U.S. patent number 3,815,327 [Application Number 05/360,143] was granted by the patent office on 1974-06-11 for method and apparatus for preventing loss of hydrocarbons to atmosphere.
Invention is credited to Clare Kenneth Viland.
United States Patent |
3,815,327 |
Viland |
June 11, 1974 |
METHOD AND APPARATUS FOR PREVENTING LOSS OF HYDROCARBONS TO
ATMOSPHERE
Abstract
A self-contained vapor recovery system for gasoline service
stations and for similar applications. Displaced hydrocarbon gases
are collected at the point of entry when a vehicle's fuel tank is
being filled, or when the service station's main storage tanks are
receiving a fresh loading of gasoline. These vapors are collected
under controlled pressure conditions, dehydrated, and passed
through a refrigerated condensation or absorption zone, and the
recovered liquid is returned to the service station's storage
tankage, preferably below the liquid level there. The essentially
hydrocarbon-free gas, now mainly air, is discharged into the
atmosphere. The invention not only helps conserve a valuable
natural resource, the petroleum from which the gasoline is made,
but also alleviates air pollution or smog formation, since unburned
hydrocarbons in the earth's atmosphere react under the influence of
sunlight with nitrogen oxides and carbon monoxide from any source
of combustion, to form a typical smog blanket. Being compact, the
apparatus occupies little valuable space in a service station; and
it requires less power than conventional apparatus.
Inventors: |
Viland; Clare Kenneth (Bodega
Bay, CA) |
Family
ID: |
26965829 |
Appl.
No.: |
05/360,143 |
Filed: |
May 14, 1973 |
Related U.S. Patent Documents
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Application
Number |
Filing Date |
Patent Number |
Issue Date |
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289757 |
Sep 15, 1972 |
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Current U.S.
Class: |
95/220; 55/310;
55/338; 141/52; 220/749; 95/271; 55/434.4; 55/309.1; 55/337;
55/459.1; 141/290 |
Current CPC
Class: |
B01D
5/0084 (20130101); B67D 7/049 (20130101); B01D
5/0081 (20130101); B01D 5/0033 (20130101); B67D
7/0476 (20130101); B67D 2007/0494 (20130101) |
Current International
Class: |
B01D
5/00 (20060101); B67D 5/01 (20060101); B67D
5/04 (20060101); B01d 050/00 () |
Field of
Search: |
;55/385,387,267-269,80,316,310,337,459,88,89,338
;141/41-43,52,59,287,307,290 ;220/85VR,85VS |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Miles; Tim R.
Assistant Examiner: Cuchlinski, Jr.; William
Attorney, Agent or Firm: Owen, Wickersham & Erickson
Parent Case Text
CROSS REFERENCE TO RELATED APPLICATION
This application is a continuation-in-part of application Ser. No.
289,757, filed Sept. 15, 1972, now abandoned.
Claims
I claim:
1. A method for preventing pollution of the atmosphere by
hydrocarbon vapors, comprising:
closing off the space between a tank to be filled and a filling
hose from access to the atmosphere during the filling of the
tank,
collecting the gasoline vapors and air displaced from said tank
during filling of said tank by liquid gasoline and also collecting
additional gasoline vapors evaporated during said filling of the
tank,
de-moisturizing the collected vapors, and air,
condensing the de-moisturized vapors to liquid form with some of
the condensed gasoline vapors still dispersed in the air, and
introducing the air and condensed vapors tangentially into a
cyclone-separation zone maintained at a temperature between about
0.degree. F. and about -40.degree. F. at an entrance velocity such
that the centrifugal force imparted is substantially greater than
the force of gravity,
completing the condensation to at least 90 percent of the
hydrocarbons boiling at and above about 31.degree. F. and
separating the hydrocarbon liquid from the air by said centrifugal
force.
2. The method of claim 1 having the additional steps of injecting
about one to three mols of tank gasoline per mol of total
hydrocarbons present in the vapor, into the vapors entering the
condensing system, to absorb part of the hydrocarbons.
