US20210178286A1 - Apparatus and Method for Separating Plant Trichomes Using a Double Vortex Turbulence - Google Patents
Apparatus and Method for Separating Plant Trichomes Using a Double Vortex Turbulence Download PDFInfo
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- US20210178286A1 US20210178286A1 US17/184,780 US202117184780A US2021178286A1 US 20210178286 A1 US20210178286 A1 US 20210178286A1 US 202117184780 A US202117184780 A US 202117184780A US 2021178286 A1 US2021178286 A1 US 2021178286A1
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- 238000000034 method Methods 0.000 title abstract description 14
- 239000007788 liquid Substances 0.000 claims abstract description 33
- 239000000463 material Substances 0.000 claims abstract description 21
- 238000001914 filtration Methods 0.000 claims abstract description 11
- 239000002028 Biomass Substances 0.000 claims description 9
- 230000002441 reversible effect Effects 0.000 claims description 8
- 239000000203 mixture Substances 0.000 claims 11
- 238000013019 agitation Methods 0.000 claims 6
- 238000001816 cooling Methods 0.000 claims 2
- 241000196324 Embryophyta Species 0.000 abstract description 32
- 239000011347 resin Substances 0.000 abstract description 32
- 229920005989 resin Polymers 0.000 abstract description 32
- 240000004308 marijuana Species 0.000 abstract description 3
- 230000002879 macerating effect Effects 0.000 abstract 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 11
- 239000000047 product Substances 0.000 description 10
- 238000009987 spinning Methods 0.000 description 4
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- 238000004140 cleaning Methods 0.000 description 3
- 239000000356 contaminant Substances 0.000 description 3
- 230000036571 hydration Effects 0.000 description 3
- 238000006703 hydration reaction Methods 0.000 description 3
- 238000000926 separation method Methods 0.000 description 3
- 238000011109 contamination Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000005096 rolling process Methods 0.000 description 2
- 238000007873 sieving Methods 0.000 description 2
- 229910001220 stainless steel Inorganic materials 0.000 description 2
- 239000010935 stainless steel Substances 0.000 description 2
- 244000025254 Cannabis sativa Species 0.000 description 1
- 235000012766 Cannabis sativa ssp. sativa var. sativa Nutrition 0.000 description 1
- 235000012765 Cannabis sativa ssp. sativa var. spontanea Nutrition 0.000 description 1
- 239000004866 Hashish Substances 0.000 description 1
- 239000006227 byproduct Substances 0.000 description 1
- 239000007795 chemical reaction product Substances 0.000 description 1
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- 239000002904 solvent Substances 0.000 description 1
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Images
Classifications
-
- 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
- B01D11/0215—Solid material in other stationary receptacles
- B01D11/0253—Fluidised bed of solid materials
- B01D11/0257—Fluidised bed of solid materials using mixing mechanisms, e.g. stirrers, jets
Definitions
- the present invention relates generally to separating sticky particulate from plant material. More specifically, the present invention relates to separating resin heads from cannabis plants.
- Hashish is a consumable compress of purified psychoactive resin from the glandular trichomes of the cannabis plant.
- the trichomes are found on the flowers, and to a lesser extent, in the stems and leaves of the plant.
- Methods such as flat screening or dry sieving require practice and skill, are inefficient, and often result in a lower quality product that contains broken leaf-matter contaminants.
- Use of chemical solvents can alter the resin and produce unwanted by-products.
- Machines such as that disclosed by Raichart in U.S. Pat. No. 9,050,631, which tumble the plant flowers and collect the sticky trichomes on sieving screens, although inexpensive, are also inefficient, and are difficult to clean and reuse.
- An example of an ice and agitator method is the cold water cleaning process and machine disclosed by Reinhard in U.S. Pat. No. 6,158,591.
- This machine uses an agitator similar to an electric mixer that macerates the leaves of the plant, damaging them before the resin can be removed.
- the machine requires the use of ice to keep the water as cold as possible, but the ice also damages the plant material, resulting in inefficiencies in the process.
- the machine also contains internal screens which are easily blocked by sticky resin and plant biomass, making them ineffective and preventing effective flow of liquid through the machine.
