US3717155A - Reconstituted tobacco product - Google Patents
Reconstituted tobacco product Download PDFInfo
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- US3717155A US3717155A US00048749A US3717155DA US3717155A US 3717155 A US3717155 A US 3717155A US 00048749 A US00048749 A US 00048749A US 3717155D A US3717155D A US 3717155DA US 3717155 A US3717155 A US 3717155A
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- United States
- Prior art keywords
- tobacco
- water
- reconstituted
- polyphenols
- washed
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Lifetime
Links
- 235000019505 tobacco product Nutrition 0.000 title abstract description 8
- 241000208125 Nicotiana Species 0.000 abstract description 77
- 235000002637 Nicotiana tabacum Nutrition 0.000 abstract description 77
- 150000008442 polyphenolic compounds Chemical class 0.000 abstract description 18
- 235000013824 polyphenols Nutrition 0.000 abstract description 18
- 239000000126 substance Substances 0.000 abstract description 7
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 33
- BDAGIHXWWSANSR-UHFFFAOYSA-N methanoic acid Natural products OC=O BDAGIHXWWSANSR-UHFFFAOYSA-N 0.000 description 20
- 239000000463 material Substances 0.000 description 16
- 238000000034 method Methods 0.000 description 16
- 238000010438 heat treatment Methods 0.000 description 14
- 238000005406 washing Methods 0.000 description 12
- OSWFIVFLDKOXQC-UHFFFAOYSA-N 4-(3-methoxyphenyl)aniline Chemical compound COC1=CC=CC(C=2C=CC(N)=CC=2)=C1 OSWFIVFLDKOXQC-UHFFFAOYSA-N 0.000 description 10
- 239000000284 extract Substances 0.000 description 10
- 235000019253 formic acid Nutrition 0.000 description 10
- PNEYBMLMFCGWSK-UHFFFAOYSA-N aluminium oxide Inorganic materials [O-2].[O-2].[O-2].[Al+3].[Al+3] PNEYBMLMFCGWSK-UHFFFAOYSA-N 0.000 description 9
- 239000003795 chemical substances by application Substances 0.000 description 9
- 239000003463 adsorbent Substances 0.000 description 8
- 239000012141 concentrate Substances 0.000 description 7
- 239000013642 negative control Substances 0.000 description 7
- 239000013641 positive control Substances 0.000 description 7
- 239000000654 additive Substances 0.000 description 6
- 239000002002 slurry Substances 0.000 description 6
- 150000001720 carbohydrates Chemical class 0.000 description 5
- 235000014633 carbohydrates Nutrition 0.000 description 5
- 239000012137 tryptone Substances 0.000 description 5
- 229930091371 Fructose Natural products 0.000 description 4
- 239000005715 Fructose Substances 0.000 description 4
- RFSUNEUAIZKAJO-ARQDHWQXSA-N Fructose Chemical compound OC[C@H]1O[C@](O)(CO)[C@@H](O)[C@@H]1O RFSUNEUAIZKAJO-ARQDHWQXSA-N 0.000 description 4
- WQZGKKKJIJFFOK-GASJEMHNSA-N Glucose Natural products OC[C@H]1OC(O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-GASJEMHNSA-N 0.000 description 4
- CZMRCDWAGMRECN-UGDNZRGBSA-N Sucrose Chemical compound O[C@H]1[C@H](O)[C@@H](CO)O[C@@]1(CO)O[C@@H]1[C@H](O)[C@@H](O)[C@H](O)[C@@H](CO)O1 CZMRCDWAGMRECN-UGDNZRGBSA-N 0.000 description 4
- 229930006000 Sucrose Natural products 0.000 description 4
- 238000010411 cooking Methods 0.000 description 4
- 239000000428 dust Substances 0.000 description 4
- 239000000975 dye Substances 0.000 description 4
- 239000008103 glucose Substances 0.000 description 4
- 238000004519 manufacturing process Methods 0.000 description 4
- 238000002360 preparation method Methods 0.000 description 4
- 239000000047 product Substances 0.000 description 4
- 239000007787 solid Substances 0.000 description 4
- 239000005720 sucrose Substances 0.000 description 4
- LFQSCWFLJHTTHZ-UHFFFAOYSA-N Ethanol Chemical compound CCO LFQSCWFLJHTTHZ-UHFFFAOYSA-N 0.000 description 3
- 150000001413 amino acids Chemical class 0.000 description 3
- 238000004040 coloring Methods 0.000 description 3
- 239000000470 constituent Substances 0.000 description 3
- 238000005520 cutting process Methods 0.000 description 3
- 239000007788 liquid Substances 0.000 description 3
- 239000002245 particle Substances 0.000 description 3
- 238000007670 refining Methods 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- GWEVSGVZZGPLCZ-UHFFFAOYSA-N Titan oxide Chemical compound O=[Ti]=O GWEVSGVZZGPLCZ-UHFFFAOYSA-N 0.000 description 2
- 230000000996 additive effect Effects 0.000 description 2
- 239000006286 aqueous extract Substances 0.000 description 2
