JP2001003818A - Gas-liquid separating device - Google Patents

Gas-liquid separating device

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Publication number
JP2001003818A
JP2001003818A JP11171803A JP17180399A JP2001003818A JP 2001003818 A JP2001003818 A JP 2001003818A JP 11171803 A JP11171803 A JP 11171803A JP 17180399 A JP17180399 A JP 17180399A JP 2001003818 A JP2001003818 A JP 2001003818A
Authority
JP
Japan
Prior art keywords
gas
liquid
outlet pipe
opening
liquid separation
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
Application number
JP11171803A
Other languages
Japanese (ja)
Inventor
Hitoshi Sakakibara
仁 榊原
Tomozo Toki
朋造 土岐
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Aisan Industry Co Ltd
Original Assignee
Aisan Industry Co Ltd
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 Aisan Industry Co Ltd filed Critical Aisan Industry Co Ltd
Priority to JP11171803A priority Critical patent/JP2001003818A/en
Publication of JP2001003818A publication Critical patent/JP2001003818A/en
Pending legal-status Critical Current

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  • Supplying Secondary Fuel Or The Like To Fuel, Air Or Fuel-Air Mixtures (AREA)

Abstract

PROBLEM TO BE SOLVED: To prevent a liquid phase fuel from invading to a canister by connecting an inlet pipe to a lower end part of a gas-liquid separating chamber, opening an outlet pipe to the inside of the gas-liquid separating chamber, and arranging foaming eliminating means for bursting air bubbles generated at an opening part of the inlet pipe before it reaches an opening part of the outlet pipe. SOLUTION: When gasoline steam flows from an opening part 6 into a bubble passage 14 through an inlet pipe 5 by positive pressure in a fuel tank, bubbles are generated at the opening part 6 at the time of flow-in, and air bubbles are generated. When the air bubbles grow, its liquid film is burst by foam eliminating member 18 such as continuous air bubble urethane. As a result, it is obstructed by a partition wall 10 that liquid phase fuel forming a liquid film is invaded from a gas communicating passage 13 into a liquid reservoir chamber 15, it drops downward the bubble passage 14, and flows to a liquid phase part of the liquid reservoir chamber 15 bypassing liquid communicating passages 16, 17 formed on both side of the bubble passage 14. On the other hand, air phase fuel is raised in the bubble passage 14, and is entered into the gas-liquid separating chamber 3 to lead to a canister bypassing the outlet pipe 7 and the like.

Description

【発明の詳細な説明】DETAILED DESCRIPTION OF THE INVENTION

【0001】[0001]

【発明の属する技術分野】本発明は気液分離装置に関す
るもので、より詳しくは、内燃機関における例えば燃料
タンクから蒸発した蒸発燃料を捕集し、これを吸気系に
放出する蒸発燃料処理装置において、前記キャニスタへ
吸入されるガソリン蒸気を気相燃料と液相燃料に分離す
る装置に関する。
BACKGROUND OF THE INVENTION 1. Field of the Invention The present invention relates to a gas-liquid separation device, and more particularly, to an evaporative fuel treatment device for collecting evaporative fuel evaporated from a fuel tank in an internal combustion engine and discharging the same to an intake system. And a device for separating gasoline vapor sucked into the canister into gaseous fuel and liquid fuel.

【0002】[0002]

【従来の技術】従来、図5に示すように、車両に搭載し
た燃料タンク101の気相部と、活性炭等の吸着剤10
2を収納したキャニスタ103との連通路104に気液
分離装置105を設け、燃料タンク101の気相部で発
生したガソリン蒸気を、連通路104で気液分離装置1
05の気液分離室106内に導入して該気液分離室10
6内で気相燃料と液相燃料に分離し、気相燃料のみをキ
ャニスタ103へ導入して、キャニスタ103内の吸着
剤102に液相燃料の高沸点分が付着して吸着剤102
が劣化するのを防止する目的の蒸発燃料処理装置が知ら
れている。
2. Description of the Related Art Conventionally, as shown in FIG. 5, a gas phase portion of a fuel tank 101 mounted on a vehicle and an adsorbent 10 such as activated carbon are used.
A gas-liquid separation device 105 is provided in a communication passage 104 with the canister 103 containing the gas tank 2, and gasoline vapor generated in a gas phase portion of the fuel tank 101 is passed through the communication passage 104 to the gas-liquid separation device 1.
05 into the gas-liquid separation chamber 106
6, the gaseous fuel and the liquid phase fuel are separated, only the gaseous fuel is introduced into the canister 103, and the high boiling point of the liquid phase fuel adheres to the adsorbent 102 in the canister 103 and the adsorbent 102
There is known an evaporative fuel processing apparatus for preventing deterioration of the fuel.

【0003】そして、前記気液分離装置105として、
図5に示すように、前記連通路104に連通する入口パ
イプ(タンクポート)107の開口部108を気液分離
室106の上部に開口し、キャニスタ103へ連通する
出口パイプ109を気液分離室106の中央部に立ち上
げてその上端を気液分離室106内へ開口したものが、
例えば特開平8−158958号公報に開示されてい
る。
[0003] As the gas-liquid separation device 105,
As shown in FIG. 5, an opening 108 of an inlet pipe (tank port) 107 communicating with the communication passage 104 is opened above the gas-liquid separation chamber 106, and an outlet pipe 109 communicating with the canister 103 is connected to the gas-liquid separation chamber. The one which is set up at the center of 106 and whose upper end is opened into the gas-liquid separation chamber 106 is
For example, it is disclosed in JP-A-8-158958.

【0004】しかし、前記のように入口パイプ107の
開口部108を気液分離室106の上部に開口したもの
においては、燃料タンク101が冷えたときの燃料タン
ク101内の負圧によって、気液分離室106内に溜っ
た液相燃料を入口パイプ107を通じて燃料タンク10
1へ逆流させる効果が少なく、液相燃料が気液分離室1
06内に溜りつづける問題がある。
However, in the case where the opening 108 of the inlet pipe 107 is opened at the upper part of the gas-liquid separation chamber 106 as described above, the gas-liquid pressure is reduced by the negative pressure in the fuel tank 101 when the fuel tank 101 is cooled. The liquid fuel stored in the separation chamber 106 is supplied to the fuel tank 10 through the inlet pipe 107.
The effect of backflow to the liquid 1 is small, and the liquid-phase fuel is
There is a problem that it stays in 06.

