CN209286789U - A kind of stevia rebaudianum malt sugar liquid glucose membrane separation plant - Google Patents
A kind of stevia rebaudianum malt sugar liquid glucose membrane separation plant Download PDFInfo
- Publication number
- CN209286789U CN209286789U CN201822058079.XU CN201822058079U CN209286789U CN 209286789 U CN209286789 U CN 209286789U CN 201822058079 U CN201822058079 U CN 201822058079U CN 209286789 U CN209286789 U CN 209286789U
- Authority
- CN
- China
- Prior art keywords
- filtration barrel
- barrel body
- welded
- conveyance conduit
- separating material
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- GUBGYTABKSRVRQ-PICCSMPSSA-N D-Maltose Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@@H]1O[C@@H]1[C@@H](CO)OC(O)[C@H](O)[C@H]1O GUBGYTABKSRVRQ-PICCSMPSSA-N 0.000 title claims abstract description 34
- 238000000926 separation method Methods 0.000 title claims abstract description 31
- 241000196324 Embryophyta Species 0.000 title claims abstract description 18
- HELXLJCILKEWJH-NCGAPWICSA-N rebaudioside A Chemical compound O([C@H]1[C@H](O)[C@@H](CO)O[C@H]([C@@H]1O[C@H]1[C@@H]([C@@H](O)[C@H](O)[C@@H](CO)O1)O)O[C@]12C(=C)C[C@@]3(C1)CC[C@@H]1[C@@](C)(CCC[C@]1([C@@H]3CC2)C)C(=O)O[C@H]1[C@@H]([C@@H](O)[C@H](O)[C@@H](CO)O1)O)[C@@H]1O[C@H](CO)[C@@H](O)[C@H](O)[C@H]1O HELXLJCILKEWJH-NCGAPWICSA-N 0.000 title claims abstract description 18
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Chemical compound OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 title claims abstract description 17
- 239000012528 membrane Substances 0.000 title claims abstract description 17
- 244000228451 Stevia rebaudiana Species 0.000 title abstract description 4
- 238000001914 filtration Methods 0.000 claims abstract description 64
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims abstract description 27
- 239000000463 material Substances 0.000 claims description 43
- 241000544066 Stevia Species 0.000 claims description 16
- 238000003466 welding Methods 0.000 claims description 5
- 238000007600 charging Methods 0.000 claims description 3
- 238000005520 cutting process Methods 0.000 claims description 3
- UEDUENGHJMELGK-HYDKPPNVSA-N Stevioside Chemical compound O([C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@H]1O[C@]12C(=C)C[C@@]3(C1)CC[C@@H]1[C@@](C)(CCC[C@]1([C@@H]3CC2)C)C(=O)O[C@H]1[C@@H]([C@@H](O)[C@H](O)[C@@H](CO)O1)O)[C@@H]1O[C@H](CO)[C@@H](O)[C@H](O)[C@H]1O UEDUENGHJMELGK-HYDKPPNVSA-N 0.000 abstract description 20
- 229940013618 stevioside Drugs 0.000 abstract description 20
- OHHNJQXIOPOJSC-UHFFFAOYSA-N stevioside Natural products CC1(CCCC2(C)C3(C)CCC4(CC3(CCC12C)CC4=C)OC5OC(CO)C(O)C(O)C5OC6OC(CO)C(O)C(O)C6O)C(=O)OC7OC(CO)C(O)C(O)C7O OHHNJQXIOPOJSC-UHFFFAOYSA-N 0.000 abstract description 20
- 235000019202 steviosides Nutrition 0.000 abstract description 20
- 229930182470 glycoside Natural products 0.000 description 5
- 150000002338 glycosides Chemical class 0.000 description 5
- 238000000034 method Methods 0.000 description 4
- 150000001720 carbohydrates Chemical class 0.000 description 3
- 235000014633 carbohydrates Nutrition 0.000 description 3
- 238000010586 diagram Methods 0.000 description 3
- 238000004064 recycling Methods 0.000 description 3
- 239000006188 syrup Substances 0.000 description 3
- 235000020357 syrup Nutrition 0.000 description 3
- 235000006092 Stevia rebaudiana Nutrition 0.000 description 2
- 241000208838 Asteraceae Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000005352 clarification Methods 0.000 description 1
- 235000009508 confectionery Nutrition 0.000 description 1
- 239000000287 crude extract Substances 0.000 description 1
- 238000002425 crystallisation Methods 0.000 description 1
- 230000008025 crystallization Effects 0.000 description 1
- 238000005265 energy consumption Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 229930182478 glucoside Natural products 0.000 description 1
- 150000008131 glucosides Chemical class 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000004519 manufacturing process Methods 0.000 description 1
