Nextleaf Solutions Ltd.

Canada

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        Patent 30
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        United States 17
        Canada 13
        World 7
        Europe 1
Date
2021 8
Before 2021 30
IPC Class
B01D 11/02 - Solvent extraction of solids 11
C07D 311/80 - DibenzopyransHydrogenated dibenzopyrans 10
A61K 36/185 - Magnoliopsida (dicotyledons) 9
A61K 31/352 - Heterocyclic compounds having oxygen as the only ring hetero atom, e.g. fungichromin having six-membered rings with one oxygen as the only ring hetero atom condensed with carbocyclic rings, e.g. cannabinols, methantheline 8
A23L 33/105 - Plant extracts, their artificial duplicates or their derivatives 5
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NICE Class
40 - Treatment of materials; recycling, air and water treatment, 6
31 - Agricultural products; live animals 4
45 - Legal and security services; personal services for individuals. 4
22 - Rope, netting, tents, awnings, sails and sacks; padding and stuffing materials 2
34 - Tobacco; smokers' articles 2

1.

GLACIAL GOLD

      
Application Number 214259500
Status Registered
Filing Date 2021-10-25
Registration Date 2023-08-02
Owner Nextleaf Solutions Ltd. (Canada)
NICE Classes  ? 34 - Tobacco; smokers' articles

Goods & Services

(1) Cannabis distillate

2.

Skid, frame, and vessel set

      
Application Number 29717294
Grant Number D0923069
Status In Force
Filing Date 2020-01-09
First Publication Date 2021-06-22
Grant Date 2021-06-22
Owner Nextleaf Solutions Ltd. (Canada)
Inventor
  • Pal, Krupal
  • Ko, Ryan Delmoral
  • Kopic, Peter
  • Parker, Ian

3.

Skid and frame set

      
Application Number 29715196
Grant Number D0922457
Status In Force
Filing Date 2019-11-28
First Publication Date 2021-06-15
Grant Date 2021-06-15
Owner Nextleaf Solutions Ltd. (Canada)
Inventor
  • Pal, Krupal
  • Ko, Ryan Delmoral
  • Kopic, Peter
  • Parker, Ian

4.

Treatment of spent cannabis biomass

      
Application Number 16705842
Grant Number 11292722
Status In Force
Filing Date 2019-12-06
First Publication Date 2021-06-10
Grant Date 2022-04-05
Owner Nextleaf Solutions Ltd. (Canada)
Inventor
  • Novitski, David Michael
  • Jia, Xuan

Abstract

2 and/or water vapor treatment in order to obtain activated carbon with a desired porosity level.

IPC Classes  ?

  • C01B 32/324 - Preparation characterised by the starting materials from waste materials, e.g. tyres or spent sulfite pulp liquor
  • B01J 20/20 - Solid sorbent compositions or filter aid compositionsSorbents for chromatographyProcesses for preparing, regenerating or reactivating thereof comprising inorganic material comprising free carbonSolid sorbent compositions or filter aid compositionsSorbents for chromatographyProcesses for preparing, regenerating or reactivating thereof comprising inorganic material comprising carbon obtained by carbonising processes
  • C01B 32/336 - Preparation characterised by gaseous activating agents
  • C07D 311/78 - Ring systems having three or more relevant rings

5.

Treatment of spent cannabis biomass with activating agent

      
Application Number 16706666
Grant Number 11440801
Status In Force
Filing Date 2019-12-06
First Publication Date 2021-06-10
Grant Date 2022-09-13
Owner Nextleaf Solutions Ltd. (Canada)
Inventor
  • Jia, Xuan
  • Novitski, David Michael

Abstract

cannabis biomass is heated in stages, the first to remove water and volatile components, and the second to reclaim leftover cannabinoids. During a third, higher temperature stage, the biomass is converted to activated carbon.

IPC Classes  ?

6.

GLACIER GOLD

      
Application Number 211078700
Status Registered
Filing Date 2021-05-31
Registration Date 2023-08-02
Owner Nextleaf Solutions Ltd. (Canada)
NICE Classes  ? 34 - Tobacco; smokers' articles

Goods & Services

(1) Cannabis distillate

7.

Acetylation of cannabinoids using sulfuric acid catalyst

      
Application Number 16571146
Grant Number 10954209
Status In Force
Filing Date 2019-09-15
First Publication Date 2021-03-18
Grant Date 2021-03-23
Owner Nextleaf Solutions Ltd. (Canada)
Inventor Novitski, David

Abstract

Cannabis oil reacts with acetic anhydride with hexane and under reflux to produce THC-O-acetate and acetic acid using sulfuric acid as a catalyst. The resulting crude product is distilled and subjected to a SALLE with hexane followed by a SALLE with petroleum ether, before being distilled again in order to obtain a refined, THC-O-acetate product.

IPC Classes  ?

  • C07D 311/80 - DibenzopyransHydrogenated dibenzopyrans
  • B01D 3/14 - Fractional distillation
  • B01D 11/04 - Solvent extraction of solutions which are liquid

8.

