U.S. patent number 3,773,303 [Application Number 05/192,045] was granted by the patent office on 1973-11-20 for method and means to operate pumping system.
Invention is credited to James E. Griffith.
United States Patent |
3,773,303 |
Griffith |
November 20, 1973 |
METHOD AND MEANS TO OPERATE PUMPING SYSTEM
Abstract
Hot and cold liquid molten congealable hydrocarbons are mixed
and otherwise prepared for pumping by a conduit and pump system for
pumping such liquids (e.g., hot asphalt). The system is cleaned by
reversing the direction of the asphalt pump to thereby pass air
reversely through the pump and the lines handling the asphalt,
returning the asphalt to the place from whence it has been
withdrawn. Air is pumped through the system prior to asphalt
pumping to mix the hot and cold asphalt.
Inventors: |
Griffith; James E. (Cincinnati,
OH) |
Family
ID: |
22708013 |
Appl.
No.: |
05/192,045 |
Filed: |
October 26, 1971 |
Current U.S.
Class: |
366/4;
222/424 |
Current CPC
Class: |
F04C
13/002 (20130101); C10C 3/12 (20130101) |
Current International
Class: |
C10C
3/12 (20060101); F04C 13/00 (20060101); C10C
3/00 (20060101); B28c 005/06 (); B28c 005/42 ();
B28c 005/46 (); B01f 005/14 () |
Field of
Search: |
;259/4,18,36,95,98,145,146,147,148,151,153,155-158,159A,DIG.17
;134/102,169C ;222/190,318,333,424 ;126/343.5 ;141/1,2,92 |
References Cited
[Referenced By]
U.S. Patent Documents
Primary Examiner: Hornsby; Harvey C.
Assistant Examiner: Levy; Stuart S.
Claims
I claim as my invention:
1. A process of storing and pumping liquid congealable hydrocarbon
comprising the steps of
providing a storage vessel, a reversible pumping means, and a flow
path between the bottom of the vessel and the pumping means,
applying heat to the body of hydrocarbon in said vessel in a
quantity at least sufficient to maintain said hydrocarbon
liquid,
first operating the pumping means in the reverse pump direction to
draw air through the pumping means and deliver it into the body of
liquid hydrocarbon adjacent the bottom of the vessel for a time
sufficient to mix said liquid hydrocarbon, and
thereafter operating the pumping means in the opposite direction to
draw liquid hydrocarbon from adjacent the body of the vessel and
into the pumping means.
2. The process of claim 1 wherein said step of first operating said
pumping means further comprises drawing at least part of the air
from the air space above said body of liquid hydrocarbon within
said vessel.
3. The process of claim 1 further comprising the step of again
operating said pumping means in said reverse pump direction after
the last said step of operating whereby the hydrocarbon in sequence
is mixed, pumped and dispensed, and the flow path for same is
cleaned.
Description
BACKGROUND AND SUMMARY OF INVENTION
This invention relates to improvements in the method and means for
handling liquid molten congealable hydrocarbons. One aspect relates
to mixing. In one aspect it relates to cleaning pumping systems
that handle hot liquids that congeal or solidify at ambient
temperatures. A specific aspect of the invention relates to
improvements in storing, pumping and cleaning a hot liquid asphalt
pumping system by passing air reversely through it using the
asphalt pump as an air compressor to accomplish this, in connection
with which the invention will be described.
Asphalt at ambient temperatures is a solid material. It can be
worked at temperatures from about 350.degree. F., or higher,
depending on what kind of asphalt or tar is being handled. For
example, roofing asphalt becomes liquid at about 350.degree. F.
Similarly they each solidify at temperatures at or below those
temperatures. Thus, in applying such materials on construction
sites and while using them it is necessary to liquefy them and
maintain them liquid which is done by the application of heat. It
is also necessary to take precaution against the asphalt hardening
in pipelines and the like by reason of getting too cool. One way of
doing this is to empty the pipelines (normally by draining them
onto the ground) as soon as the particular job or item of work is
finished, thereby giving the asphalt no opportunity for cooling to
the point where it congeals.
In fact, the difficulties and inconveniences of liquefying asphalt
and other like materials once they have hardened in a reservoir,
pipeline, or the like is so great that it is customary to apply
heat to them for extended periods of time while in storage merely
to keep them liquid.
Asphalt is kept molten or liquid during storage by applying heat.
This is commonly done with a fire tube (or equivalent heating
means) that extends into the storage vessel that holds the asphalt.
