CN104432477A - Method for processing cut stems of middle and top grade cigarettes - Google Patents
Method for processing cut stems of middle and top grade cigarettes Download PDFInfo
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- CN104432477A CN104432477A CN201410551491.9A CN201410551491A CN104432477A CN 104432477 A CN104432477 A CN 104432477A CN 201410551491 A CN201410551491 A CN 201410551491A CN 104432477 A CN104432477 A CN 104432477A
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- 235000019504 cigarettes Nutrition 0.000 title claims abstract description 52
- 238000000034 method Methods 0.000 title claims abstract description 24
- 238000012545 processing Methods 0.000 title claims abstract description 9
- 241000208125 Nicotiana Species 0.000 claims abstract description 22
- 235000002637 Nicotiana tabacum Nutrition 0.000 claims abstract description 21
- 239000000203 mixture Substances 0.000 claims abstract description 5
- 238000000605 extraction Methods 0.000 claims description 45
- 239000002904 solvent Substances 0.000 claims description 37
- 239000007788 liquid Substances 0.000 claims description 19
- ATUOYWHBWRKTHZ-UHFFFAOYSA-N Propane Chemical compound CCC ATUOYWHBWRKTHZ-UHFFFAOYSA-N 0.000 claims description 10
- LCGLNKUTAGEVQW-UHFFFAOYSA-N Dimethyl ether Chemical compound COC LCGLNKUTAGEVQW-UHFFFAOYSA-N 0.000 claims description 8
- NNPPMTNAJDCUHE-UHFFFAOYSA-N isobutane Chemical compound CC(C)C NNPPMTNAJDCUHE-UHFFFAOYSA-N 0.000 claims description 6
- 239000001273 butane Substances 0.000 claims description 5
- IJDNQMDRQITEOD-UHFFFAOYSA-N n-butane Chemical compound CCCC IJDNQMDRQITEOD-UHFFFAOYSA-N 0.000 claims description 5
- OFBQJSOFQDEBGM-UHFFFAOYSA-N n-pentane Natural products CCCCC OFBQJSOFQDEBGM-UHFFFAOYSA-N 0.000 claims description 5
- 239000001294 propane Substances 0.000 claims description 5
- LVGUZGTVOIAKKC-UHFFFAOYSA-N 1,1,1,2-tetrafluoroethane Chemical compound FCC(F)(F)F LVGUZGTVOIAKKC-UHFFFAOYSA-N 0.000 claims description 4
- VOPWNXZWBYDODV-UHFFFAOYSA-N Chlorodifluoromethane Chemical compound FC(F)Cl VOPWNXZWBYDODV-UHFFFAOYSA-N 0.000 claims description 4
- 229910018503 SF6 Inorganic materials 0.000 claims description 4
- SFZCNBIFKDRMGX-UHFFFAOYSA-N sulfur hexafluoride Chemical compound FS(F)(F)(F)(F)F SFZCNBIFKDRMGX-UHFFFAOYSA-N 0.000 claims description 4
- 229960000909 sulfur hexafluoride Drugs 0.000 claims description 4
- 239000001282 iso-butane Substances 0.000 claims description 3
- 238000012856 packing Methods 0.000 claims description 2
- RWRIWBAIICGTTQ-UHFFFAOYSA-N difluoromethane Chemical compound FCF RWRIWBAIICGTTQ-UHFFFAOYSA-N 0.000 claims 2
- 125000003963 dichloro group Chemical group Cl* 0.000 claims 1
- 230000001953 sensory effect Effects 0.000 abstract description 9
- 239000000126 substance Substances 0.000 abstract description 8
- 239000000463 material Substances 0.000 abstract description 3
- 239000000843 powder Substances 0.000 abstract description 2
- 238000009472 formulation Methods 0.000 abstract 1
- 239000000779 smoke Substances 0.000 description 10
- SNICXCGAKADSCV-JTQLQIEISA-N (-)-Nicotine Chemical compound CN1CCC[C@H]1C1=CC=CN=C1 SNICXCGAKADSCV-JTQLQIEISA-N 0.000 description 8
- 239000007789 gas Substances 0.000 description 8
- 229960002715 nicotine Drugs 0.000 description 8
- SNICXCGAKADSCV-UHFFFAOYSA-N nicotine Natural products CN1CCCC1C1=CC=CN=C1 SNICXCGAKADSCV-UHFFFAOYSA-N 0.000 description 8
- 238000001035 drying Methods 0.000 description 7
- 238000002156 mixing Methods 0.000 description 7
- 239000000047 product Substances 0.000 description 6
- 238000005096 rolling process Methods 0.000 description 6