3. The method of claim 1 having the additional steps of
de-misting the air and any condensed hydrocarbon contained therein
after said separating by agglomerating the mist into droplets of
liquid, and
returning said droplets to the separation portion of the cyclone
zone by gravity.
4. The method of claim 3, including injecting about one to three
mols of tank gasoline per mol of total hydrocarbons present in the
vapor, into the vapors entering the condensing system.
5. The method of claim 3 having the additional steps of
conducting the condensed hydrocarbon liquid from the bottom of the
cyclone-separator vessel to storage, and
venting the air and other gas to the atmosphere.
6. The method of claim 1 having the additional steps of
conducting the condensed hydrocarbon liquid at the bottom of the
cyclone separator to storage, and
venting the air and other gas from the top of the cyclone separator
to the atmosphere.
7. Apparatus for preventing pollution of the atmosphere by
hydrocarbon vapors, comprising:
means for closing off the space between a tank to be filled and a
filling hose from access to the atmosphere during the filling of
the tank,
means for collecting the gasoline vapors and air displaced from
said tank during filling thereof by liquid gasline and also for
collecting any additional gasoline vapors evaporated during said
filling of the tank,
means for de-moisturizing the collected vapors, and air,
means for condensing the collected vapors to liquid form, with some
of the condensed gasoline vapors still being dispersed in the air,
and
a cyclone separator having a tangential inlet introducing the air
and condensed vapors at an entrance velocity such that the
centrifugal force imparted is substantially greater than the force
of gravity,
means for maintaining the condensed vapors in said cyclone
separator in their condensed state so that condensation is
completed to 90 percent or more of all hydrocarbons boiling at and
above about 31.degree. F., and so that the hydrocarbon liquid is
separated from the air by said centrifugal force.
8. The apparatus of claim 7 having means for injecting tank
gasoline into the vapors before said vapors enter said means for
condensing.
9. The apparatus of claim 7 having
means for de-misting the air and any condensed hydrocarbon
contained therein after separation by agglomerating the mist into
droplets of liquid, and
means for returning said droplets to said cyclone separator by
gravity.
10. The apparatus of claim 9 having
means for conducting condensed hydrocarbon liquid at the bottom of
the cyclone separator to storage, and
means for venting the air and other gas to the atmosphere.
11. The apparatus of claim 7 having
means for conducting the condensed hydrocarbon liquid at the bottom
of the cyclone separator to storage and
means for venting the air and other gas from the top of the
cyclone-separator vessel to the atmosphere.
12. Apparatus for preventing loss of hydrocarbons to air when
filling a depleted automobile gasoline tank and when filling the
fuel-dispensing tank of the service station, comprising
a gasoline storage tank,
vapor-collecting means for collecting the hydrocarbon vapors and
air displaced from the automobile gasoline tank during filling
under slight pressure,
drying means connected to said vapor-collecting means for
demoisturizing said collected vapors and air,
condensing means connected to said drying means for condensing not
less than 90 percent of the hydrocarbons boiling at and above about
31.degree. F. to liquid form, said condensing means comprising a
housing containing refrigerated coolant, and a heat exchanger and a
cyclone-separator vessel both immersed in said refrigerated
coolant, said cyclone-separator vessel imparting a centrifugal
separating force greater than that of gravity and having a
separation zone,
a liquid collector at the bottom of the cyclone-separator zone,
conduit means connected to said liquid collector for conducting
said liquid hydrocarbon condensate to said storage tank, and
means connected to said vapor zone for venting the air and any
other gas present from the top of said cyclone-separator vessel to
the atmosphere.
13. The apparatus of claim 12 having means for injecting tank
gasoline into the vapors before said vapors enter said condensing
means.
