JPH0592477U - Degassing mixing device using check valve - Google Patents
Degassing mixing device using check valveInfo
- Publication number
- JPH0592477U JPH0592477U JP3851192U JP3851192U JPH0592477U JP H0592477 U JPH0592477 U JP H0592477U JP 3851192 U JP3851192 U JP 3851192U JP 3851192 U JP3851192 U JP 3851192U JP H0592477 U JPH0592477 U JP H0592477U
- Authority
- JP
- Japan
- Prior art keywords
- pump
- check valve
- air volume
- vacuum
- suction
- 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.)
- Pending
Links
- 238000007872 degassing Methods 0.000 title claims description 10
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 description 4
- 238000012423 maintenance Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 238000000926 separation method Methods 0.000 description 2
- 235000013305 food Nutrition 0.000 description 1
- 238000000034 method Methods 0.000 description 1
- 230000004580 weight loss Effects 0.000 description 1
Landscapes
- Vacuum Packaging (AREA)
- Compressors, Vaccum Pumps And Other Relevant Systems (AREA)
Abstract
(57)【要約】 (修正有)
【目的】 処理風量が大きいが真空到達度の低いポンプ
と処理風量が小さいが真空到達度の高いポンプを組合わ
す事により、処理風量が大きく真空到達度の高い装置を
複雑な構造を必要とせず、逆止弁を利用するだけで簡単
に小型軽量化出来、製作費も安価に製作する。
【構成】 圧力容器に逆止弁3を取り付け処理風量の大
きなポンプ1で吸引する。また別に接続口6をもうけ
て、真空到達度の高いポンプ2で吸引する時、吸気口7
から吸入される気体は4のポンプで急速に吐出され減量
される。1のポンプの到達度まで吸引すれば、容器内と
同圧になり、弁10の重さで逆止弁が閉じ、1のポンプ
の働きは停止する。しかし2のポンプが働き続け、減量
された気体を少量ずつ排出し、高い真空度まで吸引する
事が出来る。
(57) [Summary] (Corrected) [Purpose] By combining a pump with a large treatment air volume but a low vacuum achievement and a pump with a small treatment air quantity but a high vacuum achievement, It does not require a complicated structure for a high-priced device, and it can be easily made compact and lightweight by using a check valve and can be manufactured at low cost. [Structure] A check valve 3 is attached to a pressure vessel and suction is performed by a pump 1 having a large processing air volume. In addition, a separate connection port 6 is provided so that the suction port 7
The gas sucked from is rapidly discharged by the pump 4 and reduced in volume. If the suction of the pump of No. 1 is performed, the pressure becomes equal to that in the container, and the check valve closes due to the weight of the valve 10, and the operation of the pump of No. 1 stops. However, the 2nd pump continues to work, and the reduced gas can be discharged little by little and sucked up to a high degree of vacuum.
Description
【0001】[0001]
吸気を必要とする容器が大容量で高い真空度を要求される場合、時間的により 速く、装置も簡単で、小型軽量化出来、安価で維持費も安く、操作も簡単な装置 として利用出来る。 When a container that requires intake air has a large capacity and a high degree of vacuum, it can be used as a device that is faster in time, simpler in device, smaller in size and lighter in weight, cheaper in maintenance cost, and easier in operation.
【0002】[0002]
従来脱気用ポンプとしては、処理風量が大きいが真空到達度が低いものか、処 理風量は小さいが真空到達度が高い機種であって処理風量が大きく真空度の高い 機種は、後者の機種を大型化せざるを得なかった。また、前者と後者を連結して 使用する場合は、電磁弁等複雑な電気操作や差庄弁等の配管を必要としていた。 As a conventional degassing pump, a model with a large treatment air volume but a low vacuum achievement, or a model with a small treatment air quantity but a high vacuum achievement and a large treatment air volume and a high vacuum degree is the latter model. I had no choice but to upsize. In addition, when the former and the latter are connected and used, complicated electrical operations such as solenoid valves and piping such as differential valves were required.
【0003】[0003]
ポンプの大型化する場合は重量が大きくなり、コストが高く維持費も大きくな っていた。また2台の異ったポンプの連結による場合でも、操作が複雑で故障の 原因となり、コストも高くついていた。 When the size of the pump is increased, the weight is increased, the cost is high, and the maintenance cost is also high. Further, even when two different pumps are connected, the operation is complicated and causes a failure, and the cost is high.
