CN220788314U - Ultra-filtration device is used in production of mulberry leaf tea - Google Patents
Ultra-filtration device is used in production of mulberry leaf tea Download PDFInfo
- Publication number
- CN220788314U CN220788314U CN202322394650.6U CN202322394650U CN220788314U CN 220788314 U CN220788314 U CN 220788314U CN 202322394650 U CN202322394650 U CN 202322394650U CN 220788314 U CN220788314 U CN 220788314U
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- ultrafiltration
- mulberry leaf
- leaf tea
- sleeve
- filter
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- 238000000108 ultra-filtration Methods 0.000 title claims abstract description 72
- 240000000249 Morus alba Species 0.000 title claims abstract description 40
- 235000008708 Morus alba Nutrition 0.000 title claims abstract description 40
- 244000269722 Thea sinensis Species 0.000 title claims abstract 10
- 238000004519 manufacturing process Methods 0.000 title claims description 9
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 59
- 238000005189 flocculation Methods 0.000 claims abstract description 29
- 230000016615 flocculation Effects 0.000 claims abstract description 29
- 239000012528 membrane Substances 0.000 claims abstract description 25
- 239000000919 ceramic Substances 0.000 claims abstract description 21
- 238000004062 sedimentation Methods 0.000 claims abstract description 19
- 239000007788 liquid Substances 0.000 claims abstract description 16
- 239000012530 fluid Substances 0.000 claims description 2
- 238000011001 backwashing Methods 0.000 claims 1
- 238000001914 filtration Methods 0.000 abstract description 27
- 230000000694 effects Effects 0.000 abstract description 10
- 239000000706 filtrate Substances 0.000 abstract description 3
- 241001122767 Theaceae Species 0.000 description 28
- 239000000126 substance Substances 0.000 description 9
- 230000009286 beneficial effect Effects 0.000 description 5
- 230000009471 action Effects 0.000 description 4
- 238000011010 flushing procedure Methods 0.000 description 4
- 239000008280 blood Substances 0.000 description 3
- 210000004369 blood Anatomy 0.000 description 3
- 238000005192 partition Methods 0.000 description 3
- 230000002159 abnormal effect Effects 0.000 description 2
- 230000036772 blood pressure Effects 0.000 description 2
- HVYWMOMLDIMFJA-DPAQBDIFSA-N cholesterol Chemical compound C1C=C2C[C@@H](O)CC[C@]2(C)[C@@H]2[C@@H]1[C@@H]1CC[C@H]([C@H](C)CCCC(C)C)[C@@]1(C)CC2 HVYWMOMLDIMFJA-DPAQBDIFSA-N 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- OYPRJOBELJOOCE-UHFFFAOYSA-N Calcium Chemical compound [Ca] OYPRJOBELJOOCE-UHFFFAOYSA-N 0.000 description 1
- 206010020772 Hypertension Diseases 0.000 description 1
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 1
- 230000032683 aging Effects 0.000 description 1
- 230000003796 beauty Effects 0.000 description 1
- 239000011575 calcium Substances 0.000 description 1
- 229910052791 calcium Inorganic materials 0.000 description 1
- 235000001465 calcium Nutrition 0.000 description 1
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- 230000007547 defect Effects 0.000 description 1
- 230000009982 effect on human Effects 0.000 description 1
- 230000004438 eyesight Effects 0.000 description 1
- 230000036449 good health Effects 0.000 description 1
- 230000002401 inhibitory effect Effects 0.000 description 1
- 230000000968 intestinal effect Effects 0.000 description 1
- 239000000463 material Substances 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000027939 micturition Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 150000002978 peroxides Chemical class 0.000 description 1
- 239000011591 potassium Substances 0.000 description 1
- 229910052700 potassium Inorganic materials 0.000 description 1
- 235000007686 potassium Nutrition 0.000 description 1
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- 239000011573 trace mineral Substances 0.000 description 1
- 235000013619 trace mineral Nutrition 0.000 description 1
- 235000019155 vitamin A Nutrition 0.000 description 1
- 239000011719 vitamin A Substances 0.000 description 1
- 235000010374 vitamin B1 Nutrition 0.000 description 1
- 239000011691 vitamin B1 Substances 0.000 description 1
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- 239000011716 vitamin B2 Substances 0.000 description 1
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- 239000011708 vitamin B3 Substances 0.000 description 1
- 235000019154 vitamin C Nutrition 0.000 description 1
- 239000011718 vitamin C Substances 0.000 description 1
