CN115301325B - High-efficiency production device and production method of broad-spectrum plant source bactericide - Google Patents
High-efficiency production device and production method of broad-spectrum plant source bactericide Download PDFInfo
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- CN115301325B CN115301325B CN202210826538.2A CN202210826538A CN115301325B CN 115301325 B CN115301325 B CN 115301325B CN 202210826538 A CN202210826538 A CN 202210826538A CN 115301325 B CN115301325 B CN 115301325B
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- box
- freezer
- soaking
- conveying
- pipe
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- 238000004519 manufacturing process Methods 0.000 title claims abstract description 32
- 230000000844 anti-bacterial effect Effects 0.000 title claims abstract description 22
- 239000003899 bactericide agent Substances 0.000 title claims abstract description 19
- 238000002791 soaking Methods 0.000 claims abstract description 54
- 239000000843 powder Substances 0.000 claims abstract description 20
- 238000000227 grinding Methods 0.000 claims description 45
- 238000001816 cooling Methods 0.000 claims description 22
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 claims description 21
- 239000007788 liquid Substances 0.000 claims description 16
- 238000003825 pressing Methods 0.000 claims description 16
- 230000005540 biological transmission Effects 0.000 claims description 13
- 206010006514 bruxism Diseases 0.000 claims description 7
- 238000010438 heat treatment Methods 0.000 claims description 7
- 239000003480 eluent Substances 0.000 claims description 5
- 238000000034 method Methods 0.000 claims description 5
- 238000002360 preparation method Methods 0.000 claims description 4
- 238000010521 absorption reaction Methods 0.000 claims description 3
- 230000008878 coupling Effects 0.000 claims description 3
- 238000010168 coupling process Methods 0.000 claims description 3
- 238000005859 coupling reaction Methods 0.000 claims description 3
- 238000002955 isolation Methods 0.000 claims description 3
- 238000005086 pumping Methods 0.000 claims description 3
- 238000004804 winding Methods 0.000 claims description 2
- 230000002070 germicidal effect Effects 0.000 claims 3
- 238000007710 freezing Methods 0.000 abstract description 10
- 230000008014 freezing Effects 0.000 abstract description 10
- 230000000694 effects Effects 0.000 abstract description 7
- 239000000419 plant extract Substances 0.000 abstract description 5
- 238000000605 extraction Methods 0.000 abstract description 2
- 241000196324 Embryophyta Species 0.000 description 60
- 239000000243 solution Substances 0.000 description 13
- 238000005194 fractionation Methods 0.000 description 2
- 239000012634 fragment Substances 0.000 description 2
- 239000000463 material Substances 0.000 description 2
- 238000010298 pulverizing process Methods 0.000 description 2
- 239000002994 raw material Substances 0.000 description 2
- 241001061264 Astragalus Species 0.000 description 1
- 102000000541 Defensins Human genes 0.000 description 1
- 108010002069 Defensins Proteins 0.000 description 1
- 241000931143 Gleditsia sinensis Species 0.000 description 1
- 229930013930 alkaloid Natural products 0.000 description 1
- 229940069521 aloe extract Drugs 0.000 description 1
- 235000006533 astragalus Nutrition 0.000 description 1
- 244000052616 bacterial pathogen Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- YBHILYKTIRIUTE-UHFFFAOYSA-N berberine Chemical compound C1=C2CC[N+]3=CC4=C(OC)C(OC)=CC=C4C=C3C2=CC2=C1OCO2 YBHILYKTIRIUTE-UHFFFAOYSA-N 0.000 description 1
- 229940093265 berberine Drugs 0.000 description 1
- QISXPYZVZJBNDM-UHFFFAOYSA-N berberine Natural products COc1ccc2C=C3N(Cc2c1OC)C=Cc4cc5OCOc5cc34 QISXPYZVZJBNDM-UHFFFAOYSA-N 0.000 description 1
- 238000004891 communication Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000010586 diagram Methods 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 235000013399 edible fruits Nutrition 0.000 description 1
- 238000004134 energy conservation Methods 0.000 description 1
- 239000000284 extract Substances 0.000 description 1
- 238000001125 extrusion Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 229930003935 flavonoid Natural products 0.000 description 1
- 235000017173 flavonoids Nutrition 0.000 description 1
- 150000002215 flavonoids Chemical class 0.000 description 1
- 150000004676 glycans Chemical class 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 238000002347 injection Methods 0.000 description 1
- 239000007924 injection Substances 0.000 description 1
- 238000002156 mixing Methods 0.000 description 1
- 150000007524 organic acids Chemical class 0.000 description 1
- 235000005985 organic acids Nutrition 0.000 description 1
- 150000002989 phenols Chemical class 0.000 description 1
