WO2023241397A1 - 一种提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法 - Google Patents

一种提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法 Download PDF

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WO2023241397A1
WO2023241397A1 PCT/CN2023/098492 CN2023098492W WO2023241397A1 WO 2023241397 A1 WO2023241397 A1 WO 2023241397A1 CN 2023098492 W CN2023098492 W CN 2023098492W WO 2023241397 A1 WO2023241397 A1 WO 2023241397A1
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leaves
temperature
alkaline
cigar
leaf
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PCT/CN2023/098492
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English (en)
French (fr)
Inventor
吴键
周国俊
储国海
陈震
王骏
蒋健
肖卫强
夏倩
赵路灿
徐建
卢昕博
陆成飞
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浙江中烟工业有限责任公司
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Publication of WO2023241397A1 publication Critical patent/WO2023241397A1/zh

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    • A—HUMAN NECESSITIES
    • A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B3/00—Preparing tobacco in the factory
    • A24B3/12—Steaming, curing, or flavouring tobacco
    • A—HUMAN NECESSITIES
    • A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B13/00—Tobacco for pipes, for cigars, e.g. cigar inserts, or for cigarettes; Chewing tobacco; Snuff
    • A—HUMAN NECESSITIES
    • A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B3/00—Preparing tobacco in the factory
    • A—HUMAN NECESSITIES
    • A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B3/00—Preparing tobacco in the factory
    • A24B3/04—Humidifying or drying tobacco bunches or cut tobacco
    • A—HUMAN NECESSITIES
    • A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B3/00—Preparing tobacco in the factory
    • A24B3/06—Loosening tobacco leaves or cut tobacco
    • A—HUMAN NECESSITIES
    • A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B3/00—Preparing tobacco in the factory
    • A24B3/07—Cutting or removing tie leaves; Cutting-off stem butts
    • A—HUMAN NECESSITIES
    • A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B3/00—Preparing tobacco in the factory
    • A24B3/10—Roasting or cooling tobacco
    • A—HUMAN NECESSITIES
    • A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B7/00—Cutting tobacco
    • A24B7/14—Feeding or control devices for tobacco-cutting apparatus
    • A—HUMAN NECESSITIES
    • A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
    • A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
    • A24B9/00—Control of the moisture content of tobacco products, e.g. cigars, cigarettes, pipe tobacco

