A REDUCED PROTEIN RECONSTITUTED TOBACCO AND METHOD OF MAKING SAME

Abstract: A process for manufacturing reconstituted tobacco with reduced nitrogenous content by submitting cured tobacco material, including whole leaf, stems, scraps, fines and lamina, as well as burley leaf and stem, to an extraction with a solution containing sodium acetate, sodium hydroxide, potassium hydroxide or mixtures thereof. The extraction process, in addition to denitrifying the tobacco material, also produces reconstituted tobacco paper with characteristics similar to flue cured tobacco leaf.

Description: A REDUCED PROTEIN RECONSTITUTED TOBACCO AND METHOD OF MAKING SAME This invention relates generally to tobacco and reconstituted tobacco smoking materials and methods of making same. More particularly, the present invention relates to the materials and methods that provide tobacco materials with reduced nitrogenous content and also provide reconstituted tobacco paper with leaf-like characteristics. Tobacco material contains various nitrogenous compounds that can adversely affect its smoke quality. Among these nitrogenous compounds are proteins, amino acids and certain alkaloids, such as nicotine, nomicotine, anabasine and anatabine. The smoke quality of tobacco is adversely affected particularly by heterocyclic and aromatic amines, and tobacco specific nitrosamines (TSNA), as well as other compounds formed by pyrolysis or transfer of these nitrogenous compounds. Tobacco processing sometimes includes steps in which the nitrogen content of the tobacco is reduced, so as to improve the smokability of the tobacco. However, nitrogenous compounds, especially proteins, are difficult to extract from cured tobacco lamina, stem, and fibre cell walls. Insoluble proteins make up more than 90% of the total proteins found in cured tobacco. These insoluble proteins are globular in conformation, and are bound to lipoidal organocellular membranes of fibre or cellulose cell walls. Solubilisation and extraction of these insoluble proteins have traditionally proven difficult when using water or solvents under moderate digestion conditions (i.e. less than 100°C and 65-70 psig (4.481-4.826 bar)) and with shredded tobacco of a size suitable for cigarette manufacture. This difficulty is due in large part to the compact and rigid structure of fibre cells. Penetration of rigid cell wall structure by solvents has proved feasible only after thermal and/or mechanical sample treatment. However, the common result of such sample treatment is poor recovery of the solvated particulate material. Moreover, cell wall penetration does not necessarily lead to protein solubilisation, since plant proteins differ in their conformity and solubilisation patterns. More specifically, plant proteins are divided into four major classes: albumins; globulins; prolamins (also known as gliadins); and, glutelins. Albumins are soluble in water, whereas globulins are soluble in dilute salt solutions. Prolamins are soluble in dilute acid or alkali solutions, while glutelins are soluble in alcohol solutions. Some proteins, however, overlap into two of these four classifications, thereby increasing the difficulty of accurately predicting the appropriate diluent. Many of the current processes used to reduce nitrogen content in tobacco material employ enzymatic compounds and microbial agents to break down the proteins and other nitrogen-containing compounds within the tobacco. However, disadvantages arise from the use of such enzymatic compounds and agents, hi particular, enzymes are expensive, pH sensitive and degrade proteins into amino acids which tend to remain with the tobacco material. It is also thought that enzymatic compounds leave residues on tobacco material after processing. Furthermore, microbial agents used in treating tobacco tend to cause unwanted reactions that generate undesirable by-products. Therefore, there is a need to provide a process by which the nitrogen content of tobacco material may be reduced without leaving residues or undesirable by-products. This process must provide effective solubilisation of proteins and other nitrogenous compounds, as well as adequate particulate matter recovery. The present invention relates to a method for providing a reconstituted tobacco material having a reduced nitrogenous content. The tobacco material in the form of flue cured and burley whole leaf, stems, fines, lamina or scraps, and/or burley stems are contacted with an aqueous solvent. The