CN211216312U - Continuous production line for matcha pulp - Google Patents
Continuous production line for matcha pulp Download PDFInfo
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- CN211216312U CN211216312U CN201921862174.3U CN201921862174U CN211216312U CN 211216312 U CN211216312 U CN 211216312U CN 201921862174 U CN201921862174 U CN 201921862174U CN 211216312 U CN211216312 U CN 211216312U
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Abstract
The utility model provides a matcha thick liquid continuous type production line belongs to tealeaves deep-processing technical field. It includes solvent tank and blending tank, the solvent tank connect the blending tank, the blending tank on be equipped with the stirring subassembly, the blending tank bottom is connected with the circulating pump, blending tank and booster pump are connected respectively to the export of circulating pump, solid liquid mixer is connected to the booster pump, UHT steriliser is connected to solid liquid mixer, and the liquid filling machine is connected to the UHT steriliser, is equipped with first valve on the pipeline between circulating pump and blending tank, is equipped with the second valve on the pipeline between circulating pump and booster pump. The utility model discloses the process can realize the intensive mixing of green tea powder and solvent to realize the disinfection and the guarantee of continuous type, obtain green tea thick liquid.
Description
Technical Field
The utility model belongs to the technical field of tealeaves deep-processing, a tea slurry continuous type production line is related to.
Background
The matcha is a micro-powder tea product which is prepared by taking fresh tea leaves cultivated in a covering way, deactivating enzyme with steam or hot air, drying to prepare leaves as raw materials and grinding the leaves. With the development of the food field, the making requirement of matcha is higher and higher, and tea leaves are made into a tea ball after being steamed and de-enzymed; when drinking, the tea-ball is crushed into small blocks, then ground into fine powder, taken out for drinking, and tasted.
At present, with the development of tea cultivation technology and the rapid promotion of industrialization, environmental and health problems are increasingly prominent, and under the background, the production and research and development of natural nutritional products such as matcha and the like are rapidly developed. Some tea enterprises expand the business to the field of consumption terminals, and are widely applied to baking products, flour products, tea beverages, dairy products and other health-care foods. The appearance of matcha changes the consumption of tea from drinking tea to eating tea, and can completely absorb all the nutrient substances in the tea. The powdered material of the matcha is extremely fine and smooth and is easy to be absorbed by human bodies, but the fine and smooth texture is easy to cause agglomeration in the brewing or homogenizing process, and a large amount of small powdered particles are always remained under the condition of no professional tea constitution or homogenizing machine, so that the quality of the applied product is reduced.
People continuously explore, and consider that the matcha powder is mixed with solvents such as water in advance to prepare the matcha pulp, so that the problem of conglobation when the matcha powder is brewed can be avoided, and special equipment is required to prepare the matcha pulp.
SUMMERY OF THE UTILITY MODEL
The utility model aims at the above-mentioned problem, provide a matcha thick liquid continuous type production line.
In order to achieve the above purpose, the utility model adopts the following technical proposal:
the utility model provides a matcha thick liquid continuous type production line, includes solvent jar and blending tank, the solvent jar connect the blending tank, the blending tank on be equipped with the stirring subassembly, the blending tank bottom is connected with the circulating pump, blending tank and booster pump are connected respectively to the export of circulating pump, solid liquid mixer is connected to the booster pump, UHT steriliser is connected to solid liquid mixer, UHT steriliser connects the liquid filling machine, is equipped with first valve on the pipeline between circulating pump and blending tank, is equipped with the second valve on the pipeline between circulating pump and booster pump.
In the continuous production line of the tea spread slurry, a buffer tank is arranged between the UHT sterilizer and the filling machine, a discharge port of the UHT sterilizer is connected with the buffer tank, and the bottom of the buffer tank is connected with the filling machine through a delivery pump.
In the continuous production line of the tea-smearing pulp, a third valve is arranged between the solid-liquid mixer and the UHT sterilizer, and the solvent tank is connected with the mixing tank by a solvent pump.
