Oxidation reaction device for producing colored bleaching powder
By designing an annular flow guide cavity and a water temperature mixing component in the color bleach powder production device, combined with heating and cooling components, the problem of uneven temperature inside the reactor was solved, achieving uniform cooling of materials inside the reactor, avoiding material defects, and improving production quality.
Patent Information
- Application Number
- CN202520612111.1
- Authority / Receiving Office
- CN · China
- Patent Type
- Utility models(China)
- Current Assignee / Owner
- Filing Date
- 2025-04-02
- Publication Date
- 2026-03-06
- Estimated Expiration
- 2035-04-02
AI Technical Summary
In the current production process of color bleach powder, uneven temperature control inside the reactor leads to uneven heat exchange, resulting in defects such as wrinkles and chicken claw marks on the material.
It adopts an annular flow guide cavity design inside the temperature control cylinder, combined with heating and cooling components, and achieves uniform cooling of materials in the reactor through a water temperature mixing component. It is equipped with a material stirring component and a PLC controller for temperature monitoring and adjustment.
To achieve uniform cooling of materials inside the reactor, avoid the formation of wrinkles and creases, and ensure uniform temperature control inside the reactor.
Smart Images
Figure CN223969962U_ABST
Abstract
Description
Technical Field
[0001] This utility model relates to the field of color bleach powder production and preparation technology, specifically to an oxidation reaction device for color bleach powder production. Background Technology
[0002] Color-safe bleach powder is a highly efficient oxygen-based bleaching detergent. Its main component is sodium percarbonate, which dissolves in water to generate hydrogen peroxide. This hydrogen peroxide then reacts chemically to produce nascent oxygen, which destroys the pigments in the stains, thus achieving the effects of stain removal and bleaching.
[0003] In the production of color-safe bleach, various raw materials and reaction additives need to be placed in a reactor for reaction. Initially, the materials in the reactor need to be heated to promote dynamic fusion between molecules. Heating is stopped once the materials begin to react, as the various material elements automatically generate heat during the fusion process (thermal reaction). Although the temperature rise is not very high, sustained high temperatures can damage and reduce some of the active molecules in the materials, directly affecting the final performance of the bleaching powder. Current solutions mainly involve cooling with cooling pipes. However, due to the long length of the cooling pipes surrounding the reactor, uneven heat exchange and temperature drop are prone to occur during cooling. Furthermore, the initial section of the pipes is prone to wrinkles and creases in the fluid material due to excessively rapid cooling. This makes temperature control inconvenient and hinders proper temperature balance within the reactor.
[0004] Therefore, this utility model provides an oxidation reaction device for the production of color bleach powder to solve the above-mentioned problems. Utility Model Content
[0005] The purpose of this section is to outline some aspects of the embodiments of this utility model and to briefly introduce some preferred embodiments. Simplifications or omissions may be made in this section, as well as in the abstract and title of this application, to avoid obscuring the purpose of these documents; however, such simplifications or omissions should not be used to limit the scope of this utility model.
[0006] Therefore, the purpose of this utility model is to provide an oxidation reaction device for the production of color bleach powder, so as to solve the problem mentioned in the background art that the existing color bleach powder is not very convenient in terms of temperature drop operation and the temperature inside the reactor cannot be well balanced and controlled.
[0007] To achieve the above objectives, this utility model provides the following technical solution: an oxidation reaction device for producing color bleach powder, comprising a temperature control cylinder, a reaction vessel coaxial with the temperature control cylinder, a material stirring assembly inside the reaction vessel, a circumferential flow guiding cavity between the inner radial ring and the bottom of the temperature control cylinder and the reaction vessel, a heating component and a cooling component for heating and cooling the liquid medium in the circumferential flow guiding cavity respectively provided at the bottom of the temperature control cylinder, and a water temperature mixing assembly for mixing the liquid medium in the circumferential flow guiding cavity at the bottom of the temperature control cylinder.
[0008] As a preferred embodiment of the oxidation reaction device for producing color bleaching powder according to this utility model, the material stirring assembly includes a main shaft coaxially and vertically rotatably mounted on the upper inner side of the reaction vessel, spiral blades arranged along the outer periphery and height direction of the main shaft, multiple stirring paddles arranged along the height direction of the main shaft, and a motor fixed to the top of the reaction vessel for driving the main shaft to rotate axially.
