Method and apparatus for storing and transporting comminuted tobacco or the like

Abstract

Shredded tobacco is supplied from a storage reservoir to one or more cigarette making machines by way of discrete pneumatic conveying pipes. The reservoir receives fresh tobacco at regular or irregular intervals so that the quantity of tobacco in its interior is constant. The contents of the reservoir are maintained in suspension so that at least the major part of the supply of tobacco shreds forms a fluidized bed which is located directly below the intakes of the conveying pipes. When a machine requires a batch of tobacco shreds, the respective pipe is connected to a suction generating device so that it draws air from the region between the underside of the fluidized bed and the upper side of the bottom wall of the reservoir whereby the ascending current of air entrains tobacco particles directly from the fluidized bed. The supply of tobacco in the reservoir can be converted into a fluidized bed by mechanically agitating the reservoir so that the shreds move up and down and/or by causing a plurality of streamlets of compressed air to rise through perforations in the bottom wall of the reservoir. The latter may have a circular, semicircular or polygonal cross-sectional outline.

Description

BACKGROUND OF THE INVENTION

The present invention relates to a method and apparatus for storing and transporting fibrous material, and more particularly to a method and apparatus for storing and transporting comminuted tobacco. Still more particularly, the invention relates to storage of tobacco shreds and/or otherwise configurated tobacco particles, and to pneumatic transfer of metered or randomly selected quantities of such particles from the locus of storage to two or more consuming stations, e.g., to the hoppers of several discrete cigarette rod making machines.

It is already known to accumulate a supply of tobacco particles in a storage reservoir and to transfer particles of tobacco from the reservoir to one or more consuming machines by way of discrete pneumatic conveyors in the form of pipes. A drawback of presently known apparatus of the just outlined character is that the pipes are likely to be clogged by accumulations of interlaced tobacco shreds and also that the consistency of the supply of tobacco particles in the reservoir is not uniform. This presents problems in connection with metering of the quantities of tobacco particles which are to be delivered to selected consuming machines. Moreover, the quality of products which are turned out by several machines is not uniform.

OBJECTS AND SUMMARY OF THE INVENTION

An object of the invention is to provide a novel and improved method of delivering comminuted tobacco or like particulate material to two or more discrete consuming or processing machines, either seriatim, at random or simultaneously, especially for delivering tobacco shreds to discrete tobacco (e.g., cigarette) rod making machines.

Another object of the invention is to provide a method of the just outlined character which allows for controlled simultaneous delivery of comminuted fibrous material to a relatively small or a relatively large number of discrete consuming machines.

A further object of the invention is to provide a method which ensures adequate delivery of comminuted fibrous material to one or more consuming stations without undue damage to the conveyed material, especially without pronounced comminution of tobacco shreds.

An additional object of the invention is to provide a novel and improved apparatus for storage and delivery of comminuted fibrous material to one or more consuming machines, such as a battery of cigarette rod making machines which require batches of shredded tobacco at regular or irregular intervals.

Another object of the invention is to provide an apparatus of the just outlined character which treats the stored and transported material gently, which can rapidly transport large quantities of particulate material to one or more selected destinations, which can convey the material along paths of desired configuration so as to conform such paths to the space which is available between the storing area and the consuming machines, and which occupies a relatively small amount of space even though it can satisfy the requirements of a large number of consuming machines.

A further object of the invention is to provide an apparatus which is especially suited for storage and distribution of shredded tobacco in such a way that the shreds do not yield large quantities of short tobacco and/or tobacco dust.

One feature of the invention resides in the provision of a method of supplying fibrous material, especially comminuted tobacco (such as tobacco shreds) to several consuming machines (e.g., to a battery of cigarette rod making machines). The method comprises the steps of accumulating a supply of comminuted tobacco, converting at least the major part of the supply into a fluidized bed of floating tobacco, establishing discrete paths between the supply and the consuming machines, and pneumatically conveying comminuted tobacco directly from the fluidized bed to a selected consuming machine or to two or more selected consuming machines whenever the need arises.

The method may further comprise the step of admitting or feeding comminuted tobacco to the supply so as to maintain the quantity of comminuted tobacco in the fluidized bed at a substantially constant value. The conveying step may comprise transporting comminuted tobacco by suction.

At least some of the paths (such paths can be defined by pneumatic conveying pipes) can be tobacco receiving portions which extend substantially vertically from the fluidized bed, preferably vertically upwardly.

The converting step may comprise imparting to the tobacco of the supply a recurrent up-and-down movement, e.g., by mechanically agitating the ingredients of the supply.

Alternatively, the converting step may comprise subjecting comminuted tobacco of the supply to the lifting action of ascending currents of a gaseous fluid, preferably compressed air. The ascending currents of compressed air or another gas can be pulsated to achieve an even more satisfactory fluidizing action.

