JP2008155165A - Apparatus for deaerating granular material - Google Patents

Abstract

<P>PROBLEM TO BE SOLVED: To provide an apparatus for deaerating a granular material, in which the amount of the air remaining in the deaerated granular material and the amount of the air to be brought into contact with the granular material at a deaeration step are minimized. <P>SOLUTION: The apparatus 1 for deaerating the granular material is provided with a horizontal deaeration cylinder 2 having: an air chamber 9 closed/surrounded by a filtration cylinder 7 and a casing 8 for surrounding the filtration cylinder 7; a throw-in port fit to one end of the filtration cylinder 7; a discharge port fit to the other end of the filtration cylinder 7; and a horizontal screw conveyer 6 which is arranged to penetrate the inside of the filtration cylinder 7 and used for conveying the granular material from the throw-in port 4 to the discharge port. An inert gas is supplied to the inside of the throw-in port 4 from an inert gas supply port fit to the throw-in port 4 of the apparatus 1 for deaerating the granular material. <P>COPYRIGHT: (C)2008,JPO&INPIT

Description

  The present invention relates to an apparatus for deaeration of a granular material, that is, an apparatus that increases the apparent density of the granular material by deaerating air mixed in the granular material.

  Powders such as foods such as wheat flour and milk powder, and chemical products such as calcium carbonate and carbon black are mixed with a non-negligible amount of air during the manufacturing and processing. The mixed air forms fine gaps between the particles constituting the granular material, and reduces the apparent density of the granular material (that is, increases the apparent bulk).

  In general, the granular material is distributed in a packaging container such as a bag. However, when the bag is packed in a state where air is mixed, it becomes bulky, and the efficiency of transportation and storage deteriorates. In addition, a bag packed in a state where air is mixed easily deforms, and there is a risk of causing a load collapse. In addition, in the case of substances that dislike oxygen, that is, substances that combine with oxygen in the air and oxidize or denature, there is a demand to prevent substances from being exposed to oxygen during transportation and storage.

  Therefore, various devices have been proposed that deaerate the air mixed in the granular material to increase the apparent density of the granular material (decrease the apparent volume).

  For example, in Patent Document 1, an intermediate portion of a horizontally disposed cylindrical main body is used as a porous cylindrical portion, an outer cylinder having an intake / exhaust pipe is provided outside the porous cylindrical portion, and a vacuum exhaust chamber is formed. A screw conveyor for transferring the granular material is inserted inside the cylindrical main body, and deaeration is performed to degas the air mixed in the granular material while the granular material is transferred from one end of the cylindrical main body to the other end. An air device is disclosed.

  In addition, Patent Document 2 includes an inlet above a vertically disposed cylindrical main body, a vacuum exhaust chamber composed of a porous cylindrical portion and an outer cylinder at an intermediate portion of the cylindrical main body, and a cylindrical main body. A screw conveyor for transferring powder is inserted inside, and the powder injected into the inlet is deaerated while passing through the inside of the cylindrical main body. A granular material filling device discharged and filled is disclosed.

Japanese Patent Publication No. 7-47120 JP 11-348903 A

  Since the invention disclosed in Patent Document 1 includes a sintered body of fine metal fibers in the porous cylindrical portion, it effectively prevents leakage to the vacuum side of the granular material and has a high filtration efficiency. Is realized. The invention disclosed in Patent Document 2 includes a packaging container holding device and an elevating device below the cylindrical main body, and gradually lowers the holding height of the packaging container as the number of powder particles in the packaging container increases. As a result, when the granular material falls to the bottom of the packaging container in the lower position, there is no inconvenience that the granular material that has been degassed and crushed is crushed and air is mixed into the granular material again. .

  However, since the devices disclosed in Patent Document 1 and Patent Document 2 perform a deaeration process in an air atmosphere, there is a problem in that some air remains inside the granular material. Moreover, since deaeration is performed while transferring the granular material by a screw conveyor, there is also a problem that the granular material is stirred together with air during the deaeration process. In particular, in the case of substances that dislike oxygen, the deterioration in quality caused by the air remaining after deaeration and the air stirred together during the deaeration process cannot be ignored.