- the present invention addresses these issues by combining a low temperature process with a double vortex pattern of liquid flow to gently remove the resin heads from the botanical material.
- the double vortex flow is created through a uniquely shaped basin in combination with a user controlled rotator plate.
- the double vortex flow results in a gentle, yet powerful, turbulence.
- the rolling effect of this turbulence gently removes the cold-water hardened trichome heads from their stalks, yielding a much cleaner and desirable end product.
- a subsequent filtration process is used to separate the resin containing trichome heads from the liquid.
- the filtration system uses a series of different sized filters to separate elements of the plant's biomass contaminants from the trichome heads. The result is a maximum separation of the resin containing trichome heads from the plant surface with negligent to non-existent contamination.
- the present invention is a method and apparatus that separates trichome heads from plants using a double vortex liquid flow to separate the trichomes from the leaves, flowers, and stems.
- the plant parts are placed with very cold liquid in a jacketed basin which contains a rotator plate near the bottom.
- the shape of the basin is circular on the front half, and a rounded square on the back half.
- the plant biomass is soaked in this cold liquid bath until fully hydrated, such that all plant components are completely softened and any flowers begin to open.
- the user starts the rotator plate spinning, creating a central vortex.
- the outer edge of the liquid flow rolls off the back side of the rounded square portion of the basin and rolls over the mid-section of the liquid flow, creating a powerful, rolling turbulence in a second vortex.
- the direction of rotation of the rotator plate is reversed, causing more gentle turbulence as the liquid flow reverses direction.
- the rotator plate is again reversed to repeat the process. Each time the rotator plate direction is reversed, the velocity is increased to increase the power of the turbulence.
- the liquid and separated plant biomass and trichome head resin material are evacuated from the basin through a Venturi style drain which creates a powerful flow of liquid toward the external filtration system. That powerful flow is necessary to ensure the separated plant biomass and sticky trichome head resin material do not get trapped in the drain.
- the filtration system employs a series of different sized external filters to separate elements of used plant biomass, trichome head resin material, and contaminants.
- the first filter is designed to capture plant components that have passed through the drain and are not fully cleaned of resin. The plant components captured in this first filter may be removed and returned to the basin for further resin separation.
- the second filter catches the smallest botanical particles while allowing the resin components to pass through. Some resin particulate may remain with the plant material on the second filter and it may be removed and rinsed with high pressure water spray to capture more of the resin product.
- the final filter is designed to capture the resin product which is then removed from the filter for further processing.
- FIG. 1 is a perspective view of the exterior of the Double Vortex Machine showing the exterior of the Basin on a Cart, the Outflow Pipe and Valve, and the Multi-Tiered Filter Assembly.
- FIG. 2 is a view of the top of the Double Vortex Machine without a Cover or a Cart and showing the interior shape, the Rotator Plate and the location of the Venturi drain.
- FIG. 3 is a cross section of the Double Vortex Machine showing the Jacketing, a possible shape of the Rotator Plate, the location of the Motor and the Multi-Tiered Filter Assembly showing three Filters.
- FIG. 4 is a schematic showing the liquid flows in the First and Second vortexes when the Rotator Plate is spinning in the clockwise direction.
- the apparatus of the present invention is a Double Vortex Machine 101 and a Multi-Tiered Filter Assembly 102 , used in conjunction with a liquid source.
- FIG. 1 shows one possible embodiment of the invention as installed conveniently on an optional Cart 107 .
- the liquid is preferably water, and the source may be a food-grade water hose with a high pressure spray nozzle attached.
- the Double Vortex Machine 101 may also be hard plumbed to a water or other liquid source.
- the Double Vortex Machine 101 has a uniquely shaped Basin 104 , a Rotator Plate 201 , a Motor 302 , a Control Unit 103 , a Venturi Drain 202 , and an Outflow Pipe Assembly 105 .
- the Multi-Tiered Filter Assembly 102 is attached to the Outflow Pipe Assembly 105 and includes a series of removable Filters 305 , 306 , and 307 . The attributes of each element of the assembly are described throughout the following description of the extraction process.
- the process begins with hydration of the plant product in the Basin 104 of the Double Vortex Machine 101 .
- the Basin 104 is shaped such that the front half is a semi-circle and the back half is a rounded square.