ACETYLATION OF CANNABINOIDS USING SULFURIC ACID CATALYST

      
Application Number CA2019051482
Publication Number 2021/046630
Status In Force
Filing Date 2019-10-18
Publication Date 2021-03-18
Owner NEXTLEAF SOLUTIONS LTD (Canada)
Inventor Novitski, David

Abstract

A process for producing THC-O-acetate using a succession of distillation, salting-out assisted liquid-liquid extractions (SALLEs), and solvent recovery techniques. Tetrahydrocannabinol (THC) in cannabis oil dissolved in hexane reacts with acetic anhydride under reflux to produce THC-O-acetate and acetic acid using sulfuric acid as a catalyst. The resulting crude product is subjected to a SALLE with hexane followed by a SALLE with petroleum ether, before being distilled in order to obtain a refined, THC-O-acetate product.

IPC Classes  ?

  • C07D 311/80 - DibenzopyransHydrogenated dibenzopyrans
  • A61K 31/352 - Heterocyclic compounds having oxygen as the only ring hetero atom, e.g. fungichromin having six-membered rings with one oxygen as the only ring hetero atom condensed with carbocyclic rings, e.g. cannabinols, methantheline
  • C07B 41/12 - Formation or introduction of functional groups containing oxygen of carboxylic acid ester groups

9.

Acetylation of cannabigerol

      
Application Number 17013268
Grant Number 11097204
Status In Force
Filing Date 2020-09-04
First Publication Date 2020-12-24
Grant Date 2021-08-24
Owner Nextleaf Solutions Ltd. (Canada)
Inventor
  • Pal, Krupal Devendra
  • Ko, Ryan Delmoral
  • Hughes, Brock Aston
  • Casselman, Ivan Jason

Abstract

cannabis oil reacts with acetic anhydride under reflux to produce THC-O-acetate and acetic acid. The resulting crude product is distilled and subjected to a SALLE with hexane followed by a SALLE with petroleum ether, before being distilled again in order to obtain a refined, THC-O-acetate product.

IPC Classes  ?

  • B01D 3/14 - Fractional distillation
  • C07D 311/82 - Xanthenes
  • B01D 5/00 - Condensation of vapoursRecovering volatile solvents by condensation
  • B01D 3/10 - Vacuum distillation
  • B01D 1/22 - Evaporating by bringing a thin layer of the liquid into contact with a heated surface
  • B01D 11/04 - Solvent extraction of solutions which are liquid

10.

Ultrasonic cannabinoid extraction using non-flammable co-solvent

      
Application Number 16716197
Grant Number 10851038
Status In Force
Filing Date 2019-12-16
First Publication Date 2020-12-01
Grant Date 2020-12-01
Owner Nextleaf Solutions Ltd. (Canada)
Inventor
  • Novitski, David Michael
  • Jia, Xuan

Abstract

A slurry is made with ground cannabis biomass and a non-flammable co-solvent. The non-flammable co-solvent is made up of water and ethanol. The ultrasonication process extracts cannabinoids by applying ultrasound to the slurry. The slurry is then filtered, optionally centrifuged, and then distilled to obtain cannabinoid oil.

IPC Classes  ?

  • A61K 36/00 - Medicinal preparations of undetermined constitution containing material from algae, lichens, fungi or plants, or derivatives thereof, e.g. traditional herbal medicines
  • C07C 37/00 - Preparation of compounds having hydroxy or O-metal groups bound to a carbon atom of a six-membered aromatic ring
  • C07D 311/80 - DibenzopyransHydrogenated dibenzopyrans

11.

METHOD FOR ACETYLATION OF CANNABINOIDS

      
Application Number CA2019051350
Publication Number 2020/232526
Status In Force
Filing Date 2019-09-20
Publication Date 2020-11-26
Owner NEXTLEAF SOLUTIONS LTD (Canada)
Inventor
  • Pal, Krupal Devendra
  • Ko, Ryan Delmoral
  • Hughes, Brock Aston
  • Casselman, Ivan Jason

Abstract

A process for producing THC-O-acetate using a succession of distillation, salting-out assisted liquid-liquid extractions (SALLEs), and solvent recovery techniques. Tetrahydrocannabinol (THC) in cannabis oil reacts with acetic anhydride under reflux to produce THC-O-acetate and acetic acid. The resulting crude product is distilled and subjected to a SALLE with hexane followed by a SALLE with petroleum ether, before being distilled again in order to obtain a refined, THC-O-acetate product.

IPC Classes  ?

  • C07D 311/80 - DibenzopyransHydrogenated dibenzopyrans
  • A61K 31/352 - Heterocyclic compounds having oxygen as the only ring hetero atom, e.g. fungichromin having six-membered rings with one oxygen as the only ring hetero atom condensed with carbocyclic rings, e.g. cannabinols, methantheline

12.

Cannabis trichome separation using a tumbler

      
Application Number 16413424
Grant Number 11000856
Status In Force
Filing Date 2019-05-15
First Publication Date 2020-11-19
Grant Date 2021-05-11
Owner Nextleaf Solutions Ltd. (Canada)
Inventor
  • Pal, Krupal Devendra
  • Ulanowski, Thomas Adam
  • Casselman, Ivan Jason

Abstract

cannabis plant matter is agitated in a tumbler in a cooled environment to separate the trichomes from the remainder of the plant matter. The trichomes are then sieved using a sieve shaker with sieves of different mesh sizes mounted in a tower. Chilling the plant material embrittles the trichomes so that they can be removed more easily from the remainder of the plant material.

IPC Classes  ?

