CN103468403A - Method for extracting tobacco aroma substance from tobacco raw materials in directional and combined manner by using water extraction method and supercritical CO2 extraction method - Google Patents
Method for extracting tobacco aroma substance from tobacco raw materials in directional and combined manner by using water extraction method and supercritical CO2 extraction method Download PDFInfo
- Publication number
- CN103468403A CN103468403A CN2013104290649A CN201310429064A CN103468403A CN 103468403 A CN103468403 A CN 103468403A CN 2013104290649 A CN2013104290649 A CN 2013104290649A CN 201310429064 A CN201310429064 A CN 201310429064A CN 103468403 A CN103468403 A CN 103468403A
- Authority
- CN
- China
- Prior art keywords
- tobacco
- extraction
- supercritical
- aroma
- extracting
- 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.)
- Granted
Links
Images
Landscapes
- Manufacture Of Tobacco Products (AREA)
Abstract
The invention relates to a method for extracting a tobacco aroma substance from tobacco raw materials in a directional and combined manner by using a water extraction method and a supercritical CO2 extraction method. The method comprises the steps of (1) directionally extracting a polar aroma substance from tobacco by the water extraction method; (2) directionally extracting a nonpolar aroma substance from the tobacco by the supercritical CO2 extraction method; (3) mixing the polar aroma substance and the nonpolar aroma substance, wherein the proportioning ratio of the polar aroma substance to the nonpolar aroma substance is 1000: (0.1-5). According to the method, the used tobacco raw materials are tobacco leaves, cut tobaccos or wastes, such as tobacco powder, tobacco ash or tobacco stems of tiny grains, generated during tobacco processing, so that the waste is changed into the valuable, and the pollution to the environment is reduced; a water extraction tobacco concentrate and a supercritical CO2 tobacco extract are mixed in an appropriate ratio, and a composite aroma material is sprayed to reconstituted tobacco, so that the quality of the reconstituted tobacco is improved, the aroma amount is increased, the aroma charm is improved, the natural tobacco aroma is set off, the smoke dryness is lowered, the smoke-induced saliva secretion feeling is enhanced, and the degree of comfort of cigarette is increased.
Description
Technical field
The present invention relates to Field of Tobacco, relate in particular to a directed composite extracting method that grows tobacco this Studies of The Aromatic Substances of endogenous.
Background technology
Chemical composition in tobacco is numerous.Since 20 century 70s, due to the development of analysis and testing technology, the chemical composition in tobacco constantly is found.Shi Hongzhi etc. 2011 report, in the tobacco leaf through identifying, chemical composition has 4992 kinds, and wherein relevant to tobacco flavor have more than 700 kinds.In tobacco, in the molecule of flavor matter, contain-OH ,-CO ,-NH and-SH etc. is specific causes fragrant functional group, with different irritating, produces different fragrance can to people's sense of smell.According to the difference of fragrance matter functional group, tobacco flavor material can be divided into alcohols, acids, ketone, ester class and terpene etc.Mostly tobacco flavor material is secondary metabolite, therefore also can be divided into according to fragrance precursor substance in secondary metabolism the classifications such as carotenoid, phenylalanine degradation product, the western cypress alkanes of class degradation product, mailland reaction product.
Can produce the approximately tankage such as waster tobacco of 25 % in the Bian of tobacco receipts and production process can not use, and is regarded refuse treatment more, also causes the significant wastage of natural resources when to environment, bringing pollution.The recent domestic that utilizes for tankage such as waster tobaccos has risen the reconstituted tobacco method.Reconstituted tobacco, be called again tobacco sheet, it is that to utilize discarded offal, tobacco leaf fragment, offal etc. be raw material, through lixiviate, concentrated, separation, making beating, defibrination, manufacture paper with pulp, oven dry, perfuming process process, make the reconstituted tobacco thin slice of excellent property, as the cigarette weighting material, be back to production of cigarettes.