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model discloses an ultrafiltration device for producing mulberry leaf tea, which comprises a sedimentation tank, wherein the middle part of the sedimentation tank is connected with a filter through a water pipe, the lower end of the filter is connected with a water inlet at the lower end of a micro vortex flocculation tank through a water pipe and a water supply pump, the water outlet end of the micro vortex flocculation tank is connected with the water inlet end at the lower end of an ultrafiltration sleeve through a water pipe and a water supply pump, the middle part of the ultrafiltration sleeve is an ultrafiltration cavity, a plurality of ceramic membrane pipes are arranged in the ultrafiltration cavity, a plurality of ultrasonic transducers are arranged at the upper end and the lower end of the ultrafiltration sleeve, the ultrasonic transducers are in one-to-one correspondence with the ceramic membrane pipes, a concentrated water outlet is arranged above the ultrafiltration sleeve and is communicated with the ceramic membrane pipes, and an ultrafiltration water outlet and a liquid outlet are respectively arranged at the upper end and the lower end of the ultrafiltration cavity. The three-stage filtration is carried out on the mulberry leaf tea, so that the effect of full filtration is achieved, and the problems that the filtration of the mulberry leaf tea is insufficient, residues easily enter filtrate and the like in the prior art are effectively solved.
Description
Technical Field
The utility model belongs to the technical field of production equipment, and particularly relates to an ultrafiltration device for producing mulberry leaf tea.
Background
Modern medical research shows that mulberry leaves contain rich potassium, calcium, vitamins C, B1, B2, B3, A and other trace elements required by human bodies, have the unique effects of reducing blood pressure, reducing blood sugar, resisting aging, increasing endurance, reducing blood fat content, reducing cholesterol, inhibiting intestinal harmful bacteria proliferation, generating peroxide and the like, and have good health care effect on human bodies. The mulberry leaf tea prepared from the mulberry leaves can clear heat, improve eyesight, and has the functions of reducing blood pressure, reducing blood fat and promoting urination, so that the mulberry leaf tea is very popular with patients with hypertension (especially the elderly). In the production process of the mulberry leaf tea, the mulberry leaf tea needs to be sufficiently filtered, so that the mulberry leaf tea is convenient for consumers to drink, but the conventional filtering device cannot sufficiently filter, and residues always enter the final filtrate, so that the filtering effect is poor, and the taste of the product is affected.
Disclosure of Invention
Aiming at the defects, the ultrafiltration device for producing the mulberry leaf tea is simple in structure and convenient to use, three-stage filtration is carried out on the mulberry leaf tea, the effect of full filtration is achieved, and the problems that the filtration of the mulberry leaf tea is insufficient, residues are easy to enter filtrate and the like in the prior art are effectively solved.
In order to achieve the above purpose, the technical scheme adopted by the utility model for solving the technical problems is as follows: the utility model provides an ultrafiltration device is used in production of mulberry leaf tea, including the sedimentation tank, the sedimentation tank middle part is connected with the filter through the water pipe, the filter lower extreme is connected with little vortex flocculation tank lower extreme water inlet through water pipe and working shaft, little vortex flocculation tank water outlet end is connected with ultrafiltration sleeve pipe lower extreme water inlet end through water pipe and working shaft, ultrafiltration sleeve pipe middle part is the ultrafiltration chamber, ultrafiltration intracavity sets up a plurality of ceramic membrane pipes, both ends all are provided with a plurality of ultrasonic transducer about the ultrafiltration sleeve pipe, and ultrasonic transducer and ceramic membrane pipe one-to-one, ultrafiltration sleeve pipe top is provided with concentrated delivery port, concentrated delivery port communicates with each other with the ceramic membrane pipe, both ends are provided with ultrafiltration delivery port and leakage fluid dram respectively about the ultrafiltration chamber.
