CN114343235B - Cooling smoke tube - Google Patents
Cooling smoke tube Download PDFInfo
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- CN114343235B CN114343235B CN202210123880.6A CN202210123880A CN114343235B CN 114343235 B CN114343235 B CN 114343235B CN 202210123880 A CN202210123880 A CN 202210123880A CN 114343235 B CN114343235 B CN 114343235B
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- smoke tube
- cooling
- hydroxypropyl methylcellulose
- master batch
- smoke
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- 239000000779 smoke Substances 0.000 title claims abstract description 75
- 238000001816 cooling Methods 0.000 title claims abstract description 63
- UFVKGYZPFZQRLF-UHFFFAOYSA-N hydroxypropyl methyl cellulose Chemical compound OC1C(O)C(OC)OC(CO)C1OC1C(O)C(O)C(OC2C(C(O)C(OC3C(C(O)C(O)C(CO)O3)O)C(CO)O2)O)C(CO)O1 UFVKGYZPFZQRLF-UHFFFAOYSA-N 0.000 claims abstract description 52
- 239000000463 material Substances 0.000 claims abstract description 43
- PEDCQBHIVMGVHV-UHFFFAOYSA-N Glycerine Chemical compound OCC(O)CO PEDCQBHIVMGVHV-UHFFFAOYSA-N 0.000 claims abstract description 36
- 239000001866 hydroxypropyl methyl cellulose Substances 0.000 claims abstract description 36
- 229920003088 hydroxypropyl methyl cellulose Polymers 0.000 claims abstract description 36
- 235000010979 hydroxypropyl methyl cellulose Nutrition 0.000 claims abstract description 36
- 239000004594 Masterbatch (MB) Substances 0.000 claims abstract description 35
- 238000010438 heat treatment Methods 0.000 claims abstract description 18
- 239000000203 mixture Substances 0.000 claims abstract description 15
- WRIDQFICGBMAFQ-UHFFFAOYSA-N (E)-8-Octadecenoic acid Natural products CCCCCCCCCC=CCCCCCCC(O)=O WRIDQFICGBMAFQ-UHFFFAOYSA-N 0.000 claims abstract description 12
- LQJBNNIYVWPHFW-UHFFFAOYSA-N 20:1omega9c fatty acid Natural products CCCCCCCCCCC=CCCCCCCCC(O)=O LQJBNNIYVWPHFW-UHFFFAOYSA-N 0.000 claims abstract description 12
- QSBYPNXLFMSGKH-UHFFFAOYSA-N 9-Heptadecensaeure Natural products CCCCCCCC=CCCCCCCCC(O)=O QSBYPNXLFMSGKH-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000005642 Oleic acid Substances 0.000 claims abstract description 12
- ZQPPMHVWECSIRJ-UHFFFAOYSA-N Oleic acid Natural products CCCCCCCCC=CCCCCCCCC(O)=O ZQPPMHVWECSIRJ-UHFFFAOYSA-N 0.000 claims abstract description 12
- 239000002202 Polyethylene glycol Substances 0.000 claims abstract description 12
- QXJSBBXBKPUZAA-UHFFFAOYSA-N isooleic acid Natural products CCCCCCCC=CCCCCCCCCC(O)=O QXJSBBXBKPUZAA-UHFFFAOYSA-N 0.000 claims abstract description 12
- ZQPPMHVWECSIRJ-KTKRTIGZSA-N oleic acid Chemical compound CCCCCCCC\C=C/CCCCCCCC(O)=O ZQPPMHVWECSIRJ-KTKRTIGZSA-N 0.000 claims abstract description 12
- 229920001223 polyethylene glycol Polymers 0.000 claims abstract description 12
- 238000001035 drying Methods 0.000 claims abstract description 11
- 239000000843 powder Substances 0.000 claims abstract description 11
- 238000001125 extrusion Methods 0.000 claims abstract description 10
- 241000208125 Nicotiana Species 0.000 claims description 37
- 235000002637 Nicotiana tabacum Nutrition 0.000 claims description 37
- 239000004800 polyvinyl chloride Substances 0.000 claims description 28
- 229920000915 polyvinyl chloride Polymers 0.000 claims description 28
- FAPWRFPIFSIZLT-UHFFFAOYSA-M Sodium chloride Chemical compound [Na+].[Cl-] FAPWRFPIFSIZLT-UHFFFAOYSA-M 0.000 claims description 24
- WYURNTSHIVDZCO-UHFFFAOYSA-N Tetrahydrofuran Chemical compound C1CCOC1 WYURNTSHIVDZCO-UHFFFAOYSA-N 0.000 claims description 24
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 claims description 14
- XSQUKJJJFZCRTK-UHFFFAOYSA-N Urea Chemical compound NC(N)=O XSQUKJJJFZCRTK-UHFFFAOYSA-N 0.000 claims description 13
- 239000004202 carbamide Substances 0.000 claims description 13
