Mixed tobacco essence used in atomized liquid and preparation method thereof

By mixing the Figinia tobacco clean oil and Zimbabwe tobacco fractionated extract in a ratio of 1 to 3:1, the problem of poor smoking experience caused by a single type of tobacco flavor is solved, and the coordination and quality improvement of tobacco flavor is achieved. , ensuring the high quality of the atomizing liquid.

CN119157286APending Publication Date: 2024-12-20ZHUOYUE INT HLDG LTD
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Patent Information

Application Number
CN202310736530.1
Authority / Receiving Office
CN · China
Patent Type
Applications(China)
Current Assignee / Owner
Filing Date
2023-06-20
Publication Date
2024-12-20

AI Technical Summary

Technical Problem

A single type of tobacco fragrance leads to poor suction experience in the atomized liquid, which cannot effectively reduce the tobacco fragrance, and it is difficult to coordinate the tobacco aroma, miscellaneous air and irritation.

Method used

Mixed tobacco by mixing Virginia tobacco clean oil and Zimbabwe tobacco fractionated extract at a mass ratio of 1 to 3:1, and mixed tobacco is prepared by weak polar organic solvent extraction, ethanol dissolution, low temperature standstill and molecular distillation treatment. Fragrance, ensures the coordination and quality of tobacco fragrance.

Benefits of technology

It improves the tobacco fragrance, coordination and irritation of tobacco essence, avoids burnt odor, ensures that the tobacco essence does not carbonize, and improves the quality of the atomization liquid.

✦ Generated by Eureka AI based on patent content.

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Abstract

The invention belongs to the technical field of atomized liquid component design, and particularly relates to a mixed tobacco essence used in atomized liquid and a preparation method thereof, and the mixed tobacco essence comprises Ferginia tobacco absolute and Zimbabwe tobacco fractionation extract in a weight ratio of (1-3): 1. Compared with single tobacco or compound essence exceeding the proportion range, the tobacco essence has the advantages that the tobacco fragrance, harmony, offensive odor, irritation and aftertaste of the tobacco essence are integrated, the tobacco fragrance, harmony, offensive odor, irritation and aftertaste of the tobacco essence are obviously improved, no burnt smell exists, and the tobacco essence has a good taste. Therefore, the tobacco essence in the scheme is not carbonized, and the atomization quality is ensured.
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Description

Technical Field

[0001] The invention belongs to the technical field of atomizing liquid component design, and particularly relates to a mixed tobacco flavor used in atomizing liquid and a preparation method thereof. Background Art

[0002] As the world is trying to control cigarettes, electronic aerosol generators have developed rapidly as new tobacco products to meet consumers' smoking and health needs. The atomizing liquid of electronic aerosol generators is mainly composed of solvents, nicotine and flavors. Compared with traditional cigarettes, the tobacco flavor of the atomizing liquid of electronic aerosol generators is more dependent on tobacco flavors.

[0003] Tobacco extract as tobacco flavor can restore the original tobacco flavor to the greatest extent, giving cigarettes full smoke, delicate taste and pure tobacco smoking experience. However, when tobacco flavor is applied to atomizer liquid, a single type of tobacco flavor often leads to a poor smoking experience. Summary of the invention

[0004] In order to solve the above technical problems, the present invention provides a mixed tobacco flavor for use in an atomized liquid, comprising Virginia tobacco absolute oil and Zimbabwe tobacco fractionated extract in a weight ratio of 1 to 3:1.

[0005] Preferably, the weight ratio of Virginia tobacco absolute oil to Zimbabwe tobacco fractionated extract is 2:1.

[0006] The present invention also provides a method for preparing the mixed tobacco flavor used in the atomized liquid:

[0007] (1) Preparation of Virginia Tobacco Absolute Oil

[0008] After fully extracting Virginia tobacco extract with a weakly polar organic solvent, the extract is concentrated and then added to ethanol for dissolution, the resulting solution is allowed to stand at low temperature for stratification, and the upper layer solution is taken and concentrated to obtain Virginia tobacco absolute oil;

[0009] (2) Preparation of Zimbabwean tobacco fraction extract

[0010] Adding Zimbabwean tobacco extract to ethanol to dissolve, standing the obtained solution at low temperature to separate layers, taking the upper layer solution, and concentrating it to obtain Zimbabwean tobacco absolute oil, and then molecularly distilling the obtained Zimbabwean tobacco absolute oil, and the distilled light component is the Zimbabwean tobacco fractionation extract;

[0011] (3) The Virginia tobacco absolute obtained in step (1) and the Zimbabwe tobacco fractionated extract obtained in step (2) are mixed evenly.