Definitions

  • the invention belongs to the technical field of heated cigarettes, and specifically relates to a method for increasing the release of alkaline aroma components of cigar leaves in heated cigarettes.
  • Heated cigarettes use an external heat source to control the heating state of the cigarette core so that it releases tobacco products containing nicotine aerosol under low-temperature heating rather than burning conditions.
  • the raw material of the heated cigarette core is decisive for the release of smoke components and sensory quality. Influence.
  • the main forms of heated cigarette cores include granular type and reconstituted tobacco leaf type. Although the forms are different, they are usually made of tobacco raw materials as the main body and mixed with exogenous materials.
  • the tobacco in the cigarette cores is Raw material components have a greater impact on aerosol release and sensory quality.
  • cigar tobacco leaves are special in terms of physical structure, chemical composition and flavor characteristics, especially the types and contents of alkaline aroma components in the smoke of cigar tobacco raw materials. It is expected to play a positive role in modifying the original aroma of tobacco, suppressing impurities, and improving aroma quality.
  • the object of the present invention is to provide a method for increasing the release of alkaline aroma components of cigar tobacco leaves in heated cigarettes, so as to solve the problem of alkaline aroma components such as pyridines, pyrazines, and quinolines when cigar leaves are currently used as heated cigarette core materials.
  • alkaline aroma components such as pyridines, pyrazines, and quinolines when cigar leaves are currently used as heated cigarette core materials.
  • the total release amount of aroma cannot meet the needs of consumers.
  • a method for increasing the release of alkaline aroma components of cigar leaves in heated cigarettes including the following steps:
  • step S2 The tobacco leaves after vacuum regaining moisture in step S1 enter the loosening and moistening process to further increase the moisture content of the tobacco leaves and completely loosen them;
  • step S2 The tobacco leaves after being loosened and moistened in step S2 enter the leaf storage process to achieve moisture absorption and balance;
  • step S4 The tobacco leaves after storage in step S3 enter the shreding process, and the shredded leaves are controlled to a set width;
  • step S5 The shredded leaves in step S4 enter the first-level drying process and are dried by high-temperature airflow to reduce the moisture content of the shredded leaves to less than 11%;
  • step S6 The shredded leaves after the first-level drying in step S5 enter the second-level drying process and are subjected to low-temperature drum drying to reduce the moisture content of the shredded leaves to less than 4%;
  • step S7 The shredded leaves after the secondary drying in step S6 enter the fragrance adding process, and the alcohol mixed solution is added to the shredded leaves;
  • step S8 The fragrant leaf shreds in step S7 enter the silk storage process to achieve absorption and balance of the alcohol mixed solution in the leaf shreds.
  • step S1 the moisture content of the cigar leaves is increased to 15%, and the temperature of the tobacco leaves is increased to 50°C.
  • step S2 the moisture content of the cigar leaves is increased to 17%, and the temperature of the tobacco leaves is increased to 56°C.
  • the leaf storage temperature is 32°C and the leaf storage time is 4 hours.
  • the width of the shred leaves is controlled to 0.9 mm.
  • step S5 high-temperature airflow drying is performed, and the drying temperature is 200°C.
  • step S6 low-temperature drum drying is performed, and the drying temperature is 130°C.
  • the wire storage temperature is 32°C and the wire storage time is 72 hours.
  • This technical solution realizes the processing of natural cigar leaves into heated cigarette core materials by increasing the release of alkaline aroma components of cigar leaves in heated cigarettes, and can convert the pyridines, pyrazines, and quinolines in the cigar leaves in heated cigarettes.
