Roxburgh rose and lactic acid bacteria combined processing device

Abstract

The utility model relates to the technical field of roxburgh rose lactic acid bacteria processing, in particular to a roxburgh rose lactic acid bacteria combined processing device which comprises a heating bin and a cooling bin, an outer conveying pipe is fixedly intercepted between the heating bin and the cooling bin, a feeding pipe is fixedly connected to one side of the top of the heating bin, and a heating cavity is formed in the heating bin. The top end and the outer side of the heating cavity are fixedly connected with a filter plate and a heating coil respectively, the front face of the heating cavity is fixedly connected with a first external pipe and a second external pipe, and the second external pipe is communicated with the external conveying pipe. The heating cavity with the hemispherical bottom end is matched with the heating coil which surrounds the heating cavity, so that the effect of uniformly heating raw material liquid added into the heating cavity is achieved, and the effect of pre-conveying and guiding the raw material liquid passing through the outer conveying pipe is achieved through the inner conveying pipe; and the radiating fin plates on the surface are matched, so that the radiating and cooling effects are achieved.

Description

Technical Field

[0001] This utility model relates to the technical field of processing prickly pear lactic acid bacteria, and specifically to a prickly pear lactic acid bacteria composite processing device. Background Technology

[0002] The prickly pear is the fruit of the perennial deciduous shrub Rosa laevigata, also known as the mountain king fruit or prickly berry. It is a nutritious and rare fruit that is good for health and fitness. After ripening, the prickly pear is often made into a flavorful beverage with better taste by mixing it with lactic acid bacteria. This process requires the use of heating and cooling mechanisms for fermentation and cooling.

[0003] When using existing prickly pear lactic acid bacteria compound processing equipment, the heating components are not uniform enough during the heating process, which easily leads to local heating and excessively high local temperatures. At the same time, when cooling is required after heating and fermentation, the waste is usually discharged directly into the cooling mechanism through pipes. This centralized cooling method consumes a lot of energy and has low cooling efficiency.

[0004] Therefore, this utility model proposes a prickly pear lactic acid bacteria composite processing device. Utility Model Content

[0005] To address the shortcomings of existing technologies, this utility model provides a prickly pear lactic acid bacteria compound processing device, which can solve the following problems:

[0006] The heating element is not uniform enough during the heating process, which can easily lead to localized heating and excessively high local temperatures.

[0007] When cooling is required after heating and fermentation, the waste is usually discharged directly into the cooling system through pipes. This centralized cooling method has the problems of high energy consumption and low cooling efficiency.

[0008] To solve the above-mentioned technical problems, the present invention proposes the following technical solution:

[0009] A prickly pear lactic acid bacteria compound processing device includes a heating chamber and a cooling chamber. An external conveying pipe is fixedly connected between the heating chamber and the cooling chamber. An inlet pipe is fixedly connected to one side of the top of the heating chamber. A heating chamber is opened inside the heating chamber. A filter plate and a heating coil are fixedly connected to the top and the outside of the heating chamber, respectively. A first external pipe and a second external pipe are fixedly connected to the front of the heating chamber. The second external pipe is also connected to the external conveying pipe. A temperature measuring mechanism is fixedly connected to the inner wall of the heating chamber. A collection pipe is fixedly connected to one side of the heating chamber.

[0010] The cooling chamber has a cooling cavity inside, and a drive shaft and a stirring fan are embedded and fixedly connected inside the cooling cavity. A pressure relief pipe is fixedly connected to the top of the cooling chamber, and a third external pipe is fixedly connected to one side of the bottom of the cooling chamber. An insulation layer is provided on the outside of the cooling cavity. A heat dissipation cavity is provided at the bottom of the cooling chamber. An inner conveying pipe is embedded between the heat dissipation cavity and the cooling cavity. One end of the inner conveying pipe is connected to the outer conveying pipe, and heat dissipation fins are fixedly connected to the surface of the inner conveying pipe.

[0011] Furthermore, the filter plate is inclined downwards as a whole, with one end located below the feed pipe and the other end connected to the top of the collection pipe, which is arranged in a longitudinal "L" shape.

[0012] Furthermore, both the heating chamber and the top section of the heating coil are arranged vertically in a cylindrical shape, and their bottom ends are both hemispherical. An electric heater is provided on the outside of the heating coil, and the heating coil surrounds the outside of the heating chamber.

[0013] Furthermore, the second external pipe extends longitudinally in an "L" shape to the outside of the heating chamber, and a valve mechanism and a pump mechanism are installed on the external delivery pipe.