- 206010013911 Dysgeusia Diseases 0.000 description 4
- 230000003247 decreasing effect Effects 0.000 description 4
- 238000011161 development Methods 0.000 description 3
- 230000007794 irritation Effects 0.000 description 3
- IJGRMHOSHXDMSA-UHFFFAOYSA-N Atomic nitrogen Chemical compound N#N IJGRMHOSHXDMSA-UHFFFAOYSA-N 0.000 description 2
- 102000004190 Enzymes Human genes 0.000 description 2
- 108090000790 Enzymes Proteins 0.000 description 2
- 210000002421 cell wall Anatomy 0.000 description 2
- 239000003795 chemical substances by application Substances 0.000 description 2
- PXBRQCKWGAHEHS-UHFFFAOYSA-N dichlorodifluoromethane Chemical compound FC(F)(Cl)Cl PXBRQCKWGAHEHS-UHFFFAOYSA-N 0.000 description 2
- 239000012530 fluid Substances 0.000 description 2
- 238000004519 manufacturing process Methods 0.000 description 2
- VNWKTOKETHGBQD-UHFFFAOYSA-N methane Chemical compound C VNWKTOKETHGBQD-UHFFFAOYSA-N 0.000 description 2
- 239000004338 Dichlorodifluoromethane Substances 0.000 description 1
- 241000196324 Embryophyta Species 0.000 description 1
- 241000208292 Solanaceae Species 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- 235000019404 dichlorodifluoromethane Nutrition 0.000 description 1
- 238000009792 diffusion process Methods 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 230000007071 enzymatic hydrolysis Effects 0.000 description 1
- 238000006047 enzymatic hydrolysis reaction Methods 0.000 description 1
- 238000011049 filling Methods 0.000 description 1
- 230000009931 harmful effect Effects 0.000 description 1
- 239000003915 liquefied petroleum gas Substances 0.000 description 1
- 244000005700 microbiome Species 0.000 description 1
- 229910052757 nitrogen Inorganic materials 0.000 description 1
- 239000005416 organic matter Substances 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000000926 separation method Methods 0.000 description 1
- 230000000391 smoking effect Effects 0.000 description 1
- 238000002791 soaking Methods 0.000 description 1
- 239000011343 solid material Substances 0.000 description 1
- 239000013589 supplement Substances 0.000 description 1
- 238000007738 vacuum evaporation Methods 0.000 description 1
- 210000003462 vein Anatomy 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B5/00—Stripping tobacco; Treatment of stems or ribs
- A24B5/16—Other treatment of stems or ribs, e.g. bending, chopping, incising
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B15/00—Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
- A24B15/18—Treatment of tobacco products or tobacco substitutes
- A24B15/24—Treatment of tobacco products or tobacco substitutes by extraction; Tobacco extracts
- A24B15/241—Extraction of specific substances
- A24B15/243—Nicotine
Landscapes
- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Manufacture Of Tobacco Products (AREA)
Abstract
一种中高档烟用梗丝处理方法,属于梗丝处理技术领域。使用本发明的方法对梗丝进行纯化处理后,梗丝的外观形状保持良好,同时降低了梗丝中焦油释放量,去掉了梗丝中可溶性物质,然后通过加料回填,补充烟末浸提物,改善梗丝感官质量,可以很好的用于高档卷烟配方中的添加。The invention discloses a method for processing cut stems for medium and high-grade tobacco, which belongs to the technical field of cut stem processing. After using the method of the present invention to purify the cut stems, the appearance of the cut stems remains good, and at the same time, the amount of tar released from the cut stems is reduced, the soluble substances in the cut stems are removed, and then the tobacco powder extract is supplemented by adding materials and backfilling , to improve the sensory quality of shredded stems, and can be well used in high-end cigarette formulations.