  • the mass percentage of the total release amount of similar alkaline aromas is increased by 1% to 13.5%.
  • Figure 1 is a process flow chart of the method for increasing the release of alkaline aroma components of cigar leaves in heated cigarettes according to the present invention.
  • this application uses a method to increase the release of alkaline aroma components of cigar leaves in heated cigarettes to process natural cigar leaves into heated cigarette core materials, which can convert the pyridine in the cigar leaves in heated cigarettes.
  • the mass percentage of the total release of alkaline aromas such as aromatics, pyrazines, and quinolines is increased by 1% to 13.5%.
  • This technical solution also includes detection technology for alkaline aroma components in shredded tobacco prepared by the above-mentioned method of increasing the release of alkaline aroma components of cigar leaves in heated cigarettes, and is coupled to a smoke predator device (which can be built by oneself) through temperature-controlled heating. It consists of an infrared rapid heating tube furnace and a Cambridge filter collection system; the specific conditions are:
  • the mixed gas flow control system will pass a mixture of 20% oxygen and 80% nitrogen into the quartz tube at a flow rate of 0.2L/min. After aeration for 3 minutes, use The computer temperature control system raises the rapid heating furnace from room temperature to 350°C within 20 seconds and maintains it for 5 minutes, using Cambridge filters to capture the flue gas particulate matter. After heating is completed, open the heating furnace cover to continue ventilation. After cooling for 5 minutes, remove the Cambridge filter.
  • the alkaline aroma components were measured using a gas chromatography/mass spectrometer.
  • the programmed temperature rise conditions of the chromatographic column were: initial temperature 50°C (maintained for 2 minutes), heated to 160°C at a rate of 2.5°C/min (maintained for 3 minutes), and then The temperature was increased to 280°C at a rate of 20°C/min.
  • the test results are shown in Table 1:
  • the established working curves of 16 alkaline aroma components have good linear relationships, and the coefficients of determination are all greater than 0.999.
  • the detection limit of the method is between 0.23-1.58 ⁇ g/mL, and the quantitation limit is between 0.77-5.27 ⁇ g/mL. mL, the method precision is 0.94-4.26%, the recovery rate of standard addition is between 85.69-94.26%, the repeatability is good, and the recovery rate is high, indicating that this method is suitable for heating to release 16 alkalis in aerosols Content analysis of aroma components.
  • the loosening and moistening process is entered to increase the moisture content of the tobacco leaves to 17% and the temperature of the tobacco leaves to 56°C; Entering the leaf storage process, the leaf storage temperature is 32°C and the leaf storage time is 4 hours; the leaf width is controlled to 0.9mm; the first-level drying process is performed with high-temperature airflow drying at a drying temperature of 200°C; the second-level drying process is performed with a low-temperature roller Dry, the drying temperature is 130°C; take a sample to detect the release of alkaline aroma components of the cut tobacco and it is 229.86ug/g; add aroma, add 10% alcohol mixed solution to the cut leaves, and store the cut tobacco at a storage temperature of 32°C. Wire time 72h. The total amount of alkaline aroma components in cut tobacco was tested during sampling and was 194.27ug/g. The content of alkaline aroma components decreased
  • the loosening and moistening process is entered to increase the moisture content of the tobacco leaves to 17% and the temperature of the tobacco leaves to 56°C; Entering the leaf storage process, the leaf storage temperature is 32°C and the leaf storage time is 4 hours; the leaf width is controlled to 0.9mm; the first-level drying process is performed with high-temperature airflow drying at a drying temperature of 200°C; the second-level drying process is performed with a low-temperature roller Dry, the drying temperature is 130°C; take a sample to detect the release of alkaline aroma components of the cut tobacco, which is 244.31ug/g; add fragrance, add 10% alcohol mixed solution to the cut leaves, and store the cut tobacco at a storage temperature of 32°C. Wire time 72h. The total amount of alkaline aroma components in cut tobacco was tested by sampling and was 220.31ug/g. The content of alkaline aroma components
