JP2015030586A - Treatment apparatus of powder and granular material - Google Patents

Abstract

PROBLEM TO BE SOLVED: To provide a treatment apparatus of a powder and granular material where the powder and granular material is pneumatically conveyed from a first storage tank to a second storage tank and the moisture absorption of the powder and granular material in the first storage tank can be suppressed.SOLUTION: A treatment apparatus 1 of a powder and granular material is equipped with a first gas introduction part 60 to introduce an inert gas into a first storage tank 10. Accordingly, pressure reduction in the first storage tank 10 can be suppressed by introducing the inert gas into the first storage tank 10 and then the intrusion of outside air into the first storage tank 10 can be suppressed. Consequently, the powder and granular material 9 is pneumatically conveyed from the first storage tank 10 to the second storage tank 20 and the moisture absorption of the powder and granular material 9 can be suppressed.

Description

  The present invention relates to a granular material processing apparatus that supplies a granular material to a subsequent apparatus while managing the moisture content of a material composed of powder or granular material (hereinafter referred to as “a granular material”).

  2. Description of the Related Art Conventionally, in a plastic product molding process, a powder processing apparatus is used that stores powder particles such as resin pellets in a storage tank and dries them, and supplies the dried powder particles to an injection molding machine. In this kind of granular material processing apparatus, the granular material thrown into the 1st storage tank is conveyed to the 2nd downstream storage tank via a conveyance pipe. And a granular material is dried by supplying the heated gas in a 2nd storage tank.

  A conventional powder processing apparatus is described in Patent Document 1, for example.

JP 7-68552 A

  Conventionally, so-called aerodynamic conveyance in which powder particles are conveyed by generating an air flow in a conveyance tube has been used for conveying the particles from the first storage tank to the second storage tank. However, when the granular material is pneumatically conveyed in the transfer pipe connecting the first storage tank and the second storage tank, a part of the gas in the first storage tank is sucked into the transfer pipe. Therefore, the inside of the first storage tank tends to be negative pressure. For this reason, there exists a possibility that external air may penetrate | invade into the inside of a 1st storage tank from the clearance gap etc. of the lid | cover of a 1st storage tank. When outside air with high humidity enters the first storage tank, the granular material absorbs moisture, and the initial moisture content of the granular material increases.

  This invention is made | formed in view of such a situation, and can convey a granular material pneumatically from a 1st storage tank to a 2nd storage tank, and can suppress the moisture absorption of the granular material in a 1st storage tank. It aims at providing a granular material processing apparatus.

  1st invention of this application is a granular material processing apparatus, Comprising: The conveyance pipe which connects the 1st storage tank which stores a granular material, and the 2nd storage tank located in the 1st storage tank and the downstream, Air flow generating means for generating an air flow from the first storage tank to the second storage tank and a first gas introduction unit for introducing an inert gas into the first storage tank are provided in the transport pipe.

  2nd invention of this application is a granular material processing apparatus of 1st invention, Comprising: The inert gas introduce | transduced from the said 1st gas introduction part WHEREIN: The atmospheric pressure in a said 1st storage tank becomes higher than external pressure.

  3rd invention of this application is a granular material processing apparatus of 1st invention or 2nd invention, Comprising: It further has the circulation line connected to the said conveyance pipe | tube, and the inert introduced from the said 1st gas introduction part Gas is circulated in the circulation line.

  A fourth invention of the present application is any one of the powder and particle processing apparatuses according to the first to third inventions, further comprising a drying means for drying the powder and particles in the second storage tank.

  The fifth invention of the present application is any one of the granular material processing apparatuses of the first invention to the fourth invention, wherein the first storage tank has a bottomed cylindrical storage tank body having an opening in the upper part, A lid for closing the opening of the storage tank body, and the first gas introduction part has a gas introduction pipe connected to the storage tank body.

  A sixth invention of the present application is any one of the powder material processing apparatuses from the first invention to the fifth invention, wherein the powder tube is discharged from the second storage tank, and the inert tube is inactive. And a second gas introduction unit for introducing gas.