14. The apparatus of claim 12 having
means for collecting vapors and air displaced in filling said
storage tank connected to said vapor-collecting means,
bypass venting means connected to said means for collecting vapors
and air to said vapor-collecting means, and
check valve means in said bypass venting means holding a pressure
in said collected vapors of about 0.5-2.5 psig before venting.
15. The apparatus of claim 12 wherein
said vessel has a cylindrical vapor zone within and above said
separation zone of said cyclone separator wherein the linear
velocity is relatively low, and
a de-mister pad placed horizontally in said vapor zone wherein air,
gas and any condensed hydrocarbon vapor present as fine mist are
caused to pass, thereby agglomerating said mist into liquid
droplets,
said liquid droplets returning by gravity into the separation zone
of the cyclone-separator vessel.
16. The apparatus of claim 12 wherein
said vapor-collecting means comprises a housing providing an
annular space and secured to a gasoline filling hose adjacent to
its nozzle and having means for attachment to the filling spout of
said automobile gasoline tank in the same manner as the cap
normally closing said spout.
17. The apparatus of claim 16 having a vapor line from said housing
and check-valve means in said vapor line for closing off said
vapor-collecting means when no vehicles are being refueled.
Description
BACKGROUND OF THE INVENTION
This invention relates to the field of prevention of air pollution.
Specifically, it relates to a method of and apparatus for
preventing loss of gasoline fractions when filling automobile fuel
tanks and when refilling service station storage tanks. It is an
improvement on the invention disclosed in my co-pending application
Ser. No. 109,226 filed Jan. 25, 1971 now U.S. Pat. No.
3,763,901.
When a motorist stops to refuel, he may take, typically, about 71/2
U.S. gallons, which means that 71/2 gallons of gasoline vapor and
air are displaced during the refueling. Additionally, there is at
lesat an equal evaporation loss due to agitation of the fuel, which
may be warmer than the ambient temperature. This means that 15
gallons of vapor or two cubic feet of vaporized gasoline and air
are vented to the atmosphere.
Recent California laws limit vapor pressure of gasoline seasonally,
so that "summer grade," by area and date, may not exceed 9 pounds
Reid vapor pressure at 100.degree. F. This lower vapor pressure and
the evaporation control systems on late-model automobiles have
reduced losses when filling automobile tanks, and the lower vapor
pressure has helped to reduce losses when filling tanks for storage
in stations. The late-model cars commonly use a charcoal canister
to absorb and store gasoline vapors from the fuel-tank and
carburetor until their use as fuel is permissible. Thus, loss in
filling automobile tanks has been substantially reduced to about
0.5 gallons or less per 1,000 gallons transferred, but this is
additive to other losses in the filling station -- the other main
loss occurring when filling main storage tanks, where loss is in
the range of 1-3 gallons per 1,000 gallons transferred. Thus,
typical overall loss is at least 2 or more gallons per 1,000,
amounting to 5,500 grams or more per 1,000 gallons transferred.
Under California law, permissible total auto emissions of
hydrocarbons are 3.2 grams per mile in 1972, dropping to 0.4 grams
in 1975-76 for all autos sold in the U.S.A. under the 1970 Clean
Air Act, both figures based on current test procedures.
It is apparent that controls will have to be placed on the handling
of gasoline at service stations and at bulk distribution centers to
meet the stringent standards set by the 1970 Clean Air Act.
It is well known that "smog," now a major problem in most
metropolitan areas, is presently attributable about 60 percent or
more to the automobile population. Excluding CO.sub.2, automobile
exhausts and evaporation losses contribute about 68,000,000 tons
daily to the 142,000,000 tons of pollutants entering the nation's
atmosphere daily. Automobiles powered by internal combustion
engines emit into the atmosphere unburned hydrocarbons, nitrogen
oxides, and carbon monoxide, which in various combinations react in
the atmosphere under the influence of sunlight, causing a typical
smog blanket.
the device of this invention, if installed at all service stations
where auto gasoline tanks are filled and used according to the
method of this invention, should substantially help in lowering the
total quantity of hydrocarbons in the air. It would also help
conserve a valuable natural resource--the petroleum from which
gasoline is made. Additionally, over a period of time, savings at
the service stations due to reduced losses of gasoline should pay
for the necessary equipment.