- 229920001282 polysaccharide Polymers 0.000 description 1
- 239000005017 polysaccharide Substances 0.000 description 1
- 235000018102 proteins Nutrition 0.000 description 1
- 102000004169 proteins and genes Human genes 0.000 description 1
- 108090000623 proteins and genes Proteins 0.000 description 1
- 229930000044 secondary metabolite Natural products 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 210000004233 talus Anatomy 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 1
Classifications
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C2/00—Crushing or disintegrating by gyratory or cone crushers
- B02C2/10—Crushing or disintegrating by gyratory or cone crushers concentrically moved; Bell crushers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D1/00—Evaporating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D11/00—Solvent extraction
- B01D11/02—Solvent extraction of solids
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/01—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
- B01D29/03—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements self-supporting
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D3/00—Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping
- B01D3/14—Fractional distillation or use of a fractionation or rectification column
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C19/00—Other disintegrating devices or methods
- B02C19/18—Use of auxiliary physical effects, e.g. ultrasonics, irradiation, for disintegrating
- B02C19/186—Use of cold or heat for disintegrating
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C23/00—Auxiliary methods or auxiliary devices or accessories specially adapted for crushing or disintegrating not provided for in preceding groups or not specially adapted to apparatus covered by a single preceding group
- B02C23/02—Feeding devices
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B02—CRUSHING, PULVERISING, OR DISINTEGRATING; PREPARATORY TREATMENT OF GRAIN FOR MILLING
- B02C—CRUSHING, PULVERISING, OR DISINTEGRATING IN GENERAL; MILLING GRAIN
- B02C4/00—Crushing or disintegrating by roller mills
- B02C4/02—Crushing or disintegrating by roller mills with two or more rollers
- B02C4/08—Crushing or disintegrating by roller mills with two or more rollers with co-operating corrugated or toothed crushing-rollers
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B30—PRESSES
- B30B—PRESSES IN GENERAL
- B30B9/00—Presses specially adapted for particular purposes
- B30B9/02—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material
- B30B9/04—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using press rams
- B30B9/06—Presses specially adapted for particular purposes for squeezing-out liquid from liquid-containing material, e.g. juice from fruits, oil from oil-containing material using press rams co-operating with permeable casings or strainers
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D19/00—Arrangement or mounting of refrigeration units with respect to devices or objects to be refrigerated, e.g. infrared detectors
Landscapes
- Engineering & Computer Science (AREA)
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Food Science & Technology (AREA)
- Mechanical Engineering (AREA)
- Thermal Sciences (AREA)
- Physics & Mathematics (AREA)
- General Engineering & Computer Science (AREA)
- Combustion & Propulsion (AREA)
- Health & Medical Sciences (AREA)
- Toxicology (AREA)
- Medicines Containing Plant Substances (AREA)
- Crushing And Pulverization Processes (AREA)
Abstract
The invention discloses a high-efficiency production device and a production method of a broad-spectrum plant source bactericide, wherein the high-efficiency production device comprises a refrigerator, and an evaporator is arranged on one side of the refrigerator; the conveying device is arranged below the freezer, a feeding pipe is arranged between one side of the upper end of the conveying device and the freezer, and an electromagnetic valve is arranged at the middle position of the feeding pipe; the soaking box is arranged at one end of the conveying device, which is far away from the freezing box, and the other side of the lower end of the conveying device is connected with the soaking box through a powder outlet pipe, and the upper end of the soaking box is provided with an adjusting device; the fractionating box is arranged at one side of the soaking box, the fractionating box is connected with the soaking box through a conveying pipe, and a pump is arranged at the middle position of the conveying pipe; the collecting box is arranged on one side of the fractionating box, and a condensing pipe is connected between the fractionating box and the collecting box, so that the problem that the production efficiency of the bactericide is affected due to poor extraction effect of plant extract is solved.
