Apparatus for use in the preparation of smokable products

Abstract

Smokable, substantially homogeneous, flake-like or leaf-like products of approximately equal thickness, and containing tobacco and/or tobacco substitutes, are disclosed, together with a process and apparatus for obtaining said products. The apparatus comprises a belt for transporting a wetted mixture of tobacco particles, means for distributing the wetted mixture to the belt, a second belt in close confronting relationship to the transport belt and movable in the same direction but at a different speed, the second belt being adapted to spread the mixture on the transport belt and form a layer, means downstream from the second belt and adapted to be in contact with the layer of wetted mixture for at least partially cutting the layer into irregularly shaped particles, means downstream of the cutting means for removing such particles from the transport belt, and means for drying and separating the irregularly shaped particles.

Description

This invention relates to apparatus for use in preparation of smokable, substantially hemogeneous flake-like or leaf-like products of approximately equal thickness and containing tobacco and/or tobacco substitute.

In a known process for producing the afore-cited smokeable products, coarsely comminuted tobacco materials, in particular ribs and wastes, are admixed with a small amount of liquid and kneaded. The resultant crumbly, moist mass is then subsequently pressed at a pressure in excess of 101 kg/cm.sup.2 to form flakes. These are tobacco structures of large surface area which must be recut subsequently to the sizes necessary to be added to cigar fillers or to cigarette tobacco. The flakes produced during this process are flat like paper and only a low filling capacity. The mechanical expenditure for achieving the high pressures and the consumption of energy required during pressing or rolling is high. Furthermore, the subsequent cutting operation is also disadvantageous because the knives are subject to a high amount of wear which necessitates frequent replacement of the knives.

Another process is known in which the starting products are ground very fine in size, in part even in colloidal size, and are admixed with large amounts of liquid. The thin slurry obtained according to this process known as the slurry process is then measured out in a thin layer on a drying belt and is dried to form a foil. Insofar as this foil is supposed to be used as a filler for cigars or cigarettes, it must be cut again subsequently hereto. Although no pressure is employed in this process, the consumption of energy is nevertheless very high because large amounts of liquid must be removed from the mass. In addition, the above-mentioned difficulties again arise when the foil is cut. Furthermore, this process produces a thin paper-like product with a low filling capacity.

Up to now the dried, band-like foils were generally cut longitudinally and transversely into large pieces at the end of the transport belt by cutting devices (Swiss patent 530,174, column 6, line 57). This cutting causes a relatively great amount of wear to the cutting knives, in particular in the case of artificial tobaccos which contain greater amounts of inorganic additives.

A suggestion has recently been revealed by U.S. Pat. No. 3,713,358 which intends avoiding the disadvantages of the afore-cited process. In so doing, special reference is made to the corrosion problems when cutting the finished foils into large pieces as is common nowadays. This suggestion proposes cutting the flexible foils at 8 - 12 % the moisture content subsequent to leaving an endless belt by means of a plurality of parallel knives and belt devices to form pieces in the shape of a parallelogram. The great amount of wear of the cutting knives and the resultant frequent sharpening of the same are not eliminated by this proposal. Furthermore, the pieces produced in this manner attract attention in an undesirable way due to the uniform regular geometrical shapes and the resultant unnatural appearance between the natural tobaccos. In addition, they have a paper-like shape, but do not have good filling capacity as is also the case in the afore-cited artificial structures.

The invention claimed in said patent application is directed to smokeable, substantially homogeneous flake-like or leaf-like products of approximately equal thickness and containing tobacco and/or tobacco substitute.

Said parent application also claims a process for producing smokable products of the afore-stated type, which permits flake-like or leaf-like tobacco products with a good filling capacity to be made with a low expenditure of energy and low cost of construction.

Thus smokable products of the afore-cited type are characterized by an irregularly wavy configuration, irregular dimensions with substantially non-rectilinear edges, by visible porous properties and by a high filling capacity when used as cigar and/or cigarette filler and by the same color on both sides.