  Moreover, since the apparatus disclosed by patent document 1 has arrange | positioned the cylindrical main body in the horizontal direction, there exists a problem that an installation area becomes large.

  On the other hand, since the apparatus disclosed in Patent Document 2 has a cylindrical main body arranged in the vertical direction, the floor area of the installation place is reduced, but the position of the input port is increased, so that the granular material can be input. It can be difficult. In order to solve this problem, a scaffold for the worker to stand around the entrance is installed. Or measures, such as installing the apparatus which lifts a granular material to an insertion port by an electric power, are needed, and if those apparatuses are included, the installation area of the whole apparatus will become large.

  The present invention has been made to solve these problems, and minimizes the amount of air remaining in the granular material after deaeration and the amount of air that contacts the granular material during the deaeration process. The present invention provides a deaeration device for a granular material. Moreover, the granular material deaeration apparatus which minimizes an installation floor area and installation height is provided.

  The first configuration of the granular material deaeration apparatus of the present invention is a gas chamber enclosed by a cylindrical body formed of a filter body and a casing surrounding the cylindrical body; the air chamber attached to the casing; An exhaust port for discharging the gas; a granular material supply port attached to one end of the cylindrical body; a granular material discharge port attached to the other end of the cylindrical body; and an inside of the cylindrical body In a degassing device for a granular material having a decylinder having a screw conveyor for transferring the granular material from the granular material supply port toward the granular material discharge port, the granular material is attached to the granular material supply port. An inert gas supply port that supplies an inert gas to the inside of the granular material supply port is provided.

  According to this configuration, since the inert gas is blown from the inert gas supply port provided in the powder and granular material supply port, and the air in the granular material is replaced with the inert gas, all subsequent processes are inert. Performed in a gas atmosphere. For this reason, it is possible to minimize the amount of air remaining in the granular material after deaeration and the air stirred together with the granular material during the deaeration process.

  The inert gas is a generic name for chemically inert gases such as nitrogen, argon, carbon dioxide, etc., but in the present invention, only gases that are difficult to cause a chemical reaction with the granular material to be treated are used. The gas which suppresses the biochemical change (for example, fermentation and decay) of the granular material to be processed is also included in the category of the inert gas. That is, in this invention, the gas suitable for preservation | save of the granular material of a process target can be selected suitably, and can be used.

  A second configuration of the granular material degassing apparatus of the present invention is a gas chamber enclosed by a cylindrical body formed of a filter body and a casing surrounding the cylindrical body; the air chamber attached to the casing An exhaust port for discharging the gas; a granular material supply port attached to one end of the cylindrical body; a granular material discharge port attached to the other end of the cylindrical body; and an inside of the cylindrical body In the deaeration device for a granular material, which includes a decylinder having a screw conveyor for transferring the granular material from the granular material supply port toward the granular material discharge port, the air chamber is moved in the direction in which the granular material is transferred. A plurality of air chambers are formed, and the air chambers are attached to one air chamber closer to the granular material supply port than the other air chambers, and are not in the air chambers. An inert gas supply port for supplying an active gas is provided.

  According to this configuration, since the inert gas is supplied to one of the plurality of air chambers that is closer to the granular material supply port than the other air chambers, Substitution with inert gas followed by degassing. For this reason, it is possible to minimize the amount of air remaining in the granular material after deaeration and the air stirred together with the granular material during the deaeration process.

  In addition to the second configuration, the third configuration of the granular material degassing apparatus of the present invention divides the air chamber in the direction in which the granular material is transferred, and three air chambers (the granular material) The front chamber, the middle chamber, and the rear chamber are formed from the side close to the supply port.

  According to this structure, since the said air chamber was divided into three chambers, the order and frequency | count of the process of substituting air with an inert gas, and a deaeration process are changed suitably according to the property of the granular material to be processed. be able to.

  In addition to the third configuration, a fourth configuration of the granular material degassing apparatus of the present invention includes the inert gas supply port in the front chamber and the middle chamber, and the exhaust port in the rear chamber. It is characterized by having each.

  According to this configuration, since the process of replacing air with the inert gas is repeated in the front chamber and the middle chamber, the air mixed in the granular material can be sufficiently replaced with the inert gas.

