[0001] It is generally known to employ foams in chemical processes, in the manufacture of
elastomeric products, in fire fighting, in agricultural chemical applications and
in various uses in the petroleum industry. Among the uses for foam in the latter industry
are included acidizing, fracturing, cleanout, and gravel packing. There are numerous
foam generating apparatuses employed in the prior art, such as sparger tubes and closed
vessels wherein gaseous and liquid products are introduced and mixed in various ways
to create a foam. Several such devices of the prior art are disclosed in U.S. Patents
Nos. 1,753,429, 2,418,858, 3,979,326 and 4,070,302.
[0002] Problems with the aforesaid prior art devices include their bulk and weight, the
relatively high expense of manufacture, as well as the devices' tendency to create
foams of uneven quality due to their complexity and the inability of the operator
to immediately ascertain changes in foam quality. Moreover, these prior art devices
are very unsuitable for generating a foam carrying particles therein, as the introduction
of a particle-laden liquid into a prior art foam generator vessel results in immediate
and severe erosion due to the scouring action of the particles on the interior of
the vessel and associated piping. The inability to generate large volumes of such
"dirty" (particulate-laden) foams, is a major detriment to operations such as fracturing
or gravel packing an oil or gas well, where it may be beneficial from both a cost
and results standpoint to employ a foam as a carrier for the particulate matter. For
example, using foam greatly reduces the amount of carrier fluid and expensive additives
employed, and in addition places far less hydrostatic pressure on delicate formations
such as may be encountered in gas wells, or in unconsolidated formations of wells
to be gravel packed.
[0003] Other foam generating devices of a simpler design are also known in the prior art.
For example, U.S. Patent No. 3,090,444 discloses a device which draws air through
apertures in the side walls of the generator to create a foam; U.S. Patent No. 3,889,764
discloses a foam generator wherein the materials to be foamed impinge on a knife-edge
to create turbulence; U.S. Patent No. 4,330,086 discloses a tubular foam generator
having a choked liquid flow, downstream of which air is pulled into the generator
and the resulting mixture impinged on a transversely set pin and then the inner wall
of the generator to create a foam. While, as noted, above, these devices are simpler
and more compact than the aforementioned prior art devices, they nonetheless possess
inherent disadvantages. For example, the device of U.S. Patent No. 3,090,444 is still
somewhat clumsy in design, and takes quite some time and flow distance to effectively
create a foam. Moreover, this device, as well as those of U.S. Patents No. 3,889,764
and 4,330,086 are totally unsuitable for the foaming of particulate-laden fluids as
the fluid flow would quickly erode the liquid chokes and the knife-edge or pin employed
in these devices.
[0004] We have now devised a relatively uncomplex device for foam generation, which device
can be relatively easily and inexpensively produced, is wear-resistant by its design
and which permits the easy production of foam to the quality desired, even in the
case of "dirty" foams.
[0005] According to the invention, there is provided a system for generating a foam product,
comprising: means for supplying gas; means for supplying a liquid; foam generating
tee means comprising a tubular tee including a main leg and a side leg disposed at
substantially a right angle to said main leg; liquid feed manifold means adapted to
transmit said liquid from said liquid supply means to said side leg of said tee; gas
feed manifold means adapted to transmit said gas from said gas supply means to said
inlet end of said tee; and foam discharge piping means for receiving a foam product
from said tee.
[0006] The invention also includes a method of generating a foam product, comprising: introducing
a liquid stream under pressure into a tubular vessel; introducing a gas stream under
pressure into said tubular vessel; impinging said gas stream on said liquid stream
in said vessel at substantially a right angle to said liquid stream, whereby a substantially
uniform foam product is formed and discharged from said vessel.
[0007] Preferably, a choke means is associated with the main leg of the tee wherein the
gas component is introduced, the outlet of the choke means being located proximate
the inlet from the side.leg of the tee into the main leg. The foam is generated proximate
to and downstream from the intersection of the side leg with the main leg, and the
foam leaves the tee at the main leg and opposite the gas inlet end thereof.