  • the loosening and moistening process is entered to increase the moisture content of the tobacco leaves to 17%.
  • the tobacco leaf temperature is increased to 56°C; the leaf storage process is entered, the leaf storage temperature is 32°C, and the leaf storage time is 4 hours; the leaf width is controlled to 0.9mm; the first-level drying process is carried out with high-temperature airflow drying, and the drying temperature is 200°C; the second-level In the drying process, low-temperature drum drying is carried out at a drying temperature of 130°C; sampling is performed to detect the release of alkaline aroma components of the cut tobacco, which is 229.86ug/g; aroma is added, and 30% alcohol mixed solution is added to the cut leaves to store the cut tobacco.
  • the silk storage temperature is 32°C and the silk storage time is 72 hours. The total amount of alkaline aroma components in cut tobacco was tested by sampling and was 260.93ug/g.
  • the loosening and moistening process is entered to increase the moisture content of the tobacco leaves to 17% and the temperature of the tobacco leaves to 56°C; Entering the leaf storage process, the leaf storage temperature is 32°C and the leaf storage time is 4 hours; the leaf width is controlled to 0.9mm; the first-level drying process is performed with high-temperature airflow drying at a drying temperature of 200°C; the second-level drying process is performed with a low-temperature roller Dry, the drying temperature is 130°C; take a sample to detect the release of alkaline aroma components of the cut tobacco, which is 229.86ug/g; add aroma, add 20% alcohol mixed solution to the cut leaves, and store the cut tobacco at a storage temperature of 32°C. Wire time 72h. The total amount of alkaline aroma components in cut tobacco was tested by sampling and was 233.62ug/g. The content of alkaline aroma components
  • the loosening and moistening process is entered to increase the moisture content of the tobacco leaves to 17% and the temperature of the tobacco leaves to 56°C; Entering the leaf storage process, the leaf storage temperature is 32°C and the leaf storage time is 4 hours; the leaf width is controlled to 0.9mm; the first-level drying process is performed with high-temperature airflow drying at a drying temperature of 200°C; the second-level drying process is performed with a low-temperature roller Dry, the drying temperature is 130°C; take a sample to detect the release of alkaline aroma components of the cut tobacco, which is 244.31ug/g; add aroma, add 30% alcohol mixed solution to the cut leaves, and store the cut tobacco at a storage temperature of 32°C. Wire time 72h. The total amount of alkaline aroma components in cut tobacco was tested by sampling and was 271.19ug/g. The content of alkaline aroma components
  • the loosening and moistening process is entered to increase the moisture content of the tobacco leaves to 17% and the temperature of the tobacco leaves to 56°C;
  • the leaf storage temperature is 32°C and the leaf storage time is 4 hours; the width of the leaf shreds is controlled to 0.9mm; in the first-level drying step, high-temperature airflow drying is performed, and the drying temperature is 200°C; Carry out the secondary drying process, perform low-temperature drum drying, and the drying temperature is 130°C; take a sample to detect the release of alkaline aroma components of the cut tobacco, which is 244.31ug/g; perform aromatization, and add 20% alcohol mixed solution to the cut leaves.
  • the silk storage temperature is 32°C and the silk storage time is 72 hours. The total amount of alkaline aroma components in cut tobacco was tested by sampling and was 247.32ug/g.