Still further, the converting step may comprise mechanically agitating the tobacco particles of the supply and simultaneously subjecting the particles to the lifting action of ascending currents of compressed air or another gaseous fluid.

The novel features which are considered as characteristic of the invention are set forth in particular in the appended claims. The improved apparatus itself, however, both as to its construction and its mode of operation, together with additional features and advantages thereof, will be best understood upon perusal of the following detailed description of certain specific embodiments with reference to the accompanying drawing.

BRIEF DESCRIPTION OF THE DRAWING

FIG. 1 is a partly elevational and partly longitudinal vertical sectional view of an apparatus which embodies one form of the invention and has a polygonal storage reservoir for comminuted tobacco;

FIG. 2 is a transverse vertical sectional view as seen in the direction of arrows from the line II--II of FIG. 1;

FIG. 3 is a schematic partly elevational and partly longitudinal vertical sectional view of a second apparatus wherein the particles in the interior of the reservoir are converted into a fluidized bed by several streamlets of a compressed gaseous fluid;

FIG. 4 is a schematic sectional view as seen in the direction of arrows from the line IV--IV of FIG. 3;

FIG. 5 is a schematic partly elevational and partly vertical sectional view of a third apparatus wherein the tobacco is converted into a fluidized bed by resorting to pneumatic as well as mechanical converting means;

FIG. 6 is a schematic plan view of a substantially semicylindrical storage reservoir as well as of a portion of means for feeding tobacco particles into and for drawing tobacco from the reservoir;

FIG. 7 is a schematic plan view of a substantially cylindrical storage reservoir with a feeding means which discharges comminuted tobacco into the central portion of the reservoir;

FIG. 8 is a sectional view as seen in the direction of arrows from the line VIII--VIII of FIG. 7;

FIG. 9 is a schematic partly elevational and partly vertical sectional view of an apparatus wherein the intake ends of conveying pipes which transport comminuted tobacco to discrete consuming machines are disposed in the central portion of the storage reservoir;

FIG. 10 is a schematic partly side elevational and partly vertical sectional view of an apparatus wherein the storage reservoir is agitated by a drive which constitutes a modification of the drive for the reservoir shown in FIGS. 1 and 2;

FIG. 11 is a schematic plan view of the structure which is shown in FIG. 10;

FIG. 12 is a schematic partly side elevational and partly longitudinal vertical sectional view of an apparatus wherein the mechanical drive for the reservoir constitutes a modification of the drive shown in FIGS. 10 and 11;

FIG. 13 is a schematic plan view of the structure which is shown in FIG. 12; and

FIG. 14 illustrates a modification of the apparatus which is illustrated in FIGS. 1 and 2.

DESCRIPTION OF THE PREFERRED EMBODIMENTS

The apparatus which is shown in FIGS. 1 and 2 serves to transport batches of comminuted tobacco, preferably tobacco shreds 9, to sixteen discrete consuming or processing machines, e.g., to cigarette rod making machines CRMM of the type known as GARANT manufactured by the assignee of the present application. Each cigarette rod making machine has a hopper H for a supply of tobacco shreds, and such hopper can receive a batch (preferably a metered quantity) of tobacco shreds by way of one of sixteen discrete pneumatic conveying pipes 3, one for each machine CRMM.

The apparatus comprises a magazine or storage reservoir 1 (e.g., a trough) which has a rectangular cross-sectional outline and receives tobacco shreds 9 from a larger source of supply (not shown) by way of one or more tobacco feeding devices. FIG. 1 shows a single feeding device including an endless belt or band conveyor 2 which is trained over pulleys 2a (only one shown) and whose discharge end serves to deliver tobacco shreds 9 into the right-hand end portion of the reservoir 1, as viewed in FIG. 1. The delivery of shreds 9 into the reservoir 1 preferably takes place intermittently, normally (but not necessarily) at irregular intervals, so as to ensure that the quantity of tobacco shreds 9 in the reservoir is at least substantially constant irrespective of whether the reservoir supplies tobacco shreds 9 to a sigle machine CRMM, simultaneously to two discrete machines, or simultaneously to three or more discrete machines. Also, the machines CRMM can receive tobacco shreds 9 in a given sequence or at random, depending on the quantity of tobacco shreds in the hoppers H of the respective machines. FIG. 1 shows a regulating valve RV is one of the pneumatic conveyor pipes 3; such valve is connected with a suitable monitoring device MD in the hopper H of the respective machine CRMM by conductor means CM so as to open the valve RV and to thus connect the discharge end 3a of the respective pipe 3 to a pressure reducing means in the form of a suction chamber SC whenever the upper surface or side of the supply of tobacco shreds 9 in the hopper H descends to a preselected lowermost permissible level. The aforedescribed components of the means for opening and closing the regulating valve RV are commercially available parts whose design forms no part of the present invention.