In foretell matcha thick liquid continuous type production line, first valve connect the blending tank through fourth valve and fifth valve respectively, the fourth valve passes through the pipe connection blending tank and this pipeline extends to stirring component below, the fifth valve passes through the pipe connection blending tank.
In foretell tea-smearing slurry continuous type production line, the fourth valve passes through the pipe connection blender, the blender be located stirring subassembly below, the inside cavity that is of blender, the blender outer wall gathers there is the hole of mixing, the fifth valve passes through the pipe connection gondola water faucet head, the gondola water faucet head is located the top of blending tank.
In foretell tea-smearing slurry continuous type production line, the blender be the cavity tube-shape, the blender top is flat, the lateral wall and the bottom of blender all gather and have the hole of mixing, the gondola water faucet be located mixing tank top to the last 1/3 regions of bottom linear distance.
In foretell matcha thick liquid continuous type production line, the stirring subassembly including being located the inside stirring rake of blending tank, the stirring rake passes through reduction gear and connects the motor, reduction gear and motor are located the blending tank outside.
In the continuous production line of the matcha pulp, the mixer is positioned below the stirring paddle, and the aperture of the mixing hole is between 200 meshes and 300 meshes.
In the continuous production line of the tea spread pulp, a filter is arranged between the solid-liquid mixer and the third valve, and the aperture of the filter is 100 meshes.
In foretell tea-spreading thick liquid continuous type production line, the filter include first flange and second flange, be equipped with the holding chamber that is used for holding the filter screen on the first flange, first flange and second flange spiro union cooperation and compress tightly the filter screen in the holding intracavity of first flange, the aperture of filter screen be 100 meshes, first flange joint solid-liquid mixer, second flange joint third valve.
Compared with the prior art, the utility model has the advantages of:
1. the utility model discloses the process can realize the intensive mixing of green tea powder and solvent to realize the disinfection and the guarantee of continuous type, obtain green tea thick liquid.
2. After multiple filtration by a mixer, a solid-liquid mixer and a filter, the spread tea slurry with fine particles and uniform mixing is obtained, so that the quality characteristic of the spread tea slurry is improved.
3. The mixing process is rapid and uniform, and the mixing speed is rapid.
Additional advantages, objects, and features of the invention will be set forth in part in the description which follows and in part will become apparent to those having ordinary skill in the art upon examination of the following or may be learned from practice of the invention.
Drawings
Fig. 1 is a schematic structural diagram of the present invention.
Figure 2 is a schematic view of the bottom of the shower head.
Fig. 3 is a schematic view of a filter.
Fig. 4 is a schematic diagram of a blender.
In the figure: the device comprises a solvent tank 1, a mixing tank 2, a feeding port 2a, a stirring component 3, a circulating pump 4, a booster pump 5, a solid-liquid mixer 6, a UHT sterilizer 7, a filling machine 8, a first valve 9, a second valve 10, a buffer tank 11, a delivery pump 12, a third valve 13, a solvent pump 14, a fourth valve 15, a fifth valve 16, a mixer 17, a mixing hole 18, a shower head 19, a stirring paddle 20, a speed reducer 21, a motor 22, a filter 23, a first flange 24, a second flange 25 and a filter screen 27.
Detailed Description
The present invention will be further explained with reference to the accompanying drawings.
As shown in fig. 1-2, a matcha thick liquid continuous production line, includes solvent jar 1 and blending tank 2, solvent jar 1 connect blending tank 2, blending tank 2 top is equipped with dog-house 2a for throw in solid-like matcha powder, blending tank 2 on be equipped with stirring assembly 3, stirring assembly 3 is including being located blending tank 2 inside stirring rake 20, stirring rake 20 passes through reduction gear 21 and connects motor 22, reduction gear 21 and motor 22 are located blending tank 2 outsidely, motor 22 drives speed reducer 21 and rotates to drive stirring rake 20 and rotate.