- 238000010025 steaming Methods 0.000 description 1
Landscapes
- Apparatus Associated With Microorganisms And Enzymes (AREA)
Abstract
The utility model discloses a kind of stevia rebaudianum malt sugar liquid glucose membrane separation plants, including main support base, one end medial surface of the main support base is vertically welded with fixed transverse rod, the top surface of the fixed transverse rod is welded with fixed vertical bar vertically upward, position level between the fixed vertical bar is welded with filtration barrel body, front side tight loop is socketed on the outside of one end of the filtration barrel body, the filtration barrel body is socketed with rear side tight loop in one end lateral surface far from front side tight loop, the filtration barrel body is plugged with feed pipe in one end middle position close to front side tight loop, the feed pipe is welded with S-shaped conveyance conduit in one end far from filtration barrel body vertically downward, the bottom end side of the S-shaped conveyance conduit has been bolted booster pump, the bottom surface of the S-shaped conveyance conduit and booster pump is to being connected to bottom end support rod.The utility model carries out physical separation will not carry out the water that separation causes structural damage, while isolating to stevioside to be recycled.
Description
Technical field
The utility model relates to stevioside separation technology field more particularly to a kind of stevia rebaudianum malt sugar liquid glucose membrane separation plants.
Background technique
Stevioside is also known as stevioside, it is extracted from the leaf of compositae plant (plant is referred to as STEVIA REBAUDIANA in China)
A kind of glucosides come.STEVIA REBAUDIANA originates in Paraguay and Brazil, and also there is plantation in the country such as present China, Singapore, Malaysia,
Its sweet ingredient is made of stevioside and stevia A glycoside, B glycosides, C glycosides, D glycosides and E glycosides.Stevioside can extracts from dry leaves with water,
Clarification and crystallization, obtain 3 seed types in actual production, are crude extract respectively and product that purity is 50% and 90%.
It is all to be evaporated moisture using steaming process and separated that traditional stevioside, which is separated, but high-temperature steam method
The foundation structure of stevioside can be damaged, so that stevioside is not pure enough can not to carry out using and energy consumption is high when processing
It is time-consuming and laborious.
Utility model content
The purpose of this utility model is to provide a kind of stevia rebaudianum malt sugar liquid glucose membrane separation plants, by the way that stevioside is defeated from master
The amount for sending pipeline conveying into from carrying out again from feed flow observation tube, is being pressurized again then into S-shaped conveyance conduit
Stevioside enter feed pipe under pressurization under the action of pump to enter finally into inside filtration barrel body, enters cartridge filter
Stevioside is made to carry out syrup separation under the action of filtering under the filtering of oblique filter layer after body, the carbohydrate after being separated is suitable
Tiltedly filter layer flow downwardly into separating material effuser, enter later separating material conveyance conduit from separating material observation tube carry out
The observation of amount is entered finally into and is collected again in separating material collecting pipe, after entering oblique filter layer and being filtered in addition
Water section enter conveying water pipe in, then under the action of collecting water pipe carry out water recycling, progress physical separation will not be right
Stevioside, which carries out the water that separation causes structural damage, while isolating, to be recycled.
