CN220918729U - Seaweed oligosaccharide filtration equipment - Google Patents
Seaweed oligosaccharide filtration equipment Download PDFInfo
- Publication number
- CN220918729U CN220918729U CN202322482559.XU CN202322482559U CN220918729U CN 220918729 U CN220918729 U CN 220918729U CN 202322482559 U CN202322482559 U CN 202322482559U CN 220918729 U CN220918729 U CN 220918729U
- Authority
- CN
- China
- Prior art keywords
- fixedly connected
- shell
- ceramic membrane
- workbench
- wall
- 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.)
- Active
Links
- 238000001914 filtration Methods 0.000 title claims abstract description 36
- 241001474374 Blennius Species 0.000 title claims abstract description 24
- 229920001542 oligosaccharide Polymers 0.000 title claims abstract description 20
- 150000002482 oligosaccharides Chemical class 0.000 title claims abstract description 20
- 239000012528 membrane Substances 0.000 claims abstract description 63
- 239000000919 ceramic Substances 0.000 claims abstract description 56
- 230000002457 bidirectional effect Effects 0.000 claims description 17
- 230000006978 adaptation Effects 0.000 claims description 4
- 230000002093 peripheral effect Effects 0.000 claims description 3
- 239000007788 liquid Substances 0.000 abstract description 50
- 230000015556 catabolic process Effects 0.000 abstract description 28
- 238000006731 degradation reaction Methods 0.000 abstract description 28
- 241000195493 Cryptophyta Species 0.000 abstract description 11
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 11
- 238000000926 separation method Methods 0.000 abstract description 9
- 239000012535 impurity Substances 0.000 abstract description 7
- 230000009471 action Effects 0.000 description 5
- 238000000034 method Methods 0.000 description 5
- 230000008569 process Effects 0.000 description 5
- 230000005540 biological transmission Effects 0.000 description 3
- 230000005484 gravity Effects 0.000 description 3
- 238000000605 extraction Methods 0.000 description 2
- HDTRYLNUVZCQOY-UHFFFAOYSA-N α-D-glucopyranosyl-α-D-glucopyranoside Natural products OC1C(O)C(O)C(CO)OC1OC1C(O)C(O)C(O)C(CO)O1 HDTRYLNUVZCQOY-UHFFFAOYSA-N 0.000 description 1
- HDTRYLNUVZCQOY-WSWWMNSNSA-N Trehalose Natural products O[C@@H]1[C@@H](O)[C@@H](O)[C@@H](CO)O[C@@H]1O[C@@H]1[C@H](O)[C@@H](O)[C@@H](O)[C@@H](CO)O1 HDTRYLNUVZCQOY-WSWWMNSNSA-N 0.000 description 1
- HDTRYLNUVZCQOY-LIZSDCNHSA-N alpha,alpha-trehalose Chemical compound O[C@@H]1[C@@H](O)[C@H](O)[C@@H](CO)O[C@@H]1O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 HDTRYLNUVZCQOY-LIZSDCNHSA-N 0.000 description 1
- 230000003712 anti-aging effect Effects 0.000 description 1
- 230000000844 anti-bacterial effect Effects 0.000 description 1
- 230000003064 anti-oxidating effect Effects 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000020411 cell activation Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 230000007515 enzymatic degradation Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 230000014759 maintenance of location Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000005086 pumping Methods 0.000 description 1
- 238000004659 sterilization and disinfection Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000000967 suction filtration Methods 0.000 description 1
- 230000037072 sun protection Effects 0.000 description 1
- 238000005406 washing Methods 0.000 description 1
Classifications
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
- Y02A—TECHNOLOGIES FOR ADAPTATION TO CLIMATE CHANGE
- Y02A40/00—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production
- Y02A40/80—Adaptation technologies in agriculture, forestry, livestock or agroalimentary production in fisheries management
Landscapes
- Separation Using Semi-Permeable Membranes (AREA)
Abstract
The utility model belongs to the technical field of filtering equipment, in particular to seaweed oligosaccharide filtering equipment, which comprises a workbench, wherein a negative pressure hole is formed in the center of the top of the workbench, a shell is arranged at the top of the workbench, a ceramic membrane is slidably arranged in the shell, a clamping component is arranged at the top of the workbench and used for clamping and fixing the shell, and a diaphragm liquid pump is started and pouring degradation liquid of marine algae into the shell, so that the diaphragm liquid pump can pump air to the shell through the negative pressure hole, the degradation liquid of the marine algae entering the shell can pass through the ceramic membrane more quickly, impurities are trapped on the membrane, the filtering speed of the degradation liquid is improved, the working efficiency is improved, and the filtered separation liquid can be discharged through a water outlet pipe in a concentrated manner, thereby facilitating subsequent concentrated use.