The bottom of the mixing tank 2 is connected with a circulating pump 4, the circulating pump 4 is preferably a turbine pump, the outlet of the circulating pump 4 is respectively connected with the mixing tank 2 and a booster pump 5, the booster pump 5 is preferably a multi-stage high-pressure pump or a gear pump, the booster pump 5 is connected with a solid-liquid mixer 6, the solid-liquid mixer 6 is connected with a UHT sterilizer 7, the UHT sterilizer 7 is connected with a filling machine 8, a first valve 9 is arranged on a pipeline between the circulating pump 4 and the mixing tank 2, and a second valve 10 is arranged on a pipeline between the circulating pump 4 and the booster pump. The solid-liquid mixer 6 is a conventional technology, can adopt a commercially available product, and is used for improving the mixing effect between the solvent and the matcha powder to make the matcha pulp more uniform, and the UHT sterilizer 7 is an ultrahigh-temperature instantaneous sterilizer and adopts a commercially available product.
Preferably, a buffer tank 11 is arranged between the UHT sterilizer 7 and the filling machine 8, a discharge port of the UHT sterilizer 7 is connected with the buffer tank 11, the bottom of the buffer tank 11 is connected with the filling machine 8 through a delivery pump 12, materials coming out of the UHT sterilizer 7 are temporarily stored through the buffer tank 11, and when the materials reach a certain amount, the materials are filled through the filling machine 8.
In this embodiment, a third valve 13 is provided between the solid-liquid mixer 6 and the UHT sterilizer 7, the solvent tank 1 is connected to the mixing tank 2 by a solvent pump 14, the pressure at the outlet of the booster pump 5 can be adjusted by adjusting the third valve 13, and a pressure gauge is provided between the booster pump 5 and the solid-liquid mixer 6 for reading the pressure.
The first valve 9 is respectively connected with the mixing tank 2 through a fourth valve 15 and a fifth valve 16, the fourth valve 15 is connected with the mixing tank 2 through a pipeline, the pipeline extends to the lower part of the stirring component 3, and the fifth valve 16 is connected with the mixing tank 2 through a pipeline. In the circulation process, the fifth valve 16 and the second valve 10 are closed, the first valve 9 and the fourth valve 15 are opened, the materials enter the lower part of the stirring paddle 20, and the bottom stirring effect is realized on the materials, so that the matcha powder and the solvent can be quickly mixed.
Specifically, the fourth valve 15 is connected with the mixer 17 through a pipeline, the mixer 17 is located below the stirring assembly 3, the mixer 17 is hollow, mixing holes 18 are densely distributed in the outer wall of the mixer 17 and play a role in filtering, the fifth valve 16 is connected with the shower head 19 through a pipeline, the shower head 19 is located at the top of the mixing tank 2, as shown in fig. 2, small holes are formed in the bottom of the shower head 19, and the shower head can be a commercially available product or a conical hollow structure.
Because the green tea powder is light, although the green tea powder is stirred by the stirring paddle 20, the green tea powder is still not easy to be quickly mixed with the solvent, and the liquid mixture sprayed by the shower head 19 is poured on the green tea powder, so that the green tea powder can be quickly wetted, and then is quickly mixed with the solvent to form green tea slurry. The mixing holes 18 play a role of primary filtration, and break up the caked matcha powder, so that matcha pulp can be quickly homogenized. In this embodiment, the mixer 17 is located below the stirring paddle 20, and the aperture of the mixing hole 18 is between 200 and 300 meshes. The aperture of the shower head 19 is between 30 and 40 meshes, so that the blockage is prevented.
Referring to fig. 4, in this embodiment, the mixer 17 is hollow and cylindrical, the top of the mixer 17 is flat without holes, so as to be fixedly connected with the pipeline, the side wall and the bottom of the mixer 17 are densely distributed with mixing holes 18, and the shower head 19 is located at the upper 1/3 area of the linear distance from the top to the bottom of the mixing tank 2. The upper 1/3 area is defined as the length of the mixing tank 2 measured by the top and bottom of the mixing tank, and the upper 1/3 area of the length is the range where the shower head 19 can be installed.
