CN117398760A - Impurity separating device - Google Patents
Impurity separating device Download PDFInfo
- Publication number
- CN117398760A CN117398760A CN202311727212.5A CN202311727212A CN117398760A CN 117398760 A CN117398760 A CN 117398760A CN 202311727212 A CN202311727212 A CN 202311727212A CN 117398760 A CN117398760 A CN 117398760A
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- China
- Prior art keywords
- fixedly connected
- hmb
- sleeve
- side wall
- impurity
- Prior art date
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- 239000012535 impurity Substances 0.000 title claims abstract description 65
- 230000007246 mechanism Effects 0.000 claims abstract description 76
- 238000010438 heat treatment Methods 0.000 claims abstract description 46
- 238000000926 separation method Methods 0.000 claims abstract description 18
- 238000001035 drying Methods 0.000 claims abstract description 16
- 238000002156 mixing Methods 0.000 claims abstract description 14
- 238000003756 stirring Methods 0.000 claims description 15
- 238000007790 scraping Methods 0.000 claims description 6
- 239000011575 calcium Substances 0.000 abstract description 92
- 239000000843 powder Substances 0.000 abstract description 34
- 239000013078 crystal Substances 0.000 abstract description 18
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 16
- AXCZMVOFGPJBDE-UHFFFAOYSA-L calcium dihydroxide Chemical compound [OH-].[OH-].[Ca+2] AXCZMVOFGPJBDE-UHFFFAOYSA-L 0.000 abstract description 13
- 229910001861 calcium hydroxide Inorganic materials 0.000 abstract description 13
- 239000000920 calcium hydroxide Substances 0.000 abstract description 13
- 229910021645 metal ion Inorganic materials 0.000 abstract description 12
- 239000002244 precipitate Substances 0.000 abstract description 9
- 239000002994 raw material Substances 0.000 abstract description 9
- 239000007788 liquid Substances 0.000 description 44
- 239000002245 particle Substances 0.000 description 16
- 238000000034 method Methods 0.000 description 15
- 230000008569 process Effects 0.000 description 14
- 238000001704 evaporation Methods 0.000 description 6
- 230000008020 evaporation Effects 0.000 description 6
- 239000000047 product Substances 0.000 description 6
- AXFYFNCPONWUHW-UHFFFAOYSA-N 3-hydroxyisovaleric acid Chemical compound CC(C)(O)CC(O)=O AXFYFNCPONWUHW-UHFFFAOYSA-N 0.000 description 5
- 238000010586 diagram Methods 0.000 description 5
- 239000002778 food additive Substances 0.000 description 4
- 238000004140 cleaning Methods 0.000 description 3
- 230000007547 defect Effects 0.000 description 3
- 238000001914 filtration Methods 0.000 description 3
- 235000013373 food additive Nutrition 0.000 description 3
- 150000002500 ions Chemical class 0.000 description 3
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 2
- 230000009471 action Effects 0.000 description 2
- 238000006243 chemical reaction Methods 0.000 description 2
- 230000005484 gravity Effects 0.000 description 2
- 239000000126 substance Substances 0.000 description 2
- 241000251468 Actinopterygii Species 0.000 description 1
- 235000011299 Brassica oleracea var botrytis Nutrition 0.000 description 1
- 240000003259 Brassica oleracea var. botrytis Species 0.000 description 1
- 241000219823 Medicago Species 0.000 description 1
- 235000017587 Medicago sativa ssp. sativa Nutrition 0.000 description 1
- WNROFYMDJYEPJX-UHFFFAOYSA-K aluminium hydroxide Chemical compound [OH-].[OH-].[OH-].[Al+3] WNROFYMDJYEPJX-UHFFFAOYSA-K 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- -1 calcium salt-beta-hydroxy-beta-methylbutyric acid calcium Chemical compound 0.000 description 1
- 159000000007 calcium salts Chemical class 0.000 description 1
- YZHOZVWZUXBPMD-UHFFFAOYSA-N calcium;3-hydroxy-3-methylbutanoic acid Chemical compound [Ca].CC(C)(O)CC(O)=O YZHOZVWZUXBPMD-UHFFFAOYSA-N 0.000 description 1
- 238000009388 chemical precipitation Methods 0.000 description 1
- 235000020971 citrus fruits Nutrition 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000007599 discharging Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 229910052742 iron Inorganic materials 0.000 description 1
- 235000021374 legumes Nutrition 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 239000004576 sand Substances 0.000 description 1
- 235000014102 seafood Nutrition 0.000 description 1
- 239000013049 sediment Substances 0.000 description 1
- 238000001308 synthesis method Methods 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/22—Evaporating by bringing a thin layer of the liquid into contact with a heated surface
- B01D1/24—Evaporating by bringing a thin layer of the liquid into contact with a heated surface to obtain dry solids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
- B01D1/30—Accessories for evaporators ; Constructional details thereof
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/04—Combinations of filters with settling tanks
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/0018—Evaporation of components of the mixture to be separated
- B01D9/0031—Evaporation of components of the mixture to be separated by heating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D9/00—Crystallisation
- B01D9/02—Crystallisation from solutions