Description
技术领域 technical field
本发明属于梗丝处理技术领域,具体涉及一种中高档烟用梗丝处理方法。 The invention belongs to the technical field of cut stem processing, and in particular relates to a method for processing cut cut stems for medium and high-grade tobacco.
背景技术 Background technique
烟草是茄科烟草属植物,梗丝是烟叶之粗硬叶脉,约占叶重25%~30%,将其切丝后可添加于卷烟中。在中高档卷烟生产企业(烟草行业对于卷烟分五类,是按照卷烟调拨价格进行划分。这里中高档卷烟指的是一、二类卷烟),由于梗丝中含有不利于烟气、吸味及燃烧性的细胞壁物质,故其添加量极少,未能得到充分利用。作为烟草生产大国,每年我国烟叶的产量约240万吨,可产出烟梗约60万吨左右,其中能够得到有效利用的烟梗约40万吨左右,用于加工梗丝的烟梗约32万吨,制作烟草薄片的烟梗约8万吨,约有数十万吨梗丝废弃物被弃置浪费。开发“高香气、低焦油、低危害”的卷烟是我国卷烟产品的发展方向。梗丝作为卷烟产品中常用掺配品,具有填充性高、燃烧性好、在烟气中产生焦油量、危害性相对低的优点,使之用于高档卷烟产品,可以有效的控制卷烟的有害成分及焦油释放量。烟梗中总糖、总氮、烟碱和焦油含量较低,细胞壁物质含量较高(43%左右),与烟叶相比烟梗在燃吸时香气不足,吸味平淡,刺激性和劲头较小,杂气较重,尤其是木质气重。同时,由于梗丝干燥后颜色发白,与叶丝掺配后颜色不协调,影响卷后烟支外观。因此,烟梗本身存在的缺陷限制了其在中高档卷烟中的添加比例。随着生物技术的发展,许多研究者开始利用酶和微生物,改变劣等烟叶的吸食品质或提高烟梗的利用价值。 Tobacco is a plant of the genus Nicotiana in the family Solanaceae. The shredded stalk is the thick and hard vein of the tobacco leaf, accounting for about 25% to 30% of the leaf weight. It can be added to cigarettes after being shredded. In middle-to-high-end cigarette production enterprises (the tobacco industry divides cigarettes into five categories, which are divided according to the allocation price of cigarettes. Here, medium-to-high-end cigarettes refer to first- and second-class cigarettes), because the cut stems contain unfavorable smoke, taste and Combustible cell wall substances, so its addition is very small and cannot be fully utilized. As a big tobacco producing country, my country produces about 2.4 million tons of tobacco leaves each year, and about 600,000 tons of tobacco stems can be produced, of which about 400,000 tons of tobacco stems can be effectively used, and about 320,000 tons of tobacco stems are used for processing shredded stems. There are about 80,000 tons of tobacco stems for making tobacco sheets, and about hundreds of thousands of tons of shredded stems are discarded and wasted. The development of "high aroma, low tar, low harm" cigarettes is the development direction of my country's cigarette products. As a common blending product in cigarette products, shredded stems have the advantages of high filling capacity, good flammability, tar production in smoke, and relatively low hazard. It can be used in high-end cigarette products to effectively control the harmful effects of cigarettes. Composition and tar release. The content of total sugar, total nitrogen, nicotine and tar in tobacco stems is low, and the content of cell wall substances is relatively high (about 43%). Small, heavy miscellaneous gas, especially woody gas. At the same time, because the cut stems are whitish in color after drying, the color is not harmonious after being blended with the shredded leaves, which affects the appearance of the rolled cigarettes. Therefore, the defects in the tobacco stem itself limit its addition ratio in middle and high-grade cigarettes. With the development of biotechnology, many researchers began to use enzymes and microorganisms to change the smoking quality of inferior tobacco leaves or improve the utilization value of tobacco stems.