Description
Technical Field
The utility model belongs to the technical field of filtering equipment, and particularly relates to a seaweed oligosaccharide filtering device.
Background
The trehalose is an oligosaccharide obtained from marine algae by chemical and biological enzymatic degradation, and has a great demand in the development and application of products such as water retention, moisture retention, hair washing, hair care, sterilization and disinfection, antibacterial, cell activation, antioxidation, anti-aging, sun protection and the like.
The seaweed oligosaccharides are usually filtered and separated by using a tubular ceramic membrane after enzymolysis processing is finished, the common tubular ceramic membrane consists of a tube body and the ceramic membrane inside the tube body, and after the seaweed degradation liquid in processing is added into the tank body, the degradation liquid can pass through the ceramic membrane and stop impurities on the membrane, so that a separation liquid is left for subsequent use.
At present, in the prior art, when marine algae degradation liquid is filtered, the marine algae degradation liquid is directly poured into a tubular ceramic membrane, and the degradation liquid moves downwards under the action of gravity and passes through the ceramic membrane to complete filtration and separation, and because no external force is interfered, the filtration speed is lower, so that the working efficiency is reduced.
Therefore, a seaweed oligosaccharide filtration device is proposed against the above-mentioned problems.
Disclosure of utility model
In order to overcome the defects in the prior art and solve the problems, the seaweed oligosaccharide filtering equipment is provided.
The technical scheme adopted for solving the technical problems is as follows: the utility model discloses a seaweed oligosaccharide filtering device, which comprises a workbench, wherein a negative pressure hole is formed in the center of the top of the workbench, a shell is arranged at the top of the workbench, a ceramic membrane is slidably installed in the shell, a through hole is formed in the inner wall of the bottom of the shell, a connecting pipe is fixedly connected to the lower surface of the shell, the connecting pipe is positioned at the bottom of the through hole, the connecting pipe is matched with the negative pressure hole in size, a clamping assembly is arranged at the top of the workbench and used for clamping and fixing the shell, a diaphragm liquid pump is fixedly connected to the center of the bottom of the workbench, an extraction opening of the diaphragm liquid pump is positioned in the negative pressure hole, a water outlet pipe is fixedly connected to the bottom of the diaphragm liquid pump, and the inner wall of the bottom of the shell is of a peripheral high-middle low structure.
Preferably, the clamping assembly comprises a mounting groove formed in the top of the workbench, a bidirectional screw rod is rotationally connected to the mounting groove, connecting blocks are connected to two ends of the bidirectional screw rod in a threaded mode, connecting rods are fixedly connected to the tops of the connecting blocks, arc clamping plates are fixedly connected to the outer wall of one side, close to the shell, of the connecting rods, a driving motor is fixedly connected to the outer wall of the workbench, and an output shaft of the driving motor is fixedly connected with one end of the bidirectional screw rod.
Preferably, the spout has all been seted up to mounting groove both sides inner wall, the connecting block is close to the equal fixedly connected with slider of both sides outer wall of spout, slider slidable mounting is in the spout, and slider and spout size looks adaptation.
Preferably, a plurality of groups of movable grooves are formed in the top of the shell, sliding rods are slidably mounted in each movable groove, a pressing plate is fixedly connected to the outer wall of the bottom of one side, close to the ceramic membrane, of each sliding rod, springs are fixedly connected to the bottoms of the movable grooves, the tops of the springs are fixedly connected with the bottoms of the sliding rods, and a limiting assembly is arranged on the top of the shell and used for limiting the sliding rods.
