JPS5925782Y2 - Blow tank type pneumatic transport device - Google Patents

Blow tank type pneumatic transport device

Info

Publication number
JPS5925782Y2
JPS5925782Y2 JP1977175774U JP17577477U JPS5925782Y2 JP S5925782 Y2 JPS5925782 Y2 JP S5925782Y2 JP 1977175774 U JP1977175774 U JP 1977175774U JP 17577477 U JP17577477 U JP 17577477U JP S5925782 Y2 JPS5925782 Y2 JP S5925782Y2
Authority
JP
Japan
Prior art keywords
tank
powder
valve
pipe
pressure
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
Application number
JP1977175774U
Other languages
Japanese (ja)
Other versions
JPS54101792U (en
Inventor
三夫 笠井
Original Assignee
宇部興産株式会社
Priority date (The priority date 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 date listed.)
Filing date
Publication date
Application filed by 宇部興産株式会社 filed Critical 宇部興産株式会社
Priority to JP1977175774U priority Critical patent/JPS5925782Y2/en
Publication of JPS54101792U publication Critical patent/JPS54101792U/ja
Application granted granted Critical
Publication of JPS5925782Y2 publication Critical patent/JPS5925782Y2/en
Expired legal-status Critical Current

Links

Landscapes

  • Air Transport Of Granular Materials (AREA)

Description

【考案の詳細な説明】 この考案は、粉体を連続的に輸送し、輸送効率を増大さ
せうるようにしたブロータンク式空気輸送装置に関する
ものである。
[Detailed Description of the Invention] This invention relates to a blow tank type pneumatic transport device that can continuously transport powder and increase transport efficiency.

従来より、粉体輸送用のブロータンク式空気輸送装置と
しては、粉体受人槽の中間部から粉体を送出すフラクソ
式のものと、粉体受人槽の下部から粉体を送出すセラ一
式のものとが用いられているが、従来の空気輸送装置は
、バッチ運転で、1バツチ終了毎にタンク内の空気を輸
送配管を通して抜いていたため、輸送配管の効率は、相
当管長300m程度で、セメント輸送の場合は80〜8
5%、石灰石粉輸送の場合は70〜80%と低く、輸送
距離が長くなる程、その輸送効率はさらに低下していた
Traditionally, blow tank type pneumatic transport devices for transporting powder have been divided into two types: one is a flux type that sends out powder from the middle part of the powder receiving tank, and the other is a flux type that sends out powder from the bottom of the powder receiving tank. However, conventional pneumatic transport equipment operates in batches, and the air in the tank is removed through the transport piping after each batch, so the efficiency of the transport piping is limited to an equivalent pipe length of about 300 m. In the case of cement transportation, it is 80 to 8.
5%, and in the case of limestone powder transportation, it was as low as 70 to 80%, and the longer the transportation distance, the further the transportation efficiency decreased.

すなわち、従来のセラ一式のブロータンク式空気輸送装
置では、第1図に示すように、第1槽1と第2槽1aの
各下部および各側部に、それぞれ別個の開閉弁2. 2
a、 3. 3aを介して圧縮空気源4と連結した空
気供給管5. 5a、 6. 6aを取付け、第1槽
と第2槽1aの両方の粉体送出管7,7aを切替弁8を
介して途中で交わらせた後に1本の粉体輸送管9でサイ
ロ10に連結していた。
That is, in the conventional blow tank type pneumatic transport device with a cellar set, as shown in FIG. 1, separate on-off valves 2. 2
a.3. An air supply pipe 5 connected to a compressed air source 4 via 3a. 5a, 6. 6a, and the powder delivery pipes 7, 7a of both the first tank and the second tank 1a are crossed in the middle via a switching valve 8, and then connected to the silo 10 with one powder transport pipe 9. Ta.

11.113はそれぞれ第1槽1と第2槽1aの頂部の
粉体受入口12.12a部に設けた粉体受入用の開閉弁
、13,13aは所定量の粉体が槽1,1a中に受入れ
られたことを感知するレベル計、14゜14aは集塵機
15へ連結した空気排出管、16,161は空気排出管
14.14Hの途中に設けた開閉弁である。
11 and 113 are on-off valves for receiving powder provided at the powder receiving ports 12 and 12a at the top of the first tank 1 and second tank 1a, respectively; 14. 14a is an air exhaust pipe connected to the dust collector 15, and 16, 161 is an on-off valve provided in the middle of the air exhaust pipe 14.14H.

