Composite catechin extraction equipment

Abstract

The utility model discloses composite catechin extraction equipment which comprises a mashing device, the mashing device comprises a first mashing tank, a first hydraulic cylinder is arranged at the upper end of the first mashing tank, a first mashing stone is arranged in the first mashing tank, a first lifting rod is arranged at the upper end of the first mashing stone, and a second hydraulic cylinder is arranged at the lower end of the first lifting rod; the first lifting rod is connected with the first hydraulic cylinder; the dissolving device comprises a first dissolving tank, a first driving motor is arranged at the upper end of the first dissolving tank, a first stirring shaft is arranged at the lower end of the first driving motor, and a first stirring paddle is arranged at the lower end of the first stirring shaft; the concentration device comprises a first concentration tank, and a heating evaporation mechanism is arranged in the first concentration tank. According to the composite catechin extraction equipment provided by the utility model, lotus root blocks are mashed through the mashing device, catechins are rapidly dissolved through the dissolving device, and then the catechins are concentrated and extracted through the concentrating device, so that the extraction and efficiency of the catechins are ensured.

Description

Technical Field

[0001] This utility model belongs to the field of extraction devices, specifically relating to a compound catechin extraction device. Background Technology

[0002] Catechins, as polyphenolic compounds, possess excellent free radical scavenging capabilities. Some studies have reported that catechins also enhance capillary wall toughness, lower blood sugar, reduce blood cholesterol and low-density lipoprotein, resist radiation and ultraviolet rays, and have anti-mutagenic effects. Other studies have shown that catechins promote blood circulation and remove blood stasis. However, current extraction methods for catechins are not stable enough and their efficiency is not high enough, thus failing to guarantee the quality of complex catechin compounds. Summary of the Invention

[0003] To address the shortcomings of existing technologies, this invention provides a compound catechin extraction device.

[0004] To achieve the above objectives, the present invention provides the following technical solution:

[0005] A compound catechin extraction device, comprising:

[0006] A crushing device, comprising a first crushing tank, a first hydraulic cylinder at the upper end of the first crushing tank, a first crushing stone inside the first crushing tank, a first lifting rod at the upper end of the first crushing stone, and the first lifting rod being connected to the first hydraulic cylinder.

[0007] A dissolving device, comprising a first dissolving tank, a first drive motor at the upper end of the first dissolving tank, a first stirring shaft at the lower end of the first drive motor, a first stirring paddle at the lower end of the first stirring shaft, a first feed inlet at the upper end of the first dissolving tank, and a first discharge outlet at the lower end of the first dissolving tank.

[0008] A concentration device, comprising a first concentration tank, a second inlet at the upper end of the first concentration tank matching the first outlet, a second outlet at the lower end of the first concentration tank, and a heating and evaporation mechanism inside the first concentration tank.

[0009] Furthermore, the first crushing tank is provided with a first feeding hopper at its upper end and a first discharge port at its lower end. The first discharge port is hinged to a first sealing door, and a first sealing ring is provided on the first sealing door.

[0010] Furthermore, the heating and evaporation mechanism includes a first heating plate, a second heating plate, and a third heating plate. The first heating plate is located at the left end of the first concentration tank and is inclined downward to the right. The second heating plate is located at the right end of the first concentration tank and is inclined downward to the left. The third heating plate is located below the first heating plate and is inclined downward to the right. The second discharge port corresponds to the third heating plate.

[0011] Furthermore, the upper end of the first concentration tank is provided with a steam condensation mechanism, which includes a first condensation plate and a first water receiving tank. The first condensation plate is disposed at the upper end of the first concentration tank and is inclined to the lower right. The first water receiving tank is disposed at the right end of the first concentration tank and corresponds to the lower part of the first condensation plate. The right end of the first water receiving tank passes through the first concentration tank and is provided with a first drain pipe.