Preferably, the limiting component comprises a limiting groove arranged at the top of the shell, a limiting block is slidably arranged in the limiting groove, the width of the limiting groove is matched with the width of the sliding part of the limiting block, and the limiting groove is arranged on one side of the moving groove.
Preferably, the bottom of the workbench is fixedly connected with a plurality of groups of support columns.
The utility model has the beneficial effects that:
The utility model provides a seaweed oligosaccharide filtering device, which is characterized in that a diaphragm liquid pump is started and a degradation liquid of marine algae is poured into a shell, and the diaphragm liquid pump pumps air to the shell through a negative pressure hole, so that the degradation liquid of the marine algae entering the shell can pass through a ceramic membrane more quickly and retain impurities on the membrane, the filtering speed of the degradation liquid is improved, the working efficiency is improved, and the filtered separation liquid can be discharged in a concentrated manner through a water outlet pipe, thereby being convenient for subsequent concentrated use.
The utility model provides seaweed oligosaccharide filtering equipment, wherein an output shaft of a driving motor drives a bidirectional screw rod to rotate, the rotating bidirectional screw rod drives two groups of connecting blocks to move through screw thread transmission, and as the screw thread directions of two ends of the bidirectional screw rod are opposite, the two groups of connecting blocks and a connecting rod at the top of the two groups of connecting blocks can simultaneously move towards a shell, and two groups of arc clamping plates are abutted with the outer wall of the shell and clamp and fix the two groups of arc clamping plates, so that the shell is prevented from being deviated due to overlarge water flow in the filtering process, and the normal operation of filtering operation is ensured.
Drawings
The accompanying drawings, which are included to provide a further understanding of the utility model and are incorporated in and constitute a part of this specification, illustrate embodiments of the utility model and together with the description serve to explain the utility model and do not constitute a limitation on the utility model. In the drawings:
FIG. 1 is a perspective view of the present utility model;
FIG. 2 is a perspective view of a cross section of the present utility model;
FIG. 3 is a cross-sectional perspective view of the housing of the present utility model;
FIG. 4 is an enlarged view at A in FIG. 3;
FIG. 5 is an enlarged view at B in FIG. 3;
Legend description:
1. a work table; 2. a mounting groove; 3. a two-way screw rod; 4. a chute; 5. a connecting block; 6. a slide block; 7. a connecting rod; 8. an arc clamping plate; 9. a driving motor; 10. a housing; 11. a ceramic membrane; 12. a moving groove; 13. a spring; 14. a pressing plate; 15. a slide bar; 16. a limit groove; 17. a limiting block; 18. a diaphragm liquid pump; 19. a water outlet pipe; 20. a negative pressure hole; 21. a connecting pipe; 22. and a through hole.
Detailed Description
The following description of the embodiments of the present utility model will be made clearly and completely with reference to the accompanying drawings, in which it is apparent that the embodiments described are only some embodiments of the present utility model, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the utility model without making any inventive effort, are intended to be within the scope of the utility model.
Specific examples are given below.
Referring to fig. 1-5, the utility model provides a seaweed oligosaccharide filter device, which comprises a workbench 1, wherein a negative pressure hole 20 is formed in the center of the top of the workbench 1, a shell 10 is arranged at the top of the workbench 1, a ceramic membrane 11 is slidably mounted in the shell 10, a through hole 22 is formed in the inner wall of the bottom of the shell 10, a connecting pipe 21 is fixedly connected to the lower surface of the shell 10, the connecting pipe 21 is positioned at the bottom of the through hole 22, the connecting pipe 21 is matched with the negative pressure hole 20 in size, a clamping assembly is arranged at the top of the workbench 1 and used for clamping and fixing the shell 10, a diaphragm liquid pump 18 is fixedly connected to the center of the bottom of the workbench 1, an extraction opening of the diaphragm liquid pump 18 is positioned in the negative pressure hole 20, a water outlet pipe 19 is fixedly connected to the bottom of the diaphragm liquid pump 18, and the inner wall of the bottom of the shell 10 is of a peripheral high-middle low structure.