Reconstituted tobacco can lose a part of this Studies of The Aromatic Substances of tobacco in the course of processing, and needing to add a certain amount of tobacco endogenous spices increase reconstituted tobacco fragrance fragrance, improves smoke, reduces xylon gas and pungent sense.The crucial aroma component that contains organic acid, alcohols, carbonyl class, phenols, terpenes, carbohydrate, amino acids in the tobaccos such as neophytadiene, nicotine, solanone, trans-Damascenone, geranyl acetone, Megastigmatrienone, alpha, beta-lonone, phenyl aldehyde, phenylcarbinol, dihydroactinidiolide in waster tobacco, illustrate in waster tobacco and contain the important aroma component of a large amount of tobaccos, can be used as the source of tobacco flavour.
Have at present the waster tobacco water is extracted, concentrates, water extracting liquid is added in reconstituted tobacco to the fragrance fragrance that improves reconstituted tobacco.It is water that water extraction is used solvent, leaching process good economy performance, safe, strong operability, and the water-soluble flavor matters such as carbohydrate, amino acids, phenols in tobacco leaf are had to extraction effect preferably, can improve the fragrance of reconstituted tobacco.But in tobacco, exist the crucial aroma components such as a large amount of low polarity, volatile organic acid, terpenes, alcohols to adopt its extraction effect of water extraction often poor, and in extraction, concentration process, volatile aroma component may destroy and lose, and still there is the shortcoming of fragrance deficiency in the reconstituted tobacco that only adds water extracting liquid.
Supercritical liquid extraction technique has the incomparable high purity of traditional extraction process, All Pure Nature, no solvent residue and the characteristics such as pollution-free, has been widely used in now the essential oil and the spices that extract in tobacco.In volatile aromatic composition in tobacco, be nonpolar mostly or the low-pole compound, at supercritical CO
2in solubleness very large, thereby be particularly suitable for adopting supercritical CO
2extract.Use supercritical CO
2abstraction technique is the extracted tobacco aroma component from tobacco, the important aroma component contained in the aroma component that extraction obtains all obtains much bigger on composition or relative percentage composition than traditional solvent extration extraction, this essential oil is used for to the assorted gas that perfuming cigarette can obviously change the fragrance of tobacco and suppress tobacco.Adopt gas chromatograph and GC-MS to supercritical CO
2the product that obtains of extraction is analyzed, and finds to be mainly wherein nonpolar and the low-pole compound, and has comprised the aroma component that many important and suction flavors cigarette have substantial connection.
Document and patent report in the tobacco leaf the main extracting method of aroma component water extraction, alcohol extracting method, supercritical extraction, molecular distillation method etc. are arranged.Its document and Patent are as follows:
LI XUEMEIs etc. utilize supercritical CO
2extract tobacco cleaned oil from oriental tobacco leaf concrete, determined that best extractant condition is 40～45 ℃ of extraction temperature, extracting pressure is 25～30 MPa, CO
2flow 2～4 L/min, extraction time 3～5 h, add certain the solvent mixture of 4%～8% (volume ratio) as entrainment agent in extraction, can obtain being equivalent to the Turkish tobaccos absolute oil of the thick cream amount 8%～10% of raw material, experimental result also shows that entrainment agent is a vital factor of extracted tobacco absolute oil.
Zhu Renfa etc. point out in order to extract targetedly required essential oil, can add the entrainment agents such as ethyl acetate to reduce CO
2solvability, improve its selectivity, and then improve the percentage extraction of essential oil.
Chinese patent (201010131371.5) " a kind of extracting method of neutral aroma compositions in tobacco ".It is characterized in that, the tobacco after pulverizing is packed in supercritical extraction reactor, then pour supercritical CO
2fluid pressurized circulation, regulate extracting pressure 8～30MPa, 35～60 ℃ of temperature, and extraction time is 1～3 hour, solution after the tobacco extraction is carried out to two-stage decompression separation, entrainment agent is ethanol, the filler that the flash trapping stage still is filled is zeolite, the 4A molecular sieve, the mixture of ion exchange resin, the pressure of flash trapping stage still is 10～20MPa, temperature is 35～55 ℃, the pressure of the second-order separation still is 4～6MPa, temperature is 35～45 ℃, obtain neutral aroma compositions in tobacco after separation, it is apolar substance that this extracting method obtains this Studies of The Aromatic Substances, composition is comparatively single, can't reach the Production requirement of banana aldehyde and reconstituted tobacco, the plyability feature that simultaneously single technology can't complete embodiment person's character material.
