Abstract:
A production method and system for granulating powdered material wherein powdered material is fluidized by applying heated pulsating vibration air, and the fluidized powdered material is suspended up and down at a regular cycle by means of heated pulsating vibration air, the aggregated material is compressed by further vibration of pulsating vibration air, whereby the aggregated powdered material is efficiently made into granulated material with high density and rather small specific volume without causing projection on the surface and without being made porous. The production system is comprised of a granulation tank for storing powdered material to be granulated, the granulation tank having a supply port for introducing heated air at the bottom thereof, a discharge port for discharging the introduced heated air at the top thereof, and a fluidization bed provided above the supply port for receiving the powdered material. A spray apparatus for spraying a binder solution provided in the granulation tank for aggregating the powdered material stored in the granulation tank for growing the material is provided. An air source connected to the supply port of the granulation tank via a conduit pipe; heating apparatus interposed in the conduit pipe for heating the air generated from the air source; and a pulsating vibration air generation means interposed in the conduit pipe for converting the air generated from the air source to pulsating vibration air.

Description:
BACKGROUND OF THE INVENTION 
     I. Field of the Invention 
     The present invention relates to a production method and system for granulating powdered material, and more particularly relates to a production method and system for efficiently granulating powdered material with uniform property and small specific volume using pulsating vibration air. 
     II. Prior Art 
     FIG. 12 shows a known fluidized layer granulation system. 
     The granulation system  101  is comprised of a granulation tank  102 , an air source  103 , such as a blower fan, a discharge fan  104 , heating means  105 , such as a heat exchanger, and spray means  106  such as a nozzle means, for spraying a binding solution. 
     A supply port  102   a  for introducing heated air is provided under the granulation tank  102 , the air source  103  is connected to the supply port  102   a  via a conduit pipe and the heating means  105  is provided between the supply port  102   a  and the air source  103 . When the air source  103  is driven to cause the heating means  105  also to drive, the air produced by the air source  103  is heated by the heating means  105 , the heated air is supplied into the granulation tank  102  from the supply port  102   a,  and the supplied air is blown up in the granulation tank. 
     A fluidization bed  107  is provided above the supply port  102   a  in the granulation tank  102 . Powdered material A stored in the granulation tank  102  is deposited on the fluidization bed  107  when air isn&#39;t supplied to the granulation tank  102 . 
     Whereas heated air is supplied from the supply port  102   a,  the powdered material A deposited on the fluidization bed  107  floats to be mixed with the air blown upward from the fluidization bed  107  and forms a fluidized layer following the increase of the wind speed of the supplied air. 
     Further, a discharge port  102   b  is provided on the top of the granulation tank  102  and the discharge fan  104  is connected to the port  102   b  via a conduit pipe. The air supplied to the granulation tank  102  is discharged to the outside by driving the fan  104 . 
     On the other hand, the spray means  106  for spraying a binding solution is provided in the granulation tank  102  and connected with an air source  108  storing pressurized air via an air supply pipe  109 , and further a tank  110  for storing a binding solution is connected via a binding solution supply pipe  111 . A control unit  112  for adjusting the spraying amount of the spray means  106  is interposed in the middle of the pipe  111 . 
     In FIG. 12, the numeral  113  relates to a bag filter for preventing the raw powdered material A, the granulating material or the granulated material from flowing out of the granulation tank  102  and the numeral  114  relates to a dust collecting filter for eliminating dust in the air supplied to the granulation tank  102 . 
     In order to granulate material utilizing the system  101 , the raw material A is stored in the granulation tank  102 . Heated air is supplied into the tank  102  by driving the air source  103  and the heating means  105  and simultaneously the discharge fan  104  is driven, whereby the raw material A placed on the fluidization bed  107  is caused to be blown up. The heated air with constant flow amount and constant pressure is always supplied into the tank  102  by controlling the driving force of the air source  103  and the discharge fan  104  so that a desired stable fluidized layer is formed in the tank  102 . Thereafter, air with a fixed pressure is supplied to the spray means  106  for spraying a binding solution from the air source  108  and simultaneously the control unit  112  is driven. A binding solution B is sprayed from a desired spray and makes a bridge of solution between particles of the raw material A. The particles of the raw material A suspended in the granulation tank  102  as a fluidized layer mixed with air are aggregated and the aggregated particles are dried to be grown as a granulated material. 
     In the prior granulation method mentioned above, the granulated material with uniform physical properties (particle diameter, particle shape, etc) can be produced when material is granulated by spraying a binding solution from the nozzle after a dilute fluidized layer is formed by supplying a large amount of heated air with constant pressure and constant amount into the granulation tank  102 . 
     It is known that an increased speed of the particles becomes fast when particles are granulated by spraying a binding solution from the nozzle after a high density fluidized layer is formed by reducing the amount of heated air supplied into the granulation tank  102 . 
     However, when material is granulated by means of the system  101 , the granulated material becomes porous and its specific volume increases and becomes large because it is made from the particles floating in the air. In order to solve this problem, a new granulation method has been proposed in JP-A-60-183030. 
     FIG. 13 is a partially cutaway sectional view of the system disclosed in JP-A-60-183030. 
     A granulation system  201  is further provided with a rotary vane  202   a  on the fluidization bed  107  and a driving motor  202  to rotate the rotary vane  202   a  below the bed  107 . Heated air is supplied into the granulation tank  102  and the motor  202  is driven to rotate the vane  202   a  when the material A stored in the tank  102  is granulated. The material A directly receives rotating power of the vane  202   a  so that the material is prevented due to agitation from becoming porous. 
     According to the system  101  shown in FIG. 12, granulated material with a constant properties (particle diameter, particle shape, etc) is produced when material is granulated in a dilute fluidized layer by supplying a large amount of heated air into the granulation tank  102 . However, in the prior art, the concentration of the material A in a fluidized layer is dense and the particles of the material A do not doesn&#39;t have sufficient opportunity to touch each other so that particle growth becomes slow affecting the productivity of granulation. 
     Further, when a high density fluidized layer is formed in the granulation tank  102  by reducing the amount of the heated air supplied to the granulation tank  102 , each particle of the material A comes collides frequently, so that the particle growth of particle becomes fast. However, the particle diameter of the granulated material doesn&#39;t become uniform or projected parts like an antenna of a snail are formed on the surface of the particles so that granulated material with an irregular shape (not spherical) and different diameter is produced. Therefore, the system  101  can&#39;t be used when spherical granulated material is required. Furthermore, as mentioned above, the granulated material tends to be porous because the granulation is executed in air. As the result, it is difficult to produce granulated material with small specific volume. 
     When heated air is supplied at a uniform rate into the granulation tank  102 , the air may blow through a part of the material A placed on the fluidization bed  107 . In this case some of the material A in the tank  102  remains still and isn&#39;t fluidized. Granulated material isn&#39;t made from such a material, therefore, and the amount of granulated material becomes less compared to the amount of raw material A. 
     Slacking, bubbling or chanelling of the material A, which stop fluidization, may be caused in the granulation tank  102  while the material is granulated. The particle diameter, particle shape, density, and hardness of the granulated material depend on the fluidized condition of the raw material A and the granulating material. 