【0005】そこで、この問題を解決するために、本出
願人は先に図6に示すように、気液分離装置201にお
ける気液分離室202の中央部に前記と同様の出口パイ
プ203を立設するとともに、その上端の開口部204
を気液分離室202に開口し、気液分離室の下端部に入
口パイプ205の開口部206を開口し、気液分離室2
02内に溜った液相燃料を入口パイプ205を通じて燃
料タンクへ容易に逆流するようにしたものを提案した
(特願平10−119837号)。
In order to solve this problem, the present applicant has previously set up an outlet pipe 203 similar to the above at the center of a gas-liquid separation chamber 202 in a gas-liquid separation device 201 as shown in FIG. And an opening 204 at the upper end thereof.
Is opened in the gas-liquid separation chamber 202, and an opening 206 of the inlet pipe 205 is opened at the lower end of the gas-liquid separation chamber.
Japanese Patent Application No. Hei 10-119837 proposes that the liquid fuel stored in the fuel tank 02 is easily returned to the fuel tank through the inlet pipe 205.

【0006】[0006]

【発明が解決しようとする課題】しかし、前記図6に示
すように、入口パイプ205の開口部206を気液分離
室202の下端部に開口したものにおいては、燃料タン
クの気相部から入口パイプ205内へ導入された空気混
じりの燃料が入口パイプ205の開口部206から気液
分離室202内へ流入する際に図7に示すように泡立
ち、その気泡が成長して図7に示すように、その気泡を
形成する液膜300が出口パイプ203の開口部204
まで盛り上がって達し、ガソリン蒸気が出口パイプ20
3の開口部204からキャニスタへ吸引される際に、そ
の流れによって前記の液膜300が出口パイプ203か
らキャニスタへ吸引され、前記のキャニスタ内の吸着剤
102が劣化する問題がある。
However, when the opening 206 of the inlet pipe 205 is opened at the lower end of the gas-liquid separation chamber 202 as shown in FIG. When the air-mixed fuel introduced into the pipe 205 flows into the gas-liquid separation chamber 202 from the opening 206 of the inlet pipe 205, the fuel bubbles as shown in FIG. 7, and the bubbles grow as shown in FIG. In the meantime, the liquid film 300 forming the bubble is formed in the opening 204 of the outlet pipe 203.
Gasoline vapor reaches the outlet pipe 20
When the liquid film 300 is sucked from the opening 204 into the canister by the flow, the liquid film 300 is sucked from the outlet pipe 203 into the canister, and there is a problem that the adsorbent 102 in the canister is deteriorated.

【0007】そこで本発明は、前記のような燃料の泡立
ちにより発生した気泡を、出口パイプに達する以前に破
裂させて、前記のように液膜が出口パイプから吸引され
ることによる問題を解決することを目的とするものであ
る。
Therefore, the present invention solves the problem caused by the above-mentioned bubbles generated by bubbling of fuel being ruptured before reaching the outlet pipe, and the liquid film being sucked from the outlet pipe as described above. The purpose is to do so.

【0008】[0008]

【課題を解決するための手段】本発明は前記の課題を解
決するために、請求項1記載の第1の発明は、気液分離
室の下端部に入口パイプの開口部を設け、気液分離室に
出口パイプを開口し、気液分離室内に、前記入口パイプ
の開口部で発生した気泡の液膜を前記出口パイプの開口
部に達する以前に破裂させる消泡手段を設けたことを特
徴とするものである。
According to a first aspect of the present invention, an opening for an inlet pipe is provided at a lower end of a gas-liquid separation chamber. An outlet pipe is opened in the separation chamber, and defoaming means is provided in the gas-liquid separation chamber to burst a liquid film of bubbles generated at the opening of the inlet pipe before reaching the opening of the outlet pipe. It is assumed that.

【0009】気液分離室の下端部に入口パイプの開口部
を設けると、その開口部からガソリン蒸気が気液分離室
に流入する際に開口部から気泡が発生する。本発明はこ
の気泡の液膜を前記出口パイプの開口部に達する以前に
破裂させる消泡手段を設けたので、気泡を形成する液膜
が気液分離室に設けた出口パイプの開口部から吸入され
ることが防止され、液相燃料がキャニスタへ吸入される
ことを抑制する。
When an opening of the inlet pipe is provided at the lower end of the gas-liquid separation chamber, gas bubbles are generated from the opening when gasoline vapor flows into the gas-liquid separation chamber from the opening. Since the present invention is provided with defoaming means for rupture of the liquid film of the bubbles before reaching the opening of the outlet pipe, the liquid film forming the bubbles is sucked from the opening of the outlet pipe provided in the gas-liquid separation chamber. Is prevented, and the liquid fuel is prevented from being sucked into the canister.

【0010】請求項2記載の第2の発明は、気液分離室
の下部に位置して入口パイプを開口し、気液分離室の略
中央部に位置して出口パイプを立設してその上端を気液
分離室に開口し、前記入口パイプの開口部と前記出口パ
イプの間に区画壁を設けて、この区画壁により入口パイ
プの開口部側に気泡通路を、出口パイプ側に液溜め室を
区画して設け、前記気泡通路内に泡切り部材を設置し、
前記区画壁の上部には前記気泡通路と液溜め室とを連通
する気体連通路を設け、前記気泡通路の底部と液溜め室
の底部を一部において液体連通路で連通したことを特徴
とするものである。
According to a second aspect of the present invention, an inlet pipe is opened at a lower portion of the gas-liquid separation chamber, and an outlet pipe is provided upright at a substantially central portion of the gas-liquid separation chamber. An upper end is opened to the gas-liquid separation chamber, and a partition wall is provided between the opening of the inlet pipe and the outlet pipe. The partition wall forms a bubble passage on the opening side of the inlet pipe and a liquid reservoir on the outlet pipe side. A chamber is provided, and a bubble breaker is installed in the bubble passage;
A gas communication path is provided at an upper portion of the partition wall for communicating the bubble passage with the liquid reservoir, and a bottom of the bubble passage and a bottom of the liquid reservoir are partially communicated with each other by a liquid communication passage. Things.

【0011】本発明においては、気液分離室の下端部に
開口した入口パイプの開口部からガソリン蒸気が気液分
離室に流入する際に発生した気泡は、区画壁によって液
溜め室に流入することなく気泡通路を上昇する。この上
昇時において気泡の液膜は、消泡手段である泡切り部材
により破裂し消泡される。この破裂により気相燃料と液
相燃料に分離され、気相燃料は上昇して区画壁の上部に
形成した気体連通路から出口パイプの開口部へ流れ、液
相燃料は落下して気泡通路の底部に形成した液体連通路
から液溜め室へ流出する。したがって、気泡を形成する
液膜が出口パイプに達することが防止され、液相燃料が
キャニスタへ吸入されることを抑制する。
In the present invention, gas bubbles generated when gasoline vapor flows into the gas-liquid separation chamber from the opening of the inlet pipe opened at the lower end of the gas-liquid separation chamber flows into the liquid storage chamber by the partition wall. Ascends the bubble path without. At the time of this rising, the liquid film of the bubbles is ruptured and defoamed by the defoaming member which is the defoaming means. This rupture separates the gaseous fuel and the liquid-phase fuel, the gaseous fuel rises and flows from the gas communication passage formed at the upper part of the partition wall to the opening of the outlet pipe, and the liquid-phase fuel falls and falls into the bubble passage. The liquid flows out of the liquid communication passage formed at the bottom into the liquid storage chamber. Therefore, the liquid film forming bubbles is prevented from reaching the outlet pipe, and the liquid fuel is prevented from being sucked into the canister.

