CN110786513A - Method for extracting and purifying hemp full spectrum oil - Google Patents
Method for extracting and purifying hemp full spectrum oil Download PDFInfo
- Publication number
- CN110786513A CN110786513A CN201911060515.XA CN201911060515A CN110786513A CN 110786513 A CN110786513 A CN 110786513A CN 201911060515 A CN201911060515 A CN 201911060515A CN 110786513 A CN110786513 A CN 110786513A
- Authority
- CN
- China
- Prior art keywords
- extracting
- oil
- hemp
- cannabis
- purifying
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Withdrawn
Links
- 244000025254 Cannabis sativa Species 0.000 title claims abstract description 42
- 235000005607 chanvre indien Nutrition 0.000 title claims abstract description 36
- 239000011487 hemp Substances 0.000 title claims abstract description 36
- 238000000034 method Methods 0.000 title claims abstract description 36
- 235000012766 Cannabis sativa ssp. sativa var. sativa Nutrition 0.000 title claims abstract description 35
- 235000012765 Cannabis sativa ssp. sativa var. spontanea Nutrition 0.000 title claims abstract description 35
- 235000009120 camo Nutrition 0.000 title claims abstract description 35
- 238000001228 spectrum Methods 0.000 title claims abstract description 34
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 claims abstract description 39
- 238000000605 extraction Methods 0.000 claims abstract description 32
- 239000000284 extract Substances 0.000 claims abstract description 22
- 238000001035 drying Methods 0.000 claims abstract description 19
- 238000010438 heat treatment Methods 0.000 claims abstract description 15
- 238000003756 stirring Methods 0.000 claims abstract description 14
- VLKZOEOYAKHREP-UHFFFAOYSA-N n-Hexane Chemical compound CCCCCC VLKZOEOYAKHREP-UHFFFAOYSA-N 0.000 claims abstract description 13
- 238000001914 filtration Methods 0.000 claims abstract description 11
- 239000000463 material Substances 0.000 claims abstract description 8
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 claims abstract description 7
- 239000000741 silica gel Substances 0.000 claims abstract description 6
- 229910002027 silica gel Inorganic materials 0.000 claims abstract description 6
- 238000010298 pulverizing process Methods 0.000 claims abstract description 4
- 239000007788 liquid Substances 0.000 claims abstract description 3
- 239000008187 granular material Substances 0.000 claims description 7
- 238000002156 mixing Methods 0.000 claims description 7
- 238000001556 precipitation Methods 0.000 claims description 6
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 6
- 238000004440 column chromatography Methods 0.000 claims description 5
- 238000001816 cooling Methods 0.000 claims description 5
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 5
- 238000002390 rotary evaporation Methods 0.000 claims description 5
- 238000007865 diluting Methods 0.000 claims description 4
- 238000004806 packaging method and process Methods 0.000 claims description 4
- 239000002245 particle Substances 0.000 claims description 4
- 238000002791 soaking Methods 0.000 claims description 4
- 239000003480 eluent Substances 0.000 claims description 3
- 239000000499 gel Substances 0.000 claims description 3
- 238000005086 pumping Methods 0.000 claims description 3
- 239000011347 resin Substances 0.000 claims description 3
- 229920005989 resin Polymers 0.000 claims description 3
- 230000007480 spreading Effects 0.000 claims description 3
- 238000003892 spreading Methods 0.000 claims description 3
- 241000218236 Cannabis Species 0.000 claims 9
- 238000010828 elution Methods 0.000 claims 1
- 239000000945 filler Substances 0.000 claims 1
- 238000012856 packing Methods 0.000 claims 1
- CYQFCXCEBYINGO-UHFFFAOYSA-N THC Natural products C1=C(C)CCC2C(C)(C)OC3=CC(CCCCC)=CC(O)=C3C21 CYQFCXCEBYINGO-UHFFFAOYSA-N 0.000 abstract description 12
- CYQFCXCEBYINGO-IAGOWNOFSA-N delta1-THC Chemical compound C1=C(C)CC[C@H]2C(C)(C)OC3=CC(CCCCC)=CC(O)=C3[C@@H]21 CYQFCXCEBYINGO-IAGOWNOFSA-N 0.000 abstract description 12
- 229960004242 dronabinol Drugs 0.000 abstract description 12
- 239000000706 filtrate Substances 0.000 abstract description 9
- 238000000926 separation method Methods 0.000 abstract description 7
- 230000008901 benefit Effects 0.000 abstract description 6
- 230000008569 process Effects 0.000 abstract description 6
- 239000003960 organic solvent Substances 0.000 abstract description 4
- 238000005265 energy consumption Methods 0.000 abstract description 3
- 239000012141 concentrate Substances 0.000 abstract 1
- 239000013078 crystal Substances 0.000 abstract 1
- 238000002425 crystallisation Methods 0.000 abstract 1
- 230000008025 crystallization Effects 0.000 abstract 1
- 239000011521 glass Substances 0.000 abstract 1
- 239000003292 glue Substances 0.000 abstract 1
- 231100000053 low toxicity Toxicity 0.000 abstract 1
- 238000004064 recycling Methods 0.000 abstract 1
- 239000004576 sand Substances 0.000 abstract 1