第1図に示した装置では、まず、開閉弁11が開き、第
1槽1に粉体の受入れが開始され、第1槽1が満量にな
るとレベル計13が働き、開閉弁11を閉じる。
In the device shown in FIG. 1, first, the on-off valve 11 opens and the first tank 1 starts receiving powder. When the first tank 1 is full, the level meter 13 operates and the on-off valve 11 is closed. .

つぎに、切替弁8が切替わって、粉体送出管7を粉体輸
送管9に連通させるとともに、開閉弁2,3を開き、サ
イロ10への粉体の輸送を開始する。
Next, the switching valve 8 is switched to connect the powder delivery pipe 7 to the powder transport pipe 9, open the on-off valves 2 and 3, and start transporting the powder to the silo 10.

第1槽1からの輸送中に、第2槽1aは開閉弁11 a
が開き、第1槽1の場合と同じ要領で粉体の受入れを完
了する。
During transportation from the first tank 1, the second tank 1a closes the on-off valve 11a.
is opened and the reception of the powder is completed in the same manner as in the case of the first tank 1.

第1槽1からの輸送が終了すると、第1槽1内の圧力が
下がり始め、0.5〜0.6 kg/cm2Gで開閉弁
2,3が締まる。
When the transportation from the first tank 1 is completed, the pressure in the first tank 1 starts to decrease, and the on-off valves 2 and 3 are closed at 0.5 to 0.6 kg/cm2G.

つぎに、切替弁8が切替わって、粉体送出管7aが粉体
輸送管9に連通し、開閉弁2a、3aが開き、第2槽1
aからの輸送を開始する。
Next, the switching valve 8 is switched, the powder delivery pipe 7a is communicated with the powder transport pipe 9, the on-off valves 2a and 3a are opened, and the second tank 1
Start transportation from a.

以下、第1槽1からの輸送と同じ要領で2槽1,1aが
交互に粉体の受入、圧送を繰返す。
Thereafter, in the same manner as the transportation from the first tank 1, the two tanks 1 and 1a alternately repeat receiving and pumping the powder.

従来は、このようにしていたので、一方の槽1または1
aから送出される粉体がすべて完全にサイロ10内に送
り込まれないと、他方の槽1aまたは1からの粉体の輸
送が行えなかった。
Conventionally, it was done this way, so one tank 1 or 1
Unless all the powder sent out from tank a was completely sent into the silo 10, the powder from the other tank 1a or tank 1 could not be transported.

また、その切替に時間がかかつていた。In addition, it took time to make the switch.

そして、その場合の槽内圧力や輸送能力は時間の経過と
ともに第2図に示したような変化をしていた。
In that case, the pressure inside the tank and the transport capacity changed over time as shown in Figure 2.

第2図において、Tは経過時間、Plは第1槽1内の圧
力、P2は第2槽1a内の圧力、tlは第1槽1からの
粉体の圧送時間、t2は第2槽1aからの粉体の圧送時
間、t3は切替時間、t4は圧力降下時間、Qは粉体輸
送能力、Qlは計算能力、Q2は保証能力を示す。
In Fig. 2, T is the elapsed time, Pl is the pressure in the first tank 1, P2 is the pressure in the second tank 1a, tl is the time for pumping the powder from the first tank 1, and t2 is the second tank 1a. t3 is the switching time, t4 is the pressure drop time, Q is the powder transport capacity, Ql is the calculation capacity, and Q2 is the guarantee capacity.

また、点線で示したものは、粉体受人時の状態を示す。Furthermore, the dotted line indicates the state at the time of receiving the powder.

このように、従来の装置では、第2図に示した時間によ
る槽内圧力の推移などを示した図からもわかるように、
連続輸送ができず、輸送配管の使用効率はかなり悪く、
長い距離の輸送には適していなかった。
In this way, in the conventional device, as can be seen from the diagram showing the change in tank pressure over time shown in Figure 2,
Continuous transportation is not possible, and the efficiency of transportation piping is quite poor.
It was not suitable for long distance transportation.