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Crystallography & Structural Chemistry (AREA)
- Physics & Mathematics (AREA)
- Thermal Sciences (AREA)
- Extraction Or Liquid Replacement (AREA)
Abstract
The invention relates to the technical field of impurity separation, in particular to an impurity separation device, which comprises a mixing mechanism, a valve mechanism, a separation mechanism, a drying mechanism and a collecting mechanism, wherein the lower end of the mixing mechanism is provided with the valve mechanism, the lower end of the valve mechanism is provided with the separation mechanism, one end of the separation mechanism is provided with the drying mechanism, one end of the drying mechanism is provided with the collecting mechanism, the raw materials HMB-Ca, water and calcium hydroxide are poured into a first cylinder and fully stirred, so that metal ions in HMB-Ca solution react to generate insoluble precipitate, a plurality of groups of frames and heating plates are arranged, the HMB-Ca solution can be paved on a shallow layer at the upper end of the heating plate, so that the HMB-Ca solution can be quickly evaporated and crystallized, the HMB-Ca powder after impurity removal can be obtained, the scraper moves to one end to clean the HMB-Ca crystal powder attached to the upper end of the heating plate through the arranged linkage structure, and the scraper moves to one end to the other end, and the HMB-Ca crystal powder can also be discharged from one end of the frames through an opening of the frames.
Description
Technical Field
The invention relates to the technical field of impurity separation, in particular to an impurity separation device.
Background
The compound beta-hydroxy-beta-methylbutyric acid calcium, abbreviated as HMB-Ca, beta-hydroxy-beta-methylbutyric acid (HMB) is widely used in citrus fruits, certain vegetables such as cauliflower, legumes such as alfalfa and certain fish seafood, and because of the active nature of HMB, the process of the augmentation-preserving technology converts the HMB into calcium salt-beta-hydroxy-beta-methylbutyric acid calcium (HMB-Ca) by adopting a synthesis method; calcium salts are widely used, such as food additives, dietary additives, and the like.
However, the impurities in the existing HMB-Ca are mainly indissoluble mechanical impurities and some metal ions, the existing equipment is usually to dissolve HMB-Ca powder in water, the mechanical impurities mainly consist of sand and iron filings and are insoluble in water because the HMB-Ca powder is easily dissolved in water, so that the mechanical impurities can be removed by filtering HMB-Ca liquid, and the ions in the HMB-Ca powder are removed by adopting a chemical precipitation method, the principle is that indissoluble precipitate is generated by reaction with the metal ions, and then the metal ions are removed from the solution by filtering, and common precipitants are calcium hydroxide, aluminum hydroxide and the like.
The existing HMB-Ca impurity separation device has the defects that the existing device is not thorough in the process of separating HMB-Ca impurities, the existing device is complex in operation steps in the process of separating HMB-Ca impurities, so that the working efficiency is reduced, liquid is required to be evaporated in the process of removing impurities, the existing device is usually evaporated in a large container, the evaporation speed is low, the efficiency is low, and after evaporation, the crystallized powder of HMB-Ca can adhere to the bottom of the container, and the subsequent cleaning and collection of the bottom of the container are required, so that the invention designs the impurity separation device to solve the problems.
Disclosure of Invention
Aiming at the defects in the prior art, the invention provides an impurity separating device, which solves the problems that: the existing HMB-Ca impurity separation device has the defects that the existing device is not thorough in the process of separating HMB-Ca impurities, the existing device has more complicated operation steps in the process of separating HMB-Ca impurities, so that the working efficiency is reduced, liquid is required to be evaporated in the process of removing impurities, the existing device is usually evaporated in a large container, the evaporation speed is low, the efficiency is low, and the crystallized powder of HMB-Ca can be adhered to the bottom of the container after evaporation, so that the subsequent cleaning and collection of the bottom of the container are required to be carried out, and the time and labor are wasted;
in order to achieve the above purpose, the present invention is realized by the following technical scheme:
the invention provides an impurity separating device, which comprises
The device comprises a mixing mechanism, a valve mechanism, a separating mechanism, a drying mechanism and a collecting mechanism, wherein the valve mechanism is arranged at the lower end of the mixing mechanism;
preferably, the mixing mechanism comprises a bottom plate, the upper end of the bottom plate is fixedly connected with a supporting plate, the side wall of the supporting plate is fixedly connected with a feed hopper, and the side wall of the feed hopper is fixedly connected with a motor.