现有技术以直接处理梗丝居多,但由于梗丝结构致密,目前常规的利用酶制剂直接酶解梗丝的效果并不显著。若能提取出烟梗中的有效物质,并进行适当处理,去掉梗丝中可溶性物质,达到对梗丝纯化的目的。然后通过加料回填,补充浸提物,改善梗丝感官质量。这样不仅梗丝的品质能得到提高,而且能使梗丝得到更为充分的利用。 In the prior art, most of the cut stems are directly processed, but due to the compact structure of the cut stems, the effect of direct enzymatic hydrolysis of the cut stems by the conventional enzyme preparation is not significant. If the effective substances in the tobacco stems can be extracted and properly processed to remove the soluble substances in the shredded stems, the purpose of purifying the shredded stems can be achieved. Then backfill by adding materials to supplement the extract and improve the sensory quality of the shredded stems. In this way, not only the quality of the shredded stems can be improved, but also the shredded stems can be more fully utilized.
亚临界萃取是利用亚临界流体作为萃取剂,在密闭、无氧,低压的压力容器内,依据有机物相似相溶的原理,通过萃取物料与萃取剂在浸泡过程中的分子扩散过程,达到固体物料中的溶解性成分转移到液态的萃取剂中,再通过减压蒸发的过程将萃取剂与目的产物分离,最终得到目的产物的一种新型萃取与分离技术。亚临界流体是指某些化合物在温度高于其沸点但低于临界温度,且压力低于其临界压力的条件下,以液体形式存在的物质。主要有丙烷、丁烷、异丁烷、四氟乙烷(R134a)、二甲醚、六氟化硫、二氯二氟甲烷(氟利昂R12)和一氯二氟甲烷(氟利昂R22)等常温常压下为气体,经加压或降温容易液化的物质。 Subcritical extraction is to use subcritical fluid as the extraction agent, in a closed, oxygen-free, low-pressure pressure vessel, according to the principle of similar solubility of organic matter, through the molecular diffusion process of the extraction material and the extraction agent during the soaking process, to reach the solid material It is a new extraction and separation technology that transfers the soluble components in the liquid to the liquid extractant, and then separates the extractant from the target product through the process of vacuum evaporation, and finally obtains the target product. Subcritical fluid refers to the substance that some compounds exist in liquid form under the condition that the temperature is higher than its boiling point but lower than the critical temperature, and the pressure is lower than its critical pressure. There are mainly propane, butane, isobutane, tetrafluoroethane (R134a), dimethyl ether, sulfur hexafluoride, dichlorodifluoromethane (Freon R12) and monochlorodifluoromethane (Freon R22), etc. A substance that is gaseous when compressed, and is easily liquefied by pressurization or cooling.
发明内容 Contents of the invention
本发明的目的是为了提供一种中高档烟用梗丝处理方法。 The object of the present invention is to provide a method for processing cut stems for medium and high-grade tobacco.
