CN101422277B - Method for adjusting and controlling nicotine content in tobacco extract - Google Patents

Method for adjusting and controlling nicotine content in tobacco extract Download PDF

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Publication number
CN101422277B
CN101422277B CN2008102197856A CN200810219785A CN101422277B CN 101422277 B CN101422277 B CN 101422277B CN 2008102197856 A CN2008102197856 A CN 2008102197856A CN 200810219785 A CN200810219785 A CN 200810219785A CN 101422277 B CN101422277 B CN 101422277B
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nicotine content
extract
milipore filter
content
membrane module
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CN101422277A (en
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郑松明
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Guangzhou Jinye Science & Technology Development Co., Ltd.
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Guangdong Jinye Tobacco Sheet Technology Development Co Ltd
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Abstract

The invention relates to a method for adjusting and controlling the content of nicotine in a tobacco extract. The invention aims at solving the problems of complicated technique, relatively high cost, easily damaged original aromatic components in tobacco and chemical agent residue in the extract in adjusting and controlling the content of the nicotine in the tobacco extract during the production of reconstituted tobacco leaves in the existing paper-process. The technical keys are as follows: the method is characterized in that a tobacco raw material extract used in the production of the reconstituted tobacco leaves in the paper-process is selected, a solvent is used for diluting the extract to a set concentration, the diluent obtained is put into an ultrafiltration membrane circulating device for circulation and filtration to obtain a trapped liquid which is low in nicotine content and trapped by a ultrafiltration membrane and a dialyzate which is high in nicotine content and permeates the ultrafiltration membrane, wherein, the trapped liquid is used as a material which is coated on and refilled into a substrate during the production of the reconstituted tobacco leaves in the paper-process and the dialyzate is used as a material with special usage.