resulting liquid extract is separated from the tobacco fibre portion. The tobacco fibre portion is then contacted with a solution containing sodium acetate and/or sodium hydroxide and/or potassium hydroxide. The solution from the mixture is then separated from the tobacco fibre portion. The tobacco fibre portion may then be washed, refined and processed into reconstituted tobacco sheets. The liquid extract from the aqueous solvent extraction may be concentrated and added back to the sheets. These sheets may then be used in smoking articles, such as cigarettes. The reduction of nitrogenous compounds in the tobacco material provides for improved smokability and a reduction in nitrogen containing pyrolitic products emitted from smoking articles, which contain the tobacco material. It is an object of the present invention to provide a reconstituted tobacco material with reduced levels of nitrogenous compounds. It is another object of the present invention to provide a method of making a reconstituted tobacco material with reduced levels of nitrogenous compounds. It is a further object of the present invention to provide a reconstituted tobacco material paper with a cured tobacco leaf-like texture. The present invention provides a method of making a tobacco material with reduced levels of nitrogenous compounds comprising: (a) providing a tobacco material; (b) contacting said tobacco material with a first aqueous solvent to provide an aqueous tobacco extract and a tobacco fibre portion; (c) separating said aqueous tobacco extract from said tobacco fibre portion; (d) contacting at a temperature from about 50°C to 150°C said tobacco fibre portion with a solution containing one or more of a compound selected from the group consisting of sodium acetate, sodium hydroxide and potassium hydroxide, wherein said solution contains said compound in a concentration about 0.1% to 10% (w/v) of said compound; and, (e) separating said solution from said tobacco fibre portion. The period of contact is advantageously about 0.25 to 24 hours. Preferably, the solution contains about 0.75% to 1.0% (w/v) sodium acetate, and/or 0.5% to 1.0% (w/v) sodium hydroxide, and/or 0.5% to 1.0% (w/v) potassium hydroxide. Advantageously, when the solution is or comprises sodium acetate, the temperature is within the range of 60°C to 70°C for about 12-24 hours; when the solution is or comprises sodium hydroxide the temperature is within the range of 85°C to 90°C for about 3-4 hours, and when the solution is or comprises potassium hydroxide the temperature is within the range of 80°C - 90°C for about 3-4 hours. Preferably when the tobacco material comprises burley tobacco the sodium acetate solution contains 0.75 - 1.0% (w/v) sodium acetate at a temperature of about 50°C - 90°C from about 0.5 - 0.75 hours; and/or the sodium or potassium hydroxide solution contains 0.25 - 0.75% (w/v) sodium or potassium hydroxide at a temperature of 85°C - 90°C for 0.5 - 3 hours. Furthermore, the present invention provides to a reconstituted tobacco sheet formed from the tobacco material treated according to the above method. The reconstituted tobacco sheet, formed from tobacco material treated according to the method, and particularly the method in which the solution contains sodium hydroxide or potassium hydroxide in the absence of sodium acetate, exhibits physical characteristics superior to those exhibited by reconstituted tobacco sheets formed by conventional or other methods. More particularly, a reconstituted tobacco sheet formed from tobacco material treated thus has a texture and density similar to that of cured tobacco leaf. This tobacco sheet, when cut, is less likely to crumble than a reconstituted tobacco sheet formed by conventional methods, and it is stronger than either cured tobacco leaf or conventional reconstituted tobacco sheet. In order that the invention is easily understood and readily carried into effect, reference will now be had to the accompanying diagrammatic flow drawing in which: Figure 1 is a schematic of the process steps representative of the present invention. In a preferred method of carrying out the nitrogen reduction process of the present invention, tobacco materials 10 in the form of flue cured and burley stems, scraps, fines, and lamina are contacted with a first aqueous solvent, such as water, at a temperature of about 60°C to 80°C for about 0.5 to 1 hour. The contacting of the tobacco with the water 12 may be conducted in a tank or similar mixing vessel