CN101606754A - Preparation and Application of Thermally Stabilized Manganese Oxide Molecular Sieve Catalyst for Reducing CO and NO in Cigarette Smoke - Google Patents
Preparation and Application of Thermally Stabilized Manganese Oxide Molecular Sieve Catalyst for Reducing CO and NO in Cigarette Smoke Download PDFInfo
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- AMWRITDGCCNYAT-UHFFFAOYSA-L hydroxy(oxo)manganese;manganese Chemical compound [Mn].O[Mn]=O.O[Mn]=O AMWRITDGCCNYAT-UHFFFAOYSA-L 0.000 title claims abstract description 82
- 235000019504 cigarettes Nutrition 0.000 title claims abstract description 66
- 239000003054 catalyst Substances 0.000 title claims abstract description 47
- 239000002808 molecular sieve Substances 0.000 title claims abstract description 45
- URGAHOPLAPQHLN-UHFFFAOYSA-N sodium aluminosilicate Chemical compound [Na+].[Al+3].[O-][Si]([O-])=O.[O-][Si]([O-])=O URGAHOPLAPQHLN-UHFFFAOYSA-N 0.000 title claims abstract description 45
- 239000000779 smoke Substances 0.000 title claims abstract description 31
- 238000002360 preparation method Methods 0.000 title claims abstract description 8
- 229910002091 carbon monoxide Inorganic materials 0.000 title abstract description 19
- 239000000463 material Substances 0.000 claims abstract description 23
- 229910021645 metal ion Inorganic materials 0.000 claims abstract description 12
- 238000006243 chemical reaction Methods 0.000 claims description 13
- SQQMAOCOWKFBNP-UHFFFAOYSA-L manganese(II) sulfate Chemical compound [Mn+2].[O-]S([O-])(=O)=O SQQMAOCOWKFBNP-UHFFFAOYSA-L 0.000 claims description 13
- 230000009467 reduction Effects 0.000 claims description 13
- 229940099596 manganese sulfate Drugs 0.000 claims description 10
- 235000007079 manganese sulphate Nutrition 0.000 claims description 10
- 239000011702 manganese sulphate Substances 0.000 claims description 10
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- 229910052802 copper Inorganic materials 0.000 claims description 5
- 239000008367 deionised water Substances 0.000 claims description 5
- 229910021641 deionized water Inorganic materials 0.000 claims description 5
- 239000002245 particle Substances 0.000 claims description 5
- 229910052709 silver Inorganic materials 0.000 claims description 5
- 229910001960 metal nitrate Inorganic materials 0.000 claims description 4
- 239000002244 precipitate Substances 0.000 claims description 4
- 229910002651 NO3 Inorganic materials 0.000 claims description 3
- NHNBFGGVMKEFGY-UHFFFAOYSA-N Nitrate Chemical compound [O-][N+]([O-])=O NHNBFGGVMKEFGY-UHFFFAOYSA-N 0.000 claims description 3
- 229910001437 manganese ion Inorganic materials 0.000 claims description 3
- 229910052751 metal Inorganic materials 0.000 claims description 3
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- 101001018064 Homo sapiens Lysosomal-trafficking regulator Proteins 0.000 claims 1
- 102100033472 Lysosomal-trafficking regulator Human genes 0.000 claims 1
- 235000010703 Modiola caroliniana Nutrition 0.000 claims 1
- 244000038561 Modiola caroliniana Species 0.000 claims 1
- 238000006555 catalytic reaction Methods 0.000 claims 1
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- 230000003197 catalytic effect Effects 0.000 abstract description 13
- 239000000843 powder Substances 0.000 abstract description 5
- 241000208125 Nicotiana Species 0.000 description 25
- 235000002637 Nicotiana tabacum Nutrition 0.000 description 25
- FMMWHPNWAFZXNH-UHFFFAOYSA-N Benz[a]pyrene Chemical compound C1=C2C3=CC=CC=C3C=C(C=C3)C2=C2C3=CC=CC2=C1 FMMWHPNWAFZXNH-UHFFFAOYSA-N 0.000 description 16
- 238000002485 combustion reaction Methods 0.000 description 12
- 239000003463 adsorbent Substances 0.000 description 10
- 238000006722 reduction reaction Methods 0.000 description 10
- 150000004945 aromatic hydrocarbons Chemical class 0.000 description 8
- 239000007800 oxidant agent Substances 0.000 description 8
- 238000007254 oxidation reaction Methods 0.000 description 7
- 230000001590 oxidative effect Effects 0.000 description 7
- 238000001179 sorption measurement Methods 0.000 description 7
- UGFAIRIUMAVXCW-UHFFFAOYSA-N Carbon monoxide Chemical compound [O+]#[C-] UGFAIRIUMAVXCW-UHFFFAOYSA-N 0.000 description 6
- QVGXLLKOCUKJST-UHFFFAOYSA-N atomic oxygen Chemical compound [O] QVGXLLKOCUKJST-UHFFFAOYSA-N 0.000 description 6