  According to the first to sixth inventions of the present application, a pressure drop in the first storage tank is suppressed by introducing an inert gas into the first storage tank. Then, the intrusion of outside air into the first storage tank can be suppressed. Therefore, moisture absorption of the powder and granular material can be suppressed.

  In particular, according to the second invention of the present application, the intrusion of outside air into the first storage tank can be further suppressed.

  In particular, according to the third invention of the present application, by circulating the gas, the humidity and oxygen concentration of the gas in the transport pipe can be kept low. Therefore, moisture absorption of the granular material in the transport pipe can be further suppressed.

  In particular, according to the fourth invention of the present application, moisture absorption of the granular material before drying is suppressed in the first storage tank, and then the granular material is dried in the second storage tank. Thereby, the moisture content of a granular material can be stably reduced to the target moisture content. Moreover, the oxidation of a granular material can also be suppressed.

  In particular, according to the fifth invention of the present application, it is possible to introduce an inert gas from the gas introduction pipe into the inside of the storage tank body even in a state where the lid portion is opened. Therefore, it is possible to suppress the outside air from being mixed into the inside of the storage tank main body when the lid is opened and the granular material is introduced into the storage tank main body.

  In particular, according to the sixth invention of the present application, by introducing an inert gas into the exhaust pipe, moisture absorption and oxidation of the powder after the drying treatment can be prevented.

It is the figure which showed the structure of the granular material processing apparatus. It is a block diagram which shows the structure of the control system of a granular material processing apparatus. It is the flowchart which showed an example of the process in a granular material processing apparatus. It is the graph which showed the example of the change of the moisture content of the resin pellet at the time of a drying process.

  Hereinafter, preferred embodiments of the present invention will be described with reference to the drawings.

<1. Configuration of powder processing apparatus>
FIG. 1 is a diagram showing a configuration of a powder particle processing apparatus 1 according to an embodiment of the present invention. This granular material processing apparatus 1 is an apparatus that dries resin pellets 9 that are granular particles and supplies the dried resin pellets 9 to the subsequent injection molding machine 2. As shown in FIG. 1, the granular material processing apparatus 1 of the present embodiment includes a first storage tank 10, a second storage tank 20, a transfer pipe 30, a transfer circulation line 40, a drying circulation line 50, and a first gas. An introduction unit 60, a second gas introduction unit 70, and a control unit 80 are included.

  The 1st storage tank 10 is a container which stores the resin pellet 9 before drying inside. The first storage tank 10 includes a bottomed cylindrical storage tank body 11 having an opening 110 in the upper part, and a lid portion 12 placed on the upper part of the storage tank body 11. The storage tank main body 11 has a substantially cylindrical side wall 111 and a funnel-shaped bottom 112 that gradually converges from the lower end of the side wall 111 downward. A space for storing the resin pellet 9 is provided inside the storage tank body 11. The lid 12 closes the opening 110 at the top of the storage tank body 11. Moreover, when the cover part 12 is removed, the upper part of the storage tank main body 11 is opened, and the resin pellet 9 can be put into the storage tank main body 11 through the opening 110.

  The 2nd storage tank 20 is a container which stores the resin pellet 9 inside in the conveyance direction downstream from the 1st storage tank 10. The second storage tank 20 has a substantially cylindrical side wall 21, a funnel-shaped bottom part 22 that gradually converges from the lower end of the side wall 21, and a top plate part 23 that covers the upper part of the second storage tank 20. Have Inside the second storage tank 20, a space for storing and drying the resin pellets 9 is provided.

  A transport hopper 24 is installed on the upper part of the second storage tank 20. The transport hopper 24 is a container that temporarily stores the resin pellet 9 when the resin pellet 9 is supplied to the second storage tank 20. The transport hopper 24 is connected to the second storage tank 20 via an openable / closable inlet 231 provided in the top plate portion 23 of the second storage tank 20. Further, the downstream end of the transport pipe 30 is connected to the side of the transport hopper 24.