この考案はこれらの欠点をなくすためのものであり、2
槽からの粉体送出を切替える前に、あらかじめ他の槽内
の圧力を上げておき、粉体輸送の準備をしておくための
開閉弁を有する回路を設けておき、連続輸送ができるよ
うにして、輸送効率を100%近くまで増大させ、かつ
、槽を小さくできるようにしたものである。
This idea is intended to eliminate these drawbacks, and 2.
Before switching the powder delivery from the tank, increase the pressure in the other tanks in advance, and install a circuit with an on-off valve to prepare for powder transport, so that continuous transport is possible. This increases transport efficiency to nearly 100% and allows the tank to be made smaller.

つぎに、図面に示した実施例によって、この考案を説明
する。
Next, this invention will be explained with reference to embodiments shown in the drawings.

第3図におけるこの考案のl実施例を示すセラ一式のブ
ロータンク式空気輸送装置において、第1槽1と第2槽
1aの各下部および各側部には、それぞれ別個の粉体送
出用の開閉弁2,2a。
In the blow tank type pneumatic conveyance device with a cellar set showing an embodiment of this invention shown in FIG. On-off valves 2, 2a.

3.3aを介して圧縮空気源4と連結した空気供給管5
. 5a、 6. 6aを取付け、第1槽1と第2槽
1aの各側部と圧縮空気源4を連結した各空気供給管6
,6aの開閉弁3,3a部に、この開閉弁3,3aと並
列に他の開閉弁17.17 aを取付けた。
Air supply pipe 5 connected to compressed air source 4 via 3.3a
.. 5a, 6. 6a, and each air supply pipe 6 connects each side of the first tank 1 and the second tank 1a to the compressed air source 4.
, 6a, other on-off valves 17 and 17a were attached in parallel to the on-off valves 3 and 3a.

すなわち、第1槽1の側部と圧縮空気源4、および、第
2槽1aの側部と圧縮空気源4を、それぞれ別個に連結
していて、その途中に粉体送出用の開閉弁3,3aをそ
れぞれ有する各空気供給管6,6aに対して、開閉弁1
7.171を有する別個の枝管である空気供給管をそれ
ぞれ並列に設けた。
That is, the side of the first tank 1 and the compressed air source 4 and the side of the second tank 1a and the compressed air source 4 are connected separately, and an on-off valve 3 for powder delivery is connected in the middle. , 3a, each air supply pipe 6, 6a has an on-off valve 1.
Separate branch air supply pipes with 7.171 in each case were provided in parallel.

この開閉弁17.17 aは、第1槽1と第2槽1aか
らの粉体輸送の開始前に、第1槽1と第2槽1a内の圧
力をそれぞ゛れあらかじめ上げ゛ておき、粉体送出の準
備をしておき、輸送効率を向上させるために設けたもの
で、粉体送出用の開閉弁2゜2a、3,3aや空気供給
管5. 5a、 6. 6aが大容量のものであるの
に対して、この開閉弁17、171とその前後の枝管で
ある空気供給管は比較的に小容量のものを用いた。
This on-off valve 17.17a is used to increase the pressure in the first tank 1 and the second tank 1a, respectively, before starting powder transportation from the first tank 1 and the second tank 1a. This was provided in order to prepare for powder delivery and improve transportation efficiency, and includes powder delivery on-off valves 2. 5a, 6. 6a has a large capacity, whereas the on-off valves 17 and 171 and the air supply pipes which are branch pipes before and after the valves have a relatively small capacity.

第1槽1と第2槽1aの両方の粉体送出管7,7aは途
中で交わらせた後に1本の粉体輸出管9でサイロ10に
連結したが、粉体送出管7,7aが交わる部分と第1槽
1および第2槽1aとの間にはそれぞれ別個の開閉弁1
8.18 aを取付けた。
The powder delivery pipes 7, 7a of both the first tank 1 and the second tank 1a were crossed in the middle and then connected to the silo 10 with one powder export pipe 9, but the powder delivery pipes 7, 7a were Separate on-off valves 1 are provided between the intersecting portion and the first tank 1 and the second tank 1a.
8.18 a was installed.