[0012] Furthermore, the steam condensation mechanism includes a first air cooler, which is disposed outside the first concentration tank. The first condensation plate has a first S-shaped cavity, one end of which has a first air inlet pipe, and the other end of which has a first air outlet pipe. The first air inlet pipe and the first air outlet pipe are connected to the first air cooler.

[0013] The present invention discloses a compound catechin extraction device. Compared with the prior art, its advantages are that it has a simple and stable structure, can fully crush lotus root pieces through a crushing device, quickly dissolve catechins through a dissolving device, and concentrate and extract them through a concentrating device, thus ensuring the extraction efficiency of catechins. Attached Figure Description

[0014] Figure 1 This is a schematic diagram of a preferred embodiment of the present invention.

[0015] Figure 2 This is a schematic diagram of the crushing device according to a preferred embodiment of the present invention.

[0016] Figure 3 This is a schematic diagram of the structure of the dissolving device according to a preferred embodiment of the present invention.

[0017] Figure 4 This is a schematic diagram of the concentration device according to a preferred embodiment of the present invention.

[0018] Figure 5 This is a schematic diagram of the structure of the first S-shaped cavity in a preferred embodiment of the present invention.

[0019] Figure 6 This is a schematic diagram of the structure of the first dovetail groove in a preferred embodiment of the present invention.

[0020] The reference numerals in the attached drawings include: 100, first concentration tank; 110, first heating plate; 120, second heating plate; 130, third heating plate; 140, first heating element; 150, second feed inlet; 160, second discharge outlet; 170, first exhaust pipe; 171, first pressure valve; 200, first condenser plate; 210, first air outlet pipe; 220, first air inlet pipe; 230, first S-shaped cavity; 240, first dovetail groove; 250, first water receiving tank; 251. 260. First drain pipe; 300. First water-guiding rope; 310. First dissolving tank; 320. First drive motor; 330. First stirring shaft; 340. First stirring paddle; 350. First discharge port; 360. First crushing blade; 400. First crushing tank; 410. First feeding hopper; 420. First discharge port; 430. First hydraulic cylinder; 440. First crushed stone; 450. First lifting rod; 460. First sealing door; 461. First sealing ring. Detailed Implementation

[0021] This utility model discloses a compound catechin extraction device. The specific implementation of this utility model will be further described below with reference to preferred embodiments.

[0022] See attached diagram. Figure 1-6 , Figure 1 This is a schematic diagram of the structure of a preferred embodiment provided by this utility model. Figure 2 This is a schematic diagram of the crushing device according to a preferred embodiment of the present invention. Figure 3 This is a schematic diagram of the structure of the dissolving device according to a preferred embodiment of the present invention. Figure 4 This is a schematic diagram of the concentration device according to a preferred embodiment of the present invention. Figure 5 This is a schematic diagram of the structure of the first S-shaped cavity 230 according to a preferred embodiment of the present invention. Figure 6 This is a schematic diagram of the structure of the first dovetail groove 240 of the preferred embodiment provided by this utility model.

[0023] Preferred embodiment.

[0024] This embodiment provides a compound catechin extraction device, including:

[0025] The crushing device includes a first crushing tank 400, a first hydraulic cylinder 430 at the upper end of the first crushing tank 400, a first crushing stone 440 inside the first crushing tank 400, a first lifting rod 450 at the upper end of the first crushing stone 440, and the first lifting rod 450 connected to the first hydraulic cylinder 430.

[0026] A dissolving device, comprising a first dissolving tank 300, a first drive motor 310 at the upper end of the first dissolving tank 300, a first stirring shaft 320 at the lower end of the first drive motor 310, a first stirring paddle 330 at the lower end of the first stirring shaft 320, a first feed inlet 340 at the upper end of the first dissolving tank 300, and a first discharge outlet 350 at the lower end of the first dissolving tank 300;

[0027] The concentration device includes a first concentration tank 100, a second inlet 150 at the upper end of the first concentration tank 100, the second inlet 150 matching the first outlet 350, a second outlet 160 at the lower end of the first concentration tank 100, and a heating and evaporation mechanism inside the first concentration tank 100.