Description

A kind of regulate and control that tobacco is extracted or extract in the method for nicotine content
Technical field
The present invention relates to change the technology of nicotine content in the tobacco, particularly a kind of method of utilizing nicotine content in the milipore filter isolation technics regulation and control tobacco extract.Be applicable to the production of papermaking-method reconstituted tobaccos.
Background technology
Generally contain 1~3% nicotine in the natural tobacco leaf.Nicotine is commonly called as nicotine, an amount of take in can excited spirit, eliminate tired, increase thinking ability, increase work efficiency, also have certain anesthetic effect, this is the why places of smoking of many smokers.But nicotine is toxic, and excessive absorption can damage health, as bringing out nervous system disorders such as chronic pharyngitis, breathing problem, angiocardiopathy, some disease of digestive tract and headache, insomnia, inpairment of vision.Under the reality that can't give up smoking fully at present, the nicotine content that regulation and control reduce in the common cigarette has become the target that the tobacco curing industry is pursued.In addition, in order to adapt to different smokers' different requirements, the tobacco curing industry is generally produced the tobacco product of different nicotine contents by the papermaking-method reconstituted tobaccos technology, so also often need the nicotine content in extraction of regulation and control tobacco or the extract in papermaking-method reconstituted tobaccos is produced.
The prior art of nicotine content in the present existing change cigarette, a kind of medicament and application that reduces nicotine just like No. the 02159036.2nd, Chinese patent, be that liquid preparation with a kind of degrading nicotine is sprayed directly on the pipe tobacco or with the medicament powder and directly mixes in pipe tobacco, but this method can change the taste of conventional cigarette, also can cause the suction of non-cigarette material, not easy for consumers to accept.The Processes and apparatus of the producing tobacco flake in method similar to papermaking of Chinese patent No. No. 93120477.1 and for example, be after tobacco material (tobacco leaf, offal, fragment and offal) is extracted or extracts by solution, through solid-liquid separation process, substrate is used to manufacture paper with pulp with solid (fiber, half fiber, lignin etc.), to extract or extract partly through concentrating, the coating of modulation back is backfilling on the substrate, makes the papermaking-method reconstituted tobaccos product after operation such as toast, cut.During papermaking-method reconstituted tobaccos is produced, when needing the regulation and control nicotine content, generally can take out partial nicotinic by processes such as phase-splitting precipitation, chemisorbed, but complex process, cost are higher, the original aroma component of tobacco is damaged easily, also exist chemical agent extract or extract in residual problem.
Summary of the invention
In order to overcome in the existing papermaking-method reconstituted tobaccos production, the regulation and control tobacco extract or extract in higher, the original aroma component of tobacco of the existing complex process of nicotine content, cost be damaged easily, exist chemical agent extract or extract in residual defective, the purpose of this invention is to provide that a kind of improved regulation and control tobacco is extracted or extract in the method for nicotine content, can overcome the defective of prior art.
The present invention solves the technical scheme that its technical problem takes: a kind of regulate and control that tobacco is extracted or extract in the method for nicotine content, it is characterized in that: the tobacco material of getting in the papermaking-method reconstituted tobaccos production extracts or extract, with solvent dilution to concentration is 1~50%, dilution put in milipore filter (MWCO) EGR that a specification is molecular weight cut off 2000~5000 dalton (Dalton) carry out circulating filtration, obtain the trapped fluid of the low nicotine content held back by milipore filter and see through the dislysate of the high-nicotine content of milipore filter, trapped fluid is backfilling into usefulness on the substrate as coating in the papermaking-method reconstituted tobaccos production, and dislysate is used as specific use.
The so-called specific use of technique scheme be meant as the nicotine content of trapped fluid adjust compatibility agent, with doing have the substrate of specific (special) requirements to be coated with backfill liquid or to be used to make pure nicotine etc. to nicotine content.
The milipore filter EGR of technique scheme can be made of batch can, liquid pump and membrane module, be provided with milipore filter (MWCO) in the membrane module, the infusion port of batch can is connected with the inlet of liquid pump by pipeline, the liquid outlet of liquid pump is connected with membrane module by pipeline, the liquid outlet of holding back of membrane module is connected with the inlet of batch can by pipeline, the dialysis liquid outlet of membrane module is used to export dislysate, also is provided with charging aperture and valve control liquid outlet on the batch can, and the valve control liquid outlet of batch can is used to export trapped fluid.
The solvent of technique scheme is that water or concentration are lower than 30% alcoholic solution.
The so-called height of the trapped fluid nicotine content of technique scheme and dislysate nicotine content is that both compare.
Beneficial effect of the present invention: because by a milipore filter EGR, just tobacco material extraction or extract can be isolated low nicotine content part and high-nicotine content part, use its low nicotine content partly to be coated with and be backfilling on the substrate of papermaking-method reconstituted tobaccos production, just can reach the nicotine content of direct reduction papermaking-method reconstituted tobaccos; Simultaneously available high-nicotine content is partly adjusted compatibility low nicotine content part, and the nicotine content that reaches papermaking-method reconstituted tobaccos is controlled, is convenient to produce the tobacco product of different nicotine contents; The method technology of nicotine content is simple in extraction of this regulation and control tobacco or the extract, cost is low, can not destroy the original aroma component of tobacco, do not have chemical agent residual problem in extraction or extract, is a kind of desirable process that is suitable for applying.The dislysate of high-nicotine content part also can be used for producing needs the extra high special cigarettes product of nicotine content, be used to make pure nicotine or other needs the field of nicotine, and the range of application of tobacco material extraction or extract is enlarged.