- 239000003921 oil Substances 0.000 description 27
- 235000019198 oils Nutrition 0.000 description 27
- QHMBSVQNZZTUGM-UHFFFAOYSA-N Trans-Cannabidiol Natural products OC1=CC(CCCCC)=CC(O)=C1C1C(C(C)=C)CCC(C)=C1 QHMBSVQNZZTUGM-UHFFFAOYSA-N 0.000 description 15
- ZTGXAWYVTLUPDT-UHFFFAOYSA-N cannabidiol Natural products OC1=CC(CCCCC)=CC(O)=C1C1C(C(C)=C)CC=C(C)C1 ZTGXAWYVTLUPDT-UHFFFAOYSA-N 0.000 description 15
- QHMBSVQNZZTUGM-ZWKOTPCHSA-N cannabidiol Chemical compound OC1=CC(CCCCC)=CC(O)=C1[C@H]1[C@H](C(C)=C)CCC(C)=C1 QHMBSVQNZZTUGM-ZWKOTPCHSA-N 0.000 description 15
- 229950011318 cannabidiol Drugs 0.000 description 15
- PCXRACLQFPRCBB-ZWKOTPCHSA-N dihydrocannabidiol Natural products OC1=CC(CCCCC)=CC(O)=C1[C@H]1[C@H](C(C)C)CCC(C)=C1 PCXRACLQFPRCBB-ZWKOTPCHSA-N 0.000 description 15
- 240000004308 marijuana Species 0.000 description 12
- 239000010460 hemp oil Substances 0.000 description 10
- 230000000694 effects Effects 0.000 description 9
- 239000000047 product Substances 0.000 description 7
- 235000008697 Cannabis sativa Nutrition 0.000 description 6
- 230000009286 beneficial effect Effects 0.000 description 5
- 238000010521 absorption reaction Methods 0.000 description 4
- 239000003814 drug Substances 0.000 description 4
- 235000020660 omega-3 fatty acid Nutrition 0.000 description 4
- UVOLYTDXHDXWJU-UHFFFAOYSA-N Cannabichromene Chemical compound C1=CC(C)(CCC=C(C)C)OC2=CC(CCCCC)=CC(O)=C21 UVOLYTDXHDXWJU-UHFFFAOYSA-N 0.000 description 3
- VBGLYOIFKLUMQG-UHFFFAOYSA-N Cannabinol Chemical compound C1=C(C)C=C2C3=C(O)C=C(CCCCC)C=C3OC(C)(C)C2=C1 VBGLYOIFKLUMQG-UHFFFAOYSA-N 0.000 description 3
- YMWUJEATGCHHMB-UHFFFAOYSA-N Dichloromethane Chemical compound ClCCl YMWUJEATGCHHMB-UHFFFAOYSA-N 0.000 description 3
- OKKJLVBELUTLKV-UHFFFAOYSA-N Methanol Chemical compound OC OKKJLVBELUTLKV-UHFFFAOYSA-N 0.000 description 3
- DTOSIQBPPRVQHS-PDBXOOCHSA-N alpha-linolenic acid Chemical class CC\C=C/C\C=C/C\C=C/CCCCCCCC(O)=O DTOSIQBPPRVQHS-PDBXOOCHSA-N 0.000 description 3
- 229930003827 cannabinoid Natural products 0.000 description 3
- 239000003557 cannabinoid Substances 0.000 description 3
- 229940065144 cannabinoids Drugs 0.000 description 3
- 239000003795 chemical substances by application Substances 0.000 description 3
- 230000003400 hallucinatory effect Effects 0.000 description 3
- 235000021315 omega 9 monounsaturated fatty acids Nutrition 0.000 description 3
- 235000011624 Agave sisalana Nutrition 0.000 description 2
- 244000198134 Agave sisalana Species 0.000 description 2
- REOZWEGFPHTFEI-JKSUJKDBSA-N Cannabidivarin Chemical compound OC1=CC(CCC)=CC(O)=C1[C@H]1[C@H](C(C)=C)CCC(C)=C1 REOZWEGFPHTFEI-JKSUJKDBSA-N 0.000 description 2
- 208000024172 Cardiovascular disease Diseases 0.000 description 2
- HEDRZPFGACZZDS-UHFFFAOYSA-N Chloroform Chemical compound ClC(Cl)Cl HEDRZPFGACZZDS-UHFFFAOYSA-N 0.000 description 2
- 206010012335 Dependence Diseases 0.000 description 2
- 241000196324 Embryophyta Species 0.000 description 2
- 206010020772 Hypertension Diseases 0.000 description 2
- 239000004480 active ingredient Substances 0.000 description 2
- 230000032683 aging Effects 0.000 description 2
- QXACEHWTBCFNSA-SFQUDFHCSA-N cannabigerol Chemical compound CCCCCC1=CC(O)=C(C\C=C(/C)CCC=C(C)C)C(O)=C1 QXACEHWTBCFNSA-SFQUDFHCSA-N 0.000 description 2
- 208000026106 cerebrovascular disease Diseases 0.000 description 2
- 230000006378 damage Effects 0.000 description 2
- 235000014113 dietary fatty acids Nutrition 0.000 description 2
- 238000004134 energy conservation Methods 0.000 description 2
- 230000029142 excretion Effects 0.000 description 2
- 235000019197 fats Nutrition 0.000 description 2
- 239000000194 fatty acid Substances 0.000 description 2
- 229930195729 fatty acid Natural products 0.000 description 2
- 150000004665 fatty acids Chemical class 0.000 description 2
- 238000011049 filling Methods 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 230000036541 health Effects 0.000 description 2
- 201000001421 hyperglycemia Diseases 0.000 description 2
- VKOBVWXKNCXXDE-UHFFFAOYSA-N icosanoic acid Chemical compound CCCCCCCCCCCCCCCCCCCC(O)=O VKOBVWXKNCXXDE-UHFFFAOYSA-N 0.000 description 2
- 230000036039 immunity Effects 0.000 description 2
- 239000012535 impurity Substances 0.000 description 2
- 238000009776 industrial production Methods 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 238000000746 purification Methods 0.000 description 2
- 230000001105 regulatory effect Effects 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000000194 supercritical-fluid extraction Methods 0.000 description 2
- 239000006228 supernatant Substances 0.000 description 2
- 235000021122 unsaturated fatty acids Nutrition 0.000 description 2
- 150000004670 unsaturated fatty acids Chemical class 0.000 description 2
- 235000015112 vegetable and seed oil Nutrition 0.000 description 2