- 239000011780 sodium chloride Substances 0.000 claims description 12
- YLQBMQCUIZJEEH-UHFFFAOYSA-N tetrahydrofuran Natural products C=1C=COC=1 YLQBMQCUIZJEEH-UHFFFAOYSA-N 0.000 claims description 12
- 238000000034 method Methods 0.000 claims description 11
- 238000007670 refining Methods 0.000 claims description 11
- 125000006850 spacer group Chemical group 0.000 claims description 7
- 239000004698 Polyethylene Substances 0.000 claims description 6
- 238000004898 kneading Methods 0.000 claims description 6
- 238000002156 mixing Methods 0.000 claims description 6
- -1 polyethylene Polymers 0.000 claims description 6
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- 206010006784 Burning sensation Diseases 0.000 description 2
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 2
- 238000003723 Smelting Methods 0.000 description 2
- 238000010521 absorption reaction Methods 0.000 description 2
- 238000007792 addition Methods 0.000 description 2
- 229910052782 aluminium Inorganic materials 0.000 description 2
- XAGFODPZIPBFFR-UHFFFAOYSA-N aluminium Chemical compound [Al] XAGFODPZIPBFFR-UHFFFAOYSA-N 0.000 description 2
- 238000005452 bending Methods 0.000 description 2
- 238000004146 energy storage Methods 0.000 description 2
- 239000003546 flue gas Substances 0.000 description 2
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- 235000019505 tobacco product Nutrition 0.000 description 2
- QJZYHAIUNVAGQP-UHFFFAOYSA-N 3-nitrobicyclo[2.2.1]hept-5-ene-2,3-dicarboxylic acid Chemical compound C1C2C=CC1C(C(=O)O)C2(C(O)=O)[N+]([O-])=O QJZYHAIUNVAGQP-UHFFFAOYSA-N 0.000 description 1
- 241000894006 Bacteria Species 0.000 description 1
- 241001408630 Chloroclystis Species 0.000 description 1
- VEXZGXHMUGYJMC-UHFFFAOYSA-N Hydrochloric acid Chemical group Cl VEXZGXHMUGYJMC-UHFFFAOYSA-N 0.000 description 1
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- 239000011358 absorbing material Substances 0.000 description 1
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- JUPQTSLXMOCDHR-UHFFFAOYSA-N benzene-1,4-diol;bis(4-fluorophenyl)methanone Chemical compound OC1=CC=C(O)C=C1.C1=CC(F)=CC=C1C(=O)C1=CC=C(F)C=C1 JUPQTSLXMOCDHR-UHFFFAOYSA-N 0.000 description 1
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- 230000036541 health Effects 0.000 description 1
- 238000005338 heat storage Methods 0.000 description 1
- 239000004021 humic acid Substances 0.000 description 1
- 125000002887 hydroxy group Chemical group [H]O* 0.000 description 1
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- 229910052751 metal Inorganic materials 0.000 description 1
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Landscapes
- Manufacture Of Tobacco Products (AREA)
- Extrusion Moulding Of Plastics Or The Like (AREA)
Abstract
The application relates to the technical field of heating non-combustible cigarettes, in particular to a cooling smoke tube which is formed by extruding a master batch into a tube shape and then drying the tube shape, wherein the master batch comprises smoke powder, hydroxypropyl methylcellulose, polyethylene glycol, glycerol and oleic acid. The application provides a cooling material composition and a smoke tube prepared by extrusion drying of the composition, and the smoke tube has good deformation resistance and a multi-cavity structure on a physical level; in the chemical aspect, the smoke tube has good phase change performance, so that the smoke tube can be used as a supporting outer layer of a heating cigarette cooling material, not only can a supporting effect be provided, but also the suction resistance can not be reduced; the heat-insulating material can also be directly used as a cooling section for heating cigarettes, and has good cooling effect.