- WQZGKKKJIJFFOK-VFUOTHLCSA-N beta-D-glucose Chemical compound OC[C@H]1O[C@@H](O)[C@H](O)[C@@H](O)[C@@H]1O WQZGKKKJIJFFOK-VFUOTHLCSA-N 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 238000001704 evaporation Methods 0.000 description 2
- 230000008020 evaporation Effects 0.000 description 2
- 239000012065 filter cake Substances 0.000 description 2
- 239000013505 freshwater Substances 0.000 description 2
- 239000011521 glass Substances 0.000 description 2
- 230000000704 physical effect Effects 0.000 description 2
- 238000011084 recovery Methods 0.000 description 2
- 230000000717 retained effect Effects 0.000 description 2
- 239000002904 solvent Substances 0.000 description 2
- 238000001179 sorption measurement Methods 0.000 description 2
- 239000002699 waste material Substances 0.000 description 2
- QTBSBXVTEAMEQO-UHFFFAOYSA-M Acetate Chemical compound CC([O-])=O QTBSBXVTEAMEQO-UHFFFAOYSA-M 0.000 description 1
- -1 Acetate lead acetate Chemical compound 0.000 description 1
- 239000006057 Non-nutritive feed additive Substances 0.000 description 1
- 239000004952 Polyamide Substances 0.000 description 1
- 239000002253 acid Substances 0.000 description 1
- 230000002378 acidificating effect Effects 0.000 description 1
- 230000002411 adverse Effects 0.000 description 1
- 239000005018 casein Substances 0.000 description 1
- BECPQYXYKAMYBN-UHFFFAOYSA-N casein, tech. Chemical compound NCCCCC(C(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(CC(C)C)N=C(O)C(CCC(O)=O)N=C(O)C(CC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(C(C)O)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=N)N=C(O)C(CCC(O)=O)N=C(O)C(CCC(O)=O)N=C(O)C(COP(O)(O)=O)N=C(O)C(CCC(O)=N)N=C(O)C(N)CC1=CC=CC=C1 BECPQYXYKAMYBN-UHFFFAOYSA-N 0.000 description 1
- 235000021240 caseins Nutrition 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000004587 chromatography analysis Methods 0.000 description 1
- 150000001875 compounds Chemical class 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 230000001419 dependent effect Effects 0.000 description 1
- 239000012153 distilled water Substances 0.000 description 1
- 238000001035 drying Methods 0.000 description 1
- 238000002474 experimental method Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 239000000706 filtrate Substances 0.000 description 1
- 239000012634 fragment Substances 0.000 description 1
- 239000004615 ingredient Substances 0.000 description 1
- 238000002386 leaching Methods 0.000 description 1
- 229940046892 lead acetate Drugs 0.000 description 1
- 230000000873 masking effect Effects 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 229920001206 natural gum Polymers 0.000 description 1
- 238000006386 neutralization reaction Methods 0.000 description 1
- 229920002647 polyamide Polymers 0.000 description 1
- 238000004321 preservation Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 239000000741 silica gel Substances 0.000 description 1
- 229910002027 silica gel Inorganic materials 0.000 description 1
- RMAQACBXLXPBSY-UHFFFAOYSA-N silicic acid Chemical compound O[Si](O)(O)O RMAQACBXLXPBSY-UHFFFAOYSA-N 0.000 description 1
- 235000012239 silicon dioxide Nutrition 0.000 description 1
- 230000000391 smoking effect Effects 0.000 description 1
- 235000000346 sugar Nutrition 0.000 description 1
- 150000008163 sugars Chemical class 0.000 description 1
- 238000004809 thin layer chromatography Methods 0.000 description 1
- 239000004408 titanium dioxide Substances 0.000 description 1
- 210000003462 vein Anatomy 0.000 description 1
- 238000003809 water extraction Methods 0.000 description 1
- 238000005303 weighing Methods 0.000 description 1
Classifications
-
- A—HUMAN NECESSITIES
- A24—TOBACCO; CIGARS; CIGARETTES; SIMULATED SMOKING DEVICES; SMOKERS' REQUISITES
- A24B—MANUFACTURE OR PREPARATION OF TOBACCO FOR SMOKING OR CHEWING; TOBACCO; SNUFF
- A24B15/00—Chemical features or treatment of tobacco; Tobacco substitutes, e.g. in liquid form
- A24B15/18—Treatment of tobacco products or tobacco substitutes
- A24B15/24—Treatment of tobacco products or tobacco substitutes by extraction; Tobacco extracts
Definitions
- the present invention relates to an improved reconstituted tobacco essentially devoid of polyphenols and is light in color despite the use of heat in the processing operations.
