JPH0448937B2 - - Google Patents

Info

Publication number
JPH0448937B2
JPH0448937B2 JP58100918A JP10091883A JPH0448937B2 JP H0448937 B2 JPH0448937 B2 JP H0448937B2 JP 58100918 A JP58100918 A JP 58100918A JP 10091883 A JP10091883 A JP 10091883A JP H0448937 B2 JPH0448937 B2 JP H0448937B2
Authority
JP
Japan
Prior art keywords
adsorbent
adsorbent layer
fuel
layer
components
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 - Lifetime
Application number
JP58100918A
Other languages
Japanese (ja)
Other versions
JPS59226263A (en
Inventor
Shigenori Sakurai
Tooru Suzaki
Yoshihiro Shikame
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.)
Toyota Motor Corp
Original Assignee
Toyota Motor Corp
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 Toyota Motor Corp filed Critical Toyota Motor Corp
Priority to JP10091883A priority Critical patent/JPS59226263A/en
Publication of JPS59226263A publication Critical patent/JPS59226263A/en
Publication of JPH0448937B2 publication Critical patent/JPH0448937B2/ja
Granted legal-status Critical Current

Links

Classifications

    • FMECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
    • F02COMBUSTION ENGINES; HOT-GAS OR COMBUSTION-PRODUCT ENGINE PLANTS
    • F02MSUPPLYING COMBUSTION ENGINES IN GENERAL WITH COMBUSTIBLE MIXTURES OR CONSTITUENTS THEREOF
    • F02M25/00Engine-pertinent apparatus for adding non-fuel substances or small quantities of secondary fuel to combustion-air, main fuel or fuel-air mixture
    • F02M25/08Engine-pertinent apparatus for adding non-fuel substances or small quantities of secondary fuel to combustion-air, main fuel or fuel-air mixture adding fuel vapours drawn from engine fuel reservoir
    • F02M25/0854Details of the absorption canister

Landscapes

  • Engineering & Computer Science (AREA)
  • Chemical & Material Sciences (AREA)
  • Combustion & Propulsion (AREA)
  • Mechanical Engineering (AREA)
  • General Engineering & Computer Science (AREA)
  • Supplying Secondary Fuel Or The Like To Fuel, Air Or Fuel-Air Mixtures (AREA)
  • Separation Of Gases By Adsorption (AREA)

Description

【発明の詳細な説明】[Detailed description of the invention]