【0012】請求項3記載の第3の発明は、気液分離室
の下部に位置して入口パイプを開口し、気液分離室の略
中央部に位置して出口パイプを立設してその上端を気液
分離室に開口し、前記出口パイプの周囲に区画壁を設け
て、該区画壁と気液分離室を構成する周壁とで環状の気
泡通路を形成するとともに区画壁の内側に液溜め室を形
成し、前記気泡通路の上部を、前記入口パイプの開口部
と反対方向において前記液溜め室に連通し、気泡通路の
少なくとも一部の下端部を液溜め室に連通したことを特
徴とするものである。
According to a third aspect of the present invention, an inlet pipe is opened at a lower portion of the gas-liquid separation chamber, and an outlet pipe is provided upright at a substantially central portion of the gas-liquid separation chamber. An upper end is opened to the gas-liquid separation chamber, a partition wall is provided around the outlet pipe, and an annular bubble passage is formed by the partition wall and a peripheral wall constituting the gas-liquid separation chamber, and a liquid is formed inside the partition wall. A reservoir is formed, an upper portion of the bubble passage communicates with the reservoir in a direction opposite to an opening of the inlet pipe, and a lower end of at least a part of the bubble passage communicates with the reservoir. It is assumed that.

【0013】本発明においては、気液分離室の下端部に
開口した入口パイプの開口部からガソリン蒸気が気液分
離室に流入する際に発生した気泡は、区画壁によって液
溜め室に流入することなく環状の気泡通路を通って、入
口パイプの開口部と反対側へ移動する。この長い環状の
気泡通路を気泡が通る際に、この気泡通路を形成する広
い壁面に気泡が接触し、この壁面が消泡手段となって気
液の液膜が破裂される。この破裂により気相燃料と液相
燃料に分離され、その気相燃料は入口パイプの開口部と
反対側から出口パイプの開口部へ流れ、液相燃料は落下
して気泡通路の下端から液溜め室の底部へ流出する。し
たがって、気泡を形成する液膜が出口パイプへ吸入され
ることを抑制する。
In the present invention, gas bubbles generated when gasoline vapor flows into the gas-liquid separation chamber from the opening of the inlet pipe opened at the lower end of the gas-liquid separation chamber flows into the liquid storage chamber by the partition wall. Without passing through the annular bubble passage to the side opposite to the opening of the inlet pipe. When the air bubbles pass through the long annular air bubble passage, the air bubbles come into contact with a wide wall surface forming the air bubble passage, and the wall surface serves as a defoaming means, and the liquid film of gas-liquid is ruptured. This rupture separates the fuel into gaseous fuel and liquid fuel.The gaseous fuel flows from the side opposite to the opening of the inlet pipe to the opening of the outlet pipe. Spills to bottom of chamber. Therefore, the liquid film forming the bubbles is prevented from being sucked into the outlet pipe.

【0014】しかも、前記第2の発明においては、その
泡切り部材が液相燃料を保有しやすいため、この保有さ
れた液相燃料が次に流入するガソリン蒸気の圧力により
液溜め室へ押し出されるおそれがあるが、本第3の発明
では、前記の泡切り部材がなく、消泡作用は広い壁面で
行われるため前記のおそれはない。したがって、液膜が
出口パイプへ吸入されることを一層抑制する。
Moreover, in the second aspect of the present invention, since the bubble cutting member easily holds the liquid phase fuel, the held liquid phase fuel is pushed out to the liquid storage chamber by the pressure of the gasoline vapor flowing in next. Although there is a possibility, in the third aspect of the present invention, there is no such a possibility because the bubble removing member is not provided and the defoaming action is performed on a wide wall surface. Therefore, the liquid film is further suppressed from being sucked into the outlet pipe.

【0015】そして、請求項4記載の第4の発明は、前
記第3の発明において、前記気泡通路の上部における液
溜め室への開口部と前記出口パイプ間に、液溜め室への
開口部から流出する気相燃料を出口パイプに直接当たら
ないようにする変向板を設けたことを特徴とするもので
ある。
According to a fourth aspect of the present invention, in the third aspect of the present invention, an opening to the liquid reservoir is provided between the opening to the liquid reservoir above the bubble passage and the outlet pipe. A turning plate is provided to prevent the gaseous fuel flowing out of the outlet from directly hitting the outlet pipe.

【0016】本発明においては、前記気泡通路から流出
した気相燃料は変向板に当り、出口パイプの開口部へ直
接流入することが阻止される。しかもこの変向板によっ
ても消泡される。したがって、気泡を形成する液膜が出
口パイプへ吸入されることをより一層抑制する。
In the present invention, the gaseous fuel flowing out of the bubble passage hits the deflection plate and is prevented from flowing directly into the opening of the outlet pipe. Moreover, the defoaming is also performed by the deflection plate. Therefore, the liquid film forming the bubbles is further suppressed from being sucked into the outlet pipe.

【0017】[0017]

【発明の実施の形態】図1乃至図4に示す実施例に基い
て本発明の実施の形態について説明する。図1及び図2
は第1実施例を示すもので、図1は気液分離装置を示
し、図2は図1の装置における泡の発生状態を示す。
DETAILED DESCRIPTION OF THE PREFERRED EMBODIMENTS An embodiment of the present invention will be described based on an embodiment shown in FIGS. 1 and 2
1 shows a first embodiment, FIG. 1 shows a gas-liquid separation device, and FIG. 2 shows a state of generation of bubbles in the device of FIG.

【0018】図1において、気液分離装置1Aを構成す
るケース2内には気液分離室3が形成されている。ケー
ス2の周壁4には入口パイプ5が、その開口部6を周壁
4の下端部、すなわち気液分離室3の下端部に位置させ
て設けられている。該入口パイプ5は、前記図5に示す
ように燃料タンク101の気相部へ連通される。
In FIG. 1, a gas-liquid separation chamber 3 is formed in a case 2 constituting the gas-liquid separation device 1A. An inlet pipe 5 is provided on the peripheral wall 4 of the case 2 with its opening 6 located at the lower end of the peripheral wall 4, that is, at the lower end of the gas-liquid separation chamber 3. The inlet pipe 5 communicates with the gas phase of the fuel tank 101 as shown in FIG.