- the commercial method for the manufacture of reconstituted tobacco sheet requires the application of heat at some stage in the processing e.g. either in the preparative stages and/or in the drying. It is known that the color of the finished tobacco product darkens because of the heating; the level of darkening being a function of temperature and heating time. As a rule, it is desirable to produce a light colored tobacco sheet and various steps are taken to achieve this goal, for example, the addition of dyes or coloring chemicals, the addition of colormasking agents (whiteners) such as titanium dioxide or Dicalite, or control of temperature and heating time. These steps are never completely satisfactory because of the limitations under which they can be applied.
- the reconstituted tobacco sheet of the invention is light colored and prepared without resort to dyes for color preservation and without any undue limitations on the temperature and heating time used in the process. This is achieved by selectively removing from the tobacco the agents responsible for the darkening of the tobacco on heating.
- tobacco such as stems, field scrap, cuttings, whole leaf and the like
- tobacco sheet suitable for later machine processing.
- the tobacco is usually ground to colloid-forming size particles by a wet process or refining.
- the large amount of energy and time required for the preparation of these colloid-forming size tobacco particles has limited its use for the preparation of reconstituted sheets.
- the disclosed process provides a solution to this longstanding problem, and results in a great reduction in energy and time requires to obtain good quality reconstituted tobacco sheets of acceptable color.
- the object of the invention is the provision of a light colored reconstituted tobacco sheet despite the use of heat as a processing aid.
- a further object of the invention is the provision of such a desired colored sheet which does not have added dyes or color additives.
- a further object of the invention is the provision of a reconstituted tobacco sheet which has the polyphenols removed by extraction while the other desirable ingredients are retained.
- Tobacco as defined for this invention includes any type of tobacco suitable for the manufacture of reconstituted tobacco sheet, such as stem, veins, scrap and waste tobacco, cuttings and the like, as well as whole leaf or portions thereof.
- the method of making the reconstituted product involves removing from the tobacco washings the agents responsible for the darkening of the tobacco when it is exposed to heat.
- the treated washings are then returned to the tobacco being processes, and the product prepared in a conventional manner to provide a reconstituted tobacco sheet of good physical properties without detriment to the sheet color.
- a series of tests were run to isolate and determine the agents which caused tobacco darkening upon heating. The following procedure illustrates how the polyphenols were identified as the agents which cause tobacco darkening during heating.
- a sample of Bright stem dust weighing 10 gm was mixed with ml. of distilled water. The slurry was filtered on a Buchner funnel using Whatman No. 1 filter paper. The filter cake and filtrate were retained. The filter cake was subsequently mixed with 90 ml. of a predetermined liquid and the slurry transferred to a vessel, such as a mason jar, which was sealed and placed in a pressure cooker, where it was heated at 250F. at 15 psi for 2 hours.
- test results in Table 1 were obtained with various additives in the predetermined liquid and serve to illustrate that polyphenols are the agents causing the darkening of the tobacco on exposure to heat.
- Waterwashed Bright stem dust was used in all cases, unless otherwise indicated.
- the weight of the washed tobacco in each sample was' 7.0 gm. dry weight and this was suspended in 90 m1. of liquid prior to heating.
- the tobacco water washings can be treated with adsorbent material, which adds nothing to the extract, but selectively removes the darkening agent or agents by adsorption.
- tobacco water washings are passed through a column containing a selected adsorbent material, such as activated alumina. The adsorbent removes the darkening material, but leaves the other valuable tobacco constituents unchanged in the extract.
- the treated extract is then recombined with the original washed tobacco and the combination is processed into reconstituted tobacco sheet, which retains its commercially acceptable light color with no additives.
- untreated tobacco such as broken leaves, cuttings, stemmings, various fragments or waste, field scrap
- a water extraction operation so as to separate the watersoluble constituents.
- the water-soluble constituents of the tobacco or extract are separated from the insoluble portion by any convenient process, such as draining, pressing, or centrifuging.
- the aqueous extract contains various watersoluble materials, including polyphenols. This aqueous extract can then be passed through a column containing an adsorbent material, such as activated alumina.
- Continuous operation in a column can be effected by reconstituted tobacco sheet is produced.
- the extracted coloring materials can be eluted from the adsorbent so that it can be reused as desired.