- the distance from the center of the semi-circle to the flat portion of the rounded square is preferably equal to, or just slightly larger, than the radius of the semi-circle.
- the Basin 104 is preferably made of stainless steel to prevent the resin from sticking to the surface and to facilitate cleaning, but it may be made of any other suitable material.
- the Basin 104 is also preferably jacketed as shown in FIG. 3 , and may have a Cover 106 as shown in FIGS. 1 and 3 , to help maintain the liquid temperature at close to freezing.
- a Venturi Drain 202 located in the bottom of the Basin 104 , is connected to the Outflow Pipe Assembly 105 which includes a Valve 303 .
- the Valve 303 is preferably manually operated, but may also be electrically connected to, and controlled by, the Control Unit 103 .
- the Basin 104 With the Valve 303 in the closed position, the Basin 104 is filled approximately two thirds full with very cold liquid, preferably water. If a cold liquid source is not available, the temperature of the liquid may be reduced to near zero degrees Celsius via the introduction of coolant to the Jacketed Portion 304 of the Basin 104 , if the Basin 104 is jacketed.
- the plant product is placed in the Basin 104 with the very cold liquid and is soaked in this bath until all elements are fully hydrated and any flowers begin to open.
- the Rotator Plate 201 located at the geometric center of the Basin 104 , is positioned slightly above the bottom of the Basin 104 such that there is sufficient clearance beneath the Rotator Plate 201 to ensure plant material does not become trapped underneath.
- the shape of the Rotator Plate 201 is preferably fairly flat with several ribs of sufficient height to move the liquid into a First Vortex 401 when it is rotated, as shown by the arrows in FIG. 4 .
- the Rotator Plate 201 is preferably made of stainless steel, but may be made of any suitable material.
- the Rotator Plate 201 is connected mechanically to a Motor 302 which is connected electrically to the Control Unit 103 .
- the Motor 302 has variable speed capability, preferably from 300 to 1700 rpm, which may be adjusted by the user through the Control Unit 103 .
- the Control Unit 103 is preferably designed to automatically reverse the Motor 302 direction at intervals based on the adjusted speed, but this reversal may also be done manually by the user.
- the Motor 302 and Control Unit 103 components are all readily available catalogue items, and no particular model(s) or specifications are indicated.
- the user After hydration of the plant product is complete, the user starts the Rotator Plate 201 spinning using the Control Unit 103 .
- the spinning of the Rotator Plate creates a First Vortex 401 in the Basin 104 .
- the outer edge of the liquid flow rolls off the back side of the rounded square portion of the Basin 104 and rolls over the mid-section of the liquid flow, creating a Second Vortex 402 as shown in FIG. 4 .
- the direction of rotation of the Rotator Plate 201 is reversed, either automatically through design of the Control Unit 103 , or manually by the user.
- the reversal action creates more turbulence as the liquid flow reverses direction.
- double vortexes are created in the opposite direction, and the user, or the Control Unit 103 , reverses the Rotator Plate 201 direction again to repeat the process.
- the velocity is preferably increased to increase the power of the turbulence.
- the increase in velocity is preferably manually adjusted by the user, but it may also be automated in the Control Unit 103 .
- the Valve 303 in the Outflow Pipe Assembly 105 is opened and the liquid, processed plant biomass and separated trichome heads containing the resin flow through the Venturi Drain 202 to the Multi-Tiered Filter Assembly 102 .
- the Valve 303 is preferably manually operated, but may also be an electronically controlled and operated valve, such as a solenoid. If an electronically controlled valve is used, it would preferably be electrically connected to, and operated by, the Control Unit 103 .
- the Multi-Tiered Filter Assembly 102 contains at least two, and preferably three, removable Filters 305 , 306 , and 307 .
- the First Filter 305 preferably with a mesh size of approximately 190 microns, is sized to capture plant components that have passed through the drain and are not fully cleaned of resin. The plant components captured in this First Filter 305 may be removed and returned to the basin for further resin separation.
- the Multi-Tiered Filter Assembly 102 preferable contains a Middle Filter 306 with a mesh size of approximately 160 microns that will capture both trichome heads containing resin material and plant biomass of a similar size.