     Further in the prior art, unintended fine particles may be included in the granulated material. It is desired to reduce the amount of such fine particles. When the system  201  shown in FIG. 13 is used, the granulated material is prevented from being porous because the rotary agitation flow by means of the rotation of the vane  202   a.  However, it is required to provide the rotary vane  202   a  on the fluidization bed  107  and the driving motor  202  below the bed  107  for rotating the vane  202   a,  whereby the number of the parts becomes large and the system is complicated. Foreign material may be produced from the increased parts and the complication makes the cleaning of the system difficult. Such foreign material remaining in the system may be included in the granulated material and increases the risk of contamination. Therefore, such a system isn&#39;t appropriate for producing granulated material for fine chemical use such as medicine wherein a high quality granulation without contamination of foreign material is required. 
     SUMMARY OF THE INVENTION 
     The present invention is proposed to solve the above-mentioned problems. An object of the present invention is to provide a granulation method and system wherein granulated material with uniform shape, uniform diameter and uniform property and small specific volume can be easily and efficiently produced. 
     According to the granulation method of the present invention, powdered material stored in a granulation tank is produced into a granulated material with high density and small specific volume as follows. 
     The powdered material is fluidized by applying heated pulsating vibration air and is aggregated by spraying a binding solution. Therefore, the aggregated powdered material drops and is deposited on a fluidization bed by gravity accompanied by the growth of the particles while they are suspended up and down in the granulation tank according to the frequency of the pulsating vibration air. And thereafter the deposited powdered material under granulation is produced into a granulated material with high density and small specific volume while receiving compression to be high density by means of the heated pulsating vibration air. 
     According to such a production method, the deposited material under granulation is compressed to a high density by means of the vibration of the pulsating vibration air. Therefore, the projections like an antenna of a snail formed on the surface of the particles of the granulating material are peeled off and each particle of the granulating material deposited on the fluidized bed is compressed together. In the present invention, the produce of the granulated material with the projections or porous property is prevented and granulated material with uniform properties, high density and small specific volume is produced efficiently without difficulty comparing to the prior art wherein powdered material is fluidized by means of constant heated air mixed in the heated air, and a binding solution is sprayed to aggregate the material, and then the material is dried to grow as granulated material. 
     Four types of pulsating vibration air can be used in the present invention, that is, pulsating vibration air with peaks and valleys of negative pressure, air with peaks of atmospheric pressure and valleys of negative pressure, air with peaks of positive pressure and valleys of atmospheric pressure, and air with peaks and valleys of positive pressure. According to experimental findings, the granulated material with small specific volume and good quality can be obtained when pulsating vibration air with peaks and valleys of positive pressure is used. 
     It is preferable to use the pulsating vibration air with peaks and valleys of positive pressure. 
     In the specification “positive pressure” means a condition that the pressure in the granulation tank is higher than the outside pressure (atmospheric pressure). “Negative pressers” means a condition that the pressure in the granulation tank is lower than the outside pressure (atmospheric pressure). 
     As the result of the actual production using different kinds of powdered material, the amplitude, frequency and wave shape of pulsating vibration air are desirable to be changed according to the property of the powdered material (such as viscosity, diameter, specific gravity, adhesiveness, and miscibility with air of the particles of the material) in order to produce granulated material with uniform properties and small specific volume. 
     At least either amplitude, frequency and wave shape of pulsating vibration air is changed according to the property of the material. 
     According to experimental findings, granulated material with small specific volume, that is heavy material, can be obtained when the frequency of the pulsating vibration air is not less than 1 Hz but less than 10 Hz, desirably from 1 Hz to 9 Hz, more desirably from 1 Hz to 6 Hz, still more desirably 5 Hz as the result of production with the pulsating vibration air with different frequency. 
     Therefore, its preferable to set the frequency of pulsating vibration air to not less than 1 Hz but less than 10 Hz in the production method of the present invention. 
     A granulation system, with air suction means provided for an air discharge port attached at the top of a granulation tank, with an air supply means provided for an air supply port at the bottom of a granulation tank, with both the air suction means and the air supply means may be considered. As a result of the production with these different granulation systems and a pulsating air generation means, when the pulsating vibration means is provided before the air supply port at the bottom of the granulation tank and pulsating vibration air is supplied under a fluidization bed and directed upwardly, it is easy to fluidize the raw material and suspend a part of the material up and down. Further, compression by means of the vibration of the pulsating vibration air is efficiently applied on the granulation and growing material which has been dropped and deposited on the fluidization layer and the material becomes dense, whereby granulated material with specific volume is produced. 
     The granulation system of the present invention is provided with a granulation tank for storing powdered material to be granulated. The granulation tank has a supply port for introducing heated air at the bottom thereof, a discharge port for discharging the introduced heated air at the top thereof, and a fluidization bed provided above the supply port for placing the powdered material temporarily. The granulation tank is also provided with spray means for spraying a binding solution to grow the powdered material to be granulated. The system is also provided with an air source connected to the supply port of the granulation tank via a conduit pipe, heating means interposed in the conduit pipe for heating the air generated from the air source, and a pulsating vibration air generation means interposed in the conduit pipe for converting the air generated from the air source to pulsating vibration air. 
     A pulsating vibration air generation means may be provided with an on-off valve for closing and opening a conduit pipe connecting the air source and the granulation tank so that pulsating vibration air is generated by operating the valve, may generate pulsating vibration air by vibrating a plate by means of the air supplied from an air source, or may be provided with an air suction means at an air discharge port at the top of a granulation tank and an on-off valve for opening and closing a conduit pipe connecting the air discharge port and the air suction means and pulsating vibration air is generated by operating the valve. According to the productive results using the above-mentioned different pulsating vibration air generation means, a rotary type pulsating vibration air generation means is desirable in order to produce granulated material with small specific volume, and more preferably, the rotary type pulsating vibration air generation means is preferably provided between the conduit pipe connecting the air source and the granulation tank. 
     The pulsating vibration air generation means as mentioned above may be provided with a casing having a pair of connecting ports at the surrounding wall thereof and a rotary valve having a rotational axis in the center of the casing. The valve is constructed so as to divide the inside of the casing into at least two spaces. One of the pair of connecting ports is connected with the heated air supply port and the other port is connected with the air source. 
     Some materials to be granulated are easy to be mixed with air and the others are not. Therefore, it may be preferable to change the wave shape of the pulsating vibration air in order to fluidize the material stored in the granulation tank and make some of the aggregated material suspend up and down according to the frequency of the pulsating vibration air. 
     According to the granulation system of the present invention, the above-mentioned pulsating vibration air generation means is provided with a valve for opening and closing the conduit pipe connecting the air source and the heated air supply port, and a valve cam mechanism having guide rails with a specific circular pattern defining the duration and amount of open and close of the valve. The valve is opened or closed vertically in compliance with the irregular pattern of the guide rails by driving the valve cam mechanism. 
    