Description
Technical Field
The invention relates to the technical field of broad-spectrum plant source bactericide production devices, in particular to a high-efficiency production device and a production method of a broad-spectrum plant source bactericide.
Background
The plant source bactericide is plant defensin produced by utilizing some antibacterial substances or induction contained in some plants to kill or effectively inhibit the growth and development of some pathogenic bacteria. Antibacterial compounds in plants are a variety of secondary metabolites produced by plants and have antibacterial activity and include many different types of alkaloids, flavonoids, proteins, organic acids and phenolic compounds.
For example, chinese published patent No. CN102940000A, plant source broad spectrum bactericide, berberine 0.5-4.5%, astragalus polysaccharide 0.5-20%, radix tetrastigme extract 0.5-20%, aloe extract 0.5-20%, chinese honeylocust fruit 0.5-20% and the balance water, wherein the preparation of bactericide is realized by mixing the extracted plant essence.
Although the above prior art relates to the production of a bactericide by using a plant extract, a detailed obtaining method is not given in terms of a production mode of the plant extract, and the obtaining of the plant extract greatly affects the production efficiency of the bactericide, so that the existing requirements are not satisfied, and a high-efficiency production device and a production method of a broad-spectrum plant-source bactericide are proposed.
Disclosure of Invention
The invention aims to provide a high-efficiency production device and a production method of a broad-spectrum plant source bactericide, which are used for solving the problem that the production efficiency of the bactericide is affected due to poor extraction effect of plant extract in the background art.
In order to achieve the above purpose, the present invention provides the following technical solutions: a high-efficiency production device and a production method of a broad-spectrum plant source bactericide comprise a freezing box, wherein an evaporator is arranged on one side of the freezing box;
the conveying device is arranged below the freezer, a feeding pipe is arranged between one side of the upper end of the conveying device and the freezer, and an electromagnetic valve is arranged at the middle position of the feeding pipe;
The soaking box is arranged at one end of the conveying device, which is far away from the freezing box, and the other side of the lower end of the conveying device is connected with the soaking box through a powder outlet pipe, and the upper end of the soaking box is provided with an adjusting device;
the fractionating box is arranged at one side of the soaking box, the fractionating box is connected with the soaking box through a conveying pipe, and a pump is arranged at the middle position of the conveying pipe;
The collecting box is arranged on one side of the fractionating box, and a condensing pipe is connected between the fractionating box and the collecting box.
Preferably, the lower extreme of freezer is the toper structure, and crushing roller is installed to the inside rotation of toper structure, the fixed drive mechanism that is provided with in below of freezer rear end, drive mechanism's internally mounted has two meshing gears, and the meshing is connected between the meshing gear, and crushing roller's one end is fixed mutually with the meshing gear, one side fixed mounting of drive mechanism rear end has the second motor, and the output shaft and one of them meshing gear pass through the shaft coupling transmission and are connected.
Preferably, the spiral conveying blade is rotatably arranged in the conveying device, a first motor is fixedly arranged at one end of the conveying device, and an output shaft of the first motor is in transmission connection with one end of the spiral conveying blade.
Preferably, the grinding wheel is arranged at the other end of the spiral conveying blade, the grinding wheel is in a round table structure, a grinding inner gear ring is arranged at the other end inside the conveying device, the grinding inner gear ring and the grinding teeth of the grinding wheel are opposite in direction, and one end of the grinding wheel extends to the inner part of the grinding inner gear ring.
Preferably, the rotary drum is installed to the inside lower extreme of adjusting device, and rotary drum passes through the bearing connection with adjusting device, the fixed first conical gear that is provided with in upper end of rotary drum, one side meshing of first conical gear has second conical gear, and the axle and the adjusting device rotation of second conical gear are connected, the one end of second conical gear axle is provided with the crank, and the crank is located adjusting device's outside, the threaded rod is installed to the central point of rotary drum, and threaded rod and rotary drum's internal thread connection, the upper end fixed mounting of threaded rod has spacing slider, and in spacing slider's both sides extended to adjusting device's the inner wall, and spacing slider and adjusting device sliding connection, the clamp plate is installed to the lower extreme of threaded rod, and the clamp plate is located the inside of soaking case.
