JPH03293009A - Gas-liquid separator - Google Patents
Gas-liquid separatorInfo
- Publication number
- JPH03293009A JPH03293009A JP2095393A JP9539390A JPH03293009A JP H03293009 A JPH03293009 A JP H03293009A JP 2095393 A JP2095393 A JP 2095393A JP 9539390 A JP9539390 A JP 9539390A JP H03293009 A JPH03293009 A JP H03293009A
- Authority
- JP
- Japan
- Prior art keywords
- air
- passage
- casing
- flow generator
- gas
- 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
- 239000007788 liquid Substances 0.000 title claims description 21
- 238000011144 upstream manufacturing Methods 0.000 claims abstract description 4
- 238000000926 separation method Methods 0.000 claims description 8
- 230000000149 penetrating effect Effects 0.000 claims 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 25
- 230000002093 peripheral effect Effects 0.000 abstract description 4
- 238000002347 injection Methods 0.000 description 30
- 239000007924 injection Substances 0.000 description 30
- 239000000446 fuel Substances 0.000 description 8
- 238000002485 combustion reaction Methods 0.000 description 5
- 239000002245 particle Substances 0.000 description 3
- 230000000694 effects Effects 0.000 description 2
- 239000011358 absorbing material Substances 0.000 description 1
- 230000007257 malfunction Effects 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B04—CENTRIFUGAL APPARATUS OR MACHINES FOR CARRYING-OUT PHYSICAL OR CHEMICAL PROCESSES
- B04C—APPARATUS USING FREE VORTEX FLOW, e.g. CYCLONES
- B04C3/00—Apparatus in which the axial direction of the vortex flow following a screw-thread type line remains unchanged ; Devices in which one of the two discharge ducts returns centrally through the vortex chamber, a reverse-flow vortex being prevented by bulkheads in the central discharge duct
- B04C3/06—Construction of inlets or outlets to the vortex chamber
Landscapes
- Separating Particles In Gases By Inertia (AREA)
Abstract
Description
【発明の詳細な説明】
［産業上の利用分野］
本発明は、気体通路内の水分を除去する気液分離装置に
関する。DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to a gas-liquid separation device that removes moisture in a gas passage.
［従来の技術］
内燃機関の筒内燃料噴射システムとして、エアブラスト
式噴射が知られている。これは、燃料を、空気圧縮機で
加圧した空気とともに、空気噴射弁（エアブラスト弁〉
から各気筒内に噴射するシステムである。[Prior Art] Air blast injection is known as an in-cylinder fuel injection system for internal combustion engines. This injects fuel with air pressurized by an air compressor into an air injection valve (air blast valve).
This system injects fuel into each cylinder from
しかしながら、このシステムでは、吸入空気に含まれる
水蒸気が空気圧縮機通過後、高圧空気流路内で凝縮する
おそれかある。特に、低温時には、この凝縮水か空気噴
射弁内て氷結して、空気噴射弁か作動しなくなるおそ？
１がある。However, in this system, water vapor contained in the intake air may condense in the high-pressure air flow path after passing through the air compressor. Particularly at low temperatures, there is a risk that this condensed water may freeze inside the air injection valve and cause the air injection valve to malfunction.
There is 1.