- Some resin particulate may remain with the plant material on the Middle Filter 306 , and it may be removed and rinsed with high pressure water spray to capture more of the resin product.
- the Final Filter 307 preferably with a mesh size of approximately 45 microns, captures the resin product.
- the Final Filter 307 is removed and the resin is cleaned from it to be prepared for further processing.
- the Multi-Tiered Filter Assembly 102 could contain several additional intermediate filters to facilitate the filtering process.
- the cleaning of the filters could also be automated by including space and controls for high pressure liquid sprays between each of the filters.
- water is specified herein as preferable, any suitable liquid could be used as the medium for the plant material.
- the specific embodiments described herein are offered by way of example only. The embodiments were chosen and described in order to best explain the principles of the invention and its practiced applications.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Filtration Of Liquid (AREA)
Abstract
A method and apparatus for separating trichome heads containing resin from cannabis plants using a double vortex liquid flow to remove the trichome heads without macerating the plant material and a multi-tiered filtration process to isolate the resin product.
Description
- Not Applicable.
- Not Applicable.
- Not Applicable.
- The present invention relates generally to separating sticky particulate from plant material. More specifically, the present invention relates to separating resin heads from cannabis plants.
- Hashish is a consumable compress of purified psychoactive resin from the glandular trichomes of the cannabis plant. The trichomes are found on the flowers, and to a lesser extent, in the stems and leaves of the plant. Historically, separating the trichomes from the plant has been very difficult as the resin within the trichomes is quite sticky. Methods such as flat screening or dry sieving require practice and skill, are inefficient, and often result in a lower quality product that contains broken leaf-matter contaminants. Use of chemical solvents can alter the resin and produce unwanted by-products. Machines, such as that disclosed by Raichart in U.S. Pat. No. 9,050,631, which tumble the plant flowers and collect the sticky trichomes on sieving screens, although inexpensive, are also inefficient, and are difficult to clean and reuse.
- Some success has been found with a process using ice, water, and a mechanical agitator. The ice reduces the stickiness of the resin in the trichome heads, and the mechanical agitator forces the trichome heads to break away from their stalks and botanical material. In addition, the use of ice and mechanical agitators on the botanical material creates plant particulate contamination in the final resin product, creating an inferior product and harsh flavors.
- An example of an ice and agitator method is the cold water cleaning process and machine disclosed by Reinhard in U.S. Pat. No. 6,158,591. This machine uses an agitator similar to an electric mixer that macerates the leaves of the plant, damaging them before the resin can be removed. The machine requires the use of ice to keep the water as cold as possible, but the ice also damages the plant material, resulting in inefficiencies in the process. The machine also contains internal screens which are easily blocked by sticky resin and plant biomass, making them ineffective and preventing effective flow of liquid through the machine.
- The present invention addresses these issues by combining a low temperature process with a double vortex pattern of liquid flow to gently remove the resin heads from the botanical material. The double vortex flow is created through a uniquely shaped basin in combination with a user controlled rotator plate. The double vortex flow results in a gentle, yet powerful, turbulence. The rolling effect of this turbulence gently removes the cold-water hardened trichome heads from their stalks, yielding a much cleaner and desirable end product. A subsequent filtration process is used to separate the resin containing trichome heads from the liquid. The filtration system uses a series of different sized filters to separate elements of the plant's biomass contaminants from the trichome heads. The result is a maximum separation of the resin containing trichome heads from the plant surface with negligent to non-existent contamination.
- The present invention is a method and apparatus that separates trichome heads from plants using a double vortex liquid flow to separate the trichomes from the leaves, flowers, and stems. The plant parts are placed with very cold liquid in a jacketed basin which contains a rotator plate near the bottom. The shape of the basin is circular on the front half, and a rounded square on the back half. The plant biomass is soaked in this cold liquid bath until fully hydrated, such that all plant components are completely softened and any flowers begin to open.
- Following hydration, the user starts the rotator plate spinning, creating a central vortex. As the liquid swirls and picks up speed, the outer edge of the liquid flow rolls off the back side of the rounded square portion of the basin and rolls over the mid-section of the liquid flow, creating a powerful, rolling turbulence in a second vortex. After establishing this second vortex, the direction of rotation of the rotator plate is reversed, causing more gentle turbulence as the liquid flow reverses direction. When the double vortexes are created in the opposite direction, the rotator plate is again reversed to repeat the process. Each time the rotator plate direction is reversed, the velocity is increased to increase the power of the turbulence.