  On the other hand, a discharge pipe 25 for discharging the resin pellet 9 from the second storage tank 20 is connected to the lower part of the second storage tank 20. The discharge pipe 25 extends downward from a discharge port 221 provided in the bottom 22 of the second storage tank 20. The downstream end of the discharge pipe 25 is connected to the injection molding machine 2. Further, the discharge pipe 25 is provided with a discharge valve 26 that switches between opening and closing of the discharge port 221 by the movement of the valve body 261. The valve body 261 can move forward and backward between a state in which the discharge port 221 is closed and a state in which the discharge port 221 is opened by retreating to a retreat space 262 provided on the side of the discharge pipe 25. .

  The transport pipe 30 is a pipe for transporting the resin pellets 9 between the first storage tank 10 and the second storage tank 20. The upstream end of the transport pipe 30 in the transport direction is connected to a discharge port 113 provided in the bottom 112 of the first storage tank 10. On the other hand, the downstream end of the transport pipe 30 in the transport direction is connected to the side of the transport hopper 24. That is, the first storage tank 10 and the second storage tank 20 are connected by the transfer pipe 30 and the transfer hopper 24. The resin pellets 9 discharged from the first storage tank 10 are transported to the transport hopper 24 by the air flow generated in the transport pipe 30.

  The transfer circulation line 40 is a piping system that circulates gas in order to generate an air flow toward the transfer hopper 24 in the transfer pipe 30. One end of the transfer circulation line 40 is connected to the upper portion of the transfer hopper 24. The other end of the transfer circulation line 40 is connected to the transfer pipe 30. A punching metal plate 241 is provided at a connection portion between the transport circulation line 40 and the transport hopper 24. The punching metal plate 241 has a plurality of through holes that restrict the passage of the resin pellets 9 and allow the passage of air. A filter 41 and a transport blower 42 are provided in the middle of the path of the transport circulation line 40.

  When the transport blower 42 is operated, an air flow from the transport hopper 24 toward the transport pipe 30 is generated in the transport circulation line 40 as indicated by an arrow A1 in FIG. Then, as indicated by an arrow A2 in FIG. 1, an air flow from the first storage tank 10 toward the transport hopper 24 is generated inside the transport pipe 30. The resin pellets 9 discharged from the first storage tank 10 are pneumatically transported to the transport hopper 24 by the airflow.

  The fine dust sucked from the transport hopper 24 into the transport circulation line 40 is collected by the filter 41. Further, the movement of the resin pellet 9 from the transport hopper 24 to the transport circulation line 40 is blocked by the punching metal plate 241. For this reason, the resin pellet 9 is stored in the transport hopper 24 without flowing into the transport circulation line 40 side.

  After the resin pellets 9 are stored in the transport hopper 24, when the pneumatic transport is stopped and the input port 231 is automatically opened, the resin pellets are transferred from the transport hopper 24 to the second storage tank 20 through the input port 231. 9 is inserted. Thus, the resin pellet 9 is stored in the 2nd storage tank 20 by repeating the pneumatic conveyance of the resin pellet 9 from the 1st storage tank 10 to the 2nd storage tank 20, and opening | release of the insertion port 231. FIG. .

  The drying circulation line 50 is a piping system that circulates gas in order to supply hot air for drying into the second storage tank 20. One end of the drying circulation line 50 is connected to a suction port 232 provided in the top plate portion 23 of the second storage tank 20. The other end of the drying circulation line 50 passes through the side wall 21 of the second storage tank 20 and is connected to an outlet 54 disposed inside the second storage tank 20. A filter 51, a drying blower 52, and a heater 53 are provided in the middle of the route of the drying circulation line 50.

