A cooling device for glass cleaner production

Abstract

The utility model discloses a kind of cooling devices for glass cleaning agent production, including the reaction kettle for producing glass cleaning agent, further include: cooling assembly is fixed in the upper portion of reaction kettle, cooling assembly includes: for the cooling tank of infusion coolant;Fixed in the spiral pipe of cooling tank interior;Output air pipe and input air pipe are fixed in the input end of spiral pipe, reaction kettle output end is connected output air pipe by air pump, and input air pipe other end is connected with the upper portion of reaction kettle and is through-penetrating.This utility model by when glass cleaning agent is mixed in the process in reaction kettle, due to the exothermic reaction between surfactant, solvent and other raw materials and high-speed stirring cause reaction kettle internal temperature to rise, air pump starts after the high-temperature air accumulated in the upper portion of reaction kettle is extracted through the output air pipe connected, and is transported to the spiral pipe set in cooling tank interior, in the process of spiral pipe operation, high-temperature gas is fully heat exchanged with the coolant coated outside when passing through its internal flow.

Description

Technical Field

[0001] This utility model belongs to the field of glass cleaning agent production technology, and in particular relates to a cooling device for glass cleaning agent production. Background Technology

[0002] The production of glass cleaner involves adding surfactants, organic solvents (such as ethanol or isopropanol), cleaning aids, synergists, preservatives, and purified water to a reaction vessel according to a formula. Through steps such as stirring, mixing, dissolving, and stabilization, a uniform and transparent cleaning solution is produced. Its core function is to effectively remove stains, scale, and oil films from glass surfaces while maintaining a non-corrosive and residue-free cleaning effect. The entire production process requires strict control of temperature, pH value, and stirring speed to ensure stable product performance, safety, and environmental friendliness. Finally, after cooling, filtration, and aseptic filling, the finished product is obtained, suitable for various applications such as architectural glass and automotive glass.

[0003] However, existing technologies have some problems: during the production of glass cleaners, the mixing of some raw materials, such as surfactants and solvents, may undergo exothermic reactions, especially under conditions of high concentration and rapid stirring. This can cause the temperature of the reaction system to rise rapidly, resulting in the loss of volatile components such as solvents, fragrances, and preservatives, reducing the concentration of effective ingredients in the product and affecting the cleaning effect. In addition, the increase in temperature may also lead to the degradation or unstable reaction of chemical components, change the molecular structure of raw materials, and may even produce undesirable byproducts, thereby affecting the quality and safety of the product. Therefore, we propose a cooling device for the production of glass cleaners. Utility Model Content

[0004] To address the problems existing in the prior art, this utility model provides a cooling device for the production of glass cleaning agents.

[0005] This invention is implemented as follows: a cooling device for producing glass cleaning agent includes a reaction vessel for producing glass cleaning agent, and further includes a cooling assembly fixed to the upper part of the reaction vessel. The cooling assembly includes: a cooling tank for injecting coolant; a spiral tube fixed inside the cooling tank; an output gas pipe and an input gas pipe fixed to the input end of the spiral tube. The output end of the reaction vessel is connected to the output gas pipe via an air pump, and the other end of the input gas pipe is connected and communicates with the upper part of the reaction vessel. In use, the air pump is driven to draw high-temperature air from the upper part of the reaction vessel and transmit it to the spiral tube. The coolant inside the cooling tank performs liquid cooling on the gas passing through the spiral tube and transmits it back to the reaction vessel through the input gas pipe.

[0006] As a preferred embodiment of the present invention, the reactor includes a reactor body, a support plate for connecting to an indoor support structure is fixedly connected to the outside of the reactor body, and a reactor cover is fixedly installed on the upper part of the reactor body.

[0007] As a preferred embodiment of this invention, a motor is fixedly installed on the upper part of the reactor lid, and the output end of the motor is fixedly connected to a rotating shaft rotatably installed inside the reactor body. A mixing paddle for stirring glass cleaning agent material is fixedly connected to the outside of the rotating shaft.