The beneficial effects of the utility model are as follows: after the production of the mulberry leaf tea is completed, the mulberry leaf tea is put into a sedimentation tank for storage and sedimentation, the mulberry leaf tea is put into a filter through a water pipe in the middle of the sedimentation tank for preliminary filtration, filtered mixed liquor is put into a micro vortex flocculation tank through the action of a water supply pump, some substances in the mixed liquor are precipitated under the action of micro vortex, the mixed liquor is further filtered and sedimentated, then the mixed liquor enters from the lower water inlet end of an ultrafiltration sleeve through the water supply pump from the water outlet end of the upper part of the micro vortex flocculation tank, substances smaller than the drift diameter of the substances are led into an ultrafiltration cavity through the ceramic membrane pipe by the pressure difference between the inner and outer sides of the membrane of the ceramic membrane pipe, at the moment, concentrated liquor after filtration and concentration can be discharged and stored through a concentrated water outlet, and liquid in the ultrafiltration cavity can be discharged through the ultrafiltration water outlet. Meanwhile, when the ultrafiltration membrane tube works, the throughput of the ceramic membrane tube can be kept by adjusting and controlling the ultrasonic transducers at the upper end and the lower end; the ultrasonic transducers at the upper end and the lower end and corresponding power can be started when the flow is found to be smaller, the ceramic membrane tube is sufficiently cleaned, long-time working and use are facilitated, flushing is fast and convenient, and the use efficiency of the whole device is improved. And the device carries out tertiary filtration through sedimentation tank, little vortex flocculation tank and ultrafiltration sleeve pipe, realizes fully filtering the mulberry leaf tea, avoids residue and the sediment material to remain in liquid, has still realized the concentration of mulberry leaf tea to a certain extent, and it is very convenient to use.
Further, a plurality of filter screens are arranged in the filter.
The beneficial effects of adopting the further scheme are as follows: the multi-layer filter screen is used for carrying out preliminary filtration on the mulberry leaf tea from the sedimentation tank, and is convenient for carrying out subsequent filtration procedures.
Further, the number of the filter meshes is 50-150 meshes.
Further, a plurality of baffle plates are arranged in the micro-vortex flocculation tank in a staggered way.
The beneficial effects of adopting the further scheme are as follows: the arrangement of the partition plate can increase the passing path and the residence time of the mulberry leaf tea in the micro-vortex flocculation tank, so that the mulberry leaf tea is subjected to full flocculation filtration, the filtration effect is enhanced, and the filtration effect is better.
Further, a liquid storage tank for back flushing is arranged above the micro vortex flocculation tank.
The beneficial effects of adopting the further scheme are as follows: after the micro-vortex flocculation tank is used for a certain time, the micro-vortex flocculation tank can be flushed from top to bottom through liquid in the liquid storage tank, so that substances deposited in the tank are prevented from affecting the filtering effect.
Further, the water inlet end, the ultrafiltration water outlet and the concentration water outlet of the ultrafiltration sleeve are all provided with flow meters.
The beneficial effects of adopting the further scheme are as follows: the working condition of the ultrafiltration sleeve is observed through the flowmeter, when abnormal changes occur, the ultrafiltration sleeve is timely processed, if the flow is reduced, the ultrasonic transducers at the upper end and the lower end of the ultrafiltration sleeve are timely started to clean the ultrafiltration sleeve, and the normal operation of the device is ensured.