  When the drying blower 52 is operated, an air flow from the suction port 232 to the outlet 54 is generated in the drying circulation line 50 as indicated by an arrow A3 in FIG. Fine dust sucked into the circulation line 50 for drying from the second storage tank 20 is collected by the filter 51. The gas that has passed through the filter 51 is heated by the heater 53 to become hot air. Then, the hot air is blown out from the outlet 54 into the second storage tank 20. An adsorber that adsorbs moisture contained in the gas may be provided between the filter 51 and the heater 53.

  The hot air blown out from the outlet 54 is diffused into the second storage tank 20 through the gap between the resin pellets 9 stored in the second storage tank 20. Thereby, the resin pellet 9 is heated, moisture is evaporated from the resin pellet 9, and the resin pellet 9 is dried. That is, the gas diffused into the second storage tank 20 absorbs moisture from the resin pellet 9. Further, the same amount of moisture that has been absorbed by the hot air blown out from the outlet 54 is sucked into the drying circulation line 50 again from the second storage tank 20 through the suction port 232. Thus, in the present embodiment, the drying circulation line 50 functions as a drying unit that dries the resin pellets 9 in the second storage tank 20.

  The first gas introduction unit 60 is a mechanism for introducing nitrogen gas, which is an inert gas, into the first storage tank 10. The first gas introduction unit 60 includes a nitrogen gas generator 61 and a gas introduction pipe 62. The upstream end of the gas introduction pipe 62 is connected to the nitrogen gas generator 61. The downstream end of the gas introduction pipe 62 is connected to an introduction port 114 provided on the side wall 111 of the storage tank body 11. In addition, an on-off valve 63 is provided in the middle of the gas introduction pipe 62. The on-off valve 63 may be omitted, and a flow rate adjusting valve may be provided instead.

  The nitrogen gas generator 61 generates dry nitrogen gas having a positive pressure from the external atmospheric pressure and the atmospheric pressure in the first storage tank 10. For this reason, when the on-off valve 63 is opened, positive nitrogen gas is supplied from the nitrogen gas generator 61 through the gas introduction pipe 62 into the first storage tank 10. That is, nitrogen gas is forcibly introduced into the first storage tank 10. If it does so, the atmospheric pressure in the 1st storage tank 10 will become higher than an external atmospheric pressure with the said nitrogen gas. Therefore, it is possible to suppress the outside air from entering the first storage tank 10. As a result, moisture absorption of the resin pellets 9 stored in the first storage tank 10 can be suppressed.

  In particular, in this granular material processing apparatus 1, the downstream end of the gas introduction pipe 62 is connected to the storage tank body 11 instead of the lid 12. For this reason, nitrogen gas can be introduced into the inside of the storage tank main body 11 from the gas introduction pipe 62 even in a state where the lid 12 of the first storage tank 10 is removed. For example, when the resin pellet 9 is introduced into the storage tank main body 11, nitrogen gas can be continuously introduced from the gas introduction pipe 62 into the storage tank main body 11. Thereby, when the resin pellet 9 is charged, it is possible to suppress the outside air from entering the storage tank body 11 through the opening 110. Therefore, moisture absorption of the resin pellet 9 at the time of material charging can be suppressed.

  Further, when the resin pellet 9 is pneumatically conveyed in the conveyance pipe 30, a part of the gas in the first storage tank 10 is sucked out to the conveyance pipe 30. For this reason, the pressure in the 1st storage tank 10 tends to fall. However, in this granular material processing apparatus 1, the pressure drop in the first storage tank 10 can be suppressed by introducing nitrogen gas into the first storage tank 10. Therefore, it is possible to suppress the outside air from entering the first storage tank 10 while the resin pellets 9 are conveyed pneumatically. As a result, moisture absorption of the resin pellets 9 stored in the first storage tank 10 can be further suppressed.

  The second gas introduction unit 70 is a mechanism for introducing nitrogen gas, which is an inert gas, into the discharge pipe 25. The second gas introduction unit 70 includes a nitrogen gas generator 71 and a gas introduction pipe 72. The upstream end of the gas introduction pipe 72 is connected to the nitrogen gas generator 71. The downstream end of the gas introduction pipe 72 is connected to a retreat space 262 provided on the side of the discharge pipe 25. An on-off valve 73 is provided in the middle of the gas introduction pipe 72. The on-off valve 73 may be omitted, and a flow rate adjusting valve may be provided instead.