11.11 aはそれぞれ第1槽1と第2槽1aの頂部
の粉体受人口12.12a部に設けた粉体受入用の開閉
弁、13.13 aは所定量の粉体が槽1,1a中に受
入れられたことを感知するレベル計、14.14 aは
集塵機15へ連結した空気排出管、16.16 aは空
気排出管14.141の途中に設けた開閉弁である。
11.11 a is a powder receiving opening/closing valve provided in the powder receiving port 12.12a at the top of the first tank 1 and second tank 1a, respectively; , 1a, 14.14a is an air exhaust pipe connected to the dust collector 15, and 16.16a is an on-off valve provided in the middle of the air exhaust pipe 14.141.

圧縮空気源4と粉体輸送管9の始端部付近との間には、
開閉弁19を有する空気供給管20を設けて、より一層
の能率向上をはかることができるようにした。
Between the compressed air source 4 and the vicinity of the starting end of the powder transport pipe 9,
An air supply pipe 20 having an on-off valve 19 is provided to further improve efficiency.

この装置では、まず開閉弁11が開いて第1槽1への粉
体受入れを開始し、第1槽1が満量になるとレベル計1
3が働き、開閉弁11を閉じる。
In this device, the on-off valve 11 first opens to start receiving powder into the first tank 1, and when the first tank 1 is full, the level meter 1
3 works and closes the on-off valve 11.

開閉弁11が閉じたのを確認したら、開閉弁17を開き
、第1槽1内を設定圧力まで上昇させる。
After confirming that the on-off valve 11 is closed, the on-off valve 17 is opened and the pressure inside the first tank 1 is raised to the set pressure.

第1槽1内が所定の設定圧力まで上昇したら、図示して
いない圧力スイッチの作動に基づいて、開閉弁17を閉
じ、輸送準備を終える。
When the pressure inside the first tank 1 rises to a predetermined set pressure, the on-off valve 17 is closed based on the operation of a pressure switch (not shown), and the transportation preparation is completed.

最初の輸送時は、つぎに開閉弁18. 2.3を開き、
第1槽1からの粉体の輸送を開始する。
During initial transportation, the on-off valve 18. Open 2.3 and
The transportation of powder from the first tank 1 is started.

この時、第2槽1aでは開閉弁11 aを開き、粉体の
受入れを開始し、満量になるとレベル計13aが働き、
開閉弁11 aを閉じる。
At this time, in the second tank 1a, the on-off valve 11a is opened to start receiving powder, and when the second tank 1a is full, the level meter 13a is activated.
Close the on-off valve 11a.

そして、開閉弁11 aが閉じたことを確認したら、開
閉弁17 aを開き、第2槽1a内に設定圧力まで圧縮
空気を封入し、開閉弁17aを閉じる。
After confirming that the on-off valve 11a is closed, the on-off valve 17a is opened, compressed air is filled in the second tank 1a up to the set pressure, and the on-off valve 17a is closed.

第1槽1内の粉体の輸送が完了すれば、第1槽1内の圧
力が下降を始める。
When the transportation of the powder in the first tank 1 is completed, the pressure in the first tank 1 starts to decrease.

この時、開閉弁2゜3を閉じ、同時に開閉弁18a、2
a、3aを開き、第2槽1aからの粉体の輸送を開始す
る。
At this time, the on-off valve 2゜3 is closed, and at the same time the on-off valves 18a and 2
a and 3a are opened to start transporting the powder from the second tank 1a.

第1槽1では、粉体輸送完了後、開閉弁16を開き、槽
1内の空気を抜き、槽1内の圧力がO,Ikg/(7)
・G程度まで下降すれば、開閉弁11が開いて、新たな
粉体の受入れを開始する。
In the first tank 1, after the powder transportation is completed, the on-off valve 16 is opened, the air inside the tank 1 is removed, and the pressure inside the tank 1 is O, Ikg/(7).
- When the temperature drops to about G, the on-off valve 11 opens and starts accepting new powder.