in which the water and tobacco are heated and agitated. The resulting aqueous tobacco extract 15, containing flavour compounds, is separated from the tobacco fibre portion, preferably by centrifugation 14. The tobacco/water slurry may be pumped into a centrifuge from the mixing vessel and centrifugally separated therein. Once removed from the tobacco fibre portion 16, the aqueous tobacco extract 15 may be reserved for re-application to the fibre with or without separate processing. In one embodiment, the aqueous tobacco extract 15 may de-proteinated by contacting the extract with a solid phase absorbent 17, such as bentonite, in a vessel and then separated therefrom by centrifugation 19, or a similar separation process well known in the art. The nitrogen-reduced aqueous tobacco extract containing flavour compounds may then be concentrated 23 by vacuum evaporation, for example, and added back to a reconstituted tobacco paper 31. The nitrogen content of the tobacco fibre portion 16 separated from the aqueous tobacco extract 15 may be reduced by contacting the tobacco fibre portion 16 with a solution containing a mild salt, such as sodium acetate 18, and or an alkali, such as sodium hydroxide 22 and 20 and/or potassium hydroxide 21 and 22. The tobacco fibre portion 16 may be loaded into a tank or similar mixing vessel. In one embodiment, a solution containing a mass concentration from about 0.25% to 10% (weight/volume) sodium acetate (NaOAc) 18 may be charged to the vessel and contacted with the washed tobacco fibre portion at a temperature of about 50°C to 150°C for about 0.25 to 24 hours. Preferably, the solution will contain about 0.75% to 1.0% (w/v) sodium acetate and will be in contact with the tobacco fibre portion at a pH of 3.8 to 5.0 and a temperature of from about 60°C to 70°C for about 12 to 24 hours. Afterwards, the solution may be separated from the tobacco fibre portion by any means 24 well known in the art, preferably by pumping the slurry to a centrifuge wherein the fibre is centrifugally separated from the solution. The tobacco fibre portion may then be washed with second aqueous solvent, such as water, as noted by numeral 26, and further refined 28. The tobacco fibre portion may then be processed into sheets 30, to which may be added nitrogen-reduced aqueous tobacco extract 31. When burley material is treated with a solution containing sodium acetate according to this process, instead of the sodium acetate solution described above for use with non-burley material, fibrous burley material is preferably contacted with a solution containing about 0.75% to 1.0% (w/v) sodium acetate at a pH of about 3.5 to 11.0 and at a temperature of about 50°C to 90°C for about 0.50 to 0.75 hours. The liquid extract from the initial washing is usually not added back to the processed sheets when burley stem is processed in this manner. Two alternative embodiments of the nitrogen reduction process of the present invention include the initial water extraction step described herein above. However, in these two embodiments, sodium hydroxide may be added to 22, or substituted for 20, the sodium acetate. More specifically, instead of the solution described above, the tobacco fibre portion may be extracted with a solution containing about 0.1% to 10% (w/v) sodium hydroxide (NaOH), either in combination with sodium acetate and/or potassium hydroxide 22, or in the absence of sodium acetate and potassium hydroxide. If the solution contains sodium hydroxide without either sodium acetate or potassium hydroxide, then the tobacco fibre portion should be contacted with the solution for about 3.0 to 7.0 hours at a temperature of from about 50°C to 150°C. Preferably, the tobacco fibre portion is contacted with a solution containing about 0.5% to 1.0% (w/v) sodium hydroxide for about 3 to 4 hours at a temperature of from about 85°C to 90°C. The solution may thereafter be separated from the tobacco fibre portion by a method well known in the art, as noted by numeral 24, such as centrifugation. The nitrogen-reduced tobacco fibre portion may then be contacted with a second aqueous solvent, such as water 26, refined 28 and formed into sheets 30, to which liquid extract containing flavour compounds from the initial washing is added, as noted by numeral 31, for use in a smoking article 32, such as a cigarette. Additionally, potassium hydroxide (KOH) may be included in the solution with which the tobacco fibre portion is contacted. As indicated by numeral 