- The liquid and separated plant biomass and trichome head resin material are evacuated from the basin through a Venturi style drain which creates a powerful flow of liquid toward the external filtration system. That powerful flow is necessary to ensure the separated plant biomass and sticky trichome head resin material do not get trapped in the drain.
- The filtration system employs a series of different sized external filters to separate elements of used plant biomass, trichome head resin material, and contaminants. The first filter is designed to capture plant components that have passed through the drain and are not fully cleaned of resin. The plant components captured in this first filter may be removed and returned to the basin for further resin separation. The second filter catches the smallest botanical particles while allowing the resin components to pass through. Some resin particulate may remain with the plant material on the second filter and it may be removed and rinsed with high pressure water spray to capture more of the resin product. The final filter is designed to capture the resin product which is then removed from the filter for further processing.
- A more complete understanding of the present invention may be derived by referring to the detailed description and claims when considered in connection with the figures, wherein like reference numbers refer to similar items throughout the figures and:
-
FIG. 1 is a perspective view of the exterior of the Double Vortex Machine showing the exterior of the Basin on a Cart, the Outflow Pipe and Valve, and the Multi-Tiered Filter Assembly. -
FIG. 2 is a view of the top of the Double Vortex Machine without a Cover or a Cart and showing the interior shape, the Rotator Plate and the location of the Venturi drain. -
FIG. 3 is a cross section of the Double Vortex Machine showing the Jacketing, a possible shape of the Rotator Plate, the location of the Motor and the Multi-Tiered Filter Assembly showing three Filters. -
FIG. 4 is a schematic showing the liquid flows in the First and Second vortexes when the Rotator Plate is spinning in the clockwise direction. - In the following detailed description of the invention, reference is made to the accompanying drawings which form a part of the disclosure and, which show by way of illustration, and not of limitation, specific embodiments by which the invention may be practiced. The drawings, the foregoing discussion, and the following description are exemplary and explanatory only, and are not intended to limit the scope of the invention or its application in any manner.
- The apparatus of the present invention is a Double Vortex
Machine 101 and aMulti-Tiered Filter Assembly 102, used in conjunction with a liquid source.FIG. 1 shows one possible embodiment of the invention as installed conveniently on anoptional Cart 107. The liquid is preferably water, and the source may be a food-grade water hose with a high pressure spray nozzle attached. In another embodiment, theDouble Vortex Machine 101 may also be hard plumbed to a water or other liquid source. TheDouble Vortex Machine 101 has a uniquely shapedBasin 104, aRotator Plate 201, aMotor 302, aControl Unit 103, aVenturi Drain 202, and anOutflow Pipe Assembly 105. TheMulti-Tiered Filter Assembly 102 is attached to theOutflow Pipe Assembly 105 and includes a series of 305, 306, and 307. The attributes of each element of the assembly are described throughout the following description of the extraction process.removable Filters - The process begins with hydration of the plant product in the
Basin 104 of theDouble Vortex Machine 101. As shown inFIG. 2 , theBasin 104 is shaped such that the front half is a semi-circle and the back half is a rounded square. The distance from the center of the semi-circle to the flat portion of the rounded square is preferably equal to, or just slightly larger, than the radius of the semi-circle. TheBasin 104 is preferably made of stainless steel to prevent the resin from sticking to the surface and to facilitate cleaning, but it may be made of any other suitable material. TheBasin 104 is also preferably jacketed as shown inFIG. 3 , and may have aCover 106 as shown inFIGS. 1 and 3 , to help maintain the liquid temperature at close to freezing. - A
Venturi Drain 202, located in the bottom of theBasin 104, is connected to theOutflow Pipe Assembly 105 which includes aValve 303. TheValve 303 is preferably manually operated, but may also be electrically connected to, and controlled by, theControl Unit 103. With theValve 303 in the closed position, theBasin 104 is filled approximately two thirds full with very cold liquid, preferably water. If a cold liquid source is not available, the temperature of the liquid may be reduced to near zero degrees Celsius via the introduction of coolant to theJacketed Portion 304 of theBasin 104, if theBasin 104 is jacketed. The plant product is placed in theBasin 104 with the very cold liquid and is soaked in this bath until all elements are fully hydrated and any flowers begin to open. - The