It is according to the present utility model to be designed to provide a kind of stevia rebaudianum malt sugar liquid glucose membrane separation plant, including main support bottom
Seat, one end medial surface of the main support base are vertically welded with fixed transverse rod, and the top surface of the fixed transverse rod is welded vertically upward
It is connected to fixed vertical bar, the position level between the fixed vertical bar is welded with filtration barrel body, one end of the filtration barrel body
Outside is socketed with front side tight loop, and the filtration barrel body is socketed with rear side fastening in one end lateral surface far from front side tight loop
Circle, the filtration barrel body are plugged with feed pipe in one end middle position close to front side tight loop, and the feed pipe is remote
One end from filtration barrel body is welded with S-shaped conveyance conduit vertically downward, and the bottom end side of the S-shaped conveyance conduit has been bolted
The bottom surface of booster pump, the S-shaped conveyance conduit and booster pump is to being connected to bottom end support rod, and the both ends vertical welding of bottom end support rod
The medial surface in main support base is connect, the S-shaped conveyance conduit is connected with feed flow in the threaded one end far from booster pump and sees
Pipe is examined, the feed flow observation tube is connected with main delivery pipe, the cartridge filter in the threaded one end far from S-shaped conveyance conduit
Body is plugged with downwards separating material effuser in one end outer wall vertical close to rear side tight loop, and the separating material effuser is separate
One end of filtration barrel body is welded with separating material conveyance conduit, and the separating material conveyance conduit is in one end far from separating material effuser
It is threaded with separating material observation tube, the separating material observation tube is connected with point in the threaded one end far from separating material conveyance conduit
From material collecting pipe, the filtration barrel body is plugged with conveying water pipe in one end far from feed pipe, and the conveying water pipe is separate
One end of filtration barrel body is vertically welded with collection water pipe, and the medial surface oblique cutting of the filtration barrel body is connected to oblique filter layer, the mistake
The inner sidewall of filter cylinder body offers clamping groove.
Further, the number of the fixed vertical bar is two, and is respectively perpendicular the both ends position for being welded on fixed transverse rod
It sets
Further, the number of the filtration barrel body is several, and is in upper and lower superposing type water between multiple filtration barrel bodies
Flat welded is fixing position between vertical bar, is parallel to each other between multiple filtration barrel bodies
Further, the lateral surface uniform vertical level of the S-shaped conveyance conduit is welded with feed pipe, and more chargings
Pipeline is plugged on one end of filtration barrel body in one end far from S-shaped conveyance conduit
Further, the oblique filter layer is the inside for being plugged on clamping groove, and tiltedly filter layer is by feed pipe
The bottom end of the oblique filtration barrel body other end at the top of one end
Further, the separating material effuser is connected with filtration barrel body welding ends to inside
The utility model has the beneficial effect that compared with prior art
1, by the amount of conveying from carrying out stevioside from feed flow observation tube again from main delivery pipe entrance, then
It enters and stevioside enter feed pipe under pressurization under the action of booster pump again in S-shaped conveyance conduit to finally enter
To inside filtration barrel body, carry out stevioside under the action of filtering after entering filtration barrel body
Syrup separation, the carbohydrate after being separated flow downwardly into separating material effuser along oblique filter layer, enter separation later
Material conveying tube road is entered finally into and is collected again in separating material collecting pipe from the separating material observation tube amount of progress.
2, it is entered in conveying water pipe, then received by the other water section after entering oblique filter layer and being filtered
The recycling of water is carried out under the action of collector pipe, progress physical separation will not carry out separation to stevioside and cause structural damage, together
When the water isolated can be recycled.
Detailed description of the invention
Attached drawing is used to provide a further understanding of the present invention, and constitutes part of specification, practical with this
Novel embodiment is used to explain the utility model together, does not constitute limitations of the present invention.
In the accompanying drawings:
Fig. 1 be the utility model proposes a kind of stevia rebaudianum malt sugar liquid glucose membrane separation plant schematic perspective view；
Fig. 2 be the utility model proposes a kind of stevia rebaudianum malt sugar liquid glucose membrane separation plant overlooking structure diagram；
Fig. 3 be the utility model proposes the filtration barrel body of stevia rebaudianum malt sugar liquid glucose membrane separation plant a kind of face interior details
Structural schematic diagram；
Fig. 4 be the utility model proposes a kind of stevia rebaudianum malt sugar liquid glucose membrane separation plant filtration barrel body side view interior details
Structural schematic diagram.