The seaweed oligosaccharides are usually filtered and separated by using a tubular ceramic membrane after enzymolysis processing is finished, the common tubular ceramic membrane consists of a tube body and a ceramic membrane in the tube body, after the seaweed degradation liquid in processing is added into a tank body, the degradation liquid passes through the ceramic membrane and retains impurities on the membrane, so that the separation liquid is left for subsequent use, the seaweed degradation liquid is usually directly poured into the tubular ceramic membrane when being filtered in the prior art, the degradation liquid moves downwards under the action of gravity and passes through the ceramic membrane to complete filtration and separation, and the filtering speed is low due to no external force interference, so that the working efficiency is reduced. Then the connecting pipe 21 is inserted into the negative pressure hole 20, the shell 10 is fixed through the clamping assembly, the diaphragm liquid pump 18 is started after the fixing of the shell 10 is completed, and the degradation liquid of marine algae is poured into the shell 10, at the moment, the diaphragm liquid pump 18 can pump the shell 10 through the negative pressure hole 20, so that the degradation liquid of the marine algae entering the shell 10 can pass through the ceramic membrane 11 more quickly, impurities are trapped on the membrane, the filtering speed of the degradation liquid is improved, the working efficiency is further improved, the filtered separation liquid can be intensively discharged through the water outlet pipe 19, the subsequent centralized use is convenient, and the degradation liquid which is filtered in the shell 10 can be quickly moved into the through hole 22 and enters the water outlet pipe 19 through the connecting pipe 21 to be discharged; because the connecting pipe 21 and the size looks adaptation of negative pressure hole 20, so the outer wall of connecting pipe 21 can closely laminate with the inner wall of negative pressure hole 20, and the pumping in the negative pressure hole 20 can be through connecting pipe 21 is on the degradation liquid of the inside of casing 10 completely this moment to improve the filtration rate, and connecting pipe 21 can play the locate function, can guarantee the through-hole 22 of casing 10 bottom and the complete coincidence of negative pressure hole 20 when the installation, thereby guarantee that degradation liquid has good suction filtration effect.
Further, as shown in fig. 1 and fig. 2, the clamping assembly comprises a mounting groove 2 formed in the top of the workbench 1, a bidirectional screw rod 3 is rotationally connected to the mounting groove 2, connecting blocks 5 are connected to the two ends of the bidirectional screw rod 3 in a threaded manner, connecting rods 7 are fixedly connected to the tops of the connecting blocks 5, arc clamping plates 8 are fixedly connected to the outer wall of one side, close to the shell 10, of the connecting rods 7, driving motors 9 are fixedly connected to the outer wall of the workbench 1, an output shaft of each driving motor 9 is fixedly connected with one end of the bidirectional screw rod 3, when the shell 10 is placed at the top of the workbench 1, the driving motor 9 is started, an output shaft of each driving motor 9 drives the bidirectional screw rod 3 to rotate, the two groups of connecting blocks 5 are driven to move through threaded transmission, and due to the fact that the threaded directions of the two ends of the bidirectional screw rod 3 are opposite, the connecting rods 7 at the tops of the two groups of the connecting blocks 5 move towards the shell 10 simultaneously, the two groups of arc clamping plates 8 are abutted against the outer wall of the shell 10 and clamp the shell 10 fixedly, and deflection of the shell 10 is prevented in the filtering process due to water flow too much, and normal filtering operation is guaranteed.
Further, as shown in fig. 2, the sliding grooves 4 are all formed in the inner walls of the two sides of the mounting groove 2, the sliding blocks 6 are fixedly connected to the outer walls of the two sides, close to the sliding grooves 4, of the connecting block 5, the sliding blocks 6 are slidably mounted in the sliding grooves 4, the sliding blocks 6 are matched with the sliding grooves 4 in size, when the connecting block 5 moves, the sliding blocks 6 are driven to move in the sliding grooves 4, the sliding blocks 6 play a limiting role on the connecting block 5, rotation or deviation of the connecting block 5 during movement is prevented, and therefore stability of the connecting block 5 and the arc clamping plates 8 during movement is improved.