The upper side of the supply 6 of tobacco shreds 9 in the storage reservoir 1 is monitored by a detector in the form of a reflection type photocell 8 which is installed in or on a stationary carrier 4 at a level above the open upper side of the reservoir. The photocell 8 generates a signal when the supply of tobacco shreds 9 in the reservoir 1 is depleted to a predetermined extent whereby the signal initiates the starting of a motor M for the shaft 2b of the pulley 2a so that the conveyor 2 is set in motion and begins to replenish the supply 6. The carrier 4 further supports some of all of the sixteen pneumatic conveying pipes 3, preferably in such a way that each pipe can be readily detached therefrom and/or adjusted in the lengthwise direction thereof. FIGS. 1 and 2 show that the pipes 3 form two rows of eight pipes each and that these rows are adjacent to the left-hand end wall 1a of the reservoir 1, as viewed in FIG. 1, i.e., to that end wall which is remote from and is located opposite the discharge end of the conveyor 2. Each row of pipes 3 consists of four pairs of pipes, and each such pair of pipes is aligned with a pair of pipes of the other row so that the pipes 3 form four groups of four pipes each. The two rows of pipes 3 are parallel to each other and to the end walls 1a and 1b of the storage reservoir 1.

In accordance with a feature of the invention, the supply 6 of tobacco shreds 9 in the storage reservoir 1 constitutes a so-called fluidized bed (also called jet bed) consisting of floating particles which form a layer extending all the way from the end wall 1a to the end wall 1b and all the way between the two side walls 1c, 1d of the reservoir 1. Since the upper side of the supply of tobacco shreds 9 (i.e., the upper surface of the fluidized bed 6) is monitored by the photocell 8 which intermittently starts and arrests the conveyor 2, the upper side of the bed 6 is normally located at a practically fixed distance from the bottom wall or plate 1e of the reservoir 1. Such upper side (indicated at 6a) is closely adjacent to the open lower ends of the hollow frustoconical intakes or lower end portions 7 of the pipes 3. Each intake 7 tapers unwardly, i.e., in the direction of flow of tobacco shreds 9 from the interior of the reservoir 1 toward the respective machine CRMM. It will be noted that at least the lower parts of the pipes 3 (including the intakes 7) are vertical or nearly vertical so that the suction chamber SC which happens to communicate with a selected pipe 3 must draw the particles 9 from the bed 6 and in an upward direction (away from the bottom wall 1e of the reservoir 1).

The means for converting the supply of tobacco shreds 9 into the fluidized bed 6 comprises a mechanical drive 11 which agitates the storage reservoir 1 so that the shreds 9 are moved substantially up and down, i.e., they are propelled upwardly and away from the bottom wall 1e during certain stages of each recurrent movement of the storage reservoir. The drive 11 oscillates the reservoir 1 at a selected frequency. As will be described below, the drive 11 is designed to move the bottom wall 1e substantially up and down with attendant automatic conversion of tobacco shreds 9 in the interior of the reservoir 1 into a uniform fluidized bed 6 which overlies the entire bottom wall 1e and has a constant or at least nearly constant height.

The drive 11 of the converting means is constructed as follows:

The bottom wall 1e of the reservoir 1 is mounted on four discrete profiled holders which are disposed at or close to the four corners of the reservoir. FIGS. 1 and 2 show three of these holders (12a, 12b, in FIG. 2 and 13a in FIG. 1). The distance between the centers of the holders 12a, 13a is shown at B. The center of the holder 12b is disposed at the same distance from the fourth holder which is not shown in the drawing. Each holder is connected with a carrier for a discrete bearing. Two of these carriers are shown in FIGS. 1 and 2, as at 14a and 14b. Each carrier supports a rotary eccentric; the eccentrics which are mounted in the carriers 14a, 14b are respectively shown at 17a, 17b. The eccentrics 17a, 17b are mounted on a first shaft 19, and the other two eccentrics (which are not illustrated in FIGS. 1 and 2) are mounted on a shaft 21 which is parallel with the shaft 19. The axes of the shafts 19 and 21 are respectively shown at 22 and 23. Since the eccentrics are fixed to the respective shafts 19 and 21, they perform orbital movements along circular paths extending about the corresponding axes 22 and 23. Thus, when the shafts 19 and 21 are driven, the eccentrics (including those shown at 17a, 17b) move the receptacle 1 up and down via holders 12, 13 (see particularly FIG. 2) at four spaced locations which are respectively adjacent to the four corners of the bottom wall 1e.

The shafts 19 and 21 are journalled in suitable bearings which include two bearings 24a, 24b for the shaft 19 and two bearings (including the bearing 26a) for the shaft 21. These shafts respectively carry counterweights 27 and 28 in the form of eccentrically mounted discs or wheels serving to balance the forces which are generated in response to rotation of the aforediscussed eccentrics.

