[ 0057 ] fig1 shows an expansion device , broadly indicated by the reference numeral 10 , comprising a device for pre - conditioning comminuted tobacco material and an airflow dryer connected thereto , which is arranged beneath the pre - conditioning device 12 . cut tobacco particles ( lamina ) are fed into the substantially vertically arranged pre - conditioning device 12 via suitable conveyors , for example oscillating conveyor channels , and fed into the pressure proof chamber 3 of the device 12 via an upper , pressure differential proof , cellular wheel sluice 1 , the tobacco particles free - falling in said chamber . vertically , the chamber 3 expands conically downwardly in order to rule out a banking or jamming of tobacco particles . about half way down the chamber 3 , ring nozzles 2 ( see also fig2 ) are arranged flush with the inner surface area of the chamber 3 , in order to rule out catching edges which could impede the passing of the tobacco . in the embodiment shown , the discharge direction of the ring nozzles 2 is inclined downwards , to assist the conveying / flight movement of the tobacco . the discharge direction of the ring nozzles 2 may in principle , however , be directed horizontal or even upwards , against the flow of tobacco . the tobacco particles free - fall downwards in the tapered chamber 3 , and are introduced directly into the horizontal section of an airflow dryer 5 via a lower , similarly pressure differential proof , cellular wheel sluice 4 . as an alternative to the embodiment shown , a vertical flow drying section may also be used . in order to avoid build - up or jamming of tobacco in the chamber 3 , the lower cellular wheel sluice 4 , serving as a discharge sluice , is run at a slightly higher conveying volume than the upper feed sluice 1 ; this may be achieved , for example , via the speed of the sluices and / or a greater volume of the individual sluice chambers , as is evident from fig1 . as may be recognized in fig2 vapor is introduced into a ring chamber in the wall of the chamber 3 , from which the ring nozzles 2 , which are radially directed downwards into the interior of the chamber , are fed . even before tobacco particles begin to be fed to the chamber , the interior of the chamber 3 is placed under an absolutely measured pressure , by feeding saturated vapor in through the ring nozzles 2 . in this way , a pressure is built up in the interior of the chamber 3 which is dependent only on the temperature of the saturated vapor being fed in . due to the two pressure differential proof , cellular wheel sluices 1 , 4 , this pressure is maintain - ed during continuous running operation , such that extremely high dryer entry temperatures and moistness of the tobacco may be achieved , as compared with conventional methods . to avoid water vapor condensing on the inside wall of the chamber 3 , the chamber , formed as a pressure container , is provided with a heating jacket 6 , as may be recognized in fig3 and 4 . vapor of a slightly higher temperature than the temperature of the vapor sprayed in via the ring nozzles 2 is fed into the bottom of the heating jacket , and drawn off , out of the heating jacket , at the top . once it has passed through the pre - conditioning under superatomospheric pressure and thus at extremely high temperatures , the pre - heated and moistened tobacco particles fall downwards through the lower cellular wheel sluice 4 into the airflow dryer 5 , where they are swept along by the hot gas stream , and dried to the desired discharge or output moistness by the resting time in the dryer . the drying of the tobacco is characterized in the first stage by the quick vaporization , up until the cooling limit temperature is reached ; in this way , the vaporization energy is exclusively provided by the tobacco particles themselves . in the second section , the tobacco is dried by convectional exchange of material and heat . [ 0071 ] fig5 shows a diagrammatic representation of the conditioning of tobacco particles , which are introduced into a saturated vapor atmosphere in the pressurized chamber 3 at thermal equilibrium and with an entry temperature of 20 ° c . in this respect , the line marked by triangles indicates the change in moisture content of the tobacco particles having an entry moistness of 20 %, and the line marked by squares indicates the change in moisture content of the tobacco particles having an entry moistness of 18 %. as can be seen , the moisture content of tobacco particles after conditioning , expressed as a percentage , rises linearly in the range of saturated vapor temperature from 100 ° c . to 160 ° c ., such that at a saturated vapor temperature of 160 ° c ., for example , tobacco particles with an entry moistness of 18 % leave the pre - conditioning device with a discharge moistness of about 30 . 