21, the tobacco fibre portion may be contacted with a solution containing potassium hydroxide, or, as in numeral 22, the solution may contain potassium hydroxide along with sodium acetate and/or sodium hydroxide. Either one of the solutions set forth in numerals 21 and 22 may contain about 0.10%) to 10% (w/v) potassium hydroxide. Preferably, these solutions may contain about 0.5% to 1.0% (w/V) potassium hydroxide. The solution 21 containing potassium hydroxide in the absence of sodium acetate and sodium hydroxide may be contacted with the tobacco fibre portion for about 3 to 7 hours at a temperature of about 50°C to 150°C. Preferably, the tobacco fibre portion is contacted with the solution containing potassium hydroxide 21 for about 3 to 4 hours at a temperature of 80°C to 90°C. The solution containing potassium hydroxide, sodium acetate and/or sodium hydroxide 22 may be contacted with the tobacco fibre portion for about 0.25 to 24 hours at a temperature of about 50°C to 150°C. When the tobacco material being treated with sodium hydroxide or potassium hydroxide is burley stem, the fibrous portion is preferably contacted with a solution containing about 0.25%) to 0.75% (w/v) sodium hydroxide or potassium hydroxide at a temperature of about 85°C to 90°C for about 0.5 to 3 hours. Again, the liquid extract separated from the tobacco fibre portion in the initial washing with the first aqueous solvent is not added back to the reconstituted tobacco paper when the tobacco material is burley stem. The reconstituted tobacco paper formed from the process described above, particularly the embodiment in which the solution contains sodium hydroxide or potassium hydroxide 22 in the absence of sodium acetate, exhibits unique physical characteristics. These unique characteristics are exhibited by reconstituted tobacco papers formed from both flue cured and burley tobacco. In particular, the tobacco sheet formed from tobacco material treated with sodium hydroxide 20 or potassium hydroxide 22 is stronger than reconstituted tobacco paper formed by conventional methods. Also, this tobacco sheet exhibits a texture and a density that are similar to that exhibited by flue cured tobacco leaf. This reconstituted tobacco paper, when cut, will not crumble as easily as paper formed by conventional methods. Therefore, less tobacco paper is wasted in the process of making smoking articles, such as cigarettes. Thus, reconstituted tobacco paper formed by the above described process provides advantages in the cigarette making process over conventionally formed reconstituted tobacco paper. Prior to addition of the nitrogen-reduced aqueous tobacco extract, the sheets formed from tobacco treated by the preferred embodiments of this process exhibit reductions of 28% to 93%) (dry weight basis) in Kjeldahl nitrogen and 19% to 81% protein nitrogen when compared to sheets made via the conventional process, as shown in Table 1. After addition of the nitrogen-reduced liquid extract, these reconstituted tobacco sheets exhibit final reductions of 23% to 40%) (d.w.b) in Kjeldalil nitrogen, and 22% to 56% in protein nitrogen, as shown in Table 1. Table 1 Reductions in Kjeldahl nitrogen, protein nitrogen, and nitrate of tobacco extracted with salt and/or alkali solutions Extraction Conditions Nitrogen components (%) Example Starting Chemical Soln pH Temp Time Kjeldahl Protein Nitrate material (%) (°C) (h) Control 1 Ground stock 1 - - - - - 2.25 - 2.71 Control 2 Ground stock Water 100 6.8 60-80 0.5-1.0 1.72 - trace Control 3 Conventional — — — — — 1.47 1.15 0.00 sheet without added extract Control 4 Conventional 2.22 0.85 3.41 sheet with extract added back " ' Control 5 Shredded - - ~ - - 2.45 0.90 7.7 Burley stem Control 6 Shredded Water 1.00 6.8 60 0.5 2.13 - 1.49 Burley stem la Washed fibre 2 NaOAc 1.00 3.8 60 24 0.10 0.10 bcl 3 lb Washed fibre NaOAc 1.00 5.0 60 12 1.06 0.93 bcl lc Washed fibre NaOAc 1.00 8.3 60 12 1.04 0.93 bcl Id Washed fibre NaOAc 1.00 11.0 60 12 1.06 0.93 bcl 2 . Shredded NaOAc 1.00 3.8 60 18 0.33 - 0.05 Burley stem 'Formula including fiue-cured burley scrap, stem, fines, lamina, and wood pulp. 2 Solids collected after ground stock including wood pulp have been extracted with water at 60-80 C for 0.5 h. bcl = below calibration limits. Extraction Conditions Nitrogen components (%) Example Starting Chemical Soln pH Temp Time Kjeldahl Protein Nitrate material (%) (°C) (h) 3 Washed fibre NaOH 1.50 12.5 88 12 1.06 - bcl 4 Shredded NaOH 1.00 12.5 60 12 0.86 - 0.05 Burley stem 5a Washed fibre NaOH 0.25 12.5 88 3 0.57 - bcl 5b Washed fibre NaOH 0.50 12.5 88 3 0.44 0.35 bcl 5c Washed fibre NaOH 0.75 12.5 88 3 0.25 0.22 bcl 5d Washed fibre NaOH 1.00 12.5 88 3 0.28 0.28 bcl 5e Washed fibre KOH 0.50 12.5 88 3 0.83 - bcl 5f Washed fibre KOH 0.75 12.5 88 3 0.69 - bcl 6a Washed fibre NaOAc/ 0.75 - 88 4 1.00 0.93 bcl KOH 0.25 6b Washed fibre NaOAc/ 0.75 - 88 4 0.69 - bcl NaOH 0.25 6c Washed fibre NaOAc/ 0.50 - 88 4 0.71 -- bcl KOH 0.50 7a Shredded NaOAc 1.00 11.0 121 0.5 0.40 - 0.07 Burley stem 20ρsi (1.379 bar) 7b Shredded NaOH 0.25 12.5 80 0.5- 0.69 - 0.04 Burley stem 0.75 7c Shredded NaOH 0.50 12.5 80 0.5- 1.05 - 0.07 Burley stem 0.75 EXAMPLES For a better understanding of the present invention, the following Examples are incorporated herein to illustrate the present invention with no intention of being unduly limited thereby. EXAMPLE 1 A 6.8 kg mixture of tobacco materials, including flue cured and burley tobacco scraps, stems, laminae and fines having a nitrogen content of 2.25% was extracted with water at 60°C for 30 minutes as known in the art. Following centrifugation, the liquid extract was further treated with diatomaceous clay to remove nitrogenous compounds and then concentrated by vacuum evaporation. The resultant washed fibre was further extracted to remove nitrogenous compounds, as mentioned below. From the washed fibres, 80g portions were then loaded into vessel containing 400 ml of 1.0% (w/v) sodium acetate at a pH 3.8, 5.0, 8.3, or 11.0, which are Examples la, lb, lc, Id, respectively, shown in Table 1. The sodium acetate solution containing the tobacco material was then heated to 60°C for 12 to 24 hours while being agitated. After this period of heating and agitation, the liquid was separated from the tobacco fibre portion through centrifugation. The solids were rinsed with water. The final fibrous residue was then dried for 24 hours at 35°C. The sample was then tested for Kjeldahl nitrogen content and found to have a Kjeldahl nitrogen content of 1.06%) to 0.1%, exhibiting a reduction of 53.0% to 95.5%) (d.w.b) from the initial Kjeldahl nitrogen content of the tobacco material of Control 1 shown in Table 1. The fibrous material was then refined and formed into paper-like sheets on a Fourdiner type wire papermaking machine. EXAMPLE 2 Burley stem of Control 5 shown in Table 1 having a Kjeldahl nitrogen content of 2.45%, a protein content of 0.9%>, and a nitrate content of 7.7% was shredded in a Waring blender at low speed for 30 seconds and then 80 gram samples were dispersed and agitated in 400ml solution of 1.0% (w/v) sodium acetate (pH 3.8) for 18 hours which is Example 2 shown in Table 1. The liquid and solid portions were then separated by centrifugation and the tobacco stems were dried. The resulting fibrous material was found to have a nitrogen content of 0.33%) and a nitrate content of 0.05%, exhibiting a reduction in Kjeldahl nitrogen of 86.5% (d.w.b), and nitrate reduction of 99.3%> (d.w.b.), as compared to the burley stem of Control 5 of Table 1. EXAMPLE 3 This example was carried out in the same manner and with the same quantities of materials as in Example 1, the only changes being that the 400ml solution contained 1.5% (w/v) sodium hydroxide at a pH of 12.5, shown in Table 1 as Example 3. The resulting fibrous material had a 52.9% reduction in Kjeldahl nitrogen. The 12 hour extraction resulted in >60% solids loss due to fibre degradation. However, the paper-like sheet formed from this extracted residue exhibited characteristics that made it superior to conventional reconstituted paper. More specifically, the paper formed from the tobacco material treated with sodium hydroxide was light and unexpectedly strong. Unlike conventional reconstituted paper, its density and texture were very similar to flue cured tobacco leaf, but it was significantly stronger than either flue cured tobacco leaf or conventional reconstituted paper. EXAMPLE 4 This example was carried out in the same manner and with the same quantities of materials as that utilised in Example 2, except that the 400ml solution contained 1.0% (w/v) sodium hydroxide at a pH of 12.5, instead of sodium acetate. The resulting residue exhibited a 65% reduction in Kjeldahl nitrogen and a 99.3% reduction in nitrate, as compared to Control 5 shown in Table 1. The resulting paper-like sheet formed exhibited similar advantages to those exhibited by the sheet formed in Example 3. Excessive loss in solids was also