Further, as shown in fig. 3 and fig. 4, a plurality of groups of moving grooves 12 are provided at the top of the casing 10, each group of moving grooves 12 is provided with a sliding rod 15 in a sliding manner, each sliding rod 15 is fixedly connected with a pressing plate 14 near the outer wall of the bottom of one side of the ceramic membrane 11, each group of moving grooves 12 is fixedly connected with a spring 13 at the bottom, the top of the spring 13 is fixedly connected with the bottom of the sliding rod 15, the top of the casing 10 is provided with a limiting component, the limiting component is used for limiting the sliding rods 15, when the ceramic membrane 11 is installed, firstly, the bottom of the ceramic membrane 11 is aligned with one side of the pressing plate 14 in the casing 10, the bottom of the ceramic membrane 11 is moved to one side of the pressing plate 14 until the ceramic membrane 11 contacts with the upper surface of the pressing plate 14, then a worker presses down two groups of sliding rods 15, at the same time, the pressing plate 14 simultaneously moves downwards and compresses the spring 13 with the ceramic membrane 11 at the top of the pressing plate, thereby driving the ceramic membrane 11 to enter the casing 10, and then limiting the sliding rods 15 through the limiting component.
Further, as shown in fig. 4 and fig. 5, the limiting component comprises a limiting groove 16 arranged at the top of the casing 10, a limiting block 17 is slidably mounted in the limiting groove 16, the width of the limiting groove 16 is matched with the width of the sliding part of the limiting block 17, the limiting groove 16 is arranged at one side of the moving groove 12, when the ceramic membrane 11 enters the casing 10, the limiting block 17 slides to the side close to the moving groove 12, at the moment, the limiting block 17 limits the top of the sliding rod 15 and prevents the sliding rod from moving upwards under the acting force of the spring 13, so that the ceramic membrane 11 is ensured to be positioned in the casing 10 in the working process, normal development of filtering work is facilitated, when the ceramic membrane 11 needs to be replaced, only the limiting block 17 needs to slide to be separated from the side of the moving groove 12 again, at the moment, the sliding rod 15 moves upwards under the action of elastic restoring force of the spring 13 and drives the pressing plate 14 to move upwards with the ceramic membrane 11 at the top of the ceramic membrane 11, so that the top of the ceramic membrane 11 is positioned outside the casing 10, and a worker can conveniently take the ceramic membrane 11 and replace the ceramic membrane 11.
Further, as shown in fig. 1 and 5, a plurality of groups of support columns are fixedly connected to the bottom of the workbench 1, and the support columns play a supporting role on the workbench 1 during working, so that the stability of the workbench 1 during working is ensured.
Working principle: the seaweed oligosaccharide is usually filtered and separated by using a tubular ceramic membrane after enzymolysis processing is finished, the common tubular ceramic membrane consists of a tube body and the ceramic membrane in the tube body, after the seaweed degradation liquid in processing is added into a tank body, the degradation liquid passes through the ceramic membrane and retains impurities on the membrane, so that separation liquid is left for subsequent use, the seaweed degradation liquid is usually directly poured into the tubular ceramic membrane when being filtered in the prior art, the degradation liquid moves downwards under the action of gravity and passes through the ceramic membrane to complete filtration and separation, and the filtering speed is low due to no external force interference, so that the working efficiency is reduced. The rotating bidirectional screw rod 3 drives the two groups of connecting blocks 5 to move through screw transmission, and as the screw directions of the two ends of the bidirectional screw rod 3 are opposite, the two groups of connecting blocks 5 and the connecting rod 7 at the top of the bidirectional screw rod can simultaneously move towards the shell 10, and the two groups of arc clamping plates 8 are abutted against the outer wall of the shell 10 and clamp and fix the two groups of arc clamping plates, so that the shell 10 is prevented from deviating due to overlarge water in the filtering process, the normal operation of filtering operation is ensured, the shell 10 starts the diaphragm liquid pump 18 after the fixing is completed and the degradation liquid of marine algae is poured into the shell 10, at the moment, the diaphragm liquid pump 18 can pump air out of the shell 10 through the negative pressure hole 20, so that the degradation liquid of the marine algae entering the shell 10 can more quickly pass through the ceramic membrane 11 and intercept impurities on the membrane, thereby improving the filtering speed of the degradation liquid and further improving the working efficiency, and the filtered separating liquid can be discharged in a concentrated way through the water outlet pipe 19, so that the subsequent concentrated use is convenient.