[0008] It is believed that, in the method and apparatus of the present invention, a high
quality emulsion or foam is generated due to the manner in which the liquid component
is forced to make a substantially right-angle turn in its flow path. This change indirection
initiates turbulence, at which point the gas component flow induces additional turbulence
and provides efficient dispersion of the gas throughout the liquid, producing a high
quality emulsion or foam product. In addition to the efficient production of an emulsion
or a foam, the impingement of the gas flow at substantially right angles to the liquid
flow curtails the erosive effects of the liquid on the inside wall of the tee opposite
the inlet for the side leg; this curtailment is particularly critical in the foaming
or emulsification of dirty liquids carrying abrasive particulate matter, as without
it a hole would quickly be worn through the wall of the tee, or at best a weakened
wall area produced which could rupture, causing damage and serious injury.
[0009] In order to more fully understand the nature of the invention, the detailed description
set forth hereafter should be read in conjunction with the accompanying drawings,
wherein:
FIGURE 1 is a full section elevation of one embodiment of apparatus of the invention;
and
FIGURE 2 is a schematic illustration of the placement of an apparatus of the invention
in a system employed to generate and introduce a foam into a well bore to be treated.
[0010] Referring now to FIG. 1, the preferred embodiment of the apparatus of the present
invention will be described hereafter. Foam generator 10 comprises a generally tubular
tee having main leg 8 and side leg 12, side leg 12 defining liquid inlet bore 14 with
wall 16. A hammer-up type threaded union, generally indicated at 18 and well known
in the petroleum industry, connects liquid discharge piping 20 to side leg 12, piping
bore 22 communicating with and being coaxial with liquid inlet bore 14. Circular elastomeric
seal 24 is compressed between the end of piping 20 and annular seat 26 surrounding
the entrance to fluid inlet bore 14.
[0011] At the left side of FIG. 1, choke nozzle 30 is connected to end 32 of the main leg
of foam generator 10 by a hammer-up threaded union, generally referred to by reference
numeral 36, circular elastomeric seal 37 being compressed between end 32 of foam generator
10 and the inner end of choke nozzle 30. Choke insert 40 is threaded to choke nozzle
30 at threads 42; the end of choke nozzle 30 extends into gas inlet bore 38 of the
main leg which is defined by wall 34. A gas-tight seal between choke nozzle 30 and
choke insert 40 is effected by 0-ring 44, maintained in annular recess 46 on the exterior
of choke nozzle 30. Choke insert 40 includes outer tubular metal housing 48, which
is threaded to choke nozzle 30, which housing 48 carries choke insert 50 having restricted
axial bore 52 therethrough. Choke insert 50 may be of any suitable material, such
as metal or ceramic (shown in FIG. 1). The inner end 54 of axial bore 52 opens into
gas inlet bore 38 of main leg 8. The outer end 56 of axial bore 52 opens into socket
58 in which an allen wrench is used to rotate choke nozzle 30 when it is threaded
into foam generator 10. The outer end of socket 58 is open, and communicates with
gas discharge piping 60, having bore 62 defined by wall 64, which is connected to
choke nozzle 30 by hammer-up threaded union 66, circular elastomeric seal 59 being
compressed between the outer end of choke nozzle 30 and the end of gas discharge piping
60.
[0012] The area whereat the fluid and gas streams entering foam generator 10 impinge on
each other is generally indicated at 70; to the right of area 70 is foam discharge
bore 72, defined by wall 74 of foam generator 76. Foam discharge piping 80 is secured
to end 88 of foam generator 10 at the exit of foam discharge bore 72 by threaded hammer-up
union 82. Wall 84 of foam discharge piping 80 defines bore 86 within, which coaxially
communicates with foam outlet bore 72.