- 230000000694 effects Effects 0.000 description 6
- 239000003546 flue gas Substances 0.000 description 6
- 239000001301 oxygen Substances 0.000 description 6
- 229910052760 oxygen Inorganic materials 0.000 description 6
- SQGYOTSLMSWVJD-UHFFFAOYSA-N silver(1+) nitrate Chemical compound [Ag+].[O-]N(=O)=O SQGYOTSLMSWVJD-UHFFFAOYSA-N 0.000 description 6
- 230000000391 smoking effect Effects 0.000 description 6
- 239000000126 substance Substances 0.000 description 5
- GRYLNZFGIOXLOG-UHFFFAOYSA-N Nitric acid Chemical compound O[N+]([O-])=O GRYLNZFGIOXLOG-UHFFFAOYSA-N 0.000 description 4
- 238000005336 cracking Methods 0.000 description 4
- 230000036541 health Effects 0.000 description 4
- 229910017604 nitric acid Inorganic materials 0.000 description 4
- 239000011148 porous material Substances 0.000 description 4
- SWGJCIMEBVHMTA-UHFFFAOYSA-K trisodium;6-oxido-4-sulfo-5-[(4-sulfonatonaphthalen-1-yl)diazenyl]naphthalene-2-sulfonate Chemical compound [Na+].[Na+].[Na+].C1=CC=C2C(N=NC3=C4C(=CC(=CC4=CC=C3O)S([O-])(=O)=O)S([O-])(=O)=O)=CC=C(S([O-])(=O)=O)C2=C1 SWGJCIMEBVHMTA-UHFFFAOYSA-K 0.000 description 4
- ZLMJMSJWJFRBEC-UHFFFAOYSA-N Potassium Chemical compound [K] ZLMJMSJWJFRBEC-UHFFFAOYSA-N 0.000 description 3
- 230000008901 benefit Effects 0.000 description 3
- 230000015572 biosynthetic process Effects 0.000 description 3
- 238000009833 condensation Methods 0.000 description 3
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- 238000005516 engineering process Methods 0.000 description 3
- 239000000203 mixture Substances 0.000 description 3
- 230000003647 oxidation Effects 0.000 description 3
- 229910052700 potassium Inorganic materials 0.000 description 3
- 239000011591 potassium Substances 0.000 description 3
- 229910001961 silver nitrate Inorganic materials 0.000 description 3
- 230000006378 damage Effects 0.000 description 2
- 239000007789 gas Substances 0.000 description 2
- NUJOXMJBOLGQSY-UHFFFAOYSA-N manganese dioxide Chemical compound O=[Mn]=O NUJOXMJBOLGQSY-UHFFFAOYSA-N 0.000 description 2
- 150000001247 metal acetylides Chemical class 0.000 description 2
- 206010007269 Carcinogenicity Diseases 0.000 description 1
- QPLDLSVMHZLSFG-UHFFFAOYSA-N Copper oxide Chemical compound [Cu]=O QPLDLSVMHZLSFG-UHFFFAOYSA-N 0.000 description 1
- 239000005751 Copper oxide Substances 0.000 description 1
- 229920000742 Cotton Polymers 0.000 description 1
- 206010021143 Hypoxia Diseases 0.000 description 1
- 241001465754 Metazoa Species 0.000 description 1
- 206010057852 Nicotine dependence Diseases 0.000 description 1
- ATJFFYVFTNAWJD-UHFFFAOYSA-N Tin Chemical compound [Sn] ATJFFYVFTNAWJD-UHFFFAOYSA-N 0.000 description 1
- 208000025569 Tobacco Use disease Diseases 0.000 description 1
- 229910052770 Uranium Inorganic materials 0.000 description 1
- 229910021536 Zeolite Inorganic materials 0.000 description 1
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- 230000007670 carcinogenicity Effects 0.000 description 1
- 231100000260 carcinogenicity Toxicity 0.000 description 1
- 238000010531 catalytic reduction reaction Methods 0.000 description 1
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- 229910000431 copper oxide Inorganic materials 0.000 description 1
- 230000009849 deactivation Effects 0.000 description 1
- 230000007547 defect Effects 0.000 description 1
- HNPSIPDUKPIQMN-UHFFFAOYSA-N dioxosilane;oxo(oxoalumanyloxy)alumane Chemical compound O=[Si]=O.O=[Al]O[Al]=O HNPSIPDUKPIQMN-UHFFFAOYSA-N 0.000 description 1
- 229940079593 drug Drugs 0.000 description 1
- 239000003814 drug Substances 0.000 description 1
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- UQSXHKLRYXJYBZ-UHFFFAOYSA-N iron oxide Inorganic materials [Fe]=O UQSXHKLRYXJYBZ-UHFFFAOYSA-N 0.000 description 1
- 230000007246 mechanism Effects 0.000 description 1
- 229910000000 metal hydroxide Inorganic materials 0.000 description 1
- 150000004692 metal hydroxides Chemical class 0.000 description 1
- 229910044991 metal oxide Inorganic materials 0.000 description 1
- 150000004706 metal oxides Chemical class 0.000 description 1
- QJGQUHMNIGDVPM-UHFFFAOYSA-N nitrogen group Chemical group [N] QJGQUHMNIGDVPM-UHFFFAOYSA-N 0.000 description 1
- 150000002894 organic compounds Chemical class 0.000 description 1