Preferably, a filter screen is fixedly arranged at the lower end inside the soaking box.
Preferably, one side of the soaking box is also provided with an eluent adding port.
Preferably, a heating device is arranged at the lower end of the inside of the fractionating box.
Preferably, the outside winding of condenser pipe has the cooling tube, and the both ends of cooling tube all communicate with the freezer, cooling tube externally mounted has the fan, and the cooling tube sets up the isolation network with the intercommunication department of freezer.
The production method of the high-efficiency production device of the broad-spectrum plant source bactericide comprises the following steps:
Firstly, placing plants to be extracted into a freezer, after a refrigerating mechanism operates, rapidly cooling the interior of the freezer under the action of heat absorption of an evaporator, and after the set time is reached, making the plants in a frozen state;
Step two, starting a second motor to enable the two crushing rollers to rotate inwards, wherein frozen plants in the freezer are crushed into a plurality of small pieces after contacting the crushing rollers, and then enter the conveying device through the feed pipe;
Step three, a spiral conveying blade in the conveying device pushes the blocky plants to move towards the other end, the spiral conveying blade drives the grinding wheel to rotate in the rotating process, and when the blocky plants move to contact grinding teeth of the grinding inner gear ring and the grinding wheel, grinding treatment is rapidly carried out on the blocky plants, so that fine frozen plant powder is formed, and the plant powder enters a soaking box through a powder outlet pipe;
Step four, adding methanol into the soaking box, and after the soaking time is up, enabling a user to rotate a crank to enable a threaded rod to vertically move, so that a pressing plate moves downwards, pressing plant soaking liquid downwards, extruding the plant soaking liquid, and enabling the liquid to quickly pass through a filter screen;
Step five, starting a pump, conveying extruded liquid into the fractionating box through a conveying pipe, starting a heating device, distilling the liquid, storing distilled extracting solution in a collecting box, and quantitatively extracting plant extracting solution in the collecting box if different extracting solutions are required to be mixed for preparation.
Compared with the prior art, the invention has the beneficial effects that:
1. According to the invention, the plant extracting solution is obtained in the modes of freezing, grinding, soaking, filtering and distilling, the individual plants are quickly cooled under the endothermic action of the evaporator after being added into the freezing box, so that the plants are quickly frozen, then the plant structure is damaged under the opposite movement of the crushing roller, the plant is frozen, the body is hard, a plurality of tiny fragments are formed, the fragments are transported through the conveying device, the fine grinding is carried out again at the outlet, the plant raw materials are converted into a powder state, the powder state enters the soaking box through the separating outlet pipe, methanol is added into the soaking box, the grinding state is formed at a low temperature by the plant raw materials, the damage of the internal components of the plants caused by conventional drying grinding is avoided, the plant components are protected to the greatest extent, the plant components can be quickly contacted with the methanol during soaking, the pressing plate falls down after the soaking setting time, the liquid is conveyed to the lower part of the filter screen through the conveying pipeline and is heated and distilled in the fractionating box, the distilled extracting solution is stored in the collecting box, and if the different extracting solutions are required to be mixed and prepared, the plant extracting solution in the collecting box is only required to be quantitatively extracted, the plant extracting solution in the collecting box is not damaged in the production mode, and the plant extracting solution can be prevented from being damaged in the production process to the greatest extent.
2. According to the invention, the grinding annular gear and the grinding wheel are arranged in the conveying device, the plant in the broken state is extruded to the grinding wheel by the spiral conveying blade, and the spiral conveying blade drives the grinding wheel to rotate, so that the grinding treatment can be quickly carried out on the plant along with the continuous moving contact between the annular gear and the grinding teeth of the grinding wheel, so that fine frozen plant powder is formed, and the plant powder enters the soaking box through the powder outlet pipe.
