Description of Invention
[0001] The present invention relates to a method of and means for sustaining fractures radiating
from a well bore in a geological strata. In order to stimulate production of oil and
gas from subterranean wells, it has become standard practice to fracture the oil or
gas bearing strata hydraulically so that fractures radiate from the well bore. The
fractures provide channels for the flow of oil and/or gas to the well bore and enhance
the rate of production from the well. The pressures prevailing in the fractured strata
will tend to close the fractures, unless they are sustained by introducing material
into the fractures.
[0002] It is known to sustain fractures radiating from a well bore by introducing resin-coated
proppant grains into the fractures. The grains are suspended in a gell for transfer
down the well bore and into the fractures. Breakdown of the gell occurs in the fractures,
producing a liquid which can flow away from the grains and leaving the grains deposited
in the fractures. The conditions of temperature and pressure to which the grains are
subjected in the fractures results in bonding of the grains into a coherent mass by
means of the resin.
[0003] In order to promote breakdown of the gell within the fractures, there is incorporated
in the gell a source of free-radicals or other suitable agent. A persulphate is a
suitable breaker for the gell. At a temperature in the range 120 to 200 °F, a persulphate
breaker produces free radicals. However, these free radicals are reactive towards
the resin coating of the proppant grains so that the efficiency of the breaker for
the purpose of causing the breakdown of the gell is impaired. To mitigate this problem,
it is known to incorporate a relatively high proportion of the breaker in the gell
but this leads to risk of the gell breakdown occuring before the gell has reached
the required position in fractures. Premature breakdown of the gell can, for example,
lead to the formation of a coherent body of resin-bonded grains in the well bore.
[0004] In US 4 888 240, Graham et al, there is disclosed a proppant for hydraulic fracturing,
the proppant comprising a core on which there is a cured resin coating. An outer coating
is present outside the curent coating, the outer coating being a heat-curable phenolic
resin with which there is incorporated a small amount of a polyvinyl acetal and a
small amount of a mineral oil. The curable resin of the outer coating would be reactive
towards a free-radical breaker and would thus impair the efficiency of the breaker
for the purpose of causing the breakdown of a gell in which the proppant is suspended.
According to a first aspect of the present invention, there is provided a method of
sustaining fractures radiating from a well bore in geological strata wherein a resin
composition is applied to relatively inert grains and a protective coating is applied
to the grains over the resin composition, the coated grains are suspended in a gell
containing a breaker for the gell, the suspended grains are introduced down the bore
into said fractures, when in the fractures, the gell breaks down under the action
of the breaker, the protective coating breaks down and the resin composition binds
the grains into a coherent, porous mass.
[0005] According to a second aspect of the invention, there is provided a composition comprising
proppant grains suspended in a gell wherein the gell includes a breaker for the gell,
wherein the grains comprise cores, an intermediate layer on the cores and a coating
on the intermediate layer, wherein the intermediate layer comprises a resin and wherein
the coating is less reactive with respect to the breaker than is said layer.
[0006] According to a third aspect of the invention, there are provided grains suitable
for use as the proppant grains of a composition according to the second aspect of
the invention, which grains comprise cores, an intermediate layer on the cores and
a coating on the intermediate layer, wherein the intermediate layer comprises a resin
and wherein the coating is less reactive with respect to the breaker than is said
layer.
[0007] Naturally-occuring and synthetic mineral grains are suitable for use as the cores
of the proppant. The proppant cores may be silica sand or synthetic alumino silicates.
[0008] The resin composition applied to the cores of the proppant is selected for its ability
to cure, when subjected to elevated temperature and to pressure in the fractures radiating
from a well bore. Suitable phenolic resins are available commercially. The resin may
be applied as an aqueous dispersion and then dried under turbulent conditions, so
that the grains do not become bound into a coherent mass. Alternatively the resin
may be applied by a solvent, or by direct coating of the cores with the resin in a
melted condition.
[0009] The coating applied to the proppant grains over the resin is required to protect
the resin against reaction with the breaker or with free radicals or other products
derived from the breaker and is therefor required to be less reactive towards the
breaker or towards free-radicals derived from the breaker than is the resin layer.