- 238000000197 pyrolysis Methods 0.000 description 1
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- 230000004083 survival effect Effects 0.000 description 1
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- 238000005979 thermal decomposition reaction Methods 0.000 description 1
- 150000003606 tin compounds Chemical class 0.000 description 1
- 235000019505 tobacco product Nutrition 0.000 description 1
- 229910052723 transition metal Inorganic materials 0.000 description 1
- 229910000314 transition metal oxide Inorganic materials 0.000 description 1
- 150000003624 transition metals Chemical class 0.000 description 1
- 239000010457 zeolite Substances 0.000 description 1
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- Catalysts (AREA)
Abstract
降低卷烟烟气CO、NO热稳氧化锰分子筛催化剂的制备及应用,将氧化锰分子筛用作降低3卷烟烟气CO、NO的催化材料。所述的氧化锰分子筛掺杂有金属离子。本发明的催化剂为可在高温下达到600-700℃的热稳定性材料,沿着卷烟燃烧方向更长距离内具有催化活性,相比于前面所述催化剂更具有优势,且该材料在温度200℃左右即具有高的催化活性。催化剂粉末具备的热稳定性使得其只在卷烟燃烧区最高温度点才裂解,继而保证了在卷烟烟支段更大区域内和更宽温度范围(200-600℃)内能有效降低CO、NO。Preparation and application of heat-stable manganese oxide molecular sieve catalysts for reducing CO and NO in cigarette smoke. Manganese oxide molecular sieves were used as catalytic materials for reducing CO and NO in cigarette smoke. The manganese oxide molecular sieve is doped with metal ions. The catalyst of the present invention is a thermally stable material that can reach 600-700°C at a high temperature, and has catalytic activity in a longer distance along the cigarette burning direction, which is more advantageous than the aforementioned catalyst, and the material can be used at a temperature of 200 It has high catalytic activity at about ℃. The thermal stability of the catalyst powder enables it to be cracked only at the highest temperature point in the cigarette burning zone, thereby ensuring that CO and NO can be effectively reduced in a larger area and a wider temperature range (200-600°C) in the cigarette branch section. .
Description
技术领域 technical field
本发明属于卷烟制备技术领域,具体地说涉及一种降低卷烟烟气有害物质CO、NO的热稳定分子筛催化剂,该催化剂的制备方法与应用。The invention belongs to the technical field of cigarette preparation, and in particular relates to a heat-stable molecular sieve catalyst for reducing CO and NO, which are harmful substances in cigarette smoke, and a preparation method and application of the catalyst.
背景技术 Background technique
自从16世纪初烟草由美洲传入欧洲以后,人们对吸烟与健康问题产生了不同的意见和争论,特别是1954年英国皇家医学会正式发表了“吸烟与健康”的报告,综述了流行病学研究、烟草消耗趋势、烟草化学成分及其致癌性、吸烟对人和动物的制病机制等多方面的资料,明确提出吸烟对人体健康是有害的,如烟气CO能导致组织缺氧。2003年5月21日,第56届世界卫生大会上通过了WHO制定的、各成员国政府已签署的《烟草控制框架公约》不仅规定了各国政府要采取和实行有效的立法、行政或其它措施防止和减少烟草消费、烟碱成瘾和接触烟草烟气等,而且还要求对烟草制品成分进行限制。同时随着人们生活水平和生活质量的不断提高,消费者对吸烟的安全性和环境保护意识也越来越强,国际烟草面临前所未有的压力。开发低危害卷烟不仅是烟草行业发展和生存的必然趋势,也是国家烟草专卖局关于行业卷烟减害降焦的发展战略之一。Since tobacco was introduced to Europe from the Americas in the early 16th century, people have had different opinions and debates on smoking and health issues. In particular, the Royal Society of Medicine officially published a report on "Smoking and Health" in 1954, which reviewed the epidemiological Research, tobacco consumption trends, tobacco chemical components and their carcinogenicity, and the mechanism of smoking on humans and animals have clearly pointed out that smoking is harmful to human health, such as smoke CO can lead to tissue hypoxia. On May 21, 2003, the 56th World Health Assembly passed the "Framework Convention on Tobacco Control" formulated by WHO and signed by the governments of member states. It not only stipulates that governments must adopt and implement effective legislative, administrative or other measures Prevent and reduce tobacco consumption, nicotine addiction and exposure to tobacco smoke, etc., but also require restrictions on the content of tobacco products. At the same time, with the continuous improvement of people's living standards and quality of life, consumers are increasingly aware of smoking safety and environmental protection, and International Tobacco is facing unprecedented pressure. The development of low-harm cigarettes is not only an inevitable trend for the development and survival of the tobacco industry, but also one of the development strategies of the State Tobacco Monopoly Administration on reducing the harm and tar of cigarettes in the industry.
