JPH0450258Y2 - - Google Patents
Info
- Publication number
- JPH0450258Y2 JPH0450258Y2 JP11833787U JP11833787U JPH0450258Y2 JP H0450258 Y2 JPH0450258 Y2 JP H0450258Y2 JP 11833787 U JP11833787 U JP 11833787U JP 11833787 U JP11833787 U JP 11833787U JP H0450258 Y2 JPH0450258 Y2 JP H0450258Y2
- Authority
- JP
- Japan
- Prior art keywords
- tank
- suction
- path
- powder
- valve
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired
Links
- 239000000843 powder Substances 0.000 claims description 27
- 239000008187 granular material Substances 0.000 claims description 25
- 238000004891 communication Methods 0.000 claims description 21
- 238000000034 method Methods 0.000 description 10
- 239000008188 pellet Substances 0.000 description 9
- 229920003002 synthetic resin Polymers 0.000 description 9
- 239000000057 synthetic resin Substances 0.000 description 9
- 238000013459 approach Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
Landscapes
- Air Transport Of Granular Materials (AREA)
Description
【考案の詳細な説明】
〔産業上の利用分野〕
本考案は粉体や粒体等を空気搬送するために用
いられる搬送装置に関するものである。[Detailed Description of the Invention] [Industrial Application Field] The present invention relates to a conveying device used for pneumatically conveying powder, granules, and the like.
空気搬送には圧送方式と吸引方式とがあり、圧
送方式はコンプレツサー等で圧縮した空気を搬送
径路の送り出し側から送り先側に送り込み粉体や
粒体を送り出し側から送り先側に圧送する方式で
あり、吸引方式は送り先側に吸引ブロワ等を連絡
して搬送径路の送り出し側から送り先側へ粉体や
粒体を吸引する方式である。しかし圧送方式にお
いては空気は圧縮により加熱されるので合成樹脂
粒体(ペレツト)のような加熱により軟化して相
互粘着するような耐熱性のない粉体や粒体の搬送
には空気吸引方式が採用される。
There are two types of pneumatic conveyance: a pressure-feeding method and a suction method.The pressure-feeding method is a method in which air compressed by a compressor, etc. is sent from the sending side of the conveying path to the destination side, and powder and granules are forced from the sending side to the destination side. The suction method is a method in which a suction blower or the like is connected to the destination side to suck powder or granules from the sending side of the conveyance path to the destination side. However, in the pressure feeding method, the air is heated by compression, so the air suction method is used to transport non-heat resistant powders and granules that soften and stick together when heated, such as synthetic resin pellets. Adopted.
従来の吸引方式においては第2図に示すように
タンク1に吸引口2、吸引径路3、および排出シ
ユート5に連絡する連絡径路4を連絡し、該吸引
径路3にはバルブ6が介在し、かつバルブ8を付
した大気導入口7が連絡し、そして空気吸引ブロ
ワ9が連絡しており、連絡径路4の出口にはダン
パー10が取付けられている。そしてバルブ6を
開いて空気吸引ブロワ9により吸引径路3を介し
てタンク1内に吸引口2から粉体または粒体を吸
引し、タンク1内に粉体または粒体が一杯になつ
たらバルブ6を閉じて粉体または粒体の吸引を停
止し、バルブ8を開いて大気導入口7から吸引径
路3を介してタンク1内に大気圧を導入し、連絡
径路4のダンパー10を開いてタンク1内の粉体
または粒体を排出シユート5に移動させ、再びダ
ンパー10を閉じてバルブ6を開き、バルブ8を
閉じて空気吸引ブロワ9により吸引径路3を介し
てタンク1内に吸引口2から粉体または粒体を吸
引する。
In the conventional suction method, as shown in FIG. 2, a suction port 2, a suction path 3, and a communication path 4 communicating with a discharge chute 5 are connected to the tank 1, and a valve 6 is interposed in the suction path 3. An air inlet 7 with a valve 8 communicates with it, and an air suction blower 9 communicates with it, and a damper 10 is attached to the outlet of the communication path 4. Then, the valve 6 is opened, and the air suction blower 9 sucks powder or granules into the tank 1 from the suction port 2 through the suction path 3. When the tank 1 is full of powder or granules, the valve 6 is closed to stop the suction of powder or granules, open the valve 8 to introduce atmospheric pressure into the tank 1 from the atmosphere inlet 7 through the suction path 3, and open the damper 10 of the communication path 4 to stop the suction of powder or granules. The powder or granules in 1 are moved to the discharge chute 5, the damper 10 is closed again, the valve 6 is opened, the valve 8 is closed, and the air suction blower 9 blows the suction port 2 into the tank 1 via the suction path 3. Suction of powder or granules from.