When the ceramic membrane 11 is installed, firstly, the limiting block 17 slides to one side far away from the movable groove 12, the bottom of the ceramic membrane 11 is aligned to one side of the pressing plate 14 in the shell 10, the bottom of the ceramic membrane 11 moves to one side of the pressing plate 14 until the ceramic membrane 11 contacts with the upper surface of the pressing plate 14, then, a worker presses down two groups of sliding rods 15, at the moment, the pressing plate 14 drives the ceramic membrane 11 at the top of the pressing plate to move downwards together and compress the spring 13, so that the ceramic membrane 11 is driven to enter the shell 10, the sliding limiting block 17 moves to one side close to the movable groove 12, at the moment, the limiting block 17 limits the top of the sliding rods 15 and prevents the sliding rods from moving upwards under the acting force of the spring 13, so that the ceramic membrane 11 can be positioned in the shell 10 in the working process, normal development of filtering work is facilitated, and when the ceramic membrane 11 needs to be replaced, only the limiting block 17 is required to slide to one side far away from the movable groove 12 again, at the moment, the sliding rods 15 move upwards under the action of the elastic restoring force of the spring 13, and drive the pressing plate 14 and the ceramic membrane 11 at the top of the pressing plate to move upwards to be positioned outside the shell 10, so that the ceramic membrane 11 is convenient for the worker to take the ceramic membrane 11 and replace.
The foregoing has shown and described the basic principles, principal features and advantages of the utility model. It will be understood by those skilled in the art that the present utility model is not limited to the embodiments described above, and that the above embodiments and descriptions are merely illustrative of the principles of the present utility model, and various changes and modifications may be made without departing from the spirit and scope of the utility model, which is defined in the appended claims.
Claims (6)
1. A seaweed oligosaccharide filtration device, characterized in that: including workstation (1), negative pressure hole (20) have been seted up in workstation (1) top center department, workstation (1) top is provided with casing (10), install ceramic membrane (11) in casing (10) sliding, through-hole (22) have been seted up to casing (10) bottom inner wall, fixedly connected with connecting pipe (21) under casing (10), connecting pipe (21) are located through-hole (22) bottom, connecting pipe (21) and negative pressure hole (20) size looks adaptation, workstation (1) top is provided with the clamping assembly, the clamping assembly is used for carrying out the centre gripping to casing (10) fixedly connected with diaphragm pump (18) in workstation (1) bottom center department, the diaphragm pump (18) bottom fixedly connected with outlet pipe (19) are located negative pressure hole (20), the bottom inner wall of casing (10) is peripheral high, middle low structure.
2. The seaweed oligosaccharide filtration device of claim 1, wherein: the clamping assembly comprises a mounting groove (2) formed in the top of the workbench (1), a bidirectional screw rod (3) is rotationally connected to the mounting groove (2), connecting blocks (5) are connected to the two ends of the bidirectional screw rod (3) in a threaded mode, connecting rods (7) are fixedly connected to the tops of the connecting blocks (5), arc clamping plates (8) are fixedly connected to the outer wall of one side, close to the shell (10), of the connecting rods (7), a driving motor (9) is fixedly connected to the outer wall of the workbench (1), and an output shaft of the driving motor (9) is fixedly connected with one end of the bidirectional screw rod (3).