[0013] Area 90, opposite the entry of fluid inlet bore 14, is of somewhat greater wall thickness
than walls 16, 34 or 74, for reasons set forth hereafter.
[0014] FIG. 2 is schematically illustrative of a system in which the foam generator of the
present invention may be employed at a well site.
[0015] Liquid source 100, which may comprise multiple tanks of liquid with various additives
therein, such as surfactants and gelling agents, is connected to liquid feed manifold
102, which may comprise a variety of pipes, valves and joints as used in the art.
There may also be included in liquid source 100 a blender to blend particulate matter
such as sand, glass or ceramic beads, etc. with a carrier liquid, such an arrangement
and the r apparatus therefor being well known in the art. In any event, it should
be understood that liquid source 100 may be a source of a "dirty" (particulate-laden)
liquid or gel, as is employed in the prior art in acidizing, fracturing, gravel packing
or well cleanout operations.
[0016] Pump 104 draws liquid or gel from liquid source 100 through liquid feed manifold
102, greatly increasing its pressure (to several hundreds or even thousands of pounds)
and discharging the liquid or gel into liquid discharge piping 20. Pump 104 may be
a plunger-type high pressure pump, such as the HT-150 or
HT-400 pumps, employed by Halliburton Services of Duncan, Oklahoma in well treatment
operations.
[0017] Gas source 110, depicted schematically at the left side of FIG. 2, may comprise multiple
tanks containing liquid carbon dioxide or nitrogen, such as are employed in the art,
which feed through gas feed manifold 112, which may comprise a variety of pipes, valves
and joints as used in the art, into a pump 114, which may also be an HT-150 or HT-400
pump, employed by Halliburton Services. Pump 114 raises the pressure of the liquified
gas and discharges it into gas discharge piping 60. As noted with respect to FIG.
1, liquid discharge piping 20 is connected to side leg 12 of foam generator 10, while
gas discharge piping 60 is connected to end 32 of the main leg of foam generator 10
through choke nozzle 30. It should be noted that the gas carried by piping 60 may
still be in a liquified state at the time it is introduced into foam generator 10.
However, for purposes of clarity the flow thereof is referred to herein as a gas stream.
[0018] Foam discharge piping 80, secured to end 88 of main leg 8, runs from foam generator
20 into well 200, where the mixed gas and liquid is carried via tubing 202 to the
level of the well bore where it is discharged and employed in a well treating operation
such as been heretofore described and is known in the art.
[0019] The method of foam generation, or more broadly the generation of a product which
may comprise a foam product or a liquid/gas emulsion product, is effected in foam
generator 10 as follows. A liquid such as water, combined with a liquid such as water,
acid, crude oil, diesel, kerosene or other liquid which may have a surfactant and/or
a gelling agent combined therewith (gels also being encompassed by the term "liquid"
as used herein), is introduced into liquid inlet bore 14, as shown by the arrow in
bore 22. This liquid may also carry substantial amounts of particulate material, as
r noted previously. A gas such as carbon dioxide or nitrogen (which may be in a liquified
state) is introduced as shown by the arrow in bore 62 into the outer end 56 of axial
bore 52 of ceramic choke insert 50 secured to end 32 of main leg 8. The gas is accelerated
in bore 52 through the Venturi effect, and exits at inner end 54 into gas inlet bore
38 of main leg 8. The accelerated gas stream impinges on the liquid stream at area
70, the gas stream turning the fluid flow at substantially a right angle (depicted
by bent arrow) into foam discharge bore 72, the mixing of the gas with the liquid
and the turning of the liquid flow direction causing substantially immediate and uniform
mixing of the gas and liquid components into an emulsion or foam product. This emulsion
or foam product exits foam discharge bore 72 into foam discharge pipe 80, as shown
by the arrow in bore 86. This emulsion or foam product is then introduced into a well.