In addition to the third configuration, the fifth configuration of the granular material degassing apparatus of the present invention includes the exhaust port in the front chamber, the inert gas supply port in the middle chamber, and the rear chamber. Each of which has an exhaust port.

  According to this configuration, after the air mixed in the granular material is degassed in the front chamber, the granular material and the inert gas are mixed in the middle chamber, and again deaerated in the rear chamber and mixed in the granular material. Since the inert gas is removed, almost no air remains in the granular material.

  In addition to the third configuration, the sixth configuration of the granular material degassing apparatus of the present invention includes the inert gas supply port in the front chamber, the exhaust port in the middle chamber, and the rear chamber. Each of which has an inert gas supply port.

  According to this configuration, the air mixed in the granular material in the front chamber is replaced with the inert gas, and the inert gas mixed in the granular material is deaerated in the middle chamber, and then the inert gas is blown in the rear chamber. Therefore, the granular material is discharged from the granular material discharge port together with the inert gas. Therefore, since the powder and inert gas are filled together in the packaging container, the preservability of the powder is improved.

  A seventh configuration of the granular material degassing apparatus of the present invention includes a cylindrical body formed of a filter body and an air chamber enclosed by a casing surrounding the cylindrical body; the air chamber attached to the casing and the air chamber An exhaust port for discharging the gas; a granular material supply port attached to one end of the cylindrical body; a granular material discharge port attached to the other end of the cylindrical body; and an inside of the cylindrical body In a degassing apparatus for a granular material having a decylinder having a screw conveyor that transfers the granular material from the granular material supply port toward the granular material discharge port, the first degassing device arranged in the lateral direction A cylinder and a second decylinder arranged in the saddle direction, and the granular material discharge port of the first decylinder communicates with the granular material supply port of the second decylinder, and The first decylinder cylinder is attached to the granular material supply port of the first decylinder. Characterized in that it comprises an inert gas supply port for supplying the internal inert gas serial granular material supply port.

  According to this configuration, since the deaeration device is configured with the first decylinder arranged in the lateral direction and the second decylinder arranged in the vertical direction, the installation area and the installation height of the deaeration device can be reduced. Can be minimized.

  In addition, since the inert gas supply port is provided in the granular material supply port of the first decylinder so that the inert gas is supplied into the granular material supply port, the granular material is removed from the first degassing cylinder. Before entering the inside of the cylinder of the cylinder, the air mixed in the granular material can be replaced with an inert gas.

  The “lateral direction” and the “heel direction” are not limited to the horizontal direction and the vertical direction. For example, if the first decylinder is disposed obliquely so that the powder supply port is lower than the powder discharge port, the powder can be easily introduced into the powder supply port.

  An eighth configuration of the granular material deaeration device of the present invention includes a cylindrical body formed of a filter body and an air chamber enclosed by a casing surrounding the cylindrical body; the air chamber attached to the casing and the air chamber An exhaust port for discharging the gas; a granular material supply port attached to one end of the cylindrical body; a granular material discharge port attached to the other end of the cylindrical body; and an inside of the cylindrical body In a degassing apparatus for a granular material having a decylinder having a screw conveyor that transfers the granular material from the granular material supply port toward the granular material discharge port, the first degassing device arranged in the lateral direction A cylinder and a second de-cylinder arranged in the saddle direction, and the first-stage de-cylinder discharge port of the first-stage de-cylinder communicates with the second-stage de-cylinder supply port, and The first de-cylinder is inactivated inside the first de-cylinder instead of the exhaust port. Characterized in that it comprises an inert gas supply port for supplying gas

  According to this configuration, the replacement of the air in the granular material with the inert gas and the degassing of the replaced inert gas are performed by separate decylinders, so that the efficiency of the replacement and degassing is improved.

  In addition to the seventh or eighth configuration, the ninth configuration of the granular material deaeration device of the present invention includes the rotational drive device for the screw conveyor at one end of the first decylinder and the other end. A rotary bearing is provided, and the screw conveyor is supported at both ends by the rotary drive device and the rotary bearing, and the powder supply port and the powder discharge port of the first de-cylinder are driven to rotate. It is arranged between the device and the rotary bearing

  According to this configuration, since the rotation driving device and the rotary bearing are arranged outside the conveying path of the powder particles by the screw conveyor, there is no bearing in the middle of the conveying path of the powder particles. Therefore, it is possible to prevent the granular material from being damaged by the bearing lubricant or the like.

