Búsqueda Imágenes Maps Play YouTube Noticias Gmail Drive Más »
Iniciar sesión
Usuarios de lectores de pantalla: deben hacer clic en este enlace para utilizar el modo de accesibilidad. Este modo tiene las mismas funciones esenciales pero funciona mejor con el lector.


  1. Búsqueda avanzada de patentes
Número de publicaciónUS3393669 A
Tipo de publicaciónConcesión
Fecha de publicación23 Jul 1968
Fecha de presentación19 May 1966
Fecha de prioridad19 May 1966
Número de publicaciónUS 3393669 A, US 3393669A, US-A-3393669, US3393669 A, US3393669A
InventoresVardi Joseph, David T Wade
Cesionario originalExxon Research Engineering Co
Exportar citaBiBTeX, EndNote, RefMan
Enlaces externos: USPTO, Cesión de USPTO, Espacenet
Apparatus and process for adsorbing and desorbing internal combustion engine fuel vapors
US 3393669 A
Resumen  disponible en
Previous page
Next page
Reclamaciones  disponible en
Descripción  (El texto procesado por OCR puede contener errores)

y 23, 1968 J. VARDI ETAL 3,


N.J., assignors to Esso Research and Engineering Company, a corporation of Delaware Filed May 19, 1966, Ser. No. 551,411

9 Claims. (CL. 123-136) ABSTRACT OF THE DISCLOSURE Apparatus and process for opening an internal combustion engine which comprises adsorbing fuel constituents on an adsorbent bed when the engine is not operating; thereafter during engine operation desorbing said constituents from saidbed first utilizing a hot backwash purge and thereafter utilizing a cold backwash purge.

The present invention is broadly concerned with an adsorb vaporized fuel constituents and then desorbs these fuel constituents and combusts the same in the engine. The invention is particularly directed toward a unique desorption technique wherein adsorbed constituents are eificiently desorbed by the use of a hot-cold purge.

It is well known that air pollution presents health, nuisance, and economic problems, and that the fumes, vapors, and gases evolved from internal combustion motor vehicles contribute significantly to air contamination. It is also known that generally these fumes and vapors are emitted into the atmosphere from the motor vehicle as exhaust gases discharged through the tailpipe, or are due to fuel constituents which are emitted through the vent in the fuel storage tank and through vents from the carburetor bowl. For example, it has been estimated that from about 10 to 20% by volume as, for example, about 15%, by volume of the total vapors and fumes emitted to the atmosphere from an internal combustion motor vehicle are evaporated from the gasoline tank and the carburetor bowl.

The present invention is particularly concerned with the elimination of fuel losses from the vehicle fuel tank and carburetor bowl and with their ultimate use in the combustion chamber. In accordance with the present invention fuel vapors, such as hydrocarbon fuel vapors, alcohol vapors and the like, which are emitted either from the fuel reservoir or the carburetor bowl, are adsorbed on an adsorbent and thereafter desorbed by a hot-cold purge and combusted in the engine. The adsorbent may be any suitable material which will adsorb fuel constituents such as silica gel, activated carbon, and the like.

The losses from the fuel reservoir tank are caused by factors which include the rising temperature of the fuel as the vehicle is operated and rising atmospheric temperatures which cause the reservoir or fuel tank to breathe through the vent, or vents, in the fuel tank thereby emitting fuel constituents into the atmosphere. In many instances the temperature of the fuel reservoir may be from about 20 to 40 F. higher than the atomspheric or ambient temperature.

Furthermore, after the engine has been operated for a period of time and then turned off, the temperature of the fuel in the carburetor bowl rises as heatflows to the carburetor from the hot engine. The fuel is said to undergo a hot soak. Data have shown that the temperature of the fuel in the carburetor bowl can rise to as high as about 200 F. after the hot engine has been turned 01f. It has been'estimated that the loss from a gasoline tank may range from about 2 to 150 grams per day and that the hot soak loss from the carburetor bowl may range from about 2 to 50 grams per hot soak.

Thus, in accordance with the present invention as hereinbefore mentioned, these fuel vapors are adsorbed on an adsorbent and then desorbed by a hot-cold technique and combusted in the internal combustion engine. The process and apparatus of the present invention may be more fully understood by reference to the drawing illustrating an embodiment of the same.