    
     BRIEF DESCRIPTION OF THE DRAWINGS 
     FIG. 1 shows a granulation system of the present invention diagrammatically. 
     FIG. 2 is a diagrammatic sectional view of a pulsating vibration air generation means. 
     FIGS.  3 ( a ) and  3 ( b ) shows examples of pulsating vibration air applied in the present invention. 
     FIG. 4 shows a phenomenon of the inside of the granulation tank according to the present invention. In FIG.  4 ( a ) pulsating vibration air is at its peak and in FIG.  4 ( b ) pulsating vibration air is at its valley. 
     FIG. 5 is a graph showing the result of the experiment wherein the amount of air required for granulating the material of the same specific volume is compared in the present invention and the prior art. 
     FIG. 6 is a graph showing the correlation of the amount of air used for granulation and the breaking load of the granulated material. 
     FIG. 7 shows a graph compared particle size distribution of the granulated material produced by the prior art and the granulated material produced by the present invention. 
     FIG. 8 is a graph showing the correlation of the frequency of the pulsating vibration air used for granulation and the rough specific volume of the granulated material. 
     FIG. 9 is a graph showing the correlation of the frequency of the pulsating vibration air used for granulation and the particle size distribution of the granulated material. 
     FIG. 10 shows a pulsating vibration air generation means. FIG.  10 ( a ) shows a sectional side view and FIG.  10 ( b ) shows a sectional view along with X—X line in FIG.  10 ( a ). 
     FIG. 11 shows a diagrammatic view of a modification of a granulation system according to the present invention. In FIG.  11 ( a ) a vibrator is provided for a bag filter and in FIG.  11 ( b ) a cyclone is provided instead of a bag filter. 
     FIG. 12 is a diagrammatic view of the granulation system in the prior art. 
     FIG. 13 is a sectional view, partially cutaway, of the granulation system proposed in JP-A-60-183030. 
    