  • B02C 21/00 - Disintegrating plant with or without drying of the material
  • B02C 23/14 - Separating or sorting of material, associated with crushing or disintegrating with more than one separator
  • B02C 23/10 - Separating or sorting of material, associated with crushing or disintegrating with separator arranged in discharge path of crushing or disintegrating zone
  • B02C 23/16 - Separating or sorting of material, associated with crushing or disintegrating with separator defining termination of crushing or disintegrating zone, e.g. screen denying egress of oversize material
  • B07B 1/36 - Moving screens not otherwise provided for, e.g. swinging, reciprocating, rocking, tilting, or wobbling screens jigging or moving to-and-fro in more than one direction

13.

Hemp straw ash as a supplementary cementitious material

      
Application Number 16537850
Grant Number 10870603
Status In Force
Filing Date 2019-08-12
First Publication Date 2020-11-12
Grant Date 2020-12-22
Owner Nextleaf Solutions Ltd. (Canada)
Inventor
  • Talukdar, Sudip
  • Behn, Spencer
  • Rashid, Kumayl Aarifali
  • Pargar, Farhad
  • Zanotti, Cristina

Abstract

Hemp straw is ground and burnt to result in hemp straw ash for making concrete. The hemp straw ash is mixed with water, cement, fine aggregate, coarse aggregate and superplasticizer using a two-step addition process to form a concrete mixture. The two-step addition process follows a specific order for the addition of the materials to a concrete mixer drum. Concrete made using the hemp straw ash is useful for lower-strength applications.

IPC Classes  ?

14.

HEMP STRAW ASH AS A SUPPLEMENTARY CEMENTITIOUS MATERIAL

      
Application Number CA2019051454
Publication Number 2020/223785
Status In Force
Filing Date 2019-10-11
Publication Date 2020-11-12
Owner NEXTLEAF SOLUTIONS LTD (Canada)
Inventor
  • Talukdar, Sudip
  • Behn, Spencer
  • Rashid, Kumayl Aarifali
  • Pargar, Farhad
  • Zanotti, Cristina

Abstract

Hemp straw is ground and burnt to result in hemp straw ash for making concrete. The hemp straw ash is mixed with water, cement, fine aggregate, coarse aggregate and superplasticizer using a two-step addition process to form a concrete mixture. The two-step addition process follows a specific order for the addition of the materials to a concrete mixer drum. Concrete made using the hemp straw ash is useful for lower-strength applications.

IPC Classes  ?

  • C04B 28/00 - Compositions of mortars, concrete or artificial stone, containing inorganic binders or the reaction product of an inorganic and an organic binder, e.g. polycarboxylate cements
  • C04B 7/28 - Cements from oil shales, residues or waste other than slag from combustion residues

15.

Acetylation of cannabidiol

      
Application Number 16784212
Grant Number 10792584
Status In Force
Filing Date 2020-02-06
First Publication Date 2020-10-06
Grant Date 2020-10-06
Owner Nextleaf Solutions Ltd. (Canada)
Inventor
  • Pal, Krupal Devendra
  • Ko, Ryan Delmoral
  • Hughes, Brock Aston
  • Casselman, Ivan Jason

Abstract

A process for producing THC-O-acetate using a succession of distillation, salting-out assisted liquid-liquid extractions (SALLEs), and solvent recovery techniques. Tetrahydrocannabinol (THC) in cannabis oil reacts with acetic anhydride under reflux to produce THC-O-acetate and acetic acid. The resulting crude product is distilled and subjected to a SALLE with hexane followed by a SALLE with petroleum ether, before being distilled again in order to obtain a refined, THC-O-acetate product.

IPC Classes  ?

  • B01D 3/14 - Fractional distillation
  • C07D 311/82 - Xanthenes
  • B01D 11/04 - Solvent extraction of solutions which are liquid
  • B01D 3/10 - Vacuum distillation
  • B01D 1/22 - Evaporating by bringing a thin layer of the liquid into contact with a heated surface
  • B01D 5/00 - Condensation of vapoursRecovering volatile solvents by condensation

16.

CANNABIS TRICHOME SEPARATION USING CHILLED WATER

      
Document Number 03097001
Status In Force
Filing Date 2020-01-17
Open to Public Date 2020-08-27
Grant Date 2021-09-14
Owner NEXTLEAF SOLUTIONS LTD. (Canada)
Inventor
  • Casselman, Ivan
  • Ko, Ryan Delmoral
  • Pal, Krupal Devendra
  • Ulanowski, Thomas Adam

Abstract

Cannabis plant material is gently ground, mixed with chilled water and then agitated. The trichomes, being made brittle by the lowered temperature of the water, fall off the plant material during agitation. The mixture is then filtered in multiple stages to obtain the trichomes in different size fractions, which are collected separately and then dried.

IPC Classes  ?

  • A23L 33/105 - Plant extracts, their artificial duplicates or their derivatives
  • A23N 15/00 - Machines or apparatus for other treatment of fruits or vegetables for human purposesMachines or apparatus for topping or skinning flower bulbs
  • A61K 36/185 - Magnoliopsida (dicotyledons)
  • B01D 11/00 - Solvent extraction
  • B01D 21/00 - Separation of suspended solid particles from liquids by sedimentation

17.