Referring specifically to the drawing, utilizing a single adsorbent bed, vaporized fuel constituents from fuel tank 10 are passed through line 1 and adsorbed in zone 20 containing a suitable adsorbent 21. Liquid fuel is passed to the carburetor bowl 30 by means of line 2, pump 3, and line 4. Vaporized constituents from the carburetor bowl pass into the lower or one end of zone 20 by means of line 31. Air is passed through filter zone 40 and into carburetion zone 50 whereis is mixed with liquid fuel introduced from thecarburetor bowl. A flapper valve 51 controls the amount of air-fuel mixture introduced into intake manifold 60.

When theengine is operating in a conventional operation, a portion of the incoming air is passed through line 22 and enters the other end of zone 20 and backwashes through the adsorbent, thereby desorbing fuel constituents previously adsorbed. The amount of air backwashing is sufiicient to desorb the adsorbed constituents. The backwashing air containing desorbed fuel constituents passes through line 23 and is introduced into the intake manifold 60. The rate of backwashing through line 23 into manifold 60 is controlled by orifice or equivalent means 24, and auxiliary equipment (not shown). In essence, as the engine moves from idling to full throttle the rate of backwashing increases.

In accordance with the specific adaptation of the present invention, when the engine is operating adsorbed constituents are removed from the adsorbent by backwashing air therethrough utilizing initially a hot purge and then a cold purge. This may be secured by a suitable valve timing device 70, or equivalent means which initially permits hot air to be introduced into the other end of zone 20 by. means of line 71. The air for the hot purge may be heated by any suitable means such as heating coils and the like.

However, it is preferred to secure the temperature of the hot purge by introducing atmospheric air into a manifold device wherein the air is heated by the exhaust gases which are introduced into device 80 by means of line 81 and withdrawn by means of line 82. These gases are heated to a temperature above about 200 F., preferably to a temperature in the range from about 400 to 500 F. as, for example, 450 F.

It is to be understood that under certain conditions exhaust gases may be used directly as a backwashing medium. Under these conditions no air is introduced by means of line 72 but at least a portion of hot exhaust gases removed by means of line 82 is introduced into line 71 by means of line 83. Under certain conditions it may be desirable to mix air introduced by means of line 72 and exhaust gases introduced by means of line 83. The temperature of these gases may range from about 700 F. to about 800 F. It is also to be understood that in the manner of operating as described, a temperature gradient will exist throughout the bed. The temperature of the bed at the point the backwashing gases are introduced will approximate the temperature of the incoming gases, while the temperature of the one end of the bed will approximate ambient temperatures. It is also to be understood that it .4 adsorbent bed under conditions to desorb fuel constituents, and to produce a first fuel-enriched mixture, introducing said first fuel-enriched mixture into the manifold of said engine, thereafter under engine operating suction backwashing cold gas into the other end of said adsorbent bed is within the concept of the present invention during the 5 and passing the same through said adsorbent bed under backwashing cycle to introduce cold air continuously conditions to cool said bed and to produce a second fuelthrough line 22 and in the initial cycle or during the hot enriched mixture, introducing said second fuel-enriched purge to heat up the gases introduced by means of line mixture into said manifold of said engine.

22 to the desired temperature by mixing therewith heated 1O 2. Process as defined by claim 1 'Wherein said hot gas air introduced by means of line 72 or exhaust gases incomprises heated atmospheric air.

troduced into the system by means of line 83. Generally, 3. Process as defined by claim 1 wherein said hot gas if the temperature of the bed at the point where the backcomprises engine exhaust gas.

washing gases are introduced is in the range from about 4. Process as defined by claim 1 wherein said fuel is 400 to about 500 F. as, for example, about 450 F., a gasoline and wherein said adsorbent is activated carbon. a satisfactory operation will be achieved. As pointed out 5. Process as defined by claim 1 wherein the temperaheretofore, the gradient temperatures throughout the bed ture of said hot gas is in the range from above ambient will decrease in a manner that ambient temperature will to 800 F. and wherein the temperature of said cold .gas exist at the one end of the bed. is about ambient.