基于上述目的,本发明采取了如下技术方案: Based on above-mentioned purpose, the present invention has taken following technical scheme:
一种中高档烟用梗丝处理方法,包括如下步骤:保证梗丝整丝率的前提下将其打包,整体置于密闭萃取容器中,向容器中注入具有一定压力的呈液态的萃取溶剂,将梗丝完全浸没,萃取30-50分钟,萃取温度为10-60℃;萃取溶剂为丙烷、丁烷、异丁烷、四氟乙烷、二甲醚、六氟化硫、二氯二氟甲烷、一氯二氟甲烷中的一种或几种的混合物;萃取结束后,在脱除溶剂的过程中,萃取容器内的温度保持在10-60℃,从容器下部抽出液体溶剂后,从容器的上部抽出气化的溶剂,梗丝中的溶剂完全脱除后,将梗丝包从容器中整体取出;梗丝萃取后,对梗丝进行加料,加料比例为2.0—2.5wt%,加料完成后,对梗丝进行膨胀干燥、加香、筛分处理,随后按照3—5wt%比例添加到中高档卷烟中。卷制的成品卷烟焦油含量和烟气烟碱量较未添加梗丝的卷烟有所降低,且在香气量、丰满程度、烟气流畅度和劲头等方面优于未添加梗丝的卷烟。 A method for processing cut stems for medium and high-grade cigarettes, comprising the following steps: packing the cut stems under the premise of ensuring the whole cut ratio, placing the whole in a closed extraction container, injecting a liquid extraction solvent with a certain pressure into the container, Submerge the shredded stem completely, extract for 30-50 minutes, the extraction temperature is 10-60°C; the extraction solvent is propane, butane, isobutane, tetrafluoroethane, dimethyl ether, sulfur hexafluoride, dichlorodifluoro One or more mixtures of methane and chlorodifluoromethane; after the extraction, during the process of removing the solvent, the temperature in the extraction vessel is kept at 10-60°C, and after the liquid solvent is drawn out from the lower part of the vessel, the The vaporized solvent is extracted from the upper part of the container, and after the solvent in the cut stems is completely removed, the cut stem bag is taken out from the container as a whole; After completion, the cut stems are expanded, dried, flavored and sieved, and then added to middle and high-grade cigarettes in a proportion of 3-5wt%. The tar content and smoke nicotine content of finished cigarettes are lower than those of cigarettes without cut stems, and are better than cigarettes without cut stems in terms of aroma, fullness, fluency and strength of smoke.
使用本发明的方法对梗丝进行纯化处理后,梗丝的外观形状保持良好,同时降低了梗丝中焦油释放量,去掉了梗丝中可溶性物质。然后通过加料回填,补充烟末浸提物,改善梗丝感官质量,可以很好的用于高档卷烟配方中的添加。 After using the method of the invention to purify the cut stems, the appearance and shape of the cut stems are kept good, while the amount of tar released in the cut stems is reduced, and the soluble substances in the cut stems are removed. Then by adding and backfilling, the tobacco powder extract is supplemented, the sensory quality of the cut stems is improved, and it can be well used for addition in high-grade cigarette formulas.
具体实施方式 Detailed ways
以下结合具体实施例对本发明的技术方案作进一步详细说明,但本发明的保护范围并不局限于此。 The technical solutions of the present invention will be described in further detail below in conjunction with specific examples, but the protection scope of the present invention is not limited thereto.
实施例1:取梗丝1000 kg,在保证梗丝整丝率的情况下将其打包,整体置于密闭萃取容器中,注入呈液态的丁烷萃取溶剂,将梗丝完全浸没,萃取30~50分钟,萃取温度为10~60℃;萃取结束后,在脱除溶剂的过程中,萃取容器内的温度保持在10~60℃,从容器下部抽出液体溶剂后,从容器的上部抽出气化的溶剂,梗丝中的溶剂完全脱除后,将梗丝包从容器中整体取出。梗丝加料工序出口水分为37%,出口温度为55℃,加料比例为2.3wt%;梗丝干燥工序热风温度为235℃、出口水分为13.5%;梗丝加香比例为0.5wt%,梗丝按照5wt%搀兑比例添加到中高档卷烟中。卷制成品后与未添加梗丝的卷烟成品比较,卷烟焦油含量减少0.31mg/支,烟气烟碱量减少0.04mg/支,感官质量总得分提高0.27分,主要表现为香气提升,余味舒适度增加。 Example 1: Take 1000 kg of shredded stems, pack them under the condition of ensuring the whole shredded stems, place the whole in a closed extraction container, inject liquid butane extraction solvent, completely submerge the shredded stems, and extract for 30~ 50 minutes, the extraction temperature is 10~60°C; after the extraction, during the process of removing the solvent, the temperature in the extraction container is kept at 10~60°C, after the liquid solvent is drawn from the lower part of the container, the vaporized After the solvent in the shredded stems is completely removed, the shredded stems package is taken out from the container as a whole. The outlet moisture in the cut stem feeding process is 37%, the outlet temperature is 55°C, and the feeding ratio is 2.3wt%; the hot air temperature in the cut stem drying process is 235°C, and the outlet moisture is 13.5%; Silk is added to medium and high-grade cigarettes according to the blending ratio of 5wt%. Compared with the finished cigarettes without shredded stems after rolling, the tar content of cigarettes decreased by 0.31mg/cigarette, the amount of nicotine in smoke decreased by 0.04mg/cigarettes, and the total score of sensory quality increased by 0.27 points, mainly manifested in the improvement of aroma and aftertaste. Increased comfort.