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Abstract

一种提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法，将雪茄烟叶投料装桶，进入真空回潮工序，实现烟叶的初步提高含水率和温度；依次进入松散润叶工序、贮叶工序及切叶丝工序，再进入一级烘丝工序，进行高温气流干燥，实现叶丝含水率降至11％以下；进入二级烘丝工序，进行低温滚筒干燥，实现叶丝含水率降至4％以下；进入加香工序，在叶丝中加入醇类混合溶液；进入贮丝工序，实现醇类混合溶液在叶丝中吸收和平衡。该方法实现将天然雪茄烟叶加工为加热卷烟烟芯材料，可以将加热卷烟中的雪茄烟叶中吡啶类、吡嗪类、喹啉类等碱性香气的总释放量质量百分比提高1％至13.5％。

Description

一种提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法 技术领域
本发明属于加热卷烟技术领域，具体涉及一种提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法。
背景技术
加热卷烟是利用外部热源控制烟芯的受热状态，使其在低温加热而非燃烧的条件下释放含有烟碱气溶胶的烟草制品，加热卷烟的烟芯原料对烟气成分释放和感官品质有决定性影响。目前加热卷烟烟芯的形式主要有颗粒型和再造烟叶型等多种，虽形式各异，但其通常均是由烟草原料为主体与外源性物料掺混后制备而成，烟芯中烟草原料组分对气溶胶释放和感官质量影响较大。在不同类型的烟草原料中，雪茄烟叶是一种从物理组织结构、化学组成与风味特征等方面均具有特殊性的烟叶，尤其是雪茄烟叶原料的烟气中碱性香味成分的种类及含量较多，有望在修饰烟草本香、抑制杂气、改善香气品质等方面发挥积极作用。
现将天然雪茄烟叶加工为加热卷烟烟芯材料时，加热卷烟中的雪茄烟叶中因为加热温度导致吡啶类、吡嗪类、喹啉类等碱性香气的总释放量无法满足消费者的需求。
发明内容
本发明的目的是提供一种提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法，以解决现使用雪茄烟叶作为加热卷烟烟芯材料时，吡啶类、吡嗪类、喹啉类等碱性香气的总释放量无法满足消费者需求的问题。
为实现上述目的，本申请是通过以下技术方案实现的：
一种提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法，包括以下步骤：
S1、将雪茄烟叶投料装桶，进入真空回潮工序，实现烟叶的初步提高含水率和温度；
S2、步骤S1真空回潮后的烟叶进入松散润叶工序，实现烟叶的含水率进一步提高和完全松散；
S3、步骤S2经过松散润叶后的烟叶进入贮叶工序，实现水分的吸收和平衡；
S4、步骤S3贮叶后的烟叶进入切叶丝工序，将叶丝控制到设定宽度；
S5、步骤S4的叶丝进入一级烘丝工序，进行高温气流干燥，实现叶丝含水率降至11％以下；
S6、步骤S5一级烘丝后的叶丝进入二级烘丝工序，进行低温滚筒干燥，实现叶丝含水率降至4％以下；
S7、步骤S6二级烘丝后的叶丝进入加香工序，在叶丝中加入醇类混合溶液；
S8、步骤S7加香后的叶丝进入贮丝工序，实现醇类混合溶液在叶丝中吸收和平衡。
进一步的，步骤S1中的真空回潮工序，将雪茄烟叶含水率提高至15％，烟叶温度提高至50℃。