In particular, the smokeable products of the afore-cited type are characterized in that they have an irregularly wavy configuration, irregular dimensions with substantially non-rectilinear edges and visible porous properties, a high filling capacity when used as cigar or cigarette filler as well as the same color on both sides and are obtainable by deforming a moist mass containing tobacco and/or tobacco substitutes between a rotating transport surface and a counterpart surface to form a flat structure, by pushing apart the flat structure located on the transport surface and not yet dried to its final moisture content and being in a plastic state into flake or leaf shape by means of an element provided with separating forms in a squeezing operation for separation purposes and by removing the structures from the transport surface immediately thereafter and drying them to their final moisture content.

The process for producing smokable, flake-like or leaf-like products containing tobacco and/or tobacco substitute, in which a tobacco and/or a moist mass containing tobacco and/or tobacco substitutes is deformed and dried between a rotating transport and counterpart surface to form a flat structure and is brought into flake or leaf shape, is characterized in that the flat structure located on the transport surface and not yet dried to its final moisture content and being in a plastic state is pushed apart by means of an element provided with separating forms during a squeezing operation to separate said structure in flake or leaf shape, is immediately removed thereafter from said transport surface and is dried to the final moisture content.

In such process, the flakes or leaves are produced in their area size on the transport surface. In doing so, the mass which has a moisture content higher than said final moisture content is deformed to the desired size by the separating forms. This is not a cutting operating in the conventional sense so that the squeeing ridges of the separating area may be relatively dull and are therefore only subject to negliigible wear. When the flakes or leaves, which are shaped in this way and are peeled off the transport surface while still in a moist state are dried, they deform and warp to form irregular three-dimensional structures with an extraordinarily large filling capacity. The inventive process may be carried out in a small device with a low expenditure of energy, for it is not necessary to compress the mass at high pressure to form a firmly coherent foil because it is separated to form flakes or leaves before it is removed from the transport surface.

It is expedient in many cases to pre-dry the flat structure on the tranport surface, preferably by about 5% calculated on the basis of the weight of the moist mass. This pre-drying facilitates removing the flakes or leaves from the transport surface to a considerable extent. Apparently a crusted surface which prevents the flakes or leaves from sticking together when they are scraped off the transport surface is formed during the drying operation on one side. This is the case when radiant heat is used for pre-drying.

Particularly good results are obtained if the drying of the flakes or leaves to their final moisture content takes place in a suspended state by means of a gas passing on all sides of the flakes or leaves. By drying the flakes or leaves in a suspended state, in which all surfaces are in contact with the drying gas, a very low amount of energy is consumed during drying. In addition it has been shown that the flakes or leaves deform to a particularly great extent to form three-dimensional structures when they are dried freely suspended and not in contact with a surface. In this respect drying in a suspended state also improves the filling capacity of the flakes or leaves which achieve their final shape and size during the drying operation.

The tendency of the leaves or flakes to undergo irregular special deformation may be improved by pushing them apart by means of separating forms of irregular contour, separating forms being preferably used which have serrated squeezing ridges.

In the known slurry processes it was necessary to wash the starting product with large amounts of water prior to production of the tabacco mass or to grind it again in a moist state after drying grinding. Only in this way has it been possible to impart sufficient bonding capacity to the mass. If the operation was carried out with a mass of relatively low moisture content, very high pressure of 101 kg/cm.sup.2 and more were employed to obtain sufficient coherence of the reconstituted tobacco foil. The initial washing operation means a great expenditure of washing liquid whose elimination is problematical in a dirty state. High pressures and much liquid in the mass produce a high expenditure of energy during the production of pressure or when drying the mass.

According to the invention claimed in said parent application there is provided a process for producing reconstituted tobacco-containing structures, in which the result is achieved without costly washing or rinsing operations and with a low consumption of energy. This is accomplished in that the mass is admixed with a wetting agent prior to being deposited on the transport surface.

A surprising result has been that by using a wetting agent the starting products may be produced without thorough washing and coherent structures may be produced without the application of high pressure from the mass which contains only coarsely ground tobacco particles and which has been admixed with slight amounts of liquid. Apparently, the wetting agent increases the bonding capacity of the tobacco particles to such an extensive degree that a sufficiently coherent layer can be produced on the transport surface without washing as well as at a low pressure and with little liquid and flakes or leaves may be produced with a resistance of tearing which is sufficient for all practical purposes. The use of a wetting agent is also advantageous if the reconstituted tobacco structure is produced according to any other arbitrary process, for example the slurry process.