Chinese patent (201110248504.1) " method that tobacco is extracted continuously ".This patent characteristic is that tobacco powder is broken into particle diameter and is no less than 20 purpose powder, add and be equivalent to tobacco volume 10-30 water medium doubly, regulate the pH value to 9-13, and carry out ultrasonic pretreatment, ultrasonic power is no less than 20kHz, the ultrasonic pretreatment time is no less than 20 minutes, obtains ultrasonic pretreatment liquid, more further extraction nicotine, hemicellulose, xylogen, Mierocrystalline cellulose.Although the method extracting substance is comparatively thorough, but operation is comparatively complicated, more assorted this Studies of The Aromatic Substances that is not suitable for reconstituted tobacco of extracting substance adds, and the introducing of more material simultaneously can destroy the fragrance of tobacco equally, and abstraction process is single, this Studies of The Aromatic Substances extracts the specificity shortcoming.
Chinese patent (201110183851.0) " a kind of preparation method of tobacco extract granules ".The preparation method who it is characterized in that a kind of tobacco extract granules, first get tobacco leaf and/or offal and by its chopping, water or ethanol or ether are solvent extraction, obtain tobacco extract through sedimentation and filtration, reconcentration is to relative density 1.00-1.30 and to control temperature be 20～40 ℃, obtains tobacco and extracts concentrated solution or tobacco extract, then β-cyclodextrin in mass ratio: flavouring essence for tobacco is 1～3:1, flavouring essence for tobacco and β-cyclodextrin are carried out to inclusion, the inclusion time is 1/5～3 hour, obtain spices and Benexate Hydrochloride, again spices and Benexate Hydrochloride and tobacco are extracted to the common spraying drying of concentrated solution and obtain the tobacco spray-drying powder, be added into subsequently in cigarette to increase tobacco flavor, this has invented single employing water, alcohol or ether are as extracting reagent, yet the beta-cyclodextrin of follow-up interpolation is the parent of the dried particles moulding of just auxiliary person's character material only, lack the mediation of nonpolar person's character material, it is not obvious that thereby the mouthfeel aspect of tobacco promotes.
Chinese patent (200910027400) " a kind of preparation method of tobacco extract and application thereof ".The preparation method of described tobacco extract, take tobacco as raw material, through enzymolysis, ultrasonic extraction, filtration, chromatography column separation, concentrating under reduced pressure step, makes tobacco extract; The dissolve with ethanol of concentration 80% for described tobacco extract, adopt the atomizing type spray to be added in pipe tobacco.The comparatively loaded down with trivial details very difficult large-scale industrial production of this invention step, and the spices that extracts of single mode becomes singlely, can not well meet the mouthfeel demand of reproducing pipe tobacco.
Chinese patent (201210412334.0) " a kind of preparation method of tobacco cleaned oil ".Get evenly rear dress people extraction kettle of the thick extracted extract of 70g Turkish tobaccos and chemical filler mix, carry out supercritical extraction, extraction temperature 40-45 ℃, pressure 25-30MPa are squeezed into and are added 4-8% (volume ratio) entrainment agent when squeezing into flow velocity and be about the supercritical CO 2 of 2-5L/min; After reaching extraction conditions, extraction time 3-5h, obtain.Chemical filler can be the porcelain fillers such as granulated glass sphere, Raschig ring or rectangular saddle ring.
Summary of the invention
In order to solve above-mentioned technical problem, the object of the invention is to provide a kind of water extraction and supercritical CO
2extraction process method of flavor matter in directed compound extraction tobacco from tobacco material.It is simple that the method has technique, cost is low, this Studies of The Aromatic Substances good selective, with the obvious advantage aspect the reduction of the fragrance of reconstituted tobacco and lifting, compare single extraction and add this Studies of The Aromatic Substances technology, the present invention can solve the defects such as suction flavor discomfort, harsh feeling and dry sensation of reconstituted tobacco, greatly promotes the mouthfeel of reconstituted tobacco.。
The present invention for achieving the above object, adopts following technical scheme:
A kind of water extraction and supercritical CO
2extraction process method of flavor matter in directed compound extraction tobacco from tobacco material, the method comprises the following steps:
1) water extraction directed polarity flavor matter that extracts from tobacco
Tobacco material extracts 0.5～2 hour with 30～70 ℃ of 3～9 times of water gagings, extracts 1～3 time; It is 1.1～1.3mg/mL that extracting solution is concentrated into density;
2) SCF-CO 2 method nonpolar flavor matter of directed extraction from tobacco
Extraction conditions is that extraction kettle pressure is 20～30MPa, and extraction temperature is 35～45 ℃, extraction time 2～4 hours, and separation condition is that separating still pressure is 5～10 MPa, separation temperature is 35～50 ℃;
3) above-mentioned polarity flavor matter and nonpolar flavor matter are mixed, formula rate is 1000: 0.1～5.