The storage vessels with which I am concerned are normally mobile
being mounted on trucks or trailers and are generally quite large
(e.g., from about 6 ft. to about 9 ft. in their vertical dimension)
hence a significant thermal gradient (e.g., at least 20.degree. F.
in a 51/2 ft. diameter tank of the sort in the drawing or an amount
sufficient to cause vigorous and readily visible thermosyphonic
action upon applying heat through the fire tube) is established
within the asphalt in the vessel. The portion of the asphalt below
the fire tube thus is colder, even though molten, than that above
the fire tube. The practice has been to draw asphalt from a level
with or above the fire tube because the asphalt is hotter, less
viscous, flows more readily, is less likely to congeal in cold
lines or in temporary small job-site vessels, and because it is
cleaner than if drawn from the cold body of asphalt below the fire
tube. Experience has shown that debris of various particles settle
into the aforesaid colder asphalt below the fire tube. These
particles (debris) can be bits of minerals, coke, high melting
particles, dirt, and a variety of unanalyzed bodies. Over a period
of time the colder asphalt accumulates enough of this debris to
make it troublesome to pump and otherwise undesirable to use and
necessitates cleaning the storage vessel. Prior art cleaning
intervals have been as often as every six months on truck mounted
tanks.
The present invention resolves many of these problems because it
provides means to agitate and mix the colder asphalt with the
hotter material above it. This is done by providing a conduit that
extends well below the fire tube to almost the bottom of the
storage vessel and providing a reversible pump that is selectively
operated to force air through this conduit in a quantity sufficient
to agitate the colder material and/or to lower its density by
bubble entrainment therein. This action mixes the colder and hotter
portions of asphalt and disperses the debris (solid particles,
etc.) throughout. Upon completion of the mixing the pump is
reversed (preferably by driving it in its normal pumping direction,
i.e., forward) thus drawing the freshly mixed asphalt from the
bottom of the storage tank and dispensing it for use on such tanks
as roofing, highway or road surfacing and repair, and the like.
Advantages realized include use of the full volume of the storage
vessel, withdrawal of the debris in dispersed form, reduction or
elimination of downtime for cleaning the tank, and of course
elimination of need for cleaning the tank.
The present invention is also concerned with cleaning out liquid
asphalt from a pumping system, including the pump and the pipelines
connected between it and the storage tank, so that asphalt will not
have a chance to congeal or harden therein. Simply stated, this
involves reversing the direction of the asphalt pump in such a way
as to pump air as aforesaid through the pump, through the flow
paths connected between the pump and the asphalt tank, and into the
asphalt tank. This has the advantage of saving some asphalt by
returning it reversely through the pipeline or other conduit in
which it has been traveling and eliminates the well-known prior art
practice of opening a valve and letting the asphalt run out on the
ground where it is wasted.
Other objects, advantages and features of the invention will be
appreciated from a reading of the following specification and
claims in conjunction with the drawing wherein:
FIG. 1 schematically represents an asphalt storage, pumping, mixing
and cleaning system, according to the present invention suitable
for roofing asphalt it being understood that such system may be
mobile, i.e., mounted on a truck or trailer;
FIG. 2 schematically illustrates a preferred form of gear pump;
and
FIG. 3 schematically illustrates one assembled system for piping,
pumping, control, and power supply.
A body of molten asphalt 1 is stored in an insulated storage tank
comprising the inner holding tank 2, an outer jacket in the form of
a lightweight tank 3 and a layer of suitable insulation 4 between
the two tanks. The construction details of the tanks are well-known
and inasmuch as they comprise no part of the present invention, are
not further described. The tank may be mounted on a suitable
vehicle 5 such as a trailer, a truck, or it may be mounted on a
frame and be stationary at a work site.
The asphalt 1 is kept hot from the heat it receives from fire tube
7 which preferably is of the return tube type. Fuel gases from
propane tank 8 and valve 9 are burned by the burning apparatus 10
and delivered into the lower end of the fire tube 7 which is
U-shaped, and are thereafter vented to the atmosphere in a suitable
fashion.
Propane tank 8 is connected by manifolding 11 to the burner valve
and burner 9, 10. The propane tank 8 also preferably serves as a
fuel source for the prime mover engine 41.
At the time the system is to be cleaned, some asphalt has been
dispensed, hence asphalt seldom fills the tank 2 completely, there
is ordinarily an air space 12 above the asphalt. Since the air in
space 12 is in direct contact with the asphalt, it is approximately
the same temperature as the asphalt.