为了降低卷烟烟气中的有害物质,最初在卷烟滤嘴中使用了某些特殊的滤材,包括棉花、纤维素和一些人造纤维。但是,这些滤棒一般只能降低卷烟烟气粒相成份和烟气中可冷凝成份,而对卷烟烟气气相成分如CO、NO、和/或挥发性成分却没有降低去除效果。烟草科技工作者还尝试在卷烟滤嘴中使用各种吸附剂,以期达到对部分CO进行物理吸附。如美国专利No.4193412报导一种滤嘴吸附剂,它是两种高度分散的金属氧化物或金属氢氧化物的混合物。该吸附剂对提高吸附卷烟烟气某些物质有促进作用。美国专利No.3407820报导了一种含氧化锰物质的卷烟滤嘴,该滤嘴能降低卷烟烟气NOx的释放量。但很显然吸附剂吸附CO的效果并不理想。众所周知,对CO具有吸附能力的吸附剂同时亦能吸附O2。当卷烟置放在空气中时,O2先被牢牢吸附在吸附剂上,吸附剂上的吸附点达到吸附饱和后,不能再吸附CO。许多已报导的吸附剂实际上都可吸附CO2气体,但是这意味着必须采取另外的方式将CO转化为CO2,这样才能被吸附剂吸附。In order to reduce harmful substances in cigarette smoke, some special filter materials, including cotton, cellulose and some artificial fibers, were initially used in cigarette filters. However, these filter rods can generally only reduce the particle phase components of cigarette smoke and the condensable components in the smoke, but do not reduce the removal effect on the gas phase components of cigarette smoke such as CO, NO, and/or volatile components. Tobacco scientific and technological workers also try to use various adsorbents in cigarette filters in order to achieve physical adsorption of part of CO. As reported in US Patent No. 4193412, a filter adsorbent is a mixture of two highly dispersed metal oxides or metal hydroxides. The adsorbent can promote the adsorption of certain substances in cigarette smoke. US Patent No. 3407820 reports a cigarette filter tip containing manganese oxide substance, which can reduce the emission of NOx in cigarette smoke. However, it is clear that the adsorption effect of the adsorbent on CO adsorption is not ideal. It is well known that an adsorbent capable of adsorbing CO can also adsorb O 2 . When the cigarette is placed in the air, O2 is first firmly adsorbed on the adsorbent, and after the adsorption point on the adsorbent reaches adsorption saturation, CO cannot be adsorbed any more. Many of the reported adsorbents can actually adsorb CO 2 gas, but this means that another way must be used to convert CO to CO 2 before it can be adsorbed by the adsorbent.
另外一种降低CO的方法在滤嘴里添加氧化剂或者催化剂,将CO转化成CO2。美国专利No.4317460描述了一种在低温下将CO氧化成CO2的锡或锡的化合物催化剂,将这些催化剂和其他的催化材料负载在微孔载体上。但是,这种催化剂放在滤嘴中存在不可避免的缺陷,如在一般吸烟条件下,卷烟燃烧产生的各种各样的副产物会导致催化剂快速失活;催化剂即使不失活,但是催化剂上的CO催化氧化反应会导致滤嘴的温度大幅上升,消费者难以接受。Another way to reduce CO is to add an oxidant or catalyst to the filter to convert CO into CO 2 . US Patent No. 4317460 describes a tin or tin compound catalyst for the oxidation of CO to CO2 at low temperatures, these catalysts and other catalytic materials are supported on microporous supports. However, there are unavoidable defects in this catalyst being placed in the filter tip, such as under general smoking conditions, various by-products produced by cigarette combustion will lead to rapid deactivation of the catalyst; The CO catalytic oxidation reaction will cause the temperature of the filter to rise sharply, which is difficult for consumers to accept.
一种更有效的降低烟气CO的方法是在卷烟烟支段将CO催化转化为CO2。此类催化剂如美国专利No.4956330、No.5050621、No.5258330、No.5050621描述了在卷烟烟支段添加铜的氧化物和/或二氧化锰催化降低CO。美国专利No.5258340描述了一种氧化CO的过渡金属氧化物催化剂,美国专利No.4125118陈述了卷烟燃烧产生的一些有害成份及其替代品,通过在卷烟燃烧位置添加少量过渡金属混合物催化降低技术。该技术的缺点是必须对该催化剂提供大量的氧化剂以达到对CO的有效降低,而且,到目前为止,在这种材料上的非均相反应仍不充分。另外,在近卷烟燃烧点的高温区内这些材料热稳定性差,非均相反应只能在远离燃烧区的小区域内发生,催化活性不充分。美国专利No.7165553报导了具有中孔/微孔结构的沸石催化剂,将CO转化为CO2,和/或将NO转化为N2,该中孔/微孔结构催化剂对烟气有害成分具有选择性降低效果。在这两项专利里采用了纳米氧化铁,这使得催化剂在卷烟中的添加量必须增大,不利于卷烟工艺。综上所述,如果一种材料既是催化剂又是氧化剂将是催化降低CO、NO的首选材料,显然上述专利中的材料皆不具备此功能。A more effective way to reduce CO in the flue gas is to convert CO into CO 2 at the end of the cigarette. Such catalysts, such as US Patent Nos. 4,956,330, 5,050,621, 5,258,330, and 5,050,621, describe the addition of copper oxide and/or manganese dioxide to catalyze the reduction of CO in the cigarette branch section. U.S. Patent No.5258340 describes a transition metal oxide catalyst that oxidizes CO, and U.S. Patent No.4125118 states some harmful components produced by cigarette combustion and their substitutes, by adding a small amount of transition metal mixture catalytic reduction technology at the cigarette burning position . The disadvantage of this technology is that the catalyst must be supplied with a large amount of oxidant to achieve effective reduction of CO, and, so far, the heterogeneous reaction on this material is still insufficient. In addition, these materials have poor thermal stability in the high-temperature area near the burning point of cigarettes, and the heterogeneous reaction can only occur in a small area far away from the burning area, and the catalytic activity is not sufficient. U.S. Patent No. 7165553 reports a zeolite catalyst with a mesopore/microporous structure that converts CO into CO 2 and/or converts NO into N 2 . sex-reducing effect. In these two patents, nano-iron oxide is used, which makes the amount of catalyst added in the cigarette must be increased, which is not conducive to the cigarette process. To sum up, if a material is both a catalyst and an oxidant, it will be the first choice to catalyze the reduction of CO and NO. Obviously, none of the materials in the above patents has this function.