[0008] As a preferred embodiment of this invention, the cooling box is fixedly installed on the support seat on the upper part of the reactor cover, and a thermometer is fixedly installed on one side of the cooling box. During use, the thermometer is observed to monitor the temperature of the coolant inside the cooling box in real time.

[0009] As a preferred embodiment of this invention, an inlet pipe and an outlet pipe are fixedly installed at the lower part of the cooling box. Under normal conditions, the inlet pipe and the outlet pipe are sealed.

[0010] As a preferred embodiment of this invention, when the temperature of the coolant inside the cooling tank is too high, the coolant is replaced by connecting to an external coolant source through the inlet and outlet pipes.

[0011] In a preferred embodiment of this invention, the air pump is fixed to the bottom of the cooling box, and the input and output ends of the air pump are respectively connected to the output air pipe and the spiral pipe. A second rotating wheel is fixedly connected to the upper part of the rotating rod rotatably installed inside the cooling box, passing through the cooling box. The first rotating wheel fixed outside the motor output shaft is driven by the second rotating wheel. When the motor drives the mixing paddle to rotate, it synchronously drives the air pump to perform gas transmission action, thereby realizing gas liquid cooling operation.

[0012] This invention utilizes a cooling assembly located at the top of the reactor to circulate and cool the high-temperature gas generated during the production process, thereby effectively reducing the temperature of the reaction system and ensuring the stability of the glass cleaning agent's composition and production safety. Specifically, during the mixing of the glass cleaning agent in the reactor, the exothermic reaction between raw materials such as surfactants and solvents, as well as high-speed stirring, causes the internal temperature of the reactor to rise. After the air pump is started, the high-temperature air accumulated at the top of the reactor is extracted through a connected output air pipe and transported to a spiral tube located inside the cooling box. During the operation of the spiral tube, the high-temperature gas undergoes sufficient heat exchange with the coolant covering it as it flows through the tube. The coolant absorbs the heat from the gas, achieving rapid cooling and effectively reducing the gas temperature. The cooled gas is then transported back to the top of the reactor through an input air pipe connected to the output end of the spiral tube, forming a closed-loop circulation. This achieves dynamic control of the gas temperature in the reactor and avoids problems such as solvent evaporation, loss of fragrance components, or failure of preservatives caused by high temperatures. Attached Figure Description

[0013] Figure 1 This is a schematic diagram of the overall cross-sectional structure provided in an embodiment of the present utility model;

[0014] Figure 2 This is provided by the embodiment of the present utility model. Figure 1 Schematic diagram of the structure at point A in the middle;

[0015] Figure 3 This is a schematic cross-sectional view of the cooling box provided in an embodiment of the present invention;

[0016] Figure 4 This is a schematic diagram of the cooling box structure provided in another embodiment of the present invention.

[0017] In the diagram: 1. Support plate; 2. Cooling assembly; 3. Reactor body; 4. Reactor cover; 5. Motor; 6. Shaft; 7. Mixing paddle;

[0018] 201. Output air pipe; 202. Input air pipe; 203. Cooling box; 204. Spiral tube; 205. Thermometer; 206. Support base; 207. Water inlet pipe; 208. Water outlet pipe; 209. First rotating wheel; 210. Second rotating wheel; 211. Rotating rod. Detailed Implementation

[0019] To further understand the utility model content, features and effects of this utility model, the following embodiments are provided, and detailed descriptions are given in conjunction with the accompanying drawings.

[0020] The structure of this utility model will now be described in detail with reference to the accompanying drawings.