observed as in Example 3. EXAMPLE 5 This example was carried out in the same manner as Example 1, except that 350 g portions of washed fibre were extracted in a vessel with 3 litres of 0.25%, 0.5%, 0.75%, or 1.0% (w/v) sodium hydroxide at 88°C for 3 h, which are Examples 5a, 5b, 5c, 5d, respectively, of Table 1. The resulting paper showed a 74.7% to 88.8% reduction in Kjeldalil nitrogen as compared to Control 1 shown in Table 1. The resulting paper-like sheet exhibited similar advantages to those formed in Example 3 and 4. EXAMPLE 6 This example was carried out in a similar manner as Example 5, except that extraction time was 4 h and the 3 litre solutions were made up of 0.75% (w/v) sodium acetate and 0.25% (w/v) potassium hydroxide, 0.75% (w/v) sodium acetate and 0.25% (w/v) sodium hydroxide, or 0.5% (w/v) sodium acetate and 0.5% potassium hydroxide. The resulting paper showed a 55.5%) to 69.3% reduction in nitrogen, as compared to the ground stock of Control 1 shown in Table 1. The resulting sheets did not show the paper quality advantages exhibited by those in Example 3, 4, and 5. EXAMPLE 7 Burley stem was shredded in a double disc shredder and then 350g portions were dispersed in 3 litres of 1% (w/v) sodium acetate at a pH 11.0, which is Example 7a shown in Table 1, and in 3 litres of 0.25% or 0.5% (w/v) sodium hydroxide, which are Examples 7b and 7c, respectively, shown in Table 1. The sodium acetate mixture was heated in an autoclave at 121°C and 20 psi (1.379 bar) pressure for 30 min., while the sodium hydroxide mixtures were extracted in a cooker kettle at 80°C for 30-45 min. Following centrifugation, the fibrous material was refined and fonned into paper-like sheets on a Fourdiner wire papermaker. The resulting sheets were 83.7 to 57.1% lower in Kjeldahl nitrogen content than the shredded stem of Control 5 of Table 1. The sodium hydroxide treatments again resulted in sheets with more advantageous qualities than the one made via the sodium acetate process. Reconstituted tobacco paper prepared from tobacco material from Examples 1- 4 all exhibited significant reductions in nitrogen content. Treatment of tobacco materials with sodium hydroxide resulted in lower yields than those treated with sodium acetate or combinations thereof with sodium hydroxide or potassium hydroxide. However, the paper samples formed from the tobacco treated with sodium hydroxide in Examples 3, 4, 5, or 7, as well as those samples treated with potassium hydroxide in Example 5, were stronger and more similar in texture and weight to flue cured tobacco leaf than the paper formed from the tobacco treated with sodium acetate in Examples 1, 2, or 6. The foregoing detailed description and Examples are given primarily for clearness of understanding and no unnecessary limitations are to be understood therefrom for modifications will become obvious to those skilled in the art upon reading the disclosure and may be made without departing from the spirit of the invention and scope of the appended claims.

Claims: CLAIMS 1. A method of making a tobacco material with reduced levels of nitrogenous compounds comprising : (a) providing a tobacco material; (b) contacting said tobacco material with a first aqueous solvent to provide an aqueous tobacco extract and a tobacco fibre portion; (c) separating said aqueous tobacco extract from said tobacco fibre portion; (d) contacting at a temperature from about 50°C to 150°C said tobacco fibre portion with a solution containing one or more of a compound selected from the group consisting of sodium acetate, sodium hydroxide and potassium hydroxide, wherein said solution contains said compound in a concentration about 0.10% to 10% (w/v) of said compound; and, (e) separating said solution from said tobacco fibre portion. 2. The method of Claim 1, said method further comprising: (f) contacting said tobacco fibre portion with a second aqueous solvent. 3. The method of Claim 1 or 2, wherein said tobacco material is contacted with said first aqueous solvent at a temperature of about 60°C to 80°C for about 0.5 to 1 hour. 4. The method of Claim 1, 2 or 3, wherein said tobacco fibre portion is contacted with said solution for about 0.25 to 24 hours. 5. The method of Claim 1, 2, 3 or 4, wherein said solution is at a pH from about 3.5 to 14.0. 6. The method of any one of Claims 1 to 5, wherein said tobacco fibre portion is centrifugally separated from said aqueous tobacco extract. 