- 239000008158 vegetable oil Substances 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- HIXDQWDOVZUNNA-UHFFFAOYSA-N 2-(3,4-dimethoxyphenyl)-5-hydroxy-7-methoxychromen-4-one Chemical compound C=1C(OC)=CC(O)=C(C(C=2)=O)C=1OC=2C1=CC=C(OC)C(OC)=C1 HIXDQWDOVZUNNA-UHFFFAOYSA-N 0.000 description 1
- 208000019901 Anxiety disease Diseases 0.000 description 1
- 241000218235 Cannabaceae Species 0.000 description 1
- 208000031226 Hyperlipidaemia Diseases 0.000 description 1
- OYHQOLUKZRVURQ-HZJYTTRNSA-N Linoleic acid Chemical compound CCCCC\C=C/C\C=C/CCCCCCCC(O)=O OYHQOLUKZRVURQ-HZJYTTRNSA-N 0.000 description 1
- 208000005392 Spasm Diseases 0.000 description 1
- 244000228451 Stevia rebaudiana Species 0.000 description 1
- 235000006092 Stevia rebaudiana Nutrition 0.000 description 1
- 239000013543 active substance Substances 0.000 description 1
- 239000002671 adjuvant Substances 0.000 description 1
- 235000020661 alpha-linolenic acid Nutrition 0.000 description 1
- 230000036506 anxiety Effects 0.000 description 1
- 150000001491 aromatic compounds Chemical class 0.000 description 1
- 239000004566 building material Substances 0.000 description 1
- 230000001276 controlling effect Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 238000011161 development Methods 0.000 description 1
- 230000018109 developmental process Effects 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 239000003085 diluting agent Substances 0.000 description 1
- 238000007598 dipping method Methods 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000008157 edible vegetable oil Substances 0.000 description 1
- 230000002526 effect on cardiovascular system Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007613 environmental effect Effects 0.000 description 1
- 206010015037 epilepsy Diseases 0.000 description 1
- IDGUHHHQCWSQLU-UHFFFAOYSA-N ethanol;hydrate Chemical compound O.CCO IDGUHHHQCWSQLU-UHFFFAOYSA-N 0.000 description 1
- RTZKZFJDLAIYFH-UHFFFAOYSA-N ether Substances CCOCC RTZKZFJDLAIYFH-UHFFFAOYSA-N 0.000 description 1
- 238000001704 evaporation Methods 0.000 description 1
- 230000008020 evaporation Effects 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 201000005577 familial hyperlipidemia Diseases 0.000 description 1
- 239000000835 fiber Substances 0.000 description 1
- 239000012467 final product Substances 0.000 description 1
- 235000013305 food Nutrition 0.000 description 1
- 235000020664 gamma-linolenic acid Nutrition 0.000 description 1
- 238000011065 in-situ storage Methods 0.000 description 1
- 235000020778 linoleic acid Nutrition 0.000 description 1
- OYHQOLUKZRVURQ-IXWMQOLASA-N linoleic acid Natural products CCCCC\C=C/C\C=C\CCCCCCCC(O)=O OYHQOLUKZRVURQ-IXWMQOLASA-N 0.000 description 1
- 229960004488 linolenic acid Drugs 0.000 description 1
- 238000011068 loading method Methods 0.000 description 1
- 230000007774 longterm Effects 0.000 description 1
- 239000002207 metabolite Substances 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 235000021281 monounsaturated fatty acids Nutrition 0.000 description 1
- 210000005036 nerve Anatomy 0.000 description 1
- 231100001096 no neurotoxicity Toxicity 0.000 description 1
- 231100000252 nontoxic Toxicity 0.000 description 1
- 230000003000 nontoxic effect Effects 0.000 description 1
- 231100000956 nontoxicity Toxicity 0.000 description 1
- 235000020665 omega-6 fatty acid Nutrition 0.000 description 1
- 229940033080 omega-6 fatty acid Drugs 0.000 description 1
- 230000008520 organization Effects 0.000 description 1
- 230000003647 oxidation Effects 0.000 description 1
- 238000007254 oxidation reaction Methods 0.000 description 1
- 239000003208 petroleum Substances 0.000 description 1
- 235000020777 polyunsaturated fatty acids Nutrition 0.000 description 1
- 239000000843 powder Substances 0.000 description 1
- 239000011802 pulverized particle Substances 0.000 description 1
- 238000011084 recovery Methods 0.000 description 1
- 238000011160 research Methods 0.000 description 1
- 201000003068 rheumatic fever Diseases 0.000 description 1
- 238000013341 scale-up Methods 0.000 description 1
- 229930000044 secondary metabolite Natural products 0.000 description 1
- 239000008159 sesame oil Substances 0.000 description 1
- 235000011803 sesame oil Nutrition 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 241000894007 species Species 0.000 description 1
- 238000009987 spinning Methods 0.000 description 1
- 150000003505 terpenes Chemical class 0.000 description 1
- 235000007586 terpenes Nutrition 0.000 description 1
- 238000004809 thin layer chromatography Methods 0.000 description 1
- 230000001988 toxicity Effects 0.000 description 1
- 231100000419 toxicity Toxicity 0.000 description 1
- 235000013311 vegetables Nutrition 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
- A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
- A23L33/115—Fatty acids or derivatives thereof; Fats or oils
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23L—FOODS, FOODSTUFFS, OR NON-ALCOHOLIC BEVERAGES, NOT COVERED BY SUBCLASSES A21D OR A23B-A23J; THEIR PREPARATION OR TREATMENT, e.g. COOKING, MODIFICATION OF NUTRITIVE QUALITIES, PHYSICAL TREATMENT; PRESERVATION OF FOODS OR FOODSTUFFS, IN GENERAL