    
     DESCRIPTION OF THE PREFERRED EMBODIMENT 
     Preferred embodiments of the present invention will be described hereunder referring to the attached drawings. 
     FIG. 1 shows a granulation system of the present invention diagrammatically. 
     A fluidized layer granulation system  1  is comprised of a granulation tank  2 , an air source  3  such as a blower fan, a heating means  5  such as a heat exchanger, and a binding solution spray means  6  such as a nozzle means for spraying a binding solution. 
     The system  1  is newly provided with a pulsating vibration air generation means  4  between the granulation tank  2  and the air source  3  via a conduit pipe. 
     The granulation tank  2  is formed like a cylindrical hopper and is provided with a heated air supply port  2   a  at the bottom thereof. The supply port  2   a  is connected with the heating means  5  such as a heat exchanger, a filter  14 , the pulsating vibration air generation means  4 , the air source  3  via conduit pipes. 
     When the air source  3  is driven and the pulsating vibration air generation means  4  is also driven, the air generated from the source  3  is transformed into pulsating vibration air by means of the pulsating vibration air generation means  4 . Further, the pulsating vibration air is heated by the heating means  5  and the heated pulsating vibration air is supplied from the heated air supply port  2   a  into the granulation tank  2 , whereby the supplied pulsating vibration air is blown up in the granulation tank  2 . 
     A fluidization bed  7  is provided above the heated air supply port  2   a  in the granulation tank  2 . The material A stored in the granulation tank  2  is deposited on the fluidization bed  7  temporarily while pulsating vibration air isn&#39;t supplied into the tank  2 . 
     When the pulsating vibration air is supplied from the heated air supply port  2   a,  the material A builds up on the fluidization bed  7  floats in the granulation tank  2  to be mixed in the air blown up from the fluidization bed  7  so as to form a fluidization layer while the pulsating vibration air is at peak side. On the other hand when the pulsating vibration air is at valley side, the velocity of the blown-up air becomes weak. Therefore, some of the material A floating in the air drop on the fluidization bed and deposit thereon. 
     A discharge port  2   b  is provided at the top of the granulation tank  2  and the supplied pulsating vibration air in the tank  2  is naturally discharged from the port  2   b.    
     The binding solution spray means  6  is provided at a fixed position in the granulation tank  2 , connected with an air source  8  for the binding solution spray means  6  for storing pressurized air via an air supply pipe  9 , and connected with a tank  10  for storing a binding solution via a binding solution supply pipe  11 . 
     Further, a supply control means  12  is provided between the binding solution supply pipe  11  for controlling the spray amount of a binding solution B stored in the tank  10  from the spray means  6 . 
     In this embodiment a well-known liquid spray nozzle is used as the spray means  6 . The binding solution B stored in the tank  10  is supplied from the supply control means  12  and is sprayed by means of compressed air supplied from the air source for a binding solution spray  8  via the air supply pipe  9 . 
     The numeral  13  in the FIG. 1 refers to a bag filter for preventing the raw material A, the granulating material and the granulated material from flowing out of the granulation tank  2 . The numeral  14  refers to a dust collecting filter for removing dust in the air supplied into the tank  2 . 
     The construction of the pulsating vibration air generation means  4  is explained referring to FIG.  2 . 
     The pulsating vibration air generation means  4  is provided with a cylindrical casing  41  having a pair of connecting ports h 1 , h 2  at a surrounding wall  41   a  thereof and a rotary valve  42  having a rotational axis  41   b  in the center of the casing  41 . The rotary valve  42  is constructed so as to divide the inside of the casing  41  into at least two spaces. 
     One port h 1  of the pair of connecting ports h 1 , h 2  provided at the surrounding wall  41   a  is connected with the air source  3  via a conduit and the other port h 2  is connected with the granulation tank  2  via a conduit. 
     When the air source  3  and the rotary valve  42  of the pulsating vibration air generation means  4  are simultaneously driven, the air generated by driving the air source  3  is supplied into the granulation tank  2  because the air source  3  and the granulation tank  2  are communicated when the rotary valve is positioned at the solid line in the drawing. On the other hand when the rotary valve  42  is positioned at the dotted line, the air source  3  and the granulation tank  2  is blocked by the rotary valve  42 . 
     In the space, communicating with the port h 1  connecting with the air source  3 , of the two spaces divided by the rotary valve  42  in the casing  41 , the air supplied by driving the air source  3  is compressed. In the other space communicating with the port h 2  connecting with the granulation tank  2 , the compressed air is supplied into the granulation tank  2  via a conduit and pulsating vibration air of which maximum and minimum values are positive as shown in the FIG.  3 ( a ) is generated in the granulation tank  2 , whereby vibration is caused in the conduit and the granulation tank  2 . 
     A granulation method by means of the granulation system  1  is explained hereinafter. 
     At first, the raw material A is stored in the granulation tank  2 . Then the air source  3  is driven, the rotary valve  42  of the pulsating vibration air generation means  4  is driven to be rotated, and further the heating means  5  is driven. The air generated by driving the air source  3  is transformed into the pulsating vibration air as shown in FIG.  3 ( a ) so as to be supplied into the granulation tank  2 . 
     Most of the raw material A deposited on the fluidization bed  7  is mixed with the air blown up from the bed  7  to be floated in the granulation tank  2  and forms a fluidization layer when the pulsating vibration air is at its peak as shown in FIG.  4 ( a ). On the other hand when the pulsating vibration air is at its valley as shown in FIG.  4 ( b ), the air velocity becomes weak. Therefore, some of the floating material A drop and deposit on the fluidization bed  7 . Such a phenomenon appears alternately according to the pulsating vibration air. (The fluidized layer wherein the material A is fluidized and some of the material float and others drop according to the frequency of the pulsating vibration air is called “pulsating vibration air type fluidized layer” in this specification hereinafter). 
     Whether the fluidized layer becomes high density or low density at the peak of the pulsating vibration air depends on the amount and the property of the raw material stored in the granulation tank  2  and the amount of the air supplied into the tank  2  at the peak of the pulsating vibration air. 
     In the same way, whether the fluidized layer becomes high density or low density at the valley of the pulsating vibration air depends on the amount and the property of the raw material stored in the granulation tank  2 , and the amount of the air supplied into the tank at the valley of the pulsating vibration air. 
     If the air source  3  is a blower fan, the amplitude and the frequency of the pulsating vibration air supplied into the granulation tank  2  are adjusted by controlling the number of revolution of the blower fan or controlling the speed of revolution of the rotary valve  42  of the pulsating vibration generation means  4  in order that the above-mentioned phenomena appear periodically and stably and a desirable fluidization layer is formed. 
     Thereafter, a binding solution B is sprayed by a preferable spray by supplying air with a fixed pressure into the binding solution spray means  6  from the air source  8  and controlling the solution supply means  12  so that liquid bridging is formed between the particles of the material A. The particles of the material A are aggregated and dried in the pulsating vibration air fluidized layer formed by heated pulsating vibration air, whereby the particles are grown and granulated material is produced. 
     A high density fluidization layer and a low density fluidization layer are appeared alternately according to the pulsating vibration air in the granulation tank  2  because heated pulsating vibration air is supplied in the tank  2  of the granulation system  1 . 
     When the fluidization layer of the granulation tank  2  is low density, the particles grow uniformly and slowly, which is the same as when a large amount of heated air is supplied at a fixed rate in the tank  2  to granulate the particles. 
     On the other hand when the fluidization layer is high density, the particles grow swiftly, which is same as when a small amount of heated air is supplied into the tank  2  to granulate the particles. 
