature tank for organic silicone oil reaction

By designing an annular jacket and water bath temperature control module on the silicone oil reactor combined with vacuum manufacturing module, the problem of external environment affecting the reaction temperature is solved, precise control and stable maintenance of the reaction temperature is achieved, and the controllability and efficiency of the reaction are improved.

CN222816833UActive Publication Date: 2025-05-02GUANGZHOU MAITIAN NEW MATERIAL TECH CO LTD
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Patent Information

Application Number
CN202421634228.1
Authority / Receiving Office
CN · China
Patent Type
Utility models(China)
Current Assignee / Owner
Filing Date
2024-07-11
Publication Date
2025-05-02
Estimated Expiration
2034-07-11

AI Technical Summary

Technical Problem

During the silicone oil reaction, the external environment can easily affect the temperature balance inside the reaction kettle, making it difficult to maintain the reaction temperature within a suitable range.

Method used

A constant temperature tank for silicone oil reaction is designed, and the components are manufactured by a ring jacket and a water bath temperature control assembly combined with a vacuum. The inner cavity of the ring jacket is vacuumed through a vacuum pump, and the temperature is insulated and insulated by vacuum, and the temperature of the reactor is accurately controlled by a water pump and an electric heating rod.

Benefits of technology

The stable maintenance of the reaction temperature of the reactor is achieved, the holding time of constant temperature is extended, the silicone oil reaction is ensured to be carried out within the appropriate temperature range, and the controllability and efficiency of the reaction are improved.

✦ Generated by Eureka AI based on patent content.

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Abstract

The utility model discloses a constant temperature tank for organic silicone oil reaction, which comprises a reaction kettle, an annular jacket surrounding the middle section of the surface of the outer ring of the reaction kettle, and a water bath temperature control component fixed on the left side of the annular jacket, and a vacuum manufacturing component is arranged on the surface of the right side of the annular jacket. According to the utility model, the annular jacket with a hollow structure is designed in the middle section of the surface of the organic silicone oil reaction kettle, the water bath temperature control assembly and the vacuum manufacturing assembly are matched, the vacuum pump is used for vacuumizing the inner cavity of the annular jacket, and the heat insulation effect of a vacuum environment is utilized, so that the reaction temperature of the reaction kettle is maintained; the holding time of the constant temperature is prolonged; after the silicone oil reaction temperature is lower than a set threshold value, cold water is conveyed into the jacket through the water pump for cooling, and meanwhile, after a heating water source of the water storage tank is conveyed to the jacket, the effect of heating a water bath outside the reaction kettle can be achieved.
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Description

Technical Field

[0001] The utility model relates to the technical field of silicone oil reaction kettles, in particular to a constant temperature tank for organic silicone oil reaction. Background Art

[0002] Silicone oil is generally a colorless, odorless, non-toxic, non-volatile liquid. It has a very small vapor pressure, a high flash point and ignition point, and a low freezing point. With the difference in the number of chain segments n, the molecular weight increases and the viscosity also increases, so silicone oil can have various viscosities. If you want to make low-viscosity silicone oil, you can use acidic clay as a catalyst and perform polymerization at a temperature of 180°C, or use sulfuric acid as a catalyst and perform polymerization at a low temperature. Alkaline catalysts can be used to produce high-viscosity silicone oil or viscous materials.

[0003] In the process of preparing silicone oil compounds, the reaction process of silicone oil needs to be maintained within a suitable temperature range. For example, when preparing low-viscosity silicone oil in a reactor, the reactor needs to be maintained at a higher temperature threshold, while when producing high-viscosity silicone oil, the reactor needs to be maintained in a lower temperature range. However, the external environment often affects the temperature balance inside the reactor, so those skilled in the art hereby propose a thermostatic tank for organic silicone oil reaction. Utility Model Content

[0004] The utility model aims to provide a thermostatic tank for organic silicone oil reaction in view of the shortcomings of the prior art, so as to solve the problems raised in the background technology.

[0005] To achieve this purpose, the utility model adopts the following technical solutions:

[0006] A thermostatic tank for organic silicone oil reaction, comprising a reactor, an annular jacket arranged around the middle of the outer ring surface of the reactor, and a water bath temperature control component fixed on the left side of the annular jacket, and a vacuum manufacturing component is arranged on the right side surface of the annular jacket;

[0007] The water bath temperature control assembly includes a servo-electrically controlled water pump fixed on the left side of the outer surface of the annular jacket, and a water storage tank fixed on the rear side of the outer surface of the annular jacket, wherein a water suction pipe penetrating into the inner cavity of the water storage tank is fixed to the water suction end of the servo-electrically controlled water pump, and a water discharge pipe penetrating into the inner cavity of the annular jacket is fixed to the water discharge end of the servo-electrically controlled water pump;

[0008] The vacuum manufacturing assembly includes a vacuum pump fixed on the right side of the outer surface of the annular jacket, a metal pipe connected to the vacuum pump end, and an end of the metal pipe away from the vacuum pump penetrates into the inner cavity of the annular jacket.