- A23L33/00—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof
- A23L33/10—Modifying nutritive qualities of foods; Dietetic products; Preparation or treatment thereof using additives
- A23L33/105—Plant extracts, their artificial duplicates or their derivatives
-
- 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
- B01D36/00—Filter circuits or combinations of filters with other separating devices
- B01D36/04—Combinations of filters with settling tanks
-
- A—HUMAN NECESSITIES
- A23—FOODS OR FOODSTUFFS; TREATMENT THEREOF, NOT COVERED BY OTHER CLASSES
- A23V—INDEXING SCHEME RELATING TO FOODS, FOODSTUFFS OR NON-ALCOHOLIC BEVERAGES AND LACTIC OR PROPIONIC ACID BACTERIA USED IN FOODSTUFFS OR FOOD PREPARATION
- A23V2002/00—Food compositions, function of food ingredients or processes for food or foodstuffs
Abstract
The invention discloses a method for extracting and purifying hemp full-spectrum oil. Which comprises the following steps: 1. drying flowers and leaves in the sun, and coarsely crushing; 2. placing the coarsely crushed flowers and leaves into an oven for dry heat treatment; 3. pulverizing the obtained flower and leaf, and granulating; 4. extracting the obtained hemp grains in a subcritical extraction tank; 5. dissolving the concentrated extract with ethanol, and filtering; 6. concentrating the filtrate, adding silica gel, and stirring; 7. after the material glue is loaded into a pre-column, a reverse chromatographic column is used for separation; 8. concentrating and crystallizing the separated multi-spectrum oil section; 9. filtering the crystallization liquid by using a glass sand funnel, dissolving crystals obtained by filtering by using normal hexane, and extracting obtained filtrate by using normal hexane; 10. and combining the n-hexane dissolving solution and the extract, and concentrating to obtain the hemp full-spectrum oil concentrate. The method has the advantages of simple process, no tetrahydrocannabinol in the prepared hemp full-spectrum oil, low energy consumption, realization of recycling of the organic solvent, environment-friendly extraction and separation process and low toxicity.
Description
Technical Field
The invention belongs to the technical field of traditional Chinese medicine extraction processes, and particularly relates to a method for extracting and purifying full-spectrum oil of cannabis sativa.
Background
Industrial hemp (Stevia rebaudiana Bertoni) is an annual plant of the genus cannabis of the family cannabinaceae, widely distributed around the world. The Cannabis plants in the world are mainly 3 species of wild Cannabis sativa (Cannabis ruderalisisch), Indian Cannabis sativa (Cannabis indica Lam) and cultivated Cannabis sativa (Cannabis sativaL), and many Cannabis varieties and subspecies are generated in the long-term biological evolution process. Cannabis sativa contains Tetrahydrocannabinol (THC), a hallucinogenic secondary metabolite, and is one of the well-known drug-source plants. For convenience of supervision and reasonable use, the varieties of cannabis with THC content of less than 0.3% in cannabis are internationally defined as industrial cannabis which does not have drug utilization value. At present, 27 countries in the world grow industrial cannabis, and 26 industrial cannabis varieties with THC content of less than 0.3% are cultivated. The industrial hemp plants are tall and big, the branches are few, the fiber content is high, and the economic value of the industrial hemp plants relates to a plurality of aspects such as papermaking, spinning, building materials, food, medicine and the like. At present, more than one hundred Cannabinoids (CBs) are isolated from the plant cannabis sativa, mainly including Tetrahydrocannabinol (THC), Cannabidiol (CBD), Cannabinol (CBN), and cannabichromene (CBC), among which THC and CBD are the highest. Tetrahydrocannabinol (THC) has hallucinogenic addiction and limits the development of value in the medicinal field, the industrial hemp full-spectrum oil is extracted from industrial hemp, the main component cannabidiol is the main active component in cannabinoids, and the cannabidiol and the tetrahydrocannabinol have completely different active effects, are non-addictive active components and have no neurotoxicity. Has the function of protecting nerves, has no addiction, and has the functions of resisting epilepsy, spasm, rheumatic arthritis and anxiety, thereby attracting wide attention in the fields of medicine and pharmacology and becoming a research hotspot in recent years. The industrial hemp full-spectrum oil belongs to a fat-soluble mixture, components with hallucinogenic and addictive effects such as THC and the like are removed as much as possible, and a high-purity product is obtained, which is the premise for developing and applying the hemp full-spectrum oil.