Description
Technical Field
The application relates to the technical field of heating non-combustible cigarettes, in particular to a cooling smoke tube.
Background
The highest temperature of the traditional cigarette is near thousand ℃ after lighting, a large amount of chemical substances can be released by high-temperature combustion and pyrolysis of the tobacco, and part of harmful ingredients are accumulated in a human body to a certain extent to cause damage to the health of the human body, so that various substitutes of the traditional cigarette, such as novel tobacco products such as buccal cigarettes, chewing cigarettes, electronic atomized cigarettes, heating non-combustible cigarettes (HnB cigarettes) and the like, are widely appeared in the market. In various novel tobacco products, the HnB cigarettes are similar to the traditional cigarettes in smoking quality and smoking habit, and have good application prospects.
However, when solid, liquid and gas with the same temperature are taken, the sensory temperature of a human body is sequentially increased, so that a consumer can feel a certain burning sensation when smoking HnB cigarettes, and certain damage is caused to the oral viscosity, tracheal mucosa and the like of the consumer, the burning sensation is even higher due to further shortening of the smoke heat exchange time in the later stage of smoking, the smoking quality of the cigarettes is influenced, and the method has great value for cooling research of heating non-burning cigarettes. At present, the cooling measures studied at home and abroad are mainly focused on two aspects of adding cooling materials and designing a cooling structure. The existing method for adding cooling materials is to add cooling materials such as heat absorbing materials, heat storage materials, heat conducting materials and the like into a cigarette filtering section to realize the transfer of smoke heat.
Such a low smoke temperature low resistance PLA tow filter stick and a method for preparing the same are disclosed in the patent document with publication number CN108523216SA, and the method for preparing the same comprises the steps of preparing a phase change material mixture, preparing a phase change material containing a fragrance substance, preparing a slow release fragrance filter stick and the like. According to the application, by combining the addition amount of the phase change material with the low-suction-resistance PLA tow filter stick, the overall suction taste of the cigarette and the heated non-combustible cigarette is improved through triple cooling, and the smoke temperature is reduced. The application uses PLA tow filter stick as carrier, loads phase change material containing aroma substances to achieve cooling effect, wherein the PLA polylactic acid glass transition temperature is about 70 ℃, glass transition can occur at the working temperature of heating cigarettes, melting or fusion bonding phenomenon can occur, and thus flue gas pore channels are blocked, and flue gas can not circulate smoothly.
To solve this problem, an improved cooling filter stick disclosed in the patent document with publication number CN108523220a and a low-temperature cigarette containing the same are disclosed, the cooling filter stick comprises a wrapping material layer and a cooling material sheet, the cooling material sheet is formed by compounding a supporting material layer and a polymer material layer, the cooling material sheet is configured to have a beam column with longitudinal gas passage channels arranged, the supporting material layer covers the surface of the polymer material layer, and the wrapping material layer wraps the cooling material sheet to form the beam column surface, so as to form the cooling filter stick. In this application, the polymer material layer retains its original shape when it is subjected to glass transition, wherein the material of the support material layer includes, but is not limited to, fiber, paper, heat-resistant and air-permeable polymer materials (PPS, PEEK, PI, etc.), metal materials, etc. However, fibers, paper, temperature-resistant and breathable polymer materials and the like have the problems of insufficient supporting strength and easy bending and deformation, and metal materials have the problems of no air holes and large cigarette smoke resistance.
Disclosure of Invention
The application aims to solve the problems and provides a cooling smoke tube.
The technical scheme for solving the problems is that the cooling smoke tube is formed by extruding a master batch into a tube shape and then drying the tube shape, wherein the master batch comprises smoke powder, hydroxypropyl methylcellulose, polyethylene glycol, glycerol and oleic acid.
In the application, a novel smoke tube is provided, the novel smoke tube can be used as a supporting outer layer of a heating cigarette cooling material, and compared with the supporting outer layer such as a fiber paper film in the prior art, the extruded and dried material has better deformation resistance, and the bending strength of the smoke tube is preferably 0.07-1.02Mpa. Compared with the metal support outer layer, the smoke tube has a porous structure, is favorable for absorbing the heat of the smoke in the smoke tube, and can effectively reduce the absorption resistance. Meanwhile, the smoke tube has good phase change property by combining and matching materials in the master batch, and has good cooling effect by matching with the porous structure, so that the smoke tube can be directly used as a cooling section for heating cigarettes without filling cooling materials, the cooling cost for heating the cigarettes is reduced, and a series of problems caused by melting phenomenon of the cooling materials in the working process are avoided.