本発明は、自動車等の蒸発燃料吸着装置、特に
機関停止時に燃料タンクや気化器から発生する炭
化水素(HC)を効率よく捕集するキヤニスタの
構造に関する。 自動車の燃料タンクや気化器から蒸発するHC
は、低沸点のものから高沸点のものまで種々であ
るため、従来のキヤニスタのように単一種類の吸
着剤でこれらのHCを捕集することは困難であ
る。 一方石油資源保護のため、アルコールを混合し
た燃料が普及しはじめている。アルコールは蒸気
圧が高くしかも極性基を含むため、キヤニスタに
吸着剤として充填されている活性炭では、その特
性上アルコール分を捕集することが困難である。 複数種類の吸着剤を吸着すべき燃料に合せて用
いることは特開昭54−151725号に提案されてい
る。ここでは、気化器および燃料タンクから発生
するHCを吸着するために、気化器側では高沸点
分用吸着剤を用い、燃料タンク側では低沸点分用
吸着剤を用いるようになつている。しかし気化器
側では高沸点成分のみが蒸発し、燃料タンク側で
は低沸点成分のみが発生するわけではなく、これ
ら成分の割合が多いか少ないかだけのことなの
で、この提案では、燃料タンク側からHCが漏
れ、また燃料タンク側吸着剤が早期に劣化するお
それがある。また、上記提案の構成では、高沸点
分用吸着剤及び低沸点分用吸着剤が共に活性炭を
用いており、その吸着力を変化させただけの構成
であつた。このため、極性基を含むアルコール分
を確実に吸着することが困難であつた。 本発明は上記の点に鑑みてなされたものであ
り、2層構造の吸着剤の内第2の吸着剤層を第1
の吸着剤よりも極性物質を吸着しやすい材質とす
ることにより、発生源からの種々のHCあるいは
アルコール分を効果的に捕集することのできる吸
着装置を提供するものである。 このため本発明による蒸発燃料吸着装置では、
一方の端面に吸着燃料入口および離脱燃料出口を
もちまた他方の端面に大気開放口をもつ筒状容器
内に、少なくとも2つの層をなして少なくとも2
種類の吸着剤が収容され、大気開放口に近い方に
ある第2の吸着剤層を、吸着燃料入口に近い方に
ある第1の吸着剤層に対して極性物質を吸着しや
すい材料としたことを特徴とするものである。 また第1の吸着剤層と第2の吸着剤層とがフイ
ルタ板より分離されている構成としてもよい。 また、第2の吸着剤層の容積が第1の吸着剤層
の容積の20〜80%としてもよい。 更に、第2の吸着剤層を、第1の吸着剤層の活
性炭より極性物質を吸着しやすいシリカゲル、ゼ
オライトあるいはアルミナとしてもよい。 本発明の実施例を図について説明すると、蒸発
燃料吸着用キヤニスタ1は、一方の端面としての
蓋2と他方の端面としての底3とをもつ有底筒状
容器4を含み、底3には大気開放口5が形成され
ている。容器4の底3に近い範囲には環状段部6
が形成され、この段部6上に穴あき板7およびフ
イルタ板8が載せられている。このフイルタ板8
上には、蒸気燃料のうち主として低沸点成分を吸
着する粒状吸着剤の層9があり、フイルタ板10
を介してこの層9の上には、主として燃料の高沸
点成分を吸着する粒状吸着剤の層11がある。上
記各層9,11の材質を選定するに際し、低沸点
成分を吸着する粒状吸着剤の層9は、高沸点成分
を吸着する粒状吸着剤の層11よりも極性物質を
吸着しやすい材料に選定されている。また、下部
層9の容積は上部層11の容積の20〜80%とす
る。両方の層の吸着剤の種類および諸元を下表に
示す。
The present invention relates to an evaporative fuel adsorption device for an automobile or the like, and particularly to a structure of a canister that efficiently collects hydrocarbons (HC) generated from a fuel tank or a vaporizer when the engine is stopped. HC evaporated from automobile fuel tanks and vaporizers
Since the HCs vary from those with low boiling points to those with high boiling points, it is difficult to collect these HCs with a single type of adsorbent as in conventional canisters. Meanwhile, fuel mixed with alcohol is beginning to become popular in order to protect oil resources. Since alcohol has a high vapor pressure and also contains polar groups, it is difficult to collect the alcohol content with the activated carbon filled in the canister as an adsorbent due to its characteristics. The use of multiple types of adsorbents depending on the fuel to be adsorbed has been proposed in Japanese Patent Laid-Open No. 151725/1983. Here, in order to adsorb HC generated from the vaporizer and fuel tank, a high-boiling point adsorbent is used on the vaporizer side, and a low-boiling point adsorbent is used on the fuel tank side. However, this does not mean that only high-boiling point components are evaporated on the vaporizer side, and only low-boiling point components are generated on the fuel tank side, but only whether the