CANNABIS TRICHOME SEPARATION USING CHILLED WATER

      
Application Number CA2020050047
Publication Number 2020/168413
Status In Force
Filing Date 2020-01-17
Publication Date 2020-08-27
Owner NEXTLEAF SOLUTIONS LTD (Canada)
Inventor
  • Pal, Krupal Devendra
  • Ulanowski, Thomas Adam
  • Ko, Ryan Delmoral
  • Casselman, Ivan Jason

Abstract

Cannabis plant material is gently ground, mixed with chilled water and then agitated. The trichomes, being made brittle by the lowered temperature of the water, fall off the plant material during agitation. The mixture is then filtered in multiple stages to obtain the trichomes in different size fractions, which are collected separately and then dried.

IPC Classes  ?

  • A61K 36/185 - Magnoliopsida (dicotyledons)
  • A23L 33/105 - Plant extracts, their artificial duplicates or their derivatives
  • B01D 11/00 - Solvent extraction
  • B01D 21/00 - Separation of suspended solid particles from liquids by sedimentation
  • A23N 15/00 - Machines or apparatus for other treatment of fruits or vegetables for human purposesMachines or apparatus for topping or skinning flower bulbs

18.

Cannabis trichome separation using chilled water

      
Application Number 16278579
Grant Number 10780442
Status In Force
Filing Date 2019-02-18
First Publication Date 2020-08-20
Grant Date 2020-09-22
Owner Nextleaf Solutions Ltd. (Canada)
Inventor
  • Pal, Krupal
  • Ulanowski, Thomas Adam
  • Casselman, Ivan
  • Ko, Ryan Delmoral

Abstract

Cannabis plant material is gently ground, mixed with chilled water and then agitated. The trichomes, being made brittle by the lowered temperature of the water, fall off the plant material during agitation. The mixture is then filtered in multiple stages to obtain the trichomes in different size fractions, which are collected separately and then dried.

IPC Classes  ?

  • B02C 21/00 - Disintegrating plant with or without drying of the material
  • B01D 11/02 - Solvent extraction of solids
  • B01D 37/00 - Processes of filtration
  • B02C 23/20 - Adding fluid, other than for crushing or disintegrating by fluid energy after crushing or disintegrating
  • B01D 29/56 - Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition in series connection
  • B02C 23/38 - Adding fluid, other than for crushing or disintegrating by fluid energy in apparatus having multiple crushing or disintegrating zones
  • B02C 23/06 - Selection or use of additives to aid disintegrating
  • B02C 23/14 - Separating or sorting of material, associated with crushing or disintegrating with more than one separator
  • B02C 19/18 - Use of auxiliary physical effects, e.g. ultrasonics, irradiation, for disintegrating
  • A24B 15/00 - Chemical features or treatment of tobaccoTobacco substitutes, e.g. in liquid form
  • B02C 23/16 - Separating or sorting of material, associated with crushing or disintegrating with separator defining termination of crushing or disintegrating zone, e.g. screen denying egress of oversize material

19.

METHOD FOR ACETYLATION OF CANNABINOIDS

      
Document Number 03067195
Status In Force
Filing Date 2020-01-09
Open to Public Date 2020-03-26
Grant Date 2020-07-14
Owner NEXTLEAF SOLUTIONS LTD (Canada)
Inventor
  • Ko, Ryan Delmoral
  • Pal, Krupal Devendra
  • Hughes, Brock Aston
  • Casselman, Ivan Jason

Abstract

A process for producing THC-O-acetate using a succession of distillation, salting-out assisted liquid-liquid extractions (SALLEs), and solvent recovery techniques. Tetrahydrocannabinol (THC) in cannabis oil reacts with acetic anhydride under reflux to produce THC-O-acetate and acetic acid. The resulting crude product is distilled and subjected to a SALLE with hexane followed by a SALLE with petroleum ether, before being distilled again in order to obtain a refined, THC-O-acetate product.

IPC Classes  ?

  • A23L 33/10 - Modifying nutritive qualities of foodsDietetic productsPreparation or treatment thereof using additives
  • A61K 31/352 - Heterocyclic compounds having oxygen as the only ring hetero atom, e.g. fungichromin having six-membered rings with one oxygen as the only ring hetero atom condensed with carbocyclic rings, e.g. cannabinols, methantheline
  • C07D 311/80 - DibenzopyransHydrogenated dibenzopyrans

20.

METHOD FOR ACETYLATION OF CANNABIDIOL

      
Document Number 03081302
Status In Force
Filing Date 2020-01-09
Open to Public Date 2020-03-26
Grant Date 2021-01-12
Owner NEXTLEAF SOLUTIONS LTD (Canada)
Inventor
  • Ko, Ryan Delmoral
  • Pal, Krupal Devendra
  • Hughes, Brock Aston
  • Casselman, Ivan Jason

Abstract

A process for producing THC-O-acetate using a succession of distillation, salting-out assisted liquid-liquid extractions (SALLEs), and solvent recovery techniques. Tetrahydrocannabinol (THC) in cannabis oil reacts with acetic anhydride under reflux to produce THC-O-acetate and acetic acid. The resulting crude product is distilled and subjected to a SALLE with hexane followed by a SALLE with petroleum ether, before being distilled again in order to obtain a refined, THC-O-acetate product.

IPC Classes  ?