[0012] Preferably, in step (1), the weakly polar organic solvent is one or a combination of petroleum ether, n-hexane, cyclohexane, diethyl ether, dichloromethane, chloroform, and ethyl acetate.

[0013] Preferably, in step (1), the mass amount of the weak polar organic solvent is 1 to 10 times the mass of Virginia tobacco extract.

[0014] Preferably, in step (1), the mass amount of ethanol used is 1 to 10 times the mass of the concentrated extract.

[0015] Preferably, in step (1), the ethanol is anhydrous ethanol or an ethanol aqueous solution with a volume concentration of more than 95%.

[0016] Preferably, in step (1), the low temperature is -20°C to -10°C, and the standing time at low temperature is 10h to 15h.

[0017] Preferably, in step (2), the mass amount of ethanol is 1 to 10 times the mass of Zimbabwe tobacco extract.

[0018] Preferably, in step (2), the ethanol is anhydrous ethanol or an ethanol aqueous solution with a volume concentration of more than 95%.

[0019] Preferably, in step (2), the low temperature is -20°C to -10°C, and the standing time at low temperature is 10h to 15h.

[0020] Preferably, in step (2), the treatment conditions of molecular distillation are as follows: heating temperature of 50-70°C, evaporation temperature of 80-150°C, condensation temperature of the first stage of 10°C-40°C, condensation temperature of the second stage of 10°C--10°C, condensation temperature of the third stage of -10°C--30°C, rotation speed of 100-300 r / min, vacuum degree of 10-200 Pa, and flow rate of 0.5-3 ml / min.

[0021] In this scheme, Virginia tobacco pure oil and Zimbabwe tobacco fractionated extract are mixed in a mass ratio of 1 to 3:1, which not only ensures the flue-cured tobacco aroma of Virginia tobacco, but also has the unique sweet and burnt aroma of Zimbabwe tobacco. Compared with a single tobacco or a compound flavor exceeding the above-mentioned ratio range, the smoke aroma, coordination, miscellaneous smell, irritation, and aftertaste of the tobacco flavor in this scheme are significantly improved, and there is no burnt smell, which means that the tobacco flavor in this scheme is not carbonized, thereby ensuring the atomization quality. BRIEF DESCRIPTION OF THE DRAWINGS

[0022] Figure 1 The present invention is a flow chart of the preparation process of the mixed tobacco flavor used in the atomized liquid in the present application. DETAILED DESCRIPTION

[0023] The mixed tobacco flavor used in the atomizing liquid of the present application includes Virginia tobacco pure oil and Zimbabwe tobacco fractionated extract in a weight ratio of 1 to 3:1, wherein Virginia tobacco, also known as flue-cured tobacco and fire-tube flue-cured tobacco, is native to Virginia in the United States and is the main raw material for cigarettes; Zimbabwe tobacco has a unique sweet and burnt aroma, and domestic "Zhonghua Cigarettes" and "Furong King" will add a certain proportion of Zimbabwean tobacco. Some people say that every puff of "Zhonghua Cigarettes" has the taste of Zimbabwe.

[0024] The preparation method of mixed tobacco flavor is:

[0025] (1) Preparation of Virginia Tobacco Absolute Oil

[0026] The Virginia tobacco extract is fully extracted with 1 to 10 times the weight of a weakly polar organic solvent and then separated. The extract is concentrated and then added into 1 to 10 times the weight of ethanol with a volume concentration of more than 95% to dissolve. The resulting solution is allowed to stand at a low temperature of -20°C to -10°C for 10 hours to separate the layers. The upper layer solution is taken and concentrated to obtain Virginia tobacco absolute oil.