以下、第1槽1、第2槽1aは同じような要領で粉体の
受入、輸送を繰返し、第4図に示したような槽内圧力や
輸送能力の変化を繰返す。
Thereafter, the first tank 1 and the second tank 1a repeat receiving and transporting powder in the same manner, and the changes in tank internal pressure and transport capacity as shown in FIG. 4 are repeated.

そして、一方の槽1または1aからの粉体の輸送が終わ
ると、すぐに他方の槽1aまたは1への切替を行い、一
方の槽1または1a内の空気を開閉弁16または16
aと集塵機15を通して大気へ放出することによって、
粉体輸送管9内では、はぼ連続的に一定容量の粉体が輸
送できるようにした。
When the transportation of the powder from one tank 1 or 1a is finished, the switch is immediately made to the other tank 1a or 1, and the air in one tank 1 or 1a is switched to the on-off valve 16 or 16.
By discharging it into the atmosphere through a and the dust collector 15,
Inside the powder transport pipe 9, a constant amount of powder can be transported almost continuously.

第4図において、Tは経過時間、Plは第1槽1内の圧
力、P2は第2槽1a内の圧力、tlは第1槽1からの
粉体の圧送時間、t2は第2槽1aからの粉体の圧送時
間、Qは粉体輸送能力、Q3は計算能力および保証能力
を示す。
In FIG. 4, T is the elapsed time, Pl is the pressure in the first tank 1, P2 is the pressure in the second tank 1a, tl is the time for pumping the powder from the first tank 1, and t2 is the second tank 1a. Q is the powder transportation capacity, and Q3 is the calculation ability and guarantee ability.

また、点線で示したものは、粉体受人時の状態を示す。Furthermore, the dotted line indicates the state at the time of receiving the powder.

既設のセラ一式のブロータンク式空気輸送装置を改造す
る場合は、第5図に示すようにする。
When modifying an existing blow tank type pneumatic transport device for a cellar set, do so as shown in Figure 5.

この場合は、切替弁8が従来式なので、均圧配管および
補助圧送配管が必要である。
In this case, since the switching valve 8 is of a conventional type, pressure equalization piping and auxiliary pressure feeding piping are required.

したがって、第1槽1と第2槽1aの各側部と圧縮空気
源4を連結した各空気供給管6,6aの開閉弁3,3a
部に、この弁3,3aと並列に他の開閉弁17.17a
をそれぞれ取付けるとともに、切替弁8がある部分にお
いて、各粉体送出管7,7aと粉体輸送管9との間を開
閉弁18,181を有する管21,21 aでバイパス
状に連通させた。
Therefore, the on-off valves 3, 3a of the air supply pipes 6, 6a connecting each side of the first tank 1 and the second tank 1a to the compressed air source 4
In the section, another on-off valve 17.17a is installed in parallel with this valve 3, 3a.
At the same time, in the part where the switching valve 8 is located, the powder delivery pipes 7, 7a and the powder transport pipe 9 are connected in a bypass manner through pipes 21, 21a having on-off valves 18, 181. .

また、圧縮空気源4と粉体輸送管9との間に、開閉弁1
9を有する空気供給管20を取付けた。
Additionally, an on-off valve 1 is provided between the compressed air source 4 and the powder transport pipe 9.
An air supply pipe 20 with 9 was installed.

第5図に示した装置においては、まず、開閉弁11が開
き、第1槽1への粉体の受入を開始し、満量になるとレ
ベル計13が働き、開閉弁11を閉じる。
In the apparatus shown in FIG. 5, the on-off valve 11 is first opened to start receiving powder into the first tank 1, and when the first tank 1 is full, the level meter 13 is activated and the on-off valve 11 is closed.

開閉弁11が閉じたことを確認したら、開閉弁17を開
き、第1槽1内に設定圧力まで圧縮空気を封入して、開
閉弁17を閉じる。
After confirming that the on-off valve 11 is closed, the on-off valve 17 is opened, compressed air is sealed in the first tank 1 to a set pressure, and the on-off valve 17 is closed.

つぎに、切替弁8を作動させて粉体送出管7と粉体輸送
管9を連通させ、開閉弁2,3を開いて粉体の輸送を開
始する。
Next, the switching valve 8 is operated to connect the powder delivery pipe 7 and the powder transport pipe 9, and the on-off valves 2 and 3 are opened to start transporting the powder.