进一步的，步骤S2中的松散润叶工序，将雪茄烟叶含水率提高至17％，烟叶温度提高至56℃。
进一步的，步骤S3中的贮叶工序，贮叶温度32℃，贮叶时间4h。
进一步的，步骤S4中的切叶丝工序，将叶丝宽度控制0.9mm。
进一步的，步骤S5中的一级烘丝工序，进行高温气流干燥，干燥温度200℃。
进一步的，步骤S6中的二级烘丝工序，进行低温滚筒干燥，干燥温度130℃。
进一步的，步骤S7中的加香工序，在叶丝中加入20％-30％的醇类混合溶液，所述醇类混合溶液由水、乙醇、丙三醇构成，质量比水：乙醇：丙三醇＝1:4:5。
进一步的，步骤S8中的贮丝工序，贮丝温度32℃，贮丝时间72h。
本发明的有益效果是：
本技术方案通过提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法，实现将天然雪茄烟叶加工为加热卷烟烟芯材料，可以将加热卷烟中的雪茄烟叶中吡啶类、吡嗪类、喹啉类等碱性香气的总释放量质量百分比提高1％至13.5％。
附图说明
图1为本发明提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法的工艺流程图。
具体实施方式
以下结合附图对本发明的技术方案进行详细的说明，以下的实施例仅是示例性的，仅能用来解释和说明本发明的技术方案，而不能解释为是对本发明技术方案的限制。
如图1所示，本申请通过一种提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法，实现将天然雪茄烟叶加工为加热卷烟烟芯材料，其可以将加热卷烟中的雪茄烟叶中吡啶类、吡嗪类、喹啉类等碱性香气的总释放量质量百分比提高1％至13.5％。
本技术方案还包括对上述提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法制备的烟丝中碱性香气成分的检测技术，通过控温加热耦连烟气捕食装置(可以自行搭建)，主要包括红外快速升温管式炉和剑桥滤片捕集系统构成；具体条件为：
称取0.4g烟末样品置于快速升温炉的石英管内，由混合气体流量控制系统将20％氧气、80％氮气的混合气以0.2L/min的流量通入石英管内，通气3min后，使用电脑控温系统在20s内将快速升温炉从室温升至350℃，并保持5min，用剑桥滤片捕集烟气粒相物。加热完成后，打开升温炉盖继续通气，冷却5min后取下剑桥滤片。
取出剑桥滤片，用脱脂棉擦拭捕集器，一并转移至具塞玻璃瓶中.向具塞玻璃瓶中加入60mL CH2Cl2，超声萃60min。萃取结束后，转移至分液漏斗中； 加入20mL质量分数5％的HCl水溶液进行萃取，重复3次，合并水相并置于冰水浴中；滴加质量分数为20％的NaOH水溶液，调至pH为14；④加入20mL CH2Cl2进行萃取，重复3次，合并有机相，即为碱性成分萃取液；加入适量的无水硫酸钠，干燥过夜；将CH2Cl2溶液转移至浓缩瓶中，加入1mL乙酸苯乙酯的CH2Cl2内标溶液(0.508mg/mL)，60℃水浴浓缩至1mL，过0.22μm有机滤膜后进行GC-MS分析。
碱性香气成分测定，采用气相色谱/质谱联用仪进行测定，色谱柱程序升温条件为：初始温度50℃(保持2min)，以2.5℃/min的速率升温至160℃(保持3min)，再以20℃/min的速率升温至280℃。检测结果见表1所示：
表1 16种碱性香味成分的回归方程、检出限、精密度及回收率