While the pressure in the well bore may not be substantially less than that in the
injection tubing 202, the emulsion or foam product will tend to form a foam or at
the least a gas emulsion due to the warming and vaporization of the initially liquified
gas in the product.
[0020] It should be noted that the change in direction of liquid stream greatly reduces
the erosive effect of the liquid on the wall of main leg 8 opposite side leg 12. However,
as erosion cannot be entirely eliminated, area 90 may be of increased wall thickness
to reduce the possibility of failure at that point.
[0021] It should be understood that the apparatus and method of the present invention are
not limited in application to foaming or emulsification of any particular liquids
or gels, or the use of any particular gases. In fact, the apparatus and method as
disclosed herein may be employed in the formation of true emulsions, as well as foams
and emulsions which may subsequently become foams due to a lowering of pressure or
an increase in temperature transforming the initial product.
[0022] Moreover, the method and apparatus of the present invention are not limited in applicability
to the petroleum industry, but may be employed wherever an emulsion or foam is to
be formed for any purpose.
[0023] It should be further understood that the introdu- tion of gas into the main leg of
the tee of foam generator 10 provides a feature not heretofore known in the art. In
contrast to an instance where gas is introduced into the side leg, and may therefore
not sufficiently impinge upon and mix with a liquid flow in the main leg, the method
and apparatus of the present invention ensure complete mixing due to the radical change
in liquid stream direction. The impingement of the gas stream into the liquid stream
also reduces the erosive effect of a particulate liquid aimed at the side wall of
main leg 8. Moreover, the accelerated, choked gas flow provides a much more effective
barrier to the erosive liquid than an unchoked flow. Of course, the degree of choking
for optimum performance is a matter of choice depending on the liquids and gases employed,
the pressures and flow rates thereof, and the desired quality and texture of the final
emulsion or foam product. Such choice of the degree of choking, or otherwise expressed
as the diameter of bore 52 relative to that of bore 62, may be empirically determined
by the operator. As with the selection of gases and liquids and the pressures and
flow rates thereof, such determinations are well within the ability of one of ordinary
skill in the art.
1. A system for generating a foam product, comprising: means (60) for supplying gas;
means (20) for supplying a liquid; foam generating tee means (10) comprising a tubular
tee including a main leg (8) and a side leg (12) disposed at substantially a right
angle to said main leg; liquid feed manifold means (102) adapted to transmit said
liquid from said liquid supply means to said side leg of said tee; gas feed manifold
means (112) adapted to transmit said gas from said gas supply means to said inlet
end of said tee; and foam discharge piping means (80) for receiving a foam product
from said tee.
2. A system according to claim 1, for use when said liquid carries particulate material,
wherein said liquid supply means comprises: a liquid source, a source of particulate
material; and blender means to mix said liquid and said particulate material.
3. A system according to claim 1 or.2, wherein said liquid supply means includes high
pressure pump means (104), and/or said gas supply means includes high pressure pump
means (114).
.4. A system according to claim 1,2 or 3, wherein said foam generating tee means includes
gas choke means (50) in said main leg.
5. A system according to claim 4, wherein said choke means possesses a restricted
longitudinal bore (52) having an outlet disposed proximate the junction of said side
leg with said main leg, the diameter of said choke means bore being selectively variable.
6. A method of generating a foam product, comprising: introducing a liquid stream
under pressure into a tubular vessel; introducing a gas stream under pressure into
said tubular vessel; impinging said gas stream on said liquid stream in said vessel
at substantially a right angle to said liquid stream, whereby a substantially uniform
foam product is formed and discharged from said vessel.
7. A method according to claim 6, wherein said gas stream is accelerated prior to
impinging on said liquid stream.
8. A method according to claim 7, wherein said acceleration is effected through choking
said gas stream.
9. A method according to claim 6,7, or 8, wherein said liquid carries particulate
material therein.
10. A method according to claim 9, wherein said particulate-laden liquid comprises
a particulate-laden gel.