SUMMARY OF THE INVENTION
Briefly, a preferred form of my invention comprises a combination
of the following elements:
1. A tight seal at the automobile gasoline tank filler-pipe with a
screw cap of same size and similar in nature to the gasoline tank
cap, fitted with a gasket and sealed with a partial turn. A
delivery hose for gasoline is centered in this sealing device, and
vents in its release the vented vapors into an enclosed annular
space. This annular space is connected by a vapor delivery line
leading to a condenser unit. In order to prevent air entry or vapor
loss when a pump is not in use, as would be the case especially in
multiple-pump stations, each delivery line is equipped with a
check-valve to permit flow of vapors only in the direction of the
condenser unit.
2. A pressure relief valve, in each main storage tank ventline to
the atmosphere, which may be set to open at a desired predetermined
pressure differential, such as 0.5-2.5 psig. Elements (1) and (2)
provide vapor-tight means for preventing the displaced or
evaporated hydrocarbons from the tanks from entering the
atmosphere. 3. A vapor collection system comprising lines from each
pump, and from a point or points just upstream of the main storage
tank pressure relief valves (element 2), this system leading to the
condenser unit.
4. A condenser unit comprising (a) a vapor dissicator, (b) a low
temperature zone, similar to a conventional chest or horizontal
household-freezer and capable of maintaining a desired low
temperature, which will vary with the air and light hydrocarbon
content of the vapor and may be in the range of about 0.degree. F.
to about -40.degree. F., (c) a coolant bath maintained well below
the most volatile commonly-used hydrocarbon in gasoline, normal
butane, which boils at 31.degree. F., the coolant bath being large
enough to provide a "heat sink" for preventing undesirably high
temperature during short overload periods of perhaps 10 minutes
while a truck and trailer load of gasoline, usually 5,000 to 10,000
gallons, is unloaded into the main storage tanks, (d) a condenser,
preferably finned as in an automobile radiator and immersed in the
coolant bath, the condenser discharging into (e) a small
cyclone-separator to provide additional cooling and condensation
and to create, by high entry velocity, a separation force greater
than that of gravity, sufficient to force condensed hydrocarbon
liquid out the bottom of the cyclone cones and to release air,
other gas and hydrocarbon mist at relatively low velocity through a
vertical cylindrical disengaging zone above but within the
cyclone-separator vessel, and (f) a demister pad of steel-wool or
similar material in said cylindrical section to agglomerate any
entrained hydrocarbons present as a mist, returning said liquid
hydrocarbons by gravity to the separation zone of the
cyclone-separator, while venting air, substantially free of
hydrocarbons, from said cylindrical section into the
atmosphere.
5. A flexible tube or conduit for the condensed liquid
hydrocarbons, placed within the vapor-venting system of the storage
tank or tanks, and to return therein the liquid hydrocarbon
condensate from the bottom of the cyclone vessel to storage.
The above combination thus (1) prevents the gasoline vapor
displaced by liquid during filling from escaping into the
atmosphere, (2) prevents gasoline from evaporating into the
atmosphere during filling, (3) collects essentially all the
displaced and evaporated vapor and condenses it into liquid form,
and (4) recovers the liquid. The invention thus prevents both
pollution of the atmosphere and waste of valuable gasoline.
Other objects and advantages of the invention will appear from the
following description of some preferred embodiments.
BRIEF DESCRIPTION OF THE DRAWING
The drawing is a diagrammatic view in elevation and partly in
section of a gasoline vapor recovery system embodying the
principles of the invention.
DESCRIPTION OF THE PREFERRED EMBODIMENT
In the system of this invention, all lines carrying hydrocarbons
and all connections are vapor tight; so the condensing system may
be operated at a slight pressure, preferably at about 0.5 to 2.5
psig.