25 %. the achievable increase in filling capacity will now be explained by means of an example which compares pressurized pre - conditioning using the device according to fig3 for increasing tobacco temperature and moistness and subsequent airflow drying with pre - conditioning using water and vapor at normal air pressure . cut tobacco with a cut moistness after cutting of 18 % was accordingly conveyed cold through a conditioning drum ( without being conditioned ) at a tobacco mass flow rate of 200 kg / h , relative to the cut moistness of 18 %, and then driven at a vapor pressure of 5 bars through the device according to fig3 which had been pre - heated using superheated vapor at 5 bars (& gt ; 152 ° c .). in order to prevent moist cavities from forming , care must be taken that as little condensation as possible gets into the interior volume of the chamber 3 . the tobacco falling down the chamber 3 is brought up to the equilibrium temperature , which lies at about 152 ° c ., by the absorption of condensing vapor . this results in moisture absorption of about 27 % by mass . the falling time for covering a distance of about lm is only about 0 . 5 s . the tobacco thus conditioned , i . e . heated and moistened , is dried in the airflow dryer 5 to a discharge moistness of about 13 % by mass . by way of comparison with this method course in accordance with the invention , cut tobacco containing 18 % moisture was moistened to 27 % in a conventional conditioning drum and at normal ambient pressure using vapor and water , pre - heated to about 60 ° c ., and then conveyed at a rate of 200 kg / h through the device according to fig3 — without further conditioning — into the airflow dryer 5 . if the filling capacities of the tobacco from the two experiments are compared with each other at the outlet of the airflow dryer 5 , the pressure - conditioned tobacco shows an increase in filling capacity of 5 . 9 %, as compared with the comparative sample having passed through corresponding conditioning at ambient pressure in the conditioning drum . the results for filling capacity were corrected to 12 % by mass , in order to provide an exact comparability . corresponding experiments were carried out in the device according to fig3 at differing vapor pressures . the results obtained , expressed as percentage increases in filling capacity , are assembled in the following table , together with the accompanying process parameters . as a comparative sample for the given pressure conditioning as described above , 18 % moist cut tobacco and the corresponding tobacco moistness were conditioned to a tobacco temperature of 60 ° c . in a conditioning drum at ambient pressure using vapor and water , in order to ascertain the increase in filling capacity . pressure moistness equilibrium increase in in device ex device temperature filling capacity [ bar ] [% by mass ] [° c .] [%] 2 24 . 1 120 3 . 1 3 24 . 9 134 3 . 9 4 26 . 2 144 4 . 5 5 26 . 5 152 5 . 9 6 27 . 0 159 6 . 6 7 27 . 4 165 7 . 1 as can be seen , the equilibrium temperature increases as expected with the pressure in the chamber , and in turn results in a corresponding proportional increase in filling capacity . this series of experiments can , according to the quality of the cellular wheel sluices with respect to pressure and temperature , be continued in the direction of increasing pressures / temperatures . correspondingly higher equilibrium temperatures and increases in filling capacity are then to be expected . in the foregoing description preferred embodiments of the invention have been presented for the purpose of illustration and description . they are not intended to be exhaustive or to limit the invention to the precise form disclosed . obvious modifications or variations are possible in light of the above teachings . the embodiments were chosen and described to provide the best illustration of the principals of the invention and its practical application , and to enable one of ordinary skill in the art to utilize the invention in various embodiments and with various modifications as are suited to the particular use contemplated . all such modifications and variations are within the scope of the invention as determined by the appended claims when interpreted in accordance with the breadth they are fairly , legally , and equitably entitled .
the invention relates to a method for conditioning comminuted tobacco material by heating and moistening with water vapor , wherein the comminuted tobacco material free - falls down through a chamber operating in a continuous process and is treated during free - fall with water vapor via nozzles ; a hyperbaric pressure is maintained in said chamber .