「発明か解決しようとする課題］
そこで１本発明は、凝縮水の空気噴射弁内への侵入を阻
止し、空気噴射弁を良好に作動させるために、空気流路
内の水分を効率よく分離・除去できる気液分離装置を提
供しようとするものである。``Problems to be solved by the invention'' Therefore, 1. The present invention aims to efficiently separate moisture in the air flow path in order to prevent condensed water from entering the air injection valve and allow the air injection valve to operate properly.・The aim is to provide a gas-liquid separation device that can remove
［課題を解決するための手段］
本発明の構成を第１図で説明すると、水分を含む空気の
通路途中に設けられ、該空気より水分を分離する気液分
離装置３は、密閉筒状ケーシング３１内の一端に、軸心
を一致せしめて旋回流発生器３２を設けて、該旋回流発
生器３２により上流側空気通路１２よりケーシング３１
内に導入される空気を旋回せしめてこれに含まれる水分
を遠心方向へ分離するようになすとともに、上記ケーシ
ング３１の内周壁を、上記分離された水分を捕集してケ
ーシング外へ排出する排出ｎ３４となし、上記ケーシン
グ３１よりも小径で、一端が上記旋回流発生器３２に同
心に対向して開口する筒状空気導出路３３を設けて、該
空気導出路３３の少なくとも他端を上記排出路３４に連
通せしめ、がっ、上記空気導出路３３の路壁を貫通して
下流側空気通路４１を開口せしめたものである。[Means for Solving the Problems] The configuration of the present invention will be explained with reference to FIG. 1. A gas-liquid separator 3 that is provided in the middle of a passage of air containing moisture and that separates moisture from the air has a closed cylindrical casing. A swirling flow generator 32 is provided at one end of the interior of the casing 31 so that the axes coincide with each other.
The air introduced into the casing 31 is swirled so that the moisture contained therein is separated in the centrifugal direction, and the inner circumferential wall of the casing 31 is used to collect the separated moisture and discharge it to the outside of the casing. n34, a cylindrical air outlet passage 33 having a smaller diameter than the casing 31 and one end opening concentrically opposite the swirling flow generator 32 is provided, and at least the other end of the air outlet passage 33 is provided with the air outlet passage 33. The downstream air passage 41 is communicated with the air passage 34 and penetrates through the wall of the air outlet passage 33 to open the downstream air passage 41.
［作用］
上記構成の気液分離装置において、水分を含んだ空気は
旋回流発生器３２で旋回せしめられ、粒径の大きい水分
は遠心方向へ分離されてケーシング３１内周壁に捕集さ
れ、排出路３４を経てケーシング３１外へ排出される。[Operation] In the gas-liquid separator having the above configuration, the air containing moisture is swirled by the swirl flow generator 32, and moisture with large particle size is separated in the centrifugal direction, collected on the inner circumferential wall of the casing 31, and discharged. It is discharged to the outside of the casing 31 through a passage 34.
大径の水分が分離された空気は小径の空気導出路３３内
に進入するが旋回状態が維持されていることにより、空
気に混入して至った小径の水分は分離されて空気導出路
３３の路壁に付着し、ケーシング３１外へ排出される。The air from which the large-diameter moisture has been separated enters the small-diameter air outlet passage 33, but since the swirling state is maintained, the small-diameter moisture that has mixed into the air is separated and enters the air outlet passage 33. It adheres to the road wall and is discharged to the outside of the casing 31.
そして、含有水分が殆ど分離された空気が上記路壁を貫
通して空気導出路３３内に開口する下流側空気通路４１
へ流出する。A downstream air passage 41 through which air from which most of the moisture content has been separated penetrates the passage wall and opens into the air outlet passage 33.
leaks to.
なお、勢い良くケーシング３１内周壁に当たった大径の
水分は飛散するが、空気導出路３３の外壁に阻止されて
下流側空気通路４１内に侵入することは防止される。Although the large-diameter water that hits the inner circumferential wall of the casing 31 with great force scatters, it is blocked by the outer wall of the air outlet passage 33 and is prevented from entering the downstream air passage 41.
［第１実施例］
第２図は、内燃機関のエアブラスト式燃料噴射システム
に本発明の気液分離装置を適用した例である。図におい
て、１は内燃機関の各気筒Ｓに空気を供給するための空
気供給路であり、該空気供給＃ｆ１は、途中分岐して、
吸入された空気の一部か分岐路１１より空気圧縮機２に
流入するようになしである。[First Embodiment] FIG. 2 is an example in which the gas-liquid separation device of the present invention is applied to an air blast type fuel injection system for an internal combustion engine. In the figure, 1 is an air supply path for supplying air to each cylinder S of the internal combustion engine, and the air supply #f1 branches in the middle,
A portion of the sucked air flows into the air compressor 2 through the branch path 11.