The means for driving the shaft 21 comprises coplanar gears or toothed pulleys 29, 31 which are respectively fixed to the shafts 19, 21 and a toothed belt 32 which is trained over the members 29, 31. The shaft 19 receives torque from a prime mover PM (e.g., a variable-speed electric motor) which drives a series of endless V-belts 34 trained over a pulley (not shown) on the output element of the prime mover PM and over a pulley 33 on the shaft 19. The parts 34, 33, 32, 31 and 29 synchronize the movements of the eccentrics 17a, 17b with the movements of the other two eccentrics so that the angular positions of the eccentrics on the shaft 21 are always identical with the angular positions of the eccentrics 17a, 17b on the shaft 19.

The operation of the drive 11 for the storage reservoir 1 is as follows:

When the prime mover PM is on, it rotates the shaft 19 via V-belts 34 and pulley 33, and the shaft 19 rotates the shaft 21 via toothed belt 32 and gears or pulleys 29, 31. The four eccentrics including the eccentrics 17a, 17b perform synchronous orbital movements about the respective axis 22, 23. Consequently, the eccentrics move the bottom wall 1e of the storage reservoir 1 up and down. More particularly, the path of the reservoir 1 is an endless circular path. Since the speed of the prime over PM is variable, the frequency at which the reservoir 1 is oscillated can be readily selected in such a way that the shreds 9 in the interior of the reservoir are accelerated and propelled vertically upwardly so that at least the major percentage of the shreds 9 invariably forms the aforediscussed fluidized bed 6. Thus, the major percentage of shreds 9 forms a layer of separate or practically separate tobacco particles which are spaced apart from the upper side of the bottom wall 1e. The exact RPM of the output element of the prime mover PM can be readily selected in such a way that it ensures the conversion of the entire or nearly entire supply of tobacco shreds 9 into a fluidized bed or layer. The just mentioned selected RPM depends on a number of parameters, some of which are characteristic of the design of the apparatus and some of which are characteristic of the nature of agitated material in the storage reservoir 1.

The arrow 36 (shown in the right-hand portion of FIG. 2) indicates the directions of up-and-down movement of the shreds 9 in the interior of the storage reservoir 1. Such movement of tobacco shreds 9 renders it possible to establish the upper side 6a of the bed 6 at a level immediately or closely below the open lower ends of the intakes 7. Whenever the regulating valve RV in a selected conveying pipe 3 is opened in response to a signal from the associated monitoring device MD in the hopper H of the selected machine CRMM, the intake 7 of such pipe 3 sucks loosened and uniformly distributed and thoroughly and uniformly intermixed shreds 9 directly from the bed 6. In other words, the selected intake 7 draws a current 37 of air by suction from the zone below the bed 6, i.e., from the space immediately above the upper side of the bottom wall 1e. Such current 37 entrains tobacco shreds 9 from the bed 6 and conveys them into the corresponding hopper H. It can be readily seen that, when the apparatus of FIGS. 1 and 2 is in use and a pipe 3 draws a stream of tobacco shreds 9 upwardly, the shreds 9 which form part of other portions of the bed 6 migrate toward the lower end of the activated pipe 3 so as to ensure that the uniformity of thickness of the bed 6 is restored practically instantaneously. The same holds true if two or more pipes 3 draw tobacco shreds 6 at one and the same time, or if the withdrawal of tobacco shreds 9 by way of a first pipe 3 coincides only in part with withdrawal of tobacco shreds by way of one or more additional pipes 3. The just discussed migration of tobacco shreds 9 toward the loci of withdrawal of shreds from the bed 6 insures through intermixing of tobacco shreds in the bed 6 so that the latter contains a uniform mixture of longest, medium long and shorter shreds. This is highly desirable because each of the sixteen cigarette rod making machines CRMM invariably receives the same type of mixture so that the quality of cigarettes which are produced in these machines is the same or does not vary from machine to machine on the ground that the hopper or hoppers H of one machine or a certain group of machines CRMM contain a mixture which is different from the mixture in the other hopper or hoppers.

The reflection type photocell 8 generates a signal to start the motor M for the shaft 2b of the pulley 2a whenever the upper side 6a of the fluidized bed 6 descends below a preselected level. This, too, contributes to uniformity of the mixture which forms the bed 6 and thus contributes to uniformity of the quality of final products. Tobacco shreds 9 which are delivered by the conveyor 2 are immediately caused to share the up-and-down movements of the previously supplied shreds 9 to thus ensure that at least the major percentage of the supply of shreds in the storage reservoir 1 forms part of the fluidized bed 6. When the upper side 6a of the bed 6 rises to the preselected level, the signal from the photocell 8 disappears or is modified so as to arrest the motor M.