降低CO、NO更多的催化剂、吸附剂和/或氧化剂见美国专利No.6371127、No.6286516、No.6138838、No.5211684、No.4744374、No.4453553、No.4450847、No.4182348、No.4108151、No.3807416、No.3720214等。除了现有的这些技术,降低卷烟烟气CO、NO迫切需要一种更先进和更有效的方法和材料。For more catalysts, adsorbents and/or oxidants that reduce CO and NO, see US Patent Nos. 6371127, No. 6286516, No. 6138838, No. No.4108151, No.3807416, No.3720214, etc. In addition to these existing technologies, a more advanced and effective method and material are urgently needed to reduce CO and NO in cigarette smoke.
发明内容 Contents of the invention
本发明的目的旨在提供一种降低卷烟烟气CO、NO热稳氧化锰分子筛在卷烟中的应用方式。The object of the present invention is to provide an application mode of heat-stable manganese oxide molecular sieve in cigarettes for reducing CO and NO in cigarette smoke.
本发明的还一目的旨在提供一种降低卷烟烟气CO、NOx的热稳氧化锰分子筛及其制备方法,所得到的氧化锰分子筛具有良好地热稳性能,裂解温度可达到600℃。Another object of the present invention is to provide a thermally stable manganese oxide molecular sieve for reducing CO and NOx in cigarette smoke and its preparation method. The obtained manganese oxide molecular sieve has good thermal stability and the cracking temperature can reach 600°C.
本发明的目的是通过下述方式实现的:The purpose of the present invention is achieved in the following manner:
将氧化锰分子筛用作降低卷烟烟气CO、NO的催化材料。Manganese oxide molecular sieves are used as catalytic materials for reducing CO and NO in cigarette smoke.
所述的氧化锰分子筛掺杂有金属离子。The manganese oxide molecular sieve is doped with metal ions.
所述的掺杂金属离子选自Ag、Cu或Co。The doping metal ions are selected from Ag, Cu or Co.
将本发明的氧化锰分子筛制备成悬浮液,选择以喷涂方式添加在卷烟烟丝中,添加量为10-30mg/支。The manganese oxide molecular sieve of the present invention is prepared into a suspension, which is selected to be added to shredded cigarette tobacco in a spraying manner, and the added amount is 10-30 mg/cigarette.
一种氧化锰分子筛的制备方法,步骤包括:将金属硝酸盐和硫酸锰配制成PH为0.8~1.2的硝酸溶液,缓慢滴入紫红色的高锰酸钾溶液中,硫酸锰与高锰酸钾的摩尔比维持在1.0~1.5,硝酸盐金属离子与硫酸盐锰离子的质量分率为0.1~0.5%;反应生成的黑色沉淀物在90~150℃下剧烈搅拌并回流40~60h后,经过滤,去离子水洗涤,最后在100~150℃下干燥4~6h制得。A method for preparing a manganese oxide molecular sieve, the steps comprising: preparing metal nitrate and manganese sulfate into a nitric acid solution with a pH of 0.8 to 1.2, slowly dropping it into a purple-red potassium permanganate solution, manganese sulfate and potassium permanganate The molar ratio of nitrate metal ions and sulfate manganese ions is maintained at 1.0-1.5, and the mass fraction of nitrate metal ions and sulfate manganese ions is 0.1-0.5%. It is obtained by filtering, washing with deionized water, and finally drying at 100-150°C for 4-6 hours.
金属硝酸盐中的金属选自Ag、Cu或Co。The metal in the metal nitrate is selected from Ag, Cu or Co.
卷烟燃烧过程中CO的形成具有有三种途径,有机化合物的热裂解,约30%,烟草碳化物不完全燃烧,约36%,CO2与烟草碳化物反应,约23%,催化剂的活性、温度和氧气浓度是CO和CO2形成和反映的决定性因素。烟气NO的释放量比CO小很多,主要是有机混合物的热分解、N2的燃烧、各种含氮化合物的还原反应产生。催化剂的活性、温度和氧气浓度同样是NO降低的主要因素,其中催化剂的热稳定性对降低NO的释放量可能更重要,因为NO的催化氧化反应需要更高的温度。There are three ways for the formation of CO during the combustion process of cigarettes, thermal cracking of organic compounds, about 30%, incomplete combustion of tobacco carbides, about 36%, CO2 reaction with tobacco carbides, about 23%, catalyst activity, temperature and oxygen concentration are decisive factors for the formation and reflection of CO and CO2 . The emission of NO in flue gas is much smaller than that of CO, which is mainly produced by the thermal decomposition of organic mixtures, the combustion of N2 , and the reduction reactions of various nitrogen-containing compounds. Catalyst activity, temperature and oxygen concentration are also the main factors for the reduction of NO, and the thermal stability of the catalyst may be more important to reduce the release of NO, because the catalytic oxidation reaction of NO requires a higher temperature.