[0027] Wherein, the weak polar organic solvent is one or a combination of petroleum ether, n-hexane, cyclohexane, ethyl ether, dichloromethane, chloroform, and ethyl acetate;

[0028] (2) Preparation of Zimbabwean tobacco fraction extract

[0029] The Zimbabwean tobacco extract is added to ethanol with a volume concentration of 95% or more and 1 to 10 times its weight to dissolve, the obtained solution is allowed to stand at a low temperature of -20°C to -10°C for 10 hours to 15 hours for layering, the upper layer solution is taken, and concentrated to obtain Zimbabwean tobacco pure oil, and the obtained Zimbabwean tobacco pure oil is molecularly distilled. The molecular distillation treatment conditions are: heating temperature 50 to 70°C, evaporation temperature 80 to 150°C, condensation temperature of the first stage is 10°C to 40°C, condensation temperature of the second stage is 10°C to -10°C, condensation temperature of the third stage is -10°C to -30°C, rotation speed is 100 to 300 r / min, vacuum degree is 10 to 200 Pa, flow rate is 0.5 to 3 ml / min, and the light component distilled is the Zimbabwean tobacco fractionation extract;

[0030] (3) The Virginia tobacco pure oil obtained in step (1) and the Zimbabwe tobacco fractionated extract obtained in step (2) are mixed evenly to obtain the mixed tobacco flavor for use in the atomized liquid of the present application.

[0031] Example 1

[0032] (1) Preparation of Virginia Tobacco Absolute Oil

[0033] 300 g of Virginia tobacco extract was added to 750 g of petroleum ether and mixed thoroughly, and then allowed to stand for stratification to achieve extraction, the extract was separated, and then mixed thoroughly with 750 g of petroleum ether again, and then allowed to stand for stratification to achieve secondary extraction, the extract after the secondary extraction was separated and concentrated, and then added to 1500 g of anhydrous ethanol for dissolution, and the obtained solution was allowed to stand for 10 hours at a low temperature of -20°C for stratification, and the upper layer solution was taken and concentrated to obtain about 150 g of Virginia tobacco pure oil;

[0034] (2) Preparation of Zimbabwean tobacco fraction extract

[0035] 300g of Zimbabwean tobacco extract was added to 2000g of anhydrous ethanol to dissolve, and the obtained solution was allowed to stand at -15℃ for 15h to separate layers, and the upper layer solution was taken and concentrated to obtain about 200g of Zimbabwean tobacco absolute oil, and then the obtained Zimbabwean tobacco absolute oil was molecularly distilled, and the treatment conditions of molecular distillation were: heating temperature 65℃, evaporation temperature 100℃, condensation temperature of the first stage was 20℃, condensation temperature of the second stage was 0℃, condensation temperature of the third stage was -15℃, rotation speed was 300r / min, vacuum degree was 100Pa, flow rate was 3ml / min, and about 150g of light components were distilled out, which was the Zimbabwean tobacco fractionation extract;

[0036] (3) 80 g of the Virginia tobacco pure oil obtained in step (1) and 20 g of the Zimbabwe tobacco fractionated extract obtained in step (2) are mixed evenly to form a mixed tobacco flavor for use in the atomized liquid.

[0037] Example 2

[0038] (1) Preparation of Virginia Tobacco Absolute Oil

[0039] 300 g of Virginia tobacco extract was added to 1500 g of petroleum ether and mixed thoroughly, and then allowed to stand for stratification to achieve extraction, the extract was separated, and then mixed thoroughly with 1500 g of petroleum ether again, and then allowed to stand for stratification to achieve secondary extraction, the extract after the secondary extraction was separated and concentrated, and then added to 300 g of anhydrous ethanol for dissolution, and the obtained solution was allowed to stand for 12 hours at a low temperature of -10°C for stratification, and the upper layer solution was taken and concentrated to obtain about 150 g of Virginia tobacco pure oil;

[0040] (2) Preparation of Zimbabwean tobacco fraction extract

[0041] 300 g of Zimbabwean tobacco extract was added to 3000 g of anhydrous ethanol to dissolve, and the obtained solution was allowed to stand at -20°C for 10 hours to separate layers, and the upper layer solution was taken and concentrated to obtain about 200 g of Zimbabwean tobacco absolute oil, and then the obtained Zimbabwean tobacco absolute oil was molecularly distilled, and the treatment conditions of molecular distillation were: heating temperature 70°C, evaporation temperature 150°C, condensation temperature of the first stage was 40°C, condensation temperature of the second stage was 10°C, condensation temperature of the third stage was -10°C, rotation speed was 200 r / min, vacuum degree was 30 Pa, flow rate was 2 ml / min, and about 150 g of light components were distilled, which was the Zimbabwean tobacco fractionation extract;

[0042] (3) 75 g of the Virginia tobacco pure oil obtained in step (1) and 25 g of the Zimbabwe tobacco fractionated extract obtained in step (2) were mixed evenly to obtain a mixed tobacco flavor for use in the atomized liquid.