The drive 11 of FIGS. 1 and 2 has been found to invariably convert the freshly admitted tobacco shreds 9 as well as the basic supply of such shreds in the interior of the storage reservoir 1 into a highly satisfactory fluidized bed which contains a uniform mixture of shreds and whose constituents can enter one or more selected conveying pipes 3 even if the speed of the current or currents of air in such pipe or pipes is relatively low. This is due to the fact that the aforedescribed eccentrics (including the eccentrics 17a and 17b) cause the shreds 9 in the storage reservoir 1 to move up and down. i.e., vibratory movements of the reservoir 1 are such that the particles therein are propelled upwardly and thereupon descend before being propelled again with attendant formation of a fluidized bed having a desired uniform thickness and consisting of uniformly distributed and intermixed particles. Such substantially vertical movements of the particles, with no stray movement or with negligible stray movement in other directions, can be readily achieved in response to driving the shafts 19 and 21 at a given RPM. It goes without saying that the storage reservoir 1 can be replaced with a magazine having a square or other polygonal cross-sectional outline.

The designer of the improved apparatus has substantial freedom of selecting the positions of intakes 7 with reference to the walls of the reservoir 1 as well as with reference to the locus of the discharge end of the conveyor 2. This is due to the fact that the thickness or height of the fluidized bed 6 is uniform or nearly uniform in all zones of the reservoir 1 as well as that the bed 6 consists of a homogenous mixture of tobacco shreds 9. Nevertheless, it is normally preferred to place the intakes 7 at a certain distance from the discharge end of the conveyor 2, e.g., to position these components in a manner as shown in FIGS. 1 and 2 so that the intakes 7 are adjacent to one end wall 1a and the discharge end of the conveyor 2 is adjacent to the other end wall 1b of the reservoir 1.

In the apparatus of FIGS. 1 and 2, the reservoir 1 is directly connected with the holders 12, 13 which, in turn, rest directly on the eccentrics including the eccentrics 17a, 17b. In other words, and since the parts 12, 13 can be said to constitute components of the reservoir 1, the latter is mounted directly on the eccentrics.

By way of example, the storage reservoir 1 of FIGS. 1 and 2 can have a length of 1400 mm and a width of 1000 mm. The minimum height of the apparatus can be approximately 800 mm and the diameters of the pipes 3 can be somewhere between 90 and 125 mm. The power requirements of such apparatus are approximately 0.75 kW per hour. The open ends of the intakes 7 of conveying pipes 3 can be located at a distance of approximately 95 mm above the bottom wall 1e.

The customary air locks which are provided at or close to the discharge ends 3a of the pipes 3 to segregate the entrained tobacco shreds 9 from the gaseous carrier medium are not shown in the drawing. The controls of the apparatus can be designed in such a way that, once a regulating valve RV is opened, it remains open for a fixed period of time which suffices to ensure that the respective hopper H receives a predetermined quantity of tobacco shreds 9. Alternatively, the duration of tobacco transport through a selected pipe 3 can depend solely on the quantity of tobacco in the respective hopper H, i.e., the transport is interrupted only when the hopper H is refilled to a preselected level.

In the apparatus of FIGS. 3 and 4, the means for converting the supply of tobacco shreds 109 in the storage reservoir 101 into a fluidized bed 106 comprises a unit 138 which causes a plurality of streamlets 143 of a gaseous fluid, preferably compressed air, to flow upwardly through the apertures of the foraminous sieve-like bottom wall 139 of the reservoir. The unit 138 includes a plenum chamber 141 below the foraminous bottom wall 139, conduit means 142 which admits a stream of compressed gas into the plenum chamber 141, and a pump, blower or another device 142a for admitting compressed fluid into the intake end of the conduit means 142. The streamlets 143 which rise through the apertures of the bottom wall 139 entrain the shreds 109 and convert the supply of shreds in the reservoir 101 into the aforementioned fluidized bed or layer 106.

The apparatus of FIGS. 3 and 4 further comprises means for pulsating the stream of air which flows through the conduit means 142 on its way into the plenum chamber 141. Such pulsating means comprises a reciprocable valve plate 146 which is movable into and from a position of overlap with the discharge end of the conduit means 142 by a crank unit 144 shown in FIG. 4. The just described pulsating means further enhances the ability of the streamlets 143 to convert the mass of tobacco shreds 109 in the storage reservoir 101 into a uniform fluidized bed 106 wherein the larger, medium-sized and smaller shreds are uniformly distributed and which regenerates itself in a fully automatic way by supplying shreds to the region or regions where the intakes (not specifically designated) of the conveying pipes 103 draw shreds from the reservoir. The manner in which the upper side of the bed 106 in the reservoir 101 is monitored and the manner in which the conveyor 102 is driven, when necessary, to ensure that the quantity of tobacco shreds 109 in the reservoir 101 remains substantially constant, is preferably the same as described in connection with FIGS. 1 and 2.