  The nitrogen gas generator 71 generates dry nitrogen gas having a positive pressure from the external pressure and the pressure in the discharge pipe 25. Therefore, when the on-off valve 73 is opened, positive nitrogen gas is supplied from the nitrogen gas generator 71 through the gas introduction pipe 72 into the discharge pipe 25. That is, nitrogen gas is forcibly introduced into the discharge pipe 25. Then, the atmospheric pressure in the discharge pipe 25 becomes higher than the external atmospheric pressure and the pressure in the injection molding machine 2 due to the nitrogen gas. Accordingly, it is possible to suppress the gas in the injection molding machine 2 from flowing back to the discharge pipe 25. Moreover, it can suppress that the resin pellet 9 dried in the 2nd storage tank 20 absorbs moisture and oxidizes inside the discharge pipe 25.

  In particular, the temperature in the discharge pipe 25 is lower than the temperature in the second storage tank 20 to which hot air is supplied. For this reason, the resin pellet 9 discharged from the second storage tank 20 to the discharge pipe 25 easily absorbs moisture and other gas components as the temperature decreases. However, in this granular material processing apparatus 1, the humidity and oxygen concentration in the discharge pipe 25 are reduced by introducing the dried nitrogen gas into the discharge pipe 25 from the second gas introduction unit 70. Thereby, the moisture absorption and oxidation of the resin pellet 9 after a drying process are suppressed.

  In the granular material processing apparatus 1 of the present embodiment, the transport path of the resin pellet 9 from the first storage tank 10 to the discharge pipe 25 through the transport pipe 30, the transport hopper 24, and the second storage tank 20 is a substantially sealed system. It has become. When nitrogen gas is continuously introduced from the first gas introduction unit 60, the nitrogen gas is filled into the first storage tank 10, flows into the transport pipe 30, and circulates in the transport pipe 30 and the transport circulation line 40. Is done. Further, when nitrogen gas is continuously introduced from the second gas introduction part 60, the nitrogen gas fills the inside of the discharge pipe 25 and flows into the second storage tank 20, and the second storage tank 20 and the circulation for drying. Circulated in line 50. As a result, the entire transport path of the resin pellet 9 from the first storage tank 10 to the discharge pipe 25 through the transport pipe 30, the transport hopper 24, and the second storage tank 20 is filled with positive pressure nitrogen gas. Thereby, the influence of the humidity and temperature of external air can be suppressed, and the moisture content and oxidation amount of the resin pellet 9 can be suppressed as a whole apparatus.

  FIG. 2 is a block diagram showing the configuration of the control system of the powder processing apparatus 1. The control unit 80 is means for controlling the operation of each unit of the granular material processing apparatus 1. As shown in FIG. 2, the controller 80 is electrically connected to the discharge valve 26, the transport blower 42, the drying blower 52, the heater 53, the on-off valve 63, and the on-off valve 73 described above. The control unit 80 may be configured by a computer having an arithmetic processing unit such as a CPU and a memory, or may be configured by an electronic circuit. The control unit 80 controls the operation of each unit described above based on a preset program or an external input signal. Thereby, the process of the resin pellet 9 in the granular material processing apparatus 1 advances.

  Note that the discharge valve 26, the on-off valve 63, and the on-off valve 73 may be disconnected from the control unit 80 and manually operated by the user.

<2. Operation of powder processing apparatus>
Then, the process of the resin pellet 9 in the granular material processing apparatus 1 mentioned above is demonstrated. FIG. 3 is a flowchart showing an example of processing in the granular material processing apparatus 1.