  As described above, according to the present invention, after the air in the granular material is replaced with the inert gas, the inert gas in the granular material is degassed. It is possible to provide an excellent deaeration device capable of minimizing the contact between the powder and air and minimizing the deterioration of the quality of the powder due to the contact with air.

  In addition, since the de-cylinder is divided into a first de-cylinder arranged in the lateral direction and a second de-cylinder arranged in the saddle direction, a compact deaeration device that minimizes the installation area and installation height is provided. can do.

  The best mode for carrying out the present invention will be described below with reference to the drawings.

  FIG. 1 is a structural view of a deaeration device showing a first embodiment of the present invention, FIG. 1 (a) is a front view showing an internal structure with a part cut away, and FIG. It is a left side view. As shown in FIG. 1, the deaeration device 1 is composed of a lateral escape cylinder 2 and a saddle escape cylinder 3, and the lateral escape cylinder 2 is adapted to escape so that the central axes of the lateral escape cylinder 2 and the escape cylinder 3 do not intersect. Arranged behind the cylinder 3.

  An inlet 4 is arranged at the right end of the transverse cylinder 2 and a double cylinder part 5 is arranged at the center. A lateral screw conveyor 6 is installed inside the transverse cylinder 2 and introduced from the inlet 4. The granular material is transferred to the left by the horizontal screw conveyor 6, passes through the double cylinder portion 5, and reaches the left end of the horizontal escape cylinder 2. Further, the side surface at the left end of the horizontal escape cylinder 2 is opened to communicate with the dredging cylinder 3, and the granular material that has reached the left end of the lateral escape cylinder 2 flows into the dripping cylinder 3. A hopper (not shown) is mounted above the insertion port 4.

  The double cylinder portion 5 includes a cylindrical filter cylinder 7 concentrically arranged on the outer periphery of the horizontal screw conveyor 6 and a casing 8 concentrically arranged with the filter cylinder 7. That is, the horizontal screw conveyor 6, the filter cylinder 7 and the casing 8 are arranged concentrically, the filter cylinder 7 surrounds the horizontal screw conveyor 6, and the casing 8 surrounds the filter cylinder 7, and the cylinder between the filter cylinder 7 and the casing 8 is cylindrical. A shaped air chamber 9 is formed. The casing 8 is provided with an inert gas supply port 10.

  The filter cylinder 7 is constituted by a filter body that allows only gas to freely enter and exit while retaining the powder particles therein, and the filter body 7 has a metal fiber in a web shape, a net shape, or a woven shape. Use sintered material. In addition, since the detailed structure of the sintered compact of a metal fiber is disclosed by patent document 1 and patent document 2, description is abbreviate | omitted.

  A lateral drive motor 11 that rotationally drives the lateral screw conveyor 6 is installed at the rightmost end of the lateral escape cylinder 2, and a bearing 12 that rotationally supports the rotational shaft of the lateral screw conveyor 6 is installed at the leftmost end. . That is, the horizontal screw conveyor 6 is rotatably supported at both ends, and an intermediate bearing or the like for rotating and supporting the horizontal screw conveyor 6 is not disposed in the middle (that is, in the middle of the powder particle transfer path). A reverse blade 13 is attached to the left end of the horizontal screw conveyor 6. The reverse blade 13 is a screw blade having a pitch opposite to that of the main screw blade of the horizontal screw conveyor 6. Work to push back in the direction.

  A soot drive motor 14 is arranged at the top end of the soot-cylinder 3 and a double cylinder portion 15 is arranged at the bottom of the soot-cylinder 3, and the bottom end of the soot-off cylinder 3 is opened to An outlet 16 is formed. In addition, a soot screw conveyor 17 that is rotationally driven by a soot drive motor 14 is installed inside the soot removal cylinder 3, and the powder particles that have flowed into the scissor removal cylinder 3 from the side escape cylinder 2 are sent by the soot screw conveyor 17. It is transported downward, passes through the double cylinder portion 15, and is discharged to the outside from the soot discharge port 16.