FIG. 5 illustrates a portion of a further apparatus wherein all such parts which are identical with or clearly analogous to corresponding parts of the apparatus of FIGS. 1 and 2 are denoted by similar reference characters plus 200. This apparatus combines the features of the apparatus of FIGS. 1-2 and 3-4, i.e., it comprises a drive 211 for mechanically agitating the storage reservoir 201 as well as a unit 238 which causes streamlets 243 of a compressed gaseous fluid to rise through the apertures of the foraminous sieve-like bottom wall 239 of the reservoir. The plenum chamber 241 is stationary and is adjacent to the underside of the bottom wall 239. Suitable sliding seals 241a are provided to prevent escape of any compressed gas (or to limit such escape) in the region where the bottom wall 239 moves relative to the housing of the chamber 241. The drive 211 may but need not be identical with the drive 11 of FIGS. 1 and 2. The same holds true for the units 138 and 238; for example, the unit 238 need not embody an equivalent of the reciprocable gate 146. The reference characters 202, 203, 206, 209 and 242 respectively denote the feeding conveyor, the pneumatic conveying pipes, the fluidized bed the shreds and the conduit means of the pulsating means.

FIG. 6 shows a portion of a modified storage reservoir 301 which has a substantially semicircular cross-sectional outline. The conveying pipes 303 are adjacent to the concave side of the concavo-convex side wall 301a of the reservoir 301, and the discharge end of the conveyor 302 feeds tobacco shreds into a portion of the reservoir which is adjacent to the straight side wall 302b. The neighboring pipes 303 are preferably equidistant from each other and all pipes 303 are preferably equidistant from the discharge end of the feeding conveyor 302.

In the apparatus of FIGS. 7 and 8, the storage reservoir 401 is an upright cylinder having a cylindrical peripheral wall 401a. The pipes 403 are adjacent to the inner side of the wall 401a and are equidistant from the discharge end of the conveyor 402 which feeds tobacco shreds into the central portion of the interior of the reservoir 401. The neighboring pipes 403, and more particularly the intakes of neighboring pipes 403, are preferably equidistant from each other.

As shown in FIG. 8, the bottom wall 439 of the reservoir 401 has a raised portion below the discharge end of the feeding conveyor 402 and this bottom wall slopes downwardly toward the lower end of the peripheral wall 401a. The slope or inclination of the outer part of the bottom wall 439 is preferably slight. A similar construction or design of the bottom wall is possible and often advisable in the embodiment of FIG. 6, i.e., the bottom wall 339 can have a raised portion below the discharge end of the conveyor 302 and a downwardly sloping part which extends from the raised portion toward the lower end of the hollow semicylindrical wall 301a.

The apparatus which is illustrated in FIG. 9 embodies certain features of the apparatus of FIGS. 1-2, 3-4, 5 and 7-8. The main difference between this apparatus and the previously illustrated and described apparatus is that the vertical intakes of conveying pipes 503 are disposed in the central portion of the cylindrical or substantially cylindrical storage reservoir 501. The reservoir 501 is agitated mechanically by a drive 511 and its contents are agitated pneumatically by a unit 538 which is identical with or analogous to the unit 138 or 238. The foraminous bottom wall 539 of the reservoir 501 allows streamlets 543 of compressed gaseous fluid (normally air) to rise into the lower part of the reservoir 501 and to thus assist the mechanical unit 511 in converting the entire or nearly entire contents (shreds 509 supplied by conveyor 502) of the reservoir into a fluidized bed 506. The supply of shreds 509 in the reservoir 501 is replenished, when necessary, by the conveyor 502 whose discharge end is adjacent to the cylindrical peripheral wall 501a of the reservoir. The arrows 537 denote the direction of flow of air and tobacco shreds 509 into selected pipes 503. As explained in connection with FIGS. 1 and 2, the currents of air flowing into one or more selected pipes 503 are drawn from the region between the bottom wall 539 and the underside of the floating fluidized bed or layer 506, and the intakes of the selected pipes 503 draw tobacco shreds 509 directly from the bed 506.

It is clear that, in each of the heretofore described embodiments, the number of tobacco conveying pipes can be reduced below sixteen or increased to seventeen or more. Also, each apparatus can have two or more feeding conveyors which can be operated simultaneously or one after the other. For example, the apparatus of FIG. 9 can be provided with two conveyors 502 which are located diametrically opposite each other.

FIGS. 10 and 11 show a modified oscillating or agitating drive 611 for a trough-shaped storage reservoir 611 which serves the same purpose as the aforedescribed reservoir 1, 101, 201, 301, 401 or 501. The reservoir 601 is mounted on a frame 647 which, in turn, is mounted on a stationary support or base 651 by means of parallel links 649. Similar or identical links 649 are used to mount a counterweight 648 on the base 651. In the illustrated embodiment, each link 649 has a first end portion which is articulately connected wih the oscillating frame 647 for the storage reservoir 601, a second end portion which is articulately connected with the counterweight 648, and a median portion which is articulately connected with the base 651. The connecting means for the central portions and end portions of the links 649 comprises elastic elements 652 which enable the frame 647 and the counterweight 648 to move relative to the base 651. The elements 652 may consist of rubber or other suitable elastomeric material. The means for imparting reciprocatory or oscillating movements to the counterweight 648 and frame 647 comprises a simple crank drive 653 which is mounted on the base 651 and whose output element is coupled to the counterweight 648.