- a glass column cm. X 3 cm.) was filled with a slurry of 100 gm. of activated alumnia (8-14 mesh) in water. The water was allowed to drain and the column was washed repeatedly with about 500-1000 ml. fresh water. A water extract of tobacco dust obtained by the method described above was passed over the column at a flow rate such that effluent was collected at 0.5 ml. per minute. The column was then washed with water until the washings were colorless. The combined water washings and collected effluent were then concentrated to 100 ml. under vacuum in a flash evaporator using a temperature range of 363 8C. The solids content in the concentrate, as well as in the original water tobacco extract were determined and the recovery of material from the column calculated from these values. The test results are presented in Table 2.
- FIGS. in Table 2 show that the solids recovery is 73-75 percent for Bright stem extracts and 89-91 percent for Penn. stem extracts.
- the material not removed from the column by water washing was eluted off by passing 2 normal formic acid through the column. Fractions were collected at a rate of 0.5 ml per minute. The eluted samples were very dark in color. The 2 normal formic acid removed all the adsorbed material leaving the activated alumnia free of color. The alumina was washed with water until free of acid, dried in the oven (ll40C.) overnight and used again.
- the formic acid was removed from the eluate (i.e., the basic-polyphenols) by evaporation under vacuum in a flash evaporator.
- the remaining dark brown material was made up to a 100 ml. volume with water and tested for carbohydrates by a thin layer chromatography method, such as described in the Journal of Chromatography 18, 170-174 (1965).
- Samples of the effluent concentrate from the column previously referred to as well as the original tobacco-water extract were also examined for carbohydrates. The results showed that practically all of the carbohydrates found in the original tobacco-water extract'were recovered in the concentrated effluent while only significant amounts were found in the formic acid eluate.
- the material which could not be removed from the column by water could be eluted off by other suitable solvents, such as percent ethanol containing 2 normal HCl or by 2 normal HCl solution.
- suitable solvents such as percent ethanol containing 2 normal HCl or by 2 normal HCl solution.
- formic acid is preferred, since it is easily removed by evaporation under vacuum. This makes it possible to recover the solids from the formic acid eluate and their subsequent utilization in the color experiments. In an operation where these solids are of no consequence, their removal from the alumina would be carried out more economically with a 2 normal HCl solution.
- Positive control consists of washed tobacco (7 gm. dry weight) plus new water.
- Negative control consists of washed tobacco plus the obtained washings.
- FIGS. in Table 3 show that the effluent concentrate from the adsorbent column is similar in its. color properties to the positive control, while the formic acid eluate, after removing the formic acid and adjusting to volume with water, is similar to the negative control. This is particularly apparent in the Rd values.
- Adsorbents other than activated alumina, were examined. Regenerated alumina worked as well as unused alumina. Polyamide and silica gel also gave satisfactory results.
- adsorbent materials such as magnesol, silicic acid or adsorption alumina, and the like. However, these materials are fine meshed and pack easily in the columns, so as to reduce flow through the columns. A pressure source would be necessary to obtain satisfactory flow through columns using these be employed effectively spirit and scope thereof, and therefore, the invention is not to be limited, except as defined in the appended claims.
- a reconstituted smoking tobacco composition comprising extracted tobacco having incorporated therein substantially all the extracted substances less only polyphenols.
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- Chemical & Material Sciences (AREA)
- Chemical Kinetics & Catalysis (AREA)
- General Chemical & Material Sciences (AREA)
- Manufacture Of Tobacco Products (AREA)
Abstract
A reconstituted tobacco product is disclosed which is essentially free of the polyphenols. which are held responsible for undue darkness in the finished tobacco following treatment operations. The reconstituted tobacco consists essentially of an extracted tobacco which is reimpregnated with substantially all the substances extracted from the tobacco with the exception of the polyphenol fraction.
Description
nited States Patent 1 .1 acin et a1.
[54] RECONSTITUTED TOBACCO PRODUCT [75] Inventors: Harry Jacin, Norwalk; Joseph Vincent Fiore, Fairfield, both of Conn.
[73] Assignee: AMF Corporation [22] Filed: May 18, 1970 [21] Appl. No.: 48,749
[52] U.S.Cl ..131/17 AC [51] Int. Cl. ..A24b 3/14, A241) 15/08 [58] Field of Search ..131/17, 15,140-144 [56] References Cited UNITED STATES PATENTS l1/l967 Colgate ..131/140A 7/1968 Von Bethmann et a1 ..131/143 10/1905 Wimmer ..131/143 1 Feb. 20, 1973 2,582,075 l/l952 Severi ..131/143 2,934,073 4/1960 Killian..... ...131/143 X 3,110,315 11/1963 Kendvai ..l3l/l43 X 3,145,717 8/1964 Osborne et al. ..131/143 X 3,338,248 8/1967 Pavia ..l3l/l43 3,361,139 l/1968 Inoue ..131/143 Primary ExaminerMelvin D. Rein Att0meyGeorge W. Price and Murray Schaffer [57] ABSTRACT 1 Claim, No Drawings RECONSTI'IUTED TOBACCO PRODUCT This application is a divisional application of Ser. No. 639,032, filed May 17, 1967, now US. Pat. No. 3,561,451.