卷烟燃烧时主要有三个区域,即燃烧区、裂解区和冷凝区。烟丝燃烧的部分称为燃烧区,温度达到700-950℃,此区域内氧气主要是供烟丝燃烧产生CO2和水蒸气,氧气浓度极低,不完全燃烧会产生CO,碳化的烟草又使得CO2还原为CO。在此高温区域内,本发明研究的氧化剂可供氧以降低CO释放量,不需要催化剂便可达到完全燃烧。裂解区紧跟燃烧区,燃烧区燃烧产生的热量通过烟气传递到此区域内,使得此区域温度达到200-600℃,形成裂解区。这个区域内因温度不够高,主要的反应是烟草的裂解反应,是CO主要产生的区域。此区域内有少量氧气,但因温度不够高而不具备氧化性,如若有合适的催化剂将能氧化CO为CO2。影响此反应的主要因素是催化剂的热稳定性。如果催化剂在温度达到400℃就开始不稳定分解,CO氧化反应时催化剂量降低减少,另外因为CO氧化为CO2的反应速率与温度是呈指数关系,CO氧化为CO2的量大幅减少,CO得不到有效降低。本发明研制的催化剂当温度达到600℃时仍具有高的热稳定性,此区域内对CO的氧化反应具有显著的催化效果。第三个区域是冷凝区,温度在室温-200℃之间,此区域主要是烟气成分在烟丝上的冷凝/蒸发。There are three main areas when cigarettes are burned, namely the burning area, the cracking area and the condensation area. The burning part of the shredded tobacco is called the combustion zone, and the temperature reaches 700-950°C. The oxygen in this area is mainly for the shredded tobacco to burn to produce CO 2 and water vapor. The oxygen concentration is extremely low, and incomplete combustion will produce CO, and the carbonized tobacco will make CO 2 is reduced to CO. In this high-temperature region, the oxidant studied in the present invention can supply oxygen to reduce CO emission, and complete combustion can be achieved without a catalyst. The cracking zone follows the combustion zone, and the heat generated by combustion in the combustion zone is transferred to this zone through the flue gas, so that the temperature in this zone reaches 200-600°C, forming a cracking zone. Because the temperature in this area is not high enough, the main reaction is the pyrolysis reaction of tobacco, which is the area where CO is mainly produced. There is a small amount of oxygen in this area, but it is not oxidizing because the temperature is not high enough. If there is a suitable catalyst, it will be able to oxidize CO to CO 2 . The main factor affecting this reaction is the thermal stability of the catalyst. If the catalyst begins to decompose unstable when the temperature reaches 400°C, the amount of catalyst will decrease during the CO oxidation reaction. In addition, because the reaction rate of CO oxidation to CO 2 is exponentially related to the temperature, the amount of CO oxidation to CO 2 is greatly reduced, and CO cannot be effectively reduced. The catalyst developed by the invention still has high thermal stability when the temperature reaches 600° C., and has a remarkable catalytic effect on the oxidation reaction of CO in this region. The third area is the condensation area, the temperature is between room temperature and 200°C, and this area is mainly the condensation/evaporation of smoke components on the shredded tobacco.
本发明所制备得到催化剂为可在高温下达到600-700℃的热稳定性材料,沿着卷烟燃烧方向更长距离内具有催化活性,相比于前面所述催化剂更具有优势,且该材料在温度200℃左右即具有高的催化活性。催化剂粉末具备的热稳定性使得其只在卷烟燃烧区最高温度点才裂解,继而保证了在卷烟烟支段更大区域内和更宽温度范围(200-600℃)内能有效降低CO、NO。The catalyst prepared by the present invention is a thermally stable material that can reach 600-700°C at high temperature, and has catalytic activity in a longer distance along the cigarette burning direction, which is more advantageous than the above-mentioned catalyst, and the material is in It has high catalytic activity at a temperature of about 200°C. The thermal stability of the catalyst powder enables it to be cracked only at the highest temperature point in the cigarette burning zone, thereby ensuring that CO and NO can be effectively reduced in a larger area and a wider temperature range (200-600°C) in the cigarette branch section .
本发明所述催化剂粉末与现有技术中的催化剂不同之处亦是优胜之处在于催化剂粉末既是催化剂又是氧化剂。该优势的取得在于选择和采用了热稳定性材料,即使在600-700℃高温仍具有热稳定性,但是该材料又不是极端的热稳定性,当温度高于600℃时,材料分解释放出O2,充当氧化剂角色,氧化CO:The difference between the catalyst powder of the present invention and the catalyst in the prior art is that the catalyst powder is both a catalyst and an oxidant. The advantage of this advantage lies in the selection and use of thermally stable materials, which are thermally stable even at high temperatures of 600-700°C, but the material is not extremely thermally stable. When the temperature is higher than 600°C, the material decomposes and releases O 2 acts as an oxidizing agent and oxidizes CO:
2CO+O2=2CO2 2CO+O 2 =2CO 2
催化剂粉末除了充当氧化剂,同时在卷烟燃烧过程中催化下述反映,降低CO和/或NO:In addition to acting as an oxidant, the catalyst powder catalyzes the following reactions during the combustion of cigarettes to reduce CO and/or NO:
2CO+2NO=2CO2+N2 2CO+2NO=2CO 2 +N 2
与现有技术的卷烟用催化剂相比,本发明还具有以下优势:Compared with the catalyst for cigarettes of the prior art, the present invention also has the following advantages:
1)、本发明的用做降低卷烟烟气CO、NO催化剂的热稳氧化锰分子筛,由于加入金属离子的掺杂对分子筛材料的合成有一定的促进作用,材料在形貌上更加均一完整,可使得催化剂粒子直径在20nm左右,长度保持在500~600nm;1), the thermally stable manganese oxide molecular sieve used as a catalyst for reducing CO and NO in cigarette smoke of the present invention, because the doping of metal ions has a certain promotion effect on the synthesis of molecular sieve materials, the material is more uniform and complete in appearance, The diameter of catalyst particles can be kept at about 20nm, and the length can be kept at 500-600nm;
2)、本发明的热稳氧化锰分子筛,材料的孔径分布范围比较窄,分子筛主要是由孔径均一的微孔组成,且掺杂金属离子之后分子筛的比表面积增大,比表面积为7000-8000m2/g,可超过7500m2/g,孔径分布变窄。这是由于金属原子的进入使分子筛的骨架得到伸展,从而改善了氧化锰八面体分子筛的结构性能,使得其表面的吸附性能提高,孔径更为均一,进而提高了对CO、NO的反应,效果显著。2), the thermally stable manganese oxide molecular sieve of the present invention has a relatively narrow pore size distribution range of the material, and the molecular sieve is mainly composed of micropores with uniform pore size, and the specific surface area of the molecular sieve increases after doping with metal ions, and the specific surface area is 7000-8000m 2 /g, can exceed 7500m 2 /g, and the pore size distribution becomes narrow. This is because the entry of metal atoms stretches the framework of the molecular sieve, which improves the structural properties of the manganese oxide octahedral molecular sieve, improves the adsorption performance of its surface, and makes the pore size more uniform, thereby improving the reaction to CO and NO. significantly.