Thus, a tight seal is made between the automobile's filling tube
and the spout of the filling station hose, when the automobile's
gasoline tank is being filled. This tight seal may be made by any
one of the means therefor shown in co-pending patent application
Ser. No. 109,226 filed Jan. 25, 1971, or the structure shown in the
drawing of the present application may be used.
Here, the automobile has a body 11 and a filler tube 12 leading to
its gasoline tank, not shown, and having a filler spout or inlet
13.
Each gasoline pump 15,16 at the filling station is connected to a
main storage tank 17 for its grade or type of gasoline by a pipe 18
leading from an outlet 19 at the bottom of the tank 17. A hose 20
leads from the pump 15, and its outlet end or nozzle 21 is placed
in the filler tube 12.
A vapor-tight, preferably transparent cup 22 serves as a vapor
collection device. It has a screw cap 23 which may be the same size
as and similar in nature to the tank cap (not shown) of the tube
12. The screw cap 23 is provided with a gasket 24, and the
connection can then be sealed by a partial turn, just as when
putting a gasoline tank cap in place. The cup 22 may be made from a
suitable hard transparent plastic, such as rigid polyethylene, and
(although a similar device may be secured to the hose 20) in this
instance it may be placed on the filler tube 12 independently of
and before the delivery hose nozzle 21 is inserted in the tube 12.
Thus the cup 22 has a flexible gasket 25 made from
gasoline-resistant material such as neoprene or nitrile rubber,
Viton plastic, or the like; the gasket 25 is annular and is so
shaped and sized that it readily accepts the nozzle 21 and forms a
vapor-tight fit around it.
The cup 22 thus has an inner tubular wall 26 having openings 27
therethrough leading into an annular space 28, and gasoline and air
from the automobile tank are displaced by gasoline during filling
and flow from the tube 12 through the openings 27 into the enclosed
space 28, where the vapors are temporarily collected.
The invention calls for conveying this mixture of air and gasoline
vapor away from the cup 22 by a vapor-collection tube 30. For this
purpose, the tube 30 may be connected to an outlet 31 from the
space 28 by a length of plastic tubing 32 having a quick connector
33. In order to prevent the venting of vapors to the air from the
vapor-collection line 30, a check valve 34 is provided at the end
of the line 30 to allow flow of vapor only into the line 30.
A main collection line 35 collects vapor from all the lines 30 and
from a vent line 36 leading up from the upper end of the main
storage tank 17, which joins the line 35 at a juncture 37 a short
distance below a pressure relief valve 38 with a stack 39. A line
40 combines the vapors from the lines 35 and 36. The vent line 36
accommodates the displaced air and vapors when the tank 17 is being
filled, its inlet line 41 then being joined to the gasoline
delivery truck's line 42 by a vapor-tight union 43. Thus, the vent
line 36 transmits to the main vapor-collection line 35 both the
displacement vapors from filling, those resulting from agitation,
and those resulting from the "breathing" induced by temperature
changes. The pressure relief valve 38 may be set to open at a
predetermined pressure differential, such as 1.0 psig. If the
pressure exceeds the predetermined setting, the collected vapors
are vented directly to the air through the line 39 in order to
prevent the tanks and so on from damage or rupture.
The line 40 leads to a desiccant vessel 45, where the mixture of
air and gasoline vapor is de-moisturized. The vessel 45 may contain
any effective desiccant, such as silica gel, anhydrous calcium
sulfate ("Drierite"), calcium chloride, molecular sieves. This
drying is important since the condensing or absorption system is to
operate below the freezing point of water, and solidified
hydrocarbon hydrates or ice would plug the lines.
