Seasoning preparation equipment based on Maillard reaction intermediate hydrolysis

Abstract

The utility model relates to the technical field of seasoning preparation, in particular to seasoning preparation equipment based on Maillard reaction intermediate hydrolysis, which comprises a tank body, a stirring shaft is rotatably mounted at the bottom of an inner cavity of the tank body, a condensing disc covers an opening at the upper end of the tank body, and flow guide pipes of inner cavities of a plurality of flow guide bumps are sequentially communicated in series end to end. An inner cavity of the flow guide convex block is filled with heat exchange filler; flow guide through holes are formed in the side wall of the flow guide ring in a penetrating mode, and the multiple flow guide through holes are staggered pairwise. The condensation tank has the beneficial effects that the condensation disc is arranged to be of the hollow structure, the bottom wall of the condensation disc is sunken downwards to form the flow guide protruding block, the flow guide protruding block is of the hollow structure, the lower end of the flow guide protruding block is hemispherical, the inner cavity of the flow guide protruding block is filled with the heat exchange filler, and condensed liquid can flow downwards along the outer surface of the flow guide protruding block and drips into the inner cavity of the tank body again under the action of gravity; a plurality of flow guide convex blocks are uniformly distributed, so that the condensate can be ensured to uniformly drop into reactants, and the recovery efficiency is high.

Description

TECHNICAL FIELD

[0001] The utility model relates to seasoning preparation technical field, concretely is a kind of seasoning preparation equipment based on maillard reaction intermediate hydrolysis. BACKGROUND

[0002] Maillard reaction refers to the polymerization, condensation and other reactions of amino-containing compounds and carbonyl compounds at room temperature or when heated, eventually generating brown or brown-black macromolecular substances such as melanoidin or pseudo-melanin, so it is also called carbonyl amine reaction.

[0003] Chinese invention with publication number CN106268564B discloses a kind of maillard reaction tank, by setting up liquid collector in tank body, steam condensation is more easily condensed on the surface of liquid collector, in turn help to improve the recovery effect of aroma components.

[0004] However, at present, after the condensation of traditional liquid collector, the condensate will flow downward along the surface of the liquid collector and finally adhere to the inner wall of the tank, and the condensate recovery efficiency is low and difficult to mix uniformly into the reactant. Therefore, the utility model provides a kind of seasoning preparation equipment based on maillard reaction intermediate hydrolysis to solve the above problems. UTILITY MODEL CONTENTS

[0005] The utility model aims to provide a kind of seasoning preparation equipment based on maillard reaction intermediate hydrolysis to solve the problem of condensate easily adhering to the inner wall of the tank and low recovery efficiency proposed in the above background technology.

[0006] To achieve the above object, the utility model provides the following technical scheme: a kind of seasoning preparation equipment based on maillard reaction intermediate hydrolysis, comprising:

[0007] tank, the inner cavity bottom of the tank is rotatably installed with a stirring shaft, the upper end opening of the tank is covered with a condensing disc, the condensing disc is provided as a hollow structure, the bottom wall of the condensing disc is concave downward to form a plurality of uniformly distributed flow guide bosses, the flow guide bosses are hollow structure and the lower end is hemispherical, the flow guide pipe is arranged in the inner cavity of the flow guide boss, the flow guide pipes in the inner cavities of the plurality of flow guide bosses are sequentially and continuously communicated, and the inner cavities of the flow guide bosses are filled with heat exchange fillers;

[0008] A plurality of concentric flow guide rings are fixedly installed on the bottom wall of the condensing disc, flow guide through holes are formed through the side wall of the flow guide ring, and the flow guide through holes are alternately positioned with each other.

[0009] Preferably, a cover is fixedly installed at the upper opening of the condensing disc, a circulating main pipe is fixedly and continuously communicated on the surface of the cover, and the circulating main pipe is communicated with the flow guide pipe.

[0010] Preferably, the outer side of the circulating main pipe is fixedly connected with a circulating branch pipe, and the end of the circulating branch pipe penetrates through the cover and extends into the inner cavity of the condensing disc.

[0011] Preferably, the part of the flow guide pipe in the inner cavity of the flow guide bump is a spiral condensing pipe, and the condensing pipe is attached to the inner wall of the flow guide bump.