Drawings
FIG. 1 is a schematic illustration of the present utility model;
wherein, 1, a sedimentation tank; 2. a filter; 3. a micro vortex flocculation tank; 4. a partition plate; 5. an ultrafiltration sleeve; 6. a ceramic membrane tube; 7. a liquid outlet; 8. ultrafiltering a water outlet; 9. concentrating the water outlet; 10. an ultrasonic transducer; 11. a water supply pump; 12. and a liquid storage tank.
Detailed Description
The following describes the embodiments of the present utility model in detail with reference to the drawings.
In one embodiment of the utility model, as shown in fig. 1, an ultrafiltration device for producing mulberry leaf tea is provided, which comprises a sedimentation tank 1, wherein the middle part of the sedimentation tank 1 is connected with a filter 2 through a water pipe, the lower end of the filter 2 is connected with a water inlet at the lower end of a micro vortex flocculation tank 3 through a water pipe and a water supply pump 11, the water outlet end of the micro vortex flocculation tank 3 is connected with the water inlet end at the lower end of an ultrafiltration sleeve 5 through the water pipe and the water supply pump 11, an ultrafiltration cavity is arranged in the middle part of the ultrafiltration sleeve 5, a plurality of ceramic membrane pipes 6 are arranged in the ultrafiltration cavity, a plurality of HCSONIC ultrasonic transducers 10 are arranged at the upper end and the lower end of the ultrafiltration sleeve 5, the ultrasonic transducers 10 are in one-to-one correspondence with the ceramic membrane pipes 6, a concentrated water outlet 9 is arranged above the ultrafiltration sleeve 5, the concentrated water outlet 9 is communicated with the ceramic membrane pipes 6, and an ultrafiltration water outlet 8 and a liquid outlet 7 are respectively arranged at the upper end and the lower end of the ultrafiltration cavity. After the production of the mulberry leaf tea is completed, the mulberry leaf tea is put into a sedimentation tank 1 for storage and sedimentation, the mulberry leaf tea is put into a filter 2 for preliminary filtration through a water pipe in the middle of the sedimentation tank 1, the filtered mixed liquor is put into a micro vortex flocculation tank 3 under the action of a water supply pump 11, some substances in the mixed liquor are precipitated under the action of micro vortex, the mixed liquor is further filtered and sedimentated, then the mixed liquor enters from the water outlet end at the upper part of the micro vortex flocculation tank 3 through the water inlet end at the lower part of an ultrafiltration sleeve 5 through the water supply pump 11, substances smaller than the drift diameter of the substances are led into an ultrafiltration cavity through the ceramic membrane pipe 6 by the pressure difference between the inner and outer parts of the membrane of the ceramic membrane pipe 6, at the moment, the concentrated filtered liquid can be discharged and stored through a concentrated water outlet 9, and the liquid in the ultrafiltration cavity can be discharged through an ultrafiltration water outlet 8. Meanwhile, when the ultrafiltration membrane tube works, the throughput of the ceramic membrane tube 6 can be kept by adjusting and controlling the ultrasonic transducers 10 at the upper end and the lower end, and the adjustment is carried out according to the actual production condition; the ultrasonic transducers 10 at the upper end and the lower end and corresponding power can be started when the flow rate is found to be smaller, the power at the upper end and the lower end is respectively 200W and 800W, the ceramic membrane tube 6 is sufficiently cleaned, long-time working and use are convenient, flushing is fast and convenient, and the use efficiency of the whole device is convenient to improve. And the three-stage filtration is carried out through the sedimentation tank 1, the micro vortex flocculation tank 3 and the ultrafiltration sleeve 5 in the device, so that the full filtration of the mulberry leaf tea is realized, residues and sedimentated substances are prevented from remaining in liquid, the concentration of the mulberry leaf tea is realized to a certain extent, and the use is very convenient.