The principle of the masterbatch with phase change property is that: polyethylene glycol, glycerol and oleic acid are excellent phase-change energy storage materials, but the phase-change process belongs to solid-liquid phase change, and the phase-change energy storage materials become liquid completely when heated to a temperature higher than the phase-change temperature, so that the transportation, storage and application of the phase-change materials are not facilitated. Therefore, the hydroxypropyl methylcellulose is added into the phase-change material, and is used as a polymer containing a large amount of hydroxyl groups, so that a plurality of crosslinking points can be provided for the phase-change material, and the hydroxypropyl methylcellulose is used as a curing agent of the phase-change material, is subjected to physical entanglement and chemical crosslinking with the phase-change material, and can play a role in binding the phase-change material, so that the phase-change material maintains the original shape (solid state) before and after phase change, and the shaped phase-change material is formed.
As the preferable mode of the application, the master batch comprises 70-80wt% of tobacco powder, 4-7wt% of hydroxypropyl methyl cellulose, 1-2 wt% of polyethylene glycol, 2-4 wt% of glycerol, 3-5 wt% of oleic acid and the balance of water.
As a preferred aspect of the present application, the master batch is prepared by: mixing tobacco powder, hydroxypropyl methylcellulose, polyethylene glycol, glycerol, oleic acid and water to obtain a mixture, and performing mud refining treatment on the mixture.
The mud-refining process is commonly used in the ceramic firing process, and means that the particle size of the material particles is reduced by a series of means, and each material is uniformly mixed, including a mode of mechanically refining mud by a mud-refining machine and a mode of manually refining mud.
Preferably, the inner cavity of the smoke tube is provided with a spacer to divide the inner cavity of the smoke tube into a plurality of smoke channels, and the spacer is formed by drying after the master batch is extruded. The structural design of the spacer can further improve the strength of the smoke tube. The surface area of the inner cavity of the smoke tube can be increased through a plurality of smoke channels formed by the spacers, so that more smoke can be contacted with the smoke tube when the smoke tube is used independently, and the cooling effect is improved; the smoke tube is also enabled to provide a plurality of fixing points for the cooling material in the smoke tube when the smoke tube is used for supporting the outer layer of the cooling material, the cooling material can be dispersed, the surface area of the cooling material is improved, and the cooling effect can be improved.
In order to further increase the pore structure on the smoke tube, the hydroxypropyl methylcellulose is preferably modified hydroxypropyl methylcellulose, and the modified hydroxypropyl methylcellulose is a composite material with hydroxypropyl methylcellulose as a shell and polyvinyl chloride as a core. As a preferred aspect of the present application, the modified hydroxypropyl methylcellulose is prepared by the steps of: respectively dissolving hydroxypropyl methylcellulose and polyvinyl chloride in tetrahydrofuran to obtain hydroxypropyl methylcellulose solution and polyvinyl chloride solution; the polyvinyl chloride solution was added dropwise to the hydroxypropyl methylcellulose solution with stirring, and then tetrahydrofuran was removed by heating.
The coefficient of thermal expansion and cold contraction of the polyvinyl chloride is about 80, and the polyvinyl chloride is easy to deform under different temperature conditions. Preferably, when the master batch is extruded into a tube shape, the extrusion temperature is 100-150 ℃; the drying temperature is 20-30deg.C during drying. By utilizing the characteristic, when the master batch is extruded, the polyvinyl chloride is heated to expand to drive the volume of the whole modified hydroxypropyl methylcellulose particles to expand, when the master batch is cooled after extrusion, the shrinkage degree of the polyvinyl chloride is large, and the shrinkage degree of the hydroxypropyl methylcellulose shell is small, so that the hydroxypropyl methylcellulose shell forms a pore structure between polyvinyl chloride cores.
In order to avoid swelling of the polyvinyl chloride closing the pore structure upon suction, it is therefore preferred to remove the polyvinyl chloride after the pore structure has been formed. In the preparation process of the master batch, sodium chloride and urea are added to pug obtained by pug while rolling to obtain a primary material, and the primary material is covered with a polyethylene film and then aged for 24-48 hours to obtain the master batch. Wherein, sodium chloride and urea mainly provide nutrition sources for the growth of stale microorganisms, and as the optimization of the application, the mixing mass ratio of the pug, the sodium chloride and the urea is 1000: (1-5): (1-5).
