Tobacco treatment

Abstract: Provided is a method for removing polypeptides from an aqueous extract of tobacco material. The method comprises the steps of treating the extract with an insoluble adsorbent selected from hydroxyapatite or a fuller's earth mineral such as bentonite. The extract is then separated from the adsorbent. Treatment of the aqueous extract with bentonite will produce an extract having a reduced pigment and polypeptide content.

Description: TECHNICAL FIELD This is invention relates to the treatment of tobacco material to reduce its protein content. BACKGROUND ART Investigators have found that tobacco quality is improved by reducing its protein content. Although it is relatively easy to remove protein from uncured tobacco leaf, there are disadvantages to removing protein before curing. The major problem is that protein broken down during curing can form flavour compounds that are important contributors to the organoleptic properties of the smoke. Another disadvantage is that efficient extraction of green leaf usually necessitates tobacco structural changes which make it difficult to produce shredded tobacco suitable for use as a cigarette filler. Partial removal of protein from cured tobacco can be accomplished by extraction with water, with the efficiency of the extraction improving as the particle size is reduced. However, for shredded tobacco of the size normally used for cigarette manufacture, most of the protein cannot be extracted by water alone. United States Patent no. 4,407,307 describes the removal of protein from tobacco strips in an aqueous solution of a proteolytic enzyme whereby insoluble proteins are decomposed into soluble fragments. The extract is separated from the tobacco and inoculated with a yeast culture, which, as it grows, removes the soluble protein fragments in the extract by metabolic assimilation. After removal of the yeast, the protein-free extract is concentrated and added back to the tobacco strips. United States Patent no. 4,887,618 describes a process in which tobacco is first extracted with water. The tobacco residue remaining after extraction is separated from the solution, mixed with water and treated with a proteolytic enzyme. The protein-reduced tobacco is separated from the enzyme solution, rinsed and dried. The water extract is concentrated and added back to the protein reduced tobacco whereby water soluble flavour tobacco components and the nicotine is retained in the final product. The processes of the above described United States Patents rely on protease enzymes alone to remove protein from tobacco material. Our own investigations have found that enzymes which efficiently remove protein from tobacco are expensive, while those enzymes which are available in commercial quantities at a reasonable price, are much less efficient for protein removal. United States Patent no. 4,716,911 also recognizes this disadvantage and proposes using either an alkali or a combination of a protease and a non-protease depolymerase to effect protein removal. However, we have found that alkaline solutions may have a deleterious effect on the physical structure of the tobacco, and the use of a protease combined with a depolymerase may not be an economical approach to protein removal. Therefore, it is desirable to provide a technique for protein removal from tobacco that does not cause a physical degradation of the tobacco structure and is economical and efficient. It is also desirable to provide an efficient and cost effective process for removal of solubilized polypeptides (which include proteins) from an aqueous extract of tobacco, before the extract is added to solid tobacco material. In United States Patent no. 4,407,307, protein fragment in an aqueous extract was assimilated by yeast. United States Patent no. 4,941,484 describes the use of ultrafiltration to remove high molecular weight compounds, (including proteins) from an aqueous extract of tobacco before the extract is added to protein-reduced tobacco. The former method is unduly complicated by the requirement to ferment the aqueous extract in the presence of yeast. The ultrafiltration process requires the use of special apparatus and may not be useful for the removal of polypeptides outside the cut-off values of the ultrafiltration membrane employed in the procedure. It is known to treat an aqueous extract of tobacco with a solid adsorbent to remove polyphenols, for example, as described in United States Patent no. 3,561,451. Such adsorbents include alumina and polyamide which are not useful for removal of solubilized protein or polypeptides from the aqueous extract. Heretofore, there were no adsorbents known to be useful for removal of the polypeptides found in a tobacco extract in commercial batch processing. DISCLOSURE OF THE INVENTION This invention provides methods that involve the use of hydroxyapatite and fuller's earth minerals such as bentonite as insoluble adsorbents for removal of polypeptides, including proteins, from aqueous extracts of tobacco. Bentonite is a particularly effective adsorbent because of its low cost and effectiveness in small quantities. This is surprising since bentonite is