3. According to the invention, the adjusting device is arranged, the pressing plate is positioned above the outlet of the powder outlet pipe in a conventional state, so that normal material injection is not influenced, after the soaking time is reached, a user can rotate the crank, one end of the crank drives the second bevel gear in the adjusting device to rotate, and then the rotating cylinder provided with the first bevel gear is driven to rotate under the meshing effect.
4. According to the invention, the cooling pipe is arranged outside the condensing pipe, two ends of the cooling pipe extend into the refrigerator respectively, and air in the refrigerator is circulated in the cooling pipe under the action of the fan, so that the cooling efficiency is high, and meanwhile, the existing device structure is utilized, so that the effective energy conservation is realized.
Drawings
FIG. 1 is a schematic diagram of the overall structure of the present invention;
FIG. 2 is a perspective view of the present invention;
FIG. 3 is a top view of a pulverizing roll of the present invention;
FIG. 4 is an enlarged view of a portion of the area A of FIG. 1 in accordance with the present invention;
Fig. 5 is a partial enlarged view of the area B of fig. 1 in accordance with the present invention.
In the figure: 1. a freezer; 2. a soaking box; 3. a fractionation box; 4. a collection box; 5. an evaporator; 6. a pulverizing roller; 7. a feed pipe; 8. a conveying device; 9. spiral conveying blades; 10. a first motor; 11. a powder outlet pipe; 12. an adjusting device; 13. a threaded rod; 14. a limit sliding block; 15. a crank; 16. a pressing plate; 17. a filter screen; 18. a material conveying pipe; 19. a heating device; 20. a condensing tube; 21. a cooling tube; 22. pumping; 23. a blower; 24. a transmission mechanism; 25. a second motor; 26. a meshing gear; 27. grinding the inner gear ring; 28. grinding wheel; 29. a rotary drum; 30. a first bevel gear; 31. a second bevel gear.
Detailed Description
The following description of the embodiments of the present invention 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 invention, but not all embodiments.
Referring to fig. 1-5, an embodiment of the present invention is provided: a high-efficiency production device of broad-spectrum plant source bactericide and a production method thereof comprise a freezing box 1, wherein one side of the freezing box 1 is provided with an evaporator 5, the evaporator 5 is a part of a refrigerating system, and conventional medium is adopted for freezing;
The conveying device 8 is arranged below the freezer 1, a feeding pipe 7 is arranged between one side of the upper end of the conveying device 8 and the freezer 1, and an electromagnetic valve is arranged at the middle position of the feeding pipe 7;
The soaking box 2 is arranged at one end of the conveying device 8 far away from the freezing box 1, the other side of the lower end of the conveying device 8 is connected with the soaking box 2 through a powder outlet pipe 11, and the upper end of the soaking box 2 is provided with an adjusting device 12;
the fractionating box 3 is arranged on one side of the soaking box 2, the fractionating box 3 is connected with the soaking box 2 through a conveying pipe 18, and a pump 22 is arranged in the middle of the conveying pipe 18;
And a collecting tank 4 provided at one side of the fractionating tank 3, and a condensing pipe 20 is connected between the fractionating tank 3 and the collecting tank 4.
Referring to fig. 3, the lower end of the freezer 1 is in a conical structure, the crushing roller 6 is rotatably mounted in the conical structure, the transmission mechanism 24 is fixedly arranged below the rear end of the freezer 1, two meshing gears 26 are mounted in the transmission mechanism 24, the meshing gears 26 are connected with each other, one end of the crushing roller 6 is fixed with the meshing gear 26, a second motor 25 is fixedly mounted on one side of the rear end of the transmission mechanism 24, an output shaft of the second motor 25 is in transmission connection with one of the meshing gears 26 through a coupling, the output shaft of the second motor 25 drives the meshing gears 26 to rotate, and the two crushing rollers 6 rotate in opposite directions under the meshing effect to crush frozen plants.
Referring to fig. 1, a spiral conveying blade 9 is rotatably installed in a conveying device 8, a first motor 10 is fixedly installed at one end of the conveying device 8, and an output shaft of the first motor 10 is in transmission connection with one end of the spiral conveying blade 9, so that extrusion pushing of massive plants can be achieved.