proportion of these components is high or low, so in this proposal, from the fuel tank side. There is a risk of HC leaking and early deterioration of the adsorbent on the fuel tank side. Furthermore, in the proposed configuration, activated carbon is used for both the high-boiling point adsorbent and the low-boiling point adsorbent, and the structure is such that only the adsorption power thereof is changed. For this reason, it has been difficult to reliably adsorb alcohol containing polar groups. The present invention has been made in view of the above points, and the second adsorbent layer of the two-layer structure adsorbent is replaced with the first adsorbent layer.
By using a material that adsorbs polar substances more easily than other adsorbents, the present invention provides an adsorption device that can effectively collect various HC or alcohol components from sources. Therefore, in the evaporated fuel adsorption device according to the present invention,
At least two layers of at least two
The second adsorbent layer near the atmosphere opening is made of a material that easily adsorbs polar substances compared to the first adsorbent layer near the adsorbed fuel inlet. It is characterized by this. Alternatively, the first adsorbent layer and the second adsorbent layer may be separated by a filter plate. Further, the volume of the second adsorbent layer may be 20 to 80% of the volume of the first adsorbent layer. Furthermore, the second adsorbent layer may be made of silica gel, zeolite, or alumina, which can more easily adsorb polar substances than the activated carbon of the first adsorbent layer. To explain an embodiment of the present invention with reference to the drawings, a canister 1 for adsorbing evaporated fuel includes a bottomed cylindrical container 4 having a lid 2 as one end surface and a bottom 3 as the other end surface. An atmosphere opening port 5 is formed. An annular stepped portion 6 is provided in an area close to the bottom 3 of the container 4.
is formed, and a perforated plate 7 and a filter plate 8 are placed on this stepped portion 6. This filter plate 8
Above is a layer 9 of granular adsorbent that mainly adsorbs low-boiling components of the vapor fuel, and a filter plate 10
Above this layer 9 is a layer 11 of granular adsorbent which primarily adsorbs high boiling components of the fuel. When selecting the materials for each of the layers 9 and 11, the material for the granular adsorbent layer 9 that adsorbs low boiling point components is selected to be a material that can more easily adsorb polar substances than the granular adsorbent layer 11 that adsorbs high boiling point components. ing. Further, the volume of the lower layer 9 is 20 to 80% of the volume of the upper layer 11. The type and specifications of the adsorbent for both layers are shown in the table below.