[0009] As a preferred solution of the thermostatic tank for organic silicone oil reaction, a chamber is provided inside the annular jacket for water source inside the water storage tank to enter and for the vacuum pump to draw vacuum.

[0010] As a preferred solution for a thermostatic tank for silicone oil reaction, a circular hole is provided on the left side wall of the annular jacket, a pipe joint connected to the end of the drain pipe is fixed in the circular hole, a through hole is provided on the right surface of the annular jacket, a vacuum joint connected to the end of the metal pipe is arranged inside the through hole, and a one-way valve is fixed on the end of the vacuum joint away from the metal pipe port.

[0011] As a preferred solution for the thermostatic tank for silicone oil reaction, the inner cavity of the water tank is filled with water, and a plurality of electric heating rods are linearly arranged and fixed in the inner cavity of the water tank for heating the water inside the water tank.

[0012] As a preferred solution of the thermostatic tank for organic silicone oil reaction, a water inlet pipe connected to an external water source is connected to the side wall of the outer surface of the water storage tank, and a liquid level meter is installed in the inner cavity of the water storage tank.

[0013] As a preferred solution for the thermostatic tank for silicone oil reaction, a temperature sensor and an air pressure sensor are installed on the inner cavity side wall of the annular jacket to monitor the reaction temperature transmitted from the reactor to the inside of the annular jacket and to monitor the vacuum degree inside the annular jacket.

[0014] As a preferred solution for a thermostatic tank for silicone oil reaction, the upper surface of the water tank is provided with a through hole for a water pumping pipe to pass through from top to bottom, a sealing ring cooperating with the water pumping pipe is arranged inside the through hole, and the end of the water pumping pipe passing through the inner cavity of the water tank is located below the inner cavity of the water tank.

[0015] Beneficial effects of the utility model:

[0016] The utility model designs an annular jacket with a hollow structure in the middle section of the surface of an organic silicone oil reactor, matches it with a water bath temperature control component and a vacuum manufacturing component, uses a vacuum pump to evacuate the inner cavity of the annular jacket, and uses the vacuum environment to achieve the effect of heat insulation and heat preservation, thereby maintaining the reaction temperature of the reactor and prolonging the holding time of the constant temperature; and after the silicone oil reaction temperature is lower than a set threshold, cold water is transported into the jacket by a water pump to cool it down, and at the same time, after the heated water source of the water storage tank is transported to the jacket, the effect of heating the water bath outside the reactor can be achieved. BRIEF DESCRIPTION OF THE DRAWINGS

[0017] In order to more clearly illustrate the technical solutions of the embodiments of the present utility model, the following briefly introduces the drawings required for use in the embodiments of the present utility model. Obviously, the drawings described below are only some embodiments of the present utility model, and for ordinary technicians in this field, other drawings can also be obtained based on these drawings without creative work.

[0018] Figure 1 The utility model is a structural schematic diagram of a thermostatic tank for organic silicone oil reaction.

[0019] Figure 2 It is a schematic diagram of the relevant structure of the annular jacket described in the utility model.

[0020] Figure 3 It is a schematic diagram of the cutaway structure of the annular jacket described in the utility model.

[0021] Figure 4 It is a structural schematic diagram of the vacuum manufacturing assembly described in the utility model.

[0022] Figure 5 It is a structural schematic diagram of the water bath temperature control component described in the utility model.

[0023] In the figure:

[0024] 1. Reactor; 2. Annular jacket; 3. Water bath temperature control assembly; 31. Servo electric water pump; 32. Suction pipe; 33. Drain pipe; 34. Pipe joint; 35. Water storage tank; 36. Electric heating rod; 4. Vacuum manufacturing assembly; 41. Vacuum pump; 42. Metal pipe; 43. Vacuum joint; 44. One-way valve; 5. Chamber. DETAILED DESCRIPTION

[0025] The technical solution of the utility model is further explained below with reference to the accompanying drawings and through specific implementation methods.