[0012] Preferably, the lower end of the stirring shaft is externally sleeved with a sealing sleeve, and the sealing sleeve is fixedly connected with the bottom of the tank body, and a stirring motor for driving the stirring shaft to rotate is mounted on the outer side of the bottom of the tank body.

[0013] Preferably, a plurality of stirring assemblies arranged in an annular array are fixedly mounted on the outer side of the stirring shaft, and the stirring assembly comprises a plurality of stirring blades arranged in a spiral shape, and the stirring blades are flat and twisted by forty-five degrees at the end.

[0014] Preferably, a feeding pipe is communicated with the upper part of the surface of the tank body, and the feeding pipe is obliquely arranged and provided with a control valve in the middle.

[0015] Compared with the prior art, the beneficial effects of the utility model are:

[0016] The utility model discloses a hollow structure is set up to the condensing disc, and the bottom wall of condensing disc is concave downward and forms the flow guide bump, the flow guide bump is hollow structure and the lower end is semispherical, the flow guide bump inner cavity is provided with the flow guide pipe, and a plurality of flow guide pipes are communicated in turn and are connected in series, the flow guide bump inner cavity is filled with heat exchange filler, the condensing disc inner cavity is communicated with cooling medium, the lower surface of condensing disc and the outer surface of flow guide bump can all heat exchange and condense the steam that floats on the tank body inner cavity, and the condensed condensate can flow down along the outer surface of flow guide bump, and under the action of gravity, re-drops into the tank body inner cavity, the flow guide bump is provided with a plurality of even distribution, can guarantee that the condensate evenly drops into the reactant, and the recovery efficiency is high. BRIEF DESCRIPTION OF DRAWINGS

[0017] Figure 1 It is the whole structure inside schematic diagram of the utility model;

[0018] Figure 2 It is the stirring shaft structure three-dimensional schematic diagram of the utility model;

[0019] Figure 3 It is the condensing disc structure explosion schematic diagram of the utility model;

[0020] Figure 4 It is the flow guide bump structure inside schematic diagram of the utility model.

[0021] In the figure: 1, tank body; 2, stirring shaft; 21, stirring blade; 22, sealing shaft sleeve; 23, stirring motor; 3, condensing disc; 31, flow guide bump; 32, flow guide pipe; 321, condensing pipe; 33, flow guide ring; 34, flow guide through hole; 35, cover; 36, circulating main pipe; 37, circulating branch pipe; 4, feeding pipe; 41, control valve. DETAILED DESCRIPTION

[0022] In order to make the purpose, technical scheme of the present application, and the advantages are more clear and obvious, the following will be further described in detail with the embodiments of the present application. It should be understood that the specific embodiments described here are part of the embodiments of the present application, not all embodiments, only to explain the embodiments of the present application, and not for the purpose of limiting the embodiments of the present application, all other embodiments obtained by the person skilled in the art without doing creative work, belong to the scope of protection of the present application.

[0023] Please refer to Figures 1 to 4 The utility model provides a technical scheme:

[0024] Embodiment one, a kind of based on Maillard reaction intermediate hydrolysis seasoning preparation equipment, comprising: tank body 1.

[0025] Specifically, stirring shaft 2 is rotatably installed at the bottom of the inner cavity of tank body 1, and stirring shaft 2 is used to stir the reactants in the inner cavity of tank body 1 when rotating, to ensure that the reaction between materials is more sufficient and uniform, condensing disc 3 is covered at the upper end opening of tank body 1, to seal the opening of tank body 1, prevent the aroma generated during the reaction of materials in the inner cavity of tank body 1 from being lost, and steam from carrying aroma overflow the inner cavity of tank body 1, condensing disc 3 is provided as a hollow structure, the bottom wall of condensing disc 3 is concave downward to form a plurality of uniformly distributed flow guide bumps 31, flow guide bumps 31 are hollow structure and the lower end is semispherical, such as Figure 1As shown, the arrangement of multiple flow guide bumps 31 can increase the area of the lower surface of the condensing disc 3, so that the steam in the inner cavity of the tank body 1 can fully contact the lower surface of the condensing disc 3 after floating and be condensed to form condensate, and the condensate can adhere to the surface of the flow guide bump 31 and flow downward under the action of gravity until it is re-dropped into the reactant in the inner cavity of the tank body 1. A flow guide pipe 32 is arranged in the inner cavity of the flow guide bump 31, and the flow guide pipes 32 in the inner cavities of multiple flow guide bumps 31 are sequentially and circularly connected in series. The inner cavity of the flow guide bump 31 is filled with heat exchange filler, i.e. heat conduction filler, which can be used to increase the thermal conductivity of the material. Common heat conduction fillers include aluminum oxide, magnesium oxide, zinc oxide, aluminum nitride, boron nitride, silicon carbide, etc. Among them, micron-sized aluminum oxide and silicon powder are mainly used as the filler, and nanometer aluminum oxide and nitride are used as the filler in the field of high thermal conductivity. Zinc oxide is mostly used as a heat conduction paste and heat conduction silicone filler. The flow guide pipe 32 is used to continuously transport cooling medium, which can be in liquid or gaseous state. The device uses gaseous cooling medium, which can reduce the weight inside the condensing disc 3 and cooperate with the heat exchange filler in the inner cavity of the flow guide bump 31 to perform heat exchange on the surface of the flow guide bump 31, thereby ensuring that the steam can be condensed to form condensate after contacting the surface of the flow guide bump 31.