Hemp oil has excellent skin affinity as a diluent for the hemp full spectrum oil, allowing rapid absorption of the hemp full spectrum oil, while also having its unique benefits. Hemp seed oil is the highest in all oils of monounsaturated and polyunsaturated fatty acids, with an average of 89%. Is the only water-soluble vegetable oil in the world at present. A polyunsaturated linoleic omega-6 fatty acid in sesame oil at a level of 55.6 g/100 g, a polyunsaturated alpha-linolenic acid mega-3 fatty acid at a level of 17.2 g/100 g. The ratio of the two fatty acids was 3.38, very close to the World Health Organization (WHO) recommended average ratio of 4.0. Hemp seed oil is an edible oil containing both linoleic acid and alpha-linolenic acid, the direct metabolites gamma-linolenic acid (GLA) and arachidic acid (SDA). Rich in unsaturated fatty acid (omega-3, omega-6, omega-9) and various active substances, and the ratio of omega-3, omega-6, omega-9 reaches the international recommended standard (omega-3: omega-6 is less than or equal to 1: 4); the unsaturated fatty acids omega-3, omega-6 and omega-9 have health promotion effects of preventing and adjuvant treating cardiovascular disease and cerebrovascular disease (hypertension, hyperlipemia and hyperglycemia); the hemp seed oil also has the effects of improving the excretion of organisms, removing wastes in the bodies, removing bad fat in the bodies, removing free radicals of cells, increasing the immunity of the organisms, regulating the internal environment of the human bodies, improving the sleep, delaying the aging and the like; meanwhile, the hemp seed oil is the only vegetable oil dissolved in water in the world and is more beneficial to the absorption of a human body.
The full spectrum (or broad spectrum) cannabis oil is a hemp flower leaf extract without further purification and separation, and contains Cannabidiol (CBD), Cannabinol (CBN), cannabichromene (CBC), Cannabigerol (CBG), Cannabidivarin (CBDV), and the like, and sometimes terpenes and aromatic compounds. The full spectrum CBD oils are generally more viscous, darker in color, and have the vegetable taste of china-hemp. Due to the medicinal value of Cannabidiol (CBD) and the medicinal expectations of Cannabinol (CBN), cannabichromene (CBC), Cannabigerol (CBG) and Cannabidivarin (CBDV), the extraction of full spectrum oil from cannabis sativa leaves has a wide market prospect.
Some reports about the hemp full-spectrum oil extraction method exist in the current published information, and the following problems are mainly found in the prior art by comparing and researching the existing process routes:
(1) the most used method in the existing cannabidiol extraction process is a solvent extraction method, one method is that a large amount of organic solvents with high cannabidiol solubility, such as n-hexane, petroleum ether, dichloromethane, chloroform, methanol and the like, are added, although the extraction rate of cannabidiol is improved, the use of the organic solvents can harm the environment, and the solvent residues in the final product cannot be removed completely, so that the safety of the product is also influenced; the other one is ethanol as an extractant, which reduces the toxicity of organic solvents, but has the problems of low extraction rate caused by low solubility of cannabidiol, large solvent recovery loss and high cost.
(2) The supercritical CO2 fluid extraction technology is applied to a cannabidiol extraction process in recent years, and although the supercritical extraction has the advantages of strong extraction capacity, high extraction rate, strong selectivity, good product quality and the like, the supercritical extraction also has the defects of high cost, high energy consumption, difficulty in realizing industrial scale-up production and the like.
Therefore, the method which has low cost and low energy consumption and is beneficial to industrial production needs to be provided at present. According to the principle of similarity and intermiscibility of organic matters, the extraction material and the extracting agent are subjected to molecular diffusion in the soaking process, so that fat-soluble components in the solid material are transferred to the liquid extracting agent, the extracting agent is separated from a target product through the process of reduced pressure evaporation, and the target product is finally obtained. The method has the advantages of no toxicity, harmlessness, environmental protection, no pollution, no hot processing, no damage and oxidation of active ingredients in the extract, high capacity, large-scale industrial production, energy conservation, low operation cost and easy separation of products; the invention not only protects the activity of the hemp full-spectrum oil, but also completely extracts the effective components in the hemp flower and leaf. In order to make full use of the full-spectrum hemp oil, the hemp full-spectrum oil is diluted by the hemp oil, so that the hemp full-spectrum oil is more beneficial to the absorption of a human body, and meanwhile, the hemp oil also has the health-care effects of preventing and assisting in treating cardiovascular and cerebrovascular diseases (hypertension, hyperlipidemia and hyperglycemia), improving the excretion of the human body, removing wastes in the body, removing bad fat in the body, removing cell free radicals and the like, and has the effects of increasing the immunity of the human body, regulating the internal environment of the human body, improving the sleep, delaying the aging and the like.