The present invention relates to an improved reconstituted tobacco essentially devoid of polyphenols and is light in color despite the use of heat in the processing operations.
The commercial method for the manufacture of reconstituted tobacco sheet requires the application of heat at some stage in the processing e.g. either in the preparative stages and/or in the drying. It is known that the color of the finished tobacco product darkens because of the heating; the level of darkening being a function of temperature and heating time. As a rule, it is desirable to produce a light colored tobacco sheet and various steps are taken to achieve this goal, for example, the addition of dyes or coloring chemicals, the addition of colormasking agents (whiteners) such as titanium dioxide or Dicalite, or control of temperature and heating time. These steps are never completely satisfactory because of the limitations under which they can be applied. In the case of the addition of dying, coloring and masking chemicals, the introduction of extraneous material can be undesirable, especially if excessive amounts are needed to produce the desired results. Excessive use of dyes can produce leaching problems while excessive use of whiteners can result in sheets which are greyish in appearance or lack proper physical structure. In the case of controlled temperature and heating time, undesirable limits are put upon the manufacturing procedures. The reconstituted tobacco sheet of the invention is light colored and prepared without resort to dyes for color preservation and without any undue limitations on the temperature and heating time used in the process. This is achieved by selectively removing from the tobacco the agents responsible for the darkening of the tobacco on heating.
In the preparation of additive reconstituted tobacco, tobacco, such as stems, field scrap, cuttings, whole leaf and the like, is preferably uniformly comminuted and formed into tobacco sheet suitable for later machine processing. On the other hand, in the preparation of alltobacco reconstituted sheet or in reconstituted sheets wherein a more efficient utilization of the natural gums of the tobacco is desired, the tobacco is usually ground to colloid-forming size particles by a wet process or refining. However, the large amount of energy and time required for the preparation of these colloid-forming size tobacco particles has limited its use for the preparation of reconstituted sheets.
To reduce the energy expended and time involved to comminute the tobacco particles in the wet process, it is desirable to cook the tobacco prior to refining. This cooking operation reduces the refining time and simultaneously improves the physical properties of the finished product. However, the cooking causes darkening of the tobacco and hence darkens the sheets made from this cooked tobacco material, thereby making such sheets unacceptable in a number of manufactured tobacco products.
Many attempts have been made heretofore to produce reconstituted tobacco sheets using heat at some stage in the processing without the adverse darkening of the tobacco, using various techniques and methods, but, in general, such attempts have met with only limited commercial success. For example, it has been known in the art, that washing the tobacco products with water prior to treatment, replacing the washings with fresh water and then cooking the washed tobacco gives a relatively acceptable product with respect to color. However, it is unsatisfactory from an economic standpoint, since the discarded washings contain a large quantity of useful tobacco product.
The disclosed process provides a solution to this longstanding problem, and results in a great reduction in energy and time requires to obtain good quality reconstituted tobacco sheets of acceptable color.
The object of the invention is the provision of a light colored reconstituted tobacco sheet despite the use of heat as a processing aid.
A further object of the invention is the provision of such a desired colored sheet which does not have added dyes or color additives.
A further object of the invention is the provision of a reconstituted tobacco sheet which has the polyphenols removed by extraction while the other desirable ingredients are retained.
Other objects and advantages of the present invention will be apparent from the further reading of the specification and of the appended claims.
Tobacco as defined for this invention includes any type of tobacco suitable for the manufacture of reconstituted tobacco sheet, such as stem, veins, scrap and waste tobacco, cuttings and the like, as well as whole leaf or portions thereof.
In general, the method of making the reconstituted product involves removing from the tobacco washings the agents responsible for the darkening of the tobacco when it is exposed to heat. The treated washings are then returned to the tobacco being processes, and the product prepared in a conventional manner to provide a reconstituted tobacco sheet of good physical properties without detriment to the sheet color.
It has long been commonly believed that the agents responsible for the darkening of the tobacco on cooking were the carbohydrates and the amino acids, which react during the heating to form dark colored compounds, the process being called the Maillard reaction. We have discovered that neither the carbohydrates nor the amino acids darken the tobacco significantly on heating, but that polyphenols contained in the tobacco, especially the basic-polyphenols, do cause a significant darkening of the tobacco upon exposure to heating. This phenomenon is also pH dependent.