【0019】前記気液分離室3の中央部には出口パイプ
7が立設されており、該出口パイプ7の入口側の開口部
8は気液分離室3の上部に位置して開口し、出口側は連
通パイプ9に連通されている。そして、この連通パイプ
9は前記図5に示すようにキャニスタ103に連通され
る。
An outlet pipe 7 is provided upright at the center of the gas-liquid separation chamber 3, and an opening 8 on the inlet side of the outlet pipe 7 is located above the gas-liquid separation chamber 3 and opens. The outlet side is connected to a communication pipe 9. The communication pipe 9 is communicated with the canister 103 as shown in FIG.

【0020】気液分離室3内には、前記入口パイプ5の
開口部6と前記出口パイプ7との間に位置して区画壁1
0が設けられている。該区画壁10は気液分離室3の底
壁11に密着した状態で立設され、その高さH1 は、そ
の上端面10aと気液分離室3の上壁12との間に気体
連通路13が形成されるように設定されている。また、
この区画壁10の高さH1 と前記出口パイプ7の高さH
2 との関係は、H1 >H2 に設定されている。更に、区
画壁10はケース2の周壁4の内周面から内側へ所定距
離D1 だけ離れ、かつ周壁4に沿った半円状に配置され
ており、該区画壁10と周壁4間において半円状の気泡
通路14が形成され、区画壁10と出口パイプ7間に液
溜め室15が形成されている。また、区画壁10は入口
パイプ5の開口部6を中心として両側方へ均等に配置さ
れている。更に、区画壁10の両側端部10b,10c
は周壁4と離間しており、該両側端部10b,10cと
周壁4との間に、前記気泡通路14と液溜め室15とを
連通する液体連通路16,17が、少なくとも底部が連
通されるようにして形成されている。
In the gas-liquid separation chamber 3, the partition wall 1 is located between the opening 6 of the inlet pipe 5 and the outlet pipe 7.
0 is provided. The partition wall 10 is erected in close contact with the bottom wall 11 of the gas-liquid separation chamber 3, and has a height H 1 between the upper end face 10 a and the upper wall 12 of the gas-liquid separation chamber 3. The passage 13 is set to be formed. Also,
The height H 1 of the partition wall 10 and the height H of the outlet pipe 7
Relationship and 2, is set to H 1> H 2. Further, the partition wall 10 is arranged inwardly from the inner peripheral surface of the peripheral wall 4 of the case 2 by a predetermined distance D 1 and is arranged in a semicircular shape along the peripheral wall 4, and a half circle is formed between the partition wall 10 and the peripheral wall 4. A circular bubble passage 14 is formed, and a liquid reservoir 15 is formed between the partition wall 10 and the outlet pipe 7. The partition walls 10 are evenly arranged on both sides with the opening 6 of the inlet pipe 5 as a center. Furthermore, both end portions 10b, 10c of the partition wall 10
Are separated from the peripheral wall 4, and liquid communication passages 16, 17 for communicating the bubble passage 14 and the liquid storage chamber 15 at least at the bottom thereof are provided between the side ends 10 b, 10 c and the peripheral wall 4. It is formed in such a manner.

【0021】前記気泡通路14内には気泡の液膜を破裂
させる消泡手段としての泡切り部材18が収納されてい
る。該泡切り部材18としては例えば体内に連続した気
泡を有するスポンジやウレタン(ハニカム状の連続気泡
ウレタン)などを使用する。この泡切り部材18は、そ
の外周面を周壁4に密着させ、内周面を区画壁10に密
着させ、下端面を底壁11に密着させて、気泡通路14
の全体を埋めるように配置されている。これにより、泡
切り部材18は前記入口パイプ5の開口部6に密着して
いる。更に、泡切り部材18は区画壁10の上端面10
aまで設けられており、その泡切り部材18の上端は前
記出口パイプ7の開口部8の上端面よりも上方に位置し
ている。
In the bubble passage 14, a bubble removing member 18 as a defoaming means for bursting a liquid film of bubbles is accommodated. As the bubble removing member 18, for example, a sponge or urethane (honeycomb open cell urethane) having continuous cells in the body is used. The bubble removing member 18 has an outer peripheral surface in close contact with the peripheral wall 4, an inner peripheral surface in close contact with the partition wall 10, and a lower end surface in close contact with the bottom wall 11.
It is arranged to fill the whole. Thereby, the bubble removing member 18 is in close contact with the opening 6 of the inlet pipe 5. Further, the bubble-cutting member 18 is provided on the upper end face 10 of the partition wall 10.
a, and the upper end of the bubble removing member 18 is located above the upper end surface of the opening 8 of the outlet pipe 7.

【0022】以上の構造において、燃料タンク内の正圧
によりガソリン蒸気が入口パイプ5を通じてその開口部
6から気泡通路14内に流入すると、その流入の際に図
2に示すように開口部6で泡立ち、その気泡により液膜
19が発生する。しかし、その気泡が成長すると、その
液膜19は泡切り部材18により破裂する。この破裂に
より液膜19を形成していた液相燃料は区画壁10によ
り気体連通路13からの液溜め室15内への浸入が阻止
されて気泡通路14の下方へ落下し、気泡通路14の両
側に形成された液体連通路16,17を通って液溜め室
15の液相部へ流入する。
In the above structure, when gasoline vapor flows into the bubble passage 14 from the opening 6 through the inlet pipe 5 due to the positive pressure in the fuel tank, the gas flows through the opening 6 as shown in FIG. The liquid film 19 is generated by the bubbles and the bubbles. However, when the bubble grows, the liquid film 19 is ruptured by the bubble breaker 18. The liquid fuel having formed the liquid film 19 due to the rupture is prevented from entering the liquid storage chamber 15 from the gas communication passage 13 by the partition wall 10 and falls below the bubble passage 14. The liquid flows into the liquid phase portion of the liquid storage chamber 15 through the liquid communication passages 16 and 17 formed on both sides.

【0023】また、液膜19の破裂により、その気相燃
料は気泡通路14内を上昇し、区画壁10の上部に形成
された気体連通路13を通じて液溜め室15の上部へ流
入する。
Further, due to the rupture of the liquid film 19, the gaseous fuel rises in the bubble passage 14 and flows into the upper part of the liquid reservoir 15 through the gas communication passage 13 formed in the upper part of the partition wall 10.

【0024】前記の泡立ちは主として入口パイプ5の開
口部6の入口付近で発生するため、気泡通路14内は図
2(b)に示すように、D2 の範囲が気相部となり、D
3 の範囲が液相部となる。また、図2(a)に示す気泡
通路14の範囲D1 は泡立つが、この泡立ちは区画壁1
0によって液溜め室15内に伝達されず、D4 の範囲で
示す液溜め室15内の液相燃料は安定する。
Since the bubbling mainly occurs near the entrance of the opening 6 of the inlet pipe 5, the area of D 2 in the bubble passage 14 becomes a gas phase as shown in FIG.
The range of 3 is the liquid phase. Although foaming ranges D 1 of the bubble passageway 14 shown in FIG. 2 (a), the foaming partition wall 1
0 is not transmitted to the liquid reservoir chamber 15 by the liquid phase fuel in the liquid reservoir chamber 15 indicated by a range of D 4 is stabilized.