【表】 上部層11の表面上には、フイルタ板12と穴
あき板13とが載せられ、容器4の蓋2に支えら
れるばね14によつて上部層11へ押付けられて
いる。蓋2には、燃料タンク15の燃料蒸発空間
に通ずる吸着管路16に接続される吸着燃料入口
17があり、この入口17に通ずる大径導管18
は上部層11の所定の深さまで入り込んでいる。
蓋2には,さらに気化器18のフロート室19の
燃料蒸発空間から出る吸着管路いわゆるアウタベ
ント20に接続される吸着燃料入口21と、気化
器18の吸気通路22へ開口する離脱管路23に
接続される離脱燃料出口24がある。 さて燃料タンク15および気化器フロート室1
9に生ずる蒸発燃料は、それぞれ吸着管路16お
よび20を経て、入口17および21からキヤニ
スタ1内の吸着剤に吸着される。この場合燃料の
HC成分は、そのほとんどがまず上部層11の吸
着剤粒子に吸着される。しかし、極性物質を吸着
する力の弱い上部層11では、燃料に混入されて
いるアルコールのような極性基を持つ成分や、蒸
気圧の高い低沸点成分及び不飽和HCはその大部
分が上部層11を通過してしまう。 上部層11う通過した極性基を持つ成分や、蒸
気圧の高い低沸点成分及び不飽和HCはフイルタ
板状体10を通り下部層9に流入する。前記した
ように、下部層9は上部層11よりも極性物質を
吸着しやすい材質(シリカゲル、ゼオライト、ア
ルミナ)からなるため、極性基を持つアルコール
等を果実に吸着することができる。また、下部層
9は上部層11よりも蒸気圧の高い低沸点成分及
び不飽和HCを吸着する能力も高いため、これら
の物質をも有効に吸着することができる。従つ
て、上部層11を通過した各種物質も下部層9に
より確実に吸着され、大気開放口5から大気へ漏
れ出すことはない。 こうして本発明によれば、キヤニスタの吸着剤
を複数層にして、沸点の異なる燃料成分あるいは
極性基をもつ燃料成分にそれぞれ適した吸着剤を
用いることにしたので、従来は吸着剤に吸着され
ることなく大気へ放出されていたHCも充分捕集
することができる。またアルコールを混入した燃
料でも、蒸発アルコール分をこのキヤニスタで充
分捕集し、大気への放出を防止することができ
る。 なお本発明は図示した実施例に限定されるもの
ではない。例えば3種類以上の異なる吸着剤を3
層以上に積層することができ、またキヤニスタも
図示したものと異なる構造をもつことができる。
[Table] A filter plate 12 and a perforated plate 13 are placed on the surface of the upper layer 11 and are pressed against the upper layer 11 by a spring 14 supported by the lid 2 of the container 4. The lid 2 has an adsorbent fuel inlet 17 connected to an adsorption line 16 leading to the fuel evaporation space of the fuel tank 15, and a large diameter conduit 18 leading to the inlet 17.
penetrates into the upper layer 11 to a predetermined depth.
The lid 2 further includes an adsorption fuel inlet 21 connected to an adsorption pipe, so-called outer vent 20, which exits from the fuel evaporation space of the float chamber 19 of the carburetor 18, and a separation pipe 23, which opens to the intake passage 22 of the carburetor 18. There is a breakaway fuel outlet 24 connected thereto. Now, fuel tank 15 and carburetor float chamber 1
The evaporated fuel generated in the canister 9 is adsorbed by the adsorbent in the canister 1 through the inlets 17 and 21 via the adsorption lines 16 and 20, respectively. In this case, the fuel
Most of the HC components are first adsorbed onto the adsorbent particles in the upper layer 11. However, in the upper layer 11, which has a weak ability to adsorb polar substances, components with polar groups such as alcohol mixed in the fuel, low boiling point components with high vapor pressure, and unsaturated HC are mostly absorbed in the upper layer 11. I passed 11. Components with polar groups, low boiling point components with high vapor pressure, and unsaturated HCs that have passed through the upper layer 11 flow into the lower layer 9 through the filter plate 10. As described above, since the lower layer 9 is made of a material (silica gel, zeolite, alumina) that adsorbs polar substances more easily than the upper layer 11, alcohols and the like having polar groups can be adsorbed to the fruit. Further, since the lower layer 9 has a higher ability to adsorb low-boiling components having a higher vapor pressure and unsaturated HC than the upper layer 11, it can also effectively adsorb these substances. Therefore, various substances that have passed through the upper layer 11 are also reliably adsorbed by the lower layer 9, and do not leak into the atmosphere from the atmosphere opening 5. In this way, according to the present invention, the adsorbent of the canister is made into multiple layers, and adsorbents suitable for fuel components with different boiling points or fuel components with polar groups are used. It is also possible to sufficiently capture HC that would otherwise have been released into the atmosphere. Furthermore, even if fuel is mixed with alcohol, the evaporated alcohol can be sufficiently collected by this canister and prevented from being released into the atmosphere. Note that the present invention is not limited to the illustrated embodiment. For example, if three or more different adsorbents are
More than one layer can be stacked, and the canister can also have a different structure than shown.