Preferably, the mixing mechanism further comprises a first cylinder, the side wall of the supporting plate is fixedly connected with the first cylinder, the lower end of the motor is fixedly connected with a rotating shaft, the lower end of the rotating shaft is fixedly connected with a stirring rod, the upper end of the bottom plate is fixedly connected with a collecting hopper, and the upper end of the bottom plate is provided with an opening.
Preferably, the valve mechanism comprises a first hydraulic cylinder, the side wall of the first hydraulic cylinder is fixedly connected with the supporting plate, the lower end of the first hydraulic cylinder is fixedly connected with a first connecting rod, one end of the first connecting rod is fixedly connected with a conical block, and the upper end of the conical block is fixedly connected with a second connecting rod.
Preferably, the valve mechanism further comprises a rubber block, the upper end of the second connecting rod is fixedly connected with the rubber block, a connecting groove is formed in the rubber block, a first sleeve is slidably connected to the side wall of the rubber block, and the side wall of the first sleeve is fixedly connected with the first cylinder.
Preferably, the separation mechanism comprises a filter screen, the upper end of the filter screen is fixedly connected with a first sleeve, and the lower end of the filter screen is fixedly connected with a second sleeve.
Preferably, the separation mechanism further comprises a first connecting pipe, and the side wall of the second sleeve is fixedly connected with the first connecting pipe.
Preferably, the drying mechanism comprises a frame, the lower end of the frame is fixedly connected with the bottom plate, the side wall of the frame is fixedly connected with a second connecting pipe, and the side wall of the inside of the frame is tightly attached with a scraping plate.
Preferably, the drying mechanism further comprises a fixing plate, the side wall of the scraping plate is fixedly connected with the fixing plate, and the lower end of the frame is fixedly connected with a heating plate.
Preferably, the collecting mechanism comprises a second hydraulic cylinder, the upper end of the second hydraulic cylinder is fixedly connected with the bottom plate, one end of the second hydraulic cylinder is fixedly connected with a connecting block, one end of the connecting block is fixedly connected with the scraping plate, and the upper end of the bottom plate is fixedly connected with a third sleeve.
Preferably, the collecting mechanism further comprises a sliding block, a sliding rod on the inner side wall of the third sleeve is connected with the sliding block, one end of the sliding block is fixedly connected with a spring, one end of the spring is fixedly connected with the third sleeve, and one end of the sliding block is fixedly connected with a baffle.
The invention has the beneficial effects that:
according to the impurity separating device, raw material HMB-Ca, water and calcium hydroxide are poured into the first cylinder, and the stirring rod is used for pouring the water and the calcium hydroxide into the feeding hopper, so that metal ions in the HMB-Ca solution react to generate insoluble precipitate.
According to the impurity separating device, the rubber block can be used for discharging the liquid stirred in the first cylinder, and meanwhile, the conical block can be driven to move downwards to be away from the bottom ends of the filter screen and the second sleeve when the rubber block moves downwards, so that the particle impurities in the filter screen are discharged, and the filter screen can be used for filtering sediment and impurity particles in HMB-Ca liquid.
According to the impurity separating device, the HMB-Ca liquid can be spread on the shallow layer at the upper end of the heating plate through the plurality of groups of the frames and the heating plate, so that the HMB-Ca liquid can be quickly evaporated and crystallized, HMB-Ca powder after impurity removal is obtained, the scraper is enabled to move to one end through the arranged linkage structure to clean HMB-Ca crystal powder attached to the upper end of the heating plate, and the HMB-Ca crystal powder can be discharged from one end of the frame through the opening while the scraper moves to one end.
Drawings
The invention will be further described with reference to the drawings and examples.
FIG. 1 is a schematic view of the overall structure provided by the present invention;
FIG. 2 is a schematic diagram of a connection structure of a base plate and a support plate;
FIG. 3 is a schematic view of the connection structure of the feed hopper and the motor;
FIG. 4 is a schematic diagram of a connection structure of a rotating shaft and a stirring rod;
FIG. 5 is a schematic view of a connection structure between the first cylinder and the first sleeve;
FIG. 6 is a schematic diagram of a connection structure of the second connecting rod and the rubber block;
FIG. 7 is a schematic view of a frame structure;
FIG. 8 is a schematic view of a second connecting pipe;
FIG. 9 is a schematic view of a connection structure of a scraper and a fixed plate;
FIG. 10 is a schematic diagram of a connection structure of the second hydraulic cylinder and the connection block;
FIG. 11 is a schematic diagram of a slider and spring connection.