[0026] Secondly, multiple concentric flow guide rings 33 are fixedly installed on the bottom wall of the condensing disc 3. The side wall of the flow guide ring 33 is provided with a flow guide through hole 34, and multiple flow guide through holes 34 are alternately arranged. Figure 3 As shown, multiple flow guide rings 33 can divide the inner cavity of the condensing disc 3 into multiple annular small compartments, and only the flow guide through hole 34 remains connected between adjacent two small compartments. Therefore, after the cooling medium is introduced into the inner cavity of the condensing disc 3, the cooling medium can flow in a longer path in the inner cavity of the condensing disc 3, thereby ensuring that the steam in the inner cavity of the tank body 1 can also form condensate when contacting the lower surface of the condensing disc 3. In addition, a round corner is arranged at the connection between the lower surface of the condensing disc 3 and the flow guide bump 31, so that the condensate can more smoothly flow downward along the surface of the flow guide bump 31.

[0027] In order to introduce cooling medium into the inner cavity of the flow guide pipe 32, the application also has a cover 35 fixedly installed at the upper opening of the condensing disc 3. A circulation main pipe 36 is fixedly and communicatively arranged on the surface of the cover 35. The circulation main pipe 36 is in communication with the flow guide pipe 32. The circulation main pipe 36 is mainly used to transport cooling medium into the inner cavity of the flow guide pipe 32 and discharge the cooling medium from the tail end of the flow guide pipe 32, thereby ensuring that the surface of the flow guide bump 31 can always maintain a lower temperature for the steam to condense after contacting.

[0028] In order to heat exchange and cool the lower surface of the condensing disc 3, the application also has a circulating branch pipe 37 communicated with the outside of the circulating main pipe 36, the end of the circulating branch pipe 37 penetrates the cover 35 and extends into the inner cavity of the condensing disc 3, the circulating branch pipe 37 is arranged to introduce cooling medium into the inner cavity of the condensing disc 3, and the cooling medium flows in the inner cavity of the condensing disc 3, so that the lower surface of the condensing disc 3 can be heat exchanged and cooled, and the condensed liquid can also be formed after the steam contacts the lower surface of the condensing disc 3.

[0029] In order to improve the heat exchange effect of the flow guide bump 31, the part of the flow guide pipe 32 located in the inner cavity of the flow guide bump 31 is a spiral condensing pipe 321, and the condensing pipe 321 is attached to the inner wall of the flow guide bump 31, as shown in Figure 4 , the condensing pipe 321 can be in more sufficient contact with the inner wall of the flow guide bump 31, and the heat exchange effect of the flow guide bump 31 can be improved by cooperating with the heat exchange filler in the inner cavity of the flow guide bump 31. In addition, the spiral condensing pipe 321 can also prolong the flow path of the cooling medium, further improving the heat exchange effect.

[0030] In order to drive the stirring shaft 2 to work, the application also has a sealing sleeve 22 sleeved on the outside of the lower end of the stirring shaft 2, and the sealing sleeve 22 is fixedly connected with the bottom of the tank body 1. A sealing ring is arranged between the sealing sleeve 22 and the stirring shaft 2, which is used to avoid leakage of the material in the inner cavity of the tank body 1. A stirring motor 23 is installed on the outside of the bottom of the tank body 1 to drive the stirring shaft 2 to rotate, so as to control the stirring speed of the stirring shaft 2.