[0021] like Figures 1 to 4 As shown in the figure, the present invention provides a cooling device for producing glass cleaning agent, including a reaction vessel for producing glass cleaning agent, and further including: a cooling assembly 2 fixed on the upper part of the reaction vessel, the cooling assembly 2 including: a cooling tank 203 for filling with coolant; a spiral tube 204 fixed inside the cooling tank 203; an output gas pipe 201 and an input gas pipe 202 fixed at the input end of the spiral tube 204, the output end of the reaction vessel is connected to the output gas pipe 201 through a gas pump, and the other end of the input gas pipe 202 is connected and communicates with the upper part of the reaction vessel. In use, the gas pump is driven to draw high-temperature air from the upper part of the reaction vessel and transmit it to the spiral tube 204. The coolant inside the cooling tank 203 performs liquid cooling on the gas passing through the spiral tube 204 and transmits it back to the reaction vessel through the input gas pipe 202.

[0022] The aforementioned cooling device for glass cleaning agent production circulates and cools the high-temperature gas generated during the production process through a cooling component 2 located at the top of the reactor, thereby effectively reducing the temperature of the reaction system and ensuring the stability of the glass cleaning agent's components and production safety. Specifically, during the mixing of the glass cleaning agent in the reactor, the internal temperature of the reactor rises due to the exothermic reaction between raw materials such as surfactants and solvents, as well as high-speed stirring. After the air pump is started, the high-temperature air accumulated at the top of the reactor is extracted through the connected output air pipe 201 and transported to the spiral tube 204 located inside the cooling box 203. During the operation of the spiral tube 204, the high-temperature gas undergoes sufficient heat exchange with the coolant covering it as it flows through it, and the coolant absorbs the heat from the gas to achieve rapid cooling. This effectively lowers the gas temperature. The cooled gas is then transferred back to the upper part of the reactor through the input gas pipe 202 connected to the output end of the spiral tube 204, forming a closed-loop circulation. This achieves dynamic control of the gas temperature in the reactor and avoids problems such as solvent evaporation, loss of fragrance components, or failure of preservatives caused by high temperatures. At the same time, the design of the spiral tube 204 structure can improve heat exchange efficiency and increase the contact area between the gas and the coolant, thereby improving the cooling effect, ensuring the temperature constantness of the reaction process, and thus improving the production quality and product stability of the glass cleaning agent. It is especially suitable for temperature-sensitive cleaning agent formulation systems, effectively preventing problems such as raw material degradation, side reactions, or product failure caused by high temperatures. It is a cooling solution with a reasonable structure, high cooling efficiency, and safe recycling.

[0023] In this embodiment, the reactor includes a reactor body 3. A support plate 1 for connecting to an indoor support structure is fixedly connected to the outside of the reactor body 3. A reactor cover 4 is fixedly installed on the upper part of the reactor body 3. A motor 5 is fixedly installed on the upper part of the reactor cover 4. The output end of the motor 5 is fixedly connected to a rotating shaft 6 rotatably installed inside the reactor body 3. A mixing paddle 7 for stirring glass cleaning agent material is fixedly connected to the outside of the rotating shaft 6.

[0024] The reactor consists of a reactor body 3 and a reactor cover 4 mounted on it. A support plate 1 is installed on the outside of the reactor body 3. The support plate 1 is used to fix the reactor to the indoor support structure to ensure the stability and safety of the equipment during operation. A motor 5 is installed on the upper part of the reactor cover 4. The output end of the motor 5 is connected to a rotating shaft 6 arranged inside the reactor body 3 through a coupling or direct connection to realize the transmission of power.

[0025] A mixing paddle 7 is fixed on the rotating shaft 6. The mixing paddle 7 rotates at high speed under the drive of the motor 5. It is used to stir and mix the glass cleaning agent raw materials added inside the reactor, so that the components are fully integrated and evenly distributed, thereby improving the reaction efficiency and product consistency. This structural design ensures the stable transmission of hybrid power and the efficient stirring of the liquid system, while also providing heat exchange conditions for the subsequent cooling process.

[0026] In this embodiment, a cooling box 203 is fixedly installed on a support base 206 fixed to the upper part of the reactor cover 4. A thermometer 205 is fixedly installed on one side of the cooling box 203. During use, the thermometer 205 is observed to monitor the temperature of the coolant inside the cooling box 203 in real time. An inlet pipe 207 and an outlet pipe 208 are fixedly installed at the lower part of the cooling box 203. Under normal conditions, the inlet pipe 207 and the outlet pipe 208 are sealed. When the temperature of the coolant inside the cooling box 203 is too high, the coolant is replaced by connecting to an external coolant source through the inlet pipe 207 and the outlet pipe 208.