In the figure: 1. a mixing mechanism; 11. a bottom plate; 12. a support plate; 13. a feed hopper; 14. a motor; 15. a first cylinder; 16. a rotating shaft; 17. a stirring rod; 18. a collecting hopper; 19. an opening; 2. a valve mechanism; 21. a first hydraulic cylinder; 22. a first connecting rod; 23. a conical block; 24. a second connecting rod; 25. a rubber block; 26. a connecting groove; 27. a first sleeve; 3. a separation mechanism; 31. a filter screen; 32. a second sleeve; 33. a first connection pipe; 4. a drying mechanism; 41. a frame; 42. a second connection pipe; 43. a scraper; 44. a fixing plate; 45. a heating plate; 5. a collection mechanism; 51. a second hydraulic cylinder; 52. a connecting block; 53. a third sleeve; 54. a sliding block; 55. a spring; 56. and a baffle.
Detailed Description
For the purpose of making the objects, technical means and advantages of the embodiments of the present invention more clear, the technical solutions in the embodiments of the present invention will be clearly and completely described, and it is apparent that the described embodiments are some embodiments of the present invention, but not all embodiments. All other embodiments, which can be made by those skilled in the art based on the embodiments of the invention without making any inventive effort, are intended to be within the scope of the invention.
The embodiment of the invention solves the problems that the prior HMB-Ca impurity separation device has incomplete HMB-Ca impurity separation process, the prior equipment has complicated operation steps in the HMB-Ca impurity separation process, thereby reducing the working efficiency, the prior equipment needs to evaporate liquid in the impurity removal process, the prior equipment usually evaporates in a large container, the evaporation speed is low, the crystalline powder of HMB-Ca is adhered to the bottom of the container after evaporation, and the subsequent cleaning and collecting of the bottom of the container are required to take time and labor;
the technical scheme in the embodiment of the invention aims to solve the technical problems, and the overall thought is as follows: the raw materials HMB-Ca, water and calcium hydroxide are poured into the first cylinder 15 to be fully stirred, so that metal ions in the HMB-Ca solution react to generate insoluble precipitate, a plurality of groups of frames 41 and heating plates 45 are arranged to enable HMB-Ca liquid to be laid in a shallow layer at the upper end of the heating plates 45, so that the HMB-Ca liquid can be quickly evaporated and crystallized, HMB-Ca powder after impurity removal is obtained, the scraper 43 is enabled to move towards one end to clean HMB-Ca crystal powder attached to the upper end of the heating plates 45 through the arranged linkage structure, and the HMB-Ca crystal powder can be discharged from one end of the frames 41 through an opening when the scraper 43 moves towards one end;
in order to better understand the above technical solutions, the following detailed description will refer to the accompanying drawings and specific embodiments.
As shown in fig. 1 to 11, an embodiment of the present invention provides an impurity separating apparatus including
The device comprises a mixing mechanism 1, a valve mechanism 2, a separating mechanism 3, a drying mechanism 4 and a collecting mechanism 5, wherein the valve mechanism 2 is arranged at the lower end of the mixing mechanism 1, the separating mechanism 3 is arranged at the lower end of the valve mechanism 2, the drying mechanism 4 is arranged at one end of the separating mechanism 3, and the collecting mechanism 5 is arranged at one end of the drying mechanism 4; the raw materials HMB-Ca, water and calcium hydroxide are poured into the first cylinder 15 to be fully stirred, so that metal ions in the HMB-Ca solution react to generate insoluble precipitate, the HMB-Ca liquid can be paved on a shallow layer at the upper end of the heating plate 45 by adopting the plurality of groups of frames 41 and the heating plate 45, the HMB-Ca liquid can be quickly evaporated and crystallized, the HMB-Ca powder after impurity removal is obtained, the scraper 43 moves towards one end to clean HMB-Ca crystal powder attached to the upper end of the heating plate 45 through the arranged linkage structure, and the HMB-Ca crystal powder can also be discharged from one end of the frame 41 through an opening at the same time when the scraper 43 moves towards one end.