[0009] In a preferred embodiment of the oxidation reaction device for producing color bleaching powder according to this utility model, the heating component is a resistance wire heating plate, the cooling component is a semiconductor refrigeration chip, and the cooling surface of the semiconductor refrigeration chip faces the circumferential flow cavity.
[0010] As a preferred embodiment of the oxidation reaction device for producing color bleach powder according to this utility model, the water temperature mixing component includes a shaft coaxially and vertically rotatably mounted at the bottom of the temperature control cylinder, a waterproof sealing shaft located at the connection between the shaft and the temperature control cylinder, a motor II located at the bottom outer side of the temperature control cylinder for driving the shaft to rotate axially, and multiple stirring blades fixed to the outer wall of the shaft.
[0011] As a preferred embodiment of the oxidation reaction device for producing color bleaching powder according to the present invention, the outer periphery of the temperature control cylinder is also covered with a heat insulation layer, and the top of the temperature control cylinder is respectively provided with temperature sensors corresponding to the circumferential flow guide cavity and the inner cavity of the reaction vessel.
[0012] The oxidation reaction device is also equipped with a PLC controller.
[0013] In a preferred embodiment of the oxidation reaction device for producing color bleaching powder according to this utility model, a water injection valve connected to the circumferential flow guide cavity is provided on the upper outer side of the temperature control cylinder, and a drain valve connected to the circumferential flow guide cavity is provided on the lower outer side of the temperature control cylinder.
[0014] As a preferred embodiment of the oxidation reaction device for producing color bleaching powder according to this utility model, the top side of the reaction vessel is provided with a feeding port and a corresponding conveying valve cover, and the bottom side of the reaction vessel is provided with a discharge valve that extends through the outside of the temperature control cylinder.
[0015] Compared with the prior art, the beneficial effects of this utility model are as follows: When the oxidation reaction device for producing color bleach powder needs to cool down the reaction vessel and the internal materials, the cooling component is activated to rapidly cool the water in the surrounding guide cavity. At the same time, the water temperature mixing component can continuously stir the water in the guide cavity, so that the water temperature can be reduced linearly and evenly. Under this all-round water bath contact, the reaction vessel and the internal materials are also cooled evenly and linearly. At the same time, with the multiple coordination of the material stirring component, the defects such as wrinkles and claw marks caused by uneven temperature drop in traditional methods are effectively avoided, and the temperature of the contents inside the vessel is well controlled. Attached Figure Description
[0016] Figure 1 This is a schematic diagram of the overall external structure of this utility model;
[0017] Figure 2 This is a schematic diagram of the internal structure of the device of this utility model;
[0018] Figure 3 This is a schematic diagram of the water temperature mixing component of this utility model.
[0019] In the diagram: 100, Temperature control cylinder; 1001, Circular guide cavity; 110, Insulation layer; 120, Water injection valve; 130, Drain valve; 200, Reactor tank; 210, Material conveying valve cover; 220, Discharge valve; 300, Material stirring assembly; 310, Main shaft; 320, Spiral blade; 330, Stirring paddle; 340, Motor 1; 400, Heating component; 410, Cooling component; 500, Water temperature mixing assembly; 510, Shaft; 520, Waterproof sealing shaft; 530, Motor 2; 540, Stirring blade; 600, Temperature sensor. Detailed Implementation
[0020] To make the above-mentioned objectives, features and advantages of this utility model more apparent and understandable, the specific embodiments of this utility model will be described in detail below with reference to the accompanying drawings.
[0021] Secondly, this utility model is described in detail with reference to the schematic diagrams. When describing the embodiments of this utility model, for ease of explanation, the cross-sectional views showing the device structure may be partially enlarged, not according to the usual scale. Furthermore, the schematic diagrams are merely examples and should not limit the scope of protection of this utility model. In addition, in actual manufacturing, the three-dimensional spatial dimensions of length, width, and depth should be included.
[0022] To make the objectives, technical solutions, and advantages of this utility model clearer, the embodiments of this utility model will be described in further detail below with reference to the accompanying drawings.
[0023] Figures 1-3The diagram shown is a complete structural schematic of the oxidation reaction device for producing color bleach powder according to this utility model. Please refer to [link / reference]. Figures 1-3 An oxidation reaction apparatus for producing color bleach powder according to this embodiment includes a temperature control cylinder 100, a reaction vessel 200 coaxially fixed inside the temperature control cylinder 100, a material stirring assembly 300 inside the reaction vessel 200, a circumferential flow guide cavity 1001 between the inner radial ring and bottom of the temperature control cylinder 100 and the reaction vessel 200, a heating component 400 and a cooling component 410 for heating and cooling the liquid medium in the circumferential flow guide cavity 1001 respectively provided at the bottom of the temperature control cylinder 100, and a water temperature mixing assembly 500 for mixing the liquid medium in the circumferential flow guide cavity 1001 also provided at the bottom of the temperature control cylinder 100.