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

図は本発明による蒸発燃料吸着装置の構成図で
ある。 1……キヤニスタ、2……一方の端面(蓋)、
3……他方の端面(底)、4……筒状容器、5…
…大気開放口、9……第2の吸着剤層(下部層)、
11……第1の吸着剤層(上部層)、17,21
……吸着燃料入口、24……離脱燃料出口。
The figure is a configuration diagram of a vaporized fuel adsorption device according to the present invention. 1... Canister, 2... One end surface (lid),
3...other end surface (bottom), 4... cylindrical container, 5...
...Atmospheric opening, 9...Second adsorbent layer (lower layer),
11...first adsorbent layer (upper layer), 17, 21
... Adsorption fuel inlet, 24 ... Detachment fuel outlet.

Claims (1)

【特許請求の範囲】 1 一方の端面に吸着燃料入口および離脱燃料出
口をもちまた他方の端面に大気開放口をもつ筒状
容器内に、少なくとも2つの層をなして少なくと
も2種類の吸着剤が収容され、大気開放口に近い
方にある第2の吸着剤層を、吸着燃料入口に近い
方にある第1の吸着剤層に対して極性物質を吸着
しやすい材料としたことを特徴とする、蒸発燃料
吸着装置。 2 第1の吸着剤層と第2の吸着剤層とがフイル
タ板により分離されていることを特徴とする、特
許請求の範囲第1項記載の装置。 3 第2の吸着剤層の容積が第1の吸着剤層の容
積の20〜80%であることを特徴とする、特許請求
の範囲第1項または2項のいずれか記載の装置。 4 第2の吸着剤層が、第1の吸着剤層の活性炭
より極性物質を吸着しやすいシリカゲル、ゼオラ
イトあるいはアルミナからなることを特徴とする
特許請求の範囲第1項乃至第3項のいずれかに記
載の装置。
[Claims] 1. At least two types of adsorbents are contained in at least two layers in a cylindrical container having an adsorbed fuel inlet and a separated fuel outlet on one end face and an atmosphere opening on the other end face. The second adsorbent layer that is housed in the adsorbent and is located closer to the atmosphere opening is made of a material that easily adsorbs polar substances to the first adsorbent layer that is located closer to the adsorbed fuel inlet. , evaporative fuel adsorption device. 2. The device according to claim 1, characterized in that the first adsorbent layer and the second adsorbent layer are separated by a filter plate. 3. The device according to claim 1 or 2, characterized in that the volume of the second adsorbent layer is 20 to 80% of the volume of the first adsorbent layer. 4. Any one of claims 1 to 3, wherein the second adsorbent layer is made of silica gel, zeolite, or alumina, which adsorbs polar substances more easily than the activated carbon of the first adsorbent layer. The device described in.
JP10091883A 1983-06-08 1983-06-08 Vaporized fuel adsorbing device Granted JPS59226263A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP10091883A JPS59226263A (en) 1983-06-08 1983-06-08 Vaporized fuel adsorbing device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP10091883A JPS59226263A (en) 1983-06-08 1983-06-08 Vaporized fuel adsorbing device

Publications (2)

Publication Number Publication Date
JPS59226263A JPS59226263A (en) 1984-12-19
JPH0448937B2 true JPH0448937B2 (en) 1992-08-10

Family

ID=14286716

Family Applications (1)

Application Number Title Priority Date Filing Date
JP10091883A Granted JPS59226263A (en) 1983-06-08 1983-06-08 Vaporized fuel adsorbing device

Country Status (1)

Country Link
JP (1) JPS59226263A (en)

Families Citing this family (8)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0765548B2 (en) * 1986-11-05 1995-07-19 トヨタ自動車株式会社 Fuel vapor collector
JPH0765549B2 (en) * 1987-01-19 1995-07-19 トヨタ自動車株式会社 Fuel vapor collector
US5271914A (en) * 1990-04-04 1993-12-21 Tosoh Corporation Process for adsorbing the vapor of alcoholic fuels
JP3465393B2 (en) * 1995-01-06 2003-11-10 トヨタ自動車株式会社 Evaporative fuel processor for internal combustion engines
US10960342B2 (en) 2012-10-10 2021-03-30 Ingevity South Carolina, Llc Evaporative fuel vapor emission control systems
PL2906811T3 (en) 2012-10-10 2018-07-31 Ingevity South Carolina, Llc CONTROL SYSTEMS OF FUEL VAPOR EMISSIONS
JP2023069542A (en) * 2021-11-05 2023-05-18 大阪ガスケミカル株式会社 canister
JP2023069543A (en) * 2021-11-05 2023-05-18 大阪ガスケミカル株式会社 canister

Family Cites Families (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5768163U (en) * 1980-10-14 1982-04-23

Also Published As

Publication number Publication date
JPS59226263A (en) 1984-12-19

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