As preferably, the formula rate of described polarity flavor matter and nonpolar flavor matter is 1000: 2～3.
As preferably, described tobacco material is one or more mixing in offal, cigarette ash, tobacco fragment, offal or other tobacco wastes that the particle that produces in tobacco leaf, pipe tobacco or tobacco processing course is tiny.
The present invention is that the modulation to reconstituted tobacco and tobacco extract thereof is mainly manifested on some not enough composition and carries out suitable supplementing, and total and natural baccy has gap for the modulation way of this fragrant component of tobacco.The present invention is by a kind of employing water extraction and supercritical CO
2extraction process is method and the application in the tobacco product perfuming thereof of endogenous flavor matter in directed compound extraction tobacco from tobacco, comprises and adopts water extraction directed polarity flavor matter and supercritical CO of extracting from tobacco
2extraction process is the directed composite extracting method that extracts nonpolar flavor matter from tobacco, according to a certain percentage polarity flavor matter and nonpolar flavor matter are allocated again, then its composite spices that causes is added in the tobacco products such as reconstituted tobacco, promote the quality of the tobacco products such as reconstituted tobacco, increase perfume quantity, carry and raise note, set off nature cigarette perfume (or spice), reduce the flue gas drying sense, strengthen flue gas promote the production of body fluid sense, raising cigarette comfort level, reach the purpose of flavouring humectation.
The present invention has following beneficial effect:
1. tobacco material used herein is tiny offal, cigarette ash or the offal the like waste of particle produced in tobacco leaf, pipe tobacco or tobacco processing course, and " turning waste into wealth " reduced the pollution to environment;
2. the present invention is by water extraction and supercritical CO
2the method of the directed compound extraction flavor matter of extraction process, the directed tobacco endogenous flavor matter that extracts from tobacco compoundly;
3. the present invention passes through tobacco water extracting liquid and tobacco supercritical CO
2extract carries out suitably, than allotment, its composite spices that causes being sprayed in reconstituted tobacco, promotes the quality of reconstituted tobacco, increases perfume quantity, carries and raise note, set off nature cigarette perfume (or spice), reduces the flue gas drying sense, strengthens flue gas promote the production of body fluid sense, raising cigarette comfort level.
The accompanying drawing explanation
Fig. 1 is supercritical CO
2extract GC-MS analysis chart.
Fig. 2 is water extracting liquid GC-MS analysis chart.
Embodiment
As previously mentioned, according to the disclosed content in front, one of skill in the art can apply the present invention to greatest extent.It should be pointed out that the present invention aims to provide the directed composite extracting method of middle flavor matter and uses thereof that grows tobacco.Following embodiment partly provide be enough to confirm described tobacco in after the directed composite extracting method and uses thereof of flavor matter, those skilled in the art are according to the routine techniques of perfuming cigarette purposes, can expect the directed composite extracting method of flavor matter in tobacco of the present invention fully can be used in above-mentioned field and can realize expectation function, therefore the following examples can help the present invention of those skilled in the art's comprehend, but do not limit the present invention in any way.
embodiment 1:
Get useless time cigarette ash 40kg and stir and extract 1 hour with 40 ℃, 280L water, filter, it is 1.2g/mL that extracting solution is concentrated into density, gets water extracting liquid 10000 g, is added in 10 kg reconstituted tobacco substrates, in contrast sample sets.