[0028] First, lotus root pieces are placed into the first crushing tank 400. The first hydraulic cylinder 430 drives the first lifting rod 450 to repeatedly rise and fall, continuously crushing the lotus root pieces into powder. Then, the lotus root powder and water are fed into the first dissolving tank 300 through the first feed inlet 340. The first drive motor 310 drives the first stirring shaft 320 to rotate, which in turn drives the first stirring paddle 330 to rotate, accelerating the thorough mixing of tea powder and water, thus accelerating the extraction of tea polyphenols. The first crushing blade 360 ​​can also crush the tea powder in the first dissolving tank 300, accelerating the extraction of tea polyphenols. After the tea polyphenols have been fully extracted, the diluted tea polyphenol solution is sent into the first concentration tank through the first discharge port 350 and the second feed inlet 150.

[0029] Furthermore, the upper end of the first crushing tank 400 is provided with a first feeding hopper 410, and the lower end of the first crushing tank 400 is provided with a first discharge port 420. The first discharge port 420 is hinged to a first sealing gate 460, and the first sealing gate 460 is provided with a first sealing ring 461. The first sealing gate 460 can close the first discharge port 420, and the first sealing ring 461 can ensure the sealing between the first sealing gate 460 and the first discharge port 420, preventing the lotus root pieces from falling out.

[0030] Further, the heating and evaporation mechanism includes a first heating plate 110, a second heating plate 120, and a third heating plate 130. The first heating plate 110 is located at the left end of the first concentration tank 100 and is inclined downwards to the right. The second heating plate 120 is located at the right end of the first concentration tank 100 and is inclined downwards to the left. The third heating plate 130 is located below the first heating plate 110 and is inclined downwards to the right. The second discharge port 160 corresponds to the third heating plate 130. The dilute catechin solution passes sequentially through the first heating plate 110, the second heating plate 120, and the third heating plate 130, undergoing heating and evaporation to achieve concentration of the dilute tea polyphenol solution. The evaporated water vapor rises and contacts the steam condensation mechanism, where it condenses into water droplets.

[0031] Furthermore, the upper end of the first concentration tank 100 is provided with a steam condensation mechanism, which includes a first condensing plate 200 and a first water receiving tank 250. The first condensing plate 200 is disposed at the upper end of the first concentration tank 100 and is inclined to the lower right. The first water receiving tank 250 is disposed at the right end of the first concentration tank 100 and corresponds to the lower part of the first condensing plate 200. The right end of the first water receiving tank 250 passes through the first concentration tank 100 and is provided with a first drain pipe 251.

[0032] Furthermore, the steam condensation mechanism includes a first air cooler, which is located outside the first concentration tank 100. The first condensation plate 200 has a first S-shaped cavity 230. One end of the first S-shaped cavity 230 has a first air inlet pipe 220, and the other end of the first S-shaped cavity 230 has a first air outlet pipe 210. The first air inlet pipe 220 and the first air outlet pipe 210 are connected to the first air cooler.

[0033] The first air cooler introduces cold air into the first S-shaped cavity 230 through the first air inlet pipe 220, absorbing the heat from the first condenser plate 200. This allows water vapor to quickly condense into water droplets upon contact with the first condenser plate 200. Meanwhile, the hot air blown out from the first air outlet pipe 210 is cooled again by the first air cooler and blown into the first S-shaped cavity 230. After being heated and evaporated by the first heating plate 110, the second heating plate 120, and the third heating plate 130, the water in the dilute complex catechin solution evaporates. The water vapor rises and comes into contact with the first condenser plate 200, where it condenses into water droplets and slides down the first condenser plate 200 into the first water collection tank 250. The water is then drained through the first drain pipe 251, ensuring that the water content in the first concentration tank 100 continuously decreases.