The wetting agents predominantly include special wetting agents such as higher alcohols, sulfonated alcohols, sulfonated ether, lauryl sulfate, silicon, polyglycol ester and polyglycol ether or natural wetting agents such as saponins. Such special wetting agents only need to be added in slight amounts to the mass, for example approx. 0.1 - 2% calculated on the basis of the dry mass.

An adequate effect is also achieved however if the substances which are normally mixed with the tobacco as moisture retention agents are used as the wetting agent. In this case, however, it is necessary to increase the amount of the admixed agents to at least approximately one and a half times the amount common in the case of moisture retention agents. Wetting agents within this meaning can be considered to be sorbitol, diethylene glycol and glycerin as well as other conventional moisture retention agents. They are used in an amount of approx. 6 to 10% based on the dry mass.

If conventional moisture retention agents are employed as wetting agents such that they are admixed with the comminuted tobacco together with the liquid instead of with the finished product, a sufficient wetting effect with correspondingly good bonding capacity and low processing pressure is attained even if the amounts which are common in the case of moisture retention agents are not exceeded.

Admixing the wetting agent at the beginning of the process is also advantageous when special wetting agents are used because the bonding capacity is increased and the processing pressure is decreased.

In addition, mixtures of the afore-mentioned wetting agents may be used in the inventive process.

The following are examples for the process:

EXAMPLE 1:

75 g of tobacco parts which are comminuted down to a grain size of 200 .mu. and consisting of 35 g of Burley ribs and 30 g of tobacco dust are mixed well with 70 ml of water, 0.2 ml of saponin, 5 ml of diethylene glycol, 1 ml of glyoxal and 7 g of carboxymethyl cellulose. To this moist mass are subsequently added 5 g of Mg-Al-silicate, 2 g of citric acid, 1 g of TiO.sub.2 and 4 g of dextrin. This mass is deformed between two belts to form a coherent foil of about 0.1 mm thickness and is comminuted at a moisture content of 40% by means of deformation rollers to form pieces similar to tobacco leaves, is scraped off the plastic belt and is dried in a suspended state to about 15% moisture content.

EXAMPLE 2:

70 g of comminuted tobacco components, 10 g of one or more vegetable substances, e.g. sawdust, rye, wheat or maize husks are mixed well with 80 ml of water, 7 ml of diethylene glycol, 1 ml of glyoxal and 6 g of carboxymethyl cellulose. 2 g of citric acid, 1 g of TiO.sub.2 and 3 g of silicic acid are admixed to this moist mass and the process is continued as stated in Example 1.

EXAMPLE 3:

75 g of comminuted tobacco parts (grain size to approx. 150 .mu.m) consisting of 30 g of air-cured Rio Grande ribs, 30 g of coal slack below 6 mm contained in loaded lumps and 15 g of tobacco dust are mixed well with 80 ml of water, 5 ml of diethylene glycol, 2 g of potassium silicate at pH 8 and 6 g of methyl cellulose. 3 g of magnesium-aluminum silicate and 3 g of starch are subsequently admixed to this moist mass. Further processing takes place as in Example 1.

In accordance with the present invention, there is provided an apparatus for carrying out the process, which apparatus is characterized by a transport belt, an application and dosing means for uniformly applying the mass on the transport belt, a counterpart belt which runs in the same direction but slower than the transport belt and serves to spread the mass on said transport belt, a shreddi460000000000000000000000000000000000000000000000000000000000000000

Priority Claims (1)

Number	Date	Country	Kind
2363640	Dec 1973	DT

CROSS REFERENCE TO RELATED APPLICATION

This application is a division of my parent application Ser. No. 533,779, filed Dec. 18, 1974, now U.S. Pat. No. 3,986,515.

US Referenced Citations (2)

Number	Name	Date	Kind
3628541	Buchmann et al.	Dec 1971
3894544	Egri et al.	Jul 1975

Divisions (1)

	Number	Date	Country
Parent	533779	Dec 1974