【0025】以上のようであるから、出口パイプ7の開
口部8からはほぼ気相燃料のみが吸入されることにな
り、前記従来のように開口部8から気泡の液膜、すなわ
ち液相燃料が吸入されてキャニスタの吸着剤を劣化させ
ることを防止できる。
As described above, almost only the gaseous phase fuel is sucked from the opening 8 of the outlet pipe 7, and the liquid film of bubbles, ie, the liquid phase Can be prevented from deteriorating the adsorbent of the canister by being sucked.

【0026】次に図3及び図4に示す第2実施例につい
て説明する。図3は気液分離装置を示し、図4は図3の
装置における泡の発生状態を示す。気液分離装置1Bを
構成するケース2内には気液分離室3が形成されてい
る。ケース2の周壁4には、前記第1実施例と同様の入
口パイプ5が、その開口部6をケース2の周壁4の下端
部、すなわち気液分離室3の下端部に位置させて設けら
れている。
Next, a second embodiment shown in FIGS. 3 and 4 will be described. FIG. 3 shows a gas-liquid separation device, and FIG. 4 shows a state of generation of bubbles in the device of FIG. A gas-liquid separation chamber 3 is formed in a case 2 constituting the gas-liquid separation device 1B. An inlet pipe 5 similar to that of the first embodiment is provided on the peripheral wall 4 of the case 2 with the opening 6 located at the lower end of the peripheral wall 4 of the case 2, that is, at the lower end of the gas-liquid separation chamber 3. ing.

【0027】前記気液分離室3の中央部には出口パイプ
7が立設されており、該出口パイプ7の入口側の開口部
8は気液分離室3の上部に位置して開口し、出口側は前
記第1実施例と同様の連通パイプ9に連通されている。
An outlet pipe 7 is provided upright at the center of the gas-liquid separation chamber 3, and an opening 8 on the inlet side of the outlet pipe 7 is located above the gas-liquid separation chamber 3 and opens. The outlet side is connected to a communication pipe 9 similar to the first embodiment.

【0028】前記気液分離室3内には、前記の出口パイ
プ7の外周部を囲むように区画壁20が配置されてい
る。更に、該区画壁20は、周壁4と出口パイプ7との
間において出口パイプ7と同芯状に円筒状に形成されて
おり、該区画壁20と周壁4間に所定幅D5 の環状空間
からなる気泡通路21を形成し、区画壁20と出口パイ
プ7間に直径をD6 とする液溜め室15が形成されてい
る。
A partition wall 20 is arranged in the gas-liquid separation chamber 3 so as to surround the outer peripheral portion of the outlet pipe 7. Further, the partition wall 20 is formed in a cylindrical shape concentric with the outlet pipe 7 between the peripheral wall 4 and the outlet pipe 7, and an annular space having a predetermined width D 5 is formed between the partition wall 20 and the peripheral wall 4. A liquid reservoir chamber 15 having a diameter of D 6 is formed between the partition wall 20 and the outlet pipe 7.

【0029】前記区画壁20の上部には、前記出口パイ
プ7を挟んで前記入口パイプ5の開口部6と反対方向に
位置して気体連通路22が形成されている。更に、該気
体連通路22部を除く区画壁20の上端はケース2の上
壁12の内面に密着している。また、底壁11の内面か
ら前記気体連通路22の底面までの高さH3 は、底壁1
1の内面から前記出口パイプ7の上端面までの高さH2
よりも高い位置に設定されている。
A gas communication passage 22 is formed above the partition wall 20 in a direction opposite to the opening 6 of the inlet pipe 5 with the outlet pipe 7 interposed therebetween. Further, the upper end of the partition wall 20 excluding the gas communication passage 22 is in close contact with the inner surface of the upper wall 12 of the case 2. The height H 3 from the inner surface of the bottom wall 11 to the bottom surface of the gas communication passage 22 is equal to the height of the bottom wall 1.
Height H 2 from the inner surface 1 to the upper end surface of the outlet pipe 7
Is set at a higher position.

【0030】なお、気体連通路22が開口部6と正反対
側に位置する場合は、高さH3 が高さH2 と同等または
それ以下でもよい。更に、前記区画壁20の下端は、前
記出口パイプ7から連通パイプ9への水平パイプ部9a
を除いて底壁11から離間しており、区画壁20の下端
と底壁11との間に、前記気泡通路21と液溜め室15
とを連通する液体連通路23が形成されている。また、
底壁11の内面から区画壁20の下端面までの高さH4
は、底壁11の内面から入口パイプ5の開口部6の上端
6aまでの高さH5 よりも低く設定されている。
[0030] In the case where the gas communicating passage 22 is located diametrically opposite the opening 6, the height H 3 is the height H 2 and equal to or may be less. Further, a lower end of the partition wall 20 is provided with a horizontal pipe portion 9a from the outlet pipe 7 to the communication pipe 9.
Except for the bubble passage 21 and the liquid storage chamber 15 between the bottom end of the partition wall 20 and the bottom wall 11.
And a liquid communication passage 23 is formed. Also,
Height H 4 from the inner surface of the bottom wall 11 to the lower end surface of the partition wall 20
It is set lower than the height H 5 from the inner surface to the top edge 6a of the opening 6 of the inlet pipe 5 of the bottom wall 11.

【0031】前記液溜め室15内には、前記気体連通路
22と出口パイプ7の間に位置して変向板24が、図2
(b)に示すように平面的に見て気体連通路22からの
流出方向に対して傾斜して配置されており、前記気体連
通路22から液溜め室15内へ流入する気相燃料が出口
パイプ7の開口部8へ直接侵入しないようになってい
る。そして、該変向板24に当たった気相燃料は、該変
向板24と区画壁20との間の隙間からなる出口路25
から出口パイプ7側へ回り込むようになっている。
In the liquid storage chamber 15, a deflecting plate 24 is provided between the gas communication passage 22 and the outlet pipe 7 as shown in FIG.
As shown in (b), the gaseous fuel flowing from the gas communication passage 22 into the liquid storage chamber 15 is disposed at an angle with respect to the outflow direction from the gas communication passage 22 when viewed in plan. It does not directly enter the opening 8 of the pipe 7. Then, the gaseous phase fuel hitting the deflecting plate 24 is transferred to an exit passage 25 formed by a gap between the deflecting plate 24 and the partition wall 20.
From the outlet pipe 7 side.

