Neutralization and conversion equipment for sodium caseinate production

Abstract

The utility model discloses a kind of sodium caseinate production and use neutralization conversion equipment, including neutralization conversion core part, the bottom central position of neutralization conversion core part is equipped with paddle drive assembly, the driving end of paddle drive assembly is fixed with rotary center pivot through shaft coupling, the outside of rotary center pivot is connected with flow state disturbance component, fluid release port is installed in the outside of flow state disturbance component, the top of flow state disturbance component is threadedly connected with dynamic sealing adapter, the top of dynamic sealing adapter is threadedly connected with feed channel, directional feeding conveyor is installed in one end of feed channel, the other side of neutralization conversion core part is respectively welded with fluid guide connector piece.The utility model avoids that lye is added too concentrated, prevents local over-alkali, and this kind of conversion mode not only improves conversion quality, also reduces the workload of staff.

Description

Technical Field

[0001] This utility model relates to the field of sodium caseinate production technology, specifically to a neutralization and conversion device for sodium caseinate production. Background Technology

[0002] The neutralization and conversion equipment for sodium caseinate production is a specialized chemical equipment designed for the sodium caseinate production process. By controlling the neutralization reaction conditions (such as pH value, temperature, reaction time, etc.), casein is neutralized with alkaline substances (such as sodium hydroxide) to generate soluble sodium caseinate. At the same time, the conversion, mixing, and purification of the product are completed.

[0003] However, in the existing neutralization and conversion equipment for sodium caseinate production, the washed casein is usually dispersed in water to swell, and an alkaline solution is slowly added to convert the casein into soluble sodium salt. However, when adding the alkaline solution, it is usually added manually in batches. However, this method of adding the alkaline solution too frequently can easily lead to local over-alkalinity, which not only affects the conversion quality but also increases the workload of the staff. Utility Model Content

[0004] In view of the shortcomings of the existing technology, this utility model provides a neutralization conversion device for the production of sodium caseinate to solve the existing problems.

[0005] To achieve the above objectives, this utility model provides the following technical solution: a neutralization and conversion device for sodium caseinate production, comprising a neutralization and conversion core section. A paddle drive assembly is installed at the bottom center of the neutralization and conversion core section. The drive end of the paddle drive assembly is fixed to a rotation center pivot via a coupling. A fluidization disturbance component is threadedly connected to the outer side of the rotation center pivot. A fluid release port is installed on the outer side of the fluidization disturbance component. A dynamic sealing adapter is threadedly connected to the top of the fluidization disturbance component. The top of the sealed transition device is threaded with a feed channel, one end of which is equipped with a directional feeding conveyor. On the other side of the neutralization and conversion core, fluid guiding connectors are welded. There are two fluid guiding connectors, one of which is threaded with a closed recirculation pipeline. The other end of the closed recirculation pipeline is threaded with a heat exchange medium storage and transportation unit. The interior of the neutralization and conversion core is provided with a hot and cold medium interaction section. A temperature control platform is installed at the bottom of the interior of the neutralization and conversion core.

[0006] Preferably, an angular support connector is sleeved on the outer side of the feed channel, and the angular support connector is welded to the neutralization and conversion core.

[0007] Preferably, the top of the neutralization and conversion core is integrally formed with a material input section, and one side of the neutralization and conversion core is threadedly connected with a material output section.

[0008] Preferably, a stability extension member is welded to the bottom of the neutralization and conversion core, and four stability extension members are provided, which are arranged at equal intervals.

[0009] Preferably, a production line scheduling control panel is installed on the front of the heat exchange medium storage and transportation unit. The output end of the production line scheduling control panel is electrically connected to an equipment interconnection wire. One end of the equipment interconnection wire is electrically connected to a thermal detection element. The thermal detection element is threadedly connected to the neutralization and conversion core.

[0010] Preferably, a cooling medium conveying unit is installed on one side of the heat exchange medium storage and transportation unit, and the output end of the cooling medium conveying unit is threadedly connected to a sanitary fluid pipeline, which is threadedly connected to a fluid guide connector.