  In this granular material processing apparatus 1, when processing the resin pellets 9, first, the resin pellets 9 from the first storage tank 10 to the discharge pipe 25 through the transfer pipe 30, the transfer hopper 24, and the second storage tank 20. The entire conveyance path is filled with nitrogen gas (step S1). Specifically, the on-off valve 63 is opened to introduce nitrogen gas from the first gas introduction unit 60 into the first storage tank 10, and the on-off valve 73 is opened to discharge from the second gas introduction unit 70. Nitrogen gas is introduced into the tube 25. Thereby, the air in the 1st storage tank 10, the conveyance pipe 30, the conveyance hopper 24, the 2nd storage tank 20, and the discharge pipe 25 is substituted by nitrogen gas.

  Next, the resin pellet 9 is put into the first storage tank 10 (step S2). That is, the lid 12 of the first storage tank 10 is removed, and the resin pellet 9 is introduced into the storage tank body 11 through the opening 110 of the storage tank body 11. At this time, the supply of nitrogen gas from the first gas introduction unit 60 is continued. For this reason, mixing of outside air into the storage tank main body 11 is suppressed. Moreover, the resin pellet 9 thrown into the storage tank 10 is immediately placed in a dry nitrogen gas atmosphere. Thereby, the moisture absorption of the resin pellet 9 is suppressed.

  When the introduction of the resin pellet 9 is completed, the lid 12 is placed again, and the opening 110 of the storage tank body 11 is closed. Then, the transport blower 42 is operated to generate a nitrogen gas stream in the transport circulation line 40 and the transport pipe 30. If it does so, the resin pellet 9 discharged | emitted from the lower part of the 1st storage tank 10 will be pneumatically conveyed to the conveyance hopper 24 through the conveyance pipe 30 (step S3). At this time, the inside of the transport pipe 30 is filled with positive pressure nitrogen gas. For this reason, moisture absorption of the resin pellet 9 during pneumatic conveyance is suppressed.

  The resin pellets 9 stored in the transport hopper 24 are input into the second storage tank 20 when the input port 231 of the second storage tank 20 is opened. And the drying process of the resin pellet 9 is performed in the inside of the 2nd storage tank 20 (step S4). Specifically, by operating the drying blower 52 and the heater 53, hot air of nitrogen gas is supplied from the outlet 54 into the second storage tank 20. Thereby, moisture evaporates from the resin pellet 9, and the moisture content of the resin pellet 9 falls to a target value.

  When the drying process for a predetermined time is completed, the discharge valve 26 is opened. Thereby, the resin pellet 9 is discharged | emitted from the 2nd storage tank 20 through the discharge pipe 25 to the injection molding machine 2 (step S5). At this time, the temperature of the resin pellet 9 in the discharge pipe 25 is lower than that at the time of drying in step S4. However, the introduction of the nitrogen gas from the second gas introduction unit 70 to the discharge pipe 25 fills the inside of the discharge pipe 25 with the nitrogen gas. For this reason, it is suppressed that a water | moisture content and another gaseous component adsorb | suck to the resin pellet 9 after drying again.

  As described above, in this granular material processing apparatus 1, moisture absorption of the resin pellet 9 is suppressed by supplying nitrogen gas to the first storage tank 10. That is, the initial moisture content of the resin pellet 9 before drying is preliminarily managed. Then, the moisture content of the resin pellet 9 is reduced to a target value by drying the resin pellet 9 in the second storage tank 20. Thereby, the moisture content of the resin pellet 9 is accurately managed while suppressing the influence of the humidity and temperature of the outside air. Moreover, the oxidation of the resin pellet 9 can also be suppressed.

  FIG. 4 is a graph showing an example of a change in the moisture content of the resin pellet 9 when the drying treatment is performed in the second storage tank 20. As shown in FIG. 4, when the drying process proceeds in the second storage tank 20, the moisture content of the resin pellets 9 decreases as the drying time elapses. Therefore, as shown by the curves C1 and C2 in FIG. 4, the resin pellet 9 whose initial moisture content is suppressed can be lowered to the target moisture content P. However, as shown by the curve C3 in FIG. 4, if the initial moisture content is too high, the target moisture content P cannot be reached or an extremely long drying time may be required.