この時、第2槽1aでは、開閉弁11 aを開き、粉体
の受入れを開始し、満量になると、レベル計131が働
き、開閉弁11 aを閉じる。
At this time, in the second tank 1a, the on-off valve 11a is opened to start receiving the powder, and when the tank is full, the level meter 131 is activated and the on-off valve 11a is closed.

開閉弁11 aが閉じたことを確認したら、開閉弁17
aを開き、第2槽1a内に設定圧力まで圧縮空気を封入
し、開閉弁17 aを閉じる。
After confirming that on-off valve 11 a is closed, open on-off valve 17
Open the valve 17a, fill the second tank 1a with compressed air up to the set pressure, and close the on-off valve 17a.

第1槽1内の粉体の輸送が完了したら、槽1内の圧力が
下降を始める。
When the transportation of the powder in the first tank 1 is completed, the pressure in the tank 1 starts to decrease.

この時、開閉弁19.18゜18 aを開き、開閉弁2
,3を閉じると同時に、切替弁8を粉体送出管7aが粉
体輸送管9へ通じる側に切替え、その切替確認後、開閉
弁2a、3aを開き、開閉弁19.18.18 aを閉
じるが、輸送は継続する。
At this time, open the on-off valve 19.18°18a, and open the on-off valve 2.
, 3 are closed, the switching valve 8 is switched to the side where the powder delivery pipe 7a communicates with the powder transport pipe 9, and after confirming the switching, the on-off valves 2a and 3a are opened, and the on-off valves 19, 18, and 18 a are closed. Closed, but transportation continues.

第1槽1は、輸送完了後、開閉弁16が開き、槽1内空
気を抜き、0.1 kg/cm” G程度に下降すれば
、開閉弁11が開き、粉体の受入を開始する。
In the first tank 1, after the transportation is completed, the on-off valve 16 opens, the air inside the tank 1 is removed, and when the temperature drops to about 0.1 kg/cm"G, the on-off valve 11 opens and starts receiving the powder. .

以下、第1槽1、第2槽1aは同じ要領で粉体の受入、
輸送を繰返す。
Hereinafter, the first tank 1 and the second tank 1a will receive powder in the same manner.
Repeat transportation.

なお、この発明のブロータンク式空気輸送装置の実施例
としては、セラ一式のものについてのみ述べたが、これ
はフラクソ式のものにも同様にして使用できるし、セラ
一式とフラクソ式を組合せたものにも使用できる。
In addition, as an example of the blow tank type pneumatic transport device of this invention, only the one with a cella set has been described, but this can be similarly used with a fluxo type, or a combination of a cella set and a fluxo type. It can also be used for things.

このように、この考案においては、実用新案登録請求の
範囲に記載したように、第1槽と第2槽の各側部と圧縮
空気源を連結した各空気供給管の開閉弁部に、この開閉
弁と並列に他の開閉弁をそれぞれ取付け、両方の粉体送
出管が交わる部分と第1槽および第2槽との間にそれぞ
れ別個の開閉弁を取付けたので、第1槽と第2槽からの
粉体の送出を切替える前に、槽内の圧力をあらかじめ上
げておき、粉体の送出をする準備をしておくことによっ
て、切替えと同時に最大能力を連続的に発揮することが
できる。
In this way, in this invention, as described in the claims for utility model registration, this valve is installed in the on-off valve part of each air supply pipe that connects each side of the first tank and the second tank with the compressed air source. Other on-off valves were installed in parallel with the on-off valve, and separate on-off valves were installed between the intersection of both powder delivery pipes and the first tank and the second tank, so that the first tank and the second tank Before switching the powder delivery from the tank, by increasing the pressure in the tank in advance and preparing to send the powder, the maximum capacity can be continuously demonstrated at the same time as the switching. .

したがって、輸送効率を向上させ、連続輸送を行うこと
ができ、また、その結果、比較的に小さい槽を用いて充
分に遠距離まで粉体を空気輸送することができる。
Therefore, the transport efficiency can be improved, continuous transport can be carried out, and as a result, the powder can be pneumatically transported over a sufficiently long distance using a relatively small tank.