     In this case projections like an antenna of a snail are formed on the surface of the particles. However, the particles in the granulation tank  2  collide each other by up-and-down movement of the raw material A, the granulating material and the granulated material by means of the pulsating vibration air. Thereby, the projections may be broken or peeled off so that granulated material with a constant physical property having a uniform particle diameter, particle shape and etc. 
     When the pulsating vibration air is at its valley, some of the raw material A, the granulating material and the granulated material drop and deposit on the fluidization bed  7 . Pressurization is applied on such materials to be high density because tapping caused by the weight of the deposited material and the vibration of the granulation tank  2  by the pulsating vibration air are functioned on the materials. Therefore, the granulated material is prevented from being porous so as to be granulated as a high quality granulated material with small specific volume compared to the prior fluidized layer granulation method wherein particles grow while floating in the air. 
     Further in the present invention, pulsating vibration air with strength and weakness, not a fixed air flow, is applied for forming the fluidization layer by fluidizing the raw material A stored in the granulation tank  2 . Therefore, all the material A is stirred evenly and distributed efficiently by the pulsating energy of pulsating vibration air so that the whole material A can become a fluidization layer. As the result, some raw material A isn&#39;t deposited on the fluidization bed  7  to be kept still as shown in the prior art wherein a fixed and uniform air flow is supplied to the granulation tank to form a fluidization layer. Moreover, the productivity of the granulated material compared to the original raw material A becomes very high. 
     The raw material A is stirred uniformly by the pulsating energy of pulsating vibration air because pulsating vibration air with strength and weakness is applied in the present invention. It isn&#39;t appeared that the air supplied in the granulation tank  102  blows through the part of the raw material A deposited on the fluidized bed  107 , sometimes happened in the prior art wherein air is supplied at a fixed and uniform rate into the tank  102 . While in the present invention, the raw material A is easily fluidized and the produced fluidized layer is stable. Therefore, a phenomenon such as slacking, bubbling, chanelling and so on in the process of granulation which stops fluidization of the raw material is prevented or relieved compared to the prior art wherein heated air is supplied into the granulation tank  102  with a fixed and uniform rate, whereby granulated material can be easily produced. 
     The average pressure, velocity and flow rate of pulsating vibration air becomes small compared to the prior art using a fixed and uniform air because the raw material A stored in the granulation tank  2  is easily fluidized by using pulsating vibration air compared to such a prior art. Therefore, the shock energy when the raw material A, the granulating material and the granulated material collide in the process of granulation can be made small. According to this granulation method, the amount of the fine particles produced by collision of the particles is reduced because the impact caused by collision of each particles in the granulation process is small. Thereby, the amount of fine particles contained in the granulated material can be reduced. 
     In case that the air source  3  is a blower fan, the frequency, amplitude and wave shape of the pulsating vibration air can be easily changed by controlling the revolution number of the fan or by controlling the revolution speed of the rotary valve  42  of the pulsating vibration air generation means  4 . 
     Accordingly, when the frequency, amplitude and wave shape of the pulsating vibration air are changed depending on the property of the raw material A, a phenomenon such as slacking, bubbling, chanelling and so on in the process of granulation which stop fluidization of the raw material A is prevented or relieved compared to the prior art wherein heated air is supplied into the granulation tank  102  with a fixed and uniform rate, whereby granulated material can be easily produced. 
     In case that a vehicle and an active component are compound at a fixed rate as the material A, granulated material with uniform compounding rate can be produced because the raw material A stored in the granulation tank  2  is uniformly stirred to be fluidized by applying pulsating vibration air. 
     The present invention is explained based on the specific data of the experiment. 
     FIG. 5 is the result of the experiment wherein the amount of air required for producing the granulated material of the same specific volume from the original material with the same ingredient and amount was compared in the present invention and the prior art. In this case the granulation tank  2  of the same size and shape was used, the air source  3  was driven under the same condition, and the heating means  5  was heated under the same condition. 
     The system shown in FIG. 1 is used for the experiment. In the prior art, the rotary valve  42  of the pulsating vibration means  4  was stopped where the air source  3  and the granulation tank  2  were communicated (the rotary valve  42  is at the position shown in a solid line in FIG. 2) and material was granulated according to the prior method. The specific volume (ml/g) of the granulated material and the supplied flow amount (m 3 /min.) supplied into the granulation tank  2  were measured. 
     Methylcellulose dissolved in water was used as a binding solution and lactose was used as powdered raw material. (They were also used for the following experiments.) 
     In the present invention, the rotary valve  42  was rotated at 5 Hz and other conditions were the same as in the prior art. In such a condition the specific volume (ml/g) of the granulated material and the supplied flow amount (m 3 /min.) at the air supplied into the granulation tank  2  were measured. 
     As shown in FIG. 5, it is clear that the amount of air required for granulating the material of the same specific volume in the present invention is less than that in the prior art. 
     FIG. 6 is a graph showing the correlation of the amount of air used for granulation and the breaking load of the granulated material. 
     The system shown in FIG. 1 was used for the experiment. In the prior art, the rotary valve  42  of the pulsating vibration air generation means  4  was stopped where the air source  3  and the granulation tank  2  was communicated (the rotary valve  42  is at the position shown in a solid line in FIG. 2) and material was granulated according to the prior method. The supplied flow amount (m 3 /min.) of the air supplied into the granulation tank  2  was varied and the breaking load of the granulated material produced at each supplied flow amount (m 3 /min.) was measured. 
     In the present method the material was granulated when the rotary valve  42  was rotated at 5 Hz and other conditions were the same as in the prior art. Under such a condition the breaking load of the granulated material was measured. 
     According to the result in FIG. 6, hard granulated material, that is mechanically strong, is obtained in the present invention compared to the granulated material obtained in the prior art when the amount of air used for granulation is the same. 
     FIG. 7 shows a graph compared particle size distribution of the granulated material produced in the prior art and that in the present invention. 
     The system shown in FIG. 1 was used for the experiment. In the prior art, the rotary valve  42  of the pulsating vibration air generation means  4  was stopped where the air source  3  and the granulation tank  2  were communicated (the rotary valve  42  is at the position shown in a solid line in FIG. 2) and material was granulated by supplying uniform and fixed amount of heated air into the tank  2  according to the prior method. In this experiment the particle size distribution of the granulated material was measured after the granulation. 
     In the present method the material was granulated when the rotary valve  42  was rotated at 5 Hz and other conditions were the same as in the prior art. Under such a condition the particle size distribution of the granulated material was measured. 
     According to FIG. 7, it is clear that the particle size distribution of the granulated material in the present invention was sharp compared to the prior art. 
     Further according to FIG. 7, it is also clear that fine particles contained in the granulated material can be reduced in the present invention compared to the prior art. 
     Table 1 shows the result of the experiment wherein the rough specific volume of the granulated material is measured by varying the frequency of the pulsating vibration air. FIG. 8 is a graph showing the correlation of the frequency of the pulsating vibration air used for granulation and the rough specific volume of the granulated material. 
     