Preferably, the mixing mechanism 1 includes a bottom plate 11, the upper end of the bottom plate 11 is fixedly connected with a supporting plate 12, the side wall of the supporting plate 12 is fixedly connected with a feed hopper 13, the side wall of the feed hopper 13 is fixedly connected with a motor 14, the side wall of the supporting plate 12 is fixedly connected with a first cylinder 15, the lower end of the motor 14 is fixedly connected with a rotating shaft 16, the lower end of the rotating shaft 16 is fixedly connected with a stirring rod 17, the upper end of the bottom plate 11 is fixedly connected with a collecting hopper 18, and the upper end of the bottom plate 11 is provided with an opening 19; firstly, pouring raw material HMB-Ca and a certain proportion of water and calcium hydroxide into a feed hopper 13, wherein the chemical property of the HMB-Ca is white powder and is easy to dissolve in water, at the moment, starting a motor 14 to rotate, driving a rotating shaft 16 to rotate by the rotation of the motor 14, driving a stirring rod 17 to rotate by the rotation of the rotating shaft 16, driving the raw material inside a first cylinder 15 to be uniformly mixed by the rotation of the stirring rod 17, and enabling the HMB-Ca to be fully mixed with the water and the calcium hydroxide.
Preferably, the valve mechanism 2 comprises a first hydraulic cylinder 21, the side wall of the first hydraulic cylinder 21 is fixedly connected with the supporting plate 12, the lower end of the first hydraulic cylinder 21 is fixedly connected with a first connecting rod 22, one end of the first connecting rod 22 is fixedly connected with a conical block 23, the upper end of the conical block 23 is fixedly connected with a second connecting rod 24, the upper end of the second connecting rod 24 is fixedly connected with a rubber block 25, a connecting groove 26 is formed in the rubber block 25, the side wall of the rubber block 25 is slidably connected with a first sleeve 27, and the side wall of the first sleeve 27 is fixedly connected with the first cylinder 15; after the stirring is finished, the first hydraulic cylinder 21 is started to move upwards, the first hydraulic cylinder 21 moves upwards to drive the first connecting rod 22 to move upwards, the first connecting rod 22 moves upwards to drive the conical block 23 to move upwards, the conical block 23 moves upwards to block the bottom of the filter screen 31 and the bottom of the second sleeve 32, the conical block 23 moves upwards to drive the second connecting rod 24 to move upwards, the second connecting rod 24 moves upwards to drive the rubber block 25 to move upwards, the rubber block 25 moves upwards to drive the connecting groove 26 to be far away from the first cylinder 15, at the moment, HMB-Ca liquid after the stirring is finished in the first cylinder 15 flows out into the first sleeve 27 through the connecting groove 26 on the rubber block 25, HMB-Ca liquid in the first sleeve 27 enters the filter screen 31, the conical block 25 is further driven to block the lower part in the process of the downward movement of the first hydraulic cylinder 21 to block the first sleeve 27, the conical block 23 is further driven to be far away from the bottom of the second sleeve 32 in the process of the downward movement of the first hydraulic cylinder 21, impurity particles existing in the interior of the first cylinder 25 can be discharged under the action of gravity, at the moment, the impurity particles in the filter screen 31 can also slide along the inner part of the conical block 23 and the filter screen 23 can be discharged out of the filter screen 25 when the impurity particles in the second sleeve 25 is further arranged in the process of the downward movement of the conical block 23, and the filter screen 25 is further arranged to be far away from the filter screen 31, and the inner than the filter screen 25 is further driven to move down along the conical part of the filter screen 31, and the impurity particles in the inner part can be discharged into the filter screen 31, and the inner part can be further down the slide down the filter screen 23, and the impurity particles can be separated.
Preferably, the separation mechanism 3 includes a filter screen 31, the upper end of the filter screen 31 is fixedly connected with a first sleeve 27, the lower end of the filter screen 31 is fixedly connected with a second sleeve 32, and the side wall of the second sleeve 32 is fixedly connected with a first connecting pipe 33; when the liquid enters the filter screen 31 through the first sleeve 27, the liquid diffuses into the second sleeve 32, so that the liquid can pass through the filter screen 31, and the particle impurities in the HMB-Ca liquid are filtered and remain in the filter screen 31, while the HMB-Ca liquid is discharged from the first connecting pipe 33 to the upper end of the heating plate 45, and the precipitate and impurity particles in the HMB-Ca liquid can be filtered by adopting the filter screen 31.
Preferably, the drying mechanism 4 includes a frame 41, the lower end of the frame 41 is fixedly connected with the bottom plate 11, a second connecting pipe 42 is fixedly connected with the side wall of the frame 41, a scraper 43 is tightly attached to the side wall of the interior of the frame 41, a fixing plate 44 is fixedly connected with the side wall of the scraper 43, and a heating plate 45 is fixedly connected with the lower end of the frame 41; when the liquid is discharged from the first connecting pipe 33 and falls on the upper end of the heating plate 45, the frames 41 arranged around the heating plate 45 are used for collecting the liquid, the liquid flows to the upper end of the next heating plate 45 when the page of the upper end of the heating plate 45 is higher than that of the second connecting pipe 42, the HMB-Ca liquid is evenly spread on the upper end of the heating plate 45, the heating plate 45 is started to heat at the moment, the heating plate 45 heats the HMB-Ca liquid to gradually evaporate and crystallize until the liquid is completely evaporated, and at the moment, the upper end of the heating plate 45 only has HMB-Ca crystallized powder, so that mechanical impurities and metal ion residues in the HMB-Ca product are effectively reduced, the safety of the HMB-Ca product as a health-care product and a food additive is improved, and the HMB-Ca liquid can be spread in a shallow layer at the upper end of the heating plate 45 through the plurality of groups of frames 41 and the heating plate 45, so that the HMB-Ca liquid can be rapidly evaporated and crystallized, and the HMB-Ca powder after impurity removal is obtained.