[0026] Among them, the drawings are only used for illustrative explanations, and they only represent schematic diagrams rather than actual pictures, and should not be understood as limitations on this patent; in order to better illustrate the embodiments of the utility model, some parts of the drawings may be omitted, enlarged or reduced, and do not represent the size of the actual product; for those skilled in the art, it is understandable that some well-known structures and their descriptions in the drawings may be omitted.

[0027] The same or similar numbers in the drawings of the embodiments of the present invention correspond to the same or similar parts; in the description of the present invention, it should be understood that if the terms "upper", "lower", "left", "right", "inner", "outer", etc. appear, the orientation or position relationship indicated is based on the orientation or position relationship shown in the drawings, which is only for the convenience of describing the present invention and simplifying the description, rather than indicating or implying that the device or element referred to must have a specific orientation, be constructed and operated in a specific orientation. Therefore, the terms describing the position relationship in the drawings are only used for illustrative purposes and cannot be understood as a limitation on this patent. For ordinary technicians in this field, the specific meanings of the above terms can be understood according to specific circumstances.

[0028] In the description of the present invention, unless otherwise clearly specified and limited, if the term "connection" or the like appears to indicate the connection relationship between components, the term should be understood in a broad sense, for example, it can be a fixed connection, a detachable connection, or an integral connection; it can be a mechanical connection or an electrical connection; it can be a direct connection or an indirect connection through an intermediate medium, it can be the internal connection of two components or the interaction relationship between two components. For ordinary technicians in this field, the specific meanings of the above terms in the present invention can be understood according to specific circumstances.

[0029] like Figures 1 to 5 As shown, this embodiment provides a thermostatic tank for silicone oil reaction, including a reactor 1, an annular jacket 2 arranged around the middle section of the outer ring surface of the reactor 1, and a water bath temperature control component 3 fixed on the left side of the annular jacket 2, and a vacuum manufacturing component 4 is arranged on the right side surface of the annular jacket 2; the water bath temperature control component 3 includes a servo-electrically controlled water pump 31 fixed on the left side of the outer surface of the annular jacket 2, and a water storage tank 35 fixed on the rear side of the outer surface of the annular jacket 2, wherein a water suction end of the servo-electrically controlled water pump 31 is fixed with a water suction pipe 32 penetrating into the inner cavity of the water storage tank 35, and a water outlet end of the servo-electrically controlled water pump 31 is fixed with a drainage pipe 33 penetrating into the inner cavity of the annular jacket 2.

[0030] The vacuum manufacturing assembly 4 includes a vacuum pump 41 fixed to the right side of the outer surface of the annular jacket 2, a metal pipe 42 connected to the vacuum end of the vacuum pump 41, and the end of the metal pipe 42 away from the vacuum pump 41 penetrates into the inner cavity of the annular jacket 2. The interior of the annular jacket 2 is provided with a chamber 5 for the water source inside the water storage tank 35 to enter and for the vacuum pump 41 to extract vacuum.

[0031] A circular hole is provided on the left side wall of the annular jacket 2, in which a pipe joint 34 connected to the end of the drain pipe 33 is fixed; a through hole is provided on the right surface of the annular jacket 2, inside of which a vacuum joint 43 connected to the end of the metal pipe 42 is provided, and a one-way valve 44 is fixed at the end of the vacuum joint 43 away from the port of the metal pipe 42.

[0032] The inner cavity of the water storage tank 35 is filled with water, and a plurality of electric heating rods 36 are linearly arranged and fixed in the inner cavity of the water storage tank 35 for heating the water inside the water storage tank 35. A water inlet pipe connected to an external water source is connected to the outer surface side wall of the water storage tank 35, and a liquid level meter is installed in the inner cavity of the water storage tank 35.

[0033] A temperature sensor and an air pressure sensor are installed on the inner side wall of the annular jacket 2 to monitor the reaction temperature transmitted from the reactor 1 to the inside of the annular jacket 2, and to monitor the vacuum degree inside the annular jacket 2. A through hole is provided on the upper surface of the water storage tank 35 for the water pumping pipe 32 to pass through from top to bottom. A sealing ring matching the water pumping pipe 32 is provided inside the through hole, and the end of the water pumping pipe 32 passing through the inner cavity of the water storage tank 35 is located below the inner cavity of the water storage tank 35.