[0011] This utility model provides a neutralization and conversion device for the production of sodium caseinate, which has the following beneficial effects: This neutralization and conversion equipment for sodium caseinate production, equipped with a rotating central pivot, fluidized bed disturbance components, fluid release ports, a dynamic sealing adapter, a feed channel, and a directional feeding conveyor, allows operators to add washed casein to the neutralization and conversion core through the material input section. After addition, when adding alkaline solution, the operator activates the directional feeding conveyor, which draws the alkaline solution and feeds it through the feed channel and dynamic sealing adapter into the rotating central pivot. The fluid release port on the fluidized bed disturbance component sprays the alkaline solution onto the casein. During spraying, the paddle drive assembly rotates the rotating central pivot, which in turn drives the fluidized bed disturbance components to agitate the casein, ensuring the sprayed alkaline solution is evenly dispersed. This prevents over-concentration of alkali and avoids localized over-alkaliness. Furthermore, this conversion method not only improves conversion quality but also reduces the workload of operators. Attached Figure Description

[0012] Figure 1 This is a schematic diagram of the overall structure of this utility model; Figure 2 This is a partial structural diagram of the neutralization and transformation core part of this utility model; Figure 3 This is a cross-sectional view of the core part of the neutralization and transformation in this utility model; Figure 4 This is a partial structural schematic diagram of the rotation center pivot of this utility model.

[0013] In the diagram: 1. Neutralization and conversion core unit; 101. Hot and cold medium interaction unit; 102. Temperature control platform; 2. Material conveying unit; 3. Material input unit; 4. Fluid guide connection component; 5. Closed-loop recirculation pipeline; 6. Heat exchange medium storage and transportation unit; 7. Production line scheduling control panel; 8. Equipment interconnection wires; 9. Thermistor detection element; 10. Cooling medium conveyor unit; 11. Sanitary fluid pipeline; 12. Stability extension component; 13. Paddle drive assembly; 14. Rotation center pivot; 1401. Fluidization disturbance component; 1402. Fluid release port; 15. Dynamic sealing transfer device; 16. Feed channel; 17. Directional feeding conveyor; 18. Angle support connector. Detailed Implementation

[0014] The technical solutions of the present utility model will be clearly and completely described below with reference to the accompanying drawings of the embodiments of the present utility model. Obviously, the described embodiments are only some embodiments of the present utility model, and not all embodiments. All other embodiments obtained by those skilled in the art based on the embodiments of the present utility model without creative effort are within the protection scope of the present utility model.

[0015] Please see Figure 1-4 This utility model provides a technical solution: a neutralization conversion device for sodium caseinate production, including a neutralization conversion core 1. A paddle drive assembly 13 is installed at the bottom center of the neutralization conversion core 1. A rotation center pivot 14 is fixed to the drive end of the paddle drive assembly 13 via a coupling. A fluidization disturbance component 1401 is threadedly connected to the outer side of the rotation center pivot 14. A fluid release port 1402 is installed on the outer side of the fluidization disturbance component 1401. A dynamic sealing adapter 15 is threadedly connected to the top of the fluidization disturbance component 1401. The top of the sealing and conversion device 15 is threadedly connected to a feed channel 16. One end of the feed channel 16 is equipped with a directional feeding conveyor 17. On the other side of the neutralization and conversion core 1, fluid guide connectors 4 are welded. There are two fluid guide connectors 4. One end of one fluid guide connector 4 is threadedly connected to a closed recirculation pipeline 5. The other end of the closed recirculation pipeline 5 is threadedly connected to a heat exchange medium storage and transportation unit 6. A cold and hot medium interaction section 101 is opened inside the neutralization and conversion core 1. A temperature control platform 102 is installed at the bottom inside the neutralization and conversion core 1.

[0016] In this embodiment, an angled support connector 18 is sleeved on the outside of the feed channel 16. The angled support connector 18 is welded to the neutralization and conversion core 1. The angled support connector 18 can limit the feed channel 16, so that the feed channel 16 can be firmly fixed together with the neutralization and conversion core 1.

[0017] In this embodiment, the top of the neutralization and conversion core 1 is integrally formed with a material input section 3, and a material output section 2 is threadedly connected to one side of the neutralization and conversion core 1. The material input section 3 facilitates the addition of casein, and the material output section 2 facilitates the discharge of sodium caseinate.

[0018] In this embodiment, a stability extension member 12 is welded to the bottom of the neutralization and conversion core part 1. There are four stability extension members 12, which are arranged at equal intervals. The stability extension members 12 make the equipment more stable.

[0019] In this embodiment, a production line scheduling control panel 7 is installed on the front of the heat exchange medium storage and transportation unit 6. The output end of the production line scheduling control panel 7 is electrically connected to an equipment interconnection wire 8. One end of the equipment interconnection wire 8 is electrically connected to a thermal detection element 9. The thermal detection element 9 is threadedly connected to the neutralization and conversion core 1. The temperature of casein can be detected by the thermal detection element 9. When the temperature is too high, the production line scheduling control panel 7 can control the operation of the cooling component to quickly cool down the casein.