The aging is to promote the decay of organic matters in the pug to generate organic acid under the action of bacteria, so that the content of humic acid substances is increased and the decomposition of polyvinyl chloride is promoted. Meanwhile, the generated organic acid can be matched with urea added into the generated gas, and holes can be formed on pug in the gas escaping process, so that the hole quantity is improved.
The application has the beneficial effects that:
1. the application provides a cooling material composition and a smoke tube prepared by extrusion drying of the composition, and the smoke tube has good deformation resistance and a multi-cavity structure on a physical level; in the chemical aspect, the smoke tube has good phase change performance, so that the smoke tube can be used as a supporting outer layer of a heating cigarette cooling material, not only can a supporting effect be provided, but also the suction resistance can not be reduced; the heat-insulating material can also be directly used as a cooling section for heating cigarettes, and has good cooling effect.
2. The raw material of the smoke tube is mainly tobacco, and the smoke tube has the body fragrance of tobacco, and can release fragrance in the smoke passing process.
Detailed Description
The following is a specific embodiment of the present application and further describes the technical solution of the present application, but the present application is not limited to these examples.
Example 1
A cooling smoke tube is prepared through the following steps:
73 parts of tobacco powder, 4.2 parts of hydroxypropyl methylcellulose, 1.4 parts of polyethylene glycol, 2.1 parts of glycerol, 3.5 parts of oleic acid and 15.8 parts of water are mixed according to the parts by mass, and the total amount is 100 parts, and then the tobacco mixture is obtained by mixing the materials in a mixer for 30 minutes. Pouring the tobacco mixture into a vacuum mud refining machine, circularly refining mud for 3 times under the water cooling condition of water temperature of 25 ℃ to obtain tobacco mud, taking out the mud, putting the tobacco mud into an extruder, extruding the tobacco mud into a tubular structure at 120 ℃, airing the tobacco mud at 25 ℃ for three days, and cutting the tobacco mud into small sections with the length of 2cm to obtain the cooling smoke pipe.
Example 2
This embodiment is substantially the same as embodiment 1, except that:
in the application, pugs are taken out and put into an extruder, and a tubular structure with a spacer and a smoke channel in the inner cavity is extruded by using seven-core and six-fan extrusion dies at 120 ℃.
Example 3
This embodiment is substantially the same as embodiment 1, except that:
before extrusion, the tobacco pug obtained by circularly pugging 3 times is manually kneaded, and sodium chloride with the mass of 0.05 percent of the mass of the tobacco pug and urea with the mass of 0.05 percent of the mass of the tobacco pug are added every 5 minutes. Kneading for 30min, adding 0.3% sodium chloride and 0.3% urea to obtain initial material. Then the primary material is covered by a polyethylene film and then is put into a temperature of 25 ℃ and a humidity of 40 percent to be aged for 24 to 48 hours, thus obtaining the master batch. And then the master batch is put into an extruder for extrusion.
Example 4
This embodiment is substantially the same as embodiment 1, except that:
hydroxypropyl methylcellulose is replaced with modified hydroxypropyl methylcellulose of equal mass.
The modified hydroxypropyl methylcellulose is prepared by the steps of: according to the mass parts, respectively dissolving 10 parts of hydroxypropyl methylcellulose and 3 parts of polyvinyl chloride in tetrahydrofuran to obtain hydroxypropyl methylcellulose solution and polyvinyl chloride solution; the polyvinyl chloride solution was added dropwise to the hydroxypropyl methylcellulose solution with stirring, and then tetrahydrofuran was removed by heating to 70 ℃.
Example 5
This embodiment is substantially the same as embodiment 1, except that:
hydroxypropyl methylcellulose is replaced with modified hydroxypropyl methylcellulose of equal mass. The modified hydroxypropyl methylcellulose is prepared by the steps of: according to the mass parts, respectively dissolving 10 parts of hydroxypropyl methylcellulose and 3 parts of polyvinyl chloride in tetrahydrofuran to obtain hydroxypropyl methylcellulose solution and polyvinyl chloride solution; the polyvinyl chloride solution was added dropwise to the hydroxypropyl methylcellulose solution with stirring, and then tetrahydrofuran was removed by heating to 70 ℃.