[0014] Furthermore, the inner delivery pipe is an "L"-shaped copper pipe with an arc-shaped bottom end. The top section extends upward along the inside of the cooling chamber and connects to one side of the top of the cooling cavity. The heat dissipation fins are copper fins that are vertically set along the arc-shaped surface at the bottom end of the inner delivery pipe and are vertically embedded in the heat dissipation cavity.

[0015] Furthermore, the insulation layer is located above the inner conveying pipe in an "L" shape, with its bottom end conforming to the bottom surface of the cooling chamber in an arc shape, and its top section conforming to the surface of the vertical section of the cooling chamber.

[0016] Furthermore, fan mechanisms are provided at both ends of the heat dissipation cavity, and the top of the heat dissipation cavity and the heat dissipation fins are sealed together.

[0017] Furthermore, the bottom of the cooling chamber is hemispherical, and a communication port is opened on its outer side corresponding to the top of the inner conveying pipe. The drive shaft is vertically set, and a drive motor is installed at its top. Two sets of stirring fans are rectangularly staggered and located on the upper and lower sides of the drive shaft.

[0018] As can be seen from the above technical solution, the beneficial effects of this utility model are:

[0019] 1. This utility model achieves the effect of filtering the raw material liquid entering the heating chamber through the feed pipe using a filter plate, and achieves the effect of collecting the filtered particulate impurities through a collection pipe.

[0020] 2. This utility model achieves the effect of uniformly heating the raw material liquid added to the heating chamber by using a heating chamber with a hemispherical bottom and a heating coil that surrounds it.

[0021] 3. This utility model achieves the effect of pre-transporting and guiding the raw material liquid that has passed through the outer conveying pipe through the inner conveying pipe, and achieves the effect of heat dissipation and cooling by means of heat dissipation fins on the surface, and achieves the effect of heat isolation of the raw material liquid transported by the inner conveying pipe through the heat insulation layer, so as to ensure the cooling effect of the cooling chamber afterwards.

[0022] 4. This utility model achieves the effect of cooling the heat dissipation fins through the heat dissipation cavity.

[0023] 5. This utility model achieves the effect of uniformly cooling the raw material liquid through a cooling cavity with a hemispherical bottom, and achieves the effect of stirring and dissipating heat in the raw material liquid in the cooling cavity through a drive shaft in conjunction with a stirring fan. Attached Figure Description

[0024] To more clearly illustrate the specific embodiments of this utility model or the technical solutions in the prior art, the drawings used in the description of the specific embodiments or the prior art will be briefly introduced below. In all the drawings, similar elements or parts are generally identified by similar reference numerals. In the drawings, the elements or parts are not necessarily drawn to scale.

[0025] Figure 1 This is a front view of the overall structure of this utility model;

[0026] Figure 2 In this utility model Figure 1 Enlarged view of the structure at point A in the middle;

[0027] Figure 3 This is a front view of the internal structure connection of the cooling chamber in this utility model.

[0028] Figure label:

[0029] 1. Heating chamber; 2. Feed pipe; 3. Filter plate; 4. Temperature measuring mechanism; 5. Heating cavity; 6. Heating coil; 7. First external pipe; 8. Second external pipe; 9. External conveying pipe; 10. Cooling chamber; 11. Pressure relief pipe; 12. Drive shaft; 13. Agitator fan; 14. Third external pipe; 15. Collection pipe; 16. Cooling cavity; 17. Heat dissipation bottom cavity; 18. Internal conveying pipe; 19. Insulation layer; 20. Heat dissipation fins. Detailed Implementation

[0030] The embodiments of the present invention will now be described in detail with reference to the accompanying drawings. These embodiments are merely illustrative of the present invention and should not be construed as limiting the scope of protection of the present invention.

[0031] See Figure 1-3 As shown, a prickly pear lactic acid bacteria compound processing device includes a heating chamber 1 and a cooling chamber 10. An external conveying pipe 9 is fixedly connected between the heating chamber 1 and the cooling chamber 10. An inlet pipe 2 is fixedly connected to one side of the top of the heating chamber 1. A heating chamber 5 is opened inside the heating chamber 1. A filter plate 3 and a heating coil 6 are fixedly connected to the top and outside of the heating chamber 5, respectively. A first external pipe 7 and a second external pipe 8 are fixedly connected to the front of the heating chamber 5. The second external pipe 8 is also connected to the external conveying pipe 9. A temperature measuring mechanism 4 is fixedly connected to the inner wall of the heating chamber 5. A collection device is fixedly connected to one side of the heating chamber 1. The cooling chamber 10 has a cooling cavity 16 inside the pipe 15. The cooling cavity 16 is embedded with a fixedly connected drive shaft 12 and a stirring fan 13. The top of the cooling chamber 10 is fixedly connected with a pressure relief pipe 11. The bottom of the cooling chamber 10 is fixedly connected with a third external pipe 14. The outside of the cooling cavity 16 is provided with a heat insulation layer 19. The bottom of the cooling chamber 10 has a heat dissipation cavity 17. An inner conveying pipe 18 is embedded between the heat dissipation cavity 17 and the cooling cavity 16. One end of the inner conveying pipe 18 is connected to the outer conveying pipe 9. The surface of the inner conveying pipe 18 is fixedly connected with a heat dissipation fin 20.