During normal pumping or dispensing, asphalt is withdrawn from
adjacent the bottom of the storage tank 2 by means of a flow path
that includes vertically extending dip tube 14 which preferably
goes to about one to two inches from the bottom of tank 2. The
conduit 14 is part of the suction system for an asphalt pump 15.
The rest of the flow path or tank to pump connection system
comprises a horizontal line 16, a further vertical line 17 and tees
18, 19 and 20 inter-connecting the same. Tees are preferred in lieu
of elbows so that gases can be vented and lines can be opened up
and inspected or cleaned out. Thus the flow path from adjacent the
bottom of tank 2 to the inlet or suction side of pump 15 comprises
vertically upward through dip tube 14, the tee 18, horizontal line
16, the tee 19, then downwardly through pipeline 17 and tee 20
directly into the pump. The tee 19 could as easily be an elbow
except that it is desired as good design practice to have a pipe
plug 23, which is removable, available as a means for inspecting
the vertical line 17 and cleaning same should it become coked up,
plugged or the like.
A valve 22 functions as a vacuum breaker valve to avoid syphoning
out the tank. Valve 22 is opened after pumping, mixing, and pipe
cleaning are completed. Valve 22 is closed during pumping, mixing
and cleaning operations. In case of pump failure or breakdown, the
flow path from tube 16 through 17 and 20 can be drained by opening
valves 22 and 24. Valve 22 is optional in my system.
The drain valve 24 is part of the well-known prior art apparatus
and in the past has been used to drain the pipelines 16, 17 and the
pump 15 so that asphalt would not have a chance to harden therein.
While my invention prefers a system constructed with the valve 24
as a guard against emergencies, the benefits derived from using my
present invention include not having to drain asphalt through the
valve 24 and waste it by letting it run out on the ground.
In ordinary operation asphalt is withdrawn from adjacent the bottom
of the tank 2 by means of the heretofore described pump suction
line and delivered by the pump 15 through its discharge line 30. I
have illustrated a system suitable for supplying roofing asphalt
which ordinarily means that the tank 2 and its associated apparatus
is located on a truck or trailer on the ground and the asphalt must
be pumped up through line 30 one, two or more stories to a
temporary storage vessel such as barrel 31 from whence it is
applied to roofing felt and the like. Valve 32 is preferably a
lever opening gate valve that is closed when pumping into the
barrel 31. A rope or cable 32A may extend from the lever to either
the roof or the ground to facilitate operating valve 32. Valve 32
is opened to stop asphalt going to the roof by pumping the asphalt
through the return path comprising horizontal conduit or pipe 33,
elbow 34 and vertical return pipe 35 into the air space 12 through
which it falls back into the body of liquid asphalt 1.
Conduit 35 is a pipe which terminates adjacent the top of storage
tank 2. The bottom part of vertical pipe 35 does not depend down
into the body of asphalt but instead is in communication with the
air space 12.
The pump 15 is preferably a reversible gear pump. It is driven
through a reversible gear drive transmission 40 (RGT) which in turn
receives power from a suitable motor 41 by means of a clutch 42.
The gear transmission has multiple forward speeds and one reverse
speed. The motor 41 is preferably a four-cycle gasoline engine
adapted to run on propane from tank 8 although it may be any
suitable internal combustion, electrical, or other sort of drive
means. Fuel is preferably supplied to motor 41 from propane tank 8
via fuel line 11. Similarly, the clutch 42 is a suitably selected
part of power transmission equipment and may include, in
combination with the engine and the reversible gear transmission
(RGT) a torque converter, automatic transmission of the sort so
commonly found in automobiles, or the like.
The important thing is that the power drive means 40, 41, 42 can be
reversed in such a manner as to reverse the direction that gear
pump 15 turns. It is also essential that gear pump 15, or more
broadly the pumping means, be reversible, able to pump gas in the
reverse direction, and able to pump liquid in the forward
direction. The drive means 40, 41, 42 are all commercially
available as is the gear pump 15.
FIG. 2 schematically shows a preferred form of reversible gear pump
15 installed in the flow path to receive asphalt from a suction
line that includes the vertical flow portion dip tube 14 and
conduits 16, 17 plus the fittings 18, 19, 20 and to discharge
through conduit 30. FIG. 2 also shows how the piping can be
simplified from the schematic of FIG. 1 if the pump has a discharge
at right angles to its suction. Arrows in FIGS. 1 and 2 show the
direction of operation and flow for liquid, here, asphalt. When air
is pumped reversely as in mixing and conduit cleaning the air and
pump parts move in the opposite directions.
