Reaction kettle with oil bath heating and rapid cooling functions
By designing a reactor with oil bath heating and fast cooling, the problems of uneven heat distribution and slow cooling of the existing reactors are solved, efficient heating and rapid cooling are achieved, and reaction efficiency and product quality are improved.
Patent Information
- Application Number
- CN202421845021.9
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2024-07-31
- Publication Date
- 2025-03-11
- Estimated Expiration
- 2034-07-31
AI Technical Summary
The heat distribution of existing reactors is uneven during heating and the cooling speed is slow, so they cannot respond to the rapid temperature adjustment demand during production, affecting product quality and consistency.
A reactor with oil bath heating and rapid cooling is designed, and the heating space is achieved through the oil bath heating space, heat transfer is achieved using high specific heat capacity and good heat conductivity oil, and the cooling medium is circulated in the cooling pipeline network to achieve rapid cooling.
It achieves uniform heat distribution and fast cooling speed during heating, which facilitates rapid adjustment of temperature during production, and improves reaction efficiency and product quality.
Smart Images

Figure CN222586587U_ABST
Abstract
Description
Technical Field
[0001] The utility model belongs to the technical field of reaction kettles, in particular to a reaction kettle with oil bath heating and rapid cooling. Background Art
[0002] In the fields of chemical, pharmaceutical, food processing and many other industrial production, the reactor is the core equipment, and its heating and cooling efficiency plays a vital role in the quality and production efficiency of the entire chemical reaction process. The uniform heating and rapid cooling capabilities of the reactor are key factors to ensure the smooth progress of the chemical reaction, which directly affects the quality of the product and the continuity of production.
[0003] Existing reactors often face the problem of uneven heat distribution during the heating process, which not only causes changes in chemical reaction rate and selectivity, but may also cause local overheating or insufficient temperature, thus affecting the quality and consistency of the final product. In addition, the existing cooling system also has the problem of inefficiency, slow cooling speed, and inability to respond to the rapid temperature adjustment needs during the production process in a timely manner, which is particularly evident in processes that require fine control of reaction conditions. Utility Model Content
[0004] The technical problem to be solved by the utility model is to provide a reactor with oil bath heating and rapid cooling in view of the deficiencies in the above-mentioned prior art. The heat is evenly distributed during the heating process and the cooling speed is fast, which is convenient for rapid adjustment of the temperature during the production process.
[0005] In order to solve the above technical problems, the technical solution adopted by the utility model is: a reactor with oil bath heating and rapid cooling, including a reactor body, an oil bath heating space wrapped outside the reactor body, and a cooling pipe network wrapped outside the reactor body and located in the oil bath heating space.
[0006] The reactor is heated by an oil bath heating space, which is wrapped around the outside of the reactor body. Oil circulates in it, transferring heat through the high specific heat capacity and good thermal conductivity of the oil.
[0007] An oil inlet pipe is provided at the bottom of the oil bath heating space, and an oil return pipe is provided at the top, forming an oil circulation system to ensure uniform distribution of oil temperature and improve heating efficiency.
[0008] The cooling network is located in the oil bath heating space. The cooling medium (such as cooling water) circulates in the network to quickly absorb the heat in the reactor and achieve rapid cooling.
[0009] The above-mentioned reactor with oil bath heating and rapid cooling, the oil bath heating space and the reactor body are coaxially arranged, the oil bath heating space is installed with an oil inlet pipe and an oil return pipe, the connecting point between the oil inlet pipe and the oil bath heating space is located at the bottom of the oil bath heating space, and the connecting point between the oil return pipe and the oil bath heating space is located at the top of the oil bath heating space.
[0010] The above-mentioned reaction kettle with oil bath heating and rapid cooling has two rows of gas / liquid interfaces arranged near the top of the kettle body, and a solid feeding port is arranged between the two rows of gas / liquid interfaces.
[0011] A gas / liquid interface is provided on the top of the kettle body to facilitate the discharge of gas or liquid during the reaction process. At the same time, a solid feeding port is provided between two rows of gas / liquid interfaces to facilitate the addition of solid raw materials.
[0012] The reaction kettle with oil bath heating and rapid cooling is provided with temperature sensors at the top and the bottom of the rear end surface of the kettle body.
[0013] Temperature sensors are set at the top of the kettle body and the bottom of the rear end surface to monitor the temperature in the reactor in real time. The working status of the oil bath heating and cooling pipe network is adjusted through the control system to ensure that the reaction process is carried out within the set temperature range.