【0032】前記図3の構造において、燃料タンク内の
正圧によりガソリン蒸気が入口パイプ5を通じてその開
口部6から気泡通路21内に流入すると、その流入の際
に図4に示すように開口部6で泡立ち、その気泡により
液膜26が発生する。この気泡の発生時においては、開
口部6の上端6aが液体連通路23を形成する区画壁2
0の下端よりも上方位置に設定されているため、気泡は
区画壁20に当り、液体連通路23から液溜め室15内
へは侵入しない。そのため、液溜め室15内の液体が泡
立つことなくその液相燃料は安定する。
In the structure shown in FIG. 3, when the gasoline vapor flows into the bubble passage 21 from the opening 6 through the inlet pipe 5 due to the positive pressure in the fuel tank, the gas flows into the opening as shown in FIG. The liquid film 26 is generated by the bubbles at 6. When the bubble is generated, the upper end 6 a of the opening 6 is formed by the partition wall 2 forming the liquid communication passage 23.
Since the bubble is set at a position higher than the lower end of 0, the air bubble hits the partition wall 20 and does not enter the liquid storage chamber 15 from the liquid communication path 23. Therefore, the liquid phase fuel is stabilized without the liquid in the liquid storage chamber 15 foaming.

【0033】そして、開口部6で発生した気泡は区画壁
20の外周面20aに当って気泡通路21内の両側方及
び上方へ広がりながら成長する。このとき、その気泡の
液膜26は区画壁20の外周面20aと周壁4の内周面
4aに接触(衝突)し、これが消泡手段となって破裂す
る。この破裂によりその液相燃料は気泡通路21の底部
に落下する。
The air bubbles generated in the opening 6 hit the outer peripheral surface 20a of the partition wall 20 and grow while expanding on both sides and upward in the air bubble passage 21. At this time, the liquid film 26 of the bubbles comes into contact (collides) with the outer peripheral surface 20a of the partition wall 20 and the inner peripheral surface 4a of the peripheral wall 4, which bursts as defoaming means. Due to this rupture, the liquid fuel drops to the bottom of the bubble passage 21.

【0034】そして前記の破裂の繰り返しにより大きく
成長した気泡が、図4(a)に示すように気体連通路2
2に達すると、該気体連通路22から液溜め室15内に
流入する。この流入する気泡は前記図7において出口パ
イプ203に達する気泡の数よりも少なく、かつ気泡の
大きさもかなり大きくなり、その分だけ液膜による液体
量も少ない。
As shown in FIG. 4 (a), the air bubbles which have grown greatly due to the repetition of the above-mentioned rupture are formed in the gas communication passage 2 as shown in FIG.
When the pressure reaches 2, the gas flows into the liquid storage chamber 15 from the gas communication passage 22. The number of bubbles flowing in is smaller than the number of bubbles reaching the outlet pipe 203 in FIG. 7, and the size of the bubbles is considerably large, so that the amount of liquid due to the liquid film is small.

【0035】更に、前記のように気体連通路22から流
入した気泡の液膜は、変向板24によって直接出口パイ
プ7の開口部8へ流入することが阻止され、かつ変向板
24に当って破裂する。そして、消泡された気相燃料は
出口路25から矢印Yのように出口パイプ7の開口部8
に回り込み、出口パイプ7へ吸引される。
Further, as described above, the liquid film of the bubbles flowing from the gas communication passage 22 is prevented from flowing directly into the opening 8 of the outlet pipe 7 by the deflection plate 24 and hits the deflection plate 24. To burst. Then, the defoamed gaseous fuel flows from the outlet passage 25 to the opening 8 of the outlet pipe 7 as shown by the arrow Y.
And is sucked into the outlet pipe 7.

【0036】したがって、出口パイプ7からキャニスタ
へはほぼ気相燃料が吸入される。次に前記図6及び図7
に示す気液分離装置によるキャニスタへの液相燃料の流
入量と、前記本発明の第1及び第2実施例の気液分離装
置によるキャニスタへの液相燃料の流入量の測定結果を
説明する。
Therefore, almost gas-phase fuel is sucked from the outlet pipe 7 into the canister. Next, FIG. 6 and FIG.
The measurement results of the inflow amount of the liquid-phase fuel into the canister by the gas-liquid separation device shown in FIG. 1 and the inflow amount of the liquid-phase fuel into the canister by the gas-liquid separation devices of the first and second embodiments of the present invention will be described. .

【0037】測定に際しては、先ず図8に示すように、
前記図6及び図7に示す気液分離装置201の入口パイ
プ205を空気供給装置400へ連通路104で連通す
るとともに該連通路104に注射器401を備え、出口
パイプ203をメスシリンダ402へ連通した。そし
て、空気供給装置400から空気を正圧で所定量供給
し、注射器401で液体燃料を30ミリリットル注入し
た。その結果、メスシリンダ402には3ミリリットル
の液体燃料403が溜った。
At the time of measurement, first, as shown in FIG.
The inlet pipe 205 of the gas-liquid separator 201 shown in FIGS. 6 and 7 is connected to the air supply device 400 through the communication passage 104, and the communication passage 104 is provided with a syringe 401, and the outlet pipe 203 is connected to the measuring cylinder 402. . Then, a predetermined amount of air was supplied from the air supply device 400 at a positive pressure, and 30 ml of liquid fuel was injected by the syringe 401. As a result, 3 ml of liquid fuel 403 was accumulated in the measuring cylinder 402.

【0038】次で、前記の気泡分離装置201を、前記
本発明の図1及び図2に示す第1実施例の気液分離装置
1Aに取り替えて前記と同様に測定した結果、メスシリ
ンダ402には0.8ミリリットルの液体燃料が溜っ
た。
Next, the above-described bubble separation device 201 was replaced with the gas-liquid separation device 1A of the first embodiment shown in FIGS. 1 and 2 of the present invention, and the measurement was performed in the same manner as above. Has accumulated 0.8 ml of liquid fuel.

【0039】更に、本発明の図3及び図4に示す第2実
施例の気液分離装置1Bに取り替えて前記と同様に測定
した結果、メスシリンダ402には0.4ミリリットル
の液体燃料が溜った。
Further, as a result of performing measurement in the same manner as above by replacing the gas-liquid separator 1B of the second embodiment shown in FIGS. 3 and 4 of the present invention, 0.4 ml of liquid fuel is stored in the measuring cylinder 402. Was.