For a more detailed description below in conjunction with drawings and Examples to the present invention.
Description of drawings
Fig. 1 is a kind of simplified schematic diagram of embodiment of the milipore filter EGR of invention.
Among the figure: 1, batch can; 2, liquid pump; 3, membrane module; 4, milipore filter; 5, the infusion port of batch can; 6, the inlet of liquid pump; 7, the liquid outlet of liquid pump; 8, the inlet of membrane module; 9, membrane module holds back liquid outlet; 10, the inlet of batch can; 11, the dialysis liquid outlet of membrane module; 12, the charging aperture of batch can; 13, the valve control liquid outlet of batch can.
The specific embodiment
Embodiment one:
The method of nicotine content in extraction of these regulation and control tobacco or the extract is characterized in that: the tobacco material of getting in the papermaking-method reconstituted tobaccos production extracts or extract 20.00kg, and wherein nicotine content is 1.60%, and solid content is 65.2%; Be dissolved in it in the water of 70.00kg and stir, be diluted to concentration and be about 14.5%; Dilution to be put in milipore filter (MWCO) EGR that a specification is molecular weight cut off 5000 dalton (Dalton) carry out circulating filtration, operating temperature is controlled at≤and 40 ℃, operating pressure is controlled at≤23Mpa; Obtain the trapped fluid 43.29kg (concentration is 15.3%) of the low nicotine content held back by milipore filter and see through the dislysate 45.8kg (concentration is 13.6%) of the high-nicotine content of milipore filter, trapped fluid obtains medicinal extract 9.64Kg after concentrating, wherein solid content is 68.8%, nicotine content 0.84% is backfilling into on-chip material as coating in the papermaking-method reconstituted tobaccos production; Get medicinal extract 8.87kg after dislysate concentrates, wherein solid content is 70.2%, and nicotine content is 2.72%%, as the material of specific use.
As shown in Figure 1, described milipore filter EGR is by batch can 1, liquid pump 2 and membrane module 3 constitute, membrane module is provided with milipore filter (MWCO) 4 for 3 li, its specification is molecular weight cut off 5000 dalton (Dalton), the infusion port 5 of batch can is connected with the inlet 6 of liquid pump by pipeline, the liquid outlet 7 of liquid pump is connected with the inlet 8 of membrane module by pipeline, the liquid outlet 9 of holding back of membrane module is connected with the inlet 10 of batch can by pipeline, the dialysis liquid outlet 11 of membrane module is used to export dislysate, also be provided with charging aperture 12 and valve control liquid outlet 13 on the batch can 1, the valve control liquid outlet 13 of batch can is used to export trapped fluid.
Embodiment two:
The method of nicotine content in extraction of these regulation and control tobacco or the extract is characterized in that: the tobacco material of getting in the papermaking-method reconstituted tobaccos production extracts or extract 10.00kg, and wherein nicotine content is 8.73%, and solid content is 69.6%; Be dissolved in it in the water of 90.00kg and stir, be diluted to concentration and be about 7.0%; Dilution to be put in milipore filter (MWCO) EGR that a specification is molecular weight cut off 5000 dalton (Dalton) carry out circulating filtration, operating temperature is controlled at≤and 40 ℃, operating pressure is controlled at≤25Mpa; Obtain the trapped fluid 32.96kg (concentration is 15.7%) of the low nicotine content held back by milipore filter and see through the dislysate 66.54kg (concentration is 2.7%) of the high-nicotine content of milipore filter, trapped fluid obtains medicinal extract 7.52Kg after concentrating, wherein solid content is 69.0%, nicotine content 3.76% is backfilling into on-chip material as coating in the papermaking-method reconstituted tobaccos production; Dislysate so employing nanofiltration earlier concentrates, adopts conventional concentrating because concentration is too low then, gets medicinal extract 2.42Kg, and wherein solid content is 67.6%, and nicotine content is 23.52%, as the material of specific use.
As shown in Figure 1, described milipore filter EGR is by batch can 1, liquid pump 2 and membrane module 3 constitute, membrane module is provided with milipore filter (MWCO) 4 for 3 li, its specification is molecular weight cut off 5000 dalton (Dalton), the infusion port 5 of batch can is connected with the inlet 6 of liquid pump by pipeline, the liquid outlet 7 of liquid pump is connected with the inlet 8 of membrane module by pipeline, the liquid outlet 9 of holding back of membrane module is connected with the inlet 10 of batch can by pipeline, the dialysis liquid outlet 11 of membrane module is used to export dislysate, also be provided with charging aperture 12 and valve control liquid outlet 13 on the batch can 1, the valve control liquid outlet 13 of batch can is used to export trapped fluid.
Embodiment three:
The method of nicotine content in extraction of these regulation and control tobacco or the extract is characterized in that: the tobacco material of getting in the papermaking-method reconstituted tobaccos production extracts or extract 10.00kg, and wherein nicotine content is 4.33%, and solid content is 67.2%; Be dissolved in it in the water of 40.00kg and stir, be diluted to concentration and be about 12.4%; Dilution to be put in milipore filter (MWCO) EGR that a specification is molecular weight cut off 3000 dalton (Dalton) carry out circulating filtration, operating temperature is controlled at≤and 40 ℃, operating pressure is controlled at≤25Mpa; Obtain the trapped fluid 17.37kg (concentration is 24.8%) of the low nicotine content held back by milipore filter and see through the dislysate 31.47kg (concentration is 5.7%) of the high-nicotine content of milipore filter, trapped fluid obtains medicinal extract 5.49Kg after concentrating, wherein solid content is 79.1%, nicotine content 3.21% is backfilling into on-chip material as coating in the papermaking-method reconstituted tobaccos production; Get medicinal extract 2.57kg after dislysate concentrates, wherein solid content is 71.3%, and nicotine content is 8.54%, as the material of specific use.
As shown in Figure 1, described milipore filter EGR is by batch can 1, liquid pump 2 and membrane module 3 constitute, membrane module is provided with milipore filter (MWCO) 4 for 3 li, its specification is molecular weight cut off 3000 dalton (Dalton), the infusion port 5 of batch can is connected with the inlet 6 of liquid pump by pipeline, the liquid outlet 7 of liquid pump is connected with the inlet 8 of membrane module by pipeline, the liquid outlet 9 of holding back of membrane module is connected with the inlet 10 of batch can by pipeline, the dialysis liquid outlet 11 of membrane module is used to export dislysate, also be provided with charging aperture 12 and valve control liquid outlet 13 on the batch can 1, the valve control liquid outlet 13 of batch can is used to export trapped fluid.