In figure: the fixed vertical bar of the main support base of 1-, 2- fixed transverse rod, 3-, 4- filtration barrel body, the front side 5- tight loop, 6-
Rear side tight loop, 7- feed pipe, 8-S shape conveyance conduit, 9- booster pump, the bottom end 10- support rod, 11- feed flow observation tube,
12- main delivery pipe, 13- separating material effuser, 14- separating material conveyance conduit, 15- separating material observation tube, 16- separating material are collected
Pipe, 17- conveying water pipe, 18- collect water pipe, the oblique filter layer of 19-, 20- clamping groove.
Specific embodiment
The following will be combined with the drawings in the embodiments of the present invention, carries out the technical scheme in the embodiment of the utility model
Clearly and completely describe, it is clear that the described embodiments are only a part of the embodiments of the utility model, rather than whole
Embodiment.Based on the embodiments of the present invention, those of ordinary skill in the art are without making creative work
Every other embodiment obtained, fall within the protection scope of the utility model.
Referring to Fig.1-4, a kind of stevia rebaudianum malt sugar liquid glucose membrane separation plant, including main support base 1, the one of main support base 1
End medial surface is vertically welded with fixed transverse rod 2, and the top surface of fixed transverse rod 2 is welded with fixed vertical bar 3 vertically upward, fixed vertical
The number of bar 3 is two, and is respectively perpendicular the end positions for being welded on fixed transverse rod 2, and the position between fixed vertical bar 3 is horizontal
It is welded with filtration barrel body 4, the number of filtration barrel body 4 is several, and is in upper and lower superposing type horizontal welding between multiple filtration barrel bodies 4
The position between fixed vertical bar 3 is connect, is parallel to each other between multiple filtration barrel bodies 4, before being socketed on the outside of one end of filtration barrel body 4
Side tight loop 5, filtration barrel body 4 are socketed with rear side tight loop 6 in one end lateral surface far from front side tight loop 5, and filtration barrel body 4 exists
It is plugged with feed pipe 7 close to one end middle position of front side tight loop 5, feed pipe 7 hangs down in one end far from filtration barrel body 4
It is directly welded with S-shaped conveyance conduit 8 downwards, the lateral surface uniform vertical level of S-shaped conveyance conduit 8 is welded with feed pipe 7, and more
Root feed pipe 7 is plugged on one end of filtration barrel body 4, the bottom end side of S-shaped conveyance conduit 8 in one end far from S-shaped conveyance conduit 8
Face has been bolted booster pump 9, and the bottom surface of S-shaped conveyance conduit 8 and booster pump 9 is to being connected to bottom end support rod 10, and bottom end supports
The both ends of bar 10 are vertically welded in the medial surface of main support base 1, and S-shaped conveyance conduit 8 connects in the threaded one end far from booster pump 9
It is connected to feed flow observation tube 11, feed flow observation tube 11 is connected with main conveying in the threaded one end far from S-shaped conveyance conduit 8
Pipeline 12, filtration barrel body 4 are plugged with downwards separating material effuser 13 in one end outer wall vertical close to rear side tight loop 6, separate
Stream outlet pipe 13 is connected with 4 welding ends of filtration barrel body to inside, and separating material effuser 13 is in one end weldering far from filtration barrel body 4
It is connected to separating material conveyance conduit 14, separating material conveyance conduit 14 is connected with separation in the threaded one end far from separating material effuser 13
Expect that observation tube 15, separating material observation tube 15 are connected with separating material collecting pipe in the threaded one end far from separating material conveyance conduit 14
16, filtration barrel body 4 is plugged with conveying water pipe 17 in one end far from feed pipe 7, and conveying water pipe 17 is in separate filtration barrel body 4
One end, which is vertically welded with, collects water pipe 18, and the medial surface oblique cutting of filtration barrel body 4 is connected to oblique filter layer 19, and oblique filter layer 19 is grafting
In the inside of clamping groove 20, and tiltedly, filter layer 19 is the bottom of oblique 4 other end of filtration barrel body at the top of one end by feed pipe 7
End, the inner sidewall of filtration barrel body 4 offer clamping groove 20.