The composition of the coating may be such that the coating will break down under
the action of heat and pressure and permit bonding of the proppant grains into a coherent
mass by curing of the resin. Composition comprising natural and/or synthetic waxes
may be used to form the coating. Naturally-occuring and/or synthetic resins may comprise
or be incorporated in the coating composition.
[0010] Examples of coatings which rupture under pressure, to permit bonding of the proppant
grains by curing of the resin, are polyethylene, polypropylene, and polyvinylidene
chloride.
[0011] In a case where the gell is aqueous, the coating composition may incorporate water-soluble
components, for example polyacrylates, polyvinyl alcohols and polyvinyl acetates.
Silicates of alkali metals may also be used in the coating composition.
[0012] The gell may be an aqueous gell and may comprise naturally-occuring gums and modified
gums. The gell further comprises a breaker suitable for promoting break-down of the
gell under the conditions to which the gell is subjected in the fractures radiating
from the well bore. A source of free-radicals, for example a persulphate, e.g. sodium
or ammonium persulphate, is a suitable breaker for use with a gell comprising an aqueous
dispersion of gums.
[0013] The coated proppant grains may be prepared, transported and stored separately from
the gell. Prior to use, the proppant grains are dispersed in the gell and the resulting
dispersion is then pumped down a well bore and into fractures radiating from the bore.
The gell containing coated proppant grains as herein described may be preceded by
gell containing uncoated proppant grains which will be carried into parts of the fractures
remote from the well bore. The gell containing coated proppant grains will occupy
at least those parts of the fractures adjacent to the well bore.
[0014] In the fractures, the gell is subjected to pressure and to an elevated temperature.
The temperature may be within the range 120 to 200 °F. At the elevated temperature,
the breaker promotes breakdown of the gell to a relatively low viscosity aqueous mixture.
For example, free radicals released by a persulphate at the elevated temperature will
attack the carbon chain of a gum and thereby cause the breakdown of the gell. The
aqueous mixture resulting from breakdown of the gell flows to the well bore and is
drawn up the bore to the surface, leaving the coated grains in the fractures.
[0015] The protective coating on the proppant grains also will break down in the fractures.
In a case where the coating is water-soluble, the coating may, at least in part, be
carried away from the proppant grains by the aqueous mixture which results from break-down
of the gell. The effect of the temperature and pressure to which the coated grains
are subjected in the fractures also contributes to break-down of the protective coating
over a period of time which is generally longer than that required for the breaker
to act on the gell and cause break-down of the gell to a relatively low-viscosity
mixture. Break-down of the protective coating is sufficient to enable the resin layer
on the cores of the proppant grains to bind the grains into a coherent mass as the
resin cures under the temperature and pressure to which the proppant is subjected
in the fractures.
[0016] The proportion of the resin in the coated proppant grains is sufficiently high to
facilitate bonding of the cores into a coherent mass but is sufficiently low to ensure
that the resulting mass is permeable to gas and/or to oil. The proportions of resin
and mineral will, in part, be determined in accordance with the size of the mineral
grains. Typically, the mineral grains will constitute at least 95% by weight of the
coated proppant grains and the resin composition will be present in the range 1.5
to 5%, by weight, of the coated proppant grains. The weight of the protective coating
will be substantially less than that of the resin layer.
[0017] We have found that, when using coated proppant grains as herein described, satisfactory
breaking of the gell can be achieved by incorporating a persulphate at the rate of
0.5 to 2lbs, e.g. 1 or 1.5lbs, per thousand US gallons of gell (approximately 250
grams to 1000 grams, e.g. 500 or 750 grams, per 3785 litres of gell). In a comparable
composition using proppant grains coated only with a resin, it has been found necessary
to incorporate the persulphate at a rate of greater than 2, e.g. between 3 and 5lbs
per 1 thousand US gallons (greater than approximately 1000 grams, e.g. from 1500 to
2500 grams, per 3785 litres).
[0018] Suitably coated proppant grains can be prepared as follows:
[0019] High quality silica sand, or synthetic proppant with particle sizes in the range
420-840 microns (ASTM sieve no's: 20-40) is heated to 160°C. 3.0% by weight based
on the weight of sand or other proppant of a phenol/formaldehyde solid novolac resin
in granule, pastille, flake or needle form, having a molar phenol to formaldehyde
ratio of 1 to 0.8 in its initial kettle charge, is then charged onto the sand in a
known sand mixer. The sand and resin are mixed until the resin has melted and coated
the sand evenly.