As described above, the matcha pulp passing through the mixing hole 18 has been primarily broken, but the particle size of the matcha powder still needs to be further reduced, in this embodiment, the filter 23 is disposed between the solid-liquid mixer 6 and the third valve 13, the pore size of the filter 23 is 100 meshes, and the particle size of the matcha pulp passing through the filter 23 is smaller than 100 meshes.
Specifically, as shown in fig. 3, the filter 23 includes a first flange 24 and a second flange 25, the first flange 24 is provided with an accommodating cavity for accommodating the filter screen 27, the first flange 24 and the second flange 25 are screwed and matched to compress the filter screen 27 in the accommodating cavity of the first flange, the aperture of the filter screen 27 is 100 meshes, the first flange 24 is connected to the solid-liquid mixer 6, and the second flange 25 is connected to the third valve 13. The first flange 24 and the second flange 25 can be directly screwed or screwed through bolts, preferably, the bolts are screwed, so that the filter screen 27 is convenient to detach and replace.
In this embodiment, if no special description is provided, each pump may be a commercially available turbo pump, multi-stage pump, gear pump or screw pump, and those skilled in the art may select the type of the pump according to actual needs, which is not described herein again.
The utility model discloses a working process is:
according to the proportion of matcha powder and solvent, putting solvent such as water and additive such as VC into a solvent tank 1, stirring and dissolving, putting matcha powder into a mixing tank 2 through a feeding port 2a, starting a solvent pump 14, inputting the solvent in the solvent tank 1 into the mixing tank 2, starting a motor 22 to drive a stirring paddle 20 to rotate, closing a second valve 10 and a fifth valve 16, opening a first valve 9 and a fourth valve 15, starting a circulating pump 4, circulating a mixed solution through a pipeline, spraying out the mixed solution from a mixing hole 18 of a mixer 17, stirring the solution from the lower part of the stirring paddle to accelerate the mixing of the matcha powder and the solvent, circulating for about 30-60mins, opening the fifth valve 16, spraying out the mixed solution from a shower head 19, spraying matcha powder from top to bottom to accelerate the sinking of the matcha powder to mix with the solvent, closing the first valve 9, opening the second valve 10 after 30-60mins, and (3) starting a booster pump 5, adjusting the opening degree of a third valve 13 to adjust the outlet pressure of the booster pump 5, mixing the matcha pulp through a solid-liquid mixer 6, filtering the matcha pulp through a filter 23, sterilizing the matcha pulp in a UHT sterilizer 7, feeding the sterilized matcha pulp into a buffer tank 11, starting a delivery pump 12, feeding the matcha pulp into a filling machine for filling to obtain the filled matcha pulp, and refrigerating and storing the matcha pulp.
The specific embodiments described herein are merely illustrative of the spirit of the invention. Various modifications, additions and substitutions for the specific embodiments described herein may be made by those skilled in the art without departing from the spirit of the invention or exceeding the scope of the invention as defined in the accompanying claims.
Although the terms solvent tank 1, mixing tank 2, feed port 2a, agitation assembly 3, circulation pump 4, booster pump 5, solid-liquid mixer 6, UHT sterilizer 7, filling machine 8, first valve 9, second valve 10, buffer tank 11, transfer pump 12, third valve 13, solvent pump 14, fourth valve 15, fifth valve 16, mixer 17, mixing hole 18, shower head 19, paddle 20, decelerator 21, motor 22, filter 23, first flange 24, second flange 25, filter screen 27, etc., are used more herein, the possibility of using other terms is not excluded. These terms are used merely to more conveniently describe and explain the nature of the present invention and should not be interpreted as imposing any additional limitations that are contrary to the spirit of the present invention.
Claims (10)
1. The utility model provides a matcha thick liquid continuous type production line, includes solvent jar (1) and blending tank (2), solvent jar (1) connect blending tank (2), blending tank (2) on be equipped with stirring subassembly (3), its characterized in that, blending tank (2) bottom is connected with circulating pump (4), blending tank (2) and booster pump (5) are connected respectively to the export of circulating pump (4), solid liquid mixer (6) is connected in booster pump (5), UHT steriliser (7) is connected in solid liquid mixer (6), liquid filling machine (8) are connected in UHT steriliser (7), be equipped with first valve (9) on the pipeline between circulating pump (4) and blending tank (2), be equipped with second valve (10) on the pipeline between circulating pump (4) and booster pump (5).