[0043] Example 3

[0044] (1) Preparation of Virginia Tobacco Absolute Oil

[0045] Same as step (1) in Example 2;

[0046] (2) Preparation of Zimbabwean tobacco fraction extract

[0047] Same as step (2) in Example 2;

[0048] (3) 70 g of the Virginia tobacco pure oil obtained in step (1) and 35 g of the Zimbabwe tobacco fractionated extract obtained in step (2) were mixed evenly to obtain a mixed tobacco flavor for use in the atomized liquid.

[0049] Example 4

[0050] (1) Preparation of Virginia Tobacco Absolute Oil

[0051] Same as step (1) in Example 2;

[0052] (2) Preparation of Zimbabwean tobacco fraction extract

[0053] Same as step (2) in Example 2;

[0054] (3) 50 g of the Virginia tobacco pure oil obtained in step (1) and 50 g of the Zimbabwe tobacco fractionated extract obtained in step (2) are mixed evenly to obtain a mixed tobacco flavor for use in the atomized liquid.

[0055] Example 5

[0056] (1) Preparation of Virginia Tobacco Absolute Oil

[0057] Same as step (1) in Example 2;

[0058] (2) Preparation of Zimbabwean tobacco fraction extract

[0059] Same as step (2) in Example 2;

[0060] (3) 35 g of the Virginia tobacco pure oil obtained in step (1) and 70 g of the Zimbabwe tobacco fractionated extract obtained in step (2) were mixed evenly to obtain a mixed tobacco flavor for use in the atomized liquid.

[0061] Example 6

[0062] (1) Preparation of Virginia Tobacco Absolute Oil

[0063] Same as step (1) in Example 2;

[0064] (2) Preparation of Zimbabwean tobacco fraction extract

[0065] Same as step (2) in Example 2;

[0066] (3) 25 g of the Virginia tobacco pure oil obtained in step (1) and 75 g of the Zimbabwe tobacco fractionated extract obtained in step (2) were mixed evenly to obtain a mixed tobacco flavor for use in the atomized liquid.

[0067] Example 7

[0068] (1) Preparation of Virginia Tobacco Absolute Oil

[0069] 300 g of Virginia tobacco extract was added to 350 g of petroleum ether and mixed thoroughly, and then allowed to stand for stratification to achieve extraction, the extract was separated, and then mixed thoroughly with 350 g of petroleum ether again, and then allowed to stand for stratification to achieve secondary extraction, the extract after the secondary extraction was separated and concentrated, and then added to 600 g of anhydrous ethanol for dissolution, and the obtained solution was allowed to stand for 15 hours at a low temperature of -15°C for stratification, and the upper layer solution was taken and concentrated to obtain about 150 g of Virginia tobacco pure oil;

[0070] (2) Preparation of Zimbabwean tobacco fraction extract

[0071] 300g of Zimbabwean tobacco extract was added to 500g of anhydrous ethanol to dissolve, and the obtained solution was allowed to stand at -10℃ for 15h to separate layers, and the upper layer solution was taken and concentrated to obtain about 200g of Zimbabwean tobacco absolute oil, and then the obtained Zimbabwean tobacco absolute oil was molecularly distilled, and the treatment conditions of molecular distillation were: heating temperature 50℃, evaporation temperature 80℃, condensation temperature of the first stage was 10℃, condensation temperature of the second stage was -10℃, condensation temperature of the third stage was -30℃, rotation speed was 100r / min, vacuum degree was 200Pa, flow rate was 0.5ml / min, and about 150g of light components were distilled, which was the Zimbabwean tobacco fractionation extract;

[0072] (3) 20 g of the Virginia tobacco pure oil obtained in step (1) and 80 g of the Zimbabwe tobacco fractionated extract obtained in step (2) are mixed evenly to obtain a mixed tobacco flavor for use in the atomized liquid.

[0073] Example 8

[0074] (1) Preparation of Virginia Tobacco Absolute Oil

[0075] Same as step (1) in Example 2;

[0076] (2) 100 g of the Virginia tobacco pure oil obtained in step (1) is used as the mixed tobacco flavor in the atomized liquid.

[0077] Example 9

[0078] (1) Preparation of Zimbabwean tobacco fraction extract

[0079] Same as step (2) in Example 2;

[0080] (2) 100 g of the Zimbabwe tobacco fractionated extract obtained in step (1) is used as a mixed tobacco flavor in the atomized liquid.