[0027] The cooling box 203 is fixed to the upper part of the reactor cover 4 by the support 206, achieving integrated installation with the reaction device. A thermometer 205 is installed on one side of the cooling box 203 to monitor the temperature of the coolant in the box in real time. During the operation of the device, the operator can read the value displayed by the thermometer 205 to determine the cooling efficiency and whether the coolant needs to be replaced.

[0028] The bottom of the cooling tank 203 is equipped with an inlet pipe 207 and an outlet pipe 208 for the circulation and replacement of coolant. When the coolant temperature rises and the heat exchange efficiency decreases, new coolant can be introduced by opening the inlet pipe 207, while the overheated or ineffective old coolant is discharged through the outlet pipe 208, ensuring that the interior of the cooling tank 203 is always maintained in an ideal low-temperature environment, thereby ensuring the efficient cooling capacity of the gas in the spiral tube 204.

[0029] When not in operation, the inlet and outlet water pipes 208 are sealed by plugging to prevent coolant leakage and improve the safety and reliability of the device operation.

[0030] In another embodiment, the air pump is fixed at the bottom of the cooling box 203, and the input end and output end of the air pump are respectively connected to the output air pipe 201 and the spiral pipe 204. The upper part of the rotating rod 211, which is rotatably installed inside the cooling box 203, passes through the cooling box 203 and is fixedly connected to the second rotating wheel 210. The first rotating wheel 209, which is fixed outside the output shaft of the motor 5, is driven by the second rotating wheel 210. When the motor 5 drives the mixing paddle 7 to rotate, it synchronously drives the air pump to perform gas transmission action to realize gas liquid cooling operation.

[0031] The gas pump is located at the bottom of the cooling box 203. Its input end is connected to the output gas pipe 201 to extract high-temperature gas from the top of the reactor. Its output end is connected to the spiral tube 204 located in the cooling box 203 to send the extracted gas into the spiral tube 204 for cooling.

[0032] The gas is cooled by the heat exchange between the spiral tube 204 and the coolant inside the cooling box 203 and then returned to the reactor from the other end. The gas pump is driven by the rotating rod 211 inside the cooling box 203. The upper part of the rotating rod 211 extends out of the cooling box 203 and is equipped with a second rotating wheel 210. At the same time, the first rotating wheel 209 is installed on the output shaft of the motor 5. The two are linked by belt drive.

[0033] While driving the mixing paddle 7 to stir, the motor 5 synchronously drives the rotating rod 211 to rotate through the pulley linkage structure, thereby indirectly driving the air pump to operate and realizing the automatic synchronous gas circulation cooling function. This design can complete the gas pumping and liquid cooling operation without additional control devices, improving the integration and energy efficiency of the overall system, and has the advantages of compact structure and coordinated operation.

[0034] The working principle of this utility model:

[0035] During use, the high-temperature gas generated during the production process is circulated and cooled by the cooling component 2 located at the top of the reactor, thereby effectively reducing the temperature of the reaction system and ensuring the stability of the glass cleaning agent's composition and production safety. Specifically, when the glass cleaning agent is mixed in the reactor, the internal temperature of the reactor rises due to the exothermic reaction between raw materials such as surfactants and solvents, as well as high-speed stirring. After the air pump is started, the high-temperature air accumulated at the top of the reactor is extracted through the connected output air pipe 201 and transported to the spiral tube 204 located inside the cooling box 203. During the operation of the spiral tube 204, the high-temperature gas undergoes sufficient heat exchange with the coolant covering it as it flows through it. The coolant absorbs the heat of the gas to achieve rapid cooling, effectively reducing the gas temperature. The cooled gas is then transported back to the top of the reactor through the input air pipe 202 connected to the output end of the spiral tube 204, forming a closed-loop circulation. This achieves dynamic control of the gas temperature in the reactor and avoids problems such as solvent evaporation, loss of fragrance components, or failure of preservatives caused by high temperature.