[0031] In order to stir the material, the application also has a plurality of stirring assemblies arranged in a ring array on the outside of the stirring shaft 2, and the stirring assembly comprises a plurality of stirring blades 21 arranged in a spiral shape, the stirring blades 21 are flat and the end is twisted by forty-five degrees, as shown in Figure 2 , when the stirring shaft 2 rotates, the stirring blades 21 can stir the material, and at the same time, the stirring blades 21 can also stir the material in the up-down direction, so as to ensure that the condensed liquid flowing on the surface of the flow guide bump 31 can drop to each area of the material.

[0032] In order to facilitate the addition of material, the application also has a feeding pipe 4 communicated with the surface of the tank body 1, the feeding pipe 4 is inclinedly arranged, and a control valve 41 is installed in the middle part of the feeding pipe 4. The feeding pipe 4 is arranged to facilitate the workers to add material into the inner cavity of the tank body 1, and the control valve 41 is arranged to seal the inner cavity of the feeding pipe 4, so as to avoid the steam in the inner cavity of the tank body 1 overflowing along the inner cavity of the feeding pipe 4.

[0033] Although the embodiments of the present application have been shown and described, it is to be understood that various changes, modifications, substitutions and alterations can be made to these embodiments without departing from the principles and spirit of the present application, the scope of which is defined by the appended claims and their equivalents.

Claims

1. A seasoning preparation device based on the hydrolysis of Maillard reaction intermediates, characterized in that: include: Tank (1), with a stirring shaft (2) rotatably installed at the bottom of the inner cavity of the tank (1), and a condensing plate (3) covering the upper opening of the tank (1). The condensing plate (3) is hollow, and the bottom wall of the condensing plate (3) is recessed downward to form multiple evenly distributed flow guiding protrusions (31). The flow guiding protrusions (31) are hollow and the lower end is hemispherical. The inner cavity of the flow guiding protrusions (31) is provided with a flow guiding pipe (32). The flow guiding pipes (32) of the inner cavities of multiple flow guiding protrusions (31) are connected in series from end to end. The inner cavity of the flow guiding protrusions (31) is filled with heat exchange packing. Multiple concentric guide rings (33) are fixedly installed on the bottom wall of the condenser plate (3). The guide rings (33) have guide holes (34) through their side walls, and the multiple guide holes (34) are staggered in pairs.

2. The seasoning preparation equipment based on Maillard reaction intermediate hydrolysis according to claim 1, characterized in that: A cover (35) is fixedly installed at the upper opening of the condenser plate (3), and a circulation main pipe (36) is fixedly connected to the surface of the cover (35). The circulation main pipe (36) is connected to the guide pipe (32).

3. The seasoning preparation equipment based on Maillard reaction intermediate hydrolysis according to claim 2, characterized in that: The outer side of the main circulation pipe (36) is fixedly connected to a circulation branch pipe (37), the end of which penetrates the cover (35) and extends into the inner cavity of the condenser plate (3).

4. The seasoning preparation equipment based on Maillard reaction intermediate hydrolysis according to claim 1, characterized in that: The portion of the guide tube (32) located within the inner cavity of the guide protrusion (31) is a spiral-shaped condenser tube (321), and the condenser tube (321) is attached to the inner wall of the guide protrusion (31).

5. The seasoning preparation equipment based on Maillard reaction intermediate hydrolysis according to claim 1, characterized in that: A sealing sleeve (22) is fitted on the outer side of the lower end of the stirring shaft (2), and the sealing sleeve (22) is fixedly connected to the bottom of the tank (1). A stirring motor (23) for driving the stirring shaft (2) to rotate is installed on the outer side of the bottom of the tank (1).

6. The seasoning preparation equipment based on Maillard reaction intermediate hydrolysis according to claim 1, characterized in that: Multiple stirring components arranged in a ring array are fixedly installed on the outside of the stirring shaft (2). The stirring components include multiple stirring blades (21) arranged in a spiral shape. The stirring blades (21) are flat and twisted at the ends at a 45-degree angle.

7. The seasoning preparation equipment based on Maillard reaction intermediate hydrolysis according to claim 1, characterized in that: The upper surface of the tank (1) is connected to a feeding pipe (4), which is inclined and has a control valve (41) installed in the middle.

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