Before extrusion, the tobacco pug obtained by circularly pugging 3 times is manually kneaded, and sodium chloride with the mass of 0.05 percent of the mass of the tobacco pug and urea with the mass of 0.05 percent of the mass of the tobacco pug are added every 5 minutes. Kneading for 30min, adding 0.3% sodium chloride and 0.3% urea to obtain initial material. Then the primary material is covered by a polyethylene film and then is put at 25 ℃ and 40% humidity for aging for 36 hours, thus obtaining the master batch. And then the master batch is put into an extruder for extrusion.
Example 6
A cooling smoke tube is prepared through the following steps:
according to the mass parts, respectively dissolving 10 parts of hydroxypropyl methylcellulose and 1 part of polyvinyl chloride in tetrahydrofuran to obtain hydroxypropyl methylcellulose solution and polyvinyl chloride solution; the polyvinyl chloride solution was added dropwise to the hydroxypropyl methylcellulose solution under stirring, and then tetrahydrofuran was removed by heating to 66 ℃ to obtain modified hydroxypropyl methylcellulose.
According to the mass parts, 70 parts of tobacco powder, 4 parts of modified hydroxypropyl methylcellulose, 1 part of polyethylene glycol, 2 parts of glycerol, 3 parts of oleic acid and 20 parts of water are mixed together, and then the tobacco mixture is obtained after the tobacco powder, the 4 parts of modified hydroxypropyl methylcellulose, the 1 parts of polyethylene glycol, the 2 parts of glycerol, the 3 parts of oleic acid and the 20 parts of water are mixed together for 20 minutes.
Pouring the tobacco mixture into a vacuum mud refining machine, and circularly refining mud for 1 time under the water cooling condition of water temperature of 20 ℃ to obtain the tobacco mud.
Adding sodium chloride accounting for 0.01% of the mass of the tobacco pug and urea accounting for 0.01% of the mass of the tobacco pug into the tobacco pug obtained by circularly pug for 1 time, and then manually kneading for 20min to obtain the primary material. And then the primary material is covered by a polyethylene film and then is put at 20 ℃ and 50% humidity for aging for 24 hours, so as to obtain the master batch.
Putting the master batch into an extruder, extruding the master batch into a tubular structure at 100 ℃, airing the master batch for three days at 20 ℃, and cutting the master batch into small sections with the length of 2cm to obtain the cooling smoke pipe.
Example 7
A cooling smoke tube is prepared through the following steps:
according to the mass parts, respectively dissolving 10 parts of hydroxypropyl methylcellulose and 5 parts of polyvinyl chloride in tetrahydrofuran to obtain hydroxypropyl methylcellulose solution and polyvinyl chloride solution; the polyvinyl chloride solution was added dropwise to the hydroxypropyl methylcellulose solution under stirring, and then tetrahydrofuran was removed by heating to 80 ℃ to obtain modified hydroxypropyl methylcellulose.
According to the mass parts, 80 parts of tobacco powder, 7 parts of modified hydroxypropyl methylcellulose, 2 parts of polyethylene glycol, 4 parts of glycerol, 5 parts of oleic acid and 2 parts of water are mixed, and the tobacco mixture is obtained after mixing the materials for 50 minutes in a mixer.
Pouring the tobacco mixture into a vacuum mud-smelting machine, and circularly smelting mud for 5 times under the water cooling condition of water temperature of 30 ℃ to obtain the tobacco mud.
And (3) manually kneading the tobacco pug obtained by circularly pugging for 6 times, wherein sodium chloride with the mass of 0.05% of the mass of the tobacco pug and urea with the mass of 0.05% of the mass of the tobacco pug are added every 5 minutes. Kneading for 50min, adding 0.5% sodium chloride and 0.5% urea to obtain initial material. Then the primary material is covered by a polyethylene film and then is put at 30 ℃ and 30% humidity for aging for 48 hours, thus obtaining the master batch.
And (3) putting the master batch into an extruder, extruding the master batch into a tubular structure at 150 ℃, airing the master batch for three days at 30 ℃, and cutting the master batch into small sections with the length of 2cm to obtain the cooling smoke pipe.
Comparative example 1
The PPS plastic pipe is used as the cooling smoke pipe, and the thickness, the inner diameter and the outer diameter and the length of the PPS plastic pipe are consistent with those of the cooling smoke pipe in the embodiment of the application.