Rotator Plate 201, located at the geometric center of theBasin 104, is positioned slightly above the bottom of theBasin 104 such that there is sufficient clearance beneath theRotator Plate 201 to ensure plant material does not become trapped underneath. The shape of theRotator Plate 201 is preferably fairly flat with several ribs of sufficient height to move the liquid into aFirst Vortex 401 when it is rotated, as shown by the arrows inFIG. 4 . TheRotator Plate 201 is preferably made of stainless steel, but may be made of any suitable material. TheRotator Plate 201 is connected mechanically to aMotor 302 which is connected electrically to theControl Unit 103. TheMotor 302 has variable speed capability, preferably from 300 to 1700 rpm, which may be adjusted by the user through theControl Unit 103. TheControl Unit 103 is preferably designed to automatically reverse theMotor 302 direction at intervals based on the adjusted speed, but this reversal may also be done manually by the user. TheMotor 302 andControl Unit 103 components are all readily available catalogue items, and no particular model(s) or specifications are indicated. - After hydration of the plant product is complete, the user starts the
Rotator Plate 201 spinning using theControl Unit 103. The spinning of the Rotator Plate creates aFirst Vortex 401 in theBasin 104. As the liquid swirls and picks up speed, the outer edge of the liquid flow rolls off the back side of the rounded square portion of theBasin 104 and rolls over the mid-section of the liquid flow, creating aSecond Vortex 402 as shown inFIG. 4 . After establishing thisSecond Vortex 402, the direction of rotation of theRotator Plate 201 is reversed, either automatically through design of theControl Unit 103, or manually by the user. The reversal action creates more turbulence as the liquid flow reverses direction. Ultimately, double vortexes are created in the opposite direction, and the user, or theControl Unit 103, reverses theRotator Plate 201 direction again to repeat the process. - Each time the
Rotator Plate 201 direction is reversed, the velocity is preferably increased to increase the power of the turbulence. The increase in velocity is preferably manually adjusted by the user, but it may also be automated in theControl Unit 103. - After a sufficient amount of trichome heads containing resin have been separated from the plant material, the
Rotator Plate 201 rotation is stopped and the filtering portion of the process is started. TheValve 303 in theOutflow Pipe Assembly 105 is opened and the liquid, processed plant biomass and separated trichome heads containing the resin flow through theVenturi Drain 202 to theMulti-Tiered Filter Assembly 102. TheValve 303 is preferably manually operated, but may also be an electronically controlled and operated valve, such as a solenoid. If an electronically controlled valve is used, it would preferably be electrically connected to, and operated by, theControl Unit 103. - The
Multi-Tiered Filter Assembly 102 contains at least two, and preferably three, 305, 306, and 307. Theremovable Filters First Filter 305, preferably with a mesh size of approximately 190 microns, is sized to capture plant components that have passed through the drain and are not fully cleaned of resin. The plant components captured in thisFirst Filter 305 may be removed and returned to the basin for further resin separation. TheMulti-Tiered Filter Assembly 102 preferable contains aMiddle Filter 306 with a mesh size of approximately 160 microns that will capture both trichome heads containing resin material and plant biomass of a similar size. Some resin particulate may remain with the plant material on theMiddle Filter 306, and it may be removed and rinsed with high pressure water spray to capture more of the resin product. TheFinal Filter 307, preferably with a mesh size of approximately 45 microns, captures the resin product. TheFinal Filter 307 is removed and the resin is cleaned from it to be prepared for further processing. - Many modifications and variations of this invention may be made without departing from its spirit and scope, as will be appreciated by those skilled in the art. For example, the
Multi-Tiered Filter Assembly 102 could contain several additional intermediate filters to facilitate the filtering process. The cleaning of the filters could also be automated by including space and controls for high pressure liquid sprays between each of the filters. Also, although water is specified herein as preferable, any suitable liquid could be used as the medium for the plant material. The specific embodiments described herein are offered by way of example only. The embodiments were chosen and described in order to best explain the principles of the invention and its practiced applications.