[0020] In this embodiment, a cooling medium conveyor unit 10 is installed on one side of the heat exchange medium storage and transportation unit 6. The output end of the cooling medium conveyor unit 10 is threadedly connected to a sanitary fluid pipeline 11. The sanitary fluid pipeline 11 is threadedly connected to the fluid guide connector 4. When the casein temperature is too high, the cooling medium conveyor unit 10 starts to operate and draws water from inside the heat exchange medium storage and transportation unit 6. The water enters the hot and cold medium interaction section 101 through the sanitary fluid pipeline 11 to absorb the heat of the casein, thereby achieving the purpose of cooling.

[0021] Working Principle: When using the neutralization and conversion equipment for sodium caseinate production, the operator adds washed casein to the neutralization and conversion core unit 1 through the material input section 3. After addition, when adding alkaline solution, the operator starts the directional feeding conveyor 17. The directional feeding conveyor 17 draws the alkaline solution and sends it through the feed channel 16 and dynamic sealing transfer device 15 into the rotary central pivot 14. The alkaline solution is then sprayed onto the casein through the fluid release port 1402 on the fluidization disturbance component 1401. During the spraying process, the paddle drive assembly 13 drives the rotary central pivot 14 to rotate, and the rotary central pivot 14 drives the fluidization disturbance component 1401 to stir the casein, so that the sprayed alkaline solution can be fully dispersed. At the same time, the directional feeding can be controlled according to the addition requirements. The material conveyor 17 operates to control the amount and frequency of alkaline solution spraying. During the neutralization and conversion process, the temperature control platform 102 generates heat, which heats the casein to a suitable temperature. When the thermal detection element 9 detects that the temperature is too high, the cooling medium conveyor unit 10 starts up and draws water from the heat exchange medium storage and transportation unit 6. The water enters the hot and cold medium interaction section 101 through the sanitary fluid pipeline 11 to absorb the heat from the casein, thereby achieving the purpose of cooling. Then, the water flows back to the heat exchange medium storage and transportation unit 6 through the closed recirculation pipeline 5. After the conversion is complete, the converted sodium caseinate can be discharged through the material output section 2. This completes the use of this utility model. This utility model has a simple structure and is safe and convenient to use.

[0022] 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 neutralization and conversion device for the production of sodium caseinate, characterized in that: The system includes a neutralization and conversion core (1), at the bottom center of which a blade drive assembly (13) is installed. The drive end of the blade drive assembly (13) is fixed to a rotation center pivot (14) via a coupling. A fluidization disturbance component (1401) is threadedly connected to the outer side of the rotation center pivot (14). A fluid release port (1402) is installed on the outer side of the fluidization disturbance component (1401). A dynamic sealing adapter (15) is threadedly connected to the top end of the fluidization disturbance component (1401). A feed channel is threadedly connected to the top end of the dynamic sealing adapter (15). (16) A directional feeding conveyor (17) is installed at one end of the feeding channel (16). A fluid guide connector (4) is welded to the other side of the neutralization and conversion core (1). There are two fluid guide connectors (4). One end of the fluid guide connector (4) is threaded to a closed recirculation pipeline (5). One end of the closed recirculation pipeline (5) is threaded to a heat exchange medium storage and transportation unit (6). A cold and hot medium interaction section (101) is opened inside the neutralization and conversion core (1). A temperature control platform (102) is installed at the bottom inside the neutralization and conversion core (1).

2. The neutralization and conversion equipment for sodium caseinate production according to claim 1, characterized in that: An angular support connector (18) is sleeved on the outside of the feed channel (16), and the angular support connector (18) is welded to the neutralization and conversion core (1).

3. The neutralization and conversion equipment for sodium caseinate production according to claim 1, characterized in that: The top of the neutralization and conversion core (1) is integrally formed with a material input section (3), and a material output section (2) is threadedly connected to one side of the neutralization and conversion core (1).

4. The neutralization and conversion equipment for sodium caseinate production according to claim 1, characterized in that: The bottom of the neutralization and transformation core (1) is welded with a stability extension member (12), and four stability extension members (12) are provided, which are arranged at equal intervals.

5. The neutralization and conversion equipment for sodium caseinate production according to claim 1, characterized in that: The front of the heat exchange medium storage and transportation unit (6) is equipped with a production line scheduling control panel (7). The output end of the production line scheduling control panel (7) is electrically connected to an equipment interconnection wire (8). One end of the equipment interconnection wire (8) is electrically connected to a thermal detection element (9). The thermal detection element (9) is threadedly connected to the neutralization and conversion core (1).

6. The neutralization and conversion equipment for sodium caseinate production according to claim 1, characterized in that: A cooling medium conveyor unit (10) is installed on one side of the heat exchange medium storage and transportation unit (6). The output end of the cooling medium conveyor unit (10) is threadedly connected to a sanitary fluid pipeline (11), and the sanitary fluid pipeline (11) is threadedly connected to a fluid guide connector (4).

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