A series of tests were run to isolate and determine the agents which caused tobacco darkening upon heating. The following procedure illustrates how the polyphenols were identified as the agents which cause tobacco darkening during heating. A sample of Bright stem dust weighing 10 gm was mixed with ml. of distilled water. The slurry was filtered on a Buchner funnel using Whatman No. 1 filter paper. The filter cake and filtrate were retained. The filter cake was subsequently mixed with 90 ml. of a predetermined liquid and the slurry transferred to a vessel, such as a mason jar, which was sealed and placed in a pressure cooker, where it was heated at 250F. at 15 psi for 2 hours. Upon cooling, three sheets having a thickness of about 0.25-0.30 mm were cast from the slurry on 20 cm X 20 cm glass plates. The sheets were dried in an oven at 1 1 C. for about 15-20 minutes and the color of each sheet was read in a Gardner automatic color difference meter. Model AC-2A, Series 200. Readings were made by placing the plate over the Gardner aperture with the tobacco side facing the aperture. A number of readings were taken at different points on each plate so as to obtain an overall average.
The test results in Table 1 were obtained with various additives in the predetermined liquid and serve to illustrate that polyphenols are the agents causing the darkening of the tobacco on exposure to heat. Waterwashed Bright stem dust was used in all cases, unless otherwise indicated. The weight of the washed tobacco in each sample was' 7.0 gm. dry weight and this was suspended in 90 m1. of liquid prior to heating.
TABLE 1 COLOR OF SHEETS PREPARED FROM BRIGHT STEM DUST HEATED IN SOLVENTS CONTAINING VARIOUS ADDITIVES pH Before Heating pH After Materials Heating a Washed Tobacco Water (positive control) Unwashed Tobacco Water Washed Tobacco washings (negative control) Washed Tobacco Sucrose (2 gm.) Water Washed Tobacco Glucose (2 gm.) Water Washed Tobacco Fructose (2 gm.) Water Washed Tobacco Sucrose, Fructose, Glucose (2 gm. each) Water Washed Tobacco Tryptone (1 gm.) (casein digest) Water Washed Tobacco Tryptone Sucrose (1 gm. each) Water Washed Tobacco Tryptone Glucose (l gm. each) Water Washed Tobacco Tryptone Fructose (1 gm. each) Water Washed Tobacco Tryptone Glucose, Fructose Sucrose (1 gm. each) Water Washed Tobacco Water Acidic Polyphenols Basic Polyphenols Washed Tobacco Water Acidified Basic Polyphenols Washed Tobacco Water Washed Tobacco P,Acetate Sol. (10%) Water 23.4 Note: Rd Brightness Factor; black 0; white 0 Coordinates on a Chromaticity Diagram 12* Coordinates on a Chromaticity Diagram P, Acetate lead acetate As seen from the experimental results shown in Table I, the basic polyphenols make a sheet darker than' even the negative control (Rd readings 12.4 and 16.4, respectively). Furthermore, it is seen that while acidifying the basic polyphenols improves the color, it is still far below the positive control (Rd readings of 17.2 and 24.9, respectively). These results show that the sugars and amino acids do not affect the sheet color and similarly neither does the lead acetate solution used to precipitate the polyphenols.
Processes for the neutralization or removal of the polyphenol from tobacco with the addition of chemical substances are fully disclosed and described in our copending application, Ser. No. 639,066 filed May 17, 1967, now US. Pat. No. 3,540,450. The present disclosure confines itself to the removal of polyphenols without chemical substances.
.In order to extract the basic polyphenols from the tobacco without adding any chemical additive to the reconstituted tobacco sheet, the tobacco water washings can be treated with adsorbent material, which adds nothing to the extract, but selectively removes the darkening agent or agents by adsorption. For example, tobacco water washings are passed through a column containing a selected adsorbent material, such as activated alumina. The adsorbent removes the darkening material, but leaves the other valuable tobacco constituents unchanged in the extract. The treated extract is then recombined with the original washed tobacco and the combination is processed into reconstituted tobacco sheet, which retains its commercially acceptable light color with no additives.
In accordance with the disclosed process, untreated tobacco, such as broken leaves, cuttings, stemmings, various fragments or waste, field scrap, is subjected to a water extraction operation so as to separate the watersoluble constituents.
The water-soluble constituents of the tobacco or extract are separated from the insoluble portion by any convenient process, such as draining, pressing, or centrifuging. The aqueous extract contains various watersoluble materials, including polyphenols. This aqueous extract can then be passed through a column containing an adsorbent material, such as activated alumina.