实施例2:取梗丝1000 kg,在保证梗丝整丝率的情况下将其打包,整体置于密闭萃取容器中,注入呈液态的丙烷萃取溶剂,将梗丝完全浸没,萃取35-45分钟,萃取温度为30-50℃;萃取结束后,在脱除溶剂的过程中,萃取容器内的温度保持在30-50℃,从容器下部抽出液体溶剂后,从容器的上部抽出气化的溶剂,梗丝中的溶剂完全脱除后,将梗丝包从容器中整体取出。梗丝加料工序出口水分为36%,出口温度为50℃,加料比例为2.0wt%;梗丝干燥工序热风温度为245℃、出口水分为13.2%;梗丝加香比例为0.5wt%,梗丝按照3wt%搀兑比例添加到中高档卷烟中。卷制成品后与未添加梗丝的卷烟成品比较,卷烟焦油含量减少0.23mg/支,烟气烟碱量减少0.03mg/支,感官质量总得分提高0.29分,主要表现为杂气和刺激性略有降低,余味舒适度增加。 Example 2: Take 1000 kg of shredded stems, pack it under the condition of ensuring the whole shredded ratio of the cut stems, place it in a closed extraction container as a whole, inject liquid propane extraction solvent, completely submerge the shredded stems, and extract for 35-45 Minutes, the extraction temperature is 30-50°C; after the extraction is completed, during the process of removing the solvent, the temperature in the extraction container is maintained at 30-50°C, after the liquid solvent is drawn out from the lower part of the container, the vaporized gas is drawn from the upper part of the container Solvent, after the solvent in the shredded stems is completely removed, the shredded stems package is taken out from the container as a whole. The outlet moisture in the cut stem feeding process is 36%, the outlet temperature is 50°C, and the feeding ratio is 2.0wt%; the hot air temperature in the cut stem drying process is 245°C, and the outlet moisture is 13.2%; Silk is added to medium and high-grade cigarettes according to the blending ratio of 3wt%. Compared with the finished cigarettes without shredded stems after rolling, the tar content of cigarettes is reduced by 0.23mg/cigarette, the amount of nicotine in smoke is reduced by 0.03mg/cigarettes, and the total score of sensory quality is increased by 0.29 points, mainly manifested as miscellaneous gas and irritation Sexiness is slightly reduced, and the aftertaste comfort is increased.
实施例3:取梗丝1000 kg,在保证梗丝整丝率的情况下将其打包,整体置于密闭萃取容器中,注入呈液态的二甲醚萃取溶剂,将梗丝完全浸没,萃取35-45分钟,萃取温度为30-50℃;萃取结束后,在脱除溶剂的过程中,萃取容器内的温度保持在30-50℃,从容器下部抽出液体溶剂后,从容器的上部抽出气化的溶剂,梗丝中的溶剂完全脱除后,将梗丝包从容器中整体取出。梗丝加料工序出口水分为36%,出口温度为50℃,加料比例为2.5wt%;梗丝干燥工序热风温度为245℃、出口水分为13.2%;梗丝加香比例为0.5wt%,梗丝按照5wt%搀兑比例添加到中高档卷烟中。卷制成品后与未添加梗丝的卷烟成品比较,卷烟焦油含量减少0.32mg/支,烟气烟碱量减少0.05mg/支,感官质量总得分提高0.26分,主要表现为香气提升,余味舒适度增加。 Example 3: Take 1000 kg of shredded stems, pack it under the condition of ensuring the whole shredded ratio of the cut stems, place the whole in a closed extraction container, inject liquid dimethyl ether extraction solvent, completely submerge the shredded stems, and extract for 35 -45 minutes, the extraction temperature is 30-50°C; after the extraction is completed, during the process of removing the solvent, the temperature in the extraction container is maintained at 30-50°C, after the liquid solvent is drawn from the lower part of the container, the gas is drawn from the upper part of the container After the solvent in the shredded stems is completely removed, the shredded stems package is taken out from the container as a whole. The outlet moisture in the cut stem feeding process is 36%, the outlet temperature is 50°C, and the feeding ratio is 2.5wt%; the hot air temperature in the cut stem drying process is 245°C, and the outlet moisture is 13.2%; Silk is added to medium and high-grade cigarettes according to the blending ratio of 5wt%. Compared with the finished cigarettes without shredded stems after rolling, the tar content of cigarettes is reduced by 0.32mg/cigarette, the amount of nicotine in smoke is reduced by 0.05mg/cigarettes, and the total score of sensory quality is increased by 0.26 points, mainly manifested in the improvement of aroma and aftertaste. Increased comfort.