Claims (21)
1.-4. (canceled)
5. An apparatus for separating plant material from plants, the apparatus comprising:
a basin comprising a bottom, a semi-cylindrical front portion and a rounded box back portion comprising two rounded corners extending in a vertical direction;
a rotator plate located inside and exclusively adjacent the bottom of the basin, the rotator plate having an axis of rotation that is vertical; and
a reversible motor coupled to the rotator plate, such that when the basin contains a mixture of liquid and plant material and the motor rotates the flat rotator plate, a double agitation is configured to form in the mixture comprising a first vortex of the mixture about the axis, and a second agitation of the mixture adjacent to a first one of the two rounded corners of the basin.
6. The apparatus of claim 5 , further comprising a drain in the bottom coupled to a filtering system such that, when a valve is opened and the liquid is drained from the basin, processed plant biomass is captured in the filtering system.
7. The apparatus of claim 6 , wherein the filtering system comprises a valve and removable filters in series.
8. The apparatus of claim 6 wherein the basin comprises a cooling jacket and a cover to regulate a temperature of the mixture.
9. The apparatus of claim 6 , further comprising a cart that is portable on wheels, the basin is mounted to the cart, the motor is coupled vertically below the basin.
10. The apparatus of claim 9 , wherein the filtering system extends out of and is located on a side of the cart below the basin.
11. The apparatus of claim 5 , wherein the rotator plate comprises a top surface having ribs extending vertically therefrom.
12. The apparatus of claim 11 , wherein tops of the ribs on the rotator plate are rounded.
13. The apparatus of claim 11 , wherein tops of the ribs are located vertically below a cooling jacket.
14. The apparatus of claim 5 , wherein the bottom is flat and the rotator plate is flat.
15. The apparatus of claim 5 wherein, relative to the axis, a radial distance from a center of the semi-cylindrical front portion to a flat wall of the rounded box back portion is equal to or greater than a radius of the semi-cylindrical front portion.
16. The apparatus of claim 5 , wherein the basin comprises a D-shaped tub when viewed from above.
17. The apparatus of claim 5 , further comprising a control panel configured to automatically control the apparatus and reverse a rotational direction of the rotator plate at selected intervals.
18. The apparatus of claim 5 , wherein, when the rotator plate reverses rotational direction, the second agitation of the mixture is configured to move and form adjacent to a second one of the two rounded corners of the basin.
19. The apparatus of claim 5 , wherein the control panel is configured to automatically increase a speed of the reversible motor during operation.
20. The apparatus of claim 19 , wherein the speed is in a range of 300 rpm to 1700 rpm.
21. An apparatus for separating plant material from plants, the apparatus comprising:
a basin comprising a bottom, a semi-cylindrical front portion and a rounded box back portion comprising two rounded corners extending in a vertical direction;
a rotator plate located inside the basin, the rotator plate having an axis of rotation that is vertical;
a reversible motor coupled to the rotator plate, such that when the basin contains a mixture of liquid and plant material and the motor rotates the flat rotator plate, a double agitation is configured to form in the mixture comprising a first vortex of the mixture about the axis, and a second agitation of the mixture adjacent to a first one of the two rounded corners of the basin; and
when the rotator plate reverses rotational direction, the second agitation of the mixture is configured to move and form adjacent to a second one of the two rounded corners of the basin.
22. The apparatus of claim 21 wherein, relative to the axis, a radial distance from a center of the semi-cylindrical front portion to a flat wall of the rounded box back portion is equal to or greater than a radius of the semi-cylindrical front portion.
23. The apparatus of claim 21 , further comprising a control panel configured to automatically control the apparatus and reverse a rotational direction of the rotator plate at selected intervals.