  The double cylinder portion 15 includes a filter cylinder 18 disposed concentrically on the outer periphery of the rod screw conveyor 17 and a casing 19 disposed concentrically on the outer periphery of the filter cylinder 18. That is, the dredging screw conveyor 17, the filtering cylinder 18 and the casing 19 are arranged concentrically, the filtering cylinder 18 surrounds the dredging screw conveyor 17, and the casing 19 surrounds the filtering cylinder 18, and a cylinder is interposed between the filtering cylinder 18 and the casing 19. A shaped air chamber 20 is formed. The casing 19 is provided with an exhaust port 21.

  The filter cylinder 18 is configured by a filter body that allows only gas to freely enter and exit while retaining the granular material in the same manner as the filter cylinder 7. Or what was sintered as a textile form is used.

Here, an operation method of the deaeration device 1 will be described.
First, the exhaust port 21 is connected to a vacuum pump (not shown) to suck and exhaust the air in the air chamber 20, and the inert gas supply port 10 is connected to a nitrogen gas supply source (not shown) (for example, a high-pressure cylinder filled with liquefied nitrogen gas). Connect to. Nitrogen gas that has flowed into the air chamber 9 from the inert gas supply port 10 flows into the space inside the filter cylinder 7, and the double cylinder portion 5 is filled with nitrogen gas. Moreover, the horizontal drive motor 11 and the saddle drive motor 14 are started, and the horizontal screw conveyor 6 and the saddle screw conveyor 17 are rotated.

  Next, when the granular material to be treated is introduced from the inlet 4, the granular material is transferred to the left by the horizontal screw conveyor 6 and enters the double cylindrical portion 5. Since the double cylinder part 5 is filled with nitrogen gas supplied from the inert gas supply port 10, the air mixed in the granular material is replaced with nitrogen gas. The powder and nitrogen gas mixture thus obtained is further transferred leftward by the horizontal screw conveyor 6 and reaches the left end of the horizontal escape cylinder 2. The mixture that has reached the left end is pressed in the left direction by the horizontal screw conveyor 6 and is also pressed in the right direction by the reverse vane 13, loses its destination, and flows into the unsealed cylinder 3.

  The mixture that has entered inside the evacuation cylinder 3 is transferred downward by the heel screw conveyor 17 and reaches the double cylinder portion 15. At this time, since the air chamber 20 is evacuated by the vacuum pump connected to the exhaust port 21, the nitrogen gas mixed in the powder is discharged through the filter cylinder 18 and the exhaust port 21. .

  In this way, the air mixed in the granular material charged from the charging port 4 is replaced with nitrogen gas in the double cylinder portion 5 of the transverse escape cylinder 2, and the nitrogen gas is removed from the exhaust cylinder 32. The granular material deaerated by the heavy cylinder portion 15 is discharged from the soot discharge port 16. As described above, since the air in the double cylinder part 5 and the double cylinder part 15 is replaced with nitrogen gas, most of the gas that remains slightly in the granular material discharged from the soot discharge port 16 Is nitrogen gas, leaving almost no air (oxygen).

  In the present embodiment, an example in which the present invention is implemented as a single deaeration device has been described. However, a dam plate, a container holding device, a lifting device, and a load cell as disclosed in Patent Document 2 are provided below the soot discharge port 16. Etc., and a deaeration / filling device for quantitatively filling the powder containers into the packaging container.

  Moreover, when the apparatus of this invention comprises a part of deaeration and filling apparatus, in order to replace | exchange a packaging container, it is necessary to stop discharge | emission of the granular material from the soot discharge port 16 temporarily. In such a case, the operation of the horizontal screw conveyor 6 and the saddle screw conveyor 17 is stopped, but the operation of the vacuum pump connected to the exhaust port 21 is continued. In this way, the powder particles are held in the soot removal cylinder 3 by the negative pressure generated by the operation of the vacuum pump and do not fall from the soot discharge port 16. In addition, since the soot discharge port 16 is blocked by the powder particles, external air and dust do not enter the inside of the soot removal cylinder 3.

  In this embodiment, nitrogen gas is shown as an example of the inert gas, but the inert gas used in the present invention is not limited to nitrogen gas. A gas suitable for preserving the granular material to be treated can be appropriately selected and used.