       
         
               
               
               
               
               
               
               
             
           
               
                 TABLE 1 
               
               
                   
               
             
             
               
                 frequency of 
                 0 
                 1 
                 5 
                 6 
                 9 
                 10 
               
               
                 pulsating 
               
               
                 vibration air (Hz) 
               
               
                 rough specific 
                 1.896 
                 1.698 
                 1.643 
                 1.741 
                 1.768 
                 1.837 
               
               
                 volume 
               
               
                 (ml/g) 
               
               
                   
               
             
          
         
       
     
     According to the result, when pulsating vibration air with the frequency of 0 Hz (steady flow air) and 10 Hz is applied, the rough specific volume of the granulated material in the present invention applying 10 Hz pulsating vibration air is about the same as that of the prior art applying steady flow air. As shown in Table 1 and FIG. 8, the frequency of the pulsating vibration air is preferably not less than 1 Hz and less than 10 Hz. It is preferable to be from 1 Hz to 9 Hz for reducing the specific volume at 20%. To reduce 50%, the frequency is desirable from 1 Hz to 6 Hz. Pulsating vibration air with 5 Hz frequency is preferred in order to obtain the minimum rough specific volume. 
     Table 2 shows the particle size distribution of the granulated material produced by varying the frequency of the pulsating vibration air. FIG. 9 is a graph showing the correlation of the frequency of the pulsating vibration air used for granulation and the particle size distribution of the granulated material. Pulsating vibration air with 0 Hz, 1 Hz, 5 Hz, 6 Hz, 9 Hz or 10 Hz was applied and the granulated material was passed through a screen with 710 μm diameter mesh, 500 μm, 355 μm, 250 μm, 150 μm, 106 μm, or 75 μm. Then the weight of the particles remained on the mesh and the weight of the particles passed through were measured and they are shown as weight percent. The granulated material with sharp particle size distribution focused on narrow range is good quality having uniform particle diameter. 
     