In use, passing through conveying from carrying out stevioside from feed flow observation tube 11 again from the entrance of main delivery pipe 12
Amount, then into making stevioside enter charging under pressurization under the action of booster pump 9 again in S-shaped conveyance conduit 8
Pipeline 7 enters finally into inside filtration barrel body 4, makes stevioside under the filtering of oblique filter layer 19 after entering filtration barrel body 4
Syrup separation is carried out under the action of filtering, the carbohydrate after being separated flows downwardly into separating material outflow along oblique filter layer 19
In pipe 13, separating material conveyance conduit 14 is entered later from 15 amount of progress of separating material observation tube, enters finally into separation
It is collected again in material collecting pipe 16, the other water section after entering oblique filter layer 4 and being filtered enters conveying water
In pipe 17, then under the action of collecting water pipe 18 carry out water recycling.
Place is not described in detail for the utility model, is the well-known technique of those skilled in the art.
While there has been shown and described that the embodiments of the present invention, for the ordinary skill in the art,
It is understood that these embodiments can be carried out with a variety of variations in the case where not departing from the principles of the present invention and spirit, repaired
Change, replacement and variant, the scope of the utility model is defined by the appended claims and the equivalents thereof.
Claims (6)
1. a kind of stevia rebaudianum malt sugar liquid glucose membrane separation plant, including main support base (1), it is characterised in that: the main support base
(1) one end medial surface is vertically welded with fixed transverse rod (2), and the top surface of the fixed transverse rod (2) is welded with fixation vertically upward
Vertical bar (3), the position level between the fixed vertical bar (3) are welded with filtration barrel body (4), the filtration barrel body (4)
Front side tight loop (5), the filtration barrel body (4) surface cover on the outside of one end far from front side tight loop (5) are socketed on the outside of one end
It is connected to rear side tight loop (6), the filtration barrel body (4) is plugged with charging in one end middle position close to front side tight loop (5)
Pipeline (7), the feed pipe (7) are welded with S-shaped conveyance conduit (8), institute in one end far from filtration barrel body (4) vertically downward
The bottom end side for stating S-shaped conveyance conduit (8) has been bolted booster pump (9), the S-shaped conveyance conduit (8) and booster pump (9)
Bottom surface is to being connected to bottom end support rod (10), and the both ends of bottom end support rod (10) are vertically welded in the inside of main support base (1)
Face, the S-shaped conveyance conduit (8) is connected with feed flow observation tube (11) in the threaded one end far from booster pump (9), described defeated
Flow view pipe (11) is sent to be connected with main delivery pipe (12), the cartridge filter in the threaded one end far from S-shaped conveyance conduit (8)
Body (4) is plugged with downwards separating material effuser (13) in one end outer wall vertical close to rear side tight loop (6), the separation stream
Outlet pipe (13) is welded with separating material conveyance conduit (14) in one end far from filtration barrel body (4), the separating material conveyance conduit
(14) it is connected with separating material observation tube (15) in the threaded one end far from separating material effuser (13), the separating material observation tube
(15) it is connected with separating material collecting pipe (16) in the threaded one end far from separating material conveyance conduit (14), the filtration barrel body (4)
It is plugged with conveying water pipe (17) in one end far from feed pipe (7), conveying water pipe (17) is in separate filtration barrel body (4)
One end, which is vertically welded with, collects water pipe (18), and the medial surface oblique cutting of the filtration barrel body (4) is connected to oblique filter layer (19), the mistake
The inner sidewall of filter cylinder body (4) offers clamping groove (20).
2. a kind of stevia rebaudianum malt sugar liquid glucose membrane separation plant according to claim 1, it is characterised in that: the fixed vertical bar
(3) number is two, and is respectively perpendicular the end positions for being welded on fixed transverse rod (2).