Preferably, the collecting mechanism 5 includes a second hydraulic cylinder 51, an upper end of the second hydraulic cylinder 51 is fixedly connected with the bottom plate 11, one end of the second hydraulic cylinder 51 is fixedly connected with a connecting block 52, one end of the connecting block 52 is fixedly connected with the scraper 43, an upper end of the bottom plate 11 is fixedly connected with a third sleeve 53, a sliding rod on an inner side wall of the third sleeve 53 is connected with a sliding block 54, one end of the sliding block 54 is fixedly connected with a spring 55, one end of the spring 55 is fixedly connected with the third sleeve 53, and one end of the sliding block 54 is fixedly connected with a baffle 56; at this time, the second hydraulic cylinder 51 is started to move to one end, the second hydraulic cylinder 51 moves to one end to drive the connecting block 52 to move to one end, the connecting block 52 moves to one end to drive the scraper 43 to move to one end, the scraper 43 moves to one end to scrape and clean HMB-Ca crystal powder attached to the upper end of the heating plate 45, the scraper 43 moves to one end to drive the fixing plate 44 to move to one end, the fixing plate 44 moves to one end to drive the baffle 56 to move to one end, the baffle 56 moves to one end to drive the sliding block 54 to move to one end, the sliding block 54 moves to one end to be far away from the heating plate 45, so that HMB-Ca crystal powder on the upper end of the heating plate 45 can be discharged from the opening 19, the spring 55 is compressed to move to one end of the sliding block 54, the lower end of the opening 19 is used for collecting HMB-Ca crystal powder after impurities are removed, the scraper 43 moves to one end to clean HMB-Ca crystal powder attached to the upper end of the heating plate 45 through the arranged linkage structure, and the scraper 43 moves to one end, and the HMB-Ca crystal powder can be discharged from one end of the frame 41 through the opening 19.
Working principle: when the invention is used, firstly, raw material HMB-Ca, a certain proportion of water and calcium hydroxide are poured into a feed hopper 13, the chemical property of the HMB-Ca is white powder and is easy to dissolve in water, at the moment, a motor 14 is started to rotate, the motor 14 rotates to drive a rotating shaft 16 to rotate, the rotating shaft 16 rotates to drive a stirring rod 17 to rotate, the stirring rod 17 rotates to drive the raw materials in the first cylinder 15 to be uniformly mixed, so that the HMB-Ca is fully mixed with the water and the calcium hydroxide, the principle is that insoluble precipitate is generated by the reaction of the calcium hydroxide and metal ions, so that the metal ions are removed from the solution, and the raw material HMB-Ca, the water and the calcium hydroxide are poured into the first cylinder 15, and the stirring rod 17 is poured into the feed hopper 13 for the water and the calcium hydroxide, so that the metal ions in the HMB-Ca solution react to generate the insoluble precipitate.
After the stirring is finished, the first hydraulic cylinder 21 is started to move upwards, the first hydraulic cylinder 21 moves upwards to drive the first connecting rod 22 to move upwards, the first connecting rod 22 moves upwards to drive the conical block 23 to move upwards, the conical block 23 moves upwards to block the bottom of the filter screen 31 and the bottom of the second sleeve 32, the conical block 23 moves upwards to drive the second connecting rod 24 to move upwards, the second connecting rod 24 moves upwards to drive the rubber block 25 to move upwards, the rubber block 25 moves upwards to drive the connecting groove 26 to be far away from the first cylinder 15, at the moment, HMB-Ca liquid after the stirring is finished in the first cylinder 15 flows out into the first sleeve 27 through the connecting groove 26 on the rubber block 25, HMB-Ca liquid in the first sleeve 27 enters the filter screen 31, the conical block 25 is further driven to block the lower part in the process of the downward movement of the first hydraulic cylinder 21 to block the first sleeve 27, the conical block 23 is further driven to be far away from the bottom of the second sleeve 32 in the process of the downward movement of the first hydraulic cylinder 21, impurity particles existing in the interior of the first cylinder 25 can be discharged under the action of gravity, at the moment, the impurity particles in the filter screen 31 can also slide along the inner part of the conical block 23 and the filter screen 23 can be discharged out of the filter screen 25 when the impurity particles in the second sleeve 25 is further arranged in the process of the downward movement of the conical block 23, and the filter screen 25 is further arranged to be far away from the filter screen 31, and the inner than the filter screen 25 is further driven to move down along the conical part of the filter screen 31, and the impurity particles in the inner part can be discharged into the filter screen 31, and the inner part can be further down the slide down the filter screen 23, and the impurity particles can be separated.