3)、通过对催化材料在卷烟中热力学分析,本发明的热稳氧化锰分子筛选择在卷烟烟丝中添加,避免了在滤嘴中添加造成滤嘴温升的问题,进而避免了对催化材料的选取、制备过程苛刻限制。3), by analyzing the thermodynamics of the catalytic material in the cigarette, the thermally stable manganese oxide molecular sieve of the present invention is selected to be added in the shredded tobacco of the cigarette, which avoids the problem of the temperature rise of the filter caused by the addition in the filter, and then avoids the damage to the catalytic material. The selection and preparation process are strictly limited.
4)、本发明的热稳氧化锰分子筛制备的悬浮液,可通过喷涂方式均匀的添加在卷烟烟丝上,解决了传统催化剂材料在卷烟中添加不均匀性问题。4) The suspension prepared by the heat-stable manganese oxide molecular sieve of the present invention can be evenly added to cigarette shreds by spraying, which solves the problem of non-uniform addition of traditional catalyst materials in cigarettes.
5)、本发明的热稳氧化锰分子筛可显著降低卷烟烟气中CO、NO和稠环芳烃苯并[a]芘,其中CO降低可达29.2%,NO降低可达24.57%,烟气稠环芳烃苯并[a]芘降低可达28.67%。5), the heat-stable manganese oxide molecular sieve of the present invention can significantly reduce CO, NO and fused-ring aromatic hydrocarbon benzo[a]pyrene in cigarette smoke, wherein CO can be reduced by up to 29.2%, NO can be reduced by up to 24.57%, and the smoke is dense The aromatic hydrocarbon benzo[a]pyrene can be reduced by 28.67%.
具体实施方式: Detailed ways:
以下实施例旨在说明本发明而不是对本发明的进一步限定,本发明可以按发明内容所描述的任何一种方式实施。The following examples are intended to illustrate the present invention rather than to further limit the present invention, and the present invention can be implemented in any mode described in the summary of the present invention.
实施例1:Example 1:
以Cu(质量分率为0.5%)为基准,将一定比例的硫酸锰和硝酸银配制成PH=1的硝酸溶液,缓慢滴入紫红色的高锰酸钾溶液中,硫酸锰与高锰酸钾的摩尔比维持在1.4左右。反应生成的黑色沉淀物在100℃下剧烈搅拌并回流48h后,经过滤,去离子水洗涤,最后在110℃下干燥5h制得。催化剂制好后按10mg/支卷烟以喷涂方式添加在卷烟烟丝中。对卷烟烟支进行烟气分析,结果表明烟丝中添加热稳氧化锰分子筛,与对照样相比,可显著降低卷烟烟气中CO、NO和稠环芳烃苯并[a]芘,其中CO降低可达24%,NO降低可达21.98%,烟气稠环芳烃苯并[a]芘降低可达22.14%。Based on Cu (mass fraction: 0.5%), prepare a certain proportion of manganese sulfate and silver nitrate to make a nitric acid solution with pH=1, slowly drop into the purple-red potassium permanganate solution, manganese sulfate and permanganate The molar ratio of potassium is maintained at about 1.4. The black precipitate formed by the reaction was vigorously stirred at 100°C and refluxed for 48h, filtered, washed with deionized water, and finally dried at 110°C for 5h. After the catalyst is prepared, 10 mg/cigarette is added to the shredded tobacco of the cigarette by spraying. The smoke analysis of cigarette sticks shows that the addition of heat-stabilized manganese oxide molecular sieves to shredded tobacco can significantly reduce CO, NO and fused-ring aromatic hydrocarbon benzo[a]pyrene in cigarette smoke, among which CO is reduced It can reach 24%, the reduction of NO can reach 21.98%, and the reduction of fused-ring aromatic hydrocarbon benzo[a]pyrene in flue gas can reach 22.14%.