上記空気圧縮機２により加圧された空気は、上流側空気
通路たる圧縮空気路１２に吐出され、空気噴射弁４に送
られる。この圧縮空気路１２の途中には、詳細を後述す
る気液分離装置３が設けである。また、圧縮空気路の圧
力は、圧力調整器５により所定圧（ここでは、３ ｋｇ
／ ＝ｉ ＞に保持される。The air pressurized by the air compressor 2 is discharged into a compressed air passage 12, which is an upstream air passage, and is sent to an air injection valve 4. A gas-liquid separator 3, the details of which will be described later, is provided in the middle of this compressed air path 12. Moreover, the pressure of the compressed air path is set to a predetermined pressure (here, 3 kg) by the pressure regulator 5.
/ = i > is held.
燃料は、上記空気噴射弁４に近接する燃料噴射弁６より
、−旦、空気噴射弁４の圧縮空気ラインに噴射される。Fuel is first injected into the compressed air line of the air injection valve 4 from the fuel injection valve 6 adjacent to the air injection valve 4.
そして、空気噴射弁４が開弁すると同時に、圧縮空気と
共に内燃機関の気筒Ｓ内に噴射される。Then, at the same time as the air injection valve 4 opens, the air is injected into the cylinder S of the internal combustion engine together with the compressed air.
第１図には気液分離装置３の詳細を示す。図において、
気液分離装置３のケーシング３１は円筒体で、一方の端
面に上記圧縮空気路１２が同心状に接続してあり、他端
面は閉じている。FIG. 1 shows details of the gas-liquid separator 3. In the figure,
The casing 31 of the gas-liquid separator 3 is a cylindrical body, and the compressed air passage 12 is concentrically connected to one end surface of the casing 31, and the other end surface is closed.
上記ケーシング３］内には、圧縮空気の導入部に旋回流
発生器３２が設けである。旋回流発生器３２は円柱型で
、ケーシング３１と同心状に配され、支軸３２１により
支持されている。旋回流発生器３２は外周壁に複数の羽
根３２２を有し、これら羽根３２２は空気の流入方向に
対し、所定の角度傾けて取付けられている。また、旋回
流発生器３２の下流側端部はラッパ状に開いて、凝縮水
を分離する際のカイト部３２３となしである。Inside the casing 3, a swirl flow generator 32 is provided at the compressed air introduction section. The swirl flow generator 32 has a cylindrical shape, is arranged concentrically with the casing 31, and is supported by a support shaft 321. The swirling flow generator 32 has a plurality of blades 322 on the outer peripheral wall, and these blades 322 are attached at a predetermined angle with respect to the direction of air inflow. Further, the downstream end of the swirl flow generator 32 is opened in a trumpet shape, and there is no kite portion 323 for separating condensed water.
上記支軸３２１は、円板状の取付は部材３２４に支持せ
しめてあり、該取付は部材３２４はその外周をケーシン
グ３１にねし止めしである。取付は部材３２４は、ケー
シング３１の周壁に沿う開口３２５を有しており、導入
空気は、該開口３２５より、気液分離装置３内に流入す
る。The support shaft 321 is mounted in a disc shape and supported by a member 324, and the member 324 is mounted by screwing the outer periphery of the member 324 to the casing 31. The mounting member 324 has an opening 325 along the peripheral wall of the casing 31 , and the introduced air flows into the gas-liquid separation device 3 through the opening 325 .
旋回流発生器３２の下流には、空気導出路たる空気導出
管３３が、ケーシング３１と同心状に設けてあり、その
後端部はケーシング３１の閉鎖端面にねし止めされてい
る。空気導出管３３は、毛細管状の空隙を有する吸水材
がらなり、外周壁には多数の凹凸か形成しである。An air outlet pipe 33 serving as an air outlet path is provided downstream of the swirl flow generator 32 concentrically with the casing 31, and its rear end is screwed onto the closed end surface of the casing 31. The air outlet pipe 33 is made of a water-absorbing material having capillary-like voids, and has many irregularities formed on its outer peripheral wall.