Referring to fig. 4, the grinding wheel 28 is mounted at the other end of the spiral conveying blade 9, the grinding wheel 28 is in a circular truncated cone structure, the grinding inner gear ring 27 is arranged at the other end inside the conveying device 8, the grinding inner gear ring 27 and the grinding teeth of the grinding wheel 28 are opposite in direction, one end of the grinding wheel 28 extends to the inner part of the grinding inner gear ring 27, and grinding treatment of plants can be achieved while conveying the plants, so that not only is the soaking effect of the follow-up plants and methanol improved, but also the treatment efficiency is effectively improved.
Referring to fig. 1 and 5, a rotary drum 29 is installed at the lower end of the inside of the adjusting device 12, the rotary drum 29 is connected with the adjusting device 12 through a bearing, a first bevel gear 30 is fixedly arranged at the upper end of the rotary drum 29, a second bevel gear 31 is meshed with one side of the first bevel gear 30, the shaft of the second bevel gear 31 is rotationally connected with the adjusting device 12, a crank 15 is arranged at one end of the shaft of the second bevel gear 31, the crank 15 is positioned outside the adjusting device 12, a threaded rod 13 is installed at the center position of the rotary drum 29, the threaded rod 13 is connected with the internal thread of the rotary drum 29, a limit slide block 14 is fixedly arranged at the upper end of the threaded rod 13, two sides of the limit slide block 14 extend into the inner wall of the adjusting device 12, the limit slide block 14 is in sliding connection with the adjusting device 12, a pressing plate 16 is installed at the lower end of the threaded rod 13, the pressing plate 16 is positioned inside the soaking box 2, one end of the crank 15 drives the second bevel gear 31 inside the adjusting device 12 to rotate, and further drives the rotary drum 29 provided with the first bevel gear 30 to rotate under the meshing effect, the rotation effect, the rotary drum 29 is connected with the threaded rod 29 through the bearing 29, and the rotary slide block 29 can not move along with the threaded rod 13 through the bearing, and the rotation can be vertically displaced along with the rotary drum 13 through the bearing, and the rotation can be vertically displaced with the threaded rod 13.
Referring to fig. 1, a filter screen 17 is fixedly arranged at the lower end of the interior of the soaking tank 2 to prevent plant residues from entering the fractionating tank 3.
Referring to fig. 1, an eluent adding port is further provided on one side of the soaking tank 2, and the eluent is methanol.
Referring to fig. 1, a heating device 19 is installed at the lower end of the inside of the fractionation box 3.
Referring to fig. 1, a cooling tube 21 is wound around the outside of a condensing tube 20, two ends of the cooling tube 21 are communicated with a refrigerator 1, a fan 23 is mounted on the outside of the cooling tube 21, an isolation net is arranged at the communication position between the cooling tube 21 and the refrigerator 1, and air in the refrigerator 1 circulates in the cooling tube 21 under the action of the fan 23, so that the cooling efficiency is high, and meanwhile, the existing device structure is utilized, and effective energy saving is realized.
The production method of the high-efficiency production device of the broad-spectrum plant source bactericide comprises the following steps:
Firstly, placing plants to be extracted into a freezer 1, after a refrigerating mechanism operates, rapidly cooling the interior of the freezer 1 under the action of heat absorption of an evaporator, and after a set time is reached, making the plants in a frozen state;
Step two, starting a second motor 25 to enable the two crushing rollers 6 to rotate inwards, wherein frozen plants in the freezer 1 are crushed into a plurality of small blocks after contacting the crushing rollers 6, and then enter the conveying device 8 through the feed pipe 7;
Step three, the spiral conveying blades 9 in the conveying device 8 push the blocky plants to move towards the other end, the spiral conveying blades 9 can drive the grinding wheel 28 to rotate in the rotating process, and when the blocky plants move to contact grinding teeth of the grinding inner gear ring 27 and the grinding wheel 28, grinding treatment is performed on the blocky plants rapidly, so that fine frozen plant powder is formed, and the plant powder enters the soaking box 2 through the powder outlet pipe 11;
Step four, adding methanol into the soaking box 2, after the soaking time is up, a user can rotate a crank 15 to enable a threaded rod 13 to vertically move, so that a pressing plate 16 moves downwards, plant soaking liquid is pressed downwards, the plant soaking liquid is extruded, and the liquid rapidly passes through a filter screen 17;
Step five, starting a pump 22, conveying extruded liquid into the fractionating box 3 through a conveying pipe 18, starting a heating device 19, distilling the liquid, storing distilled extracting solution in the collecting box 4, and quantitatively pumping out plant extracting solution in the collecting box 4 if different extracting solutions are required to be mixed for preparation.