Generally, the time of hot purge is in the range from 6. Process as defined by claim 1 wherein the amount about 2 to 12 minutes as, for example, 3 to 5 minutes. The and temperature of hot gas introduced into said adsonbent desorption is then continued using a cold purge wherein bed is sufficient to raise the other end of said bed to a line 71 is shut off and line 22 opened so as to introduce temperature within the range of about 400 to about atmospheric air into the other end of zone 20. As described 500 F. heretofore, this technique may be modified as desired, by 25 7. Apparatus for preventing loss of fuel constituents into the use of exhaust gases, or by the continuous use of cold the atmosphere from an internal combustion motor which air, and other modifications, etc. In order to further ilcomprises in combination: (1) a fuel reservoir; (2) an adlustrate the invention a number of operations were consorption zone having a one end and another end and conducted utilizing a cold purge only and also utilizing a hot taining an adsorbent therein, (3) an engine manifold compurge followed by a cold purge. The adsorbent was charmunicating with the cylinders of said motor; (4) a first coal. The results are shown in the following table. conduit characterized by being in open communication Time Hydroon Cold Temp. of carbon Final Time on Hot Purge, Min. Purge, Purge, Removal, Percent Temp. Min. F. gm./100 gm. in ed,

Charcoal F.

4.25 4.25 471 19.0 96 104405 3 5.5 433 17.6 89 76-128 Cold Purge Only 8. 5 -80 8. 5 43 -80 Thus in the conventional operation the full adsorption with said one end of said adsorption zone and the upper capacity of the adsorbent is not utilized due to unremoved area of said fuel reservoir; (5) a second conduit characequilibrium level of hydrocarbon from the charcoal. terized by being in communication with said intake mani- However, when following the technique of the present infold and said one end of said adsorption zone; (6) a third vention utilizing a hot purge, above ambient, in the range 45 conduit characterized by being in communication with from about 150 to 800 F. effective removal of the hysaid other end of said adsorption zone and with the atdrocarbons is secured in about 3 to 5 minutes. The purge mosphere; (7) a fourth conduit characterized by being is then changed to cold (ambient) conditions to bring in communication with said other end of said adsorption the temperature of the charcoal back to normal so that zone and a source of hot gases; (8) and a timing device effective adsorption can take place as soon as a hot soak programed in a manner that during engine operation hot period starts. The adsorbent bed size can be reduced by a gases will be, during an initial period, introduced into the factor of 2-3 using this hot purge process. The above table other end of said adsorption zone and subsequent to said demonstrates the effectiveness of the process. initial period atmospheric air will be introduced into the In its broadest adaptation, the present invention covers other end of said adsorption zone, all gases during said the method of operating an engine wherein vaporous conengine operation passing through said adsorption zone, stituents of a fuel are adsorbed on an adsorbent and therewithdrawn from said one end and introduced into said after desorbed by a particular technique from said adsorbmanifold. ent and introduced into an internal combustion engine. The 8. Apparatus as defined by claim 7 wherein said respreferred adaptations are to adsorb vaporous constituents ervoir is the carburetor bowl associated with said engine. from liquid fuel reservoirs which are ahead of the car- 9. Apparatus as defined by claim 7 wherein the said buretor. These vaporous constituents are then desorbed reservoir is a fuel tank associated with said engine. by backflowing or backwashing hot and then cold gases therethrough by the action of the engine and are in- References Clted troduced as an enriched fuel-air mixture into the engine. UNITED STATES PATENTS What clalmed 3,001,519 9/1961 Dietrich et al. 123-136 1. Process of operating an internal combustion en- 3 093 124 6/1963 Wentworth gine which comprises introducing fuel constituents vapor- 3:191:587 6/1965 n 123 136 ized from a liquid pool into one end of an adsorbent bed 3 2 7 4 12/1965 Wentworth 123 136 when said engine is not running, thereafter under engine 3 23 214 2 19 J h 23 X operating suction backwashing hot gas into the other end of said adsorbent bed and passing the same through said AL LAWRENCE SMITH, Primary Examiner.