  In this respect, in the granular material processing apparatus 1 of this embodiment, as described above, moisture absorption of the resin pellets 9 before drying can be suppressed in the first storage tank 10. Thereby, the initial moisture content of the resin pellet 9 can be suppressed. Therefore, as shown by curves C1 and C2 in FIG. 4, the moisture content of the resin pellet 9 can be stably reduced to the target moisture content P. That is, since the resin pellet 9 can be always dried at a stable initial moisture content, the moisture content reached after drying can be stabilized.

<3. Modification>
Although one embodiment of the present invention has been described above, the present invention is not limited to the above embodiment.

  In the above embodiment, nitrogen gas is introduced from the first gas introduction unit 60 and the second gas introduction unit 70. However, instead of nitrogen gas, other inert gas such as argon gas may be introduced. Good. Moreover, a 1st gas introduction part and a 2nd gas introduction part may introduce | transduce an inert gas from the inert gas generator installed in the exterior of a granular material processing apparatus.

  Moreover, in said embodiment, although the resin pellet 9 was dried in the 2nd storage tank 20, the 2nd storage tank 20 is processing (for example, stirring, heat retention, etc.) other than drying with respect to the resin pellet 9. ) May be performed. Further, the second storage tank 20 may simply store the resin pellet 9 and discharge it to the subsequent apparatus.

  Moreover, the granular material processing apparatus of this invention may make granular material other than a resin pellet into a process target.

  Moreover, about the detailed structure of a granular material processing apparatus, you may differ from the structure shown by FIG. 1 of this application.

  Moreover, you may combine suitably each element which appeared in said embodiment and modification in the range which does not produce inconsistency.

DESCRIPTION OF SYMBOLS 1 Powder processing apparatus 2 Injection molding machine 9 Resin pellet 10 1st storage tank 11 Storage tank main body 12 Cover part 20 2nd storage tank 24 Conveyance hopper 25 Discharge pipe 26 Discharge valve 30 Conveyance pipe 40 Conveyance circulation line 41 Filter 42 Transport blower 50 Circulation line for drying 51 Filter 52 Drying blower 53 Heater 54 Outlet 60 First gas introduction part 61 Nitrogen gas generator 62 Gas introduction pipe 63 Opening and closing valve 70 Second gas introduction part 71 Nitrogen gas generator 72 Gas introduction pipe 73 On-off valve 80 Control unit

Claims (6)

A first storage tank for storing powder particles;
A transport pipe connecting the first storage tank and the second storage tank located downstream;
An air flow generating means for generating an air flow from the first storage tank to the second storage tank in the transport pipe;
A first gas introduction part for introducing an inert gas into the first storage tank;
The granular material processing apparatus provided with. It is a granular material processing apparatus of Claim 1, Comprising:
The granular material processing apparatus in which the atmospheric pressure in the first storage tank is higher than the external atmospheric pressure by the inert gas introduced from the first gas introduction unit. It is the granular material processing apparatus according to claim 1 or 2,
A circulation line connected to the transfer pipe;
The granular material processing apparatus with which the inert gas introduce | transduced from the said 1st gas introduction part is circulated in the said circulation line. It is the granular material processing apparatus according to any one of claims 1 to 3,
The granular material processing apparatus which further has a drying means to dry the granular material in a said 2nd storage tank. It is the granular material processing apparatus according to any one of claims 1 to 4,
The first storage tank is
A bottomed cylindrical reservoir body having an opening at the top;
A lid for closing the opening of the reservoir body;
Have
The first gas introduction unit is a granular material processing apparatus having a gas introduction pipe connected to the storage tank body. It is the granular material processing apparatus according to any one of claims 1 to 5,
A discharge pipe for discharging the granular material from the second storage tank;
A second gas introduction part for introducing an inert gas into the exhaust pipe;
The granular material processing apparatus further provided.

Images