Disclosure of Invention
In order to completely extract the effective components in the hemp flowers and leaves and fully utilize the effective components, the invention adopts a subcritical fluid technology which is non-toxic, harmless, environment-friendly, pollution-free and non-thermal processing and a method for dissolving hemp multispectral oil by using hemp oil, so that the hemp full-spectrum oil is more beneficial to the absorption of a human body.
In order to achieve the purpose, the invention is realized by the following technical scheme:
1. pretreatment: the collected flower leaves are dried in the sun in situ, the leaf stalks are removed after the drying in the sun, and the crushed leaves are collected and crushed.
2. Dry heat treatment: spreading the coarsely crushed hemp flowers and leaves in a drying tray, and controlling the thickness to be 2-5 cm; the drying box is opened, the drying temperature is set at 100 ℃ and 150 ℃, and the drying time is 2-6 hours.
3. And (3) granulating: pulverizing the dried and heat treated flower and leaf into 40-100 mesh particles, adding 15-50% industrial ethanol, stirring, and standing for 10-40 min; starting the granulator, and making the flower and leaf into cylindrical granules with the diameter of 3-6mm and the length of 1-3 cm.
4. Subcritical extraction: putting hemp grains into an extraction tank, reducing pressure, adding n-butane, soaking, extracting for 2-5h at 25-40 deg.C for 2-3 times; the obtained extracting solution is roughly filtered by a filter screen of 100-mesh and 150-mesh, the obtained filtrate is kept stand and precipitated, and the supernatant is filtered by a filter screen of 200-mesh and 300-mesh; standing the obtained filtrate for precipitation, fine-filtering with a 300-400 mesh filter screen, heating the obtained filtrate (40-65 deg.C), and reducing pressure to obtain extract; and (3) cooling, compressing and recovering the n-butane.
5. Alcohol precipitation: adding ethanol at a ratio of 1:3-6 into the extract obtained by subcritical extraction, heating, stirring and dissolving; standing at normal temperature for 3-6 hr, filtering, and concentrating.
6. Mixing materials: pouring the concentrated extract into silica gel 4-7 times of the extract, starting a stirrer, setting the temperature at 60-80 deg.C, and stirring for 2-5 hr.
7. Column chromatography: loading the stirred gel material into a pre-column, preparing 30-60% ethanol/water eluent, and filling the column chromatography with macroporous resin.
8. Concentration: concentrating the separated multispectral oil segment until no ethanol is present.
9. And (3) extraction: adding n-hexane at a ratio of 1:2 into the obtained multispectral oil segment concentrated solution, extracting for 3 times, combining the extracts, concentrating, and draining to obtain multispectral oil, and performing vacuum rotary evaporation for 2-3 hours at a rotary evaporation temperature of 95-110 ℃.
10. Diluting and subpackaging: adding oleum Sesami into qualified multispectral oil at a ratio of 1:3-5, heating, mixing, standing, cooling, and packaging.
The invention has the beneficial effects that:
the method not only protects the active ingredients in the hemp multispectral oil from being damaged and oxidized, but also has the characteristics of complete extraction, easy product separation, large material input, energy conservation, low operation cost and the like; the prepared hemp full-spectrum oil is quickly absorbed by human body, has obvious effect and simultaneously has the unique health-care function of the hemp oil.
Detailed Description
In order to make the technical means, the creation characteristics, the achievement purposes and the effects of the invention easy to understand, the invention is further described with the specific embodiments.
The specific implementation mode adopts the following technical scheme:
1. pretreatment: drying a certain amount of collected flowers and leaves in the sun on the spot until the moisture content is lower than 12%; and (4) drying in the sun, removing leaf stalks by using a self-made leaf removing machine, collecting crushed leaves, and coarsely crushing the obtained crushed leaves by using a crusher.
2. Dry heat treatment: collecting coarse hemp flower and leaf, spreading in 40 × 60cm drying plate with thickness of 2 cm; the drying oven was opened, the drying temperature was set at 110 ℃ and dried for 4 hours.
3. And (3) granulating: mixing the dried and heat treated leaves, pulverizing into 80 mesh particles, adding the pulverized particles into a mixing pot, adding 40% industrial ethanol, stirring for 5 min, and standing for 30 min; starting a granulator, and preparing the uniformly stirred hemp flower and leaf granules into cylindrical granules with the diameter of 4mm and the length of 1.5 cm; the prepared granules are poured into a drying bed to remove ethanol, and the obtained dried granules are screened by a 10-mesh screen to remove crushed powder.
4. Subcritical extraction: putting 20kg of hemp grains into an extraction tank, reducing pressure, adding n-butane for soaking, extracting for 2h at 30 ℃, and extracting for 2 times; coarsely filtering the obtained extractive solution with 100 mesh filter, standing the obtained filtrate for precipitation for 24 hr, and filtering the supernatant with 200 mesh filter screen; standing the obtained filtrate for precipitation for 24h, fine-filtering with a 300-mesh filter screen, heating the obtained filtrate to 45 ℃, and concentrating under reduced pressure to obtain 1.7kg of extract; and (3) cooling, compressing and recovering the n-butane.