实施例2:Example 2:
以Ag(质量分率为0.5%)为基准,将一定比例的硫酸锰和硝酸银配制成PH=1的硝酸溶液,缓慢滴入紫红色的高锰酸钾溶液中,硫酸锰与高锰酸钾的摩尔比维持在1.4左右。反应生成的黑色沉淀物在100℃下剧烈搅拌并回流48h后,经过滤,去离子水洗涤,最后在110℃下干燥5h制得。催化剂制好后按30mg/支卷烟以喷涂方式添加在卷烟烟丝中。对卷烟烟支进行烟气分析,结果表明烟丝中添加热稳氧化锰分子筛,与对照样相比,可显著降低卷烟烟气中CO、NO和稠环芳烃苯并[a]芘,其中CO降低可达29.2%,NO降低可达24.57%,烟气稠环芳烃苯并[a]芘降低可达28.67%。Based on Ag (mass fraction: 0.5%), prepare a certain proportion of manganese sulfate and silver nitrate to make a nitric acid solution with pH=1, slowly drop it into the purple-red potassium permanganate solution, manganese sulfate and permanganate The molar ratio of potassium is maintained at about 1.4. The black precipitate formed by the reaction was vigorously stirred at 100°C and refluxed for 48h, filtered, washed with deionized water, and finally dried at 110°C for 5h. After the catalyst is prepared, 30 mg/cigarette is added to the shredded tobacco of the cigarette by spraying. The smoke analysis of cigarette sticks shows that the addition of heat-stabilized manganese oxide molecular sieves to shredded tobacco can significantly reduce CO, NO and fused-ring aromatic hydrocarbon benzo[a]pyrene in cigarette smoke, among which CO is reduced It can reach 29.2%, NO reduction can reach 24.57%, and flue gas fused-ring aromatic hydrocarbon benzo[a]pyrene can reduce up to 28.67%.
实施例3:Example 3:
以Ag(质量分率为0.1%)为基准,将一定比例的硫酸锰和硝酸银配制成PH=1的硝酸溶液,缓慢滴入紫红色的高锰酸钾溶液中,硫酸锰与高锰酸钾的摩尔比维持在1.4左右。反应生成的黑色沉淀物在100℃下剧烈搅拌并回流48h后,经过滤,去离子水洗涤,最后在110℃下干燥5h制得。催化剂制好后按30mg/支卷烟以喷涂方式添加在卷烟烟丝中。对卷烟烟支进行烟气分析,结果表明烟丝中添加热稳氧化锰分子筛,与对照样相比,可显著降低卷烟烟气中CO、NO和稠环芳烃苯并[a]芘,其中CO降低可达21.7%,NO降低可达18.10%,烟气稠环芳烃苯并[a]芘降低可达24.24%。Based on Ag (mass fraction: 0.1%), prepare a certain proportion of manganese sulfate and silver nitrate into a nitric acid solution with pH=1, slowly drop it into the purple-red potassium permanganate solution, manganese sulfate and permanganate The molar ratio of potassium is maintained at about 1.4. The black precipitate formed by the reaction was vigorously stirred at 100°C and refluxed for 48h, filtered, washed with deionized water, and finally dried at 110°C for 5h. After the catalyst is prepared, 30 mg/cigarette is added to the shredded tobacco of the cigarette by spraying. The smoke analysis of cigarette sticks shows that the addition of heat-stabilized manganese oxide molecular sieves to shredded tobacco can significantly reduce CO, NO and fused-ring aromatic hydrocarbon benzo[a]pyrene in cigarette smoke, among which CO is reduced It can reach 21.7%, the reduction of NO can reach 18.10%, and the reduction of fused-ring aromatic hydrocarbon benzo[a]pyrene in flue gas can reach 24.24%.
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Cited By (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102218327A (en) * | 2011-04-22 | 2011-10-19 | 上海烟草集团有限责任公司 | Catalyst for reducing CO content in cigarette smoke, and preparation and application thereof |
| CN102730760A (en) * | 2011-04-07 | 2012-10-17 | 中国科学院城市环境研究所 | Preparation method of 1*1-type manganese oxide octahedral molecular sieves |
| CN109813797A (en) * | 2019-04-13 | 2019-05-28 | 中国烟草总公司郑州烟草研究院 | The rapid detection method of sulphur compound in a kind of cigarette mainstream flue gas |
| CN112371121A (en) * | 2020-12-01 | 2021-02-19 | 吉林大学 | Catalyst for eliminating formaldehyde and carbon monoxide at room temperature and preparation method thereof |
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| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102730760A (en) * | 2011-04-07 | 2012-10-17 | 中国科学院城市环境研究所 | Preparation method of 1*1-type manganese oxide octahedral molecular sieves |
| CN102218327A (en) * | 2011-04-22 | 2011-10-19 | 上海烟草集团有限责任公司 | Catalyst for reducing CO content in cigarette smoke, and preparation and application thereof |
| CN102218327B (en) * | 2011-04-22 | 2012-12-19 | 上海烟草集团有限责任公司 | Catalyst for reducing CO content in cigarette smoke, and preparation and application thereof |
| CN109813797A (en) * | 2019-04-13 | 2019-05-28 | 中国烟草总公司郑州烟草研究院 | The rapid detection method of sulphur compound in a kind of cigarette mainstream flue gas |
| CN109813797B (en) * | 2019-04-13 | 2021-07-06 | 中国烟草总公司郑州烟草研究院 | A rapid detection method for sulfur compounds in mainstream cigarette smoke |
| CN112371121A (en) * | 2020-12-01 | 2021-02-19 | 吉林大学 | Catalyst for eliminating formaldehyde and carbon monoxide at room temperature and preparation method thereof |
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Open date: 20091223 |