このような従来の空気吸引方式では粉体または
粒体の吸引搬送を連続的に行なうことが出来ず、
間欠的に行なつていたので搬送効率が悪くまたバ
ルブ操作等も煩雑なものになつていた。上記タン
クを並列に配置して交互に吸引搬送を行えば連続
的に行なうことも出来るが、この場合には切換バ
ルブ等が必要で構造が複雑になりまたバルブ操作
も一層煩雑なものになる。
With such conventional air suction methods, it is not possible to continuously suction and convey powder or granules.
Since this was done intermittently, the transfer efficiency was poor and valve operations were complicated. It is also possible to carry out the suction and conveyance continuously by arranging the tanks in parallel and alternately carrying out suction and conveyance, but in this case, a switching valve or the like is required, which complicates the structure and makes the valve operation even more complicated.
本考案は上記問題点を解決する手段として、複
数個のタンク11,12を上下に配置し、該複数
個のタンク11,12相互を連絡径路16によつ
て連絡し、該連絡径路16の出口には夫々フリー
ダンパー19をその上端部で枢着し、該複数個の
タンク11,12には夫々空気吸引ブロワ28に
連絡する吸引径路15,17を連絡した粉体もし
くは粒体の搬送装置を提供するものである。
In the present invention, as a means to solve the above-mentioned problems, a plurality of tanks 11 and 12 are arranged one above the other, the plurality of tanks 11 and 12 are connected to each other by a communication path 16, and an exit of the communication path 16 is provided. A free damper 19 is pivotally mounted at the upper end of each of the tanks 11 and 12, and a powder or granule conveying device is connected to the plurality of tanks 11 and 12 with suction paths 15 and 17 connected to an air suction blower 28, respectively. This is what we provide.
最上段のタンク11に吸引径路15を介して空
気吸引ブロワ28によつて粉体または粒体を吸引
する。この時最上段の連絡径路16のフリーダン
パー19は最上段のタンク11を介して吸引径路
15により吸引されて閉じた状態にある。最上段
のタンク11に粉体または粒体が一杯になつたら
二段目のタンク12を吸引径路17を介して空気
吸引ブロワ28によつて吸引すると最上段のタン
ク11と二段目のタンク12の内圧が等しくなり
最上段のタンク11内の粉体または粒体はその重
量により最上段の連絡径路16のフリーダンパー
19を押し開いて二段目のタンク12内に移行す
るがこの場合でも最上段のタンク11には粉体ま
たは粒体が吸引されている。この時二段目の連絡
径路18のフリーダンパー20は最上段のタンク
11および二段目のタンク12を介して吸引径路
17により吸引されて閉じた状態にある。二段目
のタンク12に粉体または粒体が一杯になつたら
二段目のタンク12の吸引径路17による吸引を
停止し該タンク12に大気を導入すると該タンク
12内の粉体または粒体はその重量により二段目
の連絡径路18のフリーダンパー20を押し開い
て三段目のタンク13内に移行する。あるいは二
段目のタンク12の吸引径路17による吸引を続
行したまま三段目のタンク13を吸引径路によつ
て吸引して二段目のタンク12と三段目のタンク
13の内圧を等しくしても二段目のタンク12内
の粉体または粒体はその重量により二段目の連絡
径路18のフリーダンパー20を押し開いて三段
目のタンク13内に移行する。このようにして最
上段のタンク11を常時吸引状態にして粉体また
は粒体を逐次下方のタンクに移送することが出来
る。
Powder or granules are sucked into the uppermost tank 11 through a suction path 15 by an air suction blower 28 . At this time, the free damper 19 of the uppermost communication path 16 is sucked by the suction path 15 via the uppermost tank 11 and is in a closed state. When the top tank 11 is full of powder or granules, the second tank 12 is sucked by the air suction blower 28 through the suction path 17, and the top tank 11 and the second tank 12 are sucked. When the internal pressures of the two tanks become equal, the powder or granules in the top tank 11 pushes open the free damper 19 of the top connection path 16 due to its weight and moves into the second tank 12. Powder or granules are sucked into the upper tank 11. At this time, the free damper 20 of the second-stage communication path 18 is sucked by the suction path 17 via the uppermost tank 11 and the second-stage tank 12, and is in a closed