known to be useful for adsorbing proteins in acidic beverages such as wine but is now shown effective for removal of proteins from more basic tobacco extracts. Furthermore, it is known that bentonite will adsorb nicotine, which may not be desirable in a tobacco treatment. Surprisingly, bentonite may be used to selectively adsorb polypeptides rather than nicotine. Bentonite is also effective for removal of pigment compounds from an aqueous extract of tobacco which is advantageous because such compounds tend to darken tobacco material when the extract is applied to the material, particularly when the extract has been heated to facilitate its concentration. This invention provides a method for removing polypeptides from an aqueous extract of tobacco material which includes combining the extract with an insoluble adsorbent selected from the group comprising hydroxyapatite and a fuller's earth mineral and, separating the extract from the adsorbent. In another aspect of this invention tobacco material is treated as described in claim 10. Tobacco material is first extracted with an aqueous solvent. This method is preferred since it is easier to ensure complete removal of surfactant and enzyme from the final tobacco product. The initial aqueous extract is separated from the insoluble tobacco residue and retained for subsequent reconstitution. The aqueous extract is treated to remove solubilized polypeptides as described below. The tobacco residue is resuspended in an aqueous solution of a surfactant or a mixture of surfactant and proteolytic enzyme. Alternatively, sequential treatment with the enzyme and surfactant may be carried out. After further protein has been solubilized, the latter solutions are separated from the tobacco residue and discarded. The extracted tobacco residue is rinsed and dried. The aqueous extract from the initial extraction is sprayed back onto the tobacco residue to make a smokable cigarette filler. Preferably, the aqueous extract is concentrated before applying to the tobacco residue. The extract is treated with hydroxyapatite or a fuller's earth mineral such as bentonite or attapulgite to remove solubilized polypeptides, and in the case of bentonite treatment, to also remove pigment compounds. In each case, the extract may be combined with the adsorbent by simply suspending the adsorbent in the solution and then removing the adsorbent by conventional means such as filtration or centrifugation. Other methods of combining the extracts or solutions with an insoluble adsorbent are well known and may be used in the method of this invention. For example, the adsorbent may be enclosed in a column or other suitable container and the extract is allowed to flow through the column or container to permit adsorption to occur. MODES FOR CARRYING OUT THE INVENTION Strip, cut or ground tobacco, and preferably cut tobacco, is extracted at 35-65°C in an aqueous solution of a surfactant or a mixture of surfactant and proteolytic enzyme. The solvent, which is usually water, but can also contain alcohols such as ethanol or methanol, is added to the tobacco material in the ratio of between 10:1 and 30:1 by weight. Preferably, the concentration of surfactant in the solvent is 0.1% - 5% w/v. The surfactant may be selected from the group including the sodium alkylsulfonates, sodium alkylsulfates, the sodium or potassium salts of carboxylic acids, sodium alkylarylsulfonates and sodium alkylsulfosuccinates. For these surfactants, the most effective have a chain length of between 8 and 12 carbon atoms. Particularly effective surfactants are sodium dodecylsulfate, sodium dodecylbenzenesulfonate and sodium dioctylsulfosuccinate (Aerosol OT* ). Cationic and non-ionic surfactants may be used but these have been found to be less effective than the anionic surfactants. The proteolytic enzyme, if used, is preferably chosen from the group comprising the bacterial and fungal enzymes. Of most interest for the purpose of this invention are the enzymes used commercially in the food and detergent industries which are available at low cost. Thus, Savinase* , Neutrase*, Enzobake* or Alcalase* available from Novo Inc. have been found to be effective for protein removal from tobacco. The proteolytic enzymes are preferably added to the solution in a concentration range of 0.1%-5% w/w of the tobacco material. The suspension of tobacco material in the solution of surfactant or surfactant and proteolytic enzyme is stirred gently for 1-18 hours. The extracted tobacco residue is separated from solubilized tobacco components by filtration or centrifugation. Up to about 65% of the initial tobacco weight may be solubilized during this extraction step. The tobacco components that go into solution are nicotine, sugars, polypeptides, amino acids, pectins, polyphenols, flavours, inorganic salts, etc. Alternatively, the tobacco material may be extracted, as described above, sequentially with solutions of surfactant and a proteolytic enzyme. In some cases, sequential treatment, particularly with enzyme treatment preceding surfactant treatment, provides a greater reduction of tobacco protein. The extract may be treated in a number of ways to