Comparative example 2
The aluminum pipe is selected as the cooling smoke pipe, and the thickness, the inner diameter and the outer diameter and the length of the aluminum pipe are consistent with those of the cooling smoke pipe in the embodiment of the application.
[ detection of flexural Strength ]
The flexural strength of the smoke tube of the examples and comparative examples was measured by a universal tester, and the measurement results are shown in Table 1 below.
[ detection of Cooling efficiency ]
Thermocouple probes were inserted at both ends of the smoke tube in examples and comparative examples, respectively, so that the smoke flow passed through the smoke tube, and the temperatures at both ends of the smoke tube were measured, respectively, and the detection results were as shown in table 1 below.
[ resistance to suction detection ]
The physical properties of cigarettes and filter rods of examples and comparative examples were measured according to section 5 of GB/T22838.5-2009: the cigarette draw resistance and the filter rod pressure drop were measured, and the measurement results are shown in table 1 below.
TABLE 1
As is clear from Table 1, the smoke tube of the present application exhibits excellent properties in both flexural strength, efficiency in lowering temperature and low resistance to absorption.
The specific embodiments described herein are offered by way of example only to illustrate the spirit of the application. Those skilled in the art may make various modifications or additions to the described embodiments or substitutions thereof without departing from the spirit of the application or exceeding the scope of the application as defined in the accompanying claims.
Claims (8)
1. The utility model provides a cooling tobacco pipe which characterized in that: the smoke tube is formed by extruding a master batch into a tube shape and then drying, wherein the master batch comprises smoke powder, hydroxypropyl methyl cellulose, polyethylene glycol, glycerol and oleic acid;
the hydroxypropyl methylcellulose is modified hydroxypropyl methylcellulose, and the modified hydroxypropyl methylcellulose is a composite material with hydroxypropyl methylcellulose as a shell and polyvinyl chloride as a core;
the modified hydroxypropyl methylcellulose is prepared by the steps of: respectively dissolving hydroxypropyl methylcellulose and polyvinyl chloride in tetrahydrofuran to obtain hydroxypropyl methylcellulose solution and polyvinyl chloride solution; the polyvinyl chloride solution was added dropwise to the hydroxypropyl methylcellulose solution with stirring, and then tetrahydrofuran was removed by heating.
2. A cooling smoke tube according to claim 1, wherein: the master batch comprises 70-80wt% of tobacco powder, 4-7wt% of hydroxypropyl methyl cellulose, 1-2 wt% of polyethylene glycol, 2-4 wt% of glycerol, 3-5 wt% of oleic acid and the balance of water.
3. A cooling smoke tube according to claim 1, wherein: the master batch is prepared by the following steps: mixing tobacco powder, hydroxypropyl methylcellulose, polyethylene glycol, glycerol, oleic acid and water to obtain a mixture, and performing mud refining treatment on the mixture.
4. A cooling smoke tube according to claim 3, wherein: the method also comprises the following steps: and (3) kneading and twisting the mud material obtained by mud refining, adding sodium chloride and urea to obtain a primary material, coating the primary material with a polyethylene film, and ageing for 24-48 hours to obtain the master batch.
5. The cooling smoke tube according to claim 4, wherein: the mixing mass ratio of the pug to the sodium chloride to the urea is 1000: (1-5): (1-5).
6. A cooling smoke tube according to claim 1, wherein: extruding the master batch into a tube shape, wherein the extrusion temperature is 100-150 ℃; the drying temperature is 20-30deg.C during drying.
7. A cooling smoke tube according to claim 1, wherein: the inner cavity of the smoke tube is provided with a spacer to divide the inner cavity of the smoke tube into a plurality of smoke channels, and the spacer is formed by drying after the master batch is extruded.
8. A cooling smoke tube according to claim 1, wherein: the flexural strength of the smoke tube is 0.07-1.02Mpa.
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CN114916700A (en) * | 2022-05-31 | 2022-08-19 | 湖北中烟工业有限责任公司 | Aroma-releasing and cooling composite material for heating non-combustible cigarettes as well as preparation method and application of composite material |
CN114847512A (en) * | 2022-06-01 | 2022-08-05 | 湖北中烟工业有限责任公司 | Puffed tobacco powder cooling material, preparation method and application thereof |
CN114947170A (en) * | 2022-06-20 | 2022-08-30 | 江苏中烟工业有限责任公司 | Medicine-fragrance type heating non-combustion cigarette sheet and preparation method thereof |
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