实施例4:取梗丝1000 kg,在保证梗丝整丝率的情况下将其打包,整体置于密闭萃取容器中,注入呈液态1,1,1,2-四氟乙烷萃取溶剂,将梗丝完全浸没,萃取50分钟,萃取温度为30℃;萃取结束后,在脱除溶剂的过程中,萃取容器内的温度保持在30℃,从容器下部抽出液体溶剂后,从容器的上部抽出气化的溶剂,梗丝中的溶剂完全脱除后,将梗丝包从容器中整体取出。梗丝加料工序出口水分为36%,出口温度为45℃,加料比例为2.3wt%;梗丝干燥工序热风温度为240℃、出口水分为13.3%;梗丝加香比例为0.5wt%,梗丝按照3wt%搀兑比例添加到中高档卷烟中。卷制成品后与未添加梗丝的卷烟成品比较,卷烟焦油含量减少0.25mg/支,烟气烟碱量减少0.03mg/支,感官质量总得分提高0.32分,主要表现为杂气和刺激性略有降低。 Example 4: Take 1000 kg of cut stems, pack them under the condition of ensuring the whole cut stems, place the whole in a closed extraction container, inject liquid 1,1,1,2-tetrafluoroethane extraction solvent, Submerge the shredded stems completely, extract for 50 minutes, and the extraction temperature is 30°C; The vaporized solvent is drawn out, and after the solvent in the shredded stems is completely removed, the shredded stems package is taken out from the container as a whole. The outlet moisture in the cut stem feeding process is 36%, the outlet temperature is 45°C, and the feeding ratio is 2.3wt%; the hot air temperature in the cut stem drying process is 240°C, and the outlet moisture is 13.3%; Silk is added to medium and high-grade cigarettes according to the blending ratio of 3wt%. Compared with the finished cigarettes without shredded stems after rolling, the tar content of cigarettes is reduced by 0.25mg/cigarette, the amount of nicotine in smoke is reduced by 0.03mg/cigarettes, and the total score of sensory quality is increased by 0.32 points, mainly manifested as miscellaneous gas and irritation Sex is slightly reduced.