state. When the second stage tank 12 is full of powder or granules, the suction through the suction path 17 of the second stage tank 12 is stopped, and when the atmosphere is introduced into the tank 12, the powder or granules in the tank 12 are removed. The weight pushes open the free damper 20 of the second-stage communication path 18 and moves into the third-stage tank 13. Alternatively, while continuing suction through the suction path 17 of the second-stage tank 12, the third-stage tank 13 is suctioned through the suction path to equalize the internal pressures of the second-stage tank 12 and the third-stage tank 13. Even so, the powder or granules in the second stage tank 12 push open the free damper 20 of the second stage communication path 18 due to its weight and move into the third stage tank 13. In this way, the uppermost tank 11 can be kept in a suction state at all times, and the powder or granules can be sequentially transferred to the lower tanks.
したがつて本考案の搬送装置にあつては粉体ま
たは粒体を連続的に搬送することが出来、またタ
ンクからタンクへの移送も粉体または粒体の重量
によつてフリーダンパーを押し開くことにより行
われるからダンパー開閉機構等も全く不必要であ
り、極めて簡単な構造のものとなる。
Therefore, with the conveying device of the present invention, powder or granules can be conveyed continuously, and the free damper can be pushed open by the weight of the powder or granules when transferring from tank to tank. Since the damper opening/closing mechanism is completely unnecessary, the structure is extremely simple.
本考案を第1図に示す一実施例により説明すれ
ば、11は第1タンクであり最上段に配され、1
2は第2タンクであり二段目に配され、13は排
出シユートであり三段目に配され、第1タンク1
1には吸引口14、第1吸引径路15、および第
1連絡径路16の入口が連絡し、第2タンク12
には該第1連絡径路16の出口、第2吸引径路1
7、および第2連絡径路18の入口が連絡し、排
出シユート13には第2連絡径路18の出口が連
絡し、該第1連絡径路16および第2連絡径路1
8の出口には夫々フリーダンパー19,20の上
端部が枢着されている。また第1タンク11およ
び第2タンク12内の第1吸引径路15および第
2吸引径路17の開口部には金網からなるフイル
ター21,22が夫々取はずし可能に被着されて
いる。第1吸引径路15および第2吸引径路17
は夫々第1バツグフイルタ23および第2バツグ
フイルタ24、第1バルブ25、第2バルブ26
を介して主吸引径路27に合流し、該主吸引径路
27には空気吸引ブロワ28が連絡し、更に第2
吸引径路17には第3バルブ30を付した大気導
入口29が連絡する。
The present invention will be explained with reference to an embodiment shown in FIG.
2 is a second tank, which is placed in the second stage; 13 is a discharge chute, which is placed in the third stage;
The suction port 14, the first suction path 15, and the inlet of the first communication path 16 communicate with the second tank 12.
an outlet of the first communication path 16, and an outlet of the second suction path 1.
7, and the inlet of the second communication path 18 communicate with each other, the outlet of the second communication path 18 communicates with the discharge chute 13, and the first communication path 16 and the second communication path 1 communicate with each other.
The upper ends of free dampers 19 and 20 are pivotally mounted to the outlets of 8, respectively. Further, filters 21 and 22 made of wire mesh are removably attached to the openings of the first suction path 15 and the second suction path 17 in the first tank 11 and the second tank 12, respectively. First suction path 15 and second suction path 17
are the first baggage filter 23, the second baggage filter 24, the first valve 25, and the second valve 26, respectively.