remove surfactant and polypeptides, or other components, before the extract is added back in concentrated form to the extracted tobacco. Polypeptides are removed from the solution using an insoluble adsorbent such as hydroxyapatite, or one of the fuller's earth minerals such as attapulgite or bentonite. Larger amounts of adsorbent remove greater amounts of protein. When hydroxyapatite is added in a quantity of about 16-25% of the initial tobacco weight (the weight of the tobacco used to provide the extract) up to about 50% of the dissolved protein is removed. When about 10% of the initial tobacco weight of attapulgite (Attagel 40* ; Engelhard) is used, all or a large proportion of the dissolved protein is removed. When bentonite is added to the tobacco extract in a quantity that is about 3-4% of the weight of the tobacco extracted, a large proportion of the protein nitrogen is removed from solution. Some nicotine is also adsorbed from solution, but this loss is minimal at the concentrations of bentonite required to remove most of the polypeptides. The quantity of bentonite may be reduced if the bentonite is slurried in a small quantity of water before adding it to the tobacco extract. Premixing with water swells the bentonite, which forms a flocculent suspension when added to the tobacco extract. Bentonite treatment is also effective in removing pigment compounds found in a tobacco extract. It appears that a tobacco extract is an effective buffer against bentonite's tendency to make a solution more alkaline. Although it is generally unnecessary in the methods of this invention to adjust the pH of the tobacco extract, the efficiency of adsorption by bentonite may be increased by reducing the pH of the extract. Flue-cured tobacco extracts typically have a pH in the range 5-6. As the pH is lowered by adding an acid, smaller quantities of bentonite may be required for polypeptide and pigment removal. The optimum pH is about 3. The pH may be adjusted by addition of any suitable acid such as hydrochloric. At this stage, other components of the extract may also be selectively removed. For example PVPP may be used as an insoluble adsorbent using the same methods as for absorbtion of polypeptides. PVPP in an amount representing 5-10% of the initial tobacco weight removes up to about 50-90% of the polyphenols in solution. Preferably the extract is concentrated to a solids concentration of between 20-50% by weight. Concentrations of between 20-30% are most efficiently achieved using reverse osmosis, using procedures known in the art such as that disclosed in United States Patent no.3,847,163. However, other methods of concentration, particularly those which preserve the flavour and other components of the extract are known and may be used. The extracted tobacco, if in the cut or strip form, may be dried by a variety of known methods. Also, a rotary dryer with steel combs attached to the inside wall of the drum, to prevent balling of the wet tobacco, may be used to dry the tobacco. The concentrated extract may be sprayed onto the tobacco residue, during or after drying. This results in a tobacco which is very similar in physical form and appearance and smoking properties to the original material, but with substantially reduced levels of protein. When sufficient bentonite is used as an adsorbent, the consequent removal of pigment compounds results in a product that is not overly darkened by the addition of the concentrated extract. If the original tobacco is in the ground form, the final product may be cast into a sheet, which, when shredded, can form all or part of a cigarette filler. In another embodiment of the invention, the tobacco is first extracted with an aqueous solvent consisting either of water or a mixture of water with an alcohol (for example, methanol or ethanol). The ratio of solvent to tobacco is preferably about 20:1 by weight but can be as low as 12:1. The extraction time may be between fifteen minutes to one hour, at a temperature between 15-60°C. The preferred conditions are 1/2 hour at 25°C. The extraction step results in some of the polypeptides and most of the sugars, nicotine, amino acids, polyphenols, etc. being removed from the tobacco into solution. The aqueous extract may be separated from the tobacco by filtration or centrifugation. Polypeptides, polyphenols, and pigment compounds etc. may be removed from this extract by the methods described in the first embodiment. The extract may be concentrated by reverse osmosis or by other known methods. The extracted tobacco residue is subjected to a further extraction step to remove protein. An aqueous solution of a surfactant such as described in the first embodiment, at a concentration in the range 0.01-5% (w/v) is added to the wet or dried tobacco residue in the ratio of 20:1 to 30:1 (solution: dry tobacco weight). Alternatively, a proteolytic enzyme such as described in the first embodiment, may be added to the surfactant solution in a concentration range of 0.1-5%. If surfactant alone is used, the tobacco slurry is agitated gently for 1-18 hours at 24-65°C. For a mixture of surfactant and enzyme, the same time may be allowed for the extraction