[0034] According to the above-mentioned preferred technical solution, the workflow of the technical solution is described as follows:

[0035] When the organic silicone oil is catalytically prepared at high temperature or low temperature inside the reactor 1, the reaction temperature of the reactor 1 will be transferred to the annular jacket 2 through heat conduction. During the temperature sensor monitoring process, the vacuum pump 41 and the metal pipe 42 are used to cooperate to realize the vacuum treatment of the chamber 5 inside the annular jacket 2, and the strong heat insulation effect under the vacuum environment is used to achieve the effect of heat preservation of the reactor 1, so that the reactor 1 is kept within the reaction temperature threshold. If the temperature of the reactor 1 is too high, the vacuum environment is released by opening the pressure relief valve on the annular jacket 2, cold water is input into the water tank 35, and cold water is input into the chamber 5 by means of the servo electric control water pump 31, and the cold water is exchanged with the temperature of the reactor 1 to achieve the effect of lowering the temperature of the reactor 1. Similarly, if the temperature of the reactor 1 is too low, the water inside the water tank 35 can be heated by the electric heating rod 36, and the hot water can be input into the chamber 5 to achieve the water bath heating treatment of the reactor 1, so as to keep the reaction of the silicone oil constant in the reaction temperature range.

[0036] It should be noted that the above specific implementations are only preferred embodiments of the present invention and the technical principles used. Those skilled in the art should understand that various modifications, equivalent substitutions, changes, etc. can be made to the present invention. However, as long as these changes do not deviate from the spirit of the present invention, they should be within the scope of protection of the present invention. In addition, some terms used in the specification and claims of this application are not restrictive, but are only for the convenience of description.

Claims

1. A thermostatic tank for silicone oil reaction, characterized in that: include: A reaction kettle (1), an annular jacket (2) arranged around the middle of the outer surface of the reaction kettle (1), and a water bath temperature control component (3) fixed on the left side of the annular jacket (2), and a vacuum manufacturing component (4) is arranged on the right side surface of the annular jacket (2); The water bath temperature control component (3) comprises a servo-electrically controlled water pump (31) fixed to the left side of the outer surface of the annular jacket (2), and a water storage tank (35) fixed to the rear side of the outer surface of the annular jacket (2), wherein a water suction pipe (32) penetrating into the inner cavity of the water storage tank (35) is fixed to the water suction end of the servo-electrically controlled water pump (31), and a water discharge pipe (33) penetrating into the inner cavity of the annular jacket (2) is fixed to the water discharge end of the servo-electrically controlled water pump (31); The vacuum manufacturing assembly (4) comprises a vacuum pump (41) fixed to the right side of the outer surface of the annular jacket (2), a metal pipe (42) connected to the vacuum extraction end of the vacuum pump (41), and an end of the metal pipe (42) away from the vacuum pump (41) penetrates into the inner cavity of the annular jacket (2).

2. The thermostatic tank for silicone oil reaction according to claim 1, characterized in that: The annular jacket (2) is provided with a chamber (5) for water from the water storage tank (35) to enter and for the vacuum pump (41) to extract vacuum.

3. The thermostatic tank for organic silicone oil reaction according to claim 1, characterized in that: A circular hole is provided on the left side wall of the annular jacket (2), in which a pipe joint (34) connected to the end of the drain pipe (33) is fixed; a through hole is provided on the right side surface of the annular jacket (2), inside of which a vacuum joint (43) connected to the end of the metal pipe (42) is provided, and a one-way valve (44) is fixed at one end of the vacuum joint (43) away from the port of the metal pipe (42).

4. The thermostatic tank for organic silicone oil reaction according to claim 1, characterized in that: The inner cavity of the water storage tank (35) is filled with water, and a plurality of electric heating rods (36) are linearly arranged and fixed in the inner cavity of the water storage tank (35) for heating the water inside the water storage tank (35).

5. The thermostatic tank for organic silicone oil reaction according to claim 1, characterized in that: A water inlet pipe connected to an external water source is connected to the side wall of the outer surface of the water storage tank (35), and a liquid level meter is installed in the inner cavity of the water storage tank (35).

6. The thermostatic tank for organic silicone oil reaction according to claim 1, characterized in that: A temperature sensor and an air pressure sensor are installed on the inner cavity side wall of the annular jacket (2) for monitoring the reaction temperature transmitted from the reactor (1) to the inside of the annular jacket (2), and for monitoring the vacuum degree inside the annular jacket (2).

7. The thermostatic tank for organic silicone oil reaction according to claim 1, characterized in that: The upper surface of the water storage tank (35) is provided with a through hole for the water pumping pipe (32) to pass through from top to bottom, a sealing ring matching the water pumping pipe (32) is arranged inside the through hole, and the end of the water pumping pipe (32) passing through the inner cavity of the water storage tank (35) is located below the inner cavity of the water storage tank (35).