由表1可知，所建立的16种碱性香味成分的工作曲线线性关系良好，决定系数均大于0.999，方法的检出限在0.23-1.58μg/mL之间，定量限在0.77-5.27μg/mL之间，方法精密度为0.94-4.26％，加标回收率介于85.69-94.26％之间，重复性较好，回收率较高，表明该方法适用于加热释放气溶胶中16种碱性香味成分的含量分析。
对比例1
巴西雪茄烟叶投料50kg，进入真空回潮工序，将雪茄烟叶含水率提高至15％，烟叶温度提高至50℃；进入松散润叶工序，将烟叶含水率提高至17％，烟叶温度提高至56℃；进入贮叶工序，贮叶温度32℃，贮叶时间4h；将叶丝宽度控制0.9mm；一级烘丝工序，进行高温气流干燥，干燥温度200℃；进行二级烘丝工序，进行低温滚筒干燥，干燥温度130℃；取样检测烟丝碱性香味成分释放量为229.86ug/g；进行加香，在叶丝中加入10％的醇类混合溶液，进行贮丝，贮丝温度32℃，贮丝时间72h。取样检测烟丝碱性香味成分总量为194.27ug/g.碱性香味成分含量下降了15.48％。
对比例2
多米尼加雪茄烟叶投料50kg，进入真空回潮工序，将雪茄烟叶含水率提高至15％，烟叶温度提高至50℃；进入松散润叶工序，将烟叶含水率提高至17％，烟叶温度提高至56℃；进入贮叶工序，贮叶温度32℃，贮叶时间4h；将叶丝宽度控制0.9mm；一级烘丝工序，进行高温气流干燥，干燥温度200℃；进行二级烘丝工序，进行低温滚筒干燥，干燥温度130℃；取样检测烟丝碱性香味成分释放量为244.31ug/g；进行加香，在叶丝中加入10％的醇类混合溶液，进行贮丝，贮丝温度32℃，贮丝时间72h。取样检测烟丝碱性香味成分总量为220.31ug/g.碱性香味成分含量下降了9.82％。
实施例1
巴西雪茄烟叶投料50kg，进入真空回潮工序，将雪茄烟叶含水率提高至15％，烟叶温度提高至50℃；进入松散润叶工序，将烟叶含水率提高至17％， 烟叶温度提高至56℃；进入贮叶工序，贮叶温度32℃，贮叶时间4h；将叶丝宽度控制0.9mm；一级烘丝工序，进行高温气流干燥，干燥温度200℃；进行二级烘丝工序，进行低温滚筒干燥，干燥温度130℃；取样检测烟丝碱性香味成分释放量为229.86ug/g；进行加香，在叶丝中加入30％的醇类混合溶液，进行贮丝，贮丝温度32℃，贮丝时间72h。取样检测烟丝碱性香味成分总量为260.93ug/g.碱性香味成分含量提高了13.52％。
实施例2
巴西雪茄烟叶投料50kg，进入真空回潮工序，将雪茄烟叶含水率提高至15％，烟叶温度提高至50℃；进入松散润叶工序，将烟叶含水率提高至17％，烟叶温度提高至56℃；进入贮叶工序，贮叶温度32℃，贮叶时间4h；将叶丝宽度控制0.9mm；一级烘丝工序，进行高温气流干燥，干燥温度200℃；进行二级烘丝工序，进行低温滚筒干燥，干燥温度130℃；取样检测烟丝碱性香味成分释放量为229.86ug/g；进行加香，在叶丝中加入20％的醇类混合溶液，进行贮丝，贮丝温度32℃，贮丝时间72h。取样检测烟丝碱性香味成分总量为233.62ug/g.碱性香味成分含量提高了1.64％。
实施例3
多米尼加雪茄烟叶投料50kg，进入真空回潮工序，将雪茄烟叶含水率提高至15％，烟叶温度提高至50℃；进入松散润叶工序，将烟叶含水率提高至17％，烟叶温度提高至56℃；进入贮叶工序，贮叶温度32℃，贮叶时间4h；将叶丝宽度控制0.9mm；一级烘丝工序，进行高温气流干燥，干燥温度200℃；进行二级烘丝工序，进行低温滚筒干燥，干燥温度130℃；取样检测烟丝碱性香味成分释放量为244.31ug/g；进行加香，在叶丝中加入30％的醇类混合溶液，进行贮丝，贮丝温度32℃，贮丝时间72h。取样检测烟丝碱性香味成分总量为271.19ug/g.碱性香味成分含量提高了11％。
实施例4
多米尼加雪茄烟叶投料50kg，进入真空回潮工序，将雪茄烟叶含水率提高至15％，烟叶温度提高至50℃；进入松散润叶工序，将烟叶含水率提高至17％，烟叶温度提高至56℃；进入贮叶工序，贮叶温度32℃，贮叶时间4h；将叶丝宽度控制0.9mm；一级烘丝工序，进行高温气流干燥，干燥温度200℃； 进行二级烘丝工序，进行低温滚筒干燥，干燥温度130℃；取样检测烟丝碱性香味成分释放量为244.31ug/g；进行加香，在叶丝中加入20％的醇类混合溶液，进行贮丝，贮丝温度32℃，贮丝时间72h。取样检测烟丝碱性香味成分总量为247.32ug/g.碱性香味成分含量提高了1.23％。
这里基于的术语和表述方式只是用于描述，本发明并不应局限于这些术语和表述。使用这些术语和表述并不意味着排除任何示意和描述(或其中部分)的等效特征，应认识到可能存在的各种修改也应包含在权利要求范围内。其他修改、变化和替换也可能存在。相应的，权利要求应视为覆盖所有这些等效物。
同样，需要指出的是，虽然本发明已参照当前的具体实施例来描述，但是本技术领域中的普通技术人员应当认识到，以上的实施例仅是用来说明本发明，在没有脱离本发明精神的情况下还可做出各种等效的变化或替换，因此，只要在本发明的实质精神范围内对上述实施例的变化、变型都将落在本发明的权利要求书的范围内。