embodiment 2:
Get useless time cigarette ash 40kg and stir and extract 1 hour with 50 ℃, 200L water, filter, it is 1.2g/mL that extracting solution is concentrated into density, and water extracting liquid is standby; Get waster tobacco 3kg supercritical CO
2extracted, extraction conditions is that extraction kettle pressure is 25MPa, and extraction temperature is 40 ℃, CO
2flow is 200L/ hour, and extraction time is 4 hours; Separating still pressure is 5 MPa, and separation temperature is 45 ℃, obtains the 115g extract after extraction; Get water extracting liquid 10000 g and supercritical CO
2extract 30 g, both are added into after mixing in 10 kg reconstituted tobacco substrates, by the sensory evaluating smoking, compare fragrance texture, perfume quantity with the control sample group and all promote to some extent than control sample, tobacco aroma performance more clear, more naturally.Stimulation, clean level slightly descend, and it is good that moisture feeling keeps.
embodiment 3:
Get useless time cigarette ash 40kg and stir and extract 1 hour with 40 ℃, 200L water, extract 2 times, filter, it is 1.1g/mL that extracting solution is concentrated into density, and water extracting liquid is standby; Get useless time cigarette ash 6kg supercritical CO
2extracted, extraction conditions is that extraction kettle pressure is 20MPa, and extraction temperature is 35 ℃, CO
2flow is 180L/ hour, and extraction time is 3 hours; Separating still pressure is 5.5 MPa, and separation temperature is 40 ℃, obtains the 265g extract after extraction; Get water extracting liquid 10000 g and supercritical CO
2extract 20 g, both are added into after mixing in 10 kg reconstituted tobacco substrates, pass through the sensory evaluating smoking, compare fragrance texture, perfume quantity with the control sample group than all liftings to some extent of control sample, cigarette perfume (or spice) sends out more thoroughly, fuller, some manifests sweet sense, stimulates, clean level slightly descends.
embodiment 4:
Get useless time cigarette ash 30kg and stir and extract 1 hour with 70 ℃, 210L water, extract 2 times, filter, it is 1.2g/mL that extracting solution is concentrated into density, gets the 10kg offal and extracts 1 hour with 70 ℃, 45L water, filters, it is 1.22g/mL that extracting solution is concentrated into density, then by cigarette ash and offal concentrated solution, merges standby; Get useless time cigarette ash 7kg supercritical CO
2extracted, extraction conditions is that extraction kettle pressure is 30MPa, and extraction temperature is 45 ℃, CO
2flow is 180L/ hour, and extraction time is 3.5 hours; Separating still pressure is 6.5 MPa, and separation temperature is 45 ℃, obtains the 315g extract after extraction; Get cigarette ash and offal water extracting liquid 10000 g and supercritical CO
2extract 50 g, both are added into after mixing in 10 kg reconstituted tobacco substrates, pass through the sensory evaluating smoking, compare fragrance texture, perfume quantity with the control sample group than all liftings to some extent of control sample, cigarette perfume (or spice) sends out more thoroughly, fuller, some manifests sweet sense, stimulates, clean level slightly descends.
embodiment 5:
Get waster tobacco 40kg and stir and extract 2 hours with 60 ℃, 320L water, extract 2 times, filter, it is 1.2g/mL that extracting solution is concentrated into density, and concentrated solution is standby; Get waster tobacco 4kg supercritical CO
2extracted, extraction conditions is that extraction kettle pressure is 25MPa, and extraction temperature is 40 ℃, CO
2flow is 180L/ hour, and extraction time is 4 hours; Separating still pressure is 5.5 MPa, and separation temperature is 35 ℃, obtains the 215g extract after extraction; Get cigarette ash and offal water extracting liquid 10000 g and supercritical CO
2extract 40 g, both are added into after mixing in 10 kg reconstituted tobacco substrates, pass through the sensory evaluating smoking, compare fragrance texture, perfume quantity with the control sample group than all obviously liftings of control sample, cigarette perfume (or spice) sends out more thoroughly, fuller, sweet sense is more remarkable, stimulates, clean level descends.
embodiment 6:
Supercritical CO
2extract GC-MS analyzes: get 2mL sample and 4mL dichloromethane extraction, and vibration, ultrasonic, stratification, take off the stillness of night, and 5000rpm is centrifugal, and membrane filtration is got the 1ml sample introduction.Instrument: Agilent GC/MS, its gas chromatogram as shown in Figure 1.