【0040】以上の測定結果から、本発明の実施例によ
れば、前記図6及び図7に示すものに比べて、キャニス
タへの液相燃料の流入量を低減できることが判明した。
なお、前記図1及び図2に示す第1実施例のものにおい
ては、泡切り部材18内の液相燃料が液溜め室15内へ
流出しにくく泡切り部材18内に保有されやすい。その
ため、次の高圧のガソリン蒸気が開口部6から流入した
場合、前記泡切り部材18内に保有されていた液相燃料
が上方へ押し出されて出口パイプ7へ吸入されるおそれ
がある。
From the above measurement results, it was found that according to the embodiment of the present invention, it is possible to reduce the amount of liquid-phase fuel flowing into the canister as compared with the embodiment shown in FIGS.
In the first embodiment shown in FIGS. 1 and 2, the liquid-phase fuel in the bubble removing member 18 does not easily flow into the liquid storage chamber 15 and is easily retained in the bubble removing member 18. Therefore, when the next high-pressure gasoline vapor flows in from the opening 6, there is a possibility that the liquid-phase fuel held in the bubble breaker 18 is pushed upward and is sucked into the outlet pipe 7.

【0041】これに対し、前記図3及び図4に示す第2
実施例のものによれば、気泡通路21内に前記のような
液相燃料を保有するものがなく、かつ気泡は周壁4の内
周面4aや区画壁20の外周面20aなどの大きな接触
(衝突)面積で消泡される。
On the other hand, in the second embodiment shown in FIGS.
According to the embodiment, there is no liquid fuel in the bubble passage 21 as described above, and the bubbles are in large contact with the inner peripheral surface 4a of the peripheral wall 4 and the outer peripheral surface 20a of the partition wall 20 (FIG. Defoamed in the (collision) area.

【0042】したがって、図3及び図4の第2実施例に
よれば図1及び図2に示す第1実施例の問題が解消さ
れ、前記測定結果の如く、キャニスタへの液相燃料への
吸入量が前記3者のうちで最も低くすることができる。
Therefore, according to the second embodiment shown in FIGS. 3 and 4, the problem of the first embodiment shown in FIGS. 1 and 2 is solved, and as shown in the measurement result, the liquid-phase fuel is introduced into the canister. The amount can be the lowest of the three.

【0043】なお、前記各実施例の周壁4は平面形状を
角形にしてもよい。
The peripheral wall 4 in each of the above embodiments may have a square planar shape.

【0044】[0044]

【発明の効果】以上のようであるから請求項1記載の発
明によれば、消泡手段を設けたことによって、気液分離
室に設けた出口パイプからキャニスタへ流入される液相
燃料の量を低減し、キャニスタにおける吸着剤の劣化を
防止できる。
As described above, according to the first aspect of the present invention, by providing the defoaming means, the amount of the liquid-phase fuel flowing into the canister from the outlet pipe provided in the gas-liquid separation chamber is provided. And the deterioration of the adsorbent in the canister can be prevented.

【0045】請求項2記載の発明によれば、泡切り部材
が消泡手段となり前記と同様の効果を発揮できる。請求
項3記載の発明によれば、前記請求項2記載の発明より
も一層キャニスタへ流入される液相燃料の量を低減し、
一層吸着剤の劣化を防止できる。
According to the second aspect of the present invention, the bubble removing member serves as a defoaming means, and can exert the same effect as described above. According to the third aspect of the invention, the amount of the liquid-phase fuel flowing into the canister is further reduced as compared with the second aspect of the invention,
The deterioration of the adsorbent can be further prevented.

【0046】そして、請求項4記載の発明によれば、変
向板を設けたことによって、キャニスタへ流入される液
相燃料の量をより一層低減し、より一層吸着剤の劣化を
防止できる。
According to the fourth aspect of the present invention, the provision of the deflection plate can further reduce the amount of liquid-phase fuel flowing into the canister, and can further prevent the deterioration of the adsorbent.

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

【図1】本発明の第1実施例を示すもので、(a)は縦
断面図、(b)は(a)におけるA−A線断面図。
FIGS. 1A and 1B show a first embodiment of the present invention, in which FIG. 1A is a longitudinal sectional view, and FIG. 1B is a sectional view taken along line AA in FIG.

【図2】図1に示す実施例における泡立ち状態を示すも
ので、(a)は縦断面図、(b)は(a)におけるA−
A線断面図。
FIGS. 2A and 2B show a foaming state in the embodiment shown in FIG. 1, wherein FIG. 2A is a longitudinal sectional view, and FIG.
FIG.

【図3】本発明の第2実施例を示すもので、(a)は縦
断面図、(b)は(a)におけるB−B線断面図。
3A and 3B show a second embodiment of the present invention, in which FIG. 3A is a longitudinal sectional view, and FIG. 3B is a sectional view taken along line BB in FIG. 3A.

【図4】図3に示す実施例における泡立ち状態を示すも
ので、(a)は縦断面図、(b)は(a)におけるB−
B線断面図。
4A and 4B show a bubbling state in the embodiment shown in FIG. 3, wherein FIG. 4A is a longitudinal sectional view, and FIG.
B sectional drawing.

【図5】本発明の気液分離装置を適用する蒸発燃料処理
装置を示す図。
FIG. 5 is a diagram showing an evaporated fuel processing apparatus to which the gas-liquid separation device of the present invention is applied.

【図6】本出願人が先に提案した気液分離装置を示すも
ので、(a)は縦断面図、(b)は(a)におけるC−
C線断面図。
FIGS. 6A and 6B show a gas-liquid separation device previously proposed by the present applicant, wherein FIG. 6A is a longitudinal sectional view, and FIG.
C line sectional drawing.

【図7】図6の気液分離装置の泡立ち状態を示すもの
で、(a)は縦断面図、(b)は(a)におけるC−C
線断面図。
FIGS. 7A and 7B show a bubbling state of the gas-liquid separator of FIG. 6, wherein FIG. 7A is a longitudinal sectional view, and FIG.
Line sectional view.

【図8】気液分離を測定する装置を示す略図。FIG. 8 is a schematic diagram showing an apparatus for measuring gas-liquid separation.

【符号の説明】[Explanation of symbols]

1A,1B 気液分離装置 2 ケース 3 気液分離室 4 周壁 5 入口パイプ 6 開口部 7 出口パイプ 8 開口部 10 区画壁 13 気体連通路 14,21 気泡通路 15 液溜め室 16,17 液体連通路 18 消泡手段である泡切り部材 19,26 液膜 20 消泡手段である区画壁 22 気体連通路 23 液体連通路 24 変向板 1A, 1B Gas-liquid separator 2 Case 3 Gas-liquid separation chamber 4 Peripheral wall 5 Inlet pipe 6 Opening 7 Outlet pipe 8 Opening 10 Partition wall 13 Gas communication path 14, 21 Bubble path 15 Liquid storage chamber 16, 17 Liquid communication path 18 Defoaming member as defoaming means 19, 26 Liquid film 20 Partition wall as defoaming means 22 Gas communication passage 23 Liquid communication passage 24 Deflection plate

Claims (4)