[0032] In this embodiment of the utility model, the filter plate 3 is inclined downwards as a whole, with one end located below the feed pipe 2 and the other end sleeved above the collection pipe 15. The collection pipe 15 is arranged in a longitudinal "L" shape. The filter plate 3 achieves the effect of filtering the raw material liquid that enters the heating chamber 1 through the feed pipe 2, and the collection pipe 15 achieves the effect of collecting the filtered particulate impurities.

[0033] The top sections of both the heating chamber 5 and the heating coil 6 are cylindrical and vertically arranged, and the bottom ends of both are hemispherical. An electric heater is provided on the outside of the heating coil 6. The heating coil 6 surrounds the outside of the heating chamber 5. By using the heating chamber 5 with its hemispherical bottom end to surround the heating coil 6, the raw material liquid added to the heating chamber 5 can be uniformly heated.

[0034] The raw material liquid enters the heating chamber 5 through the feed pipe 2. The inclined filter plate 3 filters the raw material liquid, filtering out particulate impurities. The particulate impurities are concentrated on the filter plate 3 and collected in the collection pipe 15 along the inclined filter plate 3. The raw material liquid enters the heating chamber 5 for heating treatment. The heating chamber 5, which is hemispherical at the bottom, together with the heating coil 6 surrounding it on the outside, can achieve uniform heating treatment according to the change of liquid flow rate, avoiding local heating.

[0035] The second external pipe 8 extends longitudinally in an "L" shape to the outside of the heating chamber 1. The external conveying pipe 9 is equipped with a valve mechanism and a pump mechanism. The internal conveying pipe 18 is an "L" shaped copper pipe with an arc-shaped bottom end. The top section extends upward along the inside of the cooling chamber 10 and connects to one side of the top of the cooling cavity 16. The heat dissipation fins 20 are copper fins that are vertically set along the arc-shaped bottom surface of the internal conveying pipe 18 and are vertically embedded in the heat dissipation cavity 17. The insulation layer 19 is located above the internal conveying pipe 18 and is "L" shaped. Its bottom end is attached to the bottom surface of the cooling chamber 10 in an arc shape, and its top section is attached to the vertical section surface of the cooling chamber 10. The internal conveying pipe 18 achieves the effect of pre-conveying and guiding the raw material liquid passing through the external conveying pipe 9. The heat dissipation fins 20 on the surface achieve the effect of heat dissipation and cooling. The insulation layer 19 achieves the effect of isolating the heat of the raw material liquid conveyed by the internal conveying pipe 18, ensuring the subsequent cooling effect of the cooling chamber 10.

[0036] After heating, the raw material liquid is transported through the outer conveying pipe 9 to the inner conveying pipe 18. The raw material liquid is then transported from the top of the cooling chamber 16 through the inner conveying pipe 18. This top-down conveying method can effectively pre-cool the raw material liquid, removing some of the heat to reduce the energy consumption of the cooling chamber 10. During this process, some of the heat contained in the heated raw material liquid is dispersed through the inner conveying pipe 18 and the heat dissipation fins 20, ensuring the cooling efficiency of the subsequent cooling chamber 10.

[0037] Fan mechanisms are provided at both ends of the heat dissipation cavity 17, and the top of the heat dissipation cavity 17 and the heat dissipation fin 20 are sealed together. The heat dissipation cavity 17 achieves the effect of cooling the heat dissipation fin 20.

[0038] After some of the heat in the raw material liquid after heat treatment is conducted onto the heat dissipation fins 20, the fan mechanism set at both ends of the heat dissipation cavity 17 is activated to dissipate the heat concentrated on the heat dissipation fins 20 outward.

[0039] The cooling chamber 16 has a hemispherical bottom and a corresponding opening on its outer side at the top of the inner conveying pipe 18. The drive shaft 12 is vertically positioned and has a drive motor at its top. Two sets of agitators 13 are rectangularly staggered and located on the upper and lower sides of the drive shaft 12. The cooling chamber 16, with its hemispherical bottom, can uniformly cool the raw material liquid. The drive shaft 12, in conjunction with the agitators 13, can agitate and dissipate heat from the raw material liquid in the cooling chamber 16.