【0004】[0004]
以上の問題を解決するために処理風量が大きく高真空度のポンプを作り出す手 段として図1の様に圧力容器(5)に逆止弁(3)を取り付け処理風量が大きい が、真空到達圧力の低いポンプ(1)の接続口(4)とし、処理風量が小さいが 真空到達圧力の高いポンプ(2)の接続口(6)を取り付ける。吸気口(7)を 取り付け脱気を必要とする容器(9)に接続する(4)と(6)に(1)と(2 )を接続して、(1)と(2)を同時運転する時(9)の中に気体(8)はまず (1)の働きにより、短時間で排出される。(1)の真空到達点まで脱気すれば (4)の部分の圧力と(8)の圧力とが同圧となり逆止弁の弁(10)が重さで 、自動的に閉じ(2)のポンプの働きのみ作動を続ける。(8)は(1)の働き で残量が少なくなっているため、(2)のポンプの小さい処理風量でも処理する 事が出来、高い真空度に到達する事が出来る。この点を利用して特色をもった二 つ以上のポンプを組合わせる事により、大きな効果を生み出す事を目的とした逆 止弁を利用した脱気用ミキシング装置。 In order to solve the above problems, a check valve (3) is attached to the pressure vessel (5) as shown in Fig. 1 as a means to create a pump with a large processing air volume and a high vacuum level. And the connection port (6) of the pump (2) having a small processing air volume but a high vacuum reaching pressure is attached. Connect the inlet (7) to the container (9) that needs degassing, connect (1) and (2) to (4) and (6), and operate (1) and (2) simultaneously During the operation (9), the gas (8) is first discharged in a short time by the action of (1). If degassing is performed up to the vacuum reaching point in (1), the pressure in the part (4) and the pressure in (8) become the same pressure, and the check valve (10) is automatically closed by weight (2). Only the pump function of continues to operate. Since the remaining amount of (8) is small due to the function of (1), it is possible to process with a small processing air volume of the pump of (2), and it is possible to reach a high degree of vacuum. Taking advantage of this point, by combining two or more pumps with special characteristics, a degassing mixing device that uses a check valve for the purpose of producing a large effect.
【0005】[0005]
この考案の使用法は、処理風量が大きく真空度の高い装置として使用する場合 、処理風量は(1)の能力で決定し、真空到達圧力は(2)の能力で設定出来る ための目的に応じた選定が可能となるため、必要に応じた装置として使用出来、 小型軽量化が可能となる。また図3の様に(5)の内部にホッパー(11)を設 置し、ドレン口(12)及びドレンコック(13)を設置する事により水分離機 能を有するミキシングタンクとして使用する事が出来る。 The usage of this invention is that, when used as a device with a large processing air volume and a high degree of vacuum, the processing air volume is determined by the capacity of (1) and the ultimate vacuum pressure can be set by the capacity of (2) according to the purpose. Since it can be selected, it can be used as a device as needed and can be made compact and lightweight. Further, as shown in FIG. 3, a hopper (11) is installed inside (5) and a drain port (12) and a drain cock (13) are installed so that it can be used as a mixing tank having a water separating function. I can.
【0006】[0006]
食品等鮮度保持のための真空パックや、大容量の容器内の真空のスピード化、 脱気による減量パック等高い真空度が要求され、なおかつ短時間に脱気する装置 全搬に利用する事が出来る。また、水分離機能をもうける事により、水を含んだ 内容量のものでも、高真空度を保ち、スピーディに脱気する事が可能となる。 A vacuum pack for maintaining the freshness of foods, speeding up the vacuum in a large-capacity container, and a high-vacuum pack such as a weight loss pack by degassing are required. I can. In addition, by providing a water separation function, it is possible to maintain high vacuum and degas quickly even if the content volume contains water.
【0007】[0007]
それぞれの長所を有する二台以上のポンプのその長所のみを引出して合体し、 ハイレベルな脱気装置を作り出す事により、ポンプの能力に合った組合わせが自 由に選択出来る利点と、小型軽量になり、設備費が安価となり、維持費も安く操 作も簡単になり、脱気時間の短縮効果を生み出す事が可能となった。 By drawing out and combining only the advantages of two or more pumps with their respective advantages to create a high-level deaerator, the advantage is that the combination that matches the pump's ability can be freely selected, and it is small and lightweight. As a result, equipment costs are low, maintenance costs are low, operation is simple, and it is possible to reduce the degassing time.
【図1】本考案の斜視図。FIG. 1 is a perspective view of the present invention.
【図2】本考案の断面図。FIG. 2 is a sectional view of the present invention.
【図3】本考案に水分離機能を内蔵させた断面図。FIG. 3 is a sectional view of the present invention with a water separation function incorporated therein.