The main suction path 27 is connected to an air suction blower 28, and a second air suction blower 28 is connected to the main suction path 27.
An atmospheric air inlet 29 equipped with a third valve 30 communicates with the suction path 17 .
上記構成において、先ず第1バルブ25を開き
第2バルブ26と第3バルブ30を閉じて空気吸
引ブロワ28を作動させ主吸引径路27、第1吸
引径路15を介して吸引口14から第1タンク1
1内に合成樹脂ペレツトを吸引する。この場合フ
リーダンパー19は第1タンク11を介して吸引
され閉じた状態にある。第1タンク11内に合成
樹脂ペレツトが一杯になつたら第2バルブ26を
開いて主吸引径路27、第2吸引径路17を介し
て第2タンク12内の空気を吸引し、第1タンク
11と第2タンク12とが等圧に近づいた時点で
第1タンク11内の合成樹脂ペレツトはその重量
によりフリーダンパー19を押し開いて第1連絡
径路16を介して第2タンク12へ移行する。こ
の場合フリーダンパー20は第2タンク12を介
して吸引され閉じた状態にある。この時第1バル
ブ25を閉じて第1タンク11内の空気の吸引を
停止してもよい。第1バルブ25を開いたまゝに
しても閉じた場合でも第2タンク12内の空気は
第2吸引径路17によつて吸引されており、フリ
ーダンパー19は開いているから合成樹脂ペレツ
トの第1タンク11への吸引はこの間においても
続行されている。第2タンク12が合成樹脂ペレ
ツトで一杯になつたら、第2バルブ26を閉じて
第2タンク12内の空気の吸引を停止してから第
3バルブ30を開いて大気導入口29から第2吸
引径路17を介して第2タンク12へ大気を導入
する。そして第2タンク12内の合成樹脂ペレツ
トは第2タンク12内が大気圧に近ずいた時点で
その重量により排出シユート13に移行し排出さ
れる。この場合第2バルブ26を閉じた時には第
2タンク12は大気を導入する前に第1バルブ2
5を開いて第1タンク11を吸引する。この状態
ではフリーダンパー19は吸引閉鎖され、合成樹
脂ペレツトの吸引口14から第1タンク11内へ
の吸引は続行される。なお合成樹脂ペレツトが第
1吸引径路15および第2吸引径路17へ吸引さ
れることはフイルター21,22により防止さ
れ、合成樹脂ペレツトに付着している微粉がフイ
ルター21,22を通過し第1吸引径路15およ
び第2吸引径路17へ吸引され、更に主吸引径路
27を介して空気吸引ブロワ28に吸引されるこ
とは第1バツグフイルタ23および第2バツグフ
イルタ24により防止される。なお微粉が存在し
ない場合にはバツグフイルタは不要になる。 In the above configuration, first, the first valve 25 is opened, the second valve 26 and the third valve 30 are closed, and the air suction blower 28 is operated to pass from the suction port 14 to the first tank via the main suction path 27 and the first suction path 15. 1
The synthetic resin pellets are sucked into the container. In this case, the free damper 19 is sucked through the first tank 11 and is in a closed state. When the first tank 11 is full of synthetic resin pellets, the second valve 26 is opened and the air in the second tank 12 is sucked through the main suction path 27 and the second suction path 17, and the first tank 11 and When the pressure of the first tank 11 approaches the same as that of the second tank 12, the synthetic resin pellets in the first tank 11 push open the free damper 19 due to its weight and transfer to the second tank 12 via the first communication path 16. In this case, the free damper 20 is sucked through the second tank 12 and is in a closed state. At this time, the first valve 25 may be closed to stop suction of the air in the first tank 11. Whether the first valve 25 is left open or closed, the air in the second tank 12 is sucked through the second suction path 17, and since the free damper 19 is open, the first Suction into the tank 11 continues during this time as well. When the second tank 12 is full of synthetic resin pellets, close the second valve 26 to stop sucking the air in the second tank 12, and then open the third valve 30 to start the second suction from the air inlet 29. Atmospheric air is introduced into the second tank 12 via the path 17. When the pressure inside the second tank 12 approaches atmospheric pressure, the synthetic resin pellets in the second tank 12 are transferred to the discharge chute 13 due to their weight and are discharged. In this case, when the second valve 26 is closed, the second tank 12 closes the first valve 26 before introducing the atmosphere.