ケーシング′３１の下方には、空気噴射弁４が配しであ
る。該空気噴射弁４より延びる下流側空気通路たる噴射
空気流ｎ４１は、ケーシング３１、および空気導出管３
３の管壁を貫通して、空気導出管３３内に突出しており
、空気導出管３３に流入した空気は、この噴射空気流路
４１を経て空気噴射弁４へ送られる。An air injection valve 4 is arranged below the casing '31. The injection air flow n41, which is a downstream air passage extending from the air injection valve 4, is connected to the casing 31 and the air outlet pipe 3.
3 and protrudes into the air outlet pipe 33, and the air flowing into the air outlet pipe 33 is sent to the air injection valve 4 via this injection air flow path 41.
上記空気導出管３３の外周に形成される空間は、旋回流
により外周方向に分離された水分の排出路３４としであ
る。上記排出８３４の下流側端部には、下方より圧力調
整器５が接続してあり、該圧力調整器５を介してリリー
フ空気通路５１と連通している。The space formed around the outer circumference of the air outlet pipe 33 serves as a discharge path 34 for moisture separated in the outer circumferential direction by the swirling flow. A pressure regulator 5 is connected to the downstream end of the discharge 834 from below, and communicates with the relief air passage 51 via the pressure regulator 5.
上記圧力調整器５は、弁体５２と、弁体５２を下方から
押圧するリターンスプリング５３とを有する。上記気液
分離装置３内の圧力が所定圧力を越えると、弁体５２は
、リターンスプリング５３のバネ力に抗して下方に押し
下げられ、リリーフ空気道ｆｆＪ５１を開いて、余分な
圧力をリリーフする。同時に、排出路３４に流入した水
分か排出される。The pressure regulator 5 has a valve body 52 and a return spring 53 that presses the valve body 52 from below. When the pressure inside the gas-liquid separator 3 exceeds a predetermined pressure, the valve body 52 is pushed down against the spring force of the return spring 53 to open the relief air passage ffJ51 and relieve the excess pressure. . At the same time, the moisture that has flowed into the discharge path 34 is discharged.
次に、本発明の気液分離装置の作用を説明する。Next, the operation of the gas-liquid separator of the present invention will be explained.
第２図において、分岐路１１より空気圧縮機２に流入し
た空気は、加圧され、圧縮空気路１２に吐出される。圧
縮空気中に含まれる水分は、圧縮空気路１２内で冷やさ
れて凝縮し、圧縮空気とともに、気液分離装置３内に流
入する。In FIG. 2, air flowing into the air compressor 2 from the branch path 11 is pressurized and discharged into the compressed air path 12. Moisture contained in the compressed air is cooled and condensed in the compressed air path 12, and flows into the gas-liquid separator 3 together with the compressed air.
第１図において、圧縮空気と凝縮水は、旋回流発生器３
２外用部の羽根３２２の取付角度に沿った旋回流となる
。この旋回流により凝縮水は外周方向に分離され、粒径
の大きな水滴はガイド部３２３で外側に振切られ、ケー
シング３１の内壁を伝わって排出路３４へ流入する。排
出路３４へ流入した凝縮水はリリーフ空気とともにリリ
ーフ空気道ＪｉＪ５１より排出される。この際、噴射空
気流路４１は空気導出管３３により保護され、分離され
た凝縮水が飛散して、空気噴射弁４へ流入することを防
いでいる。In Fig. 1, compressed air and condensed water are transferred to swirl flow generator 3.
A swirling flow follows the mounting angle of the blades 322 of the second external use part. This swirling flow separates the condensed water in the outer circumferential direction, and water droplets with large particle sizes are shaken off to the outside by the guide portion 323 and flow along the inner wall of the casing 31 into the discharge path 34 . The condensed water that has flowed into the discharge passage 34 is discharged from the relief air passage JiJ51 together with the relief air. At this time, the injection air passage 41 is protected by the air outlet pipe 33 to prevent the separated condensed water from scattering and flowing into the air injection valve 4.