       
         
               
               
               
               
               
               
               
             
               
               
               
               
               
               
               
             
           
               
                 TABLE 2 
               
               
                   
               
               
                 frequency of pulsating 
                   
                   
                   
                   
                   
                   
               
               
                 vibration air (Hz) 
                 0 
                 1 
                 5 
                 6 
                 9 
                 10 
               
               
                   
               
             
             
               
                   
               
             
          
           
               
                 ON 710 μm (Weight %) 
                 16.5 
                 41.8 
                 23.4 
                 22.1 
                 19.8 
                 18.2 
               
               
                 ON 500 μm (weight %) 
                 19.7 
                 19.4 
                 25.0 
                 24.6 
                 23.3 
                 22.2 
               
               
                 ON 355 μm (weight %) 
                 26.1 
                 24.2 
                 36.2 
                 36.1 
                 36.0 
                 35.7 
               
               
                 ON 250 μm (weight %) 
                 20.2 
                 11.6 
                 13.3 
                 14.7 
                 17.2 
                 19.2 
               
               
                 ON 150 μm (weight %) 
                 12.2 
                 2.9 
                 2.0 
                 2.5 
                 3.7 
                 4.7 
               
               
                 ON 106 μm (weight %) 
                 5.3 
                 0.0 
                 0.0 
                 0.0 
                 0.0 
                 0.0 
               
               
                 ON 75 μm (weight %) 
                 0.0 
                 0.0 
                 0.0 
                 0.0 
                 0.0 
                 0.0 
               
               
                 PASS THROUGH (weight %) 
                 0.0 
                 0.0 
                 0.0 
                 0.0 
                 0.0 
                 0.0 
               
               
                   
               
             
          
         
       
     