It will be evident to those skilled in the art that the invention is not limited to the details of the foregoing illustrative embodiments, and that the present invention may be embodied in other specific forms without departing from the spirit or essential characteristics thereof. The present embodiments are, therefore, to be considered in all respects as illustrative and not restrictive, the scope of the invention being indicated by the appended claims rather than by the foregoing description, and all changes which come within the meaning and range of equivalency of the claims are therefore intended to be embraced therein. Any reference sign in a claim should not be construed as limiting the claim concerned.
Claims (4)
1. The utility model provides a high efficiency apparatus for producing of broad spectrum plant source germicide, includes freezer (1), the lower extreme of freezer (1) is the toper structure, and crushing roller (6) are installed in the inside rotation of toper structure, evaporimeter (5) are installed to one side of freezer (1), its characterized in that:
The conveying device (8) is arranged below the freezer (1), a feeding pipe (7) is arranged between one side of the upper end of the conveying device (8) and the freezer (1), an electromagnetic valve is arranged at the middle position of the feeding pipe (7), a spiral conveying blade (9) is rotatably arranged in the conveying device (8), a first motor (10) is fixedly arranged at one end of the conveying device (8), an output shaft of the first motor (10) is in transmission connection with one end of the spiral conveying blade (9), a grinding wheel (28) is arranged at the other end of the spiral conveying blade (9), the grinding wheel (28) is of a round table structure, an inner gear ring (27) is arranged at the other end of the inner part of the conveying device (8), the grinding direction of the inner gear ring (27) is opposite to the grinding direction of the grinding teeth of the inner gear ring (28), and one end of the grinding wheel (28) extends to the inner part of the grinding ring (27);
The soaking box (2) is arranged at one end of the conveying device (8) far away from the freezer (1), the other side of the lower end of the conveying device (8) is connected with the soaking box (2) through a powder outlet pipe (11), an adjusting device (12) is arranged at the upper end of the soaking box (2), a rotary drum (29) is arranged at the lower end of the inside of the adjusting device (12), the rotary drum (29) is connected with the adjusting device (12) through a bearing, a first conical gear (30) is fixedly arranged at the upper end of the rotary drum (29), a second conical gear (31) is meshed at one side of the first conical gear (30), the shaft of the second conical gear (31) is rotationally connected with the adjusting device (12), a crank (15) is arranged at one end of the shaft of the second conical gear (31), the crank (15) is positioned outside the adjusting device (12), a threaded rod (13) is arranged at the center position of the rotary drum (29), the threaded rod (13) is connected with the internal thread of the rotary drum (29), a first conical gear (30) is fixedly arranged at the upper end of the rotary drum (29), a second conical gear (31) is meshed with the adjusting device (12), a limit pressing plate (14) is fixedly arranged at the two sides of the upper end of the rotary drum (13), the limit pressing plate (14) is fixedly connected with the limit pressing plate (14) and the limit pressing plate (14) is fixedly arranged at the two sides of the limit pressing device (12), the pressing plate (16) is positioned in the soaking box (2), a filter screen (17) is fixedly arranged at the lower end of the inside of the soaking box (2), an eluent adding port is further formed in one side of the soaking box (2), and an eluent adding port is further formed in one side of the soaking box (2);
The fractionating box (3) is arranged on one side of the soaking box (2), the fractionating box (3) is connected with the soaking box (2) through a conveying pipe (18), a pump (22) is arranged at the middle position of the conveying pipe (18), and a heating device (19) is arranged at the lower end of the inside of the fractionating box (3);
And the collecting box (4) is arranged on one side of the fractionating box (3), and a condensing pipe (20) is connected between the fractionating box (3) and the collecting box (4).