FIGS. 12 and 13 illustrate a modification of the structure of FIGS. 10 and 11. The crank drive 653 of FIG. 10 is replaced with a twin crank drive 754 which forms part of the drive means 711 for the storage reservoir 701. The output element 754a of the drive 754 is articulately connected with the frame 747 for the reservoir 701, and the other output element 745b of the drive 754 is articulately connected with the counterweight 748. The median portion of the drive 754 is mounted on an upright column 751a of the support or base 751. The reference characters 756 denote links in the form of leaf springs which connect the frame 747 and the counterweight 748 with the support 751. These leaf springs replace or are used in addition to the elastic elements 652 of FIGS. 10 and 11.

The apparatus of FIG. 14 is similar to that of FIGS. 1 and 2. Therefore, the parts which are analogous to or identical with those shown in FIGS. 1 and 2 are denoted by similar reference characters plus 800. The direction in which the particles of tobacco advance through the reservoir 801 (i.e., from the feeding device 802 toward the pipes 803) under the action of the agitating means 811 is indicated by an arrow 825. The upstream and downstream ends of the reservoir 801 (as viewed in the direction of the arrow 825) are respectively adjacent to signal generating monitoring devices 810 and 815 in the form of photocells or analogous light-sensitive detectors. These detectors are respectively located ahead of and behind the pipes 803. If desired, the photocells 810 and 815 can be replaced by capacitive limit switches or the like. The monitoring devices 810 and 815 are directed toward discrete portions of the upper surface of the fluidized bed 806 in the reservoir 801 and are connected with a control means 820 of known design which, in turn, is connected with the prime mover PM for the variable-frequency agitating means 811. When the monitoring device 810 detects a rise in the level of tobacco particles in the respective portion of the fluidized bed 806 or a pileup of particles in the respective portion of the reservoir 801, it transmits a signal to the control means 820 which automatically increases the RPM of the prime mover PM and hence the frequency of the agitating means 811. However, if the monitoring device 815 detects a rise in the level of tobacco particles in the corresponding portion of the fluidized bed 806 or an accumulation of tobacco particles in the respective portion of the reservoir 801 (behind the pipes 803), it transmits a signal to the control means 820 in order to cause the latter to automatically reduce the RPM of the prime mover PM and to thus reduce the frequency of the agitating means 811. Thus, in each instance, the control means 820 cooperates with the monitoring device 810 or 815 to bring about an equalization of the upper level and hence a stabilization of the fluidized bed 806.

Control means which can be used in the apparatus of FIG. 14 to increase or reduce the RPM of a prime mover and hence the frequency of agitating means which is driven by the prime mover in response to signals which are generated by two discrete level monitoring devices is disclosed, for example, in U.S. Pat. No. 4,037,712 granted July 26, 1977 to Wochnowski.

An important advantage of the improved method and apparatus is that the major part of the supply of tobacco particles in the storage reservoir invariably floats above the bottom wall, i.e., that the major part of such supply constitutes a fluidized bed wherein the particles are uniformly mixed and do not tend to adhere to each other. On the contrary, the conversion of a stream which is delivered by the feeding conveyor (such as the conveyor 2 of FIG. 1) into a fluidized layer or bed invariably entails at least some loosening and disentangling of tobacco particles, especially if the particles are shreds. The uniform mixture of larger, smaller and medium-sized particles which form the fluidized bed can be readily entrained toward a selected consuming or processing machine even if the speed of the air stream in a conveying pipe is relatively low. As explained above, the intake of a selected conveying pipe draws air from the region below the fluidized bed and the ascending current of air first propels and thereupon automatically draws tobacco particles directly from the fluidized bed. The aforedescribed tendency of the fluidized bed to regenerate itself, i.e., to fill in the void or voids which develop therein as a result of entrainment of tobacco particles via one or more selected conveying pipes, is highly desirable and advantageous because it further reduces the likelihood of undue accumulation of and clumping or interlacing of tobacco shreds in certain regions of the storage reservoir. Moreover, there is no need to return surplus tobacco from the hopper or hoppers H of the consuming machine or machines; this is also desirable since the transport of tobacco shreds invariably results in the formation of so-called shorts and/or tobacco dust, i.e., of fragments whose dimensions are too small and, therefore, are not suited for the making of a satisfactory rod-like tobacco filler which is thereupon wrapped into cigarette paper or the like and severed to yield plain cigarettes, cigars or cigarillos of desired length.

Upward transport of tobacco shreds from the fluidized bed (i.e., such orientation of the lower portions of conveying pipes that the particles of tobacco travel vertically upwardly, at least in the region immediately above the upper side of the fluidized bed) has been found to be especially desirable and advantageous for several reasons. Thus, the intakes of several pipes can be placed close to each other and the rate of flow of compressed gas (air) into and through the pipes is quite satisfactory.