Citas de patentes
Patente citada Fecha de presentación Fecha de publicación Solicitante Título
US3001519 *8 Ago 196026 Sep 1961Gen Motors CorpFuel vapor loss elimination system
US3093124 *23 Dic 196011 Jun 1963Gen Motors CorpEngine fuel vapor recovery system and method
US3191587 *18 Ago 196029 Jun 1965 Device for controlling the hydrocar- bon evaporation losses from automo- tive vehicles
US3221724 *27 Ene 19647 Dic 1965Gen Motors CorpVapor recovery system
US3236214 *20 Ago 196222 Feb 1966A O J CorpFuel economizer and exhaust gas purifier for internal combustion engines
Citada por
Patente citante Fecha de presentación Fecha de publicación Solicitante Título
US3518977 *15 Abr 19687 Jul 1970F & E Mfg CoFuel emission control system
US3713273 *3 May 197130 Ene 1973R CoffeeMethod and apparatus for storing gases and fueling internal combustion engines
US3902874 *13 Dic 19732 Sep 1975Shell Oil CoVapor recovery and disposal system
US4191154 *3 Feb 19784 Mar 1980Toyota Jidosha Kogyo Kabushiki KaishaEvaporated fuel vapor control device for use in an internal combustion engine
US4280466 *26 Mar 197928 Jul 1981General Motors CorporationEvaporative emission control device
US4683862 *15 Oct 19864 Ago 1987General Motors CorporationFuel vapor storage canister
US4714485 *15 Oct 198622 Dic 1987General Motors CorporationFuel vapor storage canister
US5288307 *28 Ago 199222 Feb 1994The Dow Chemical CompanyMethod to reduce fuel vapor emissions
US5840104 *18 Dic 199624 Nov 1998Nissan Motor Co., Ltd.Canister structure for automobile
US6432179 *30 Mar 200113 Ago 2002Honeywell International Inc.Vapor-adsorbent filter for reducing evaporative fuel emissions, and method of using same
US655023817 Ago 200122 Abr 2003Daimlerchrysler AgApparatus for reducing the emission of vaporized hydrocarbons in a fuel supply system
US716357423 Mar 200416 Ene 2007Honeywell International, Inc.Evaporative emissions filter
US718280219 Mar 200327 Feb 2007Honeywell International, Inc.Evaporative emissions filter
US73445861 Nov 200418 Mar 2008Honeywell International, Inc.Evaporative emissions filter
US737796626 Ago 200427 May 2008Honeywell International, Inc.Adsorptive assembly and method of making the same
US7655166 *29 Ene 20082 Feb 2010Honeywell International Inc.Evaporative emissions filter
US815692415 Oct 200817 Abr 2012Kohler Co.Systems and methods for regulating purge flow rate in an internal combustion engine
US8216349 *24 Dic 200910 Jul 2012Fram Group Ip LlcEvaporative emissions filter
US86779783 Mar 201125 Mar 2014Kohler Co.System and method for carburetor venting
US20040182240 *19 Mar 200323 Sep 2004Bause Daniel E.Evaporative emissions filter
US20050000362 *23 Mar 20046 Ene 2005Bause Daniel E.Evaporative emissions filter
US20050145224 *1 Nov 20047 Jul 2005Zulauf Gary B.Evaporative emissions filter
US20060042468 *26 Ago 20042 Mar 2006Smith Robert LAdsorptive assembly and method of making the same
US20080184891 *29 Ene 20087 Ago 2008Zulauf Gary BEvaporative emissions filter
US20090100828 *15 Oct 200823 Abr 2009Hudak Eric BSystems and Methods for Regulating Purge Flow Rate in an Internal Combustion Engine
US20100101542 *24 Dic 200929 Abr 2010Zulauf Gary BEvaporative emissions filter
US20110214645 *3 Mar 20118 Sep 2011Kohler Co.System and method for carburetor venting
US20150176534 *24 Jul 201425 Jun 2015Rem Technology Inc.System and method for controlling a flow of vent gases to a natural gas engine
Clasificación de EE.UU.123/520, 96/144, 96/136, 261/72.1, 95/146, 55/DIG.280
Clasificación internacionalF02M25/08
Clasificación cooperativaY10S55/28, F02M2025/0881, F02M25/089
Clasificación europeaF02M25/08L