  Further, in this embodiment, the example in which the inert gas supply port 10 is provided in the casing 8 of the double cylinder portion 5 of the transverse escape cylinder 2 has been shown, but the installation location of the inert gas supply port 10 is limited to this. It is not a thing. For example, if it is provided inside the inlet 4 and the inside of the inlet 4 is filled with an inert gas, all processes of deaeration of the granular material by the deaerator 1 are performed in an inert gas atmosphere. As a result, the chances of the powder particles coming into contact with air are further reduced. In this case, the inert gas supply port 10 provided in the casing 8 of the double cylinder portion 5 of the transverse cylinder 2 is connected to a vacuum pump so that both the lateral cylinder 2 and the cylinder 3 are deaerated. You may make it perform.

  FIG. 2 is a cross-sectional view of a double cylinder portion of a deaeration device showing a second embodiment of the present invention. As shown in the figure, the double cylinder portion 31 is composed of a filter cylinder 32 and a casing 33, and includes a cylindrical air chamber 34 between the filter cylinder 32 and the casing 33. Although common to the heavy cylinder portions 5 and 15, the air chamber 34 is divided by a partition wall 35, and is different in that it is divided into three chambers: a front chamber 34a, a middle chamber 34b, and a rear chamber 34c.

  The front chamber 34a, the middle chamber 34b, and the rear chamber 34c are provided with a front chamber intake / exhaust port 36a, a middle chamber intake / exhaust port 36b, and a rear chamber intake / exhaust port 36c, respectively. In FIG. 2, only two of the front chamber intake / exhaust ports 36 a are visible, but three are arranged on the same circumference of the outer periphery of the casing 33.

  A hopper 37 is attached to the upper end of the double cylinder part 31, and the lower end of the double cylinder part 31 is opened to form a discharge port 38.

  Either a vacuum pump or an inert gas supply source can be selected and connected to the front chamber intake / exhaust port 36a, the middle chamber intake / exhaust port 36b, and the rear chamber intake / exhaust port 36c. For example, if the front chamber intake / exhaust port 36a is connected to a vacuum pump, the front chamber intake / exhaust port 36a functions as an exhaust port, so the air in the granular material introduced from the hopper 37 passes through the front chamber 34a. Discharged. Similarly, if an inert gas supply source is connected to the middle chamber intake / exhaust port 36b and a vacuum pump is connected to the rear chamber intake / exhaust port 36c, the particulates are blown with inert gas when passing by the side of the middle chamber 34b. Then, it is deaerated again when it passes by the rear chamber 34c. That is, in this case, processing is performed in the order of degassing-inert gas supply (replacement) -degassing, and finally the gas is discharged from the discharge port 38.

  The selection of whether a vacuum pump or an inert gas supply source is connected to the front chamber intake / exhaust port 36a, in other words, the selection of the deaeration process and the process of replacing air with an inert gas, This is done according to the physical properties of the body. For example, various sequences such as degassing-substitution-degassing, substitution-degassing-degassing, substitution-degassing-substitution can be selected.

  In addition, it seems that supplying inert gas again after deaeration, such as substitution-deaeration-substitution, contradicts the original function of the deaeration device. This sequence is selected when it is desired to positively fill the container with an inert gas.

1 is a structural diagram of a deaeration device showing a first embodiment of the present invention. It is sectional drawing of the double cylinder part of the deaeration apparatus which shows the 2nd Example of this invention.

Explanation of symbols

DESCRIPTION OF SYMBOLS 1 Deaeration device 2 Horizontal de-cylinder 3 竪 De-cylinder 4 Input port 5 Double cylinder part 6 Horizontal screw conveyor 7 Filter cylinder 8 Casing 9 Air chamber 10 Inert gas supply port 11 Horizontal drive motor 12 Bearing 13 Reverse blade 14 竪 drive Electric motor 15 Double cylinder portion 16 竪 discharge port 17 竪 screw conveyor 18 filter cylinder 19 casing 20 air chamber 21 exhaust port 31 double cylinder portion 32 filter cylinder 33 casing 34 air chamber 34a front chamber 34b middle chamber 34c rear chamber 35 partition 36a Front chamber intake / exhaust port 36b Middle chamber intake / exhaust port 36c Rear chamber intake / exhaust port 37 Hopper 38 Discharge port