The filter 2 is provided with a plurality of filter screens, the mesh number of which is 50-100 meshes; the multi-layer filter screen is used for carrying out preliminary filtration on the mulberry leaf tea from the sedimentation tank 1, so that the follow-up filtration process is convenient to carry out. A plurality of baffle plates 4 are arranged in the micro vortex flocculation tank 3 in a staggered way; the arrangement of the partition plate 4 can increase the passing path and the residence time of the mulberry leaf tea in the micro-vortex flocculation tank 3, and perform sufficient flocculation filtration on the mulberry leaf tea, so that the filtration effect is enhanced, and the filtration effect is better. A liquid storage tank 12 for back flushing is arranged above the micro vortex flocculation tank 3; after the micro-vortex flocculation tank 3 is used for a certain time, the micro-vortex flocculation tank 3 can be washed from top to bottom through the liquid in the liquid storage tank 12, so that substances deposited in the tank are prevented from affecting the filtering effect. The water inlet end, the ultrafiltration water outlet 8 and the concentration water outlet 9 of the ultrafiltration sleeve 5 are provided with a beauty control LDG-SUP flowmeter; the working condition of the ultrafiltration sleeve 5 is observed through the flowmeter, when abnormal changes occur, the ultrafiltration sleeve is timely processed, if the flow is reduced, the ultrasonic transducers 10 at the upper end and the lower end of the ultrafiltration sleeve 5 are timely started to clean the ultrafiltration sleeve, and the normal operation of the device is ensured.
Although specific embodiments of the utility model have been described in detail with reference to the accompanying drawings, it should not be construed as limiting the scope of protection of the present patent. Various modifications and variations which may be made by those skilled in the art without the creative effort are within the scope of the patent described in the claims.
Claims (6)
1. The utility model provides a mulberry leaf tea production is with ultrafiltration device, its characterized in that, includes the sedimentation tank, the sedimentation tank middle part is connected with the filter through the water pipe, the filter lower extreme is connected with little vortex flocculation tank lower extreme water inlet through water pipe and working shaft, little vortex flocculation tank water outlet is connected with ultrafiltration sleeve pipe lower extreme water inlet end through water pipe and working shaft, ultrafiltration sleeve pipe middle part is the ultrafiltration chamber, the ultrafiltration intracavity sets up a plurality of ceramic membrane pipes, ultrafiltration sleeve pipe upper and lower both ends all are provided with a plurality of ultrasonic transducer, just ultrasonic transducer with ceramic membrane pipe one-to-one, ultrafiltration sleeve pipe top is provided with concentrated delivery port, concentrated delivery port with ceramic membrane pipe communicates with each other, ultrafiltration chamber upper and lower both ends are provided with ultrafiltration delivery port and leakage fluid dram respectively.
2. An ultrafiltration device for producing mulberry leaf tea according to claim 1 wherein a plurality of filter screens are provided in said filter.
3. An ultrafiltration device for producing mulberry leaf tea according to claim 2, wherein the number of the filter mesh is 50 to 150 mesh.
4. An ultrafiltration device for producing mulberry leaf tea according to claim 1, wherein a plurality of baffles are arranged in the micro vortex flocculation tank in a staggered manner.
5. An ultrafiltration device for producing mulberry leaf tea according to claim 1, wherein a liquid storage tank for backwashing is arranged above the micro vortex flocculation tank.
6. An ultrafiltration device for producing mulberry leaf tea according to claim 1, wherein the water inlet end of the ultrafiltration sleeve, the ultrafiltration water outlet and the concentration water outlet are provided with flow meters.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
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CN202322394650.6U CN220788314U (en) | 2023-09-04 | 2023-09-04 | Ultra-filtration device is used in production of mulberry leaf tea |
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CN202322394650.6U CN220788314U (en) | 2023-09-04 | 2023-09-04 | Ultra-filtration device is used in production of mulberry leaf tea |
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Publication Number | Publication Date |
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CN220788314U true CN220788314U (en) | 2024-04-16 |
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CN202322394650.6U Active CN220788314U (en) | 2023-09-04 | 2023-09-04 | Ultra-filtration device is used in production of mulberry leaf tea |
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2023
- 2023-09-04 CN CN202322394650.6U patent/CN220788314U/en active Active
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