[0081] The mixed tobacco flavors obtained in the above examples were made into atomized liquids respectively. The atomized liquids were prepared by weighing the mixed tobacco flavors, adding them to a mixed solvent of PG:VG=1:1 (mass ratio), and mixing them evenly to form an atomized liquid. The mass fraction of the mixed tobacco flavors in the atomized liquid was 20%. Then, an atomizer containing a ceramic atomizer core was used to perform an atomization evaluation test. The results are shown in the following table:

[0082]

[0083]

[0084] As can be seen from the above table, in this scheme, Virginia tobacco absolute oil and Zimbabwe tobacco fractionation extract are mixed in a mass ratio of 1 to 3:1, which not only ensures the flue-cured tobacco aroma of Virginia tobacco, but also has the unique sweet and burnt aroma of Zimbabwe tobacco. Compared with a single tobacco or a compound flavor exceeding the above ratio range, the smoke aroma, coordination, miscellaneous smell, irritation and aftertaste of the tobacco flavor in this scheme are significantly improved, and there is no burnt smell, which means that the tobacco flavor in this scheme is not carbonized, ensuring the atomization quality.

Claims

1. A mixed tobacco flavor for use in atomized liquid, Features: The mixed tobacco essence comprises Virginia tobacco absolute oil and Zimbabwe tobacco fractionation extract in a weight ratio of 1 to 3:

1.

2. The mixed tobacco flavor for atomizing liquid according to claim 1, Features: The weight ratio of the Virginia tobacco absolute oil to the Zimbabwe tobacco fractionated extract is 2:

1.

3. A method for preparing a mixed tobacco flavor for atomized liquid as claimed in claim 1 or 2, Features: The preparation method is: (1) Preparation of Virginia Tobacco Absolute Oil After fully extracting Virginia tobacco extract with a weakly polar organic solvent, the extract is concentrated and then added to ethanol for dissolution, the resulting solution is allowed to stand at low temperature for stratification, and the upper layer solution is taken and concentrated to obtain the Virginia tobacco absolute oil; (2) Preparation of Zimbabwean tobacco fraction extract Adding Zimbabwean tobacco extract to ethanol to dissolve, standing the obtained solution at low temperature to separate layers, taking the upper layer solution, and concentrating it to obtain Zimbabwean tobacco absolute oil, and then molecularly distilling the obtained Zimbabwean tobacco absolute oil, and the distilled light component is the Zimbabwean tobacco fractionation extract; (3) The Virginia tobacco absolute obtained in step (1) and the Zimbabwe tobacco fractionated extract obtained in step (2) are mixed evenly.

4. The method for preparing the mixed tobacco flavor for atomized liquid according to claim 3, Features: The weakly polar organic solvent in step (1) is one or a combination of petroleum ether, n-hexane, cyclohexane, ethyl ether, dichloromethane, chloroform, and ethyl acetate.

5. The method for preparing the mixed tobacco flavor for atomized liquid according to claim 3, Features: The mass amount of the weak polar organic solvent in step (1) is 1 to 10 times the mass of the Virginia tobacco extract.

6. The method for preparing the mixed tobacco flavor for atomized liquid according to claim 3, Features: The ethanol in step (1) is anhydrous ethanol or an ethanol aqueous solution with a volume concentration of more than 95%.

7. The method for preparing the mixed tobacco flavor for atomized liquid according to claim 3, Features: The low temperature in step (1) is -20°C to -10°C, and the standing time at the low temperature is 10h to 15h.

8. The method for preparing the mixed tobacco flavor for atomized liquid according to claim 3, Features: The ethanol in step (2) is anhydrous ethanol or an ethanol aqueous solution with a volume concentration of more than 95%.

9. The method for preparing the mixed tobacco flavor for atomized liquid according to claim 3, Features: The low temperature in step (2) is -20°C to -10°C, and the standing time at the low temperature is 10h to 15h.

10. The method for preparing the mixed tobacco flavor for atomized liquid according to claim 3, Features: The treatment conditions of the molecular distillation in step (12) are as follows: a heating temperature of 50 to 70°C, an evaporation temperature of 80 to 150°C, a condensation temperature of 10 to 40°C in the first stage, a condensation temperature of 10 to -10°C in the second stage, a condensation temperature of -10 to -30°C in the third stage, a rotation speed of 100 to 300 r / min, a vacuum degree of 10 to 200 Pa, and a flow rate of 0.5 to 3 ml / min.

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