一方、粒径の小さな水滴が、完全に分離されずに圧縮空
気とともに空気導出管３３に流入した場合にも、空気の
旋回流か維持されているため、水滴は外周方向に分離さ
れ、空気導出管３３の毛細管状空隙に速やかに吸収され
る。吸収された水分は、空気導出管３３外壁に設けた凹
凸により効率よく放散され、排出ｆ￥８３４からリリー
フ空気とともに排出される。On the other hand, even when water droplets with a small particle size are not completely separated and flow into the air outlet pipe 33 together with the compressed air, the swirling flow of air is maintained, so the water droplets are separated in the outer circumferential direction and the air outlet pipe 33 is not completely separated. It is quickly absorbed into the capillary space of the tube 33. The absorbed moisture is efficiently dissipated by the unevenness provided on the outer wall of the air outlet pipe 33, and is discharged from the exhaust f\834 together with the relief air.
このようにして、圧縮空気中の水分は確実に分離され、
凝縮水が空気噴射弁へ侵入することを阻止できる。In this way, moisture in the compressed air is reliably separated and
Condensed water can be prevented from entering the air injection valve.
［第２実施例］ 第３図には本発明の第２の実施例を示す。[Second example] FIG. 3 shows a second embodiment of the invention.
図において、気液分離装置３のケーシング３１は両端閉
鎖の円筒体であり、一方の端面に旋回流発生装置３２を
固定しである。圧縮空気路１２は、旋回流発生装置３２
下方のケーシング３１壁に垂直に接続され、旋回流発生
装置３２に接線方向より圧縮空気か流入するようになし
である。In the figure, a casing 31 of the gas-liquid separation device 3 is a cylindrical body with both ends closed, and a swirling flow generating device 32 is fixed to one end surface. The compressed air path 12 includes a swirl flow generator 32
It is connected perpendicularly to the wall of the lower casing 31 so that compressed air flows tangentially into the swirl flow generator 32.
圧縮空気路１２は、上記第１実施例の如くケーシング３
１と同心状に接続してし、本実施例の如く接線方向に設
けてもかまわない。The compressed air passage 12 is connected to the casing 3 as in the first embodiment.
1, and may be connected concentrically with 1, or may be provided in a tangential direction as in this embodiment.
旋回流発生器３２の下流には、空気導出管３３が、旋回
流発生器３２およびケーシング３１と同心状に配しであ
る。空気導出管３３は、ケーシング３１の端面を貫通し
て延ひ、下方に屈曲して圧力調整器５に接続されている
。空気導出管３３の途中には、空気噴射弁４か接続して
あり、噴射空気流Ｆ＃ｊ４１が空気導出管３３内に突出
開口している。An air outlet pipe 33 is arranged downstream of the swirl flow generator 32 and concentrically with the swirl flow generator 32 and the casing 31 . The air outlet pipe 33 extends through the end face of the casing 31, is bent downward, and is connected to the pressure regulator 5. An air injection valve 4 is connected in the middle of the air outlet pipe 33, and an injected air flow F#j41 projects into the air outlet pipe 33.
上記空気導出管３３の下方には、これとほぼ平行にドレ
ーン通路３５が配してあり、該ドレーン通路３５は上記
ケーシング３１の筒壁下端部に開口して排出路３４と連
通している。ここて、ドレーン通路３５はケーシング３
１との接続部において、ケーシング３１に空気の旋回方
向と同一の接線方向に開口している。また、ドレーン通
路３５の他端は、上記空気導出管３３と、空気噴射弁４
接続位置より下流で合流しており、圧力調整器５を介し
てリリーフ流路５］に連通している。A drain passage 35 is arranged below the air outlet pipe 33 and substantially parallel thereto, and the drain passage 35 opens at the lower end of the cylindrical wall of the casing 31 and communicates with the discharge passage 34 . Here, the drain passage 35 is connected to the casing 3
1, the opening is opened in the casing 31 in the same tangential direction as the swirling direction of the air. The other end of the drain passage 35 is connected to the air outlet pipe 33 and the air injection valve 4.