In the supercritical extraction sample, aroma component content is as following table:
Contain a large amount of tobacco flavor matters in supercritical extract, wherein the component contents such as organic acid, ketone, ester class, alcohols are higher.
embodiment 7:
Water extracting liquid GC-MS analyzes: get 2mL sample and 4mL dichloromethane extraction, and vibration, ultrasonic, stratification, take off the stillness of night, and 5000rpm is centrifugal, and membrane filtration is got the 1ml sample introduction.Instrument: Agilent GC/MS, its gas chromatogram is as Fig. 2.From the GC-MS collection of illustrative plates, in water extracting liquid, volatile aroma component content is extremely low.
Claims (3)
1. a water extraction and supercritical CO
2extraction process method of flavor matter in directed compound extraction tobacco from tobacco material, is characterized in that the method comprises the following steps:
1) water extraction directed polarity flavor matter that extracts from tobacco
Tobacco material extracts 0.5 ~ 2 hour with 30 ~ 70 ℃ of 3 ~ 9 times of water gagings, extracts 1 ~ 3 time; It is 1.1 ~ 1.3mg/mL that extracting solution is concentrated into density;
2) supercritical CO
2extraction process is the nonpolar flavor matter of directed extraction from tobacco
Extraction conditions is that extraction kettle pressure is 20 ~ 30MPa, and extraction temperature is 35 ~ 45 ℃, extraction time 2 ~ 4 hours, and separation condition is that separating still pressure is 5 ~ 10 MPa, separation temperature is 35 ~ 50 ℃;
3) above-mentioned polarity flavor matter and nonpolar flavor matter are mixed, formula rate is 1000: 0.1 ~ 5.
2. a kind of water extraction according to claim 1 and supercritical CO
2extraction process method of flavor matter in directed compound extraction tobacco from tobacco material, it is characterized in that: the formula rate of polarity flavor matter and nonpolar flavor matter is 1000: 2 ~ 3.
3. a kind of water extraction according to claim 1 and supercritical CO
2extraction process method of flavor matter in directed compound extraction tobacco from tobacco material is characterized in that: tobacco material is one or more mixing in offal, cigarette ash, tobacco fragment, offal or other tobacco wastes that the particle that produces in tobacco leaf, pipe tobacco or tobacco processing course is tiny.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310429064.9A CN103468403B (en) | 2013-09-18 | 2013-09-18 | A kind of water extraction and supercritical CO 2extraction process method of flavor matter in directed compound collecting tobacco from tobacco material |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201310429064.9A CN103468403B (en) | 2013-09-18 | 2013-09-18 | A kind of water extraction and supercritical CO 2extraction process method of flavor matter in directed compound collecting tobacco from tobacco material |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN103468403A true CN103468403A (en) | 2013-12-25 |
| CN103468403B CN103468403B (en) | 2016-01-27 |
Family
ID=49793448
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201310429064.9A Active CN103468403B (en) | 2013-09-18 | 2013-09-18 | A kind of water extraction and supercritical CO 2extraction process method of flavor matter in directed compound collecting tobacco from tobacco material |
Country Status (1)
| Country | Link |
|---|---|
| CN (1) | CN103468403B (en) |
Cited By (11)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104000302A (en) * | 2014-06-17 | 2014-08-27 | 云南中烟工业有限责任公司 | Electronic cigarette liquid and quality detecting method thereof |
| CN104450186A (en) * | 2014-10-29 | 2015-03-25 | 山东中烟工业有限责任公司 | Method for preparing tobacco herbal fragrant substance for cigarette solution of electronic cigarette |
| CN104585863A (en) * | 2015-01-20 | 2015-05-06 | 川渝中烟工业有限责任公司 | Electronic cigarette juice |
| CN106124679A (en) * | 2016-07-06 | 2016-11-16 | 云南中烟工业有限责任公司 | One assay method growing tobacco middle group compounds of aldehydes and ketones |