2. The high efficiency apparatus for producing a broad spectrum plant source germicide according to claim 1, wherein: the refrigerator is characterized in that a transmission mechanism (24) is fixedly arranged below the rear end of the refrigerator (1), two meshing gears (26) are arranged in the transmission mechanism (24), the meshing gears (26) are connected in a meshed mode, one end of the crushing roller (6) is fixed with the meshing gears (26), a second motor (25) is fixedly arranged on one side of the rear end of the transmission mechanism (24), and an output shaft of the second motor (25) is connected with one of the meshing gears (26) in a transmission mode through a coupling.
3. The high-efficiency production apparatus for broad-spectrum plant-source germicides according to claim 2, wherein: the outside winding of condenser pipe (20) has cooling tube (21), and cooling tube (21) both ends all communicate with freezer (1), cooling tube (21) externally mounted has fan (23), and cooling tube (21) sets up the isolation network with the intercommunication department of freezer (1).
4. A method for producing a high efficiency production apparatus based on the broad spectrum plant source bactericide according to claim 3, characterized in that: the method comprises the following steps:
firstly, placing plants to be extracted into a freezer (1), after a refrigerating mechanism operates, rapidly cooling the interior of the freezer (1) under the action of heat absorption of an evaporator, and after a set time is reached, making the plants in a frozen state;
Step two, starting a second motor (25) to enable the two crushing rollers (6) to rotate inwards, wherein frozen plants in the freezer (1) are crushed into a plurality of small blocks after contacting the crushing rollers (6), and then enter the conveying device (8) through the feed pipe (7);
Thirdly, a spiral conveying blade (9) in the conveying device (8) pushes blocky plants to move towards the other end, the spiral conveying blade (9) can drive a grinding wheel (28) to rotate in the rotating process, and when the blocky plants move to contact grinding teeth of the grinding inner gear ring (27) and the grinding wheel (28), the blocky plants are quickly subjected to grinding treatment, so that fine frozen plant powder is formed, and the plant powder enters the soaking box (2) through the powder outlet pipe (11);
Step four, adding methanol into the soaking box (2), and after the soaking time is reached, rotating a crank (15) by a user to enable a threaded rod (13) to vertically displace, so that a pressing plate (16) moves downwards, pressing plant soaking liquid downwards, extruding the plant soaking liquid, and enabling the liquid to quickly pass through a filter screen (17);
Step five, starting a pump (22), conveying extruded liquid into the fractionating box (3) through a conveying pipe (18), starting a heating device (19), distilling the liquid, storing distilled extracting solution in a collecting box (4), and quantitatively pumping out plant extracting solution in the collecting box (4) if different extracting solutions are required to be mixed for preparation.
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| CN213494106U (en) * | 2020-11-03 | 2021-06-22 | 中北大学 | Juice extraction element is used in plant processing |
| CN215609910U (en) * | 2021-06-29 | 2022-01-25 | 天津芸熙生物技术有限公司 | Plant extract separation and purification device |
| KR102438486B1 (en) * | 2022-01-12 | 2022-08-30 | 농업회사법인 주식회사 레인보우테크 | Device for processing and recycling organic waste such as discarded animals and plants |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN1596660A (en) * | 2003-09-19 | 2005-03-23 | 武长安 | Natural plant source bactericide and its preparation method |
| CN106719645A (en) * | 2016-09-19 | 2017-05-31 | 黑龙江省农业科学院植物脱毒苗木研究所 | It is a kind of to prevent and treat botanical fungicide of dry rot of potato and preparation method thereof |
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| CN110142999A (en) * | 2019-05-24 | 2019-08-20 | 山西得尔新能源汽车有限公司 | A kind of graphene composite material production vegetation water extract equipment and its extraction process |
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| CN215609910U (en) * | 2021-06-29 | 2022-01-25 | 天津芸熙生物技术有限公司 | Plant extract separation and purification device |
| KR102438486B1 (en) * | 2022-01-12 | 2022-08-30 | 농업회사법인 주식회사 레인보우테크 | Device for processing and recycling organic waste such as discarded animals and plants |
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| CN115301325A (en) | 2022-11-08 |
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