When the liquid enters the filter screen 31 through the first sleeve 27, the liquid diffuses into the second sleeve 32, so that the liquid can pass through the filter screen 31, and the particle impurities in the HMB-Ca liquid are filtered and remain in the filter screen 31, while the HMB-Ca liquid is discharged from the first connecting pipe 33 to the upper end of the heating plate 45, and the precipitate and impurity particles in the HMB-Ca liquid can be filtered by adopting the filter screen 31.
When the liquid is discharged from the first connecting pipe 33 and falls on the upper end of the heating plate 45, the frames 41 arranged around the heating plate 45 are used for collecting the liquid, the liquid flows to the upper end of the next heating plate 45 when the page of the upper end of the heating plate 45 is higher than that of the second connecting pipe 42, the HMB-Ca liquid is evenly spread on the upper end of the heating plate 45, the heating plate 45 is started to heat at the moment, the heating plate 45 heats the HMB-Ca liquid to gradually evaporate and crystallize until the liquid is completely evaporated, and at the moment, the upper end of the heating plate 45 only has HMB-Ca crystallized powder, so that mechanical impurities and metal ion residues in the HMB-Ca product are effectively reduced, the safety of the HMB-Ca product as a health-care product and a food additive is improved, and the HMB-Ca liquid can be spread in a shallow layer at the upper end of the heating plate 45 through the plurality of groups of frames 41 and the heating plate 45, so that the HMB-Ca liquid can be rapidly evaporated and crystallized, and the HMB-Ca powder after impurity removal is obtained.
At this time, the second hydraulic cylinder 51 is started to move to one end, the second hydraulic cylinder 51 moves to one end to drive the connecting block 52 to move to one end, the connecting block 52 moves to one end to drive the scraper 43 to move to one end, the scraper 43 moves to one end to scrape and clean HMB-Ca crystal powder attached to the upper end of the heating plate 45, the scraper 43 moves to one end to drive the fixing plate 44 to move to one end, the fixing plate 44 moves to one end to drive the baffle 56 to move to one end, the baffle 56 moves to one end to drive the sliding block 54 to move to one end, the sliding block 54 moves to one end to be far away from the heating plate 45, so that HMB-Ca crystal powder on the upper end of the heating plate 45 can be discharged from the opening 19, the spring 55 is compressed to move to one end of the sliding block 54, the lower end of the opening 19 is used for collecting HMB-Ca crystal powder after impurities are removed, the scraper 43 moves to one end to clean HMB-Ca crystal powder attached to the upper end of the heating plate 45 through the arranged linkage structure, and the scraper 43 moves to one end, and the HMB-Ca crystal powder can be discharged from one end of the frame 41 through the opening 19.
The foregoing has shown and described the basic principles, principal features and advantages of the invention. It will be understood by those skilled in the art that the present invention is not limited to the foregoing examples, and that the foregoing description and description are merely illustrative of the principles of this invention, and various changes and modifications may be made without departing from the spirit and scope of the invention, which is defined in the appended claims. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (10)
1. An impurity separation device, characterized in that: the device comprises a mixing mechanism (1), a valve mechanism (2), a separating mechanism (3), a drying mechanism (4) and a collecting mechanism (5), wherein the valve mechanism (2) is arranged at the lower end of the mixing mechanism (1), the separating mechanism (3) is arranged at the lower end of the valve mechanism (2), the drying mechanism (4) is arranged at one end of the separating mechanism (3), and the collecting mechanism (5) is arranged at one end of the drying mechanism (4);
the mixing mechanism (1) comprises a bottom plate (11), wherein the upper end of the bottom plate (11) is fixedly connected with a supporting plate (12), the side wall of the supporting plate (12) is fixedly connected with a feed hopper (13), and the side wall of the feed hopper (13) is fixedly connected with a motor (14).
2. An impurity separating device according to claim 1, wherein: the mixing mechanism (1) further comprises a first cylinder (15), the side wall of the supporting plate (12) is fixedly connected with the first cylinder (15), the lower end of the motor (14) is fixedly connected with a rotating shaft (16), the lower end of the rotating shaft (16) is fixedly connected with a stirring rod (17), the upper end of the bottom plate (11) is fixedly connected with a collecting hopper (18), and the upper end of the bottom plate (11) is provided with an opening (19).