Claims (6)

  1. One kind regulate and control that tobacco is extracted or extract in the method for nicotine content, it is characterized in that: the tobacco material of getting in the papermaking-method reconstituted tobaccos production extracts or extract, with solvent dilution to concentration is 1~50%, putting dilution into a specification is to carry out circulating filtration in molecular weight cut off 2000~5000 daltonian milipore filter EGRs, obtain the trapped fluid of the low nicotine content held back by milipore filter and see through the dislysate of the high-nicotine content of milipore filter, trapped fluid is backfilling into on-chip material as coating in the papermaking-method reconstituted tobaccos production, and dislysate is as the material of specific use.
  2. 2. press the method for nicotine content in the described regulation and control of claim 1 tobacco extraction or the extract, it is characterized in that described milipore filter EGR is made of batch can, liquid pump and membrane module, be provided with milipore filter in the membrane module, the infusion port of batch can is connected with the inlet of liquid pump by pipeline, the liquid outlet of liquid pump is connected with membrane module by pipeline, the liquid outlet of holding back of membrane module is connected with the inlet of batch can by pipeline, the dialysis liquid outlet of membrane module is used to export dislysate, also be provided with charging aperture and valve control liquid outlet on the batch can, the valve control liquid outlet of batch can is used to export trapped fluid.
  3. 3. by the method for nicotine content in claim 1 or 2 described regulation and control tobaccos extractions or the extract, it is characterized in that described solvent is that water or concentration are lower than 30% alcoholic solution.
  4. 4. press the method for nicotine content in claim 2 or 3 described regulation and control tobaccos extractions or the extract, it is characterized in that the tobacco material during getting papermaking-method reconstituted tobaccos produces extracts or extract 20.00kg, wherein nicotine content is 1.60%, solid content is 65.2%, be dissolved in it in the water of 70.00kg and stir, be diluted to concentration and be about 14.5%, putting dilution into a specification is to carry out circulating filtration in the molecular weight cut off 5000 daltonian milipore filter EGRs, operating temperature is controlled at≤and 40 ℃, operating pressure is controlled at≤23Mpa, obtain the trapped fluid 43.29kg of the low nicotine content held back by milipore filter and see through the dislysate 45.8kg of the high-nicotine content of milipore filter, trapped fluid obtains medicinal extract 9.64Kg after concentrating, wherein solid content is 68.8%, nicotine content 0.84%, be backfilling into on-chip material as coating in the papermaking-method reconstituted tobaccos production, after concentrating, dislysate gets medicinal extract 8.87kg, wherein solid content is 70.2%, nicotine content is 2.72%, material as specific use, described milipore filter EGR is by batch can, liquid pump and membrane module constitute, and are provided with milipore filter in the membrane module, specification is molecular weight cut off 5000 dalton.
  5. 5. press the method for nicotine content in claim 2 or 3 described regulation and control tobaccos extractions or the extract, it is characterized in that the tobacco material during getting papermaking-method reconstituted tobaccos produces extracts or extract 10.00kg, wherein nicotine content is 8.73%, solid content is 69.6%, be dissolved in it in the water of 90.00kg and stir, be diluted to concentration and be about 7.0%, putting dilution into a specification is to carry out circulating filtration in the molecular weight cut off 5000 daltonian milipore filter EGRs, operating temperature is controlled at≤and 40 ℃, operating pressure is controlled at≤25Mpa, obtain the trapped fluid 32.96kg of the low nicotine content held back by milipore filter and see through the dislysate 66.54kg of the high-nicotine content of milipore filter, trapped fluid obtains medicinal extract 7.52Kg after concentrating, wherein solid content is 69.0%, nicotine content 3.76%, be backfilling into on-chip material as coating in the papermaking-method reconstituted tobaccos production, adopt nanofiltration to concentrate earlier, adopt conventional concentrating then, get medicinal extract 2.42Kg, wherein solid content is 67.6%, nicotine content is 23.52%, material as specific use, described milipore filter EGR is by batch can, liquid pump and membrane module constitute, and are provided with milipore filter in the membrane module, specification is molecular weight cut off 5000 dalton.
  6. 6. press the method for nicotine content in claim 2 or 3 described regulation and control tobaccos extractions or the extract, it is characterized in that the tobacco material during getting papermaking-method reconstituted tobaccos produces extracts or extract 10.00kg, wherein nicotine content is 4.33%, solid content is 67.2%, be dissolved in it in the water of 40.00kg and stir, be diluted to concentration and be about 12.4%, putting dilution into a specification is to carry out circulating filtration in the molecular weight cut off 3000 daltonian milipore filter EGRs, operating temperature is controlled at≤and 40 ℃, operating pressure is controlled at≤25Mpa, obtain the trapped fluid 17.37kg of the low nicotine content held back by milipore filter and see through the dislysate 31.47kg of the high-nicotine content of milipore filter, trapped fluid obtains medicinal extract 5.49Kg after concentrating, wherein solid content is 79.1%, nicotine content 3.21%, be backfilling into on-chip material as coating in the papermaking-method reconstituted tobaccos production, after concentrating, dislysate gets medicinal extract 2.57kg, wherein solid content is 71.3%, nicotine content is 8.54%, material as specific use, described milipore filter EGR is by batch can, liquid pump and membrane module constitute, and are provided with milipore filter in the membrane module, specification is molecular weight cut off 3000 dalton.
CN2008102197856A 2008-12-02 2008-12-02 Method for adjusting and controlling nicotine content in tobacco extract Active CN101422277B (en)