Pump 15 is preferably a Viking Pump series 124 or 4124 with either
mechanical or packed seals. The pump has a housing 51 with inlet
and outlet connections 52 and 53, a rotor gear 54 within the
housing which rotor is driven by motor 41, a stator or vane 55, and
an idler or pinion gear 56 that is driven by the rotor 54.
My invention comprises the method of mixing asphalt in the tank and
of cleaning the hot molten liquid asphalt out of the pumping
circuit which primarily comprises the delivery or pump suction
lines 14, 16 and 17. This is done by opening valve 32 and -- by
manipulating the clutch 42 and reversible drive 40 -- putting the
pump in reverse so that fluid passing therethrough goes in a
direction opposite to that indicated by the arrows in the drawing.
The valve 32 may be either open or closed during air pumping
depending on whether the operator wants to use hot air from within
the air space 12 (open 32) or is amenable to using a mixture of
same with whatever air is drawn in reversely from the open end of
conduit 30.
Anyhow, with the pump running in reverse and valve 32 open air is
moved through the pump, reversely back up through line 17 and
through line 16 then down through line 14, pushing asphalt ahead of
it to the reservoir 2. By moving air through such lines for a
sufficient length of time, almost all of the asphalt can be removed
from the lines thus assuring that it will not be able to congeal
therein and plug them up thus creating a problem when the system
has started up again. Such asphalt as may coat the pipelines or the
pump very slightly will be removed in very short order when the
system is started up to pump hot asphalt again because the hot
asphalt then will melt readily any such thin coating and carry it
on through the system. Any back-syphon action is prevented by the
air trap formed when horizontal pipe 16 is blown clear of
asphalt.
The same things are done to prepare to pump asphalt, e.g., when
coating a roof, valve 32 is optionally (preferably) opened and
valves 22 and 24 are closed, the engine 41 is started and the gear
transmission 40 is shifted to the reverse (i.e., the air pumping)
speed, the clutch 42 is engaged, and the pump 15 is therefore
caused to act as an air compressor to draw air in through conduits
30 and 33 and their inter-connecting fittings 18, 19, 20 and direct
it through the conduits 17, 16, 14 and their connecting fittings
(e.g., tees 18, 19, 20) to where it emerges from the lower end 60
of conduit 14 into the colder portion 61 of the asphalt 1 (below
the fire tube 7). The burner 10 is meanwhile operating to send hot
gases through the fire tube 7 and continues to do so. The pump 15
is driven for a time sufficient to agitate and mix the colder
asphalt and hot asphalt. In a tank 2 of 64 inch diameter X 72
inches long (nominally 1000 gallons) this operating time is about
10 minutes minimum when running at 550 rpm a pump capable of
delivering 35 gpm at 400 rpm. My preferred speeds at 550 rpm with
the Viking gear pump of FIG. 2 are about 550 rpm for air pumping
and 2200 rpm for asphalt pumping.
Preferably the steps in the preceding paragraph are carried out
immediately before asphalt is to be pumped and dispensed. When the
asphalt mixing step has thus been completed valve 32 is closed
(valves 22, 24 remain closed during all normal operations), the
clutch is disengaged, the gear transmission is shifted to the
appropriate forward speed and the clutch is re-engaged whereupon
asphalt is drawn into the lower end 60 of conduit 14, thence
vertically upward and on to the intake of pump 15, and then
discharged from the pump through conduit 30, to a place of use
shown in FIG. 1.
As already noted the above steps are conducted in reverse sequence
(i.e., asphalt is first pumped then air is compressed) to remove
asphalt from the conduits 30, 17, 16, 14. Air is pumped as the
final step, as aforesaid, to do this. The engine is then shut off.
The burner 10 or other heating means is operated continuously
through this procedure and thereafter if any asphalt remains in the
tank.
While my invention has been described in connection with the
handling of hot asphalt especially in roofing asphalt systems, it
is to be understood that it is equally applicable to other systems
for handling liquid congealable materials such as liquid molten
congealable hydrocarbons including those selected from the group
consisting of road asphalt, tar, paraffin, pitch, and so forth.
It has been known to use a reversible pump to clean concrete or
cement out of concrete lines. See U.S. Pat. No. 3,572,652.
* * * * *