实施例5:取梗丝1000 kg,在保证梗丝整丝率的情况下将其打包,整体置于密闭萃取容器中,注入呈液态的六氟化硫萃取溶剂,将梗丝完全浸没,萃取30分钟,萃取温度为50℃;萃取结束后,在脱除溶剂的过程中,萃取容器内的温度保持在50℃,从容器下部抽出液体溶剂后,从容器的上部抽出气化的溶剂,梗丝中的溶剂完全脱除后,将梗丝包从容器中整体取出。梗丝加料工序出口水分为37%,出口温度为55℃,加料比例为2.5wt%;梗丝干燥工序热风温度为235℃、出口水分为13.5%;梗丝加香比例为0.5wt%,梗丝按照3wt%搀兑比例添加到中高档卷烟中。卷制成品后与未添加梗丝的卷烟成品比较,卷烟焦油含量减少0.23mg/支,烟气烟碱量减少0.04mg/支,感官质量总得分提高0.30分,主要表现为杂气和刺激性略有降低。 Example 5: Take 1000 kg of shredded stems, pack it under the condition of ensuring the whole shredded ratio of the cut stems, place it in a closed extraction container as a whole, inject liquid sulfur hexafluoride extraction solvent, completely submerge the shredded stems, and extract 30 minutes, the extraction temperature is 50°C; after the extraction is completed, during the process of removing the solvent, the temperature in the extraction container is kept at 50°C, and after the liquid solvent is drawn out from the lower part of the container, the vaporized solvent is drawn out from the upper part of the container. After the solvent in the shreds is completely removed, the shredded stem package is taken out from the container as a whole. The outlet moisture in the cut stem feeding process is 37%, the outlet temperature is 55°C, and the feeding ratio is 2.5wt%; the hot air temperature in the cut stem drying process is 235°C, and the outlet moisture is 13.5%; Silk is added to medium and high-grade cigarettes according to the blending ratio of 3wt%. Compared with the finished cigarettes without shredded stems after rolling, the tar content of cigarettes is reduced by 0.23mg/cigarette, the amount of nicotine in smoke is reduced by 0.04mg/cigarettes, and the total score of sensory quality is increased by 0.30 points, mainly manifested as miscellaneous gas and irritation Sex is slightly reduced.
实施例6:取梗丝1000 kg,在保证梗丝整丝率的情况下将其打包,整体置于密闭萃取容器中,注入呈液态的丙烷和丁烷的混合物液化石油气萃取溶剂,将梗丝完全浸没,萃取50分钟,萃取温度为40℃;萃取结束后,在脱除溶剂的过程中,萃取容器内的温度保持在40℃,从容器下部抽出液体溶剂后,从容器的上部抽出气化的溶剂,梗丝中的溶剂完全脱除后,将梗丝包从容器中整体取出。梗丝加料工序出口水分为37%,出口温度为55℃,加料比例为2.3wt%;梗丝干燥工序热风温度为245℃、出口水分为13.2%;梗丝加香比例为0.5wt%,梗丝按照5wt%搀兑比例添加到中高档卷烟中。卷制成品后与未添加梗丝的卷烟成品比较,卷烟焦油含量减少0.36mg/支,烟气烟碱量减少0.06mg/支,感官质量总得分提高0.22分,主要表现为余味舒适度增加。 Example 6: Take 1000 kg of shredded stems, pack it under the condition of ensuring the whole shredded ratio of stems, and place it in a closed extraction container as a whole, inject a mixture of liquid propane and butane as an extraction solvent of liquefied petroleum gas, and extract the stems The silk is completely submerged, extracted for 50 minutes, and the extraction temperature is 40°C; after the extraction is completed, during the process of removing the solvent, the temperature in the extraction container is kept at 40°C, after the liquid solvent is drawn from the lower part of the container, the gas is drawn from the upper part of the container After the solvent in the shredded stems is completely removed, the shredded stems package is taken out from the container as a whole. The outlet moisture in the cut stem feeding process is 37%, the outlet temperature is 55°C, and the feeding ratio is 2.3wt%; the hot air temperature in the cut stem drying process is 245°C, and the outlet moisture is 13.2%; Silk is added to medium and high-grade cigarettes according to the blending ratio of 5wt%. Compared with the finished cigarettes without shredded stems after rolling, the tar content of cigarettes decreased by 0.36mg/cigarette, the amount of nicotine in smoke decreased by 0.06mg/cigarettes, and the total score of sensory quality increased by 0.22 points, mainly manifested in the increase of aftertaste comfort .
以上列举的仅是实现本发明的几个具体实施例。显然,本发明不限于以上实施例,还可以有许多变形。本领域的普通技术人员能从本发明公开的内容直接导出或联想到的所有变形,均应认为是本发明的保护范围。 What are listed above are only a few specific embodiments for realizing the present invention. Obviously, the present invention is not limited to the above embodiments, and many variations are possible. All deformations that can be directly derived or associated by those skilled in the art from the content disclosed in the present invention should be considered as the protection scope of the present invention.
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