2. The continuous matcha pulp production line of claim 1, wherein a buffer tank (11) is arranged between the UHT sterilizer (7) and the filling machine (8), the discharge port of the UHT sterilizer (7) is connected with the buffer tank (11), and the bottom of the buffer tank (11) is connected with the filling machine (8) through a delivery pump (12).
3. The continuous matcha pulp production line of claim 1, wherein a third valve (13) is arranged between the solid-liquid mixer (6) and the UHT sterilizer (7), and the solvent tank (1) is connected with the mixing tank (2) by a solvent pump (14).
4. The continuous matcha pulp production line of claim 3, wherein the first valve (9) is connected with the mixing tank (2) through a fourth valve (15) and a fifth valve (16), respectively, the fourth valve (15) is connected with the mixing tank (2) through a pipeline, the pipeline extends to the lower part of the stirring assembly (3), and the fifth valve (16) is connected with the mixing tank (2) through a pipeline.
5. The matcha pulp continuous production line of claim 4, characterized in that the fourth valve (15) is connected with the mixer (17) through a pipeline, the mixer (17) is arranged below the stirring component (3), the mixer (17) is hollow, the outer wall of the mixer (17) is densely provided with mixing holes (18), the fifth valve (16) is connected with the shower head (19) through a pipeline, and the shower head (19) is arranged at the top of the mixing tank (2).
6. The continuous matcha pulp production line of claim 5, wherein the mixer (17) is hollow cylinder, the top of the mixer (17) is flat, the side wall and the bottom of the mixer (17) are provided with mixing holes (18), and the shower head (19) is positioned in the upper 1/3 area of the straight line distance from the top to the bottom of the mixing tank (2).
7. The continuous matcha pulp production line of claim 6, wherein the stirring assembly (3) comprises a stirring paddle (20) positioned inside the mixing tank (2), the stirring paddle (20) is connected with a motor (22) through a speed reducer (21), and the speed reducer (21) and the motor (22) are positioned outside the mixing tank (2).
8. The continuous production line of matcha pulp as claimed in claim 7, wherein the mixer (17) is located below the stirring paddle (20), and the diameter of the mixing hole (18) is between 200 and 300 meshes.
9. The continuous production line of matcha pulp as claimed in claim 3, wherein a filter (23) is arranged between the solid-liquid mixer (6) and the third valve (13), and the pore size of the filter (23) is 100 meshes.
10. The matcha pulp continuous production line of claim 9, wherein the filter (23) comprises a first flange (24) and a second flange (25), the first flange (24) is provided with a containing cavity for containing the filter screen (27), the first flange (24) and the second flange (25) are in threaded fit and press the filter screen (27) in the containing cavity of the first flange, the aperture of the filter screen (27) is 100 meshes, the first flange (24) is connected with the solid-liquid mixer (6), and the second flange (25) is connected with the third valve (13).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921862174.3U CN211216312U (en) | 2019-10-31 | 2019-10-31 | Continuous production line for matcha pulp |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201921862174.3U CN211216312U (en) | 2019-10-31 | 2019-10-31 | Continuous production line for matcha pulp |
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| CN211216312U true CN211216312U (en) | 2020-08-11 |
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| CN201921862174.3U Active CN211216312U (en) | 2019-10-31 | 2019-10-31 | Continuous production line for matcha pulp |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111999489A (en) * | 2020-09-21 | 2020-11-27 | 上海科华生物工程股份有限公司 | Filtering and dispersing equipment and method for continuous production of latex immunoturbidimetry |
-
2019
- 2019-10-31 CN CN201921862174.3U patent/CN211216312U/en active Active
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN111999489A (en) * | 2020-09-21 | 2020-11-27 | 上海科华生物工程股份有限公司 | Filtering and dispersing equipment and method for continuous production of latex immunoturbidimetry |
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