They merge downstream from the connection position and communicate with the relief channel 5 via the pressure regulator 5.
上記構成において、旋回流によって外周方向へ分離さｒ
ｔた凝縮水は、ケーシング３１内壁を伝って排出路３４
に流入し、ドレーン通路３５を経てリリーフ流路５］よ
り排出される。また、圧縮空気に混入して空気導出管３
３内に流入する一部の凝縮水は、旋回流が維持されてい
るため、外周方向へ分離されて空気導出管３３内壁下方
を伝わり、リリーフ流路５１から排出される。この時、
空気噴射弁４の噴射空気流路４１は、空気導出管３３の
内壁に対し、十分突出しているので、凝縮水が空気噴射
弁４内に流入することはない。In the above configuration, the swirling flow separates r toward the outer circumference.
The condensed water flows along the inner wall of the casing 31 and flows into the discharge passage 34.
and is discharged from the relief channel 5 through the drain passage 35. In addition, the compressed air may be mixed with the air outlet pipe 3.
Since a swirling flow is maintained, a part of the condensed water flowing into the air outlet pipe 33 is separated in the outer circumferential direction, travels below the inner wall of the air outlet pipe 33, and is discharged from the relief channel 51. At this time,
Since the injection air passage 41 of the air injection valve 4 protrudes sufficiently from the inner wall of the air outlet pipe 33, condensed water does not flow into the air injection valve 4.
［発明の効果］
以上のように、本発明の気液分離装置を使用すれば、空
気流路内を流通する水分を確実に分離、除去することが
できる。従って、例えば、エアブラスト式燃料噴射装置
に適用されて優れた効果を発揮し、凝縮水の空気噴射弁
への侵入を防止して、装置の信頼性を向上させることが
できる。[Effects of the Invention] As described above, by using the gas-liquid separator of the present invention, water flowing through the air flow path can be reliably separated and removed. Therefore, when applied to, for example, an air blast type fuel injection device, it can exhibit excellent effects, prevent condensed water from entering the air injection valve, and improve the reliability of the device.
第１図〜第２図は本発明の一実施例を示し、第１図は気
液分離装置の全体断面図、第２図は気液分離装置を内燃
機関のエアブラスト式燃料噴射装置に適用した例を示す
図、第３図は本発明の他の実施例を示す、気液分離装置
の全体断面図である。
１２・・・・・・圧縮空気路（上流側空気通路）３・・
・・・・気液分離装置
３１・・・・・・ケーシング
３２・・・・・・旋回流発生器
３３・・・・・・空気導出管（空気導出路）３４・・・
・・・排出路
４１・・・・・・噴射空気流Ｂ（下流側空気道Ｂ）第１
図
第２図Figures 1 and 2 show one embodiment of the present invention, with Figure 1 being an overall sectional view of a gas-liquid separation device, and Figure 2 showing the application of the gas-liquid separation device to an air blast type fuel injection device for an internal combustion engine. FIG. 3 is an overall sectional view of a gas-liquid separator according to another embodiment of the present invention. 12... Compressed air passage (upstream air passage) 3...
... Gas-liquid separator 31 ... Casing 32 ... Swirling flow generator 33 ... Air outlet pipe (air outlet path) 34 ...