【特許請求の範囲】[Claims] 【請求項1】 気液分離室の下端部に入口パイプの開口
部を設け、気液分離室に出口パイプを開口し、気液分離
室内に、前記入口パイプの開口部で発生した気泡の液膜
を前記出口パイプの開口部に達する以前に破裂させる消
泡手段を設けたことを特徴とする気液分離装置。
An opening of an inlet pipe is provided at a lower end of a gas-liquid separation chamber, an outlet pipe is opened in the gas-liquid separation chamber, and a liquid of bubbles generated at the opening of the inlet pipe is provided in the gas-liquid separation chamber. A gas-liquid separation device, further comprising defoaming means for bursting the membrane before reaching the opening of the outlet pipe.
【請求項2】 気液分離室の下部に位置して入口パイプ
を開口し、気液分離室の略中央部に位置して出口パイプ
を立設してその上端を気液分離室に開口し、前記入口パ
イプの開口部と前記出口パイプの間に区画壁を設けて、
この区画壁により入口パイプの開口部側に気泡通路を、
出口パイプ側に液溜め室を区画して設け、前記気泡通路
内に泡切り部材を設置し、前記区画壁の上部には前記気
泡通路と液溜め室とを連通する気体連通路を設け、前記
気泡通路の底部と液溜め室の底部を一部において液体連
通路で連通したことを特徴とする気液分離装置。
2. An inlet pipe is opened at a lower part of the gas-liquid separation chamber, and an outlet pipe is erected at a substantially central part of the gas-liquid separation chamber, and an upper end thereof is opened at the gas-liquid separation chamber. Providing a partition wall between the opening of the inlet pipe and the outlet pipe,
This partition wall forms a bubble passage on the opening side of the inlet pipe,
A liquid storage chamber is defined on the outlet pipe side, a bubble cut-off member is installed in the bubble passage, and a gas communication passage communicating the bubble passage and the liquid storage chamber is provided at an upper portion of the partition wall, A gas-liquid separator characterized in that the bottom of the bubble passage and the bottom of the liquid storage chamber are partially connected by a liquid communication passage.
【請求項3】 気液分離室の下部に位置して入口パイプ
を開口し、気液分離室の略中央部に位置して出口パイプ
を立設してその上端を気液分離室に開口し、前記出口パ
イプの周囲に区画壁を設けて、該区画壁と気液分離室を
構成する周壁とで環状の気泡通路を形成するとともに区
画壁の内側に液溜め室を形成し、前記気泡通路の上部
を、前記入口パイプの開口部と反対方向において前記液
溜め室に連通し、気泡通路の少なくとも一部の下端部を
液溜め室に連通したことを特徴とする気泡分離装置。
3. An inlet pipe is opened at a lower part of the gas-liquid separation chamber, and an outlet pipe is erected at a substantially central part of the gas-liquid separation chamber, and an upper end thereof is opened at the gas-liquid separation chamber. Providing a partition wall around the outlet pipe, forming an annular bubble passage with the partition wall and a peripheral wall constituting a gas-liquid separation chamber, and forming a liquid reservoir inside the partition wall; Wherein the upper part of the air bubble communicates with the reservoir in a direction opposite to the opening of the inlet pipe, and at least a lower end of at least a part of the bubble passage communicates with the reservoir.
【請求項4】 前記気泡通路の上部における液溜め室へ
の開口部と前記出口パイプ間に、液溜め室への開口部か
ら流出する気相燃料を出口パイプに直接当たらないよう
にする変向板を設けたことを特徴とする請求項3記載の
気液分離装置。
4. A diversion between the opening to the reservoir at the upper part of the bubble passage and the outlet pipe so that the gas-phase fuel flowing out from the opening to the reservoir does not directly hit the outlet pipe. The gas-liquid separation device according to claim 3, further comprising a plate.
JP11171803A 1999-06-18 1999-06-18 Gas-liquid separating device Pending JP2001003818A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP11171803A JP2001003818A (en) 1999-06-18 1999-06-18 Gas-liquid separating device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP11171803A JP2001003818A (en) 1999-06-18 1999-06-18 Gas-liquid separating device

Publications (1)

Publication Number Publication Date
JP2001003818A true JP2001003818A (en) 2001-01-09

Family

ID=15930019

Family Applications (1)

Application Number Title Priority Date Filing Date
JP11171803A Pending JP2001003818A (en) 1999-06-18 1999-06-18 Gas-liquid separating device

Country Status (1)

Country Link
JP (1) JP2001003818A (en)

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JP2013181495A (en) * 2012-03-02 2013-09-12 Piolax Inc Gas-liquid separating device
KR20140134309A (en) * 2012-02-27 2014-11-21 디이이씨 아이엔씨 Oxygen-rich plasma generators for boosting internal combustion engines
CN109516518A (en) * 2018-12-11 2019-03-26 华北水利水电大学 A kind of gas-liquid separation device for biological hydrogen production process gassiness high viscosity liquid
US10494992B2 (en) 2018-01-29 2019-12-03 Hytech Power, Llc Temperature control for HHO injection gas
US10605162B2 (en) 2016-03-07 2020-03-31 HyTech Power, Inc. Method of generating and distributing a second fuel for an internal combustion engine

Cited By (13)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
KR20140134309A (en) * 2012-02-27 2014-11-21 디이이씨 아이엔씨 Oxygen-rich plasma generators for boosting internal combustion engines
US11879402B2 (en) 2012-02-27 2024-01-23 Hytech Power, Llc Methods to reduce combustion time and temperature in an engine
KR102048722B1 (en) * 2012-02-27 2019-11-26 디이이씨 아이엔씨 Oxygen-rich plasma generators for boosting internal combustion engines
JP2013181495A (en) * 2012-03-02 2013-09-12 Piolax Inc Gas-liquid separating device
US11280261B2 (en) 2016-03-07 2022-03-22 HyTech Power, Inc. Systems for HHO gas second fuel distribution and control
US11815011B2 (en) 2016-03-07 2023-11-14 Hytech Power, Llc Generation and regulation of HHO gas
US10605162B2 (en) 2016-03-07 2020-03-31 HyTech Power, Inc. Method of generating and distributing a second fuel for an internal combustion engine
US10619562B2 (en) 2018-01-29 2020-04-14 Hytech Power, Llc Explosion safe electrolysis unit
US10746094B2 (en) 2018-01-29 2020-08-18 Hytech Power, Llc Onboard HHO gas generation system for heavy duty trucks
US10494992B2 (en) 2018-01-29 2019-12-03 Hytech Power, Llc Temperature control for HHO injection gas
US11828219B2 (en) 2018-01-29 2023-11-28 Hytech Power, Llc Rollover safe electrolysis unit for vehicles
CN109516518B (en) * 2018-12-11 2023-09-29 华北水利水电大学 Gas-liquid separation device for gas-containing high-viscosity liquid in biological hydrogen production process
CN109516518A (en) * 2018-12-11 2019-03-26 华北水利水电大学 A kind of gas-liquid separation device for biological hydrogen production process gassiness high viscosity liquid

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