Continuous operation in a column can be effected by reconstituted tobacco sheet is produced. The extracted coloring materials can be eluted from the adsorbent so that it can be reused as desired.
The following examples are set forth to demonstrate the method of this invention.
A glass column cm. X 3 cm.) was filled with a slurry of 100 gm. of activated alumnia (8-14 mesh) in water. The water was allowed to drain and the column was washed repeatedly with about 500-1000 ml. fresh water. A water extract of tobacco dust obtained by the method described above was passed over the column at a flow rate such that effluent was collected at 0.5 ml. per minute. The column was then washed with water until the washings were colorless. The combined water washings and collected effluent were then concentrated to 100 ml. under vacuum in a flash evaporator using a temperature range of 363 8C. The solids content in the concentrate, as well as in the original water tobacco extract were determined and the recovery of material from the column calculated from these values. The test results are presented in Table 2.
The FIGS. in Table 2 show that the solids recovery is 73-75 percent for Bright stem extracts and 89-91 percent for Penn. stem extracts.
The material not removed from the column by water washing was eluted off by passing 2 normal formic acid through the column. Fractions were collected at a rate of 0.5 ml per minute. The eluted samples were very dark in color. The 2 normal formic acid removed all the adsorbed material leaving the activated alumnia free of color. The alumina was washed with water until free of acid, dried in the oven (ll40C.) overnight and used again.
The formic acid was removed from the eluate (i.e., the basic-polyphenols) by evaporation under vacuum in a flash evaporator. The remaining dark brown material was made up to a 100 ml. volume with water and tested for carbohydrates by a thin layer chromatography method, such as described in the Journal of Chromatography 18, 170-174 (1965). Samples of the effluent concentrate from the column previously referred to as well as the original tobacco-water extract were also examined for carbohydrates. The results showed that practically all of the carbohydrates found in the original tobacco-water extract'were recovered in the concentrated effluent while only significant amounts were found in the formic acid eluate.
It should be noted that the material, which could not be removed from the column by water could be eluted off by other suitable solvents, such as percent ethanol containing 2 normal HCl or by 2 normal HCl solution. Advantageously, formic acid is preferred, since it is easily removed by evaporation under vacuum. This makes it possible to recover the solids from the formic acid eluate and their subsequent utilization in the color experiments. In an operation where these solids are of no consequence, their removal from the alumina would be carried out more economically with a 2 normal HCl solution.
The effluent concentrates were made up to volume and recombined with the washed tobacco. The slurries were treated in a manner as described above, The obtained sheets were examined in a Gardner colorimeter, and the results are presented in Table 3.
TABLE 3 GARDNER READINGS ON SHEETS PREPARED FROM VARIOUS EFFLUENTS AND ELUATES FROM ALUMINA COLUMNS pH of Tobacco Fraction Tob. Rd a+ b+ Slurry Bright EffluentConcentrate 5.8 21.5 37 17.5 Bright EffluentConcentrate 5.6 24.6 Bright Effluent Concentrate 4.7 24.6 5.4 34.4 Bright Formic Acid Eluate 3.2 17.4 4.1 22.7 Bright (positive control) 5.3 24.8 3.9 35.0 Bright (negative control) 4.8 16.8 4.8 22.3 Penn. Effluent Concentrate 6.3 19.6 5.0 24.6 Penn. Formic Acid Eluate 3.8 17.1 6.1 23.3 Penn. (positive control) 7.0 19.3 5.2 24.6 Penn. (negative control) 6.2 17.4 5.3 22.8 Bulgarian Efiluent Concentrate 5.1 15.8 Bulgarian (positive control) 5.7 15.3 Bulgarian (negative control) 5.2 11.3
Note: Positive control consists of washed tobacco (7 gm. dry weight) plus new water. Negative control consists of washed tobacco plus the obtained washings.
The FIGS. in Table 3 show that the effluent concentrate from the adsorbent column is similar in its. color properties to the positive control, while the formic acid eluate, after removing the formic acid and adjusting to volume with water, is similar to the negative control. This is particularly apparent in the Rd values.
Adsorbents, other than activated alumina, were examined. Regenerated alumina worked as well as unused alumina. Polyamide and silica gel also gave satisfactory results.
Other adsorbent materials could be used, such as magnesol, silicic acid or adsorption alumina, and the like. However, these materials are fine meshed and pack easily in the columns, so as to reduce flow through the columns. A pressure source would be necessary to obtain satisfactory flow through columns using these be employed effectively spirit and scope thereof, and therefore, the invention is not to be limited, except as defined in the appended claims.