[0036] It should be noted that, in this document, relational terms such as "first" and "second" are used only to distinguish one entity or operation from another, and do not necessarily require or imply any such actual relationship or order between these entities or operations. Furthermore, the terms "comprising," "including," or any other variations thereof are intended to cover non-exclusive inclusion, such that a process, method, article, or apparatus that comprises a list of elements includes not only those elements but also other elements not expressly listed, or elements inherent to such process, method, article, or apparatus.

[0037] Although embodiments of the present invention have been shown and described, it will be understood by those skilled in the art that various changes, modifications, substitutions and alterations can be made to these embodiments without departing from the principles and spirit of the present invention, the scope of which is defined by the appended claims and their equivalents.

Claims

1. A cooling apparatus for producing glass cleaning agent, comprising a reaction vessel for producing glass cleaning agent, characterized in that, Also includes: A cooling assembly (2) fixed to the upper part of the reactor, the cooling assembly (2) comprising: Cooling tank (203) for filling coolant; The spiral tube (204) is fixed inside the cooling box (203); An output gas pipe (201) and an input gas pipe (202) are fixed at the input end of the spiral tube (204). The output end of the reactor is connected to the output gas pipe (201) via a gas pump. The other end of the input gas pipe (202) is connected to the upper part of the reactor. In use, the air pump is driven to draw high-temperature air from the top of the reactor and transmit it to the spiral tube (204). The coolant inside the cooling box (203) performs liquid cooling on the gas passing through the spiral tube (204) and transmits it back to the reactor through the input air pipe (202).

2. The cooling device for producing a glass cleaning agent according to claim 1, wherein: The reactor includes a reactor body (3), a support plate (1) for connecting with an indoor support structure is fixedly connected to the outside of the reactor body (3), and a reactor cover (4) is fixedly installed on the upper part of the reactor body (3).

3. The cooling device for producing a glass cleaner according to claim 2, wherein: A motor (5) is fixedly installed on the upper part of the reactor cover (4). The output end of the motor (5) is fixedly connected to a rotating shaft (6) that is rotatably installed inside the reactor body (3). A mixing paddle (7) for stirring glass cleaning agent material is fixedly connected to the outside of the rotating shaft (6).

4. The cooling device for producing a glass cleaner according to claim 2, wherein: The cooling box (203) is fixedly installed on the support base (206) on the upper part of the reactor cover (4), and a thermometer (205) is fixedly installed on one side of the cooling box (203). When in use, the thermometer (205) is observed to monitor the temperature of the coolant inside the cooling box (203) in real time.

5. The cooling device for producing a glass cleaner according to claim 4, wherein: The lower part of the cooling box (203) is fixedly equipped with a water inlet pipe (207) and a water outlet pipe (208). The inlet pipe (207) and outlet pipe (208) are sealed.

6. The cooling device for producing a glass cleaning agent according to claim 5, wherein: When the temperature of the coolant inside the cooling tank (203) is too high, the coolant is replaced by connecting to an external coolant source through the inlet pipe (207) and outlet pipe (208).

7. The cooling device for producing a glass cleaner according to claim 3, wherein: The air pump is fixed to the bottom of the cooling box (203), and the input and output ends of the air pump are respectively connected to the output air pipe (201) and the spiral pipe (204). The upper part of the rotating rod (211) rotatably installed inside the cooling box (203) passes through the cooling box (203) and is fixedly connected to the second rotating wheel (210). The first rotating wheel (209) fixed outside the output shaft of the motor (5) is driven by the second rotating wheel (210). When the motor (5) drives the mixing paddle (7) to rotate, it synchronously drives the air pump to perform gas transmission action, thereby realizing gas liquid cooling operation.

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