A further important advantage of the improved apparatus is its compactness and its ability to supply comminuted tobacco to a large number of consuming machines, either simultaneously or seriatim. Furthermore, and since the connections between the storage reservoir and the discrete consuming machines are extremely simple (each such connection merely comprises a pipe), the improved apparatus can be readily attached to or combined with any presently known consuming machines whereby such consuming machines may but need not be of the same vintage, type and/or size.

An additional advantage of the improved apparatus is its low maintenance cost. Clogging of various pipes and/or excessive drying of tobacco shreds in the reservoir can be avoided in a very efficient manner by the simple expedient of evacuating the contents of the storage reservoir before the apparatus is brought to a stop, i.e., the contents of the reservoir are preferably transferred into the hoppers H of the consuming machines CRMM before the apparatus and the consuming machines are brought to a halt.

Still another advantage of the improved apparatus is that its storage reservoir can receive comminuted tobacco from any conventional major source, e.g., directly from one or more shredding machines or directly from a rotary drum which conditions the shreds by uniformizing their moisture content prior to introduction into the reservoir. The belt conveyor or conveyors which are shown in the drawing can be replaced by or used simultaneously with pneumatic means for delivering tobacco shreds into the reservoir. Other means which can supply tobacco shreds to the reservoir include customary bulking chutes or conveyor means for drawing tobacco shreds directly from a silo.

Without further analysis, the foregoing will so fully reveal the gist of the present invention that others can, by applying current knowledge, readily adapt it for various applications without omitting features that, from the standpoint of prior art, fairly constitute essential characteristics of the generic and specific aspects of our contribution to the art and, therefore, such adaptations should and are intended to be comprehended within the meaning and range of equivalence of the appended claims.

Claims

1. A method of supplying tobacco or similar particulate material to several, consumers, especially for supplying shredded tobacco to a plurality of cigarette rod making machines, comprising the steps of accumulating a supply of particulate material; converting at least the major part of said supply into a fluidized bed of floating particulate material; establishing discrete paths between said supply and the consumers; pneumatically conveying particulate material directly from said fluidized bed to selected consumers whenever the need arises; and admitting particulate material to said supply so as to maintain the quantity of particulate material in the fluidized bed at a substantially constant value.

2. The method of claim 1, wherein said conveying step comprises transporting particulate material by suction.

3. The method of claim 1, wherein at least some of said paths have material receiving portions which extend substantially vertically from the fluidized bed.

4. The method of claim 3, wherein the material receiving portions of said paths extend upwardly from the fluidized bed.

5. The method of claim 1, wherein said converting step comprises imparting to the particulate material of said supply a recurrent up-and-down movement.

6. The method of claim 5, wherein said movement imparting step includes mechanically agitating the particulate material of said supply.

7. The method of claim 1, wherein said converting step includes subjecting the particulate material of said supply to the lifting action of ascending currents of a gaseous fluid.

8. The method of claim 7, wherein said fluid is compressed air.

9. The method of claim 7, further comprising the step of pulsating said ascending currents of gaseous fluid.

10. The method of claim 7, wherein said converting step further includes mechanically agitating the particulate material of said supply.

11. A method of supplying tobacco or similar particulate material to several consumers, especially for supplying shredded tobacco to a plurality of cigarette making machines, comprising the steps of accumulating a supply of particulate material; converting at least the major part of said supply into a fluidized bed of floating particulate material; establishing between said supply and the consumers a plurality of discrete paths each of which has an intake above the fluidized bed; automatically leveling the fluidized bed irrespective of distribution of the intakes of said paths, including imparting substantially vertical up-and-down movements to the particulate material of said supply; and pneumatically conveying particulate material directly from said fluidized bed to selected consumers whenever the need arises.

12. A method of supplying tobacco or similar particulate material to several consumers, especially for supplying shredded tobacco to a plurality of cigarette making machines, comprising the steps of accumulating a supply of particulate material; converting at least the major part of said supply into a fluidized bed of floating particulate material; establishing discrete paths between said supply and the consumers; pneumatically conveying particulate material directly from said fluidized bed to selected consumers whenever the need arises; monitoring the quantity of particulate material in said supply; and admitting particulate material to said supply when the monitored quantity is depleted to a predetermined value.

13. The method of claim 12, wherein said monitoring step includes monitoring the level of the upper surface of the fluidized bed.

14. The method of claim 12, wherein said converting step comprises mechanically oscillating the particulate material.

15. The method of claim 12, wherein said converting step includes confining said supply in a reservoir and agitating the reservoir at a variable frequency, and further comprising the step of equalizing the upper surface of the fluidized bed including monitoring the level of the upper surface in at least a portion of the reservoir and varying said frequency in response to changes in the level of the monitored upper surface.