     According to Table 2 and FIG. 9, the particle size distribution of the granulated material produced at 5 Hz or 10 Hz pulsating vibration air is focused on narrow range. However, about 5 Hz pulsating vibration air is preferable because the rough specific volume is small and the particle size distribution is focused on narrow range as shown in Tables 1, 2 and FIGS. 8,  9  when the rough specific volume is further considered. 
     When a dissolution test is executed for the granulated material produced at 1 Hz, 5 Hz, 6 Hz, 9 Hz and 10 HZ according to a rotating basket method described in Japanese Pharmacopoeia (the eleventh edition), similar dissolution pattern is seen. 
     When the granulated material produced according to the present method is used, tablets or capsules can be made small without influencing the solubility of the tablets or the capsules. Therefore, the compliance of a patient for dosing the tablets or the capsules can be highly improved and its dosing efficiency can be advanced. 
     The rotary type pulsating vibration air generation means is used as the pulsating vibration air generation means  4  and is provided between the conduit pipe connecting the air source  3  and the granulation tank  2  in the above-mentioned embodiments. However, it is one of the preferred embodiments. An on-off valve such as a solenoid valve may be provided between the conduit pipe connecting the air source  3  and the granulation tank  2 . In this case pulsating vibration air of which maximum is positive and minimum is atmospheric pressure as shown in FIG.  3 ( b ) may be produced in the granulation tank  2  by communicating and shutting the air supplied from the air source  3  by opening and closing the conduit by means of the on-off valve. 
     The pulsating vibration air supplied into the granulation tank  2  is naturally discharged from the discharged port  2   b  of the tank  2  in the embodiments mentioned above. However, it is also one of the preferred embodiments. A suction means may be provided for the discharge port  2   b  and another pulsating vibration air generation means may be further provided between the conduit connecting the discharge port and the suction means. 
     In this case the suction means of the discharge port  2   b  is supplementarily provided to promote smooth discharge of the supplied pulsating vibration air out of the granulation tank  2 . It is preferable pulsating vibration air, which fluidizes the raw material and some of which suspend up and down according to its frequency, is designed to be supplied in heated condition below the fluidization bed  7  to upward and the granulation tank  2  keeps the pressure more than atmospheric pressure. 
     When another pulsating vibration air generation means is further provided between the conduit connecting the discharge port  2   b  and the suction means, it is preferable that such a pulsating vibration air generation means is supplementary for changing the wave shape a little or promoting rise of the raw material A in the granulation tank  2  relative to the pulsating vibration air generation means  4 . 
     Some raw material A are easy to be mixed with air and the others are not. Therefore, it may be preferable to change the wave shape of the pulsating vibration air in order to fluidize the material stored in the granulation tank and make the aggregated material suspend up and down according to the frequency of the pulsating vibration air. 
     FIG. 10 shows the granulation system provided with the pulsating vibration air generation means which can easily change its wave shape into a desirable one. 
     A piston type pulsating vibration air generation means  4 A is provided instead of the pulsating vibration air generation means  4  of FIG.  2 . The pulsating vibration air generation means  4 A is provided with a valve  45  for opening and closing a conduit  43  connecting the air source  3  and the heated air supply port  2   a  and a valve cam mechanism  46  having a specific circular pattern  46   p  regulating the open-close duration and the amount of the valve  45 . 
     A rotary drum is used as the valve cam mechanism  46  and is provided rotatably around an axis  48   a  by means of a driving means  48  such as a motor. Upper rails  46   u  and a lower rail  46   d  with desirable specific circular patterns  46   p  are provided in a circumferential direction of the drum  46 . An opening  47  is provided between the upper rails  46   u  so as to surround the drum  46  in a circumferential direction as shown in FIG. 10 ( b ). 
     A power transmission axis  50  is connected with the valve  45  and is provided with an attachment  51  for rotatably fitting rollers  52  at its bottom end. The diameter D 52  of the rollers  52  is designed to be the length D 46   u - 46   d  between the upper rail  46   u  and the lower rail  46   d.    
     The width of the opening  47  is set to be a little larger than the width of the attachment  51 . The attachment  51  and the power transmission axis  50  are fitted in the opening  47  vertically. 
     Each roller  52  is provided between the lower rail  46   d  and the upper rail  46   u  and outside of the opening  47  respectively. 
     An air introduction pipe  44  is connected with the conduit  43 , a solenoid valve  53  for opening and closing the pipe  44 , and a filter  54  attached to the end of the pipe  44 . 
     According to the pulsating vibration air generation means  4 A, the valve  45  is closed when the specific circular pattern  46   p  is at its peak  46   t  and the valve  45  is opened when the pattern  46   p  is at its valley  46   v . The opening degree of the valve  45  depends on the depth D 46   v  of the valley  46   v  of the specific circular pattern  46   p . The opening time of the valve  45  depends on the length L 46   v  of the valley  46   v  and the rotation speed of the rotary drum  46 . 
     How the pulsating vibration air with a desirable wave shape is generated is described according to the pulsating vibration air generation means  4 A. 
     When the air source  3  is driven to rotate the rotary drum  46  at a fixed rotation speed, the valve  45  is opened and closed in compliance with the specific circular pattern  46   p.    
     The rotary drum  46  with different specific circular pattern  46   p  may be used, the driving source of the air source  3  may be changed, the rotation speed of the drum  46  may be changed, or the solenoid valve  51  may be opened and closed in order to generate pulsating vibration air with a desirable wave shape, frequency and amplitude in the granulation tank  2 . 
     According to such a pulsating vibration air generation means  4 A, fluidization process can be executed easily by utilizing pulsating vibration air with desirable wave shape, frequency and amplitude wherein the raw material A stored in the granulation tank  2  can be fluidized and some of the fluidized material A can suspend up and down in compliance with the frequency of the pulsating vibration air. 
     If a vibrating means  21  is provided for a bag filter  13  and the bag filter  13  is vibrated by driving the vibrating means  21 , clogging of the bag filter  13  during granulation can be prevented. Therefore, cleaning of the bag filter  13  during granulation isn&#39;t required so that granulation becomes easy. 
     The vibrating means  21  is provided with a vibration air source  22  such as a blower fan, a hollow conduit pipe  23 , a control valve  24  such as a solenoid valve provided at the downstream of the air source  22 , an elastic membrane  25 , and a wire  26 . One end of the pipe  23  is connected with the air source  22  and the other end is provided with the membrane  25  so as to close the hollow inside of the pipe  23 . One end of the wire  26  is connected to the membrane  25  and the other end is connected to the bag filter  13 . The source  22  is driven to supply air into the pipe  23 , and intermittent air flow is generated by opening and closing the control valve  24  at a fixed cycle. The membrane  25  is expanded and returned to its original form by the intermittent air flow, whereby the intermittent air is transformed into a vibration energy at the downstream of the membrane  25 . Such generated vibration energy is transmitted to the bag filter  13  via the wire  26  to be vibrated. 
     In the above-mentioned embodiment a blower fan is used as the air source  3 , however, a gas cylinder containing compressed air or compressed inert gas may be used as the air source  3 . 
     As shown in FIG.  11 ( b ), a cyclone  31  may be used instead of the bag filter  13  to prevent the raw material A, the granulating material and the granulated material from flowing out of the granulation tank  2 . 
     As mentioned above, according to the granulation method of the present invention, powdered material is fluidized by applying heated pulsating vibration air, and aggregated when the binder solution is sprayed, then the aggregated powdered material drops and deposits on the fluidized bed while suspending up and down according to the frequency of the pulsating vibration air. And finally the granulating material deposited on the fluidized bed is compressed to be high density further by means of heated pulsating vibration air. Therefore, the projections like an antenna of a snail is prevented from appearing on the surface of the particles of the granulating material and the granulated material doesn&#39;t become porous. Accordingly, heavy granulated material, which has uniform property such as particle diameter and shape and small specific volume, can be produced in a short time compared to the prior art wherein a low density fluidization layer is formed by increasing the amount of the air supplied in the granulation tank. 
     Whereas according to the granulation system of the present invention, the pulsating vibration air generation means is provided prior to the air supply port provided at the bottom of the granulation tank and the heated pulsating vibration air is supplied below the fluidization bed to upwards. The raw powdered material can be fluidized to be aggregated together and thus aggregated material can suspend up and down according to the frequency of the pulsating vibration air and drop and deposit on the fluidization bed. And then, the deposited material is compressed to be airtight by further supplying heated pulsating vibration air. Therefore, heavy granulated material, which has uniform property, such as particle diameter and shape, and high density and small specific volume, can be produced in a short time.