Claims (9)

  1. 一种提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法，其特征在于，包括以下步骤：
    S1、将雪茄烟叶投料装桶，进入真空回潮工序，实现烟叶的初步提高含水率和温度；
    S2、步骤S1真空回潮后的烟叶进入松散润叶工序，实现烟叶的含水率进一步提高和完全松散；
    S3、步骤S2经过松散润叶后的烟叶进入贮叶工序，实现水分的吸收和平衡；
    S4、步骤S3贮叶后的烟叶进入切叶丝工序，将叶丝控制到设定宽度；
    S5、步骤S4的叶丝进入一级烘丝工序，进行高温气流干燥，实现叶丝含水率降至11％以下；
    S6、步骤S5一级烘丝后的叶丝进入二级烘丝工序，进行低温滚筒干燥，实现叶丝含水率降至4％以下；
    S7、步骤S6二级烘丝后的叶丝进入加香工序，在叶丝中加入醇类混合溶液；
    S8、步骤S7加香后的叶丝进入贮丝工序，实现醇类混合溶液在叶丝中吸收和平衡。
  2. 根据权利要求1所述的提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法，其特征在于，步骤S1中的真空回潮工序，将雪茄烟叶含水率提高至15％，烟叶温度提高至50℃。
  3. 根据权利要求1所述的提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法，其特征在于，步骤S2中的松散润叶工序，将雪茄烟叶含水率提高至17％，烟叶温度提高至56℃。
  4. 根据权利要求1所述的提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法，其特征在于，步骤S3中的贮叶工序，贮叶温度32℃，贮叶时间4h。
  5. 根据权利要求1所述的提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法，其特征在于，步骤S4中的切叶丝工序，将叶丝宽度控制0.9mm。
  6. 根据权利要求1所述的提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法，其特征在于，步骤S5中的一级烘丝工序，进行高温气流干燥，干燥温度200℃。
  7. 根据权利要求1所述的提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法，其特征在于，步骤S6中的二级烘丝工序，进行低温滚筒干燥，干燥温度130℃。
  8. 根据权利要求1所述的提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法，其特征在于，步骤S7中的加香工序，在叶丝中加入20％-30％的醇类混合溶液，所述醇类混合溶液由水、乙醇、丙三醇构成，质量比水：乙醇：丙三醇＝1:4:5。
  9. 根据权利要求1所述的提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法，其特征在于，步骤S8中的贮丝工序，贮丝温度32℃，贮丝时间72h。
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Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060144411A1 (en) * 2003-07-15 2006-07-06 Valentino Mercati Process for obtaining tobacco leaves with a standardized nicotine content and/or improved combustibility
CN101116527A (zh) * 2007-09-12 2008-02-06 厦门卷烟厂 一种卷烟加工过程中的叶丝干燥方法
CN109602061A (zh) * 2018-12-18 2019-04-12 湖北中烟工业有限责任公司 一种新型烟草用烟丝加工工艺
CN112754054A (zh) * 2021-01-20 2021-05-07 浙江中烟工业有限责任公司 一种新型加热卷烟烟丝的在线干燥方法
CN112998297A (zh) * 2021-03-19 2021-06-22 湖北中烟工业有限责任公司 一种改善雪茄烟叶品质的处理方法
CN114868949A (zh) * 2022-06-16 2022-08-09 浙江中烟工业有限责任公司 一种提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法

Family Cites Families (3)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN1211029C (zh) * 2000-01-07 2005-07-20 吴立祥 加热型烟具
CN103549643B (zh) * 2013-10-17 2016-02-03 川渝中烟工业有限责任公司 应用蒸汽爆破与干冰膨胀改善雪茄芯烟可用性的方法
CN103549657A (zh) * 2013-11-12 2014-02-05 黄争鸣 加热型低温卷烟及其制备方法

Patent Citations (6)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20060144411A1 (en) * 2003-07-15 2006-07-06 Valentino Mercati Process for obtaining tobacco leaves with a standardized nicotine content and/or improved combustibility
CN101116527A (zh) * 2007-09-12 2008-02-06 厦门卷烟厂 一种卷烟加工过程中的叶丝干燥方法
CN109602061A (zh) * 2018-12-18 2019-04-12 湖北中烟工业有限责任公司 一种新型烟草用烟丝加工工艺
CN112754054A (zh) * 2021-01-20 2021-05-07 浙江中烟工业有限责任公司 一种新型加热卷烟烟丝的在线干燥方法
CN112998297A (zh) * 2021-03-19 2021-06-22 湖北中烟工业有限责任公司 一种改善雪茄烟叶品质的处理方法
CN114868949A (zh) * 2022-06-16 2022-08-09 浙江中烟工业有限责任公司 一种提高加热卷烟中雪茄烟叶碱性香气成分释放量的方法

Non-Patent Citations (1)

* Cited by examiner, † Cited by third party
Title
AOXI JIN: "Cigar Process (II)", TOBACCO SCIENCE & TECHNOLOGY, 30 June 1979 (1979-06-30), pages 33 - 42, XP093117695 *

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