...Discharge path 41...Injection air flow B (downstream airway B) first
Figure 2
Claims (1)
を分離する気液分離装置であって、密閉筒状ケーシング
内の一端に、軸心を一致せしめて旋回流発生器を設けて
、該旋回流発生器により上流側空気通路よりケーシング
内に導入される空気を旋回せしめてこれに含まれる水分
を遠心方向へ分離するようになすとともに、上記ケーシ
ングの内周壁を、上記分離された水分を捕集してケーシ
ング外へ排出する排出路となし、上記ケーシングよりも
小径で、一端が上記旋回流発生器に同心に対向して開口
する筒状空気導出路を設けて、該空気導出路の少なくと
も他端を上記排出路に連通せしめ、かつ、上記空気導出
路の路壁を貫通して下流側空気通路を開口せしめたこと
を特徴とする気液分離装置。A gas-liquid separator installed in the middle of a passage of air containing moisture to separate moisture from the air, in which a swirling flow generator is provided at one end of a sealed cylindrical casing with its axes aligned with each other. The swirling flow generator swirls the air introduced into the casing from the upstream air passage to separate moisture contained therein in a centrifugal direction, and the inner circumferential wall of the casing is used to remove the separated moisture. A cylindrical air outlet passage is provided which has a diameter smaller than that of the casing and has one end opening concentrically opposite the swirl flow generator. A gas-liquid separation device, characterized in that at least the other end thereof is communicated with the discharge passage, and a downstream air passage is opened by penetrating the wall of the air discharge passage.
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2095393A JPH03293009A (en) | 1990-04-11 | 1990-04-11 | Gas-liquid separator |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| JP2095393A JPH03293009A (en) | 1990-04-11 | 1990-04-11 | Gas-liquid separator |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| JPH03293009A true JPH03293009A (en) | 1991-12-24 |
Family
ID=14136408
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| JP2095393A Pending JPH03293009A (en) | 1990-04-11 | 1990-04-11 | Gas-liquid separator |
Country Status (1)
| Country | Link |
|---|---|
| JP (1) | JPH03293009A (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004509733A (en) * | 2000-06-06 | 2004-04-02 | バッテル メモリアル インスティテュート | Microsystem capillary separation |
| WO2005018779A1 (en) * | 2003-08-26 | 2005-03-03 | Hydrogenics Corporation | Apparatus for separating liquid from a process gas stream of an electrochemical cell stack |
| WO2005018778A1 (en) * | 2003-08-26 | 2005-03-03 | Hydrogenics Corporation | An energy and/or mass exchange apparatus having an integrated fluid separator |
| WO2005028077A1 (en) * | 2003-09-22 | 2005-03-31 | Hydrogenics Corporation | Separator for removing liquid from fluid |
| JP2021005498A (en) * | 2019-06-26 | 2021-01-14 | アイシン精機株式会社 | Gas-liquid separator |
-
1990
- 1990-04-11 JP JP2095393A patent/JPH03293009A/en active Pending
Cited By (9)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JP2004509733A (en) * | 2000-06-06 | 2004-04-02 | バッテル メモリアル インスティテュート | Microsystem capillary separation |
| WO2005018779A1 (en) * | 2003-08-26 | 2005-03-03 | Hydrogenics Corporation | Apparatus for separating liquid from a process gas stream of an electrochemical cell stack |
| WO2005018778A1 (en) * | 2003-08-26 | 2005-03-03 | Hydrogenics Corporation | An energy and/or mass exchange apparatus having an integrated fluid separator |
| JP2007503295A (en) * | 2003-08-26 | 2007-02-22 | ハイドロジェニクス コーポレイション | Energy and / or mass exchanger integrated with fluid separator |
| JP2007503296A (en) * | 2003-08-26 | 2007-02-22 | ハイドロジェニクス コーポレイション | Apparatus for separating liquid from process gas stream of an electrochemical cell stack |
| US7311765B2 (en) | 2003-08-26 | 2007-12-25 | Hydrogenics Corporation | Energy and/or mass exchange apparatus having an integrated fluid separator |
| US7338545B2 (en) | 2003-08-26 | 2008-03-04 | Hydrogenics Corporation | Apparatus for separating liquid from a process gas stream of an electrochemical cell stack |
| WO2005028077A1 (en) * | 2003-09-22 | 2005-03-31 | Hydrogenics Corporation | Separator for removing liquid from fluid |
| JP2021005498A (en) * | 2019-06-26 | 2021-01-14 | アイシン精機株式会社 | Gas-liquid separator |
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