5 and suck the first tank 11. In this state, the free damper 19 is closed by suction, and the suction of the synthetic resin pellets from the suction port 14 into the first tank 11 continues. Note that the synthetic resin pellets are prevented from being sucked into the first suction path 15 and the second suction path 17 by the filters 21 and 22, and the fine powder adhering to the synthetic resin pellets passes through the filters 21 and 22 and is sucked into the first suction path 15 and the second suction path 17. The first bag filter 23 and the second bag filter 24 prevent the air from being sucked into the path 15 and the second suction path 17 and further into the air suction blower 28 via the main suction path 27 . Note that if there is no fine powder, the bag filter is not necessary.
上記したように粉体または粒体が第1タンクか
ら第2タンクに移行する間、第2タンクから排出
シユートに移行する間も粉体または粒体の第1タ
ンクへの吸引は断続することなく行われる。 As mentioned above, while the powder or granules are transferred from the first tank to the second tank or from the second tank to the discharge chute, the suction of the powder or granules to the first tank is not interrupted. It will be done.
本実施例以外、タンクは三個以上配置してもよ
い。 Other than this embodiment, three or more tanks may be arranged.
第1図は本考案の一実施例の系統図、第2図は
従来例の説明図である。
図中、11……第1タンク、12……第2タン
ク、13……排出シユート、14……吸引口、1
5……第1吸引径路、16……第1連絡径路、1
7……第2吸引径路、18……第2連絡径路、1
9,20……フリーダンパー、25……第1バル
ブ、26……第2バルブ、27……主吸引径路、
28……空気吸引ブロワ、29……大気導入口、
30……第3バルブ。
FIG. 1 is a system diagram of an embodiment of the present invention, and FIG. 2 is an explanatory diagram of a conventional example. In the figure, 11...first tank, 12...second tank, 13...discharge chute, 14...suction port, 1
5...First suction path, 16...First communication path, 1
7...Second suction path, 18...Second communication path, 1
9, 20...Free damper, 25...First valve, 26...Second valve, 27...Main suction path,
28...Air suction blower, 29...Atmospheric inlet,
30...Third valve.
Claims (1)
ンク相互を連絡径路によつて連絡し、該連絡径路
の出口には夫々フリーダンパーをその上端部で枢
着し、該複数個のタンクには夫々空気吸引ブロワ
に連絡する吸引径路を連絡したことを特徴とする
粉体もしくは粒体の搬送装置。 A plurality of tanks are arranged one above the other, the plurality of tanks are connected to each other by a communication path, and a free damper is pivotally mounted at the upper end of each outlet of the communication path, and the plurality of tanks are connected to each other by a communication path. A conveying device for powder or granules, characterized in that each suction path is connected to an air suction blower.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11833787U JPH0450258Y2 (en) | 1987-07-31 | 1987-07-31 |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP11833787U JPH0450258Y2 (en) | 1987-07-31 | 1987-07-31 |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| JPS6424032U JPS6424032U (en) | 1989-02-09 |
| JPH0450258Y2 true JPH0450258Y2 (en) | 1992-11-26 |
Family
ID=31362604
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP11833787U Expired JPH0450258Y2 (en) | 1987-07-31 | 1987-07-31 |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0450258Y2 (en) |
Families Citing this family (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP4158009B2 (en) * | 2001-12-11 | 2008-10-01 | 信越化学工業株式会社 | Synthetic quartz glass ingot and method for producing synthetic quartz glass |
-
1987
- 1987-07-31 JP JP11833787U patent/JPH0450258Y2/ja not_active Expired
Also Published As
| Publication number | Publication date |
|---|---|
| JPS6424032U (en) | 1989-02-09 |
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