Claims (9)

An air chamber enclosed by a cylindrical body formed of a filter body and a casing surrounding the cylindrical body;
An exhaust port which is attached to the casing and discharges gas in the air chamber;
A granular material supply port attached to one end of the cylindrical body;
Powder outlet attached to the other end of the cylindrical body;
And in the deaeration device of a granular material provided with the decylinder which has a screw conveyor which penetrates the inside of the above-mentioned cylindrical body, and transfers a granular material from the above-mentioned granular material supply port toward the above-mentioned granular material discharge port ,
An apparatus for degassing a granular material, comprising an inert gas supply port that is attached to the granular material supply port and supplies an inert gas into the granular material supply port. An air chamber enclosed by a cylindrical body formed of a filter body and a casing surrounding the cylindrical body;
An exhaust port which is attached to the casing and discharges gas in the air chamber;
A granular material supply port attached to one end of the cylindrical body;
Powder outlet attached to the other end of the cylindrical body;
And in the deaeration device of a granular material provided with the decylinder which has a screw conveyor which penetrates the inside of the above-mentioned cylindrical body, and transfers a granular material from the above-mentioned granular material supply port toward the above-mentioned granular material discharge port ,
While dividing the air chamber in the transfer direction of the granular material to form a plurality of air chambers,
Among the plurality of air chambers, there is provided an inert gas supply port that is attached to one air chamber that is closer to the granular material supply port than the other air chambers and supplies an inert gas into the air chamber. A degassing device for a granular material. The air chamber is divided in the direction in which the granular material is transferred to form three air chambers (referred to as the front chamber, the middle chamber, and the rear chamber from the side close to the powder supply port). A deaerator for a granular material according to claim 2. 4. The granular material deaeration apparatus according to claim 3, wherein the inert gas supply port is provided in the front chamber and the middle chamber, and the exhaust port is provided in the rear chamber. 4. The granular material deaeration apparatus according to claim 3, wherein the front chamber includes the exhaust port, the middle chamber includes the inert gas supply port, and the rear chamber includes the exhaust port. The granular material deaeration apparatus according to claim 3, wherein the front chamber includes the inert gas supply port, the middle chamber includes the exhaust port, and the rear chamber includes the inert gas supply port. . An air chamber enclosed by a cylindrical body formed of a filter body and a casing surrounding the cylindrical body;
An exhaust port which is attached to the casing and discharges gas in the air chamber;
A granular material supply port attached to one end of the cylindrical body;
Powder outlet attached to the other end of the cylindrical body;
And a degassing device for a granular material comprising a decylinder having a screw conveyor that penetrates the cylindrical body and transfers the granular material from the granular material supply port toward the granular material discharge port. ,
A first de-cylinder arranged laterally;
A second decylinder arranged in the saddle direction;
The granular material discharge port of the first decylinder communicates with the granular material supply port of the second decylinder and is attached to the granular material supply port of the first decylinder. An apparatus for degassing a granular material, comprising an inert gas supply port for supplying an inert gas into the granular material supply port of one decylinder. An air chamber enclosed by a cylindrical body formed of a filter body and a casing surrounding the cylindrical body;
An exhaust port which is attached to the casing and discharges gas in the air chamber;
A granular material supply port attached to one end of the cylindrical body;
Powder outlet attached to the other end of the cylindrical body;
And a degassing device for a granular material comprising a decylinder having a screw conveyor that penetrates the cylindrical body and transfers the granular material from the granular material supply port toward the granular material discharge port. ,
A first de-cylinder arranged laterally;
A second decylinder arranged in the saddle direction,
The first decylinder is provided with an inert gas supply port for supplying an inert gas to the inside of the first decylinder instead of the exhaust port. A rotary drive device for the screw conveyor is provided at one end of the first decylinder, a rotary bearing is provided at the other end, and the screw conveyor is supported at both ends by the rotary drive device and the rotary bearing.
The said granular material supply port and said granular material discharge port of a said 1st decylinder are arrange | positioned between the said rotation drive device and the said rotary bearing, The Claim 7 or Claim 8 characterized by the above-mentioned. Powder deaerator.

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