7. The method of any one of Claims 1 to 5, wherein said tobacco fibre portion is centrifugally separated from said solution. 8. A reconstituted tobacco sheet containing tobacco material treated in accordance with the method of any one of Claims 1 to 7. 9. The method of any one of Claims 1 to 7, wherein said tobacco fibre portion is contacted with said solution containing from about 0.75 %> to 1.0% (w/v) sodium acetate. 10. The method of Claim 9, wherein contacting of said tobacco fibre portion with said solution containing about 0.75 % to 1.0% (w/v) sodium acetate is at a temperature of from about 60°C to about 70°C for about 12 to 24 hours. 11. The method of Claim 10, wherein said solution is at a pH of 3.8 to 5.0. 12. The method of any one of Claims 1 to 7 or 9 to 11, wherein said tobacco fibre portion is contacted with said solution containing about 0.5% to 1.0% (w/v) sodium hydroxide. 13. The method of Claim 12, wherein contacting of said tobacco fibre portion with said solution containing about 0.5 %> to 1.0% (w/v) sodium hydroxide is at a temperature of from about 85°C to about 90°C for about 3 to 4 hours. 14. A reconstituted tobacco sheet containing tobacco material treated in accordance with the method of Claim 13. 15. The method of any one of Claims 1 - 7 or 9 - 13, wherein said tobacco fibre portion is contacted with said solution containing about 0.5%) to 1.0% (w/v) potassium hydroxide. 16. The method of Claim. 15, wherein contacting of said tobacco fibre portion with said solution containing about 0.5% to 1.0% (w/v) potassium hydroxide is at a temperature of from about 80°C to about 90°C for about 3 to 4 hours. 17. A reconstituted tobacco sheet containing tobacco material treated in accordance with the method of Claim 16. 18. The method of any one of preceding Claims 1-7, 9-13 or 15-16, wherein said tobacco material includes flue cured tobacco. 19. The method of any one of preceding Claims 1-7, 9-13 or 15-17, wherein said tobacco material includes burley tobacco. 20. The method of Claim 19, wherein said tobacco fibre portion is contacted with said solution containing about 0.75%> to 1.0% (w/v) sodium acetate. 21. The method of Claim 20, wherein contacting of said tobacco fibre portion with said solution containing about 0.75% to 1.0% (w/v) sodium acetate is at a temperature of about 50°C to 90°C for about 0.50 to 0.75 hours. 22. The method of Claim 21, wherein said solution is at a pH of 3.5 to 11.0. 23. The method of Claim 19, wherein said tobacco fibre portion is contacted with said solution containing about 0.25%o to 0.75% sodium hydroxide. 24. The method of Claim 23, wherein contacting of said tobacco fibre portion with said solution containing about 0.25% to 0.75% (w/v) sodium hydroxide is at a temperature of about 85°C to about 90°C for about 0.5 to 3.0 hours. 25. A reconstituted tobacco sheet containing tobacco material treated in accordance with the method of Claim 24. 26. The method of Claim 19, wherein said tobacco fibre portion is contacted with said solution containing about 0.25%> to 0.75% potassium hydroxide. 27. The method of Claim 26, wherein contacting of said tobacco fibre portion with said solution containing about 0.25% to 0.75% (w/v) potassium hydroxide is at a temperature of about 85°C to about 90°C for about 0.5 to 3.0 hours. 28. A reconstituted tobacco sheet containing tobacco material treated in accordance with the method of Claim 27. 29. A method according to any one of Claims 1-7, 9-13, 15-16, 18-24 or 26-27, wherein said solution contains at least two compounds selected from said group. 30. A method according to any one of Claims 1-7, 9-13, 15-16, 18-24 or 26-27, wherein said solution is either sodium hydroxide or potassium hydroxide. 31. A reconstituted sheet containing tobacco material treated in accordance with the method of Claim 29 or 30. 32. A reconstituted sheet containing tobacco material treated substantially as hereinabove described with reference to Figure 1 hereof. 33. A method of making a tobacco material with reduced levels of nitrogenous compounds substantially as hereinabove described with reference to any one of Examples 1-7 hereof.

Inventors: BAKER TERRYL VANETTER, BRADLEY KENNETH JOHN JR, CONWAY WILLIAM RICHER, DREXLER WALTER MICHAEL, MUA JEAN-PAUL, BAKER, TERRYL, VANETTER, BRADLEY, KENNETH, JOHN, JR., CONWAY, WILLIAM, RICHER, DREXLER, WALTER, MICHAEL, MUA, JEAN-PAUL
Applicants: BRITISH AMERICAN TOBACCO CO, BRITISH AMERICAN TOBACCO (INVESTMENTS) LIMITED
Application year: 2001
Main classification: A24B15
IPC codes: A24B15