What we claim is:
1. A reconstituted smoking tobacco composition comprising extracted tobacco having incorporated therein substantially all the extracted substances less only polyphenols.
Applications Claiming Priority (1)
Application Number | Priority Date | Filing Date | Title |
---|---|---|---|
US4874970A | 1970-05-18 | 1970-05-18 |
Publications (1)
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US3717155A true US3717155A (en) | 1973-02-20 |
Family
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Family Applications (1)
Application Number | Title | Priority Date | Filing Date |
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US00048749A Expired - Lifetime US3717155A (en) | 1970-05-18 | 1970-05-18 | Reconstituted tobacco product |
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US (1) | US3717155A (en) |
Cited By (3)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
US4562633A (en) * | 1984-03-01 | 1986-01-07 | Ortner Freight Car Company | Railway box car conversion to highway trailer-carrying flatcar and method of accomplishing it |
WO1989004661A1 (en) * | 1987-11-19 | 1989-06-01 | Indaus International Pty Ltd | Nicotine compositions |
US20090032036A1 (en) * | 2006-04-14 | 2009-02-05 | Hiromi Uematsu | Apparatus for producing a flavor for expanded tobacco material and method of producing same |
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US802487A (en) * | 1903-12-28 | 1905-10-24 | Karl Wimmer | Treatment of tobacco for the removal of nicotin. |
US2582075A (en) * | 1947-09-18 | 1952-01-08 | Severi Mentore | Process for removing nicotine from tobacco |
US2934073A (en) * | 1959-04-08 | 1960-04-26 | Henry E Killian | Cigarette |
US3110315A (en) * | 1960-07-27 | 1963-11-12 | Lendvai Andrew | Denicotinization of tobacco |
US3145717A (en) * | 1959-10-22 | 1964-08-25 | C H Dexter & Sons Inc | Methods of making tobacco web material |
US3338248A (en) * | 1964-08-27 | 1967-08-29 | Pavia Charles | Process of treating tobacco |
US3351066A (en) * | 1965-07-20 | 1967-11-07 | Harry R Colgate | Chemical composition alteration of tobacco |
US3361139A (en) * | 1964-08-07 | 1968-01-02 | Inoue Yoshitaro | Method of making filter material for cigarettes |
US3390685A (en) * | 1965-03-11 | 1968-07-02 | Eresta Warenhandelsgmbh | Process for extracting substances from plant particles |
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Publication number | Priority date | Publication date | Assignee | Title |
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US802487A (en) * | 1903-12-28 | 1905-10-24 | Karl Wimmer | Treatment of tobacco for the removal of nicotin. |
US2582075A (en) * | 1947-09-18 | 1952-01-08 | Severi Mentore | Process for removing nicotine from tobacco |
US2934073A (en) * | 1959-04-08 | 1960-04-26 | Henry E Killian | Cigarette |
US3145717A (en) * | 1959-10-22 | 1964-08-25 | C H Dexter & Sons Inc | Methods of making tobacco web material |
US3110315A (en) * | 1960-07-27 | 1963-11-12 | Lendvai Andrew | Denicotinization of tobacco |
US3361139A (en) * | 1964-08-07 | 1968-01-02 | Inoue Yoshitaro | Method of making filter material for cigarettes |
US3338248A (en) * | 1964-08-27 | 1967-08-29 | Pavia Charles | Process of treating tobacco |
US3390685A (en) * | 1965-03-11 | 1968-07-02 | Eresta Warenhandelsgmbh | Process for extracting substances from plant particles |
US3351066A (en) * | 1965-07-20 | 1967-11-07 | Harry R Colgate | Chemical composition alteration of tobacco |
Cited By (6)
Publication number | Priority date | Publication date | Assignee | Title |
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US4562633A (en) * | 1984-03-01 | 1986-01-07 | Ortner Freight Car Company | Railway box car conversion to highway trailer-carrying flatcar and method of accomplishing it |
WO1989004661A1 (en) * | 1987-11-19 | 1989-06-01 | Indaus International Pty Ltd | Nicotine compositions |
US5158771A (en) * | 1987-11-19 | 1992-10-27 | Spindler Frank R | Nicotine compositions |
US5326563A (en) * | 1987-11-19 | 1994-07-05 | Spindler Frank R | Nicotine compositions |
US20090032036A1 (en) * | 2006-04-14 | 2009-02-05 | Hiromi Uematsu | Apparatus for producing a flavor for expanded tobacco material and method of producing same |
US9066539B2 (en) * | 2006-04-14 | 2015-06-30 | Japan Tobacco Inc. | Apparatus for producing a flavor for expanded tobacco material |
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