  • C07C 39/23 - Compounds having at least one hydroxy or O-metal group bound to a carbon atom of a six-membered aromatic ring polycyclic, containing six-membered aromatic rings and other rings, with unsaturation outside the aromatic rings
  • C07C 67/08 - Preparation of carboxylic acid esters by reacting carboxylic acids or symmetrical anhydrides with the hydroxy or O-metal group of organic compounds
  • C07C 69/16 - Acetic acid esters of dihydroxylic compounds

21.

METHOD AND SYSTEM FOR SHATTER EXTRACTION

      
Application Number CA2019051070
Publication Number 2020/051679
Status In Force
Filing Date 2019-08-05
Publication Date 2020-03-19
Owner NEXTLEAF SOLUTIONS LTD (Canada)
Inventor
  • Ko, Ryan Delmoral
  • Hughes, Brock

Abstract

Concentrated cannabis extract is obtained from raw cannabis plant material using a mixed solvent extraction process. The cannabis is soaked and agitated in a chilled mixture of butane, propane and isobutane. After removing the solid plant material, the remaining solvent mixture, now with dissolved extracts, is heated to remove the solvents. The remaining, viscous oil is then heated in a vacuum oven to purge the traces of solvent and result in a brittle shatter.

IPC Classes  ?

  • A61K 36/185 - Magnoliopsida (dicotyledons)
  • B01D 11/02 - Solvent extraction of solids
  • C11B 1/00 - Production of fats or fatty oils from raw materials
  • C11B 1/10 - Production of fats or fatty oils from raw materials by extracting
  • C11B 9/00 - Essential oilsPerfumes
  • A23L 33/105 - Plant extracts, their artificial duplicates or their derivatives

22.

Method for acetylation of cannabinoids

      
Application Number 16415782
Grant Number 10569189
Status In Force
Filing Date 2019-05-17
First Publication Date 2020-02-25
Grant Date 2020-02-25
Owner Nextleaf Solutions Ltd. (Canada)
Inventor
  • Pal, Krupal Devendra
  • Ko, Ryan Delmoral
  • Hughes, Brock Aston
  • Casselman, Ivan Jason

Abstract

A process for producing THC-O-acetate using a succession of distillation, salting-out assisted liquid-liquid extractions (SALLEs), and solvent recovery techniques. Tetrahydrocannabinol (THC) in cannabis oil reacts with acetic anhydride under reflux to produce THC-O-acetate and acetic acid. The resulting crude product is distilled and subjected to a SALLE with hexane followed by a SALLE with petroleum ether, before being distilled again in order to obtain a refined, THC-O-acetate product.

IPC Classes  ?

  • B01D 3/14 - Fractional distillation
  • C07D 311/82 - Xanthenes
  • B01D 5/00 - Condensation of vapoursRecovering volatile solvents by condensation
  • B01D 3/10 - Vacuum distillation
  • B01D 1/22 - Evaporating by bringing a thin layer of the liquid into contact with a heated surface
  • B01D 11/04 - Solvent extraction of solutions which are liquid

23.

Elevated multi-stage chilled filter system

      
Application Number 16660018
Grant Number 10646793
Status In Force
Filing Date 2019-10-22
First Publication Date 2020-02-13
Grant Date 2020-05-12
Owner Nextleaf Solutions Ltd. (Canada)
Inventor Ko, Ryan Delmoral

Abstract

Refrigerated solvent is fed through a cooling jacket around an essential element extraction vessel. After circulating through the cooling jacket, the solvent is re-chilled and at least some of the solvent is passed into the extraction vessel, in which essential elements dissolve into the solvent. Downstream of the extraction vessel, after adsorbent media treatment, the extracted oil and solvent mixture is filtered, in a chilled state, through one or more filtration units. A filtration unit may be a system of vertically oriented filters of decreasing pore size sealed and insulated from the atmosphere. Pressurized gas is used to force the oil and solvent through the filters. Each filter stage has a removable lid, which provides convenient access for replacing the filter cartridge without disturbing the thermally insulated sidewalls of the filter stage.

IPC Classes  ?

  • B01D 11/02 - Solvent extraction of solids
  • B01D 29/56 - Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups Filtering elements therefor with multiple filtering elements, characterised by their mutual disposition in series connection
  • B01D 15/18 - Selective adsorption, e.g. chromatography characterised by constructional or operational features relating to flow patterns
  • C11B 1/10 - Production of fats or fatty oils from raw materials by extracting
  • B01D 15/00 - Separating processes involving the treatment of liquids with solid sorbentsApparatus therefor
  • C11B 3/12 - Refining fats or fatty oils by distillation
  • C11B 3/14 - Refining fats or fatty oils by distillation with the use of indifferent gases or vapours, e.g. steam

24.

NEXTLEAF

      
Application Number 018181715
Status Registered
Filing Date 2020-01-17
Registration Date 2020-05-22
Owner Nextleaf Solutions Ltd. (Canada)
NICE Classes  ?
  • 22 - Rope, netting, tents, awnings, sails and sacks; padding and stuffing materials
  • 31 - Agricultural products; live animals
  • 40 - Treatment of materials; recycling, air and water treatment,
  • 45 - Legal and security services; personal services for individuals.

Goods & Services

Hemp. Unprocessed agricultural and horticultural products; Seeds for horticultural purposes; Agricultural seeds; Edible pet treats. Provision of cannabis and hemp processing services, namely processing of dried cannabis and hemp into THC and CBD distillate oil. Licensing services; Licensing of cannabis and hemp processing services, namely processing of dried cannabis and hemp into THC and CBD distillate oil.