The dried mixture of air and vapors passes from the desiccant
vessel 45 by a conduit 46 to a condenser unit 50, where it flows
first into a finned heat-exchanger tube 51 immersed in a bath 52 of
a suitable liquid coolant. A preferred coolant is a 50 percent
solution of ethylene glycol in water. The bath 52 is kept in the
range of about 0.degree. F. to -40.degree. F., by a refrigerating
unit 53, which may be like that of a household freezer and has a
chest or housing 54. The finned heat-exchanger tube 51 is
preferably placed in a downwardly slanting position in the bath 52
in order to provide a thermo-syphon circulation of the contained
coolant. However, if desired, the coolant may be mechanically
agitated to improve the heat transfer rate. Here, the gasoline
vapors condense and become liquid.
The chilled effluent from the tube 51 flows into a cyclone
separator 55 via a line 56 and a tangential inlet 57. The cyclone
separator 55 is fully immersed in the bath 52. The inlet velocities
are substantial when the main tank 17 is being filled and is
appreciable when an automobile's tank is being filled. For example,
gasoline is normally sent into the main tank 17 at a rate of about
400 to 450 gallons per minute, so that vapor velocities into the
tangential inlet 57 may be about 60 feet per second or more;
moreover, the radius of the cyclone 55 is necessarily small, so
that the separating force between the air and the liquid condensate
is great, typically 200 or more times the force of gravity.
The condensed liquid collects in the bottom of the cyclone
separator 55 and leaves it through a conduit 60, which flows back
into the main storage tank 17. A convenient way to do this is to
employ hydrocarbon-resistant flexible tubing and to place the
conduit 60 inside the vapor lines 40 and 36, insofar as is
practicable.
The substantially hydrocarbon-free air leaves the cyclone separator
55 via a central orifice 61 in a horizontal plate 62 and flows into
a low-velocity chamber 63. The orifice 61 occupies, preferably,
about 8 percent to 25 percent of the area of the plate 62. As
insurance against loss of some liquid as mist, the low-velocity
chamber 63 may contain a de-mister pad 64 of suitable material,
such as stainless steel wool, which agglomerates any mist into
droplets. Thus, substantially dry, clean air, free of condensate,
leaves the chamber 63 through an outlet 65 and passes by a conduit
66 to the vent stack 39.
"Winter grade" gasoline presently has no legal vapor-pressure
limit, hence may be expected to contain more normal butane than
"summer grade" gasoline. Some refiners may even see fit to add some
propane or isobutane, should these hydrocarbons be in excess of
other needs. The presence of such additional light hydrocarbons in
a vapor which is mostly air may result in equilibrium condensation
temperature as low as about -40.degree. F. for 90 percent
hydrocarbon recovery as liquid. While such operating temperatures
pose no special problems other than use of a proper refrigerant,
including the Freon-type compound monochlorodifluoro methane known
as Refrigerant 502, ammonia, or propane and do not effect
refrigeration horsepower requirements appreciably, it may be
desirable to inject a small amount of tank gasoline into the tank
vapors before they enter the condenser-liquid recovery unit. This
enables a somewhat higher coolant temperature for 90 percent
hydrocarbon recovery or, alternately, a greater recovery at a given
temperature, by taking advantage of the combination absorption and
higher equilibrium temperature effects. Unless a large amount of
gasoline is injected, the refrigeration load increase is small. An
economical amount is about 1 to 3 mols of gasoline per mol of total
hydrocarbons in the vapor.
To accomplish this, a pump 67 may take suction on the tank gasoline
in line 18 whenever the pressure at a sensor 70 exceeds a
predetermined figure, as when a main storage tank is being filled.
The pump 67 discharges the tank gasoline through a line 68 into the
vapor line 46 at a point 69 just before the vapors enter the
condenser 51. In tanks using a submersible pump to supply the
gasoline-dispensing pumps, the pressure sensor 70 would actuate
this submersible tank pump and supply the gasoline into the line
68.
To those skilled in the art to which this invention relates, many
changes in construction and widely differing embodiments and
applications of the invention will suggest themselves without
departing from the spirit and scope of the invention. The
disclosures and the description herein are purely illustrative and
are not intended to be in any sense limiting.
* * * * *