3. An impurity separating device according to claim 1, wherein: the valve mechanism (2) comprises a first hydraulic cylinder (21), the side wall of the first hydraulic cylinder (21) is fixedly connected with a supporting plate (12), the lower end of the first hydraulic cylinder (21) is fixedly connected with a first connecting rod (22), one end of the first connecting rod (22) is fixedly connected with a conical block (23), and the upper end of the conical block (23) is fixedly connected with a second connecting rod (24).
4. An impurity separating device according to claim 3, wherein: the valve mechanism (2) further comprises a rubber block (25), the upper end of the second connecting rod (24) is fixedly connected with the rubber block (25), a connecting groove (26) is formed in the rubber block (25), a first sleeve (27) is slidably connected to the side wall of the rubber block (25), and the side wall of the first sleeve (27) is fixedly connected with the first cylinder (15).
5. An impurity separating apparatus according to claim 4, wherein: the separating mechanism (3) comprises a filter screen (31), the upper end of the filter screen (31) is fixedly connected with a first sleeve (27), and the lower end of the filter screen (31) is fixedly connected with a second sleeve (32).
6. An impurity separating apparatus according to claim 5, wherein: the separating mechanism (3) further comprises a first connecting pipe (33), and the side wall of the second sleeve (32) is fixedly connected with the first connecting pipe (33).
7. An impurity separating device according to claim 1, wherein: the drying mechanism (4) comprises a frame (41), the lower end of the frame (41) is fixedly connected with the bottom plate (11), a second connecting pipe (42) is fixedly connected with the side wall of the frame (41), and a scraping plate (43) is tightly attached to the inner side wall of the frame (41).
8. An impurity separating device according to claim 7, wherein: the drying mechanism (4) further comprises a fixing plate (44), the side wall of the scraping plate (43) is fixedly connected with the fixing plate (44), and the lower end of the frame (41) is fixedly connected with a heating plate (45).
9. An impurity separating device according to claim 1, wherein: the collecting mechanism (5) comprises a second hydraulic cylinder (51), the upper end of the second hydraulic cylinder (51) is fixedly connected with the bottom plate (11), one end of the second hydraulic cylinder (51) is fixedly connected with a connecting block (52), one end of the connecting block (52) is fixedly connected with the scraping plate (43), and the upper end of the bottom plate (11) is fixedly connected with a third sleeve (53).
10. An impurity separating device according to claim 9, wherein: the collecting mechanism (5) further comprises a sliding block (54), a sliding rod on the inner side wall of the third sleeve (53) is connected with the sliding block (54), one end of the sliding block (54) is fixedly connected with a spring (55), one end of the spring (55) is fixedly connected with the third sleeve (53), and one end of the sliding block (54) is fixedly connected with a baffle plate (56).
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| CN202311727212.5A CN117398760B (en) | 2023-12-15 | 2023-12-15 | Impurity separating device |
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| CN202311727212.5A CN117398760B (en) | 2023-12-15 | 2023-12-15 | Impurity separating device |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| CN212941745U (en) * | 2020-05-18 | 2021-04-13 | 安徽福相安油脂工业有限公司 | Supplementary stifled mechanism of producing oil that prevents of usefulness of edible vegetable oil production |
| CN115010293A (en) * | 2022-05-31 | 2022-09-06 | 安徽超越环保科技股份有限公司 | Method for treating useful components in mixed waste acid containing heavy metal ions |
| CN115869699A (en) * | 2022-12-02 | 2023-03-31 | 武汉江汉化工设计有限公司 | Lithium hexafluorophosphate purification device and purification method |
| CN116785975A (en) * | 2023-07-31 | 2023-09-22 | 长沙鑫兴环保科技有限公司 | Refined aluminum sulfate edulcoration device |
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Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN212941745U (en) * | 2020-05-18 | 2021-04-13 | 安徽福相安油脂工业有限公司 | Supplementary stifled mechanism of producing oil that prevents of usefulness of edible vegetable oil production |
| CN115010293A (en) * | 2022-05-31 | 2022-09-06 | 安徽超越环保科技股份有限公司 | Method for treating useful components in mixed waste acid containing heavy metal ions |
| CN115869699A (en) * | 2022-12-02 | 2023-03-31 | 武汉江汉化工设计有限公司 | Lithium hexafluorophosphate purification device and purification method |
| CN116785975A (en) * | 2023-07-31 | 2023-09-22 | 长沙鑫兴环保科技有限公司 | Refined aluminum sulfate edulcoration device |
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