[0024] The material stirring assembly 300 includes a main shaft 310 coaxially and vertically rotatably mounted on the upper inner side of the reactor 200, spiral blades 320 arranged along the outer periphery and height of the main shaft 310, multiple stirring paddles 330 arranged along the height of the main shaft 310, and a motor 340 fixed to the top of the reactor 200 for driving the main shaft 310 to rotate axially. In use, the motor 340 drives the main shaft 310, spiral blades 320, and stirring paddles 330 to rotate synchronously. The spiral blades 320 continuously lift the material at the bottom of the reactor 200 upwards, creating alternating mixing with the upper material. Simultaneously, the rotating stirring paddles 330 forcefully stir and fuse the alternating vertical and radial flow of the material. This combined action not only improves the material fusion efficiency but also ensures even temperature distribution. The heating element 400 uses a resistance wire heating plate, and the cooling element 410 uses a semiconductor cooling chip, with the cooling surface of the semiconductor cooling chip facing the circumferential flow guide cavity 1001. It is understood that the resistance wire heating plate and the semiconductor cooling chip have excellent unit heating / cooling efficiency, enabling rapid heating and cooling of the water in the circumferential flow guide cavity 1001. The water temperature mixing assembly 500 includes a shaft 510 coaxially and vertically rotatably mounted at the bottom of the temperature regulating cylinder 100, a waterproof sealing shaft 520 located at the connection between the shaft 510 and the temperature regulating cylinder 100, a motor 530 located at the bottom outer side of the temperature regulating cylinder 100 for driving the shaft 510 to rotate axially, and multiple stirring blades 540 fixed to the outer wall of the shaft 510. Specifically, in this embodiment, when it is necessary to cool down the reactor 200 and the materials inside, the cooling component 410 is activated to rapidly cool the water in the circumferential guide cavity 1001. At the same time, the water temperature mixing component 500 can continuously agitate the water in the guide cavity, so that the water temperature can be reduced linearly and evenly. Under this all-round water bath contact, the reactor 200 and the materials inside are also cooled evenly and linearly. At the same time, with the multiple cooperation of the material stirring component 300, the defects such as wrinkles and claw marks caused by uneven temperature drop in traditional methods are effectively avoided.
[0025] Preferably, the outer periphery of the temperature regulating cylinder 100 is further covered with a heat insulation layer 110, and the top of the temperature regulating cylinder 100 is respectively equipped with temperature sensors 600 corresponding to the circumferential flow guide cavity 1001 and the inner cavity of the reaction vessel 200; the oxidation reaction device is also equipped with a PLC controller. It can be understood that the heat insulation layer 110 can prevent the external temperature from interfering with the water temperature in the circumferential flow guide cavity 1001. In addition, the temperature sensors 600 can monitor the water temperature in the circumferential flow guide cavity 1001 and the temperature of the material in the reaction vessel 200 in real time. The control system will accurately adjust the output power and time of the cooling components 410, etc., according to the temperature changes between the two, making the operation more reasonable.
[0026] Preferably, a water injection valve 120 connected to the circumferential flow guide cavity 1001 is provided on the upper outer side of the temperature regulating cylinder 100, and a drain valve 130 connected to the circumferential flow guide cavity 1001 is provided on the lower outer side of the temperature regulating cylinder 100. It can be understood that liquid medium can be injected into the circumferential flow guide cavity 1001 by opening the water injection valve 120, and water in the flow guide cavity can be discharged by opening the drain valve 130. Furthermore, a feeding port and a corresponding conveying valve cover 210 are provided on one side of the top of the reaction vessel 200, and a discharge valve 220 is provided on one side of the bottom of the reaction vessel 200, extending through the outer side of the temperature regulating cylinder 100. The main and auxiliary materials of color bleach powder can be added to the reaction vessel 200 by opening the conveying valve cover 210, and after the materials have completed the fusion reaction, the materials are discharged by opening the discharge valve 220.