25.

CLOSED LOOP CHILLED SOLVENT FEED FOR CANNABINOID EXTRACTION

      
Document Number 03063941
Status In Force
Filing Date 2018-11-08
Open to Public Date 2019-05-16
Grant Date 2020-02-18
Owner NEXTLEAF SOLUTIONS LTD (Canada)
Inventor Ko, Ryan Delmoral

Abstract

Refrigerated solvent is fed through a cooling jacket around an essential element extraction vessel. After circulating through the cooling jacket, the solvent is re-chilled and at least some of the solvent is passed into the extraction vessel, in which essential elements dissolve into the solvent. Downstream of the extraction vessel, after adsorbent media treatment, the extracted oil and solvent mixture is filtered, in a chilled state, through one or more filtration units. A filtration unit may be a system of vertically oriented filters of decreasing pore size sealed and insulated from the atmosphere. Pressurized gas is used to force the oil and solvent through the filters. Each filter stage has a removable lid, which provides convenient access for replacing the filter cartridge without disturbing the thermally insulated sidewalls of the filter stage.

IPC Classes  ?

  • A23L 33/105 - Plant extracts, their artificial duplicates or their derivatives
  • A61K 31/05 - Phenols
  • A61K 31/352 - Heterocyclic compounds having oxygen as the only ring hetero atom, e.g. fungichromin having six-membered rings with one oxygen as the only ring hetero atom condensed with carbocyclic rings, e.g. cannabinols, methantheline
  • A61K 36/185 - Magnoliopsida (dicotyledons)
  • B01D 11/02 - Solvent extraction of solids
  • C07C 39/23 - Compounds having at least one hydroxy or O-metal group bound to a carbon atom of a six-membered aromatic ring polycyclic, containing six-membered aromatic rings and other rings, with unsaturation outside the aromatic rings
  • C07D 311/80 - DibenzopyransHydrogenated dibenzopyrans

26.

CLOSED LOOP CHILLED SOLVENT FEED FOR CANNABINOID EXTRACTION

      
Application Number CA2018051416
Publication Number 2019/090428
Status In Force
Filing Date 2018-11-08
Publication Date 2019-05-16
Owner NEXTLEAF SOLUTIONS LTD (Canada)
Inventor Ko, Ryan Delmoral

Abstract

Refrigerated solvent is fed through a cooling jacket around an essential element extraction vessel. After circulating through the cooling jacket, the solvent is re-chilled and at least some of the solvent is passed into the extraction vessel, in which essential elements dissolve into the solvent. Downstream of the extraction vessel, after adsorbent media treatment, the extracted oil and solvent mixture is filtered, in a chilled state, through one or more filtration units. A filtration unit may be a system of vertically oriented filters of decreasing pore size sealed and insulated from the atmosphere. Pressurized gas is used to force the oil and solvent through the filters. Each filter stage has a removable lid, which provides convenient access for replacing the filter cartridge without disturbing the thermally insulated sidewalls of the filter stage.

IPC Classes  ?

  • B01D 11/02 - Solvent extraction of solids
  • A23L 33/105 - Plant extracts, their artificial duplicates or their derivatives
  • A61K 31/05 - Phenols
  • A61K 31/352 - Heterocyclic compounds having oxygen as the only ring hetero atom, e.g. fungichromin having six-membered rings with one oxygen as the only ring hetero atom condensed with carbocyclic rings, e.g. cannabinols, methantheline
  • A61K 36/185 - Magnoliopsida (dicotyledons)
  • C07C 39/23 - Compounds having at least one hydroxy or O-metal group bound to a carbon atom of a six-membered aromatic ring polycyclic, containing six-membered aromatic rings and other rings, with unsaturation outside the aromatic rings
  • C07D 311/80 - DibenzopyransHydrogenated dibenzopyrans

27.

CLOSED-LOOP MULTI-STAGE CHILLED FILTER SYSTEM

      
Document Number 03023563
Status In Force
Filing Date 2018-11-08
Open to Public Date 2019-05-10
Grant Date 2019-12-24
Owner NEXTLEAF SOLUTIONS LTD. (Canada)
Inventor Ko, Ryan Delmoral

Abstract

A series of vertically oriented filters of decreasing pore size is sealed from the atmosphere. Pressurized gas is used to force the liquid to be filtered through the filters. The filter stages are thermally insulated from ambient temperatures in order to maintain the liquid passing through at a reduced temperature. Each filter stage has a removable lid, which provides convenient access for replacing the filter cartridge, allowing it to be changed without disturbing the thermally insulated sidewalls of the filter stage.

IPC Classes  ?

  • B01D 27/08 - Construction of the casing
  • B01D 27/14 - Cartridge filters of the throw-away type having more than one filtering element

28.