5. Alcohol precipitation: putting the obtained extract into a 20L rotary evaporator, adding 10L industrial ethanol, heating to 70 deg.C, and dissolving for 1 h; after completely dissolving, standing at normal temperature for 6 hours, filtering with rapid filter paper, dissolving the filter residue with 5L industrial ethanol under heating for 0.5 hour, standing at normal temperature for 6 hours, mixing the filtrates, and concentrating to 2L.
6. Mixing materials: starting a small-sized mixer, adding 12kg of silica gel according to the obtained extract amount, pouring the concentrated hot-dipping paste into the mixer, setting the temperature at 70 ℃, and starting vacuum stirring for 5 hours.
7. Column chromatography: and (3) filling the stirred gel into a pre-column, knocking and jolting, firstly using 5 column volumes of ethanol water solution (30%) to pass through the column, collecting the front impurities, then using 52% (ethanol/water) eluent to elute, and judging and collecting according to thin-layer chromatography.
8. Concentration: the multispectral oil fractions obtained by separation are combined and concentrated in vacuum by a rotary evaporator until no ethanol is available.
9. And (3) extraction: pouring the obtained multi-spectrum oil-segment concentrated solution into an extraction tank, adding twice of n-hexane for extraction for three times, combining the extracts, concentrating and pumping the combined extracts by using a rotary evaporator, and carrying out rotary evaporation at the temperature of 95 ℃.
10. Diluting and subpackaging: detecting the dried multispectral oil, adding 5 times of edible oleum Sesami, heating, stirring, standing, cooling, and packaging.
The prepared hemp full-spectrum oil content meter is as follows:
the multispectral oil obtained in the experiment has comprehensive components and extremely low impurity content, the extraction and purification process has the advantages of complete extraction, large extraction amount, complete separation, greenness, no residue and the like, and the process method is very suitable for mass production.
The foregoing shows and describes the general principles and features of the present invention, together with the advantages thereof. It will be understood by those skilled in the art that the present invention is not limited to the embodiments described above, which are described in the specification and illustrated only to illustrate the principle of the present invention, but that various changes and modifications may be made therein without departing from the spirit and scope of the present invention, which fall within the scope of the invention as claimed. The scope of the invention is defined by the appended claims and equivalents thereof.
Claims (9)
1. A method for extracting and purifying hemp full-spectrum oil is characterized by comprising the following steps:
step 1, pretreatment: drying the collected flower leaves in the sun, removing leaf stalks after drying in the sun, and collecting crushed leaves and coarse crushing;
step 2, dry heat treatment: spreading the coarsely crushed hemp flowers and leaves in a drying tray, and drying at high temperature;
step 3, granulating: pulverizing the dried and heat treated leaves to obtain cylindrical granules;
step 4, subcritical extraction: putting hemp grains into an extraction tank, reducing pressure, adding n-butane for soaking, and extracting for 2-3 times;
and 5, alcohol precipitation: adding ethanol into the extract obtained by subcritical extraction, heating, stirring for dissolving, filtering, and concentrating;
step 6, stirring materials: pouring the concentrated extract into silica gel, and stirring to obtain uniform material gel;
and 7, column chromatography: macroporous resin is used as filler, and ethanol/water is used for elution;
step 8, concentration: concentrating the separated multispectral oil segment until no ethanol exists;
and 9, extraction: extracting the obtained multi-spectrum oil section concentrated solution by using normal hexane, concentrating and pumping;
step 10, diluting and subpackaging: dissolving the obtained multispectral oil with oleum Sesami, diluting, and packaging.
2. The method for extracting and purifying cannabis full spectrum oil according to claim 1, wherein the method comprises the following steps: the water content of the hemp flowers and leaves in the step 1 is controlled below 10% after being aired, and the particles after coarse crushing are controlled to be about 20 meshes.
3. The method for extracting and purifying cannabis full spectrum oil according to claim 1, wherein the method comprises the following steps: in the step 2, the hemp flowers and leaves are flatly paved in a drying disc, and the thickness is controlled to be 2-5 cm; the drying temperature is 100 ℃ and 150 ℃, and the drying time is 2-6 hours.
4. The method for extracting and purifying cannabis full spectrum oil according to claim 1, wherein the method comprises the following steps: crushing the flowers and leaves subjected to the dry heat treatment in the step 3 into 40-100 mesh particles, adding 15-50% of industrial ethanol, uniformly stirring, and standing for 10-40 min; making into cylindrical granule with diameter of 3-6mm and length of 1-3 cm.
5. The method for extracting and purifying cannabis full spectrum oil according to claim 1, wherein the method comprises the following steps: adding ethanol with the weight ratio of 1:3-6 into the extract obtained by subcritical extraction in the step 5, heating, stirring and dissolving; standing at normal temperature for 3-6 hr, filtering, and concentrating.
6. The method for extracting and purifying cannabis full spectrum oil according to claim 1, wherein the method comprises the following steps: pouring the extract liquid obtained by concentration in the step 6 into silica gel, wherein the using amount of the silica gel is 4-7 times of that of the extract, stirring at the temperature of 60-80 ℃, and stirring for 2-5 hours.