[0027] In summary, the oxidation reaction apparatus for producing color bleach powder according to this embodiment, when it is necessary to cool down the reaction vessel 200 and the materials inside, activates the cooling component 410 to rapidly cool the water in the circumferential guide cavity 1001. At the same time, the water temperature mixing component 500 can continuously agitate the water in the guide cavity, so that the water temperature can be reduced linearly and evenly. Under this all-round water bath contact, the reaction vessel 200 and the materials inside are also cooled evenly and linearly. At the same time, with the multiple coordination of the material stirring component 300, the formation of wrinkles and chicken claw marks on the material caused by uneven temperature drop in the traditional method is effectively avoided, and the temperature of the material inside the vessel is well controlled and balanced.
[0028] Although the present invention has been described above with reference to embodiments, various modifications can be made and components can be replaced with equivalents without departing from the scope of the present invention. In particular, as long as there is no structural conflict, the features in the embodiments disclosed in this invention can be combined with each other in any way. The lack of an exhaustive description of these combinations in this specification is merely for the sake of brevity and resource conservation. Therefore, the present invention is not limited to the specific embodiments disclosed herein, but includes all technical solutions falling within the scope of the claims.
Claims
1. An oxidation reaction apparatus for producing color bleach powder, characterized in that, The application relates to a temperature-adjusting cylinder (100) internally fixed with a reaction kettle (200) coaxial with the temperature-adjusting cylinder (100), wherein a material stirring assembly (300) is arranged in the reaction kettle (200), a ring-shaped guide cavity (1001) is arranged between the bottom of the temperature-adjusting cylinder (100) and the reaction kettle (200), heating components (400) and refrigerating components (410) are arranged at the bottom of the temperature-adjusting cylinder (100) and used for heating and cooling liquid medium in the ring-shaped guide cavity (1001), and a water temperature mixing and stirring assembly (500) is arranged at the bottom of the temperature-adjusting cylinder (100) and used for mixing the liquid medium in the ring-shaped guide cavity (1001).
2. The oxidation reaction device for producing a color bleaching powder according to claim 1, characterized by: The material stirring assembly (300) comprises a main shaft (310) coaxially and vertically rotatably arranged at the upper end of the inside of the reaction kettle (200), spiral blades (320) arranged along the outer circumferential side and height direction of the main shaft (310), a plurality of stirring paddles (330) arranged along the height direction of the main shaft (310), and a motor (340) fixed to the top of the reaction kettle (200) and used for driving the axial rotation of the main shaft (310).
3. The oxidation reaction apparatus for producing a color bleaching powder according to claim 1, characterized by: The heating components (400) adopt resistance wire heating plates, the refrigerating components (410) adopt semiconductor refrigerating sheets, and the refrigerating surfaces of the semiconductor refrigerating sheets face the ring-shaped guide cavity (1001).
4. The oxidation reaction apparatus for producing a color bleaching powder according to claim 1, characterized by: The water temperature mixing and stirring assembly (500) comprises a shaft rod (510) coaxially and vertically rotatably arranged at the bottom of the temperature-adjusting cylinder (100), a waterproof sealing shaft (520) arranged at the connecting position of the shaft rod (510) and the temperature-adjusting cylinder (100), a motor (530) arranged at the bottom of the outside of the temperature-adjusting cylinder (100) and used for driving the axial rotation of the shaft rod (510), and a plurality of stirring blades (540) fixed to the outer side wall of the shaft rod (510).
5. The oxidation reaction apparatus for producing a color bleaching powder according to claim 1, characterized by: The outside of the temperature-adjusting cylinder (100) is further wrapped with a heat preservation layer (110), and temperature sensors (600) corresponding to the ring-shaped guide cavity (1001) and the inner cavity of the reaction kettle (200) are further arranged at the top of the temperature-adjusting cylinder (100). The oxidation reaction device is further provided with a PLC controller.
6. The oxidation reaction apparatus for producing a color bleaching powder according to claim 1, characterized by: A water injection valve (120) is arranged at the upper part of the outside of the temperature-adjusting cylinder (100) and communicated with the ring-shaped guide cavity (1001), and a water drainage valve (130) is arranged at the lower part of the outside of the temperature-adjusting cylinder (100) and communicated with the ring-shaped guide cavity (1001).
7. The oxidation reaction apparatus for producing a color bleaching powder according to claim 1, characterized by: A feeding port and a feeding valve cover (210) corresponding to the feeding port are arranged at one side of the top of the reaction kettle (200), and a discharging valve (220) penetrating through the outside of the temperature-adjusting cylinder (100) is arranged at one side of the bottom of the reaction kettle (200).