24. The apparatus of claim 21 , wherein the control panel is configured to automatically increase a speed of the reversible motor during operation.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US17/184,780 US20210178286A1 (en) | 2017-08-18 | 2021-02-25 | Apparatus and Method for Separating Plant Trichomes Using a Double Vortex Turbulence |
Applications Claiming Priority (3)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| US201762547600P | 2017-08-18 | 2017-08-18 | |
| US16/103,972 US10933347B2 (en) | 2017-08-18 | 2018-08-16 | Apparatus and method for separating plant trichomes using a double vortex turbulence |
| US17/184,780 US20210178286A1 (en) | 2017-08-18 | 2021-02-25 | Apparatus and Method for Separating Plant Trichomes Using a Double Vortex Turbulence |
Related Parent Applications (1)
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| US16/103,972 Continuation US10933347B2 (en) | 2017-08-18 | 2018-08-16 | Apparatus and method for separating plant trichomes using a double vortex turbulence |
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| US16/881,422 Active 2038-11-09 US10933348B2 (en) | 2017-08-18 | 2020-05-22 | Apparatus and method for separating plant trichomes using a double vortex turbulence |
| US17/184,019 Abandoned US20210178285A1 (en) | 2017-08-18 | 2021-02-24 | Apparatus and Method for Separating Plant Trichomes Using a Double Vortex Turbulence |
| US17/184,780 Abandoned US20210178286A1 (en) | 2017-08-18 | 2021-02-25 | Apparatus and Method for Separating Plant Trichomes Using a Double Vortex Turbulence |
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| US16/881,422 Active 2038-11-09 US10933348B2 (en) | 2017-08-18 | 2020-05-22 | Apparatus and method for separating plant trichomes using a double vortex turbulence |
| US17/184,019 Abandoned US20210178285A1 (en) | 2017-08-18 | 2021-02-24 | Apparatus and Method for Separating Plant Trichomes Using a Double Vortex Turbulence |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| US12036485B1 (en) * | 2019-07-16 | 2024-07-16 | Green Vault Systems, LLC | Continuous flow cold water extraction |
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| Publication number | Priority date | Publication date | Assignee | Title |
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| US10933347B2 (en) * | 2017-08-18 | 2021-03-02 | Delta Separations, Llc | Apparatus and method for separating plant trichomes using a double vortex turbulence |
| US11167225B2 (en) * | 2019-01-18 | 2021-11-09 | Spiral Water Technologies, Inc. | Plant trichome filtration and concentration |
| US11931669B2 (en) * | 2020-05-14 | 2024-03-19 | John C. Digertt, Inc. | Cannabis extraction system and method |
Citations (2)
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|---|---|---|---|---|
| US6158591A (en) * | 1998-02-24 | 2000-12-12 | Delp; Reinhard C. | Method and apparatus for extracting plant resins |
| CN205340617U (en) * | 2015-11-26 | 2016-06-29 | 东至县鑫农菌业有限公司 | Stirring device |
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| LU82145A1 (en) * | 1980-02-07 | 1981-09-10 | Cipari | IMPROVEMENTS IN PROCESSES AND PLANTS USING YEAST |
| US9050631B2 (en) | 2013-02-06 | 2015-06-09 | Cullen Raichart | Apparatus and related methods for extracting resins from cannabis |
| CN104745472B (en) * | 2015-04-14 | 2017-09-19 | 长春工程学院 | A plant tissue culture tank |
| US10933347B2 (en) * | 2017-08-18 | 2021-03-02 | Delta Separations, Llc | Apparatus and method for separating plant trichomes using a double vortex turbulence |
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2018
- 2018-08-16 US US16/103,972 patent/US10933347B2/en active Active
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- 2020-05-22 US US16/881,422 patent/US10933348B2/en active Active
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- 2021-02-25 US US17/184,780 patent/US20210178286A1/en not_active Abandoned
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US6158591A (en) * | 1998-02-24 | 2000-12-12 | Delp; Reinhard C. | Method and apparatus for extracting plant resins |
| CN205340617U (en) * | 2015-11-26 | 2016-06-29 | 东至县鑫农菌业有限公司 | Stirring device |
Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US12036485B1 (en) * | 2019-07-16 | 2024-07-16 | Green Vault Systems, LLC | Continuous flow cold water extraction |
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| US10933347B2 (en) | 2021-03-02 |
| US20200282328A1 (en) | 2020-09-10 |
| US10933348B2 (en) | 2021-03-02 |
| US20190054393A1 (en) | 2019-02-21 |
| US20210178285A1 (en) | 2021-06-17 |
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