3. The seaweed oligosaccharide filtration device of claim 2, wherein: spout (4) have all been seted up to mounting groove (2) both sides inner wall, connecting block (5) are close to both sides outer wall of spout (4) and all fixedly connected with slider (6), slider (6) slidable mounting is in spout (4), and slider (6) and spout (4) size looks adaptation.
4. A seaweed oligosaccharide filtration device as claimed in claim 3, wherein: the ceramic membrane is characterized in that a plurality of groups of moving grooves (12) are formed in the top of the shell (10), sliding rods (15) are slidably mounted in each group of moving grooves (12), a pressing plate (14) is fixedly connected to the outer wall of one side of each sliding rod (15) close to the ceramic membrane (11), springs (13) are fixedly connected to the bottoms of the moving grooves (12), the tops of the springs (13) are fixedly connected with the bottoms of the sliding rods (15), and limiting components are arranged at the tops of the shell (10) and used for limiting the sliding rods (15).
5. A seaweed oligosaccharide filtration device as claimed in claim 4, wherein: the limiting assembly comprises a limiting groove (16) arranged at the top of the shell (10), a limiting block (17) is slidably arranged in the limiting groove (16), the width of the limiting groove (16) is matched with the width of the sliding part of the limiting block (17), and the limiting groove (16) is arranged on one side of the moving groove (12).
6. The seaweed oligosaccharide filtration device of claim 1, wherein: and a plurality of groups of support columns are fixedly connected to the bottom of the workbench (1).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322482559.XU CN220918729U (en) | 2023-09-12 | 2023-09-12 | Seaweed oligosaccharide filtration equipment |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN202322482559.XU CN220918729U (en) | 2023-09-12 | 2023-09-12 | Seaweed oligosaccharide filtration equipment |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| CN220918729U true CN220918729U (en) | 2024-05-10 |
Family
ID=90965709
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN202322482559.XU Active CN220918729U (en) | 2023-09-12 | 2023-09-12 | Seaweed oligosaccharide filtration equipment |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN220918729U (en) |
-
2023
- 2023-09-12 CN CN202322482559.XU patent/CN220918729U/en active Active
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN207042059U (en) | A kind of water treatment facilities | |
| CN210543584U (en) | Primary filtering structure of horizontal water treatment equipment | |
| CN220918729U (en) | Seaweed oligosaccharide filtration equipment | |
| CN114669119A (en) | Ceramic membrane filtering and separating device | |
| CN203750236U (en) | Back washing filter implementing through compressing variable fibers | |
| CN113149256A (en) | High-efficient sewage treatment device of environmental protection that can be clean | |
| CN116371203A (en) | Self-circulation sewage treatment system | |
| CN215756778U (en) | Oil field fracturing fluid processing apparatus | |
| CN215195782U (en) | Anti-blocking electromagnetic proportional control valve | |
| CN115501686A (en) | Electronic silica sol purification equipment | |
| CN213652032U (en) | Secondary reverse osmosis water treatment machine | |
| CN208054968U (en) | A kind of graphene adsorption treatment dyeing waste water device | |
| CN209865413U (en) | Titanium dioxide production is with circulation pressure filter | |
| CN218687008U (en) | Filter equipment is used in silica gel production | |
| CN211717073U (en) | Filter cake dryer | |
| CN219744125U (en) | Sewage treatment mud discharging device | |
| CN212016943U (en) | Silicon carbide film filter | |
| CN214159178U (en) | Industrial wastewater membrane filtration treatment system | |
| CN217627889U (en) | Ozone catalytic oxidation and carbon fiber combined filler filter integrated equipment | |
| CN220989989U (en) | Domestic sewage treatment device | |
| CN215233329U (en) | A doublestage reverse osmosis water processor for gauze mask production | |
| CN214577572U (en) | Piston pump casting with multiple channels switched | |
| CN220091018U (en) | Reverse osmosis equipment | |
| CN216041585U (en) | Sewage lifting equipment with ball check valve | |
| CN217163885U (en) | Ultrafiltration membrane water purifier with high water yield |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| GR01 | Patent grant | ||
| GR01 | Patent grant |