また、この考案では、大容量の開閉弁と並列に小容量の
開閉弁を設け、粉体送出前に小容量の開閉弁のみを開い
て槽内の圧力を上げるようにしたので、槽内の圧力が所
定圧になって開閉弁を閉じるまでに槽内の圧力が上がり
すぎることがなく、その結果、方の粉体送出管から新た
に送出される粉体が、粉体が送出されている他方の粉体
送出管へ逆流して、その管がつまったり、能力がおちた
りすることもなく、円滑に連続して粉体送出が行われる
In addition, with this idea, a small capacity on-off valve is installed in parallel with a large-capacity on-off valve, and only the small-capacity on-off valve is opened before the powder is sent out to increase the pressure inside the tank. The pressure inside the tank does not rise too much until the pressure reaches the specified pressure and closes the on-off valve, and as a result, the powder newly sent out from the powder delivery pipe is Powder can be delivered smoothly and continuously without backflow to the other powder delivery pipe, which will not clog that pipe or reduce its capacity.

また、この考案では、前記並列に設けた開閉弁が小容量
なので、一方の空気輸送管で空気を輸送して粉体を送出
しているとき、他方の検測の小容量の前記開閉弁を開い
ても、現在空気を送っている空気輸送管側の能力がほと
んどおちることがなく、円滑な粉体送出ができる。
In addition, in this invention, since the on-off valves installed in parallel have a small capacity, when one of the air transport pipes is transporting air and sending out powder, the on-off valves of the other inspection with a small capacity are used. Even if it is opened, the capacity of the air transport pipe that is currently sending air will hardly decrease, allowing smooth powder delivery.

【図面の簡単な説明】[Brief explanation of drawings]

第1図はこの考案に類似した従来の装置の1例を示す回
路図、第2図は第1図の装置における槽内圧力等を示す
線図、第3図はこの考案の1実施例を示す回路図、第4
図は第2図の装置における槽内圧力等を示す線図、第5
図はこの考案の他の実施例を示す回路図である。 1・・・・・・第1槽、1a・・・・・・第2槽、2.
2a、 3゜3 a、 11.11 a、 16.17
.17 a、 18.18 a、 19・・・・・・開
閉弁、5.5a、 6.6a、 20・・・・・・空気
供給管、7.7a・・・・・・粉体送出管、8・・・・
・・切替弁、9・・・・・・粉体輸出管、10・・・・
・・サイロ、12,12a・・・・・・材料受入口。
Fig. 1 is a circuit diagram showing an example of a conventional device similar to this invention, Fig. 2 is a diagram showing the pressure inside the tank, etc. in the device of Fig. 1, and Fig. 3 is an example of an embodiment of this invention. Circuit diagram shown, 4th
The figure is a diagram showing the pressure inside the tank in the device shown in Figure 2, and the diagram shown in Figure 5.
The figure is a circuit diagram showing another embodiment of this invention. 1...First tank, 1a...Second tank, 2.
2a, 3゜3 a, 11.11 a, 16.17
.. 17a, 18.18a, 19...Opening/closing valve, 5.5a, 6.6a, 20...Air supply pipe, 7.7a...Powder delivery pipe , 8...
...Switching valve, 9...Powder export pipe, 10...
...Silo, 12, 12a... Material receiving port.

Claims (1)