7. The method for extracting and purifying cannabis full spectrum oil according to claim 1, wherein the method comprises the following steps: the column chromatography packing in the step 7 is macroporous resin, and the eluent is 30-60% ethanol/water.
8. The method for extracting and purifying cannabis full spectrum oil according to claim 1, wherein the method comprises the following steps: and (3) adding n-hexane with the ratio of 1:2 into the multispectral oil section concentrated solution obtained in the step (9) for extraction for 3 times, combining the extract solutions, concentrating and pumping to dryness, and performing vacuum rotary evaporation on the obtained multispectral oil for 2-3 hours at the rotary evaporation temperature of 95-110 ℃.
9. The method for extracting and purifying cannabis full spectrum oil according to claim 1, wherein the method comprises the following steps: and (3) adding the cannabis oil into the qualified multispectral oil detected in the step 10 according to the proportion of 1:3-5, heating and mixing uniformly, standing, cooling and packaging.
Priority Applications (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201911060515.XA CN110786513A (en) | 2019-11-01 | 2019-11-01 | Method for extracting and purifying hemp full spectrum oil |
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
CN201911060515.XA CN110786513A (en) | 2019-11-01 | 2019-11-01 | Method for extracting and purifying hemp full spectrum oil |
Publications (1)
Publication Number | Publication Date |
---|---|
CN110786513A true CN110786513A (en) | 2020-02-14 |
Family
ID=69442480
Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
---|---|---|---|
CN201911060515.XA Withdrawn CN110786513A (en) | 2019-11-01 | 2019-11-01 | Method for extracting and purifying hemp full spectrum oil |
Country Status (1)
Country | Link |
---|---|
CN (1) | CN110786513A (en) |
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112011399A (en) * | 2020-08-21 | 2020-12-01 | 滇麻生物科技(曲靖)有限公司 | Method for preparing polyphenol resin oil from industrial hemp |
CN112206703A (en) * | 2020-09-29 | 2021-01-12 | 哈尔滨市汉博生物科技有限公司 | Pretreatment method before supercritical extraction of industrial hemp flowers and leaves |
-
2019
- 2019-11-01 CN CN201911060515.XA patent/CN110786513A/en not_active Withdrawn
Cited By (2)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN112011399A (en) * | 2020-08-21 | 2020-12-01 | 滇麻生物科技(曲靖)有限公司 | Method for preparing polyphenol resin oil from industrial hemp |
CN112206703A (en) * | 2020-09-29 | 2021-01-12 | 哈尔滨市汉博生物科技有限公司 | Pretreatment method before supercritical extraction of industrial hemp flowers and leaves |
Similar Documents
Publication | Publication Date | Title |
---|---|---|
CN110304994B (en) | Method for extracting high-purity cannabidiol from industrial cannabis sativa | |
CN102250195B (en) | Method for producing xanthoceraside | |
CN102106931B (en) | Method for producing diverse extracts of berry tea | |
CN108929201A (en) | A kind of method that Subcritical Water Extraction technology extracts cannabidiol | |
CN109646992B (en) | Method for extracting cannabidiol concentrate from industrial cannabis sativa | |
CN101463027B (en) | Method for extracting and separating flavone and anthocyanidin from elder fruit | |
CN111099970A (en) | Method for industrially extracting cannabidiol from industrial cannabis sativa | |
CN104710391A (en) | Method for extracting luteolin and beta-sitosterol from peanut shells | |
CN111285916A (en) | Preparation method of centella asiatica extract with high content of total asiaticosides | |
CN110786513A (en) | Method for extracting and purifying hemp full spectrum oil | |
CN101982471B (en) | Technological process for extracting aucubin from fruits of eucommia ulmoides oliver | |
CN111393400B (en) | Method for preparing squalene, vitamin E and sterol from fructus momordicae seed kernels | |
CN111116323A (en) | Microwave-assisted subcritical technology for extracting cannabidiol and preparation method thereof | |
CN113754518A (en) | Method for efficiently purifying cannabidiol from industrial cannabis sativa leaves | |
CN112723997A (en) | Green process for extracting high-purity bakuchiol | |
CN110776534B (en) | Efficient extraction system and extraction method of elsholtzia alkaloid | |
CN109320569A (en) | A method of extracting high-purity baicalin from radix scutellariae | |
CN107892688A (en) | A kind of method that Berberine hydrochloride is prepared from golden cypress | |
CN110922413A (en) | Extraction and separation method of glabridin | |
CN106317005B (en) | Method for extracting rose flavone from rose dreg water | |
CN101306027B (en) | Extracting method of medical mangrove acanthus total flavonoids | |
CN111138404A (en) | Cannabis sativa root extract and preparation method thereof | |
CN104606264A (en) | Extraction method of sterculia nobilis polyphenol | |
CN102648939A (en) | Preparation method for geum aleppicum polyphenol | |
CN111848356A (en) | Preparation method of cannabidiol |
Legal Events
Date | Code | Title | Description |
---|---|---|---|
PB01 | Publication | ||
PB01 | Publication | ||
SE01 | Entry into force of request for substantive examination | ||
SE01 | Entry into force of request for substantive examination | ||
WW01 | Invention patent application withdrawn after publication | ||
WW01 | Invention patent application withdrawn after publication |
Application publication date: 20200214 |