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Families Citing this family (9)

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Publication number Priority date Publication date Assignee Title
GB201213870D0 (en) 2012-08-03 2012-09-19 British American Tobacco Co Tobacco extract, preparation thereof
CN102907760A (en) * 2012-09-03 2013-02-06 上海聚华科技股份有限公司 Method for regulating chemical components of tobacco material
CN104305518A (en) * 2014-09-22 2015-01-28 江苏凯米膜科技股份有限公司 Membrane extraction process for tobacco leaching liquor
CN104489893B (en) * 2014-12-29 2017-07-07 安徽中烟再造烟叶科技有限责任公司 Papermaking-method reconstituted tobaccos are coated with liquid purification system and its purification technique
CN108271341B (en) 2015-06-26 2022-11-11 奥驰亚客户服务公司 Compositions and methods for producing tobacco plants and articles with altered alkaloid content
CN107741378A (en) * 2017-10-18 2018-02-27 湖北中烟工业有限责任公司 A kind of detection method of reconstituted tobacco coating fluid degree of purity
CN108968132B (en) * 2018-10-09 2021-08-03 湖北中烟工业有限责任公司 Preparation method of reconstituted tobacco coating liquid
CN109363228A (en) * 2018-12-17 2019-02-22 湖北中烟工业有限责任公司 A kind of reconstituted tobacco chemical component regulation method based on membrane separation technique
CN112244345A (en) * 2020-11-04 2021-01-22 上海烟草集团有限责任公司 Reconstituted tobacco extracting solution and preparation method and application thereof

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CN1157285A (en) * 1996-02-12 1997-08-20 贵州省毕节地区制药厂 Process for producing nicotine
CN101045726A (en) * 2007-04-20 2007-10-03 沈阳师范大学 Extraction of nicotine from waste tabacco leaf and offal by lactescence membrane method
CN101103839A (en) * 2006-07-13 2008-01-16 河南省轻工业科学研究所 Paper-making method producing recombination tobacco leaf method

Patent Citations (3)

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Publication number Priority date Publication date Assignee Title
CN1157285A (en) * 1996-02-12 1997-08-20 贵州省毕节地区制药厂 Process for producing nicotine
CN101103839A (en) * 2006-07-13 2008-01-16 河南省轻工业科学研究所 Paper-making method producing recombination tobacco leaf method
CN101045726A (en) * 2007-04-20 2007-10-03 沈阳师范大学 Extraction of nicotine from waste tabacco leaf and offal by lactescence membrane method

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Owner name: GUANGDONG JINYE TECHNOLOGY DEVELOPMENT CO., LTD.

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