[0014] The above-mentioned reaction kettle with oil bath heating and rapid cooling has an isobaric interface arranged on the rear end surface of the kettle body and a pressure sensor arranged on the top of the kettle body.
[0015] By setting up isobaric interfaces and pressure sensors, the pressure in the reactor can be monitored and controlled to ensure that the reaction is carried out under safe and stable pressure conditions. This is especially important in environments that require high or low pressure reactions.
[0016] The above-mentioned reaction kettle with oil bath heating and rapid cooling has a stirrer connected to the front end of the kettle body, a stirring paddle is arranged inside the kettle body, and the stirring paddle is transmission-connected to the stirrer.
[0017] The above-mentioned reactor with oil bath heating and rapid cooling, the stirring paddle is a plowshare spiral ribbon composite stirring paddle.
[0018] The front end of the kettle is connected to an agitator, and a stirring paddle is arranged inside. The agitator drives the stirring paddle to rotate, so as to achieve uniform stirring of the reaction materials and improve the uniformity and efficiency of the reaction.
[0019] The stirring paddle adopts a plowshare-ribbon composite design, which can more effectively mix and disperse the reactants and promote the reaction.
[0020] The above-mentioned reactor with oil bath heating and rapid cooling has a protective shell wrapped outside the oil bath heating space.
[0021] The above-mentioned reaction kettle with oil bath heating and rapid cooling has connecting frames arranged on both sides of the protective shell.
[0022] The outside of the oil bath heating space is wrapped with a protective shell to protect the oil bath heating system from the influence of the external environment and improve the safety and durability of the equipment.
[0023] Connecting frames are arranged on both sides of the protective shell to facilitate the fixing and installation of the reactor, thereby improving the stability of the equipment and the convenience of operation.
[0024] Compared with the prior art, the utility model has the following advantages: through the oil bath heating and rapid cooling mode, the material in the reaction kettle can be efficiently heated and rapidly cooled, thereby improving the reaction efficiency and product quality.
[0025] The technical solution of the utility model is further described in detail below through the accompanying drawings and embodiments. BRIEF DESCRIPTION OF THE DRAWINGS
[0026] Figure 1 It is a structural schematic diagram of the utility model.
[0027] Figure 2 It is a top view of the utility model.
[0028] Figure 3 for Figure 2 AA section view.
[0029] Figure 4 This is a schematic diagram of the structure inside the oil bath heating space.
[0030] Description of reference numerals:
[0031] 1—kettle body; 2—oil bath heating space; 3—cooling pipe network;
[0032] 4—Oil inlet pipeline; 5—Oil return pipeline; 6—Gas / liquid interface;
[0033] 7—Solid feeding port; 8—Material discharge port; 9—Temperature sensor;
[0034] 10—Isobaric interface; 11—Pressure sensor; 12—Agitator;
[0035] 13—Agitator paddle; 14—Protective casing; 15—Connecting frame. DETAILED DESCRIPTION
[0036] like Figure 1 — Figure 4 As shown, a reaction kettle with oil bath heating and rapid cooling includes a kettle body 1, an oil bath heating space 2 wrapped around the outside of the kettle body 1, and a cooling pipe network 3 wrapped around the outside of the kettle body 1 and located in the oil bath heating space 2.
[0037] In this embodiment, the oil bath heating space 2 and the kettle body 1 are coaxially arranged, and an oil inlet pipe 4 and an oil return pipe 5 are installed on the oil bath heating space 2. The connecting point between the oil inlet pipe 4 and the oil bath heating space 2 is located at the bottom of the oil bath heating space 2, and the connecting point between the oil return pipe 5 and the oil bath heating space 2 is located at the top of the oil bath heating space 2.
[0038] By coaxially arranging the oil bath heating space 2 and the kettle body 1, and rationally arranging the oil inlet pipe 4 and the oil return pipe 5, uniformity and high efficiency of oil bath heating are achieved, while ensuring the recycling of oil and improving thermal efficiency.
[0039] In this embodiment, two rows of gas / liquid interfaces 6 are provided near the top of the kettle body 1 , a solid feed port 7 is provided between the two rows of gas / liquid interfaces 6 , and a material discharge port 8 is provided at the bottom of the kettle body 1 .