3. a kind of stevia rebaudianum malt sugar liquid glucose membrane separation plant according to claim 1, it is characterised in that: the filtration barrel body
(4) number be several, and between multiple filtration barrel bodies (4) in upper and lower superposing type level be welded on fixed vertical bar (3) it
Between position, be parallel to each other between multiple filtration barrel bodies (4).
4. a kind of stevia rebaudianum malt sugar liquid glucose membrane separation plant according to claim 1, it is characterised in that: the S-shaped delivery pipe
The lateral surface uniform vertical level in road (8) is welded with feed pipe (7), and more feed pipes (7) are far from S-shaped conveyance conduit
(8) one end is plugged on one end of filtration barrel body (4).
5. a kind of stevia rebaudianum malt sugar liquid glucose membrane separation plant according to claim 1, it is characterised in that: the oblique filter layer
It (19) is to be plugged on the inside of clamping groove (20), and tiltedly filter layer (19) is oblique mistake at the top of one end by feed pipe (7)
The bottom end of filter cylinder body (4) other end.
6. a kind of stevia rebaudianum malt sugar liquid glucose membrane separation plant according to claim 1, it is characterised in that: the separating material outflow
Pipe (13) is connected with filtration barrel body (4) welding ends to inside.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822058079.XU CN209286789U (en) | 2018-12-10 | 2018-12-10 | A kind of stevia rebaudianum malt sugar liquid glucose membrane separation plant |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201822058079.XU CN209286789U (en) | 2018-12-10 | 2018-12-10 | A kind of stevia rebaudianum malt sugar liquid glucose membrane separation plant |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN209286789U true CN209286789U (en) | 2019-08-23 |
Family
ID=67657628
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201822058079.XU Expired - Fee Related CN209286789U (en) | 2018-12-10 | 2018-12-10 | A kind of stevia rebaudianum malt sugar liquid glucose membrane separation plant |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN209286789U (en) |
-
2018
- 2018-12-10 CN CN201822058079.XU patent/CN209286789U/en not_active Expired - Fee Related
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN102040519A (en) | Method for preparing chlorogenic acid in Eucommia ulmoides leaves | |
| CN101633676A (en) | Method for preparing high-purity stachyose by using plant chromatographic separation technology | |
| CN209286789U (en) | A kind of stevia rebaudianum malt sugar liquid glucose membrane separation plant | |
| CN109400570B (en) | Anthocyanin extraction system | |
| WO2021104105A1 (en) | System and process for pretreating sugarcane juice before membrane filtration | |
| CN208857177U (en) | A kind of anhydrous solvent Tea Saponin extraction element | |
| CN212308463U (en) | System used in production process of eucommia ulmoides fine powder | |
| CN213570258U (en) | Production line preparation system for extracting polysaccharides and flavones from bamboo pulping liquid | |
| CN205885839U (en) | Separation and purification device of preparation barrenwort extract product | |
| CN207545889U (en) | One kind isolates and purifies system | |
| CN219701115U (en) | Plant beverage purification separator | |
| CN209144109U (en) | A kind of essential oil extract knockout drum | |
| CN207562389U (en) | A kind of inulin extracts enrichment facility | |
| CN208356281U (en) | Edible fungi polysaccharide ultrafiltration apparatus | |
| CN220918413U (en) | Reagent recovery device for bulk drug production | |
| CN218901429U (en) | Ultra-filter for crude extract of placenta protein | |
| CN204637640U (en) | A kind of device extracting mogroside V from Momordica grosvenori | |
| CN213431819U (en) | Preparation system for extracting polysaccharide flavone alkaloid from Moraceae plant liquid | |
| CN102172441B (en) | Impurity removal system for mesona chinensis liquid | |
| CN202015526U (en) | Immortal grass liquid impurity removing system | |
| CN209711375U (en) | A kind of fruit inspissated juice production experiment porch | |
| CN218166031U (en) | Sugar liquid waste residue utilization device | |
| CN214345630U (en) | A separation and filtration device for extracting ground ginseng polysaccharide | |
| CN212067873U (en) | Special filter for pectin filtration | |
| CN201541652U (en) | Egg yolk and egg white separator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20190823 |