【実用新案登録請求の範囲】[Scope of utility model registration request] 第1槽と第2槽の各下部および各側部に、圧縮空気源と
それぞれ別個の粉体送出用の開閉弁を介して連結した空
気供給管をそれぞれ取付け、第1槽と第2槽の両方の粉
体送出管を途中で交わらせた後に1本の粉体輸送管でサ
イロに連結したブロータンク式空気輸送装置において、
第1槽の側部と圧縮空気源および第2槽の側部と圧縮空
気源をそれぞれ別個に連結していて、その途中に前記粉
体送出用の開閉弁をそれぞれ有する各空気供給管に対し
て、粉体送出前に第1槽内および第2槽内の圧力をそれ
ぞれあらかじめ上け゛ておくための前記各空気供給管と
各開閉弁よりも小容量の開閉弁を有する別個の空気供給
管をそれぞれ並列に設け、前記第1槽および第2槽の両
方の粉体送出管が交わる部分と第1槽および第2槽との
間に設けた各粉体輸送管に、それぞれ別個の開閉弁を取
付けたブロータンク式空気輸送装置。
An air supply pipe connected to a compressed air source via a separate on-off valve for powder delivery is installed at the bottom and each side of each of the first and second tanks. In a blow tank type pneumatic transport device in which both powder delivery pipes intersect in the middle and are connected to a silo with a single powder transport pipe,
For each air supply pipe that separately connects the side of the first tank and the compressed air source, and the side of the second tank and the compressed air source, and has an on-off valve for sending out the powder in the middle. In order to increase the pressure in the first tank and the second tank in advance before sending out the powder, separate air supply pipes each having an on-off valve with a smaller capacity than the above-mentioned air supply pipes and on-off valves are provided. A separate on-off valve is provided for each powder transport pipe provided in parallel and between the first tank and the second tank and the intersection of the powder delivery pipes of both the first tank and the second tank. Installed blow tank type pneumatic transport device.
JP1977175774U 1977-12-28 1977-12-28 Blow tank type pneumatic transport device Expired JPS5925782Y2 (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP1977175774U JPS5925782Y2 (en) 1977-12-28 1977-12-28 Blow tank type pneumatic transport device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP1977175774U JPS5925782Y2 (en) 1977-12-28 1977-12-28 Blow tank type pneumatic transport device

Publications (2)

Publication Number Publication Date
JPS54101792U JPS54101792U (en) 1979-07-18
JPS5925782Y2 true JPS5925782Y2 (en) 1984-07-27

Family

ID=29183659

Family Applications (1)

Application Number Title Priority Date Filing Date
JP1977175774U Expired JPS5925782Y2 (en) 1977-12-28 1977-12-28 Blow tank type pneumatic transport device

Country Status (1)

Country Link
JP (1) JPS5925782Y2 (en)

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5147754U (en) * 1974-10-02 1976-04-09

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5147754U (en) * 1974-10-02 1976-04-09

Also Published As

Publication number Publication date
JPS54101792U (en) 1979-07-18

Similar Documents

Publication Publication Date Title
CN108790216B (en) Wind power generation blade integrated pouring assembly line and pouring process thereof
CN109397547A (en) Integrated folded foundation-free concrete mixing station
CN108265983A (en) A kind of high-rise building appts. for transferring ready-mixed concrete
JPS5925782Y2 (en) Blow tank type pneumatic transport device
CN104197193A (en) Pipeline control system and pipeline precooling method for marine natural gas storage tank
CN204768532U (en) Material mixing equipment
CN111925454B (en) System and method for preparing hematite inhibitor corn starch for reverse flotation
CN207738102U (en) A kind of Chips Conveying System
CN208715510U (en) Powder body material and staple fiber mix sack-filling device
CN208982011U (en) A kind of coal mine High Position Drilling wind-driving grouting device
CN208373465U (en) A kind of intelligence Full automatic feed and vacuum defoamation two-component glue pouring machine
CN204816974U (en) Realize feed equipment of automatic ration control of powder
CN108405277A (en) A kind of intelligence Full automatic feed and vacuum defoamation two-component glue pouring machine
CN206395469U (en) The dry husky water of built-in type send system
JPS587571B2 (en) Control method for powder transport equipment
CN211282230U (en) Powder material transportation semitrailer with discharge pipeline arranged at bottom
CN217227970U (en) A finished product packing plant for production of cement base self-leveling mortar
CN212402699U (en) Lime quantitative adding device
CN214649358U (en) Filling device of light gypsum that plasters
CN217921997U (en) Automatic rice feeding device for rice wine steaming bed
CN219488918U (en) Pneumatic conveying and sending tank
CN208714222U (en) Integrated folded foundation-free concrete mixing station
JPH1135155A (en) Powder vacuum transfer method and cement conveying method using former method in manufacture of concrete
JPS6077023A (en) Apparatus for transferring pulverulent body with pneumatic power
CN206230695U (en) Dry-mixed mortar production line and its buffering storage tank