CANNABINOID EXTRACTION PROCESS USING BRINE

      
Document Number 03063960
Status In Force
Filing Date 2018-09-07
Open to Public Date 2019-04-04
Grant Date 2020-03-10
Owner NEXTLEAF SOLUTIONS LTD (Canada)
Inventor
  • Ko, Ryan Delmoral
  • Hughes, Brock
  • Pal, Krupal Devendra
  • Samuelsson, Alexzander

Abstract

Raw cannabis plant material is mixed with ethanol and spun-dry to extract cannabinoids. The ethanol may be chilled before adding it to the raw cannabis plant material, and a non-polar solvent stage may be used to increase the yield of the extraction. The resulting crude oil and ethanol with the dissolved cannabinoids is separated from the raw cannabis plant material and filtered to remove particulates, waxes, lipids, fats and dissolved impurities. The ethanol is then evaporated from the resulting mixture of oil and ethanol, and the remaining oil then undergoes brine- washing, decarboxylation and distillation to obtain the cannabinoids and other desirable volatile phytochemicals.

IPC Classes  ?

  • A61K 31/05 - Phenols
  • A61K 31/352 - Heterocyclic compounds having oxygen as the only ring hetero atom, e.g. fungichromin having six-membered rings with one oxygen as the only ring hetero atom condensed with carbocyclic rings, e.g. cannabinols, methantheline
  • A61K 36/185 - Magnoliopsida (dicotyledons)
  • B01D 11/02 - Solvent extraction of solids
  • C07C 39/23 - Compounds having at least one hydroxy or O-metal group bound to a carbon atom of a six-membered aromatic ring polycyclic, containing six-membered aromatic rings and other rings, with unsaturation outside the aromatic rings
  • C07D 311/80 - DibenzopyransHydrogenated dibenzopyrans

29.

CANNABINOID EXTRACTION PROCESS USING BRINE

      
Application Number CA2018051096
Publication Number 2019/060986
Status In Force
Filing Date 2018-09-07
Publication Date 2019-04-04
Owner NEXTLEAF SOLUTIONS LTD (Canada)
Inventor
  • Ko, Ryan Delmoral
  • Hughes, Brock
  • Pal, Krupal Devendra
  • Samuelsson, Alexzander

Abstract

Raw cannabis plant material is mixed with ethanol and spun-dry to extract cannabinoids. The ethanol may be chilled before adding it to the raw cannabis plant material, and a non-polar solvent stage may be used to increase the yield of the extraction. The resulting crude oil and ethanol with the dissolved cannabinoids is separated from the raw cannabis plant material and filtered to remove particulates, waxes, lipids, fats and dissolved impurities. The ethanol is then evaporated from the resulting mixture of oil and ethanol, and the remaining oil then undergoes brine- washing, decarboxylation and distillation to obtain the cannabinoids and other desirable volatile phytochemicals.

IPC Classes  ?

  • A61K 36/185 - Magnoliopsida (dicotyledons)
  • A61K 31/05 - Phenols
  • A61K 31/352 - Heterocyclic compounds having oxygen as the only ring hetero atom, e.g. fungichromin having six-membered rings with one oxygen as the only ring hetero atom condensed with carbocyclic rings, e.g. cannabinols, methantheline
  • B01D 11/02 - Solvent extraction of solids
  • C07C 39/23 - Compounds having at least one hydroxy or O-metal group bound to a carbon atom of a six-membered aromatic ring polycyclic, containing six-membered aromatic rings and other rings, with unsaturation outside the aromatic rings
  • C07D 311/80 - DibenzopyransHydrogenated dibenzopyrans

30.

Closed-loop multi-stage chilled filter system

      
Application Number 15809980
Grant Number 10245525
Status In Force
Filing Date 2017-11-10
First Publication Date 2019-04-02
Grant Date 2019-04-02
Owner Nextleaf Solutions Ltd. (Canada)
Inventor Ko, Ryan Delmoral

Abstract

A series of vertically oriented filters of decreasing pore size is sealed from the atmosphere. Pressurized gas is used to force the liquid to be filtered through the filters. The filter stages are thermally insulated from ambient temperatures in order to maintain the liquid passing through at a reduced temperature. Each filter stage has a removable lid, which provides convenient access for replacing the filter cartridge, allowing it to be changed without disturbing the thermally insulated sidewalls of the filter stage.

IPC Classes  ?

  • B01D 11/00 - Solvent extraction
  • B01D 11/02 - Solvent extraction of solids
  • B01D 46/00 - Filters or filtering processes specially modified for separating dispersed particles from gases or vapours

31.

NEXTLEAF

      
Serial Number 88107284
Status Registered
Filing Date 2018-12-20
Registration Date 2020-03-03
Owner Nextleaf Solutions Ltd. (Canada)
NICE Classes  ? 40 - Treatment of materials; recycling, air and water treatment,

Goods & Services

Provision of hemp processing services, namely, the processing of dried industrial hemp

32.

NEXTLEAF

      
Serial Number 87622769
Status Registered
Filing Date 2018-12-20
Registration Date 2020-02-18
Owner NEXTLEAF SOLUTIONS LTD. (Canada)
NICE Classes  ? 40 - Treatment of materials; recycling, air and water treatment,

Goods & Services

Provision of hemp processing services, namely, the processing of dried industrial hemp into distillate oil

33.