| WO2020002585A1 (en) | 2018-06-29 | 2020-01-02 | Nerudia Limited | A method for manufacturing reconstituted plant material |
| WO2020002589A1 (en) | 2018-06-29 | 2020-01-02 | Nerudia Limited | A method for manufacturing reconstituted plant material |
| WO2020002583A1 (en) | 2018-06-29 | 2020-01-02 | Nerudia Limited | A method for manufacturing reconstituted plant material |
| CN113638265A (en) * | 2020-05-11 | 2021-11-12 | 中国烟草总公司郑州烟草研究院 | Cigarette flavor for cigarette paper coating liquid and application thereof, cigarette paper coating liquid and cigarette |
| CN114504118A (en) * | 2022-02-15 | 2022-05-17 | 河北中烟工业有限责任公司 | Charging liquid for heating cigarette, preparation method of charging liquid and heating cigarette |
| US11766067B2 (en) | 2017-05-15 | 2023-09-26 | Nicoventures Trading Limited | Ground tobacco composition |
| US12075810B2 (en) | 2017-05-15 | 2024-09-03 | Nicoventures Trading Limited | Method of making a tobacco extract |
Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102199490A (en) * | 2010-03-24 | 2011-09-28 | 郑州轻工业学院 | Method for extracting neutral aroma compositions in tobacco |
| CN102871212A (en) * | 2012-10-08 | 2013-01-16 | 安徽中烟工业有限责任公司 | Method for producing paper-making reconstituted tobacco |
| CN102994228A (en) * | 2012-10-25 | 2013-03-27 | 罗瑞雪 | Preparation method of tobacco absolute |
| CN103242960A (en) * | 2013-05-15 | 2013-08-14 | 云南瑞升烟草技术（集团）有限公司 | Method for preparing tobacco flower absolute oil by using supercritical CO2 extraction |
-
2013
- 2013-09-18 CN CN201310429064.9A patent/CN103468403B/en active Active
Patent Citations (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102199490A (en) * | 2010-03-24 | 2011-09-28 | 郑州轻工业学院 | Method for extracting neutral aroma compositions in tobacco |
| CN102871212A (en) * | 2012-10-08 | 2013-01-16 | 安徽中烟工业有限责任公司 | Method for producing paper-making reconstituted tobacco |
| CN102994228A (en) * | 2012-10-25 | 2013-03-27 | 罗瑞雪 | Preparation method of tobacco absolute |
| CN103242960A (en) * | 2013-05-15 | 2013-08-14 | 云南瑞升烟草技术（集团）有限公司 | Method for preparing tobacco flower absolute oil by using supercritical CO2 extraction |
Non-Patent Citations (1)
| Title |
|---|
| 王宁: "再造烟叶生产过程中提取工艺技术研究", 《中国优秀硕士学位论文全文数据库 工程科技辑》 * |
Cited By (14)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104000302A (en) * | 2014-06-17 | 2014-08-27 | 云南中烟工业有限责任公司 | Electronic cigarette liquid and quality detecting method thereof |
| CN104450186A (en) * | 2014-10-29 | 2015-03-25 | 山东中烟工业有限责任公司 | Method for preparing tobacco herbal fragrant substance for cigarette solution of electronic cigarette |
| CN104450186B (en) * | 2014-10-29 | 2017-04-19 | 山东中烟工业有限责任公司 | Method for preparing tobacco herbal fragrant substance for cigarette solution of electronic cigarette |
| CN104585863A (en) * | 2015-01-20 | 2015-05-06 | 川渝中烟工业有限责任公司 | Electronic cigarette juice |
| CN104585863B (en) * | 2015-01-20 | 2016-08-24 | 川渝中烟工业有限责任公司 | A kind of tobacco juice for electronic smoke |
| CN106124679A (en) * | 2016-07-06 | 2016-11-16 | 云南中烟工业有限责任公司 | One assay method growing tobacco middle group compounds of aldehydes and ketones |
| US11766067B2 (en) | 2017-05-15 | 2023-09-26 | Nicoventures Trading Limited | Ground tobacco composition |
| US12075810B2 (en) | 2017-05-15 | 2024-09-03 | Nicoventures Trading Limited | Method of making a tobacco extract |
| WO2020002585A1 (en) | 2018-06-29 | 2020-01-02 | Nerudia Limited | A method for manufacturing reconstituted plant material |
| WO2020002583A1 (en) | 2018-06-29 | 2020-01-02 | Nerudia Limited | A method for manufacturing reconstituted plant material |
| WO2020002589A1 (en) | 2018-06-29 | 2020-01-02 | Nerudia Limited | A method for manufacturing reconstituted plant material |
| CN113638265A (en) * | 2020-05-11 | 2021-11-12 | 中国烟草总公司郑州烟草研究院 | Cigarette flavor for cigarette paper coating liquid and application thereof, cigarette paper coating liquid and cigarette |