but a narrower temperature range such as 30-40°C should be used to avoid denaturing the enzyme. Sequential treatment with enzyme and surfactant may be carried out. Following extraction, the tobacco residue may be separated from the solution by filtration or centrifugation and the residue rinsed thoroughly with water. The tobacco residue may then be dried and the concentrated extract sprayed back onto the tobacco residue, as described in the first embodiment. EXAMPLE I Two hundred and fifty grams (250 g) of a single grade of flue-cured tobacco, cut at 35 cpi, was extracted with 5 litres of water containing 100 g of sodium dodecylsulphate (SDS). The extraction was carried out for 18 hours at 60-70°C with gentle stirring. The tobacco residue was separated from the solution by filtration and dried using a small rotary drier. After correction for moisture content, it was calculated that 66% of the tobacco weight was in the solute. The initial nitrogen content of the tobacco, as determined by the Kjeldahl method, was 1.82% (on a dry weight basis) while the extracted tobacco had a nitrogen content of 0.94% (on a dry weight basis). Thus 82% of the nitrogen in the tobacco was solubilized. The extract was cooled to 4°C and the precipitated SDS collected by filtration. This resulted in recovery of 68% of the SDS. The remaining SDS was precipitated by adding 6g of CaCl 2 to the solution. The precipitate was removed by filtration. Fifty grams (50 g) of hydroxyapatite (Calcium phosphate tribasic; Mallinckrodt)was added to the solution, stirred for 1/2 hour, and removed by filtration. The protein content of the solution was measured before and after treatment by the BioRad* method. Hydroxyapatite reduced protein content by about 50%. The extract was allowed to evaporate at 25°C until it was sufficiently concentrated to spray back onto the extracted tobacco residue. EXAMPLE 2 300 g of flue-cured shredded tobacco was extracted with 6 litres of water for 1 hour at 30°C. The tobacco extract was separated from the tobacco material by centrifugation and divided into 200 ml aliquots, which were treated with various quantities of either hydroxyapatite (Mallinckrodt) or bentonite (Fisher; Purified Grade). The adsorbents were added as dry powders to the extracts and the resulting suspensions were shaken for 15 minutes. The extracts were filtered and protein nitrogen determined by the Bio Rad* method. Kjeldahl nitrogen, nicotine and total sugars were determined for freeze dried samples of the extract. The results are given in Table III. The presence of pigment compounds in the extract was noticeably reduced when the amount of bentonite used was equivalent to 4%, or more, of the weight of the tobacco used to provide the extract.

Claims: A method for reducing the polypeptide content of an aqueous extract of tobacco comprising the steps of combining the extract with hydroxyapatite or a fuller's earth mineral as an insoluble adsorbent, and separating the extract from the adsorbent. A method according to Claim 1, wherein the adsorbent is attapulgite. A method according to Claim 1, wherein the adsorbent is hydroxyapatite. A method according to Claim 3, wherein the hydroxyapatite is suspended in the extract in an amount which is at least 16% of the weight of the tobacco used to provide the extract. A method according to Claim 1, wherein the adsorbent is bentonite. A method according to Claim 5, wherein the amount of bentonite is at least 1% of the weight of the tobacco used to provide the extract and the bentonite is suspended in the extract. A method according to Claim 6, wherein the amount of bentonite is at least 4% of the weight of the tobacco used to provide the extract. A method according to Claim 5, wherein the pH of the extract containing the bentonite is adjusted to about 3. A method according to any preceding claim, wherein the tobacco used to provide the extract is cured tobacco. A method for treating tobacco material which comprises the steps of: (a) extracting the tobacco material with an aqueous solvent; (b) separating the aqueous extract from the tobacco material; (c) treating said tobacco material with a surfactant; (d) removing the surfactant and extracted polypeptides from the tobacco material resulting from step (c); (e) subjecting the aqueous extract resulting from step (b) to the method described in any one of Claims 1 to 9; and (f) combining an aqueous extract resulting from step (e) with a tobacco material resulting from step (d). A method according to Claim 10, wherein a proteolytic enzyme is used and removed in addition to the surfactant in steps (c) and (d). A method according to Claim 11, wherein the extracted tobacco material is treated in steps (c) and (d) sequentially with with the proteolytic enzyme and the surfactant. A method according to any one of Claims 10 to 12, wherein the aqueous extract of step (e) is concentrated prior to step (f).

Inventors: BILIMORIA MINOO H, DE GRANDPRE YVES D, PORTER ANDREW R, BILIMORIA, MINOO, H., DE GRANDPRE, YVES D., PORTER, ANDREW R.
Applicants: IMP TOBACCO CANADA LTD, IMPERIAL TOBACCO CANADA LIMITED
Application year: 1992
Main classification: A24B15
IPC codes: A24B15