[0040] The raw material liquid is transported to the cooling chamber 16 through the inner conveying pipe 18. Then, the drive shaft 12 drives the stirring fan 13 to stir the raw material liquid. The generated heat vapor and the large amount of heat-containing vapor discharged during the fall of the raw material liquid are discharged outward through the pressure relief pipe 11.

[0041] Finally, it should be noted that the above embodiments are only used to illustrate the technical solutions of this utility model, and not to limit it. Although the utility model has been described in detail with reference to the foregoing embodiments, those skilled in the art should understand that modifications can still be made to the technical solutions described in the foregoing embodiments, or equivalent substitutions can be made to some or all of the technical features. Such modifications or substitutions do not cause the essence of the corresponding technical solutions to deviate from the scope of the technical solutions of the embodiments of this utility model, and they should all be covered within the scope of the claims and specification of this utility model.

Claims

1. A prickly pear lactic acid bacteria compound processing device, characterized in that: Including heating bin (1) and cooling bin (10), the heating bin (1) and cooling bin (10) between fixed intercept with outer conveying pipe (9), the top side of heating bin (1) is fixedly connected with inlet pipe (2), the inside of heating bin (1) is provided with heating cavity (5), the top end and the outside of heating cavity (5) are fixedly connected with filter plate (3) and heating coil (6) respectively, the front of heating cavity (5) is fixedly connected with first outer connecting pipe (7) and second outer connecting pipe (8), second outer connecting pipe (8) is connected with outer conveying pipe (9) simultaneously, the inner wall of heating cavity (5) is fixedly connected with temperature measuring mechanism (4), one side of heating bin (1) is fixedly connected with collecting pipe (15); The inside of cooling bin (10) is provided with cooling cavity (16), the inside of cooling cavity (16) is embedded with fixedly connected drive shaft (12) and stirring fan (13), the top end of cooling bin (10) is fixedly connected with pressure relief pipe (11), one side of the bottom end of cooling bin (10) is fixedly connected with third outer connecting pipe (14), the outside of cooling cavity (16) is provided with temperature insulation layer (19), the bottom end of cooling bin (10) is provided with heat dissipation bottom cavity (17), the inside of heat dissipation bottom cavity (17) and cooling cavity (16) is embedded with inner conveying pipe (18), one end of inner conveying pipe (18) is connected with outer conveying pipe (9), the surface of inner conveying pipe (18) is fixedly connected with heat dissipation fin plate (20).

2. The Malus sieboldii lactic acid bacteria complex processing apparatus according to claim 1, characterized by: The filter plate (3) is inclined downward as a whole, one end of which is below the inlet pipe (2), and the other end is above the collecting pipe (15).

3. The Malus sieboldii lactic acid bacteria complex processing apparatus according to claim 1, characterized by: The top section of the heating cavity (5) and the heating coil (6) is cylindrical and vertically arranged, and the bottom end of both is semispherical.

4. The Malus sieboldii lactic acid bacteria complex processing apparatus according to claim 1, characterized by: The second outer connecting pipe (8) is "L" shaped and extends longitudinally outside the heating bin (1), and the outer conveying pipe (9) is provided with a valve mechanism and a pump body mechanism.

5. The Malus sieboldii lactic acid bacteria complex processing apparatus according to claim 1, characterized by: The inner conveying pipe (18) is a "L" shaped copper pipe, the bottom end of which is arc-shaped, and the top section extends upward along the inside of the cooling bin (10) and is connected with one side of the top of the cooling cavity (16), the heat dissipation fin plate (20) is a copper fin plate, which is vertically arranged along the arc-shaped surface of the bottom end of the inner conveying pipe (18), and the heat dissipation fin plate (20) is vertically embedded in the heat dissipation bottom cavity (17).

6. The Malus sieboldii lactic acid bacteria complex processing apparatus according to claim 1, characterized by: The temperature insulation layer (19) is above the inner conveying pipe (18) and is "L" shaped, the bottom end of which is arc-shaped and attached to the bottom surface of the cooling bin (10), and the top section is attached to the vertical surface of the cooling bin (10).

7. The Malus sieboldii lactic acid bacteria complex processing apparatus according to claim 1, characterized by: Both ends of the heat dissipation bottom cavity (17) are provided with fan mechanisms, and the top of the heat dissipation bottom cavity (17) and the position where the heat dissipation fin plate (20) is connected are sealingly connected.

8. The Malus sieboldii lactic acid bacteria complex processing apparatus according to claim 1, characterized by: The bottom end of the cooling cavity (16) is semispherical, and a communication port is formed on the outside corresponding to the top end of the inner conveying pipe (18), the drive shaft (12) is vertically arranged, and a drive motor is provided at the top end, the stirring fan (13) is arranged in two groups in a rectangular staggered manner on the left and right sides of the drive shaft (12).

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