1 処理風量は大きいが真空到達圧力の低いポンプ 2 処理風量は小さいが真空到達圧力の高いポンプ 3 逆止弁 4 処理風量の大きいポンプの接続口 5 圧力容器 6 真空到達圧力の高いポンプの接続口 7 吸気口 8 脱気を必要とする気体 9 脱気を必要とする容器 10 逆止弁の中に内蔵された弁 11 ホッパー 12 ドレン口 13 ドレンコック 1 Pump with large amount of treated air but low ultimate pressure of vacuum 2 Pump with small amount of treated air but high ultimate pressure of vacuum 3 Check valve 4 Connection port for pump with large amount of treated air 5 Pressure vessel 6 Connection port for pump with high ultimate pressure of vacuum 7 Intake port 8 Gas that needs degassing 9 Container that needs degassing 10 Valve built in the check valve 11 Hopper 12 Drain port 13 Drain cock
Claims (1)
ポンプ(1)と処理風量が小さく真空到達点の高い脱気
ポンプ(2)を組合わせる時、圧力容器に吸気口と
(2)用の接続口と逆止弁を取り付けた(1)用の接続
口をもうけることにより、吸気を必要とする容器の中の
気体を(1)のポンプと(2)のポンプで、大風量の気
体を処理して吸引し、(1)のポンプの到達圧力と、吸
気を必要とする容器の圧力が等しくなれば、逆止弁の弁
が落ちて(1)のポンプの吸引が停止し、(2)のポン
プで残った小風量の気体を真空到達点の高い圧力まで吸
引することにより、処理風量が大きく、真空到達点の高
いポンプを作り出すことの出来る逆止弁を利用した脱気
用ミキシング装置。1. When a deaeration pump (1) having a large treated air volume and a low vacuum reaching point and a deaeration pump (2) having a small treated air quantity and a high vacuum reaching point are combined, an intake port (2) is provided in a pressure vessel. By providing a connection port for (1) equipped with a check valve and a check valve, the gas in the container that needs to be inhaled can be supplied with a large air volume by the pump of (1) and the pump of (2). When the gas is processed and sucked, and the ultimate pressure of the pump of (1) becomes equal to the pressure of the container that requires suction, the check valve falls and the suction of the pump of (1) stops. By degassing a small amount of gas remaining in the pump of (2) up to a high pressure at the vacuum reaching point, a deaeration using a check valve that can create a pump with a large processing air volume and a high vacuum reaching point Mixing equipment.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3851192U JPH0592477U (en) | 1992-05-12 | 1992-05-12 | Degassing mixing device using check valve |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP3851192U JPH0592477U (en) | 1992-05-12 | 1992-05-12 | Degassing mixing device using check valve |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH0592477U true JPH0592477U (en) | 1993-12-17 |
Family
ID=12527297
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP3851192U Pending JPH0592477U (en) | 1992-05-12 | 1992-05-12 | Degassing mixing device using check valve |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH0592477U (en) |
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008031904A (en) * | 2006-07-27 | 2008-02-14 | Cosmopower Inc | Apparatus for generating negative pressure and intensified pressure |
| JP2016090192A (en) * | 2014-11-10 | 2016-05-23 | 三浦工業株式会社 | Vacuum cooling device |
-
1992
- 1992-05-12 JP JP3851192U patent/JPH0592477U/en active Pending
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2008031904A (en) * | 2006-07-27 | 2008-02-14 | Cosmopower Inc | Apparatus for generating negative pressure and intensified pressure |
| JP2016090192A (en) * | 2014-11-10 | 2016-05-23 | 三浦工業株式会社 | Vacuum cooling device |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| GB1474655A (en) | Suction stabilizer for reciprocating pumps and stabilizing method | |
| JPH09511202A (en) | Method and apparatus for reducing emissions from storage tank exhaust pipes | |
| JPS62501825A (en) | Methods and apparatus used for dispensing and measuring volume of liquid foods | |
| CA1038835A (en) | Low vacuum pumping system | |
| JPH0592477U (en) | Degassing mixing device using check valve | |
| CN101514699B (en) | Oil-gas separation circular arc type inside engaged gear combined oil pump | |
| JPS6111473A (en) | Automatic gas vent apparatus in reciprocating pump | |
| CN210769348U (en) | Composite strong self-suction centrifugal pump set | |
| JPS6339799B2 (en) | ||
| US2242714A (en) | Liquid dispensing apparatus | |
| JP2715256B2 (en) | Steam-water separator structure of priming pump | |
| JP2001317426A (en) | Fuel supply device | |
| JPH072002Y2 (en) | Separation device for liquids with different specific gravities | |
| JP2003038905A (en) | Deaeration apparatus | |
| JPH0663878U (en) | Diaphragm pump | |
| CN222942982U (en) | Oil-water separation tank for separating turpentine | |
| CN110841348A (en) | Machine tool workpiece adsorption clamping filtering equipment and adsorption clamping filtering method | |
| CN203051141U (en) | Single-screw water lubrication oil-less air compressor integrated device | |
| JPS607725Y2 (en) | Artificial kidney dialysate deaerator | |
| JPS643451Y2 (en) | ||
| JPH0534265Y2 (en) | ||
| JPS601768Y2 (en) | Multi-stage vacuum degassing equipment | |
| JPH0478472U (en) | ||
| JPH07136641A (en) | Vent device of gas-liquid mixed fluid | |
| JP2822619B2 (en) | Hydraulic system |