| CN114504118A (en) * | 2022-02-15 | 2022-05-17 | 河北中烟工业有限责任公司 | Charging liquid for heating cigarette, preparation method of charging liquid and heating cigarette |
| CN114504118B (en) * | 2022-02-15 | 2023-01-13 | 河北中烟工业有限责任公司 | Charging liquid for heating cigarette, preparation method of charging liquid and heating cigarette |
Also Published As
| Publication number | Publication date |
|---|---|
| CN103468403B (en) | 2016-01-27 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| CN103468403B (en) | A kind of water extraction and supercritical CO 2extraction process method of flavor matter in directed compound collecting tobacco from tobacco material | |
| CN103484245B (en) | The one directed composite extracting method growing tobacco this Studies of The Aromatic Substances of endogenous | |
| CN103462205B (en) | Reconstructed tobacco leaves containing basic incense substances in tobaccos prepared by water extraction method and ethanol extraction method and cigarettes produced by reconstructed tobacco leaves | |
| CN104450186B (en) | Method for preparing tobacco herbal fragrant substance for cigarette solution of electronic cigarette | |
| CN105029681B (en) | Natural perfume material refined liquid, tobacco juice suitable for tobacco juice for electronic smoke and preparation method thereof | |
| CN104351944B (en) | A kind of tobacco flavoring agent and methods and applications thereof | |
| CN105861154A (en) | A method of directionally separating aroma substances from tobacco by utilizing supercritical extraction and molecule distillation and applications of the aroma substances | |
| CN103462206B (en) | A kind of reconstituted tobacco of this Studies of The Aromatic Substances of tobacco endogenous containing directed compound collecting and cigarette prepared therefrom | |
| CN105779128A (en) | Cigarette product with high sensorial comfort level | |
| CN106036982B (en) | A kind of preparation method and applications of cigarette bay leaf extract | |
| CN105212262A (en) | A kind of preparation method of tobacco flavor material | |
| CN102586019B (en) | Preparation method and application of neutral aroma components in grain phase of smoke of high-quality tobacco leaves | |
| CN104687246A (en) | Porous moringa oleifera particles, preparation method of porous moringa oleifera particles as well as cigarette filter stick containing porous particles | |
| CN103468405B (en) | A kind of water extraction and the ethanol extraction method method of this Studies of The Aromatic Substances in directed compound collecting tobacco from tobacco material | |
| CN106307606A (en) | Method for preparing high-fragrance tobacco extract | |
| CN103783660A (en) | Supercritical extraction method of aroma substances in tobacco leaf fragments and application of aroma substances | |
| CN103468406B (en) | This Studies of The Aromatic Substances of tobacco endogenous of a kind of directed compound collecting | |
| CN103462204B (en) | Reconstituted tobacco containing composite tobacco aroma substances prepared by water extraction method and supercritical CO2 extraction method and cigarette prepared of same | |
| CN107232638A (en) | A kind of upgrading purification process of raisin extract and its application | |
| CN104152268A (en) | Tobacco perfume material prepared by compound enzyme enzymolysis coupling Maillard reaction, and preparation method and application of tobacco perfume material | |
| CN102732381B (en) | Preparation method of fermented tobacco Dendranthema indicum essential oil | |
| CN103478892B (en) | This Studies of The Aromatic Substances in the tobacco of water extraction and ethanol extraction method directed compound collecting from tobacco material | |
| CN102793262A (en) | Tobacco flavor as well as preparation and use methods thereof | |
| CN101569438A (en) | Method for preparing mulberry cigarette flavor | |
| CN103704872B (en) | A kind of have reconstituted tobacco of fragrant and sweet style and uses thereof |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| C14 | Grant of patent or utility model | ||
| GR01 | Patent grant |