[0040] A gas / liquid interface 6 and a solid feed port 7 are provided on the top of the reactor body 1 to facilitate the addition and discharge of gas / liquid materials and the addition of solid raw materials during the reaction process, thereby improving the convenience of operation and the practicality of the reactor.
[0041] In this embodiment, temperature sensors 9 are provided on the top and the bottom of the rear end surface of the kettle body 1 .
[0042] Temperature sensors 9 are arranged at the top of the kettle body 1 and the bottom of the rear end surface to monitor the temperature in the reactor in real time, ensure accurate temperature control during the reaction process, and improve the controllability of the reaction.
[0043] In this embodiment, an isobaric interface 10 is disposed on the rear end surface of the kettle body 1 , and a pressure sensor 11 is disposed on the top of the kettle body 1 .
[0044] By providing the isobaric interface 10 and the pressure sensor 11, the pressure in the reactor can be monitored and controlled to ensure that the reaction is carried out under safe and stable pressure conditions, thereby improving the safety of the reaction.
[0045] In this embodiment, the front end of the kettle body 1 is connected to a stirrer 12 , and a stirring paddle 13 is arranged inside the kettle body 1 . The stirring paddle 13 is transmission-connected to the stirrer 12 .
[0046] By connecting the stirrer 12 to the front end of the kettle body 1 and arranging a stirring paddle 13 inside, the reaction materials can be uniformly stirred, thereby improving the uniformity and efficiency of the reaction.
[0047] In this embodiment, the stirring paddle 13 is a plowshare-ribbon composite stirring paddle 13 .
[0048] The plowshare-ribbon composite stirring paddle 13 is used. This stirring paddle 13 design can more effectively mix and disperse the reaction substances, improve the stirring efficiency, and promote the reaction.
[0049] In this embodiment, the outer side of the oil bath heating space 2 is wrapped with a protective shell 14 .
[0050] The outer side of the oil bath heating space 2 is wrapped with a protective shell 14, which can protect the oil bath heating space 2 from the influence of the external environment and improve the safety and durability of the equipment.
[0051] In this embodiment, connecting frames 15 are provided on both sides of the protective shell 14 .
[0052] Connecting frames 15 are arranged on both sides of the protective shell 14 to facilitate the fixing and installation of the reactor, thereby improving the stability of the equipment and the convenience of operation.
[0053] The above is only a preferred embodiment of the present invention and does not constitute any limitation to the present invention. Any simple modification, change and equivalent structural change made to the above embodiments according to the technical essence of the present invention shall still fall within the protection scope of the technical solution of the present invention.
Claims
1. A reactor with oil bath heating and rapid cooling, characterized in that: It includes a kettle body, an oil bath heating space wrapped around the outside of the kettle body, and a cooling pipe network wrapped around the outside of the kettle body and located in the oil bath heating space; the oil bath heating space and the kettle body are coaxially arranged, an oil inlet pipe and an oil return pipe are installed on the oil bath heating space, the connecting point between the oil inlet pipe and the oil bath heating space is located at the bottom of the oil bath heating space, and the connecting point between the oil return pipe and the oil bath heating space is located at the top of the oil bath heating space.
2. A reactor with oil bath heating and rapid cooling according to claim 1, characterized in that: Two rows of gas / liquid interfaces are arranged near the top of the kettle body, and a solid feeding port is arranged between the two rows of gas / liquid interfaces.
3. A reactor with oil bath heating and rapid cooling according to claim 1, characterized in that: The top of the kettle body and the bottom of the rear end surface are both provided with temperature measuring sensors.
4. A reactor with oil bath heating and rapid cooling according to claim 1, characterized in that: The rear end surface of the kettle body is provided with an isobaric interface, and the top of the kettle body is provided with a pressure sensor.
5. A reactor with oil bath heating and rapid cooling according to claim 1, characterized in that: The front end of the kettle body is connected with a stirrer, and a stirring paddle is arranged inside the kettle body, and the stirring paddle is transmission-connected with the stirrer.
6. A reactor with oil bath heating and rapid cooling according to claim 5, characterized in that: The stirring paddle is a plowshare-ribbon composite stirring paddle.
7. A reactor with oil bath heating and rapid cooling according to claim 1, characterized in that: The outer side of the oil bath heating space is wrapped with a protective shell.
8. A reaction kettle with oil bath heating and rapid cooling according to claim 7, characterized in that: Connecting frames are arranged on both sides of the protective shell.