[0020] A hexamine solution (44% w/w) in water is added to the sand mixture. The amount of
hexamine solution is such that the weight of solid hexamine added is 13% of the weight
of the resin mixed with the sand. When all the water has evaporated, a second protective
overcoating is then put onto the sand, which is still at an elevated temperature in
the mixer. There is used for the overcoating a wax which is solid at ambient temperature,
a phenolic resole resin which is solid at ambient temperatures but has a low melting
point, an emulsion of polyvinylidene chloride, a solution of a phenolic resole resin,
a solution of natural wood resin products, for example, colophony, or a solution of
a gum. The solution may be in water or some other solvent. In a case where there is
used for the overcoating a resin, this resin is selected to have low reactivity with
gell breakers.
[0021] The composition which is to form the overcoating is added to the mixture in the mixer
while the temperature of that mixture is still elevated. The amount of this composition
depends upon the surface area and type of substrate. For example, in the case of Chelford
20/40 sand, use of the composition which forms the overcoating in an amount which
is 0.9% by weight of solid material, based on the weight of the sand, achieves the
required protective coat. In the case of the synthetic proppant Carbolite 20/40, use
to form the overcoating of an amount which provides a weight of the solid overcoating
material which is 0.8% of the weight of synthetic proppant provides a satisfactory
protective coating. Proppants which have larger surface area require greater amounts
of coating composition and proppants which have lower surface area require less coating
composition. When the coating material has melted and coated the substrate, in the
case of a low-melting point, solid material, or when the solvent has been driven off
by the residual heat of the substrate, in the case of a coating composition which
is a solution, and the temperature has fallen sufficiently to ensure that the overcoating
is not molten, the mixture is discharged from the mixer and is passed through a vibrating
screen to ensure that there are no agglomerations. The coated proppant is then cooled
in a fluidised bed.
[0022] The features disclosed in the foregoing description, or the following claims, or
the accompanying drawings, expressed in their specific forms or in terms of a means
for performing the disclosed function, or a method or process for attaining the disclosed
result, or a class or group of substances or compositions, as appropriate may, separately
or in any combination of such features, be utilised for realising the invention in
diverse forms thereof.
1. A method of sustaining fractures radiating from a well bore in geological strata,
wherein a resin composition is applied to relatively inert grains and a protective
coating is applied to the grains over the resin composition, the coated grains are
suspended in a gell containing a breaker for the gell, the suspended grains are introduced
down the bore into said fractures and when in the fractures the gell breaks down under
the action of the breaker, the protective coating breaks down, and the resin composition
binds the grains into a coherent, porous mass.
2. A method according to Claim 1 wherein said protective coating breaks down under the
action of heat and pressure.
3. A method according to Claim 1 wherein the protective coating breaks down by dissolution
of water-soluble components in an aqueous gell.
4. A composition comprising proppant grains suspended in a gell which includes a breaker
for the gell; wherein the grains comprise cores, an intermediate layer on the cores,
and a coating on the intermediate layer; the intermediate layer comprising a resin
and the coating being less reactive with respect to the breaker than is said layer.
5. A composition according to Claim 4 wherein the proppant grains are transported unstored
separately from the gell and dispersed into the gell prior to use thereof.
6. A composition according to Claim 4 or Claim 5 comprising 0.5 to 2lbs persulphate per
thousand US gallons of gell (approximately 250 grams - 1 kg per 3785 litres).
7. Grains suitable for use as the proppant grains of a composition according to any one
of Claims 4 to 6, said grains comprising cores, an intermediate layer on the cores,
and a coating on the intermediate layer, wherein the intermediate layer comprises
a resin and the coating is less reactive with respect to the breaker than is said
intermediate layer.
8. Grains according to Claim 7 wherein said coating comprises natural and/or synthetic
waxes.
9. Grains according to Claim 7 wherein said coating comprises polyethylen, polypropylene
or polyvinylidene chloride.
10. Grains according to any one of Claim 7 wherein the gell is aqueous and the coating
incorporates water-soluble components.