CANNABINOID EXTRACTION PROCESS AND SYSTEM

      
Document Number 03016078
Status In Force
Filing Date 2018-08-31
Open to Public Date 2018-09-09
Grant Date 2019-09-17
Owner NEXTLEAF SOLUTIONS LTD. (Canada)
Inventor
  • Ko, Ryan Delmoral
  • Hughes, Brock

Abstract

Raw plant material is mixed with ethanol under pressure to extract essential elements. The resulting crude oil and ethanol with the dissolved essential elements is separated from the raw plant material and filtered to remove particulates, waxes, lipids, fats and dissolved impurities. The ethanol is then evaporated from the resulting mixture of crude oil and ethanol, and the remaining crude oil then undergoes decarboxylation and distillation to obtain the essential elements. The ethanol may be chilled before adding it to the raw plant material.

IPC Classes  ?

34.

CANNABINOID EXTRACTION AND DISTILLATION

      
Document Number 03051325
Status In Force
Filing Date 2018-08-31
Open to Public Date 2018-09-09
Grant Date 2020-05-05
Owner NEXTLEAF SOLUTIONS LTD. (Canada)
Inventor
  • Ko, Ryan Delmoral
  • Hughes, Brock

Abstract

Raw plant material is mixed with ethanol under pressure to extract essential elements. The resulting crude oil and ethanol with the dissolved essential elements is separated from the raw plant material and filtered to remove particulates, waxes, lipids, fats and dissolved impurities. The ethanol is then evaporated from the resulting mixture of crude oil and ethanol, and the remaining crude oil then undergoes decarboxylation and distillation to obtain the essential elements. The ethanol may be chilled before adding it to the raw plant material.

IPC Classes  ?

  • A61K 31/352 - Heterocyclic compounds having oxygen as the only ring hetero atom, e.g. fungichromin having six-membered rings with one oxygen as the only ring hetero atom condensed with carbocyclic rings, e.g. cannabinols, methantheline
  • A61K 36/185 - Magnoliopsida (dicotyledons)
  • B01D 11/02 - Solvent extraction of solids

35.

NEXTLEAF

      
Application Number 191794700
Status Registered
Filing Date 2018-08-31
Registration Date 2019-06-24
Owner Nextleaf Solutions Ltd. (Canada)
NICE Classes  ?
  • 22 - Rope, netting, tents, awnings, sails and sacks; padding and stuffing materials
  • 31 - Agricultural products; live animals
  • 40 - Treatment of materials; recycling, air and water treatment,
  • 45 - Legal and security services; personal services for individuals.

Goods & Services

(1) Hemp (2) Agricultural and horticultural products, namely, natural plants and flowers, living plants, plant cuttings, seeds for horticultural purposes, agricultural seeds, dried plants; Edible treats for pets; (1) Provision and licensing of cannabis and hemp processing services, namely the processing of dried cannabis and hemp into THC and CBD distillate oil;

36.

Cannabinoid extraction process and system

      
Application Number 15721344
Grant Number 09987567
Status In Force
Filing Date 2017-09-29
First Publication Date 2018-06-05
Grant Date 2018-06-05
Owner NEXTLEAF SOLUTIONS LTD. (Canada)
Inventor Ko, Ryan Delmoral

Abstract

Raw plant material is mixed with ethanol under pressure to extract essential elements. The resulting crude oil and ethanol with the dissolved essential elements is separated from the raw plant material and filtered to remove particulates, waxes, lipids, fats and dissolved impurities. The ethanol is then evaporated from the resulting mixture of crude oil and ethanol, and the remaining crude oil then undergoes decarboxylation and distillation to obtain the essential elements. The ethanol may be chilled before adding it to the raw plant material.

IPC Classes  ?

  • B01D 11/02 - Solvent extraction of solids
  • C07D 311/80 - DibenzopyransHydrogenated dibenzopyrans
  • B01D 3/08 - Distillation or related exchange processes in which liquids are contacted with gaseous media, e.g. stripping in rotating vesselsAtomisation on rotating discs
  • B01D 15/00 - Separating processes involving the treatment of liquids with solid sorbentsApparatus therefor
  • C07C 37/86 - SeparationPurificationStabilisationUse of additives by treatment giving rise to a chemical modification

37.

NEXTLEAF

      
Application Number 185945300
Status Registered
Filing Date 2017-09-26
Registration Date 2019-06-24
Owner Nextleaf Solutions Ltd. (Canada)
NICE Classes  ?
  • 31 - Agricultural products; live animals
  • 40 - Treatment of materials; recycling, air and water treatment,
  • 45 - Legal and security services; personal services for individuals.

Goods & Services

(1) Hemp (2) Agricultural and horticultural products, namely, natural plants and flowers, living plants, plant cuttings, seeds for horticultural purposes, agricultural seeds, dried plants, hemp; Edible treats for pets; (1) Provision and licensing of cannabis and hemp processing services, namely the processing of dried cannabis and hemp into THC and CBD distillate oil;

38.

NEXTLEAF

      
Application Number 185945200
Status Registered
Filing Date 2017-09-26
Registration Date 2019-06-24
Owner Nextleaf Solutions Ltd. (Canada)
NICE Classes  ?
  • 31 - Agricultural products; live animals
  • 40 - Treatment of materials; recycling, air and water treatment,
  • 45 - Legal and security services; personal services for individuals.

Goods & Services

(1) Hemp (2) Agricultural and horticultural products, namely, natural plants and flowers, living plants, plant cuttings, seeds for horticultural purposes, agricultural seeds, dried plants, hemp; Edible treats for pets; (1) Provision and licensing of cannabis and hemp processing services, namely the processing of dried cannabis and hemp into THC and CBD distillate oil;