[0034] Furthermore, the lower end of the first condenser plate 200 is provided with a plurality of first dovetail grooves 240, and the right end of the first dovetail groove 240 is provided with a first water-guiding rope 260, the other end of the first water-guiding rope 260 being disposed in the first water-receiving tank 250. When the first condenser plate 200 condenses water vapor, the first dovetail grooves 240 can adsorb water droplets and guide the water droplets to the end of the first dovetail grooves 240. Through the guidance of the first water-guiding rope 250, the water droplets flow into the first water-receiving tank 250, reducing the probability of water droplets dripping back into the complex catechin solution, thereby improving the extraction efficiency of complex catechins.

[0035] It is worth mentioning that the technical features such as the first air conditioner involved in this utility model patent application should be regarded as prior art. The specific structure, working principle, and possible control methods and spatial arrangement of these technical features can be adopted using conventional choices in the field, and should not be regarded as the utility model point of this utility model patent. This utility model patent will not be further elaborated in detail.

[0036] For those skilled in the art, modifications can still be made to the technical solutions described in the foregoing embodiments, or equivalent substitutions can be made to some of the technical features. Any modifications, equivalent substitutions, improvements, etc., made within the spirit and principles of this utility model should be included within the protection scope of this utility model.

Claims

1. A compound catechin extraction device, characterized in that, include: A crushing device, comprising a first crushing tank (400), a first hydraulic cylinder (430) at the upper end of the first crushing tank (400), a first crushing stone (440) inside the first crushing tank (400), a first lifting rod (450) at the upper end of the first crushing stone (440), and the first lifting rod (450) being connected to the first hydraulic cylinder (430); A dissolving device, comprising a first dissolving tank (300), a first drive motor (310) at the upper end of the first dissolving tank (300), a first stirring shaft (320) at the lower end of the first drive motor (310), a first stirring paddle (330) at the lower end of the first stirring shaft (320), a first feed inlet (340) at the upper end of the first dissolving tank (300), and a first discharge outlet (350) at the lower end of the first dissolving tank (300). The concentration device includes a first concentration tank (100), the upper end of the first concentration tank (100) is provided with a second inlet (150), the second inlet (150) is matched with the first outlet (350), the lower end of the first concentration tank (100) is provided with a second outlet (160), and the first concentration tank (100) is provided with a heating and evaporation mechanism.

2. The compound catechin extraction device according to claim 1, characterized in that, The first crushing tank (400) is provided with a first feeding hopper (410) at its upper end and a first discharge port (420) at its lower end. The first discharge port (420) is hinged to a first sealing door (460) and a first sealing ring (461) is provided on the first sealing door (460).

3. The compound catechin extraction device according to claim 2, characterized in that, The heating and evaporation mechanism includes a first heating plate (110), a second heating plate (120), and a third heating plate (130). The first heating plate (110) is located at the left end of the first concentration tank (100) and is inclined to the lower right. The second heating plate (120) is located at the right end of the first concentration tank (100) and is inclined to the lower left. The third heating plate (130) is located below the first heating plate (110) and is inclined to the lower right. The second discharge port (160) corresponds to the third heating plate (130).

4. The compound catechin extraction device according to claim 3, characterized in that, The upper end of the first concentration tank (100) is provided with a steam condensation mechanism, which includes a first condensing plate (200) and a first water receiving tank (250). The first condensing plate (200) is located at the upper end of the first concentration tank (100) and is inclined to the lower right. The first water receiving tank (250) is located at the right end of the first concentration tank (100) and corresponds to the lower part of the first condensing plate (200). The right end of the first water receiving tank (250) passes through the first concentration tank (100) and is provided with a first drain pipe (251).

5. The compound catechin extraction device according to claim 4, characterized in that, The steam condensation mechanism includes a first air cooler, which is located outside the first concentration tank (100). The first condenser plate (200) has a first S-shaped cavity (230). One end of the first S-shaped cavity (230) has a first air inlet pipe (220), and the other end of the first S-shaped cavity (230) has a first air outlet pipe (210). The first air inlet pipe (220) and the first air outlet pipe (210) are connected to the first air cooler.

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